Abstract
Consideration is given to a tray liquid in the intermediate state between ideal displacement and total mixing, for which purpose the degree of attaining the latter state by the liquid is introduced. The composition of the vapor after leaving an ideal tray is assumed to be in equilibrium with that of the liquid in its intermediate state. Four variants of interrelation of the real and ideal trays are considered; the efficiencies for the vapor and the liquid are proved to be equal for each of them. Ratios for the efficiencies of all the variants are obtained. A comparison is made of the efficiency ratios as functions of liquid mixing.
Similar content being viewed by others
References
V. V. Kafarov,Fundamental Principles of Mass Transfer [in Russian], Moscow (1972), pp. 276–289.
J. Perry,Handbook for Chemical Engineers [Russian translation], Vol. 2, Leningrad (1969), pp. 24–27.
V. V. Pavlechko,Inzh.-Fiz. Zh.,72, No. 4, 764–770 (1999).
E. V. Murphree,Ind. Eng. Chem.,17, No. 7, 747–750 (1925).
A. G. Medina, N. Ashton, and C. McDermott,Chem. Eng. Sci.,34, No. 9, 1105–1112 (1979).
H. Hausen,Chem. Ing. Tech.,25, No. 10, 595–597 (1953).
V. N. Pavlechko,Tr. BGTU, Ser. III, Khim. Khim. Tekhnol., Issue VI, 131–138 (1998).
V. N. Pavlechko,Tr. BGTU, Ser. III, Khim. Khim. Tekhnol., Issue VI, 138–144 (1998).
Author information
Authors and Affiliations
Additional information
Translated from Inzhenerno-Fizicheskii Zhurnal, Vol. 73, No. 3, pp. 514–519, May–June, 2000.
Rights and permissions
About this article
Cite this article
Pavlechko, V.N. Comparison of the efficiencies of rectification trays in countercurrent motion of phases with allowance for liquid mixing. J Eng Phys Thermophys 73, 500–506 (2000). https://doi.org/10.1007/BF02681791
Received:
Issue Date:
DOI: https://doi.org/10.1007/BF02681791