1. Instrument Training Material
Flow Measurement
Instrument Training Material

2. Aim Understand the basic principle of flow measurement.
Knowing different type of flow measuring device available in YYCG.

3. Flow! What? Requirement for flow to occur?
Movement of a liquid or a gas from one point to another.
Requirement for flow to occur?
Upstream pressure MUST be higher then downstream.

4. Flow Profile Types
Laminar flow region with Reynolds number below 2,000.
Turbulent flow with Reynolds number greater than 4000.
Transitional flow with Reynolds number between 2000 and 4000.

5. Flow Measurement
Through a closed piping is one of the most important aspects of process control.
Flow is generally measured by measuring velocity V through a known area A. A V

6. Q v = A · V Flow Measurement Volumetric flow: Units: Where:
A = the cross sectional area of the flow carrier (pipe)
V = the fluid’s velocity
Units:
m3/day,
m3/hr,
liters/min,
gal/min,
ft3/sec,

7. Flow Measurement Mass flow, Q m = Q v · r Units: kg/hr, ton/day,
Where:
Qv is the Volumetric Flow Rate.
r is the density of the liquid.
Units:
kg/hr,
ton/day,
lb/hr,
lb/sec.
Q m, is obtained by multiplying Q v with the density r of the liquid, or

8. Flow Measurement Flow rate. Reynolds Number
Measure of flow at specific point of measurement.
Reynolds Number
Basic equations of flow assume the velocity of flow is uniform across a given cross section.
Re = vDr/m
Where n = the flow velocity
D the inside diameter of the pipe
r is the fluid density
m is the fluid velocity
Q m, is obtained by multiplying Q v with the density r of the liquid, or

9. Differential Pressure Flow meter
Contains two elements
Primary element
Some type of restriction that is place inside a pipe to cause a differential pressure
Secondary element
Normally a differential pressure transmitter

10. DP Flow Meters When liquid flow through the restriction
Velocity increases
Pressure decreases
Pressure upstream is higher than the pressure downstream
Base on the principle that as fluid flows through a pipe restriction, its velocity increases and its pressure decreases. So, the pressure on the upstream side of the restriction is higher than the pressure on the downstream side.

11. DP Flow Meters
Flow rate through the restriction is proportional to the square root of the DP across the restriction
V = k Sq (DP)
The DP TX measures the different in pressure or delta P and converts that value to an output that can be used by signal conditioning equipment to indicate flow rate
Base on the principle that as fluid flows through a pipe restriction, its velocity increases and its pressure decreases. So, the pressure on the upstream side of the restriction is higher than the pressure on the downstream side.

12. Head Meters or DP Flow Meters
Based on measuring the differential pressure created by the fluid when flowing through a restriction installed in the process line.
Velocity is directly proportional to the square root of the differential pressure across the restriction,
; where constant 2 p 1
1-ß 4
k =
V = k dP
Q v = A · V =
p d 2 4 p 1
1-ß dP C •
where ß = d / D; d is constriction diameter in m; D is pipe diameter in m; dP is deferential pressure in N/m2;
p - the density of the liquid, kg/m3; C - discharge coefficient(actual flow/theoretical flow).

13. Head Meters or DP Flow Meters
Generally cheaper, simple, reliable and offer more flexibility than other flow measurement methods.
Consists of two components: Primary device - placed in the pipe to restrict the flow and develop a differential pressure.
Secondary device - measures the differential pressure and provides a readout or signal for transmission to a control system.

14. Types of Primary Elements
Orifice plate
Widely used in industrial applications
It is simple and least expensive
Produces a greater overall pressure loss
Effectively utilized for clean fluid where line pressure losses or pumping costs are not critical

15. Orifice plate Operating principle: Plate inserted in process line.
Differential pressure developed across the orifice plate is measured to determine the flow rate.
Maintain steady flow through the orifice plate, the velocity must increase as it passes through the orifice.
Lowest pressure occurs where the velocity is the highest.
Greater the flow larger the dp across the orifice plate.

16. Types of Primary Elements
Type of orifice Plate:

17. Types of Primary Elements
Venturi Tubes.
exhibit a very low pressure loss.
the largest and most costly.
operate by gradually narrowing the diameter of the pipe.
Their applications are generally restricted to those requiring a low pressure drop and high accuracy reading.

18. Types of Primary Elements
Flow nozzles may be thought of as a variation on the Venturi tube. The nozzle opening is an elliptical restriction in the flow but with no outlet area for pressure recovery. The flow nozzle is a high velocity Flowmeter used where turbulence is high such as in steam flow at high temperatures. The pressure drop of a flow nozzle falls between that of the Venturi tube and the orifice plate.

19. Types of Primary Elements
Pitot Tubes consists of two hollow tubes that sense the pressure at different places within the pipe. These tubes can be mounted separately in the pipe or installed together in one casing as a single device. One tube measures the stagnation or impact pressure (velocity head plus potential head) at a point in the flow. The other tube measures only the static pressure (potential head), usually at the wall of the pipe.

20. Advantages of DP flowmeters
Universally suitable for applications involving liquids, gas and steam.
Excellent method, even under extreme process conditions, high temp and high pressure.
Dp transmitters can be replaced during operation with process shutdown.
Robust primary elements, no entirely mechanical and no moving parts.

21. Disadvantages of Dp flowmeters
Suitable for low-viscosity fluids
Metering gas flow require steady process conditions, pressure, temperature must be constant
Measuring system required additional valves and impulse lines

22. Variable area flowmeters
Simple and Cost Effective for measuring Liquid or Gases.
Consist of upright, tapered tube in which a float made of glass or metal hovers on the fluid flow entering the bottom of the tube.
The force exerted on the float by the fluid depends on its density, viscosity and rate of flow.

23. Variable area flowmeters
Higher the flow rate and, consequently, the force of the flow, the higher the float will rise in the tapered, graduated tube.
The annular gap between the float and the wall of the tube widens as the float moves up, until the force acting on the float are balanced and the float hovers at a steady height.

24. Variable area flowmeters
Advantages:
Usable for liquid, gas or steam application
Low cost method of flow metering due to the simple design
No power supply needed
Devices with sight glasses allow for an easy and dependable on-site process and flow monitoring
Low pressure losses

25. Variable area flowmeters
Disadvantages.
Measuring accuracy depends on the process conditions and the fluid properties.
Fluid specific calibration necessary.
Limited turndown (Max. 10:1).
Affected be entrained matter.
Can be used only for low-viscosity fluids.
No totalizing function.
Meter has to be installed in a vertical pipe.

26. Vortex Meters The operating principle.
based on the phenomenon of vortex shedding known as the von Karman effect.
As fluid passes a bluff body, it separates and generates small eddies or vortices that are shed alternately along and behind each side of the bluff body.
These vortices cause areas of fluctuating pressure that are detected by a sensor.
The output depends on the calibration constant, or K-factor.

27. Vortex Equation
Vortex Frequency
Flow Rate =
K-factor

28. Vortex Meter
In this example, the passage of a vortex causes a slight bow of a wing placed downstream of the bluff body.
The bend is measured by a piezoelectric crystal sensor in contact with the top of the wing.

29. Magnetic Flow meter
Based on Faraday’s Law of Magnetic Induction, which states that a voltage is induced into a conductor moving through a magnetic field.
With electromagnetic measuring principle, the flowing fluid is the moving conductor.
E +H Promag

30. Magnetic Flow meter
The induced voltage is proportionally related to the flow velocity.
Using the pipe cross-sectional area, the flow volume is calculated.
The DC magnetic field is generated by a switched direct current of alternating polarity.

31. Turbine Flow Meter
Uses a multi-bladed rotor that is supported by bearings within a pipe section perpendicular to the flow.
Fluid drives the rotor at a velocity that is proportional to the fluid velocity and, consequently, to the overall volume flow rate.
A magnetic coil outside the meter produces an alternating voltage as each blade cuts the coil’s magnetic lines of flux.

32. Turbine Flow Meter
Typical schematic of pick-up assembly and generated waveform are shown.
When the blade at point A passes the cone point B , the magnetic field produced by the permanent magnet is deflected by its presence, generating a voltage in the coil (positive pulse in the waveform).

33. Turbine Flow Meter
A negative pulse is produced when the blade travel from B to C.
One pulse represents a unit volume, hence, turbine output can be rated in pulses per gallon or any other units desired.

34. Thank You
Next….. Control Valve