Solubilities of 10-undecenoic acid and geraniol in supercritical carbon dioxide

被引:37
作者
Lamba, Neha [1 ]
Narayan, Ram C. [1 ]
Modak, Jayant [1 ]
Madras, Giridhar [1 ]
机构
[1] Indian Inst Sci, Dept Chem Engn, Bangalore 560012, Karnataka, India
关键词
Solubilities; Empirical models; Association model; Akaike information criteria; FLUID EXTRACTION; ENZYMATIC-SYNTHESIS; UNDECYLENIC ACID; PHASE-EQUILIBRIA; FATTY-ACIDS; ESTERS; SOLIDS; DERIVATIVES; OILS; FRACTIONATION;
D O I
10.1016/j.supflu.2015.09.026
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 solubilities of 10-undecenoic acid and geraniol in supercritical carbon dioxide were measured at 308, 313,323 and 333K, and at pressures of 10-18 MPa. Solubilities (in mole fraction),ranged from 0.4 x 10(-3) to 17.4 x 10(-3) for 10-undecenoic acid and 2.7 x 10(-3) to 25 x 10(-3) for geraniol, respectively. The AARD was around 11% and 5% for these models for 10-undecenoic acid and geraniol, respectively. The solubilities of both compounds showed retrograde behavior wherein the solubilities decrease with temperature at isobaric conditions. The solubility of geraniol was higher than 10-undecenoic acid at all investigated temperatures and pressures. The data were found to be self consistent based on the Mendez-Santiago model. New models based on association theory using van Laar and Margules activity coefficient models for solute in liquid phase were derived, and used to correlate the solubilities. (C) 2015 Elsevier B.V. All rights reserved.
引用
收藏
页码:384 / 391
页数:8
相关论文
共 50 条
[1]   SUPERCRITICAL FLUID EXTRACTION WITH CARBON-DIOXIDE AND ETHYLENE [J].
ADACHI, Y ;
LU, BCY .
FLUID PHASE EQUILIBRIA, 1983, 14 (OCT) :147-156
[2]   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
[3]   Fractionation of plant extracts by supercritical fluid extraction and direct introduction in capillary gas chromatography using a programmable temperature vaporizer [J].
Blanch, GP ;
Caja, MM ;
del Castillo, MLR ;
Santa-María, G ;
Herraiz, M .
JOURNAL OF CHROMATOGRAPHIC SCIENCE, 1999, 37 (10) :407-410
[4]   AIC model selection and multimodel inference in behavioral ecology: some background, observations, and comparisons [J].
Burnham, Kenneth P. ;
Anderson, David R. ;
Huyvaert, Kathryn P. .
BEHAVIORAL ECOLOGY AND SOCIOBIOLOGY, 2011, 65 (01) :23-35
[5]   An association model for the solubilities of pharmaceuticals in supercritical carbon dioxide [J].
Ch, Rajasekhar ;
Madras, Giridhar .
THERMOCHIMICA ACTA, 2010, 507-08 :99-105
[6]   Separation of catechins from green tea using carbon dioxide extraction [J].
Chang, CMJ ;
Chiu, KL ;
Chen, YL ;
Chang, CY .
FOOD CHEMISTRY, 2000, 68 (01) :109-113
[7]   SOLUBILITY OF SOLIDS AND LIQUIDS IN SUPERCRITICAL GASES [J].
CHRASTIL, J .
JOURNAL OF PHYSICAL CHEMISTRY, 1982, 86 (15) :3016-3021
[8]   High-pressure fluid phase equilibria - Experimental methods and systems investigated (1994-1999) [J].
Christov, M ;
Dohrn, R .
FLUID PHASE EQUILIBRIA, 2002, 202 (01) :153-218
[9]   ENZYMATIC-SYNTHESIS OF GERANIOL AND CITRONELLOL ESTERS BY DIRECT ESTERIFICATION IN N-HEXANE [J].
CLAON, PA ;
AKOH, CC .
BIOTECHNOLOGY LETTERS, 1993, 15 (12) :1211-1216
[10]   HEPTALDEHYDE AND UNDECYLENIC ACID FROM CASTOR-OIL [J].
DAS, G ;
TRIVEDI, RK ;
VASISHTHA, AK .
JOURNAL OF THE AMERICAN OIL CHEMISTS SOCIETY, 1989, 66 (07) :938-941