Solubility of 3,5-Dinitrobenzoic Acid in Supercritical Carbon Dioxide with Cosolvent at Temperatures from (308 to 328) K and Pressures from (10.0 to 21.0) MPa

被引:21
作者
Tang, Zhao [1 ]
Jin, Jun-su [1 ]
Zhang, Ze-ting [1 ]
Yu, Xiang-yun [1 ]
Xu, Jing-nian [1 ]
机构
[1] Beijing Univ Chem Technol, Coll Chem Engn, Beijing 100029, Peoples R China
基金
中国国家自然科学基金;
关键词
P-TOLUENESULFONAMIDE; BEHENIC ACID; BENZOIC-ACID; CO2; FLUIDS; HYDROXYBENZOATE; MIXTURES; ASPIRIN; ETHANOL; SOLIDS;
D O I
10.1021/je100331h
中图分类号
O414.1 [热力学];
学科分类号
摘要
The solid solubility of 3,5-dinitrobenzoic acid in supercritical carbon dioxide with cosolvent, ethanol, ethyl acetate, n-propanol, and ethylene glycol was measured using a flow-type apparatus at temperatures from (308 to 328) K and in the pressure range of (10.0 to 21.0) MPa. The mole fraction of cosolvent was 0.015, 0.035, and 0.055, respectively. The experimental results showed that the equilibrium solubility of 3,5-dinitrobenzoic acid can be effectively enhanced in the presence of all cosolvents. A semiempirical model, the Sovova model, was modified by adding a function of temperature (7). The accuracy of the modified Sovova model was tested and verified by the solubility data of 17 kinds of solid compounds from the literature. In addition, the modified Sovova model was successfully used to correlate the experimental solubility data of 3,5-dinitrobenzoic acid in supercritical carbon dioxide with different cosolvents, and the average absolute relative deviation (AARD) ranged from (2.2 to 8.8) %.
引用
收藏
页码:3834 / 3841
页数:8
相关论文
共 37 条
  • [1] Solubilities of solids in supercritical fluids .2. Polycyclic aromatic hydrocarbons (PAHs) plus CO2/cosolvent
    Anitescu, G
    Tavlarides, LL
    [J]. JOURNAL OF SUPERCRITICAL FLUIDS, 1997, 11 (1-2) : 37 - 51
  • [2] Solubility of disperse dyes in supercritical carbon dioxide and ethanol
    Banchero, M.
    Ferri, A.
    Manna, L.
    Sicardi, S.
    [J]. FLUID PHASE EQUILIBRIA, 2006, 243 (1-2) : 107 - 114
  • [3] Supercritical fluids: technology and application to food processing
    Brunner, G
    [J]. JOURNAL OF FOOD ENGINEERING, 2005, 67 (1-2) : 21 - 33
  • [4] MODIFICATION OF SUPERCRITICAL FLUID PHASE-BEHAVIOR USING POLAR COSOLVENTS
    DOBBS, JM
    WONG, JM
    LAHIERE, RJ
    JOHNSTON, KP
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1987, 26 (01) : 56 - 65
  • [5] Particle generation for pharmaceutical applications using supercritical fluid technology
    Fages, J
    Lochard, H
    Letourneau, JJ
    Sauceau, M
    Rodier, E
    [J]. POWDER TECHNOLOGY, 2004, 141 (03) : 219 - 226
  • [6] Solubilities of Hexadecanoic and Octadecanoic Acids in Supercritical CO2 With and Without Cosolvents
    Garlapati, Chandrasekhar
    Madras, Giridhar
    [J]. JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2008, 53 (12) : 2913 - 2917
  • [7] Solubility of behenic acid in supercritical carbon dioxide with ethanol
    Guan, B
    Liu, ZM
    Han, BX
    Yan, HK
    [J]. JOURNAL OF SUPERCRITICAL FLUIDS, 1999, 14 (03) : 213 - 218
  • [8] Effect of acetic acid plus acetonitrile and ethanol plus acetonitrile mixed cosolvents on the solubility of stearic acid in supercritical CO2
    Guan, B
    Han, BX
    Yan, HK
    [J]. FLUID PHASE EQUILIBRIA, 1998, 149 (1-2) : 277 - 286
  • [9] Solubility of behenic acid in supercritical CO2 with n-pentane or n-octane cosolvents
    Guan, B
    Liu, ZM
    Han, BX
    Yan, HK
    [J]. JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1999, 44 (06) : 1204 - 1206
  • [10] Gupta R.B., 2007, SOLUBILITY SUPERCRIT