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Engineering reference

Water & Wastewater Treatment: theory, method, and sources

This environmental & energy engineering workspace publishes 10 governing equations, 5 stated assumptions, 1 documented boundary, and 2 sources so the numbers it returns can be checked rather than taken on trust.

Calculations run locallyCalculation & source methodology

How this tool works

Ten modules cover clarifier surface overflow rate, detention time, BOD removal kinetics, chlorine dosing and CT disinfection credit, activated sludge food-to-microorganism ratio, solids retention time, oxygen demand, sludge production, and filter loading.

The activated sludge modules use the same MLSS and flow basis, so F/M ratio, SRT, aeration demand, and sludge yield can be evaluated as one consistent process design.

Calculators and topics covered

  • water
  • wastewater
  • treatment
  • disinfection
  • clarifier
  • BOD
  • activated sludge
  • SRT
  • chlorine CT
  • filter loading

Core equations

surface overflow rate:SOR=QA\text{surface overflow rate:}\quad SOR = \frac{Q}{A}detention time:t=VQ\text{detention time:}\quad t = \frac{V}{Q}first-order BOD removal:C=C0ekt\text{first-order BOD removal:}\quad C = C_{0} e^{- kt}chlorine dose:dose=demand+target  residualmass=dose×Q\text{chlorine dose:}\quad \begin{gathered}\text{dose} = \text{demand} + \text{target}\; \text{residual}\\\text{mass} = \text{dose} \times Q\end{gathered}CT product:CT=residual×contact  time,  compared  with  the  target  CT\text{CT product:}\quad CT = \text{residual} \times \text{contact}\; \text{time},\; \text{compared}\; \text{with}\; the\; \text{target}\; CTfood-to-microorganism ratio:FM=QBODVMLSS\text{food-to-microorganism ratio:}\quad \frac{F}{M} = \frac{Q \cdot \mathrm{BOD}}{V \cdot MLSS}solids retention time:SRT=VMLSSQw  Xw+Qe  Xe\text{solids retention time:}\quad \mathrm{SRT} = \frac{V \cdot MLSS}{Q_{w}\; X_{w} + Q_{e}\; X_{e}}oxygen demand:O2=Q(BODinBODout)factor\text{oxygen demand:}\quad O_{2} = Q \left(\mathrm{BOD}_{in} - \mathrm{BOD}_{\mathrm{out}}\right) \cdot \text{factor}sludge production:Px=YQ(BODinBODout)1+kdSRT\text{sludge production:}\quad P_{x} = \frac{Y \cdot Q \left(\mathrm{BOD}_{in} - \mathrm{BOD}_{\mathrm{out}}\right)}{1 + k_{d} \cdot \mathrm{SRT}}filter loading rate:v=QArun  hours\text{filter loading rate:}\quad v = \frac{Q}{A \cdot run\; \mathrm{hours}}

Method and assumptions

Assumptions

  • Reactors are treated as completely mixed and at steady state; diurnal and storm flow variation is not modelled.
  • BOD removal follows first-order kinetics with a single rate constant at the stated temperature.
  • CT values must be compared against the correct pathogen, temperature, and pH table from the governing regulation.
  • Activated sludge relationships assume a conventional process without nutrient removal or selector zones.
  • Yield and decay coefficients are typical literature values and vary with wastewater strength and temperature.

Limitations and design boundaries

  • Educational screening calculations only. Treatment design and operation require representative testing, current regulations, redundancy, process controls, safety analysis, and qualified professional review.

Sources and references

Primary sources are preferred for ratings, standards, manufacturer data, and externally defined constants.

Source policy
  • Metcalf & Eddy, Wastewater Engineering: Treatment and Resource Recovery
  • AWWA and ASCE, Water Treatment Plant Design