Mixed oxide based catalyst for the conversion of carbon dioxide to syngas and method of preparation and use
    1.
    发明授权
    Mixed oxide based catalyst for the conversion of carbon dioxide to syngas and method of preparation and use 有权
    用于将二氧化碳转化为合成气的混合氧化物基催化剂及其制备和使用方法

    公开(公告)号:US08962702B2

    公开(公告)日:2015-02-24

    申请号:US13315083

    申请日:2011-12-08

    IPC分类号: C07C27/00

    摘要: The invention relates to a catalyst and process for making syngas mixtures including hydrogen, carbon monoxide and carbon dioxide. The process comprises contacting a gaseous feed mixture containing carbon dioxide and hydrogen with the catalyst, where the catalyst comprises Mn oxide and an auxiliary metal oxide selected from the group consisting of La, Ca, K, W, Cu, Al and mixtures or combinations thereof. The process enables hydrogenation of carbon dioxide into carbon monoxide with high selectivity, and good catalyst stability over time and under variations in processing conditions. The process can be applied separately, but can also be integrated with other processes, both up-stream and/or down-stream including methane reforming or other synthesis processes for making products like alkanes, aldehydes, or alcohols.

    摘要翻译: 本发明涉及一种制备合成气混合物的催化剂和方法,包括氢气,一氧化碳和二氧化碳。 该方法包括使含有二氧化碳和氢气的气态进料混合物与催化剂接触,其中催化剂包含Mn氧化物和选自La,Ca,K,W,Cu,Al及其混合物或组合的辅助金属氧化物 。 该方法能够以高选择性将二氧化碳氢化为一氧化碳,并且随着时间和处理条件的变化,催化剂的稳定性良好。 该方法可以分开应用,但也可以与上游和/或下游的其它方法(包括甲烷重整或用于制备产物如烷烃,醛或醇的其它合成方法)整合。

    MIXED OXIDE BASED CATALYST FOR THE CONVERSION OF CARBON DIOXIDE TO SYNGAS AND METHOD OF PREPARATION AND USE
    2.
    发明申请
    MIXED OXIDE BASED CATALYST FOR THE CONVERSION OF CARBON DIOXIDE TO SYNGAS AND METHOD OF PREPARATION AND USE 有权
    用于将二氧化碳转化为合成物的混合氧化物催化剂及其制备和使用方法

    公开(公告)号:US20130150466A1

    公开(公告)日:2013-06-13

    申请号:US13315083

    申请日:2011-12-08

    摘要: The invention relates to a catalyst and process for making syngas mixtures including hydrogen, carbon monoxide and carbon dioxide. The process comprises contacting a gaseous feed mixture containing carbon dioxide and hydrogen with the catalyst, where the catalyst comprises Mn oxide and an auxiliary metal oxide selected from the group consisting of La, Ca, K, W, Cu, Al and mixtures or combinations thereof. The process enables hydrogenation of carbon dioxide into carbon monoxide with high selectivity, and good catalyst stability over time and under variations in processing conditions. The process can be applied separately, but can also be integrated with other processes, both up-stream and/or down-stream including methane reforming or other synthesis processes for making products like alkanes, aldehydes, or alcohols.

    摘要翻译: 本发明涉及一种制备合成气混合物的催化剂和方法,包括氢气,一氧化碳和二氧化碳。 该方法包括使含有二氧化碳和氢气的气态进料混合物与催化剂接触,其中催化剂包含Mn氧化物和选自La,Ca,K,W,Cu,Al及其混合物或组合的辅助金属氧化物 。 该方法能够以高选择性将二氧化碳氢化为一氧化碳,并且随着时间和处理条件的变化,催化剂的稳定性良好。 该方法可以分开应用,但也可以与上游和/或下游的其它方法(包括甲烷重整或用于制备产物如烷烃,醛或醇的其它合成方法)整合。

    MODIFIED ZINC FERRITE CATALYST AND METHOD OF PREPARATION AND USE
    3.
    发明申请
    MODIFIED ZINC FERRITE CATALYST AND METHOD OF PREPARATION AND USE 有权
    改性锌铁氧体催化剂及其制备和使用方法

    公开(公告)号:US20120059208A1

    公开(公告)日:2012-03-08

    申请号:US12874479

    申请日:2010-09-02

    摘要: A catalyst for oxidative dehydrogenation of organic compounds is provided by forming a solution of catalyst precursor components comprised of Fe+3 and Zn+2 cations and at least one other modifier element cation in water to form an aqueous solution of the catalyst precursor components. The modifier element cation has a standard reduction potential of from greater than about −2.87 E° (V) to less than about −0.036 E° (V) with a valence of +2. A base is separately and simultaneously added to the aqueous solution in amounts to maintain the pH of the aqueous solution at a pH of from about 8.5 to about 9.5 as the catalyst precursor components. The catalyst precursor components are allowed to react and precipitate out of solution as a precipitate. The resulting precipitate is calcined to form a modified zinc ferrite catalyst compound.

    摘要翻译: 通过在水中形成由Fe + 3和Zn + 2阳离子和至少一种其它改性元素阳离子组成的催化剂前体组分的溶液以形成催化剂前体组分的水溶液来提供有机化合物的氧化脱氢催化剂。 改性剂元素阳离子具有大于约-2.87E(V)至小于约-0.036E(V)的标准还原电位,其价态为+2。 单独地并且同时地将碱加入到水溶液中,其用量将水溶液的pH保持在约8.5至约9.5的pH作为催化剂前体组分。 催化剂前体组分作为沉淀物反应并沉淀出溶液。 将所得沉淀物煅烧以形成改性的锌铁氧体催化剂化合物。

    Modified zinc ferrite catalyst and method of preparation and use
    4.
    发明授权
    Modified zinc ferrite catalyst and method of preparation and use 有权
    改性锌铁氧体催化剂及其制备方法

    公开(公告)号:US08551443B2

    公开(公告)日:2013-10-08

    申请号:US12874479

    申请日:2010-09-02

    IPC分类号: C07C15/00

    摘要: A catalyst for oxidative dehydrogenation of organic compounds is provided by forming a solution of catalyst precursor components comprised of Fe+3 and Zn+2 cations and at least one other modifier element cation in water to form an aqueous solution of the catalyst precursor components. The modifier element cation has a standard reduction potential of from greater than about −2.87 E° (V) to less than about −0.036 E° (V) with a valence of +2. A base is separately and simultaneously added to the aqueous solution in amounts to maintain the pH of the aqueous solution at a pH of from about 8.5 to about 9.5 as the catalyst precursor components. The catalyst precursor components are allowed to react and precipitate out of solution as a precipitate. The resulting precipitate is calcined to form a modified zinc ferrite catalyst compound.

    摘要翻译: 通过在水中形成由Fe + 3和Zn + 2阳离子和至少一种其它改性元素阳离子组成的催化剂前体组分的溶液以形成催化剂前体组分的水溶液来提供有机化合物的氧化脱氢催化剂。 改性剂元素阳离子具有大于约-2.87E(V)至小于约-0.036E(V)的标准还原电位,其价态为+2。 单独地并且同时地将碱加入到水溶液中,其用量将水溶液的pH保持在约8.5至约9.5的pH作为催化剂前体组分。 催化剂前体组分作为沉淀物反应并沉淀出溶液。 将所得沉淀物煅烧以形成改性的锌铁氧体催化剂化合物。

    Method of forming a syngas mixture
    5.
    发明授权
    Method of forming a syngas mixture 有权
    形成合成气混合物的方法

    公开(公告)号:US08551434B1

    公开(公告)日:2013-10-08

    申请号:US13537302

    申请日:2012-06-29

    IPC分类号: B01D53/14

    摘要: A method for making a syngas mixture is accomplished by introducing a gaseous feed mixture containing carbon dioxide and hydrogen into a reactor containing a non-zinc catalyst. The catalyst contacts the gaseous feed mixture to form syngas mixture reaction products. The reaction takes place in the presence of nickel-containing and/or iron-containing materials. The gaseous feed mixture is introduced into the reactor at a reactor inlet temperature of from 700° C. to 800° C., with the reaction being carried out at substantially adiabatic conditions or wherein the syngas mixture reaction products are removed from the reactor at a reactor outlet temperature of from 500° C. to 600° C.

    摘要翻译: 制备合成气混合物的方法是通过将含有二氧化碳和氢气的气态进料混合物引入含有非锌催化剂的反应器来完成的。 催化剂接触气态进料混合物以形成合成气混合反应产物。 反应在含镍和/或含铁材料的存在下进行。 将气态进料混合物在700℃至800℃的反应器入口温度下引入反应器,反应在基本上绝热的条件下进行,或者其中合成气混合物反应产物在反应器中以 反应器出口温度为500℃至600℃