The Extent of Sulfur Removal from Gas Oil by Cobalt Molybdenum Catalyzed Trickle Flow Hydrodesulfurization

The Extent of Sulfur Removal from Gas Oil by Cobalt Molybdenum Catalyzed Trickle Flow Hydrodesulfurization
Title The Extent of Sulfur Removal from Gas Oil by Cobalt Molybdenum Catalyzed Trickle Flow Hydrodesulfurization PDF eBook
Author Robert Li-Huang Sun
Publisher
Pages 68
Release 1972
Genre Desulfurization
ISBN

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Hydrodesulfurization of a Residual Fuel from Wilmington, Calif., Crude Oil

Hydrodesulfurization of a Residual Fuel from Wilmington, Calif., Crude Oil
Title Hydrodesulfurization of a Residual Fuel from Wilmington, Calif., Crude Oil PDF eBook
Author Clyde M. Frost
Publisher
Pages 22
Release 1970
Genre Desulfurization
ISBN

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Hydrodesulfurization of Gas Oil Catalyzed by in Situ Molybdenum Compounds

Hydrodesulfurization of Gas Oil Catalyzed by in Situ Molybdenum Compounds
Title Hydrodesulfurization of Gas Oil Catalyzed by in Situ Molybdenum Compounds PDF eBook
Author Boonchai Seentrakoon
Publisher
Pages 224
Release 2006
Genre Catalysts
ISBN 9789741433759

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In situ decomposition of ammonium and tetrabutylammonium thiomolybdate (ATM and TBATM) were used to synthesize unsupported MoS[subscript 2] catalysts, the in situ activation consisted of decomposing the thiomolybdate precursors in the presence of hydrocarbon solvent under H[subscript 2] pressure at 350degrees Celsius during the hydrodesulfurization (HDS) of dibenzothiophene (DBT) or 4,6-dimethydibenzothiophene (4,6-DMDBT) as sulfur model compounds. In situ generated MOS[subscript 2] catalysts were characterized by XRD, BET, EDX and SEM. Parameters affecting the HDS reaction were investigated: hydrogen pressure, reaction time, amount of precursor, types of precursor, cobalt and nickel promoters, and water addition. Inhibition of pyridine was also examined. The results showed that, cobalt and nickel addition enhanced HDS activity of both in situ generated MoS[subscript 2] catalysts from ATM and TBATM precursors. The use of ATM precursor with added water for in situ generation of MoS[subscript 2] catalyst can lead to 100% conversion of HDS of 4,6-DMDBT under 30 atm H[subscript 2] pressure at 350degrees celsius. Model reaction suggested that water addition led to a high surface area, highly active MoS[subscript 2] catalyst. The optimal mole ratio of H[subscript 2]O/ATM = 1200 performed the highest surface area (559 m[superscript 2]/g). In addition, the catalysts could reduce the sulfur contents of straight run gas oil (SRGO) from 6100 ppm to 3250 ppm and from 310 ppm to 100 ppm in light cycle oil (LCO).

Commercialization of Cobalt Promoted Molybdenum Disulfide Hydrodesulfurization Unsupported Catalyst

Commercialization of Cobalt Promoted Molybdenum Disulfide Hydrodesulfurization Unsupported Catalyst
Title Commercialization of Cobalt Promoted Molybdenum Disulfide Hydrodesulfurization Unsupported Catalyst PDF eBook
Author Juan Hilario Leal
Publisher
Pages 101
Release 2016
Genre Catalysis
ISBN

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Energy Research Abstracts

Energy Research Abstracts
Title Energy Research Abstracts PDF eBook
Author
Publisher
Pages 632
Release 1988
Genre Power resources
ISBN

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Proceedings

Proceedings
Title Proceedings PDF eBook
Author American Petroleum Institute
Publisher
Pages 692
Release 1953
Genre Petroleum industry and trade
ISBN

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Chemical Reactions as a Means of Separation-sulfur Removal

Chemical Reactions as a Means of Separation-sulfur Removal
Title Chemical Reactions as a Means of Separation-sulfur Removal PDF eBook
Author Billy L. Crynes
Publisher Marcel Dekker
Pages 368
Release 1977
Genre Technology & Engineering
ISBN

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