Coal liquefaction process using ash as a catalyst
    1.
    发明授权
    Coal liquefaction process using ash as a catalyst 失效
    使用ASH作为催化剂的煤液化过程

    公开(公告)号:US3671418A

    公开(公告)日:1972-06-20

    申请号:US3671418D

    申请日:1970-12-18

    Inventor: GATSIS JOHN G

    CPC classification number: C10G1/083 C10G1/006

    Abstract: A method for the liquefaction of coal using a solvent extraction process in which finely-divided coal, a solvent, and a catalystacting ash derived from coal are admixed and subjected to solvent extraction conditions. The ash utilized in the solvent extraction process is a substantially carbon-free residue resulting from the decarbonization of coal.

    Abstract translation: 使用溶剂萃取方法对煤进行液化的方法,其中将来自煤的细分散的煤,溶剂和催化剂作用的灰分混合并进行溶剂萃取条件。 在溶剂萃取过程中使用的灰分是由煤脱碳产生的基本无碳残余物。

    Multiple-stage slurry processing for black oil conversion
    8.
    发明授权
    Multiple-stage slurry processing for black oil conversion 失效
    用于黑油转换的多级浆液处理

    公开(公告)号:US3622495A

    公开(公告)日:1971-11-23

    申请号:US3622495D

    申请日:1970-01-22

    CPC classification number: C10G65/04

    Abstract: A catalytic slurry process for effecting the conversion of a hydrocarbonaceous charge stock containing asphaltenes, metallic contaminants and excessive quantities of sulfurous compounds. The slurry constitutes the charge stock, hydrogen and from about 1.0 percent to about 25.0 percent by weight of finely divided catalyst particles. The charge stock is converted by processing the slurry in at least two individual reaction zones having separation facilities therebetween. That portion of the first reaction zone product effluent containing the catalyst particles and unconverted nondistillables is processed in a succeeding reaction zone. At least the major portion of the product effluent from the succeeding reaction zone is recycled to combine with the fesh feed charge stock. Preferred catalysts are the unsupported sulfides of the metals from Groups V-B, VI-B and VIII.

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