Effect of Nanoparticles and Surfactant on Phase Inversion of Two Phases

In the present study, a pressure drop technique was used to identify the phase inversion point of oil-in-water to water-in-oil flows through a horizontal pipe and to study the effect of additives (nanoparticles, cationic surfactant and blend  nanoparticles-surfactant) on the critical dispersed volu...

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Main Author: Nada M. Farhan
Format: Article
Language:English
Published: University of Baghdad/College of Engineering 2017-03-01
Series:Iraqi Journal of Chemical and Petroleum Engineering
Subjects:
Online Access:http://ijcpe.uobaghdad.edu.iq/index.php/ijcpe/article/view/198
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spelling doaj-b597022ee3014b589377d54834bc0c122020-11-25T00:29:27ZengUniversity of Baghdad/College of EngineeringIraqi Journal of Chemical and Petroleum Engineering1997-48842618-07072017-03-01181Effect of Nanoparticles and Surfactant on Phase Inversion of Two PhasesNada M. Farhan In the present study, a pressure drop technique was used to identify the phase inversion point of oil-in-water to water-in-oil flows through a horizontal pipe and to study the effect of additives (nanoparticles, cationic surfactant and blend  nanoparticles-surfactant) on the critical dispersed volume fraction (phase inversion point). The measurements were carried  for mixture velocity ranges from 0.8 m/sec to 2.3 m/sec. The results showed that at low mixture velocity 0.8 and 1 m/sec there is no effect of additives and velocity on phase inversion point, while at high mixture velocities the phase inversion point for nanoparticles and blend (nanoparticles/surfactant) systems was delayed (postponed) to a higher value of the dispersed phase volume fraction (oil volume fraction) compared to the system of surfactant where the phase inversion point was occurred at low dispersion phase volume fraction. For all systems the desperation volume fraction at the point of inversion decreases with increasing mixture velocity. Indeed, the results showed that surfactant was more effective on phase inversion point than solid nanoparticles. http://ijcpe.uobaghdad.edu.iq/index.php/ijcpe/article/view/198Phase inversion, surfactant, nanoparticles, oil-water flow, and pressure drop.
collection DOAJ
language English
format Article
sources DOAJ
author Nada M. Farhan
spellingShingle Nada M. Farhan
Effect of Nanoparticles and Surfactant on Phase Inversion of Two Phases
Iraqi Journal of Chemical and Petroleum Engineering
Phase inversion, surfactant, nanoparticles, oil-water flow, and pressure drop.
author_facet Nada M. Farhan
author_sort Nada M. Farhan
title Effect of Nanoparticles and Surfactant on Phase Inversion of Two Phases
title_short Effect of Nanoparticles and Surfactant on Phase Inversion of Two Phases
title_full Effect of Nanoparticles and Surfactant on Phase Inversion of Two Phases
title_fullStr Effect of Nanoparticles and Surfactant on Phase Inversion of Two Phases
title_full_unstemmed Effect of Nanoparticles and Surfactant on Phase Inversion of Two Phases
title_sort effect of nanoparticles and surfactant on phase inversion of two phases
publisher University of Baghdad/College of Engineering
series Iraqi Journal of Chemical and Petroleum Engineering
issn 1997-4884
2618-0707
publishDate 2017-03-01
description In the present study, a pressure drop technique was used to identify the phase inversion point of oil-in-water to water-in-oil flows through a horizontal pipe and to study the effect of additives (nanoparticles, cationic surfactant and blend  nanoparticles-surfactant) on the critical dispersed volume fraction (phase inversion point). The measurements were carried  for mixture velocity ranges from 0.8 m/sec to 2.3 m/sec. The results showed that at low mixture velocity 0.8 and 1 m/sec there is no effect of additives and velocity on phase inversion point, while at high mixture velocities the phase inversion point for nanoparticles and blend (nanoparticles/surfactant) systems was delayed (postponed) to a higher value of the dispersed phase volume fraction (oil volume fraction) compared to the system of surfactant where the phase inversion point was occurred at low dispersion phase volume fraction. For all systems the desperation volume fraction at the point of inversion decreases with increasing mixture velocity. Indeed, the results showed that surfactant was more effective on phase inversion point than solid nanoparticles.
topic Phase inversion, surfactant, nanoparticles, oil-water flow, and pressure drop.
url http://ijcpe.uobaghdad.edu.iq/index.php/ijcpe/article/view/198
work_keys_str_mv AT nadamfarhan effectofnanoparticlesandsurfactantonphaseinversionoftwophases
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