A novel proportional-integral-derivative control configuration with application to the control of batch distillation

Industrial and Engineering Chemistry Research

Volumn 39, Issue 2, 2000, Pages 432-440

  Alvarez Ramirez, Jose ^a   Monroy Loperena, Rosendo ^b   Cervantes, Ilse ^c   Morales, America ^a  

^a UNIVERSIDAD AUTÓNOMA METROPOLITANA   (Mexico)

^b Estrategia Sinergica SA de CV   (Mexico)

^c SEPI   (Mexico)

Author keywords

[No Author keywords available]

Indexed keywords

ALGORITHMS; COMPOSITION; CONTROL SYSTEM SYNTHESIS; ERROR COMPENSATION; FEEDBACK CONTROL; NONLINEAR CONTROL SYSTEMS; NONLINEAR SYSTEMS; NUMERICAL METHODS; PROPORTIONAL CONTROL SYSTEMS; TUNING;

BATCH DISTILLATION; CLOSED LOOP TIME CONSTANT; DISTILLATE COMPOSITION; ESTIMATION TIME CONSTANT; MODELLING ERROR COMPENSATION TECHNIQUES; PROPORTIONAL INTEGRAL DERIVATIVE CONTROL; REDUCED ORDER OBSERVER;

DISTILLATION;

BATCH DISTILLATION; MODELING ERROR; PROPORTIONAL CONTROL SYSTEM;

ANALYTIC METHOD; ARTICLE; BACTERIUM CULTURE; CONTROL SYSTEM; DERIVATIZATION; DISTILLATION; FEEDBACK SYSTEM; LINEAR SYSTEM; SIMULATION;

EID: 0034131776     PISSN: 08885885     EISSN: None     Source Type: Journal    
DOI: 10.1021/ie990287c     Document Type: Article

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