乳酸生产分批和补料分批发酵器进化优化方法初探

IF 3 Q2 ENGINEERING, CHEMICAL Digital Chemical Engineering Pub Date : 2023-09-01 DOI:10.1016/j.dche.2023.100105
Ashish M. Gujarathi , Swaprabha P. Patel , Badria Al Siyabi
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引用次数: 1

摘要

采用差分进化(DE)算法和遗传算法(GA)对分批发酵和补料分批发酵方式生产阿拉伯枣汁乳酸的动力学参数进行了估计。采用前馈控制、指数进给和改进指数进给等不同的进给方法来获得最优的动力学参数。通过最小化实验数据与模拟模型结果之间的最小二乘误差,找到两种发酵方法的全局最优动力学参数集。在分批和补料分批发酵方法(包括不同的投料策略)中,DE算法的结果要么是目标函数的最小值,要么是生物量生长(X)、底物消耗(S)和产物形成(P)的实验值与模型预测值之间的残差平方和的最小值。使用了六种不同的DE算法策略,并比较了它们在指数投料分批发酵罐中的性能。通过对算法控制参数的分析,确定了指数进料间歇式发酵罐最适合的DE策略为best/1/bin和current to best/1/bin。这篇手稿强调了在给定的生化发酵罐上单个算法性能的局限性和改进。
本文章由计算机程序翻译,如有差异,请以英文原文为准。

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Insight into evolutionary optimization approach of batch and fed-batch fermenters for lactic acid production

Differential evolution (DE) algorithm and genetic algorithm (GA) are used in this study to estimate a set of kinetic parameters for Arabic date juice-based lactic acid production via batch and fed-batch mode of fermentation. Different feeding approaches like feed-forward control, exponential-, and modified exponential- feed are employed to obtain optimum kinetic parameters. The global optimum sets of kinetic parameters for both fermentation methods are found by minimizing the least square error between the experimental data and the simulated model results. In both batch and fed-batch fermentation methods (including different feeding strategies) the DE algorithm resulted in either the least value of the objective function or the least value of the sum of the square of residual errors between the experimental and model-predicted values for biomass growth (X), substrate consumption (S), and product formation (P). Six different strategies of the DE algorithm are used and their performance is compared for exponential feeding fed-batch fermenter. For exponential feeding fed-batch fermenter best suitable DE strategies were found to be best/1/bin and current to best/1/bin based on algorithm control parameters analysis. This manuscript highlights the limitations and improvements in the performance of individual algorithms on the given biochemical fermenters.

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