recordADM1_parameters
Partial record for the parameters of the adm1 model
Extends from TransiEnt.Basics.Icons.Record (Icon for records).
Information
1. Purpose of model
(Description)
2. Level of detail, physical effects considered, and physical insight
(Description)
3. Limits of validity
(Description)
4. Interfaces
(none)
5. Nomenclature
(no elements)
6. Governing Equations
(no equations)
7. Remarks for Usage
(none)
8. Validation
(no validation or testing necessary)
9. References
(none)
10. Version History
Model created by Philipp Jahneke (philipp.koziol@tuhhl.de), Sept 2018
Model adapted for TransiEnt by Jan Westphal (j.westphal@tuhh.de) in May 2020
Parameters
| Type | Name | Default | Description |
|---|---|---|---|
| SI.StoichiometricNumber | f_sI_xc | Soluble inerts from Composites | |
| SI.StoichiometricNumber | f_xI_xc | Particulate inerts from Composites | |
| SI.StoichiometricNumber | f_ch_xc | Carbohydrates from Composites | |
| SI.StoichiometricNumber | f_pr_xc | Proteins from Composites | |
| SI.StoichiometricNumber | f_li_xc | Lipids from Composites | |
| SI.StoichiometricNumber | f_fa_li | Fatty Acids from Lipids | |
| SI.StoichiometricNumber | f_h2_su | Hydrogen from Sugars | |
| SI.StoichiometricNumber | f_bu_su | Butyrate from Sugars | |
| SI.StoichiometricNumber | f_pro_su | Propionate from Sugars | |
| SI.StoichiometricNumber | f_ac_su | Acetate from Sugars | |
| SI.StoichiometricNumber | f_h2_aa | Hydrogen from Amino Acids | |
| SI.StoichiometricNumber | f_va_aa | Valerate from Amino Acids | |
| SI.StoichiometricNumber | f_bu_aa | Butyrate from Amino Acids | |
| SI.StoichiometricNumber | f_pro_aa | Propionate from Amino Acids | |
| SI.StoichiometricNumber | f_ac_aa | Acetate from Amino Acids | |
| ADM1_Units.MoleContent | C_su | Carbon Content of Sugars in molC/kgCOD | |
| ADM1_Units.MoleContent | C_aa | Carbon Content of Amino Acids in molC/kgCOD | |
| ADM1_Units.MoleContent | C_fa | Carbon Content of LCFA in molC/kgCOD | |
| ADM1_Units.MoleContent | C_va | Carbon Content of Valerate in molC/kgCOD | |
| ADM1_Units.MoleContent | C_bu | Carbon Content of Butyrate in molC/kgCOD | |
| ADM1_Units.MoleContent | C_pro | Carbon Content of Propionate in molC/kgCOD | |
| ADM1_Units.MoleContent | C_ac | Carbon Content of Acetate in molC/kgCOD | |
| ADM1_Units.MoleContent | C_h2 | Carbon Content of Hydrogen in molC/kgCOD | |
| ADM1_Units.MoleContent | C_ch4 | Carbon Content of Methane in molC/kgCOD | |
| ADM1_Units.MoleContent | C_sI | Carbon Content of soluble Inerts in molC/kgCOD | |
| ADM1_Units.MoleContent | C_xc | Carbon Content of Composites in molC/kgCOD | |
| ADM1_Units.MoleContent | C_ch | Carbon Content of Carbohydrates in molC/kgCOD | |
| ADM1_Units.MoleContent | C_pr | Carbon Content of Proteins in molC/kgCOD | |
| ADM1_Units.MoleContent | C_li | Carbon Content of Lipids in molC/kgCOD | |
| ADM1_Units.MoleContent | C_bac | Carbon Content of Microorganisms in molC/kgCOD | |
| ADM1_Units.MoleContent | C_xI | Carbon Content of Particulate Inerts in molC/kgCOD | |
| ADM1_Units.MoleContent | N_aa | Nitrogen Content of Amino Acids in molN/kgCOD | |
| ADM1_Units.MoleContent | N_I | Nitrogen Content of Inerts in molN/kgCOD | |
| ADM1_Units.MoleContent | N_xc | Nitrogen Content of Composites in molN/kgCOD | |
| ADM1_Units.MoleContent | N_bac | Nitrogen Content of Microorganisms in molN/kgCOD | |
| Real | Y_su | Yield of Biomass on Sugars in kgCOD/kgCOD | |
| Real | Y_aa | Yield of Biomass on Amino Acids in kgCOD/kgCOD | |
| Real | Y_fa | Yield of Biomass on LCFA in kgCOD/kgCOD | |
| Real | Y_c4 | Yield of Biomass on Valerate and Butyrate in kgCOD/kgCOD | |
| Real | Y_pro_meso | Yield of Biomass on Propionate in kgCOD/kgCOD | |
| Real | Y_pro_therm | Yield of Biomass on Propionate in kgCOD/kgCOD | |
| Real | Y_ac | Yield of Biomass on Acetate in kgCOD/kgCOD | |
| Real | Y_h2 | Yield of Biomass on Hydrogen in kgCOD/kgCOD | |
| ADM1_Units.KineticRateConstant | k_dis_meso | Disintegration Rate of Composites in 1/s | |
| ADM1_Units.KineticRateConstant | k_hyd_ch_meso | Hydrolyisis Rate of Carbohydrates in 1/s | |
| ADM1_Units.KineticRateConstant | k_hyd_pr_meso | Hydrolyisis Rate of Proteins in 1/s | |
| ADM1_Units.KineticRateConstant | k_hyd_li_meso | Hydrolyisis Rate of Lipids in 1/s | |
| ADM1_Units.KineticRateConstant | k_dec_meso | Decay Rate of Microorganisms in 1/s | |
| ADM1_Units.KineticRateConstant | k_dec_ac_meso | Decay Rate of Acetate Degraders in 1/a | |
| ADM1_Units.KineticRateConstant | k_dis_therm | Disintegration Rate of Composites in 1/s | |
| ADM1_Units.KineticRateConstant | k_hyd_ch_therm | Hydrolyisis Rate of Carbohydrates in 1/s | |
| ADM1_Units.KineticRateConstant | k_hyd_pr_therm | Hydrolyisis Rate of Proteins in 1/s | |
| ADM1_Units.KineticRateConstant | k_hyd_li_therm | Hydrolyisis Rate of Lipids in 1/s | |
| ADM1_Units.KineticRateConstant | k_dec_therm | Decay Rate of Microorganisms in 1/s | |
| ADM1_Units.KineticRateConstant | k_m_su_meso | Maximum Uptake Rate of Sugar by Sugar degraders in kgCOD/kgCOD * 1/s | |
| ADM1_Units.KineticRateConstant | k_m_aa_meso | Maximum Uptake Rate of Amino Acid by Amino Acid degraders in kgCOD/kgCOD * 1/s | |
| ADM1_Units.KineticRateConstant | k_m_fa_meso | Maximum Uptake Rate of LCFA by LCFA degraders in kgCOD/kgCOD * 1/s | |
| ADM1_Units.KineticRateConstant | k_m_c4_meso | Maximum Uptake Rate of Valerate and Butyrate by C4 degraders in kgCOD/kgCOD * 1/s | |
| ADM1_Units.KineticRateConstant | k_m_pro_meso | Maximum Uptake Rate of Propionate by Propionate degraders in kgCOD/kgCOD * 1/s | |
| ADM1_Units.KineticRateConstant | k_m_ac_meso | Maximum Uptake Rate of Acetate by Acetate degraders in kgCOD/kgCOD * 1/s | |
| ADM1_Units.KineticRateConstant | k_m_h2_meso | Maximum Uptake Rate of Hydrogen by Hydrogen degraders in kgCOD/kgCOD * 1/s | |
| ADM1_Units.KineticRateConstant | k_m_su_therm | Maximum Uptake Rate of Sugar by Sugar degraders in kgCOD/kgCOD * 1/s | |
| ADM1_Units.KineticRateConstant | k_m_aa_therm | Maximum Uptake Rate of Amino Acid by Amino Acid degraders in kgCOD/kgCOD * 1/s | |
| ADM1_Units.KineticRateConstant | k_m_fa_therm | Maximum Uptake Rate of LCFA by LCFA degraders in kgCOD/kgCOD * 1/s | |
| ADM1_Units.KineticRateConstant | k_m_c4_therm | Maximum Uptake Rate of Valerate and Butyrate by C4 degraders in kgCOD/kgCOD * 1/s | |
| ADM1_Units.KineticRateConstant | k_m_pro_therm | Maximum Uptake Rate of Propionate by Propionate degraders in kgCOD/kgCOD * 1/s | |
| ADM1_Units.KineticRateConstant | k_m_ac_therm | Maximum Uptake Rate of Acetate by Acetate degraders in kgCOD/kgCOD * 1/s | |
| ADM1_Units.KineticRateConstant | k_m_h2_therm | Maximum Uptake Rate of Hydrogen by Hydrogen degraders in kgCOD/kgCOD * 1/s | |
| ADM1_Units.ConcentrationCOD | K_S_su_meso | Concentration of Sugar at which (uninhibited) uptake equals half of maximum uptake | |
| ADM1_Units.ConcentrationCOD | K_S_aa_meso | Concentration of Amino Acids at which (uninhibited) uptake equals half of maximum uptake | |
| ADM1_Units.ConcentrationCOD | K_S_fa_meso | Concentration of LCFA at which (uninhibited) uptake equals half of maximum uptake | |
| ADM1_Units.ConcentrationCOD | K_S_c4_meso | Concentration of Valerate or Butyrate at which (uninhibited) uptake equals half of maximum uptake | |
| ADM1_Units.ConcentrationCOD | K_S_pro_meso | Concentration of Propionate at which (uninhibited) uptake equals half of maximum uptake | |
| ADM1_Units.ConcentrationCOD | K_S_ac_meso | Concentration of Acetate at which (uninhibited) uptake equals half of maximum uptake | |
| ADM1_Units.ConcentrationCOD | K_S_h2_meso | Concentration of Hydrogen at which (uninhibited) uptake equals half of maximum uptake | |
| ADM1_Units.ConcentrationCOD | K_S_su_therm | Concentration of Sugar at which (uninhibited) uptake equals half of maximum uptake | |
| ADM1_Units.ConcentrationCOD | K_S_aa_therm | Concentration of Amino Acids at which (uninhibited) uptake equals half of maximum uptake | |
| ADM1_Units.ConcentrationCOD | K_S_fa_therm | Concentration of LCFA at which (uninhibited) uptake equals half of maximum uptake | |
| ADM1_Units.ConcentrationCOD | K_S_c4_therm | Concentration of Valerate or Butyrate at which (uninhibited) uptake equals half of maximum uptake | |
| ADM1_Units.ConcentrationCOD | K_S_pro_therm | Concentration of Propionate at which (uninhibited) uptake equals half of maximum uptake | |
| ADM1_Units.ConcentrationCOD | K_S_ac_therm | Concentration of Acetate at which (uninhibited) uptake equals half of maximum uptake | |
| ADM1_Units.ConcentrationCOD | K_S_h2_therm | Concentration of Hydrogen at which (uninhibited) uptake equals half of maximum uptake | |
| Real | pH_UL | pH-Value at which no Inhibition due to low pH occurs | |
| Real | pH_LL | pH-Value at which Uptake and growth are limited to 0.05, thus pH-Inhibition can be considered complete | |
| Real | pH_UL_ac | pH-Value at which Acetate Degraders are not inhibited due to low pH occurs | |
| Real | pH_LL_ac | pH-Value at which Uptake through Acetate Degraders limited to 0.05, thus pH-Inhibition can be considered complete | |
| Real | pH_UL_h2 | pH-Value at which Hydrogen Degraders are not inhibited due to low pH occurs | |
| Real | pH_LL_h2 | pH-Value at which Uptake through Hydrogen Degraders limited to 0.05, thus pH-Inhibition can be considered complete | |
| SI.Concentration | K_S_IN | Inhibition parameter regarding inhibition due to Nitrogen-Defficiency | |
| ADM1_Units.ConcentrationCOD | K_I_H2_fa_meso | Hydrogen Concentration at which LCFA-Degraders are hindered | |
| ADM1_Units.ConcentrationCOD | K_I_H2_c4_meso | ||
| ADM1_Units.ConcentrationCOD | K_I_H2_pro_meso | ||
| SI.Concentration | K_I_NH3_meso | ||
| ADM1_Units.ConcentrationCOD | K_I_H2_c4_therm | ||
| ADM1_Units.ConcentrationCOD | K_I_H2_pro_therm | ||
| SI.Concentration | K_I_NH3_therm | 11 | |
| Real | Kw_ref | ||
| SI.MolarEnergy | deltH0_w | Heat of AcidBase-Reaction | |
| SI.Concentration | Ka_CO2_ref | ||
| SI.MolarEnergy | deltH0_CO2 | Heat of AcidBase-Reaction | |
| SI.Concentration | Ka_HCO3_ref | ||
| SI.MolarEnergy | deltH0_HCO3 | Heat of AcidBase-Reaction | |
| SI.Concentration | Ka_NH4_ref | ||
| SI.MolarEnergy | deltH0_NH4 | Heat of AcidBase-Reaction | |
| SI.Concentration | Ka_H2S_ref | ||
| SI.MolarEnergy | deltH0_H2S | Heat of AcidBase-Reaction | |
| SI.Concentration | Ka_HAc_ref | ||
| SI.Concentration | Ka_HAc_max | ||
| SI.Concentration | Ka_HPro_ref | ||
| SI.Concentration | Ka_HPro_max | ||
| SI.Concentration | Ka_HBu_ref | ||
| SI.Concentration | Ka_HBu_max | ||
| SI.Concentration | Ka_HVa_ref | ||
| Real | k_AB | ||
| ADM1_Units.KineticRateConstant | k_L | Gas-liquid transfer coefficient in 1/s | |
| Real | KH_h2_ref | Henry's law coefficient for Hydrogen | |
| SI.MolarEnergy | deltH0_H_h2 | Heat of Reaction of liquid-gas transfer of Hydrogen at 298K in J/mol | |
| Real | KH_ch4_ref | Henry's law coefficient for Methane | |
| SI.MolarEnergy | deltH0_H_ch4 | Heat of Reaction of liquid-gas transfer of Methane at 298K in J/mol | |
| Real | KH_co2_ref | Henry's law coefficient for Carbondioxide | |
| SI.MolarEnergy | deltH0_H_co2 | Heat of Reaction of liquid-gas transfer of Carbondioxide at 298K in J/mol | |
| SI.PartialPressure | p_h2o_ref | Vapor Pressure of water at 298K in Pa | |
| SI.MolarEnergy | deltH0_vap | Evaporation Heat at 298K in J/mol | |
| SI.MolarEnergy | deltE_su_1 | Reaction Energy of sugar conversion path 1 (50%) per mol sugar at mesophilic conditions | |
| SI.MolarEnergy | deltE_su_2 | Reaction Energy of sugar conversion path 2 (35%) per mol sugar at mesophilic conditions | |
| SI.MolarEnergy | deltE_su_3 | Reaction Energy of sugar conversion path 3 (15%) per mol sugar at mesophilic conditions | |
| SI.MolarEnergy | deltE_aa | Reaction Energy of Amino Acids conversion to acetate, CO2 and ammonia per mol amino acids at mesophilic conditions | |
| SI.MolarEnergy | deltE_fa | Reaction Energy of fatty acids (palmitate) conversion to acetate and hydrogen per mol fatty acid at mesophilic conditions | |
| SI.MolarEnergy | deltE_va | Reaction Energy of valerate conversion to propionate, acetate and hydrogen per mol valerate at mesophilic conditions | |
| SI.MolarEnergy | deltE_bu | Reaction Energy of butyrate conversion to acetate and hydrogen per mol butyrate at mesophilic conditions | |
| SI.MolarEnergy | deltE_pro | Reaction Energy of propionate conversion to acetate, CO2 and hydrogen per mol propionate at mesophilic conditions | |
| SI.MolarEnergy | deltE_ac | Reaction Energy of acetate conversion to CH4 and CO2 per mol acetate at mesophilic conditions | |
| SI.MolarEnergy | deltE_h2 | Reaction Energy of methanation per mol h2 at mesophilic conditions | |
| SI.MolarMass | M_cod_su | Chemical Oxygen Demand in kgCOD per mole Glucose (sugar) | |
| SI.MolarMass | M_cod_aa | Chemical Oxygen Demand in kgCOD per mole Alanine and 2 mole Glycine (Stickland Reaction) | |
| SI.MolarMass | M_cod_fa | Chemical Oxygen Demand in kgCOD per mole Palmitate (fatty acid) | |
| SI.MolarMass | M_cod_va | Chemical Oxygen Demand in kgCOD per mole Valyric Acid | |
| SI.MolarMass | M_cod_bu | Chemical Oxygen Demand in kgCOD per mole Butyric Acid | |
| SI.MolarMass | M_cod_pro | Chemical Oxygen Demand in kgCOD per mole Propionic Acid | |
| SI.MolarMass | M_cod_ac | Chemical Oxygen Demand in kgCOD per mole Acetic Acid | |
| SI.MolarMass | M_cod_h2 | Chemical Oxygen Demand in kgCOD per mole Hydrogen | |
| SI.MolarMass | M_cod_ch4 | Chemical Oxygen Demand in kgCOD per mole Methane | |
| Real | ThOD_Xc | ThOD kgCOD per kg Composites from Lübken et al. (2007). Modelling the energy balance of an anaerobic digester fed with cattle manure and renewable energy crops. | |
| Real | ThOD_XI | ThOD in kgCOD per kg Inerts (Lignin) from Koch, et. al. (2010). Biogas from grass silage–measurements and modeling with ADM1. | |
| Real | ThOD_Xch | ThOD in kgCOD per kg Carbohydrates from Koch, et. al. (2010). Biogas from grass silage–measurements and modeling with ADM1. | |
| Real | ThOD_Xli | ThOD in kgCOD per kg lipids from Koch, et. al. (2010). Biogas from grass silage–measurements and modeling with ADM1. | |
| Real | ThOD_Xpr | ThOD in kgCOD per kg Protein from Koch, et. al. (2010). Biogas from grass silage–measurements and modeling with ADM1. | |
| Real | ThOD_bac | ThOD in kgCOD per kg Microorganisms from Lübken et al. (2007). Modelling the energy balance of an anaerobic digester fed with cattle manure and renewable energy crops. | |
| Real | k_p | pipe resistance coefficient |