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Massachusetts Institute of Technology

Entropy generation minimization of a heat and mass exchanger for use in a humidification-dehumidification desalination system

Abstract

dc:description.abstract

The physical mechanisms of entropy generation in a condenser with high fractions of non-condensable gases are examined using control volume, scaling, and boundary layer techniques, with the aim of defining a criterion for minimum entropy generation rate that is useful in engineering analyses. This process is particularly relevant in humidification-dehumidification desalination systems, where minimizing entropy generation per unit water produced is critical to maximizing system performance. Control volume techniques are first employed, and shown to be ill-suited to understanding why and how balancing a heat and mass exchanger minimizes entropy generation. As a result, a more complex, boundary layer model is introduced; the process is modeled by a consideration of the vapor-gas boundary layer alone, as it is the dominant thermal resistance and, consequently, the largest source of entropy production in many practical condensers with high fractions of non-condensable gases. Most previous studies of condensation have been restricted to a constant wall temperature, but it is shown here that for high concentrations of non-condensable gases, a varying wall temperature--obtained from balancing the heat and mass exchanger-greatly reduces total entropy generation rate. Further, it is found that the diffusion of the condensing vapor through the vapor-non-condensable mixture boundary layer is the larger and often dominant mechanism of entropy production in such a condenser. As a result, when seeking to design a unit of desired heat transfer and condensation rates for minimum entropy generation, minimizing the variance in the driving force associated with diffusion yields a closer approximation to the minimum overall entropy generation rate than does equipartition of temperature difference. Finally, a rigorous, and general definition of balancing for any heat and mass exchanger is discussed.

Degree

thesis:*
Department dc:contributor.department
Massachusetts Institute of Technology. Dept. of Mechanical Engineering.
Grantor dc:publisher
Massachusetts Institute of Technology
Year dc:date.issued
2012

Author and committee

dc:creator, dc:contributor.*
Author dc:creator
  • Thiel, Gregory P
Advisor dc:contributor.advisor
  • John H. Lienhard, V.

Subjects

dc:subject × 1

Rights

dc:rights
Statement dc:rights
  • M.I.T. theses are protected by copyright. They may be viewed from this source for any purpose, but reproduction or distribution in any format is prohibited without written permission. See provided URL for inquiries about permission.
Language dc:language.iso
eng

Identifiers

dc:identifier.*
Handle dc:identifier.uri
http://hdl.handle.net/1721.1/74945
OAI identifier oai:identifier
oai:dspace.mit.edu:1721.1/74945

Chain of custody

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MIT
Base URL
dspace.mit.edu/oai/request
Last updated
2026-07-22
Source record
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citation

Thiel, Gregory P. Entropy generation minimization of a heat and mass exchanger for use in a humidification-dehumidification desalination system. Massachusetts Institute of Technology, 2012. http://hdl.handle.net/1721.1/74945