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A mathematical model and an iterative procedure to calculate holdup and pressure drop in horizontal gas‐liquid flow is developed. The predictions of the model agree with well over a hundred data points collected with air‐water and air‐glycerine solutions in 0.0254‐, 0.0381‐, and 0.0508‐m. diameter pilot pipelines. A design procedure using the verified model is presented.
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Russell et al. (1974) studied this question.
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