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Optimal Control Theory
Batch Beer Fermentation
General Case
• Min/max
General Case
• Min
• Φ = Endpoint cost
• L =Lagrangian
• u = Control
• X= State
General Case
• Min
• Φ = Endpoint cost- final product
• L =Lagrangian
• u = Control
• X= State
General Case
• Min
• Φ = Endpoint cost- final product
• L = Lagrangian – describes dynamics of system
• u = Control
• X= State
General Case
• Min
• Φ = Endpoint cost- final product
• L = Lagrangian – describes dynamics of system
• u = Control – what we can do to the system
• X= State
General Case
• Min
• Φ = Endpoint cost- final product
• L = Lagrangian – describes dynamics of system
• u = Control – what we can do to the system
• X= State – properties of the system
Case of Beer
• Min
• Φ = Endpoint cost- profit, quality
• X= State – properties of the system
• u = Control – what we can do to the system
• L = Lagrangian – describes dynamics of system
Case of Beer
• Min
• Φ = Endpoint cost- profit, quality
• X= State – concentrations of yeast and organic
and inorganic chemical species.
• u = Control – what we can do to the system
• L = Lagrangian – describes dynamics of system
Case of Beer
• Min
• Φ = Endpoint cost- profit, quality
• X= State – concentrations of yeast and organic
and inorganic chemical species.
• u = Control – temperature
• L = Lagrangian – describes dynamics of system
Case of Beer
• Min
• Φ = Endpoint cost- profit, quality
• X= State – concentrations of yeast and organic
and inorganic chemical species.
• u = Control – temperature
• L = Lagrangian – equations relating state
variables and controls.
Quadratic Case
• Chemical Reactions
• A+BC
• Rate = k[A]^a[B]^b
• a and b are determined experimentally
• Used to determine mechanisms
• [] = concentration
Beer Basics
Fermentation
• Yeast consume sugars and produce CO2 and
ethanol.
• The yeast also produce other chemicals.
• Most side products are bad: ketones, aldehydes,
sulfur compounds, other alcohols; however, esters
are good.
• Main factors influencing side products are
temperature, amino acids, and pH levels.
Controls
• Commercial breweries can control
• Temperature – refrigeration (most important)
• Can be expensive
• pH, amino acids, sugar, yeast– initial conditions
Optimization
• Different methods have been used
• Sequential quadratic programming (SQP)
• Gradient method
• Dynamic programming
• Calculus of variations
• Neural Networks
• Multiple objectives to consider
• Professional results:
• Most conclusions end up at a very narrow region between 10-15*C
• SQP method found a rapid rise to 13*C then slow accent to 13.5*C
• Difference is 6.7% increase in ethanol production
Simple Model
• Assumptions
• Yeast is the only consumer of resources
• Sugar is the only growth limiting resource
• Wort is deoxygenated at t=0
• Temperature and pressure are constant
• Production of side products are minimal/ignored
Simple model
• Relates yeast, alcohol and sugar levels.
• System of nonlinear ODEs
dS=-m*Y*S
dY=k*S*Y - d*Y^2 - p*A*Y
dA=b*Y*S
k, d, p, m, b = constants @ temp=T
Results
Constants chosen for visible
details not accuracy.
Units on vertical axis are
arbitrary and different for each
plot.
Sources
• G.E. Carrillo-Ureta, P.D. Roberts, V.M. Becerra, Optimal
Control of a Fermentation Process
• W. Fred Rameriz, Jan Maciejowski, Optimal Beer
Fermentation
• Pascale B. Dengis, L.R. Ne´Lissen, Paul G. Rouxhet,
mechanisms of yeast flocculation: comparison of top and
bottom-fermenting strains, applied and environmental
microbiology, Feb. 1995, p. 718-728, Vol. 61,No. 2
• http://en.wikipedia.org/wiki/Optimal_control
• Anatoly Zlotnik

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(GWG_2)OptimalControlTheory.pptx

  • 1. Optimal Control Theory Batch Beer Fermentation
  • 3. General Case • Min • Φ = Endpoint cost • L =Lagrangian • u = Control • X= State
  • 4. General Case • Min • Φ = Endpoint cost- final product • L =Lagrangian • u = Control • X= State
  • 5. General Case • Min • Φ = Endpoint cost- final product • L = Lagrangian – describes dynamics of system • u = Control • X= State
  • 6. General Case • Min • Φ = Endpoint cost- final product • L = Lagrangian – describes dynamics of system • u = Control – what we can do to the system • X= State
  • 7. General Case • Min • Φ = Endpoint cost- final product • L = Lagrangian – describes dynamics of system • u = Control – what we can do to the system • X= State – properties of the system
  • 8. Case of Beer • Min • Φ = Endpoint cost- profit, quality • X= State – properties of the system • u = Control – what we can do to the system • L = Lagrangian – describes dynamics of system
  • 9. Case of Beer • Min • Φ = Endpoint cost- profit, quality • X= State – concentrations of yeast and organic and inorganic chemical species. • u = Control – what we can do to the system • L = Lagrangian – describes dynamics of system
  • 10. Case of Beer • Min • Φ = Endpoint cost- profit, quality • X= State – concentrations of yeast and organic and inorganic chemical species. • u = Control – temperature • L = Lagrangian – describes dynamics of system
  • 11. Case of Beer • Min • Φ = Endpoint cost- profit, quality • X= State – concentrations of yeast and organic and inorganic chemical species. • u = Control – temperature • L = Lagrangian – equations relating state variables and controls.
  • 12. Quadratic Case • Chemical Reactions • A+BC • Rate = k[A]^a[B]^b • a and b are determined experimentally • Used to determine mechanisms • [] = concentration
  • 14. Fermentation • Yeast consume sugars and produce CO2 and ethanol. • The yeast also produce other chemicals. • Most side products are bad: ketones, aldehydes, sulfur compounds, other alcohols; however, esters are good. • Main factors influencing side products are temperature, amino acids, and pH levels.
  • 15. Controls • Commercial breweries can control • Temperature – refrigeration (most important) • Can be expensive • pH, amino acids, sugar, yeast– initial conditions
  • 16. Optimization • Different methods have been used • Sequential quadratic programming (SQP) • Gradient method • Dynamic programming • Calculus of variations • Neural Networks • Multiple objectives to consider • Professional results: • Most conclusions end up at a very narrow region between 10-15*C • SQP method found a rapid rise to 13*C then slow accent to 13.5*C • Difference is 6.7% increase in ethanol production
  • 17. Simple Model • Assumptions • Yeast is the only consumer of resources • Sugar is the only growth limiting resource • Wort is deoxygenated at t=0 • Temperature and pressure are constant • Production of side products are minimal/ignored
  • 18. Simple model • Relates yeast, alcohol and sugar levels. • System of nonlinear ODEs dS=-m*Y*S dY=k*S*Y - d*Y^2 - p*A*Y dA=b*Y*S k, d, p, m, b = constants @ temp=T
  • 19. Results Constants chosen for visible details not accuracy. Units on vertical axis are arbitrary and different for each plot.
  • 20. Sources • G.E. Carrillo-Ureta, P.D. Roberts, V.M. Becerra, Optimal Control of a Fermentation Process • W. Fred Rameriz, Jan Maciejowski, Optimal Beer Fermentation • Pascale B. Dengis, L.R. Ne´Lissen, Paul G. Rouxhet, mechanisms of yeast flocculation: comparison of top and bottom-fermenting strains, applied and environmental microbiology, Feb. 1995, p. 718-728, Vol. 61,No. 2 • http://en.wikipedia.org/wiki/Optimal_control • Anatoly Zlotnik