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Computational Evaluation of a C-A Heat Pump

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href="https://publications.waset.org/search?q=Young-Jin%20Baik">Young-Jin Baik</a>, <a href="https://publications.waset.org/search?q=Minsung%20Kim"> Minsung Kim</a>, <a href="https://publications.waset.org/search?q=Young-Soo%20Lee"> Young-Soo Lee</a>, <a href="https://publications.waset.org/search?q=Ki-Chang%20Chang"> Ki-Chang Chang</a>, <a href="https://publications.waset.org/search?q=Seong-Ryong%20Park"> Seong-Ryong Park</a> </p> <p class="card-text"><strong>Abstract:</strong></p> The compression-absorption heat pump (C-A HP), one of the promising heat recovery equipments that make process hot water using low temperature heat of wastewater, was evaluated by computer simulation. A simulation program was developed based on the continuity and the first and second laws of thermodynamics. Both the absorber and desorber were modeled using UA-LMTD method. In order to prevent an unfeasible temperature profile and to reduce calculation errors from the curved temperature profile of a mixture, heat loads were divided into lots of segments. A single-stage compressor was considered. A compressor cooling load was also taken into account. An isentropic efficiency was computed from the map data. Simulation conditions were given based on the system consisting of ordinarily designed components. The simulation results show that most of the total entropy generation occurs during the compression and cooling process, thus suggesting the possibility that system performance can be enhanced if a rectifier is introduced. <iframe src="https://publications.waset.org/8702.pdf" style="width:100%; height:400px;" frameborder="0"></iframe> <p class="card-text"><strong>Keywords:</strong> <a href="https://publications.waset.org/search?q=Waste%20heat%20recovery" title="Waste heat recovery">Waste heat recovery</a>, <a href="https://publications.waset.org/search?q=Heat%20Pump." title=" Heat Pump."> Heat Pump.</a> </p> <p class="card-text"><strong>Digital Object Identifier (DOI):</strong> <a href="https://doi.org/10.5281/zenodo.1334712" target="_blank">doi.org/10.5281/zenodo.1334712</a> </p> <a href="https://publications.waset.org/8702/computational-evaluation-of-a-c-a-heat-pump" class="btn btn-primary btn-sm">Procedia</a> <a href="https://publications.waset.org/8702/apa" target="_blank" rel="nofollow" class="btn btn-primary btn-sm">APA</a> <a href="https://publications.waset.org/8702/bibtex" target="_blank" rel="nofollow" class="btn btn-primary btn-sm">BibTeX</a> <a href="https://publications.waset.org/8702/chicago" target="_blank" rel="nofollow" class="btn btn-primary btn-sm">Chicago</a> <a href="https://publications.waset.org/8702/endnote" target="_blank" rel="nofollow" class="btn btn-primary btn-sm">EndNote</a> <a href="https://publications.waset.org/8702/harvard" target="_blank" rel="nofollow" class="btn btn-primary btn-sm">Harvard</a> <a href="https://publications.waset.org/8702/json" target="_blank" rel="nofollow" class="btn btn-primary btn-sm">JSON</a> <a href="https://publications.waset.org/8702/mla" target="_blank" rel="nofollow" class="btn btn-primary btn-sm">MLA</a> <a href="https://publications.waset.org/8702/ris" target="_blank" rel="nofollow" class="btn btn-primary btn-sm">RIS</a> <a href="https://publications.waset.org/8702/xml" target="_blank" rel="nofollow" class="btn btn-primary btn-sm">XML</a> <a href="https://publications.waset.org/8702/iso690" target="_blank" rel="nofollow" class="btn btn-primary btn-sm">ISO 690</a> <a href="https://publications.waset.org/8702.pdf" target="_blank" class="btn btn-primary btn-sm">PDF</a> <span class="bg-info text-light px-1 py-1 float-right rounded"> Downloads <span class="badge badge-light">1720</span> </span> <p class="card-text"><strong>References:</strong></p> <br>[1] Hult茅n M, Berntsson T. "The compression/absorption cycle - influence of some major parameters on COP and a comparison with the compression cycle," Int J Refrig 1999;22:91-106. <br>[2] Itard L."Wet compression versus dry compression in heat pumps working with pure refrigerants or non-azeotropic mixtures," Int J Refrig 1995;18:495-504. <br>[3] Klein S. 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