A parametric study on energy exergy and exergoeconomic assessments of a modified auto-cascade refrigeration cycle supported by a dual evaporator refrigerator
| dc.contributor.author | Ibrahim Karacayli | |
| dc.contributor.author | Lutfiye Altay | |
| dc.contributor.author | A. Hepbasli | |
| dc.contributor.author | Karacayli, Ibrahim | |
| dc.contributor.author | Hepbasli, Arif | |
| dc.contributor.author | Altay, Lutfiye | |
| dc.date.accessioned | 2025-10-06T17:48:59Z | |
| dc.date.issued | 2024 | |
| dc.description.abstract | This paper presents an evaluation of the energetic exergetic and exergoeconomic performances of a modified auto-cascade refrigeration (MACR) cycle integrated with a dual evaporator refrigerator (DER) to determine optimum operating conditions. DER facilitates a reduction in the compression ratio allowing the low-boiling-point component to release more heat before entering the evaporator. In this study the R170/R290 refrigerant mixture which has a low global warming potential but an explosion risk was used. The main purpose of this study is to eliminate the risk of explosion by reducing the compressor discharge temperature and at the same time to enhance the overall cycle performance. To achieve this DER is used instead of air-cooled coils which have limited cooling performance. Despite an ambient temperature of 35°C the MACR cycle achieved a remarkable 51.29 % reduction in compressor discharge temperature when the separator inlet temperature was reduced to 10°C by the DER. It also results in a 72.73% reduction in compression work rate and a significant 137.02% increase in cooling effect compared to the conventional auto-cascade refrigeration cycle. Furthermore the MACR cycle exhibits notable improvements in total exergy destruction rate and exergy destruction cost rate with a 75.23% and a 76.07% reduction respectively. Simultaneously the exergy efficiency and the exergoeconomic factor increased by 266.67% and 179.15% respectively. The MACR cycle achieves optimum energy and exergy performance with a 60% R170 mass fraction and 0.50 vapor quality resulting in 1.429kW compression work rate a COP of 0.70 and an exergy efficiency of 26.66 %. The optimum exergoeconomic performance is achieved with a 40% R170 mass fraction and 0.50 vapor quality. © 2024 Elsevier B.V. All rights reserved. | |
| dc.description.sponsorship | The main objective of this study is to develop a modified ACR cycle supported by DER, referred to as MACR cycle. In this study, a DER was implemented to reduce the temperature of the binary refrigerant mixture at the inlet of the separator. The DER is employed to condense a binary refrigerant mixture, whose temperature is lowered by an air-cooled condenser, and to cool the low-boiling-point component as it enters the separator. This approach allows for an increased heat extraction from the primary cycle and offers the flexibility to deactivate the DER in situations where ambient air temperatures drop too low.The modified ACR cycle, known as MACR, includes an IHE supported by a DER. The components of the MACR cycle, as illustrated in Fig. 1(a), include a compressor (I), an air-cooled heat exchanger (AHE) (II), a condenser (III), a separator (IV), four expansion valves (EV1, EV2, EV3 and EV4), a cascade heat exchanger (CHE) (VI), an IHE (VII), an evaporator (IX), an auxiliary compressor (X), and an auxiliary condenser (XI). The distinction between the MACR and ACR cycles, as depicted in Fig. 1(b)–is the incorporation of the DER. This addition serves to lower the separator inlet temperature of the binary refrigerant mixture at high pressure and temperature, irrespective of the outdoor temperature, and it enhances the cooling effect by reducing the temperature of the low-boiling-point component.This study presents energy, exergy, and exergoeconomic analyses of the MACR cycle, which is supported by the DER, and operates with a binary refrigerant mixture of R170/R290 at an outdoor temperature of 35 °C. It also examines the effects of design parameters, such as separator inlet temperature, vapor quality at the separator inlet, and the mass fraction of R170 on various performance metrics, including compressor discharge temperature, total compression work rate, cooling effect, COP, exergy destruction rate, unit cost of cooling, exergy destruction cost rate, total product cost rate, and exergoeconomic factor. These analyses were performed for vapor qualities ranging from 0.40 to 0.60. The separator inlet temperature was reduced from 40 °C to 10 °C by the DER. Subsequently, these analyses were repeated while varying the mass fraction of the low-boiling-point component in the mixture between 0.40 and 0.60. | |
| dc.description.sponsorship | College of Pharmacy, COP, (0.60); Department of Environment Regulation, Government of Western Australia, DER, (R170/R290) | |
| dc.identifier.doi | 10.1016/j.energy.2024.130255 | |
| dc.identifier.isbn | 0080319424, 0080328016, 0080340016, 0080311202, 0080305326, 0080316549, 008032780X, 9780080327808 | |
| dc.identifier.issn | 03605442, 18736785 | |
| dc.identifier.issn | 0360-5442 | |
| dc.identifier.issn | 1873-6785 | |
| dc.identifier.scopus | 2-s2.0-85183531980 | |
| dc.identifier.uri | https://www.scopus.com/inward/record.uri?eid=2-s2.0-85183531980&doi=10.1016%2Fj.energy.2024.130255&partnerID=40&md5=58f2d6ab6555eea9bac6331d72ecf53f | |
| dc.identifier.uri | https://gcris.yasar.edu.tr/handle/123456789/8226 | |
| dc.identifier.uri | https://doi.org/10.1016/j.energy.2024.130255 | |
| dc.language.iso | English | |
| dc.publisher | Elsevier Ltd | |
| dc.relation.ispartof | Energy | |
| dc.rights | info:eu-repo/semantics/closedAccess | |
| dc.source | Energy | |
| dc.subject | Auto-cascade Refrigeration, Compressor Discharge Temperature, Dual Evaporator Refrigeration, Exergoeconomic, Exergy Destruction Cost Rate, Exergy Destruction Rate | |
| dc.subject | Exergoeconomic | |
| dc.subject | Exergy Destruction Cost Rate | |
| dc.subject | Auto-Cascade Refrigeration | |
| dc.subject | Compressor Discharge Temperature | |
| dc.subject | Dual Evaporator Refrigeration | |
| dc.subject | Exergy Destruction Rate | |
| dc.title | A parametric study on energy exergy and exergoeconomic assessments of a modified auto-cascade refrigeration cycle supported by a dual evaporator refrigerator | |
| dc.type | Article | |
| dspace.entity.type | Publication | |
| gdc.author.id | Altay, Lutfiye/0000-0003-4946-3615 | |
| gdc.author.id | Karacayli, Ibrahim/0000-0002-4459-1450 | |
| gdc.author.scopusid | 55131010100 | |
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| gdc.author.wosid | Karacayli, Ibrahim/L-9871-2017 | |
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| gdc.description.department | ||
| gdc.description.departmenttemp | [Karacayli, Ibrahim] Ege Univ, Grad Sch Nat & Appl Sci, TR-35100 Bornova, Izmir, Turkiye; [Altay, Lutfiye] Ege Univ, Fac Engn, Dept Mech Engn, TR-35100 Bornova, Izmir, Turkiye; [Hepbasli, Arif] Yasar Univ, Fac Engn, Dept Energy Syst Engn, TR-35100 Bornova, Izmir, Turkiye | |
| gdc.description.publicationcategory | Makale - Uluslararası Hakemli Dergi - Kurum Öğretim Elemanı | |
| gdc.description.startpage | 130255 | |
| gdc.description.volume | 291 | |
| gdc.description.woscitationindex | Science Citation Index Expanded | |
| gdc.identifier.openalex | W4391001540 | |
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| gdc.oaire.keywords | Exergoeconomic | |
| gdc.oaire.keywords | Exergy Destruction Rate | |
| gdc.oaire.keywords | Exergy Destruction Cost Rate | |
| gdc.oaire.keywords | Compressor Discharge Temperature | |
| gdc.oaire.keywords | Dual Evaporator Refrigeration | |
| gdc.oaire.keywords | Auto-Cascade Refrigeration | |
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| gdc.virtual.author | Hepbaşli, Arif | |
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| person.identifier.scopus-author-id | Karacayli- Ibrahim (57209641127), Altay- Lutfiye (57194034206), Hepbasli- A. (55131010100) | |
| project.funder.name | The main objective of this study is to develop a modified ACR cycle supported by DER referred to as MACR cycle. In this study a DER was implemented to reduce the temperature of the binary refrigerant mixture at the inlet of the separator. The DER is employed to condense a binary refrigerant mixture whose temperature is lowered by an air-cooled condenser and to cool the low-boiling-point component as it enters the separator. This approach allows for an increased heat extraction from the primary cycle and offers the flexibility to deactivate the DER in situations where ambient air temperatures drop too low.The modified ACR cycle known as MACR includes an IHE supported by a DER. The components of the MACR cycle as illustrated in Fig. 1(a) include a compressor (I) an air-cooled heat exchanger (AHE) (II) a condenser (III) a separator (IV) four expansion valves (EV1 EV2 EV3 and EV4) a cascade heat exchanger (CHE) (VI) an IHE (VII) an evaporator (IX) an auxiliary compressor (X) and an auxiliary condenser (XI). The distinction between the MACR and ACR cycles as depicted in Fig. 1(b)–is the incorporation of the DER. This addition serves to lower the separator inlet temperature of the binary refrigerant mixture at high pressure and temperature irrespective of the outdoor temperature and it enhances the cooling effect by reducing the temperature of the low-boiling-point component.This study presents energy exergy and exergoeconomic analyses of the MACR cycle which is supported by the DER and operates with a binary refrigerant mixture of R170/R290 at an outdoor temperature of 35 °C. It also examines the effects of design parameters such as separator inlet temperature vapor quality at the separator inlet and the mass fraction of R170 on various performance metrics including compressor discharge temperature total compression work rate cooling effect COP exergy destruction rate unit cost of cooling exergy destruction cost rate total product cost rate and exergoeconomic factor. These analyses were performed for vapor qualities ranging from 0.40 to 0.60. The separator inlet temperature was reduced from 40 °C to 10 °C by the DER. Subsequently these analyses were repeated while varying the mass fraction of the low-boiling-point component in the mixture between 0.40 and 0.60. | |
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