Experimental study of convective condensation in an inclined smooth tube. Part II: Inclination effect on pressure drops and void fractions

Author:

Lips Stéphane,Meyer Josua P.

Publisher

Elsevier BV

Subject

Fluid Flow and Transfer Processes,Mechanical Engineering,Condensed Matter Physics

Reference28 articles.

1. In-tube condensation performance of refrigerants considering penalization terms (exergy losses) for heat transfer and pressure drop;Cavallini;Int. J. Heat Mass Transfer,2010

2. Prediction of two-phase pressure gradients of refrigerants in horizontal tubes;Ould Didi;Int. J. Refrig.,2002

3. A simple friction pressure drop correlation for two-phase flow in pipes;Müller-Steinhagen;Chem. Eng. Process.,1986

4. R. Grönnerud, Investigation of liquid hold-up, flow-resistance and heat transfer in circulation type evaporators. Part IV: Two-phase flow resistance in boiling refrigerants, Bull. De l’Inst. Du Froid, Annexe. 1 (1972).

5. Experimental investigation on condensation heat transfer and pressure drop of new HFC refrigerants (R134a, R125, R32, R410A, R236ea) in a horizontal smooth tube;Cavallini;Int. J. Refrig.,2001

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