EngOpt
2012 – 3rd International Conference on Engineering Optimization, Rio de
Janeiro, Brazil, 01 - 05 July 2012.
Optimal
approach for multicomponent distillation in a petrochemical plant in operation
Maria A. Osorio, Abraham Sanchez, Erika Muñoz, Mayra Ruiz, Oscar
Arroyo
asanchez@cs.buap.mx
ing.erikita@gmail.com
mreyes_77@hotmail.com
oscar_arroyo@hotmail.com
Department of Chemical Engineering, 2 Department of Computer Science, Universidad
Autonoma de Puebla, Mexico
Abstract
Addresses
the case of the multicomponent distillation of methanol in a petrochemical
industry in operation in Puebla, Mexico, with a process synthesis approach that
uses a superstructure containing all possible combinations in which the
elements can be separated from the mixture.
Researchers employ actual data from sequence of the current
distillation columns, combining them with the data obtained from HYSYS
simulation. This superstructure contains the actual data for the option that is
currently in operation and the data obtained with simulation for options that
have not been implemented.
Free Full Text Source: http://www.engopt.org/paper/493.pdf
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