Performance analysis of four bed adsorption water desalination/refrigeration system, comparison of AQSOA-Z02 to silica-gel

Abstract Although many water desalination techniques have been introduced decades ago, there are still areas around the world suffering from fresh water shortages. The widespread of desalination technologies is limited due to their high energy consumption, cost and adverse environmental impact. Recently, adsorption technology for water desalination has been investigated showing potential of using low temperature waste heat (50–85 °C) thus reducing energy consumption and CO2 emissions. This work mathematically investigates the performance of 4 bed adsorption cycle using two different adsorbents, silica-gel and an advanced zeolite material AQSOA-Z02, produced by Mitsubishi-plastics for fresh water production and cooling. The work studied effects of evaporator and heat source temperatures on water production rate and cooling capacity. Results showed that at low chilled water temperatures below 20 °C, AQSOA-Z02 outperforms silica-gel with water production of 6.2 m3 of water/day and cooling of 53.7 Rton/tonne of AQSOA-Z02 compared to 3.5 m3 of water/day and 15.0 Rton/tonne of silica-gel. While, at chilled water temperatures above 20 °C, AQSOA-Z02 and silica-gel have comparable performance with around 7 m3 of water/day and 60 Rton of cooling. Since cooling applications require chilled water temperature less than 20 °C, therefore AQSOA-Z02 is more suitable for applications where cooling and fresh water are needed.

[1]  Kyaw Thu,et al.  Study on a waste heat-driven adsorption cooling cum desalination cycle , 2012 .

[2]  R. AL-Dadah,et al.  Characterisation of metal organic frameworks for adsorption cooling , 2012 .

[3]  Ruzhu Wang,et al.  Progress in the development of solid–gas sorption refrigeration thermodynamic cycle driven by low-grade thermal energy , 2014 .

[4]  Hassan E.S. Fath,et al.  Techno-economic assessment and environmental impacts of desalination technologies , 2011 .

[5]  M. Goldsworthy,et al.  Experimental analysis and numerical modelling of an AQSOA zeolite desiccant wheel , 2015 .

[6]  Kyaw Thu,et al.  Adsorption desalination: An emerging low-cost thermal desalination method , 2013 .

[7]  Raya Al-Dadah,et al.  Comparative Analysis of Desalination Technologies , 2014 .

[8]  Kyaw Thu,et al.  Operational strategy of adsorption desalination systems , 2009 .

[9]  R. AL-Dadah,et al.  Effect of Evaporator Temperature on the Performance of Water Desalination/Refrigeration Adsorption System Using AQSOA-ZO2 , 2015 .

[10]  Kyaw Thu,et al.  Advanced Adsorption Cooling cum Desalination Cycle: A Thermodynamic Framework , 2011 .

[11]  Eric Hu,et al.  Thermodynamic cycles of adsorption desalination system , 2012 .

[12]  José M. Corberán,et al.  Modelling of an adsorption system driven by engine waste heat for truck cabin A/C. Performance estimation for a standard driving cycle , 2010 .

[13]  S. F. Smeding,et al.  Silicagel-water adsorption cooling prototype system for mobile air conditioning , 2009 .

[14]  Nikolay Voutchkov,et al.  Desalination Technology : Health and Environmental Impacts , 2010 .

[15]  H. Ettouney,et al.  Fundamentals of Salt Water Desalination , 2002 .

[16]  Kim Choon Ng,et al.  Experimental investigation of an adsorption desalination plant using low-temperature waste heat , 2005 .

[17]  Anutosh Chakraborty,et al.  Thermodynamic formalism of water uptakes on solid porous adsorbents for adsorption cooling applications , 2014 .

[18]  Un Water,et al.  Water Security & the Global Water Agenda , 2013 .

[19]  Yung-Tse Hung,et al.  Membrane and Desalination Technologies , 2011 .

[20]  M. Biggs,et al.  Thermodynamic analysis of an adsorption-based desalination cycle , 2010 .

[21]  Kyaw Thu,et al.  Solar-assisted dual-effect adsorption cycle for the production of cooling effect and potable water , 2009 .

[22]  S. S. Murthy,et al.  Solar Driven Adsorption Desalination System , 2014 .