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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Autores principales:	Bashir Y. Sherhan, Areej D. Abbas, Qusay F. Alsalhy, Thamera K. Abbas, yusra M. Mahdi, Noura A. Abdul Kareem, Alaa A. Rashad, Zahraa W. Rashad, Aiden A. Shawkat
Formato:	article
Lenguaje:	EN
Publicado:	Al-Khwarizmi College of Engineering – University of Baghdad 2016
Materias:	Chemical engineering TP155-156 Engineering (General). Civil engineering (General) TA1-2040
Acceso en línea:	https://doaj.org/article/e2b2232036a7404db19084659bd7bfe2
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spelling	oai:doaj.org-article:e2b2232036a7404db19084659bd7bfe22021-12-02T07:14:47ZProduced Water Treatment Using Ultrafiltration and Nanofiltration Membranes1818-1171https://doaj.org/article/e2b2232036a7404db19084659bd7bfe22016-09-01T00:00:00Zhttp://www.iasj.net/iasj?func=fulltext&aId=113811https://doaj.org/toc/1818-1171The 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. AlsalhyThamera K. Abbasyusra M. MahdiNoura A. Abdul KareemAlaa A. RashadZahraa W. RashadAiden A. ShawkatAl-Khwarizmi College of Engineering – University of BaghdadarticleChemical engineeringTP155-156Engineering (General). Civil engineering (General)TA1-2040ENAl-Khawarizmi Engineering Journal, Vol 12, Iss 3, Pp 10-18 (2016)
institution	DOAJ
collection	DOAJ
language	EN
topic	Chemical engineering TP155-156 Engineering (General). Civil engineering (General) TA1-2040
spellingShingle	Chemical engineering TP155-156 Engineering (General). Civil engineering (General) TA1-2040 Bashir Y. Sherhan Areej D. Abbas Qusay F. Alsalhy Thamera K. Abbas yusra M. Mahdi Noura A. Abdul Kareem Alaa A. Rashad Zahraa W. Rashad Aiden A. Shawkat 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.
format	article
author	Bashir Y. Sherhan Areej D. Abbas Qusay F. Alsalhy Thamera K. Abbas yusra M. Mahdi Noura A. Abdul Kareem Alaa A. Rashad Zahraa W. Rashad Aiden A. Shawkat
author_facet	Bashir Y. Sherhan Areej D. Abbas Qusay F. Alsalhy Thamera K. Abbas yusra M. Mahdi Noura A. Abdul Kareem Alaa A. Rashad Zahraa W. Rashad Aiden A. Shawkat
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	2016
url	https://doaj.org/article/e2b2232036a7404db19084659bd7bfe2
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Produced Water Treatment Using Ultrafiltration and Nanofiltration Membranes

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