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机构地区:[1]东华理工大学化学生物与材料科学学院,江西抚州344000
出 处:《化学反应工程与工艺》2007年第2期136-140,182,共6页Chemical Reaction Engineering and Technology
基 金:江西省自然科学基金资助项目(0520002);抚州市科技攻关计划项目(2004727)
摘 要:采用浸渍法制备γ-Al_2O_3负载Cu-Zn催化剂并用Co改性.考察了Cu-Zn负载量、Co用量、反应温度和质量空速对催化剂性能的影响.对催化剂进行100h的稳定性评价实验,并采用X射线衍射仪(XRD)对催化剂进行表征.实验结果表明.当Cu,Zn,Al和Co的摩尔比为1.00:2.00:3.00:0.51时.Cu-Zn/γ-Al_2O_3(Co)的催化性能和稳定性比较好.在413K,氢气流速为0.5mL/s,糠醛空速为2h^(-1)条件下,糠醇的选择性达100%,糠醛转化率达94.6%,比使用单纯Cu-Zn/γ-Al_2O_3催化剂的转化率提高11%。催化剂中Cu晶相是催化活性中心.Co的加入抑制了Cu的氧化.提高了催化剂的活性和稳定性.Cu-Zn/γ-Al2O3 catalysts with Cu and Zn supported on γ-A12O3 were prepared by impregnation method and were modified by adding Co (the modified catalyst was called Cu-Zn/γ-A12O3 (Co)). Effects of amount of Cu, Zn cand Co, reaction temperature and space velocity on the performance of Cu-Zn/γ-A12O3 (Co) were investigated in a fixed-bed and 100 h stability tests of the catalyst were carried out. The experimental results showed that the optimal molar ratio of Cu, Zn, Al to Co in the Cu-Zn/γ-A12O3 (Co) was 1.00:2.00:3.00:0.51. Under the reaction conditions that reaction temperature was 413 K, rate of flow of H2 was 0.5 mL/s and space velocity of furfural was 2 h^-1 , conversion of furfural and selectivity of furfuryl alcohol were 94.6% and 100% respectively. The structure of the catalysts was characterized by X-ray diffraction patterns (XRD). Cu crystal in Cu-Zn/modified γ-A12O3 was the catalytic activity centre of Cu-Zn/γ-A12O3 catalyst and Co added could suppress oxidation of Cu and improve the activity and stability of the Cu-Zn/γ-A12O3 (Co) catalyst.
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