There is considerable interest in the beneficial reuse of coal fly ash as a soil amendment on coal refuse piles. One method of application would be to blend the coal refuse and the fly ash before deposition in a refuse pile. A field experiment was initiated to measure the effects of bulk blending fly ash with coal refuse on water quality and plant growth parameters. Fly ash (class F) from three sources were used in the experiment. Two of the fly ashes were acidic and the third was alkaline. Trenches were excavated in a coal refuse pile to a depth of 2 m and the refuse was blended with fly ash and then returned to the trench. In other plots the ash was applied as a surface amendment. A treatment of a bulk blend of 5% (w/w) rock phosphate was also included in the experiment. Large volume lysimeters were installed in some trenches to collect the leachates. The fly ash treatments appear to improve the quality of the leachates when compared to the leachates from the untreated plots. The fly ash amended treatments have lower leachate concentrations of Fe and Al. Initially the fly ash treatments showed high levels of leachate B, however those levels have decreased with time. Millet (Setaria italica) yields from the first year of the experiment were highest n the alkaline fly ash and rock phosphate blended plots. In the second growing season, the two bulk blends with alkaline fly ash had the highest yields. In the third growing season all treatments had higher yield levels than the untreated control plots. The positive effects of the fly ash on leachate quality were attributed to the alkalinity of the ash, and the increase in yield was attributed to the increases in water holding capacity due to fly ash treatments.
Our present understanding of coal fly ash leaching in a disposal environment has largely been obtained from freshly, unreacted ashes and not from ashes, which have been allowed to weather in the open. The authors showed in a previous paper that alkaline fly ash weathers relatively rapidly into soil-like material when disposed in the open. In this paper, it is argued that fly ash, analogous to volcanic ash, has a high potential for large-scale utilisation in forestry and agriculture. A new concept of sustainable ash disposal and utilization in India is presented. 11 refs., 3 figs.
Topics covered include: mitigation of acid mine drainage (with fly ash, CFB ash, Aquafix system lime treatment of coal refuse); overburden analyses, spreadsheet for predicting acid mine drainage; technical information for fighting acid mine drainage; monitoring of passive treatment systems; and predicting the alkalinity generated by anoxic limestone drains.
The main constituents of coalash are silica and alumina accounting for 70%, and the remaining constituents contain calcium at about 5%. When coalash contacts with water, the water presents strong alkalinity. The prevention thereof, if possible at all, is effective for ash use in land reclamation, more effective utilization, and environment preservation. When water is sprayed into coal combustion waste gas, a neutralization phenomenon occurs to reduce pH of the recovered coalash. This has been proposed in the wet-type desulfurization method using limestone, which is explained as follows: adsorption of water into coalash surface occurs first, then SO2 in the waste gas is dissolved into this adsorbed water, and finally reacts with calcium on the coalash surface, producing CaSO{sub 4} and CaSO{sub 3}. However, the pH calculated from the ion balance in a sample ash liquation test does not strictly agree with the measurement value. Since infiltration of sulfur compounds into coalash particles is not recognized in all of the samples, factors other than dissolution of SO2, for example structural change in the ash particle surface due to existence of the adsorbed water can neither be ignored. (NEDO)
This paper presents data on widespread abnormal accumulations of lanthanides and yttrium (REY) in many coal deposits worldwide. High REY contents (>0.1%) have been found in coal seams and coalashes, as well as in the host and basement rocks of some coal basins. For a preliminary evaluation of coalashes as an REY raw material, not only the abundance but also the individual REY compositions were taken into account in this paper. Three REY distribution patterns for high-REY coalashes are fixed, with LREY- (LaN/LuN>1), MREY- (LaN/SmN1), and HREY- (LaN/LuN<1) enrichment. Four genetic types of REY enrichment in coal basin can be identified: 1) terrigenous type, with REY input by surface waters; 2) tuffaceous type, connected with falling and leaching of acid and alkaline volcanic a...
Four different ranks of coal have been sampled and separated into different density fractions by Float-Sink. The contents of some trace elements in each density fraction has been analyzed by ICAP. The analyzed data show that the alkaline-earth metals (Be, Sr, and Ba) have their special distributions in coal: Be and Sr may exist in the form of organic matter. Ba often has the highest content in the middle density fraction (1.4--1.5). The relative relationship between ash (or sulfur) and the trace element in a certain type of coal was obtained by using linear regression approach. Results show that there is no significant correlation between the contents of ash or sulfur and those of Be, Sr, and Ba. On the other hand, the linear regression was done among the trace elements of 17 types of coal. The results also show that there is no significant correlation between ash or sulfur and alkaline-earth metals.
The use of cattle manure (referred to as feedlot biomass, FB) as a fuel source has the potential to solve both waste disposal problems and reduce fossil fuel based CO{sub 2} emissions. Previous attempts to utilize animal waste as a sole fuel source have met with only limited success due to the higher ash, higher moisture, and inconsistent properties of FB. Thus, a co-firing technology is proposed where FB is ground, mixed with coal, and then fired in existing pulverized coal fired boiler burner facilities. It was found that FB has approximately half the heating value of coal, twice the volatile matter of coal, four times the N content of coal on heat basis, and due to soil contamination during collection, the ash content is almost 9 10 times that of low ash (5%) coal. The addition of < 5% crop residues had little apparent effect on heating value. The main value of composting for combustion fuel would be to improve physical properties and to provide homogeneity. The energy potential of FB diminished with composting time and storage; however, the DAF HHV is almost constant for ration, FB-raw, partially composted and finished composted. The fuel N per GJ is considerably high compared to coal, which may result in increased NOx emissions. The N and S contents per GJ increase with composting of FB while the volatile ash oxide% decreases with composting. Based on heating values and alkaline oxides, partial composting seems preferable to a full composting cycle. Even though the percentage of alkaline oxides is reduced in the ash, the increased total ash percentage results in an increase of total alkaline oxides per unit mass of fuel. The adiabatic flame temperature for most of the biomass fuels can be empirically correlated with ash and moisture percentage. 11 refs., 6 figs., 9 tabs.
Trace and major elements in coalash particles from dump of 'Nikola Tesla A' power plant in Obrenovac near Belgrade (Serbia) can cause pollution, due to leaching by atmospheric and surface waters. In order to assess this leaching potential, dump ash samples were subjected to extraction with solutions of decreasing pH values (8.50, 7.00, 5.50, and 4.00), imitating the reactions of the alkalineash particles with the possible alkaline, neutral, and acidic (e.g., acid rain) waters. The most recently deposited ash represents the greatest environmental threat, while 'aged' ash, because of permanent leaching on the dump, was shown to have already lost this pollution potential. On the basis of the determined leachability, it was possible to perform an estimation of the acidity of the regional rainfalls in the last decades.
Trace and major elements in coalash particles from dump of “Nikola Tesla A” power plant in Obrenovac near Belgrade (Serbia) can cause pollution, due to leaching by atmospheric and surface waters. In order to assess this leaching potential, dump ash samples were subjected to extraction with solutions of decreasing pH values (8.50, 7.00, 5.50, and 4.00), imitating the reactions of the alkalineash particles with the possible alkaline, neutral, and acidic (e.g., acid rain) waters. The most recently deposited ash represents the greatest environmental threat, while “aged” ash, because of permanent leaching on the dump, was shown to have already lost this pollution potential. On the basis of the determined leachability, it was possible to perform an estimation of the...
This experimental study is based on the innovative idea of using pulverized coal fly ash as a wet-end filler in papermaking. This is the first evaluation of the possible use of fly ash in the paper industry. Coal-based thermal power plants throughout the world are generating fly ash as a solid waste product. The constituents of fly ash can be used effectively in papermaking. Fly ash has a wide variation in particle size, which ranges from a few micrometers to one hundred micrometers. Fly ash acts as an inert material in acidic, neutral, and alkaline papermaking processes. Its physical properties such as bulk density (800-980 kg/m{sup 3}), porosity (45%-57%), and surface area (0.138-2.3076 m{sup 2}/g) make it suitable for use as a paper filler. Fly ash obtained from thermal power plants using pulverized coal was fractionated by a vibratory-sieve stack. The fine fraction with a particle size below 38 micrometers was used to study its effect on the important mechanical-strength and optical properties of paper. The effects of fly-ash addition on these properties were compared with those of kaolin clay. Paper opacity was found to be much higher with fly ash as a filler, whereas brightness decreased as the filler percentage increased Mechanical strength properties of the paper samples with fly ash as filler were superior to those with kaolin clay.
Coal fired electric power plants produce 50% of the electricity consumed in the US and generate large volumes of fly ash and other coal combustion by-products (CCBs). The majority of the CCB materials are disposed of in surface impoundments and landfills located throughout the US. Fly ash contains trace elements such as As, B, Cr, Mo, Ni, Se, Sr and V which can have a negative impact on the environment due to leaching by acid rain and groundwater with time. The potential release of these toxic trace elements into the environment is a big concern for the US power industry due to the high cost involved in lining the old and existing ash disposal sites. As a result, simple and effective treatment techniques are needed to stabilize the coal combustion by-products produced by power plants in the ash disposal sites and also to increase the use of coal fly ash for beneficial purposes. This paper reports the results of batch experiments designed to chemically treat coal fly ash with ferrous sulfate solution by promoting the formation of insoluble iron oxy- hydroxide phases that immobilize the toxic trace elements. Four fly ash samples, three acidic (HA, HB and MA) and one alkaline (PD), were treated with a ferrous sulfate (FS) solution (322 ppm Fe) and a ferrous sulfate + calcium carbonate (FS+CC) solution (322 ppm Fe and 28 ppm CaCO3) at solid:liquid ratios of 1:3 and 1:30. The effectiveness of this treatment technique was evaluated by the batch sequential leaching of treated and untreated coal fly ash samples using a synthetic acid rain (SAR) solution (USEPA Method 1312B) and also by a 7-step sequential chemical extraction procedure (SCEP) to understand the mechanism of treatment. The unbuffered FS solution at the 1:30 ratio was highly successful in reducing the mobility of the oxyanionic trace elements As (24-91%), Cr (82-97%), Mo (79-100%), Se (41-87%) and V (55-100%). However, the unbuffered FS treatment failed to reduce the mobility of B, Ni and Sr for the acidic fly ash samples. The buffered FS + CC solution greatly increased the mobility of the oxyanionic trace elements in the acidic fly ash samples, except for Cr in HA and HB fly ash. The buffered FS+CC solution reduced the mobility of all the trace elements except Ni in the alkaline PD fly ash. The ferrous sulfate treatment can be applied directly to the fresh fly ash produced in the electric power plants as well as to the fly ash already placed in the ash disposal facilities. A preliminary estimate indicates that ferrous sulfate treatment of fly ash at a power plant would be cost effective.
The mineral and chemical compositions and some trace element contents (As, Ba, Cr, Mn, Mo, Sb, Th, U and V) in coal and coalash samples from the Huaibei coal field in China were studied. This high volatility bituminous coal has low moisture and S contents, moderate ash yield and high calorific value. The coalash is abundant in aluminosilicates as the contents of the Fe oxides are relatively similar to the sum of the alkaline earth oxides. The minerals identified in the coal are mainly quartz, kaolinite, pyrite and calcite and, to lesser extents, dolomite, ankerite, illite, chlorite, opal, feldspars, marcasite, gypsum, melanterite and hematite. Common minerals in the high temperature ash (815 C) are original quartz and newly formed anhydrite, lime, hematite and Ca-Mg silicates. Some trace elements such as Cr {gt} Th {gt} V {gt} Mo in the coal (in particular Cr and Th) and Cr {gt} Th {gt} V in the coalash (in particular Cr) are enriched in comparison with the Clarke concentrations.
The stratigraphic and geographic distribution of early tonsteins in later Permian of south-western China has been systematically studied in this report. By means of contrast and research the eight seams' tonsteins characteristics of the petrography, mineralogy and geochemistry, it can be confirmed that all the tonsteins are alkaline-volcanic ash derived tonsteins from a different age. This finding has filled the record gap of alkaline-volcanic ash sediment in the coal formations of the world. Besides, it has important application value and theoretical significance. 8 refs., 4 figs., 1 tab.
In the Coal Combustion Laboratory (CCL) this quarter, controlled laboratory experiments were carried out to better understand the late stages of coal combustion and its relation to unburned carbon levels in fly ash. Optical in situ measurements were made during char combustion at high carbon conversions and the optical data were related to particle morphologies revealed by optical microscopy on samples extracted under the same conditions. Results of this work are reported in detail below. In the data presented below, we compare the fraction of alkali metal loss to that of the alkaline earth metals as a function of coal rank to draw conclusions about the mechanism of release for the latter. Figure 2.1 illustrates the fractional release of the major alkali and alkaline earth metals (Na, K, Ca, Mg) as a function of coal rank for a series of coals and for several coal blends. All data are derived from combustion experiments in Sandia`s Multifuel Combustor (MFC) and represent the average of three to eight experiments under conditions where the mass loss on a dry, ash-free (daf) basis exceeds 95 %. There are no missing data in the figure. The several coals with no indicated result exhibited no mass loss of the alkali or alkaline earth metals in our experiments. There is a clear rank dependence indicated by the data in Fig. 2.1, reflecting the mode of occurrence of the material in the coal.
The paper discusses a greenhouse experiment that was performed to evaluate the feasibility of using an artificial soil medium produced from alkalinecoal fly ash and sewage sludge for the growth of Agropyron elongatum (tall wheat grass). Sludge was amended with ash at an application rate of 0, 5, 10, 35 and 50% (w/w). Each mixture was the mixed with a loamy soil at either 1:1 or 1:5 (v/v) and incubated under greenhouse conditions for 3 weeks prior to plant growth experiment. Addition of the ash-sludge mixture significantly improved the seedling emergence and dry weight yields of Agropyron. No excessive accumulation of heavy metals was noted owing to the ash-sludge amendment. The increased yield even at a high amendment rate of 35% ash-sludge mixture at 1:1 v/v soil mixing ratio indicates the potential use of the ash-sludge mixture as an artificial soil mix for agricultural use.
Coal material Zeolitic was synthesized from fly ashes (baghouse to filter fly ash and cyclone to filter fly ash) by hydrothermal alkaline activation. The potential application of the zeolitic product will be decontamination of waters from acid mines drainage was evaluated. The results showed that the dose of 30 g material L{sup -1} of zeolitic allowed to water you reach acceptable quality levels to after treatment. Both precipitation and cation-exchange you process accounted will be the reduction in the pollutant concentration in the treated waters.
Coal-fired electric power plants in the US generated over 130 million tons of fly ash and other combustion waste materials last year. While approximately 35% of the produced coal combustion by-products (CCBs) are recycled for beneficial use, the majority of the waste is impounded in lagoons and landfills located throughout the country. The EPA is currently re-evaluating these disposal facilities for regulation under Subtitle D. The objective of this study is to determine and compare the adsorption capacities of fresh and weathered fly ash for the toxic metals arsenic, boron, chromium, molybdenum, and selenium in order to evaluate the long-term mobility of these metals in the ash disposal environment. Two power plant sites were selected for study, one producing acidic ash and the other alkalineash. Weathered ash samples were collected at each site from cores drilled from the surface through the bottom of ponds that have been closed for more than 35 years. Fresh fly ash was obtained directly from the power plants. Batch experiments were performed to study the competitive adsorption of As, B, Cr, Mo and Se on fresh and weathered ash materials. Experiments performed at pH values of 3, 4, 6, 8 and 10, using initial metal concentrations of 5 mg/L, show similar adsorption behavior for both ash compositions. The metal selectivity sequence for fresh fly ash is As >> Mo > Cr ~ Se ~ B. Maximum arsenic adsorption on fresh fly ash occurs at pH = 6 with almost 100% removal, while maximum arsenic adsorption on weathered ash takes place at pH = 3. Maximum adsorption of B, Cr, Mo and Se occurs at pH = 3 for both fresh and weathered ash. The experiments indicate that the adsorption capacity of fly ash for the metals of interest is reduced by weathering. Experiments are currently underway to compare the adsorption capacity of fresh and weathered fly ash for varying initial metal concentrations, ionic strength and solid/liquid ratio.
A pilot scale study was conducted to evaluate the effect of lime and alkalinecoal fly ash (CFA) on the reduction of pathogens in pig manure during alkaline stabilization and suppression of re-growth during post-stabilization incubation. Pig manure was mixed with CFA at 25%, 33% and 50%, and a control without fly ash was maintained. To these manure-ash mixtures, lime was added at the rate of 2% or 4% and incubated for 8 days. During the incubation, the population of Salmonella, fecal coliforms, Escherichia coli, fecal Streptococcus and total bacteria were enumerated. After the alkaline stabilization process, the mixtures were incubated under green house condition to evaluate the re-growth of pathogens. During the 8-day alkaline stabilization, Salmonella, fecal coliforms, E. coli and fecal Streptococcus were completely devitalized in manure-ash-lime mixtures, whereas in the control, incubation reduced the pathogen and total bacterial population by 2-3 logs. Fecal streptococcus was destructed within 4 days of alkaline stabilization, whereas other pathogens needed 8 days for their destruction. During the incubation in green house, an increase in the population of the pathogens and total bacteria was observed. Results indicate that alkaline stabilization of pig manure with lime at 4% and CFA at 50% is effective in devitalizing the pathogens and reducing the post-stabilization re-growth. PMID:19442442
Introduction of coal fly ash into aquatic systems poses a potential environmental hazard because of its heavy metal content. Here we investigate the relationship between solid phase transformations, fluid composition, and metal release and speciation during prolonged wet aging of a class C and class F coal fly ash. The class C ash causes rapid alkalinization of water that is neutralized over time by CO(2) uptake from air and calcite precipitation. The resulting aqueous metal concentrations are below regulatory limits with the exception of Cr; solubility constraints suggest this is released as chromate. Limited As release is accompanied by no change in solid-phase speciation, but up to 35% of the Zn in the ash dissolves and reprecipitates in secondary phases. Similar processes inhibit Ba and Cu release. In contrast, the class F ash causes rapid acidification of water and initially releases substantial quantities of As, Se, Cr, Cu, Zn, and Ba. Arsenic concentrations decline during aging because of adsorption to the iron oxide-rich ash; this is aided by As(III) oxidation. Precipitation processes lower Ba and Cr concentrations during aging. Se, Cu, and Zn concentrations remain elevated during wet aging and solid-phase Zn speciation is not affected by ash-water reactions. Total metal contents were poor predictors of metal release, which is predominantly controlled by metal speciation and the effects of ash-water reactions on fluid pH. While contact with atmospheric gases has little effect on class F ash, carbonation of class C ash inhibits metal release and neutralizes the alkalinity produced by the ash. PMID:23035817
A study has been made of the processing of the coalash leachate produced in the course of treating coalash by a combination of water and acid leaching. In wet magnetic separation experiments in which 6.7-14.5 wt% of the test material was retained by the magnet, the leachate contained Ca, Na and K. Only negligible amounts of other elements were eluted. Small quantities of heavy metals were eluted by using dilute hydrochloric acid to leach the material which was not retained by the magnet. Finally, coalash leachate processing experiments were carried out in which the alkaline leachate obtained by water leaching was gradually added to the acid leachate. This procedure enabled Al, Fe and Cr to be precipitated and removed. Elements such as Ca, Na, K, Cu and Cd remained in solution, while elements such as Mg, Zn and Si were partially separable by precipitation. 6 references.
Abstract in english The concentrations of heavy metals in two kinds of Brazilian coals at 100° C (acid digestion) and at 850° C were studied (ashes the obtained in muffle furnace with and without addition of limestone). Data were analyzed by flame atomic absorption, using the air acetylene flame. For Pb, Zn, Ni, Mn and Cu the metal concentration obtained the acid digestion were higher than metal concentration were obtained in tests in the muffle furnace. This behavior observed in the muffl (more) e furnace occurs because these metals are fixed in stable sulfated compounds in the ashes, which are difficult to dissociate at flame temperature, and also due to the volatile character of the metals, mainly Pb and Zn. There was a constant concentration in the ashes in of Cr the acid digestion and muffle furnace tests. Results from tests using an XRD apparatus indicated, he formation of sulfated compounds in the ashes for both. coals. The analysis using microprobe electronic showed retention of metals like Ni, Mn, Cu, Fe, Ti and Ca. For both coals, the low mobility of most of the metals studied occured due to the alkaline pH of sulfated ashes. These metals in the ash from coal combustion in fluidized bed reactor were also studied and showed similar results, enabling a scale-up to pilot scale.
Alkalinecoal fly ash and lime were tested for their effectiveness in pathogen removal from biosolids at different time intervals and temperatures. Coal fly ash at 10 and 35% w/w was mixed with dewatered biosolids and then the ash-biosolids mixture was mixed separately with 0, 1.1, 2.2, 4.4, 8.5, 11, and 18% calcium oxide (w/w on a dry weight basis) with and without heating to 55 degrees C. Total bacteria, salmonella, and total coliforms were monitored at various time intervals. Both ash-biosolids mixtures with or without lime amendment had a significantly lower total bacterial population than the biosolids control, but the residual indigenous bacterial flora in the ash and lime stabilized biosolids still maintained a population of greater than 10(4) g(-1) dry biosolids. Alkaline-stabilized biosolids with a lime amendment rate greater than 8.5% could maintain pH greater than or equal to 12 for more than 2 hours, which effectively removed total coliforms and salmonella in the mixture. Heat treatment to 55 degrees C and a storage time of 14 days provided an added advantage resulting in a further reduction in pathogens for all treatments. It is recommended that 10% ash-biosolids mixture should be amended with a minimum of 8.5% lime on a dry weight basis for at least 2 hours to achieve acceptable levels of salmonella and total coliforms to ensure no pathogenic risk following land application. PMID:11765997
Bottom ash from one mass-burn incinerator and one refuse derived fuel incinerator was subjected to laboratory testing and evaluation of physical and chemical properties and behavior. Testing was performed on natural bottom ash and bottom ash amended with other fine grained natural aggregates such as clay and coal fly ash. Gradation analyses show that bottom ash is similar in grain size distribution to a well-graded gravelly sand. Bottom ash has lower compacted density and specific gravity than a typical well-graded coarse grained natural aggregate but has equivalent or higher strength properties. This indicates bottom ash could be used as a structural fill. While pre- and post-processing have been used to remove ferrous particles, a significant quantity of ferrous particles remain following processing. The permeability of the bottom ash is similar to well-graded coarse grained natural aggregates but can be reduced significantly with the blending of fine-grained natural aggregates. The addition of 10 percent by weight of clay will reduce the permeability sufficiently to meet the USEPA criteria for a landfill cap/liner. Based on limited TCLP testing the bottom ash is categorized as non-hazardous under USEPA guidelines. However, batch and column leaching tests produce leachate that is alkaline and demonstrates elevated levels of soluble metals and salts. The levels of some soluble metals and chlorides in the leachate exceed USEPA drinking water standards indicating that further amending would be necessary to be able to use bottom ash outside the landfill setting.
Coal fly ash from thermal power generating stations has become a valuable byproduct in various commercial and environmental applications due to its cementitious, alkaline, and pozzolanic properties. It is used as a raw material in cement production, and also as a replacement for cement in concrete production. This study provided physical, chemical, and mineralogical characterizations of fresh and landfilled coal fly ash from a thermal generation station in Ontario. Fly ash behaviour under various environmental conditions was examined. Tests were conducted to characterize fly ash acid neutralization capacity and heavy metal sorption capacity. The study showed that fresh and landfilled fly ash samples showed significant variations in morphology, mineralogy, and chemical composition. X-ray diffraction studies demonstrated that weathering of the fly ash caused the formation of secondary minerals. The study also showed that the heavy metals from both fresh and landfilled fly ash samples were below leachate criteria set by the provincial government. It was concluded that both fresh and landfilled fly ash are suitable for various environmental and engineering applications. 55 refs., 5 tabs., 11 figs.
An overview is presented on possible mechanisms that control the leaching behaviour of the oxyanion forming elements As, Cr, Mo, Sb, Se, V and W in cementituous systems and alkaline solid wastes, such as municipal solid waste incinerator bottom ash, fly ash and air pollution control residues, coal fly ash and metallurgical slags. Although the leachability of these elements generally depends on their redox state, speciation measurements are not common. Therefore, experimental observations available in the literature are combined with a summary of the thermal behaviour of these elements to assess possible redox states in freshly produced alkaline wastes, given their origin at high temperature. Possible redox reactions occurring at room temperature, on the other hand, are reviewed because the...
Twenty-two fly ashes selected to provide a representative cross-section of coal classification and combustion techniques were analysed for physical and chemical characteristics that might indicate a potential for reaction with SO/sub 2/ in a flue gas desulphurisation process. Each ash was tested for its SO/sub 2/ removal potential as a slurry injected into a 1000 ft/sup 3//min spray dryer/fabric filter pilot plant. The reactivity of the fly ashes correlated with a combined effect of total slurry alkalinity in conjunction with the available surface area which suggested a surface-controlled reaction. The results further suggested that the utilisation of slower reacting alkaline species such as carbonate could be enhanced by a longer contact time with the flue gas such as is provided in a baghouse filter operation.
An arsenic-rich (As = 55 ppm) bituminous feed coal from the Black Warrior Basin, Alabama and its derivative fly ash (As = 230 ppm) were selected for detailed investigation of arsenic residence and chemical forms. Analytical techniques included microbeam analysis, selective extraction, and As K-edge X-ray absorption fine-structure (XAFS) spectroscopy. Most As in the coal is contained in a generation of As-bearing pyrite (FeS{sub 2}) that formed in response to epigenetic introduction of hydrothermal fluids. XAFS results indicate that approximately 50% of the As in the coal sample occurs as the oxidized As(V) species, possibly the result of incipient oxidation of coal and pyrite prior to our analysis. Combustion of pyrite and host coal produced fly ash in which 95% of As is present as As(V). Selective extraction of the fly ash with a carbonate buffer solution (pH = 10) removed 49% of the As. A different extraction with an HCl-NH{sub 2}OH mixture, which targets amorphous and poorly crystalline iron oxides, dissolved 79% of the As. XAFS spectroscopy of this highly acidic (pH = 3.0) fly ash indicated that As is associated with some combination of iron oxide, oxyhydroxide, or sulfate. In contrast, a highly alkaline (pH = 12.7) fly ash from Turkey shows most As associated with a phase similar to calcium orthoarsenate (Ca{sub 3}(AsO{sub 4}){sub 2}). The combined XAFS results indicate that fly ash acidity, which is determined by coal composition and combustion conditions, may serve to predict arsenic speciation in fly ash. 57 refs., 8 figs., 3 tabs.
In Situ Technology, Inc., ''InTech,'' has designed a new process for recovery of uranium from coal in situ. Prime objectives of the program reported herein are to reduce two uncertainties related to eventual commercialization of the process. The first uncertainty concerns appropriate field sites and their potential. The work involved laboratory tests and analysis of field samples, burning the samples to ash and leaching uranium from residual ash at laboratory scale, and burning the samples to ash and leaching uranium from residual ash at pilot plant scale. Laboratory and pilot plant tests were designed to simulate significant elements of the underground process. Field samples from New Mexico averaged 0.061% U/sub 3/O/sub 8/ and from North Dakota 0.058% of U/sub 3/O/sub 8/ in the coal, both on a dry basis. Phase I laboratory tests on New Mexico field samples were successfully conducted with no difficulties in reducing uraniferous coal to ash. Leaching tests resulted in uranium recoveries to 77.9% with acid leach and to 56% with alkaline leach. Phase II laboratory and pilot plant scale tests were successfully conducted on North Dakota field samples, but required supplemental fuel and/or enrichment for reducing uraniferous coal to ash. Acid leaching of residual ash resulted in uranium recoveries to 83.8%. Acid consumption was 71.0 pounds per ton during pilot plant scale leaching tests. The overall analysis and test program is considered to be highly successful and resulted in significant reduction of the uncertainties for eventual commercialization of the process. 3 refs.
The leaching behavior of eight specimens of fixed-bed lignite-gasification ash, including ash from the Great Plains (GPGA) plant in Beulah, North Dakota, was studied. Four batch leaching tests were used: (1) EPA-EP; (2) a test with synthetic ND groundwater; (3) ASTM D3987-81; (4) long-term (120 day). One GPGA ash was leached according to the draft TCLP protocol. The EPA-EP test leachates from all of the ashes had metal concentrations a factor of ten or more below the values that define a hazardous waste according to the RCRA criteria. The ash specimens were highly alkaline and produced pH's in the range 10-13 during tests 2-4. Leachates from the EPA-EP test had RCRA metal concentrations comparable to, or less than, those derived from combustion ash derived from the same coal. The metal concentrations in leachates from tests 2 and 3 were also well below the RCRA limits. The long-term test used liquid-to-solid ratios of 2:1 and 20:1 and deionized water. During the 120 days, at least 5% of the Na, K, Al, S (as SO4), As, Mo, Se, B, and V in the ash was extracted.
A pot experiment was conducted to investigate the boron (B) bioavailability to corn seedlings (Zea mays L) in an artificial soil mix produced from alkalinecoal fly ash and sewage sludge under greenhouse conditions. Sludge was amended with ash at an application rate of 0, 5, 10, 35 and 50% (w/w), and each mixture was then mixed with a loamy soil at either 1:1 or 1:5 (v/v). Both water soluble B (WS-B) and hot water soluble B (HWS-B) increased with an increase in the fly ash amendment rate. Plant tissue B contents also increased according to the rate of ash amendment, and at high ash application rates, more than 70% of the tissue B content was accumulated in leaves. Among the plant organs, B contents of young leaves showed a better correlation with HWS-B contents than with WS-B, and HWS-B gave a better indication on soil B availability. Boron toxicity symptoms in leaf margins were observed in 50% and 35% ash-amended sludge at 1:1 soil-mixing ratio, with shoot B reaching 225 mg kg{sup -1}. However, a significant yield reduction was observed only at 50% ash-amended sludge at 1:1 v/v, indicating that factors in addition to B might affect plant growth.
Fly ash is a by-product of coal-fired electricity generation plants. The prevalent practice of disposal is as slurry of ash and water to storage or ash ponds located near power stations. This has lain to waste thousands of hectares of land all over the world. Since leaching is often the cause of off-site contamination and pathway of introduction into the human environment, a study on the genotoxic effects of fly ash leachate is essential. Leachate prepared from the fly ash sample was analyzed for metal content, and tested for mutagenicity and genotoxicity. Analyses of metals show predominance of the metals - sodium, silicon, potassium, calcium, magnesium, iron, manganese, zinc, and sulphate. The Ames Salmonella mutagenicity assay, a short-term bacterial reverse mutation assay, was conducted on two-tester strains of Salmonella typhimurium strains TA97a and TA102. For genotoxicity, the alkaline version of comet assay on fly ash leachate was carried in vitro on human blood cells and in vivo on Nicotiana plants. The leachate was directly mutagenic and induced significantconcentration-dependent increases in DNA damage in whole blood cells, lymphocytes, and in Nicotiana plants. The comet parameters show increases in tail DNA percentage (%), tail length (mu m), and olive tail moment (arbitrary units). Our results indicate that leachate from fly ash dumpsites has the genotoxic potential and may lead to adverse effects on vegetation and on the health of exposed human populations.
Quality evaluation in coal is discussed, including such features as: combustibility; ignitability; ash loading; slagging propensity; fouling propensity; base-acid ratio in ash; total alkali; dust collectability; abrasion propensity of coal and ash; unburned carbon in ash; and use of coalash in the cement industry. Emissions such as SO{sub x}, NO{sub x}; dusts and CO{sub 2} are described for various coals. 19 figs., 13 tabs.
Fundamental tests and pelletizing tests of hardened mixtures of fly ash, cement and gypsum (FCG), plus tests of hardened coalash-slag mixtures and hardened FCG-sand mixtures are reported. The various tests have provided data of relevance to a number of areas in which coalash is used, e.g., for water-barrier materials, hardened coalash mixtures (for wave dissipating blocks, fishing reefs, etc.), in coalash disposal (with prior pelletizing) and in the solidification of harmful wastes. 1 reference.
Municipal solid waste (MSW) incineration is a common and effective practice to reduce the volume of solid waste in urban areas. However, the byproduct of this process is a fly ash (IFA), which contains large quantities of toxic contaminants. The purpose of this research study was to analyze the chemical, physical and mechanical behaviors resulting from the gradual introduction of IFA to an alkaline activated coal fly ash (CFA) matrix, as a mean of stabilizing the incinerator ash for use in industrial construction applications, where human exposure potential is limited. IFA and CFA were analyzed via X-ray fluorescence (XRF), X-ray diffraction (XRD) and Inductive coupled plasma (ICP) to obtain a full chemical analysis of the samples, its crystallographic characteristics and a detailed count ...
Under the sponsorship of the U.S. Department of Energy, the environmental impact and potential contamination from landfilled fly ash (coal conversion solid residues - CCSRs) have been studied at field sites in Ohio. The progressive increase of moisture content within pilot cells over depth and time facilitated intensive chemical processes and generation of highly alkaline (pH of 10 to 12) leachate. Chemistry of pore water from lysimeters and ASTM leachate from fly ash and soil cores indicate the leachate potential to migrate out of deposit and impact the pore water quality of surrounding soils. Na, SO{sub 4} and, particularly, K, Cl, pH, and EC appeared to be valuable indicator parameters for tracking potential leachate transport both within the cells and below the ash/soil interface.
Potential leaching of trace elements from older, unlined fly ash disposal facilities is a serious threat to groundwater and surface water contamination. Therefore, effective methods for containing the pollutant elements within the unlined coal combustion products (CCPs) disposal facilities are required to minimize any potential impact of leachate emanating from such facilities into the nearby environment. Because surfactant-modified zeolite (SMZ) has the potential to sequester both cationic and anionic trace elements from aqueous solutions, bench-scale batch and column experiments were performed to test its ability to remediate trace elements in leachates generated from both alkaline and acidic fly ash samples. Fly ash leachate treatment results showed the potential application of SMZ as a...
Short-term leaching test results of alkaline fly ash from Yenikoy coal-fired power plant were reported in this paper. ASTM D-3987-85 and TCLP-1311 test methods were applied to determine leaching behavior of selected elements namely, Fe, Ca, Cu, Co, Cd, Mn, Ni, Pb Zn, and Cr (VI) at different particle size fractions and test conditions. Chemical, mineralogical and morphological characterizations of ash samples were also performed using chemical, XRD and SEM-EDS analysis methods. The results showed that CaO dominates in the Yenikoy fly ash sample which directly affects the mobility of trace elements by determining the pH of the leaching medium. Higher mobility values of Cd, Co Cu, Pb, Ni and Zn elements were observed for TCLP-1311 procedure. The concentration of these elements in leachates s...
A simple, rapid and precise method for fluorine determination has been developed where pyrohydrolysis of the coal sample with oxygen and steam in a conventional tube furnace and absorption in alkaline solution are followed by measurements of fluorine with an ion selective electrode. Boron, beryllium and lithium were determined simultaneously by high voltage spark optical emission spectrometry (OES), however, this was not accurate for 1500 C ash samples generated in the volatility study (part 6) due to mineralogical effects, and a further method based on ash dissolution and measurement using inductively coupled plasma OES has been developed. An alternative procedure for beryllium determination is outlined using acid dissolution of ash and atomic absorption spectrophotometric measurement. 2 refs.
Zeolitic sorbents for CO2 adsorption were prepared from waste coal fly ash (FA) through hydrothermal treatment at various ratios of NaOH/FA and NaAlO2/FA, including an initial alkali fusion step. The fusion step decomposed the fly ash into very small amorphous particulate zeolite forms. The fly ash was converted to Na-P1 type with a NaOH/FA ratio of 0.5 and Na-A type with a NaAlO2/FA ratio of 0.53. The product properties were affected by the reaction temperature: Na-P1 and Na-A types were formed at 100?C. Temperatures above 140?C led to the formation of more sodalite because of the redissolving and recrystallization of zeolite crystals. Alkali metal and alkaline earth metal cations were impregnated in the synthesized Na-P1 and Na-A zeolite through an ion-exchange method. The completed zeol...
This research was carried out to study the characteristics and the potential utilization of coal fly ash-based synthetic aggregates (CSA) with oil palm waste as an alternative container substrate for ornamental-plant production. CSA only, oil palm waste only, and two mixing ratios of CSA with oil palm waste at the ratio of 1:5 and 1:10 (V/V) were utilized under this study. Zeolite was utilized as a standard substrate to compare characteristics of other substrates. The physical and chemical properties of all substrates were characterized. Scanning electron microscopy (SEM) of coal fly ash and CSA were conducted in order to study the structural configuration of the CSA. Developed CSA gave an alkaline pH (9.82), high electrical conductivity (96.1 mS m-1), high cation concentrations, high wate...
Dry alkaline flue gas desulfurization by-products (dry lime and limestone FGD scrubber ashes) including the American Electric Power (AEP) Tidd PFBC bed and cyclone ash, are being evaluated for beneficial uses via land application for agriculture, mine reclamation, and soil stabilization in a 5 year study that began December, 1990. A 1989 Battelle Memorial Institute report had recommended that the highest priority in stimulating reuse of FGD by-products was the sponsoring of in-field research of coal combustion products generated from high sulfur midwestern coals to (a) better understand and quantify the leach rate, fate and transport of sulfates and trace metals and (b) demonstrate the level of protection necessary to build public acceptance of land-based reuses.
The utilization and disposal of alkaline waste materials such as slag and coal fly ash as cement aggregates and raw materials in cement manufacturing can pose environmental and health hazards because these waste materials usually contain elevated concentration of toxic elements. This study examined the possibility of controlling the pore water chemistry of these waste materials in order to induce the secondary mineral formation of Mg-bearing minerals as major sorbing solids for oxyanions during the utilization and disposal of alkaline wastes. The formation of Mg-bearing minerals was examined at ambient temperature and alkaline pH conditions in the Mg?Si?Al system. The interaction of Mg-bearing minerals with oxyanions using arsenate as an analog was examined during and after mineral formati...
Sequential leaching experiments on coal utilization by-products (CUB) were coupled with chemical and strontium (Sr) isotopic analyses to better understand the influence of coal type and combustion processes on CUB properties and the release of elements during interaction with environmental waters during disposal. Class C fly ash tended to release the highest quantity of minor and trace elements—including alkaline earth elements, sodium, chromium, copper, manganese, lead, titanium, and zinc—during sequential extraction, with bottom ash yielding the lowest. Strontium isotope ratios ({sup 87}Sr/{sup 86}Sr) in bulk-CUB samples (total dissolution of CUB) are generally higher in class F ash than in class C ash. Bulk-CUB ratios appear to be controlled by the geologic source of the mineral matter in the feed coal, and by Sr added during desulfurization treatments. Leachates of the CUB generally have Sr isotope ratios that are different than the bulk value, demonstrating that Sr was not isotopically homogenized during combustion. Variations in the Sr isotopic composition of CUB leachates were correlated with mobility of several major and trace elements; the data suggest that arsenic and lead are held in phases that contain the more radiogenic (high-{sup 87}Sr/{sup 86}Sr) component. A changing Sr isotope ratio of CUB-interacting waters in a disposal environment could forecast the release of certain strongly bound elements of environmental concern. This study lays the groundwork for the application of Sr isotopes as an environmental tracer for CUB–water interaction.
Strongly alkaline fluidized bed combustion ash is commonly used to control acid mine drainage in West Virginia coal mines. Objectives include acid neutralization and immobilization of the primary AMD pollutants: iron, aluminum and manganese. The process has been successful in controlling AMD though doubts remain regarding mobilization of other toxic elements present in the ash. In addition, AMD contains many toxic elements in low concentrations. And, each mine produces AMD of widely varying quality. So, predicting the effect of a particular ash on a given coal mine's drainage quality is of particular interest. In this chapter we compare the results of a site-specific ash leaching procedure with two large-scale field applications of FBC ash. The results suggested a high degree of predictability for roughly half of the 25 chemical parameters and poor predictability for the remainder. Of these, seven parameters were successfully predicted on both sites: acidity, Al, B, Ba, Fe, Ni and Zn while electrical conductivity, Ca, Cd, SO4, Pb and Sb were not successfully predicted on either site. Trends for the remaining elements: As, Ag, Be, Cu, Cr, Hg, Mg, Mn, pH, Se Tl and V were successfully predicted on one but not both mine sites.
Fluidized bed combustion (FBC) is a relatively new technology that is used commercially for the combustion of coal. In Illinois, this technology is valuable because it allows the combustion of Illinois high sulfur coal without pollution of the atmosphere with vast quantities of sulfur oxides. In FBC, coal is mixed with limestone or dolomite either before injection into the combustion chamber or in the combustion chamber. As the coal burns, sulfur in the coal is oxidized to S0{sub 2} and this is trapped by reaction with the limestone or dolomite to form gypsum (CaSO{sub 4} {center_dot} 2H{sub 2}O). Solid by-products from FBC are generally a mixture of calcium oxide, gypsum, coalash, and unburned coal. The present research project is designed to provide initial data on one possible use of FBC waste. FBC wastes from five different locations in Illinois are mixed with coal slurry solids (CSS) from two different coal preparation plants at Illinois coal mines. In mixtures of FBC waste and coal slurry solids, the alkaline components of the FBC waste are expected to react with acid produced by the oxidation of pyrite in the coal slurry solid. An objective of this research is to determine the chemical composition of aqueous leachates from mixtures of FBC wastes, generated under various operating conditions, and the coal slurry solids. These data will be used in future research into the ability of such mixtures to support seed germination and plant growth. The final goal of this and future research is to determine whether mixed FBC waste and coal slurry solids can be used as a satisfactory growing medium in slurry pond reclamation. The chemical analyses of the 8 starting solids (5 FBC wastes, 2 Css samples, and 1 agricultural limestone sample) were completed.
This document summarizes microscopy study of concrete prepared from cement and fly ash (25% fly ash and 75% cement by weight), which covers coal fly ash and biomass fly ash. All the fly ash concrete has the statistical equal strength from one day to one year after mix. Scanning electron microscopy (SEM), Energy dispersive X-ray (EDX) and environmental scanning electron microscopy (ESEM) analysis show that both coal and biomass fly ash particles undergo significant changes of morphology and chemical compositions in concrete due to pozzolanic reaction, although biomass fly ash differs substantially from coal fly ash in its fuel resources. 8 refs., 17 figs., 1 tab.
...quantity, if the coalash is mixed with construction and demolition waste, the beneficial use must be authorized...chapter. Coalash mixed with municipal waste--excluding construction and demolition waste--must not be beneficially used...
The leaching behaviour of various solid residues from the semidry and the wet (gypsum-producing) flue gas desulfurization (FGD) processes at coal fired power plants has been investigated using both column and batch leaching tests in the laboratory and large scale open air lysimeter leaching tests. The purpose of the project was to provide data needed for an evaluation of the short and long term environmental impacts of disposal of these residues. The leachate produced by the semidry residues is usually alkaline and dominated by inorganic salt components. Major trace elements are Cr and Mo, As, Ba, Se and V are often present at somewhat lower concentration levels. The concentrations of most contaminants are highest at low L/S values and levels off to low concentrations as the leaching progresses. Calcium and sulfate concentrations often remain high. Use of seawater instead of fresh water for the slaking of lime in the semidry process increases the amount of sodium, chloride, calcium and potassium available for leaching from the residues. The leachate produced by the gypsum residue is a saturated solution of calcium sulfate. If the gypsum is stabilized by coal fly ash, the amount of leachable trace elements increases with increasing fly ash content. The leachability of trace elements in gypsum sludge stabilized with 30% fly ash is of the same order of magnitude as that of the gypsum residue stabilized in the same way. The trace element leachability is somewhat lower for FDG products than for coal fly ash. FGD residues containing e.g. 30% of coal fly ash appear to possess good geotechnical properties in relation to disposal. (AB) 21 refs.
Coal-based power generation is a principal source of electricity in India and many other countries. About 15-30% of the total amount of residue generated during coal combustion is fly ash (FA). FA is generally alkaline in nature and contains many toxic metals like Cr, Pb, Hg, As and Cd along with many essential elements like S, B, Ca, Na, Fe, Zn, Mn and P. Dumped FA contaminates the biosphere by mobilization of its fine particles and hazardous metals. Despite the negative environmental impact of FA, coal continues to be a major source of power production in India and therefore FA disposal is a major environmental issue. To overcome this problem, FA dumping sites have been started as a potential resource for biomass production of tree species. Phytoremediation is a strategy that uses plants...
A process for removing sulfur and ash from coal and other carbonaceous materials involving treating an aqueous slurry of coal or other carbonaceous materials at an elevated temperature below the oxidation temperature of the coal or other carbonaceous materials in the presence of an oxidizing agent capable of reducing pyritic sulfides to a soluble state with: (a) an alkaline earth metal and/or alkali metal chloride, a catalyst comprising one or more deliquescent halogen compounds, barium chloride, potassium chloride or mixtures thereof, and one or more reducing oxides, chromate salts or mixtures thereof, and an inorganic acid, or (b) a formulation comprising one or more hypochlorites and the above-described catalyst or catalyst and acid.
Abstract in english The effect of synthetic zeolites on stabilizing Zn-contaminated soil using 0.01 mol L-1 CaCl2 leaching solution in batch experiments was investigated. The zeolites were synthesized from coalash by hydrothermal treatment with alkaline solution. The additive enhanced the sorption capacity of the soil and reduced leaching. Zinc leaching was reduced by more than 80% using a minimum of 10% additive. The higher cation exchange capacity of the zeolite/soil mixtures and higher p (more) H were responsible for stabilizing Zn in soil. The poly(2-aminobenzenesulfonic acid)-coated mercury thin-film electrode was used for the determination of zinc.
Coalash is one of several industrial wastes that can be utilized as admixtures for concrete. The authors discuss the production of coalash, its properties and the current status of its use. Accounts are also given of the development and properties of hardened coalash mixtures. As an illustration of the use of such mixtures, the construction of man-made fishing reefs is described. The idea of utilizing coalash to build an artificial undersea ridge is also examined.
An investigation was conducted to determine the ability of chemical treatment to reduce the leaching of metals from fly ash. A further objective was to determine the effect of cofiring refuse-derived fuels with coal on leachate composition. Samples of fly ash were treated with portland cement, chemically pure lime, and phosphoric acid and subjected to a column leaching process. The leachates were composited weekly and analyzed using X-ray fluorescence and atomic absorption spectrometry. Portland cement or lime reduced the quantity of leached arsenic 40 to 80% from the control samples, whereas those samples fixed with phosphoric acid yielded 50 times more arsenic. Generally, the samples treated with portland cement showed the most uniform reduction in leachate concentrations. Leachates from fly ash produced upon cofiring refuse-derived fuel with coal showed consistently higher concentrations of all elements except for calcium, selenium, and alkalinity. Compaction and curing of the chemically treated ash samples showed little improvement in the ability to control the amount and types of metals appearing in leachates.
ASTM C 618 prohibits use of biomass fly ashes in concrete. This document compares the properties of biomass fly ashes from cofired (herbaceous with coal), pure wood combustion and blended (pure wood fly ash blended with coal fly ash) to those of coal fly ash in concrete. The results illustrate that with 25% replacement (wt%) of cement by fly ash, the compressive strength (one day to one year) and the flexure strength (at 56th day curing) of cofired and blended biomass fly ash concrete is statistically equal to that of two coal fly ash concrete in this investigation (at 95% confidence interval). This implies that biomass fly ash with co-firing concentration within the concentration interest to commercial coal-biomass co-firing operations at power plants and blended biomass fly ash within a certain blending ratio should be considered in concrete. 37 refs., 10 figs., 2 tabs.
Papers are presented under the headings: coal structure and properties, coal and coal derived products/NMR techniques, pyrolysis/gasification/combustion, coal and fly ash composition, beneficiation and transport, brown coal chemistry and uses, coal hydrogenation studies, hydrogenation studies, and brown coal hydrogenation - catalytic. All papers are abstracted separately.
The coal, sewage sludge, water and chemical additives are milled to produce coal-sludge slurry as a substitute for coal-water slurry in entrained-flow gasification, co-gasification of coal and sewages sludge can be achieved. The ash fusion temperature is an important factor on the entrained-flow gasifier operation. In this study, the ash fusion temperatures (DT, ST, HT and FT) of three kinds of coals (A, B and C), two kinds of sewage sludges (W1 and W2) and series of coal-sewage blends were determined, and the mineral composition during the ash melting process was analyzed by X-ray diffraction (XRD). The results showed that the ash fusion temperatures of most coal-sewage blends are lower than those of the coals and sewage sludges. The ashes have different mineral composition at different temperature during the heating process. It was found that the mineral composition of AW1 blend ash is located in the low-temperature eutectic region of the ternary phase diagram of SiO{sub 2}-Al{sub 2}O{sub 3}-CaO. The minerals found in BW1 blend ash are almost the same as those in B coalash. Kyanite is detected in CW1 blend ash, which results in the ash fusion temperatures of CW1 blend ash higher than those of C coal. We found that sodium mineral matters are formed because of NaOH added to W2, which can reduce the ash fusion temperature of coal-sewage blends. 27 refs., 6 figs., 2 tabs.
Strict interpretation of ASTM C 618 excludes non-coal fly ashes, such as biomass fly ashes from addition in concrete. Biomass fly ash in this investigation includes (1) cofired fly ash from burning biomass with coal; (2) wood fly ash and (3) blended fly ash (wood fly ash mixing with coal fly ash). A set of experiments conducted on concrete from pure cement and cement with fly ash provide basic data to assess the effects of several biomass fly ashes on the performances of freezing and thawing (F-T) and rapid chloride permeability test (RCPT). The F-T tests indicate that all fly ash concrete has statistically equal or less weight loss than the pure cement concrete (control). The RCPT illustrate that all kinds of fly ash concrete have lower chloride permeability than the pure cement control concrete. 37 refs., 5 figs.
INTRODUCTION: Flowing of the acid mine drainage may contaminate the adjacent water bodies causing substantial changes in the aquatic ecosystem. This aspect is the most relevant problem in the southern of Santa Catarina once the contaminated areas are inserted in the watershed of the Araranguá, Urussanga, and Tubarăo rivers, increasing the need for recovery studies. These areas are between Criciúma, Içara, Urussanga, Siderópolis, Lauro Müller, Orleans, and Alfredo Wagner towns where a conservation unit exist called the Environmental Preservation Area of Baleia Franca. Aiming to compare the kinetics of the ash derived from burning coal and to neutralize acid mine drainage, different neutralizer, limestone, fly, and bottom ash, was mounted on a pilot scale experiment. DISCUSSION: The transport parameters showed the same order of infiltration and dispersion: fly ash limestone. The order of measured alkalinity was: limestone limestone kinetics of acidic drainage neutralization was first order with reaction rate constant k?=?0.0963 min(-1), bottom ash was 3/4 with k?=?0.0723 mol(1/4) L(-1/4) min(-1), and the fly ash had higher order kinetics, 4/3, with reaction rate constant k?=?27.122 L(1/3) mol(-1/3) min(-1). However, by mathematical modeling, it was found that due to a combination of transport and kinetics, only limestone treatment reached a pH above 6 within 5 years, corresponding to the ideal as planned. PMID:22227807
Potential leaching of trace elements from older, unlined fly ash disposal facilities is a serious threat to groundwater and surface water contamination. Therefore, effective methods for containing the pollutant elements within the unlined coal combustion products (CCPs) disposal facilities are required to minimize any potential impact of leachate emanating from such facilities into the nearby environment. Because surfactant-modified zeolite (SMZ) has the potential to sequester both cationic and anionic trace elements from aqueous solutions, bench-scale batch and column experiments were performed to test its ability to remediate trace elements in leachates generated from both alkaline and acidic fly ash samples. Fly ash leachate treatment results showed the potential application of SMZ as an effective permeable reactive barrier (PRB) material to control the dispersion of heavy metals and metalloids from ash disposal sites. Quantitative comparison of the elemental composition of SMZ-treated and untreated leachates indicated that SMZ was effective in decreasing the concentrations of trace elements in fly ash leachates. Similarly, SMZ treatment column experiments showed the delayed peak leaching events and overall reductions in leachate concentrations of trace elements. The effectiveness of SMZ column treatments, however, decreased with time potentially due to the saturation of sorption sites. PMID:22721834
The Gas Research Institute (GRI) estimates that by the year 2010, 40% or more of U.S. gas supply will be provided by supplements including substitute natural gas (SNG) from coal. These supplements must be cost competitive with other energy sources. The first generation technologies for coal gasification e.g. the Lurgi Pressure Gasification Process and the relatively newer technologies e.g. the KBW (Westinghouse) Ash Agglomerating Fluidized-Bed, U-Gas Ash Agglomerating Fluidized-Bed, British Gas Corporation/Lurgi Slagging Gasifier, Texaco Moving-Bed Gasifier, and Dow and Shell Gasification Processes, have several disadvantages. These disadvantages include high severities of gasification conditions, low methane production, high oxygen consumption, inability to handle caking coals, and unattractive economics. Another problem encountered in catalytic coal gasification is deactivation of hydroxide forms of alkali and alkaline earth metal catalysts by oxides of carbon (CO{sub x}). To seek solutions to these problems, a team consisting of Clark Atlanta University (CAU, a Historically Black College and University, HBCU), the University of Tennessee Space Institute (UTSI) and Georgia Institute of Technology (Georgia Tech) proposed to identify suitable low melting eutectic salt mixtures for improved coal gasification. The research objectives of this project were to: Identify appropriate eutectic salt mixture catalysts for coal gasification; Assess agglomeration tendency of catalyzed coal; Evaluate various catalyst impregnation techniques to improve initial catalyst dispersion; Determine catalyst dispersion at high carbon conversion levels; Evaluate effects of major process variables (such as temperature, system pressure, etc.) on coal gasification; Evaluate the recovery, regeneration and recycle of the spent catalysts; and Conduct an analysis and modeling of the gasification process to provide better understanding of the fundamental mechanisms and kinetics of the process.
The waste low-calcium Czech brown coal fly ash represents a considerable environmental burden due to the quantities produced and the potentially high content of leachable heavy metals. The heterogeneous microstucture of the geopolymer Mn [-(Si-O)z-Al-O]nwH2O, that forms during the alkaline activation, was examined by means of microcalorimetry, XRD, TGA, DSC, MIP, FTIR, NMR MAS (29Si, 27Al, 23Na), ESEM, EDS, and EBSD. The leaching of heavy metals and the evolution of compressive strength were also monitored. The analysis of raw fly ash identified a number of different morphologies, unequal distribution of elements, Fe-rich rim, high internal porosity, and minor crystalline phases of mullite and quartz. Microcalorimetry revealed exothermic reactions with dependence on the activator alkalinit...
Based on the pot experiments, the germination rates of Zoysia Japonica planted in coalashes and in soils were examined, and then the weed protection by coal-ashes in the field planted with Zoysia Japonica was investigated in the period of lawn construction. The results indicate that the germination rate of Zoysia Japonica planted in coal-ashes with pot experiments is 83%, while that of CK is 84.33%. In field experiments, the rate of weed control by coal-ashes exceeds 96% and the favorite thickness of coal-ashes was about 2 cm. 9 refs., 1 fig., 4 tabs.
A two year investigation is being carried out to design a system for the inexpensive treatment of ash pond effluent or leachate. Twelve different coals were burned in three different types of boilers to determine the influence of coal composition, ash fusion temperatures, boiler additives, combustion conditions and co-firing of natural gas or oil with the coal, on the composition of the fly ash and bottom ash as well as the leaching and sorbate characteristics of the fly ash produced. The trace element analysis in the twelve coals and their respective fly and bottom ashes as well as surface analysis of a selected number of fly ashes using ESCA is reported. The leaching characteristics of the fly ashes with respect to pH have been defined for several trace elements. For low ash fusion coals, Sn, Ni, Mo, Cu, Cr and Mn tend to concentrate in the bottom ash, whereas Ti, Zn and Ba tend to concentrate in the fly ash. Cd, Pb and V did not show a preference. For high ash fusion coal, Sn, Sd, Pb, Mo, Cu, Cr, Ba and V concentrate in the bottom ash and Ti, Ni, Zn and Mn in the fly ash. An increase in boiler temperature favored lower concentrations of the above trace elements in the fly ash from low ash fusion coals. Smaller fly ash particles contained higher concentrations of the above trace elements than larger fly ash particles produced from the same coal. Leaching of Cd, B, Sn, Ni, Pb, Mo, Cu, Cr, Zn, Mu and Fe from the fly ash was found to be directly proportional to (1) the amount of these trace elements present, (2) decreases in pH, (3) decreases in boiler temperatures and (4) increases in ash fusion temperatures. In general fly ash particles which leached the least amount of the above elements exhibited the best sorbate characteristics.
Techniques and criteria for targeted coal exploration are discussed in relation to two fundamental coal diagrams - the Quinn Coking Coal Diagram{copyright} and the Quinn Thermal Coal Diagram{copyright}. Coal rank, petrographic composition and ash composition are combined to narrow down the search area for specific products such as hard coking coal, high ash fusion thermal coal and PCI coal. The Quinn Thermal Coal Diagram of the Bowen Basin in Australia, and the Quinn Coal Diagram for the Tavan Tolgoi coal deposit in Mongolia are discussed. 6 refs., 4 figs., 1 tab.
Twenty-four coal samples representing the four major rank types were analyzed by the x-ray RIM methodology which includes mass absorption analysis by x-ray transmission and quantitative x-ray powder diffraction. Twenty-three separate mineral species were observed in the samples, many of which could be quantified in the whole coal analysis. Several mineral species at levels of 5 wt % or less were observed only in the ashed scans. Some dehydration and reconstitution reactions were observed in the ashing process, including the combination of organically bound alkaline-earth elements and sulfur to form bassanite and magnesium sulfates. Quartz and kaolinite dominated the silicate mineral portion of the mineralogy, whereas calcite and siderite represented the carbonate; pyrite with associated sulfate oxidation products were generally present as well. The x-ray transmission studies were successful in estimating the carbonaceous matter in the whole coal samples and comparison of the reduced chemical oxides from the x-ray data with direct analyses from the Penn State data sheets revealed good correlations, although significant departures occurred for some species and a systematic underestimation of aluminum oxide from the x-ray clay peaks was observed. This study suggests that the RIM procedure can be applied to coal mineral and amorphous component analysis on a routine basis. 20 refs., 9 figs., 4 tabs.
Conventional coal fly-ash (CFA) and two coal-biomass fly-ashes (CBFAs) were obtained at a thermoelectric power station (Atikokan, Ontario) from combustion of undiluted lignite coal and co-combustion of lignite coal with up to 66% wood pellets (on a thermal basis). Fly-ashes were characterized and analyzed for use as cement admixtures. Co-combustion did not markedly change the fly-ash composition, owing to an extremely low ash content of wood pellets compared to lignite coal; toxic metals and minor elements were within ranges reported for other coal fly-ashes. All fly-ashes had losses on ignition (LOI) <1 wt% and therefore complied with ASTM LOI regulations for use in concrete. All fly-ashes contained major amorphous phases, along with quartz and periclase. Partial substitution of cement wi...
Dry alkaline flue gas desulfurization by-products (dry FGD scrubber ashes) are being evaluated for beneficial uses via land application for agriculture, mine reclamation, and soil stabilization in a 5 year, 4.4 million dollars research program based in Ohio. There are seven financial sponsors, mainly the Ohio Coal Development Office (50%) and the U.S. Dept. of Energy (25%). This paper provides a brief project overview. It includes a description of four generic dry FGD processes used in Ohio, i.e., lime injection multistage burner (LIMB) process, duct injection, calcium spray dryer and fluidized bed combustion. Work covered included: greenhouse studies on substituting alkaline FGD by-products for conventional lining materials in mine reclamation and agronomic applications; a LIMB ash stockpile study to study leachate quality; and use of LIMB ash to condition and compost sewage sludges. Field studies are planned to demonstrate the feasibility of using FGD by-products as substitutes for traditional agronomic liming materials on both crop production soils and overburden acid mine spoils. 6 refs., 7 tabs.
A western Kentucky power plant conducted a series of test burns with coal+tire-derived fuel (tdf) and coal+tire-derived fuel+petroleum coke blends. Collections of fuel, fly ash, and bottom ash/slag were made from the cyclone-fired unit under four fuel combinations: coal, coal+ca. 1% tdf, coal+ca. 3% tdf, and coal+ca. 3% tdf+petroleum coke. Fly ash carbons derived from the three fuel types can be distinguished, allowing an assessment of the impact of co-combustion on fly ash quality. While certain aspects of the ash chemistry are distinctive, Zn increasing in tdf-derived fly ash and Ni and V increasing in petroleum coke-derived fly ash, changes in the coal source between sampling dates complicate the assessment of the chemistry.
At the Preston coal mine, an underground operation in the Hoskissons seam produces a high-energy, low-ash, low-sulphur thermal coal for both local and export customers plus specialised coals for specific applications.
A range of interactions of microorganisms with coal is considered. Topics include: coal biodegradation; microorganisms and acid mine drainage; biological treatment of acid coal mine drainage; and bacteria and fly ash leaching. 68 refs.
Stable operation, in other words the achievement of a succession of uniform filtration cycles of reasonable length is a key issue in high-temperature gas filtration with ceramic media. Its importance has rather grown in recent years, as these media gain in acceptance due to their excellent particle retention capabilities. Ash properties have been known for some time to affect the maximum operating temperature of filters. However, softening and consequently ''stickiness'' of the ash particles generally depend on composition in a complex way. Simple and accurate prediction of critical temperature ranges from ash analysis--and even more so from coal analysis--is still difficult without practical and costly trials. In general, our understanding of what exactly happens during break-down of filtration stability is still rather crude and general. Early work was based on the concept that ash particles begin to soften and sinter near the melting temperatures of low-melting, often alkaline components. This softening coincides with a fairly abrupt increase of stickiness, that can be detected with powder mechanical methods in a Jenicke shear cell as first shown by Pilz (1996) and recently confirmed by others (Kamiya et al. 2001 and 2002, Kanaoka et al. 2001). However, recording {sigma}-{tau}-diagrams is very time consuming and not the only off-line method of analyzing or predicting changes in thermo-mechanical ash behavior. Pilz found that the increase in ash stickiness near melting was accompanied by shrinkage attributed to sintering. Recent work at the University of Karlsruhe has expanded the use of such thermo-analytical methods for predicting filtration behavior (Hemmer 2001). Demonstrating their effectiveness is one objective of this paper. Finally, our intent is to show that ash softening at near melting temperatures is apparently not the only phenomenon causing problems with filtration, although its impact is certainly the ''final catastrophe''. There are other significant changes in regeneration at intermediate temperatures, which may lead to long-term deterioration.
The EU regulations are restrictive with regard to solid residues and waste management. Research efforts to develop satisfying solutions are thus necessary. The GEOASH project aims, on one hand, at producing new geopolymeric matrixes using the advantageous properties of fine particles extracted from (co)-combustion fly ashes for the long-term stabilisation of inorganic hazardous wastes and, on the other, at predicting technologies for the recycling of coalashes into added-value products which could be integrated in manufacture processes, allowing a reduction of primary resources consumption. The new geopolymer matrixes produced at room temperature in moderate alkaline conditions display a compressive strength of 60-80 MPa that is not affected by the particle size of the starting fly ashes. High content of unburned carbon (10 %) in the fly ash inhibits the reactions. The higher the amorphous phases content in fly ashes the higher the polymerisation degree typical of the geopolymer framework. Additionally, fly ashes with a high SiO{sub 2}/Al{sub 2}O{sub 3} ratio require less chemical reagents to reach high compressive strength, reducing significantly the cost of the geopolymerisation. Considering the pilot plant tests performed with a semi-industrial mixer, it appears that the amounts of water and chemical reagents may be reduced at pilot plant scale without an appreciable sacrifice in the properties of the geopolymer solids. Despite the rather satisfying results obtained by the leaching tests applied to two multimetal wastes that are difficult to stabilise, such as the MSWI residues and arc furnace dust solidified/stabilised in fly ash-based geopolymer matrixes, further research is still needed. 43 refs., 44 figs., 49 tabs.
Four low-rank coals were investigated for fouling severity using bench and pilot combustion testing and microanalytical examination of fouling deposits. The coals contained varying levels of alkali and alkaline-earth elements that are commonly associated with initiating and accelerating ash fouling, including Na, Mg, K, Ca, and Fe. Combustion testing revealed that fouling deposits generated from these coals shared common chemical and physical properties. Four test coals from western US coal fields were selected, including the Beulah and Gascoyne lignites from western North Dakota and the Colstrip subbituminous coal from Montana, and the Utah Wasatch from Utah. Deposits were ranked from low-fouling to severe-fouling based on deposit build-up rate, deposit strength, and liquid-phase viscosity, which was calculated based on the chemistry and the gas temperature near the deposits at the time of quenching. Microanalysis of the deposits using scanning electron microscopy revealed that the gluing material or phase that was responsible for the cementing of the severe-fouling deposits that the gluing material or phase that was responsible for the cementing of the severe-fouling deposits was a low-melting-point sodium-calcium-rich silicate.
The enormous and worldwide production of coal fly ash cannot be durably isolated from the weathering cycle, and the weathering characteristics of fly ash must be known to understand the long-term environmental impact. The authors studied the weathering of two coal fly ashes and compared them with published data from weathered volcanic ash, it's closest natural analogue. Both types of ash contain abundant aluminosilicate glass, which alters to noncrystalline clay. However, this study reveals that the kinetics of coal fly ash weathering are more rapid than those of volcanic ash because the higher pH of fresh coal fly ash promotes rapid dissolution of the glass. After about 10 years of weathering, the noncrystalline clay content of coal fly ash is higher than that of 250-year-old volcanic ash. The observed rapid clay formation together with heavy metal fixation imply that the long-term environmental impact of coal fly ash disposal may be less severe and the benefits more pronounced than predicted from previous studies on unweathered ash. Their findings suggest that isolating coal fly ash from the weathering cycle may be counterproductive because, in the long-term under conditions of free drainage, fly ash is converted into fertile soil capable of supporting agriculture.
Boron and its compounds are environmentally hazardous substance and are well-known condensed products that appear in coal fly ash during combustion of coal in coal-fired electric power stations. In a previous study, we suggested that boron in coal fly ash obtained from Nantun coal in China, identified as Ash-N, may exist on the surface of relatively large coal fly ash particles or as very fine particles generated by homogeneous nucleation. Although the characterization of boron in coal fly ash is important for its effective stabilization or removal, its detection is quite difficult because of its low concentration in coal fly ash and its light atomic weight. In the present work, solid-state magic angle spinning nuclear magnetic resonance (MAS-NMR) technique has been applied to reveal the l...
The responses of soil algae, vascular plants, and invertebrates to soils collected along a toxicity gradient of post-mining sites were measured in laboratory toxicity tests, and the responses were compared with field pattern of communities of these organisms along this gradient. The study was performed in the Sokolov coal mining district (Czech Republic) where three types of soil materials were sampled: highly acidic coal-rich clays (pH 2.8+/-0.4), slightly acidic tertiary volcanic ashes (4.6+/-1.6), and alkaline tertiary clays (8.2+/-0.1). Laboratory tests with eight species of algae, two species of invertebrates (Enchytraeus crypticus and Folsomia candida), and one plant species (Sinapis alba) gave similar results and showed that besides low pH and the associated solubility of Al, As con...
Solids such as char, ash, and refractory organic compounds are removed from coal-derived liquids from coal liquefaction processes by the pressure precoat filtration method using particles of 85-350 mesh material selected from the group of bituminous coal, anthracite coal, lignite, and devolatilized coals as precoat materials and as body feed to the unfiltered coal-derived liquid.
Indian oxidized non coking coal is not directly suitable for High Concentration Coal Slurry (HCCS) combustion process due to its high ash content. The development of a process to produce clean coal for HCCS process using column flotation techniques and suitable reagents to recover fine particles efficiently is described. A product with 12-13% ash with recovery of 85-90% combustibles was recovered from a feed coal containing 40-42% ash. 33 refs., 4 figs., 5 tabs.
Coal-based power generation produces over 750Mt of coalash per year globally, but under 50% of world production is utilised. Large amounts of fly ash are either stored temporarily in stockpiles, disposed of in ash landfills or lagooned. Coalash is viewed as a major potential source of release of many environmentally sensitive elements to the environment. This paper encompasses over 90 publications on coal fly ash and demonstrates that a large number of elements are tightly bound to fly ash and may not be easily released to the environment, regardless of the nature of the ash. This review provides an extensive look at the extent to which major and trace elements are leached from coal fly ash. It also gives an insight into the factors underlying the leachability of elements and addresses t...
China is one of the primary coal users, and is likely to remain so. With the increase in coal use, the amount of ash generated also increases. A use for this ash has to be found and utilisation of coal fly ash has also increased. This paper describes uses for ash in Shanghai, mostly in the construction industry. Fly ash is used in concrete, in landscaping roads, in the production of building materials, and in agriculture. Research is also being performed on the uses of high calcium fly ash (HFA). 13 refs., 5 figs., 11 tabs.
The fouling potential of subbituminous coals is proportional to sodium content, tending to plateau at higher sodium levels. It increases exponentially with coalash content at all sodium levels. At similar sodium and ash levels, subbituminous coal fouling potentials are at least as great as of lignite. On the basis of samples tested and other ash survey work on Western coals, there is no evidence of the simultaneous occurrence of high sodium and high ash, a coincidental condition that would lead to high fouling in subbituminous coals. Because of this, subbituminous coals in general can be expected to show less ash fouling problems than lignite coals. In general, experience burning Western coals in Eastern boilers would indicate that samples having high sodium would give very severe fouling conditions by Eastern standards, whereas samples with low sodium would give fouling experiences comparable to the normal experience with Eastern coals.
Pilot studies are reported of the waste product utilization of power plant coalash as a building material for man-made fishing reefs. Items investigated include: 1) the strength of hardened coalash; 2) forming of the hardened ash product; 3) leaching of harmful materials; 4) behaviour of fish with respect to the reef. Although the economics and other aspects of this use of coalash have still to be studied, the present tests have yielded good results as regards strength, leaching and the attachment of organisms, thereby confirming the possibility of utilizing coalash for man-made fishing reefs. 3 references, 26 figures, 19 tables.
By-product generation from coal combustion in coal-fired thermal power plants has been increasing worldwide and reached to 125 million tons in the U.S. and 100 million tons in Europe. Coal-fired thermal power plants have a share of about 20% in Turkey's electricity production. Almost 57 million tons of coal with varying ash content of 20-55% was consumed in those plants. Uranium and thorium radioactivity of ashes of low rank coals limits the use of ashes. Consuming local bituminous coals, Catalagzi Thermal Power Station has been producing 0.65 million tons of ash including fly ash (80%) and bottom ash (20%), which have a potential use in civil engineering. The majority of the fly ash has already been used in cement or directly in concrete mortars. This study was aimed to evaluate the botto...
Paradise Steam-Electric Plant coal-fired facility in Muhlenberg County, Kentucky. This project is to construct a dredge pond near the Jacobs Creek ash pond capable of storing fly ash dredged from the ash pond. This will provide approximately 10 years of additional fly ash storage in the fly ash pond. Effluent from the dredge pond will be returned to the Jacobs Creek ash pond for discharge to Jacobs Creek. 4 figs., 5 tabs.
Rice is a plant that requires high levels of silica (Si). As a silicate NOD source to rice, coal fly ash (hereafter, fly ash), which has an alkaline pH and high available silicate and boron (B) contents, was mixed with phosphor-gypsum (hereafter, gypsum, 50%, wt wt{sup -1}), a by-product from the production of phosphate fertilizer, to improve the fly ash limitation. Field experiments were carried out to evaluate the effect of the mixture on soil properties and rice (Oryza sativa) productivity in silt loam (SiL) and loamy sand (LS) soils to which 0 (FG 0), 20 (FG 20), 40 (FG 40), and 60 (FG 60) Mg ha{sup -1} were added. The mixture increased the amount of available silicate and exchangeable calcium (Ca) contents in the soils and the uptake of silicate by rice plant. The mixture did not result in accumulation of heavy metals in soil and an excessive uptake of heavy metals by the rice grain. The available boron content in soil increased with the mixture application levels up to 1.42 mg kg{sup -1} following the application of 60 Mg ha{sup -1} but did not show toxicity. The mixture increased significantly rice yield and showed the highest yields following the addition of 30-40 Mg ha{sup -1} in two soils. It is concluded that the fly ash and gypsum mixture could be a good source of inorganic soil amendments to restore the soil nutrient balance in rice paddy soil.
Samples of coal, furnace bottom ash and pulverised fly ash were collected from the two electric companies in Hong Kong. The samples were collected over a period of 1 year and therefore they were representatives of the annual consumption of coal as well as the annual production of the ashes. Special ...
This cleanup verification package documents completion of remedial action for the 126-F-1, 184-F Powerhouse Ash Pit. This waste site received coalash from the 100-F Area coal-fired steam plant. Leakage of process effluent from the 116-F-14 , 107-F Retention Basins flowed south into the ash pit, contaminating the northern portion.
This cleanup verification package documents completion of remedial action for the 126-F-1, 184-F Powerhouse Ash Pit. This waste site received coalash from the 100-F Area coal-fired steam plant. Leakage of process effluent from the 116-F-14 , 107-F Retention Basins flowed south into the ash pit, contaminating the northern portion.
Dry alkaline flue gas desulfurization by-products (dry lime and limestone FGD scrubber ashes) including the American Electric Power (AEP) Tidd PFBC bed and cyclone ash, are being evaluated for beneficial uses via land application for agriculture, mine reclamation, and soil stabilization in a 5 year study that began December, 1990. A 1989 Battelle Memorial Institute report had recommended that the highest priority in stimulating reuse of FGD by-products was the sponsoring of in-field research of coal combustion products generated from high sulfur midwestern coals to (a) better understand and quantify the leach rate, fate and transport of sulfates and trace metals and (b) demonstrate the level of protection necessary to build public acceptance of land-based reuses (1). The specific objectives of the demonstration project are as follows: To characterize the material generated from dry FGD processes; to demonstrate the utilization of dry FGD by-products as an soil amendment material on agricultural lands and on abandoned and active surface coal mines in Ohio; to demonstrate the use of dry FGD by-product as an engineering material for soil stabilization; to determine the quantities of dry FGD material than can be utilized in each of these applications; to determine the environmental and economic impact of utilizing the material.
Brown coal samples from the Jiri surface mine in the Sokolov basin were analyzed. Content of the following elements was determined: sodium, potassium, calcium, magnesium, manganese, copper, zinc, chromium, nickel, cadmium, lead, strontium, beryllium and vanadium. Elementary composition of the initial coal samples, of ashes from coal combustion and of tetrahydrofuran coal extract was comparatively evaluated. Hazards of coal spontaneous combustion increased with increasing content of aliphatic structures in combustible coal matter. Samples of coal with highest susceptibility to spontaneous combustion were characterized by increased iron content in the tetrahydrofuran extract. Coal samples with the highest susceptibility to spontaneous combustion were characterized by increased titanium content in coalash. 9 refs.
A process is described for breaking oil-in-water emulsions formed during recovery of bitumen or heavy oil. It comprises contacting the emulsion with a high ash particulate agent selected from high ash particulate agent selected from high ashcoal rejects, fly ash from coking gas and red mud from the production of alumina.
One objective of this study was to characterize the microbial demetalization and desulfurization of coal by the bacterium Thiobacillus ferrooxidans under aerobic conditions. The effects of type of coal, coal particle size, and nutrient concentration on the bacterial leaching of coal were investigated. Ash fusion temperatures of treated and untreated coal samples were measured and an attempt was made to relate variations to the coal and ash properties. Another objective was to determine the extent of dissolution of different metals from coal residues by the action of native autotrophic bacteria under aerobic conditions. The effects of inorganic nutrient supplements were also studied. It was concluded that microbial action on bituminous coals under aerobic conditions can lead to significant reductions in inorganic sulfur, metals and total ash content, as well as considerable increase of ash fusion temperatures of the remaining ash.
Most Chinese coal is difficult to wash. Dense medium cleaning and froth flotation are being used to an increasing extent. Jig washing of unsized coal is the usual method. Fine coal may discard much of its high-ash slime in the jig, thereby reducing the froth flotation feed and its ash content. Development of improved equipment in China is discussed.
In this paper a new method and device for on-line control of ash content of coal, based on the measurement of coal natural radioactivity is presented. The article also presents the laboratory and operational tests results of the RODOS ash monitor and its usability. Examples are given using Polish Upper Silesian coals. 8 refs., 5 figs., 3 tabs.
The alkaline fusion method was used to enhance the reactivity of volcanic ash for geopolymer synthesis. To that end, different mixtures of fused soda-volcanic ash (fused volcanic ash) were used to assess reactivity for geopolymer synthesis. The amount of amorphous phase was determined both in the volcanic ash and the fused volcanic ash and X-ray diffraction analysis was used to evaluate effect of the alkaline fusion method. Different geopolymer mortars were prepared by alkaline activation of mixtures of powders of fused volcanic ash and metakaolin and river sand using sodium silicate as activator. Metakaolin was considered as consumer of excess of alkali contained in the fused volcanic ash. The geopolymer mortars were characterized by determination of setting time, linear shrinkage, compre...
Optical microscopy has been an extremely useful tool for many industrial sectors in the past. This paper introduces some of the potential applications of using coal and fly ash carbon microscopy for the combustion process and steam coal industry. Coal and fly ash carbon microscopic classification criteria are described. Plant sample data are presented which demonstrate that these techniques can be useful for coal selection and for problem solving in the coal-fired power plant environment. Practical recommendations for further study are proposed.
ABSTRACT. The aim of this paper is to demonstrate on a ... the determination of the ash content in bituminous coal [7] The ash-forming elements .... determination in water sludge [25] and for the cobalt determination in hydrocarbons';. [26] The ...
This research focuses on the valuable utilization of spray dryer ash (SDA) and investigates its performance in concrete for structural and transportation applications. Based on the challenges associated with coalash (including SDA) and the economic costs...
In this work, the pozzolanic and hydraulic properties of ashes originating from various sources were studied in model systems such as ash and ash-lime pastes. The sources of studied ashes were: fluidized combustion of brown coal, pulverized combustion of brown coal and pulverized combustion of hard coal. This article is a continuation of our previously published studies on cement pastes with mentioned ashes. The following experimental techniques were applied: calorimetry, thermal analysis (TG, DTG) and infrared absorption (IR). Previously drawn conclusions relating to the reactivity of ashes in an environment containing Ca2+ ions were confirmed. According to these conclusions, an ash originating from fluidized combustion of coal exhibited higher reactivity compared to other ashes from pulv...
Values of moisture, volatile matter and ash obtained by TGA were compared with those obtained by the ASTM methods. The standard deviations for coal were similar to the ASTM values for moisture and v.m. but higher for ash.
Estimation of perspectives for ash microspheres production at coal burning thermal power stations , development of methods for their quality certification. Creation of a database for ash microspheres in Russian Federation.
The existing use of coalash in South Africa for the management of hazardous waste is described. These include the use of fly ash extended cement in the manufacture of concrete encapsulation cells, the use of coarse ash in road making, the use of coalash as a cover material, the mitigation of hazards associated with flammable wastes and the use of coalash in the co-disposal of hazardous liquid wastes. The potential utilisation of coalash in other aspects of hazardous waste management is also described, including: lining of disposal sites, capping and sealing of waste, microencapsulation, remedial measures, mopping up spills, incineration, scrubbing in fluidised beds, zeolites and general drainage purposes. Some factors which have limited the utilisation of coalash in hazardous waste management have also been listed. 13 refs.
The clinker ash is a coalash generated by the coal-fired power station. It is characterized by its lightweight particle with asperity due to foaming during production process resulted in high shear stiffness and strength and high permeability. It is, therefore, increasingly used for the embankment material, the base course material, and the drainage material. Moreover, the application has started to be investigated for the vertical drain method and the compaction pile method. However, the physical characteristics and the mechanical characteristics of clinker ash have not been understood yet. It is expected that the stock yard for coalashes will be insufficient as production of the coalash will increase. It is necessary to use the coalash more to maintain the global environment. The design parameter for clinker ash to apply to the embankment material was experimentally investigated in this research.
This paper discusses methods of utilization of fly ash produced by fossil-fuel power plants fired by brown coal as fertilizer in agriculture. Fly ashes from 3 major brown coal basins in Poland are investigated: Konin, Turow and Belchatow. Fly ash of Konin brown coal is superior to the two others. Fly ash of Konin brown coal is characterized by a high content of calcium and magnesium oxides, about 30% and 40% respectively. Konin fly ash can be used as an efficient means of soil neutralization. It also has a high content of useful mineral components and can be efficiently used as a mineral fertilizer. Addition of Konin fly ash to soil increases content of exchangeable cations. Fly ash mixed together with run-of-mine brown coal fertilizes the soil with such components as calcium, magnesium, sulfur, iron and manganese. (5 refs.)
We used a suite of techniques to characterize the mineralogy, geochemistry, and arsenic speciation in lagooned combustion waste (ash) from coal burning and ash buried under agricultural soil since 1965 when a dam of one of the ash ponds failed. Coal seams from Novaky (Slovakia) contain low-temperature hydrothermal mineralization with orpiment (As2S3). The lagooned ash waste has 1000-1400ppm As and consists of vesicular and compact glasses (86.29% of the ash with an average of 0.13wt.% As2O5), spheroidal glasses (2.53% of the ash; 1.35wt.% As2O5), unburned coal particles (7.76% of the ash; 0.10wt.% As2O5) with calcite veins (0.27% of the ash; 1.60wt.% As2O5), as well as quartz, plagioclase, and traces of poorly crystalline mullite (3.15% of the ash; 0.01wt.% As2O5). The major As carriers ar...
Sonochemical decomposition of hydrazine in aqueous suspension of coalash particles was investigated in the different pH solutions. It was clearly found that the initial rate of hydrazine decomposition and adsorption is strongly dependent on the amount of coalash and pH. At pH 1, the amount of the hydrazine adsorption on coalash was very small and hydrazine was mainly decomposed by ultrasonic irradiation. At pH 4, hydrazine was mainly adsorbed on coalash and not decomposed by ultrasonic irradiation. At pH 8, the sonochemical decomposition and the adsorption on coalash proceeded simultaneously. These results were due to the interactions between the degree of the protonation of hydrazine, the electric charge of coalash and the amount of OH radicals formed in the sonolysis of water.
Granulated coalash was used to restore water environment in a brackish-water lake, Nakaumi, Japan, whose sediment was heavily deteriorated with organic substances. Number of bivalves, Tapes japonica and Scapharca subcrenata, which were important fisheries resources, were significantly recovered 2-3 years after the granulated coalash covering. Oxydation-reduction potential of the amended sediment with the coalash was significantly high compared to those with natural sand. Dissolved oxygen concentration in the overlying water was also high at the coalash amendment site. This means, the sediment oxygen consumption was depressed by covering with the granulated coalash. From these results, granulated coalash can be effective to restore water environment and bivalve habitat by amending the organically-enriched sediments.
Elemental analysis of coalash is routinely carried out using a variety of modern instrumental techniques. Most commonly X-ray fluorescence spectrometry (XRF), inductively coupled plasma emission spectrometry (ICP-AES) and atomic absorption spectrometry (AAS) techniques are used for the analysis of elements present in coalash at major and minor levels. ICP-AES, AAS and inductively coupled plasma mass spectrometry (ICP-MS) techniques are routinely used for the determination of trace elements in coalash. Standard methods of coalash elemental analysis have been developed by for example, Standards Australia - AAS methods and ASTM - AAS methods. Standards Australia is currently drafting a standard method for the analysis of coalash using XRF. This paper briefly outlines the principles of the most common methodologies and discusses the need for regular inter-laboratory test programs to maintain the quality of coalash elemental analyses. (author). 1 tab., 6 refs.
To use fly ash and coal waste effectively, the current technologies for reprocessing and recycling these wastes into eco-building materials were reviewed, such as utilizing fly ash as the component of fly ash cement and low heat cement after the processes of separation, removal of carbon remains and fine comminution, calcining coal waste into kaolin and meta-kaolin with suspension technology, and preparing clinkerless alkali-activated geopolymer materials with fly ash and meta-kaolin.
This report contains the results of an investigation of 11 fly ashes, obtained from pulverized-coal-fired furnaces of various designs and located in different parts of the United States. Seven of the fly ashes were the combustion products of bituminous coals; three fly ashes came from subbituminous coal; and the remaining specimen from lignite coal. The calcium oxide content of the fly ashes from bituminous coals was less than 7%; that of the other fly ashes varied from about 15 to 27%. The silicon dioxide/aluminum oxide ratio in the 11 fly ashes ranged from 1.45 to 2.80. The purpose of this investigation was to obtain complete physical-chemical characterization data on the fly ashes and to correlate these characteristics with (1) the coal source and furnace type, and (2) the performance of the fly ash in portland cement-fly ash mortars. The performance of a given fly ash in portland cement-fly ash mixtures was found to be independent of the coal source and furnace design. The calcium content and particle size distribution of the fly ash were judged the two most important parameters determining the relative reactivity of the fly ashes. ASTM procedures for classifying fly ashes and testing their pozzolanic activity did not prove useful in evaluating the performance characteristics of the fly ash in portland cement mortars. New test procedures are recommended for assessing the relative reactivity of different fly ashes when a fly ash is to be used as mineral admixture in portland cement concrete. 4 references, 19 figures, 8 tables.
The waste low-calcium Czech brown coal fly ash represents a considerable environmental burden due to the quantities produced and the potentially high content of leachable heavy metals. The heterogeneous microstucture of the geopolymer M(n) [-(Si-O)(z)-Al-O](n).wH(2)O, that forms during the alkaline activation, was examined by means of microcalorimetry, XRD, TGA, DSC, MIP, FTIR, NMR MAS ((29)Si, (27)Al, (23)Na), ESEM, EDS, and EBSD. The leaching of heavy metals and the evolution of compressive strength were also monitored. The analysis of raw fly ash identified a number of different morphologies, unequal distribution of elements, Fe-rich rim, high internal porosity, and minor crystalline phases of mullite and quartz. Microcalorimetry revealed exothermic reactions with dependence on the activator alkalinity. The activation energy of the geopolymerization process was determined as 86.2kJ/mol. The X-ray diffraction analysis revealed no additional crystalline phases associated with geopolymer formation. Over several weeks, the (29)Si NMR spectrum testified a high degree of polymerization and Al penetration into the SiO(4) tetrahedra. The (23)Na NMR MAS spectrum hypothesized that sodium is bound in the form of Na(H(2)O)(n) rather than Na(+), thus causing efflorescence in a moisture-gradient environment. As and Cr(6+) are weakly bonded in the geopolymer matrix, while excellent immobilization of Zn(2+), Cu(2+), Cd(2+), and Cr(3+) are reported. PMID:19303704
The leaching of inorganics including heavy metals from coalashes has recently received extensive attention. This study was undertaken to understand the rate of leaching of metals from coalash and the significant factors affecting the rate, and to develop an approach to predict leaching rates. The rate of leaching of zinc was characterized quantitatively for one coal bottom ash using a pseudokinetic mechanism. The resulting rate constants were correlated over a pH range of 1.3-9.3.
The leaching of inorganics including heavy metals from coalashes has recently received much attention. This study was undertaken in order to understand the rate of leaching of metals from coalash and the significant factors affecting the rate, and to develop an approach to predict leaching rates. The rate of leaching of Zn was characterised quantitatively for one coal bottom ash using a pseudo-kinetic mechanism. The resulting rate constants were correlated over a pH range of 1.3 - 9.3.
The utilization of fly ash would be greater and more versatile if it could be substantially freed from coal (unburned carbon) particles. Representative sample of the fly ash for this study was obtained from Soma Power Plant, Turkey. Flotation of Soma Power Plant fly ash sample to recover coal (unburned carbon) particles gave a coal fraction of 37.56% ash with 65.06% burnable yield at conditions: pH 6.0, 30{degree}C and 6.24 l/t concentration of kerosene + pine oil. The effects of pH, temperature and concentration of reagents on the flotation of fly ash was investigated. 9 refs., 3 figs., 2 tabs.
The report gives results of research to: (1) develop methodology for the field-collection of coal-ash leachate; (2) chemically characterize ash leachates from power plants using different coal sources; (3) determine the characteristics of the hydrogeochemical environment in which the leachate occurs; and (4) determine the attenuation of coal-ash leachate by various soil types. Groundwater monitoring wells were installed around ash ponds at two TVA plants. Continuous soil-core samples were collected and analyzed periodically. Ash leachate was percolated through different clays and soils to study attenuation rates.
This paper reviews apparatus developed by Soviet research institutes to determine coalash content under laboratory and operational conditions as well as for express information on ash content in coal moving on a belt conveyor. The following aspects are reviewed: design, construction, capacity, principle of operation, accuracy, errors, dimensions, weight, energy consumption, maximum grain size and moisture content in coal, maximum thickness of the coal layer, duration of analysis. Block schemes of some of the apparatus are also given. The ZAR-2 automated X ray ash meter determines ash content with error not exceeding 0.5%, the BRA-9 fluorescent X ray analyzer determines ash content with error not exceeding 0.5% and sulfur content with error not exceeding 0.3%. The RKT-2 radioisotopic ash meter (using gamma absorption method) determines ash content in laboratory samples of coal with grain size up to 3 mm and weight up to 0.6 kg. The EhAZ express analyzer developed by the Skochinski Institute determines ash content in 3 minutes in a 7 kg coal sample with coal grains up to 25 mm in diameter and moisture content up to 15%; maximum error does not exceed 5%. Five ash meters developed for continuous measurement of ash content in a coal layer moving on a belt conveyor are also evaluated: RAM-1M, RKTP-1, RKTP-2, RKTP-3 and VSKZ-1. (20 refs.) (In Russian)
Low-rank coals can be processed into non-fouling coal, ultra-low ashcoal, and coals containing catalysts. Systematic studies of the action of acid to reduce ash in a number of low-rank coals have shown total ash reduction varied from 96% to 30%; the extent of ash reduction was limited by the nature of minerals, which may be removed using various acids, including HF, to produce ultra-low ashcoal. A commercial process must operate at elevated temperatures, but this must not produce toxic wastewater; data are provided to show that wastewater may be treated and water recycled without polluting the environment. The addition of effective catalysts results in enhanced reactivity of the coal to oxygen and steam; experimental data show high yield of H2 from char and steam, and accompanying post-g...
With the aim of utilizing pulverized coal combustion ash (obtained from coal-fired power stations) as a soil improver for agricultural land, potatoes, spinach, Japanese radishes and soya beans were grown in volcanic ash soil with up to 50% coalash admixture. At mixing ratios of 10-30%, soil pH, EC and concentrations of Ca and B increased, and faster growth and greater yields of crops were obtained. This improvement is thought to be due to the addition of coalash resulting in 1) adjustment of soil pH level, 2) accelerated absorption of elements essential to growth (B, Mo) and 3) an increase in the available moisture. 32 references.
Most electricity in the world is conventionally generated using coal, oil, natural gas, nuclear energy, or hydropower. Due to environmental concerns, there is a growing interest in alternative energy sources for heat and electricity production. The major by-products obtained from coal combustion are fly ash, bottom ash, boiler slag, and flue gas desulfurization (FGD) materials. The solid wastes produced in coal-fired power plants create problems for both power-generating industries and environmentalists. The coal fly ash and bottom ash samples may be used as cementitious materials.
Most electricity in the world is conventionally generated using coal, oil, natural gas, nuclear energy, or hydropower. Due to environmental concerns, there is a growing interest in alternative energy sources for heat and electricity production. The major by-products obtained from coal combustion are fly ash, bottom ash, boiler slag, and flue gas desulfurization (FGD) materials. The solid wastes produced in coal-fired power plants create problems for both power-generating industries and environmentalists. The coal fly ash and bottom ash samples may be used as cementitious materials.
Literature is reviewed on the effects which trace elements contained in coalash may have on ruminants, the aim being to assess the use of ground reclaimed with coalash for grazing domestic animals or for growing fodder crops. It is reported that the trace elements absorbed directly by domestic animals amounts to 1-18% of the total dry solids. When grass grown in soil with coalash admixture is added to the feed, levels of selenium in the blood of ruminants increase slightly. The same increase in selenium occurs when coalash is added directly to the feed. No adverse effects were detected in the latter case. 64 references.
This report presents an overview of investigations into the fly ash formation and sulphation process that occurs when brown coal is burnt. A code has been developed to simulate the chemistry of ash formation. The results of this project show that for the coals considered the chemistry of sodium species in a coal flame is central to the ash formation and fouling. Aluminium based additives have been tested on two Loy Yang coals. The tests show that the additives exert a pronounced influence on ash formation, probably via changes in the heterogeneous condensation of sodium compounds.
Contents: The Chemical Analysis of Argonne Premium Coal Samples: An Introduction; Rehydration of Desiccated Argonne Premium Coal Samples; Determination of 62 Elements in 8 Argonne Premium CoalAsh Samples by Automated Semiquantitative Direct-Current Arc Atomic Emission Spectrography; Determination of 18 Elements in 5 Whole Argonne Premium Coal Samples by Quantitative Direct-Current Arc Atomic Emission Spectrography; Determination of Major and Trace Elements in Eight Argonne Premium Coal Samples (Ash and Whole Coal) by X-Ray Fluorescence Spectrometry; Determination of 29 Elements in 8 Argonne Premium Coal Samples by Instrumental Neutron Activation Analysis; Determination of Selected Elements in CoalAsh from Eight Argonne Premium Coal Samples by Atomic Absorption Spectrometry and Atomic Emission Spectrometry; Determination of 25 Elements in CoalAsh from 8 Argonne Premium Coal Samples by Inductively Coupled Argon Plasma-Atomic Emission Spectrometry; Determination of 33 Elements in CoalAsh from 8 Argonne Premium Coal Samples by Inductively Coupled Argon Plasma-Mass Spectrometry; Determination of Mercury and Selenium in Eight Argonne Premium Coal Samples by Cold-Vapor and Hydride-Generation Atomic Absorption Spectrometry; Determinaton of Carbon, Hydrogen, and Nitrogen in Eight Argonne Premium Coal Samples by Using a Gas Chromatographic Analyzer with a Thermal Conductivity Detector; and Compilation of Multitechnique Determinations of 51 Elements in 8 Argonne Premium Coal Samples.
24 papers were presented. Those covering coal included: the PTC process for agglomerating carbonaceous fines; encapsulation of toxic waste materials by fly ash agglomeration; emission screening of coal/sorbent fuels; physical characteristic measurements for reconstituted coal pellets; pelletising and reslurrying characteristics of ultrafine coal; extrusion of coal logs with coal-asphalt mixtures; chemomechanical weakening of materials; and binderless briquetting of peat, lignite, subbituminous and bituminous coal in roll presses.
The co-combustion of biomass with coal by utilities offers a means of reducing CO{sub 2} emissions and achieving the UK Government's renewable energy targets. Co-firing of biomass with pulverised coal is now common in UK utility boilers, with levels of replacement of coal by biomass steadily increasing. Although biomass supply and handling present major problems, the impact of the inorganic component of the biomass on boiler ash behaviour is also a cause for concern. Biomasses typically have lower inorganic contents than coals, but the biomass ashes have very different chemical compositions from coalashes - the alkali components in the biomass affect the deposition behaviour of the mainly aluminosilicate coalash. A wide range of biomasses have been mixed with typical power station bituminous coals at replacement levels of up to 60wt%. The coal-biomass mixtures have been combusted on the entrained flow reactor at Imperial College; deposit samples have been collected and their chemical composition and microstructure characterised. The results indicate that both the biomass ash chemistry and ash content are important in determining the effect of biomass co-firing on coalash deposition. Calculated ash viscosities can be used to compare the degrees of sintering of deposits from different coal-biomass mixtures. Although no two biomasses are the same, biomasses can be grouped together in terms of their impact on boiler deposition. 2 refs., 5 figs., 7 tabs.
A technique for effectively utilizing coalash generated by coal thermalpower stations is described. It consists of adding lime and plaster to coalash and curing their mixture with water using steam to form a hard mass. Its features are as follows: (1) Both coalash and waste plaster generated by coal thermal power stations can be utilized. (2) Coalash particles are combined with (3CaO.Al/sub 2/O/sub 3/.3CaSO/sub 4/.32H/sub 2/O) produced by the reaction between alumina contained in coalash and added lime and plaster; therefore, coalash is formed into a hard mass. The pH of the solution of liquified coalash is low, and the heavy metal content is also low. (3) Processing cost is low, and coalash may assume various forms depending on the processing condition: slurry, powder, or mass. Possible applications including deep and shallow ground improvement, base, buried, artificial fish gathering, absorbing, and construction materials. (24 figs, 5 tabs, 3 refs)
Emissions of B, Br, Cl, F, Hg and Se from pulverized coal-fired power plants in The Netherlands have been investigated in order to be able to estimate possible environmental consequences. Gas samples were taken from the flue gas down-stream of the electrostatic precipitators using activated charcoal cartridges and impingers (for F and Cl) at 120 C. Apart from direct gas measurements volatile emissions can be deduced from balance studies. The imbalance between ingoing coal and outgoing ash streams could then be assigned to vapor phase emissions. Another approach is to compare the concentration of an element in the coalash with the concentration in the bottom ash, collected ash and fly ash, assuming coalash is divided over these ash streams in a ratio of 10%, 90% and 0.1% respectively. Analyses were carried out by means of neutron activation analysis and standard chemical procedures. Results are presented. 3 tabs., 3 refs.
In this literature report is provided a status for the present knowledge level on ash properties when co-firing coal and biomass. The fly ash formed in boilers using co-firing of coal and straw do have a large influence on ash deposit formation, boiler corrosion, fly ash utilization and operation of flue gas cleaning equipment. This survey includes discussions on the inorganic constituents transformation during straw and coal combustion, alkali-ash and alkali sulfur reactions, a survey of power plant and test rig co-firing experiments, a discussion of equilibrium calculations, a discussion of alkali getter experiments and a discussion of modeling of alkali reaction with kaolin. Presently there is still a need for a better understanding of especially the reaction of potassium with coalash, thereby making better predictions of co-firing ash properties.
A large volume of fly ash is produced that does not meet current American Society for Testing and Materials (ASTM) specifications for use in the production of cement and concrete but could be used for other applications. In many cases, coalash is required to meet ASTM specifications even when they are clearly inappropriate for the application (i.e., structural fill). Creating a classification system for fly ash that facilitates the use of performance-based specifications for use applications will broaden the utilization options for coalash, resulting in elimination of disposal costs and opportunities for industry to develop new products and expand the use of coalash in existing products. The inadequacy of the current classification system is one of the major technical barriers to increased coal by-product utilization. The goal of this project is to develop a classification system for fly ash that will provide a means of evaluating fly ash suitability for applications.
Malodor emissions limit public acceptance of using municipal biosolids as natural organic resources in agricultural production. We aimed to identify major odorants and to evaluate odor concentrations associated with land application of anaerobically digested sewage sludges (Class B) and their alkaline (lime and coal fly ash)-stabilized products (Class A). These two types of biosolids were applied at 12.6 tonnes ha(-1) (dry weight) to microplots of very fine clayey Vertisol in the Jezreel Valley, northern Israel. The volatile organic compounds (VOCs) emitted from the biosolids before and during alkaline stabilization and after incorporation into the soil were analyzed by headspace solid-phase microextraction followed by gas chromatography-mass spectrometry. Odor concentrations at the plots were evaluated on site with a Nasal Ranger field olfactometer that sniffed over a defined land surface area through a static chamber. The odors emitted by anaerobically digested sewage sludges from three activated sludge water treatment plants had one characteristic chemical fingerprint. Alkaline stabilization emitted substantial odors associated with high concentrations of ammonia and release of nitrogen-containing VOCs and did not effectively reduce the potential odor annoyance. Odorous VOCs could be generated within the soil after biosolids incorporation, presumably because of anaerobic conditions within soil-biosolids aggregates. We propose that dimethyl disulfide and dimethyl trisulfide, which seem to be most related to the odor concentrations of biosolids-treated soil, be used as potential chemical markers for the odor annoyance associated with incorporation of anaerobically digested sewage sludges. PMID:21869502
The feasibility of using ash-free coal as the fuel in a direct carbon fuel cell (DCFC) was investigated. Tubular-electrolyte-supported single cells were operated at high temperatures with continuous fuel feeding equipment. A single cell consisted of an yttria-stabilized zirconia (YSZ) electrolyte tube support, a NiO-YSZ cermet anode, and an LSM-YSZ composite cathode. The solvent extraction method was used to remove mineral matter and ash from raw coal. From thermal gravimetric analysis, the ash content of the ash-free coal was found to be nearly zero, but its volatile matter content was 38.34 wt.%. Scanning electron microscopy (SEM) observations and visualization tests were carried out for characterization of the interface of the ash-free coal; the results showed that the ash-free coal was...
The effect of coal fly ash on nutrient transformations during sludge composting co-composting sewage sludge with coal fly ash was evaluated by co-composting sewage sludge with coal fly ash. Dewatered anaerobically-digested sewage sludge was mixed with sawdust used as a bulking agent at 2:1 (w/w), and the mixtures were amended with coal fly ash at 0, 10, 25 and 35% and composted for 100 days. Addition of coal fly ash raised the pH of the sludge compost throughout the composting period; but significant inhibition of decomposition activity occurred only at 35% ash amendment level. Soluble organic carbon and total C decreased according to composting time, whereas total N showed an opposite trend for all treatments.
The boron content in un-oxidised and weathered coals from E. Siberia was found to fluctuate between 210 and 1620 g/t. The knowledge is useful for cases where the coalash is to be used in agriculture.
The chemical compositions and trace element contents (Zn, Cu, Co, Cr, Ni, Pb, Cd, As, B, Hg, Sr, Se, Be, Ba, Mn, Th, V, U) in coal and coalash samples from Tamnava-Zapadno Polje coal field in Serbia were studied. The coal from this field belongs to lignite. This high volatility coal has high moisture and low S contents, moderate ash yield, and high calorific value. The coalash is abundant in alumosilicates. Many trace elements such as Ni > Cd > Cr > B > As > Cu > Co > Pb > V > Zn > Mn in the coal and Ni > Cr > As > B > Cu > Co = Pb > V > Zn > Mn in the coalash are enriched in comparison with Clarke concentrations.
The chemical compositions and trace element contents (Zn, Cu, Co, Cr, Ni, Pb, Cd, As, B, Hg, Sr, Se, Be, Ba, Mn, Th, V, U) in coal and coalash samples from Tamnava-Zapadno Polje coal field in Serbia were studied. The coal from this field belongs to lignite. This high volatility coal has high moisture and low S contents, moderate ash yield, and high calorific value. The coalash is abundant in alumosilicates. Many trace elements such as Ni > Cd > Cr > B > As > Cu > Co > Pb > V > Zn > Mn in the coal and Ni > Cr > As > B > Cu > Co = Pb > V > Zn > Mn in the coalash are enriched in comparison with Clarke concentrations.
A method of making prosopis wood rice husk white coal is described. Such white coal offers advantages like gum utilization, good holding strength, tolerable ash content, and desirable combustion characteristics.
The report is a compilation of environmental characterization data for wastewaters from low- and medium-Btu coal gasification facilities. Fixed-bed, entrained-bed, and ash-agglomerating fluidized-bed coal gasification processes were examined. The fixed-bed gasifiers are the Chapm...
Coalash, and particularly fine fly ash, remain one of the principal practical and environmental problems in coal-based power generation. In particular, submicron aerosols are identified with direct inhalation risk. Submicron ash is thought to arise from mineral vaporization during char combustion, followed by nucleation, condensation and coagulation to yield an aerosol. While aerosols are predominantly made out of volatile alkali minerals, they also can include refractory oxides that are chemically reduced to more volatile forms within the char particle and vaporized. Most of the ash of size greater than 1 {mu}m is generated by agglomeration of mineral as the char particle bums out. These two principal mechanisms are thought to account for most of the ash generated in coal combustion. Previous research has shown that various forms of coal treatment can influence the yields of fine ash from combustion. The research reported here investigates various forms of treatment, including physical coal cleaning, aerodynamic sizing, degree of grinding, and combinations of these on both aerosol yields and on yields of fine residual ash (1-4 {mu}m). The work also includes results from the combustion of artificial chars that include individual mineral elements. This research shows that these various forms of coal treatment can significantly change ash characteristics. While none of the treatments affected the bulk of the residual ash size distribution significantly, the yield of the ash aerosol mode (d<0.5 {mu}m) and fine residual ash mode (1-4 {mu}m) are changed by the treatments.
The nature of mineral matter in coal determines its transformation into ash during combustion and the nature of resulting ash, (eg chemical composition and particle size distribution), and subsequently influences the ash deposition behaviour. The conventional indices for ash deposition based on the chemical composition of ash and the Ash Fusion Temperatures did not prove to be adequate due to the heterogeneous nature of mineral matter. The paper discusses two new techniques required for estimating the performance: the Computer Controlled Scanning Electron Microscopy (CCSEM) and Thermo-Mechanical Analysis (TMA). The behaviour of mineral matter is primarily influenced by three parameters: the mineral type (quartz, siderite, calcite or pyrites), grain size, and whether the mineral grains are within the coal matrix or not. CCSEM of coal provides such information on mineral matter in coal. CCSEM data are, therefore, processed to predict the fouling and slagging characteristics of several coals. TMA describes thermal behaviour of ash deposits over complete range of temperature and gives much more information compared to what standard Ash Fusion Temperatures provide. The analysis from such a technique can be used to characterise the ash deposits in terms of their structure and thermal properties. The two techniques together with the thermodynamic calculations have capabilities of characterising coal in terms of their ash depositional behaviour and the resulting ash deposits in terms of their structure. 22 refs., 4 figs.
Results from recent UK chromium XAFS analysis of several coal and ash samples are reported. Illinois No. 6 parent coal, Illinois NO. 6 physically beneficiated coal, and two coals from the Penn State Coal Bank (DECS-2 and DECS-12), were found to contain chromium in the +3 oxidation state. No evidence for the carcinogenic and toxic +6 oxidation state (i.e., CrO{sub 4}{sup {minus}2}) was found. Ash samples were generated from each of these coals in a PSIT laboratory scale reactor at 1500{degrees}C and 7% oxygen. Subsequent XAFS analysis of these ash samples also identified only Cr+3 in the ash. As discussed further in Section 3, if the results of this study can be considered general for bituminous coals, then the absence of the (+6) chromate state in both the coal and the ash implies that the hazard posed by chromium in coal combustion is small, absent high concentrations of chromium in the ash (> 100 ppM). Of the two major oxidation states of chromium, the CrO{sub 4}{sup {minus}2} oxidation state can be both toxic and carcinogenic, whereas the Cr{sup 3+} oxidation state at such low concentration levels (< 100 ppM) does not pose a significant health risk. If the results of this study can be considered to be general, then the absence of the chromate state in both coal and combustion ash would imply that the hazard posed by chromium in coal utilization is minimal.
Results from recent UK chromium XAFS analysis of several coal and ash samples are reported. Illinois No. 6 parent coal, Illinois NO. 6 physically beneficiated coal, and two coals from the Penn State Coal Bank (DECS-2 and DECS-12), were found to contain chromium in the +3 oxidation state. No evidence for the carcinogenic and toxic +6 oxidation state (i.e., CrO{sub 4}{sup {minus}2}) was found. Ash samples were generated from each of these coals in a PSIT laboratory scale reactor at 1500{degrees}C and 7% oxygen. Subsequent XAFS analysis of these ash samples also identified only Cr+3 in the ash. As discussed further in Section 3, if the results of this study can be considered general for bituminous coals, then the absence of the (+6) chromate state in both the coal and the ash implies that the hazard posed by chromium in coal combustion is small, absent high concentrations of chromium in the ash (> 100 ppM). Of the two major oxidation states of chromium, the CrO{sub 4}{sup {minus}2} oxidation state can be both toxic and carcinogenic, whereas the Cr{sup 3+} oxidation state at such low concentration levels (< 100 ppM) does not pose a significant health risk. If the results of this study can be considered to be general, then the absence of the chromate state in both coal and combustion ash would imply that the hazard posed by chromium in coal utilization is minimal.
The paper compiled the papers presented in the 6th Conference on Coal Utilization Technology held in September 1996. With relation to the fluidized bed boiler, reported were Field operation test of Wakamatsu PFBC combined cycle power plant and Development of pressurized internally circulating fluidized bed combustion technology. Regarding the coal reformation, Development of advanced coal cleaning process, Coal preparation and coal cleaning in the dry process, etc. Concerning the combustion technology, Study of the O2/CO2 combustion technology, Development of pressurized coal partial combustor, etc. About the CWM, Development of low rank coals upgrading and their CWM producing technology, Technique of CWM distribution system, etc. Relating to the coalash, Engineering characteristics of the improved soil by deep mixing method using coalash, Employment of fluidized bed ash as a basecourse material, On-site verification trials using fly ash for reclamation behind bulkheads, Water permeabilities of pulverized fuel ash, Separation of unburned carbon from coal fly ash through froth flotation, Practical use technology of coalash (POZ-O-TEC), etc
In this study, we focused on optimizing a part of the furnace and operating conditions of the fiber yielding system from fused coalash to expand ash utilization for building materials; promotion of ash use is desirable because slag inhibits the elution of toxic heavy metals, such as Hg, Pb and As, to undetectable levels, making the fibers safe to use. In particular, the fiber materials from coalash slag are expected to be used as thermal insulators and acoustic materials. We designed a coalash fusing furnace which is suitable for the fiber manufacturing and recovery process. To manufacture fiber materials which are both safe and homogeneous, the slag viscosity had to be stabilized to approximately 1 Pa·s at the slag-tapping hole of the furnace. However, the slag temperature at 1 Pa·s was too high to measure. Thus, we estimated the slag temperature at 1 Pa·s using Riboud’s and Urbain’s expressions. To control the slag viscosity and temperature, CaCO3 addition to coalash was effective. When the basicity (CaO/SiO2(wt%/wt%)) of the coalash sample was 0.98, the fused slag temperature at 1 Pa·s was estimated as 1563 °C. Then, we verified that to yield 1 Pa·s fusing slag from 120 kg/h coalash, the necessary fuel quantity of the coalash fusing furnace was 40 kg/h coal and 4 m3N/h LPG.
This project comprised laboratory and large scale lysimeter studies of the leaching properties of coal fly ashes and flue gas desulphurisation (FGD) products from the spray dryer absorption (SDA) process, laboratory and lysimeter investigations of the mobility of two key components, Cr(VI) and Mo(VI), of coal combustion residue leachates in soils, simulation of the migration of Cr(VI) and Mo(VI) in soil using numerical modelling of laboratory results, field investigations at an old coal fly ash disposal site, and theoretical calculations of ageing processes of coal fly ash. The overall purpose was to improve the tools available for reliable assessment of the environmental impact of disposal of coal combustion residues.
Abstract in english For this study, magnetic composite of zeolite-magnetite was prepared by mixing magnetite nanoparticles suspension with synthetic zeolite. The nanoparticles in suspension were synthesized by precipitating iron ions in a NaOH solution. The zeolite was synthesized from coal fly ash by alkaline hydrothermal treatment. The magnetic composite was characterized by XDR, SEM, magnetization measurements, IR, and BET surface area. Batch tests were carried out to investigate the adso (more) rption of metal ions of Zn2+, Cd2+ and Pb2+ from aqueous solution onto magnetic composite. Adsorption isotherms were analyzed using Freundlich and Langmuir equations. The adsorption equilibrium data fitted well to the Langmuir equation with maximum adsorption capacities in the range of 28.5-127 mg g-1.
To optimise pulverized peat combustion it is necessary to sort out the influence from parameters like particle size and fuel moisture content on ignition and burnout. Peat contains significant amounts of sulphur but the ash is often rich in calcium and alkaline which can absorb some of it. The influence of combustion and fuel parameters on SO[sub 2]-as well as NO[sub x]-emission is important to clarify. Four different swedish peat qualities were originally included in the study. As one of them was not available, a Finnish briquettized peat was used to study the pretreatment on the milling. Pulverized coal was used as a reference fuel. The experimental equipment consisted of a crusher, a drier and a hammer mill for pulverization. The experimental furnace was a plug-flow reactor with a pre-mix burner. Some of the results were: At equal moisture content there were less fines (<100 [mu]m) from the briquettized peat than from the Swedish peat due to shorter residence time in the mill. Both moisture content and particle size distribution had a significant influence on ignition time. Dry, finely milled peat had an ignition delay of about 20 ms and the moist peat with a high amount of coarse particles had an ignition delay of c 100 ms. The ignition and volatile release is approx. as quick for peat as for coal but the burnout time for coal is much longer although there is a great scatter in the peat data. Sulphur absorption of the ashes amounted to 60-80% for peat and 44% for coal, of the theoretical maximum.
To optimise pulverized peat combustion it is necessary to sort out the influence from parameters like particle size and fuel moisture content on ignition and burnout. Peat contains significant amounts of sulphur but the ash is often rich in calcium and alkaline which can absorb some of it. The influence of combustion and fuel parameters on SO{sub 2}-as well as NO{sub x}-emission is important to clarify. Four different swedish peat qualities were originally included in the study. As one of them was not available, a Finnish briquettized peat was used to study the pretreatment on the milling. Pulverized coal was used as a reference fuel. The experimental equipment consisted of a crusher, a drier and a hammer mill for pulverization. The experimental furnace was a plug-flow reactor with a pre-mix burner. Some of the results were: At equal moisture content there were less fines (<100 {mu}m) from the briquettized peat than from the Swedish peat due to shorter residence time in the mill. Both moisture content and particle size distribution had a significant influence on ignition time. Dry, finely milled peat had an ignition delay of about 20 ms and the moist peat with a high amount of coarse particles had an ignition delay of c 100 ms. The ignition and volatile release is approx. as quick for peat as for coal but the burnout time for coal is much longer although there is a great scatter in the peat data. Sulphur absorption of the ashes amounted to 60-80% for peat and 44% for coal, of the theoretical maximum.
Prediction of ash and sulphur content of coal used in coal fired power plants is important for the precautions to be taken to prevent environmental pollution. In this study, the ash and sulphur content of coal from the Collolar Coal Area were estimated using the Kriging method at different block dimensions. The effect of block dimensions on the estimations was determined. 6 refs., 5 figs., 4 tabs.
The Quarterly Technical Progress Report for the University of North Dakota Energy Research Center includes work on gasification waste water treatment and reuse, hydrogen production, coal/water slurry preparation, low rank coal liquefaction, SO/sub x//NO/sub x/ air pollution control, particulate characterization, waste characterization, fine coal cleaning, combustor research and ash fouling, fluidized-coal combustion, fuel slurry combustion, ash and slag characterization, organic structure, distribution of inorganics, physical properties, moisture, supercritical gas extraction, pyrolysis and devolatilization. (LTN)
Physical determination of the chemical composition and actual density of the ash in coal and coal batch reveals that they are statistically related, as confirmed by high values of the multiple-correlation and determination coefficients. The proposed method of determining the actual density of the ash in coal and batch permits significantly more rapid prediction of the reactivity CRI and postreactive strength CSR of coke produced from such coal (batch).
Chemical interactions of disposed coal fly ash with O2, CO2, and infiltrating rain-water lead to chemical alteration, flushing/leaching of soluble chemical species locked in different physico-chemical forms as the coal fly ash is aging. This study was carried out to gain insight into the chemical alterations and its effects on the mobility patterns of chemical species in weathered coal fly ash. Weathered coal fly ash samples of ages 1 year and 20 years were sampled at a coal burning power station in the Mpumalanga Province, South Africa. The chemical and mineralogical compositions of the weathered coal fly ash were investigated using X-ray fluorescence spectrometry, inductive coupled plasma-optical emission spectrometry, ion chromatography, X-ray diffraction, and Fourier transform infrared...
It was found that only fly and bottom ashes are the solid wastes of water-coal slurry gasification in a direct-flow gasifier. The yields and chemical compositions of fly and bottom ashes obtained after the gasification of water-coal slurries prepared using brown (B) and long-flame (D) coals from the Berezovskii and Mokhovskii strip mines (Kansk-Achinsk and Kuznetsk Basins, respectively) were characterized. Based on an analysis of currently available information, the areas of utilization of fly and bottom ashes after water-coal slurry gasification with dry ash removal were summarized. The use of these wastes in the construction of high-ways and earthwork structures (for the parent coals of B and D grades) and in the manufacture of ash concrete (for the parent coal of D grade) is most promis...
On December 22, 2008 a dike containing coal fly ash from the Tennessee Valley Authority Kingston Fossil Plant near Kingston Tennessee USA failed and resulted in the largest coalash spill in U.S. history. Coalash, a by-product of coal combustion, is known to contain multiple contaminants of concern, including arsenic and selenium. The purpose of this study was to investigate species differences in the bioaccumulation of arsenic and selenium and potential factors contributing to these differences (i.e., trophic dynamics and gut pH) in the vicinity of the Kingston coalash spill. Elevated levels of arsenic and selenium were observed in various tissues of largemouth bass, white crappie, bluegill and redear sunfish from sites associated with the Kingston coalash spill. Highest concentrations...
The distribution characteristics of arsenic in fly ash from typical coal-fired power plants in the southwest of China is studied. It is found that the concentration of arsenic increases in the order of: coal particles--fly ash at ESP inlet--ESP fly ash--fly ash at ESP outlet, and reaches its climax in fly ash at ESP outlet. The concentration of arsenic in breathable particulates with different size-grade takes on an increasing trend overall with the decrease of the size-grade. It is concluded that the distribution characteristics of arsenic is a direct reaction result between fly ash and arsenic. There are four probable reaction mechanisms: the arsenic is dissolved by the silicate melting-mass; it reacts with some chemical components in fly ash and produces stable substance; it is adsorbed by fly ash; it condenses on the surface of fly ash. 10 refs., 3 figs., 4 tabs.
This project will evaluate the technical, economic, and environmental feasibility of filling abandoned underground mine voids with alkaline, advanced coal combustion wastes (fluidized-bed combustion (FBC) ash). Both pneumatic and hydraulic injection methods will be investigated. Success will be measured in terms of technical feasibility of the approach (i.e., percent void filling), cost, environmental benefits (acid mine drainage and subsidence control) and environmental impacts (noxious ion release). Phase I of the project is scheduled for 18 months starting in February 1994 and is concerned with the development of the grout and a series of predictive models. These models will be verified through the field phases and will allow the results to be packaged in such a way that the technology can be easily adapted to different site conditions. Phase I will also redesign a pneumatic ejector, that was developed to stow limestone, to efficiently stow FBC ash. Bench-scale testing will verify the redesign in Phase I. The 12-month Phase II is a small-scale field test at Anker Energy`s Fairfax mine. An inactive panel will be used to evaluate flow, strength, and pressure requirements for hydraulic (grout) injection. The Phase II pneumatic injection activities will take place at an Anker Energy mine in Preston County, West Virginia. Air flow requirements, pressure requirements, stowing rate (tons per hour), and stowing efficiency (distance blown) will be determined. Phase III is to take 26 months and will be a full-scale test at Anker`s 11-acre Long Ridge mine site. The mine will be filled using both pneumatic and hydraulic injection methods. It is expected that the FBC ash will replace what is now an acid mine pool with an alkaline solid so that the groundwater will tend to flow around rather than through the previously mined areas.
The 1971 US Clean Air Act (CAA) and the 1977 and 1990 amendments have required a considerable evolution of the quality of coal burned by utilities and in the type of pollution control equipment needed to reduce SO{sub 2} and NO{sub x} emissions. Any change in coal quality or emission`s control implies a change in the amount, type, and quality of coal combustion by-products (CCB). CCB is a collective term for fly ash, bottom ash and boiler slag, and flue-gas desulfurization (FGD) or fluidized-bed combustion produced in coal burning. Studies by the University of Kentucky in 1978, 1992 and 1997, have focused on the amount, quality, and end use of CCBs from Kentucky power plants, with emphasis on fly ash. The evolution of clean air standards has impacted the quality and volume of CCBs in several ways: (1) switching from high to lower sulfur coal generates less spinel phases and greater amounts of alumino-silicate glasses; (2) switching to Powder River Basin subbituminous coals produces Class C fly ash, compared to Class F fly ash from the combustion of the typical eastern bituminous coal; (3) the wider use of beneficiated coals reduces the amount of fly ash and bottom ash produced; (4) use of a wider rank range into the coal blend increases the potential of unburned carbon caused by inefficient combustion of non-design coals; (5) the inclusion of non-coal fuels, such as petroleum coke and with tire-derived fuel, in the coal blend; (6) reduction of NO{sub x} emissions has generally meant an initial increase in the amount of carbon in the fly ash; (7) addition of FGD means an added CCB stream, either a calcium sulfite which is mixed with fly ash and landfilled, or a calcium sulfate, sold for wallboard manufacture. The modification of the petrology and chemistry of the fly ash impacts the potential for utilization. 26 refs., 3 figs., 8 tabs.
The mineral matter in the eight reference North American coal samples of the Argonne Premium Coal series has been investigated on a quantitative basis using X-ray diffraction (XRD) techniques. X-ray diffraction data obtained from electronic low-temperature (oxygen-plasma) ash (LTA) residues, from ashes produced by heating the coals in air at 370C, and also from the raw coals themselves, were evaluated using an interactive data processing system (<SCP>siroquant) based on Rietveld interpretation methods. The results from the three types of material (LTA, 370C ash and raw coal) were compared for each sample. This allowed the components present in the raw coals in crystalline form to be recognised separately from mineral artifacts produced, particularly in the low-rank coals, from interaction of organically associated elements (Ca, S, etc.) during the two ashing processes. After the allowance for the production of any artifacts, the quantitative mineral assemblages identified from XRD of the raw coals were found to be consistent, even for coals having a relatively low ash percentage (around 5%), with the results obtained from the respective mineral concentrates prepared by the ashing methods. The effects of heating the coal to 370C could also be distinguished, relative to the raw coal or the LTA, through changes in components such as pyrite and the clay minerals. Although some areas of uncertainty exist, particularly with magnesium in the low-rank coals, the calculated chemical compositions of the coalash derived from the mineral mixtures identified for each coal were also found to be consistent with the results of direct chemical analysis of the respective coalash materials.
This work reports a kinetic study on the gasification of Brazilian coal with steam using a thermobalance. The coal is a high ash content (>50 wt%) subbituminous, run of mine coal (Charqueadas). Comparison of the present results with other data published shows that this coal is highly reactive.
On December 22, 2008 a dike containing coal fly ash from the Tennessee Valley Authority Kingston Fossil Plant near Kingston Tennessee USA failed and resulted in the largest coalash spill in U.S. history. Coalash, a by-product of coal combustion, is known to contain multiple contaminants of concern, including arsenic and selenium. The purpose of this study was to investigate species differences in the bioaccumulation of arsenic and selenium and potential factors contributing to these differences (i.e., trophic dynamics and gut pH) in the vicinity of the Kingston coalash spill. Elevated levels of arsenic and selenium were observed in various tissues of largemouth bass, white crappie, bluegill and redear sunfish from sites associated with the Kingston coalash spill. Highest concentrations of selenium were found in redear sunfish with liver concentrations as high as 24.83mg/kg dry weight and ovary concentrations up to 10.40mg/kg dry weight at coalash-associated sites. Investigations into the gut pH and trophic dynamics of redear sunfish and bluegill demonstrated a large difference in the gut physiology between these two species. Redear sunfish stomach and intestinal pH was found to be 1.1 and 0.16 pH units higher than in bluegill, respectively. In addition, fish from coalash-associated sites showed enrichment differences ((15)N and (13)C) compared to no ash sites, indicating differences in food web dynamics between sites. These results imply the incorporation of coalash-associated compounds into local food webs and/or a shift in diet at ash sites compared to the no ash reference sites. Based on these results, further investigation into a broader food web at ash-associated sites is warranted. PMID:22947506
Co-firing straw with coal in pulverized fuel boilers can cause problems related to fly ash utilization, deposit formation, corrosion and SCR catalyst deactivation due to the high contents of Cl and K in the ash. To investigate the interaction between coal and straw ash and the effect of coal quality on fly ash and deposit properties, straw was co-fired with three kinds of coal in an entrained flow reactor. The compositions of the produced ashes were compared to the available literature data to find suitable scaling parameters that can be used to predict the composition of ash from straw and coal co-firing. Reasonable agreement in fly ash compositions regarding total K and fraction of water soluble K was obtained between co-firing in an entrained flow reactor and full-scale plants. Capture of potassium and subsequent release of HCl can be achieved by sulphation with SO2 and more importantly, by reaction with Al and Si in the fly ash. About 70-80% K in the fly ash appears as alumina silicates while the remainder K is mainly present as sulphate. Lignite/straw co-firing produces fly ash with relatively high Cl content. This is probably because of the high content of calcium and magnesium in lignite reacts with silica so it is not available for reaction with potassium chloride. Reduction of Cl and increase of S in the deposits compared to the fly ashes could be attributed to sulphation of the deposits.
Due to the oil crisis in the seventies of the last century coal was reintroduced as fuel for electricity generating plants in the Netherlands. Coal fly ash is one of the products of the combustion of powder coal in these plants. In the Netherlands all coal fly ash produced, is used mainly for cement and concrete. At present more than 20 years of experience exists of concrete structures with coal fly ash. Hence, there is enough experience to validate the laboratory research performed in the past and to investigate the effect of coal fly ash on durability. Six Dutch concrete structures have been investigated with respect to performance over the years in service. This report summarises the results of this investigation as well as the durability of concrete structures with coal fly ash documented in the German and British literature. The results obtained show that the concrete with coal fly ash of all Dutch structures investigated, having an age of 4.5 to 16 years, was in excellent condition. No defects, due to coal fly ash were observed. In all cases the compressive strength has increased relative to the 28 days strength. In combination with portland cement the increase can be more than 100% over a period of 10 years.The increase in compressive strength will be due to an increase in the density of the cement stone in concrete. Therefore the resistance to ingress of aggressive compounds in concrete will more increase for portland cement concrete with fly ash than without. The results are in accordance with those of British research into coal fly ash concrete structures. in case of blast furnace slag cement, CEM III/B A or B, the difference in compressive strength development of concrete with and without coal fly ash of the same 28 days strength in time is small. Moreover the increase in strength after 28 days is small in comparison with portland cement concrete with coal fly ash. No indications of any deteriorating mechanism were found. In two cases corrosion of reinforcement was observed due to bad execution. In both cases the cover on the reinforcement appeared to be 10 mm or less. Depassivation has occurred due to carbonation. A German investigation into a prestressed railway sleeper does not show any sign of stress corrosion due to coal fly ash.The use of coal fly ash in concrete can prevent the occurrence of alkali-aggregate reaction. The concrete of all structures investigated shows a high resistance against diffusion. Also the chloride penetration resistance appeared to be high. Coal fly ash provides portland cement concrete with a higher resistance against penetration of aggressive compounds and oxygen.This improves the durability of the concrete. 20 refs.
China will continue to be one of the largest coal producers and users in the world. The high volume of coal use in China has focused attention on the amounts of toxic trace elements released from coal combustions and also the valuable trace elements extracted or potentially utilized from coalash. Compared to world coals, Chinese coals have normal background values for most trace elements, with the exception of higher Li (31.8mg/g), Zr (89.5mg/g), Nb (9.44mg/g), Ta (0.62mg/g), Hf (3.71mg/g), Th (5.84mg/g), and rare earth elements ( La-Lu+Y, 136mg/g). This is not only due to the higher ash yields of Chinese coals but also to alkali volcanic ashes found in some southwestern coals. The background values of toxic elements of Hg (0.163mg/g), As (3.79mg/g), and F (130mg/g) in Chinese coals are c...
In Coal Energy Technology Center of National Academy of Sciences and Ministry of Energy Industry of Ukraine (CETC) coal combustion and gasification technology in pressurized circulating fluidized bed (PCFB) under pressure up to 2.5 MPa with preliminary pyrolysis of initial coal in pyrolyzer is developed. Pyrolysis of coal is executed for the account of thermo-contact recirculating coke-ash residue (CAR) with an initial coal on path of return. The thermal capacity of plant in mode of coal combustion under pressure 1.2 MPa will be 2.5 MW[sub th]. Obtained heat after combustion will be used for domestic heating and hot water-supply for CETC. High ashcoal will be burnt (Ukrainian coal of a AC type (anthracite culm) and lean coal with ash content above 25%). This technology will be used to power blocks by capacity 200 MW[sub e] after tests in demonstration scale. 2 refs., 4 figs., 2 tabs.
In Coal Energy Technology Center of National Academy of Sciences and Ministry of Energy Industry of Ukraine (CETC) coal combustion and gasification technology in pressurized circulating fluidized bed (PCFB) under pressure up to 2.5 MPa with preliminary pyrolysis of initial coal in pyrolyzer is developed. Pyrolysis of coal is executed for the account of thermo-contact recirculating coke-ash residue (CAR) with an initial coal on path of return. The thermal capacity of plant in mode of coal combustion under pressure 1.2 MPa will be 2.5 MW{sub th}. Obtained heat after combustion will be used for domestic heating and hot water-supply for CETC. High ashcoal will be burnt (Ukrainian coal of a AC type (anthracite culm) and lean coal with ash content above 25%). This technology will be used to power blocks by capacity 200 MW{sub e} after tests in demonstration scale. 2 refs., 4 figs., 2 tabs.
This lesson provides an introduction to the use of coal as an energy source. Topics include the history of coal usage, applications of coal as an energy source, and major suppliers of coal (the United States). There is also discussion of how coal is created, located, and produced, and technologies for burning it more cleanly. The lesson includes a hands-on activity in which students measure the ash content of various types of coal.
Municipal solid waste (MSW) combustor ash was combined with Portland cement to form blocks which were placed in Conscience Bay, Long Island Sound, New York. During a 4·5-year period, ash blocks were returned to the laboratory to examine changes in the total elemental content of the ash blocks following placement. A continuous loss of calcium, potassium and zinc from the ash blocks was measured following submersion. Calculated effective diffusion coefficients ranged from 4·75 × 10-8 cm2s-1 for potassium to 5·56 × 10-8 cm2 s-1 for calcium. In contrast, lead an cadmium were effectively retained within the cementitious matrix of the submerged ash blocks. Following seawater submersion, the substitution of magnesium for calcium in the ash block pore spaces, the alkalineash block porewaters and the encapsulation of ash particles within the Portland cement matrix contribute to reduce the leaching of contaminants from ash blocks in the marine environment.
Ash disposals, coal-water slurry fuel and its feedstocks were analyzed for concentrations of major mineral elements based on sulfur free and ash basis. Elements with most concentration levels were found to be silicon, aluminum and iron with silicon having the highest concentration level. The size analysis of the fly ash particles revealed that 90% of particles have sizes less than 30 microns.
The need of 100% utilization of ash produced at coal-fired power stations is substantiated. The specific features of ash as a source of raw materials for various industry branches are considered. It is shown that integrated reprocessing of ash makes it possible to utilize it completely for producing concentrates that can be used in metallurgy, industry of construction materials, and other industry branches.
Process conditions are briefly described for conventional and advanced power systems. The advanced systems include both combustion and gasification processes. We discuss problems in coal-based power generation systems, including deposition, agglomeration and sintering of bed materials, and ash attack are discussed. We also discuss methods of mitigating ash problems and anticipated changes anticipated in ash use by converting from conventional to advanced systems.
Mössbauer spectroscopy and X-ray diffraction techniques have been used to characterize the iron-bearing phases in coal and their ash formed at 500°C. The analysis of the Mössbauer parameters and X-ray diffraction results show the presence of siderite, illite, pyrite and kaolinite in coal and hematite in ash as dominant minerals.
Moessbauer spectroscopy and X-ray diffraction techniques have been used to characterize the iron-bearing phases in coal and their ash formed at 500deg C. The analysis of the Moessbauer parameters and X-ray diffraction results show the presence of siderite, illite, pyrite and kaolinite in coal and hematite in ash as dominant minerals. (orig.).
The objectives of this work were to characterize the interactions of coal fly ash with polycyclic aromatic hydrocarbons (PAH`s) and their derivatives, and to attempt to understand the influence of surface properties of coalash in the chemical transformations of PAH`s.
The objectives of this research program include: the identification of the partitioning of inorganic coal constituents among vapor, submicron fume, and fly ash products generated during pulverized coal combustion; identification of fundamental processes by which the transformation of minerals and organically associated species occurs; the incorporation of the effects of combustion stoichiometry into an engineering model for ash formation.
Sensory irritation caused by fly ash from oil-fired (OF), fluidized bed coal (FB) combustion and conventional coal (CC) combustion power plants, and from Mt. St. Helens volcano (VA) was studied in mice. The irritating sensation due to contact with fly ash or its constituents was ...
In this study, the speciation of heavy metals such as arsenic, selenium, lead, zinc and mercury in coal combustion products (CCPs) was evaluated using sequential extraction procedures. Coal fly ash, bottom ash and flue gas desulphurization (FGD) sludge samples were used in the ex...
Fly ash, bottom ash and slag are waste products left in large amounts after the burning coal. Flows of mercury are presented as an example representing an assumed coal consumption of 23,5 Mton/year at some time after the year 2000. In this example, the am...
The mineral composition for salty coals (SC) of Western Donbas, using X-ray-phase analysis of cold oxygen plasma ashes, have been determined. The transformation of native minerals during ashing processes of coals at 600 C, 800 C and during long-time keeping were studied. Brief characteristics of rational ways for SC application was given. (orig.)
Fatty acid type ionic collectors were used as an alternative to conventional oily collectors, kerosene, and pine oil mixture in the flotation of coal tailing with 46.1% ash. The conventional collectors could not reduce the ash content of the concentrate below 22%. On the other hand, ionic collectors were found to be significantly better at reducing the ash content down to 13%. It was concluded that despite their lower flotation yield and higher consumption, certain ionic collectors could be used successfully in coal flotation where cleaner concentrates are required from coal fines with high ash content.
In order to discover the thickness of soil cover required for the utilization of land reclaimed with coalash as farmland, a small root-box was used in an experimental study of the relation between crop growth and root development and thickness of soil cover. The growth of carrots improved with increasing soil thickness, while that of spinach was unaffected. In thin soil covers the underlying coalash obstructed normal root extension and the taproot was short. It is thought that this tendency for the roots to avoid the underlying coalash is due to the hardness, pH and low vapour-phase percentage of the ash. (5 refs.) (In Japanese)
Detailed heat and mass balance calculations and emission performance projections are presented for an atmospheric fluidized bed boiler bottom retrofit at the 927 MWt (steam output) Komorany power station and district heating plant in the Czech Republic. Each of the ten existing boilers are traveling grate stoker units firing a local, low-rank brown coal. This fuel, considered to be representative of much of the coal deposits in Central Europe, is characterized by an average gross calorific value of 10.5 MJ/kg (4,530 Btu/lb), an average dry basis ash content of 47 %, and a maximum dry basis sulfur content of 1.8 % (3.4 % on a dry, ash free basis). The same fuel supply, together with limestone supplied from the region will be utilized in the retrofit fluidized bed boilers. The primary objectives of this retrofit program are, (1) reduce emissions to a level at or below the new Czech Clean Air Act, and (2) restore plant capacity to the original specification. As a result of the AFBC retrofit and plant upgrade, the particulate matter emissions will be reduced by over 98 percent, SO{sub 2} emissions will be reduced by 88 percent, and NO{sub x} emissions will be reduced by 38 percent compared to the present grate-fired configuration. The decrease in SO{sub 2} emissions resulting from the fluidized bed retrofit was initially predicted based on fuel sulfur content, including the distribution among organic, pyritic, and sulfate forms; the ashalkalinity; and the estimated limestone calcium utilization efficiency. The methodology and the results of this prediction were confirmed and extended by pilot scale combustion trials at a 1.0 MWt (fuel input), variable configuration test facility in France.
The SAM method is a method to form solidified ground by scattering a combining material which consists of coalash as its base and a small amount of additives and is stabilized with water at an appropriate mixing rate, placing reinforcing materials, such as sheets and nets, within or below the impregnated ground, and compacting the ground. The solidified ground is about 20 to 50 cm thick and has a compressive strength of 10 kgf/cm/sup 2/ or more. The ash column method is a method to form cylindrical ash columns in soft ground using geotextile sacks containing coalash and additives (cement and plaster). Coalash slurry with additives is delivered into the sacks inserted in ground. The coalash slurry, when filling up the sacks, is pressurized while expanding the ground; the slurry is dehydrated because water escapes into surrounding ground; columns are thus formed. These two methods seem widely applicable to civil engineering work. (5 figs, 2 photos)
The thesis contains an experimental study of the fusion and sintering of ashes collected during straw and coal/straw co-firing.A laboratory technique for quantitative determination of ash fusion has been developed based on Simultaneous Thermal Analysis (STA). By means of this method the fraction of melt in the investigated ashes has been determined as a function of temperature. Ash fusion results have been correlated to the chemical and mineralogical composition of the ashes, to results from a standard ash fusion test and to results from sintering experiments. Furthermore, the ash fusion results have been employed in a simple model for prediction of ash deposit formation, the results of which have been compared to ash deposition formation rates measured at the respective boilers.The ash fusion results were found to directly reflect the ash compositional data:a) Fly ashes and deposits from straw combustion are characterised by a large fraction of KCl and a smaller fraction of K-, Ca-, Al-silicates and quartz. The salt part of these ashes melt in the temperature range from 600-750°C, whereas the silicate part predominantly melts between 1000 and 1200°C. Increasing salt (KCl) content in the ashes lead to increased melt fractions in the temperature range 600-750°C.b) Bottom ashes from straw combustion consist purely of silicates, with varying ratios of the quite refractory Al-silicates and quartz to the less refractory K- and Ca-silicates. Bottom ashes melt in the temperature range 800-1300°C, and a trend of higher fusion temperatures with increasing contents of Al-silicates and quartz was found.c) Fly ashes, bottom ashes and deposits from coal/straw co-firing were all found to consist mainly of metal-alumina and alumina-silicates. These ashes all melt in the temperature range 1000-1400°C.Comparison of the obtained ash fusion results to results from the commonly used standard ash fusion test revealed that at the Initial Deformation Temperature, IDT, substantive melt formation had occurred. The difference between the melting onset, as determined by the STA, and the IDT varied typically between -300 - -50°C for salt rich ashes and between -150 - +40°C for silicate-rich ashes. Melt fractions present at the IDT varied between 0 - 35% melt for silicate rich ashes and between 10 - 70% melt for salt rich ashes. This emphasises that the IDT does not denote the onset of ash melting, the biggest deviations being found for salt rich (i.e. straw derived) ashes.A simple model assuming proportionality between fly ash fusion and deposit formation was found to be capable of ranking deposition rates for the different straw derived fly ashes, whereas for the fly ashes from coal/straw co-firing, the model only had a qualitative agreement with the measured ash deposit formation rates.Sintering measurements were carried out by means of compression strength testing of ash pellets. This method showed to not be applicable for the salt rich fly ash derived from straw combustion. For the fly ashes obtained during coal/straw co-firing, substantive sintering strength was observed to build up in the ashes below the melting onset. The strength obtained was thus assumed to be due to viscous flow sintering, and the sintering onset was for the four ashes investigated simultaneous to a calculated ash viscosity of 1-3 · 106 Pa·s.In conclusion, the employed laboratory technique to measure ash fusion gives a more detailed andprecise melt quantification compared to conventionally used techniques, and since ash fusion is important for ash deposition propensities, the employed method is judged to bring valuable new information. The measurement principle is not especially designed for studying ashes from combustion, so the method is as well applicable for other types of materials, for which a detailed characterisation of the melting behaviour is relevant.
Coal being a limited source of energy, extraction of energy from other sources like lignite, coal-refuse, and biomass is being attempted worldwide. The minerals and inorganic elements present in fuel feeds pose different technological and environmental concerns. Lignite ash, refuse ash, and biomass ash collected from Indian power plants burning lignite, coal-refuse, and mustard stalk, respectively, were analyzed for physico-chemical characteristics and trace elements. The lignite ash has high SiO2, CaO, MgO, Al2O3, and SO3; the refuse ash has high SiO2 and Fe2O3, but low SO3; the biomass ash has high SiO2 (but low Al2O3), and high CaO, MgO, K2O, Na2O, SO3, and P2O5. A substantial presence of chloride (2.1%) was observed in the biomass ash. Quartz is the most abundant mineral species. Other...
The major objective of this work was to characterize the interactions of coal fly ash with polycyclic aromatic hydrocarbons (PAHS) and their derivatives, and to attempt to understand the influence of the surface properties of coalash (and other atmospheric particles) on the chemical transformations of polycyclic aromatic compounds. Our studies have concentrated on the photochemical behavior of PAHs sorbed form the vapor phase on coal fly ashes, and compositional subfractions obtained therefrom. The PAHs are deposited onto the fly ash substrates from the vapor phase, using apparatus and techniques developed in this laboratory in order to simulate, as closely as possible under laboratory conditions, the processes by which PAHs deposit onto fly ash particles in the atmosphere. In this report phototransformation of pyrene sorbed on fly ash fractions, and phototransformations of 1-nitropyrene sorbed on fly ash fractions are discussed.
Two respirable coal fly-ash samples (<3MUm) were evaluated for physical properties, chemical composition and biological activity, including cytotoxicity and mutagenicity. The two fly-ash samples were collected from a pressurized fluidized-bed combustion miniplant and from a conventional-combustion plant, both burning eastern US coal. The two samples were found to have different physical and chemical properties. Both samples were toxic in two mammalian cell systems, with fluidized bed combustion fly ash showing higher toxicity in both assay systems. For conventional-combustion fly ash, no mutagenicity was detected in bioassay of the whole particles. A series of organic solvents was employed to identify the most efficient solvent for removing mutagens from coal fly ash. Extracts of fluidized-bed combustion fly ash were found to be mutagenic when dichloromethane, acetone or cyclohexane were employed: much lower mutagenic activity was found in dichloromethane and acetone extracts of conventional combustion fly ash.
Above 50% of fly ash discharged from Pulverized coal combustor (PCC-ash) are used by cement industry in Japan. Since the limestone is fed as the in-bed desulferization material into the pressurized fluidized bed coal combustor(PFBC), PFBC ash contains considerable amount of CaSO{sub 4} and unreacted CaO. PFBC-ash is difficult to feed into the cement kiln like as PCC-ash, since CaSO{sub 4} is easily decomposed and then the sulfer is accumulated in the kiln. In case that PFBC-ash is used as the landfill materials, CaO contained in PFBC-ash is dissolved in water, consequently it is difficult to treat the PFBC-ash. To utilize the PFBC-ash, various materials have been tried to be produced. However, most of them could not economically succeeded to develop the industrial process. PFBC ash consists of the fly ash collected from the cyclones and the filter, and of the boiler ash discharged from the combustor. The fly ash contains mainly SiO{sub 2}, Al{sub 2}O{sub 3} and Fe{sub 2}O{sub 3} like as the clay. The boiler ash contains more calcium compounds such as CaSO{sub 4} and unreacted CaO, CaCO{sub 3}. These calcium compounds have the self-hardening property. In this paper, a new process to produce a heat insulator from PFBC-ash is proposed.
The most important structural components of coalash obtained by coal combustion in 'Nikola Tesla A' power plant located near Belgrade (Serbia) are amorphous alumosilicate, alpha-quartz, and mullite. The phase composition of coalash can be altered to obtain zeolite type NaA that crystallizes in a narrow crystallization field (SiO{sub 2}/Al{sub 2}O{sub 3}; Na{sub 2}O/SiO{sub 2}; H{sub 2}O/Na{sub 2}O ratios). Basic properties (crystallization degree, chemical composition, the energy of activation) of obtained zeolites were established. Coalash extracts treated with obtained ion-exchange material showed that zeolites obtained from coalash were able to reduce the amounts of iron, chromium, nickel, zinc, copper, lead, and manganese in ash extracts, thus proving its potential in preventing pollution from dump effluent waters.
The most important structural components of coalash obtained by coal combustion in “Nikola Tesla A” power plant located near Belgrade (Serbia) are amorphous alumosilicate, ?-quartz, and mullite. The phase composition of coalash can be altered to obtain zeolite type NaA that crystallizes in a narrow crystallization field (SiO2/Al2O3; Na2O/SiO2; H2O/Na2O ratios). Basic properties (crystallization degree, chemical composition, the energy of activation) of obtained zeolites were established. Coalash extracts treated with obtained ion-exchange material showed that zeolites obtained from coalash were able to reduce the amounts of iron, chromium, nickel, zinc, copper, lead, and manganese in ash extracts, thus proving its potential in preventing pollution from dump effluent...
A comparative technology evaluation is made of competing technologies - pulverized coal (PC), stoker-fired and circulating fluidized-bed boilers - for firing high-ash waste coal. Operating experience from Ukraine and India indicates that PC-fired boilers burning high-ash waste coal can be repowered with circulating fluidized-bed (CFB) technology. This has been necessary due to poor boiler availability, equipment deterioration, ash content variation in the fuel, and increasingly stringent emissions regulations. Due to these considerations, CFB technology was selected for Ebensburg Power Company`s high-ash waste coal project. The 55 MW B&W CFB boiler at Ebensburg Power, Pennsylvania, USA has successfully fired high-ash waste coal since May 1991. Operating experience of the Ebensburg CFB boiler, including availability, maintenance, and emissions is discussed.
The quality of shallow groundwater in coal-ash disposal basin of varying age was studied over a three year period. These basins are associated with a power production facility located on the Savannah River Site (SRS) near Aiken, South Carolina. The old basin had not received ash inputs during the past 15 years. These results indicate that coalash disposal basins may be a source of groundwater contamination for time periods in excess of 15 years.
The chemical composition and morphology of fly ash captured in cyclone, bottom ash and ultrafine particles separated in the low pressure impactor produced by the two modes of combustion (oxidation and reduction conditions) are determined. The two types of brown coal from the North Bohemian basin are characterized by reflectance, maceral, mineralogical and chemical composition. It was found that composition and morphology of fly ash depends on reaction conditions, coal quality and size distribution of particles. (orig.)
LIFAC is a more recent addition to flue gas desulphurization methods for reducing sulphur emissions during coal combustion for the production of electricity. Ashes from the combustion of a low-sulphur lignite coal using LIFAC technology were used to evaluate different ash management strategies. The ashes, as produced and after treatment by the CERCHAR hydration process, were examined for their disposal characteristics and their utilization potential in concrete. They were also evaluated as underground disposal material using the AWDS process. PMID:15823742
19 papers are presented covering thermogravimetric analysis - problem solving in coal utilization, excess moisture and excess taxes, sulphur in coal analysis using inorganic calibration standards, SPC management of coal sampling, quick coal test procedures, low volatile coal usage in boilers, environmental assessments - sampling concerns, relationships of HGI to petrographic composition, coal slurry analysis by inductively coupled plasma spectroscopy, microwave ashing of coal samples, bulk sampling and washing of lignite at Mae Moh mine, (Thailand), weigh bin systems, digital load cell technology, HGI - a new yardstick, statistical evaluation of on-line analyser performance, influence of size consist on inherent moisture determination in low rank coals, university coal chemistry programmes, and on the job training.
Simple hyperbolic equations have been fitted to the results of coal cleaning operations, calculated in the form of m-curves, i.e. mass of cleaned coal vs. coal. Both basic coal washability data and simulated coal cleaning results accurately fit the equations. The analytical properties of the curves have been used to predict optimum settings of cleaning units in parallel stream systems. For predictions of moderate accuracy (cleaned coalash content within 0.5% of a specified ash content) optimum settings can be established by the mathematical model without elaborate iteration or search procedures thereby simplifying the optimization.
The coal research work of the University of North Dakota Energy Research Center is reviewed: coal gasification waste water and its treatment for reuse in cooling towers; hydrogen production from low rank coal (reactivity and catalysts); coal-water slurry preparation (hydrothermal water removal); coal liquefaction; SO/sub 2//NO/sub x/ control (pressure hydrated lime - preparation and use); particulates; fine coal cleaning; combustion; ash fouling; fluidized-bed combustion; ashes; slags; molecular structure; minerals; physical properties (moisture, surface area, wetting heat, small angle scattering); supercritical gas extraction; pyrolysis; and devolatilization. (LTN)
A coal preparation plant is discussed to remove sulfur, ash and other impurities from coal. The low-cost SO/sub 2/ reduction strategy has secondary benefits to boiler operability. Coal-cleanability studies were performed after the coal-prep plant came on line to reduce SO/sub 2/ emissions from Paradise Station's three Cyclone-fired boilers. The ash content of the coal was reduced to 8% in 1981. When all three units burned cleaned coal in 1983, the CRFOR dropped to 13.7%. Taking the reduction in forced-outage rate from 1983 and 1985, the resulting saving in replacement-energy costs alone is $4.8 million in 1984 dollars.
Discusses use of kriging, in particular its simplified version called point kriging, for forecasting variations of coal seam thickness, calorific value, ash and sulfur content. These variations are determined under conditions of the Lublin coal basin using geostatic and statistical methods. Analyses show that point kriging supplies accurate results only for coal seam thickness. Forecasting variations of ash or sulfur content in coal or its calorific value by means of point kriging is impossible due to the random character of variations. Accuracy of forecasting variations of coal seam thickness using point kriging was verified in a deposit area with an already explored coal seam. 8 refs.
Some existing alternative applications of coal fly ash such as cement manufacturing; road construction; landfill; and concrete and waste stabilisation use fresh ash directly collected from coal-fired power generating stations. Thus, if the rate of usage continues, the demand for fresh ash for various applications will exceed supply and use of weathered dry disposed ash will become necessary alternative. As a result it's imperative to understand the chemistry and pH behaviour of some metals inherent in dry disposed fly ash. The bulk chemical composition as determined by XRF analysis showed that SiO"2, Al"2O"3 and Fe"2O"3 were the major oxides in fresh ash and unsaturated weathered ashes. The unsaturated weathered ashes are relatively depleted in CaO, Fe"2O"3, TiO"2, SiO"2, Na"2O and P"2O"5 ...
The medium coking coal fines of - 0.5 mm from Jharia coal field were taken for this investigation. The release analysis of the composite coal reveals that yield is very low at 10.0% ash, about 25% at 14% ash and 50% at 17% ash level. The low yield is caused by the presence of high ash finer fraction. The size-wise ash analysis of - 0.5 mm coal indicated that - 0.5 + 0.15 mm fraction contains less ash than - 0.15 mm fraction. Thus, the composite feed was split into - 0.5 + 0.15 mm and - 0.15 mm fractions and subjected to flotation separately. The low ash bearing fraction (- 0.5 + 0.15 mm) was subjected to two stages collectorless flotation to achieve the concentrate with 10% ash. The cleaner concentrate (18.9%) with 10% ash was recovered which has an application in metallurgical industries. The concentrate of 30.2% yield with 12.5% ash could be achieved in one stage collectorless flotation which is suitable for use in coke making as sweetener. As the - 0.15 mm fraction contains relatively high ash, collector aided flotation using sodium silicate was performed to get a concentrate of 23.6% yield with about 17% ash. The blending of this product with cleaner tail obtained from - 0.5 + 0.15 mm produces about 35.0% yield with 17% ash and that can be utilized for coke making. The reject from the two fractions can be used for conventional thermal power plant or cement industries using a 23.5% ash after one stage collector aided flotation and the final tailings produced content ash of 61.6% can be used for fluidization combustion bed (FBC). This eventually leads to complete utilization of coal. (author)
The sulphur and ash contents with respect to their size, mineralogical, chemical and the washability properties of Yozgat-Ayridam lignites were determined. It is shown that clean coals containing low ash (13-14%) and sulphur (0.73-1.32%) can be produced by using hand-sorting, heavy medium separation, flotation, jig and a shaking table. The total clean coal obtained had 13.7% ash, 1.15% S and higher calorific value of 6231 kcal/kg, dry basis. In addition, 80.83% of combustible portion was recovered in the clean coal concentrate. Thus Ayridam`s coal can be concentrated by using physical cleaning methods. 8 refs., 11 figs., 19 tabs.
The total annual production of coal combustion by-products in the USA is expected to exceed 150 million Mg by the year 2000. Agricultural utilisation may offer a partial solution to disposal problems, but the benefits and risks associated with using these materials must be assessed. Four coal combustion by-products, bed ash (BA) and fly ash (FA) from a fluidised-bed combustion furnace and stabilised scrubber sludge (SS) and a high gypsum content by-product (G) from flue gas desulphurisation processes were added to two soils at rates of 0, 20, 40 and 80 g kg{sup -1}. The growth and elemental composition of `Gulf` annual ryegrass (Lolium multiflorum L.) were evaluated in the treated soils. Adding FA, SS and G to both soils at application rates of up to 80 g kg{sup -1} was not detrimental to the growth of ryegrass and resulted in higher yields than controls in some instances. Adding BA created a high alkalinity, high soluble-salt environment that initially inhibited seedling germination and significantly reduced yields of dry matter, so it will probably need to be restricted to rates of lime requirement. Ryegrass concentrations of Cu, Zn, Ni, Pb Cd and Cr were similar in control and treated soils, but levels of B, Se, As and Mo were raised in treatments. Based on low trace-element concentrations in ryegrass shoots and in soil solution, Se from FA application may be the only potential food-chain risk associated with application of the four coal combustion by-products used in this investigation. 28 refs., 4 figs., 4 tabs.
Mitigation of greenhouse gases emission is one of the most important issues in energy engineering. Biomass is a potential renewable source but with limited use in large scale energy production because of the relative smaller availability as compared to fossil fuels, mainly to coal. Besides, the costs concerning transportation must be well analysed to determine its economic viability. An alternative for the use of biomass as a primary source of energy is the co-firing, that is the possibility of using two or more types of fuels combined in the combustion process. Biomass can be co-fired with coal in a fraction between 10 to 25% in mass basis (or 4 to 10% in heat-input basis) without seriously impacting the heat release characteristics of most boilers. Another advantage of cofiring, besides the significant reductions in fossil CO{sub 2} emissions, is the reduced emissions of NO{sub x} and SO{sub x}. As a result, co-firing is becoming attractive for power companies worldwide. This paper presents results of some experimental analysis on co-firing coal with rice straw in a combustion reactor. The influence of biomass thermal share in ash composition is also discussed, showing that alkali and earth alkaline compounds play the most important role on the fouling and slagging behavior when co-firing. Some fusibility correlations that can assist in the elucidation of these behavior are presented and discussed, and then applied to the present study. Results show that for a biomass thermal share up to 20%, significant changes are not expected in fouling and slagging behavior of ash. (author)
This study was carried out to examine the characteristics and potential utilization of synthetic soil aggregates (SSA) produced by mixing acidic 'Kunigami Mahji' soil in Okinawa, Japan, with waste materials, such as coal fly ash, used paper and starch, as media for crop growth. A series of different SSA were produced by incorporating various percentages (i.e. 0, 20, 40, 60, 80 and 100%) of coal fly ash into the 'Kunigami Mahji' soil with used paper and starch. The increased percentages of added coal fly ash, used paper and starch significantly decreased the particle and bulk densities of SSA compared with the original 'Kunigami Mahji' soil because of the low particle and bulk densities of the coal fly ash (2.10 and 0.96 g cm{sup -3}, respectively). Maximum water-holding capacity and saturated hydraulic conductivity were increased with the formation of SSA with coal fly ash, used paper and starch binder compared with the original 'Kunigami Mahji' soil. The saturated hydraulic conductivity values of the SSA increased because of their low bulk density compared with the original soil. The addition of coal fly ash, used paper and starch to the acidic (pH=4.62) 'Kunigami Mahji' soil to form SSA increased the pH (6.70 - 9.96), electrical conductivity, exchangeable cation concentration and cation exchange capacity. The addition of coal fly ash up to 60% increased the aggregate strength. The growth and yield of komatsuna and soybean crops with SSA as a crop growth medium was assessed. Both crops showed the highest growth and yield when grown with SSA containing 20% of coal fly ash. Synthetic soil aggregates containing more than 20% of coal fly ash reduced plant growth and yield. Therefore, SSA produced from 'Kunigami Mahji' soil with 20% of coal fly ash, used paper and starch can be successfully used as a medium for crop growth.
The State Electricity Commission of Victoria generates about 85% of its electrical capacity from the combustion of brown coal mined from extensive coal reserves in the Latrobe Valley region, producing approximately 460,000 tons of solid waste annually. This is expected to rise to 550,000 tons per year by 1994. Approximately 80% (wt) of solid waste if fly ash. Black coal fly ashes have been extensively used as extenders for Portland cement, but brown coalashes are traditionally less satisfactory in cement systems because of their lower hydraulicity and inferior contribution of the ash to the strength development of the matrix. The composition of Latrobe Valley coal and the distribution of ash-forming constituents in the coal result in the formation of a unique fly ash during combustion. The unusual composition and properties of the ash initiated the present study on the potential for using this material in cement and concretes. The work reported in this paper describes physical and chemical characteristics of Latrobe Valley fly ashes and discusses the formation of cement blends containing various amounts of fly ash and their properties. Preliminary results show moderate strength development in the products.
Western Australia relies largely on electricity generated by the combustion of coal reserves (namely Collie coal) from the South Western region of Australia. As there is limited information regarding the conversion characteristics of Collie coal, a study was therefore initiated to investigate the mineral behaviour of Collie coal during combustion. In the present work, an attempt has been made to compare raw coal and ash samples obtained from a local power station boiler located in Collie, Western Australia. The coal samples were combusted in a Lab-scale Combustion Simulator (LCS), located at the Energy Research Centre of the Netherlands. The analytical results obtained on raw coal samples were also compared with LCS derived ash samples. Advanced/improved Computer Controlled Scanning Electron Microscopy (CCSEM) techniques, at ECN, were employed to carry out detailed mineral analysis on coal as well as ash samples resulted from LCS and power station boilers. Analytical data is presented to show similarities observed in ash characteristics of LCS and power station derived ash samples thereby highlighting the importance of simulated experiments in the LCS. Discussions will also address the relevance of improved CCSEM techniques and their usefulness in relating coal mineral matter (in terms of included and excluded minerals) to the ash characteristics in coal fired power station boilers. (Abstract only)
Fine ash particles formed during coal combustion in power stations can remain airborne for long periods and can result in deleterious health effects when inhaled and deposited in the lungs. Previous studies have shown that combustion of coals of different rank can result in differences in the amount and chemistry of the submicron ash particles. This study examines the variability occurring between the submicron ashes formed from coals of similar rank. Five Australian bituminous coals were burned in a laminar flow drop tube furnace in two different oxygen environments to determine the amount and composition of submicron ash formed. The experimental setup is described and the repeatability of the experiments is discussed. The largest variability in submicron ash yield occurred as a result of coal selection. The coal with high sulfur content showed the highest amount of submicron ash yield. Both the elemental composition and yield of submicron ash were greatly affected by increasing the oxygen partial pressure of the oxidizing gas from 0.21 to 0.50 atm. All coals showed an increase in submicron ash yield at the elevated oxygen partial pressure. 33 refs., 5 figs., 5 tabs.
Whether the particle size distribution of fly ash influences selenium uptake by onions grown on coal fly ash-amended growth media was investigated. Two fly ashes having differing percentages of finely sized particles were used as plant growth amendments at percentages in the media to yield equal concentrations of selenium. Selenium concentrations in the harvested onion bulbs were found to be independent of fly ash particle size distribution.
As early as in the fifties fly ash of the RWE Grosskraftwerk Fortuna was utilized as lime fertilizer and mortar binder. In the mine power plants of Rheinbraun AG in the rhenish lignite district low-ash briquetting coal is fired which results in a more even fly ash quality. These ashes are utilized as a mineral lime fertilizer and due to their calcium and magnesium content they are able to nourish the plant. They are suitable for recover and conservation fertilizing. (orig.).
Twenty-six fly ash specimens from N. Dakota, Wyoming and Montana lignite and sub-bituminous coals have been studied by X-ray diffraction. Chemically these western fly ashes are characterised by higher CaO + MgO + SO/sub 3/ contents and lower Al/sub 2/O/sub 3/ + SiO/sub 2/ contents than eastern bituminous fly ashes. The western fly ashes have greater proportions of crystalline materials, the characteristic phase being quartz, lime periclase, anhydrite, ferrite spinel, tricalcium aluminate, merwinite and melilite.
Coal fly ash emitted from coal thermal power plants generally contains tens ppm of arsenic, one of the hazardous elements in coal, during combustion and their elution to soil or water has become a public concern. In this study, the acid washing process developed by the authors was applied to the removal of arsenic from coal fly ash. Laboratory- and bench-scale investigations on the dissolution behavior of arsenic from various coal fly ash samples into dilute H2SO4 were conducted. Arsenic in the coal fly ash samples were dissolved into H2SO4 solutions rapidly. However, its concentrations decreased with an increase in the pH of H2SO4 solution in some cases. The species of arsenic in the dilute H2SO4 was estimated as H3AsO4, and its anionic species was considered to adsorb with the elevation ...
The development of a procedure for assessing the ash material inventory and size distribution in the bed of a circulating fluidized bed coal combustor at steady state is described. A model was developed for the quantitative assessment of the size distribution of bed inert material where the bed consists of fuel ash only. Fuel attrition and ash attrition rate are used to assess the generation and destination of primary ash particles. The importance of primary ash particle size distribution and ash attrition to the inventory of bed inert solids is discussed. 19 refs., 5 figs., 4 tabs.
Coal fly ash emitted from coal thermal power plants generally contains tens ppm of arsenic, one of the hazardous elements in coal, during combustion and their elution to soil or water has become a public concern. In this study, the acid washing process developed by the authors was applied to the removal of arsenic from coal fly ash. Laboratory- and bench-scale investigations on the dissolution behavior of arsenic from various coal fly ash samples into dilute H(2)SO(4) were conducted. Arsenic in the coal fly ash samples were dissolved into H(2)SO(4) solutions rapidly. However, its concentrations decreased with an increase in the pH of H(2)SO(4) solution in some cases. The species of arsenic in the dilute H(2)SO(4) was estimated as H(3)AsO(4), and its anionic species was considered to adsorb with the elevation of pH under the presence of ash particle. Such adsorption behavior was enhanced under the presence of Fe ion in the solution. The sufficient removal of arsenic was achieved by controlling pH and avoiding the adsorption of arsenic on the surface of coal fly ash particles, and the elution of arsenic from coal fly ash sample was successfully below the regulation limit. PMID:20570439
Biomass not only has a considerable potential as an additional fuel source but also shows a reasonable cost level in comparison to other renewable energies. The practicable fuel types are both residual material from forestry and agriculture, such as wood or straw, and especially cultivated reproducible feedstock such as Miscanthus Sinensis, whole cereal plants, poplars, or willows. Besides as single fuel, it is also considered to be sensible to utilize biomass in co-combustion in existing firing systems, such as pc-fired power stations. Biomass or sewage sludge utilized as additional fuel in coal combustion systems has consequences on combustion behavior, emissions, corrosion and residual matter. The effects of burning sewage sludge and agricultural residuals such as straw and manure as well as specially grown energy plants in combination with coal were studied in a 0.5 MW pulverized fuel test facility and a 20 kW electrically heated combustor. A major aspect of the investigations had been the required preparation and milling of the additional fuels. The investigations showed that in co-combustion of straw with coal, a grinding of 6 mm and finer is sufficient. The definitely coarser milling degree of biomass delays combustion and is observable by in-flame measurements. The investigations reveal that biomass addition has a positive effect on emissions. Since biomass in most cases contains considerably less sulphur than coal, an increasing biomass share in the thermal output makes the SO{sub 2} emissions decrease proportionally. In addition, SO{sub 2} can partly be captured in the ash by the alkaline-earth fractions of the biomass ash. As for sewage sludge, the emissions of SO{sub 2} correlate with the sulphur content of the fuel and, hence, rise with an increasing share of this biomass. Independently from the type, biomass shows a considerably stronger release of volatile matter. This latter fact may have a positive impact on NOx emissions when NOx-reducing techniques are applied. Within the framework of these investigations the following configurations were used: (1) unstaged combustion with preblending of coal and biomass, (2) air-staged combustion with preblending of coal and biomass, (3) reburning with biomass as reduction fuel, and (4) various burner configurations. The results show that the burner design and operation mode have a great influence on the NOx emissions of combined flames. Air staging and reburning are effective measures to reduce the NOx emissions of combined fuels. NOx emissions smaller than 300 mg/m at 6% O{sub 2} can be reached with all fuels.
The major objective of this project was to develop mixture proportions for controlled low-strength material (CLSM) using clean coalash obtained from atmospheric fluidized bed combustion (AFBC). A clean coalash is defined as the ash derived from SO{sub x} and NO{sub x} control technologies. The specific ashes used for this project were: (1) circulating fluidized bed boiler fly ash and bottom ash and (2) stoker-type boiler fly ash and bottom ash. These two coalash samples were characterized for physical and chemical properties. Chemical properties and water leaching tests were also performed on the hardened CLSM. Many initial CLSM mixtures were developed by blending the two types of ash. Tests conducted on the final three selected CLSM mixtures included compressive strength, bleeding, setting and hardening, settlement, length change of hardened CLSM, permeability, mineralogy, and chemical water leach testing. Results show that acceptable CLSM material can be developed by blending the fluidized bed boiler ash with the stoker boiler ash. Recommendations for a pilot scale manufacturing application of the three CLSM mixtures were made based upon the lab test results.
The properties of high-calcium oil shale fly ash and low-calcium coal fly ash, which are produced in Israeli power stations, were investigated. High-calcium oil shale fly ash was found to contain a great amount of CaO{sub free} and SO{sub 3} in the form of lime and anhydrite. Mixtures of high-calcium oil shale fly ash and low-calcium coal fly ash, termed fly ash binder, were shown to cure and have improved strength. The influence of the composition and curing conditions on the compressive strength of fly ash binders was examined. The microstructure and the composition of fly ash binder after curing and long-term exposure in moist air, water and open air conditions were studied. It was determined that ettringite is the main variable in the strength and durability of cured systems. The positive effect of calcium silicate hydrates, CSH, which are formed by interaction of high-calcium oil shale fly ash and low-calcium coal fly ash components, on the carbonation and dehydration resistance of fly ash binder in open air is pronounced. It was concluded that high-calcium oil shale fly ash with high CaO{sub free} and SO{sub 3} content can be used as a binder for building products.
There are no specific standards for biomass ash analysis in China, so the standards for coalash analysis are usually used to determine the property of biomass ash. Three kinds of biomass including rice straw, pine sawdust and Chinese Parasol Tree leaf burned at 815 C, 600 C and 500 C respectively corresponding to the temperature required in the standard of GB and ASTM. The ash content and composition were analyzed. Based on the ash composition results, the volatilization of alkali oxides in biomass ash and slagging/fouling problems related to biomass thermochemical conversion were investigated. The alkali metals were relatively more volatile with the increasing of ashing temperature. The crystalline phase composition and surface morphology characteristics of the ash particles were investigated by XRD and SEM analysis. The increasing ashing temperature resulted in the decreasing of the diffraction intensities of metal salts and the increasing of the diffraction intensities of silicon compound. Ash fusion temperatures were measured by 5E-AFII Ash Fusion Analyzer. The results indicated that the ash content, composition, crystalline phases composition, surface morphology and ash fusibility were all closely related to ashing temperatures. The analysis at 600 C ashing temperature was regarded as the optimal for an exact determination of ash properties. (author)
The main characteristics of fly ash from Greek coal-fired boilers are presented in this paper in relation to its exploitation potential. Both fuel and fly ash samples were collected and analyzed according to the ASTM Standards. Apart from the typical analyses (proximate, ultimate, ash analysis and calorific value), an ICP-AES spectrometer was used for the analysis of heavy metals in the ash. Experimental measurements in order to determine the radioactivity content of raw fuel and the fly ash were carried out as well. A representative fly ash sample from Ptolemais power plant was evaluated and tested as filler in Self-Compacting Concrete (SCC). Ashes from the Greek brown coal are classified in type C, most of the fly ash being produced in Ptolemais of Northern Greece, while the rest in Megalopolis. Ptolemais fly ash is rich in calcium compounds, while Megalopolis fly ash contains more pyrite. Increased heavy metal concentrations are observed in the fly ash samples of Greek coal. Greek fly ash appears to have not only pozzolanic but also hydraulic behaviour. Furthermore, Greek fly ash, depending on its origin, may have relatively high natural radioactivity content, reaching in the case of Megalopolis fly ash 1 kBq kg{sup -1} of {sup 226}Ra. The laboratory results showed that fly ashes can be a competitive substitute to conventional limestone filler material in SCC. Fly ash is mostly used in Greece in cement industry replacing cement clinker and aiming to the production of special types of Portland cements. However, a more aggressive utilisation strategy should be developed, since low quantities of the total produced fly ash are currently further utilised. (author)
The minor and trace element content of coal is of great interest because of the potential environmental impact resulting from their release during coal combustion. Results will be presented from the investigation of how trace elements in western and eastern Kentucky bituminous coals partition (1) in advanced cleaning techniques prior to combustion and (2) in the solid waste streams during coal combustion. For the coal cleaning studies, samples of run-of-mine coal were subjected to a commercially available laboratory scale column floatation process followed by various hydrothermal leaching treatments. For the combustion studies, samples of feed coal, bottom ash, and fly ash were collected from single source western and eastern Kentucky coal fired powered plants. The trace element composition of coal and coal byproducts were obtained using particle induced x-ray emission (PIXE) and instrumental neutron activation analysis (INAA). Modes of occurrence for some of the elements were determined using x-ray absorption fine structure (XAFS) spectroscopy to augment the compositional data.
The principle of coal cleaning using humic acid is as follows. Humic acid is an anionic polyelectrolyte which possesses a high density of carboxyl groups. The mechanism of coal depression involves the selective adsorption of humic acid on the hydrophobic coal through hydrophobic bonding. Pyrite and ash are hydrophilic in nature and are separated from the carbonaceous part of the coal, thus resulting in a cleaner coal. The adsorption characteristics of humic acid on coal are discussed. Humic acid adsorption on coal is modeled in terms of Langmuir adsorption isotherms. Coal cleaning was carried out using humic acid and xanthic acid for coal depression and mineral matter flotation, respectively. Dramatic decrease decrease in ash content was observed while significant recovery of the original coal was accomplished in these flotation experiments. The heating recovery ratios as a function of the xanthic acid addition are also reported. 4 refs., 6 figs., 1 tab.
This report describes the gasification of several coals in the Shell Coal Gasification Process at SCGP-1. This represents a wide variety of coals, including Illinois No. 5 -- the base coal -- Maple Creek, Buckskin, Blacksville No. 2, Pyro No. 9, and Drayton. These results demonstrate the unique flexibility of the Shell Coal Gasification Process in handling a wide range of coals. These coals have significant differences in coal properties, including moisture content, reactivity, ash content, ash viscosity, and calcium, chlorine, and sulfur levels. Process results are presented for each coal, including gasifier performance and efficiency calculations. Analytical data, including trace element analyses, are provided for the feedstock coal, the slag and flyslag solids, and the major gas and liquid streams in the plant. 13 refs., 57 figs., 41 tabs.
Black shale and coal Clarke values are the average trace element contents in the World black shales and coals. These calculations are made in Russian geochemistry but up to now are poorly known in the West. Modern tables of black shale and coal Clarkes are presented, based on comprehensive calculations using very large amount of information (thousands analyses of black shales, coals, and coalashes for trace elements). In black shale geochemistry, three figures were calculated for each main lithologies: terrigenous (+ tuff), chert, and carbonate. Two Clarke estimations are presented, named lithological (K{sub 1}) and lithostratigraphical (K{sub 2}). In coal geochemistry, seven figures were calculated for each trace element: average content in hard coals and their ashes; average content in brown coals and their ashes; average content in all coals and their ashes; and coal affinity index (or coalphile index) average content in all ashes/Clarke values of sedimentary rocks. The black shale and coal Clarkes presented here provide an important scientific base for many geochemical comparisons and issues. (author)
Analyzes beryllium content in brown coal from the North Bohemian brown coal district in Czechoslovakia. The following aspects are evaluated: trace elements in brown coal from the North Bohemian district in comparison to other coal basins in Czechoslovakia (the Kladno and Sokolov brown coal districts, the Ostrava-Karvina region with black coals, coals from various basins in the USSR, the GDR, France, the USA and Belgium). Geochemistry of beryllium compounds in brown coal from the North Bohemian basin is analyzed: types of beryllium compounds, beryllium in organic matter and inorganic compounds in coal, beryllium origin (biogenetic activity of Miocenic flora, clays accumulated during sedimentation, sorption processes in the biochemical and geochemical phases, binding of beryllium with mineral components), ash content in coal, correlations of ash content and beryllium content in coal and in ashes, behavior of beryllium compounds during brown coal combustion in commercial boilers used in power plants (beryllium content in flue gases, in fly ash and in slags), environmental hazards associated with beryllium in brown power coals (environmental hazards are characterized as low). 34 refs.
Four Australian coals, Blair Athol, Ebenezer, Newlands and Warkworth coals, were demineralized by Ca(OH){sub 2} digestion at 300{degree}C, followed by washing with dilute HCl. Ash contents decreased from 8.8-15.4% to 1% for Blair Athol, Newlands and Warkworth coals, and from 14.9% to 2.8% for Ebenezer coal. The CaO/ash ratio is an important factor affecting coal demineralization; the maximum ash removals were achieved at CaO/ash ratios in the range 0.6-1 g/g for all the coals. The major minerals in the original coals were kaolinite and quartz, with some montmorillonite and carbonates. Kaolinite and quartz hydrothermally reacted with Ca(OH){sub 2} to form calcium-bearing hydrated silicates and aluminosilicates, such as tobermorite and hibschites, that could be dissolved in acid. With increasing CaO/ash ratio in excess of the optimum value, the removal of quartz significantly decreased; there also remains some calcium in treated coal, depending on digestion conditions and coal type. A lower ash removal from Ebenezer is due to a lower quartz removal and more remaining calcium. 16 refs., 8 figs., 4 tabs.
Table of Contents includes: Coal technology and coal-related experience of Mitsubishi Heavy Industries, Ltd., Research and development of a COM Carrier; Unmanned operation of spreader stoker coal-fired ship; Prediction of coal-dust saltation and dispersion; Development of large coal-storage silos with wedge-shaped Hopper Systems; 1,000 MW Supercritical sliding pressure; Operation boiler fired with various types of coals; Conversion of heavy-oil, Gas-firing boiler into coal-firing boiler; Planning and operational result of Yokosuka No. 1 and 2 Boilers; COM Conversion; Development of high-performance Mitsubishi-CE Bowl Mill; Operating performance and updated technology of flue-gas desulfurization system for coal-firing thermal power plants; Current technology on electrostatic precipitator for coal-fired boiler; Ash-treatment system in coal-firing thermal plant; RandD of CWM combustion; Development of de-ashing method for coal fine particles; Tangential corner-fired boiler with low-volatile-matter content coals; Design of large-capacity pressurized two-stage entrained-flow-type coal gasifier for utility power plant; Technical observation on gas turbines burning coal gas; Evaluation technique of wear properties of imported coals for world wide countries; Studies on upgrading of low-grade coals by heat treatment; Evaluation of coal-liquefaction process; Research and development of deashing and hydrocracking technology for coal-derived liquid-solvent deashing and ebullated bed reactor;application of laser-measurement technologies to coal-water mixture combustion studies.
The seams are 0.5-2.5 m thick, and inclined at 70-100 gon with friable roof and floor strata. The high-ashcoal is blended with imported German coals and other Iranian coals for metallurgical coke production, and is also used in a power station. The coal is expensive because of the geological conditions, the newness of the coal mining industry, and the great distances between the mine and consumers. (In German)
The increasing demand for thermal coal for electricity generating power plants, especially in the Asia - Pacific region, is causing operators to consider a wider range of coals to increase their diversity of suppliers and the lower fuel costs. This report examines the combustion performance of Queensland Bowen Basin coals. It focuses on the combustion performance of these medium volatile coals in the Stanwell power station. The pilot-scale evaluations on low volatile coals and the use of these coals in blends has shown that these Bowen Basin coals can be burned in blends with higher volatile coals, resulting in better flame stability characteristics and carbon-in-ash. 13 refs., 11 figs., 6 tabs.
Under the auspices of the Department of Energy and private industry, considerable progress has been made in: preparation of coal-water fuels; combustion of low-ashcoal-based fuel forms; and in processes to provide deeply-cleaned coal. Since the inception of the project, we have: developed formulations for stabilizing wet filter cake into a granular free flowing material (Mulled Coal); applied the formulation to wet cake from a variety of coal sources ranging from anthracite to subbituminous coal; evaluated effects of moisture loss on mull properties; and developed design concepts for equipment for preparing the Mulled Coal and converting it into Coal Water Fuel.
Indian economic growth is significant and real rate of economic growth continues 9% for several years. UN predicts that the population of India will outstrip China in 2030. Coal resources are placed more expectations on in rapid increase of demand for energy. On the one hand, Indian coal is characteristic having normally high ash content and difficulty of coal separation. This report introduces coal demand and supply, coal field, issues of coal utilization, road map and present movement of CCT, specialty of Indian coal and issues of coal preparation technology through JCOAL's study carried out more than 5 years.
The presence of large amounts of alkali metals, chlorine and sulphur in most biomass fuels - compared to coal - can create serious ash-related problems such as deposition, agglomeration and/or corrosion. This paper discusses the viscosity characteristics of fly ash from the co-combustion of various coal/biomass blends in a pilot scale pf-boiler. The produced data provide information on the melting of the ash and its flow characteristics, as a function of temperature, which may be used to modify the temperature profile of the boiler in order to avoid slagging. Straw co-firing lowers the ash viscosity leading to higher stickiness of the ash particles. Wood co-firing has only minor effects, due to the composition of wood ash and the low percentage of wood in the coal/biomass blend.
Coal bottom ashes produced from three thermal power plants were used in column and batch experiments to investigate the adsorption capacity of the coalash. Hydrogen sulfide and leachates collected from three sanitary landfill sites were used as adsorbate gas and solutions, respectively. Experimental results showed that coal bottom ash could removal H{sub 2}S from waste gas or reduce the concentrations of various pollutants in the leachate. Each gram of bottom ash could remove up to 10.5 mg of H{sub 2}S. In treatment the landfill leachate, increasing ash dosage increased the removal efficiency but decreased the adsorption amount per unit mass of ash. The adsorption of pollutants in the leachate conformed to Freundlich's adsorption model. 14 refs., 12 figs., 3 tabs.
The problem of pollution caused by coal-fired thermal power plants is still of importance because of the tremendous growth in use of electrical energy. The wastewaters of a typical coal fired power plant include cooling tower blowdown, wastewaters from ash handling system, boiler blow-down, regenerate wastes, floor and yard drains, coal pile run off, etc. The solid waste is the fly ash. The present communication deals with the physico-chemical characteristics of fly ash pond effluent and the fly ash and their effects on certain chemical properties of soil, seed germination pattern and the growth of some crop plants. The plants selected for these studies were as follows: for fly ash pond effluent - kidney bean ([ital Phaseolus aureus]) and lady's finger ([ital Abelmoschus esculentus]), whereas for the fly ash - wheat ([ital Triticum aestivum]) and pea ([ital Pisum sativum]). 20 refs., 7 tabs.
Fly ash from electrostatic precipitators at the Belchatow power plant was used as a stabilizing additive to sand from spoil banks of the Belchatow surface mine. Fly ash hardening and its dependence on relation of ash to water was analyzed. Compression strength of fly ash after a minimum hardening time was higher that that of soil samples from Belchatow. Mixing fly ash with sand was especially economic. During the experiments sand to fly ash ratio ranged from 1:0.2 to 1:0.5. Fly ash ratio of 1:0.3 was optimum. Compression strength of sand mixed with 30% fly ash exceeded that of sand alone, irrespective of moisture content. Use of fly ash for stabilizing spoil banks consisting of sand from the Belchatow brown coal mine is recommended. 6 refs.
Factors are analyzed which influence erosion by fly ash of boilers with coal fired furnaces. The analysis is based on tests and experiments carried out in Czechoslovakia. Brown coal from major brown coal basins in Czechoslovakia and from the USSR, and black coal from Ostrava-Karvina and Poland were used. Investigation results are shown in 2 tables and 7 diagrams. Erosion caused by fly ash depends on the mean size of fly ash grains. Erosion reaches the maximum when the mean size of fly ash grains amounts to 90 micron. Effects of travelling speed of fly ash grains on erosion are shown in a diagram. Erosive effects of fly ash are also influenced by ash content and mineral composition of ashes. Erosive effects depend on content of silica and aluminium oxides. In the case of brown coal used in power plants in Czechoslovakia content of silica and aluminium oxides is more or less constant. With increasing combustion temperature over 1,550 C erosive effects of fly ash increase. Temperature effects are insignificant when combustion temperature ranges from 1,000 C to 1,550 C. 23 references.
As the operator of Castle Peak Power Station, one of the largest coal-fired power stations in the world, CLP Power currently produces nearly 350,000 t of coalash ever year. The peak production of ash at Castle Peak occurred in 1992, when it reached close to one million t. Instead of disposing of this ash as a waste product, CLP Power has been promoting its use as a construction material since the 1980s. After a lengthy process of gaining acceptance by the construction industry, coalash is now used successfully in a variety of applications. This can only be achieved through a concerted marketing effort supported by extensive research, and by investing in facilities required to turn coalash into a product of considerable commercial value. This article reports CLP Power's success in Hong Kong. 3 figs.
Previous plant testing had been limited to the processing of minus 100 mesh classifier overflow (Upper Freeport Coal {approximately} 20% ash) with the 6-inch air-sparged hydrocyclone (ASH-6C) as reported at Coal Prep 92. The ASH-6C unit was found to provide separation efficiencies equivalent, or superior, to separations with the ASH-2C system. During the summer of 1992 the construction of the first 15-inch air-sparged hydrocyclone prototype was completed by the Advanced Processing Technologies, Inc. Installation at the Homer City Coal Preparation Plant was accomplished and testing began in October 1992. The ASH-15C unit can operate at a flowrate as high as 1,000 gpm. Experimental results are reported with respect to capacity, combustible recovery and clean coal quality.
Theoretical and experimental basis is provided for a method of determining ash and iron content of coal utilizing X-ray radiometric data. Tests are described made on coal samples of known composition (7-15% ash content of coal and 0.30% iron content of ash). A three-component mixture of carbon, aluminosilicate and iron was used as control sample. Radiometric analyzer type RPS40-01 and plutonium 238 as source of primary gamma radiation were used for determining relationships between intensity of gamma ray scatter and fluorescent radiation of iron. The method was tested on Karaganda coal preparation products and showed that ash content varied between 8% and 13.6% and iron content between 1.8% and 15.6%. Tests carried out indicate that this method may also be used to assess content of other ash forming elements, e.g. calcium, aluminium and silica. 6 refs.
Laboratory results from an initial study on the removal of SO2 from gas mixtures are reported using air-sparged hydrocyclone (ASH) technology. Tap water and alkaline solutions were used for absorption, and the influence of gas flow rate, water flow rate, and length of the ASH unit were investigated. The research results indicate thatthe air-sparged hydrocyclone can be used as a highly efficient absorber for SO2 emissions. The ASH allows for 97% SO2 removal using water alone for sulfur dioxide content in the gas phase of 5 g/m3. All SO2 is removed in weakly alkaline solution (0.01 mol NaOH/dm3). PMID:15773494
The scope of work for this task was limited to the development of a general process to evaluate coal fly ash for use in applications beyond cement and concrete. Two coal fly ash samples were evaluated for appropriateness in structural fill as an example of how to use alternative classification protocol as ash use standards are developed for the industry. The goal of this project is to develop a classification system for fly ash based on parameters that relate to performance specification of engineering and construction applications. The new classification system will provide a means of evaluating the suitability of coalash for use in certain products that currently have no reality-based standards or classifications. Recent work by the American Society for Testing and Materials (ASTM) Committee E50 on Pollution Prevention has proposed a standard practice for use of coalash for structural fill applications. Energy & Environmental Research Center (EERC) coalash researchers have worked on preparing this standard practice, and the development of criteria for the coalash to be used in this application will facilitate the use of this standard once approved by ASTM. A preliminary flowchart for classification criteria was developed and is shown in figure 1.
Coalash obtained by coal combustion in the "Nikola Tesla A" power plant in Obrenovac, near Belgrade, Yugoslavia, is mixed with water of the Sava river and transported to the dump. In order to assess pollution caused by leaching of some minor and major elements during ash transport through the pipeline, two sets of samples (six samples each) were subjected to a modified sequential extraction. The first set consisted of coalash samples taken immediately after combustion, while the second set was obtained by extraction with river water, imitating the processes that occur in the pipeline. Samples were extracted consecutively with distilled water and a 1 M solution of KCl, pH 7, and the differences in extractability were compared in order to predict potential pollution. Considering concentrations of seven trace elements as well as five major elements in extracts from a total of 12 samples, it can be concluded that lead and cadmium do not present an environmental threat during and immediately after ash transport to the dump. Portions of zinc, nickel and chromium are released during the ash transport, and arsenic and manganese are released continuously. Copper and iron do not present an environmental threat due to element leaching during and immediately after the coalash suspension and transport. On the contrary, these elements, as well as chromium, become concentrated during coalash transport. Adsorbed portions of calcium, magnesium and potassium are also leached during coalash transport. PMID:11341293
Ash deposition characteristics under high-temperature pulverized coal reaction conditions were studied using a horizontal pulverized coal reactor with pre-combustor to produce high-temperature vitiated air. The ash deposition experiments were performed by inserting a water-cooled tube into the reactor. Burning two types of coal with different melting temperature and ash content, and the ash deposition phenomena were visually and quantitatively elucidated.As a result, the quantity of ash deposition on the tube surface increases with an increase of the surface temperature. This is because the burning particles in the upper stream of the tube are radiatively cooled down under low temperature condition of the tube surface. Both the structure and quantity of ash deposition depend on coal types such as melting temperature and ash content. The deposition rate at the beginning of deposition, obtained by the peripheral width of deposition layer on the tube surface, is correlated as an Arrhenius-type equation since viscosity of the molten ash can be correlated as an Arrhenius-type equation. Hence, it suggests that the ash deposition phenomena may relate to the viscosity of molten ash.
The use of coal fines leads to a more efficient coal combustion, but a negative side-effect is the deposition of ash particulates on the walls of the combustor or gasifier. Knowledge of the performance of the coal fines particulates improves the operation of the combustion process. The coal fines conversion consists of the next chronologic processes: grinding of the coal to particulates of 50 micrometer and smaller; the complex transport of the particulates in the transport air and the combustion air determined by the Stokes number and the speed of fall; the injection of the coal fines into the boiler or furnace; the combustion for which the speed of heating and the burn-out time are essential process variables; and, the deposition of solid ashes and filtration of fly ash. An overview is given of the present knowledge of the performance of coal particulates in the above-mentioned processes. 3 figs., 8 refs., 1 tab.
The goal of this project was to develop and test an innovative coal cleaning process to reduce the ash content of coal and produce ultra clean coal (UCC). Coal samples that were prepared from concentrates of Iran's Zirab and Tabas coal preparation plants were found to have initial ash contents of 8.31 and 10.36%, respectively. These coals were demineralized with the combination of microwave irradiation pretreatment and dual acid leaching processes with HF followed by HNO3 in a batch reactor. For samples that were microwaved and leached with HF, the reduction in ash ranged from 22 to 76% and from 22 to 82% for Zirab and Tabas coal samples, respectively, depending on leaching conditions. Microwave irradiation pretreatment had a positive effect on demineralization with HF, especially for the ...
This report is a detailed review of the progress in research programs at the University of North Dakota Energy Research Center on low rank coals, involving especially: gasification pilot plant waste water treatment and reuse, hydrogen production, coal-water slurry production (and study of rheology of slurries and coal drying), combustion and fluidizied-bed combustion, flue gas characterization and purification, ashes and boiler fouling, fine coal preparation, ashes and slags characterization, chemical structure of low rank coal, moisture, supercritical solvent extraction, pyrolysis and devolatilization. (LTN)
Conventional coal fly-ash (CFA) and two coal-biomass fly-ashes (CBFAs) were obtained at a thermoelectric power station (Atikokan, Ontario) from combustion of undiluted lignite coal and co-combustion of lignite coal with up to 66% wood pellets (on a thermal basis). Fly-ashes were characterized and analyzed for use as cement admixtures. Co-combustion did not markedly change the fly-ash composition, owing to an extremely low ash content of wood pellets compared to lignite coal; toxic metals and minor elements were within ranges reported for other coal fly-ashes. All fly-ashes had losses on ignition (LOI) <1 wt% and therefore complied with ASTM LOI regulations for use in concrete. All fly-ashes contained major amorphous phases, along with quartz and periclase. Partial substitution of cement with fly-ash (up to 40 wt%) had a moderate effect on the entrained air content of mortars (up to 2.5%), but this difference vanished upon addition of air entraining agent (0.6 mL/kg of cementitious material). Substituted mortars exceeded 75% of the strength of ash-free mortar after 28 days of curing (therefore meeting ASTM requirements for strength development), and by 90 days, met or surpassed 100% of the strength of ash-free mortar. Amending mortar with 20 wt% CFA or CBFA had no effect on its durability following repeated freeze-thaw cycles when air content was kept constant. Also, no micromineralogical differences were observed between hydrated CFA- and CBFA-amended mortars, with fly-ash particles reacting with Ca ions originating from dissolution of cement clinker or calcium hydroxide. 53 refs., 17 figs., 3 tabs.
Utilize sintering method to extract alumina from coalash. The effects of sintering flux categories, sintering flux cooperation, sintering flux dosage, temperature and time on the leaching ratio of alumina from coalash was studied. The results show that sodium hydroxide can extract the most alumina from coalashes than natronite and lime at a lower temperature and the leaching ratio of alumina is higher when sintered coalashes is mixed with sodium hydroxide and lime. Suitable quantities of lime can accelerate sodium hydroxide to leach the alumina from coalash. The factors of sintering process such as alkali ratio, calcium ratio, sintering temperature, sintering time have a great impact on the leaching ratio of alumina in coalash. These influencing factors was investigated by orthogonal experiment. The order of influence from big to small of these four factors is calcium ratio, sintering time, alkali ratio, sintering temperature. When the alkali ratio is 2:1, the calcium ratio is 0.5:1.0, sintering temperature is 700{sup o}C and sintering time is 30 min, the leaching ratio of alumina in coalash reached 76.20%. 14 refs., 2 figs., 4 tabs.
Coal mines are required to provide ventilation to occupied portions of underground mines. Concrete block is used in this process to construct air duct walls. However, normal concrete block is heavy and not easy to work with and eventually fails dramatically after being loaded due to mine ceiling convergence and/or floor heave. Autoclaved cellular concrete block made from (70{plus_minus}%) coal fly ash is lightweight and less rigid when loaded. It is lighter and easier to use than regular concrete block for underground mine applications. It has also been used in surface construction around the world for over 40 years. Ohio Edison along with eight other electric utility companies, the Electric Power Research Institute (EPRI), and North American Cellular Concrete constructed a mobile demonstration plant to produce autoclaved cellular concrete block from utility fly ash. To apply this research in Ohio, Ohio Edison also worked with the Ohio Coal Development Office and CONSOL Inc. to produce autoclaved cellular concrete block not only from coalash but also from LIMB ash, SNRB ash, and PFBC ash from various clean coal technology projects sponsored by the Ohio Coal Development Office. The purpose of this project was to demonstrate the potential for beneficial use of fly ash and clean coal technology by-products in the production of lightweight block.
Several approaches are established to analyse the fouling and slagging propensities of coalashes, but the same cannot be said of solid recovered fuel (SRF) ashes. This work has been conducted by using some fouling and slagging indicators, which are commonly applicable to coalashes, on SRF ashes to ascertain their applicability. In this work, laboratory prepared ashes derived from municipal solid waste (MSW), sewage sludge, demolition wood, shredded rubber tyres, and plastic/paper fluff are analysed for their fusibility leading to fouling and slagging using three approaches; the ash fusibility temperatures (AFT), ternary phase diagrams, and fouling/slagging indices. The results from each approach are examined to determine the inclination of the ashes toward fouling and slagging. A subsequ...
This paper introduces an economical and simple experimental method to measure the onset sintering temperature of mixed coalash. The pressure drop along with the ash bar versus temperature raised at range of 2{sup o}C/min 4{sup o}C/min temperature-increasing rate is measured with air flow rate at 10 mL/min 40 mL/min. The onset sintering temperature of mixed coalash is the temperature at which the pressure drop reaches maximum. The onset sintering temperatures of IHI CFB boiler ash and Qin Guangdao CFB boiler ash were measured. The onset sintering temperature of IHI CFB boiler ash is 900{sup o}C {+-} 10{sup o}C, which can partially explain the phenomena of the IHI CFB boiler can not run smoothly due to the sintering of ash and slag. 7 refs., 6 figs.
For several years, Municipal Solid Waste Incineration (MSWI) bottom ash and coal fly ash have been reused in civil engineering. Although their physical-chemical characteristics are very studied, the toxicity of these materials is the issue of few works. This study aims at contributing to the evaluation of the impact on the ecosystems of the valorization of these residues of thermal processes (RTP) in road engineering. We have compared the potential toxicity of MSWI bottom ash resulting from traditional collection and MSWI bottom ash resulting from selective collection. Since physicochemical parameters of MSWI bottom ash weathering is quite important, we will see the effect of artificial carbonation on the potential toxicity. We have chosen to work with whole-cell microorganisms from the compartment of the producers (algae: Chlorella vulgaris) and from the compartment of the decomposers (yeasts: Saccharomyces cerevisiae). The use of tests using global metabolism (algae growth) and more specific tests (enzymatic activities) have allowed to compare the potential toxicity of MSWI bottom ash resulting from traditional collection and MSWI bottom ash resulting from selective collection. These bioassays have shown that artificial carbonation may decrease the potential toxicity of these MSWI bottom ash. The behavior of coal fly ash used in various scenarios of pilots of road has also been revealed. The development of an optical bio-sensor with immobilized whole cells will enable on line and in-situ monitoring of pollutants salting out MSWI bottom ash and coal fly-ash from pilots of roads. (author)
The present paper reports the result of Moessbauer spectroscopic investigations of the transformations of different iron-bearing minerals in some Indian coals of different geological origin with varying mineral contents during their ashing and pulverized fuel combustion (PFC). The iron-bearing minerals thus characterised in the coals include Fe{sup 2+}-illite (Lodna, Jammu and Singareni coals); pyrite (Jammu, and Singareni coals, in the latter in association with marcasite); siderite (Lodna coal); ankerite (Singareni coal); and szomolnokite (Jammu coal). The corresponding ashes produced after ashing at 800{degree}C are found to contain in general, Fe{sup 3+}-glass silicate and haematite, with additional species of magnesioferrite in Singareni coalash, wherein Fe{sup 3+}-glass silicate is the decomposition product of Fe{sup 2+}-illite, and haematite is that of oxidation of pyrite and siderite, magnesioferrite being derived from ankerite. Quite different from this, the Moessbauer spectra of the fly ashes produced as a result of PFC in Vijayawada and Kothagudam Thermal Power Stations are very complex, comprising superimposed sextets and doublets of oxides (haematite, magnetite, geothite), Fe{sup 3+}-silicate and Fe{sup 3+}/Fe{sup 2+}-mullite, indicative of local nature of combustion (viz. method of firing, mineralogy of coals, as well as residence times of coal particles in the flame zone) via intricate mineral interactions during PFC in lower and higher temperature zones under both oxidising and reducing conditions. These studies thus provide clues to the reaction pathways during the combustion process. 37 refs., 4 figs., 2 tabs.
A technique employing SEM-based automated image analysis (AIA) has been developed for assessing the association of mineral particles with coal, and thus the cleanability of that coal, when the characteristics of the separation process are known. Data resulting from AIA include the mineral distribution by particle size, mineral phase, and extent of association with coal. This AIA technique was applied to samples of {minus}325 mesh ({minus}44 {mu}m) coal from the Indiana No. 3, Upper Freeport, and Sunnyside (UT) seams. The coals were subjected to cleaning by float-sink separations at 1.3, 1.4, 1.6, and 1.9 specific gravity and by froth flotation. For the three coals, the float-sink procedure at a given specific gravity produced different amounts of clean coal, but with similar ash content. Froth flotation removed much less ash, yielding a product ash content of {approximately}8% for the Upper Freeport coal, regardless of recovery, while reducing the ash content to less than 5% for the other two coals. The AIA results documented significantly more association of minerals with the Upper Freeport coal, which thus led to the poor ash reduction.
The fractal structure of five different coals with carbon content of 79 to 91% was studied by adsorption of nitrogen. It was shown that the coal surfaces have a fractal nature and their irregularity depends on coal rank, ash content and H/C ratio. 3 refs., 1 tabs.
The Eastern Kentucky Coal Field has been, and continues to be, a major source of high quality coal for electric utilities, and the steel industry` Economical coal resources are primarily confined to the Breathitt Formation, which contains more than 100 named coal beds. Analyses of over 1,500 samples show these beds to average 10.7 percent ash, and 1.7 percent sulfur. These values are not spatially or temporally uniform, however. A stratigraphic comparison of eight major economical coal beds/zones shows average ash yields to increase, and become more variable, in younger coals. This trend may be related to the increased occurrence of coal splitting in younger coals, with otherwise low ashcoal being intercalated with higher ashcoal, shale, and siltstone. Average total sulfur contents. in contrast, assume a more normal distribution, with the oldest and youngest coal beds/groups being lower in sulfur, and middle-aged beds/groups being higher in sulfuric. Average Arsenic concentrations mirror this trend. This trend may be a function of these middle-aged beds/groups being capped by well-developed, widespread marine zones, in contrast to younger and older beds/groups which are more commonly covered by strata of fresh water origin. Spatial trends are also evident. Geographically, the Eastern Kentucky Coal Field is divided into six Reserve Districts.
The objective of this project is to demonstrate pulse combustion induced acoustic enhancement of coalash agglomeration and sulfur capture at conditions typical of coal-fired turbines. Results of experiments conducted on a process development unit with a pulverized coal and four different sorbents for sulfur capture have been performed. Results are briefly discussed.
Presentations at the International Conference on Ferroalloy Production relating to new carbon reducing agents as an alternative to coke are briefly summarized. Such reducing agents include lightweight reducing agents (peat, lignin, wood chips), coal D and the corresponding semicoke, lean coal, oil coke, low-ashcoal, and Karelian shungite. The results of their industrial use are described.
A method of recovering coal liquids and producing metallurgical coke utilizes low ash, low sulfur coal as a parent for a coal char formed by pyrolysis with a volatile content of less than 8%. The char is briquetted and heated in an inert gas over a prescribed heat history to yield a high strength briquette with less than 2% volatile content.
Effect of magnetization on oxygen concentration, pH, surface zeta potential, and wet heat of flotation pulp were researched. The result shows that magnetization treatment can improve the floatablility of coal and increase the difference in wet heat among coal, refuse, and pyrite, which is favorable for slime flotation and for removing sulfur and ash from coal.
In the reported study, the rate of reaction of finely dispersed ash-rich coal with steam in the range of temperatures of 1650-2100/degree/K has been determined. The behavior of the porous structure of the coal has been studed. It has been shown that at the temperature investigated the reaction profoundly changes the internal specific surface of the coal particles. 3 refs.
Assam coal was reductively acylated by using zinc dust, acetic acid and phenol. This reaction resulted in enhanced extractability of coal in quinoline. The residue extracted after the first step was further reductively acylated which rendered it further extractable in quinoline. Three successive steps could solubilize the coal to the extent of 58 per cent on ash balance basis.
this article discusses the internal friction, fluidity, adhesion forces and tensile strength of pulverized coal and coalash at different temperatures and moisture contents. Different types of coal are studied and the results compared with the same properties of other particulate substances. (32 refs.) (In Japanese)
Coal extraction experiments were conducted using a coal, containing ca. 10% ash, from the Tshikondeni mine in South Africa. This coal dissolves only to a limited extent in pure polar aprotic solvents such as dimethylformamide (DMF) and N-methyl-2-pyrrolidinone (NMP). However, the addition of a stron...
The mineral matter in typical feed coals used in South African gasification processes and the ash derived from gasifying such coals have been investigated using a variety of mineralogical, chemical and electron microscope techniques. The mineral matter in the feed coals consists mainly of kaolinite,...
Studies laboratory production of high quality and water resistant fuel from low-grade brown coal, peat and bagasse. Raw materials investigated were Bulgarian Maritza-Iztok brown coal (20.7% ash, 5% sulfur content), Merseburg saliniferous brown coal from the GDR (2.82% sodium oxide content), Bulgarian Elkhovo brown coal (38% ash, 6% sulfur content), Kansk-Achinsk hard brown coal (11.4% ash content), Emstaler Niederung peat (23.4% ash) and Cuban sugar cane bagasse. The common feature of briquets produced from all materials is their disintegration in water within a few hours due to swelling of clay minerals and organic matter. Semicoking to 600/sup o/C or high temperature coking to 1,000/sup o/C is pointed out as a method of producing a high quality combustion coke with compression strength higher than 20 MPa. The coked briquets will withstand disintegration by water impact. Graphs and tables are provided showing briquetting and coking parameters applied. 19 refs.
For this quarter, West Virginia University has completed the extraction of the Hydrocarbon Technology, Inc. (HTI) O-6 bottoms coal product. Recall that the material was vacuum distilled earlier at the Koppers Technical Center in Harmarville, PA to remove liquefaction solvent and other low-boiling substances. There are now approximately 25 kg (about 55 pounds) of extracted coal product available for further testing and evaluation. A portion of the extracted HTI coal liquid was converted into green coke in a laboratory-scale atmospheric still coker. The ash content of 0.7 wt% may be too high for the extracted coal liquid to be used directly in carbon products. To reduce the ash-reforming constituents further, a series of filtrations was performed using a Millipore pressure filter apparatus. Table 2 lists the results of the ash determinations for the coal material after filtration through filters of different particle retention capability. Efforts are now being pursued to remove the ash forming material by selective extraction.
The role of slimes in coal flotation has been the subject of controversy in the literature, and the present study is designed to determine the effect of the nature of the clay on coal flotation. Kaolinite and illite, which do not significantly depress coal flotation, contaminate the floated clean coal largely by carry-over with the froth, though electrostatic attachment to the coal contributes in a lesser way to the ash content of the froth. Bentonite greatly depresses all but the most hydrophobic of coals by armour-coating of the bubbles, preventing coarse particle attachment, and increasing slime coatings, all because of its high surface area, charged sites, and ion-exchange-capacity. Common clay dispersants were found to depress coal flotation. Fuel oil improves coal recovery in the presence of clay slimes, but the ash and pyrite content of the floated coal also increases. 4 figs., 7 tabs., 37 refs.
For much of the U.S., coal-fired power plants are the most important source of electricity for domestic and industrial use. Large quantities of fly ash and other coal combustion by-products are produced every year, the majority of which is impounded in lagoons and landfills located throughout the country. Many older fly ash disposal facilities are unlined and have been closed for decades. Fly ash often contains high concentrations of toxic trace elements such as arsenic, boron, chromium, molybdenum, nickel, selenium, lead, strontium and vanadium. Trace elements present in coal fly ash are of potential concern due to their toxicity, high mobility in the environment and low drinking water MCL values. Concern about the potential release of these toxic elements into the environment due to leaching of fly ash by acid rain, groundwater or acid mine drainage has prompted the EPA to develop national standards under the subtitle D of the Resource Conservation and Recovery Act (RCRA) to regulate ash disposal in landfills and surface impoundments. An attempt is made to predict the leaching of toxic elements into the environment by studying trace element partitioning in coal fly ash. A seven step sequential chemical extraction procedure (SCEP) modified from Filgueiras et al. (2002) is used to determine the trace element partitioning in seven coal fly ash samples collected directly from electric power plants. Five fly ash samples were derived from Eastern Bituminous coal, one derived from Western Sub-bituminous coal and the other derived from Northern Lignite. The sequential chemical extraction procedure gives valuable information on the association of trace elements: 1) soluble fraction, 2) exchangeable fraction, 3) acid soluble fraction, 4) easily reducible fraction, 5) moderately reducible fraction, 6) poorly reducible fraction and 7) oxidizable organics/sulfide fraction. The trace element partitioning varies with the composition of coal fly ash which is influenced by the type of coal burned. Preliminary studies show that in some fly ash samples, significant amounts of As, B, Mo, Se, Sr and V are associated with the soluble and exchangeable fraction, and thus would be highly mobile in the environment. Lead, on the other hand, is mainly associated with the amorphous Fe and Mn oxide fractions and would be highly immobile in oxidizing conditions, but mobile in reducing conditions. Ni and Cr show different associations in different fly ash samples. In most fly ash samples, significant amounts of the trace elements are associated with more stable fractions that do not threaten the environment. The study of trace element partitioning in coal fly ash thus helps us to predict their leaching behavior under various conditions.
Controlled incubation studies (120 h at 37{sup o}C) using a mixture of 32% biosolids and 68% wood shavings (dry weight basis) amended with ash (biosolids blend:ash = 1:0.3, dry weight) were conducted to evaluate the influence of ash on odor emissions and biological activity of the mix. Three coal fly ashes (high carbon, medium carbon, and low carbon), wood fly ash, and activated carbon were evaluated against a no-ash control. The concentration of dimethyl disulfide (DMDS), dimethyl sulfide (DMS), and CO{sub 2} in the exhaust gas was measured at 0, 24, 48, 72, 96, and 120 h. Data were used to calculate emission rates and cumulative emission, which were analyzed to determine treatment differences. Results show that peak emission rates of DMDS and DMS in the no-ash control treatment were 41.9 and 1.89 {mu}g/kg/min, respectively, while 120-h cumulative emissions were 189.95 and 11.39 mg/kg, respectively. Amendments reduced peak DMDS emission rates in all treatments. Percent reductions were highest in activated carbon and wood fly ash at 90% and 63%, respectively. For the three coal fly ashes, percent reduction ranged from 18% to 24%. Percent reduction in 120-h cumulative DMDS emission for high carbon, medium carbon, and low carbon coalashes, wood ash, and activated carbon compared to the no-ash control were 41%, 29%, 53%, 59%, and 89%, respectively. In contrast, the peak emission rate for DMS increased while using two coalash treatments and the wood fly ash treatment, where percent increases were 54% to 122% compared to the control. There was no difference in biological activity between treatments based on maximum CO{sub 2} production rates, which were in the range of 34 to 42 mg/kg/min. These rates correspond to 2.04 to 2.52 mg/g/hr of CO{sub 2} production, representing high biological activity.
The need to recycle waste products is becoming more crucial as the cost of their disposal escalates and the availability of conventional materials becomes scarce. Two such by-products of the coal industry, coal refuse and fly ash, have shown promise as construction materials. In view of the projected shift from oil to coal for electric power generation, the already abundant supply of both coal refuse and fly ash is expected to increase along with their disposal cost. This report outlines the findings of a study into the utilization of coal refuse-fly ash compositions as highway base course material. It includes a discussion of the results from an extensive laboratory testing program into the physical and engineering properties of mixtures of these waste products and a comparison of serviceability index and physical damage parameters based on the VESYS Predictive Design Procedure between crushed stone and coal refuse-fly ash compositions. These findings indicate that substituting stabilized coal refuse-fly ash blends in place of conventional base course material is technically and economically feasible. In-service usage of these stabilized mixtures should now be verified by appropriate field testing. The report also presents procedures for developing design mixes and conducting field tests of coal refuse-fly ash base course material.
Contents, concentration trends, and modes of occurrence of 67 elements in coals, coalashes, and combustion wastes at eleven Bulgarian thermoelectric power stations (TPS) were studied. A number of trace elements in coal and coalash have concentrations greater than their respective worldwide average contents (Clarke values). Trace elements are concentrated mainly in the heavy accessory minerals and organic matter in coal. In decreasing order of significance, the trace elements in coal may occur as: element-organic compounds; impurities in the mineral matter; major components in the mineral matter; major and impurity components in the inorganic amorphous matter; and elements in the fluid constituent. A number of trace elements in the waste products, similar to coalashes, exceed known Clarke contents. Trace elements are mainly enriched in non-magnetic, heavy and fine-grained fractions of fly ash. They are commonly present as impurities in the glass phases, and are included in the crystalline components. Their accessory crystalline phases, element-organic compounds, liquid and gas forms, are of subordinate importance. Some elements from the chalcophile, lithophile and siderophile groups may release into the atmosphere during coal burning. For others, the combustion process appears to be a powerful factor causing their relative enrichment in the fly ash and rarely in the bottom ash and slag. 65 refs., 1 fig., 11 tabs.
Current regulations classify fly ash as a prescribed waste and prohibit its disposal in regular landfill. Treatment of the fly ash can reduce the leach rate of metals, and allow it to be disposed in less prescribed landfill. A geopolymer matrix was investigated as a potential stabilisation method for brown coal fly ash. Precipitator fly ash was obtained from electrostatic precipitators and leached fly ash was collected from ash disposal ponds, and leaching tests were conducted on both types of geopolymer stabilised fly ashes. The ratio of fly ash to geopolymer was varied to determine the effects of different compositions on leaching rates. Fourteen metals and heavy metals were targeted during the leaching tests and the results indicate that a geopolymer is effective at reducing the leach rates of many metals from the fly ash, such as calcium, arsenic, selenium, strontium and barium. The major element leachate concentrations obtained from leached fly ash were in general lower than that of precipitator fly ash. Conversely, heavy metal leachate concentrations were lower in precipitator fly ash than leached pond fly ash. The maximum addition of fly ash to this geopolymer was found to be 60wt% for fly ash obtained from the electrostatic precipitators and 70wt% for fly ash obtained from ash disposal ponds. The formation of geopolymer in the presence of fly ash was studied using 29Si MAS-NMR and showed that a geopolymer matrix was formed. X-ray diffraction (XRD) analysis and scanning electron microscopy (SEM) imaging showed the interaction of the fly ash with the geopolymer, which was related to the leachate data and also the maximum percentage fly ash addition. PMID:15511575
Current regulations classify fly ash as a prescribed waste and prohibit its disposal in regular landfill. Treatment of the fly ash can reduce the leach rate of metals, and allow it to be disposed in less prescribed landfill. A geopolymer matrix was investigated as a potential stabilisation method for brown coal fly ash. Precipitator fly ash was obtained from electrostatic precipitators and leached fly ash was collected from ash disposal ponds, and leaching tests were conducted on both types of geopolymer stabilised fly ashes. The ratio of fly ash to geopolymer was varied to determine the effects of different compositions on leaching rates. Fourteen metals and heavy metals were targeted during the leaching tests and the results indicate that a geopolymer is effective at reducing the leach rates of many metals from the fly ash, such as calcium, arsenic, selenium, strontium and barium. The major element leachate concentrations obtained from leached fly ash were in general lower than that of precipitator fly ash. Conversely, heavy metal leachate concentrations were lower in precipitator fly ash than leached pond fly ash. The maximum addition of fly ash to this geopolymer was found to be 60 wt% for fly ash obtained from the electrostatic precipitators and 70 wt% for fly ash obtained from ash disposal ponds. The formation of geopolymer in the presence of fly ash was studied using 29Si MAS-NMR and showed that a geopolymer matrix was formed. X-ray diffraction (XRD) analysis and scanning electron microscopy (SEM) imaging showed the interaction of the fly ash with the geopolymer, which was related to the leachate data and also the maximum percentage fly ash addition.
underground coal extraction systems The model documentation includes the programming .... wet scrubbing), and the alkalinity and heat value of the coal being scrubbed ...... The EEA coal model does not directly simulate the interaction between ...... obtained from EPA's Utility FGD Survey The report is published quarterly ...
It was proven that alkaline catalysts such as K2C03 and KOH, were the most effective catalysts in the gasification process of coal. The way of introducing the catalyst, e.g., by dry mixing with the coal, by impregnating coal with water solutions of the ca...
In 1980, the Belville Amendments to RCRA instructed EPA to 'conduct a detailed and comprehensive study and submit a report' to Congress on the 'adverse effects on human health and the environment, if any, of the disposal and utilization' of coalash. In both 1988 and 1999, EPA submitted reports to Congress and recommended coalash should not be regulated as hazardous waste. After the failure of a Tennesse power plant's coalash disposal facility, EPA will be proposing new disposal regulations.
Since 1967, at least six ash utilization symposiums have been held in the United States, with papers presented by several European authors on the utilization of coal by-products in Eastern Europe. There is currently over 80,000 megawatts of installed coal-fired capacity available in that region. Unfortunately, of the 117,778,000 tonnes of fly ash, bottom ash, and slag produced in Eastern Europe in 1989, only 13% was utilized. This paper outlines the research and levels and kinds of coal by-product utilization taking place in Eastern Europe since the late 1960s.
Based on the higher ash content in clean coal from flotation processes carboxymethylcellulose was added (CMC) as depressant to reduce the ash content of clean coal. The paper analyzed the depressant mechanism by Fourier Transform Infrared Spectroscopy. The results show that the ash content can be reduced by 1-2% when adding CMC 30 g/t in the flotation process, and the depressant mechanism is that CMC can selectively absorb to gangue to enhance its hydrophilic characteristics and enlarge the surface properties difference between coal and gangue, in order to inhibit gangue. 4 refs., 4 figs., 4 tabs.
Two commonly used revegetation species, Kentucky 31 tall fescue (Festuca arundinacea Schreb.) and Lincoln smooth brome (Bromus inermis Leyss.), were grown for 60 days in pots containing coarse coal mine refuse (referred to as gob, pH = 3.5) amended with either lime or alkaline powerplant fly ash. Both species were also grown in pots containing a silt loam surface soil as a control. Morphological growth parameters were measured over time; dry weights and shoot/root ratios were determined at harvest. Concentrations of Al, As, Cd, Co, Cr, Cu, Fe, Hg, Mn, Ni, Pb, Se, V, and Zn in the plant shoots were determined by atomic absorption spectrophotometry. Plant growth of both species was not as good on either lime- or fly ash-amended gob as it was on surface soil; however, more vigorous growth occurred on lime-amended gob than on fly ash-amended gob. Significant differences (rho < 0.05) in the tissue concentrations of Cd, Co, Fe, Hg, Mn, Pb, V, and Zn were found among the plants grown on the three substrates. Except for Hg and Pb, these elements were higher in plants grown on at least one of the amended-gob substrates than in plants grown on surface soil. Significant substrate differences were not observed for Al, As, Cr, Cu, Ni, and Se. The tissue concentrations of some elements - notably Al, Cu, Fe, Mn, V, and Zn - were high enough in plants from one or more of the substrates to either approach or exceed concentrations which have been reported to be associated with toxic effects in some plant species.
Two commonly used revegetation species, Kentucky 31 tall fescue (Festuca arundinacea Schreb.) and Lincoln smooth brome (Bromus inermis Leyss.) were grown for 60 days in pots containing coarse coal mine refuse (referred to as gob, pH = 3.5) that was amended with lime or alkaline fly ash. Both species were also grown in pots containing a silt-loam surface soil as a control. Morphological growth parameters were measured over time; dry weights and shoot:root ratios were determined at harvest. Concentrations of Al, As, Cd, Co, Cr, Cu, Fe, Hg, Mn, Ni, Pb, Se, V, and Zn in the plant shoots were determined by atomic absorption spectrophotometry. Plant growth of both species was not as good on either lime- or fly ash-amended gob as it was on surface soil. Although plant height and length of the longest lead were not significantly different (p > 0.10) at the end of the experiment for plants grown on the two amended-gob substrates, parameters giving an indication of plant vigor (i.e., number of leaves and stems, width of the longest lead, and biomass) were significantly greater (p < 0.01) for plants grown on lime-amended gob than for those grown on fly ash-amended gob. Significant (p < 0.05) differences in the tissue concentrations of Cd, Co, Fe, Hg, Mn, Pb, V, and Zn were found among the plants grown on the three substrates. Except for Hg and Pb, these elements were higher in plants grown on at least one of the amended-gob substrates than in plants grown on surface soil. Significant substrate differences were not observed for Al, As, Cr, Cu, Ni, and Se. The tissue concentrations of some elements - notably Al, Cu, Fe, Mn, V, and Zn - were high enough in plants from one or more of the substrates to either approach or exceed concentrations that have been reported to be associated with toxic effects in some plant species.
The CONSOL research combustor, equipped with a low-NO{sub x} burner, was used to assess the impact of coal properties on NO{sub x} emissions and loss-on-ignition (LOI) for coals ranging in rank from lignite to low-volatile bituminous. The coal property variables were volatile matter content, nitrogen content, pulverized coal fineness and coal rank. Volatile matter content was the coal property with the greatest effect on NO{sub x} emissions, followed by coal rank, nitrogen content and coal fineness. High-volatile bituminous coals produced lower NO{sub x} emissions than low-volatile bituminous coals, regardless of the nitrogen content. With some exceptions, lower rank coals produced lower NO{sub x} emissions. For the bituminous coals, the effect of coal fineness on NO{sub x} emissions depended on the volatile matter content; finer coal grinds reduced NO{sub x} emissions for high-volatile coals and increased NO{sub x} emissions for low-volatile coals. Coal rank was the coal property with the greatest effect on LOI; lower rank coals produced lower LOI. LOI correlated strongly with the oxygen content of the coal (a measure of reactivity and rank) and the coalash content. Finer coal grinds significantly reduced LOI.
If energy sources are to be called renewable, they must be used on the conditions set by nature and natural balance must be maintained. The ash from biofuels from forests contains almost all the minerals and nutrients (except nitrogen) which were present in the fuel and should be recycled to the forest. This conference paper describes the composition and properties of ash, its production and handling, and its ecological effects when recycled. The chemical properties of ash depend largely on the content of minerals, nutrients and heavy metals in the fuel, and on how the combustion process is conducted. Ash from bioforests or from waste combustion may contain heavy metals and may be unsuitable for recycling. Ash is strongly alkaline and needs processing before recycling. In forests that grow on peat the addition of ash causes a strong growth of trees. On firm ground, however, the effect of adding ash is more in the nature of long-time forest care. 4 refs.
Rainwater samples of a rural region around a coal plant in the northeast of Parana State (Brazil) were evaluated. Samples of bulk and wet deposition were analyzed during a one-year period (June 1999 - June 2000). A great number of rain events (70%) presented pH values below 5.6 (volume weight mean - VWM was pH = 4.9 {+-} 0.7), indicating that the region rainwater was lightly acid. The anions and cations concentrations results in the sampled rainwater showed a high sulphate concentration (69 {mu}eq L{sup -1}), followed by the cations concentration of sodium, calcium and ammonium (35, 32 and 30 {mu}eq L{sup -1}, respectively). The analysis of different data of the region showed that one probable source of the high sodium concentration could be from adsorbed sodium at the fly ash after the coal burning process. Due to the great contribution of these cations in the sulphate neutralization action, the rainwater of this region had only a lightly acid characteristic, which not caused a significant environmental impact. The study of the local soil showed that the soil characteristic was of an acid soil and bioavailable concentration of the alkaline (calcium, magnesium and potassium) and acid (aluminium) cations presented high calcium concentration [(1001{+-} 357) mg kg{sup -1}] compared with the other cations. The determination of the soil sensitivity to acid rain was calculated by the ratio BC/Al{sup 3+} (BC is the sum of the alkaline cations) and presented an average value of (5.1 {+-} 3.3). The preliminary evaluation of the soil susceptibility to acid rain by the ratio BC/Al{sup 3+}, showed that the local soil and type of vegetation (tropical savannah) were sensitive to acid deposition. A long term of this impacting condition (acid rain) could be harmful to the soil and vegetation quality. (author)
The purpose of this study is to compare the suitability of five laboratory methods for predicting the ash sintering occurring during the combustion of biomass. The studied methods have been the following: fusibility under DIN norms, measurement of the compression strength of ash pellet previously heated at different temperatures, manual disintegration of biomass ash obtained at different temperatures, relating alkaline earth oxides to alkaline oxides, and representation in a ternary phase diagram SiO{sub 2}-CaO-K{sub 2}O. The two last theoretical methods are based on the analysis of biomass ash elements. The ash sintering behaviour results obtained with these methods for different biomasses have been compared with the ash sintering results obtained in combustion tests of the same biomasses in a 1 MWth bubbling fluidised bed combustion (BFBC) pilot plant, with silica as initial bed material. The compression method does not predict adequately the ash sintering behaviour of woody fuels and other biomasses with a lower content in alkaline elements. The disintegration and fusibility methods predict with success the sintering behaviour of most of the tested biomasses. Both theoretical methods have been less reliable to predict the ash sintering behaviour than disintegration and fusibility test methods. 13 refs., 4 figs., 3 tabs.
The aim of the present investigation was to identify and quantify the iron mineral phases present in South African coal from various coal fields and in coalash, after industrial and laboratory combustion processes, and to determine the changes that occur in these phases during weathering. Iron in coal is mainly associated with sulphur in the minerals pyrite and jarosite, whilst other iron-bearing minerals such as illite and ankerite also occur, but also occurs as a trace element in kaolinite, a major clay mineral present in coal. The amounts of these minerals vary considerably in coals from diverse origins and thus coal samples from six coal-producing areas in South Africa were studied by means of Mössbauer spectroscopy and SEM analyses. With the aid of Mössbauer spectroscopy, the iron-bearing minerals were identified in the coal, coalash and weathered coal, whereas in the SEM analyses, apart from these minerals, the non-iron-bearing minerals were identified and found to be mainly quartz, clay minerals and carbonates. Differences in mineral composition were found between the coals from the different regions. Ash samples, obtained from the Lethabo electricity power plant, South Africa, were investigated and laboratory simulations were performed to obtain a comparable analysis of the industrial ash samples. At the high temperatures (~1400°C) of combustion in the power plant, fly ash and agglomerates are produced and the Mössbauer spectra resulted in two poorly developed doublets, typical of glass. In the laboratory simulation, carried out at temperatures ranging from 200° to 1200°C it was clearly observed how the pyrite changed to hematite and finally was taken up in the glass in addition to the hematite that formed. The high amount of calcium present, identified by SEM analyses, resulted in the agglomeration occurring of the fly ash. The weathering products were also identified using the same techniques and it was noticed that the pyrite changed to a sulphate when the wet coal was exposed to air drying.
In the frame of WP4 of the EOS LT Co-firing program, the ash formation and deposition of selected coal/biomass blends under oxyfuel and air conditions were studied experimentally in the ECN lab scale coal combustor (LCS). The fuels used were Russian coal, South African coal and Greek Lignite, either combusted separately or in blends with cocoa and olive residue. The first trial period included tests with the Russian and South African coals and their blends with cocoa, the second trial period included Lignite with olive residue tests and a final period firing only Lignite and Russian coal, mainly to check and verify the observed results. During the testing, also enriched air combustion was applied, in order to establish conclusions whether a systematic trend on ash formation and deposition exists, ranging from conventional air, to enriched air (improving post combustion applications) until oxyfuel conditions. A horizontal deposition probe equipped with thermocouples and heat transfer sensors for on line data acquisition, and a cascade impactor (staged filter) to obtain size distributed ash samples including the submicron range at the reactor exit were used. The deposition ratio and the deposition propensity measured for the various experimental conditions were higher in all oxyfuel cases. No significant variations in the ash formation mechanisms and the ash composition were established. Finally the data obtained from the tests performed under air and oxy-fuel conditions were utilised for chemical equilibrium calculations in order to facilitate the interpretation of the measured data; the results indicate that temperature dependence and fuels/blends ash composition are the major factors affecting gaseous compound and ash composition rather than the combustion environment, which seems to affect neither the ash and fine ash (submicron) formation, nor the ash composition. The ash deposition mechanisms were studied in more detail in Part II of this report.
Graphic techniques exist which can accurately predict values for calorific value, organic sulfur, and several other constituents of the organic portion of beneficiated coal sample fractions. These techniques also permit a determination of coal rank to be made without the use of approximations required in the standard procedure. In beneficiation studies, plots of the calorific value of each fraction vs its ash content invariably produce straight lines. The Y axis intercept is the mineral-matter-free Btu value used (on the moist basis) to determine coal rank, and the X axis intercept is a value we will call ``maximum ash.`` These two constants permit us to calculate all future Btu values of fractions of this coal from the ash, alone. Plots of organic sulfur vs ash sometimes produce lines which are straight and at other times curved. In any event, they can be used to read off values of organic sulfur corresponding to a particular ash value in lieu of analyses. When all values truly represent only organic sulfur, the X axis intercept must occur at the same maximum ash value obtained from the Btu/ash curve. When the line is straight, the Y axis intercept is the mineral-matter-free organic sulfur, and all future organic sulfur values may be calculated from these two constants and the ash. Fractions of IBC-101 with varying ash contents were produced by froth flotation. The various fractions were analyzed by the coal analysis laboratory and the particular data type was plotted in each case vs the individual ash content of each fraction, using Lotus 123 and Freelance software packages. These plots permit more accurate determination of mineral matter, Btu, organic sulfur, and organic and inorganic carbon, hydrogen, nitrogen, and volatile matter. This information represents a more complete knowledge of coal. In addition, the plots permit accurate estimation of these values from ash and total sulfur analyses alone and thus can save time and analytical expense.
Coalash obtained from Nikola Tesla A power plant in Obrenovac, near Belgrade, Yugoslavia, is mixed with water of the Sava river and transported to the dump. In order to assess pollution caused by leaching of some minor and major elements during ash transport through the pipeline, two sets of samples (six samples each) were subjected to a modified sequential extraction. The first set consisted of coalash samples taken immediately after combustion, while the second set was obtained by extraction with river water, imitating the processes that occur in the pipeline. Samples were extracted consecutively with distilled water and a 1 M solution of KCl, pH 7, and the differences in extractability were compared in order to predict potential pollution. It is concluded that lead and cadmium do not present an environmental threat during and immediately after ash transport to the dump. Portions of zinc, nickel and chromium are released during the ash transport, and arsenic and manganese are released continuously. Copper and iron do not present an environmental threat due to element leaching during and immediately after the coalash suspension and transport. On the contrary, these elements, as well as chromium, become concentrated during coalash transport. Adsorbed portions of calcium, magnesium and potassium are also leached during coalash transport.
In recent years, fine particles have been correlated with various harmful effects on health, and many countries have imposed restrictions on emission of these particles/ambient standards. Fine ash particles are formed during coal combustion in power stations and a small proportion elude air pollution control devices to be emitted into the atmosphere. This material has come under considerable scrutiny in recent years. Previous studies have shown that combustion of coals of different rank can result in differences in the amount and chemistry of the submicron ash particles. However, only a limited number of laboratory studies have sought to determine the amount and composition of submicron ash formed from the combustion of different coals of similar rank. This study compares the submicron ashes formed from five bituminous Australian coals of similar rank. The five coals were burned in a laminar flow drop tube furnace in two different oxygen environments to determine the amount and composition of submicron ash formed. The experimental setup and ash analysis techniques are described and the repeatability of the experiments is discussed. The variability in the submicron ash yield and the submicron ash composition are presented and discussed. 21 refs., 4 figs., 5 tabs.
The phenomenon of a kelp-dominated community changing to a crust-dominated community, which is called “barren-ground”, is progressing in the world, and causing serious social problems in coastal areas. Among several suggested causes of “barren-ground”, we focused on the lack of Fe in seawater. Kelp needs more than 200 nM of Fe to keep its community. However there are the areas where the concentration of Fe is less than 1 nM, and the lack of Fe leads to the “barren-ground.” Coalash is one of the appropriate materials to compensate the lack of Fe for the kelp growth, because the coalash is a waste from the coal combustion process and contains more than 5 wt% of Fe. The rate of Fe elution from coal fly ash to water can be increased by 20 times after melting in Ar atmosphere, because 39 wt% of the Fe(III) of coal fly ash was reduced to Fe(II). Additionally molten ash from the IGCC (integrated coal gasification combined cycle) furnace in a reducing atmosphere and one from a melting furnace pilot plant in an oxidizing atmosphere were examined. Each molten ash was classified into two groups; cooled rapidly with water and cooled slowly without water. The flux of Fe elution from rapidly cooled IGCC molten ash was the highest; 9.4 × 10–6 g m–2 d–1. It was noted that the coalash melted in a reducing atmosphere could elute Fe effectively, and the dissolution of the molten ash itself controlled the rate of Fe elution in the case of rapidly cooled molten ash.
The phenomenon of a kelp-dominated community changing to a crust-dominated community, which is called 'barren-ground', is progressing in the world, and causing serious social problems in coastal areas. Among several suggested causes of 'barren-ground', we focused on the lack of Fe in seawater. Kelp needs more than 200 nM of Fe to keep its community. However there are the areas where the concentration of Fe is less than 1 nM, and the lack of Fe leads to the 'barren-ground.' Coalash is one of the appropriate materials to compensate the lack of Fe for the kelp growth, because the coalash is a waste from the coal combustion process and contains more than 5 wt% of Fe. The rate of Fe elution from coal fly ash to water can be increased by 20 times after melting in Ar atmosphere, because 39 wt% of the Fe(III) of coal fly ash was reduced to Fe(II). Additionally molten ash from the IGCC (integrated coal gasification combined cycle) furnace in a reducing atmosphere and one from a melting furnace pilot plant in an oxidizing atmosphere were examined. Each molten ash was classified into two groups; cooled rapidly with water and cooled slowly without water. The flux of Fe elution from rapidly cooled IGCC molten ash was the highest; 9.4 x 10{sup -6} g m{sup -2} d{sup -1}. It was noted that the coalash melted in a reducing atmosphere could elute Fe effectively, and the dissolution of the molten ash itself controlled the rate of Fe elution in the case of rapidly cooled molten ash.
In recent years, fine particles have been found to be the cause of various harmful effects on health, and many countries have imposed restrictions on emission of these particles. Fine ash particles are formed during coal combustion in power stations and, if not collected in the air pollution control devices, are emitted into the atmosphere. The fine ash particles can remain airborne for long periods and can result in deleterious health effects when inhaled and deposited in the lungs. Previous studies have shown that combustion of coals of different rank can result in differences in the amount and chemistry of the submicron ash particles. This study examines the variability occurring between the submicron ashes formed from coals of similar rank. Five Australian bituminous coals were burned in a laminar flow drop tube furnace in two different oxygen environments to determine the amount and composition of submicron ash formed. The experimental setup is described and the repeatability of the experiments is discussed. The variability in the submicron ash yield as a percentage of the total ash collected and the submicron ash composition are presented and discussed. This paper presents experimental results rather than a detailed discussion on its interpretation. However, the results indicate that the condensation of evaporated species is responsible for the formation of ash particles smaller than 0.3 {mu}m.36 refs., 5 figs., 6 tabs.
The objective of the current work was to investigate the oxidation reactivity of fly ash carbons, using thermogravimetric analysis techniques. Good measures of the oxidation reactivity of fly ash carbon were the critical temperature (T{sub cr}) and the late burnout temperature (T{sub late}). The lower the critical temperature of the fly ash carbon, the more reactive the sample. By contrast, the higher T{sub late}, the less reactive the fly ash carbon. The difference between T{sub cr} and T{sub late} provided information about the reactivity distribution and was mainly dependent on fly ash carbon content (Loss-On-Ignition (LOI)). Fly ash carbons having different origins, some from lower rank coals and some from higher rank coals had slightly different reactivities. Class C fly ash carbons from low rank coals were more reactive than the typical class F fly ash carbons from higher rank coals. The reactivity parameters did not, however, provide any additional ability to predict the suitability of a given ash for use in concrete.
The use of biomass for power generation can result in significant economical and environmental benefits. The greenhouse emissions can be reduced as well as the cost of the produced electricity. However, ash-related problems, including slagging, agglomeration, and corrosion, can cause frequent unscheduled shutdowns, decreasing the availability and increasing the cost of the produced power. In addition, the fouling of the heat exchange surfaces reduces the system efficiency. In this work the melting and rheological properties of various biomass and biomass/ coalash samples were studied by using a high-temperature rotational viscometer and a hot stage XRD. The produced data were used to calculate the operating temperature of a pilot-scale entrained flow reactor during the cocombustion of biomass/ coal samples in order to ensure the slag flow and to avoid corrosion of the walls due to liquid slag/metal interaction. Biomass ash proved to have significantly different melting behavior compared to that of the coalash. Furthermore, the addition of biomass to coalash led to lower viscosity and subsequently to higher stickiness of the produced ash particles. The melting behavior of the slag generated by the cocombustion tests appeared to be somewhat different compared to that of the laboratory-prepared ash samples. The heated stage XRD data provide useful information regarding the reactions among the various ash compounds and the phase transformations during the heating and cooling of the ash samples and helped the explanation of the produced viscosity curves.
The coal sample is first ashed with high temperature ashing or with RF plasma low temperature ashing. The coalash or fly ash can be analyzed for major ash elements by fusing with lithium tetraborate in an automatic fusion device, the Claisse Fluxer. The ash samples are also dissolved in a Parr bomb in a mixture of aqua regia and HF. Subsequently, the solutions are analyzed for eight major (Al,Ca,Fe,K,Mg,Na,Si and Ti) and 20 trace elements (As,B,Ba,Be,Cd,Co,Cr,Cu,Li, Mn,Mo,Ni,P,Pb,Sb,Se,Sr,U,V,and Zn) by inductively coupled plasma emission spectroscopy. Mercury in coal and fly ash is determined on a separate aliquot by the cold vapor atomic absorption technique. Fluorine and chlorine in the samples are determined by fusing with Na2CO3 and Eschka mixture, respectively, and then measuring the two ions in solution with specific ion electrodes. Oxygen in the samples can be determined rapidly and nondestructively by 14-MeV neutron activation analysis. These methods have been tested by analyzing several NBS coal and fly ash standards with good accuracy and reproducibility.
The coal sample is first ashed with high temperature ashing or with RF plasma low temperature ashing. The coalash or fly ash can be analyzed for major ash elements by fusing with lithium tetraborate in an automatic fusion device, the Claisse Fluxer. The ash samples are also dissolved in a Parr bomb in a mixture of aqua regia and HF. Subsequently, the solutions are analyzed for eight major (Al, Ca, Fe, K, Mg, Na, Si, and Ti) and 20 trace elements (As, B, Ba, Be, Cd, Co, Cr, Cu, Li, Mn, Mo, Ni, P, Pb, Sb, Se, Sr, U, V, and Zn) by inductively coupled plasma emission spectroscopy. Mercury in coal and fly ash is determined on a separate aliquot by the cold vapor atomic absorption technique. Fluorine and chlorine in the samples are determined by fusing with Na/sub 2/CO/sub 3/ and Eschka mixture, respectively, and then measuring the two ions in solution with specific ion electrodes. Oxygen in the samples can be determined rapidly and nondestructively by 14-MeV neutron activation analysis. These methods have been tested by analyzing several NBS coal and fly ash standards with good accuracy and reproducibility. 10 tables.
Male Syrian golden hamsters were given 15 weekly intratracheal instillations with suspensions of coal fly ash or oil fly ash. Controls were instilled with saline containing gelatine (0.5 g/100 mL) or to check particle effects with suspensions of hematite (Fe/sub 2/O/sub 3/). The common weekly dose was 4.5 mg/hamster. In addition, one subgroup of hamsters was treated with oil fly ash at a weekly dose of 3.0 mg/hamster and another with coal fly ash at a weekly dose of 6.0 mg/hamster. Other groups of hamsters were treated with suspensions of benzo(a)pyrene (BaP) or with suspensions on coal fly ash, oil fly ash, or Fe/sub 2/O/sub 3/ coated with BaP. The mass median aerodynamic diameters of the coal and oil fly ashes were 4.4 microns and 28 microns, respectively. Hamsters treated with oil fly ash showed a higher frequency of bronchiolar-alveolar hyperplasia than hamsters in the other treatment groups. Squamous dysplasia and squamous metaplasia were most frequent in animals treated with suspensions of BaP or BaP-coated particles. The earliest appearance of a tumor, the highest incidence of tumors, and the highest incidence of malignant tumors were observed in hamsters treated with oil fly ash coated with BaP. Squamous cell carcinoma and adenosquamous carcinoma were the most frequent malignant tumors. No malignant tumors and only few benign tumors were observed in hamsters instilled with suspensions of fly ash not coated with BaP. The present study gives no indication that coal fly ash could create more serious health problems than oil fly ash.
This report examines the upstream factors affecting particulate emissions from pulverised coal fired power plants. It identifies the opportunities for prevention of the emissions before the particulate control system. Coal quality affects the fly ash and flue gas properties which control the performance of particulate control units. Coal cleaning reduces particulate emissions. Care must be taken as coal cleaning decreases the sulphur content which may increase the fly ash resistivity. Switching to low sulphur coals or low heating value coals decreases the ESP efficiency. Coal blending can either improve or impair the ESP performance, depending on the coals being blended. Dry bottom boilers produce much higher particulate loads to ESPs or fabric filters than wet bottom boilers. Most combustion modifications increase unburned carbon in the fly ash, lowering the ESP efficiency. The impact can be mitigated by firing high reactivity or high volatile coals, reducing the size of coal particles, and optimising combustion. Flue gas conditioning improves the ESP performance by modifying the fly ash characteristics. It is an effective way to upgrade ESPs when switching to low-sulphur coals or meeting more stringent emission legislation. 105 refs., 26 figs., 6 tabs.
The U.S. Geological Survey (USGS) conducted the National Coal Quality Inventory (NaCQI) between 1999 and 2005 to address a need for quality information on coals that will be mined during the next 20-30 years. Collaboration between the USGS, State geological surveys, universities, coal burning utilities, and the coal mining industry plus funding support from the Electric Power Research Institute (EPRI) and the U.S. Department of Energy (DOE) permitted collection and submittal of coal samples for analysis. The chemical data (proximate and ultimate analyses; major, minor and trace element concentrations) for 729 samples of raw or prepared coal, coal associated shale, and coal combustion products (fly ash, hopper ash, bottom ash and gypsum) from nine coal producing States are included. In addition, the project identified a new coal reference analytical standard, to be designated CWE-1 (West Elk Mine, Gunnison County, Colorado) that is a high-volatile-B or high-volatile-A bituminous coal with low contents of ash yield and sulfur, and very low, but detectable contents of chlorine, mercury and other trace elements.
At present, of the approximately 4 million tons of coalash generated each year, only about 50% is utilized while the remainder is discarded in landfills. Because it will become more difficult to secure landfill space in the future, it is desirable to promote better utilization of coalash as a concrete admixture. When coalash is used as a concrete admixture it is very difficult to control the mixing process because the unburnt carbon contained in the coalash absorbs the air-entraining agent. This paper deal with development of a new nonionic air-entraining agent which is unaffected by the type of coalash, and reports the experimental results and its effect on the properties of mortar and concrete utilizing large amounts of fly ash, as compared with those of other air-entraining agent. The results of this study show that the amount of air entrained using the new air-entraining agent is stable when a high ratio of coalash to concrete is used, and it was confirmed that the new air-entraining agent does not affect the properties of the concrete. 9 refs., 17 figs., 7 tabs.
The quarterly report on low-rank coal research contains information on (1) gasification waste water, water treatment and reuse, (2) hydrogen production from low-rank coals, (3) preparation and combination of coal water slurries, including coal preparation (drying), (4) liquefaction of low-rank coals, (5) pollution control of nitrogen and sulfur oxides, (6) particulate, ash slag and waste characterization, (7) combustion research and fouling of boilers by low-rank coal, (8) the organic structure of coal and the distribution of inorganic trace elements, (9) physical properties and moisture (including measuring methods), (10) supercritical solvent extraction, and (11) pyrolysis and devolatization. (LTN)
This report was prepared as an account of an international delegation to the symposium. Opening and closing speeches, summaries of the technical sessions, and lists of delegates are included. 13 papers presented by the international delegation are given. These covered recent advances in methanol and liquid fuels from coal, the Voest-Alpine process, ammonia manufacture based on the Texaco Coal Gasification Process, liquid redox sulphur recovery, Lurgi Processes, Prenflo demonstration plant, BGL slagging gasifier in integrated coal gasification combined cycle power generation, Rheinbraun HTW process, operation of a high pressure ash-agglomerating coal gasifier, entrained flow coal gasification, Kellog/KRW IGCC system, Dow Coal Gasification Process, and the Shell Coal Gasification Process.
Analyzes pyrite grain size, form and microlithotype association in brown coal from the North Bohemia brown coal basin. The following aspects are evaluated: types of pyrite (grain geometry, crystalline forms, etc.), chemical composition, association with individual types of microlithotypes, correlations of coalash content and pyrite content, correlations of coal density and pyrite content, methods of pyrite separation, effects of coal sampling method on accuracy of pyrite determination in coal. Examples of determining pyrite content in brown coal from the CSA and the Nastup mines are discussed. 20 refs.
Flue coals are a mixture from crushed coals in a fluid medium, e.g. water, methanol or oil. In part they are used for hydraulically transport by using a fluid medium. But they also were used as oil compensation, as employment to the Texaco gasification and for pumping of paste for coal hydrogenation. By wanting ash-poor dispersions of coal in oil one have to knead in water grinding coal with the same quantity of oil; the watery phase, that means the formed suspension of coal slime contains the ashforming parts of the coal. (orig.).
Fly ash (100 mg/kg body weight) was administered intratracheally to 14-day pregnant rats for 6 consecutive days. On day 20 of gestation the translocation of metals present in the fly ash to various maternal and fetal organs was studied. Fly ash administration to pregnant mothers retarded the growth of fetal heart and kidney as determined by their weights. Fly ash instillation increased organ levels of nearly all the metals studied in both mother and fetus. Most of the metals present in coal fly ash were transferred in significant amounts through placenta to several fetal organs. However, the pattern of their distribution into various fetal organs was different for different metals.
Policies for reducing NOx emissions have led power plants to restrict O{sub 2}, resulting in high-carbon fly ash production. Therefore, some potentially useful fly ash, such as the economizer fly ash, is discarded without a thorough knowledge of its composition. In order to characterize this type of fly ash, samples were collected from the economizer Portuguese power plant burning two low-sulfur bituminous coals. Characterization was also performed on economizer fly ash subsamples after wet sieving, density and magnetic separation. Analysis included atomic absorption spectroscopy, loss-on-ignition, scanning electron microscopy/energy-dispersive X-ray spectroscopy, optical microscopy, and micro-Raman spectroscopy.
Lethabo Power Station is capable of generating 3700 MW, burning low-grade coal, with a high ash content. The ash is disposed off by controlled staking of the moist ash on a designated ash dump. In the early 1980's, several possible options were considered. Moist stacking on level spoils and overburden was selected. The climatic balance for the area was evaluated and it was assigned a 'B' classification. Investigations done in the past were studied to see if practice supported the belief that there is a very low risk of leachate production from the ash dump. (orig.)
Due to the environmental problems created by large-scale fly ash from pulverized coal combustion throughout the world, efforts are being made to recycle these materials. An important component of the recycling effort is using fly ash to improve low-fertility soils. Because availability of many nutrients is very low in fly ash, available range of such nutrients must be improved to increase the effectiveness of fly ash as a soil amendment. In the present study, the possibility is assessed of increasing P bioavailability in fly ash through vercomposting in a yard experiment. Vercomposting involves using epigeic earthworms to increase the microbial population in vermicasts and helps produce high quality compost in a lesser time. Among different combinations fly ash and organic matter, P availability in fly ash due to vermicomposting was significantly higher in the 1:1 fly ash to cow dung treatment compared with the other treatments. 12 refs., 1 fig., 6 tabs.
Fly ash, a by-product of coal combustion, is often stored in landfills. Stabilization of fly ash deposits can be hindered by phytotoxic levels of B and soluble salts in the ash. Two greenhouse studies were conducted with the objective of improving cover crop establishment on landfills containing fly ash. In one experiment, eight cover crop species were screened for tolerance to fly ash and fly ash-amended soil, as measured by seedling emergence and early shoot growth. Hairy vetch, red clover, and tall fescue were identified as having the best potential for stabilization of fly ash deposits. Another experiment determined if amending fly ash with a co-compost produced from municipal refuse and sewage sludge, would improve the establishment and growth of tall fescue and Korean lespedeza. The co-compost had no effect on fescue alone, but increased emergence and early growth of lespedesa and a fescue-lespedeza mixture.
There are no specific standards for biomass ash analysis in China, so the standards for coalash analysis are usually used to determine the property of biomass ash. Three kinds of biomass including rice straw, pine sawdust and Chinese Parasol Tree leaf burned at 815 degreeC, 600 degreeC and 500 degreeC respectively corresponding to the temperature required in the standard of GB and ASTM. The ash content and composition were analyzed. Based on the ash composition results, the volatilization of alkali oxides in biomass ash and slagging/fouling problems related to biomass thermochemical conversion were investigated. The alkali metals were relatively more volatile with the increasing of ashing temperature. The crystalline phase composition and surface morphology characteristics of the ash part...
Class F fly ash and bottom ash are the solid residue byproducts produced by coal-burning electric utilities. They are usually disposed of together as a waste in utility disposal sites with a typical disposal rate of 80% fly ash and 20% bottom ash. Direct use of these materials in construction projects consuming large volumes of materials, such as highway embankment construction, not only provides a promising solution to the disposal problem, but also an economic alternative to the use of traditional materials. Representative samples of class F fly and bottom ash were collected from two utility power plants in Indiana and tested for their mechanical properties (compaction, permeability, strength, stiffness, and compressibility). Three mixtures of fly and bottom ash with different mixture ratios (i.e., 50, 75, and 100% fly ash content by weight) were prepared for testing. Test results indicated that ash mixtures compare favorably with conventional granular materials.
This report compiles results from analyses of ashes from combustion of pure wood fuel and mixture of fuels. Data on macro element concentrations, trace and heavy metal concentrations and concentrations of PAH are presented. Leachate analyses and results from curing tests are also included. All these parameters are important for the possibility of using mixed ashes as fertilizers. The content of K, Ca and Mn is lower and the content of Si, Al and Fe is higher in the ashes resulting from cofiring of coal or peat with wood fuel as compared to combustion of pure wood fuel. Cd is normally the heavy metal which limit the land spreading of ashes. When cofiring wood with coal, peat and oil normally the content of the heavy metals is in the same range as with pure wood fuel. When cofiring with coal and peat there is a risk for higher amounts of As, Cr, Ni, Hg, Mo and V. When cofiring with oil there is a risk for higher amounts of Cr, Cu, Ni, Mo and V. The content of polyaromatic hydrocarbons (PAH) is generally low (<0.5 {mu}g/g dry ash) in ashes from combustion of forest fuel if the concentration of organic carbon in the ash is low. At the analysis of combined firing with wood fuel and coal or oil no existence of PAH could be detected in the fly ashes. However, a fly ash from combined firing of peat and wood fuel showed a content of 19.5 {mu}g/g dry ash. The solubility of trace elements and heavy metals is low for wood ash from combustion depending on the high pH in the pores of the ash. The same is applicable to ashes from combined firing of coal, oil and peat with wood fuels. Curing led to the formation of calcium hydroxide, calcium carbonate, gypsum and ettringite. Due to the higher sulphate levels, the reactions involving CaSO{sub 4} are more important for fly ash from wood/coal and wood/peat ash than for pure wood ash. The release of alkali metals was normally not affected by curing. The release of phosphorus was very low as has also been noted during leaching tests carried out with pure wood ash 46 refs, 20 tabs
The present work reports the results of investigation of microbial dissolution of metals from coal and coal residues under aerobic and anaerobic conditions. T. Ferroxidans under aerobic conditions, released significant amounts of sulfur and iron from the different coals tested. This led to reductions in ash content and more significantly to substantial increases in ash fusion temperatures of over 400/degree/F. Thus microbial coal treatment provides a cleaning approach that enhances ash and hence coal quality. Treatment of coal residues under aerobic conditions resulted in solubilization by native autotrophic bacteria of varying amounts of trace metals such as arsenic, chromium, nickel and lead. Under anaerobic conditions, significant amounts of iron, chromium and manganese were solubilized along with the release of trace metals. Mechanisms of metal removal will also be discussed in the paper. 2 tabs.
Further agglomeration tests were conducted in a series of tests designed to determine the effects of various parameters on the size and structure of the agglomerates formed, the rate of agglomeration, coal recovery, and ash rejection. For this series of tests, finely ground Pittsburgh No. 8 coal has been agglomerated with i-octane in a closed mixing system with a controlled amount of air present to promote particle agglomeration. The present results provide further evidence of the role played by air. As the concentration of air in the system was increased from 4.5 to 18 v/w% based on the weight of coal, coal recovery and ash rejection both increased. The results also show that coal recovery and ash rejection were improved by increasing agitator speed. On the other hand, coal recovery was not affected by a change in solids concentration from 20 to 30 w/w%.
Further agglomeration tests were conducted in a series of tests designed to determine the effects of various parameters on the size and structure of the agglomerates formed, the rate of agglomeration, coal recovery, and ash rejection. For this series of tests, finely ground Pittsburgh No. 8 coal has been agglomerated with i-octane in a closed mixing system with a controlled amount of air present to promote particle agglomeration. The present results provide further evidence of the role played by air. As the concentration of air in the system was increased from 4.5 to 18 v/w% based on the weight of coal, coal recovery and ash rejection both increased. The results also show that coal recovery and ash rejection were improved by increasing agitator speed. On the other hand, coal recovery was not affected by a change in solids concentration from 20 to 30 w/w%.
About 85 % of the 100 Mt/a of brown coal currently extracted in the Rhenish mining area is fired for power generation in the large power plants of RWE Energie AG . Here, steam coal having ash contents of more than 2.5 % wt. is used. Around 15 Mt/a of brown coal with lower ash contents is supplied as briquetting coal to Rheinbraun`s upgrading plants for the production of briquettes, fluidized-bed coal, pulverized coal and rotary hearth furnace coke. Approximately one quarter of this amount is fired in the three Rheinbraun-owned mine-mouth power plants to produce process steam and electric power. In this process, approx. 80,000 t/a of fly ash having high CaO and MgO contents is obtained. Some investigations which were made in respect of these substances` possible applications will be introduced in the following.
A set of six coals was ashed at four separate temperatures. Ashes and whole coals were analysed, using X-ray fluorescence spectrometry, atomic absorption spectrometry, optical emission and inductively coupled plasma emission spectrometries, selective ion electrode potentiometry, and/or instrumental neutron activation analysis, for 58 inorganic elements at trace through to major constituent levels. An auxiliary selection of coals and their ash residues was also analysed for a limited number of elements in order to supplement or clarify the results from the primary set. New volatility information for up to 30 elements was obtained. Only six of the elements determined were volatilized to a significant extent to temperatures to 815 C while a further ten were volatilized variously from coals at a temperature of 1500 C. Boron displayed unusual volatility patterns being retained at 815 C for all coals but exhibiting volatility with some coals at lower and higher temperatures. 48 refs.
The effects of leaching subbituminous coal samples from Boragolai and Ledo collieries of Makum coal field, Assam, India, with aqueous sodium hydroxide solution on removal of ash and sulphur, were investigated. Mild alkali treatment for relatively short period leads to removal of ash from the coal samples. Increase of alkali concentration and treatment time has negative effect on ash reduction due to formation and accumulation of insoluble sodium aluminosilicate. Boragolai coal is less demineralized than Ledo coal and is attributed to presence of higher amount of alkali-soluble silica and alumina. Alkali treatment leads to over 70% removal of the inorganic sulphur in the coal samples. Desulphurization increases with increase in alkali concentration and treatment time.
This study is principally concerned with characterizing the organic part of coal combustion fly ashes. High carbon fly ashes are becoming more common as by-products of low-NOx combustion technology, and there is need to learn more about this fraction of the fly ash. The project team consists of two universities, Brown and Princeton, and an electrical utility, New England Power. A sample suite of over forty fly ashes has been gathered from utilities across the United States, and includes ashes from a coals ranging in rank from bituminous to lignite. The characterizations of these ashes include standard tests (LOI, Foam Index), as well as more detailed characterizations of their surface areas, porosity, extractability and adsorption behavior. The ultimate goal is, by better characterizing the material, to enable broadening the range of applications for coal fly ash re-use beyond the current main market as a pozzolanic agent for concretes. The potential for high carbon-content fly ashes to substitute for activated carbons is receiving particular attention. The work performed to date has already revealed how very different the surfaces of different ashes produced by the same utility can be, with respect to polarity of the residual carbon. This can help explain the large variations in acceptability of these ashes as concrete additives.
This study is principally concerned with characterizing the organic part of coal combustion fly ashes. High carbon fly ashes are becoming more common as by-products of low-NOx combustion technology, and there is need to learn more about this fraction of the fly ash. The project team consists of two universities, Brown and Princeton, and an electrical utility, New England Power. A sample suite of over forty fly ashes has been gathered from utilities across the United States, and includes ashes from a coals ranging in rank from bituminous to lignite. The characterizations of these ashes include standard tests (LOI, Foam Index), as well as more detailed characterizations of their surface areas, porosity, extractability and adsorption behavior. The ultimate goal is, by better characterizing the material, to enable broadening the range of applications for coal fly ash re-use beyond the current main market as a pozzolanic agent for concretes. The potential for high carbon-content fly ashes to substitute for activated carbons is receiving particular attention. The work performed to date has already revealed how very different the surfaces of different ashes produced by the same utility can be, with respect to polarity of the residual carbon. This can help explain the large variations in acceptability of these ashes as concrete additives.
An assessment of the potential environmental and health impacts of radionuclides in the coal fuel cycle is being conducted at Mound. This paper describes our studies evaluating the potential for migration of radionuclides from ash disposal sites. Studies at a power plant burning western US coal dealt with an assessment of potential radiation doses from coalash ponds and leachate discharges of radionuclides from the ponds. Emanation of radon-222 from the ash is relatively low. The emanation of radon-222 from the ash pond (radium-226 at 4.5 pCi/g) is predicted to be about six times less than from soil (radium-226 at 1 pCi/g). Ash with radium-226 at 25 pCi/g would approximate emanation of radon-222 from soil. At 1000 m from the center of the ash pond area, radon-222 from the ash pond is predicted to be 1000 to 6000 times less than background (0.1 to 0.5 pCi/liter). Pathways exist for transport of radionuclides leached from ash into the aquifer beneath the holding ponds, but concentrations of radionuclides in water leaving the pond are lower than concentrations in groundwater which is upgradient of the ponds. Leachability of the ash is quite low, on the order of 0.002% in one month, and flow of ash sluicing water (3% of the volume of the ponds each day) has actually diluted normal background concentrations of radionuclides in the aquifer between the ponds and the adjacent river.
The composition and properties of ash formed during coal firing have a major impact on boiler performance. Higher ash content in the coal can mean higher costs associated with coal handling, transportation, ash removal and ash disposal along with higher costs due to the increased ash content`s deleterious effects on pulverizing, combustion and heat transfer. ABB C-E Services, Inc. has conducted research for many years on what might be done to minimize the adverse effects of ash on boiler performance. Recently, ABB C-E Services has studied the effects of firing system modifications on ash composition and properties and the effect these firing system modifications have on overall furnace performance. The subject of this paper is the impact of the installation of the CFS Concentric Firing System on the propensity for boiler wall ash deposition. For this study, CFS yaw angles were varied and particle samples were collected at the waterwalls for the different yaw angles tested. These ash samples were analyzed for ash composition. The results showed that with a larger CFS yaw angle (the air stream directed more towards the boiler walls) the base/acid ratio, iron content and sulfur content of the particle samples collected at the waterwall were reduced. This effect is due to several contributing factors: (1) an oxidizing environment produced by injecting more air toward the walls; and (2) an aerodynamic change which impacts the particle combustion time/temperature history.
Potential use of PEO/PPO triblock co-polymers to improve coal flotation in the presence of an insoluble collector was investigated. In the absence of polymers, coal particles were observed to agglomerate in the flotation cell. The extent and the structure of the agglomerates were found to be a function of coal type and collector amount. Non-selective agglomeration between coal and ash particles was considered to be the main reason for selectivity problems in the coal flotation. Mechanical emulsification of the collector promoted agglomeration. This led to an increase in recovery for high rank coals, but the ash rejection was poor. For low rank coals, emulsification alone did not improve flotation. Addition of block co-polymers improved flotation of high rank, coals by increasing selectivity. This was attributed to modification of coal surface by the polymers, which reduced non-selective agglomeration. For low to medium rank coals, polymers acted as both emulsifiers for the collector and modifiers for the coal particles. The agglomerates were smaller and more hydrophobic. The clean coal recovery increased substantially with a lowering of the ash content for these type of coals. 36 refs., 5 figs., 2 tabs.
Paleogene bituminous coals of low rank (R{sub aver} = 0.63 and 0.69%, respectively) occurring in two Spitsbergen (Norway) regions: Longyearbyen and Kaffioyra, were analyzed to find occurrence and distribution of the following trace elements: Be, Cd, Co, Cr, Cu, Li, Mn, Mo, Ni, Pb, V, Zn. Inductively Coupled Plasma-Atomic Emission Spectrometry (ICP-AES) was used for ash derived from combusted coals, their extracts, and macromolecular fractions. Trace element concentrations were investigated to find occurrence variability and a degree of trace element affinity to organic and inorganic coal fraction in the coals from both regions. Maceral and elemental composition of these coals was also determined. Kaffioyra and Longyearbyen coals show significant differences in the composition of their organic and mineral matter, reflected both in petrographic properties and elemental compositions. The Kaffioyra coals are characterized by higher contents of vitrinite group macerals, lower contents of inetrinite group macerals, and lower concentrations of carbon, hydrogen, and sulphur. The Kaffioyra coals show higher content of clay minerals and carbonates than the Longyearbyen coals. Trace element contents in ash of coals from both Spitsbergen regions are below the average contents of these elements in the world's bituminous coals. Coals of both regions differ in trace element concentration and their occurrence variability. The main carrier of trace elements in coals of both regions is ash of biogenetic and sorptive origin while in the range of high concentrations of trace elements terrigenic input also plays an important role. (author)
This research project focuses on pollutants from the combustion of mixtures of dried municipal sewage sludge (MSS) and coal. The objective is to determine the relationship between (1) fraction sludge in the sludge/coal mixture, and (2) combustion conditions on (a) NOx concentrations in the exhaust, (b) the size segregated fine and ultra-fine particle composition in the exhaust, and (c) the partitioning of toxic metals between vapor and condenses phases, within the process. The proposed study will be conducted in concert with an existing ongoing research on toxic metal partitioning mechanisms for very well characterized pulverized coals alone. Both high NOx and low NOx combustion conditions will be investigated (unstaged and staged combustion). Tradeoffs between CO{sub 2} control, NO{sub x} control, and inorganic fine particle and toxic metal emissions will be determined. Previous research results have demonstrated that the inhalation of coal/MSS ash particles cause an increase in lung permeability than coalash particles alone. Elemental analysis of the coal/MSS ash particles showed that Zn was more abundant in these ash particles than the ash particles of coalash alone.
This paper reports the existence patterns of sodium in Ikeshima coals. The coal samples were collected from a 4-shaku seam and an 18-shaku lower seam and their debris. Samples of lump-form appearing homogeneous to the naked eye were selected, and part of them was put aside for scanning microscope observation, and about 20 grams from the remainder were pulverized to finer than 150[mu]m to be used for low-temperature ashing, ash measurement, and fluorescent X-ray analysis. Mineral composition in the coal was investigated using X-ray diffraction, and the samples from debris were crushed to identify the minerals using X-ray diffraction. The Ikeshima coal contains plagioclase, analcime, paragonite and I/S seam as Na containing minerals. Among the minerals, analcime and paragonite are formed in the fissures and pores in relatively low ashcoals. Sodium content is well correlated with ash content. Sodium in high ashcoals, and shale and tuff samples mainly depends on plagioclase, and sodium in low ashcoals on analcime, paragonite and plagioclase. 8 refs., 5 figs.
To study the relationship between the composition of minerals in coal and de-ashing characteristics by physical separation, six kinds of coals are used to investigate the minimum ash content of each coal, and the relation with the removal rate of ash content, recovery rate of combustible components, and separation efficiency is investigated. De-ashing characteristics obtained by gravity separation are different according to the kinds of coal. The amount of each mineral in coal is calculated basing on the result of X-ray diffraction of low temperature ash and ICP (inductively coupled plasma) emission spectral analysis of high temperature ash. Quartz and kaolinite are major minerals in the coals. Quartz, kaolinite, pyrite, and iron oxide in coal can be removed comparatively easily by physical separation, but calcite, MgO, Na2O, K2O, P2O5, and TiO2 are difficult to be removed. It is made clear that the minimum content attainable can be estimated based on the amounts of minerals hard to be removed by separation utilizing gravity difference. 10 refs., 9 figs., 6 tabs.
Hydrogen sulfide is highly toxic to benthic organisms and may cause blue tide with depletion of dissolved oxygen in water column due to its oxidation. The purpose of this study is to reveal the combined adsorption and oxidation mechanisms of hydrogen sulfide on granulated coalash that is a byproduct from coal electric power stations to apply the material as an adsorbent for hydrogen sulfide in natural fields. Sulfur species were identified in both liquid and solid phases to discuss removal mechanisms of the hydrogen sulfide with the granulated coalash. Batch experiments revealed that hydrogen sulfide decreased significantly by addition of the granulated coalash and simultaneously the sulfate ion concentration increased. X-ray absorption fine structure analyses showed hydrogen sulfide was adsorbed onto the granulated coalash and successively oxidized by manganese oxide (III) contained in the material. The oxidation reaction of hydrogen sulfide was coupling with reduction of manganese oxide. On the other hand, iron containing in the granulated coalash was not involved in hydrogen sulfide oxidation, because the major species of iron in the granulated coalash was ferrous iron that is not easily reduced by hydrogen sulfide. PMID:22487226
Thirteen Miocene coal samples from three active open pit and underground coal mines in the Kutai Basin (East Kalimantan, Indonesia) were collected. According to our microscopical and geochemical investigations, coal samples from Sebulu and Centra Busang coal mines yield high sulfur and pyrite contents as compared to the Embalut coal mine. The latter being characterized by very low sulfur (<1%) and pyrite contents. The ash, mineral, total sulfur, iron (Fe) and pyrite contents of most of the coal samples from the Sebulu and Centra Busang coal mines are high and positively related in these samples. Low contents of ash, mineral, total sulfur, iron (Fe) and pyrite have been found only in sample TNT-32 from Centra Busang coal mine. Pyrite was the only sulfur form that we could recognize under re...
A novel process to produce ash-free coal, called Hyper-Coal (HPC), has been developed based on the coal liquefaction with organic solvent extraction. Seventy wt% of combustible contents can be extracted from raw coal via the dissolution in 1-methylnaphthalen at 633K, reducing the ash and alkali contents to less than 1000 and 0.5ppm, respectively. This process is also a promising approach to separate toxic trace elements from fuel constituent in coal before its combustion. Mercury is one of the toxic trace elements of growing concern, because mercury emission from a coal combustion process to the atmosphere has been becoming a serious problem in the coal use all over the world. Therefore, in this study, various intermediate products such as coal-organic solvent slurry were sampled from the ...
The present study deals with the assessment and improvement of trace element analysis reliability in coalash and coalash leachates. Eight Italian Laboratories from ENEL and four French laboratories from EDF took part in this test. Two samples were studied (a certified reference material NIST 1633a and a fly ash with unknown unconcentration coming from an Italian coal-fired power plant) and eleven trace elements (As, Cd, Cr, Cu, Hg, Ni Ph, Sb, Se, V and Zn) were analysed. A `standardised` mineralization procedure for the fly ash samples, which employs a microwave oven was validated by means of this Round Robin Test. For the analysis step, flame atomic absorption spectrometry (FAAS), graphite furnace atomic absorption spectrometry (GFAAS) or inductively coupled plasma atomic emission spectrometry (ICP-AES) were employed. Leaching tests were applied to the unknown ash sample, following the Italian standard test (IRSA, using acetic acid) and the French standard test (AFNOR, using demineralized water).
The US has over 800 million tons of coalash stockpiled and available for aboveground mining. Increased use of coal will add 100 million tons a year. Fly ash, which represents about 75% of the total, is the most versatile in its range of applications. These include the manufacture of cement, brick, roofing felt, mineral-wool insulation, highway subgrading, etc. Bottom ash, or boiler slag, is useful for sand blasting, water treatment filtration, road deicing, cold mix asphalt, and structural fill. Demonstrations using ash for these and other uses have been impressive. Using coalash will not only eliminate stockpiling problems, but will preserve other natural resources and create high-value and high-quality products.
Using low temperature ashing in an oxygen plasma, the mineral matter in coals can be isolated and studied. A quantitative X-ray diffraction (XRD) technique has been developed, using accepted procedures, for the analysis of minerals (illite, gypsum, kaolinite, quartz, ankerite and pyrite) in low temperature coalash (LTA). This XRD method should theoretically produce mineral totals approaching 100%, unless non-crystalline material is present. However, working with material ashed to constant weight gave mineral totals of between 50% and 80%; totals generally being lowest when the ash content of the coal was low. Further work showed that this shortfall was due to residual organic material that can be removed by repeated fine-grinding and ashing. 12 refs., 3 figs., 5 tabs.
Iron-57 Mössbauer spectroscopic studies were carried out at room temperature on samples of coal, slag (bottom ash) and mechanical ash collected from Bhatinda (India) thermal power plant. Hyperfine parameters such as isomer shift, quadrupole splitting and total internal magnetic field of 57Fe nuclei were used to characterize various iron-bearing minerals. The observed parameters indicate the presence of pyrite, siderite and ankerite in coal sample while magnetic fractions of mechanical ash and slag samples show the formation of hematite and Al-substituted magnesio-ferrite. The non-magnetic fraction of slag ash shows the dominance of Fe2+ phases while that of mechanical ash demonstrates the formation of both Fe2+ and Fe3+ phases. These findings are compared with Mössbauer and magnetic susceptibility studies on fly ash samples of Panipat (India) thermal power plant reported earlier.
In the liquefaction of coal which has high ash content and produces little distillation residue, the increase in ash concentration in the distillation residue during distillation process causes to lower the fluidity of the distillation residue to make the extraction difficult, interfering with the stable operation of liquefaction process. The object of the present invention is to enable a stable operation of the distillation process by removing ash from the processed distillation residue and recirculating the residue in the coal liquefaction process. Solvent extraction, super critical extraction, centrifugal separation, gravity sedimentation, gravity separation can be applied to the removal of ash content. Locations for the addition of ash-removed distillation residue can be immediately before the distillation process, in liquefaction process, in hydrogenating process, etc. The ash removed distillation residue has the effect of improving the yield of liquefaction because liquefied oil is produced by hydrocracking. 2 figures, 4 tables.
This research investigated the compressive strength, microstructure and thermal analysis of autoclaved and air cured structural lightweight concrete made with coal bottom ash and silica fume. The results show that bottom ash lightweight concrete autoclaved for 6h gives compressive strength similar to the bottom ash lightweight concrete air cured for 28 days and found that the compressive strength of both bottom ash lightweight concrete increased when silica fume was added to the mix. The highest compressive strength obtained for all mixes was found when coal bottom ash was used at 20% with the addition of silica fume at 5% and that this strength value is significantly higher than that of Portland cement control. The thermal conductivity of all bottom ash lightweight concrete at 28 days and...
Two combustion tests were performed in a fluidized bed combustor of a thermo-electric power plant: (1) combustion of coal; (2) co-combustion of coal (68.7% w/w), sewage sludge (9.2% w/w) and meat and bone meal (MBM) (22.1% w/w). Three samples of ashes (bottom, circulating and fly ashes) were collected in each combustion test. The ashes were submitted to the following assays: (a) evaluation of the leaching behaviour; (b) stabilization/solidification of fly ashes and evaluation of the leaching behaviour of the stabilized/solidified (s/s) materials; (c) production of concrete from bottom and circulating ashes. The eluates of all materials were submitted to chemical and ecotoxicological characterizations. The crude ashes have shown similar chemical and ecotoxicological properties. The s/s mate...
Fly ash is a by-product of coal-fired electricity generation plants. The prevalent practice of disposal is as slurry of ash and water to open lands or ash ponds located near power plants and this has lain to waste thousands of hectares all over the world. Wind and leaching are often the causes of off-site contamination from fly ash dumpsites. Vetiver (Vetiveria zizanioides) grown on fly ash for three months showed massive, mesh-like growth of roots which could have a phytostabilizing effect. The plant achieved this without any damage to its nuclear DNA as shown by comet assay done on the root nuclei, which implies the long-term survival of the plant on the remediation site. Also, when Vetiver is used for phytoremediation of coal fly ash, its shoots can be safely grazed by animals as very l...
Co-firing of straw and coal on existing pulverised coal fired power plants may cause problems with deposition, corrosion, deactivation of SCR catalysts and impedes the utilisation of the fly ash, because of the high chlorine and potassium content of straw. Experiments with co-combustion of straw and coal on boilers plants have shown, that when maximal 20% of straw on a thermal basis is applied the most serious problems is the deactivation of high dust SCR catalysts and the deterioration of fly ash quality. The objective of this work was to evaluate a large-scale pre-treatment process for straw. The process applies pyrolysis at a moderate temperature, where the alkaline is retained in the char. The char is then washed and char and pyrolysis gasses can be co-fired with coal without causing serious problems. Fundamental laboratory studies as well as technical investigations were conducted to evaluate the pre-treatment concept. The laboratory studies were mainly done to improve the understanding of potassium and chlorine release during pyrolysis and the extraction of char with water. Some work were also done with respect to particle characterisation, straw pyrolysis kinetic and straw char combustion. The technical evaluation of a plant with 20 tons/hour capacity included investigations of possible reactor technologies, waste water handling, power efficiency and investment costs. Based on the laboratory experiments a pyrolysis temperature of 500 to 600 deg. C is recommended for the pre-treatment process. A high degree of pyrolysis is obtained without a significant release of potassium to the gas, but a release of 30 to 60% of the chlorine can not be avoided. Extraction of potassium from char with water is a two-step process, where the first step is a fast dissolution of potassium salts and the second step is a slow release of potassium from the interior of the char particle. A high potassium removal during char wash could not be obtained for all types of char within reasonable retention times. It can be concluded that pre-treatment of straw by pyrolysis and char wash is economically favourable in comparison with separate straw fired boilers, but the target of 90% potassium removal can not be met by the process and the time for commercialisation will be long. By an alternative pre-treatment method, leaching of straw, a removal efficiency of 95% can be obtained and this method is therefore recommended. (au)
Starting from practical results obtained on substituting pit coal and lignite for fuel oil and natural gas as cement burning fuels, it is attempted to find a relationship between coal quality and operating result. A proposed method of assessing the suitability of fuels is based on the results of physical and mathematical modelling. The results of the calculations for soft lignite, high-ashcoal and high-grade coal are discussed in comparison with those for fuel oil and natural gas.
Progress in research programs on low rank coal is reported under the following headings: Gasification wastewater treatment and reuse, hydrogen production, preparation of coal-water fuel slurries, coal liquefaction, 50/sub x//NO/sub x/ control, particualte characterization, cleaning of coal fines, fouling of boilers and heat exchangers, fluidized-bed combustion, combustion of fuel slurries, ash and slag characterization, molecular structure measurement of physical properties and moisture, supercritical solvent extraction, pyrolysis and devolatilization. (LTN)
The use of coal in the United States is reviewed and more efficient ways to use coal are discussed. The author points out that coal is an incredibly rich source of hydrocarbons and its poisons can be subject to far more advanced treatments than is possible with simple combustion. The author advocates coal gasification and liquification, and he discusses methods for treating fly ash. (JMT)
For the economy of any co-firing process, it is important that the common waste management options of ash remain practical. Ash from bituminous coal combustion is typically handed to the construction industry. This paper describes the current European legislation on use of ash for construction purposes. Also, it presents an experimental study on the suitability of fly ash from combustion of mixtures of bituminous coal and municipal sewage sludge as additive to cement and concrete, and for use in open-air construction works, based on the ash chemical composition and the characteristics of the extract of the ash. Presently, two European standards forbid the use of ash from co-firing as additive to cement or concrete. This study shows that ash derived from coal and sewage sludge co-firing contains generally less unburned carbon, alkali, magnesium oxide, chlorine, and sulfate than coalash. Only the concentration of free lime in mixed ash is higher than in coal, even though, at least up to 25% of the thermal input, still below the requirements of the standards. This ash also meets the requirements for the use of fly ash in open-air construction works--concentration and mobility of few elements--although this management option is forbidden to ash from co-firing. The leaching of Cd, Cr, Cu, Ni, Pb and Zn was investigated with three leaching tests. The concentration of these metals in the extracts was below the detection limit in most cases. The concentration of Cu and Zn in the extract from fly ash was found to increase with increasing share of sewage sludge in the fuel mixture. However, the concentration of these two metals in the extract is not regulated. This study indicates that excluding a priori the use of ash from co-firing as a suitable additive for construction material could cause an unnecessary burden on the environment, since probably ash would have to be disposed of in landfill. However, allowing this requires the modification of current European standards to include limitations on all elements and compounds, absent in coal but which might be present in other fuels, that are deleterious for the quality of construction materials. PMID:11150129
Research is described into the reactive components formed during the hydration of two types of coal-based fly ash. Physical research methods are employed, namely X-ray diffraction, differential thermal analysis, optical and electron microscopy. 6 references.
Cultivation tests of six types of crop were carried out in a growing medium consisting of washed sandy soil into which three kinds of coalash had been mixed. The aim of the tests was a basic investigation of the adsorption and accumulation by crops of trace elements derived from coalash. 1) The growth of kidney beans and soya beans was markedly inhibited by the presence of coalash. Although the growth of cabbages and of the above-ground parts of Japanese radishes was hardly affected, growth of the radish roots was retarded. 2) Investigations were made of the concentrations of ten elements in the crops grown. It was discovered that the concentrations of As, B, Mo, Se and Sr tended to rise when coalash had been added, but that the Mn concentration dropped. The trends seen in the concentration of Fe, Sb and Zn varied from one crop to another. (14 refs.) (In Japanese)
In this paper, microwave digestion conditions have been optimised to achieve complete recoveries for the ash-forming inorganic elements in coal and coal combustion fly ash, during the analysis by inductively coupled plasma optical emission spectroscopy (ICP-OES). The elements analysed include six major (Al, Ca, Fe, K, Mg and Na) and twelve trace (As, Ba, Be, Co, Cr, Cu, Li, Mn, Ni, Pb, Sr and V). Seven reference samples have been tested, including two standard coal references, SRM1632c and SARM19, their corresponding high-temperature ashes (HTAs), and three coal fly ash references, SRM1633c, SRM2690 and BCR38. The recoveries of individual elements in these samples have been examined intensively, as a function of the amount of hydrofluoric acid (HF, 0–2.0ml), microwave power (900W v...
Low quality coal and waste can be burned in fluidised beds. Tests have shown that South African mine waste with an ash content of 40% can be burned successfully. The activities of Fluidised Combustion Contractors Ltd., are described.
Samples of two high-aluminum coals and an associated fly ash were collected from a coal-fired power plant and a coalfield in Inner Mongolia, China. The mineralogy and physicochemical characteristics of low-temperature ash (LTA), high-temperature ash (HTA), and fly ash from those coals were studied by X-ray diffraction (XRD), X-ray fluorescence (XRF), and field scanning electron microscopy with energy dispersive X-ray spectroscopy (FSEM-EDX). The transformation of typical aluminum-bearing minerals at high temperature was investigated by systematic drop tube furnace (DTF) experiments and thermogravimetric analysis. The results show that the aluminum-bearing minerals in the high-Al coal are mainly boehmite and kaolinite. High temperature treatment transforms the aluminum-rich minerals to gamm...
The mercury adsorption capacity of a residual oil fly ash (ROFA) sample collected form Florida Power and Light Company's Port Everglades Power Plant was evaluated using a bituminous coal combustion flue gas simulator and fixed-bed testing protocol. A size...
A new separation technology for pulverized coals in cement plants was proposed. Two pulverized coals, NJ and ZZ, were sampled in two cement plants in China. Not only the ash and volatile matter content but also the size of the ash-containing particles and of those from which volatiles have to evolve have been determined with a float-sink method and a laser particle size analyzer. As the coal needed in a kiln and in a calciner is usually at a ratio of 4:6 in calorific value, the pulverized coals can be separated at 60 m and 50 m for NJ and ZZ samples, respectively. It was found that the ash content (air dry base) of the coarser part of NJ sample was 23.51%, in contrast to 34.72% before separation. Similarly, the ash content (air dry base) of the coarser part of ZZ sample was 13.86%, in cont...
Jul 20, 2004 ... recommends that procuring agencies specify that tire repair and retread .... Coal fly ash and ground granulated blast furnace (GGBF) slag are .... Steel from the EAF process contains a total of 100% recovered steel, of which ...
may contain coal fly ash or ground granulated blast furnace (GGBF) slag. ... Motor Vehicle Tires – Tire means the following types of tires: Passenger car tires, light and ..... Steel from the EAF process contains a total of 100% recovered steel ...
Twenty-one elements were determined after acid digestion, using interference correction factors. Recoveries were low for only Cr and alkali metals with direct digestion of coal, and for the more volatile elements with ashing before digestion.
Jun 5, 2012 ... The selenium time bomb has three components: (1) high food-chain bioaccumulation; ... (3) landfill disposal of seleniferous fly ash from coal-fired power plants; and (4) mobilization of selenium from animal feedlot wastes.
Coalash disposal is one of the main problems in thermal power plant unit. Currently, a number of waste management systems are being tried for effective disposal of coalash. In this paper, coalash from thermal power plant unit was successfully utilized for synthesis of mullite ceramic by using transferred arc plasma processing (TAP) technique. For this purpose, bauxite was added with coalash by 0, 25, 50 and75 weight ratio. The compositions were thoroughly mixed by ball milling and were melted in the transferred arc plasma torch at 10kW input power level for 3min. Argon was used as plasma forming gas. The phase and microstructure formation of the melted samples were investigated by XRD and SEM images. The results show that the additions of bauxite greatly influenced the phase formation ...
The production of ash particles from coal combustion limits it`s use as a fuel. On mechanism by which small ash particles are formed is the generation of submicron aerosols through a vaporization/condensation mechanism. Previous work has shown that coal cleaning can lead to increased emissions of aerosols. This research will investigate the means or aerosol formation in coals and the effects that various methods of coal cleaning have on aerosol production, and whether or not cleaning can be performed in a manner that will not lend itself to aerosol formation.
The initial goal of the research project was to develop methods of coal surface control in advanced froth flotation to achieve 90% pyritic sulfur rejection, while operating at Btu recoveries above 90% based on run-of-mine quality coal. Moreover, the technology is to concomitantly reduce the ash content significantly (to six percent or less) to provide a high-quality fuel to the boiler (ash removal also increases Btu content, which in turn decreases a coal`s emission potential in terms of lbs SO{sub 2}/million Btu). (VC)
The quality of fly ash is of considerable importance to fly ash utilizers. The fly ash puzzolanic activity is one of the most important properties that determines the role of fly ash as a binding agent in the cementing process. The puzzolanic activity, however is a function of fly ash particle size and chemical composition. These parameters are closely related to the process of fly ash formation in pulverized coal fired furnaces. In turn, it is essential to understand the transformation of mineral matter during coal combustion. Due to the particle-to-particle variation of coal properties and the random coalescence of mineral particles, the properties of fly ash particles e.g. size, SiO{sub 2} content, viscosity can change considerably from particle to particle. These variations can be described by the use of the probability theory. Since the mean values of these randomly changing parameters are not sufficient to describe the behavior of individual fly ash particles during the formation of concrete, therefore it is necessary to investigate the distribution of these variables. Examples of these variations were examined by the Computer Controlled Scanning Electron Microscopy (CCSEM) for particle size and chemical composition for Texas lignite and Eagel Butte mineral matter and fly ash. The effect of combustion on the variations of these properties for both the fly ash and mineral matter were studied by using a laminar flow reactor. It is shown in our paper, that there are significant variations (about 40-50% around the mean values) of the above-listed properties for both coal samples. By comparing the particle size and chemical composition distributions of the mineral matter and fly ash, it was possible to conclude that for the Texas lignite mineral matter, the combustion did not effect significantly the distribution of these properties, however, for the Eagel Butte coal the combustion had a major impact on these mineral matter parameters.
Graphic techniques exist which can accurately predict values for calorific value, organic sulfur, and several other constituents of the organic portion of beneficiated coal sample fractions. These techniques also permit a determination of coal rank to be made without the use of approximations required in the standard procedure. In beneficiation studies, plots of the calorific value of each fraction vs its ash content invariably produce straight lines. The Y axis intercept is the mineral-matter-free Btu value used (on the moist basis) to determine coal rank and the X axis intercept is a value we will call ``maximum ash.`` These two constants permit us to calculate all future Btu values of fractions of this coal from the ash, alone. Plots of organic sulfur vs ash sometimes produce lines which are straight and at other times curved. In any event, they can be used to read off values of organic sulfur corresponding to a particular ash value in lieu of analyses. When all values truly represent only organic sulfur, the X axis intercept must occur at the same maximum ash value obtained from the Btu/ash curve. When the line is straight, the Y axis intercept is the mineral-matter-free organic sulfur, and all future organic sulfur values may be calculated from these 2 constants and the ash. Fractions of IBC-101 with varying ash contents were produced by froth flotation. The various fractions were analyzed by the coal analysis laboratory and the particular data type was plotted in each case vs the individual ash content of each fraction, using Lotus 123 and Freelance software packages. Such plots for calorific value and organic sulfur have, so far, been discussed in the second quarterly report. A comparison of the graphic mineral matter value with the usual one calculated from the Parr approximation was also discussed in that report. In this third quarterly report we examine the curves for volatiles, fixed carbon, total carbon, total hydrogen, and nitrogen vs ash.
This paper presents a stochastic analysis of coalbed methane (CBM) resources for a coal seam in southeast Qinshui Basin, China. Log and laboratory data are used to predict the coal thickness, coalash content and coal gas content. Using reservoir modelling, the distributions of the karst collapse column (KCC), coal seam thickness, coal quality and coal gas content are generated. The convergent interpolation and sequential Gaussian simulation methods are used to model the surface and structure of the coal seam. The structural models are determined by the surface structure and coal seam thickness. Based on the structural models, the coal and KCC are converted to two facies and their distributions are obtained using object modelling. The coal density distributions are simulated based on each ...
For study the lead emission amount from coal combustion and its environment effect, the lead content of coal, ash and cinder of power station and coal-fired boiler, the lead content of dusts in the period of heating time and the non-heating time in Xi'an City were studied in this paper. The results show that amount of lead emission from 1 ton coal combustion, which lead content in coal was 30 g, was 20 g in atmosphere. The rate of lead emission of coal combustion was about 66%. About 10 million tons of coal was straight burning every year in Xi'an City and suburb, those coal mainly come from Permo-Carboniferous coal in Weibei coal mine, Shaanxi, their average lead content was 30 mg/kg. So the total lead emission from coal combustion to atmosphere was about 200 t annually in Xi'an City. PMID:11987396
A total of 48 samples, feed (run-of-mine) coals and their combustion residues (fly ash and bottom ash) were systematically collected twice a week over a 4 week period (June 1998) from two boiler units (I and II) of the Cayirhan power plant (630 MW) that burns zeolite-bearing coals of late Miocene age. The feed coals are high in moisture (22.8% as-received) content and ash (44.9%) yield and total S content (5.1%), and low in calorific value (2995 kcal/kg). The mineralogy of the feed coals contains unusually high contents of the zeolites (clinoptilolite/heulandite and analcime), which are distributed within the organic matter of coal. Other minerals determined are gypsum, quartz, feldspar, pyrite, dolomite, calcite, cristobalite and clays. Common minerals in the crystalline phase of the combustion residues are anhydrite, feldspar, quartz, hematite, lime and Ca-Mg silicate. Minor and trace amounts of magnetite, cristobalite, maghemite, gehlenite, calcite and clinoptilolite/heulandite are also present in the combustion residues. Trace element contents of the feed coals, except for W, fall within the estimated range of values for most world coals; however, the mean values of Mn, Ta, Th, U and Zr are near maximum values of most world coals. Elements such as As, Bi, Ge, Mo, Pb, Tl, W and Zn are enriched more in the fly ash compared to the bottom ash.
An ash level control system is provided which incorporates an ash level meter to automatically control the ash bed level of a coal gasifier at a selected level. The ash level signal from the ash level meter is updated during each cycle that a bed stirrer travels up and down through the extent of the ash bed level. The ash level signal is derived from temperature measurements made by thermocouples carried by the stirrer as it passes through the ash bed and into the fire zone immediately above the ash bed. The level signal is compared with selected threshold level signal to determine if the ash level is above or below the selected level once each stirrer cycle. A first counter is either incremented or decremented accordingly. The registered count of the first counter is preset in a down counter once each cycle and the preset count is counted down at a selected clock rate. A grate drive is activated to rotate a grate assembly supporting the ash bed for a period equal to the count down period to maintain the selected ash bed level. In order to avoid grate binding, the controller provides a short base operating duration time each stirrer cycle. If the ash bed level drops below a selected low level or exceeds a selected high level, means are provided to notify the operator.
In this paper, synthesis of geopolymer from fluidized bed combustion (FBC) ash and pulverized coal combustion (PCC) fly ash was studied in order to effectively utilize both ashes. FBC-fly ash and bottom ash were inter-ground to three different finenesses. The ashes were mixed with as-received PCC-fly ash in various proportions and used as source material for synthesis of geopolymer. Sodium silicate (Na{sub 2}SiO{sub 3}) and 10 M sodium hydroxide (NaOH) solutions at mass ratio of Na{sub 2}SiO{sub 3}/NaOH of 1.5 and curing temperature of 65 deg. C for 48 h were used for making geopolymer. X-ray diffraction (XRD), scanning electron microscopy (SEM), degree of reaction, and thermal gravimetric analysis (TGA) were performed on the geopolymer pastes. Compressive strength was also tested on geopolymer mortars. The results show that high strength geopolymer mortars of 35.0-44.0 MPa can be produced using mixture of ground FBC ash and as-received PCC-fly ash. Fine FBC ash is more reactive and results in higher degree of reaction and higher strength geopolymer as compared to the use of coarser FBC ash. Grinding increases reactivity of ash by means of increasing surface area and the amount of reactive phase of the ash. In addition, the packing effect due to fine particles also contributed to increase in strength of geopolymers.
Streptomyces setonii 75Vi2 produces an extracellular coal-solubilizing component(s) in the absence of coal. The heat stability, relatively low molecular weight, and insensitivity to proteases of the substance(s) responsible for coal solubilization indicate that the mechanism is nonenzymatic. This report describes factors affecting the production and activity of this substance(s) and the similarity in action to alkaline buffer solutions in solubilizing coal.
Streptomyces setonii 75Vi2 produces an extracellular coal-solubilizing component(s) in the absence of coal. The heat stability, relatively low molecular weight, and insensitivity to proteases of the substance(s) responsible for coal solubilization indicate that the process is nonenzymatic. This report describes factors affecting the production and activity of this substance(s) and the similarity in its action to alkaline buffer solutions in solubilizing coal. 7 refs., 7 tabs.
Washing tests were performed with 5 x 5 x 200 cm{sup 3} laboratory flotation columns on bituminous coal pulps from Zonguldak (Turkey) containing 47.52% of ash. The final product contains 10% of ash with a 73.52% recovery. A re-washing of this concentrate allows to obtain a final product with 5.88% of ash and a 59.27% recovery. Abstract only. (J.S.)
This paper reports on the kinetics of mobilization of trace inorganics from impounded ashes from the Savannah River coal burning steam plant. The magnitude of release of As, Cd, Cr and Ni from both old and recent ash basin sediment cores is also reported. Experimental data on the potential for groundwater contamination by trace inorganics released by the impounded ashes is reported and discussed. The groundwater contained unacceptable levels of As, Mn, and Ni.
An algorithm is described which leads directly to a unique set of coal washing parameters which, in two or more parallel streams, will give maximum yield of product at a given ash. This occurs when all parallel streams are washed to the same incremental ash. This strategy is shown to offer a considerable increase in yield compared to the simpler strategy of washing each stream to the same sumulative ash. 5 refs., 1 fig., 9 tabs.
Some ionic collectors were used as an alternative to conventional non-ionic collectors to obtain clean concentrates from fine coal samples containing 46.1% ash. Mixtures of kerosene and pine oil were used as conventional reagents while commercial fatty acids were used as ionic collectors. Flotation results showed that conventional collectors could not reduce the ash content of concentrate below 21.0% whereas, ionic collectors were found significantly better at reducing the ash content down to 16%, but their yields were lower.
This program will demonstrate the effectiveness of a unique approach which uses a bimodal distribution composed of large sorbent particles and fine fly ash particles to enhance ash agglomeration and sulfur capture at conditions found in direct coal-fired turbines. Under the impact of high-intensity sound waves, sorbent reactivity and utilization, it is theorized, will increase while agglomerates of fly ash and sorbents are formed which are readily collected in commercial cyclones.
It has been reported that fly ash collected from the stack breeching of a conventional coal-fired power plant contains mutagenic material which can be extracted into horse serum or organic solvents. This result caused concern that similar material might be present in the fly ash released from oil-burning power plants. By using the five tester strains of Salmonella typhimurium, the authors have demonstrated the presence of mutagens on oil fly ash collected from an oil-burning power plant.
The aim of this investigation is to compile and to draw conclusions regarding the characteristics of pure wood fuel ashes, and to a lesser degree of ashes from mixed firing of wood fuels mixed with coal, oil, or peat. The study also illuminates different treatment methods to improve the spreading technique, to clean the ashes from heavy metals, and to lessen the amount of unburnt material. Also discussed is the treatment costs. 50 refs, 16 tabs
This paper describes the progress of studies using coalash mixed with organic byproducts in a compost process as a means of converting ash to a desirable commercial product. Mixtures of fly and bottom ash, broiler chicken littler manure, sawdust and pine bark were successfully composted during the winter of 1994. The recipes and compost procedures for production of the manufactured soils are described. The physical, biological and chemical properties of the manufactured soils are being studied and the initial results presented.
A process for preparing a stabilized coal particle suspension which includes the steps of providing an aqueous media substantially free of coal oxidizing constituents, reducing, in a nonoxidizing atmosphere, the particle size of the coal to be suspended to a size sufficiently small to permit suspension thereof in the aqueous media and admixing the coal of reduced particle size with the aqueous media to release into the aqueous media coal stabilizing constituents indigenous to and carried by the reduced coal particles in order to form a stabilized coal particle suspension. The coal stabilizing constituents are effective in a nonoxidizing atmosphere to maintain the coal particle suspension at essentially a neutral or alkaline pH. The coal is ground in a nonoxidizing atmosphere such as an inert gaseous atmosphere to reduce the coal to a sufficient particle size and is admixed with an aqueous media that has been purged of oxygen and acid-forming gases.
There is a growing need of using low-grade coals because of higher quest for power generation. In the present carbon-constrained environment, there is a need of upgrading these coals in terms of moisture, ash, and/or other trace elements. The current paper reviews technologies used mainly categorized as drying for reducing moisture and cleaning the coal for reducing mineral content of coal and related harmful constituents, such as sulfur and mercury. The earliest upgrading of high-moisture lignite involved drying and manufacturing of briquettes. Drying technologies consist of both evaporative and non-evaporative (dewatering) types. The conventional coal cleaning used density separation in water medium. However, with water being a very important resource, conservation of water is pushing toward the development of dry cleaning of coal. There are also highly advanced coal-cleaning technologies that produce ultra-clean coals and produce coals with less than 0.1% of ash. The paper discusses some of the promising upgrading technologies aimed at improving these coals in terms of their moisture, ash, and other pollutant components. It also attempts to present the current status of the technologies in terms of development toward commercialization and highlights on problems encountered. It is obvious that still the upgrading goal has not been realized adequately. It can therefore be concluded that, because reserves for low-grade coals are quite plentiful, it is important to intensify efforts that will make these coals usable in an acceptable manner in terms of energy efficiency and environmental protection. 68 refs., 7 figs.
Kawasaki Heavy Industries completed for the Electric Power Development Company's Takehara Power Station, Unit 3 (700MW), an extremely sophisticated coalash handling plant, which has been performing satisfactorily since it started operation in March 1983. The plant's system complies with the latest requirements, such as automated operation, energy savings, environmental controls, ash utilization, bulk transport for the large kinds of imported coals, etc.
The present article describes briefly the concerns regarding the rehabilitation of coal fly ash basins through standardized afforestation technology i.e. ''ecological engineering'' to mitigate environmental pollution as well as scarcity of fuel wood by generating additional bio-resources and combating the adverse effects of climate change through carbon sequestration. Such models of ecological engineering are considered presently as an efficient tool for rehabilitation of abandoned coal fly ash basins.
A prototype IGCC plant is being developed in Europe, which is designed to gasify all common steam coals. High ash, sulphur and chlorine contents are admissible. The plant meets all regulations on environmental compatibility and safe operation. It is intended to demonstrate that this new technology is also economically justifiable. Special measures in the coal gas generation unit achieve an undercutting of current pollution control regulations, including: fly ash recycling, Claus tail gas recycle, and fuel gas conditioning. 8 figs.
For filling the pits produced in brown coal mining, according to the invention, a material is used which is not toxic to comply with the dumping regulations and which is a mixture of desulphurisation sludge and fly ash. The sludge originates from flue gas washing working with a lime suspension which is situated after a brown coal-fired powerstation boiler and the fly ash originates from an electrostatic filter also assigned to this boiler.
Effect of entrapment of water flow on fine coal flotation was studied. The relation between constant of water flotation rate and flotation time was investigated and the water recycling model was determined. The entrapment model of water flow about the relation between the recovery of fine particle and that of water in concentration was established. Finally, the equation about ash in fine clean coal at any time was derived by introducing a de-ashing coefficient.
For the manufacture of high value carbon products like premium coke and carbon fibers from coal tar pitch, the separation of ash resp. particles insoluble in quinoline (QI) is necessary. The filtration of coal tar pitch with a suitable filter aid makes a satisfactory separation of ash and QI possible. A throughput of up to 350 kg/m/sup 2/h per filter unit can be achieved under optimum conditions. (orig.).
Higher disposal costs, greater longterm liabilities associated with landfilling, and lack of landfill capacity are some of the major reasons that drive the emphasis towards reuse. Recycling of waste products from coal combustion, flue-gas desulfurization and spent bed materials from fluidized-beds are discussed in this paper. Use of fly ash in concrete and coalash for structural fill and road construction are some of the examples given. 4 figs., 1 tab.
This project contains activities on: Rheology of ashes from co-firing of coal and biomass; Investigation of ash and deposit formation in full-scale utility boilers; and Selective catalytic reduction: Deactivation under biomass combustion. A fly ash and deposit investigation was carried out as part of the SK Power Company test programme on co-firing of biomasses in a grate-fired boiler. The alternative biomasses (wood chips, olive stones and shea nuts) contain more K, S, and Cl, than wheat straw, and higher fly ash mass loading (mass of fly ash/volume of flue gas) was observed when co-firing alternative biomasses with wheat straw. Anyhow, no significant change in deposit structure when co-firing alkali-rich biomass was observed: KCl is glues residual ash particles together, independent of the feedstock mixture. Thus it can be concluded that co-firing of the actual biomasses in boilers designed for straw-firing, at the present shares is not problematic, from an ash formation and/or deposit build-up point-of-view. Anyhow the increase in ash mass loading in the flue gas, may cause increased build-up of particulate deposits in the convective pass of the boiler. Mature deposit samples from the Masnedoe and Ensted straw-fired boilers were investigated by SEM and EDX. Each deposit sample was classified into an inner, an intermediate, and an outer main layer. The outermost deposit layers at Masnedoe and Ensted looked chemically quite similar, even though they were of different colours. The intermediate layer at Ensted contained many Si- and Ca-rich particles glued together by melted KCI, while the intermediate deposit layers at Masnedoe were different. Since the straw fuels probably are similar, the differences observed in the deposit chemistry must be induced by the higher temperature of the Masnedoe deposit. An experimental method has been set up for viscosity determinations on ashes from co-firing with wheat straw. The method contains a pre-treatment of the ashes, where salts are washed off, residual carbon is burnt off and the ashes are pre-melted. The choice of sensor material is a trade-off between the inertness and softness of Pt{sub 80}Rh{sub 20} and the hardness and 0{sub 2}-intolerance of molybdenum. The use of graphite or a ceramic material for sensors is not advisable. Measurements should be conducted with as low a rotational speed as allowed by the limitations in the apparatus accuracy. If a gas flow is used, the implications on measurement uncertainty should be investigated. Temperature deviations in the range of 20 deg. C are very possible. In co-firing of coal and biomass, salts will condense out on the aluminisilicate-rich fly ash particles upon cooling. Such ashes should be washed in order to remove the salts. Alkali salts are generally water soluble whereas alkaline earth salts not. Carbon is highly reducing, and if carbon is present in the melt, it reduces iron in the melt to free iron. This changes the characteristics of the melt, and if platinum crucibles are used, the free iron will alloy with the platinum to form a low melting eutectic that causes the crucible to be wrecked. Residual carbon in ashes is removed by heating in air. All samples should be premelted or pelletised and sintered in a separate premelt crucible. This is done for volume reduction, controlled boil-up and homogenisation. An experimental and theoretical study of deactivation of SCR catalysts under biomass combustion has been carried out. It has been shown by laboratory experiments that KCl and K{sub 2}SO{sub 4} are highly poisonous for the commercial type SCR catalysts. It is not possible to regain activity by increasing the operating temperature. The life time may be prolonged by increasing the V-content of the catalyst. However, catalysts with a high V content may become active for oxidation of NH{sub 3} to NO at high levels of potassium. It is possible to regenerate deactivated catalysts to some extent. By wash in sulphuric acid followed by wash in water the activity was restored to about 50% of the activity of a fresh catalyst at 250 deg. C. Two bench scale reactors have been constructed and tested. In the laboratory bench scale reactor it is possible to expose full scale SCR elements to a synthetic areosol of well defined composition. A reactor model for the SCR monoliths has been developed and showed good agreement with experimental data from the laboratory bench scale reactor. (EHS)
Western Research Institute in conjunction with the Electric Power Research Institute, Foster Wheeler Energy International, Inc. and the U.S. Department of Energy Technology Center (METC), has undertaken a research and demonstration program designed to examine the market potential and the technical feasibility of ash use options for pressurized fluidized bed combustion (PFBC) ashes. The assessment is designed to address six applications, including: (1) structural fill, (2) road base construction, (3) supplementary cementing materials in portland cement, (4) synthetic aggregate, and (5) agricultural/soil amendment applications. Ash from low-sulfur subbituminous coal-fired Foster Wheeler Energia Oy pilot circulating PFBC tests in Karhula, Finland, and ash from the high-sulfur bituminous coal-fired American Electric Power (AEP) bubbling PFBC in Brilliant, Ohio, were evaluated in laboratory and pilot-scale ash use testing. This paper addresses the technical feasibility of ash use options for PFBC unit using low- sulfur coal and limestone sorbent (karhula ash) and high-sulfur coal and dolomite sorbents (AEP Tidd ash).
This paper presents the study of the combustion of granular dry sewage sludge performed on a pilot fluidized bed system. The results of monocombustion of sludge and co-combustion with coal were compared with those of coal combustion for ash partitioning, the formation of gaseous pollutants, and heavy metals behavior. It was found that the mineral matter of sludge was essentially retained as bottom ash. The production of fine ash was small during the monocombustion but was high during co-combustion due to the tendency of coal to produce fine ash, which also contained unburned char. The degree of heavy metal volatilization was found to be slightly higher during co-combustion than in monocombustion; however, most of the metals were retained in the ash and their emissions were found to be below the regulated levels. Hg was completely volatilized. However, during combustion trials involving coal, Hg was captured in the cyclone ash at temperatures below 300{sup o}C. During sludge monocombustion the retention of Hg in cyclone ash containing low loss on ignition (LOI) was not enough to decrease emissions below the EU regulated levels; hence, it is necessary to install dedicated flue gas treatment for Hg removal. The leachability and ecotoxicity of sludge and ash were also compared with the new regulatory limits for landfill disposal in the European Union (EU).
The technical objectives of this project are to: identify the partitioning of inorganic coal constituents among vapor, submicron fume, and fly ash products generated during combustion; identify fundamental processes of mineral transformation;incorporate the effects of combustion stoichiometry into an engineering model for ash formation.
A three-day slagging trial is reported which has been performed in the 2.5 MW semi-industrial sized IFRF Furnace No. 1. In the trial the build-up of ash deposits on deposit probes has been followed while simultaneously the transformations of the coal-ash ...
Male Syrian golden hamsters were given 15 weekly intratracheal instillations with suspensions of coal fly ash or oil fly ash. Controls were instilled with saline containing gelatine (0.5 g/100 mL) or to check particle effects with suspensions of hematite (Fe2O3). The common weekly dose was 4.5 mg/ha...
The authors examine the most commonly used techniques for predicting the potential leachate quality of wastes. Three coal-related waste types - slag material and a power station bottom ash and fly ash - were used to demonstrate some of the variances in different leachate prediction methods.
To produce and evaluate the use of aluminum ''ashalloys''--metal matrix composites that incorporate coal fly ash--in the commercial manufacture of cast automotive parts. The use of fly ash as an additive will help reduce the weight and cost of automotive parts, improve selected material properties, and reduce energy consumption and pollution.
An experimental-analytical method is proposed for assessing the methodological error in determining the ash content due to fluctuation in coal density; this method takes account of the sensitivity of the ?-albedo method. Fluctuations in the packing density that are not correlated with the ash content make a real contribution to the methodological error.
The inorganic constituents or ash contained in pulverized coal significantly increase the environmental and economic costs of coal utilization. For example, ash particles produced during combustion may deposit on heat transfer surfaces, decreasing heat transfer rates and increasing maintenance costs. The minimization of particulate emissions often requires the installation of cleanup devices such as electrostatic precipitators, also adding to the expense of coal utilization. Despite these costly problems, a comprehensive assessment of the ash formation and had never been attempted. At the start of this program, it was hypothesized that ash deposition and ash particle emissions both depended upon the size and chemical composition of individual ash particles. Questions such as: What determines the size of individual ash particles What determines their composition Whether or not particles deposit How combustion conditions, including reactor size, affect these processes remained to be answered. In this 6-year multidisciplinary study, these issues were addressed in detail. The ambitious overall goal was the development of a comprehensive model to predict the size and chemical composition distributions of ash produced during pulverized coal combustion. Results are described.
The inorganic constituents or ash contained in pulverized coal significantly increase the environmental and economic costs of coal utilization. For example, ash particles produced during combustion may deposit on heat transfer surfaces, decreasing heat transfer rates and increasing maintenance costs. The minimization of particulate emissions often requires the installation of cleanup devices such as electrostatic precipitators, also adding to the expense of coal utilization. Despite these costly problems, a comprehensive assessment of the ash formation and had never been attempted. At the start of this program, it was hypothesized that ash deposition and ash particle emissions both depended upon the size and chemical composition of individual ash particles. Questions such as: What determines the size of individual ash particles? What determines their composition? Whether or not particles deposit? How combustion conditions, including reactor size, affect these processes? remained to be answered. In this 6-year multidisciplinary study, these issues were addressed in detail. The ambitious overall goal was the development of a comprehensive model to predict the size and chemical composition distributions of ash produced during pulverized coal combustion. Results are described.
An improvement in the lime-sinter process for recovering alumina from pulverized coal fly ash is disclosed. The addition of from 2 to 10 weight percent carbon and sulfur to the fly ash-calcium carbonate mixture increase alumina recovery at lower sintering temperatures.
This paper describes a study undertaken to investigate if cleaning coal to a lower ash by conventional or advanced methods might remove potential pollutants and be cost effective, lower ash content, improve power station efficiency, and the value of sulfur credits that would accrue.
It has already been reported that wet ash turns into a strong alkali agent, which can cause full-thickness skin burns. A case is presented which has the particularity of sustained, self-inflicted contact with wet ash. The coal used was the self-igniting type normally used for burning scented weed or...
The fly ash has found a growing use for the last 25 years, mainly in the public works sector. The fly ash obtained by the combustion of the brown coal of Gardanne contains a major proportion of lime (of the order of 40%) which ensures to it very interesting specific applications, mainly road building materials and fabrication of cements.
Eight samples of fly ash from combustion of hard coal and brown coal were chosen for catalytic testing probing their ability to catalyse redox, radical and acid-base reactions. The catalytic activity of fly ash in decomposition of perhydrol varies from moderate to very high. In phenol hydroxylation with use of perhydrol, the fly ash samples are inert or show weak to medium activity. Catalytic activity of the fly ash in selective oxidation of toluene is low. The fly ashes were inert in oxidizing dehydrogenation of propane and oxidation of propylene. Their activity in the conversion of isopropanol is high, pointing to the existence of acid centres. In the catalytic decomposition of cumene the fly ash shows only dehydrating properties with only traces of cracking activity which shows that only weak acid centres are present. The catalytic properties of fly ash depend on the coal origin, its nature (hard or brown), combustion technology (with or without desulphurisation) or pretreatment (water extraction). The fly ash from combustion of brown coal was the most catalytically active of the samples tested. 13 refs., 4 tabs.
After ashing of the coal at 450 C for 4 hours the ash was digested with HF-HNO/sub 3/-H/sub 2/SO/sub 4/ and the filtrate was analyzed with a high-resolution echelle spectrometer to avoid spectral interferences. Ge recovery was complete.
An inductively coupled plasma optical emission spectrometer was used for the determination of boron in coalash samples. The procedure includes high-temperature ashing, followed by hydrofluoric acid plus aqua regia leaching in a microwave oven. The applicability of this method has been verified by precision and accuracy tests.
Various aspects of external fouling are discussed: processes by which fouling develops; the deposition mechanisms involved; the general structure of fouling once it has developed; external fouling and the components of coalash (the relation between the amount of fouling and the melting characteristics and viscosity of the ash components). 46 references
Coal is a heterogeneous material containing organic combustible matter and mineral matter. The mineral matter (i.e., impurities) may be broadly divided into two categories; those forming ash and those that contribute sulfur. Such ash-forming and sulfur-containing impurities may b...
A process for recycling coal fines and ash particles in the reaction effluent from a fluidized bed gasification reactor for further gasification is disclosed. Surfaces of the reactor exit pipeline, cyclone inlet pipeline and first stage cyclone are maintained at a temperature lower than that of the effluent through the use of cooling jackets, thereby preventing ash adhesion on the surfaces.
This paper describes activities executed by the Coal Mining Research Center, Japan during fiscal 1994. The following themes are listed as the headlines: high-level coal mining technologies, technologies to improve and automate excavation facilities, technologies to automate transport facilities at open-cut coal mines, coal bed classifying technologies using supersonic waves, development of a high-level process for treating coal cleaning waste water, activities of collecting and exchanging technical information with overseas countries, development of coal mining facilities to improve in-shaft work efficiency, development of a high-efficiency system for in-shaft excavation, development of mechanized excavation facilities, development of a high-speed automation technology for in-shaft transportation, improvement of capacities in coal mining transportation facilities, light-weight bubble concrete manufacturing tests and coalash submergence and dissolution tests purposed for more utilization of coalash, tests related to coal carbonization, safety measures for ground pressure and gas, measures to prevent spontaneous ignition, measures to improve in-shaft environments, and means for better application of safety facilities and devices. Operations commissioned from NEDO include selection and investigation on coals for coal gasification, discussions on coal liquefaction technologies (liquefying reactions, carbonizing reactions, and environmental harmonization), a joint discussion activity with China on environment harmonizing coal utilization systems, and investigations on coal bed gases. 20 figs., 1 tab.
Here discussion is confined to the coal chemistry of the transition metals, some of which are known to play catalytic roles in coal combustion, and to the coal chemistry of the halogens. The presence of F and Cl at the per cent levels in some coals is significant for combustion technologies (concerned with corrosion problems, etc.) and for problems related to atmospheric emissions. The analytical data reported pertain to samples of raw coal, ash from coal, lignite and tar sand, as well as NBS standard reference coals and coalash. The non-reference coals are bituminous coals from Western Canadian mines, hosted in Cretaceous formations. The lignites are from North Dakoga and Ontario, and the tar sand from Fort McMurray, Alberta. The British Columbia coals are from different seams in the same mine, as are the Alberta coals. The analytical techniques employed in all these studies are spark source mass spectroscopy (SSMS) and electron spectroscopy for chemical analysis (ESCA). The concentrations, obtained by SSMS, of transition metals and halogens for some North American coals and coal-related materials are compared to data available for coal from various sources and to crustal abundances.
It was reported last quarter that attempts to reduce the ash content of the Hydrocarbon Technology, Inc. (HTI) bottoms material following N-methyl pyrrolidone (NMP) extraction and centrifugation produced a coal-derived pitch with an ash content of 0.7 wt%. Additional processing by pressure filtration through a 0.2 {micro}m Teflon filter produced a coal-derived pitch with an ash content of 0.5 wt%. The latter result indicates that the ash-forming constituents are sub-micron in dimensions. Because the ash exhibited the color of an iron oxide, the assumption was made that the ash-forming matter is primarily iron based. Thus, a portion of the inorganics may be soluble in a dilute solution of HCI acid. To test this assumption, 200 g of the coal liquid were redissolved in 1.5 L of NMP. Table 1 compares some data of the properties of the acid-washed coal liquid with those from centrifugation alone. It is evident that the acid treatment was effective in reducing the quantity of ash significantly. In addition, because some of the lighter coal components were discarded with the supernatant liquid, the coke yield, real density, and softening point temperature all increased.
The main goal of this project is to develop a bench-scale procedure to design and fabricate advanced brake and structural composite materials from Illinois coal combustion residues. Scanning electron microscopy (SEM), differential scanning calorimetry (DSC), differential thermal analysis (DTA), and transmission-Fourier transform infrared (FTIR) were conducted on PCC fly ash (Baldwin), FBC fly ash (ADM unit1-6), FBC fly ash (S.I. coal), FBC spent bed ash (ADM unit1-6), bottom ash, and scrubber sludge (CWLP) residues to characterize their geometrical shapes, mineral phases, and thermal stability. Our spectroscopic results indicate that the scrubber sludge is mainly composed of a gypsum-like phase whose lattice structure is different from the lattice structure of conventional gypsum, and sludge does not contain hannebachite (CaSO{sub 3}0.5H{sub 2}O) phase. In the second and third quarters the focus of research has been on developing protocols for the formation of advanced brake composites and structural composites. Our attempts to fabricate brake frictional shoes, in the form of 1.25 inch disks, from PCC fly ash, FBC spent bed ash, scrubber sludge, coal char, iron particles, and coal tar were successful. Based on the experience gained and microscopic analyses, we have now upscaled our procedures to fabricate 2.5 inch diameter disks from coal combustion residues. The SEM and Young`s modulus analyses of brake composites fabricated at 400 psi < Pressure < 2200 psi suggest pressure has a strong influence on the particle packing and the filling of interstices in our composites.
Investigations carried out by the Institute of Geology and Geotechnics of the Academy of Sciences of Czechoslovakia are discussed. The investigations were aimed at determining the optimum conditions for in situ solution mining of brown coal using alkaline solutions. Twelve brown coal samples with carbon content ranging from 64.5 to 90.7% were treated with sodium hydroxide solution with concentration ranging from 1 to 5%. Effects of hydrogen peroxide (15%) and ethanolamine (5%) also were investigated. Proportion of the 3 compounds in water was the following: 500 ml sodium hydroxide, 100 ml ethanolamine and 20 ml hydrogen peroxide. Effects of coal grain size on its disintegration in the alkaline solution also were analyzed. Conditions of in situ solution mining were simulated in the laboratory. Investigations showed that the optimum coal grain size was 2 mm, in which case disintegration efficiency depended on carbon content in coal. The lower the carbon content was, the more efficient was the alkaline disintegration. Alkaline solutions did not influence brown coal with carbon content higher than 85%. The optimum concentration of sodium hydroxide was 3%. Addition of hydrogen peroxide and ethanolamine did not influence disintegration. When alkaline solution was pumped 96 h long into a borehole, it penetrated coal to a depth of 2 mm causing swelling of the borehole walls but not coal disintegration. 8 references.
The generation of fly ash during coal combustion represents a considerable solid waste disposal problem in the state of Illinois and nationwide. In fact, the majority of the three million tons of fly ash produced from burning Illinois bituminous coals is disposed of in landfills. The purpose of this study was to obtain a preliminary assessment of the technical feasibility of mitigating this solid waste problem by making fired bricks with the large volume of fly ash generated from burning Illinois coals. Test bricks were produced by the extrusion method with increasing amounts (20-50% by weight) of fly ash as a replacement for conventional raw materials. The chemical characteristics and engineering properties of the test bricks produced with and without 50 wt% of fly ash substitutions were analyzed and compared. The properties of the test bricks containing fly ash were at least comparable to, if not better than, those of standard test bricks made without fly ash and met the commercial specifications for fired bricks. The positive results of this study suggest that further study on test bricks with fly ash substitutions of greater than 50wt% is warranted. Successful results could have an important impact in reducing the waste disposal problem related to class F fly ash while providing the brick industry with a new low cost raw material. Copyright ?? 2001 Taylor & Francis.
State of Research: The Pressurized Pulverized Coal Combustion Combined Cycle (PPCCCC) with a directly fired gas turbine can reach electrical efficiencies beyond 50%. The required gas quality upstream the gas turbine has not been reached yet at temperatures above 1000 C. One approach tested is the precipitation of ash and alkalines at temperatures above the ash melting point. This principle contains problems concerning the remaining content of ash and alkalines in the flue gas and damages to the refractory materials due to corrosion. Goal of the Investigation: An alternative process had to be investigated in which the flue gas is cleaned according to the state of the art, i.e. below the ash fusion temperature. This principle requires cooling down the flue gas and heating it up again after cleaning in a high temperature heat exchanger. Method: A ceramic tube-and-shell heat exchanger in a model scale was designed and was operated at realistic conditions in an atmospheric test plant in connection with a high temperture precipitation. Result: The heat exchanger showed a good performance concerning design and material. The expected temperatures were not reached totally because of untight joints. Clogging occurred in the tube entrances at high temperatures because of sintered ash agglomerates. First tests to clean the entrances during operation showed positive results. The ash precipitation by means of a cyclone and ceramic filter candles was performed without difficulties. Conclusion: Avoiding and improving joints will help to achieve higher temperatures. A process of cleaning the tubes in-line has to be introduced to prevent the clogging effects. If this is successfully done for high temperatures, an attractive principle for a PPCCCC-process is available which reaches the gas purity required. (orig.) [German] Derzeitiger Stand der Forschung: Der Kohlenstaubdruckfeuerungs-Kombiprozess mit direkt befeuerter Gasturbine verspricht elektrische Wirkungsgrade ueber 50%. Die dazu notwendige Gasreinheit vor der Gasturbine ist bislang bei Temperaturen ueber 1000 C nicht erreichbar. Als ein Ansatz wird versucht, die notwendige Abscheidung von Asche und Alkaliverbindungen oberhalb der Aschefliesstemperatur durchzufuehren. Problematisch hierbei sind v.a. der verbleibende Asche- und Alkaliengehalt im Rauchgas und Korrosionsschaeden an den Feuerfestmaterialien. Zielsetzung der Untersuchung: Eine alternative Schaltung sollte untersucht werden, in der die Gasreinigung nach Stand der Technik unterhalb des Ascheerweichungspunktes erfolgt. Dazu ist eine Abkuehlung und anschliessende Wiederaufheizung des Rauchgases in einem Hochtemperatur-Waermeaustauscher erforderlich. Methode: Eine keramischer Rohrbuendel-Waermeaustauscher im Modellmassstab wurde konstruiert und in einer drucklosen Versuchsanlage zusammen mit einer Heissgasentstaubung unter realen Bedingungen betrieben. Ergebnis: Der Waermeaustauscher erwies sich in Konstruktion und Werkstoffwahl als geeignet. Wegen Undichtigkeiten konnten die angestrebten hohen Temperaturen nicht ganz erreicht werden. Bei hohen Temperaturen verstopfte versinternde Asche die Rohreingaenge. Erste Vorversuchen zur Reinigung der Rohr im Betrieb erbrachten positive Ergebnisse. Die Abscheidung der Asche durch Zyklon und keramische Filterkerzen gelang problemlos. Schlussfolgerung: Bei Vermeidung bzw. Verbesserung von undichten Verbindungen liessen sich hoehere Temperaturen erreichen. Gelingt die Reinigung der Rohreingaenge im Betrieb bei hohen Temperaturen, steht ein Verfahren zur Verfuegung, mit dem die fuer den Prozess noetige Gasreinheit erreicht wird. (orig.)
There is uncertainty as to the rates of coal fly ash needed for optimum physiological processes and growth. In the current study we tested the hyothesis that photosynthetic pigments concentrations and CO{sub 2} assimilation (A) are more sensitive than dry weights in plants grown on media amended with coal fly ash. We applied the Terrestrial Plant Growth Test (Guideline 208) protocols of the Organization for Economic Cooperation and Development (OECD) to monocots (barley (Hordeum vulgare) and ryegrass (Secale cereale)) and dicots (canola (Brasica napus), radish (Raphanus sativus), field peas (Pisum sativum), and lucerne (Medicago sativa)) on media amended with fly ashes derived from semi-bituminous (gray ash) or lignite (red ash) coals at rates of 0, 2.5, 5.0, 10, or 20 Mg ha(-1). The red ash had higher elemental concentrations and salinity than the gray ash. Fly ash addition had no significant effect on germination by any of the six species. At moderate rates ({<=}10 Mg ha{sup -1}) both ashes increased (P < 0.05) growth rates and concentrations of chlorophylls a and b, but reduced carotenoid concentrations. Addition of either ash increased A in radish and transpiration in barley. Growth rates and final dry weights were reduced for all of the six test species when addition rates exceeded 10 Mg ha{sup -1} for gray ash and 5 Mg ha{sup -1} for red ash. We concluded that plant dry weights, rather than pigment concentrations and/or instantaneous rates of photosynthesis, are more consistent for assessing subsequent growth in plants supplied with fly ash.
There is uncertainty as to the rates of coal fly ash needed for optimum physiological processes and growth. In the current study we tested the hyothesis that photosynthetic pigments concentrations and CO{sub 2} assimilation (A) are more sensitive than dry weights in plants grown on media amended with coal fly ash. We applied the Terrestrial Plant Growth Test (Guideline 208) protocols of the Organization for Economic Cooperation and Development (OECD) to monocots (barley (Hordeum vulgare) and ryegrass (Secale cereale)) and dicots (canola (Brasica napus), radish (Raphanus sativus), field peas (Pisum sativum), and lucerne (Medicago sativa)) on media amended with fly ashes derived from semi-bituminous (gray ash) or lignite (red ash) coals at rates of 0, 2.5, 5.0, 10, or 20 Mg ha(-1). The red ash had higher elemental concentrations and salinity than the gray ash. Fly ash addition had no significant effect on germination by any of the six species. At moderate rates ({<=}10 Mg ha{sup -1}) both ashes increased (P < 0.05) growth rates and concentrations of chlorophylls a and b, but reduced carotenoid concentrations. Addition of either ash increased A in radish and transpiration in barley. Growth rates and final dry weights were reduced for all of the six test species when addition rates exceeded 10 Mg ha{sup -1} for gray ash and 5 Mg ha{sup -1} for red ash. We concluded that plant dry weights, rather than pigment concentrations and/or instantaneous rates of photosynthesis, are more consistent for assessing subsequent growth in plants supplied with fly ash.
Studies were conducted on the ashes derived from imported coals to assess the effects of difference in chemical and mineralogical composition to provide a basis for considering the approaches to the production of potassium silicate fertilizer using such ashes. 1. Citric acid-soluble potassium and acid-soluble silicic acid in the potassium silicate fertilizers using imported coalashes were increased by potassium material addition. 2. Potassium silicate fertilizers using the ashes of imported coals such as Workworth did not pass the official standard of potassium silicate fertilizers. 3. This difference in chemical and mineralogical composition was identified as a factor that would affect the production of potassium silicate fertilizer. 4. The potassium silicate fertilizer produced from Workworth Coal washes with aluminium, iron and calcium added passed the official standard. These results indicate that the ashes from imported coals which are low in calcium, iron, and aluminum compared to domestic coals can be used to produce a potassium silicate fertilizer that meets the specification if these elements are added to the ashes during processing.
A research and development program is being conducted by the University of Kentucky/Center for Applied Energy Research, Sandia National Laboratories, LDP Associates and CONSOL Inc. to improve current coal liquefaction technology by physical and chemical pretreatments of the coal and recycle oil. These pretreatment steps include: (1) agglomeration of the coal with ash-containing recycle oil to simultaneously reject coalash and recycle-oil ash, (2) fluid coking of the distillation bottoms (ash-purge) stream and recycle of the coker overhead, (3) dewaxing of the distillate portion of the recycle oil, and (4) low-severity hydrotreatment of the coker overhead and dewaxed oil using hydrogen from an in-situ water-gas shift reaction. These pretreatment steps will remove the ash and unconverted coal, reducing the ash load in the system and simultaneously recovering the maximum amount of organics. Dewaxing and hydrotreatment will yield a high-quality recycle oil distillate. These pretreatment steps are being evaluated technically and economically to develop an improved conceptual liquefaction process. The baseline process to which the improved process will be compared is the Two-Stage Liquefaction Process as it was practiced at the Wilsonville, AL, USA Advanced Coal Liquefaction Test Facility.
Chemical and biological experiments measured the solubility of 16 elements in coal fly ash and the short-term toxicity of coal fly ash to clams and phytoplankton. Of the elements studied, 10 to 60% of the As, Br, Cr, Sb, Se, Ni, Pb, and Sr dissolved within a 24-hour period. Elements which were less than 10% soluble in 24-hours included Cu, Zn, Na, La, Sc, Fe, Co and Eu. Littleneck clams (Protothaca staminea) were exposed to coal fly ash in flowing seawater for a 25-day period. At the end of the exposure Cu concentration in gills was 15 ..mu..g g/sup -1/ dry wt compared to 6 ..mu..g g/sup -1/ in control clams. Elements that were not elevated in the exposed clams were Mn, Fe, Ni, Zn, Se and As. The effects of the soluble fraction of coal fly ash on primary production was measured by /sup 14/C uptake rate on coastal phytoplankton. The addition of soluble coal fly ash material had no effect on the /sup 14/C uptake rate of phytoplankton. These measurements were made in the productive Washington shelf water during August. The literature indicates coal fly ash has a relatively low toxicity to plants and animals. Disposal methods could be designed so EPA water quality criteria levels would not be exceeded except in the immediate vicinity of the dumpsite.
Municipal Solid Waste Incineration (MSWI) produces different sorts of residues, bottom ash, fly ashes and Air Pollution Control (APC) residues. Generally, fly ashes and APC residues are mixed at the MSWI plant and manage as a sole residue. In this study, fly ashes and APC residues have been sampled separately at different Belgian MSWI plant and analysed by X-ray fluorescence in order to highlight the composition differences that may appear between the solids. Ca and Cl are found to be the major elements in most of the samples. Lithophilic elements, such as Al and Si, are richer in furnace and boiler ashes, as can be expected. Leaching tests also show differences between the residues; leachates from furnace and boiler ashes are alkaline while those from bag filter residues present a pH valu...
An improved process for catalytic solvent refining or hydroliquefaction of non-anthracitic coal at elevated temperatures under hydrogen pressure in a solvent comprises using as catalyst a mixture of a 1,2- or 1,4-quinone and an alkaline compound, selected from ammonium, alkali metal, and alkaline earth metal oxides, hydroxides or salts of weak acids.
This Energy & Environmental Research Center (EERC) Year 2 Biomass Utilization Final Technical Report summarizes multiple projects in biopower or bioenergy, transportation biofuels, and bioproducts. A prototype of a novel advanced power system, termed the high-temperature air furnace (HITAF), was tested for performance while converting biomass and coal blends to energy. Three biomass fuels--wood residue or hog fuel, corn stover, and switchgrass--and Wyoming subbituminous coal were acquired for combustion tests in the 3-million-Btu/hr system. Blend levels were 20% biomass--80% coal on a heat basis. Hog fuel was prepared for the upcoming combustion test by air-drying and processing through a hammer mill and screen. A K-Tron biomass feeder capable of operating in both gravimetric and volumetric modes was selected as the HITAF feed system. Two oxide dispersion-strengthened (ODS) alloys that would be used in the HITAF high-temperature heat exchanger were tested for slag corrosion rates. An alumina layer formed on one particular alloy, which was more corrosion-resistant than a chromia layer that formed on the other alloy. Research activities were completed in the development of an atmospheric pressure, fluidized-bed pyrolysis-type system called the controlled spontaneous reactor (CSR), which is used to process and condition biomass. Tree trimmings were physically and chemically altered by the CSR process, resulting in a fuel that was very suitable for feeding into a coal combustion or gasification system w