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U.S. Department of Energy
Office of Scientific and Technical Information

Integrated two stage liquefaction: extract recycle to first stage. Quarterly technical progress report, January 1-March 31, 1981

Technical Report ·
OSTI ID:5412975
This program combines a research study on Catalytic Expanded Bed Hydroprocessing of Coal Extracts (Task 1) and the operation of an Integrated Two-Stage Liquefaction process development unit (Task 2). The Task 1 baseline run closely reproduced earlier results obtained with New Brunswick process development units, when operated at similar reaction conditions. However, a two-to three-fold increase in the internal recycle rate increased extract conversion by as much as 20%. The integrated operation of Task 2 continued with equilibrated solvent. Three Short Contact Time (SCT) runs resulted in conversions of 89.7 to 93.8 percent of the moisture, ash-free (MAF) coal feed. The deasher recovered 74 to 83% of the extract from the SCT product. The second charge of LC-Fining catalyst has accumulated an age of almost 400 pounds of 850/sup 0/F+ feed per pound of catalyst. Conversion activity has held constant, while some decline has been detected in denitrogenation activity. Product quality remains high, with less than 0.2% nitrogen in the C/sub 5/-850/sup 0/F product. The chemical hydrogen consumption in the LC-Fining reaction constitutes about 90% of the overall hydrogen consumption of the Integrated PDU.
Research Organization:
Lummus Co., Bloomfield, NJ (USA); Cities Service Research and Development Co., Tulsa, OK (USA). Cities Service Technical Center
DOE Contract Number:
AC22-79ET14804
OSTI ID:
5412975
Report Number(s):
DOE/ET/14804-6; ON: DE82009315
Country of Publication:
United States
Language:
English