Sensitivity of azeotropic states to activity coefficient model parameters and system variables
暂无分享,去创建一个
[1] J. Wisniak,et al. Vapor-liquid equilibriums in the ternary systems water-formic acid-acetic acid and water-acetic acid-propionic acid , 1977 .
[2] Stanley M. Walas,et al. Phase equilibria in chemical engineering , 1985 .
[3] H. Renon. DECHEMA Chemistry Data Series , 1990 .
[4] Eugene L. Allgower,et al. Numerical continuation methods - an introduction , 1990, Springer series in computational mathematics.
[5] Michael F. Doherty,et al. A new pressure-swing-distillation process for separating homogeneous azeotropic mixtures , 1992 .
[6] M. F. Malone,et al. Computing azeotropes in multicomponent mixtures , 1993 .
[7] Sosonkina Maria,et al. HOMPACK90: A Suite of FORTRAN 90 Codes for Globally Convergent Homotopy Algorithms , 1996 .
[8] Masha Sosonkina,et al. Algorithm 777: HOMPACK90: a suite of Fortran 90 codes for globally convergent homotopy algorithms , 1997, TOMS.
[9] P. I. Barton,et al. Computation of heteroazeotropes. Part II: efficient calculation of changes in phase equilibrium structure , 2000 .
[10] P. I. Barton,et al. Computation of heteroazeotropes. Part I: Theory , 2000 .
[11] N. Kalogerakis,et al. Applied parameter estimation for chemical engineers , 2000 .
[12] Michael F. Malone,et al. Conceptual design of distillation systems , 2001 .
[13] N. Aslam,et al. Reliable computation of binary homogeneous azeotropes of multi-component mixtures at higher pressures through equation of states , 2004 .