A rigorous minlp model for the optimal synthesis and operation of utility plants

Chemical Engineering Research and Design

Volumn 76, Issue 3, 1998, Pages 246-258

  Bruno, J C ^a   Fernandez, F ^a   Castells, F ^a   Grossmann, I E ^b  

^a UNIVERSITAT ROVIRA I VIRGILI   (Spain)

^b CARNEGIE MELLON UNIVERSITY   (United States)

Author keywords

Mixed integer optimization; Process integration; Utility systems

Indexed keywords

CHEMICAL EQUIPMENT; COMPUTER SOFTWARE; COST EFFECTIVENESS; ENTHALPY; ENTROPY; INDUSTRIAL HEATING; INTEGER PROGRAMMING; MATHEMATICAL MODELS; NONLINEAR EQUATIONS; NONLINEAR PROGRAMMING; PROCESS ENGINEERING; STEAM TURBINES;

MIXED INTEGER NONLINEAR PROGRAMMING; SOFTWARE PACKAGE STEAM;

CHEMICAL PLANTS;

EID: 0032028387     PISSN: 02638762     EISSN: None     Source Type: Journal    
DOI: 10.1205/026387698524901     Document Type: Article

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