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Optimisation of high-temperature heat pump cascades with internal heat exchangers using refrigerants with low global warming potential

机译:使用具有低全球变暖潜能的制冷剂优化带有内部热交换器的高温热泵级联

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High-temperature heat pumps (HTHPs) based on vapour compression can be used for industrial low-grade waste heat valorisation, which can aid in mitigating climate change. Currently, the performance of HTHPs operating at high-temperatures lifts is limited; therefore, advanced configurations become an opportunity for their utilisation. This paper presents an HTHP cascade with configurations of internal heat exchangers (IHXs) that uses low GWP refrigerants in both high-stage (HS) (HCFO-1233zd(E), HFO-1336mzz(Z), HCFO-1224yd(Z), and pentane) and low-stage (LS) (HFO-1234yf, HFO-1234ze(E), butane, isobutane, and propane) cycles. Prior to the analysis and presentation of results, an optimisation of the operating conditions is performed based on intermediate temperature and IHX effectiveness in both stage cycles. Results indicate that butane and isobutane appear to be the most convenient working LS fluids from the point of view of coefficient of performance (COP). The highest system performance is obtained using pentane and HFO-1336mzz(Z) in the HS cycle. Compared to third-generation refrigerants (HFC-245fa/HFC-134a), a slight COP improvement is obtained using HCFO-1233zd(E), and HCFO-1224yd(Z). A comparable or even lower volumetric flow rate at the HS compression suction is also observed. The use of pentane/butane achieved maximum COP (3.15), which is a 13% improvement compared to COP obtained when HFC-245fa/HFC-134a is employed.
机译:基于蒸汽压缩的高温热泵(HTHP)可用于工业低品位废热平衡,这有助于缓解气候变化。当前,在高温升降机上运行的HTHP的性能受到限制。因此,高级配置成为其利用的机会。本文介绍了一种具有内部热交换器(IHXs)配置的HTHP级联,该热交换器在两个高级(HS)(HCFO-1233zd(E),HFO-1336mzz(Z),HCFO-1224yd(Z),和戊烷)和低级(LS)(HFO-1234yf,HFO-1234ze(E),丁烷,异丁烷和丙烷)循环。在分析和呈现结果之前,基于两个阶段的中间温度和IHX有效性对运行条件进行优化。结果表明,从性能系数(COP)的角度来看,丁烷和异丁烷似乎是最方便的LS流体。在HS循环中使用戊烷和HFO-1336mzz(Z)可获得最高的系统性能。与第三代制冷剂(HFC-245fa / HFC-134a)相比,使用HCFO-1233zd(E)和HCFO-1224yd(Z)可使COP略有改善。还观察到在HS压缩吸力下可比甚至更低的体积流量。使用戊烷/丁烷可获得最大COP(3.15),与使用HFC-245fa / HFC-134a时获得的COP相比,提高了13%。

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