摘要
Partial oxidation of methane（POM） co-fed with CO_2 to syngas in a novel catalytic BaCo_（0.6）Fe_（0.2）Ta_（0.2）O_（3-δ） oxygen permeable membrane reactor was successfully reported.Adding CO_2 to the partial oxidation of methane reaction not only alters the ratio of CO/H_2,but also increases the oxygen permeation flux and CH_4 conversion.Around 96%CH_4 conversion with more than 93%CO_2 conversion and 100%CO selectivity is achieved,which shows an excellent reaction performance.A steady oxygen permeation flux of 15 mL/（cm^2 min） is obtained during the 100-h operation,which shows good stability as well.
Partial oxidation of methane（POM） co-fed with CO_2 to syngas in a novel catalytic BaCo_（0.6）Fe_（0.2）Ta_（0.2）O_（3-δ） oxygen permeable membrane reactor was successfully reported.Adding CO_2 to the partial oxidation of methane reaction not only alters the ratio of CO/H_2,but also increases the oxygen permeation flux and CH_4 conversion.Around 96%CH_4 conversion with more than 93%CO_2 conversion and 100%CO selectivity is achieved,which shows an excellent reaction performance.A steady oxygen permeation flux of 15 mL/（cm^2 min） is obtained during the 100-h operation,which shows good stability as well.
基金
the financial support by Natural Science Foundation of China(Nos.U0834004 and 20936001)
the Science-Technology Plan of Guangzhou City(No.2009J1-C511-1)
the Fundamental Research Funds for the Central Universities,SCUT(No.2009220038)
