Deasphalting, deashing and upgrading of coal liquids. Quarterly technical progress report, January-March 1980

Technical Report · Sun Jun 01 04:00:00 EDT 1980

DOI:https://doi.org/10.2172/5369548· OSTI ID:5369548

Riedl, F. J.; deRosset, A. J.

Continuing work on deashing SRC-I filter feed has yielded deashed oils containing 0.004 wt % ash or less. The lowest reject bottoms yield was 18.8 wt %. This fails to meet the target of 15% maximum rejection. A summary of the deashing work on SRC-I filter feed has also shown that rejection decreased with use of higher boiling point solvents, with addition of up to 10% light aromatic component to the solvent, and with increased operating temperature. The hydrotreatment of the deashed oil derived from SRC-I filter feed yielded oils containing 9.99 wt % and 10.17 wt % hydrogen. Recoveries of oil ranged from 99.20 to 99.65 wt %. Hydrogen consumption was 1080 to 1090 SCFB hydrogen. Two deashed oils derived from UOP coal liquefaction product have been catalytically cracked. Conversions ranged from 44 to 60 vol %.

• Research Organization: UOP, Inc., Des Plaines, IL (USA). Corporate Research Center
• OSTI ID: 5369548
• Report Number(s): FE-2645-06
• Country of Publication: United States
• Language: English

Related Subjects

01 COAL, LIGNITE, AND PEAT
010402 -- Coal
Lignite
& Peat-- Purification & Upgrading
010405* -- Coal
Lignite
& Peat-- Hydrogenation & Liquefaction
CATALYTIC CRACKING
CHEMICAL REACTIONS
COAL LIQUEFACTION
COAL LIQUIDS
CRACKING
DATA
DATA FORMS
DEASHING
DECOMPOSITION
EXPERIMENTAL DATA
HYDROGENATION
INFORMATION
LIQUEFACTION
NUMERICAL DATA
ORGANIC SOLVENTS
PYROLYSIS
SOLVENTS
SRC PROCESS
TABLES
TEMPERATURE DEPENDENCE
THERMOCHEMICAL PROCESSES