A Novel Proportional−Integral-Derivative Control Configuration with Application to the Control of Batch Distillation-Reference-Cited by-同舟云学术

A Novel Proportional−Integral-Derivative Control Configuration with Application to the Control of Batch Distillation

Published:1999-12-16 Issue:2 Volume:39 Page:432-440
ISSN:0888-5885
Container-title:Industrial & Engineering Chemistry Research
language:en
Short-container-title:Ind. Eng. Chem. Res.

Author:

Alvarez-Ramirez Jose¹,Monroy-Loperena Rosendo¹,Cervantes Ilse¹,Morales America¹

Affiliation:

1. División de Ciencias Básicas e Ingeniería, Universidad Autonoma MetropolitanaIztapalapa, Apartado Postal 55-534, México D.F., 09340 México, Estrategia Sinérgica, S.A. de C.V., Paseo de los Pirules 124, Col. Paseos de Taxqueña, México D.F., 04250 México, and Escuela Superior de Ingeniería Mecánica y Eléctrica, SEPI, Avenida Santa Ana 1000, Col. San Francisco Culhuacan, México D.F., 04430 México

Publisher

American Chemical Society (ACS)

Subject

Industrial and Manufacturing Engineering,General Chemical Engineering,General Chemistry

Link

https://pubs.acs.org/doi/pdf/10.1021/ie990287c

Reference16 articles.

1. Simple PI and PID tuning for open-loop unstable systems

2. Design of pole placing controllers for stable and unstable systems with pure time delay

3. A modified Smith predictor and controller for unstable processes with time delay

4. A new Smith predictor for controlling a process with an integrator and long dead-time

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