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U.S. Department of Energy
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Zinc halide hydrocracking process for distillate fuels from coal. Annual technical progress report, February 1, 1977--January 31, 1978

Technical Report ·
DOI:https://doi.org/10.2172/6609731· OSTI ID:6609731
The major efforts during the year were (1) to construct a 1 TPD Process Development Unit (PDU) for conversion of coal to distillate fuels using a molten zinc chloride catalyst and (2) to explore the effects of operating variables on a 2 lb/hr continuous bench-scale unit and develop correlations predicting conversion and product yields with Montana subbituminous coal. Construction of the PDU is 88% complete, and break-in of the liquefaction sections is underway. Correlations of conversion with residence time were developed for temperatures from 385 to 427/sup 0/C (725 to 800/sup 0/F), and pressures of 16.5 and 24.1 MPa (2400 and 3500 psig). Yields per ton of MAF coal were up to 4.3 bbls gasoline and 1.0 bbl of higher boiling distillate in one pass. The raw gasoline had Research Octane Numbers of 90.6 to 92.3 and low nitrogen and sulfur. Single runs showed that other subbituminous coals and bituminous coal could be successfully converted with the process. A secondary zinc recovery step was developed to increase overall zinc recovery from 98.5-99.0 to 99.5-99.6% via fluidized bed treatment of the primary coal ash with HCl-air at 1038/sup 0/C (1900/sup 0/F). Savings of 3.5 cents/gallon of gasoline are estimated. Work continues to improve rejection of other ash metals. Attached as Appendix A are three reports which chronicled a 1975 economic study on conversion of coal extract to gasoline. Zinc chloride processing is estimated to save 8 to 16% over ebullated-bed hydrocracking, hydrotreating and reforming to make the same product.
Research Organization:
Conoco Coal Development Co., Library, PA (USA). Research Div.
OSTI ID:
6609731
Report Number(s):
FE-1743-49
Country of Publication:
United States
Language:
English