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a) Design a feedfoward controller based on a steady-state analysis (xsp=0.1 mol/m3, ysp=0.08 mol/m3)  b) Design a feedfoward controller based on a dynamic analysis. c) Design a PI feedback controller based on the Direct Synthesis (DS) approach with  ?

a) Design a feedfoward controller based on a steady-state analysis (xsp=0.1 mol/m3, ysp=0.08 mol/m3)  b) Design a feedfoward controller based on a dynamic analysis. c) Design a PI feedback controller based on the Direct Synthesis (DS) approach with  ?

Introductory Circuit Analysis (13th Edition)
Introductory Circuit Analysis (13th Edition)
13th Edition
ISBN:9780133923605
Author:Robert L. Boylestad
Publisher:Robert L. Boylestad
Chapter1: Introduction
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a) Design a feedfoward controller based on a steady-state analysis (xsp=0.1 mol/m3, ysp=0.08 mol/m3) 

b) Design a feedfoward controller based on a dynamic analysis.

c) Design a PI feedback controller based on the Direct Synthesis (DS) approach with  ?cl =20 .

d) Given the controller designed in part c, and setpoint ysp(t)= S(t) , calculate the ISE. 

 

 

Distillate D, y Feed F, z Bottoms В, х Figure 1: Distillation column
Transcribed Image Text:Distillate D, y Feed F, z Bottoms В, х Figure 1: Distillation column
1. The distillation column in Fig. 1 has the following transfer function model: Y'(s) D'(s) 2e-20s Y'(s) 95s +1' F'(s) 0.5e-30s 60s + 1 with Gm = Gy = G; = 1. Note: D is MV and F is DV.
Transcribed Image Text:1. The distillation column in Fig. 1 has the following transfer function model: Y'(s) D'(s) 2e-20s Y'(s) 95s +1' F'(s) 0.5e-30s 60s + 1 with Gm = Gy = G; = 1. Note: D is MV and F is DV.
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