2013
DOI: 10.1016/j.ijrefrig.2012.09.017
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Theoretical study on a novel R32 refrigeration cycle with a two-stage suction ejector

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Cited by 43 publications
(12 citation statements)
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“…The evaporating temperature of the evaporator t e varies from À30 to 5°C, and the superheating degree for the evaporator Dt e is set at zero; The isentropic efficiency of the compressor is assumed to be g s ¼ 0:75 [31]. For the simplicity, the ejector isentropic efficiencies are assumed to be g n ¼ 0:9, g m ¼ 0:85 and g d ¼ 0:8 [32]. It should be noted that in the following simulations the cycle performances are evaluated on per unit of mass at the compressor suction inlet.…”
Section: Resultsmentioning
confidence: 99%
“…The evaporating temperature of the evaporator t e varies from À30 to 5°C, and the superheating degree for the evaporator Dt e is set at zero; The isentropic efficiency of the compressor is assumed to be g s ¼ 0:75 [31]. For the simplicity, the ejector isentropic efficiencies are assumed to be g n ¼ 0:9, g m ¼ 0:85 and g d ¼ 0:8 [32]. It should be noted that in the following simulations the cycle performances are evaluated on per unit of mass at the compressor suction inlet.…”
Section: Resultsmentioning
confidence: 99%
“…No improvement was found under extreme cooling and heating conditions. Yu et al [63] proposed a new ejector enhanced vapour compression refrigeration cycle ( Figure 7) operating with refrigerant R32, which improves the COPh and volumetric capacity by more than [8.8, 9.3]% and [13.6, 9.7]%, respectively. Finally, the use of an internal heat exchanger (IHX) is not recommended for R32 because it reduces the COPc and increases the discharge temperature, even though this component can enlarge the energy efficiency for some of its mixtures, as with R407C or R410A [64].…”
Section: Performance and Discharge Temperature Concern Of Pure R32mentioning
confidence: 99%
“…Under stable primary and secondary flow conditions and optimum geometrical parameters, a pressure recovery of over 32.8% was achieved with the adjustable ejector (Lino et al, 2012). Yu et al (2013) presented a cycle operating with an ejector system with two suction inlets to recover the expansion losses. MEJ 3 in Table 5 illustrates the developed cycle.…”
Section: Multiple Ejector Cyclesmentioning
confidence: 99%