1996
DOI: 10.1016/s0167-6911(96)00057-6
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On constrained infinite-time linear quadratic optimal control

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Cited by 263 publications
(113 citation statements)
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“…The normalized inputs into the system are the ows of monomer MMA u 1 , monomer VA u 2 , initiator u 3 , and transfer agent u 4 , and the temperature of the reactor jacket u 5 . The normalized outputs of the systems are the polymer production rate y 1 , mole fraction of MMA in the polymer y 2 , average molecular weight of the polymer y 3 , and reactor temperature y 4 .…”
mentioning
confidence: 99%
“…The normalized inputs into the system are the ows of monomer MMA u 1 , monomer VA u 2 , initiator u 3 , and transfer agent u 4 , and the temperature of the reactor jacket u 5 . The normalized outputs of the systems are the polymer production rate y 1 , mole fraction of MMA in the polymer y 2 , average molecular weight of the polymer y 3 , and reactor temperature y 4 .…”
mentioning
confidence: 99%
“…The inclusion of P can improve the performance the MPC controller (with a fixed-length horizon) to some extent and the stability can be guaranteed when H p is sufficiently large [3,12,18].…”
Section: Mpc Controller Developmentmentioning
confidence: 99%
“…The final cost matrix P may be taken as the solution of the algebraic Riccati equation. With the assumption that no constraints are active for N k ≥ this corresponds to an infinite horizon LQ criterion, and the MPC is stabilizing [5]. It is shown in [1] that by substituting:…”
Section: Explicit Mpc and Exact Mp-qpmentioning
confidence: 99%