Measurement of VLE (TPx or TPxy data) for hydrogen sulfide plus (dimethylsulfide or ethylmethylsulfide or carbon disulfide) and methane solubilities in (dimethylsulfide or ethylmethylsulfide or methylmercaptan or ethylmercaptan)

被引:9
作者
Guilbot, P.
Fischer, K.
Valtz, A.
Theveneau, P.
Baba-Ahmed, A.
Richon, D.
机构
[1] CNRS FRE 2861, CEP TEP, Mines Paris Tech, F-77305 Fontainebleau, France
[2] Carl von Ossietzky Univ Oldenburg, Lab Themophys Properties GmbH Inst, F-26129 Oldenburg, France
关键词
VLE measurements; H2S; carbonylsulfide; dimethylsulfide; ethylmethylsulfide; ethylmercaptan; methylmercaptan; methane; binary interaction parameters; PSRK equation;
D O I
10.1016/j.fluid.2007.07.013
中图分类号
O414.1 [热力学];
学科分类号
摘要
VLE data (gas solubilities (TPx data) or complete TPxy data) were measured for the following systems: hydrogen sulfide (H2S) + dimethylsulfide (DMS) at 278, 293, 313, and 333 K. H2S + ethylmethyl sulfide (EMS) at 293 and 313 K. H2S + carbon disulfide (CS2) at 273, 298, 323, and 348 K. methane (CH4) + DMS at 253, 273, 293, and 313 K. CH4 +EMS at 248, 273, 293, and 313 K. CH4 + methylmercaptan (MM) at 243, 258, 273, 293, and 298 K. CH4 + ethylmercaptan (EM) at 273, 293, and 313 K. These data were used to establish new binary interaction parameters for the predictive Soave-Redlich-Kwong (PSRK) group contribution of state. The extension of the PSRK parameter matrix allows now to perform reliable phase equilibrium calculations for systems with any hydrocarbons and sulfur compounds. The mean relative deviation of PSRK compared to the experimental data for the bubble point pressures is less than 2% and the mean absolute deviation for the vapor phase composition is 0.03 in terms of mole fraction. (c) 2007 Elsevier B.V. All rights reserved.
引用
收藏
页码:49 / 59
页数:11
相关论文
共 11 条
[1]   Further development, status and results of the PSRK method for the prediction of vapor-liquid equilibria and gas solubilities [J].
Fischer, K ;
Gmehling, J .
FLUID PHASE EQUILIBRIA, 1996, 121 (1-2) :185-206
[2]   Experimental determination of oxygen and nitrogen solubility in organic solvents up to 10 MPa at temperatures between 298 K and 398 K [J].
Fischer, K ;
Wilken, M .
JOURNAL OF CHEMICAL THERMODYNAMICS, 2001, 33 (10) :1285-1308
[3]   Further development of the PSRK model for the prediction of gas solubilities and vapor-liquid-equilibria at low and high pressures II [J].
Gmehling, J ;
Li, JD ;
Fischer, K .
FLUID PHASE EQUILIBRIA, 1997, 141 (1-2) :113-127
[4]   Rapid on-line sampler-injector: a reliable tool for HT-HP sampling and on-line GC analysis [J].
Guilbot, P ;
Valtz, A ;
Legendre, H ;
Richon, D .
ANALUSIS, 2000, 28 (05) :426-431
[5]   Vapor-liquid equilibrium data and critical points for the system H2S+COS.: Extension of the PSRK group contribution equation of state [J].
Guilbot, P ;
Théveneau, P ;
Baba-Ahmed, A ;
Horstmann, S ;
Fischer, K ;
Richon, D .
FLUID PHASE EQUILIBRIA, 2000, 170 (02) :193-202
[6]   PSRK - A GROUP CONTRIBUTION EQUATION OF STATE BASED ON UNIFAC [J].
HOLDERBAUM, T ;
GMEHLING, J .
FLUID PHASE EQUILIBRIA, 1991, 70 (2-3) :251-265
[7]   PSRK group contribution equation of state: revision and extension III [J].
Horstmann, S ;
Fischer, K ;
Gmehling, J .
FLUID PHASE EQUILIBRIA, 2000, 167 (02) :173-186
[8]   NEW APPARATUS TO PERFORM FAST DETERMINATIONS OF MIXTURE VAPOR-LIQUID-EQUILIBRIA UP TO 10-MPA AND 423-K [J].
LAUGIER, S ;
RICHON, D .
REVIEW OF SCIENTIFIC INSTRUMENTS, 1986, 57 (03) :469-472
[9]   A NEW EQUATION OF STATE AND TABLES OF THERMODYNAMIC PROPERTIES FOR METHANE COVERING THE RANGE FROM THE MELTING LINE TO 625-K AT PRESSURES UP TO 1000-MPA [J].
SETZMANN, U ;
WAGNER, W .
JOURNAL OF PHYSICAL AND CHEMICAL REFERENCE DATA, 1991, 20 (06) :1061-1155
[10]  
VALTZ A, 1998, RR162 GAS PROC ASS