Smart DP Flow Metering - tuv-sud.co.uk · Square Edged Orifice Plate •ISO 5167-2 •βrange 0.1...
Transcript of Smart DP Flow Metering - tuv-sud.co.uk · Square Edged Orifice Plate •ISO 5167-2 •βrange 0.1...
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Smart DP Flow MeteringA summary of Established Technology and Latest Innovation
Gary Fish
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DP Flow Measurement
• Established Technology
• Large range of line sizes, materials, connection interfaces, etc
• Customised solutions
• New innovations and improvements
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Square Edged Orifice Plate
• ISO 5167-2
• β range 0.1 to 0.75
• Min ReD 5 x 103
• Max ReD ∞
• Permanent Pressure loss: β dependent between 42% and 98% of ΔP
• Uncalibrated Uncertainty Cd 0.5% (for β between 0.2 & 0.6)
• General Flow metering applications- gas allocation and fiscal standard
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Conical Entrance Orifice Plate
• ISO TR 15377
• β range 0.1 to 0.316
• Min ReD 80
• Max ReD 6.3 x 104 (for β 0.316)
• Uncalibrated Uncertainty Cd 2%
• Application – viscous fluids
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Quarter-Circle Orifice Plate
• ISO TR 15377
• β range 0.245 to 0.6
• Min ReD 245 (for β 0.245)
• Max ReD 6 x 104 (for β 0.6)
• Uncalibrated Uncertainty Cd 2% to 2.5%
• Application – viscous fluids
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Eccentric Orifice Plate
• ISO TR 15377
• β range 0.46 to 0.84
• Min ReD 4.2 x 103
• Max ReD 8.4 x 105
• Uncalibrated Uncertainty Cd 1% to 2% (can be calibrated to improve)
• Application – entrained gas in liquid service, entrained liquid in gas service, sediments, etc
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ISA 1932 Nozzle
• ISO 5167-3
• β range 0.3 to 0.8
• Min ReD 2 x 104 (for β 0.44 or greater)
• Max ReD 1 x 107
• Uncalibrated Uncertainty Cd 0.8% to 1.2% (β dependent)
• Permanent Pressure loss: between 25% and 80% of ΔP (typical)
• high velocity, steam flow.
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Long Radius Nozzle
• ISO 5167-3
• β range 0.2 to 0.8
• Min ReD 1 x 104
• Max ReD 1 x 107
• Uncalibrated Uncertainty Cd 2%
• Permanent Pressure loss: between 24% and 92% of ΔP (typical)
• high velocity, steam flow.
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• ISO 5167-3
• β range 0.316 to 0.775
• Min ReD 1.5 x 105
• Max ReD 2 x 106
• Uncalibrated Uncertainty Cd 1.2% to 1.7%
• Permanent Pressure loss: between 5% and 20% of ΔP (typical)
• high velocity, steam flow. Low permanent pressure loss
Venturi Nozzle
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• ISO 5167-4
• β range 0.4 to 0.75
• Min ReD 2 x 105
• Max ReD 1x 106
• Uncalibrated Uncertainty Cd 1% (for ReD limits shown)
• ReD limits increased according to Annex B – with increased uncertainty
• Permanent Pressure loss: between 5% and 20% of ΔP
• General Flow metering applications- gas allocation, high velocity, low maintenance and intervention. Low permanent pressure loss.
Machined Venturi
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• ISO 5167-4
• β range 0.4 to 0.7
• Min ReD 2 x 105
• Max ReD 2 x 106
• Uncalibrated Uncertainty Cd 1.5% (for ReD limits shown)
• ReD limits increased according to Annex B – with increased uncertainty
• Permanent Pressure loss: between 5% and 20% of ΔP
• General Flow metering applications- gas allocation, high velocity, low maintenance and intervention. Low permanent pressure loss.
Fabricated Venturi
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‘As Cast’ Venturi
• ISO 5167-4
• β range 0.3 to 0.75
• Min ReD 2 x 105
• Max ReD 2 x 106
• Uncalibrated Uncertainty Cd 0.7% (for ReD limits shown)
• ReD limits increased according to Annex B – with increased uncertainty
• Permanent Pressure loss: between 5% and 20% of ΔP
• General Flow metering applications- gas allocation, high velocity, low maintenance and intervention. Low permanent pressure loss.
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Cone Meter
• ISO 5167-5
• β range 0.45 to 0.75
• Min ReD 8 x 104
• Max ReD 1.2 x 107
• Uncalibrated Uncertainty Cd 5%
• Permanent Pressure loss: between 48% and 72% of ΔP (typical)
• General Metering applications, allocation, shorter overall installation than Venturi meter
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• ISO 5167-6 (not yet published)
• β range 0.377 to 0.791
• Min ReD 1 x 104 note 1
• Max ReD 9 x 106
• Uncalibrated Uncertainty Cd 4%
• Permanent Pressure loss: between 47% and 79% of ΔP (typical)
• Suspended solids, viscous fluids note 1
Note 1 : Standard will be based upon available data – Wedge Meters have been known to operate at
Re =500, but will require calibration- resulting in much lower uncertainty also.
Wedge Meter
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Dall Tube
• No International Standard
• β range 0.3 to 0.8
• Min ReD 5 x 104
• Max ReD∞
• Uncalibrated Uncertainty Cd 3%
• Permanent Pressure loss: between 2.5% and 8% of ΔP (typical)
• Clean process fluids, very low pressure loss requirements
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Comparison table for DP Devices
Device Standard
Limits of use
Uncertainty Permanent PressureLine Size (mm) β ReD
Min Max Min Max Min Max
Cd
(UNCALIBRATED)
loss (% of ΔP)
SQUARE EDGED ORIFICE PLATE ISO 5167-2 50 1000 0.1 0.75 5 x 103 ∞ 0.5% NOTE 1 42% to 98%
CONICAL ENTRANCE ORIFICE
PLATEISO TR 15377 25 500 0.1 0.316 80 6.3 x 10
4
2% 86% to 98%
QUARTER-CIRCLE ORIFICE PLATE ISO TR 15377 25 500 0.245 0.6 245 6 x 104
2% to 2.5% 53% to 91%
ECCENTRIC ORIFICE PLATE ISO TR 15377 100 1000 0.46 0.84 4.2 x 103
8.4 x 105
1% to 2% 36% to 77%
ISA 1932 NOZZLE IS0 5167-3 50 500 0.3 0.8 2 x 104
1 x 107
0.8% to 1.2% 25% to 83%
LONG RADIUS NOZZLE ISO 5167-3 50 630 0.2 0.8 1 x 104
1 x 107
2% 24% to 92%
VENTURI NOZZLE ISO 5167-3 65 500 0.316 0.775 1.5 x 105
2 x 106
1.2% to 1.7% 5% to 20%
MACHINED VENTURI ISO 5167-4 50 250 0.4 0.75 2 x 105
1 x 106
1% 5% to 20%
FABRICATED VENTURI ISO 5167-4 200 1200 0.4 0.7 2 x 105
2 x 106
1.50% 5% to 20%
AS CAST' VENTURI ISO 5167-4 100 800 0.3 0.75 2 x 105
2 x 106
0.70% 5% to 20%
CONE METER ISO 5167-5 50 500 0.45 0.75 8 x 104
1.2 x 107
5% 48% to 72%
WEDGE METER ISO 5167-6 NOTE 2 50 600 0.377 0.791 1 x 104
9 x 106
4% 47% to 79%
DALL TUBE NO STANDARD 150 3000 0.3 0.8 5 x 104 ∞ 3% 2.5% to 8%
Notes
1 For β between 0.2 and 0.6
2 Not yet published
All Cd Uncertainties can be reduced with flow calibration over entire operating range
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Upstream Straight Length requirements – 1off 90o bend
Upsteam lengths may be reduced with Cd
uncertainties increasing
Generic DP Device βlim
L βlim
L
ORIFICE 0.1 6D 0.75 44D
NOZZLE 0.2 10D 0.8 46D
VENTURI 0.3 8D 0.75 16D
CONE METER 0.45 3D 0.75 6D
WEDGE METER 0.377 7D 0.791 7D
DALL TUBE 0.3 3D 0.8 13D
β L
0.5 22D
0.5 14D
0.5 9D
0.5 3D
0.5 7D
0.5 4D
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Upstream Straight Length requirements – 1off 90o bend
Generic DP Device Uncalibrated C
dUncertainty β L
ORIFICE (Square edged) 0.50% 0.5 22D
NOZZLE (ISA 1932) 0.80% 0.5 14D
VENTURI (Machined) 1.00% 0.5 9D
CONE METER 5% 0.5 3D
WEDGE METER 4% 0.5 7D
DALL TUBE 3% 0.5 4D
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Upstream Straight Length requirements – 1off 90o bend
Generic DP Device Uncalibrated C
dUncertainty β L
ORIFICE (Square edged) 1.0% 0.5 9D
NOZZLE (ISA 1932) 1.3% 0.5 7D
VENTURI (Machined) 1.5% 0.5 3D
CONE METER 5%* 0.5 3D*
WEDGE METER 4%* 0.5 7D*
DALL TUBE 3.5% 0.5 3D
*No data published in ISO regarding shorterlength uncertainty
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Differential Pressure Transmitter Technology
• Largest contribution to enhanced DP meter uncertainty in recent years
• Example 1 :
• Yokogawa EJX130A, ref accuracy :+/-0.04% of span (3σ)
• Example 2:
• Rosemount 3051CD (ranges 2-4), ref accuracy :+/-0.04% of span (3σ)
• Full ‘transparent’ uncertainty analysis can be carried out for DP meters
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DP Meter Uncertainty Analysis
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Myth : The Differential Pressure is limited to 500mbar for an orifice plate
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Limits for Orifice Plate DP
• End User/Operator specifications stating for instance DP limited to 500mbar
• Why ?
• There is no need – providing :
• Permanent Pressure loss is acceptable
• Orifice Plate Elastic or Plastic Deformation is considered
• DP is within expansibility limits
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Myth : The flow turndown for DP devices is only 3:1
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For mass flow uncertainty below 0.8% we need the DP uncertainty <1%.
Turndown/rangeability is the ratio of the largest to smallest flow rate that can be metered to the meter’s stated flow rate prediction uncertainty at a stated confidence level.
Claim / belief: “You only get 3:1 with an orifice”
Turndown / Rangeability
…With 1 DP Transmitter[200 , 2000] = 10:1 on DP~3.2:1 flow range
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Example : 30m/s, 25kg/m3, 12” pipe ~260,000 Sm3/hBeta = 0.6, DP = ~2000mbar
DP H: 0-2000mbarDP M: 0-300mbarDP L: 0-50mbar
Turndown / RangeabilityExample, stacked transmitters
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30m/s, 25kg/m3, 12” pipe 260,000Sm3/hBeta = 0.6, DP = ~2000mbar
DP H: 0-2000mbarDP M: 0-300mbarDP L: 0-50mbar
min: 30% of max flow -> 3.3:1 min: 11% of max flow -> 9.1:1min: 4.5% of max flow -> 22:1
Turndown / RangeabilityExample, stacked transmitters
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Turndown / Rangeability
+/-0.8%
0 m/s
100% of flow rate(30 m/s)
+/-0.8%
0 m/s
100% of flow rate(30 m/s)
4.5% of flow rate(1.35 m/s)
100%/3.3% = 30i.e. ‘turndown = 30:1’
100%/4.5% = 22i.e. ‘turndown = 22:1’
e.g. USM
e.g. Orifice
Claim / belief: “You only get 3:1 with an orifice”
?3.3% of flow rate(1 m/s)
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Turndown / Rangeability
+/-0.8%
0 m/s
100% of flow rate(30 m/s)
3.3% of flow rate(1 m/s)
+/-0.8%
0 m/s
100% of flow rate(30 m/s)
4.5% of flow rate(1.35 m/s)
100%/3.3% = 30i.e. ‘turndown = 30:1’
100%/4.5% = 22i.e. ‘turndown = 22:1’
e.g. USM
e.g. Orifice
Difference? 30:1 from 22:1 is an increase in flow range of (1.2/95.5) 1.26%
Claim / belief: “You only get 3:1 with an orifice”
Similar Turndown to USM in practice
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Turndown / Rangeability• Later life example. Reduced Pressure and Flow
• E.g. Max flow: 3 m/s, (i.e. 15,500 Sm3/h)
• USM fixed at ≈ 30 m/s > U (m/s) > 1 m/s, (10% of USM full scale flow).
• 0.6β orifice meter produces 12mbar, (8% of orifice meter full scale flow).
• Easy improvement :change the beta
• 0.2β orifice meter produces 1150mbar
1150 ≥ DP mbar ≥ 5 gives 3 ≥ U (m/s) ≥ 0.2 150:1
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Myth : The permanent pressure loss is always too high with DP devices
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Permanent Pressure Loss
Higher PPL may sometimes be significant, but meter PPL should be seen in context.
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Permanent Pressure Loss
12”, sch 40 gas (ordinary) pipe
• 40 Bar, 150C, 31.8 kg/m3, 15 m/s, 140 MMSCFD
Components in pipe:
• Globe valve (3/4 open) for control
• Open butterfly valve (emergency shut off)
• 4 elbows, T-junction, sample probe, 2 thermowells
• A flow conditioner & flow meter
What is the PPL across the system? What relative impact on overall PPL does the meter system have?
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Permanent Pressure Loss
2*
2
avlossloss
VKP
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Permanent Pressure Loss
2*
2
avlossloss
VKP
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Permanent Pressure Loss
2*
2
avlossloss
VKP
• The PPL is dependent on the length of pipe.
• Most pipe systems are long, that’s why it’s convention to call pipe loss the ‘major’ loss!
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Permanent Pressure Loss
• Often pipe losses dwarf any meter PPL.
(Gas transmission compressor stations are > 40 miles apart, platform to shore is miles long etc.)
• Other calibrated DP devices can offer the measurement accuracy requirements and low pressure losses – eg Venturi, Dall tube, etc
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Myth : DP devices don’t have diagnostic capabilities
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Validation / Diagnostics• Combination of advancement in transmitter technology and specialised
innovative developments the following diagnostics are available for DP meters
• Incorrect Metrology Data• Excessive Flow Disturbance• Contamination Build Up• Saturated DP Tx• Drifting DP Tx• Incorrectly Spanned DP Tx• DP Below Tx Range• Two Phase Flow• Electrical Loop Integrity• Plugged Lines• Process Leakage• Improved Overall Safety Integrity• Etc,Etc..
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Validation / Diagnostics - Orifice
Excellent diagnostics – No calibration required.
• 3 x Flow Rate Comparisons• 3 x DP Ratio Comparisons• 1 x DP Integrity Check• DP Synchronisation / turbulence checks
Reasonably objective
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Thankyou ! : Questions ?