Two-stage coal liquefaction process
Abstract
An improved SRC-I two-stage coal liquefaction process which improves the product slate is provided. Substantially all of the net yield of 650.degree.-850.degree. F. heavy distillate from the LC-Finer is combined with the SRC process solvent, substantially all of the net 400.degree.-650.degree. F. middle distillate from the SRC section is combined with the hydrocracker solvent in the LC-Finer, and the initial boiling point of the SRC process solvent is increased sufficiently high to produce a net yield of 650.degree.-850.degree. F. heavy distillate of zero for the two-stage liquefaction process.
- Inventors:
-
- Allentown, PA
- Perkiomenville, PA
- Vancouver, CA
- Publication Date:
- Research Org.:
- INTERNATIONAL COAL REFINING CO
- OSTI Identifier:
- 865301
- Patent Number(s):
- US 4491511
- Assignee:
- International Coal Refining Company (Allentown, PA)
- DOE Contract Number:
- AC05-78OR03054
- Resource Type:
- Patent
- Country of Publication:
- United States
- Language:
- English
- Subject:
- two-stage; coal; liquefaction; process; improved; src-i; improves; product; slate; provided; substantially; net; yield; 650; degree; -850; heavy; distillate; lc-finer; combined; src; solvent; 400; -650; middle; section; hydrocracker; initial; boiling; increased; sufficiently; produce; zero; liquefaction process; coal liquefaction; process solvent; heavy distillate; two-stage coal; stage liquefaction; two-stage liquefaction; stage coal; /208/
Citation Formats
Skinner, Ronald W, Tao, John C, and Znaimer, Samuel. Two-stage coal liquefaction process. United States: N. p., 1985.
Web.
Skinner, Ronald W, Tao, John C, & Znaimer, Samuel. Two-stage coal liquefaction process. United States.
Skinner, Ronald W, Tao, John C, and Znaimer, Samuel. Tue .
"Two-stage coal liquefaction process". United States. https://www.osti.gov/servlets/purl/865301.
@article{osti_865301,
title = {Two-stage coal liquefaction process},
author = {Skinner, Ronald W and Tao, John C and Znaimer, Samuel},
abstractNote = {An improved SRC-I two-stage coal liquefaction process which improves the product slate is provided. Substantially all of the net yield of 650.degree.-850.degree. F. heavy distillate from the LC-Finer is combined with the SRC process solvent, substantially all of the net 400.degree.-650.degree. F. middle distillate from the SRC section is combined with the hydrocracker solvent in the LC-Finer, and the initial boiling point of the SRC process solvent is increased sufficiently high to produce a net yield of 650.degree.-850.degree. F. heavy distillate of zero for the two-stage liquefaction process.},
doi = {},
url = {https://www.osti.gov/biblio/865301},
journal = {},
number = ,
volume = ,
place = {United States},
year = {1985},
month = {1}
}
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