Assessing control strategies for the supercritical extraction from coffee beans: process-based control versus proportional integral derivative

ABSTRACT This article addresses the formulation of a generic model control (GMC) in a supercritical fluid extraction unit (SFE). This alternative control is solved by formulating performance objectives subject to constraints on manipulated, controlled and associated variables. This study shows the p...

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Bibliographic Details
Published inJournal of food process engineering Vol. 28; no. 5; pp. 494 - 505
Main Authors Riverol, C, Cooney, J
Format Magazine Article
LanguageEnglish
Published Oxford, UK and Malden, USA Blackwell Science Inc 01.10.2005
Blackwell
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ISSN0145-8876
1745-4530
DOI10.1111/j.1745-4530.2005.030.x

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Summary:ABSTRACT This article addresses the formulation of a generic model control (GMC) in a supercritical fluid extraction unit (SFE). This alternative control is solved by formulating performance objectives subject to constraints on manipulated, controlled and associated variables. This study shows the performance of the control strategy depends on how the constraints are formulated. The batch extraction of caffeine is the problem proposed in this article. The presence of constraints in the optimization problem makes the overall system nonlinear even though the process dynamics are assumed linear. Hence, the “best” control strategy was determined using field data obtained directly from the pilot plant and compared with the decoupled proportional integral derivative control system actually installed in the plant.
Bibliography:istex:9933864F4C7CB16F82B11F16278E07477160D485
ark:/67375/WNG-C54P8MKT-J
ArticleID:JFPE030
ObjectType-Article-1
SourceType-Scholarly Journals-1
ObjectType-Feature-2
content type line 23
ISSN:0145-8876
1745-4530
DOI:10.1111/j.1745-4530.2005.030.x