Numerical–Theoretical Analysis of Heat Transfer, Pressure Drop, and Fouling in Internal Helically Ribbed Tubes of Different Geometries

A numerical analysis of heat transfer and pressure drop for turbulent flow in a series of 15.54-mm inside diameter helically ribbed tubes has been performed. The ranges of geometric parameters were number of rib starts (10 to 40), helix angle (25 to 55 degrees), and rib height (0.3 to 0.6 mm). The effect of grid independence was extensively examined. The computational results match well with the experimental data to validate the accuracy of the numerical model. The effect of each main parameter, rib starts, helix angle, and rib height, on heat transfer and pressure drop is investigated. Considering fouling in practical situations, the ratio of pitch over rib height is an important parameter to select the tubes. It is advisable to select tubes with pitch over rib height ratio greater than 3.5, which have better heat transfer and lower fouling potential.

[1]  W. Tao,et al.  Prediction of fully developed turbulent heat transfer of internal helically ribbed tubes – An extension of Gnielinski equation , 2012 .

[2]  Wei Li,et al.  Modeling cooling tower fouling in helical-rib tubes based on Von-Karman analogy , 2010 .

[3]  R. Webb Single-phase heat transfer, friction, and fouling characteristics of three-dimensional cone roughness in tube flow , 2009 .

[4]  Louay M. Chamra,et al.  Correlating heat transfer and friction in helically-finned tubes using artificial neural networks , 2007 .

[5]  K. Jansen,et al.  ANALYSIS OF HEAT TRANSFER CHARACTERISTICS IN INTERNALLY FINNED TUBES , 2004 .

[6]  Michael K. Jensen,et al.  Geometry Effects on Turbulent Flow and Heat Transfer in Internally Finned Tubes , 2001 .

[7]  W. Li,et al.  Fouling in enhanced tubes using cooling tower water: Part I: long-term fouling data , 2000 .

[8]  Wei Li,et al.  Fouling in enhanced tubes using cooling tower water: Part II: combined particulate and precipitation fouling , 2000 .

[9]  Ralph L. Webb,et al.  Heat transfer and friction characteristics of internal helical-rib roughness , 2000 .

[10]  James G. Withers,et al.  Tube-Side Heat Transfer and Pressure Drop for Tubes Having Helical Internal Ridging with Turbulent/Transitional Flow of Single-Phase Fluid. Part 1. Single-Helix Ridging , 1980 .

[11]  T. C. Carnavos Heat Transfer Performance of Internally Finned Tubes in Turbulent Flow , 1980 .

[12]  T. C. Carnavos Cooling Air in Turbulent Flow with Internally Finned Tubes , 1979 .

[13]  Felix Hueber,et al.  Principles Of Enhanced Heat Transfer , 2016 .

[14]  Pedro J. Mago,et al.  Experimental determination of heat transfer and friction in helically-finned tubes , 2008 .

[15]  K. Jansen,et al.  Fin shape effects in turbulent heat transfer in tubes with helical fins , 2002 .

[16]  M. Jensen,et al.  Numerical Investigation of Turbulent Flow and Heat Transfer in Internally Finned Tubes , 1999 .

[17]  R. Webb Performances Cost Effectiveness, and Water-Side Fouling Considerations of Enhanced Tube Heat Exchangers for Boiling Service with Tube-Side Water Flow , 1982 .

[18]  V. Gnielinski New equations for heat and mass transfer in turbulent pipe and channel flow , 1976 .