SCHOOL OF CHEMICAL ENGINEERING

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副教授

崔现宝

现任职称/职务:副教授
通讯地址:天津大学化工学院化工研究所
电子邮箱:cxb@tju.edu.cn
办公电话:27404493

学术成就:

部分学术论文:

[1] Huan,Liu, Xianbao Cui,Ying Zhang,Tianyang Feng,Zhen Yang. Isobaric vapor–liquid equilibrium ofethanenitrile + water + 1,2-ethanediol + 1-ethyl-3-methylimidazoliumchloride. Fluid Phase Equilib. 2014, 378, 13-20.

[2] Yanmei Peng, Xianbao Cui*, Ying Zhang, Tianyang Feng, Zheng Tian and Lexing Xue. Kinetic Study of Transesterification of methyl acetate with ethanol catalyzed by 4-(3-Methyl-1-imidazolio)-1-butanesulfonic acid triflate. Applied Catalysis A: General,2013, 466: 131-136.

[3] Jialin Cai, Shensheng Zhen, Dengpan Gao, Xianbao Cui. Phase Equilibrium (VLE, LLE, and VLLE) Data of the Ternary System:Ionic Liquid [OMIM][PF6] + Butan-1-ol + Butyl Acetate. J. Chem. Eng. Data 2014, 59(7), 2171–2176.

[4] Yanmei Peng, Xianbao Cui*, Ying Zhang, Tianyang Feng, Zheng Tian and Lexing Xue. Kinetics of Transesterification of Methyl Acetate and Ethanol Catalyzed by Ionic Liquid. Int. J. Chem. Kinet.,2014, 46:116–125.

[5]  Lexing Xue, Xianbao Cui,* Ying Zhang, Tianyang Feng, Zheng Tian, and Yanmei Peng. Solid−Liquid   Equilibria of 1‑Ethyl-3-methylimidazolium Hexafluorophosphate + Polyols. J. Chem. Eng. Data 2013, 58(9), 2389-2394.

[6]  Zheng Tian, Xianbao Cui∗, Jialin Cai, Ying Zhang, Tianyang Feng, Yanmei Peng, Lexing Xue. Isobaric VLE data for the system of butan-1-ol + butyl ethanoate + 1-butyl-3-methylimidazolium bis[(trifluoromethyl) sulfonyl]imide, Fluid Phase Equilib., 2013, 352:75-79.

[7]  Rui Li, Xianbao Cui, Ying Zhang, Tianyang Feng and Jialin Cai. Vapor−Liquid Equilibrium and Liquid−Liquid Equilibrium of Ethyl Acetate + Ethanol + 1-Ethyl-3-methylimidazolium Acetate. J. Chem. Eng. Data 2012, 57(3), 911–917.

[8] Xianbao Cui,Jialin Cai,Ying Zhang, Rui Li and Tianyang Feng. Kinetics of Transesterification of Methyl Acetate and n-Butanol Catalyzed by Ionic Liquid. Ind. & Eng.Chem. Res., 2011,50(20):11521-11527.

[9]  Cai Jialin,Cui Xianbao, Yang Zhicai. Simulation for Transesterification of Methyl Acetate and n-Butanol in a Reactive and Extractive Distillation column Using Ionic Liquids as Entrainer and Catalyst. Chinese J. Chem. Eng., 2011,19(5):754-762

[10] Jialin Cai, Xianbao Cui, Ying Zhang, Rui Li and Tianyang Feng. Vapor Liquid Equilibrium and Liquid Liquid Equilibrium of Methyl Acetate + Methanol + 1-Ethyl-3-methylimidazoliumMethyl Acetate. J. Chem. Eng. Data 2011, 56(2), 282–287.

[11] Jialin Cai, Xianbao Cui, Ying Zhang, Rui Li and Tianyang Feng. Isobaric Vapor-Liquid Equilibrium for Methanol + Methyl Acetate+1-Octyl-3-methylimidazolium Hexafluorophosphate at 101.3 kPa. J. Chem. Eng. Data, 2011, 56(6), 2884–2888.

[12] Xianbao Cui,Xiaokai Zhang, Ying Zhang and Tianyang Feng. Batch Distillation in a Batch Stripper with a Side Withdrawal for Purification of Heat-Unstable Compounds. Ind. &Eng.Chem. Res.,2010,49(14):6521-6529. 

[13] Xianbao Cui, Ying Zhang,Tianyang Feng and Zhicai Yang. Batch Distillation in a Column with a Side Withdrawal for Separation of a Ternary Mixture with a Decomposing Reaction, Ind. & Eng. Chem. Res.,2009,48(10):5111-5116.

[14] Cui Xianbao, Zhai Yarui, Yang Zhicai, Feng Tianyang, Zhang Ying. Solvent selection for extractive distillation by the universal quasichemical functional group activity coefficient(UNIFAC) group contribution method, Chinese J. Chem. Eng., 2004, 12(6):862-868

[15] Xianbao Cui, Zhicai Yang, Huaiqi Shao and Hongmei Qu. Batch Distillation in a Column with a Cold Middle Vessel for Heat-sensitive Compounds, Ind. & Eng. Chem. Res., 2001, 40(3):879-884