Prediction of Two-Phase Pressure Gradients of Refrigerants in Horizontal Tubes

By M. Didi, N. Kattan, John Richard Thome. 2002

318 citations recorded by the source corpus.

Abstract Two-phase pressure drop data were obtained for evaporation in two horizontal test sections of 10.92 and 12.00 mm diameter for five refrigerants (R-134a, R-123, R-402A, R-404A and R-502) over mass velocities from 100 to 500 kg/m2 s and vapor qualities from 0.04 to 1.0. These data have then been compared against seven two-phase frictional pressure drop prediction methods. Overall, the method by Muller-Steinhagen and Heck (Muller-Steinhagen H, Heck K. A simple friction pressure drop correlation for two-phase flow in pipes. Chem. Eng. Process 1986;20:297–308) and that by Gronnerud (Gronnerud R. Investigation of liquid hold-up, flow-resistance and heat transfer in circulation type evaporators, part IV: two-phase flow resistance in boiling refrigerants. Annexe 1972-1, Bull. de l'Inst. du Froid, 1979) were found to provide the most accurate predictions while the widely quoted method of Friedel (Friedel L. Improved friction drop correlations for horizontal and vertical two-phase pipe flow. European Two-phase Flow Group Meeting, paper E2; June 1979; Ispra, Italy) gave the third best results. The data were also classified by two-phase flow pattern using the Kattan-Thome-Favrat (Kattan N, Thome JR, Favrat D. Flow boiling in horizontal tubes. Part 1: development of a diabatic two-phase flow pattern map. J. Heat Transfer 1998;120:140–7; Kattan N, Thome JR, Favrat D. Flow boiling in horizontal tubes. Part 2; new heat transfer data for five refrigerants. J Heat Transfer 1998;120:148–55; Kattan N, Thome JR, Favrat D. Flow boiling in horizontal tubes. Part 3: development of a new heat transfer model based on flow patterns. J. Heat Transfer 1998;120:156–65) flow pattern map. The best available method for annular flow was that of Muller-Steinhagen and Heck. For intermittent flow and stratified-wavy flow, the best method in both cases was that of Gronnerud. It was observed that the peak in the two-phase frictional pressure gradient at high vapor qualities coincided with the onset of dryout in the annular flow regime.

Subfields: Mechanical Engineering

View Paper: https://www.semanticscholar.org/paper/15c4a286fb8aaa73483d0c300986be81e4f8f41b

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Citations in the corpus

Two-phase flow in inclined tubes with specific reference to condensation: A review (2011, unknown): “For example, Ould Didi et al. (2002) compared their experimental”
New prediction methods for CO2 evaporation inside tubes: Part I – A two-phase flow pattern map and a flow pattern based phenomenological model for two-phase flow frictional pressure drops (2008, methodology): “As the predictions of two-phase flow frictional pressure drops with the leading methods often cause errors of more than 50% [7-9, 20], efforts are increasingly being made to improve the accuracy of two-phase flow pressure drop predictions.”
Thermophysical properties and heat transfer performance of Al2O3/R-134a nanorefrigerants (2013, methodology): “A correlation proposed by Müller-Steinhagen and Heck [33] was used to determine the frictional pressure drop of pure refrigerant [19].”