Heat transfer and pressure drop penalization terms (exergy losses) during flow boiling of refrigerants

Author:

Steven Brown J.1,Zilio Claudio2,Brignoli Riccardo2,Cavallini Alberto2

Affiliation:

1. Department of Mechanical Engineering; The Catholic University of America; Washington, DC; 20064; USA

2. Dipartimento di Ingegneria Industriale; University of Padova; Via Venezia, 1; 35131; Padova; Italy

Publisher

Wiley

Subject

Energy Engineering and Power Technology,Fuel Technology,Nuclear Energy and Engineering,Renewable Energy, Sustainability and the Environment

Reference19 articles.

1. Investigation of flow boiling in horizontal tubes: Part II- Development of a new heat transfer model for stratified-wavy, dryout and mist flow regimes;Wojtan;International Journal of Heat and Mass Transfer,2005

2. Flow pattern based two-phase frictional pressure drop model for horizontal tubes, Part II: New phenomenological model;Moreno Quiben;International Journal of Heat and Fluid Flow,2007

3. Granryd E Optimum circuit tube length and pressure drop on the refrigerant side of evaporators Proceedings of the International Refrigeration and Air Conditioning Conference 1992

4. Cavallini A Censi G Del Col D Doretti L Rossetto L Longo GA Reduction of global warming impact in the HP/AC industry by employing new HFC refrigerants Proceedings of Clima 2000/Napoli 2001 World Congress 2001

5. A general correlation for flow boiling in tubes and annuli;Gungor;International Journal of Heat and Mass Transfer,1986

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