MBR Quick Sizing Calculator
Estimate a solids-balanced bioreactor volume, calculated HRT, membrane area, peak flow, and preliminary process indicators.
Use this catalogue as the biological-design branch of the MBR Design Tools workflow. Start with flow and solids assumptions, then move through nutrient removal, aeration, membrane interface, sludge, cost, and post-treatment checks. Each tool exposes its governing equations and assumptions for review before detailed process modelling.
Establish the flow envelope, equalization, pumping, and first-pass reactor and membrane sizing basis before making detailed biological selections.
Estimate a solids-balanced bioreactor volume, calculated HRT, membrane area, peak flow, and preliminary process indicators.
Screen cumulative balancing storage, equalized discharge flow, peak-flow attenuation, transfer-pump power, and annual transfer energy from a transparent daily flow pattern.
Screen pipe velocity, Hazen–Williams friction, fitting loss, total dynamic head, preliminary pump power, motor margin, and annual pumping energy.
Screen net design flux, module area, membrane trains, N+1 availability, air-scour hand-off, and flux-regulated train dispatch.
Translate reactor volume, loading, solids concentration, SRT, wasting, and sludge production into a traceable solids balance.
Estimate steady-state MLVSS and MLSS concentration from removed BOD, SRT, HRT, biomass yield, endogenous decay, and solids fraction assumptions.
Calculate biological solids inventory, SRT, wasting-rate targets, and the effect of effluent solids losses using a transparent mass balance.
Extend excess solids into dewatering feed, cake mass and volume, liquor return, polymer demand, operating duty, annual cake, and preliminary storage.
Use temperature, ammonia, nitrate, phosphorus, recycle, carbon, and alkalinity assumptions to test nutrient-removal feasibility and chemical demand.
Check temperature-corrected nitrifier growth, theoretical and safety-adjusted minimum SRT, selected-SRT margin, ammonia loading, oxygen, and alkalinity.
Estimate ammonia nitrification, nitrate denitrification, oxygen and alkalinity effects, carbon demand, and preliminary anoxic-zone volume.
Size supplementary liquid-carbon demand, product feed, storage, post-anoxic hydraulics, and alkalinity recovery for nitrate polishing.
Estimate internal mixed-liquor recycle, nitrate-N removal load, and preliminary anoxic-zone volume for MLE and pre-denitrification MBR systems.
Estimate total-phosphorus removal and preliminary ferric chloride or alum product dose after selected biological phosphorus removal.
Estimate alkalinity demand and residual alkalinity associated with biological nitrification, and calculate supplemental chemical dosing.
Connect biological oxygen demand, basin zoning, membrane area, air scour, and operating energy. Use supplier data and actual air-system conditions for final selection.
Screen aerobic and anoxic volumes, biological oxygen demand, field oxygen-transfer efficiency, peak airflow, and thermodynamic isentropic blower power.
Calculate full-duty and time-weighted membrane air demand from active train area, SADm, scour sequencing, altitude, and inlet-air conditions.
Aggregate biological aeration, membrane air scour, pumping, chemicals, membrane replacement, sludge, labour, and fixed costs into annual energy and direct-OPEX screens.
Check membrane cleaning demand, permeate indicators, and the final disinfection barrier after the biological and membrane basis is established.
Screen sequential membrane-cleaning solution make-up, commercial product dose, annual chemical demand, cleaning water, and direct chemical cost.
Estimate permeate BOD from soluble and particulate BOD fractions, biological-removal assumptions, and membrane retention of residual particulates.
Size validated UV-reactor duty and chlorination product demand, T10, CT, and preliminary contact-basin volume for MBR permeate.
Use each result in the next check only after confirming units, basis, sampling quality, and whether the value is measured, assumed, OEM-supplied, or calculated.
| Upstream result | Next use | Check before hand-off |
|---|---|---|
| Equalized flow and transfer-pump duty | Hydraulic profile, reactor sizing, and design flow | Peak routing, operating levels, pump control, bypass, and actual tank geometry |
| Reactor volume, MLSS/MLVSS, SRT, yield, and decay | Solids inventory, wasting, nitrification, and sludge production | Measured solids, temperature, load variability, and mass-balance closure |
| Nitrification and nitrogen-removal demand | Alkalinity, carbon, internal recycle, oxygen, and anoxic-zone checks | Ammonia, nitrate, alkalinity, pH, temperature, and treatment objectives |
| Online membrane area, installed area, trains, and flux | Air scour, energy, cleaning, and lifecycle-cost screens | Membrane OEM basis, peak flow, recovery, temperature, isolation, and standby philosophy |
| Sludge production, WAS, polymer, cake, and return liquor | Dewatering, storage, sidestream, and downstream biological loading | Sampling method, equipment, polymer selection, return timing, and disposal route |
| Permeate quality and disinfection duty | Reuse monitoring, residual control, storage, and contingency | End-use criteria, local requirements, validation basis, and failure response |
Design note: Biological systems are dynamic. Seasonal load, temperature, influent variability, membrane configuration, oxygen-transfer capability, actual solids losses, and permit requirements must be considered in detailed design.
Each calculator is a transparent preliminary screen, not a substitute for a process model, pilot or bench testing, OEM data, permit criteria, or qualified engineering review. Use measured site inputs where available, record units and assumptions, and check the linked method and limitations on the individual calculator page.
Documentation revision: 2026-10-02. By: mbr-network.com. Please retain a dated calculation record when a result informs a design discussion.