Published September 2006 | Version v1
Journal article

Thermodynamically equivalent distillation schemes to the Petlyuk column for ternary mixtures

  • 1. Universidad de Guanajuato, Facultad de Quimica, Noria Alta s/n, Guanajuato, Gto. 36050 (Mexico)
  • 2. Instituto Tecnologico de Celaya, Departamento de Ingenieria Quimica, Av. Tecnologico y Garcia Cubas s/n, Celaya, Gto. 38010 (Mexico)

Description

Thermally coupled distillation sequences for ternary separations have been shown to provide significant energy savings with respect to the conventional direct and indirect distillation sequences. Although the Petlyuk column is generally more efficient than the other thermally coupled schemes, its structure creates potential operating problems because of the bi-directional vapour interconnecting streams. In this paper, second law calculations were performed for the Petlyuk column and six alternative distillation schemes that show unidirectional flows; in principle, such alternative configurations are expected to present better operational properties than those of the original Petlyuk column. The results indicate that the proposed distillation arrangements have values of thermodynamic efficiency very close to that of the Petlyuk column. This result is important because let us establish that the alternative distillation sequences: (i) are thermodynamically equivalent to the Petlyuk column, (ii) could be more easily implemented in practice, and (iii) also achieve significant energy savings

Additional details

Identifiers

DOI
10.1016/j.energy.2005.10.007;
PII
S0360-5442(05)00195-7;

Publishing Information

Journal Title
Energy (Oxford)
Journal Volume
31
Journal Issue
12
Journal Page Range
p. 1840-1847
ISSN
0360-5442
CODEN
ENEYDS

INIS

Country of Publication
United Kingdom
Country of Input or Organization
International Atomic Energy Agency (IAEA)
INIS RN
38015067
Subject category
S71: CLASSICAL AND QUANTUM MECHANICS, GENERAL PHYSICS;
Descriptors DEI
CONFIGURATION; DISTILLATION; EFFICIENCY; MIXTURES; THERMODYNAMICS; VAPORS
Descriptors DEC
DISPERSIONS; FLUIDS; GASES; SEPARATION PROCESSES

Optional Information

Copyright
Copyright (c) 2005 Elsevier Science B.V., Amsterdam, The Netherlands, All rights reserved.