Abstract | ||
---|---|---|
A nonlinear dynamical system, in which the feed rates of glycerol and alkali are taken as the control functions, is first proposed to formulate the fed-batch culture of 1,3-propanediol (1,3-PD) production. To maximize the 1,3-PD concentration at the terminal time, a constrained optimal control model is then presented. A solution approach is developed to seek the optimal feed rates based on control vector parametrization method and improved differential evolution algorithm. The proposed methodology yielded an increase by 32.17% of 1,3-PD concentration at the terminal time. |
Year | DOI | Venue |
---|---|---|
2012 | 10.1155/2012/245315 | JOURNAL OF APPLIED MATHEMATICS |
Keywords | Field | DocType |
optimal control | Mathematical optimization,Optimal control,Parametrization,Control theory,Control vector,Nonlinear dynamical systems,Fermentation,Fed-batch culture,Mathematics,Differential evolution algorithm | Journal |
Volume | Issue | ISSN |
2012 | null | 1110-757X |
Citations | PageRank | References |
0 | 0.34 | 7 |
Authors | ||
4 |
Name | Order | Citations | PageRank |
---|---|---|---|
Chongyang Liu | 1 | 31 | 5.81 |
Zhaohua Gong | 2 | 22 | 5.31 |
Zhaoyi Huo | 3 | 0 | 0.34 |
Bangyu Shen | 4 | 1 | 0.69 |