Numerical and experimental investigation of multiple heat exchanger modules in cooling and desalination adsorption system using metal organic framework

被引:22
作者
Albaik, Ibrahim [1 ]
Elsheniti, Mahmoud Badawy [2 ,3 ]
Al-Dadah, Raya [1 ]
Mahmoud, Saad [1 ]
Solmaz, Ismail [4 ]
机构
[1] Univ Birmingham, Dept Mech Engn, Birmingham B15 2TT, W Midlands, England
[2] King Saud Univ, Coll Engn, Mech Engn Dept, Riyadh 11451, Saudi Arabia
[3] Alexandria Univ, Fac Engn, Mech Engn Dept, Alexandria 21544, Egypt
[4] Ataturk Univ, Dept Mech Engn, TR-25240 Erzurum, Turkey
基金
英国工程与自然科学研究理事会;
关键词
Adsorption desalination; Aluminium fumarate; Numerical modelling; Specific daily water production; ALUMINUM FUMARATE; ADSORBENT BED; PERFORMANCE ANALYSIS; MASS-TRANSFER; WATER; PUMP; CPO-27(NI); PRESSURE; CHILLER; MODEL;
D O I
10.1016/j.enconman.2021.114934
中图分类号
O414.1 [热力学];
学科分类号
摘要
The cooling and desalination adsorption system is a heat-activated system based on the solid sorption process. The main challenge in this system is concentrated to decrease the energy consumption of this system using a low desorption temperature (less than 90 degrees C) while maintaining a good performance. A scaled-up adsorption system using multiple heat exchanger modules packed with commercially available metal-organic framework material that operates at low desorption temperature, was numerically and experimentally investigated in the present paper. Three-dimensional and two-dimensional axisymmetric numerical models were developed to simulate heat and mass transfer phenomena considering the internal and external mass transfer in the adsorbent domains. Effects of the modules' connection options and vapor gap between modules on the system performance were examined. The highest coefficient of performance was achieved when connecting the modules in series, affected by the considerable reduction in the heating power. However, the increase in the effective amount of adsorbate resulted in the best specific cooling power when connecting the modules in parallel. Additionally, A scaled-up adsorption cooling/desalination system using 23.2 kg of Aluminium Fumarate packed in 16 modules was constructed and evaluated experimentally. The system produced desalinated water of 201 L/day and cooling capacity of 5.25 kW at the evaporator, condenser, and desorption water temperatures of 24 degrees C, 25 degrees C, and 85 degrees C, respectively. The specific daily water production decreased by 16.3% when the water salinity increased from 90 to 100,000 ppm, while the lowest specific electrical energy consumption of the proposed system is 1.87 kWh/m(3). The theoretical and experimental results will enable further scaling up of an efficient MOF adsorption system for cooling and water desalination.
引用
收藏
页数:21
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