气体压缩机
离心式压缩机
制冷剂
热泵
Lift(数据挖掘)
往复式压缩机
机械工程
马赫数
热力学
总压比
工程类
机械
环境科学
核工程
材料科学
热交换器
航空航天工程
物理
计算机科学
数据挖掘
作者
Ahti Jaatinen‐Värri,Juha Honkatukia,Antti Uusitalo,Teemu Turunen-Saaresti
标识
DOI:10.1016/j.applthermaleng.2023.122087
摘要
Heat pumps are identified as crucial technology for decarbonising the heat production. Especially for large-scale, high-temperature heat pumps, the use of centrifugal compressors has been seen as an attractive technological option, but there are very few detailed studies available discussing the compressor designs with different refrigerants for high-temperature heat pumps. This study combines the analyses of a 500 kW two-stage heat pump cycle and centrifugal compressor designs. The study qualitatively assesses the feasibility of compressor designs and provides information on how the dimensions, efficiency, and rotational speed are influenced by cycle conditions and the refrigerant. Temperature lift and evaporation temperature were varied with eight working fluids, including hydrocarbons and hydrofluoro-olefins. The estimated COPs were 2.0–2.55 with the highest values observed with pentane isopentane. The compressor rotational speeds were between 20 – 50 krpm with hydrocarbons requiring higher values than fluids containing fluorine. The predicted compressor efficiencies were between 77% to 84%, with low pressure compressor reaching higher efficiencies than the high-pressure compressor. However, high compressor Mach numbers were observed, and the Mach number seems to be the main obstacle for the increase of the heat pump temperature lift when centrifugal compressors are used.
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