2011•Unpublished venueRequires access

Heat transfer correlations of forced convective boiling for pure refrigerants in micro-fin tubes

Yuanlin ChangHua

Open publisher page 0 citations

Abstract

The evaporation heat transfer coefficient of pure refrigerants R-22 and R-124 in micro-fin tubes were measured at the reduced pressure of 0.15, the mass flux from 100 to 400 kg/m 2 s, the flow quality from 0.1 to 0.9, and the heat flux from 5 to 20 kW/m 2 . The evaporation heat transfer coefficient of pure refrigerant in micro-fin tube is 1.5e3.0 times higher than that of smooth tube. In this article, the single phase forced convection heat transfer coefficient of micro-fin tube is introduced to predict the evaporation heat transfer coefficient of pure refrigerant in micro-fin tubes. The present correlations provide reasonable agreement with the experimental data. The prediction values mostly fall within � 30%.

About this research paper

What this paper is about

The evaporation heat transfer coefficient of pure refrigerants R-22 and R-124 in micro-fin tubes were measured at the reduced pressure of 0.15, the mass flux from 100 to 400 kg/m 2 s, the flow quality from 0.1 to 0.9, and the heat flux from 5 to 20 kW/m 2 . The evaporation heat transfer coefficient of pure refrigerant in micro-fin tube is 1.5e3.0 times higher than that of smooth tube. In this article, the single phase forced convection heat transfer coefficient of micro-fin tube is introduced to predict the evaporation heat transfer coefficient of pure refrigerant in micro-fin tubes. The present correlations provide reasonable agreement with the experimental data. The prediction values mostly fall within � 30%.

Why it matters

A significance statement is not available in the OpenAlex record.

Key contribution

A contribution statement is not available in the OpenAlex record.

Method / approach

Method details are not available in the OpenAlex metadata.

Main findings

Findings are not separately available in the OpenAlex metadata.

Limitations

Limitations are not available in the OpenAlex metadata.

Applications

Application details are not available in the OpenAlex metadata.

Available abstract

The evaporation heat transfer coefficient of pure refrigerants R-22 and R-124 in micro-fin tubes were measured at the reduced pressure of 0.15, the mass flux from 100 to 400 kg/m 2 s, the flow quality from 0.1 to 0.9, and the heat flux from 5 to 20 kW/m 2 . The evaporation heat transfer coefficient of pure refrigerant in micro-fin tube is 1.5e3.0 times higher than that of smooth tube. In this article, the single phase forced convection heat transfer coefficient of micro-fin tube is introduced to predict the evaporation heat transfer coefficient of pure refrigerant in micro-fin tubes. The present correlations provide reasonable agreement with the experimental data. The prediction values mostly fall within � 30%.

Key concepts: Heat transfer coefficient, Refrigerant, Fin, Thermodynamics, Evaporation, Heat flux, Materials science, Heat transfer

Related papers

Back to paper searchBrowse research topicsOriginal source
Heat transfer correlations of forced convective boiling for pure refrigerants in micro-fin tubes — Research Paper | ScholarLens