modeling and analysis of anaerobic digestion in a bioreactor
TRANSCRIPT
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Modeling and Analysis of Anaerobic Digestion in aBioreactor
Christina Berti
REU 2013
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Advantages of Wastewater Treatment
Recycle water
Produce biogas
Minimal pollution
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Advantages of Wastewater Treatment
Recycle water
Produce biogas
Minimal pollution
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Advantages of Wastewater Treatment
Recycle water
Produce biogas
Minimal pollution
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Degradation Process
Biodegradable Organic Matter Inert Material,Biproducts
Acidogenesis
Hydrolysis
Acidogenesis
Acetogenesis
46%
70%
20%
40%
13%
100%
21%
30%
34%
21%5%
Methanogenesis
S2
S2
X2
X1
S1
Amino Acids, Simple Sugars Fatty Acids
Proteins Carbohydrates Lipids
Propionate, Butyrate, etc.
Hydrogen, Carbon DioxideAcetate
Biogas
Complex Organic MatterRaw Material: sludge, slurries, lump compound
Methane, Carbon Dioxide
Figure : Detailed Flowchart of Model for Biogas Production
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Condensed 4-Dimensional (two-step reaction process)System
Definition
4-Dimensional System:
S ′1 = −X1k1(µ1(S1)) + D(S1in − S1)X ′1 = X1(µ1(S1) − Dα)S ′2 = D(S2in − S2) + X1k2(µ1(S1)) − X2k3(µ2(S2))X ′2 = X2(µ2(S2) − Dα)
(1)
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Parameter Value Ranges and Definitions
S1in and S2in : Input substrate concentrations.
k1, k2, k3 : Pseudo-stoichiometric coefficients based on natureof bioreactions.
α : Fraction of biomass not retained in the digester (accountsfor decoupling of Hydraulic Retention Time from SolidRetention Time).
D: Dilution factor for incoming and outgoing substrate andbacteria.
µ1(S1) and µ2(S2) are functions used to demonstrate thegrowth of bacteria 1 and 2, respectively.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Parameter Value Ranges and Definitions
S1in and S2in : Input substrate concentrations.
k1, k2, k3 : Pseudo-stoichiometric coefficients based on natureof bioreactions.
α : Fraction of biomass not retained in the digester (accountsfor decoupling of Hydraulic Retention Time from SolidRetention Time).
D: Dilution factor for incoming and outgoing substrate andbacteria.
µ1(S1) and µ2(S2) are functions used to demonstrate thegrowth of bacteria 1 and 2, respectively.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Parameter Value Ranges and Definitions
S1in and S2in : Input substrate concentrations.
k1, k2, k3 : Pseudo-stoichiometric coefficients based on natureof bioreactions.
α : Fraction of biomass not retained in the digester (accountsfor decoupling of Hydraulic Retention Time from SolidRetention Time).
D: Dilution factor for incoming and outgoing substrate andbacteria.
µ1(S1) and µ2(S2) are functions used to demonstrate thegrowth of bacteria 1 and 2, respectively.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Parameter Value Ranges and Definitions
S1in and S2in : Input substrate concentrations.
k1, k2, k3 : Pseudo-stoichiometric coefficients based on natureof bioreactions.
α : Fraction of biomass not retained in the digester (accountsfor decoupling of Hydraulic Retention Time from SolidRetention Time).
D: Dilution factor for incoming and outgoing substrate andbacteria.
µ1(S1) and µ2(S2) are functions used to demonstrate thegrowth of bacteria 1 and 2, respectively.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Parameter Value Ranges and Definitions
S1in and S2in : Input substrate concentrations.
k1, k2, k3 : Pseudo-stoichiometric coefficients based on natureof bioreactions.
α : Fraction of biomass not retained in the digester (accountsfor decoupling of Hydraulic Retention Time from SolidRetention Time).
D: Dilution factor for incoming and outgoing substrate andbacteria.
µ1(S1) and µ2(S2) are functions used to demonstrate thegrowth of bacteria 1 and 2, respectively.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Simplified Two-Step Reaction Process
Definition
Two Steps:
Acidogenesis : k1S1µ1(S1)X1−→ X1 + k2S2
Methanogenesis : k3S2µ2(S2)X2−→ X2 + k4CH4
(2)
Acidogenesis: Organic substrate (S1) is broken down into volatilefatty acids (S2) by acidogenic bacteria (X1).
Methanogenesis: Volatile fatty acids (S2) are degraded to produceCH4 and CO2 by methanogenic bacteria (X2).
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Concerns Regarding Approach to Attaining Steady-State
Two Main Concerns:
Growth of Bacteria
Substrate Degredation and Product Formation
To attain a steady-state: The substrate flow and gas productionmust remain constant and continuous. The growth requirementsfor bacteria must remain constant over time.
Definition
4-Dimensional System:
0 = −X1k1(µ1(S1)) + D(S1in − S1)0 = X1(µ1(S1) − Dα)0 = D(S2in − S2) + X1k2(µ1(S1)) − X2k3(µ2(S2))0 = X2(µ2(S2) − Dα)
(3)
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Concerns Regarding Approach to Attaining Steady-State
Two Main Concerns:
Growth of Bacteria
Substrate Degredation and Product Formation
To attain a steady-state: The substrate flow and gas productionmust remain constant and continuous. The growth requirementsfor bacteria must remain constant over time.
Definition
4-Dimensional System:
0 = −X1k1(µ1(S1)) + D(S1in − S1)0 = X1(µ1(S1) − Dα)0 = D(S2in − S2) + X1k2(µ1(S1)) − X2k3(µ2(S2))0 = X2(µ2(S2) − Dα)
(3)
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Steady-State
Substrate Balance: dSdt = DS0 − DS + dS
dt
Bacteria Balance: dXdt = DX0 − DX + µ(S)X + kdX
Equilibrium point: dXdt = 0 dS
dt = 0 as t −→∞
dSdt and dX
dt : Accumulation
DS0 and DX0: Diluted Input DS and DX : Diluted Output
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Different Approaches
Each differential system under study was characterized by itsunique combination of two of the numerous hypothesized bacterialgrowth functions; our study included application of the Monod andHaldane functions of bacteria growth [d ],
Monod: µ1(S1) = m1S1K1+S1
Haldane: µ2(S2) = m2S2
K2+S2+S22
KI
m1 and m2: Define the maximum attainable speeds of X1 andX2 growth, respectively.
K1 and K2 : Substrate Concentrations at 50 percent ofmaximum specific growth rate(see graph).
KI : Substrate concentration where bacteria growth is reducedto 50 percent of it’s maximum growth rate due to substrateinhibition (see graph).
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Different Approaches
Each differential system under study was characterized by itsunique combination of two of the numerous hypothesized bacterialgrowth functions; our study included application of the Monod andHaldane functions of bacteria growth [d ],
Monod: µ1(S1) = m1S1K1+S1
Haldane: µ2(S2) = m2S2
K2+S2+S22
KI
m1 and m2: Define the maximum attainable speeds of X1 andX2 growth, respectively.
K1 and K2 : Substrate Concentrations at 50 percent ofmaximum specific growth rate(see graph).
KI : Substrate concentration where bacteria growth is reducedto 50 percent of it’s maximum growth rate due to substrateinhibition (see graph).
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Different Approaches
Each differential system under study was characterized by itsunique combination of two of the numerous hypothesized bacterialgrowth functions; our study included application of the Monod andHaldane functions of bacteria growth [d ],
Monod: µ1(S1) = m1S1K1+S1
Haldane: µ2(S2) = m2S2
K2+S2+S22
KI
m1 and m2: Define the maximum attainable speeds of X1 andX2 growth, respectively.
K1 and K2 : Substrate Concentrations at 50 percent ofmaximum specific growth rate(see graph).
KI : Substrate concentration where bacteria growth is reducedto 50 percent of it’s maximum growth rate due to substrateinhibition (see graph).
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Bacteria Growth Kinetics
0 4 80
m
S (Substrate Concentration)
Monod Model of Bacteria Growth Kineticsu(S) = (mS)/(K+S)
u(S
)
Approaching Maximum Growth Rate (m)
50% Maximum Growth Rate (m/2)
Substrate Concentration (K) at m/2
Figure : Monod Model for Bacteria Growth Kinetics
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Bacteria Growth Kinetics
0 10 20 30 40 50 600
0.1
0.2
0.3
0.4
0.5
0.6
S (Substrate Concentration)
Haldane Model of Bacteria Growth Kinetics u(S) = (mS)/(K+S+(S2)/KI)
u(S
)
50% Maximum GrowthRate of Bacteria
Substrate Concentration (KI) at 50% ofMaximum Growth Rate of Bacteria
Substrate Concentration(K1) at 50% of MaximumGrowth Rate of Bacteria
Figure : Haldane Model for Bacteria Growth Kinetics
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Theory Behind Four-Dimensional Systems A and B
Two Hypotheses:
4-Dimensional System A: The growth rates of X1 and X2 areboth increasing functions of added substrate (S1 and S2).
µ1(S1) = m1S1K1+S1
µ2(S2) = m2S2K2+S2
4-Dimensional System B: The growth rate of X1 is anincreasing function of substrate (S1) and the growth rate ofX2 approaches a maximum at a medium substrateconcentration (KI = medium S2 concentration).
µ1(S1) = m1S1K1+S1
µ2(S2) = m2S2
K2+S2+S22
KI
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Introduction of Foreign Toxin
S ′1 = −X1k1e−yµ(µ1(S1)) + D(S1in − S1)
X ′1 = X1(e−yµµ1(S1) − Dα)S ′2 = D(S2in − S2) + X1k2e
−yµ(µ1(S1)) − X2k3(µ2(S2))X ′2 = X2(µ2(S2) − Dα)y ′ = D(yin − y)− X2k4µ3(y)
(4)
where y represents the toxin.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Inhibition Caused by Foreign Species
Types of Inhibition
Competitive Inhibition: A foreign species similar in structureto the substrate binds to the enzymes, inhibiting reactionspots.
Noncompetitive Inhibition: A foreign species not necessarilysimilar in structure to the substrate binds to the enzymesand/or enzyme-substrate complexes, preventing completion ofthe reaction.
Uncompetitive Inhibition: A foreign species not necessarilysimilar in structure to the substrate binds to theenzyme-substrate complexes, preventing completion of thereaction.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Inhibition Caused by Foreign Species
Types of Inhibition
Competitive Inhibition: A foreign species similar in structureto the substrate binds to the enzymes, inhibiting reactionspots.
Noncompetitive Inhibition: A foreign species not necessarilysimilar in structure to the substrate binds to the enzymesand/or enzyme-substrate complexes, preventing completion ofthe reaction.
Uncompetitive Inhibition: A foreign species not necessarilysimilar in structure to the substrate binds to theenzyme-substrate complexes, preventing completion of thereaction.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Inhibition Caused by Foreign Species
Types of Inhibition
Competitive Inhibition: A foreign species similar in structureto the substrate binds to the enzymes, inhibiting reactionspots.
Noncompetitive Inhibition: A foreign species not necessarilysimilar in structure to the substrate binds to the enzymesand/or enzyme-substrate complexes, preventing completion ofthe reaction.
Uncompetitive Inhibition: A foreign species not necessarilysimilar in structure to the substrate binds to theenzyme-substrate complexes, preventing completion of thereaction.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Effect of a Toxin
0
S (Substrate Concentration)
Inhibition Caused by Foreign Species
Gro
wth
Rat
e o
f B
acte
ria
Maximum Attainable Growth Rateof Bacteria in Presence of
Noncompetitively orUncompetitively Behaving
ForeignSpecies
MaximumAttainable
Growth Rate ofBacteria
Maximum AttainableGrowth Rate of Bacteria in
Presence of Competitively BehavingForeign Species
Figure : Illustrations of Competition by Non-Substrate Species
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Five-Dimensional Systems
The four systems differed amongst each other in terms of themodels used to represent X2 growth and toxin consumption.
Four Hypotheses:
5-Dimensional System A: The Monod model is used torepresent the growth rate of X1, the Haldane model is used torepresent the growth rate of X2, and the Monod model is usedto represent the consumption rate of the toxin.
µ(S1) = m1S1K1+S1
µ(S2) = m2S2
K2+S2+S22
KI1
µ(y) = m4yK4+y
5-Dimensional System B: The Monod model is used torepresent the growth rate of X1, the Haldane model is used torepresent both the growth rate of X2 and the consumptionrate of the toxin.
µ(S1) = m1S1K1+S1
µ(S2) = m2S2
K2+S2+S22
KI1
µ(y) = m4y
K4+y+ y2
KI2
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Five-Dimensional Systems
The four systems differed amongst each other in terms of themodels used to represent X2 growth and toxin consumption.
Four Hypotheses:
5-Dimensional System A: The Monod model is used torepresent the growth rate of X1, the Haldane model is used torepresent the growth rate of X2, and the Monod model is usedto represent the consumption rate of the toxin.
µ(S1) = m1S1K1+S1
µ(S2) = m2S2
K2+S2+S22
KI1
µ(y) = m4yK4+y
5-Dimensional System B: The Monod model is used torepresent the growth rate of X1, the Haldane model is used torepresent both the growth rate of X2 and the consumptionrate of the toxin.
µ(S1) = m1S1K1+S1
µ(S2) = m2S2
K2+S2+S22
KI1
µ(y) = m4y
K4+y+ y2
KI2
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Five-Dimensional Systems
The four systems differed amongst each other in terms of themodels used to represent X2 growth and toxin consumption.
Four Hypotheses:
5-Dimensional System C: The Monod model is used torepresent the growth rate of X1, the growth rate of X2, andthe consumption rate of the toxin.
µ(S1) = m1S1K1+S1
µ(S2) = m2S2K2+S2
µ(y) = m4yK4+y
5-Dimensional System D: The Monod model is used torepresent the growth rate of Bacteria 1 and 2, and theHaldane model is used to represent the consumption rate ofthe toxin.
µ(S1) = m1S1K1+S1
µ(S2) = m2S2K2+S2
µ(y) = m4y
K4+y+ y2
KI2
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Five-Dimensional Systems
The four systems differed amongst each other in terms of themodels used to represent X2 growth and toxin consumption.
Four Hypotheses:
5-Dimensional System C: The Monod model is used torepresent the growth rate of X1, the growth rate of X2, andthe consumption rate of the toxin.
µ(S1) = m1S1K1+S1
µ(S2) = m2S2K2+S2
µ(y) = m4yK4+y
5-Dimensional System D: The Monod model is used torepresent the growth rate of Bacteria 1 and 2, and theHaldane model is used to represent the consumption rate ofthe toxin.
µ(S1) = m1S1K1+S1
µ(S2) = m2S2K2+S2
µ(y) = m4y
K4+y+ y2
KI2
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Six-Dimensional System
S ′1 = −X1k1(µ1(S1)) + D(S1(1 + (rv)) − S1)X ′1 = X1(P(µ1(S1) − Dα))S ′2 = D(0− S2) + X1k2(µ1(S1)) − X2k3(µ2(S2))X ′2 = X2(µ2(S2) − Dα)u′ = u(1 − u2 − v2) − 2πv
v ′ = v(1 − u) − v2) + 2πu
(5)
where S1(1 + (rv)) = S1(t) = S1(1 + (r sin(2πt)))and 0 ≤ r ≤ 1.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Solving the 4-Dimensional Systems
Algebraically Determine all Attainable Equilibria
x0 = (S1, X1, S2, X2)
Linearize nonlinear system by formulating Jacobian matricesand solving for respective eigenvalue functions.
A = Df (x0) det(A− Iλ) = 0
Determine the number of potential equilibrium points andexpected behavior of each one according to the calculatedeigenvalues.
Verify Algebraically Determined Discoveries with Illustrationsof Behavior
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Solving the 4-Dimensional Systems
Algebraically Determine all Attainable Equilibria
x0 = (S1, X1, S2, X2)
Linearize nonlinear system by formulating Jacobian matricesand solving for respective eigenvalue functions.
A = Df (x0) det(A− Iλ) = 0
Determine the number of potential equilibrium points andexpected behavior of each one according to the calculatedeigenvalues.
Verify Algebraically Determined Discoveries with Illustrationsof Behavior
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Solving the 4-Dimensional Systems
Algebraically Determine all Attainable Equilibria
x0 = (S1, X1, S2, X2)
Linearize nonlinear system by formulating Jacobian matricesand solving for respective eigenvalue functions.
A = Df (x0) det(A− Iλ) = 0
Determine the number of potential equilibrium points andexpected behavior of each one according to the calculatedeigenvalues.
Verify Algebraically Determined Discoveries with Illustrationsof Behavior
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Solving the 4-Dimensional Systems
Algebraically Determine all Attainable Equilibria
x0 = (S1, X1, S2, X2)
Linearize nonlinear system by formulating Jacobian matricesand solving for respective eigenvalue functions.
A = Df (x0) det(A− Iλ) = 0
Determine the number of potential equilibrium points andexpected behavior of each one according to the calculatedeigenvalues.
Verify Algebraically Determined Discoveries with Illustrationsof Behavior
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Possible Results
Hyperbolic Equilibria
All eigenvalues are nonzero values, nor are any ofthem purely imaginary.
Saddle
Stable NodeFocus
Nonhyperbolic Equilibria
One eigenvalue is equal to zero or is purelyimaginary. The system is susceptible to a bifurcationwith small changes in parameter values.
Center
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Possible Results
Hyperbolic Equilibria
All eigenvalues are nonzero values, nor are any ofthem purely imaginary.
SaddleStable Node
Focus
Nonhyperbolic Equilibria
One eigenvalue is equal to zero or is purelyimaginary. The system is susceptible to a bifurcationwith small changes in parameter values.
Center
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Possible Results
Hyperbolic Equilibria
All eigenvalues are nonzero values, nor are any ofthem purely imaginary.
SaddleStable NodeFocus
Nonhyperbolic Equilibria
One eigenvalue is equal to zero or is purelyimaginary. The system is susceptible to a bifurcationwith small changes in parameter values.
Center
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Types of Bifurcations
Bifurcation Value = Parameter Value at which Bifurcation Occurs(Dilution Factor, D, acted as the variable parameter value)
Transcritical BifurcationNo change in the number of equilibrium points.Switch in stability of equilibria at bifurcation value.
Fold/Saddle-Node Bifurcation
Change in number of equilibrium points into stableand unstable points.
Pitchfork BifurcationChange in number of equilibrium points from one tothree.
Hopf Bifurcation
Periodic orbits arise from an equilibrium point as itchanges stability at bifurcation value.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Types of Bifurcations
Bifurcation Value = Parameter Value at which Bifurcation Occurs(Dilution Factor, D, acted as the variable parameter value)
Transcritical BifurcationNo change in the number of equilibrium points.Switch in stability of equilibria at bifurcation value.
Fold/Saddle-Node Bifurcation
Change in number of equilibrium points into stableand unstable points.
Pitchfork BifurcationChange in number of equilibrium points from one tothree.
Hopf Bifurcation
Periodic orbits arise from an equilibrium point as itchanges stability at bifurcation value.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Types of Bifurcations
Bifurcation Value = Parameter Value at which Bifurcation Occurs(Dilution Factor, D, acted as the variable parameter value)
Transcritical BifurcationNo change in the number of equilibrium points.Switch in stability of equilibria at bifurcation value.
Fold/Saddle-Node Bifurcation
Change in number of equilibrium points into stableand unstable points.
Pitchfork BifurcationChange in number of equilibrium points from one tothree.
Hopf Bifurcation
Periodic orbits arise from an equilibrium point as itchanges stability at bifurcation value.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Types of Bifurcations
Bifurcation Value = Parameter Value at which Bifurcation Occurs(Dilution Factor, D, acted as the variable parameter value)
Transcritical BifurcationNo change in the number of equilibrium points.Switch in stability of equilibria at bifurcation value.
Fold/Saddle-Node Bifurcation
Change in number of equilibrium points into stableand unstable points.
Pitchfork BifurcationChange in number of equilibrium points from one tothree.
Hopf Bifurcation
Periodic orbits arise from an equilibrium point as itchanges stability at bifurcation value.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Solving 5 and 6 Dimensional Systems
Precise solutions for equilibria were not found algebraically.
Investigation carried out by analysis of the systems usingXPPAUT.
Bifurcations identified and verified algebraically usingSotomayor’s Theorem, then further analyzed using MATLABR2012b when necessary.
Wolfram Mathematica 9.0 used to find any equilibria in themodels, behavior determination of equilibria using MATLABR2012b.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Solving 5 and 6 Dimensional Systems
Precise solutions for equilibria were not found algebraically.
Investigation carried out by analysis of the systems usingXPPAUT.
Bifurcations identified and verified algebraically usingSotomayor’s Theorem, then further analyzed using MATLABR2012b when necessary.
Wolfram Mathematica 9.0 used to find any equilibria in themodels, behavior determination of equilibria using MATLABR2012b.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Solving 5 and 6 Dimensional Systems
Precise solutions for equilibria were not found algebraically.
Investigation carried out by analysis of the systems usingXPPAUT.
Bifurcations identified and verified algebraically usingSotomayor’s Theorem, then further analyzed using MATLABR2012b when necessary.
Wolfram Mathematica 9.0 used to find any equilibria in themodels, behavior determination of equilibria using MATLABR2012b.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Solving 5 and 6 Dimensional Systems
Precise solutions for equilibria were not found algebraically.
Investigation carried out by analysis of the systems usingXPPAUT.
Bifurcations identified and verified algebraically usingSotomayor’s Theorem, then further analyzed using MATLABR2012b when necessary.
Wolfram Mathematica 9.0 used to find any equilibria in themodels, behavior determination of equilibria using MATLABR2012b.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Solving the 5 and 6 Dimensional Systems
When linearizing a six-dimensional system around a periodicorbit of period τ , a total of six Floquet multipliers are solvedfor from a 6 x 6 Monodromy matrix:
λi , 1 < i < 6
Using XPPAUT, find the number of stable Floquet multiplierscorresponding to each periodic orbit of interest.
x ′ = f (x , λ) → x ′ = A(t)x M = A(τ)
Solution: x(t) = x(t + τ), for all t ∈ IR.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Solving the 5 and 6 Dimensional Systems
When linearizing a six-dimensional system around a periodicorbit of period τ , a total of six Floquet multipliers are solvedfor from a 6 x 6 Monodromy matrix:
λi , 1 < i < 6
Using XPPAUT, find the number of stable Floquet multiplierscorresponding to each periodic orbit of interest.
x ′ = f (x , λ) → x ′ = A(t)x M = A(τ)
Solution: x(t) = x(t + τ), for all t ∈ IR.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Solving the 5 and 6 Dimensional Systems
When linearizing a six-dimensional system around a periodicorbit of period τ , a total of six Floquet multipliers are solvedfor from a 6 x 6 Monodromy matrix:
λi , 1 < i < 6
Using XPPAUT, find the number of stable Floquet multiplierscorresponding to each periodic orbit of interest.
x ′ = f (x , λ) → x ′ = A(t)x M = A(τ)
Solution: x(t) = x(t + τ), for all t ∈ IR.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Solving the 5 and 6 Dimensional Systems
Hyperbolic periodic orbit:Exactly one Floquet multiplier must be equal to one.
Stable Hyperbolic: Remaining Floquet multipliersare less than one.Unstable Hyperbolic: At least one remaining Floquetmultiplier is greater than one.
Nonhyperbolic periodic orbit:More than one Floquet multiplier is located on the unit circle.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Solving the 5 and 6 Dimensional Systems
Hyperbolic periodic orbit:Exactly one Floquet multiplier must be equal to one.
Stable Hyperbolic: Remaining Floquet multipliersare less than one.Unstable Hyperbolic: At least one remaining Floquetmultiplier is greater than one.
Nonhyperbolic periodic orbit:More than one Floquet multiplier is located on the unit circle.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Results from 4-Dimensional System A
Four equilibria were found:
Equilibrium 1: (S1in, 0, S2in, 0)
Always Exists
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Results from 4-Dimensional System A
Four equilibria were found:
Equilibrium 2: (S1in, 0, S∗2 (D), X ∗2 (D))
S∗2 (D) = DK2αm2−Dα X ∗2 (D) = 1
k3α(S2in − DK2α
m2−Dα)
Conditions that must hold for point to exist:
m2 > Dα
S2in ≥ ( DK2αm2−Dα)
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Results from 4-Dimensional System A
Four equilibria were found:
Equilibrium 2: (S1in, 0, S∗2 (D), X ∗2 (D))
S∗2 (D) = DK2αm2−Dα X ∗2 (D) = 1
k3α(S2in − DK2α
m2−Dα)
Conditions that must hold for point to exist:
m2 > DαS2in ≥ ( DK2α
m2−Dα)
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Results from 4-Dimensional System A
Four equilibria were found:
Equilibrium 3: (S∗1 (D), X ∗1 (D), S∗2in(D), 0)
S∗1 (D) = DK1αm1−Dα X ∗1 (D) = 1
k1α(S1in − DK1α
m1−Dα)
S∗2in(D) = S2in + (k2k1 )(S1in − DK1αm1−Dα)
Conditions that must hold for point to exist:
m1 > Dα
S1in ≥ ( DK1αm1−Dα)
S2in ≥ (k2k1 )(S1in − DK1αm1−Dα)
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Results from 4-Dimensional System A
Four equilibria were found:
Equilibrium 3: (S∗1 (D), X ∗1 (D), S∗2in(D), 0)
S∗1 (D) = DK1αm1−Dα X ∗1 (D) = 1
k1α(S1in − DK1α
m1−Dα)
S∗2in(D) = S2in + (k2k1 )(S1in − DK1αm1−Dα)
Conditions that must hold for point to exist:
m1 > DαS1in ≥ ( DK1α
m1−Dα)
S2in ≥ (k2k1 )(S1in − DK1αm1−Dα)
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Results from 4-Dimensional System A
Four equilibria were found:
Equilibrium 3: (S∗1 (D), X ∗1 (D), S∗2in(D), 0)
S∗1 (D) = DK1αm1−Dα X ∗1 (D) = 1
k1α(S1in − DK1α
m1−Dα)
S∗2in(D) = S2in + (k2k1 )(S1in − DK1αm1−Dα)
Conditions that must hold for point to exist:
m1 > DαS1in ≥ ( DK1α
m1−Dα)
S2in ≥ (k2k1 )(S1in − DK1αm1−Dα)
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Results from 4-Dimensional System A
Four equilibria were found:
Equilibrium 4: (S∗1 (D), X ∗1 (D), S∗2 (D),X ∗2in(D))
S∗1 (D) = DK1αm1−Dα X ∗1 (D) = 1
k1α(S1in− DK1α
m1−Dα) S∗2 (D) = DK2αm2−Dα
X ∗2in(D) = 1k3α
[S2in − DK2αm2−Dα + (k2k1 )(S1in − DK1α
m1−Dα)]
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Results from 4-Dimensional System A
Conditions that must hold for point to exist (Equilibrium Point 4):
m1 > Dα m2 > Dα S1in ≥ ( DK1αm1−Dα)
S2in + (k2k1 )(S1in − DK1αm1−Dα) ≥ ( DK2α
m2−Dα)
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Results from 4-Dimensional System A
Equilibrium Point 1
0 5 106.5
7
7.5
8
8.5
0 5 100.09
0.095
0.1
0.105
0 5 1040
60
80
100
0 5 10−0.14
−0.12
−0.1
−0.08
0 5 10 15 207.9
8
8.1
8.2
0 5 10 15 20−10
−8
−6
−4x 10
−3
0 5 10 15 2035
40
45
50
0 5 10 15 200
0.02
0.04
0.06
0.08
0.1
Figure : Case 8: Saddle (left) and Case 9: Stable Node (right). In Case8, solutions are moving away from (8, 0, 50, 0) as t −→∞. In Case 9,solutions are moving towards (8, 0, 50, 0) as t −→∞.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Results from 4-Dimensional System A
Equilibrium Point 2
0 20 40 600
2
4
6
8
10
0 20 40 600.1
0.2
0.3
0.4
0.5
0 20 40 600
20
40
60
80
0 20 40 600.2
0.4
0.6
0.8
1
0 5 10
0.35
0.4
0.45
0.5
0 5 100
0.02
0.04
0.06
0.08
0.1
0 5 1015.5
16
16.5
17
17.5
0 5 100.26
0.27
0.28
0.29
0.3
Figure : Case 7: Saddle (left) and Case 11: Stable Node (right). In Case7, solutions are moving away from (9.0811, 0, 12.9454, 0.28312) ast −→∞. In Case 11, solutions are moving towards (0.4285, 0, 17.0765,0.2638) as t −→∞.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Results from 4-Dimensional System A
Equilibrium Point 3
0 5 10 150.054
0.056
0.058
0.06
0 5 10 150.96
0.965
0.97
0.975
0.98
0 5 10 150
100
200
300
0 5 10 150
0.5
1
1.5
2
0 5 100.02
0.021
0.022
0.023
0 5 102.5
2.55
2.6
0 5 1066.5
67
67.5
68
0 5 109.6
9.8
10
10.2x 10
−9
Figure : Case 7: Saddle (left) and Case 11: Stable Node (right). In Case7, solutions are moving away from (0.0554, 0.9742, 221.273, 0) ast −→∞. In Case 11, solutions are moving towards 0.02167, 2.577,67.603, 0) as t −→∞.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Results from 4-Dimensional System A
Equilibrium Point 4
0 2000 4000 60007
7.2
7.4
7.6
7.8
8x 10
−3
0 2000 4000 60000.065
0.07
0.075
0.08
0 2000 4000 6000
1.4
1.6
1.8
2
0 2000 4000 60000.006
0.008
0.01
0.012
0.014
0 50 100 1500.46
0.465
0.47
0.475
0.48
0 50 100 1500.49
0.5
0.51
0.52
0 50 100 15010
20
30
40
0 50 100 1500
0.1
0.2
0.3
0.4
Figure : Case 4: Stable Node (left) and Case 5: Stable Node (right). InCase 4, solutions are moving towards (0.0076, 0.0743, 1.9314, 0.00735)as t −→∞. In Case 5, solutions are moving towards (0.4623, 0.5108,37.5477, 0.00667) as t −→∞.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Set of Parameter Values used to Solve 4-DimensionalSystems
m1 m2 k1 k2 k3 α1.2 1.1 25 250 268 0.5
K1 K2 KI S1in S2in D2 10 40 8 50 variable
Table : Parameter values used to solve 4-Dimensional Systems
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Bifurcations found for 4-Dimensional System A
Equilibrium Point 1 (S1in, 0, S2in, 0):
Proved Transcritical bifurcation exists when
D = D∗1 = ( 1α)( m2S2in
K2+S2in) or when
D = D∗2 = ( 1α)( m1S1in
K1+S1in)
When given parameter values are substituted into system, D∗1 = 116
and D∗2 = 1.92.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Bifurcations found for 4-Dimensional System A
Equilibrium Point 2: (S1in, 0, S∗2 (D), X ∗2 (D)):
Proved Transcritical bifurcation exists when
D = D∗ = ( 1α)( m1S1in
K1+S1in)
When the following parameter values are substituted into system,D∗ = 0.1173.
Randomly generated parameter values using MATLAB:
m1 = 1.3038, k2 = 168.9636, K1 = 2.3323, m2 = 0.0253,α = 0.1739, K2 = 19.892, S1in = 9.7551, S2in = 83.0481,k1 = 33.5826
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Bifurcations found for 4-Dimensional System A
Equilibrium Point 3 (S∗1 (D), X ∗1 (D), S∗2in(D), 0):
Proved Transcritical bifurcation exists when
D = D∗ = ( 1α)( m2q1
K2+q1) such that
q1 = S2in + (k2k1 )(S1in − DK1αm1−Dα)
When given parameter values are substituted into system,D∗ = 1.877.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Bifurcations found for 4-Dimensional System A
Equilibrium Point 4 (S∗1 (D), X ∗1 (D), S∗2 (D), X ∗2in(D)):
Proved Transcritical bifurcation exists when
D = D∗ = ( 1K2α
)(S2in + (k2k1 )(S1in − K1Dαm1−Dα))(m2 − Dα)
such that
S2in + (k2k1 )(S1in − K1Dαm1−Dα) = K2Dα
m2−Dα
A Hopf Bifurcation test was performed algebraically and usingMATLAB, but no results were generated.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Bifurcations found for 4-Dimensional System A
Equilibrium Point 4 (S∗1 (D), X ∗1 (D), S∗2 (D), X ∗2in(D)):
Proved Transcritical bifurcation exists when
D = D∗ = ( 1K2α
)(S2in + (k2k1 )(S1in − K1Dαm1−Dα))(m2 − Dα)
such that
S2in + (k2k1 )(S1in − K1Dαm1−Dα) = K2Dα
m2−Dα
A Hopf Bifurcation test was performed algebraically and usingMATLAB, but no results were generated.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Bifurcations found for 4-Dimensional System A
7
8
9
10
11
12
13
S1
1.7 1.8 1.9 2 2.1 2.2D
Figure : Illustration of Transcritical Bifurcations found for Monod Modelusing given parameter values: D∗ = 1.833, D∗ = 1.92, D∗ = 1.877.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Results from 4-Dimensional System B
Up to six equilibria were found:
Equilibrium 1: (S1in, 0, S2in, 0)
Always Exists
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Results from 4-Dimensional System B
Up to six equilibria were found:
Equilibrium 2: (S∗1 (D), X ∗1 (D), S∗2in(D), 0)
S∗1 (D) = DK1αm1−Dα X ∗1 (D) = 1
k1α(S1in − DK1α
m1−Dα)
S∗2in(D) = S2in + X ∗1 (D)k2α
Conditions that must hold for point to exist:
m1 > Dα
S1in ≥ ( DK1αm1−Dα)
S2in + (k2k1 )(S1in − DK1αm1−Dα) ≥ 0
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Results from 4-Dimensional System B
Up to six equilibria were found:
Equilibrium 2: (S∗1 (D), X ∗1 (D), S∗2in(D), 0)
S∗1 (D) = DK1αm1−Dα X ∗1 (D) = 1
k1α(S1in − DK1α
m1−Dα)
S∗2in(D) = S2in + X ∗1 (D)k2α
Conditions that must hold for point to exist:
m1 > DαS1in ≥ ( DK1α
m1−Dα)
S2in + (k2k1 )(S1in − DK1αm1−Dα) ≥ 0
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Results from 4-Dimensional System B
Up to six equilibria were found:
Equilibrium 2: (S∗1 (D), X ∗1 (D), S∗2in(D), 0)
S∗1 (D) = DK1αm1−Dα X ∗1 (D) = 1
k1α(S1in − DK1α
m1−Dα)
S∗2in(D) = S2in + X ∗1 (D)k2α
Conditions that must hold for point to exist:
m1 > DαS1in ≥ ( DK1α
m1−Dα)
S2in + (k2k1 )(S1in − DK1αm1−Dα) ≥ 0
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Results from 4-Dimensional System B
Up to six equilibria were found:
Equilibrium 3: (S1in, 0, S1∗2 (D), X 1
2 (D))
S1∗2 (D) = (KI
2y )[(1− y) + ((1− y)2 − (4K2KI
)(y2))1/2]
X 12 (D) = 1
k3α(S2in − S1∗
2 (D))
y = Dαm2
Conditions that must hold for point to exist:Amputate my foot...
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Results from 4-Dimensional System B
Up to six equilibria were found:
Equilibrium 4: (S1in, 0, S2∗2 (D), X 2
2 (D))
S2∗2 (D) = (KI
2y )[(1− y)− ((1− y)2 − (4K2KI
)(y2))1/2]
X 22 (D) = 1
k3α(S2in − S2∗
2 (D))
y = Dαm2
Conditions that must hold for point to exist:End world hunger...
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Results from 4-Dimensional System B
Up to six equilibria were found:
Equilibrium 5: (S∗1 (D), X ∗1 (D), S1∗2 (D), X 1∗
2 (D))
S∗1 (D) = DK1αm1−Dα X ∗1 (D) = 1
k1α(S1in − DK1α
m1−Dα)
S1∗2 (D) = (KI
2y )[(1− y) + ((1− y)2 − (4K2KI
)(y2))1/2]
X 1∗2 (D) = ( 1
k3α)(S∗2in(D)− S1∗
2 (D))
y = Dαm2
Conditions that must hold for point to exist:Give up first born son...
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Results from 4-Dimensional System B
Up to six equilibria were found:
Equilibrium 6: (S∗1 (D), X ∗1 (D), S2∗2 (D), X 2∗
2 (D))
S∗1 (D) = DK1αm1−Dα X ∗1 (D) = 1
k1α(S1in − DK1α
m1−Dα)
S2∗2 (D) = (KI
2y )[(1− y)− ((1− y)2 − (4K2KI
)(y2))1/2]
X 2∗2 (D) = ( 1
k3α)(S∗2in(D)− S2∗
2 (D))
y = Dαm2
Conditions that must hold for point to exist:Amputate my other foot...
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Results from 4-Dimensional System B
Equilibrium Point 1
0 5 102
4
6
8
0 5 100.1
0.2
0.3
0.4
0.5
0 5 1040
60
80
100
120
0 5 100
0.02
0.04
0.06
0.08
0.1
0 10 20 30 406.5
7
7.5
8
0 10 20 30 400
0.02
0.04
0.06
0.08
0.1
0 10 20 30 4045
50
55
60
0 10 20 30 400
0.02
0.04
0.06
0.08
0.1
Figure : Case 5: Saddle (left) and Case 8: Stable Node (right). In Case5, solutions are moving away from (8, 0, 50, 0) as t −→∞. In Case 8,solutions are moving towards (8, 0, 50, 0) as t −→∞.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Results from 4-Dimensional System B
Equilibrium Point 2
0 50 100 150 2000.16
0.165
0.17
0.175
0.18
0 50 100 150 2000.95
1
1.05
1.1
0 50 100 150 200102
104
106
108
110
0 50 100 150 2000
0.02
0.04
0.06
0.08
0.1
0 5 10 15 200.02
0.022
0.024
0.026
0.028
0.03
0 5 10 15 200.069
0.07
0.071
0.072
0.073
0 5 10 15 200
20
40
60
0 5 10 15 200.1
0.2
0.3
0.4
0.5
Figure : Case 2: Stable Node (left) and Case 8: Saddle (right). In Case2, solutions are approaching (0.1672, 1.059, 110.474, 0) as t −→∞. InCase 8, solutions are moving away from (0.0272, 0.07557, 42.014, 0) ast −→∞.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Results from 4-Dimensional System B
Equilibrium Points 3 and 4
0 5 10 15 200
2
4
6
8
10
0 5 10 15 200
0.5
1
1.5
0 5 10 15 200
20
40
60
0 5 10 15 200
0.01
0.02
0.03
0.04
0 100 200 300 4002.2
2.4
2.6
2.8
3
0 100 200 300 4000
0.02
0.04
0.06
0.08
0.1
0 100 200 300 4000.4
0.5
0.6
0.7
0 100 200 300 4000.18
0.2
0.22
0.24
Figure : Equilibrium Point 3 Case A6: Saddle (left) and Equilibrium Point4 Case C4: Stable Node (right). In EqPt 3 Case A6, solutions are movingaway from (8.6266, 0, 7.08424, 0.03633) as t −→∞. In EqPt 4 Case C4,solutions are moving towards (3.0224, 0, 0.4495, 0.1948) as t −→∞.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Results from 4-Dimensional System B
Equilibrium Point 6
0 50 100 150 2000.4
0.41
0.42
0.43
0 50 100 150 2000.0125
0.013
0.0135
0.014
0 50 100 150 2000.3
0.305
0.31
0.315
0.32
0.325
0 50 100 150 2000.42
0.43
0.44
0.45
Figure : Equilibrium Point 6 Case B5: Stable Node. In EqPt 6 Case B5,solutions are moving towards (0.4116, 0.014, 0.3016, 0.4401) ast −→∞. No random parameters were generated that agreed with thepredicted results from any cases of Equilibrium Point 5.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Bifurcations found from 4-Dimensional System B
Equilibrium Point 1 (S1in, 0, S2in, 0):
Proved Transcritical bifurcation exists when
D = D∗1 = ( 1α)( m1S1in
K1+S1in) or when
D = D∗2 = ( 1α)( m2S2in
K2+S2in+S22inKI
)
When given parameter values are substituted into system,D∗1 = 1.92 and D∗2 = 0.898.
A Pitchfork Bifurcation test was performed algebraically and
using MATLAB in the case where K2 =S22inKI
, but no resultswere generated.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Bifurcations found from 4-Dimensional System B
Equilibrium Point 1 (S1in, 0, S2in, 0):
Proved Transcritical bifurcation exists when
D = D∗1 = ( 1α)( m1S1in
K1+S1in) or when
D = D∗2 = ( 1α)( m2S2in
K2+S2in+S22inKI
)
When given parameter values are substituted into system,D∗1 = 1.92 and D∗2 = 0.898.
A Pitchfork Bifurcation test was performed algebraically and
using MATLAB in the case where K2 =S22inKI
, but no resultswere generated.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Bifurcations found from 4-Dimensional System B
Equilibrium Point 2: (S∗1 (D), X ∗1 (D), S∗2in(D), 0):
Proved Transcritical bifurcation exists when
D = D∗ = ( 1α)( m2x
K2+x+ x2
KI
) such that
x = S2in + (k2k1 )(S1in − K1Dαm1−Dα)
When the following parameter values are substituted intosystem, D∗ = 0.4305.Randomly generated parameter values using MATLAB:
m1 = 1.6362, k2 = 250.9017, K1 = 1.419,m2 = 1.109, α = 0.2349, K2 = 3.7185,S1in = 10.7751, S2in = 66.2991, k1 = 15.396,KI = 24.1864, k3 = 268.
A Pitchfork Bifurcation test was performed algebraically and usingMATLAB in the case where K2 = x2
KI, but no results were
generated.Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Bifurcations found from 4-Dimensional System B
Equilibrium Point 3: (S1in, 0, S1∗2 (D), X 1
2 (D)):
Proved Transcritical bifurcation exists when
D = D∗ = ( 1α)( m1S1in
K1+S1in)
When the following parameter values are substituted into system,D∗ = 0.4993.Randomly generated parameter values using MATLAB:
m1 = 0.6323, k2 = 101.7029, K1 = 1.6611, m2 = 1.824,α = 0.9722, K2 = 8.0747, S1in = 5.4899, S2in = 77.3912,k1 = 5.0144, k3 = 268, KI = 25.164.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Bifurcations found from 4-Dimensional System B
Equilibrium Point 4: (S1in, 0, S2∗2 (D), X 2
2 (D)):
Proved Transcritical bifurcation exists when
D = D∗ = ( 1α)( m1S1in
K1+S1in)
When the following parameter values are substituted into system,D∗ = 0.2567.Randomly generated parameter values using MATLAB:
m1 = 0.2811, k2 = 51.6183, K1 = 1.0457, m2 = 1.3676,α = 0.9074, K2 = 13.2164, S1in = 5.0548, S2in = 6.2729,k1 = 8.4958, k3 = 268, KI = 49.88.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Bifurcations found from 4-Dimensional System B
Equilibrium Point 5: (S∗1 (D), X ∗1 (D), S1∗2 (D), X 1∗
2 (D))
Equilibrium Point 6: (S∗1 (D), X ∗1 (D), S2∗2 (D), X 2∗
2 (D))
Hopf Bifurcation tests were performed for both equilibria, but nodata was generated.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Results from 5-Dimensional System A
m1 m2 k1 k2 k3 α1 3.2 30 215 100 0.3
K1 K2 KI1 KI2 S1in S2in D7 200 500 400 40 5 variable
m4 k4 K4 yin µ1 5 1 5 0.06
Table : Parameter values used for solving 5-Dimensional Systems
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
5-Dimensional System A
Combination of functions applied:
Monod model for the growth of Bacteria 1
µ(S1) = m1S1K1+S1
Haldane model for the growth of Bacteria 2
µ(S2) = m2S2
K2+S2+S22
KI1
Monod model for the consumptions of Toxin
µ(y) = m4yK4+y
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
5-Dimensional System A
Combination of functions applied:
Monod model for the growth of Bacteria 1
µ(S1) = m1S1K1+S1
Haldane model for the growth of Bacteria 2
µ(S2) = m2S2
K2+S2+S22
KI1
Monod model for the consumptions of Toxin
µ(y) = m4yK4+y
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
5-Dimensional System A
Combination of functions applied:
Monod model for the growth of Bacteria 1
µ(S1) = m1S1K1+S1
Haldane model for the growth of Bacteria 2
µ(S2) = m2S2
K2+S2+S22
KI1
Monod model for the consumptions of Toxin
µ(y) = m4yK4+y
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Bifurcations found when Solving 5-Dimensional System A
30
32
34
36
38
40
42
S1
1.7 1.8 1.9 2 2.1 2.2 2.3 2.4D
Figure : Illustration of Bifurcations found for 5-Dimensional System A,Saddle-Node Bifurcation point: D∗ = 2.30067.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Stable Periodic Orbit of 5-Dimensional System A
33
33.5
34
34.5
35
35.5
0.5
0.6
0.7
0.8
0.930
40
50
60
Figure : Presence of Stable Periodic Orbit in 5D System A. Though aHopf bifurcation exists in this system from which stable periodic orbitsare generated, the nonhyperbolic equilibrium point corresponding to thedetected Hopf bifurcation displayed a negative solution for X2. Unstableequilibria found: (40, 0, 5, 0, 5), (40, 0, 48.24, -1.44, -0.61). Wegraphed only 3-D projections of the solutions: S1, X1, and S2.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Results from 5-Dimensional System B
Combination of functions applied:
Monod model for the growth of Bacteria 1
µ(S1) = m1S1K1+S1
Haldane model for the growth of Bacteria 2
µ(S2) = m2S2
K2+S2+S22
KI1
Haldane model for the consumptions of Toxin
µ(y) = m4y
K4+y+ y2
KI2
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Results from 5-Dimensional System B
Combination of functions applied:
Monod model for the growth of Bacteria 1
µ(S1) = m1S1K1+S1
Haldane model for the growth of Bacteria 2
µ(S2) = m2S2
K2+S2+S22
KI1
Haldane model for the consumptions of Toxin
µ(y) = m4y
K4+y+ y2
KI2
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Results from 5-Dimensional System B
Combination of functions applied:
Monod model for the growth of Bacteria 1
µ(S1) = m1S1K1+S1
Haldane model for the growth of Bacteria 2
µ(S2) = m2S2
K2+S2+S22
KI1
Haldane model for the consumptions of Toxin
µ(y) = m4y
K4+y+ y2
KI2
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Bifurcations found when Solving 5-Dimensional System B
0
10
20
30
40
50
60
S1
-0.5 0 0.5 1 1.5 2 2.5D1
Figure : Illustration of Bifurcations found for 5-Dimensional System B,Saddle-Node Bifurcation point: D∗ = 2.03477.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Stable Periodic Orbit of 5-Dimensional System B
3333.5
3434.5
3535.5
0.5
0.6
0.7
0.8
0.935
40
45
50
55
3234
3638
4042
0.5
0.6
0.7
0.8
0.90
10
20
30
40
50
60
Figure : Proof of Stable Periodic Orbit in 5D System B, D∗ = 2.035.Though a Hopf bifurcation exists in this system from which stableperiodic orbits are generated, the nonhyperbolic equilibrium pointcorresponding to the detected Hopf bifurcation displayed a negativesolution for X2. Unstable equilibria found using Wolfram Mathematica9.0: (40, 0, 5, 0, 5) and (34.22, 0.64, 48.24, -0.06, 5.12) whenD∗ = 2.03477.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Results from 5-Dimensional System C
Combination of functions applied:
Monod model for the growth of Bacteria 1
µ(S1) = m1S1K1+S1
Monod model for the growth of Bacteria 2
µ(S2) = m2S2K2+S2
Monod model for the consumptions of Toxin
µ(y) = m4yK4+y
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Results from 5-Dimensional System C
Combination of functions applied:
Monod model for the growth of Bacteria 1
µ(S1) = m1S1K1+S1
Monod model for the growth of Bacteria 2
µ(S2) = m2S2K2+S2
Monod model for the consumptions of Toxin
µ(y) = m4yK4+y
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Results from 5-Dimensional System C
Combination of functions applied:
Monod model for the growth of Bacteria 1
µ(S1) = m1S1K1+S1
Monod model for the growth of Bacteria 2
µ(S2) = m2S2K2+S2
Monod model for the consumptions of Toxin
µ(y) = m4yK4+y
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Bifurcations found when Solving 5-Dimensional System C
0
10
20
30
40
50
60
S1
-0.5 0 0.5 1 1.5 2 2.5D1
Figure : Illustration of Bifurcations found for 5-Dimensional System C,D∗ = 2.30567 at saddle-node bifurcation point.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Results from 5-Dimensional System D
Combination of functions applied:
Monod model for the growth of Bacteria 1
µ(S1) = m1S1K1+S1
Monod model for the growth of Bacteria 2
µ(S2) = m2S2K2+S2
Haldane model for the consumptions of Toxin
µ(y) = m4y
K4+y+ y2
KI2
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Results from 5-Dimensional System D
Combination of functions applied:
Monod model for the growth of Bacteria 1
µ(S1) = m1S1K1+S1
Monod model for the growth of Bacteria 2
µ(S2) = m2S2K2+S2
Haldane model for the consumptions of Toxin
µ(y) = m4y
K4+y+ y2
KI2
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Results from 5-Dimensional System D
Combination of functions applied:
Monod model for the growth of Bacteria 1
µ(S1) = m1S1K1+S1
Monod model for the growth of Bacteria 2
µ(S2) = m2S2K2+S2
Haldane model for the consumptions of Toxin
µ(y) = m4y
K4+y+ y2
KI2
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Bifurcations found when Solving 5-Dimensional System D
0
10
20
30
40
50
60
S1
-0.5 0 0.5 1 1.5 2 2.5D1
Figure : Illustration of Bifurcations found for 5-Dimensional System D,D∗ = 2.305139 at saddle-node bifurcation point.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Parameter values used when solving 6-Dimensional Systems
m1 = 3, m2 = 0.75
k1 = 10, k2 = 5.2254, k3 = 40
K1 = 0.5, K2 = 0.15, KI = 1
S1 = 6, S2 = 0, α = 1, p = 1, r = 0.5.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Parameter values used when solving 6-Dimensional Systems
m1 = 3, m2 = 0.75
k1 = 10, k2 = 5.2254, k3 = 40
K1 = 0.5, K2 = 0.15, KI = 1
S1 = 6, S2 = 0, α = 1, p = 1, r = 0.5.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Parameter values used when solving 6-Dimensional Systems
m1 = 3, m2 = 0.75
k1 = 10, k2 = 5.2254, k3 = 40
K1 = 0.5, K2 = 0.15, KI = 1
S1 = 6, S2 = 0, α = 1, p = 1, r = 0.5.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Parameter values used when solving 6-Dimensional Systems
m1 = 3, m2 = 0.75
k1 = 10, k2 = 5.2254, k3 = 40
K1 = 0.5, K2 = 0.15, KI = 1
S1 = 6, S2 = 0, α = 1, p = 1, r = 0.5.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
6-Dimensional System
Functions applied:
Haldane model for the growth of Bacteria 2
µ(S2) = m2S2
K2+S2+S22
KI
Periodic inflow of S1in of amplitude ”r”, in the hopes ofgenerating oscillating solutions.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
6-Dimensional System
Functions applied:
Haldane model for the growth of Bacteria 2
µ(S2) = m2S2
K2+S2+S22
KI
Periodic inflow of S1in of amplitude ”r”, in the hopes ofgenerating oscillating solutions.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
6-Dimensional System
Bifurcation Results of 6-Dimensional System
0
1
2
3
4
5
6
7
S2
0 0.05 0.1 0.15 0.2 0.25 0.3 0.35 0.4 0.45 0.5D
0.064
0.065
0.066
0.067
0.068
0.069
0.07
X2
0 0.2 0.4 0.6 0.8r
Figure : Saddle-Node Bifurcation of Periodic Orbits, D∗ = 0.4196 atsaddle-node bifurcation point.
Surprising Results: Saddle-Node Bifurcation of Periodic Orbits
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
6-Dimensional System
Bifurcation Results of 6-Dimensional System
00.05
0.10.15
0.2
0.570.580.590.60.610.620
0.2
0.4
0.6
0.8
1
1.2
1.4
1.6
1.8
0
0.1
0.2 0.580.590.60.610.620.63
0
0.1
0.2
0.3
0.4
0.5
0.6
0.7
0.8
Figure : Periodic Orbits of Opposite Stability converging at Saddle-NodeBifurcation Point. Green: stable, Blue: unstable.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
6-Dimensional System
Bifurcation Results of 6-Dimensional System
0.02
0.025
0.03
0.035
0.04
0.045
0.05
0.055
0.06
0.065
0.07
0.580.585
0.590.595
0.60.605
0.610.615
0
0.05
0.1
0.15
0.2
Figure : Stability statuses of Periodic Orbits 6 and 14. Left: Orbit 6,D∗ = 0.2313 (stable), Right: Orbit 14, D∗ = 0.3937 (unstable).
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Equilibria Results of 6-Dimensional System
0.0417
0.0417
0.0418
0.0418
0.59580.5958
0.59580.5958
0
0.5
1
1.5
2
2.5
Figure : Unstable Equilibria found for system using specific set ofparameter values. (0.0417725, 0.595823, 0.0690168, 0.0761099, 0, 0)and (0.0417725, 0.595823, 2.17338, 0.0235007, 0, 0) when D∗ = 0.2313.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Further Research to be Done
6-Dimensional System: Find heteroclinic orbits connectingtwo unstable periodic orbits rather than solely orbits ofopposite stability.
5-Dimensional Systems:
Toxin has a profound influence on the growth of X2.Toxin acts immediately on S2 accumulation ratherthan indirectly through S1 reaction by X1.
Analysis of environmental conditions to find the most idealsetting for digestion. Provide flexibility for maximum bacteriagrowth velocity parameters: m1 , m2, and m4.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Further Research to be Done
6-Dimensional System: Find heteroclinic orbits connectingtwo unstable periodic orbits rather than solely orbits ofopposite stability.
5-Dimensional Systems:
Toxin has a profound influence on the growth of X2.Toxin acts immediately on S2 accumulation ratherthan indirectly through S1 reaction by X1.
Analysis of environmental conditions to find the most idealsetting for digestion. Provide flexibility for maximum bacteriagrowth velocity parameters: m1 , m2, and m4.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
Further Research to be Done
6-Dimensional System: Find heteroclinic orbits connectingtwo unstable periodic orbits rather than solely orbits ofopposite stability.
5-Dimensional Systems:
Toxin has a profound influence on the growth of X2.Toxin acts immediately on S2 accumulation ratherthan indirectly through S1 reaction by X1.
Analysis of environmental conditions to find the most idealsetting for digestion. Provide flexibility for maximum bacteriagrowth velocity parameters: m1 , m2, and m4.
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
References
[1] B. Benyahia, T. Sari, B. Cherki, J. Harmand, “Bifurcation andStability Analysis of a Two Step Model for Monitoring AnaerobicDigestion Process”. Journal of Process Control 22 (2012).
[2] O. Bernard and J. Hess, “Design and Study of a RiskManagement Criterion for an Unstable Anaerobic WastewaterTreatment Process”. French Research Institute of ComputerScience and Automatic Control. (2007).
[3] R. Cooke, “Wastewater Treatment Methods and Disposal”@ONLINE. July 2013. URL =http://water.me.vccs.edu/courses/ENV149/methods.htm.
[4] K. Cornely and C. Pratt, “Essential Biochemistry”. 2ndedition New York: Wiley. (2011).
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
References
[5] B. Ermentrout, “Simulating, Analyzing, and AnimatingDynamical Systems: A Guide to XPPAUT for Researchers andStudents”. Philadelphia: Society for Industrial and AppliedMathematics. (2002).
[6] M. Gerber, R. Span, “An Analysis of Available MathematicalModels for Anaerobic Digestion of Organic Substances forProduction of Biogas”. International Gas Union ResearchConference. (2008).
[7] Y. Li and J.S. Muldowney, “On Bendixson’s Criterion*”.Journal of Differential Equations 106, 27-39 (1993).
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor
Introduction Systems to Study Mathematical Approach to Solving Systems Results Concluding Thoughts
References
[8] J. Rebaza, “A First Course in Applied Mathematics”. NewJersey: Wiley. (2012).
[9] J. Senisterra, “Dynamical Analysis of the Anaerobic DigestionModel as Proposed by Hess and Bernard”. Print.
[10] M. Weederman, “Analysis of a Model for the Effects of anExternal Toxin on Anaerobic Digestion”. Mathematical Biosciencesand Engineering 9 (2012).
Christina Berti Modeling and Analysis of Anaerobic Digestion in a Bioreactor