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,...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°C, 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.展开更多
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 oxi...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.展开更多
基金This work was supported by the National High Technology Research and Development Program (Grant No. 715-006-0122)the "973" Project of the Ministry of Science and Technology, China (Grant No. G1999022401).
文摘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°C, 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.
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)
文摘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.
