The influence of functional end groups on the high-pressure phase equilibria of long chain molecules in supercritical propane

被引:21
作者
Schwarz, C. E. [1 ]
Bonthuys, G. J. K. [1 ]
Knoetze, J. H. [1 ]
Burger, A. J. [1 ]
机构
[1] Univ Stellenbosch, Dept Proc Engn, ZA-7602 Stellenbosch, South Africa
关键词
phase equilibria; propane; supercritical; long chain hydrocarbons; functional end groups;
D O I
10.1016/j.supflu.2008.03.008
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
The influence of various functional end groups on the high-pressure phase equilibria of long chain molecules in supercritical propane was studied by comparing the bubble/dew point pressure of a range of long chain molecules. All long chain molecules had a hydrocarbon segment containing 14 carbon atoms but different functional end groups. Insufficient published data exists for phase equilibria of these types of molecules in supercritical propane, thus prompting experimental work. Bubble/dew point measurements in the temperature range 375-410 K were conducted in a high-pressure phase equilibrium cell to determine the influence of the functional end groups. The alkane (with no functional end group) is the most soluble, followed by the ethyl ester, the methyl ester and the alcohol. The carboxylic acid is the least soluble. The influence of the functional end groups may be explained by considering the structure and polarity of the end groups. It was found that an increase in polarity and/or a decrease in shielding of the polar groups resulted in a decrease in the solubility of the molecules, which in turn resulted in an increase in the bubble/dew point pressures. (C) 2008 Elsevier B.V. All rights reserved.
引用
收藏
页码:233 / 237
页数:5
相关论文
共 19 条
[1]   Measurement of phase equilibria of supercritical ethane and paraffins [J].
du Rand, M ;
Nieuwoudt, I .
JOURNAL OF SUPERCRITICAL FLUIDS, 2001, 21 (03) :181-193
[2]   Effect of acetic acid plus acetonitrile and ethanol plus acetonitrile mixed cosolvents on the solubility of stearic acid in supercritical CO2 [J].
Guan, B ;
Han, BX ;
Yan, HK .
FLUID PHASE EQUILIBRIA, 1998, 149 (1-2) :277-286
[3]   FLUID-PHASE EQUILIBRIUM STUDIES ON TERNARY AND QUATERNARY MIXTURES OF CARBON-DIOXIDE WITH 1-DODECANOL, DODECANOIC ACID, QUINOXALINE AND 1,8-OCTANEDIOL AT 393.2 K AND AT PRESSURES UP TO 40 MPA [J].
KORDIKOWSKI, A ;
SCHNEIDER, GM .
FLUID PHASE EQUILIBRIA, 1995, 105 (01) :129-139
[4]   SOLUBILITY OF 1-HEXADECANOL AND PALMITIC ACID IN SUPERCRITICAL CARBON-DIOXIDE [J].
KRAMER, A ;
THODOS, G .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1988, 33 (03) :230-234
[5]   SOLUBILITY OF 1-OCTADECANOL AND STEARIC-ACID IN SUPERCRITICAL CARBON-DIOXIDE [J].
KRAMER, A ;
THODOS, G .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1989, 34 (02) :184-187
[6]  
Lide DR., 2004, CRC Handbook of Chemistry and Physics, DOI DOI 10.1080/08893110902764125
[7]   SOLUBILITY OF FATTY-ACIDS IN SUPERCRITICAL CARBON-DIOXIDE [J].
MAHESHWARI, P ;
NIKOLOV, ZL ;
WHITE, TM ;
HARTEL, R .
JOURNAL OF THE AMERICAN OIL CHEMISTS SOCIETY, 1992, 69 (11) :1069-1076
[8]   Vapor-liquid equilibria and densities for the system butane plus hexacontane [J].
Nieuwoudt, I .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1996, 41 (05) :1024-1027
[9]  
Perry R., 1997, PERRYS CHEM ENG HDB, V7th
[10]   PHASE-EQUILIBRIA IN BINARY-MIXTURES OF PROPANE AND HEXACONTANE [J].
PETERS, CJ ;
DEROO, JL ;
ARONS, JD .
FLUID PHASE EQUILIBRIA, 1993, 85 :301-312