Pilot-Scale Evaluation of Flat-Sheet Membrane Bioreactor for In Situ Retrofitting Textile Dyeing Wastewater Treatment Plant.

Chaoqun Zhou, Chunhai Wei, Huarong Yu, Hongwei Rong, Kang Xiao

Abstract read

In one paragraph

Article in Membranes, 2026. The graph could read no effect estimate from its abstract, so it casts no vote on the map. Not yet cited in PubMed.

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0citing papers in PubMed

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1 · What the graph read from it

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4 · The record

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5 · Who and what money

Authors and funding

5 authors.

Chaoqun ZhouDepartment of Municipal Engineering, School of Civil Engineering and Transportation, Guangzhou University, Guangzhou 510006, China.

Chunhai WeiDepartment of Municipal Engineering, School of Civil Engineering and Transportation, Guangzhou University, Guangzhou 510006, China.ORCID 0000-0002-4336-8556

Huarong YuDepartment of Municipal Engineering, School of Civil Engineering and Transportation, Guangzhou University, Guangzhou 510006, China.

Hongwei RongDepartment of Municipal Engineering, School of Civil Engineering and Transportation, Guangzhou University, Guangzhou 510006, China.

Kang XiaoBeijing Yanshan Earth Critical Zone National Research Station, College of Resources and Environment, University of Chinese Academy of Sciences, Beijing 101408, China.ORCID 0000-0001-6475-1960

Funding

No grant is acknowledged in the PubMed record.

6 · The paper itself

Abstract

It is promising to in situ retrofit the activated sludge process with a membrane bioreactor (MBR) to increase treatment capacity and improve effluent quality in a textile dyeing wastewater treatment plant (WWTP). Membrane selection among commercial products for real engineering applications is critical for this specific wastewater, and little information is available in the literature. This study systematically evaluated the application potential of two flat-sheet microfiltration membranes made of polyvinylidene fluoride (PVDF) and polyether sulfone (PES) in pilot-scale MBRs for in situ retrofitting textile dyeing WWTP. During the four stages with different loads, both membranes achieved nearly the same effluent quality and rejection performance. Both membranes showed little trans-membrane pressure (TMP) increase at an average flux of 15 L/(m

Indexed as

chromacolloidscontact anglemacromolecular organicsmembrane foulingpermeabilityreverse osmosis pretreatmentturbiditywastewater reusezeta potential

Identifiers

PMID41745500

DOI10.3390/membranes16020059

PMCPMC12942177

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