使用环保制冷剂的高温双级亚临界热泵

Paweł Obstawski, Krzysztof Tomczuk
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摘要

本文介绍了一种在空气-水系统中运行并使用环保制冷剂的双级亚临界压缩机热泵的设计。该热泵专用于有高温中央供暖系统的建筑,并使用壁挂式散热器作为热接收器。该设备的第一级使用 R290 制冷剂,第二级使用 R1234 ze(E) 制冷剂。该设备的额定加热能力为 10 千瓦,低源温度范围为 -20÷10 °C。对机组的制冷系统进行了设计,并进行了模拟试验,以确定机组在低源温度为-20 ÷10 °C、第一级制冷剂冷凝温度为 20 °C、25 °C、30 °C、第二级制冷剂冷凝温度为 30 ÷60 °C时的运行参数。性能系数(COP)值是根据第一和第二阶段产生的热量与消耗的电量来确定的,根据运行参数的不同,其值在 2.55 至 5.6 之间。根据运行参数的不同,COP 值在 1.5 至 2.9 之间。研究发现,通过无级调节 I 级和 II 级压缩机的容积效率,可以使 I 级的制热能力与 II 级的制冷能力相匹配,从而将 COP 值提高 50%。
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High-Temperature Two-Stage Subcritical Heat Pump Running on Environmentally Friendly Refrigerants
The paper presents the design of a two-stage subcritical compressor heat pump operating in an air-to-water system and running on environmentally friendly refrigerants. The pump is dedicated to buildings where there is a high-temperature central heating system and wall-mounted radiators are used as heat receivers. The first stage of the unit was supplied with R290 refrigerant and the second stage with R1234 ze(E) refrigerant. The nominal heating capacity of the unit is 10 kW for a lower source temperature in the range -20÷10 °C. The unit›s refrigeration system was designed and simulation tests were carried out to determine the unit›s operating parameters for the lower source temperature in the range -20÷10 °C, the condensation temperature of the stage I refrigerant for values: 20 °C, 25 °C, 30 °C and the condensation temperature of the stage II refrigerant in the range 30÷60 °C. The value of the coefficient of performance (COP) was determined in relation to the heating capacity generated in stages I and II to the electricity consumed, which value, depending on the operating parameters, ranges from 2.55 to 5.6. The value of the COP related to the heating capacity received from the stage II condenser to the total capacity consumed by the stage I and II compressor, depending on the operating parameters, ranges from 1.5 to 2.9. It was found that by using a stepless adjustment of the volumetric efficiency of the stage I and II compressor, it is possible to match the heating capacity of stage I to the cooling capacity of stage II and thus increase the COP value by 50%.
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