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Experimental results of an absorption-compression heat pump using the working fluid ammonia/water for heat recovery in industrial processes

机译:使用工作流体氨/水进行吸收压缩热泵的实验结果,用于工业过程中热回收

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The full potential of hybrid absorption-compression heat pumps, which can cover heating demands at temperatures of around 100 degrees C and provide additional cooling in industrial processes, has yet to be exploited. Although research has also been conducted on alternative systems, the natural working pair NH3 and H2O still has numerous advantages, being a very economic and thermodynamically well-suited refrigerant for this application. Striving for the development of a heat pump system that can cover a large range of heating demands at a temperature of about 80 degrees C and create useful cooling power in industrial processes, a test rig was designed and built at the Institute for Thermodynamics at the Leibniz University in Hanover. According to the targeted heating power of 50 kW, the components of the system are chosen based on a simulation model that solves mass, energy and component-specific balance equations for each of the parts simultaneously. This simulation is later used to compare and evaluate experimental data. Constant parameters are water-inlet temperatures at the heat source of 59 degrees C and at the heat sink of 50 degrees C. Depending on the mass flow of ammonia-poor solution and the condensation pressure, the heating capacity and the COP of the test rig are investigated. The range of the poor solution mass flow is from 0.21 kg/s to 0.31 kg/s, while the absorption pressure is varied between 13.5 bar and 16.5 bar. The COP of heating reaches a maximum of 2.5, providing more than 40 kW of heating power at a maximum internal temperature lift of 43 K. (C) 2018 Elsevier Ltd and IIR. All rights reserved.
机译:混合吸收压缩热泵的全部电位,可以在大约100摄氏度的温度下覆盖加热需求并在工业过程中提供额外的冷却,尚未被利用。尽管在替代系统上也进行了研究,但自然工作对NH3和H2O仍然具有许多优势,是这种应用的非常经济和热力学良好的制冷剂。追求一种热泵系统,可以在大约80摄氏度的温度下覆盖大范围的加热需求,并在工业过程中创造有用的冷却功率,在莱布尼兹的热力学研究所设计和建造了试验台汉诺威大学。根据50 kW的目标加热功率,基于仿真模型选择系统的组件,该模拟模型同时为每个部件求解质量,能量和特定于元件的平衡方程。此模拟后来用于比较和评估实验数据。恒定参数是在59摄氏度的热源和50摄氏度的散热器处的水入口温度。根据氨溶液的质量流量和冷凝压力,加热容量和试验台的COP调查。较差的溶液质量流量的范围为0.21kg / s至0.31kg / s,而吸收压力在13.5巴和16.5巴之间变化。加热的COP最多达到2.5,在最大内部温度升降机为43 K.(c)2018 Elsevier Ltd和IIR,提供超过40kW的加热功率。版权所有。

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