Produced Water Treatment Using Ultrafiltration and Nanofiltration Membranes
The application of ultrafiltration (UF) and nanofiltration (NF) processes in the handling of raw produced water have been investigated in the present study. Experiments of both ultrafiltration and nanofiltration processes are performed in a laboratory unit, which is operated in a cross-flow pattern...
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Al-Khwarizmi College of Engineering – University of Baghdad
2017
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oai:doaj.org-article:d768d69aa4ff4b988e9326cda5cd62252021-12-02T05:52:07ZProduced Water Treatment Using Ultrafiltration and Nanofiltration Membranes1818-11712312-0789https://doaj.org/article/d768d69aa4ff4b988e9326cda5cd62252017-12-01T00:00:00Zhttp://alkej.uobaghdad.edu.iq/index.php/alkej/article/view/304https://doaj.org/toc/1818-1171https://doaj.org/toc/2312-0789 The application of ultrafiltration (UF) and nanofiltration (NF) processes in the handling of raw produced water have been investigated in the present study. Experiments of both ultrafiltration and nanofiltration processes are performed in a laboratory unit, which is operated in a cross-flow pattern. Various types of hollow fiber membranes were utilized in this study such as poly vinyl chloride (PVC) UF membrane, two different polyether sulfone (PES) NF membranes, and poly phenyl sulfone PPSU NF membrane. It was found that the turbidity of the treated water is higher than 95 % by using UF and NF membranes. The chemical oxygen demand COD (160 mg/l) and Oil content (26.8 mg/l) were found after treatment according to the allowable limits set by means of world health organization WHO water quality standards. The final composition of SO4-2 (110 mg/l) and NO3 (48.4 mg/l) components within the produced water after treatment were agreed with the permissible limits of WHO, whereas Cl-1 (8900 mg/l) component is not in the allowable limits. Finally by the use of PVC, PES and PPSU hollow fiber membranes; this method is seen to be not sufficient to remove the salinity of the produced water. Bashir Y. SherhanAreej D. AbbasQusay F. AlsalhyAlaa A. RashadZahraa W. RashadAiden A. ShawkatThamera K. Abbasyusra M. MahdiNoura A. Abdul KareemAl-Khwarizmi College of Engineering – University of BaghdadarticleUltrafiltration membraneNanofiltration membraneOily wastewaterProduced waterDesalinationChemical engineeringTP155-156Engineering (General). Civil engineering (General)TA1-2040ENAl-Khawarizmi Engineering Journal, Vol 12, Iss 3 (2017) |
institution |
DOAJ |
collection |
DOAJ |
language |
EN |
topic |
Ultrafiltration membrane Nanofiltration membrane Oily wastewater Produced water Desalination Chemical engineering TP155-156 Engineering (General). Civil engineering (General) TA1-2040 |
spellingShingle |
Ultrafiltration membrane Nanofiltration membrane Oily wastewater Produced water Desalination Chemical engineering TP155-156 Engineering (General). Civil engineering (General) TA1-2040 Bashir Y. Sherhan Areej D. Abbas Qusay F. Alsalhy Alaa A. Rashad Zahraa W. Rashad Aiden A. Shawkat Thamera K. Abbas yusra M. Mahdi Noura A. Abdul Kareem Produced Water Treatment Using Ultrafiltration and Nanofiltration Membranes |
description |
The application of ultrafiltration (UF) and nanofiltration (NF) processes in the handling of raw produced water have been investigated in the present study. Experiments of both ultrafiltration and nanofiltration processes are performed in a laboratory unit, which is operated in a cross-flow pattern. Various types of hollow fiber membranes were utilized in this study such as poly vinyl chloride (PVC) UF membrane, two different polyether sulfone (PES) NF membranes, and poly phenyl sulfone PPSU NF membrane. It was found that the turbidity of the treated water is higher than 95 % by using UF and NF membranes. The chemical oxygen demand COD (160 mg/l) and Oil content (26.8 mg/l) were found after treatment according to the allowable limits set by means of world health organization WHO water quality standards. The final composition of SO4-2 (110 mg/l) and NO3 (48.4 mg/l) components within the produced water after treatment were agreed with the permissible limits of WHO, whereas Cl-1 (8900 mg/l) component is not in the allowable limits. Finally by the use of PVC, PES and PPSU hollow fiber membranes; this method is seen to be not sufficient to remove the salinity of the produced water.
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format |
article |
author |
Bashir Y. Sherhan Areej D. Abbas Qusay F. Alsalhy Alaa A. Rashad Zahraa W. Rashad Aiden A. Shawkat Thamera K. Abbas yusra M. Mahdi Noura A. Abdul Kareem |
author_facet |
Bashir Y. Sherhan Areej D. Abbas Qusay F. Alsalhy Alaa A. Rashad Zahraa W. Rashad Aiden A. Shawkat Thamera K. Abbas yusra M. Mahdi Noura A. Abdul Kareem |
author_sort |
Bashir Y. Sherhan |
title |
Produced Water Treatment Using Ultrafiltration and Nanofiltration Membranes |
title_short |
Produced Water Treatment Using Ultrafiltration and Nanofiltration Membranes |
title_full |
Produced Water Treatment Using Ultrafiltration and Nanofiltration Membranes |
title_fullStr |
Produced Water Treatment Using Ultrafiltration and Nanofiltration Membranes |
title_full_unstemmed |
Produced Water Treatment Using Ultrafiltration and Nanofiltration Membranes |
title_sort |
produced water treatment using ultrafiltration and nanofiltration membranes |
publisher |
Al-Khwarizmi College of Engineering – University of Baghdad |
publishDate |
2017 |
url |
https://doaj.org/article/d768d69aa4ff4b988e9326cda5cd6225 |
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