2020
DOI: 10.1016/j.jprocont.2020.07.005
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Stabilization of an unstable tubular reactor by nonlinear passive output feedback control

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Cited by 11 publications
(6 citation statements)
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“…In (A1) T, c : [0, 1] × R + → R with T(s, t) representing the reactor temperature at s ∈ [0, 1] and time t ≥ 0, c(s, t) the concentration, D being the diffusion coefficient, v the superficial velocity (assumed to be constant), η the heat interchange coefficient between the cooling jacket with temperature T c (s, t) (that can be used as a control input [27]), δ the adiabatic temperature rise, ρ : R + → R + the reaction rate function, γ the Arrhenius coefficient, and T e , c e the (constant) feed temperature and concentration, respectively.…”
Section: Appendix a Tubular Reactor Modelmentioning
confidence: 99%
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“…In (A1) T, c : [0, 1] × R + → R with T(s, t) representing the reactor temperature at s ∈ [0, 1] and time t ≥ 0, c(s, t) the concentration, D being the diffusion coefficient, v the superficial velocity (assumed to be constant), η the heat interchange coefficient between the cooling jacket with temperature T c (s, t) (that can be used as a control input [27]), δ the adiabatic temperature rise, ρ : R + → R + the reaction rate function, γ the Arrhenius coefficient, and T e , c e the (constant) feed temperature and concentration, respectively.…”
Section: Appendix a Tubular Reactor Modelmentioning
confidence: 99%
“…Considering in a first approximation that the temperature deviation can be neglected (e.g., due to some appropriate control through the cooling jacket temperature [27]) one ob-…”
Section: Appendix a Tubular Reactor Modelmentioning
confidence: 99%
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“…An optimal integral SMC‐based CNF is suggested for an electrostatic micro‐mirror [27]. An unstable reactor can be stabilized by a passive output feedback control [28].…”
Section: Introductionmentioning
confidence: 99%
“…From this set of possible equilibria, the unstable steady state is usually of industrial interest as it corresponds to a high reaction efficiency with admissible temperature. Thus, many studies have been dedicated to the control of tubular reactors described by partial differential equations models around the unstable steady state profile [1,6,8,13,12,22,24,28,32].…”
mentioning
confidence: 99%