Nonlinear predictive control for maximization of CO2 bio-fixation by microalgae in a photobioreactor

被引:42
作者
Tebbani, Sihem [1 ]
Lopes, Filipa [2 ]
Filali, Rayen [1 ]
Dumur, Didier [1 ]
Pareau, Dominique [2 ]
机构
[1] SUPELEC, Control Dept, Syst Sci E3S, F-91192 Gif Sur Yvette, France
[2] Ecole Cent Paris, Lab Genie Proc & Mat, F-92295 Chatenay Malabry, France
关键词
Microalgae; Photobioreactor; Nonlinear model predictive control; Interval observers; GENERIC MODEL CONTROL; FED-BATCH CULTURES; CARBON-DIOXIDE; INTERVAL OBSERVERS; MITIGATION; SYSTEMS;
D O I
10.1007/s00449-013-0928-0
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
In the framework of environment preservation, microalgae biotechnology appears as a promising alternative for CO2 mitigation. Advanced control strategies can be further developed to maximize biomass productivity, by maintaining these microorganisms in bioreactors at optimal operating conditions. This article proposes the implementation of Nonlinear Predictive Control combined with an on-line estimation of the biomass concentration, using dissolved carbon dioxide concentration measurements. First, optimal culture conditions are determined so that biomass productivity is maximized. To cope with the lack of on-line biomass concentration measurements, an interval observer for biomass concentration estimation is built and described. This estimator provides a stable accurate interval for the state trajectory and is further included in a nonlinear model predictive control framework that regulates the biomass concentration at its optimal value. The proposed methodology is applied to cultures of the microalgae Chlorella vulgaris in a laboratory-scale continuous photobioreactor. Performance and robustness of the proposed control strategy are assessed through experimental results.
引用
收藏
页码:83 / 97
页数:15
相关论文
共 52 条
[1]   Bioprocess control: Advances and challenges [J].
Alford, Joseph S. .
COMPUTERS & CHEMICAL ENGINEERING, 2006, 30 (10-12) :1464-1475
[2]  
[Anonymous], 1987, Unconstrained Optimization: Practical Methods of Optimization
[3]   Dynamic optimization of chemical and biochemical processes using restricted second-order information [J].
Balsa-Canto, E ;
Banga, JR ;
Alonso, AA ;
Vassiliadis, VS .
COMPUTERS & CHEMICAL ENGINEERING, 2001, 25 (4-6) :539-546
[4]   Modelling of a continuous pilot photobioreactor for microalgae production [J].
Baquerisse, D ;
Nouals, S ;
Isambert, A ;
dos Santos, PF ;
Durand, G .
JOURNAL OF BIOTECHNOLOGY, 1999, 70 (1-3) :335-342
[5]  
Bastin G, 1990, Process Measurement and Control, V1
[6]  
Becerra-Celis G, 2009, THESIS ECOLE CENTRAL
[7]   NONLINEAR CONTROL OF CHEMICAL PROCESSES - A REVIEW [J].
BEQUETTE, BW .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1991, 30 (07) :1391-1413
[8]   Nonlinear observers for a class of biological systems: Application to validation of a phytoplanktonic growth model [J].
Bernard, O ;
Sallet, G ;
Sciandra, A .
IEEE TRANSACTIONS ON AUTOMATIC CONTROL, 1998, 43 (08) :1056-1065
[9]   Hurdles and challenges for modelling and control of microalgae for CO2 mitigation and biofuel production [J].
Bernard, Olivier .
JOURNAL OF PROCESS CONTROL, 2011, 21 (10) :1378-1389
[10]   Cultivation, photobioreactor design and harvesting of microalgae for biodiesel production: A critical review [J].
Chen, Chun-Yen ;
Yeh, Kuei-Ling ;
Aisyah, Rifka ;
Lee, Duu-Jong ;
Chang, Jo-Shu .
BIORESOURCE TECHNOLOGY, 2011, 102 (01) :71-81