Accurate modeling of supercritical CO2 for sustainable processes: Water + CO2 and CO2 + fatty acid esters mixtures

被引:20
作者
Llovell, F. [1 ]
Vega, L. F. [1 ,2 ]
机构
[1] MATGAS Res Ctr, Barcelona 08193, Spain
[2] Carburos Met Air Prod Grp, Barcelona 08009, Spain
关键词
Modeling supercritical fluids; Crossover soft-SAFT; Phase equilibrium; Critical line; Carbon dioxide; Water; Fatty acid esters; Sustainable processes; DIRECTIONAL ATTRACTIVE FORCES; EQUATION-OF-STATE; VAPOR-LIQUID-EQUILIBRIUM; FATTY-ACID METHYL; PHASE-EQUILIBRIA; CARBON-DIOXIDE; THERMODYNAMIC PROPERTIES; RENORMALIZATION-GROUP; BINARY-MIXTURES; INTERFACIAL PROPERTIES;
D O I
10.1016/j.supflu.2014.09.040
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
Supercritical fluid technology has allowed significant improvements in several industrial processes, and there are still many opportunities for further applications in new emergent areas. This contribution provides some perspectives on drivers and opportunities for new or advanced applications of supercritical fluids, including the search for sustainable processes and healthy products. It also addresses some of the needs, such as using refined modeling tools with a specific treatment taking into account the long range fluctuations in the density (or composition for the case of mixtures) as one approaches the critical point to accurately design the process in this region. New results are presented on the application of the crossover soft-SAFT equation of state to two motivating systems involving supercritical CO2, the CO2-water mixture and the solubility of supercritical CO2 in fatty acid esters. Both systems are challenging from a modeling perspective as they are highly non-ideal. Crossover soft-SAFT gives very accurate results, compared to available experimental systems, for the CO2-water mixtures. The equation is also able to predict the critical line in quantitative agreement with experimental data with one constant binary parameter, being a step forward in modeling the behavior of this mixture. The equation also gives excellent results when modeling the solubility of supercritical CO2 in fatty acid esters, with two binary parameters, independent of the temperature and composition, in this case. (C) 2014 Elsevier B.V. All rights reserved.
引用
收藏
页码:86 / 95
页数:10
相关论文
共 64 条
[1]   Modeling the solubility of light reservoir components, HCFCs and HFCs in water using the CPA and sPC-SAFF equations of state [J].
Abolala, Mostafa ;
Varaminian, Farshad .
JOURNAL OF MOLECULAR LIQUIDS, 2013, 187 :359-367
[2]   Modeling the vapor-liquid equilibrium and association of nitrogen dioxide/dinitrogen tetroxide and its mixtures with carbon dioxide [J].
Belkadi, A. ;
Llovell, F. ;
Gerbaud, V. ;
Vega, L. F. .
FLUID PHASE EQUILIBRIA, 2008, 266 (1-2) :154-163
[3]  
Bias F.J., 1998, IND ENG CHEM RES, V37, P660, DOI DOI 10.1021/IE970449+
[4]  
Blas FJ, 1997, MOL PHYS, V92, P135, DOI 10.1080/00268979709482082
[5]   Critical behavior and partial miscibility phenomena in binary mixtures of hydrocarbons by the statistical associating fluid theory [J].
Blas, FJ ;
Vega, LF .
JOURNAL OF CHEMICAL PHYSICS, 1998, 109 (17) :7405-7413
[6]  
Brandalize M.V., 2014, CHEM ENG RES DESIGN
[7]   THE SOLUBILITY OF CARBON-DIOXIDE IN WATER AT LOW-PRESSURE [J].
CARROLL, JJ ;
SLUPSKY, JD ;
MATHER, AE .
JOURNAL OF PHYSICAL AND CHEMICAL REFERENCE DATA, 1991, 20 (06) :1201-1209
[8]   SAFT - EQUATION-OF-STATE SOLUTION MODEL FOR ASSOCIATING FLUIDS [J].
CHAPMAN, WG ;
GUBBINS, KE ;
JACKSON, G ;
RADOSZ, M .
FLUID PHASE EQUILIBRIA, 1989, 52 :31-38
[9]   NEW REFERENCE EQUATION OF STATE FOR ASSOCIATING LIQUIDS [J].
CHAPMAN, WG ;
GUBBINS, KE ;
JACKSON, G ;
RADOSZ, M .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1990, 29 (08) :1709-1721
[10]   Encapsulation and co-precipitation processes with supercritical fluids: Fundamentals and applications [J].
Cocero, Maria Jose ;
Martin, Angel ;
Mattea, Facundo ;
Varona, Salima .
JOURNAL OF SUPERCRITICAL FLUIDS, 2009, 47 (03) :546-555