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机构地区:[1]江苏工业学院化学化工学院,江苏常州213164
出 处:《石油化工》2009年第6期608-612,共5页Petrochemical Technology
基 金:国家重大基础研究前期研究项目(2003CCA03200);江苏省高技术研究项目(BG2006015);江苏省高校重大基础研究项目(06KJA5013)
摘 要:在连续流动固定床反应器上,用HZSM-5分子筛催化苯与碳酸二乙酯(DEC)进行烷基化反应合成乙苯;采用X射线衍射、NH3程序升温脱附和吡啶吸附红外光谱等手段对HZSM-5分子筛进行了表征;考察了HZSM-5分子筛的硅铝比n(SiO2)∶n(Al2O3)、反应温度和原料配比对烷基化反应的影响。实验结果显示,随硅铝比的增加,HZSM-5分子筛的酸量减少,酸强度减弱;硅铝比为200的HZSM-5分子筛的催化活性最高。以硅铝比200的HZSM-5分子筛为催化剂,适宜的烷基化反应条件为:反应温度653K、反应压力0.5MPa、n(苯)∶n(DEC)=4、重时空速1h-1、催化剂用量5mL。在此条件下,苯的转化率为42.5%,乙苯的选择性达到85.5%。Synthesis of ethylbenzene by alkylation of benzene with diethyl carbonate (DEC) was carried out in a continuous flow fixed-bed reactor over HZSM-5 molecular sieves. The molecular sieves in use were of different n( SiO2 ) : n( Al2O3 ) ratios. The HZSM-5 molecular sieves were characterized by means of XRD, NH3-TPD and pyridine-IR. With increasing of n ( SiO2 ) : n ( Al2O3 ) in HZSM-5 molecular sieves, the amount and strength of acidic sites on HZSM-5 molecular sieves decreased, but the conversion of benzene and selectivity to ethylbenzene increased. Maximum conversion of benzene and maximum selectivity to ethylbenzene could be obtained when n (SiO2 ) : n (Al2O3 ) in HZSM-5 molecular sieves was 200. Further increasing of n ( SiO2 ) : n ( Al2O3 ) tended to a lowering of both. Effects of reaction temperature and n (benzene) : n (DEC) in feed on the alkylation were also studied. Under optimal conditions:reaction temperature 653 K, reaction pressure 0.5 MPa, n (benzene) : n(DEC) 4, WHSV 1 h^-1, catalyst dosage 5 mL, conversion of benzene and selectivity to ethylbenzene were 42.5 % and 85.5 %, respectively.
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