工艺优化
工艺工程
过程(计算)
生产(经济)
工业生产
原材料
批量生产
间歇式反应器
非线性系统
计算机科学
利润(经济学)
产量(工程)
工程类
数学优化
数学
运营管理
化学
生物化学
物理
材料科学
有机化学
量子力学
环境工程
凯恩斯经济学
冶金
经济
催化作用
宏观经济学
微观经济学
操作系统
作者
Jan G. Rittig,Jan C. Schulze,Lars Henrichfreise,Sebastian Recker,Ron Feller,Alexander Mitsos,Adel Mhamdi
出处
期刊:Computer-aided chemical engineering
日期:2023-01-01
卷期号:: 1175-1180
标识
DOI:10.1016/b978-0-443-15274-0.50187-6
摘要
Modeling and optimization of fed-batch reactors with several multi-step reaction pathways is challenging due to the nonlinear dynamic system behavior and large number of kinetic parameters. We showcase the model-based optimization of an industrial (20 m3) fed-batch reactor by using our open-source dynamic optimization software DyOS. First, we build a detailed mechanistic model of the fed-batch reactor. Second, we conduct parameter estimation of the mechanistic model with 25 states and 44 fitting parameters using historic time-series industrial production data. Third, we perform dynamic multi-stage optimization and identify optimal feeding profiles for the operation, targeting improvements in economic profit over the established experience-based production routine. We demonstrate substantial economic improvement: The optimized production recipe can save up to 10% of raw material at the same yield of main product. Our findings underline the strong capabilities of model-based process optimization and its application to industrial challenges in process design and operation.
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