Control Loops Flashcards

1
Q

What is the software of a control loop? (4)

A
  1. setpoint
  2. manipulated variable
  3. disturbance variable
  4. controlled variable
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2
Q

What is the setpoint?

A

The setpoint is the predetermined desired value for the controlled variable. The aim of the control loop is to ensure that the controlled variable remains at the setpoint

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3
Q

What is the manipulated variable?

A

The manipulated variable has a direct influence on the controlled variable. By varying the manipulated variable in response to disturbances, the controlled variable can remain at its setpoint.

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4
Q

What is a disturbance variable?

A

The disturbance variables that varies and pushes the controlled variable from the setpoint.

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5
Q

What is the controlled variable?

A

It is the measured variable. It is the thing that we are trying to maintain at its setpoint.

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6
Q

What is the hardware of a control loop? (3)

A
  1. Sensor
  2. Controller
  3. Control Element
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7
Q

What is the role of the sensor?

A

Measures the system variable and serves as a signal source for the control loop.

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8
Q

What is the role of the controller?

A

To perform the functions of computation and comparison with the setpoint to determine how much action is required.

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9
Q

What is the role of the control element?

A

It is a piece of equipment which exerts a direct influence on the process. It receives the signal from the controller and takes the appropriate action. It is generally a control valve.

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10
Q

What are the characteristics of on-off control?

A

Saw-tooth pattern, cyclic, fluctuates between a maximum and minimum value. Doesn’t reach setpoint.

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11
Q

When is on-off control suitable to be used?

A

For non-critical conditions such as temperature (turning on and off a heater) or level control.

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12
Q

Disadvantages of on-off control.

A

Unsuitable for the control of flow, wear on the final control element if rapid opening and shutting of valve, poor control.
If the deadzone is large then there is not rapid opening and closing but the deviation from the setpoint is large. If the deadzone is small then there is a smaller deviation from setpoint but quick opening and shutting. Neither are desirable

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13
Q

How are the error and the action taken in proportional only control related?

A

The action taken by the control loop is directly proportional to the error in the system.

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14
Q

What are the characteristics of proportional only control?

A

There is an offset, usually oscillations at the beginning. There is an off set due to the equation for proportional only control V = K*epsilon + V0. V0 causes an offset and for the controlled variable to settle at a constant value which is different from the setpoint.

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15
Q

What is the equation for the error?

A

epsilon = SP - PV (setpoint - process variable)

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16
Q

What is the equation for proportional only control?

A

V = K*epsilon + V0
V is the adjustment or signal for adjustment in the control loop
K is the proportional constant or gain of the loop
epsilon is the error
V0 is the signal output with no error

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17
Q

How are K and the proportional band (PB) related?

A

K = 1/PB

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18
Q

What happens if there is large K ( small PB)?

A

Then there is a small offset but oscillatory (unstable) behaviour.

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19
Q

What happens if there is small K ( large PB)?

A

Then there is a large offset but stable behaviour (there are no oscillations)

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20
Q

What are the advantages of the proportional only control?

A

It gives a fast response, and can provide good stability.

21
Q

What are the disadvantages of proportional only control?

A

Offset and overshoot, always has to go past setpoint.

22
Q

What is the relationship between the error and the action taken in integral control?

A

The action taken is always proportional to the integral of the sum of the errors.

23
Q

Why is integral action always used with proportional control?

A

It is too slow a response and the action builds up over time.

24
Q

What is the advantage of using integral action control with proportional control?

A

It eventually removes the offset that is found in proportional only control. This is because the constant is removed and replaced by the integral of the error over time.

25
Q

What is the equation for proportional-integral action control?

A

V = K(epsilon + (1/Ti)*integral of epsilon dt

where Ti is the integral action time

26
Q

What happens if the integral time (Ti) is too small?

A

There is strong integral action and the offset is quickly removed but there is potentially unstable behaviour.

27
Q

What happens if the integral time (Ti) is too large?

A

There is weak integral action control, it takes longer for the offset to be removed but the response is more stable.

28
Q

What is the relationship between derivative action and error.

A

The derivative control action is proportional to the rate of change of the error

29
Q

Disadvantage of derivative only control?

A

There could be a large offset from the setpoint, but as long as there is no change in the behaviour then no action is taken. Derivative control can lead to the amplification of noise.

30
Q

Advantage of using derivative action with proportional-integral action?

A

It removes the overshoot

31
Q

The equation for PID control

A

V = K(epsilon + (1/Ti)integral of epsilon dt + Tdderivative epsilon/dt)

32
Q

When is PID not used?

A

When the measurement is noisy because then this leads to instability.

33
Q

Proportional, Integral, Derivative in terms of time frames

A

Proportional action controls the present
Integral action controls the past
Derivative action controls the future

34
Q

What happens if derivative action time, Td is large?

A

There is vigorous derivative control action but this leads to instability.

35
Q

Briefly describe feedback control

A

The measured variable is the controlled variable. The sensor measures the system variable and transforms it into an electrical signal. The signal is then passed on to the controller. The controller compares to setpoint and determines the action to be taken. The electrical signal is then passed on to the final control element and the appropriate action is taken

36
Q

Advantages of feedback control

A

Little knowledge is required for the process. No model is required for the system, the manipulated variable is adjusted according to the extent of the error. It is entirely empirical, as long as an adjustment is being made in the correct sense then the control system should remove disturbances

37
Q

Disadvantages of feedback control

A
  • The error is required to pass through the system before action is taken
  • Large magnitude disturbances can sometimes not be corrected for - use feedforward control This most commonly occurs because there is not a linear relationship between the disturbance and the controlled variable.
  • Large time delay - then use a cascade control loop. This is especially true when only the feed flow rate can be varied.
38
Q

Briefly describe feedforward control

A

The sensor measures the disturbance which has the most dire effect on the controlled variables. The controller then predicts the effect that this disturbance would have on the controlled variable and computes how much action needs to be taken. The manipulated variable is adjusted accordingly using the final control element.

39
Q

Disadvantages of feedforward control

A

A lot of operator skill is required - there needs to a deep understanding of all the disturbances that have occurred on the process in the past. There is complex computation required, it involves determining exactly how much change is required for specific change in disturbance. There is no monitoring of controlled variable. Assume that all disturbance s are known in advances.

40
Q

Advantages of feedforward control

A

The disturbances have no effect on the overall process.

41
Q

Two causes of disturbances in a feedback control loop.

A
  1. The system has been disturbance

2. The setpoint has been changed. In absence of any external disturbance, a change in setpoint will introduce error.

42
Q

Describe cascade control in terms of the manipulated and measured variables

A

There is one manipulated variable and more than one measured variable.

43
Q

Describe the inner and outer loop of cascade control

A

The outer loop - the input to the controller is the measured value of the variable to be controlled. The setpoint is supplied by the operator. It passes output signal to inner loop.
The inner loop - it measures a second variable whose value affects the controlled variable. (MEASURES A DISTURBANCE) Setpoint is supplied by output from outer loop. Its output signal is supplied to manipulated variable

44
Q

Advantage of using cascade control rather than feedback control

A

It gives a faster response. It is especially if inner loop is much faster than outer loop.

45
Q

Disadvantages of PID control

A

The computation is complex because 3 tuning parameters are required, also it can cause the amplification of noisy signals.

46
Q

Why is the valve always placed downstream of the indicator?

A

Because the valve alters the properties of the stream

47
Q

Why is the valve always downstream from a compressor?

A

Compressors have high energy requirements, making them expensive. It will be most cost effective to place the compressor at the front of the process and then vary the pressure by throttling the output downstream.

48
Q

What is the rise time in proportional control?

A

It is the time taken to go from 10 % to 90% of its steady state value.

49
Q

What is the settling time in proportional control?

A

It is the time taken to reach 95% of its steady state value.