Summary
Two-phase frictional pressure drop characteristics of an R-410A/oil mixture flow boiling inside a straight, smooth tube with an outside diameter of 7.0 mm were investigated experimentally. Experimental parameters include an evaporation temperature of 5°C, mass fluxes from 200 to 400 kg/(m2.s), heat fluxes from 7.56 to 15.12 kW/m2, inlet vapour qualities from 0.2 to 0.7, and nominal oil concentrations from 0 to 5%. The test results show that frictional pressure drop of an R-410A/oil mixture increases with the mass flux, the presence of oil enhances two-phase frictional pressure drop, and the effect of oil on frictional pressure drop is found to be more evident at higher vapour qualities where the local oil concentrations are higher. A new correlation to predict the local frictional pressure drop of an R-410A/oil mixture flow boiling inside a straight, smooth tube is developed based on the local properties of the refrigerant/oil mixture, and it agrees with 92% of the experimental data within a deviation of plus or minus 15%.
Details
- Original title: Measurement and correlation of frictional pressure drop of R-410A/oil mixture flow boiling in a 7 mm straight smooth tube.
- Record ID : 2008-2435
- Languages: English
- Source: HVAC&R Research - vol. 14 - n. 5
- Publication date: 2008/09
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Indexing
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Themes:
Heat transfer;
Lubricants;
Blends - Keywords: R410A; Horizontal tube; Correlation; Bare pipe; Mixture; Oil; Expérimentation; Flow; Refrigerant; Boiling; Pressure drop
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