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Massachusetts Institute of Technology

Development of energy efficient membrane distillation systems

Abstract

dc:description.abstract

Membrane distillation (MD) has shown potential as a means of desalination and water purification. As a thermally driven membrane technology which runs at relatively low pressure, which can withstand high salinity feed streams, and which is potentially more resistant to fouling, MD could be used for desalination where reverse osmosis is inadequate. The use of thermal energy, and the ease of construction at small scale, makes this technology attractive for off-grid or renewable power applications as well. However, most research on MD has focused on maximizing purified water output per unit of membrane area as opposed to minimizing system energy consumption and cost. Current MD systems suffer from poor energy efficiency, with reported performance rarely exceeding that of a simple solar still. This thesis explores means to optimize the design of MD for energy efficiency to make it competitive with existing thermal desalination systems, with particular focus on the Air Gap Membrane Distillation (AGMD) configuration. A detailed ID numerical model to explore the effect of design parameters on energy efficiency was developed. Means to enhance energy recovery from hot discharge brine without additional brine concentration, and reduce diffusion resistance by means of reducing pressure in the air gap were explored. A novel configuration delivering solar flux directly to the membrane, and multi-stage, multi-pressure configurations comparable to MSF were also developed. A parameter to relate the performance of a benchscale experiment with similar membrane and gap size to a production system was developed and validated. Small scale experiments were conducted to verify performance for the novel solar powered configuration, reduced gap pressure, and capturing energy from hot discharge brine. Experiments demonstrated the efficacy of a solar absorbing membrane to provide heat to the cycle, and established a benefit of deforming the membrane into the gap under hydraulic pressure; reducing gap size and measurably improving performance. Parametric studies have shown the effectiveness of using the model to design larger, more practical, competitive systems; establishing the importance of long flow lengths, low mean membrane flux, and large membrane area in the design of efficient MD systems.

Degree

thesis:*
Department dc:contributor.department
Massachusetts Institute of Technology. Department of Mechanical Engineering.
Grantor dc:publisher
Massachusetts Institute of Technology
Year dc:date.issued
2013

Author and committee

dc:creator, dc:contributor.*
Author dc:creator
  • Summers, Edward K
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/1721.1/84402
OAI identifier oai:identifier
oai:dspace.mit.edu:1721.1/84402

Chain of custody

source
Harvested from
MIT
Base URL
dspace.mit.edu/oai/request
Last updated
2026-07-22
Source record
OAI-PMH GetRecord
citation

Summers, Edward K. Development of energy efficient membrane distillation systems. Massachusetts Institute of Technology, 2013. http://hdl.handle.net/1721.1/84402