Analytical Synthesis of Non-Linear Control Algorithms of a Chemical Reactor Thermal Mode
Abstract
:1. Introduction
2. Control Object Description and Control Problem Statement
2.1. Control Algorithm Synthesis by the ADAR Method Based on a Sequential Set of Invariant Manifolds
2.2. Synthesis of a Cascade Thermal Control System
2.3. Computer Simulation of the Control System
- V = 500 L, Vc = 290 L;
- CAin = 19.74 mol/L, CBin = 10.93 mol/L;
- υ1 = 1.5 L/min, υ2 = 3.5 L/min, υ = 5 L/min, υc = 3.84 L/min;
- t1 = 20 °C, t2 = 30 °C, tcin = 20 °C;
- K = 12 kJ/(m2·min·K), F = 2.9 m2;
- ρ = 0.9 kg/L, ρc = 1 kg/L;
- C = 2 kJ/(kg·K), Cc = 4.18 kJ/(kg·K);
- ΔH = 80 kJ/mol, E1 = 48635 J/mol, k10 = 109860 l/(mol·min).
3. Conclusions
Author Contributions
Funding
Institutional Review Board Statement
Informed Consent Statement
Conflicts of Interest
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Labutin, A.N.; Vaško, M.; Kuric, I.; Nevinitsyn, V.Y.; Sága, M.; Zagarinskaya, Y.N.; Volkova, G.V. Analytical Synthesis of Non-Linear Control Algorithms of a Chemical Reactor Thermal Mode. Processes 2021, 9, 644. https://doi.org/10.3390/pr9040644
Labutin AN, Vaško M, Kuric I, Nevinitsyn VY, Sága M, Zagarinskaya YN, Volkova GV. Analytical Synthesis of Non-Linear Control Algorithms of a Chemical Reactor Thermal Mode. Processes. 2021; 9(4):644. https://doi.org/10.3390/pr9040644
Chicago/Turabian StyleLabutin, Alexander Nikolaevich, Milan Vaško, Ivan Kuric, Vladimir Yuryevich Nevinitsyn, Milan Sága, Yulia Nikolaevna Zagarinskaya, and Galina Vitalievna Volkova. 2021. "Analytical Synthesis of Non-Linear Control Algorithms of a Chemical Reactor Thermal Mode" Processes 9, no. 4: 644. https://doi.org/10.3390/pr9040644