Av Finn Aakre Haugen (finn.haugen@usn.no) IA3112 Automatiseringsteknikk og EK3114 Automatisering og vannkraftregulering Høstsemesteret 2017 Gain scheduling.

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Presentation transcript:

Av Finn Aakre Haugen (finn.haugen@usn.no) IA3112 Automatiseringsteknikk og EK3114 Automatisering og vannkraftregulering Høstsemesteret 2017 Gain scheduling Av Finn Aakre Haugen (finn.haugen@usn.no) Aut.tek. 2017. HSN/F. Haugen

Conservative tuning (good stability, but sluggish control) 2 Problem: Assume that the dynamic properties of the process to be controlled vary with the operating point. With fixed PID settings, the control system may get poor stability, or become sluggish Solutions: Conservative tuning (good stability, but sluggish control) Adaptive tuning (optimal settings all the time, i.e. the control system gets good stability and fast control): Model-based PID parameter adjustment Gain scheduling based on experiments Here, we concentrate on Gain scheduling. Aut.tek. 2017. HSN/F. Haugen

Control system with controller parameter 3 Control system with controller parameter updating using Gain scheduling: Aut.tek. 2017. HSN/F. Haugen

= Table of sets (here 3) of PID parameter values: 4 Gain schedule = Table of sets (here 3) of PID parameter values: PID set 1 PID set 2 PID set 3 Aut.tek. 2017. HSN/F. Haugen

How to interpolate between the tabular values of 5 How to interpolate between the tabular values of controller parameters and GS variable? Let's focus on controller gain Kp (the same principles apply to Ti and Td as well). PID set 1 PID set 2 PID set 3 Aut.tek. 2017. HSN/F. Haugen

How to interpolate between the tabular values of 6 How to interpolate between the tabular values of controller parameters and GS variable? Aut.tek. 2017. HSN/F. Haugen

An example: Temperature control system 7 An example: Temperature control system where process dynamics varies with flow Aut.tek. 2017. HSN/F. Haugen

In the example: How do process parameters depend on flow? 8 In the example: How do process parameters depend on flow? Responses in temperature after 10% step in control signal to heater: Large flow (24 kg/min) Small flow (12 kg/min) Process gain Inverse of flow ~ Time constant Inverse of flow ~ Time delay Inverse of flow ~ Aut.tek. 2017. HSN/F. Haugen

Observations (from previous slide): Process gain Inverse of flow ~ Time constant Inverse of flow ~ Time delay Inverse of flow ~ Implication: When PID controller has fixed parameters: If flow is reduced, the stability of the control loop is reduced. How to maintain stability and speed of the control system despite flow variations? By adjusting the controller parameters based on flow measurement! So, flow is selected as GS variable. Aut.tek. 2017. HSN/F. Haugen

Simulator: Gain scheduling 10 Simulator: Gain scheduling Aut.tek. 2017. HSN/F. Haugen