Article ID Journal Published Year Pages File Type
145419 Chemical Engineering Journal 2016 9 Pages PDF
Abstract

•The optimization with an innovative MS-PUFM system was evaluated.•The two-phased anaerobic bioreactors coupling with the MS-PUFM system was tested.•Anaerobic mesophilic bioreactors were used.•Mesh screen contributed 20% decrease of operating cost and 33% increase of permeate flux.

To alleviate problems of membrane bioreactors with membrane fouling control, the optimization of the two-phased anaerobic mesophilic bioreactors coupling with the MS-PUFM system was evaluated. The chemical oxygen demand (COD) removal efficiency of anaerobic sludge digestion with the MS-PUFM system was raised from 40% to 97%. VFA concentration was sustained to be in the range 110–138 mg L−1, which was within the optimum range. In the methanogenic bioreactor, methane generation was improved due to the effective reduction of methanogene washout with the MS-PUFM system, and the optimum operating pressure of the MS-PUFM system resulted less than 3 kgf cm−2. Mesh screen contributed 20% decrease of operating cost and 33% increase of permeate flux from 10 to 15 L m−2 h−1 with preliminary solids reduction. As a result, the MS-PUFM system showed practical feasibilities for the digestion of sewage sludge, where current commercial system processes utilizing higher biomass density are not appropriate.

Related Topics
Physical Sciences and Engineering Chemical Engineering Chemical Engineering (General)
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