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U.S. Department of Energy
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Process development for improved SRC options. Kerr-McGee Critical Solvent Deashing and Fractionation Studies. Final report

Technical Report ·
OSTI ID:6314376
The SRC-1/2 Process, a coal liquefaction process which includes Kerr-McGee Critical Solvent Deashing (CSD), was demonstrated in a blocked-out fashion in continuous bench-scale units. This work demonstrated that conventional SRC-I as well as Short-Residence-Time vacuum bottoms could be successfully deashed and fractionated and that the fractionated portion of the soluble coal product, Light SRC, could be added to liquefaction solvent to improve its quality. An amount of Light SRC equivalent to that which was initially added to liquefaction solvent was recovered in the CSD Process in most cases to maintain Light SRC recycle. Light SRC balance is dependent upon material balance restraints, along with limitations in the CSD Process to recover the Light SRC. However, these restraints were found to be satisfied over a wide range of liquefaction severities. Other CSD Bench-Scale work included studies directed toward increasing the recovery of soluble coal products and determining the operating restraints required to produce Light SRC. This work utilized feeds obtained from the Wilsonville SRC Pilot Plant. It was found that soluble coal product recovery was inversely proportional to the first-stage CSD temperature and that the fractionation step was sensitive to deashing solvent to feed ratio. The SRC-1/2 Process was not, however, fully integrated and therefore these results are not necessarily indicative of steady-state conditions. Integrated experiments are required to verify these findings.
Research Organization:
Kerr-McGee Corp., Oklahoma City, OK (USA)
OSTI ID:
6314376
Report Number(s):
EPRI-AP-1932; ON: DE81903785
Country of Publication:
United States
Language:
English