4.7 Article

Experimental studies on absorption-compression hybrid refrigeration system using 1,1,1,2-tetrafluoroethane/tetraethylene glycol dimethyl ether as working pair

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APPLIED THERMAL ENGINEERING
卷 223, 期 -, 页码 -

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PERGAMON-ELSEVIER SCIENCE LTD
DOI: 10.1016/j.applthermaleng.2023.120001

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Experimental investigation; Absorption-compression; Organic absorbent; Low-grade heat source

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The feasibility of combining novel halogenated hydrocarbon-based working pairs with low-pressure compression-assisted absorption refrigeration system (LCARS) was proven by experimental analysis. A prototype of the hybrid refrigeration system with the capacity of 1 kW was designed and tested using R134a-DMETEG as the working pair, demonstrating improved performance in LCARS compared to the single-stage absorption refrigeration system (SSARS). The study showed that LCARS increased the coefficient of performance (COP) by up to 91.04% and efficiently utilized lower-grade heat sources, offering a feasible technical approach for the application of absorption systems in safety-critical and lightweight scenarios.
The feasibility of combining novel halogenated hydrocarbon-based working pairs with low-pressure compres-sion-assisted absorption refrigeration system (LCARS) was proved for the first time from the experimental perspective. An experimental prototype of the absorption-compression hybrid refrigeration system with a 1 kW cooling capacity was designed and tested to explore actual performances of selected R134a-DMETEG and per-formance improvements from compression in LCARS. At an evaporation temperature of approximately 5 degrees C, as the hot water inlet temperature and the solution flow rate change from 75 to 95 degrees C and 1.2-2.7 L/min, respectively, the coefficient of performance (COP) in the single-stage absorption refrigeration system (SSARS) varies from 0.211 to 0.412. At an increased evaporation temperature of approximately 10 degrees C, as the hot water inlet temperature and flow rate increase from 70 to 80 degrees C and 1.18-2.89 L/min, respectively, the COP in the SSARS varies from 0.238 to 0.552, while the COP in LCARS is improved and varies from 0.470 to 0.617. The LCARS increases the COP by a maximum of 91.04 % and can utilize a lower-grade heat source more efficiently due to its higher optimal COP at reduced hot water inlet temperatures. This study provided one feasible technical approach of combined use of R134a-DMETEG and LCARS to make up for the application limitations of traditional working pairs, contributing to application promotions of absorption systems, especially for the occasions with high requirement on safety and lightweight.

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