通过实验设计和透氧量测定研究焦炉煤气(cokeovengas,COG)或天然气中的甲烷在透氧膜反应器中的部分氧化重整途径，提出反应器内的“重整透氧”机理模型.在由混合导体和催化床构成的透氧膜反应器中，催化床主要实现甲烷裂解和催化重整的功能，在膜表面处的催化金属微粒完成了还原性气体的“吸附—溢流—氧化”过程，进而强化混合导体内部的氧离子传导.

By studying the partial oxidation of cokeovengas (COG) and CH₄ in oxygenpermeable membrane reactor through designing experiments and test of oxygen permeation, a “reformingpermeation” model in a membrane reactor is proposed. A membrane reactor is composed of an oxygenpermeable membrane and a catalyst bed. The catalyst bed mainly realizes the pyrolysis of CH₄ and catalytic reforming, and metal particles on the membrane surface accomplishes the “adsorption—spillover—oxidation” processes of the reducing compositions in the gas to promote conduction of oxygen ion in mixed conductors.