Isobaric Vapor-Liquid Equilibrium Data at 101.3 kPa for the Binary System Acetamide plus N,N-Dimethyl Formamide and the Quaternary System sec-Butyl Alcohol plus sec-Butyl Acetate plus Acetamide plus N,N-Dimethyl Formamide

被引:0
|
作者
Zhang, Xuemei [1 ]
Lyu, Qiuhua [1 ]
Hao, Xin [2 ]
Jian, Chungui [3 ]
机构
[1] Tianjin Univ, Sch Chem Engn & Technol, Tianjin 300350, Peoples R China
[2] Wanhua Chem Grope Co Ltd, Yantai 264000, Shandong, Peoples R China
[3] Peiyang Chem Equipment Co Ltd, Tianjin, Peoples R China
关键词
DIMETHYL-SULFOXIDE; TERNARY-SYSTEM; THERMODYNAMIC CONSISTENCY; IONIC LIQUID; DEHYDROGENATION; EXPRESSION; 2-BUTANOL; CATALYSTS; ENERGY;
D O I
10.1021/acs.jced.2c00280
中图分类号
O414.1 [热力学];
学科分类号
摘要
Isobaric vapor-liquid equilibrium (VLE) data for the binary system acetamide + N,N-dimethyl formamide (DMF) and the quaternary system sec-butyl alcohol (SBA) + sec-butyl acetate (SBAC) + acetamide + DMF were measured at 101.3 kPa. The VLE data were verified to be thermodynamically consistent by the Fredenslund test and Wisniak's L-W test. In addition, the binary interaction parameters of UNIQUAC, Wilson, and NRTL models for DMF-acetamide were obtained by correlating the binary VLE data. UNIQUAC, Wilson, NRTL, and COSMO-UNIFAC models were employed to predict the VLE data, and the results were compared with the experimental results. Compared with the result without entrainers, the effect of mixed solvent acetamide + DMF (the mass ratio of acetamide to DMF is 1:1) can enhance the relative volatility of SBAC to SBA obviously.
引用
收藏
页码:2426 / 2434
页数:9
相关论文
共 50 条
  • [41] Experimental Isobaric Vapor-Liquid Equilibrium for Binary Systems of Ethyl Methyl Carbonate plus Methanol, plus Ethanol, plus Dimethyl Carbonate, or plus Diethyl Carbonate at 101.3 kPa
    Zhang, Xuemei
    Zuo, Jian
    Jian, Chungui
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2010, 55 (11): : 4896 - 4902
  • [42] Liquid-Liquid Equilibria for the Ternary System n-Butyl Acetate plus Pyrocatechol plus Water at Different Temperatures at 101.3 kPa
    Wang, Baohe
    Rong, Mingjie
    Wang, Pinpin
    Chen, Shuang
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2016, 61 (09): : 3184 - 3189
  • [44] Isobaric vapor-liquid equilibria for water plus acetic acid plus (N-methyl pyrrolidone or N-methyl acetamide)
    Chang, WX
    Wan, H
    Guan, GF
    Yao, HQ
    FLUID PHASE EQUILIBRIA, 2006, 242 (02) : 204 - 209
  • [45] Isobaric Vapor-Liquid Equilibrium for the Binary Systems (Diethylamine plus Ethanol), (Ethanol plus N,N-Diethylethanolamine), and (Diethylamine plus N,N-Diethylethanolamine) at p = (80.0 and 40.0) kPa
    Yang, Changsheng
    Zhang, Ping
    Qin, Zhenli
    Feng, Yang
    Zeng, Hao
    Sun, Feizhong
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2014, 59 (03): : 750 - 756
  • [46] Isobaric Vapor-Liquid Equilibrium for the Binary Systems of sec Butyl Acetate plus Methyl Ethyl Ketone, 2-Methoxyethanol, or 1,2-Dimethoxyethane at 101.3 kPa
    Jiang, Zhankun
    Ma, Shoutao
    Wang, Lei
    Sun, Guoxin
    Cui, Yu
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2016, 61 (01): : 336 - 341
  • [47] ISOTHERMAL VAPOR-LIQUID-EQUILIBRIA OF WATER PLUS N,N-DIMETHYL-FORMAMIDE SYSTEMS
    IULIAN, O
    HAMPLEA, L
    SANDULESCU, I
    REVUE ROUMAINE DE CHIMIE, 1995, 40 (01) : 7 - 11
  • [48] Vapor-liquid equilibria for water plus acetic acid plus (N,N-dimethylformamide or dimethyl sulfoxide) at 13.33 kPa
    Peng, Yong
    Ping, Lijuan
    Lu, Shengli
    Mao, Jianwei
    FLUID PHASE EQUILIBRIA, 2009, 275 (01) : 27 - 32
  • [49] Phase equilibria of ternary systems of carbon dioxide plus ethanol, dimethyl sulfoxide, or N,N-dimethyl formamide plus water at elevated pressures including near critical regions
    Chiu, Hung-Yu
    Tiwikrama, Ardila Hayu
    Gou, You-Ren
    Lin, Ho-mu
    Lee, Ming-Jer
    FLUID PHASE EQUILIBRIA, 2016, 429 : 84 - 92
  • [50] Isobaric Vapor-Liquid Equilibrium Data for the Acetone plus Hexamethyl Disiloxane plus Ethyl Acetate Ternary System at 101.3 kPa: Determination and Correlation
    Li, Chunli
    Gong, Siqi
    Li, Hao
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2018, 63 (09): : 3621 - 3627