Nonlinear PI Control for High Purity Distillation Column

碩士 === 國立臺灣大學 === 化學工程學研究所 === 87 === High-purity distillation columns are very important unit operations in petrochemical industry. In addition to the process interaction problems and possible operating constraints, these columns exhibit very strong asymmetric nonli...

Full description

Bibliographic Details
Main Authors: Lin, Jyh-Ming, 林志銘
Other Authors: Huang, Hsaio-Ping
Format: Others
Language:zh-TW
Published: 1999
Online Access:http://ndltd.ncl.edu.tw/handle/56515630932841410054
id ndltd-TW-087NTU00063033
record_format oai_dc
spelling ndltd-TW-087NTU000630332016-02-01T04:12:24Z http://ndltd.ncl.edu.tw/handle/56515630932841410054 Nonlinear PI Control for High Purity Distillation Column 非線性PI控制在高純度蒸餾塔之應用 Lin, Jyh-Ming 林志銘 碩士 國立臺灣大學 化學工程學研究所 87 High-purity distillation columns are very important unit operations in petrochemical industry. In addition to the process interaction problems and possible operating constraints, these columns exhibit very strong asymmetric nonlinear behavior, and tend to be very ill-conditioned too. Also, for most industrial columns, composition measurements are rarely available on-line; control is therefore often based on temperature measurements. When only one-point temperature control is implented, the control is relatively simple. In order to save energy consumption while tightly control product qualities of the top and the bottom streams, two-point temperature control strategy is necessary. Two-point temperature control of high-purity distillation column is an important challenging problem in petrochemical industry because of the particular difficult dynamic characteristics associated with the high-purity columns. Two-loop PID control because of its single-loop control nature and also because it is a linear controller, the closed-loop control performance is limited. In order to improve control, advance control of high-purity distillation column is advocated. This research utilizes a simple empirical nonlinear dynamic model form especially suited for high-purity column characteristics. A nonlinear PID control algorithm is proposed based on this nonlinear empirical model. In this nonlinear PID controllers, the controller gain and also the reset time will vary in response to the operating condition changes. Closed-loop results for a methanol-ethanol column and a debutanizer show superior control performance of this nonlinear PID controller. This nonlinear PID control method is very easy to implement, thus should have very good potential to be widely applicable in high-purity columns. Huang, Hsaio-Ping 黃孝平 1999 學位論文 ; thesis 133 zh-TW
collection NDLTD
language zh-TW
format Others
sources NDLTD
description 碩士 === 國立臺灣大學 === 化學工程學研究所 === 87 === High-purity distillation columns are very important unit operations in petrochemical industry. In addition to the process interaction problems and possible operating constraints, these columns exhibit very strong asymmetric nonlinear behavior, and tend to be very ill-conditioned too. Also, for most industrial columns, composition measurements are rarely available on-line; control is therefore often based on temperature measurements. When only one-point temperature control is implented, the control is relatively simple. In order to save energy consumption while tightly control product qualities of the top and the bottom streams, two-point temperature control strategy is necessary. Two-point temperature control of high-purity distillation column is an important challenging problem in petrochemical industry because of the particular difficult dynamic characteristics associated with the high-purity columns. Two-loop PID control because of its single-loop control nature and also because it is a linear controller, the closed-loop control performance is limited. In order to improve control, advance control of high-purity distillation column is advocated. This research utilizes a simple empirical nonlinear dynamic model form especially suited for high-purity column characteristics. A nonlinear PID control algorithm is proposed based on this nonlinear empirical model. In this nonlinear PID controllers, the controller gain and also the reset time will vary in response to the operating condition changes. Closed-loop results for a methanol-ethanol column and a debutanizer show superior control performance of this nonlinear PID controller. This nonlinear PID control method is very easy to implement, thus should have very good potential to be widely applicable in high-purity columns.
author2 Huang, Hsaio-Ping
author_facet Huang, Hsaio-Ping
Lin, Jyh-Ming
林志銘
author Lin, Jyh-Ming
林志銘
spellingShingle Lin, Jyh-Ming
林志銘
Nonlinear PI Control for High Purity Distillation Column
author_sort Lin, Jyh-Ming
title Nonlinear PI Control for High Purity Distillation Column
title_short Nonlinear PI Control for High Purity Distillation Column
title_full Nonlinear PI Control for High Purity Distillation Column
title_fullStr Nonlinear PI Control for High Purity Distillation Column
title_full_unstemmed Nonlinear PI Control for High Purity Distillation Column
title_sort nonlinear pi control for high purity distillation column
publishDate 1999
url http://ndltd.ncl.edu.tw/handle/56515630932841410054
work_keys_str_mv AT linjyhming nonlinearpicontrolforhighpuritydistillationcolumn
AT línzhìmíng nonlinearpicontrolforhighpuritydistillationcolumn
AT linjyhming fēixiànxìngpikòngzhìzàigāochúndùzhēngliùtǎzhīyīngyòng
AT línzhìmíng fēixiànxìngpikòngzhìzàigāochúndùzhēngliùtǎzhīyīngyòng
_version_ 1718173927256096768