4.5 Article

Compact Carbon-Based Membrane Reactors for the Intensified Anaerobic Decolorization of Dye Effluents

Journal

MEMBRANES
Volume 12, Issue 2, Pages -

Publisher

MDPI
DOI: 10.3390/membranes12020174

Keywords

anaerobic decolorization; dye effluents; graphene oxide membrane; matrimid membrane

Funding

  1. European Union's Horizon 2020 research and innovation programme under the Marie Sklodowska-Curie grant [713679]
  2. Universitat Rovira i Virgili (URV) [2017MFP-COFUND-18]
  3. MCIN/AEI [RTI2018-096467-B-I00]
  4. ERDF A way of making Europe [RTI2018-096467-B-I00]
  5. Universitat Rovira i Virgili [2021PFR-URV-87]
  6. Comissionat per a Universitats i Recerca, DIUE de la Generalitat de Catalunya [2017 SGR 396]

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This study explores the application of ceramic-supported carbon membrane bioreactors and ceramic-supported graphene oxide membrane bioreactors in treating dye wastewater. The results show that the conductive surface of the graphene oxide membrane is more efficient in removing color from dye solutions.
Carbon-based membranes integrated with anaerobic biodegradation are presented as a unique wastewater treatment approach to deal with dye effluents. This study explores the scope of ceramic-supported carbon membrane bioreactors (B-CSCM) and ceramic-supported graphene oxide membrane bioreactors (B-CSGOM) to decolorize azo dye mixtures (ADM) and other dyes. The mixture was prepared using an equimolar composition of monoazo Acid Orange 7, diazo Reactive Black 5, and triazo Direct Blue 71 dye aqueous solution. Afterwards, as in the ADM experiment, both compact units were investigated for their ability in the biodecolorization of Methylene Blue (MB) and Rhodamine B (RhB) dye solutions, which do not belong to the azo family. The obtained outcomes revealed that the conductive surface of the graphene oxide (GO) membrane resulted in a more efficient and higher color removal of all dye solutions than B-CSCM under a wide feed concentration and permeate flux ranges. The maximum color removal at low feed concentration (50 mg center dot L-1) and permeate flux (0.05 L center dot m(-2)center dot h(-1)) was 96% for ADM, 98% for MB and 94% for RhB, whereas it was 89%, 94% and 66%, respectively, for B-CSCM. This suggests that the robust, cost-effective, efficient nanostructures of B-CSGOM can successfully remove diverse azo dye solutions from wastewater better than the B-CSCM does.

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