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    • 1. 发明授权
    • Biomass conversion process
    • 生物质转换过程
    • US08003835B2
    • 2011-08-23
    • US12606804
    • 2009-10-27
    • Steve YanikRobert BartekPaul O'ConnorDennis StamiresMichael Brady
    • Steve YanikRobert BartekPaul O'ConnorDennis StamiresMichael Brady
    • C07C1/00F27B15/08
    • 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 f) 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℃的温度下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, 包含烃的第一产物; 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 - 催化剂混合物装载到在约200℃至约400℃的温度范围内操作的第二提升管,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f)将第三流出物与废催化剂分离。
    • 3. 发明授权
    • Modular biomass treatment unit
    • 模块化生物质处理装置
    • US08558043B2
    • 2013-10-15
    • US12717744
    • 2010-03-04
    • Steve YanikPaul O'ConnorRobert Bartek
    • Steve YanikPaul O'ConnorRobert Bartek
    • C07C1/00C10G1/10
    • C10L9/083C10G3/42C10G3/49C10G2300/1014C10G2300/1037C10L1/04Y02E50/15Y02P30/20
    • A modular biomass treatment unit includes a first module having a pretreater and a first frame for transportation to and operation at a site adjacent to a solid biomass growth source. The pretreater is operable to process solid biomass to produce a plurality of solid biomass particles for conversion into a fuel or specialty chemical. The first frame supports the pretreater during transportation to and operation at the site adjacent to the solid biomass growth source. The modular biomass treatment unit can also include additional modules each comprising a reactor, a separator, and a frame for transportation to and operation at a site such as the site adjacent to the solid biomass growth source.
    • 模块化生物质处理单元包括具有预处理器和第一框架的第一模块,用于运输到与固体生物质生长源相邻的位置并在其操作。 预处理器可操作地处理固体生物质以产生用于转化成燃料或特种化学品的多个固体生物质颗粒。 第一个框架在运输过程中支持预处理器,并在与固体生物质生长生长源相邻的地点操作。 模块化生物质处理单元还可以包括附加的模块,每个模块包括反应器,分离器和框架,用于运输到诸如邻近固体生物质生长源的部位的位置和操作。
    • 10. 发明申请
    • PROCESS CONTROL BY BLENDING BIOMASS FEEDSTOCKS
    • 通过混合生物量饲料进行过程控制
    • US20120160658A1
    • 2012-06-28
    • US13284321
    • 2011-10-28
    • Robert BartekSteve Yanik
    • Robert BartekSteve Yanik
    • C10B57/00C10B45/00
    • C10C5/00C10B53/02C10G2300/1014C10L1/02Y02E50/14Y02P20/145Y02P30/20
    • A process and system is disclosed for optimizing a key parameter of a biomass feedstock that enhances bio-oil production. The process and system involves optimizing the values of the key parameter in multiple biomass feedstocks by regulating their feed rates and blending those feedstocks to produce a cumulative biomass feedstock with an optimal value for the key parameter. The key parameter in the biomass feedstocks is measured and the feed rates of the multiple biomass feedstocks are adjusted in order to produce a cumulative biomass feedstock exhibiting optimal values for the desired key parameter. The key parameters can include compositional properties, such as lignin content or mineral content, and/or fluidization properties of the biomass materials, such as density, particle cohesion force, or particle size.
    • 公开了一种用于优化增强生物油生产的生物质原料的关键参数的方法和系统。 该过程和系统包括通过调节其进料速率并混合这些原料以产生具有关键参数的最佳值的累积生物质原料来优化多个生物质原料中关键参数的值。 测量生物质原料中的关键参数,并且调整多种生物质原料的进料速率以产生显示所需关键参数的最佳值的累积生物质原料。 关键参数可以包括诸如木质素含量或矿物质含量的组合性质和/或生物质材料的流化性质,例如密度,颗粒内聚力或粒度。