首页> 外文会议>Asia-Pacific Congress on Catalysis:Abstracts vol.1; 20031012-15; Dalian(CN) >Catalytic Conversion of Light Hydrocarbons in an Oxygen-Permeable Membrane Reactor
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Catalytic Conversion of Light Hydrocarbons in an Oxygen-Permeable Membrane Reactor

机译:透氧膜反应器中轻烃的催化转化

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Dense mixed-conducting oxygen-permeable membrane is selectively permeable to oxygen at high temperature, but not to nitrogen or any other gases. Thus, only oxygen from air can be transported through the membrane to the inside of the reactor, where it reacts with light hydrocarbons, at the same time electrons can transport back to the oxygen-reduction side. Oxygen transports through the membrane in the form of oxygen ion, so there are many oxygen species (O~-, O~(2-), O_2~(2-), O~(2-), O_2) on the membrane surface. Different reactions need the different oxygen species, so the membrane offers a potential solution to several problems in the catalytic conversion of light hydrocarbons. In this presentation, we will discuss the catalytic conversion of methane and ethane in the oxygen-permeable membrane reactor made of Ba_(0.5)Sr_(0.5)Co_(0.8)Fe_(0.2)O_(3-d) (BSCF).
机译:致密的混合导电透氧膜在高温下对氧气具有选择性的渗透性,而对氮气或任何其他气体则不能。因此,只有空气中的氧气可以通过膜输送到反应器内部,在这里它与轻质烃反应,同时电子可以输送回氧气还原侧。氧气以氧离子的形式穿过膜,因此在膜表面上存在许多氧(O〜-,O〜(2-),O_2〜(2-),O〜(2-),O_2) 。不同的反应需要不同的氧种类,因此该膜为轻烃催化转化中的若干问题提供了潜在的解决方案。在此演示文稿中,我们将讨论由Ba_(0.5)Sr_(0.5)Co_(0.8)Fe_(0.2)O_(3-d)(BSCF)制成的透氧膜反应器中甲烷和乙烷的催化转化。

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