A novel extractive membrane bioreactor for treating biorefractory organic pollutants in the presence of high concentrations of inorganics: application to a synthetic acidic effluent containing high concentrations of chlorophenol and salt

Citation
W. Liu et al., A novel extractive membrane bioreactor for treating biorefractory organic pollutants in the presence of high concentrations of inorganics: application to a synthetic acidic effluent containing high concentrations of chlorophenol and salt, J MEMBR SCI, 181(1), 2001, pp. 127-140
Citations number
63
Categorie Soggetti
Chemistry,"Chemical Engineering
Journal title
JOURNAL OF MEMBRANE SCIENCE
ISSN journal
03767388 → ACNP
Volume
181
Issue
1
Year of publication
2001
Pages
127 - 140
Database
ISI
SICI code
0376-7388(20010115)181:1<127:ANEMBF>2.0.ZU;2-D
Abstract
Traditional bioprocesses have difficulties treating biorefractory organic p ollutants in waste streams that contain high concentrations of inorganics. A novel hybrid process, combining liquid-liquid extraction and a membrane b ioreactor, has been designed to treat such an effluent. To demonstrate the viability of this process, a synthetic wastewater was designed to represent the sort of effluent that often results from the speciality organic chemic als sector. This model effluent contains high concentrations of chloropheno ls (CPs) (1000 mg l(-1)), salts (15% w/w) and has a pH of less than 1. Expe rimental work was combined with process design to estimate the likely treat ment costs for such an effluent. The proposed treatment process has three a dvantages. 1. The water insoluble solvent serves as a barrier to prevent the salts and acids in the raw wastewater from entering the bioreactor where they are in hibitory. 2. Due to their acidity, CPs are easily extracted from the acidic effluent, leaving a low concentration (<100 mg l(-1)). They are stripped from the so lvent into an alkaline aqueous stripping stream at a moderate concentration . The bioreactor can then be operated at much higher CP concentrations than the stringent regulatory discharge standard of 100 mg l(-1). At the higher concentration the biodegradation rate of the CPs increases by over a twent y-fold. 3, Two hydrophilic ceramic membranes effect oil/water (o/w) emulsion separa tion and biomass separation. These are operated alternately for each purpos e in opposing directions. Thus one filtration serves as backflush of the ot her and vice versa, reducing membrane fouling. This process could also be used for treating other wastewaters containing o rganic priority pollutants that are either acids or bases. (C) 2001 Elsevie r Science B.V. All rights reserved.