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作 者:张跃[1] 崔志强[1] 严生虎[1] 刘建武[1] 沈介发[1]
机构地区:[1]常州大学精细化工研究所,江苏常州213164
出 处:《天然气化工—C1化学与化工》2011年第1期16-19,共4页Natural Gas Chemical Industry
摘 要:在微型固定床反应器中对Zn-ZrO2/SiO2催化甲醇直接非氧化脱氢制备无水甲醛进行了研究。实验中考察了催化剂组成、反应温度及质量空速对脱氢反应的影响。结果显示,在进料气中φ(CH3OH)为35%,反应温度为800K,质量空速为35mL/(g.s)的优化反应条件下,甲醇的转化率达到100%,甲醛的选择性为63%。结合催化剂的活性评价及X射线光电子能谱、电子扫描电镜、热重等技术显示,采用均匀沉淀法制备的Zn-ZrO2/SiO2催化剂,活性组分能均匀分散在载体上,且对甲醇的非氧化脱氢具有高效的催化作用。助剂ZnO的引入可以有效抑制反应过程中催化剂的烧结,极大程度的增强催化剂的稳定性。Methanol direct dehydrogenation to anhydrous formaldehyde using Zn-ZrO2/SiO2 as catalyst was studied in a fixed-bed microreactor.Effects of catalyst composition,reaction temperature,space velocity on the dehydrogenation reaction were investigated.It was found that under the optimized conditions of feed gas methanol volume fraction of about 35%,reaction temperature of 800K,space velocity of about 35ml.g-1.s-1,the conversion rate of methanol reached 100%,and the selectivity to formaldehyde was 63%.The results of XRD,SEM,TG measurements and catalyst evaluation showed that the catalysts prepared by uniform co-precipitation had active components uniformly dispersing on them,which exhibited excellent performances for methanol direct dehydrogenation.Doping ZnO promoter into the ZrO2/SiO2 catalyst could effectively inhibit its sintering during reaction and thus greatly enhance the stability of the catalyst.
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