Investigations on the Use of Different Ceramic Membranes For Efficient Oil-Field Produced Water Treatment

dc.citation.doi10.1016/j.desal.2009.09.088en_US
dc.citation.epage996en_US
dc.citation.issue3en_US
dc.citation.jtitleDesalinationen_US
dc.citation.spage991en_US
dc.citation.volume250en_US
dc.contributor.authorEbrahimi, Mehrdad
dc.contributor.authorWillershausen, Daniel
dc.contributor.authorShams-Ashaghi, Kikavous
dc.contributor.authorEngel, Larisa
dc.contributor.authorPlacido, Laura
dc.contributor.authorMund, Peter
dc.contributor.authorBolduan, Peter
dc.contributor.authorCzermak, Peter
dc.contributor.authoreidpczermaken_US
dc.date.accessioned2010-04-08T15:39:25Z
dc.date.available2010-04-08T15:39:25Z
dc.date.issued2010-01-30
dc.date.published2010en_US
dc.description.abstractEfficient performance of the combination of treatment processes for oilfield produced water generated from oil tank dewatering was investigated in the study presented below. By-produced wastewater is generated in significant quantity during exploitation of crude oil and gas from onshore and offshore production operations. This wastewater, commonly referred to as “produced water”, has distinctive characteristics, due to their organic and inorganic compounds. However, these characteristics change from well to well. The treatment process investigated here consists of a pre-treatment step utilizing microfiltration (0.1 and 0.2µm pore size filters) and/or a simulated batch dissolved air flotation (DAF), and a multistage post-treatment step utilizing cross-flow ultra- (0.05µm pore size and 20kDa molecular weight cut-off filters), and nanofiltration (1 and 0.75kDa MWCO filters). Filters used were ceramic membranes. To determine the separation capability of the processes described, various parameters, such as trans-membrane pressure varying from 0.5 to 2 bar, cross-flow velocity in the range of 0.6 to 1.3m/s, influent oil concentration ranging from 32 to 5420 parts per million (ppm) and different membrane cleaning methods used were investigated. The average permeate flux varied from 3.4 to 3300 l/h*m²*bar, total oil removal was up to 99.5% and total organic carbon removal reached 49%.en_US
dc.description.versionArticle (author version)
dc.identifier.urihttp://hdl.handle.net/2097/3520
dc.relation.urihttp://doi.org/10.1016/j.desal.2009.09.088en_US
dc.subjectCeramic membraneen_US
dc.subjectOilfielden_US
dc.subjectProduced water treatmenten_US
dc.subjectMicrofiltrationen_US
dc.subjectUltrafiltrationen_US
dc.subjectNanofiltrationen_US
dc.subjectSimulated flotationen_US
dc.subjectMembrane foulingen_US
dc.subjectPermeate flux rateen_US
dc.subjectOil removalen_US
dc.titleInvestigations on the Use of Different Ceramic Membranes For Efficient Oil-Field Produced Water Treatmenten_US
dc.typeTexten_US

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