综合智慧能源 ›› 2026, Vol. 48 ›› Issue (6): 68-81.doi: 10.3969/j.issn.2097-0706.2026.06.006

• 储能与调峰技术 • 上一篇    下一篇

面向工业余热回收的150 ℃高温耦合热泵性能研究

孙健(), 刘敏慧(), 胡芸蓉, 薛健豪, 胡志武, 杜小泽()   

  1. 华北电力大学 新能源电力系统全国重点实验室北京 102206
  • 收稿日期:2026-04-14 修回日期:2026-05-21 出版日期:2026-06-25
  • 作者简介:孙健(1985),男,副教授,博士,从事新型热泵及综合能源优化技术等方面的研究,s@ncepu.edu.cn
    刘敏慧(2001),女,硕士生,从事工业领域耦合热泵技术方面的研究,liuminhui0426@163.com
    杜小泽(1970),男,教授,博士生导师,从事强化传热与节能、多能互补综合能源系统等方面的研究,duxz@ncepu.edu.cn
  • 基金资助:
    国家科技计划项目(2024XAGG0022);国家自然科学基金项目(52090062)

Study on performance of a 150 ℃ high-temperature coupled heat pump for industrial waste heat recovery

SUN Jian(), LIU Minhui(), HU Yunrong, XUE Jianhao, HU Zhiwu, DU Xiaoze()   

  1. State Key Laboratory of Alternate Electrical Power System with Renewable Energy SourcesNorth China Electric Power UniversityBeijing 102206, China
  • Received:2026-04-14 Revised:2026-05-21 Published:2026-06-25
  • Supported by:
    National Science and Technology Program of China(2024XAGG0022);National Natural Science Foundation of China(52090062)

摘要:

针对现有耦合热泵缺少适配150 ℃供热工况的工质优选、热力及经济性综合分析的短板,提出了一种150 ℃压缩-吸收耦合高温热泵机组,以实现低品位余热高效提质,降低工业高温供热能耗与运行成本。基于稳态热力学方法建立系统数学模型,对高压侧单工质和低压侧二元混合工质进行筛选,分析蒸发-冷凝器温度、制热温度、余热出口温度及水蒸气压缩机压比对机组热力性能的影响,并进行经济性对比。结果表明:高压侧优选工质为反式-1-氯-3,3,3-三氟丙烯;低压侧优选混合工质为正戊烷(R601)/顺式-1,3,3,3-四氟丙烯,R601最佳摩尔分数为0.69,系统性能系数(COP)为5.16;蒸发-冷凝器温度由85 ℃升高至95 ℃时,COP由2.16降至2.02,制热量由739.29 kW增至761.26 kW;制热温度由140 ℃升高至160 ℃时,COP由2.22降至1.97,制热量由727.00 kW增至774.95 kW;余热出口温度由40 ℃升高至50 ℃时,COP由1.91升至2.14,而制热量由1 314.83 kW降至617.46 kW;水蒸气压缩机压比由1.20升高至1.70时,COP由2.14降至2.06,溴化锂浓溶液质量分数由54.16%升至58.02%,循环倍率由6.56降至4.79。在相同供热量条件下,耦合热泵系统小时运行成本分别较燃气锅炉和电锅炉降低55.6%和72.8%。研究表明,该耦合热泵机组兼具良好的热力性能与经济性,在工业中低温余热深度回收及高温供热替代方面具有较好的应用前景。

关键词: 工业余热利用, 高温热泵, 压缩-吸收耦合热泵, 混合工质, 经济性分析

Abstract:

There is insufficient research on working fluid optimization, thermodynamic characteristics and economic performance analysis of existing coupled heat pumps providing 150 ℃ heat supply. Therefore, a 150 ℃ compression-absorption coupled high-temperature heat pump unit was proposed, to improve the utilization rate of low-temperature waste heat, lower the energy consumption in industrial high-temperature heat supply and decrease the operational costs of the unit. A system mathematical model was established based on steady-state thermodynamics, and pure working fluids on the high-pressure side and binary mixed working fluids on the low-pressure side were screened. The effects of evaporator-condenser temperature, heating temperature, waste heat outlet temperature, and compression ratio of the water vapor compressor on the thermodynamic performance of the unit were analyzed, and comparison of economic efficiency was conducted. The results showed that the optimal working fluid on the high-pressure side was trans-1-chloro-3,3,3-trifluoropropene, the optimal mixed working fluid on the low-pressure side was n-Pentane(R601)/cis-1,3,3,3-tetrafluoropropene, the optimal mole fraction of R601 was 0.69, and the coefficient of performance (COP) of the system was 5.16. When the evaporator-condenser temperature increased from 85 ℃ to 95 ℃, the COP decreased from 2.16 to 2.02, while the heating capacity increased from 739.29 kW to 761.26 kW. When the heating temperature increased from 140 ℃ to 160 ℃, the COP decreased from 2.22 to 1.97, while the heating capacity increased from 727.00 kW to 774.95 kW. When the waste heat outlet temperature increased from 40 ℃ to 50 ℃, the COP increased from 1.91 to 2.14, while the heating capacity decreased from 1 314.83 kW to 617.46 kW. When the compression ratio of the water vapor compressor increased from 1.20 to 1.70, the COP decreased from 2.14 to 2.06, the mass fraction of concentrated lithium bromide solution increased from 54.16% to 58.02%, and the circulation ratio decreased from 6.56 to 4.79. Under the same heating capacity, the hourly operating cost of the coupled heat pump system was reduced by 55.6% and 72.8% compared to gas boilers and electric boilers, respectively. The findings indicate that the coupled heat pump unit shows good thermodynamic performance and economic efficiency, and has promising application prospects in deep recovery of industrial medium- and low-temperature waste heat and substitution for high-temperature heat supply.

Key words: industrial waste heat utilization, high-temperature heat pump, compression-absorption coupled heat pump, mixed working fluid, economic analysis