Solubility of Ethylene Glycol in Supercritical Carbon Dioxide at Pressures up to 19.0 MPa

被引:19
作者
Jiang, Chun-yue [1 ]
Sun, Zhi-juan [1 ]
Pan, Qin-min [2 ]
Pi, Jian-biao [1 ]
机构
[1] Zhejiang Univ Technol, Coll Chem Engn & Mat Sci, Zhejiang Prov Key Lab Biofuel, Hangzhou 310014, Zhejiang, Peoples R China
[2] Soochow Univ, Dept Polymer Sci & Engn, Suzhou 215123, Jiangsu, Peoples R China
基金
美国国家科学基金会;
关键词
SOLID-STATE POLYMERIZATION; FLUID; POLY(BISPHENOL; LIQUIDS;
D O I
10.1021/je3002249
中图分类号
O414.1 [热力学];
学科分类号
摘要
The experimental equilibrium solubility of ethylene glycol in supercritical carbon dioxide was measured by the static method at temperatures between (313.15 and 353.15) K and pressures up to 19.0 MPa, and the effects of temperature and pressure on the solubility were investigated. The experimental results show that the solubility ranged from ethylene glycol mole fraction of 0.83.10(-2) (353.15 K, 7.0 MPa) to 4.2940(-2) (353.15 K, 19.0 MPa), and the solubility increased with increasing pressure at a constant temperature, but a crossover pressure point (about 16.0 MPa) has been observed in the solubility isotherms at the temperature range from (313.15 to 353.15) K. Moreover, the experimental results were correlated with the Peng-Robinson equation of state using the quadratic mixing rules of the two-fluid van der Waals (vdW2) as well as the modified associative model; both correlations demonstrated satisfactory results, with an average absolute relative deviation (AARD) less than 5 %.
引用
收藏
页码:1794 / 1802
页数:9
相关论文
共 31 条
[1]   Solubilities of 1-nonanol, 1-undecanol, 1-tridecanol, and 1-pentadecanol in supercritical carbon dioxide at T = 323.15 K [J].
Artal, M ;
Pauchon, V ;
Embid, JM ;
Jose, J .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1998, 43 (06) :983-985
[2]   The phase partition of disperse dyes in the dyeing of polyethylene terephthalate with a supercritical CO2/methanol mixture [J].
Banchero, Mauro ;
Ferri, Ada ;
Manna, Luigi .
JOURNAL OF SUPERCRITICAL FLUIDS, 2009, 48 (01) :72-78
[3]   Supercritical and near-critical CO2 in green chemical synthesis and processing [J].
Beckman, EJ .
JOURNAL OF SUPERCRITICAL FLUIDS, 2004, 28 (2-3) :121-191
[4]  
Burke A, 1997, POLYM PREPR, V38, P387
[5]   SOLUBILITY OF SOLIDS AND LIQUIDS IN SUPERCRITICAL GASES [J].
CHRASTIL, J .
JOURNAL OF PHYSICAL CHEMISTRY, 1982, 86 (15) :3016-3021
[6]   Solubility of Ethanamide and 2-Propenamide in Supercritical Carbon Dioxide. Measurements and Correlation [J].
Coelho, Jose P. ;
Bernotaityte, Karolina ;
Miraldes, Marisa A. ;
Mendonca, Andreia F. ;
Stateva, Roumiana P. .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2009, 54 (09) :2546-2549
[7]  
DeSimone J. M., 2002, SCIENCE, V5582, P99
[8]   High-pressure fluid-phase equilibria: Experimental methods and systems investigated (2005-2008) [J].
Fonseca, Jose M. S. ;
Dohrn, Ralf ;
Peper, Stephanie .
FLUID PHASE EQUILIBRIA, 2011, 300 (1-2) :1-69
[9]   SIGNIFICANCE OF THE CROSSOVER PRESSURE IN SOLID SUPERCRITICAL FLUID PHASE-EQUILIBRIA [J].
FOSTER, NR ;
GURDIAL, GS ;
YUN, JSL ;
LIONG, KK ;
TILLY, KD ;
TING, SST ;
SINGH, H ;
LEE, JH .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1991, 30 (08) :1955-1964
[10]   Solubility of methane and carbon dioxide in ethylene glycol at pressures up to 14 MPa and temperatures ranging from (303 to 423) K [J].
Galvao, A. C. ;
Francesconi, A. Z. .
JOURNAL OF CHEMICAL THERMODYNAMICS, 2010, 42 (05) :684-688