Thermodynamic modeling of the phase behavior of binary systems of ionic liquids and carbon dioxide with the group contribution equation of state

被引:71
作者
Breure, Bianca [1 ]
Bottini, Susana B. [2 ]
Witkamp, Geert-Jan [3 ]
Peters, Cor J. [1 ]
机构
[1] Delft Univ Technol, DelftChemTech, Fac Sci Appl, NL-2628 BL Delft, Netherlands
[2] Univ Nacl Sur, CONICET, PLAPIQUI, Bahia Blanca, Argentina
[3] Delft Univ Technol, Fac Mech Maritime & Mat Engn, Lab Proc Equipment, NL-2628 CA Delft, Netherlands
关键词
D O I
10.1021/jp0776098
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
The group contribution equation of state (GC-EOS) was applied to predict the phase behavior of binary systems of ionic liquids of the homologous families 1-alkyl-3-methylimidazolium hexafluorophosphate and tetrafluoroborate with CO2. Pure group parameters for the new ionic liquid functional groups [-mim][PF6] and [-mim][BF4] and interaction parameters between these groups and the paraffin (CH3, CH2) and CO2 groups were estimated. The GC-EOS extended with the new parameters was applied to predict high-pressure phase equilibria in binary mixtures of the ionic liquids [emim][PF6], [bmim][PF6], [hmim][PF6], [bmim][BF4], [hmim][BF4], and [omim][BF4] with CO2. The agreement between experimental and predicted bubble point data for the ionic liquids was excellent for pressures up to 20 MPa, and even for pressures up to about 100 MPa, the agreement was good. The results show the capability of the GC-EOS to describe phase equilibria of systems consisting of ionic liquids.
引用
收藏
页码:14265 / 14270
页数:6
相关论文
共 40 条
[1]   Modeling of activity coefficients of aqueous solutions of quaternary ammonium salts with the electrolyte-NRTL equation [J].
Belvèze, LS ;
Brennecke, JF ;
Stadtherr, MA .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2004, 43 (03) :815-825
[2]   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
[3]   Green processing using ionic liquids and CO2 [J].
Blanchard, LA ;
Hancu, D ;
Beckman, EJ ;
Brennecke, JF .
NATURE, 1999, 399 (6731) :28-29
[4]  
Bondi A, 1968, PHYS PROPERTIES MOL
[5]   FRIEDEL CRAFTS REACTIONS IN AMBIENT-TEMPERATURE MOLTEN-SALTS [J].
BOON, JA ;
LEVISKY, JA ;
PFLUG, JL ;
WILKES, JS .
JOURNAL OF ORGANIC CHEMISTRY, 1986, 51 (04) :480-483
[6]   Ionic phosphine ligands with cobaltocenium backbone: Novel ligands for the highly selective, biphasic, rhodium-catalyzed hydroformylation of 1-octene in ionic liquids [J].
Brasse, CC ;
Englert, U ;
Salzer, A ;
Waffenschmidt, H ;
Wasserscheid, P .
ORGANOMETALLICS, 2000, 19 (19) :3818-3823
[7]   Why is CO2 so soluble in imidazolium-based ionic liquids? [J].
Cadena, C ;
Anthony, JL ;
Shah, JK ;
Morrow, TI ;
Brennecke, JF ;
Maginn, EJ .
JOURNAL OF THE AMERICAN CHEMICAL SOCIETY, 2004, 126 (16) :5300-5308
[8]   CATALYTIC DIMERIZATION OF PROPENE BY NICKEL-PHOSPHINE COMPLEXES IN 1-BUTYL-3-METHYLIMIDAZOLIUM CHLORIDE/ALETXCL3-X (X=0,1) IONIC LIQUIDS [J].
CHAUVIN, Y ;
EINLOFT, S ;
OLIVIER, H .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1995, 34 (04) :1149-1155
[9]   High-pressure phase Behavior of systems with ionic liquids: Part IV. Binary system carbon dioxide+1-hexyl-3-methylimidazolium tetrafluoroborate [J].
Costantini, M ;
Toussaint, VA ;
Shariati, A ;
Peters, CJ ;
Kikic, I .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2005, 50 (01) :52-55
[10]  
Daubert T., 1996, PHYS THERMODYNAMIC P