Measurement, correlation and thermodynamic modeling of the solubility of Ketotifen fumarate (KTF) in supercritical carbon dioxide: Evaluation of PCP-SAFT equation of state

被引:100
作者
Sodeifian, Gholamhossein [1 ,2 ]
Ardestani, Nedasadat Saadati [1 ]
Sajadian, Seyed Ali [1 ]
Panah, Hamidreza Soltani [3 ]
机构
[1] Univ Kashan, Dept Chem Engn, Fac Engn, Kashan 8731753153, Iran
[2] Univ Kashan, Lab Supercrit Fluids & Nanotechnol, Kashan 8731753153, Iran
[3] Tarbiat Modares Univ, Dept Chem Engn, POB 14115-111, Tehran, Iran
关键词
Solubility; Supercritical fluid; Ketotifen fumarate (KTF); Anti-histamine and anti-inflammatory drug; PCP-SAFT EoS; ARTIFICIAL NEURAL-NETWORK; SOLUTE SOLUBILITY; RESPONSE-SURFACE; FLUID EXTRACTION; PETROLEUM FLUID; SOLID COMPOUNDS; ESSENTIAL OIL; CLOUD POINT; OPTIMIZATION; PRESSURE;
D O I
10.1016/j.fluid.2017.11.016
中图分类号
O414.1 [热力学];
学科分类号
摘要
Solubility measurement of desired solid component(s) represents a primary and crucial step of feasibility study on production process of a nanoparticle drug through supercritical fluid (SCF) technology. Ketotifen fumarate (KTF) is an effective anti-histamine and anti-inflammatory drug with a wide spectrum of applications in treatment and prevention of a variety of mucosal and skin allergies. In this research, for the first time, solubility of KTF was determined experimentally in supercritical carbon dioxide (SC-CO2) at different temperatures in the range 308.2-338.2 K and different pressures in the range 120-300 bar. Obtained in mole fraction, KTF solubility was in the range of 0.211 x 10(-4) to 10.766 x 10(-4). To predict solubility of the solid solute drug in supercritical fluid, experimental data modeling was successfully accomplished by using two different groups of models, i.e. six density-based empirical models, namely Chrastil, Khansari, Bartle, Spark and Bian models, and two equations of state (EoS), namely PengRobinson (PR) and Perturbed-Chain Statistical Associating Fluid (PCP-SAFT). Results of analysis of variance (ANOVA) indicated the Peng-Robinson model as the model of choice for predicting solubility of KTF in SC-CO2. Using correlation results, the heat of drug-CO2 solvation and that of drug vaporization were approximated as 223.77 and 0.09577 kJ/mol, respectively. (C) 2017 Elsevier B.V. All rights reserved.
引用
收藏
页码:102 / 114
页数:13
相关论文
共 70 条
[31]   GENERALIZED THERMODYNAMIC CORRELATION BASED ON 3-PARAMETER CORRESPONDING STATES [J].
LEE, BI ;
KESLER, MG .
AICHE JOURNAL, 1975, 21 (03) :510-527
[32]   Modeling the liquid-liquid equilibrium of petroleum fluid and polar compounds containing systems with the PC-SAFT equation of state [J].
Liang, Xiaodong ;
Yan, Wei ;
Thomsen, Kaj ;
Kontogeorgis, Georgios M. .
FLUID PHASE EQUILIBRIA, 2015, 406 :147-155
[33]   On petroleum fluid characterization with the PC-SAFT equation of state [J].
Liang, Xiaodong ;
Yan, Wei ;
Thomsen, Kaj ;
Kontogeorgis, Georgios M. .
FLUID PHASE EQUILIBRIA, 2014, 375 :254-268
[34]   High-pressure vapor-liquid equilibria of the second generation biofuel blends (2-methylfuran plus iso-octane) and (2-methyltetrahydrofuran plus di-n-butyl ether): Experiments and PCP-SAFT modeling [J].
Liebergesell, B. ;
Kaminski, S. ;
Pauls, C. ;
de Loos, Th. W. ;
Vlugt, T. J. H. ;
Leonhard, K. ;
Bardow, A. .
FLUID PHASE EQUILIBRIA, 2015, 400 :95-102
[35]  
LYMAN WJ, 1990, HDB CHEM PROPERTY ES
[36]   Modeling the solubilities of fatty acids in supercritical carbon dioxide [J].
Madras, G ;
Kulkarni, C ;
Modak, J .
FLUID PHASE EQUILIBRIA, 2003, 209 (02) :207-213
[37]   The solubility of solids in supercritical fluids [J].
Méndez-Santiago, J ;
Teja, AS .
FLUID PHASE EQUILIBRIA, 1999, 158 :501-510
[38]  
Montgomery D., 2013, DESIGN ANAL EXPT, V8
[39]   Experimental measurements and thermodynamic modeling of the cloud point pressure for solubility of copolymers of vinyl acetate and dibutyl maleate in supercritical CO2 [J].
Panah, Hamidreza Soltani ;
Haghtalab, Ali ;
Abdollahi, Mandi ;
Mohammadi, Amir H. ;
Ramjugernath, Deresh ;
Nelson, Wayne Michael ;
Moghaddam, Abdolsamad Zarringhalam ;
Hemmati, Mahmood .
FLUID PHASE EQUILIBRIA, 2016, 425 :136-142
[40]   Solubility of Δ9-tetrahydrocannabinol in supercritical carbon dioxide: Experiments and modeling [J].
Perrotin-Brunel, Helene ;
Perez, Pablo Cabeza ;
van Roosmalen, Maaike J. E. ;
van Spronsen, Jaap ;
Witkamp, Geert-Jan ;
Peters, Cor J. .
JOURNAL OF SUPERCRITICAL FLUIDS, 2010, 52 (01) :6-10