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Study on a twin-bed adsorption refrigeration system using R134a-activated carbon pair

机译:使用R134a活性炭对的双床吸附式制冷系统的研究

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摘要

A low capacity twin-bed adsorption refrigeration system has been built with R134a as a refrigerant and activated carbon as the adsorbent. Simple tube-in-tube heat exchangers have been fabricated and have been used as the adsorber beds. Activated carbon (granular type) has been filled in the annular space of the inner tube and outer tube. A plate heat exchanger has been used as the condenser and the temperature of cooling water has been maintained between 25℃ and 30℃, also the evaporator has been custom designed as per requirements. A mathematical model has also been developed and the results obtained have been found to be comparable. While operating the system in the single-bed mode a cooling power of 250.4 W has been obtained with a coefficient of performance (COP) of 0.38 with an average evaporator temperature of 18.4℃ against a predicted value of 263.7 W with a COP of 0.41. While operating in the twin-bed mode a cooling power of 281.3 W with a COP of 0.47 with an average evaporator temperature of 17.6℃ has been obtained against a predicted value of 294.5 W with a COP of 0.52.
机译:以R134a为制冷剂,活性炭为吸附剂的低容量双床吸附制冷系统已经建成。已经制造了简单的管中管式热交换器并将其用作吸附床。活性碳(颗粒状)已填充在内管和外管的环形空间中。板式换热器被用作冷凝器,冷却水的温度保持在25℃至30℃之间,蒸发器也根据要求进行了定制设计。还开发了数学模型,并且发现获得的结果是可比较的。在单床模式下运行系统时,已获得250.4 W的冷却功率,性能系数(COP)为0.38,平均蒸发器温度为18.4℃,而预测值为263.7 W,COP为0.41。在双床模式下运行时,制冷功率为281.3 W,COP为0.47,平均蒸发器温度为17.6℃,而预测值为294.5 W,COP为0.52。

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