Numerical Simulation of the Transient Development of Slug Flow in Horizontal Pipes

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Abstract:

Slug flow regime in two and multi-phase flow in pipes is a complicated flow phenomena representing challenge in the design of the piping system. In the present work, water/air two phase flow was modeled and simulated as 3 dimensional, transient, and incompressible flow using Volume of Fluid technique in STAR-CCM+ software. The simulation was conducted to predict and evaluate the air-water slug flow in a horizontal pipe with 0.16 m diameter and 7 m long. The superficial velocities for both phases were extracted from Baker chart slug zone. The results were validated against experimental bench marking referenced in Baker chart and the proposed VOF technique shows a good capability in simulating the development of the slug flow regime. This model could be utilized for simulation of various two phase flow regimes.

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300-304

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January 2016

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[1] BAKER, O., Simultaneous flow of oil and gas, Oil Gas J. 53 (1954) 185-195.

Google Scholar

[2] S. Ghorai, K.D.P. Nigam, CFD modeling of flow profiles and interfacial phenomena in two-phase flow in pipes, Chem. Eng. Process. 45 (2006) 55–65.

DOI: 10.1016/j.cep.2005.05.006

Google Scholar

[3] T. Frank, NUMERICAL SIMULATION OF SLUG FLOW REGIME FOR AN AIR-WATER TWO-PHASE FLOW IN HORIZONTAL PIPES, (2005), 1–13.

Google Scholar

[4] Ansari, M.R. and Shokri, V., Numerical modeling of slug flow initiation in horizontal channels using a two-fluid model, Int. J. Heat Fluid Flow, 32, (2011)145–155.

DOI: 10.1016/j.ijheatfluidflow.2010.09.002

Google Scholar

[5] E. C. Rogero, Experimental Investigation of Developing Plug and Slug Flows, PhD, Mechanical Engineering, Universität München, Germany, (2009).

Google Scholar

[6] Sandra C.K. De Schepper, Geraldine J. Heynderickx ∗, Guy B. Marin, CFD modeling of all gas–liquid and vapor–liquid flow regimes predicted by the Baker chart, Chemical Engineering Journal 138 (2008) 349–357.

DOI: 10.1016/j.cej.2007.06.007

Google Scholar