High-pressure hydrogenation of crude shale oil. [At 800 to 900/sup 0/F; use of several catalysts including W or Co molybdates]

Crude shale oil, obtained by the retorting of Colorado oil shale in a gas-flow retort, was hydrogenated over several solid catalysts in a continuous high-pressure unit on a once-through basis. At 9000 lb./sq.in.. gage hydrogen pressure and at temperatures of 800 'to 900'F ., a product oil essentially free of sulfur and nitrogen and suitable for further processing by standard petroleum methods can be produced. Using tungsten or cobalt molybdate catalysts. 40 to 50 vol. % of the product oil obtained by hydrogenation can be utilized as high-quality diesel fuel (octane ratings of 50 to 60). Depending on the type of catalyst used and the temperature of operation, hydrogen consumption varied from 2000 to 2800 cu.ft../ bbl. of shale-oil feed.

Data and Resources

Field Value
Citation "\"Pelipetz, M.G. Wolfson, M.L. ; Ginsberg, H. ; Clark, E.L.\""
Is NETL associated "\"Yes\""
NETL Point of Contact "\"Roy Long\""
NETL Point of Contact's Email "\"Roy.long@netl.doe.gov\""
NETL program or project "\"KMD\""
Publication Date "\"1/1/1952\""
Groups
  • AmeriGEOSS
  • Global Provider
Tags
  • amerigeo
  • amerigeoss
  • ckan
  • edx
  • energy
  • energy-data-exchange
  • geo
  • geoss
  • global
  • kmd
isopen True
license_id other-open
license_title Other (Open)
metadata_created 2025-11-25T21:04:05.605693
metadata_modified 2025-11-25T21:04:05.605698
notes Crude shale oil, obtained by the retorting of Colorado oil shale in a gas-flow retort, was hydrogenated over several solid catalysts in a continuous high-pressure unit on a once-through basis. At 9000 lb./sq.in.. gage hydrogen pressure and at temperatures of 800 'to 900'F ., a product oil essentially free of sulfur and nitrogen and suitable for further processing by standard petroleum methods can be produced. Using tungsten or cobalt molybdate catalysts. 40 to 50 vol. % of the product oil obtained by hydrogenation can be utilized as high-quality diesel fuel (octane ratings of 50 to 60). Depending on the type of catalyst used and the temperature of operation, hydrogen consumption varied from 2000 to 2800 cu.ft../ bbl. of shale-oil feed.
num_resources 1
num_tags 10
title High-pressure hydrogenation of crude shale oil. [At 800 to 900/sup 0/F; use of several catalysts including W or Co molybdates]