Modeling of physical and chemical equilibrium for the direct synthesis of dimethyl carbonate at high pressure conditions

被引:22
作者
Santos, B. A. V. [1 ]
Silva, V. M. T. M. [1 ]
Loureiro, J. M. [1 ]
Barbosa, D. [2 ]
Rodrigues, A. E. [1 ]
机构
[1] Univ Porto, Fac Engn, Dept Chem Engn, Lab Separat & React Engn, P-4200465 Oporto, Portugal
[2] Univ Porto, Fac Engn, Dept Chem Engn, Lab Proc Environm & Energy Engn, P-4200465 Oporto, Portugal
关键词
Equations of state; Supercritical CO2; Dimethyl carbonate; Vapour-liquid equilibrium; VAPOR-LIQUID-EQUILIBRIUM; ETHYLENE CARBONATE; ORGANIC CARBONATES; PHASE-EQUILIBRIA; CUBIC EQUATIONS; MIXING RULE; METHANOL; DIOXIDE; TRANSESTERIFICATION; CO2;
D O I
10.1016/j.fluid.2012.08.022
中图分类号
O414.1 [热力学];
学科分类号
摘要
The physical and chemical equilibrium for direct synthesis of dimethyl carbonate is studied using the Soave-Redlich-Kwong equation of state coupled with five different mixing rules: one fluid van der Walls (1PVDW), modified first order Huron-Vidal (mHV1), modified second order Huron-Vidal (mHV2), linear combination of Vidal and Michelsen (LCVM), and Wong-Sandler (WS). The models parameters were adjusted from experimental vapour-liquid equilibrium data, from the literature, for the relevant binary systems. The mHV2 mixing rule showed to be the best model to predict phase equilibrium for this system. Then, the DMC equilibrium yield was modeled based on the SRK/mHV2 model. The Gibbs free energy of formation, for DMC, was adjusted from our experimental reaction equilibrium data in order to predict the equilibrium constant. (c) 2012 Elsevier B.V. All rights reserved.
引用
收藏
页码:41 / 51
页数:11
相关论文
共 66 条
[1]  
Anastas P.T., 1998, Green chemistry: theory and practice
[2]   Kinetic studies of carbonylation of methanol to dimethyl carbonate over Cu+X zeolite catalyst [J].
Anderson, SA ;
Root, TW .
JOURNAL OF CATALYSIS, 2003, 217 (02) :396-405
[3]   COMPUTATIONAL METHODS FOR HIGH-PRESSURE PHASE-EQUILIBRIA AND OTHER FLUID-PHASE PROPERTIES USING A PARTITION-FUNCTION .2. MIXTURES [J].
ANDERSON, TF ;
PRAUSNITZ, JM .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1980, 19 (01) :9-14
[4]  
Aouissi A, 2010, TRANSIT METAL CHEM, P1
[5]   Gas-Phase Synthesis of Dimethyl Carbonate from Methanol and Carbon Dioxide Over Co1.5PW12O40 Keggin-Type Heteropolyanion [J].
Aouissi, Ahmed ;
Al-Othman, Zeid Abdullah ;
Al-Amro, Amro .
INTERNATIONAL JOURNAL OF MOLECULAR SCIENCES, 2010, 11 (04) :1343-1351
[6]   CHEMISTRY OF PHOSGENE [J].
BABAD, H ;
ZEILER, AG .
CHEMICAL REVIEWS, 1973, 73 (01) :75-91
[7]  
Ballivet-Tkatchenko D., 2010, C R CHIM
[8]   Direct synthesis of dimethyl carbonate with supercritical carbon dioxide: Characterization of a key organotin oxide intermediate [J].
Ballivet-Tkatchenko, Danielle ;
Chambrey, Stephane ;
Keiski, Riitta ;
Ligabue, Rosane ;
Plasseraud, Laurent ;
Richard, Philippe ;
Turunen, Helka .
CATALYSIS TODAY, 2006, 115 (1-4) :80-87
[9]   High-pressure (vapor plus liquid) equilibrium in binary mixtures of (carbon dioxide plus water or acetic acid) at temperatures from 313 to 353 K [J].
Bamberger, A ;
Sieder, G ;
Maurer, G .
JOURNAL OF SUPERCRITICAL FLUIDS, 2000, 17 (02) :97-110
[10]  
Bhattacharya A.K., 1988, US Patent, Patent No. [4,785,130,1988, 4785130]