Solar liquid desiccant regeneration and nanofluids in evaporative cooling for greenhouse food production in Saudi Arabia

被引:68
作者
Abu-Hamdeh, Nidal H. [1 ]
Almitani, Khalid H. [1 ]
机构
[1] King Abdulaziz Univ, Dept Mech Engn, Fac Engn, POB 40844, Jeddah 21511, Saudi Arabia
关键词
Evaporative cooling; Liquid desiccant; Solar energy; Nanofluids; AIR-CONDITIONING SYSTEM; THERMAL-CONDUCTIVITY; HOT CLIMATES; PERFORMANCE; DEHUMIDIFICATION; TECHNOLOGY;
D O I
10.1016/j.solener.2016.04.048
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
080707 [能源环境工程]; 082001 [油气井工程];
摘要
This article is about using solar energy and liquid desiccant to provide evaporative cooling systems of spaces occupied by plants in high ambient humidity climate. The system took full benefit of the regeneration of liquid desiccant by pure solar energy. The effect of airflow on the predicted and measured average daily maximums of greenhouse temperatures obtained using desiccant system and those obtained with conventional evaporative cooling for the month of June was investigated and reported. The desiccant evaporative cooling system lowered the average daily maximum temperatures in the greenhouse by about 6 degrees C relative to conventional evaporative cooling system. Furthermore, shell and tube heat exchanger configuration was adopted to simulate pipes implanted in the desiccant pad and fed with nanofluids supplied from a cooling tower. The effects of changing volume fractions of nanoparticles on energy effectiveness and heat transfer coefficient of an assumed shell and tube heat exchanger have been analyzed and discussed. Improvements on convective heat transfer coefficient of 7.20-14.40%, 6.20-12.30%, and 5.50-9.01% were obtained for 0.01-0.04 volume concentrations of Al2O3-W, Fe3O4-W, and ZnO-W nanofluids, respectively. In addition, energy effectiveness has been analyzed and enhancements of 27.50-50.10%, 25.01-40.10%, and 24.00-32.02% were obtained for volume fractions from 0.01 to 0.04 of ZnO, Fe3O4, and Al2O3 nanoparticles, respectively, suspended in water with constant mass flow rates of fluids. Dynamic indicators (life cycle and annualized life cycle costs) were applied to evaluate the economic-effectiveness of this energy supply system. The total life cycle cost was found to be $11,206 and the annualized life cycle cost for this system was found to be 1317 $/year. (c) 2016 Elsevier Ltd. All rights reserved.
引用
收藏
页码:202 / 210
页数:9
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