Separation of azeotrope (allyl alcohol plus water): Isobaric vapour-liquid phase equilibrium measurements and extractive distillation

被引:48
|
作者
Wu, Jingyu [1 ]
Xu, Dongmei [1 ]
Shi, Puyun [1 ]
Gao, Jun [1 ]
Zhang, Lianzheng [1 ]
Ma, Yixin [1 ]
Wang, Yinglong [2 ]
机构
[1] Shandong Univ Sci & Technol, Coll Chem & Environm Engn, Qingdao 266590, Peoples R China
[2] Qingdao Univ Sci & Technol, Coll Chem Engn, Qingdao 266042, Peoples R China
来源
关键词
Allyl alcohol; Azeotrope; Vapour-liquid equilibrium; Extractive distillation; BINARY-SYSTEMS; THERMODYNAMIC CONSISTENCY; 101.33; KPA; EXPRESSION; MIXTURES; BENZENE; ACETATE; ENERGY; XYLENE; ACID;
D O I
10.1016/j.jct.2017.11.009
中图分类号
O414.1 [热力学];
学科分类号
摘要
To separate the azeotrope of (allyl alcohol + water) by extractive distillation, N-methyl-2-pyrrolidone, N-methyl formamide and ethylene glycol were selected as extractive agents, and the isobaric VLE data for the binary systems of (allyl alcohol + N-methyl-2-pyrrolidone), (allyl alcohol + N-methyl formamide) and (allyl alcohol + ethylene glycol) were determined at 101.3 kPa by a modified Rose type recirculating still. The thermodynamic consistency of the experimental data was checked by the Herington, van Ness, infinite dilution, and pure component consistency method. Meanwhile, the experimental data were correlated by the NRTL, UNIQUAC and Wilson activity coefficient models, and the binary interaction parameters of the three models were regressed. All the correlated results by the NRTL, UNIQUAC, and Wilson models agreed well with the experimental data. Furthermore, the extractive distillation processes with the extractive agents were presented to separate the azeotrope of (allyl alcohol + water). (C) 2017 Elsevier Ltd.
引用
收藏
页码:139 / 146
页数:8
相关论文
共 50 条
  • [31] Calculations of the vapour-liquid phase equilibrium for the formaldehyde-water-trioxane system
    Warsaw University of Technology, Faculty of Chemical and Process Engineering, Warynskiego 1, 00-645 Warsaw, Poland
    Chem. Process Eng., 2008, 1 (3-12):
  • [32] Vapour-liquid equilibrium for tripropylene glycol plus aromatic hydrocarbons binary systems: Measurements and modelling
    Fendu, Elena M.
    Nicolae, Marilena
    Oprea, Florin
    FLUID PHASE EQUILIBRIA, 2016, 425 : 188 - 195
  • [33] Calculations of the vapour-liquid phase equilibrium for the formaldehyde-water-trioxane system
    Pohorecki, Ryszard
    Moniuk, Wladyslaw
    Machniewski, Piotr
    CHEMICAL AND PROCESS ENGINEERING-INZYNIERIA CHEMICZNA I PROCESOWA, 2008, 29 (01): : 3 - 12
  • [34] Extractive distillation separation of isopropanol- isopropyl acetate azeotrope: Vapor-liquid equilibrium measurement and process optimization
    Ma, Yixin
    Hu, Zeyu
    Yang, Lin
    Zhang, Lianzheng
    Liu, Shanshan
    Zhang, Zhishan
    Xu, Dongmei
    Gao, Jun
    Wang, Yinglong
    JOURNAL OF CHEMICAL THERMODYNAMICS, 2025, 205
  • [35] Measurement and prediction of isobaric vapour-liquid equilibrium data of the system ethanol plus methanol plus 2-methoxy-2-methylpropane
    Arce, A
    Martinez-Ageitos, J
    Rodil, E
    Soto, A
    FLUID PHASE EQUILIBRIA, 1998, 146 (1-2) : 139 - 153
  • [36] Isobaric vapour-liquid equilibrium for binary system of cyclohexanol plus cyclohexylbenzene at (5, 10, 15, 20 and 25) kPa
    Guo, Chunhao
    Tang, Yang
    Wan, Jinru
    Zuo, Yue
    Wang, Yong
    Wang, Yichang
    Wang, Xunqiu
    JOURNAL OF CHEMICAL THERMODYNAMICS, 2020, 144
  • [37] Vapor-Liquid Equilibrium for Binary Systems of Allyl Alcohol plus Water and Allyl Alcohol plus Benzene at 101.3 kPa
    Li, Jing
    Hua, Chao
    Xiong, Shuai
    Bai, Fang
    Lu, Ping
    Ye, Jiayi
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2017, 62 (10): : 3004 - 3008
  • [38] Separation of azeotrope 2,2,3,3-tetrafluoro-1-propanol and water by extractive distillation using ionic liquids: Vapor-liquid equilibrium measurements and interaction analysis
    Diao, Baotao
    Wang, Zenghui
    Yang, Hui
    Zhang, Lianzheng
    Xu, Dongmei
    Gao, Jun
    Wang, Yinglong
    JOURNAL OF MOLECULAR LIQUIDS, 2019, 292
  • [39] Isobaric vapour-liquid equilibrium of α-terpineol highly diluted in hydroalcoholic mixtures at 101.3 kPa: Experimental measurements and thermodynamic modeling
    Zanghelini, Gabriela
    Athes, Violaine
    Esteban-Decloux, Martine
    Giampaoli, Pierre
    Vitu, Stephane
    JOURNAL OF CHEMICAL THERMODYNAMICS, 2022, 171
  • [40] Isobaric Vapor-Liquid Phase Equilibrium Measurements for Allyl Alcohol with Chloroform, Ethyl Acetate, and Methyl Propionate at 101.3 kPa
    Diao, Baotao
    Wang, Ke
    Xu, Dongmei
    Gao, Jun
    Ma, Zhun
    Zhang, Lianzheng
    Wang, Yinglong
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2019, 64 (02): : 682 - 687