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AbstractAbstract
[en] This paper presents experimental results on the effect of a surfactant on the flow patterns, pressure drop and heat-transfer coefficients in two-phase, two-component upward flow in a vertical tube. A comparison between the water-air and surfactant solution-air data showed that the surfactant produced very little effect on flow pattern transitions except for the bubble-slug transition. Bubble flow was observed for the surfactant solution-air where slug flow existed for water-air data. The surfactant solution-air frictional pressure drop data were slightly lower than water-air data where differences existed. Slight effects of the surfactant on the heat-transfer coefficients were observed with surfactant solution-air heat-transfer coefficients being lower than the water-air in the region where differences in the flow patterns were observed. The present data were also compared with some correlations to validate their prediction capabilities
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Tien, C.L.; Carey, V.P.; Ferrell, J.K; p. 2283-2288; ISBN 3-540-16896-6;
; 1986; p. 2283-2288; Hemisphere Publishing; New York, NY (USA); International heat transfer conference; San Francisco, CA (USA); 17-22 Aug 1986

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Book
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Conference
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