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Modeling and simulation of solar collector/regenerator for liquid desiccant cooling systems

机译:液体干燥剂冷却系统的太阳能集热器/蓄热器的建模与仿真

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摘要

Solar liquid collector/regenerator combines solar photothermic transformation and liquid regeneration together for solar energy-driven liquid desiccant cooling systems. A group of dimensionless heat and mass transfer equations describing the heat and mass transfer process in the solar C/R(Collector/ Regenerator) were obtained by introducing total temperature difference (△T_0) and dimensionless heat loss coefficient (-h_z). The increment of solution concentration △C was increased 2.9-3.5%/℃ and 5.3%/℃ for increasing unit inlet temperature of air stream and solution respectively and increased about 6.2%/(g/ kg) and 0.9%/(g/kg) for decreasing unit inlet humidity ratio of air and solution concentration. Besides, the increasing number of heat transfer units (NTU), air-to-salt mass flow rate ratio (ASMR) and total temperature difference (△T_0) can increase the performance of solution regeneration significantly. Compared to parallel flow regeneration, the performance of counterflow regeneration was increased about 10%.
机译:太阳能液体收集器/蓄热器将太阳能光热转化和液体再生结合在一起,用于太阳能驱动的液体干燥剂冷却系统。通过引入总温差(△T_0)和无量纲热损失系数(-h_z),获得了描述太阳能C / R(收集器/蓄热器)中传热和传质过程的一组无量纲传热和传质方程。随着气流和溶液单位入口温度的增加,溶液浓度△C的增加分别增加了2.9-3.5%/℃和5.3%/℃,分别增加了约6.2%/(g / kg)和0.9%/(g / kg) ),以降低空气和溶液浓度的单位入口湿度比。此外,增加传热单元(NTU)的数量,气盐质量流量比(ASMR)和总温差(△T_0)可以显着提高溶液再生的性能。与平行流再生相比,逆流再生的性能提高了约10%。

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