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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:致密的混合透氧透氧膜在高温下选择性地渗透到氧气,但不是氮气或任何其他气体。因此,只有来自空气的氧气可以通过膜传送到反应器的内部,在那里它与光烃反应,同时电子可以将电子输送回氧还原侧。氧气以氧离子的形式传输氧气,因此膜表面上有许多氧物种(O〜 - ,O〜(2-),O_2〜(2-),O〜(2-),O_2) 。不同的反应需要不同的氧气物种,因此膜在轻质烃的催化转化中提供了若干问题的潜在解决方案。在本介绍中,我们将讨论由Ba_(0.5)Sr_(0.5)CO_(0.2)Fe_(0.2)O_(3-D)(BSCF)制成的氧渗透膜反应器中甲烷和乙烷的催化转化。

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