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
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
收藏
相关论文
共 50 条
  • [21] Implementation of a Reactive Dividing Wall Distillation Column in a Pilot Plant
    Sandoval-Vergara, Rodrigo
    Omar Barroso-Munoz, Fabricio
    Hernandez-Escoto, Hector
    Gabriel Segovia-Hernandez, Juan
    Hernandez, Salvador
    Rico-Ramirez, Vicente
    18TH EUROPEAN SYMPOSIUM ON COMPUTER AIDED PROCESS ENGINEERING, 2008, 25 : 229 - 234
  • [22] MIMO Neural Network Model for Pilot Plant Distillation Column
    Abdullah, Z.
    Ahmad, Z.
    Aziz, N.
    10TH INTERNATIONAL SYMPOSIUM ON PROCESS SYSTEMS ENGINEERING, 2009, 27 : 531 - 536
  • [23] Controller Design and Implementation for a Pilot Plant Binary Distillation Column
    Bhat, Vinayambika S.
    Thirunavukkarasu, I.
    George, V. I.
    Sreelatha, C.
    PROCEEDINGS OF 2018 IEEE DISTRIBUTED COMPUTING, VLSI, ELECTRICAL CIRCUITS AND ROBOTICS (DISCOVER), 2018, : 71 - 75
  • [24] Performance Enhancement of Binary Batch Distillation Column Pilot Plant
    Kale, Shashikant R.
    Agashe, Sudhir D.
    2014 INTERNATIONAL CONFERENCE ON CONTROL, INSTRUMENTATION, COMMUNICATION AND COMPUTATIONAL TECHNOLOGIES (ICCICCT), 2014, : 344 - 348
  • [25] EFFECT OF VAPOR MIXING ON TRAY EFFICIENCY OF DISTILLATION COLUMN
    KATAYAMA, H
    IMOTO, T
    NIPPON KAGAKU KAISHI, 1972, 8 (09) : 1745 - &
  • [26] Mass transfer in ternary distillation with sieve tray column
    Mortaheb, HR
    Iimuro, Y
    Kosuge, H
    Asano, K
    JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 2000, 33 (04) : 597 - 604
  • [27] Modeling and control of a temperature-based high-purity distillation column
    Chien, IL
    Ogunnaike, BA
    CHEMICAL ENGINEERING COMMUNICATIONS, 1997, 158 : 71 - 105
  • [28] DISTILLATION COLUMN CONTROL
    MCNEAIR, SJ
    AUSTRALIAN JOURNAL OF INSTRUMENTATION & CONTROL, 1976, 32 (06): : 127 - 132
  • [29] Distillation column control
    Henry, RM
    Mujtaba, IM
    APPLICATION OF MULTI-VARIABLE SYSTEM TECHNIQUES (AMST '98), 1998, : 65 - 73
  • [30] Distillation column control
    Morrison, T
    CHEMICAL ENGINEERING PROGRESS, 1999, 95 (02) : 7 - +