HYDRODESULFURIZATION, DEOXYGENATION AND DEWAXING PROCESSES WITH WATER STABLE CATALYSTS FOR BIOMASS-CONTAINING HYDROCARBON FEEDSTOCKS
    1.
    发明申请
    HYDRODESULFURIZATION, DEOXYGENATION AND DEWAXING PROCESSES WITH WATER STABLE CATALYSTS FOR BIOMASS-CONTAINING HYDROCARBON FEEDSTOCKS 审中-公开
    用于生物质含烃油料的水稳定催化剂的水解,脱氧和脱蜡工艺

    公开(公告)号:US20130338414A1

    公开(公告)日:2013-12-19

    申请号:US13906907

    申请日:2013-05-31

    Abstract: This invention relates to a method for hydroprocessing feedstreams containing both sulfur-containing mineral oils and biomass-derived feedstocks in a single reactor configuration. The process produces a desulfurized, deoxygenated and dewaxed hydrocarbon product having reduced oxygen content, increased iso-paraffin content, low n-paraffin content, and good cold flow properties. In preferred embodiments, the processes herein utilize water tolerant hydrodewaxing catalysts in order to prevent deactivation and/or catalyst loss due to water produced during the deoxygenation reactions in the biomass components.

    Abstract translation: 本发明涉及在单一反应器构型中加氢处理含有含硫矿物油和生物质衍生原料的原料流的方法。 该方法产生具有降低的氧含量,增加的异链烷烃含量,低正链烷烃含量和良好的冷流特性的脱硫,脱氧和脱蜡的烃产物。 在优选的实施方案中,本文的方法使用耐水加氢脱蜡催化剂,以防止由于在生物量组分中的脱氧反应期间产生的水而导致的失活和/或催化剂损失。

    Process intensification for reverse flow reactors

    公开(公告)号:US11220429B2

    公开(公告)日:2022-01-11

    申请号:US16838726

    申请日:2020-04-02

    Abstract: Systems and methods are provided for improving thermal management and/or efficiency of reaction systems including a reverse flow reactor for performance of at least one endothermic reaction and at least one supplemental exothermic reaction. The supplemental exothermic reaction can be performed in the recuperation zone of the reverse flow reactor system. By integrating the supplemental exothermic reaction into the recuperation zone, the heat generated from the supplemental exothermic reaction can be absorbed by heat transfer surfaces in the recuperation zone. The adsorbed heat can then be used to heat at least one of the fuel and the oxidant for the combustion reaction performed during regeneration, thus reducing the amount of combustion that is needed to achieve a desired temperature profile at the end of the regeneration step.

    PROCESS INTENSIFICATION FOR REVERSE FLOW REACTORS

    公开(公告)号:US20210061657A1

    公开(公告)日:2021-03-04

    申请号:US16838726

    申请日:2020-04-02

    Abstract: Systems and methods are provided for improving thermal management and/or efficiency of reaction systems including a reverse flow reactor for performance of at least one endothermic reaction and at least one supplemental exothermic reaction. The supplemental exothermic reaction can be performed in the recuperation zone of the reverse flow reactor system. By integrating the supplemental exothermic reaction into the recuperation zone, the heat generated from the supplemental exothermic reaction can be absorbed by heat transfer surfaces in the recuperation zone. The adsorbed heat can then be used to heat at least one of the fuel and the oxidant for the combustion reaction performed during regeneration, thus reducing the amount of combustion that is needed to achieve a desired temperature profile at the end of the regeneration step.

    CO2 HYDROGENATION IN REVERSE FLOW REACTORS

    公开(公告)号:US20210061656A1

    公开(公告)日:2021-03-04

    申请号:US16838654

    申请日:2020-04-02

    Abstract: Systems and methods are provided for hydrogenation of CO2 in a reverse flow reactor environment via a reverse water gas shift reaction. A reverse flow reactor environment is suitable for performing endothermic reactions at high temperatures, where a reactant flow is passed into the reactor in a first portion of the cycle in a first flow direction while a combustion or heating flow is passed into the reactor during a second portion of the reaction cycle from the opposite direction. This can allow for efficient heating of surfaces within the reactor to provide heat for the endothermic reverse water gas shift reaction while reducing or minimizing incorporation of combustion products into the desired reaction products.

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