Please use this identifier to cite or link to this item: https://doi.org/10.1016/j.ijheatmasstransfer.2008.10.012
Title: Operational strategy of adsorption desalination systems
Authors: Thu, K. 
Ng, K.C. 
Saha, B.B.
Chakraborty, A.
Koyama, S.
Keywords: Adsorption desalination
Performance ratio
Regeneration temperature
Specific daily water production
Issue Date: Mar-2009
Source: Thu, K., Ng, K.C., Saha, B.B., Chakraborty, A., Koyama, S. (2009-03). Operational strategy of adsorption desalination systems. International Journal of Heat and Mass Transfer 52 (7-8) : 1811-1816. ScholarBank@NUS Repository. https://doi.org/10.1016/j.ijheatmasstransfer.2008.10.012
Abstract: This paper presents the performances of an adsorption desalination (AD) system in two-bed and four-bed operational modes. The tested results are calculated in terms of key performance parameters namely, (i) specific daily water production (SDWP), (ii) cycle time, and (iii) performance ratio (PR) for various heat source temperatures, mass flow rates, cycle times along with a fixed heat sink temperature. The optimum input parameters such as driving heat source and cycle time of the AD cycle are also evaluated. It is found from the present experimental data that the maximum potable water production per tonne of adsorbent (silica gel) per day is about 10 m3 whilst the corresponding performance ratio is 0.61, and a longer cycle time is required to achieve maximum water production at lower heat source temperatures. This paper also provides a useful guideline for the operational strategy of the AD cycle. © 2008 Elsevier Ltd. All rights reserved.
Source Title: International Journal of Heat and Mass Transfer
URI: http://scholarbank.nus.edu.sg/handle/10635/85520
ISSN: 00179310
DOI: 10.1016/j.ijheatmasstransfer.2008.10.012
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