# Activated Sludge Models (ASM1, ASM2d, ASM3) > **Used by**: `biological-process-engineer` agent, `reactor` node, `monster` node > **Validation**: Verified against IWA publications, WaterTAP documentation, and peer-reviewed literature ## ASM1 — Activated Sludge Model No. 1 **Source**: Henze, M., Grady, C.P.L., Gujer, W., Marais, G.v.R., Matsuo, T. (1987). IAWPRC Task Group on Mathematical Modelling for Design and Operation of Biological Wastewater Treatment. **Published**: IWA Scientific and Technical Report No. 1 ### 13 Components (State Variables) | Symbol | Description | Type | |--------|-------------|------| | S_I | Soluble inert organic matter | Soluble | | S_S | Readily biodegradable substrate | Soluble | | X_I | Particulate inert organic matter | Particulate | | X_S | Slowly biodegradable substrate | Particulate | | X_B,H | Active heterotrophic biomass | Particulate | | X_B,A | Active autotrophic biomass | Particulate | | X_P | Particulate products from biomass decay | Particulate | | S_O | Dissolved oxygen | Soluble | | S_NO | Nitrate and nitrite nitrogen | Soluble | | S_NH | Ammonium nitrogen (NH₄⁺-N) | Soluble | | S_ND | Soluble biodegradable organic nitrogen | Soluble | | X_ND | Particulate biodegradable organic nitrogen | Particulate | | S_ALK | Alkalinity (molar units) | Soluble | ### 8 Processes 1. **Aerobic growth of heterotrophs**: S_S + S_O + S_NH → X_B,H (Monod kinetics) 2. **Anoxic growth of heterotrophs**: S_S + S_NO + S_NH → X_B,H (denitrification) 3. **Aerobic growth of autotrophs**: S_NH + S_O → X_B,A + S_NO (nitrification) 4. **Decay of heterotrophs**: X_B,H → X_P + X_S (death-regeneration concept) 5. **Decay of autotrophs**: X_B,A → X_P + X_S 6. **Ammonification of soluble organic nitrogen**: S_ND → S_NH 7. **Hydrolysis of entrapped organics**: X_S → S_S 8. **Hydrolysis of entrapped organic nitrogen**: X_ND → S_ND ### Key Kinetic Parameters (default values at 20°C) | Parameter | Symbol | Default | Unit | Description | |-----------|--------|---------|------|-------------| | Max. heterotrophic growth rate | μ_H | 6.0 | d⁻¹ | | | Half-saturation (substrate) | K_S | 20.0 | g COD/m³ | | | Half-saturation (oxygen, het.) | K_O,H | 0.2 | g O₂/m³ | | | Half-saturation (nitrate) | K_NO | 0.5 | g NO₃-N/m³ | | | Heterotrophic decay rate | b_H | 0.62 | d⁻¹ | | | Max. autotrophic growth rate | μ_A | 0.8 | d⁻¹ | | | Half-saturation (ammonia) | K_NH | 1.0 | g NH₃-N/m³ | | | Half-saturation (oxygen, aut.) | K_O,A | 0.4 | g O₂/m³ | | | Autotrophic decay rate | b_A | 0.05 | d⁻¹ | | | Anoxic reduction factor | η_g | 0.8 | — | | | Hydrolysis rate | k_h | 3.0 | g X_S/(g X_B,H · d) | | | Yield (heterotrophic) | Y_H | 0.67 | g COD/g COD | | | Yield (autotrophic) | Y_A | 0.24 | g COD/g N | | | Fraction to X_P | f_P | 0.08 | — | | ### Temperature Correction Arrhenius-type: k(T) = k(20) · θ^(T-20) Common θ values: - Heterotrophic growth: θ = 1.072 - Autotrophic growth: θ = 1.103 (nitrifiers are very temperature-sensitive) - Decay: θ = 1.04 ### Presentation Format The model is presented in the **Petersen matrix** (also called Gujer matrix) format, where rows are processes and columns are components. Each cell contains the stoichiometric coefficient for how a process affects a component. ## ASM2d — Activated Sludge Model No. 2d **Source**: Henze, M., Gujer, W., Mino, T., Matsuo, T., Wentzel, M.C., Marais, G.v.R., van Loosdrecht, M.C.M. (1999) **Published**: IWA Scientific and Technical Report No. 3; also Water Science & Technology 39(1), 165-182 ### Key Extensions over ASM1 - Adds **biological phosphorus removal** by phosphorus accumulating organisms (PAOs) - Includes **denitrifying PAOs** (simultaneous P-removal and denitrification) - 19 components, 21 processes - Models storage of poly-hydroxy-alkanoates (PHA) and polyphosphate (poly-P) by PAOs - Includes fermentation of readily biodegradable substrate ### Additional Components (beyond ASM1) - S_F: Fermentable, readily biodegradable substrate - S_A: Fermentation products (acetate) - S_PO4: Soluble ortho-phosphate - X_PAO: Phosphorus accumulating organisms - X_PP: Poly-phosphate stored by PAOs - X_PHA: Poly-hydroxy-alkanoates stored by PAOs ## ASM3 — Activated Sludge Model No. 3 **Source**: Gujer, W., Henze, M., Mino, T., van Loosdrecht, M.C.M. (1999); updated in Henze et al. (2001) **Published**: IWA Scientific and Technical Report No. 9 ### Key Differences from ASM1 - **Replaces death-regeneration** with endogenous respiration (conceptually simpler) - **Introduces storage polymers** (X_STO) for heterotrophic biomass — substrate is first stored, then used for growth - 13 state variables, 12 reactions - More suitable for dynamic simulation and control applications - Eliminates the problematic simultaneous storage/growth ambiguity in ASM1 ### Storage-Based Metabolism In ASM3, heterotrophs first store readily biodegradable substrate as internal storage products (X_STO), then grow on these stored products. This two-step process better reflects observed biological behavior. ## Choosing Between Models | Criterion | ASM1 | ASM2d | ASM3 | |-----------|------|-------|------| | Carbon & nitrogen | Yes | Yes | Yes | | Phosphorus removal | No | Yes | Via separate Bio-P module | | Computational cost | Low | High | Medium | | Calibration effort | Low | High | Medium | | Best for | Carbon/N only WWTPs | Bio-P plants | Dynamic control | ## Authoritative References 1. Henze, M. et al. (1987). "Activated Sludge Model No. 1" — IAWPRC Scientific and Technical Report No. 1 2. Henze, M. et al. (1995). "Activated Sludge Model No. 2" — IAWQ Scientific and Technical Report No. 3 3. Henze, M. et al. (1999). "Activated Sludge Model No. 2d" — Water Sci. Technol. 39(1), 165-182 4. Gujer, W. et al. (1999). "Activated Sludge Model No. 3" — Water Sci. Technol. 39(1), 183-193 5. Henze, M. et al. (2000). "Activated Sludge Models ASM1, ASM2, ASM2d and ASM3" — IWA Publishing, ISBN 9781900222242 6. Jeppsson, U. (1996). "Modelling Aspects of Wastewater Treatment Processes" — Lund University PhD thesis (comprehensive ASM1 parameter listing)