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Adaptive dissolved oxygen control through the glycerol feeding in a recombinant Pichia pastoris cultivation in conditions of oxygen transfer limitation

机译:在氧气转移受限的条件下,通过在重组毕赤酵母培养物中添加甘油来自适应控制溶解氧

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摘要

In high cell density cultivation processes the productivity is frequently constrained by the bioreactor maximum oxygen transfer capacity. The productivity can often be increased by operating the process at low dissolved oxygen concentrations close to the limitation level. This may be accomplished with a closed-loop controller that regulates the dissolved oxygen concentration by manipulating the dominant carbon source feeding rate. In this work we study this control problem in a pilot 50l bioreactor with a high cell density recombinant P. pastoris cultivation in complex media. The study focuses on the design of accurate stable adaptive controllers, with guaranteed exponential convergence and its relation with the calibration of controller parameters. Two adaptive control strategies were tested in the pilot bioreactor: a model reference adaptive controller with a linear reference model and an integral feedback controller with adaptive gain. The latter alternative proved to be more robust to errors in the measurements of the off-gas composition. Concerning the instrumentation, algorithms were derived assuming that both the dissolved oxygen tension and off-gas composition are measured on-line, but also the case of only dissolved oxygen being measured is addressed. It was verified that the measurement of off-gas composition might not improve the controller performance due to measurement and process time delays.
机译:在高细胞密度培养过程中,生产率经常受到生物反应器最大氧气传输能力的限制。通常可以通过在接近极限水平的低溶解氧浓度下操作过程来提高生产率。这可以通过闭环控制器来实现,该控制器通过控制主要碳源的进料速率来调节溶解氧的浓度。在这项工作中,我们研究了在具有复杂培养基的高细胞密度重组巴斯德毕赤酵母培养的中试50l生物反应器中的控制问题。该研究的重点是具有保证指数收敛性及其与控制器参数校准的关系的精确稳定的自适应控制器的设计。在中试生物反应器中测试了两种自适应控制策略:具有线性参考模型的模型参考自适应控制器和具有自适应增益的积分反馈控制器。事实证明,后一种选择对废气成分测量中的误差更加可靠。关于仪器,推导了算法,假定在线测量溶解氧的张力和废气成分,而且还解决了仅测量溶解氧的情况。已经证实,由于测量和处理时间的延迟,废气成分的测量可能不会改善控制器的性能。

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