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Relevant bibliographies by topics / Petroleum Hydrogenation

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Academic literature on the topic 'Petroleum Hydrogenation'

Author: Grafiati

Published: 4 June 2021

Last updated: 1 February 2022

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Journal articles on the topic "Petroleum Hydrogenation"

1

Haslam, R. T., and R. P. Russell. "THE HYDROGENATION OF PETROLEUM." Journal of the American Society for Naval Engineers 43, no. 2 (2009): 360–65. http://dx.doi.org/10.1111/j.1559-3584.1931.tb03762.x.

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2

Vail', Yu K., I. A. Pugach, V. M. Kurganov, and M. L. Zlotnikov. "Hydrogenation processing of petroleum residues." Chemistry and Technology of Fuels and Oils 22, no. 9 (1986): 447–51. http://dx.doi.org/10.1007/bf00722271.

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3

Wei, Caiqin, Xiaopeng Chen, Jingjing Xue, et al. "A small eggshell Ni/SFC3R catalyst for C5 petroleum resin hydrogenation: preparation and characterization." RSC Advances 6, no. 54 (2016): 49113–22. http://dx.doi.org/10.1039/c6ra07720j.

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4

Glyzdova, DV, N. S. Smirnova, D. A. Shlyapin, and P. G. Tsyrul’nikov. "Gas-phase and liquid-phase hydrogenation of acetylene in lean and enriched mixtures over supported modified palladium catalysts." Российский химический журнал 62, no. 1-2 (2019): 89–109. http://dx.doi.org/10.6060/rcj.2018621-2.7.

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In the presented review the results of studies devoted to the selective hydrogenation of acetylene to ethylene over bimetallic palladium-containing catalysts are systematized. General regularities and peculiarities of the catalysts action in gas-phase hydrogenation of traces of acetylene in the acetylene-ethylene mixture obtained by pyrolysis of petroleum raw materials, as well as in the process of liquid-phase hydrogenation of mixtures enriched with acetylene and hydrogen are analyzed. The advantages of obtaining ethylene by hydrogenation of acetylene in the liquid phase are shown and ways of

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5

Yu, Chong, Hui Huang, Qianwen Li, et al. "New advances in catalysts for C9 petroleum resin hydrogenation." IOP Conference Series: Earth and Environmental Science 513 (July 8, 2020): 012003. http://dx.doi.org/10.1088/1755-1315/513/1/012003.

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6

Azami, K., O. Kato, H. Takashima, S. Yamamoto, and Y. Sanada. "Effects of hydrogenation of petroleum pitch on mesophase formation." Journal of Materials Science 28, no. 4 (1993): 885–89. http://dx.doi.org/10.1007/bf00400870.

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7

PLATONOV, V., J. VALDES, A. VOLEPSHTEIN, et al. "Hydrogenation of asphaltenes of petroleum of the Cuban Matansas field." Petroleum Chemistry U.S.S.R. 28, no. 1 (1988): 53–60. http://dx.doi.org/10.1016/0031-6458(88)90030-5.

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8

Smith, J. W., and T. D. Gilbert. "A QUEST FOR A NEW PARAMETER IN PETROLEUM EXPLORATION GEOCHEMISTRY." APPEA Journal 27, no. 1 (1987): 98. http://dx.doi.org/10.1071/aj86010.

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Primary Australian terrestrially-derived crudes are characterised by high wax and n-alkane contents. These characteristics, as determined by hydrogenation and hydrous pyrolysis, appear to be unrelated to either the chemical or petrographic compositions of Victorian brown coal lithotypes. Furthermore, since relationships between chemical and petrographic composition are obscure, a re-examination of current concepts which relate these established source rock parameters to liquid hydrocarbon generating potentials is warranted.The content of thermally stable, longer-chain, n-alkyl components in so

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9

Li, Ai Min, Li Han, Zhi Min Zong, and Xian Yong Wei. "GC/MS Analysis of Products from Catalytic Hydroconversion of Dagang Vacuum Residue with Y Zeolite." Advanced Materials Research 712-715 (June 2013): 317–20. http://dx.doi.org/10.4028/www.scientific.net/amr.712-715.317.

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The petroleum ether-insoluble fraction of Dagang vacuum residue (DVR-PEIF) was subject to catalytic hydrogenation in the presence of Y zeolite. Most of compounds detected with GC/MS in the PE-soluble fraction of products from DVR-PEIF are saturated hydrocarbons, including chain alkanes and cyclanes. Small amounts of olefins and heteroatom-containing compounds (HOs) were also identified.

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10

Petrukhina, N. N., E. M. Zakharyan, S. A. Korchagina, M. V. Nagieva, and A. L. Maksimov. "Hydrogenation of petroleum resins in the presence of supported sulfide catalysts." Petroleum Chemistry 58, no. 1 (2018): 48–55. http://dx.doi.org/10.1134/s0965544118010127.

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Dissertations / Theses on the topic "Petroleum Hydrogenation"

1

Sullivan, David Lawrence. "Hydrodesulfurization of thiophene, tetrahydrothiophene and 1-butanethiol on model silica-supported molybdenum and tungsten catalysts /." Digital version accessible at:, 1998. http://wwwlib.umi.com/cr/utexas/main.

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2

Guan, Jie. "Ceramic membranes of mixed ionic-electronic conductors for hydrogen separation." Diss., Georgia Institute of Technology, 1998. http://hdl.handle.net/1853/19423.

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3

Bundhoo, Adam. "Contribution à l'étude mécanistique de la synthèse Fischer-Tropsch: préparation et caractérisation de catalyseurs de cobalt et de nickel." Doctoral thesis, Universite Libre de Bruxelles, 2010. http://hdl.handle.net/2013/ULB-DIPOT:oai:dipot.ulb.ac.be:2013/210084.

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Ce travail de doctorat s’inscrit dans le cadre de la recherche fondamentale inhérente à la réaction catalytique d’hydrogénation du CO, qui permet de produire du pétrole de synthèse à partir des autres ressources fossiles disponibles à l’état naturel (gaz naturel et charbon).<p>Les objectifs de ce travail s’articulent autour de deux méthodes originales, respectivement de préparation et de caractérisation des catalyseurs. La première permet la formation in situ de catalyseurs par voie oxalique, alors que la seconde est une méthode de cinétique transitoire chimique appliquée à la réaction CO + H2

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4

Furlong, Brian Keith. "Selective hydrogenation of 1,3-butadiene in 1-butene over alumina supported palladium and palladium/copper catalysts." Thesis, 1994. http://hdl.handle.net/1911/13832.

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Copper addition to palladium increases both activity and selectivity in the selective hydrogenation of 1,3-butadiene to n-butenes. The bimetal catalyst (Cu/Pd:2/1(atomic)) hydrogenates the diene to virtually 100% conversion without significant n-butene isomerization or butane formation. While at moderate conversions monometallic palladium is quite selective for n-butene production, 1-butene is quickly isomerized and saturated at higher conversions resulting from butadiene's inability to monopolize the active surface at lower partial pressures. Copper also promotes higher trans-2-butene selecti

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Books on the topic "Petroleum Hydrogenation"

1

Ancheyta, Jorge. Asphaltenes: Chemical transformation during hydroprocessing of heavy oils. Taylor & Francis, 2009.

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2

Hydroprocessing of Heavy Oils and Residua (Chemical Industries). CRC, 2007.

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3

Speight, James G., and Jorge Ancheyta. Hydroprocessing of Heavy Oils and Residua. Taylor & Francis Group, 2007.

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4

G, Speight J., and Ancheyta Jorge, eds. Hydroprocessing of heavy oils and residua. Taylor & Francis, 2007.

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5

Asphaltenes: Chemical Transformation during Hydroprocessing of Heavy Oils. CRC, 2008.

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6

Ancheyta, Jorge, Mohan Singh Rana, and Fernando Trejo. Asphaltenes: Chemical Transformation During Hydroprocessing of Heavy Oils. Taylor & Francis Group, 2010.

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Book chapters on the topic "Petroleum Hydrogenation"

1

Infantes-Molina, A., A. Romero-Perez, D. Eliche-Quesada, J. Merida-Robles, A. Jimenez-Lopez, and E. Rodriguez-. "Transition Metal Sulfide Catalysts for Petroleum Upgrading – Hydrodesulfurization Reactions." In Hydrogenation. InTech, 2012. http://dx.doi.org/10.5772/45629.

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2

Lucien, J. P., J. P. van den Berg, G. Germaine, H. M. J. H. van Hooijdonk, M. Gjers, and G. L. B. Thielemans. "Shell Middle Distillate Hydrogenation Process." In Catalytic Hydroprocessing of Petroleum and Distillates. CRC Press, 2020. http://dx.doi.org/10.1201/9781003067306-16.

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3

Magnabosco, L. M. "A Mathematical Model for Cataytic Hydrogenation of Aromatics in Petroleum Refining Feedstocks." In Catalysts in Petroleum Refining 1989, Proceedings of the Conference on Catalysts in Petroleum Refining. Elsevier, 1989. http://dx.doi.org/10.1016/s0167-2991(08)61085-x.

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4

Nakagawa, S., T. Ono, S. Murata, M. Nomura, and T. Sakai. "Hydrogenation of aromatic compounds related to fuels over a hydrogen storage alloy." In catalysts in Petroleum Refining and Petrochemical Industries 1995, Proceedings of the 2nd International Conference on Catalysts in Petroleum refining and Petrochemical Industries. Elsevier, 1996. http://dx.doi.org/10.1016/s0167-2991(96)80050-4.

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5

Yui, Sok M. "Two-Stage Hydrotreating of a Bitumen-Derived Middle Distillate to Produce Diesel and Jet Fuels, and Kinetics of Aromatics Hydrogenation." In Catalytic Hydroprocessing of Petroleum and Distillates. CRC Press, 2020. http://dx.doi.org/10.1201/9781003067306-13.

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6

Inui, T., and J. B. Kim. "High quality gasoline synthesis by selective oligomerization of light olefins and successive hydrogenation." In catalysts in Petroleum Refining and Petrochemical Industries 1995, Proceedings of the 2nd International Conference on Catalysts in Petroleum refining and Petrochemical Industries. Elsevier, 1996. http://dx.doi.org/10.1016/s0167-2991(96)80049-8.

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7

Nakamura, I., and K. Fujimoto. "Hydrocracking of paraffiinic hydrocarbons over hybridcatalysts containing H-ZSM-5 zeolite and supported hydrogenation catalyst." In catalysts in Petroleum Refining and Petrochemical Industries 1995, Proceedings of the 2nd International Conference on Catalysts in Petroleum refining and Petrochemical Industries. Elsevier, 1996. http://dx.doi.org/10.1016/s0167-2991(96)80024-3.

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8

Doraiswamy, L. K. "Homogeneous Catalysis." In Organic Synthesis Engineering. Oxford University Press, 2001. http://dx.doi.org/10.1093/oso/9780195096897.003.0014.

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Catalysis by soluble complexes of transition metals is a rapidly gaining mode of catalysis in organic synthesis. These metals form bonds with one or more carbons in an organic reactant resulting in complexes that are known as organometallic complexes. Catalysis by these complexes is often referred to as homogeneous catalysis. Among the important applications of homogeneous catalysis in organic synthesis are isomerization of olefins; hydrogenation of olefins (carried out using Wilkinson type catalysts); oligomerization; hydroformylation of olefins to aldehydes with CO and H2 (the oxo process); carbonylation of unsaturated hydrocarbons and alcohols with CO (and coreactants such as water); oxidation of olefins to aldehydes, ketones, and alkenyl esters (Wacker process); and metathesis of olefins (a novel kind of disproportionation). Enantioselective catalysis that rivals enzymes in selectivity is a major development in homogeneous catalysis. As a result, many earlier processes in the pharmaceutical and perfumery industries are being replaced by more elegant syntheses using soluble catalysts in which “handedness” is introduced in the critical step of the process, thus avoiding the costly separation of racemic mixtures. In view of its importance in organic synthesis, enantioselective (or asymmetric) catalysis was briefly introduced in Chapter 6 and is again considered as a powerful synthetic tool in Chapter 9. This chapter is concerned with the use in general of homogeneous catalysis in organic synthesis (including asymmetric synthesis). Among the several books and reviews written on the subject, the following may be mentioned: Halpern (1975, 1982), Bau et al. (1978), Parshall (1980), Masters (1981), Collman and Hegedus (1980), Eby and Singleton (1983), Chaudhari (1984), Davidson (1984), Kegley and Pinhas (1986), Collman et al. (1987), Parshall and Nugent (1988), Noyori and Kitamura (1989), Parshall and Ittel (1992), Gates (1992), Chan (1993), Akutagawa (1995). Gas (or liquid)-phase reactions on solid catalysts are among the most common industrial reactions. However, homogeneous catalysis is rapidly catching up. Excluding applications in petroleum refining, the dollar value of organic chemicals produced worldwide by homogeneous catalysis (more than $35 billion) is quite impressive compared to that by heterogeneous catalysis (more than $45 billion). Attempts are now under way to find an integrated approach to homogeneous and heterogeneous catalyses (Moulijn et al., 1993).

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Conference papers on the topic "Petroleum Hydrogenation"

1

Gurumoorthi, Gurulakshmanan, Balaji Vanjilingam, and Ganesh Digraskar. "Conversion of Olefins in LPG through hydrogenation." In International Petroleum Technology Conference. International Petroleum Technology Conference, 2011. http://dx.doi.org/10.2523/iptc-14454-ms.

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2

Gurumoorthi, Gurulakshmanan, Balaji Vanjilingam, and Ganesh Digraskar. "Conversion of Olefins in LPG through hydrogenation." In International Petroleum Technology Conference. International Petroleum Technology Conference, 2011. http://dx.doi.org/10.2523/14454-ms.

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3

Qin, Mu, Guangxu Cheng, Zaoxiao Zhang, Qing Li, and Jianxiao Zhang. "Numerical Simulation of Temperature Field and Residual Stress in Multi-Pass Welds in 2.25Cr-1Mo-0.25V Steel Plate and Comparison With Experimental Measurements." In ASME 2017 Pressure Vessels and Piping Conference. American Society of Mechanical Engineers, 2017. http://dx.doi.org/10.1115/pvp2017-65617.

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The 2.25Cr-1Mo-0.25V steels are widely used in the petroleum chemical industry for the manufacturing of pressure vessels. The multi-pass welding is a critical type of fabrication in hydrogenation reactor. However, very complicated residual stresses could be generated during the multi-pass welding process. The presence of residual stresses could have significant influence on the performance of welded product. In the present work, the transient temperature distribution and residual stress distribution in welding of 2.25Cr-1Mo-0.25V steel are analyzed by using numerical method. An uncoupled therm

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4

Doty, F. David, Glenn N. Doty, John P. Staab, and Laura L. Holte. "Toward Efficient Reduction of CO2 to CO for Renewable Fuels." In ASME 2010 4th International Conference on Energy Sustainability. ASMEDC, 2010. http://dx.doi.org/10.1115/es2010-90362.

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Three major challenges — grid stability, domestic oil limitations, and climate change — could all be addressed simultaneously by using off-peak electrical energy to recycle CO2 into liquid fuels (such as gasoline, jet fuel, and diesel). Simulations have shown that recent innovations should make it practical to reduce CO2 to CO at over 66% of theoretical efficiency limits. When combined with other process advances, it would then be possible to synthesize most hydrocarbons and alcohols from point-source CO2 and clean off-peak grid energy (wind or nuclear) at system efficiencies in the range of 5

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