A novel hybrid simulation-optimization approach for the optimal design of multicomponent distillation columns


Autoria(s): Reyes-Labarta, Juan A.; Caballero, José A.; Marcilla, Antonio
Contribuinte(s)

Universidad de Alicante. Departamento de Ingeniería Química

Cálculo del Equilibrio entre Fases

Procesado y Pirólisis de Polímeros

Data(s)

02/07/2012

02/07/2012

01/06/2012

Resumo

Póster presentado en Escape 22, European Symposium on Computer Aided Process Engineering, University College London, UK, 17-20 June 2012.

This work introduces a systematic and analytical tray by tray method for the optimal and rigorous design of multicomponent distillation columns where, for a given feasible separation, convergence is almost always guaranteed in calculation times comparable to those used by commercial simulation packages. However, in this case the total number of stages and the optimal feed location are simultaneously determined. The distillate flow rate and the reflux ratio can be optimised in an outer loop providing the method a great flexibility. The commercial process simulator Hysys® has been used to solve the rigorous VLE using the available thermodynamic models such as NRTL, and MatLab® to implement the optimization algorithm.

Spanish Ministerio de Ciencias e Innovación (PPQ, CTQ2009-14420-C02-02).

Identificador

7378

http://hdl.handle.net/10045/23196

Idioma(s)

eng

Relação

Ingeniería Química

Fundamentos de Operaciones de Separación

Direitos

Licencia Creative Commons Reconocimiento-NoComercial-SinObraDerivada 3.0

info:eu-repo/semantics/openAccess

Palavras-Chave #Distillation #Tray-type separators #Multicomponent mixtures #Hybrid simulation-optimization #Optimal processes design #Ponchon-Savarit method #Ingeniería Química
Tipo

info:eu-repo/semantics/conferenceObject