Nowadays, the minimization of the refrigerant charge in refrigerating and air conditioning equipment is an important issue for the new environmental challenges. This paper presents R134a flow boiling heat transfer and pressure drop measurements inside a small microfin tube with internal diameter of 3.4 mm. This study is carried out in a new experimental facility built at the Dipartimento di Ingegneria Industriale of the University of Padova especially designed to study both single and two phase heat transfer processes in micro structured surfaces. The microfin tube was brazed inside a copper plate and electrically heated from the bottom by means of a wire resistance. Several T-type thermocouples were inserted in the wall to measure the temperature distribution during the phase change process. In particular, the experimental measurements were carried out at constant saturation temperature of 30 °C, by varying the refrigerant mass velocity between 190 kg m-2 s-1 and 940 kg m-2 s-1, the vapour quality from 0.2 to 0.95 at three different heat fluxes 10, 25, and 50 kW m-2. The experimental results are presented in terms of two-phase heat transfer coefficient, onset of dryout vapour quality, and frictional pressure drop as a function of the operative test conditions.
Experimental Measurements of R134a Flow Boiling Inside a 3.4 mm ID Microfin Tube
MANCIN, SIMONE;DIANI, ANDREA;ZILIO, CLAUDIO;ROSSETTO, LUISA
2013
Abstract
Nowadays, the minimization of the refrigerant charge in refrigerating and air conditioning equipment is an important issue for the new environmental challenges. This paper presents R134a flow boiling heat transfer and pressure drop measurements inside a small microfin tube with internal diameter of 3.4 mm. This study is carried out in a new experimental facility built at the Dipartimento di Ingegneria Industriale of the University of Padova especially designed to study both single and two phase heat transfer processes in micro structured surfaces. The microfin tube was brazed inside a copper plate and electrically heated from the bottom by means of a wire resistance. Several T-type thermocouples were inserted in the wall to measure the temperature distribution during the phase change process. In particular, the experimental measurements were carried out at constant saturation temperature of 30 °C, by varying the refrigerant mass velocity between 190 kg m-2 s-1 and 940 kg m-2 s-1, the vapour quality from 0.2 to 0.95 at three different heat fluxes 10, 25, and 50 kW m-2. The experimental results are presented in terms of two-phase heat transfer coefficient, onset of dryout vapour quality, and frictional pressure drop as a function of the operative test conditions.Pubblicazioni consigliate
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