Processes and Systems for the Conversion of Hydrocarbons

    公开(公告)号:US20210002186A1

    公开(公告)日:2021-01-07

    申请号:US16979374

    申请日:2019-03-01

    Abstract: A process for endothermic dehydrogenation including contacting a catalyst material in a moving bed reactor having at least one reaction zone, the moving bed reactor comprising a heat exchanger containing a heating medium, wherein the catalyst material and the heating medium do not contact one another, and wherein at least 50% of the delta enthalpy of the at least one reaction zone is provided by the heat exchanger; and contacting a feedstock comprising hydrocarbons with the catalyst material in the at least one reaction zone of the moving bed reactor under reaction conditions to convert at least a portion of the hydrocarbons to a first effluent comprising a product comprising alkenes, alkynes, cyclic hydrocarbons, and/or aromatics.

    Process for Converting Syngas to Aromatics and Catalyst System Suitable Therefor
    14.
    发明申请
    Process for Converting Syngas to Aromatics and Catalyst System Suitable Therefor 审中-公开
    将合成气转化为芳烃和催化剂体系的方法适用于此

    公开(公告)号:US20160207846A1

    公开(公告)日:2016-07-21

    申请号:US14965099

    申请日:2015-12-10

    Abstract: The present invention relates to a multistage process and catalyst system therefor to convert syngas to aromatics. In a first stage, syngas is converted to a C1-C4 alcohol mixture by contacting syngas with a first catalyst comprising rhodium or copper at moderate temperature. In a second stage, the C1-C4 alcohol mixture is converted into an aromatic product by contact with a second catalyst comprising a molecular sieve and at least one Group 8-14 element, the molecular sieve having a Constraint Index about 1 to 12 and a silica to alumina ratio of about 10 to 100 at effective conversion conditions. The final aromatic product is rich in benzene, toluene, and xylenes (e.g. greater than 50% aromatics on a hydrocarbon basis).

    Abstract translation: 本发明涉及一种用于将合成气转化为芳族化合物的多级方法和催化剂体系。 在第一阶段,通过使合成气与中等温度的包含铑或铜的第一催化剂接触将合成气转化为C1-C4醇混合物。 在第二阶段中,C1-C4醇混合物通过与包含分子筛和至少一种第8-14族元素的第二催化剂接触而转化成芳香族产物,分子筛具有约1-12的约束指数和 在有效转化条件下,二氧化硅与氧化铝的比例约为10-100。 最终的芳香族产物富含苯,甲苯和二甲苯(例如在烃基上大于50%的芳族化合物)。

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