EventsThe 5th International Electronic Conference on Processes
Published
This submission belongs to the session S4. Process Control, Monitoring and Machine Learning of the event The 5th International Electronic Conference on Processes
Published date
15 Oct, 2026
Academic Editor
author-avatarRavendra Singh
Citation
Mirjalol Yusupov, Zafar Turakulov, Sarvar Rejabov, Control-Oriented Dynamic Modeling of Mashing and Fermentation Processes in Beer Production, in Proceedings of The 5th International Electronic Conference on Processes, 20 October–22 October 2026, MDPI: Basel, Switzerland
Share
Email
Facebook
Twitter
LinkedIn

Control-Oriented Dynamic Modeling of Mashing and Fermentation Processes in Beer Production

image
1. Department of Automation and Digital Control, Tashkent Institute of Chemical Technology, Tashkent, Uzbekistan
2. Department of Industrial Automation, Tashkent State Technical University, Tashkent, Uzbekistan
Abstract

Beer production involves interconnected physicochemical and biochemical processes whose dynamic behaviour substantially affects product quality, process duration, and resource consumption. This study develops an integrated, control-oriented mathematical model of the mashing and fermentation stages of beer production. The mashing process was represented as a four-stage cascade system operating at temperature levels of 45, 63, 72, and 78 °C. Component mass balances, Arrhenius-type temperature-dependent kinetic expressions, and enzymatic hydrolysis relationships were used to describe malt extraction and the formation of fermentable sugars. The final sugar concentration obtained from the mashing model was subsequently introduced as the substrate input to the fermentation model. The fermentation process was described using substrate, biomass, and ethanol concentrations as the principal state variables. The Balling relationship was combined with microbial growth and product-formation equations to establish a nonlinear dynamic model. Monod, Aiba, and Tessier kinetic formulations were evaluated using laboratory observations obtained from an industrial brewery. The Monod model demonstrated the closest agreement with the measured growth behavior, with an estimated maximum specific growth rate of 0.92 h⁻¹, a half-saturation constant of 2.4 g L⁻¹, and a coefficient of determination of 0.985. The resulting nonlinear equations were linearized around nominal operating points and transformed into state-space form to support subsequent controller synthesis. Simulation in Python reproduced the expected exponential reduction in substrate concentration, biomass development, and gradual saturation of ethanol production. The proposed integrated model provides a computationally efficient representation of the main brewing stages and can serve as a basis for model predictive control, state estimation, digital-twin development, and real-time process optimization.

Keywords
beer production
mashing
fermentation
biokinetic model
Monod kinetics
state-space model
process simulation
Adsorptive Removal of Cr(VI) from Synthetic Wastewater Using PVA-Capped CuS/Bentonite Nanocomposites: Kinetic and Isotherm Studies
Phase-Aware Takagi–Sugeno Fuzzy Predictive Control with Moving-Horizon Estimation for Beer Fermentation