Relevant bibliographies by topics / Bitumen upgrading process

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  1. Journal articles
  2. Dissertations / Theses
  3. Conference papers

Academic literature on the topic 'Bitumen upgrading process'

Author: Grafiati
Published: 4 June 2021
Last updated: 4 February 2022

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Journal articles on the topic "Bitumen upgrading process"

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Gholami, Rahman, Anton Alvarez‐Majmutov, Mohamed Ali, and Jinwen Chen. "Understanding bitumen partial upgrading through process modelling and simulation." Canadian Journal of Chemical Engineering 99, no. 1 (2020): 222–34. http://dx.doi.org/10.1002/cjce.23850.

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Kishita, Atsushi, Satoru Takahashi, Yuki Yamasaki, Fangmin Jin, Takehiko Moriya, and Heiji Enomoto. "Desulfurization of Bitumen by Hydrothermal Upgrading Process in Supercritical Water with Alkali." Journal of the Japan Petroleum Institute 49, no. 4 (2006): 177–85. http://dx.doi.org/10.1627/jpi.49.177.

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Shah, Amjad A., Robert P. Fishwick, Gary A. Leeke, Joseph Wood, Sean P. Rigby, and Malcolm Greaves. "Experimental Optimization of Catalytic Process In Situ for Heavy-Oil and Bitumen Upgrading." Journal of Canadian Petroleum Technology 50, no. 11/12 (2011): 33–47. http://dx.doi.org/10.2118/136870-pa.

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Rajan, V. S. V., and R. Tipman. "A Method for Improving the Quality of Bituminous Froth From Water Extraction of Oil Sands." Journal of Energy Resources Technology 114, no. 4 (1992): 261–66. http://dx.doi.org/10.1115/1.2905951.

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Bituminous froths produced from the water extraction of oil sands contain significant quantities of sand and water which must be removed prior to upgrading the bitumen to synthetic crude oil. This paper presents a summary of the study of a simple twostep process for removing most of the solid and water contaminants from the bituminous froth. Low-quality froths containing 10–30 percent bitumen at temperatures of 40–70°C were improved in quality to 50–60 percent bitumen by heating the raw froth to ~ 90°C and settling the product in a gravity settler. The gravity settling vessel incorporated uniq
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Gemayel, Jimmy El, Arturo Macchi, Robin Hughes, and Edward John Anthony. "Simulation of the integration of a bitumen upgrading facility and an IGCC process with carbon capture." Fuel 117 (January 2014): 1288–97. http://dx.doi.org/10.1016/j.fuel.2013.06.045.

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Wang, Hui, Annaïg Le Person, Xu Zhao, et al. "A low-temperature hydrogen production process based on H2S splitting cycle for sustainable oil sands bitumen upgrading." Fuel Processing Technology 108 (April 2013): 55–62. http://dx.doi.org/10.1016/j.fuproc.2012.04.010.

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Soiket, Md I. H., A. O. Oni, E. D. Gemechu, and A. Kumar. "Life cycle assessment of greenhouse gas emissions of upgrading and refining bitumen from the solvent extraction process." Applied Energy 240 (April 2019): 236–50. http://dx.doi.org/10.1016/j.apenergy.2019.02.039.

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Perez–Perez, A., M. Mujica Chacín, I. Bogdanov, A. Brisset, and O. Garnier. "Simulations of In-Situ Upgrading Process: Interpretation of Laboratory Experiments and Study of Field-Scale Test." SPE Journal 24, no. 06 (2019): 2711–30. http://dx.doi.org/10.2118/190695-pa.

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Summary In–situ upgrading (IU) is a promising method of improved viscous– and heavy–oil recovery. The IU process implies a reservoir heating up and exposure to a temperature higher than 300°C for a time period long enough to promote a series of chemical reactions. The pyrolysis reactions produce lighter oleic and gaseous components, while a solid residue remains underground. In this work, we developed a numerical model of IU using laboratory experience (kinetics measurements and core experiments) and validated the results by applying our model to an IU field–scale test published in the literat
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Ado, Muhammad Rabiu. "Effect of reservoir pay thickness on the performance of the THAI heavy oil and bitumen upgrading and production process." Journal of Petroleum Exploration and Production Technology 10, no. 5 (2020): 2005–18. http://dx.doi.org/10.1007/s13202-020-00840-5.

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Zhu, Yuanzheng, Gimyeong Seong, Takio Noguchi, et al. "Highly Cr-Substituted CeO2 Nanoparticles Synthesized Using a Non-equilibrium Supercritical Hydrothermal Process: High Oxygen Storage Capacity Materials Designed for a Low-Temperature Bitumen Upgrading Process." ACS Applied Energy Materials 3, no. 5 (2020): 4305–19. http://dx.doi.org/10.1021/acsaem.0c00026.

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Dissertations / Theses on the topic "Bitumen upgrading process"

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El, Gemayel Gemayel. "Integration and Simulation of a Bitumen Upgrading Facility and an IGCC Process with Carbon Capture." Thèse, Université d'Ottawa / University of Ottawa, 2012. http://hdl.handle.net/10393/23274.

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Hydrocracking and hydrotreating are bitumen upgrading technologies designed to enhance fuel quality by decreasing its density, viscosity, boiling point and heteroatom content via hydrogen addition. The aim of this thesis is to model and simulate an upgrading and integrated gasification combined cycle then to evaluate the feasibility of integrating slurry hydrocracking, trickle-bed hydrotreating and residue gasification using the Aspen HYSYS® simulation software. The close-coupling of the bitumen upgrading facilities with gasification should lead to a hydrogen, steam and power self-sufficient u
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Conference papers on the topic "Bitumen upgrading process"

1

Marriott, T., M. F. Gonzalez, L. Carbognani, et al. "Visbreaking Based Integrated Process for Bitumen Upgrading and Hydrogen Production." In Canadian International Petroleum Conference. Petroleum Society of Canada, 2006. http://dx.doi.org/10.2118/2006-074.

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Shah, Amjad Ali, Robert P. Fishwick, Gary A. Leeke, Joseph Wood, Sean P. Rigby, and Malcolm Greaves. "Experimental Optimization of Catalytic Process In-Situ for Heavy Oil and Bitumen Upgrading." In Canadian Unconventional Resources and International Petroleum Conference. Society of Petroleum Engineers, 2010. http://dx.doi.org/10.2118/136870-ms.

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Mokrys, I. J., and R. M. Butler. "In-Situ Upgrading of Heavy Oils and Bitumen by Propane Deasphalting: The Vapex Process." In SPE Production Operations Symposium. Society of Petroleum Engineers, 1993. http://dx.doi.org/10.2118/25452-ms.

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Morris, Antony, Reiner Kuhr, and James McKinnell. "The Pebble Bed Modular Reactor (PBMR) as a Source of High Quality Process Heat for Sustainable Oil Sands Expansion." In Fourth International Topical Meeting on High Temperature Reactor Technology. ASMEDC, 2008. http://dx.doi.org/10.1115/htr2008-58216.

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Bitumen extraction, processing and upgrading consume large quantities of natural gas for production of steam, hot water and hydrogen. Massive expansion of bitumen production is planned in response to increasing energy demands, higher oil prices, and the desire for energy security. The Pebble Bed Modular Reactor (“PBMR”) in its Process Heat configuration supports applications that are likely to compete in a cost effective and environmentally sustainable way with natural gas fired boilers for the production of steam for bitumen recovery. Technology development work to produce hydrogen using this
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Pardo, Carlos, and Ralph Dickau. "Facilities and Controls in a Heated Bitumen Pipeline." In 2004 International Pipeline Conference. ASMEDC, 2004. http://dx.doi.org/10.1115/ipc2004-0171.

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World scale deposits of oil sands (bitumen) in Northern Alberta, Canada are being developed to extract hydrocarbons from the sand using surface mining processes and new techniques such us Steam Assisted Gravity Drainage (SAGD) or “SagDee” as it is commonly referred to in the industry. This method employs numerous steam injection wells to heat the bitumen to reduce its viscosity and separate it from the sand particles. The heavy tar-like bitumen must either be upgraded to a light synthetic crude on site or diluted with natural gas condensate or a light oil to be able to pump the blend over long
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Rahman, Mohammad A., Johana Gomez, Ted Heidrick, Brian A. Fleck, and Jennifer McMillan. "Correlations of the Droplet Size-Velocity of the Two-Phase, Air/Liquid Spray Using a Particle-Dynamic-Analyzer." In ASME 2008 Fluids Engineering Division Summer Meeting collocated with the Heat Transfer, Energy Sustainability, and 3rd Energy Nanotechnology Conferences. ASMEDC, 2008. http://dx.doi.org/10.1115/fedsm2008-55330.

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In the heavy oil process industry preheated bitumen and steam are mixed upstream of the feed nozzle and subsequently injected into fluid bed coker reactors via feed nozzles. To achieve high liquid product yields, the bitumen should contact a large number of fluidized coke particles quickly and uniformly. One of the drawbacks of the spray issuing from the nozzle is the potential pulsation within the spray and in the feeding conduit, which is highly undesirable to yield high productivity. These pulsations result in poor atomization and in most instances, a slug of liquid is ejected out of the no
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Padamsey, R., R. T. Bailey, T. J. Cyr, and R. Lott. "(HC) Process - A Viable Alternate For Upgrading Alberta Bitumens." In Annual Technical Meeting. Petroleum Society of Canada, 1994. http://dx.doi.org/10.2118/94-44.

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