Current capability
- In-development process-family and treatment-train foundation
- MBR equipment-planning basis with transparent historical defaults
- Influent, treatment objective and assumption context
Part of the Total Water Design Suite
Biological treatment as a configurable process train.
Municipal and industrial biological-treatment concepts from influent characterization through aeration, sludge, MBR planning and reuse context.
Sign in to open Total Bio Design → Request accessMunicipal and industrial biological-treatment concepts from influent characterization through aeration, sludge, MBR planning and reuse context.
Influent flow, BOD/COD, TSS, nutrients, temperature, targets, operating assumptions and MBR availability basis.
Preliminary train context, process/MBR planning values, energy and residuals framing with visible assumptions.
Configuration breadth is separate from validated solver coverage; historical flux defaults are editable assumptions.
In Development. Not an OEM guarantee or complete released solver; ionic chemistry remains necessary for RO reuse evaluation.
INTEGRATION ROLE AND MATURITY
Designed to provide treated-effluent and sludge context; receiving applications retain their own physics.
6–18 h conceptual biological-treatment study
Illustrative planning assumption—not a measured customer outcome or guarantee. Actual time depends on project complexity, data quality, current tools, alternatives, review requirements and user experience.
Biological process and MBR planning sample state: planned publication. Validated, sanitized sample artifacts are currently unavailable; publication is planned. No downloadable evidence is implied.
Engineering-preview process families: MBBR, SBR, anaerobic treatment, anoxic/aerobic trains, clarifiers, nutrient removal, recycle/side-stream treatment, and sludge thickening/dewatering. Per-unit calculations remain at their disclosed maturity; this breadth is not a released performance guarantee.
Inputs and outputs: influent flow, BOD/COD/TSS, nutrients, temperature, objectives and operating basis produce a transparent train, treated-effluent, air/pump/cleaning quantities, sludge/residuals context and limitations. BOD/COD/TSS cannot infer ions for downstream RO.
MBR planning: editable gross-to-net flux, cycles/downtime, membrane area, N+1 trains, active versus installed area, operating/standby logic, modules/racks, offline peak flux, air, pumps and cleaning quantities are exposed. Downtime is represented in the available operating area so peak flux is not hidden by installed area.
Controlled handoffs: Pretreatment→Bio is engineering preview; Bio→RO/reuse is awaiting validation; Bio→Water Balance is engineering preview; sludge/residuals→ZLD is planned; Bio→Economics is planned. Activity ranges: 1–4 h basis/fractionation; 3–8 h train/mass balance; 3–8 h aeration/recycle/sludge; 3–7 h MBR planning; 2–5 h effluent/compliance/report; 6–18 h overall concept.