A mathematical model for pressure drop of two-phase dry-plug flow in circular mini/micro channels |
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| Institution: | 1. Budker Institute of Nuclear Physics, Lavrentieva 11, Novosibirsk 630090, Russia;2. Novosibirsk State University, Pirogova 2, Novosibirsk 630090, Russia;1. Shandong Key Laboratory of Oil-Gas Storage and Transportation Safety, China University of Petroleum, Qingdao 266580, Shandong, PR China;2. SINOPEC Star Petroleum Co., Ltd., Beijing 100083, PR China;1. Department of Chemical and Biological Engineering, University of Alabama, Tuscaloosa, AL 35487, USA;2. Nalco Champion, An Ecolab Company, Sugar Land, TX 77478, USA;3. Anadarko Petroleum Corporation, The Woodlands, TX 77380, USA;4. Department of Chemical and Biomolecular Engineering, New York University, Brooklyn, NY 11201, USA |
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| Abstract: | Dry-plug flow is a variation of two-phase plug flow that occurs in small scale channels and refers to the dry wall conditions at gas portions of the flow regime. Previous experimental studies found a significant increase in pressure drop in this flow regime from the two-phase wet-plug flow regime. In this work an analytical model for the pressure drop of this flow regime is developed and phenomena that influence pressure drop are examined. Unlike previous models, the proposed model seems to be applicable to a wide range of capillary numbers and give good estimations for all static contact angles. Contact angle hysteresis turned out to play a major role in inducing pressure drop in this flow regime. Model’s predictions were in good agreement with previous experimental data. Finally the model is applied to very low capillary number region and pressure drop predictions for this region are presented. |
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