Vapor-liquid equilibria of monoacylglicerol plus monoacylglicerol or alcohol or fatty acid at subatmospheric pressures

被引:8
|
作者
Damaceno, Daniela S. [1 ]
Ceriani, Roberta [1 ]
机构
[1] Univ Estadual Campinas, Fac Chem Engn, Av Albert Einstein 500, BR-13083852 Campinas, SP, Brazil
基金
巴西圣保罗研究基金会;
关键词
Monoacylglycerols; Oils/fats; Biodiesel; Boiling points; Vapor-liquid equilibrium; DSC technique; DIFFERENTIAL SCANNING CALORIMETRY; ACYL MIGRATION KINETICS; METHYL BUTANOATE; BINARY-SYSTEMS; DSC TECHNIQUE; MIXTURES; OIL; EXPRESSION; BIODIESEL; LUBRICITY;
D O I
10.1016/j.fluid.2017.08.013
中图分类号
O414.1 [热力学];
学科分类号
摘要
Partial acylglycerols are relevant minor compounds in the oil/fat industry. They represent important role to the food industry, as surface-active agents and emulsifiers. Also, they are present in the biodiesel production and its separation steps. Therefore, knowledge of their thermophysical properties are critical to product and process design. Considering that, this study aims at determining by the DSC technique novel boiling point data for two monoacylglycerols, namely, monononanoin and monolaurin at subatmospheric pressures, and for four binary fatty mixtures at selected pressures (TPx data), i.e. lauric acid + monocaprylin (3.42 kPa), monononanoin + monolaurin (2.06 kPa), monononanoin + hexadecanol (2.02 kPa), and monolaurin + octadecanol (2.05 kPa). As expected, the system with two monoacylglycerols (monononanoin + monolaurin) showed an ideal behavior. On the other hand, the other systems presented non-ideal behavior. Experimental data were successfully regressed by the Wilson, the NRTL and the UNIQUAC models. Predictive capacity of the UNIFAC method and its different versions was tested, and results indicated that improvements concerning lipid systems are still necessary. These improvements must be based on diverse and qualified experimental data. (C) 2017 Elsevier B.V. All rights reserved.
引用
收藏
页码:135 / 142
页数:8
相关论文
共 50 条
  • [21] Vapor-liquid equilibria and densities of CO2 with four unsaturated fatty acid esters at elevated pressures
    Chang, CMJ
    Lee, MS
    Li, BC
    Chen, PY
    FLUID PHASE EQUILIBRIA, 2005, 233 (01) : 56 - 65
  • [22] Isobaric vapor-liquid equilibria for water plus acetic acid plus sodium acetate
    Vercher, E
    Vázquez, MI
    Martínez-Andreu, A
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2003, 48 (02): : 217 - 220
  • [23] Isobaric vapor-liquid equilibria for water plus acetic acid plus lithium acetate
    Vercher, E
    Vázquez, MI
    Martínez-Andreu, A
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2001, 46 (06): : 1584 - 1588
  • [24] Isobaric vapor-liquid equilibria for water plus acetic acid plus potassium acetate
    Vercher, E
    Orchillés, AV
    Vázquez, MI
    Martínez-Andreu, AA
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2004, 49 (03): : 566 - 569
  • [25] VAPOR-LIQUID EQUILIBRIA - BINARY SYSTEM NITROMETHANE-NITROETHANE AT SUBATMOSPHERIC PRESSURE
    CANTONI, A
    FELDMAN, J
    INDUSTRIAL AND ENGINEERING CHEMISTRY, 1953, 45 (11): : 2580 - 2584
  • [26] VAPOR-LIQUID EQUILIBRIUM OF NAPHTHALENE - N-TETRADECANE SYSTEM AT SUBATMOSPHERIC PRESSURES
    HAYNES, S
    VANWINKLE, M
    INDUSTRIAL AND ENGINEERING CHEMISTRY, 1954, 46 (02): : 334 - 338
  • [27] Vapor-liquid equilibria of ammonia plus ionic liquid mixtures
    Yokozeki, A.
    Shiflett, Mark B.
    APPLIED ENERGY, 2007, 84 (12) : 1258 - 1273
  • [28] Reevaluation of vapor-liquid equilibria for butadiene plus styrene
    Lu, BCY
    Ni, LW
    Taylor, M
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1996, 41 (02): : 287 - 291
  • [29] Vapor-liquid equilibria of water plus monoethanolamine system
    Park, Sung Jin
    Shin, Hun Yong
    Min, Byoung-Moo
    Cho, Ara
    Lee, Jeon-Seop
    KOREAN JOURNAL OF CHEMICAL ENGINEERING, 2009, 26 (01) : 189 - 192
  • [30] Vapor-liquid equilibria for the ternary system of carbon dioxide plus ethanol plus ethyl acetate at elevated pressures
    Cheng, CH
    Chen, YP
    FLUID PHASE EQUILIBRIA, 2006, 242 (02) : 169 - 175