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Studies On Co3O4-CeO2 And Composite Oxide Catalysts For CO Preferential Oxidation

Posted on:2017-02-08Degree:MasterType:Thesis
Country:ChinaCandidate:X L LvFull Text:PDF
GTID:2271330503469148Subject:Chemical processes
Abstract/Summary:PDF Full Text Request
As a new type of green energy, Fuel Cells have the advantages of fuel diversity,energy efficiency, environmental friendliness, which have been extensively studied in recent years. The proton exchange membrane fuel cell(PEMFC) shows its bright application prospect. In addition to the general advantages of fuel cells, the PEMFC also has the advantages of low temperature, long life, fast start,etc. Hydrogen, as the fuel of PEMFC, usually contains about 1% of CO, a trace amount of CO can lead to fuel cells electrode poisoning.CO preferential oxidation(PROX) can effectively reduce CO content to ppm level. As non-noble metal catalyst, the catalytic performance of the transition metal oxide catalysts can be compared with Pt series and other noble metal catalysts.The Co3O4-CeO2 and its composite oxide catalysts were prepared by the co-precipitation.The samples prepared were characterized and analyzed by TEM,HRTEM,EDX, XRD, BET, TPR. And studied several aspects: Different cobalt cerium of the aCo3O4-bCeO2 and the relationship between the catalytic properties and structures,addition of H2O2, Influence on the catalytic performance of aCo3O4-bCeO2 catalysts doped with Mn and Cu, and the effects of sintering temperature. A series of data were obtained through the study.The study found that when Co/Ce ratio is 8:1,calcination temperature is 350℃,the8Co3O4-1CeO2 catalyst has the largest specific surface area and the lowest reduction temperature than other catalysts and also showed the best catalytic performance, CO conversion rate can reach 100% at 155℃, the selectivity of catalyst was 100% at the time of CO fully converted. The addition of H2O2 did not improve the catalytic performance,the CO complete conversion temperature is reduced to 135 ℃ of the 8Co3O4-1CeO2 catalyst without H2O2. The particle size of the catalyst was significantly decreased and the surface dispersion was improved after the addition of manganese and copper,also the interaction between Co-Ce was enhanced and the reduction temperature was decreased.The CO complete conversion temperature is 95℃ and 115℃ of 8Co3O4-1CeO2-2MnO2 and 8Co3O4-1CeO2-1CuO.Without H2O2 or adding too little and too much additives will not effectively improve the catalytic activity of cobalt based catalysts. The CO complete conversion temperature is 135℃ and 175℃ of 8Co3O4-1CeO2-2Mn O2 and8Co3O4-1CeO2-1CuO when the calcination temperature is 500℃. The rise of calcinationtemperature increased the sintering of catalyst, which lead to a decrease in the activity of the catalyst than the calcination temperature of 350 ℃.
Keywords/Search Tags:Rich hydrogen gas, CO preferential oxidation, Co3O4-CeO2, Co3O4-CeO2-MOx
PDF Full Text Request
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