CATALYTIC EFFECTS OF OXYGEN CARRIER BASED CHEMICL-LOOPING REFORMING OF CH4 WITH CO2
    2.
    发明申请
    CATALYTIC EFFECTS OF OXYGEN CARRIER BASED CHEMICL-LOOPING REFORMING OF CH4 WITH CO2 审中-公开
    基于氧气载体的CH4与CO 2的化学反应的催化作用

    公开(公告)号:US20160332150A1

    公开(公告)日:2016-11-17

    申请号:US15152245

    申请日:2016-05-11

    Abstract: The invention relates to CeO2 and La2O3 for catalyzing Fe2O3—Al2O3 based chemical-looping reforming of CH4 with CO2 (CL-DRM). The reaction performance of all the composite oxygen carriers was evaluated in a fixed-bed reactor at atmospheric pressure condition. The influencing factors, including temperature and time-on-stream (TOS) were investigated. The characteristics of the oxygen carriers were checked with Brunauer-Emmett-Teller (BET) analysis and X-ray diffraction (XRD). The reducibility of the composite materials was elucidated with temperature-programmed reduction by CH4 (CH4-TPR). Preliminary experimental observations suggest that the simultaneous presence of CeO2 and La2O3 can not only enhance the reactivity of Fe2O3—Al2O3 toward CH4 oxidation and its oxygen releasing rate for fast reaction kinetics, but also improve the reactivity of its reduced form toward CO2 splitting.

    Abstract translation: 本发明涉及用于催化基于Fe 2 O 3 -Al 2 O 3的CH 2与CO 2(CL-DRM)的化学循环重整的CeO 2和La 2 O 3。 在常压条件下,在固定床反应器中评价了所有复合载体的反应性能。 研究了影响因素,包括温度和时间(TOS)。 用Brunauer-Emmett-Teller(BET)分析和X射线衍射(XRD)检查氧载体的特征。 通过CH4(CH4-TPR)的温度程序化还原来阐明复合材料的还原性。 初步实验观察表明,CeO2和La2O3的同时存在不仅可以提高Fe2O3-Al2O3对CH4氧化的反应性及其释放速度,而且可以提高其还原形式对CO2分解的反应性。

    Catalytic effects of oxygen carrier based chemical-looping reforming of CH4 with CO2

    公开(公告)号:US10478807B2

    公开(公告)日:2019-11-19

    申请号:US15607954

    申请日:2017-05-30

    Abstract: The invention relates to CeO2 and La2O3 for catalyzing Fe2O3—Al2O3 based chemical-looping reforming of CH4 with CO2 (CL-DRM). The reaction performance of all the composite oxygen carriers was evaluated in a fixed-bed reactor at atmospheric pressure condition. The influencing factors, including temperature and time-on-stream (TOS) were investigated. The characteristics of the oxygen carriers were checked with Brunauer-Emmett-Teller (BET) analysis and X-ray diffraction (XRD). The reducibility of the composite materials was elucidated with temperature-programmed reduction by CH4 (CH4-TPR). Preliminary experimental observations suggest that the simultaneous presence of CeO2 and La2O3 can not only enhance the reactivity of Fe2O3—Al2O3 toward CH4 oxidation and its oxygen releasing rate for fast reaction kinetics, but also improve the reactivity of its reduced form toward CO2 splitting.

    Coal gasification with FeCO3 catalyst

    公开(公告)号:US10093874B2

    公开(公告)日:2018-10-09

    申请号:US14663205

    申请日:2015-03-19

    Abstract: Embodiments described herein generally relate to iron carbonate utilized as a catalyst in coal gasification processes. An FeCO3 catalyst is active in both pyrolysis and gasification operations, and may increase carbon conversion rate and reduce the activation energy of coal gasification. Methods described herein also include suitable processing conditions for performing coal gasification with the FeCO3 catalyst.

    Methods of catalytic hydrogenation for ethylene glycol formation

    公开(公告)号:US10086364B2

    公开(公告)日:2018-10-02

    申请号:US14749441

    申请日:2015-06-24

    Abstract: Embodiments described herein generally relate to hydrogenation catalysts, syntheses of hydrogenation catalysts, and apparatus and methods for hydrogenation. Methods for forming a hydrogenation catalyst may include mixing a silica generating precursor with a copper precursor and adding an ammonium salt to an end pH of between about 5 to about 9. Methods for hydrogenating an oxalate may include forming a reaction mixture by flowing a hydrogenation catalyst to a reactor, flowing a hydrogen source to the reactor, and flowing an oxalate to the reactor, wherein the hydrogenation catalyst has a particle size between about 10 nm to about 40 nm. Methods may further include reacting the oxalate to form ethylene glycol.

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