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晶化条件对HZSM-5分子筛合成收率和性能的影响 被引量:2

Effects of crystallization conditions on the yields and properties of HZSM-5 molecular sieves
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摘要 考察了SiO2-Al2O3-TPABr-NH3·H20—H2O体系晶化时间、晶化温度和原料用量等对合成HZSM-5性能的影响。当n(SiO2):n(Al2O3)=100、n(TPABr):n(SiO2)=0.1、n(NH3):n(SiO2)=1.5、n(H2O):n(SiO2)=22和晶种添加质量分数为4%时,180℃静态晶化72h,合成收率与相对结晶度分别为10.1%和99.8%,对应理论收率为11.4%,合成收率与理论收率比为0.89。当投料n(SiO2):n(A1203)从50增加到400,合成收率与结晶度分别超过8.9%和82.8%,合成收率与理论收率比为0.76—0.89;样品酸量随着n(SiO:):n(Al2O3)的增加逐渐减小,比表面积为405m2·g-1,合成样品HZSM-5对甲醇制烯烃反应具有良好的酸催化活性。设定反应条件,采用投料n(SiO2):n(AlO3)=250的样品,甲醇转化率、丙烯选择性和C=2~C=4选择性分别为100%、39.27%和62.01%。 In SiO2-Al2O3-TPABr-NH3 · H2O-H2O system, the effects of hydrothermal crystallization time and temperatures, and raw material amounts on the yields and properties of as-synthesized HZSM-5 molecular sieve were investigated. The results showed that the yield and relative erystallinity of as-synthesized samples were 10. 1% and 99. 8%, respectively, under the condition as follows: n ( SiO2 ) : n ( Al2O3 ) = 100, n(TPABr): n(SiO2) =0.1 ,n(NH3) : n(SiO2) = 1.5,n(H2O) : n(SiO2) = 22,seed crystal amount 4%, crystallization temperature 180 ℃ and crystallization time 72 h. The corresponding theoretical yield was 11.4%, and the ratio of the yield of as-synthesized samples to the theoretical yield was 0. 89. As n(SiO2): n(Al2O3) of the raw material enhanced from 50 to 400, the yield and erystallinity of the assynthesized samples remained more than 8.9% and 82.8% ,respectively, and the ratio of as-synthesized sample yield to the theoretical yield was 0.76 - 0.89. The acid amount of the as-synthesized samples decreased gradually with the increase of n ( SiO2 ) : n ( A1203 ) of the raw material. The as-synthesized HZSM-5 molecular sieve with BET surface area of 405 m2 · g-1 exhibited good acid catalytic activity for methanol-to-olefins reaction. At the set condition, methanol conversion, the selectivity to propylene and C2=-C4= light olefins were 100%, 39.27% and 62.01%, respectively, using HZSM-5 molecular sieve catalyst prepared with the raw material of n ( SiO2 ) : n ( A12 03 ) = 250.
出处 《工业催化》 CAS 2015年第7期520-526,共7页 Industrial Catalysis
基金 科技部国家重点基础研究前期研究项目课题(2012CB723106) 国家自然科学基金资助项目(21166020)
关键词 催化剂工程 HZSM-5分子筛 直接合成 晶化条件 catalyst engineering HZSM-5 molecular sieve direct synthesis crystallization conditions
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