Control of an Industrial Scale Bioreactor using a PAT Analyser

S. Goldrick, E. Mercer, G. Montague, D. Lovett, B. Lennox
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引用次数: 2

Abstract

Abstract This work investigates the application of a “Process Analytical Technology” (PAT) analyser to control the substrate concentration over traditional sequential batch control for an industrial scale fed-batch penicillin fermentation. A simulation that utilises the historical data from four batches, where a sequential batch control strategy was implemented, was used as the benchmark reference for this comparison. The simulation accurately predicts the main outputs variables of biomass and penicillin, given the inputs from the historical data set. The simulation includes a PAT analyser, used to build a calibration model with the available off-line substrate concentration from one of the batches. The prediction from this calibration model was used as the controlled variable within a proportional integral (PI) controller to manipulate the substrate feed rate for the three remaining batches. Performance of each control strategy was analysed by comparing the final penicillin yield of each batch. An increase of 35, 20 and 9% was observed for the three batches controlled using the PI controller compared with the sequential batch control strategy.
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用PAT分析仪控制工业规模的生物反应器
摘要:本工作研究了“过程分析技术”(PAT)分析仪在工业规模补料批青霉素发酵过程中控制底物浓度的应用。利用来自四个批次的历史数据的模拟(其中实现了顺序批次控制策略)被用作该比较的基准参考。给定历史数据集的输入,模拟准确地预测了生物质和青霉素的主要输出变量。模拟包括一个PAT分析仪,用于建立一个校准模型,该模型具有来自其中一个批次的可用离线底物浓度。该校准模型的预测被用作比例积分(PI)控制器中的控制变量,以操纵剩余三个批次的底物进料速率。通过比较每批青霉素的最终产率,分析各控制策略的效果。与顺序批控制策略相比,使用PI控制器控制的三个批次增加了35%,20%和9%。
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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