eprintid: 632
rev_number: 2
eprint_status: archive
userid: 1
dir: disk0/00/00/06/32
datestamp: 2023-11-09 15:48:46
lastmod: 2023-11-09 15:48:46
status_changed: 2023-11-09 15:22:51
type: article
metadata_visibility: show
creators_name: Minh, V.T.
creators_name: Abdul Rani, A.M.
title: Modeling and control of distillation column in a petroleum process
ispublished: pub
keywords: Adaptive Control; Adaptive controllers; Boil-up rate; Calculation procedure; Initial design; Linear model; Modeling and control; Modeling and simulation; Modeling simulation; Non-linear model; Process dynamics; Reduced order; Reference models; Reflux rate; Three phasis, Adaptive control systems; Computer simulation; Distillation; Distillation columns; Dynamic analysis, Model reference adaptive control
note: cited By 19
abstract: This paper introduces a calculation procedure for modeling and control simulation of a condensate distillation column based on the energy balance (L-V) structure. In this control, the reflux rate L and the boilup rate V are used as the inputs to control the outputs of the purity of the distillate overhead and the impurity of the bottom products. The modeling simulation is important for process dynamic analysis and the plant initial design. In this paper, the modeling and simulation are accomplished over three phases: the basic nonlinear model of the plant, the full-order linearised model, and the reduced-order linear model. The reduced-order linear model is then used as the reference model for a model-reference adaptive control (MRAC) system to verify the applicable ability of a conventional adaptive controller for a distillation column dealing with the disturbance and the model-plant mismatch as the influence of the plant feed disturbances. Copyright © 2009 V. T. Minh and A. M. Abdul Rani.
date: 2009
official_url: https://www.scopus.com/inward/record.uri?eid=2-s2.0-73449140086&doi=10.1155%2f2009%2f404702&partnerID=40&md5=dee294e5a2e5ade91899e7dd3fbb4534
id_number: 10.1155/2009/404702
full_text_status: none
publication: Mathematical Problems in Engineering
volume: 2009
refereed: TRUE
issn: 1024123X
citation:   Minh, V.T. and Abdul Rani, A.M.  (2009) Modeling and control of distillation column in a petroleum process.  Mathematical Problems in Engineering, 2009.   ISSN 1024123X