INGENIA

ENV-23

ADM1 growth snapshot

μ = μm S/(Ks+S) · KI/(KI+I). Monod with non-competitive inhibition.

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BiokineticsBatstone ADM1

Governing equation

μ=μmSKS+SKIKI+I\mu=\mu_m\dfrac{S}{K_S+S}\dfrac{K_I}{K_I+I}

where

\mu_m
Max growth (1/d)
S
Substrate (kg/m³)
K_S
Half-saturation (kg/m³)
K_I
Inhibition KI (kg/m³)
I
Inhibitor (kg/m³)
\mu
Specific growth (1/d)

Lecture brief

Historical brief

Streeter–Phelps (1925) oxygen sag, settling theory and Guldberg–Waage kinetics made water and air quality a rate problem. The lab computes sag, overflow and a snapshot of reactor mass balance. This sheet (ENV-23 — ADM1 growth snapshot) is the form associated with Batstone ADM1. Working symbols: μm\mu_m, SS, KSK_S, KIK_I, II \rightarrow μ\mu. ADM1 uses hyperbolic uptake for anaerobic digestion, multiplied by an inhibition term for pH, NH3 or H2.

Purpose

Purpose: compute μ\mu from μm\mu_m, SS, KSK_S, KIK_I, II in Environmental via μ=μmSKS+SKIKI+I\mu=\mu_m\dfrac{S}{K_S+S}\dfrac{K_I}{K_I+I} μ = μm S/(Ks+S) · KI/(KI+I). Monod with non-competitive inhibition. Use it when a real environmental question must be answered in SI before a code check.

Live realistic example

In symbols

Live case. Given μm=0.4001/d\mu_m = 0.400\,\mathrm{1/d}, S=2.000kg/m3S = 2.000\,\mathrm{kg/m^{3}}, KS=0.500kg/m3K_S = 0.500\,\mathrm{kg/m^{3}}, KI=0.050kg/m3K_I = 0.050\,\mathrm{kg/m^{3}}, I=0.010kg/m3I = 0.010\,\mathrm{kg/m^{3}}, the governing relation μ=μmSKS+SKIKI+I\mu=\mu_m\dfrac{S}{K_S+S}\dfrac{K_I}{K_I+I} yields μ=0.26671/d\mu = 0.2667\,\mathrm{1/d}. A digester, a substrate bar, an inhibitor shade. Move a slider: the numbers are this situation, not a canned story.

Calculator

Inputs

Outputs

  • Specific growth \mu0.2667 1/d
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ENV-23 · reactor
00:0 / 00:08

Narration of this film

A digester, a substrate bar, an inhibitor shade.

ADM1 uses hyperbolic uptake for anaerobic digestion, multiplied by an inhibition term for pH, NH3 or H2.

Reading speed

Watch on YouTube