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contributor authorMark A. Chaiko
date accessioned2017-05-09T00:20:10Z
date available2017-05-09T00:20:10Z
date copyrightNovember, 2006
date issued2006
identifier issn0098-2202
identifier otherJFEGA4-27225#1324_1.pdf
identifier urihttp://yetl.yabesh.ir/yetl/handle/yetl/133856
description abstractA finite-volume approach, based on the MUSCL-Hancock method, is presented and applied to liquid-column separation transients in pipelines. In the mathematical model, sudden closure of a valve on the downstream end of a pipeline initiates the hydraulic transient, while a head tank maintains constant upstream pressure. The two-phase fluid is treated as a homogeneous mixture, and changes in fluid pressure are assumed to occur at constant entropy. Effects of pipe elasticity on wave propagation speed are included in the model by coupling the circumferential stress-strain relation for the pipe wall to the local fluid pressure. In regions of the domain where the solution is smooth, second-order accuracy is achieved by means of data reconstruction based on sloping-difference formulas. Slope limiting prevents the development of spurious oscillations in the neighborhood of steep wave fronts. Data reconstruction leads to a piece-wise linear representation of the solution, which is discontinuous across cell boundaries. In order to advance the solution in time, a Riemann problem is solved on each cell junction to obtain mass and momentum flux contributions. A splitting technique, which separates flux terms from gravity and frictional effects, allows the compatibility equations for the Riemann problem to be expressed as total differentials of fluid velocity and an integral that depends only on the fluid pressure. Predictions for large-amplitude pressure pulses caused by liquid-column separation and rejoining are compared against experimental data available in the literature. Amplitude and timing of the predicted pressure response shows reasonably good agreement with experimental data even when as few as 20–40 computational cells are used to describe axial variations in fluid conditions along a pipeline of approximately 35m in length. An advantage of the current method is that it does not give rise to spurious oscillations when grid refinement is performed. The presence of nonphysical oscillations has been a drawback of a commonly used method based on discrete vapor cavities and characteristic treatment of wave propagation.
publisherThe American Society of Mechanical Engineers (ASME)
titleA Finite-volume Approach for Simulation of Liquid-column Separation in Pipelines
typeJournal Paper
journal volume128
journal issue6
journal titleJournal of Fluids Engineering
identifier doi10.1115/1.2353271
journal fristpage1324
journal lastpage1335
identifier eissn1528-901X
keywordsPressure
keywordsSeparation (Technology)
keywordsFluids
keywordsWaves
keywordsPipelines
keywordsValves
keywordsEquations
keywordsSimulation
keywordsPipes
keywordsVapors
keywordsOscillations AND Flow (Dynamics)
treeJournal of Fluids Engineering:;2006:;volume( 128 ):;issue: 006
contenttypeFulltext


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