首页> 外国专利> PROCESS FOR PRODUCING CARBON DIOXIDE AND HYDROGEN FROM CARBON MONOXIDE AND STEAM USING MIXED OXIDES OF COPPER,ZINC AND CHROMIUM AS CATALYST AND PROCESS FOR PRODUCING SAID CATALYST

PROCESS FOR PRODUCING CARBON DIOXIDE AND HYDROGEN FROM CARBON MONOXIDE AND STEAM USING MIXED OXIDES OF COPPER,ZINC AND CHROMIUM AS CATALYST AND PROCESS FOR PRODUCING SAID CATALYST

机译:以铜,锌,铬混合氧化物为催化剂,从一氧化碳和蒸气中制取二氧化碳和氢气的方法

摘要

A process for bringing the water-gas reaction system CO2 + H2 sX CO + H2O towards its state of equilibrium comprises contacting a gaseous mixture containing at least the reactants or the products of that system with a catalyst comprising the product of partly reducing the mixed oxides of Cu, Zn and Cr. The reactants may be furnished by the products of a catalysed hydrocarbon/steam reaction at elevated temperature. The ratio of hydrogen to carbon oxides in the gas fed to the Cu-Zn-Cr catalyst may be adjusted if desired by the addition of CO or CO2 on both, or of hydrogen, from a source other than a primary reformer. The process may be used for making CO2 and H2 at temperatures as low as 100-350 DEG C., and pressures of 50 atmospheres. Examples are given. Specifications 902,148, 908,505, 916,216 and 953,877 are referred to.ALSO:A process for producing oxygenated hydrocarbons comprises bringing a substantially sulphur-free gaseous mixture of hydrogen, carbon monoxide and carbon dioxide at elevated temperature and pressure into contact with a catalyst comprising the product of partly reducing the mixed oxides of Cu, Zn and Cr. In particular, the synthesis of methanol from CO, CO2 and H2 at 200-300 DEG C. and 1-350 atmospheres is described. General reference is made to the production of alcohols, aldehydes, ketones and mixtures thereof; the catalysts may be used for both hydrogenation and dehydrogenation. Specifications 902,148, 908,505, 916,216 and 953,877 are referred to.ALSO:Copper, zinc and chromium are coprecipitated from solution as one or more compounds readily convertible to oxides, under such conditions that at the end of the precipitation stage at most a minor part of the precipitated copper compound is decomposed. The Cu, Zn, Cr composite may thereafter be reduced in a stream of hydrogen, as such, or supported on unspecified carriers. Specifications 902,148, 908,505, 916,216 and 953,877 are referred to.
机译:使水-气反应系统CO 2 + H 2 sX CO + H 2 O达到其平衡状态的方法包括使至少包含该反应物或该系统产物的气态混合物与催化剂接触,该催化剂包含部分还原该混合物的产物。铜,锌和铬的氧化物。可以通过在升高的温度下催化的烃/蒸汽反应的产物来提供反应物。如果需要,可以通过在初级转化器以外的来源中在两者上添加CO或CO 2或添加氢气来调节送入Cu-Zn-Cr催化剂中的气体中氢气与碳氧化物的比例。该方法可用于在低至100-350℃的温度和50个大气压的压力下制备CO 2和H 2。举了例子。参照规格902,148,908,505,916,216和953,877.ALSO:一种生产含氧烃的方法,包括使氢气,一氧化碳和二氧化碳的基本无硫的气态混合物在高温和高压下与包含该产物的催化剂接触部分还原铜,锌和铬的混合氧化物。特别地,描述了在200-300℃和1-350个大气压下由CO,CO 2和H 2合成甲醇。一般涉及醇,醛,酮及其混合物的生产。该催化剂可用于氢化和脱氢。参照规格902,148,908,505,916,216和953,877.ALSO:铜,锌和铬以一种或多种易于转化为氧化物的化合物的形式从溶液中共沉淀,在沉淀阶段结束时至多为一小部分。沉淀的铜化合物分解。此后,可以在氢气流中还原Cu,Zn,Cr复合材料,或将其负载在未指定的载体上。参考规格902,148、908,505、916,216和953,877。

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