Crystalline metal-organic framework cobalt （II） benzenetricarboxylate C%（BTC）2·12H2O （MOF-Co） has been prepared using solvothermal method. The reaction of cobalt （II） nitrate and 1,3,5-benzenetriearboxyl...Crystalline metal-organic framework cobalt （II） benzenetricarboxylate C%（BTC）2·12H2O （MOF-Co） has been prepared using solvothermal method. The reaction of cobalt （II） nitrate and 1,3,5-benzenetriearboxylic （BTC） acid in a mixed solution of N,N-dimethylformarnide （DMF）/C2H5OH/H2O （1：1：1, v/v） at low temperature for short reaction times produced this crystalline compound. Compared with traditional hydrothermal method, a mixed solution method for the synthesis of crystalline metal complex was found to be highly efficient. After water molecules were removed from this metal complex, its exposed nodes served as active sites. When this MOF-Co was employed in the oxidation of CO, it showed good catalytic properties causing 100% conversion of CO to CO2 at low temperature of 160 ℃.展开更多
Due to coexisting of H2, CO2 and H2O with CO in hydrogen-rich gas produced from methanol reforming, the selective CO oxidation is companied with the side reactions of H2 oxidation, as well as CO or CO2 methanation and...Due to coexisting of H2, CO2 and H2O with CO in hydrogen-rich gas produced from methanol reforming, the selective CO oxidation is companied with the side reactions of H2 oxidation, as well as CO or CO2 methanation and reverse water-gas shift reaction（RWGS）. This paper investigated the effects of the above side reactions on the selective CO oxidation over a 0.5% Pt/Al2O3 monolithic catalyst. The results showed that after 50% H2 is added into the reactants, the highest CO conversion is only 98.3% at 180℃ when the feed molar ratio of O2 to CO is 1, and the corresponding outlet CO concentration is 180×10 -6 . Adding 50% H2 into the reactants accelerate CO oxidation at low temperatures; the catalyst active reaction temperature window shifts down about 40℃ . CO produced from RWGS is 80×10 -6 at 200℃ indicating that the effect of RWGS on selective CO oxidation becomes obvious at temperatures higher than 200℃. On the other side, CO or CO2 methanation does not take place even at 300℃ under current conditions and has little effects on the selective CO oxidation.展开更多
基金Funded by the Natural Science Foundation of Hubei Province,China(No.2011CDA070)Research Fund for the Doctoral Program of Hubei University for Nationalities(No.MY2014B013)
文摘Crystalline metal-organic framework cobalt （II） benzenetricarboxylate C%（BTC）2·12H2O （MOF-Co） has been prepared using solvothermal method. The reaction of cobalt （II） nitrate and 1,3,5-benzenetriearboxylic （BTC） acid in a mixed solution of N,N-dimethylformarnide （DMF）/C2H5OH/H2O （1：1：1, v/v） at low temperature for short reaction times produced this crystalline compound. Compared with traditional hydrothermal method, a mixed solution method for the synthesis of crystalline metal complex was found to be highly efficient. After water molecules were removed from this metal complex, its exposed nodes served as active sites. When this MOF-Co was employed in the oxidation of CO, it showed good catalytic properties causing 100% conversion of CO to CO2 at low temperature of 160 ℃.
基金The project was supported by the National Key Basic Research Program of China(973)(2013CB933104)National Natural Science Foundation of China(21525313,20973161,21373192)+1 种基金MOE Fundamental Research Funds for the Central Universities,China(WK2060030017)MPG-CAS Partner Group Program and Collaborative Innovation Center of Suzhou Nano Science and Technology~~
文摘Due to coexisting of H2, CO2 and H2O with CO in hydrogen-rich gas produced from methanol reforming, the selective CO oxidation is companied with the side reactions of H2 oxidation, as well as CO or CO2 methanation and reverse water-gas shift reaction（RWGS）. This paper investigated the effects of the above side reactions on the selective CO oxidation over a 0.5% Pt/Al2O3 monolithic catalyst. The results showed that after 50% H2 is added into the reactants, the highest CO conversion is only 98.3% at 180℃ when the feed molar ratio of O2 to CO is 1, and the corresponding outlet CO concentration is 180×10 -6 . Adding 50% H2 into the reactants accelerate CO oxidation at low temperatures; the catalyst active reaction temperature window shifts down about 40℃ . CO produced from RWGS is 80×10 -6 at 200℃ indicating that the effect of RWGS on selective CO oxidation becomes obvious at temperatures higher than 200℃. On the other side, CO or CO2 methanation does not take place even at 300℃ under current conditions and has little effects on the selective CO oxidation.
