Optimal control of a two-stage reactor system
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T. Hirmajer
und
M. Fikar
Abstract
Optimal operation policies were investigated for a batch reactor system with two different operation stages. At the end of the first nonisothermal stage one of the reactants was added. Since that moment the reactor was operated isothermally. In each stage behavior of the reactor was described by a set of differential equations. The maximum conversion problem was investigated subject to various operating constraints. Dynamic optimization based on the control vector parametrization was used to find the optimal control profile. Gradients of the resulting nonlinear programming problem were obtained by adjoint method based on the optimal control theory.
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© 2006 Institute of Chemistry, Slovak Academy of Sciences
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Artikel in diesem Heft
- FTIR study of gamma-irradiated cis-1,4-polyisoprene
- Comparison of betaine and l-stachydrine as phase-transfer catalysts in Michael addition and Darzens reaction
- Synthesis and cyclization reactions with pyrazolopyrimidinyl keto esters part I. Reactivity of pyrazolopyrimidinyl β-keto ester and pyrazolopyrimidinyl α,β-unsaturated ketones
- Electrodeposition of mercury film on electrodes modified with clay minerals
- Properties of Ni-W alloy coatings on steel substrate
- Effect of chloride ions on the kinetics of nitrobenzene reduction by powdered iron
- Displacement washing of pulp with urea solutions
- Methane esterification in oleum
- Momentum transfer in an agitated vessel with off-centred impellers
- Optimal control of a two-stage reactor system
- Effect of span 20 concentration on oxalic acid production from post-refining fatty acids by Aspergillus niger XP
- Citric acid production from raw glycerol by acetate mutants of Yarrowia lipolytica
- Phosphonium ionic liquids as new, reactive extractants of lactic acid
