Briat Corentin, Khammash Mustafa
Department of Biosystems Science and Engineering, ETH Zürich , Basel, 4058 Switzerland.
ACS Synth Biol. 2018 Feb 16;7(2):419-431. doi: 10.1021/acssynbio.7b00188. Epub 2018 Jan 30.
The production of complex biomolecules by genetically engineered organisms is one of the most promising applications of metabolic engineering and synthetic biology. To obtain processes with high productivity, it is therefore crucial to design and implement efficient dynamic in vivo regulation strategies. We consider here the microbial biofuel production model of Dunlop et al. (2010) for which we demonstrate that an antithetic dynamic integral control strategy can achieve robust perfect adaptation for the intracellular biofuel concentration in the presence of poorly known network parameters and implementation errors in certain rate parameters of the controller. We also show that the maximum equilibrium extracellular biofuel productivity is fully defined by some of the network parameters and, in this respect, it can only be achieved when all the corresponding parameters are perfectly known. Since this optimum is a network property, it cannot be improved by the use of any controller that measures the intracellular biofuel concentration and acts on the production of pump proteins. Additional intrinsic fundamental properties for the process are also unveiled, the most important ones being the existence of a conservation relation between the productivity and the toxicity, a low sensitivity of the optimal productivity with respect to a poor implementation of the set-point for the intracellular biofuel, and a strong intrinsic robustness property of the optimal productivity with respect to poorly known parameters. Taken together, these results demonstrate that a high and robust equilibrium rate of production for the extracellular biofuel can be achieved when the parameters of the model are poorly known and those of the controllers are poorly implemented. Finally, several advantages of the proposed dynamic strategy over a static one are also emphasized.
通过基因工程生物体生产复杂生物分子是代谢工程和合成生物学最具前景的应用之一。因此,为了获得高生产率的过程,设计和实施高效的动态体内调控策略至关重要。我们在此考虑Dunlop等人(2010年)的微生物生物燃料生产模型,我们证明了一种对偶动态积分控制策略能够在网络参数未知以及控制器某些速率参数存在实施误差的情况下,实现对细胞内生物燃料浓度的鲁棒完美适应。我们还表明,最大平衡细胞外生物燃料生产率完全由一些网络参数确定,在这方面,只有当所有相应参数完全已知时才能实现。由于这个最优值是一种网络属性,通过使用任何测量细胞内生物燃料浓度并作用于泵蛋白生产的控制器都无法提高它。该过程的其他内在基本属性也被揭示出来,其中最重要的是生产率和毒性之间存在守恒关系,最优生产率对细胞内生物燃料设定点实施不佳的低敏感性,以及最优生产率对未知参数的强内在鲁棒性。综上所述,这些结果表明,当模型参数未知且控制器参数实施不佳时,仍可实现细胞外生物燃料的高且鲁棒的平衡生产速率。最后,还强调了所提出的动态策略相对于静态策略的几个优点。