Wednesday, July 31, 2013

GENERAL INSTRUMENATION QUESTION AND ANSWERS



Que. :  Explain Cascade Control system with a diagram. What would happier if a single controller were used ?
Ans. :  Cascade means two controllers is series. One of them is the Master or Primary and the second is the secondary of slave controller. The output of the secondary controller operates the final control element, that is the valve.

LOOP EXPLANATION :

The output of the temp. transmitter goes as measurement signal to the TIC which is the master controller. Similarly the output of pressure transmitter goes as measurement signal to the PIC which is the secondary controller.

The output of TIC comes at set point to PIC which is turn operates the valve. The reqd. temp. is set on the TIC.

USE OF CASCADE SYSTEM :

Cascade loops are invariably installed to prevent outside disturbances from entering the process. The conventional single controller as shown in the diagram cannot responds to a change in the fuel gas pressure until its effect is felt by the process temp. sensor. In other words an error in the detected temperature has to develop before corrective action can be taken. The cascade loop in contrast responds immediately correcting for the effect of pressure change, before it could influence the process temperature. The improvement in control quality due to cascading is a function of relative speeds and time lags. A slow primary (Master) variable and a secondary (Slave) variable which responds quickly to disturbances represent a desirable combination for this type of control. If the slave can respond quickly to fast disturbances then these will not  be allowed to enter the process and thereby will not upset the control of primary (master) variable. It can be said that use of cascade control on heat transfer equipment contributes to fast recovery from load changes or other disturbances.

Que. :  Explain ratio control system.

Ans. :  A ratio control system is characterized by the fact that variations in the secondary variable do not reflect back on the primary variable. In the above diagram 0 a ratio control system the secondary flow is hold in some proportion to a primary uncontrollable flow.

If we assume that the output of primary transmitter is A, and the output of the secondary transmitter is B, And that multiplication factor of the ratio relay is K, then for equilibrium conditions which means set valve is equal to measured valve, we find the following relation :

KA - B = 0

or B/A = K, where 'K' is the ratio setting of the relay.


Que. :  What is Furnace Draft control ?

Ans. :  Balanced draft boilers are generally used negative furnace pressure. When both forced draft and induced draft are used together, at some point in the system the pressure will be the same as that of atmosphere. Therefore the furnace pressure must be negative to prevent hot gas leakage. Excessive vacuum in the furnace however produces heat losses through air infiltration. The most desirable condition is that the one have is a very slight ( about 0.1" H20 ) negative pressure of the top of furnace.

Que. :  What is feed back control ? What is feed forward control ? Discuss its application ?

Ans. :
FEEDBACK CONTROL :

Feed back control involves the detection of the controlled variable and counteracting of charges its it’s value relative to set point, by adjustment of a manipulated variable. This mode of control necessities that the disturbance variable must affect the controlled variable itself before correction can take place. Hence the term 'feedback' can imply a correction 'back' in terms of time, a correction that should have taken place earlier when the disturbance occurred.

FEED FORWARD CONTROL :

Feed forward control system is a system in which corrective action is based on measurement of disturbances inputs into the process. This mode of control responds to a disturbance such that is instantly compensates for that error which the disturbance would have otherwise caused in the controlled variable letter in time.

Feed forward control relies on a prediction. As can be seen from the figure of feed forward control a necessary amount of input goes to the process. This measurement goes to the controller which gives output to the control valve. The control valve regulates the flow.

FEED BACK CONTROL :

In feed forward control no difference between the desired result and actual result need exist before corrective action is taken in feed back control a difference must exist. Hence, open loop or feed forward control is capable of perfect control, but feed back is not. Due to economic impractality of precision , predicting the amount of correction necessary to achieve satisfactory results with feed forward control, feed back control is most often used. In order to properly choose the type of feed back controller for a particular process application, two factors time and gain must be considered.


Que. :  What are Intrinsically safe system ?

Ans. :  Intrinsic safety is a technique for designing electrical equipment for safe use in locations made hazardous by the presence of flammable gas or vapors in air.

"Defn. :" Intrinsically safe circuit is one in which any spark or thermal effect produce either normally or under specified fault conditions is incapable of causing ignition of a specified gas or vapor in air mixture at the most easily ignited concentration.

HAZARDOUS AREAS :

The specification of products or systems sold as intrinsically safe must state in what hazardous areas they are infect intrinsically safe. Universal cooling of hazardous areas has not, unfortunately, been adopted in all countries. However two sets of codes in common use are.



Que. :  What does a transmitter output start from 3-15 psi or (0.2 - 1 Kg/Cm2) or 4 - 20 ma. etc. ?

Ans. :  The transmitter output stance from what is known as "live zero". This system has specific advantages :

1. The systems automatically alarms when the signal system becomes inoperative.

2. The output areas is linear ( Ratio of 1 : 5 ).

DEAD ZERO SIGNAL :

The advantage is that it does not have to be biased to true zero. A "Live zero" gives the computer additional information, so that it can takes appropriate alarm action in case of a measurement failure, because it can discriminate between a transmitter operating, but transmitting a zero measurement and a failure, in the signal system.

Que. :  What is force balance and motions balance principle ?

Ans. : 

FORCE BALANCE PRINCIPLE :

"A controller which generates and output signal by opposing torque’s".



The input force is applied on the input bellows which novas the beam. This crackles nozzle back pressure. The nozzle back pressure is sensed by the balancing bellows which brings the beam to balance. The baffle movement is very less about 0.002" for full scale output.



MOTION BALANCE PRINCIPLE :

"A controller which generates an output signal by motion of its parts".



The increase in input signal will cause the baffle to move towards the nozzle. The nozzle back pressure will increase. This increase in back pressure acting on the balancing bellows, will expands the bellows, there by moving the nozzle upward. The nozzle will move untill motion (almost) equals the input (baffle) motion.
Advantages of force Balance :

1. Moving parts are fever.

2. Baffle movement is negligible.

3. Frictional losses are less.


INFORMATION ABOUT CONTROL VALVES



      Que. :  What is a control valves ?

Ans. :  A control valve is the final control element, which directly changes the valve of the manipulated variable by changing the rate of flow of control agent.

A control valve consists of an operator and valve body. The operator provides the power to vary the position of the valve plug inside the body. The plug is connected to the operator by a stem, which slides through a stuffing box. The air signal from the controller is applied above the diaphragm. The increasing air signal from the controller is applied above the diaphragm. An increasing air signal will push the operator stem downwards against the force exerted by the spring on the diaphragm plate. The valve is adjusted in such a way that the plug starts moving when 3 psi is applied to the diaphragm and touches the seat when 15 psi is applied gm. Thus an increase in air pressure will close the valve. Hence the home "Air to Close". Another type is "Air to open", such that 3 psi on the diaphragm the value is closed and 15 psi air signal it in fully open.

Que. :  What are the different types of control valves ?

Ans. :  The commonly used control valves can be divided as follows.

1. Depending on Action.

2. Depending on the Body.

1. DEPENDING ON ACTION :
Depending on action there are two types of control valves, (1) Air to close, (2) Air to open.

2. DEPENDING ON BODY :
1. Globe valves single or double seated.

2. Angle valves.

3. Butterfly valves.

4. Three way valves.

Que. :  What is the use of single seated valve ?     

Ans. :  The single seated valve is used on smaller sizes, and in valve of larger sizes, where an absolute shut off is required. The use of single seated valve is limited by pressure drop across the valve in the closed or almost closed position.

Que. :  What is the use of double seated valve ?

Ans. :  In double seated valves the upward and downward forces on the plug due to reduction of fluid pressure are nearly equalized. It is generally used on bigger size valves and high pressure systems. Actuator forces required are less i.e. A small size actuator.

Que. :  What is CV of a valve ?

Ans. :  CV is the capacity of a valve and is defined as :

"No of gallons per minute of water which passes through a fully open valve at a pressure drop of 1 psi.

The valve coefficient CV is proportional to the area 'A' between the plug and valve seat measured perpendicularly to the direction of flow.

Que. :  What are the different types of actuators ?

Ans. :  The different types of actuators are :

1. Diaphragm Operated.

2. Piston Operated.

Que. :  What types of bonnets would you use of high temp. and low temp. ?

Ans. : 
HIGH TEMP. : Bonnets are provided with radiation fins to prevent glad packing from getting damaged.


ON VCF LOW TEMP. : Extended bonnets are used to prevent gland packing from getting frcored.

Que. :  How will you work on a control valve while it is line ?

Ans. :  While the control valve is in line the control valve has to be got by passed and secondly the line has to be drained and depressurized.

Que. :  What is the use of  a valve positioner ?

Ans. :  The valve positioner is used for following reasons :

1. Quick Action control valve.

2. Valve hysteresis.

3. Valves used on viscous liquids.

4. Split Range.

5. Line pressure changes on valve.

6. Valve Bench set not standard.

7. Reversing valve operation.

Que. :  When can a by pass be not used on a positioner ?

Ans. :  A by pass on a positioner cannot be used when :

1. Split Range operation.

2. Reverse Acting Positioner.

3. Valve bench set not standard.

Que. :  What is the use of link connected to the valve positioner ?

Ans. :  The link serves as the feed back to the value. Ant valve movement is sensed by this link. Sometimes due to line pressure changes on H.P. service the valve position may be changed, the link in turn senses this change and the positioner will produce an output which will operate the valve to the original position.

Que. :  What is the use of  booster relays ?

Ans. :  Booster relays are essentially air load, self contained pressure regulators. They are 
classified into three broad groups :

1. Volume Boosters : These are used to multiply the available volume of air signal.

2. Ratio Relays : Use to multiply or divide the pressure of an input signal.

3. Reversing Relays : This produces a decreasing output signal for an increasing input signal.

Que. :  What is the use of Angle valves ?

Ans. :  Angle valves are used where very high pressure drops are required and under very severe conditions. Where the conventional type of valve would be damaged by erosion.

Que. :  What is the use of butterfly valves ?

Ans. :  Butterfly valves are used only in systems where a small pressure drop across the valve is allowed. The butterfly is fully open when the disc rotates by 90. A drawback of this valve is that even a very small angular displacement produces a big change in flow.



Que. :  What is the use of three way valves ?

Ans. :  Three way control valves are only used on special systems, where a dividing or mixture of flows according to a controlled ratio is required.

Que. :  What is a cage valve ?

Ans. :  A cage valve uses a piston with piston ring seal attached to the single seated valve "plug". Here the hydrostatic forces acting on the top or the piston or below the valve plug tend to cancel out. The seat ring is clamped in by a cage. Cage valves are generally used for noise reduction.

Que. :  What are the advantages of Camflex valves ?

Ans. :  Camflex valves are intermediates between globe valve and butterfly valve. The plug rotates 60' for full opening.

ADVANTAGE :

1. Actuator forces required are very less.
2. Extended bonnet and hence can be used on any service i.e. on high temp. and very low temp.
3. Variations in flow.
4. Light weight.



Que. :  What are the different types of plugs ?

Ans. :  The different types of plugs are generally used are :
( 1 ) V. port plug          ( 2 ) Contoured plug

V. PORT PLUG :

Ported plug are generally used on double seated valves. This is because ported plugs, have a more constant off balance area.

CONTOURED PLUGE :

Contoured plugs are generally used on single seated valve with small trim sizes.

Que. :  What are the different valve characteristic ?

Ans. :  The different types of valve characteristic are :
1. Linear                     2. Equal Percentage               3. Quick Opening.

LINEAR : The valve opening to flow rate is a linear curve

EQUAL PERCENTAGE :

For equal increments of valve opening it will give equal increment in flow rate range. At small opening the flow will also be small.

QUICK OPENING :

At small opening the increments in flow rate is more. At higher opening the flow rate becomes steady.

QUE. : What is a solenoid valve ? Where it is used ?

Ans. :  A solenoid is electrically operated valve. It consist of a solenoid ( coil ) in which a magnetic plunger moves which is connected to the plug and tends to open or close the value. There are two types of solenoid valves :
1. Normally open                    2. Normally closed

USE : It is used for safety purpose.

Que. :  How will you change the valve characteristics with positioner ?

Ans. :  The positioner contains different types of came in it. selection of the proper can the valve opening characteristics can be changed.


Que. :  How will you change the action of a control valve ?
Ans. : 
1. If the control valve is without bottom cap. The actual needs to be changed.

2. If bottom cap is provided.

a) Disconnect the stem from  the actuator stem.

b) Separate the body from the bonnet.

c) Remove the bottom cap and the plug from body.

d) Detach the plug from the stem by removing the pin.

e) Fix the stem at the other end of the plug and fix the pin back.

f) Turn the body upside down. Connect it to the bonnet after inserting the plug and stem.

g) Connect back the stem to the actuator stem.

h) Fix back the bottom cap.

i) Calibrate the valve.


 Que. :  How will you select the control valve characteristics ?

Ans. :  The graphic display of flow various lift shows then the Desired or inherent characteristic is changed by variations pressure drop. This occurs as the process changes from condition where most of pressure drop takes place at the control valve is a condition where most of the pressure drop is generally distributed through rest of the system.

% Flow : This variation in where most of the total drop take place is one of the most important aspects is choosing the proper valve characteristics for give process.
Flow control : Normally Equal percentage valve is used.
Pressure Control : Normally linear valve is used to maintain a constant pressure drop.
Temp. Control : Normally equal percentage valve is used.
Liquid Level Control : Normally linear valve is used.

Basically in selecting a valve characteristic two important point have to be taken into account.
a) There should be a linear relationship between the position of the plug and the flow through the valve in a wide range of change in the pressure drop across the valve.
b) The pressure drop across a valve should be as low as possible.

Que. :  An operator tells you that a control valve in a stuck ? How will you start checking ?

Ans. : 
1. First of all get the control valve is passed from operation.

2. Check the lingual to the diaphragm of the control valve.

3. Disconnect it possible the actuator stem from the control valve stem.

4. Stroke the actuator and see whether the actuator operates or not. It not then the diaphragm may be punctured.

5. If the actuator operates connect it back to the plug stem stroke the control valve. If it does not operate loosen the gland nuts a bit and see if it operates. If it does not then the control valve has to be removed from the line to w/shop.

Que. :  Where is an Air to close and Air to open control valves used  ?
Ans. :
AIR TO CLOSE :
1. Reflux lines.

2. Cooling water lines.

3. Safety Relief services.

AIR TO OPEN :
1. Feed lines.

2. Steam Service.

Que. :  Why does control valve operate at IS psi ?

Ans. :  On higher pressure the actuator sizes becomes bigger in area. The actual force produced by the actuator.

Force = Pressure  x  Area.

           = 15 psi  x Area If Area = 15"

Force produced = 15 psi  x  25" pounes.

CONTROL SYSTEM



AUTOMATIC CONTROLLER :

It is a device which measured the value of variable quantity or condition and operates to correct or lie it deviation of this measured value from a selected reference.

AUTOMATIC CONTROL SYSTEM :

It is any operable arrangement of one or more automatic controllers in closed loops with one or more processes.

SELF OPERATED CONTROLLER :

It is one in which all the energy needed to operate the final control element is derived from the controlled medium through the primary element.

RELAY OPERATED CONTROLLER :

It is one in which the energy transmitted through the primary element is either supplemented or amplified for operating the final control element by employing energy from another sources.

PROCESS :

A process comprises the collective function performed in and by the equipment in which a variable is to be controlled.

SELF REGULATION :

It is an inherent characteristic of the process which aids in limiting the deviation of the controlled variable.

CONTROLLED VARIABLE :

The controlled variable is that quantity and condition which is measured and controlled.

CONTROLLED MEDIUM :

It is that process energy or material in which a variable is controlled. The controlled variable is a condition or characteristic of the controlled medium. For e.g. where temperature of water in a tank is automatically controlled, the controlled variable is temperature and controlled medium is water.

MANIPULATED VARIABLE :

It is that quantity or condition which is varied by the automatic controller so as to affect the value of the controlled variable.


CONTROL AGENT :

It is that process energy or material of which the manipulated variation is a condition or characteristic. The manipulated variable is a condition or characteristic of the control agent. For e.g. when a final control element changes the fuel gas flow to burner the manipulated variable is flow the control agent is fuel gas.

ACTUATING SIGNAL :

The actuating signal is the difference at anytime between the reference input and a signal related to the controlled variable. This basically known as error signal.

DEVIATION :It is the difference between the actual value of the controlled variable and the value of the controlled variable corresponding with set point.

OFFSET :

It is the steady state difference between the control point and the value of the controlled variable corresponding with set point

CORRECTIVE ACTION :

It is the variation of the manipulated variable produced by the controlling means. The controlling means operates the final control element ( control value ) which in turn varies the manipulated variable.

REFERENCE INPUT :

It is the reference signal in an automatic controller.

SET POINT :

It is the position to which the control point setting mechanism is set.

CONTROL POINT :

It is the value of the controlled variable which under any fixed set of conditions the automatic controller operates to maintain.

PRIMARY FEEDBACK :

It is the signal which is related with the reference input to obtain the actuating signal. Simply stated primary feedback is the actual measurement of the controlled variable which when compared with the desired measurement of the controlled variable produces the actuating signal.

POSITIONING ACTION :

It is that in which there is a predetermined relation between the value of the controlled variable and the position of the final control element.

PROPORTIONAL ACTION :

It is that in which there is a continuous linear relationship between the value of the actual measurement of the controlled variable and the value position.

FLOATING ACTION :

It is that in which there is a predetermined relation between the deviation and speed of final control element.

DERIVATIVE ACTION :

It is that in which there is a predetermined relation between a time derivative of the controlled variable and position of final control element.

REST ACTION :

It is the value movement at a speed proportional to the magnitude of deviation.

RATE ACTION :

It is that in which there is a continuos linear relation between the rate of change of controlled variable and position of final control element. Rate action produces value motion proportional to the rate of change of actual measurement.

PROPORTIONAL BAND :

It is the range of values of the controlled variable which correspond to the full operating range of the final control element.


RESET RATE :

It is the number of times/minute that the effect of proportional position action upon the final control element is repeated by proportional speed floating action.

There are two ways of expressing reset action :

1. Reset time and  2. Reset Rate

1. Reset Rate : It is commonly expressed as a number of "repeats" per minute. It is determined by dividing.
a) Travel of final control element ( Value stroke ) in one minute as a result of the effect of proportional speed floating action.
b) The travel as a result of the effect of proportional position action with the same deviation in both cases.

2. Reset Time : It is the time interval by which the rate is commonly expressed in minutes. It is determined by subtracting.
a) The time required for a selected motion of the final control element resulting from combined effect of the proportional position plus rate action.

b) The time required for the same motion  as a result of the effect of proportional position action alone with the same rate of change of controlled variable in both cases or expressed in another way. It is the time lead in terms of air pressure on the control value produced by rate action compared with proportional position action for the same rate of change of actual measurement in both cases.

Que. :  Explain the application of proportional integral and derivative.

Ans. : 
PROPORTIONAL CONTROL ONLY :
Proportional control only attempts to return a measurement to the set point after a load upset has occurred. How ever it is impossible for a proportional controller to return the measurement exactly to the set point.
USE : It is normally used for level controls. It reduces the effect of a load change but it can not eliminate it.

PROPNT RESET CONTROL :

Reset action is introduced to eliminate offset. It will integrate any difference between measurement and set point and cause the controller's output to change until the difference between the measurement and set point is zero. Reset will act as long as the error exists.

USE: Proportional + Reset controllers are by far the common types used in industrial process control and where predominate dead times occur.

PROPNT RESET + DERIVATIVE :

Derivative or rate action helps the controller overcome system inertia and result in faster, more precise control. Derivative action occurs whenever the measurement signal changes. Under study conditions the rate action does not act. Derivative allows the controller to inject more corrective action.
USED : On temperature controls.




Que. :  What is difference gap control ?

Ans. :  Differential gap control is similar to on off control except that a band or gap exists around the control point.

USE : In industry differential gap control is often found in non critical level control applications where it is desirable only to prevent a tank from flooding or drying. When a measured variable exceeds the upper gap the control valve will open fully or be closed fully. Similarly when it exceeds the lower gap it will open or close fully.

Que. :  Where is on off control used ?

Ans. :  On off control is used when

1. Precise control is not needed.

2. Processes that have sufficient capacity to allow the final operator to keep up with the measurement cycle.

3. It is mainly used in refrigeration and are conditioning systems.

Que. : 
Ans. :  When reset action is applied in controllers Where the measurement is away from the set point for long periods the rest may drive the output to its maximum resulting in rest wind up. When the process starts again the output will no come off its maximum until the measurement crosses the so point causing large overshoots. This problem can be avoid by including antireset wind up circuit which eliminates the problem of output saturation.

Que. :  Why is reset called integral and Rate derivative ?

Ans. :  RESET is called integral because of the mathematical relationship to the output.

RATE is called derivative because

Oi = rd (e) / dt +O0

Oi = Output at any instant

e   = error signal

O0 = Output at zero error.

t     = time.
PROPORTIONAL ACTION :
            Oi = 100 / PB  x  e  + O0

Que. :  Explain tuning of controllers.

Ans. :  Tuning basically involves adjustment of proportional. Integral  and derivative parameters to achieve good control. The gain, time constants, and dead times around the loop will dictate the settings of various parameters of the controller.

Tuning methods are broadly classified into two :

1. Closed Loop Method : e.g. Ultimate Gain Method.
2. Open Loop Method : e.g. process Reaction curve.

ULTIMATE GAIN METHOD :

The term ultimate gain was attached to this method because its use require the determination of the ultimate gain (sensitivity) and ultimate period. The ultimate sensitivity Ku is the maximum allowable value of gain (for a controller with only Proportional mode) for which the system is stable. The ultimate period is the period of the response with the gain set at its ultimate value.

PROCESSORS REACTION CURVE :

To deter mine the process reaction curve, the following steps are recommended. :

1.   Let the system come to steady state at the normal load level.

2.   Place the controller on manual.

3.   Manually set the output of the controller at the value at which it was operating in the automatic mode.

4.   Allow the system to reach the steady state.

5.   With controller on manual, impose a step changes in the output of controller, which is an signal to value.

6.   Record the response of controlled variable.

7.   Return the controller output to its previous value and return the controller to auto operation.

Que. :  Explain the working of an electronic P.I.D. controller.

Ans. : 
Input from the measurement transmitter is compared with the set point voltage to produce a deviation signal. The deviation signal is combined with a characterized feed back signal to provide the input for the function generator amplifier. This amplifiers output is delivered to the feed back network, and to the final output which is a 10-50m.a. do signal for actuation of final operators.

PROPN ACTION : It is a obtained by adjusting the magnitude of feed back signal. An increase in negative feed back means less effective gain and thus a broader proportional band.

REST ACTION : It is obtained by charging the reset capacitor at a rate  determined by the value of reset resister. The reset resister is variable, and constitutes reset adjustment.

DERIVATIVE ACTION : The connection of a derivative capacitor across the feedback circuit delays feedback until the capacitor is charged to a value approaching amplifier output. This delay is controlled by value of derivative resister. This resister is variable and constitutes derivative adjustment.

Que. :  What is an analogue integrator and an analogue differentiators ?
Ans. :

ANALOGUE INTEGRATOR :

ANALOGUE DIFFERENTIATORS :

Que. :  What is anti reset wind up ?

Ans. :  If the limit acts in the feed back section of the control amplifiers integral circuit, the controller output will immediately begin to drive in the opposite direction as soon as the process signal crosses the set point. This approach is referred to as antireset wind up.

Que. :  What are De saturators ?

Ans. :  When, in some processes, e.g. batch process, long transient responses are expected during which a sustained deviation is present the controller integral action continuously drives the output to a minimum or maximum value. This phenomenon is called "integral saturation of the control unit". When this condition.

Que. :  Explain the working of Rotameter.

Ans. :  Variable area meters are special form of head meters. Where in the area of flow restrictor is varied. So as to hold the differential pressure constant. The rotameters consists of a vertical tapered tube through which the metered fluid flows in upward direction. A "float" either spherical or cone shaped, actually more dense than the fluid being measured, creates an annular passage between its maximum circumference and the weight of the tapered tube. As the flow varies the "float" rises or falls to vary the area of the passage so that the differential across it just balances the gravitational force on the "float" i.e. the differential pressure is maintained constant. The position of the "float" is the measured of the rate of flow.

Que. :  Explain the working of a magnetic meter.

Ans. :  An electric potential is developed when a conductor is moved across the magnetic field. In most electrical machinery the conductor is a "wire"; the principle is equally applicable to a moving, electrically conductive liquid. The primary device of commercial magnetic meters consists of a straight cylindrical electrically insulated tube with a pair of electrodes nearly flush with the tube wall and located at opposite ends of a tube diameter. A uniform a.c. magnetic field is provided at right angles to electrode diameter and to the axis of the tube. The a.c. voltage developed at the electrodes is proportional to the volume flow rate of fluid, and to a magnetic field strength. This device is limited to electrically conducting liquids. The magnetic meter is particularly suited to measurement of slurries and dirty fluids, since there are no location for solids to collect except the walls of the tube itself.

 Que. :  Explain the working of a turbine meter.

Ans. :  Turbine meters consist of a straight flow tube within which a turbine or fan is free to rotate, about its axis which is fixed along the center line of the tube. Straightening rances upstream of the turbine minimizes possible rotational components of fluid flow. In most units a magnetic pick-up system senses the rotation of the rotor through the tube wall. The turbine meter is a flow rate device, since the rotor speed is directly proportional to flow rate. The output is usually in the form of electrical pulses from the magnetic pick-up with a frequency proportional to flow rate. Turbine meter are primarily applied to measurement of clean and noncorossive hydrocarbons.


Que. :  Explain the working of a Pitot tube.

Ans. :  The pitot tube measures the velocity at point in the conduct. If quantity rate measurement is desired, it must be calculated from the ratio of average velocity to the velocity at the point of measurement.


PRINCIPLE : If a tube is placed with its open and facing into a stream of fluid, then the fluid impinging on the open end will be brought to rest, and the kinetic energy converted to pressure energy. This the pressure built up in the tube will be greater than that in the free stream by the impact pressure or pressure produced by loss of kinetic energy. The increase in pressure will depend upon the square of the velocity of the stream. The difference is measured between the pressure in the tube and static pressure of the stream. The static pressure is measured by a tapping in the wall of the main or by a tapping incorporated in the pitot static tube itself. The difference between the pressure in the tube and static pressure will be a measure of the impact pressure and therefore of the velocity of the stream oil.

Que. :  Where is the integral orifice used ?

Ans. :  Integral orifice is used to measure small flow rates. It is mounted directly on the secondary device. The integral orifice diameter varies between 0.020 inch and 0.250 inch diameter. The integral orifice finds considerable use in laboratory and pitot plants.

Calculation of flow rate :

            Qn / Fc = Ks  x  Cwi  x  Fa  x  Fm  x  ( Gp / Ge ) hw

Que. :  Explain the working of a target meter.

Ans. :
The target meter combines in a single unit both a primary element and a force balance flow rate transmitter. A circular disc (or target) supported concentrically in the pipe carrying the flowing fluid results in an annular orifice configuration. Pressure difference developed by the fluid flow through this annular orifice produces a force on target proportional to the square of the flow rate. This force is carried out of the pipe through a rod passing through a diaphragm seal, and is measured by a pneumatic or electronic force balance system identical with the mechanism of the force balance D.P. cell. The advantages of the target meter lies primarily in its single unit construction the primary device and responsive mechanism in a single structure. This eliminates the diff. pressure fluid connections in most heads meters. This is particularly used for sticky and dirty material which may plug up differential connections and for liquids which require elevated temperatures to avoid solidification, this elimination of liquid connection is useful.

{     Wm     } 2

F = {------------------------------ }

{ Cst   Fa   Fm   Fc cf }

Que. :  Where is a quadrant orifice used ?

Ans. :  If the fluid is viscous and the operating Reynolds number is low quadrant orifice is preferred

Que. :  What are types of taps used for orifices ?
Ans. : 

1. FLANGE TAPS :
This are most commonly used on pipe sizes of 2 inches or larger. They are located in the orifice flange 2 inch from upstream and 1 inch downstream from the faces 0 orifice plate.

2. CORNER TAPS :

On pipe sizes less than 2 inches corner taps located directly at the face of the orifice plate.

3. VENA CONTRACTA AND REDIUS TAE :

Vena contracta taps located at 1 pipe diameter upstream and at point of minimum pressure downstream. There are mostly widely used for measurement of steam.

Radius taps are located 1 pipe diameter upstream and 1/2 pipe diameter downstream for the inlet face of the orifice are a close approximation to vena contracta taps upto 0.72 d / D.

4. FACE FLOW TAPS :

Face flow taps are located at 2 1/2  pipe diameter upstream and B pipe diameter downstream. Full flow taps at 2 1/2 and B pipe diameter have the same advantage as vena contracta or radius taps.

QUE. : What is Reynolds number ?

Ans. :  Dynamic similarity implies a correspondence of fluid forces in two systems. In general situation there are many classes of forces that influence the behavior of fluids. Some of these are inertial viscous, gravitational, compressibility, pressure and elastic forces. Certain dimensionless ratio are developed based on fluid properties. Velocities and dimension, which are essentially force ratio.

The more important of these are Reynolds number

SVD

u

For most applications in practical flow measurement the Reynolds number is taken to be sufficient criterion of dynamic similarly. The magnitude of Reynolds number not only indicates whether the flow is laminar or turbulent but also furnishes the probable shape of velocity profile. Due to the strong role it plays as an indicator of varying flow characteristics, many of the deviation from the theoretical equations are called Reynaldo number effects.


Que. :  How would you choose differential range ?

Ans. :  The most common diff. range for liquid measurement is 0-100" H20. This range is high enough to minimize the errors caused by unequal heads in the seal chambers, differences in temps. of load lines etc. The 100" range permits an increase in capacity upto 400" and a decrease down upto 20" by merely changing range tubes or range adjustment.

Que. :  What are positive Displacement meters ?
Ans. : 

PRINCIPLE :

The principle of measurement is that as the liquid flows through the meter it moves a measuring element which seals off the measuring chamber into a series of measuring compartments each holding a definite volume. As the measuring element moves, these compartments are successively filled and emptied. Thus for each complete of the measuring element a fixed quantity of liquid is permitted to pass from the inlet to the outlet of the meter. The seal between measuring element and the measuring chamber is provided by a film of measured liquid. The number of cycle of the measuring element is indicated by means of a pointer moving over the dial, a digital totalizer or some other form of register, driven from the measuring element through an adjustable gearing.



The most common forms of positive displacement meters are :



1.   Reciprocating Piston type.

2.   Rotating or Oscillating Piston type.

3.   Nutating Disc type.

4.   Fluted Spiral Rotor type.

5.   Sliding vane type.

6.   Rotating vane type.

7.   Oval Gear type.