高温热泵的热设计和优化与丹麦的区域供热相结合,用于工艺供热:"Optimisation d'une pompe à chaleur haute température en cascade intégrée au chauffage urbain, référencée au Danemark pour l'approvisionnement en chaleur industrielle: conception thermique et sélection du fluide de travail"。

Mohsen Sadeghi, Tage Petersen, Zhenyu Yang, Benjamin Zühlsdorf, Kim Stenholdt Madsen
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引用次数: 0

摘要

这项工作旨在评估和优化与区域供热(DH)集成的级联高温热泵(HTHP)的性能,以便为工业流程生产 160°C 的 1 兆瓦蒸汽。区域供热(DH)网络一次环路中 80 ℃ 的热量被视为热源,通过 HTHP 蒸发器冷却 70 ℃ 后供应给区域供热(DH)二次环路。优化结果表明,临界温度最高的碳氢化合物戊烷是高温环路中最有希望与蒸汽配对使用的制冷剂,其 COP 最高,达到 2.66。然而,在安全和压缩机选型问题上,丁烷是一个很好的候选者;其容积加热能力(VHC)约为戊烷的两倍,而高温环路的 COP 仅降低了约 4%。此外,从理论上讲,注水可成功控制蒸汽压缩机的排气温度,在压缩机出口处仅有 0.9 K 的过热;并可将其功耗和 HTHP COP 分别降低 4.3 % 和 1.7 %。此外,技术经济分析表明,与传统的天然气锅炉和电锅炉相比,HTHP 技术具有更好的商业价值。
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Thermal design and optimization of high-temperature heat pump integrated with district heating benchmarked in Denmark for process heat supply: “Optimisation d'une pompe à chaleur haute température en cascade intégrée au chauffage urbain, référencée au Danemark pour l'approvisionnement en chaleur industrielle: conception thermique et sélection du fluide de travail”

This work aims to assess and optimize the performance of cascade high-temperature heat pump (HTHP) integrated with district heating (DH) to produce 1 MW steam at 160°C for the industrial processes. The heat available in the primary loop of the DH network at 80 °C is considered as the heat source; which is cooled down 70 °C through the HTHP evaporator, before supplying the DH secondary loop. The use of alternative hydrocarbons in the low-temperature loop are examined; and considering the gas compressor limitation, the HTHP performance of using each refrigerant is optimized and compared to each other.

The optimization results reveal that pentane- hydrocarbon with the highest critical temperature- is the most promising refrigerant to be paired with steam in the high-temperature loop, reaching the highest COP of 2.66. However, concerning safety and compressor sizing issues, butane is an excellent candidate; with volumetric heating capacity (VHC) of about two times more than that of pentane, in the expense of just about 4 % reduction in the HTHP COP. In addition, water injection theoretically controls the steam compressor discharge temperature successfully, with just 0.9 K superheating at the compressor outlet; and reduces its power consumption and the HTHP COP up to 4.3 % and 1.7 %, respectively. Moreover, techno-economic analysis demonstrates that the HTHP technology shows a better business case compared to the conventional natural gas and electric boilers.

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