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contributor authorF. B. Freitas Rachid
contributor authorDepartment of Mechanical Engineering
contributor authorR. M. Baptista
contributor authorSenior Petroleum Engineer
contributor authorJ. H. Carneiro de Araujo
contributor authorComputer Science
date accessioned2017-05-09T00:07:52Z
date available2017-05-09T00:07:52Z
date copyrightJune, 2002
date issued2002
identifier issn0098-2202
identifier otherJFEGA4-27173#528_1.pdf
identifier urihttp://yetl.yabesh.ir/yetl/handle/yetl/126983
description abstractThis paper presents a model for predicting the contaminated mixing volume arising in pipeline batch transfers without physical separators. The proposed technique represents an improvement over the existing methods since it takes into account time-dependent flow rates and accurate concentration-varying axial dispersion coefficients. The governing equation of the model forms a nonlinear boundary-value problem that is solved by a finite element method coupled to the Newton’s method. A comparison among the theoretical predictions of this method, a field test, and other classical procedures show that the proposed method exhibits the best estimate over the whole range of admissible concentrations investigated.
publisherThe American Society of Mechanical Engineers (ASME)
titlePredicting Mixing Volumes in Serial Transport in Pipelines
typeJournal Paper
journal volume124
journal issue2
journal titleJournal of Fluids Engineering
identifier doi10.1115/1.1459078
journal fristpage528
journal lastpage534
identifier eissn1528-901X
keywordsFlow (Dynamics)
keywordsPipelines
keywordsMixtures
keywordsViscosity
keywordsEquations
keywordsFluids
keywordsPumps
keywordsReynolds number AND Boundary-value problems
treeJournal of Fluids Engineering:;2002:;volume( 124 ):;issue: 002
contenttypeFulltext


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