CATALYST COMPOSITION
    3.
    发明申请

    公开(公告)号:US20250135439A1

    公开(公告)日:2025-05-01

    申请号:US18835647

    申请日:2022-02-18

    Abstract: Prior to reaction in an isomerization unit, the feed may be purified by contact with a composition comprising an alumina based catalyst including Group I or Group II cations or combinations thereof in a range from about 0 wt % to about 20 wt % Group I or Group II cations. In some embodiments, the alumina based catalyst has one or more of the following properties; pore volume in pores of less than 70 Å pore diameter of less than about 15% of Total Pore Volume: a pore volume in pores of greater than 350 Å pore diameter of less than 10% of Total Pore Volume; a median pore diameter by volume of less than 120 Å; a water pore volume of less than 1.10 cc/g;: and a surface area of greater than 160 m2/g.

    PROCESS FOR CONVERTING A BIOMASS MATERIAL
    5.
    发明申请
    PROCESS FOR CONVERTING A BIOMASS MATERIAL 审中-公开
    转化生物质材料的方法

    公开(公告)号:US20140330057A1

    公开(公告)日:2014-11-06

    申请号:US14265411

    申请日:2014-04-30

    Abstract: A process for converting a biomass material comprising a) pyrolyzing a biomass material to produce a biomass-derived pyrolysis product; b) mixing at least part of the biomass-derived pyrolysis product and a petroleum-derived hydrocarbon composition, which petroleum derived hydrocarbon composition has a C7-asphaltenes content of equal to or more than 0.2 wt %, based on the total weight of the petroleum-derived hydrocarbon composition, to produce a hydrocarbon-containing mixture; c) dewatering the hydrocarbon-containing mixture to produce a dewatered hydrocarbon-containing mixture; d) contacting the dewatered hydrocarbon-containing mixture with hydrogen in one or more ebullating bed reactors comprising a catalyst at a temperature in the range from 350 to 500° C. to produce a reaction product.

    Abstract translation: 一种用于转化生物质材料的方法,包括a)热解生物质材料以产生生物质衍生的热解产物; b)将至少部分生物质衍生的热解产物和石油衍生的烃组合物混合,所述石油衍生的烃组合物具有基于石油的总重量等于或大于0.2重量%的C7-沥青质含量 得到的含烃混合物; c)使含烃混合物脱水以产生脱水的含烃混合物; d)使脱水的含烃混合物与氢在一个或多个沸腾床反应器中接触,所述反应床包含催化剂,温度为350-500℃,以产生反应产物。

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