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Partial oxidation of methane to syngas in tubular oxygenpermeable reactor Partial oxidation of methane to syngas in tubular oxygenpermeable reactor

Partial oxidation of methane to syngas in tubular oxygenpermeable reactor

  • 期刊名字:科學(xué)通報(bào)
  • 文件大小:
  • 論文作者:Wang Haihui,CONG You,YANG Weis
  • 作者單位:State Key Laboratory of Catalysis
  • 更新時(shí)間:2023-02-15
  • 下載次數(shù):
論文簡(jiǎn)介

A dense Ba0.5Sr0.5Co0.8Fe0.2O3-δ membrane tube was prepared by the extruding method. Furthermore, a membrane reactor with this tubular membrane was successfully applied to partial oxidation of methane (POM) reaction,in which the separation of oxygen from air and the partial oxidation of methane are integrated in one process. At 875℃,94% of methane conversion, 98% of CO selectivity, 95% of H2 selectivity, and as high as 8.8 mL/(min @cm2) of oxygen flux were obtained. In POM reaction condition, the membrane tube shows a very good stability.

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