以活性炭-乙醇为工作对的吸附制冷系统研究

I. M. Astina, R. Sokha, P. Darmanto
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引用次数: 3

摘要

吸附式制冷系统是一种热源驱动的替代制冷系统,可以利用余热和太阳能。本文报道了乙醇-活性炭(AC)作为吸附剂对的实验。实验采用两层吸附床作为热压缩机。当散热器温度分别为200℃、25℃和30℃时,乙醇- ac对可在热源温度为90℃和1000℃时工作。实验结果表明,当热水温度为1000℃,冷却水温度为30℃时,系统的性能系数(COP)高于其他测试工况。此外,由于手动间歇操作两个吸附层,系统的COP在长时间运行时平均为0.19。当吸附床解吸温度为85℃、解吸压力为85.52 kPa、加热时间为80 min时,最大吸附量为0.302 kg/kg·AC,一个运行周期的制冷量为23.61 kJ。实验结果表明,乙醇- ac是一种适合与吸附系统配套使用的冷却系统。它可以在低温驱动热源下工作,并且具有环保行为,并且工作对易于在商业市场上找到。
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Study on Adsorption Refrigeration System Using Activated Carbon-Ethanol as Working Pair
The adsorption refrigeration system is an alternative refrigeration system powered by thermal source so that it is possible to use waste heat and solar energy. This paper reports the experiment of the ethanol-activated carbon (AC) as the adsorbateadsorbent pair. Experimental work was conducted with two adsorption beds as thermal compressor. Ethanol-AC pair can be operated with the heat source temperatures 90o C and 100o C for different heat sink temperature 20o C, 25o C and 30o C, respectively. The experimental result shows when temperature of the hot water 100o C and the cooling water temperature 30o C, the system give the higher coefficient of performance (COP) than another testing operation condition. Additionally, the COP of the system is varying a long operating in average 0.19 due to manually intermittent operation of both adsorption beds. The maximum adsorption capacity is 0.302 kg/kg·AC while the desorption temperature, desorption pressure and heating time of the adsorption bed are 85o C, 85.52 kPa and 80 minutes, respectively, and the cooling capacity is 23.61 kJ for a operating cycle. The experimental result proved that the ethanol-AC is suitable pair with the adsorption system for cooling application. It can be operated at low temperature driven heat source, and has an environmentally friendly behavior and the working pair is easy to be found in the commercial market.
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