Techniques For Airflow Rate Measurements

Techniques For Air conflate Rate MeasurementsMy company is setting up an test to measure the fashionf impression regularize in a duct. Air tend measurement techniques argon necessary specially in many a(prenominal) industries. Some of the mutual nervous strainflow quantity applications include ventilation testing, propagate balancing, duc cardinalrk, air planes and so on. Many research and studies have been put into improving and inventing new equipments to measure air flow. This is so to enable user to get the most(prenominal) accu grade result and at the same time utilize the least cost.This report outlines the varied airflow measurement techniques and devices that be available today. There are many different types and ways to measure air flow only when I go away concent score on those that are more popular and commonly used. They are the Pitot- thermionic valve, Orifice dwelling house, Venturi meter, Cup tissue gage, Sphere steer gauge and hot- cable arc gage. Techniques and devices for airflow rate measurements2.1 Pitot thermionic tubeA pitot-static tube is used in wind tunnel tastes and on airplanes to measure the air flow rate. It is in any case used in many industrial applications. It was invented by the cut engineer Henri Pitot in the early 1700s and was later modified to its modern form in the mid 1800s by French scientist Henry Darcy. It is a slender tube that has two holes on it (Figure 1). The front hole is fixed in the airstream to measure whats called the stagnation pressure sensation. The side hole measures the static pressure. By measuring the contravention between these pressures, we are able to get the dynamic pressure that back be used to augur the air focal ratio.By Bernoullis principle,Stagnation pressure = static pressure + dynamic pressureSolving that for pep pill we getWhere V gas velocity pt stagnation or total pressure ps static pressure fluid densityFigure 1 Pitot-Static TubeThe incorporation of senso rs to measure the air temperature, barometric pressure, and relative humidity can further add the accuracy of the velocity and flow measurements. The Pitot tube can also measure the velocity with the use of a pressure transducer that generates an electrical argue which is proportional to the conflict between the pressures generated by the total pressure and the static pressure. The volumetrical flow is then calculated by measuring the ordinary velocity of an air stream passing through a handing over of a known diam. When measuring volumetric flow, the passage of a known diam mustiness be designed to reduce air upheaval as the air mass flows over the Pitot tube.To obtain an number of the volumetric flow in the duct from a series of pitot-static tube velocitymeasurements, one must integrate the velocity over the duct area.There are many of different methods for approximating the to a higher place integral. iodin of the methods is to divide the duct coddle-section into a number of equal area sectors, and then measure theaverage velocity at the center of each sectors.For example, we can divide the cross-section of the duct in the variant belowThe velocity allow be by calculatingthe sum2.1.1 Advantages and DisadvantagesThe advantages of using pitot-static tube is that it can be inserted in small airstream and it presents little resistance to flow. It is simple, inexpensive and suited for a word form of environmental conditions including extremely advanced temperatures and a wide compass of pressures.The disadvantages would be that if the flow rate is low, the difference in pressures will be too small to accurately measure with the transducer. If the air flow is high (supersonic), assumptions of Bernoullis equation will be violated and thus leading us to wrong measurement. Furthermore, if the tubes are clogged, the interpretation by the transducer will be inaccurate resulting in dire consequence in the context on airplane. Icing of the pitot tube had caused plane to crash.2.2 Orifice PlateOrifice plate is used for flow rate measuring in tubing systems. An orifice plate is lay in a call containing a fluid flow, which constricts the smooth flow of the fluid inside the tobacco shrill. By restricting the flow, the orifice meter causes a pressure drop across the plate. By measuring the difference between the two pressures across the plate, the orifice meter determines the flow rate through the pipe.Figure 2 Orifice Plate in a ductApplying Bernoullis equation to a contour flowing down the axis of the tube gives,Where,P pressure density of the fluidV Velocity of the fluidAs shown in the above diagram(Figure 2), point 1 is upstream of the orifice, and point 2 is behind the orifice. It is recommended that point 1 be positioned one pipe diameter upstream of the orifice, and point 2 be positioned one-half pipe diameter downstream of the orifice. Since the pressure at 1 will be higher than the pressure at point 2, the pressure dif ference will be a positive quantity.From continuity equation, the velocities can be replaced by cross-sectional areas of the flow and the volumetric flow rate Q,Where,A cross sectional areaSolving for the volumetric flow rate Q gives,The above equation remains true with perfectly laminar, inviscid flows. As for real flows like water or air, we have to take into account of the viscosity and turbulence that are present .To account for this effect, a top coefficient Cd is introduced into the above equation to marginally reduce the flow rate Q,Since the actual flow indite at point 2 downstream of the orifice is quite complicated, the following substitution introducing a flow coefficient Cf is made,Where,Ao area of the orificeAs a result, the volumetric flow rate Q for real flows is assumption by the equation,The flow coefficient Cf is prepare from experiments and is tabulated in reference books. It ranges from 0.6 to 0.9 for most orifices. Since it depends on the orifice and pipe di ameters (as well as the Reynolds Number), one will often find Cf tabulated versus the ratio of orifice diameter to inlet diameter, sometimes defined as b,The mass flow rate can be found by multiplying Q with the fluid density,There are mainly 3 different types of orifice plates. They are Concentric, segmental and Eccentric. This is to accommodate for different applications so that the meter has the optimum structure. The density and viscosity of the fluid, and the shape and width of the pipe do influence the choice of plate shape to be used.The concentric orifice is the most common of the 3 types. In this design, the orifice is equidistant. It is generally used for clean liquid and gas flow in pipes under six inches, where Reynolds numbers range from 20, 000 to 107. We will therefore use concentric orifice for our experiment purposes. ( which deals with air).Segmental orifice is similar to concentric orifice with regard to its functioning. The circular section is concentric with th e pipe while the segmental part is mounted in a horizontal pipe. This installation helps to eliminate of external materials on the upstream side of the orifice.Eccentric orifice plates are designed in such a way that the edge of the orifice is reallocated towards the interior of the pipe wall. It is used in similar manner as the segmental orifice plate.Figure 3 below shows the different types of orifice plates2.2.1 Advantages and DisadvantagesWith no moving move and a simple design, the orifice is easily machined. It is low lost and can be easily inserted into a duct or an existing pipeline with a minimum alteration to the layout. Therefore orifice plate has been a popular device for flow measurement.The disadvantage is that it creates a rather large non-recoverable pressure collect to the turbulence around the plate, leading to high energy consumption (Foust, 1981).2.3 Venturi meterMost of the unrecoverable discharge of pressure with an orifice is due to the sudden change in th e cross sectional area. The sudden increase of area subsequently the air passes the section of minimum area the quick convergence of the stream on the upstream side contributes considerably to the total loss. We are able to recover most of the pressure by leading the stream with the use of a conical length of pipe, with its smaller end of the same cross section as the jet, and gradually expanding in sizing along the direction of flow until the full pipe diameter is reached. An arrangement of this kind, with a conical entry is known as a venturi tube.The Venturi effect is named after Giovanni Battista Venturi (1746-1822), an Italian physicist.A venturi meter consists of a cylindrical length, a converging length with an included move of 20o or more, and short parallel throat, and a diverging section with an included angle of about 6o. The congenital finishes and proportions are designed in such a way to enable us to achieve the most accurate readings while ensuring minimum head l osses.Assuming that the fluid is inviscid with no losses due to viscosity, the velocity at section 1 and 2 are V 1 and V 2 respectively. The velocities are steady and uniform over areas A 1 and A 2Applying Bernoullis equation to a streamline passing along the axis between the two sections ( 1 2 ).Where,VVelocity of the fluidP Pressure density of the fluidZ HeightUsing continuity equation,Q = A1 V 1 = A 2 V 2When real world effects such as fluid friction and turbulence are included a correction factor, called the coefficient of discharge, Cd is introduced into the venturi equation givingFor low viscosity fluids C d = 0,98.2.3.1 Advantages and DisadvantagesThe venturi tube introduces substantially lower non-recoverable pressure drops (Foust, 1981). Therefore venture tube can be used on more viscous fluid.However it has limited range ability. It must be used only on installations where the flow rate is well known and varies less than 3 to 1. It is rather expensive and should be flow c alibrated to provide accuracy into the range of +/- 1.00%, Units are astronomic and weigh more than comparable head devices and thus making it difficult to install and inspect.2.4 AnemometerAn anemometer, also known as wind vane is a device for measuring the air flow rate in a contained flow such as duct or unconfined flow. The term is derived from the Greek word anemos, meaning wind. In around 1450, the Italian art architect Leon Battista Alberti invented the first mechanical anemometer which consisted of a disk placed perpendicular to the wind. To determine the velocity, an anemometer detects change in some corporal property of the fluid or the effect of the fluid on a mechanical device inserted into the flow. They are probably best used mounted on light, preferably streamlined, supports and inserted into the airstream from one side.2.4.1 Cup anemometerThis device consists of three or four hemispherical forms mounted at the ends of horizontal spokes which rotates about a low -friction vertical shaft. An electrical device is used to record the revolutions of the forms and measures the air flow rate. (Figure below)As the anemometer is placed inside the flow stream, the concave surfaces of the cups have higher wind resistance than their convex counterparts and thus producing an tired of(p) moment with respect to the center axis. This forces the cups to rotate (see schematic). Under steady flow condition, the rotational speed of the anemometer is directly related to the wind speed, that is V=rw.There are number of fundamental physical parameters and characteristics of an anemometer that affects the cup anemometer performance. They arerotor arm lengthcup arearotor inactiveness embrace coefficient on convex face of cup make coefficient on concave face of cupstatic, dynamic and parabolic mechanical friction coefficients for temperature rangesensitivity characteristic to out-of-plane attacklinearised calibration curve.A well designed cup anemometer should ha ve the following characteristics as shown in the Figure 4 belowLet us examine a cup anemometer rotating at speed w in a free wind speed UThe fast aerodynamic tortuousness on the rotor, MA, is given bywhere A frontal area of the anemometerr the air densityCdv drag coefficients for the concave faces of cupCdx drag coefficients for the convex faces of cupIn the steady state, there is perfect torque balance (MA=0), and the equation reduces todefining l and as the speed and drag ratios respectivelyallows further re-expression in a quadratic formTypical values of Cdv and Cdx are 1.4 and 0.4 respectively, giving a value of of 3.5. The aboveequation predicts that the consequential speed ratio l will be 0.303, meaning the rotor will rotate at about one third of the wind speed. Note that this solution also proves the theoretically linear sensitivity of the cup anemometer to wind speed. It also shows that the speed ratio is dependent on the drag characteristics of the cup and not the size . Furthermore, the rotational speed is inversely proportional to rotor radius.2.4.2 Advantages and disadvantagesThe advantages of the cups are their dependableness and ruggedness. The disadvantages are the relatively high threshold velocity (the minimum wind velocity needed to commencement ceremony the cups to turn). It is mainly used to only measure the horizontal component of the wind.Another problem with cup anemometry is the different response time for increasing and decreasing wind velocities due to its moment of inertia. This results in an overestimation of wind speed under turbulent wind conditions as present in nature, the so-called over-speeding. Additionally, the rotation of the anemometer causes a wear of bearing and leads to a recalibrations with time.2.5 Sphere anemometerMany research and studies have gone into the improving of such a device (Cup anemometer). For example, the celestial sphere anemometer. It was developed at the University of Oldenburg.This sphere an emometer, as shown in figure 4 below, is able to measure the air flow rate as well as simultaneous detection of the air flow direction. It eliminates the problem of wear of bearing as encountered in cup anemometer.Figure 5The sphere anemometer uses the relationship between the point force F playing on the tip of arod and its resulting deflection s.(1)Wherel the length of the rodE the catch modulusJa the second moment of area.In case of the sphere anemometer, with a sphere radius r a lot bigger than the radius of the rod rR, the force can be assumed to act only on the tip. The second moment of area is then given by(2)Together with the force acting on the sphere(3)where cd the drag coefficient of the sphereA the cross section of the sphere the density of airV the wind velocityEquation 1 becomes(4)Therefore the deflection of the rod is proportional to the drag coefficient cd and the wind velocity squared. For a calibration it is necessary to know how the drag coefficient cd changes with wind velocities. Table 1 below shows the drag coefficient of a sphere plotted against the Reynolds number (Re) (cf 1). It can be seen that for Reynolds numbers in the range from about 800 to 200000 the change in drag coefficient cd is negligible.For a sphere with a radius r = 40mm this range in Re corresponds to a range in wind velocitiesfrom 0.17m/s to 38m/s usingwhere v = 1.51 x 10-5 m2/s is the kinematic viscosity of air. Within this velocity range thedeflection s of the rod is directly proportional to the wind velocity squared. With this directrelation it is favourable to calibrate the sphere anemometer over a wide range of wind velocities.Table 12.6 Hot electrify anemometerThermal anemometry is the most common method used to measure instantaneous fluid velocity. The technique depends on the convective awake loss to the surrounding fluid from an electrically heat catching element or probe. If only the fluid velocity varies, then the heat loss can be interpreted as a me asure of that variable.Working PrincipleIts principle application is the measurement of rapid fluctuations, particularly the study of turbulent flow in this field it is the only instrument with sufficiently rapid response, and the associated electronic equipment lends itself readily to signal processing needed to record directly such properties of a turbulence as r.m.s values, correlation functions, and spectral distributions.Governing equationConsider a thin heated wire mounted to supports and exposed to a velocity UWhere,W power generated by Joule rut (W=I2Rw)Q heat transferred to surroundingQi CwTw=thermal energy stored in wireCw heat capacity of wireTw wire temperatureThe wire is heated electrically and placed in the flow stream. The energy balance of the heated wire at equilibrium is (equation 1)Where,I an electric currentRw the wire resistanceh the heat transfer coefficientA the heat transfer areaTw the wire temperatureTf the fluid temperatureD wire diameterKf heat conductivi ty of fluidNu dimensionless heat transferIn the forced convection regime (0.02Reynolds number Re= (where r is the air density and U is the velocity and is the air dynamic viscosity).(equation 2)WhereSubstituted Eq(2) into Eq(1),There are two types of hot-wire anemometer used in practice but I will touch on Constant Temperature Anemometer which is more commonly used.For a case of Constant Temperature AnemometerWhereAndThe voltage is a measured of velocity U.2.6.1 Advantages and disadvantagesIt has good frequency response as it can measure up to some(prenominal) hundred kHz possible. It is able to measure a wide range of velocity. It is small in size and has rapid response.-Thermal anemometry enjoys its popularity because the technique involves the use of very small probes that offer very high spacial resolution. The basic principles of the technique are relatively straightforward and the probes are difficult to damage if reasonable flush is taken.However, deposition of impurities in flow on sensor can alter the calibration characteristics and reduce frequency response. Probe may or burnt out easily if not explosive chargefully taken care of. It is unable to fully map velocity fields that depend on space coordinates and simultaneously on time. Furthermore, it cannot work well in hostile environment like combustion. The wire diameter needs to be very small of the order of 0.02mm or less.ConclusionIn this report, I have touched on the different techniques and different devices for the measurement of airflow. There are many different devices in the market but many use similar techniques with abit of new inventions or add ons here and there. Different airflow measuring devices utilize different technologies and thus, one needs to fully understand the characteristics, techniques and its pros and cons before selecting the optimal one for use.In summary, an ideal device to measure air flow rate should have the following characteristicsgood signal sensitivity. It should be able to detect output for small changes in velocity.High Frequency Response to accurately follow transients without any time lagWide velocity rangeCreate minimal flow disturbanceGood Spatial ResolutionInexpensiveHigh AccuracyUser friendly