Predicting Mixing Volumes in Serial Transport in PipelinesSource: Journal of Fluids Engineering:;2002:;volume( 124 ):;issue: 002::page 528Author:F. B. Freitas Rachid
,
Department of Mechanical Engineering
,
R. M. Baptista
,
Senior Petroleum Engineer
,
J. H. Carneiro de Araujo
,
Computer Science
DOI: 10.1115/1.1459078Publisher: The American Society of Mechanical Engineers (ASME)
Abstract: This 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.
keyword(s): Flow (Dynamics) , Pipelines , Mixtures , Viscosity , Equations , Fluids , Pumps , Reynolds number AND Boundary-value problems ,
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contributor author | F. B. Freitas Rachid | |
contributor author | Department of Mechanical Engineering | |
contributor author | R. M. Baptista | |
contributor author | Senior Petroleum Engineer | |
contributor author | J. H. Carneiro de Araujo | |
contributor author | Computer Science | |
date accessioned | 2017-05-09T00:07:52Z | |
date available | 2017-05-09T00:07:52Z | |
date copyright | June, 2002 | |
date issued | 2002 | |
identifier issn | 0098-2202 | |
identifier other | JFEGA4-27173#528_1.pdf | |
identifier uri | http://yetl.yabesh.ir/yetl/handle/yetl/126983 | |
description abstract | This 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. | |
publisher | The American Society of Mechanical Engineers (ASME) | |
title | Predicting Mixing Volumes in Serial Transport in Pipelines | |
type | Journal Paper | |
journal volume | 124 | |
journal issue | 2 | |
journal title | Journal of Fluids Engineering | |
identifier doi | 10.1115/1.1459078 | |
journal fristpage | 528 | |
journal lastpage | 534 | |
identifier eissn | 1528-901X | |
keywords | Flow (Dynamics) | |
keywords | Pipelines | |
keywords | Mixtures | |
keywords | Viscosity | |
keywords | Equations | |
keywords | Fluids | |
keywords | Pumps | |
keywords | Reynolds number AND Boundary-value problems | |
tree | Journal of Fluids Engineering:;2002:;volume( 124 ):;issue: 002 | |
contenttype | Fulltext |