TY - JOUR
T1 - Controllability analysis of thermally coupled distillation systems
T2 - Five-component mixtures
AU - Segovia-Hernández, Juan Gabriel
AU - Ledezma-Martínez, Minerva
AU - Carrera-Rodríguez, Marcelino
AU - Hernández, Salvador
PY - 2007/1/3
Y1 - 2007/1/3
N2 - The theoretical control properties and dynamic responses under closed-loop operation of thermally coupled distillation sequences for the separation of five-component mixtures of hydrocarbons were compared to those of conventional distillation sequences. Seven thermally coupled arrangements were investigated: five thermally coupled distillation sequences with three recycles and two thermally coupled distillation schemes with two recycles. The preliminary steady-state design of complex schemes was obtained by starting from a conventional distillation sequences and then optimizing for minimum energy consumption [Calzon-McConville, C. J.; Rosales-Zamora, M. B.; Segovia-Hernández, J. G.; Hernández, S.; Rico-Ramírez, V. Design and Optimization of Thermally Coupled Distillation Schemes for the Separation of Multicomponent Mixtures. Ind. Eng. Chem. Res. 2006, 45, 724]. The control properties of the sequences considered were obtained by using the singular value decomposition technique at zero frequency. It was found that, in general, the coupled schemes present theoretical control properties similar to or better than those of conventional distillation sequences. This result was corroborated by using rigorous closed-loop dynamic simulations. As a result, one can conclude that the energy savings predicted for thermally coupled distillation sequences are achieved without introducing additional control problems if we assume constant pressure drops in columns.
AB - The theoretical control properties and dynamic responses under closed-loop operation of thermally coupled distillation sequences for the separation of five-component mixtures of hydrocarbons were compared to those of conventional distillation sequences. Seven thermally coupled arrangements were investigated: five thermally coupled distillation sequences with three recycles and two thermally coupled distillation schemes with two recycles. The preliminary steady-state design of complex schemes was obtained by starting from a conventional distillation sequences and then optimizing for minimum energy consumption [Calzon-McConville, C. J.; Rosales-Zamora, M. B.; Segovia-Hernández, J. G.; Hernández, S.; Rico-Ramírez, V. Design and Optimization of Thermally Coupled Distillation Schemes for the Separation of Multicomponent Mixtures. Ind. Eng. Chem. Res. 2006, 45, 724]. The control properties of the sequences considered were obtained by using the singular value decomposition technique at zero frequency. It was found that, in general, the coupled schemes present theoretical control properties similar to or better than those of conventional distillation sequences. This result was corroborated by using rigorous closed-loop dynamic simulations. As a result, one can conclude that the energy savings predicted for thermally coupled distillation sequences are achieved without introducing additional control problems if we assume constant pressure drops in columns.
UR - http://www.scopus.com/inward/record.url?scp=33846708653&partnerID=8YFLogxK
U2 - 10.1021/ie060635s
DO - 10.1021/ie060635s
M3 - Artículo
SN - 0888-5885
VL - 46
SP - 211
EP - 219
JO - Industrial and Engineering Chemistry Research
JF - Industrial and Engineering Chemistry Research
IS - 1
ER -