4.7 Article

High-temperature-steam-driven, varied-pressure, humidification-dehumidification system coupled with reverse osmosis for energy-efficient seawater desalination

Journal

ENERGY
Volume 37, Issue 1, Pages 482-493

Publisher

PERGAMON-ELSEVIER SCIENCE LTD
DOI: 10.1016/j.energy.2011.11.007

Keywords

Carrier gas; Desalination; Humidification; Thermal vapor compression; Power and water co-production; Reverse osmosis

Funding

  1. King Fahd University of Petroleum and Minerals through the Center for Clean Water and Clean Energy at MIT and KFUPM
  2. MIT Legatum Center for development and entrepreneurship
  3. U.S. Department of State

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The specific thermal energy consumed by steam driven thermal desalination systems can be decreased significantly by reducing the total entropy rate of steam used per unit mass of distilled water produced in the system. This specific entropy rate can be reduced by using a high pressure, saturated steam at a low specific entropy and high specific enthalpy. However, the temperature of steam that can be used is limited owing to scale formation considerations. In this manuscript, we propose a novel carrier gas based desalination cycle which can use steam at a high temperature (> 120 degrees C) without causing formation of hard scales. This system is based on the principle of HDH (humidification dehumidification) desalination. Various salient features of this cycle are analyzed in this paper bringing out its merits and demerits. Important system and component parameters are identified to facilitate optimal operation and design. The energy performance of this new system is compared with all existing desalination systems including MSF, MED. MVC and RO. It has been found that the performance of the new system is comparable to existing thermal desalination systems and is much higher than conventional HDH systems. (C) 2011 Elsevier Ltd. All rights reserved.

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