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- W2092082326 abstract "The Hydrocracking Section of the 1.2 TPD (45 kg/h) PDU completed a program feeding SRC-I with recycle of all +200/sup 0/C distillate. As expected from smaller-scale work, a gasoline yield of 49% was obtained, corresponding to 67% if all +200/sup 0/C were recycled to extinction. The final research octane number was down from 93 to 87, indicating that conditions were slightly too severe to produce the desired 90-92 RON. The Regeneration Section of the PDU is being revised to upgrade melt handling and is on schedule. The laboratory study of the effect of ash metal chlorides on catalyst activity concludes that the build-up of KCl, NaCl, CaCl/sub 2/ and FeCl/sub 2/ should be limited by equilibria involved to levels where the reduction of catalyst activity will be small. An economic estimate for a commercial plant making 53,000 bbl/SD (8.4 x 10/sup 6/ liters/SD) of gasoline from Western coal projects gasoline costs which encourage further development of the process." @default.
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- W2092082326 date "1979-06-29" @default.
- W2092082326 modified "2023-09-26" @default.
- W2092082326 title "Zinc halide hydrocracking process for distillate fuels from coal. Quarterly technical progress report, February 1-April 30, 1979" @default.
- W2092082326 doi "https://doi.org/10.2172/5630942" @default.
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