The Riedel vapor pressure correlation and multi-property optimization

被引:8
作者
Hogge, Joseph W. [1 ]
Giles, Neil F. [1 ]
Knotts, Thomas A. [1 ]
Rowley, Richard L. [1 ]
Wilding, W. Vincent [1 ]
机构
[1] Brigham Young Univ, Dept Chem Engn, Provo, UT 84602 USA
关键词
Riedel correlation; Vapor pressure; Heat capacity; Multi-property optimization; ORGANIC OXYGEN COMPOUNDS; OCTANE-ENHANCING ADDITIVES; LIQUID-EQUILIBRIUM DATA; EXCESS ENTHALPY DATA; EQUATION-OF-STATE; TERT-BUTYL ETHER; PLUS N-BUTANE; BUBBLE-TEMPERATURE-MEASUREMENTS; SATURATED HEAT-CAPACITIES; ETHYL 1,1-DIMETHYLETHYL ETHER;
D O I
10.1016/j.fluid.2016.08.032
中图分类号
O414.1 [热力学];
学科分类号
摘要
The Riedel vapor pressure correlation is a useful model that has been employed for decades. The shape of the temperature dependent correlation is a strong function of the value of the final coefficient (denoted as E), particularly at the low temperature end. Vapor pressure data can be accurately correlated with different values of E, but properties derived from vapor pressure are more sensitive to the value of E. Such properties include enthalpy of vaporization and liquid heat capacity. Because these three properties are linked through rigorous thermodynamic relationships (including the Clapeyron equation and the derivative of enthalpy of vaporization), a multi-property optimization is possible to obtain the value of E that will give the best thermodynamic picture for the compound. To determine the effects of the final coefficient on subsequent properties, E was varied from 1 to 6 in integer steps and for E = 0.5, and vapor pressure data were fit for several well-known compounds. These correlations were then tested to see how well they predict enthalpy of vaporization and liquid heat capacity data. The results indicate that the traditional practice of setting E = 6 rarely produces the best thermodynamic consistency, and that E = 2 is superior for many compounds. The improved vapor pressure correlations were then used to predict triple point pressures with favorable results that compare well with the literature. (C) 2016 Elsevier B.V. All rights reserved.
引用
收藏
页码:149 / 165
页数:17
相关论文
共 468 条
[1]  
Aim K., 1980, Journal of Chemical Engineering Data, V25, P100
[2]  
AKITA Y, 1977, SYNTHESIS-STUTTGART, P792
[3]   Isobaric vapour-liquid equilibria for mixtures containing halogenated hydrocarbons at atmospheric pressure -: I.: Binary mixtures of trichloromethane+1,2-dichloroethane, 1,2-dichloroethane+1,1,2,2-tetrachloroethane, trichloromethane+1,1,2,2-tetrachloroethane and n-heptane+1,1,2,2-tetrachloroethane [J].
Al-Hayan, MNM ;
Newsham, DMT .
FLUID PHASE EQUILIBRIA, 1999, 166 (01) :91-100
[4]   Vapor-liquid equilibrium of octane-enhancing additives in gasolines -: 6.: Total pressure data and GE for binary and ternary mixtures containing 1, 1-dimethlethyl methyl ether (MTBE), methanol and n-hexane at 313.15 K [J].
Alonso, C ;
Montero, EA ;
Chamorro, CR ;
Segovia, JJ ;
Martín, MC ;
Villamañán, MA .
FLUID PHASE EQUILIBRIA, 2004, 217 (02) :157-164
[5]   Vapor-liquid equilibrium of octane-enhancing additives in gasolines -: 5.: Total pressure data and GE for binary and ternary mixtures containing 1,1-dimethylpropyl methyl ether (TAME), 1-propanol and n-hexane at 313.15 K [J].
Alonso, C ;
Montero, EA ;
Chamorro, UR ;
Segovia, JJ ;
Martín, MC ;
Villamañán, MA .
FLUID PHASE EQUILIBRIA, 2003, 212 (1-2) :81-95
[6]   Vapour-liquid equilibrium of octane-enhancing additives in gasolines 2.: Total pressure data and gE for binary and ternary mixtures containing tert-amylmethyl ether (TAME), tert-amyl alcohol (TAOH) and n-hexane [J].
Alonso, C ;
Montero, EA ;
Chamorro, CR ;
Segovia, JJ ;
Martín, MC ;
Villamañán, MA .
FLUID PHASE EQUILIBRIA, 2001, 182 (1-2) :241-255
[7]   Phase equilibrium properties of binary and ternary mixtures containing dibutyl ether, cyclohexane, and heptane or 1-hexene at T=313.15 K [J].
Alonso-Tristan, Cristina ;
Villamanan, Miguel A. ;
Chamorro, Cesar R. ;
Segovia, Jose J. .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2008, 53 (07) :1486-1491
[8]   THERMODYNAMIC PROPERTIES OF ORGANIC OXYGEN COMPOUNDS .38. VAPOR-PRESSURES OF SOME ALIPHATIC-KETONES [J].
AMBROSE, D ;
ELLENDER, JH ;
LEES, EB ;
SPRAKE, CHS ;
TOWNSEND, R .
JOURNAL OF CHEMICAL THERMODYNAMICS, 1975, 7 (05) :453-472
[10]   THERMODYNAMIC PROPERTIES OF ORGANIC OXYGEN COMPOUNDS .43. VAPOR-PRESSURES OF SOME ETHERS [J].
AMBROSE, D ;
ELLENDER, JH ;
SPRAKE, CHS ;
TOWNSEND, R .
JOURNAL OF CHEMICAL THERMODYNAMICS, 1976, 8 (02) :165-178