Model predictive control of fermentation in biofuel production
View Patent ↗System and method for managing batch fermentation in biofuel production. An optimizer executes a nonlinear multivariate predictive model of a batch fermentation process in accordance with an end of batch objective specifying a target end of batch biofuel concentration to determine an optimal batch trajectory over a temporal control horizon specifying a biofuel and/or sugar concentration trajectory over the batch fermentation process. A nonlinear control model for the batch fermentation process that includes the temporal control horizon driven by biofuel concentration during the batch fermentation process is executed per the determined optimal batch trajectory using received process information as input, thereby generating model output including target values for manipulated variables for the batch fermentation process, including batch fermentation temperature. The batch fermentation process is controlled per the target values to produce biofuel in accordance with the determined optimal batch trajectory, to substantially optimize the end of batch biofuel yield.
1. A method for managing a batch fermentation process in a biofuel production process, comprising:
providing a nonlinear control model, comprising a nonlinear predictive model of a batch fermentation process of a biofuel production process, wherein the nonlinear predictive model is a function of a volumetric change in a fermentation tank, temperature, and enzyme concentration;
providing an optimal batch temperature trajectory;
executing the nonlinear control model in accordance with the optimal batch temperature trajectory, thereby generating model output comprising target values for a plurality of manipulated variables for the batch fermentation process, wherein the target values comprise a target enzyme addition staging profile during filling of the fermentation tank; and
controlling an enzyme addition rate during filling of the fermentation tank in accordance with the target enzyme addition staging profile.
2. The method of claim 1 , wherein the nonlinear control model further comprises a shrinking temporal control horizon during the batch fermentation process;
wherein the method further comprises providing an end-of batch biofuel concentration objective to the nonlinear predictive model; and
wherein providing the optimal batch temperature trajectory comprises causing an optimizer to execute the nonlinear predictive model, thereby determining the optimal batch temperature trajectory over the shrinking temporal control horizon in accordance with the end-of-batch biofuel concentration objective.
3. The method of claim 2 , further comprising:
receiving a constraint on sugar concentration over the batch fermentation process, or a constraint on end-of-batch sugar concentration.
4. The method of claim 3 , wherein the optimal batch temperature trajectory over the shrinking temporal control horizon is determined subject to the constraint.
5. The method of claim 3 , wherein the target values for the plurality of manipulated variables are determined subject to the constraint.
6. The method of claim 1 , further comprising:
repeating said executing the nonlinear control model, and said controlling, in an iterative manner.
7. The method of claim 6 , wherein said repeating said executing the nonlinear control model further comprises generating target values comprising a fermentation temperature staging profile for the fermentation batch.
8. The method of claim 1 , wherein the nonlinear predictive model is further a function of yeast concentration, yeast addition, yeast activity, biomass concentration, batch progress, or pH.
9. A computer-accessible memory medium that stores program instructions for managing a batch fermentation process in a biofuel production process, wherein the memory medium stores:
a nonlinear control model, comprising a nonlinear predictive model of a batch fermentation process of a biofuel production process, wherein the nonlinear predictive model is a function of a volumetric change in a fermentation tank temperature, and enzyme concentration;
program instructions executable to:
provide an optimal batch temperature trajectory;
execute the nonlinear control model in accordance with the optimal batch temperature trajectory, thereby generating model output comprising target values for a plurality of manipulated variables for the batch fermentation process, wherein the target values comprise a target enzyme addition staging profile during filling of the fermentation tank; and
control an enzyme addition rate during filling of the fermentation tank in accordance with the target enzyme addition staging profile.
10. The memory medium of claim 9 , wherein the nonlinear control model further comprises a shrinking temporal control horizon during the batch fermentation process;
wherein the program instructions are further executable to provide an end-of batch biofuel concentration objective to the nonlinear predictive model; and
wherein the program instructions that are executable to provide the optimal batch temperature trajectory comprise program instructions that cause an optimizer to execute the nonlinear predictive model, thereby determining the optimal batch temperature trajectory over the shrinking temporal control horizon in accordance with the end-of-batch biofuel concentration objective.
11. The memory medium of claim 10 , wherein the program instructions are further executable to receive a constraint on sugar concentration over the batch fermentation process, or a constraint on end-of-batch sugar concentration.
12. The memory medium of claim 11 , wherein the optimal batch temperature trajectory over the shrinking temporal control horizon is determined subject to the constraint.
13. The memory medium of claim 11 , wherein the target values for the plurality of manipulated variables are determined subject to the constraint.
14. The memory medium of claim 9 , wherein the program instructions are further executable to repeat said executing the nonlinear control model, and said controlling, in an iterative manner.
15. The memory medium of claim 14 , wherein said repeating said executing the nonlinear control model further comprises generating target values comprising a fermentation temperature staging profile for the fermentation batch.
16. The memory medium of claim 9 , wherein the nonlinear predictive model is further a function of yeast concentration, yeast addition, yeast activity, biomass concentration, batch progress, or pH.
17. A system for managing a batch fermentation process in a biofuel production process, comprising:
a fermenter;
a nonlinear control model, comprising a nonlinear predictive model of a batch fermentation process of a biofuel production process, wherein the nonlinear predictive model is a function of a volumetric change in a fermentation tank temperature, and enzyme concentration; and
a control system operatively coupled to the nonlinear control model and the fermenter, wherein the control system is operable to:
provide an optimal batch temperature trajectory;
execute the nonlinear control model in accordance with the optimal batch temperature trajectory, thereby generating model output comprising target values for a plurality of manipulated variables for the batch fermentation process, wherein the target values comprise a target enzyme addition staging profile during filling of the fermentation tank; and
control an enzyme addition rate during filling of the fermentation tank in accordance with the target enzyme addition staging profile.
18. The system of claim 17 , wherein the nonlinear control model further comprises a shrinking temporal control horizon during the batch fermentation process;
wherein the control system is further operable to provide an end-of batch biofuel concentration objective to the nonlinear predictive model; and
wherein providing the optimal batch temperature trajectory comprises causing an optimizer to execute the nonlinear predictive model, thereby determining the optimal batch temperature trajectory over the shrinking temporal control horizon in accordance with the end-of-batch biofuel concentration objective.
19. The system of claim 18 , wherein the control system is further operable to receive a constraint on sugar concentration over the batch fermentation process, or a constraint on end-of-batch sugar concentration.
20. The system of claim 19 , wherein the optimal batch temperature trajectory over the shrinking temporal control horizon is determined subject to the constraint.
21. The method of claim 19 , wherein the target values for the plurality of manipulated variables are determined subject to the constraint.
22. The system of claim 17 , wherein the control system is further operable to repeat said executing the nonlinear control model, and said controlling, in an iterative manner.
23. The system of claim 22 , wherein said repeating said executing the nonlinear control model further comprises generating target values comprising a fermentation temperature staging profile for the fermentation batch.
24. The system of claim 17 , wherein the nonlinear predictive model is further a function of yeast concentration, yeast addition, yeast activity, biomass concentration, batch progress, or pH.
25. The system of claim 17 , wherein the control system is distributed over a plurality of computers.