Liquid-liquid equilibrium data for systems containing of formic acid, water, and primary normal alcohols at T=298.2 K

被引:16
作者
Gilani, H. Ghanadzadeh [1 ]
Asan, Sh [2 ]
机构
[1] Univ Guilan, Dept Chem Engn, Rasht 41335, Iran
[2] Univ Urmia, Dept Chem, Fac Sci, Orumiyeh, Iran
关键词
Formic acid; Liquid-liquid equilibrium; Tie-line data; NRTL model; UNIQUAC model; CONVENTIONAL SOLVENT SYSTEMS; TERNARY-SYSTEMS; PHASE-EQUILIBRIA; EXTRACTION EQUILIBRIA; CARBOXYLIC-ACIDS; ACETIC-ACIDS; PLUS; MIXTURES; TOLUENE;
D O I
10.1016/j.fluid.2013.06.006
中图分类号
O414.1 [热力学];
学科分类号
摘要
Solubility and tie-line data for the ternary systems of (water + formic acid + aliphatic alcohols) were measured at T=298.2 K and atmospheric pressure. The organic solvents were four primary normal alcohols, i.e. 1-butanol, 1-pentanol, 1-hexanol, and 1-heptanol. The phase diagrams for all these ternary systems are of type-1. The immiscibility region was found to be larger for the ternary system containing 1-heptanol. The experimental LLE data were correlated using the NRTL and the UNIQUAC models, and the binary interaction parameters were calculated. The Othmer-Tobias correlation equation was used to ascertain the quality of the LLE data for each system. Distribution coefficients and separation factors were evaluated over the immiscibility regions. The experimental results indicate the advantage of 1-heptanol as the preferred solvent for the recovery of formic acid from water. (C) 2013 Elsevier B.V. All rights reserved.
引用
收藏
页码:24 / 28
页数:5
相关论文
共 35 条
[1]   STATISTICAL THERMODYNAMICS OF LIQUID-MIXTURES - NEW EXPRESSION FOR EXCESS GIBBS ENERGY OF PARTLY OR COMPLETELY MISCIBLE SYSTEMS [J].
ABRAMS, DS ;
PRAUSNITZ, JM .
AICHE JOURNAL, 1975, 21 (01) :116-128
[2]  
Bartholome E., 1974, ULLMANNS ENCYKLOPADI, V7, P362
[3]   Quaternary phase equilibrium of water-carboxylic acid mixture (formic-propionic acid or acetic-propionic acid)-solvent liquid systems at 298.15 K [J].
Baslioglu, Burcu ;
Cehreli, Suheyla .
FLUID PHASE EQUILIBRIA, 2011, 312 :85-92
[4]   Liquid phase equilibria of (water plus propionic acid plus oleyl alcohol) ternary system at several temperatures [J].
Bilgin, Mehmet ;
Arisoy, Cigdem .
FLUID PHASE EQUILIBRIA, 2006, 250 (1-2) :59-63
[5]   Liquid phase equilibria of (water plus formic acid plus diethyl carbonate or diethyl malonate or diethyl fumarate) ternary systems at 298.15 K and atmospheric pressure [J].
Bilgin, Mehmet ;
Birman, Imge .
FLUID PHASE EQUILIBRIA, 2011, 302 (1-2) :249-253
[6]   Extraction equilibria of formic and acetic acids from aqueous solution by phosphate-containing extractants [J].
Cai, WB ;
Zhu, SL ;
Piao, XL .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2001, 46 (06) :1472-1475
[7]  
Darton R., 1997, DIST ABS 97 3 DAY S, V1
[8]   (Liquid plus liquid) equilibria of (water plus propionic acid+2-ethyl-1-hexanol): Experimental data and correlation [J].
Ghanadzadeh, H. ;
Ghanadzadeh, A. ;
Bahrpaima, Kh. ;
Saadat, S. L. Seyed .
JOURNAL OF CHEMICAL THERMODYNAMICS, 2008, 40 (05) :879-884
[9]   Tie-line data for water-formic acid-1-decanol ternary system at T=298.2, 303.2, 313.2, and 323.2 K [J].
Gilani, H. Ghanadzadeh ;
Azadian, M. .
THERMOCHIMICA ACTA, 2012, 547 :141-145
[10]  
Iloukhani H., 2007, J CHEM THERMODYN, V39, P1231