Simultaneous production of cooling and freshwater by an integrated indirect evaporative cooling and humidification-dehumidification desalination cycle
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Chen, Qian
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King Abdullah Univ Sci & Technol, Water Desalinat & Reuse Ctr, Thuwal 23955, Saudi ArabiaKing Abdullah Univ Sci & Technol, Water Desalinat & Reuse Ctr, Thuwal 23955, Saudi Arabia
Chen, Qian
[1
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Burhan, Muhammad
[1
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Shahzad, Muhammad Wakil
[1
,2
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Ybyraiymkul, Doskhan
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King Abdullah Univ Sci & Technol, Water Desalinat & Reuse Ctr, Thuwal 23955, Saudi ArabiaKing Abdullah Univ Sci & Technol, Water Desalinat & Reuse Ctr, Thuwal 23955, Saudi Arabia
Ybyraiymkul, Doskhan
[1
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Akhtar, Faheem Hassan
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King Abdullah Univ Sci & Technol, Water Desalinat & Reuse Ctr, Thuwal 23955, Saudi ArabiaKing Abdullah Univ Sci & Technol, Water Desalinat & Reuse Ctr, Thuwal 23955, Saudi Arabia
Akhtar, Faheem Hassan
[1
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Ng, Kim Choon
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King Abdullah Univ Sci & Technol, Water Desalinat & Reuse Ctr, Thuwal 23955, Saudi ArabiaKing Abdullah Univ Sci & Technol, Water Desalinat & Reuse Ctr, Thuwal 23955, Saudi Arabia
Ng, Kim Choon
[1
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[1] King Abdullah Univ Sci & Technol, Water Desalinat & Reuse Ctr, Thuwal 23955, Saudi Arabia
[2] Northumbria Univ, Newcastle Upon Tyne, Tyne & Wear, England
Cooling and freshwater represent two fundamental demands in hot and arid regions. This paper reports the integration of an indirect evaporative cooler (IEC) and a humidification-dehumidification desalination cycle (HDH) for the simultaneous production of cooling and freshwater. To take full advantage of system integration, the purge air from IEC is supplied to HDH to promote water productivity. A pilot IEC unit is firstly designed and tested to achieve the temperatures and humidity of the outlet air steams. Results reveal that the IEC unit is able to cool down the supply air to below 25 degrees C under different outdoor conditions, and the purge air temperature is also 5-10 degrees C lower than the intake air temperature. Employing the IEC purge air as the working air, the HDH cycle is then investigated analytically. Under the operation ranges considered, the freshwater productivity and gain-output ratio (GOR) are 25-125 L/hr and 1.6-2.5, respectively, which are higher than other HDH configurations operating under the same conditions. Finally, the performance of the combined IEC-HDH system is evaluated. The overall coefficient of performance (COP) and Second-law efficiency are found to be 2.1-2.5 and 3-26%, respectively. Further improvement of efficiency can be achieved by integrating with adsorption or vapor compression refrigeration cycles.
机构:
Univ Missouri Columbia, Coll Engn, Multiphys Energy Res Ctr MERC, Columbiaville, MI 65211 USAUniv Missouri Columbia, Coll Engn, Multiphys Energy Res Ctr MERC, Columbiaville, MI 65211 USA
Mohammed, Ramy H.
Spitzenberger, Jeremy
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Univ Missouri Columbia, Coll Engn, Multiphys Energy Res Ctr MERC, Columbiaville, MI 65211 USAUniv Missouri Columbia, Coll Engn, Multiphys Energy Res Ctr MERC, Columbiaville, MI 65211 USA
Spitzenberger, Jeremy
Mohammadian, Shahabeddin K.
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Univ Missouri Columbia, Coll Engn, Multiphys Energy Res Ctr MERC, Columbiaville, MI 65211 USAUniv Missouri Columbia, Coll Engn, Multiphys Energy Res Ctr MERC, Columbiaville, MI 65211 USA
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VIT Univ, Sch Mech Engn, Res & Green Technol Ctr CO2, Vellore 632014, Tamil Nadu, IndiaVIT Univ, Sch Mech Engn, Res & Green Technol Ctr CO2, Vellore 632014, Tamil Nadu, India
Chiranjeevi, C.
Srinivas, T.
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VIT Univ, Sch Mech Engn, Res & Green Technol Ctr CO2, Vellore 632014, Tamil Nadu, IndiaVIT Univ, Sch Mech Engn, Res & Green Technol Ctr CO2, Vellore 632014, Tamil Nadu, India
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VIT Univ, Sch Mech & Bldg Sci, Res & Green Technol Ctr CO2, Vellore 632014, Tamil Nadu, IndiaVIT Univ, Sch Mech & Bldg Sci, Res & Green Technol Ctr CO2, Vellore 632014, Tamil Nadu, India
Chiranjeevi, C.
Srinivas, T.
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VIT Univ, Sch Mech & Bldg Sci, Res & Green Technol Ctr CO2, Vellore 632014, Tamil Nadu, IndiaVIT Univ, Sch Mech & Bldg Sci, Res & Green Technol Ctr CO2, Vellore 632014, Tamil Nadu, India