Control properties of thermally coupled distillation sequences for different operating conditions

被引:46
作者
Segovia-Hernandez, Juan Gabriel [1 ]
Hernandez-Vargas, Esteban Abelardo [1 ]
Marquez-Munoz, Jorge Alberto [1 ]
机构
[1] Univ Guanajuato, Fac Quim, Guanajuato 36050, Mexico
关键词
thermally coupled distillation schemes; control properties; energy consumption; THERMODYNAMIC ANALYSIS; ENERGY-EFFICIENCY; CONTROL BEHAVIOR; OPTIMAL-DESIGN; COLUMN; CONTROLLABILITY; OPTIMIZATION; INDUSTRIAL; SYSTEMS;
D O I
10.1016/j.compchemeng.2006.08.004
中图分类号
TP39 [计算机的应用];
学科分类号
081203 ; 0835 ;
摘要
The understanding of the dynamic behavior of distillation columns has received considerable attention due to the fact that distillation is one of the most widely used unit operations in chemical process industries. Thermally coupled distillation sequences (TCDS) can provide significant energy savings with respect to the operation of sequences based on conventional distillation columns. TCDS exhibit a complex structure, with recycle streams, that appear to affect their controllability properties. One potential solution to this problem has been suggested through the operation of TCDS under conditions that do not provide minimum energy consumption. The basic idea is that if one changes the operation point, the control properties might change as well. In this work, we analyze the dynamic behavior of two TCDS structures under different operating points, including the one with minimum energy consumption. The control analysis properties are analyzed with the application of the singular value decomposition technique at zero frequency and closed-loop dynamic responses using standard PI controllers. The results show that the controllability properties of distillation sequences may change significantly depending on the selected operation point. (C) 2006 Elsevier Ltd. All rights reserved.
引用
收藏
页码:867 / 874
页数:8
相关论文
共 32 条
[1]  
Abad-Zarate EF, 2006, CAN J CHEM ENG, V84, P381
[2]  
ABDULMUTALIB MI, 1998, T I CHEM ENG-LOND, V76, P308
[3]   Rigorous comparative study of energy-integrated distillation schemes [J].
Annakou, O ;
Mizsey, P .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1996, 35 (06) :1877-1885
[4]   DYNAMIC SIMULATION OF A DISTILLATION COLUMN SEPARATING A MULTICOMPONENT MIXTURE [J].
BERBER, R ;
KARADURMUS, E .
CHEMICAL ENGINEERING COMMUNICATIONS, 1989, 84 :113-127
[5]   Optimal design of thermally coupled distillation columns [J].
Dünnebier, G ;
Pantelides, CC .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1999, 38 (01) :162-176
[6]   ENERGY-REQUIREMENTS OF NONCONVENTIONAL DISTILLATION SYSTEMS [J].
FIDKOWSKI, Z ;
KROLIKOWSKI, L .
AICHE JOURNAL, 1990, 36 (08) :1275-1278
[7]   Thermodynamic analysis of thermally coupled distillation sequences [J].
Flores, OA ;
Cárdenas, JC ;
Hernández, S ;
Rico-Ramírez, V .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2003, 42 (23) :5940-5945
[8]  
Harmsen GJ, 2004, CHEM ENG PROCESS, V43, P671, DOI 10.1016/j.cep.2003.02.003
[9]  
Hernández S, 2003, CAN J CHEM ENG, V81, P1087
[10]  
Hernandez S, 1996, CHEM ENG RES DES, V74, P357