MODELING THE CONFIGURATION CHARACTERISTICS AND OPERATING REGIMES OF A BINARY DISTILLATION COLUMN FOR CONTROL

被引：0

作者：

Juarez-Romero, D. ^{[1
]}

Lopez-Estrada, F. R. ^{[3
]}

Astorga-Zaragoza, C. M. ^{[2
]}

Alvarado, V. ^{[2
]}

Hernandez, J. A. ^{[1
]}

Tellez-Anguiano, A. C. ^{[2
]}

机构：

[1] Univ Autonoma Estado Morelos, Ctr Invest Ingn & Ciencias Aplicadas, Cuernavaca 62209, Morelos, Mexico

[2] Ctr Nacl Invest & Desarrollo Tecnol, Cuernavaca 62490, Morelos, Mexico

[3] Inst Tecnol Tuxtla Gutierrez, Dept Ingn Elect & Elect, Gutierrez 29000, Chiapas, Mexico

来源：

REVISTA MEXICANA DE INGENIERIA QUIMICA | 2010年 / 9卷 / 03期

关键词：

distillation column dynamics; condensate subcooling; model fidelity; distillation column configuration; DYNAMIC-MODEL; STARTUP;

D O I：

暂无

中图分类号：

O69 [应用化学];

学科分类号：

081704 ;

摘要：

This work describes a mathematical model for a distillation column which includes mass, composition, and energy balances, where the thermodynamic and equilibrium properties are represented by an equation of state. This model focuses on the specific configuration of the boiler (container plus boiling vessel) and the vertical condenser (with an external cooling jacket plus a helical pipe) and also on the effect of atmospheric and subcooling conditions in the condenser. For the sake of flexibility and to represent consistently the semi-continuous conditions during the startup, the equations are solved as a DAEs set. Results are compared with experimental data from a Methanol-Ethanol mixture in a 10-tray distillation column. The effects of configuration and operating conditions on the model fidelity are discussed. The model describes the semi-continuous hydraulics and the desired temperature profile that is expected to be used for process control.

引用

页码：367 / 382

页数：16

共 50 条

[41] Model Identification and Predictive Control of a Laboratory Binary Distillation Column
Drgona, Jan
Klauco, Martin
Valo, Richard
Bendzala, Jakub
Fikar, Miroslav
PROCEEDINGS OF THE 2015 20TH INTERNATIONAL CONFERENCE ON PROCESS CONTROL (PC), 2015, : 357 - 362
[42] ONLINE MULTIVARIABLE ADAPTIVE-CONTROL OF A BINARY DISTILLATION COLUMN
THAM, MT
VAGI, F
MORRIS, AJ
WOOD, RK
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1991, 69 (04): : 997 - 1009
[43] Design of an Internal Model Control for SISO Binary Distillation Column
Mishra, Rakesh Kumar
Dan, Tarun Kumar
2013 IEEE INTERNATIONAL CONFERENCE ON EMERGING TRENDS IN COMPUTING, COMMUNICATION AND NANOTECHNOLOGY (ICE-CCN'13), 2013, : 666 - 669
[44] HGA fuzzy supervisory control system of a binary distillation column
Pratishthananda, S
Glankwamdee, W
10TH IEEE INTERNATIONAL CONFERENCE ON FUZZY SYSTEMS, VOLS 1-3: MEETING THE GRAND CHALLENGE: MACHINES THAT SERVE PEOPLE, 2001, : 501 - 504
[45] DISTURBANCE DECOUPLING CONTROL WITH STABILITY FOR A BINARY DISTILLATION COLUMN.
Ohno, Hiromu
Nakanishi, Eiji
Memoirs of the Faculty of Engineering, Kobe University, 1982, (29): : 143 - 159
[46] Control of Binary Distillation Column Using Fuzzy PI Controllers
Javadi, Shahram
Hosseini, Jabber
PROCEEDINGS OF THE 8TH INTERNATIONAL CONFERENCE ON APPLICATIONS OF ELECTRICAL ENGINEERING/8TH INTERNATIONAL CONFERENCE ON APPLIED ELECTROMAGNETICS, WIRELESS AND OPTICAL COMMUNICATIONS, 2009, : 103 - 110
[47] NONLINEAR MODEL-BASED CONTROL OF A BINARY DISTILLATION COLUMN
TROTTA, A
BAROLO, M
COMPUTERS & CHEMICAL ENGINEERING, 1995, 19 : S519 - S524
[48] Control of Binary Distillation Column Using Fuzzy PI Controllers
Javadi, Shahram
Hosseini, Jabber
PROCEEDINGS OF THE 9TH WSEAS INTERNATIONAL CONFERENCE ON SIGNAL PROCESSING, COMPUTATIONAL GEOMETRY AND ARTIFICIAL VISION (ISCGAV'09), 2009, : 145 - +
[49] TRIANGULAR DECOUPLING FOR A BINARY DISTILLATION COLUMN UNDER PRESSURE CONTROL
SHIMIZU, K
MATSUBARA, M
IEEE TRANSACTIONS ON AUTOMATIC CONTROL, 1985, 30 (05) : 474 - 477
[50] MINIMUM DEVIATION ADAPTIVE-CONTROL OF A BINARY DISTILLATION COLUMN
KIM, YH
KIM, MH
KIM, JB
JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 1994, 27 (02) : 253 - 256

← 1 2 3 4 5 →