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    • 4. 发明申请
    • BIOMASS CONVERSION PROCESS
    • 生物量转换过程
    • WO2010062611A2
    • 2010-06-03
    • PCT/US2009062241
    • 2009-10-27
    • KIOR INCBARTEK ROBERTYANIK STEVEO'CONNOR PAULSTAMIRES DENNISBRADY MICHAEL
    • BARTEK ROBERTYANIK STEVEO'CONNOR PAULSTAMIRES DENNISBRADY MICHAEL
    • C10G1/08
    • C10G1/08C10B49/22C10B53/02C10B57/02C10G1/006C10G3/42C10G3/57Y02E50/14Y02E50/32Y02P20/145Y02P30/20
    • A method for converting solid biomass into hydrocarbons includes contacting the solid biomass with a catalyst in a first riser operated at a temperature in the range of from about 50° C to about 200° C to thereby produce a first biomass-catalyst mixture and a first product comprising hydrocarbons; a) separating the first product from the first biomass-catalyst mixture; c) charging the first biomass-catalyst mixture to a second riser operated at a temperature in the range of from about 200° C to about 400° C to thereby produce a second biomass-catalyst mixture and a second product comprising hydrocarbons; d) separating the second product from the second biomass-catalyst mixture; e) charging the second biomass-catalyst mixture to a third riser operated at a temperature greater than about 450° C to thereby produce a spent catalyst and a third product comprising hydrocarbons; and 0 separating the third effluent from the spent catalyst.
    • 将固体生物质转化为烃的方法包括使固体生物质与在约50℃至约200℃的温度范围内操作的第一提升管中的催化剂接触,从而产生第一生物质 - 催化剂混合物和第一 包含烃的产品; a)将第一产物与第一生物质 - 催化剂混合物分离; c)将第一生物质 - 催化剂混合物装入在约200℃至约400℃范围内操作的第二提升管中,从而产生第二生物质 - 催化剂混合物和包含烃的第二产物; d)将第二产物与第二生物质 - 催化剂混合物分离; e)将第二生物质 - 催化剂混合物装入在大于约450℃的温度下操作的第三提升管,从而产生废催化剂和包含烃的第三产物; 和0将第三流出物与废催化剂分离。