Nonlinear model predictive control of a biofuel fermentation process
First Claim
1. A method for managing a batch fermentation process in a biofuel production process, comprising:
- providing a nonlinear control model of yeast growth and fermentable sugar concentration for biofuel production in a batch fermentation process of a biofuel production process, wherein yeast growth is a function of a cooler return temperature of a fermenter, metabolic heat generation in the fermenter, and a volumetric change in a fermentation tank;
receiving process information for the batch fermentation process, wherein the process information includes the fermenter cooler return temperature;
executing the nonlinear control model of yeast growth and fermentable sugar concentration using the process information as input, thereby determining target values of one or more fermentation process variables and an optimal batch temperature trajectory during filling of the fermentation tank that substantially maximizes yeast growth and achieves target fermentable sugar concentrations, wherein the one or more target values comprise a mash flow rate or a yeast addition rate; and
controlling the mash flow rate or the yeast addition rate during filling of the fermentation tank in accordance with the determined target values for the one or more fermentation process variables and the optimal batch temperature trajectory.
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Abstract
A system and method are provided for managing batch fermentation in a biofuel production process. A nonlinear control model of yeast growth and fermentable sugar concentration for biofuel (e.g., fuel ethanol) production in a batch fermentation process (pure and/or fed-batch fermentation) of a biofuel production process is provided. Process information for the batch fermentation process is received, and the nonlinear control model executed using the process information as input to determine values of one or more fermentation process variables for the batch fermentation process, e.g., fermentation temperature and/or enzyme flow, for substantially maximizing yeast growth and achieving target fermentable sugar concentrations. The batch fermentation process is then controlled in accordance with the determined values for the one or more fermentation process variables to substantially maximize yeast growth and achieve target fermentable sugar concentrations, where substantially maximizing yeast growth and achieving target fermentable sugar concentrations substantially maximizes biofuel production in the batch fermentation process.
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Citations
23 Claims
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1. A method for managing a batch fermentation process in a biofuel production process, comprising:
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providing a nonlinear control model of yeast growth and fermentable sugar concentration for biofuel production in a batch fermentation process of a biofuel production process, wherein yeast growth is a function of a cooler return temperature of a fermenter, metabolic heat generation in the fermenter, and a volumetric change in a fermentation tank; receiving process information for the batch fermentation process, wherein the process information includes the fermenter cooler return temperature; executing the nonlinear control model of yeast growth and fermentable sugar concentration using the process information as input, thereby determining target values of one or more fermentation process variables and an optimal batch temperature trajectory during filling of the fermentation tank that substantially maximizes yeast growth and achieves target fermentable sugar concentrations, wherein the one or more target values comprise a mash flow rate or a yeast addition rate; and controlling the mash flow rate or the yeast addition rate during filling of the fermentation tank in accordance with the determined target values for the one or more fermentation process variables and the optimal batch temperature trajectory. - View Dependent Claims (2, 3, 4, 5, 6, 7, 8, 9, 10)
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11. A computer-accessible memory medium configured for managing a batch fermentation process in a biofuel production process, wherein the memory medium stores:
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a nonlinear control model of yeast growth and fermentable sugar concentration for biofuel production in a batch fermentation process of a biofuel production process, wherein yeast growth is a function of a cooler return temperature of a fermenter, metabolic heat generation in the fermenter, and a volumetric change in a fermentation tank; and program instructions, executable to perform; receiving process information for the batch fermentation process, wherein the process information includes the fermenter cooler return temperature; executing the nonlinear control model of yeast growth and fermentable sugar concentration using the process information as input, thereby determining target values of one or more fermentation process variables and an optimal batch temperature trajectory during filling of the fermentation tank that substantially maximizes yeast growth and achieves target fermentable sugar concentrations, wherein the one or more target values comprise a mash flow rate or a yeast addition rate; and controlling the mash flow rate or the yeast addition rate during filling of the fermentation tank in accordance with the determined target values for the one or more fermentation process variables and the optimal batch temperature trajectory. - View Dependent Claims (12, 13, 14, 15, 16, 17, 18, 19, 20)
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21. A system for managing a batch fermentation process in a biofuel production process, comprising:
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a processor; and a memory medium coupled to the processor, wherein the memory medium stores; a nonlinear control model of yeast growth and fermentable sugar concentration for biofuel production in a batch fermentation process of a biofuel production process, wherein yeast growth is a function of a cooler return temperature of a fermenter, metabolic heat generation in the fermenter, and a volumetric change in a fermentation tank; and program instructions, executable by the processor to; receive process information for the batch fermentation process, wherein the process information includes the fermenter cooler return temperature; execute the nonlinear control model of yeast growth and fermentable sugar concentration using the process information as input, thereby determining target values of one or more fermentation process variables and an optimal batch temperature trajectory during filling of the fermentation tank that substantially maximizes yeast growth and achieves target fermentable sugar concentrations, wherein the one or more target values comprise a mash flow rate or a yeast addition rate; and control the mash flow rate or the yeast addition rate during filling of the fermentation tank in accordance with the determined values for the one or more fermentation process variables and the optimal batch temperature trajectory. - View Dependent Claims (22, 23)
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Specification