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机构地区:[1]清华大学化学工程系,北京市绿色反应工程与工艺重点实验室,北京100084
出 处:《化工学报》2009年第8期1981-1987,共7页CIESC Journal
基 金:中石油基础研究基金项目
摘 要:采用负载型Rh/MgO/γ-Al2O3催化剂研究了毫秒级甲烷蒸汽重整过程,在水碳比为1和3的条件下,详细考察了反应温度、空速和催化剂Rh含量对反应转化率和选择性的影响。研究结果表明,Rh/MgO/γ-Al2O3催化剂在毫秒级操作条件下具有良好的催化性能,使用5%(质量分数)Rh催化剂,在水碳比3、反应温度1150K、空速641.11 L·(gcat)-1·h-1时,CH4转化率约90%,CO2选择性约20%,毫秒级接触时间反应行为即可接近热力学平衡。高温有利于毫秒级甲烷蒸汽重整过程。Steam reforming of methane (SRM) on Rh/MgO/γ-Al2O3 catalyst with contact time of milliseconds for producing hydrogen was studied. The effects of reactor temperature, space velocity and rhodium loading were investigated in detail at the H2O/CH4 molar ratio of 1 or 3. The results showed that Rh/MgO/γ-Al2O3 catalyst was extremely active and stable during the process of methane steam reforming. Under the conditions of rhodium loading of 5% (mass), H2O/CH4 molar ratio of 3, reaction temperature at 1150 K and space velocity at 641.11 L · (g cat) ^-1 · h^-1, methane conversion could reach 90% and the selectivity to carbon dioxide was about 20%. The reaction performance approached nearly thermodynamic equilibrium within milliseconds contact time. A high reaction temperature benefited the progress of the reaction.
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