Experimental studies on the evaporative heat transfer and pressure drop of CO2 and CO2/propane mixtures flowing upward in smooth and micro-fin tubes with outer diameter of 5mm for an inclination angle of 45°

Author:

Cho Jin Min,Kim Yong Jin,Kim Min Soo

Publisher

Elsevier BV

Subject

Mechanical Engineering,Building and Construction

Reference16 articles.

1. An experimental investigation of the motion of long bubbles in inclined tubes;Bendikson;Int. J. Multiphase Flow,1984

2. Bredesen, A.M., Hafner, A., Pettersen, J., Neksa, P., Aflekt, K., 1997. Heat transfer and pressure drop for in-tube evaporation of CO2. IIF-IIR-Commission B1 with E1 & E2, College Park, Maryland, USA, pp. 35–40

3. A physically based on correlation for the effects of power law rheology and inclination on slug bubble rise velocity;Carew;Int. J. Multiphase Flow,1995

4. Characteristics of gas–liquid two-phase flow in small diameter inclined tubes;Cheng;Chem. Eng. Sci.,2001

5. New flow boiling heat transfer model and flow pattern map for carbon dioxide evaporating inside horizontal tubes;Cheng;Int. J. Heat Mass Transfer,2006

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