2020
DOI: 10.1016/j.applthermaleng.2020.115022
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Numerical investigation on vapor-liquid two-phase compression in the cylinder of rotary compressors

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Cited by 20 publications
(6 citation statements)
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“…10 ). Both variations of the pressure and the liquid mass flow rate have two peaks, which is consistent with the experimental results in the literature 11 . In general, even with high initial liquid volume fraction, the maximum pressure in the cylinder during liquid compression process for the rotary is small and does not exceed 3 times the discharge pressure.…”
Section: Resultssupporting
confidence: 91%
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“…10 ). Both variations of the pressure and the liquid mass flow rate have two peaks, which is consistent with the experimental results in the literature 11 . In general, even with high initial liquid volume fraction, the maximum pressure in the cylinder during liquid compression process for the rotary is small and does not exceed 3 times the discharge pressure.…”
Section: Resultssupporting
confidence: 91%
“…10). Both variations of the pressure and the liquid mass flow rate have two peaks, which is consistent with the experimental results in the literature 11 .…”
Section: Effect Of Initial Liquid Volume Fraction On Two-phase Compre...supporting
confidence: 91%
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“…Amongst the replacement refrigerants with low GWP, R290 was found to have the best performance [182] and in an investigation on two-phase compression in the event of liquid slugging [183], R290 also had the least detrimental effect on the compressor due to the large difference in its specific volume between the liquid and vapor phases. Extensive research on the performance of the rolling piston compressor with R290 was thus carried out, which included transient start-up investigations [93,94], and effects of component deformation [103] in lieu of the associated higher operating pressures.…”
Section: Refrigerantsmentioning
confidence: 99%
“…20 At high IVFR, the fluid inhaled into the suction chamber contained liquid droplets that would enhance the heat transfer between the fluid and chamber walls. Nevertheless, as the quality of the two-phase fluid was close to 1 and the two-phase fluid was assumed to be homogeneous, the single-phase heat transfer coefficients between refrigerant and chamber walls 20,22,23 were adopted in our heat transfer model. The two-phase mixture properties were used for calculating the heat transfer coefficients.…”
Section: Mathematic Modelmentioning
confidence: 99%