Hydrogenation of shale-oil coker distillate. [Over fized-bed Co--Mo catalyst at 1500 lb/sq. in. gage and 835/sup 0/F]

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This work was undertaken to prepare a large quantity of jet and Diesel fuel from crude shale oil by recycle coking followed by hydrogenation of the coker distillate at 1500 pounds per square inch gage pressure and 835 F over a fixed-bed cobalt molybdate catalyst.

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Clark, E.L. Hiteshue, R.W. ; Kandiner, H.J. ; Morris, B. ---- Roy Long, Hydrogenation of shale-oil coker distillate. [Over fized-bed Co--Mo catalyst at 1500 lb/sq. in. gage and 835/sup 0/F], 2016-09-29, https://edx.netl.doe.gov/dataset/hydrogenation-of-shale-oil-coker-distillate-over-fized-bed-co-mo-catalyst-at-1500-lb-sq-in-gag

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Field	Value
Last Updated	September 29, 2016, 19:04 (LMT)
Created	September 29, 2016, 19:04 (LMT)
Citation	Clark, E.L. Hiteshue, R.W. ; Kandiner, H.J. ; Morris, B. ---- Roy Long, Hydrogenation of shale-oil coker distillate. [Over fized-bed Co--Mo catalyst at 1500 lb/sq. in. gage and 835/sup 0/F], 2016-09-29, https://edx.netl.doe.gov/dataset/hydrogenation-of-shale-oil-coker-distillate-over-fized-bed-co-mo-catalyst-at-1500-lb-sq-in-gag
Netl Product	yes
Poc Email	Roy.long@netl.doe.gov
Point Of Contact	Roy Long
Program Or Project	KMD
Publication Date	1951-1-1

Hydrogenation of shale-oil coker distillate. [Over fized-bed Co--Mo catalyst at 1500 lb/sq. in. gage and 835/sup 0/F]

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