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MBR (Membrane Bioreactor): Fitting the Secondary Clarifier + Filter into a Single Tank for Reliable Industrial Wastewater Reuse
Nationwide (petrochemical, paper, leachate, dyeing, pharma)
75 t/d – 2500 m³/d

MBR (Membrane Bioreactor): Fitting the Secondary Clarifier + Filter into a Single Tank for Reliable Industrial Wastewater Reuse

The conventional activated sludge process relies on the secondary clarifier to settle solids by gravity — when settling is poor, the effluent turns turbid. MBR uses a membrane to sieve the sludge from the water, allowing the biological tank to hold a high sludge concentration of 8–12 g/L and producing effluent with suspended solids below 1 NTU. Drawing on a large-scale survey in China and multiple real project accounts, this article explains flux, energy consumption, membrane life and selection in one pass.

Gaowutong · Industrial Water Treatment Technology Series · For industry technical professionals · All data sourced from published literature and project records

First, draw the boundary: MBR is not "just another biological process" but an integration of biological treatment + membrane separation — it uses an ultrafiltration/microfiltration membrane (typically PVDF) to directly replace the secondary clarifier and downstream filtration. Because solids-liquid separation relies on sieving rather than settling, the biological tank can maintain an MLSS of 8–12 g/L (versus only 2–4 g/L for conventional activated sludge); at the same throughput the tank volume can shrink to 1/3–1/5, and the effluent stays free of solids no matter how well the sludge settles.

1. Principle: Biological Degradation + Membrane Retention, Merging the Secondary Clarifier and Tertiary Filtration

The MBR flow path is straightforward:

  1. Biological degradation: the wastewater first passes through anaerobic/anoxic/aerobic zones, where microorganisms degrade organics and remove nitrogen and phosphorus — the same as a conventional process;
  2. Membrane retention: the mixed liquor enters the membrane tank, where under gentle suction the water passes through a membrane on the order of 0.1 μm to become permeate, while the activated sludge is 100% retained and returned to the biological stage, forming a sludge-water loop.

Aeration plays a dual role here: it supplies oxygen to the microorganisms and generates a shearing air flow that scours the membrane surface to delay fouling. Because the membrane holds all the sludge in the system, the MLSS can be raised almost without limit, giving rise to the engineering advantage of a small tank, high concentration and good effluent.

MBR process flow diagram: pretreatment – anaerobic/anoxic – aerobic biological treatment – membrane tank retention – permeate, replacing the secondary clarifier
Figure 1. MBR process schematic: the membrane tank replaces the secondary clarifier; sludge is fully retained and recirculated, and the effluent reaches reuse grade without secondary clarification (drawn by Gaowutong)

2. Three Core Parameters: Flux, MLSS and Energy Consumption (the Fundamentals of Selection)

A large-scale MBR survey in China (Zhang et al., Engineering 2021, covering dozens of industrial/municipal MBRs) gives the following actual operating ranges for industrial wastewater:

① Membrane Flux — how much water each unit of membrane area produces

Industrial MBR design flux is typically 15–25 LMH (L/m²·h), with an actual average of about 15.9 LMH. But higher is not always better: a higher flux saves membrane area and lowers capital cost, yet the fouling rate and aeration energy rise in tandem. Several project reports note that once flux exceeds 18–20 LMH, the TMP (transmembrane pressure) rises markedly faster.

② MLSS (Sludge Concentration) — how concentrated the biological tank can run

Measured MLSS in industrial MBRs is mostly 8–12 g/L (average 10.3 g/L), 3–5 times that of a conventional process. This high concentration delivers a high volumetric loading (e.g., a papermaking MBR reaches 3.2 kgCOD/(m³·d), 2.3 times the activated sludge process) and a much smaller footprint.

③ Energy Consumption — Aeration Is the Biggest Share

A modern industrial MBR consumes about 0.3–0.7 kWh/m³ per tonne of water (aeration + suction), and very large installations can push this down to 0.3–0.5 kWh/m³. Because municipal/reuse scenarios include tertiary treatment, conventional processes also need 0.6–1.2 kWh/m³ — the two are now close. In the Kubota submerged pilot, aeration accounts for nearly 50% of total energy — so saving aeration is saving MBR money.

15–25LMH typical design flux
8–12g/L biological-tank MLSS (activated sludge: only 2–4)
0.3–0.7kWh/m³ energy per tonne of water
4–7years membrane life (about 5 on average)
Curve showing flux vs TMP rise and energy consumption relationship
Figure 2. Flux has an economical range: the higher the flux, the faster the TMP rise (fouling) and the steeper the aeration energy — engineering should find the fouling-energy inflection point rather than simply pushing higher (trend schematic, drawn by Gaowutong)

3. Real Project Accounts (All from Published Project Cases)

Industry / ScaleProcess and Key Operating ConditionsEffluent / Removal PerformanceSource
Petrochemical wastewater / 2500 m³/dSubmerged MBR (PVDF), MLSS 10500, influent COD 480–1200Effluent COD 18–22 mg/L; 0.38 kWh per tonne; treatment cost RMB 1.26 (34% lower than the original SBR); payback 4.2 yearsYangpu ethylene petrochemical MBR project case (2026 technical guide)
Wastepaper pulp and papermaking / 2000 m³/dHydrolysis acidification + MBR + UF + RO, PVDF flat sheet 0.03 μm, MLSS 10000, flux 16 LMHEffluent COD 32 mg/L (95.3%); reuse rate 95%; treatment cost RMB 4.0→2.8 per tonne; annual saving about RMB 7.2 millionPapermaking wastewater MBR optimization guide (2024)
Waste incineration leachate / 1000 m³/dPretreatment + anaerobic IOC + external MBR + NF/RO, MBR-stage MLSS 15 g/LMBR-stage COD removal ~90%, NH₃-N/TN >97%; overall effluent COD 20–60 mg/LEverbright Environment, Water Purification Technology 2022
Printing and dyeing wastewater / 2000 m³/dMBR + RO, PVDF hollow fiber 0.03 μm, flux 10–18 LMHOverall recovery 85–90%; RO permeate TDS<200, color removal >99%, COD<20; operating cost 0.8–1.5 USD/m³TheWay Membranes project case
Pharmaceutical wastewater / 60 m³/dEnviQ submerged flat-sheet PVDF 0.04 μm, flux 16 LMH, MLSS 3000–8000Turbidity <1 NTU, stable permeate flow of 3 m³/h since 2022QUA EnviQ project case
Note: the Ningbo Yinzhou waste transfer station uses a PTFE hollow-fiber MBR (75 t/d) with COD removal >92%, NH₄⁺-N >99% and TN >80%, producing no concentrate and achieving full on-site disposal of the leachate — showing that membrane-material selection matters greatly for hard-to-treat wastewater.

4. How to Choose the Membrane: PVDF Flat Sheet vs Hollow Fiber, and PTFE for Tough Duty

Membrane material and configuration are the watershed in MBR selection:

  • PVDF (polyvinylidene fluoride): currently the dominant choice — chemical- and heat-resistant with a wide pH range. Flat-sheet modules have wide channels that resist fouling by fibers and grease, allow single-sheet replacement and cost less to maintain, making them the preferred option for food processing, papermaking and printing and dyeing; hollow-fiber modules have high packing density and an initial flux of up to 25–30 LMH, but their narrow channels clog easily and often require whole-module replacement. Industry reports give: flat-sheet energy 0.3–0.5 kWh/m³, hollow-fiber 0.4–0.7 kWh/m³. Even in harsh environments such as printing and dyeing, PVDF can still reach a 5–8 year life.
  • PTFE (polytetrafluoroethylene): tougher, longer-lived and higher-flux — the Ningbo leachate case benefits from exactly this. Its downside is cost; it suits high-concentration, hard-to-treat streams that demand a long service life.

Favorable price trend: the price of MBR membrane elements in China has fallen from about RMB 940/(m³·d) in 2013 to about RMB 370/(m³·d) in 2019, and membrane life is generally 4–7 years (about 5 on average) — a key reason MBR has moved in recent years from expensive to affordable.

Comparison of PVDF flat-sheet, hollow-fiber and PTFE membrane materials
Figure 3. Membrane material/configuration comparison: PVDF flat sheet (fouling-resistant · single-sheet replacement) vs hollow fiber (dense · whole-module replacement) vs PTFE (durable · costly) (drawn by Gaowutong)

5. Economics: Membranes Are Costly, but They Save Space, Sludge and Deliver Stable Effluent

  • Small footprint: by replacing the secondary clarifier and filter, MBR typically occupies 40%–60% less land than a conventional process — critical where land is scarce or for underground construction (the petrochemical case above cut its footprint by 62%).
  • Less sludge: sludge yield of 0.2–0.4 kgTSS/kgCOD, markedly lower than conventional processes; in the petrochemical case the sludge-yield coefficient was only 0.25, cutting hazardous-waste disposal costs by RMB 890,000 a year.
  • Operating-cost structure: chemical costs for industrial MBR average about RMB 1.17/(m³·d), roughly 60% of total treatment OPEX (average 1.94) — mainly from maintenance and recovery cleaning chemicals for the membrane.

6. Four Pitfalls Engineering Must Watch Closely

1. Membrane Fouling Is the No. 1 Enemy

A slow TMP rise and flux decline are the norm. The countermeasure is a combined punch: intermittent aeration plus online backwashing (the papermaking case backwashes every 25 minutes) and quarterly recovery chemical cleaning (CIP); aeration intensity must be sufficient to strip the attached layer through turbulent shear (the papermaking case raised aeration to 1800 L/(m²·h) to control fiber fouling).

2. Aeration Accounts for Nearly Half the Energy

As noted, aeration accounts for nearly 50% of total energy. Using jet aeration to push oxygen utilization above 35% and optimizing the air-to-water ratio is the most direct lever for cutting energy.

3. High-Salinity/Reuse Requires Source Segregation + RO

MBR only retains suspended solids and macromolecules and does not remove salt. Reuse applications (especially printing and dyeing and leachate) must be followed by UF + RO; high-TDS brine must be diverted at the source, otherwise both RO recovery and membrane life will be dragged down.

4. Membrane Replacement Is a Hidden Cost

With a life of 4–7 years, replacement accounts for a significant share of O&M. Prefer flat-sheet (single-sheet replacement) over hollow-fiber (whole-module replacement) to save money long term; regular CIP can extend membrane life by 25%–30%.

7. One-Line Selection Advice

Suitable for: industrial wastewater where land is tight, effluent quality must be high and stable (reuse or strict discharge), sludge reduction is desired, and scale is small-to-medium (tens to tens of thousands of m³/d).

Not suitable for: large-flow scenarios that only seek the lowest initial investment, have no reuse requirement and face relaxed discharge limits — there a conventional AO + secondary clarifier is usually more economical. Leave MBR to the hard requirements of reuse and stable effluent.

Illustration note: three figures were generated for this article — Figure 1 MBR process flow diagram (membrane tank replacing the secondary clarifier), Figure 2 flux-energy/fouling inflection-point curve, and Figure 3 membrane material/configuration comparison, each placed in its corresponding section. The figures are trend/schematic drawings based on real project and literature data, not original measured charts.

References (Verified Sources)

  1. Zhang J, Xiao K, Liu Z, et al. Large-Scale Membrane Bioreactors for Industrial Wastewater Treatment in China: Technical and Economic Features, Driving Forces, and Perspectives. Engineering, 2021, 7:868–880 (doi:10.1016/j.eng.2020.09.012).
  2. Technical Guide for the Wastewater Treatment Plan of Danzhou Yangpu Economic Development Zone (2026 Optimized Edition) — an MBR treatment case at a petrochemical enterprise. wateretechs.com.
  3. MBR Membrane Bioreactor Treatment of Papermaking Wastewater: Guide to 300 nm Pore-Size Optimization and Measured Per-Tonne Cost (2024). wateretechs.com.
  4. Chen J, Xiao C, Gui H, et al. Engineering case of leachate treatment at a municipal solid waste incineration power plant [J]. Water Purification Technology, 2022, 41(3):100-103,109.
  5. TheWay Membranes. MBR for Textile Wastewater: Color Removal & Reuse.
  6. QUA. EnviQ® Submerged MBR at a Leading Pharma Company (case study, since 2022).
  7. Bouhabib B, et al. Monitoring and analysis of the energy cost of an MBR (Kubota pilot, Spain). Desalination, 2009 (doi:10.1016/j.desal.2009.06.018).
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