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以硅酸钠为硅源、硫酸铝为铝源、CTAB为模板剂,采用水热法合成了骨架负载型固体酸Al-MCM-41介孔分子筛催化剂,并通过X射线衍射(XRD)、扫描电子显微镜(SEM)和红外(IR)方法对其进行了表征,同时研究了该催化剂在二芳基乙烷合成反应中的催化性能. 考察了各种反应因素的影响,确定其最佳合成条件为:原料m(苯乙烯)∶m(二甲苯)=1∶7.5,催化剂用量为1%(总投料质量分数),反应时间为3 h,反应温度为140 ℃,产率可达87.1%,比传统催化剂浓硫酸提高了17%. 研究结果表明,该催化剂是替代液体酸合成二芳基乙烷的理想固体酸催化剂.

Al-MCM-41 mesoporous sieves were synthesized by using Na2SiO3 as silica source, Al2(SO4)3 as aluminum source, and cetyltrimethylammonium bromide(CTAB) as template under hydrothermal condition. The Al-MCM-41 mesoporous sieves were characterized by X-ray diffraction(XRD), scanning electron microscopy(SEM) and infrared spectroscopy(IR). The synthesis of diphenylethane over Al-MCM-41 catalyst and its catalytic performance were investigated. The results show that the optimal conditions were the mass percent of catalyst was 1% of the feed stock;molar ratio of xylene to styrene was 7.5∶1;reaction temperature was 140 ℃ and reaction time 3 h. The yield of diphenylethane under such conditions was about 87.1%, which was 17% higher than the yield when traditional sulfuric acid was used as catalyst. The results show that Al-MCM-41 is a promising solid acid catalyst for the synthesis of diphenylethylane instead of liquid acid.

参考文献

[1] LIN Chen(林晨),LI Rui-Lian(李瑞莲).Fujian Chem Technol(福建化工)[J],2004,1:19
[2] WANG Chun-Hua(王春华),JI Chun-Nuan(纪春暖),QU Rong-Jun(曲荣君),SUN Chang-Mei(孙昌梅),WANG Jing(王静).Chem Res Appl(化学研究与应用)[J],2005,17(1):78
[3] Kwak B S,Kim T J.Catal Lett[J],1999,59:55
[4] WANG Chun-Hua(王春华),QU Rong-Jun(曲荣君),JI Chun-Nuan(纪春暖),SUN Chang-Mei(孙昌梅),CHEN Xi-Lei(陈希磊).Chem World(化学世界)[J],2004,5:258
[5] TANG Qing-Hua(唐清华).Chem Eng(化学工程师)[J],2005,4:11
[6] REN Tao(任涛),HOU Xin(侯鑫),WANG Fu-Li(王富丽),XIAO Bing(肖兵),WANG Xue-Li(王学丽),LIAN Pi-Yong(连丕勇).Ind Catal(工业催化)[J],2006,14(11):37
[7] CHI Cai-Xia(迟彩霞),LI Xiao-Xu(李晓旭),WEI Chang-Ping(魏长平).J Changchun Univ Sci Technol(长春理工大学学报)[J],2006,29(3):85
[8] ZHANG Ming-Jin(张铭金),YAO Rui-Ping(姚瑞平),ZHAO Hui-Zhong(赵惠忠),CHEN Lei(陈雷),DENG Feng(邓风).J Wuhan Univ Sci Technol(武汉科技大学学报)[J],2005,28(2):154
[9] LI Zhong-Yan(李忠燕),TU Yong-Shan(涂永善),YANG Chao-He(杨朝合).Ind Catal(工业催化)[J],2005,13(2):12
[10] Xie C X,Liu F S,Yu S T,Xie F F,Li L,Zhang S F,Yang J Z.Catal Commun[J],2008,9:1 132
[11] Beck J S,Vartuli J C,Roth W J,Leonowicz M E,Kresge C T,Schmitt K D,Chu C T-W,Olson D H,Sheppard E W,McCullen S B,Higgins J B,Schlenkert J L.J Am Chem Soc[J],1992,114(27):10 834
[12] XIE Fang-Fei(谢芳菲),LIU Fu-Sheng(刘福胜),XIE Cong-Xia(解从霞),YU Shi-Tao(于世涛),GE Xiao-Ping(葛晓萍).J Qingdao Univ Sci Technol(青岛科技大学学报)[J],2007,28(1):34
[13] Palani A,Pandurangan A.J Mole Catal A:Chem[J],2006,245:101
[14] Rabindran Jermy B,Pandurangan A.Catal Commun[J],2008,9:577
[15] Rabindran Jermy B,Pandurangan A.Appl Catal A:General[J],2005,295:185
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