Experimental study of convective condensation in an inclined smooth tube. Part II: Inclination effect on pressure drops and void fractions
- 1 January 2012
- journal article
- Published by Elsevier in International Journal of Heat and Mass Transfer
- Vol. 55 (1-3) , 405-412
Abstract
No abstract availableKeywords
Funding Information
- National Research Foundation
- Council for Scientific and Industrial Research, South Africa
This publication has 21 references indexed in Scilit:
- In-tube condensation performance of refrigerants considering penalization terms (exergy losses) for heat transfer and pressure dropInternational Journal of Heat and Mass Transfer, 2010
- Comparison of frictional pressure drop models during annular flow condensation of R600a in a horizontal tube at low mass flux and of R134a in a vertical tube at high mass fluxInternational Journal of Heat and Mass Transfer, 2010
- Flow pattern based two-phase frictional pressure drop model for horizontal tubes, Part II: New phenomenological modelInternational Journal of Heat and Fluid Flow, 2007
- Flow pattern based two-phase frictional pressure drop model for horizontal tubes. Part I: Diabatic and adiabatic experimental studyInternational Journal of Heat and Fluid Flow, 2007
- Pressure Drop During Refrigerant Condensation Inside Horizontal Smooth, Helical Microfin, and Herringbone Microfin TubesJournal of Heat Transfer, 2004
- Prediction of two-phase pressure gradients of refrigerants in horizontal tubesInternational Journal of Refrigeration, 2002
- Experimental investigation on condensation heat transfer and pressure drop of new HFC refrigerants (R134a, R125, R32, R410A, R236ea) in a horizontal smooth tubeInternational Journal of Refrigeration, 2001
- Turbulent film condensation of high pressure steam in a vertical tubeInternational Journal of Heat and Mass Transfer, 2000
- Heat transfer and pressure drop during condensation of refrigerants inside horizontal enhanced tubesInternational Journal of Refrigeration, 2000
- A simple friction pressure drop correlation for two-phase flow in pipesChemical Engineering and Processing - Process Intensification, 1986