1. CHAPTER 9 Control System Instrumentation
ERT 210/4 Process Control
CHAPTER 9
Control System Instrumentation
Hairul Nazirah bt Abdul Halim
Office:

2. Subtopic
Transducer (Sensor & Transmitter)
Final Control Element – Control valve

3. Control System Instrumentation
Transducers and Transmitters
transducer - typically consists of a sensing element combined with a driving element (transmitter).
Figure 9.3 A typical process transducer.

4. Transducers for process measurements convert the magnitude of a process variable (e.g., flow rate, pressure, temperature, level, or concentration) into a signal that can be sent directly to the controller.
The sensing element is required to convert the measured quantity, that is, the process variable, into some quantity more appropriate for mechanical or electrical processing within the transducer.

5. Standard Instrumentation Signal Levels
Before 1960, instrumentation in the process industries utilized pneumatic (air pressure) signals to transmit measurement and control information almost exclusively.
These devices make use of mechanical force-balance elements to generate signals in the range of 3 to 15 psig, an industry standard.
Since about 1960, electronic instrumentation has come into widespread use.
Signal range: 1-5 mA, 4-20 mA, 10-50mA, 0-50V.
Most industrial analog instrumentation use 4-20 mA

6. Standard Instrumentation Signal Levels
Pneumatic instruments utilize physical displacement in the measurement medium such as movement of diaphragm
Pneumatic instruments are intrinsically safe (even in hazardous or explosive environments)

7. Sensors
Main categories of measurements used in process control:
Temperature
Pressure
Flow rate
Liquid level
Composition

9. Temperature Sensor
On-line measurement by:
Thermocouples & resistance temperature detector (RTD) – up to 10000C
Pyrometer and filled – above 9000C
System thermometer.

10. Differential Pressure
On-line measurement by:
- Liquid column
- Elastic element: Bourdon tube, diaphragm
- Optical fiber sensor: measure pressure in high- temperature environments (>11000C)

11. Liquid or gas flow rate
Flow rate can be measured indirectly using pressure drop across orifice or venturi
Other measurements:
Rotameter
Turbine flowmeter
Ultrasonic
Magnetic

12. Liquid level
Level can be measured using:
Float-activated
Head devices
Electrical (Conductivity)
Radiation
Radar

13. Chemical Composition
On-line measurement by:
Gas-liquid chromatography (GLC)
Gas chromatography (GC)
Infrared (IR) spectroscopy
UV spectroscopy (UV spectrophotometer)
Magnetic resonance analysis (MRA)
Refractive index (RI)
Electrophoresis

14. Transmitters
Converts the sensor output to a signal level appropriate for input to a controller, such as 4 to 20 mA.
Transmitters are generally designed to be direct acting.
Commercial transmitters have an adjustable input range (or span).
For example, a temperature transmitter might be adjusted so that the input range of a platinum resistance element (the sensor) is 50 to 150 °C.

15. In this case, the following correspondence is obtained:
Input
Output
50 °C
4 mA
150 °C
20 mA
Lower limit or zero of 50 °C
Range or span of 100 °C
The relation between transducer output and input is

16. For any linear instrument, the gain (Km):
The gain of the measurement element Km is 0.16 mA/°C.

17. Figure 9.4 A linear instrument calibration showing its zero and span.

18. Example
Several linear transmitters have been installed and calibrated as follows:
Voltage transmitter
Level: m 5 VDC
0.5 m VDC
a) Develop an expression for the output of the transmitter as a function of its input. Be sure to include appropriate units.
b) What are the gain, zero and span of the transmitter? Is the gain constant or variable?

19. Final Control Elements
Final control element (actuator) is the device that enables a process variable to be manipulated.
There are many different ways to manipulate the flows of material and energy into and out of a process.
Final control elements (usually control valves) adjust the flow rates of materials, and indirectly, the rates of energy transfer to and from the process.
Variable speed air compressor – adjust air flow rates
Variable speed pump - adjust the flow rates of material

20. Control Valves
Automatic control valve - Simple and widely used method to adjust flow rate of fluid.
The control valve components include the valve body, trim, seat, and actuator.
Control valves are either linear or rotary in design.

21. Globe valve
Linear valve
Open and close by moving a plug vertically away from the orifice and seat

22. Rotary valve
Closed by a 900 turn of the closing element
Used for both on-off and flow modulating control valve
Ball valve :
Plug valve:

23. Figure 9.7 A pneumatic control valve (air-to-open).

24. Air-to-Open vs. Air-to-Close Control Valves
Air-to-open: output signal , pressure on the diaphragm compresses the spring
Pulling the stem out open the valve further
Air-to-close: output signal , pressure on the diaphragm compresses the spring
Valve stem downward close the valve further

25. Normally, the choice of A-O or A-C valve is based on safety considerations.
We choose the way the valve should operate (full flow or no flow) in case of a transmitter failure.
Hence, A-O and A-C valves often are referred to as fail-closed and fail-open, respectively.

26. EXAMPLE
Consider the control valve on the steam for the endothermic CSTR shown in Figure Determine whether an air-to-open (A-O) or air-to-close (A-C) valve actuator should be used in this case.

28. Solution
If the valve were A-C (fail open), excessive steam flow to the heat exchanger would result causing a reactor temperature in excess of the normal operating value.
If the valve were A-O (fail closed), the reactor would simply cool off, which is not desirable but is preferred in this case.
Therefore, an A-O actuator should be selected in this case.

29. Example 9.1
Pneumatic control valves are to be specified for the applications listed below. State whether an A-O or A-C valve should be used for the following manipulated variables and give reason(s).

30. Flow of effluent from a wastewater treatment holding tank into a river.
Ans: A-O (fail closed) to prevent excessive and perhaps untreated waste from entering the stream
Flow of cooling water to a distillation condenser.
Ans: A-C (fail open) to ensure that overhead vapor is completely condensed before it reaches the receiver.

31. Valve Positioners
Pneumatic control valves can be equipped with a valve positioner, a type of mechanical or digital feedback controller that senses the actual stem position, compares it to the desired position, and adjusts the air pressure to the valve accordingly.

33. Specifying and Sizing Control Valves
A design equation used for sizing control valves :
q = flow rate,
= flow characteristic,
= pressure drop across the valve,
gs = specific gravity of the fluid.

34. Specification of the valve size is dependent on the so-called valve characteristic f.
Three control valve characteristics are mainly used:
- linear
- quick opening
- equal percentage

35. Figure 9.8 Control valve characteristics.

36. For a fixed pressure drop across the valve, the flow characteristic is related to the lift , that is, the extent of valve opening, by one of the following relations:
where R is a valve design parameter that is usually in the range of 20 to 50.

37. Rangeability
The rangeability of a control valve is defined as the ratio of maximum to minimum input signal level.
For control valves, rangeability translates to the need to operate the valve within the range 0.05 ≤ f ≤ 0.95 or a rangeability of 0.95/0.05 = 19.

38. To Select an Equal Percentage Valve:
Plot the pump characteristic curve and , the system pressure drop curve without the valve, as shown in Fig
- The difference between these two curves is
- The pump should be sized to obtain the desired value of , for example, 25 to 33%, at the design flow rate qd.

39. Figure 9.10 Calculation of the valve pressure drop from the pump characteristic curve and the system pressure drop without the valve

40. Calculate the valve’s rated Cv, the value that yields at least 100% of qd with the available pressure drop at that higher flow rate.
Compute q as a function of using Eq. 9-2, the rated Cv, and from (a).
A plot of the valve characteristic (q vs. ) should be reasonably linear in the operating region of interest (at least around the design flow rate). If it is not suitably linear, adjust the rated Cv and repeat.

41. Example 9.2
A pump furnishes a constant head of 40 psi over the entire flow rate range of interest. The heat exchanger pressure drop is 30 psig at 200 gal/min (qd) and can be assumed to be proportional to q2. Select the rated Cv of the valve and plot the installed characteristic for the following case:
a) A linear valve that is half open at the design flow rate.

42. Figure 9. 9. A control valve placed in series with a
Figure 9.9 A control valve placed in series with a pump and a heat exchanger. Pump discharge pressure is constant.

43. Solution
First we write an expression for the pressure drop across the heat exchanger

44. Because the pump head is constant at 40 psi, the pressure drop available for the valve is
Figure 9.11 illustrates these relations.
Note that in all four design cases at qd.

45. Figure 9.11 Pump characteristic and system pressure drop for Example 9.2.

46. First calculate the rated Cv using Eq. 9-2.
A linear valve that is half open at the design flow rate.
qd = design flow rate = 200 gal/min
Half open linear control valve, f = = 0.5
= 10 psi

47. For a linear characteristic valve, use the relation between and q from Eq. 9-2:
Using Eq. 9-9 and values of from Eq. 9-7, the installed valve characteristic curve can be plotted.

48. Figure 9.12 Installed valve characteristics for Example 9.2.