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Flow Measurements

   Posted On :  23.09.2016 10:24 pm

The flow rate of a fluid flowing in a pipe under pressure is measured for a variety of applications, such as monitoring of pipe flow rate and control of industrial processes.






The flow rate of a fluid flowing in a pipe under pressure is measured for a variety of applications, such as monitoring of pipe flow rate and control of industrial processes. Differential pressure flow meters, consisting of orifice, flow nozzle, and venturi meters, are widely used for pipe flow measurement and are the topic of this course. All three of these meters use a constriction in the path of the pipe flow and measure the difference in pressure between the undisturbed flow and the flow through the constriction. That pressure difference can then be used to calculate the flow rate. Flow meter is a device that measures the rate of flow or quantity of a moving fluid in an open or closed conduit.


Flow measuring devices are generally classified into four groups. They are



1.  Mechanical type flow meters


Fixed restriction variable head type flow meters using different sensors like orifice plate, venturi tube, flow nozzle, pitot tube, dall tube, quantity meters like positive displacement meters, mass flow meters etc. fall under mechanical type flow meters.


2.  Inferential type flow meters

Variable area flow meters (Rotameters), turbine flow meter, target flow meters etc.


3.  Electrical type flow meters


Electromagnetic flow meter, Ultrasonic flow meter, Laser doppler Anemometers etc. fall under electrical type flow meter.


4.  Other flow meters


Purge flow regulators, Flow meters for Solids flow measurement, Cross-correlation flow meter, Vortex shedding flow meters, flow switches etc.





Orifice Flow Meter




An Orifice flow meter is the most common head type flow measuring device. An orifice plate is inserted in the pipeline and the differential pressure across it is measured.



Principle of Operation

The orifice plate inserted in the pipeline causes an increase in flow velocity and a corresponding decrease in pressure. The flow pattern shows an effective decrease in cross section beyond the orifice plate, with a maximum velocity and minimum pressure at the venacontracta.



The flow pattern and the sharp leading edge of the orifice plate which produces it are of major importance. The sharp edge results in an almost pure line contact between the plate and the effective flow, with the negligible fluid-to-metal friction drag at the boundary.



Types of Orifice Plates




The simplest form of orifice plate consists of a thin metal sheet, having in it a square edged or a sharp edged or round edged circular hole.


There are three types of orifice plates namely


1. Concentric


2. Eccentric and


3. Segmental type.

The concentric type is used for clean fluids. In metering dirty fluids, slurries and fluids containing solids, eccentric or segmental type is used in such a way that its lower edge coincides with the inside bottom of the pipe. This allows the solids to flow through without any obstruction. The orifice plate is inserted into the main pipeline between adjacent flanges, the outside diameters of the plate being turned to fit within the flange bolts. The flanges are either screwed or welded to the pipes.




The concentric orifice plate is used to measure flow rates of pure fluids and has a wide applicability as it has been standardized


·        The eccentric and segmental orifice plates are used to measure flow rates of fluids containing suspended materials such as solids, oil mixed with water and wet steam.




·        It is very cheap and easy method to measure flow rate


·        It has predictable characteristics and occupies less space


·        Can be used to measure flow rates in large pipes




·       The vena-contracta length depends on the roughness of the inner wall of the pipe and sharpness of the orifice plate. In certain case it becomes difficult to tap the minimum pressure due the above factor


·       Pressure recovery at downstream is poor, that is, overall loss varies from 40 to 90% of the differential pressure.


·       In the upstream straightening vanes are a must to obtain laminar flow conditions.


·       The orifice plate gets corroded and due to this after sometime, inaccuracy occurs. The coefficient of discharge is low.


Venturi Meter



General performance and calculations are similar to those for orifice plates. In these devices, there is a continuous contact between the fluid flow and the surface of the primary device.


It consists of a cylindrical inlet section equal to the pipe diameter, a converging conical section in which the cross sectional area decreases causing the velocity to increase with a corresponding increase in the velocity head and a decrease in the pressure head; a cylindrical throat section where the velocity is constant so that the decreased pressure head can be measured and a diverging recovery cone where the velocity decreases and almost all of the original pressure head is recovered. The unrecovered pressure head is commonly called as head loss.



This flow  meter  is  limited  to  use  on  clean,  non- corrosive liquids and gases, because it is impossible to clean out or flush out the pressure taps if they clog up with dirt or debris.


Short Form Venturi Tubes


In an effort to reduce costs and laying length, manufactures developed a second generation, or short-form venturi tubes shown in Figure 5.19.

There were two major differences in this design. The internal annular chamber was replaced by a single pressure tap or in some cases an external pressure averaging chamber, and the recovery cone angle was increased from 7 degrees to 21 degrees. The short form venture tubes can be manufactured from cast iron or welded from a variety of materials compatible with the application.


The pressure taps are located one-quarter to one-half pipe diameter upstream of the inlet cone and at the middle of the throat section. A piezometer ring is sometimes used for differential pressure measurement. This consists of several holes in the plane of the tap locations. Each set of holes is connected together in an annular ring to give an average pressure. Venturis with piezometer connections are unsuitable for use with purge systems used for slurries and dirty fluids since the purging fluid tends to short circuit to the nearest tap holes. Piezometer connections are normally used only on very large tubes or where the most accurate average pressure is desired to compensate for variations in the hydraulic profile of the flowing fluid. Therefore, when it is necessary to meter dirty fluids and use piezometer taps, sealed sensors which mount flush with the pipe and throat inside wall should be used. Single pressure tap venturis can be purged in the normal manner when used with dirty fluids. Because the venturi tube has no sudden changes in contour, no sharp corners, and no projections, it is often used to measure slurries and dirty fluids which tend to build up on or clog of the primary devices.



Flow Nozzle


Flange Type Flow Nozzle

The Flow nozzle is a smooth, convergent section that discharges the flow parallel to the axis of the downstream pipe. The downstream end of a nozzle approximates a short tube and has the diameter of the venacontracta of an orifice of equal capacity. Thus the diameter ratio for a nozzle is smaller or its flow coefficient is larger. Pressure recovery is better than that of an orifice. Figure shows a flow nozzle of flange type.



1. Permanent pressure loss lower than that for an orifice plate.


2. It is suitable for fluids containing solids that settle.


3. It is widely accepted for high pressure and temperature steam flow.




1. Cost is higher than orifice plate.


2. It is limited to moderate pipe sizes, it requires more maintenance.



Pitot tube


An obstruction type primary element used mainly for fluid velocity measurement is the Pitot tube.




Consider Figure which shows flow around a solid body. When a solid body is held centrally and stationary in a pipeline with a fluid streaming down, due to the presence of the body, the fluid while approaching the object starts losing its velocity till directly in front of the body, where the velocity is zero. This point is known as the stagnation point. As the kinetic head is lost by the fluid, it gains a static head. By measuring the difference of   pressure between that at normal flow line and that at the   stagnation point, the velocity is found out. This principle is used in pitot tube sensors.

Fig 5.21 Flow through solid body

Fig 5.22 Pitot tube


A common industrial type of pitot tube consists of a cylindrical probe inserted into the air stream, as shown in Figure. Fluid flow velocity at the upstream face of the probe is reduced substantially to zero. Velocity head is converted to impact pressure, which is sensed through a small hole in the upstream face of the probe. A corresponding small hole in the side of the probe senses static pressure. A pressure instrument measures the differential pressure, which is proportional to the square of the stream velocity in the vicinity of the impact pressure sensing hole.


The velocity equation for the pitot tube is given by,




1. No pressure loss.


2. It is relatively simple.


3. It is readily adapted for flow measurements made in very large pipes or ducts




1. Poor accuracy.


2. Not suitable for dirty or sticky fluids and fluids containing solid particles.


3. Sensitive to upstream disturbances.







The orificemeter, Venturimeter and flow nozzle work on the principle of constant area variable pressure drop. Here the area of obstruction is constant, and the pressure drop changes with flow rate. On the other hand Rotameter works as a constant pressure drop variable area meter. It can be only be used in a vertical pipeline. Its accuracy is also less (2%) compared to other types of flow meters. But the major advantages of rotameter are, it is simple in construction, ready to install and the flow rate can be directly seen on a calibrated scale, without the help of any other device, e.g. differential pressure sensor etc. Moreover, it is useful for a wide range of variation of flow rates (10:1).


The basic construction of a rotameter is shown in figure. It consists of a vertical pipe, tapered downward. The flow passes from the bottom to the top. There is cylindrical type metallic float inside the tube. The fluid flows upward through the gap between the tube and the float. As the float moves up or down there is a change in the gap, as a result changing the area of the orifice. In fact, the float settles down at a position, where the pressure drop across the orifice will create an upward thrust that will balance the downward force due to the gravity. The position of the float is calibrated with the flow rate.


Fig 5.23 Rotameter


γ1= Specific weight of the float


γ2= specific weight of the fluid


ν= volume of the float

Af= Area of the float.


At= Area of the tube at equilibrium (corresponding to the dotted line)


Fd = Downward thrust on the float Fu = Upward thrust on the float


The major source of error in rotameter is due to the variation of density of the fluid. Besides, the presence of viscous force may also provide an additional force to the float.





·        Can be used to measure flow rates of corrosive fluids

·        Particularly useful to measure low flow rates



·        Flow conditions are visible


·        Flow rate is a linear function(uniform flow scales)


·        Can be used to measure flow rates of liquids, gases and vapour


·        By changing the float, tapered tube or both, the capacity of the rotameter can be changed.




·       They should be installed vertically


·       They cannot be used for measurements in moving objects


·       The float will not be visible when coloured fluids are used, that is, when opaque fluid are used.


·       For high pressure and temperature fluid flow measurements, they are expensive


·       They cannot be used for fluids containing high percentage of solids in suspension.


Tags : Mechanical - Metrology and Measurements - Measurement of Power, Flow and Temperature Related Properties
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