Weeks 1&2 Flashcards

(51 cards)

1
Q

Objectives of control

A
  • Maintain the process at desired operational state
  • Safely transition the process between operational states
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2
Q

Measured parameter of interest that we want to control

A

Output

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3
Q

Parameters which may or may not be manipulated to affect this outcome

A

Inputs

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4
Q

Affect the outcome but cannot be manipulated. Inputs that cannot be controlled by an operator or control system

A

Disturbances

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5
Q

Produces a measured value for use in control system

A

Measurement device

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6
Q

Sends a signal to the final control element to maintain tank level by adjusting supply flowrate based on the error ε

A

Controller

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7
Q

Unpredictable changes in the process

A

Load changes

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8
Q

Value at which it is desired to
maintain the controlled variable

A

Set point

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9
Q

Error

A

Set point - Measured Value

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10
Q

Variable which is changed to control the controlled variable. Must be able to be changed by operator/control system and can be readily and directly manipulated,

A

Manipulated Variable

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11
Q

The condition of a system is monitored by a sensor, which provides
this information to the controller
2. The comparator in the controller determines the value of the error
signal (difference between actual and target value)
3. Based on the value of the error signal, the controller transmits a
signal to the final control element to change the value of the
manipulated variable
* The sensor, whose signal is fed into the control system to complete
the feedback loop, continually monitors the new value, of the
controlled variable
* In this way the control system acts continuously, to maintain the
controlled variable within acceptable limits of its set point

A

Closed Loop Control

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12
Q

Stop a process in an emergency

A

Safety Instrumented systems (SIS)

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13
Q

Economics: maintain optimum output
Product Specs: maintain product ‘on spec’
Environment : maintain effluent/atmospheric releases within allowable levels
Safety: Maintain equipment within operating specs, prevent hazardous situations

A

Motivations of control

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14
Q

Require continuous monitoring and control actions

A

Continuous processes

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15
Q

Cheaper and simpler than a controller - used for instructions like “start” and “stop”

A

Switch

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16
Q

Practical approach to problem solving that may not necessarily provide an optimum solution
Typically easier and more direct that other approaches

A

Heuristic Approach

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17
Q

1) Identify obvious control loops (e.g. level, flow, pressure, temperature)
2) Identify process variables that affect product quality and production spec.
3) Provide additional loops required for safe operation
4) Provide monitoring equipment
5) Provide sample points as necessary
6) Provide recorders if necessary
7) Provide interlocks and alarms

A

Heuristic Approach

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18
Q

Input variable that can affect the performance of a system

A

Load Variable

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19
Q

Uses secondary measurements to infer the value of primary variables that are difficult to measure directly e.g. composition

A

Inferential control

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20
Q

Two or more controllers are cascaded to control one or more process variable. Controllers are said to be “in cascade” when the output (OP.1) of the first or primary controller (master) is used to manipulate the set-point (SP.2) of another or secondary controller (slave)

A

Cascade control

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21
Q

More commonly uses switches (on/off) rather than controllers

A

Batch processes

22
Q

Automatically stop the pump when the tank is full.

A

Level Switches

23
Q

Required when basic process safety control system has failed to keep the process in a safe state.

Executes a specific safety-related task in the event of a specific dangerous condition.

A

Safety Instrumented Systems (SIS)

24
Q

Safety instrumented systems process

A
  1. Sensor(s) to detect dangerous condition
  2. Controller (logic solver) to decide when to shut down the process
  3. Final control element(s) to perform shutdown function - isolation valve or override solenoid to force control valve to shutdown state

Use two in series for additional safety
Solenoid and pneumatic actutors to avoid common cause failure

25
Predicative control Useful where final controlled variable cannot be measured Measure process disturbances Knowledge of process is required
Feed forward control
26
Avantage of feed forward control
Control acts as soon as a disturbance occurs - Does not have to wait for variation in output stream - Quickly canvels out the effect of a disturbance
27
Disadvantage of feed forward control
Takes no account of how the overall system reacts (process disturbance) ## Footnote Hence often used together with feedback control
28
Effects of the disturbances on the controlled cariable are used to adjust the manipulated cariable and so correct for the disturbances
Closed loop control/ feedback control
29
Used when it is necessary to keep the flowrate of two streams in the same ratio. ## Footnote A typical ratio system would perform flow measurements on both streams and control only one of them to maintain the ratio
Ratio control
30
Degrees of freedom
Number of independent variables - number of independent equations | DOF = v - n
31
Number of independent variables that must be specified in order to define the process completely.
Degrees of freedom ## Footnote The process can only be controlled when all the degrees of freedom have been specified
32
All quantities in the model that are known constants (or parameters than can be specified) on the basis of known physical properties, equipment dimensions etc.
Independent variables
33
These are based on conservation of mass and energy (overall and for components)
Independent equations
34
Value of the controller output when there is no control action
Bias
35
Proportional control equation
Proportional control = Bias + (controller gain * error) ## Footnote J = J0 + KcE
36
Offset
37
Ratio of change of the output variable (responding variable) to the change of the input varian;e
Gain
38
________ gain means a relatively small error signal can drive the final control element to the ends of its range
High ## Footnote The process acts very like an ON/OFF controller
39
________ gain means an error signal may only produce a slight adjustment to the final control element
Low ## Footnote Too low gain means the process takes a long time to get near the set point. Final control element may not be using full range.
40
Proportional-Integral Control
J = J0 + Kc ( ε + (1/τ1) ∫ ε dt)
41
Used to elimate offset by measuring the average error over time
Proportional Integral (PI)
42
Proportional-Derivative Control (PD)
𝐽 = 𝐽0 + 𝐾𝐶𝜀 +𝐾𝐷 𝑑𝜀/𝑑𝑡 | KD = Derivative gain
43
Derivative action provides a signal proportional to the rate of the change in error
Proportional Derivative | When a controlled variable is steady, the derivative component is zero W
44
Acts against overshoots and oscillation
Proportional Derivative ## Footnote Acts against rapid changes in error: quicker changes = bigger action
44
Derivative action allows a ____ proportional gain to be used
higher ## Footnote Due to damping effect
45
Needed to elimate offset
Integral
46
Compromise between Proportional Integral and Proportional Derivative
Proportional Derivative Control (PID) ## Footnote Fast response, no offset, little oscillation
47
Empirically selecting the right controller settings
Control Loop Tuning
48
Ziegler Nichols method for controller tuning
1. Bring the system to the desired operational level 2. Using proportional control only, introduce a set-point change and vary gain, Kc , until the system starts to oscillate continuously 3. Define ultimate gain - KU and period of oscillation - PU then use them to generate your settings based on ZN recommendations
49
An experimental method for determining the settings for your control system
Ziegler Nichols method for controller tuning
50