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SO_4^(2-)/ZrO_2-SBA-15催化剂合成条件研究 被引量:2

Study on synthesis conditions of SO_4^(2-)/ZrO_2-SBA-15
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摘要 以介孔分子筛SBA-15为载体,利用溶胶-凝胶法,在SBA-15的合成过程中引入活性组分SO42-/ZrO2,得到了含有SO42-/ZrO2的SBA-15介孔固体酸催化剂SO42-/ZrO2-SBA-15。以乙酸正丁酯的合成为探针反应,考察了SO42-/ZrO2的合成条件及负载型催化剂SO24-/ZrO2-SBA-15合成条件对催化剂催化活性的影响。确定催化剂的合成条件为:m(模板剂)∶m(去离子水)∶m[盐酸(质量分数为36%)]∶m(正硅酸乙酯)∶m(八水氧氯化锆)=4.0∶98.0∶25.1∶8.48∶5.6;搅拌温度为40℃;加入硅源,搅拌20 h后,加入八水氧氯化锆;焙烧温度为650℃;硫酸溶液的浓度为3 mol/L。负载型催化剂制备过程中,滴加氨水后最佳的pH为9~10,在介孔分子筛合成过程中引入超强酸所得的催化剂活性最高。 Sol-gel method was used in experiment and SO2-4/ZrO2 was introduced during synthesis process of mesoporous molecular sieve SBA-15.SO2-4/ZrO2-SBA-15 mesoporous solid acid catalyst was synthesized with SBA-15 as supporter and with SO2-4/ZrO2 as active constituent.With the synthesis of n-butyl acetate as probe reaction,influences of synthesis conditions for SO2-4/ZrO2 and supported SO2-4/ZrO2-SBA-15 catalyst on catalytic activity were investigated. Synthesis conditions of catalyst were confirmed as follows: m(template) : m(deionized water) : m(HCl,mass fraction of 36% ) : m ( tetraethyl orthosilicate ) : m ( ZrOCl2·8H2O) = 4. 0: 98.0:25.1: 8.48:5.6 ; stirring temperature was 40 ℃ ; added silica source at first, then added ZrOCl2· 8H2O after stirring for 20 h;calcination temperature was 650℃ ;and concentration of sulfuric acid was 3 mol/L. In synthesis process of supported catalyst the optimum pH value should be at 9 - 10 after adding ammonia and the catalyst that introducing supper acid in systhesis process of mesoporous molecular sieve had the best catalytic activity.
出处 《无机盐工业》 CAS 北大核心 2009年第11期22-23,共2页 Inorganic Chemicals Industry
关键词 固体超强酸 SO42-/ZrO2 SBA-15 介孔分子筛 solid supper acid SO2-4/ZrO2 SBA-15 mesoporous molecular sieve
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