Analysis of Multi-Loop Control Structures of Dividing-Wall Distillation Columns Using a Fundamental Model

被引:13
作者
Tututi-Avila, Salvador [1 ,2 ]
Jimenez-Gutierrez, Arturo [2 ]
Hahn, Juergen [1 ]
机构
[1] Rensselaer Polytech Inst, Dept Biomed Engn, Dept Chem & Biol Engn, Troy, NY 12180 USA
[2] Inst Tecnol Celaya, Dept Ingn Quim, Celaya 38010, Gto, Mexico
关键词
dividing-wall column; distillation; petlyuk; IMC;
D O I
10.3390/pr2010180
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Dividing-wall columns (DWCs) have significant potential as energy-efficient processes for the separation of multicomponent mixtures. However, in addition to an efficient steady state design, dynamics and control also play a major part for the success of a technology. This is especially so for complex distillation systems. This paper investigates the dynamics of a dividing wall column used for the separation of ternary mixtures. A detailed dynamic first principles-based model of the column I s developed in gPROMS. The model is used to generate data used for control loop pairing via the Relative Gain Array (RGA), and controller parameters are found by using Internal Model Control (IMC) tuning. The best control structures for DWC systems, involving four different ternary mixtures, and two different feed compositions for each mixture, are investigated.
引用
收藏
页码:180 / 199
页数:20
相关论文
共 53 条
[1]   A method to draw fully thermally coupled distillation column configurations for multicomponent distillation [J].
Agrawal, R .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2000, 78 (A3) :454-464
[2]   RIGOROUS DYNAMIC-MODELS OF DISTILLATION-COLUMNS [J].
CHOE, YS ;
LUYBEN, WL .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1987, 26 (10) :2158-2161
[3]   Complex distillation arrangements: Extending the Petlyuk ideas [J].
Christiansen, AC ;
Skogestad, S ;
Lien, K .
COMPUTERS & CHEMICAL ENGINEERING, 1997, 21 :S237-S242
[4]  
Coulson J. M., 2009, COULSON RICHARDSONS, V1, P895
[5]   Dividing wall column-A breakthrough towards sustainable distilling [J].
Dejanovic, I. ;
Matijasevic, Lj. ;
Olujic, Z. .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2010, 49 (06) :559-580
[6]   Optimal design of thermally coupled distillation columns [J].
Dünnebier, G ;
Pantelides, CC .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1999, 38 (01) :162-176
[7]   Control structure selection for three-product Petlyuk (dividing-wall) column [J].
Dwivedi, Deeptanshu ;
Halvorsen, Ivar J. ;
Skogestad, Sigurd .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2013, 64 :57-67
[8]   Energy saving and capital cost evaluation in distillation column sequences with a divided wall column [J].
Errico, Massimiliano ;
Tola, Giuseppe ;
Rong, Ben-Guang ;
Demurtas, Daniele ;
Turunen, Ilkka .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2009, 87 (12A) :1649-1657
[9]   COMPARISON OF ENERGY MODELS FOR DISTILLATION-COLUMNS [J].
FUENTES, C ;
LUYBEN, WL .
INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1982, 21 (03) :323-325
[10]   The interactions of design, control and operability in reactive distillation systems [J].
Georgiadis, MC ;
Schenk, M ;
Pistikopoulos, EN ;
Gani, R .
COMPUTERS & CHEMICAL ENGINEERING, 2002, 26 (4-5) :735-746