Estimation of diffusion coefficients in bitumen solvent mixtures as derived from low field NMR spectra

International Nuclear Information System (INIS)

Wen, Y.; Bryan, J.; Kantzas, A.

2005-01-01

Use of solvents for the extraction of heavy oil and bitumen appears to be an increasingly feasible technology. Both vapour extraction and direct solvent injection are considered for conventional exploration and production schemes, while solvent dilution of bitumen is a standard technique in oil sands mining. Mass transfer between solvent and bitumen is a poorly understood process. In some cases, it is totally ignored compared to viscous force effects. In other cases, phenomenological estimations of diffusion and dispersion coefficients are used. Low field NMR has been used successfully in determining both solvent content and viscosity reduction in heavy oil and bitumen mixtures with various solvents. As a solvent comes into contact with a heavy oil or bitumen sample, the mobility of hydrogen bearing molecules of both solvent and oil changes. These changes are detectable through changes in the NMR relaxation characteristics of both solvent and oil. Relaxation changes can then be correlated to mass flux and concentration changes. Based on Fick's Second Law, a diffusion coefficient, which is independent of concentration, was calculated against three oils and six solvents. (author)

Reduction of light cycle oil in catalytic cracking of bitumen-derived crude HGOs through catalyst selection

Energy Technology Data Exchange (ETDEWEB)

Ding, Fuchen; Xu, Chunming [State Key Laboratory of Heavy Oil Processing, China University of Petroleum Beijing, 102200 (China); Ng, Siauw H. [National Centre for Upgrading Technology, 1 Oil Patch Drive, Suite A202, Devon, Alberta (Canada); Yui, Sok [Syncrude Research Centre, 9421-17 Avenue, Edmonton, Alberta (Canada)

2007-09-15

In an attempt to reduce the production of light cycle oil (LCO), a non-premium fluid catalytic cracking (FCC) product in North America, a large-pore catalyst containing rare-earth-exchanged Y (REY) zeolite, was used to crack two Canadian bitumen-derived crude heavy gas oils (HGOs) hydrotreated to different extents. For comparison, a regular equilibrium FCC catalyst with ultra-stable Y (USY) zeolite and a conventional western Canadian crude HGO were also included in the study. Cracking experiments were conducted in a fixed-bed microactivity test (MAT) reactor at 510 C, 30 s oil injection time, and varying catalyst-to-oil ratios for different conversions. The results show that pre-cracking of heavy molecules with wide-pore matrix, followed by zeolite cracking, enhanced conversion at the expense of light and heavy cycle oils at a constant catalyst-to-oil ratio, giving improved product selectivities (e.g., higher gasoline and lower dry gas, LCO, and coke yields, in general, at a given conversion). To systematically assess the benefits of employing the specialty catalyst over the regular catalyst in cracking Canadian HGOs, individual product yields were compared at common bases, including constant catalyst-to-oil ratios, conversions, and coke yields for three feeds, and at maximum gasoline yield for one feed. In most cases, the preferred choice of large-pore zeolite-rich catalyst over its counterpart was evident. The observed cracking phenomena were explained based on properties of catalysts and characterization data of feedstocks, including their hydrocarbon type analyses by gas chromatograph with a mass-selective detector (GC-MSD). (author)

Oil shale : could Shell's experimental oil shale technology be adapted to Alberta's bitumen carbonates?

Energy Technology Data Exchange (ETDEWEB)

Roche, P.

2006-07-01

Although Shell has been trying to develop technologies to economically extract oil from shale containing kerogen for the last 25 years, the volume of oil Shell produced from its Mahogany Research Project in Colorado has added up to less than 2500 bbls in total, and the company has recently devoted $400 million to purchase leases on carbonate reservoirs in Alberta. This article examined whether or not the technologies developed by Shell for oil shales could be used to profitably extract bitumen from carbonates. Extracting bitumen from carbonates may be easier than producing oil from shale, as the resource in carbonates is already oil, whereas the oil in oil shale is actually kerogen, which needs to be chemically cracked at extremely high temperatures. Although the technical feasibility of an in situ cracking process has been proven, work remains to be done before Shell can invest in a commercial-scale oil shale project. Challenges to oil shale production include preventing groundwater from entering target zones and keeping produced fluids out of the groundwater. However, a freeze wall test has recently been designed where chilled liquid is circulated through a closed-loop pipe system to freeze formation water, sealing off an area about the size of a football field from the surrounding strata. The energy requirements of the process that Shell is testing to produce shale oil in Colorado remain unprofitably high, as higher temperatures are necessary for thermal cracking. Shell has yet to make a decision as to what energy sources it will use to make the production process economically viable. An energy conservation group in Colorado has claimed that production of 100,000 bbls of shale oil would require the largest power plant in Colorado history. 2 figs.

Mechanical lifter for recovering highly viscous oil and bitumens

Energy Technology Data Exchange (ETDEWEB)

Rakhmanov, R N; Akhunov, A M; Asfandiyarov, Kh A; Maksutov, R A

1982-01-01

A mechanical lifter is described for recovering highly viscous oil and bitumens. The lifter differs from the known and has significant advantages over them. The lifter was made and tested on a stand well.

Effect of annealing conditions on the molecular properties and wetting of viscoelastic bitumen substrates by liquids

Directory of Open Access Journals (Sweden)

Salomé dos Santos

2017-01-01

Full Text Available Typically, in the production of asphalt concrete, bitumen and mineral aggregates are heated and mixed at temperatures above 100 °C. After the mixing process bitumen ideally coats the mineral aggregates and remains in the form of thin films. Because bitumen is highly temperature sensitive, the study of its properties in terms of chemistry, microstructure and rheology as a function of different annealing conditions is very relevant. The resultant molecular properties have a direct correlation to bitumen macroscopic response to liquids such as water, which is of extreme relevance to the understanding of the detrimental effect of water on asphalt pavements. The wetting characteristics play a crucial role on the extension of detachment of bitumen from the mineral aggregates when asphalt is exposed to wet conditions. Therefore, in this work, the effect of the annealing temperature and cooling history on the chemistry, microstructure and wetting of bitumen films was studied. Crystalline microstructures were identified in bulk and on the surface of the bitumen films. Larger crystals presenting higher crystallinity degree were identified when the annealed bitumen films were cooled slowly. Moreover, higher annealing temperatures increased the oxidation level. The change of the rheological properties due to the alterations of the annealing conditions produced changes in the wetting characteristics. For instance, the advancing motion of a liquid drop on the viscoelastic bitumen substrate presented an intermittent behaviour due to the deformation of bitumen at the liquid-bitumen-air contact line. Consequently, changes in the contact angles were also observed. Keywords: Bitumen, Crystallization, Oxidation, Advancing contact angle, Wetting

Heavy gas oils as feedstock for petrochemicals

Energy Technology Data Exchange (ETDEWEB)

Clark, P.D. [Nova Chemicals Ltd., Calgary, AB (Canada); Du Plessis, D. [Alberta Energy Research Inst., Edmonton, AB (Canada)]|[Alberta Economic Development and Trade, Edmonton, AB (Canada)

2004-07-01

This presentation reviewed the possibilities for converting heavy aromatic compounds and gas oils obtained from Alberta bitumen into competitively priced feedstock for high value refined products and petrochemicals. Upgrading bitumen beyond synthetic crude oil to refined products and petrochemicals would add value to bitumen in Alberta by expanding the petrochemical industry by providing a secure market for co-products derived from the integration of bitumen upgrading and refining. This presentation also reviewed conventional feedstocks and processes; by-products from bitumen upgrading and refining; production of light olefins by the fluid catalytic cracking (FCC) and hydrocracking process; deep catalytic cracking, catalytic pyrolysis and PetroFCC processes; technical and economic evaluations; and opportunities and challenges. Conventional feeds for steam cracking were listed along with comparative yields on feedstock. The use of synthetic gas liquids from oil sands plants was also reviewed. Current FCC type processes for paraffinic feedstocks are not suitable for Alberta's bitumen, which require better technologies based on hydrotreating and new ring opening catalysts. tabs., figs.

Bitumen on Water: Charred Hay as a PFD (Petroleum Flotation Device

Directory of Open Access Journals (Sweden)

Nusrat Jahan

2015-10-01

Full Text Available Global demand for petroleum keeps increasing while traditional supplies decline. One alternative to the use of conventional crude oils is the utilization of Canadian bitumen. Raw bitumen is a dense, viscous, semi-liquid that is diluted with lighter crude oil to permit its transport through pipelines to terminals where it can then be shipped to global markets. When spilled, it naturally weathers to its original form and becomes dense enough to sink in aquatic systems. This severely limits oil spill recovery and remediation options. Here we report on the application of charred hay as a method for modifying the surface behavior of bitumen in aquatic environments. Waste or surplus hay is abundant in North America. Its surface can easily be modified through charring and/or chemical treatment. We have characterized the modified and charred hay using solid-state NMR, contact angle measurements and infrared spectroscopy. Tests of these materials to treat spilled bitumen in model aquatic systems have been undertaken. Our results indicate that bitumen spills on water will retain their buoyancy for longer periods after treatment with charred hay, or charred hay coated with calcium oxide, improving recovery options.

Processing options for bitumen upgrading

International Nuclear Information System (INIS)

Harji, A.N.; Koppel, P.E.; Mazurek, W.L.; Meysami, P.

2003-01-01

It is estimated that 178 billion barrels of oil can be recovered from Alberta's vast heavy oil reserves. The challenge lies in the logistics of recovering, upgrading and transporting the oil to market. The Canadian Energy Research Institute conducted a recent study to determine market potential by 2007 for diluted bitumen and synthetic crude oil produced from upgraded bitumen. The viability for a wide range of bitumen feedstocks was assessed along with the sensitivity of refinery demand to their prices. The 3 major markets for western Canadian bitumen include PADD 2 in the United States, western Canada, and Ontario. Bitumen is too viscous to transport by pipeline and cannot be processed by most of the existing refineries. Therefore, in order to develop a mass market for the product, bitumen must undergo the energy intensive upgrading process at existing refineries. The factors impacting which method of upgrading is most suitable were discussed with particular attention to the impact that Canada's ratification of the Kyoto Protocol may have on Alberta's bitumen resource in terms of costs of complying with greenhouse gas reduction initiatives. The authors emphasized that it is crucial to customize an upgrading project to meet site and market specific factors. 8 refs., 3 tabs., 3 figs

Pipeline transportation of emerging partially upgraded bitumen

International Nuclear Information System (INIS)

Luhning, R.W.; Anand, A.; Blackmore, T.; Lawson, D.S.

2002-01-01

The recoverable reserves of Canada's vast oil deposits is estimated to be 335 billion barrels (bbl), most of which are in the Alberta oil sands. Canada was the largest import supplier of crude oil to the United States in 2001, followed by Saudi Arabia. By 2011, the production of oil sands is expected to increase to 50 per cent of Canada's oil, and conventional oil production will decline as more production will be provided by synthetic light oil and bitumen. This paper lists the announced oil sands projects. If all are to proceed, production would reach 3,445,000 bbl per day by 2011. The three main challenges regarding the transportation and marketing of this new production were described. The first is to expand the physical capacity of existing pipelines. The second is the supply of low viscosity diluent (such as natural gas condensate or synthetic diluent) to reduce the viscosity and density of the bitumen as it passes through the pipelines. The current pipeline specifications and procedures to transport partially upgraded products are presented. The final challenge is the projected refinery market constraint to process the bitumen and synthetic light oil into consumer fuel products. These challenges can be addressed by modifying refineries and increasing Canadian access in Petroleum Administration Defense District (PADD) II and IV. The technology for partial upgrading of bitumen to produce pipeline specification oil, reduce diluent requirements and add sales value, is currently under development. The number of existing refineries to potentially accept partially upgraded product is listed. The partially upgraded bitumen will be in demand for additional upgrading to end user products, and new opportunities will be presented as additional pipeline capacity is made available to transport crude to U.S. markets and overseas. The paper describes the following emerging partial upgrading methods: the OrCrude upgrading process, rapid thermal processing, CPJ process for

Delayed coking studies on Athabasca bitumen and Cold Lake heavy oil

Energy Technology Data Exchange (ETDEWEB)

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

2009-07-01

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

Comparison of product selectivity during hydroprocessing of bitumen derived gas oil in the presence of NiMo/Al{sub 2}O{sub 3} catalyst containing boron and phosphorus

Energy Technology Data Exchange (ETDEWEB)

D. Ferdous; A.K. Dalai; J. Adjaye [University of Saskatchewan, SK (Canada). Catalysis and Chemical Reactor Engineering Laboratories, Department of Chemical Engineering

2006-06-15

A detailed experimental study was performed in a trickle-bed reactor using bitumen derived gas oil. The objective of this work was to compare the activity of NiMo/Al{sub 2}O{sub 3} catalyst containing boron or phosphorus for the hydrotreating and mild hydrocracking of bitumen derived gas oil. Experiments were performed at the temperature and LHSV of 340-420{sup o}C and 0.5-2 h{sup -1}, respectively, using NiMo/Al{sub 2}O{sub 3} catalysts containing 1.7 wt% boron or 2.7 wt% phosphorus. In the temperature range of 340-390{sup o}C, higher nitrogen conversion was observed from boron containing catalyst than that from phosphorus containing catalyst whereas in the same temperature range, phosphorus containing catalyst gave higher relative removal of sulfur than boron containing catalyst. Phosphorus containing catalyst showed excellent hydrocracking and mild hydrocracking activities at all operating conditions. Higher naphtha yield and selectivity were obtained using phosphorus containing catalyst at all operating conditions. Maximum gasoline selectivity of {approximately}45 wt% was obtained at the temperature, pressure, and LHSV of 400{sup o}C, 9.4 MPa and 0.5 h{sup -1}, respectively, using catalyst containing 2.7 wt% phosphorus. 40 refs., 13 figs., 1 tab.

Markets for Canadian bitumen-based feedstock

International Nuclear Information System (INIS)

Marshall, R.; Lauerman, V.; Yamaguchi, N.

2001-02-01

This study was undertaken in an effort to determine the market potential for crude bitumen and derivative products from the Western Canadian Sedimentary Basin in 2007. As part of the study, CERI assessed the economic viability of a wide range of bitumen-based feedstock based on their refining values, investigated the sensitivity of refinery demand to the prices of these feedstocks, and examined the competitiveness of bitumen-based feedstocks and conventional crudes. A US$18.00 per barrel price for West Texas Intermediate at Cushing, Oklahoma, was assumed in all calculations, including other crude prices, as well as for Western Canadian and US crude oil production forecasts. Four different scenarios have been considered, but only the 'most plausible' scenario is discussed in the report. Consequently, Hydrocracked/Aromatics Saturated Synthetic Crude Oil, which is currently only a hypothetical product, is excluded from consideration. The availability of historical price differentials for the various competing crudes was another assumption used in developing the scenario. Proxy prices for the bitumen-based feedstock were based on their respective supply costs. The study concludes that the principal dilemma facing bitumen producers in Western Canada is to determine the amount of upgrading necessary to ensure an economic market for their product in the future. In general, the greater the degree of upgrading, the higher is the demand for bitumen-based feedstock. However, it must be kept in mind that the upgrading decisions of other bitumen producers, along with many other factors, will have a decisive impact on the economics of any individual project. The combination of coking capacity and asphalt demand limits the market for heavy and extra-heavy crudes. As a result, the researchers concluded that major expansion of heavy crude conversion capacity may have to wait until the end of the current decade. The economic market for bitumen-based blends in 2007 is estimated at

Energy consumption and greenhouse gas emissions in the recovery and extraction of crude bitumen from Canada’s oil sands

International Nuclear Information System (INIS)

Nimana, Balwinder; Canter, Christina; Kumar, Amit

2015-01-01

Highlights: • A model to estimate energy consumption and GHG emissions in oil sands is presented. • The model is developed from fundamental engineering principles. • Cogeneration in the oil sands has the ability to offset GHG emissions. • The effect of key parameters is investigated through a sensitivity analysis. - Abstract: A model – FUNNEL-GHG-OS (FUNdamental ENgineering PrinciplEs-based ModeL for Estimation of GreenHouse Gases in the Oil Sands) was developed to estimate project-specific energy consumption and greenhouse gas emissions (GHGs) in major recovery and extraction processes in the oil sands, namely surface mining and in situ production. This model estimates consumption of diesel (4.4–7.1 MJ/GJ of bitumen), natural gas (52.7–86.4 MJ/GJ of bitumen) and electricity (1.8–2.1 kW h/GJ of bitumen) as fuels in surface mining. The model also estimates the consumption of natural gas (123–462.7 MJ/GJ of bitumen) and electricity (1.2–3.5 kW h/GJ of bitumen) in steam assisted gravity drainage (SAGD), based on fundamental engineering principles. Cogeneration in the oil sands, with excess electricity exported to Alberta’s grid, was also explored. Natural gas consumption forms a major portion of the total energy consumption in surface mining and SAGD and thus is a main contributor to GHG emissions. Emissions in surface mining and SAGD range from 4.4 to 7.4 gCO 2 eq/MJ of bitumen and 8.0 to 34.0 gCO 2 eq/MJ of bitumen, respectively, representing a wide range of variability in oil sands projects. Depending upon the cogeneration technology and the efficiency of the process, emissions in oil sands recovery and extraction can be reduced by 16–25% in surface mining and 33–48% in SAGD. Further, a sensitivity analysis was performed to determine the effects of key parameters on the GHG emissions in surface mining and SAGD. Temperature and the consumption of warm water in surface mining and the steam-to-oil ratio (SOR) in SAGD are major parameters

Upgrading of bitumen using supercritical water

Energy Technology Data Exchange (ETDEWEB)

Kayukawa, T. [JGC Corp., Ibaraki (Japan)

2009-07-01

This presentation outlined the technical and economic aspects of thermal cracking by supercritical water. Supercritical water (SCW) is a commonly used method for upgrading heavy oil to produce pipeline-transportable oil from high-viscous bitumen. The process uses water and does not require hydrogen nor catalysts. Pre-heated bitumen and water enter a vertical reactor with flows of counter current at the supercritical point of water. The upgraded synthetic crude oil (SCO) and pitch are obtained from the top of the reactor when the bitumen is thermally cracked. Bench-scale studies have shown that Canadian oil sands bitumen can be converted to 80 volume per cent of SCO and 20 volume per cent of pitch. The SCO has satisfied Canadian pipeline specifications in terms of API gravity and kinetic viscosity. The kinetic viscosity of the pitch has also satisfied boiler fuel specifications. tabs., figs.

Synthesis of quaternary derivatives of ortho-coco di-amido toluene and investigation of these compounds as cationic bitumen emulsifier

Energy Technology Data Exchange (ETDEWEB)

Hassanzadeh, Masoumeh; Tayebi, Leila; Dezfouli, Hedieh; Kambarani, Masoud; Avval, Parviz Ahmadi [Tehran Univ. (Iran, Islamic Republic of). ACECR, Designing Chemical Process Research Group

2012-05-15

Bitumen emulsions are preferred over conventional pavement systems due to their biologically and environmentally acceptable formulation, safety, low viscosity, storage stability, and cost effectiveness. The present investigation deals with the systematic study to synthesize ortho-cocodi-amido toluene and four quaternary derivatives by amidation of coconut oil and ortho toluene diamine (OTD), followed by quaternization with formaldehyde, formic acid mixture, and acrylonitrile, resulted in a new quaternary compound useful as cationic emulsifier in bitumen emulsions. The roles of temperature and reaction time in determining optimum conditions were investigated as well. Emulsifying behavior of these quaternary compounds was studied by sieve residue test, settlement and storage stability test of emulsified asphalt, and water solubility. The results show that the acrylonitrile imidazolinium derivative of o-cocodi-amido toluene (VI) can be used as a rapid-medium setting emulsifier. (orig.)

Effect of different sizes of palm oil fuel ash (POFA) towards physical properties of modified bitumen

Science.gov (United States)

Raja Zulkefli, R. N. A.; Yaacob, H.; Putra Jaya, R.; Warid, M. N. M.; Hassan, N.; Hainin, M. R.; Idham, M. K.

2018-04-01

In the past decades, numerous numbers of studies have been carried out to find ways enhancing properties of bitumen. Other than using polymer, agricultural waste such as palm oil fuel ash (POFA) is one of the waste products that can be used to modify bitumen. In this study, the physical and rheological properties of POFA modified bitumen were examined based on different grinding hour and different percentage of POFA. The bitumen were mixed with different percentages of POFA (0, 5 and 7%) which passed through 0.075 mm sieve and grinded at different period (1 and 4 hour). The samples were then tested and compared to conventional bitumen. From TEM results, POFA grinded at 1 hour have sizes between 3-7 µm while POFA grinded for 4 hours have finer sizes between 500 nm to 3 µm. The results showed that fineness of POFA affect properties of bitumen significantly. Decreasing in penetration value and decreasing in softening temperature indicates that the modified bitumen becomes harder than conventional bitumen. Modified bitumen gives best results when added with 7% POFA sizes of 500 nm to 3 µm compared to 3 to 7 µm.

The need for a marketing strategy for Alberta bitumen

Energy Technology Data Exchange (ETDEWEB)

Redford, D.A. (Alberta Oil Sands Technology and Research Authority, Edmonton, AB (Canada))

1993-03-01

Over the past 15 years, government and industry have invested heavily in research and development of new technology for extracting bitumen from the Alberta oil sands. The results have been a dramatic increase in the fraction of oil sands deposits that could be economically exploited and a drop in production costs. However, no rapid increase in bitumen recovery has been achieved and most new bitumen production projects have been postponed or cancelled. This is the result of very variable prices for bitumen and the inadequacy of a marketing strategy which relies on the sale of raw bitumen. Options such as transport of bitumen to southern markets are limited by the need to reduce bitumen viscosity for pipelining and by the limited market for emulsified or diluted bitumen. Another possible strategy, conversion of the bitumen to synthetic crude oil, is limited by high costs, product characteristics (too much diesel and not enough gasoline), and a market limited to specialized refineries. A third strategy is to convert and refine bitumen to transportation fuels in Alberta, using inexpensive local natural gas, and transporting the products through existing pipeline facilities. 3 figs.

The need for a marketing strategy for Alberta bitumen

International Nuclear Information System (INIS)

Redford, D.A.

1993-01-01

Over the past 15 years, government and industry have invested heavily in research and development of new technology for extracting bitumen from the Alberta oil sands. The results have been a dramatic increase in the fraction of oil sands deposits that could be economically exploited and a drop in production costs. However, no rapid increase in bitumen recovery has been achieved and most new bitumen production projects have been postponed or cancelled. This is the result of very variable prices for bitumen and the inadequacy of a marketing strategy which relies on the sale of raw bitumen. Options such as transport of bitumen to southern markets are limited by the need to reduce bitumen viscosity for pipelining and by the limited market for emulsified or diluted bitumen. Another possible strategy, conversion of the bitumen to synthetic crude oil, is limited by high costs, product characteristics (too much diesel and not enough gasoline), and a market limited to specialized refineries. A third strategy is to convert and refine bitumen to transportation fuels in Alberta, using inexpensive local natural gas, and transporting the products through existing pipeline facilities. 3 figs

Autosolvent effect of bitumen in thermal cracking; Netsubunkai hanno ni okeru bitumen no jiko yobai koka

Energy Technology Data Exchange (ETDEWEB)

Mikuni, M.; Sato, M.; Hattori, H. [Hokkaido University, Sapporo (Japan). Center for Advanced Research of Energy Technology; Nagaishi, H.; Sasaki, M.; Yoshida, T. [Hokkaido National Industrial Research Institute, Sapporo (Japan)

1996-10-28

Tar sand bitumen is petroleum-based ultra-heavy oil, and has a great amount of reserve like coal. However, there are still a lot of problems for its highly effective utilization. This paper discusses whether the light components in bitumen show independent behavior during the thermal cracking of heavy components, or not. Solvent effect and reaction mechanism during the thermal cracking are also derived from the change of their chemical structures. Athabasca tar sand bitumen was separated into light and heavy fractions by vacuum distillation based on D-1660 of ASTM. Mixtures of the both fractions at various ratios were used as samples. Negative effect of the light fraction on cracking of the heavy fraction was observed with dealkylation and paraffin formation Polymerization of the dealkylated light fraction to the heavy fraction was suggested due to lack of hydrogen in the thermal cracking under nitrogen atmosphere, which resulted in the formation of polymer. 3 refs., 6 figs.

New technology for producing petrochemical feedstock from heavy oils derived from Alberta oil sands

International Nuclear Information System (INIS)

Oballa, M.; Simanzhenkov, V.; Clark, P.; Laureshen, C.; Plessis du, D.

2006-01-01

This paper presented the results of a study demonstrating the feasibility of producing petrochemical feedstock or petrochemicals from vacuum gas oils derived from oil sands. A typical bitumen upgrader flow scheme was integrated with several new technologies and coupled with an ethane/propane cracker. Technologies included steam cracking, fluid catalytic cracking (FCC); and the catalytic pyrolysis process (CPP). The scheme was then integrated with the Nova Heavy Oil Cracking (NHC) technology. The NHC process uses a reactor to perform catalytic cracking followed by a main tower that separates gas and liquid products. Aromatic ring cleavage (ARORINCLE) technology was explored as a method of catalytic treatment. Experimental runs were conducted in a laboratory scale fixed bed reactor. A stacked catalyst bed was used, followed by a zeolite-based noble metal catalyst. Examples from process run results were presented. Results indicated that the NHC technology should be used on an FCC unit technology platform. The ARORINCLE technology was considered for use on a hydrotreating unit technology platform. Once the catalysts are fully developed and demonstrated, the economics of the technologies will be enhanced through the construction of world-scale complexes integrating upgrading, refining and petrochemical plants. refs., tabs., figs

Self lubrication of bitumen froth in pipelines

International Nuclear Information System (INIS)

Joseph, D.D.

1997-01-01

In this paper I will review the main properties of water lubricated pipelines and explain some new features which have emerged from studies of self-lubrication of Syncrudes' bitumen froth. When heavy oils are lubricated with water, the water and oil are continuously injected into a pipeline and the water is stable when in a lubricating sheath around the oil core. In the case of bitumen froth obtained from the Alberta tar sands, the water is dispersed in the bitumen and it is liberated at the wall under shear; water injection is not necessary because the froth is self-lubricating

Improving Asphalt Mixture Performance by Partially Replacing Bitumen with Waste Motor Oil and Elastomer Modifiers

Directory of Open Access Journals (Sweden)

Sara Fernandes

2017-08-01

Full Text Available The environmental concern about waste generation and the gradual decrease of oil reserves has led the way to finding new waste materials that may partially replace the bitumens used in the road paving industry. Used motor oil from vehicles is a waste product that could answer that demand, but it can also drastically reduce the viscosity, increasing the asphalt mixture’s rutting potential. Therefore, polymer modification should be used in order to avoid compromising the required performance of asphalt mixtures when higher amounts of waste motor oil are used. Thus, this study was aimed at assessing the performance of an asphalt binder/mixture obtained by replacing part of a paving grade bitumen (35/50 with 10% waste motor oil and 5% styrene-butadiene-styrene (SBS as an elastomer modifier. A comparison was also made with the results of a previous study using a blend of bio-oil from fast pyrolysis and ground tire rubber modifier as a partial substitute for usual PG64-22 bitumen. The asphalt binders were tested by means of Fourier infrared spectra and dynamic shear rheology, namely by assessing their continuous high-performance grade. Later, the water sensitivity, fatigue cracking resistance, dynamic modulus and rut resistance performance of the resulting asphalt mixtures was evaluated. It was concluded that the new binder studied in this work improves the asphalt mixture’s performance, making it an excellent solution for paving works.

Primary migration of Jurassic coal-derived oil in Santanghu basin

Energy Technology Data Exchange (ETDEWEB)

Zhang, W.; Zhong, N.; Ren, D. [China University of Mining and Technology, Beijing (China). Dept of Resource Exploitation Engineering

2000-11-01

It is known that the differential evolution of the multiple macerals results in 'oil generation by stage', and that 'early generation, early expulsion' is one of the preconditions for the efficient accumulation of the coal-derived oil. Based upon the study on the evolution of the physical properties, related to the hydrocarbon expulsion, of the Jurassic organic rock in Santanghu basin during the course of maturation, the mechanism of the primary migration of its coal-derived oil was discussed. The rapid loss of the inherent moisture in the organic rock was not accordant with the main generation stage of the coal-derived oil, so it was unrealistic that the oil migrated by dissolution in the expelled water. It is thought that the special forming mechanism of the continuous 'bitumen network' under the condition of over-pressure and an earlier history of primary migration may be essential to the Jurassic coal-derived oil in Santanghu basin. 17 refs., 4 figs.

THE IMPROVEMENT OF TECHNOLOGY PRODUCTION OF BITUMEN FOR THE ROAD PAVING

Directory of Open Access Journals (Sweden)

N. A. Belova

2016-01-01

Full Text Available Aim. The oil (artificial bitumens, got by conversion of the oil cheese, are broadly used in the road construction. The track record of the development road covering, studies, bound with improvement their characteristic and development of the competitions among technology is presented in this article.Methods. Nowdays the modern developments in the field of production bitumen road marks are implemented using such technological-go acceptance as chemical actuated heavy oil cheese, which principles are based on regulation of the energybetween molecular interactions and optimization their dimensionality, allowing raise quality bitumen.Results. Adjusting the depth of recovery of the oxidized product, it is possible to obtain different composition, plasticity and heat resistance of the bitumen. The residual bitumen obtained by two-stage oxidation with subsequent vacuum distillation of the oxidized product comply with GOST 60/90. Vacuum gas oil in the production of residual bitumen corresponds to the motor fuel for marine installations.Conclusion. Today, the bitumen production leaves on positions packed-valuable segment oil processing industry. The Main customer roads - a state. Herewith important role as ideologues of the development of the culture road construction plays the Federal road agency, supporting developing competition amongst leading technology. Introduction new technology at conversion remaining component oils, founded on do active cheese to account physical and chemical of the influence, with using the modern equipment, including equipment, using subject to influence effects, ultrasonic and electro-magnetic fields, and others, allows to get the qualitative road bitumens from majority of the oils, scanned earlier unfit for production bitumen.

Bitumen still seen as potential anchor on crude prices

International Nuclear Information System (INIS)

Jaremko, G.

2001-01-01

Researchers at the Canadian Energy Research Institute have released a 225-page technical report on downstream oil-refining markets entitled 'Markets for Canadian bitumen-based feedstock'. The report claims that 22 of 27 refineries that buy western Canadian production are not planning to improve their ability to process heavy grades of oil any time soon. Instead, investments will focus on complying with environmental requirements for reformulated refined products, particularly to eliminate sulphur impurities in gasoline and diesel fuel. Another focus will be to upgrade raw bitumen output into synthetic crude. It was shown that over the next 7 years, Canadian and U.S. oil markets have the potential to increase growth in bitumen production from 244,000 barrels per day (bpd) to 555,000 bpd. The potential for additional, upgraded synthetic crude oil is even greater, from 450,000 bpd to 806,000 bpd. Increasing the output of synthetic crude oil is considered to be an effective way to reduce North America's reliance on imported oil. Untreated, discount-priced bitumen can replace diminishing Canadian and U.S. production of refinery-ready light oil. The report projects that a US$1-per-barrel discount for Canadian heavy oil would generate sales of 140,000 barrels daily. The effect of a $1 discount would be almost twice as great for synthetic crude oil. Heavy oil sales rely greatly on maintaining a discount off prices for light grades. A $1-per-barrel premium could destroy demand for bitumen-based blends. Moody's Investors Service claims that deep discounting reflects global market conditions, risking Canadian production of heavy oil grades and seasonal lows in demand for bitumen as a raw material for asphalt

Improved cracking characteristics of bitumen through advanced froth treatment process

Energy Technology Data Exchange (ETDEWEB)

Ng, S.H. [National Centre for Upgrading Technology, Devon, AB (Canada); Dabros, T. [Natural Resources Canada, Devon, AB (Canada). CANMET Advanced Separation Technologies Laboratory; Humphries, A. [Albemarle Catalysts Co., Houston, TX (United States)

2006-07-01

Fluid catalytic cracking (FCC) is the dominant refinery conversion process for producing transportation fuels. Feed to the FCC unit is heavy gas oil (HGO). Its quality depends on the crude used and the processes involved. Bitumen-derived crude (BDC), including synthetic crude oil (SCO) is less superior to produce FCC feed than stocks from conventional sources. As a result, North American refiners have limited the use of BDC in their conventional FCC-based operations. This paper examined the improved cracking characteristics of bitumen through an advanced froth treatment process. This involved processing of the bitumen with paraffinic solvent in froth treatment with removal of some asphaltenes, CCR precursors, and metals. The paper discussed the experimental and subsequent results and discussion, including cracking characteristics; product quality; synergetic effect; and economic benefits. It was concluded that the poisoning effect by some deleterious components such as nitrogen compounds in feeds on the catalyst could be reduced or compensated for by higher C/O ratios (more catalyst per unit weight of feed). In addition, as conversion increased, sulfur in gasoline decreased slightly and linearly with more or less the same magnitude for the two bitumens. 5 refs., 1 tab., 3 figs.

Managing hydrogen and molecules in bitumen upgrading : technology and research opportunities

Energy Technology Data Exchange (ETDEWEB)

Gray, M.G. [Alberta Univ., Edmonton, AB (Canada). Dept. of Chemical and Materials Engineering

2006-07-01

An innovative concept in oil sands mining, extraction and upgrading was presented with reference to selectively removing metals. The approach presently used to upgrade bitumen is to drive the properties of slurry mixtures closer to conventional crude oils. However, it is necessary to remove unwanted contaminants and to convert nearly all of the vacuum residues. The yield and value of the final product can be improved by maximizing the hydrogen content of the liquid products. The currently used and proposed upgrading methods are based on technologies developed between 1929 and 1954, including coking, hydrotreating, hydroconversion, and gasification. This study compared the main technologies for upgrading in terms of management of raw materials and hydrogen. The feasibility of improving recovery by using new approaches to separate bitumen was considered. It was concluded that the rejection of large fractions of bitumen as coke or asphaltenes is undesirable. New thermal process face design challenges such as distillation versus cracking coking and fouling. There is much potential for breakthrough in asphaltene precipitation technologies, based on paraffinic froth treatment concepts. tabs., figs.

NMR measurement of bitumen at different temperatures.

Science.gov (United States)

Yang, Zheng; Hirasaki, George J

2008-06-01

Heavy oil (bitumen) is characterized by its high viscosity and density, which is a major obstacle to both well logging and recovery. Due to the lost information of T2 relaxation time shorter than echo spacing (TE) and interference of water signal, estimation of heavy oil properties from NMR T2 measurements is usually problematic. In this work, a new method has been developed to overcome the echo spacing restriction of NMR spectrometer during the application to heavy oil (bitumen). A FID measurement supplemented the start of CPMG. Constrained by its initial magnetization (M0) estimated from the FID and assuming log normal distribution for bitumen, the corrected T2 relaxation time of bitumen sample can be obtained from the interpretation of CPMG data. This new method successfully overcomes the TE restriction of the NMR spectrometer and is nearly independent on the TE applied in the measurement. This method was applied to the measurement at elevated temperatures (8-90 degrees C). Due to the significant signal-loss within the dead time of FID, the directly extrapolated M0 of bitumen at relatively lower temperatures (viscosity, the extrapolated M0 of bitumen at over 60 degrees C can be reasonably assumed to be the real value. In this manner, based on the extrapolation at higher temperatures (> or = 60 degrees C), the M0 value of bitumen at lower temperatures (index (HI), fluid content and viscosity were evaluated by using corrected T2.

An Embryonic Field of Study: The Aquatic Fate and Toxicity of Diluted Bitumen.

Science.gov (United States)

Alsaadi, Ftoon; Hodson, Peter V; Langlois, Valerie S

2018-01-01

Canada has experienced a significant increase in the transport of diluted bitumen (dilbit), a predominant oil sands product that combines bitumen with diluents derived from oil-gas condensates and other proprietary compounds. The proportion of diluent and the chemical composition of dilbit vary to meet seasonal transport requirements. While the toxic effects of a variety of crude and refined oils are well-studied, the toxicity of dilbit to aquatic species is less well known. This focused review summarizes dilbit production, chemistry, and the few data on toxicity to aquatic species. These data suggest that un-weathered dilbit would cause effects on fish equivalent to those of conventional oils, but its toxicity may be lower, depending on interactions among test conditions, the behavior of dilbit added to water and the species tested.

Process and apparatus for recovering of oil, bitumen, tar, resins, etc

Energy Technology Data Exchange (ETDEWEB)

1921-11-06

A process for recovering oil, bitumen, tar, and resins from oil shale, oil sands, Fuller's earth, peat, brown coal, mineral coal, and wood, through direct action of superheated steam on the material, is characterized by the fact that superheated steam with or without mixing of inert gases at a temperature, which lies below the decomposition temperature of the material being treated, is passed through the material with a high velocity. It leaves through nozzles, used in steam turbines. A method of carrying out the process in which solution medium is used for action on the material is characterized by the fact that solvents such as benzine and benzol are mixed with steam in different quantities.

Canadian heavy crude oil and bitumen: Some new and old ideas

International Nuclear Information System (INIS)

Scott, G.R.

1992-01-01

Canadian conventional heavy oil and bitumen production has been steadily increasing over the last five years. This rise is forecast to continue under modest future crude oil pricing assumptions. During 1990 and 1991, the heavy oil market suffered from wide pricing differentials relative to light crude due to market reductions in Montreal and a feedstock shift at Uno-Ven's Chicago refinery, as well as an increase in the percentage of heavy in the world crude oil supply because of the Iraqi war. These have been offset by price-related bitumen production cuts and minor refinery capacity growth at other locations. The industry is poised for positive change with modest but stable prices and reduced light-heavy differentials caused, in part, by anticipated market expansion due to the June start-up of the Conco coker (50,000 bbl/d) in Montana and the anticipated late fall start up of the Bi-Provincial Upgrader in Saskatchewan (50,000 bbl/d blend). For the future, refinery upgrading and new grass roots refinery additions are suggested for western Canada. Associated transportation savings and condensate blending stock costs are two areas of advantage. Taken together with environmental problems in other densely populated market areas, it makes sense to build new heavy processing capacity near Edmonton but only after all current capacity is debottlenecked and inexpensive additions to current facilities are completed. New capacity will only be built when the heavy/light price differential on feed stock provides economic justification. 11 refs., 2 tabs

Riding out the perfect storm : new technology offers cost-effective solution for bitumen upgrading

Energy Technology Data Exchange (ETDEWEB)

Ross, E.

2007-03-15

An innovative technology designed to partially upgrade heavy oil and bitumen bottoms was presented. The technology was to produce a lighter oil available for transport by pipeline without the use of a diluent or hydrogen. The process also allows coke byproducts to be burnt as fuel to generate steam. Ivanhoe's HTL process uses a continuous, short contact time thermal conversion process that takes place at moderate temperatures and at atmospheric pressures. A circulating transported bed of sand in the system is used to heat the feedstock of heavy oil or bitumen vacuum tower bottoms. Carbon is rejected in the HTL reactor as the long hydrocarbon chains are cracked and coke is deposited on the sand during thermal conversion. The cracked product is then vaporized. The coke-covered sand, vacuum tower bottoms (VTBs), transport gas, and feed that survive the first pass in the reactor are separated in a high temperature cyclone system. Fluids are quenched and vapors are condensed with light oil to maximize liquid yield and minimize undesirable secondary thermal cracking reactions. The resulting liquid is then sent to the product tank for blending, or is recovered in a product distillation tower for further separation. A percentage of the non-condensable gas is recycled to the reactor system for use as transport gas for the circulating sand. Sorbent is added to the heavy oil feed to the distillation tower section to reduce the total acid number (TAN) of the feed as well as to capture sulphur released in the reactor section. Ivanhoe plans to use the technology to process Athabasca bitumen at its California demonstration plant, which is now processing 1000 bbls a day of California heavy feedstock oil. It was concluded that the technology can be used in heavy oil reservoirs anywhere in the world. 2 figs.

Distribution of clay minerals in the process streams produced by the extraction of bitumen from Athabasca oil sands

Energy Technology Data Exchange (ETDEWEB)

Kaminsky, H.A.W.; Etsell, T.H.; Ivey, D.G. [Alberta Univ., Edmonton, AB (Canada). Dept. of Chemical and Materials Engineering; Omotoso, O. [Natural Resources Canada, Devon, AB (Canada). CETC

2009-02-15

The clay minerals present in the oil sands were studied with particular reference to how they are partitioned in bitumen ore during the extraction process. Bitumen production from surface-mined oil sands accounts for nearly two-thirds of the total bitumen production in Alberta. Every cubic meter of mined ore results in 1.3 cubic meters of mature fine tailings (MFT). The characteristic differences between the clay minerals that report to the froth versus the tailings streams were also examined to determine which minerals could impact different unit operations in the bitumen extraction process. X-ray diffraction and random powder samples were used to quantify the clay minerals. Particle size distribution and clay activity balances were also conducted. The degree of partitioning during the conditioning and flotation stages in a batch extractor was determined by the surface properties of the clay minerals. The water-continuous tailings stream was separated into fine and coarse tailings fractions through sedimentation. The study showed that bitumen-clay interactions may be dominated by kaolinite or iron oxides. Clays are responsible for the poor settling behaviour of MFTs. The clay minerals present in the oil sands include illite, illite-smectite, kaolinite, kaolinite-smectite, and chlorite. The close proximity of the tailings ponds to the Athabasca River and volatile organic compounds (VOCs) emission require that the ponds be reclaimed to a natural landscape before mine closure. In addition to its impact on fine tailings reclamation, clay mineralogy plays a role in extraction froth flotation and emulsion stability during froth treatment. The mineralogy of the froth solids was found to be different from the mineralogy of the middlings and tailings solids. 39 refs., 6 tabs., 6 figs.

The big bitumen breakthrough

International Nuclear Information System (INIS)

Koch, G.

1996-01-01

The ongoing transformation of the oilsands and heavy oil sector from a poor cousin a few years ago into the cornerstone of the Alberta oil industry, was discussed. Much of this change is due to the development of SAGD (steam assisted gravity drainage) technology for the underground recovery of heavy oil and tarry bitumens, aided by partly government-funded research, and boosted by a revised provincial royalty regime. The thermal recovery process makes use of a pair of horizontal injection and recovery wells, drilled one above the other. The efficiency of this new technology could produce a shift in the petroleum industry's spending towards oil sands and heavy oil if investors conclude that it is more profitable to produce heavy oil than conventional light oil. Some of the oil sands producers that are poised to invest billions of dollars in various underground bitumen projects in Alberta over the next five years include Suncor, Syncrude, Alberta Energy Co., Amoco Canada, Elan Energy, Imperial Oil Resources, CS Resources, Koch Oil, and Gulf Resources. The ultimate goal is recovery costs of $6 per barrel, which is comparable to the costs of the conventional oil sector. The added advantage of oil sands production is, of course, the virtual elimination of the exploration risk. 3 figs

Evolution of sulfur speciation in bitumen through hydrous pyrolysis induced thermal maturation of Jordanian Ghareb Formation oil shale

Science.gov (United States)

Birdwell, Justin E.; Lewan, Michael; Bake, Kyle D.; Bolin, Trudy B.; Craddock, Paul R.; Forsythe, Julia C.; Pomerantz, Andrew E.

2018-01-01

Previous studies on the distribution of bulk sulfur species in bitumen before and after artificial thermal maturation using various pyrolysis methods have indicated that the quantities of reactive (sulfide, sulfoxide) and thermally stable (thiophene) sulfur moieties change following consistent trends under increasing thermal stress. These trends show that sulfur distributions change during maturation in ways that are similar to those of carbon, most clearly illustrated by the increase in aromatic sulfur (thiophenic) as a function of thermal maturity. In this study, we have examined the sulfur moiety distributions of retained bitumen from a set of pre- and post-pyrolysis rock samples in an organic sulfur-rich, calcareous oil shale from the Upper Cretaceous Ghareb Formation. Samples collected from outcrop in Jordan were subjected to hydrous pyrolysis (HP). Sulfur speciation in extracted bitumens was examined using K-edge X-ray absorption near-edge structure (XANES) spectroscopy. The most substantial changes in sulfur distribution occurred at temperatures up to the point of maximum bitumen generation (∼300 °C) as determined from comparison of the total organic carbon content for samples before and after extraction. Organic sulfide in bitumen decreased with increasing temperature at relatively low thermal stress (200–300 °C) and was not detected in extracts from rocks subjected to HP at temperatures above around 300 °C. Sulfoxide content increased between 200 and 280 °C, but decreased at higher temperatures. The concentration of thiophenic sulfur increased up to 300 °C, and remained essentially stable under increasing thermal stress (mg-S/g-bitumen basis). The ratio of stable-to-reactive+stable sulfur moieties ([thiophene/(sulfide+sulfoxide+thiophene)], T/SST) followed a sigmoidal trend with HP temperature, increasing slightly up to 240 °C, followed by a substantial increase between 240 and 320 °C, and approaching a constant value (∼0.95) at

Proceedings of the 3. NCUT meeting on upgrading and refining of heavy oil, bitumen and synthetic crude oil and the 2. symposium on stability and compatibility during the production, transportation and refining of petroleum

International Nuclear Information System (INIS)

2003-01-01

This conference highlights new developments in refining processes for heavy oil, bitumen, and synthetic crudes. The oil sands/heavy oil industry in Canada has grown significantly in the last decade and could triple by 2012 to reach 2.6 million barrels per day. Experts from the petroleum industry, government organizations and technology providers attended this conference which identified technology gaps and areas where improvements are needed. The presentations demonstrated that many new technologies associated with heavy oil bitumen upgrading and refining have posed compatibility and stability challenges for pipeliners, upgraders and refiners. One of the issues addressed at the conference was the effect of upgrading technologies on market price due to the expected increase in production. Another important issue is how production of bitumen can be increased without significantly increasing greenhouse gas emissions from the refineries and upgrading facilities. The sessions of the conference were entitled: new technology developments in bitumen upgrading; secondary upgrading developments and expanded product opportunities; environmental issues and expanded oil sands development; and, stability and compatibility during the production, transportation and refining of petroleum. Twenty six presentations were indexed separately for inclusion in this database. tabs., figs

Estimation of bitumen and clay content in fine tailings

International Nuclear Information System (INIS)

Motta Cabrera, S.C.; Bryan, J.; Kantzas, A.

2007-01-01

Fine tailings are the components of tailings ponds and the by-product of the oil sand extraction process, consisting mostly of water with small amounts of bitumen, sand, silts and clays. Because of the large volumes of tailings, an important environmental and production process issue involves the reduction of the remaining bitumen in the tailings stream. This paper presented the results of a study that used low field nuclear magnetic resonance (NMR) in order to estimate the bitumen, clay and water content of synthetic tailings samples. NMR is a non-destructive technique that is utilized to determine compositions of oil and brine emulsions and the viscosity of heavy oil and bitumen as well as in reservoir characterization, measuring properties such as permeability, porosity, mobile and immobile fluids, and fluid saturations. The study prepared and tested numerous samples with variable water, bitumen, sand and clay concentrations in the NMR tool under ambient conditions. Two qualities of water and bitumen were used to prepare the synthetic samples. Each type of water and bitumen was analyzed as a single substance and in a mixture with the typical solids found in tailings composition. These included kaolinite, illite, sodium montmorillonite and sand. These synthetic samples were analyzed using different mixing configurations, as a function of time and in two different NMR tools. It was concluded that NMR is a potential application for on-line determination of tailings streams composition. 18 refs., 3 tabs., 17 figs

Synthesis, characterization and performance of NiMo catalysts supported on titania modified alumina for the hydroprocessing of different gas oils derived from Athabasca bitumen

Energy Technology Data Exchange (ETDEWEB)

Ferdous, D.; Bakhshi, N.N.; Dalai, A.K. [Catalysis and Chemical Reactor Engineering Laboratories, Department of Chemical Engineering, University of Saskatchewan, 57 Campus Drive, Saskatoon, Sask. (Canada); Adjaye, J. [Syncrude Canada Ltd., Edmonton Research Center, No. 9421, 17th Avenue, Edmonton, Alta. (Canada)

2007-03-08

In this work, a series of NiMo/Al{sub 2}O{sub 3} catalyst was prepared using different Al{sub 2}O{sub 3} supports modified by titania (0-9 wt%). All modified supports and fresh catalysts were characterized by BET surface area, pore volume and pore diameter measurement, TPR, TPD, XRD, FTIR and Raman spectroscopy analyses. The initial activity of these catalysts were tested in a trickle-bed reactor using three different gas oils such as light gas oil (LGO), blended gas oil (blended: 50% LGO and 50% HGO) and heavy gas oil (HGO), all derived from Athabasca bitumen. Little structural change in alumina was observed with the incorporation of titania. XRD analysis showed the well dispersion of Ni and Mo on the support. Titania in alumina increased the formation of polymolybdenum oxide on the catalyst as evident from TPR and Raman analyses. Weak-intermediate-strong acid sites on the catalyst were observed at all titania concentrations. The Lewis and Bronsted acidity on the catalyst surface increased with the increase in titania concentration from 0 to 9 wt%. Nitrogen conversion increased from 57 to 71 wt%, from 83 to 93 wt% and from 75 to 80 wt% for LGO, blended and HGO, respectively and also sulfur conversion of LGO increased from 86 to 92 wt% when titania concentration was increased from 0 to 9 wt%. For blended and HGO, sulfur conversion was in the range 96-99 wt% at all titania concentrations. (author)

1952 : bitumen beginnings

International Nuclear Information System (INIS)

Anon.

2008-01-01

In 1952, Imperial Oil used trains to deliver the first volumes of Alberta crude to the west coast. The Trans Mountain crude oil pipeline system was completed in 1953. Even in the early 1950s, the McMurray tar sands were recognized as the world's largest source of petroleum, containing an estimated 100 to 300 billion barrels of bitumen. A group of 10 companies had taken out permit rights on 250,000 acres in Alberta, just west of the Saskatchewan border. They began a core hole drilling program on the leases that are now part of Syncrude Canada and Suncor extraction projects. An experimental extraction operation was also carried out by Swedish Shale Oil Company to determine the economic feasibility of oil sands development. The bitumen extraction process used at the Bitumount plant involved heat. The Sun Oil Company applied for permits covering 100,000 acres on the east side of the Athabasca River, near the Bitumount plant. The leases are currently incorporated into several oilsands development projects, including Syncrude Canada's Aurora mine. At the time, Sun Oil also launched a core hole drilling program with plans to conduct further exploratory and development drilling. Other key events in 1952 included the Bonnie Glen discovery well that produced 240 barrels per day, and approval to export gas from the Peace River region. 1 tab., 1 fig

Selective extraction of natural bitumen

International Nuclear Information System (INIS)

Starshov, M.; Starshov, I.

1991-01-01

The work performed in the field of natural bitumen extraction is aimed at maximum separation of organic phase. On treating bituminous rocks with solvents, the associated metals are extracted together with the organic phase and may further exert a negative effect on refining of natural bitumen. the authors propose a simplified two stage technique for the extraction of bitumen which enables to utilize V and Ni contained in the concentrate of the second stage extraction (Table). At the first stage, negative bitumen is extracted with the summary content of metals not exceeding 0.005%. This allows to avoid de metallization of native bitumen and subject it to treatment by catalytic cracking. during this stage gasoline and kerosene fractions, different oil distillates and condensates can be used as solvents. at the second stage, aromatic and halo id compounds bearing wastes and by-products, i.e. cheap and non deficient reagents, serve as solvents. The technology was tested under laboratory conditions using Tatar bituminous sands. It is also possible to use one solvent only, however, on condition that at first the oil product with the summary metal content below 0.005%, and then the remaining product is extracted. The proposed technology has proved so universal that it can be applied to refining any type of raw material to be found in the territory of the Tatar republic, using surface extraction complexes. (author). 9 refs., tab

Project scenarios for bitumen upgrading

International Nuclear Information System (INIS)

Koppel, P.E.; Mazurek, W.L.; Harji, A.

2002-01-01

The established reserves of Alberta's heavy oil resources are 178 billion barrels, and potential recoverable reserves are 315 billion barrels. The challenge of production includes the logistics of recovery, upgrading and transportation to market. Utilization of the bitumen is not simple because bitumen is too viscous to transport by pipeline. In addition, it is not processable by most existing refineries unless it can be upgraded through dilution. This paper examined different factors regarding the economic viability of various upgrading methods of a wide range of bitumen feedstocks. The study also examined the sensitivity of refinery demand to the prices of these feedstocks, along with the competitiveness among bitumen-based feedstock and conventional crudes. Western Canada, Ontario and the PADD II district in the United States are the 3 major markets for western Canadian bitumen based feedstock, the demand for which depends on refinery configurations and asphalt demand. This paper described the following 4 generic scenarios that describe Alberta bitumen upgrading projects: (1) adjacent to open pit mines, (2) adjacent to steam assisted gravity drainage (SAGD) facilities, (3) remotely located from resource production at an existing refinery, and (4) pipeline bitumen. It was noted that producers should determine the best way to upgrade the bitumen to ensure there is an economic market for the product, but they should also be aware not to over process the bitumen so as not to leave existing refinery facilities under-utilized. 2 refs., 1 tab., 3 figs

In-situ water vaporization improves bitumen production during electrothermal processes

Energy Technology Data Exchange (ETDEWEB)

Wang, J. [Calgary Univ., AB (Canada); McGee, B. [E-T Energy, Calgary, AB (Canada); Kantzas, A. [Calgary Univ., AB (Canada). Tomographic Imaging and Porous Media Laboratory

2008-10-15

Electro-thermal processes are now being considered as an alternative or complementary process to steam injection processes. This study used an in situ vaporized water process to optimize electrothermal processes for steam injection enhanced oil recovery (EOR). A simulation tool was used to model electro-thermal processes in an Athabasca oil sands reservoir. Incremental oil recovery was estimated based on a 3-block conceptual model. A field scale model was then used to investigate the effects of electrode spacing, water injection rates, and electrical heating rates on bitumen recovery. Results of the simulation studies were then analyzed using a statistical tool in order to determine optimal conditions for maximizing bitumen production. Results of the study showed that incremental recovery using the water vaporization technique resulted in oil recovery rates of 25 per cent original oil in place (OOIP). Sensitivity analyses showed that medium electrical heating rates, low water injection rates, and small spacings between electrodes maximized bitumen production rates. It was concluded that the technique can be used alone or combined with other methods to economically produce bitumens. 2 refs., 7 tabs., 9 figs.

Trace metals in heavy crude oils and tar sand bitumens

Energy Technology Data Exchange (ETDEWEB)

Reynolds, J.G.

1990-11-28

Fe, Ni, and V are considered trace impurities in heavy crude oils and tar sand bitumens. In order to understand the importance of these metals, we have examined several properties: (1) bulk metals levels, (2) distribution in separated fractions, (3) size behavior in feeds and during processing, (4) speciation as a function of size, and (5) correlations with rheological properties. Some of the results of these studies show: (1) V and Ni have roughly bimodal size distributions, (2) groupings were seen based on location, size distribution, and Ni/V ratio of the sample, (3) Fe profiles are distinctively different, having a unimodal distribution with a maximum at relatively large molecular size, (4) Fe concentrations in the tar sand bitumens suggest possible fines solubilization in some cases, (5) SARA separated fractions show possible correlations of metals with asphaltene properties suggesting secondary and tertiary structure interactions, and (6) ICP-MS examination for soluble ultra-trace metal impurities show the possibility of unexpected elements such as U, Th, Mo, and others at concentrations in the ppB to ppM range. 39 refs., 13 figs., 5 tabs.

Markets for Canadian bitumen-based feedstock

International Nuclear Information System (INIS)

Lauerman, V.

2001-01-01

The best types of refineries for processing western Canadian bitumen-based feedstock (BBF) were identified and a potential market for these feedstock for year 2007 was calculated. In addition, this power point presentation provided an estimation of potential regional and total demand for BBF. BBF included Athabasca bitumen blend, de-asphalted blend, coked sour crude oil (SCO), coked sweet SCO, hydrocracked SCO and hydrocracked/aromatic saturated SCO (HAS). Refinery prototypes included light and mixed prototypes for primary cracking units, light and heavy prototypes for primary coking units, as well as no coking, coking severe and residuum prototypes for primary hydrocracking units. The presentation included graphs depicting the natural market for Western Canadian crudes as well as U.S. crude oil production forecasts by PADD districts. It was forecasted that the market for bitumen-based feedstock in 2007 will be tight and that the potential demand for bitumen-based blends would be similar to expected production. It was also forecasted that the potential demand for SCO is not as promising relative to the expected production, unless price discounting or HAS will be available. 11 figs

Naphtha interaction with bitumen and clays : a preliminary study

Energy Technology Data Exchange (ETDEWEB)

Afara, M.; Munoz, V.; Mikula, R. [Natural Resources Canada, Devon, AB (Canada). CANMET Western Research Centre

2010-07-01

This PowerPoint presentation described a preliminary study conducted to characterize naphtha interactions with bitumen and clays. Coarse tailings, fluid-fine tailings, and froth treatment tailings are produced as a result of surface mine oil sands operations. Solvents are used to produce the bitumens, but the actual fraction of the solvent that evaporates and contributes to VOCs from tailing ponds is poorly understood. This study examined the interactions between the solvent, bitumen and mineral components in froth treatment tails. The study was conducted with aim of quantifying the VOC or solvent escaping from the froth treatment tailings. Samples containing bitumen, clay, a bitumen-clay mixture, or MFT were spiked with 3000 ppm of solvent. The amount of naphtha released was monitored by gas chromatography, mass spectrometry, and flame ionization detection of the evolved gases. The results were expressed as a percentage of the total hydrocarbon peak area of the sample versus a control. Results of the study showed that the naphtha interacted more strongly with the bitumen than with kaolinite and the clay minerals from the oil sands. Although initial solvent evaporation was reduced in the presence of bitumens and clays, long-term solvent releases will need to be quantified. tabs., figs.

Hydrocarbons and oxygen compounds in the bitumens of kukersite oil shales

Energy Technology Data Exchange (ETDEWEB)

Pais, R; Klesment, I; Pobul, L

1979-01-01

This is a continuation of an earlier work which described commercial batches of kukersite in terms of oxidative kerogen destruction. The low concentration of bitumen in the kerogen and its group composition indicate that this bitumen is syngenetic. The authors studied the way in which the bitumen and kerogen are structurally connected. They also analyzed four commercial batches of kukersite and asphaltite, the organic-rich dark-colored layer found in the middle of the kukersite strate. Whereas American studies of Colorado shales containing 10-20% bitumen from organic matter have indicated, based on the identical structures of the bitumen and kerogen that there is a genetic relationship between them, the present study rarely found such structural elements in the bitumen and kerogen. The kukersite contained little bitumen--0.7% of the total organic matter. The authors believed that the different composition of the bitumen and kerogen does not prove that they are epigenetic. Kukersite also fails to follow the rule that the paraffins of ancient shales have KHapprox.1 and carbon chains shorter than C/sub 22/.

Directions in refining and upgrading of heavy oil and bitumen

International Nuclear Information System (INIS)

Dawson, B.; Parker, R. J.; Flint, L.

1997-01-01

The expansion of heavy oil transportation, marketing and refining facilities over the past two decades have been reviewed to show the strides that several Canadian refiners have taken to build up the facilities required to process synthetic crude oil (SCO). Key points made at a conference, convened by the National Centre for Upgrading Technology (NCUT), held in Edmonton during September 1997 to discuss current and future directions in the refining and marketing of heavy oil, bitumen and SCO, were summarized. Among the key points mentioned were: (1) the high entry barriers faced by centralized upgraders, (2) the advantages of integrating SCO or heavy oil production with downstream refining, (3) the stiff competition from Venezuela and Mexico that both SCO and heavy oil will face in the U.S. PADD II market, (4) the differences between Canadian refiners who have profited from hydrocracking and are better able to handle coker-based SCO, and American refiners who rely chiefly on catalytic cracking and are less able to process the highly aromatic SCO, and (5) the disproportionate cost in the upgrading process represented by the conversion of asphaltenes. Challenges and opportunities for key stakeholders, i.e. producers, refiners, marketers and technology licensors also received much attention at the Edmonton conference

Rheological, structural and chemical evolution of bitumen under gamma irradiation

International Nuclear Information System (INIS)

Mouazen, M.; Poulesquen, A.; Bart, F.; Masson, J.; Charlot, M.; Vergnes, B.

2013-01-01

Bitumen derived from crude oil by fractional distillation has been used in the nuclear industry as a radioactive waste encapsulation matrix. When subjected to α, β and γ self-irradiation, this organic matrix undergoes radiolysis, generating hydrogen bubbles and modifying the physical and chemical properties of the material. In this paper, the effects of irradiation on bitumen materials, especially in terms of its physical, chemical, structural and rheological properties, were characterized at radiation doses ranging from 1 to 7 MGy. An increase in the shear viscosity and melt yield stress was observed with increasing doses. Similarly, the elastic and viscous moduli (G' and G'') increase with the dose, with a more pronounced increase for G' that reflects enhanced elasticity arising from radiation-induced cross-linking. In addition, a low-frequency plateau is observed for G', reflecting pseudo-solid behavior and leading to an increase of the complex viscosity. This behavior is due to increased interactions between asphaltene particles, and to aromatization of the bitumen by γ-radiations. Cross-linking of bitumen enhances its strength, as confirmed by various techniques (modulated DSC, DTA/TGA, SEC, FTIR and XRD). (authors)

Hydrogenate bitumen, says Canmet

Energy Technology Data Exchange (ETDEWEB)

Pruden, B B; Denis, J M

1977-06-01

The refining of Canada's heavy oils and in particular oil sand bitumens is complicated by the presence of mineral matter (clay and salt), chemically bound nickel, vanadium, iron, sulfur, and nitrogen. Upgrading is necessary before conventional refining because of the high pitch content of the bitumens. The Canada Centre for Mineral and Energy Technology (CANMET), of the Department of Energy. Mines and Resources, has developed a thermal hydrocracking process which concentrates all of the metals and mineral matter in a small pitch fraction and produces a high yield of low viscosity distillate for subsequent catalytic hydrorefining. Scientists at CANMET also have been working on the development of catalysts for an alternative direct catalytic hydrocracking process. Hydrocracking processes, when compared to the coking processes now employed or envisaged by industry for the next 5 yr, have several advantages which are listed.

Electro-thermal dynamic stripping process : integrating environmentalism with bitumen production

Energy Technology Data Exchange (ETDEWEB)

McGee, B.C.W.; McDonald, C.W. [Society of Petroleum Engineers, Canadian Section, Calgary, AB (Canada)]|[E-T Energy, Calgary, AB (Canada); Little, L. [Society of Petroleum Engineers, Canadian Section, Calgary, AB (Canada)]|[Alberta Energy Research Inst., Edmonton, AB (Canada)

2008-10-15

This paper presented a new method of in situ oil sands extraction developed by Calgary-based E-T Energy. The Electro-Thermal Dynamic Stripping Process (ET-DSP) uses electricity to melt oil sands deposits that are too deep for open pit mining. The energy intensity of production compares favourably with alternative thermal bitumen extraction techniques and water consumption for the process is comparatively low, with all produced water being re-injected into the producing formation without any treatment. With ET-DSP, electrodes are drilled and completed next to the oil sands formation which ensures that the electrical currents are forced to flow to the oil sands formation. The viscosity of the bitumen is lowered by the heat from the current, thereby making the fluid flow more readily into vertical extraction wells. ET-DSP uses electricity directly from the power grid, and does not produce any greenhouse gas (GHG) emissions of its own. The process has the potential to allow operators to focus on areas of oil sands reservoirs that have remained inaccessible. Field studies confirmed that the production of bitumen using this method was achieved with reduced greenhouse gas emissions as compared to other thermal recovery process. The bitumen had trace amount of sand and no emulsions. 5 refs., 5 figs.

Effect of illite clay and divalent cations on bitumen recovery

Energy Technology Data Exchange (ETDEWEB)

Ding, X. [SNC-Lavalin Inc., Calgary, AB (Canada); Repka, C. [Baker Petrolite Corp., Fort McMurray, AB (Canada); Xu, Z.; Masliyah, J. [Alberta Univ., Edmonton, AB (Canada). Dept. of Chemical and Materials Engineering

2006-12-15

Nearly 35 per cent of Canada's petroleum needs can be met from the Athabasca oil sands, particularly as conventional sources of petroleum decline. The interactions between bitumen and clay minerals play a key role in the recovery process of bitumen because they affect bitumen aeration. The 2 clays minerals found in various oil sands extraction process streams are kaolinite and illite. In this study, doping flotation tests using deionized water and electrokinetic studies were performed to examine the effect of illite clays on bitumen recovery. The effect of magnesium ions was also examined and compared with calcium ions. This paper also discussed the effects of temperature and tailings water chemistry. The negative effect of illite clay on bitumen recovery was found to be associated with its acidity. Denver flotation cell measurements indicated that the addition of calcium or magnesium ions to the flotation deionized water had only a slight effect on bitumen recovery, but the co-addition of illite clay and divalent cations resulted in a dramatic reduction in bitumen recovery. The effect was more significant at lower process temperature and low pH values. Zeta potential distributions of illite suspensions and bitumen emulsions were measured individually and as a mixture to determine the effect of divalent cations on the interaction between bitumen and illite clay. The presence of 1 mM calcium or magnesium ions in deionized water had a pronounced effect on the interactions between bitumen and illite clay. Slime coating of illite onto bitumen was not observed in zeta potential distribution measurements performed in alkaline tailings water. When tests were conducted using plant recycle water, the combination of illite clay and divalent cations did not have an adverse effect on bitumen recovery. 25 refs., 3 tabs., 15 figs.

Natural zeolite bitumen cracking

Energy Technology Data Exchange (ETDEWEB)

Kuznicki, S.M.; McCaffrey, W.C.; Bian, J.; Wangen, E.; Koenig, A. [Alberta Univ., Edmonton, AB (Canada). Dept. of Chemical and Materials Engineering

2006-07-01

A study was conducted to demonstrate how low cost heavy oil upgrading in the field could reduce the need for diluents while lowering the cost for pipelining. Low cost field upgrading could also contribute to lowering contaminant levels. The performance of visbreaking processes could be improved by using disposable cracking agents. In turn, the economics of field upgrading of in-situ derived bitumen would be improved. However, in order to be viable, such agents would have to be far less expensive than current commercial cracking catalysts. A platy natural zeolite was selected for modification and testing due to its unique chemical and morphological properties. A catalyst-bearing oil sand was then heat-treated for 1 hour at 400 degrees C in a sealed microreactor. Under these mild cracking conditions, the catalyst-bearing oil sand produced extractable products of much lower viscosity. The products also contained considerably more gas oil and middle distillates than raw oil sand processed under the same conditions as thermal cracking alone. According to model cracking studies using hexadecane, these modified mineral zeolites may be more active cracking agents than undiluted premium commercial FCC catalyst. These materials hold promise for partial upgrading schemes to reduce solvent requirements in the field. tabs., figs.

Bitumen performance and chemistry in solvent refined bitumen blends

Science.gov (United States)

Holleran, Glynn; Holleran, Irina; Wilson, Douglas J.

2017-09-01

In years gone past most oil companies in Australia and New Zealand (NZ) developed experts that bridged the divide between refining and paving. This was supported by laboratories in Australia and sometimes Asia. This is no longer the case and many refineries have ceased bitumen production or closed. With the market moving towards imports and control to supply companies disconnects on bitumen passing a national specification and performance on the road. This reduces both durability and increases costs. This has been addressed by development in NZ of a performance specification for hot mix asphalt binders (including modified) and work being done on sealing grades. This paper discusses the development of the HMA specification with respect to crude sources and the development of methodologies to assess imported binders for suitability in all applications including emulsion. The conclusion is that bitumen quality may be maintained by use of these methodologies that include, chromatographic analysis, measurement of thermodynamic internal stability (Heithaus), aging, and Dynamic Shear Rheometry testing and mix performance testing in the laboratory. This forms a regime capable of use in any context and this leads to better durability of surfaces and extended service life.

Effect of Temperature and Process on Quantity and Composition of Laboratory-generated Bitumen Emissions.

Science.gov (United States)

Bolliet, Christophe; Kriech, Anthony J; Juery, Catherine; Vaissiere, Mathieu; Brinton, Michael A; Osborn, Linda V

2015-01-01

In this study we investigated the impact of temperature on emissions as related to various bitumen applications and processes used in commercial products. Bitumen emissions are very complex and can be influenced in quantity and composition by differences in crude source, refining processes, application temperature, and work practices. This study provided a controlled laboratory environment to study five bitumen test materials from three European refineries; three paving grade, one used for primarily roofing and some paving applications, and one oxidized industrial specialty bitumen. Emissions were generated at temperatures between 140°C and 230°C based on typical application temperatures of each product. Emissions were characterized by aerodynamic particle size, total organic matter (TOM), simulated distillation, 40 individual PACs, and fluorescence (FL-PACs) spectroscopy. Results showed that composition of bitumen emissions is influenced by temperature under studied experimental conditions. A distinction between the oxidized bitumen with flux oil (industrial specialty bitumen) and the remaining bitumens was observed. Under typical temperatures used for paving (150°C-170°C), the TOM and PAC concentrations in the emissions were low. However, bitumen with flux oil produced significantly higher emissions at 230°C, laden with high levels of PACs. Flux oil in this bitumen mixture enhanced release of higher boiling-ranged compounds during application conditions. At 200°C and below, concentrations of 4-6 ring PACs were ≤6.51 μg/m(3) for all test materials, even when flux oil was used. Trends learned about emission temperature-process relationships from this study can be used to guide industry decisions to reduce worker exposure during processing and application of hot bitumen.

Process for refining shale bitumen

Energy Technology Data Exchange (ETDEWEB)

Plauson, H

1920-09-19

A process is disclosed for refining shale bitumen for use as heavy mineral oil, characterized by mixtures of blown hard shale pitch and heavy mineral oil being blown with hot air at temperatures of 120 to 150/sup 0/ with 1 to 3 percent sulfur, and if necessary with 0.5 to 3 percent of an aldehyde.

Hydroprocessing full-range of heavy oils and bitumen using ultradispersed catalysts at low severity

Science.gov (United States)

Peluso, Enzo

The progressive exhaustion of light crude oils is forcing the petroleum industry to explore new alternatives for the exploitation of unconventional oils. New approaches are searching for technologies able to produce, transport and refine these feedstocks at lower costs, in which symbiotic processes between the enhanced oil recovery (EOR) and the conventional upgrading technologies are under investigation. The process explored in this thesis is an interesting alternative for in-situ upgrading of these crude oils in the presence of ultradispersed (UD) catalysts, which are included as a disperse phase able to circulate along with the processed feed. The objectives of this work are: (a) study the performance of UD catalysts in the presence of a full range (non fractioned) heavy oil and bitumen and (b) evaluate the recyclability of the UD catalysts. Four different heavy crude oils were evaluated in the presence with UD catalysts at a total pressure of 2.8 MPa, residence time of 8 hours and reaction temperatures from 360 up to 400ºC. Thermal and catalytic hydro-processing were compared in terms of conversion and product stability. A comparison between the different crude oils was additionally derived in terms of SARA, initial micro-carbon content and virgin oil stability among other properties. Advantages of catalytic hydro-processing over thermal hydro-processing were evidenced, with UD catalysts playing an essential hydrogenating role while retarding coke formation; microcarbon and asphaltenes reduction in the presence of UD catalysts was observed. To evaluate the feasibility of recycling the UD catalysts, a micro-slurry recycled unit was developed as part of this research. These main results showed: (a) a successful design of this unit, (b) that temperature, LHSV and fractional recycling ratio have more impact on VGO conversion, while pressure has almost no effect, and (c) an UD catalysts agglomeration process was detected, however this process is slow and reversible.

Heavy oil supply economics and supply response to low oil prices

International Nuclear Information System (INIS)

Fisher, L.

1999-01-01

The dynamics of the heavy oil industry are examined, including prices, market demand, supply and supply costs. Price assumptions are provided for the reference case oil price (west Texas intermediate at Cushing). Supply cost methodology is explained. Capital and operating costs for various heavy oil and synthetic sources are derived from modeling results. The range of supply costs for heavy oil and bitumen from various sources, supply costs in terms of reference case market values and in terms of 1995-1996 average market values for Bow River crude, are derived. The CERI long term supply forecast model is explained. Western Canada upstream oil and gas cash flow and capital expenditures, eastern Canada exploration and expenditures by hydrocarbon type, and Canadian heavy oil and bitumen production based on reference case prices are estimated. Based on these projections the outlook for heavy oil at reference case prices for better than average quality resources is judged to be economic. Lower quality resources will require technology gains for successful commercialization. SAGD is a likely candidate in this respect. Again based on reference prices, production is forecast to decline by 100 Kb/d over the next five years. Diluent supply is considered to be adequate throughout the forecast period. As far as thermal bitumen is concerned, the growth could, in fact, exceed the projection, but if so, more upgrading will be required. 11 figs

Experimental optimization of catalytic process in-situ for heavy oil and bitumen upgrading

Energy Technology Data Exchange (ETDEWEB)

Shah, A.; Fishwick, R.P.; Leeke, G.A.; Wood, J. [Birmingham Univ., Birmingham (United Kingdom); Rigby, S.P.; Greaves, M. [Bath Univ., Bath (United Kingdom)

2010-07-01

Peak crude oil production is expected to occur in the second decade of this century, followed by a phase of permanent decline in conventional crude oil production. However, very large resources of heavy oil and bitumen exist throughout the world, most notably in Canada and Venezuela. The high viscosity and density of these non-conventional crude oils require more energy intensive operations for production and upgrading, and also for transportation. As such, they are more costly to extract. This paper described some of the technological innovations that are being considered to extract heavier oil supplies with reduced environmental impact. The toe-to-heel air injection (THAI) process and its catalytic added-on (CAPRI) process combine in-situ combustion with catalytic upgrading using an annular catalyst packed around a horizontal producer well. Results of an experimental study concerning optimization of catalyst type and operating conditions showed that CAPRI can effect further upgrading of partially upgraded THAI oil, with upgrading levels of viscosity and API gravity dependent upon temperature and flow rate. 20 refs., 8 tabs., 10 figs.

Speciation of Heavy Metals in Sediment of Agbabu Bitumen deposit ...

African Journals Online (AJOL)

Michael Horsfall

environmental impact assessment of bitumen exploitation on animal resources of Ode – Irele. (Lameed and Ogunsusi, 2002), compositional analysis of the oil component of the Nigerian bitumen (Oderinde and Olanipekun, 1991),. Distribution of Polycyclic Aromatic hydrocarbons in soils and water from the vicinity of Agbabu ...

Transformation of heavy gas oils derived from oil sands to petrochemical feedstock

Energy Technology Data Exchange (ETDEWEB)

Du Plessis, D.; Laureshen, C. [Alberta Energy Research Inst., Edmonton, AB (Canada)

2006-07-01

Alberta's petrochemical industry is primarily based on ethane. However, ethane could potentially impede future growth of Alberta's petrochemical industry because of increasing cost and diminishing supplies. Alternately, the rapidly growing oil sands production could provide abundant new feedstocks. Different integration schemes and technologies were evaluated in this study. Research on converting bitumen-derived heavy gas oil into petrochemical feedstock has resulted in the development of two novel technologies and process integration schemes, notably the NOVA heavy oil laboratory catalyst (NHC) process and the aromatic ring cleavage (ARORINCLE) process. This paper described progress to date on these two projects. The paper presented the experimental results for each scheme. For the ARORINCLE process, results were discussed in terms of the effect of process parameters on the hydrogenation step; effect of process parameters on the ring cleavage step; and integrating the upgrading and petrochemical complex. Early laboratory stage results of these two technologies were found to be encouraging. The authors recommended that work should progress to larger scale demonstration of the NHC and ARORINCLE technologies., 13 refs., 2 tabs., 5 figs.

Ranking oil sands bitumen recovery techniques

Energy Technology Data Exchange (ETDEWEB)

Lam, A.; Nobes, D.S.; Lipsett, M.G. [Alberta Univ., Edmonton, AB (Canada). Dept. of Mechanical Engineering

2009-07-01

The preference ranking organization method (PROMETHEE) was used to assess and rank 3 techniques for in situ bitumen recovery: (1) steam assisted gravity drainage; (2) vapour extraction (VAPEX); and (3) toe-to-heel air injection (THAI). The study used a business scenario where management-type indicators included potential production rates; estimated overall operating costs; energy consumption; facilities requirement; recovery efficiency; and energy loss. Amounts of carbon dioxide (CO{sub 2}) emissions were also considered, as well as the production depth, formation thickness, and API gravity of the produced bitumen. The study showed that THAI recovery methods had the most beneficial criteria weighting of the 3 processes, while SAGD was the least favourable choice. However, SAGD processes are the most widely used of the 3 processes, while THAI has only been demonstrated on a limited scale. It was concluded that the maturity of a technology should be weighted more heavily when using the PROMETHEE method. 8 refs., 2 tabs.

Structural Evolution of Kerogen and Bitumen during Thermal Maturation examined by Fourier-Transform Infrared Spectroscopy

Science.gov (United States)

Craddock, P. R.; Le Doan, T. V.; Pomerantz, A.

2014-12-01

Kerogen—the organic matter that is solid and insoluble in organic solvents—is a key component of organic-rich mudstones. The composition of kerogen affects the storage and transport of hydrocarbons in these unconventional resources and is known to change with thermal maturity. We report here using FTIR spectroscopy, the compositional characteristics of kerogen as a function of thermal maturity, together with the compositional characteristics of the organic phase, bitumen—the organic matter that is solid, but soluble in organic solvents. Kerogen is consumed during thermal maturation, whereas bitumen is an intermediary formed at low maturity from kerogen and consumed at higher maturities in formation of oil and gas. Bitumen relative to kerogen has higher aliphatic content, lower aromatic content, and lower abundance of oxygenated functions. At low maturity (vitrinite reflectance equivalent VRe ~ 0.5-0.9 %), the average length of aliphatic chains in bitumen increases during bitumen formation. At higher thermal maturities (VRe > 1.0-1.3 %), average aliphatic chain length decreases as bitumen is consumed. This evolution contrasts to that in kerogen, where aliphatic chain lengths shorten during all stages of maturation. Breakdown of kerogen appears to be driven by cleavage of oxygen functions at low maturity and removal of aliphatic carbons at higher maturities. These aliphatic-rich fragments may comprise the bitumen, and may in part explain the solubility of bitumen in organic solvents. Bitumen shows evidence of oxidation at low thermal maturity, a phenonemom not documented for kerogen. Bitumen maturation and degradation at higher thermal maturity is driven by cleavage and loss of aliphatic carbons, and is coincident with the maximum generation of oil and gas. The aromatic content of bitumen and of kerogen both increase during maturation as a consequence of the loss of aliphatic carbon. The oil and gas generation potential of the residual organic matter thus

Bitumen to refined products and petrochemicals : a preliminary assessment

International Nuclear Information System (INIS)

Crandall, G.

2004-01-01

Purvin and Gertz is an energy consulting firm that provides advise to the energy sector. A review of western Canadian crude oil supply suggests that oil sands production will surpass declining conventional production. Oil sands supply includes synthetic crude oil (SCO), bitumen and diluent. It is expected that oil sands will increase from 42 per cent of western supply in 2002 to 78 per cent in 2015. This presentation reviewed the potential of Alberta's oil sands and presented a recent study of refined products and petrochemicals from bitumen. Upgrading, refining and petrochemical case studies were presented. In particular, the author examined if a Canadian oil sands upgrading project with high capital costs can be competitive with competing projects in the United States and internationally. In addition to supply and demand issues, the presentation examined infrastructure capability and market potential in the United States. The economic potential and risks of preferred business cases compared to upgrading to SCO were also evaluated. tabs., figs

Preconditioning methods to improve SAGD performance in heavy oil and bitumen reservoirs with variable oil phase viscosity

Energy Technology Data Exchange (ETDEWEB)

Gates, I.D. [Gushor Inc., Calgary, AB (Canada)]|[Calgary Univ., AB (Canada). Dept. of Chemical and Petroleum Engineering; Larter, S.R.; Adams, J.J.; Snowdon, L.; Jiang, C. [Gushor Inc., Calgary, AB (Canada)]|[Calgary Univ., Calgary, AB (Canada). Dept. of Geoscience

2008-10-15

This study investigated preconditioning techniques for altering reservoir fluid properties prior to steam assisted gravity drainage (SAGD) recovery processes. Viscosity-reducing agents were distributed in mobile reservoir water. Simulations were conducted to demonstrate the method's ability to modify oil viscosity prior to steam injection. The study simulated the action of water soluble organic solvents that preferentially partitioned in the oil phase. The solvent was injected with water into the reservoir in a slow waterflood that did not displace oil from the near wellbore region. A reservoir simulation model was used to investigate the technique. Shu's correlation was used to establish a viscosity correlation for the bitumen and solvent mixtures. Solvent injection was modelled by converting the oil phase viscosity through time. Over the first 2 years, oil rates of the preconditioned case were double that of the non-preconditioned case study. However, after 11 years, the preconditioned case's rates declined below rates observed in the non-preconditioned case. The model demonstrated that oil viscosity distributions were significantly altered using the preconditioners. The majority of the most viscous oil surrounding the production well was significantly reduced. It was concluded that accelerated steam chamber growth provided faster access to lower viscosity materials at the top of the reservoir. 12 refs., 9 figs.

Biological marker distribution in coexisting kerogen, bitumen and asphaltenes in Monterey Formation diatomite, California

Science.gov (United States)

Tannenbaum, E.; Ruth, E.; Huizinga, B. J.; Kaplan, I. R.

1986-01-01

Organic-rich (18.2%) Monterey Formation diatomite from California was studied. The organic matter consist of 94% bitumen and 6% kerogen. Biological markers from the bitumen and from pyrolysates of the coexisting asphaltenes and kerogen were analyzed in order to elucidate the relationship between the various fractions of the organic matter. While 17 alpha(H), 18 alpha(H), 21 alpha(H)-28,30-bisnorhopane was present in the bitumen and in the pryolysate of the asphaltenes, it was not detected in the pyrolysates of the kerogen. A C40-isoprenoid with "head to head" linkage, however, was present in pyrolysates of both kerogen and asphaltenes, but not in the bitumen from the diatomite. The maturation level of the bitumen, based on the extent of isomerization of steranes and hopanes, was that of a mature oil, whereas the pyrolysate from the kerogen showed a considerably lower maturation level. These relationships indicate that the bitumen may not be indigenous to the diatomite and that it is a mature oil that migrated into the rock. We consider the possibility, however, that some of the 28,30-bisnorhopane-rich Monterey Formation oils have not been generated through thermal degradation of kerogen, but have been expelled from the source rock at an early stage of diagenesis.

New Insight into the Kinetics of Deep Liquid Hydrocarbon Cracking and Its Significance

Directory of Open Access Journals (Sweden)

Wenzhi Zhao

2017-01-01

Full Text Available The deep marine natural gas accumulations in China are mainly derived from the cracking of liquid hydrocarbons with different occurrence states. Besides accumulated oil in reservoir, the dispersed liquid hydrocarbon in and outside source also is important source for cracking gas generation or relayed gas generation in deep formations. In this study, nonisothermal gold tube pyrolysis and numerical calculations as well as geochemical analysis were conducted to ascertain the expulsion efficiency of source rocks and the kinetics for oil cracking. By determination of light liquid hydrocarbons and numerical calculations, it is concluded that the residual bitumen or hydrocarbons within source rocks can occupy about 50 wt.% of total oil generated at oil generation peak. This implies that considerable amounts of natural gas can be derived from residual hydrocarbon cracking and contribute significantly to the accumulation of shale gas. Based on pyrolysis experiments and kinetic calculations, we established a model for the cracking of oil and its different components. In addition, a quantitative gas generation model was also established to address the contribution of the cracking of residual oil and expulsed oil for natural gas accumulations in deep formations. These models may provide us with guidance for gas resource evaluation and future gas exploration in deep formations.

Impact of the Ageing on Viscoelastic Properties of Bitumen with the Liquid Surface Active Agent at Operating Temperatures

Science.gov (United States)

Iwański, Marek; Cholewińska, Malgorzata; Mazurek, Grzegorz

2017-10-01

The paper presents the influence of the ageing on viscoelastic properties of the bitumen at road pavement operating temperatures. The ageing process of bituminous binders causes changes in physical and mechanical properties of the bitumen. This phenomenon takes place in all stages of bituminous mixtures manufacturing, namely: mixing, storage, transport, placing. Nevertheless, during the service life it occurs the increase in stiffness of asphalt binder that is caused by the physical hardening of bitumen as well as the influence of oxidation. Therefore, it is important to identify the binder properties at a high and low operating temperatures of asphalt pavement after simulation of an ageing process. In the experiment as a reference bitumen, the polymer modified bitumen PMB 45/80-65 was used. The liquid surface active agent FA (fatty amine) was used as a bitumen viscosity-reducing modifier. It was added in the amount of 0,2%, 0,4% and 0,6% by the bitumen mass. All binder properties have been determined before ageing (NEAT) and after long-term ageing simulated by the Pressure Ageing Vessel method (PAV). To determine the binder properties at high temperatures the dynamic viscosity at 60°C was tested. On the basis of test results coming from the dynamic viscosity test it was calculated the binder hardening index. The properties at a low temperature were determined by measuring the creep modulus using Bending Beam Rheometer (BBR) at four temperatures: -10°C, -16°C, -22°C and -28°C. The stiffness creep modulus “S” and parameter “m” were determined. On the basis of dynamic viscosity test it was found that the ageing process caused a slight decrease in a dynamic viscosity. The level of a hardening index considerably increased at 0.6% fatty amine content. The long-term ageing process had a minor effect on stiffening of a polymer modified bitumen with FA additive regardless of a low temperature and an amount of fatty amine content.

Methods for producing and upgrading liquid hydrocarbons from Alberta coal. [Canada - Alberta

Energy Technology Data Exchange (ETDEWEB)

1992-01-01

Production of synthetic crude oils by co-processing coal and heavy oil or bitumen has been the subject of research efforts in Alberta since 1979. This booklet describes the treatment that is necessary for these crude oils to become suitable as feedstocks for refineries as evolved in research projects. Sections are headed: hydroprocessing of coal-based liquids; functional group analysis; isotopic studies of co-processing schemes; chemistry of coal liquefaction; co-processing process development; molecular interactions between heavy oil and coal species during co-processing; combined processing of coal, heavy oil and natural gas; and coprocessing of coal and bitumen with molten halide catalysts. 33 refs., 8 figs.

Coliquefaction of coal, tar sand bitumen and plastic (interaction among coal, bitumen and plastic); Sekitan/tar sand bitumen/plastic no kyoekika ni okeru kyozon busshitsu no eikyo

Energy Technology Data Exchange (ETDEWEB)

Yamaguchi, H.; Okuyama, Y.; Matsubara, K. [NKK Corp., Tokyo (Japan); Kamo, T.; Sato, Y. [National Institute for Resources and Environment, Tsukuba (Japan)

1996-10-28

For the improvement of economy, coliquefaction of coal, tar sand bitumen and plastic was performed under low hydrogen pressure, to investigate the influence of interaction among these on the liquefaction characteristics. For comparison, coliquefaction was also performed under the hydrogen pressure same as the NEDOL process. In addition, for clarifying its reaction mechanism, coliquefaction of dibenzyl and plastic was performed as a model experiment, to illustrate the distribution of products and composition of oil, and to discuss the interaction between dibenzyl and various plastics, and between various plastics. Under direct coal liquefaction conditions, coprocessing of Tanito Harum coal, Athabasca tar sand and plastic was carried out under low hydrogen pressure with an autoclave. The observed value of oil yield was higher than the calculated value based on the values from separate liquefaction of coal and plastic, which suggested the interaction between coal and the mixed plastic. The results of coliquefaction of coal, tar sand bitumen and plastic could be explained from the obtained oil yield and its composition by the coliquefaction of dibenzyl and plastic. 2 refs., 3 tabs.

The extraction of bitumen from western oil sands. Final report, July 1989--September 1993

Energy Technology Data Exchange (ETDEWEB)

Oblad, A.G.; Bunger, J.W.; Dahlstrom, D.A.; Deo, M.D.; Fletcher, J.V.; Hanson, F.V.; Miller, J.D.; Seader, J.D.

1994-03-01

Research and development of surface extraction and upgrading processes of western tar sands are described. Research areas included modified hot water, fluidized bed, and rotary kiln pyrolysis of tar sands for extraction of bitumen. Bitumen upgrading included solvent extraction of bitumen, and catalytic hydrotreating of bitumen. Characterization of Utah tar sand deposits is also included.

Irradiation tests on bitumen and bitumen coated materials

International Nuclear Information System (INIS)

Tabardel-Brian, R.; Rodier, J.; Lefillatre, G.

1969-01-01

The use of bitumen as a material for coating high-activity products calls for prior study of the resistance of bitumen to irradiation. After giving briefly the methods of preparation of bitumen- coated products, this report lists the equipment which has been used for carrying out the β and γ irradiations of these products, and gives the analytical results obtained as a function of the dose rates chosen and of the total integrated dose. Finally, some conclusions have been drawn concerning the best types of bitumen. It should be stressed that some bitumens apparently underwent no degradation whatsoever nor any volume increase, for a total integrated dose of 1.8 x 10 10 rads. (authors) [fr

Applicability of CO{sub 2}-based Vapex process to recover Athabasca bitumen

Energy Technology Data Exchange (ETDEWEB)

Badamchi-Zadeh, A.; Maini, B.B.; Yarranton, H.W. [Calgary Univ., AB (Canada). Dept. of Chemical and Petroleum Engineering

2008-10-15

This paper described an experimental apparatus designed to test Vapex process performance in Athabasca bitumen. The study examined the effectiveness of carbon dioxide (CO{sub 2}) as a carrier gas for propane in the Vapex process. The procedure was designed to provide data on the compositional changes in the vapor chamber and solution gas, as well as to more accurately measure the density and viscosity of produced oil. A total of 4 Vapex experiments were conducted in a model packed with glass beads and saturated with Athabasca bitumen. Pure propane, and 2 different mixtures of CO{sub 2} and propane were used as solvents. The study examined stabilized live oil production rates; average fractions of the solvent in the produced oil, the density and viscosity of the produced oil, and the average composition of the solvent in the test vapor chamber. The compositional changes were mapped using an equations of state (EOS) model. The study demonstrated that the Vapex compositional path follows a multi-contact immiscible process that included condensing compositional gravity drainage. Results indicated that while pure propane is a more effective means of recovering Athabasca bitumens, non-condensable gases such as CO{sub 2} must be mixed with propane in order to ensure that the dew point pressure of the solvent remains above reservoir pressures. The study showed that CO{sub 2} can be used to effectively reduce the viscosity of bitumen in conjunction with propane. However, the phase behavior of solvent and bitumen systems in reservoir conditions must be characterized in order to select appropriate injection gas ratios. 17 refs., 3 tabs., 12 figs.

The use of bitumen for storing radioactive waste resulting from oil industry containing Ra-226

International Nuclear Information System (INIS)

Takriti, S.; Shweikani, R.; Abdulhafiz, M.; Salman, M.

2009-12-01

The releases of radon gas from NORM waste contained in two different forms of bitumen samples have been investigated. The artificial NORM source samples were made by mixing NORM with bitumen. The sources surrounded by different thickness of bitumen layers to prepare the first form of samples. While, the NORM powder was put inside bitumen samples prepared as a cylindrical shape with different thickness. The results showed that the release of radon from the bitumen samples was different in case of sources and powder. The results illustrated that the release of radon from the bitumen samples was decrees linearly with the samples thicknesses (in both cases source and powder). On the other hand, the release from the cement samples was proportional inversely with the different thickness (for comparison). In addition, many other supporting experiments were performed, as γ-ray spectroscopy measurements showed that the cement is better than the bitumen in shielding process, while the bitumen is better than cement to prevent the releases of radon. (authors)

Characterization of industrial wastes as raw materials for Emulsified Modified Bitumen (EMB) formulation

Science.gov (United States)

Najib Razali, Mohd; Isa, Syarifah Nur Ezatie Mohd; Salehan, Noor Adilah Md; Musa, Musfafikri; Aziz, Mohd Aizudin Abd; Nour, Abdurahman Hamid; Yunus, Rosli Mohd

2018-04-01

This study was conducted to characterize industrial wastes for formulation of emulsified modified bitumen (EMB) in relation to their physical characteristic and elemental composition. This analysis will give information either raw materials from industrial wastes can be used for EMB formulation. Bitumen is produced from crude oil that is extracted from the ground which categorizes the crude oil as one of the non-renewable form of product. A vast environmental problem issues arises in Malaysia cause by the excessive manufacturing activity that lead to a miss-management of industrial waste has leads to the used of industrial waste in the EMB formulation. Industrial waste such as polystyrene, polyethylene and used automotive oil can be used as alternative to formulate bitumen. Then a suitable emulsifier needs to be added to produce the final product which is EMB. The emulsifier will yield a charge depends on its properties to bind the oily bitumen with water. Physical characteristic studies were performed by thermogravimetric Analysis (TGA), differential scanning calorimetry (DSC), flash point test, density rest and moisture content test. Fourier Transform Infrared Spectroscopy (FTIR) analysis was measured to determine the material’s molecular composition and structure.

Gas chromatograph study of bitumen from oil shale of Amman Formation (upper cretaceous), NW Jordan

International Nuclear Information System (INIS)

Darwish, H.; Mustafa, H.

1997-01-01

The extractable organic matter of seven outcrop samples of Amman Formation Oil Shale have been analysed by Gas Chromatography (GC). The bitumen is rich in heterocompounds contents (> 60 wt%). Gas chromatograms show a predominance of iosprenoids, specially phytane over n-alkanes, and low carbon preference index (CPI). This indicates that the organic matter is immature, and its origin is mainly of marine organisms. These rocks could be possible source rocks due to the high content of hydrocarbon. (authors). 22 refs., 4 figs. 3 tabs

Performance of NiWP/Al2O3 catalyst for hydroprocessing of light gas oils derived from Athabasca bitumen

Energy Technology Data Exchange (ETDEWEB)

Owusu-Boakye, A.; Ferdous, D.; Dalai, A.K. [Saskatchewan Univ., Saskatoon, SK (Canada). Dept. of Chemistry and Chemical Engineering; Adjaye, J. [Syncrude Canada Ltd., Edmonton, AB (Canada). Edmonton Research Centre

2004-07-01

The quality of diesel fuel in terms of cetane number and coloring is diminished if it has a high content of aromatics which cause the formation of undesirable emissions in exhaust gases. These compounds typically occur as mono, di, tri and polyaromatics. In response to strict environmental regulations, middle distillates now have fewer aromatics. Sulphur and nitrogen compounds in diesel fuels also cause the formation of SOx and NOx in the atmosphere, but the aromatic hydrogenation of diesel fuels is more complex than any of the hydrodesulphurization (HDS) or hydrodenitrogenation (HDN) processes. The NiWP/Al{sub 2}O{sub 3} catalyst in a trickle-bed reactor was used under a range of temperature and pressure conditions to study the reactivity of vacuum, atmospheric and hydrocracked light gas oils produced from Athabasca bitumen. The hydrogen feed ratio was kept constant and product samples from different feedstocks were analyzed with respect to sulfur, nitrogen and aromatic content. The study also included a comparison of gasoline selectivity and kinetic parameters for HDS and HDN reactions for the feed materials.

Experimental study of simultaneous Athabasca bitumen recovery and upgrading using ultradispersed catalysts injection

Energy Technology Data Exchange (ETDEWEB)

Hashemi, R.; Pereira, P. [University of Calgary (Canada)

2011-07-01

As the demand for oil is continuously increasing, the need for unconventional resources is rising. Oil extraction from bitumen and heavy oil reservoirs requires advanced techniques in order to decrease the viscosity of the oil. To increase the recovered original oil in place (OOIP) of a reservoir and decrease refining costs, new techniques to upgrade oil in situ are being developed. The current study investigates the use of ultra-dispersed (UD) submicronic catalysts to decrease oil viscosity. The experiment involved the injection of the catalyst and hydrogen gas in a sand pack saturated with Athabasca bitumen. Analysis was carried out by building recovery curves, and by comparing the oil recovery from the catalyzed process with that of catalyst-free processes. The study demonstrated that the oil recovered from the new technique had higher API gravity and lower viscosity, indicating the success of the in situ upgrading process.

Surface microstructure of bitumen characterized by atomic force microscopy.

Science.gov (United States)

Yu, Xiaokong; Burnham, Nancy A; Tao, Mingjiang

2015-04-01

Bitumen, also called asphalt binder, plays important roles in many industrial applications. It is used as the primary binding agent in asphalt concrete, as a key component in damping systems such as rubber, and as an indispensable additive in paint and ink. Consisting of a large number of hydrocarbons of different sizes and polarities, together with heteroatoms and traces of metals, bitumen displays rich surface microstructures that affect its rheological properties. This paper reviews the current understanding of bitumen's surface microstructures characterized by Atomic Force Microscopy (AFM). Microstructures of bitumen develop to different forms depending on crude oil source, thermal history, and sample preparation method. While some bitumens display surface microstructures with fine domains, flake-like domains, and dendrite structuring, 'bee-structures' with wavy patterns several micrometers in diameter and tens of nanometers in height are commonly seen in other binders. Controversy exists regarding the chemical origin of the 'bee-structures', which has been related to the asphaltene fraction, the metal content, or the crystallizing waxes in bitumen. The rich chemistry of bitumen can result in complicated intermolecular associations such as coprecipitation of wax and metalloporphyrins in asphaltenes. Therefore, it is the molecular interactions among the different chemical components in bitumen, rather than a single chemical fraction, that are responsible for the evolution of bitumen's diverse microstructures, including the 'bee-structures'. Mechanisms such as curvature elasticity and surface wrinkling that explain the rippled structures observed in polymer crystals might be responsible for the formation of 'bee-structures' in bitumen. Despite the progress made on morphological characterization of bitumen using AFM, the fundamental question whether the microstructures observed on bitumen surfaces represent its bulk structure remains to be addressed. In addition

Decreasing polycyclic aromatic hydrocarbons emission from bitumen using alternative bitumen production process

International Nuclear Information System (INIS)

Rasoulzadeh, Y.; Mortazavi, S.B.; Yousefi, A.A.; Khavanin, A.

2011-01-01

In 1988, the National Institute for Occupational Safety and Health (NIOSH) recommended that bitumen fumes should also be considered a potential occupational carcinogen and management practices such as engineering controls should be implemented. Changing the production process of bitumen, as a source control method, was investigated in our study. For the first time, a novel alternative process was used to produce paving grade bitumen with decreased PAH emissions as well as improved bitumen performance grade (PG). Post-consumer latex and natural bitumen (NB) were used as additives to obtain 60/70 modified bitumen directly from the vacuum bottom (VB) without any need for air-blowing. The emissions were produced by a laboratory fume generation rig and were sampled and analyzed by GC-Mass and GC-FID as described in NIOSH method 5515. The PG of the resulting modified 60/70 bitumen in this study covers a wider range of climatic conditions and has higher total resistance against deformation than conventional 60/70 bitumen. The total PAH emissions from modified 60/70 bitumen (100.2619 ng/g) were decreased approximately to 50% of PAHs emitted from conventional 60/70 bitumen (197.696 ng/g). Therefore, it is possible to obtain modified bitumen with lower PAH emissions and better quality than conventional bitumen via additives and without air-blowing.

Bituminization process of radioactive liquid wastes by domestic bitumen

International Nuclear Information System (INIS)

Sang, H.L.

1977-11-01

A study has been carried out of the incorporation of intermediate level wastes in bitumen. Two kinds of wastes: a) an evaporator concentrate from a PWR (containing boric acid), b) second cycle wastes from the Purex process (containing sodium salts), were satisfactorily incorporated into a mixture of straight and blown domestic bitumen, to yield a product containing 50wt% solids. The products were stable to radiation exposure of 5'8x10 8 rads. Leach rates were measured in both distilled and sea water over periods up to 200 days at 5 0 C and 25 0 C and at both 1 atm and 8 atm pressure. Results confirmed that long term storage of the products would be satisfactory

Design and optimization of hybrid ex situ/in situ steam generation recovery processes for heavy oil and bitumen

Energy Technology Data Exchange (ETDEWEB)

Yang, X.; Gates, I.D. [Calgary Univ., AB (Canada). Dept. of Chemical and Petroleum Engineering; Larter, S.R. [Calgary Univ., AB (Canada). Dept. of Geoscience]|[Alberta Ingenuity Centre for In Situ Energy, Edmonton, AB (Canada)

2008-10-15

Hybrid steam-air based oil recovery techniques were investigated using advanced 3-D reactive thermal reservoir simulations. The hybrid techniques combined ex situ steam and in situ steam generation processes in order to raise efficiency, lower natural gas consumption, and reduce gas emissions. The steam-air based processes used 70 per cent of the energy of conventional steam assisted gravity drainage (SAGD) techniques to recover the same amount of oil. The process used an SAGD wellpair arrangement, where steam and air were injected through the top injection well. The kinetic parameters used in the study were developed by history matching a combustion tube experiments with Athabasca bitumen conducted to predict cumulative bitumen and gas production volumes and compositions. A total of 6 SAGD and 6 in situ combustion simulations were conducted with steam oxygen volume ratios set at 50 per cent steam and 50 per cent oxygen. Various case studies were considered over a 5 year period. Carbon dioxide (CO{sub 2}) emissions were also measured as well as cumulative water and methane consumption rates. Results of the study were used to develop an optimized hybrid operation that consisted of a SAGD well pair arrangement operating with cyclic steam-oxygen injection at high pressures. It was concluded that the high pressure operation increased the steam partial pressure within the reservoir and enhanced combustion performance. A 29 per cent improvement in the cumulative energy to oil ratio was obtained. 23 refs., 2 tabs., 9 figs.

Process of recovering bitumen from shale

Energy Technology Data Exchange (ETDEWEB)

Ryan, H D

1918-03-26

A step in the recovery of bitumen from solids which consists in digesting the solids with heavy oil under the action of heat and agitation at a temperature insufficiently high to effect substantial distillation of heavy fractions, but high enough to liquefy heavy hydrocarbons contained in the solids, and then separating solid residual matter, substantially as described.

Diluent and bitumen, an uneasy mix : considerations for treating, blending, transportation, marketing and refining

Energy Technology Data Exchange (ETDEWEB)

Todd, C. [Connacher Oil and Gas Ltd., Calgary, AB (Canada)

2009-07-01

This presentation evaluated several issues regarding the use of diluent as a blending agent with Canadian bitumen. Heavy and viscous crude oils are commonly diluted with condensates and gasolines. This improves field processing, transportability in pipelines and acceptability in markets and refineries. The demand for such diluent is increasing because of the large amounts of heavy oil and bitumen currently produced in Canada. The current tenable price of diluents has meant that a wide range of diluent sources and components are finding their way into the Canadian diluent supply stream. This has raised concerns regarding diluent performance and the affect on blended crude oils. The cost of diluent is among the most controllable expense associated with most bitumen production projects. Market factors were considered in this presentation, such as supply demand; price and infrastructure; operational processing and blending issues; diluent quality and component variability; and downstream issues such as refinery processing and production. tabs., figs.

The composition of acids in bitumen and in products from saponification of kerogen: Investigation of their role as connecting kerogen and mineral matrix

Energy Technology Data Exchange (ETDEWEB)

Razvigorova, M.; Budinova, T.; Tsyntsarski, B.; Petrova, B. [Bulgarian Academy of Sciences, Institute of Organic Chemistry, 1113 Sofia, Acad. Bonchev Str., bl. 9 (Bulgaria); Ekinci, E. [ISIK University, Kumbaba Mevkii, 34980 Istanbul (Turkey); Atakul, H. [Istanbul Technical University, Department of Chemical Engineering, Maslak, 34469 Istanbul (Turkey)

2008-11-03

In order to obtain more information and to understand the nature of relation between organic and mineral matter in oil shales, the compositions of soluble bitumen fractions obtained by extraction from Bulgarian oil shales before and after demineralization with 10% HCl, concentrated HF, and a HF/HCl mixture were investigated. The four extracts were quantitatively examined by IR and {sup 1}H NMR spectroscopy. The investigation of isolated acidic material of the bitumen fractions showed that the fatty acids are present in bitumen fractions as free acids, esters and salts. The amount of free acids in bitumen is very small. The dominant part of bitumen acids is associated with mineral components of the oil shales as well as part of them is included in the mineral matrix, and can be separated only after deep demineralization. The kerogen of the oil shales, obtained after separation of the bitumen fractions and mineral components, was subjected to saponification in order to determine the amount of acids, bound as esters to the kerogen matrix. The major components found were n-carboxylic, {alpha},{omega}-di-carboxylic, and aromatic acids. The connection of kerogen with mineral components is accomplished by the participation of carboxylic and complicated ester bonds. Experimental data for the composition of bitumen acids give evidence that algae and terrestrial materials are initial sources in the formation of soluble organic matter of Bulgarian oil shale. (author)

Use and trade of bitumen in antiquity and prehistory: molecular archaeology reveals secrets of past civilizations

Science.gov (United States)

Connan, J.

1999-01-01

Natural asphalt (or bitumen) deposits, oil seepage and liquid oil shows are widespread in the Middle East, especially in the Zagros mountains of Iran. Ancient people from northern Iraq, south-west Iran and the Dead Sea area extensively used this ubiquitous natural resource until the Neolithic period (7000 to 6000 BC). Evidence of earlier use has been recently documented in the Syrian desert near El Kown, where bitumen-coated flint implements, dated to 40,000 BC (Mousterian period), have been unearthed. This discovery at least proves that bitumen was used by Neanderthal populations as hafting material to fix handles to their flint tools. Numerous testimonies, proving the importance of this petroleum-based material in Ancient civilizations, were brought to light by the excavations conducted in the Near East as of the beginning of the century. Bitumen remains show a wide range of uses that can be classified under several headings. First of all, bitumen was largely used in Mesopotamia and Elam as mortar in the construction of palaces (e.g. the Darius Palace in Susa), temples, ziggurats (e.g. the so-called 'Tower of Babel' in Babylon), terraces (e.g. the famous 'Hanging Gardens of Babylon') and exceptionally for roadway coating (e.g. the processional way of Babylon). Since the Neolithic, bitumen served to waterproof containers (baskets, earthenware jars, storage pits), wooden posts, palace grounds (e.g. in Mari and Haradum), reserves of lustral waters, bathrooms, palm roofs, etc. Mats, sarcophagi, coffins and jars, used for funeral practices, were often covered and sealed with bitumen. Reed and wood boats were also caulked with bitumen. Abundant lumps of bituminous mixtures used for that particular purpose have been found in storage rooms of houses at Ra's al-Junayz in Oman. Bitumen was also a widespread adhesive in antiquity and served to repair broken ceramics, fix eyes and horns on statues (e.g. at Tell al-Ubaid around 2500 BC). Beautiful decorations with stones

Comparison of P-containing {gamma}-Al{sub 2}O{sub 3} supported Ni-Mo bimetallic carbide, nitride and sulfide catalysts for HDN and HDS of gas oils derived from Athabasca bitumen

Energy Technology Data Exchange (ETDEWEB)

Sundaramurthy, V.; Dalai, A.K. [Catalysis and Chemical Reaction Engineering Laboratories, Department of Chemical Engineering, University of Saskatchewan, Saskatoon, SK (Canada); Adjaye, J. [Syncrude Edmonton Research Centre, Edmonton, AB (Canada)

2006-09-01

Phosphorus containing {gamma}-Al{sub 2}O{sub 3} supported bimetallic Ni-Mo carbide, nitride and sulfide catalysts have been synthesized from an oxide precursor containing 12.73wt.% Mo, 2.54wt.% Ni and 2.38wt.% P and characterized by elemental analysis, pulsed CO chemisorption, surface area measurements, X-ray diffraction, temperature-programmed reduction and DRIFT spectroscopy of CO adsorption. DRIFT spectroscopy of adsorbed CO on activated catalysts showed that carbide and nitride catalysts have surface exposed sites of Mo{sup o+} (0oil and heavy gas oil derived from Athabasca bitumen in the temperature range 340-370 and 375-400{sup o}C respectively at 8.8MPa. The gradual transformation of Ni-Mo carbide and nitride phases into Ni-Mo sulfide phases was observed during precoking period, and the formed Ni-Mo sulfide phases enhanced the HDN and HDS activities of carbide and nitride catalysts. The {gamma}-Al{sub 2}O{sub 3} supported Ni-Mo bimetallic sulfide catalyst was found to be more active for HDN and HDS of light gas oil and heavy gas oil than the corresponding carbide and nitride catalysts on the basis of unit weight. (author)

Chinese refining capacity for Canadian heavy oil

International Nuclear Information System (INIS)

Bruce, G.W.

2006-01-01

This paper discussed China's refining capacity in relation to exports of Canadian heavy oil. Demand for oil is increasing throughout the world, and China is expected to consume 25 per cent of the projected yearly oil supplies. Alberta currently has an estimated 174 billion barrels of recoverable bitumen, and produces 1.06 million barrels per day. Production is expected to increase to 4.5 million barrels per day by the year 2020. Currently bitumen blends are refined and diluted with naphtha and sweet synthetic crude oil. Bitumen is a challenging feedstock for refineries, and requires thermal production methods or gasification processes. Primary conversion into sour synthetic crude is typically followed by hydrocracking and further refining into finished petroleum products. There are currently 50 refineries in China with a 7.4 million barrel per day capacity. Coastal refineries using imported crude oil have a 4 million barrel per day capacity. New facilities are being constructed and existing plants are being upgraded in order to process heavier and more sour crude oils. However, current refining capabilities in Chinese refineries have a limited ability for resid conversion. It was concluded that while China has a refining infrastructure, only refineries on the coast will use oil sands-derived feedstocks. However, there are currently opportunities to design refineries to match future feedstocks. tabs., figs

Effect of Recycled Waste Polymers, Natural Bitumen and HVS Cut on the Properties of Vacuum Bottom

Directory of Open Access Journals (Sweden)

Y. Rasoulzadeh

2013-01-01

Full Text Available The neat bitumen, an oil refining by-product, has its own inherent weakness under long-time loading at low and high temperatures. These performance limitations of neat bitumen have led researchers to modify its physical andmechanical properties. According to several studies, polymers can be used to modify the properties of bitumen. Due to much lower production costs and aiming to reduce environmental impacts, recycled waste polymers are preferred as compared with virgin polymers. In this study, the effect of recycled waste polymers including crumb rubber modifier (CRM, polyethylene and latex and non-polymeric materials such as natural bitumen (NB and heavy vacuum slops (HVS cut on physical and mechanical properties of vacuum bottom residue (VB of crude oil distillation was investigat-ed. Based on the results, recycled waste polyethylene and NB can improve the performance grade of VB at high temperatures and CRM, latex and HVS can improve the performance grade of VB at low temperatures. Thus, by designing various blends of these additives with VB, different modified bitumens can be directly obtained from VB without any need to air-blowing process.

Catalytic conversion of carboxylic acids in bio-oil for liquid hydrocarbons production

International Nuclear Information System (INIS)

Wang, Shurong; Guo, Zuogang; Cai, Qinjie; Guo, Long

2012-01-01

Bio-oil must be upgraded to be suitable for use as a high-grade transport fuel. Crude bio-oil has a high content of carboxylic acids which can cause corrosion, and the high oxygen content of these acids also reduces the oil’s heating value. In this paper, acetic acid and propanoic acid were chosen as the model carboxylic acids in bio-oil. Their behavior in the production of liquid hydrocarbons during a catalytic conversion process was investigated in a micro-fixed bed reactor. The liquid organic phase from this catalytic conversion process mainly consisted of liquid hydrocarbons and phenol derivatives. Under the condition of low Liquid Hourly Space Velocity (LHSV), the liquid organic phase from acetic acid cracking had a selectivity of 22% for liquid hydrocarbons and a selectivity of 65% for phenol derivatives. The composition of the organic products changed considerably with the LHSV increasing to 3 h −1 . The selectivity for liquid hydrocarbons increased up to 52% while that for phenol derivatives decreased to 32%. Propanoic acid performed much better in producing liquid hydrocarbons than acetic acid. Its selectivity for liquid hydrocarbons was as high as 80% at LHSV = 3 h −1 . A mechanism for this catalytic conversion process was proposed according to the analysis of the components in the liquid organic phases. The pathways of the main compounds formation in the liquid organic phases were proposed, and the reason why liquid hydrocarbons were more effectively produced when using propanoic acid rather than acetic acid was also successfully explained. In addition, BET and SEM characterization were used to analyze the catalyst coke deposition. -- Graphical abstract: Display Omitted Highlights: ► High content of carboxylic acids in bio-oil causes its corrosiveness. ► Acetic acid and propanoic acid are two dominant acids in bio-oil. ► Liquid hydrocarbons were produced by cracking of these two dominant acids. ► A mechanism model was proposed to explain

Effect of nitrogen and phosphate limitation on utilization of bitumen ...

African Journals Online (AJOL)

The degradation of bitumen was found to be associated with the production of carbon (IV) oxide, natural gas and oil. As a result of using nitrogen limited and phosphate limited media, 1750 and 1250 cm3 of gas and 0.95 and 0.85 g/l of oil were obtained respectively. Nitrogen and phosphate limitation have profound effect on ...

Effect of nitrogen and phosphate limitation on utilization of bitumen ...

African Journals Online (AJOL)

PRECIOUS

2009-12-15

Dec 15, 2009 ... utilization of bitumen and production of bitu-oil and gas by a bacterial ... nitrogen and phosphorus, with a consequent limitation on degradation of the ..... concluded that in industrial setting, carbon starvation in anaerobic ...

Effect of processing temperature on the bitumen/MDI-PEG reactivity

Energy Technology Data Exchange (ETDEWEB)

Martin-Alfonso, M.J.; Partal, P.; Navarro, F.J.; Garcia-Morales, M. [Departamento de Ingenieria Quimica, Facultad de Ciencias Experimentales, Campus de ' El Carmen' , Universidad de Huelva, 21071, Huelva (Spain); Bordado, J.C.M. [Chemical and Biological Engineering Department, IBB, Instituto Superior Tecnico, Av. Rovisco Pais 1049-001 Lisbon (Portugal); Diogo, A.C. [Materials Engineering Department, Instituto Superior Tecnico, Av. Rovisco Pais 1049-001 Lisbon (Portugal)

2009-04-15

Reactive polymers are lately gaining acceptance to give added value to a residue of the crude oil refining process such as bitumen. The resulting material should display enhanced mechanical properties to be considered for advanced applications in construction. In the present paper, we report the effect of processing temperature on the reaction between bitumen compounds and an isocyanate-based reactive polymer, synthesized by reaction of polymeric MDI (4,4'-diphenylmethane diisocyanate) with a low molecular weight polyethylene-glycol (PEG). Rheokinetics experiments, viscosity measurements at 60 C, atomic force microscopy (AFM) characterization, thin layer chromatography (TLC-FID) analysis and thermogravimetric studies (TGA) were performed on the reactive polymer and on samples of MDI-PEG modified bitumen containing 2 wt.% of the polymer. Results showed the existence of an optimum processing temperature arisen as a consequence of opposite effects: microstructural availability for the formation of a polymer-bitumen network, reaction ability and polymer thermal degradation. Consequently, this study aims to serve as a guideline for the refining and asphalt industries facing the stage of selecting the optimum processing parameters. (author)

Catalytic cracking of the top phase fraction of bio-oil into upgraded liquid oil

International Nuclear Information System (INIS)

Sunarno; Rochmadi,; Mulyono, Panut; Budiman, Arief

2016-01-01

The energy consumption is increasing, while oil reserves as a primary energy resource are decreasing, so that is the reason seeking alternative energy source is inevitable. Biomass especially oil palm empty fruit bunches (EFB) which is abundant in Indonesia can be processed into bio-oil by pyrolysis process. The potential for direct substitution of bio-oil for petroleum may be limited due to the high viscosity, high oxygen content, low heating value, and corrosiveness. Consequently, upgrading of the bio-oil before use is inevitable to give a wider variety of applications of its liquid product. Furthermore, upgrading process to improve the quality of bio-oil by reduction of oxygenates involves process such as catalytic cracking. The objective of this research is to study the effect of operation temperature on yield and composition of upgraded liquid oil and to determine physical properties. Bio-oil derived from EFB was upgraded through catalytic cracking using series tubular reactor under atmospheric pressure on a silica-alumina catalyst. Results show that increasing temperature from 450 to 600 °C, resulting in decreasing of upgraded liquid oil (ULO) yield, decreasing viscosity and density of ULO, but increasing in calorimetric value of ULO. The increasing temperature of cracking also will increase the concentration of gasoline and kerosene in ULO.

Catalytic cracking of the top phase fraction of bio-oil into upgraded liquid oil

Energy Technology Data Exchange (ETDEWEB)

Sunarno [Chemical Engineering Department, Riau University, Kampus Binawidya KM 12,5 Pekanbaru 28293 (Indonesia); Chemical Engineering Department, Gadjah Mada University, Jalan Grafika No. 2 Bulaksumur,Yogyakarta 55281 (Indonesia); Rochmadi,; Mulyono, Panut [Chemical Engineering Department, Gadjah Mada University, Jalan Grafika No. 2 Bulaksumur,Yogyakarta 55281 (Indonesia); Budiman, Arief, E-mail: abudiman@ugm.ac.id [Chemical Engineering Department, Gadjah Mada University, Jalan Grafika No. 2 Bulaksumur,Yogyakarta 55281(Indonesia); Center for Energy Studies, Gadjah Mada University, Sekip K1A, Yogyakarta 55281 (Indonesia)

2016-06-03

The energy consumption is increasing, while oil reserves as a primary energy resource are decreasing, so that is the reason seeking alternative energy source is inevitable. Biomass especially oil palm empty fruit bunches (EFB) which is abundant in Indonesia can be processed into bio-oil by pyrolysis process. The potential for direct substitution of bio-oil for petroleum may be limited due to the high viscosity, high oxygen content, low heating value, and corrosiveness. Consequently, upgrading of the bio-oil before use is inevitable to give a wider variety of applications of its liquid product. Furthermore, upgrading process to improve the quality of bio-oil by reduction of oxygenates involves process such as catalytic cracking. The objective of this research is to study the effect of operation temperature on yield and composition of upgraded liquid oil and to determine physical properties. Bio-oil derived from EFB was upgraded through catalytic cracking using series tubular reactor under atmospheric pressure on a silica-alumina catalyst. Results show that increasing temperature from 450 to 600 °C, resulting in decreasing of upgraded liquid oil (ULO) yield, decreasing viscosity and density of ULO, but increasing in calorimetric value of ULO. The increasing temperature of cracking also will increase the concentration of gasoline and kerosene in ULO.

Study on possible explosive reactions of sodium nitrate-bitumen mixtures initiated by a shock wave

International Nuclear Information System (INIS)

Savornin, J.; Vasseur, C.

1986-01-01

Potential hazards of the mixture sodium nitrate-bitumen obtained by embedding in bitumen liquid radioactive effluents concentrated by evaporation are studied in case of accidental shock wave. A theoretical evaluation based on thermodynamical data show a low probability, nevertheless different from zero. No explosion occurred in tests realized in severe conditions. In conclusion there is no risk of detonation of large quantity of bitumen-nitrates stored in 200-liter drum in radioactive waste storage [fr

[Imperial Oil's Cold Lake oil sands operations

International Nuclear Information System (INIS)

Dingle, H. B.

1999-01-01

Imperial Oil Limited's Cold Lake oil sands resources, production and operations in Alberta are discussed. Cold Lake is the company's largest single asset and its largest source of crude oil production. In 1998, Cold Lake accounted for just under half of Imperial's total liquid production, averaging more than 135,000 barrels of bitumen a day. Despite the very difficult operating conditions experienced by the oil sands industry in 1998, Imperial Oil's Cold Lake operations generated a positive cash flow and earnings. Just as important, the near and long-term potential of Cold Lake property continues to be strong, even with the tough market conditions today and the foreseeable future. Proved reserves at the end of 1997 were 1.3 billions barrels, equal to about 24 years of current production, but even more important is Imperial's resource base in the Athabasca region, which represents 150 years of production at current rates. Although production forecasts for the near future are are revised downward because of production shut-in due to low prices, the company is confident of its long-term prospects mainly because of existing infrastructure, superior reservoir quality, 30 years worth of operating improvements and established bitumen-blend markets. Details of the company's future Cold Lake development plans are discussed. The need to continue technology development, which has been at the core of the industry's growth in the past and will continue to be the key to the future, are emphasized

Waste reduction algorithm used as the case study of simulated bitumen production process

Directory of Open Access Journals (Sweden)

Savić Marina A.

2011-01-01

Full Text Available Waste reduction algorithm - WAR is a tool helping process engineers for environmental impact assessment. WAR algorithm is a methodology for determining the potential environmental impact (PEI of a chemical process. In particular, the bitumen production process was analyzed following three stages: a atmospheric distillation unit, b vacuum distillation unit, and c bitumen production unit. Study was developed for the middle sized oil refinery with capacity of 5000000 tones of crude oil per year. Results highlight the most vulnerable aspects of the environmental pollution that arise during the manufacturing process of bitumen. The overall rates of PEI leaving the system (PEI/h - Iout PEI/h are: a 2.14105, b 7.17104 and c 2.36103, respectively. The overall rates of PEI generated within the system - Igen PEI/h are: a 7.75104, b -4.31104 and c -4.32102, respectively. Atmospheric distillation unit have the highest overall rate of PEI while the bitumen production unit have the lowest overall rate of PEI. Comparison of Iout PEI/h and Igen PEI/h values for the atmospheric distillation unit, shows that the overall rate of PEI generated in the system is 36.21% of the overall rate of PEI leaving the system. In the cases of vacuum distillation and bitumen production units, the overall rate of PEI generated in system have negative values, i.e. the overall rate of PEI leaving the system is reduced at 60.11% (in the vacuum distillation unit and at 18.30% (in the bitumen production unit. Analysis of the obtained results for the overall rate of PEI, expressed by weight of the product, confirms conclusions.

Hydrogen production from wind energy in Western Canada for upgrading bitumen from oil sands

International Nuclear Information System (INIS)

Olateju, Babatunde; Kumar, Amit

2011-01-01

Hydrogen is produced via steam methane reforming (SMR) for bitumen upgrading which results in significant greenhouse gas (GHG) emissions. Wind energy based hydrogen can reduce the GHG footprint of the bitumen upgrading industry. This paper is aimed at developing a detailed data-intensive techno-economic model for assessment of hydrogen production from wind energy via the electrolysis of water. The proposed wind/hydrogen plant is based on an expansion of an existing wind farm with unit wind turbine size of 1.8 MW and with a dual functionality of hydrogen production and electricity generation. An electrolyser size of 240 kW (50 Nm 3 H 2 /h) and 360 kW (90 Nm 3 H 2 /h) proved to be the optimal sizes for constant and variable flow rate electrolysers, respectively. The electrolyser sizes aforementioned yielded a minimum hydrogen production price at base case conditions of $10.15/kg H 2 and $7.55/kg H 2 . The inclusion of a Feed-in-Tariff (FIT) of $0.13/kWh renders the production price of hydrogen equal to SMR i.e. $0.96/kg H 2, with an internal rate of return (IRR) of 24%. The minimum hydrogen delivery cost was $4.96/kg H 2 at base case conditions. The life cycle CO 2 emissions is 6.35 kg CO 2 /kg H 2 including hydrogen delivery to the upgrader via compressed gas trucks. -- Highlights: ► This study involves development of a data intensive techno-economic model for estimation cost of hydrogen production from wind energy. ► Wind energy based electricity is used for electrolysis to produce hydrogen in Western Canada for bitumen upgrading for oil sands. ► Several scenarios were developed to study the electricity generation and hydrogen production from wind energy. ► The cost of production of hydrogen is significantly higher than natural based hydrogen in Western Canada.

Understanding the relationship : bitumen production and the Athabasca River

Energy Technology Data Exchange (ETDEWEB)

Daughney, S. [Hatch Ltd., Mississauga, ON (Canada)

2009-07-01

This presentation discussed oil sands activities in relation to water use and the Athabasca River. Surface mining uses truck and shovel methods to extract shallow oil sands deposits comprised of bitumen, connate water, coarse sands, and clays. The process involves the use of significant amounts of fresh water. The bitumens are slurried at turbulent conditions in a hydrotransport line which directs the bitumens towards a froth treatment process and diverts coarse sand and fine tailings. The tailings are stored in ponds or used to construct dykes. Water trapped with tailings materials cannot be recycled, and must be replaced from fresh sources. Various consolidate and non-consolidated tailings strategies are being developed to address mature fine tailings (MFT) accumulations. Generic water balance analyses are conducted in order to determine the distribution of site water inputs and losses as well as to determine river water use intensity. A water management framework and tailings performance criteria has been developed for the lower Athabasca River. The framework has been designed to determine cautionary thresholds for the river. River water withdrawals are cumulative for all industries. Intakes may be restricted by 2012. Water from storage must be used to supplement available flow from the river. It was concluded that strategies must also be developed to meet tailings disposal requirements. tabs., figs.

Preliminary organic geochemical investigation of the Kimmeridgian oil shales. [United Kingdom

Energy Technology Data Exchange (ETDEWEB)

Williams, P F.V.; Douglas, A G

1980-01-01

The Kimmeridge oil shales have assumed renewed significance because of their role as the prime source-rock for North Sea oil, and because of the need to assess their potential as a possible future supply of shale oil. This paper presents the results of a preliminary investigation of selected Kimmeridge oil shales. The immature shales are rich in organic matter with a dominantly marine type II kerogen showing evidence of algal contributions and a general sparsity of land-derived, higher plant detritus. Column chromatographic and capillary column gas chromatographic examinations of bitumens, pyrolysates and pyrolysis gas chromatograms of kerogen isolates show a predominance of aromatics in the hydrocarbon fractions, with bitumen n-alkane gas chromatograms showing evidence of algal-derived organic matter with n-alkane maxima in the n-C/sub 17/ region. Possible contributions from lower land plants are indicated by a second n-alkane maximum at n-C/sub 23/, whilst higher land plant detritus makes only a limited contribution. Reflected light microscopic examination of the shales also shows a general sparsity of recognizable land-derived woody or herbaceous material. Shale oil compositions reflect their pyrolytic origin, with unsaturates forming a large part of the aliphatic hydrocarbon fraction, together with significant amounts of isoprenoid alkanes; organic sulphur compounds are also prominent in the hydrocarbon fractions. Finally, considerable amounts of sterane and pentacyclic triterpane hydrocarbons have been found in the bitumen aliphatic hydrocarbon fractions, their distributions allowing Blackstone samples to be differentiated from those of lower stratigraphic levels.

Shale-oil-derived additives for fuel oils

International Nuclear Information System (INIS)

Raidma, E.; Leetsman, L.; Muoni, R.; Soone, Y.; Zhiryakov, Y.

2002-01-01

Studies have shown that the oxidation, wearing, and anticorrosive properties of shale oil as an additive to liquid fuels and oils enable to improve the conditions of their use. Studies conducted by Institute of Oil Shale have shown that it is possible, on the basis of shale oil produced by Viru Keemia Grupp AS (Viru Chemistry Group Ltd.) and, particularly, on the basis of its fractions 230-320 and 320-360 deg C to produce efficient and stable additives for liquid fuels to improve their combustion and storage properties. In the production of additives from shale oil the prerequisite taken into account is its complexity of composition and high concentration of neutral and phenolic oxygen compounds. Additives produced from shale oil have multifunctional properties which enable to improve operational data of liquid fuels and to increase the power of diesel engines and boilers. (author)

Decision 99-8 : Shell Canada Limited application to construct and operate an oil sands bitumen upgrader in the Fort Saskatchewan area : Shell Canada Products Limited application to amend refinery approval in the Fort Saskatchewan area

International Nuclear Information System (INIS)

1999-01-01

The Alberta Energy and Utilities Board considered an application by Shell Canada Limited to construct and operate an oil sands bitumen upgrader on Shell's property adjoining the existing Scotford refinery in the County of Strathcona. The upgrader would process bitumen from Shell's proposed Muskeg River Mine, located 70 km north of Fort McMurray, and other feedstocks available in the area. The Board also considered an application for an amendment to the existing Scotford refinery approval, Industrial Development Permit 89-10, for the processing of 3.75 million cubic metres per year of sour conversion feedstock. Under a coordinated application process, Shell filed a joint Shell Scotford Upgrader application/Environmental Impact Assessment. Issues considered with respect to these applications were: technology selection, air/health, sulphur recovery, noise/traffic, and land use conflict. Shell stated that its Scotford refinery is the most energy efficient refinery in the Americas and that is has the highest liquid yield per unit volume of crude oil feedstock of any refinery in the world. The refinery's hydrocracking capacity would make it possible to use hydro-conversion technology for its upgrader which is environmentally advantageous. After examining all of the evidence pertaining to the applications, the Board found the projects to be in the public interest and is prepared to approve the Scotford Upgrader and Scotford Refinery modifications assuming that certain prescribed conditions are met

Ecotoxicological impacts of effluents generated by oil sands bitumen extraction and oil sands lixiviation on Pseudokirchneriella subcapitata

Energy Technology Data Exchange (ETDEWEB)

Debenest, T., E-mail: tdebenest@yahoo.fr [Environment Canada, Fluvial Ecosystem Research, 105 McGill Street, 7 floor, Montreal, Quebec, H2Y 2E7 (Canada); Turcotte, P. [Environment Canada, Fluvial Ecosystem Research, 105 McGill Street, 7 floor, Montreal, Quebec, H2Y 2E7 (Canada); Gagne, F., E-mail: francois.gagne@ec.gc.ca [Environment Canada, Fluvial Ecosystem Research, 105 McGill Street, 7 floor, Montreal, Quebec, H2Y 2E7 (Canada); Gagnon, C.; Blaise, C. [Environment Canada, Fluvial Ecosystem Research, 105 McGill Street, 7 floor, Montreal, Quebec, H2Y 2E7 (Canada)

2012-05-15

The exploitation of Athabasca oil sands deposits in northern Alberta has known an intense development in recent years. This development has raised concern about the ecotoxicological risk of such industrial activities adjacent to the Athabasca River. Indeed, bitumen extraction generated large amounts of oil sands process-affected water (OSPW) which are discharged in tailing ponds in the Athabasca River watershed. This study sought to evaluate and compare the toxicity of OSPW and oil sands lixiviate water (OSLW) with a baseline (oil sands exposed to water; OSW) on a microalgae, Pseudokirchneriella subcapitata, at different concentrations (1.9, 5.5, 12.25, 25 and 37.5%, v/v). Chemical analyses of water-soluble contaminants showed that OSPW and OSLW were enriched in different elements such as vanadium (enrichment factor, EF = 66 and 12, respectively), aluminum (EF = 64 and 15, respectively), iron (EF = 52.5 and 17.1, respectively) and chromium (39 and 10, respectively). The toxicity of OSPW on cells with optimal intracellular esterase activity and chlorophyll autofluorescence (viable cells) (72 h-IC 50% < 1.9%) was 20 times higher than the one of OSW (72 h-IC 50% > 37.5%, v/v). OSLW was 4.4 times less toxic (IC 50% = 8.5%, v/v) than OSPW and 4.5 times more toxic than OSW. The inhibition of viable cell growth was significantly and highly correlated (<-0.7) with the increase of arsenic, beryllium, chromium, copper, lead, molybdenum and vanadium concentrations. The specific photosynthetic responses studied with JIP-test (rapid and polyphasic chlorophyll a fluorescence emission) showed a stimulation of the different functional parameters (efficiency of PSII to absorb energy from photons, size of effective PSII antenna and vitality of photosynthetic apparatus for energy conversion) in cultures exposed to OSPW and OSLW. To our knowledge, our study highlights the first evidence of physiological effects of OSPW and OSLW on microalgae.

A bitumen compound for pavements

Energy Technology Data Exchange (ETDEWEB)

Kanadzava, K.; Simagata, R.

1982-08-17

A bitumen compound is proposed which is produced through addition of finely ground coal ash to a bituminous material and subsequent homogenization of the mixture. The following may be used as the bituminous material: solid petroleum bitumen (a penetration of 10 to 150), soft petroleum bitumen (a penetration of 150 to 500), a semioxidized bitumen, a mixture of semioxidized and directly distilled bitumen, bitumen diluted by a petroleum distillate, bituminous mixtures which include rubber, tar, synthetic resins and so on. It is best to use wastes from central thermal electric power plants (TETs), which operate on coal, with a great content of oxides of aluminum, iron and calcium, as the coal ash. The ash is added to the bitumen in a volume of 10 to 40 percent. The compound may include a surfactant (PAV), dispersers, additives which increase the stability to layering and others. The compound is marked by increased resistance to softening in the summer, reduced brittleness at low temperatures and good adhesion to a filler.

Methods for producing and upgrading liquid hydrocarbons from Alberta coal

Energy Technology Data Exchange (ETDEWEB)

1992-01-01

This publication describes a number of research projects into hydrotreating, the treatment necessary for synthetic crude oils to become suitable as feedstocks for refineries. The projects include the hydroprocessing of coal-based liquids, functional group analysis, isotopic studies of co-processing schemes, and co-processing coal and bitumen with molten halide catalysts.

The impact of energy derivatives on the crude oil market

Energy Technology Data Exchange (ETDEWEB)

Fleming, J.; Ostdiek, B. [Jones Graduate School of Management, Rice University, MS 531, P.O. Box 1892 Houston, TX (United States)

1999-04-01

We examine the effects of energy derivatives trading on the crude oil market. There is a common public and regulatory perception that derivative securities increase volatility and can have a destabilizing effect on the underlying market. Consistent with this view, we find an abnormal increase in volatility for three consecutive weeks following the introduction of NYMEX crude oil futures. While there is also evidence of a longer-term volatility increase, this is likely due to exogenous factors, such as the continuing deregulation of the energy markets. Subsequent introductions of crude oil options and derivatives on other energy commodities have no effect on crude oil volatility. We also examine the effects of derivatives trading on the depth and liquidity of the crude oil market. This analysis reveals a strong inverse relation between the open interest in crude oil futures and spot market volatility. Specifically, when open interest is greater, the volatility shock associated with a given unexpected increase in volume is much smaller. (Copyright (c) 1999 Elsevier Science B.V., Amsterdam. All rights reserved.)

The impact of energy derivatives on the crude oil market

International Nuclear Information System (INIS)

Fleming, J.; Ostdiek, B.

1999-01-01

We examine the effects of energy derivatives trading on the crude oil market. There is a common public and regulatory perception that derivative securities increase volatility and can have a destabilizing effect on the underlying market. Consistent with this view, we find an abnormal increase in volatility for three consecutive weeks following the introduction of NYMEX crude oil futures. While there is also evidence of a longer-term volatility increase, this is likely due to exogenous factors, such as the continuing deregulation of the energy markets. Subsequent introductions of crude oil options and derivatives on other energy commodities have no effect on crude oil volatility. We also examine the effects of derivatives trading on the depth and liquidity of the crude oil market. This analysis reveals a strong inverse relation between the open interest in crude oil futures and spot market volatility. Specifically, when open interest is greater, the volatility shock associated with a given unexpected increase in volume is much smaller. (Copyright (c) 1999 Elsevier Science B.V., Amsterdam. All rights reserved.)

Changes in the composition and properties of Ashalchinskoye bitumen-saturated sandstones when exposed to water vapor

Science.gov (United States)

Korolev, E.; Eskin, A.; Kolchugin, A.; Morozov, V.; Khramchenkov, M.; Gabdelvalieva, R.

2018-05-01

Ashalchinskoye bitumen deposit is an experimental platform for testing technology of high-viscosity oil extraction from reservoir rocks. Last time for enhanced of oil recovery in reservoir used pressurization a water vapor with a temperature of ∼ 180 ° C (SAGD technology). However, what happens in sandstone reservoir is little known. We did a study of the effects of water vapor on the structural components of bitumen saturated sandstone. In paper were studied the rock samples at base condition and after one week exposure by water vapour. The thermal analysis showed that steaming helps to removes light and middle oil fractions with a boiling point up to 360 ° C from oil saturated sandstones. Content of heavy oil fractions virtually unchanged. Studying the composition of water extractions of samples showed that the process of aquathermolysis of oil is accompanied by a lowering of the pH of the pore solution from 7.4 to 6.5 and rise content in several times of mobile cations Ca2+, Mg2+ and HCO3 -, SO4 2- anions. Follows from this that the thermal steam effect by bitumen saturated sandstones leads to partial oxidation of hydrocarbons with to form a carbon dioxide. The source of sulfate ions were oxidized pyrite aggregates. Due to the increasing acidity of condensed water, which fills the pore space of samples, pore fluid becomes aggressive to calcite and dolomite cement of bitumen saturated sandstones. As a result of the dissolution of carbonate cement the pore fluid enriched by calcium and magnesium cations. Clearly, that the process is accompanied by reduction of contact strength between fragments of minerals and rocks. Resulting part of compounds is separated from the outer side of samples and falls to bottom of water vapor container. Decreasing the amount of calcite and dolomite anions in samples in a steam-treated influence is confirmed by X-Ray analysis. X-Ray analysis data of study adscititious component of rocks showed that when influenced of water vapor to

Catalytic cracking of bio-oil to organic liquid product (OLP).

Science.gov (United States)

Hew, K L; Tamidi, A M; Yusup, S; Lee, K T; Ahmad, M M

2010-11-01

The main objective of this paper is to find the optimum operating condition to upgrade the EFB-derived pyrolysis oil (bio-oil) to liquid fuel, mainly gasoline using Taguchi Method. From the analysis that has been done, it is found that the optimum operating condition for heterogeneous catalytic cracking process is at 400 degrees C, 15min of reaction time using 30g of catalyst weight where operating at this condition produced the highest yield of gasoline fraction which is 91.67 wt.%. This observation proves that EFB-derived pyrolysis oil could be upgraded via heterogeneous catalytic cracking to produce gasoline.

Modification of the process for separating and recovering oil from oil-sands, etc

Energy Technology Data Exchange (ETDEWEB)

Preller, H

1922-08-30

A method of carrying out the process according to Patent 400,122 especially for washing oil or bitumen-bearing mineral materials contaminated with more or less clay, marl, and so forth is characterized in that the oil-bearing raw material is first washed in an opposing stream of warm water for separating the larger part of the oil and settling the larger part of the rock. At the same time the fine clay suspended during the washing operation to a large extent and the remaining rock particles, which are unbound from the oil, by means of a regulatable water stream for further washing are carried into a receptacle of greater cross section, where by the very slow rise of the liquid the finer oil particles find an opportunity to ascend.

Bituminization of liquid radioactive wastes. Part 1

International Nuclear Information System (INIS)

Gradev, G.D.; Ivanov, V.I.; Stefanova, I.G.; Milusheva, A.G.; Guteva, E.S.; Zhelyazkov, V.T.; Stefanov, G.I.; G'oshev, G.S.

1991-01-01

Salt-bitumen products are produced by the method of 'hot mixing' of some Bulgarian bitumens (road bitumen PB 66/99 and the hydroinsulating bitumen HB 80/25) and salts (chlorides, sulphates, borates, salt mixtures modelling the liquid waste from nuclear power plants) in different ratios to determine the optimum conditions for bituminization of liquid radioactive waste. The penetration, ductility and softening temperature were determined. The sedimentation properties and the thermal resistance of the various bitumen-salt mixtures were studied. The most suitable bitumen for technological research at the Kozloduy NPP was found to be the road bitumen PB 66/90 with softening temperature at 48 o C. The optimum amount of salts incorporated in the bitumen - about 45% - was found. No exothermal effects were observed in the bituminization process in the temperature range of up to 200 o C. The results obtained may be useful in the elaboration of a technology for bituminization of liquid radioactive wastes in the Kozloduy NPP. 4 tabs., 5 figs., 4 refs

Supplying synthetic crude oil from Canadian oil sands: A comparative study of the costs and CO2 emissions of mining and in-situ recovery

International Nuclear Information System (INIS)

Méjean, Aurélie; Hope, Chris

2013-01-01

High crude oil prices and the eventual decline of conventional oil production raise the issue of alternative fuels such as non-conventional oil. The paper describes a simple probabilistic model of the costs of synthetic crude oil produced from Canadian oil sands. Synthetic crude oil is obtained by upgrading bitumen that is first produced through mining or in-situ recovery techniques. This forward-looking analysis quantifies the effects of learning and production constraints on the costs of supplying synthetic crude oil. The sensitivity analysis shows that before 2035, the most influential parameters are the learning parameter in the case of in-situ bitumen and the depletion parameter in the case of mined bitumen. After 2035, depletion dominates in both cases. The results show that the social cost of CO 2 has a large impact on the total costs of synthetic crude oil, in particular in the case of synthetic crude oil from in-situ bitumen, due to the carbon intensity of the recovery techniques: taking into account the social cost of CO 2 adds more than half to the cost of producing synthetic crude oil from mined bitumen in 2050 (mean value), while the cost of producing synthetic crude oil from in-situ bitumen more than doubles. - Highlights: • We model the cost of Canadian synthetic crude oil (SCO) using Monte-Carlo techniques. • We reveal the uncertainty associated with each input parameter. • We quantify the effect of learning, depletion and CO 2 using sensitivity analyses. • Accounting for the social cost of CO 2 doubles the cost of SCO from in-situ bitumen. • CO 2 pricing could have a large effect on the economics of the oil sands

Investigation of the Bitumen Modification Process Regime Parameters Influence on Polymer-Bitumen Bonding Qualitative Indicators

Science.gov (United States)

Belyaev, P. S.; Mishchenko, S. V.; Belyaev, V. P.; Belousov, O. A.; Frolov, V. A.

2018-04-01

The objects of this study are petroleum road bitumen and polymeric bituminous binder for road surfaces obtained by polymer materials. The subject of the study is monitoring the polymer-bitumen binder quality changes as a result of varying the bitumen modification process. The purpose of the work is to identify the patterns of the modification process and build a mathematical model that provides the ability to calculate and select technological equipment. It is shown that the polymer-bitumen binder production with specified quality parameters can be ensured in apparatuses with agitators in turbulent mode without the colloidal mills use. Bitumen mix and modifying additives limiting indicators which can be used as restrictions in the form of mathematical model inequalities are defined. A mathematical model for the polymer-bitumen binder preparation has been developed and its adequacy has been confirmed.

Properties and long-term behaviour of bitumen and radioactive waste-bitumen mixtures

International Nuclear Information System (INIS)

Eschrich, H.

1980-10-01

Part I represents a survey of the properties and the long-term behaviour of pure bitumens and mixtures of bitumens with radioactive reactor and reprocessing wastes. This survey includes information on the origin, amounts, and composition of the various wastes considered for bituminization and the different waste bituminization techniques used. The influence of various factors on the quality of waste-bitumen products and on the radiological safety during transport, short- and long-term storage of the final products is described. Special consideration is given to the most important safety relevant factors associated to the use of bitumen as matrix material for radioactive wastes, such as leach-resistance, radiolysis, chemical and mechanical stability, combustibility, and microbial attack. Part II consists of a comprehensive bibliography on the bituminization of radioactive wastes, giving about 300 references to literature published from the beginning of the use of bitumen in radioactive waste management in 1960 until the beginning of 1979. Methods for the quality control of bituminous materials and some useful data are given in an annex. (author)

IARC 1987 re-evaluation of carcinogenicity of mineral oils and bitumens - CONCAWE comments and interpretation

Energy Technology Data Exchange (ETDEWEB)

1988-10-01

Following the IARC response to CONCAWE comments on their 1987 re-evaluation of carcinogenicity of mineral oils and bitumens, CONCAWE decided that a revised version of Report No. 87/63 should be published in this report. The objective is to ensure that all who may be concerned with carcinogenicity classifications of these petroleum products, including national and international regulatory authorities, are aware of the reasons for the differences between the 1984 and 1987 IARC classifications and of CONCAWE's reservations concerning the revised classifications. This document reviews important differences between the new and previous evaluations, which are summarized in tabular form, and also indicates how the differences have occurred. In addition, it provides CONCAWE's interpretation of the available evidence, taking into account points discussed with IARC. 1 tab.

Breaking through the bitumen upgrading barriers with the UOP Uniflex Process

Energy Technology Data Exchange (ETDEWEB)

Gillis, D. [UOP LLC, Des Plaines, IL (United States)

2009-07-01

High costs and environmental concerns are some of the challenges facing bitumen upgrading. In addition, yields from conventional process such as coking and ebullated bed hydrocracking are much lower than desired. As such, there is a need for processes that can maximize conversion and selectively produce transportation boiling range products, particularly distillates. There are both technical and financial challenges in providing a reliable high-conversion technology. UOP has developed the UOP Uniflex Process, a commercially based high-conversion residue upgrading process that selectively converts residues from conventional crude oils and bitumen to transportation fuels and high quality synthetic crude oil. The unique features of this technology were described along with commercialization background. Recent advances being developed by UOP under the AERI Hydrocarbon Upgrading Demonstration Program were also described, with particular reference to catalyst design, engineering design and residue by-product utilization. This presentation also outlined UOP's latest flow scheme options for use with existing upgrading technologies. tabs., figs.

HDN and HDS of different gas oils derived from Athabasca bitumen over phosphorus-doped NiMo/{gamma}-Al{sub 2}O{sub 3} carbides

Energy Technology Data Exchange (ETDEWEB)

Sundaramurthy, V.; Dalai, A.K. [Catalysis and Chemical Reaction Engineering Laboratories, Department of Chemical Engineering, University of Saskatchewan, Saskatoon, Sask. S7N 5A9 (Canada); Adjaye, J. [Syncrude Edmonton Research Centre, Edmonton, Alta. T6N 1H4 (Canada)

2006-10-26

A series of phosphorous-doped {gamma}-Al{sub 2}O{sub 3} supported Ni-Mo bimetallic carbide catalysts (PNiMo{sub 2}C/Al{sub 2}O{sub 3}) with 0-4.5wt.% Ni, 13wt.% Mo and 2.5wt.% P were synthesized and characterized by elemental analysis, pulsed CO chemisorption, surface area measurement, X-ray diffraction (XRD), near-edge X-ray absorption fine structure (NEXAFS), DRIFT spectroscopy of CO adsorption and H{sub 2} temperature programmed reduction. XRD indicated the formation of pure {beta}-Mo{sub 2}C phase in these catalysts, whereas the near edge X-ray absorption fine structure of C K-edge confirmed the formation of carbidic carbons. DRIFT spectra of adsorbed CO revealed that Ni or P addition to Mo{sub 2}C/Al{sub 2}O{sub 3} catalyst not only increases the number of surface Mo sites, but also promotes the reducibility of Mo. The partial sulfidation of Mo{sub 2}C phase in the presence of H{sub 2}S/H{sub 2} gas mixture at 370{sup o}C was evidenced by DRIFTS of adsorbed CO. The HDN and HDS activities of these PNiMo{sub 2}C/Al{sub 2}O{sub 3} catalysts were performed in a trickle bed reactor using light gas oil (LGO) and heavy gas oil (HGO) derived from Athabasca bitumen at 8.8MPa and compared with the unpromoted Mo carbide (Mo{sub 2}C/Al{sub 2}O{sub 3}), P doped Mo carbide (PMo{sub 2}C/Al{sub 2}O{sub 3}) and Ni promoted Mo carbide (NiMo{sub 2}C/Al{sub 2}O{sub 3}). The P doped Ni-Mo bimetallic carbide catalysts showed enhanced HDN activity compared to the Mo{sub 2}C/Al{sub 2}O{sub 3}, NiMo{sub 2}C/Al{sub 2}O{sub 3} and PMo{sub 2}C/Al{sub 2}O{sub 3} catalysts. The maximum N and S conversions, respectively, were obtained over PNiMo{sub 2}C/Al{sub 2}O{sub 3} and NiMo{sub 2}C/Al{sub 2}O{sub 3} catalysts containing 2.5wt.% Ni. (author)

Application of oxy-fuel CO2 capture for In-situ bitumen extraction from Canada's oil sands

Energy Technology Data Exchange (ETDEWEB)

Bohm, Mark; Goold, Scott; Laux, Stefan; Sharma, Apoorva; Aasen, Knut; Neu, Ben

2010-09-15

The CO2 Capture Project, along with Praxair, Devon Canada, Cenovus Energy and Statoil are executing a project to demonstrate oxy-fuel combustion as a practical and economic method for CO2 capture from once-through steam generators used in the in-situ production of bitumen in the Canadian Oil Sands. The goal of the project is to develop a reliable, lower cost solution for capturing CO2 that will eliminate up to 90% of the GHG emissions from in-situ operations. The participants will present results of Phase I of this project, and will also outline the future Phases to pilot this technology.

Bitumen based modified substance

International Nuclear Information System (INIS)

Kostolanyi, P.

1987-01-01

The necessary amounts of tetrahydrosilicic acid and methyl phenyl silicon oil are added to molten bitumen heated to temperatures of 50 to 200 degC. The mixture is thoroughly mixed and let to cool. The structure of the product comes close to gel and its properties (penetration, softening point, workability time, penetration index) may be changed in dependence on the amount of additions and on the time and temperature of heating. The advantage of the thus prepared modified material is its shorter workability time, its ability to bind materials with a certain water content, and its relatively low price. It may be used for fixing and storing low-and medium-level radioactive organic and thickened waste waters. (E.S.)

Process for treating oil shale

Energy Technology Data Exchange (ETDEWEB)

1920-08-22

A process for treating oil shale is characterized in that the shale is first finely ground, then heated in the presence of steam in a high-pressure retort at 1 to 50 atmospheres pressure at a temperature of 200/sup 0/ to 450/sup 0/C and then with large amounts of water with or without materials forming emulsions with water or with oil. Solution medium suitable for bitumen or paraffin is beaten up in a rapid hammer mill until all or most all of the oil or bitumen is emulsified. The emulsion is separated by filter-pressing and centrifuging from the solid shale residue and the oil or bitumen is again separated from the emulsion medium by heating, acidulating, standing, or centrifuging, and then in known ways is further separated, refined, and worked up.

Heavy oil and bitumen : thinking caps on : researchers look at new and greener ways to get at the heavy oil prize

Energy Technology Data Exchange (ETDEWEB)

Harrison, L.

2008-01-15

New steam stimulation processes developed by the Alberta Ingenuity Centre for In Situ Energy were discussed. The J-well and gravity-assisted steam stimulation (JAGD) process uses a steam injection well located within the top few metres of a reservoir and a production well comprised of an inclined J-shaped well. JAGD is a transitional cold production-to-thermal-production technology. High pressure steam is used to heat and loosen the bitumen so that it flows to the producer well below. The configuration was designed to cut through mud and shale layers and is suitable for poor quality reservoirs. Simulations conducted in Athabasca reservoirs have demonstrated that JAGD uses approximately 75 per cent of the steam typically used in steam assisted gravity drainage (SAGD) processes. The iSAGD process was designed to reposition parallel wells in order to increase oil mobility. Researchers at the centre are also investigating a catalytic air-stream process called CASPAR which aims to upgrade oil from 10 degrees API to 16 degrees API within the reservoir. The process involves a mixture of heat, catalyst hydrogen, steam, air and water in the reservoir. The process leaves heavier ends of oil underground as well as fractions of greenhouse gases (GHGs). Research is also being conducted on expanding-solvent SAGD (ES-SAGD) a process that adds butane to steam in order to reduce water use. 3 figs.

Ultrasound-assisted oxidative desulfurization of bitumen

Science.gov (United States)

Kamal, Wan Mohamad Ikhwan bin Wan; Okawa, Hirokazu; Kato, Takahiro; Sugawara, Katsuyasu

2017-07-01

Bitumen contains a high percentage of sulfur (about 4.6 wt %). A hydrodesulfurization method is used to remove sulfur from bitumen. The drawback of this method is the requirement for a high temperature of >300 °C. Most of the sulfur in bitumen exists as thiophene. Oxidative desulfurization (ODS), involving oxidizing sulfur using H2O2, then removing it using NaOH, allows the removal of sulfur in thiophene at low temperatures. We removed sulfur from bitumen using ODS treatment under ultrasound irradiation, and 52% of sulfur was successfully removed. Additionally, the physical action of ultrasound assisted the desulfurization of bitumen, even at low H2O2 concentrations.

Characterization and Behavior of Cold Lake Blend and Western Canadian Select Diluted Bitumen Products

Science.gov (United States)

Unconventional diluted bitumen (dilbit) oil products present an increasing environmental concern because of extensive transport in North America, recent spills into aquatic habitats, and limited understanding of environmental fate and toxicity. Dilbits are blends of highly weathe...

Crustaceans from bitumen clast in Carboniferous glacial diamictite extend fossil record of copepods.

Science.gov (United States)

Selden, Paul A; Huys, Rony; Stephenson, Michael H; Heward, Alan P; Taylor, Paul N

2010-08-10

Copepod crustaceans are extremely abundant but, because of their small size and fragility, they fossilize poorly. Their fossil record consists of one Cretaceous (c. 115 Ma) parasite and a few Miocene (c. 14 Ma) fossils. In this paper, we describe abundant crustacean fragments, including copepods, from a single bitumen clast in a glacial diamictite of late Carboniferous age (c. 303 Ma) from eastern Oman. Geochemistry identifies the source of the bitumen as an oilfield some 100-300 km to the southwest, which is consistent with an ice flow direction from glacial striae. The bitumen likely originated as an oil seep into a subglacial lake. This find extends the fossil record of copepods by some 188 Ma, and of free-living forms by 289 Ma. The copepods include evidence of the extant family Canthocamptidae, believed to have colonized fresh water in Pangaea during Carboniferous times.

Application of zeolite-based catalyst to hydrocracking of coal-derived liquids

Energy Technology Data Exchange (ETDEWEB)

Shimada, H.; Sato, T.; Yoshimura, Y.; Hinata, A.; Yoshitomi, S.; Castillo Mares, A.; Nishijima, A. (National Chemical Laboratory for Industry, Tsukuba (Japan))

1990-06-01

Y-zeolite supported catalysts were applied to the hydrocracking of coal-derived liquids. By the introduction of two-stage upgrading consisting of hydrotreating and hydrocracking, Wandoan coal-derived middle distillate was hydrocracked over Ni-Mo/Y-zeolite, producing a high gasoline fraction yield. Zeolite supported catalysts gave little hydrocracked compounds in the hydroprocessing of coal-derived heavy oils, even after hydrotreatment. The reaction inhibitors which seriously poison the active sites of zeolites were found to be small nitrogen-containing molecules. In the hydroprocessing of coal-derived heavy oils, zeolite supported catalysts were inferior to alumina supported catalysts. This is due to the high hydrocracking but low hydrogenation activity of zeolite supported catalysts. 22 refs., 5 figs., 11 tabs.

Smoke reduction from pool fires using ferrocene and derivatives

International Nuclear Information System (INIS)

Mitchell, J.B.A.; Moir, M.E.

1992-01-01

A series of acyl and alkyl substituted ferrocene derivatives were tested as smoke control agents in laboratory-scale burn tests. In the tests, the soot produced by a given volume was collected on a filter and its weight measured to determine the relative smoke reducing effectiveness of the various derivatives. As the molecular weight of the derivative increases, the effectiveness decreases when added at a fixed weight concentration. The heavier derivatives were much less effective on a per-weight basis than ferrocene, while the multiply substituted compounds appeared to be more effective. In field tests conducted to evaluate the effectiveness of ferrocene in reducing smoke during combustion of other hydrocarbon fuels, it was found that there was a very large soot yield from gasoline fuel, higher than for crude oil even when ferrocene was used. In meso-scale tests, a drastic reduction in smoke yield was obtained when using a new liquid smoke-control additive during combustion of dilbit (bitumen diluted by gas condensate) floating on water. 3 refs., 5 figs., 1 tab

On the determination of diffusivities of volatile hydrocarbons in semi-solid bitumen

International Nuclear Information System (INIS)

Tang, J. S.

2001-01-01

Carbon dioxide, supercritical ethane and propane have been considered as solvents to recover heavy oil. Given that mixing solvent with bitumen is one of the important parameters governing the performance of the solvent extraction processes, good understanding of solvent dispersion is essential for the proper design of the process. Produced bitumen can still contain some residual volatile hydrocarbons after gas flashing off a three-phase separator. When exposed to the air due to a spill or ruptured line, these residual hydrocarbons can escape and create air pollution problems. Consequently, knowledge of the diffusivities of volatile components in bitumen is needed to assess the extent of environmental damage that may result from bitumen spill or working loss of vapour to the atmosphere. This paper discusses the de-coupled transfer model developed by this author (and described in a paper in vol. 78 of this journal) and its limiting solution, and provides a re-intrepretation of the method by Fu and Phillips (1979) which in turn was based on the late-time limiting solution advanced by Tang and Zhang (2000). The analysis indicates that gas purging is a valid method for determining the diffusion coefficients of trace, volatile hydrocarbons in bitumen. However, the assumption of de-coupling may not be appropriate for large diffusion flux and slow gas flow. Furthermore, improper use of the limiting solution theory could lead to a 25 per cent error in calculating the diffusion coefficient. 14 refs., 2 tabs., 8 figs

Localized enrichment of polycyclic aromatic hydrocarbons in soil, spruce needles, and lake sediments linked to in-situ bitumen extraction near Cold Lake, Alberta

International Nuclear Information System (INIS)

Korosi, J.B.; Irvine, G.; Skierszkan, E.K.; Doyle, J.R.; Kimpe, L.E.; Janvier, J.; Blais, J.M.

2013-01-01

The extraction of bitumen from the Alberta oil sands using in-situ technologies is expanding at a rapid rate; however, investigations into the environmental impacts of oil sands development have focused on surface mining in the Athabasca region. We measured polycyclic aromatic hydrocarbons (PAH) in soils, spruce needles, and lake sediment cores in the Cold Lake oil sands region to provide a historical and spatial perspective on PAH contamination related to in-situ extraction activities. A pronounced increase in PAH concentrations was recorded in one of two study lakes (Hilda Lake) corresponding to the onset of commercial bitumen production in ∼1985. Distance from extraction rigs was not an important predictor of PAH concentrations in soils, although two samples located near installations were elevated in alkyl PAHs. Evidence of localized PAH contamination in Hilda Lake and two soil samples suggests that continued environmental monitoring is justified to assess PAH contamination as development intensifies. -- Highlights: •In-situ bitumen extraction linked to rise in alkyl PAHs in one of two study lakes. •Alkyl PAHs elevated in two soil samples. •PAH contamination likely related to effluent sources, not atmospheric deposition. -- PAHs in sediments and soils were generally low in areas adjacent to in-situ bitumen extraction rigs in the Cold Lake Alberta oil sands, but evidence of localized contamination at some sites was evident

Technology of Anticorrosive Protection of Steel Constructions by Coatings Based on Rapid-Hardening Bitumen-Latex Emulsion

Directory of Open Access Journals (Sweden)

Nykyforchyn, H.M.

2016-01-01

Full Text Available The recipes of rapid-hardening bitumen-latex emulsions and coatings on its base are created, in-laboratory tests of their physical, chemical and anticorrosive properties are carried out. The technology of anticorrosive protection and the installation technical documentation for making of aqueous bitumen-latex emulsion is developed, installation is mounted and a pilot lot of rapid-hardening emulsion is produced. Experimental-industrial approbation of the technology of coating formation on pipes in oil and gas industry is carried out.

[Research on Oil Sands Spectral Characteristics and Oil Content by Remote Sensing Estimation].

Science.gov (United States)

You, Jin-feng; Xing, Li-xin; Pan, Jun; Shan, Xuan-long; Liang, Li-heng; Fan, Rui-xue

2015-04-01

Visible and near infrared spectroscopy is a proven technology to be widely used in identification and exploration of hydrocarbon energy sources with high spectral resolution for detail diagnostic absorption characteristics of hydrocarbon groups. The most prominent regions for hydrocarbon absorption bands are 1,740-1,780, 2,300-2,340 and 2,340-2,360 nm by the reflectance of oil sands samples. These spectral ranges are dominated by various C-H overlapping overtones and combination bands. Meanwhile, there is relatively weak even or no absorption characteristics in the region from 1,700 to 1,730 nm in the spectra of oil sands samples with low bitumen content. With the increase in oil content, in the spectral range of 1,700-1,730 nm the obvious hydrocarbon absorption begins to appear. The bitumen content is the critical parameter for oil sands reserves estimation. The absorption depth was used to depict the response intensity of the absorption bands controlled by first-order overtones and combinations of the various C-H stretching and bending fundamentals. According to the Pearson and partial correlation relationships of oil content and absorption depth dominated by hydrocarbon groups in 1,740-1,780, 2,300-2,340 and 2,340-2,360 nm wavelength range, the scheme of association mode was established between the intensity of spectral response and bitumen content, and then unary linear regression(ULR) and partial least squares regression (PLSR) methods were employed to model the equation between absorption depth attributed to various C-H bond and bitumen content. There were two calibration equations in which ULR method was employed to model the relationship between absorption depth near 2,350 nm region and bitumen content and PLSR method was developed to model the relationship between absorption depth of 1,758, 2,310, 2,350 nm regions and oil content. It turned out that the calibration models had good predictive ability and high robustness and they could provide the scientific

Shale oil. II. Gases from oil shale

Energy Technology Data Exchange (ETDEWEB)

McKee, R H; Manning, P D.V.

1927-01-01

Oil shale (from Colorado) was pyrolyzed, and the gaseous products obtained were studied. The organic material present in oil shale contains carboxyl groups that lose carbon dioxide during pyrolysis before the formation of soluble bitumen. Nitrogen was evolved as ammonia in two stages and was not continuous. The first evolution was from loosely combined nitrogen structures, whereas the second was from more stable forms. No hydrocarbons were present as such in the kerogen. The gaseous products from oil-shale pyrolysis were similar to those obtained by distillation of colophony, amber, coal, and wood. This places the kerogen of the oil shale in the same series of carbonaceous substances as those from which coals are formed. Kerogen appeared to be decomposed in three steps; namely, to insoluble bitumen, to soluble bitumen, and to oil (gas evolution accompanied each step). Its low solubility and the character of its pyrolytic gas indicated that kerogen is largely a resinous residue from vegetation of the past era and may have been formed by the tranportation of coal-forming organic debris to inland salty lakes or carried to the sea by clay-laden waters. The salt water and the natural settling action precipitated the clay and organic matter in an almost homogeneous deposit. Oil shales have existed to the present time because they have not been subjected to high pressures or elevated temperatures that would have changed them to petroleum.

Design of Hybrid Steam-In Situ Combustion Bitumen Recovery Processes

International Nuclear Information System (INIS)

Yang Xiaomeng; Gates, Ian D.

2009-01-01

Given enormous capital costs, operating expenses, flue gas emissions, water treatment and handling costs of thermal in situ bitumen recovery processes, improving the overall efficiency by lowering energy requirements, environmental impact, and costs of these production techniques is a priority. Steam-assisted gravity drainage (SAGD) is the most widely used in situ recovery technique in Athabasca reservoirs. Steam generation is done on surface and consequently, because of heat losses, the energy efficiency of SAGD can never be ideal with respect to the energy delivered to the sandface. An alternative to surface steam generation is in situ combustion (ISC) where heat is generated within the formation through injection of oxygen at a sufficiently high pressure to initiate combustion of bitumen. In this manner, the heat from the combustion reactions can be used directly to mobilize the bitumen. As an alternative, the heat can be used to generate steam within the formation which then is the agent to move heat in the reservoir. In this research, alternative hybrid techniques with simultaneous and sequential steam-oxygen injection processes are examined to maximize the thermal efficiency of the recovery process. These hybrid processes have the advantage that during ISC, steam is generated within the reservoir from injected and formation water and as a product of oxidation. This implies that ex situ steam generation requirements are reduced and if there is in situ storage of combustion gases, that overall gas emissions are reduced. In this research, detailed reservoir simulations are done to examine the dynamics of hybrid processes to enable design of these processes. The results reveal that hybrid processes can lower emitted carbon dioxide-to-oil ratio by about 46%, decrease the consumed natural gas-to-oil ratio by about 73%, reduce the cumulative energy-to-oil ratio by between 40% and 70% compared to conventional SAGD, and drop water consumption per unit oil produced

Jojoba oil and derivates

Energy Technology Data Exchange (ETDEWEB)

Wisniak, T

1977-01-01

Jojoba oil differs from all known seed oils by its almost complete absence of glycerides, making it more a liquid wax than a fat. It has become important as a possible substitute for sperm-whale oil to produce lubricants, lubricant additives and other products. The plant occurs naturally in southern Arizona and N.W. Mexico and its oil has long been used by Indians for medicinal, culinary, ritual and other purposes. It tolerates extreme daily fluctuations of temperature and grows well under the difficult soil and moisture conditions of the region. In the first part of this review the plant and its uses are described, including its floral, fruit and seed anatomy and the use of liquid wax during germination. Stored coryledon wax is used up by the embryo as a linear function of time during the first 30 days of germination and growth. Before germination, seeds weight about 0.59 mg and contain about 54% wax. The second and greater part of the review deals with jojoba oil (its extraction, properties, molecular description, toxicity and composition), jojoba meal, which remains after the oil has been extracted, and the chemical modification of the oil.

Extra heavy crudes and bitumens in the new EST technology

International Nuclear Information System (INIS)

Montanari, R.

2001-01-01

Strategic and market reasons dictate for the diversification of the supply sources. The huge reserves of extra heavy crudes and oil sands bitumen will provide the answer in this direction, but it is mandatory the availability of a suitable technology to process these poor quality feedstocks. EST Technology, developed by Snamprogetti and EniTecnologie, allows to get full conversion to produce high quality distillates [it

Gasification reactivities of cokes derived from Athabasca bitumen

Energy Technology Data Exchange (ETDEWEB)

Furimsky, E.

1985-10-01

Gasification reactivities of cokes obtained from Athabasca bitumen by delayed coking and fluid coking were compared in fixed and fluidized bed systems. In both systems the C + O/sub 2/ reaction accounted for the most of converted carbon. The C + H/sub 2/O reaction proceeded to a smaller extent. The bulk reactivity of the fluid coke was higher than that of delayed coke, when comparing -20 to +60 mesh particles in fluidized bed and -14 to +20 mesh particles in fixed bed, respectively. However, the reactivity of the delayed coke expressed per unit of surface area was markedly higher than that of the fluid coke. 9 figs., 7 tabs., 6 refs. (A.V.)

Morphology, Microstructure and Physico-Mechanical Properties of Pasargad Bitumen, Modified by Ethylene-Vinyl Acetate Copolymer (EVA and Nanoclay

Directory of Open Access Journals (Sweden)

Arezoo Ghaempour

2015-09-01

Full Text Available Due to the characteristics such as flexibility, adhesion, hydrophobicity and low price, bitumen is used in different construction and insulation industries. The major problem with the bitumen material is its restricted physico-mechanical properties, mainly high temperature rutting and low temperature cracking. The aim of this work was to modify bitumen, produced in Tabriz Pasargad Oil Company, and evaluation of its different properties to make it suitable for the weather conditions of North West of Iran. The physico-mechanical, morphological and rheological characteristics of EVA/Cloisite 15A modified bitumen were studied.Two different feeding instructions were used in the mixing of bitumen with modifiers.In the first method, EVA and Cloisite 15A nanoclay were simultaneously added into the molten bitumen and in the second method, EVA and Cloisite 15A were premixed in an internal mixer before adding the polymer/nanoclay nanocomposite into the molten bitumen. The results showed that addition of nanoclay and polymer into the bitumen, led increased softening point and a decrease in the penetration of base bitumen, in which the extent of changes, was higher for the samples prepared by masterbatch method. The rheological properties of the pre-mixed samples exhibited more improvement and these samples showed more elastic behavior. The results of optical microscopy showed that the pre-mixing of polymer and nanoclay led to a more uniform distribution of the swollen polymer phase at the base bitumen. These samples also showed higher morphology stability than those samples prepared in single step. These effects were related to the probable localization of nanoclay at the interface of the two phases.

Coals to Newcastle: Will Alberta become a crude oil importer?

International Nuclear Information System (INIS)

Haessel, W.; Foley, D.J.

1991-01-01

The security of markets for Canadian heavy crude oil (HCO) under different conditions is examined. The emphasis of the study is on the conditions under which bitumen blend from Alberta could penetrate certain markets that have generally been identified as potential prospects. A secondary question concerns the cost reductions in bitumen production and upgrading that would be needed for bitumen blend and synthetic crude oil (SCO) to penetrate these same markets if long-term oil prices settle at US$18/bbl for Saudi light delivered to the USA Gulf Coast in 2010. A brief overview is first presented of some of the world and US factors that will affect the demand for Canadian HCO, with specific reference to the demand in the northern USA in 2010. The determination of the volume of HCO that can or will be processed at a refinery or a combination of refineries in a given market is then discussed. The cost and volume numbers for 2010 as provided in the National Energy Board's latest Canadian energy supply and demand forecast are used in the analysis. It is concluded that all traditional markets outside of the Canadian prairies could be lost if world oil prices stay below US$18/bbl for extended periods. At prices below US$17/bbl, bitumen producers would have trouble competing with imported crude oils in Edmonton unless bitumen production costs decline from current levels. The potential for bitumen production costs to decline enough for diluted bitumen to compete with US$18/bbl oil is better than the prospect for SCO costs to decrease enough to compete in eastern Canada or the northern USA at those price levels. 9 figs., 8 tabs

Enhancement of Hydrodynamic Processes in Oil Pipelines Considering Rheologically Complex High-Viscosity Oils

Science.gov (United States)

Konakhina, I. A.; Khusnutdinova, E. M.; Khamidullina, G. R.; Khamidullina, A. F.

2016-06-01

This paper describes a mathematical model of flow-related hydrodynamic processes for rheologically complex high-viscosity bitumen oil and oil-water suspensions and presents methods to improve the design and performance of oil pipelines.

EM-SAGD/EM-GD : electromagnetic heating method : sustainable improvement of in-situ bitumen recovery

Energy Technology Data Exchange (ETDEWEB)

Wacker, B.; Diehl, D.; Huber, N.; Torlak, M.; Koolman, M. [Siemens AG, Munich (Germany)

2010-07-01

This paper described an electro-magnetic heating technology for the in situ recovery of bitumen. Studies have indicated that the technology promises a higher yield of bitumen with a smaller surface footprint than other bitumen production technologies. A laboratory study conducted with an inductor loop embedded in a 1 meter{sup 3} sand-box demonstrated that the technology is technically feasible. A series of field tests were then conducted by Siemens in a conductive subsurface later in Deggendorf, Germany. The field test included remotely operated surface equipment that was tested under down-scaled field conditions over a period of 6 months. New fiber optic sensors were used to obtain underground temperature readings. The field tests demonstrated a rise in temperature caused by the induction of eddy currents through electromagnetic fields in the conductive sub-surface. Results of the study will be used at an oil sands reservoir in 2011. The process can be combined with steam assisted gravity drainage (SAGD) processes. 4 refs., 7 figs.

Innovative Additive for Bitumen Based on Processed Fats

Science.gov (United States)

Babiak, Michał; Kosno, Jacek; Ratajczak, Maria; Zieliński, Krzysztof

2017-10-01

Various additives, admixtures and modifiers are used to improve technical properties and strength characteristics of building materials. Manufacturers of waterproofing materials, concrete, ceramics and bitumen have to use innovative, increasingly complex and costly additives, admixtures or modifiers. As a result, simple and inexpensive substances have been replaced by complex, long chain polymers, multi component resins or plastics. For economic and ecological reasons waste materials are more frequently used as additives, admixtures and modifiers. Nowadays the most commonly used physical modifiers of bitumen belong to the group of polymers - large molecular organic compounds of natural origin or being the result of planned chemical synthesis. Polymers are substances that do not chemically react with bitumen, they act as fillers or create a spatial network within bitumen (the so called physical cross-linking). The development of organic chemistry has allowed the synthesis of a number of substances chemically modifying bitumen. The most promising are heterocyclic organic compounds belonging to the group of imidazolines. The aim of the study presented in this paper was to demonstrate the suitability of processed natural and post-refining fat waste (diamidoamine dehydrate) as bitumen modifier. This paper discusses the impact of adding technical imidazoline on selected bitumen characteristics. Samples of bitumen 160/220, which is most commonly used for the production of waterproofing products, were analysed. For base bitumen and bitumen modified with technical imidazoline the following measurements were taken: measurement of the softening point by Ball and Ring method, determination of the breaking point by Fraass method and needle penetration measurement at 25°C. Later the samples were aged using TFOT laboratory method and the basic characteristics were determined again. The results showed that a small amount of imidazoline improved bitumen thermoplastic parameters at

Conventional OTSG development for heavy liquid fuel firing in thermal applications

Energy Technology Data Exchange (ETDEWEB)

Setchfield, W.P. [Mitchell Engineers Ltd., Glasgow, Scotland (United Kingdom); Roset, J.N. [Total S.A., Paris (France); Schaffer, M. [Total E and P Canada Ltd., Calgary, AB (Canada); O' Connor, D. [MEG Energy Inc., Calgary, AB (Canada); Kense, K. [TIW Western Inc., Calgary, AB (Canada)

2008-10-15

The demand for natural gas is expected to increase as a result of future expansion in Canadian extra heavy oil in-situ thermal production, such as steam assisted gravity drainage or SAGD projects. Natural gas is the current predominant fuel utilized for the associated steam generation. Potential natural gas shortages and related price volatility require that operators consider alternative fuels for the projected growth of in-situ thermal production in Alberta. This paper targeted the use of bitumen from upstream sites and derivative residues from upgrading activities as the most convenient alternative fuel sources for thermal operators of established horizontal type gas fired once through steam generators (OTSGs). The paper presented the methodology, the issues associated with bitumen or residue burning and the related technical solutions in developing a multi-fuel OTSG product. The paper provided background information on conventional OTSG design development, conventional OTSG existing deign, and general description of conventional OTSG. The paper also described the configuration of a radiant furnace, convection module, and theories and definitions such as heavy liquid fuels. A description and application of the equipment and processes as well as a presentation of the data and results was then offered. The multi fuel OTSG design is considered to be a practical and workable product capable of firing heavy liquid fuels. However, the design changes have had a significant impact when compared with conventional OTSG boilers. 11 figs.

Hydrogenation of rapeseed oil for production of liquid bio-chemicals

International Nuclear Information System (INIS)

Pinto, F.; Martins, S.; Gonçalves, M.; Costa, P.; Gulyurtlu, I.; Alves, A.; Mendes, B.

2013-01-01

Highlights: ► Production of renewable liquid hydrocarbons through rapeseed oil hydrogenation. ► Hydrogenation at lower temperature and lower hydrogen pressures. ► Test of a catalyst commonly employed in petrochemical industry. ► Improve of hydrogenation process viability by decreasing operational costs. ► Analysis of hydrogenated product applications as bio-chemicals. -- Abstract: The main objective of rapeseed oil hydrogenation tests was the production of liquid bio-chemicals to be used as renewable raw material for the production of several chemicals and in chemical synthesis to substitute petroleum derived stuff. As, hydrogenation of vegetable oils is already applied for the production of biofuels, the work done focused in producing aromatic compounds, due to their economic value. The effect of experimental conditions on rapeseed oil hydrogenation was studied, namely, reaction temperature and time with the aim of selecting the most favourable conditions to convert rapeseed oil into liquid valuable bio-chemicals. Rapeseed oil was hydrogenated at a hydrogen initial pressure of 1.10 MPa. Reaction temperature varied in the range from 200 °C to 400 °C, while reaction times between 6 and 180 min were tested. The performance of a commercial cobalt and molybdenum catalyst was also studied. The highest hydrocarbons yields were obtained at the highest temperature and reaction times tested. At a temperature of 400 °C and at the reaction time of 120 min hydrocarbons yield was about 92% in catalyst presence, while in the absence of the catalyst this value decreased to 85%. Hydrocarbons yield was even higher when the reaction time of 180 min was used in the presence of catalyst, as the yield of 97% was observed. At these conditions hydrocarbons formed had a high content of aromatic compounds, around 50%. For this reason, the viscosity values of hydrogenated oils were lower than that established by EN590, which together with hydrogenated liquids composition

Optical and UV-Aging Properties of LDH-Modified Bitumen

Directory of Open Access Journals (Sweden)

Xing Liu

2015-07-01

Full Text Available Layered double hydroxides (LDHs are an ultraviolet-light (UV resistant material. In this study, LDHs were used to modify bitumen. The optical and UV aging properties of LDHs modified bitumen were investigated. Firstly, the thin films of bitumen, with and without LDHs, were prepared. By using the UV-Vis spectrophotometer, absorbance, reflectance, and transmittance of bituminous thin film were evaluated. The morphology of LDHs-modified bitumen was observed by using fluorescence microscopy (FM. Finally, the aging resistance of LDH-modified bitumen was investigated by using the UV-aging oven. Results indicated that the LDHs, especially with 5 wt % in the bitumen, can effectively absorb and reflect the UV light and improve the UV-aging resistance of bitumen. This implied that the addition of LDHs into bitumen had the potential to prolong the service life of asphalt pavement.

Achievement report for fiscal 1997 on research under New Sunshine Program. Research on heavy oil hydrogenation and heavy oil/coal coprocessing; 1997 nendo jushitsuyu no suisoka shori narabi ni jushitsuyu/sekitan no coprocessing ni kansuru kenkyu seika hokokusho

Energy Technology Data Exchange (ETDEWEB)

NONE

1998-02-01

The achievements of the Hokkaido National Industrial Research Institute relating to the titled research are reported. In the study relating to the structural properties of heavy oils, the structures of products of Green River shale oil carbonization is analyzed, heterofunctional groups contained in the oil are subjected to FT-IR (Fourier transform infrared) spectroscopic analysis, and their forms of existence are investigated. In the study relating to the hydrogenation process of heavy oils, findings obtained from experiments are reported, which involve the processing of shale oil by hydrogenation and changes brought about in its chemical structure, hydrogenation of oil sand bitumen, kinetics of hydrocracking of bitumen at a high conversion rate, and a lumping model for bitumen hydrocracking reaction. In the study relating to the coprocessing of heavy oil/coal, coprocessing is experimented for coal and shale oil, coal and oil sand bitumen, and other combinations, and the results are reported. Also, a review is made of the transfer of hydrogen in coprocessing. (NEDO)

Oil shale, shale oil, shale gas and non-conventional hydrocarbons

Directory of Open Access Journals (Sweden)

Clerici A.

2015-01-01

Full Text Available In recent years there has been a world “revolution” in the field of unconventional hydrocarbon reserves, which goes by the name of “shale gas”, gas contained inside clay sediments micropores. Shale gas finds particular development in the United States, which are now independent of imports and see a price reduction to less than one third of that in Europe. With the high oil prices, in addition to the non-conventional gas also “oil shales” (fine-grained sedimentary rocks that contain a large amount of organic material to be used both to be directly burned or to extract liquid fuels which go under the name of shale oil, extra heavy oils and bitumen are becoming an industrial reality. Both unconventional gas and oil reserves far exceed in the world the conventional oil and gas reserves, subverting the theory of fossil fuels scarcity. Values and location of these new fossil reserves in different countries and their production by comparison with conventional resources are presented. In view of the clear advantages of unconventional fossil resources, the potential environmental risks associated with their extraction and processing are also highlighted.

Natural analogues of bitumen and bituminized radioactive waste

International Nuclear Information System (INIS)

Hellmuth, K.-H.

1989-07-01

Occurrences of natural bitumen provide possibilities to identify and assess materials, processes, phenomena and conditions in nature which can serve as model cases valid also with respect to a final repository. Natural bitumens meet the basic requirements for use as natural analogues. In natural sites, processes of bitumen formation and degradation often work simultaneously. The major processes are thermal alteration, evaporation, reaction with water, biodegradation, oxidation, weathering and radiation degradation. Progress in analytical organic geochemistry made during recent years has enabled a deeper understanding of the structural and compositional effects of these processes on bitumen. This is necessary in natural analogue applications. The time scales involved in degradation processes, as observed in natural occurrences, exceed the time scales dictated by the half-lives of most important fission products in low and medium level waste by orders of magnitude. Only exposure to the weather at the surface leads to a more rapid destruction of bitumen. Trace metals in bitumen arenot released until the matrix is completely destroyed. Products of radiation degradation and weathering of bitumen are able, to a certain degree, to delay migration of the metal ions released. Impregnation with bitumen may effectively reduce the microbial decomposition of easily destructable organic waste components, as can be deduced on the basis of the excellent preservation of fossils observed in bitumen. The complexity of all the natural sites described requires extensive understanding of the origin and kind of organic material in bitumen, its maturation, migration, alteration and degradation and of the geological and tectonic evolution of the site. The latter is used for establishing the time scale

Comparative analysis of fiscal terms for Alberta oil sands and international heavy and conventional oils

International Nuclear Information System (INIS)

Van Meurs, P.

2007-01-01

There are considerable differences between international heavy oil and Alberta oil sands projects, notably the high viscosity of the bitumen in the oil sands reservoirs. The oil sands bitumen do not flow to wells without heating the bitumen, thereby adding to the already high cost of Alberta oil sand operations. This report provided an economic comparison of Alberta oil sands and international heavy oil projects. It also included a brief scoping review to compare with conventional oil regimes. Full exploration costs including the costs of dry holes were allocated to conventional oil operations in order to obtain a proper comparison. This investigation included the costs of dry holes. The report was a follow up to an earlier study released on April 12, 2007 on the preliminary fiscal evaluation of Alberta oil sand terms. The report provided an economic framework and described project selection. It then provided a discussion of production, costs and price data. Four adjusted projects were presented and compared with Alberta. The Venezuelan royalty formula was also discussed. Last, the report provided a detailed fiscal analysis. Comparisons were offered with Cold Lake and Athabasca Mine. A review of some other fiscal systems applicable to conventional oil were also outlined. It was concluded that Alberta oil sands developments are very competitive. It would be possible to modestly increase government revenues, without affecting the international competitive position of Alberta with respect to conventional oil. There is also some possibility to increase the base royalty on the Alberta oil sands without losing competitiveness. tabs., figs

Changes of Properties of Bitumen Binders by Additives Application

Science.gov (United States)

Remišová, Eva; Holý, Michal

2017-10-01

Requirements for properties of bituminous binders are determined in the European standards. The physico-chemical behaviour of bitumen depends on its colloidal structure (asphaltenes dispersed into an oily matrix constituted by saturates, aromatics and resins) that depends primarily on its crude source and processing. Bitumen properties are evaluated by group composition, elementary analysis, but more often conventional or functional tests. Bitumen for road uses is assessed according to the physical characteristics. For the purpose of improving the qualitative properties of bitumen and asphalts the additives are applied e.g. to increase elasticity, improving the heat stability, improving adhesion to aggregate, to decrease viscosity, increasing the resistance to aging, to prevent binder drainage from the aggregate surface, etc. The objective of presented paper is to assess and compare effect of additives on properties of bitumen binders. In paper, the results of bitumen properties, penetration, softening point, and dynamic viscosity of two paving grade bitumen 35/50, 50/70 and polymer modified bitumen PmB 45/80-75 are analyzed and also the changes of these properties by the application of selected additives (Sasobit, Licomont BS100, Wetfix BE and CWM) to improve adhesion to aggregate and improve workability. Measurements of properties have been performed according to the relevant European standards. The laboratory tests showed significantly increasing the softening point of paving grade bitumen 50/70 and 35/50 by 13 to 45°C. The effect of various additives on bitumen softening point is different. Penetration varies according to type of bitumen and type of used additive. The penetration values of modified bitumen PmB 45/80-75 with additives Sasobit and Licomont BS100 show increase of bitumen stiffness of 16 0.1mm and a shift in the gradation. The changes in penetration and in softening point significantly shown when calculating on Penetration index as a parameter of

Effects of smectite on the oil-expulsion efficiency of the Kreyenhagen Shale, San Joaquin Basin, California, based on hydrous-pyrolysis experiments

Science.gov (United States)

Lewan, Michael D.; Dolan, Michael P.; Curtis, John B.

2014-01-01

The amount of oil that maturing source rocks expel is expressed as their expulsion efficiency, which is usually stated in milligrams of expelled oil per gram of original total organic carbon (TOCO). Oil-expulsion efficiency can be determined by heating thermally immature source rocks in the presence of liquid water (i.e., hydrous pyrolysis) at temperatures between 350°C and 365°C for 72 hr. This pyrolysis method generates oil that is compositionally similar to natural crude oil and expels it by processes operative in the subsurface. Consequently, hydrous pyrolysis provides a means to determine oil-expulsion efficiencies and the rock properties that influence them. Smectite in source rocks has previously been considered to promote oil generation and expulsion and is the focus of this hydrous-pyrolysis study involving a representative sample of smectite-rich source rock from the Eocene Kreyenhagen Shale in the San Joaquin Basin of California. Smectite is the major clay mineral (31 wt. %) in this thermally immature sample, which contains 9.4 wt. % total organic carbon (TOC) comprised of type II kerogen. Compared to other immature source rocks that lack smectite as their major clay mineral, the expulsion efficiency of the Kreyenhagen Shale was significantly lower. The expulsion efficiency of the Kreyenhagen whole rock was reduced 88% compared to that of its isolated kerogen. This significant reduction is attributed to bitumen impregnating the smectite interlayers in addition to the rock matrix. Within the interlayers, much of the bitumen is converted to pyrobitumen through crosslinking instead of oil through thermal cracking. As a result, smectite does not promote oil generation but inhibits it. Bitumen impregnation of the rock matrix and smectite interlayers results in the rock pore system changing from water wet to bitumen wet. This change prevents potassium ion (K+) transfer and dissolution and precipitation reactions needed for the conversion of smectite to

Liquid Crystal Formation from Sunflower Oil: Long Term Stability Studies.

Science.gov (United States)

da Rocha-Filho, Pedro Alves; Maruno, Mônica; Ferrari, Márcio; Topan, José Fernando

2016-06-09

The Brazilian biodiversity offers a multiplicity of raw materials with great potential in cosmetics industry applications. Some vegetable oils and fatty esters increase skin hydration by occlusivity, keeping the skin hydrated and with a shiny appearance. Sunflower (Helianthus annus L.) oil is widely employed in cosmetic emulsions in the form of soaps, creams, moisturizers and skin cleansers due to the presence of polyphenols and its high vitamin E content. Liquid crystals are systems with many applications in both pharmaceutical and cosmetic formulations and are easily detected by microscopy under polarized light due to their birefringence properties. The aim of this research was to develop emulsions from natural sunflower oil for topical uses. Sunflower oil (75.0% w/w) was combined with liquid vaseline (25.0% w/w) employing a natural self-emulsifying base (SEB) derivative. The high temperature of the emulsification process did not influence the antioxidant properties of sunflower oil. Fatty esters were added to cosmetic formulations and extended stability tests were performed to characterize the emulsions. Fatty esters like cetyl palmitate and cetyl ester increase the formation of anisotropic structures. O/W emulsions showed acidic pH values and pseudoplastic behavior. The presence of a lamellar phase was observed after a period of 90 days under different storage conditions.

Polyfunctional Modifiers for Bitumen and Bituminous Materials with High Performance

Directory of Open Access Journals (Sweden)

Alim Feizrakhmanovich Kemalov

2018-01-01

Full Text Available Over the last decade increase in capacity and the intensity of vehicular traffic has increased manifoldly, including heavy trucks, super singles, and higher tire pressures, resulting in significant increase of dynamic loads on the road surface which in turn lead to high quality requirements for bitumen in order to avoid premature wear and failure of asphalt concrete pavements. One of the possibilities to increase the quality of bitumen is to use special additives and modifiers that can provide a high adhesion to mineral filler and inhibit the aging and degradation processes in the asphalt coating. To achieve this, in the present study composite modifiers based on bisimidazolines derivatives were synthesized. The developed polyfunctional modifier (PFM of complex action provides enhanced thermal stability, significantly improves the adhesion between bitumen binder and aggregates, and also improves the physical-mechanical properties of the asphalt concrete. Based on the test results it is recommended to use the synthesized samples of the PFM additive with complex action in asphalt mixtures for road paving.

Optimum conditions for maximising pyrolysis liquids of oil palm empty fruit bunches

International Nuclear Information System (INIS)

Sulaiman, F.; Abdullah, N.

2011-01-01

As production of palm oil is expanding, a more efficient use of oil palm biomass to obtain more energy from oil palm plantations is investigated. The work was carried out on a fluidised bed bench scale fast pyrolysis unit, with the objective of determining the important conditions and key variables which are required to maximise the liquid yield and its quality. The investigation on the impact of reactor temperature, varying residence time by changing the nitrogen flow rate and combined impact of ash content and particle size on the product yields is presented. The properties of the liquid product were analysed and compared with wood derived bio-oil and petroleum fuels. It was found that in all cases the liquid product separated into two phases presenting difficulties for fuel applications, which are critically discussed. Potential solutions are also proposed which include upgrading of the liquid for fuel applications and other useful applications. -- Highlights: → Fibre analysis, proximate analysis and elemental analysis were carried out in this work. → Thermal degradation behaviour of EFB using thermogravimetry and differential thermogravimetry curves is in good agreement with other studies. → Maximum yield for liquids was determined to be around 55% at reactor temperature, 450 o C utilising residence time of 1.03 s → The low organic yield obtained for highest ash content of size below 150 μm is not due to low closure. → The phase separated liquid produced would present a challenging fuel due to its high viscosity and high water content.

Horizontal well impact on heavy oil supply

International Nuclear Information System (INIS)

Bowers, B.; Bielecki, J.; Hu, J.; Wall, B.; Drummond, K.

1993-01-01

Horizontal wells can take advantage of gravity drainage mechanisms, which can be important in conventional heavy oil and bitumen recovery. Horizontal drilling will impact on the development of established conventional heavy oil pools by infill drilling and application of enhanced recovery techniques. There will also be an impact on the development of extensions to established and newly discovered heavy oil pools, as well as a major impact on development of bitumen resources. To assess the impact of horizontal drilling on heavy oil supply, high-impact and low-impact scenarios were evaluated under specified oil-price assumptions for four heavy oil areas in Saskatchewan and Alberta. Horizontal well potential for infill drilling, waterflood projects, and thermal projects was assessed and estimates were made of such developments as reserves additions and heavy oil development wells under the two scenarios. In the low case, projected supply of conventional heavy oil and bitumen stabilizes at a level in the 90,000-94,000 m 3 /d after 1994. In the high case, overall supply continuously grows from 80,000 m 3 /d in 1992 to 140,000 m 3 /d in 2002. Through application of horizontal drilling, reserves additions in western Canada could be improved by ca 100 million m 3 by 2002. 14 figs., 6 tabs

Post Retort, Pre Hydro-treat Upgrading of Shale Oil

Energy Technology Data Exchange (ETDEWEB)

Gordon, John

2012-09-30

Various oil feedstocks, including oil from oil shale, bitumen from tar sands, heavy oil, and refin- ery streams were reacted with the alkali metals lithium or sodium in the presence of hydrogen or methane at elevated temperature and pressure in a reactor. The products were liquids with sub- stantially reduced metals, sulfur and nitrogen content. The API gravity typically increased. Sodi- um was found to be more effective than lithium in effectiveness. The solids formed when sodium was utilized contained sodium sulfide which could be regenerated electrochemically back to so- dium and a sulfur product using a "Nasicon", sodium ion conducting membrane. In addition, the process was found to be effective reducing total acid number (TAN) to zero, dramatically reduc- ing the asphaltene content and vacuum residual fraction in the product liquid. The process has promise as a means of eliminating sulfur oxide and carbon monoxide emissions. The process al- so opens the possibility of eliminating the coking process from upgrading schemes and upgrad- ing without using hydrogen.

Experimental investigation of changes in methane adsorption of bitumen-free Woodford Shale with thermal maturation induced by hydrous pyrolysis

Science.gov (United States)

Hu, Haiyan; Zhang, Tongwei; Wiggins-Camacho, Jaclyn D.; Ellis, Geoffrey S.; Lewan, Michael D.; Zhang, Xiayong

2014-01-01

This study quantifies the effects of organic-matter (OM) thermal maturity on methane (CH4) sorption, on the basis of five samples that were artificially matured through hydrous pyrolysis achieved by heating samples of immature Woodford Shale under five different time–temperature conditions. CH4-sorption isotherms at 35 °C, 50 °C, and 65 °C, and pressures up to 14 MPa on dry, solvent-extracted samples of the artificially matured Woodford Shale were measured. The results showed that CH4-sorption capacity, normalized to TOC, varied with thermal maturity, following the trend: maximum oil (367 °C) > oil cracking (400 °C) > maximum bitumen/early oil (333 °C) > early bitumen (300 °C) > immature stage (130 °C). The Langmuir constants for the samples at maximum-oil and oil-cracking stages are larger than the values for the bitumen-forming stages. The total pore volume, determined by N2 physisorption at 77 K, increases with increased maturation: mesopores, 2–50 nm in width, were created during the thermal conversion of organic-matter and a dramatic increase in porosity appeared when maximum-bitumen and maximum-oil generation stages were reached. A linear relationship between thermal maturity and Brunauer–Emmett–Teller (BET) surface area suggests that the observed increase in CH4-sorption capacity may be the result of mesopores produced during OM conversion. No obvious difference is observed in pore-size distribution and pore volume for samples with pores 2 physisorption at 273 K. The isosteric heat of adsorption and the standard entropy for artificially matured samples ranged from 17.9 kJ mol−1 to 21.9 kJ mol−1 and from −85.4 J mol−1 K−1 to −101.8 J mol−1 K−1, respectively. These values are similar to the values of immature Woodford kerogen concentrate previously observed, but are larger than naturally matured organic-rich shales. High-temperature hydrous pyrolysis might have induced Lewis acid sites on both organic and mineral surfaces

Integrated report on the toxicological mitigation of coal liquids by hydrotreatment and other processes. [Petroleum and coal-derived products

Energy Technology Data Exchange (ETDEWEB)

Guerin, M.R.; Griest, W.H.; Ho, C.H.; Smith, L.H.; Witschi, H.P.

1986-06-01

Research here on the toxicological properties of coal-derived liquids focuses on characterizing the refining process and refined products. Principle attention is given to the potential tumorigenicity of coal-derived fuels and to the identification of means to further reduce tumorigenicity should this be found necessary. Hydrotreatment is studied most extensively because it will be almost certainly required to produce commercial products and because it is likely to also greatly reduce tumorigenic activity relative to that of crude coal-liquid feedstocks. This report presents the results of a lifetime C3H mouse skin tumorigenicity assay of an H-Coal series of oils and considers the relationships between tumorigenicity, chemistry, and processing. Lifetime assay results are reported for an H-Coal syncrude mode light oil/heavy oil blend, a low severity hydrotreatment product, a high severity hydrotreatment product, a naphtha reformate, a heating oil, a petroleum-derived reformate, and a petroleum derived heating oil. Data are compared with those for an earlier study of an SRC-II blend and products of its hydrotreatment. Adequate data are presented to allow an independent qualitative assessment of the conclusions while statistical evaluation of the data is being completed. The report also documents the physical and chemical properties of the oils tested. 33 refs., 14 figs., 53 tabs.

Geochemistry of radioactive elements in bituminous sands and sandstones of Permian bitumen deposits of Tatarstan (east of the Russian plate)

Science.gov (United States)

Mullakaev, A. I.; Khasanov, R. R.; Badrutdinov, O. R.; Kamaletdinov, I. R.

2018-05-01

The article investigates geochemical features of Permian (Cisuralian, Ufimian Stage and Biarmian, Kazanian Stage of the General Stratigraphic Scale of Russia) bituminous sands and sandstones located on the territory of the Volga-Ural oil and gas province (Republic of Tatarstan). Natural bitumens are extracted using thermal methods as deposits of high-viscosity oils. In the samples studied, the specific activity of natural radionuclides from the 238U (226Ra), 232Th, and 40K series was measured using gamma spectrometry. As a result of the precipitation of uranium and thorium and their subsequent decay, the accumulation of radium (226Ra and 228Ra) has been shown to occur in the bituminous substance. In the process of exploitation of bitumen-bearing rock deposits (as an oil fields) radium in the composition of a water-oil mixture can be extracted to the surface or deposited on sulfate barriers, while being concentrated on the walls of pipes and other equipment. This process requires increased attention to monitoring and inspection the environmental safety of the exploitation procedure.

Alberta oil sands crudes : upgrading and marketing

International Nuclear Information System (INIS)

Ashar, M.

2008-01-01

Open pit mining and in situ techniques, such as steam stimulation, are used to recover Alberta's bitumen and heavy oil resources, which have higher viscosities than conventional hydrocarbons. The bitumen is typically upgraded to synthetic crude oil (SCO). In the simplest processing scheme, the bitumen is blended with diluent for ease in pipeline transport and then processed at refineries with upgrading facilities. The bitumen is also upgraded to light SCO at world-scale upgraders in Alberta. The SCO is then processed at refineries in downstream markets. The 2 categories of upgrading, notably primary and secondary upgrading, were described in this article along with technology options for both categories. Slurry hydrocracking is regarded as the most interesting emerging residual fuel upgrading technology. It combines special catalyst mixes with the latest slurry reactor designs as well as innovative catalyst capture and recycle schemes to produce very high conversions and potentially superior upgrading economics. The increase in volume and rate of SCO from Alberta provides refiners in the oil sands marketing sector an unprecedented choice of opportunities to improve profitability. Key trends indicate that production will increase substantially from 2008 to 2030. 5 figs

Alberta oil sands crudes : upgrading and marketing

Energy Technology Data Exchange (ETDEWEB)

Ashar, M. [Suncor Energy, Fort McMurray, AB (Canada)

2008-05-15

Open pit mining and in situ techniques, such as steam stimulation, are used to recover Alberta's bitumen and heavy oil resources, which have higher viscosities than conventional hydrocarbons. The bitumen is typically upgraded to synthetic crude oil (SCO). In the simplest processing scheme, the bitumen is blended with diluent for ease in pipeline transport and then processed at refineries with upgrading facilities. The bitumen is also upgraded to light SCO at world-scale upgraders in Alberta. The SCO is then processed at refineries in downstream markets. The 2 categories of upgrading, notably primary and secondary upgrading, were described in this article along with technology options for both categories. Slurry hydrocracking is regarded as the most interesting emerging residual fuel upgrading technology. It combines special catalyst mixes with the latest slurry reactor designs as well as innovative catalyst capture and recycle schemes to produce very high conversions and potentially superior upgrading economics. The increase in volume and rate of SCO from Alberta provides refiners in the oil sands marketing sector an unprecedented choice of opportunities to improve profitability. Key trends indicate that production will increase substantially from 2008 to 2030. 5 figs.

Oil sands supply outlook

International Nuclear Information System (INIS)

Dunbar, R.

2004-01-01

In March 2004, The Canadian Energy Research Institute released a report on the expected future supply from Alberta's oil sands. The report indicates that the future for the already well-established oil sands industry is promising, particularly given the outlook for oil prices. The challenges facing the industry include higher industry supply costs and the need for innovative commercial and technological solutions to address the risks of irregularities and changes in crude oil prices. In 2003, the industry produced 874 thousand barrels per day of synthetic crude oil and unprocessed crude bitumen. This represents 35 per cent of Canada's total oil production. Current production capacity has increased to 1.0 million barrels per day (mbpd) due to new projects. This number may increase to 3.5 mbpd by 2017. Some new projects may be deferred due to the higher raw bitumen and synthetic crude oil supply costs. This presentation provided supply costs for a range of oil sands recovery technologies and production projections under various business scenarios. tabs., figs

The road that's taken : Alberta's bitumen and the world of asphalt

International Nuclear Information System (INIS)

Bentein, J.

2009-01-01

Approximately one third of the bitumen produced by the oil sands industry in Canada is used as asphalt in roads and roofing materials. Crude oils used for asphalt production require very little refining. The asphalt market has become a key profit centre for some Cold Lake operators. Imperial Oil has established a research centre devoted to asphalt production at its Sarnia-based refinery. A decline in heavy oil supplies from Mexico and Venezuela has left Canada with a larger margin of the asphalt market. Industry leaders predict that demand for asphalt products will grow by 2.6 per cent per year. A sharp increase in asphalt prices led to many construction delays in 2007. Trials are now being conducted on a new warm mix paving technology that allows users to lower the temperature of asphalt by 20 to 30 degrees C when paving. 2 figs

Determination of organic products resulting of chemical and radiochemical decompositions of bitumen. Applications to embedded bitumens

International Nuclear Information System (INIS)

Walczak, I.

2000-01-01

Bitumen can be used for embedding most of wastes because of its high impermeability and its relatively low reactivity with of chemicals. Bituminization is one of selected solutions in agreement with nuclear safety, waste compatibility and economic criteria. Bitumen, during storage, undergoes an auto-irradiation due to embedded radio-elements. During this stage,drums are not airtight then oxygen is present. In disposal configuration, water, which is a potential vector of radioactivity and organic matter, is an other hazard factor liable to deteriorate the containment characteristics of bitumen wastes. The generation of water-soluble organic complexing agents can affect the integrity of the wasteform due to an increase of the radionuclides solubility. The first aim of this work is the quantitative and qualitative characterisation of soluble organic matter in bitumen leachates. Different leaching solutions were tested (various pH, ionic strength, ratio S/V). When the pH of the leaching solutions increases, the total organic carbon released increases as well. Identified molecules are aromatics like naphthalene, oxidised compounds like alcohols, linear carbonyls, aromatics, glycols and nitrogen compounds. For the cement equilibrated solution (pH 13.5), the effect of ionic strength becomes significative and influences the release of soluble organic matter. This soluble organic matter can be bio-degraded if microorganisms can growth. The second aim of this work is to study the effect of radio-oxidative ageing on the bitumen confinement properties. During radio-oxidation, the chemical properties of bitumen are modified. The μ-IRTF analysis shows the formation of hydroxyl compounds and aromatic acids. The formation of these polar groups does not influence in our study the water uptake. However the organic matter release increases significantly with the irradiation dose. (author)

The containment of heavy oil in flowing water

International Nuclear Information System (INIS)

Brown, H.M.; Goodman, R.H.; Nicholson, P.

1992-01-01

Viscous bitumen from Alberta oil sand deposits is diluted with a gas condensate before pipeline transport. Because of its unique properties, the diluent/bitumen mix (dilbit) may require novel containment and recovery techniques in the case of an accidental spill. Preliminary experiments were conducted in a large flowing water channel to determine whether several conventional containment devices could be utilized to trap weathered and emulsified dilbit and bitumen. These devices included a conventional river boom, a nylon fine-weave net, and a low-pressure bubble barrier. The behavior of the oil samples during boom failure was noted in order to understand more completely the mechanisms of failure. The river boom failed to hold viscous floating oil by vortex shedding at flows of under 0.25 m/s. A fine mesh net successfully trapped both floating and mid-channel neutrally buoyant oil but the retention time depends on the oil viscosity. The bubble barrier was not successful in trapping either floating viscous oil or neutrally buoyant oil. At low water velocities, the barrier was able to divert some oils but in an inconsistent manner. The results indicate that conventional barriers need improvement to be effective at higher water velocities and suggest that new concepts in containment should be considered. 9 refs., 3 figs., 2 tabs

Heavy mineral concentration from oil sand tailings

Energy Technology Data Exchange (ETDEWEB)

Chachula, F.; Erasmus, N. [Titanium Corp. Inc., Regina, SK (Canada)

2008-07-01

This presentation described a unique technique to recover heavy minerals contained in the froth treatment tailings produced by oil sand mining extraction operations in Fort McMurray, Alberta. In an effort to process waste material into valuable products, Titanium Corporation is developing technology to recover heavy minerals, primarily zircon, and a portion of bitumen contained in the final stage of bitumen processing. The process technology is being developed to apply to all mined oil sands operations in the Fort McMurray region. In 2004, Titanium Corporation commissioned a pilot research facility at the Saskatchewan Research Council to test dry oil sands tailings. In 2005, a bulk sampling pilot plant was connected to the fresh oil sands tailings pipeline on-site in Fort McMurray, where washed sands containing heavy minerals were processed at a pilot facility. The mineral content in both deposited tailings and fresh pipeline tailings was assessed. Analysis of fresh tailings on a daily basis identified a constant proportion of zircon and higher levels of associated bitumen compared with the material in the deposited tailings. The process flow sheet design was then modified to remove bitumen from the heavy minerals and concentrate the minerals. A newly modified flotation process was shown to be a viable processing route to recover the heavy minerals from froth treatment tailings. 8 refs., 9 tabs., 12 figs.

Canadian oil sands : supply and potential for market growth

International Nuclear Information System (INIS)

Crandall, G.

2004-01-01

Canadian oil sands recoverable reserves rank second only to Saudi Arabia and present enormous potential, particularly through technological gains. This paper discussed the market potential for oil sands both globally and in North America. It was estimated that oil sands production would eventually surpass declining conventional production, increasing from 42 per cent of Western supply in 2002 to 78 per cent in 2015. Recoverable reserves were an estimated 174 billion barrels, with cumulative production at 4 billion barrels between 1967 to 2003. Statistics of U.S. and Canadian markets for crude oil were presented to the year 2020. A flow chart of oil sands products and market outlets was presented, as well as details of existing and potential markets for Canadian crude oil. Oil sands product dispositions were outlined, with the prediction that Asia may emerge as an incremental market. World crude oil production statistics were presented by type. World residual supply and demand estimates were presented, including details of conversion capacity and requirements for residual processing capacity in refineries and field upgraders. American refinery feedstocks were presented by type, with the identification of an increase in heavy crude runs. It was noted that recent pricing provided a strong incentive to add refining conversion capacity to process heavy oil. An outline of a study completed for the Alberta government and industry was presented, in which upgrading to light synthetic crude was determined as a base case. The value added to process bitumen beyond upgrading was discussed in relation to the upgrading of American refineries to process bitumen blends and synthetic crude. Potential cases for upgrading bitumen were presented, along with a comparison of capital costs. An overall economic comparison of projects was provided. Various measures to maximize markets for oil sands products in Alberta were presented. It was suggested that U.S. markets should absorb more new

Bitumen pyrolysis

International Nuclear Information System (INIS)

Braehler, G.; Noll, T.

2014-01-01

In the past bitumen was a preferred matrix for the embedding of low and intermediate level radioactive waste: its geological history promised long term stability in final repositories. A great variety of waste has been embedded: technological waste, spent ion exchange resins, concrete, rubble, etc. Liquid waste like evaporator concentrates can be dried and embedded simultaneously in extruders, allowing simple processes and equipment. Unfortunately, during long term intermediate storage the bituminized waste drums proved out being not as stable as expected: a significant number turned out to be no longer acceptable for final disposal, and some of them even needed repacking to enable further intermediate storage. A method to rework such drums with bituminized radioactive waste seems to be urgently needed. Pyrolysis and pyro-hydrolysis (= pyrolysis with water steam added) have a long history for the treatment of organic waste: spent solvent (TBP), spent ion exchange resins, alpha waste (predominantly PVC), etc. Due to its low process temperature and the endothermic character, such processes offer significant safety advantages, as compared to incineration or dissolving in organic solvents. Results of lab-scale investigations and concepts for facilities are presented. (authors)

Rheological properties of crumb rubber modified bitumen containing antioxidant

International Nuclear Information System (INIS)

Mohamed, A. A; Omar, Husaini; Hamzah, M.O; Ismail, H.

2009-01-01

Rheology has become a useful tool in the characterization of the bitumen performance on the pavement. Visco-elastic properties of crumb rubber modified bitumen with antioxidants (CR30) were determined by the means of rheological measurement. This measurement led to a better knowledge of bitumen behavior that occurs when subjected to different thermal and mechanical conditions, as seen during road construction and services in the field. Dynamic Shear Rheometer (DSR) was used to characterize the rheology of the binders before and after oven aging. The binders were aged for 3 and 9 days. Results of a compatibility test showed that the addition of CR30 modified bitumen is compatible with the base bitumen. The results of unaged samples indicated that the addition of 1% CR30 and 5% CR30 modified binders caused an increase in G value as a result of the rheological changes. Results showed that aging has significant influence on bitumen rheology, by increasing complex modulus and decreasing phase angle. (author)

Bitumen pressure cell installation and monitoring procedure: Draft

International Nuclear Information System (INIS)

1987-02-01

A 6-in. (150-mm)-thick bitumen layer will be placed between the upper shaft preliminary concrete lining and the steel lining component of the final lining. The function of this layer is twofold; first, it will act as a compliant sealing layer which, because of the bitumen's fluid properties, will remain effective even if the concrete and steel lining components suffer significant strains; and second, it will help to ensure a uniform transmission of rock or hydrostatic loads to the inner lining components. A type 200--300 penetration grade bitumen (ASTM D946) will be used, with 32% by weight of added limestone flour. The purpose of the limestone flour is to ensure that the bitumen has a density which is greater than that of the formation fluids, resulting in a positive pressure gradient from the bitumen to the ground water. The resulting mixture will have a specific gravity of about 1.25 at 60/degree/F (15/degree/C). Pressure measurements in the bitumen layer are needed in order to determine loads on the inner lining components. Although some initial loading will occur in response to excavation, full rock and hydrostatic loads will not develop until post-construction thawing of the freeze wall is complete. Loads transmitted by the bitumen layer to the other lining components will be those which act radially, i.e., the bitustatic pressure, or the radial stress if deviatoric stresses develop

Optimisation of bitumen emulsion properties for ballast stabilisation

International Nuclear Information System (INIS)

D’Angelo, G.; Lo Presti, D.; Thom, N.

2017-01-01

Ballasted track, while providing economical and practical advantages, is associated with high costs and material consumption due to frequent maintenance. More sustainable alternatives to conventional ballasted trackbeds should therefore aim at extending its durability, particularly considering ongoing increases in traffic speed and loads. In this regard, the authors have investigated a solution consisting of bitumen stabilised ballast (BSB), designed to be used for new trackbeds as well as in reinforcing existing ones. This study presents the idea behind the technology and then focuses on a specific part of its development: the optimisation of bitumen emulsion properties and dosage in relation to ballast field conditions. Results showed that overall bitumen stabilisation improved ballast resistance to permanent deformation by enhancing stiffness and damping properties. Scenarios with higher dosage of bitumen emulsion, higher viscosity, quicker setting behaviour, and harder base bitumen seem to represent the most desirable conditions to achieve enhanced in-field performance. [es

The compositional study of nitrogen and oxygen compounds in products of heavy oil primary and secondary upgrading processes. Final report

Energy Technology Data Exchange (ETDEWEB)

Chmielowiec, J.

1986-02-01

The primary objective was to characterize nitrogen and oxygen compound types in the upgraded products derived from Athabasca bitumen. Nitrogen compounds, depending on their nature and concentrations, in charge stocks to catalytic processess (hydro-processes and reforming) can severely limit or poison the catalyst activity. Oxygen compounds are corrosive (especially naphthenic acids) and can promote gum formation as part of the deterioration of the hydrocarbons in the petroleum product. A secondary objective was to evaluate the advantages and limitations of in-house mass spectrometry and infrared spectroscopy methods for analyzing specific classes of polar compounds in naphthas, middle distillates, and gas oils. An analytical procedure that was based on the discrimination of polar compound classes using liquid chromatography followed by mass spectrometric analysis was tested. The chemical intelligence on the fractions obtained from Athabasca bitumen and its upgrading products has been advanced by determining structural characteristics of the nitrogen and oxygen components. This report describes the determination of the distributions of nitrogen and oxygen compounds in samples from various process streams. This procedure is capable of providing information useful for evaluating hydrodenitrogenation and hydrodeoxygenation reactions.

A series of NiMo/Al{sub 2}O{sub 3} catalysts containing boron and phosphorus. Part 2. Hydrodenitrogenation and hydrodesulfurization using heavy gas oil derived from Athabasca bitumen

Energy Technology Data Exchange (ETDEWEB)

Ferdous, D.; Dalai, A.K. [Catalysis and Chemical Reactor Engineering Laboratories, Department of Chemical Engineering, University of Saskatchewan, Saskatoon (Canada) SK S7N 5C9; Adjaye, J. [Syncrude Canada Ltd., Edmonton Research Center (Canada)

2004-04-08

The hydrodenitrogenation (HDN) and hydrodesulfurization (HDS) activity of a series of NiMo/Al{sub 2}O{sub 3} catalyst containing boron (B) and phosphorus (P) were tested in a trickle bed reactor using heavy gas oil derived from Athabasca bitumen. Detailed characterization of these catalysts is given in Part I of this paper. Addition of B and P caused the formation of extremely strong acid sites on the catalyst and enhanced its HDN activity. The total (TN), basic (BN) and non-basic nitrogen (NBN) conversions increased from 61.9 to 78.0wt.%, from 78.9 to 93.0wt.% and from 52.8 to 70.0wt.%, respectively, with the increase in B concentration from 0 to 1.7wt.% to NiMo/Al{sub 2}O{sub 3} catalyst. Similarly, TN, BN and NBN conversions increased from 61.9 to 78.4wt.%, from 78.9 to 91.0wt.%, and from 52.8 to 71.6wt.% with the addition of 2.7wt.% P. Though the addition of B and P to NiMo/Al{sub 2}O{sub 3} catalyst did not show any significant effect on S conversion, the HDN and HDS activities of the catalyst containing 1.7wt.% B and the one containing 2.7wt.% P are comparable to those of a commercial catalyst. The activity over extended period indicated that catalysts L and K were more stable (lower deactivation rate) in terms of nitrogen removal activity than catalyst B (reference catalyst). On the other hand, the stability for sulfur removal was comparable with catalyst B. Selected catalysts after use were characterized using BET surface area, TPR, TPD and SEM techniques which were correlated further with their activities.

Gas-to-liquids : who cares?

International Nuclear Information System (INIS)

Yakobson, D.L.

1999-01-01

An overview of gas-to-liquids (GTL) technology was presented along with its capital costs, economics and market niche. GTL technology is a process developed by Fischer-Tropsch in the 1920s, in which carbonaceous feedstock is catalytically converted into synthetic oil. The feedstock can be natural gas, coal, or refinery bottoms, bitumen, Orimulsion TM or biomass. The process involves the making of a gaseous mixture of hydrogen and carbon monoxide and then feeding that mixture into a reactor containing a catalyst. The last step involves the processing of the synthetic oil into fractions for sale. The issue of whether GTL will compete with refinery production or supplement it was also raised. The potential for GTL projects in North America were reviewed. The five companies which have matured GTL technologies are Exxon, Rentech, Sasol, Shell and Syntroleum

SOVENT BASED ENHANCED OIL RECOVERY FOR IN-SITU UPGRADING OF HEAVY OIL SANDS

Energy Technology Data Exchange (ETDEWEB)

Munroe, Norman

2009-01-30

With the depletion of conventional crude oil reserves in the world, heavy oil and bitumen resources have great potential to meet the future demand for petroleum products. However, oil recovery from heavy oil and bitumen reservoirs is much more difficult than that from conventional oil reservoirs. This is mainly because heavy oil or bitumen is partially or completely immobile under reservoir conditions due to its extremely high viscosity, which creates special production challenges. In order to overcome these challenges significant efforts were devoted by Applied Research Center (ARC) at Florida International University and The Center for Energy Economics (CEE) at the University of Texas. A simplified model was developed to assess the density of the upgraded crude depending on the ratio of solvent mass to crude oil mass, temperature, pressure and the properties of the crude oil. The simplified model incorporated the interaction dynamics into a homogeneous, porous heavy oil reservoir to simulate the dispersion and concentration of injected CO2. The model also incorporated the characteristic of a highly varying CO2 density near the critical point. Since the major challenge in heavy oil recovery is its high viscosity, most researchers have focused their investigations on this parameter in the laboratory as well as in the field resulting in disparaging results. This was attributed to oil being a complex poly-disperse blend of light and heavy paraffins, aromatics, resins and asphaltenes, which have diverse behaviors at reservoir temperature and pressures. The situation is exacerbated by a dearth of experimental data on gas diffusion coefficients in heavy oils due to the tedious nature of diffusivity measurements. Ultimately, the viscosity and thus oil recovery is regulated by pressure and its effect on the diffusion coefficient and oil swelling factors. The generation of a new phase within the crude and the differences in mobility between the new crude matrix and the

Process for separating and recovering oil from oil-sands, etc

Energy Technology Data Exchange (ETDEWEB)

Preller, H

1921-02-24

A process for separating and recovering oil from oil-sands, bitumen from oil-chalk, oil-shale, and coal, according to Patent 400,122, is described. It is characterized in that the mined material falling on account of its weight is exposed to the running hot water in circulation through the wash-chamber and the clarifying chamber arranged separate or built on (circulation) being obtained by pumps or injectors in a regulatable motion.

Saskatchewan's place in Canadian oil sands

Energy Technology Data Exchange (ETDEWEB)

Schramm, L.L. [Saskatchewan Research Council, Regina, SK (Canada); Kramers, J.W. [Owl Ventures Inc., Edmonton, AB (Canada); Isaacs, E.E. [Alberta Energy Research Inst., Edmonton, AB (Canada)

2010-11-15

The current daily bitumen and synthetic crude production from the Western Canada Sedimentary Basin is 180,000 m{sup 3}, which represents approximately 40 percent of crude oil produced in Canada. In a time of peaking conventional oil production, the search for new oil reserves has led to unconventional in-situ bitumen and heavy oil resources, including shallow in-situ resources. The great difficulty in producing bitumen and managing water flows in such reservoirs will require innovative approaches and increasingly environmentally sustainable practices. This paper presented an overview of shallow in-situ oil sands and the novel recovery technologies that are being developed that will reduce the use of steam and fresh water, and also reduce greenhouse gas emissions. Research and development programs are currently underway to develop and demonstrate such new technologies. Promising technologies include the solvent vapour extraction and hybrid thermal solvent extraction processes that are being developed and demonstrated in large-scale three-dimensional scaled physical models and associated numerical simulation models. Electrical heating and gravity stable combustion are other examples of technologies that could play a significant role in developing these resources. 81 refs., 3 tabs., 8 figs.

Liquid oil production from shale gas condensate reservoirs

Science.gov (United States)

Sheng, James J.

2018-04-03

A process of producing liquid oil from shale gas condensate reservoirs and, more particularly, to increase liquid oil production by huff-n-puff in shale gas condensate reservoirs. The process includes performing a huff-n-puff gas injection mode and flowing the bottom-hole pressure lower than the dew point pressure.

Rheological testing of crumb rubber modified bitumen

CSIR Research Space (South Africa)

Mturi, GAJ

2011-08-01

Full Text Available used to analyse crumb rubber modified (CRM) bitumen is that the specified gap setting in the configuration of the DSR between the upper and lower test platens is too small to accommodate crumb rubber particles. DSR testing of CRM bitumen therefore...

Constant strain rate experiments and constitutive modeling for a class of bitumen

Science.gov (United States)

Reddy, Kommidi Santosh; Umakanthan, S.; Krishnan, J. Murali

2012-08-01

The mechanical properties of bitumen vary with the nature of the crude source and the processing methods employed. To understand the role of the processing conditions played in the mechanical properties, bitumen samples derived from the same crude source but processed differently (blown and blended) are investigated. The samples are subjected to constant strain rate experiments in a parallel plate rheometer. The torque applied to realize the prescribed angular velocity for the top plate and the normal force applied to maintain the gap between the top and bottom plate are measured. It is found that when the top plate is held stationary, the time taken by the torque to be reduced by a certain percentage of its maximum value is different from the time taken by the normal force to decrease by the same percentage of its maximum value. Further, the time at which the maximum torque occurs is different from the time at which the maximum normal force occurs. Since the existing constitutive relations for bitumen cannot capture the difference in the relaxation times for the torque and normal force, a new rate type constitutive model, incorporating this response, is proposed. Although the blended and blown bitumen samples used in this study correspond to the same grade, the mechanical responses of the two samples are not the same. This is also reflected in the difference in the values of the material parameters in the model proposed. The differences in the mechanical properties between the differently processed bitumen samples increase further with aging. This has implications for the long-term performance of the pavement.

Rates and Mechanisms of Oil Shale Pyrolysis: A Chemical Structure Approach

Energy Technology Data Exchange (ETDEWEB)

Fletcher, Thomas; Pugmire, Ronald

2015-01-01

Three pristine Utah Green River oil shale samples were obtained and used for analysis by the combined research groups at the University of Utah and Brigham Young University. Oil shale samples were first demineralized and the separated kerogen and extracted bitumen samples were then studied by a host of techniques including high resolution liquid-state carbon-13 NMR, solid-state magic angle sample spinning 13C NMR, GC/MS, FTIR, and pyrolysis. Bitumen was extracted from the shale using methanol/dichloromethane and analyzed using high resolution 13C NMR liquid state spectroscopy, showing carbon aromaticities of 7 to 11%. The three parent shales and the demineralized kerogens were each analyzed with solid-state 13C NMR spectroscopy. Carbon aromaticity of the kerogen was 23-24%, with 10-12 aromatic carbons per cluster. Crushed samples of Green River oil shale and its kerogen extract were pyrolyzed at heating rates from 1 to 10 K/min at pressures of 1 and 40 bar and temperatures up to 1000°C. The transient pyrolysis data were fit with a first-order model and a Distributed Activation Energy Model (DAEM). The demineralized kerogen was pyrolyzed at 10 K/min in nitrogen at atmospheric pressure at temperatures up to 525°C, and the pyrolysis products (light gas, tar, and char) were analyzed using 13C NMR, GC/MS, and FTIR. Details of the kerogen pyrolysis have been modeled by a modified version of the chemical percolation devolatilization (CPD) model that has been widely used to model coal combustion/pyrolysis. This refined CPD model has been successful in predicting the char, tar, and gas yields of the three shale samples during pyrolysis. This set of experiments and associated modeling represents the most sophisticated and complete analysis available for a given set of oil shale samples.

Breaking the bottleneck : how best can we bring oil sands products to demanding markets

International Nuclear Information System (INIS)

Prince, D.

2006-01-01

Alberta-based Altex Energy Ltd. is pursuing the development of an innovative heavy oil/bitumen pipeline from Alberta to the United States Gulf Coast (USGC). This energy infrastructure development company is led by a proven management team that developed and constructed the 3,700 km long Alliance Pipeline system. This presentation included a map of the $3.7 billion dollar Alliance Pipeline that identified the mainline compressor stations, lateral compressor stations, area offices and head offices. It was noted that oilsands will represent the most significant resource plays for many years. A graph indicating bitumen supply forecasts from 2005 to 2020 suggests that bitumen production will have exponential growth over the foreseeable future. Labor, materials and infrastructure limitations will create barriers to oilsands growth, as will uncertain market access. For that reason, assured pipeline capacity is needed along with an infrastructure to refineries and a favourable competitive balance for Canadian producers. The presentation addressed issues regarding marketing choices and the challenges of upgrading in Alberta. The economics of diluting heavy oil was also discussed along with industry response to the diluent challenge. Altex's proposed solution of a new direct greenfield pipeline from Alberta to the USGC would reach the largest refinery market in North America as well as the largest heavy oil/bitumen consuming regions. The Altex solution would be complementary to heavy oil/bitumen in Alberta. The proprietary pipeline technology permits alternative diluents, eliminating much of the diluent penalty. It mitigates the risks of upgrading in Alberta and competes on a cost basis with other expansion alternatives. The Altex pipeline system eliminates the need for costly condensate diluent, but accepts all current diluents. It transports up to 90 per cent more bitumen than clean diluted bitumen in a conventional pipeline. It can also transport as much as 175 per cent

The case for a large heavy oil stream

International Nuclear Information System (INIS)

Reimer, P.

2005-01-01

EnCana Corporation markets significant proprietary and third party crude oil production in North America. This presentation presented details of EnCana's projected resources as well as estimated proved reserves in Canadian oil sands. Details of the Western Canadian heavy oil market were presented. Issues concerning Western Canadian Select (WCS) were also presented, including details of distillation and asphalt characteristics. Details of the WCS synthetic bitumen synergy were examined, as well as quality management issues. It was suggested that further optimization of WCS facilities include reduced operating complexity; less tank proliferation; delivery quality consistency; and reliability. WCS refiner advantages were also evaluated. Shipping and ramping details were discussed, along with growth potential. It was noted that WCS satisfies all the criteria for a benchmark crude. It was concluded that the case for a large Canadian heavy oil stream includes reduced operating complexity; optimized logistics; delivery quality consistency; improved stream liquidity; and enhanced price discovery. tabs., figs

Solids precipitation in crude oils, gas-to-liquids and their blends

Science.gov (United States)

Ramanathan, Karthik

Gas-to-liquids (GTL) liquids are obtained from syngas by the Fischer-Tropsch synthesis. The blending of GTL liquids produced from natural gas/coal reserves and crude oils is a possibility in the near future for multiple reasons. Solids precipitation is a major problem in pipelines and refineries leading to significant additional operating costs. The effect of the addition of a paraffinic GTL liquid to crude oils on solids precipitation was investigated in this study. A Fourier transform infrared (FT-IR) spectroscopic technique was used to obtain solid-liquid equilibria (SLE) data for the various samples. The SLE of multiple systems of model oils composed of n-alkanes was investigated preliminarily. Blends of a model oil simulating a GTL liquid composition and a crude oil showed that the wax precipitation temperature (WPT) decreased upon blending. Three crude oils from different geographic regions (Alaskan North Slope, Colorado and Venezuela) and a laboratory-produced GTL liquid were used in the preparation of blends with five different concentrations of the GTL liquid. The wax precipitation temperatures of the blends were found to decrease with the increasing addition of the GTL liquid for all the oils. This effect was attributed to the solvent effect of the low molecular weight-paraffinic GTL liquid on the crude oils. The weight percent solid precipitated that was estimated as a function of temperature did not show a uniform trend for the set of crude oils. The asphaltene onset studies done on the blends with near-infrared spectroscopy indicated that the addition of GTL liquid could have a stabilizing effect on the asphaltenes in some oils. Analytical techniques such as distillation, solvent separation, HPLC, GC, and GPC were used to obtain detailed composition data on the samples. Two sets of compositional data with 49 and 86 pseudo-components were used to describe the three crude oils used in the blending work. The wax precipitation was calculated using a

Liquid ultrasonic flow meters for crude oil measurement

Energy Technology Data Exchange (ETDEWEB)

Kalivoda, Raymond J.; Lunde, Per

2005-07-01

Liquid ultrasonic flow meters (LUFMs) are gaining popularity for the accurate measurement of petroleum products. In North America the first edition of the API standard ''Measurement of liquid hydrocarbons by ultrasonic flow meters using transit time technology'' was issued in February 2005. It addresses both refined petroleum products and crude oil applications. Its field of application is mainly custody transfer applications but it does provide general guidelines for the installation and operation of LUFM's other applications such as allocation, check meters and leak detection. As with all new technologies performance claims are at times exaggerated or misunderstood and application knowledge is limited. Since ultrasonic meters have no moving parts they appear to have fewer limitations than other liquid flow meters. Liquids ultrasonic flow meters, like turbine meters, are sensitive to fluid properties. It is increasingly more difficult to apply on high viscosity products then on lighter hydrocarbon products. Therefore application data or experience on the measurement of refined or light crude oil may not necessarily be transferred to measuring medium to heavy crude oils. Before better and more quantitative knowledge is available on how LUFMs react on different fluids, the arguments advocating reduced need for in-situ proving and increased dependency on laboratory flow calibration (e.g. using water instead of hydrocarbons) may be questionable. The present paper explores the accurate measurement of crude oil with liquid ultrasonic meters. It defines the unique characteristics of the different API grades of crude oils and how they can affect the accuracy of the liquid ultrasonic measurement. Flow testing results using a new LUFM design are discussed. The paper is intended to provide increased insight into the potentials and limitations of crude oil measurement using ultrasonic flow meters. (author) (tk)

Dynamics and structure of water-bitumen mixtures

DEFF Research Database (Denmark)

Lemarchand, Claire; Greenfield, Michael L.; Hansen, Jesper Schmidt

2016-01-01

Systems of Cooee bitumen and water up to 4% mass are studied by molecular dynamics simulations. The cohesive energy density of the system is shown to decrease with an increasing water content. This decrease is due mainly to an increase in the interaction energy which is not high enough to counter......Systems of Cooee bitumen and water up to 4% mass are studied by molecular dynamics simulations. The cohesive energy density of the system is shown to decrease with an increasing water content. This decrease is due mainly to an increase in the interaction energy which is not high enough...... droplets being more stable at the highest temperature simulated. The droplet is mainly located close to the saturates molecules in bitumen. Finally, it is shown that the water dynamics is much slower in bitumen than in pure water because it is governed by the diffusion of the droplet and not of the single...

Experimental data on compressive strength and durability of sulfur concrete modified by styrene and bitumen.

Science.gov (United States)

Dehestani, M; Teimortashlu, E; Molaei, M; Ghomian, M; Firoozi, S; Aghili, S

2017-08-01

In this data article experimental data on the compressive strength, and the durability of styrene and bitumen modified sulfur concrete against acidic water and ignition are presented. The percent of the sulfur cement and the gradation of the aggregates used are according to the ACI 548.2R-93 and ASTM 3515 respectively. For the styrene modified sulfur concrete different percentages of styrene are used. Also for the bitumen modified sulfur concrete, different percentages of bitumen and the emulsifying agent (triton X-100) are utilized. From each batch three 10×10×10 cm cubic samples were casted. One of the samples was used for the compressive strength on the second day of casting, and one on the twenty-eighth day. Then the two samples were put under the high pressure flame of the burning liquid gas for thirty seconds and their ignition resistances were observed. The third sample was put into the acidic water and after twenty eight days immersion in water was dried in the ambient temperature. After drying its compressive strength has been evaluated.

Assessment of Physicochemical Properties of some Bitumens from ...

African Journals Online (AJOL)

natural bitumen resources and potentials for sustained production of bitumen in large quantity, but basic ... Ondo State, and a manufactured type from Kaduna Refining and Petrochemical ..... Policies and Practices in Pavement Design and.

Energy infrastructure modeling for the oil sands industry: Current situation

International Nuclear Information System (INIS)

Lazzaroni, Edoardo Filippo; Elsholkami, Mohamed; Arbiv, Itai; Martelli, Emanuele; Elkamel, Ali; Fowler, Michael

2016-01-01

Highlights: • A simulation-based modelling of energy demands of oil sands operations is proposed. • Aspen simulations used to simulate delayed coking-based upgrading of bitumen. • The energy infrastructure is simulated using Aspen Plus achieving self-sufficiency. • Various scenarios affecting energy demand intensities are investigated. • Energy and CO_2 emission intensities of integrated SAGD/upgrading are estimated. - Abstract: In this study, the total energy requirements associated with the production of bitumen from oil sands and its upgrading to synthetic crude oil (SCO) are modeled and quantified. The production scheme considered is based on the commercially applied steam assisted gravity drainage (SAGD) for bitumen extraction and delayed coking for bitumen upgrading. In addition, the model quantifies the greenhouse gas (GHG) emissions associated with the production of energy required for these operations from technologies utilized in the currently existing oil sands energy infrastructure. The model is based on fundamental engineering principles, and Aspen HYSYS and Aspen Plus simulations. The energy demand results are expressed in terms of heat, power, hydrogen, and process fuel consumption rates for SAGD extraction and bitumen upgrading. Based on the model’s output, a range of overall energy and emission intensity factors are estimated for a bitumen production rate of 112,500 BPD (or 93,272 BPD of SCO), which were determined to be 262.5–368.5 MJ/GJ_S_C_O and 14.17–19.84 gCO_2/MJ_S_C_O, respectively. The results of the model indicate that the majority of GHG emissions are generated during SAGD extraction (up to 60% of total emissions) due to the combustion of natural gas for steam production, and the steam-to-oil ratio is a major parameter affecting total GHG emissions. The developed model can be utilized as a tool to predict the energy demand requirements for integrated SAGD/upgrading projects under different operating conditions, and

Examination of oil sands projects : gasification, CO{sub 2} emissions and supply costs

Energy Technology Data Exchange (ETDEWEB)

Elliott, K. [Energy Resources Conservation Board, Calgary, AB (Canada)

2008-10-15

Non-conventional resources such as Alberta's oil sands are experiencing increased global interest because of the decline in global conventional oil and natural gas reserves. Bitumen extraction and upgrading is an energy intensive process. This paper provided a general discussion of Alberta's oil sands reserves, production and energy requirements. The paper discussed the application of different technologies to the oil sands, and in particular, the use of gasification as a method to produce bitumen-derived synthesis gas. Two oil sands projects currently under construction and implementing gasification technology were briefly described. The paper also provided a comparison of emission intensities from projects that employ gasification leading to a forecast of carbon dioxide equivalent emissions from the oil sands. The impact of Alberta's legislation and the federal framework on greenhouse gas emissions were also examined. Last, the paper discussed a supply cost methodology to compare an integrated extraction and upgrading project using gasification versus a similar project using a conventional steam methane reforming process (SMR). It was concluded that after comparing carbon dioxide emission intensities across different types of projects, the type of project that would be most heavily impacted by greenhouse gas emissions penalties was an in-situ extraction with an upgrading project that employed gasification technology. 36 refs., 5 tabs., 12 figs., 1 appendix.

Cerro Negro bitumen degradation by a consortium of marine benthic microorganisms

Energy Technology Data Exchange (ETDEWEB)

Potter, T.L.; Duval, B. [USDA-ARA, Tifton, GA (USA). Southeast Watershed Research Laboratory

2001-01-01

Cerro Negro bitumen, separated from an Orimulsion sample, was incubated for up to 120 days with sediments collected at a petroleum-impacted site in Tampa Bay, Florida. Biodegradation conditions were optimized by increasing bitumen surface area, continuous agitation on a shaker apparatus, use of a complete growth medium, and maintenance at 37{degree}C. Aerobic degradation conditions were promoted by maintaining sediment contact with the laboratory atmosphere. Bitumen recovered in solvent extracts when compared to autoclaved controls decreased by up to 40% during the first 56 days. There was no detectable change after this. Molasses addition and use of a culture enriched from the sediments did not change the extent or rate of decrease in bitumen recovery. Chemical fractionation of bitumen control and degraded bitumen showed that aromatic and aliphatic fractions were depleted by {approx} 50%. Accumulation of polars was observed; however, the apparent increase was relatively small when compared to the mass loss of the other fractions. Selected biomarker ratios were not affected by incubation indicating their utility for fingerprinting the source bitumen in environmental samples. PAH distribution in the aromatic fraction favored the higher alkyl-homologues with the relative degree of alkylation increasing as the mass of bitumen recovered decreased with degradation. The study showed that up to 40% of the bitumen was bioaccessible and that bioremediation may be a treatment option for sediments contaminated with bitumen by an Orimulsion spill. 36 refs., 8 figs., 5 tabs.

Oil sands: Strategies for future development - An overview

International Nuclear Information System (INIS)

Yildirim, E.

1995-01-01

The Alberta Chamber of Resources developed a Task Force in 1993 to promote oil sands development, and to identify and publicize the social and economic benefits of oil sands operations. Formation, mission of the National Task Force, impediments and opportunities for development were summarized. Attributes of oil sands, benefits of their development, impediments to development, strategic development and potential growth scenarios were discussed. Cooperation between government and industry was deemed essential. Recommendations included development of a bitumen pipeline network, provision of incentives to encourage development, encouragement of risk and reward sharing between bitumen producers and up graders, and diversification of products and by-products. 7 figs., 12 refs

Developing new markets for oil sands products

International Nuclear Information System (INIS)

Crandall, G.

2004-01-01

This paper presents a review by Purvin and Gertz of western Canadian crude oil supply. This energy consulting firm provides advise to the energy sector. It suggests that oil sands production will surpass declining conventional production. Oil sands supply includes bitumen, synthetic crude oil (SCO), and diluent. It is forecasted that oil sands will increase from 42 per cent of western supply in 2002 to 78 per cent in 2015. The potential of Alberta's oil sands was discussed along with a recent study of refined products and petrochemicals from bitumen. Upgrading, refining and petrochemical case studies were presented. The author examined if a Canadian oil sands upgrading project with high capital costs can be competitive with competing projects in the United States and internationally. In addition to supply and demand issues, the presentation examined infrastructure capability and market potential in the United States. The economic potential and risks of preferred business cases compared to upgrading to SCO were also evaluated. 15 figs

Research on the technology of constructing a protection with joint use of no-fines concrete and bitumen

Directory of Open Access Journals (Sweden)

Mikhasek Andrey

2017-01-01

Full Text Available To build a bank slope protection of a hydraulic structure, a technology is proposed that involves building a framework of no-fines concrete and pouring it with hot bituminous materials. Implementation of this technology requires conducting a research on bitumen penetration into the protection plate body. The research involved developing models of non-stationary filtration under varied bitumen viscosity. The research involved experimental observation in laboratory environment. Models of movement of a variable viscosity liquid in a porous medium were proposed, and their study in laboratory environment allowed for identifying the depth of penetration, which is an important result to solve engineering objectives.

Asian-Pacific markets : a new strategy for Alberta oil

International Nuclear Information System (INIS)

Laureshen, C.J.; Du Plessis, D.; Xu, C.M.; Chung, K.H.

2004-01-01

Alberta's oil sands contain an estimated crude bitumen-in-place of nearly 2.5 trillion barrels. Production has increased to the point where it has overtaken non-conventional sources, and is expected to reach more than 2 million barrels per day by 2012, and over 5 million barrels per day by 2030. Although it is assumed that most of this production will be marketed in the United States, the industry is facing many constraints that could affect potential crude oil production and existing market share. The Asian-Pacific region is an obvious new market for Canadian heavy oil and bitumen due to an increasing demand for petroleum products in that region and the potential for reaching the California market with the same pipeline. This paper examined the following three criteria that will determine the success of any initiative to move Canadian crude oil to Asian-Pacific markets: (1) a sustainable supply of crude from Alberta; a pipeline to transport the crude to a deepwater port on the west coast; and, a guaranteed market at the other end. The feasibility of marketing Alberta heavy oil and bitumen to Asia was also discussed. 12 refs., 1 tab., 8 figs

Improvement of mineral oil saturated and aromatic hydrocarbons determination in edible oil by liquid-liquid-gas chromatography with dual detection.

Science.gov (United States)

Zoccali, Mariosimone; Barp, Laura; Beccaria, Marco; Sciarrone, Danilo; Purcaro, Giorgia; Mondello, Luigi

2016-02-01

Mineral oils, which are mainly composed of saturated hydrocarbons and aromatic hydrocarbons, are widespread food contaminants. Liquid chromatography coupled to gas chromatography with flame ionization detection represents the method of choice to determine these two families. However, despite the high selectivity of this technique, the presence of olefins (particularly squalene and its isomers) in some samples as in olive oils, does not allow the correct quantification of the mineral oil aromatic hydrocarbons fraction, requiring additional off-line tools to eliminate them. In the present research, a novel on-line liquid chromatography coupled to gas chromatography method is described for the determination of hydrocarbon contamination in edible oils. Two different liquid chromatography columns, namely a silica one (to retain the bulk of the matrix) and a silver-ion one (which better retains the olefins), were coupled in series to obtain the mineral oil aromatic hydrocarbons hump free of interfering peaks. Furthermore, the use of a simultaneous dual detection, flame ionization detector and triple quadrupole mass spectrometer allowed us not only to quantify the mineral oil contamination, but also to evaluate the presence of specific markers (i.e. hopanes) to confirm the petrogenic origin of the contamination. © 2015 WILEY-VCH Verlag GmbH & Co. KGaA, Weinheim.

Biodegradation of hydrocarbon compounds in Agbabu natural bitumen

African Journals Online (AJOL)

Infrared spectral changes and gravimetric analysis from the preliminary biodegradability study carried out on Agbabu Natural Bitumen showed the vulnerability of the bitumen to some bacteria: Pseudomonas putrefaciens, Pseudomonas nigrificans, Bacillus licheniformis, Pseudomonas fragi and Achromobacter aerogenes.

The Making of a Liquid Soap Process From Used Wasted Cooking Oil and Coconut Oil Mixture

OpenAIRE

S.T., M.T., Zulkarnain

2011-01-01

This Moment, used frying oil has not been used well and only used discarded as household waste or industrial. Therefore, to use of used frying oil as raw material a liquid soap will provide added value for used frying oil. The main purpose of this research is to cultivative used frying oil become a liquid soap way saponification with potassium hidroxide . This research do with variation feed ratio that is used frying oil and coconut oil (0:1; 0,5:1; 1:1; 1,5:1; and 2:1) and time of saponifica...

Preliminary fingerprinting analysis of Alberta oil sands and related petroleum products

International Nuclear Information System (INIS)

Yang, C.; Wang, Z.D.; Hollebone, B.; Brown, C.E.; Yang, Z.Y.; Landriault, M.; Fieldhouse, B.

2009-01-01

This paper reported on a study that presented a preliminary quantitative chemical characterization of Alberta oil sands and many other related Alberta oils such as oil sand bitumen, Cold Lake bitumen, Albian heavy synthetic crude, and Alberta Mixed sweet blend. The rapid increase in production of the Alberta oil sands has resulted in unprecedented environmental concern. The mining, extraction and production of oil sands such resulted in huge consumption of water resources, huge emission of greenhouse gas and large number of tailings ponds. In addition, accidental spills in the transportation and usage of oil sands will potentially cause considerable impact on the environment. It is therefore essential to have the ability to characterize Alberta oil sands and their oil products. The specific chemical properties of the oil sands bitumen must be known. Therefore, this study collected quantitative data on the concentration and distribution profiles of target compounds in Alberta oil sands and its petroleum products. The chemical fingerprints of 5 Alberta oil sands and their related petroleum products were studied using gas chromatography/flame ionization detection (GC/FID) and gas chromatography/mass spectrometry (GC/MS). The characterized hydrocarbons were n-alkanes; target alkylated PAHs and other EPA priority PAHs; biomarker terpanes and steranes; and bicyclic sesquiterpanes. The information acquired during this study will provide the basis for oil-oil correlation and differentiation in future environmental applications relevant to oil sands. 24 refs., 6 tabs., 4 figs.

The development of polyurethane modified bitumen emulsions for cold mix applications

OpenAIRE

Carrera Páez, Virginia; Cuadri Vega, Antonio Abad; García Morales, Moisés; Partal López, Pedro

2015-01-01

Bitumen emulsions stand for an alternative paving practice to the traditional hot-mix asphalts. In addition, modified bitumen emulsions show a better performance than unmodified ones. This work studies the feasibility of obtaining polyurethane modified bitumen emulsions, in which an isocyanate-functionalized polyol constitutes the bitumen modifier (in varying concentration from 1 to 4 wt.%). Storage stability and high in-service performance are evaluated by means of evolution of droplet size ...

Leaching studies on ion exchange resins immobilized in bitumen matrix

International Nuclear Information System (INIS)

Grosche Filho, C.E.; Chandra, U.; Villalobos, J.P.

1986-01-01

Many samples of bitumen mixed with ion exchange resin labelled with 134 Cs were prepared to study radionuclide leaching from bitumen waste forms. The resins used in tests were nuclear grade mixed cationic/aniocic bead resins. Different bitumen types were assayed: two distilled and two oxidized bitumens. Leached fractions were collected accordingly to the recommendation of ISO method, with complete exchange of leachant after each sampling. The volume collected for analysis was one liter. Marinelli beckers were used to improve counting efficiency in a Ge(Li) detector. The diffusion coefficients for samples prepared with distilled and oxidized bitumens were obtained. Mathematical models of transport phenomena applied to cylindrical geometry was employed to fit experimental data aiming to explain leaching mechanism and predict the long time behavior of immobilized radionuclides. (M.C.K.) [pt

Routine Testing of Bitumen Binders

Science.gov (United States)

Holý, Michal; Remišová, Eva

2017-12-01

The quality of bituminous binders used in the construction and maintenance of road surfaces is currently assessed by empirical testing based on obtaining one value for specific boundary conditions, which were designed about 100 years ago. Basic empirical tests include the softening point and penetration, but the practice shows that these tests appear to be inadequate. The evaluation of changes of bitumen properties during the production and paving process of bituminous mixture is also important. The paper points out how the "traditional" tests as softening point and penetration and viscosity are sufficient to evaluate properties of bitumen binders.

Oxidative Desulfurization of Fuel Oil by Pyridinium-Based Ionic Liquids

OpenAIRE

Erhong Duan; Dishun Zhao; Yanan Wang

2009-01-01

In this work, an N-butyl-pyridinium-based ionic liquid [BPy]BF4 was prepared. The effect of extraction desulfurization on model oil with thiophene and dibenzothiophene (DBT) was investigated. Ionic liquids and hydrogen peroxide (30%) were tested in extraction-oxidation desulfurization of model oil. The results show that the ionic liquid [BPy]BF4 has a better desulfurization effect. The best technological conditions are: V(IL)/V(Oil) /V(H2O2) = 1:1:0.4, temperature 55 °C, the time 30 min. The ...

Effects of Waste Plastic on the Physical and Rheological Properties of Bitumen

Science.gov (United States)

Ezree Abdullah, Mohd; Asyiqin Ahmad, Nurul; Putra Jaya, Ramadhansyah; Hassan, Norhidayah Abdul; Yaacob, Haryati; Rosli Hainin, Mohd

2017-05-01

Plastic disposal is one of the major problems for developing countries like Malaysia, at the same time Malaysia needs a large network of roads for its smooth economic and social development. The limited source of bitumen needs a deep thinking to ensure fast road construction. Therefore, the use of plastic waste in road construction not only can help to protect environment but also able to help the road construction industry. The aims of this research are to study the effects of waste plastic on rheological properties of bitumen. Modified bitumen was prepared by using blending techniques. Bitumen was heated and plastic waste was slowly added. Rheological properties of bitumen were performance by penetration, softening point, viscosity and direct shear rheometer test. The results showed that when content of plastic waste increase, the penetration value, softening point and viscosity of bitumen also increase. Generally, plastic waste improves the performance of bitumen when it was added into bitumen. It can be said that the usage helps to improve the performance of the road pavement which also reduces the rutting effect.

Geochemical characterization of the hydrous pyrolysis products from a recent cyanobacteria-dominated microbial mat

Energy Technology Data Exchange (ETDEWEB)

Franco, N.; Mendoça-Filho, J.G.; Silva, T.F.; Stojanovic, K.; Fontana, L.F.; Carvalhal-Gomes, S.B.V.; Silva, F.S.; Furukawa, G.G.

2016-07-01

Hydrous pyrolysis experiments were performed on a recent microbial mat sample from Lagoa Vermelha, Brazil, to determine whether crude oil can be generated and expelled during artificial maturation of the Organic Matter (OM). The experiments were conducted at 280ºC, 330ºC and 350ºC during 20h. Two types of liquid pyrolysis products, assigned as free oil and bitumen, were isolated and analyzed. Free oil represents free organic phase released by hydrous pyrolysis, whereas bitumen was obtained by extraction from the solid pyrolysis residue with dichloromethane. Changes in the OM maturity were determined using Rock-Eval parameters and biomarker maturity ratios of original sample and pyrolysis products. Biomarker compositions of original sample extract and liquid pyrolysates were used for determination of dominant bacterial source. The yields of free oil and bitumen showed that a microbial mat OM has a high liquid hydrocarbons generation potential. Rock-Eval maturity parameters, biopolymer and biomarker compositions indicate a significant increase of the OM maturity during hydrous pyrolysis. At 280ºC the release of free, adsorbed and occluded compounds was observed; however, without a cracking of the OM. At 330ºC the generation of bitumen and free oil is mostly related to the OM cracking. The highest yield of free oil was recorded at this temperature. Distribution of biomarkers in the extract of original sample and liquid pyrolysates confirms cyanobacteria-dominated microbial mats, whereas the identification of long chain n-alkane series, with maximum at C26, and prominent C30 hop-17(21)-ene additionally suggest the presence of sulfate reducing bacteria. (Author)

Molecular weight distribution of Athabasca bitumen

Energy Technology Data Exchange (ETDEWEB)

Champagne, P J; Manolakis, E; Ternan, M

1985-03-01

A sample of whole Athabasca bitumen has been fractionated by preparative g.p.c. The weights of the fractions have been determined and their molecular weights measured by several methods. In contras to previously published data, consistent results were obtained using different solvents (THF, benzene/water) and using different techniques (v.p.o., f.p.d. and g.c.-m.s.). This has resulted in a accurate definition of the molecular weight distribution of Athabasca bitumen.

Rheological modification of bitumens with new poly-functionalized furfural analogs

Energy Technology Data Exchange (ETDEWEB)

Alejandro Martinez; Antonio Paez; Nazario Martin [Universidad Complutense, Madrid (Spain). Departamento de Quimica Organica

2008-06-15

The rheological properties of bitumens modified with different aldehydes show that furfural is a very efficient reagent. An optimization of the reaction conditions involving concentration, acid catalyst, reaction time and temperature has been performed. In order to determine the influence of the furan ring and the formyl groups on the reactivity of bitumens, a series of new organic molecules as chemical reagents bearing up to six furan rings and four formyl groups, have been reacted with a B 80/100 bitumen. The results indicate a remarkably better performance than furfural, leading to harder modified bitumens. 31 refs., 3 figs., 5 tabs.

Irradiation tests on bitumen and bitumen coated materials; Essais d'irradiation de bitume et d'enrobes bitumineux

Energy Technology Data Exchange (ETDEWEB)

Tabardel-Brian, R.; Rodier, J.; Lefillatre, G. [Commissariat a l' Energie Atomique, Chusclan (France). Centre de Production de Plutonium de Marcoule

1969-07-01

The use of bitumen as a material for coating high-activity products calls for prior study of the resistance of bitumen to irradiation. After giving briefly the methods of preparation of bitumen- coated products, this report lists the equipment which has been used for carrying out the {beta} and {gamma} irradiations of these products, and gives the analytical results obtained as a function of the dose rates chosen and of the total integrated dose. Finally, some conclusions have been drawn concerning the best types of bitumen. It should be stressed that some bitumens apparently underwent no degradation whatsoever nor any volume increase, for a total integrated dose of 1.8 x 10{sup 10} rads. (authors) [French] Dans le cadre de l'enrobage par le bitume des produits de haute activite, il est necessaire de verifier au prealable, la tenue du bitume a l'irradiation. Apres un bref rappel de la preparation des enrobes bitumineux, le present rapport regroupe les moyens qui ont ete mis en oeuvre, pour effectuer leurs irradiations sous rayonnement {beta} et sous rayonnement {gamma}, ainsi que les resultats des analyses qui ont ete faites en fonction des debits de doses choisis et de la dose totale integree. Enfin, des conclusions ont ete tirees sur les types de bitume a retenir. On peut souligner que certains bitumes n'ont subi aucune degradation apparente ni augmentation de volume pour une dose totale integree de 1.8 x 10{sup 10} rads. (auteurs)

BioDiesel as Additive in High Pressure and Temperature Steam Recovery of Heavy Oil and Bitumen Utilisation d’un biogazole comme additif pour la récupération d’huile lourde et de bitume par injection de vapeur à hautes pression et température

Directory of Open Access Journals (Sweden)

Babadagli T.

2012-05-01

Full Text Available Use of additives to improve the efficiency of thermal heavy oil and bitumen recovery processes has been studied extensively over the decades. Two common types of additives used in thermal applications, mainly steam assisted recovery, are solvents and surfactants. Commercial use of solvents has setbacks due to their high costs and retrieval difficulties. Cost and stability of the surfactants under reservoir operating temperature and pressure are the major concerns. We propose the use of bioDiesel such as fatty acids methyl ester as a surfactant additive reducing heavy oil/bitumen-water interfacial tension in steam assisted recovery processes. Advantages of using bioDiesel as a surfactant additive are that bioDiesel is chemically stable under the operating pressure and temperature of the reservoir, it causes no harm on bitumen fuel quality and on release water chemistry and its use is economically feasible. We conducted a series of steam assisted bitumen recovery experiments to clarify the additional recovery potential and efficiency improvement capacity of bioDiesel. High pressure steam at 1.8 MPa pressure, 205°C was used in these tests at a 900 g/h feed rate. The porous media used was a normal grade oil sands ore obtained from a surface mine operation in Northern Alberta, Canada. Oil sands ore was packed in a basket and placed in a high pressure cell. Bitumen recovery experiments were performed by spraying canola oil fatty acid methyl ester on oil sands ore at a 2 g/kg-bitumen dosage. These tests show that bitumen recovery efficiency increases over 40%. In another series of tests, tall oil fatty acids methyl ester was injected into a high pressure steam line at a 8.3 g-bioDiesel/kg-steam dosage. Because of the solubility of bioDiesel in bitumen, the effect of bioDiesel on bitumen recovery could not be accurately concluded. Vapor pressure measurements performed on canola oil and tall oil derived bioDiesel samples suggest that saturation

The extraction of bitumen from western oil sands

International Nuclear Information System (INIS)

Oblad, A.G.; Bunger, J.W.; Dahlstrom, D.A.; Deo, M.D.; Hanson, F.V.; Miller, J.D.; Seader, J.D.

1992-08-01

The University of Utah tar sand research and development program is concerned with research and development on Utah is extensive oil sands deposits. The program has been intended to develop a scientific and technological base required for eventual commercial recovery of the heavy oils from oil sands and processing these oils to produce synthetic crude oil and other products such as asphalt. The overall program is based on mining the oil sand, processing the mined sand to recover the heavy oils and upgrading them to products. Multiple deposits are being investigated since it is believed that a large scale (approximately 20,000 bbl/day) plant would require the use of resources from more than one deposit. The tasks or projects in the program are organized according to the following classification: Recovery technologies which includes thermal recovery methods, water extraction methods, and solvent extraction methods; upgrading and processing technologies which covers hydrotreating, hydrocracking, and hydropyrolysis; solvent extraction; production of specialty products; and environmental aspects of the production and processing technologies. These tasks are covered in this report

US crude oil, natural gas, and natural gas liquids reserves

International Nuclear Information System (INIS)

1992-01-01

This report presents estimates of proved reserves of crude oil, natural gas, and natural gas liquids as of December 31, 1991, as well as production volumes for the United States, and selected States and State subdivisions for the year 1991. Estimates are presented for the following four categories of natural gas: total gas (wet after lease separation), its two major components (nonassociated and associated-dissolved gas), and total dry gas (wet gas adjusted for the removal of liquids at natural gas processing plants). In addition, two components of natural gas liquids, lease condensate and natural gas plant liquids, have their reserves and production data presented. Also included is information on indicated additional crude oil reserves and crude oil, natural gas, and lease condensate reserves in nonproducing reservoirs. A discussion of notable oil and gas exploration and development activities during 1991 is also presented

Thermophysical properties of biodiesel and related systems: (Liquid + liquid) equilibrium data for castor oil biodiesel

International Nuclear Information System (INIS)

Mazutti, Marcio A.; Voll, Fernando A.P.; Cardozo-Filho, Lúcio; Corazza, Marcos L.; Lanza, Marcelo; Priamo, Wagner L.; Oliveira, J. Vladimir

2013-01-01

Highlights: ► (Liquid + liquid) equilibrium data for multicomponent castor oil FAME and FAEE castor oil. ► Tie-lines and solubility curves (binodal) by cloud-point method for FAME and FAEE systems. ► Experimental data correlated using the UNIQUAC model. -- Abstract: This work reports new liquid–liquid solubility values (binodal curves) as well as (liquid + liquid) equilibrium data for, ternary and quaternary systems containing fatty acid methyl esters (FAME) and fatty acid ethyl esters (FAEE) from castor oil, water, glycerol, methanol and anhydrous ethanol at T = (303.15, 318.15, and 333.15) K. Solubility curves (binodal) were also obtained by the cloud-point method for binary systems containing FAME, FAEE, water, or glycerol. All results obtained can be considered of good quality. The experimental values were correlated using the UNIQUAC model, whose results presented good performance and satisfactory fitting of equilibrium values

Non-Newtonian behavior and molecular structure of Cooee bitumen under shear flow

DEFF Research Database (Denmark)

Lemarchand, Claire; Bailey, Nicholas; Daivis, Peter

2015-01-01

The rheology and molecular structure of a model bitumen (Cooee bitumen) under shear are investigated in the non-Newtonian regime using non-equilibrium molecular dynamics simulations. The shear viscosity, normal stress differences, and pressure of the bitumen mixture are computed at different shear...... rates and different temperatures. The model bitumen is shown to be a shear-thinning fluid at all temperatures. In addition, the Cooee model is able to reproduce experimental results showing the formation of nanoaggregates composed of stacks of flat aromatic molecules in bitumen. These nanoaggregates...

Shale oil. I. Genesis of oil shales and its relation to petroleum and other fuels

Energy Technology Data Exchange (ETDEWEB)

McKee, R H; Manning, P D.V.

1927-01-01

Oil-shale kerogen originated from resinous vegetation residues of past eras, whereas well petroleum was formed from oil shales by pressure and mild heat. Petroleum migrated to its present reservoir from neighboring oil-shale deposits, leaving a residue of black bituminous shales. The high carbon dioxide content of gases present in petroleum wells originated from kerogen, as it gives off carbon dioxide gas before producing soluble oil or bitumen.

Future directions conventional oil supply, Western Canada

International Nuclear Information System (INIS)

Campbell, G.R.; Hayward, J.

1997-01-01

The history of the Canadian oil industry was briefly sketched and the future outlook for crude oil and natural gas liquids in western Canada was forecast. The historical review encompassed some of the significant events in history of the Canadian oil industry, including the Leduc discovery in 1947, the Swan Hills discovery in 1957, the start of commercial production from the Athabasca oil sands in 1967, the discovery of the Hibernia oilfield offshore Newfoundland in 1979, and the onset of the use of horizontal production wells in western Canada in 1987. The resource base, supply costs, and the technology that is being developed to reduce costs and to improve recovery, were reviewed. Future oil prices were predicted, taking into account the costs associated with technological developments. It was suggested that the character of the industry is undergoing a change from an industry dominated by conventional supply to a mixed industry with increasing volume of heavy oil, primary bitumen, synthetic oil and frontier supply replacing 'conventional' light crude oil. Projections into the future are subject to uncertainty both on the supply as well as on the demand side. The potential impact of technology can significantly affect demand, and technological developments can yield additional supplies which exceed current expectations. 10 figs

Comparison between different liquid-liquid and solid phase methods of extraction prior to the identification of the phenolic fraction present in olive oil washing wastewater from the two-phase olive oil extraction system

Directory of Open Access Journals (Sweden)

S. Jiménez-Herrera

2017-09-01

Full Text Available Phenolic compounds from olive mill wastewater (OMW, are characterized by a strong antioxidant activity. At the same time, they represent an environmental problem because they are difficult to degrade. The purpose of this work was to identify these biologically active compounds in the OMW from two-phase olive oil production in order to convert a polluting residue into a source of natural antioxidants. After optimizing the extraction process of phenolic compounds using liquid-liquid extraction (LLE and solid phase extraction (SPE methods, it was determined that the most appropriate sequence comprised a previous centrifugation to remove the lipid fraction, followed by liquid extraction with ethyl acetate or SPE. The most important compounds identified in olive oil washing wastewater (OOWW were tyrosol, hydroxytyrosol and succinic acid; whereas the ones in the wastewater derived from the washing of the olives (OWW were cresol, catechol, 4-methylcatechol, hydrocinnamic acid and p-hydroxy-hydrocinnamic acid.

Comparison between different liquid-liquid and solid phase methods of extraction prior to the identification of the phenolic fraction present in olive oil washing wastewater from the two-phase olive oil extraction system

International Nuclear Information System (INIS)

Jiménez-Herrera, S.; Ochando-Pulido, J.M.; Martínez-Ferez, A.

2017-01-01

Phenolic compounds from olive mill wastewater (OMW), are characterized by a strong antioxidant activity. At the same time, they represent an environmental problem because they are difficult to degrade. The purpose of this work was to identify these biologically active compounds in the OMW from two-phase olive oil production in order to convert a polluting residue into a source of natural antioxidants. After optimizing the extraction process of phenolic compounds using liquid-liquid extraction (LLE) and solid phase extraction (SPE) methods, it was determined that the most appropriate sequence comprised a previous centrifugation to remove the lipid fraction, followed by liquid extraction with ethyl acetate or SPE. The most important compounds identified in olive oil washing wastewater (OOWW) were tyrosol, hydroxytyrosol and succinic acid; whereas the ones in the wastewater derived from the washing of the olives (OWW) were cresol, catechol, 4-methylcatechol, hydrocinnamic acid and p-hydroxy-hydrocinnamic acid. [es

EFFECT OF HYDROGENATED, LIQUID AND GHEE OILS ON SERUM LI-PIDS PROFILE

Directory of Open Access Journals (Sweden)

Noushin Mohammadifard

2010-11-01

Full Text Available BACKGROUND: Trans fatty acids are known as the most harmful type of dietary fats, so this study was done to compare the effects of hydrogenated, liquid and ghee oils on serum lipids profile of healthy adults.    METHODS: This study was a randomized clinical trial conducted on 129 healthy participants aged from 20 to 60 years old who were beneficiaries of Imam-e-Zaman charitable organization. Subjects were randomly divided into 3 groups and each group was treated with a diet containing cooking and frying liquid, ghee, or hydrogenated for 40 days. Fasting serum lipids, including total cholesterol (TC, triglyceride (TG, LDL-cholesterol (LDL-C, HDL-cholesterol (HDL-C, apoprotein A (Apo A, and apoprotein B (Apo B were measured before and after the study.    RESULTS: TC, TG and Apo B had a significant reduction in the liquid oil group compared to the hydrogenated oil group. In the ghee group TG declined and Apo A increased significantly (p < 0.01. Liquid oil group had a significant reduction in HDL-C, compared to the ghee oil group (P < 0.05.     CONCLUSION: It was concluded that consuming liquid oil along with frying oil caused to reduce all serum lipid levels. However, ghee oil only reduced TG and increased HDL-C levels.      Keywords: Serum lipids, Apoproteins, Liquid oil, Hydrogenated oil, Ghee, Clinical trial

Assessment of Physicochemical Properties of some Bitumens from ...

African Journals Online (AJOL)

Assessment of the results vis-a-vis available information on bitumens elsewhere indicate that any clear surface or underground natural bitumen obtainable in the region of Agbabu village in Ondo State, and a manufactured type from Kaduna Refining and Petrochemical Company (KRPC) in the country are comparable with ...

Characteristics of gas-liquid dynamics in operation of oil fields producing non-Newtonian crude oils

Energy Technology Data Exchange (ETDEWEB)

Mirzadzhanzade, A Kh; Khasaev, A M; Gurbanov, R S; Akhmedov, Z M

1968-08-01

Experimental studies have shown that crude oils from Azerbaidzhan, Uzbekistan, Tataria, Kazakhstan and other areas have anomalous properties under reservoir conditions. Such crude oils are non-Newtonian and (1) obey Darcys Law at low velocities; (2) obey an exponential law at higher velocities; and (3) obey a modified Darcys Law at most velocities. A discussion is given of (1) flow of non-Newtonian crude oils together with gas or water; (2) flow of non-Newtonian crude oils in well tubing; (3) behavior of wells producing non-Newtonian crude oils; and (4) pumping of non-Newtonian oils in wells. Experiments have shown that a visco-plastic liquid does not fill pump inlets completely; as the diameter of the pump inlet decreases so also does the degree of liquid filling. A statistical analysis of production data from 160 fields with Newtonian oil and 129 fields with non- Newtonian oil has shown that much higher production is obtained from fields with Newtonian crude oils.

Petroleum.

Science.gov (United States)

McManus, T. R.; And Others

1989-01-01

This review of petroleum covers: crude oil; fuels, gaseous and liquid; lubricants, oils, and greases; asphalts, bitumens, tars, and pitches; hydrocarbons; physical properties; metals in oil; nonmetallic elements and heterocompounds; and analytical methods and apparatus. (MVL)

Complexation of Cu2+, Ni2+ and UO22+ by radiolytic degradation products of bitumen

International Nuclear Information System (INIS)

Loon, L.R. Van; Kopajtic, Z.

1990-05-01

The radiolytic degradation of bitumen was studied under conditions which reflect those which will exist in the near field of a cementitious radioactive waste repository. The potential complexation capacity of the degradation products was studied and complexation experiments with Cu 2+ , Ni 2+ and UO 2 2+ were performed. In general 1:1 complexes with Cu 2+ , Ni 2+ and UO 2 2+ , with log K values of between 5.7 and 6.0 for Cu 2+ , 4.2 for Ni 2+ and 6.1 for UO 2 2+ , were produced at an ionic strength of 0.1 M. The composition of the bitumen water was analysed by GC-MS and IC. The major proportion of the bitumen degradation products in solution were monocarboxylic acids (acetic acid, formic acid, myric acid, stearic acid ...), dicarboxylic acids (oxalic acid, phthalic acid) and carbonates. The experimentally derived log K data are in good agreement with the literature and suggest that oxalate determines the speciation of Cu 2+ , Ni 2+ and UO 2 2+ in the bitumen water below pH=7. However, under the high pH conditions typical of the near field of a cementitious repository, competition with OH-ligands will be large and oxalate, therefore, will not play a significant role in the speciation of radionuclides. The main conclusion of the study is that the radiolytic degradation products of bitumen will have no influence on radionuclide speciation in a cementitious near field and, as such, need not to be considered in the appropriate safety assessment models. (author) 12 figs., 11 tabs., 31 refs

Oxidative desulfurization of fuel oil by pyridinium-based ionic liquids.

Science.gov (United States)

Zhao, Dishun; Wang, Yanan; Duan, Erhong

2009-10-28

In this work, an N-butyl-pyridinium-based ionic liquid [BPy]BF(4) was prepared. The effect of extraction desulfurization on model oil with thiophene and dibenzothiophene (DBT) was investigated. Ionic liquids and hydrogen peroxide (30%) were tested in extraction-oxidation desulfurization of model oil. The results show that the ionic liquid [BPy]BF(4) has a better desulfurization effect. The best technological conditions are: V(IL)/V(Oil) /V(H(2)O(2)) = 1:1:0.4, temperature 55 degrees C, the time 30 min. The ratio of desulfurization to thiophene and DBT reached 78.5% and 84.3% respectively, which is much higher than extraction desulfurization with simple ionic liquids. Under these conditions, the effect of desulfurization on gasoline was also investigated. The used ionic liquids can be recycled up to four times after regeneration.

Oxidative Desulfurization of Fuel Oil by Pyridinium-Based Ionic Liquids

Directory of Open Access Journals (Sweden)

Erhong Duan

2009-10-01

Full Text Available In this work, an N-butyl-pyridinium-based ionic liquid [BPy]BF4 was prepared. The effect of extraction desulfurization on model oil with thiophene and dibenzothiophene (DBT was investigated. Ionic liquids and hydrogen peroxide (30% were tested in extraction-oxidation desulfurization of model oil. The results show that the ionic liquid [BPy]BF4 has a better desulfurization effect. The best technological conditions are: V(IL/V(Oil /V(H2O2 = 1:1:0.4, temperature 55 °C, the time 30 min. The ratio of desulfurization to thiophene and DBT reached 78.5% and 84.3% respectively, which is much higher than extraction desulfurization with simple ionic liquids. Under these conditions, the effect of desulfurization on gasoline was also investigated. The used ionic liquids can be recycled up to four times after regeneration.

Liquid fuels from Canadian coals

Energy Technology Data Exchange (ETDEWEB)

Taylor, G. W.

1979-06-15

In Canadian energy planning, the central issue of security of supply must be addressed by developing flexible energy systems that make the best possible use of available resources. For liquid fuel production, oil sands and heavy oil currently appear more attractive than coal or biomass as alternatives to conventional crude oil, but the magnitude of their economic advantage is uncertain. The existence of large resources of oil sands, heavy oils, natural gas and low-sulfur coals in Western Canada creates a unique opportunity for Canadians to optimize the yield from these resources and develop new technology. Many variations on the three basic liquefaction routes - hydroliquefaction, pyrolysis and synthesis - are under investigation around the world, and the technology is advancing rapidly. Each process has merit under certain circumstances. Surface-mineable subbituminous and lignite coals of Alberta and Saskatchewan appear to offer the best combination of favorable properties, deposit size and mining cost, but other deposits in Alberta, Nova Scotia and British Columbia should not be ruled out. The research effort in Canada is small by world standards, but it is unlikely that technology could be imported that is ideally suited to Canadian conditions. Importing technology is undesirable: innovation or process modification to suit Canadian coals and markets is preferred; coprocessing of coal liquids with bitumen or heavy oils would be a uniquely Canadian, exportable technology. The cost of synthetic crude from coal in Canada is uncertain, estimates ranging from $113 to $220/m/sup 3/ ($18 to $35/bbl). Existing economic evaluations vary widely depending on assumptions, and can be misleading. Product quality is an important consideration.

Experimental investigation of the role of rock fabric in gas generation and expulsion during thermal maturation: Anhydrous closed-system pyrolysis of a bitumen-rich Eagle Ford Shale

Science.gov (United States)

Shao, Deyong; Ellis, Geoffrey S.; Li, Yanfang; Zhang, Tongwei

2018-01-01

Gold-tube pyrolysis experiments were conducted on miniature core plugs and powdered rock from a bitumen-rich sample of Eagle Ford Shale to investigate the role of rock fabric in gas generation and expulsion during thermal maturation. The samples were isothermally heated at 130, 300, 310, 333, 367, 400, and 425 °C for 72 h under a confining pressure of 68.0 MPa, corresponding to six levels of induced thermal maturity: pre-oil generation (130 °C/72 h), incipient oil/bitumen generation (300 and 310 °C/72 h), early oil generation (333 °C/72 h), peak oil generation (367 °C/72 h), early oil cracking (400 °C/72 h), and late oil cracking (425 °C/72 h). Experimental results show that gas retention coupled with compositional fractionation occurs in the core plug experiments and varies as a function of thermal maturity. During the incipient oil/bitumen generation stage, yields of methane through pentane (C1–C5) from core plugs are significantly lower than those from rock powder, and gases from core plugs are enriched in methane. However, the differences in C1–C5 gas yield and composition decrease throughout the oil generation stage, and by the oil cracking stage no obvious compositional difference in C1–C5 gases exists. The decrease in the effect of rock fabric on gas yield and composition with increasing maturity is the result of an increase in gas expulsion efficiency. Pyrolysis of rock powder yields 4–16 times more CO2 compared to miniature core plugs, with δ13CCO2 values ranging from −2.9‰ to −0.6‰, likely due to carbonate decomposition accelerated by reactions with organic acids. Furthermore, lower yields of gaseous alkenes and H2 from core plug experiments sugge

Bitumen modified with recycled polyurethane foam for employment in hot mix asphalt

Directory of Open Access Journals (Sweden)

Miguel Ángel Salas

2018-01-01

Full Text Available A wide variety of modifiers have been applied to bitumen in order to enhance their properties and performance. Among them, polymers have been mainly used. The aim of this paper is to assess the use of polyurethane foam waste as a bitumen modifier for hot mix asphalts. The polyurethane foam is a by-product of the manufacturing of polyurethane for thermal insulation. From a bitumen with a penetration grade of 50/70, various samples with percentages of waste material in weight ranging from 1% to 5% were produced and tested. Samples with 5% of waste material or more became rough and were refused due to their poor workability. A bituminous mixture with modified bitumen with a 4% of polyurethane was manufactured and compared with a sample with the same aggregates and original bitumen. Results in Marshall test showed that a mix with polymer modified bitumen yielded improvements in stability and a lower deformability. This result suggests that the employment of polyurethane foam waste is a promising bitumen modifier, contributing also to recycle waste materials.

Financial oil derivatives: from options to oil warrants and synthetic oilfields

International Nuclear Information System (INIS)

Trabia, Xavier

1992-01-01

This study aims to shed light on some of the most interesting financial oil derivatives issued so far in order to assess the potential of this new wave of innovative funding instruments. In Part I some theoretical background is provided and applied to the problem of the American futures option. The ''binomial'' model for valuing future option contracts is presented and the most accurate alternatives for pricing American futures options are reviewed. The role of these numerical procedures in valuing more complex options involved in oil warrants is examined. Comments are made on the behaviour of volatility, which stands as a key interface between theory and practice in oil trading on the oil futures market. Part II of the study describes in detail some of the most famous new financial oil derivatives. Some final conclusions are drawn on the potential of oil trusts and synthetic oilfields to be involved in project and general funding in the oil industry. (44 figures, 11 tables, 53 references) (UK)

Methodology of calibration for nucleonic multiphase meter technology for SAGD extra heavy oil

Energy Technology Data Exchange (ETDEWEB)

Pinguet, B.; Pechard, P.; Guerra, E. [Schlumberger Canada Ltd., Calgary, AB (Canada); Arendo, V.; Shaffer, M.; Contreras, J. [Total, Paris (France)

2008-10-15

The challenges facing bitumen metering in steam assisted gravity drainage operations were discussed with reference to high operating temperatures, steam pressure in the gas phase, foaming, emulsion and small density differences between bitumen and produced water. A metering tool that can deal with these operating constraints was presented. The multiphase meter (MFM) uses a multi-energy gamma ray (nuclear fraction) meter together with a venturi tube to provide accurate monitoring and optimization of oil, water, gas and steam production. This paper presented the specific strengths of the MFM with emphasis on its ability to correctly meter the liquid/gas phases depending on the calibration method and operating measurement range. The paper presented a study of the main parameters which could influence the measurement associated with this technology. The study was based on practical and simulated data and evaluated the impact of changes in each parameter. The purpose of the paper was to improve the understanding of this technology and how to apply it to bitumen metering and provide a guideline of the technology for future users in the oil industry. It described the combination venturi-nucleonic measurement parameters, such as mass flow rate; fraction meter; solution triangle of the fraction meter; primary and secondary output; fluid properties information; and uncertainty associated to any technology. A sensitivity analysis study to identify the dependency to some key fluid parameters was also described. It was concluded that MFM can be used in a stand-alone configuration. 7 refs., 2 tabs., 22 figs.

Relation Between Bitumen Content and Percentage Air Voids in Semi Dense Bituminous Concrete

Science.gov (United States)

Panda, R. P.; Das, Sudhanshu Sekhar; Sahoo, P. K.

2018-06-01

Hot mix asphalt (HMA) is a heterogeneous mix of aggregate, mineral filler, bitumen, additives and air voids. Researchers have indicated that the durability of the HMA is sensitive on the actual bitumen content and percentage air void. This paper aims at establishing the relationship between the bitumen content and the percentage air voids in Semi Dense Bituminous Concrete (SDBC) using Viscosity Grade-30 (VG-30) bitumen. Total 54 samples have been collected, for formulation and validation of relationship and observed that the percentage air voids increases with decrease in actual bitumen content and vice versa. A minor increase in percentage air voids beyond practice of designed air voids in Marshall Method of design is required for better performance, indicating a need for reducing the codal provision of minimum bitumen content for SDBC as specified in Specification for Road & Bridges (Fourth Revision) published by Indian Road Congress, 2001. The study shows a possibility of reducing designed minimum bitumen content from codal provision for SDBC by 0.2% of weight with VG-30 grade of Bitumen.

Relation Between Bitumen Content and Percentage Air Voids in Semi Dense Bituminous Concrete

Science.gov (United States)

Panda, R. P.; Das, Sudhanshu Sekhar; Sahoo, P. K.

2018-02-01

Hot mix asphalt (HMA) is a heterogeneous mix of aggregate, mineral filler, bitumen, additives and air voids. Researchers have indicated that the durability of the HMA is sensitive on the actual bitumen content and percentage air void. This paper aims at establishing the relationship between the bitumen content and the percentage air voids in Semi Dense Bituminous Concrete (SDBC) using Viscosity Grade-30 (VG-30) bitumen. Total 54 samples have been collected, for formulation and validation of relationship and observed that the percentage air voids increases with decrease in actual bitumen content and vice versa. A minor increase in percentage air voids beyond practice of designed air voids in Marshall Method of design is required for better performance, indicating a need for reducing the codal provision of minimum bitumen content for SDBC as specified in Specification for Road & Bridges (Fourth Revision) published by Indian Road Congress, 2001. The study shows a possibility of reducing designed minimum bitumen content from codal provision for SDBC by 0.2% of weight with VG-30 grade of Bitumen.

Effect of waste polymer addition on the rheology of modified bitumen

Energy Technology Data Exchange (ETDEWEB)

M. Garcia-Morales; P. Partal; F.J. Navarro; C. Gallegos [Universidad de Huelva, Huelva (Spain). Departamento de Ingenieria Quimica, Facultad de Ciencias Experimentales

2006-05-15

This paper deals with the modification of petroleum bitumen with four different types of waste polymers. EVA, EVA/LDPE blend, crumb tire rubber and ABS, all of them coming from recycling plants of waste plastic materials, were used as modifying agents of the bitumen employed in the pavement building. Optical microscopy, modulated calorimetry and a set of different rheological tests were developed in order to characterise the modified bitumens. The results obtained reveal that tire rubber as well as its blends with other polymers can be considered as an interesting modifier of the bitumen in a wide range of temperatures. As an elastomer, it endows the pavement a higher flexibility, which makes it more resistant to the traffic loading. The blend composed of EVA and LDPE displays quite promising results at high in-service temperatures, due to the development of a polymer network throughout the modified bitumen. Furthermore, the calorimetry tests carried out demonstrate different degrees of compatibility between the bitumen and the polymers used. 45 refs., 8 figs., 3 tabs.

Response to heavy, non-floating oil spilled in a Great Lakes river environment: a multiple-lines-of-evidence approach for submerged oil assessment and recovery

Science.gov (United States)

Dollhopf, Ralph H.; Fitzpatrick, Faith A.; Kimble, Jeffrey W.; Capone, Daniel M.; Graan, Thomas P.; Zelt, Ronald B.; Johnson, Rex

2014-01-01

The Enbridge Line 6B pipeline release of diluted bitumen into the Kalamazoo River downstream of Marshall, MI in July 2010 is one of the largest freshwater oil spills in North American history. The unprecedented scale of impact and massive quantity of oil released required the development and implementation of new approaches for detection and recovery. At the onset of cleanup, conventional recovery techniques were employed for the initially floating oil and were successful. However, volatilization of the lighter diluent, along with mixing of the oil with sediment during flooded, turbulent river conditions caused the oil to sink and collect in natural deposition areas in the river. For more than three years after the spill, recovery of submerged oil has remained the predominant operational focus of the response. The recovery complexities for submerged oil mixed with sediment in depositional areas and long-term oil sheening along approximately 38 miles of the Kalamazoo River led to the development of a multiple-lines-of-evidence approach comprising six major components: geomorphic mapping, field assessments of submerged oil (poling), systematic tracking and mapping of oil sheen, hydrodynamic and sediment transport modeling, forensic oil chemistry, and net environmental benefit analysis. The Federal On-Scene Coordinator (FOSC) considered this information in determining the appropriate course of action for each impacted segment of the river. New sources of heavy crude oils like diluted bitumen and increasing transportation of those oils require changes in the way emergency personnel respond to oil spills in the Great Lakes and other freshwater ecosystems. Strategies to recover heavy oils must consider that the oils may suspend or sink in the water column, mix with fine-grained sediment, and accumulate in depositional areas. Early understanding of the potential fate and behavior of diluted bitumen spills when combined with timely, strong conventional recovery methods can

Probing Trace-elements in Bitumen by Neutron Activation Analysis

NARCIS (Netherlands)

Nahar, S.N.; Schmets, A.J.M.; Scarpas, Athanasios

Trace elements and their concentrations play an important role in both chemical and physical properties of bitumen. Instrumental Neutron Activation Analysis (INAA) has been applied to determine the concentration of trace elements in bitumen. This method requires irradiation of the material with

Vegetable oil based liquid nanocomposite dielectric

Directory of Open Access Journals (Sweden)

Leon Chetty

2013-01-01

Full Text Available Physically smaller dielectric materials would improve the optimisation of space for power systems. Development of nanotechnology provides an effective way to improve the performances of insulating oils used in power system applications. In this research study, we focused on the development of nanomodified vegetable oils to be used in power transformers. Higher conduction currents were observed in virgin linseed oil than in virgin castor oil. However, for both virgin linseed and virgin castor oil, the DC conduction current increased approximately linearly with the applied DC voltage. In nanomodified linseed oil, the characteristic curve showed two distinct regions: a linear region (at lower applied voltage and a saturation region (at slightly higher voltage. Conversely, in nanomodified castor oil, the characteristic curve showed three distinct regions: a linear region (at lower applied voltage, a saturation region (at intermediate applied voltage and an exponential growth region (at higher applied voltage. The nanomodified linseed oil exhibited a better dielectric performance than the nanomodified castor oil. Overall, the addition of nanodielectrics to vegetable oils decreased the dielectric performance of the vegetable oils. The results of this study contribute to the understanding of the pre-breakdown phenomenon in liquid nanocomposite dielectrics.

Greenhouse gases: How does heavy oil stack up?

International Nuclear Information System (INIS)

Ottenbreit, R.J.

1991-01-01

Life-cycle emissions of direct greenhouse gases (GHG) have been calculated to elucidate the global warming impacts of various fossil fuel feedstocks. Calculations were made for the transportation sector using five fossil fuel sources: natural gas, light crude oil, conventional heavy oil, crude bitumen recovered through in-situ steam stimulation, and crude bitumen recovered through mining. Results suggest that fuels sourced from light crude oil have the lowest GHG emissions, while conventional heavy oil has the highest GHG emission levels for this application. Emissions of methane can constitute a significant portion of the life-cycle GHG emissions of a fossil fuel. For all the fossil fuels examined, except conventional heavy oil, GHG emissions associated with their production, transport, processing, and distribution are less than one third of their total life-cycle emissions. The remainder is associated with end use. This confirms that consumers of fossil fuel products, rather than fossil fuel producers, have the most leverage to reduce GHG emissions. 2 figs

Investigation on the effects of gamma irradiation on bitumen

International Nuclear Information System (INIS)

Mello, M.S.; Braz, D.; Motta, L.M.G.

2011-01-01

Brazil has more than 218,000 km of asphalt-paved highways. Bitumen is a generic term for natural or manufactured black or dark-colored solid, semisolid, or viscous cementitious materials that are composed mainly of high molecular weight hydrocarbons (90-95%). Several papers have shown that the irradiation process has changed the mechanical behavior in some polymers. This work aims to analyze the behavior of Brazilian irradiated Bitumen (CAP 50-70). In order to provide a preliminary evaluation, bitumen samples and cylindrical specimens of asphaltic mixture were tested. The bitumen samples were irradiated 0.1 to 300 kGy, and asphaltic mixture specimen was irradiated 5 to 300 kGy. The cylindrical asphaltic mixture specimen of 10.16 cm diameter used in this study was molded using an asphalt-aggregate mixture. The specimens were irradiated in LIN/UFRJ/Brazil using a Gamma cell Co 60 source of gamma irradiation with an applied dose rate of 29.7 Gy/min. After irradiated, the bitumen samples were subjected to penetration test and the asphaltic mixtures were subjected to indirect tensile strength test (diametral compression) for determination of the resilient modulus, according to ASTM method D 4123. The results of these experiments for each dose were compared with the control (nonirradiated). As expected, the penetration results showed that the ratio (irradiated/non-irradiated) decreases with increasing of irradiation dose for bitumen samples and the resilient modulus results showed that the ratio (irradiated/non-irradiated) increases with increasing of irradiation dose for asphaltic mixture. (author)

Production acceleration and injectivity enhancement using steam-propane injection for Hamaca extra-heavy oil

Energy Technology Data Exchange (ETDEWEB)

Rivero, J. A.; Mamora, D. D. [Texas A and M University, El Paso, TX (United States)

2005-02-01

The possibility of enhanced recovery in the Orinoco Belt in Venezuela, the world's largest known hydrocarbon deposit, by using propane as a steam additive, is discussed. In a laboratory study the steam-propane injection accelerated the start of oil production by 21 per cent, compared to production with steam alone. The experiments illustrated that the inclusion of even small amounts of propane has considerable beneficial effect on the rate of bitumen production. Even though total bitumen recovery and ultimate residual oil saturation did not change, the acceleration of bitumen recovery is considered to have a significant impact on the net present value of the recovery process. 17 refs., 1 tab., 13 figs.

From oil sands to transportation fuels, to electricity, to hydrogen

International Nuclear Information System (INIS)

Yildirim, E.

1993-01-01

The Alberta Chamber of Resources programs and initiatives on oil sands and heavy oil, and strategies for revitalizing oilsands development in Alberta are described. The regional upgrader and satellite production facilities concept, and technology requirements for mineable oil sands by the year 2010 are discussed. Strategic alliances in furtherence of oil sands research and development and the National Task Force on Oil Sands Strategies are described. Changes in requirements for transportation fuels due to stricter regulations and environmental initiatives will cause a trend to lighter fuels with more hydrogen content, less aromatics, nitrogen, sulfur and metals. A preferred refinery configuration will be able to process heavier crudes and synthetic crudes, have no heavy fuel oil product, low sulfur products, low aromatics with high octane, and low operating cost. A regional or central facility that combines the processing capabilities of a bitumen upgrader with the process units of a refinery is preferred. Advantages of this concept are: value addition to the feedstock is maximized; dependence on refineries is eliminated; restriction on synthetic crude oil volumes due to capacity limitations at refineries is eliminated; directly marketable finished products are produced; more stringent quality specifications are satisfied; and the synergies between upgrading and refining improve overall economics of processing. It is recommended that the concept of regional upgraders be adopted for Alberta, strategic alliances be encouraged, incentives for bitumen production be provided, and a bitumen pipeline network be developed. 12 refs

Effect of non-homogeneous spatial distributions of surfactants on the stability of high-content bitumen-in-water emulsions

International Nuclear Information System (INIS)

Urbina-Villalba, German; Garcia-Sucre, Maximo

2000-01-01

In order to study the effects of non-homogeneous spatial distributions of surfactants on the drop size of high-content bitumen-in-water emulsions, a modification of a standard Brownian Dynamics algorithm was employed. The new algorithm is able to simulate the evolution of oil/water emulsions towards flocculation and coalescence. The simulation boxes contain 216 and 125 particles initially distributed in a homogeneous simple cubic arrangement, corresponding to bitumen/water volume fractions of 0.30 and 0.51, respectively. The particles interact through a DLVO potential dependent on the total surfactant concentration, spatial surfactant distribution, and the amount of surfactant adsorbed to the bitumen/water interface. As will be shown in this article, certain combinations of the referred variables can produce a wide variety of repulsive potentials between similar drops. The variation of the total number of drops with time does not obey the usual analytical formalisms developed for more diluted cases, and instead, a simple exponential decrease of the number of drops with time is found. Such behavior has already been confirmed by experiment. Some similarities between the present results and those previously published for more diluted systems are discussed [es

Bio-Detergent oil derivative used frying

Directory of Open Access Journals (Sweden)

Alfonso Jesús Torres Ortega

2011-04-01

Full Text Available Currently, the global trend towards sustainable development for environmental friendly products such as biosurfactants shows an excellent performance. Anionic surface active agents can be produced from renewable natural raw materials such as vegetable oils mainly derived from palm oil. Methyl ester sulfonate is an active component of highly biodegradable detergents, one advantage compared with detergents derived from petrochemicals which generate a high pollutant load. This paper proposes the study of sulfonation with sulfur trioxide of esters derived from waste cooking oil which main component is palm oil. The falling film reactor allows determining the conditions of the process at pilot scale. The experimentation allowed an enhancement of empirical equations in the equipment implemented for this purpose and to determine some physicochemical properties. The comparison obtained for this same process with petrochemicals compounds indicates that the model could be applied to any film sulfonation but adjusting the parameters and specific conditions, such as the physicochemical properties of the compounds used, since the sulfonation process described in this work is one of the more complicated cases. The technological development presented here seeks to contribute with the industrial needs to promote green chemical industry for the production of biosurfactant from waste frying oil.

Electrical insulating liquid: A review

Directory of Open Access Journals (Sweden)

Deba Kumar Mahanta

2017-08-01

Full Text Available Insulating liquid plays an important role for the life span of the transformer. Petroleum-based mineral oil has become dominant insulating liquid of transformer for more than a century for its excellent dielectric and cooling properties. However, the usage of petroleum-based mineral oil, derived from a nonrenewable energy source, has affected the environment for its nonbiodegradability property. Therefore, researchers direct their attention to renewable and biodegradable alternatives. Palm fatty acid ester, coconut oil, sunflower oil, etc. are considered as alternatives to replace mineral oil as transformer insulation liquid. This paper gives an extensive review of different liquid insulating materials used in a transformer. Characterization of different liquids as an insulating material has been discussed. An attempt has been made to classify different insulating liquids-based on different properties.

Process for separating and recovering oil from oil-sands, etc

Energy Technology Data Exchange (ETDEWEB)

Preller, H

1920-07-14

A process for separating and recovering oil from oil-sands, bitumen from oil-chalk, oil shale, and coal is characterized in that the material to be separated feeds, by a self-acting feeding arrangement, to a system with slowly rotating drums alternating in different directions and thereby it is exposed to the action of hot water running opposite to the rotation, direction of the drum, with addition of extraction-medium, so that the light material is washed out and rises to the top. It is carried off, while the heavy material sinks to the bottom and, by bucket-conveyor is removed.

Sulphur output from oil sands : dramatically changing Alberta's sulphur balance

International Nuclear Information System (INIS)

D'Aquin, G.

2008-01-01

This paper discussed sulphur production from Alberta's gas and oil sands industries. While sulfur derived from natural gas production in the province is expected to decline as natural gas reserves diminish, Alberta's oil sands contain high amounts of sulphur. It is not yet known how much sulphur will be produced from the province's oil sands facilities. Alberta had considerable stockpiles of sulphur in the 1970s. By 1980, inventories began to decline. By 1996, output had increased to 7.1 million tonnes. Alberta's sulphur inventory reached 9.7 million tonnes following the collapse of the Soviet Union's government mandated fertilizer industry. In 2006, sulphur supplies in Alberta reached 12 million tonnes. Reduced global output has now lowered sulphur stockpiles. Increases in sulphur prices tend to reduce market demand, and lower prices will not typically change the volume of sulphur produced as a byproduct of oil and gas operations. Bitumen-derived sulphur output is expected to exceed gas-derived sulphur output in the near future. Sulphur from oil sands processing is expected to increase by 5 million tonnes by 2017. Increased sulphur production levels in Alberta will present a significant challenge for all sectors of the hydrocarbon industry. It was concluded that developing a plan for storing, selling or disposing of the sulphur will help to ensure the profitability of oil sands operations

Japan's involvement in oil sands development

International Nuclear Information System (INIS)

Sugiura, T.

1994-01-01

According to Japanese national policy, exploration and development by Japanese companies in overseas countries are promoted in order to ensure stable oil supplies. Japan Canada Oil Sands Limited (JACOS), part of the JAPEX group, was established during the 1978 world oil crisis to explore and develop Canadian oil sand resources in accordance with Japan's national policy. The JAPEX group, including JACOS, has invested $123 million in oil sands projects in Alberta. JAPEX's first involvement in oil sands was in the Primrose Project operated by Norcen in the Cold Lake area. Five years of cyclic steam stimulation pilot tests did not produce sufficiently good results to justify further operation. The second involvement was the PCEJ Project, a joint effort by four companies that are participating in a bitumen recovery test project in the Athabasca Deposit. JACOS holds 2,452 km 2 of oil sands leases in Alberta. Tests conducted since 1978 in the PCEJ Project include multiwell steam injection pilot tests, some of which showed promise. JACOS is also participating in steam assisted gravity drainage projects and in federal/provincial research programs. Obstacles identified in developing Alberta oil sands are the lack of a bitumen pipeline to Edmonton and the insufficient length of oil sands leases (currently 10 years), given the difficulties of oil sand development. 10 figs

Ionic Liquids as Additives of Coffee Bean Oil in Steel-Steel Contacts

Directory of Open Access Journals (Sweden)

James Grace

2015-10-01

Full Text Available Environmental awareness and ever-growing restrictive regulations over contamination have increased the need for more environmentally-friendly lubricants. Due to their superior biodegradability and lower toxicity, vegetable oils are a good alternative to replace currently-used mineral oils. However, vegetable oils show low oxidation and thermal stability and poor anti-wear properties. Most of these drawbacks can be attenuated through the use of additives. In the last decade, ionic liquids have emerged as high-performance fluids and lubricant additives due to their unique characteristics. In this study, the tribological behavior of two phosphonium-based ionic liquids is investigated as additives of coffee bean oil in steel-steel contact. Coffee bean oil-ionic liquid blends containing 1, 2.5, and 5 wt% of each ionic liquid are studied using a block-on-flat reciprocating tribometer and the test results are compared to commercially-available, fully-formulated lubricant. Results showed that the addition of the ionic liquids to the coffee bean oil reduces wear volume of the steel disks, and wear values achieved are comparable to that obtained when the commercially-available lubricant is used.

Should you trust your heavy oil viscosity measurement?

Energy Technology Data Exchange (ETDEWEB)

Nelson, L.; Miller, K.; Almond, R. [Petrovera Resources Ltd., Edmonton, AB (Canada)

2003-07-01

For the last 60 years, the heavy oil and bitumen reservoirs from western Canada have been exploited with varying degrees of success. There are many factors that may effect heavy oil and bitumen production rates. Primary production rates, which vary greatly from field to field, were found to improve with the addition of steam. Viscosity is the single most valued criteria in predicting cold production response from a new field. It is also the criteria used to determine whether thermal process are needed to reduce oil viscosity, or whether horizontal or vertical wells should be used. This study examined why production forecasts based on oil viscosity alone have been poor. It is based on an extensive data collection project in the Elk Point area reservoir which has lower than expected and erratic cold production rates. Viscosity values from the same wells were found to vary by a factor of four or more. One of the objectives of this study was to encourage commercial labs to develop an industry-wide standard method of heavy oil sample cleaning and viscosity measurement. It is generally understood that viscosity increases with an increase in the concentration of asphaltenes, but there is little information to quantify the relationship. Some studies suggest that viscosity increases logarithmically with increasing asphaltenes. It was concluded that the prediction of the viscosity of heavy oils and bitumens is very empirical, but there are ways to improve data comparisons and evaluation by applying available information from other scientific fields. 23 refs., 5 tabs., 6 figs.

Sludge derived fuel technique of sewage sludge by oil vacuum evaporation drying

International Nuclear Information System (INIS)

Kim, Seokhwan; Lim, Byungran; Lee, Sookoo

2010-01-01

Sewage sludge contains high content of organic materials and its water content is also very high about 80% even after filtration process. Landfill as a sludge treatment methods can cause odor problem and leachate production which can derive the secondary contamination of soil and groundwater. The ocean dumping will be prohibited according to the London Convention and domestic stringent environmental regulation. Based on domestic agenda on organic sewage sludge treatment, the ocean disposal will be prohibited from 2012, thus alternative methods are demanded. Sludge derived fuel (SDF) technology can alleviate the emission of greenhouse gas and recover energy from sludge. For proper treatment and SDF production from sludge, the vacuum evaporation and immersion frying technology was adopted in this research. This technology dries moisture in sludge after mixing with oil such as Bunker C oil, waste oil or waste food oil etc. Mixing sludge and oil secures liquidity of organic sludge to facilitate handling throughout the drying process. The boiling temperature could be maintained low through vacuum condition in whole evaporation process. This study was performed to find the optimum operating temperature and pressure, the mixing ratio of sludge and oil. Finally, we could obtained SDF which moisture content was less than 5%, its heating value was over 4,500 kcal/ kg sludge. This heating value could satisfy the Korean Fuel Standard for the Recycle Products. Assessed from the perspective of energy balance and economic evaluation, this sludge drying system could be widely used for the effective sludge treatment and the production of SDF. (author)

Plastic waste to liquid oil through catalytic pyrolysis using natural and synthetic zeolite catalysts.

Science.gov (United States)

Miandad, R; Barakat, M A; Rehan, M; Aburiazaiza, A S; Ismail, I M I; Nizami, A S

2017-11-01

This study aims to examine the catalytic pyrolysis of various plastic wastes in the presence of natural and synthetic zeolite catalysts. A small pilot scale reactor was commissioned to carry out the catalytic pyrolysis of polystyrene (PS), polypropylene (PP), polyethylene (PE) and their mixtures in different ratios at 450°C and 75min. PS plastic waste resulted in the highest liquid oil yield of 54% using natural zeolite and 50% using synthetic zeolite catalysts. Mixing of PS with other plastic wastes lowered the liquid oil yield whereas all mixtures of PP and PE resulted in higher liquid oil yield than the individual plastic feedstocks using both catalysts. The GC-MS analysis revealed that the pyrolysis liquid oils from all samples mainly consisted of aromatic hydrocarbons with a few aliphatic hydrocarbon compounds. The types and amounts of different compounds present in liquid oils vary with some common compounds such as styrene, ethylbenzene, benzene, azulene, naphthalene, and toluene. The FT-IR data also confirmed that liquid oil contained mostly aromatic compounds with some alkanes, alkenes and small amounts of phenol group. The produced liquid oils have high heating values (HHV) of 40.2-45MJ/kg, which are similar to conventional diesel. The liquid oil has potential to be used as an alternative source of energy or fuel production. Copyright © 2017 Elsevier Ltd. All rights reserved.

Degradation and stabilization of coal derived liquid. (IV). ; Effect of alcohol on coloration of coal derived light oil. Sekitan ekikayu no anteika. (IV). ; Sekitan ekikayu no chakushoku yokusei ni oyobosu alcohol no tenka koka

Energy Technology Data Exchange (ETDEWEB)

Ukegawa, K.; Matsumura, A.; Kondo, T. (National Research Institute for Pollution and Resources, Tsukuba (Japan)); TAhara, N. (Nitto Denko Corp., Osaka (Japan)); Nakamura, E. (New Energy and Industrial Technology Development Organization, Tokyo (Japan)); Niki, E. (The University of Tokyo, Tokyo (Japan). Research Center for ADvanced Science and Technology)

1990-01-20

In order to improve the color stability of a coal derived light oil, the effect of hydrotreating and various additives has been studied. The color stability has been evaluated through measuring changes in absorbance by flow-cell spectrophotometer. Following results have been obtained: The color stabilities of hydrotreated coal derived light oils were improved remarkably with increasing hydrotreating temperature and pressure. Mild hydrotreating made the color stability of the coal derived light oil much better than the fuel oil, even though the nitrogen removal was very small. Phenolic compounds additives could not improve the color stability of the coal derived light oil. Alcohol, especially methanol, made the coloration rate of the coal derived light oil small to a great extent, on account of hydrogen bonding between methanol and nitrogen compounds in the fuel oil. 4 refs., 4 figs., 3 tabs.

Bitumen-petrolatum hydroinsulation employment in the South-Ukrainian NPP building

International Nuclear Information System (INIS)

Donskov, V.A.; Pochepko, V.P.; Ryaboshapko, Yu.I.; Savenkov, V.V.; Chaplygin, L.A.; Chernyavskij, V.L.

1982-01-01

Method of accomplishment of external hydroinsulation of ferroconcrete constructions by bitumen-petrolatum compositions used in the South-Ukrainian NPP building is described. The speciality of this method lies in establishing the combined cover, which includes concrete layer impregnated by modified petrolatum, and the covering layer from bitumen and petrolatum mixture, and performs not only functions of hydroinsulation but also anticorrosive protection under conditions of highly agressive waters action. Physicomechanical characteristics of bitumen-petrolatum compositions are given and the installation for applying of hydroinsulation compositions is described

Effect of Ultraviolet Aging on Rheology and Chemistry of LDH-Modified Bitumen

Directory of Open Access Journals (Sweden)

Xing Liu

2015-08-01

Full Text Available Layered double hydroxides (LDHs are an ultravioletlight (UV-resistant material. In this study, two types of LDHs (Mg-Al-LDHs and Zn-Al-LDHs were applied to modify bitumen by melt-blending. The effect of ultraviolet aging on the rheology and chemistry of LDH-modified bitumen was studied by means of dynamic shear rheometer (DSR, thin-layer chromatography with flame ionization detection (TLC-FID, Fourier transform infrared spectroscopy (FTIR, and Ultraviolet-Visible (UV-Vis spectrophotometry to reveal the mechanisms of action for LDHs and bitumen. The results showed that within the UV spectra (220–400 nm, the reflectance of Zn-Al-LDHs was larger than that of Mg-Al-LDHs. These two LDHs have different influences on the performance of bitumen. Mg-Al-LDHs had a more obvious influence on the physical and dynamic rheological properties of bitumen than Zn-Al-LDHs. Zn-Al-LDHs improved the UV-aging resistance of bitumen more. The reason can be that the reflectance of the Zn-Al-LDHs to the UV light is larger than that of the Mg-Al-LDHs. The Zn-Al-LDH-modified bitumen had more potential to improve the UV-aging resistance during the service life of asphalt pavement.

Characterization of Bitumen Micro-Mechanical Behaviors Using AFM, Phase Dynamics Theory and MD Simulation

Directory of Open Access Journals (Sweden)

Yue Hou

2017-02-01

Full Text Available Fundamental understanding of micro-mechanical behaviors in bitumen, including phase separation, micro-friction, micro-abrasion, etc., can help the pavement engineers better understand the bitumen mechanical performances at macroscale. Recent researches show that the microstructure evolution in bitumen will directly affect its surface structure and micro-mechanical performance. In this study, the bitumen microstructure and micro-mechanical behaviors are studied using Atomic Force Microscopy (AFM experiments, Phase Dynamics Theory and Molecular Dynamics (MD Simulation. The AFM experiment results show that different phase-structure will occur at the surface of the bitumen samples under certain thermodynamic conditions at microscale. The phenomenon can be explained using the phase dynamics theory, where the effects of stability parameter and temperature on bitumen microstructure and micro-mechanical behavior are studied combined with MD Simulation. Simulation results show that the saturates phase, in contrast to the naphthene aromatics phase, plays a major role in bitumen micro-mechanical behavior. A high stress zone occurs at the interface between the saturates phase and the naphthene aromatics phase, which may form discontinuities that further affect the bitumen frictional performance.

Characterization of Bitumen Micro-Mechanical Behaviors Using AFM, Phase Dynamics Theory and MD Simulation.

Science.gov (United States)

Hou, Yue; Wang, Linbing; Wang, Dawei; Guo, Meng; Liu, Pengfei; Yu, Jianxin

2017-02-21

Fundamental understanding of micro-mechanical behaviors in bitumen, including phase separation, micro-friction, micro-abrasion, etc., can help the pavement engineers better understand the bitumen mechanical performances at macroscale. Recent researches show that the microstructure evolution in bitumen will directly affect its surface structure and micro-mechanical performance. In this study, the bitumen microstructure and micro-mechanical behaviors are studied using Atomic Force Microscopy (AFM) experiments, Phase Dynamics Theory and Molecular Dynamics (MD) Simulation. The AFM experiment results show that different phase-structure will occur at the surface of the bitumen samples under certain thermodynamic conditions at microscale. The phenomenon can be explained using the phase dynamics theory, where the effects of stability parameter and temperature on bitumen microstructure and micro-mechanical behavior are studied combined with MD Simulation. Simulation results show that the saturates phase, in contrast to the naphthene aromatics phase, plays a major role in bitumen micro-mechanical behavior. A high stress zone occurs at the interface between the saturates phase and the naphthene aromatics phase, which may form discontinuities that further affect the bitumen frictional performance.

Optimization bitumen-based upgrading and refining schemes

Energy Technology Data Exchange (ETDEWEB)

Munteanu, M.; Chen, J. [National Centre for Upgrading Technology, Devon, AB (Canada); Natural Resources Canada, Devon, AB (Canada). CanmetENERGY

2009-07-01

This poster highlighted the results of a study in which the entire refining scheme for Canadian bitumen as feedstocks was modelled and simulated under different process configurations, operating conditions and product structures. The aim of the study was to optimize the economic benefits, product quality and energy use under a range of operational scenarios. Optimal refining schemes were proposed along with process conditions for existing refinery configurations and objectives. The goal was to provide guidelines and information for upgrading and refining process design and retrofitting. Critical steps were identified with regards to the upgrading process. It was concluded that the information obtained from this study would lead to significant improvement in process performance and operations, and in reducing the capital cost for building new upgraders and refineries. The simulation results provided valuable information for increasing the marketability of bitumen, reducing greenhouse gas emissions and other environmental impacts associated with bitumen upgrading and refining. tabs., figs.

Process water treatment in Canada's oil sands industry : 1 : target pollutants and treatment objectives

International Nuclear Information System (INIS)

Allen, E.W.

2008-01-01

The continuous recycling of tailings pond water in the oil sands industry has contributed to an overall decline in water quality used for bitumen recovery, general water consumption, and remedial activities. This paper reviewed process water quality and toxicity data from 2 long-term oil sands operations. The aim of the study was to determine potential roles for water treatment and provide benchmarks for the selection of candidate water treatment technologies in the oil sands region of Alberta. An overview of the oil sands industry was provided as well as details of bitumen recovery processes. The study examined target pollutants and exceedances identified in environmental and industrial water quality guidelines. The study demonstrated that the salinity of tailings pond water increased at a rate of 75 mg per litre per year between 1980 and 2001. Increases in hardness, chloride, ammonia, and sulphates were also noted. Naphthenic acids released during bitumen extraction activities were determined as the primary cause of tailings pond water toxicity. A summary of recent studies on experimental reclamation ponds and treatment wetlands in the oil sands region was included. 19 refs., 4 tabs., 11 figs

Identification of CYP1A inducing compounds in crude oil

Energy Technology Data Exchange (ETDEWEB)

Khan, C.W.; Hodson, P.V. [Queen' s Univ., Kingston, ON (Canada). Dept. of Biology; Hollebone, B.P.; Wang, Z. [Environment Canada, Ottawa, ON (Canada). Environmental Technology Advancement Directorate; Brown, R.S. [Queen' s Univ., Kingston, ON (Canada). Dept. of Chemistry

2004-07-01

One of the major sources of polycyclic aromatic hydrocarbons (PAHs) in aquatic ecosystems is crude oil. PAHs are responsible for developmental malformations in the early life stages of fish. The induction of CYP1A enzyme is characteristic of developmental toxicity caused by crude oil. As such, it is an effective biomarker of PAH uptake. It is not known which PAHs cause toxicity because of the complex chemical composition of crude oil. In this study, an approach called Toxicity Identification and Evaluation (TIE) was used with different crude oils to separate bioavailable PAHs into petroleum sub-fractions. The extent of CYP1A induction in rainbow trout was measured after 48 hour exposures to each fraction. Low temperature vacuum distillation was used to create white gas, kerosene, coal tar/bitumen and wax fractions. Hepatic CYP1A activity was induced by whole oil and some fractions. The highest PAH concentration was found in the coal tar/bitumen fraction which accounted for most CYP1A induction in whole oil. The wax fraction also caused moderate CYP1A induction, but the white gas fraction did not cause any CYP1A induction. The hypothesis that alkyl PAH may be the most significant source of CYP1A inducers in the coal tar/bitumen fraction was supported by chemical analysis of CYP1A induction potency. Results showed that benzo[a]pyrene accounts for nearly all of the CYP1A induction caused by the wax fraction.

Recent technological advances in the application of nano-catalytic technology to the enhanced recovery and upgrading of bitumen and heavy oils

Energy Technology Data Exchange (ETDEWEB)

Pereira Almao, P. [Calgary Univ., AB (Canada). Schulich School of Engineering

2013-11-01

Advances in Nanotechnology, such as manufacturing of nano-catalysts allow the online (during processing) and on site production of nano-catalysts for heavy oils upgrading. These inventions have also facilitated the development of two lines of heavy oils upgrading processes that make use of nano-catalysts for producing upgraded oil: In Situ Upgrading and Field Upgrading. Producing chemical upgrading of heavy oils is achievable and economically viable at lower temperatures and lower pressures than used in most upgraders if the use of nano-catalysts were implemented. The spontaneity of thermal, steam and hydro processing reactions for converting the different chemical families of hydrocarbons present in the heaviest fractions of heavy oils and bitumen (HO-B) into lighter products was shown recently. Spontaneity was measured by the value of the change of free energy at low pressure. These undesirable paths are spontaneous and uncontrollable under thermal cracking conditions, and require providing years of residence time for intermolecular hydrogen redistribution to minimize olefins polymerization, if at all possible. Instead, hydroprocessing in the presence of hydrogen activating catalysts would create an abundance of hydrogen radicals impeding large molecules condensation and olefins proliferation. In Situ Upgrading: performs coupled Enhanced Oil Recovery with In Reservoir Upgrading via Hot Fluid Injection (HFI). The heat handling of this HFI process and the production of transportable oil with no need of diluent from the start of operation completes the originality of it. This technology uses heavy fractions separated from produced oil to reintroduce heat into the reservoir along with suspended nano-catalysts and hydrogen. These components react in the well bore and inside the reservoir to release more heat (hydroprocessing reactions are exothermic) producing light gases and volatile hydrocarbons that contribute to increase oil detachment from the rock resulting in

In situ analytical pyrolysis of coal macerals and solid bitumens by laser micropyrolysis GC-MS

Energy Technology Data Exchange (ETDEWEB)

Greenwood, P.F.; George, S.C.; Pickel, W. [CSIRO Petroleum, PO Box 136, NSW 1670 N. Ryde (Australia); Zhu, Y. [Petroleum Geochemistry Research Center, Jianghan Petroleum University, Jingzhou, 434102 Hubei (China); Zhong, N. [Applied Geochemistry Laboratory, University of Petroleum, Changping, 102200 Beijing (China)

2001-04-01

Specific macerals in coals and distinct solid organic bitumens within limestones from northern China were separately analysed in situ by laser micropyrolysis gas chromatography-mass spectrometry. The major pyrolysates from the resinite and cutinite macerals included aromatic hydrocarbons such as alkylnaphthalenes, alkylbenzenes, alkyltetralins (in the resinite) and alkylphenols (in the cutinite), and aliphatic hydrocarbons such as n-alk-1-enes, n-alkanes, pristane and phytane. The same classes of hydrocarbons were also detected in co-occurring vitrinites, including very similar relative distributions of alkylnaphthalenes in the case of the resin-rich coal. Several observed quantitative differences are consistent with previous molecular data from maceral concentrates. The qualitative similarity of the maceral data suggest (1) extensive assimilation of free hydrocarbons by all macerals within the coals; or (2) inefficient targeting of the macerals by the laser, although microscopic observation showed that the laser craters were generally constrained within surface boundaries of the maceral. The organic composition of a solid bitumen within a Carboniferous limestone was characterised by a distinctive distribution of C{sub 0}-C{sub 4} alkyldibenzofurans, as well as alkylbenzenes, alkylnaphthalenes and a low molecular weight distribution of n-alk-1-enes and n-alkanes. These data suggest the solid bitumen comprises a strongly aromatic matrix with terrestrially-derived oxygen functionality and alkyl linkages. The same aromatic and aliphatic hydrocarbon products were also detected in the morphologically homogenous carbonates hosting the solid bitumens, indicating the presence of sub-microscopic organic moieties throughout the limestone.

Influence of the prepolymer molecular weight and free isocyanate content on the rheology of polyurethane modified bitumens

OpenAIRE

Carrera Páez, Virginia; Cuadri Vega, Antonio Abad; García Morales, Moisés; Partal López, Pedro

2014-01-01

Isocyanate-based modification is lately gaining acceptance as a successful way to give added value to bitumen, a crude oil refining by-product. In order to study the influence of prepolymer type on the rheological properties of the resulting binders, six prepolymers synthesized from polypropylene-glycols (PPG) with varying molecular weight (between 440 and 2425) and different molar excess of a polymeric MDI (4,4’-diphenylmethane diisocyanate) were used. Two modification procedures, either inv...

Solidification of oils and organic liquids

International Nuclear Information System (INIS)

Clark, D.E.; Colombo, P.; Neilson, R.M. Jr.

1982-07-01

The suitability of selected solidification media for application in the disposal of low-level oil and other organic liquid wastes has been investigated. In the past, these low-level wastes (LLWs) have commonly been immobilized by sorption onto solid absorbents such as vermiculite or diatomaceous earth. Evolving regulations regarding the disposal of these materials encourage solidification. Solidification media which were studied include Portland type I cement; vermiculite plus Portland type I cement; Nuclear Technology Corporation's Nutek 380-cement process; emulsifier, Portland type I cement-sodium silicate; Delaware Custom Materiel's cement process; and the US Gypsum Company's Envirostone process. Waste forms have been evaluated as to their ability to reliably produce free standing monolithic solids which are homogeneous (macroscopically), contain < 1% free standing liquids by volume and pass a water immersion test. Solidified waste form specimens were also subjected to vibratory shock testing and flame testing. Simulated oil wastes can be solidified to acceptable solid specimens having volumetric waste loadings of less than 40 volume-%. However, simulated organic liquid wastes could not be solidified into acceptable waste forms above a volumetric loading factor of about 10 volume-% using the solidification agents studied

Coating of evaporation concentrates with bitumen. Progress Report No. 1

International Nuclear Information System (INIS)

Rodier, J.; Lefillatre, G.; Rodi, L.; Cudel, Y.

1968-01-01

Laboratory tests have been carried out on the coating by bitumen of evaporation concentrates having a free nitric acidity of 1 N or 2.5 N, and a high mineralization (400 gm/litre). In order to neutralize the free acidity and to trap the radio-elements, these concentrates have been subjected before coating to various treatments designed to decrease the solubility. As a result of these treatments, sludges were obtained which could be coated directly with the bitumen. By measuring the radioactive diffusion factors of the bitumen coated products immersed both in ordinary and sea water, it was possible to compare the efficiency of the processes developed and of the various types of bitumen used. On the whole the radioactive diffusion tests were satisfactory and the process using successive co-precipitations (hydroxides, nickel ferrocyanide, barium sulphate) was chosen. From the bitumens tried out, a straight - asphalt, Mexphalt 40/50 was selected for low and medium activity concentrates as it ensures good isolation of the radio-elements; an air-blowing asphalt, Mexphalte R 90/40, was chosen for concentrates of high activity because of its higher resistance to irradiation. As a result of this work, a simple coating technology was evolved and pilot experiments will soon begin. Briefly, it appears that although a method for coating evaporation concentrates with bitumen has been defined, it will inevitably be necessary to devise a specific decontamination process each time that a new type of concentrate is encountered (composition, nature of the salts, radio-element distribution). (author) [fr

The significance of petroleum bitumen in ancient Egyptian mummies.

Science.gov (United States)

Clark, K A; Ikram, S; Evershed, R P

2016-10-28

Mummification was practised in ancient Egypt for more than 3000 years, emerging from initial observations of buried bodies preserved by natural desiccation. The use of organic balms (and other funerary practices) was a later introduction necessitated by more humid burial environments, especially tombs. The dark colour of many mummies led to the assumption that petroleum bitumen (or natural asphalt) was ubiquitous in mummification; however, this has been questioned for more than 100 years. We test this by investigating 91 materials comprising balms, tissues and textiles from 39 mummies dating from ca 3200 BC to AD 395. Targeted petroleum bitumen biomarker (steranes and hopanes) analyses by gas chromatography-mass spectrometry selected ion monitoring (GC-MS SIM, m/z 217 and 191) showed no detectable bitumen use before the New Kingdom (ca 1550-1070 BC). However, bitumen was used in 50% of New Kingdom to Late Period mummies, rising to 87% of Ptolemaic/Roman Period mummies. Quantitative determinations using (14)C analyses reveal that even at peak use balms were never more than 45% w/w bitumen. Critically, the dark colour of balms can be simulated by heating/ageing mixtures of fats, resins and beeswax known to be used in balms. The application of black/dark brown balms to bodies was deliberate after the New Kingdom reflecting changing funerary beliefs and shifts in religious ideology.This article is part of the themed issue 'Quantitative mass spectrometry'. © 2016 The Authors.

Solid colloidal particles inducing coalescence in bitumen-in-water emulsions.

Science.gov (United States)

Legrand, J; Chamerois, M; Placin, F; Poirier, J E; Bibette, J; Leal-Calderon, F

2005-01-04

Silica particles are dispersed in the continuous phase of bitumen-in-water emulsions. The mixture remains dispersed in quiescent storage conditions. However, rapid destabilization occurs once a shear is applied. Observations under the microscope reveal that the bitumen droplets form a colloidal gel and coalesce upon application of a shear. We follow the kinetic evolution of the emulsions viscosity, eta, at constant shear rate: eta remains initially constant and exhibits a dramatic increase after a finite time, tau. We study the influence of various parameters on the evolution of tau: bitumen droplet size and volume fraction, silica diameter and concentration, shear rate, etc.

The effect of low molecular weight multifunctional additives on heavy oil viscosity

Energy Technology Data Exchange (ETDEWEB)

Oldenburg, T.B.P.; Yarranton, H.W.; Larter, S.R. [Calgary Univ., AB (Canada)

2010-07-01

Crude oils contain many small multifunctional low molecular weight components that act as linking molecules between larger functionalized species. The linkage molecules have a significant impact on the flow properties of hydrocarbon systems. This study investigated the use of a low molecular weight multiheteroatom species (LMWMH) as a molecular Velcro linking high molecular weight components together. LMWMH species were added to Albertan bitumens and heavy oil, and their impact on viscosity was investigated. Results of the experimental studies were then compared with the effects of hydrocarbon solvents on similar samples. The LMWMH species included bifunctional species and analogous alkyl and aryl monoamines that acted as blocking molecules to hinder the association of larger petroleum species. Density and viscosity measurements were conducted. A correlation method was used to predict the viscosity of the solvent-diluted heavy oil and bitumen samples. The study showed that of the tested additives, only aniline demonstrated an additional viscosity-reducing effect. The aniline inhibited asphaltene association and is a promising candidate for enhanced in-situ bitumen viscosity reduction. 23 refs., 4 tabs.

Proceedings of ITOHOS 2008 : The 2008 SPE/PS/CHOA International Thermal Operations and Heavy Oil Symposium : Heavy Oil : Integrating the Pieces

International Nuclear Information System (INIS)

2008-10-01

This multi-disciplinary conference and exhibition combined the Society of Petroleum Engineers (SPE) and the Petroleum Society's (PS) international thermal operations and heavy oil symposium, and the Canadian Heavy Oil Association's (CHOA) annual business meeting. The conference provided a forum to examine emerging technologies and other critical issues affecting the global heavy oil and bitumen industry. The most current technologies from around the world that enhance the recovery of heavy oil and bitumen from oil sand deposits were also showcased. The technical program encompassed the economic, technical, and environmental challenges that the petroleum industry is currently facing. The sessions of the conference were entitled: artificial lift; mining, extraction and cold production; simulation; solvent processes; reservoir characterization; steam generation and water treatment; and, in-situ combustion in Canada. The conference also featured a series of short courses and tutorials on heavy oil wellbore completions and design; drilling horizontal heavy oil wells and steam assisted gravity drainage (SAGD) wells; geomechanical based reservoir monitoring; thermal well design; fiber optic thermal monitoring; heavy oil thermal recovery and economics; wellbore slotting; advanced geomechanics; and, an overview of cold heavy oil production with sand (CHOPS). All 91 presentations from the conference have been catalogued separately for inclusion in this database. refs., tabs., figs

Proceedings of ITOHOS 2008 : The 2008 SPE/PS/CHOA International Thermal Operations and Heavy Oil Symposium : Heavy Oil : Integrating the Pieces

Energy Technology Data Exchange (ETDEWEB)

NONE

2008-10-15

This multi-disciplinary conference and exhibition combined the Society of Petroleum Engineers (SPE) and the Petroleum Society's (PS) international thermal operations and heavy oil symposium, and the Canadian Heavy Oil Association's (CHOA) annual business meeting. The conference provided a forum to examine emerging technologies and other critical issues affecting the global heavy oil and bitumen industry. The most current technologies from around the world that enhance the recovery of heavy oil and bitumen from oil sand deposits were also showcased. The technical program encompassed the economic, technical, and environmental challenges that the petroleum industry is currently facing. The sessions of the conference were entitled: artificial lift; mining, extraction and cold production; simulation; solvent processes; reservoir characterization; steam generation and water treatment; and, in-situ combustion in Canada. The conference also featured a series of short courses and tutorials on heavy oil wellbore completions and design; drilling horizontal heavy oil wells and steam assisted gravity drainage (SAGD) wells; geomechanical based reservoir monitoring; thermal well design; fiber optic thermal monitoring; heavy oil thermal recovery and economics; wellbore slotting; advanced geomechanics; and, an overview of cold heavy oil production with sand (CHOPS). All 91 presentations from the conference have been catalogued separately for inclusion in this database. refs., tabs., figs.

Clean energy and hydrogen for oil sands development with CANDU SCWR nuclear reactors and Cu-Cl cycles

International Nuclear Information System (INIS)

Wang, Z.L.; Naterer, G.F.; Gabriel, K.S.

2010-01-01

In this paper, the unique capabilities and advantages of SCWR technology for cleaner oil sands development are discussed from two perspectives: lower temperature steam generation by supercritical water for steam assisted gravity drainage (SAGD), and hydrogen production for oil sands upgrading by coupling SCWR with the thermochemical copper-chlorine (Cu-Cl) cycle. The heat requirements for bitumen extraction from the oil sands and the hydrogen requirements for bitumen upgrading are evaluated. A conceptual layout of SCWR coupled with oil sands development is presented. The reduction of CO 2 emissions due to the use of SCWR and thermo chemical hydrogen production cycle is also analyzed. (author)

Effect of transesterification degree and post-treatment on the in-service performance of NCO-functionalized vegetable oil bituminous products

OpenAIRE

Cuadri Vega, Antonio Abad; García Morales, Moisés; Navarro Domínguez, Francisco Javier; Partal López, Pedro

2014-01-01

The bitumen modification through polyurethane prepolymers presents significant benefits for the manufacture of bituminous products for the paving industry. In this sense, this work explores the use, as bitumen modifier, of a novel reactive prepolymer synthesized by reaction of 4,4´,diphenylmethane diisocyanate (MDI) and a vegetable oil-based polyol, castor oil (CO), previously transesterified with pentaerythritol. On the one hand, thermal analysis on transesterified CO revealed a highly stabl...

Bitumen nanocomposites with improved performance

KAUST Repository

Kosma, Vasiliki

2017-11-29

Bitumen-clay nanocomposite binders with styrene-butadienestyrene triblock copolymer, SBS, and combinations of SBS and crumb rubber (CR) with different CR/SBS ratios have been synthesized and characterized. In addition to the binder, samples containing the binder and concrete sand (with a weight ratio 1:9) were prepared. The modified binders were studied in terms of filler dispersion, storage stability, mechanical performance and water susceptibility. We demonstrate that the samples containing nanoclays consistently outperform those based only on the polymer additives. We also find that nanocomposite samples based on a combination of SBS and CR are best, since in addition to other improvements they show excellent storage stability. Our work shows that substituting CR with SBS as a bitumen additive and combining it with inexpensive nanoclays leads to new materials with enhanced performance and improved stability for practical asphalt applications.

Considerations when ranking stochastically modeled oil sands resource models for mining applications

Energy Technology Data Exchange (ETDEWEB)

Etris, E.L. [Society of Petroleum Engineers, Canadian Section, Calgary, AB (Canada)]|[Petro-Canada, Calgary, AB (Canada); Idris, Y.; Hunter, A.C. [Petro-Canada, Calgary, AB (Canada)

2008-10-15

Alberta's Athabasca oil sands deposit has been targeted as a major resource for development. Bitumen recovery operations fall into 2 categories, namely mining and in situ operations. Mining recovery is done above ground level and consists of open pit digging, disaggregation of the bitumen-saturated sediment through crushing followed by pipeline transport in a water-based slurry and then separation of oil, water and sediment. In situ recovery consists of drilling wells and stimulating the oil sands in the subsurface with a thermal treatment to reduce the viscosity of the bitumen and allow it to come to the surface. Steam assisted gravity drainage (SAGD) is the most popular thermal treatment currently in use. Resource models that simulate the recovery process are needed for both mining and in situ recovery operations. Both types can benefit from the advantages of a stochastic modeling process for resource model building and uncertainty evaluation. Stochastic modeling provides a realistic geology and allows for multiple realizations, which mining operations can use to evaluate the variability of recoverable bitumen volumes and develop mine plans accordingly. This paper described the processes of stochastic modelling and of determining the appropriate single realization for mine planning as applied to the Fort Hills oil sands mine which is currently in the early planning stage. The modeling exercise was used to estimate the in-place resource and quantify the uncertainty in resource volumes. The stochastic models were checked against those generated from conventional methods to identify any differences and to make the appropriate adaptations. 13 refs., 3 tabs., 16 figs.

Effect of heating rate on thermal cracking characteristics and kinetics of Xinjiang oil sand bitumen by TG-FTIR

Science.gov (United States)

Hao, Junhui; Zhang, Jinhong; Qiao, Yingyun; Tian, Yuanyu

2017-08-01

This work was aimed to investigate effects of heating rate on thermal cracking behaviors, distribution of gaseous products and activation energy of the thermal cracking process of Xinjiang oil sand bitumen (OSB). The thermal cracking experiments of Xinjiang OSB were performed by using thermogravimetric analyzer (TGA) at various heating rates of 10, 20, 50, 80 and 120 K/min. The evolving characteristic of gaseous products produced from the thermal cracking process was evaluated by the Fourier transform infrared spectrometry (FTIR) connected with TG. The kinetic parameters of the thermal cracking process of Xinjiang OSB at each of heating rate were determined by the Coats-Redfern model. The result show that the temperature intervals of DE volatilization stage and main reaction stage, the ((dw/dt) max and Tmax in thermal cracking process of Xinjiang OSB all increased with the increasing heating rate. While the heating rate has not obvious effect on the coke yield of Xinjiang OSB. Furthermore, the maximum absorbance of gaseous products and corresponding temperature became larger as the heating rate increases. The activation energy of this two stage both presented increasing trend with the rising heating rate, while the increasing content of that of DE volatilization stage was weaker compared to that of main reaction stage.

Freeze-Thaw Performance and Moisture-Induced Damage Resistance of Base Course Stabilized with Slow Setting Bitumen Emulsion-Portland Cement Additives

Directory of Open Access Journals (Sweden)

Mojtaba Shojaei Baghini

2015-01-01

Full Text Available Freeze-thaw (FT cycles and moisture susceptibility are important factors influencing the geotechnical characteristics of soil-aggregates. Given the lack of published information on the behavior of cement-bitumen emulsion-treated base (CBETB under environmental conditions, especially freezing and thawing, this study investigated the effects of these additives on the CBETB performance. The primary goal was to evaluate the resistance of CBETB to moisture damage by performing FT, Marshall conditioning, and AASHTO T-283 tests and to evaluate the long-term stripping susceptibility of CBETB while also predicting the liquid antistripping additives to assess the mixture’s durability and workability. Specimens were stabilized with Portland cement (0%–6%, bitumen emulsion (0%–5%, and Portland cement-bitumen emulsion mixtures and cured for 7 days, and their short- and long-term performances were studied. Evaluation results of both the Marshall stability ratio and the tensile strength ratio show that the additions of additives increase the resistance of the mixtures to moisture damage. Results of durability tests performed for determining the resistance of compacted specimens to repeated FT cycles indicate that the specimen with the 4% cement-3% bitumen emulsion mixture significantly improves water absorption, volume changes, and weight losses. This indicates the effectiveness of this additive as a road base stabilizer with excellent engineering properties for cold regions.

Detection of argan oil adulteration with vegetable oils by high-performance liquid chromatography-evaporative light scattering detection.

Science.gov (United States)

Salghi, Rachid; Armbruster, Wolfgang; Schwack, Wolfgang

2014-06-15

Triacylglycerol profiles were selected as indicator of adulteration of argan oils to carry out a rapid screening of samples for the evaluation of authenticity. Triacylglycerols were separated by high-performance liquid chromatography-evaporative light scattering detection. Different peak area ratios were defined to sensitively detect adulteration of argan oil with vegetable oils such as sunflower, soy bean, and olive oil up to the level of 5%. Based on four reference argan oils, mean limits of detection and quantitation were calculated to approximately 0.4% and 1.3%, respectively. Additionally, 19 more argan oil reference samples were analysed by high-performance liquid chromatography-refractive index detection, resulting in highly comparative results. The overall strategy demonstrated a good applicability in practise, and hence a high potential to be transferred to routine laboratories. Copyright © 2013 Elsevier Ltd. All rights reserved.

Stabilization of Softwood-Derived Pyrolysis Oils for Continuous Bio-oil Hydroprocessing

Energy Technology Data Exchange (ETDEWEB)

Olarte, Mariefel V.; Zacher, Alan H.; Padmaperuma, Asanga B.; Burton, Sarah D.; Job, Heather M.; Lemmon, Teresa L.; Swita, Marie S.; Rotness, Leslie J.; Neuenschwander, Gary N.; Frye, John G.; Elliott, Douglas C.

2015-10-15

The use of fast pyrolysis as a potential renewable liquid transportation fuel alternative to crude oil depends on successful catalytic upgrading to produce a refinery-ready product with oxygen content and qualities (i.e. specific functional group or compound content) that is compatible with the product’s proposed insertion point. Catalytic upgrading of bio-oil requires high temperature and pressure, while similar to crude oil hydrotreating, is not as straightforward for the thermally unstable pyrolysis oil. For years, a two-temperature zone, downflow trickle bed reactor was the state-of-the art for continuous operation. However, pressure excursion due to plug formation still occurred, typically at the high temperature transition zone, leading to a process shutdown within 140 h. Recently, a bio-oil pre-treatment process, together with a robust commercial catalyst, was found to be enabling the continuous operation of the two-zone hydroprocessing system. Here, we report the results on pre-treating bio-oil at 413 K and 8.4 MPa of flowing H2 (500 L H2/L bio-oil, 0.5 L bio-oil/L catalyst bed) and the attempts to characterize this oil product to understand the chemistry which enabled the long-term processing of bio-oil.

Applications in the oil sands industry for Particlear{sup R} silica microgel

Energy Technology Data Exchange (ETDEWEB)

Moffett, B. [DuPont Chemical Solutions Enterprise, Wilmington, DE (United States)

2009-07-01

This presentation demonstrated the use of Particlear{sup R} silica microgel in the oil sands industry. The silica-based coagulant is an amorphous silicon dioxide microgel solution. The surface area of a football field can be obtained using 2.7 grams of the substance. The coagulation mechanism is achieved by charge neutralization and inter-particle bridging. The microgel is manufactured at the point of use from commodity chemicals, water, and carbon dioxide (CO{sub 2}). Applications for the microgel include potable water treatment, paper retention, and animal processing wastewater. In the oil sands industry, Particlear{sup R} can be used in tailings flocculation, thickened tailings drying, steam assisted gravity drainage (SAGD) water treatment, and enhanced bitumen recovery. It was concluded that the microgel can be used in many oil sands processing and liquid-solid separation processes in order to remove dissolved solids and organics and increase the rate of solids dewatering. tabs., figs.

Monitoring the petroleum bitumen characteristics changes during their interaction with the polymers

Science.gov (United States)

Belyaev, P. S.; Mishchenko, S. V.; Belyaev, V. P.; Frolov, V. A.

2017-08-01

The subject of the study is the characteristics (penetration, softening temperature, ductility and elasticity) of a road binder based on petroleum bitumen. The work purpose is to monitor the changes in the characteristics of petroleum bitumen when it interacting with polymers: thermoplastic elastomer, low-density polyethylene, including the adhesive additive presence. To carry out the research a special laboratory facility was designed and manufactured with two blade mixers providing intensive turbulent mixing and the possibility to effect on the transition process of combining the components in a polymer-bitumen binder. To construct a mathematical model of the polymer-bitumen binder characteristics dependence from the composition, methods of statistical experiments planning were used. The possibility of the expensive thermoplastic elastomers replacement with polyethylene is established while maintaining acceptable polymer-bitumen binder quality parameters. The obtained results are proposed for use in road construction. They allow to reduce the roads construction cost with solving the problem of recycling long-term waste packaging from polyethylene.

Hydrodenitrogenation and hydrodesulphurization of heavy gas oil using NiMo/Al{sub 2}O{sub 3} catalyst containing phosphorous : experimental and kinetic studies

Energy Technology Data Exchange (ETDEWEB)

Ferdous, D.; Dalai, A.K. [Saskatchewan Univ., Saskatoon, SK (Canada). Dept. of Chemical Engineering; Adjaye, J. [Syncrude Canada Ltd., Edmonton, AB (Canada). Edmonton Research Centre

2005-10-01

Oil sand bitumens and their derived products contain high levels of nitrogen and sulfur compounds which cause the formation of SOx and NOx in the atmosphere. These compounds also deactivate the catalysts used in fluid catalytic cracking and hydrocracking. This study focused on finding a better catalyst to efficiently remove sulphur and nitrogen from oil sand-derived heavy gas oils. The NiMo/Al{sub 2}O{sub 3} catalyst with phosphorous (P) was used in a trickle-bed reactor under a range of temperature and pressure conditions to study the reactivity of vacuum, atmospheric and hydrocracked heavy gas oils produced from Athabasca bitumen. The concentration of phosphorous was maintained at 2.7 wt per cent, while the hydrogen flow rate and catalyst weight were maintained constant at 50 mL/min and 4 g respectively. An ANOVA analysis of experimental data was performed to optimize the process conditions for hydrodenitrogenation (HDN) and hydrodesulphurization (HDS) reactions. Kinetic studies for HDN and HDS reactions were studied within the temperature range of 340 to 400 degrees C using the power law model and the Langmuir-Hinshelhood model. It was shown that HDN and HDS of heavy gas oil follows first order kinetics. The activation energies for HDN and HDS reactions from the power law and Langmuir-Hinshelhood models were 94 and 96 kJ/mol and 113 and 137 kJ/mol, respectively. It was concluded that nitrogen and hydrogen sulfide adsorption have a significant influence on HDN and HDS reactions. 32 refs., 8 tabs., 7 figs.

The eye of the beholder : oil sands calamity or golden opportunity?

International Nuclear Information System (INIS)

McColl, D.

2009-02-01

Alberta's oil sands deposits are one of the largest hydrocarbon deposits in the world, and the oil sands industry has become a significant driving force in the Canadian economy. However, development in the region has slowed as a result of the recent economic downturn. This paper discussed the future of the oil sands industry, and argued that excess global oil supplies will need to be consumed before the industry fully recovers. Increased liquidity and higher oil prices are also required in order to help the industry recover. Oil sands data were aggregated and classified according to their various stages of development. Projections of bitumen production were based on the summation of all announced projects. Assumptions were adjusted to reflect current and likely near-term future outlooks for oil sands development. Results of the study indicated that the pace of development is expected to slow. Current leases will be developed at a slower pace. Prices in excess of $70 will be required for the industry to continue expanding as well as to generate a rate of return that can be reinvested into the Canadian economy. It was concluded that opportunities for current oil sands operators and new project proponents should take advantage of lower prices to source materials and equipment. 3 figs

Highly effective ionic liquids for biodiesel production from waste vegetable oils

Directory of Open Access Journals (Sweden)

Fathy A. Yassin

2015-03-01

Full Text Available As conventional energy sources deplete, the need for developing alternative energy resources which are environment friendly becomes more imperative. Vegetable oils are attracting increased interest in this purpose. The methanolysis of vegetable oil to produce a fatty acid methyl ester (FAME, i.e., biodiesel fuel was catalyzed by commercial ionic liquid and its chloride modification. The imidazolium chloride ionic liquid was frequently chosen for the synthesis of biodiesel. The dual-functionalized’ ionic liquid is prepared by a direct combination reaction between imidazolium cation and various metal chlorides such as CoCl2, CuCl2, NiCl2, FeCl3 and AlCl3. Imidazolium tetrachloroferrate was proved to be a selective catalyst for the methanolysis reaction at a yield of 97% when used at 1:10, catalyst: oil ratio for 8 h at 55 °C. Operational simplicity, reusability of the used catalyst for 8 times at least, high yields and no saponification are the key features of this methodology. The dynamic viscosity and density of the upgraded vegetable oil decreased from 32.1 cP and 0.9227 g/cm3 to 10.2 cP and 0.9044 g/cm3 respectively, compared to those of the base vegetable oil. The objective of this study was the synthesis and characterization of biodiesel using commercial ionic liquid and its chloride modification. The ionic liquid catalysts were characterized using FTIR, Raman spectroscopy, DSC, TG and UV.

ELASTICITY OF BITUMEN BINDERS AND THE FACTORS CAUSING IT

Directory of Open Access Journals (Sweden)

A. Galkin

2015-12-01

Full Text Available The article deals with the influence of the initial bitumen penetration grade and different con-centrations of the mineral filler on the elasticity of the polymer-modified bitumen (PMB with 3 and 6 % of SBS type polymer. The dependences of elasticity of the PMB on the test conditions – such as the temperature and the stress state level are shown additionally.

In situ viscosity of oil sands using low field NMR

International Nuclear Information System (INIS)

Bryan, J.; Moon, D.; Kantzas, A.

2005-01-01

In heavy oil and bitumen reservoirs, oil viscosity is a vital piece of information that will have great bearing on the chosen EOR scheme and the recovery expected. Prediction of in situ viscosity with a logging tool would he very beneficial in reservoir characterization and exploitation design. Low field NMR is a technology that has shown great potential as a tool for characterizing hydrocarbon properties in heavy oil and bitumen reservoirs. An oil viscosity correlation has previously been developed that is capable of providing order of magnitude viscosity estimates for a wide range of oils taken from various fields in Alberta. This paper presents tuning procedures to improve the NMR predictions for different viscosity ranges, and extends the NMR viscosity model to in situ heavy oil in unconsolidated sands. The results of this work show that the NMR oil peak can be de-convoluted from the in situ signals of the oil and water, and the bulk viscosity correlation that was developed for bulk oils can he applied to predict the in situ oil viscosity. These results can be translated to an NMR logging tool algorithm, allowing for in situ measurements of oil viscosity at the proper reservoir conditions. (author)

Experimental investigations on a diesel engine operated with fuel blends derived from a mixture of Pakistani waste tyre oil and waste soybean oil biodiesel.

Science.gov (United States)

Qasim, Muhammad; Ansari, Tariq Mahmood; Hussain, Mazhar

2017-10-18

The waste tyre and waste cooking oils have a great potential to be used as alternative fuels for diesel engines. The aim of this study was to convert light fractions of pyrolysis oil derived from Pakistani waste vehicle tyres and waste soybean oil methyl esters into valuable fuel and to reduce waste disposal-associated environmental problems. In this study, the waste tyre pyrolysis liquid (light fraction) was collected from commercial tyre pyrolysis plant and biodiesel was prepared from waste soybean oil. The fuel blends (FMWO10, FMWO20, FMWO30, FMWO40 and FMWO50) were prepared from a 30:70 mixture of waste tyre pyrolysis liquid and waste soybean oil methyl esters with different proportions of mineral diesel. The mixture was named as the fuel mixture of waste oils (FMWO). FT-IR analysis of the fuel mixture was carried out using ALPHA FT-IR spectrometer. Experimental investigations on a diesel engine were carried out with various FMWO blends. It was observed that the engine fuel consumption was marginally increased and brake thermal efficiency was marginally decreased with FMWO fuel blends. FMWO10 has shown lowest NOx emissions among all the fuel blends tested. In addition, HC, CO and smoke emissions were noticeably decreased by 3.1-15.6%, 16.5-33.2%, and 1.8-4.5%, respectively, in comparison to diesel fuel, thereby qualifying the blends to be used as alternative fuel for diesel engines.

Role of crude oil in the genesis of Mississippi Valley-type deposits. Evidence from the Cincinnati arch

Energy Technology Data Exchange (ETDEWEB)

Kesler, S.E.; Jones, H.D. (Univ. of Michigan, Ann Arbor, MI (United States)); Furman, F.C. (Univ. of Missouri, Rolla, MO (United States)); Sassen, R. (Texas A M Univ., College Station, TX (United States)); Anderson, W.H. (Univ. of Kentucky, Lexington, KY (United States)); Kyle, J.R. (Univ. of Texas, Austin, TX (United States))

1994-07-01

Mississippi Valley-type (MVT) sulfide minerals and oil from deposits along the Cincinnati arch have almost identical [delta][sup 34]S values (-9% to +9% for MVT sulfides, -12% to +9% for oils). These values are very similar to those for MVT sulfides and oil in the Illinois-Kentucky district and support their proposed inclusion in a regional hydrothermal system. Many MVT deposits with low [delta][sup 34]S values are closely associated with oil, whereas MVT deposits with high [delta][sup 34]S values often contain bitumen. Reduced sulfur in MVT deposits with high [delta][sup 34]S values probably came from thermochemical sulfate reduction, whereas that in MVT deposits with low [delta][sup 34]S values probably came from oil and related organic matter. Oil-related sulfur could have been derived from oil fields or disseminated oil and other organic matter in regional wallrocks. 44 refs., 3 figs., 2 tabs.

US crude oil, natural gas, and natural gas liquids reserves, 1992 annual report

Energy Technology Data Exchange (ETDEWEB)

1993-10-18

This report presents estimates of proved reserves of crude oil, natural gas, and natural gas liquids as of December 31, 1992, as well as production volumes for the United States, and selected States and State subdivisions for the year 1992. Estimates are presented for the following four categories of natural gas: total gas (wet after lease separation), its two major components (nonassociated and associated-dissolved gas), and total dry gas (wet gas adjusted for the removal of liquids at natural gas processing plants). In addition, two components of natural gas liquids, lease condensate and natural gas plant liquids, have their reserves and production data presented. Also included is information on indicated additional crude oil reserves and crude oil, natural gas, and lease condensate reserves in nonproducing reservoirs. A discussion of notable oil and gas exploration and development activities during 1992 is provided.

US crude oil, natural gas, and natural gas liquids reserves, 1992 annual report

International Nuclear Information System (INIS)

1993-01-01

This report presents estimates of proved reserves of crude oil, natural gas, and natural gas liquids as of December 31, 1992, as well as production volumes for the United States, and selected States and State subdivisions for the year 1992. Estimates are presented for the following four categories of natural gas: total gas (wet after lease separation), its two major components (nonassociated and associated-dissolved gas), and total dry gas (wet gas adjusted for the removal of liquids at natural gas processing plants). In addition, two components of natural gas liquids, lease condensate and natural gas plant liquids, have their reserves and production data presented. Also included is information on indicated additional crude oil reserves and crude oil, natural gas, and lease condensate reserves in nonproducing reservoirs. A discussion of notable oil and gas exploration and development activities during 1992 is provided

Comparative study of modified bitumen binder properties collected from mixing plant and quarry.

Science.gov (United States)

Mustafa Kamal, M.; Abu Bakar, R.; Hadithon, K. A.

2017-11-01

Quality control and assurance are essential in pavement construction. In general, the properties of bitumen change as it ages in bulk storage, transport, and storage on site. The minimization of bituminous hardening during storing, transportation and mixing depends on careful control of binder temperature. Hence therefore, bitumen should always be stored and handled at the lowest temperature possible, consistent with efficient use. The objective of the work is to monitor the quality of bitumen samples collected from mixing plant and quarry. Results showed that, samples modified bitumen which collected from quarry showed some adverse effects on rheological properties and physical properties after subjecting to high temperature storage within a period of time. The dynamic stiffness, elastic properties and other common binder properties were deteriorated too. The chemical changes that occurred during storage were analysed using Fourier transform infra-red spectroscopy (FTIR). Thus studies developed an understanding of bitumen ageing in storage.

Heavy and hot : bitumen-specific technology fuels growth at Cold Lake-Bonnyville

Energy Technology Data Exchange (ETDEWEB)

Byfield, M.

2008-08-15

The bitumen corridor between Fort McMurray, Wood Buffalo, and the Cold Lake region is now providing more than half of the province's total crude oil. Growth in the region has been attributed to new technology developments for oil sands drilling and production. Progressive cavity pumps (PCPs) are estimated to have increased production at the Lloyd minister site by 75 per cent. New steel-on-steel pumps have been designed to withstand temperatures of 350 degrees C. The pumps do not require the use of elastomers to line the steel stator. The region's production levels have also been boosted by the use of drilling megapads capable of improving recovery levels by 20 per cent. Many of the region's operators are now using combined steam assisted gravity drainage (SAGD), cyclic steam stimulation (CSS) and cold production technologies. Despite the use of advanced technologies, development in the region is still inhibited by manpower shortages. Oil companies operating in the region are now working to build adequate municipal infrastructure for new employees, and are offering substantial bonuses to entice new workers to relocate to the region. 2 figs.

Common ground : bitumen and gas producers come together to find gas-over-bitumen solutions

Energy Technology Data Exchange (ETDEWEB)

Ross, E.

2005-08-01

The gas-over-bitumen issue has meant that hundreds of natural gas wells remain closed while regulatory hearings and research activities continue. The Alberta Energy and Utilities Board should soon reach a final decision on the status of gas wells considered to be a threat to thermal extraction of underlying oil sands. This article discussed collaborative efforts by oil and gas companies to resolve these issues, including the use of fluid injection technology, low pressure Steam-Assisted Gravity Drainage (SAGD) and artificial lift. The objective of the Gas Reinjection and Production Experiment (GRIPE) is to reinject gas to displace natural gas being produced. The pilot project, conducted by Paramount Resources Ltd., consists of 2 injector wells, 4 producers and 12 observation wells that measure gas pressure in the reservoir. The project also includes a 2 stage compressor modified to handle flue gas. According to reservoir simulations, Paramount should be able to recover between 50 to 60 per cent of the remaining gas in place. Results from the pilot suggest that the technique could result in more than half the currently shut-in pools being re-opened. It was suggested that gas-by-gas displacement may result in higher recovery rates because there is usually more remaining gas in place. It was noted that EnCana Corporation has also been repressurizing a depleted natural gas pool by injecting compressed air rather than flue gas. Various other projects were reviewed, including the use of electric submersible pumps, low pressure SAGD and new SAGD well pair configurations. It was concluded that the artificial lift and low pressure SAGD technical sub-committee have now filed 10 applications for funding under the Alberta Energy Department's Innovative Energy Technology Program.

Effects of operating conditions on compositional characteristics and reaction kinetics of liquid derived by delayed coking of nigerian petroleum residue

Directory of Open Access Journals (Sweden)

O. O. Bello

2006-09-01

Full Text Available The thermal upgrading of Nigerian petroleum residue was studied at relatively low pressure in a delayed coking reactor system. In this work, the intent was to investigate the effects of process variables such as reaction temperature (200(0C to 600(0C, reaction time (0 to 120min, additive concentration loading and additive-to-residue ratio on the amounts and quality of organic liquid product (OLP. The liquid products derived from the delayed coking process were characterized by means of instrumental analysis of gas-liquid chromatography. Results obtained from the analyses of the OLP revealed an upward trend of the conversion process and the selectivity of the aromatic compounds with additive-to-residue ratio (ARR and increase in temperature. This led to maximum yield of 37.2% achieved with ARR of 5 compared to 31% achieved with ordinary thermal conversion. The selectivity for aromatic hydrocarbons was maximum at 83.1wt% the selectivity towards aromatics and aliphatic hydrocarbons were highest for methanol-potassium hydroxide and methanol respectively. In all additive system cases, maximum OLP was produced at an optimum reaction temperature of 370(0C in the delayed coking reactor and at higher residence time. The gaseous product consisted of carbon monoxide and carbon dioxide and C1 - C6 hydrocarbons, which amounted to about 20 to 30 wt% of liquid distillate. The information obtained in this study show that the organic liquid products are amenable to characterization procedure and provided the basis for the identification of processes for upgrading Nigerian petroleum residue and such other starting materials such as bitumen or fossil fuel coal liquids.

Analysis of heavy oils: Method development and application to Cerro Negro heavy petroleum

Energy Technology Data Exchange (ETDEWEB)

None

1989-12-01

On March 6, 1980, the US Department of Energy (DOE) and the Ministry of Energy and Mines of Venezuela (MEMV) entered into a joint agreement which included analysis of heavy crude oils from the Venezuelan Orinoco oil belt. The purpose of this report is to present compositional data and describe new analytical methods obtained from work on the Cerro Negro Orinoco belt crude oil since 1980. Most of the chapters focus on the methods rather than the resulting data on Cerro Negro oil, and results from other oils obtained during the verification of the method are included. In addition, published work on analysis of heavy oils, tar sand bitumens, and like materials is reviewed, and the overall state of the art in analytical methodology for heavy fossil liquids is assessed. The various phases of the work included: distillation and determination of routine'' physical/chemical properties (Chapter 1); preliminary separation of >200{degrees} C distillates and the residue into acid, base, neutral, saturated hydrocarbon and neutral-aromatic concentrates (Chapter 2); further separation of acid, base, and neutral concentrates into subtypes (Chapters 3--5); and determination of the distribution of metal-containing compounds in all fractions (Chapter 6).

Analysis of heavy oils: Method development and application to Cerro Negro heavy petroleum

Energy Technology Data Exchange (ETDEWEB)

Carbognani, L.; Hazos, M.; Sanchez, V. (INTEVEP, Filial de Petroleos de Venezuela, SA, Caracas (Venezuela)); Green, J.A.; Green, J.B.; Grigsby, R.D.; Pearson, C.D.; Reynolds, J.W.; Shay, J.Y.; Sturm, G.P. Jr.; Thomson, J.S.; Vogh, J.W.; Vrana, R.P.; Yu, S.K.T.; Diehl, B.H.; Grizzle, P.L.; Hirsch, D.E; Hornung, K.W.; Tang, S.Y.

1989-12-01

On March 6, 1980, the US Department of Energy (DOE) and the Ministry of Energy and Mines of Venezuela (MEMV) entered into a joint agreement which included analysis of heavy crude oils from the Venezuelan Orinoco oil belt.The purpose of this report is to present compositional data and describe new analytical methods obtained from work on the Cerro Negro Orinoco belt crude oil since 1980. Most of the chapters focus on the methods rather than the resulting data on Cerro Negro oil, and results from other oils obtained during the verification of the method are included. In addition, published work on analysis of heavy oils, tar sand bitumens, and like materials is reviewed, and the overall state of the art in analytical methodology for heavy fossil liquids is assessed. The various phases of the work included: distillation and determination of routine'' physical/chemical properties (Chapter 1); preliminary separation of >200{degree}C distillates and the residue into acid, base, neutral, saturated hydrocarbon and neutral-aromatic concentrates (Chapter 2); further separation of acid, base, and neutral concentrates into subtypes (Chapters 3-5); and determination of the distribution of metal-containing compounds in all fractions (Chapter 6).

An investigation of problematic solids in oil sands processing : separation and characterization of organic matter strongly bound to oil sands solids

Energy Technology Data Exchange (ETDEWEB)

McCracken, T.; Woods, J.R.; Kung, J.; Fu, D.; Kingston, D.; Kotlyar, L.S. [National Research Council of Canada, Ottawa, ON (Canada). Inst. for Chemical Process and Environmental Technology; Sparks, B.D. [V. Bede Technical Associates, Ottawa, ON (Canada)

2009-07-01

Some of the solid fractions in Athabasca oilsands are associated with strongly bound organic matter that is insoluble in toluene, a solvent commonly used to extract bitumen. The presence of toluene insoluble organic matter (TIOM) increases oil wettability of solids which may adversely affect the release of bitumen from the oilsands. Some of the solid material from the coking operation may be carried over to downstream operations where it can cause fouling. This study used supercritical fluid extraction with methanol to remove TIOM from oilsands after extraction of bitumen by toluene. The methanol extract (ME) is soluble in toluene and was analyzed. Results were compared with corresponding bitumen fractions prepared using a modified HPLC SARA separation technique. Number average molecular weights for the ME were similar to those for resins separated from bitumen. The study also showed that the number of alkyl substituents on aromatic ring systems and the lengths of paraffinic straight chains for resins and ME samples were similar, with only minor differences in terms of H/C atomic ratios and aromaticities. The ME was more polar than the resin and asphaltene fractions, which may explain the selective adsorption of this fraction. tabs., figs.

It's all about the bitumen : oilsands producers have the attention of the world

International Nuclear Information System (INIS)

Jaremko, D.

2005-01-01

Within 10 years, oilsands growth will make Canada the fifth largest oil producing country in the world, thereby greatly increasing Canada's political power. A review of oil sands development was presented, with reference to the way in which Steam Assisted Gravity Drainage (SAGD) has revolutionized the industry. Recent acquisitions have pointed to the growing level of international interest in the oilsands industry. Construction details of the Surmont project were discussed along with Devon Canada's SAGD project at Jackfish where about 100 well-pairs are expected to be drilled. Petrobank Energy and Resources is constructing its Whitesands project, which will employ the first field-scale application of the toe-to-heel air injection (THAI) recovery method which has lower operating costs and which uses less water and creates fewer greenhouse (GHG) emissions. The pilot was designed to produce up to 1800 barrels per day of partially upgraded bitumen. Details of CNRI's Horizon project were presented, including construction plans and schedules. Shell Canada's increased budget for the first expansion of the Athabasca Oilsands Project was reviewed with reference to their strategic decision to pre-build infrastructure for future expansions. Details of Suncor Energy's production goals were also reviewed, including details of new upgraders and applications. Syncrude's continuing expansions were discussed, as well as their current production levels. An outline of UTS Energy Corporation and Petro-Canada's plans concerning the Fort Hills Mining Project was presented, with details of the new BITMIN extraction process. It was noted that Imperial Oil has filed regulatory applications for the Kearl Oilsands Project, which have estimated total recoverable bitumen resources of 4.4 billion barrels. Husky Energy's Sunrise Project was discussed, as well as MEG Energy's regulatory approval for the first phase of the Christina Lake Regional Project. The Canadian Association of Petroleum

Techno-economic assessment of hydrogen production from underground coal gasification (UCG) in Western Canada with carbon capture and sequestration (CCS) for upgrading bitumen from oil sands

International Nuclear Information System (INIS)

Olateju, Babatunde; Kumar, Amit

2013-01-01

Highlights: • Development of a techno-economic model for UCG-CCS and SMR-CCS. • Estimation of H 2 production costs with and without CCS for UCG and SMR. • UCG is more economical for H 2 production with CCS. • SMR is more cost efficient for H 2 production without CCS. • Cost competiveness is highly sensitive to the IRR differential between UCG and SMR. - Abstract: This paper examines the techno-economic viability of hydrogen production from underground coal gasification (UCG) in Western Canada, for the servicing of the oil sands bitumen upgrading industry. Hydrogen production for bitumen upgrading is predominantly achieved via steam methane reforming (SMR); which involves significant greenhouse gas (GHG) emissions along with considerable feedstock (natural gas) cost volatility. UCG is a formidable candidate for cost-competitive environmentally sustainable hydrogen production; given its negligible feedstock cost, the enormity of deep coal reserves in Western Canada and the favourable CO 2 sequestration characteristics of potential UCG sites in the Western Canadian sedimentary basin (WCSB). Techno-economic models were developed for UCG and SMR with and without CCS, to estimate the cost of hydrogen production including delivery to a bitumen upgrader. In this paper, at base case conditions, a 5% internal rate of return (IRR) differential between UCG and SMR was considered so as to account for the increased investment risk associated with UCG. The cost of UCG hydrogen production without CCS is estimated to be $1.78/kg of H 2 . With CCS, this increases to range of $2.11–$2.70/kg of H 2 , depending on the distance of the site for CO 2 sequestration from the UCG plant. The SMR hydrogen production cost without CCS is estimated to be $1.73/kg of H 2 . In similar fashion to UCG, this rises to a range of $2.14 to $2.41/kg of H 2 with the consideration of CCS. Lastly, for hydrogen production without CCS, UCG has a superior cost competitiveness in comparison to SMR

Sulphur output from oil sands : dramatically changing Alberta's sulphur balance

Energy Technology Data Exchange (ETDEWEB)

D' Aquin, G. [Con-Sul Inc., Bigfork, MT (United States)

2008-07-01

This paper discussed sulphur production from Alberta's gas and oil sands industries. While sulfur derived from natural gas production in the province is expected to decline as natural gas reserves diminish, Alberta's oil sands contain high amounts of sulphur. It is not yet known how much sulphur will be produced from the province's oil sands facilities. Alberta had considerable stockpiles of sulphur in the 1970s. By 1980, inventories began to decline. By 1996, output had increased to 7.1 million tonnes. Alberta's sulphur inventory reached 9.7 million tonnes following the collapse of the Soviet Union's government mandated fertilizer industry. In 2006, sulphur supplies in Alberta reached 12 million tonnes. Reduced global output has now lowered sulphur stockpiles. Increases in sulphur prices tend to reduce market demand, and lower prices will not typically change the volume of sulphur produced as a byproduct of oil and gas operations. Bitumen-derived sulphur output is expected to exceed gas-derived sulphur output in the near future. Sulphur from oil sands processing is expected to increase by 5 million tonnes by 2017. Increased sulphur production levels in Alberta will present a significant challenge for all sectors of the hydrocarbon industry. It was concluded that developing a plan for storing, selling or disposing of the sulphur will help to ensure the profitability of oil sands operations.

The interaction between bitumen matrix and chemical components of radioactive wastes of WWER type

International Nuclear Information System (INIS)

Selucky, P.; Sazavsky, P.; Peka, V.; Krupka, M.

2000-01-01

The interaction between bitumen matrix and chemical components of WWER type radioactive wastes was studied. So called ''cold'' model bitumen products were prepared and compared with real products using macroDTA method. On the basis of obtained curves, the evaluation of bitumen product fire risks was performed with the aim to minimize risks of bituminization process. (authors)

Upgrading Unconventional Oil Resources with the EST Process

Energy Technology Data Exchange (ETDEWEB)

Delbianco, Alberto; Meli, Salvatori; Panariti, Nicolleta; Rispoli, Giacomo

2007-07-01

We strongly believe that unconventional oils will play a much larger role in the growth of supply than is currently recognized. As a matter of fact, whereas the earth's conventional proven world oil reserves are 1.3 trillion barrels, extra-heavy plus bitumen resources amount to about 4 trillion barrels. The unconventional oils are characterized by low API gravity (<10), high viscosity and high concentration of poisons such as sulphur, nitrogen, metals, and asphaltenes. For this reason, a key role for the full exploitation of these hydrocarbon resources is played by the downstream processes that are required to upgrade and convert them into valuable products. In this scenario, Eni has developed a novel hydrocracking process (EST: Eni Slurry Technology) which is particularly well-suited for the conversion and upgrading of heavy feedstocks (conventional vacuum residues, extra-heavy oils and bitumen). EST employs nano-sized hydrogenation catalysts and an original process scheme that allow complete feedstock conversion to an upgraded synthetic crude oil (SCO) with an API gravity gain greater than 20 and avoid the production of residual by-products, such as pet-coke or heavy fuel oil. A Commercial Demonstration Unit (CDP) of 1200 bbl/d capacity is successfully operating in the Eni's Taranto refinery since November 2005. (auth)

Preliminary fiscal evaluation of Alberta oil sands terms

International Nuclear Information System (INIS)

Van Meurs, P.

2007-01-01

The cost of oil sands projects varies significantly. While costs have escalated considerably over the past few years, oil prices have gone significantly higher. This report provided an economic evaluation of the current fiscal terms applicable to Alberta oil sands. The analysis was done to evaluate the profitability of oil sand projects to investors under current conditions based on the generic royalty regime based on bitumen values. The objective of the royalty review was to determine whether Albertans received a fair share from their oil and gas resources. It discussed the wide variety of oil sands projects in Alberta using five case studies as examples. Cases involving steam assisted gravity drainage (SAGD) operations were assessed for both the Athabasca Mine and Cold Lake. The report provided a discussion of the economic assumptions including economic cases as well as production, costs and price data. It then provided the preliminary results of the economic-fiscal evaluation from the investor perspective including profitability indicators; international comparisons; internal rate of return; and net present value. The government perspective was also discussed with reference to attractiveness indicators; royalties as a percentage of bitumen values; and non-discounted and discounted government take. A royalty and tax feature analysis was also provided. Several issues for possible further review were also presented. tabs

Modified bitumen for embedding of radioactive wastes

International Nuclear Information System (INIS)

Bozkurt, C.

1984-11-01

This work describes new possibilities of using polymer modified bitumen as matrix material for embedding of low- and medium level radioactive wastes. Epoxy resins, polyurethane resins and styrene-butadiene-copolymers with 20-40 weight per cent are used as modifying agents. Penetration and softening point (ring and ball) of modified samples have been measured. Further the resistance to toluene and leaching rate in n-heptane have been determined. Within these polymer bitumen combinations investigated, the epoxy resins having a high epoxid equivalent weight with dicarbooxylic acid anhydrid hardeners and tertiary amin accelerators give the most dense network, highest thermodimensional stability and lowest leaching rate in organic solvents. 71 refs., 9 figs., 6 tabs

Effect of black rice husk ash on the physical and rheological properties of bitumen

Science.gov (United States)

Romastarika, Raissa; Jaya, Ramadhansyah Putra; Yaacob, Haryati; Nazri, Fadzli Mohamed; Agussabti, Ichwana, Jayanti, Dewi Sri

2017-08-01

Black rice husk ash (BRHA) waste product is inexpensive and can be obtained from rice mills. Reuse of waste product is ideal to reduce pollution, because disposal is decreased or eliminated. The commercial value of BRHA has increased, and it is suitable for use in road construction. In this study, BRHA waste was ground using a grinding ball mill for 120 min to form fine powder. BRHA was then sieved to less than 75 µm. At the laboratory, BRHA was mixed with bitumen to replace 2%, 4%, and 6% of the total weight, whereas 0% represented the control sample. The penetration, softening point, dynamic shear rheometer (DSR) and rolling thin film oven (RTFO) were investigated in this study. Results showed that bitumen became harder, whereas the rate of penetration decreased when the replacement amount of BRHA increased. Softening point test of bitumen also revealed an increase. The short-term aging test revealed that modification of bitumen could relieve the effect of aging. BRHA waste added into bitumen improved the performance of bitumen. Therefore, the usage of BRHA could help improve the performance of road pavement and reduce the rutting effect.

Evaluation of bitumen-rubber asphalt manufactured from modified binder at lower viscosity

CSIR Research Space (South Africa)

O'Connell, Johannes S

2010-08-01

Full Text Available In South Africa, crumb tyre-modified bitumen commnly known as bitumen-rubber binder has viscosity limits specified by the current edition of TG1: The Use of Modified Bituminous Binders in Road Construction. As the crumb rubber is 'digested...

Study of the thermal and mechanical sensitivity of bitumen/oxygen salt mixtures

International Nuclear Information System (INIS)

Backof, E.; Diepold, W.

1975-07-01

The safe handling characteristics of radioactive wastes containing nitrate salts to be fixed in bitumen for ultimate storage in salt mines according to a process developed at the Karlsruhe Nuclear Research Center have been examined with respect to their combustibility and shock sensitivity in tests of inactive bitumen/salt mixtures. Samples containing 40% bitumen and 60% nitrates of alkali, alkaline earth, and heavy metals, organic acids and rare earths were used to determine the thermal sensitivity (ignition temperature, duration of burning, heating under contained conditions), the mechanical sensitivity (shock sensitivity) and, in order to simulate major shock stresses, the sensitivity against detonation stresses. A few basic experiments were also performed on some beta-irradiated inactive samples. It appeared that although the addition of nitrates increased the combustibility of bitumen, neither the high thermal nor the detonation stresses resulted in any explosion-type reaction. (orig.) [de

US crude oil, natural gas, and natural gas liquids reserves 1996 annual report

Energy Technology Data Exchange (ETDEWEB)

NONE

1997-12-01

The EIA annual reserves report series is the only source of comprehensive domestic proved reserves estimates. This publication is used by the Congress, Federal and State agencies, industry, and other interested parties to obtain accurate estimates of the Nation`s proved reserves of crude oil, natural gas, and natural gas liquids. These data are essential to the development, implementation, and evaluation of energy policy and legislation. This report presents estimates of proved reserves of crude oil, natural gas, and natural gas liquids as of December 31, 1996, as well as production volumes for the US and selected States and State subdivisions for the year 1996. Estimates are presented for the following four categories of natural gas: total gas (wet after lease separation), nonassociated gas and associated-dissolved gas (which are the two major types of wet natural gas), and total dry gas (wet gas adjusted for the removal of liquids at natural gas processing plants). In addition, reserve estimates for two types of natural gas liquids, lease condensate and natural gas plant liquids, are presented. Also included is information on indicated additional crude oil reserves and crude oil, natural gas, and lease condensate reserves in nonproducing reservoirs. A discussion of notable oil and gas exploration and development activities during 1996 is provided. 21 figs., 16 tabs.

Asian interests in Alberta oil sands

International Nuclear Information System (INIS)

Du Plessis, D.; Laureshen, C.

2004-01-01

The growing Asian interest in Alberta's oil sands and import opportunities was discussed along with the feasibility of marketing bitumen to Asia. Asia is an obvious new market for Canadian heavy oil and bitumen due to an increasing demand for petroleum products in Japan, Korea, Taiwan and China. This paper examined the following three criteria that will determine the success of any initiative to move Canadian crude oil to Asian-Pacific markets: (1) a sustainable supply from Alberta; a pipeline to transport the crude to a deepwater port on the west coast; and, a guaranteed market at the other end. The basis for Asian interest in Alberta's oil sands is the sustainable secure supply of oil for growing Asian markets; heavy dependence on supplies from the Middle East; the desire to diversify supply sources; and, opportunities to invest in oil sands developments. Examples of Asian (Japan, Korea, Taiwan and China) missions to Alberta were presented along with the challenges of getting products to market with reference to Enbridge's new market access plan, Terasen's staged capacity expansion for heavy crudes and refined products, and sea transport from Prince Rupert. The paper also included graphs depicting world GDP; incremental increase in world primary energy demand by fuel for 2000 to 2020; world oil demand by region; oil demand by region in Asia; oil demand and supply in northeast Asia (Japan, China, Korea) and dependence level on Middle Eastern oil; oil demand and supply in China; China's petroleum production and consumption; refined products market forecast for 2000 to 2020; 2002 crude oil imports to Asia; 2004 refining capacity; product quality comparisons; cost competitive study; and energy policy objectives for China, Japan, Korea and Taiwan. 19 figs

Evaluation of bitumens for nuclear facilities radioactive waste immobilization

International Nuclear Information System (INIS)

Guzella, Marcia F.R.; Silva, Tania V. da; Loiola, Roberto; Monte, Lauro J.B.

2000-01-01

The activities developed at the Nuclear Technology Development Centre, Centro de Desenvolvimento da Tecnologia Nuclear - CDTN/CNEN, include the research and development work of the radioactive wastes immobilization in different kind of bitumen. The present work describes the bituminization of simulated low level wastes of evaporator concentrates.Two types of bitumen are used for incorporation of the simulated wastes generated by nuclear power plants. Studies on rheological properties, leaching data, differential thermoanalysis and water content of the waste-products have been carried out. (author)

Liquidity effects and FFA returns in the international shipping derivatives market

OpenAIRE

Alizadeh, Amir H.; Kappou, K; Tsouknidis, Dimitris; Visvikis, Ilias

2015-01-01

The study examines the impact of liquidity risk on freight derivatives returns. The Amihud liquidity ratio and bid–ask spreads are utilized to assess the existence of liquidity risk in the freight derivatives market. Other macroeconomic variables are used to control for market risk. Results indicate that liquidity risk is priced and both liquidity measures have a significant role in determining freight derivatives returns. Consistent with expectations, both liquidity measures are found to hav...

Market opportunities and challenges for oil sands

International Nuclear Information System (INIS)

Wise, T.H.

2004-01-01

The use of Alberta bitumen as a clean fuel depends on upgrading, transportation, and refining processes. Forecasts show that oil sands production, which includes synthetic crude oil (SCO), will surpass declining conventional production from the Western Canada Sedimentary Basin. The challenges facing the oils sands processing industry include: crude oil prices which affect the producer's market; market expansion options; diluent availability/cost; supply cost competitiveness; and, regional processing. The common market issues include light/heavy crude prices, oil sands crude qualities, prices of oil sands crudes, pipeline infrastructure, and competitive supplies. The issues facing the refiners are: refining margins, security of crude supply, refined product quality, and competitive product supply. It was noted that Alberta must retain or increase its share of the Midwest market. The market expansion options were reviewed for both downstream (refining) and upstream (upgrading) operations. New pipeline capacity is needed to reach more distant markets such as Southern Midwest, Washington, and California. The market is nearly saturated for Canada's heavy oil supply. More upgrading will be required as bitumen production increases. Market growth is still possible for Canada's SCO but according to forecasts, the market could also become saturated. To increase demand and allow supplies to grow, SCO prices may fall below light crude prices. It was noted that a balance must be achieved in order for producers to increase production and for refiner/upgraders to expand their conversion capacity. 13 figs

Mechanical Properties of Millet Husk Ash Bitumen Stabilized Soil Block

Directory of Open Access Journals (Sweden)

M. T. Abdulwahab

2017-06-01

Full Text Available This study presents an investigation into the improvement of strength and durability properties of lateritic soil blocks using Millet Husk Ash (MHA and Bitumen as additives so as to reduce its high cost and find alternative disposal method for agricultural waste. The lateritic soil samples were selected and treated with 0%, 10%, 15%, 20%, 30%, 40% and 50% of MHA by weight of laterite. The lateritic soil-MHA mixture was later admixed with 0%, 2%, 4%, 6%, 8%, 10%, 12% and 14% cut-back bitumen solution by weight of laterite. Both the natural lateritic soil, lateritic and MHA, and the blend of Soil, MHA and Bitumen were first subjected to physical and chemical analysis using X-Ray Fluorescence (XRF and Scanning Electromagnetic Machine (SEM to determine their engineering properties followed by the performance test on bricks cast with varying quantities of the additives. A total of one hundred and ninety two (192 cubes were tested for moisture absorption, erodability and compressive strength tests. The result of the test showed that MHA and Bitumen acted as pozzolana in performance test on the soil blocks. Up to 30% MHA – laterite and 20% MHA admixed with 8% laterite were found to give optimum compressive strength of 10.8N/mm2 and 10.9N/mm2 for the bricks produced. The result also showed that about 50% MHA blended with 14% Bitumen solution ensured water tight bricks. Thus the use of MHA as partial replacement of cement will provide an economic use of by-product and consequently produce a cheaper soil block construction without comprising its strength.

Development of the Write Process for Pipeline-Ready Heavy Oil

Energy Technology Data Exchange (ETDEWEB)

Lee Brecher; Charles Mones; Frank Guffey

2009-03-07

Work completed under this program advances the goal of demonstrating Western Research Institute's (WRI's) WRITE{trademark} process for upgrading heavy oil at field scale. MEG Energy Corporation (MEG) located in Calgary, Alberta, Canada supported efforts at WRI to develop the WRITE{trademark} process as an oil sands, field-upgrading technology through this Task 51 Jointly Sponsored Research project. The project consisted of 6 tasks: (1) optimization of the distillate recovery unit (DRU), (2) demonstration and design of a continuous coker, (3) conceptual design and cost estimate for a commercial facility, (4) design of a WRITE{trademark} pilot plant, (5) hydrotreating studies, and (6) establish a petroleum analysis laboratory. WRITE{trademark} is a heavy oil and bitumen upgrading process that produces residuum-free, pipeline ready oil from heavy material with undiluted density and viscosity that exceed prevailing pipeline specifications. WRITE{trademark} uses two processing stages to achieve low and high temperature conversion of heavy oil or bitumen. The first stage DRU operates at mild thermal cracking conditions, yielding a light overhead product and a heavy residuum or bottoms material. These bottoms flow to the second stage continuous coker that operates at severe pyrolysis conditions, yielding light pyrolyzate and coke. The combined pyrolyzate and mildly cracked overhead streams form WRITE{trademark}'s synthetic crude oil (SCO) production. The main objectives of this project were to (1) complete testing and analysis at bench scale with the DRU and continuous coker reactors and provide results to MEG for process evaluation and scale-up determinations and (2) complete a technical and economic assessment of WRITE{trademark} technology to determine its viability. The DRU test program was completed and a processing envelope developed. These results were used for process assessment and for scaleup. Tests in the continuous coker were intended to

U.S. crude oil, natural gas, and natural gas liquids reserves 1997 annual report

Energy Technology Data Exchange (ETDEWEB)

Wood, John H.; Grape, Steven G.; Green, Rhonda S.

1998-12-01

This report presents estimates of proved reserves of crude oil, natural gas, and natural gas liquids as of December 31, 1997, as well as production volumes for the US and selected States and State subdivisions for the year 1997. Estimates are presented for the following four categories of natural gas: total gas (wet after lease separation), nonassociated gas and associated-dissolved gas (which are the two major types of wet natural gas), and total dry gas (wet gas adjusted for the removal of liquids at natural gas processing plants). In addition, reserve estimates for two types of natural gas liquids, lease condensate and natural gas plant liquids, are presented. Also included is information on indicated additional crude oil reserves and crude oil, natural gas, and lease condensate reserves in nonproducing reservoirs. A discussion of notable oil and gas exploration and development activities during 1997 is provided. 21 figs., 16 tabs.

Fuel options for oil sands

International Nuclear Information System (INIS)

Wise, T.

2005-01-01

This presentation examined fuel options in relation to oil sands production. Options include steam and hydrogen (H 2 ) for upgrading; natural gas by pipeline; bitumen; petroleum coke; and coal. Various cost drivers were also considered for each of the fuel options. It was noted that natural gas has high energy value but the capital cost is low, and that coke's energy value is very low but the capital cost is high. A chart forecasting energy prices was presented. The disposition of Western Canada's northern gas situation was presented. Issues concerning rail transportation for coal were considered. Environmental concerns were also examined. A chart of typical gas requirements for 75,000 B/D oil sands projects was presented. Issues concerning steam generation with gas and mining cogeneration with gas fuel and steam turbines were discussed, as well as cogeneration and H 2 with gas fuels and steam turbines. Various technology and fuel utility options were examined, along with details of equipment and processes. Boiler technologies were reviewed by type as well as fuel and steam quality and pressure. Charts of cogeneration with gas turbine and circulation fluid bed boilers were presented. Gasification processes were reviewed and a supply cost basis was examined. Cost drivers were ranked according to energy, operating considerations and capital investment. Results indicated that fuel costs were significant for gas and coal. Capital costs and capital recovery charge was most significant with coal and gasification technology. Without capital recovery, cash costs favour the use of bitumen and coke. Gasification would need lower capital and lower capital recovery to compete with direct burning. It was concluded that direct burning of bitumen can compete with natural gas. With price volatility anticipated, dual fuel capability for bitumen and gas has merit. Petroleum coke can be produced or retrieved from stockpiles. Utility supply costs of direct burning of coke is

21 CFR 172.862 - Oleic acid derived from tall oil fatty acids.

Science.gov (United States)

2010-04-01

... 21 Food and Drugs 3 2010-04-01 2009-04-01 true Oleic acid derived from tall oil fatty acids. 172... FOOD FOR HUMAN CONSUMPTION Multipurpose Additives § 172.862 Oleic acid derived from tall oil fatty acids. The food additive oleic acid derived from tall oil fatty acids may be safely used in food and as...

Oxidative desulfurization of dibenzothiophene from model oil using ionic liquids as extracting agent

Science.gov (United States)

Taha, Mohd F.; Atikah, N.; Chong, F. K.; Shaharun, Maizatul S.

2012-09-01

The oxidative desulfurization of dibenzothiophene (DBT) from model oil (in n-dodecane) was carried out using ionic liquid as the extractant and catalyst, and hydrogen peroxide (H2O2) in combination with acetic acid (CH3COOH) and sulphuric acid (H2SO4) as the oxidant. The ionic liquids used were 1-butyl-3-methylimidazolium octyl sulphate ([Bmim][OcSO4]) and 1-butyl-3-methylimidazolium acetate ([Bmim][Ac]). The effect of the amounts of H2O2 on oxidative desulphurization of model oil was first investigated without the usage of ionic liquids at room temperature. The results indicate that greater amount of H2O2 give higher desulfurization and the maximum desulfurization in this study, i.e. 34 %, was occurred when the molar ratio of H2O2 to sulfur was 5:1. With the usage of ionic liquid and the molar ratio of 5:1 (H2O2:sulfur), the efficiency of DBT removal from model oil was increased significantly in terms of percent removal and removal time. Ionic liquid of [Bmim][OcSO4] performed better than [Bmim][Ac] with 72 % DBT removal. When molar ratio of H2O2 to sulphur was 5:1, volume ratio of ionic liquid to model oil was 1:1 and mixing time was 60 min at room temperature. The results indicate the potential of ionic liquids as the extractant and catalyst for oxidative desulfurization of hydrocarbon fuels.

Canada's oil sands: nuclear power in an integrated energy economy

Energy Technology Data Exchange (ETDEWEB)

Isaacs, E. [Alberta Energy Research Inst., Calgary, Alberta (Canada)

2008-07-01

This paper discusses the role of nuclear power in Canada's oil sands industry. It outlines the oil sands resource in Alberta and the various industrial projects to recover the oil from the tar sands. It points to continuing innovation in technology since the 1930's. The hydrogen required for upgrading bitumen is made from natural gas. Finally, it discusses the next wave of oil sands production technologies.

Transesterification of waste oil to biodiesel using Brønsted acid ionic liquid as catalyst

Directory of Open Access Journals (Sweden)

C. Xie

2013-05-01

Full Text Available Brønsted acid ionic liquids were employed for the preparation of biodiesel using waste oil as the feedstock. It was found that IL 1–(3–sulfonic acidpropyl–3–methylimidazole hydrosulfate–[HO3S-pmim]HSO4 was an efficient catalyst for the reaction under the optimum conditions: n(oil:n(methanol 1:12, waste oil 15.0 g, ionic liquid 2.0 g, reaction temperature 120 oC and reaction time 8 h, the yield of biodiesel was more than 96%. The reusability of the ionic liquid was also investigated. When the ionic liquid was repeatedly used for five times, the yield of product was still more than 93%. Therefore, an efficient and environmentally friendly catalyst was provided for the synthesis of biodiesel from waste oils.

Biodegradation of bituminous products from processing liquid radioactive wastes

International Nuclear Information System (INIS)

Tibensky, L.; Krejci, F.; Hladky, E.; Halama, D.

1988-01-01

One of the possible ways of disturbing the stability of bituminous products from liquid radioactive waste processing, is biodegradation caused by common microorganisms. Pseudomonas bacteria and a Bacillus cereus culture were selected for experimental study of cultivation of microorganisms. Experiments with mixed cultures were also performed. Pitches, ajatin and imidazoline were used as inhibitors. The thin layer and the emulsion methods were used in assessing biological corrosion. The results of the experiments are discussed with respect to the dependence of bacterial growth on bitumen biodegradation, the effect of pH on bitumen degradation and the effect of inhibitors on bitumen biodegradation. The salts contained in bituminous products were not found to significantly affect the rate of destruction. The degree of degradation was found to mainly depend on the bitumen, its chemical composition, and on the conditions of storage. It was also found that inhibitor additions in some cases modified the properties of the matrix such that it became more liquid. The coefficient of extractibility thus increased of matrix salts. The recultivation of bacteria on a full-value medium resulted in the loss of the inhibitory effect. In some cases, the inhibitor even stimulated the growth of microorganisms. The use of inhibitors in an effort to achieve biostability of bituminous products thus did not solve the problem. (Z.M.). 2 tabs., 9 refs

Growing markets to sustain oil sands development

International Nuclear Information System (INIS)

Wise, T.H.

2003-01-01

The utilization of Alberta bitumen for the clean fuels market depends on upgrading, transportation, and refining processes. Forecasts show that oil sands production, which includes synthetic crude oil (SCO), will surpass declining conventional production in Western Canada. Several issues pose a challenge to the oil sands processing industry. The producers' market is affected by crude oil prices, market expansion options, diluent availability/cost, supply cost competitiveness, and regional processing. The common market issues include light/heavy crude prices, oil sands crude qualities, prices of oil sands crudes, pipeline infrastructure, and competitive supplies. The issues facing the refiners are: refining margins, security of crude supply, refined product quality, and competitive product supply. A brief review of markets for Canadian crude oil, including synthetic crude, was provided. The share of the Midwest market by Alberta must be retained and increased. The market expansion options were reviewed for both downstream (refining) and upstream (upgrading) operations. To reach more distant markets such as Southern Midwest, Washington, and California, new pipeline capacity would be required. The market is nearly saturated for Canada's heavy oil supply. More upgrading will be required as bitumen production increases. Market growth is still possible for Canada's SCO but according to forecasts, the market could also become saturated. To increase demand and allow supplies to grow, SCO prices may fall below light crude prices. It was noted that a balance must be achieved in order for producers to increase production and for refiner/upgraders to expand their conversion capacity. tabs., figs

Distribution and Thermal Maturity of Devonian Carbonate Reservoir Solid Bitumen in Desheng Area of Guizhong Depression, South China

Directory of Open Access Journals (Sweden)

Yuguang Hou

2017-01-01

Full Text Available The distribution of solid bitumen in the Devonian carbonate reservoir from well Desheng 1, Guizhong Depression, was investigated by optical microscope and hydrocarbon inclusions analysis. Vb and chemical structure indexes measured by bitumen reflectance, laser Raman microprobe (LRM, and Fourier transform infrared spectroscopy (FTIR were carried out to determine the thermal maturity of solid bitumen. Based on the solid bitumen thermal maturity, the burial and thermal maturity history of Devonian carbonate reservoir were reconstructed by basin modeling. The results indicate that the fractures and fracture-related dissolution pores are the main storage space for the solid bitumen. The equivalent vitrinite reflectance of solid bitumen ranges from 3.42% to 4.43% converted by Vb (% and LRM. The infrared spectroscopy analysis suggests that there are no aliphatic chains detected in the solid bitumen which is rich in aromatics C=C chains (1431–1440 cm−1. The results of Vb (%, LRM, and FTIR analysis demonstrate that the solid bitumen has experienced high temperature and evolved to the residual carbonaceous stage. The thermal evolution of Devonian reservoirs had experienced four stages. The Devonian reservoirs reached the highest reservoir temperature 210–260°C during the second rapid burial-warming stage, which is the main period for the solid bitumen formation.

Co-liquefaction of Elbistan Lignite with Manure Biomass; Part 2 - Effect of Biomass Type, Waste to Lignite Ratio and Solid to Liquid Ratio

Science.gov (United States)

Karaca, Hüseyin; Koyunoglu, Cemil

2017-12-01

Most coal hydrogenation processes require a large quantity of hydrogen. In general, a coal derived liquid such as anthracene oil was used as a hydrogen donor solvent. Tetralin, partially hydrogenated pyrene, phenantrene and coal-derived solvents, which contain hydroaromatic compounds, are efficient solvents to donate hydrogen. In an attempt to reduce the high cost of hydrogen, part of the hydrogen was replaced by a low cost hydrogen donor solvent. This must be hydrogenated during or before the process and recycled. To reduce the cost of hydrogen donor vehicles instead of liquids recycled from the liquefaction process or several biomass types, industrial by products, liquid fractions derived from oil sands bitumen were successfully used to solubilize a coal from the past. In an attempt to reduce the high cost of hydrogen, part of the hydrogen was replaced by a low cost hydrogen donor solvent. However, when hydrogen is supplied from the hydroaromatic structures present in the solvent, the activity of coal minerals is too low to rehydrogenate the solvent in-situ. Nevertheless, a decrease of using oxygen, in addition to enhanced usage of the hydrogen supply by using various waste materials might lead to a decrease of the cost of the liquefaction procedure. So instead of using tetralin another feeding material such as biomass is becoming another solution improving hydrogen donor substances. Most of the liquefaction process were carried out in a batch reactor, in which the residence time of the liquefaction products is long enough to favour the retrogressive reactions, early studies which are related to liquefaction of coal with biomass generally focus on the synergetic effects of coal while biomass added. Early studies which are related to liquefaction of coal with biomass generally focus on the synergetic effects of coal while biomass added. Alternatively, to understand the hydrogen transfer from biomass to coal, in this study, Elbistan Lignite (EL) with manure, tea

Future tools : from reservoir-embedded seismic to nanotechnological bitumen upgrading, scientists are unlocking new ways to extract and process fossil fuels

Energy Technology Data Exchange (ETDEWEB)

Collison, M.

2006-10-15

A review of reservoir monitoring tools and methods designed by research centres and high-tech firms in Alberta was presented. The National Centre for Upgrading Technology is currently examining the use of biological catalysts for partially upgrading bitumens at remote field production sites to lower the viscosity and density of heavy oil and reduce the environmental impacts associated with refining. Geo-scientists at the University of Calgary are using a combination of geophysical methods to improve coalbed methane and tight gas extraction processes. Research at the university has centred around multi-component seismic exploration, which uses a shear wave measurement to provide an image of the ground's rigidity and can discriminate between fluid types to produce different pictures of the subsurface. In addition to investigating the conversion of seismic waves to radio emissions, the university is also examining the integration of electromagnetic or electrical methods with seismic methods. Multi-component seismic is now being evaluated for the purpose of monitoring carbon dioxide (CO{sub 2}) enhanced recovery operations and sequestration at a demonstration project near Drayton Valley. Time-lapse monitoring will allow the research team to compare seismic surveys done months apart and identify changes caused by the growing pressure due to CO{sub 2} injection. It was suggested that a new nanotechnology fabrication facility created as part of the National Research Council (NRC) technology cluster will help scientists to discover new approaches in bitumen processing through a better understanding of the properties that cause bitumen to foul upgrading and transportation equipment. Many students are now using nanotechnology methods to understand how large bitumen molecules interact with catalyst surfaces. 4 figs.

Oil sands naphthenic acids: a review of properties, measurement, and treatment.

Science.gov (United States)

Brown, Lisa D; Ulrich, Ania C

2015-05-01

The Alberta oil sands contain one of the world's largest reserves of oil - over 169 billion barrels of bitumen are economically recoverable with current extraction technologies. Surface mining and subsequent hot water extraction of bitumen from the ore generates about nine cubic meters of raw tailings per cubic meter of oil. Oil sands facilities are required to operate under a policy of zero water discharge, resulting in ponds containing more than one billion cubic meters of tailings, a mixture of sand, fines and process-affected water. Process-affected water contains numerous organic compounds, including naphthenic acids (NAs), which have been identified as the primary source of acute toxicity of process-affected water. Developments in analytical techniques, aerobic biodegradability, and treatment via chemical oxidation (ozone) of NAs are reviewed. The field continues to be challenged by the lack of a cost-effective, accurate analytical technique for NAs or an understanding of all the organic constituents in process-affected water that may be contributing to observed toxicity and thus requiring treatment. Copyright © 2015 Elsevier Ltd. All rights reserved.

Utilization of Liquid Smoke from Oil Palm Empty Fruit Bunches on Raw Rubber Processing

Directory of Open Access Journals (Sweden)

Hidayati Hidayati

2011-06-01

Full Text Available Research utilization of liquid smoke from oil palm empty fruit bunches of raw rubber has been made to utilize solid waste from industrial processing of oil palm empty fruit bunches of oil palm so that it becomes economically valuable products. This research has been done by pyrolysis of oil palm empty fruit bunches at a temperature of 400oC for 5, 6, 7 and 8 hours. The results show that the pyrolysis liquid smoke oil palm empty fruit bunches for 8 hours give a high concentration of phenol and acetic acid, respectively 5% and 0.454%. Liquid smoke that has been obtained is used as a coagulant in raw rubber plantation crops of the people residing in the village of Ambawang, Kubu Raya District, West Kalimantan. Results of treatment of liquid smoke on raw rubber  show that the rubber products that have been frozen and dried are superior in terms of color, smell and drying time compared with the treatment of formic acid and water battery which has been added so far on raw rubber by the local rubber farmers.

Solidification/stabilisation of liquid oil waste in metakaolin-based geopolymer

Energy Technology Data Exchange (ETDEWEB)

Cantarel, V.; Nouaille, F.; Rooses, A.; Lambertin, D., E-mail: david.lambertin@cea.fr; Poulesquen, A.; Frizon, F.

2015-09-15

Highlights: • Formulation with 20 vol.% of oil in a geopolymer have been successful tested. • Oil waste is encapsulated as oil droplets in metakaolin-based geopolymer. • Oil/geopolymer composite present good mechanical performance. • Carbon lixiviation of oil/geopolymer composite is very low. - Abstract: The solidification/stabilisation of liquid oil waste in metakaolin based geopolymer was studied in the present work. The process consists of obtaining a stabilised emulsion of oil in a water-glass solution and then adding metakaolin to engage the setting of a geopolymer block with an oil emulsion stabilised in the material. Geopolymer/oil composites have been made with various oil fraction (7, 14 and 20 vol.%). The rigidity and the good mechanical properties have been demonstrated with compressive strength tests. Leaching tests evidenced the release of oil from the composite material is very limited whereas the constitutive components of the geopolymer (Na, Si and OH{sup −}) are involved into diffusion process.

The 2003 Update of the ASPO Oil and Gas Depletion Model

Energy Technology Data Exchange (ETDEWEB)

Campbell, Colin; Sivertsson, Anders [Uppsala Univ. (Sweden). Hydrocarbon Depletion Study Group

2003-07-01

What we can term the ASPO Oil and Gas Depletion Model has developed over many years, based on an evolving knowledge of the resource base, culled from many sources, and evolving ideas about how to model depletion. It is sure that the estimates and forecasts are incorrect. The question is: By how much? The model recognises so-called Regular Oil, which excludes the following categories: Oil from coal and shale; Bitumen and synthetics derived therefrom; Extra Heavy Oil (<10 deg API); Heavy Oil (10-17 deg API); Deepwater Oil (>500 m); Polar Oil; Liquids from gas fields and gas plants. It has provided most oil to-date and will dominate all supply far into the future. Its depletion therefore determines the date of peak. The evidence suggests that about 896 Gb (billion barrels) had been produced to end 2002; about 871 Gb remain to produce from known fields and about 113 Gb is expected to be produced from new fields. It is convenient to set a cut-off of, say 2075, for such production, to avoid having to worry about the tail end that can drag on for a long time. A simple depletion model assumes that production declines at the current Depletion Rate (annual production as a percentage of future production) or at the Midpoint Rate in countries that have not yet reached Midpoint (namely half the total). The five main Middle East producers, which hold about half of what remains, are assumed to exercise a swing role, making up the difference between world demand and what the other countries can supply. The base case scenario assumes that consumption will be on average flat until 2010 because of recession; and that the Middle East swing role will end then, as in practice those countries will no longer have the capacity to discharge it. Whether the Iraq war results in extending or shortening the swing role remains to be seen. Adding the contributions of the other categories of oil and gas liquids gives an overall peak in 2010. Gas depletes differently, being more influenced by

The 2003 Update of the ASPO Oil and Gas Depletion Model

Energy Technology Data Exchange (ETDEWEB)

Campbell, Colin; Sivertsson, Anders [Uppsala Univ. (Sweden). Hydrocarbon Depletion Study Group

2003-07-01

What we can term the ASPO Oil and Gas Depletion Model has developed over many years, based on an evolving knowledge of the resource base, culled from many sources, and evolving ideas about how to model depletion. It is sure that the estimates and forecasts are incorrect. The question is: By how much? The model recognises so-called Regular Oil, which excludes the following categories: Oil from coal and shale; Bitumen and synthetics derived therefrom; Extra Heavy Oil (<10 deg API); Heavy Oil (10-17 deg API); Deepwater Oil (>500 m); Polar Oil; Liquids from gas fields and gas plants. It has provided most oil to-date and will dominate all supply far into the future. Its depletion therefore determines the date of peak. The evidence suggests that about 896 Gb (billion barrels) had been produced to end 2002; about 871 Gb remain to produce from known fields and about 113 Gb is expected to be produced from new fields. It is convenient to set a cut-off of, say 2075, for such production, to avoid having to worry about the tail end that can drag on for a long time. A simple depletion model assumes that production declines at the current Depletion Rate (annual production as a percentage of future production) or at the Midpoint Rate in countries that have not yet reached Midpoint (namely half the total). The five main Middle East producers, which hold about half of what remains, are assumed to exercise a swing role, making up the difference between world demand and what the other countries can supply. The base case scenario assumes that consumption will be on average flat until 2010 because of recession; and that the Middle East swing role will end then, as in practice those countries will no longer have the capacity to discharge it. Whether the Iraq war results in extending or shortening the swing role remains to be seen. Adding the contributions of the other categories of oil and gas liquids gives an overall peak in 2010. Gas depletes differently, being more influenced by

U.S. crude oil, natural gas, and natural gas liquids reserves 1995 annual report

Energy Technology Data Exchange (ETDEWEB)

NONE

1996-11-01

The EIA annual reserves report series is the only source of comprehensive domestic proved reserves estimates. This publication is used by the Congress, Federal and State agencies, industry, and other interested parties to obtain accurate estimates of the Nation`s proved reserves of crude oil, natural gas, and natural gas liquids. These data are essential to the development, implementation, and evaluation of energy policy and legislation. This report presents estimates of proved reserves of crude oil, natural gas, and natural gas liquids as of December 31, 1995, as well as production volumes for the US and selected States and State subdivisions for the year 1995. Estimates are presented for the following four categories of natural gas: total gas (wet after lease separation), nonassociated gas and associated-dissolved gas (which are the two major types of wet natural gas), and total dry gas (wet gas adjusted for the removal of liquids at natural gas processing plants). In addition, reserve estimates for two types of natural gas liquids, lease condensate and natural gas plant liquids, are presented. Also included is information on indicated additional crude oil reserves and crude oil, natural gas, and lease condensate reserves in nonproducing reservoirs. A discussion of notable oil and gas exploration and development activities during 1995 is provided. 21 figs., 16 tabs.

Deoxy-liquefaction of three different species of macroalgae to high-quality liquid oil.

Science.gov (United States)

Li, Jinhua; Wang, Guoming; Chen, Ming; Li, Jiedong; Yang, Yaoyao; Zhu, Qiuyan; Jiang, Xiaohuan; Wang, Zonghua; Liu, Haichao

2014-10-01

Three species of macroalgae (Ulva lactuca, Laminaria japonica and Gelidium amansii) were converted into liquid oils via deoxy-liquefaction. The elemental analysis, FTIR and GC-MS results showed that the three liquid oils were all mainly composed of aromatics, phenols, alkanes and alkenes, other oxygen-containing compounds, and some nitrogen-containing compounds though there were some differences in terms of their types or contents due to the different constituents in the macroalgae feedstocks. The oxygen content was only 5.15-7.30% and the H/C molar ratio was up to 1.57-1.73. Accordingly, the HHV of the three oils were 42.50, 41.76 and 40.00 MJ/kg, respectively. The results suggested that U. lactuca, L. japonica and G. amansii have potential as biomass feedstock for fuel and chemicals and that deoxy-liquefaction technique may be an effective way to convert macroalgae into high-quality liquid oil. Copyright © 2014 Elsevier Ltd. All rights reserved.

Effect of CuO receptor on the liquid yield and composition of oils derived from liquefaction of coals by microwave energy

International Nuclear Information System (INIS)

Yagmur, Emine; Simsek, Emir H.; Aktas, Zeki; Togrul, Taner

2008-01-01

The effects of microwave receptor to coal (receptor/coal) ratio and the period of heating by microwave energy on the solubilization of Turkish coals in tetralin have been investigated. CuO was used as microwave receptor. The amount of receptor and the type of coal significantly affected the yield of liquid product. The addition of the CuO receptor caused to increase in the lignite conversions to oil fractions. The yield of THF soluble fraction increased in the presence of CuO receptor, however, due to catalytic effect of CuO, the yields of preasphaltene (PAS) and asphaltene (AS) decreased. The oil fractions were obtained from the experiments treated by microwave energy in the presence of 3/5 CuO/coal ratio and in the absence of receptor for 20 min liquefaction periods. The compositions of the oil fractions were determined by GC/MS. The composition of the oil fractions of the coals strongly depends on the type of coal. It was observed that the oil fractions contain oxygenated aromatic compounds in addition to condensed aromatic structures. Considerable amounts of 3,4-dihydro-1(2H)-naphthalenone (alpha-tetralone) were found in the oil fractions of lignites treated by microwave energy

Effects of SBS Configuration on Performance of High Modulus Bitumen Based on Dynamic Mechanical Analysis

Directory of Open Access Journals (Sweden)

Ming Liang

2016-07-01

Full Text Available High modulus bitumens modified by polystyrene-block-polybutadiene-block-polystyrene (SBS with different molecular structure were investigated on dynamic shear rheometer and fluorescence microscopy to evaluate viscoelastic properties and morphology of binders. The results shows that storage modulus (G’ is obviously less than loss modulus (G”, which means viscous behaviour of bitumen is dominant, and anti-rutting factor (G* ⁄ sin δ is markedly enhanced by star SBS than by linear SBS. The morphology indicated that star SBS improved the softening point more obviously, tending to form a cross-linked network in bitumen. As for linear SBS, it is dispersed in bitumen in the form of globules and enhances the ductility of binder.

Plant Oil-Derived Epoxy Polymers toward Sustainable Biobased Thermosets.

Science.gov (United States)

Wang, Zhongkai; Yuan, Liang; Ganewatta, Mitra S; Lamm, Meghan E; Rahman, Md Anisur; Wang, Jifu; Liu, Shengquan; Tang, Chuanbing

2017-06-01

Epoxy polymers (EPs) derived from soybean oil with varied chemical structures are synthesized. These polymers are then cured with anhydrides to yield soybean-oil-derived epoxy thermosets. The curing kinetic, thermal, and mechanical properties are well characterized. Due to the high epoxide functionality per epoxy polymer chain, these thermosets exhibit tensile strength over an order of magnitude higher than a control formulation with epoxidized soybean oil. More importantly, thermosetting materials ranging from soft elastomers to tough thermosets can be obtained simply by using different EPs and/or by controlling feed ratios of EPs to anhydrides. © 2017 WILEY-VCH Verlag GmbH & Co. KGaA, Weinheim.

Price models for oil derivates in Slovenia

International Nuclear Information System (INIS)

Nemac, F.; Saver, A.

1995-01-01

In Slovenia, a law is currently applied according to which any change in the price of oil derivatives is subject to the Governmental approval. Following the target of getting closer to the European Union, the necessity has arisen of finding ways for the introduction of liberalization or automated approach to price modifications depending on oscillations of oil derivative prices on the world market and the rate of exchange of the American dollar. It is for this reason that at the Agency for Energy Restructuring we made a study for the Ministry of Economic Affairs and Development regarding this issue. We analysed the possible models for the formation of oil derivative prices for Slovenia. Based on the assessment of experiences of primarily the west European countries, we proposed three models for the price formation for Slovenia. In future, it is expected that the Government of the Republic of Slovenia will make a selection of one of the proposed models to be followed by enforcement of price liberalization. The paper presents two representative models for price formation as used in Austria and Portugal. In the continuation the authors analyse the application of three models that they find suitable for the use in Slovenia. (author)

Statistically Enhanced Model of In Situ Oil Sands Extraction Operations: An Evaluation of Variability in Greenhouse Gas Emissions.

Science.gov (United States)

Orellana, Andrea; Laurenzi, Ian J; MacLean, Heather L; Bergerson, Joule A

2018-02-06

Greenhouse gas (GHG) emissions associated with extraction of bitumen from oil sands can vary from project to project and over time. However, the nature and magnitude of this variability have yet to be incorporated into life cycle studies. We present a statistically enhanced life cycle based model (GHOST-SE) for assessing variability of GHG emissions associated with the extraction of bitumen using in situ techniques in Alberta, Canada. It employs publicly available, company-reported operating data, facilitating assessment of inter- and intraproject variability as well as the time evolution of GHG emissions from commercial in situ oil sands projects. We estimate the median GHG emissions associated with bitumen production via cyclic steam stimulation (CSS) to be 77 kg CO 2 eq/bbl bitumen (80% CI: 61-109 kg CO 2 eq/bbl), and via steam assisted gravity drainage (SAGD) to be 68 kg CO 2 eq/bbl bitumen (80% CI: 49-102 kg CO 2 eq/bbl). We also show that the median emissions intensity of Alberta's CSS and SAGD projects have been relatively stable from 2000 to 2013, despite greater than 6-fold growth in production. Variability between projects is the single largest source of variability (driven in part by reservoir characteristics) but intraproject variability (e.g., startups, interruptions), is also important and must be considered in order to inform research or policy priorities.

40 CFR 60.101a - Definitions.

Science.gov (United States)

2010-07-01

... or converting the SO2 to a sulfur product. Petroleum means the crude oil removed from the earth and the oils derived from tar sands, shale, and coal. Petroleum refinery means any facility engaged in producing gasoline, kerosene, distillate fuel oils, residual fuel oils, lubricants, asphalt (bitumen) or...

Improving Energy Efficiency In Thermal Oil Recovery Surface Facilities

Energy Technology Data Exchange (ETDEWEB)

Murthy Nadella, Narayana

2010-09-15

Thermal oil recovery methods such as Cyclic Steam Stimulation (CSS), Steam Assisted Gravity Drainage (SAGD) and In-situ Combustion are being used for recovering heavy oil and bitumen. These processes expend energy to recover oil. The process design of the surface facilities requires optimization to improve the efficiency of oil recovery by minimizing the energy consumption per barrel of oil produced. Optimization involves minimizing external energy use by heat integration. This paper discusses the unit processes and design methodology considering thermodynamic energy requirements and heat integration methods to improve energy efficiency in the surface facilities. A design case study is presented.

Distribution and quantitative assessment of world crude oil reserves and resources

Science.gov (United States)

Masters, Charles D.; Root, David H.; Dietzman, William D.

1983-01-01

World Demonstrated Reserves of crude oil are approximately 723 billion barrels of oil (BBO). Cumulative production is 445 BBO and annual production is 20 BBO. Demonstrated Reserves of crude-oil have declined over the past 10 years consistent with discoveries lagging production over the same period. The assessment of Undiscovered Resources shows a 90 percent probability that the amount discoverable lies between 321 and 1,417 BBO, 550 BBO being the most likely value. The most likely value for Ultimate recoverable resources is 1,718 BBO. The distribution of Ultimate Resources of crude oil will remain highly skewed toward the Middle East; no frontier areas that have potentials large enough to significantly affect present distribution are recognized. Rates of discovery have continued to decline over the past 20 years even though exploration activity has increased in recent years. Prudence dictates, therefore, that the low side of the assessment of Undiscovered Resources be responsibly considered and that alternate energy sources be a part of future planning. Extra-heavy oil and bitumen are assessed separately, with Reserves being figured as the annual productive capacity of installed facilities times 25 years. The annual production of extra-heavy oil is about 8 million barrels and of bitumen about 60 million barrels.

In-situ burning of heavy oils and Orimulsion : mid-scale burns

International Nuclear Information System (INIS)

Fingas, M.F.; Fieldhouse, B.; Brown, C.E.; Gamble, L.

2004-01-01

In-situ burning is considered to be a viable means to clean oil spills on water. In-situ burning, when performed under the right conditions, can reduce the volume of spilled oil and eliminate the need to collect, store, transport and dispose of the recovered oil. This paper presented the results of bench-scale in-situ burning tests in which Bunker C, Orimulsion and weathered bitumen were burned outdoors during the winter in burn pans of approximately 1 square metre. Each test was conducted on salt water which caused the separation of the bitumen from the water in the Orimulsion. Small amounts of diesel fuel was used to ignite the heavy oils. Quantitative removal of the fuels was achieved in all cases, but re-ignition was required for the Orimulsion. Maximum efficiency was in the order of 70 per cent. The residue was mostly asphaltenes and resins which cooled to a solid, glass like material that could be readily removed. The study showed that the type of oil burned influences the behaviour of the burns. Bunker C burned quite well and Orimulsion burned efficiently, but re-ignition was necessary. It was concluded that there is potential for burning heavy oils of several types in-situ. 6 refs., 7 tabs., 18 figs

Alberta oil sands royalty regime

International Nuclear Information System (INIS)

Asgarpour, S.

2004-01-01

The long term objective of the Oil Sands Business Unit of Alberta Energy is to pave the way for Alberta's bitumen production to reach 3 million barrels per day by 2020. This presentation described the national government's role in resource development. It was emphasized that since the Crown is the owner of the oil sands resource, it would benefit by providing strategic leadership and by generating a larger royalty base. The oil sands fiscal regime was described with reference to generic royalty, risk sharing, investment, and project economics. Business rule principles were also outlined along with criteria for project expansions. Both upstream and downstream challenges and opportunities were listed. 4 figs

The Anti-Staphylococcus aureus Effect of Combined Echinophora platyloba Essential Oil and Liquid Smoke in Beef

Science.gov (United States)

Pilevar, Zahra; Hajimehdipoor, Homa; Shahraz, Farzaneh; Alizadeh, Leyla; Mahmoudzadeh, Maryam

2017-01-01

Summary In the current study, the antibacterial effect of Echinophora platyloba essential oil and common liquid smoke (individually and in combination) against Staphylococcus aureus in beef meat samples is investigated. Using an automated microbiological growth analyser and the turbidimetric technique, the minimum inhibitory concentrations (MIC) and the minimum bactericidal concentrations (MBC) of the essential oil and liquid smoke were determined. Anti-S. aureus activity of essential oil and liquid smoke (individually and in combination) was defined by disk diffusion assay, generation time and cell constituent release. Apart from that, the interactions between these two compounds were measured by the checkerboard assay and by calculating the fractional inhibitory concentration (FIC) indices. Related MIC values of essential oil and smoke were found to be 7200 and 5500 mg/L, and MBC values were 8500 and 8000 mg/L, respectively. The conducted organoleptic assay showed that the addition of 0.05 g of essential oil and 0.6 g of liquid smoke to 100 g of meat samples did not have adverse effect on the overall acceptance. Weaker antibacterial effect against Staphylococcus aureus was observed when only Echinophora platyloba essential oil was used than when it was used in combination with liquid smoke. PMID:28559740

Separation of oil and grease from oil sludge using surfactant

International Nuclear Information System (INIS)

Ainon Abdul Aziz; Syed Hakimi Sakuma Syed Ahmad; Zalina Laili

2005-01-01

The objective of the experiments was to observe the efficiency of the surfactant to remove oil and grease from oil sludges using various surfactant concentration ranging from 10 %, 15 %, 20 % and 30 %. The surfactant solution consists of two mixtures of Aqua 2000 and D Bond. The oil sludge were subjected to heating and surfactant treatment process. Remaining oil and grease concentration were observed on the oil sludges after treatment. Small scale experiments were conducted by heating process, without heating process and heating process with addition of sodium chloride. Surfactant solution was added in each process. Results shows that there is separation of oil and grease from the oil sludges. There were formation of mini emulsions (oil in water). The higher the concentration of surfactant used, the higher the concentrations of mini emulsion formed as observed. Solid remains after the treatment process were found to contain lesser oil concentration with presence of bitumen, sediment, organic and inorganic materials. After a washing process using distilled water, the solid was still black but less oily than before the treatment. There is no separation of oil occurred in aqueous solution for the control experiment. (Author)

Use of a thin-film evaporator for bitumen coating of radioactive concentrates

International Nuclear Information System (INIS)

Lefillatre, G.; Rodier, J.; Hullo, R.; Cudel, Y.; Rodi, L.

1969-01-01

Following the development in the laboratory of a process for coating evaporation concentrates with bitumen, a technological study of this coating process has been undertaken. The report describes a pilot installation for the bitumen coating of concentrates, which uses a thin-film evaporator LUWA L 150. The first, inactive series of tests was designed to determine the maximum and optimum capacities of the evaporator by varying the amounts of bitumen and of concentrate, the rotor speed and the thermo-fluid temperature. Two rotors were tested, one of conventional type, the other a model especially designed for high viscosity products. The maximum capacity of evaporation of the apparatus is 72 kg/hr for a heating temperature of 221 deg. C. During normal operation, the evaporator can produce 50 kg/hr of coated product containing 55 to 60 per cent of bitumen (Mexphalte 40/50), the water content of the product remaining under 0.5 per cent. A second series of tests will shortly be carried out on this pilot installation using, in particular, bituminous emulsions containing mainly Mexphalte 40/50 and 80/100. (authors) [fr

Chemical aspects of shale and shale oils

Energy Technology Data Exchange (ETDEWEB)

Hackford, J E

1922-01-01

To prove that the kerogen in oil shale is a form of bitumen, several experiments were made with oil shale and a heavy asphaltic oil mixed with fuller's earth. When distilled, both the oil shale and asphalt-impregnated fuller's earth yielded paraffin oil, wax, and hydrogen sulfide (if sulfur was present). Both yielded ammonia if nitrogen was present. The organic material in each was partly isolated by extraction with pyridine and appeared to be the same. Oil shale is a marl that was saturated with oil or through which oil has passed or filtered. The insolubilities of its organic compounds are due to a slightly elevated temperature for a prolonged period and to the retaining effect exerted by the finely divided marl. The marl exerted a selective action on the oil and absorbed the asphaltum, sulfur, and nitrogen compounds from the oil. The class of oil evolved from a shale depended on the nature of the original compounds absorbed. Asphaltenes obtained from crude oil by precipitation with ethyl ether produced distillation products of water, hydrogen sulfide, ammonia, oil, wax, and a carbonaceous residue. Water was formed by decomposition of oxyasphaltenes and hydrogen sulfide by decomposition of thioasphaltenes. Ammonia was evolved during decomposition if lime was present, but if there was not sufficient free lime present, pyridine and pyrrole derivatives were redistilled as such. The oil and wax that resulted from the dry distillation were true decomposition products and equaled about 60 weight-percent of the asphaltenes. The oil and wax content of the mixture varied between 8 and 10 percent. The carbonaceous residue, which represented approximately 40 percent of the original asphaltene, was a decomposition product of the asphaltenes. Geologic comparisons of oil-shale deposits and oil-well fields were also made.

Volume Stability of Bitumen Bound Building Blocks

Directory of Open Access Journals (Sweden)

Thanaya I.N.A.

2010-01-01

Full Text Available This paper covers results of laboratory investigations on the volume stability of masonry units incorporating waste materials bound with bitumen (Bitublocks, due to moisture adsorption, thermal exposure and vacuum saturation. The materials used were steel slag, crushed glass, coal fly ash, and 50 pen bitumen. The samples were produced in hot mix method, compacted, then exposed to moist and temperature. It was found that moisture adsorption from the environment caused the Bitublock to expand. The samples with less intense curing regime experienced lower expansion and became stable faster, and vice versa. Under thermal condition (at 70°C, the samples with less intense curing regime underwent higher expansion, and vice versa. They were also highly reversible. Their volume stability was found unique under water exposure. The expansion on first vacuum saturation cycle was irreversible, then largely reversible on the following cycles.

In-vial liquid-liquid microextraction-capillary electrophoresis method for the determination of phenolic acids in vegetable oils.

Science.gov (United States)

Abu Bakar, Nur Bahiyah; Makahleh, Ahmad; Saad, Bahruddin

2012-09-12

An in-vial liquid-liquid microextraction method was developed for the selective extraction of the phenolic acids (caffeic, gallic, cinnamic, ferulic, chlorogenic, syringic, vanillic, benzoic, p-hydroxybenzoic, 2,4-dihydroxybenzoic, o-coumaric, m-coumaric and p-coumaric) in vegetable oil samples. The optimised extraction conditions for 20 g sample were: volume of diluent (n-hexane), 2 mL; extractant, methanol: 5 mM sodium hydroxide (60:40; v/v); volume of extractant, 300 μL (twice); vortex, 1 min; centrifugation, 5 min. Recoveries for the studied phenolic acids were 80.1-119.5%. The simultaneous determination of the phenolic acid extracts was investigated by capillary electrophoresis (CE). Separations were carried out on a bare fused-silica capillary (50 μm i.d.× 40 cm length) involving 25 mM sodium tetraborate (pH 9.15) and 5% methanol as CE background electrolyte in the normal polarity mode, voltage of 30 kV, temperature of 25°C, injection time of 4s (50 mbar) and electropherograms were recorded at 200 nm. The phenolic acids were successfully separated in less than 10 min. The validated in-vial LLME-CE method was applied to the determination of phenolic acids in vegetable oil samples (extra virgin olive oil, virgin olive oil, pure olive oil, walnut oil and grapeseed oil). The developed method shows significant advantages over the current methods as lengthy evaporation step is not required. Copyright © 2012 Elsevier B.V. All rights reserved.

Liquid Soap Production with Blends Of Rubber Seed Oil (RSO) And ...

African Journals Online (AJOL)

The production of liquid detergent using locally sourced palm fruit bunch (Elaeis Guineesis) waste saponier has been investigated. An optimum blend ratio of rubber seed oil to palm kernel oil RSO:PKO 20:80 being constituent elements used for the production of the soap; was obtained using the Duncan Multiple Range ...

Peering into Alberta’s Darkening Future: How Oil Prices Impact Alberta’s Royalty Revenues

Directory of Open Access Journals (Sweden)

Sarah Dobson

2015-03-01

Full Text Available The price of oil just keeps collapsing — and the fate of Alberta’s revenues is buckling with it. Going into March 2015, it seemed as if prices might have finally found a bottom, somewhere between US$48 and US$52. By the second week of March, they began falling again, to the low forties. These are prices the Alberta government had not even ventured to fathom when first putting together its forecasts for the impact of falling oil prices on the province’s finances. Come the fourth quarter of the Alberta government’s 2014/15 fiscal year, the province’s finances will begin to really feel the blow from the plunge in oil, as royalty payments dry up significantly. Come the 2015/16 fiscal year, the situation becomes even bleaker. In fact, the current fiscal year will seem pleasant compared to the next one. Due to a stronger than expected first half of the year, actual bitumen and crude oil royalties collected in Alberta from April to September 2014 exceeded estimates by $1.3 billion. That will mitigate some of the damage that the continuing slide in prices will cause by the year’s end, with the government’s third quarter update showing expected year-end crude oil and bitumen royalty revenues falling short of the budget target by $549 million. So severe has the fall in oil prices been that, in March 2015, the number of barrels of conventional oil that the government collects in royalties could plummet by up to 53,000 barrels from the 2014/15 budget forecast, declining to just 4,100 barrels per day. This suggests that prices may be nearing a point where royalty collection from conventional crude oil production is at risk of being virtually eliminated. Bitumen royalties are not faring much better. Relative to July 2014, per barrel royalties in February 2015 have potentially declined by 60 to 90 per cent. All told, the combined effect of the changing exchange rate, lower prices, and the lower royalty rates that take effect in this low

Simultaneous determination of six synthetic phenolic antioxidants in edible oils using dispersive liquid-liquid microextraction followed by high-performance liquid chromatography with diode array detection.

Science.gov (United States)

Xu, Shuangjiao; Liu, Liangliang; Wang, Yanqin; Zhou, Dayun; Kuang, Meng; Fang, Dan; Yang, Weihua; Wei, Shoujun; Xiao, Aiping; Ma, Lei

2016-08-01

A simple, rapid, organic-solvent- and sample-saving pretreatment technique, called dispersive liquid-liquid microextraction, was developed for the determination of six synthetic phenolic antioxidants from edible oils before high-performance liquid chromatography with diode array detection. The entire procedure was composed of a two-step microextraction and a centrifugal process and could be finished in about 5 min, only consuming only 25 mg of sample and 1 mL of the organic solvent for each extraction. The influences of several important parameters on the microextraction efficiency were thoroughly investigated. Recovery assays for oil samples were spiked at three concentration levels, 50, 100 and 200 mg/kg, and provided recoveries in the 86.3-102.5% range with a relative standard deviation below 3.5%. The intra-day and inter-day precisions for the analysis were less than 3.8%. The proposed method was successfully applied for the determination of synthetic phenolic antioxidants in different oil samples, and satisfactory results were obtained. Thus, the developed method represents a viable alternative for the quality control of synthetic phenolic antioxidant concentrations in edible oils. © 2016 WILEY-VCH Verlag GmbH & Co. KGaA, Weinheim.

Deterpenation of eucalyptus essential oil by liquid + liquid extraction: Phase equilibrium and physical properties for model systems at T = 298.2 K

International Nuclear Information System (INIS)

Gonçalves, Daniel; Koshima, Cristina Chiyoda; Nakamoto, Karina Thiemi; Umeda, Thayla Karla; Aracava, Keila Kazue; Gonçalves, Cintia Bernardo; Rodrigues, Christianne Elisabete da Costa

2014-01-01

Highlights: • Fractionation of essential oil compounds. • Liquid + liquid equilibria of limonene, citronellal, ethanol and water were studied. • Distribution coefficients of limonene and citronellal were evaluated. • Densities and viscosities of the phases were experimentally determined. • Solvent selectivities and physical properties were dependent on citronellal and water mass fractions. -- Abstract: As the principal source in Brazil of eucalyptus essential oil extracts, Eucalyptus citriodora contains citronellal, an oxygenated compound responsible for the flavour characteristics. Deterpenation processes, consisting of the removal of terpenic hydrocarbons with the subsequent concentration of the oxygenated compounds, can be used to improve the aromatic characteristics of this essential oil. The purpose of this work was to perform a study of the technical feasibility of using a liquid + liquid extraction process to deterpenate eucalyptus essential oil. Model systems with various mixtures of limonene and citronellal (representing eucalyptus essential oil) as well as solvent (ethanol with various water mass fractions) were used to obtain liquid + liquid equilibrium data. The raffinate and extract phases were also analyzed to characterize the physical properties (density and viscosity). The equilibrium data were used to adjust the NRTL and UNIQUAC parameters. Two empirical models, the simple mixing rule and the Grunberg–Nissan model, were evaluated for use in the descriptions of the densities and viscosities, respectively, of the samples. Increasing the water content in the solvent resulted in decreases in the limonene and citronellal distribution coefficients, with consequential increases in the solvent selectivity values. Increasing values of the densities and viscosities, especially for the solvent-rich phases, were associated with systems using high amounts of hydrated ethanolic solvents

Castor Oil Transesterification Catalysed by Liquid Enzymes

DEFF Research Database (Denmark)

Andrade, Thalles; Errico, Massimiliano; Christensen, Knud Villy

2017-01-01

In the present work, biodiesel production by reaction of non-edible castor oil with methanol under enzymatic catalysis is investigated. Two liquid enzymes were tested: Eversa Transform and Resinase HT. Reactions were performed at 35 °C and with a molar ratio of methanol to oil of 6:1. The reaction...... time was 8 hours. Stepwise addition of methanol was necessary to avoid enzyme inhibition by methanol. In order to minimize the enzyme costs, the influence of enzyme activity loss during reuse of both enzymes was evaluated under two distinct conditions. In the former, the enzymes were recovered...... and fully reused; in the latter, a mixture of 50 % reused and 50 % fresh enzymes was tested. In the case of total reuse after three cycles, both enzymes achieved only low conversions. The biodiesel content in the oil-phase using Eversa Transform was 94.21 % for the first cycle, 68.39 % in the second, and 33...

Physical characteristics of tetrahydroxy and acylated derivatives of jojoba liquid wax

Science.gov (United States)

Jojoba liquid wax is a mixture of esters of long chain fatty acids and fatty alcohols, mainly (C38:2-C46:2). The oil exhibits excellent emolliency on the skin and therefore is a component in many personal care cosmetic formulations. The virgin oil is a component of the seed of the Jojoba (Simmondsia...

Determination of organic products resulting of chemical and radiochemical decompositions of bitumen. Applications to embedded bitumens; Determination des produits organiques d'alterations chimiques et radiochimiques du bitume. Applications aux enrobes bitumes

Energy Technology Data Exchange (ETDEWEB)

Walczak, I

2000-01-27

Bitumen can be used for embedding most of wastes because of its high impermeability and its relatively low reactivity with of chemicals. Bituminization is one of selected solutions in agreement with nuclear safety, waste compatibility and economic criteria. Bitumen, during storage, undergoes an auto-irradiation due to embedded radio-elements. During this stage,drums are not airtight then oxygen is present. In disposal configuration, water, which is a potential vector of radioactivity and organic matter, is an other hazard factor liable to deteriorate the containment characteristics of bitumen wastes. The generation of water-soluble organic complexing agents can affect the integrity of the wasteform due to an increase of the radionuclides solubility. The first aim of this work is the quantitative and qualitative characterisation of soluble organic matter in bitumen leachates. Different leaching solutions were tested (various pH, ionic strength, ratio S/V). When the pH of the leaching solutions increases, the total organic carbon released increases as well. Identified molecules are aromatics like naphthalene, oxidised compounds like alcohols, linear carbonyls, aromatics, glycols and nitrogen compounds. For the cement equilibrated solution (pH 13.5), the effect of ionic strength becomes significative and influences the release of soluble organic matter. This soluble organic matter can be bio-degraded if microorganisms can growth. The second aim of this work is to study the effect of radio-oxidative ageing on the bitumen confinement properties. During radio-oxidation, the chemical properties of bitumen are modified. The {mu}-IRTF analysis shows the formation of hydroxyl compounds and aromatic acids. The formation of these polar groups does not influence in our study the water uptake. However the organic matter release increases significantly with the irradiation dose. (author)

Biodegradation of polyurethane derived from castor oil

Directory of Open Access Journals (Sweden)

José M. Cangemi

2008-09-01

Full Text Available The aim of this research was to study the biodegradation of a polymer derived from castor oil, which is a renewable, natural material that is a practical alternative for the replacement of traditional polyurethane foams. Due to its molecular structure, which contains polyester segments derived from vegetable oil, the polymeric surface is susceptible to microorganism attack. This study tested the biological degrading agent that was in contact with the microorganisms resulting from microbiological grease degrading agents, when foam was inoculated. Solid-media agar-plate tests were conducted for their potential to evaluate the biodegradation of polymeric particles by specific strains of microorganisms during 216 hours. The growth rate was defined. This technique provides a way of distinguishing the degradation abilities of microorganisms from the degradability of materials.

Characterization of organic matter associated with uranium deposits in the Francevillian formation of Gabon (Lower Proterozoic)

International Nuclear Information System (INIS)

Cortial, F.; Gauthier-Lafaye, F.; Weber, F.; Oberlin, A.

1990-01-01

Elemental analysis, organic petrography, and high-resolution transmission electron microscopy were used to study organic matter in Lower Proterozoic rocks of the Francevillian Series in Africa. Results show a convincing relationship between solid bitumens derived from thermal alteration of crude oil, and deposition of uraninite ores. Evidence is presented that suggests the presence of migration paths for crude oil in associated sandstones. Moreover, the solid bitumens appear to have been further altered by radiation damage as a consequence of oxidation and uranium mineralization. (author)

21 CFR 524.2620 - Liquid crystalline trypsin, Peru balsam, castor oil.

Science.gov (United States)

2010-04-01

... 21 Food and Drugs 6 2010-04-01 2010-04-01 false Liquid crystalline trypsin, Peru balsam, castor... NEW ANIMAL DRUGS § 524.2620 Liquid crystalline trypsin, Peru balsam, castor oil. (a)(1) Specifications... delivered to the wound site contains 0.12 milligram of crystalline trypsin, 87.0 milligrams of Peru balsam...

How does market concern derived from the Internet affect oil prices?

International Nuclear Information System (INIS)

Guo, Jian-Feng; Ji, Qiang

2013-01-01

Highlights: • The impact of market concern derived from the Web on oil volatility is analysed. • It has an equilibrium relationship between oil prices and long-run market concern. • The short-run market concerns have an asymmetric influence on oil price volatility. • The Internet can exaggerate the impact of information shocks on oil price. - Abstract: With the acceleration of oil marketisation and the rapid development of electronic information carriers, external information shocks can be easily and quickly transmitted to the oil market through the Internet. This paper analyses the impact of short- and long-run market concerns, derived from search query volumes in Google for different domains around the oil market on oil volatility using co-integration and the modified EGARCH model. Empirical results suggest there is a long-term equilibrium relationship between oil prices and long-run market concern for oil prices and oil demand. The short-run market concerns for the 2008 financial crisis and the Libyan war convulsion have a significant and asymmetric influence on oil price volatility. This indicates that market concern transmitted through the Internet can strengthen the linkage between oil price changes and external events by influencing the expectation of market traders, and to some extent it can exaggerate the impact of nonfundamental information shocks

Research on swelling clays and bitumen as sealing materials for radioactive waste repositories

International Nuclear Information System (INIS)

Allison, J.A.; Wilson, J.; Mawditt, J.M.; Hurt, J.C.

1991-01-01

This report describes a programme of research to investigate the performance of composite seals incorporating adjacent blocks of swelling clay and bitumen. It is shown that the interaction of the materials can promote a self-sealing mechanism which prevents water penetration, even when defects are present in the bitumen layer. A review of the swelling properties of highly compacted bentonite and magnesium oxide is presented, and the characteristic sealing properties of bituminous materials are described. On the basis of this review, it is concluded that bentonite is the preferred candidate material for use in composite clay/bitumen seals for intermediate-level radioactive waste repositories. However, it is thought that magnesium oxide may have other sealing applications for high-level waste repositories. A programme of laboratory experiments is described in which relevant swelling and intrusion properties of highly compacted bentonite blocks and the annealing characteristics of oxidised and hard-grade industrial bitumens are examined. The results of composite sealing experiments involving different water penetration routes are reported, and factors governing the mechanism of self-sealing are described. The validation of the sealing concept at a laboratory scale indicates that composite bentonite/bitumen seals could form highly effective barriers for the containment of radioactive wastes. Accordingly, recommendations are made concerning the development of the research, including the implementation of full-scale demonstration experiments to simulate conditions in an underground repository. 13 tabs., 41 figs., 62 refs

It's all about the bitumen : oilsands producers have the attention of the world

Energy Technology Data Exchange (ETDEWEB)

Jaremko, D.

2005-09-01

Within 10 years, oilsands growth will make Canada the fifth largest oil producing country in the world, thereby greatly increasing Canada's political power. A review of oil sands development was presented, with reference to the way in which Steam Assisted Gravity Drainage (SAGD) has revolutionized the industry. Recent acquisitions have pointed to the growing level of international interest in the oilsands industry. Construction details of the Surmont project were discussed along with Devon Canada's SAGD project at Jackfish where about 100 well-pairs are expected to be drilled. Petrobank Energy and Resources is constructing its Whitesands project, which will employ the first field-scale application of the toe-to-heel air injection (THAI) recovery method which has lower operating costs and which uses less water and creates fewer greenhouse (GHG) emissions. The pilot was designed to produce up to 1800 barrels per day of partially upgraded bitumen. Details of CNRI's Horizon project were presented, including construction plans and schedules. Shell Canada's increased budget for the first expansion of the Athabasca Oilsands Project was reviewed with reference to their strategic decision to pre-build infrastructure for future expansions. Details of Suncor Energy's production goals were also reviewed, including details of new upgraders and applications. Syncrude's continuing expansions were discussed, as well as their current production levels. An outline of UTS Energy Corporation and Petro-Canada's plans concerning the Fort Hills Mining Project was presented, with details of the new BITMIN extraction process. It was noted that Imperial Oil has filed regulatory applications for the Kearl Oilsands Project, which have estimated total recoverable bitumen resources of 4.4 billion barrels. Husky Energy's Sunrise Project was discussed, as well as MEG Energy's regulatory approval for the first phase of the Christina Lake Regional

Laboratory performance testing of an extruded bitumen containing a surrogate, sodium nitrate-based, low-level aqueous waste

International Nuclear Information System (INIS)

Mattus, A.J.; Kaczmarsky, M.M.

1986-01-01

Laboratory results of a comprehensive, regulatory performance test program, utilizing an extruded bitumen and a surrogate, sodium nitrate-based waste, have been compiled at the Oak Ridge National Laboratory (ORNL). Using a 53 millimeter, Werner and Pfleiderer extruder, operated by personnel of WasteChem Corporation of Paramus, New Jersey, laboratory-scale, molded samples of type three, air blown bitumen were prepared for laboratory performance testing. A surrogate, low-level, mixed liquid waste, formulated to represent an actual on-site waste at ORNL, containing about 30 wt % sodium nitrate, in addition to eight heavy metals, cold cesium and strontium was utilized. Samples tested contained three levels of waste loading: that is, forty, fifty and sixty wt % salt. Performance test results include the ninety day ANS 16.1 leach test, with leach indices reported for all cations and anions, in addition to the EP Toxicity test, at all levels of waste loading. Additionally, test results presented also include the unconfined compressive strength and surface morphology utilizing scanning electron microscopy. Data presented include correlations between waste form loading and test results, in addition to their relationship to regulatory performance requirements

The pebble bed modular reactor (PBMR) as a source of high quality process heat for sustainable oil sands expansion

International Nuclear Information System (INIS)

Morris, A.; Kuhr, R.

2008-01-01

Bitumen extraction, processing and upgrading consumes large quantities of natural gas for production of steam, hot water and hydrogen. Massive expansion of bitumen production is planned in response to energy demands, oil prices, and the desire for energy security. The PBMR in its Process Heat configuration supports applications that compete in a cost effective and environmentally sustainable way with natural gas fired boilers and steam methane reforming. The PBMR has the benefit of size, passive nuclear safety characteristics (encompassing Generation IV safety principles), high reliability, high temperature process heat (750-950 o C) in a modular design suited to the oil sands industry. (author)

Process water treatment in Canada's oil sands industry : 2 : a review of emerging technologies

International Nuclear Information System (INIS)

Allen, E.W.

2008-01-01

This review was conducted to identify candidate treatment technologies for treating oil sands process water. The oil sands industry in Canada uses large volumes of fresh water in order to extract bitumen deposits. The development of process water treatment technologies has become a critical issue for the industry, particularly as oil sand production is expected to triple in the next decade. However, treatment technologies must be adapted to consider the fouling potential of bitumens and fine clays as well as the effect of alkaline process water on treatment performance. The review included developments in chemical modifications to membranes and adsorbents designed to improve pollutant removal and reduce fouling; hybridization technologies designed to enhance the biological treatment of toxic feedwaters; recent advances in photocatalytic oxidation technologies for organic compounds; and new designs for large-scale treatment wetlands for polluted waste waters. It was concluded that major knowledge gaps must be optimized and preliminary studies must be conducted in order to understand how the treatment technologies will be affected by the chemical and physical characteristics of oil sands process water. 188 refs., 8 tabs

Integrated oil production and upgrading using molten alkali metal

Science.gov (United States)

Gordon, John Howard

2016-10-04

A method that combines the oil retorting process (or other process needed to obtain/extract heavy oil or bitumen) with the process for upgrading these materials using sodium or other alkali metals. Specifically, the shale gas or other gases that are obtained from the retorting/extraction process may be introduced into the upgrading reactor and used to upgrade the oil feedstock. Also, the solid materials obtained from the reactor may be used as a fuel source, thereby providing the heat necessary for the retorting/extraction process. Other forms of integration are also disclosed.

A modified approach for isolation of essential oil from fruit of Amorpha fruticosa Linn using microwave-assisted hydrodistillation concatenated liquid-liquid extraction.

Science.gov (United States)

Chen, Fengli; Jia, Jia; Zhang, Qiang; Gu, Huiyan; Yang, Lei

2017-11-17

In this work, a modified technique was developed to separate essential oil from the fruit of Amorpha fruticosa using microwave-assisted hydrodistillation concatenated liquid-liquid extraction (MHD-LLE). The new apparatus consists of two series-wound separation columns for separating essential oil, one is the conventional oil-water separation column, and the other is the extraction column of components from hydrosol using an organic solvent. Therefore, the apparatus can simultaneously collect the essential oil separated on the top of hydrosol and the components extracted from hydrosol using an organic solvent. Based on the yield of essential oil in the first and second separation columns, the effects of parameters were investigated by single factor experiments and Box-Behnken design. Under the optimum conditions (2mL ethyl ether as the extraction solvent in the second separation column, 12mL/g liquid-solid ratio, 4.0min homogenate time, 35min microwave irradiation time and 540W microwave irradiation power), satisfactory yields for the essential oil in the first separation column (10.31±0.33g/kg) and second separation column (0.82±0.03g/kg) were obtained. Compared with traditional methods, the developed method gave a higher yield of essential oil in a shorter time. In addition, GC-MS analysis of the essential oil indicated significant differences of the relative contents of individual volatile components in the essential oils obtained in the two separation columns. Therefore, the MHD-LLE technique developed here is a good alternative for the isolation of essential oil from A. fruticosa fruit as well as other herbs. Copyright © 2017 Elsevier B.V. All rights reserved.

Determination of organic products resulting of chemical and radiochemical decompositions of bitumen. Applications to embedded bitumens; Determination des produits organiques d'alterations chimiques et radiochimiques du bitume. Applications aux enrobes bitumes

Energy Technology Data Exchange (ETDEWEB)

Walczak, I

2000-01-27

Bitumen can be used for embedding most of wastes because of its high impermeability and its relatively low reactivity with of chemicals. Bituminization is one of selected solutions in agreement with nuclear safety, waste compatibility and economic criteria. Bitumen, during storage, undergoes an auto-irradiation due to embedded radio-elements. During this stage,drums are not airtight then oxygen is present. In disposal configuration, water, which is a potential vector of radioactivity and organic matter, is an other hazard factor liable to deteriorate the containment characteristics of bitumen wastes. The generation of water-soluble organic complexing agents can affect the integrity of the wasteform due to an increase of the radionuclides solubility. The first aim of this work is the quantitative and qualitative characterisation of soluble organic matter in bitumen leachates. Different leaching solutions were tested (various pH, ionic strength, ratio S/V). When the pH of the leaching solutions increases, the total organic carbon released increases as well. Identified molecules are aromatics like naphthalene, oxidised compounds like alcohols, linear carbonyls, aromatics, glycols and nitrogen compounds. For the cement equilibrated solution (pH 13.5), the effect of ionic strength becomes significative and influences the release of soluble organic matter. This soluble organic matter can be bio-degraded if microorganisms can growth. The second aim of this work is to study the effect of radio-oxidative ageing on the bitumen confinement properties. During radio-oxidation, the chemical properties of bitumen are modified. The {mu}-IRTF analysis shows the formation of hydroxyl compounds and aromatic acids. The formation of these polar groups does not influence in our study the water uptake. However the organic matter release increases significantly with the irradiation dose. (author)

REDISTILAT ASAP CAIR CANGKANG KELAPA SAWIT SEBAGAI BAHAN PENGAWET BAKSO SAPI [Redistilled Liquid Smoke of Oil-Palm Shells as a Preservative for Beef Meatballs

Directory of Open Access Journals (Sweden)

Suminar Setiati Achmadi

2015-06-01

Full Text Available Liquid smoke has been used to extend the shelf life of food. However, its composition varies considerably depending on the type of raw materials used and preparation precedure. Liquid smoke derived from palm oil shell is potential due to the abundance of its byproduct sources in the palm oil industry. This study thus aims to prepare the best fraction of liquid smoke that can extend the shelf life of beef meatballs at room temperature. The raw liquid smoke was redistilled at 80, 90, and 100°C and was used as an ingredient in the beef meatballs production. The gas chromatography-mass spectrometry identification showed that there were no harmful compounds such as derivatives of tar and polycyclic aromatic hydrocarbons. Liquid smoke produced from redistillation at 80°C had the best result for providing higher acid value and lower pH, i.e. 5.14% and 2.26, respectively. The LC50 value of the redistilled liquid smoke in brine shrimp lethality assay was 0.16%. Inhibition zones of 0.1 and 0.8% redistilled liquid smoke on the antibacterial test against Staphylococcus aureus were both 6.10 mm, while the zones of inhibition for Escherichia coli were 0 and 7.0 mm, respectively. These resulting inhibition zones were less effective than that of 100 ppm chloramphenicol, i.e. 14.2 mm on S. aureus and 12.6 mm on E. coli. The usage of redistilled liquid smoke at concentration of 0.8% in meatballs was found to inhibit total microbial growth greater than that of the addition at 0.1%. Moreover, the addition of redistilled liquid smoke inhibited the growth of microbial up to 18 hours at room temperature.

Oil and gas information 1995

International Nuclear Information System (INIS)

1996-07-01

This reference book on current developments in oil and gas supply and demand contains country-specific statistics for OECD countries on production, trade, demand and prices. This book is divided in four parts. Part 1 gives the statistics sources for oil, gas and by products (lubricants, bitumen, paraffin waxes etc..) supply, demand, consumption, origin, feedstocks, import and export prices, spot and end-user prices and taxes, and gives also the definitions of products, supply and consumption items reported in this book. Part 2 provides summary tables of world oil and gas market developments with time series back to the early 1970's. Parts 3 and 4 provide, in tables form, a more detailed and comprehensive picture of oil and gas supply and demand for the OECD by region and individual countries. (J.S.)

(Liquid + liquid) equilibrium for systems composed of clove and allspice essential oil compounds and hydrous ethanol at T = 298.2 K

International Nuclear Information System (INIS)

Koshima, Cristina C.; Umeda, Thayla K.; Nakamoto, Karina T.; Venâncio, Larissa L.; Aracava, Keila K.; Rodrigues, Christianne E.C.

2016-01-01

Highlights: • A fraction enriched in oxyterpenes can be obtained via the deterpenation process. • Liquid extraction with hydrous ethanol can be applied to essential oil deterpenation. • Distribution coefficients of caryophyllene, methyl eugenol and eugenol were studied. • Eugenol has the highest distribution coefficient compared to the data in the literature. • Phase compositions were well described by the NRTL parameters. - Abstract: In the deterpenation process of essential oils, a fraction enriched in oxyterpenes is obtained. When compared to terpenic hydrocarbons, this fraction is more stable and soluble in water, maintaining the characteristic flavor and fragrance of the crude oil. Solvent extraction is an interestingly popular technique that is proposed for the fractionation of essential oils (once it can be performed under atmospheric pressure and ambient temperature) and contributes to the maintenance of the sensory quality of essential oils. The use of hydrous ethanol as a solvent for the (liquid + liquid) extraction process has shown advantages when the components of interest are completely soluble in ethanol, and their partition can be adjusted based on the level of hydration of the solvent. In addition, for some purposes, the fractions obtained from the separation process can be used without removing the solvent. Therefore, the primary goal of this study was to investigate the (liquid + liquid) equilibrium at T = (298.2 ± 0.1) K of model systems composed of (caryophyllene + eugenol + ethanol + water) (i.e., a clove essential oil model system) and (caryophyllene + methyl eugenol + eugenol + ethanol + water) (i.e., an allspice essential oil model system) to provide the information required for the proper design and optimization of the associated deterpenation processes. For both systems studied, it was noted that increased water content in the solvent decreases the extraction of the essential compounds and increases the selectivity of the

Microbial communities involved in methane production from hydrocarbons in oil sands tailings.

Science.gov (United States)

Siddique, Tariq; Penner, Tara; Klassen, Jonathan; Nesbø, Camilla; Foght, Julia M

2012-09-04

Microbial metabolism of residual hydrocarbons, primarily short-chain n-alkanes and certain monoaromatic hydrocarbons, in oil sands tailings ponds produces large volumes of CH(4) in situ. We characterized the microbial communities involved in methanogenic biodegradation of whole naphtha (a bitumen extraction solvent) and its short-chain n-alkane (C(6)-C(10)) and BTEX (benzene, toluene, ethylbenzene, and xylenes) components using primary enrichment cultures derived from oil sands tailings. Clone libraries of bacterial 16S rRNA genes amplified from these enrichments showed increased proportions of two orders of Bacteria: Clostridiales and Syntrophobacterales, with Desulfotomaculum and Syntrophus/Smithella as the closest named relatives, respectively. In parallel archaeal clone libraries, sequences affiliated with cultivated acetoclastic methanogens (Methanosaetaceae) were enriched in cultures amended with n-alkanes, whereas hydrogenotrophic methanogens (Methanomicrobiales) were enriched with BTEX. Naphtha-amended cultures harbored a blend of these two archaeal communities. The results imply syntrophic oxidation of hydrocarbons in oil sands tailings, with the activities of different carbon flow pathways to CH(4) being influenced by the primary hydrocarbon substrate. These results have implications for predicting greenhouse gas emissions from oil sands tailings repositories.

Removal of Basic Nitrogen Compounds from Fuel Oil with [Hnmp]H2PO4 Ionic Liquid

Directory of Open Access Journals (Sweden)

Z. Zhou

2017-04-01

Full Text Available Ionic liquid (IL N-methyl pyrrolidone dihydrogen phosphate ([Hnmp]H2PO4 was synthesized and its structure was characterized with FT-IR spectroscopy and 1H NMR. The denitrogenation performance of the ionic liquid was investigated using Fushun shale diesel oil that included 0.52 w% basic nitrogen as feedstock. Experiment results showed that under the operating conditions with temperature of 30 °C, 1:7 (w/w IL: oil, reaction time of 20 min, and settling time of 2 h, the ionic liquid exhibited good denitrogenation performance achieving 86.27 % basic N-extraction efficiency and the yield of refined diesel oil can reach more than 90 %. In addition, the basic N-removal efficiency can still reach 54 % during four recycles of the ionic liquid.

Apparatus for utilizing liquid hydrocarbons such as shale oil, etc

Energy Technology Data Exchange (ETDEWEB)

Dorset, M

1868-02-29

The hydrocarbon liquids such as petroleum, shale oil, naphtha, cresol, coal tar, or other mineral, animal or vegetable oil are placed in a heater or special generator analogous to ordinary generators for vapors and to which the name vaporizer has been given in the description. This vaporizer is furnished with all kinds of safety devices, such as valves, manometer, float indicating the level, standard stopcock, etc., and is heated by the combustion of the vapors produced by it.

Dewatering Behaviour of Fine Oil Sands Tailings : An Experimental Study

NARCIS (Netherlands)

Yao, Y.

2016-01-01

Oil sands tailings are a warm aqueous suspension of sand, silt, clay, residual bitumen and naphtha. The tailings are hydraulically transported and stored in tailing ponds where they segregate, with the sand settling from suspension forming beaches and the remaining tailings flowing to the middle of

Forecasting and evaluations of crude oil processing and oil derivatives consumption in Republic of Macedonia up to 2000 year

International Nuclear Information System (INIS)

Janevski, Risto

1998-01-01

Elaboration of various analysis in an energetic field is a quite usual, but inevitable action, procedure and investigation. Also, in a field of crude oil processing and oil derivatives consumption these analyses are a base for making a various range of forecasting and evaluations. How many of these forecasting and evaluations will be credible it depends mostly of diligent, precise and accurate data and experiences in the previous years. This part refers to forecasting and evaluations of crude oil processing and oil derivatives consumption in a short period up to 2000 year in Republic of Macedonia. (Author)

Partial Discharge Phase Distribution Of Palm Oil As Insulating Liquid

Directory of Open Access Journals (Sweden)

Abdul Rajab

2011-04-01

Full Text Available Due to the low biodegradability level of mineral oil and its susceptibility to the fire, palm oil was proposed as alternative insulating liquid. This paper discusses partial discharge (PD in palm oil under sinusoidal voltages and the comparison with mineral oil. PD was generated using a needle-plane electrode configuration which is enable enhancing electric field at the needle tip. PD pulses were detected using RC detector and they were measured using a Computer-based partial discharge measurement system. The results showed that PD activities in both oils are similar. The PD was initiated at the negative polarity of applied voltage. The discharges took place in both polarity’s of applied voltage with PD number was higher at negative one. Several discharges phenomena showed the presence of space charge which changed electric field and governed PD activities besides the main field introduced by voltage application.

Crude oil price shocks and stock returns. Evidence from Turkish stock market under global liquidity conditions

Energy Technology Data Exchange (ETDEWEB)

Berk, Istemi [Koeln Univ. (Germany). Energiewirtschaftliches Inst.; Aydogan, Berna [Izmir Univ. of Economics (Turkey). Dept. of International Trade and Finance

2012-09-15

The purpose of this study is to investigate the impacts of crude oil price variations on the Turkish stock market returns. We have employed vector autoregression (V AR) model using daily observations of Brent crude oil prices and Istanbul Stock Exchange National Index (ISE- 1 00) returns for the period between January 2, 1990 and November 1, 2011. We have also tested the relationship between oil prices and stock market returns under global liquidity conditions by incorporating a liquidity proxy variable, Chicago Board of Exchange's (CBOE) S and P 500 market volatility index (VIX), into the model. Variance decomposition test results suggest little empirical evidence that crude oil price shocks have been rationally evaluated in the Turkish stock market. Rather, it was global liquidity conditions that were found to account for the greatest amount of variation in stock market returns.

The development of today's mineable oil sands projects, the key factors influencing economics

International Nuclear Information System (INIS)

Lynn, J.R.

1991-01-01

Many factors influence the perception of economic performance for developing projects. Some of these factors can be controlled by the developer, while some are outside the developer's sphere of influence. Technology selection, management systems, stakeholder involvement, environmental responsiveness and risk management are areas that may be influenced, however interest rates, product prices and currency exchange all have a measurable effect on project economics and are beyond a developer's control. Economic considerations for evaluating mineable oil sand development projects are outlined, focussing on the key factors unique to such developments in general and to the OSLO project in particular. The OSLO project is a proposed $5 billion energy development that entails constructing an open pit oil sands mine and a bitumen extraction facility north of Fort McMurray, Alberta, coupled with a bitumen upgrader in the Redwater area. 7 figs

The sweet world of liquid crystals : The synthesis of non-amphiphilic carbohydrate-derived liquid crystals

NARCIS (Netherlands)

Smits, E

1998-01-01

The research in carbohydrate-derived liquid crystals was initiated by a review article by Jeffrey in 1986. This is rather late if one considers that the research on liquid crystals underwent a revival already in the 1960s after the discovery of the liquid crystal display (LCD). Carbohydrates were

Continuous distillation of oil-bearing rocks

Energy Technology Data Exchange (ETDEWEB)

1923-11-14

A continuous process of distilling petroleum-bearing, asphaltic, or bituminous rocks to free bitumen is characterized by vaporizing hydrocarbons solid, pasty, or liquid from petroleum-containing asphaltic or bituminous rocks to free bitumen without ever reaching the temperatures at which they can produce decomposition, the necessary heat being furnished by combustion of part of the hydrocarbons of the treated rocks. A furnace for carrying out the process of claim 1 is characterized by consisting of a cavity lined inside with reflector, of variable section and with a throat at the upper part for charging the material to be treated and means for blowing the lower part of the furnace with the air necessary for combustion and inert gas for regulating the combustion and removal of the hydrocarbons.

Maximize Liquid Oil Production from Shale Oil and Gas Condensate Reservoirs by Cyclic Gas Injection

Energy Technology Data Exchange (ETDEWEB)

Sheng, James [Texas Tech Univ., Lubbock, TX (United States); Li, Lei [Texas Tech Univ., Lubbock, TX (United States); Yu, Yang [Texas Tech Univ., Lubbock, TX (United States); Meng, Xingbang [Texas Tech Univ., Lubbock, TX (United States); Sharma, Sharanya [Texas Tech Univ., Lubbock, TX (United States); Huang, Siyuan [Texas Tech Univ., Lubbock, TX (United States); Shen, Ziqi [Texas Tech Univ., Lubbock, TX (United States); Zhang, Yao [Texas Tech Univ., Lubbock, TX (United States); Wang, Xiukun [Texas Tech Univ., Lubbock, TX (United States); Carey, Bill [Los Alamos National Lab. (LANL), Los Alamos, NM (United States); Nguyen, Phong [Los Alamos National Lab. (LANL), Los Alamos, NM (United States); Porter, Mark [Los Alamos National Lab. (LANL), Los Alamos, NM (United States); Jimenez-Martinez, Joaquin [Los Alamos National Lab. (LANL), Los Alamos, NM (United States); Viswanathan, Hari [Los Alamos National Lab. (LANL), Los Alamos, NM (United States); Mody, Fersheed [Apache Corp., Houston, TX (United States); Barnes, Warren [Apache Corp., Houston, TX (United States); Cook, Tim [Apache Corp., Houston, TX (United States); Griffith, Paul [Apache Corp., Houston, TX (United States)

2017-11-17

The current technology to produce shale oil reservoirs is the primary depletion using fractured wells (generally horizontal wells). The oil recovery is less than 10%. The prize to enhance oil recovery (EOR) is big. Based on our earlier simulation study, huff-n-puff gas injection has the highest EOR potential. This project was to explore the potential extensively and from broader aspects. The huff-n-puff gas injection was compared with gas flooding, water huff-n-puff and waterflooding. The potential to mitigate liquid blockage was also studied and the gas huff-n-puff method was compared with other solvent methods. Field pilot tests were initiated but terminated owing to the low oil price and the operator’s budget cut. To meet the original project objectives, efforts were made to review existing and relevant field projects in shale and tight reservoirs. The fundamental flow in nanopores was also studied.

TECHNOLOGY OF REPAIRING OPERATIONAL SUITABILITY BITUMEN-RUBEROID CARPET

Directory of Open Access Journals (Sweden)

MISHUK K. M.

2017-01-01

Full Text Available Raising of problem. In the article is presented the analysis of the existing technologies for the restoration of the operational usability of bitumen-polymeric carpet, which allowed to identify their disadvantages, suggested ways to solve problems and highlighted the results of the studies. Firstly, existing bitumen-ruberoid carpet has a residual hydro insulating capacity that can be effectively used. Secondly, the physical condition of the repaired carpet has different types of defects and damage without the proper removal of which is difficult to ensure the desired outcome. The applying of additional layers in conditions of moistening of the lower layers and other defects contributes to their conservation and accelerated loss of operational integrity.Removal of these impacts can be up to 40-50% of all work, can not provide the required effectiveness outcomes in terms of durability, reliability and cost. Therefore the problem is to find ways to achieve a longer after repairing operation with simultaneous reduction of consumables indicators. Purpose of the study is to develop technological solutions serviceability restoration of roofing using unrolling technologies on the principles to minimize the impact of negative factors and the maximum possible use and strengthen the remaining hydro potential of the insulating coating through the use of special impregnating - saturating compositions. Features such compositions are based on the ability to deeply penetrate the thick bitumen-ruberoid carpet and restore his lost components and provide increased water resistance. Conclusion. The article can be introduced in practice of repair-refurbishable works of soft roofing covering of buildings and constructions.

The splitting of P and NG and oil sands rights: an historical perspective

Energy Technology Data Exchange (ETDEWEB)

Coombs, F. D. [Alberta Department of Energy, Edmonton, AB (Canada)

1997-12-31

Changes in the Mines and Minerals Act of Alberta are described to illustrate the evolution of the priorities and thinking over time that led to the present administration of oil sands and natural gas as separate minerals. Natural gas was first excluded from the definition of bituminous sands in 1955. The definition of bituminous sands was changed in 1957 to include natural gas once again. In a further change in 1978, both petroleum and natural gas were excluded from the definition of oil sands. More changes followed in 1984, when petroleum was added back into the definition, leaving natural gas as the only mineral excluded from the definition of oil sands. The 1984 change was triggered by changes in the Oil Sands Conservation Act. It is the current definition, which includes `sands and other rock materials containing crude bitumen, and any other mineral substances, other than natural gas, in association with that crude bitumen`. It was a resource conservation issue in the past, and it is a conservation issue today, although much influenced by changes in technology and increased knowledge and understanding of the relevant factors. 2 tabs.

Proceedings of the oil sands and heavy oil technologies conference and exhibition

International Nuclear Information System (INIS)

2009-01-01

This conference provided a forum for oil sands industry leaders to review the current and future state of technology in this frontier environment. Presentations were delivered by key personnel involved in groundbreaking projects with a renewed focus on oil sands technology and equipment, viewed from the strategic level with case studies and reports on application technologies designed to optimize oil sands operations. The presentations addressed a wide range of issues related to the environmental impacts of oil sands processing facilities, including innovative water and wastewater solutions for heavy oil producers for bitumen mining, in-situ and upgrading facilities. New advances in sulphur treatment technologies were highlighted along with technologies designed to increase the energy efficiency and energy consumption rates of upgrader and processing facilities. Advances in carbon dioxide (CO 2 ) capture and storage systems were also discussed along with geopolitical and economic evaluations of the future of the oil sands industry. The conference featured 59 presentations, of which 48 have been catalogued separately for inclusion in this database. refs., tabs., figs

Unconventional imports

International Nuclear Information System (INIS)

Yamaguchi, N.D.

2001-01-01

This article focuses on bitumens and bitumen products from Canadian oil sands and explores how they will affect the Canadian oil industry and the US refining industry. The falling production of crude, the growing demand for it, and the stagnating refining capacity in the US are reported, and Canadian and Mexican exports to the US, the definition of bitumens and bitumen quality, and the position of Canada as world leader in bitumen resources are considered. Bitumen production techniques, sales of bitumens and synthetic crude, the production outlook, and the quality and refining of bitumen and synthetic crude are examined. Plots illustrating North American crude refining capacity, production and demand for 1980-2000; US crude imports from Canada and Mexico (1981-2000), world proven oil reserves (2001), world bitumen resources, and Canadian oil production (1998-2000) are provided. Details of the composition of crudes and bitumens, and recent synthetic crude production are tabulated

Epoxy modified bitumen : Chemical hardening and its interpretation

NARCIS (Netherlands)

Apostolidis, P.; Pipintakos, G.; van de Ven, M.F.C.; Liu, X.; Erkens, Sandra; Scarpas, Athanasios

2018-01-01

Epoxy modified bitumen (EMB) is a promising technology for long lasting paving materials ensuring higher resistance to rutting, oxygen- and moisture-induced damage. In this paper, an analysis of the chemical reactions that take place during the chemical hardening process (curing) of epoxy modified