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Process for converting methane into ethane in a membrane reactor

机译:在膜反应器中将甲烷转化为乙烷的方法

摘要

The invention relates to a process for producing ethane comprising contacting methane with a metal catalyst selected from metal hydrides, organometallic compounds, organometallic hydrides and metal clusters, in a reaction zone and forming a reaction mixture comprising ethane and hydrogen, the reaction zone comprising a membrane reactor equipped with a selective hydrogen-permeable membrane. It also relates to the use of such a membrane reactor for activating the metal catalyst to reach its maximum activity during the initial reaction phase in the process for converting methane into ethane. The membrane can be selected from microporous inorganic membranes and dense inorganic membranes preferably chosen from metallic, ceramic or cermet (ceramic-metal) membranes, preferably from palladium and/or palladium alloy membranes and from proton-conducting ceramic membranes. One of the main advantages of the process relates to the methane conversion rate which very quickly reaches an extremely high maximum during the initial reaction phase of the conversion, so that the global methane conversion rate is very high, while maintaining a very high selectivity for ethane.
机译:本发明涉及一种生产乙烷的方法,该方法包括使甲烷与选自金属氢化物,有机金属化合物,有机金属氢化物和金属簇的金属催化剂在反应区中接触,并形成包含乙烷和氢的反应混合物,该反应区包含膜。装有选择性氢可渗透膜的反应器。还涉及这种膜反应器在使甲烷转化为乙烷的过程中的初始反应阶段中活化金属催化剂以达到其最大活性的用途。该膜可选自微孔无机膜和致密无机膜,其优选选自金属,陶瓷或金属陶瓷(陶瓷-金属)膜,优选选自钯和/或钯合金膜以及质子传导陶瓷膜。该方法的主要优点之一是甲烷转化率,该甲烷转化率在转化的初始反应阶段非常快地达到极高的最大值,因此总体甲烷转化率非常高,同时保持了对乙烷的非常高的选择性。 。

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