recordADM1_parameters_manure_bulkowska

Record with the parameters of Bulkowska et al.

Extends from TransiEnt.Producer.Gas.BiogasPlant.Base.ADM1.Records.ADM1_parameters (Partial record for the parameters of the adm1 model).

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

[1] Bułkowska, K., et al. (2015). ADM1-based modeling of anaerobic codigestion of maize silage and cattle manure–calibration of parameters and model verification (part II)

[2] Bułkowska, K., et al. (2015).ADM1-based modeling of anaerobic codigestion of maize silage and cattle manure – a feedstock characterisation for model implementation (part I)

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

TypeNameDefaultDescription
SI.StoichiometricNumberf_sI_xc (from ADM1_parameters)Soluble inerts from Composites
SI.StoichiometricNumberf_xI_xc (from ADM1_parameters)Particulate inerts from Composites
SI.StoichiometricNumberf_ch_xc (from ADM1_parameters)Carbohydrates from Composites
SI.StoichiometricNumberf_pr_xc (from ADM1_parameters)Proteins from Composites
SI.StoichiometricNumberf_li_xc (from ADM1_parameters)Lipids from Composites
SI.StoichiometricNumberf_fa_li (from ADM1_parameters)Fatty Acids from Lipids
SI.StoichiometricNumberf_h2_su (from ADM1_parameters)Hydrogen from Sugars
SI.StoichiometricNumberf_bu_su (from ADM1_parameters)Butyrate from Sugars
SI.StoichiometricNumberf_pro_su (from ADM1_parameters)Propionate from Sugars
SI.StoichiometricNumberf_ac_su (from ADM1_parameters)Acetate from Sugars
SI.StoichiometricNumberf_h2_aa (from ADM1_parameters)Hydrogen from Amino Acids
SI.StoichiometricNumberf_va_aa (from ADM1_parameters)Valerate from Amino Acids
SI.StoichiometricNumberf_bu_aa (from ADM1_parameters)Butyrate from Amino Acids
SI.StoichiometricNumberf_pro_aa (from ADM1_parameters)Propionate from Amino Acids
SI.StoichiometricNumberf_ac_aa (from ADM1_parameters)Acetate from Amino Acids
ADM1_Units.MoleContentC_su (from ADM1_parameters)Carbon Content of Sugars in molC/kgCOD
ADM1_Units.MoleContentC_aa (from ADM1_parameters)Carbon Content of Amino Acids in molC/kgCOD
ADM1_Units.MoleContentC_fa (from ADM1_parameters)Carbon Content of LCFA in molC/kgCOD
ADM1_Units.MoleContentC_va (from ADM1_parameters)Carbon Content of Valerate in molC/kgCOD
ADM1_Units.MoleContentC_bu (from ADM1_parameters)Carbon Content of Butyrate in molC/kgCOD
ADM1_Units.MoleContentC_pro (from ADM1_parameters)Carbon Content of Propionate in molC/kgCOD
ADM1_Units.MoleContentC_ac (from ADM1_parameters)Carbon Content of Acetate in molC/kgCOD
ADM1_Units.MoleContentC_h2 (from ADM1_parameters)Carbon Content of Hydrogen in molC/kgCOD
ADM1_Units.MoleContentC_ch4 (from ADM1_parameters)Carbon Content of Methane in molC/kgCOD
ADM1_Units.MoleContentC_sI (from ADM1_parameters)Carbon Content of soluble Inerts in molC/kgCOD
ADM1_Units.MoleContentC_xc (from ADM1_parameters)Carbon Content of Composites in molC/kgCOD
ADM1_Units.MoleContentC_ch (from ADM1_parameters)Carbon Content of Carbohydrates in molC/kgCOD
ADM1_Units.MoleContentC_pr (from ADM1_parameters)Carbon Content of Proteins in molC/kgCOD
ADM1_Units.MoleContentC_li (from ADM1_parameters)Carbon Content of Lipids in molC/kgCOD
ADM1_Units.MoleContentC_bac (from ADM1_parameters)Carbon Content of Microorganisms in molC/kgCOD
ADM1_Units.MoleContentC_xI (from ADM1_parameters)Carbon Content of Particulate Inerts in molC/kgCOD
ADM1_Units.MoleContentN_aa (from ADM1_parameters)Nitrogen Content of Amino Acids in molN/kgCOD
ADM1_Units.MoleContentN_I (from ADM1_parameters)Nitrogen Content of Inerts in molN/kgCOD
ADM1_Units.MoleContentN_xc (from ADM1_parameters)Nitrogen Content of Composites in molN/kgCOD
ADM1_Units.MoleContentN_bac (from ADM1_parameters)Nitrogen Content of Microorganisms in molN/kgCOD
RealY_su (from ADM1_parameters)Yield of Biomass on Sugars in kgCOD/kgCOD
RealY_aa (from ADM1_parameters)Yield of Biomass on Amino Acids in kgCOD/kgCOD
RealY_fa (from ADM1_parameters)Yield of Biomass on LCFA in kgCOD/kgCOD
RealY_c4 (from ADM1_parameters)Yield of Biomass on Valerate and Butyrate in kgCOD/kgCOD
RealY_pro_meso (from ADM1_parameters)Yield of Biomass on Propionate in kgCOD/kgCOD
RealY_pro_therm (from ADM1_parameters)Yield of Biomass on Propionate in kgCOD/kgCOD
RealY_ac (from ADM1_parameters)Yield of Biomass on Acetate in kgCOD/kgCOD
RealY_h2 (from ADM1_parameters)Yield of Biomass on Hydrogen in kgCOD/kgCOD
ADM1_Units.KineticRateConstantk_dis_meso (from ADM1_parameters)Disintegration Rate of Composites in 1/s
ADM1_Units.KineticRateConstantk_hyd_ch_meso (from ADM1_parameters)Hydrolyisis Rate of Carbohydrates in 1/s
ADM1_Units.KineticRateConstantk_hyd_pr_meso (from ADM1_parameters)Hydrolyisis Rate of Proteins in 1/s
ADM1_Units.KineticRateConstantk_hyd_li_meso (from ADM1_parameters)Hydrolyisis Rate of Lipids in 1/s
ADM1_Units.KineticRateConstantk_dec_meso (from ADM1_parameters)Decay Rate of Microorganisms in 1/s
ADM1_Units.KineticRateConstantk_dec_ac_meso (from ADM1_parameters)Decay Rate of Acetate Degraders in 1/a
ADM1_Units.KineticRateConstantk_dis_therm (from ADM1_parameters)Disintegration Rate of Composites in 1/s
ADM1_Units.KineticRateConstantk_hyd_ch_therm (from ADM1_parameters)Hydrolyisis Rate of Carbohydrates in 1/s
ADM1_Units.KineticRateConstantk_hyd_pr_therm (from ADM1_parameters)Hydrolyisis Rate of Proteins in 1/s
ADM1_Units.KineticRateConstantk_hyd_li_therm (from ADM1_parameters)Hydrolyisis Rate of Lipids in 1/s
ADM1_Units.KineticRateConstantk_dec_therm (from ADM1_parameters)Decay Rate of Microorganisms in 1/s
ADM1_Units.KineticRateConstantk_m_su_meso (from ADM1_parameters)Maximum Uptake Rate of Sugar by Sugar degraders in kgCOD/kgCOD * 1/s
ADM1_Units.KineticRateConstantk_m_aa_meso (from ADM1_parameters)Maximum Uptake Rate of Amino Acid by Amino Acid degraders in kgCOD/kgCOD * 1/s
ADM1_Units.KineticRateConstantk_m_fa_meso (from ADM1_parameters)Maximum Uptake Rate of LCFA by LCFA degraders in kgCOD/kgCOD * 1/s
ADM1_Units.KineticRateConstantk_m_c4_meso (from ADM1_parameters)Maximum Uptake Rate of Valerate and Butyrate by C4 degraders in kgCOD/kgCOD * 1/s
ADM1_Units.KineticRateConstantk_m_pro_meso (from ADM1_parameters)Maximum Uptake Rate of Propionate by Propionate degraders in kgCOD/kgCOD * 1/s
ADM1_Units.KineticRateConstantk_m_ac_meso (from ADM1_parameters)Maximum Uptake Rate of Acetate by Acetate degraders in kgCOD/kgCOD * 1/s
ADM1_Units.KineticRateConstantk_m_h2_meso (from ADM1_parameters)Maximum Uptake Rate of Hydrogen by Hydrogen degraders in kgCOD/kgCOD * 1/s
ADM1_Units.KineticRateConstantk_m_su_therm (from ADM1_parameters)Maximum Uptake Rate of Sugar by Sugar degraders in kgCOD/kgCOD * 1/s
ADM1_Units.KineticRateConstantk_m_aa_therm (from ADM1_parameters)Maximum Uptake Rate of Amino Acid by Amino Acid degraders in kgCOD/kgCOD * 1/s
ADM1_Units.KineticRateConstantk_m_fa_therm (from ADM1_parameters)Maximum Uptake Rate of LCFA by LCFA degraders in kgCOD/kgCOD * 1/s
ADM1_Units.KineticRateConstantk_m_c4_therm (from ADM1_parameters)Maximum Uptake Rate of Valerate and Butyrate by C4 degraders in kgCOD/kgCOD * 1/s
ADM1_Units.KineticRateConstantk_m_pro_therm (from ADM1_parameters)Maximum Uptake Rate of Propionate by Propionate degraders in kgCOD/kgCOD * 1/s
ADM1_Units.KineticRateConstantk_m_ac_therm (from ADM1_parameters)Maximum Uptake Rate of Acetate by Acetate degraders in kgCOD/kgCOD * 1/s
ADM1_Units.KineticRateConstantk_m_h2_therm (from ADM1_parameters)Maximum Uptake Rate of Hydrogen by Hydrogen degraders in kgCOD/kgCOD * 1/s
ADM1_Units.ConcentrationCODK_S_su_meso (from ADM1_parameters)Concentration of Sugar at which (uninhibited) uptake equals half of maximum uptake
ADM1_Units.ConcentrationCODK_S_aa_meso (from ADM1_parameters)Concentration of Amino Acids at which (uninhibited) uptake equals half of maximum uptake
ADM1_Units.ConcentrationCODK_S_fa_meso (from ADM1_parameters)Concentration of LCFA at which (uninhibited) uptake equals half of maximum uptake
ADM1_Units.ConcentrationCODK_S_c4_meso (from ADM1_parameters)Concentration of Valerate or Butyrate at which (uninhibited) uptake equals half of maximum uptake
ADM1_Units.ConcentrationCODK_S_pro_meso (from ADM1_parameters)Concentration of Propionate at which (uninhibited) uptake equals half of maximum uptake
ADM1_Units.ConcentrationCODK_S_ac_meso (from ADM1_parameters)Concentration of Acetate at which (uninhibited) uptake equals half of maximum uptake
ADM1_Units.ConcentrationCODK_S_h2_meso (from ADM1_parameters)Concentration of Hydrogen at which (uninhibited) uptake equals half of maximum uptake
ADM1_Units.ConcentrationCODK_S_su_therm (from ADM1_parameters)Concentration of Sugar at which (uninhibited) uptake equals half of maximum uptake
ADM1_Units.ConcentrationCODK_S_aa_therm (from ADM1_parameters)Concentration of Amino Acids at which (uninhibited) uptake equals half of maximum uptake
ADM1_Units.ConcentrationCODK_S_fa_therm (from ADM1_parameters)Concentration of LCFA at which (uninhibited) uptake equals half of maximum uptake
ADM1_Units.ConcentrationCODK_S_c4_therm (from ADM1_parameters)Concentration of Valerate or Butyrate at which (uninhibited) uptake equals half of maximum uptake
ADM1_Units.ConcentrationCODK_S_pro_therm (from ADM1_parameters)Concentration of Propionate at which (uninhibited) uptake equals half of maximum uptake
ADM1_Units.ConcentrationCODK_S_ac_therm (from ADM1_parameters)Concentration of Acetate at which (uninhibited) uptake equals half of maximum uptake
ADM1_Units.ConcentrationCODK_S_h2_therm (from ADM1_parameters)Concentration of Hydrogen at which (uninhibited) uptake equals half of maximum uptake
RealpH_UL (from ADM1_parameters)pH-Value at which no Inhibition due to low pH occurs
RealpH_LL (from ADM1_parameters)pH-Value at which Uptake and growth are limited to 0.05, thus pH-Inhibition can be considered complete
RealpH_UL_ac (from ADM1_parameters)pH-Value at which Acetate Degraders are not inhibited due to low pH occurs
RealpH_LL_ac (from ADM1_parameters)pH-Value at which Uptake through Acetate Degraders limited to 0.05, thus pH-Inhibition can be considered complete
RealpH_UL_h2 (from ADM1_parameters)pH-Value at which Hydrogen Degraders are not inhibited due to low pH occurs
RealpH_LL_h2 (from ADM1_parameters)pH-Value at which Uptake through Hydrogen Degraders limited to 0.05, thus pH-Inhibition can be considered complete
SI.ConcentrationK_S_IN (from ADM1_parameters)Inhibition parameter regarding inhibition due to Nitrogen-Defficiency
ADM1_Units.ConcentrationCODK_I_H2_fa_meso (from ADM1_parameters)Hydrogen Concentration at which LCFA-Degraders are hindered
ADM1_Units.ConcentrationCODK_I_H2_c4_meso (from ADM1_parameters)
ADM1_Units.ConcentrationCODK_I_H2_pro_meso (from ADM1_parameters)
SI.ConcentrationK_I_NH3_meso (from ADM1_parameters)
ADM1_Units.ConcentrationCODK_I_H2_c4_therm (from ADM1_parameters)
ADM1_Units.ConcentrationCODK_I_H2_pro_therm (from ADM1_parameters)
SI.ConcentrationK_I_NH3_therm (from ADM1_parameters)11
RealKw_ref (from ADM1_parameters)
SI.MolarEnergydeltH0_w (from ADM1_parameters)Heat of AcidBase-Reaction
SI.ConcentrationKa_CO2_ref (from ADM1_parameters)
SI.MolarEnergydeltH0_CO2 (from ADM1_parameters)Heat of AcidBase-Reaction
SI.ConcentrationKa_HCO3_ref (from ADM1_parameters)
SI.MolarEnergydeltH0_HCO3 (from ADM1_parameters)Heat of AcidBase-Reaction
SI.ConcentrationKa_NH4_ref (from ADM1_parameters)
SI.MolarEnergydeltH0_NH4 (from ADM1_parameters)Heat of AcidBase-Reaction
SI.ConcentrationKa_H2S_ref (from ADM1_parameters)
SI.MolarEnergydeltH0_H2S (from ADM1_parameters)Heat of AcidBase-Reaction
SI.ConcentrationKa_HAc_ref (from ADM1_parameters)
SI.ConcentrationKa_HAc_max (from ADM1_parameters)
SI.ConcentrationKa_HPro_ref (from ADM1_parameters)
SI.ConcentrationKa_HPro_max (from ADM1_parameters)
SI.ConcentrationKa_HBu_ref (from ADM1_parameters)
SI.ConcentrationKa_HBu_max (from ADM1_parameters)
SI.ConcentrationKa_HVa_ref (from ADM1_parameters)
Realk_AB (from ADM1_parameters)
ADM1_Units.KineticRateConstantk_L (from ADM1_parameters)Gas-liquid transfer coefficient in 1/s
RealKH_h2_ref (from ADM1_parameters)Henry's law coefficient for Hydrogen
SI.MolarEnergydeltH0_H_h2 (from ADM1_parameters)Heat of Reaction of liquid-gas transfer of Hydrogen at 298K in J/mol
RealKH_ch4_ref (from ADM1_parameters)Henry's law coefficient for Methane
SI.MolarEnergydeltH0_H_ch4 (from ADM1_parameters)Heat of Reaction of liquid-gas transfer of Methane at 298K in J/mol
RealKH_co2_ref (from ADM1_parameters)Henry's law coefficient for Carbondioxide
SI.MolarEnergydeltH0_H_co2 (from ADM1_parameters)Heat of Reaction of liquid-gas transfer of Carbondioxide at 298K in J/mol
SI.PartialPressurep_h2o_ref (from ADM1_parameters)Vapor Pressure of water at 298K in Pa
SI.MolarEnergydeltH0_vap (from ADM1_parameters)Evaporation Heat at 298K in J/mol
SI.MolarEnergydeltE_su_1 (from ADM1_parameters)Reaction Energy of sugar conversion path 1 (50%) per mol sugar at mesophilic conditions
SI.MolarEnergydeltE_su_2 (from ADM1_parameters)Reaction Energy of sugar conversion path 2 (35%) per mol sugar at mesophilic conditions
SI.MolarEnergydeltE_su_3 (from ADM1_parameters)Reaction Energy of sugar conversion path 3 (15%) per mol sugar at mesophilic conditions
SI.MolarEnergydeltE_aa (from ADM1_parameters)Reaction Energy of Amino Acids conversion to acetate, CO2 and ammonia per mol amino acids at mesophilic conditions
SI.MolarEnergydeltE_fa (from ADM1_parameters)Reaction Energy of fatty acids (palmitate) conversion to acetate and hydrogen per mol fatty acid at mesophilic conditions
SI.MolarEnergydeltE_va (from ADM1_parameters)Reaction Energy of valerate conversion to propionate, acetate and hydrogen per mol valerate at mesophilic conditions
SI.MolarEnergydeltE_bu (from ADM1_parameters)Reaction Energy of butyrate conversion to acetate and hydrogen per mol butyrate at mesophilic conditions
SI.MolarEnergydeltE_pro (from ADM1_parameters)Reaction Energy of propionate conversion to acetate, CO2 and hydrogen per mol propionate at mesophilic conditions
SI.MolarEnergydeltE_ac (from ADM1_parameters)Reaction Energy of acetate conversion to CH4 and CO2 per mol acetate at mesophilic conditions
SI.MolarEnergydeltE_h2 (from ADM1_parameters)Reaction Energy of methanation per mol h2 at mesophilic conditions
SI.MolarMassM_cod_su (from ADM1_parameters)Chemical Oxygen Demand in kgCOD per mole Glucose (sugar)
SI.MolarMassM_cod_aa (from ADM1_parameters)Chemical Oxygen Demand in kgCOD per mole Alanine and 2 mole Glycine (Stickland Reaction)
SI.MolarMassM_cod_fa (from ADM1_parameters)Chemical Oxygen Demand in kgCOD per mole Palmitate (fatty acid)
SI.MolarMassM_cod_va (from ADM1_parameters)Chemical Oxygen Demand in kgCOD per mole Valyric Acid
SI.MolarMassM_cod_bu (from ADM1_parameters)Chemical Oxygen Demand in kgCOD per mole Butyric Acid
SI.MolarMassM_cod_pro (from ADM1_parameters)Chemical Oxygen Demand in kgCOD per mole Propionic Acid
SI.MolarMassM_cod_ac (from ADM1_parameters)Chemical Oxygen Demand in kgCOD per mole Acetic Acid
SI.MolarMassM_cod_h2 (from ADM1_parameters)Chemical Oxygen Demand in kgCOD per mole Hydrogen
SI.MolarMassM_cod_ch4 (from ADM1_parameters)Chemical Oxygen Demand in kgCOD per mole Methane
RealThOD_Xc (from ADM1_parameters)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.
RealThOD_XI (from ADM1_parameters)ThOD in kgCOD per kg Inerts (Lignin) from Koch, et. al. (2010). Biogas from grass silage–measurements and modeling with ADM1.
RealThOD_Xch (from ADM1_parameters)ThOD in kgCOD per kg Carbohydrates from Koch, et. al. (2010). Biogas from grass silage–measurements and modeling with ADM1.
RealThOD_Xli (from ADM1_parameters)ThOD in kgCOD per kg lipids from Koch, et. al. (2010). Biogas from grass silage–measurements and modeling with ADM1.
RealThOD_Xpr (from ADM1_parameters)ThOD in kgCOD per kg Protein from Koch, et. al. (2010). Biogas from grass silage–measurements and modeling with ADM1.
RealThOD_bac (from ADM1_parameters)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.
Realk_p (from ADM1_parameters)pipe resistance coefficient