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Catalytic partial oxidation of methane to syngas in a fixed-bed reactor with an O2-distributor:The axial temperature profile and species profile study

机译:在带有O2分配器的固定床反应器中甲烷催化部分氧化为合成气:轴向温度分布和物种分布研究

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摘要

Catalytic partial oxidation of methane(CPOM)to syngas has been investigated in a fixed-bed reactor with an O2-distributor(FR-OD).The axial temperature profile and species profile along the Ni or Rh-based catalyst bed have been measured at different conditions.As the O2 was distributed radially into the catalyst bed through several rows of holes arranged at the special zone of the OD,a microenvironment maintaining a low O2/CH4 ratio(0.10-0.22)was provided in the catalyst bed.The hotspot phenomena appeared at the entrance of the catalyst bed have been effectively controlled.A more uniform temperature profile along the catalyst bed has been given,which is beneficial to the stability of catalyst and the safety of reactor operation.
机译:在具有O2分布器(FR-OD)的固定床反应器中研究了甲烷催化部分氧化为合成气的现象,并在Ni或Rh基催化剂床上测量了轴向温度分布和物种分布。由于O2通过在OD的特殊区域布置的几排孔径向分布到催化剂床中,因此在催化剂床中提供了一个维持低O2 / CH4比(0.10-0.22)的微环境。有效地控制了在催化剂床入口出现的现象。给出了沿催化剂床更均匀的温度曲线,这有利于催化剂的稳定性和反应器的安全性。

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