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介孔分子筛负载SO3H基区域选择性催化硝化邻二甲苯
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奚立民(1957-),男,教授,从事有机催化的研究与教学。e-mail: xilm@tzvtc.com

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浙江省科技计划重大项目(2006C11026)


Nitration of o-Xylene by Regioselective Catalysis with SO3H Group Supported on Esoporous Molecular Sieve
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    采用直接合成法制备出由MCM-41介孔分子筛负载SO3H的催化剂,探讨了催化剂表面的酸中心组成,并考察了不同工艺条件下邻二甲苯区域选择性硝化的催化性能。用硫酸钡重量法、透射电镜(TEM)和N2吸附-脱附表征了MCM-41-SO3H的结构。结果表明,MCM-41-SO3H保持了MCM-41的介孔结构,BET表面积高达560 m2·g-1,表面含有质子酸中心; 得到最宜的工艺条件: 催化剂焙烧温度290 ℃,反应温度65 ℃,m邻二甲苯/m催化剂=27,n硝酸/n邻二甲苯=2.5,反应时间3 h,邻二甲苯转化率为92.4%,3,4-二甲基硝基苯的含量达到83.3%。

    Abstract:

    Catalyst of SO3H group supported on mesoporous MCM-41 was prepared by direct-synthesis method. The composition of acid sites on catalyst surface was discussed, and the catalytic performance of o-xylene regioselective nitration was investigated under various technology conditions. The structure of MCM-41-SO3H was characterized by the gravimetry of BaSO4, transmission electronic microscopy(TEM) and N2 adsorption/desorption. Results show that mesoporous structure of MCM-41 is maintained in the MCM-41-SO3H system, there are Bronsted acid sites on catalyst surface with high BET surface area of 560 m2·g-1. The optimum conditions of technology are as follows: calcination temperature of catalyst is 290 ℃, the reaction is 65 ℃ for 3 h with mo-xylene/mcatalyst being 27 and nnitric acid/no-xylene being 2.5 to get o-xylene conversion of 92.4%, mass percentage of 3,4-dimethylnitrobenzene reaching up to 83.3%.

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奚立民.介孔分子筛负载SO3H基区域选择性催化硝化邻二甲苯[J].含能材料, 2008, 16(3):333-336.
XI Li-min. Nitration of o-Xylene by Regioselective Catalysis with SO3H Group Supported on Esoporous Molecular Sieve[J]. Chinese Journal of Energetic Materials, 2008, 16(3):333-336.

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  • 收稿日期: 2007-12-17
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  • 在线发布日期: 2011-05-06
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