GAX制冷机分支循环性能的理论分析

Q. R. Al-amir, N. Y. Khudair
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引用次数: 0

摘要

在本研究中,研究了用NH3-H2O对操作的分支GAX吸收循环,以评估其在稳态条件下的性能。使用工程方程求解器(EES)软件实现循环建模。分析包括质量方程、物种方程和能量守恒方程。该分析用于模拟标称容量为95TR的空调应用中的GAX吸收式制冷机的利用率。这种制冷机使用太阳能收集器作为热源。在不同的热源温度(140-185°C)、冷凝器出口温度(30-48°C)和蒸发器出口温度(2-11°C)下选择操作参数;分流比(0至0.18);氨浓度差(0.25-036),溶液泵中的质量流量mr=1kg/s;热交换器的有效性?0.8。结果表明,平均COP对分支式GAX吸收式制冷机的平均COP和制冷量随着发电机和蒸发器温度的升高而增加,而随着冷凝器温度的升高则降低的运行条件是敏感的。模拟结果还表明,分流比和氨浓度差对吸收式制冷机的性能有显著影响。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
THE ORETICAL ANALYSIS ON THE PERFORMANCE OF BRANCHED GAX CHILLER CYCLE
In this study, a branched GAX absorption cycle operating with NH3-H2O pair has beeninvestigated to assess its performance under steady state conditions. The cycle modeling isimplemented using Engineering Equation Solver (EES) software. Analysis includesequations of mass, species and energy conservation. The analysis is used to simulate a GAXabsorption chiller utilization for air conditioning applications with a nominal capacity of 95TR. This chiller uses solar collectors as heat source. The operating parameters are selected atdifferent values of the heat source temperature (140 - 185°C), condenser exit temperature(30 to 48°C), evaporator exit temperature (2 to 11°C) ; split ratio (0 to 0.18); the difference inammonia concentration(0.25-036), mass flow rate in solution pump mr=1 kg/s; heatexchanger effectiveness ? ? 0.8. The results showed that the average COP is sensitive tooperating conditions where the average COP and cooling capacity of the branched GAXabsorption chiller increase with increasing generator and evaporator temperature whereasthey decrease with increasing condenser temperature. Simulation results also show that thesplit ratio and ammonia concentration difference have a significant impact on theperformance of absorption chiller.
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