FLOW METER GROUPS: 1. Quantity meter - POSITVE DISPLACEMENT METERS - WEIGHERS - REPROCICATING PISTON - ROTATING VANES 2. Rate of flow meters - ORIFICE PLATES - VENTURI TUBES - TURBINE METERS - VORTEX METERS
Dec 13, 2015
FLOW METER GROUPS:
1.Quantity meter- POSITVE DISPLACEMENT METERS- WEIGHERS- REPROCICATING PISTON- ROTATING VANES
2.Rate of flow meters- ORIFICE PLATES- VENTURI TUBES- TURBINE METERS- VORTEX METERS
FLOW MEASURING PARTS:
1. Primary element - in contact with fluid
2. Transducer - convert flow to a readable signal
ORIFICE METER IS:Restriction to create pressure drop
MAIN CHARACTERISTICS:- Simple construction - Easy duplicating- Extensive calibration work done- Adopted as standard
HOW DOES IT WORK?
-PRESSURE PROFILE UPSTREAM/DOWNSTERAM THE ORIFICE
-INCREASE OF FLUID VELOCITY IN VENA CONTARCTA
-PRESSURE RECOVERY 5 TO 8 D DOWNSTREAM
-PRESSURE LOSS
-DIFFERENTIAL PRESSURE PROPORTIONAL TO SQUARE OF THE RATE OF FLOW
HISTORY
- FIRST USE BY GIOVANNI VENTURI IN 1797
- MODERN VENTURI BY HERSCHEL 1886
- EXTENSIVE EXPERIMENTAL WORK BY AGA IN 1935
- MPMS 14-3 IS UPDATED VERSION OF AGA
- ISO 5167 IS INTERNATIONALLY ADDOPTED
GAS LAWS
- MOLECULA IS THE SMALLEST PARTICLE IN FREE AND UNDECOMPOSED STATE
- MOLECULES MOTION IMPACT IS MEASURED AS PRESSURE
- TEMPERATURE INFLENCE ON THE MOTION OF MOLECULAS
- AT ABSOLUTE ZERO PRESSURE AND TEMPERATURE THERE IS NO ACTIVITY
THE VOLUME OF IDEAL GAS IS:
- INVERSELY PROPORTIONAL TO THE ABSOLUTE PRESSURE (BOYLS LAW)
- DIRECTLY PROPORTIONAL TO THE ABSOLUTE TEMPERATURE (CHARLES LAW)
- THIS IS COMMONLY WRITTEN AS THE FOLLOWING EQUATION:
P1 x V1 / T1 = P2 x V2 / T2
ORIFICE GAS EQUATION:
QV = K x Cd x Ev x Y1 x d2 x (Tb / Pb) x
[(Pf1 x Zb x hw) / (Gr x Zf1 x Tf)]0.5
WHERE IS:
QV - STANDARD VOLUME FLOWRATECd - COEFFICIENT OF DISCHARGEEv - VELOCITY OF APPROACH FACTORY1 - EXPANSION FACTORd - ORIFICE PLATE BORE Tb - BASE TEMPERATUREPb - BASE PRESSUREPf1 - FLOWING PRESSURE UPSTREAMTf - FLOWING TEMPERATUREZb - COMPRESSIBILITY AT BASE CONDITIONSZf1 - COMPRESSIBILITY AT FLOWING (UP.) CONDITIONSHw - ORIFICE DIFFERENTIAL PRESSUREGr - REAL GAS RELATIVE DENSITY
ORIFICE PLATE COEFFICIENT OF DISCHARGE (Cd)
- EMPIRICALLY DETERMINED
- TO BE VALID THE ORIFICE MUST BE MANUFACTURED ACCORDING TO M.P.M.S
- DEPENDS ON THE REYNOLDS NUMBER, TAP LOCATION, METER TUBE DIAMETER AND ORIFICE DIAMETER
VELOCITY OF APPROACH FACTOR (EV)
- CORRECTS THE CHANGE IN VELOCITY BETWEEN THE UPSTREAM CONDITION AND THE VELOCITY IN THE ORIFICE BORE.
- DEPENDS ON BETA RATIO
EXPANSION FACTOR (Y1 OR Y2)
- CORRECTS THE DENSITY CHANGE BETWEEN THE MEASURING TAPS AND DENSITY AT THE ORIFICE PLANE
- Y1 OR Y2 DEPENDS IF THE STATIC PRESSURE IS MEASURED ON THE UPPSTRAEAM OR DOWNSTREAM TAP.
- Y2 IS SMALLER THAN Y1
ORIFICE PLATE BORE DIAMETER (d)
- ACTUAL DIAMETER AT FLOWING CONDITIONS
- CORRECTION MUST BE DONE IF THE TEMPERATURE AT WHICH THE PLATE WAS BORED IS DIFFERENT FROM THE OPERATING
GAS SPECIFIC GRAVITY (Gr)
- REPRESENTS A PHYSICAL CHARACTERISTICS OF THE GAS
- REPRESENTS THE RATIO BETWEEN THE DENSITY OF GAS DIVIDED BY AIR AT SAME CONDITIONS
- WITH GIVE FORCE MORE GAS WITH LOWER Gr IS PASING THROUGH AN ORIFICE
COMPRESSIBILITY (Zf)
- THE REAL GAS COMPRESS MORE THAN THE IDEAL GAS PREDICTS
- THE ABOVE RATIO IS CALLED COMPRESSIBILITY
- CALCULATED BY AGA 8
- ROUGHLY THE COMPRESSIBILITY AFFECTS THE VOLUME BY 0,5% EACH 100 PSIG
BETA RATIO ()
- IS THE RATIO OF ORIFICE BORE DIVIDED BY PIPE INTERNAL BORE
- THE LIMITS ARE 0.2 AND 0.7
CRITICAL FLOW
- OCCURS WHEN THE VELOCITY OF THE GAS OR VAPOR REACHES THE SPEED OF SOUND
- GAS CAN NOT TRAVEL ANY FASTER
- APPLICATION IN FLOW LIMITING DEVICES (RO)
- A RULE OF THUMB SAYS THAT CRITICAL FLOW OCCURS WHEN P2 IS LES THAN 50% OF P1
ADVANTAGES OF ORIFICE METERS
- FLOW CAN BE ACCURATELLY DETERMINED WITHOUT FLOW CALIBRATION
- ALL OTHER METERS REQUIRE FLOW CALIBRATION AT OPERATING CONDITIONS
- WELL ESTABLISHED PROCEDURES CONVERTS DIFFERENTIAL PRESSURE INTO FLOW RATE
- THE CALCULATION COEFFICIENTS ARE BASED ON ACCURATELY MEASURABLE DIMENSIONS
- SIMPLE, RUGGED, WIDELLY ACCEPTED, RELIABLE AND INEXPENSIVE
RELIABILITY
- THE COEFFICIENTS CALCULATED BY AGA 3 ARE SUBJECT TO UNCERTAINITY ON APPROX. 0.5%
- THIS IS FOR BETA FROM 0.2 TO 0.7
- FOR BETA BETWEEN 0.1 - 0.2 AND 0.7 - 0.75 THE ADDITIONAL UNCERTAINITY SHOULD BE ADDED.
- THE REYNOLDS NUMBER BELOW 1,000,000 WILL INCREASE UNCERTAINITY
- REYNOLDS NUMBER PRACTICAL LIMIT IS 4,000
RANGEABILITY
- CALLED ALSO "TURN DOWN RATIO" IS THE RATIO BETWEEN MAXIMUM AND MINIMUM MEASURABLE FLOW WITH DECLARED ACCURACY
- COMMON RANGEABILITY FROM 3 TO 1
- ADOPTING MULTIPLE DIFFERENTIAL PRESSURE TRANSMITTER (STACK) THE RANGEABILITY CAN BE INCREASED
REPEATABILITY
- THE METER CAPABILITY TO INDICATE THE SAME READING AT THE SAME FLOW
- THE READINGS MAY OR MAY NOT BE ACCURATE BUT CAN BE REPEATABLE
- THIS CAPABILITY IS IMPORTANT WHEN FLOW METER IS USED FOR FLOW CONTROL
PRESSURE LOSS CHARACTERISTICS
1. ORIFICE - HIGHEST
2. FLOW NOZZLE
3. SHORT CONE VENTURI
4. STANDARD VENTURI
5. LO-LOSS TUBE
ORIFICE PLATE TYPES
- CONCENTRIC ORIFICE, SQUARE EDGE - STANDARD
- ECCENTRIC ORIFICE PLATE - FOR GASES WITH LIQUIDS OR LIQUIDS WITH SEDIMENTS
- QUADRANT EDGE - HIGH VISCOSITY FLUIDS
- CONIC EDGE - AT REYNOLDS NUMBERS LOWER THAN FOR QUADRANT EDGE
PRESSURE TAP LOCATION
- FLANGE TAPS - ONE INCH UP AND DOWNSTREAM FROM THE ORIFICE FACE
- PIPE TAPS - 2,5D UPSTREAM AND 8D DOWNSTREAM AT POINT OF MAXIMUM PRESSURE RECOVERY
- VENA CONTRACTA TAPS - 1D UPSTREAM AND AT THE POINT OF MINIMUM PRESSURE DOWNSTREAM
- CORNER TAPS - ADJACENT TO THE PLATE FACES
ORIFICE PLATE HOLDERS
- ORIFICE FLANGES
- SENIOR ORIFICE FITTING
- JUNIOR ORIFICE FITTING
- SIMPLEX ORIFICE HOLDER
- METER TUBES