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Interactive Opportunity Assessment Demo and Seminar (Deminar) Series  for Web Labs – Online Process Control Lab  Access and Use May 27, 2010 Sponsored by Emerson, Experitec, and Mynah Created by Greg McMillan and Jack Ahlers Website - Charlie Schliesser (csdesignco.com)
Welcome ,[object Object],[object Object]
Top Ten Reasons Why an Automation Engineer  Makes a Great Spouse or at Least a Wedding Gift   ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
Top Ten Reasons Why an Automation Engineer  Makes a Great Spouse or at Least a Wedding Gift   ,[object Object]
Today we are on Location of Virtual Plants
Free Access to Virtual Plants
My Planned Uses of Virtual Plants ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],Features of Online Process Control Labs “ Hands-On Learning” Provides the  Best Educational Experience”
click button for each desired lab (concurrent labs are possible) click on arrow  to return to this main lab menu  DeltaV Operate Main Screen Click to restore PID setpoint,  PID mode, PID limits, PID tuning, PID options, process dynamics, measurement dynamics,  disturbance dynamics, and control valve dynamics
performance metrics are generated in Run mode click to select mode click to get PID faceplate click to get trend chart click to enter time for Test and Run modes (load upsets occur in Test and Run modes) click any block in block diagram to get access to data entry screen for PID options and run conditions (process, measurement, upset, and valve details)
Secondary (inner loop) PID’s setpoint is primary (outer loop) PID’s output AC1- 1  is  primary  PID and AC1- 2  is  secondary  PID
Feedforward signal added to PID output use a measurement of the disturbance AC1- 1  is  primary  PID and AC1- 2  is  secondary  PID
University of Texas Unit Operations Lab Reactor Click for Dynamics
See article “Virtual Plant Provides Real Insights” in  Chemical Processing, http://www.chemicalprocessing.com/articles/2008/255.html   Click for Dynamics
click on open folder to select your lab trend chart if your lab trend chart is not already open
configured upsets occur in Run and Test modes performance metrics are computed in Run mode click on value to get data entry screen with pull down menu for mode
click on value to get data entry screen to enter new value (pull down menu for PID structure has 8 choices)
click on value to get data entry screen to enter new value  (process dynamics can only be changed in Explore mode) primary process and secondary process Lag2 has values for PV increasing  and PV decreasing (the minimum Lag2 for process simulator stability is 1 sec) for an integrating process type, the integrating process gain is the  process gain multiplied by factor divided by Lag2 (units of 1/sec) create nonlinear gain by clicking on factor values and entering multiplier of primary process gain  Lag2 must be largest time  constant in primary process Lag2 must be largest time  constant in secondary process
click on value to get data entry screen to enter new value refresh time is time between communications to PID (periodic reporting) sensitivity is minimum change in measurement for communication (exception reporting) Feedforward Gain and “Dynamic Compensation”  (Lead-Lag) are accessible in  Feedforward  Loop Lab 03
click on value to get data entry screen to enter new value configured upsets do not occur in Explore mode
click on value to get data entry screen to enter new value create nonlinear valve by clicking on %Flow values and entering % of max flow  “ Valve Step %” is step size of stair-case response  (valve’s resolution limit) “ Valve L/L Lag” is Lag time of Lead/Lag &  “ Valve L/L Lead” is Lead time of Lead/Lag applied to valve signal to kick actuator thru deadband (backlash) and stick-slip (stiction) permissible value  range is 0 – 100 negative number
Click on magnifying glass to get detail view of limits and tuning Click on Duncan to get DeltaV Insight for “On-Demand” and “Adaptive” tuning
“ On-Demand Tuning” automatically identifies dynamics from relay oscillation introduced click on PID tag and then Tune
“ Adaptive Tuning” automatically identifies dynamics from setpoint or manual output change or injected pulse (For More Info See Emerson Exchange 2009 Presentation on DeltaV Insight for Loop Monitoring and Tuning) click on PID tag and then Tune
Online Process Control Lab Access ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
Help Us Improve These Deminars! WouldYouRecommend.Us/105679s21/
Join Us June 9, Wednesday  10:00 am  CDT ,[object Object],[object Object],[object Object],[object Object]
QUESTIONS?

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On-line Process Control Lab Access and Use Deminar

  • 1. Interactive Opportunity Assessment Demo and Seminar (Deminar) Series for Web Labs – Online Process Control Lab Access and Use May 27, 2010 Sponsored by Emerson, Experitec, and Mynah Created by Greg McMillan and Jack Ahlers Website - Charlie Schliesser (csdesignco.com)
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  • 5. Today we are on Location of Virtual Plants
  • 6. Free Access to Virtual Plants
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  • 9. click button for each desired lab (concurrent labs are possible) click on arrow to return to this main lab menu DeltaV Operate Main Screen Click to restore PID setpoint, PID mode, PID limits, PID tuning, PID options, process dynamics, measurement dynamics, disturbance dynamics, and control valve dynamics
  • 10. performance metrics are generated in Run mode click to select mode click to get PID faceplate click to get trend chart click to enter time for Test and Run modes (load upsets occur in Test and Run modes) click any block in block diagram to get access to data entry screen for PID options and run conditions (process, measurement, upset, and valve details)
  • 11. Secondary (inner loop) PID’s setpoint is primary (outer loop) PID’s output AC1- 1 is primary PID and AC1- 2 is secondary PID
  • 12. Feedforward signal added to PID output use a measurement of the disturbance AC1- 1 is primary PID and AC1- 2 is secondary PID
  • 13. University of Texas Unit Operations Lab Reactor Click for Dynamics
  • 14. See article “Virtual Plant Provides Real Insights” in Chemical Processing, http://www.chemicalprocessing.com/articles/2008/255.html Click for Dynamics
  • 15. click on open folder to select your lab trend chart if your lab trend chart is not already open
  • 16. configured upsets occur in Run and Test modes performance metrics are computed in Run mode click on value to get data entry screen with pull down menu for mode
  • 17. click on value to get data entry screen to enter new value (pull down menu for PID structure has 8 choices)
  • 18. click on value to get data entry screen to enter new value (process dynamics can only be changed in Explore mode) primary process and secondary process Lag2 has values for PV increasing and PV decreasing (the minimum Lag2 for process simulator stability is 1 sec) for an integrating process type, the integrating process gain is the process gain multiplied by factor divided by Lag2 (units of 1/sec) create nonlinear gain by clicking on factor values and entering multiplier of primary process gain Lag2 must be largest time constant in primary process Lag2 must be largest time constant in secondary process
  • 19. click on value to get data entry screen to enter new value refresh time is time between communications to PID (periodic reporting) sensitivity is minimum change in measurement for communication (exception reporting) Feedforward Gain and “Dynamic Compensation” (Lead-Lag) are accessible in Feedforward Loop Lab 03
  • 20. click on value to get data entry screen to enter new value configured upsets do not occur in Explore mode
  • 21. click on value to get data entry screen to enter new value create nonlinear valve by clicking on %Flow values and entering % of max flow “ Valve Step %” is step size of stair-case response (valve’s resolution limit) “ Valve L/L Lag” is Lag time of Lead/Lag & “ Valve L/L Lead” is Lead time of Lead/Lag applied to valve signal to kick actuator thru deadband (backlash) and stick-slip (stiction) permissible value range is 0 – 100 negative number
  • 22. Click on magnifying glass to get detail view of limits and tuning Click on Duncan to get DeltaV Insight for “On-Demand” and “Adaptive” tuning
  • 23. “ On-Demand Tuning” automatically identifies dynamics from relay oscillation introduced click on PID tag and then Tune
  • 24. “ Adaptive Tuning” automatically identifies dynamics from setpoint or manual output change or injected pulse (For More Info See Emerson Exchange 2009 Presentation on DeltaV Insight for Loop Monitoring and Tuning) click on PID tag and then Tune
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  • 26. Help Us Improve These Deminars! WouldYouRecommend.Us/105679s21/
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