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    • 1. 发明授权
    • Process for converting carbon-based energy carrier material
    • 用于转换碳基能量载体材料的方法
    • US08709239B2
    • 2014-04-29
    • US13892728
    • 2013-05-13
    • KiOR, Inc.
    • Paul O'ConnorDennis StamiresJacob Adriaan Moulijn
    • C10C3/02
    • C10G1/086C10B49/20C10G1/08C10G11/18Y02E50/14
    • A process is disclosed process for converting a solid or highly viscous carbon-based energy carrier material to liquid and gaseous reaction products, said process comprising the steps of: a) contacting the carbon-based energy carrier material with a particulate catalyst material b) converting the carbon-based energy carrier material at a reaction temperature between 200° C. and 450° C., preferably between 250° C. and 350° C., thereby forming reaction products in the vapor phase. In a preferred embodiment the process comprises the additional step of: c) separating the vapor phase reaction products from the particulate catalyst material within 10 seconds after said reaction products are formed. In a further preferred embodiment step c) is followed by: d) quenching the reaction products to a temperature below 200° C.
    • 公开了一种将固体或高粘度碳基能量载体材料转化为液体和气态反应产物的方法,所述方法包括以下步骤:a)使碳基能量载体材料与颗粒催化剂材料接触b)将 在200℃至450℃的反应温度下,优选250℃至350℃之间的碳基能量载体材料,从而在气相中形成反应产物。 在优选实施方案中,该方法包括以下附加步骤:c)在所述反应产物形成后10秒内从气态反应产物与颗粒状催化剂材料分离。 在另一优选实施方案中,步骤c)之后是:d)将反应产物淬灭至低于200℃的温度
    • 2. 发明申请
    • Improved Process for Converting Carbon-Based Energy Carrier Material
    • 改进碳基能量载体材料的改进方法
    • US20130245346A1
    • 2013-09-19
    • US13892728
    • 2013-05-13
    • KIOR, INC.
    • Paul O'ConnorDennis StamiresJacob Adriaan Moulijn
    • C10G1/08
    • C10G1/086C10B49/20C10G1/08C10G11/18Y02E50/14
    • A process is disclosed process for converting a solid or highly viscous carbon-based energy carrier material to liquid and gaseous reaction products, said process comprising the steps of: a) contacting the carbon-based energy carrier material with a particulate catalyst material b) converting the carbon-based energy carrier material at a reaction temperature between 200° C. and 450° C., preferably between 250° C. and 350° C., thereby forming reaction products in the vapor phase. In a preferred embodiment the process comprises the additional step of: c) separating the vapor phase reaction products from the particulate catalyst material within 10 seconds after said reaction products are formed. In a further preferred embodiment step c) is followed by: d) quenching the reaction products to a temperature below 200° C.
    • 公开了一种将固体或高粘度碳基能量载体材料转化为液体和气态反应产物的方法,所述方法包括以下步骤:a)使碳基能量载体材料与颗粒催化剂材料接触b)将 在200℃至450℃的反应温度下,优选250℃至350℃之间的碳基能量载体材料,从而在气相中形成反应产物。 在优选实施方案中,该方法包括以下附加步骤:c)在所述反应产物形成后10秒内从气态反应产物与颗粒状催化剂材料分离。 在另一优选实施方案中,步骤c)之后是:d)将反应产物淬灭至低于200℃的温度