/
1 CBE 1 CBE

1 CBE - PowerPoint Presentation

natalia-silvester
natalia-silvester . @natalia-silvester
Follow
368 views
Uploaded On 2017-01-12

1 CBE - PPT Presentation

MET 433 14 Mar 12 Model of Stirred Tank Heater Goal set up models to simulate and see effect of tuning parameters 1 st principles Chaps 3 6 transfer functions just looked at this a bit ID: 509077

stirred tank polymath heater tank stirred heater polymath taui step response cbe controller class transfer change set models model

Share:

Link:

Embed:

Download Presentation from below link

Download Presentation The PPT/PDF document "1 CBE" is the property of its rightful owner. Permission is granted to download and print the materials on this web site for personal, non-commercial use only, and to display it on your personal computer provided you do not modify the materials and that you retain all copyright notices contained in the materials. By downloading content from our website, you accept the terms of this agreement.


Presentation Transcript

Slide1

1

CBE

/ MET 433

14 Mar 12Model of Stirred Tank Heater

Goal: set up models to simulate and see effect of tuning parameters

1

st

principles (Chaps 3 – 6);

transfer functions (just looked at this a bit)

process simulators (

AspenPlus

Dynamics; CBE 450/550 class)Slide2

2

+

+

-

+

energy balance on tank w/o controlStirred Tank Heater (w/ PI Controller)

PI controller equationSlide3

3

Let:

Stirred Tank Heater (w/ PI Controller)Slide4

4

ODE Solver (POLYMATH; MATLAB; MATHCAD;

etc)

Polymath code:

step= if (t<1) then (0) else (1)Ti = 0 + step * 10Slide5

5

ODE Solver: POLYMATH

Polymath code (stirred tank heater):d(C) / d(t) = -1/tau*C + KT/tau*Ti + K1KT/tau*M

C(0) = 0d(errsum) / d(t) = R – Cerrsum(0) = 0tau = 5 # min

KT = 0.5 # %TO/degCK1KT = 0.8 # %TO/%COR = 0 # set point stays sameM = Kc*(R-C) + Kc/tauI*errsumstep = if (t<1) then (0) else (1)Ti = 0 + step * 10 # step change disturbanceKc = 1.3 # %CO/%TOtauI = 10 # mint(0) = 0t(f) = 100 # minIn Class Demo / Exercise:Polymath DemonstrationBuild model in Polymath (ODE solver)Solve; graph C vs tExplore:Try P-only controllerAdjust Kc and tauI to get QADTry different Kc/tauI setsCan you get underdamped response?What is response to step change in R(t); holding Ti at the SS value?Slide6

6

CBE

/ MET 433

Model of Stirred Tank Heater

Goal: set up models to simulate and see effect of tuning parameters

1

st

principles (Chaps 3 – 6);

transfer functions (just looked at this a bit)

process simulators (

AspenPlus

Dynamics; CBE 450/550 class)Slide7

7

+

+

-

+Stirred Tank Heater (transfer function simulator)

Transfer function simulator: Loop Pro Developer (Control Station) In Class Demo / Exercise:Build model in Loop Pro Developer (Custom Process)Turn on PI Controller and set Kc and tauIExplore:Change load (Ti) up by 10 to 60%; observe system responseChange back to 50%; observe responseTry P-only controllerAdjust Kc and tauI to get QADTry different Kc/tauI settingsCan you get underdamped response?What is response to step change in R(t) to 60%?Slide8

8

CBE

/ MET 433

Model of Stirred Tank Heater

Goal: set up models to simulate and see effect of tuning parameters

1

st

principles (Chaps 3 – 6);

transfer functions (just looked at this a bit)process simulators

(

AspenPlus

Dynamics; CBE 450/550 class)Slide9

9

SAVE your Polymath and Loop Pro Developer Models !!

Related Contents


Next Show more