个人简历
1978年出生，教授，天津大学博士，海河学者
研究领域
化工过程建模与优化；反应精馏；精密精馏
近期论文
1. Wang H, Wu C, Bu X, et al. A benign preparation of sec-butanol via transesterification from sec-butyl acetate using the acidic Imidazolium ionic liquids as catalysts[J]. Chemical Engineering Journal, 2014,246(12):366-372.2. Wang H X, Bu X W, Yang J B, et al. Isobaric (vapor+liquid) equilibrium data for the binary system methanol+2-butyl alcohol and the quaternary system methyl acetate+methanol+2-butyl alcohol+2-butyl acetate at P =101.33kPa[J]. Journal of Chemical Thermodynamics, 2014,74(74):85-90.3. Wang H, Bu X, Huang Z, et al. Synthesis of Methacrylic Anhydride by Batch Reactive Distillation: Reaction Kinetics and Process[J]. Industrial & Engineering Chemistry Research, 2014,53(44):17317-17324.4. Wang H, Xiao J, Shen Y, et al. Reply to “Comments on ‘Experimental Measurements of Vapor–Liquid Equilibrium Data for the Binary System of Methanol + 2-Butyl Acetate, 2-Butyl Alcohol + 2-Butyl Acetate and Methyl Acetate + 2-Butyl Acetate at 101.33 kPa’”[J]. Journal of Chemical & Engineering Data, 2013,58(12):3563-3566.5. Wang H, Li L, Ye C. Isobaric vapor–liquid equilibria of the binary system acetone + acetone oxime methyl ether at 101.3 kPa[J]. Fluid Phase Equilibria, 2013,342(342):42-46.6. Jia D, Wang H, Cheng L, et al. Liquid–Liquid Equilibrium for the Ternary System Acetone Oxime Methyl Ether–Acetone–Water[J]. Journal of Chemical & Engineering Data, 2013,58(6):1602-1605.7. Xiao L, Wang Q, Wang H, et al. Isobaric vapor-liquid equilibrium data for the binary system methyl;acetate plus isopropyl acetate and the quaternary system methyl acetate;plus methanol plus isopropanol plus isopropyl acetate at 101.3 kPa[J]. Fluid Phase Equilibria, 2013,344:79-83.8. Ye C, Wang H, Huang G, et al. Adsorption and desorption of DMF on macroporous resin NKA-II in the fixed bed[J]. Chemical Engineering Research & Design, 2013,91(12):2713-2720.9. 王红星, 李海勇, 张希, 等. 碳酸二甲酯与乙醇酯交换反应动力学[J]. 高校化学工程学报, 2014(3):580-585.10. 王红星, 陈锦溢, 从娟. 催化剂包传质效率的研究[J]. 计算机与应用化学, 2012,29(5):532-536.11. 王红星, 李海勇, 刘雪艳. 酯交换合成碳酸二乙酯反应精馏工艺的模拟[J]. 计算机与应用化学, 2013(5).12. 王红星, 张希, 黄智贤, 等. 萃取处理PTA精制废水工艺模拟计算与设计[J]. 福州大学学报, 2014,42(2):317-320.13. Wang H X, Ji Z Y, Li X G, et al. Study on mass transfer process of bubble-free aeration by using membranes[J]. Chemical Engineering, 2008.14. Wang H X, Wang Y X. Mathematical Simulation of Flow Field of PEMFC[J]. Journal of Tianjin University, 2007.15. Hongxing W, Li X U, Yuxin W. Two-phase flow across-the-channel model of PEMFC (Ⅰ)Model development[J]. Journal of Chemical Industry/s&/sengineering:china, 2007,58(7):1691-1698.16. Hongxing W, Li X U, Yuxin W. Two-phase flow across-the-channel model of PEMFC (Ⅱ) Cell performance affected by channel design[J]. Journal of Chemical Industry & Engineering, 2007,58(7):1699-1705.17. Cao P Z, Wang H X, Wang Y X. Design of flow channels for proton exchange membrane fuel cells[J]. Chinese Journal of Power Sources, 2007,31(4):341-343.18. Wang H X, Wang Y X. Estimation Method for Nonuniform Degree of Fluid Distribution in Fuel Cell Stacks[J]. Journal of Tianjin University, 2007,40(3):371-376.19. Wang H X, Li X U, Wang Y X. A along-the-channel model for cathode channels for H_2/air proton exchange membrane fuel cells[J]. Chinese Journal of Power Sources, 2006,30(7):582-587.20. Wang H, Wang Y. Model for design of cathode channels for H2/O2 proton exchange membrane fuel cells[J]. Journal of Chemical Industry & Engineering, 2006,57(1):97-103.
