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A New Type Hydrogen Permeable Membrane and Application for H2O2 Synthesis

机译:一种新型氢渗透膜和H2O2合成的应用

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Development of a hydrogen permeable membrane reactor in chemical process has been desired because of a great reduction of energy consumption. Previous studies were limited to Pd membranes. A new type of hydrogen permeable membrane layered three sheets (a reduction-Pt-catalyst sheet | a proton and electron co-conductive sheet | an oxidation-Ptcatalyst sheet) was developed. The middle sheet was prepared by casting a paste of carbon powder and Nafion solution. When a gas mixture of H2 and He (1:1) was introduced to the oxidation-catalyst compartment at 298 K, a high concentration of H2 was observed in the reduction-catalyst compartment, a maximum H2/He ratio as 217. H2 selectively permeated through the membrane. This concept was applied for synthesis of H2O2. When O2 and H2 were respectively introduced to the Co-N-C reduction-catalyst and the Pt oxidation-catalyst, production of a pure H2O2 aqueous solution of 3.8 mol dm~(-3) was succeeded with a good selectivity as 42% based on H2 at 278 K.
机译:由于能源消耗大大减少,因此需要在化学过程中开发氢渗透的膜反应器。先前的研究仅限于PD膜。开发了一种新型的氢渗透膜分层三片(开发了质子和电子共导板|氧化型 - Ptcatalyst表)。中间纸是通过铸造碳粉和Nafion溶液糊制备的。当将H2的气体混合物和He(1:1)引入298 K的氧化催化剂室时,在还原催化剂室中观察到高浓度的H2,最大H2/HE比为217。通过膜渗透。该概念用于H2O2的合成。当分别将O2和H2分别引入CO-N-C还原催化剂和PT氧化催化剂时,纯H2O2水溶液的生产为3.8 mol DM〜(-3)的成功,以良好的选择性为基础,基于H2,其良好的选择性为42%在278 K.

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