Maximizing productivity of a continuous fermenter using nonlinear adaptive optimizing control

被引:9
|
作者
Saha, P [1 ]
Patwardhan, SC [1 ]
Rao, VSR [1 ]
机构
[1] Indian Inst Technol, Dept Chem Engn, Chennai 600036, India
关键词
Specific Growth Rate; Closed Loop; Measurement Noise; Point Change; Loop Performance;
D O I
10.1007/s004490050553
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
The control of a continuously operated fermenter at its maximum productivity level gives rise to a difficult control problem as the location of the optimum operating point changes due to the disturbances. In addition, the fermenter exhibits a change in the sign of the steady state gain near the optimum operating point. This study is aimed at developing an on-line optimizing control scheme that can track the changing location of the steady state optimum so as to maximize the fermenter productivity. A nonlinear Laguerre model, whose parameters are estimated on-line, is used for tracking the optimum operating point. The control at the optimum point is achieved using an adaptive nonlinear MPC strategy that uses the nonlinear Laguerre model for prediction. The efficiency of the proposed algorithm is demonstrated by simulating the control of a continuous fermenter that exhibits shift in the location of the optimum operating point in response to the changes in the maximum specific growth rate. The proposed on-line optimizing control strategy is shown to result in a considerable improvement in the closed loop performance even in the presence of measurement noise.
引用
收藏
页码:15 / 21
页数:7
相关论文
共 50 条
  • [1] Maximizing productivity of a continuous fermenter using nonlinear adaptive optimizing control
    P. Saha
    S. C. Patwardhan
    V. S. Ramachandra Rao
    Bioprocess Engineering, 1999, 20 : 15 - 21
  • [2] Tracking Economic Optimum of a Continuous Fermenter using Adaptive Dual Nonlinear MPC
    Kumar, Kunal
    Patwardhan, Sachin C.
    Noronha, Santosh
    2019 58TH ANNUAL CONFERENCE OF THE SOCIETY OF INSTRUMENT AND CONTROL ENGINEERS OF JAPAN (SICE), 2019, : 581 - 586
  • [3] OPTIMIZING CONTROL OF A CONTINUOUS STIRRED-TANK FERMENTER USING A NEURAL-NETWORK
    NORMANDIN, A
    THIBAULT, J
    GRANDJEAN, BPA
    BIOPROCESS ENGINEERING, 1994, 10 (03): : 109 - 113
  • [4] Optimizing nonlinear adaptive control allocation
    Tjonnås, J
    Johansen, TA
    MODELING IDENTIFICATION AND CONTROL, 2006, 27 (01) : 43 - 56
  • [5] NONLINEAR ADAPTIVE OPTIMIZATION OF BIOMASS PRODUCTIVITY IN CONTINUOUS BIOREACTORS
    SAUVAIRE, P
    MELLICHAMP, DA
    AGRAWAL, P
    BIOPROCESS ENGINEERING, 1991, 7 (03): : 101 - 114
  • [6] Multi-input multi-output control of a continuous fermenter using nonlinear model based controllers
    Prabirkumar Saha
    Qiuping Hu
    Gade Pandu Rangaiah
    Bioprocess Engineering, 1999, 21 : 533 - 542
  • [7] Multi-input multi-output control of a continuous fermenter using nonlinear model based controllers
    Saha, Prabirkumar
    Hu, Qiuping
    Rangaiah, Gade Pandu
    Bioprocess and Biosystems Engineering, 21 (06): : 533 - 542
  • [8] Maximizing the productivity of the microalgae Scenedesmus AMDD cultivated in a continuous photobioreactor using an online flow rate control
    McGinn, Patrick J.
    MacQuarrie, Scott P.
    Choi, Jerome
    Tartakovsky, Boris
    BIOPROCESS AND BIOSYSTEMS ENGINEERING, 2017, 40 (01) : 63 - 71
  • [9] Maximizing the productivity of the microalgae Scenedesmus AMDD cultivated in a continuous photobioreactor using an online flow rate control
    Patrick J. McGinn
    Scott P. MacQuarrie
    Jerome Choi
    Boris Tartakovsky
    Bioprocess and Biosystems Engineering, 2017, 40 : 63 - 71
  • [10] Multi-input multi-output control of a continuous fermenter using nonlinear model based controllers
    Saha, P
    Hu, QP
    Rangaiah, GP
    BIOPROCESS ENGINEERING, 1999, 21 (06) : 533 - 542