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Cr2O3气相催化1,1,2-三氯乙烷脱HCl性能
引用本文:董朝霞,宋通洋,鲁继青,谢冠群,罗孟飞. Cr2O3气相催化1,1,2-三氯乙烷脱HCl性能[J]. 应用化学, 2019, 36(5): 515-523. DOI: 10.11944/j.issn.1000-0518.2019.05.180245
作者姓名:董朝霞  宋通洋  鲁继青  谢冠群  罗孟飞
作者单位:浙江师范大学物理化学研究所,先进催化材料教育部重点实验室 浙江 金华 321004
基金项目:浙江省自然科学基金(LY16B070001)资助项目
摘    要:采用沉淀法制备了不同焙烧温度的Cr2O3催化剂,用于1,1,2-三氯乙烷(TCE)气相脱氯化氢制备二氯乙烯的反应。 采用X射线衍射(XRD)、氢气程序升温还原(H2-TPR)、氨气程序升温脱附(NH3-TPD)、X射线光电子能谱(XPS)表征手段,研究了Cr2O3催化剂气相催化裂解TCE脱氯化氢反应及其反应机理。 结果表明,Cr2O3催化剂上TCE气相脱氯化氢反应的转化率随着催化剂焙烧温度的升高逐渐降低,然而顺-1,2-二氯乙烯(cis-DCE)的选择性先增大后减小。 400 ℃焙烧的Cr2O3催化剂催化性能最好,TCE转化率为70.8%,顺-1,2-二氯乙烯的选择性为90.0%。 然而,催化剂的单位面积反应速率随着焙烧温度升高先提高后下降,400 ℃焙烧催化剂的单位面积反应速率为0.801×10-2 μmol/(s·m2)。 催化剂的单位面积反应速率和顺-1,2-二氯乙烯(cis-DCE)的选择性与催化剂表面Cr2O3物种具有很好的对应关系,表明催化剂表面Cr2O3物种有利于脱氯化氢反应。 以酸中心为活性中心计算得到的转换频率(TOF)变化趋势与单位面积反应速率相一致,400 ℃焙烧的催化剂的TOF为2.82×10-5 s-1,表明Cr2O3催化剂Cr物种合适的平均价态(~3.20)有利于脱氯化氢反应。

关 键 词:Cr2O3催化剂  1  1  2-三氯乙烷  脱氯化氢  顺-1  2-二氯乙烯  表面Cr2O3物种  
收稿时间:2018-07-17

Gas Phase Dehydrochlorination of 1,1,2-Trichloroethane over Cr2O3 Catalysts
DONG Zhaoxia,SONG Tongyang,LU Jiqing,XIE Guanqun,LUO Mengfei. Gas Phase Dehydrochlorination of 1,1,2-Trichloroethane over Cr2O3 Catalysts[J]. Chinese Journal of Applied Chemistry, 2019, 36(5): 515-523. DOI: 10.11944/j.issn.1000-0518.2019.05.180245
Authors:DONG Zhaoxia  SONG Tongyang  LU Jiqing  XIE Guanqun  LUO Mengfei
Affiliation:Key Laboratory of the Ministry of Education for Advanced Catalysis Materials,Institute of Physical Chemistry,Zhejiang Normal University,Jinhua,Zhejiang 321004,China
Abstract:A series of Cr2O3 catalysts was prepared by a precipitation method and tested for the gas phase dehydrochlorination of 1,1,2-trichloroethane(TCE) to synthesize cis-1,2-dichloroethylene(cis-DCE). X-ray diffraction(XRD), hydrogen temperature-programmed reduction(H2-TPR), ammonia temperature-programmed desorption(NH3-TPD) and X-ray photoelectron spectroscopy(XPS) were used to study the dehydrochlorination of TCE on Cr2O3 catalyst and its reaction mechanism. It is found that the conversion ratio of TCE on the catalysts decreases with the increase of the calcination temperature, while the selectivity to cis-DCE first increases and then decreases. The best performance is obtained on the catalyst calcined at 400 ℃, with a TCE conversion ratio of 70.8% and a cis-DCE selectivity of 90.0%. In addition, the areal specific reaction rate also first increases and then decreases with the increase of the calcination temperature, with the highest value being obtained on the catalysts calcined at 400 ℃(0.801×10-2 μmol/(s·m2). The catalytic behaviors of the catalysts are well related to their surface Cr2O3 species. Turnover frequencies(TOFs) calculated based on the surface acidity and the highest value being obtained on the catalysts calcined at 400 ℃(2.82×10-5 s-1) show that the oxidation states of the surface Cr species are important for the reaction and the Cr species with an average valence of 3.2 are appropriate for the reaction.
Keywords:Cr2O3 catalysts  1  1  2-trichloroethane  dehydrochlorination  cis-1  2-dichloroethylene  surface Cr2O3 species
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