Journals / Turkish Journal of Engineering and Environmental Sciences / 1998 / Cilt: 22 - Sayı: 1

Self-Tuning and Conventional Control of an Industrial Scale Packed Distillation Column

Pages
1–8
DOI
—
🏛️Bibliographic metadata and full text access for this article are provided via DergiPark.
DergiPark Record ↗
✨

AI Summary & Key Takeaways

AI Insight
⚡ TL;DR(Too Long; Didn't Read)

The success of the various control actions are estimated using an integral square of the error (ISE) criterion and it is shown that self-tuning PID control provides better control than conventional PID action for the cases stud-ied.

📌 3 Key Takeaways

🎯
Objective & Hypothesis:The performance of self-tuning and a variety of conventional control strategies are examined when applied to the over-head product composition control of a packed distillation column.
📊
Key Findings & Data:These control strategies are tested under various sets of condi-tions on a packed distillation column situated B.P.
💡
Conclusion & Impact:The success of the various control actions are estimated using an integral square of the error (ISE) criterion and it is shown that self-tuning PID control provides better control than conventional PID action for the cases stud-ied.
🔬Design:Research Article
📍Scope:Comprehensive Sample
⚙️Variables:Self-Tuning Control · Conventional Control · Packed Distillation Column

Abstract

The performance of self-tuning and a variety of conventional control strategies are examined when applied to the over-head product composition control of a packed distillation column. These control strategies are tested under various sets of condi-tions on a packed distillation column situated B.P. Chemicals, South Wales, U.K. Conventional PID control action is employed throughout-being considered the most likely type of control action for this application. The controller parameters were estimated using three different closed loop response tuning criteria for discrete controllers, viz. those due to Yuwana and Seborg (YS), Jutan and Rodriguez (YS-JR) and Wardle and Heathcock (YS-WH). An additional criterion (YS-JR-decrease gain) is proposed in the present work and is found to give better control than YS-JR method in a number of cases. The best conventional PID action is com-pared with self-tuning PID control. The success of the various control actions are estimated using an integral square of the error (ISE) criterion and it is shown that self-tuning PID control provides better control than conventional PID action for the cases stud-ied.

Özet

The performance of self-tuning and a variety of conventional control strategies are examined when applied to the over-head product composition control of a packed distillation column. These control strategies are tested under various sets of condi-tions on a packed distillation column situated B.P. Chemicals, South Wales, U.K. Conventional PID control action is employed throughout-being considered the most likely type of control action for this application. The controller parameters were estimated using three different closed loop response tuning criteria for discrete controllers, viz. those due to Yuwana and Seborg (YS), Jutan and Rodriguez (YS-JR) and Wardle and Heathcock (YS-WH). An additional criterion (YS-JR-decrease gain) is proposed in the present work and is found to give better control than YS-JR method in a number of cases. The best conventional PID action is com-pared with self-tuning PID control. The success of the various control actions are estimated using an integral square of the error (ISE) criterion and it is shown that self-tuning PID control provides better control than conventional PID action for the cases stud-ied.

🔖

Cite This Article

HAPOĞLU, H., BALAS, C. E., WARDLE, A. P. (1998). Self-Tuning and Conventional Control of an Industrial Scale Packed Distillation Column. Turkish Journal of Engineering and Environmental Sciences, Cilt: 22 - Sayı: 1, 1–8. https://ajindex.com/articles/369415

📄 Full Text PDF Viewer

📄

PDF görüntüleyici hazırlanıyor...