Phase equilibrium measurements of (methane plus benzene) and (methane plus methylbenzene) at temperatures from (188 to 348) K and pressures to 13 MPa

被引:19
作者
Hughes, Thomas J. [1 ]
Kandil, Mohamed E. [1 ]
Graham, Brendan F. [1 ]
Marsh, Kenneth N. [1 ]
Huang, Stanley H. [2 ]
May, Eric F. [1 ]
机构
[1] Univ Western Australia, Ctr Energy, Sch Mech & Chem Engn, Crawley, WA 6009, Australia
[2] Chevron Energy Technol Co, Houston, TX 77002 USA
基金
澳大利亚研究理事会;
关键词
Methane; Benzene; Methylbenzene; Toluene; (Vapor plus liquid) equilibrium; (Liquid plus liquid) equilibrium; VAPOR-LIQUID-EQUILIBRIA; BINARY-MIXTURES; TOLUENE SYSTEM; SOLUBILITY; GAS; BEHAVIOR; METHANE+BENZENE; HEXANE; POINT;
D O I
10.1016/j.jct.2014.12.031
中图分类号
O414.1 [热力学];
学科分类号
摘要
New isothermal pTxy data are reported for (methane + benzene) and (methane + methylbenzene (toluene)) at pressures up to 13 MPa over the temperature range (188 to 313) K using a custom-built (vapor + liquid) equilibrium (VLE) apparatus. The aim of this work was to investigate literature data inconsistencies and to extend the measurements to lower temperatures. For (methane (1) + benzene (2)), measurements were made along six isotherms from (233 to 348) K at pressures to 9.6 MPa. At temperatures below 279 K there was evidence of a solid phase, and thus only vapor phase samples were analyzed at these temperatures. For the (methane (1) + methylbenzene (3)) system, measurements were made along seven isotherms from T = (188 to 313) K at pressures up to 13 MPa. Along the 198 K isotherm, a significant change in the data's p, x slope was observed indicating (liquid + liquid) equilibria at higher pressures. The data were compared with literature data and with calculations made using the Peng-Robinson (PR) equation of state (EOS). For both binary systems our data agree with much of the literature data that also deviate from the EOS in a similar manner. However, the data of Elbishlawi and Spencer (1951) for both binary systems, which appear to have received an equal weighting to other data in the EOS development, are inconsistent with the results of our measurements and data from other literature sources. (C) 2015 Elsevier Ltd. All rights reserved.
引用
收藏
页码:141 / 147
页数:7
相关论文
共 26 条
[1]   IMPROVED DUMAS METHOD FOR MOLECULAR WEIGHT DETERMINATION [J].
ANDERSON, HH ;
SHUBIN, LD .
ANALYTICAL CHEMISTRY, 1957, 29 (05) :852-854
[2]  
[Anonymous], 2014, MULT VERS 4 4
[3]  
[Anonymous], 2014, US GUID MOD PHYS PRO
[4]   VAPOR-LIQUID EQUILIBRIA OF METHANE-TOLUENE SYSTEM AT LOW TEMPERATURES AND HIGH PRESSURES [J].
CHANG, HL ;
KOBAYASHI, R .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1967, 12 (04) :517-+
[5]   SECOND CROSS VIRIAL COEFFICIENTS OF BENZENE-GAS MIXTURES FROM HIGH PRESSURE SOLUBILITY MEASUREMENTS A COMPARISON WITH GAS CHROMATOGRAPHIC VALUES [J].
COAN, CR ;
KING, AD .
JOURNAL OF CHROMATOGRAPHY, 1969, 44 (3-4) :429-&
[6]   SOLUBILITY OF METHANE IN BENZENE, NAPHTHALENE, PHENANTHRENE, AND PYRENE AT TEMPERATURES FROM 323 TO 433-K AND PRESSURES TO 11.3 MPA [J].
DARWISH, NA ;
GASEM, KAM ;
ROBINSON, RL .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1994, 39 (04) :781-784
[7]   RESPONSE FACTORS FOR GAS CHROMATOGRAPHIC ANALYSES [J].
DIETZ, WA .
JOURNAL OF GAS CHROMATOGRAPHY, 1967, 5 (02) :68-&
[8]   EQUILIBRIUM RELATIONS OF 2 METHANE-AROMATIC BINARY SYSTEMS AT 150-DEGREES-F [J].
ELBISHLAWI, M ;
SPENCER, JR .
INDUSTRIAL AND ENGINEERING CHEMISTRY, 1951, 43 (08) :1811-1815
[9]   Simulating the capture of CO2 from natural gas: New data and improved models for methane plus carbon dioxide plus methanol [J].
Hughes, Thomas J. ;
Kandil, Mohamed E. ;
Graham, Brendan F. ;
May, Eric F. .
INTERNATIONAL JOURNAL OF GREENHOUSE GAS CONTROL, 2014, 31 :121-127
[10]   DEW-POINT LOCI FOR METHANE-TOLUENE SYSTEM [J].
HWANG, SC ;
KOBAYASHI, R .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1977, 22 (04) :409-410