Application of a group contribution equation of state for the thermodynamic modeling of the binary systems CO2-1-butyl-3-methyl imidazolium nitrate and CO2-1-hydroxy-1-propyl-3-methyl imidazolium nitrate

被引:30
作者
Bermejo, M. D. [1 ,3 ]
Martin, A. [1 ,3 ]
Foco, G. [4 ]
Cocero, M. J. [3 ]
Bottini, S. B. [4 ]
Peters, C. J. [1 ,2 ]
机构
[1] Delft Univ Technol, Fac Mech Maritime & Mat Engn, Dept Proc & Energy, Lab Proc Equipment, NL-2628 CA Delft, Netherlands
[2] Petr Inst, Dept Chem Engn, Abu Dhabi, U Arab Emirates
[3] Univ Valladolid, High Pressure Proc Grp, Dept Chem Engn & Environm Technol, E-47011 Valladolid, Spain
[4] UNS CONICET, PLAPIQUI, RA-8000 Bahia Blanca, Buenos Aires, Argentina
关键词
Ionic liquids; Carbon dioxide; Phase behavior; Group contribution equation of state; PRESSURE PHASE-BEHAVIOR; LIQUID 1-N-BUTYL-3-METHYLIMIDAZOLIUM HEXAFLUOROPHOSPHATE; SUPERCRITICAL CARBON-DIOXIDE; MOLECULAR-DYNAMICS SIMULATION; IONIC LIQUID/ORGANIC MIXTURES; ACTIVITY-COEFFICIENTS; GAS SOLUBILITY; TPC-PSAFT; FORCE-FIELD; GC-EOS;
D O I
10.1016/j.supflu.2009.05.004
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070305 [高分子化学与物理];
摘要
It is known that the properties of ionic liquids (ILs) can be tuned by appropriate selection of cations and anions. Even when an infinite number of ionic liquids can be generated, only a limited number of families of anions and cations are used. The group contribution equation of state (GC-EoS) is a promising method for calculating the phase behavior of the ILs. If the parameters of the characteristic functional group of a family are fitted by using data of a reduced number of ILs of the family, the phase behavior of all the ILs of the same family can be predicted using exclusively the data of the pure component. Previously, the parameters of the IL families with an imidazolium-based cation and the anions PF6, BF4 and Tf2N have been fitted to experimental data. In this work, the GC-EoS has been used to calculate the CO2-IL phase behavior of two ionic liquids with an imidazolium-based cation and a nitrate anion: 1-butyl-3-methyl imidazolium nitrate (BMImNO(3)) and 1-hydroxy-1-propyl-3-methyl imidazolium nitrate (HOPMImNO(3))To fit the parameters of the functional group 3-methyl imidazolium nitrate (MImNO(3) experimental activity coefficients at infinite dilution (gamma(infinity)) of the BMImNO(3) with alkanes and alcohols are used together with the experimental data. The average error of the calculated bubble points is 2.6% in pressure for the system CO2-BMImNO(3) and 6.7% for the system CO2-HOPMImNO(3). The activity coefficients at infinite dilution (gamma(infinity)) are predicted with an average deviation of 6.9%. (C) 2009 Published by Elsevier B.V.
引用
收藏
页码:112 / 117
页数:6
相关论文
共 59 条
[1]
Capturing the solubility Behavior of CO2 in ionic liquids by a simple model [J].
Andreu, Jordi S. ;
Vega, Lourdes F. .
JOURNAL OF PHYSICAL CHEMISTRY C, 2007, 111 (43) :16028-16034
[2]
Prediction of binary VLE for imidazolium based ionic liquid systems using COSMO-RS [J].
Banerjee, T ;
Singh, MK ;
Khanna, A .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2006, 45 (09) :3207-3219
[3]
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
[4]
Liquid-Vapor Equilibrium of the Systems Butylmethylimidazolium Nitrate-CO2 and Hydroxypropylmethylimidazolium Nitrate-CO2 at High Pressure: Influence of Water on the Phase Behavior [J].
Bermejo, M. Dolores ;
Montero, Marta ;
Saez, Elisa ;
Florusse, Louw J. ;
Kotlewska, Aleksandra J. ;
Cocero, M. Jose ;
van Rantwijk, Fred ;
Peters, Cor J. .
JOURNAL OF PHYSICAL CHEMISTRY B, 2008, 112 (43) :13532-13541
[5]
Insights into the structure and dynamics of a room-temperature ionic liquid:: Ab initio molecular dynamics simulation studies of 1-n-butyl-3-methylimidazolium hexafluorophosphate ([bmim][PF6]) and the [bmim][PF6]-CO2 mixture [J].
Bhargava, B. L. ;
Balasubramanian, S. .
JOURNAL OF PHYSICAL CHEMISTRY B, 2007, 111 (17) :4477-4487
[6]
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
[7]
Green processing using ionic liquids and CO2 [J].
Blanchard, LA ;
Hancu, D ;
Beckman, EJ ;
Brennecke, JF .
NATURE, 1999, 399 (6731) :28-29
[8]
Bondi A., 1968, PHYS PROPERTIES MOL
[9]
Thermodynamic modeling of the phase behavior of binary systems of ionic liquids and carbon dioxide with the group contribution equation of state [J].
Breure, Bianca ;
Bottini, Susana B. ;
Witkamp, Geert-Jan ;
Peters, Cor J. .
JOURNAL OF PHYSICAL CHEMISTRY B, 2007, 111 (51) :14265-14270
[10]
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