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