Modeling and Control of Tray Temperature Along with Column Pressure in a Pilot Plant Distillation Column

被引：0

作者：

Rajaraman J. ^{[1
]}

Indiran T. ^{[2
]}

Yadav E.S. ^{[3
]}

Selvanathan S.P. ^{[4
]}

机构：

[1] Department of Electronics and Instrumentation Engineering, Sri Chandrasekharendra Saraswathi Viswa Mahavidyalaya, Tamilnadu, Kanchipuram

[2] Department of Instrumentation and Control Engineering, Manipal Institute of Technology, Manipal Academy of Higher Education, Karnataka, Manipal

[3] Department of Electronics and Instrumentation Engineering, Vignan Institute of Technology and Science, Deshmuki, Telangana, Hyderabad

[4] Department of Chemical Engineering, Manipal Institute of Technology, Manipal Academy of Higher Education, Karnataka, Manipal

来源：

SN Computer Science | 2020年 / 1卷 / 6期

关键词：

Centralized controller; Decentralized controller; Decoupler design; MIMO process;

D O I：

10.1007/s42979-020-00352-3

中图分类号：

学科分类号：

摘要：

A simple control technique based on centralized and decentralized structure is discussed here for a tray temperature along with pressure developed inside the column for a pilot plant distillation column. The flow rate of vapor condenser cooling water is used to control the pressure (P) developed inside the column. The flow rate of the water to condense the vapor increases, when the column pressure increases and vice versa. Some of the other factor that has an impact on the column pressure is the boil-up rate, rate of reflux ow, feed rate, set point change in composition. The internal reflux and the speed of the vapor through the column gets affected by the pressure developed. There exists a strong interaction between the two interdependent variables pressure and temperature. The goal is to regulate the temperature and pressure near the bottom tray by nominally manipulating the reflux flow and boilup rate. © 2020, Springer Nature Singapore Pte Ltd.

引用

共 50 条

[1] Nonlinear Modelling and Fuzzy Control of Steam Temperature for Distillation Column Pilot Plant
Hambali, Najidah
Ab Manan, Muhammad Hafizi
Mohammad, Nurul Nadia
[J]. 2022 IEEE 18TH INTERNATIONAL COLLOQUIUM ON SIGNAL PROCESSING & APPLICATIONS (CSPA 2022), 2022, : 192 - 197
[2] EXPERIMENTAL TRANSIENT RESPONSE OF A PILOT-PLANT DISTILLATION COLUMN .4. RESPONSE OF A 10-TRAY COLUMN
LUYBEN, WL
VERNEUIL, VS
GERSTER, JA
[J]. AICHE JOURNAL, 1964, 10 (03) : 357 - 364
[3] TRAY SELECTION FOR COLUMN TEMPERATURE CONTROL
WOOD, CE
[J]. CHEMICAL ENGINEERING PROGRESS, 1968, 64 (01) : 85 - &
[4] Robust model predictive control of a pilot plant distillation column
Martin, Paulo A.
Odloak, Darci
Kassab, Fuad
[J]. CONTROL ENGINEERING PRACTICE, 2013, 21 (03) : 231 - 241
[5] ADVANCED MULTIVARIABLE CONTROL OF A PILOT-PLANT DISTILLATION COLUMN
OGUNNAIKE, BA
LEMAIRE, JP
MORARI, M
RAY, WH
[J]. AICHE JOURNAL, 1983, 29 (04) : 632 - 640
[6] A novel control methodology for a pilot plant azeotropic distillation column
Rueda, Lina M.
Edgar, Thomas F.
Eldridge, Robert B.
[J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2006, 45 (25) : 8361 - 8372
[7] NEARLY OPTIMAL CONTROL OF A PILOT-PLANT DISTILLATION COLUMN
MERLUZZI, P
BROSILOW, CB
[J]. AICHE JOURNAL, 1972, 18 (04) : 739 - &
[8] Tray efficiency alcohol distillation column
Muntean, M
Naghiu, A
[J]. Bulletin of the University of Agricultural Sciences and Veterinary Medicine, Vol 59: AGRICULTURE, 2003, 59 : 212 - 214
[9] Dynamic Simulation of a Tray Distillation Column
Yamal, Evelyn t
Martinez, Olga
[J]. INGENIERIA UC, 2009, 16 (01): : 65 - 70
[10] TRAY EFFICIENCY OF COLUMN IN MULTICOMPONENT DISTILLATION
KAFAROV, VV
BOYARINO.AI
VETOKHIN, VN
[J]. DOKLADY AKADEMII NAUK SSSR, 1972, 202 (05): : 1143 - &

← 1 2 3 4 5 →