Evaluation of optimal activity coefficient models for modeling and simulation of liquid-liquid equilibrium of biodiesel plus glycerol plus alcohol systems

被引:25
作者
do Carmo, Frederico R. [1 ]
Evangelista, Nathan S. [1 ]
de Santiago-Aguiar, Rilvia S. [1 ]
Fernandes, Fabiano A. N. [1 ]
de Sant'Ana, Hosiberto B. [1 ]
机构
[1] Univ Fed Ceara, Dept Engn Quim, Grp Pesquisa Termofluidodinam Aplicada, BR-60455760 Fortaleza, CE, Brazil
关键词
Liquid-liquid equilibrium; Activity coefficient model; Biodiesel-glycerol-alcohol systems; Parameter estimation; PHASE-EQUILIBRIUM; TERNARY MIXTURES; METHYL OLEATE; FATTY-ACIDS; SOYBEAN OIL; OLEIC-ACID; CANOLA OIL; 313.15; K; ETHANOL; PREDICTION;
D O I
10.1016/j.fuel.2014.01.108
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Biodiesel is considered a good alternative for diesel engines, given its characteristics, for being non-toxic and for being a more environmental-friendly fuel. A liquid-liquid equilibrium (LLE), comprising biodiesel + glycerol + alcohol, occurs during the production of biodiesel. The use of reliable thermodynamics models is essential to describe biodiesel + glycerol + alcohol systems as to design and analyze the process and its equipment. In this work, experimental data of 34 different systems (27 for biodiesel + glycerol + alcohol; and 7 for methyl oleate + glycerol + methanol) were used for parameter estimation and to evaluate four of the main activity coefficient models (ASOG, UNIFAC, UNIFAC-LLE and UNIFAC-Dortmund) that could be used with biodiesel systems. Additionally, binary parameters for glycerol/methanol, methanol/methyl oleate and glycerol/methyl oleate have been estimated by NRTL and UNIQUAC models. Root mean square deviations (RMSD) have been used to compare experimental and simulated data. RMSD analysis showed that the UNIFAC-Dortmund model was the model that best represented the biodiesel liquid-liquid equilibrium. Best representation of the system followed the order: UNIFAC-Dortmund > ASOG > UNIFAC-LLE > UNIFAC > UNIQUAC > NRTL. (C) 2014 Elsevier Ltd. All rights reserved.
引用
收藏
页码:57 / 65
页数:9
相关论文
共 38 条
  • [1] STATISTICAL THERMODYNAMICS OF LIQUID-MIXTURES - NEW EXPRESSION FOR EXCESS GIBBS ENERGY OF PARTLY OR COMPLETELY MISCIBLE SYSTEMS
    ABRAMS, DS
    PRAUSNITZ, JM
    [J]. AICHE JOURNAL, 1975, 21 (01) : 116 - 128
  • [2] Phase equilibria in ternary mixtures of methyl oleate, glycerol, and methanol
    Andreatta, Alfonsina E.
    Casas, Lidia M.
    Hegel, Pablo
    Bottini, Susana B.
    Brignole, Esteban A.
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2008, 47 (15) : 5157 - 5164
  • [3] Liquid-liquid equilibrium for systems of canola oil, oleic acid, and short-chain alcohols
    Batista, E
    Monnerat, S
    Kato, K
    Stragevitch, L
    Meirelles, AJA
    [J]. JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1999, 44 (06) : 1360 - 1364
  • [4] Prediction of liquid-liquid equilibrium for systems of vegetable oils, fatty acids, and ethanol
    Batista, E
    Monnerat, S
    Stragevitch, L
    Pina, CG
    Gonçalves, CB
    Meirelles, AJA
    [J]. JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1999, 44 (06) : 1365 - 1369
  • [5] Integrated Process Modeling and Product Design of Biodiesel Manufacturing
    Chang, Ai-Fu
    Liu, Y. A.
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2010, 49 (03) : 1197 - 1213
  • [6] Reverse-Phase Ternary Phase Diagram, Tie Lines, and Plait Point for Commercial Biodiesel-Glycerol-Methanol
    Csernica, Stephen N.
    Hsu, James T.
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2011, 50 (02) : 1012 - 1016
  • [7] Development of a new model for biodiesel viscosity prediction based on the principle of corresponding state
    do Carmo, F. R.
    Sousa, P. M., Jr.
    Santiago-Aguiar, R. S.
    de Sant'Ana, H. B.
    [J]. FUEL, 2012, 92 (01) : 250 - 257
  • [8] Liquid-Liquid Equilibria for Castor Oil Biodiesel plus Glycerol plus Alcohol
    Franca, Bruno B.
    Pinto, Fabio M.
    Pessoa, Fernando Luiz P.
    Uller, Angela Maria C.
    [J]. JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2009, 54 (09) : 2359 - 2364
  • [9] GROUP-CONTRIBUTION ESTIMATION OF ACTIVITY-COEFFICIENTS IN NONIDEAL LIQUID-MIXTURES
    FREDENSLUND, A
    JONES, RL
    PRAUSNITZ, JM
    [J]. AICHE JOURNAL, 1975, 21 (06) : 1086 - 1099
  • [10] Transesterification of soybean frying oil to biodiesel using heterogeneous catalysts
    Georgogianni, K. G.
    Katsoulidis, A. P.
    Pomonis, P. J.
    Kontominas, M. G.
    [J]. FUEL PROCESSING TECHNOLOGY, 2009, 90 (05) : 671 - 676