2014
DOI: 10.1016/j.ijrefrig.2014.04.006
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Preliminary experimental results on the R134a refrigeration system using a two-phase ejector as an expander

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Cited by 69 publications
(13 citation statements)
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“…The maximum COP and the second law efficiency are approximately 7% and 5% higher than those of the conventional cycle. Ersoy and Bilir Sag [187] tested a R124a EERS and, depending on the operating condition, the COP was 6.2-14.5% higher than that of the conventional system. Bilir Sag et al [182] (experimental study using R134a) reported an increase of COP by 7.34-12.87% and an increase of the exergy efficiency of 6.6-11.24% compared to a conventional system.…”
Section: Ejector Expansion Refrigeration System (Eers)mentioning
confidence: 98%
“…The maximum COP and the second law efficiency are approximately 7% and 5% higher than those of the conventional cycle. Ersoy and Bilir Sag [187] tested a R124a EERS and, depending on the operating condition, the COP was 6.2-14.5% higher than that of the conventional system. Bilir Sag et al [182] (experimental study using R134a) reported an increase of COP by 7.34-12.87% and an increase of the exergy efficiency of 6.6-11.24% compared to a conventional system.…”
Section: Ejector Expansion Refrigeration System (Eers)mentioning
confidence: 98%
“…Another comparison for R1234yf with Li et al [14] shows that for component efficiency η m = 95% (others are same), the deviation maximum COP (5.979 in present study and 5.94 in previous study [14]) is about 1%. The code has been also validated with experimental data for R134a [21]. For the condenser temperature at 53.28 • C, and evaporator temperature at 8.67 • C with 12 • C superheat, and 79% compressor isentropic efficiency (calculated based on test data), the entrainment ratio (0.64 experimental and 0.671 predicted) and area ratio (5.35 experimental and 5.93 predicted) are deviated by 4.7% and 9.8%, respectively.…”
Section: Resultsmentioning
confidence: 99%
“…Concerning two-phase operation, comparisons were made regarding the choked mass flow through a convergent divergent nozzle and the effect of the primary inlet saturation on the entrainment ratio. Figure 5 compares the predicted entrainment ratio values against experimental data from different studies [8,10,24,[34][35][36] with varying dimensions, working gases and operating conditions. As a first step, friction and mixing losses are neglected here such that:…”
Section: Validation Of the Thermodynamic Modelmentioning
confidence: 99%