Please use this identifier to cite or link to this item: https://hdl.handle.net/10356/100406
Title: Performance investigation of advanced adsorption desalination cycle with condenser–evaporator heat recovery scheme
Authors: Thu, Kyaw
Kim, Young Deuk
Myat, Aung
Chakraborty, Anutosh
Ng, Kim Choon
Keywords: DRNTU::Engineering::Mechanical engineering::Energy conservation
Issue Date: 2013
Source: Thu, K., Kim, Y. D., Myat, A., Chakraborty, A., & Ng, K. C. (2013). Performance investigation of advanced adsorption desalination cycle with condenser–evaporator heat recovery scheme. Desalination and Water Treatment, 51(1-3), 150-163.
Series/Report no.: Desalination and water treatment
Abstract: Energy or heat recovery schemes are keys for the performance improvement of any heat-activated cycles such as the absorption and adsorption cycles. We present two innovative heat recovery schemes between the condensing and evaporating units of an adsorption desalination (AD) cycle. By recovering the latent heat of condenser and dumping it into the evaporative process of the evaporator, it elevates the evaporating temperature and hence the adsorption pressure seen by the adsorbent. From isotherms, this has an effect of increasing the vapour uptake. In the proposed configurations, one approach is simply to have a run-about water circuit between the condenser and the evaporator and a pump is used to achieve the water circulation. This run-around circuit is a practical method for retrofitting purposes. The second method is targeted towards a new AD cycle where an encapsulated condenser–evaporator unit is employed. The heat transfer between the condensing and evaporative vapour is almost immediate and the processes occur in a fully integrated vessel, thereby minimizing the heat transfer resistances of heat exchangers.
URI: https://hdl.handle.net/10356/100406
http://hdl.handle.net/10220/18626
DOI: http://dx.doi.org/10.1080/19443994.2012.693659
Rights: © 2013 Desalination Publications. This paper was published in Desalination and Water Treatment and is made available as an electronic reprint (preprint) with permission of Desalination Publications. The paper can be found at the following official DOI: [http://dx.doi.org/10.1080/19443994.2012.693659]. One print or electronic copy may be made for personal use only. Systematic or multiple reproduction, distribution to multiple locations via electronic or other means, duplication of any material in this paper for a fee or for commercial purposes, or modification of the content of the paper is prohibited and is subject to penalties under law.
Fulltext Permission: open
Fulltext Availability: With Fulltext
Appears in Collections:MAE Journal Articles

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