Volume, surface and UNIQUAC interaction parameters for imidazolium based ionic liquids via Polarizable Continuum Model

被引:186
作者
Banerjee, T [1 ]
Singh, MK [1 ]
Sahoo, RK [1 ]
Khanna, A [1 ]
机构
[1] Indian Inst Technol, Dept Chem Engn, Kanpur 208016, Uttar Pradesh, India
关键词
polarizable continuum model; volume and surface parameters; solute cavity; Gaussian; 98; imidazolium based ionic liquids;
D O I
10.1016/j.fluid.2005.05.017
中图分类号
O414.1 [热力学];
学科分类号
摘要
Ionic liquids (ILs) have shown great potential as solvent/media for reactions and separations. However, the physico-chemical characteristics of ILs are scarce and the limitless different combinations of cations and anions further complicate the matter. The ternary tie line data along with the binodal curve gives a fair indication regarding the feasibility of the ILs as solvents. Most of the ternary (with ILs) liquid-liquid equilibrium data available in literature has been correlated through the NRTL model as r and q are not available. The absence of the volume and surface parameters poses a hindrance in calculation of the binary interaction parameters for UNIQUAC and UNIEFAC models. A novel method has been developed for deriving these volume and surface parameters from the Polarizable Continuum Model (PCM). PCM is widely used for studying solvation effects. Here, the solute is represented by a charge distribution in a molecular shaped cavity embedded in an infinite polarizable dielectric medium. GEnerating POLyhedra (GEPOL), which is based on the concept of solvent excluding surface, is used for calculating this cavity. This novel approach for volume and surface parameters has been verified initially for 71 compounds belonging to several homologous series (paraffins, isoparaffins, olefins, naphthenes, aromatics, alkynes, alcohols, ketones, aldehydes, acids, esters and amines) and 24 solvents. The predicted values of r and q for alcohols, ethers and oxygen containing systems showed significant deviations (2.5-20% for r and 5-25% for q) from the literature values. The values of r and q obtained by PCM method have been applied to 17 ternary systems and I quaternary system belonging to these deviant components. The PCM method gives a significantly better fit (average of 60% improvement in rmsd) for all the systems studied. This approach has been used to estimate the structural parameters for 25 dialkylimidazolium based ILs. Subsequently, these values have been used to estimate the UNIQUAC interaction parameters for seven IL based ternary systems, giving a 40% improvement in rmsd over NRTL. (c) 2005 Elsevier B.V. All rights reserved.
引用
收藏
页码:64 / 76
页数:13
相关论文
共 60 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]  
ALBERTO A, 1994, J CHEM ENG DATA, V39, P378
[3]   Liquid-liquid equilibria of the ternary system water plus acetic acid+1-heptanol [J].
Aljimaz, AS ;
Fandary, MSH ;
Alkandary, JK ;
Fahim, MA .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2000, 45 (02) :301-303
[4]   APPLICATION OF UNIQUAC EQUATION TO CALCULATION OF MULTICOMPONENT PHASE-EQUILIBRIA .2. LIQUID-LIQUID EQUILIBRIA [J].
ANDERSON, TF ;
PRAUSNITZ, JM .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1978, 17 (04) :561-567
[5]   Solubilities and thermodynamic properties of gases in the ionic liquid 1-n-butyl-3-methylimidazolium hexafluorophosphate [J].
Anthony, JL ;
Maginn, EJ ;
Brennecke, JF .
JOURNAL OF PHYSICAL CHEMISTRY B, 2002, 106 (29) :7315-7320
[6]   tert-amyl ethyl ether separation from its mixtures with ethanol using the 1-butyl-3-methylimidazolium trifluoromethanesulfonate ionic liquid:: Liquid-liquid equilibrium [J].
Arce, A ;
Rodríguez, O ;
Soto, A .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2004, 43 (26) :8323-8327
[7]   Experimental determination of liquid-liquid equilibrium using ionic liquids:: tert-amyl ethyl ether plus ethanol plus 1-octyl-3-methylimidazolium chloride system at 298.15 K [J].
Arce, A ;
Rodríguez, O ;
Soto, A .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2004, 49 (03) :514-517
[8]   Liquid-liquid equilibrium for tert-amyl ethyl ether plus methanol plus water [J].
Arce, A ;
Martínez-Ageitos, J ;
Rodríguez, O ;
Soto, A .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2001, 46 (03) :557-561
[9]  
*ASP TECHN INC, 1998, ASP PLUS VER 10 0
[10]   Recovery of organic products from ionic liquids using supercritical carbon dioxide [J].
Blanchard, LA ;
Brennecke, JF .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2001, 40 (01) :287-292