Skip to main content

DESIGN OF PI CONTROLLER WITH INPUT CONSTRAINT: APPLICATION ON BLENDING PROCESS

Buy Article:

$51.00 plus tax (Refund Policy)

Abstract:

ABSTRACT

Because of their simplicity, reliability and effectiveness, proportional–integral–derivative (PID) controllers remain the most widely used controllers in the process industries. Actuator saturation is among the most common and significant problem in control systems design. Normal PID controller does not take this into consideration. Normally, an anti-windup compensator is employed in the system to overcome the problem. In this contribution, a new set of controller tuning relations is developed to tune the PI controller when the system is under saturation. The blending process was described as first order plus time delay (FOPTD) process and an expression is developed for saturation level, U as a function of controller gain, Kc with the range of R 0.4–2 (ratio of time delay to time constant). The proposed tuning rule relate the parameters of the controller to the parameters of a FOPTD model of the plant to a step change in the set point. The proposed method was applied to PI controller and tested on the process of blending system of sweetened condensed milk. The performance of the controller with various tuning formulae incorporated with classical anti-windup strategies has been compared. The simulation results showed that the proposed method could give satisfactory performance in controlling the process. PRACTICAL APPLICATIONS

The proposed tuning method can be applied to a proportional–integral (PI) controller and can be tested to any first order plus time delay process, for example, spray-drying process, pasteurization and blending process with or without input saturation. If the final product of the food process is deviated from the set point, it will send a signal to the PI controller tuned by proposed tuning method and the actuator will receive the signal from the PI controller and, finally, the actuator will control the opening of the valve. It can ensure that the controlled variable in the food processes is within the set point and at the same time avoid the input saturation. With this proper control strategy incorporated to any food process, it can ensure the safety of plant and at the same time achieve higher profits.

Document Type: Research Article

DOI: http://dx.doi.org/10.1111/j.1745-4530.2009.00418.x

Affiliations: 1: Department of Process and Food Engineering 2: Department of Chemical and Environmental EngineeringUniversiti Putra Malaysia 43400 SerdangSelangor, Malaysia

Publication date: February 1, 2010

bsc/jfpe/2010/00000033/A00101s1/art00017
dcterms_title,dcterms_description,pub_keyword
6
5
20
40
5

Access Key

Free Content
Free content
New Content
New content
Open Access Content
Open access content
Subscribed Content
Subscribed content
Free Trial Content
Free trial content
Cookie Policy
X
Cookie Policy
ingentaconnect website makes use of cookies so as to keep track of data that you have filled in. I am Happy with this Find out more