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Instrumentation & Control

Integral (Reset) Windup, Jacketing Logic and the Velocity PI Form. A valve cannot open more than all the way. A pump cannot go slower than stopped. Yet an improperly programmed control algorithm can issue such commands. To increase our comfort level with the idea that different vendors cast the same PI algorithm in different forms, we choose the independent, continuous, position PI form for this discussion:. CO = controller output signal (the wire out). CObias = controller bias or null value. Our previou...

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Integral (Reset) Windup, Jacketing Logic and the Velocity PI Form. A valve cannot open more than all the way. A pump cannot go slower than stopped. Yet an improperly programmed control algorithm can issue such commands. To increase our comfort level with the idea that different vendors cast the same PI algorithm in different forms, we choose the independent, continuous, position PI form for this discussion:. CO = controller output signal (the wire out). CObias = controller bias or null value. Our previou...
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Instrumentation & Control | hsconntrol.blogspot.com Reviews

https://hsconntrol.blogspot.com

Integral (Reset) Windup, Jacketing Logic and the Velocity PI Form. A valve cannot open more than all the way. A pump cannot go slower than stopped. Yet an improperly programmed control algorithm can issue such commands. To increase our comfort level with the idea that different vendors cast the same PI algorithm in different forms, we choose the independent, continuous, position PI form for this discussion:. CO = controller output signal (the wire out). CObias = controller bias or null value. Our previou...

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1

Instrumentation & Control: March 2011

http://hsconntrol.blogspot.com/2011_03_01_archive.html

Integral (Reset) Windup, Jacketing Logic and the Velocity PI Form. A valve cannot open more than all the way. A pump cannot go slower than stopped. Yet an improperly programmed control algorithm can issue such commands. To increase our comfort level with the idea that different vendors cast the same PI algorithm in different forms, we choose the independent, continuous, position PI form for this discussion:. CO = controller output signal (the wire out). CObias = controller bias or null value. Our previou...

2

Instrumentation & Control: Sample Time Impacts Controller Performance

http://hsconntrol.blogspot.com/2011/03/sample-time-impacts-controller.html

Sample Time Impacts Controller Performance. There are two sample times, T, used in process controller design and tuning. One is the control loop sample time that specifies how often the controller samples the measured process variable (PV) and then computes and transmits a new controller output (CO) signal. The other is the rate at which CO and PV data are sampled and recorded during a bump test of our process. Bump test data is used to design and tune our controller prior to implementation. Did I just a...

3

Instrumentation & Control: PI Disturbance Rejection in the Jacketed Stirred Reactor

http://hsconntrol.blogspot.com/2011/03/pi-disturbance-rejection-in-jacketed.html

PI Disturbance Rejection in the Jacketed Stirred Reactor. PI Disturbance Rejection in the Jacketed Stirred Reactor. The control objective for the jacketed reactor is to minimize the impact on reactor operation when the temperature of the liquid entering the cooling jacket changes (detailed discussion here). As a base case study, we establish here the performance capabilities of a PI controller in achieving this objective. Signal to valve that adjusts cooling jacket liquid flow rate (controller output, %).

4

Instrumentation & Control: P-Only Disturbance Rejection of the Gravity Drained Tanks

http://hsconntrol.blogspot.com/2011/03/p-only-disturbance-rejection-of-gravity.html

P-Only Disturbance Rejection of the Gravity Drained Tanks. In a previous article, we looked at the structure of the P-Only algorithm and we considered some design issues associated with implementation. We also studied the set point tracking (or servo) performance of this simple controller for the heat exchanger process. Gravity Drained Tanks Process. A graphic of the gravity drained tanks process is shown below :. Step 1: Determine the Design Level of Operation (DLO). Our primary objective is to reject d...

5

Instrumentation & Control

http://hsconntrol.blogspot.com/2011/03/p-only-control-algorithm-simplest.html

The P-Only Control Algorithm. The simplest algorithm in the PID family is a proportional or P-Only controller. Like all automatic controllers, it repeats a measurement-computation-action procedure at every loop sample time, T, following the logic flow shown in the block diagram below (click for large view):. Starting at the far right of the control loop block diagram above:. A sensor measures and transmits the current value of the process variable, PV, back to the controller (the 'controller wire in').

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Instrumentation & Control

Integral (Reset) Windup, Jacketing Logic and the Velocity PI Form. A valve cannot open more than all the way. A pump cannot go slower than stopped. Yet an improperly programmed control algorithm can issue such commands. To increase our comfort level with the idea that different vendors cast the same PI algorithm in different forms, we choose the independent, continuous, position PI form for this discussion:. CO = controller output signal (the wire out). CObias = controller bias or null value. Our previou...

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