. . "\u010Cl\u00E1nek je v\u011Bnov\u00E1n r\u016Fzn\u00FDm p\u0159\u00EDstup\u016Fm k \u0159\u00EDzen\u00ED destila\u010Dn\u00EDch kolon se dv\u011Bmi vstupy a dv\u011Bmi v\u00FDstupy. Koncentrace destil\u00E1tu a zbytku jsou \u0159\u00EDzeny: dv\u011Bmi decentralizovan\u00FDmi PID regul\u00E1tory, PID regul\u00E1tory s kompenz\u00E1torem, dvourozm\u011Brov\u00FDm prediktivn\u00EDm regul\u00E1torem a neline\u00E1rn\u00EDm prediktivn\u00EDm regul\u00E1torem."@cs . "TITO control of distillation column (PID, decoupling, GPC, nonlinear GPC)" . "978-80-7194-927-5" . "7"^^ . "105-111" . . . . "RIV/00216275:25510/07:00006217" . . . "Univerzita Pardubice" . "TITO control of distillation column (PID, decoupling, GPC, nonlinear GPC)"@en . "RIV/00216275:25510/07:00006217!RIV08-MSM-25510___" . "[3C9C3781900A]" . . . . "Pardubice" . "Pardubice" . . "Paper deals with different two-input two-output (TITO) control approaches for high-purity binary distillation column. Distillate and bottom product concentrations are controlled with: two decentralized (independent) PID controllers, two PID controllers with decoupling term, TITO Generalized Predictive Controller (GPC) - [1], [2], nonlinear TITO GPC. Three different control structures are considered (L,V), (D,V) and (D/(L+D),V/B). The work arises and continues in [3] and [4] where the column model was derived and step responses of the different control structures and PID TITO control experiments were studied."@en . "2007-01-17+01:00"^^ . "Dvourozm\u011Brov\u00E9 \u0159\u00EDzen\u00ED destila\u010Dn\u00ED kolony (PID, decoupling, GPC, neline\u00E1rn\u00ED GPC)"@cs . . . "Paper deals with different two-input two-output (TITO) control approaches for high-purity binary distillation column. Distillate and bottom product concentrations are controlled with: two decentralized (independent) PID controllers, two PID controllers with decoupling term, TITO Generalized Predictive Controller (GPC) - [1], [2], nonlinear TITO GPC. Three different control structures are considered (L,V), (D,V) and (D/(L+D),V/B). The work arises and continues in [3] and [4] where the column model was derived and step responses of the different control structures and PID TITO control experiments were studied." . . "Sborn\u00EDk p\u0159\u00EDsp\u011Bvk\u016F II. konference s mez. \u00FA\u010Dast\u00ED Teorie dopravn\u00EDch syst\u00E9m\u016F 2007" . . . "distillation; TITO control; PID; decoupling; GPC"@en . "Honc, Daniel" . "Havl\u00ED\u010Dek, Libor" . "Haber, Robert" . "3"^^ . "TITO control of distillation column (PID, decoupling, GPC, nonlinear GPC)" . "455243" . "TITO control of distillation column (PID, decoupling, GPC, nonlinear GPC)"@en . . "Dvourozm\u011Brov\u00E9 \u0159\u00EDzen\u00ED destila\u010Dn\u00ED kolony (PID, decoupling, GPC, neline\u00E1rn\u00ED GPC)"@cs . "25510" . "2"^^ . . . "Z(MSM0021627505)" .