WorldWideScience

Sample records for beehive coke

  1. Construction and operation of a demonstration plant of Beehive ovens for producing coke with the utilization of the energy of gases

    Energy Technology Data Exchange (ETDEWEB)

    Chaves, A.D. [Pedagogic and Tecnologic Univ. of Colombia, Tunja (Colombia); White, A. [Colombian Company of Coal Limited, Santafe de Bogota (Colombia)

    1995-12-31

    In Colombia, except the company Acerias Paz de Rio, the production of coke is done using Beehive furnaces and the gases that are produced in the process are expelled to the atmosphere producing a lot of contamination and deterioration of the environment. The Colombia Company of Coal Ltd, Ecocarbon and the Pedagogic and Technologic University of Colombia, state entities, have canalized financial and technical efforts to develop a Demonstrative Plant with 6 Beehive ovens with a duct for collecting the gases and using the energy from de gases in Samaca`s factories of bricks. Samaca is a town with approximately 15.000 habitants, situated in the department of Boyaca at 140 kilometers from Santafe de Bogota, and 25 kilometers from Tunja (where the Pedagogic and Technologic University of Colombia is situated). It`s main activities are coal mining and agriculture.

  2. South Africa faces coke shortage

    Energy Technology Data Exchange (ETDEWEB)

    NONE

    1998-05-01

    Iscor Vanderbijlpark in South Africa may need to import substantial tonnages of coking coal as a result of increasing quality demands on coke at Vanderbiljpark (to support the recently installed PCI process) as well as the Newcastle works. Availability of coke is not only a problem for the South African steel industry but is a global problem as the production of coke in Western countries has declined over the past three years. A massive expansion in coke-making capacity is happening in China but the Chinese beehive ovens create serious pollution problems. A world shortage of coke of 30 million t/y by 2005 is estimated, rising to over 60 million t/y by 2010 of no new capacity is created. Steelmakers have succeeded in reducing their consumption of coke, by pulverised coal injection by better distribution of components in the furnace shaft and by decline in use of the blast furnace-basic oxygen furnace route, but the industry is still facing serious shortages of coke.

  3. Dale Coke: Coke Farm

    OpenAIRE

    Farmer, Ellen

    2010-01-01

    Dale Coke grew up on an apricot orchard in California’s Santa Clara Valley. In 1976 he bought ten acres of farmland near Watsonville in Santa Cruz County but continued to work repairing fuel injection systems rather than farming at his new home. In 1981, a struggle with cancer inspired him to rethink his life and become an organic farmer. His neighbor, who had grown strawberries using pesticides and chemical fertilizers, asserted that strawberries could not be grown organically. Coke set out ...

  4. Detection of Pesticides in Active and Depopulated Beehives in Uruguay

    Directory of Open Access Journals (Sweden)

    Horacio Heinzen

    2011-09-01

    Full Text Available The influence of insecticides commonly used for agricultural purposes on beehive depopulation in Uruguay was investigated. Honeycombs, bees, honey and propolis from depopulated hives were analyzed for pesticide residues, whereas from active beehives only honey and propolis were evaluated. A total of 37 samples were analyzed, representing 14,800 beehives. In depopulated beehives only imidacloprid and fipronil were detected and in active beehives endosulfan, coumaphos, cypermethrin, ethion and chlorpyrifos were found. Coumaphos was present in the highest concentrations, around 1,000 µg/kg, in all the propolis samples from active beehives. Regarding depopulated beehives, the mean levels of imidacloprid found in honeycomb (377 µg/kg, Standard Deviation: 118 and propolis (60 µg/kg, Standard Deviation: 57 are higher than those described to produce bee disorientation and fipronil levels detected in bees (150 and 170 µg/kg are toxic per se. The other insecticides found can affect the global fitness of the bees causing weakness and a decrease in their overall productivity. These preliminary results suggest that bees exposed to pesticides or its residues can lead them in different ways to the beehive.

  5. Coke dust enhances coke plant wastewater treatment.

    Science.gov (United States)

    Burmistrz, Piotr; Rozwadowski, Andrzej; Burmistrz, Michał; Karcz, Aleksander

    2014-12-01

    Coke plant wastewater contain many toxic pollutants. Despite physico-chemical and biological treatment this specific type of wastewater has a significant impact on environment and human health. This article presents results of research on industrial adsorptive coke plant wastewater treatment. As a sorbent the coke dust, dozen times less expensive than pulverized activated carbon, was used. Treatment was conducted in three scenarios: adsorptive after full treatment with coke dust at 15 g L(-1), biological treatment enhanced with coke dust at 0.3-0.5 g L(-1) and addition of coke dust at 0.3 g L(-1) prior to the biological treatment. The enhanced biological treatment proved the most effective. It allowed additional removal of 147-178 mg COD kg(-1) of coke dust. PMID:25113994

  6. Increasing the strength of metallurgical coke by adding modified petroleum coke to the coking batch

    Energy Technology Data Exchange (ETDEWEB)

    M.I. Stukov; V.S. Zagainov; Y.B. Kukolev; N.S. Andreichikov; P.V. Shtark; A.V. Vishnyakov; V.A. Antonova; S.N. Soboleva [Eastern Coal-Chemistry Institute, Yekaterinburg (Russian Federation)

    2009-08-15

    Box-coking data show the possibility of increasing the yield and strength of metallurgical coke by introducing a coking additive in the batch. Specifically, this additive is a product of slow coking of heavy petroleum residues, characterized by excellent thermoplastic properties: clinkering properties and plastic temperature range. A Russian patent has been obtained for the coking additive.

  7. How Bees Deter Elephants: Beehive Trials with Forest Elephants (Loxodonta africana cyclotis) in Gabon.

    Science.gov (United States)

    Ngama, Steeve; Korte, Lisa; Bindelle, Jérôme; Vermeulen, Cédric; Poulsen, John R

    2016-01-01

    In Gabon, like elsewhere in Africa, crops are often sources of conflict between humans and wildlife. Wildlife damage to crops can drastically reduce income, amplifying poverty and creating a negative perception of wild animal conservation among rural people. In this context, crop-raiding animals like elephants quickly become "problem animals". To deter elephants from raiding crops beehives have been successfully employed in East Africa; however, this method has not yet been tested in Central Africa. We experimentally examined whether the presence of Apis mellifera adansonii, the African honey bee species present in Central Africa, deters forest elephants (Loxodonta Africana cyclotis) from feeding on fruit trees. We show for the first time that the effectiveness of beehives as deterrents of elephants is related to bee activity. Empty hives and those housing colonies of low bee activity do not deter elephants all the time; but beehives with high bee activity do. Although elephant disturbance of hives does not impede honey production, there is a tradeoff between deterrence and the quantity of honey produced. To best achieve the dual goals of deterring elephants and producing honey colonies must maintain an optimum activity level of 40 to 60 bee movements per minute. Thus, beehives colonized by Apis mellifera adansonii bees can be effective elephant deterrents, but people must actively manage hives to maintain bee colonies at the optimum activity level. PMID:27196059

  8. How Bees Deter Elephants: Beehive Trials with Forest Elephants (Loxodonta africana cyclotis in Gabon.

    Directory of Open Access Journals (Sweden)

    Steeve Ngama

    Full Text Available In Gabon, like elsewhere in Africa, crops are often sources of conflict between humans and wildlife. Wildlife damage to crops can drastically reduce income, amplifying poverty and creating a negative perception of wild animal conservation among rural people. In this context, crop-raiding animals like elephants quickly become "problem animals". To deter elephants from raiding crops beehives have been successfully employed in East Africa; however, this method has not yet been tested in Central Africa. We experimentally examined whether the presence of Apis mellifera adansonii, the African honey bee species present in Central Africa, deters forest elephants (Loxodonta Africana cyclotis from feeding on fruit trees. We show for the first time that the effectiveness of beehives as deterrents of elephants is related to bee activity. Empty hives and those housing colonies of low bee activity do not deter elephants all the time; but beehives with high bee activity do. Although elephant disturbance of hives does not impede honey production, there is a tradeoff between deterrence and the quantity of honey produced. To best achieve the dual goals of deterring elephants and producing honey colonies must maintain an optimum activity level of 40 to 60 bee movements per minute. Thus, beehives colonized by Apis mellifera adansonii bees can be effective elephant deterrents, but people must actively manage hives to maintain bee colonies at the optimum activity level.

  9. The triumphs of coke

    Energy Technology Data Exchange (ETDEWEB)

    Mott, R.A.

    2004-07-01

    This is a reproduction of a booklet specially written by Dr R.A. Mott and designed by Mr G.E. Hall to mark the jubilee of the Coke Oven Managers' Association, founded in 1915. Whilst mentioning early methods of making coke in Great Britain, it deals particularly with the many developments in coke usage which took place before 1915 and is complementary to the 'History of coke making' written by Dr Mott in 1936. Uses covered include: for malting, for non-ferrous metal making, in an iron blast furnace, in crucible steel making, in the chafery and puddling process, in a foundry cupola, and in railway locomotives. 15 ills.

  10. Centralized coke gasification study

    Energy Technology Data Exchange (ETDEWEB)

    du Plessis, Duke [Alberta Innovates (Canada); Pietrusik, Debbie [Alberta Finance and Enterprise (Canada)

    2011-07-01

    By the year 2020 Alberta will produce 3 million barrels of bitumen per day. Refining bitumen yields several by-products such as petroleum coke and off-gasses. These products can be further utilized as a low cost feedstock for additional applications to increase revenue. Alberta currently has the largest amount of coke stockpiled in the world. The presentation explores what is the most profitable way to use this coke and what future technologies would improve the economic and environmental impact of the process. The development of methane and hydrogen becomes competitive at intermediate gas and oil prices. The next generation of gasification technologies is going to be cheaper, efficient and much smaller. Pilot projects have shown positive results. Economies of scale can be reached simply by only 20-30% of annual coke production. The high cost of the current technology is creating the biggest challenge but new technologies and process innovations have the potential to drive down cost.

  11. Coke quality requirements in POSCO

    Energy Technology Data Exchange (ETDEWEB)

    Song, J.; Yi, J.; Wang, H. [POSCO (Republic of Korea). Cokemaking Dept.

    2001-07-01

    The 26 overheads describes coke quality requirements in POSCO, Republic of Korea. It is concluded that it is necessary to develop new coal and to prompt technical development in order to produce high quality coke. To improve coke quality. Posco had applied DMAIC (define, measurement, analysis, improvement, control) technique which is part of Six-Sigma activity.

  12. Effect of coking conditions on Rankin coefficient of coke cake

    Energy Technology Data Exchange (ETDEWEB)

    Arima, T.; Fukuda, K.; Kato, K. [Nippon Steel Corp. Ltd., Futtsu (Japan). Environmental & Process Technology Center

    2004-09-01

    An innovative cokemaking process, SCOPE21 (Super Coke Oven for Productivity and Environmental enhancement toward the 21st century), has been developed by JISF (The Japan Iron and Steel Federation) and CCUJ (Center for Coal Utilization, Japan). As a cokemaking process, it is important to guarantee safe and stable pushing. Coke pushing behavior was studied by using a pilot-scale coke oven and influence of coking conditions on the Rankin coefficient was investigated. It was found that Rankin coefficient was dependent on lateral shrinkage and fissure density in coke cake and that it can be controlled by controlling the fissure density in SCOPE21 process.

  13. Sterilization of beehive material with a double inductively coupled low pressure plasma

    Science.gov (United States)

    Priehn, M.; Denis, B.; Aumeier, P.; Kirchner, W. H.; Awakowicz, P.; Leichert, L. I.

    2016-09-01

    American Foulbrood is a severe, notifiable disease of the honey bee. It is caused by infection of bee larvae with spores of the gram-positive bacterium Paenibacillus larvae. Spores of this organism are found in high numbers in an infected hive and are highly resistant to physical and chemical inactivation methods. The procedures to rehabilitate affected apiaries often result in the destruction of beehive material. In this study we assess the suitability of a double inductively coupled low pressure plasma as a non-destructive, yet effective alternative inactivation method for bacterial spores of the model organism Bacillus subtilis on beehive material. Plasma treatment was able to effectively remove spores from wax, which, under protocols currently established in veterinary practice, normally is destroyed by ignition or autoclaved for sterilization. Spores were removed from wooden surfaces with efficacies significantly higher than methods currently used in veterinary practice, such as scorching by flame treatment. In addition, we were able to non-destructively remove spores from the highly delicate honeycomb wax structures, potentially making treatment of beehive material with double inductively coupled low pressure plasma part of a fast and reliable method to rehabilitate infected bee colonies with the potential to re-use honeycombs.

  14. High coking value pitch

    Energy Technology Data Exchange (ETDEWEB)

    Miller, Douglas J.; Chang, Ching-Feng; Lewis, Irwin C.; Lewis, Richard T.

    2014-06-10

    A high coking value pitch prepared from coal tar distillate and has a low softening point and a high carbon value while containing substantially no quinoline insolubles is disclosed. The pitch can be used as an impregnant or binder for producing carbon and graphite articles.

  15. Texture of cokes in relation to parameters of coal and coke

    OpenAIRE

    Pěgřimočová, J.

    2013-01-01

    The article presents a proposal of the simplified classification of textures of coke and the relationship between the texture parameters of coke both coal, from which the coke was made, and properties of the coke.

  16. Organic pollution removal from coke plant wastewater using coking coal.

    Science.gov (United States)

    Gao, Lihui; Li, Shulei; Wang, Yongtian; Sun, Hao

    2015-01-01

    Coke plant wastewater (CPW) is an intractable chemical wastewater, and it contains many toxic pollutants. This article presents the results of research on a semi-industrial adsorption method of coking wastewater treatment. As a sorbent, the coking coal (CC) was a dozen times less expensive than active carbon. The treatment was conducted within two scenarios, as follows: (1) adsorption after biological treatment of CPW with CC at 40 g L(-1); the chemical oxygen demand (COD) removal was 75.66%, and the concentration was reduced from 178.99 to 43.56 mg L(-1); (2) given an adsorption by CC of 250 g L(-1) prior to the biological treatment of CPW, the eliminations of COD and phenol were 58.08% and 67.12%, respectively. The CC that adsorbed organic pollution and was returned to the coking system might have no effect on both coke oven gas and coke. PMID:26114284

  17. COMPARING STUDY OF BLENDING PREHEATING MODIFIED COAL COKING AND STAMPING COKING FOR DONGSHEN COAL

    Institute of Scientific and Technical Information of China (English)

    伍林; 尹学琼; 魏贤勇; 宗志敏; 陈清如

    1999-01-01

    The compaison of the properties of coke of three coking methods is introduced. The mechanical properties and high temperature reactivity of coke blending preheating modified Dongshen coal are improved obviously than those of normal coke, and achieve or exceed that of stamping coke. This method shews more ability of expending coking coal resources.

  18. Programmed heating of coke ovens for increased coke size

    Energy Technology Data Exchange (ETDEWEB)

    Jenkins, D.R.; Mahoney, M.R. [University of Newcastle, Callaghan, NSW (Australia)

    2010-11-15

    Large, uniform sized coke is desirable for blast furnace use. It has previously been shown that the coke oven flue temperature in the first few hours of coking is a key determinant of coke size. In this paper, the authors present a new programmed heating approach, which is called pulsed heating, aiming to increase coke mean size at a given average flue temperature. The approach takes into account the charging sequence in coke oven batteries and the authors demonstrate how existing operating practice can be modified in batteries with suitable heating systems to achieve the desired heating programme. A mathematical model of fissure formation provides a prediction of the increase in coke mean size using pulsed heating, compared with standard heating. Pilot scale experiments have also been performed to validate the modelling approach. The results of the modelling indicate that the mean coke size can be increased by several millimetres in some cases, although results from the pilot scale show that pulsed heating increases coke size, but by a smaller amount than that predicted by the model. The potential advantages and limitations of pulsed heating are discussed, as well as opportunities for further investigation of the approach.

  19. PROSPECTS FOR COKE BREEZE RECOVERY

    Directory of Open Access Journals (Sweden)

    D. N. Mihnovets

    2012-01-01

    Full Text Available Researches give grounds to believe in the possibility of receiving briquettes from coke waste mixed with peat dry coal and their use for smelting iron in the cupola or as a household fuel.

  20. Silica Brick for Coke Oven

    Institute of Scientific and Technical Information of China (English)

    Wang Jing

    2007-01-01

    @@ 1 Scope This standard specifies the classification,specification,test method,quality appraisal procedure,labeling,packing,transportation,storage and quality certification of silica brick for coke oven.

  1. Continuous coking of heavy feedstocks

    Energy Technology Data Exchange (ETDEWEB)

    Sullivan, Douglas W. [Lidcon, Inc (United States)

    2011-07-01

    A new process for continuous coking and decoking has been developed by Lidcon Inc. This process uses bitumen, vacuum tower residues, or a heavy CCR stock. The Lidcon process produces a higher liquid yield and lowers solid coke production. It also reduces the effects on the environment by lowering the amount of utilities that are needed to power the unit, while improving fire and worker safety. The reactor also produces coke continuously. The theoretical advantage of such a reactor configuration is that it has a short high temperature residence time for volatiles while improving the mass transfer of volatiles through the residue. The dimensions of the reactor are approximately 28' long with a 7' diameter. The weight of the unit is 20,000lbs. The Lidcon process can deliver a higher level of efficiency while reducing the amount of coke that is produced.

  2. The mechanism of coking pressure generation I: Effect of high volatile matter coking coal, semi-anthracite and coke breeze on coking pressure and plastic coal layer permeability

    Energy Technology Data Exchange (ETDEWEB)

    Seiji Nomura; Merrick Mahoney; Koichi Fukuda; Kenji Kato; Anthony Le Bas; Sid McGuire [Nippon Steel Corporation, Chiba (Japan). Environment and Process Technology Center

    2010-07-15

    One of the most important aspects of the cokemaking process is to control and restrain the coking pressure since excessive coking pressure tends to lead to operational problems and oven wall damage. Therefore, in order to understand the mechanism of coking pressure generation, the permeability of the plastic coal layer and the coking pressure for the same single coal and the same blended coal were measured and the relationship between them was investigated. Then the 'inert' (pressure modifier) effect of organic additives such as high volatile matter coking coal, semi-anthracite and coke breeze was studied. The coking pressure peak for box charging with more uniform bulk density distribution was higher than that for top charging. It was found that the coking pressure peaks measured at different institutions (NSC and BHPBilliton) by box charging are nearly the same. The addition of high volatile matter coking coal, semi-anthracite and coke breeze to a low volatile matter, high coking pressure coal greatly increased the plastic layer permeability in laboratory experiments and correspondingly decreased the coking pressure. It was found that, high volatile matter coking coal decreases the coking pressure more than semi-anthracite at the same plastic coal layer permeability, which indicates that the coking pressure depends not only on plastic coal layer permeability but also on other factors. Coking pressure is also affected by the contraction behavior of the coke layer near the oven walls and a large contraction decreases the coal bulk density in the oven center and hence the internal gas pressure in the plastic layer. The effect of contraction on coking pressure needs to be investigated further. 33 refs., 18 figs., 5 tabs.

  3. Experimental study on shrinkage characteristics of semi-coke/coke under gradient temperature during coking process

    Energy Technology Data Exchange (ETDEWEB)

    Fu, Z.; Guo, Z.; Wang, S. [Chinese Academy of Sciences, Beijing (China)

    2006-04-15

    A furnace equipped with a removable measuring scale in the side was applied to study on the shrinkage characteristics of semi-coke/coke under gradient temperature during coking process. 1500 g coking coal was used in the test. The effects of coking time, central temperature, heating-up rate and gradient temperature on lateral shrinkage were studied under different heating rate. The results show that the coal begins to shrink at a central temperature range of 280 to 360{sup o}C and ends at about 900{sup o}C. The lateral shrinkage is in a range of 5 mm to 8.5 mm and lateral shrinkage ratio is 7 to 12%. Generally, the gradient temperature increases and lateral shrinkage decreases with increasing heating-up rate and density. The central temperature of beginning shrinkage, the second shrinkage peak, gradient temperature of different locations and shrinkage coefficient of coal decreases with the increase of heating rate. The central temperature of beginning shrinkage and gradient temperature of different locations increase with increasing density. But the increase of density has no influence on shrinkage coefficient and shrinkage peak. In addition, the temperature rise rates at different locations are different during different coking stages. 9 refs., 9 figs., 1 tab.

  4. EFFICIENCY OF FORMING NUCLEUS COLONIES IN ORDER TO DECREASE POPULATION OF Varroa destructor (ANDRESON AND TRUEMAN, 2000 IN BEEHIVES

    Directory of Open Access Journals (Sweden)

    Zlatko Puškadija

    2003-12-01

    Full Text Available Forming of nucleus colonies is efficient method in growth control of Varroa destructor population. Its goal is to decrease parasite’s pressure on bee colony. The advantage of this bio-technical measurement lays in its implement during vegetation season which delays use of the chemical resources for Varroa destructor control population in beehives for the post major honey harvest period. Nucleus colonies were formed from approx. half of sealed brood (35.5 ± 5.8 dm² and average of 5915 ± 912 bees. Results showed that there were 37.2 ± 5.6% mites removed from parental colonies. Minimum was 30.8%, and maximum was 45.5%. Due to such relatively small efficiency, this method cannot be recommended as unique, but it can be effective if it is applied in the post spring's honey harvest period as a part of growth reduction strategy of Varroa destructor population in beehive.

  5. Assessment of coke oven emissions exposure among coking workers

    Energy Technology Data Exchange (ETDEWEB)

    Chen, M.L.; Mao, I.F.; Wu, M.T.; Chen, J.R.; Ho, C.K.; Smith, T.J.; Wypij, D.; Christiani, D.C. [National Yang Ming University, Taipei (Taiwan). Dept. of Public Health

    1999-01-01

    Coking workers are regularly exposed to coke oven emissions, which consist primarily of polycyclic aromatic hydrocarbons and volatile organic compounds. This study measured the workers` exposure to the benzene soluble fraction of total particulates (BSF). Personal breathing-zone samples of BSF and total particulates were taken from all study subjects for 3 consecutive days. The highest BSF concentrations were found among the topside oven workers. Among the samples at the topside oven 84% exceeded the Occupational Safety and Health Administration standard (150 {mu}g/m{sup 3} BSF). The percentage of BSF in total particulates varied across job classifications, ranging from 0.3% in wharf men to 24% in tar chasers. Area sampling indicated that the BSF concentration at the topside area was sixty fold higher than that at the administrative area, which was approximately 2 km from the coke oven plant.

  6. 46 CFR 148.04-15 - Petroleum coke, uncalcined; petroleum coke, uncalcined and calcined (mixture).

    Science.gov (United States)

    2010-10-01

    ... 46 Shipping 5 2010-10-01 2010-10-01 false Petroleum coke, uncalcined; petroleum coke, uncalcined and calcined (mixture). 148.04-15 Section 148.04-15 Shipping COAST GUARD, DEPARTMENT OF HOMELAND... Requirements for Certain Material § 148.04-15 Petroleum coke, uncalcined; petroleum coke, uncalcined...

  7. The mechanism of coking pressure generation II: Effect of high volatile matter coking coal, semi-anthracite and coke breeze on coking pressure and contraction

    Energy Technology Data Exchange (ETDEWEB)

    Merrick Mahoney; Seiji Nomura; Koichi Fukuda; Kenji Kato; Anthony Le Bas; David R. Jenkins; Sid McGuire [BHP Billiton Technology, Shortland, NSW (Australia)

    2010-07-15

    One of the most important aspects of the cokemaking process is to control and limit the coking pressure since excessive coking pressure can lead to operational problems and oven wall damage. Following on from a previous paper on plastic layer permeability we have studied the effect of contraction of semi-coke on coking pressure and the effect of organic additives on contraction. A link between contraction (or simulated contraction) outside the plastic layer and coking pressure was demonstrated. The interaction between this contraction, local bulk density around the plastic layer and the dependence of the permeability of the plastic layer on bulk density was discussed as possible mechanisms for the generation of coking pressure. The effect of blending either a high volatile matter coal or one of two semi-anthracites with low volatile matter, high coking pressure coals on the coking pressure of the binary blends has been explained using this mechanism. 25 refs., 10 figs., 4 tabs.

  8. Comparison of coke burning on catalysts coked in a commericial plant and in the laboratory

    Energy Technology Data Exchange (ETDEWEB)

    Pieck, C.L.; Parera, J.M. (Instituto de Investigaciones en Catalisis y Petroquimica, Santiago del Estero 2654, 3000 Santa Fe (AR))

    1989-12-01

    This paper reports a commercial catalyst coked in a commercial naphtha reforming unit compared with a laboratory catalyst and the fresh commercial one coked during laboratory experiments at pressures lower than the commercial one. The carbon concentration on the catalyst and hydrogen/carbon ratio of the coke were measured. Temperature-programmed oxidation and test reactions for metallic and acidic functions of the coked catalysts were performed. The main difference is in the coke composition and its distribution over the catalytic functions of the catalyst. Compared to the commercially coked catalyst, the coke on the laboratory coked catalysts is richer in hydrogen, covers the metallic function in a higher proportion, and is burnt faster. The catalytic activity for hydrogenation (metallic reaction) of the laboratory-coked catalyst is decreased more, but it is partially recovered by increasing the hydrogen pressure. The decrease on the acidic activity produced by coking is similar on both catalysts.

  9. Effects of atamp-charging coke making on strength and high temperature thermal properties of coke.

    Science.gov (United States)

    Zhang, Yaru; Bai, Jinfeng; Xu, Jun; Zhong, Xiangyun; Zhao, Zhenning; Liu, Hongchun

    2013-12-01

    The stamp-charging coke making process has some advantages of improving the operation environment, decreasing fugitive emission, higher gas collection efficiency as well as less environmental pollution. This article describes the different structure strength and high temperature thermal properties of 4 different types of coke manufactured using a conventional coking process and the stamp-charging coke making process. The 4 kinds of cokes were prepared from the mixture of five feed coals blended by the petrography blending method. The results showed that the structure strength indices of coke prepared using the stamp-charging coke method increase sharply. In contrast with conventional coking process, the stamp-charging process improved the coke strength after reaction but had little impact on the coke reactivity index. PMID:25078828

  10. K2 Discovers a Busy Bee: An Unusual Transiting Neptune Found in the Beehive Cluster

    CERN Document Server

    Obermeier, Christian; Schlieder, Joshua E; Crossfield, Ian J M; Petigura, Erik A; Howard, Andrew W; Sinukoff, Evan; Isaacson, Howard; Ciardi, David R; David, Trevor J; Hillenbrand, Lynne A; Beichmann, Charles A; Howell, Steve B; Horch, Elliot; Everett, Mark; Hirsch, Lea; Teske, Johanna; Christiansen, Jessie L; Lépine, Sébastien; Aller, Kimberly M; Liu, Michael C; Saglia, Roberto P; Livingston, John; Kluge, Matthias

    2016-01-01

    Open clusters have been the focus of several exoplanet surveys but only a few planets have so far been discovered. The \\emph{Kepler} spacecraft revealed an abundance of small planets around small, cool stars, therefore, such cluster members are prime targets for exoplanet transit searches. Kepler's new mission, K2, is targeting several open clusters and star-forming regions around the ecliptic to search for transiting planets around their low-mass constituents. Here, we report the discovery of the first transiting planet in the intermediate-age (800 Myr) Beehive cluster (Praesepe). K2-95 is a faint ($\\mathrm{Kp = 15.5\\,mag}$) $\\mathrm{M3.0\\pm0.5}$ dwarf from K2's Campaign 5 with an effective temperature of $\\mathrm{3471 \\pm 124\\,K}$, approximately solar metallicity and a radius of $\\mathrm{0.402 \\pm 0.050 \\,R_\\odot}$. We detected a transiting planet with a radius of $\\mathrm{3.47^{+0.78}_{-0.53} \\, R_\\oplus}$ and an orbital period of 10.134 days. We combined photometry, medium/high-resolution spectroscopy, ad...

  11. Two 'b's in the Beehive: The Discovery of the First Hot Jupiters in an Open Cluster

    CERN Document Server

    Quinn, S N; Latham, D W; Buchhave, L A; Cantrell, J R; Dahm, S E; Fürész, G; Szentgyorgyi, A H; Geary, J C; Torres, G; Bieryla, A; Berlind, P; Calkins, M C; Esquerdo, G A; Stefanik, R P

    2012-01-01

    We present the discovery of two giant planets orbiting stars in Praesepe (also known as the Beehive Cluster), the first known hot Jupiters in an open cluster. Pr0201b orbits a V=10.52 late F dwarf with a period of 4.4264 +/- 0.0070 days and has a minimum mass of 0.540 +/- 0.039 Mjup, and Pr0211b orbits a V=12.06 late G dwarf with a period of 2.1451 +/- 0.0012 days and has a minimum mass of 1.844 +/- 0.064 Mjup. Because they reside in a cluster, the ages of these planets are amongst the best-determined of any planet outside our own solar system. As we endeavor to learn more about the frequency and characteristics of planets, the environment in which most stars form -- open clusters like Praesepe -- may provide essential clues to this end. This discovery will allow, for the first time, a direct estimate of the short-period giant planet frequency in open clusters.

  12. Cooperative mobile agents search using beehive partitioned structure and Tabu Random search algorithm

    Science.gov (United States)

    Ramazani, Saba; Jackson, Delvin L.; Selmic, Rastko R.

    2013-05-01

    In search and surveillance operations, deploying a team of mobile agents provides a robust solution that has multiple advantages over using a single agent in efficiency and minimizing exploration time. This paper addresses the challenge of identifying a target in a given environment when using a team of mobile agents by proposing a novel method of mapping and movement of agent teams in a cooperative manner. The approach consists of two parts. First, the region is partitioned into a hexagonal beehive structure in order to provide equidistant movements in every direction and to allow for more natural and flexible environment mapping. Additionally, in search environments that are partitioned into hexagons, mobile agents have an efficient travel path while performing searches due to this partitioning approach. Second, we use a team of mobile agents that move in a cooperative manner and utilize the Tabu Random algorithm to search for the target. Due to the ever-increasing use of robotics and Unmanned Aerial Vehicle (UAV) platforms, the field of cooperative multi-agent search has developed many applications recently that would benefit from the use of the approach presented in this work, including: search and rescue operations, surveillance, data collection, and border patrol. In this paper, the increased efficiency of the Tabu Random Search algorithm method in combination with hexagonal partitioning is simulated, analyzed, and advantages of this approach are presented and discussed.

  13. Chemical composition of coal and coke ash

    Energy Technology Data Exchange (ETDEWEB)

    Pluzhnikov, A.I.; Tsymbal, G.L.

    1983-05-01

    Karaganda Metals uses low sulphur coal from Karaganda and Kuzbass coalfields and is seeking ways of improving coke in terms of ash and its effect on blast furnace operations, chiefly coke rate reduction. Ash in coke has a critical effect on iron quality, slag composition and desulphurisation. The index used to demonstrate the change in coke consistency during incineration in the blast furnace is that of pyrolytic change: this closely reflects changes in coal charge composition. Control of coke ash content by suitably selecting the charge can be used to influence slag basicity and iron quality.

  14. Bio-coke as an alternative to petroleum coke and metallurgical coke; Bio-cokes als alternatief voor petroleumcokes en metallurgische cokes

    Energy Technology Data Exchange (ETDEWEB)

    Croezen, H.J.; Van Lieshout, M. [CE Delft, Delft (Netherlands); Sevenster, M.N. [Sevenster Environmental Consultancy, Australian Capital Territory ACT (Australia)

    2012-11-15

    In the framework of elaborating the Dutch Roadmap Chemistry 2030), CE Delft has conducted an exploratory study for the Association of the Dutch Chemical Industry (VNCI) on the options of replacing (petroleum) coke in the chemical sector by biocokes. Coke is used as a reducing agent and/or raw material in four companies in the Dutch chemical industry (Tronox, ESD-SIC, Thermphos, Aluchemie). Replacing coke at these four companies can potentially yield a direct CO2 reduction of expectedly several hundreds of kilotons per year. For a first exploration of the options of bio-coke, CE Delft first conducted a desk study to get information on the quality and production costs for bio-coke. Subsequently, CE Delft had contact with the four chemical companies and a made a number of company visits. Moreover, the technical, economic and organizational capabilities, constraints and requirements with regard to a possible (partial) switch to biocokes have been explored. Based on the information available so far it can be concluded that biocokes seems to be a technically and economically interesting innovation. For implementation to finally take place, it is necessary to gain better insight in the technical and economic potential [Dutch] In verband met de uitwerking van de Routekaart Chemie 2030 heeft CE Delft voor VNCI een verkenning uitgevoerd naar de mogelijkheden voor vervanging van (petroleum)cokes in de chemische sector door biocokes. Cokes wordt gebruikt als reductiemiddel en/of grondstof bij een viertal bedrijven in de Nederlandse chemie (Tronox, ESD-SIC, Thermphos, Aluchemie). Het vervangen van cokes bij deze vier bedrijven kan in potentie een directe CO2-reductie van naar verwachting enkele honderden kilotonnen/jaar opleveren. Voor een eerste verkenning van de mogelijkheden van bio-cokes heeft CE Delft eerst een bureaustudie uitgevoerd naar informatie over kwaliteit van en productiekosten voor bio-cokes. Vervolgens heeft CE Delft contact gehad met de vier chemische

  15. Fissure formation in coke. 2: Effect of heating rate, shrinkage and coke strength

    Energy Technology Data Exchange (ETDEWEB)

    D.R. Jenkins; M.R. Mahoney [CSIRO, North Ryde, NSW (Australia). Mathematical and Information Sciences

    2010-07-15

    We investigate the effects of the heating rate, coke shrinkage and coke breakage strength upon the fissure pattern developed in a coke oven charge during carbonisation. This is done principally using a mechanistic model of the formation of fissures, which considers them to be an array of equally spaced fissures, whose depth follows a 'period doubling' pattern based upon the time history of the fissures. The model results are compared with pilot scale coke oven experiments. The results show that the effect of heating rate on the fissure pattern is different to the effect of coke shrinkage, while the effect of coke breakage strength on the pattern is less pronounced. The results can be seen in both the shape and size of resulting coke lumps after stabilisation. The approach gives the opportunity to consider means of controlling the carbonisation process in order to tune the size of the coke lumps produced. 7 refs., 18 figs., 4 tabs.

  16. K2CO3 catalysis on the reactivity of top charged coke and stamp charged coke

    Science.gov (United States)

    Pang, Qing-hai; Zhang, Jian-liang; Qi, Cheng-lin; Ma, Chao; Kong, De-wen; Mao, Rui

    2013-01-01

    The catalysis of K2CO3 on the reactivity of top charged coke and stamp charged coke from Pansteel in China was studied. The coke reaction index of the stamp charged coke was 1%-2% higher than that of the top charged coke. Under the catalysis of K2CO3, the coke reaction index of both cokes approximately increased by 4%, 6%, 10% and 6% at 900, 1000, 1100 and 1200°C, respectively. The reactivity of the K-enriched stamp charged coke was 1%-2% higher than that of the K-enriched top charged coke below 1100°C. However, only negligible differences were found in the temperature zone between 1100 and 1200°C. Scanning electron microscopy images illustrated that pores in the top charged coke were smaller and equally distributed, while relatively more big pores exist non-homogenously in stamp charged coke. Due to the different processes in production, the stamp charged coke was more porous and most of the pores tended to be applanate. Cracks were observed in the microstructure of the stamp charged coke during the carbon solution reaction, implying the inferior quality of the stamp charged coke to the top charged coke at high temperature. Diffusion of K during the carbon solution reaction was studied by the energy dispersive spectrometry. It is found that K gradually spreads into the center of lumpy coke with the rising of temperature and is equally distributed on the edges of pores at 1200°C. Besides, oxidation reactions of functional groups become faster with the catalysis of K.content

  17. A heating partition for a coking furnace

    Energy Technology Data Exchange (ETDEWEB)

    Strelov, K.K.; Ivanova, A.V.; Kaufman, A.A.; Kuznetsov, G.I.; Likhogub, Ye.P.; Turman, D.S.; Varshavskiy, T.P.; Volfovskiy, G.M.

    1983-01-01

    A coking furnace heating partition (OPKT) is proposed in order to increase reliability by increasing its strength. The proposal includes equipping with a vertical wall (St) made of Dinas brick and positioning it along the longitudinal axis of the coking furnace heating panel. The dividing walls are made of Dinas brick and their faces are disposed between the bricks of the wall of the coking chamber (KK). The surface of the coking chamber wall is made from magnesite or corundum brick which makes up 70 to 80 percent of the operational surface (Pv) of the wall. The presence of the vertical wall in combination with the

  18. Investigation on activated semi-coke desulfurization

    Institute of Scientific and Technical Information of China (English)

    SHANGGUAN Ju; LI Zhuan-li; LI Chun-hu

    2005-01-01

    An activated semi-coke with industrial-scale size was prepared by high-pressure hydrothermal chemistry activation, HNO3oxidation and calcination activation in proper order from Inner Mongolia Zhalainuoer semi-coke, which is rich in resource and cheap in sale.SO2 adsorption capacity on this activated semi-coke was assessed in the fixed bed in the temperature range of 60-170℃, space velocity range of 500-1300 h-1, SO2 concentration of 1000-3000 ppmv, and N2 as balance. The surface area, elemental and proximate analysis for both raw semi-coke and activated semi-cokes were measured. The experimental results showed that the activated semi-coke has a high adsorption capacity for sulfur dioxide than the untreated semi-coke. This may be the result of increase of surface area on activated semi-coke and surface oxygen functional groups with basicity characteristics. Comparison to result of FTIR, it is known that group of-C-O-C- may be active center of SO2 catalytic adsorption on activated semi-coke.

  19. Targeting "Plan Colombia": A Critical Analysis of Ideological and Political Visual Narratives by the Beehive Collective and the Drug Enforcement Administration Museum

    Science.gov (United States)

    Erler, Carolyn

    2008-01-01

    This article compares the Beehive Collective's "Plan Colombia" to a museum exhibition representing the official U.S. position on Plan Colombia. Through a dialectical (Kellner & Share, 2007; Greene, 1988) reading of "Plan Colombia" and "Target America," I examine how each uses visual narrative to promote a particular reading of Plan Colombia.…

  20. Production of conductive coke for cathodic protection

    Energy Technology Data Exchange (ETDEWEB)

    Mogollon, E.G.; Henao, L.E.; Pacheco, L.A.; Ortiz, J.L.; Diaz, J.J. [Universidad Nacional de Colombia, Bogota (Colombia). Departamento de Quimica

    1999-07-01

    The reduction of resistivity of coke by means of the cocarbonization of mixtures of coking coals was studied using coal tar as an additive. Optimum temperature and blending conditions for decreased resistivity were investigated. The effect of particle size on the dependency of coal rank was investigated. 2 refs., 4 figs., 2 tabs.

  1. Neutron probe monitoring of water in coke

    International Nuclear Information System (INIS)

    Coke moisture ranges between 5 and 7%. At coke sampling, inaccuracies occur in water content assessment. The results alter depending on hourly and daily samples and on sampling points. In the blast furnace situation where the knowledge of coke moisture is important for determining specific consumption of coke, the neutron moisture gauge continuous method has been proven. The effect was studied of different contents of volatile compounds in coke, as were the effects of the types of steel and the wall thickness of the neutron probe protective tube and those of big lumps of coke and of anomalous moisture on determination accuracy. The neutron probe operation may also be affected by bulk density and by consistency of the coke granulometric composition. The steel protective tube should be made of a strong material guaranteeing long-term invariability of measuring conditions. Mixing should not take place of compacting and bulk operation coke. Under these conditions, measurement can be sufficiently accurate. (M.D.). 2 tabs., 1 fig., 5 refs

  2. Effect of coke strength on blast furnace performance

    Energy Technology Data Exchange (ETDEWEB)

    Belyshov, V.N.; Emushintsev, V.V.; Minikes, E.E.; Tsymbal, G.L.; Vakulin, V.N.

    1985-09-01

    The authors report on results of a study, conducted from 1979 to 1982, analyzing the effect of the strength of commercially produced coke on furnace performance, for furnaces of different volumes. The effect of coke strength on blast-furnace performance was analyzed in two directions: determination of the dependence of coke loss from fragmentation on coke strength indices; evaluation of the effect of the coke strength on melting indices. It is found that high-strength coke is needed for large-volume furnaces and that reduction in coke strength helps cause tuyere burning.

  3. Characterization of residual coke during burning

    Energy Technology Data Exchange (ETDEWEB)

    Pieck, C.L.; Jablonski, E.L.; Parera, J.M. (Inst. de Investigaciones in Catalisis y Petroquimica, Santiago del Estero 2654, 3000 Santa Fe (Argentina)); Frety, R. (Conventionne a l' Univ. Claude Bernard, Lyon I (France))

    1992-04-01

    In this paper coke remaining from the partial burning of coke deposited during the commercial re-forming of naphtha on a Pt-Re/Al[sub 2]O[sub 3] catalyst is studied. Burning temperatures are 623-923 K, and the remaining coke is characterized by temperature-programmed oxidation, X-ray diffraction, electron diffraction, IR, [sup 13]C CP-MAS NMR, electron spectroscopy for chemical analysis, electron paramagnetic resonance, and chemical analysis. After coke is burned at 673 K, the residual coke shows the minimum value in the H/C ratio and the maximum in the thickness of the aromatic layers, degree of organization, C==O concentration, binding energy of C 1s, peak width, and g value. This agrees with the model of coke burning: at low temperatures, the burning is selective; the more hydrogenated and amorphous carbonaceous species are burnt first. At high temperatures, the burning is nonselective and all species are simultaneously burnt. Coke is partially oxidized during burning, and intermediate species with C==O and C--OH groups are formed.

  4. The New-Generation Technology for Making Petroleum Needle Coke

    Institute of Scientific and Technical Information of China (English)

    Shi Changzhi; Shen Haiping; Long Jun; Xie Changjiang

    2003-01-01

    The current technology for producing the petroleum needle coke is apt to cause overflow of feedstock from the coke drums, instability in operation of coking unit, low mechanical strength of petroleum coke, and high percentage of coke powder, leading to difficulties in improving the overall quality of needle coke. Therefore, we have developed a new technology for producing the needle coke,featuring the manipulation of temperature range in a narrow scale at high pressure coupled with feedstock alternations. This new kind of technology has been successfully applied in a 60kt/a commercial coking unit. Provided that demand for the feedstock quality is satisfied, petroleum needle coke meeting the international quality standard can be manufactured using RIPP's technology for producing petroleum needle coke.

  5. Short communication. Platform for bee-hives monitoring based on sound analysis. A perpetual warehouse for swarms daily activity

    Energy Technology Data Exchange (ETDEWEB)

    Atauri Mezquida, D.; Llorente Martinez, J.

    2009-07-01

    Bees and beekeeping are suffering a global crisis. Constant information on swarms conditions would be a key to study new diseases like colony collapse disorder and to develop new beekeeping tools to improve the hive management and make it more efficient. A platform for beehives monitoring is presented. It is based on the analysis of the colonies buzz which is registered by a bunch of sensors sending the data to a common database. Data obtained through sound processing shows plenty of patterns and tendency lines related to colonies activities and their conditions. It shows the potential of the sound as a swarm activity gauge. The goal of the platform is the possibility to store information about the swarms activity. The objective is to build a global net of monitored hives covering apiaries with different climates, razes and managements. (Author) 21 refs.

  6. Effects of seasonal variations and collection methods on the mineral composition of propolis from Apis mellifera Linnaeus Beehives.

    Science.gov (United States)

    Souza, E A; Zaluski, R; Veiga, N; Orsi, R O

    2016-06-01

    The effects of seasonal variations and the methods of collection of propolis produced by Africanized honey bees Apis mellifera Linnaeus, 1758, on the composition of constituent minerals such as magnesium (Mg), zinc (Zn), iron (Fe), sodium (Na), calcium (Ca), copper (Cu), and potassium (K) were evaluated. Propolis was harvested from 25 beehives by scraping or by means of propolis collectors (screen, "intelligent" collector propolis [ICP], lateral opening of the super [LOS], and underlay method). During the one-year study, the propolis produced was harvested each month, ground, homogenized, and stored in a freezer at -10 ºC. Seasonal analyses of the mineral composition were carried out by atomic absorption spectrophotometry and the results were evaluated by analysis of variance (ANOVA), followed by Tukey-Kramer's test to compare the mean values (pminerals (Mg, Fe, Na, Ca, and Cu), and the propolis harvesting method affects the contents of 4 minerals (Mg, Zn, Fe, and Ca). PMID:26934152

  7. Effects of altitude and beehive bottom board type on wintering losses of honeybee colonies under subtropical climatic conditions

    Energy Technology Data Exchange (ETDEWEB)

    Ucak-Koc, A.

    2014-06-01

    The effects of altitude and beehive bottom board types (BBBT) on the wintering performance of honeybee colonies were investigated in the South Aegean Region of Turkey: Experiment I (E-I), with 32 colonies, in 2010-2011, and Experiment II (E-II), with 20 colonies, in 2011-2012. Each lowland (25 m) and highland (797 m) colony was divided randomly into two BBBT subgroups, open screen floor (OSF) and normal bottom floor (NBF), and wintered for about three months. In E-I, the local genotype Aegean ecotype of Anatolian bee (AE) and Italian race (ItR) were used, while in E-II, only the AE genotype was present. In E-I, the effect of wintering altitudes on the number of combs covered with bees (NCCB), and the effects of BBBT on brood area (BA) and the NCCB were found to be statistically significant (p < 0.05), but the effects of genotype on BA and NCCB were statistically insignificant (p > 0.05). In the E-II, the effect of wintering altitude on beehive weight was found to be statistically significant (p < 0.05), while its effect on the NCCB was statistically insignificant (p > 0.05). The wintering losses in the highland and lowland groups in E-I were determined to be 25% and 62.5% respectively. In contrast to this result, no loss was observed in E-II for both altitudes. In E-I, the wintering losses for both OSF and NBF groups were the same (43.75%). In conclusion, under subtropical climatic conditions, due to variations from year to year, honeybee colonies can be wintered more successfully in highland areas with OSF bottom board type. (Author)

  8. Effects of altitude and beehive bottom board type on wintering losses of honeybee colonies under subtropical climatic conditions

    Directory of Open Access Journals (Sweden)

    Aytul Ucak-Koc

    2013-12-01

    Full Text Available The effects of altitude and beehive bottom board types (BBBT on the wintering performance of honeybee colonies were investigated in the South Aegean Region of Turkey: Experiment I (E-I, with 32 colonies, in 2010–2011, and Experiment II (E-II, with 20 colonies, in 2011–2012. Each lowland (25 m and highland (797 m colony was divided randomly into two BBBT subgroups, open screen floor (OSF and normal bottom floor (NBF, and wintered for about three months. In E-I, the local genotype Aegean ecotype of Anatolian bee (AE and Italian race (ItR were used, while in E-II, only the AE genotype was present. In E-I, the effect of wintering altitudes on the number of combs covered with bees (NCCB, and the effects of BBBT on brood area (BA and the NCCB were found to be statistically significant (p0.05. In the E-II, the effect of wintering altitude on beehive weight was found to be statistically significant (p0.05. The wintering losses in the highland and lowland groups in E-I were determined to be 25% and 62.5% respectively. In contrast to this result, no loss was observed in E-II for both altitudes. In E-I, the wintering losses for both OSF and NBF groups were the same (43.75%. In conclusion, under subtropical climatic conditions, due to variations from year to year, honeybee colonies can be wintered more successfully in highland areas with OSF bottom board type.

  9. Influence of low-density polyethylene addition on coking pressure

    OpenAIRE

    Melendi, Sonia; Barriocanal, C.; R. Alvarez; M.A. Diez

    2014-01-01

    Different amounts of low-density polyethylene (LDPE) were added to a bituminous coal used to produce metallurgical coke. The effect of the plastic waste on the carbonization process and more exactly, on the coking pressure were investigated. A movable wall oven at semi-pilot scale was used for measuring coking pressure generated. It was found that coking pressure increases for low LDPE addition levels (1-3 wt.%); however higher amounts of LDPE reduce coking pressure. To explain this behavior ...

  10. Technical Progress of China's Delayed Coking Technology

    Institute of Scientific and Technical Information of China (English)

    Zhang Lixin; Li Hejie

    2005-01-01

    This article introduces the recent advances of China in the fields of process technology of delayed coking, enlarged equipment size, hydraulic decoking, automatic control and environmental protection. By the end of 2004 the total capacity of delayed coking units in China had reached 37.24Mt/a with the maximum coke drum diameter equating to 9.4 m. This article also presents the investment in delayed cokers and the current production status while pointing out the existing problems and future development trends.

  11. The coke drum thermal kinetic effects

    Energy Technology Data Exchange (ETDEWEB)

    Aldescu, Maria M.; Romero, Sim; Larson, Mel [KBC Advanced Technologies plc, Surrey (United Kingdom)

    2012-07-01

    The coke drum thermal kinetic dynamics fundamentally affect the coker unit yields as well as the coke product properties and unit reliability. In the drum the thermal cracking and polymerization or condensation reactions take place in a semi-batch environment. Understanding the fundamentals of the foaming kinetics that occur in the coke drums is key to avoiding a foam-over that could result in a unit shutdown for several months. Although the most dynamic changes with time occur during drum filling, other dynamics of the coker process will be discussed as well. KBC has contributed towards uncovering and modelling the complexities of heavy oil thermal dynamics. (author)

  12. Cancer mortality among coke oven workers.

    OpenAIRE

    Redmond, C K

    1983-01-01

    The OSHA standard for coke oven emissions, which went into effect in January 1977, sets a permissible exposure limit to coke oven emissions of 150 micrograms/m3 benzene-soluble fraction of total particulate matter (BSFTPM). Review of the epidemiologic evidence for the standard indicates an excess relative risk for lung cancer as high as 16-fold in topside coke oven workers with 15 years of exposure or more. There is also evidence for a consistent dose-response relationship in lung cancer mort...

  13. Nitrogen Chemistry and Coke Transformation of FCC Coked Catalyst during the Regeneration Process

    OpenAIRE

    Junjun Shi; Jianyu Guan; Dawei Guo; Jiushun Zhang; Liam John France; Lefu Wang; Xuehui Li

    2016-01-01

    Regeneration of the coked catalyst is an important process of fluid catalytic cracking (FCC) in petroleum refining, however, this process will emit environmentally harmful gases such as nitrogen and carbon oxides. Transformation of N and C containing compounds in industrial FCC coke under thermal decomposition was investigated via TPD and TPO to examine the evolved gaseous species and TGA, NMR and XPS to analyse the residual coke fraction. Two distinct regions of gas evolution are observed du...

  14. Fundamentals of Delayed Coking Joint Industry Project

    Energy Technology Data Exchange (ETDEWEB)

    Michael Volk; Keith Wisecarver

    2004-09-26

    Delayed coking evolved steadily over the early to mid 1900s to enable refiners to convert high boiling, residual petroleum fractions to light products such as gasoline. Pound for pound, coking is the most energy intensive of any operation in a modern refinery. Large amounts of energy are required to heat the thick, poor-quality petroleum residuum to the 900 to 950 degrees F required to crack the heavy hydrocarbon molecules into lighter, more valuable products. One common misconception of delayed coking is that the product coke is a disadvantage. Although coke is a low valued (near zero economic value) byproduct, compared to transportation fuels, there is a significant worldwide trade and demand for coke as it is an economical fuel. Coke production has increased steadily over the last ten years, with further increases forecast for the foreseeable future. Current domestic production is near 111,000 tons per day. A major driving force behind this increase is the steady decline in crude quality available to refiners. Crude slates are expected to grow heavier with higher sulfur contents while environmental restrictions are expected to significantly reduce the demand for high-sulfur residual fuel oil. Light sweet crudes will continue to be available and in even greater demand than they are today. Refiners will be faced with the choice of purchasing light sweet crudes at a premium price, or adding bottom of the barrel upgrading capability, through additional new investments, to reduce the production of high-sulfur residual fuel oil and increase the production of low-sulfur distillate fuels. A second disadvantage is that liquid products from cokers frequently are unstable, i.e., they rapidly form gum and sediments. Because of intermediate investment and operating costs, delayed coking has increased in popularity among refiners worldwide. Based on the 2000 Worldwide Refining Survey published in the Oil and Gas, the delayed coking capacity for 101 refineries around the world

  15. Modelling of a coke oven heating wall

    OpenAIRE

    Landreau, M.; Isler, D.; Gasser, A.; Blond, E.; Daniel, J.-L.

    2011-01-01

    International audience This work deals with thermomechanical modelling of a coke oven heating wall. The objective is to define the safe limits of coke oven battery operating conditions compatible with a long service life in terms of thermal and mechanical stresses. For this purpose a 3D thermomechanical model of a heating wall taking into account the assembly of bricks and joints was developed with PRISME Laboratory. To build an efficient and complete model, different parameters must be ta...

  16. The identification of dangerously coking coals

    Energy Technology Data Exchange (ETDEWEB)

    Barriocanal, C.; Patrick, J.W.; Walker, P.A. [Loughborough Univ. of Technology, Leicestershire (United Kingdom)] [and others

    1995-12-31

    When coals are carbonised in slot-type ovens, layers of plastic coal are formed parallel to the oven walls and move progressively inwards eventually meeting at the oven centre. It is within these plastic layers that the principal processes which result in particulate coal being converted into porous, fused coke take place. For some coals, usually having volatile matter contents between 17 and 25wt% (dry, ash-free basis), these processes are accompanied by the generation of measurable gas pressures within the plastic layers which attain maximum levels when the two layers meet at the oven centre. These pressures are transmitted through the coke to the oven walls, causing damage if sufficiently high. Other coals, similar in chemical analysis and swelling properties, can be carbonised with impunity. The technical aspects of the coking pressure phenomenon are well known. However, the fundamental processes involved in the generation of internal gas pressures are not fully understood. Thus, before being used in blends for commercial coke production, potentially dangerous coals are tested by carbonising upwards of 180kg charges in moveable-wall ovens and measuring directly the pressures exerted on the walls. Clearly, it would be helpful if dangerously coking coals could be identified from laboratory tests. Preliminary findings of a laboratory study designed to gain further insight into coking pressure development are presented in this paper. Internal gas pressures have been ascribed to volatiles trapped within either the plastic envelope or the plastic layer implying an overlap of the temperature ranges of volatile release and fluidity. An attempts to assess this view using, initially, thermogravimetric analysis and Gieseler plastometry and, later, a coking bomb are described, the results being related to internal gas pressures measured in a 1.5kg double-wall oven.

  17. NUMERICAL SIMULATION FOR A PROCESS ANALYSIS OF A COKE OVEN

    Institute of Scientific and Technical Information of China (English)

    Zhancheng Guo; Huiqing Tang

    2005-01-01

    A computational fluid dynamic model is established for a coking process analysis of a coke oven using PHOENICS CFD package. The model simultaneously calculates the transient composition, temperatures of the gas and the solid phases, velocity of the gas phase and porosity and density of the semi-coke phase. Numerical simulation is illustrated in predicting the evolution of volatile gases, gas flow paths, profiles of density, porosity of the coke oven charge,profiles of temperatures of the coke oven gas and the semi-coke bed. On the basis of above modeling, the flow of coke oven gas (COG) blown from the bottom of the coke oven into the porous semi-coke bed is simulated to reveal whether or not and when the blown COG can uniformly flow through the porous semi-coke bed for the purpose of desulfurizing the semi-coke by recycling the COG. The simulation results show that the blown COG can uniformly flow through the semi-coke bed only after the temperature at the center of the semi-coke bed has risen to above 900 ℃.

  18. Coke fouling monitoring by electrical resistivity

    Energy Technology Data Exchange (ETDEWEB)

    Bombardelli, Clovis; Mari, Livia Assis; Kalinowski, Hypolito Jose [Universidade Tecnologica Federal do Parana (UTFPR), Curitiba, PR (Brazil). Programa de Pos-Graduacao em Engenharia Eletrica e Informatica Industrial (CPGEI)

    2008-07-01

    An experimental method to simulate the growth of the coke fouling that occurs in the oil processing is proposed relating the thickness of the encrusted coke to its electrical resistivity. The authors suggest the use of the fouling electrical resistivity as a transducer element for determining its thickness. The sensor is basically two electrodes in an electrically isolated device where the inlay can happen in order to compose a purely resistive transducer. Such devices can be easily constructed in a simple and robust form with features capable to face the high temperatures and pressures found in relevant industrial processes. For validation, however, it is needed a relationship between the electrical resistivity and the fouling thickness, information not yet found in the literature. The present work experimentally simulates the growth of a layer of coke on an electrically insulating surface, equipped with electrodes at two extremities to measure the electrical resistivity during thermal cracking essays. The method is realized with a series of consecutive runs. The results correlate the mass of coke deposited and its electrical resistivity, and it can be used to validate the coke depositions monitoring employing the resistivity as a control parameter. (author)

  19. APPLICABILITY OF COKE PLANT CONTROL TECHNOLOGIES TO COAL CONVERSION

    Science.gov (United States)

    The report gives results of comparisons of process and waste stream characteristics from the Byproduct coke over process with selected gasification and liquefaction processes. It includes recommendations regarding control technologies for air, water, and solid wastes. Coke oven c...

  20. METALLURGICAL COKE INDUSTRY PARTICULATE EMISSIONS: SOURCE CATEGORY REPORT

    Science.gov (United States)

    The report gives results of a study to develop particulate emission factors based on cutoff size for inhalable particles for the metallurgical coke industry. After a review of available information characterizing particulate emissions from metallurgical coke plants, the data were...

  1. Fissure formation in coke. 3: Coke size distribution and statistical analysis

    Energy Technology Data Exchange (ETDEWEB)

    D.R. Jenkins; D.E. Shaw; M.R. Mahoney [CSIRO, North Ryde, NSW (Australia). Mathematical and Information Sciences

    2010-07-15

    A model of coke stabilization, based on a fundamental model of fissuring during carbonisation is used to demonstrate the applicability of the fissuring model to actual coke size distributions. The results indicate that the degree of stabilization is important in determining the size distribution. A modified form of the Weibull distribution is shown to provide a better representation of the whole coke size distribution compared to the Rosin-Rammler distribution, which is generally only fitted to the lump coke. A statistical analysis of a large number of experiments in a pilot scale coke oven shows reasonably good prediction of the coke mean size, based on parameters related to blend rank, amount of low rank coal, fluidity and ash. However, the prediction of measures of the spread of the size distribution is more problematic. The fissuring model, the size distribution representation and the statistical analysis together provide a comprehensive capability for understanding and predicting the mean size and distribution of coke lumps produced during carbonisation. 12 refs., 16 figs., 4 tabs.

  2. Three-dimensional beehive-like hierarchical porous polyacrylonitrile-based carbons as a high performance supercapacitor electrodes

    Science.gov (United States)

    Yao, Long; Yang, Guangzhi; Han, Pan; Tang, Zhihong; Yang, Junhe

    2016-05-01

    Three-dimensional beehive-like hierarchical porous carbons (HPCs) have been prepared by a facile carbonization of polymethylmethacrylate (PMMA)/polyacrylonitrile (PAN) core-shell polymer particle followed by KOH activation. The all-organic porogenic core-shell precursor was synthesized by a simple and green surfactant-free emulsion polymerization. The as-obtained HPCs show favorable features for electrochemical energy storage such as high specific surface area of up to 2085 m2 g-1, high volume of pores up to 1.89 cm3 g-1, hierarchical porosity consisting of micro, meso, and macropores, turbostratic carbon structure, uniform pore size and rich oxygen-doping (21.20%). The supercapacitor performance of HPCs exhibit a high specific capacitance 314 F g-1 at a current density of 0.5 A g-1 and 237 F g-1 at a current density of 20 A g-1, ultra-high rate capability with 83% retention rate from 1 to 20 A g-1 and outstanding cycling stability with 96% capacitance retention after 2000 cycles. The facile, efficient and green synthesis strategy for novel HPCs from polymer sources could find use in supercapacitors, lithium ion batteries, fuel cells and sorbents.

  3. Influence of biomass on metallurgical coke quality

    OpenAIRE

    Montiano Redondo, María de Garabandal; Díaz-Faes González, Elvira; Barriocanal Rueda, Carmen; Álvarez García, Ramón

    2014-01-01

    Two industrial coal blends used in coke making were subjected to tests in order to assess the influence of waste sawdust (SC2 from chestnut and SP1 from pine) on the quality of the coke produced. The biomass was added in quantities of up to 5 wt.%. It was observed that biomass produced a substantial decrease in the plastic properties of the industrial coal blend, with reductions in Gieseler maximum fluidity of around 50% for 3 wt.% additions of the two different sawdusts. Carbonizations with ...

  4. Fundamentals of Delayed Coking Joint Industry Project

    Energy Technology Data Exchange (ETDEWEB)

    Volk Jr., Michael; Wisecarver, Keith D.; Sheppard, Charles M.

    2003-02-07

    The coking test facilities include three reactors (or cokers) and ten utilities. Experiments were conducted using the micro-coker, pilot-coker, and stirred-batch coker. Gas products were analyzed using an on-line gas chromatograph. Liquid properties were analyzed in-house using simulated distillation (HP 5880a), high temperature gas chromatography (6890a), detailed hydrocarbon analysis, and ASTM fractionation. Coke analyses as well as feedstock analyses and some additional liquid analyses (including elemental analyses) were done off-site.

  5. 单种焦煤结焦性能及其混配性研究%Coking capacity and coking compatibility of coking coals

    Institute of Scientific and Technical Information of China (English)

    项茹; 宋子逵; 薛改凤; 鲍俊芳

    2012-01-01

    The quality and coking capacity of 5 coking coals from different mines were analyzed and compared, and coal blend coking experiment was conducted. The results show, although the coking capacity of the coals doesn't differ much, their process indexes and coking microstructures are remarkably different. During blending and coking, if the coking has abundant plastometers with high fluxion and expansion and more coarse coking grains, its coking compatibility with different coals will be good and the coke quality will also be high, and vice versa.%对5种不同矿点的焦煤进行煤质分析和单种煤结焦性能比较,并进行配煤炼焦试验研究.结果表明,尽管单种焦煤的结焦性能接近,但其工艺性质及成焦显微结构存在较大差异.在配煤炼焦中,胶质体含量丰富、胶质体的流变性和膨胀性高、成焦粗粒镶嵌结构多的焦煤,与不同炼焦煤的混配性强,所得焦炭质量较优.

  6. Fundamentals of Delayed Coking Joint Industry Project

    Energy Technology Data Exchange (ETDEWEB)

    Michael Volk Jr; Keith Wisecarver

    2005-10-01

    Delayed coking evolved steadily over the early to mid 1900s to enable refiners to convert high boiling, residual petroleum fractions to light products such as gasoline. Pound for pound, coking is the most energy intensive of any operation in a modern refinery. Large amounts of energy are required to heat the thick, poor-quality petroleum residuum to the 900 to 950 degrees F required to crack the heavy hydrocarbon molecules into lighter, more valuable products. One common misconception of delayed coking is that the product coke is a disadvantage. Although coke is a low valued (near zero economic value) byproduct, compared to transportation fuels, there is a significant worldwide trade and demand for coke as it is an economical fuel. Coke production has increased steadily over the last ten years, with further increases forecast for the foreseeable future. Current domestic production is near 111,000 tons per day. A major driving force behind this increase is the steady decline in crude quality available to refiners. Crude slates are expected to grow heavier with higher sulfur contents while environmental restrictions are expected to significantly reduce the demand for high-sulfur residual fuel oil. Light sweet crudes will continue to be available and in even greater demand than they are today. Refiners will be faced with the choice of purchasing light sweet crudes at a premium price, or adding bottom of the barrel upgrading capability, through additional new investments, to reduce the production of high-sulfur residual fuel oil and increase the production of low-sulfur distillate fuels. A second disadvantage is that liquid products from cokers frequently are unstable, i.e., they rapidly form gum and sediments. Because of intermediate investment and operating costs, delayed coking has increased in popularity among refiners worldwide. Based on the 2000 Worldwide Refining Survey published in the Oil and Gas, the delayed coking capacity for 101 refineries around the world

  7. The Value Proposition of 'Teck Coke Limited' Should Teck Enter the Coke Trade?

    OpenAIRE

    Colin Wilfred Petryk

    2011-01-01

    This paper will review the business case for Teck to enter the metallurgical cokemarket for the steel industry. The trend impacting investment is the growing demand forsteel. There are two coke battery technologies to choose from; environmental concernsmake the heat recovery oven the preferred technology. Four countries were considered inwhich to build the coke plant; Teck’s relationship with Chile and Chile’s desire forforeign investment makes it the best choice. Market size was estimated us...

  8. Chemical composition of ash in coal and coke

    Energy Technology Data Exchange (ETDEWEB)

    Pluzhnikov, A.I.; Tsymbal, G.L.

    1983-05-01

    Ash content in coke influences coke consumption rate by blast furnaces. In the Karaganda steelworks a 1% ash content decrease in coke reduces coke consumption by a blast furnace by 1 to 1.6%. Ash content in coke depends on ash content in a coal mixture and ash content in a coal mixture depends on ash content and washability of coal components. Not all ash components are of identical importance for blast furnace coke production. Investigations show that silica and aluminium oxides are only slightly influenced by thermal degradation and reduction reactions which take place during coking. Coal pyrolysis decisively influences content of sodium oxides, potassium oxides or iron oxides. Sodium and potassium carbonates are also unstable and undergo degradation. Taking into consideration that silica and aluminium oxides are not influenced by thermal degradation during coking an increase in the two oxides in a coal mixture used for coking causes an ash content increase in coke. Examples of coal from the Kuzbass and the Vorkuta mines are given. Replacing 5% of the KZh and K coal from Karaganda with G6 coal from the Kuzbass characterized by the identical ash content but by higher content of silica and aluminium oxides causes an increase in ash content in coke ranging from 1.6 to 1.8%. (8 refs.)

  9. Generic methods for coke oven gas desulphurisation

    Energy Technology Data Exchange (ETDEWEB)

    Wilfried Seyfferth; Rainer Dittmer; Holger Thielert [ThyssenKrupp EnCoke GmbH, Bochum (Germany)

    2004-07-01

    The presentation gives an overview of the most common desulphurisation processes suitable for coke oven gas. Dry oxidative processes mentioned include the iron oxide and the zinc oxide process; wet oxidative processes outlined are the Stretford, Perox, Takahax, Thylox, Fumaks and LoCat; and neutralizaiton or absorption/stripping processes described are the Sulfiban, CYCLASULF, VACASULF and Soda Lye scrubbing processes. 22 figs.

  10. 77 FR 32998 - Foundry Coke From China

    Science.gov (United States)

    2012-06-04

    ... The Commission instituted this review on December 1, 2011 (76 FR 74810) and determined on March 5, 2012 that it would conduct an expedited review (77 FR 15123, March 14, 2012). The Commission... COMMISSION Foundry Coke From China Determination On the basis of the record \\1\\ developed in the subject...

  11. Alternative method for assessing coking coal plasticity

    Energy Technology Data Exchange (ETDEWEB)

    Dzuy Nguyen; Susan Woodhouse; Merrick Mahoney [University of Adelaide (Australia). BHP Billiton Newcastle Technology Centre

    2008-07-15

    Traditional plasticity measurements for coal have a number of limitations associated with the reproducibility of the tests and their use in predicting coking behaviour. This report reviews alternative rheological methods for characterising the plastic behaviour of coking coals. It reviews the application of more fundamental rheological measurements to the coal system as well as reviewing applications of rheology to other physical systems. These systems may act as potential models for the application of fundamental rheological measurements to cokemaking. The systems considered were polymer melts, coal ash melts, lava, bread making and ice cream. These systems were chosen because they exhibit some physically equivalent processes to the processes occurring during cokemaking, eg, the generation of bubbles within a softened system that then resolidifies. A number of recommendations were made; the steady and oscillatory shear squeeze flow techniques be further investigated to determine if the measured rheology characteristics are related to transformations within the coke oven and the characteristics of resultant coke; modification of Gieseler plastometers for more fundamental rheology measurements not be attempted.

  12. Nitrogen Chemistry and Coke Transformation of FCC Coked Catalyst during the Regeneration Process

    Science.gov (United States)

    Shi, Junjun; Guan, Jianyu; Guo, Dawei; Zhang, Jiushun; France, Liam John; Wang, Lefu; Li, Xuehui

    2016-01-01

    Regeneration of the coked catalyst is an important process of fluid catalytic cracking (FCC) in petroleum refining, however, this process will emit environmentally harmful gases such as nitrogen and carbon oxides. Transformation of N and C containing compounds in industrial FCC coke under thermal decomposition was investigated via TPD and TPO to examine the evolved gaseous species and TGA, NMR and XPS to analyse the residual coke fraction. Two distinct regions of gas evolution are observed during TPD for the first time, and they arise from decomposition of aliphatic carbons and aromatic carbons. Three types of N species, pyrrolic N, pyridinic N and quaternary N are identified in the FCC coke, the former one is unstable and tends to be decomposed into pyridinic and quaternary N. Mechanisms of NO, CO and CO2 evolution during TPD are proposed and lattice oxygen is suggested to be an important oxygen resource. Regeneration process indicates that coke-C tends to preferentially oxidise compared with coke-N. Hence, new technology for promoting nitrogen-containing compounds conversion will benefit the in-situ reduction of NO by CO during FCC regeneration. PMID:27270486

  13. Nitrogen Chemistry and Coke Transformation of FCC Coked Catalyst during the Regeneration Process

    Science.gov (United States)

    Shi, Junjun; Guan, Jianyu; Guo, Dawei; Zhang, Jiushun; France, Liam John; Wang, Lefu; Li, Xuehui

    2016-06-01

    Regeneration of the coked catalyst is an important process of fluid catalytic cracking (FCC) in petroleum refining, however, this process will emit environmentally harmful gases such as nitrogen and carbon oxides. Transformation of N and C containing compounds in industrial FCC coke under thermal decomposition was investigated via TPD and TPO to examine the evolved gaseous species and TGA, NMR and XPS to analyse the residual coke fraction. Two distinct regions of gas evolution are observed during TPD for the first time, and they arise from decomposition of aliphatic carbons and aromatic carbons. Three types of N species, pyrrolic N, pyridinic N and quaternary N are identified in the FCC coke, the former one is unstable and tends to be decomposed into pyridinic and quaternary N. Mechanisms of NO, CO and CO2 evolution during TPD are proposed and lattice oxygen is suggested to be an important oxygen resource. Regeneration process indicates that coke-C tends to preferentially oxidise compared with coke-N. Hence, new technology for promoting nitrogen-containing compounds conversion will benefit the in-situ reduction of NO by CO during FCC regeneration.

  14. Nitrogen Chemistry and Coke Transformation of FCC Coked Catalyst during the Regeneration Process.

    Science.gov (United States)

    Shi, Junjun; Guan, Jianyu; Guo, Dawei; Zhang, Jiushun; France, Liam John; Wang, Lefu; Li, Xuehui

    2016-06-08

    Regeneration of the coked catalyst is an important process of fluid catalytic cracking (FCC) in petroleum refining, however, this process will emit environmentally harmful gases such as nitrogen and carbon oxides. Transformation of N and C containing compounds in industrial FCC coke under thermal decomposition was investigated via TPD and TPO to examine the evolved gaseous species and TGA, NMR and XPS to analyse the residual coke fraction. Two distinct regions of gas evolution are observed during TPD for the first time, and they arise from decomposition of aliphatic carbons and aromatic carbons. Three types of N species, pyrrolic N, pyridinic N and quaternary N are identified in the FCC coke, the former one is unstable and tends to be decomposed into pyridinic and quaternary N. Mechanisms of NO, CO and CO2 evolution during TPD are proposed and lattice oxygen is suggested to be an important oxygen resource. Regeneration process indicates that coke-C tends to preferentially oxidise compared with coke-N. Hence, new technology for promoting nitrogen-containing compounds conversion will benefit the in-situ reduction of NO by CO during FCC regeneration.

  15. Coking coals of Mongolia: Distribution and resources

    Science.gov (United States)

    Erdenetsogt, Bat-Orshikh; Jargal, Luvsanchultem

    2016-04-01

    The coal deposits of Mongolia tend to become younger from west to east and can be subdivided into two provinces, twelve basins, and three areas. Main controlling factor of coal rank is the age of coal bearing sequences. Western Mongolian coal-bearing province contains mostly high rank bituminous coal in strata from Late Carboniferous. The basins in southern Mongolia and the western part of central Mongolia have low rank bituminous coal in strata from the Permian. The northern and central Mongolian basins contain mainly Jurassic subbituminous coal, whereas the Eastern Mongolian province has Lower Cretaceous lignite. Mongolian known coking coal reserves are located in western, southern and northern Mongolia and related to Carboniferous, Permian and Jurassic sequences, respectively. Pennsylvanian Nuurstkhotgor coal deposit is located in northwestern Mongolia (in Western Mongolian coal-bearing province). The coals have 1-7.5 crucible swelling number (CSN) and 0-86 G-index. Vitrinite reflectance value (Rmax in oil) varies from 0.7% to 1.2% and sulfur content is low, ranging from 0.3% to 0.6% with an average of 0.4%. Coal reserve is estimated to be 1.0 billion ton, of which half is coking coal. Upper Permian Khurengol deposit is situated in western Mongolia (in Western Mongolian coal-bearing province). CSN and G-index of coal are 8-9 and 54-99, respectively. The coals have Rmax of 1.1 to 1.7% (average 1.4%) and sulfur content of 0.2 to 0.6% (average 0.4%). Coking coal reserve of the deposit is estimated to be 340 million ton. Upper Permian Tavantolgoi, the largest coking coal deposit, lies in southern Mongolia (in South Gobi coal-bearing basin). The coals have CSN of 1 to 7.5 and Rmax of 0.7% to 1.2%. Sulfur content is low, ranging from 0.5% to 0.9%. Coal reserve is estimated to be 6.0 billion ton, of which 2.0 billion ton is accounted as coking coal. Lower-Middle Jurassic Ovoot coal is located in northern Mongolia (in Orkhon-Selenge coal-bearing area). This is one of

  16. REDUCING POWER PRODUCTION COSTS BY UTILIZING PETROLEUM COKE

    Energy Technology Data Exchange (ETDEWEB)

    Kevin C. Galbreath; Donald L. Toman; Christopher J. Zygarlicke

    1999-09-01

    Petroleum coke, a byproduct of the petroleum-refining process, is an attractive primary or supplemental fuel for power production primarily because of a progressive and predictable increase in the production volumes of petroleum coke (1, 2). Petroleum coke is most commonly blended with coal in proportions suitable to meet sulfur emission compliance. Petroleum coke is generally less reactive than coal; therefore, the cofiring of petroleum coke with coal typically improves ignition, flame stability, and carbon loss relative to the combustion of petroleum coke alone. Although petroleum coke is a desirable fuel for producing relatively inexpensive electrical power, concerns about the effects of petroleum coke blending on combustion and pollution control processes exist in the coal-fired utility industry (3). The Energy & Environmental Research Center (EERC) completed a 2-year technical assessment of petroleum coke as a supplemental fuel. A survey questionnaire was sent to seven electric utility companies that are currently cofiring coal and petroleum coke in an effort to solicit specific suggestions on research needs and fuel selections. An example of the letter and survey questionnaire is presented in Appendix A. Interest was expressed by most utilities in evaluating the effects of petroleum coke blending on grindability, combustion reactivity, fouling, slagging, and fly ash emissions control. Unexpectedly, concern over corrosion was not expressed by the utilities contacted. Although all seven utilities responded to the question, only two utilities, Northern States Power Company (NSP) and Ameren, sent fuels to the EERC for evaluation. Both utilities sent subbituminous coals from the Power River Basin and petroleum shot coke samples. Petroleum shot coke is produced unintentionally during operational upsets in the petroleum refining process. This report evaluates the effects of petroleum shot coke blending on grindability, fuel reactivity, fouling/slagging, and

  17. New characterisation tests of the coke behaviour at high temperature

    Energy Technology Data Exchange (ETDEWEB)

    Danloy, G.; Pesneux, P.; Fischbach, J.P. (and others) [CRM, Liege (Belgium)

    2009-07-01

    New laboratory tests have been developed to characterise the coke behaviour at high temperature under conditions similar to those encountered in the blast furnace, especially in terms of gasification degree. The CRM Cokarac test characterises the evolution of coke size distribution under mechanical, chemical and thermal stresses during increasing residence time under gasification conditions prevailing in the blast furnace. Two Corus tests characterise the resistance of coke submitted to the actions of liquid iron and slag. A CPM test characterises the strength of coke after a constant weight loss. The validity of these new tests has been demonstrated by comparing the modifications of the coke grain size and microscopic texture resulting from the tests with those undergone by coke in the blast furnace. The latter have been measured by comparing cokes sampled by a tuyere probe with cokes sampled before charging into the blast furnace. Industrial cokes from a wide variety of sources have been tested. Moreover, to highlight the sensitivity of the new tests and their innovative content, cokes differing greatly by their CRI and CSR indices have been produced in the pilot coke oven plant of CPM. The results of the new tests showed only little correlation with the classical coke characterisation indices (I10, I40) and with the standard CRI-CSR indices, which indicates that they really bring new information on coke properties. The applicability of these new tests on a routine basis has been evaluated in order to allow the ironmaking industry to better characterise coke quality. 15 refs., 90 figs., 23 tabs., 13 apps.

  18. Widespread Occurrence of Chemical Residues in Beehive Matrices from Apiaries Located in Different Landscapes of Western France

    Science.gov (United States)

    Lambert, Olivier; Piroux, Mélanie; Puyo, Sophie; Thorin, Chantal; L'Hostis, Monique; Wiest, Laure; Buleté, Audrey; Delbac, Frédéric; Pouliquen, Hervé

    2013-01-01

    Background The honey bee, Apis mellifera, is frequently used as a sentinel to monitor environmental pollution. In parallel, general weakening and unprecedented colony losses have been reported in Europe and the USA, and many factors are suspected to play a central role in these problems, including infection by pathogens, nutritional stress and pesticide poisoning. Honey bee, honey and pollen samples collected from eighteen apiaries of western France from four different landscape contexts during four different periods in 2008 and in 2009 were analyzed to evaluate the presence of pesticides and veterinary drug residues. Methodology/Findings A multi-residue analysis of 80 compounds was performed using a modified QuEChERS method, followed by GC-ToF and LC−MS/MS. The analysis revealed that 95.7%, 72.3% and 58.6% of the honey, honey bee and pollen samples, respectively, were contaminated by at least one compound. The frequency of detection was higher in the honey samples (n = 28) than in the pollen (n = 23) or honey bee (n = 20) samples, but the highest concentrations were found in pollen. Although most compounds were rarely found, some of the contaminants reached high concentrations that might lead to adverse effects on bee health. The three most frequent residues were the widely used fungicide carbendazim and two acaricides, amitraz and coumaphos, that are used by beekeepers to control Varroa destructor. Apiaries in rural-cultivated landscapes were more contaminated than those in other landscape contexts, but the differences were not significant. The contamination of the different matrices was shown to be higher in early spring than in all other periods. Conclusions/Significance Honey bees, honeys and pollens are appropriate sentinels for monitoring pesticide and veterinary drug environmental pollution. This study revealed the widespread occurrence of multiple residues in beehive matrices and suggests a potential issue with the effects of these residues

  19. Widespread occurrence of chemical residues in beehive matrices from apiaries located in different landscapes of Western France.

    Directory of Open Access Journals (Sweden)

    Olivier Lambert

    Full Text Available BACKGROUND: The honey bee, Apis mellifera, is frequently used as a sentinel to monitor environmental pollution. In parallel, general weakening and unprecedented colony losses have been reported in Europe and the USA, and many factors are suspected to play a central role in these problems, including infection by pathogens, nutritional stress and pesticide poisoning. Honey bee, honey and pollen samples collected from eighteen apiaries of western France from four different landscape contexts during four different periods in 2008 and in 2009 were analyzed to evaluate the presence of pesticides and veterinary drug residues. METHODOLOGY/FINDINGS: A multi-residue analysis of 80 compounds was performed using a modified QuEChERS method, followed by GC-ToF and LC-MS/MS. The analysis revealed that 95.7%, 72.3% and 58.6% of the honey, honey bee and pollen samples, respectively, were contaminated by at least one compound. The frequency of detection was higher in the honey samples (n = 28 than in the pollen (n = 23 or honey bee (n = 20 samples, but the highest concentrations were found in pollen. Although most compounds were rarely found, some of the contaminants reached high concentrations that might lead to adverse effects on bee health. The three most frequent residues were the widely used fungicide carbendazim and two acaricides, amitraz and coumaphos, that are used by beekeepers to control Varroa destructor. Apiaries in rural-cultivated landscapes were more contaminated than those in other landscape contexts, but the differences were not significant. The contamination of the different matrices was shown to be higher in early spring than in all other periods. CONCLUSIONS/SIGNIFICANCE: Honey bees, honeys and pollens are appropriate sentinels for monitoring pesticide and veterinary drug environmental pollution. This study revealed the widespread occurrence of multiple residues in beehive matrices and suggests a potential issue with the effects

  20. Coking coal of Checua Lenguazaque area

    International Nuclear Information System (INIS)

    In this report a summary of the main characteristics of the coal of the area of Checua-Samaca is presented. Using the main works carried out on this area, the most important geologic, physical-chemical, technological and petrographic aspects are compiled that are considered essential to carry out a technical evaluation of these coal and all the analyses they take to conclude that in this area, bituminous coal are presented with very good coking properties, on the other hand, it is demonstrated by the use that is given to the coal extracted by the small existent mining. However, keeping in mind the demands of the international market of the coking coal, it becomes necessary to improve the existent geologic information to be able to make reliable stratigraphic correlations

  1. The Corex process - ironmaking without coke

    Energy Technology Data Exchange (ETDEWEB)

    Flickenschild, J.; Hauk, R. (Deutsche Voest-Alpine Industrieanlagenbau GmbH Duesseldorf (Germany, F.R.))

    1990-12-01

    The high cost of coke making and the environmental problems involved as well as the increasing price of natural gas for DRI production were the reasons for the development of the COREX process for the production of hot metal based on a wide range of ordinary steam coals. After the successful operation of a CORX pilot plant, the first commercial plant was built at Iscor in Pretoria, South Africa, and is now in full operation. 3 refs., 9 figs., 17 tabs.

  2. BRAND COMMITMENTAS ACOMPONENTOFBRAND EQUITY- ARESEARCH CONCERNING COKE

    OpenAIRE

    Ridvan Karalar; Hakan Kiraci

    2007-01-01

    Brand equity is affected by many factors such as brand commitment, brand awareness, perceived quality and brand association. One of them brand royalty is important component of brand equity. In this research, it was investigated consumers’ brand preferences, brand royalty level and brand commitment factors on brands on coke product placed beverage sector. Asurvey carried out on 500 students at Dumlupinar University Economics and Administrative Sciences Faculty. The participants of this stud...

  3. Petroleum coke slags :characterization and dissolution

    OpenAIRE

    Lu, Jun

    1997-01-01

    Slags are crystalline to vitreous by-product materials generated in many high temperature industrial processes. This study presents a general technique for the identification of the phases present in petroleum coke gasification slags. documents the phase assemblages and textures, and finally determines the dissolution of vanadium from these slags as part of the considerations of potential resource reclamation. The general identification procedure utilizes (1) recognition of separa...

  4. Mortality in retired coke oven plant workers.

    OpenAIRE

    Chau, N.; Bertrand, J P; Mur, J M; Figueredo, A; Patris, A.; Moulin, J J; Pham, Q T

    1993-01-01

    A previous study on 536 retired coke oven plant workers in Lorraine Collieries (France) reported an excess of deaths from lung cancer (standardised mortality ratio (SMR) = 251) compared with the French male population. Occupational exposures during working life were retraced for each subject, but the number of deaths during the observation period (1963-82) was small, and smoking habits were known only for dead subjects. In 1988, the cohort was re-examined (182 deaths occurred between 1963 and...

  5. A static approach towards coke collapse modelling in blast furnace

    Energy Technology Data Exchange (ETDEWEB)

    Nag, S.; Basu, S. Yu, A.B.

    2009-10-15

    Burden distribution control in a blast furnace has a close relationship with wind acceptance and gas utilisation. Quantification of radial distribution of ore and coke is important for proper control of blast furnace operation. Charging of metallic burden over a layer of coke causes a portion of the coke layer to get dislodged from its original position, similar to the situation observed when a heavy material is dropped on a bed of lighter particles. This phenomenon, designated 'coke collapse', significantly changes the ore/coke distribution in the radial direction and thus affects the permeability of the furnace shaft. In the present work a mathematical model for quantifying the amount of coke collapse has been proposed on the basis of 'stability of slope theory'. The calculation from this model has been compared with the results from experiments in simplified physical models. Predictions of the mathematical model are in good agreement with experimental results.

  6. Study on combustion characteristics of petroleum coke residual oil slurry

    Energy Technology Data Exchange (ETDEWEB)

    Shou Weiyi; Xu Xiaoming; Cao Xinyu [and others

    1997-07-01

    Petroleum coke residual oil slurry (POS) is one of prospect substitute of oil burned in many industrial boilers and utilities in China. It is a mixture of pulverized petroleum coke, residual oil and slurry oil. We carried out a series of experiments to study its ignition and combustion mechanism. Experimental results show that the ignition temperature of petroleum coke is higher than normal anthracite and meager coal, and it is difficult to be burned in oil-fired furnace directly. The petroleum coke`s combustion property is improved greatly after mixing with residual oil and slurry oil. The combustion process of POS can be divided into three phases: preheating, kindling and homogenous combustion, burning of the petroleum coke residue. The combustion condition of POS is close to bituminous and coal-oil-mixture (COM).

  7. Toxicological assessment of green petroleum coke.

    Science.gov (United States)

    McKee, Richard H; Herron, Deborah; Beatty, Patrick; Podhasky, Paula; Hoffman, Gary M; Swigert, James; Lee, Carol; Wong, Diana

    2014-01-01

    Green petroleum coke is primarily inorganic carbon with some entrained volatile hydrocarbon material. As part of the petroleum industry response to the high production volume challenge program, the potential for reproductive effects was assessed in a subchronic toxicity/reproductive toxicity screening test in rats (OECD 421). The repeated-dose portion of the study provided evidence for dust accumulation and inflammatory responses in rats exposed to 100 and 300 mg/m(3) but there were no effects at 30 mg/m(3). In the reproductive toxicity screen, the frequency of successful matings was reduced in the high exposure group (300 mg/m(3)) and was not significantly different from control values but was outside the historical experience of the laboratory. The postnatal observations (external macroscopic examination, body weight, and survival) did not indicate any treatment-related differences. Additional tests conducted to assess the potential hazards to aquatic (fish, invertebrates, and algae) and soil dwelling organisms (earthworms and vascular plants) showed few effects at the maximum loading rates of 1000 mg coke/L in aquatic studies and 1000 mg coke/kg soil in terrestrial studies. The only statistically significant finding was an inhibition of algal growth measured as either biomass or growth rate. PMID:24179031

  8. Urinary 1-hydroxypyrene concentrations in coke oven workers

    OpenAIRE

    Wu, M T; Mao, I F; Ho, C.K.; Wypij, D; Lu, P. L.; Smith, T. J.; Chen, M. L.; Christiani, D C

    1998-01-01

    OBJECTIVES: To investigate the relation of individual occupational exposure to total particulates benzene soluble fraction (BSF) of ambient air with urinary 1-hydroxypyrene (1-OHP) concentrations among coke oven workers in Taiwan. METHODS: 80 coke oven workers and 50 referents were monitored individually for the BSF of breathing zone air over three consecutive days. Exposures were categorised as high, medium, or low among coke oven workers based on exposure situations. The high exposure...

  9. 76 FR 77020 - Agency Information Collection Activities; Submission for OMB Review; Comment Request; Coke Oven...

    Science.gov (United States)

    2011-12-09

    ... Information Collection Activities; Submission for OMB Review; Comment Request; Coke Oven Emissions ACTION... Administration (OSHA) sponsored information collection request (ICR) titled, ``Coke Oven Emissions,'' to the...: The purpose of Coke Oven Emissions Standard and its information collection requirements, codified...

  10. Visualization of coke state in hydraulic decoking process

    Science.gov (United States)

    Guo, Qian; Tong, Xinglin; Deng, Chengwei; Zhang, Cui; Huang, Di; Chen, Liang; Xiong, Jiaguo

    2016-05-01

    The relationship model of the sound signal and the coke state can be established through multiple test and comparison of the noise signal and the coke operation. By collecting data, we summarize the main frequency power fluctuation range of the sound signal in kinds of state, and extract the nearest 5 decision results for reference. The weighted value of each result according to the update time has gradually increased. On the basis of that, we developed visualization software, real-time reflect out coke coking tower state. Animation refresh rate is second level, and the vertical height can be accurate to 0.1m.

  11. Mortality of coke plant workers in The Netherlands.

    OpenAIRE

    Swaen, G M; Slangen, J J; Volovics, A.; Hayes, R B; Scheffers, T; Sturmans, F.

    1991-01-01

    During the production of coke, large quantities of coke oven gas are emitted. People who work on the top or on the sides of coke ovens are exposed to this oven gas, which contains a range of carcinogenic chemicals. To investigate the cancer risks under these work conditions, a retrospective study was undertaken. In total 11,399 former workers were enrolled in the study. Of these, 5639 had worked in the coke plant for at least six months between 1945 and 1969. The other 5740 had worked in anot...

  12. An installation for the intake of coke and the outlet of gases during unloading of coke furnaces

    Energy Technology Data Exchange (ETDEWEB)

    Marapulets, G.N.; Butko, A.V.; Likhogub, Ye.P.; Nayman, A.M.; Pevnyy, V.P.; Yatsura, V.A.; Zinchenko, V.I.

    1982-01-01

    An installation is proposed for receiving coke and the outlet of gases during unloading of coke furnaces, which includes a coke directing dolly, a basket with a dust trapping hood attached to it, a gas outlet, telescopic branchpipe, whose fixed part is attached to the upper part of the hood and a collector for outlet of the gas in the device for purification located parallel to the battery of coking furnaces. To increase the reliability and effectiveness of outlet of the gases, the gas outlet branchpipe is installed horizontally and the telescopic branchpipe is connected by means of levers and linkages to the basket of the coke guide dolly. The dust trapping hood is equipped with an additional, horizontal, gas outlet branchpipe and the gas outlet branchpipes are installed at a distance equal to the distance between the coking furnaces.

  13. Full scale treatment of phenolic coke coking waste water under unsteady conditions

    Energy Technology Data Exchange (ETDEWEB)

    Suschka, Jan [Institute for Ecology of Industrial Areas, Katowice (Poland); Morel, Jacek; Mierzwinski, Stanislaw; Januszek, Ryszard [Coke Plant Przyjazn, Dabrowa Gornicza (Poland)

    1993-12-31

    Phenolic waste water from the largest coke coking plant in Poland is treated at a full technical scale. From the very beginning it became evident that very high qualitative variations in short and long periods were to be expected. For this purpose, the biological treatment plant based on activated sludge is protected through preliminary physical-chemical treatment and the results are secured by a final chemical stage of treatment. Nevertheless, improvements in the performance of the treatment plant have been found necessary to introduce. In this work, the experience gained over the last five years is described and developed improvements were presented. 3 refs., 9 figs., 1 tab.

  14. Coal Beneficiation Technology for Coking & Non-Coking Coal Meant For Steel and Thermal Power Plants

    OpenAIRE

    Manoj Kumar Sharma; Gohil Priyank; Nikita Sharma

    2015-01-01

    There are 21 coking coal washeries in production both in private and public sectors. Production of clean coal in these washeries during 1989-90 was 12 million tonne and it is expected to go up to 37 million, tonne during 2015-16. Planning Commission has taken the decision that non-coking coal meant for Thermal Power Plants situated far away from feeding coalfield, should be beneficiated. Coal Washing is a process of separation mainly based on difference in Specific Gravity of Coal and associa...

  15. Combustion kinetics of the coke on deactivated dehydrogenation catalysts

    NARCIS (Netherlands)

    Luo, Sha; He, Songbo; Li, XianRu; Li, Jingqiu; Bi, Wenjun; Sun, Chenglin

    2015-01-01

    The coke combustion kinetics on the deactivated catalysts for long chain paraffin dehydrogenation was studied by the thermogravimetry and differential thermogravimetry (TG–DTG) technique. The amount and H/C mole ratio of the coke were determined by the TG and elemental analysis. And the comprehensiv

  16. 29 CFR 1926.1129 - Coke oven emissions.

    Science.gov (United States)

    2010-07-01

    ... 29 Labor 8 2010-07-01 2010-07-01 false Coke oven emissions. 1926.1129 Section 1926.1129 Labor... (CONTINUED) SAFETY AND HEALTH REGULATIONS FOR CONSTRUCTION Toxic and Hazardous Substances § 1926.1129 Coke oven emissions. Note: The requirements applicable to construction work under this section are...

  17. CARCINOGEN ASSESSMENT OF COKE OVEN EMISSIONS (REVISED DRAFT)

    Science.gov (United States)

    Coke oven workers in Allegheny County, Pennsylvania and at 10 non-Allegheny County coke plants in the United States and Canada were found to be at an excess risk of mortality from cancer of all sites and from cancer of the lungs, bronchus, and trachea, kidney, and prostate. An im...

  18. Wear resistance of coke-crushing hammers

    OpenAIRE

    Zupanič, Franc

    2015-01-01

    This work investigated several methods for improving the wear resistance of the 42CrMo4 tool steel used for coke-crushing hammers. The methods embraced heat treatment for obtaining different combinations of strength and ductility of the bulk steel, and surface-engineering processes comprising TiN thin-film deposition using magnetron-sputtering, nitriding and WC/Ni weld deposit surfaced by gas metal arc (GMA) method. The wear-resistance was tested under industrial conditions. Oil quenching and...

  19. Carbon Tubular Morphologies in Blast Furnace Coke

    OpenAIRE

    Stanislav S. Gornostayev; Jouko J. Härkki

    2008-01-01

    The paper reports on the first occurrence of microscale carbon tubular morphologies (CMTs) in a blast furnace (BF) coke. The CMTs were probably formed as a result of the conversion of solid disordered carbon via liquid phase metal particles involving a gas phase containing a substantial amount of N 2 and O 2 . The presence of CMTs may lie behind the generation of the smallest fraction of fines in BF exhaust dust. If the amount of CMTs present in the BF exhausts gases at any particular metallu...

  20. Carbon Tubular Morphologies in Blast Furnace Coke

    Directory of Open Access Journals (Sweden)

    Stanislav S. Gornostayev

    2008-01-01

    Full Text Available The paper reports on the first occurrence of microscale carbon tubular morphologies (CMTs in a blast furnace (BF coke. The CMTs were probably formed as a result of the conversion of solid disordered carbon via liquid phase metal particles involving a gas phase containing a substantial amount of N2 and O2. The presence of CMTs may lie behind the generation of the smallest fraction of fines in BF exhaust dust. If the amount of CMTs present in the BF exhausts gases at any particular metallurgical site proves to be substantial, it could become a subject of environmental concern.

  1. Coke deactivation of catalysts for hydroprocessing of heavy petroleum feedstocks

    International Nuclear Information System (INIS)

    Harwell's principal contribution to the study of the role of coke in the deactivation of catalysts for hydroprocessing of heavy petroleum feedstocks has been the development and application of nuclear microprobe methods to measure the distributions of hydrogen, carbon, nitrogen and other elements in coked catalyst pellets. Nuclear microprobe methods have been developed that allow the measurement of the distribution of carbon, hydrogen, nitrogen and heavier elements in coked catalyst pellets. At present analysis by both deuteron and helium-4 ion beams is necessary to cover the complete range of elements. The potential of using helium-3 irradiation alone to measure all elements is as yet unrealised. Applications have included studies of the variability of profiles in batches of used pellets, investigation of interrelationships between coke components and limited kinetic studies. Many of these applications have proved to be successful and nuclear microprobe methods should continue to be exploited studies of catalyst coking. (au)

  2. Effect of physical disturbance on the structure of needle coke

    Science.gov (United States)

    Zhao, Shi-Gui; Wang, Bao-Cheng; Sun, Quan

    2010-10-01

    Through different preparation technology, this paper reports that the needle coke is prepared with coal-tar pitch under the effect of magnetic field and ultrasonic cavitation. It studies the effect of physical disturbance on the structure of needle coke. The structure of needle coke is characterized by scanning electron microscope and x-ray diffractometer, and the influence mechanism is analysed. Results showed that the structure and property of needle coke could be effectively improved by magnetic field and ultrasonic cavitations, such as degree of order, degree of graphitization and crystallization. Comparatively speaking, the effect of magnetic field was greater. The graphitization degree of needle coke prepared under the effect of magnetic field is up to 45.35%.

  3. Soluções conservantes em sorvetão pós-colheita Preservative solutions in beehive ginger post-harvest

    Directory of Open Access Journals (Sweden)

    Maria Herbênia Lima Cruz Santos

    2008-11-01

    Full Text Available O objetivo deste trabalho foi estudar alguns aspectos da fisiologia pós-colheita de inflorescências de sorvetão cultivadas no Submédio São Francisco. Hastes florais recém-colhidas foram submetidas a diferentes tratamentos (água destilada; 75mg L-1 de nitrato de prata - AgNO3; 1000mg L-1 de cloreto de cobalto - CoCl2; 5mg L-1 de ácido giberélico - GA3 - Progibb® e 10mg L-1 de 6-Benzilaminopurina - BAP, em ambiente com temperatura e umidade controlada por 15 dias. A vida pós-colheita foi acompanhada a partir da escala de notas, da massa da matéria fresca e do consumo da solução conservante. O tratamento com AgNO3 em hastes de sorvetão, foi o mais eficiente na manutenção da vida de vaso de sorvetão, porém, devido a sua toxidez, recomenda-se o uso de GA3.The objective of this research was to study some physiological post-harvest aspect of beehive ginger inflorescences grown in the lower middle San Francisco river basin. Flower stems just harvested were submitted to different treatments (distilled water; 75mg L-1 of silver nitrate - AgNO3; 1000mg L-1 of cobalt chloride - CoCl2; 5mg L-1 de GA3 - Progibb® and 10mg L-1 of 6-benzylamino purine - BAP, in an environment with controlled temperature and humidity, for 15 days. The post-harvest life was monitored from grading scale, fresh weight, and consumption of the preservative solution. The treatment with silver nitrate was the most efficient to keep the vase life of beehive ginger, however due to its toxity, the use of GA3 is recommended.

  4. Combination of beehive matrices analysis and ant biodiversity to study heavy metal pollution impact in a post-mining area (Sardinia, Italy).

    Science.gov (United States)

    Satta, Alberto; Verdinelli, Marcello; Ruiu, Luca; Buffa, Franco; Salis, Severyn; Sassu, Antonio; Floris, Ignazio

    2012-11-01

    Mining activities represent a major source of environment contamination. The aim of this study was to evaluate the use of bees and ants as bioindicators to detect the heavy metal impact in post-mining areas. A biomonitoring programme involving a combination of honeybee hive matrices analysis and ant biodiversity survey was conducted over a 3-year period. The experimental design involved three monitoring stations where repeated sampling activities focused on chemical detection of cadmium (Cd), chrome (Cr) and lead (Pb) from different matrices, both from hosted beehives (foraging bees, honey and pollen) and from the surrounding environment (stream water and soil). At the same time, ant biodiversity (number and abundance of species) was determined through a monitoring programme based on the use of pitfall traps placed in different habitats inside each mining site. The heavy metal content detected in stream water from the control station was always below the analytical limit of quantification. In the case of soil, the content of Cd and Pb from the control was lower than that of mining sites. The mean heavy metal concentrations in beehive matrices from mining sites were mainly higher than the control, and as a result of regression and discriminant analysis, forager bee sampling was an efficient environmental pollution bioindicator. Ant collection and identification highlighted a wide species variety with differences among habitats mostly associated with vegetation features. A lower variability was observed in the polluted landfill characterised by lack of vegetation. Combined biomonitoring with forager bees and ants represents a reliable tool for heavy metal environmental impact studies.

  5. Combination of beehive matrices analysis and ant biodiversity to study heavy metal pollution impact in a post-mining area (Sardinia, Italy).

    Science.gov (United States)

    Satta, Alberto; Verdinelli, Marcello; Ruiu, Luca; Buffa, Franco; Salis, Severyn; Sassu, Antonio; Floris, Ignazio

    2012-11-01

    Mining activities represent a major source of environment contamination. The aim of this study was to evaluate the use of bees and ants as bioindicators to detect the heavy metal impact in post-mining areas. A biomonitoring programme involving a combination of honeybee hive matrices analysis and ant biodiversity survey was conducted over a 3-year period. The experimental design involved three monitoring stations where repeated sampling activities focused on chemical detection of cadmium (Cd), chrome (Cr) and lead (Pb) from different matrices, both from hosted beehives (foraging bees, honey and pollen) and from the surrounding environment (stream water and soil). At the same time, ant biodiversity (number and abundance of species) was determined through a monitoring programme based on the use of pitfall traps placed in different habitats inside each mining site. The heavy metal content detected in stream water from the control station was always below the analytical limit of quantification. In the case of soil, the content of Cd and Pb from the control was lower than that of mining sites. The mean heavy metal concentrations in beehive matrices from mining sites were mainly higher than the control, and as a result of regression and discriminant analysis, forager bee sampling was an efficient environmental pollution bioindicator. Ant collection and identification highlighted a wide species variety with differences among habitats mostly associated with vegetation features. A lower variability was observed in the polluted landfill characterised by lack of vegetation. Combined biomonitoring with forager bees and ants represents a reliable tool for heavy metal environmental impact studies. PMID:22532121

  6. Effects of Additives on Sulfur Transformation, Crystallite Structure and Properties of Coke during Coking of High-sulfur Coal

    Institute of Scientific and Technical Information of China (English)

    Sheng-fu ZHANG; Liang-ying WEN; Kun WANG; Chong ZOU; Jian XU

    2015-01-01

    High-sulfur coal, as an alternative coal source, has a relatively high proportion in coal reserves. However, the feature of high sulfur content, which can cause environmental pollution and poor quality of molten iron, restrains its utilization in coking industry. Coking experiments of high-sulfur coal with Fe2O3, La2O3 and CaO as additives were carried out in order to ifx the sulfur in coke. The effects of additives on sulfur distribution, crystallite structure, surface morphology and properties of coke were inves-tigated. The results indicate that CaO can be used as sulfur-ifxing agent in coking process, and CaS is the main mineralogical phase of the sulfur-contained mineral constituents in coke. Fe2O3 and La2O3 facilitate the conversion of CaO to CaS. The additives mainly inlfuence the crystallite height and the average interlayer spacingd002 of coke. The addition of La2O3 increases the value of the crys-tallite heightwhile the addition of CaO and Fe2O3 decreases it. CaO leads the pores of coke to increase with its physical action and agglomerating characteristic. Fe2O3and C can form (Fe,C), resulting in the pulverization and erosion of the pore wall. La2O3 makes the coke surface become more compact and thinner. The reactivity of coke increases with the decrease of crystallite height and crystallite layer number.

  7. Coke: Capacity Expansion and Production Closure / Restriction Go Side by Side

    Institute of Scientific and Technical Information of China (English)

    2007-01-01

    @@ With the "self production restriction" and the "closure of small coking enterprises" in the coking sector and the rapid demand increase in downstream metallurgical and chemical sectors, a basic supply/demand balance of coke was achieved in 2006 and the price of coke also made a gradual pickup from the second quarter of 2007.

  8. Effect of nut coke on the performance of the ironmaking blast furnace

    NARCIS (Netherlands)

    Song, Q.

    2013-01-01

    The blast furnace consumes a large amount of high quality metallurgy coke (size 35-80 mm) in addition to ore in the form of pellets and sinter. This coke is the coarse fraction, derived from the coke plant. The fine fraction (8 -35 mm), arise after sieving, named nut coke, can’t be directly used in

  9. Coke Oven Gas Based Methanol Production Capacity Reached 1.2 Mt/a in China

    Institute of Scientific and Technical Information of China (English)

    2008-01-01

    @@ Coke oven gas is one of the main byproducts of coke chemicals industry.One ton of coke formed can generate 430 m3of coke oven gas.Adoption of appropriate chemical processing method can convert methane contained in the coke oven gas into CO that can be further converted into methanol.It is learned that currently China has constructed and commissioned ten projects for manufacture of methanol fromcoke oven gas with the total production capacity reaching 1.2 Mt/a methanol.More than twenty coke gas-to-methanol units are under construction or in the stage of project design with their overall production capacity reaching nearly 3.0 Mt/a methanol.Relevant experts have indicated that the enterprises provided with coke production lines are capable of constructing coke gas-to-methanol projects to realize coproduction of coke and methanol while utilizing their own coke gas resources.

  10. Research on the evolvement of morphology of coking coal during the coking process.

    Science.gov (United States)

    Zhong, Xiangyun; Wu, Shiyong; Liu, Yang; Zhao, Zhenning; Zhang, Yaru; Bai, Jinfeng; Xu, Jun; Xi, Bai

    2013-12-01

    The evolvement of morphology and structure of the coal with different metamorphic degrees during coking process in the vertical furnace was investigated by infrared Image detector. Moreover, the temperature distribution in the radial direction and the crack formation were also studied in heating process. The results show that the amount of crack and the shrinkage level of char decrease with the coal rank rising. In addition, the initial temperature of crack formation for char increases with the coal rank rising.

  11. The effect of blast furnace coke quality on the possibility of its use

    OpenAIRE

    Konstanciak, A.

    2013-01-01

    In the paper behavior of the blast-furnace coke in the high temperature was presented. Comparative analysis of the chemical composition of the blast-furnace coke and the heat treatment of it were done. Coefficients M10 and M40 with the thermo-abrasiveness for chosen cokes were compared. The influence of ash content of the coke on the blast-furnace bed permeability was defined. Usefulness of the coke to blast-furnace process was also defined.

  12. Study and Application of Sealing Material for Coke Oven Chamber

    Institute of Scientific and Technical Information of China (English)

    GAN Feifang; TAI Li

    2005-01-01

    A kind of dry refractory sealing material has been developed to repair the fine cracks in coke oven chamber. With silica sand as the main raw material, the sealing material is blown into coke oven chamber by compressed air while being applied, and bonded to brick surface or filled in fine cracks of chamber under right pressure. The physical properties of the material are similar to those of silica bricks during its application. So it can be adapted to conditions of coke oven and has good service life. The study and application results of the sealing material are described in this paper.

  13. THE INERT HOLDING RATIO OF COAL ANDTHE STRENGTH OF COKE

    Institute of Scientific and Technical Information of China (English)

    陈鹏

    1996-01-01

    The variation regularity of coke strength was investigated in terms of the genetic fac-tors and petrographic parameters of coal in collaboration with the technical properties of coal. Aconcept of inert holding ratio of coal was proposed. There is an optimal inert holding ratio for dif-ferent ranks of coals for making coke with highest combined strength. The additive property of in-ert holding ratio under normal conditions was demonstrated with actual examples of coal blending.Thus it is possible to predict the combined strength of coke through reflectance, content of inertcomponents and caking index (Ro, max-I-G) diagram system.

  14. RESEARCH ON THE QUALITY PRICE RATIO OF COKING COAL

    Institute of Scientific and Technical Information of China (English)

    陶树人; 王永君

    1994-01-01

    If assortment price parity of Clean coling coal and its quallty price difference is nonreasortable, it doesn't guide in improving the qualiry metaljurgical eoking coal and may be influence the economic benefit of metallurgical enterprises. This paper propose the principles and mathematic model for determination assortment parity of ciean cokingcoal and its quality difference of ash content in clean coking coa in order to urge wasberies into producing superior clean coking coal which is under condition of consideration both intorest waskcries and interest metallurgical industry. It canbe used as a method in theory to make price stra,iegics under condition of socialism maket economic for washeries of clean coking coal

  15. Causes Leading to Formation of Shot Cokes and Measures for Its Prevention in Super Viscous Oil Delayed Coking Unit

    Institute of Scientific and Technical Information of China (English)

    Chen Chunmao; Zhang Feng; Yan Guangxu; Guo Shaohui

    2007-01-01

    Shot cokes are frequently formed in the delayed coking unit treating the super viscous oil at PetroChina's Liaohe Petrochemical Company. Considerable work has been carried out to avoid the formation of shot cokes. The test results obtained have shown that the property of super viscous oil has played a key role in the formation of shot cokes. After adjusting and optimizing the process indices the operating regime of the delayed coking unit at a throughput of 118t/h of the super viscous oil is specified as follows: a reaction temperature of 498-502℃, a reaction pressure of 0.17-0.25 MPa, a recycle ratio of 0.5-0.6 and a fractionation tower bottom temperature of 355-365 ℃. In the meantime,the delayed coking process has adopted measures to enhance pre-fractionation of the feedstock to rationally remove light fractions and maintain a steady gas velocity in order to avoid the formation of shot cokes.

  16. TGA and DMA studies of blends from very good coking Zofiowka coal and various carbon additives: Weakly coking coals, industrial coke and carbonized plants

    Energy Technology Data Exchange (ETDEWEB)

    Krzesinska, M. [Centre of Polymer and Carbon Materials, Polish Academy of Sciences, Marii Curie- Sklodowskiej 34, PL-41819 Zabrze (Poland); Silesian Technical University, Department of Electron Technology, Institute of Physics, Krzywoustego 2, PL-44100 Gliwice (Poland); Szeluga, U.; Majewska, J.; Pusz, S.; Czajkowska, S. [Centre of Polymer and Carbon Materials, Polish Academy of Sciences, Marii Curie- Sklodowskiej 34, PL-41819 Zabrze (Poland); Smedowski, L. [Silesian Technical University, Department of Electron Technology, Institute of Physics, Krzywoustego 2, PL-44100 Gliwice (Poland); Kwiecinska, B. [AGH-University of Science and Technology, Aleja Mickiewicza 30, PL-30059 Krakow (Poland)

    2010-04-01

    The aim of this work is to study the effects of various carbon additives, blended with very good coking coal, on the thermal decomposition of the blends. The blends possess fixed content (50 wt.%) of very good coking coal from the Zofiowka Mine. The remaining components of the blends are worse coking coals collected from the Janina, Krupinski, Szczyglowice, Jas-Mos mines (coals of carbon content ranging from 73 up to 92 wt.%), and very porous carbons: coke (from the coking plant Zdzieszowice), as well as woody stems of bamboo and yucca carbonized at 400 C. The content of porous carbon in a blend does not exceed 20 wt.%. Thermogravimetric analysis (TGA) and dynamic mechanical analysis (DMA) are used in the study. The weight loss during low-temperature pyrolysis (< 600 C), and storage/loss elastic moduli measured as a function of the increasing temperature are related to the kind and concentration of additives. The temperature dependences of elastic moduli determined for binary coal blends differ clearly from those of ternary coal blends. The consumption of energy during the interaction of the components in binary blends was found to be distinctly bigger than the one observed for ternary blends. Non-softening additives such as carbonized plants and low rank coal, containing many functional groups, diminish both moduli of the blends distinctly. However, the addition of coke does not reduce the value of the elastic moduli but increases the width of the maximum occurring in the temperature dependence of the moduli. The influence of the coke additive on rheological properties of the blends, different in comparison with the remaining additives studied, was assigned with different number of functional groups and radicals. (author)

  17. Methanol gasoline blend from petroleum coke sources

    Energy Technology Data Exchange (ETDEWEB)

    Netzer, David [Consulting Chemical Engineer (United States); Wallsgrove, Chris [Process Engineering Manager (United States)

    2011-07-01

    In Alberta, a large amount of petroleum coke is produced as a byproduct from processes relating to bitumen upgrading and refining. Unfortunately, there is little to no market for this product in the province. This presentation addresses concerns relating to the concept of converting the otherwise wasted petcoke into methanol and using it as a blending component in gasoline. The presentation tackles issues relating to environmental impact, economics, renewability, toxicity, safety, and vehicle design by analyzing and comparing the proposed methanol/gasoline (M-10) to that of an ethanol/gasoline (E-10). The presentation covers analysis of the CO2 emissions, an analysis of the finances, and a number of scenarios involving the improper use or accidental spillage of M-10. Through the comparison of methanol/gasoline and ethanol/gasoline, the presentation demonstrated that converting the petcoke byproduct into methanol for use as a gasoline blend is a viable option.

  18. Coke Formation During Hydrocarbons Pyrolysis. Part One: Steam Cracking Formation de coke pendant la pyrolise des hydrocarbures. Première partie : vapocraquage

    OpenAIRE

    Weill J.; Broutin P.; Billaud F.; Gueret C.

    2006-01-01

    Thermal cracking is always accompanied by coke formation, which becomes deposited on the wall and limits heat transfers in the reactor while increasing pressure drops and possibly even plugging up the reactor. This review article covers undesirable coking operations in steam craking reactors. These coking reactions may take place in the gas phase and/or on the surface of the reactor, with coke being produced during pyrolysis by a complex mechanism that breaks down into a catalytic sequence an...

  19. Prediction of coking dynamics for wet coal charge

    Directory of Open Access Journals (Sweden)

    Kardaś Dariusz

    2015-09-01

    Full Text Available A one-dimensional transient mathematical model describing thermal and flow phenomena during coal coking in an oven chamber was studied in the paper. It also accounts for heat conduction in the ceramic oven wall when assuming a constant temperature at the heating channel side. The model was solved numerically using partly implicit methods for gas flow and heat transfer problems. The histories of temperature, gas evolution and internal pressure were presented and analysed. The theoretical predictions of temperature change in the centre plane of the coke oven were compared with industrialscale measurements. Both, the experimental data and obtained numerical results show that moisture content determines the coking process dynamics, lagging the temperature increase above the water steam evaporation temperature and in consequence the total coking time. The phenomenon of internal pressure generation in the context of overlapping effects of simultaneously occurring coal transitions - devolatilisation and coal permeability decrease under plastic stage - was also discussed.

  20. [Health risk assessment of coke oven PAHs emissions].

    Science.gov (United States)

    Bo, Xin; Wang, Gang; Wen, Rou; Zhao, Chun-Li; Wu, Tie; Li, Shi-Bei

    2014-07-01

    Polycyclic aromatic hydrocarbons (PAHs) produced by coke oven are with strong toxicity and carcinogenicity. Taken typical coke oven of iron and steel enterprises as the case study, the dispersion and migration of 13 kinds of PAHs emitted from coke oven were analyzed using AERMOD dispersion model, the carcinogenic and non-carcinogenic risks at the receptors within the modeling domain were evaluated using BREEZE Risk Analyst and the Human Health Risk Assessment Protocol for Hazardous Waste Combustion (HHRAP) was followed, the health risks caused by PAHs emission from coke oven were quantitatively evaluated. The results indicated that attention should be paid to the non-carcinogenic risk of naphthalene emission (the maximum value was 0.97). The carcinogenic risks of each single pollutant were all below 1.0E-06, while the maximum value of total carcinogenic risk was 2.65E-06, which may have some influence on the health of local residents. PMID:25244863

  1. RESIDUA UPGRADING EFFICIENCY IMPROVEMENT MODELS: WRI COKING INDEXES

    Energy Technology Data Exchange (ETDEWEB)

    John F. Schabron; Joseph F. Rovani, Jr.; Francis P. Miknis; Thomas F. Turner

    2003-06-01

    Pyrolysis experiments were conducted with three residua at 400 C (752 F) at various residence times. The wt % coke and gaseous products were measured for the product oils. The Western Research Institute (WRI) Coking Indexes were determined for the product oils. Measurements were made using techniques that might correlate with the Coking Indexes. These included spin-echo proton nuclear magnetic resonance spectroscopy, heat capacity measurements at 280 C (536 F), and ultrasonic attenuation. The two immiscible liquid phases that form once coke formation begins were isolated and characterized for a Boscan residuum pyrolyzed at 400 C (752 F) for 55 minutes. These materials were analyzed for elemental composition (CHNS), porphyrins, and metals (Ni,V) content.

  2. Mineral matter in coals and their reactions during coking

    Energy Technology Data Exchange (ETDEWEB)

    Grigore, Mihaela; French, David [The Commonwealth Scientific and Industrial Research Organisation (CSIRO) - Energy Technology, Lucas Heights, NSW 2234 (Australia); Sakurovs, Richard [The Commonwealth Scientific and Industrial Research Organisation (CSIRO) - Energy Technology, Newcastle, NSW 2300 (Australia); Sahajwalla, Veena [School of Materials Science and Engineering, The University of New South Wales, Sydney, NSW 2052 (Australia)

    2008-12-01

    Degradation of coke in the blast furnace is influenced by its inherent mineral matter, the formation of which is itself dependent upon the nature of the coal mineral matter. To date few studies have been made of coke mineralogy and its relationship to the mineralogy of the parent coal. In this study the effect of carbonisation on coal mineral matter has been investigated by a detailed quantitative mineralogical examination of nine cokes and their parent coals. The quantitative analysis was performed on X-ray diffraction patterns of the mineral matter of cokes and coals, using SIROQUANT {sup trademark}. Coke mineralogy and its composition varied strongly between cokes, more strongly than variations in elemental composition of the ash. The mineral matter in the studied cokes consisted of crystalline mineral phases and also significant levels of amorphous phase (ranging between 44 and 75%). Decomposition of clays such as kaolinite, montmorillonite, illite and chamosite produced the amorphous phase and some of the crystalline mineral phases such as mullite, {gamma}-alumina, spinel, cristobalite and leucite. The type of association of mineral matter in coals had an important role in how the clays decomposed. For example, association of kaolinite with silica-bearing minerals in intimate intermixture favoured formation of mullite over {gamma}-alumina. Akermanite and diopside result from reaction of kaolinite with associated calcium bearing minerals (calcite, dolomite or ankerite). Quartz, fluorapatite and the three polymorphs of TiO{sub 2} (anatase, brookite and rutile) were the coal minerals that were least affected during carbonisation, as they were also found in the cokes, yet even they were affected in some cases. (author)

  3. Use of thermogravimetry for proximate analysis of coals and cokes

    Energy Technology Data Exchange (ETDEWEB)

    Ottaway, M.

    1982-08-01

    An alternative method for the proximate analysis of coals and cokes using a thermobalance is described. The test measures water content, volatile matter, fixed carbon, and ash residue and takes <10 min to complete. The variety of coals and cokes tested in this investigation have given results which showed good correlation with values from the prescribed method. The thermogravimetric technique appears to be a feasible rapid alternative to standard methods for proximate analysis. (11 refs.)

  4. Coke formation during thermal cracking of a heavy crude oil

    OpenAIRE

    Urán Castaño, Laura Cristina

    2015-01-01

    Abstract: A pseudo-mechanism for the production of coke during the thermal cracking of a Colombian heavy crude oil was proposed based on thermal cracking experiments carried out at TGA and at horizontal tube furnace at atmospheric conditions. In-situ combustion (ISC) is a thermal method that improves the recovery of heavy crude oils and involves complex phenomena such as heat and mass transfers, low-temperature oxidation of the liquid phase (LTO), and cracking reactions that yield coke, a car...

  5. Mathematical modeling of a rotary hearth coke calciner

    OpenAIRE

    Hilde C. Meisingset; Jens G. Balchen

    1995-01-01

    A mathematical model of a rotary hearth coke calciner is developed. The model is based on first principles including the most important dynamic phenomena. The model is a thermodynamic model involving heat and mass transfer and chemical reactions. Fundamental mass and energy balance equations for the coke phase, the gas phase and the lining are formulated. For the gas phase, a stationary model is used. The equations are solved numerically, and simulated temperature profiles are shown in this p...

  6. Modeling elementary reactions in coke formation from first principles

    OpenAIRE

    Van Speybroeck, Veronique; Hemelsoet, Karen; Minner, Bert; Guy B. Marin; WAROQUIER, MICHEL

    2009-01-01

    Abstract Theoretical calculations are presented on elementary reactions which are important during coke formation in a thermal cracking unit. This process is known to proceed through a free radical chain mechanism. The elementary reaction steps that lead to the growth of the coke surface can be divided into five classes of reversible reactions : hydrogen abstraction, substitution, gas phase olefin addition to radical surface species, gas phase radical addition to ...

  7. Mathematical modeling of a rotary hearth coke calciner

    Directory of Open Access Journals (Sweden)

    Hilde C. Meisingset

    1995-10-01

    Full Text Available A mathematical model of a rotary hearth coke calciner is developed. The model is based on first principles including the most important dynamic phenomena. The model is a thermodynamic model involving heat and mass transfer and chemical reactions. Fundamental mass and energy balance equations for the coke phase, the gas phase and the lining are formulated. For the gas phase, a stationary model is used. The equations are solved numerically, and simulated temperature profiles are shown in this paper.

  8. Therapeutic Effect of Beehive Extract for Treatment of Allergic Rhinitis%蜂巢提取物治疗变应性鼻炎疗效观察

    Institute of Scientific and Technical Information of China (English)

    张凤姣; 李维榕; 罗岳雄; 赵红霞; 李万瑶

    2015-01-01

    [目的] 观察蜂巢提取物对变应性鼻炎患者的临床疗效. [方法] 将符合纳入标准的60例受试者, 随机分为大剂量组和小剂量组各30例. 大剂量组给予口服蜂巢提取物15 g/次, 3次/ d; 小剂量组给予口服蜂巢提取物5 g/次, 3次/ d; 服用1周为1个疗程, 2组均服用4个疗程后观察疗效, 并于停服1个月时随访. [结果] (1) 大剂量组总有效率为90.00%,小剂量组为93.00%, 2组比较 (秩和检验), 差异无统计学意义 (P>0.05). (2) 治疗后及随访时, 2组患者总症状视觉模拟评分量表 (Uni-VAS)、 鼻结膜炎生活质量量表 (RQLQ) 各维度评分均显著降低 (P0.05). [结论] 口服大剂量和小剂量蜂巢提取物均能显著改善变应性鼻炎患者的症状, 两者总体疗效相当, 但随访时小剂量组在症状量表评分方面有回升 (即复发) 的趋势.%Objective To observe the therapeutic effect of beehive extract for the treatment of allergic rhinitis. Methods Sixty qualified subjects were evenly randomized into large dose group and small dose group, 30 in each group. The large dose group was given oral use of beehive extract 15 g per time, and the small dose group was given 5 g per time, three times per day. One week constituted a treatment period, and the treatment lasted 4 courses. After treatment, the therapeutic effect was evaluated in both groups. Follow-up was carried out one month after suspension of medicine. Results ( 1) The total effective rate was 90.00% in the large dose group, and was 93.00% in the small dose group, and the rank sum test results showed the difference was insignificant between the two groups (P>0.05) . (2) After treatment and during follow-up, the scores of general symptom Visual Analog Scale ( Uni-VAS) and the scores of Rhinoconjunctivitis Quality of Life Questionnaire ( RQLQ) were decreased in both groups ( P0.05) . Conclusion Oral use of large or small dose of beehive extract shows certain therapeutic effect for

  9. Correlation between porous structure and fracture stress for metallurgical coke

    Energy Technology Data Exchange (ETDEWEB)

    Gardien, J.F.; Lemaire, E.; Dubs, A.; Osmont, P.; Laurent, J.P.; Steiler, J.M. (Institut de Recherches de la Siderurgie Francaise, Maizieres-les-Metz (France))

    1994-05-26

    Various samples of coke have been characterized by diametral compression and the geometry of the porous network has been analysed in terms of fractal structure. It is found that the coke studied exhibits a fractal behaviour on at least two decades. Diametral compression test leads to two different ways of breaking; brittle fracture, and in some cases complex fracture. As expected, the fracture stress is not linked with the fractal dimension in case of brittle fracture, but with the mean size of the largest pores. In case of complex loading conditions, the fracture strength is linked with the fractal dimension. The models of Cook and of Anderson, which integrate fractal description of porous materials in Griffith's theory, do not seem to be valid concerning coke material. The present approach of characterising the porous structure of coke by the fractal dimension seems adapted to explain coke strength, especially under complex stress conditions, but should be extended to an increased number of coke type samples.

  10. Transformations of pyrite during formation of metallurgical coke

    Energy Technology Data Exchange (ETDEWEB)

    Stanislav Gornostayev; Jouko Haerkki; Olavi Kerkkonen [University of Oulu, Oulu (Finland). Laboratory of Process Metallurgy

    2009-10-15

    The desulfurization of pyrite during the coking process leads to the formation of phases of varying size, shape and composition. The phases are represented mostly by Fe and S-bearing associations, which can be divided into two categories: those represented only by of Fe-S phases (three varieties), and aggregates containing both sulfides and almost pure iron. There are also Fe-O and Fe-S-O phases, which were probably formed after the coke was pushed from the coke oven. It is suggested that the formation of Fe and S-bearing associations can cause the appearance of cracks and cavities in the coke matrix, which, together with the pressure of the released SO{sub 2} gas, will detract from the strength of the coke. Large grains of pyrite can create weaker spots than do smaller ones, and the incomplete decomposition of pyrite will cause migration of the remaining part of the sulfur to the blast furnace, affecting the reactions there. This may be more common in cokes of relatively low porosity and small pore size and in those made from coals with large pyrite grains. 17 refs., 2 figs., 1 tab.

  11. Effects of Annealing on Microstructure and Microstrength of Metallurgical Coke

    Science.gov (United States)

    Xing, Xing; Zhang, Guangqing; Rogers, Harold; Zulli, Paul; Ostrovski, Oleg

    2013-12-01

    Two metallurgical cokes were heat treated at 1673 K to 2273 K (1400 °C to 2000 °C) in a nitrogen atmosphere. The effect of heat treatment on the microstructure and microstrength of metallurgical cokes was characterized using X-ray diffraction, Raman spectroscopy, and ultra-microindentation. In the process of heat treatment, the microstructure of the metallurgical cokes transformed toward the graphite structure. Raman spectroscopy of reactive maceral-derived component (RMDC) and inert maceral-derived component (IMDC) indicated that the graphitisation degree of the RMDC was slightly lower than that of the IMDC in the original cokes; however graphitisation of the RMDC progressed faster than that of the IMDC during annealing, and became significantly higher after annealing at 2273 K (2000 °C). The microstrength of cokes was significantly degraded in the process of heat treatment. The microstrength of the RMDC was lower, and of its deterioration caused by heat treatment was more severe than IMDC. The degradation of the microstrength of cokes was attributed to their increased graphitisation degree during the heat treatment.

  12. Fissure formation in coke. 1: The mechanism of fissuring

    Energy Technology Data Exchange (ETDEWEB)

    D.R. Jenkins; M.R. Mahoney; J.C. Keating [CSIRO Mathematical and Information Sciences, North Ryde, NSW (Australia)

    2010-07-15

    Pilot scale coke oven experiments, in which carbonisation has been arrested after 2 and 4 h, have been used to identify key aspects of the initial formation and propagation of fissuring in coke. The experiments show that the primary fissure network is formed within the first few hours of coking and the fissures propagate towards the centre of the oven as coking progresses. They also show that some of the initially formed fissures stop propagating, thus increasing the effective fissure spacing as coking continues. A model for the propagation of regular crack arrays has been used to identify the cause of the initial formation of the fissure network, evaluate the fissure spacing and explain the fissure coarsening effect. The coarsening is shown to be due to an instability, in the form of every second fissure stopping. The formation of lateral fissures is shown to be due to tensile stress formation near the tips of stopped fissures and also to increased shrinkage due to a maximum in the coke contraction coefficient at around 700{sup o}C. 45 refs., 11 figs., 1 tab.

  13. Damage Diagnosis for High Temperature Coke-oven Chamber Walls

    Science.gov (United States)

    Sugiura, Masato; Sakaida, Michitaka; Fujikake, Yohichi; Irie, Keisuke

    Metallurgical coke is needed as reducing reagent and energy source in blast furnaces. Most of coke ovens in Japan have been working over 30 years and have become gradually decrepit. A coke oven consists of many coking chambers, and each chamber is 6 m high, 16 m long and 0.4m wide. Uneven damage at the chamber-wall surface such as brick erosion and carbon deposition disturbs production because the coke is pushed horizontally when discharged from the chamber. To diagnose the chamber wall which is constantly sustained at a high temperature, we have developed a water-cooling heat-resistance probe. Line scan cameras mounted in the probe obtain thermal images of the entire chamber-wall surfaces with high resolution. In addition, to measure topographical information of the wall, a laser light-section method combined with line-scan-camera imaging has been considered. It is emphasized that the diagnosis probe works under enormously severe conditions, such as at a temperature of over 1000°C and inside a width of only 0.4m. Clarifying the appearance of chamber-wall damages in operating aged coke ovens, we proposed the index relating unevenness of a chamber-wall surface to pushing load. The index is utilized for the guidance enabling effective repairs of damaged oven walls.

  14. Fatigue behaviour of coke drum materials under thermal-mechanical cyclic loading

    Directory of Open Access Journals (Sweden)

    Jie Chen

    2014-01-01

    Full Text Available Coke drums are vertical pressure vessels used in the delayed coking process in petroleum refineries. Significant temperature variation during the delayed coking process causes damage in coke drums in the form of bulging and cracking. There were some studies on the fatigue life estimation for the coke drums, but most of them were based on strain-fatigue life curves at constant temperatures, which do not consider simultaneous cyclic temperature and mechanical loading conditions. In this study, a fatigue testing system is successfully developed to allow performing thermal-mechanical fatigue (TMF test similar to the coke drum loading condition. Two commonly used base and one clad materials of coke drums are then experimentally investigated. In addition, a comparative study between isothermal and TMF lives of these materials is conducted. The experimental findings lead to better understanding of the damage mechanisms occurring in coke drums and more accurate prediction of fatigue life of coke drum materials.

  15. Electrochemical treatment of COD in biologically pretreated coking wastewater using Ti/RuO2-IrO2 electrodes combined with modified coke

    Institute of Scientific and Technical Information of China (English)

    HE Xu-wen; LIU Li-yuan; GONG Jing-wen; WANG Jian-bing; QIN Qiang; WANG Hao

    2011-01-01

    The electrochemical treatment of COD contained in biologically pretreated coking wastewater treated by a three-dimensional electrode system with modified coke as the particle electrode was investigated.And the electrochemical perfomance of the coke modified with various active components was studied.The results show that the coke modified with Fe(NO3)2 has the lowest energy consumption and higher COD removal rate under the same condition,and the modified coke has better surface characteristics for the purpose of this study.In addition,the kinetic constant was also calculated.The study shows that the three-dimensional electrode system with Fe(NO3)2-modified coke can give a satisfactory solution in biologically pretreated coking wastewater.

  16. Coking Wastewater Treatment by Coke Powder Activation%焦粉活化处理焦化废水

    Institute of Scientific and Technical Information of China (English)

    彭兴华; 张远行

    2012-01-01

    In our report, activated coke and coking wastewater treatment were performed by changing the chemical reagent type, concentration and time, and the removal rates of activated coke on volatile phenol, COD substances, ammonia and non-ferrous material in coking wastewater were analyzed. The results indicated that the effects of steam modified coke powder were superior to that of chemical reagent modified coke powder; the volatile phenol removal rate, COD removal rate, ammonia-nitrogen removal rate and chroma removal rate of which was 98.67% , 83.05% , 37.52% , 94. 71% , respectively; the ammonia-nitrogen removal rate of coke powder treated with HNO3(5 mol · L-1) attained 49.33%.%通过改变化学试剂种类、浓度和时间等3个因素来活化焦粉并处理焦化废水的实验,研究了活化焦粉对焦化废水中的挥发酚、COD物质、氨氮和有色物的去除率.结果表明:水蒸气改性焦粉的处理效果优于化学试剂改性焦粉的处理效果.水蒸气改性后的焦粉,其处理废水中挥发酚的去除率可达98.67%,COD去除率可达83.05%,氨氮去除率可达37.52%,色度去除率可达94.71%.采用5mol·L-1的HNO3活化焦粉,氨氮去除率效果较好,可达49.33%.

  17. Intercalation mechanisms of lithium into graphitized needle cokes

    Institute of Scientific and Technical Information of China (English)

    苏玉长; 尹志民; 徐仲榆

    2001-01-01

    A needle coke was graphitized at different heat treatment temperature (2000℃ to 3000℃). The electrochemical intercalation mechanism of Li into the graphitized coke has been studied in Li|1mol*L-1 LiClO4+ethylene carbonate/diethylene carbonate|graphite cells, using an in-situ X-Ray diffraction (XRD) technique. The study of Li-C intercalation processes of the graphitized coke reveals that there are three major types of intercalation behavior. The first is uniformly intercalated at all Li-C compounds in graphitized coke heated at 2250℃; the second is obviously staging phenomenon during intercalating for the graphitized coke heated at 2750℃; the third is cointercalation of solvated Li-ion at high potential (>0.3V) and then lithium electrochemical intercalation at lower potential for that heated at 3000℃, resulting in the decrease of capacity and efficiency of graphite negative electrode for lithium-ion secondary battery.

  18. Disposal of Waste Plastics With Traditional Coking Process

    Institute of Scientific and Technical Information of China (English)

    CAI Jiu-ju; YU Guang-wei; LIAO Hong-qiang; QIAN Kai; ZHAO Pen; HE Ya-bin

    2006-01-01

    A new technology for treating waste plastics (WP) by traditional coking process was introduced. With a thermo-balance and a 10 g atmospheric fixed bed reactor, the thermo-gravimetric behavior and product were studied during co-coking of WP with blended coal. And then, using a coke-oven with capacity of 200 kg, the characteristics of products were assessed. The results showed that there is an overlapping temperature range (200-550 ℃) of decomposition between WP and blended coal, and the pyrolysis synergism index η and synergism strength β proposed could evaluate the synergism between them. 1% of added WP results in the maximum synergism in all series experiments. The increase of added WP decreases the synergism. Tar yield in co-coking is increased with the decrease of water yield for synergism. Moreover, it was also found that the quality indexes of coke, such as M10, M40, CRI and CSR, are degraded with the increase of WP until 4%, though the quality of tar and gas is optimized for WP addition.

  19. Pretreatment of coking wastewater using anaerobic sequencing batch reactor (ASBR)

    Institute of Scientific and Technical Information of China (English)

    LI Bing; SUN Ying-lan; LI Yu-ying

    2005-01-01

    A laboratory-scale anaerobic sequencing batch reactor (ASBR) was used to pretreat coking wastewater. Inoculated anaerobic granular biomass was acclimated for 225 d to the coking wastewater, and then the biochemical methane potential (BMP)of the coking wastewater in the acclimated granular biomass was measured. At the same time, some fundamental technological factors, such as the filling time and the reacting time ratio (tf/tr), the mixing intensity and the intermittent mixing mode, that affect anaerobic pretreatment of coking wastewater with ASBR, were evaluated through orthogonal tests. The COD removal efficiency reached 38%~50% in the stable operation period with the organic loading rate of 0.37~0.54 kg COD/(m3.d) at the optimum conditions of tf/tr, the mixing intensity and the intermittent mixing mode. In addition, the biodegradability of coking wastewater distinctly increased after the pretreatment using ASBR. At the end of the experiment, the microorganism forms on the granulated sludge in the ASBR were observed using SEM (scanning electron microscope) and fluoroscope. The results showed that the dominant microorganism on the granular sludge was Methanosaeta instead of Methanosarcina dominated on the inoculated sludge.

  20. Industrial Experiment on Coke Spraying With ZBS Additive in Blast Furnace

    Institute of Scientific and Technical Information of China (English)

    ZHU Zi-zong; ZHANG Zhu-ming; TANG Qi-yong; YANG Xue-feng; ZHANG Kun-hua; ZHAO Xian-sheng

    2006-01-01

    In order to improve the thermal properties of coke, an industrial experiment on the coke spraying with ZBS additive solution was carried out at coking plant and No.6 blast furnace (2 000 m3) of Kunming Iron and Steel Co Ltd. The coke reaction index (CRI) of the coke spraying with ZBS additive solution decreases by 10.56%, and the coke strength after reaction (CSR) increases by 7.80% in comparison with those of the un-sprayed coke. During the experiment, the average iron output increases by 66.69 t/d, and the coke rate is reduced by 5.21 kg per ton iron, while the fluctuation of furnace temperture is small, and sulphur content in hot metal and 100% of hot metal are acceptable.

  1. Using ultrafine particles from a coal washing plant in metallurgical coke production

    OpenAIRE

    Jesús Manuel Gutierrez Bernal; William Fernando Mora Pulido; Luís Ignacio Rodríguez Varela; Javier Ramírez; José de Jesús Díaz Velásquez

    2011-01-01

    Blending ultrafine particles from a coal washing plant was studied for coke production by briquetting using 6%w coal tar as binder. The ultrafine coal particles were characterised and a pilot coking test was made in a Koppers’ furnace. Coke quality was evaluated by proximate analysis, stability (micum 10 and micum 40), coke reactivity index (CRI) with CO2 and the coke’s mechanical strength after reaction with carbon dioxide (CSR index). Briquetting results showed that was possible to obtain c...

  2. Properties of Spent Active Coke Particles Analysed via Comminution in Spouted Bed

    OpenAIRE

    Bronislaw Buczek

    2013-01-01

    Samples of active coke, fresh and spent after cleaning flue gases from communal waste incinerators, were investigated. The outer layers of both coke particles were separately removed by comminution in a spouted bed. The samples of both active cokes were analysed by means of densities, mercury porosimetry, and adsorption technique. Remaining cores were examined to determine the degree of consumption of coke by the sorption of hazardous emissions (SO2, HCl, and heavy metals) through its bed. Di...

  3. Textural changes in metallurgical coke prepared with polyethylene

    Institute of Scientific and Technical Information of China (English)

    Stanislav S.Gornostayev; Jyrki J.Heino; Tommi M.T.Kokkonen; Hannu T.Makkonen; Satu M.M.Huttunen; Timo M.J.Fabritius

    2014-01-01

    The effect of high-density polyethylene (HDPE) on the textural features of experimental coke was investigated using polar-ized-light optical microscopy and wavelet-based image analysis. Metallurgical coke samples were prepared in a laboratory-scale furnace with 2.5%, 5.0%, 7.5%, 10.0%, and 12.5%HDPE by mass, and one sample was prepared by 100%coal. The amounts and distribution of textures (isotropic, mosaic and banded) and pores were obtained. The calculations reveal that the addition of HDPE results in a decrease of mosaic texture and an increase of isotropic texture. Ethylene formed from the decomposition of HDPE is considered as a probable reason for the texture modifications. The approach used in this study can be applied to indirect evaluation for the reactivity and strength of coke.

  4. Interactions between coking coals and plastics during co-pyrolysis

    Energy Technology Data Exchange (ETDEWEB)

    Richard Sakurovs [CSIRO, North Ryde, NSW (Australia). Division of Energy Technology

    2003-10-01

    Blends of three Australian coking coals and polypropylene, polystyrene, polyacrylonitrile and polyphenylene sulfide were prepared and the extent to which the blends fused on heating was monitored using proton magnetic resonance thermal analysis in order to identify interactions between them that could affect their fluidity. Different plastics had different effects. Polystyrene strongly reduced the fluidity of all of the coals, confirming previous findings. Polypropylene did not affect the fluidity of the two coking coals of lower rank. Polyphenylene sulfide reduced the fluidity of the coals at temperatures near the solidification temperature of the coals, and polyacrylonitrile appeared to increase the fluidity of the coals at temperatures near the softening temperature of the coals. The very different effects different plastics have on coal fluidity show that the interaction between plastics and coals must be carefully examined before plastics are added to coking coal blends. 28 refs., 6 figs., 1 tab.

  5. Coke yield and heat transfer in reaction of liquid-solid agglomerates of Athabasca vacuum residue

    Energy Technology Data Exchange (ETDEWEB)

    Ali, M.; Courtney, M.; Boddez, L.; Gray, M. [Alberta Univ., Edmonton, AB (Canada). Dept. of Chemical and Materials Engineering

    2010-02-15

    Delayed coking and fluid-bed coking are the most common commercial processes used by the petroleum industry for the thermal conversion of vacuum residues into petroleum distillate products. This paper presented the results of an experimental study of coke yield at long reaction times from agglomerates of coke particles and Athabasca vacuum residue (AVR). The ultimate coke yield was determined for a range of agglomerate thicknesses, liquid concentrations and reaction temperatures. The agglomerates were heated on Curie-point alloy strips in an induction furnace at 503 and 530 degrees C until all toluene-soluble material was converted. A simple heat transfer model was used to describe the temperature profile within the agglomerates. Coke yield results from agglomerates were compared to the coke yield results from reacting thin films of vacuum residue. The average coke yield from the agglomerates was 23 per cent, while the coke yield from thin films of 20 {mu}m thickness was 11 per cent, which supports the role of mass transfer in coke formation reactions. The ultimate coke yield was insensitive to vacuum residue concentration, agglomerate size, and reaction temperature. According to control experiments on thin films of liquid at different heating rates, the temperature-time history has little effect on the ultimata coke yield. 13 refs., 2 tabs., 10 figs.

  6. 40 CFR 63.302 - Standards for by-product coke oven batteries.

    Science.gov (United States)

    2010-07-01

    ... batteries. 63.302 Section 63.302 Protection of Environment ENVIRONMENTAL PROTECTION AGENCY (CONTINUED) AIR... National Emission Standards for Coke Oven Batteries § 63.302 Standards for by-product coke oven batteries... oven emissions from each affected existing by-product coke oven battery that exceed any of...

  7. [Characterization of PAHs in fly ashes from coke production].

    Science.gov (United States)

    Mu, Ling; Peng, Lin; Liu, Xiao-Feng; Bai, Hui-Ling; Zhang, Jian-Qiang

    2013-03-01

    In order to investigate the characteristics of polycyclic aromatic hydrocarbons (PAHs) in ashes from coking, PAHs in ashes from three coke production plants were analyzed with GC-MS, and the distribution characteristics of PAHs and potential toxicity risk were discussed. The sum of 16 EPA prior PAHs varied from 8.17 x 10(2) to 5.17 x 10(3) microg x g(-1). PAH contents from the coke oven (stamp charging) with the height of 3.2 m were two times higher than those from the one (top charging) with the height of 6.0 m, and PAHs in ashes from coal charging were significantly higher than those from coke pushing in the same plant. Four-ring and five-ring PAHs were the dominant species in ashes from coking and the sum of them accounted for more than 80.00% of total PAHs. Chrysene (Chr), benzo [a] anthracene (BaA) and benzo [b] fluoranthene (BbF) were abundant in all ash samples. The content of total BaP-based toxic equivalency (BaPeq) ranged from 1.64 x 10(2) to 9.57 x 10(2) microg x g(-1). From the carcinogenic point of view, besides benzo [a] pyrene (BaP), dibenz [a,h] anthracene (DbA) contributed most to the overall toxicity of PAHs, followed by BaA and BbF. BaPeq concentration from coal charging was 5.21-fold higher than that from coke pushing, indicating that different reuse ways should be considered based on their specific toxicity profiles of PAHs. PMID:23745428

  8. Optimization of the coke-oven activated sludge plants

    Energy Technology Data Exchange (ETDEWEB)

    Raizer Neto, Ernesto [Santa Catarina Univ., Florianopolis, SC (Brazil); Colin, Francois [Institut de Recherches Hydrologiques, 54 - Nancy (France); Prost, Christian [Laboratoire de Sciences de Genie Chimique, Nancy (France)

    1993-12-31

    In the coke-oven activated sludge plants one of the greatest problems of malfunction is due to inffluent variability. The composition and, or, concentration variations of the inffluent substrate, which can cause an unstable system, are function of the pollutant load. Nevertheless, the knowledge of the kinetic biodegradation of the coke-oven effluent represents the limiting factor to develop an effective biological treatment. This work describes a computational model of the biological treatment which was elaborated and validated from continuous pilot scale experiments and calibrated by comparing its predictions to the pilot experiment`s results. 12 refs., 9 figs., 3 tabs.

  9. Characterisation of coking activity during supercritical hydrocarbon pyrolysis

    OpenAIRE

    Gascoin, Nicolas; Gillard, Philippe; Bouchez, Marc

    2008-01-01

    cited By (since 1996) 5 International audience The active cooling of the Supersonic Combustion Ramjet engine, for hypersonic flight purpose, is ensured thanks to fuel, n-dodecane for the present study. The endothermic fuel pyrolysis, starting above 800 K, could generate an unwanted coke formation. Experimental tests up to 1125 K and between 1 MPa and 6 MPa have been performed on the hydrocarbon fuel pyrolysis to evaluate the coking activity. 316L stainless steel, low carbon steel an...

  10. Methods for measuring moisture content in the coal and coke

    International Nuclear Information System (INIS)

    As a result of modern mining methods and the increase of fine coal recovery for economic reasons, there has been growing interest in measuring and controlling the moisture content of the coal and coke. In recent decades moisture determination of the coal and coke has been extensively investigated and applied worldwide. The methods for measuring moisture include nuclear and non-nuclear techniques. This paper introduces the basic principle and principal specification of various techniques for moisture determination and reviews advantage and disadvantage for various methods and also put forward the tendency at present

  11. 利用铁桶试验预测工业焦炉成焦质量的研究%Prediction of the Coke Quality of Industrial Coke Oven Using Test Coke Oven

    Institute of Scientific and Technical Information of China (English)

    刘守军; 杨颂; 何小刚; 吕青

    2011-01-01

    为优化炼焦炉入炉煤配方以及提高焦炭产品质量,利用20 kg铁桶随炉试验以预测工业焦炉的成焦质量,并建立了预测数学模型.结果表明,利用20 kg铁桶试验可准确预测工业焦炉成焦强度,二者表现出很好的相关性,可直接用于指导工业生产过程中的配煤操作,具有很强的实用性.%In order to optimize coking coal blending and increase coke quality,a 20 kg test coke oven was adopted iuside industrial coke oven to predict the coke quality of industrial coke oven. A mathematical model was established for the prediction. Results show that the test coke oven predicted industrial coke oven accurately in coke quality with good correlation. Therefore,it is applicable to guiding coal blending for industrial production.

  12. Effect of alkaline elements on the reactivity, strength and structural properties of blast furnace cokes

    Directory of Open Access Journals (Sweden)

    A. Bhattacharyya

    2015-07-01

    Full Text Available The present study concerns itself on the adverse effects of alkaline elements like sodium and potassium on blast furnace cokes. To achieve a deeper insight on the effects of alkaline elements on coke reactivity and strength, industrial coke samples impregnated with different alkaline species in various amounts have been tested under standard conditions to find out their Coke Reactivity Index (CRI and Coke Strength after Reaction (CSR values. Scanning electron microscopy, petrographic and Raman Spectrometric investigations demonstrate the change of structural properties. The mechanism of catalysis has been postulated.

  13. Using ultrafine particles from a coal washing plant in metallurgical coke production

    Directory of Open Access Journals (Sweden)

    Jesús Manuel Gutierrez Bernal

    2011-01-01

    Full Text Available Blending ultrafine particles from a coal washing plant was studied for coke production by briquetting using 6%w coal tar as binder. The ultrafine coal particles were characterised and a pilot coking test was made in a Koppers’ furnace. Coke quality was evaluated by proximate analysis, stability (micum 10 and micum 40, coke reactivity index (CRI with CO2 and the coke’s mechanical strength after reaction with carbon dioxide (CSR index. Briquetting results showed that was possible to obtain coke having 19.0 % CRI and 75.6% CSR, these being the characteristics required in metallurgical processes.

  14. Coke formation in the oxidative dehydrogenation of ethylbenzene to styrene by TEOM

    OpenAIRE

    Nederlof, C.; P. Vijfhuizen; Zarubina, V.; Melián-Cabrera, I.; Kapteijn, F.; Makkee, M.

    2014-01-01

    A packed bed microbalance reactor setup (TEOM-GC) is used to investigate the formation of coke as a function of time-on-stream on γ-Al2O3 and 3P/SiO2 catalyst samples under different conditions for the ODH reaction of ethylbenzene to styrene. All samples show a linear correlation of the styrene selectivity and yield with the initial coverage of coke. The COX production increases with the coverage of coke. On the 3 wt% P/SiO2 sample, the initial coke build-up is slow and the coke deposition ra...

  15. Application research on hydraulic coke cutting monitoring system based on optical fiber sensing technology

    Science.gov (United States)

    Zhong, Dong; Tong, Xinglin

    2014-06-01

    With the development of the optical fiber sensing technology, the acoustic emission sensor has become one of the focal research topics. On the basis of studying the traditional hydraulic coke cutting monitoring system, the optical fiber acoustic emission sensor has been applied in the hydraulic coke cutting monitoring system for the first time, researching the monitoring signal of the optical fiber acoustic emission sensor in the system. The actual test results show that using the acoustic emission sensor in the hydraulic coke cutting monitoring system can get the real-time and accurate hydraulic coke cutting state and the effective realization of hydraulic coke cutting automatic monitoring in the Wuhan Branch of Sinopec.

  16. Properties of Spent Active Coke Particles Analysed via Comminution in Spouted Bed

    Science.gov (United States)

    Buczek, Bronislaw

    2013-01-01

    Samples of active coke, fresh and spent after cleaning flue gases from communal waste incinerators, were investigated. The outer layers of both coke particles were separately removed by comminution in a spouted bed. The samples of both active cokes were analysed by means of densities, mercury porosimetry, and adsorption technique. Remaining cores were examined to determine the degree of consumption of coke by the sorption of hazardous emissions (SO2, HCl, and heavy metals) through its bed. Differences in contamination levels within the porous structure of the particles were estimated. The study demonstrated the effectiveness of commercial active coke in the cleaning of flue gases. PMID:24459454

  17. Properties of spent active coke particles analysed via comminution in spouted bed.

    Science.gov (United States)

    Buczek, Bronislaw

    2013-01-01

    Samples of active coke, fresh and spent after cleaning flue gases from communal waste incinerators, were investigated. The outer layers of both coke particles were separately removed by comminution in a spouted bed. The samples of both active cokes were analysed by means of densities, mercury porosimetry, and adsorption technique. Remaining cores were examined to determine the degree of consumption of coke by the sorption of hazardous emissions (SO2, HCl, and heavy metals) through its bed. Differences in contamination levels within the porous structure of the particles were estimated. The study demonstrated the effectiveness of commercial active coke in the cleaning of flue gases. PMID:24459454

  18. The effect of blast furnace coke quality on the possibility of its use

    Directory of Open Access Journals (Sweden)

    A. Konstanciak

    2013-04-01

    Full Text Available In the paper behavior of the blast-furnace coke in the high temperature was presented. Comparative analysis of the chemical composition of the blast-furnace coke and the heat treatment of it were done. Coefficients M10 and M40 with the thermo-abrasiveness for chosen cokes were compared. The influence of ash content of the coke on the blast-furnace bed permeability was defined. Usefulness of the coke to blast-furnace process was also defined.

  19. Feasibility of Combustion of Petroleum Coke in 230t/h Circulating Fluidized Bed Boiler

    Institute of Scientific and Technical Information of China (English)

    HAN Dong-tai; SONG Zheng-chang; XU Tao

    2003-01-01

    In order to reuse the high sulfur petroleum coke, the waste in chemical industry, as fuel of power plant for energy recovery, the combustion property of petroleum coke was researched experimentally in circulating fluidized bed (CFB) boiler. The performance of the boiler in burning mixed fuel with different ratios of coal to petroleum coke is obtained. Based on the experimental data, Factors influencing the stability of combustion,thermal efficiency of boiler, and emissions and desulphurisation are discussed. This study demonstrates that the combustion of petroleum coke in CFB boiler is applicable, and has great significance on the design and operation of CFB boiler to burn petroleum coke.

  20. Prediction of the Coke Strength with 40 kg Testing Coke Oven%运用40 kg试验焦炉预测焦炭机械强度

    Institute of Scientific and Technical Information of China (English)

    郝洪洲; 张增旭; 王海燕; 陈双管; 杨永珍

    2001-01-01

    介绍了用40 kg试验焦炉进行的炼焦试验及Micum转鼓测定,可预测焦炭的机械强度的方法和结果,并建立试验焦炉与生产焦炉之间的关系。%Description of following:experiment of 40 kg testing coke oven,measurement of Micum drum,method and result of the prediction on the coke strength as well as the relationship between the testing coke oven and the production coke oven.

  1. A method for discharging gas from banks of horizontal coking furnaces

    Energy Technology Data Exchange (ETDEWEB)

    Varshavskiy, T.P.; Sukhorukov, V.I.

    1983-01-01

    In the method for discharging gases from a bank of horizontal coking furnaces, which includes discharge of gases from the loading period through a gas collector on the coke side with feeding into it of the coke gas with a reduced NOx content, discharge of the gases of the coking period through the gas collector on the machine side, in order to increase the service life of the furnace lining, 25 to 50 percent of the gases of the coking period are discharged through the gas collector on the coking side. The method provides for smokeless loading of the coking furnaces, a normal NOx content in the coking gas and creates conditions for maintaining the required temperature in the head part of the lining of the coking chambers. The operation of a coking bank based on the proposed method makes it possible to produce conditioned coke gas for nitric acid production. The service life of the heads is increased by 2 times as compared with the prototype.

  2. Oil sand process-affected water treatment using coke adsorption

    Energy Technology Data Exchange (ETDEWEB)

    Gamal El-Din, M.; Pourrezaei, P.; Chelme-Ayala, P.; Zubot, W. [Alberta Univ., Edmonton, AB (Canada). Dept. of Civil and Environmental Engineering

    2010-07-01

    Oil sands operations generate an array of oil sands process-affected water (OSPW) that will eventually be released to the environment. This water must be evaluated within conventional and advanced water treatment technologies. Water management strategies propose options for increased reuse and recycling of water from settling ponds, as well as safe discharge. This presentation outlined the typical composition of OSPW. Constituents of concern in OSPW include suspended solids, hydrocarbons, salts, ammonia, trace metals, and dissolved organics such as naphthenic acids (NAs). Petroleum coke is one of the by-products generated from bitumen extraction in the oil sands industry and can be used as one of the possible treatment processes for the removal of organic compounds found in OSPW. Activated carbon adsorption is an effective process, able to adsorb organic substances such as oils, radioactive compounds, petroleum hydrocarbons, poly aromatic hydrocarbons and various halogenated compounds. The objectives of this study were to evaluate the production of activated carbon from petroleum coke using steam as the activation media; to determine the factors affecting the absorption of NAs; and to evaluate the activated coke adsorption capacity for the reduction of NAs and dissolved organic carbons present in OSPW. It was concluded that petroleum non-activated coke has the ability to decrease COD, alkalinity, and NA concentration. tabs., figs.

  3. The Coke Zero Game - Analyse af advergames som kommunikationsprodukt

    OpenAIRE

    Scherfig, Valentin T.; Bendixen, Maria; Larsen, Line N.; Gudmundsson, Soffia

    2010-01-01

    Dette projekt behandler kommunikationsgenren advergames, med udgangspunkt i The Coke Zero Game (2008). Spillet analyseres som kommunikationsprodukt, ved brug af spilteori og empiri i form af fokusgruppeinterview. Opgaven konkluderer på, hvorvidt spillet formår at kommunikere et givent budskab.

  4. Hard coal and coke - determination of volatile matter

    Energy Technology Data Exchange (ETDEWEB)

    NONE

    2010-07-01

    The volatile matter is determined as the loss in mass, less that due to moisture, when coal or coke is heated out of contact with air under standardised conditions. The apparatus and procedure are specified so that one or more determinations can be performed simultaneously in the future.

  5. EVALUATION OF THE POTENTIAL CARCINOGENICITY OF COKE OVEN EMISSIONS

    Science.gov (United States)

    Coke oven emissions are known human carcinogens, classified as weight-of-evidence Group A under the EPA Guidelines for Carcinogen Risk Assessment (U.S. EPA, 1986a). vidence on potential carcinogenicity from animal studies is "Sufficient,". and the evidence rom human studies is "S...

  6. Co-gasification of oil sand coke with coal

    Energy Technology Data Exchange (ETDEWEB)

    Vejahati, Farshid; Gupta, Rajender [Alberta Univ., Edmonton, AB (Canada). Dept. of Chemical and Materials Engineering

    2013-07-01

    Gasification of oil sand delayed coke with sub-bituminous and lignite coals was performed in an atmospheric entrained flow gasifier using steam and oxygen as gasifying agents. The underlying objective of this work was to assess the effects of the operating variables (i.e. temperature, oxygen and steam concentrations) and coal/coke blending ratio on gasification performance in a high-temperature in order to find the possible synergies in co-gasification of the fuels. Experiments were conducted at 1,400 C, using steam and oxygen to carbon weight ratios of (0.36-1.08) and (0.07-0.2), respectively in N{sub 2} carrier gas. The coke to coal weight ratios of 1/3, 1/2, and 2/3 were used for the blending tests. Particle size of 53-90 {mu}m with d{sub 50} = 75 {mu}m were used. In terms of char reactivity, blending did not show any significant positive effect. Slight deviations from linear additive line are in the order of experiment error. Gasification efficiency was also following a linear additive trend once more pointing out the lack of synergy in entrained flow gasification systems. The results however, showed that higher coke content clearly favored the H{sub 2} production.

  7. The development of coke smelting and the industrial revolution

    OpenAIRE

    Macfarlane, Alan

    2004-01-01

    Abraham Darby and the origins of the industrial revolution in Britain. Alan Macfarlane talks to John about the reasons for the area near Birmingham becoming the epi-centre of the industrial development, and the development of coke furnaces and iron smelting.

  8. Coke Reactivity in Simulated Blast Furnace Shaft Conditions

    Science.gov (United States)

    Haapakangas, Juho; Suopajärvi, Hannu; Iljana, Mikko; Kemppainen, Antti; Mattila, Olli; Heikkinen, Eetu-Pekka; Samuelsson, Caisa; Fabritius, Timo

    2016-08-01

    Despite the fact that H2 and H2O are always present in the gas atmosphere of a blast furnace shaft, their role in the solution-loss reactions of coke has not been thoroughly examined. This study focuses on how H2 and H2O affect the reaction behavior and whether a strong correlation can be found between reactivity in the conditions of the CRI test (Coke Reactivity Index) and various simulated blast furnace shaft gas atmospheres. Partial replacement of CO/CO2 with H2/H2O was found to significantly increase the reactivity of all seven coke grades at 1373 K (1100 °C). H2 and H2O, however, did not have a significant effect on the threshold temperature of gasification. The reactivity increasing effect was found to be temperature dependent and clearly at its highest at 1373 K (1100 °C). Mathematical models were used to calculate activation energies for the gasification, which were notably lower for H2O gasification compared to CO2 indicating the higher reactivity of H2O. The reactivity results in gas atmospheres with CO2 as the sole gasifying component did not directly correlate with reactivity results in gases also including H2O, which suggests that the widely used CRI test is not entirely accurate for estimating coke reactivity in the blast furnace.

  9. Catalytic effect of black liquor on the gasification reactivity of petroleum coke

    Energy Technology Data Exchange (ETDEWEB)

    Zhan, Xiuli; Zhou, ZhiJie; Wang, Fuchen [Kay Laboratory of Coal Gasification of Ministry of Education, East China University of Science and Technology, Shanghai 200237 (China)

    2010-05-15

    CO{sub 2} gasification of petroleum coke using black liquor as a catalyst was performed in a thermogravimetric analyzer (TGA) under temperatures 1223-1673 K at ambient pressure to evaluate the effect of black liquor loading on petroleum coke gasification. It was found that the gasification reactivity of petroleum coke was improved greatly by black liquor. The gasification reactivity was affected by different loading methods in the order: wet grinding > dry grinding > physical impregnation > dry mix. The catalytic activity of black liquor was higher than that of pure alkali metal. The effect of temperature on the gasification reactivity of petroleum coke was changed by black liquor. The reactivity reaches its maximum at 1573 K. The reactivity of petroleum coke was found higher than that of Shenfu coal when black liquor loading is 5 wt.% (of petroleum coke), clearly demonstrating that black liquor could be an effective catalyst for petroleum coke gasification. (author)

  10. Coke Formation During Hydrocarbons Pyrolysis. Part Two: Methane Thermal Cracking Formation de coke pendant la pyrolyse des hydrocarbures. Deuxième partie : pyrolyse du méthane

    OpenAIRE

    Billaud F.; Broutin P.; Busson C.; Gueret C.

    2006-01-01

    Part one of this article dealt with coking in a steam cracking furnace. In this process, coke deposition is a very complex phenomenon due to the number of parameters involved. Nevertheless, for this process, coke deposition is a secondary reaction which does not affect steam cracking yields. It is completely different for methane thermal cracking. Coke is one of the main products of this reaction. Part two of this article deals with coke deposition on the walls of the reactors used for methan...

  11. Electrical conductivity of the screening residuals of coke production in context of ferrochromium production in a submerged arc furnace

    Energy Technology Data Exchange (ETDEWEB)

    Rousu, Arto; Mattila, Olli [Lab. of Process Metallurgy, Univ. of Oulu (Finland)

    2009-11-15

    Coke is used as a reducing agent in the production of ferrochromium in a submerged arc furnace (SAF). Its good electrical conductivity compared to other input materials makes it a dominant current conductivity substance in the burden. The resistance of the coke has to be high enough to ensure the proper functionality of the furnace. Used cokes for submerged arc furnace production are relatively small in size compared to e.g. blast furnace (BF) cokes. A common practice is to use screening residual coke, which is too small for the BF, in SAF. The goal of this study was to show differences in the electrical properties of screening residual cokes compared to coke formed in different parts of the coke battery, in dependence of particle size. The resistances of different cokes were measured and XRD measurements were performed to define the crystallographic structure of the selected cokes. The results indicate that small coke particles have higher overall resistance, which is due to their internal properties. This small weakly carbonized coke is formed in the middle of the coking battery and is subject to changes in varying coking practices. Continuous quality control of screening residual coke is needed to use it in the SAF. (orig.)

  12. Factory automation of Yawata coke furnace No.5; Yawata No.5 cokes ro no FA ka

    Energy Technology Data Exchange (ETDEWEB)

    Nakagawa, Y.; Sakaida, M.; Uematsu, H.; Furuta, K. [Nippon Steel Corp., Tokyo (Japan)

    1994-12-25

    A coke furnace of attended operation was factory-automated to an unattended operation. The following improvements were attempted on a furnace with an output as high as 140 productions a day: Mounting on a tractor trolley of the charging trolley an automation device that operates ascension pipes in ten furnaces ahead in the charge furnace has reduced the cycle time by 8% and increased the generated COG by 1%. The furnace outputting work operating on the synchronous work of the moving machine was modeled after the actual state of operation to develop a cycle time simulator that calculates the total outputting work time of one furnace group. This simulator has made discussions on different operation patterns of the moving machine possible as described below and realized the improvement. Changing the charging trolley work patterns resulted in reducing the cycle time by 5%. With an objective to improve the stopping accuracy and reduce the expense, the VVVF feedback control and the electric stopping position inching control were adopted. In addition, improvements were achieved in the run stopping accuracy and automatic operation. This factory-automation realized an operation at the automation rate of 97%. The furnace outputting time for 140 productions a day in the case of intervention of manual works at 3% is 1275 minutes. 2 refs., 9 figs., 1 tab.

  13. Automatic operation systems for the coke oven top; Cokes ro rojo sagyo no jidoka tachiage jokyo

    Energy Technology Data Exchange (ETDEWEB)

    Saji, T.; Kitayama, Y. [Sumitomo Metal Industries, Ltd., Osaka (Japan)

    1994-10-13

    This paper describes an outline of automatic operation on the coke oven top, which has been conducted at the Kashima Steel Works, Sumitomo Metal Industries, Ltd. For the automatic operation on the oven top, unmanned operation of the charging car, mechanization of works on the oven top, centralized control, and simplification of the system were introduced. This automatic system consists of the charging car, central station, charging car station, and quenching car automation system. For the automatic travel motion control, braking by the electric regenerative brake and disk brake was adopted. The oven center standing control is carried out by using the position and distance information of interlock cable and the oven center sensor. Standing accuracy of the oven center of charging car was designed to be up to {plus_minus}10 mm. High detection accuracy can be obtained through the optical cutting image processing. The carbon removing apparatus for inlet port, oven top cleaner dust treatment apparatus, and charging level measurement apparatus were added to the charging car, which were required for the automatic operation on the oven top. As a result, the automatic ratio more than 99% could be achieved. 6 figs., 4 tabs.

  14. Changes in a coke structure due to reaction with carbon dioxide

    Energy Technology Data Exchange (ETDEWEB)

    Pusz, S.; Majewska, J.; Pilawa, B. [Centre of Polymer and Carbon Materials, Polish Academy of Sciences, M. Curie-Sklodowskiej 34, PL-41819 Zabrze (Poland); Krzesinska, M. [Centre of Polymer and Carbon Materials, Polish Academy of Sciences, M. Curie-Sklodowskiej 34, PL-41819 Zabrze (Poland); Silesian Technical University, Department of Electron Technology, Institute of Physics, Krzywoustego 2, PL-44100 Gliwice (Poland); Smedowski, L. [Silesian Technical University, Department of Electron Technology, Institute of Physics, Krzywoustego 2, PL-44100 Gliwice (Poland); Kwiecinska, B. [AGH-University of Science and Technology, Aleja Mickiewicza 30, PL-30059 Krakow (Poland)

    2010-04-01

    Technological properties of a coke directly depend on a coke structure, i.e., on carbon matrix (a solid phase in a porous medium) and on pore system. Coke structure is deeply transformed during blast furnace operation and one of the most important factors responsible for that is the CO{sub 2} gasification. The objective of this work was to investigate changes of the physical structure of a coke upon the reaction with carbon dioxide to evaluate the effects of structural transformations on technological properties of a coke. Selected physical parameters of cokes produced in a laboratory scale were carried out prior to and after the reaction with CO{sub 2}. The following physical methods were used for the study: helium gas densitometry, physical adsorption of N{sub 2}, optical microscopy, transmission electron microscopy (TEM), ultrasonic measurements and electron paramagnetic resonance spectroscopy (EPR). The results showed that the reaction with CO{sub 2} distinctly affects the physical structure of coke. Coke solid matrix becomes better ordered, with greater structural units, while development of pore structure consists in the enlargement and coalescence of pores and the increase of specific surface area. Great increase of coke porosity after the reaction with CO{sub 2} seems to be more affecting the final strength and reactivity of coke than the transformation of carbon matrix. (author)

  15. Granulation of coke breeze fine for using in the sintering process

    Directory of Open Access Journals (Sweden)

    Mohamed F.M.

    2010-01-01

    Full Text Available Coke breeze is the main fuel used in the sintering process. The value of -3+1 mm. represents the most favorable particle size for coke breeze in the sintering process. About 20% of total coke fines (-0.5 mm are produced during different steps of preparation. Introducing these fines during the sintering process proves to be very harmful for different operating parameters. Thus ,this study aims at investigating the production of granules resulting from these fines using molasses as organic binder and its application in sintering of an iron ore. The results showed that the granules having the highest mechanical properties were obtained with 14.5 wt % molasses addition. The sintering experiments were performed by using coke breeze in different shapes (-3+1 mm in size, coke breeze without sieving and coke breeze granules -3+1 mm. The reduction experiments, microscopic structure and X-ray analysis for the produced sinter were carried out. The results revealed that, all sinter properties (such as shatter test, productivity of sinter machine and blast furnace, reduction time and chemical composition for produced sinter by using coke breeze with size -3+1 mm and coke breeze granules were almost the same. The iron ore sinter which was produced by using coke breeze without sieving yielded low productivity for both sinter machine and blast furnace. Furthermore, using coke breeze without sieving in sintering of an iron ore decreases the vertical velocity of sinter machine and increases the reduction time.

  16. Mild coal extraction for the production of anode coke from Blue Gem coal

    Energy Technology Data Exchange (ETDEWEB)

    Rodney J. Andrews; Terry Rantell; David Jacques; James C. Hower; J. Steven Gardner; Mike Amick [University of Kentucky, Lexington, KY (United States). Center for Applied Energy Research

    2010-09-15

    The quality and availability of petroleum coke used in the manufacture of carbon anodes for aluminum production is a growing concern to the industry. Coke quality and yields have progressively declined as changes in refinery practice and the move towards processing an increasing proportion of heavier sour crudes have affected coke properties, resulting in an increase in the metal impurities and sulfur content of the coke. An alternative supply of anode coke is required to supplement or eventually replace calcined petroleum coke. The significant domestic reserves of coal could represent a viable carbon resource for anode production, provided defined coke specifications can be met and at a cost that is economically viable. The principal objective of this study was to examine the feasibility of producing anode grade coke by the UKCAER process for the mild solvent extraction of coal. Blue Gem coal from Eastern Kentucky was dissolved in a high boiling point solvent, the mineral matter and unreacted products removed by filtration, and the clean coal liquid converted to coke. The performance of the coal in solvent extraction was compared to a very reactive coal from Western Kentucky. A simple solvent-extraction screening test was established to assess potential candidate materials and process variables without the need for prolonged and complex routines. The coals were assessed in more detail to determine the optimum process conditions by conducting larger scale extraction tests to yield sufficient material for conversion to coke. The green cokes were calcined and the products characterized. The composition and structure of the calcined cokes were compared to typical petroleum coke and assessed for their use in the fabrication of carbon anodes. 21 refs., 11 figs., 4 tabs.

  17. Emissions of polycyclic aromatic hydrocarbons from coking industries in China

    Institute of Scientific and Technical Information of China (English)

    Ling Mu; Lin Peng; Junji Cao; Qiusheng He; Fan Li; Jianqiang Zhang; Xiaofeng Liu

    2013-01-01

    This study set out to assess the characteristics of polycyclic aromatic hydrocarbon (PAH) emission from coking industries,with field samplings conducted at four typical coke plants.For each selected plant,stack flue gas samples were collected during processes that included charging coal into the ovens (CC),pushing coke (PC) and the combustion of coke-oven gas (CG).Sixteen individual PAHs on the US EPA priority list were analyzed by gas chromatography/mass spectrometry (GC/MS).Results showed that the total PAH concentrations in the flue gas ranged from 45.776 to 414.874 μg/m3,with the highest emission level for CC (359.545 μg/m3).The concentration of PAH emitted from the CC process in CP1 (stamp charging) was lower than that from CP3 and CP4 (top charging).Low-molecular-weight PAHs (i.e.,two-to three-ring PAHs) were predominant contributors to the total PAH contents,and Nap,AcPy,Flu,PhA,and AnT were found to be the most abundant ones.Total BaPeq concentrations for CC (2.248 iμg/m3) were higher than those for PC (1.838 μg/m3) and CG (1.082 μg/m3),and DbA was an important contributor to carcinogenic risk as BaP in emissions from coking processes.Particulate PAH accounted for more than 20% of the total BaPeq concentrations,which were significantly higher than the corresponding contributions to the total PAH mass concentration (5%).Both particulate and gaseous PAH should be taken into consideration when the potential toxicity risk of PAH pollution during coking processes is assessed.The mean total-PAH emission factors were 346.132 and 93.173 μg/kg for CC and PC,respectively.

  18. 降低捣固焦炉炼焦耗热量的措施%Measures to reduce the coking heat consumption of stamp-charging coke oven

    Institute of Scientific and Technical Information of China (English)

    陶汝佩; 李红军

    2015-01-01

    对捣固焦炉炼焦耗热量高开展研究。在保证焦炭质量的前提下,研究了配合煤水分、焦炉炉顶空间温度、废气温度的影响,采用适当的焦饼中心温度及合理的空气过剩系数,加强对焦炉炉体保温管理,严格控制焦炉操作等措施来降低炼焦耗热量,效果显著。%This paper studies the reason for high coking heat consumption of stamp-charging coke oven. The influence of moisture content,coke oven top space temperature,and waste gas temperature was studied. Under the precondition of ensuring coke quality,measures such as adopting suitable coke cake center temperature and suitable excess air coefficient,enhancing the management of coke oven proper temperature,and strictly controlling the operation of coke oven were taken to reduce the coking heat consumption. The effect turned out to be remarkable.

  19. Combined XRD and Raman studies of coke types found in SAPO-34 after methanol and propene conversion

    DEFF Research Database (Denmark)

    Wragg, David S.; Grønvold, Arne; Voronov, Alexey;

    2013-01-01

    oligomerisation (PO) reactions. The coke caused by MTO leads to two distinct sets of HRPD peaks which can be indexed by two SAPO-34 unit cells with different lattice parameters and coke contents. We believe that these unit cells represent different zones of the catalyst filled with different coke types. PO coking...... does not lead to splitting of the diffraction peaks. Raman spectra show differences between the coke types produced by MTO and PO with the same overall trend of increasingly polyaromatic coke with increasing coke mass. The intensity of the monocyclic and polyaromatic peaks in the MTO Raman spectra...... correspond to the phase fractions of the two cell types used in the Rietveld refinement, suggesting a link between the two phases and the two coke types. The PO Raman spectra have a stronger polyaromatic band at low coke, suggesting that polyaromatics form faster. In situ powder XRD studies suggest...

  20. Ignition Dynamic Parameters for Coke in Cement Calciners

    Institute of Scientific and Technical Information of China (English)

    2001-01-01

    The mathematical ignition model was established and researches of ignition dynamic parameters for coke in some typical coal samples from cement plants was carried out according to circumstances of coal combusted in cement plants.In order to get the ignitioin temperature Tpi of carbon particles more accurately,the temperature rising experimental method was used and the actual heating circumstances for pulverized coal in calciners(in cement plants)were also considered.With this method,the accurate determination of the ignition temperature of coke in coal was achieved,so as to get some ignition dynamic parameters.These research results provide a theoretical basis for investigating coal ignition characteristics more scientifically and more accurately.

  1. Integrated coke, asphalt and jet fuel production process and apparatus

    Science.gov (United States)

    Shang, Jer Y.

    1991-01-01

    A process and apparatus for the production of coke, asphalt and jet fuel m a feed of fossil fuels containing volatile carbon compounds therein is disclosed. The process includes the steps of pyrolyzing the feed in an entrained bed pyrolyzing means, separating the volatile pyrolysis products from the solid pyrolysis products removing at least one coke from the solid pyrolysis products, fractionating the volatile pyrolysis products to produce an overhead stream and a bottom stream which is useful as asphalt for road pavement, condensing the overhead stream to produce a condensed liquid fraction and a noncondensable, gaseous fraction, and removing water from the condensed liquid fraction to produce a jet fuel-containing product. The disclosed apparatus is useful for practicing the foregoing process. the process provides a useful method of mass producing and jet fuels from materials such as coal, oil shale and tar sands.

  2. 干熄焦工艺对6 m 焦炉焦炭质量的影响%Influence of coke dry quenching on coke quality in 6 m coke oven

    Institute of Scientific and Technical Information of China (English)

    周尽晖; 丁玲; 韩军; 王世杰; 王光辉

    2015-01-01

    In this paper ,the coke wet quenching (CWQ) coke and coke dry quenching (CDQ) coke pro‐duced in 6 meters oven under the same coal blending ratio were analyzed and compared .The influence of CDQ on the quality of coke was studied .The results show that CDQ has no great influence on ash content and sulfur content of coke ,and has little influence on the real density ,porosity ,ash composi‐tion and optical texture indexes of coke .However ,CDQ can significantly improve the parameters such as maturity ,mean size ,size uniformity ,pore size distribution ,mechanical strength and thermal properties ,etc .%选取6m焦炉焦炭,对干、湿法熄焦焦炭进行质量对比分析,研究干熄焦对焦炭质量的影响。结果表明,干熄焦对焦炭的灰分和硫含量改变不大,对焦炭的真密度、气孔率、灰成分和光学组织指数影响较小,对焦炭的成熟度、平均粒度、粒度均匀系数、孔径分布、机械强度和热态强度等的改善明显。

  3. Standard method for proximate analysis of coal and coke

    Energy Technology Data Exchange (ETDEWEB)

    1975-01-01

    ASTM methods are cited that cover the determination of moisture, volatile matter, and ash and the calculation of fixed carbon in coals and cokes sampled and prepared by prescribed methods. The methods cited may be used to establish rank of coals, to show the ratio of combustible to incombustible constituents, to provide the basis for buying and selling, and to evaluate for beneficiation or for other purposes. (BLM)

  4. Utilization of petrographic analysis for determination of petroleum coke mixtures

    OpenAIRE

    TOPRAK, Selami; SÜTCÜ, Emine CİCİOĞLU; GÜLEN, Fatma Jale

    2014-01-01

    This study was carried out on mostly imported, processed petrocokes, which are also commercially known as "petcoke" or "petroleum coke". Petrocoke is imported in great amounts and is occasionally consumed domestically without conscientious thought. It is not a well-known material, though there is an idea of its genesis. The samples, their analysis, and their images are essential to be kept in mind for further investigations, since it is not an environmental...

  5. Assessment of PAH-exposure among coke oven workers

    Energy Technology Data Exchange (ETDEWEB)

    Vahakangas, K. [and others] [Oulu University, Oulu (Finland)

    1992-12-31

    Levels of BaP diol epoxide - DNA adducts in urine and blood were monitored for workers at the Raahe coking plant, Finland, and other relevant information was collected. All adduct values were low, but oven battery workers had slightly higher values than matched controls. Antibodies to these adducts increased somewhat after work at the plant started, no differences between smokers and non-smokers were found.

  6. Lung function in retired coke oven plant workers.

    OpenAIRE

    Chau, N.; Bertrand, J P; Guenzi, M.; Mayer, L; Téculescu, D; Mur, J M; Patris, A.; Moulin, J J; Pham, Q T

    1992-01-01

    Lung function was studied in 354 coke oven plant workers in the Lorraine collieries (Houillères du Bassin de Lorraine, France) who retired between 1963 and 1982 and were still alive on 1 January 1988. A spirometric examination was performed on 68.4% of them in the occupational health service. Occupational exposure to respiratory hazards throughout their career was retraced for each subject. No adverse effect of occupational exposure on ventilatory function was found. Ventilatory function was,...

  7. Partial briquetting vs direct addition of biomass in coking blends

    OpenAIRE

    Montiano Redondo, María de Garabandal; Díaz-Faes González, Elvira; Barriocanal Rueda, Carmen

    2014-01-01

    In this work partial briquetting is employed as a means of biomass densification to allow for biomass inclusion in coking coal blends. The effect of increasing the bulk density was evaluated by comparison with direct addition. Two briquettes of different composition were studied. The influence of the briquettes on the Gieseler plasticity of the coals was determined. It was found that the effect of the binder was not enough to compensate for the decrease in plasticity produced by the inert com...

  8. Prediction of coking dynamics for wet coal charge

    OpenAIRE

    Kardaś Dariusz; Polesek-Karczewska Sylwia; Ciżmiński Przemysław; Stelmach Sławomir

    2015-01-01

    A one-dimensional transient mathematical model describing thermal and flow phenomena during coal coking in an oven chamber was studied in the paper. It also accounts for heat conduction in the ceramic oven wall when assuming a constant temperature at the heating channel side. The model was solved numerically using partly implicit methods for gas flow and heat transfer problems. The histories of temperature, gas evolution and internal pressure were presented and analysed. The theoretical predi...

  9. Milling Process of Petroleum Coke for Sintered Steel Applications

    OpenAIRE

    Velasco, F.; S. Guzmán; Rabanal, M. E.; Jiménez-Mateos, J. M.; Echeberria, J.; Ayerbe, E.; Calero, J.

    2011-01-01

    The effect of milling on different properties of a petroleum coke has been evaluated. The material was subjected to planetary milling at two different rates (400 and 600 rev min-1) for different times up to 48 h. The milled material was characterised by scanning electron microscopy, X-ray diffraction, sieve analysis, thermal analysis, chemical analysis, specific surface area and compressibility has been undertaken. The results show that the milling produces a very quick loss of the crystal st...

  10. Technology for Coking of Heavy Crude Oil with High Acid Number

    Institute of Scientific and Technical Information of China (English)

    Jiang Wen; Zhao Yujun; Cheng Gang; Li Chao; Shen Haiping; Cui Long

    2005-01-01

    Sudan Khartoum Refinery Co. has selected a unique route featuring delayed coking of crude in connection with the highly sour and high-calcium heavy crude extracted from Sudanese oil block No. 6.The crude oil after pretreatment for calcium removal is subjected to coking for removal of acids and metals with the coker products being further processed. The crude oil extracted from Sudanese oil block No. 6contains as high as 13 mg KOH/g of crude in addition to a calcium content of 1600 ppm. This article makes an analysis on problems related with the operation of commercial delayed coking unit for processing of highly sour crude and bring forth measures to solve these problems. The liquid yield resulted from coking of crude oil can reach 82m%, and the petroleum coke can meet the quality requirement for class 3B petroleum coke.

  11. Charging trolley for coke oven. Beskikingsvogn for koksovn

    Energy Technology Data Exchange (ETDEWEB)

    Gregor, K.; Feldhaus, K.

    1984-06-04

    The patent application describes a charging trolley for coke ovens. The trolley has a cover raising device which may be moved along a vertical track in order to raise covers for the oven sharge openings. At the coking process considerable amounts of combustion and coke gases are liberated. They contain large amounts of pollutants such as dust, finely devided solids and various other components. The pollutants settle on the convers and at the openings which leads to less satisfactory stopping and a leak of gases containing such pollutants to the surroundings. In order to avoid or at least reduce considerably such leaks in a simple and reliable way and with little loss of time, a cover cleaning device is constructed. It has at least 2 cleaning segments equipped with cleaning devices wich may move between a position swung away from and one covering the motion track. By help of the cleaning device it is possible to clean the stopper sheets on the covers without disturbing the operation. As a result the opening stoppers are improved and undesired pollution is considerably reduced. The claims concern the design of the charge trolley and the covering and cleaning devices in particular. 4 drawings.

  12. Formation of coke precursors from pyrene-based model compounds

    Energy Technology Data Exchange (ETDEWEB)

    Alshareef, Ali H.; Gray, Murray R. [Department of Chemical and Materials Engineering, University of Alberta (Canada)], email: murray.gray@ualberta.ca; Azyat, Khalid [Department of Chemistry, University of Alberta (Canada); Tykwinski, Rik [Friedrich-Alexander-Universitat (Germany)

    2010-07-01

    This work highlights understanding the thermal behavior and coking mechanism of pyrene-based model compounds. Microcarbon residue (MCR) was estimated for a thermally cracked model compound (Py-m-Phenyl-Py) using a thermal gravimetric analyzer (TGA). Nevertheless, when the coke produced by this process was analyzed it revealed insignificant information; hence, microreactor experiments were implemented to better analyze residual structures. Py-m-Phenyl-Py was converted with 30% and a mass spectrometry was performed on high molecular weight products, whereas, low molecular cracked weight products were analyzed using GC-MS. It was shown that the products obtained from this process matched those obtained by free-radical cracking. Moreover, MALDI-TOF analysis was used to reveal the addition product, and a spectrum of products was generated. It was shown that most of these products were yielded from the same species. It was believed that cyclization might be characterized by the dehydrogenation of the addition products, and coke precursors were generated due to olefin formation and radical additions.

  13. Human health risk characterization of petroleum coke calcining facility emissions.

    Science.gov (United States)

    Singh, Davinderjit; Johnson, Giffe T; Harbison, Raymond D

    2015-12-01

    Calcining processes including handling and storage of raw petroleum coke may result in Particulate Matter (PM) and gaseous emissions. Concerns have been raised over the potential association between particulate and aerosol pollution and adverse respiratory health effects including decrements in lung function. This risk characterization evaluated the exposure concentrations of ambient air pollutants including PM10 and gaseous pollutants from a petroleum coke calciner facility. The ambient air pollutant levels were collected through monitors installed at multiple locations in the vicinity of the facility. The measured and modeled particulate levels in ambient air from the calciner facility were compared to standards protective of public health. The results indicated that exposure levels were, on occasions at sites farther from the facility, higher than the public health limit of 150 μg/m(3) 24-h average for PM10. However, the carbon fraction demonstrated that the contribution from the calciner facility was de minimis. Exposure levels of the modeled SO2, CO, NOx and PM10 concentrations were also below public health air quality standards. These results demonstrate that emissions from calcining processes involving petroleum coke, at facilities that are well controlled, are below regulatory standards and are not expected to produce a public health risk. PMID:26520182

  14. Identification of causes of oil sands coke leachate toxicity

    Energy Technology Data Exchange (ETDEWEB)

    Puttaswamy, N.; Liber, K. [Saskatchewan Univ., Regina, SK (Canada)

    2010-07-01

    The potential causes of oil sands coke leachate toxicity were investigated. Chronic 7-day toxicity tests were conducted to demonstrate that oil sands coke leachates (CL) are acutely toxic to Ceriodaphnia dubia (C. dubia). CLs were generated in a laboratory to perform toxicity identification evaluation (TIE) tests in order to investigate the causes of the CL toxicity. The coke was subjected to a 15-day batch leaching process at 5.5 and 9.5 pH values. The leachates were then filtered and used for chemical and toxicological characterization. The 7-day estimates for the C. dubia survival were 6.3 for a pH of 5.5 and 28.7 per cent for the 9.5 CLs. The addition of EDTA significantly improved survival and reproduction in a pH of 5.5 CL, but not in a pH of 9.5 CL. The toxicity of the pH 5.5 CL was removed with a cationic resin treatment. The toxicity of the 9.5 pH LC was removed using an anion resin treatment. Toxicity re-appeared when nickel (Ni) and vanadium (V) were added back to the resin-treated CLs. Results of the study suggested that Ni and V were acting as primary toxicants in the pH 5.5 CL, while V was the primary cause of toxicity in the pH 9.5 CL.

  15. Wet oxidation of real coke wastewater containing high thiocyanate concentration.

    Science.gov (United States)

    Oulego, Paula; Collado, Sergio; Garrido, Laura; Laca, Adriana; Rendueles, Manuel; Díaz, Mario

    2014-01-01

    Coke wastewaters, in particular those with high thiocyanate concentrations, represent an important environmental problem because of their very low biodegradability. In this work, the treatment by wet oxidation of real coke wastewaters containing concentrations of thiocyanate above 17 mM has been studied in a 1-L semi-batch reactor at temperatures between 453 and 493 K, with total oxygen pressures in the range of 2.0-8.0 MPa. A positive effect of the matrix of real coke wastewater was observed, resulting in faster thiocyanate degradation than was obtained with synthetic wastewaters. Besides, the effect of oxygen concentration and temperature on thiocyanate wet oxidation was more noticeable in real effluents than in synthetic wastewaters containing only thiocyanate. It was also observed that the degree of mineralization of the matrix organic compounds was higher when the initial thiocyanate concentration increased. Taking into account the experimental data, kinetic models were obtained, and a mechanism implying free radicals was proposed for thiocyanate oxidation in the matrix considered. In all cases, sulphate, carbonates and ammonium were identified as the main reaction products of thiocyanate wet oxidation. PMID:24269931

  16. An additive for a petroleum coke and water suspension

    Energy Technology Data Exchange (ETDEWEB)

    Khiguti, K.; Igarasi, T.; Isimura, Y.; Kharaguti, S.; Tsudzina, T.

    1983-03-04

    The patent covers an additive for a petroleum coke and watersuspension which contains soap of an aliphatic acid (AM) and or a salt of a maleic acid copolymer (SMK). The aliphatic acid soap is a salt of an alkaline earth metal of C6 to C22 aliphatic acid, an ammonium salt or a salt of a lower amine. The maleic acid copolymer is a salt (sodium, NH4) of a lower amine of a maleic anhydride copolymer with a copolymerizing vinyl additive. Capric acid, lauric acid, palmatic acid, aleic and other acids may be used as the aliphatic acid, while methylamine, trimethylamine, diethanolamine, morpholine and so on may be used as the lower amine salt. Ethylene, vinylchloride, methyl(meta)acrylate and so on are used as the polymerizing vinyl compound. The molar ratio of the maleic anhydride to the polymerizing vinyl compound is in a range from 1 to 1 to 1 to 10 (preferably 1 to 1 to 1 to 3). The maleic acid copolymer has a mean molecular mass within 1,000 to 5,000. The additive with the optimal composition contains a solvent, a thickener, an anticorrosion substance, anticoagulants, surfacants (PAV) and so on. A highly concentrated suspension of oil coke and water with a 50 to 75 percent concentration of powder form petroleum coke may be produced using the patented additive. Such a suspension is characterized by low viscosity, high stability and forms no foam during processing.

  17. Human health risk characterization of petroleum coke calcining facility emissions.

    Science.gov (United States)

    Singh, Davinderjit; Johnson, Giffe T; Harbison, Raymond D

    2015-12-01

    Calcining processes including handling and storage of raw petroleum coke may result in Particulate Matter (PM) and gaseous emissions. Concerns have been raised over the potential association between particulate and aerosol pollution and adverse respiratory health effects including decrements in lung function. This risk characterization evaluated the exposure concentrations of ambient air pollutants including PM10 and gaseous pollutants from a petroleum coke calciner facility. The ambient air pollutant levels were collected through monitors installed at multiple locations in the vicinity of the facility. The measured and modeled particulate levels in ambient air from the calciner facility were compared to standards protective of public health. The results indicated that exposure levels were, on occasions at sites farther from the facility, higher than the public health limit of 150 μg/m(3) 24-h average for PM10. However, the carbon fraction demonstrated that the contribution from the calciner facility was de minimis. Exposure levels of the modeled SO2, CO, NOx and PM10 concentrations were also below public health air quality standards. These results demonstrate that emissions from calcining processes involving petroleum coke, at facilities that are well controlled, are below regulatory standards and are not expected to produce a public health risk.

  18. Effect of pretreatment methods of raw material on coking of needle coke from coal tar pitch by delayed coking%原料预处理方法对延迟焦化成焦的影响

    Institute of Scientific and Technical Information of China (English)

    吴甦; 王磊; 王小冰; 菜闯

    2012-01-01

    介绍了针状焦的工业生产方法,分析了不同的原料软沥青处理方法以及原料的结构和组成对延迟焦化成焦的影响.%The methods of manufacturing needle coke were introduced. And the effects of different pretreatment methods, the structure and composition of the raw material on the formation of needle coke from coal tar pitch by delayed coking were analyzed.

  19. 46 CFR 148.04-17 - Petroleum coke, calcined, at 130 °F or above.

    Science.gov (United States)

    2010-10-01

    ... 46 Shipping 5 2010-10-01 2010-10-01 false Petroleum coke, calcined, at 130 °F or above. 148.04-17...-17 Petroleum coke, calcined, at 130 °F or above. (a) The requirements of this part do not apply to bulk shipments of petroleum coke, calcined, on any vessel when the material is less than 130 °F....

  20. China's Coke Industrial and Trade Policy Over 2000–2013: Its Evolution and Effects

    OpenAIRE

    Shuyun Wang; Zesheng Sun

    2014-01-01

    This paper systematically discusses the evolution of China's industrial and trade policy regarding coke and the effects of this policy over the past decade, particularly from 2004 to 2013. We found that: (1) due to the impact of China's strict industrial policies, the country's coal and coke industry is still competitive. These policies have also helped the Chinese government achieve its goal of maintaining security and energy conservation. (2) China's coke trade policies did not reduce the v...

  1. THE EFFECT OF HYDROGEN ON COKE REMOVAL FROM Ga/HZMS5 CATALYSTS

    Directory of Open Access Journals (Sweden)

    M.G.F. Rodrigues

    1997-09-01

    Full Text Available The presence of gallium on HZMS5 zeolites increases the rate of coke elimination in their regeneration in hydrogen. The gallium species should contribute to the hydrogenation of the coke molecules and the acid sites should favour their crackings. However, the location of the coke molecules (near the outer surface and near the gallium species instead of their nature seems to be the determining parameter for their elimination

  2. THE EFFECT OF HYDROGEN ON COKE REMOVAL FROM Ga/HZMS5 CATALYSTS

    OpenAIRE

    Rodrigues M.G.F.; Magnoux P.; Guisnet M.; Choudhary V.R.

    1997-01-01

    The presence of gallium on HZMS5 zeolites increases the rate of coke elimination in their regeneration in hydrogen. The gallium species should contribute to the hydrogenation of the coke molecules and the acid sites should favour their crackings. However, the location of the coke molecules (near the outer surface and near the gallium species) instead of their nature seems to be the determining parameter for their elimination

  3. Effect Coke and Metal Deposition on Catalyst Deactivation of Early Stages of Resid Hydrodesulfurization Operation

    OpenAIRE

    出井, 一夫; 高橋, 武重; 甲斐, 敬美; IDEI, Kazuo; TAKAHASHI, Takeshige; KAI, Takami

    2001-01-01

    The hydrodesulfurization reaction with two kinds of atmospheric residues was carried out over three kinds of catalysts with different mean pore diameters to obtain catalysts with different deposited amounts of coke and metal on their surfaces. Elemental analysis and physical properties were carried out to elucidate the effects of coke and metal depositions on catalyst deactivation at an early stage of the reaction. Coke density (pc) and metal density (pm) calculated from the mean pore diamete...

  4. Granulation of coke breeze fine for using in the sintering process

    OpenAIRE

    Mohamed F.M.; El-Hussiny N.A.; Shalabi M.E.H.

    2010-01-01

    Coke breeze is the main fuel used in the sintering process. The value of -3+1 mm. represents the most favorable particle size for coke breeze in the sintering process. About 20% of total coke fines (-0.5 mm) are produced during different steps of preparation. Introducing these fines during the sintering process proves to be very harmful for different operating parameters. Thus ,this study aims at investigating the production of granules resulting from these fines using molasses as organ...

  5. Comparison of the quality of the coke produced at different scales

    OpenAIRE

    Díaz-Faes González, Elvira; García Cimadevilla, José Luis; Barriocanal Rueda, Carmen; Díez Díaz-Estébanez, M.ª Antonia; Álvarez García, Ramón

    2007-01-01

    A series of coking coals covering a wide range of coalification, thermoplastic properties and geographical origin were carbonized at two different scales. All the coals used are available in the international market and they are used by the cokemaking industry in blend preparation. The cokes were produced in two movable wall ovens of 15 and 300 kg capacity available at INCAR-CSIC facilities. The quality of the cokes was assessed by means of reactivity towards carbon dioxide and mechanical ...

  6. Modélisation thermomécanique d'un piédroit de four à coke

    OpenAIRE

    Landreau, Matthieu

    2009-01-01

    This study lies within the framework of European project called Coke Oven Operating Limits. This thesis deals with the thermomechanical modelling of a coke oven heating wall. The heating wall is an alveolar masonry, heated thanks to gas at high temperature (superior to 1200°C). During coking time in coke ovens, there is a pyrolysis of coal to coke which implies a coke swelling pressure on chamber wall. The aim of this project is to determine the maximal lateral pressure allowed by these struc...

  7. High PCI and low coke rate BF operation in ArcelorMittal Flat Carbon Europe

    Energy Technology Data Exchange (ETDEWEB)

    Dauwels, G.; Clairay, S.; Hess, E.; Janz, J.; Goimard, J.C.; Eymond, J.L. [ArcelorMittal (France)

    2008-07-01

    Coke production capacity within ArcelorMittal is not sufficient to provide the amount of coke needed for the total hot metal production. In order to address the challenges regarding coke availability, ArcelorMittal Flat Carbon Europe (FCE) sector has applied a low coke operation pulverized coal injection (PCI) technology to 17 of its blast furnaces across Europe. This paper described the charging pattern, blast conditions, hearth drainage and burden quality needed for high PCI rates. The coal injection rates of the different blast furnaces has been increased from 150-180 kg/thm to 180-200 kg/thm with a good replacement ratio. The lessons learned from high coal injection rate operations were discussed. The long term objective for FCE is to average a coal injection level of 200-220 kg/thm. This paper also discussed issues of coal quality, such as selection of coal; influence of coal quality on the blast furnace operation; and influence of coke quality on hearth drainage and hot metal quality. Coke quality was also discussed in terms of coke requirements and new global coke quality parameters. The difficulties in increasing PCI rate were shown to be associated with ferrous burden quality, particularly sinter. Adjustments to coke layer thickness can prevent instabilities. 8 refs., 23 figs.

  8. Analysis of changes in the chemical composition of the blast furnace coke at high temperatures

    Directory of Open Access Journals (Sweden)

    A. Konstanciak

    2012-12-01

    Full Text Available Purpose: The main purpose of this paper was to analyze the behavior of coke in the blast furnace. The analysis of changes in chemical composition of coke due to impact of inert gas and air at different temperatures was made. The impact of the application of the thermoabrasion coefficient on the porosity of coke was also analyzed.Design/methodology/approach: By applying the Computer Thermochemical Database of the TERMO system (REAKTOR1 and REAKTOR3 three groups of substances can be distinguished. The chemical composition of blast furnace coke and the results of calculations of changes of chemical composition of coke heat treated under certain conditions were compared. The structural studies of these materials were presented.Findings: The results of the analysis of ash produced from one of Polish cokes was taken for consideration. This is not the average composition of Polish coke ashes, nevertheless it is representative of most commonly occurring chemical compositions.Practical implications: Thanks to the thermochemical calculations it is possible to predict ash composition after the treatment in a blast furnace. Those information was crucial and had an actual impact on determining the coke quality.Originality/value: Presentation of the analytical methods which, according to author, can be very useful to evaluate and identify the heat treatment for blast furnaces cokes. The research pursued represents part of a larger project carried out within the framework of Department Extraction and Recycling of Metals, Czestochowa University of Technology.

  9. Relevance of the composition of municipal plastic wastes for metallurgical coke production

    Energy Technology Data Exchange (ETDEWEB)

    S. Melendi; M.A. Diez; R. Alvarez; C. Barriocanal [Instituto Nacional del Carbon (INCAR), Oviedo (Spain)

    2011-04-15

    This study is concerned with the effects of the composition of mixed plastic wastes on the thermoplastic properties of coal, the generation of coking pressure and the quality of the resulting cokes in a movable wall oven at semipilot scale. The mixed plastic wastes were selected to cover a wide spectrum in the relative proportions of high- and low-density polyethylenes (HDPE and LDPE), polypropylene (PP), polystyrene (PS) and polyethylene terephthalate (PET). From the results it was deduced that the reduction in Gieseler fluidity in the coal blend is linked to the total amount of polyolefins in the waste. It was also found that these thermoplastics increase the pressure exerted against the wall in the course of the coking process and that coke quality is maintained or even improved. However, when the level of aromatic polymers such PS and PET are increased at the expense of polyolefins, the coking pressure decreases. Thus, the amount of aromatic polymers such as PS and PET in the waste is critical, not only for controlling Gieseler fluidity and coking pressure, but also for avoiding deterioration in coke quality (reactivity towards CO{sub 2} CRI and mechanical strength of the partially-gasified coke CSR). An amount of polyolefins in the waste lower than 65 wt.% for a secure coking pressure is established. 43 refs., 7 figs., 4 tabs.

  10. Graphitization of Coke and Its Interaction with Slag in the Hearth of a Blast Furnace

    Science.gov (United States)

    Li, Kejiang; Zhang, Jianliang; Liu, Yanxiang; Barati, Mansoor; Liu, Zhengjian; Zhong, Jianbo; Su, Buxin; Wei, Mengfang; Wang, Guangwei; Yang, Tianjun

    2016-04-01

    Coke reaction behavior in the blast furnace hearth has yet to be fully understood due to limited access to the high temperature zone. The graphitization of coke and its interaction with slag in the hearth of blast furnace were investigated with samples obtained from the center of the deadman of a blast furnace during its overhaul period. All hearth coke samples from fines to lumps were confirmed to be highly graphitized, and the graphitization of coke in the high temperature zone was convinced to start from the coke surface and lead to the formation of coke fines. It will be essential to perform further comprehensive investigations on graphite formation and its evolution in a coke as well as its multi-effect on blast furnace performance. The porous hearth cokes were found to be filled up with final slag. Further research is required about the capability of coke to fill final slag and the attack of final slag on the hearth bottom refractories since this might be a new degradation mechanism of refractories located in the hearth bottom.

  11. System for reducing emissions during coke oven charging; System zur Emissionsverringerung beim Fuellen von Koksoefen

    Energy Technology Data Exchange (ETDEWEB)

    Schuecker, Franz-Josef [ThyssenKrupp Industrial Solutions AG, Dortmund (Germany). Head of Oven Machine Dept., Coke Plant Technologies

    2014-10-01

    This article describes a process which reduces emissions from coke production in coke plants. The focus is on the charging process, which can be partly responsible for the fact that statutory emissions limits, which were originally met, are exceeded as coke plants get older. This article presents a solution in the form of a newly developed system that allows the oven charging system - the charging car - to respond to age-related changes in the geometry of a coke oven and thereby reduce the level of emissions.

  12. Application of SketchUp in Coke Oven Three-Dimensional Digital Modeling

    OpenAIRE

    Shuguang Ouyang; Jie Xu; Xiaoli Su; Zikan Wang

    2013-01-01

    Coke oven, which is a large industrial furnace, is complex in structure. A two-dimensional structure diagram can hardly help one observe the inner structure of a coke oven or master its working principle comprehensively. In order to solve this problem, a complete 3D digital model of a coke oven is generated by assembling the three-dimensional models of coke oven components created with SketchUp. It enables users to section the various components of the cove oven. The outer appearance and inne...

  13. Feedback control strategy of longitudinal temperature and finished carbonization time for coke oven and its application

    Institute of Scientific and Technical Information of China (English)

    Fang Huo; Zhi Wen; Dong Chen; Yueling Shen; Yongqin Zhang; Xiaoming Zhi

    2004-01-01

    Based on the detailed analysis of the third coke oven in BaoSteel, a feedback control strategy of longitudinal temperature and finished carbonization time of coke ovens was proposed and it was applied to the third coke oven in BaoSteel. As a result, the ratio of the instance that the absolute deviation of the longitudinal temperature is within ±7°C and the finished carbonization time within ± 10 rain is more than 80%, having acquired the patent saving effect of an energy consumption lowered by 2.92%. At the same time, it can provide an example for the same coke ovens inside and outside the nation.

  14. Smoke and Dust Control During Coke Discharging from Coking Oven%焦炉出焦过程中的烟尘治理

    Institute of Scientific and Technical Information of China (English)

    王晓琴; 郝志强

    2011-01-01

    In order to control the smoke phenomenon during the coke discharging from the coking oven,the smoke and dust sources during the coke discharging from the coking oven in the Coking Plant of Taiyuan Town Gas Company were analyzed.In the comparison with three smoke and dust control alternatives,the second dust control system added on the coke receiving car was proposed to solve the smoke and dust problem.The applied results showed that the smoke and dust during the coke discharging was effectively controlled after the second dust control system measure applied.%为治理焦炉出焦过程中的冒烟现象,分析了太原煤气公司焦化厂焦炉出焦过程中的烟尘来源,通过对比3种治理烟尘的方案,提出采用在拦焦车上增加二次除尘系统的方法解决烟尘问题。实施结果表明,采用此措施后使出焦过程中散发的烟尘量得到了有效治理。

  15. Parametric Study of Gasification of the Mexican Petroleum Coke: Effect Feed Petroleum Coke on Energetic Characteristic of the Synthetic Gas (syngas)

    OpenAIRE

    Longoria-Ramírez R.; González-Rocha J.C.; Urquiza-Beltrán G.

    2011-01-01

    In this work, a parametric study the gasification of the Mexican petroleum coke from the refineries of Cd Madero (CRM) and Cadereyta, Nuevo León (CRC) is performed. It is evaluates the energy behavior of the gasification process with objective to research which feedstock of petroleum coke has a be?? er yield of energy. Effect feed petroleum coke on energy characteristics of the clear synthetic gas (gasl): molar composition of CO and H2, High Heating Value (HHVgasl), energy power (Ogasl), Cold...

  16. Effects of Coke Calcination Level on Pore Structure in Carbon Anodes

    Science.gov (United States)

    Fang, Ning; Xue, Jilai; Lang, Guanghui; Bao, Chongai; Gao, Shoulei

    2016-02-01

    Effects of coke calcination levels on pore structure of carbon anodes have been investigated. Bench anodes were prepared by 3 types of cokes with 4 calcination temperatures (800°C, 900°C, 1000°C and 1100°C). The cokes and anodes were characterized using hydrostatic method, air permeability determination, mercury porosimetry, image analysis and confocal microscopy (CSLM). The cokes with different calcination levels are almost the same in LC values (19-20 Å) and real density (1.967-1.985 g/cm3), while the anode containing coke calcined at 900°C has the lowest open porosity and air permeability. Pore size distribution (represented by Anode H sample) can be roughly divided into two ranges: small and medium pores in diameter of 10-400 μm and large pores of 400-580 μm. For the anode containing coke calcined at 800°C, a number of long, narrow pores in the pore size range of 400-580 μm are presented among cokes particles. Formation of these elongated pores may be attributed to coke shrinkages during the anode baking process, which may develop cracking in the anode under cell operations. More small or medium rounded pores with pore size range of 10-400 μm emerge in the anodes with coke calcination temperatures of 900°C, 1000°C and 1100°C, which may be generated due to release of volatiles from the carbon anode during baking. For the anode containing coke calcined at 1100°C, it is found that many rounded pores often closely surround large coke particles, which have potential to form elongated, narrow pores.

  17. Coke Formation During Hydrocarbons Pyrolysis. Part One: Steam Cracking Formation de coke pendant la pyrolise des hydrocarbures. Première partie : vapocraquage

    Directory of Open Access Journals (Sweden)

    Weill J.

    2006-11-01

    Full Text Available Thermal cracking is always accompanied by coke formation, which becomes deposited on the wall and limits heat transfers in the reactor while increasing pressure drops and possibly even plugging up the reactor. This review article covers undesirable coking operations in steam craking reactors. These coking reactions may take place in the gas phase and/or on the surface of the reactor, with coke being produced during pyrolysis by a complex mechanism that breaks down into a catalytic sequence and a noncatalytic sequence. After a brief description of different experimental set-ups used to measure the coke deposition, on the basis of research described in the literature, the different factors and their importance for coke formation are listed. In particular, we describe the effects of surface properties of stainless-steel and quartz reactors as well as the influence of the cracked feedstock, of temperature, of dilution, of residence time and of the conversion on coke deposition. Some findings about the morphology of coke are described and linked to formation mechanisms. To illustrate this review, some particularly interesting research is referred to concerning models developed to assess coke formation during propane steam cracking. Le craquage thermique est toujours accompagné de la formation de coke qui, en se déposant à la paroi, limite les transferts de chaleur au réacteur, augmente les pertes de charges et même peut boucher celui-ci. Cet article fait le point sur les réactions indésirables de cokage dans les réacteurs de vapocraquage. Ces réactions de cokage peuvent avoir lieu en phase gazeuse et/ou sur la surface du réacteur, le coke étant produit pendant la pyrolyse par un mécanisme complexe qui se décompose en une séquence catalytique et une séquence non catalytique. Après une brève présentation des différents montages expérimentaux utilisés pour mesurer le dépôt de coke, il est mentionné, à partir de travaux de la

  18. Preparation and Anti-coking Property of SiO2/S Coating on HP40 Tube

    Institute of Scientific and Technical Information of China (English)

    周建新; 徐宏; 张莉; 刘京雷; 戚学贵; 彭博

    2007-01-01

    SiO2/S coating was prepared on the inner surface of an HP40 tube using dimethyldisulfide and tetraethylorthosilicate by atmospheric pressure chemical vapor deposition (APCVD) to alleviate catalytic coking on the inner surface of radiant tube for ethylene production in petrochemical plants. The comparative coking experiments with the coated and uncoated HP40 tubes were carried out under the same cracking conditions. SiO2/S coating was compact and had excellent anti-coking property. The coke on the coated HP40 tube was about 22% of that on the uncoated HP40 tube, and only small granular coke was deposited on the coated HP40 tube. However, the filamentous coke formed on the uncoated HP40 tube. The thermal stability of SiO2/S coating was satisfactory at cracking temperature, and the anti-coking property of SiO2/S coating was still over 60% after 3 coking and decoking cycles.

  19. On-site raw gas cut-off during the shut down of Baosteel phase I coke ovens

    Institute of Scientific and Technical Information of China (English)

    ZHOU Haizhong

    2015-01-01

    The preparation and implementation of raw coke oven gas cut-off,which was the key process involved with shutting down the Baosteel phase I coke ovens,were investigated,and the main technical points and countermeasures are presented.

  20. 焦炉推焦粉尘治理工艺选择及设备配置%Technological Selection of Dust Treatment and Equipment Collocation While Coking in Coke Oven

    Institute of Scientific and Technical Information of China (English)

    姜乃斌; 邢显昌

    2012-01-01

      The article probes into the technological selection of dust treatment and equipment col ocation while coke choosing in coke oven; makes focus on and analyzes the three main topics of flue dust col ection, transportation and dust filter-ing of dust treatment in coke oven tapping.

  1. Modulating influence of cytochrome P-450 MspI polymorphism on serum liver function profiles in coke oven workers

    OpenAIRE

    Wu, M T; Ho, C.K.; Huang, S.L.; Yeh, Y. F.; C. L. Liu; Mao, I F; Christiani, D C

    1999-01-01

    OBJECTIVES: It was reported previously that topside oven workers with heavy exposure to coke oven emissions had increased serum activities of hepatic aminotransferase in one coke oven plant. This study was conducted to investigate the modifying effect of CYP1A1 MspI polymorphism on liver function profiles in coke oven workers. METHODS: 88 coke oven workers from a large steel company in Taiwan were studied in 1995-6. Exposure was categorised by work area: topside oven workers and sideove...

  2. Characterization of semi-coke generated by coal-based direct reduction process of siderite

    Institute of Scientific and Technical Information of China (English)

    朱德庆; 罗艳红; 潘建; 周仙霖

    2015-01-01

    Solid wastes derived from metallurgical industries pose a significant threat to environment. The utilization and disposal of these solid wastes are the major concern in the world. Semi-coke generated in coal-based direct reduction process of iron ore is a by-product and its suitable utilization is not available so far. In order to handle it properly, the characteristics of this by-product were comprehensively investigated. A series of analysis methods were used to demonstrate its mineral compositions, petrography and physico-chemical properties. The results reveal that the semi-coke has poor washability. The fixed carbon content of semi-coke reaches 76.11% and the gross calorific value is 28.10 MJ/kg, both of which are similar to those of traditional sinter coke breeze. Also, semi-coke ash possesses lower content of SiO2, Al2O3, S and higher content of CaO and MgO, which could improve the strength of sinter ore when partially substituting for coke breeze in sintering. Semi-coke features well-development porous structure and higher reaction activity, which predicts that the sintering speed could be elevated to some extent when employing it as a partial replacement of coke breeze, so the studies further suggest that the potential adverse effect of the high reactivity on sintering process could be weakened by adequately coarsening the semi-coke’s particle size.

  3. Application of fine-grained coke breeze fractions in the process of iron ore sintering

    Directory of Open Access Journals (Sweden)

    M. Niesler

    2014-01-01

    Full Text Available The testing cycle, described in the paper, included fine-grained coke breeze granulation tests and iron concentrate sintering tests with the use of selected granulate samples. The use of granulated coke breeze in the sintering process results in a higher process efficiency, shorter sintering duration and fuel saving.

  4. Influence of nut coke on iron ore sinter reducibility under simulated blast furnace conditions

    Energy Technology Data Exchange (ETDEWEB)

    Mousa, E.A.; Senk, D.; Babich, A.; Gudenau, H.W.

    2010-04-15

    One of the most important factors to increase the economic efficiency of the blast furnace process is to reduced coke losses (undersieve product known as nut coke). In recent years there has been increased interest in mixing nut coke in the sinter layers. In order to clarify the influence of nut coke on sinter reducibility, sinter and sinter-nut coke mixtures were isothermally reduced with 30%CO-70%N{sub 2} at 1173-1523 K using a muffle furnace supported by an on-line gas analyser. Reflected light microscopy, scanning electron microscopy and X-ray technique were used to characterise the microstructure and the different phases developed in the original and reduced sinter. Sinter reduced without nut coke participation exhibited reduction retardation at elevated temperatures (>1373 K) while the presence of nut coke prevented such phenomena. The rate controlling mechanism of sinter and sinter-nut coke mixture was predicted from the correlation between apparent activation energy calculations, mathematical modelling derived from gas-solid reaction model and microstructure examination.

  5. Nature of nitrogen specie in coke and their role in NOx formation during FCC catalyst regeneration.

    NARCIS (Netherlands)

    Babich, I.V.; Seshan, K.; Lefferts, L.

    2005-01-01

    NOx emission during the regeneration of coked fluid catalytic cracking (FCC) catalysts is an environmental problem. In order to follow the route to NOx formation and try to find ways to suppress it, a coked industrial FCC catalyst has been prepared using model N-containing compounds, e.g., pyridine,

  6. 77 FR 15123 - Foundry Coke From China; Scheduling of an Expedited Five-Year Review

    Science.gov (United States)

    2012-03-14

    ... its notice of institution (76 FR 74810, December 1, 2011) of the subject five-year review was adequate... COMMISSION Foundry Coke From China; Scheduling of an Expedited Five-Year Review AGENCY: United States...)) (the Act) to determine whether revocation of the antidumping duty order on foundry coke from...

  7. 76 FR 74810 - Foundry Coke From China; Institution of a Five-Year Review

    Science.gov (United States)

    2011-12-01

    ... duty order on imports of foundry coke from China (66 FR 48025). Following five-year reviews by Commerce... order on imports of foundry coke from China (72 FR 1214). The Commission is now conducting a second..., and F (19 CFR part 207), as most recently amended at 76 FR 61937 (October 6, 2011). \\1\\ No response...

  8. Recycling of waste mill oil through non-recovery coke making

    Energy Technology Data Exchange (ETDEWEB)

    Barman, S.C.; Kumar, P.P.; Patil, B.R.; Kinlekar, A.; Reddy, S. [JSW Steel Ltd., Karnataka (India)

    2009-07-01

    A plant scale trial was conducted to recycle the mill oil waste through non recovery coke oven route. The waste mill oil was added in the coal blend as a binder before hammer mill and charged in the ovens. JSW Steel has non-recovery coke ovens synergized with vibro-compaction technology to produce coke of 1.2 Mtpa. About 300 L of the mill oil which is generated in the hot strip mill daily was used in the trial. A cake density of 1.1 t/m{sup 3} has been achieved using vibro-compaction with optimized moisture, oil addition and crushing fineness. The coke produced with and without oil of same coal blend and coking conditions, was tested and compared. It is observed that utilization of mill oil has not shown any deteriorating effect on coke quality. There is a marginal increase in flue gas as well as oven crown temperature which helped to increase the power generation. This present paper describes the effect of mill oil addition on coke quality and the oven thermal conditions and the feasibility of recycling the waste through non recovery coke ovens at JSW Steel Ltd.

  9. Development and Application of Zero Expansion Silica Brick for Hot Repairing of Coke Oven

    Institute of Scientific and Technical Information of China (English)

    ZHANG Xiuqin; ZHI Xiaoming; WANG Hongmei

    2003-01-01

    In order to meet the needs of hot repairing technology of coke oven, the zero expansion silica brick with super properties has been developed, and the problem of poor thermal stability of common silica brick has been overcomned. This product can be directly used after being rapidly heated after construction. At present, it has been applied in coke ovens in Italy and Baosteel.

  10. RECOVERY AND DESTRUCTIVE TREATMENT OF HARMFUL SUBSTANCE IN COKING PLANT WASTEWATER

    Institute of Scientific and Technical Information of China (English)

    Cheng Jianguang

    2000-01-01

    This paper discussed the comprehensive treatment of coking plant effluent.Cyanide-containing and phenol wastewater was first recovered and utilized respectively, and then, mixed it with other low harmful wastewater for destroying treatment.Treated water was reused in quenching coke.

  11. Coal and coke - analysis and testing. Determination of trace elements. Coal, coke and fly-ash. Determination of fluorine content. Pyrohydrolysis method

    Energy Technology Data Exchange (ETDEWEB)

    NONE

    2001-06-29

    This Standard sets out a procedure for the pyrohydrolytic separation of fluorine from coal, coke and fly-ash and for determination of fluorine by gravimetric processing and either ion potentiometry or ion chromatography.

  12. Application of 150t/h coke dry quenching technique in Bengang coke oven%150t/h干熄焦在本钢焦炉的应用

    Institute of Scientific and Technical Information of China (English)

    全喜红

    2009-01-01

    The main process of 150t/h coke dry quenching technique in Bengang No. 6 and 7 coke oven were introduced. According to actual operation data, the environmental protection effect and energy saving characteristic of coke dry quenching technology were analyzed. It will be of great importance in the application and dissemination of coke dry quenching technology, especially that of Chinese property.%介绍了本钢6、7号焦炉干熄焦的主要工艺流程,通过实际数据详细分析了干熄焦运行的节能效益及环保效应,对国内干熄焦技术推广与应用将起到积极的推动作用.

  13. Study on soot purifying of molding shop in coking factory

    Institute of Scientific and Technical Information of China (English)

    LI Duo-song; ZHANG Hui; BAI Xiang-yu

    2006-01-01

    Exhaust gas in molding shop was complicated in component and characteristic in Iow thickness asphalt smoke, mass steam-gas and dust. It was difficult to purify the soot with common purifier. So we must consider them roundly and develop new multifunction purifier. PFP multifunction soot purifier was made on the base of design optimization and was installed at Shenhuo Coking Factory in 2004. The combined effects of multi- mechanism in purifier make purifying ratio keep in high level. The remove ratio of smut reaches at 92.8%, and asphalt smoke at 83.7%.

  14. Failure analysis of the impellers of coke plant

    OpenAIRE

    Souvik Das; Goutam Mukhopadhyay; Sandip Bhattacharyya

    2014-01-01

    Premature failure of the impeller blade of coke plant has been investigated. The component functioned during the CGC gas intake cycle. The component rotates at 1480 rpm with a volumetric flow of 720 m3/min of flue gas with temperature about 200–300 °C. The failed component reveals exposed surface of a crack that extended slightly beyond the assembly weld. From macro-structural observation under-filled region in welding is observed which is detrimental because it acts as a stress concentration...

  15. The Kinetics for Electrochemical Removal of Ammonia in Coking Wastewater

    Institute of Scientific and Technical Information of China (English)

    LIANG Zhenhai; LI Su; GUO Wenqian; FAN Caimei

    2011-01-01

    Electrochemical removal of ammonia is a new and effective method in coking wastewater.The reaction mechanism of ammonia removal was proved by stable polarization curve in this paper.First,the supposing of reaction steps of the electrode were proposed.And then reaction parameter of the electrode was measured by Tafel curve.Finally,the reaction mechanism was determined by quasi-equilibrium approach.The results showed that Cl2+H2O→HOCl+H++Cl was the rate-determining step,the calculated apparent transfer coefficient was uniform to the experimental value.

  16. 76 FR 52350 - Coke Oven Emissions Standard; Extension of the Office of Management and Budget's (OMB) Approval...

    Science.gov (United States)

    2011-08-22

    ... Occupational Safety and Health Administration Coke Oven Emissions Standard; Extension of the Office of...) approval of the information collection requirements specified in the Standard on Coke Oven Emissions (29... requirements in the Coke Oven Emissions Standard provide protection for workers from the adverse health...

  17. Delayed coking studies on Athabasca bitumen and Cold Lake heavy oil

    Energy Technology Data Exchange (ETDEWEB)

    Govindhakannan, J.; Khulbe, C. [National Centre for Upgrading Technology, Devon, AB (Canada); Natural Resources Canada, Devon, AB (Canada). CanmetENERGY

    2009-07-01

    This poster highlighted the results of a study that quantified the delayed coking product yields of Athabasca bitumen and Cold Lake heavy oil. It also investigated the effect of operating pressure and feed rates on product yield and quality. The effect of pressure on conversion of sulphur and nitrogen was also examined. Experimental results revealed that the yield of liquid products decreases and the yields of coke and gases increase as the operating pressure increases. Sulphur and nitrogen conversions increase with increasing pressure. In this study, the yield and quality of delayed coking products were not influenced by the variation in feed rates. It was concluded that feed rate changes do not significantly affect the yield and quality of delayed coking products because the residual liquid and coke trapped in the coker drum reside there for a duration that approaches infinity, compared to much smaller average residence time for vapor-phase compounds. tabs., figs.

  18. Microwave-assisted grinding of metallurgical coke; Molienda asistida con microondas de un coque metalurgico

    Energy Technology Data Exchange (ETDEWEB)

    Ruisanchez, E.; Juarez-Perez, E. J.; Arenillas, A.; Bermudez, J. M.; Menendez, J. A.

    2014-10-01

    Metallurgical cokes are composed of graphitic carbon (s2p2) and different inorganic compounds with very different capacities to absorb microwave radiation. Moreover, due to the electric conductivity shown by the metallurgical cokes, microwave radiation produces electric arcs or microplasmas, which gives rise to hot spots. Therefore, when these cokes are irradiated with microwaves some parts of the particle experiment a rapid heating, while some others do not heat at all. As a result of the different expansion and stress caused by thermal the shock, small cracks and micro-fissures are produced in the particle. The weakening of the coke particles, and therefore an improvement of its grind ability, is produced. This paper studies the microwave-assisted grinding of metallurgical coke and evaluates the grinding improvement and energy saving. (Author)

  19. Effect of physical disturbance on the structure of needle coke - article no. 108101

    Energy Technology Data Exchange (ETDEWEB)

    Zhao, S.G.; Wang, B.C.; Sun, Q.A. [Taiyuan University of Technology, Taiyuan (China)

    2010-10-15

    Through different preparation technology, this paper reports that the needle coke is prepared with coal-tar pitch under the effect of magnetic field and ultrasonic cavitation. It studies the effect of physical disturbance on the structure of needle coke. The structure of needle coke is characterized by scanning electron microscope and x-ray diffractometer, and the influence mechanism is analysed. Results showed that the structure and property of needle coke could be effectively improved by magnetic field and ultrasonic cavitations, such as degree of order, degree of graphitization and crystallization. Comparatively speaking, the effect of magnetic field was greater. The graphitization degree of needle coke prepared under the effect of magnetic field is up to 45.35%.

  20. Application of SketchUp in Coke Oven Three-Dimensional Digital Modeling

    Directory of Open Access Journals (Sweden)

    Shuguang Ouyang

    2013-01-01

    Full Text Available Coke oven, which is a large industrial furnace, is complex in structure. A two-dimensional structure diagram can hardly help one observe the inner structure of a coke oven or master its working principle comprehensively. In order to solve this problem, a complete 3D digital model of a coke oven is generated by assembling the three-dimensional models of coke oven components created with SketchUp. It enables users to section the various components of the cove oven. The outer appearance and inner structure of the oven components also can be displayed visually from several different orientations. Moreover, it is convenient to storage and carry, operation easily and fast. It can be displayed on an ordinary computer and occupies no space at the laboratory. Meanwhile, a large sum of money that used for purchasing a physical coke oven model can be saved.

  1. Promoted slurryability of petroleum coke-water slurry by using black liquor as an additive

    Energy Technology Data Exchange (ETDEWEB)

    Zhan, Xiuli; Zhou, Zhijie; Wang, Fuchen [Key Laboratory of Coal Gasification of Ministry of Education, East China University of Science and Technology, Shanghai 200237 (China); Kang, Wanzhong [School of Resource and Environmental Engineering, East China University of Science and Technology, Shanghai 200237 (China)

    2010-10-15

    The purpose of this paper is to prepare the petroleum coke-water slurry with a maximal coke mass fraction and the superior slurry natures using black liquor as an additive. The variations of rheological properties, contact angle, fluidity, stability and zeta potential of the coke-water slurry with different black liquor dosages were investigated. It was observed that the addition of a black liquor dosage around 1.0 wt.% of the petroleum coke remarkably improved the rheological properties, fluidity and stability of the slurry, and the slurry could hold a mass of petroleum coke as high as 70 wt.%, with the superior apparent viscosity, fluidity and stability available for practical utilization. (author)

  2. Identification and removal of polycyclic aromatic hydrocarbons in wastewater treatment processes from coke production plants.

    Science.gov (United States)

    Zhang, Wanhui; Wei, Chaohai; Yan, Bo; Feng, Chunhua; Zhao, Guobao; Lin, Chong; Yuan, Mengyang; Wu, Chaofei; Ren, Yuan; Hu, Yun

    2013-09-01

    Identification and removal of polycyclic aromatic hydrocarbons (PAHs) were investigated at two coke plants located in Shaoguan, Guangdong Province of China. Samples of raw coking wastewaters and wastewaters from subunits of a coke production plant were analyzed using gas chromatography-mass spectrometry (GC/MS) to provide a detailed chemical characterization of PAHs. The identification and characterization of PAH isomers was based on a positive match of mass spectral data of sample peaks with those for PAH isomers in mass spectra databases with electron impact ionization mass spectra and retention times of internal reference compounds. In total, 270 PAH compounds including numerous nitrogen, oxygen, and sulfur heteroatomic derivatives were positively identified for the first time. Quantitative analysis of target PAHs revealed that total PAH concentrations in coking wastewaters were in the range of 98.5 ± 8.9 to 216 ± 20.2 μg/L, with 3-4-ring PAHs as dominant compounds. Calculation of daily PAH output from four plant subunits indicated that PAHs in the coking wastewater came mainly from ammonia stripping wastewater. Coking wastewater treatment processes played an important role in removing PAHs in coking wastewater, successfully removing 92 % of the target compounds. However, 69 weakly polar compounds, including PAH isomers, were still discharged in the final effluent, producing 8.8 ± 2.7 to 31.9 ± 6.8 g/day of PAHs with potential toxicity to environmental waters. The study of coking wastewater herein proposed can be used to better predict improvement of coke production facilities and treatment conditions according to the identification and removal of PAHs in the coke plant as well as to assess risks associated with continuous discharge of these contaminants to receiving waters. PMID:23589270

  3. The Transient Modal Dynamic Analysis of a Coke Tower

    Institute of Scientific and Technical Information of China (English)

    XIE Teng-teng; SUN Tie; XING Ling; ZHANG Su-xiang

    2012-01-01

    Dynamic analysis must be performed when the duration of the applied load is short or if the load is dynamic in nature. Wind load, as a random load, can lead to the vibration of the coke tower. In order to study the influence to the strength of the coke tower by wind, ABAQUS was used to conduct the transient modal dynamic analysis of the wind load. The response of the structure during loading and unloading was mainly observed. The results indicate that, with the effect of wind, the maximal nodal displacement appears at the top of the tower, which is 0.79 mm; while the maximal stress locates at the node around the skirt, the maximum is 3.26 MPa. Both of the displacement and stress cannot cause the failure of the structure. After loading and unloading, the structure engenders vibration along the loading direction. The frequency is 10 Hz, under the effect of external loads, it may easily cause the resonance of the structure, which can cause damage to the structure. So it must be taken into consideration during the process of design and operation.

  4. Mineralogy and phase transition of oil sands coke ash

    Energy Technology Data Exchange (ETDEWEB)

    Heemun Jang; Thomas H. Etsell [University of Alberta, Edmonton, AB (Canada). Department of Chemical and Materials Engineering

    2006-08-15

    Coke obtained from Syncrude and Suncor was investigated to characterize the metals and minerals by ashing it at various temperatures. Samples were collected by high temperature ashing at 100{sup o}C intervals from 400 to 1200{sup o}C. Samples were also obtained from low temperature ashing (LTA) which gives little effect on the mineral assemblage compared to HTA samples. X-ray diffraction patterns of Suncor and Syncrude coke ash were analyzed qualitatively and quantitatively to characterize the mineral phases in the sample and their thermal transition behavior. In Suncor ash, kaolinite, illite, gypsum, anhydrite, microcline, anorthite, hematite, sillimanite and quartz were dominant phases in ash from the LTA temperature up to 700{sup o}C, and mullite, cristobalite, hercynite, albite, anorthite, pseudobrookite and other iron-titanium oxides were dominant mineral phases from 700 to 1200{sup o}C. In Syncrude ash, illite, anhydrite, quartz, anorthite, microcline, sillimanite and hematite were dominant up to 700{sup o}C, and hercynite, anorthite, albite, pseudobrookite and other iron-titanium oxides were dominant up to 1200{sup o}C. The higher quantities of Ca, K and Na, and the lower quantities of V, Fe and Ni in Syncrude ash resulted in higher amorphocity and the different mineral phases. 32 refs., 3 figs., 5 tabs.

  5. An additive for a petroleum coke and water suspension

    Energy Technology Data Exchange (ETDEWEB)

    Khiguti, K.; Igarasi, T.; Isimura, Y.; Kharaguti, S.; Tsudzino, T.

    1982-10-18

    An additive to a petroleum coke and water suspension is proposed. The additive consists of a compound with the formula (RCONHCH2C(R')HO(AO)1H, where R is a C1 to C30 unsaturated acyl group, R' is hydrogen, CH3, A is C2 to C4 alkylene, l = 0 to 500, m + n = 0 to 1,000, salt of alkaline metal, salt of ammonium or salt of lower amine and sulfurous ether. The method may be used to produce an aqueous suspension which has a concentration of petroleum coke powder of 50 to 70 percent. The viscosity of the suspension is low, the stability high, no floculation or sedimentation are observed and there is no foam formation. Monoethanolamide, diethanolamide, monoesoproyanolamide and diisopropanolamide of C1 to C30 acid of the fatty series or alkylenoxide (ethylenoxide, propylenoxide, isobutylenoxide and tetrahydrofurane) are used as the (RCONHCH2C(R')HO(AO)1H and a lithium salt

  6. Treatment of coking wastewater by using manganese and magnesium ores

    Energy Technology Data Exchange (ETDEWEB)

    Chen Tianhu; Huang Xiaoming; Pan Min [School of Resources and Environmental Engineering, Hefei University of Technology, Hefei City 230009 (China); Jin Song, E-mail: sjin@uwyo.edu [MWH Americas, 3665 JFK Parkway, Suite 206, Fort Collins, CO 80525 (United States); Department Civil and Architectural Engineering, University of Wyoming, Laramie, WY 82071 (United States); Peng Suchuan [School of Resources and Environmental Engineering, Hefei University of Technology, Hefei City 230009 (China); Fallgren, Paul H. [Western Research Institute, 365 North 9th Street, Laramie, WY 82072 (United States)

    2009-09-15

    This study investigated a wastewater treatment technique based on natural minerals. A two-step process using manganese (Mn) and magnesium (Mg) containing ores were tested to remove typical contaminants from coking wastewater. Under acidic conditions, a reactor packed with Mn ore demonstrated strong oxidizing capability and destroyed volatile phenols, chemical oxygen demand (COD){sub ,} and sulfide from the coking wastewater. The effluent was further treated by using Mg ore to remove ammonium-nitrogen and phosphate in the form of magnesium ammonium phosphate (struvite) precipitates. When pH of the wastewater was adjusted to 1.2, the removal efficiencies for COD, volatile phenol and sulfide reached 70%, 99% and 100%, respectively. During the second step of precipitation, up to 94% of ammonium was removed from the aqueous phase, and precipitated in the form of struvite with phosphorus. The struvite crystals showed a needle-like structure. X-ray diffraction and transmission electron microscopy were used to characterize the crystallized products.

  7. Laser ultrasonic furnace tube coke monitor. Quarterly technical progress report No. 1, May 1--August 1, 1998

    Energy Technology Data Exchange (ETDEWEB)

    NONE

    1998-08-15

    The overall aim of the project is to demonstrate the performance and practical use of a laser ultrasonic probe for measuring the thickness of coke deposits located within the high temperature tubes of a thermal cracking furnace. This aim will be met by constructing an optical probe that will be tested using simulated coke deposits that are positioned inside of a bench-scale furnace. Successful development of the optical coke detector will provide industry with the only available method for on-line measurement of coke deposits. The optical coke detector will have numerous uses in the refining and petrochemical sectors including monitoring of visbreakers, hydrotreaters, delayed coking units, vacuum tower heaters, and various other heavy oil heating applications where coke formation is a problem. The coke detector will particularly benefit the olefins industry where high temperature thermal crackers are used to produce ethylene, propylene, butylene and other important olefin intermediates. The ethylene industry requires development of an on-line method for gauging the thickness of coke deposits in cracking furnaces because the current lack of detailed knowledge of coke deposition profiles introduces the single greatest uncertainty in the simulation and control of modern cracking furnaces. The laser ultrasonic coke detector will provide operators with valuable new information allowing them to better optimize the decoking turnaround schedule and therefore maximize production capacity.

  8. Preparation of modified semi-coke by microwave heating and adsorption kinetics of methylene blue.

    Science.gov (United States)

    Wang, Xin; Peng, Jin-Hui; Duan, Xin-Hui; Srinivasakannan, Chandrasekar

    2013-01-01

    Preparation of modified semi-coke has been achieved, using phosphoric acid as the modifying agent, by microwave heating from virgin semi-coke. Process optimization using a Central Composite Design (CCD) design of Response Surface Methodology (RSM) technique for the preparation of modifies semi-coke is presented in this paper. The optimum conditions for producing modified semi-coke were: concentration of phosphoric acid 2.04, heating time 20 minutes and temperature 587 degrees C, with the optimum iodine of 862 mg/g and yield of 47.48%. The textural characteristics of modified semi-coke were analyzed using scanning electron microscopy (SEM) and nitrogen adsorption isotherm. The BET surface area of modified semi-coke was estimated to be 989.60 m2/g, with the pore volume of 0.74 cm3/g and a pore diameter of 3.009 nm, with micro-pore volume contributing to 62.44%. The Methylene Blue monolayer adsorption capacity was found to be mg/g at K. The adsorption capacity of the modified semi-coke highlights its suitability for liquid phase adsorption application with a potential usage in waste water treatment. PMID:24779145

  9. Three-dimensional modelling of in-furnace coal/coke combustion in a blast furnace

    Energy Technology Data Exchange (ETDEWEB)

    Y.S. Shen; B.Y. Guo; A.B. Yu; P.R. Austin; P. Zulli [University of New South Wales, Sydney, NSW (Australia). Lab for Simulation and Modelling of Particulate Systems

    2011-02-15

    A three-dimensional mathematical model of the combustion of pulverized coal and coke is developed. The model is applied to the region of lance-blowpipe-tuyere-raceway-coke bed to simulate in-furnace phenomena of pulverized coal injection in an ironmaking blast furnace. The model integrates not only pulverized coal combustion model in the blowpipe-tuyere-raceway-coke bed but also coke combustion model in the coke bed. The model is validated against the measurements under different conditions. The comprehensive in-furnace phenomena are investigated in the raceway and coke bed, in terms of flow, temperature, gas composition, and coal burning characteristics. The underlying mechanisms for the in-furnace phenomena are also analysed. The simulation results indicate that it is important to include recirculation region in the raceway and the coke bed reactions for better understanding in-furnace phenomena. The model provides a cost-effective tool for understanding and optimizing the in-furnace flow-thermo-chemical characteristics of the PCI operation in full-scale blast furnaces. 32 refs., 10 figs., 3 tabs.

  10. The Release of Trace Elements in the Process of Coal Coking

    Directory of Open Access Journals (Sweden)

    Jan Konieczyński

    2012-01-01

    Full Text Available In order to assess the penetration of individual trace elements into the air through their release in the coal coking process, it is necessary to determine the loss of these elements by comparing their contents in the charge coal and in coke obtained. The present research covered four coke oven batteries differing in age, technology, and technical equipment. By using mercury analyzer MA-2 and the method of ICP MS As, Be, Cd, Co, Hg, Mn, Ni, Se, Sr, Tl, V, and Zn were determined in samples of charge coal and yielded coke. Basing on the analyses results, the release coefficients of selected elements were determined. Their values ranged from 0.5 to 94%. High volatility of cadmium, mercury, and thallium was confirmed. The tests have shown that although the results refer to the selected case studies, it may be concluded that the air purity is affected by controlled emission occurring when coke oven batteries are fired by crude coke oven gas. Fugitive emission of the trace elements investigated, occurring due to coke oven leaks and openings, is small and, is not a real threat to the environment except mercury.

  11. The effects of the coke addition and the heating time on the efficiency of chlorination process

    International Nuclear Information System (INIS)

    The preparation of mixed pellet, ZrO2, coke and sucrose, for chlorinating process of ZrO2 pellet has been performed. In this experiments the studied parameters were coke addition and the heating time. The addition of coke was 9.72 grams, 10.5 grams and 11 for the mixture of the 87 grams ZrO2 and 3.5 grams sucrose. The purpose of the coke addition is to from ZrC, which is corresponding to Kroll process with carbon-chlor methos. The weight of cokes had been calculated beyond the stoichiometry. The heating times was held in 10 minutes, 15 minutes, and 20 minutes at the temperature of 100oC that was below the evaporation coke temperature of 315oC. The result show that the efficiency of chlorinating of ZrO2 pellet could be reached of 82.16% with the addition of coke mass of 11 grams at the heating temperature of 100oC with the heating time of 20 minutes

  12. Parametric Study of Gasification of the Mexican Petroleum Coke: Effect Feed Petroleum Coke on Energetic Characteristic of the Synthetic Gas (syngas

    Directory of Open Access Journals (Sweden)

    Longoria-Ramírez R.

    2011-07-01

    Full Text Available In this work, a parametric study the gasification of the Mexican petroleum coke from the refineries of Cd Madero (CRM and Cadereyta, Nuevo León (CRC is performed. It is evaluates the energy behavior of the gasification process with objective to research which feedstock of petroleum coke has a be?? er yield of energy. Effect feed petroleum coke on energy characteristics of the clear synthetic gas (gasl: molar composition of CO and H2, High Heating Value (HHVgasl, energy power (Ogasl, Cold Gas Efficiency (CGEgasl and thermal efficiency of gasification (?tg is realized. The parametric study has been realized for 0.64 = oxygen/coke = 1.11 ratio with the fl ow of oxygen (6036.388 kg/h and steam/oxygen of 23% both constant. It is observed that in oxygen/coke 0.77 and 0.94 ratio it is present the best energy characteristics of the gasl from CRM and CRC, respectively. The best energy characteristics relationship of the gasl fined are: molar composition CO (65.6, 68.5, H2 (32.29, 29.13, HHVgasl (14054.6 kJ/kggasl, 13438.76 kJ/kggasl, Ogasl (204.86 GJ/h, 178.02 GJ/h, CGEgasl (74.43%, 71.14%, ?tg (86.2%, 83.22%. The gasification of petroleum coke CRM produced energy with 26.20 MJ/kgcoque rates whereas that gasification of the petroleum coke CRC produced 27.74 MJ/kgcoque rates.

  13. Effect of the surface properties of an activated coke on its desulphurization performance

    Institute of Scientific and Technical Information of China (English)

    ZHANG Xiang-lan; ZHANG Yan; DING Fang-sheng; HUANG Qi-jiang; LI Yuan

    2009-01-01

    Commercial coke was modified by H2O2 and/or NH3·H2O to obtain an activated coke containing additional oxygen func-tional groups and/or nitrogen functional groups. The aim of the modification was to enhance the SO2 adsorption capacity of the activated coke. Several techniques, including total nitrogen content measurements, SO2 adsorption, XPS and FTIR analysis, were used to characterize the coke samples. The XPS and FTIR spectra suggest the existence of-CONH2 groups in the H2O2 plus ammo-nia modified coke. The SO2 adsorption capacity of an activated coke increases slightly with an increase in H2O2 concentration dur-ing the modification process. The desulphurization performance of a modified coke is considerably enhanced by increasing the treatment temperature during ammonia modification. The amount of nitrogen in a coke modified by H2O2 plus NH3·H2O is the highest, and the SO2 adsorption capacity of the coke is also the highest (89.9 mg/gC). The NH3·H2O (only) modified sample has lower nitrogen content and lower desulphurization capacity (79.9 mg/gC). H2O modification gives the lowest SO2 adsorption capacity (28.9 mg/gC). The H2O2 pre-treatment is beneficial for the introduction of nitrogen onto the surface of a sample during the following ammonia treatment process.

  14. The correlation between nitrogen species in coke and NOx formation during regeneration☆

    Institute of Scientific and Technical Information of China (English)

    Teng Li; Chaohe Yang; Xiaobo Chen⁎; Libo Yao; Wei Liang; Xuemei Ding

    2016-01-01

    Nitrogen oxides (NOx) emission during the regeneration of coked fluid catalytic cracking (FCC) catalysts is an en-vironmental issue. In order to identify the correlations between nitrogen species in coke and different nitrogen-containing products in tail gas, three coked catalysts with multilayer structural coke molecules were prepared in a fixed bed with model compounds (o-xylene and quinoline) at first. A series of characterization methods were used to analyze coke, including elemental analysis, FT-IR, XPS, and TG–MS. XPS characterization indicates all coked catalysts present two types of nitrogen species and the type with a higher binding energy is related with the inner part nitrogen atoms interacting with acid sites. Due to the stronger adsorption ability on acid sites for basic nitrogen compounds, the multilayer structural coke has unbalanced distribution of carbon and ni-trogen atoms between the inner part and the outer edge, which strongly affects gas product formation. At the early stage of regeneration, oxidation starts from the outer edge and the product NO can be reduced to N2 in high CO concentration. At the later stage, the inner part rich in nitrogen begins to be exposed to O2. At this period, the formation of CO decreases due to lack of carbon atoms, which is not beneficial to the reduction of NO. There-fore, nitrogen species in the inner part of multilayer structural coke contributes more to NOX formation. Based on the multilayer structure model of coke molecule and its oxidation behavior, a possible strategy to control NOX emission was discussed merely from concept.

  15. Factors affecting the microwave coking of coals and the implications on microwave cavity design

    OpenAIRE

    Binner, Eleanor; Medeira-Munoyerro, Maria; Huddle, Thomas; Kingman, S. W.; Dodds, Chris; Dimitrakis, G.; Robinson, John P.; Lester, Edward

    2014-01-01

    The work carried out in this paper assessed how processing conditions and feedstock affect the quality of the coke produced during microwave coke making. The aim was to gather information that would support the development of an optimised microwave coke making oven. Experiments were carried out in a non-optimised 2450 MHz cylindrical cavity. The effect of treatment time (15–120 min), power input (750 W–4.5 kW) and overall power input (1700–27,200 kWh/t) on a range of coals (semi-bituminous–an...

  16. The Release of Trace Elements in the Process of Coal Coking

    OpenAIRE

    Jan Konieczyński; Elwira Zajusz-Zubek; Magdalena Jabłońska

    2012-01-01

    In order to assess the penetration of individual trace elements into the air through their release in the coal coking process, it is necessary to determine the loss of these elements by comparing their contents in the charge coal and in coke obtained. The present research covered four coke oven batteries differing in age, technology, and technical equipment. By using mercury analyzer MA-2 and the method of ICP MS As, Be, Cd, Co, Hg, Mn, Ni, Se, Sr, Tl, V, and Zn were determined in samples of ...

  17. Structural variations and physical properties of lignin coke

    International Nuclear Information System (INIS)

    The studied lignin is a by-product of the process of ethanol production from eucaliptus. It was heat-treated under inert atmosphere conditions at increasing temperatures from 3000C up to 26000C. This material has about 35 weight % of carbon yield and low ash content (0.70 w %). The structural variations were studied by wide-angle X-ray diffraction, small-angle X-ray scattering and infra-red spectroscopy. The bulk and the ''real'' density of the samples have also been determined as a function of the heat treatment temperatures. These experimental results enabled us to establish a mechanism of structure variation based on the formation of a graphite-like and porous structure within the initially amorphous lignin matrix. It has been possible to specify the adequate heat treatment temperature based upon the lignin coke applications. (author)

  18. Energy efficiency of alternative coke-free metallurgical technologies

    Energy Technology Data Exchange (ETDEWEB)

    V.G. Lisienko; A.V. Lapteva; A.E. Paren' kov [Ural State Technical University - Ural Polytechnic Institute, Yekaterinburg (Russian Federation)

    2009-02-15

    Energy analysis is undertaken for the blast-furnace process, for liquid-phase processes (Corex, Hismelt, Romelt), for solid-phase pellet reduction (Midrex, HYL III, LP-V in a shaft furnace), for steel production in systems consisting of a blast furnace and a converter, a Midrex unit and an arc furnace, or a Romelt unit and an arc furnace, and for scrap processing in an arc furnace or in an LP-V shaft furnace. Three blast-furnace processes with sinter and coke are adopted as the basis of comparison, as in: the standard blast-furnace process used in Russia; the improved blast-furnace process with coal-dust injection; and the production of vanadium hot metal from vanadium-bearing titanomagnetite ore (with a subsequent duplex process, ferrovanadium production, and its use in the arc furnace).

  19. Repair of the bottom bricks of 6 m coke oven coking chamber%6m焦炉炭化室底部砖的修补

    Institute of Scientific and Technical Information of China (English)

    蒋忠平; 朱婷婷

    2015-01-01

    This paper introduces a method for overall repair of the bottom bricks of coking chamber, and proposes a control plan for temperature management during repairing. Practical production shows that the repaired coking chamber has similar indexes with other coking chambers, and from which coke can be pushed out easily. Therefore, the risk of high temperature radiation to human body is reduced and the service life of coke oven is prolonged.%介绍了对炭化室底部砖进行整体修补的方法,并对期间的温度管理提出了控制方案,生产实践表明,该炭化室推焦正常,各方面指标与其他炭化室无明显差异,降低了高温辐射对人体的伤害,延长了焦炉的使用寿命。

  20. A small-angle neutron scattering investigation of coke deposits on catalysts

    International Nuclear Information System (INIS)

    Small-angle neutron scattering (SANS) has been used to characterize a silica-alumina catalyst before and after coke deposition. The reaction used to deactivate the catalyst was the isomerization of xylenes. The results showed that, while most of the surface area in this type of catalyst resides in the ultrafine pores of diameters less than 1 nm occupying about 7% of the sample volume, there appears to be no coke deposition in these pores. The coke seems to coat the solid structures of 3.3-nm diameter which are of capillary shape. Such structures occupy about 6% of the sample volume. The coke was found to correspond to amonolayer of composition CH0.3 with a density of 1660 kg/m3

  1. Influence of carbonization conditions on micro-pore structure of foundry formed coke produced with char

    Energy Technology Data Exchange (ETDEWEB)

    Jun Qiao; Jianjun Wu; Jingru Zu; Zhiyuan Gao; Guoli Zhou

    2009-07-01

    There are few studies on coke's micro-pore structure in recent years, however, micro-pore structure of foundry coke determines its macroscopically quality index and reactivity in cupola furnace. Effect of such factors on micro-pore structure were investigated under different carbonization conditions with certain ratio of raw materials and material forming process in this article as charging temperature (A); braised furnace time (B); heating rate of the first stage (C)and the second stage (D) and holding time of ultimate temperature (E). Research showed that charging temperature was the most influential factor on the coke porosity, pore volume, pore size and specific surface area. It is suggested that formation of plastic mass and releasing rate of volatile during carbonization period are two main factors on microstructure of foundry coke while charging temperature contributes most to the above factors. 6 refs., 4 figs., 9 tabs.

  2. Study of ways of reducing coke use at non-integrated metallurgical plants

    Energy Technology Data Exchange (ETDEWEB)

    S.A. Feshchenko; V.I. Pleshkov; I.N. Shishchuk; A.V. Buev [Svobodnyi Sokol (Russian Federation). Lipetsk Metallurgical Plant

    2006-03-15

    To reduce the costs of blast-furnace smelting, the Svobodnyi Sokol plant has devised a comprehensive program of organizational-technical measures that include study of ways of reducing coke consumption. To do this, the plant began operating its blast furnaces with schungite when making foundry and conversion pig irons. Using schungite in the charge employed to make foundry iron makes it possible to save a significant (10-15%) amount of coke. The value of the coefficient that characterizes the replacement of coke by schungite varies broadly and can reach 1.0 or more, depending on the grade of iron being made and the furnace operating regime. The same coefficient has a value of 0.57 kg coke/kg schungite when 12-15 kg schungite/ton pig is used to make conversion pig iron.

  3. Effect of injecting inert particles on coking prohibition and particle velocity uniformization in downer reactors

    Energy Technology Data Exchange (ETDEWEB)

    Zhang, J.Y.; Zhu, Y.; Tian, Y.J.; Xie, K.C. [Fuzhou University, Fuzhou (China). Inst. of Chemical Engineering & Technology

    2007-02-15

    The coking observation and particle flow behaviour in both thermal plasma and cold plexiglas downers were investigated in a binary particle system formed by injecting coarse inert particles (carrying coke away and scouring wall) and fine coal powders into the downer reactor. The results demonstrate that this scheme is a rational selection to prevent coking on downer walls and improve particle velocity distribution along the radial direction. When injected coarse particles mixed with fine powders in downers, the fluctuation of local particle velocity in the radial direction becomes smaller and two peaks in the radial distribution of local particle velocity occur due to the improved dispersing character and flow structure, which are beneficial to the thermo-plasma coal cracking reaction and coking prevention.

  4. Gasification characteristics of coke and mixture with coal in an entrained-flow gasifier

    Energy Technology Data Exchange (ETDEWEB)

    See Hoon Lee; Sang Jun Yoon; Ho Won Ra; Young Il Son; Jai Chang Hong; Jae Goo Lee [Korean Institute of Energy Research, Taejon (Republic of Korea). Gasification Research Group

    2010-08-15

    To enhance clean energy utilization and reduce greenhouse gases, various gasification technologies have been developed in the world. The gasification characteristics, such as syngas flow rate, compositions, cold gas efficiency and carbon conversion, of petroleum coke and mixture of petroleum coke and lignite were investigated in a 1 T/d entrained-flow gasifier (ID. 0.2 m x height 1.7 m) with quencher as a syngas cooler. CO concentration was 31-42 vol% and H{sub 2} concentration was almost 22 vol% in the gasification experiments of petroleum coke. In the case of mixture of petroleum coke and lignite, CO concentration was 37-47 vol% and H{sub 2} concentration was almost 25 vol% due to synergy effect. The gasification of mixture resulted in higher syngas heating value and cold gas efficiency because of the higher H{sub 2} and CO composition in syngas.

  5. Fe-Si droplets associated with graphite on blast furnace coke

    Science.gov (United States)

    Gornostayev, Stanislav S.; Fabritius, Timo M. J.; Kerkkonen, Olavi; Härkki, Jouko J.

    2012-06-01

    Fe-Si droplets on the surface of blast furnace (BF) coke from 25 to 50 cm at the tuyere level are mostly composed of Fe3Si, which has various shapes (round, elongated, and irregular) and penetration degrees into the BF coke matrix. The shapes and penetration degrees may depend on the saturation of molten iron by silicon during interaction with the coke matrix. The droplets are covered by a tiny shell of carbon. Graphite observed inside the droplets can be divided into two categories: well-formed tabular crystals with relatively large size and flakes with structures similar as those in cast iron. The textures of the droplets reflect composition, interaction with the coke matrix, and cooling conditions.

  6. Gasification characteristics of coke and mixture with coal in an entrained-flow gasifier

    Energy Technology Data Exchange (ETDEWEB)

    Lee, See Hoon; Yoon, Sang Jun; Ra, Ho Won; Son, Young Il; Hong, Jai Chang; Lee, Jae Goo [Gasification Research Group, Korea Institute of Energy Research, 71-2 Jang-dong, Yuseong-gu, Daejeon 305-343 (Korea)

    2010-08-15

    To enhance clean energy utilization and reduce greenhouse gases, various gasification technologies have been developed in the world. The gasification characteristics, such as syngas flow rate, compositions, cold gas efficiency and carbon conversion, of petroleum coke and mixture of petroleum coke and lignite were investigated in a 1 T/d entrained-flow gasifier (I.D. 0.2 m x height 1.7 m) with quencher as a syngas cooler. CO concentration was 31-42 vol% and H{sub 2} concentration was almost 22 vol% in the gasification experiments of petroleum coke. In the case of mixture of petroleum coke and lignite, CO concentration was 37-47 vol% and H{sub 2} concentration was almost 25 vol% due to synergy effect. The gasification of mixture resulted in higher syngas heating value and cold gas efficiency because of the higher H{sub 2} and CO composition in syngas. (author)

  7. Heat Transfer Characteristics of Calcined Petroleum Coke in Waste Heat Recovery Process

    Directory of Open Access Journals (Sweden)

    Bin Zheng

    2016-01-01

    Full Text Available This paper reports the results of heat transfer characteristics of calcined petroleum coke in waste heat recovery process. The model of heat exchanger was set up. The model has been used to investigate the effects of porosity (0.58 to 0.79, equivalent heat conductivity coefficient (0.9 to 1.1, and equivalent specific heat (0.9 to 1.1. The calculated values of calcined petroleum coke temperature showed good agreement with the corresponding available experimental data. The temperature distribution of calcined petroleum coke, the calcined petroleum coke temperature at heat exchanger outlet, the average heat transfer coefficient, and the heat recovery efficiency were studied. It can also be used in deriving much needed data for heat exchanger designs when employed in industry.

  8. Lymphohaematopoietic system cancer incidence in an urban area near a coke oven plant: an ecological investigation

    OpenAIRE

    Parodi, S; Vercelli, M; Stella, A.; Stagnaro, E; Valerio, F.

    2003-01-01

    Aims: To evaluate the incidence risk of lymphohaematopoietic cancers for the 1986–94 period in Cornigliano, a district of Genoa (Italy), where a coke oven is located a few hundred metres from the residential area.

  9. Estimation of cytogenetic risk among coke oven workers exposed to polycyclic aromatic hydrocarbons.

    Science.gov (United States)

    Sureshkumar, Shanmugam; Balachandar, Vellingiri; Devi, Subramaniam Mohana; Arun, Meyyazhagan; Karthickkumar, Alagamuthu; Balamuralikrishnan, Balasubramanian; Sankar, Kathannan; Mustaqahamed, Shafi Ahammed Khan; Dharwadkar, Shanwaz N; Sasikala, Keshavarao; Cho, Ssang-Goo

    2013-01-01

    Polycyclic aromatic hydrocarbons (PAHs) result from the incomplete combustion of natural or synthetic organic materials. The working environment at a coke plant can negatively affect the employed workers who were exposed to coke oven emissions containing PAHs, which formed and released into the environment by the process of pyrolysis of coke. This study aims to analyze the relationship between the exposure of PAHs and the risk of genetic damages such as chromosomal alteration (CA), micronucleus (MN), and DNA damage (PCR-RFLP) in peripheral blood lymphocytes of 27 coke oven workers and equal number of control subjects. The exposed subjects and controls were divided into two groups based on their age (group Icoke oven workers under risk should be monitored for adverse effects of the any long-term exposure. PMID:24040626

  10. Thermal construction of hot coke oven%焦炉的热态施工

    Institute of Scientific and Technical Information of China (English)

    郑晓锋

    2014-01-01

    Coke oven project quality influenced by various factors , the most important including ma-sonry, oven, hot production and production .The importance of construction quality of coke oven tem-perature is not inferior to coke oven masonry and oven .The construction of hot construction site and technical solutions were presented , and provide reference for the future construction of coke oven .%焦炉工程质量受到多方面因素的影响,最重要的包括砌筑、烘炉、热态施工和开工生产这几个因素。其中,焦炉热态施工质量的重要性不次于焦炉的砌筑和烘炉。介绍热态施工的施工点和技术方案,为今后焦炉的施工提供参考。

  11. Coke formation on HFAU and HEMT zeolites. Influence of the reaction temperature and propene pressure

    Science.gov (United States)

    Doka Nassionou, G. A.; Magnoux, P.; Guisnet, M.

    1999-02-01

    The formation of coke from propene (Pp = 1.3 kPa and 13 kPa) was investigated on HFAU and HEMT zeolites in a microbalance for temperatures ranging from 120 °C to 450 °C. For both zeolites, the greater the propene pressure and the lower the temperature the faster the initial coke formation. However for high propene pressure, initial coke formation is faster with HEMT zeolite. This can be related to the stronger acidity of the HEMT sample. For low propene pressure and after 420 minutes of coking, a minimum in coke is observed for T = 350 ^circC, which can be related to the difference between the rate of formation and the rate of retention of coke molecules. At low temperature, due to their low volatility, oligomers are easily formed and retained in the zeolite pores. These molecules can be totally eliminated by an adequate thermal treatment in vacuum. At higher temperature, only aromatic or polyaromatic compounds which present a size larger than the pore apertures can be retained in the cavities of the zeolites. The greater the reaction time, the faster the retention. Whatever the reaction temperature, coke molecules are more homogeneously distributed in the HEMT crystallites than in those of HFAU samples. For this latter zeolite coke molecules are preferentially formed in the cavities located near the outer surface of the crystallites (shell coking). La formation de coke à partir du propène (Pp = 1,3 et 13 kPa) a été étudiée en microbalance sur zéolithes HFAU et HEMT dans une gamme de température variant de 120 à 450°C. La vitesse initiale de formation de coke dépend de la pression du propène, de la température et également de la zéolithe. Ainsi, pour une forte pression en propène, la vitesse initiale de formation de coke est toujours plus importante sur HEMT que sur HFAU. Ceci est à relier à la plus grande acidité et à la présence de sites acides plus forts sur HEMT. Après 420 minutes de réaction, et pour une faible pression en propène le

  12. Zeolite deactivation during hydrocarbon reactions: characterisation of coke precursors and acidity, product distribution

    OpenAIRE

    Wang, B.

    2008-01-01

    The catalytic conversion of hydrocarbons over zeolites has been applied in large scale petroleum-refining processes. However, there is always formation and retention of heavy by-products, called coke, which causes catalyst deactivation. This deactivation is due to the poisoning of the acid sites and/or pore blockage. The formation of coke on hydrocarbon processing catalysts is of considerable technological and economic importance and a great deal of work has been carried out to this study. Th...

  13. Functionalization of Petroleum Coke-Derived Carbon for Synergistically Enhanced Capacitive Performance

    OpenAIRE

    Zhang, Yan; Li, Xuejin; Huang, Jufeng; Xing, Wei; Yan, Zifeng

    2016-01-01

    Petroleum coke is a valuable and potential source for clean energy storage if it could be modified legitimately and facilely. In the present study, porous carbon with high surface area and abundant oxygen-containing groups was prepared from petroleum coke by chemical activation and modification processes. The as-prepared carbon exhibits a high surface area (1129 m2 · g−1) and stable micrographic structure. It presents a high specific capacitance and excellent rate performance in KOH electroly...

  14. Electrochemical Oxidation Using BDD Anodes Combined with Biological Aerated Filter for Biotreated Coking Wastewater Treatment

    OpenAIRE

    Wang, C.R.; Hou, Z. F.; M. R. Zhang; J. Qi; Wang, J.

    2015-01-01

    Coking wastewater is characterized by poor biodegradability and high microorganism toxicity. Thus, it is difficult to meet Grade I of Integrated Wastewater Discharge Standard of China by biological treatment technology; specifically, COD cannot meet above standard due to containing refractory organics. A novel coupling reactor, electrochemical oxidation using BDD anodes and biological aerated filter (BAF), has been developed for carbon and nitrogen removal from biotreated coking wastewater, f...

  15. Using Lymphocyte and Plasma Hsp70 as Biomarkers for Assessing Coke Oven Exposure among Steel Workers

    OpenAIRE

    Yang, Xiaobo; Zheng, Jinping; Bai, Yun; Tian, Fengjie; Yuan, Jing; Sun, Jianya; Liang, Huashan; Guo, Liang; Tan, Hao; Chen, Weihong; Tanguay, Robert M.; Wu, Tangchun

    2007-01-01

    Background Hsp70, an early-response protein induced when organisms are confronted with simple or complicated environmental stresses, can act as either a cellular protector or a danger signal. Objectives The goal of this study was to evaluate levels of lymphocyte and/or plasma Hsp70 as biomarkers for assessing exposure response to complex coke oven emissions (COEs). Methods We recruited 101 coke oven workers and determined levels of polycyclic aromatic hydrocarbon (PAH) exposure, urinary 1-hyd...

  16. Chinese Standards on Refractories Fireclay Brick and Semi-silica Brick for Coke Oven

    Institute of Scientific and Technical Information of China (English)

    Wang Jing

    2009-01-01

    @@ 1 Scope This standard specifies the technical requirements,test methods,quality appraisal procedure,packing,transportation,storage,and quality certificate of fireclay brick and semi-silica brick for coke oven. This standard is applicable to the fireclay brick and semi-silica brick for coke oven,and the bricks for inner linings of carbon furnace,gas generator and shaft furnace.

  17. Optical Microscopy and SEM Study of Pyrolytic Carbon Deposits from Coke Ovens

    OpenAIRE

    Barranco, Richelieu; Patrick, John W.; Snape, Colin E.; Wu, Tao; Poultney, Ruth M.; Barriocanal Rueda, Carmen; Díez Díaz-Estébanez, M.ª Antonia

    2007-01-01

    The presence of pyrolytic carbon deposits can cause a number of serious problems in the operation of a coke oven. The main objective of the investigation was to study the nature and characteristics of pyrolytic carbon deposits in industrial coke ovens, with particular emphasis on the nature of the carbon deposited adjacent to the oven walls. Study of the carbon deposits by optical microscopy and SEM showed a variable concentration of carbon entities as well as differences in packing density.

  18. Lung cancer mortality and exposure to polycyclic aromatic hydrocarbons in British coke oven workers

    OpenAIRE

    Miller, Brian G.; Doust, Emma; Cherrie, John W.; Hurley, J Fintan

    2013-01-01

    Background Workers on coke oven plants may be exposed to potentially carcinogenic polycyclic aromatic hydrocarbons (PAHs), particularly during work on the ovens tops. Two cohorts, employees of National Smokeless Fuels (NSF) and the British Steel Corporation (BSC) totalling more than 6,600 British coke plant workers employed in 1967, had been followed up to mid-1987 for mortality. Previous analyses suggested an excess in lung cancer risk of around 25%, or less when compared with Social Class I...

  19. Relevance of the composition of municipal plastic wastes for metallurgical coke production

    OpenAIRE

    Melendi, Sonia; M.A. Diez; R. Alvarez; Barriocanal, C.

    2011-01-01

    This study is concerned with the effects of the composition of mixed plastic wastes on the thermoplastic properties of coal, the generation of coking pressure and the quality of the resulting cokes in a movable wall oven at semipilot scale. The mixed plastic wastes were selected to cover a wide spectrum in the relative proportions of high- and low-density polyethylenes (HDPE and LDPE), polypropylene (PP), polystyrene (PS) and polyethylene terephthalate (PET). From the results it was deduced t...

  20. Biomarkers of carcinogen exposure and cancer risk in a coke plant.

    OpenAIRE

    Assennato, G; Ferri, G M; Tockman, M S; Poirier, M C; Schoket, B; Porro, A.; Corrado, V.; Strickland, P T

    1993-01-01

    To evaluate the association between an indicator of carcinogen exposure (peripheral blood leukocyte DNA adducts of polycyclic aromatic hydrocarbons) and an early indicator of neoplastic transformation (sputum epithelial cell membrane antigens binding by monoclonal antibodies against small cell lung cancer and against nonsmall cell lung cancer), a survey of 350 coke-oven workers and 100 unexposed workers was planned. This paper reports a pilot investigation on a subgroup of 23 coke-oven worker...

  1. Temperature-programmed oxidation of coked noble metal catalysts after autothermal reforming of n-hexadecane

    Energy Technology Data Exchange (ETDEWEB)

    Kauppi, E.I.; Linnekoski, J.A.; Krause, A.O.I.; Veringa Niemelae, M.K. [Aalto University, School of Science and Technology, Department of Biotechnology and Chemical Technology, Research Group Industrial Chemistry, P.O. Box 16100, FI-00076 Aalto (Finland); Kaila, R.K. [VTT Technical Research Centre of Finland, Biologinkuja 7, Espoo, P.O. Box 1001, FI-02044 VTT (Finland)

    2010-08-15

    Autothermal reforming (ATR) of n-hexadecane was carried out on zirconia-supported mono- and bimetallic noble metal (Rh, Pt) catalysts at 600, 700, and 800 C. After ATR, the reactivity of coke deposits (2.8-9.9 wt%) on the catalysts was investigated by temperature-programmed oxidation (TPO). Analysis of the results obtained from ATR and TPO experiments at various temperatures and on the different catalysts gave information on the reaction conditions where the detrimental coke can be minimized and allows estimating the nature of carbon deposits. H{sub 2} production increased with temperature on the tested Rh-containing catalysts and the ZrO{sub 2} support, but decreased as a function of temperature on the Pt catalyst. The formation of coke was least at 800 C, evidently due to the intensifying reaction of carbon and steam with increasing temperature, as well as to the better activity of the catalysts. The amount of coke formed was highest at 700 C. Comparison of the TPO profiles obtained for the monometallic Rh and Pt catalysts with the bimetallic RhPt revealed differences in the nature of carbon deposits on their surface. At 600 C, the coke formed on the monometallic Rh and Pt catalysts was located mostly on the support, whereas on the bimetallic RhPt catalyst the formation of this type of coke was suppressed. The bimetallic RhPt catalyst also exhibited better tolerance toward coking at 700 C. Therefore, although the selectivity toward hydrogen was not related to the amount of coke formed, the deactivation patterns differed on the mono- and bimetallic catalysts. (author)

  2. Improvement on coke cake center temperature measurement of 7m coke oven battery%7m 焦炉焦饼中心温度测量方法的改进

    Institute of Scientific and Technical Information of China (English)

    党平

    2014-01-01

    This paper analyzes the advantages and disadvantages of traditional coke cake center tem-perature measurement and modern automatic coke cake temperature measuring system. As to the diffi-culties in coke cake center temperature measurement of 7m coke oven battery,it is recommended to adopt horizontal tube inserting method to measure the coke cake center temperature,which has been applied to large scale coke oven battery successfully.%分析传统焦饼中心温度测量方法以及现代化焦饼自动测量系统的优缺点,针对7m 焦炉焦饼中心温度测量困难等问题,提出横向插管法测量焦饼中心温度,并成功运用于大型焦炉焦饼中心温度的测量。

  3. Research on the application of large pilot coke oven in coking companies%大型试验焦炉在焦化企业的应用研究

    Institute of Scientific and Technical Information of China (English)

    线葵娟; 龙晓阳; 金辉; 王旭; 徐申

    2015-01-01

    介绍了200kg试验焦炉的结构和配套设备,并与6m生产焦炉进行对比炼焦试验。结果表明,200kg试验焦炉所得焦炭质量与生产焦炉所得焦炭质量具有显著的线性关系,利用该关系可有效指导生产配煤。%This paper introduces the structure and corollary equipment of 200kg pilot coke oven. Coking experiments were performed to compare with 6m production coke oven. The result shows that the coke quality produced by the 200kg pilot coke oven has obvious linear relation with that produced by production coke oven. This relationship can be used to guide coal blending.

  4. Volatiles production from the coking of coal; Sekitan no netsubunkai ni okeru kihatsubun seisei

    Energy Technology Data Exchange (ETDEWEB)

    Yamashita, Y.; Saito, H.; Inaba, A. [National Institute for Resources and Environment, Tsukuba (Japan)

    1996-10-28

    In order to simplify the coke manufacturing process, a coke production mechanism in coal pyrolysis was discussed. Australian bituminous coal which can produce good coke was used for the discussion. At a temperature raising rate of 50{degree}C per minute, coal weight loss increases monotonously. However, in the case of 3{degree}C, the weight loss reaches a peak at a maximum ultimate temperature of about 550{degree}C. The reaction mechanism varies with the temperature raising rates, and in the case of 50{degree}C per minute, volatiles other than CO2 and propane increased. Weight loss of coal at 3{degree}C per minute was caused mainly by methane production at 550{degree}C or lower. When the temperature is raised to 600{degree}C, tar and CO2 increased, and so did the weight loss. Anisotropy was discerned in almost of all coke particles at 450{degree}C, and the anisotropy became remarkable with increase in the maximum ultimate temperature. Coke and volatiles were produced continuously at a temperature raising rate of 50{degree}C per minute, and at 3{degree}C per minute, the production of the coke and volatiles progressed stepwise as the temperature has risen. 7 refs., 6 figs.

  5. Discrete Element Method Modeling of the Rheological Properties of Coke/Pitch Mixtures

    Directory of Open Access Journals (Sweden)

    Behzad Majidi

    2016-05-01

    Full Text Available Rheological properties of pitch and pitch/coke mixtures at temperatures around 150 °C are of great interest for the carbon anode manufacturing process in the aluminum industry. In the present work, a cohesive viscoelastic contact model based on Burger’s model is developed using the discrete element method (DEM on the YADE, the open-source DEM software. A dynamic shear rheometer (DSR is used to measure the viscoelastic properties of pitch at 150 °C. The experimental data obtained is then used to estimate the Burger’s model parameters and calibrate the DEM model. The DSR tests were then simulated by a three-dimensional model. Very good agreement was observed between the experimental data and simulation results. Coke aggregates were modeled by overlapping spheres in the DEM model. Coke/pitch mixtures were numerically created by adding 5, 10, 20, and 30 percent of coke aggregates of the size range of 0.297–0.595 mm (−30 + 50 mesh to pitch. Adding up to 30% of coke aggregates to pitch can increase its complex shear modulus at 60 Hz from 273 Pa to 1557 Pa. Results also showed that adding coke particles increases both storage and loss moduli, while it does not have a meaningful effect on the phase angle of pitch.

  6. Automation techniques of coke oven moving machines; Kokusuro ido kikai no jidoka gijutsu

    Energy Technology Data Exchange (ETDEWEB)

    Inayama, A.; Noguchi, H.; Shibata, T. [Kawasaki Steel Corporation, Tokyo (Japan). Chiba Works

    1999-12-01

    In a coke oven plant, four associated moving machines are used for coal charging, coke pushing, coke guiding and transportation. Except quenching cars, which are easy for automation, pusher cars, coal charging cars and coke guide cars had been driven by boarded operators respectively. Since 1994, Kawasaki Steel has been tried to realize the automatic no-man operation of the moving cars, including the pusher car that was considered to be difficult, at Chiba Works No. 6 and No. 7 coke oven plants. Consideration to the oven bodies deteriorated through the respective usage of 19 and 26 years, and preventive function to manual interruption during the detected light fault of equipment, are the key issues to achieve this goal in order to modify and improve the existing equipment. For automation techniques of the moving cars developed at Chiba Works No. 6 and No. 7 coke oven plants, the feature of the automation system and the current operating condition are described in this paper. (author)

  7. Removal of sulfur in coke oven gas by mixing ZnO-based additive into coal

    Institute of Scientific and Technical Information of China (English)

    郭占成; 唐惠庆; 叶树锋

    2001-01-01

    A new technology for recycling EAF dust and removal of sulfur from coking oven gas was investigated. The new technology does not need to set up special equipment to treat COG (coke oven gas), and it is only acquired by mixing the ZnO-base additive into the coke coal. In the stage of pyrolysis of the coal volatile, ZnO of the additive combines with H2S, CS2, COS and C2H2SH of coal gas, forming ZnS in coal char. In the stage of coking of the coal char, Zn is gasified with S, then the gas Zn react with H2S, CS2, COS and C2H2SH, forming ZnS in coal gas and depositing as dust. After the collected ZnS dust was regenerated, it can be recycling as the additive again. The sulfur in coal gas can be completely removed if the mole ratio of the added Zn to the volatilized S is more than 1, and the sulfur in coke is also slightly decreased comparing with the coke without the additive. The EAF dust containing ZnO and Fe2O3 can be the base material of the desulfurizing additive.

  8. Application of coke dry quenching technology in the production of the cleaning type heat recovery coke oven%干熄焦技术在清洁型热回收焦炉中的应用

    Institute of Scientific and Technical Information of China (English)

    黄岭

    2011-01-01

    对清洁型热回收焦炉熄焦方式进行了评价,指出干熄焦技术在节能、环保、改善焦炭质量以及经济效益上的积极意义。%By assessing the method of coke quenching technology of the cleaning type heat recovery coke oven,the positive significance of coke dry quenching technology in energy-saving,environmental protection,the quality of coke improving and economic effect was displayed.

  9. Impact of a semi-industrial coke processing plant in the surrounding surface soil. Part II: PAH content

    OpenAIRE

    García Fernández, Roberto; Díaz Somoano, Mercedes; Calvo Díez, Montserrat; López Antón, María Antonia; Suárez, Sonia; Suárez Ruiz, Isabel; Martínez Tarazona, María Rosa

    2012-01-01

    Topsoil samples taken from different areas of a disused experimental coking plant were analysed in order to determine their polycyclic aromatic hydrocarbon (PAH) concentration. The variation in concentrations as a function of distance from the coking oven battery was studied and a reduction in PAH concentration as the distance to the coking ovens' battery increases was observed. Two exceptions are the area in the vicinity of the tar distillation section of the plant, with a strong contributio...

  10. The Evolution of Structural Order as a Measure of Thermal History of Coke in the Blast Furnace

    Science.gov (United States)

    Lundgren, Maria; Khanna, Rita; Ökvist, Lena Sundqvist; Sahajwalla, Veena; Björkman, Bo

    2014-04-01

    Investigations were carried out on cokes heat treated in the laboratory and on cokes extracted from the experimental blast furnace (EBF) raceway and hearth. X-ray diffraction (XRD) measurements were performed to investigate changes in structural order ( L c), chemical transformations in coke ash along with comparative thermodynamic equilibrium studies and the influence of melt. Three data processing approaches were used to compute L c values as a function of temperature and time and linear correlations were established between L c and heat treatment temperatures during laboratory investigations. These were used to estimate temperatures experienced by coke in various regions of EBF and estimated raceway temperatures were seen to follow the profile of combustion peak. The MgAl2O4 spinel was observed in coke submerged in slag during laboratory studies and in cokes found further into the raceway. Coke in contact with hot metal showed XRD peaks corresponding to presence of Fe3Si. The intensity of SiO2 peak in coke ash was seen to decrease with increasing temperature and disappeared at around 1770 K (1500 °C) due to the formation of SiC. This study has shown that the evolution of structural order and chemical transformations in coke could be used to estimate its thermal history in blast furnaces.

  11. Formation of a Mineral Layer during Coke Dissolution into Liquid Iron and Its Influence on the Kinetics of Coke Dissolution Rate

    Science.gov (United States)

    Chapman, Michael W.; Monaghan, Brian J.; Nightingale, Sharon A.; Mathieson, John G.; Nightingale, Robert J.

    2008-06-01

    The formation and development of the mineral layer that forms between coke and liquid iron during carbon dissolution has been characterized. Coke particles (-2 mm, +0.5 mm) were added to the top surface of an iron 2 mass pct C melt at representative iron-making temperatures, for periods of time between 2 and 120 minutes, before being quenched. The quenched samples were then sectioned, and the solidified coke-melt interfacial region analyzed in the scanning electron microscope (SEM). Analysis showed that a mineral layer was present at the interface at all experimental temperatures (1450 °C to 1550 °C) from 2 minutes and persisted beyond 120 minutes. The mineral layer was found to be composed of calcium aluminate phases, with the proportions of these phases dictating its morphology. Further, changes observed in the rate of carbon dissolution from the coke were related to the composition and morphology of the mineral layer. The effect of this mineral layer on the rate of carbon dissolution has been interpreted as a change in the reaction control mechanism.

  12. 防止炉膛结焦和垮大焦%Prevention of Coking and Off Coking in the Boiler Furnace

    Institute of Scientific and Technical Information of China (English)

    吕哲

    2015-01-01

    This paper mainly describes the main factors affecting the boiler coking, these include coal composition and ash melting point,furnace temperature and the distribution of temperature field, air dynamic field ect.. So, the main measures to prevent coking and off coking in the furnace are control of coking coal into the furnace, improvement of the aerodynamic field in furnace, control of furnace temperature, prevention of the oxygen deficient combustion, the heating surface cleaning, ect..%本文主要叙述了影响锅炉结焦的主要因素包括:原煤成份及灰熔点、炉膛温度及温度场分布、空气动力场等,故防止炉膛结焦和垮大焦的主要措施包括:控制易结焦煤种入炉、改善炉内空气动力场、控制炉膛温度、防止缺氧燃烧、保持受热面清洁等。

  13. A device for removing gases during unloading of coke ovens

    Energy Technology Data Exchange (ETDEWEB)

    Yatsura, V.A.; Matsegora, N.T.; Mikhaylenko, V.Ya.; Nayman, A.M.; Stepko, G.V.

    1983-01-01

    In the device for outlet of gases during unloading of coking furnaces, which includes a dust trapping hood, a collector for outlet of the gases with valves, a gas collecting chamber with openings on the side wall, which is located above the collector and has drives for vertical movement of the collector channels and a connecting branch pipe, attached to the dust trapping hood, in order to increase the operational reliability, the gas collecting chamber is fixed above the collector and is equipped with vertical partitions which divide it into sections, whose number is equal to the number of furnaces being serviced, the connecting branch pipe is equipped with runners mounted on its exterior surface (Pv) and interacting with the side wall of the gas collection chamber and the connecting branch pipe is attached to the dust trapping hood by means of shock absorbers. The device provides for continuous abutment between the dust trapping hood and the gas collector, which makes it possible to perform dust trapping throughout the entire cycle of coal outlet, including the time for fulfillment of auxiliary operations. The device is operationally reliable, since the shifting of the hood and the unevennesses of the solid wall along which the abutting device moves are eliminated by the compensators, which prevents failures.

  14. Kinetic model on coke oven gas with steam reforming

    Institute of Scientific and Technical Information of China (English)

    ZHANG Jia-yuan; ZHOU Jie-min; YAN Hong-jie

    2008-01-01

    The effects of factors such as the molar ratio of H2O to CH4 (n(H2O)/n(CH4)), methane conversion temperature and time on methane conversion rate were investigated to build kinetic model for reforming of coke-oven gas with steam. The results of experiments show that the optimal conditions for methane conversion are that the molar ratio of H2O to CH4 varies from 1.1 to 1.3and the conversion temperature varies from 1 223 to 1 273 K. The methane conversion rate is more than 95% when the molar ratio ofH2O to CH4 is 1.2, the conversion temperature is above 1 223 K and the conversion time is longer than 0.75 s. Kinetic model of methane conversion was proposed. All results demonstrate that the calculated values by the kinetic model accord with the experimental data well, and the error is less than 1.5%.

  15. Mechanism for sludge acidification in aerobic treatment of coking wastewater

    International Nuclear Information System (INIS)

    This work was undertaken to investigate the cause of sludge acidification that led to disruption of the activated sludge process treating coking wastewater from a steel-making plant in Taiwan. An activated sludge reactor (ASR) with a working volume of 80 L was used as a model system to simulate the behavior of the real wastewater treatment process. Parameters that may cause acidification or inactivation of the sludge (NH3, SCN-, S2O32- and CN-) were studied individually to examine for their effects on the performance of the ASR. The results show that high loading of NH3, SCN- and CN- did not lead to pH decrease, while the ASR attained 85% COD removal and nearly 100% SCN degradation. In contrast, when the wastewater was supplemented with ca. 1000 mg/L of S2O32-, the pH dropped to nearly 4.0 in 2 days and the COD and SCN removal yields were significantly lower (at 50 and 0-20%, respectively). Thus, overloading of S2O32- was apparently a key factor causing sludge acidification. The results suggest that to ensure a normal functioning of the activated sludge, the influent S2O32- concentration should be closely monitored and that the pH control of the ASR is indispensable when the S2O32- loading is in excess

  16. Colour change of soft denture liners after storage in coffee and coke.

    Science.gov (United States)

    Goiato, Marcelo Coelho; Zuccolotti, Bruna Carolina Rossatti; Moreno, Amália; dos Santos, Daniela Micheline; Pesqueira, Aldiéris Alves; Dekon, Stefan Fiuza de Carvalho

    2011-06-01

    This study was to evaluate the colour change of soft denture liners after thermocycling and storage in coffee and coke. Four liners, two silicone-based (Sofreliner S and Reline GS) and two acrylic resin-based (Soft Confort and Dentuflex), were evaluated in this study. Ten samples were obtained for each group. After 2000 cycles of thermocycling with baths of 5°C and 55°C, five samples were stored in coffee and the remaining samples in coke. The colour alteration was evaluated in a reflection spectrophotometer before and after thermocycling, and after 1, 3, 24, 48 and 96h of storage in coffee and coke. Data were submitted to anova and Tukey's HSD test (α=0.05). Thermocycling and storage period represented a higher statistically significant influence for the resin liners than for the silicone materials. Coke did not influence the colour stability of the materials during storage. However, the coffee solution generated statistically significant colour alteration in the material Soft Confort. In the comparison between the coffee and coke solutions, there was no statistically significant difference for colour alteration only for the material Dentuflex. The silicone liners presented better colour stability following thermocycling and storage independent of the solution. The coffee solution was a statistically significant factor for colour alteration of the material Soft Confort. PMID:20082643

  17. Physico-chemical treatment of coke plant effluents for control of water pollution in India

    Energy Technology Data Exchange (ETDEWEB)

    Ghose, M.K. [Indian School of Mines, Dhanbad (India). Center of Mining Environmental

    2002-01-01

    Coal carbonizing industries in India are important and are growing every year. Large quantities of liquid effluents produced in this industry contain a large amount of suspended solids, high biochemical oxygen demand (BOD), chemical oxygen demand (COD), phenols, ammonia and other toxic substances, which are causing serious surface water pollution in the area. There is a large number of coke plants in the vicinity of Jharia Coal Field (JCF). The working principle of a coke plant and the effluents produced is described. One large coke plant was chosen to evaluate characteristics of the effluent and to suggest a proper treatment method. Present effluent treatment system was found to be inadequate and a large quantity of a very good quality coke breeze is being lost, which is also causing siltation on the riverbed in addition to surface water pollution. Physico-chemical treatment has been considered as a suitable option for the treatment of coke plant effluents. A scheme has been proposed for the treatment, which can be suitably adopted for the recycling, reuse or safe disposal of the treated effluent. Various unit process and unit operations are discussed. The process may be useful on industrial scale for various sites so as to maintain a clean environment.

  18. Advanced treatment of biologically pretreated coking wastewater by a bipolar three-dimensional electrode reactor.

    Science.gov (United States)

    Zhang, Chunhui; Lin, Hui; Chen, Jun; Zhang, Wenwen

    2013-01-01

    Electrochemical oxidation is a promising technology for the treatment ofbio-refractory wastewater. In this research, advanced treatment of coking wastewater which had previously undergone A/O (anaerobic-aerobic biological) treatment was investigated over Ti/RuO2 x IrO2 anode, stainless steel cathode and coke powder particle electrodes which were packed into the electrodes in a bipolar three-dimensional electrode reactor (BTDR). The results showed that the removal efficiency of COD and ammonia nitrogen increased with applied current density. The main influencing factors of BTDR were evaluated by an orthogonal test, including reaction time, plate distance, current density, plate amounts and aeration flow rate. With reaction time of 60 min, plate distance of 1.0 cm, current density of 20 mA/cm2 and plate amounts of four pairs, most of the contaminants in coking wastewater can be remediated by BTDR, which can then meet the discharge limit for coking wastewater in China. For organic pollutants, 12 kinds of organic pollutants can be completely removed, and the removal efficiencies of 11 kinds of organic pollutants are between 13.3 and 70.3% by advanced treatment with BTDR. We conclude that there is great potential for BTDR in engineering applications as a final treatment for coking wastewater. PMID:24350493

  19. Highly coke-resistant ni nanoparticle catalysts with minimal sintering in dry reforming of methane.

    Science.gov (United States)

    Han, Joung Woo; Kim, Chanyeon; Park, Jun Seong; Lee, Hyunjoo

    2014-02-01

    Nickel catalysts are typically used for hydrogen production by reforming reactions. Reforming methane with carbon dioxide, called dry reforming of methane (DRM), is a good way to produce hydrogen or syngas (a mixture of hydrogen and carbon monoxide) from two notable greenhouse gases. However, Ni catalysts used for DRM suffer from severe coke deposition. It has been known that small Ni nanoparticles are advantageous to reduce coke formation, but the high reaction temperature of DRM (800 °C) inevitably induces aggregation of the nanoparticles, leading to severe coke formation and degraded activity. Here, we develop highly coke-resistant Ni catalysts by immobilizing premade Ni nanoparticles of 5.2 nm in size onto functionalized silica supports, and then coating the Ni/SiO2 catalyst with silica overlayers. The silica overlayers enable the transfer of reactants and products while preventing aggregation of the Ni nanoparticles. The silica-coated Ni catalysts operate stably for 170 h without any degradation in activity. No carbon deposition was observed by temperature programmed oxidation (TPO), transmission electron microscopy (TEM), X-ray diffraction (XRD), and Raman spectroscopy. The Ni catalysts without silica coating show severe sintering after DRM reaction, and the formation of filamentous carbon was observed. The coke-resistant Ni catalyst is potentially useful in various hydrocarbon transformations. PMID:24402833

  20. Experimental study on catalytic steam gasification of natural coke in a fluidized bed

    Energy Technology Data Exchange (ETDEWEB)

    Zhao, Changsui; Lin, Liangsheng; Pang, Keliang; Xiang, Wenguo; Chen, Xiaoping [School of Energy and Environment, Southeast University, Nanjing 210096, Jiangsu (China)

    2010-08-15

    The gasification characteristics of natural coke from Peicheng mine with steam were investigated in a fluidized bed reactor. The effects of catalyst type, composition and dosage of catalyst on the yield, components and heating value of product gas, and carbon conversion rate were examined. The results show that fluidized bed gasification technology is an effective way to gasify natural coke. Also the results indicate that individual addition of K-, Ca-, Fe-, Ni-based catalyst effectively increases the gasification reaction rate of the natural coke samples. With the increase in catalyst dosage, the yield and heating value of product gas per hour increase obviously, and carbon conversion rate is improved substantially. Each of aforementioned catalysts has similar catalytic effect and trend, among which the effect of Ca-based catalyst is a little weaker. The optimum metal atom ratio of mixed catalyst is Fe/Ni/others 35/55/10, and the mixed catalyst displays maximum catalytic performance when the catalyst dosage in the natural coke is about 4%. The experimental findings provide an interesting reference for large-scale development and utilization of natural coke. (author)

  1. Coking wastewater increases micronucleus frequency in mouse in vivo via oxidative stress.

    Science.gov (United States)

    Zhu, Na; Li, Hongyan; Li, Guangke; Sang, Nan

    2013-10-01

    Coking wastewater has caused serious health risk in coal-producing areas of China, however its toxic effects have not been well understood. The genotoxicity induced by coking wastewater on mice in vivo and its possible oxidative mechanisms were investigated via observing the induction of micronuclei in polychromatic erythrocytes of mouse bone marrow, and subsequently determining the antioxidative enzyme activities (superoxide dismutase Cu, Zn-SOD, Se-dependent glutathione peroxidase, and catalase), thiobarbituric acid reactive substance contents and protein carbonyl levels in brains and livers of mice. Results showed that the tested coking wastewater caused a significant increase of micronucleus frequencies in a concentration-dependent manner. Also, the sample increased lipid peroxidation and protein oxidation levels, which was accompanied by changes in antioxidative status. Interestingly, pre-treatment with an antioxidant (vitamin C) led to a statistical reduction in the micronucleus frequency caused by coking wastewater. This implies that coking wastewater induces evident genetic damage in mammalian cells, and exposure to polluted areas might pose a potential genotoxic risk to human beings; in the process, oxidative stress played a crucial role. PMID:24494500

  2. Preliminary Study of Thermal Treatment of Coke Wastewater Sludge Using Plasma Torch

    Science.gov (United States)

    Li, Mingshu; Li, Shengli; Sun, Demao; Liu, Xin; Feng, Qiubao

    2016-10-01

    Thermal plasma was applied for the treatment of coke wastewater sludge derived from the steel industry in order to investigate the feasibility of the safe treatment and energy recovery of the sludge. A 30 kW plasma torch system was applied to study the vitrification and gas production of coke wastewater sludge. Toxicity leaching results indicated that the sludge treated via the thermal plasma process converted into a vitrified slag which resisted the leaching of heavy metals. CO2 was utilized as working gas to study the production and heat energy of the syngas. The heating value of the gas products by thermal plasma achieved 8.43 kJ/L, indicating the further utilization of the gas products. Considering the utilization of the syngas and recovery heat from the gas products, the estimated treatment cost of coke wastewater sludge via plasma torch was about 0.98 CNY/kg sludge in the experiment. By preliminary economic analysis, the dehydration cost takes an important part of the total sludge treatment cost. The treatment cost of the coke wastewater sludge with 50 wt.% moisture was calculated to be about 1.45 CNY/kg sludge dry basis. The treatment cost of the coke wastewater sludge could be effectively controlled by decreasing the water content of the sludge. These findings suggest that an economic dewatering pretreatment method could be combined to cut the total treatment cost in an actual treatment process.

  3. Comparison between UV and VUV photolysis for the pre- and post-treatment of coking wastewater.

    Science.gov (United States)

    Xing, Rui; Zheng, Zhongyuan; Wen, Donghui

    2015-03-01

    In this study, ultraviolet (UV) and vacuum ultraviolet (VUV) photolysis were investigated for the pre-treatment and post-treatment of coking wastewater. First, 6-fold diluted raw coking wastewater was irradiated by UV and VUV. It was found that 15.9%-35.4% total organic carbon (TOC) was removed after 24 hr irradiation. The irradiated effluent could be degraded by the acclimated activated sludge. Even though the VUV photolysis removed more chemical oxygen demand (COD) than UV, the UV-irradiated effluent demonstrated better biodegradability. After 4 hr UV irradiation, the biological oxygen demand BOD5/COD ratio of irradiated coking wastewater increased from 0.163 to 0.224, and its toxicity decreased to the greatest extent. Second, the biologically treated coking wastewater was irradiated by UV and VUV. Both of them were able to remove 37%-47% TOC within 8 hr irradiation. Compared to UV, VUV photolysis could significantly improve the transparency of the bio-treated effluent. VUV also reduced 7% more ammonia nitrogen (NH4+-N), 17% more nitrite nitrogen (NO2--N), and 18% more total nitrogen (TN) than UV, producing 35% less nitrite nitrogen (NO3--N) as a result. In conclusion, UV irradiation was better in improving the biodegradability of coking wastewater, while VUV was more effective at photolyzing the residual organic compounds and inorganic N-species in the bio-treated effluent.

  4. Colour change of soft denture liners after storage in coffee and coke.

    Science.gov (United States)

    Goiato, Marcelo Coelho; Zuccolotti, Bruna Carolina Rossatti; Moreno, Amália; dos Santos, Daniela Micheline; Pesqueira, Aldiéris Alves; Dekon, Stefan Fiuza de Carvalho

    2011-06-01

    This study was to evaluate the colour change of soft denture liners after thermocycling and storage in coffee and coke. Four liners, two silicone-based (Sofreliner S and Reline GS) and two acrylic resin-based (Soft Confort and Dentuflex), were evaluated in this study. Ten samples were obtained for each group. After 2000 cycles of thermocycling with baths of 5°C and 55°C, five samples were stored in coffee and the remaining samples in coke. The colour alteration was evaluated in a reflection spectrophotometer before and after thermocycling, and after 1, 3, 24, 48 and 96h of storage in coffee and coke. Data were submitted to anova and Tukey's HSD test (α=0.05). Thermocycling and storage period represented a higher statistically significant influence for the resin liners than for the silicone materials. Coke did not influence the colour stability of the materials during storage. However, the coffee solution generated statistically significant colour alteration in the material Soft Confort. In the comparison between the coffee and coke solutions, there was no statistically significant difference for colour alteration only for the material Dentuflex. The silicone liners presented better colour stability following thermocycling and storage independent of the solution. The coffee solution was a statistically significant factor for colour alteration of the material Soft Confort.

  5. 焦炉顶装改捣固后工艺及焦炭质量对比%Comparison of the process and coke quality for modifying top charging coke oven battery to stamp charging

    Institute of Scientific and Technical Information of China (English)

    马力辉

    2015-01-01

    This paper introduces the change of process and coke quality after modifying the 4. 3m top charging coke oven battery to stamp charging. After the modification, the coke yield has almost remained same as before,while the coke strength at cold and hot conditions has increased,and the coke screening has been improved,the metallurgical coke rate could be increased by 2. 5%,coke nut yield has been reduced by 1. 5%,and coke breeze yield has been reduced by 0. 5%.%介绍了4.3m焦炉顶装改造为捣固生产后工艺和焦炭质量的变化,由顶装改造为捣固生产后,产量基本保持不变,焦炭的冷热态强度提高,焦炭筛分改善,冶金焦率可以提高2.5%,焦丁产率降低1.5%,焦末产率降低0.5%。

  6. Measurements of volatile hydrocarbons in ambient air coking plant `Walbrzych`

    Energy Technology Data Exchange (ETDEWEB)

    Michalski, R.; Weglarz, A.; Skrok, R. [Polish Academy of Sciences, Zabrze (Poland). Inst. of Environmental Engineering

    1998-12-31

    The air is a matrix very difficult to handle. In addition, the pollutants are usually present at very low concentrations. Many techniques can be used to collect air samples. The simplest way is to use special containers, but this procedure is expensive and time-consuming. The adsorption of pollutants on adsorbents shows a growing interest, despite the difficulty to choose the appropriate support in order to obtain quantitative yields. To overcome this problem, two or three types of adsorbents may be used in series for collecting a wide range of analytes. In addition, the miniaturization of these techniques (i.e. microtraps and solid-phase microextraction) is also very promising: easy to handle, low cost, no solvent required, detection limits at ppt level when sensitive detectors are used. If we have no money for this modern equipment we must use traditional methods for compounds determination. This paper describes measurements of volatile hydrocarbons (such as benzene, toluene, ethylbenzene, xylene and phenol) in ambient air of coking plant `Walbrzych` Measuring points were at streets: Beethoven 4, Dworcowa 2, Kosteckiego 5 and Zamkowa 1. BTEX were collected on graphitized carbon and phenol on Chromosorb 102. After that samples were extracted by solvents (dichloromethane for BTEX or benzene for phenol). Next step was the analysis by gas chromatography with flame ionization detector without preconcentration. The lower limit of detection was circa 0.01 {mu}g/m{sup 3} for each of the determined compounds. These measurements of hydrocarbons in town of Walbrzych were performed for two years from 1996 to 1998. 2 tabs.

  7. Failure analysis of the impellers of coke plant

    Directory of Open Access Journals (Sweden)

    Souvik Das

    2014-10-01

    Full Text Available Premature failure of the impeller blade of coke plant has been investigated. The component functioned during the CGC gas intake cycle. The component rotates at 1480 rpm with a volumetric flow of 720 m3/min of flue gas with temperature about 200–300 °C. The failed component reveals exposed surface of a crack that extended slightly beyond the assembly weld. From macro-structural observation under-filled region in welding is observed which is detrimental because it acts as a stress concentration site. The microstructure from the weld zone showed severe intergranular corrosion degradation. Micro cracks and cracks have been observed at several locations, mostly originating from the weld zone. From the EDS analysis of the failed sample it is observed that there is a deposition of Cr along the grain boundary. From the mode of failure it indicates that probable reason for the premature failure is due to sensitization of the component. In this case, the precipitation of chromium carbides may be occurred during welding operation when the heat affected zone (HAZ experiences a particular temperature range (550–850 °C. From the microstructure it is observed that the welding operation was not proper and there is every chance that there is heat generation in around sensitization range leading to precipitation of chromium carbides consumed the alloying element – chromium from a narrow band along the grain boundary and this makes the zone anodic to the unaffected grains. The chromium depleted zone becomes the preferential path for corrosion attack or crack propagation if under tensile stress. Thus it leads to premature failure of the component during service.

  8. Elevated Levels of Urinary 8-Hydroxy-2′-deoxyguanosine, Lymphocytic Micronuclei, and Serum Glutathione S-Transferase in Workers Exposed to Coke Oven Emissions

    OpenAIRE

    Liu, Ai-Lin; Lu, Wen-Qing; Wang, Zeng-Zhen; Chen, Wei-Hong; Lu, Wen-Hong; Yuan, Jing; Nan, Pei-Hong; Sun, Jian-Ya; Zou, Ya-Lin; Zhou, Li-Hong; Zhang, Chi; Wu, Tang-chun

    2005-01-01

    To investigate associations among occupational exposure to coke oven emissions (COEs), oxidative stress, cytogenotoxic effects, change in the metabolizing enzyme glutathione S-transferase (GST), and internal levels of polycyclic aromatic hydrocarbons (PAHs) in coke oven workers, we recruited 47 male coke oven workers and 31 male control subjects from a coke oven plant in northern China. We measured the levels of 1-hydroxypyrene (1-OHP) and 8-hydroxy-2′-deoxyguanosine (8-OHdG) in urine, micron...

  9. Research on Loading Attachment of One Set Coke Dry Quenching System Applied to Various Types of Coke Ovens%适应不同型式焦炉干熄焦系统装入装置的研制

    Institute of Scientific and Technical Information of China (English)

    侯建锋; 赫占坤; 王涛

    2013-01-01

    Designs of the coke-loading connector and the seal mechanism of one set coke dry quenching applied to various types of coke ovens have been described respectively .Successful research on loading attachment of one set coke dry quenching applied to various types of coke ovens could reduce initial investment of the device and implement energy saving and consumption reducing .%  介绍了不同焦炉炉型,不同型式焦罐共用一套干熄焦的装焦连接装置的设计,以及装焦密封机构的设计。不同型式焦炉干熄焦共用一套装入装置的研制成功,可以减少设备前期投入,节能降耗。

  10. Differences in physical properties and CO{sub 2} gasification reactivity between coal char and petroleum coke

    Energy Technology Data Exchange (ETDEWEB)

    Wu, Y.Q.; Wu, S.Y.; Gu, J.; Gao, J.S. [East China University of Science & Technology, Shanghai (China)

    2009-09-15

    This paper mainly investigated the physical properties and gasification reactivity of coal char and petroleum coke, separately at the high temperature pyrolysis (950-1400{sup o}C) with slow heating rate and pyrolysis pressure of the atmospheric pressure and at the pressurized pyrolysis (the atmospheric pressure to 3 MPa) with rapid heating rate and the pyrolysis temperature of 950{sup o}C. Some significant differences in those between coal chars and petroleum coke were found. The high temperature pyrolysis caused more easily the graphitization of petroleum coke than that of coal char, especially in the higher temperature range. The increasing pyrolysis temperature resulted in the decrease of surface areas of coal char and the increase of surface areas of petroleum coke. As the pyrolysis pressure was elevated from the atmospheric pressure to 3 MPa, surface areas of petroleum coke initially increased and then decreased, while those of coal chars presented an opposite tendency. The increasing pyrolysis temperature was adverse to the gasification activity of coal chars and was favorable for the gasification activity of petroleum coke. Also, the effects of the pyrolysis pressure on the gasification activity of coal char and petroleum coke were significantly different. The gasification activity of petroleum coke was obviously lower than that of coal chars, and even lower than that of the natural graphite.

  11. Peculiarities of accumulation of nonstructural carbohydrates in shoots of various species of acer genus in conditions of coke process

    Directory of Open Access Journals (Sweden)

    V. S. Bilchuk

    2005-11-01

    Full Text Available The research results on influence of the by-product-coking industry emission on starch and saccharose accumulation in sprouts of the Acer L. species are presented. The toxic ingredients of the coke production wastes inhibit the process of starch hydrolysis that provokes considerable decrease of the sugars content and negative influence on the plants’ winter hardiness are established.

  12. 77 FR 34012 - Foundry Coke Products From the People's Republic of China: Continuation of Antidumping Duty Order

    Science.gov (United States)

    2012-06-08

    ... Five-Year (``Sunset'') Review, 76 FR 74775 (December 1, 2011). \\2\\ See Foundry Coke Products from the... FR 20788 (April 6, 2012) and accompanying Issues and Decision Memorandum. \\3\\ See Foundry Coke Products from China Determination, 77 FR 32998 (June 4, 2012), and USITC Publication 4326 (May 29,...

  13. Pre-commissioning of 120 kt/a Unit for Hydrotreating Crude Coke Oven Benzene Implemented at Baoyuan Chemical Company

    Institute of Scientific and Technical Information of China (English)

    2008-01-01

    @@ The Baoyuan Chemical Company, Ltd. in Taiyuan has per-formed the precommissioning of a 120 kt/a unit for hydrotreating crude coke oven benzene. This unit is the phase II construction of the 300 kt/a crude benzene hydrotreating project, which adopts the process technology for hydrotreating crude coke oven benzene developed indepen-dently by our own efforts.

  14. KRESS INDIRECT DRY COOLING SYSTEM, BETHLEHEM STEEL'S COKE PLANT DEMONSTRATION AT SPARROWS POINT, MARYLAND - VOLUME 2. APPENDICES G-N

    Science.gov (United States)

    The report evaluates the Kress Indirect Dry Cooling (KIDC) process, an innovative system for handling and cooling coke produced from a slot-type by-product coke oven battery. The report is based on the test work and demonstration of the system at Bethlehem Steel Corporation's Sp...

  15. Influence of blending methods on the co-gasification reactivity of petroleum coke and lignite

    Energy Technology Data Exchange (ETDEWEB)

    Zhan, X.L.; Jia, J.; Zhou, Z.J.; Wang, F.C. [East China University of Science & Technology, Shanghai (China)

    2011-04-15

    The purpose of this paper is to investigate the influence of blending methods on the co-gasification of petroleum coke and lignite with CO{sub 2} using a thermogravimetric system at 0.1 MPa. The weight loss curves, XRD analysis, SEM images, BET specific surface area, were investigated. It was observed that petroleum coke shows a low reactivity because of the graphitic carbon structure, low catalyst content and small specific surface area. Blending with lignite can get a high reactivity. The co-gasification reactivity was significantly influenced by blending methods. Wet grinding is much effective than dry grinding. Long grinding time made lignite show greater BET specific area. And the sample in long grinding time has more association chances between petroleum coke and AAEM species. The co-gasification reactivity increases linearly with a rise of BET specific area.

  16. Incorporation of petroleum coke into red ceramic; Incorporacao de coque de petroleo em ceramica vermelha

    Energy Technology Data Exchange (ETDEWEB)

    Freitas, L.A. de; Monteiro, S.N.; Sanchez, R.; Vieira, C.M.F. [Laboratorio de Materiais Avancados - LAMAV, Universidade Estadual do Norte Fluminense Darcy Ribeiro - UENF, Campos dos Goytacazes, RJ (Brazil)], e-mails: sanchez@uenf.br, vieira@uenf.br

    2011-04-15

    This work has as its objective the evaluation of the effect of incorporation of petroleum coke in the physical and mechanical properties of red ceramic. Compositions were prepared with 0%, 1%, 2% and 4 wt.% of petroleum coke incorporated into a kaolinitic clayey body. Rectangular specimens were formed by extrusion to fire at 850 deg C and 1050 deg C. The determined physical and mechanical properties were flexural rupture strength and water absorption. The microstructure of the fired ceramics was evaluated by optical microscopy. The results show that the petroleum coke waste can significantly contribute to reduce the energy consumption during the firing stage. However, incorporations must be done in amounts around 1 wt.% to avoid deleterious effect on the water absorption of the ceramic. (author)

  17. Experimental investigations of ammonia adsorption and nitric oxide reduction on activated coke

    Energy Technology Data Exchange (ETDEWEB)

    Sirko Ogriseck; Gloria Patricia Galindo Vanegas [Infraserv GmbH & Co. Hoechst KG, Frankfurt am Main (Germany)

    2010-06-01

    In this work the enhancement of ammonia adsorption on activated coke has been investigated to increase the efficiency of the denitrification in the dry flue gas cleaning system located at Infraserv GmbH & Co. Hoechst KG in Frankfurt am Main, Germany. The influence of loading temperatures and sulfur components content of the activated coke on the ammonia adsorption were studied. Additionally, urea was tested as an alternative loading substance. Increasing ammonia adsorption was observed by raising loading temperatures. The highest ammonia loading was possible at the highest temperature tested at 469{sup o}C. The activated coke loaded at these conditions, as well as the one loaded with urea, was found to have higher denitrification efficiency than that loaded at present conditions of about 114{sup o}C. The results of this study allowed the recommendation of possible measures to be applied in the plant to increase its denitrification efficiency.

  18. Effect and mechanism of coking residual ammonia water treating by flue gas

    Institute of Scientific and Technical Information of China (English)

    2001-01-01

    The treatment of coking residual ammonia water has been a bigdifficult problem at home and abroad, and there is no breakthrough research achievement in the past. The invention patent "The method of treating all coking wastewater or treating coking residual ammonia water by flue gas" has been successfully used in Huaian Steel Works for high concentration and organic industry wastewater treatment. Not only can it realize the wastewater zero discharge, but also the wastewater treatment has an effect of de-sulfur and de-nitrogen for flue gas. So that the flue gas exhaustcan meet the requirement of emission standard. The mass transfer and heat transfer, fly ash absorption and coagulation, acid and alkali neutralization reaction, catalysis oxidation and reduction reaction in flue gas would be the major factors.

  19. Model Predictive Control with Feedforward Strategy for Gas Collectors of Coke Ovens

    Institute of Scientific and Technical Information of China (English)

    Kai Li; Dewei Li; Yugeng Xi; Debin Yin

    2014-01-01

    In coking process, the production quality, equipment life, energy consumption, and process safety are all influenced by the pressure in gas collector pipe of coke oven, which is frequently influenced by disturbances. The main control objectives for the gas collector pressure system are keeping the pressures in collector pipes at appropriate operating point. In this paper, model predictive control (MPC) strategy is introduced to control the collector pressure system due to its ability to handle constraint and good control performance. Based on a method proposed to simplify the system model, an extended state space model predictive control is designed, which combines the feedforward strategy to eliminate the disturbance. The simulation results in a system with two coke ovens show the feasibility and effectiveness of the control scheme.

  20. Thermodynamic analysis for a regenerative gas turbine cycle in coking process

    Directory of Open Access Journals (Sweden)

    Zelong Zhang, Lingen Chen, Yanlin Ge, Fengrui Sun

    2014-01-01

    Full Text Available A regenerative gas turbine cycle driven by residual coke oven gas is proposed in this paper. The thermal efficiency and the work output (per ton of coke of the system are analyzed based on thermodynamics and the theory of gas turbine cycle. The influences of the gas release rate, the residual gas rate and the effectiveness of regenerator on the performance of the cycle are analyzed by using numerical examples. It is found that the work output increases with the increase of the residual gas rate while decreases with the increase of the gas release rate. The cycle with regenerator can reach higher thermal efficiency and bigger work output, which means that the coke oven gas is used more effectively. Moreover, there exist two optimal pressure ratios of compressor which lead the maximum thermal efficiency and the maximum specific work, respectively.

  1. The treatment of a deposited lignite pyrolysis wastewater by adsorption using activated carbon and activated coke

    Energy Technology Data Exchange (ETDEWEB)

    Wiessner, A.; Remmler, M.; Kuschk, P.; Stottmeister, U. [UFZ-Umweltforschungszentrum Leipzig-Halle GmbH, Leipzig (Germany). Dept. of Remediation Research

    1998-07-31

    This paper investigated activated carbon and activated coke adsorption for the treatment of highly contaminated discoloured industrial wastewater with a wide molecular size distribution of organic compounds. Lignite pyrolysis wastewater from a filled open-cast coal mine was used for continuous and discontinuous experiments. The investigations were performed using water samples taken from various depths of the deposits ponds. A comparison of the capacities of the adsorption materials used showed, that because of its large number of macro and mesopores, activated coke is more suitable for wastewater treatment and in addition cheaper than activated carbon.

  2. Decomposition of Organic Compounds in Coke Plant Wastewater by Ultrasonic Irradiation and Its Combined Process

    Institute of Scientific and Technical Information of China (English)

    XU Jin-qiu; JIA Jin-ping; WANG Jing-wei

    2004-01-01

    The paper deals with the degradation of the organic compounds in the coke plant wastewater by the combined process of ultrasonic irradiation and activated sludge. The influence factors of the ultrasonic degradation effect such as air atmosphere, initial concentration, ultrasonic power density and the category and consumption of catalyst were investigated. A water quality model was used to explain the degradation of different kinds of organic compounds in the coke plant wastewater by ultrasonic irradiation. After the wastewater was treated by the combined process of ultrasonic irradiation and activated sludge, the COD degradation efficiency was 95. 74 %, which is 63. 49% higher than that by the process of activated sludge alone.

  3. Coke fouling process on the oil refining; Processo de incrustacao por coque no refino do petroleo

    Energy Technology Data Exchange (ETDEWEB)

    Bombardelli, Clovis; Fiorentin, Leila D.; Negrao, Cezar O.R.; Franco, Admilson T. [Centro Federal de Educacao Tecnologica do Parana (CEFET-PR), Curitiba, PR (Brazil). Programa de Pos-Graduacao em Engenharia Mecanica e de Materiais (PPGEM)

    2004-07-01

    The heavy crude fraction processing is performed under very high vacuum to minimize thermal cracking which cause coke deposition and damage the equipment. The current tendency is to process heavier oil leading to higher process temperatures and consequently to greater fouling. This situation demands better knowledge fouling process by carbonization. This problem is pronounced in the residual gasoil region of a vacuum distillation unit because it obstructs the recirculation circuits and the spray system with serious environmental and economics implications. This paper review the main correlated published work related to coke generation and fouling and presents a discussion about the works. (author)

  4. Effect of Contact Resistance on Bulk Resistivity of Dry Coke Beds

    Science.gov (United States)

    Eidem, P. A.; Runde, M.; Tangstad, M.; Bakken, J. A.; Zhou, Z. Y.; Yu, A. B.

    2009-06-01

    Measurements show that bulk resistivity of dry coke beds decreases with increasing particle size. A further development of a coke bed model is proposed to explain this correlation. By image analysis, it has been determined that the total porosity increases with increasing particle size. An increased total porosity of the particles decreases the mechanical strength of the particles. In the modeling work, the strength of the coke particles is introduced through Young’s modulus. By the use of discrete element method (DEM) modeling of a dry coke bed, the particle-to-particle contact area variation with varying particle size and particle strength has been introduced into a model of the dry coke bed. This was done by the introduction of the concept of the Holm’s radius, known from metal contact theory for describing how the contact resistance is affected by the material resistivity and the contact area. By assuming a decrease in the particle strength due to increased porosity of the coke particles with increasing particle size, the calculated bulk resistivity for 7.3-mm particles with a Young’s modulus of 1.0 GPa is 5.24·10-3 Ωm and 3.44·10-3 Ωm for the 20-mm particles with a Young’s modulus of 0.1 GPa. By comparison, the measured bulk resistivity of the Corus coke is 4.67 ± 0.30·10-3 Ωm for the 5- to 10-mm fraction and 3.71 ± 0.45·10-3 Ωm for the 15- to 20-mm fraction. The measured contact resistance of Swedish Steel AB (SSAB) coke decreases with increasing contact area size from a contact diameter of 5 mm to a contact diameter of 30 mm. This is probably due to an increasing number of electrical contact spots. When two spheres are in contact, the measured contact resistance is lower compared to the 5-mm-diameter contact, which indicates that the increased contact pressure has lowered the contact resistance. This supports the modeling results.

  5. Effects of mechanical activation on the carbothermal reduction of chromite with metallurgical coke

    Directory of Open Access Journals (Sweden)

    Kenan Yıldız

    2010-06-01

    Full Text Available The carbothermal reduction of mechanically activated chromite with metallurgical coke under an argon atmosphere was investigated at temperatures between 1100 and 1400°C and the effects of the mechanical activation on chromite structure were analyzed by x-ray diffraction (XRD and scanning electron microscopy (SEM. An increase in specific surface area resulted in more contact points. The activation procedure led to amorphization and structural disordering in chromite and accelerated the degree of reduction and metalization in the mixture of chromite and metallurgical coke. Carbothermal reduction products were analzed by using scanning electron microscopy (SEM/EDS.

  6. Heat Transfer Characteristics of Calcined Petroleum Coke in Waste Heat Recovery Process

    OpenAIRE

    Bin Zheng; Yongqi Liu; Lichen Zou; Ruiyang Li

    2016-01-01

    This paper reports the results of heat transfer characteristics of calcined petroleum coke in waste heat recovery process. The model of heat exchanger was set up. The model has been used to investigate the effects of porosity (0.58 to 0.79), equivalent heat conductivity coefficient (0.9 to 1.1), and equivalent specific heat (0.9 to 1.1). The calculated values of calcined petroleum coke temperature showed good agreement with the corresponding available experimental data. The temperature distri...

  7. Non-competitive market behaviour in the international coking coal market

    International Nuclear Information System (INIS)

    In this paper, a primal dual programming model of international coking coal trade is constructed to test for non-competitive market behaviour. World trade in 1996 is simulated under perfect competition and various non-competitive market structures. Statistical tests are used to compare simulated trade flows with actual data. Assuming Cournot-Nash behaviour, an all consumer oligopsony market structure is preferred to alternative models. Under an all consumer oligopsony world coking coal prices and trade are lower than under perfect competition. Under an oligopsonistic structure welfare gains from productivity increases in Australian coal mines might largely accrue to coal buyers

  8. "The Real Thing:" Nominal Price Rigidity of the Nickel Coke, 1886-1959

    OpenAIRE

    Levy, Daniel; Young, Andrew

    2004-01-01

    We report that the price of a 6.5oz Coke was 5¢ from 1886 until 1959. Thus, we are documenting a nominal price rigidity that lasted more than 70 years! The case of Coca-Cola is particularly interesting because during the 70-year period there were substantial changes in the soft drink industry as well as two World Wars, the Great Depression, and numerous regulatory interventions and lawsuits, which led to substantial changes in the Coca-Cola market conditions. The nickel price of Coke, neverth...

  9. Thermodynamic analysis for a regenerative gas turbine cycle in coking process

    OpenAIRE

    Zelong Zhang, Lingen Chen, Fengrui Sun

    2014-01-01

    A regenerative gas turbine cycle driven by residual coke oven gas is proposed in this paper. The thermal efficiency and the work output (per ton of coke) of the system are analyzed based on thermodynamics and the theory of gas turbine cycle. The influences of the gas release rate, the residual gas rate and the effectiveness of regenerator on the performance of the cycle are analyzed by using numerical examples. It is found that the work output increases with the increase of the residual gas r...

  10. Urinary 1-hydroxypyrene in coke oven workers relative to exposure, alcohol consumption, and metabolic enzymes

    OpenAIRE

    Zhang, J; Ichiba, M.; Hara, K.; S. Zhang; Hanaoka, T.; Pan, G.; Yamano, Y.; K. Takahashi; Tomokuni, K

    2001-01-01

    OBJECTIVES—To investigate the influence of personal lifestyle—such as smoking and alcohol consumption—on urinary 1-hydroxypyrene (1-OHP) concentrations in coke oven workers exposed to polycyclic aromatic hydrocarbons (PAHs) and to evaluate the association of 1-OHP concentrations with the genetic polymorphism of several metabolic enzymes including cytochrome P-450 (CYP) 1A1 and glutathione S-tranferases (GSTs).
METHODS—The study population contained 162 coke oven workers and 58 controls employ...

  11. Construction solutions applied at coke oven battery no. 7 in the aspect of international requirements

    Energy Technology Data Exchange (ETDEWEB)

    Tadeusz Maj; Mariola Honisz; Wladyslaw Latocha; Wiktor Humer; Ludwik Kosyrczyk [' Zdzieszowice' Coking Plant Ltd. (Poland)

    2004-07-01

    15 slides/overheads outline this presentation. In February 2003 a new coke oven battery was put into operation in Zdzieszowice. In view of Poland's joining the European Union a series of technical solutions were implemented to improve working conditions in addition to improving the technology of the coking process. The paper describes the actions taken over one and a half years of operation. These include maintaining the recommended low level of NOx emission (comparable to that of CO) by waste gas recirculation.

  12. [Aerosol size distribution of organic carbon and elemental carbon on the top of coke oven and in the plant area].

    Science.gov (United States)

    Liu, Xiao-Feng; Peng, Lin; Bai, Hui-Ling; Mu, Ling; Song, Chong-Fang

    2013-08-01

    In order to investigate the characteristic of organic carbon (OC) and elemental carbon (EC) in particles on the top of coke oven and in the plant area, the particle matter samples of five size fraction including or = 10.2 microm were collected using Staplex234 cascade impactor, and OC and EC were analyzed by Elementar Analysensysteme GmbH vario EL cube. The mass concentrations of OC and EC associated with TSP on the top of coke oven were 291.6 microg x m(-3) and 255.1 microg x m(-3), while those in the plant area were 377.8 microg x m(-3) and 151.7 microg x m(-3). The mass concentration of secondary organic carbon (SOC) in particles with size of coke oven. The mass concentration of EC in TSP in the plant area was lower than that on the top of coke oven, while the mass concentration of OC in the plant area was significantly higher than that on the top of coke oven. The mass concentrations of OC and EC associated with particles less than 10.2 microm in the plant area were far higher than those in the atmosphere of area where the coke plant is located. The OC and EC in particles, which were collected both on the top of coke oven and in the plant area, were mainly enriched in fine particles. The size distribution of OC showed a clear distinction between the coke oven top and the plant area, which revealed that OC in the plant area was more preferably enriched in fine particles than that on the top of coke oven, and the same size distribution of EC was found on the top of coke oven and in the plant area. In the plant area, the mass concentration of SOC and the contribution of SOC to OC increased with the decreasing diameter in particles with diameter of less than 10.2 microm. PMID:24191535

  13. Reduction in toxicity of coking wastewater to aquatic organisms by vertical tubular biological reactor.

    Science.gov (United States)

    Zhou, Siyun; Watanabe, Haruna; Wei, Chang; Wang, Dongzhou; Zhou, Jiti; Tatarazako, Norihisa; Masunaga, Shigeki; Zhang, Ying

    2015-05-01

    We conducted a battery of toxicity tests using photo bacterium, algae, crustacean and fish to evaluate acute toxicity profile of coking wastewater, and to evaluate the performance of a novel wastewater treatment process, vertical tubular biological reactor (VTBR), in the removal of toxicity and certain chemical pollutants. A laboratory scale VTBR system was set up to treat industrial coking wastewater, and investigated both chemicals removal efficiency and acute bio-toxicity to aquatic organisms. The results showed that chemical oxygen demand (COD) and phenol reductions by VTBR were approximately 93% and 100%, respectively. VTBR also reduced the acute toxicity of coking wastewater significantly: Toxicity Unit (TU) decreased from 21.2 to 0.4 for Photobacterium phosphoreum, from 9.5 to 0.6 for Isochrysis galbana, from 31.9 to 1.3 for Daphnia magna, and from 30.0 to nearly 0 for Danio rerio. VTBR is an efficient treatment method for the removal of chemical pollutants and acute bio-toxicity from coking wastewater.

  14. [Priority pollutants ranking and screening of coke industry based on USEtox model].

    Science.gov (United States)

    Hao, Tian; Du, Peng-Fei; Du, Bin; Zeng, Si-Yu

    2014-01-01

    Thesis aims at evaluating and setting priority to human toxicity and ecotoxicity of coking pollutants. A field research and sampling project are conducted in coke plant in Shanxi so as to complete the coke emission inventory. The USEtox model representing recommended practice in LCIA characterization is applied to the emission inventory to quantify the potential impacts on human toxicity and ecotoxicity of emerging pollutants. Priority pollutants, production procedures and effects of changing plant site on the toxicity are analyzed. As conclusions, benzo(a) pyrene, benzene, Zn and As are identified as the priority pollutants in human toxicity, while pyrene and anthracene in ecotoxicity. Coal charging is the dominant procedure for organic toxicity and priority pollutants include benzo (a) pyrene, benzene, naphthalene, etc. While coke drenching is the dominant procedure for metal toxicity and priority pollutants include Zn, As, Ti, Hg etc. Emission to rural environment can reduce the organic toxicity significantly compared to the emission to urban environment. However, the site changing has no effect on metal toxicity and might increase the risk of the metal pollution to rural water and soil. PMID:24720220

  15. 40 CFR 63.303 - Standards for nonrecovery coke oven batteries.

    Science.gov (United States)

    2010-07-01

    ... each day of operation, the work practices specified in § 63.306(b)(6) and record the performance of the work practices as required in § 63.306(b)(7). (b) No owner or operator shall cause to be discharged or... to be discharged or allow to be discharged to the atmosphere coke oven emissions from each...

  16. Coke drums inspection and evaluation using stress and strain analysis techniques

    Energy Technology Data Exchange (ETDEWEB)

    Haraguchi, Marcio Issamu [Tricom Tecnologia e Servicos de Manutencao Industrial Ltda., Piquete, SP (Brazil); Samman, Mahmod [Houston Engineering Solutions, Houston, TX (United States); Tinoco, Ediberto Bastos; Marangone, Fabio de Castro; Silva, Hezio Rosa da; Barcelos, Gustavo de Carvalho [Petroleo Brasileiro S.A. (PETROBRAS), Rio de Janeiro, RJ (Brazil)

    2012-07-01

    Coke drums deform due to a complex combination of mechanical and thermal cyclic stresses. Bulges have progressive behavior and represent the main maintenance problem related to these drums. Bulge failure typically result in through-wall cracks, leaks, and sometimes fires. Such failures generally do not represent a great risk to personnel. Repairs needed to maintain reliability of these vessels might require extensive interruption to operation which in turn considerably impacts the profitability of the unit. Therefore the condition, progression and severity of these bulges should be closely monitored. Coke drums can be inspected during turnaround with 3D Laser Scanning and Remote Visual Inspection (RVI) tools, resulting in a detailed dimensional and visual evaluation of the internal surface. A typical project has some goals: inspect the equipment to generate maintenance or inspection recommendations, comparison with previous results and baseline data. Until recently, coke drum structural analysis has been traditionally performed analyzing Stress Concentration Factors (SCF) thought Finite Element Analysis methods; however this technique has some serious technical and practical limitations. To avoid these shortcomings, the new strain analysis technique PSI (Plastic Strain Index) was developed. This method which is based on API 579/ ASME FFS standard failure limit represents the state of the art of coke drum bulging severity assessment has an excellent correlation with failure history. (author)

  17. Derivation of heat value of coke/char from proximate analysis

    Energy Technology Data Exchange (ETDEWEB)

    Roy, R.R.P. (and others)

    From experimental data on high-, medium- and low-temperature cokes or chars, the following formulae were derived: gross CV (kcal/kg) 80(FC) + 76(VM); hydrogen content 0.224(VM). All values are on the air-dried basis.

  18. Blast furnace operating conditions manipulation for reducing coke consumption and CO{sub 2} emission

    Energy Technology Data Exchange (ETDEWEB)

    Bahgat, Mohamed; Abdel Halim, Khaled S.; El-Kelesh, Heba Ali; Nasr, Mahmoud I. [Central Metallurgical Research and Development Institute (CMRDI), Cairo (Egypt)

    2012-07-15

    A comparative reduction behavior of wuestite samples prepared from iron ore sinter was investigated to find the optimum way for reducing coke consumption and CO{sub 2} emission in blast furnace technology. A series of wuestite reduction experiments was carried out using different gas mixtures. A correlation between the experimental results and real data of blast furnaces at Egyptian Iron and Steel Company (EISCO) was demonstrated in order to optimize the coke consumption inside blast furnaces. Different theoretical models were applied on real data of blast furnaces to calculate the effect of operation parameters on the coke consumption. It was found that the wuestite reducibility can be controlled and enhanced using certain ratio of H{sub 2} and CO gases. Such kind of enhancement decreases the remaining quantity of unreduced wuestite which descends to the high temperature region of blast furnace. The theoretical analysis of real data using certain values of H{sub 2} and CO shows that increasing the amount of natural gas injection in blast furnace of EISCO will decrease the degree of direct reduction of iron oxide and consequently will decrease the amount of coke consumption. (Copyright copyright 2012 WILEY-VCH Verlag GmbH and Co. KGaA, Weinheim)

  19. 75 FR 11936 - USS Clairton Coke Works, Clairton, PA; Notice of Termination of Investigation

    Science.gov (United States)

    2010-03-12

    ... From the Federal Register Online via the Government Publishing Office DEPARTMENT OF LABOR Employment and Training Administration USS Clairton Coke Works, Clairton, PA; Notice of Termination of Investigation Pursuant to Section 223 of the Trade Act of 1974, as amended, an investigation was initiated in response to a petition filed on June 26,...

  20. Shift from coke to coal using direct reduction method and challenges

    Energy Technology Data Exchange (ETDEWEB)

    Okonkwo Paul Chukwuleke; Jiu-ju Cai; Sam Chukwujekwu; Song Xiao [Deakin University, Waurn Ponds, Vic. (Australia)

    2009-03-15

    Ironmaking involves the separation of iron ores. It not only represents the first step in steelmaking but also is the most capital-intensive and energy-intensive process in the production of steel. The main route for producing iron for steelmaking is to use the blast furnace, which uses metallurgical coke as the reductant. Concerns over the limited resources, the high cost of coking coals, and the environmental impacts of coking and sinter plants have driven steelmakers to develop alternative ironmaking processes that can use non-coking coals to reduce iron ores directly. Since the efficiency and productivity of modern large capacity blast furnaces will be difficult to surpass, blast furnaces will continue to retain their predominant position as the foremost ironmaking process for some time to come. The alternative ironmaking processes are therefore expected to play an increasingly significant role in the iron and steel industry, especially in meeting the needs of small-sized local and regional markets. It is likely that the importance of direct reduced iron (DRI) and hot metal as sources of virgin iron will continue to increase, especially in the developing countries where steelmaking is, and will be, primarily based on electric arc furnace (EAF) minimills. Consequently, the challenges that are faced by the new technology have to be embraced.

  1. Coke formation in the oxidative dehydrogenation of ethylbenzene to styrene by TEOM

    NARCIS (Netherlands)

    Nederlof, C.; Vijfhuizen, P.; Zarubina, V.; Melian-Cabrera, I.; Kapteijn, F.; Makkee, M.

    2014-01-01

    A packed bed microbalance reactor setup (TEOM-GC) is used to investigate the formation of coke as a function of time-on-stream on gamma-Al2O3 and 3P/SiO2 catalyst samples under different conditions for the ODH reaction of ethylbenzene to styrene. All samples show a linear correlation of the styrene

  2. Coke formation in the oxidative dehydrogenation of ethylbenzene to styrene by TEOM

    NARCIS (Netherlands)

    C. Nederlof; P. Vijfhuizen; V. Zarubina; I. Melián-Cabrera; F. Kapteijn; M. Makkee

    2014-01-01

    A packed bed microbalance reactor setup (TEOM-GC) is used to investigate the formation of coke as a function of time-on-stream on γ-Al2O3 and 3P/SiO2 catalyst samples under different conditions for the ODH reaction of ethylbenzene to styrene. All samples show a linear correlation of the styrene sele

  3. Application of CyboCon Advanced Adjustment and Control Software Package in Delayed Coking Unit

    Institute of Scientific and Technical Information of China (English)

    Guo Hua

    2002-01-01

    This article refers to application of the CyboCon software package based upon the model-free adaptive control (MFA) in the 800-kt/a delayed coking unit to realize an advanced adjustment and control strategy for the temperature control of the heater. Operation tests have revealed the convenience in operating system and simplicity in maintenance, leading to good economic benefits.

  4. ANGULAR DISTORTION ALLOWABLE VALUE AND ASSESS METHOD OF WELD ON COKE TOWER

    Institute of Scientific and Technical Information of China (English)

    2007-01-01

    A graph as the new engineering method for estimate the safety of bulging deformation of coke tower is proposed. Through stresses analysis of circumferential weld of coke tower and comparing the stresses produced by pressure with heat stress of steady state, residual stress, bending stress produced by both itself weight and wind loads, it showed that the stresses produced by pressure on the angle distortion are the main factor of equivalent stress of the combined stress. After comparing four kinds of stress controlling conditions, the relation to stress with depth of angular distortion, grade of curvature of angular distortion and half of region of angular distortion has been inferred. Graph of deformation allowable value of coke tower for different condition by angular distortion and half of region of angular distortion has been plotted. The five steps for its engineering use have been explained. The lighter the grade of curvature is, the larger of bulge allowance, may be, and the bigger of depth of angular distortion may pose too. For the coke tower with a popular structure of Dg 5 400 mm×28 mm, the result by graph is nearly more than the result of two formulas formed by other research, the error is less than 7.0%. But, the graph can be easily applied to different size of angular distortion.

  5. Sensory evaluation and electronic tongue analysis for sweetener recognition in coke drinks

    Science.gov (United States)

    Szöllősi, Dániel; Kovács, Zoltán; Gere, Attila; Sípos, László; Kókai, Zoltán; Fekete, András

    2011-09-01

    Consumption of beverages with low energy has an increasing role. Furthermore hydrolyzed starch products such as inverted syrup show a wide application in the beverage industry. Therefore the importance of methods which can monitor the usage of natural and artificial sweeteners is increasing. The task was to describe the relevant sensory attributes and to determine the applicability of the electronic tongue to discriminate the coke drink samples with different sweeteners. Furthermore the aim was to find relationship between the taste attributes and measurement results provided by electronic tongue. An Alpha Astree Electronic Tongue and a trained sensory panel were used to evaluate the coke samples. Panelists found significant differences between the samples in 15 cases from the 18 sensory attributes defined previously by the consensus group. Coke drinks containing different kind of sweeteners can be characterized according to these sensory attributes. The samples were definitely distinguished by the electronic tongue. The main difference was found between the samples made with natural and artificial sweeteners. However electronic tongue was able to distinguish samples containing different kind of artificial and different kind of natural sweeteners, as well. Taste attributes of coke drinks determined by sensory panel were predicted by partial least squares regression method based on the results of electronic tongue with close correlation and low prediction error.

  6. Biomarkers of polycyclic aromatic hydrocarbon exposure in European coke oven workers.

    Science.gov (United States)

    Talaska, Glenn; Thoroman, Jeff; Schuman, Brenda; Käfferlein, Heiko Udo

    2014-12-01

    Biomonitoring is an excellent method for capturing the results of all exposures, regardless of route. Coke oven workers include certain groups that have the potential for high exposure to polycyclic aromatic hydrocarbons (PAH) and other materials. Biomarkers of exposure to these agents include PAH metabolites as markers of internal dose and carcinogen-DNA adducts as measure of effective dose. The purpose of this study was to determine the levels of these biomarkers in persons with different job duties in a modern coke oven plant. We report that the mean levels of 1-hydroxypyrene (1HP) and carcinogen DNA adducts in the exfoliated urothelial cells of coke oven workers are increased the closer a group of workers is to the ovens and highest in the top oven workers with average 1HP level of 11.6 μg/l and 22 adducts per 10(9) unadducted nucleotides. Both 1HP and carcinogen DNA adduct levels increased in supervisors, area workers, side oven workers, top and side oven workers, and top oven workers, respectively. These data are the first to demonstrate an increase in target organ genotoxicity in coke oven workers and a relationship with other biomarkers. Future studies will determine the identity of the DNA adducts, their correlation with 1HP levels and the relationship between levels in individual workers. PMID:25445007

  7. 40 CFR 63.305 - Alternative standards for coke oven doors equipped with sheds.

    Science.gov (United States)

    2010-07-01

    ... 40 Protection of Environment 9 2010-07-01 2010-07-01 false Alternative standards for coke oven doors equipped with sheds. 63.305 Section 63.305 Protection of Environment ENVIRONMENTAL PROTECTION AGENCY (CONTINUED) AIR PROGRAMS (CONTINUED) NATIONAL EMISSION STANDARDS FOR HAZARDOUS AIR POLLUTANTS FOR SOURCE CATEGORIES National Emission...

  8. Coke, char and organic waste behaviour in the blast furnace with high injection rate

    Directory of Open Access Journals (Sweden)

    Gudenau, H. W.

    2003-10-01

    Full Text Available Blast furnace operation with low coke rate, high amount of auxiliary hydrocarbons and use of nut coke causes a change in coke quality requirements. In particular, not burned in the raceway residues of injected substances (char and ash can influence the coke behaviour. Therefore combustion efficiency of various organic wastes with and without pulverized coal injection (PCI and coal char has been investigated under the raceway simulation conditions. Mixing of various substances improves their combustion efficiency. Study on coke gasification by carbon dioxide in the presence of char showed that with the increase of char concentration, coke strength reduction becomes smaller. The reactivity of char with CO2 is higher than that of coke. Therefore char is consumed preferentially. In presence of injected char, total pore volume in coke and its wear resistance were increased. Coke reactivity and microstructure in the presence of various kinds of ash has been studied. Many ash spheres were observed on the surface of coke matrix and its size was dependent on ash properties.

    La operación del horno alto con una tasa baja de coque, una cantidad elevada de hidrocarburos auxiliares y el empleo de coque calibrado, origina un cambio en las necesidades de calidad del coque. En particular, pueden influir en el comportamiento del coque los residuos inquemados en el raceway (cavidad enfrente a las toberas del horno de las sustancias que se inyectan (char y cenizas. El char es el residuo de carbón que se origina después que el carbón libera sus sustancias volátiles. Por tanto, se ha investigado la eficiencia de la combustión de varios residuos orgánicos con y sin inyección de carbón pulverizado (ICP y char, bajo las condiciones de simulación del raceway. La mezcla de varias sustancias mejora la eficiencia a la combustión. El estudio de la gasificación del coque por el dióxido de carbono en la

  9. Coke state determination in the blast furnace hearth using a tuyere probe

    Energy Technology Data Exchange (ETDEWEB)

    Negro, P.; Pierret, H.; Steiler, J.M. (Institut de Recherches de la Siderurgie Francaise (IRSID), 78 - Saint-Germain-en-Laye (France)); Lao, D.; Eymond, J.L.; Fauchoit, P. (Sollac, 59 - Dunkerque (France)); Eibes, C.; Blaise, G.; Urvoy, A.; Helleisen, M.; Giroldini, F.; Hartig, M.; Rausch, H.

    1993-04-01

    Coke samplings at blast furnace tuyeres are a powerful mean to study the behaviour of the lower part of the furnace. A tuyere probe has been installed since April 1985 on the BF 2 at Sollac Fos. This probe is 19 m long and 11 tons weight. It uses a 265 mm internal diameter pipe which samples materials until the centre of the BF. Up-to-now, 28 trials have been completed. The results obtained with this probe allow: a better understanding of the phenomena occurring in the blast furnace hearth, to establish several relationships between the internal state of the hearth and the operation conditions, to build and validate a new image of the cohesive zone and the coke state, to measure and understand the influence of coal injection on the BF operation. Since April 1991, a movable tuyere probe has been in operation within Usinor Sacilor Group. This machine is more lighter than the fixed one weighing only 5.5 tons and smaller measuring 5 m long for 1.3 m width. The probe is a 260 mm internal diameter pipe which can be introduced for 4.25 m in the furnace. In 20 months, it is more than 40 coke core borings which have been achieved on 9 different furnaces of 4 different plants. These two probes are complementary. The fixed probe is only used through one tuyere of one BF. In addition, this probe can reach the centre of the furnace and give a complete description of the materials present along the radius. The movable machine cannot reach the centre of the BF, but it authorizes the study of: some very different BF operating conditions, the influence of the feed materials qualities in a large range, the heterogeneity between several tuyeres of one BF, the effect of the BF size. This text presents our approach in coke quality research, relying upon the results of coke core borings. 6 refs., 17 figs.

  10. Coke state determination in the blast furnace hearth using a tuyere probe

    Energy Technology Data Exchange (ETDEWEB)

    Negro, P.; Pierret, H.; Steiler, J. [and others] [Institut de Recherches de la Siderurgie Francaise (IRSID), Saint-Germain-en-Laye (France)

    1996-11-01

    Coke samplings at blast furnace tuyeres are a powerful means to study the behaviour of the lower part of the furnace. A tuyere probe has been installed since April 1985 on the BF2 at Sollac Fos. This probe is 19 m long and 11 tons in weight. It uses a 265 mm internal diameter pipe which samples materials in the centre of the BF. Up to now, 28 trials have been completed. The results obtained allow: a better understanding of the phenomena occurring in the blast furnace hearth, to establish several relationships between the internal state of the hearth and operation conditions, to build and validate a new image of the cohesive zone and the coke state, to measure and understand the influence of coal injection on the BF operation. Since April 1991, a movable tuyere probe has been in operation within Usinor Sacilor Group. This machine is lighter than the fixed one weighing only 5.5 tons and smaller measuring 5 m long for 1.3 m width. The probe is a 260 mm internal diameter pipe which can be introduced 4.25 m into the furnace. In 20 months, more than 40 coke core borings have been achieved on 9 different furnaces in 4 different plants. These two probes are complementary. The fixed probe is only used through one tuyere of one BF. In addition, this probe can reach the centre of the furnace and give a complete description of the materials present along the radius. The movable machine cannot reach the centre of the BF, but it enables the study of: some very different BF operating conditions, the influence of the feed materials qualities in a large range, the heterogeneity between several tuyeres of one BF, and the effect of the BF size. This paper presents an approach in coke quality research, relying upon the results of coke core borings.

  11. Evaluation of biomarkers in plasma, blood, and urine samples from coke oven workers: significance of exposure to polycyclic aromatic hydrocarbons.

    OpenAIRE

    Ovrebø, S; Haugen, A; Farmer, P B; Anderson, D.(California Institute of Technology, Pasadena, USA)

    1995-01-01

    OBJECTIVE--The aim was to assess the significance of two biomarkers; antibody to benzo(a)pyrene DNA adducts and concentration of hydroxyethylvaline haemoglobin adducts in samples from a well studied group of coke oven workers. As a measure of exposure we have used 1-hydroxypyrene in urine. METHODS--Urine and blood samples were collected from coke oven workers and a control group. Samples from coke oven plant workers were collected in January and June. 1-Hydroxypyrene was measured in urine by ...

  12. Coke Formation During Hydrocarbons Pyrolysis. Part Two: Methane Thermal Cracking Formation de coke pendant la pyrolyse des hydrocarbures. Deuxième partie : pyrolyse du méthane

    Directory of Open Access Journals (Sweden)

    Billaud F.

    2006-11-01

    Full Text Available Part one of this article dealt with coking in a steam cracking furnace. In this process, coke deposition is a very complex phenomenon due to the number of parameters involved. Nevertheless, for this process, coke deposition is a secondary reaction which does not affect steam cracking yields. It is completely different for methane thermal cracking. Coke is one of the main products of this reaction. Part two of this article deals with coke deposition on the walls of the reactors used for methane thermal cracking. After a brief description of the different set-ups used to study coke deposition, the main parameters involved are listed. The importance of temperature, conversion, type of diluent, and hydrocarbon partial pressure will be enhanced. To conclude, two approaches to the mechanism are proposed to explain coke formation during methane thermal cracking. La première partie de cet article faisait le point sur les réactions indésirables de cokage dans les réacteurs de vapocraquage : dans le cadre de ce procédé, la formation de coke est un phénomène complexe du fait du nombre important de paramètres mis en jeu. Toutefois, pour ce procédé, la réaction de formation du coke à la paroi des réacteurs est une réaction secondaire qui n'affecte pas les rendements de vapocraquage. Ceci est complètement différent dans le cas de la pyrolyse thermique du méthane, procédé pour lequel le coke est un produit principal et indésirable de la réaction. La seconde partie de cet article est consacrée plus particulièrement à la formation du coke, lors de la pyrolyse du méthane et présente les principaux résultats expérimentaux décrits dans la littérature. Parmi les différents montages expérimentaux utilisés pour mesurer le dépôt de coke, il est mentionné, à partir des travaux de la littérature, les 2 techniques suivantes : - la technique de la paroi chaude, - la technique du fil chaud. Pour la première technique, les montages exp

  13. JN60-6型焦炉降低炼焦耗热量的措施%Measures for decreasing coking heat consumption of JN60-6 coke oven

    Institute of Scientific and Technical Information of China (English)

    刘君红; 邱岳

    2015-01-01

    Based on actual production condition of coke oven,a series of measures were taken to deal with the problems of COG pipeline,resistance of coke oven gas main pipe,flow meter measurement and other factors affecting coking heat consumption. As a result,coke oven gas consumption was effec-tively controlled and reduced remarkably.%根据焦炉实际生产,针对焦炉煤气管线、焦炉煤气主管阻力、流量计计量及其他影响炼焦耗热量的问题采取了一系列措施,改进后焦炉煤气使用量得到有效控制,炼焦耗热量明显降低。

  14. Reducing Heat Consumption of Coking Production Practice of Tamping Coke Oven%降低捣固焦炉炼焦耗热量的生产实践

    Institute of Scientific and Technical Information of China (English)

    杨一平

    2012-01-01

    捣固焦炉由于其特殊的生产操作方式,焦炉耗热量较高。通过实施原料煤质量、焦炉热工管理、生产操作等方面生产控制,为捣固焦炉炼焦耗热量的降低提供了有效途径。%Because of its special operation mode, tamping coke oven has higher heat consumption of coke oven. In this ifaper, through the implementation of raw coal quality, coke thermal management, production operations and other aspects of the production control for tamping coke oven, an effective way in reducing which provides were provided.

  15. Problem Analysis and Improvement in Stamping Coke Production by Transformed Top Charging Coke Oven%顶装焦炉改为捣固焦生产后的问题及改进

    Institute of Scientific and Technical Information of China (English)

    王即胜; 刘成雷; 常宇

    2014-01-01

    In order to reduce production cost, Jinan Steel transformed three 4.3 m top charging coke ovens for stamping coke production. Because of relatively small shrinkage of the coal in coking process, imperfect transformation facilities, unreasonable operation and other reasons, some problems appeared in the production, for example, large coke pushing current, serious leaking of oven body and poor dedusting effect. By controlling the G value of mixed coal below 72, reducing the density of briquette heap, narrowing the width of briquettes and other measures, the existent problems were avoided or relieved. In view of different structure and production characteristics between top charging coke oven and tamping coke oven, caution should be taken in the top charging coke oven transformed to tamping coke production.%为降低生产成本,济钢将3座4.3 m顶装焦炉改为捣固焦生产。由于入炉煤在结焦过程中收缩量相对变小,配套设施改造不完善,操作不合理等原因,导致生产中出现推焦电流过大、炉体窜漏严重、除尘效果差等问题。通过控制配合煤G值在72以下,降低煤饼堆比重,缩小煤饼宽度等措施,存在的问题得到了避免或缓解。鉴于顶装焦炉和捣固焦炉不同的结构及生产特点,应谨慎考虑顶装焦炉改捣固焦生产。

  16. Torrefaction reduction of coke formation on catalysts used in esterification and cracking of biofuels from pyrolysed lignocellulosic feedstocks

    Energy Technology Data Exchange (ETDEWEB)

    Kastner, James R; Mani, Sudhagar; Hilten, Roger; Das, Keshav C

    2015-11-04

    A bio-oil production process involving torrefaction pretreatment, catalytic esterification, pyrolysis, and secondary catalytic processing significantly reduces yields of reactor char, catalyst coke, and catalyst tar relative to the best-case conditions using non-torrefied feedstock. The reduction in coke as a result of torrefaction was 28.5% relative to the respective control for slow pyrolysis bio-oil upgrading. In fast pyrolysis bio-oil processing, the greatest reduction in coke was 34.9%. Torrefaction at 275.degree. C. reduced levels of acid products including acetic acid and formic acid in the bio-oil, which reduced catalyst coking and increased catalyst effectiveness and aromatic hydrocarbon yields in the upgraded oils. The process of bio-oil generation further comprises a catalytic esterification of acids and aldehydes to generate such as ethyl levulinate from lignified biomass feedstock.

  17. Surface modification of graphite by coke coating for reduction of initial irreversible capacity in lithium secondary batteries

    Science.gov (United States)

    Yoon, Songhun; Kim, Hanjun; Oh, Seung M.

    Surface modification of graphite to reduce the irreversible capacity loss during the first charging period of graphite anodes is described. For the surface modification, artificial graphite (Lonza KS44) is dispersed in a tetrahydrofuran/acetone solution which contains coal tar pitch. The solvent is then evaporated. The loaded pitch component is converted to coke by a heat treatment at 1000°C in argon atmosphere. The resulting coke-coated graphite has a smaller surface area than that of the pristine one. The reduction of surface area, which is due to the coverage of pores of <10 nm by the coke component, causes a decrease in the irreversible capacity on the first cycle. The extent of electrolyte decomposition, gas evolution and surface film growth is also less with the coke-coated graphite electrode.

  18. Study on Development Trend of Coke Oven Machinery%焦炉机械发展趋势分析

    Institute of Scientific and Technical Information of China (English)

    乔科佳; 房斌贝

    2016-01-01

    通过对我国焦炉机械行业当前的生产状况、产能等进行分析,结合国家在焦化行业的现行产业政策,对焦炉机械行业的发展趋势和市场需求进行预测,指出焦炉机械供应商应该采取的应对措施。%Based on the current production situations and capacity of coke oven machinery industry in China and the existing coking industrial policy of China, the paper predicts the development trend of coke oven machinery industry and the market demand and puts forward measures that shall be taken by the coke oven machinery supplier to respond to the market change.

  19. Waste heat conducting system for side burner regenerative coke oven batteries with divided heating system. [German Patent

    Energy Technology Data Exchange (ETDEWEB)

    Thiersch, F.; Strobel, M.; Schmitz, T.

    1980-08-21

    In the well known waste heat removal system for side burner regenerative coking over batteries with divided heating system both flues could be used simultaneously and equally. The flues in the longitudinal direction of the battery open into a common chimney foot connection at one end of the battery. They are individually connected via opposite groups of transverse flues to opposite groups of waste heat elbows of waste heat valves on the machine and on the coke side.

  20. Results of the simulation of gasification of the mexican petroleum coke from the refineries of Ciudad Madero and Cadereyta

    Directory of Open Access Journals (Sweden)

    G. Urquiza–Beltrán

    2008-04-01

    Full Text Available This paper evaluates in terms of energy the gasification of the petroleum coke from the refineries of Cd Madero and Cadereyta in Mexico. The energy evaluation of the synthetic gas (syngas focuses mainly on the chemical composition of the clean syngas (gasl and its energy characteristics: heating value, the energy power, the cold gas efficiency and the thermal efficiency of gasification. The results of the simulation indicate that the gasification of the petroleum coke from Cadereyta called CRC, produces a gasl with better performance and energy characteristics than those obtained when gasifying the coke of petroleum from Cd. Madero, called CRM. When the CRC is gasified, the rate of production of gasl obtained is of 2.07 kggasl/kgcoque, while the rate of production of gasl for the CRM is 1.89 kggasl/kgcoque. The HHV of the gasl of the CRC is 12 729.56 kJ/kggasl while for the CRM is 11 639.13 kJ/kggasl. The energy power of the gasl of the CRC is greater, with a difference of 25.87 GJ/h, with regard to the energy power of the gasl of the CRM. Under the specified conditions of operation, energy is generated ata rate of 26.46 MJ/kgcoque coke in the gasification of the CRC coke of petroleum, while when gasifying the CRM coke of petroleum 22.09 MJ/kgcoque are generated. Currently, the petroleum coke produced in the refinery of Madero is consumed in the power plants of Tamuín, San Luis Potosí, Mexico, while the petroleum coke produced by the refinery of Cadereyta is used in the cement industry.

  1. Comparative carcinogenic potencies of particulates from diesel engine exhausts, coke oven emissions, roofing tar aerosols and cigarette smoke.

    OpenAIRE

    Albert, R E

    1983-01-01

    Mammalian cell mutagenesis, transformation and skin tumorigenesis assays show similar results in comparing the potencies of diesel, coke oven, roofing tar and cigarette smoke particulates. These assay results are reasonably consistent with the comparative carcinogenic potencies of coke oven and roofing tar emissions as determined by epidemiological studies. The bacterial mutagenesis assay tends to show disproportionately high potencies, particularly with diesel particulates. Results to date e...

  2. Assessment of potential damage to DNA in urine of coke oven workers: an assay of unscheduled DNA synthesis.

    OpenAIRE

    Roos, F.; Renier, A.; Ettlinger, J; Iwatsubo, Y; Letourneux, M; Haguenoer, J M; Jaurand, M C; Pairon, J C

    1997-01-01

    OBJECTIVES: A study was conducted in coke oven workers to evaluate the biological consequences of the exposure of these workers, particularly production of potential genotoxic factors. METHODS: 60 coke oven workers and 40 controls were recruited in the same iron and steel works. Exposure to polycyclic aromatic hydrocarbons (PAHs) was assessed by job and measurement of 1-hydroxypyrene (1OHP) in urine samples. An unscheduled DNA synthesis assay was performed on rat pleural mesothelial cells use...

  3. Correlation Between Toluene Environmental Monitoring and Biological Index of Urinary Hippuric Acid of Workers in the Coke Industry

    OpenAIRE

    MM Amin; Kalantari, A.; N BASHARDOOST; AR Bahrami; M. Rismanchian; Gh Mirsatari; Mansouri, F.

    2007-01-01

    Introduction: Toluene is an organic solvent that it is one of the byproducts in the coke industry. Exposure to toluene causes central nervous system dysfunction and others disorders. Many workers are exposed to toluene due to leakage from tracks. Therefore the aim of this study was to determine the levels of exposure through environmental and biological monitoring of toluene Methods: Air toluene sampling of air inhaled by 36 coke oven workers was done by using activated charcoal tubes and per...

  4. Inhibition of coking and metal dusting on conventional alloys by using a nickel-tin intermetallic coating

    OpenAIRE

    Geers, Christine

    2013-01-01

    Coking and Metal Dusting are high temperature corrosion phenomena occurring at 400 to 900°C under highly reducing conditions with low oxygen partial pressures and high carbon activities. Coking is the catalytical deposition of carbon on steels or nickel base alloys. Metal Dusting is a rapid material loss due to massive carburization and graphite precipitation within the metal matrix, causing the loss of integrity. Both phenomena have been investigated for the last fifty years. Metals suscepti...

  5. Reaction Mechanism for the Formation of Nitrogen Oxides (NO x ) During Coke Oxidation in Fluidized Catalytic Cracking Units

    KAUST Repository

    Chaparala, Sree Vidya

    2015-06-11

    Fluidized catalytic cracking (FCC) units in refineries process heavy feedstock obtained from crude oil distillation. While cracking feed, catalysts get deactivated due to coke deposition. During catalyst regeneration by burning coke in air, nitrogen oxides (NOx) are formed. The increase in nitrogen content in feed over time has resulted in increased NOx emissions. To predict NOx concentration in flue gas, a reliable model for FCC regenerators is needed that requires comprehensive understanding and accurate kinetics for NOx formation. Based on the nitrogen-containing functional groups on coke, model molecules are selected to study reactions between coke-bound nitrogen and O2 to form NO and NO2 using density functional theory. The reaction kinetics for the proposed pathways are evaluated using transition state theory. It is observed that the addition of O2 on coke is favored only when the free radical is present on the carbon atom instead of nitrogen atom. Thus, NOx formation during coke oxidation does not result from the direct attack by O2 on N atoms of coke, but from the transfer of an O atom to N from a neighboring site. The low activation energies required for NO formation indicate that it is more likely to form than NO2 during coke oxidation. The favorable pathways for NOx formation that can be used in FCC models are identified. Copyright © 2015 Taylor & Francis Group, LLC.

  6. BEEHIVE: Sustainable Methodology for Fashion Design

    OpenAIRE

    Morais, C.; Carvalho, C.; Broega, A. C.

    2014-01-01

    ISBN: 978 88 6493 027 5 The proposal methodology tends to close the “product fashion cycle”, defending the existence of a good waste management policy, so that the clothing are thrown away can be reused or recycled to come back again as material to produce yarn, fabric or knit. Subsequently these materials should be include in the production of sustainable apparel, whose design methodologies should be concerned in providing more durable garments and being possible to transform according to...

  7. Thermal and electrochemical studies of carbons for Li-ion batteries. 1. Thermal analysis of petroleum and pitch cokes

    Science.gov (United States)

    Jiang, W.; Tran, T.; Song, X.; Kinoshita, K.

    Thermal analyses involving simultaneous thermal gravimetric analysis (TGA) and differential thermal analysis (DTA) were used to study the air oxidation of petroleum (fluid and needle cokes) and coal-tar pitch cokes. The intent of this study is to understand the relationship between the structure of carbonaceous materials and their thermal oxidation behavior in air (Part 1). A correlation between the thermal oxidative properties of cokes and their electrochemical Li-intercalation performance is discussed in the following paper (Part 2). The carbon samples were heat-treated at temperatures up to 2800°C, and three thermal parameters were determined — ignition temperature ( Ti), temperature maximum ( Tm) in the DTA curves, and the temperature at which 15% carbon weight loss was attained ( T15). The measurements showed trends that are consistent with prior reports that the active sites on the surface and not the total surface area (TSA) are responsible for the thermal behavior of the carbons. Because of the difference in the graphitizability of petroleum and pitch cokes that was obtained by heat treatment, variations in the thermal parameters were observed. Needle cokes are the most easily graphitized and this is reflected in the higher values of the thermal parameters compared to the fluid and pitch cokes.

  8. Application of multivariate data analysis in the construction of predictive model for the chemical properties of coke

    Science.gov (United States)

    Sajdak, Marcin; Smędowski, Łukasz

    2013-09-01

    The aim of this work was to develop a statistical model which can predict values describing chemical composition of cokes performed in industrial scale. This model was developed on the basis of data that were taken from the production system used in the one of Polish coking plant. Elaborated equation include quality parameters of initial coals that form coal blends as well as contribution of additions such as coke and petrochemical coke. These equations allow to predict chemical composition of coke, e.g. contributions of: sulphur, ash, phosphorus and chlorine within the coke. A model was elaborated with use of STATISTICA 10 program and it is based on factor and multiply regression analyses. These analyses were chosen from among few kinds of regression analyses. They allowed to develop prediction model with the required goodness of fit between calculated and actual values. Goodness of fit was elaborated with: • residuals analyses, • residues normality and predicted normality • mean absolute error • Pearson correlation confidence

  9. Prediction of the quality of coke obtained from vacuum residues by using spectroscopy infrared FTIR-ART

    Science.gov (United States)

    León, A. Y.; Rodríguez, N. A.; Mejía, E.; Cabanzo, R.

    2016-02-01

    According to the trend of the heavy crudes and high demand of fuels, it is projected a considerable increase in the production of vacuum residues. With the purpose of taking advantage of these loads, the refineries have been improving conversion processes for the production of better quality distillates. However, as increasing the severity conditions and the species content of resins and asphaltenes high concentrations of coke are obtained. To provide an insight into the quality and cokes properties, in this study fifty (50) coke samples obtained from vacuum residues processed under conditions of thermal cracking and hydroconversion were selected. Each coke was analysed in detail with properties such as fixed carbon, volatile material, ash, and calorific value. Subsequently, a characterization methodology was developed to predict the properties of cokes, by using partial least squares regression, and infrared spectroscopy (FTIR-ATR) in the spectral range from 4000 to 500cm-1. The models obtained by chemometrics allowed to predict the quality of the coke produced from vacuum residues with reliable responses in short periods of time.

  10. [Preliminary investigation on emission of PCDD/Fs and DL-PCBs through flue gas from coke plants in China].

    Science.gov (United States)

    Sun, Peng-Cheng; Li, Xiao-Lu; Cheng, Gang; Lu, Yong; Wu, Chang-Min; Wu, Chang-Min; Luo, Jin-Hong

    2014-07-01

    According to the Stockholm Convention, polychlorinated dibenzo-p-dioxins/dibenzofurans (PCDD/Fs) and dioxin-like polychlorinated biphenyls (DL-PCBs) are classified into unintentionally produced persistent organic pollutants (UP-POPs), and named dioxins. Coke production as a thermal process contains organic matters, metal and chlorine, is considered to be a potential source of dioxins. Intensive studies on the emission of dioxins from coking industry are still very scarce. In order to estimate the emission properties of dioxins through coke production, isotope dilution HRGC/HRMS technique was used to determine the concentration of dioxins through flue gas during heating of coal. Three results were obtained. First, total toxic equivalents at each stationary emission source were in the range of 3.9-30.0 pg x m(-3) (at WHO-TEQ) for dioxins which was lower than other thermal processes such as municipal solid waste incineration. Second, higher chlorinated PCDD/Fs were the dominant congeners. Third, emissions of dioxins were dependent on coking pattern. Stamping coking and higher coking chamber may lead to lower emission. PMID:25244832

  11. Multispecies acute toxicity evaluation of wastewaters from different treatment stages in a coking wastewater-treatment plant.

    Science.gov (United States)

    Zhao, Jian-Liang; Jiang, Yu-Xia; Yan, Bo; Wei, Chaohai; Zhang, Li-Juan; Ying, Guang-Guo

    2014-09-01

    Coking wastewater contributes approximately 5% of the total discharge volume of industrial wastewaters every year in China. The toxicity of coking wastewater to aquatic organisms is still unknown. The authors evaluated the toxicity of wastewater from different treatment stages in a coking wastewater treatment plant, South China, using 5 test species belonging to different trophic levels: luminous bacteria, green alga, a crustacean, duckweed, and zebrafish embryos. The raw influent displayed the highest toxicity to the test species, with toxic units ranging from 16.2 to 1176. The toxicity in the wastewater was then gradually removed by sequential primary treatment, biological fluidized-bed treatment, and secondary clarifier treatment. The toxic unit of the final effluent was reduced to 2.26 for the green alga (Pseudokirchneriella subcapitata) and to 0 for the other 4 organisms. Quantitative analysis of metals and polycyclic aromatic hydrocarbons (PAHs) and qualitative scanning by gas chromatography-mass spectrometry showed the presence of a variety of pollutants in the coking wastewaters. Multivariate statistical analysis revealed that the toxicity in the coking wastewater was correlated to the chemical oxygen demand, total nitrogen, ammonia nitrogen, volatile phenols, sulfide, metals (Cr, As, Sb, Hg, Pb, and Ni), and ΣPAHs. Based on the results, it is required to set a safety emission limit value for the discharge of coking wastewater to protect aquatic organisms in the receiving water bodies. PMID:25042296

  12. Novel carbon-rich additives preparation by degradative solvent extraction of biomass wastes for coke-making.

    Science.gov (United States)

    Zhu, Xianqing; Li, Xian; Xiao, Li; Zhang, Xiaoyong; Tong, Shan; Wu, Chao; Ashida, Ryuichi; Liu, Wenqiang; Miura, Kouichi; Yao, Hong

    2016-05-01

    In this work, two extracts (Soluble and Deposit) were produced by degradative solvent extraction of biomass wastes from 250 to 350°C. The feasibilities of using Soluble and Deposit as additives for coke-making were investigated for the first time. The Soluble and Deposit, having significantly higher carbon content, lower oxygen content and extremely lower ash content than raw biomasses. All Solubles and most of Deposits can melt completely at the temperature ranged from 80 to 120°C and 140 to 180°C, respectively. The additions of Soluble or Deposit into the coke-making coal significantly improved their thermoplastic properties with as high as 9°C increase of the plastic range. Furthermore, the addition of Deposit or Soluble also markedly enhanced the coke quality through increasing coke strength after reaction (CSR) and reducing coke reactivity index (CRI). Therefore, the Soluble and Deposit were proved to be good additives for coke-making. PMID:26871958

  13. Functionalization of Petroleum Coke-Derived Carbon for Synergistically Enhanced Capacitive Performance

    Science.gov (United States)

    Zhang, Yan; Li, Xuejin; Huang, Jufeng; Xing, Wei; Yan, Zifeng

    2016-03-01

    Petroleum coke is a valuable and potential source for clean energy storage if it could be modified legitimately and facilely. In the present study, porous carbon with high surface area and abundant oxygen-containing groups was prepared from petroleum coke by chemical activation and modification processes. The as-prepared carbon exhibits a high surface area (1129 m2 · g-1) and stable micrographic structure. It presents a high specific capacitance and excellent rate performance in KOH electrolyte. Even at an ultrahigh current density of 50 A · g-1, the specific capacitance of the prepared carbon can still reach up to an unprecedented value of 261 F · g-1 with a superhigh retention rate of 81 %. In addition, the energy density of this material in aqueous electrolyte can be as high as 13.9 Wh · kg-1. The high energy density and excellent rate performance ensure its prosperous application in high-power energy storage system.

  14. Formation of nitrogen-containing compounds during slow pyrolysis and oxidation of petroleum coke

    Energy Technology Data Exchange (ETDEWEB)

    Furimsky, E.; Ohtsuka, Y. [IMAF Group, Ottawa, ON (Canada)

    1997-09-01

    The petroleum coke from a fluid coking process was pyrolyzed in helium and oxidized in 1% and 4% O{sub 2} and in air, with the aim to determine N-containing compounds such as HCN, NH{sub 3}, NO, and N{sub 2}O. The experiments were performed with and without limestone. NO was the major product during all oxidation runs. N{sub 2}O was formed only in air. In this case, N{sub 2}O formation was delayed when compared with that of NO. The addition of limestone decreased formation of HCN and increased that of NH{sub 3}, whereas NO formation was least affected. 36 refs., 8 figs., 6 tabs.

  15. Study on CO2 gasification reactivity and physical characteristics of biomass, petroleum coke and coal chars.

    Science.gov (United States)

    Huo, Wei; Zhou, Zhijie; Chen, Xueli; Dai, Zhenghua; Yu, Guangsuo

    2014-05-01

    Gasification reactivities of six different carbonaceous material chars with CO2 were determined by a Thermogravimetric Analyzer (TGA). Gasification reactivities of biomass chars are higher than those of coke and coal chars. In addition, physical structures and chemical components of these chars were systematically tested. It is found that the crystalline structure is an important factor to evaluate gasification reactivities of different chars and the crystalline structures of biomass chars are less order than those of coke and coal chars. Moreover, initial gasification rates of these chars were measured at high temperatures and with relatively large particle sizes. The method of calculating the effectiveness factor η was used to quantify the effect of pore diffusion on gasification. The results show that differences in pore diffusion effects among gasification with various chars are prominent and can be attributed to different intrinsic gasification reactivities and physical characteristics of different chars. PMID:24642484

  16. Reducibility mill scale industrial waste via coke breeze at 850-950ºC

    Directory of Open Access Journals (Sweden)

    Gaballah N.M.

    2015-01-01

    Full Text Available Mill scale is a very attractive industrial waste due to its elevated iron content (about = 69.33% Fe besides being suiTab. for direct recycling to the blast furnace via sintering plant. In this paper the characteristics of raw materials and the briquettes produced from this mill scale were studied by different methods of analyses. The produced briquettes were reduced with different amounts of coke breeze at varying temperatures, and the reduction kinetics was determined. The activation energy of this reaction ≈ 61.5 kJ/mole for reduction of mill scale with coke breeze in the form of briquettes with 2% molasses where the chemical reaction interface model is applicable.

  17. STUDY ON MICROTEXTURE OF COKE PRODUCED FROM CONVERTING LIGNITE BY USING CARBON MONOXIDE AND WATER

    Institute of Scientific and Technical Information of China (English)

    王洁; 郭黔杰

    1992-01-01

    Lignite,generally containing high levels of side chains and oxyfunctional groups,cannot lead to the formation of ordered coke texture. Changes in the properties of the lack of plasticity and fluidity during carbonization using a mixture of carbon monoxide and water conversion process were studied by the microscope photometry,by plotting Rmnx values against Rm,Rmin and bireflectance, as well as quantitative estimation of the optical anisotropy, based on 500 pointcounts. The classification of the carbon forms of this converted lignite is proposed as follows: Isotropic ,Mosaic ,Fibrous ,Flow & Leaf,Mesophase-sphere ,Fusitic ,Inertic ,Pore & fissure. This microtextures of coke were also analysed by using X-ray diffraction. It reveals that the values of diffractional angle,interlayer spacing (002) and the height of the crystallite are in good relationship with the degree of polymerization from the original lignite to its water gas shift reaction products.

  18. Development and Application of High Quality Silica Brick for Coke Ovens

    Institute of Scientific and Technical Information of China (English)

    WANGHongmei; XIAOChangyu

    1998-01-01

    As coke oven becoming larger,silica brick for coke oven is required to be of high uqality,Luoyang Refractories(Grop)Co.Ltd.(LRCO) has re-searched the mineralizer which contains Ca2+,R+,Al3+,F-,emphatically and proposed the principle of composite mineralizer basd on the properties of raw materials used .High performance silia brick which is characterized by low thermal expansion rate,good high temperature properties,residual quartz<0.5%,true density 2.31,and high bulk density silica brick for carbonization room with apparent porosity 13% ,bulk density l.96 g/cm3 have been developed and produced successfully by LR-CO.The quality of the bricks has reached the inter-national advenced level.

  19. Effects of three industrial wastes on kinetic characteristics of petroleum coke-CO{sub 2} gasification

    Energy Technology Data Exchange (ETDEWEB)

    Zou Jian-hui; Zhou Zhi-jie; Dai Zheng-hua; Liu Hai-feng; Wang Fu-chen; Yu Zun-hong [East China University of Science & Technology, Shanghai (China). Institute of Clean Coal Technology

    2008-07-01

    Three industrial wastes including black liquor from papermaking industry, coal slag, and sludge were used as catalysts for petroleum coke-CO{sub 2} gasification. The gasification kinetics characteristics with and without a catalyst were studied using a pressurized thermo gravimetric analyzer (TGA). It is shown that gasification rate increases with increasing conversion and then decreases after reaching a maximal rate for noncatalytic gasification, while decreases in whole course for catalytic gasification. The proposed normal distribution function model describes well the kinetic curve for both noncatalytic and catalytic gasification. The calculated activation energy of noncatalytic petroleum coke-CO{sub 2} gasification is 197.7 kJ/mol, which is in accordance with the reported data. The activities of three catalysts are contributed to the content of metal species. The black liquor in papermaking industry rich in Na species has the best activity, and its gasification rate is six times as that of noncatalytic gasification. 19 refs., 11 figs., 4 tabs.

  20. Comparative investigations of zeolite catalyst deactivation by coking in the conversion of methanol to hydrocarbons

    OpenAIRE

    Evensen, Kjetil Gurholt

    2014-01-01

    With large countries as India and China in tremendous development accompanied by a growing worldwide population, questions arise in how energy demands can be met in the post-oil society. The methanol-to-hydrocarbon process, catalysed by Brønsted acidic zeolites, constitutes an alternative route for the production of gasoline and other valuable hydrocarbons from feedstocks such as natural gas and coal. Catalyst deactivation by coke formation is nevertheless a big concern, and a better understa...

  1. Raw materials inventory management for a Coke plant / by Christoffel van Dijk

    OpenAIRE

    Van Dijk, Christoffel

    2005-01-01

    Analysis of inventory management and logistics for a metallurgical coke plant at Mittal Steel, Vanderbijlpark Works , Gauteng, South Africa. Inventory management and logistics is a concept, which has shown considerable development in the post-World War II era. The concept of applying inventory and logistics as a business function initially emerged during the price wars era and evolved during the quest for quality era. Thereafter, business inventory and logistics had a promotion/marketing focu...

  2. Tried and True: Using Diet Coke and Mentos to Teach Scientific Inquiry

    Science.gov (United States)

    Murray, Tracey Arnold

    2011-01-01

    Adding mint Mentos candy to a two-liter bottle of Diet Coke produces a fountain of soda foam that can reach 3 m high. A demonstration such as this can get a "Wow" out of most audiences, usually followed by a "Do it again!"--but can it be used to teach anything? The answer is a definite "Yes," and what follows is a guided inquiry activity that…

  3. Selection, follow-up, and analysis in the Coke Oven Study.

    Science.gov (United States)

    Rockette, H E; Redmond, C K

    1985-05-01

    The current standard for exposure to coke oven emissions sets a permissible exposure of 150 micrograms benzene-soluble fraction of total particulate matter/m3. The major epidemiologic study that formed the basis for this standard including a review of the evidence of a dose-response relationship between exposure to coal tar pitch volatiles and lung cancer is reviewed. Particular attention was given to the selection of the cohort, follow-up procedures, and the evolution of the analysis.

  4. Dynamics study on effect of temperature to Nitrous nitrification reaction of coking wastewater

    Institute of Scientific and Technical Information of China (English)

    SHAN Ming-jun; ZHANG Hai-ling; LU Yan-li

    2007-01-01

    Dynamic effects of NO2 - - N accumulation were discussed owing to temperature. In different temperature, a series ofvmax and Ks were found considering the relation between the temperature and rate of ammonia nitrogen transforming into NO2 - - N. The kinetics models, which reflected the conditions of ammonia nitrogen transforming into NO2 - - N in the treatment process of the coking wastewater, were built up. The characteristic coefficient temperature was determined according to Arrhenius.

  5. Health survey of former workers in a Norwegian coke plant: Part. 1. Estimation of historical exposures

    OpenAIRE

    Romundstad, P. R.; Ronneberg, A.; Leira, H. L.; Bye, T.

    1998-01-01

    OBJECTIVE: To estimate historical exposure levels at a coke plant for all agents considered to be of importance for epidemiological studies of mortality and cancer incidence. METHODS: Time weighted average exposure (8 h TWA) was estimated based on personal measurements for polycyclic aromatic hydrocarbons (PAHs) and carbonaceous particulates. Exposure to quartz was estimated relative to the concentration of carbonaceous particulates. These estimates were adjusted for the use of airstrea...

  6. Fuel Pyrolysis through Porous Media: Coke Formation and Coupled effect on Permeability

    OpenAIRE

    Fau, Guillaume; Gascoin, Nicolas; Gillard, Philippe; Bouchez, Marc; Steelant, Johan

    2012-01-01

    International audience The development of hypersonic vehicles (up to Mach 10) leads to an important heating of the whole structure. The fuel is thus used as a coolant. It presents an endothermic decomposition with possible coke formation. Its additional permeation through the porous structure involves internal convection. This implies very complex phenomena (heat and mass transfers with chemistry). In this paper, the n-dodecane pyrolysis is studied through stainless steel porous medium up ...

  7. Beyond Thomas Mun: the economic ideas of Edward Coke, Francis Bacon and Lionel Cranfield

    OpenAIRE

    Carlos Eduardo Suprinyak

    2013-01-01

    This paper proposes to approach the economic ideas which prevailed in England during the early 17th century by moving beyond the historical and analytical exegesis of the printed pamphlets of the time, and focusing instead on the intellectual perspectives brought to bear upon economic matters by three of the most prominent public figures of late Jacobean England: Lionel Cranfield, Francis Bacon, and Edward Coke. As civil servants, all three of them were directly involved in the formulation of...

  8. Coke precursor as an intermediate during the alkylation of isobutane/butene over a solid superacid

    Institute of Scientific and Technical Information of China (English)

    XIE; Wenhua; FU; Qiang

    2004-01-01

    Alkylation of isobutane/butene was conducted on a Brφnsted-Lewis conjugated solid superacid. It is found that some hydrocarbons accumulated on the catalyst surface. These hydrocarbons, as called coke precursor, played an intermediate role at the initial stage of the alkylation before they lead the catalyst to lose its activity. The presence of the intermediate is beneficial to the alkylation between isobutane and butene, while increase the TMP content and TMP/DMH ratio in the products.

  9. Solid mineral fuels - coke - determination of moisture in the general analysis test sample

    Energy Technology Data Exchange (ETDEWEB)

    NONE

    2010-07-01

    The determination of moisture in the general analysis test sample is required to correct the results of certain analytical determinations, e.g. volatile matter and hydrogen, for the effect of water in the determination and to allow all determinations to be corrected to a dry basis. This standard specifies a method for the determination of moisture in the general analysis test sample of coke.

  10. [Enhanced bioremediation of coking plant soils contaminated with polycyclic aromatic hydrocarbons].

    Science.gov (United States)

    Lu, Xiao-Xia; Li, Xiu-Li; Ma, Jie; Wu, Shu-Ke; Chen, Chao-Qi; Wu, Wei

    2011-03-01

    Soil samples contaminated with polycyclic aromatic hydrocarbons (PAHs) were collected from Beijing Coking Plant. The purposes were to isolate PAHs degrading bacteria from the soils, determine their appropriate living condition, enrich them and apply them in the enhanced bioremediation of the contaminated soils. Using each of the 16 USEPA priority PAHs as the sole carbon source, PAHs degrading bacteria were isolated using the method of plate streaking and identified by genetic analysis. In total seven species of PAHs degrading bacteria were obtained. When mixed, these bacteria could degrade the 16 (2-6 cyclic) PAHs studied at appropriate concentrations. In the liquid medium, when the total concentration of the 16 PAHs (sigma PAH16) was 17 microg/mL, single bacteria could grow well and degrade the PAHs. However, when sigma PAH16 was 166 microg/mL, the growth and activity of either single PAHs degrading bacteria or a mixture of the seven PAHs degrading bacteria were inhibited. Aiming at the contaminated soils from Beijing coking plant, five treatments were performed, i.e., control (C), addition of nutrient (N), addition of nutrient and PAHs degrading bacteria (N + B), addition of nutrient and surfactant (N +S), addition of nutrient and PAHs degrading bacteria and surfactant (N + B + S). After five weeks of experiment, compared to the C treatment, the mean removal rate of the 16 PAHs in the N + B treatment was increased 32%, and the mean removal rate of the 16 PAHs in the N + B + S treatment was increased 46% (the mean removal rate of the 10 4-6 cyclic PAHs was increased 52%). The addition of PAHs degrading bacteria and surfactant could significantly enhance the degradation of PAHs in the soils. This study provides evidence for the enhanced bioremediation of PAHs contaminated soil for Beijing coking plant and other coking plants.

  11. Determination of reactivity parameters of model carbons, cokes and flame-chars

    DEFF Research Database (Denmark)

    Sørensen, Lasse Holst; Gjernes, Erik; Jessen, Thomas;

    1996-01-01

    Reactivity profiles are defined and measured with thermogravimetry for a dense metallurgical Longyear coke, a polymer-derived porous active carbon, Carboxen 1000, and three flame-chars, Illinois #6, Pittsburgh #8 and New Mexico Blue #1. For each sample it is found that the reactivity profile can ...... reactivity measure is used to rank fuels with very different structural profiles, at varying levels of burnout, temperature and oxygen partial pressure. Keyword: TGA,Reactivity,Coal...

  12. Thermal and hydraulic effects of coke deposit in hydrocarbon pyrolysis process

    OpenAIRE

    Gascoin, Nicolas; Abraham, Grégory; Gillard, Philippe

    2012-01-01

    International audience Fuel pyrolysis can be of benefit for regenerative cooling techniques due to its endothermic effect in ensuring the thermal resistance of hypersonic vehicles and structures. Among pyrolysis species production, there is that of coke formation. A numerical code is used in this paper to investigate the related phenomena, based on two experiments using Titanium (Ti) and Stainless Steel (SS) reactors, which present different pyrolysis rates under similar operating conditio...

  13. Estimation of individual dermal and respiratory uptake of polycyclic aromatic hydrocarbons in 12 coke oven workers.

    OpenAIRE

    VanRooij, J G; Bodelier-Bade, M M; Jongeneelen, F.J.

    1993-01-01

    Twelve workers from a coke plant in The Netherlands participated in an intensive skin monitoring programme combined with personal air sampling and biological monitoring during five consecutive eight hour workshifts. The purpose of the study was to make a quantitative assessment of both the dermal and respiratory intake of polycyclic aromatic hydrocarbons (PAHs). Pyrene was used as a marker compound for both dermal and respiratory exposure to PAHs. The biological measure for the internal expos...

  14. CO2 recycling by means of reforming of coke oven gas for methanol production

    Directory of Open Access Journals (Sweden)

    J. M. Bermúdez

    2013-01-01

    Full Text Available The steelmaking industry is the largest energyconsuming manufacturing sector. As a consequence of this, the CO2 emissions from this sector account for about 5-7 % of the total anthropogenic CO2 emissions. For this reason, increasing efforts are being made to find solutions that might help diminish these emissions and increase energy efficiency. A better management of the coke oven gas (COG surplus is one of the proposed solutions...

  15. Association between urinary 1-hydroxypyrene and genotoxic effects in coke oven workers

    OpenAIRE

    Siwinska, E; Mielzynska, D; Kapka, L

    2004-01-01

    Methods: Blood and urine samples were collected immediately after a shift at the end of a working week from 50 coke oven workers and 50 control workers not exposed to PAHs. Methods included: (1) biomarkers of exposure: urinary 1-hydroxypyrene (HpU), urinary mutagenicity by the plate Salmonella test with strains TA98 and YG1024 after metabolic activation, expressed as mutagenic rate (MR98 and MR1024, respectively), urinary cotinine; and (2) biomarkers of biological effects in peripheral blood ...

  16. CO2 recycling by means of reforming of coke oven gas for methanol production

    OpenAIRE

    J. M. Bermúdez

    2013-01-01

    The steelmaking industry is the largest energyconsuming manufacturing sector. As a consequence of this, the CO2 emissions from this sector account for about 5-7 % of the total anthropogenic CO2 emissions. For this reason, increasing efforts are being made to find solutions that might help diminish these emissions and increase energy efficiency. A better management of the coke oven gas (COG) surplus is one of the proposed solutions...

  17. Biological monitoring of workers exposed to benzene in the coke oven industry.

    OpenAIRE

    Drummond, L; Luck, R; Afacan, A. S.; Wilson, H K

    1988-01-01

    Workers in the coke oven industry are potentially exposed to low concentrations of benzene. There is a need to establish a well validated biological monitoring procedure for low level benzene exposure. The use of breath and blood benzene and urinary phenol has been explored in conjunction with personal monitoring data. At exposures of about 1 ppm benzene, urinary phenol is of no value as an indicator of uptake/exposure. Benzene in blood was measured by head space gas chromatography but the co...

  18. Equilibrium prediction of CO2 reforming of coke oven gas: Suitability for methanol production

    OpenAIRE

    Bermúdez Menéndez, José Miguel; Arenillas de la Puente, Ana; Menéndez Díaz, José Ángel

    2012-01-01

    [EN] A thermodynamic study of the equilibrium of the CO2 reforming of coke oven gas (COG) was carried out with the aid of Aspen Plus® software. The influence of various operation conditions (temperature, pressure, COG composition and CO2/CH4 ratio) upon different parameters (conversions, yields, outlet composition, carbon production, by-products) was studied in order to evaluate the suitability of the process for producing a synthesis gas appropriate for methanol production. It was establishe...

  19. 关于开发薄炉墙焦炉的研讨%Study on development of coke oven with thin oven wall

    Institute of Scientific and Technical Information of China (English)

    叶小虎; 鲁彦; 秦瑾; 周向

    2015-01-01

    This paper studies the influence of thin oven wall of 6m coke oven battery to coke oven proper strength, coking time, coke output and power consumption.For coke oven battery with thin oven wall,after careful calculation and with suitable measures adopted,coke output can be main-tained,and at the same time,gas consumption and environment pollution are reduced.%研究了6m焦炉炉墙减薄对焦炉炉体强度、结焦时间、焦炭产量以及炼焦能耗的影响。经详细计算及采用适当的调节措施,选用薄炉墙焦炉不但能够保持焦炭产量,还可以减少煤气耗量和环境污染等。

  20. Effect of oxygen potential on sulphur dioxide activation of oil sands fluid coke and characteristics of activated coke in mercury adsorption

    Energy Technology Data Exchange (ETDEWEB)

    Morris, E.A.; Jia, C.Q. [Toronto Univ., ON (Canada). Dept. of Chemical Engineering and Applied Chemistry; Tong, S. [Wuhan Univ. of Science and Technology, Wuhan, Hobei (China). Dept. of Chemical Engineering

    2007-07-01

    A sulphur-impregnated activated carbon (SIAC) technology was modified for use in copper smelters in order to mitigate mercury and sulphur dioxide (SO{sub 2}) emissions. Elemental sulphur was captured as a co-product. The study examined the feasibility of reducing levels of SO{sub 2} using fluid coke in the copper smelter flue. SIAC properties were optimized in order to capture vapour phase mercury. Raw fluid coke samples were used to measure SO{sub 2} flow rates. Gas composition was varied to mimic concentrations found during normal operation of copper converters. Gas chromatography was used to analyze reactions products and to prove the hypothesis that mercury capacity is influenced by the oxygen potential of the activation gas due to changes in surface sulphur types developed from reduced sulphur species. Results of the study showed that oxygen levels at 5 per cent did not play a significant role in pore development. It was concluded that increased residence times contributed to reductions in SO{sub 2} and elemental S yields. 13 refs., 1 tab., 7 figs.

  1. 焦炉熄焦车轨道的不停产改造%Coke Oven Coke Quenching Car Track Does not Stop the Transformation

    Institute of Scientific and Technical Information of China (English)

    李峰

    2011-01-01

    Our four coke ovens put into operation one after another since 2006,had since put out car rail because design reason coke,rail base,rail fixed false loose,vibration,had been up and down was restricted by one of the bottleneck of the production,brougt a lot to the production security problems,frequent equipment accidents,maintenance cost was high,the health were difficult to maintain.For not influence production,focal car rail based out reform scheme choosing not to stop production maintenance way,six months time,the orbit transformation,the more obvious effects.%我公司4座焦炉自2006年陆续投产以来,熄焦车轨道因为设计原因,轨道基础松动,轨道固定不实,上下振动,一直是制约生产的一大瓶颈,给生产带来很大的安全隐患,频繁出现设备事故,维修成本高,现场卫生难以保持。为不影响生产,熄焦车轨道基础改造方案选择了不停产检修方式,6个月时间,轨道改造完毕,效果比较明显。

  2. Mercury oxidation and adsorption characteristics of potassium permanganate modified lignite semi-coke

    Institute of Scientific and Technical Information of China (English)

    Huawei Zhang; Jitao Chen; Peng Liang; Li Wang

    2012-01-01

    The adsorption characteristics of virgin and potassium permanganate modified lignite semi-coke (SC) for gaseous Hg0 were investigated in an attempt to produce more effective and lower price adsorbents for the control of elemental mercury emission.Brunauer-Emmett-Teller (BET) measurements,X-ray powder diffraction (XRD) and X-ray photoelectron spectroscopy (XPS) were used to analyze the surface physical and chemical properties of SC,Mn-SC and Mn-H-SC before and after mercury adsorption.The results indicated that potassium permanganate modification had significant influence on the properties of semi-coke,such as the specific surface area,pore structure and surface chemical functional groups.The mercury adsorption efficiency of modified semi-coke was lower than that of SC at low temperature,but much higher at high temperature.Amorphous Mn7+,Mn6+ and Mn4+ on the surface of Mn-SC and Mn-H-SC were the active sites for oxidation and adsorption of gaseous Hg0,which oxidized the elemental mercury into Hg2+ and captured it.Thermal treatment reduced the average oxidation degree of Mnx+ on the surface of Mn-SC from 3.80 to 3.46.However,due to the formation of amorphous MnOx,the surface oxidation active sites for gaseous Hg0 increased,which gave Mn-H-SC higher mercury adsorption efficiency than that of Mn-SC at high temperature.

  3. Health-hazard evaluation report No. HETA-88-377-2120, Armco Coke Oven, Ashland Kentucky

    International Nuclear Information System (INIS)

    In response to a request from the Oil, Chemical and Atomic Workers International Union, a study was made of possible hazardous working conditions at ARMCO Coke Oven (SIC-3312), Ashland, Kentucky. The facility produces about 1,000,000 tons of coke annually. Of the approximately 400 total employees at the coke oven site, 55 work in the by products area. Air quality sampling results indicated overexposure to both benzene (71432) and coal tar pitch volatiles (CTPVs). Airborne levels of benzene ranged as high as 117 parts per million (ppm) with three of 17 samples being above the OSHA limit of 1ppm. Airborne concentrations of CTPVs ranged as high as 0.38mg/cu m with two of six readings being above OSHA limit of 0.2mg/cu m. Several polynuclear aromatic hydrocarbons were also detected. The authors conclude that by products area workers are potentially overexposed to carcinogens, including benzene, CTPVs, and polynuclear aromatic hydrocarbons. An epidemiologic study is considered unlikely to yield meaningful information at this time, due to the small number of workers and the short follow up period. The authors recommend specific measures for reducing potential employee exposures, including an environmental sampling program, a preventive maintenance program, improved housekeeping procedures, and reducing exposure in operators' booths

  4. Modeling and Simulation of Petroleum Coke Calcination in Pot Calciner Using Two-Fluid Model

    Science.gov (United States)

    Xiao, Jin; Huang, Jindi; Zhong, Qifan; Zhang, Hongliang; Li, Jie

    2016-02-01

    The aim of this work was to establish a mathematical model for the analysis of calcining process of petroleum coke in a 24-pot calciner via computational fluid dynamics (CFD) numerical simulation method. The model can be divided into two main parts (1) heterogeneous reacting flow of petroleum coke calcination in the pot was simulated using a two-fluid model approach where the gas and solid phase are treated as a continuous phases; and (2) the standard turbulence equations combined with the finite rate/eddy-dissipation combustion model and discrete ordinates model were solved for the turbulent gas reacting flow in the flue. The model of the calcining process was implemented in ANSYS Fluent 15.0 (commercial CFD software) and validated by industrial production data. After the validation research, the model has been applied to inspect the distribution features of the temperature field in the furnace, the concentration field of residual moisture and volatiles in the petroleum coke, and the vector velocity field of gas and solid phases. This research can provide a theoretical basis for optimizing the structure and improving the automatic control level of a pot calciner.

  5. Effect of paste humidity on kinetics of carbothermal reduction of extruded barite and coke mixture

    Science.gov (United States)

    Salem, A.; Jamshidi, S.

    2012-08-01

    The effect of the moisture content of barite-coke paste on the kinetics of carbothermal reduction was investigated to understand the role of extrusion technique on this type of solid-gas reaction. The pastes were formulated using the typical natural barite and coke powders normally used in the industrial scale. 0.65 wt.% carboxyl methyl cellulose and different amounts of distilled water, ranging 24.3-34.4% were added to the mixed powders. The obtained pastes were then shaped by a laboratory extruder. The extrusion process was assessed by determining the total porosity of dry samples. The samples in the form of disc were isothermally heated at different temperatures in the range of 800-950 °C and the conversion of barite into barium sulfide was measured by the iodometry. The reduction data were analyzed by a modified kinetic model and the frequency factor and activation energy were calculated to evaluate the reduction mechanism. It was found that the moisture content of the paste significantly affects the active site density due to increasing contact surface area between coke and barite particles.

  6. The Effect of Sulfur Concentration in Liquid Iron on Mineral Layer Formation During Coke Dissolution

    Science.gov (United States)

    Chapman, Michael W.; Monaghan, Brian J.; Nightingale, Sharon A.; Mathieson, John G.; Nightingale, Robert J.

    2011-08-01

    The effects of sulfur concentration in liquid iron on mineral layer development between coke and iron as coke dissolves in a 2 mass pct carbon-iron liquid have been investigated at 1773 K (1500 °C). The initial sulfur in iron concentrations used ranged from 0.006 to 0.049 mass pct. Key findings include that the two-stage dissolution behavior exhibited in the carbon transfer from coke to iron, as reported in a previous study by the authors, at low initial sulfur in iron contents, was also apparent at the higher values used in this study. This two-stage behavior was attributed to a change in the mineral layer density as a result of changes in mineral morphology at the interface. In addition to confirming the two-stage behavior of the carbon-transfer kinetics at the higher sulfur concentration in iron levels, after a period of time, a solid calcium sulfide layer formed on the mineral layer. The sulfide layer formed after approximately 40 minutes, and the proportion of sulfide in the mineral layer increased with increased experimental time and initial sulfur concentration in iron. It was usually found at the iron side of the mineral layer and was associated with calcium-enriched calcium aluminates. Thermodynamic analysis of this layer confirmed that the sulfide is stabilized as the mineral layer is enriched by calcium.

  7. Development and Commercial Application of High-Platinum CCR Catalyst with Low Coke Deposition Rate

    Institute of Scientific and Technical Information of China (English)

    Ma Aizeng; Pan Jincheng; Yang Sennian

    2007-01-01

    By means of selecting proper additives and optimizing catalyst composition and preparation procedures,a high-platinum and low coke deposition catalyst PS-Ⅶ for continuous catalytic reforming (CCR)without reducing its specific surface area has been successfully developed.This catalyst PS-Ⅶ was evaluated in a 100-mL pilot test unit.Study results showed that under the same reaction conditions the newly developed catalyst PS-Ⅶ achieved a 26%reduction in coke deposition as compared to the existing high-platinum CCR catalyst.This catalyst upon its first commercial application in a 1.39Mt/a CCR unit had exhibited good anti-attrition performance and good stability in terms of its specific surface area.Compared to the original CCR catalyst this PS-Ⅶ type catalyst could reduce the coke deposition by 27.32%when operating on feedstock with low potential aromatic content,along with apparent increase in C6+liquid yield,hydrogen yield and aromatics yield,which could grapple with the problem associated with the catalyst regeneration constraints after CCR capacity expansion to ensure the longcycle high-load operation of the CCR unit.

  8. Use of shungite rock in place of some coke for ferroalloy smelting

    Energy Technology Data Exchange (ETDEWEB)

    Strakhov, V.M.; Maksimov, Yu.S.

    1986-07-01

    A study is described of the feasibility of using Class III shungite (20-35% carbon content) for ferroalloy production. Heat treatment analysis of samples showed that separation of CO began at 1300 C and reached a maximum at 1550-1650 C. Trial production of 25% ferrosilicon showed that coke carbon could be replaced with shungite carbon, resulting in a charge composition of 20-5 mm coke, 70-25 mm quartzite and 80-20 mm shungite rock. Use of 3% and 6% shungite in charges reduced coke consumption by 10.6-14.8%, quartzite consumption by 3.5-6.9% and electricity consumption by 0.5-2.7%. Overall cost reductions were 5.8% in first period (3% shungite) and 1.8% in second period (6% shungite). It is concluded that production of FS25 and FS18 ferroalloys at ferroalloy plants in the south would require about 29 kt of shungite rock and lead to savings of over 400,000 rubles. 11 references.

  9. The effect of treatment stages on the coking wastewater hazardous compounds and their toxicity.

    Science.gov (United States)

    Wei, Xiao-xue; Zhang, Zi-yang; Fan, Qing-lan; Yuan, Xiao-ying; Guo, Dong-sheng

    2012-11-15

    This study investigated the change of hazardous materials in coking wastewater at different treatment stages (anaerobic, anaerobic/aerobic, anaerobic/aerobic/photo degradation, anaerobic/aerobic/ozone oxidation treatment) and the effects of them on the development of maize embryos and the activity of amylase and protease in maize seeds. Moreover the interaction of refractory organic matters in the wastewater at different treatment stages with amylase and protease also were determined in vitro. The results show that the biodegradable and the refractory organic compounds in the wastewater both can affect maize embryo development (germination inhibition rate is 19.3% for biodegradable organic compounds). As the treatment stage preceding, the inhibition effect of coking wastewater on the development of the maize embryo (for germination inhibition rates change from 49.3% to 24.6%) and on enzymatic activity (inhibition rates change from 63.9% to 22.4% for amylase) decreases gradually, but the photo-degradation treatment to anaerobic/aerobic effluent can increase its toxicity. The changes in the ability of the refractory organic compounds to bind with enzyme proteins, combined with the analysis of the organic components by GC/MS, show that in the process of coking wastewater treatment no new toxic chemicals were produced. PMID:23022415

  10. Ionic Liquid Catalyst Used in Deep Desulfuration of the Coking Benzene for Producing Sulfurless Benzene

    Institute of Scientific and Technical Information of China (English)

    ZHOU Xia-Ping; WANG Yan-Liang; MENG Fan-Wei; FAN Xing-Ming; QIN Song-Bo

    2008-01-01

    For the widening need of benzene used in organic synthesis, ionic liquid catalyst was prepared to study the process of deep desulfuration in the coking benzene. The result shows that the effect of de-thiophene by the ionic liquid catalyst (N-methyl imidazolium hydrogen sulfate [Hmim][HSO4]) is related to its acid function value.Hammett indicator was used to determine the acid function value H0 of the ionic liquid. It can be concluded that while the acid function value is in the range from -4 to -12, the ionic liquid catalyst can make the concentration certain acid quantity and strength, the ionic liquid catalyst helps to form alkyl thiophene through Friedel-Crafts reaction, which differs from the character of benzene and it is absolutely necessary for the separation and refinement of benzene. But overabundant quantity and higher acid value of [Hmim][HSO4] are more suitable for the side copolymerization of benzene, thiophene and alkene, thereby affecting repeated use of the ionic liquid catalyst([Hmim][HSO4]). In our research, thiophene derivant produced by desulfurization in the coking benzene was used as the polymer to provide the passing channel of the charges. The ionic liquid composition in poor performance after repeated use was made to prepare conductive material (resisting to static electricity) as an "electron-receiving" and "electron-giving" doping agent. The result shows that thiophene derivant after desulfuration in the coking benzene can be used to prepare doping conductive materials.

  11. Automation of the works over coke oven; Kokusu ro rojo sagyo no jidoka

    Energy Technology Data Exchange (ETDEWEB)

    Kitayama, Y.; Saji, T. [Sumitomo Metal Industries Ltd., Osaka (Japan)

    1995-06-25

    As a recent trend on the coke manufacture, some requirements for environmental countermeasures and working environment improvements have become stronger. As a countermeasure against such requirements, automation of moving machines is cited. Recently, Kashima Iron works conducted automation of the works over the coke oven. Here is introduced its outline. As its basic concept, it was adopted following items; all coal waggons was renewed with manless operation, all works over coke oven were mechanized and became manless, integrated monitoring and controlling from central control room were conducted, simplification of system was conducted by the co-ownership of information with present automation system, and so forth. As a result, energy saving of the operators was established. As its system construction, in order to use effectively interlocks and information transfers with each moving machine, a construction to cooperate with the present system and to execute automatic remote operation of new equipments was built up. At present, some countermeasures have been examined mainly on improvement of unsufficient items in the program, and its automation ratio is above 99%. 6 figs., 4 tabs.

  12. Biomonitoring of polycyclic aromatic hydrocarbons from coke oven emissions and reproductive toxicity in nonsmoking workers.

    Science.gov (United States)

    Jeng, Hueiwang Anna; Pan, Chih-Hong; Lin, Wen-Yi; Wu, Ming-Tsang; Taylor, Steven; Chang-Chien, Guo-Ping; Zhou, Guodong; Diawara, Norou

    2013-01-15

    The objective of the cross-sectional study was to assess whether exposure to polycyclic aromatic hydrocarbons (PAHs) from coke oven emissions contributed to alteration of semen quality and sperm DNA integrity in nonsmoking workers. Nonsmoking coke oven workers from a steel plant in Taiwan served as the exposure groups (topside-oven workers for the high exposure group and side-oven workers for the low exposure group), and administrators and security personnel in the plant served as the control. An exposure assessment was conducted to determine both particulate and gaseous phase of PAH levels and urinary 1-hydroxypyrene (1-OHP) levels. Semen quality was analyzed according to WHO guidelines. DNA fragmentation and bulky DNA adducts were measured to assess sperm DNA integrity. There was no significant difference in sperm concentrations, vitality, and DNA fragmentation between the exposed group and the control. The high exposure group experienced significantly lower percentages of normal morphology as compared with the control (p=0.0001). Bulky DNA adducts were detected in the exposed group that were significant higher than the control (p=0.04). Exposure to PAHs from coke-oven emissions could contribute to increased levels of bulky DNA adducts in sperm. PMID:23314003

  13. Coupling thermogravimetric and acoustic emission measurements: its application to study the inhibition of catalytic coke deposition

    Energy Technology Data Exchange (ETDEWEB)

    Ropital, Francois; Dascotte, Philippe; Marchand, Pierre [Institut Francais du Petrole, 1 Avenue Bois Preau, 92952 Rueil-Malmaison (France); Faure, Thierry; Lenain, Jean-Claude; Proust, Alain [Euro Physical Acoustics, 27 Rue Magellan, 94373 Sucy-en-Brie Cedex (France)

    2004-07-01

    In order to improve the knowledge on the high temperature behaviour of metallic materials, the coupling of several in situ physical analysis methods is a promising way. For this purpose a thermogravimetric balance has been equipped with a specific acoustic emission device in order to continuously measure the mass variation of the corrosion sample and the acoustic emission transient under experimental conditions of temperature and gas phase compositions that are representative of the industrial environments. The catalytic coke deposition condition that is a major problem for the refinery and petrochemical industries, has been studied with such a device. The carbon deposition on reactor walls can induce localised disruption in the process such as heat-transfer reduction and pressure drops. To prevent these perturbations, proper selections of the metallurgical or internal coating compositions of the equipment, or the injection of accurate amount of inhibitors have to be decided. The feasibility of the coupling at high temperature of thermogravimetric and acoustic emission has been demonstrated. This new technique has been applied to study the inhibition of the catalytic coke deposition on pure iron by sulphur additives in the temperature range of 650 deg. C and under different mixed atmospheres of hydrocarbon and hydrogen contents. Good correlation has been obtained between the coking rates measured by thermogravimetric measurements and the intensities of the acoustic emission parameters. (authors)

  14. Mortality due to respiratory cancers in the coke oven plants of the Lorraine coalmining industry (Houillères du Bassin de Lorraine).

    OpenAIRE

    Bertrand, J P; Chau, N.; Patris, A.; Mur, J M; Pham, Q T; Moulin, J J; Morviller, P; Auburtin, G; Figueredo, A; Martin, J.

    1987-01-01

    The main activity of the Houillères du Bassin de Lorraine (Lorraine Collieries), employing 23,000 operatives and executives, is coalmining. The coke production is carried out by two coke oven plants with a workforce of respectively 747 and 552 workers. The coal coking process entails the emission of noxious products such as polycyclic aromatic hydrocarbons (PAH) from the ovens. The influence of occupational exposure on mortality due to respiratory cancers, and particularly to lung and upper r...

  15. Natureza do coque formado sobre a mordenita durante a transalquilação de benzeno Nature of the coke formed on mordenite during benzene transalkylation

    Directory of Open Access Journals (Sweden)

    Maria do Carmo Rangel

    2003-05-01

    Full Text Available Zeolite catalysts have been extensively used in petroleum refining and the chemical industry although they are deactivated by coke deposition. In order to find the best condition to avoid deactivation, the coke formation on H-mordenite was studied in this work. The coke was produced during benzene transalkylation with C9+ aromatics, under several reaction conditions. It was found that hydrogenated coke was produced in all samples without affecting the selectivity of toluene and xylene formation. This is explained in terms of the mordenite structure and the presence of hydrogen.

  16. Development of phased array and tofd simultaneous inspection system for coke drum

    Energy Technology Data Exchange (ETDEWEB)

    Oka, M. [Sumitomo Heavy Industries, Ltd., Toyo Works, Quality Assurance Dept., Ehime (Japan); Kawashima, K. [S.H.I. Examination and Inspection, Ltd., Inspection and Engineering Dept., Ehime (Japan)

    2004-07-01

    Our current AUT (automatic ultrasonic testing) system is ''phased array linear scan and dual TOFD (time of fight diffraction) simultaneous inspection system'' which has been applied to the pre-service inspection at shop in lieu of radiography as per ASME Code case 2235-4 and the in-service inspection at user's turnaround stage for the circumferential and longitudinal weld joints of shell courses of coke drum. The coke drum is 13-30 feet in diameter and 80-100 feet in height. The base material of coke drum is either C-1/2Mo steel, 1Cr-1/2Mo steel, 1.25Cr-1/2Mo steel, or 2.25Cr-1Mo steel with type 410S or 405 stainless steel cladding material, and clad restoration weld material is either Inconel 82, Inconel 625 or same material as the cladding material (13Cr stainless steel). It is too difficult to detect the flaws in the clad restoration weld by the conventional manual UT and/or TOFD, but phased array can clearly detect them. In order to improve the capability to detect and size the low cycle fatigue crack caused in the clad restoration weld and its heat affected zone due to the cyclic operation of coke drum ''phased array sector scan'' has been adopted. This paper reports the verification test results of ''dual phased array sector scan'' (the simultaneous scanning by a pair of phased array probes placed equally for the centerline of weld joint) in comparison with the verification test results of TOFD, and introduces the characteristic of our current AUT system. In consideration with the verification test results in this paper, we would like to propose that ''dual phased array sector scan and dual TOFD simultaneous inspection system'' (the simultaneous inspection by four (4) kinds of AUT) will be applied to the in-service inspection for the coke drum and other important reactors overlaid inside by stainless steel or inconel at the oil refineries and/or petrochemical plants. (orig.)

  17. Effect of Extracted Compositions of Liquefaction Residue on the Structure and Properties of the Formed-coke

    Directory of Open Access Journals (Sweden)

    Song Yong-hui

    2016-01-01

    Full Text Available The purpose of this paper is to study the effect of extracted compositions of the de-ash liquefaction residue (D-DCLR on pyrolysis products yields, compressive strength and composition of the formed-coke, which was prepared by co-pyrolysis of the low metamorphic pulverized coal and D-DCLR. The scanning electron microscope (SEM and the Fourier Transform Infrared (FT-IR were used to characterize the morphology and functional group of the formed-coke, respectively. The results showed that the extracted compositions of D-DCLR were heavy oil (HS, asphaltene (A, pre-asphaltene (PA and tetrahydrofuran isolusion (THFIS, whose contents were 5.10%, 40.90%, 14.4%, 39.60%, respectively. During the pyrolysis process, HS was the main source of tar, and HS, A as well as PA were conducive to improve gas yields. The THFIS helped to improve the yield of the formed-coke up to 89.5%, corresponding to the compressive strength was only 147.7N/ball for the coke. A and PA were the key factors affecting the compressive strength and surface structure of the formed-coke. The compressive strength of coke could be up to 728.0N/ball with adding D-DCLR, which reduced by 50% after the removal of A and PA. The FT-IR analysis showed that the types of surface functional groups of the formed-coke were remained the same after co-pyrolysis, but the absorption peak intensity of each functional group was changed.

  18. A novel approach to mitigating sulphur dioxide emissions and producing a mercury sorbent material using oil-sands fluid coke

    Energy Technology Data Exchange (ETDEWEB)

    Morris, E.; Jia, C.Q. [Toronto Univ., ON (Canada). Dept. of Chemical Engineering and Applied Chemistry; Tong, S. [Wuhan Univ. of Science and Technology, Wuhan (China). Dept. of Chemical Engineering

    2008-07-01

    Pyrometallurgical smelting operations are a major source of sulphur dioxide (SO{sub 2}) which is a precursor to acid rain and increased levels of UV-B penetration in boreal lakes. Mercury is also released in copper smelter off-gas, which can bioaccumulate and cause neurological disorders and death in humans. Fluid coke is produced in massive quantities as a by-product of bitumen upgrading at Syncrude Canada's facility in Fort McMurray, Alberta. Oilsands fluid coke can be used to reduce SO{sub 2} and produce elemental sulphur as a co-product. This process was dubbed SOactive. The reaction physically activates the fluid coke to produce a sulphur-impregnated activated carbon (SIAC) which is known as ECOcarbon. Some studies have indicated that SIAC is well suited for the removal of vapour phase mercury, mainly due to the formation of stable mercuric sulphide species. This paper discussed the findings made to date in relation to the SOactive process and the characterization of ECOcarbons. The paper discussed the use of fluid coke for reducing SO{sub 2} emissions while producing elemental sulphur as well as coke-SO{sub 2}-oxygen (O{sub 2}) and coke-SO{sub 2}-water (H{sub 2}O) systems. The paper also examined the production of SIAC products for use in capturing vapour phase mercury. The paper presented the materials and methodology, including an illustration of the apparatus used in reduction of SO{sub 2} and activation of fluid coke. It was concluded that more work is still needed to analyse the effect of O{sub 2} and SO{sub 2} reduction and SIAC properties under smelter flue gas conditions. 10 refs., 1 tab., 8 figs.

  19. The Practice of Top-charged Coke Oven Being Modified into Stamp-charged Coke Oven%顶装炼焦改造为捣固炼焦的生产实践

    Institute of Scientific and Technical Information of China (English)

    黄书明

    2012-01-01

    介绍了JN43-80型焦炉由顶装炼焦改为捣固炼焦的改造工程,对比了改造前后炼焦用煤质量指标、配煤煤种和比例、用煤量、焦炭质量指标、化工产品回收率等.顶装炼焦改为捣固炼焦具有减少主焦煤配入量、增加气煤的配入量、提高焦炭产量等优势,通过改造,可使焦化企业降本增效.%The revamping of the model JN43-80 coke oven from the top-charged oven into the stamp-charged one was introduced. The feed coal quality, the number of coal blends, their blending ratio, coal consumption, the quality of the coke produced, the recovery ratio of the chemical products, etc. before and after the revamping were compared, which indicated that such a revamping resulted in a reduction of the main coking coal, an increase of the gas coal blend, and an increase of the coke output. The coking enterprise can thus reduce its production cost and increase its profitability.

  20. Influence of electrolytes (TEABF4 and TEMABF4) on electrochemical performance of graphite oxide derived from needle coke.

    Science.gov (United States)

    Yang, Sunhye; Kim, Ick-Jun; Choi, In-Sik; Bae, Mi-Kyeong; Kim, Hyun-Soo

    2013-05-01

    The structure of needle coke was changed to graphite oxide structure after oxidation treatment with 70 wt.% of nitric acid and sodium chlorate (NaClO3), and the inter-layer distance of the oxidized needle coke was expanded to 6.9 angstroms. The first charge profile of the oxidized needle coke-cell with 1.2 M TEMABF4/acetonitrile solution displayed that the intercalation of electrolyte ions into the inter-layer occurred at 1.0 V, which value is lower than 1.3 V of the oxidized needle coke-cell with 1.2 M TEABF4/acetonitrile solution. After first charge/discharge, the cell using TEMABF4 electrolyte exhibited smaller electrode resistance of 0.05 omega, and larger specific volume capacitance of 25.5 F/ml at the two-electrode system in the potential range 0-2.5 V than those of the cell using TEABF4 electrolyte. Compared to the TEABF4 electrolyte, better electrochemical performance of the TEMABF4 electrolyte in the oxidized needle coke may be caused by the smaller cation (TEMA+) size and better ion mobility in the nanopores between inter-layers. PMID:23858941

  1. Proposal of a novel multifunctional energy system for cogeneration of coke, hydrogen, and power - article no. 052001

    Energy Technology Data Exchange (ETDEWEB)

    Jin, H.G.; Sun, S.; Han, W.; Gao, L. [Chinese Academy of Sciences, Beijing (China)

    2009-09-15

    This paper proposes a novel multifunctional energy system (MES), which cogenerates coke, hydrogen, and power, through the use of coal and coke oven gas (COG). In this system, a new type of coke oven, firing coal instead of COG as heating resource for coking, is adopted. The COG rich in H{sub 2} is sent to a pressure swing adsorption (PSA) unit to separate about 80% of hydrogen first, and then the PSA purge gas is fed to a combined cycle as fuel. The new system combines the chemical processes and power generation system, along with the integration of chemical conversion and thermal energy utilization. In this manner, both the chemical energy of fuel and thermal energy can be used more effectively. With the same inputs of fuel and the same output of coking heat, the new system can produce about 65% more hydrogen than that of individual systems. As a result, the thermal efficiency of the new system is about 70%, and the exergy efficiency is about 66%. Compared with individual systems, the primary energy saving ratio can reach as high as 12.5%. Based on the graphical exergy analyses, we disclose that the integration of synthetic utilization of COG and coal plays a significant role in decreasing the exergy destruction of the MES system. The promising results obtained may lead to a clean coal technology that will utilize COG and coal more efficiently and economically.

  2. Reduction of FeO in EAF steelmaking slag by blends of metallurgical coke and end-of-life tyre

    Energy Technology Data Exchange (ETDEWEB)

    Dankwah, James R.; Koshy, Pramod; Sahajwalla, Veena [Centre for Sustainable Materials Research and Technology, School of Materials Science and Engineering, University of New South Wales, Sydney, NSW (Australia); O' Kane, Paul [OneSteel Sydney Mill, Rooty Hill, NSW (Australia)

    2012-08-15

    The reduction of FeO-containing slag by blends of metallurgical coke and end-of-life tyres (RT) have been investigated through experiments conducted in a laboratory-scale horizontal tube furnace. Composite pellets of EAF slag (47.1% FeO) with coke, RT, and blends of coke/RT (in four different proportions) were rapidly heated at 1550 C under high purity argon gas and the off gas was continuously analyzed for CO and CO{sub 2}using an online infrared (IR) gas analyzer. The extent of reduction after 10 min, level of carburization and desulfurization, and the total amount of CO{sub 2} emissions were determined for each carbonaceous reductant. The results indicate that the extent of reduction, level of carburization and desulfurization of the reduced metal are significantly improved when coke is blended with RT. Blending of coke with RT resulted in a decrease in direct CO{sub 2} emissions from the reduction reactions. (Copyright copyright 2012 WILEY-VCH Verlag GmbH and Co. KGaA, Weinheim)

  3. 7.63 m捣固焦炉配套焦罐车的设计%The Design of 7.63 m Hot Coke Buskets Car for 7.63 Meters of Tamping Coke Oven

    Institute of Scientific and Technical Information of China (English)

    宫文龙; 左强

    2014-01-01

    7.63 meters hot coke buskets car is one of the key dry quenching machine for 7.63 m series of tamping coke oven ,is the first largest domestic tamping tank car ,use the advanced technology such as oven number identification ,automatic registra‐tion ,and successfully built a tamping coke oven with environmental protection machinery and equipment .%7.63 m捣固焦炉配套焦罐车是为7.63 m捣固系列焦炉配套的干熄焦机械之一,是国内首台最大的捣固焦罐车,采用炉号识别、自动对位等先进技术,成功地打造了又一捣固焦炉用的环保型机械设备。

  4. 配型煤炼焦技术的研究与实践%Research and Practice of Coal Blending Coking Technology

    Institute of Scientific and Technical Information of China (English)

    高丽

    2013-01-01

    Coal blending coking technology could improve the adhesion of coal, enhanced coke strength, high quality coal resource saving. Paper analyzed properties of coking coal blending for coking coal mechanism, introduced Nippon Steel iftted with Sumitomo Metal and coal briquette coke making process, as well as various coking plants matched the result through the coke oven experiment and the production practice which the coal coking obtained.%配型煤炼焦技术可以改善煤料的粘结性,增强焦炭强度,节约优质煤资源。文章分析了配型煤炼焦对炼焦煤料性能的影响机理,介绍了新日铁配型煤和住友金属配型煤炼焦工艺,以及各焦化厂通过焦炉实验和生产实践总结的配型煤炼焦的结果。

  5. Using the stable HSPA1A promoter-driven luciferase reporter HepG2 cells to assess the overall toxicity of coke oven emissions

    Institute of Scientific and Technical Information of China (English)

    信丽丽

    2013-01-01

    Objective Using the stable HSPA1A(HSP70-1) promoter-driven luciferase reporter HepG2 cells(HepG2/HSPA1A cells) to assess the overall toxicity of coke oven emissions. Methods The stable HepG2/HSPA1A cells were treated with different concentrations of coke oven

  6. KRESS INDIRECT DRY COOLING SYSTEM, BETHLEHEM STEEL'S COKE PLANT DEMONSTRATION AT SPARROWS POINT, MARYLAND - VOLUME 1. TECHNICAL REPORT AND APPENDICES A-F

    Science.gov (United States)

    The report evaluates the Kress Indirect Dry Cooling (KIDC) process, an innovative system for handling and cooling coke produced from a slot-type by-product coke oven battery. he report is based on the test work and demonstration of the system at Bethlehem Steel Corporation's Spar...

  7. Lung function changes in coke oven workers during 12 years of follow up

    Energy Technology Data Exchange (ETDEWEB)

    Wu, J.; Griffiths, D.; Kreis, I.A.; Darling, C. [University of Wollongong, Wollongong, NSW (Australia). Graduate School of Public Health

    2004-08-01

    The paper investigates the effect of exposure to coke oven emissions on the lung function of coke oven workers. The study population, followed from 1978 and 1990, was 580 male workers with at least two sets of lung function measurements (FVC, FEV1, FEV1/FVC, and FEF25-75%). An annual rate of change (time slope) for age and height adjusted lung function index was estimated for each subject. This 'time slope' was then treated as the response variable in a weighted multiple regression analysis with selected predictors. For all 580 subjects, each year of working in the 'operation' group (the most exposed) was found to increase the FVC decline by around 0.7 ml/year (95% CI 0.1 to 1.3 ml/year). After the exclusion of 111 subjects without detailed work history, the above finding was confirmed and each year of exposure in 'operation'' was also found to increase the FEV1 decline by around 0.8 ml/year (95% CI 0.1 to 1.4 ml/year). These findings are consistent with the results of previous cross-sectional studies. Work duration in the most exposed position in the coke ovens was associated with increased annual decline for FVC and FEV1. The estimated effect of one year of work exposure in 'operation' is equivalent, in terms of the reduction in lung function, to an estimated 2.1 pack-years of smoking for FVC and 1.2 pack-years of smoking for FEV1.

  8. Genetic damage induced by organic extract of coke oven emissions on human bronchial epithelial cells.

    Science.gov (United States)

    Zhai, Qingfeng; Duan, Huawei; Wang, Yadong; Huang, Chuanfeng; Niu, Yong; Dai, Yufei; Bin, Ping; Liu, Qingjun; Chen, Wen; Ma, Junxiang; Zheng, Yuxin

    2012-08-01

    Coke oven emissions are known as human carcinogen, which is a complex mixture of polycyclic aromatic hydrocarbon. In this study, we aimed to clarify the mechanism of action of coke oven emissions induced carcinogenesis and to identify biomarkers of early biological effects in a human bronchial epithelial cell line with CYP1A1 activity (HBE-CYP1A1). Particulate matter was collected in the oven area on glass filter, extracted and analyzed by GC/MS. DNA breaks and oxidative damage were evaluated by alkaline and endonucleases (FPG, hOGG1 and ENDO III)-modified comet assays. Cytotoxicity and chromosomal damage were assessed by the cytokinesis-block micronucleus cytome (CBMN-Cyt) assay. The cells were treated with organic extract of coke oven emissions (OE-COE) representing 5, 10, 20, 40μg/mL extract for 24h. We found that there was a dose-effect relationship between the OE-COE and the direct DNA damage presented by tail length, tail intensity and Olive tail moment in the comet assay. The presence of lesion-specific endonucleases in the assays increased DNA migration after OE-COE treatment when compared to those without enzymes, which indicated that OE-COE produced oxidative damage at the level of pyrimidine and purine bases. The dose-dependent increase of micronuclei, nucleoplasmic bridges and nuclear buds in exposed cells was significant, indicating chromosomal and genomic damage induced by OE-COE. Based on the cytotoxic biomarkers in CBMN-Cyt assay, OE-COE may inhibit nuclear division, interfere with apoptosis, or induce cell necrosis. This study indicates that OE-COE exposure can induce DNA breaks/oxidative damage and genomic instability in HBE-CYP1A1 cells. The FPG-comet assay appears more specific for detecting oxidative DNA damage induced by complex mixtures of genotoxic substances. PMID:22522113

  9. Analysis of coke precursor on catalyst and study on regeneration of catalyst in upgrading of bio-oil

    Energy Technology Data Exchange (ETDEWEB)

    Guo, Xiaoya; Zheng, Yong; Zhang, Baohua; Chen, Jinyang [Department of Chemical Engineering, Shanghai University, Shanghai 201800 (China)

    2009-10-15

    Catalyst HZSM-5 was used in bio-oil catalytic cracking upgrading. The precursor of coke on the catalyst was analyzed by means of TGA, FTIR and C13 NMR. Precursors of coke deposited in the pore of the molecular sieve were mainly aromatic hydrocarbon with the boiling point range from 350 C to 650 C. Those on the outer surface of the pellet precursor were identified as saturated aliphatic hydrocarbons with the boiling point below 200 C. The activity of HZSM-5 was studied after regeneration. In terms of yield of organic distillate and formation rate of coke, results showed that catalytic activity change moderately during the first three times of regeneration. (author)

  10. The adsorption of oil sands naphthenic acids from process-affected tailings water using activated petroleum coke

    Energy Technology Data Exchange (ETDEWEB)

    Small, C.C.; Hashisho, Z.; Ulrich, A.C. [Alberta Univ., Edmonton, AB (Canada). Dept. of Civil and Environmental Engineering

    2010-07-01

    Eighty percent of the organic acids in the Athabasca oil sands region are comprised of naphthenic acids that are toxic to a variety of aquatic life-forms as well as being highly corrosive. This PowerPoint presentation discussed a method of adsorbing naphthenic acids from process-affected water. Activated petroleum coke was studied in order to investigate optimal physical activation conditions for adsorbing oil sands naphthenic acids. Experimental tests were conducted in a centrifuge and analyzed with Fourier transform infrared (FTIR) spectrometry, scanning electron microscopy (SEM) and fluorescence spectrometry. The study demonstrated that delayed and fluid petroleum cokes can be turned into high surface area carbons with increased activation time, temperature, and steam rate. The coke can be used as an adsorbent to remove oil sands naphthenic acids. tabs., figs.

  11. Coke Formation in a Zeolite Crystal During the Methanol-to-Hydrocarbons Reaction as Studied with Atom Probe Tomography.

    Science.gov (United States)

    Schmidt, Joel E; Poplawsky, Jonathan D; Mazumder, Baishakhi; Attila, Özgün; Fu, Donglong; de Winter, D A Matthijs; Meirer, Florian; Bare, Simon R; Weckhuysen, Bert M

    2016-09-01

    Understanding the formation of carbon deposits in zeolites is vital to developing new, superior materials for various applications, including oil and gas conversion processes. Herein, atom probe tomography (APT) has been used to spatially resolve the 3D compositional changes at the sub-nm length scale in a single zeolite ZSM-5 crystal, which has been partially deactivated by the methanol-to-hydrocarbons reaction using (13) C-labeled methanol. The results reveal the formation of coke in agglomerates that span length scales from tens of nanometers to atomic clusters with a median size of 30-60 (13) C atoms. These clusters correlate with local increases in Brønsted acid site density, demonstrating that the formation of the first deactivating coke precursor molecules occurs in nanoscopic regions enriched in aluminum. This nanoscale correlation underscores the importance of carefully engineering materials to suppress detrimental coke formation.

  12. Coke Formation in a Zeolite Crystal During the Methanol-to-Hydrocarbons Reaction as Studied with Atom Probe Tomography.

    Science.gov (United States)

    Schmidt, Joel E; Poplawsky, Jonathan D; Mazumder, Baishakhi; Attila, Özgün; Fu, Donglong; de Winter, D A Matthijs; Meirer, Florian; Bare, Simon R; Weckhuysen, Bert M

    2016-09-01

    Understanding the formation of carbon deposits in zeolites is vital to developing new, superior materials for various applications, including oil and gas conversion processes. Herein, atom probe tomography (APT) has been used to spatially resolve the 3D compositional changes at the sub-nm length scale in a single zeolite ZSM-5 crystal, which has been partially deactivated by the methanol-to-hydrocarbons reaction using (13) C-labeled methanol. The results reveal the formation of coke in agglomerates that span length scales from tens of nanometers to atomic clusters with a median size of 30-60 (13) C atoms. These clusters correlate with local increases in Brønsted acid site density, demonstrating that the formation of the first deactivating coke precursor molecules occurs in nanoscopic regions enriched in aluminum. This nanoscale correlation underscores the importance of carefully engineering materials to suppress detrimental coke formation. PMID:27485276

  13. Partial briquetting of coal charges as a means of utilizing lower-grade coal for coke making

    Energy Technology Data Exchange (ETDEWEB)

    Pieters, B.J. (Iscor Limited, Newcastle (South Africa))

    1991-08-01

    The paper describes the difficulties experienced with inferior coking coals as Iscor began using larger blast furnaces for the production of liquid iron. Research conducted at Iscor from 1977 to 1979 showed that benefits could be gained from the use of partially briquetted charges, and it was decided to install briquetting plants at the Vanderbijlpark and Newcastle Works. Details are given of the latter plant, which was supplied by a consortium consisting of Voest Alpine, Didier Engineering, and Sumitomo Metal Industries. Sumitomo also supplied information on the optimization of coke quality along the lines of their Sumicoal System. The results have been a marked improvement in coke quality, much better blast-furnace operation, and increased productivity. 11 figs., 3 tabs.

  14. Organic extracts of coke oven emissions can induce genetic damage in metabolically competent HepG2 cells.

    Science.gov (United States)

    Xin, Lili; Wang, Jianshu; Guo, Sifan; Wu, Yanhu; Li, Xiaohai; Deng, Huaxin; Kuang, Dan; Xiao, Wei; Wu, Tangchun; Guo, Huan

    2014-05-01

    Coke oven emissions (COEs) containing various carcinogenic polycyclic aromatic hydrocarbons (PAHs) represent the coal-burning pollution in the air. Organic pollutants in the aerosol and particulate matter of COEs were collected from the bottom, side, and top of a coke oven. The Comet assay and cytokinesis-block micronucleus cytome assay were conducted to analyze the genetic damage of extractable organic matter (EOM) of COEs on HepG2 cells. All the three EOMs could induce significant dose-dependent increases in Olive tail moment, tail DNA, and tail length, micronuclei, nucleoplasmic bridges, and nuclear buds frequencies, which were mostly positively correlated with the total PAHs concentration in each EOM. In conclusion, EOMs of COEs in the three typical working places of coke oven can induce DNA strand breaks and genomic instability in the metabolically competent HepG2 cells. The PAHs in EOMs may be important causative agents for the genotoxic effects of COEs. PMID:24709322

  15. Health-hazard evaluation report HETA 85-441-1765, New Boston Coke Corporation, New Boston, Ohio

    Energy Technology Data Exchange (ETDEWEB)

    O' Malley, M.A.

    1986-12-01

    In response to a request from the Industrial Commission of Ohio, worker complaints of skin disease at the New Boston Coke Corporation, New Boston, Ohio were investigated. The request was based on seven reports of dermatitis thought to be associated with steam exposure during coke quenching. Quench water had a pH of 8.85 and contained phenol, ammonia, calcium-oxide, and suspended particulates (82% organic compounds); no irritant threshold levels were found for these compounds. Skin tests in rabbits showed a minimal irritant capacity for quench water. Medical records did not reveal the origin of dermatitis. Active skin lesions were characterized as nummular eczema or atopic dermatitis, which were not thought to be of occupational origin. The author concludes that coke-quenching steam does not pose a skin hazard, but certain work activities may aggravate existing skin conditions. Recommendations include elimination of abrasive cleansing agents, use of skin moisturizers after washing, and prompt medical evaluation of skin complaints.

  16. Matrix endor studies of the carbonization of West Canadian coking coals

    Science.gov (United States)

    West, P. R.; Cannon, S. E.

    1981-02-01

    Cretaceous bituminous coals of known rank R¯0 max, vitrinite reflectance) have been examined by ESR (electron spin resonance) and ENDOR (electron nuclear double resonance) techniques. Both highly oxidised (outcrop) and unoxidised mine-run Balmer coal from the Crowsnest field have been subjected to heat treatment (200-900°C), and the matrix proton ENDOR signal studied as a function of applied microwave and rf power. Changes in ENDOR line shape and intensity are described with particular emphasis on the presoftening region of the unoxidised coal. A comparative study of the carbonization of hvb and 1vb coking coal from the Crowsnest is reported.

  17. Increasing Liquid Yield and Diesel Fraction in Delayed Coking Process: Mechanism of Liquid Formation

    Institute of Scientific and Technical Information of China (English)

    Mominou Nchare; Shen Benxian; Xu Jiaoliang

    2007-01-01

    The thermal upgrading of two residual oils with different characteristics was studied in a laboratory-scale continuous delayed coking unit.The goal was to investigate the influence of the process variables such as temperature,reaction time and additive on liquid yield and products distribution.A maximum liquid yield of 73% was achieved compared to 69% with the commercial unit.This yield was even increased to 75% under the effect of an additive.The fractionation of liquid oil by simulated vacuum distillation showed a high yield of diesel(46.9%).compared to 28% for the commercial unit.

  18. Lignite coke moving bed adsorber for cement plants - BAT or beyond BAT?

    Energy Technology Data Exchange (ETDEWEB)

    Schoenberger, H. [European Commission, Seville (Spain). Joint Research Center

    2011-06-15

    The IPPC Directive requires permits which must contain emission limit values and other conditions based on BAT. The BAT are characterised and the terms 'conditional BAT' and 'beyond BAT' are defined and explained. The borderline between BAT and beyond BAT is explained by means of an outstanding example which is the lignite coke moving bed adsorber for the abatement of the waste gas from a cement plant where waste for co-incineration is fed to a considerable extent is described in detail. Worldwide, this technique has been successfully applied at one cement plant for sixteen years.

  19. Toxicity of coke wastewater treated with advanced oxidation by Fenton process supported by ultrasonic field

    OpenAIRE

    Kwarciak-Kozłowska Anna; Krzywicka Aleksandra

    2016-01-01

    The aim of the presented study was to determine the toxicity of wastewater from the production of coke. The wastewater was treated with advanced oxidation involving ultrasonic field with Fenton’s reagent (the amplitude was 61.5 μm and sonication time 8 min). Two doses of iron and four doses of hydrogen peroxide were used. The amount of hydrogen peroxide was proportional to the value of the chemical oxygen demand of raw wastewater, ranging from COD/H2O2 ratio of 1:2.5 to 1:20. Two tests were u...

  20. Petroleum Coke in the Urban Environment: A Review of Potential Health Effects

    OpenAIRE

    Caruso, Joseph A; Kezhong Zhang; Schroeck, Nicholas J.; Benjamin McCoy; McElmurry, Shawn P.

    2015-01-01

    Petroleum coke, or petcoke, is a granular coal-like industrial by-product that is separated during the refinement of heavy crude oil. Recently, the processing of material from Canadian oil sands in U.S. refineries has led to the appearance of large petcoke piles adjacent to urban communities in Detroit and Chicago. The purpose of this literature review is to assess what is known about the effects of petcoke exposure on human health. Toxicological studies in animals indicate that dermal or inh...

  1. Dry reforming of coke oven gases over activated carbon to produce syngas for methanol synthesis

    OpenAIRE

    Bermúdez Menéndez, José Miguel; Fidalgo Fernández, Beatriz; Arenillas de la Puente, Ana; Menéndez Díaz, José Ángel

    2010-01-01

    [EN] The dry reforming of coke oven gases (COG) over an activated carbon used as catalyst has been studied in order to produce a syngas suitable for methanol synthesis. The primary aim of this work was to study the influence of the high amount of hydrogen present in the COG on the process of dry reforming, as well as the influence of other operation conditions, such us temperature and volumetric hourly space velocity (VHSV). It was found that the reverse water gas shift (RWGS) reaction takes ...

  2. Coke deterioration mechanism in lump zone of blast furnace%高炉块状带焦炭劣化机理

    Institute of Scientific and Technical Information of China (English)

    吕青青; 杜屏; 周俊兰

    2016-01-01

    The condition of gas flow condition and temperature condition in lump zone of blast furnace is simulated. The impacts of particle size,coke quenching way and coke types affecting coke deterioration in lump zone of blast furnace were studied. In addition,the catalyze mechanism of K2CO3 and Na2CO3 catalyzing CO2 and coke reaction were also stud-ied. The results show that:small size coke and wet quenching coke have higher loss mass and generate more powder than large size coke and dry quenching coke;Stamping coke deterioration degree is less than top charging coke in the initial re-action,as reacting time increases,stamping coke deterioration increases obviously and is higher than that of the top charg-ing coke;Alkali metal and coke ash formed in a kind of catalyst complex. The complex causes that the initial reaction tem-perature decrease,and destroys the crystal structure,causing loss mass increased and coke getting powdery heavily;The catalytic effect of K2CO3 is higher than Na2CO3.%模拟高炉块状带气流和温度条件,研究了粒度、熄焦方式和焦炭类型对焦炭劣化影响,以及高炉上部碱金属K2CO3和Na2CO3催化焦炭与CO2的反应机理.结果表明:小粒度焦炭和湿熄焦炭失碳率较高,产生的粉末量多;捣固焦炭在反应开始时劣化程度低于顶装焦炭,随着反应时间增加,劣化程度高于顶装焦炭;碱金属会与焦炭中的灰分形成催化复合物,导致焦炭与CO2反应的起始温度降低,破坏焦炭的微晶结构,失碳率增加,粉化加重;K2CO3的催化作用高于Na2CO3的催化作用.

  3. Study and modelling of deactivation by coke in catalytic reforming of hydrocarbons on Pt-Sn/Al{sub 2}O{sub 3} catalyst; La microbalance inertielle: etude et modelisation cinetique de la desactivation par le coke en reformage catalytique des hydrocarbures sur catalyseur Pt-Sn/Al{sub 2}O{sub 3}

    Energy Technology Data Exchange (ETDEWEB)

    Mathieu-Deghais, S.

    2004-07-01

    Catalytic reforming is the refining process that produces gasoline with a high octane number. During a reforming operation, undesired side reactions promote the formation of carbon deposits (coke) on the surface of the catalyst. As the reactions proceed, the coke accumulation leads to a progressive decrease of the catalyst activity and to a change in its selectivity. Getting this phenomenon under control is interesting to optimize the industrial plants. This work aims to improve the comprehension and the modeling of coke formation and its deactivating effect on reforming reactions, while working under conditions chosen within a range as close as possible to the industrial conditions of the regenerative process. The experimental study is carried out with a micro unit that is designed to observe simultaneously the coke formation and its influence on the catalyst activity. A vibrational microbalance reactor (TEOM - Tapered Element Oscillating Microbalance) is used to provide continuous monitoring of coke. On-line gas chromatography is used to observe the catalyst activity and selectivity as a function of the coke content. The coking experiments are performed on a fresh Pt-Sn/alumina catalyst, with mixtures of hydrocarbon molecules of 7 carbon atoms as hydrocarbon feeds. The coking tests permitted to highlight the operating parameters that may affect the amount of coke, and to identify the hydrocarbon molecules that behave as coke intermediate. A kinetic model for coke formation could be developed through the compilation of these results. The catalytic activity analysis permitted to point out the coke effect on both of the active phases of the catalyst, to construct a simplified reforming kinetic model that simulates the catalyst activity under the reforming conditions, and to quantify deactivation via deactivation functions. (author)

  4. Significant Positive Correlation of Plasma BPDE-Albumin Adducts to Urinary 1-Hydroxypyrene in Coke Oven Workers

    Institute of Scientific and Technical Information of China (English)

    HONG WANG; TANG-CHUN WU; XIAO-BO YANG; AI-LIN LIU; HONG-YAN ZHEN; LIANG GUO; HUA-SHAN LIANG; YONG-YI BI; YUN BAI; YONG-WEN CHEN

    2007-01-01

    Objective To investigate the application of BPDE-albumin adducts as monitoring biomarkers for coke oven workers exposed to polycyclic aromatic hydrocarbons(PAHs)and to explore possible relationship between BPDE-albumin adducts and urinary 1-hydroxypyrene (1-OHP)levels in them.Methods Thirty-seven coke oven workers from a coke plant and 47 controls without the occupational exposure to PAHs were recruited in this study.The levels of plasma BPDE-albumin adducts and urinary 1-OHP were analyzed using high performance liquid chromatography.Results The median levels of BPDE-albumin adducts(42.10 fmol/mg albumin)and urinary 1-OHP(5.46 μmol/mol creatinine)were significantly higher in coke oven workers than in controls(14.16 fmol/mg albumin,2.96 μmol/mol creatinine,respectively;P<0.01).Multiple logistic regression analysis showed that coke oven workers were at higher risk of having BPDE-albumin adduct levels above 25.30 prnol/mg albumin(OR=1.79,P<0.01)and urinary 1-OHP levels above 4.13 μmol/mol creatinine(OR=2.45,P<0.05).There was a positive correlation between the levels of BPDE-albumin adducts and urinary 1-OHP in all subjects(rs=0.349,P<0.01).Conclusion BPDE-albumin adduct is a useful biomarker for monitoring long-term exposure to PAHs,and plasma BPDE-albumin adducts level is significantly correlated to urinary 1-OHP levels in coke oven workers.

  5. Partial Replacement of the 6 m Coke oven Column%6米焦炉焦侧炉柱局部更换实践

    Institute of Scientific and Technical Information of China (English)

    郭涛

    2015-01-01

    结合山钢股份莱芜分公司焦化厂5#、6#焦炉104#焦侧炉柱变形情况的测量分析,介绍了6米焦炉焦侧炉柱局部更换过程,为类似作业提供经验。%According to the measurement analysis of deformation of the coke column of NO .104 coking chamber of NO .5/NO.6 coke oven in coking plant of Shandong Iron and Steel Ltd .Laiwu Branch, we introduce how to replace the part of the 6m coke oven’s column.This thesis provides valuable experience for the future similar works .

  6. DTA and TGA study of MeSo4 (Me = Fe, Co, Ni dissociation in the presence of coke

    Directory of Open Access Journals (Sweden)

    Boyanov B.S.

    2002-01-01

    Full Text Available MeSO4 (Me = Fe, Co, Ni dissociation is investigated in order to estimate the effect of temperature, time and presence of coke as reducer on the degree and mechanism of dissociation. It is proved that the presence of coke decreases the dissociation temperature considerably and increases the degree of MeSO4 dissociation. Based on the obtained experimental data, a mechanism of the processes is proposed. The obtained results can be used in the industrial production of non-ferrous metals for explaining the processes that take place in the reduction of zinc and lead cakes in order to achieve favorable environmental, technical and economic results.

  7. Effects of operating conditions on compositional characteristics and reaction kinetics of liquid derived by delayed coking of nigerian petroleum residue

    OpenAIRE

    Bello, O. O.; B. T. Ademodi; Macaulay, S. R. A.; G. K. Latinwo

    2006-01-01

    The thermal upgrading of Nigerian petroleum residue was studied at relatively low pressure in a delayed coking reactor system. In this work, the intent was to investigate the effects of process variables such as reaction temperature (200(0)C to 600(0)C), reaction time (0 to 120min), additive concentration loading and additive-to-residue ratio on the amounts and quality of organic liquid product (OLP). The liquid products derived from the delayed coking process were characterized by means of i...

  8. Reducibility study of Rossetta ilmenite ore briquettes and powder with coke breeze at 800-1100°C

    Directory of Open Access Journals (Sweden)

    Abd el Gawad Hala H.

    2013-01-01

    Full Text Available Ilmenite ore fine and coke breeze as reduced material were briquetted with different amounts of organic materials such as molasses or pitch were studied in this investigation. The produced briquettes at reasonable condition were reduced in nitrogen atmosphere at temperature range 800 - 1100oC to determine the factors controlling the reduction and to determine the controlling mechanism. Also ilmenite ore fine with coke breeze were reduced at the same temperature range in nitrogen atmosphere without briquetting process, for the sake of comparison.

  9. Performance and microbial community analysis of the anaerobic reactor with coke oven gas biomethanation and in situ biogas upgrading

    DEFF Research Database (Denmark)

    Wang, Wen; Xie, Li; Luo, Gang;

    2013-01-01

    (HFM). With pH control at 8.0, the added H2 and CO were fully consumed and no negative effects on the anaerobic degradation of sewage sludge were observed. The maximum CH4 content in the biogas was 99%. The addition of SCOG resulted in enrichment and dominance of homoacetogenetic genus Treponema......A new method for simultaneous coke oven gas (COG) biomethanation and in situ biogas upgrading in anaerobic reactor was developed in this study. The simulated coke oven gas (SCOG) (92% H2 and 8% CO) was injected directly into the anaerobic reactor treating sewage sludge through hollow fiber membrane...

  10. Research Progress of Coking Waste Water Treatment%焦化废水处理研究进展

    Institute of Scientific and Technical Information of China (English)

    付禹华; 王兵; 何昌应; 孔德顺

    2016-01-01

    综述了焦化废水处理的几种常用方法,就每种方法的优缺点进行了分析,并对焦化废水处理的研究方向进行了展望。%The paper reviewed several commonly used methods of coking waste water treatment,the advantages and disadvantages of each method were analyzed,and the research direction of coking waste water treatment was discussed.

  11. Refrigeration cycle for cryogenic separation of hydrogen from coke oven gas

    Institute of Scientific and Technical Information of China (English)

    Kun CHANG; Qing LI; Qiang LI

    2008-01-01

    Ten billion cubic meters of hydrogen are dissip-ated to the environment along with the emission of coke-oven gas every year in China. A novel cryogenic separation of hydrogen from coke oven gas is proposed to separate the hydrogen and liquefy it simultaneously, and the cooling capacity is supplied by two refrigeration cycles. The perform-ance of the ideal vapor refrigeration cycle is analyzed with methane and nitrogen as refrigerant respectively. The results show that the coefficient of performance (COP) of methane refrigeration cycle is 2.7 times that of nitrogen refrigeration cycle, and the figure of merit (FOM) of methane refrigera-tion cycle is 1.6 times that of nitrogen refrigeration cycle. The performance of ideal gas refrigeration cycle is also analyzed with neon, hydrogen and helium as refrigerant respectively. The results show that both the coefficient of performance and figure of merit of neon refrigeration cycle is the highest. It is thermodynamically possible to arrange the refrigeration cycle with methane and neon as refrigerant, respectively.

  12. Kinetics of petroleum coke/biomass blends during co-gasification

    Science.gov (United States)

    Zhang, Jian-liang; Guo, Jian; Wang, Guang-wei; Xu, Tao; Chai, Yi-fan; Zheng, Chang-le; Xu, Run-sheng

    2016-09-01

    The co-gasification behavior and synergistic effect of petroleum coke, biomass, and their blends were studied by thermogravimetric analysis under CO2 atmosphere at different heating rates. The isoconversional method was used to calculate the activation energy. The results showed that the gasification process occurred in two stages: pyrolysis and char gasification. A synergistic effect was observed in the char gasification stage. This effect was caused by alkali and alkaline earth metals in the biomass ash. Kinetics analysis showed that the activation energy in the pyrolysis stage was less than that in the char gasification stage. In the char gasification stage, the activation energy was 129.1-177.8 kJ/mol for petroleum coke, whereas it was 120.3-150.5 kJ/mol for biomass. We also observed that the activation energy calculated by the Flynn-Wall-Ozawa (FWO) method were larger than those calculated by the Kissinger-Akahira-Sunosen (KAS) method. When the conversion was 1.0, the activation energy was 106.2 kJ/mol when calculated by the KAS method, whereas it was 120.3 kJ/mol when calculated by the FWO method.

  13. Fly ashes from coal and petroleum coke combustion: current and innovative potential applications.

    Science.gov (United States)

    González, Aixa; Navia, Rodrigo; Moreno, Natalia

    2009-12-01

    Coal fly ashes (CFA) are generated in large amounts worldwide. Current combustion technologies allow the burning of fuels with high sulfur content such as petroleum coke, generating non-CFA, such as petroleum coke fly ash (PCFA), mainly from fluidized bed combustion processes. The disposal of CFA and PCFA fly ashes can have severe impacts in the environment such as a potential groundwater contamination by the leaching of heavy metals and/or particulate matter emissions; making it necessary to treat or reuse them. At present CFA are utilized in several applications fields such as cement and concrete production, agriculture and soil stabilization. However, their reuse is restricted by the quality parameters of the end-product or requirements defined by the production process. Therefore, secondary material markets can use a limited amount of CFA, which implies the necessity of new markets for the unused CFA. Some potential future utilization options reviewed herein are zeolite synthesis and valuable metals extraction. In comparison to CFA, PCFA are characterized by a high Ca content, suggesting a possible use as neutralizers of acid wastewaters from mining operations, opening a new potential application area for PCFA that could solve contamination problems in emergent and mining countries such as Chile. However, this potential application may be limited by PCFA heavy metals leaching, mainly V and Ni, which are present in PCFA in high concentrations.

  14. Influence of mass transfer on thermogravimetric analysis of combustion and gasification reactivity of coke

    Energy Technology Data Exchange (ETDEWEB)

    Andreas Jess; Ann-Kathrin Andresen [Universitaet Bayreuth, Bayreuth (Germany). Department of Chemical Engineering

    2010-07-15

    Non-isothermal TG/DTG measurements are widely used to determine kinetic parameters of oxidation and gasification of carbons, e.g. by multi-heating rate methods. Thereby it is important to avoid spurious effects due to diffusion limitations. In this work, TG/DTG experiments with activated carbon were conducted under isothermal and non-isothermal conditions. The agreement of the experimental results with results of simulations based on the intrinsic kinetics, pore diffusion and external diffusion in/to the sample (crucible) is very good. The simulations show that mass transfer has an unwanted influence on TG measurements, if the concentration of the gaseous reactant (O{sub 2} and CO{sub 2}) is too low and/or the heating rate is too high. Based on literature data, the simulation was extended to blast furnace coke with a very low reactivity and to highly reactive coke from pyrolysis of miscanthus sinensis. The simulations and theoretical considerations lead to a criterion to exclude the influence of mass transfer on TG measurements a priori. This criterion is valid for combustion as well as for gasification with steam or carbon dioxide. 26 refs., 11 figs., 1 tab.

  15. The assessment of the coke wastewater treatment efficacy in rotating biological contractor.

    Science.gov (United States)

    Cema, G; Żabczyński, S; Ziembińska-Buczyńska, A

    2016-01-01

    Coke wastewater is known to be relatively difficult for biological treatment. Nonetheless, biofilm-based systems seem to be promising tool for such treatment. That is why a rotating biological contactor (RBC) system focused on the Anammox process was used in this study. The experiment was divided into two parts with synthetic and then real wastewater. It was proven that it is possible to treat coke wastewater with RBC but such a procedure requires a very long start-up period for the nitritation (190 days), as well as for the Anammox process, where stable nitrogen removal over 70% was achieved after 400 days of experiment. Interestingly, it was possible at a relatively low (20.2 ± 2.2 °C) temperature. The polymerase chain reaction-denaturing gradient gel electrophoresis (PCR-DGGE) based monitoring of the bacterial community showed that its biodiversity decreased when the real wastewater was treated and it was composed mainly of GC-rich genotypes, probably because of the modeling influence of this wastewater and the genotypes specialization. PMID:26942544

  16. Fly ashes from coal and petroleum coke combustion: current and innovative potential applications

    Energy Technology Data Exchange (ETDEWEB)

    Gonzalez, A.; Navia, R.; Moreno, N. [University La Frontera, Temuco (Chile). Dept. of Chemical Engineering

    2009-12-15

    Coal fly ashes (CFA) are generated in large amounts worldwide. Current combustion technologies allow the burning of fuels with high sulfur content such as petroleum coke, generating non-CFA, such as petroleum coke fly ash (PCFA), mainly from fluidized bed combustion processes. The disposal of CFA and PCFA fly ashes can have severe impacts in the environment such as a potential groundwater contamination by the leaching of heavy metals and/or particulate matter emissions; making it necessary to treat or reuse them. At present CFA are utilized in several applications fields such as cement and concrete production, agriculture and soil stabilization. However, their reuse is restricted by the quality parameters of the end-product or requirements defined by the production process. Therefore, secondary material markets can use a limited amount of CFA, which implies the necessity of new markets for the unused CFA. Some potential future utilization options reviewed herein are zeolite synthesis and valuable metals extraction. In comparison to CFA, PCFA are characterized by a high Ca content, suggesting a possible use as neutralizers of acid wastewaters from mining operations, opening a new potential application area for PCFA that could solve contamination problems in emergent and mining countries such as Chile. However, this potential application may be limited by PCFA heavy metals leaching, mainly V and Ni, which are present in PCFA in high concentrations.

  17. Shift From Coke to Coal Using Direct Reduction Method and Challenges

    Institute of Scientific and Technical Information of China (English)

    Okonkwo Paul Chukwuleke; CAI Jiu-ju; Sam Chukwujekwu; XIAO Song

    2009-01-01

    Ironmaking involves the separation of iron ores. It not only represents the first step in steelmaking but also is the most capital-intensive and energy-intensive process in the production of steel. The main route for producing iron for steelmaking is to use the blast furnace, which uses metallurgical coke as the reduetant. Concerns over the limited re-sources, the high cost of eoking coals, and the environmental impacts of eoking and sinter plants have driven steel-makers to develop alternative ironmaking processes that can use non-coking coals to reduce iron ores directly. Since the efficiency and productivity of modern large capacity blast furnaces will be difficult to surpass, blast furnaces will continue to retain their predominant position as the foremost ironmaking process for some time to come. The alterna-tive ironmaking processes are therefore expected to play an increasingly significant role in the iron and steel industry, especially in meeting the needs of small-sized local and regional markets. It is likely that the importance of direct re-duced iron (DRI) and hot metal as sources of virgin iron will continue to increase, especially in the developing coun-tries where steelmaking is, and will be, primarily based on electric arc furnace (EAF) minimills. Consequently, the challenges that are faced by the new technology have to be embraced.

  18. Effect of reflux ratio on COD and nitrogen removals from coke plant wastewaters.

    Science.gov (United States)

    Shi, X L; Hu, X B; Wang, Z; Ding, L L; Ren, H Q

    2010-01-01

    A laboratory-scale anaerobic-anoxic-aerobic-moving bed biofilm reactor (A1-A2-O-MBBR) system was undertaken to treat coke plant wastewaters from two different factories (wastewater A and B). Wastewater B had higher BOD5/COD ratio and COD/TN ratio than wastewater A. The effects of reflux ratios on COD, TN and NH3-N removals were studied. Results indicated that, with the reflux ratio increased from 2 to 5, COD removals of wastewater A and wastewater B increased from 57.4% to 72.6% and 78.2% to 88.6%, respectively. Meanwhile, TN removals were also increased accompanying reflux ratio rise, from 53.1% to 74.4% for wastewater A and 64.2% to 83.5% for wastewater B. At the same reflux ratio, compared with wastewater A, higher COD and TN removal efficiencies were observed in wastewater B, which had higher BOD5/COD and COD/TN ratio. Reflux ratio had no significant influence on NH3-N removal; 99.0% of the overall NH3-N removal efficiency was achieved by the system for both coke plant wastewaters at any tested reflux ratio. MBBR was effective in NH3-N removal, and about 95% of the NH3-N was removed in the MBBR. PMID:20555197

  19. Petroleum Coke in the Urban Environment: A Review of Potential Health Effects

    Directory of Open Access Journals (Sweden)

    Joseph A. Caruso

    2015-05-01

    Full Text Available Petroleum coke, or petcoke, is a granular coal-like industrial by-product that is separated during the refinement of heavy crude oil. Recently, the processing of material from Canadian oil sands in U.S. refineries has led to the appearance of large petcoke piles adjacent to urban communities in Detroit and Chicago. The purpose of this literature review is to assess what is known about the effects of petcoke exposure on human health. Toxicological studies in animals indicate that dermal or inhalation petcoke exposure does not lead to a significant risk for cancer development or reproductive and developmental effects. However, pulmonary inflammation was observed in long-term inhalation exposure studies. Epidemiological studies in coke oven workers have shown increased risk for cancer and chronic obstructive pulmonary diseases, but these studies are confounded by multiple industrial exposures, most notably to polycyclic aromatic hydrocarbons that are generated during petcoke production. The main threat to urban populations in the vicinity of petcoke piles is most likely fugitive dust emissions in the form of fine particulate matter. More research is required to determine whether petcoke fine particulate matter causes or exacerbates disease, either alone or in conjunction with other environmental contaminants.

  20. Treatment of coke plant wastewater by SND fixed biofilm hybrid system

    Institute of Scientific and Technical Information of China (English)

    QI Rong; YANG Kun; YU Zhao-xiang

    2007-01-01

    In this article, coke plant wastewater was treated by a simultaneous nitrifying and denitrifying (SND) fixed biofilm hybrid system. The results showed that suitable parameters of the system were important for the performance of the bio-degradation system. The chemical oxygen demand (COD) removal efficiency in this system was satisfactory, higher than 94%, and ammonia nitrogen was higher than 95%. The effluent COD concentration could meet the discharge standard, except for very few situations. The results showed that a sufficient carbon source was important for making ammonia nitrogen concentration meet the discharge standard. Then the TN removal efficiency in this system can be brought higher than 94%. Dissolved oxygen (DO) is very important to the performance of the SND bio-degradation system, and the suitable DO is about 3.5-4.0 mg/L at the forepart of reactor. In addition, the performance of the system was almost not affected by pH value. The results show that the system is feasible to treat coke plant wastewater.

  1. Treatment of coke plant wastewater by A/O fixed biofilm system

    Institute of Scientific and Technical Information of China (English)

    YU Zhaoxiang; QI Rong; YIN Yanjun

    2005-01-01

    Coke plant wastewater was treated by an anaerobic-aerobic (A/O) biofilm system. A lab-scale experiment, during which semi-soft media were packed in both the anaerobic and the aerobic reactors, was carried out. The influence parameters, such as HRT, C/N ratio, OLR, and the recycling flow rate on the performance of the system, were studied. The results showed that a sufficient carbon source was important to the performance of bio-degradation system. The COD removal rate increased from 64.15% to 83.28% by raising C/N in wastewater from 2.5 (no external carbon source) to 5. But the effluent COD concentration was still a little higher than the discharge standard. In order to make it meet the discharge standard, a deep treatment, coagulation, was applied, which was proved as an effective method. Then the effluent COD concentration can be brought to lower than 200 mg·L-1. The NH4-N removal rate in this system was satisfactory, being higher than 99%. In addition, it was almost not affected by both C/N ratio and coagulation treatment. The results show that the system is feasible to treat coke plant wastewater.

  2. Functionalization of Petroleum Coke-Derived Carbon for Synergistically Enhanced Capacitive Performance.

    Science.gov (United States)

    Zhang, Yan; Li, Xuejin; Huang, Jufeng; Xing, Wei; Yan, Zifeng

    2016-12-01

    Petroleum coke is a valuable and potential source for clean energy storage if it could be modified legitimately and facilely. In the present study, porous carbon with high surface area and abundant oxygen-containing groups was prepared from petroleum coke by chemical activation and modification processes. The as-prepared carbon exhibits a high surface area (1129 m(2) · g(-1)) and stable micrographic structure. It presents a high specific capacitance and excellent rate performance in KOH electrolyte. Even at an ultrahigh current density of 50 A · g(-1), the specific capacitance of the prepared carbon can still reach up to an unprecedented value of 261 F · g(-1) with a superhigh retention rate of 81 %. In addition, the energy density of this material in aqueous electrolyte can be as high as 13.9 Wh · kg(-1). The high energy density and excellent rate performance ensure its prosperous application in high-power energy storage system. PMID:27009530

  3. Instability of biological nitrogen removal in a cokes wastewater treatment facility during summer

    International Nuclear Information System (INIS)

    Failure in nitrogen removal of cokes wastewater occurs occasionally during summer season (38 deg. C) due to the instability of nitrification process. The objective of this study was to examine why the nitrification process is unstable especially in summer. Various parameters such as pH, temperature, nutrients and pollutants were examined in batch experiments using activated sludge and wastewater obtained from a full-scale cokes wastewater treatment facility. Batch experiments showed that nitrification rate of the activated sludge was faster in summer (38 deg. C) than in spring or autumn (29 deg. C) and the toxic effects of cyanide, phenol and thiocyanate on nitrification were reduced with increasing temperature. Meanwhile, experiment using continuous reactor showed that the reduction rate in nitrification efficiency was higher at 38 deg. C than at 29 deg. C. In conclusion, the instability of full-scale nitrification process in summer might be mainly due to washing out of nitrifiers by fast growth of competitive microorganisms at higher temperature under increased concentrations of phenol and thiocyanate

  4. Study on the adsorption characteristics of modified semi-coke used for treating biologically treated effluent from coking wastewater%改性兰炭对焦化废水生化出水的吸附特性

    Institute of Scientific and Technical Information of China (English)

    王丽娜; 刘尚超; 张垒; 付本全

    2012-01-01

    Semi-coke that has been modified with steam at high temperature is used for the static adsorption of TOC in biochemically treated effluent from coking wastewater. The effects of influencing factors, such as adsorption time, pH,adsorbent dosage,particle size,etc.,on the treatment efficiency are investigated. The results show that after adding 20 g/L 1 -2 mm of modified semi-coke to wastewater whose pH is 4, at room temperature and adsorption time 30 min,the TOC removing rate of biochemically treated effluent from the coking wastewater is more than 60%. The concentration and variety of the organisms in samples after the adsorption process have decreased greatly.%利用水蒸气高温改性后的兰炭静态吸附焦化废水生化出水中的TOC,考察了吸附时间、pH、吸附剂用量、粒径等因素对处理效果的影响.结果表明,向废水(pH=4)中投加20 g/L改性兰炭(粒径1~2 mm),室温下吸附30 min后,对焦化废水生化出水的TOC去除率在60%以上.吸附后水样中的有机物浓度和种类都大幅下降.

  5. Coke formation over zeolites and CeO2-zeolites and its influence on selective catalytic reduction of NOx

    International Nuclear Information System (INIS)

    Selective catalytic reduction, various possible reasons of coke formation, and temperature programmed oxidation of coke deposits are studied over HFER, HZSM-5 and 15|wt% CeO2-H zeolites. The materials are characterised by TGA, NH3-TPD and in-situ FTIR measurements. HFER based catalysts showed superior NOx (NO+NO2) conversion in SCR with propene compared with HZSM-5 based catalysts. It is found that NO2 (formed by the oxidation of NO) is not the only important intermediate in determining the extent of NOx conversion. The topology and acidity of the zeolites play an important role in selective activation of propene and its reaction with NO2. Over HZSM-5 based catalysts the rate of deposition of carbonaceous compounds is higher than the rate of reaction of activated propene with NO2, leading to unselective reduction to NO. The nature and the amount of the carbonaceous products deposited over the zeolites are found to depend on the acidity, structure of the zeolite and reaction conditions (inert or oxidative atmosphere). Coke deposition rate is enhanced in the presence of oxygen and most of the coke is retained by the zeolite which is detrimental for NOx reduction. in-situ IR studies show that hydrocarbon deposits are more heterogeneous and carbon rich over HZSM-5 compared with HFER. TPO studies show that only a negligible fraction of hydrocarbon deposits are active in NOx conversion

  6. Modification of coal-tar pitch by air-blowing. II. Influence on coke structure and properties

    Energy Technology Data Exchange (ETDEWEB)

    Fernandez, J.J.; Figueiras, A.; Granda, M.; Bermejo, J.; Parra, J.B.; Menendez, R. [Instituto Nacional del Carbon, Oviedo (Spain)

    1995-12-31

    This study is concerned with the use of air-blowing to improve pitch properties as matrix precursor of carbon-carbon composites. Two commercial coal-tar pitches, an impregnating pitch and a binder pitch, and their air-blown products obtained at temperatures between 250 and 300{degree}C, were pyrolysed in a horizontal tube furnace at 1000{degree}C. Cokes were characterized by light microscopy to monitor the influence of air-blowing on their optical texture. Density and porosity of cokes were determined by helium densimetry and mercury porosimetry, and their strength and reactivity by a microstrength test and thermogravimetric analysis, respectively. Results show that air-blowing of the impregnating pitch produces a decrease of the optical texture of coke, while in the case of the binder pitch there is an improvement of the microcrystalline structure. Moreover, air-blowing brings about a substantial increase in the density and strength of cokes, and a decrease in their porosity and reactivity. 14 refs., 5 figs., 6 tabs.

  7. Gas Production with Coproduction of Methanol through Dry Quenching of Coke Developed by Yantai Tonqve Chemical/Yantai University

    Institute of Scientific and Technical Information of China (English)

    2008-01-01

    @@ The Yantai Tongye Chemical Technology Co.,Ltd.and Yantai University have jointly studied and developed the proprietary technology for gas generation through dry quenching of coke with co-production of methanol.Currently this technology has been successfully licensed and the engineering and the design work is underway.

  8. Catalytic fast pyrolysis of mushroom waste to upgraded bio-oil products via pre-coked modified HZSM-5 catalyst.

    Science.gov (United States)

    Wang, Jia; Zhong, Zhaoping; Ding, Kuan; Xue, Zeyu

    2016-07-01

    In this paper, HZSM-5 catalyst was modified by pre-coked to cover the strong external acid sites by methanol to olefins reaction, and the modified catalysts were then applied to conduct the catalyst fast pyrolysis of mushroom waste for upgraded bio-fuel production. Experiment results showed that the strong external acid sites and specific surface area decreased with pre-coked percentage increasing from 0% to 5.4%. Carbon yields of hydrocarbons increased at first and then decreased with a maximum value of 53.47%. While the obtained oxygenates presented an opposite variation tendency, and the minimum values could be reached when pre-coked percentage was 2.7%. Among the achieved hydrocarbons, toluene and p-xylene were found to be the main products, and the selectivity of p-xylene increased at first and then decreased with a maximum value of 34.22% when the pre-coked percentage was 1.3%, and the selectivity of toluene showed the opposite tendency with a minimum value of 25.47%. PMID:27065226

  9. Investigations concerning the mechanism of action of brown-coal coke particles in aerobic biological waste water treatment

    International Nuclear Information System (INIS)

    At the start of this work experience with the use of brown coal coke in the activated sludge process was lacking entirely. It therefore was necessary to carry through preliminary experiments in order to practically test the effect of Grown-coal coke. In two technical-scale experiments and a pilot test, very good results were obtained with the application of brown-coal coke to activated sludge. These, and previously published results, permitted to evolve moodel concepts of the mechanism of action of coal, especially brown coal coke, in activated sludge. According to these concepts the coal particles act as buffers and a temporary adsorbent of oxygen and waste water constituents. This in turn stimulates the colonization of the surface with microorganisms. In order to corroborate these model concepts, the - adsorption and desorption of solved oxygen to coal in a watery medium and - the effect of coal over a longer period of time were investigated. The results in essence confirm the model concepts. (UWa)

  10. 41 CFR 101-26.4904-416 - DD Form 416: Purchase Request for Coal, Coke, or Briquettes.

    Science.gov (United States)

    2010-07-01

    ... 41 Public Contracts and Property Management 2 2010-07-01 2010-07-01 true DD Form 416: Purchase Request for Coal, Coke, or Briquettes. 101-26.4904-416 Section 101-26.4904-416 Public Contracts and Property Management Federal Property Management Regulations System FEDERAL PROPERTY MANAGEMENT REGULATIONS SUPPLY AND PROCUREMENT 26-PROCUREMENT...

  11. Coke formation and performance of an intermediate-temperature solid oxide fuel cell operating on dimethyl ether fuel

    Energy Technology Data Exchange (ETDEWEB)

    Su, Chao; Ran, Ran; Wang, Wei; Shao, Zongping [State Key Laboratory of Materials-Oriented Chemical Engineering, College of Chemistry and Chemical Engineering, Nanjing University of Technology, No. 5 Xin Mofan Road, Nanjing 210009 (China)

    2011-02-15

    Dimethyl ether (DME) as a fuel of SOFCs is investigated with great attention paid to coke formation over the Ni-YSZ anode. DME is easily decomposed to CH{sub 4}, CO and H{sub 2} at temperatures above 700 C, with total conversion occurring at 850 C over the Ni-YSZ catalyst. These data suggest that the DME electro-oxidation likely proceeds via an indirect pathway. O{sub 2}-TPO analysis, laser Raman spectroscopy and SEM-EDX characterizations demonstrate coke formation over Ni-YSZ, which is obvious and become more prevalent at higher temperatures. The introduction of CO{sub 2} in the fuel gas decreases the CH{sub 4} selectivity and effectively suppresses coke formation above 700 C. The suppression effect is increasingly apparent at higher temperatures. At 850 C, the anode still maintains geometric integrity after exposure to DME-CO{sub 2} (1:1, volume ratio) under OCV condition. With DME or DME-CO{sub 2}, the fuel cell power output is comparable to results obtained by operating with 3% water humidified hydrogen. No obvious cell degradation from the anode is observed when operating with DME-CO{sub 2}, while it is obvious with DME. The introduction of CO{sub 2} may be a good choice to suppress the coke formation when operating on DME; however, the proper selection of operation temperature is of significant importance. (author)

  12. 76 FR 59681 - Middletown Coke Company, LLC; Supplemental Notice That Initial Market-Based Rate Filing Includes...

    Science.gov (United States)

    2011-09-27

    ... From the Federal Register Online via the Government Publishing Office DEPARTMENT OF ENERGY Federal Energy Regulatory Commission Middletown Coke Company, LLC; Supplemental Notice That Initial Market-Based Rate Filing Includes Request for Blanket Section 204 Authorization This is a supplemental notice in the above-referenced proceeding...

  13. 77 FR 20788 - Foundry Coke Products From the People's Republic of China: Final Results of Expedited Second...

    Science.gov (United States)

    2012-04-06

    ...'') Review, 76 FR 74775 (December 1, 2011); see also Notice of Amended Final Determination of Sales at Less... 66 FR 48025 (September 17, 2001) (``Order''). We received a complete substantive response from the... International Trade Administration Foundry Coke Products From the People's Republic of China: Final Results...

  14. 40 CFR Appendix A to Subpart L of... - Operating Coke Oven Batteries as of April 1, 1992

    Science.gov (United States)

    2010-07-01

    ... 40 Protection of Environment 9 2010-07-01 2010-07-01 false Operating Coke Oven Batteries as of April 1, 1992 A Appendix A to Subpart L of Part 63 Protection of Environment ENVIRONMENTAL PROTECTION AGENCY (CONTINUED) AIR PROGRAMS (CONTINUED) NATIONAL EMISSION STANDARDS FOR HAZARDOUS AIR POLLUTANTS FOR SOURCE CATEGORIES National Emission...

  15. Refinaria do Nordeste: petroleum coke handling system; Refinaria do Nordeste: desafios do sistema de movimentacao de coque verde de petroleo

    Energy Technology Data Exchange (ETDEWEB)

    Medeiros, Luiz G. de; Cabral, Jose Mauro B. [PETROBRAS S.A., Ipojuca, PE (Brazil). Refinaria do Nordeste (RNEST); Lucredi, Hedewandro A. [PETROBRAS S.A., Paulinia, SP (Brazil). Refinaria de Paulinia (REPLAN); Barros, Francisco Carlos da C. [PETROBRAS S.A., Rio de Janeiro, RJ (Brazil). Centro de Pesquisas (CENPES)

    2008-07-01

    The Delayed Coking Units - DCU - are adequate to the scheme for processing heavy oils where the market of fuel oil or asphalt is low or not profitable. The DCU's are conversion units that produce, in addition to the gas and liquid distilled products, the petcoke. The petcoke, depending on the characteristics, is used in various applications like as in the aluminum, iron, thermoelectric and cement industries. The petcoke is solid and its logistics is quite different from most of the products handled by PETROBRAS; therefore, this product has been a constant challenge in relation to the market requirements. Due to the importance of the DCU at Refinaria do Nordeste, and the petcoke production capacity, the coke handling system was projected in order to ensure the refinery operational continuity. The project permits the expedition and loading of 10,000 tons of petcoke within a period of 12 hours of work for cargo vessel. In the development of the processing project of Refinaria do Nordeste efforts were made to optimize the Delayed Coking Unit for the production of distilled products and the quality of the coke. The DCU operating conditions were projected so as to produce petcoke with quality adequate to the iron and aluminum industry. (author)

  16. Quantification of the Existence Ratio of Non-Adhesion Grain Boundaries and Factors Governing the Strength of Coke Containing Low-Quality Coal

    Science.gov (United States)

    Kanai, Tetsuya; Yamazaki, Yoshiaki; Zhang, Xiaoqing; Uchida, Ataru; Saito, Yasuhiro; Shoji, Masakazu; Aoki, Hideyuki; Nomura, Seiji; Kubota, Yukihiro; Hayashizaki, Hideyuki; Miyashita, Shigeto

    “Non-adhesion grain boundaries” are formed when low-quality coal grains do not adhere to other grains in the carbonization process because of the low dilation of coke. To better understand the effects of non-adhesion grain boundaries on coke strength, the relationship between the existence ratio of non-adhesion grain boundaries and coke strength was investigated quantitatively. The existence ratio of non-adhesion grain boundaries were measured quantitatively by observing the fracture cross-section of coke using scanning electron microscopy (SEM). Coke strength was measured with a diametral-compression test and an I-shape drum index test. As a result, non-adhesion grain boundaries increased with an increase in the blending ratio of low-quality coal. In particular, non-adhesion grain boundaries increased rapidly when the blending ratio of low-quality coal was over 50%. When the ratio was less than 50%, low-quality coals adhered to other caking coal. However, not many low-quality coals adhered to other caking coals when the ratio was over 50%. The tensile strength of coke was not affected by the porosity of coke. However, the tensile strength and the drum index were affected by the existence ratio of non-adhesion grain boundaries. Tensile strength decreased rapidly even for a few non-adhesion grain boundaries because significant defects caused a fracture in the diametral-compression test. However, the I-shape drum index decreased linearly with the existence ratio of the non-adhesion grain boundaries because many fractures occurred during 600 rotations in the drum. The strength of coke containing low-quality coal is governed by the existence ratio of non-adhesion grain boundaries rather than mean values such as the porosity of coke.

  17. Utilization of Coke Oven Gas and Converter Gas in the Direct Reduction of Lump Iron Ore

    Science.gov (United States)

    Mousa, Elsayed Abdelhady; Babich, Alexander; Senk, Dieter

    2014-04-01

    The application of off-gases from the integrated steel plant for the direct reduction of lump iron ore could decrease not only the total production cost but also the energy consumption and CO2 emissions. The current study investigates the efficiency of reformed coke oven gas (RCOG), original coke oven gas (OCOG), and coke oven gas/basic oxygen furnace gas mixtures (RCOG/BOFG and OCOG/BOFG) in the direct reduction of lump iron ore. The results were compared to that of reformed natural gas (RNG), which is already applied in the commercial direct reduction processes. The reduction of lump ore was carried out at temperatures in the range of 1073 K to 1323 K (800 °C to 1050 °C) to simulate the reduction zone in direct reduction processes. Reflected light microscopy, scanning electron microscopy, and X-ray diffraction analysis were used to characterize the microstructure and the developed phases in the original and reduced lump iron ore. The rate-controlling mechanism of the reduced lump ore was predicted from the calculation of apparent activation energy and the examination of microstructure. At 1073 K to 1323 K (800 °C to 1050 °C), the reduction rate of lump ore was the highest in RCOG followed by OCOG. The reduction rate was found to decrease in the order RCOG > OCOG > RNG > OCOG-BOF > RCOG-BOFG at temperatures 1173 K to 1323 K (900 °C to 1050 °C). The developed fayalite (Fe2SiO4), which resulted from the reaction between wüstite and silica, had a significant effect on the reduction process. The reduction rate was increased as H2 content in the applied gas mixtures increased. The rate-determining step was mainly interfacial chemical reaction with limitation by gaseous diffusion at both initial (20 pct reduction) and moderate (60 pct reduction) stages of reduction. The solid-state diffusion mechanism affected the reduction rate only at moderate stages of reduction.

  18. Influence of ultrasonic on the coking amount of catalyst (Ni/γ-Al2O3) for the dry reforming of benzene

    Institute of Scientific and Technical Information of China (English)

    YANG Guo-lai; CHEN Han-ping; MI Tie; FENG Bo

    2007-01-01

    The lnfluence of ultrasonic treatment on the coking amount of a nickel-based catalyst(Ni/l2O3)for the reaction of reforming with carbon dioxide of Benzeno was investigated.The results show that ultrasonic treatment modify the pore size distribution of the catalysts significantly and also reduce the amount of coke formed on the catalyst.The reduction in the coking amount is not sensitive to the power output of the ultrasonic treatment device in the power range tested(120 W and 500 W).

  19. Development and Testing of the Advanced CHP System Utilizing the Off-Gas from the Innovative Green Coke Calcining Process in Fluidized Bed

    Energy Technology Data Exchange (ETDEWEB)

    Chudnovsky, Yaroslav; Kozlov, Aleksandr

    2013-08-15

    Green petroleum coke (GPC) is an oil refining byproduct that can be used directly as a solid fuel or as a feedstock for the production of calcined petroleum coke. GPC contains a high amount of volatiles and sulfur. During the calcination process, the GPC is heated to remove the volatiles and sulfur to produce purified calcined coke, which is used in the production of graphite, electrodes, metal carburizers, and other carbon products. Currently, more than 80% of calcined coke is produced in rotary kilns or rotary hearth furnaces. These technologies provide partial heat utilization of the calcined coke to increase efficiency of the calcination process, but they also share some operating disadvantages. However, coke calcination in an electrothermal fluidized bed (EFB) opens up a number of potential benefits for the production enhancement, while reducing the capital and operating costs. The increased usage of heavy crude oil in recent years has resulted in higher sulfur content in green coke produced by oil refinery process, which requires a significant increase in the calcinations temperature and in residence time. The calorific value of the process off-gas is quite substantial and can be effectively utilized as an “opportunity fuel” for combined heat and power (CHP) production to complement the energy demand. Heat recovered from the product cooling can also contribute to the overall economics of the calcination process. Preliminary estimates indicated the decrease in energy consumption by 35-50% as well as a proportional decrease in greenhouse gas emissions. As such, the efficiency improvement of the coke calcinations systems is attracting close attention of the researchers and engineers throughout the world. The developed technology is intended to accomplish the following objectives: - Reduce the energy and carbon intensity of the calcined coke production process. - Increase utilization of opportunity fuels such as industrial waste off-gas from the novel

  20. Quantitative analysis of ammonium salts in coking industrial liquid waste treatment process based on Raman spectroscopy

    Science.gov (United States)

    Cao, Ya-Nan; Wang, Gui-Shi; Tan, Tu; Cai, Ting-Dong; Liu, Kun; Wang, Lei; Zhu, Gong-Dong; Mei, Jiao-Xu

    2016-10-01

    Quantitative analysis of ammonium salts in the process of coking industrial liquid waste treatment is successfully performed based on a compact Raman spectrometer combined with partial least square (PLS) method. Two main components (NH4SCN and (NH4)2S2O3) of the industrial mixture are investigated. During the data preprocessing, wavelet denoising and an internal standard normalization method are employed to improve the predicting ability of PLS models. Moreover, the PLS models with different characteristic bands for each component are studied to choose a best resolution. The internal and external calibration results of the validated model show a mass percentage error below 1% for both components. Finally, the repeatabilities and reproducibilities of Raman and reference titration measurements are also discussed. Project supported by the National Natural Science Foundation of China (Grant Nos. 41405022 and 61475068).

  1. New Coke Oven Facilities at Linhuan Coal Chemical Company Adopt LyondellBasell's Aromatics Extraction Process

    Institute of Scientific and Technical Information of China (English)

    2008-01-01

    @@ The new 80 kt/a coal chemical unit at the Linhuan Coal Chemical Company in Anhui province will adopt the aro-matics extraction process licensed by LyondellBasell Company. This unit is expected to come on stream by 2009.This technology is suitable for manufacture of high-purity aromatics with broad adaptability and large scale produc-tion capability. In the previous year LyondellBasell was awarded six patents on aromatics extraction process. It is told that the achievements to be adopted by the Linhuan Coal Chemical Company are partly a series of aromatics extrac-tion processes for recovery of coke oven light oil performed by LyondellBasell.

  2. Fully automatic apparatus for proximate analysis and total sulfur analysis of coal and coke

    Energy Technology Data Exchange (ETDEWEB)

    Ishibashi, Y.; Fukumoto, K.; Maeda, K.; Ogawa, A.; Goto, K.; Ishii, T.

    1987-02-01

    For the purpose of saving labor and improving working conditions, the full automatic apparatus for the proximate analysis and total sulfur analysis of coal and coke was developed. Objects of this automation were to quantify inherent moisture, ash, volatile matter and total sulfur. Quantitative determination of inherent moisture, ash and volatile matter was made gravimetrically. Total sulfur was measured by combustion and acid and base titration, using a conductivity glass electrode sensor. The robot was set to the center of the automatic apparatus and relevant apparatuses were arranged in concentric circular locations. The computer carried out condition control of each apparatus, sequence control by operating demand and operation completing signal, and progress control of analysis. Very high correlation between the conventional method and this automatic method was confirmed. 4 refs., 9 figs., 3 tabs.

  3. Toxicity of coke wastewater treated with advanced oxidation by Fenton process supported by ultrasonic field

    Directory of Open Access Journals (Sweden)

    Kwarciak-Kozłowska Anna

    2016-03-01

    Full Text Available The aim of the presented study was to determine the toxicity of wastewater from the production of coke. The wastewater was treated with advanced oxidation involving ultrasonic field with Fenton’s reagent (the amplitude was 61.5 μm and sonication time 8 min. Two doses of iron and four doses of hydrogen peroxide were used. The amount of hydrogen peroxide was proportional to the value of the chemical oxygen demand of raw wastewater, ranging from COD/H2O2 ratio of 1:2.5 to 1:20. Two tests were used to determine the toxicity (algae growth inhibition test and Lepidium test. It was found that more toxic to algae was wastewater treated by Fenton’s reagent containing a higher dose of iron. A similar inhibitory effect was observed on the germination of cress seeds.

  4. The influence of Ni loading on coke formation in steam reforming of acetic acid

    Energy Technology Data Exchange (ETDEWEB)

    An, Lu; Dong, Changqing; Yang, Yongping; Zhang, Junjiao; He, Lei [National Engineering Laboratory of Biomass Power Generation Equipment, North China Electric Power University, Beijing 102206 (China)

    2011-03-15

    Steam reforming of acetic acid on Ni/{gamma}-Al{sub 2}O{sub 3} with different nickel loading for hydrogen production was investigated in a tubular reactor at 600 C, 1 atm, H2O/HAc = 4, and WHSV = 5.01 g-acetic acid/g-cata.h{sup -1}. The catalysts were characterized by temperature programmed oxidation (TPO) and differential thermal analysis (DTA), X-ray photoelectron spectroscopy (XPS) and transmission electron microscopy (TEM). The results showed that the amount of deposited carbidic-like carbon decreased and graphitic-like carbon increased with Ni loading increasing from 9 to 15 wt%. The Ni/{gamma}-Al{sub 2}O{sub 3} catalyst with 12 wt% Ni loading had higher catalytic activity and lower coke deposited rate. (author)

  5. Reactivation of coked H-ZSM-5 by treatment with hydrogen and alkanes

    Energy Technology Data Exchange (ETDEWEB)

    Bauer, F.; Ernst, H. [Univ. of Leipzig (Germany); Geidel, E. [Univ. of Hamburg (Germany); Schoedel, R. [Leuna-Werke GmbH (Germany)

    1996-11-01

    The conversion of methanol to hydrocarbons on zeolite H-ZSM-5, in particular the long-term stability of the catalyst, was studied under different reaction conditions. Whereas no significant change in the product distribution was observed, hydrogen and alkane-containing recycle gases show lower deactivation rates than nitrogen. In addition, spent catalysts were partially reactivated by alkane treatment, increasing the time on stream before an oxidative regeneration procedure is required. Lower alkanes such as propane and isobutane yield the best results. The influence of hydrogen-containing gases on the deactivation rate and on the nature of coke on zeolite H-ZSM-5 indicates dissociative adsorption of hydrogen and alkanes on a few sites with enhanced activity. Surface hydrogen species formed by adsorption of alkanes are assumed to make possible the hydrocracking of carbonaceous deposits. 20 refs., 6 figs., 2 tabs.

  6. STUDY ON REDUCING AND MELTING BEHAVIOR OF MILL SCALE/PETROLEUM COKE BLEND

    Directory of Open Access Journals (Sweden)

    Bruno Deves Flores

    2015-07-01

    Full Text Available Self-reducing tests were carried out under isothermal and non-isothermal condition in a muffle furnace, aiming to assess the reduction and melting of a self-reducing blend of mill scale and petroleum coke (85-15% in weight. The products obtained were analyzed by mass loss and wet analysis. Further investigations for the products from the non-isothermal condition were done by X-ray diffraction, nude eye inspection and carbon analyzer. It was observed that mass loss fraction and metallization degree are directly related and both increase with time and temperature. In the non-isothermal maximum mass loss was achieved in 8 minutes, reaching metallization degrees above 90%. It was observed that the reduction of iron oxide occurs mainly in solid state and the smelting of the samples is directly related to the iron carburization process. Thus, the use of self-reducing mixtures shows a possible way to recycle mill scale.

  7. Joint Implementation Analysis: A Case Study of the Japan-China Coke Dry Quenching (CDQ) Project

    Institute of Scientific and Technical Information of China (English)

    2000-01-01

    One of the key issues for "Joint Implementation" is how to define a plausible baseline, a necessary benchmark for calculating net Greenhouse Gases (GHGs) emission reductions through a comparative approach. Based on a thorough case study of the China-Japan Coke Dry Quenching (CDQ) project, the first approved pilot project in China under the "Activities Implemented Jointly" (AIJ) framework, the paper not only describes in detail the complete procedure of baseline definition of the case project, but also discusses its approach to baseline determination. Furthermore, cost-benefit analysis of GHGs mitigation is conducted according to the baseline. This empirical case study, based on real AIJ project data, will be beneficial for the development of future projects under Kyoto mechanisms such as "Clean Development Mechanism" and "Joint Implementation".

  8. Oil Coking Prevention Using Electric Water Pump for Turbo-Charge Spark-Ignition Engines

    Directory of Open Access Journals (Sweden)

    Han-Ching Lin

    2014-01-01

    Full Text Available Turbocharger has been widely implemented for internal combustion engine to increase an engine's power output and reduce fuel consumption. However, its operating temperature would rise to 340°C when engine stalls. This higher temperature may results in bearing wear, run-out, and stick, due to oil coking and insufficient lubrication. In order to overcome these problems, this paper employs Electric Water Pump (EWP to supply cool liquid to turbocharger actively when the engine stalls. The system layout, operating timing, and duration of EWP are investigated for obtaining optimal performance. The primarily experimental results show that the proposed layout and control strategy have a lower temperature of 100°C than the conventional temperature 225°C.

  9. Synthesis of aluminum nitride in a coke-calcium reduction bed using nitrogen in air

    Institute of Scientific and Technical Information of China (English)

    Ehsan Noorizadeh Dehkordi; H.R. Samim Banihashemi; R. Naghizadeh; H.R.Rezaie; M.Goodarzi

    2015-01-01

    An experimental study on the heating of a mixture of aluminum and lithium hydroxide (LiOH) powders in a reductive bed under air atmosphere is reported. The formation of aluminum nitride (AlN) during this process was the focus of this study. The formation of AlN was achieved using LiOH as an additive and heating the sample in a resistance furnace in a specially designed double crucible within a bed of a mixture of coke and filamentous calcium. The temperature range of the reaction was between 700°C and 1100°C. The optimum tem-perature of 1100°C and the optimum LiOH amount (5wt%) required to achieve maximum yield were determined by powder X-ray diffrac-tion (XRD) analysis. Scanning electron microscopy (SEM) micrographs clearly indicated the transformation of grain structures from rods (700°C) to cauliflower shapes (1100°C).

  10. The Development of Coke Carried—Heat Gasification Coal—Fired Combined Cycle

    Institute of Scientific and Technical Information of China (English)

    LiZhao; XiangdongXu

    1999-01-01

    Carried-Heat Partial Gasification Combined cycle is a novel combined cycle which was proposed by Thermal Engineering Department of Tsinghua University in 1992,The idea of the system comes from the situation that the efficiency of the power plants in china is much lower than that of the advanced countries,but the coal consumption is much higher,which brings about the waste of primary energy resources and the pollution of the environment.With the deep study of the gasification technology,Coke Carried-Heat Gasification Coal-Fired Combined Cycle,as the improved system,came into birth in 1996 based on the partial gasification one,At the end of 1997,a new cycle scheme similar to IGCC was created.This paper focuses on several classes combined cycle put forward by Tsinghua University,depending on the plant configuration and carbon conversion,making the solution a viable and attractive option for efficient coal utilization.

  11. Environmental protection in design and operation of dryers for small coking coal

    Energy Technology Data Exchange (ETDEWEB)

    Micinski, A.; Skorupa, J.; Wala, H.; Zimny, J.

    1987-01-01

    The ROW dryers for drying flotation concentrates of coking coal were designed for minimum dust and SO/sub 2/ emission. The ROW-2 drum dryer together with its dedusting equipment is presented and described. Parameters of the ROW-1 and ROW-2 dryer related to dedusting were measured and are shown in a table. The measured values of dust emission from the dryer drum had a significant range (1.9-6.6 Mg/h) as they depend on final concentrate humidity, air flow through the dryer and other factors. Effectiveness of the cyclone batteries was high (86.3-95.1%, predominantly over 92.5%). Effectiveness of dedusters with Venturi tubes was 81.3-92.3%. The cumulative effectiveness was 97.4-99.6%. During wet dedusting 15-50% of SO/sub 2/ is absorbed and the acidified water is recirculated so that the atmosphere and surface waters are protected. 3 refs.

  12. Evaluation of pitches and cokes from solvent-extracted coal materials

    Energy Technology Data Exchange (ETDEWEB)

    McHenry, E.R.

    1996-12-01

    Three initial coal-extracted (C-E) samples were received from the West Virginia University (WVU) Chemical Engineering Department. Two samples had been hydrogenated to obtain pitches that satisfy Theological requirements. One of the hydrogenated (HC-E) samples had been extracted by toluene to remove ash and higher molecular weight aromatic compounds. We were unable to measure the softening point and viscosity of the non-hydro treated solid extract sample, Positive characteristics in the HC-E materials were softening points of 113-119{degrees}C, low sulfur and ash. The oxygen and nitrogen content of the HC-E samples may limit future usage in premium carbon and graphite products. Coking values were similar to petroleum pitches. Laboratory anode testing indicates that in combination with standard coal-tar pitch, the HC-E material can be used as a binder pitch.

  13. Ammonium nitrogen removal from coking wastewater by chemical precipitation recycle technology.

    Science.gov (United States)

    Zhang, Tao; Ding, Lili; Ren, Hongqiang; Xiong, Xiang

    2009-12-01

    Ammonium nitrogen removal from wastewater has been of considerable concern for several decades. In the present research, we examined chemical precipitation recycle technology (CPRT) for ammonium nitrogen removal from coking wastewater. The pyrolysate resulting from magnesium ammonium phosphate (MAP) pyrogenation in sodium hydroxide (NaOH) solution was recycled for ammonium nitrogen removal from coking wastewater. The objective of this study was to investigate the conditions for MAP pyrogenation and to characterize of MAP pyrolysate for its feasibility in recycling. Furthermore, MAP pyrolysate was characterized by scanning electron microscope (FESEM), transmission electron microscope (TEM), Fourier transform infrared spectroscopy (FTIR) as well as X-ray diffraction (XRD). The MAP pyrolysate could be produced at the optimal condition of a hydroxyl (OH(-)) to ammonium molar ratio of 2:1, a heating temperature of 110 degrees C, and a heating time of 3h. Surface characterization analysis indicated that the main component of the pyrolysate was amorphous magnesium sodium phosphate (MgNaPO(4)). The pyrolysate could be recycled as a magnesium and phosphate source at an optimum pH of 9.5. When the recycle times were increased, the ammonium nitrogen removal ratio gradually decreased if the pyrolysate was used without supplementation. When the recycle times were increased, the ammonium nitrogen removal efficiency was not decreased if the added pyrolysate was supplemented with MgCl(2).6H(2)O plus Na(2)HPO(4).12H(2)O during treatment. A high ammonium nitrogen removal ratio was obtained by using pre-formed MAP as seeding material. PMID:19850316

  14. Coking-resistant Ni-ZrO2/Al2O3 catalyst for CO methanation

    Institute of Scientific and Technical Information of China (English)

    Qing Liu; Fangna Gu; Jiajian Gao; Huifang Li; Guangwen Xu∗; Fabing Su∗

    2014-01-01

    Highly coke-resisting ZrO2-decorated Ni/Al2O3 catalysts for CO methanation were prepared by a two-step process. The support was first loaded with NiO by impregnating method and then modified with ZrO2 by deposition-precipitation method (IM-DP). Nitrogen adsorption-desorption, X-ray diffraction, scanning electron microscopy, transmission electron microscopy, thermogravimetric analysis, H2 temperature-programmed reduction and desorption, NH3 temperature-programmed desorption, and zeta potential analysis were employed to characterize the samples. The results revealed that, compared with the catalysts with the same composition prepared by co-impregnation (CI) and sequential impregnation (SI) methods, the Ni/Al2O3 catalyst prepared by IM-DP showed much enhanced catalytic performance for syngas methanation under the condition of atmospheric pressure and a high weight hourly space velocity of 120000 mL·g−1·h−1. In a 80 h life time test under the condition of 300–600◦C and 3.0 MPa, this catalyst showed high stability and resistance to coking, and the amount of deposited carbon was only 0.4 wt%. On the contrary, the deposited carbon over the catalyst without ZrO2 reached 1.5 wt%after a 60 h life time test. The improved catalytic performance was attributed to the selective deposition of ZrO2 nanoparticles on the surface of NiO rather than Al2O3, which could be well controlled via changing the electrostatic interaction in the DP procedure. This unique structure could enhance the dissociation of CO2 and generate surface oxygen intermediates, thus preventing carbon deposition on the Ni particles in syngas methanation.

  15. Petroleum coke adsorption as a water management option for oil sands process-affected water

    Energy Technology Data Exchange (ETDEWEB)

    Zubot, Warren [Syncrude Canada Ltd., Research and Development, Edmonton, Alberta, Canada T6N 1H4 (Canada); MacKinnon, Michael D. [OSPM Solutions Ltd., Hamilton, Ontario, Canada L8H 6X2 (Canada); Chelme-Ayala, Pamela; Smith, Daniel W. [University of Alberta, Department of Civil and Environmental Engineering, Edmonton, Alberta, Canada T6G 2W2 (Canada); Gamal El-Din, Mohamed, E-mail: mgamalel-din@ualberta.ca [University of Alberta, Department of Civil and Environmental Engineering, Edmonton, Alberta, Canada T6G 2W2 (Canada)

    2012-06-15

    Water is integral to both operational and environmental aspects of the oil sands industry. A water treatment option based on the use of petroleum coke (PC), a by-product of bitumen upgrading, was examined as an opportunity to reduce site oil sands process-affected water (OSPW) inventories and net raw water demand. Changes in OSPW quality when treated with PC included increments in pH levels and concentrations of vanadium, molybdenum, and sulphate. Constituents that decreased in concentration after PC adsorption included total acid-extractable organics (TAO), bicarbonate, calcium, barium, magnesium, and strontium. Changes in naphthenic acids (NAs) speciation were observed after PC adsorption. A battery of bioassays was used to measure the OSPW toxicity. The results indicated that untreated OSPW was toxic towards Vibrio fischeri and rainbow trout. However, OSPW treated with PC at appropriate dosages was not acutely toxic towards these test organisms. Removal of TAO was found to be an adsorption process, fitting the Langmuir and Langmuir-Freundlich isotherm models. For TAO concentrations of 60 mg/L, adsorption capacities ranged between 0.1 and 0.46 mg/g. This study demonstrates that freshly produced PC from fluid cokers provides an effective treatment of OSPW in terms of key constituents' removal and toxicity reduction. - Highlights: Black-Right-Pointing-Pointer Treatment of oil sands process-affected water (OSPW) using petroleum coke (PC) adsorption was investigated. Black-Right-Pointing-Pointer PC was effective at adsorbing naphthenic acids with higher cyclicity. Black-Right-Pointing-Pointer OSPW treated with PC at appropriate dosages was not toxic towards Vibrio fisheri and rainbow trout. Black-Right-Pointing-Pointer The adsorption of organic acids fitted the Langmuir and Langmuir-Freundlich isotherm models. Black-Right-Pointing-Pointer PC has the potential to be an effective adsorbent to treat OSPW either directly or as a pretreatment step.

  16. PAH source fingerprints for coke ovens, diesel and, gasoline engines, highway tunnels, and wood combustion emissions

    Science.gov (United States)

    Khalili, Nasrin R.; Scheff, Peter A.; Holsen, Thomas M.

    To evaluate the chemical composition (source fingerprint) of the major sources of polyaromatic hydrocarbons (PAHs) in the Chicago metropolitan area, a study of major PAH sources was conducted during 1990-1992. In this study, a modified high-volume sampling method (PS-1 sampler) was employed to collect airborne PAHs in both the particulate and gas phases. Hewlett Packard 5890 gas chromatographs equipped with the flame ionization and mass spectrometer detectors (GC/FID and GC/MS) were used to analyze the samples. The sources sampled were: coke ovens, highway vehicles, heavy-duty diesel engines, gasoline engines and wood combustion. Results of this study showed that two and three ring PAHs were responsible for 98, 76, 92, 73 and 80% of the total concentration of measured 20 PAHs for coke ovens, diesel engines, highway tunnels, gasoline engines and wood combustion samples, respectively. Six ring PAHs such as indeno(1,2,3- cd)pyrene and benzo( ghi)perylene were mostly below the detection limit of this study and only detected in the highway tunnel, diesel and gasoline engine samples. The source fingerprints were obtained by averaging the ratios of individual PAH concentrations to the total concentration of categorical pollutants including: (a) total measured mass of PAHs with retention times between naphthalene and coronene, (b) the mass of the 20 PAHs measured in this study, (c) total VOCs, and (d) total PM10. Since concentrations of the above categorical pollutants were different for individual samples and different sources, the chemical composition patterns obtained for each categorical pollutant were different. The source fingerprints have been developed for use in chemical mass balance receptor modeling calculations.

  17. Coke size effects on the temperature profile in iron ore sintering; Efeito da granulometria do coque no perfil de temperatura na sinterizacao de minerio de ferro

    Energy Technology Data Exchange (ETDEWEB)

    Bordon, M.A. [Escola de Engenharia Maua, Sao Paulo, SP (Brazil); Takano, C. [Sao Paulo Univ., SP (Brazil). Escola Politecnica

    1995-12-31

    This paper shows, for hematite iron sintering in laboratory scale, the evolution of the thermal profile affected by the coke particle size.The coke was classified into three size ranges: from +0.149 to -0.84 mm, from +1.68 to -2.38 mm, and from +3.38 to 4.0 mm. The results showed that the highest temperature peaks associated to the lowest coke consumption were obtained with coke within +1.68 and -2.38 mm. Larger particles increasing the sintering time by means of longer combustion time needed for each particle which results in widening the thermal profile, and in lowering the maximum temperature. Finer particles decrease the initial permeability and also widen the thermal profile with lower temperature, but they are less deleterious than larger sizes (+3.38 mm) 14 refs., 4 figs., 3 tabs.

  18. Enhancement of Head Temperature in 6 m-Tall Coke Oven%提高6米焦炉炉头温度

    Institute of Scientific and Technical Information of China (English)

    杨鹏

    2014-01-01

    Low temperature of oven head affects the coke production , maintenance of furnace body , heating control and the service life of coke oven .The reason of the low temperature of 8# coke oven head is analyzed .By adopting corresponding measures , the head temperature of coke oven has been enhanced .%炉头温度低会影响炼焦生产、炉体维护、加热控制和焦炉寿命,文章分析了8#焦炉炉头温度低的原因,通过采取相应的改进措施,达到提高焦炉炉头温度的目的。

  19. Determination of waste gas circulation flow in large coke oven battery%大型生产焦炉废气循环测定

    Institute of Scientific and Technical Information of China (English)

    杨冠楠; 王进先; 张熠; 吴添; 刘超

    2015-01-01

    介绍了一种焦炉废气循环量的测定方法,使用氩气成功地测定了7m焦炉在混合煤气和焦炉煤气加热时的废气循环量,由测定结果可知,焦炉煤气比混合煤气加热时的废气循环量高.%This paper introduces a determination method for waste gas circulation flow of coke oven battery. It has successfully determined the waste gas circulation flow on 7m coke oven battery respec-tively heated with coke oven gas and mixed gas,and the determination results show that the waste gas circulation flow is higher when heated with coke oven gas than mixed gas.

  20. Application of unroofing renovation in hot repair of coke oven battery%揭顶翻修技术在焦炉热维修中的应用

    Institute of Scientific and Technical Information of China (English)

    牟彪

    2015-01-01

    针对焦炉炉体出现的墙面剥蚀、炉间框缝缺料、过顶砖裂缝、炉底砖龟裂和破损等问题,采用揭顶翻修技术对焦炉进行热维修,维修效果良好,焦炉生产正常,具有一定的借鉴意义。%Regarding to the problems of coke oven proper such as denudation of oven wall, gap between oven bricks,crack on the crossover bricks,chopping and damage of bottom bricks,unroofing renovation technique is adopted to repair coke oven battery under hot state.The result is good and the coke oven battery after repair is in normal operation.The application of this technique in Jiusteel has reference significance for other coking plants.