Studies in the synthesis of control structures for chemical processes

Part IV. Design of steady‐state optimizing control structures for chemical process units

Research output: Contribution to journalArticle

51 Citations (Scopus)

Abstract

The design of the steady‐state optimizing control for a single unit is formulated within the framework of the nonlinear mathematical programming theory. Alternative implementational strategies are developed and a multilevel screening procedure is proposed to arrive at the best optimizing control configuration. Numerical examples on a fluid catalytic cracking unit and a distillation column demonstrate the systematic design and the synthesis of the most promising optimizing control structures for these systems.

Original languageEnglish (US)
Pages (from-to)975-991
Number of pages17
JournalAICHE Journal
Volume26
Issue number6
DOIs
StatePublished - Jan 1 1980
Externally publishedYes

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Chemical Phenomena
Distillation
Chemical reactions
Programming theory
Fluid catalytic cracking
Distillation columns
Nonlinear programming
Screening

ASJC Scopus subject areas

  • Biotechnology
  • Environmental Engineering
  • Chemical Engineering(all)

Cite this

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abstract = "The design of the steady‐state optimizing control for a single unit is formulated within the framework of the nonlinear mathematical programming theory. Alternative implementational strategies are developed and a multilevel screening procedure is proposed to arrive at the best optimizing control configuration. Numerical examples on a fluid catalytic cracking unit and a distillation column demonstrate the systematic design and the synthesis of the most promising optimizing control structures for these systems.",
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