Rosemount Annubar Primary Flow Element Flow Test Data Book Manuals & Guides

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Reference Manual

Rosemount 485 Annubar Rosemount 585 Annubar

00821-0100-4809, Rev BA July 2009

Rosemount Annubar® Primary Flow Element Flow Test Data Book

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Reference Manual

00821-0100-4809, Rev BA July 2009

Rosemount Annubar

Flow Test Data Book

Rosemount Annubar Primary Flow Element Flow Test Data Book

NOTICE

Read this manual before working with the product. For personal and system safety, and for optimum product performance, make sure to thoroughly understand the contents before installing, using, or maintaining this product.

Customer Central

1-800-999-9307 (7:00 a.m. to 7:00 P.M. CST)

National Response Center

1-800-654-7768 (24 hours a day) Equipment service needs

International

1-(952) 906-8888

The products described in this document are NOT designed for nuclear-qualified applications.

Using non-nuclear qualified products in applications that require nuclear-qualified hardware or products may cause inaccurate readings.

For information on Rosemount nuclear-qualified products, contact an Emerson Process Management Sales Representative.

. .

Fisher-

Rosemount satisfies all obligations coming from legislation to harmonize product

requirements in the European Union

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Reference Manual

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Rosemount Annubar

Flow Test Data Book

SECTION 1 Annubar Technology

SECTION 2 How the Annubar Works

SECTION 3 Flow Coefficient Reynolds Number Independence

SECTION 4 Annubar Flow Theory

Rosemount Annubar Primary Flow Element. . . . . . . . . . . . . . . . . . . . . . . . . . . .1-1

Testing. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .1-1

Mechanical and Structural Testing . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .1-2

In-House Performance Testing . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .1-2

Independent Laboratory Testing . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .1-2

On-Site Performance Tests. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .1-2

Rosemount Annubar Flow Element Test Advantages. . . . . . . . . . . . . . . . . .1-2

Overview. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .2-1

Design and Performance . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .2-2

Rosemount 485 Annubar Sensor Design . . . . . . . . . . . . . . . . . . . . . . . . . . .2-2

Rosemount 585 Annubar Sensor Design . . . . . . . . . . . . . . . . . . . . . . . . . . .2-5

Flow Coefficient Overview . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .3-1

Benefits. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .3-1

Rosemount Annubar Reynolds Number Ranges . . . . . . . . . . . . . . . . . . . . . . . .3-2

Nomenclature . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .4-1

Flow Equation Derivation . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .4-2

Blockage Equation Derivation. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .4-3

Conclusion . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .4-5

SECTION 5 Test Facilities and Procedures

SECTION 6 References

Overview. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .5-1

Testing Laboratories. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .5-1

Rosemount Boulder, Colorado Flow Laboratory . . . . . . . . . . . . . . . . . . . . . .5-1

Alden Research Laboratories (ARL) . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .5-1

SwRI Gas Research Institute (GRI), Meter Research Facility (MRF) . . . . . .5 -1

Utah Water Research Laboratories (UWRL). . . . . . . . . . . . . . . . . . . . . . . . .5-1

Colorado Engineering Experimental Sation Inc (CEESI). . . . . . . . . . . . . . . .5-1

Gravimetric Procedure . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .5-2

Testing Performed by Sensor Size. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .5-3

485 Sensor Size 1 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .5-4

485 Sensor Size 2 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .5-10

485 Sensor Size 3 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .5-26

585 Sensor Size 11 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .5-28

585 Sensor Size 22 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .5-39

585 Sensor Size 44 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .5-49

TOC-1

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Rosemount Annubar Flow Test Data Book

Reference Manual

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TOC-2

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Flow Test Data Book

Section 1 Annubar Technology

Rosemount Annubar Primary Flow Element . . . . . . . . . .page 1-1

Rosemount Annubar Flow Element Test Advantages . . .page 1-2

The Rosemount Annubar primary flow element maintains the traditional strengths of Averaging Pitot Tubes (APTs) with improved performance. The strengths of the Rosemount Annubar include:

• Low permanent pressure loss

• A flow coefficient independence of Reynolds number

• Simple installation, including a gear drive insertion and retraction device

• The highest signal to noise ratio of any APT (Model 485)

• 485 Uncalibrated Accuracy: ±0.75%

• 485 Calibrated Accuracy: up to ±0.5%

• 585 Uncalibrated Accuracy: ±1.50%

• 585 Calibrated Accuracy: up to ±0.5%

• Integral temperature measurement

• Direct transmitter mounting capability

ROSEMOUNT ANNUBAR PRIMARY FLOW ELEMENT

The Rosemount 485 Annubar primary flow element is the fifth generation Annubar. This design is comprised of three separate tubes that are drawn to produce a unique geometrical shape that produces a high and low pressure signal and contains an integral thermowell. The geometry change to the sensor required testing to establish a characterization curve and to determine a new flow coefficient.

The Rosemount 585 Annubar primary flow element is machined from a single piece of barstock in a diamond shape with sharp edges to produce a flow coefficient that is more linear to Reynold’s number than other designs.

Testing Tests performed on the Annubar primary flow elements are divided into five

major categories:

• Research and development testing

• Mechanical and structural testing

• In-house performance testing

• Independent laboratory testing

• On-site performance testing

All categories are on-going and continue to be a part of the current Emerson test program for the Annubar primary flow ele m en ts.

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Rosemount Annubar Flow Test Data Book

Mechanical and Structural Testing

Material and structural testing at:

Reference Manual

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July 2009

Rosemount performed mechanical and structural testing 485 585

Material hardness X Moments of inertia X X Fatigue life X X Fluid loading due to lift and drag forces X Static bend tests X Allowable stress limits X X Failure analysis X X Vibration analysis X X

• Hauser Laboratories

• MicroMotion Laboratory

• Eden Prairie Flow Laboratory

In-House Performance Testing

Independent Laboratory Testing

On-Site Performance Tests

ROSEMOUNT ANNUBAR FLOW ELEMENT TEST ADVANTAGES

Hundreds of flow tests were perfor med in the Em erson flow laborator y in 2-in. to 12-in. pipeline, using independently certified magnetic meters as primary reference meters. Baseline K-values, sign al no ise , cavitation, high and low Reynolds number limitations, methods of installations, static modeling, and straight-run requirements are just a few of the in- house performance tests th at were performed on the Rosemount Annubar primaries.

Rosemount Annubar primary flow element models were tested at four independent laboratories:

• Alden Research Laboratory (ARL)

• Colorado Engineering Experiment Station, Inc. (CEESI)

• Southwest Research Institute (SwRI)

• Utah Water Research Lab (UWRL)

Certified flow-data sheets were supplied from each of these facilities in pipelines ranging from 2-in. to 24-in. over a wide range of Reynolds number s. A representative sample of independent tests conducted at Emerson and independent laboratories are Section 5: Test Facilities and Procedures.

Emerson Process Management has a field service department that performs on-site performance tests and in-line calibrations for customers with unique installations or applications.

Emerson test procedures incorporat e th e follo win g criter ia and adv an tages:

• Flow test data were collected over a flow turndown range of 10:1 in most cases

• All coefficients are ±0.75% (95% confidence) of the published K-value of a particular 485 Annubar flow element.

• All coefficients are ±1.50% (95% confidence) of the published K-value of a particular 585 Annubar flow element.

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Reference Manual

QKDP

Flow

Stagnation Pressure

Impact

Pressure

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Rosemount Annubar

Flow Test Data Book

Section 2 How the Annubar Works

Overview . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .page 2-1

Design and Performance . . . . . . . . . . . . . . . . . . . . . . . . . . page 2-2

OVERVIEW The Rosemount Annubar primary flow element is a device used to measure

the flow of a liquid, gas or steam fluid that flows through a pipe. It enables flow measurement by creating a differential pressure (DP) that is proportional to the square of the velocity of the fluid in the pipe, in accordance with Bernoulli's theorem. This DP is measured and converted int o a fl ow rate usin g a secondary device, such as a DP pressure transmitter.

The flow is related to DP through the following relationship.

Equation 2-1

where:

Figure 2-2. Cross Section of the Rosemount 485 Annubar in a Flow Stream

Q = Flow Rate K = Annubar Flow Coefficient DP = Differential Pressure

For a more complete discussion on the flow equation, refer to Section 4: Annubar Flow Theory.

The Annubar generates a DP by creating blockage in the pipe and acting as an obstruction to the fluid. The velocity of the fluid is decreased and stalled as it reaches the front surface the Annubar sensor, creating the impact/high pressure.

The Rosemount Annubar senses the impact pressure by utilizing either a frontal slot (485) or sensing hole (585) design, which opens into the high pressure chamber. This high pressure chamber connects directly into the DP transmitter for measurement.

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Rosemount Annubar

DP PHPL–=

Thermowell

Low Pressure Plenum

Low Pressure Plenums

High Pressure

Plenum

Flow Test Data Book

Figure 2-3. Cross Section of the Rosemount 585 Annubar in a Flow Stream

As the fluid continues around the Annubar sensor, it creates a lower velocity profile on the backside of the sensor, creating the low/suction pressure downstream of the Annubar. Individual ports, located on the backside of the Annubar sensor measure this low pressure. Working on the same principle as the high pressure, an average low pressure is maint aine d in th e lo w pr essure chamber that connects directly into the transmitter for measurement.

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July 2009

DESIGN AND PERFORMANCE

Rosemount 485 Annubar Sensor Design

Figure 2-5. Cross-Section of the Rosemount 485 Annubar

The resultant differential pressure is the difference between the impact (high) pressure reading and the suction (low) pressure reading as seen below.

Equation 2-4

where: PH = High Pressure PL = Low Pressure

The 485 Annubar is T-shaped in design and is constructed in three scaled sizes for use in a wide range of pipe diameters. Its design includes a single high-pressure plenum, three common low-pressure plenums, and an integral thermowell.

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Upstream slot for accurate averaging

Seal weld between high pressure and low pressure plenums

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Rosemount Annubar

Flow Test Data Book

Differential Pressure (DP) Signal

The T-shaped design of the 485 Annubar generates more differential pressure than any APT. The flat upstream surface of the sensor is perpendicular to the direction of flow, which results in a high and very stable drag coefficient. Since the flow coefficient, or k factor (see Equation 2-1), is a function of the drag coefficient, this produces a large, repeatable and predictable DP signal for a given velocity.

The magnitude of the DP signal is directly related to measurement accuracy and the amount of primary element turndown, particularly at lower flow rates. One traditional limitation of APT technology is that accuracy degrades at lower flow rates as a result of the minimal DP produced. The Rosemount 485 extends the lower range limit that an APT can measure and maintain performance as a result of the additional DP generated.

Impact (High) Pressure Measurement

As mentioned in the “Overview” on page 2-1, the Rosemount 485 Annubar measures the impact (high) pressure with a frontal slot design. The laser cut slots extend across the entire front surface of the sensor to maximize the amount of the velocity flow profile measured and increase the accuracy o f the measurement. Multiple slots are used to maintain the structura l integrity of the bar. A seal weld is visible around the perimeter of th e slots and is u sed to seal the high pressure chamber from the low pressure chamber to prevent any leakage potential. Testing revealed that the raised surface of the weld does not have any effect on performance so it is not removed.

Figure 2-6. Rosemount 485 Frontal Slot Design

The patented slot design replaces sensing ports used by traditional APTs. This slot “integrates” the velocity flow profile and improves the accuracy of the measurement. By “integrating” the flow profile, a consistent series of data is recorded across the pipe diameter instead of limited samples taken at a few discreet points. By increasing the number of samples taken across the pipe of the actual flow rate, the accuracy of the measurement is improved.

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Rosemount Annubar

Stagnation

Zone

Short Arrows Indicate Low Velocities

Boundary Layer Separation Point

Long Arrows Indicate High Velocities

Flow Test Data Book

Suction (Low) Pressure Measurement

The Rosemount 485 Annubar measures the suction (low) pressure with sensing ports located in stagnation zones on the backside of the sensor. As the fluid comes into contact with the 485 Annubar sensor and separates from the front edges, the velocity and turbulence level of the fluid in the area directly behind the sensor is greatly decreased. The low velocity and turbulence level in this stagnation zone significantly reduces any pressure variation in this region. Individual sensing ports are drilled in this location to detect the suction (low) pressure.

The number of ports located on the backside of a given sensor is a fun ction of pipe size and mathematically determined by the same Cheb yshev principles of previous Annubar designs.

Figure 2-7. Velocity Graph

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2-4

Surface Texture

As the flow over any surface in the flow stream is increased, the character of the fluid flow near that surface goes through a transition. At a certain critical flow rate, the level of turbulence in this region, termed the boundary layer, increases sharply. This increase in turbulence in the boundary layer on the front surface of the 485 Annubar causes a marked change in the separation of the flow at the edge, which in turn affects the accuracy of the differential pressure signal. The transition from the non-turbulent (laminar) to a turbulent boundary layer condition is an inescapable fact described by the principles of fluid dynamics. However, it has been found that altering the roughness or texture of the surface adjacent to the boundary layer can control the flow at which that transition takes place.

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Reference Manual

Low Pressure Plenums

High Pressure

Plenum

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Rosemount Annubar

Flow Test Data Book

The front surface of the 485 Annubar sensor is tailored to the customer's flow application. In high flow applications (where the maximum expected flow exceeds one million Reynolds number), the surface is textured to increase the level of turbulence at a given flow rate. This ensures that the transition from laminar to turbulent flow in the boundary layer occurs at flows below (and outside) the customer's measurement ra nge. For lower flow applications, the surface is left smooth to maintain a laminar boundary layer forcing the transition to occur above the maximum flow that will be seen in the application.

Rosemount 585 Annubar Sensor Design

Figure 2-8. Cross-Section of the Rosemount 585 Annubar

The 585 Annubar is diamond-shaped in design and is constructed in three scaled sizes for use in a wide range of pipe diameters.

Reynolds Number Considerations

As the flow over any surface in the flow stream is increased, the character of the fluid flow near that surface goes through a transition. At a certain critical flow rate, the level of turbulence in this region, termed the boundary layer, increases sharply. This increase in turbulence in the boundary layer on the front surface of the 585 Annubar causes a marked change in the separation of the flow at the edge, which in turn affects the accuracy of the differential pressure signal. The transition from the non-turbulent (laminar) to a turbulent boundary layer condition is an inescapable fact described by the principles of fluid dynamics. However, on the 585 model, the sharp edges on the side of the Annubar produce a more consistent separation point, resultin g in a flow coefficient that is linear over the entire range of pipe reynolds numbers that are typically encountered in flow measurement applications.

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Rosemount Annubar Flow Test Data Book

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Flow Test Data Book

Section 3 Flow Coefficient Reynolds

Number Independence

Flow Coefficient Overview . . . . . . . . . . . . . . . . . . . . . . . . . page 3-1

Benefits . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . page 3-1

Rosemount Annubar Reynolds Number Ranges . . . . . .page 3-2

FLOW COEFFICIENT OVERVIEW

The flow coefficient (K–factor) is the ratio of the actual flow rate to the calculated (theoretical) flow rate. The accuracy of the Rosemount Annubar relates directly to the flow coefficient. The flow coefficient is empirica lly determined by testing a representative sample of flowmeters to establish the relationship between flowrate and the DP induced across the primary element.

This sampling of flow coefficients is generally plotted as a function of key flow-meter variables. For averaging pitot tubes, flow coefficients are plotted against the meter's pipe blockage.

Curve-fitting techniques are used to generate an equation that best fits the sampling of flow coefficients. This curve-fit equation becomes the basis for a manufacturer's published flow coefficients. These published flow coefficients are used for flowmeters in nearly all untested conditions.

Rosemount has supplemented the flow coeffi cient equations discussed above with the blockage equation derived in Section 4 of this document. This blockage equation defines a relationship between flow coefficient and blockage that substantiates the results of empi rical testing. Extensive APT testing conducted by Rosemount over the past 35 years support the theoretical equation.

BENEFITS The K-factor of an Annubar is a function of the blockage the probe present s to

the flow stream. The flow coefficient of many other primary elements is a function of Reynolds number. This characteristic of Annubar performance offers significant benefits over other pr imary elements.

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K-factor independence can be attributed to a constant separation point at the edges of the Annubar and to the probe's ability to take a proper average. Thus:

• It allows measurement of a wide range of Reynolds numbers without a correction factor for changing Reynolds numbers.

• Any variations in the K-factor with changing Reynolds number are due to scatter and fall within ±0.75% of the published K-value for the 485 Annubar.

• Any variations in the K-factor with changing Reynolds number are due to scatter and fall within ±1.50% of the published K-value for the 585 Annubar.

Page 16

Rosemount Annubar

dV



--------------------- -=

Flow Test Data Book

The K-to-blockage theoretical link demonstrates a higher degree of confidence in Rosemount Annubar K-factors than shown by flowmeters that use only an empirical database to determine flow coefficients. Rosemount is the first company to identify and use theoretical equations linking self-averaging pitot-tube flow coefficients to pipe blockage.

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July 2009

ROSEMOUNT ANNUBAR REYNOLDS NUMBER RANGES

Table 3-1. Rod Reynolds Number Lower Limits

For a Rosemount Annubar to operate accurately, the flowing media must travel at a velocity sufficient to separate from the edges of the Annubar.

Drag coefficients, lif t coeffic ients, sep aration point s, and pressure distributions around bluff bodies are best de scribed by “rod” Reynolds numbers. There is a minimum rod Reynolds number at which the flowing fluid will not properly separate from the edges of the T shape. The rod Reynolds number can be calculated using Equation 3-1.

Equation 3-1

where: d = Probe Width (feet or meters) V = Velocity of fluid (ft/sec or meters/second)  = Density of fluid (lbm/ft

or kg/m3)

 = Viscosity of fluid (lbm/ft-sec or kg/meter-sec) Minimum rod Reynolds numbers for the Ro se mou nt Annub ar can be fou nd in

Table 3-1.

Sensor Size Minimum Rod Reynolds Number (Rd) Probe Width (d)

feet meters

485 Annubar

1 6500 0.0492 0.0150 2 12500 0.0883 0.0269 3 25000 0.1613 0.0491

585 Annubar

11 6500 0.0667 0.0203 22 10000 0.1000 0.0305 44 25000 0.1900 0.0579

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Reference Manual

cross-sectional area of sensor

cross-sectional area of pipe

Actual Flow Rate (QA)

Theoretical Flow Rate (Q

)

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Flow Test Data Book

Section 4

Annubar Flow Theory

Nomenclature . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . page 4-1

Flow Equation Derivation . . . . . . . . . . . . . . . . . . . . . . . . . .page 4-2

Blockage Equation Derivation . . . . . . . . . . . . . . . . . . . . . . page 4-3

Conclusion . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . page 4-5

Annubar flow equations are built on basic hydraulic principles. The theoretical link to these concepts increases confidence in an Annubar measurement when compared to other measurement s that are based solely on empirical data.

NOMENCLATURE The following symbols are used in the derivation of the flow equation and the

blockage equation: A = cross sectional area of the pipe B = blockage ratio = C

= integration constant

f(B) = function of blockage h

= differential pressure caused by blockage

h

= differential pressure caused by shape of sensor

h = total differential pressure = h gc = gravitational constant K

= flow coefficient =

P = fluid pressure Q

= actual flow rate

= theoretical flow rate

V = average fluid velocity  = fluid density z = height above an arbitrary datum plane Unless noted otherwise, subscript 1 denotes an upstream condition and

subscript 2 denotes a downstream or throat co nditio n.

+ h

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Page 18

Rosemount Annubar

---------



------ gcz

---------



------ gcz

++=

P1P2–



------------------------

h

1P2

–



-------------------=

2gch=

QaKAAV=

QaKAA12gch=

Flow Test Data Book

Reference Manual

00821-0100-4809, Rev BA

July 2009

FLOW EQUATION DERIVATION

The flow equation relates the DP induced across a primary element to the velocity of the fluid in the pipe. As with other differential-pressure flowmeters, Rosemount Annubar equations are based on the Bernoulli equation:

Equation 4-1

For incompressible fluids  element are negligible so z

= 2. Changes in elevation around a primary

= z2.

Also, assume the velocity just within the mouth of the impact-sensing ports is zero, (V

= 0). While minor circulation may occur within the high pressure

chamber of the Rosemount Annubar, this flow is extremely small and may be considered negligible.

Solving for V

yields:

Equation 4-2

The net differential pressure produced can be rewritten as:

Equation 4-3

Substituting Equation 4-3 into Equation 4-2 yields:

Equation 4-4

Like the orifice plate and venturi meter, the general equation describing the actual flow in a pipe for the Rosemount Annubar is:

Equation 4-5

In Equation 4-4, V

is the average velocity of the fluid traveling past the

sensor on the downstream side; whereas, in Equation 4-5, V is the average velocity in the pipe. Differences between these two velocities (V absorbed in the flow coefficient (K

and V) are

Combining Equation 4-4 and Equation 4-5 yields:

Equation 4-6

Equation 4-6 is the flow equation used to relate differential pressure induced across the primary element to flow rate for the Rosemount Annubar.

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Reference Manual

KAfB=

h

P1P2–



------------------------

---------

–==

A1V11A2V2

------

A21B–A

1B–

------------ -





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Rosemount Annubar

Flow Test Data Book

BLOCKAGE EQUATION DERIVATION

Because the flow coefficient compensates for the difference between V2 and V, it must be recognized that (K obstructed area the sensor itself causes in the pipe. More specifically, (K

) will be a function of the amount of

) is

a function of the sensor's blockage in the pipe.

Equation 4-7

This is analogous to the velocity-of-approach factor for an orifice plate or a venturi meter. The following derivation uniquely determines f(B) in Equation 4-7. Discussion is limited to fluid flows in the turbulent regime for which Rosemount Annubar flow measurement is intended. Development of the equations applies to primary flow elements that are geometrically similar.

Beginning with Equation 4-6, the differential pressure produced by a primary flow element can be dissected into two parts:

•

Differential pressure due to the primary flow element's blockage (h

•

Differential pressure due to the shape o f the primar y flow element (h

Focusing on the differential pressure contribution due to the primary flow element's blockage (h

Equation 4-8

In the derivation of the blockage equation V velocity in the pipe prior to encountering the primary flow element, V

), Equation 4-1 can be rearranged:

is defined as the average fluid

equals

the accelerated velocity past the primary flow element.

)

Using the conservation of mass:

Equation 4-9

For incompressible fluids, 

= 2, Equation 4-9 can be simplified:

Equation 4-10

Where: A

= Cross-sectional area of the pipe

= Cross-sectional area of the pipe less the amount blocked by the sensor

can be rewritten in terms of A and the flow element's blockage:

Equation 4-11

Substituting into Equation 4-10 yields:

Equation 4-12

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Rosemount Annubar

h

---------

1B–

-------------------- -





1–=

QaKAA1 2gch=

12gchBhS

------------------------------------------------------=

K

h

----------

1 2

-- -

A12g

---------------------

h

BhS

+

3 2

-- -–

–=

h

B

--------- -

---------

1B–

3–

K

h

----------

K

h

--------------

h

B

--------------

=

K

B

----------

1 2

-- -–





A12g

---------------------

h

BhS

+

3 2

-- -–

---------

1B–

3–

=

------=

h hBhA+=

K

B

----------

A12gch

-----------------------------







– 1B–

3–

=

A12gch

-----------------------------=

K

B

---------- K

1B–

3–

KAd

----------







–



1B–3–Bd



1 2

-- -

2–

C1+

1 2

-- -

1B–

2–

Flow Test Data Book

Substituting Equation 4 -12 into Equation 4-8:

Equation 4-13

Recall the general equation relating the actual flow in a pipe to the Rosemount Annubar signal (Equation 4-6):

Where:

h = The total differential pressure produced by the flow elem e nt h = h

Substituting into Equation 4-6 and rearranging yields:

Equation 4-14

Differentiate Equation 4-14 with respect to the differential pressure contribution due to the primary flow element's blockage (h remains constant.

+ hS

Reference Manual

00821-0100-4809, Rev BA

July 2009

), assuming hS

Equation 4-15

Differentiate Equation 4-13 with respect to the primary flow element's blockage (B).

Equation 4-16

Combine with Equation 4-15 and Equation 4-16.

Equation 4-17

Substitute and and simplify:

Equation 4-18

Substitute and simplify:

4-4

Equation 4-19

Rearrange and integrate:

Equation 4-20

Page 21

Reference Manual

1B–

–

------------------------------------------=

1C2B–

–

--------------------------------------------------=

B0

–

--------------------=

–

--------------------

00821-0100-4809, Rev BA July 2009

Rosemount Annubar

Flow Test Data Book

Where C1 = constant of integration, solve for KA, redefining the integration constant C

Equation 4-21

(B) represents the actual blockage in the pipe caused by the Rosemount Annubar. Because downstream pressure is sensed past the flow element's widest cross-section, the effective blockage of the sensor will be a fraction of the actual blockage. Therefore, define an ef fective blockage as C represents a fraction of the actual blockage. Equation 4-21 can be rewritten:

Equation 4-22

Equation 4-22 shows that there is a direct relationship between a primary flow element flow coefficient K Equation 4-22 becomes:

Equation 4-23

as 2C1.

B where C2

and its blockage. As blockage approaches zero,

Thus, as blockage approaches zero, the primary flow element flow coefficient approaches a constant value , the stream-flow coefficient.

This constant value is the primary flow element flow coefficien t due only to the primary flow element's shape (h

), and is analogous to placing the primary

flow element in an infinitely large pipe with no confining walls. The constants C

and C2 in Equation 4-22 are determined experimentally.

Once determined, Equation 4-22 becomes the theoretical link between the flow coefficient and the flow element blockage.

CONCLUSION While empirical testing of a flowmeter is the most accurate means of

determining the meter's flow coefficient, many flowmeters use untested predicted flow coefficient.

•

Untested flow coefficients are based on a representative sample of empirically determined flow coefficients and on theories that link the flow coefficient to physical parameters in the pipe.

•

Like an orifice plate or a venturi meter, an averaging pitot tube has a theoretical relationship between its flow coefficient and parameters in the pipe.

•

An averaging pitot tube's flow coefficient is related to it s blockage in the pipe. This blockage dependency is necessary because the sensor it self reduces the effective pipe flow area.

•

For an orifice plate and a venturi meter, the velocity-of-approach factor is the theoretical link between the meter's flow coefficient and it's beta ratio. For a Rosemount Annubar, Equation 4-22 describes the theoretical relationship between the sen so r's flow coe fficient and its blockage in the pipe.

•

Using a theoretical basis, in addition to empirical testing, for the prediction of untested flow coefficients provides a much higher degree of confidence in these untested values.

4-5

Page 22

Rosemount Annubar Flow Test Data Book

Reference Manual

00821-0100-4809, Rev BA

July 2009

4-6

Page 23

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00821-0100-4809, Rev BA July 2009

Rosemount Annubar

Flow Test Data Book

Section 5 Test Facilities and Procedures

Overview . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .page 5-1

Testing Laboratories . . . . . . . . . . . . . . . . . . . . . . . . . . . . . page 5-1

Gravimetric Procedure . . . . . . . . . . . . . . . . . . . . . . . . . . . .page 5-2

Testing Performed by Sensor Size . . . . . . . . . . . . . . . . . .page 5-3

485 Sensor Size 1 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .page 5-4

485 Sensor Size 2 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .page 5-10

485 Sensor Size 3 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .page 5-26

585 Sensor Size 11 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .page 5-28

585 Sensor Size 22 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . page 5-39

585 Sensor Size 44 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . page 5-49

OVERVIEW The following descriptions of tests and testing methods are abbreviated

versions. For detailed descriptions of the individual laboratories contact the facility in question.

TESTING LABORATORIES

Rosemount Boulder, Colorado Flow Laboratory

Alden Research Laboratories (ARL)

SwRI Gas Research Institute (GRI), Meter Research Facility (MRF)

Utah Water Research Laboratories (UWRL)

Colorado Engineering Experimental Sation Inc (CEESI)

The Rosemount Annubars are tested and calibrated in water at Rosemount Inc. Line sizes available for testing range from 0.50 in. to 12 in. A secondary set of reference meters, routinely calibrated against a gravimetric primary standard, provide an uncertainty of 0.25 percent. Calibrations that use the primary-measurement device, gravimetric method, can be calibrated with an uncertainty of 0.1 percent.

Flowmeters are calibrated at ARL using the gravimetric method. This method has been found to produce a consistent accuracy of ±0.25% over extended periods.

Flowmeters are tested and calibrated on a recirculating natural gas loop. A sonic nozzle bank provides secondary flow calibration. This permits high repeatability and excellent test accuracies via calibration against the gravimetric primary standards. The sonic nozzle banks produce an accuracy on flow rate of 0.25% of reading.

Flowmeters are calibrated at UWRL using either calibrated nozzles or gravimetric method.

CEESI has two facilities, using different calibration methods:

• The Nunn, Colorado Facility uses compressed air stored in cylinders and discharged through a calibrated nozzle.

• The Garner IA Facility uses high-pressure natural gas from a transmission line that is measured via a calibrated nozzle.

www.rosemount.com

Page 24

Rosemount Annubar Flow Test Data Book

Reference Manual

00821-0100-4809, Rev BA

July 2009

GRAVIMETRIC PROCEDURE

Piping is selected to match the inside diameter of th e flowmeter under test. Carbon steel piping is normally used for these tests. Gaskets between pipe flanges are carefully installed and checked to ensure that they not interfere with the flow. Proper alignment of the flowmeter with the piping is maintained.

After all piping is secured with bolts, couplings, or clamps. Water is gradually introduced into the line. Flows are set to purge air from the system and to bring the flowmeter to steady-state temperature. After operating the system for a period of time, the control valve (at the downstream end of the test line) is closed. Air is then purged from all instrumentation lines, instruments, and the flowmeter.

After air purging, and with the control valve in the closed position, all instrumentation is checked for zero-flow indication. Calibration test runs are not started until all instrumentation reads zero at the no flow condition.

The flow rate is set by adjusting the control valve at the end of the test line to a desired flow. This flow is allowed to stabilize and reach steady-state condition. This condition is achieved when the average flow-meter readout is constant with time. At this point, the calibration run begins.

A calibration run consists of simultaneously recording the flowmeter output while the weighing tank is filled and the filling process is timed. Electronic timers are activated and deactivated by elec tr ic eye s on the switch way. Outputs are recorded at 1–15 Hz during this time. The duration of the run is typically between 50 and 100 seconds. For higher flow rates, the limiting factor is the capacity of the weighing tank.

In addition to recording weight and time, the water temperature, air temperature weigh tank, and air temperature adjacent to the readout are recorded. Barometric pressure is also recorded at the start and at the end of the test.

After a run is completed, the control valve is reset to another flow rate and the process is repeated. Runs are normally conducted at 12 different flow rates, approximately equally spaced from the maximum to the minimum flow rates. In some cases, the maximum flow obtainable by the test facility determines the upper flow limit of the test.

5-2

Page 25

Reference Manual

00821-0100-4809, Rev BA July 2009

Rosemount Annubar

Flow Test Data Book

TESTING PERFORMED BY SENSOR SIZE

The followings tests are provided on the following pages Rosemount 485 Sensor Size 1:

• Water, FI-210, 3-in. Schedule 40 (see page 5-4)

• Natural Gas, FI-260, 3-in. Schedule 40 (see page 5-6)

• Natural Gas, FI-261, 3-in. Schedule 40 (see page 5-8)

Rosemount 485 Sensor Size 2:

• Natural Gas and Water, FI-156, 8-in. Schedule 80 (see page 5-10)

• Water, FI-162, 3-in. Schedule 40 (see page 5-12)

• Water, FI-163, 3-in. Schedule 40 (see page 5-14)

• Water, FI-169, 10-in. Schedule 40 (see page 5-16)

• Natural Gas and Water, FI-178, 8-in. Schedule 80 (see page 5-18)

• Natural Gas and Water, FI-179, 8-in. Schedule 80 (see page 5-20)

• Natural Gas, FI-180, 6-in. Schedule 40 (see page 5-22)

• Natural Gas, FI-181, 6-in. Schedule 40 (see page 5-24)

Rosemount 485 Sensor Size 3

• Water, FI-307, 24-in. Schedule Standard (see page 5-26)

Rosemount 585 Sensor Size 11:

• Water, 585-11-1, 4-in. Schedule 40 (page 5-29)

• Water, 585-11-1, 4-in. Schedule 40 (page 5-31)

• Water, 585-11-7, 10-in. Schedule 40 (page 5-33)

• Water, 585-11-6, 8-in. Schedule 40 (page 5-34)

• Water, 585-11-5, 6-in. Schedule 40 (page 5-35)

• Water, 585-11-5, 6-in. Schedule 40 (page 5-36)

• Water, 585-11-3, 4-in. Schedule 80 (page 5-37)

• Air, 585-11-1, 4-in. Schedule 40 (page 5-38)

Rosemount 585 Sensor Size 22:

• Water, 585-22-1, 6-in. Schedule 80 (page 5-40)

• Water, 585-22-1, 6-in. Schedule 80 (page 5-42)

• Water, 585-22-5, 10-in. Schedule 40 (page 5-43)

• Water, 585-22-5, 10-in. Schedule 40 (page 5-44)

• Water, 585-22-5, 10-in. Schedule 40 (page 5-45)

• Water, 585-22-2, 5-in. Schedule 40 (page 5-46)

• Water, 585-22-2, 5-in. Schedule 40 (page 5-47)

• Air, 585-22-5, 8-in. Schedule 10 (page 5-48)

Rosemount 585 Sensor Size 33

• Water, 585-44-1, 16-in. STD (page 5-50)

• Water, 585-44-1, 24-in. STD (page 5-51)

• Water, 585-44-1, 12-in. STD (page 5-52)

• Natural Gas, 585-44-10, 12-in. STD (page 5-53)

5-3

Page 26

Rosemount Annubar

0.4800

0.4850

0.4900

0.4950

0.5000

0.5050

0.5100

0.5150

0.5200

1.0E+04 1.0E+05 1.0E+06

Pipe Reynolds Numbe r

pub

0.75% K

pub

Reynolds Number low limit

+/-

Flow Test Data Book

485 SENSOR SIZE 1

Test Laboratory: Rosemount Boulder, Colorado Flow Lab

Sensor Size: 1 Fluid: Water Sensor Serial Number: Fl-210 Nominal Pipe Size: 3-in. Schedule 40

Test Date: May 15, 2000 Pipe I.D.: 3.097-in (78.66 mm) Blockage: 24.26% K

: 0.5099

pub

Reference Manual

00821-0100-4809, Rev BA

July 2009

5-4

Page 27

Reference Manual

00821-0100-4809, Rev BA July 2009

Rosemount Annubar

Flow Test Data Book

Table 5-1. Rosemount Boulder, Colorado Flow Lab, Water.

Data Point Number

1 4.70E + 05 20.00 285.186 66.7 19.3 38.7 2.67 1.020 62.32 469.63 0.5115 2 4.75E + 05 20.25 291.907 66.7 19.3 38.7 2.67 1.020 62.32 475.45 0.5118 3 4.25E + 05 18.09 233.873 66.7 19.3 39.1 2.70 1.019 62.32 424.91 0.5110 4 4.29E + 05 18.22 237.029 66.9 19.4 39.1 2.70 1.017 62.31 427.95 0.5113 5 4.05E + 05 17.17 210.633 67.0 19.4 39.3 2.71 1.016 62.31 403.09 0.5108 6 4.14E + 05 17.49 218.940 67.3 19.6 39.2 2.70 1.012 62.31 410.78 0.5106 7 3.70E + 05 15.66 175.154 67.2 19.6 39.6 2.73 1.013 62.31 367.64 0.5109 8 3.68E + 05 15.58 173.340 67.2 19.6 39.6 2.73 1.012 62.31 365.77 0.5110 9 3.16E + 05 13.39 128.240 67.0 19.4 36.5 2.52 1.015 62.31 314.53 0.5108 10 3.20E + 05 13.59 132.030 67.0 19.4 36.5 2.52 1.015 62.31 319.18 0.5109 11 2.99E + 05 12.70 115.145 67.0 19.4 36.9 2.54 1.015 62.31 298.33 0.5113 12 3.04E + 05 12.89 118.684 67.0 19.4 36.9 2.54 1.015 62.31 302.63 0.5109 13 2.76E + 05 11.71 97.853 67.0 19.4 37.2 2.56 1.015 62.31 274.96 0.5112 14 2.80E + 05 11.89 100.734 67.0 19.4 37.2 2.58 1.015 62.31 279.21 0.5117 15 2.24E + 05 9.51 64.686 67.0 19.4 37.5 2.59 1.015 62.31 223.30 0.5107 16 2.30E + 05 9.75 67.826 67.0 19.4 37.4 2.58 1.015 62.31 228.95 0.5113 17 2.04E + 05 8.67 53.779 67.0 19.4 37.5 2.59 1.015 62.31 203.49 0.5103 18 2.09E + 05 8.88 56.323 67.0 19.4 37.5 2.59 1.016 62.31 208.48 0.5109 19 1.02E + 05 4.32 13.357 66.9 19.4 35.2 2.43 1.017 62.31 101.40 0.5103 20 1.07E + 05 4.54 14.751 66.9 19.4 35.2 2.43 1.017 62.32 106.53 0.5102 21 6.06E + 04 2.58 4.795 66.8 19.3 35.9 2.48 1.019 62.32 60.60 0.5090 22 6.56E + 04 2.79 5.610 66.7 19.3 35.9 2.148 1.020 62.32 65.62 0.5096 23 3.86E + 04 1.65 1.973 66.5 19.2 25.4 1.75 1.022 62.32 38.66 0.5062 24 4.49E + 04 1.92 2.658 66.5 19.2 25.4 1.75 1.023 62.32 45.06 0.5083

Pipe Reynolds Number

Differential

Velocity

ft/sec. in Water °F °C psig bar cP lb/ft

Pressure

Temperature Pressure Viscosity Density Flow Rate K

Reynolds Number Low Limit: 31495

GPM

5-5

Page 28

Rosemount Annubar

0.4800

0.4850

0.4900

0.4950

0.5000

0.5050

0.5100

0.5150

0.5200

1.0E+05 1.0E+06 1.0E+07 Pipe R eynolds Number

pub

0.75% K

pub

+/-

Flow Test Data Book

Sensor Size: 1 Fluid: Natural gas (185 psi) Sensor Serial Number: Fl-260 Nominal Pipe Size: 3-in. Schedule 40

Test Laboratory: SwRI Flow Lab

Test Date: August 22, 2002 Pipe I.D.: 3.068-in (77.9 mm) Blockage: 24.49% K

: 0.5084

pub

Reference Manual

00821-0100-4809, Rev BA

July 2009

5-6

Page 29

Reference Manual

00821-0100-4809, Rev BA July 2009

Rosemount Annubar

Flow Test Data Book

Table 5-2. SwRI Flow Labs, Natural Gas (185 psi)

Gas Exp.

File Pressure Temperature Density DP Re D K

psia °F lb/ft

000 202.5993 69.18282 0.625256 425.7187 5170457 0.51071 0.99523 0.59 7.782182 001 202.6013 69.18553 0.625259 425.7972 5170316 0.51066 0.99523 0.59 7.782003 002 202.5994 69.15164 0.625297 425.7294 5170481 0.51067 0.99523 0.59 7.781837 003 201.5583 69.43139 0.621619 306.1838 4374677 0.51048 0.99655 0.59 6.586276 004 201.5599 69.40691 0.621656 306.2264 4374799 0.51042 0.99655 0.59 6.586208 005 201.5369 69.3722 0.621652 306.1974 4374683 0.5104 0.99655 0.59 6.585636 006 200.8503 69.7511 0.619006 204.6737 3578087 0.51138 0.99768 0.59 5.389227 007 200.8377 69.7335 0.618989 204.7528 3577890 0.51125 0.99768 0.59 5.388787 008 200.7973 69.67277 0.618939 204.592 3577455 0.51135 0.99769 0.59 5.387597 009 200.1507 69.95492 0.616529 123.6027 2778837 0.51174 0.9986 0.59 4.186452 010 200.1393 69.91759 0.616541 123.5444 2778784 0.51182 0.9986 0.59 4.186121 011 200.1204 69.91065 0.616489 123.5626 2778465 0.51174 0.9986 0.59 4.18559 012 199.8453 70.4162 0.614976 63.06322 1983918 0.51214 0.99928 0.59 2.990931 013 199.8302 70.45454 0.614873 63.04856 1983498 0.51216 0.99928 0.59 2.990477 014 199.8061 70.47626 0.61477 63.05495 1983119 0.5121 0.99928 0.59 2.989999 015 199.3174 71.82439 0.611521 22.80306 1191144 0.51365 0.99974 0.59 1.79961 016 199.2619 71.86183 0.611299 22.77319 1190568 0.51386 0.99974 0.59 1.798835 017 199.2151 71.81538 0.61121 22.79317 1190234 0.51349 0.99974 0.59 1.798191 018 199.5703 72.70587 0.611203 2.65138 401055 0.50791 0.99997 0.59 0.606773 019 199.5145 73.05611 0.610585 2.64952 400679 0.50814 0.99997 0.59 0.606531 020 199.4588 73.31953 0.610078 2.64417 400334 0.50863 0.99997 0.59 0.606254

in H2O in. lb/s

Factor

Probe Width

Mass Flow

5-7

Page 30

Rosemount Annubar

0.4800

0.4850

0.4900

0.4950

0.5000

0.5050

0.5100

0.5150

0.5200

1.0E+05 1.0E+06 1.0E+ 07 Pipe Reynolds Number

pub

0.75% K

pub

+/-

Flow Test Data Book

Sensor Size: 1 Fluid: Natural gas (185 psi) Sensor Serial Number: Fl-261 Nominal Pipe Size: 3-in. Schedule 40

Test Laboratory: SwRI Flow Lab

Test Date: August 22, 2002 Pipe I.D.: 3.068-in (77.9 mm) Blockage: 24.49% K

: 0.5084

pub

Reference Manual

00821-0100-4809, Rev BA

July 2009

5-8

Page 31

Reference Manual

00821-0100-4809, Rev BA July 2009

Rosemount Annubar

Flow Test Data Book

Table 5-3. SwRI Flow Labs, Natural Gas (185 psi)

Gas Exp.

File Pressure Temperature Density DP Re D K

psia °F lb/ft

022 202.8247 69.03876 0.626134 429.9236 5170632 0.50779 0.99519 0.59 7.780826 023 202.8007 69.03179 0.626067 429.6451 5169961 0.50791 0.99519 0.59 7.779712 024 202.7756 68.96634 0.626073 429.6553 5169905 0.50784 0.99519 0.59 7.778808 025 201.6693 69.20293 0.622241 308.8323 4373337 0.50771 0.99652 0.59 6.581931 026 201.6491 69.24744 0.622096 309.0335 4372184 0.50751 0.99652 0.59 6.580654 027 201.6101 69.23643 0.621986 308.6848 4371092 0.5077 0.99652 0.59 6.578869 028 201.1633 69.68273 0.619948 206.8046 3578432 0.50837 0.99766 0.59 5.389369 029 201.1247 69.68246 0.619826 206.7449 3577270 0.50833 0.99766 0.59 5.387594 030 201.0782 69.66862 0.619697 206.6449 3576206 0.50834 0.99767 0.59 5.385848 031 200.505 69.53053 0.618117 124.5604 2778664 0.50877 0.99859 0.59 4.183545 032 200.4762 69.37682 0.618224 124.5957 2778848 0.50856 0.99859 0.59 4.182799 033 200.447 69.30812 0.61822 124.5066 2778721 0.50867 0.99859 0.59 4.182145 034 200.0181 69.9976 0.615975 63.51227 1981658 0.509 0.99928 0.59 2.985605 035 199.9286 70.08919 0.615575 63.49648 1980105 0.5089 0.99928 0.59 2.983665 036 199.8472 70.19513 0.615182 63.44048 1978503 0.50896 0.99928 0.59 2.98172 037 199.1532 71.49677 0.611342 22.84423 1186026 0.51079 0.99974 0.59 1.790918 038 199.0394 71.29086 0.611244 22.84238 1185647 0.51052 0.99974 0.59 1.789749 039 198.9264 71.09116 0.611141 22.79827 1185285 0.51073 0.99974 0.59 1.788623 040 199.3829 74.01337 0.608892 2.64419 398073 0.50679 0.99997 0.59 0.603472 041 199.241 74.74033 0.607537 2.6376 397198 0.50743 0.99997 0.59 0.602815 042 199.1592 75.24209 0.606655 2.64077 396584 0.5071 0.99997 0.59 0.602347

in H2O in. lb/s

Factor

Probe Width

Mass Flow

5-9

Page 32

Rosemount Annubar

+/-

Flow Test Data Book

485 SENSOR SIZE 2

Test Laboratory: SwRI Flow Lab and Rosemount Boulder, Colorado Flow Lab

Sensor Size: 2 Fluid: Natural gas (350 psi) and Water Sensor Serial Number: Fl-156 Nominal Pipe Size: 8-in. Schedule 80

Reference Manual

00821-0100-4809, Rev BA

July 2009

Test Date: February 13, 2001 (SwRI), December 18, 2000 (DSI) Pipe I.D.: 7.634-in (193.9 mm) Blockage: 17.38% K

: 0.5544

pub

5-10

Page 33

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00821-0100-4809, Rev BA July 2009

Rosemount Annubar

Flow Test Data Book

Table 5-4. SwRI Flow Labs, Natural Gas (350 psi)

Gas Exp.

File Pressure Temperature Density DP Re D K

psia °F lb/ft

000 351.05 70.420 1.16231 57.073 6860864 0.5529 0.9995 1.042 26.083 001 350.97 70.117 1.16415 57.074 6866857 0.5525 0.9995 1.042 26.086 002 350.94 70.140 1.16398 57.146 6866155 0.5522 0.9995 1.042 26.084 003 350.91 70.133 1.16390 57.110 6865564 0.5523 0.9995 1.042 26.082 004 350.53 70.182 1.16242 39.673 5718707 0.5522 0.9996 1.042 21.725 005 350.49 70.187 1.16237 39.633 5718194 0.5525 0.9996 1.042 21.723 006 350.50 70.172 1.16242 39.706 5718456 0.5519 0.9996 1.042 21.724 007 350.10 70.182 1.16096 22.302 4294705 0.5534 0.9998 1.042 16.314 008 350.07 70.175 1.16091 22.288 4294396 0.5535 0.9998 1.042 16.313 009 350.07 70.201 1.16083 22.272 4294104 0.5537 0.9998 1.042 16.313 010 349.91 70.141 1.16043 9.887 2863651 0.5542 0.9999 1.042 10.877 011 349.88 70.136 1.16033 9.890 2863475 0.5541 0.9999 1.042 10.877 012 349.82 70.139 1.16011 9.886 2863079 0.5542 0.9999 1.042 10.875 019 349.19 70.415 1.15714 0.399 572224 0.5525 1.0000 1.042 2.174 022 349.32 70.746 1.15670 0.395 571852 0.5547 1.0000 1.042 2.174 023 349.38 70.618 1.15724 0.395 572081 0.5553 1.0000 1.042 2.174 026 348.77 70.058 1.15662 9.844 2853932 0.5543 0.9999 1.042 10.837 027 349.61 70.138 1.15934 6.308 2288047 0.5546 0.9999 1.042 8.691 028 349.57 70.130 1.15924 6.301 2287657 0.5548 0.9999 1.042 8.689 029 349.54 70.099 1.15920 6.307 2287696 0.5545 0.9999 1.042 8.689 030 349.50 70.131 1.15902 3.541 1713710 0.5544 1.0000 1.042 6.509 031 349.46 70.159 1.15882 3.538 1713422 0.5547 1.0000 1.042 6.508 032 349.44 70.157 1.15880 3.536 1713262 0.5548 1.0000 1.042 6.507 033 349.58 70.125 1.15935 1.563 1141348 0.5557 1.0000 1.042 4.335 034 349.53 70.091 1.15928 1.565 1141235 0.5552 1.0000 1.042 4.334 035 349.51 70.057 1.15929 1.565 1141168 0.5551 1.0000 1.042 4.334

025 349.38 70.618 1.15724 R2 –0.014

in H2O in. lb/s

Forced Zero DP Run

572081 0.5553 1 1.042 2.174

R1 0.001

Factor

Probe Width

Mass Flow

Table 5-5. Rosemount Boulder, Colorado Flow Lab, Water

Data Point Number

1 8.03E + 05 14.02 118.295 66.0 18.89 22.8 1.57 1.030 62.32 2642.15 0.5568 2 8.09E + 05 14.13 119.941 66.0 18.89 22.8 1.57 1.030 62.32 2643.91 0.5573 3 6.73E + 05 11.75 83.542 66.0 18.89 24.5 1.69 1.030 62.32 2404.31 0.5554 4 6.77E + 05 11.82 83.958 66.0 18.89 24.4 1.68 1.030 62.32 2425.52 0.5571 5 5.46E + 05 9.54 54.750 66.0 18.89 27.3 2.02 1.030 62.32 1995.94 0.5571 6 5.46E + 05 9.54 55.095 66.0 18.89 27.1 1.87 1.030 62.32 2011.41 0.5551 7 4.23E + 05 7.38 32.526 66.0 18.89 29.0 2.00 1.029 62.32 1673.09 0.5587 8 4.21E + 05 7.35 32.407 66.0 18.89 29.0 2.00 1.030 62.32 1682.18 0.5575 9 3.35E + 05 5.84 20.657 66.0 18.89 31.5 2.17 1.029 62.32 1358.43 0.5553 10 3.33E + 05 5.81 20.330 66.0 18.89 31.5 2.17 1.029 62.32 1357.83 0.5568 11 2.07E + 05 3.62 7.917 66.1 18.94 33.9 2.34 1.029 62.32 1050.11 0.5550 12 2.07E + 05 3.61 7.902 66.1 18.94 33.9 2.34 1.029 62.32 1045.96 0.5545 13 1.61E + 05 2.80 4.755 66.1 18.94 35.7 2.46 1.028 62.32 831.75 0.5550 14 1.67E + 05 2.90 5.083 66.1 18.94 35.8 2.47 1.028 62.32 827.42 0.5556 15 1.21E + 05 2.10 2.685 66.2 19.00 37.6 2.59 1.027 62.32 514.62 0.5548 16 1.25E + 05 2.18 2.881 66.2 19.00 37.7 2.60 1.027 62.32 513.65 0.5543

Pipe Reynolds Number

Differential

Velocity

ft/sec. in Water °F °C psig bar cP lb/ft

Pressure

Temperature Pressure Viscosity Density Flow Rate K

Reynolds Number Low Limit: 91471

GPM

5-11

Page 34

Rosemount Annubar

0.4800

0.4850

0.4900

0.4950

0.5000

0.5050

0.5100

0.5150

0.5200

1.0E+04 1.0E+05 1.0E+06

Pipe Reynolds Number

0.5300

0.5350

0.5400

0.5450

0.5500

0.5550

0.5600

0.5650

0.5700

1.0E+04 1.0E+05 1.0E+06

Pipe Reynolds Number

pub

0.75% K

pub

Reynolds Number low limit

+/-

Flow Test Data Book

Test Laboratory: Rosemount Boulder, Colorado Flow Lab

Sensor Size: 2 Fluid: Water Sensor Serial Number: Fl-162 Nominal Pipe Size: 3-in. Schedule 40

Test Date: December 19, 2000 Pipe I.D.: 8.006-in (203.4 mm) Blockage: 16.60% K

: 0.5588

pub

Reference Manual

00821-0100-4809, Rev BA

July 2009

5-12

Page 35

Reference Manual

00821-0100-4809, Rev BA July 2009

Rosemount Annubar

Flow Test Data Book

Table 5-6. Rosemount Boulder, Colorado Flow Lab, Water.

Data Point Number

1 1.05E + 06 17.16 176.063 67.5 19.7 23.2 1.60 1.009 62.31 2692.78 0.5586 2 1.04E + 06 16.91 170.395 67.6 19.8 23.5 1.62 1.008 62.31 2653.94 0.5596 3 9.52E + 05 15.51 143.617 67.6 19.8 25.0 1.72 1.008 62.31 2432.93 0.5588 4 9.56E + 05 15.57 144.939 67.6 19.8 24.9 1.72 1.008 62.31 2442.91 0.5585 5 7.86E + 05 12.81 97.625 67.5 19.7 27.8 1.92 1.008 62.31 2009.60 0.5598 6 7.90E + 05 12.87 98.542 67.5 19.7 27.7 1.91 1.008 62.31 2018.65 0.5597 7 6.57E + 05 10.70 68.137 67.5 19.7 29.6 2.04 1.008 62.31 1679.69 0.5601 8 6.61E + 05 10.77 68.602 67.5 19.7 29.6 2.04 1.008 62.31 1689.70 0.5615 9 5.29E + 05 8.63 44.337 67.5 19.7 32.1 2.21 1.008 62.31 1353.36 0.5594 10 5.29E + 05 8.62 44.258 67.5 19.7 32.1 2.21 1.009 62.31 1352.01 0.5594 11 4.10E + 05 6.68 26.607 67.5 19.7 34.5 2.38 1.008 62.31 1048.52 0.5595 12 4.09E + 05 6.67 26.595 67.5 19.7 34.5 2.38 1.009 62.31 1047.05 0.5588 13 3.24E + 05 5.27 16.488 67.5 19.7 36.4 2.51 1.008 62.31 827.35 0.5608 14 3.24E + 05 5.29 16.780 67.5 19.7 36.4 2.51 1.008 62.31 829.84 0.5576 15 2.01E + 05 3.27 6.402 6 7.6 19.8 38.3 2.64 1.007 62.31 513.85 0.5590 16 1.99E + 05 3.23 6.194 67.6 19.8 38.3 2.64 1.007 62.31 507.30 0.5610 17 1.56E + 05 2.54 3.866 6 7.7 19.8 39.1 2.70 1.007 62.31 398.49 0.5578 18 1.59E + 05 2.59 4.033 67.6 19.8 39.1 2.70 1.007 62.31 406.78 0.5575 19 1.19E + 05 1.94 2.274 6 7.4 19.7 36.9 2.54 1.010 62.31 304.88 0.5565 20 1.21E + 05 1.97 2.365 67.4 19.7 36.9 2.54 1.010 62.31 309.76 0.5544

Pipe Reynolds Number

Differential

Velocity

ft/sec. in Water °F °C psig bar cP lb/ft

Pressure

Temperature Pressure Viscosity Density Flow Rate K

Reynolds Number Low Limit: 95851

GPM

5-13

Page 36

Rosemount Annubar

0.5400

0.5450

0.5500

0.5550

0.5600

0.5650

0.5700

0.5750

0.5800

1.0E+04 1.0E+05 1.0E+06 1.0E+07

Pipe Reynolds Number

pub

0.75% K

pub

Reynolds Number low limit

+/-

Flow Test Data Book

Test Laboratory: Rosemount Boulder, Colorado Flow Lab

Sensor Size: 2 Fluid: Water Sensor Serial Number: Fl-163 Nominal Pipe Size: 3-in. Schedule 40

Test Date: December 19, 2000 Pipe I.D.: 8.006-in (203.4 mm) Blockage: 16.57% K

: 0.5589

pub

Reference Manual

00821-0100-4809, Rev BA

July 2009

5-14

Page 37

Reference Manual

00821-0100-4809, Rev BA July 2009

Rosemount Annubar

Flow Test Data Book

Table 5-7. Rosemount Boulder, Colorado Flow Lab, Water.

Data Point Number

1 1.02E + 06 16.86 168.772 66.4 19.11 23.4 1.61 1.024 62.32 2645.00 0.5605 2 1.02E + 06 16.88 169.030 66.4 19.11 23.4 1.61 1.024 62.32 2648.52 0.5608 3 9.37E + 05 15.50 142.682 66.4 19.11 24.9 1.72 1.024 62.32 2431.94 0.5604 4 9.40E + 05 15.56 144.054 66.4 19.11 24.9 1.72 1.024 62.32 2441.24 0.5599 5 7.74E + 05 12.81 97.615 66.4 19.11 27.7 1.91 1.024 62.32 2010.45 0.5601 6 7.76E + 05 12.85 98.035 66.4 19.11 27.6 1.90 1.024 62.32 2016.53 0.5606 7 6.46E + 05 10.69 67.498 66.4 19.11 29.6 2.04 1.024 62.32 1677.80 0.5622 8 6.50E + 05 10.76 68.786 66.4 19.11 29.5 2.03 1.024 62.32 1688.54 0.5604 9 5.20E + 05 8.61 44.210 66.4 19.11 32.1 2.21 1.024 62.32 1350.52 0.5591 10 5.22E + 05 8.65 44.141 66.4 19.11 32.0 2.21 1.025 62.32 1357.34 0.5624 11 4.02E + 05 6.65 26.214 66.4 19.11 34.5 2.38 1.024 62.32 1043.95 0.5613 12 4.03E + 05 6.67 26.242 66.4 19.11 34.4 2.37 1.024 62.32 1047.24 0.5627 13 3.19E + 05 5.27 16.480 66.4 19.11 36.3 2.50 1.024 62.32 827.58 0.5612 14 3.20E + 05 5.29 16.649 66.4 19.11 36.3 2.50 1.024 62.32 830.79 0.5605 15 1.98E + 05 3.28 6.340 66.5 19.12 38.2 2.63 1.022 62.32 514.15 0.5621 16 1.98E + 05 3.28 6.348 66.5 19.12 38.2 2.63 1.023 62.32 514.42 0.5620 17 1.53E + 05 2.53 3.806 66.6 19.22 39.1 2.70 1.022 62.32 397.26 0.5605 18 1.59E + 05 2.62 4.047 66.5 19.12 39.0 2.69 1.022 62.32 410.80 0.5621 19 1.17E + 05 1.94 2.242 66.4 19.11 37.7 2.60 1.024 62.32 304.33 0.5594 20 1.19E + 05 1.98 2.345 66.4 19.11 37.6 2.60 1.024 62.32 309.91 0.5571 21 8.40E + 04 1.39 1.178 66.5 19.12 38.8 2.68 1.023 62.32 217.69 0.5522 22 8.51E + 04 1.41 1.214 66.5 19.12 38.9 2.68 1.023 62.32 220.67 0.5513

Pipe Reynolds Number

Differential

Velocity

ft/sec. in Water °F °C psig bar cP lb/ft

Pressure

Temperature Pressure Viscosity Density Flow Rate K

Reynolds Number Low Limit: 96035

GPM

5-15

Page 38

Rosemount Annubar

0.5500

0.5550

0.5600

0.5650

0.5700

0.5750

0.5800

0.5850

0.5900

1.0E+ 04 1.0E+ 05 1.0E+06 Pipe Reynolds Number

pub

0.75% K

pub

Reynolds Number low limit

+/-

Flow Test Data Book

Test Laboratory: Rosemount Boulder, Colorado Flow Lab

Sensor Size: 2 Fluid: Water Sensor Serial Number: Fl-169 Nominal Pipe Size: 10-in. Schedule 40

Test Date: December 14, 2000 Pipe I.D.: 10.020-in (254.5 mm) Blockage: 13.24% K

: 0.5766

pub

Reference Manual

00821-0100-4809, Rev BA

July 2009

5-16

Page 39

Reference Manual

00821-0100-4809, Rev BA July 2009

Rosemount Annubar

Flow Test Data Book

Table 5-8. Rosemount Boulder, Colorado Flow Lab, Water.

Data Point Number

1 9.40E + 05 12.42 86.257 66.5 19.17 19.7 1.36 1.023 62.32 3053.31 0.5777 2 9.44E + 05 12.47 86.908 66.5 19.17 19.6 1.35 1.023 62.32 3065.38 0.5778 3 8.92E + 05 11.78 77.591 66.5 19.17 21.1 1.45 1.023 62.32 2895.02 0.5775 4 9.00E + 05 11.88 79.133 66.5 19.17 20.9 1.44 1.023 62.32 2920.24 0.5768 5 8.31E + 05 10.97 67.272 66.5 19.17 22.7 1.57 1.023 62.32 2697.62 0.5779 6 8.36E + 05 11.04 67.803 66.5 19.17 22.6 1.56 1.023 62.32 2714.69 0.5793 7 7.36E + 05 9.72 52.897 66.5 19.17 25.0 1.72 1.023 62.32 2389.81 0.5774 8 7.35E + 05 9.71 52.731 66.5 19.17 25.1 1.73 1.023 62.32 2386.74 0.5775 9 6.52E + 05 8.61 41.499 66.5 19.17 26.8 1.85 1.023 62.32 2115.39 0.5770 10 6.55E + 05 8.64 41.433 66.5 19.17 26.8 1.85 1.023 62.32 2124.83 0.5800 11 5.23E + 05 6.90 26.152 66.5 19.17 29.4 2.03 1.023 62.32 1696.60 0.5829 12 5.23E + 05 6.90 26.481 66.5 19.17 29.4 2.03 1.023 62.32 1696.31 0.5792 13 3.99E + 05 5.26 15.470 66.5 19.17 32.4 2.23 1.022 62.32 1293.20 0.5777 14 3.98E + 05 5.25 15.417 66.5 19.17 32.4 2.23 1.023 62.32 1290.32 0.5774 15 2.76E + 05 3.65 7.493 66.6 19.22 35.8 2.47 1.022 62.32 896.62 0.5756 16 2.77E + 05 3.66 7.518 66.6 19.22 35.8 2.47 1.022 62.32 898.83 0.5760 17 1.83E + 05 2.41 3.242 66.6 19.22 37.7 2.60 1.021 62.32 593.42 0.5791 18 1.89E + 05 2.49 3.453 66.6 19.22 37.6 2.59 1.021 62.32 610.98 0.5777 19 1.49E + 05 1.96 2.153 66.7 19.28 38.4 2.65 1.020 62.32 481.46 0.5766 20 1.47E + 05 1.93 2.090 66.7 19.28 38.4 2.65 1.020 62.32 474.56 0.5767

Pipe Reynolds Number

Differential

Velocity

ft/sec. in Water °F °C psig bar cP lb/ft

Pressure

Temperature Pressure Viscosity Density Flow Rate K

Reynolds Number Low Limit: 120202

GPM

5-17

Page 40

Rosemount Annubar

0.5300

0.5350

0.5400

0.5450

0.5500

0.5550

0.5600

0.5650

1.0E+05 1.0E+06 1.0E+07 Pipe Reynolds Number

pub

0.75% K

pub

+/-

Flow Test Data Book

Test Laboratory: SwRI Flow Lab and Rosemount Boulder, Colorado Flow Lab

Sensor Size: 2 Fluid: Natural gas (400 psi) and Water Sensor Serial Number: Fl-178 Nominal Pipe Size: 8-in. Schedule 80

Reference Manual

00821-0100-4809, Rev BA

Test Date: August 20, 2002 (SwRI), August 12, 2002 (DSI) Pipe I.D.: 7.591-in (192.8 mm) Blockage: 17.70% K

: 0.5527

pub

July 2009

5-18

Page 41

Reference Manual

00821-0100-4809, Rev BA July 2009

Rosemount Annubar

Flow Test Data Book

Table 5-9. SwRI Flow Labs, Natural Gas (400 psi)

Gas Exp.

File Pressure Temperature Density DP Re D K

psia °F lb/ft

000 399.2381 70.36406 1.264664 66.712 7612648 0.55186 0.99949 1.062 29.10727 001 399.2067 70.32793 1.264664 66.68185 7612393 0.55194 0.99949 1.062 29.10464 002 399.1785 70.35466 1.264492 66.67262 7611555 0.55197 0.99949 1.062 29.10245 003 401.0847 70.26102 1.271108 56.3852 7013626 0.55166 0.99957 1.062 26.81987 004 401.0365 70.26235 1.270862 56.38691 7012511 0.55161 0.99957 1.062 26.81553 005 401.0253 70.27148 1.270798 56.31914 7012143 0.55193 0.99957 1.062 26.81443 006 399.3239 70.3362 1.264849 37.65638 5720938 0.55183 0.99971 1.062 21.8737 007 399.3395 70.2757 1.265077 37.74814 5721538 0.55112 0.99971 1.062 21.87411 008 399.3772 70.27707 1.265199 37.72615 5722033 0.55131 0.99971 1.062 21.87617 009 398.9396 70.29922 1.263531 19.68531 4132344 0.55145 0.99985 1.062 15.79815 010 398.9114 70.32668 1.263357 19.68902 4131817 0.55138 0.99985 1.062 15.7967 011 398.8833 70.27533 1.263412 19.6594 4131944 0.55176 0.99985 1.062 15.79594 012 399.3192 70.55387 1.263538 7.45387 2544265 0.55195 0.99994 1.062 9.731082 013 399.2472 70.64496 1.263034 7.45405 2542988 0.55184 0.99994 1.062 9.727386 014 399.1706 70.67073 1.262704 7.45083 2542013 0.55184 0.99994 1.062 9.723914 015 399.5884 70.81895 1.263728 1.05499 958885 0.55309 0.99999 1.062 3.669006 016 399.414 70.77697 1.263284 1.05756 958396 0.55219 0.99999 1.062 3.666819 017 399.2506 70.66026 1.263075 1.05486 958057 0.55264 0.99999 1.062 3.664815 018 398.4257 69.58176 1.263432 1.82996 1265740 0.55333 0.99999 1.062 4.833638 019 398.424 69.60608 1.263355 1.8346 1265675 0.55264 0.99999 1.062 4.833563 020 398.4658 69.5973 1.263521 1.83347 1265838 0.55284 0.99999 1.062 4.83415

in H2O in. lb/s

Factor

Probe Width

Mass Flow

Table 5-10. Rosemount Boulder, Colorado Flow Lab, Water.

Data Point Number

1 1.10E + 06 18.798 218.205 67.9 19.9 23.4 1.61 1.003 62.31 2652.10 0.5496 2 1.10E + 06 18.766 217.799 68.2 20.1 23.4 1.61 0.999 62.31 2647.54 0.5492 3 1.03E + 06 17.563 189.676 68.3 20.2 24.7 1.70 0.998 62.30 2477.85 0.5507 4 1.02E + 06 17.356 185.657 68.4 20.2 24.8 1.71 0.997 62.30 2448.66 0.5501 5 8.46E + 05 14.359 127.131 68.5 20.3 27.6 1.90 0.995 62.30 2025.88 05500 6 8.50E + 05 14.399 128.115 68.6 20.3 27.6 1.90 0.994 62.30 2031.52 0.5494 7 7.05E + 05 11.946 88.169 68.6 20.3 29.7 2.05 0.994 62.30 1685.45 0.5494 8 7.08E + 05 11.987 88.495 68.6 20.3 29.7 2.05 0.994 62.30 1691.21 0.5503 9 5.63E + 05 9.534 56.159 68.6 20.3 32.1 2.21 0.993 62.30 1345.12 0.5494 10 5.67E + 05 9.608 56.961 68.6 20.3 32.0 2.21 0.993 62.30 1355.48 0.5498 11 4.35E + 05 7.364 33.437 68.7 20.4 34.4 2.37 0.993 62.30 1038.89 0.5499 12 4.40E + 05 7.442 34.197 68.7 20.4 34.3 2.36 0.993 62.30 1049.99 0.5496 13 3.44E + 05 5.827 20.989 68.7 20.4 36.2 2.50 0.992 62.30 822.03 0.5492 14 3.47E + 05 5.873 21.365 68.7 20.4 36.2 2.50 0.992 62.30 828.55 0.5487

Pipe Reynolds Number

Differential

Velocity

ft/sec. in Water °F °C psig bar cP lb/ft

Pressure

Temperature Pressure Viscosity Density Flow Rate K

GPM

5-19

Page 42

Rosemount Annubar

0.5300

0.5350

0.5400

0.5450

0.5500

0.5550

0.5600

0.5650

0.5700

1.0E+ 0 5 1.0E+ 0 6 1.0E+ 07 Pipe Reynolds Number

pub

0.75% K

pub

+/-

Flow Test Data Book

Test Laboratory: SwRI Flow Labs and Rosemount Boulder, Colorado Flow Lab

Sensor Size: 2 Fluid: Natural gas (400 psi) and Water Sensor Serial Number: Fl-179 Nominal Pipe Size: 8-in. Schedule 80

Reference Manual

00821-0100-4809, Rev BA

Test Date: August 20, 2002 (SwRI), August 12, 2002 (DSI) Pipe I.D.: 7.591-in (192.8 mm) Blockage: 17.70% K

: 0.5527

pub

July 2009

5-20

Page 43

Reference Manual

00821-0100-4809, Rev BA July 2009

Rosemount Annubar

Flow Test Data Book

Table 5-11. SwRI Flow Labs, Natural Gas (400 psi)

Gas Exp.

File Pressure Temperature Density DP Re D K

psia °F lb/ft

022 400.5934 70.09192 1.26894 67.19104 7636204 0.55056 0.99949 1.062 29.19194 023 400.5734 70.11051 1.268819 67.15411 7634966 0.55067 0.99949 1.062 29.18791 024 400.5566 70.02399 1.269014 67.15976 7635645 0.55058 0.99949 1.062 29.18677 025 400.1057 70.14067 1.267159 56.44205 6991771 0.55035 0.99957 1.062 26.72838 026 400.0123 70.13284 1.266849 56.37616 6989717 0.55057 0.99957 1.062 26.71984 027 400.0015 70.0372 1.267091 56.36834 6990797 0.55056 0.99957 1.062 26.72022 028 400.3373 70.21033 1.267706 37.88483 5730654 0.55046 0.99971 1.062 21.91022 029 400.269 70.10329 1.267769 37.9004 5730493 0.55023 0.99971 1.062 21.90594 030 400.1888 69.96667 1.267898 37.90305 5731232 0.55014 0.99971 1.062 21.90417 031 399.6013 69.87253 1.266207 19.74952 4137256 0.55034 0.99985 1.062 15.80868 032 399.5592 69.84549 1.266144 19.76687 4137037 0.55006 0.99985 1.062 15.80713 033 399.5333 69.77977 1.266249 19.73404 4137651 0.55052 0.99985 1.062 15.80791 034 399.5284 70.37971 1.26449 7.5027 2542949 0.54953 0.99994 1.062 9.723809 035 399.3698 70.32362 1.264122 7.48151 2541621 0.55004 0.99994 1.062 9.717724 036 399.2254 70.17006 1.264083 7.46435 2540924 0.5504 0.99994 1.062 9.712693 037 398.3805 69.89757 1.262096 1.83461 1263339 0.55212 0.99999 1.062 4.826624 038 398.196 69.68668 1.262089 1.83028 1263176 0.55252 0.99999 1.062 4.824399 039 398.0698 69.56982 1.262005 1.8311 1262935 0.5522 0.99999 1.062 4.822573 040 399.5883 69.26618 1.267972 1.06446 958785 0.54841 0.99999 1.062 3.660332 041 399.4414 69.1862 1.267713 1.06426 958549 0.54831 0.99999 1.062 3.658928 042 399.3669 69.1327 1.267599 1.06372 958345 0.54831 0.99999 1.062 3.657825

in H2O in. lb/s

Factor

Probe Width

Mass Flow

Table 5-12. Rosemount Boulder, Colorado Flow Lab, Water.

Data Point Number

1 1.09E + 06 18.731 217.392 67.5 19.7 23.4 1.61 1.008 62.31 2642.59 0.5487 2 1.10E + 06 18.783 218.619 67.8 19.9 23.3 1.61 1.005 62.31 2649.95 0.5486 3 1.01E + 06 17.333 186.289 67.9 19.9 24.8 1.71 1.004 62.31 2445.36 0.5485 4 1.02E + 06 17.353 186.452 68.0 20.0 24.7 1.70 1.002 62.31 2448.23 0.5489 5 8.41E + 05 14.353 126.967 68.1 20.1 27.5 1.90 1.001 62.31 2025.02 0.5501 6 8.43E + 05 14.362 128.085 68.2 20.1 27.5 1.90 0.999 62.31 2026.28 0.5481 7 7.02E + 05 11.936 88.252 68.3 20.2 29.6 2.04 0.998 62.30 1683.93 0.5487 8 7.05E + 05 11.983 88.378 68.4 20.2 29.6 2.04 0.997 62.30 1690.66 0.5505 9 5.64E + 05 9.567 56.423 68.5 20.3 32.0 2.21 0.995 62.30 1349.74 0.5500 10 5.65E + 05 9.576 56.368 68.6 20.3 32.0 2.21 0.994 62.30 1351.00 0.5508 11 4.36E + 05 7.383 33.529 68.6 20.3 34.4 2.37 0.993 62.30 1041.66 0.5507 12 4.37E + 05 7.410 33.805 68.6 2.3 34.3 2.36 0.994 62.30 1045.43 0.5504 13 3.44E + 05 5.826 20.874 68.7 20.4 36.2 2.50 0.993 62.30 821.93 0.5507 14 3.46E + 05 5.853 21.162 68.6 20.3 36.1 2.49 0.993 62.30 825.71 0.5494 15 2.17E + 05 3.662 8.351 68.7 20.4 37.8 2.61 0.992 62.30 516.64 0.5472 16 2.18E + 05 3.691 8.474 68.7 2.4 37.8 2.61 0.992 62.30 520.75 0.5476

Pipe Reynolds Number

Differential

Velocity

ft/sec. in Water °F °C psig bar cP lb/ft

Pressure

Temperature Pressure Viscosity Density Flow Rate K

GPM

5-21

Page 44

Rosemount Annubar

0.5000

0.5050

0.5100

0.5150

0.5200

0.5250

0.5300

0.5350

0.5400

1.0E+ 06 1.0E+07 Pipe R eynolds Number

pub

0.75% K

pub

+/-

Flow Test Data Book

Sensor Size: 2 Fluid: Natural gas (400 psi) Sensor Serial Number: Fl-180 Nominal Pipe Size: 6-in. Schedule 40

Test Laboratory: SwRI Flow Labs

Test Date: August 20, 2002 Pipe I.D.: 6.059-in (153.9 mm) Blockage: 22.17% K

: 0.5257

pub

Reference Manual

00821-0100-4809, Rev BA

July 2009

5-22

Page 45

Reference Manual

00821-0100-4809, Rev BA July 2009

Rosemount Annubar

Flow Test Data Book

Table 5-13. SwRI Flow Labs, Natural Gas (400 psi)

Gas Exp.

File Pressure Temperature Density DP Re D K

psia °F lb/ft

044 402.2264 69.78825 1.275065 183.1904 9572419 0.52261 0.99888 1.062 29.20216 045 402.2249 69.78545 1.275068 183.1652 9571925 0.52262 0.99888 1.062 29.20053 046 402.2003 69.78291 1.274993 183.2267 9571523 0.52252 0.99888 1.062 29.19909 047 401.3388 69.80605 1.272042 127.3168 7973641 0.52258 0.99922 1.062 24.3224 048 401.324 69.81554 1.271968 127.2576 7973870 0.52273 0.99922 1.062 24.32337 049 401.2841 69.82552 1.271805 127.3385 7973102 0.52255 0.99922 1.062 24.32124 050 400.6831 69.95078 1.269517 81.63868 6380432 0.52263 0.9995 1.062 19.46474 051 400.6703 69.78475 1.269958 81.62017 6382775 0.52267 0.9995 1.062 19.46715 052 400.6707 69.83695 1.26979 81.6921 6382281 0.52247 0.9995 1.062 19.46712 053 399.7075 69.59795 1.267281 38.66373 4391472 0.52268 0.99976 1.062 13.38829 054 399.6934 69.57008 1.267315 38.6696 4391638 0.52263 0.99976 1.062 13.38823 055 399.7024 69.64079 1.26714 38.67824 4391271 0.52262 0.99976 1.062 13.3885 056 398.9556 69.13239 1.266025 15.53221 2790645 0.52382 0.9999 1.062 8.501159 057 398.9794 69.18728 1.265945 15.53455 2790692 0.52385 0.9999 1.062 8.50201 058 398.9846 69.26121 1.265675 15.55648 2790406 0.52354 0.9999 1.062 8.502069 059 399.77 70.43433 1.264888 2.89146 1202055 0.52419 0.99998 1.062 3.669187 060 399.5529 70.87255 1.262895 2.8918 1200207 0.52408 0.99998 1.062 3.665766 061 399.2911 71.17313 1.261155 2.89022 1198483 0.52404 0.99998 1.062 3.66196

in H2O in. lb/s

Factor

Probe Width

Mass Flow

5-23

Page 46

Rosemount Annubar

0.5000

0.5050

0.5100

0.5150

0.5200

0.5250

0.5300

0.5350

0.5400

1.0E+ 06 1.0E+07 Pipe R eynolds Number

pub

0.75% K

pub

+/-

Flow Test Data Book

Sensor Size: 2 Fluid: Natural gas (400 psi) Sensor Serial Number: Fl-181 Nominal Pipe Size: 6-in. Schedule 40

Test Laboratory: SwRI Flow Labs

Test Date: August 21, 2002 Pipe I.D.: 6.059-in (153.9 mm) Blockage: 22.17% K

: 0.5257

pub

Reference Manual

00821-0100-4809, Rev BA

July 2009

5-24

Page 47

Reference Manual

00821-0100-4809, Rev BA July 2009

Rosemount Annubar

Flow Test Data Book

Table 5-14. SwRI Flow Labs, Natural Gas (400 psi)

Gas Exp.

File Pressure Temperature Density DP Re D K

psia °F lb/ft

000 402.1318 70.22332 1.273031 182.2164 9567169 0.52445 0.99888 1.062 29.20375 001 402.1396 70.23601 1.27302 182.2515 9565927 0.52435 0.99888 1.062 29.20053 002 402.1459 70.20831 1.273122 182.2548 9566150 0.52431 0.99888 1.062 29.20007 003 401.4724 70.12239 1.271117 126.7637 7974761 0.52422 0.99922 1.062 24.33706 004 401.4468 70.15948 1.270924 126.7554 7973279 0.5242 0.99922 1.062 24.33376 005 401.4389 70.22195 1.270708 126.6872 7971112 0.52429 0.99922 1.062 24.32932 006 400.8714 70.22616 1.268799 81.33865 6382353 0.52412 0.9995 1.062 19.47868 007 400.8555 70.18685 1.26886 81.21389 6382646 0.5245 0.9995 1.062 19.47842 008 400.7853 70.12505 1.268806 81.24182 6382324 0.52434 0.9995 1.062 19.4755 009 403.3504 69.91417 1.278022 38.91319 4431173 0.524 0.99976 1.062 13.52238 010 403.3576 69.91348 1.278048 38.9336 4431585 0.52391 0.99976 1.062 13.52364 011 403.3601 69.92616 1.278038 38.91548 4431612 0.52405 0.99976 1.062 13.52397 012 399.7687 70.02187 1.266071 15.51266 2794122 0.52552 0.9999 1.062 8.523624 013 399.7375 69.97731 1.266096 15.51172 2794003 0.52547 0.9999 1.062 8.522671 014 399.6968 69.91672 1.266136 15.49649 2793974 0.52567 0.9999 1.062 8.521782 015 399.6242 70.38922 1.264523 2.87541 1202830 0.52601 0.99998 1.062 3.671184 016 399.5218 70.62444 1.2635 2.87366 1201883 0.52614 0.99998 1.062 3.669494 017 399.4349 70.80791 1.26268 2.88596 1201079 0.52497 0.99998 1.062 3.66797

in H2O in. lb/s

Factor

Probe Width

Mass Flow

5-25

Page 48

Rosemount Annubar

0.5600

0.5650

0.5700

0.5750

0.5800

0.5850

0.5900

0.5950

0.6000

1.0E+ 05 1.0E+ 06 1.0E+ 07 Pipe Reynol ds Number

pub

0.75% K

pub

Reynolds Number low limit

+/-

Flow Test Data Book

485 SENSOR SIZE 3

Sensor Size: 3 Fluid: Water Sensor Serial Number: Fl-307 Nominal Pipe Size: 24-in. Schedule Standard

Test Laboratory: Alden Research Labs

Test Date: July 25, 2001 Pipe I.D.: 23.340-in (592.8 mm) Blockage: 10.47% K

: 0.5845

pub

Reference Manual

00821-0100-4809, Rev BA

July 2009

5-26

Page 49

Reference Manual

00821-0100-4809, Rev BA July 2009

Rosemount Annubar

Flow Test Data Book

Table 5-15. Alden Research Labs, Water.

Run Number

1 107 41.5 95 35 97008 44002 40.024 16.7074 17592 94.790 3.6997 0.5829 2 107 41.5 95 35 96976 43987 40.017 16.7274 17590 95.088 3.7028 0.5820 3 107 41.5 95 35 97022 44008 40.093 16.6368 17565 93.741 3.6976 0.5853 4 107 41.5 95 35 96403 43727 44.924 15.2151 15576 73.852 3.2855 0.5848 5 107 41.5 95 35 96375 43715 44.969 15.2099 15557 73.784 3.2813 0.5844 6 107 41.5 95 35 96306 43684 44.876 15.2076 15578 73.754 3.2890 0.5852 7 107 41.5 95 35 95867 43485 57.724 12.6661 12056 44.124 2.5479 0.5855 8 107 41.5 95 35 96041 43564 57.810 12.6539 12060 44.000 2.5513 0.5867 9 107 41.5 95 35 95863 43483 57.746 12.6681 12051 44.144 2.5521 0.5852 10 107 41.5 95 35 95307 43231 77.732 19.7422 8901 24.253 1.8868 0.5832 11 108 42.2 95 35 95388 43267 77.879 19.6499 8892 23.970 1.8868 0.5859 12 108 42.2 95 35 95370 43259 77.865 19.7187 8892 24.180 1.8887 0.5834 13 108 42.2 95 35 94838 43017 126.452 13.5666 5445 8.969 1.1577 0.5867 14 108 42.2 95 35 94929 43059 126.555 13.6116 5446 9.053 1.1579 0.5837 15 108 42.2 95 35 94885 43039 126.432 13.5905 5449 9.014 1.1596 0.5855

Line Temp Air Temp Net Weight

°F °C °F °C lb kg seconds GPM Inch W/C x 10

Reynolds Number Low Limit: 303906

Run Duration

mA Square Root Output

Flow

Differential Head

Pipe Reynold Number

5-27

Page 50

Rosemount Annubar Flow Test Data Book

Reference Manual

00821-0100-4809, Rev BA

July 2009

585 SENSOR SIZE 11

Table 5-16. Flow Coefficient Data Summary: Sensor 11

Calibration

Number

18243 DSI 4" S40 DS-879 4.055 25.1% 0.5623 0.5633 18249 DSI 4" S40 DS-879 4.055 25.1% 0.5625 0.5633 18964 DSI 10" S40 DS-878 10.083 10.1% 0.6398 0.6351 19057 DSI 8" S40 DS-859 7.990 12.7% 0.6186 0.6238 19219 DSI 6" S40 DS-1003 6.123 16.6% 0.6090 0.6063 19232 DSI 6" S40 DS-1003 6.123 16.6% 0.6090 0.6063 19766 DSI 4" S80 DS-889 3.800 26.8% 0.5496 0.5539

07DSC-0009 CEESI-CO 4" S40 DS-879 4.055 25.1% 0.5621 0.5633

LAB Pipe Size Spool No ID Blockage

Calibrated Average K

Published K

5-28

Page 51

Reference Manual

00821-0100-4809, Rev BA July 2009

Sensor Size: 11 Fluid: Water Sensor Serial Number: 585-11-1 Pipe Size: 4-in. S40 Test Spool: DS-879

Rosemount Annubar

Flow Test Data Book

Test Laboratory: Rosemount Boulder, Colorado Flow Lab

Test Date: September 28, 2007 Test Pipe Dia.: 4.055-in (103 mm) Blockage: 25.12% K

: 0.5633

pub

Average K: 0.5618 Calibration ID: 18243

5-29

Page 52

Rosemount Annubar Flow Test Data Book

Reference Manual

00821-0100-4809, Rev BA

July 2009

Data

Point

Number

1 707.7 160.7 181.95 452.4 71.1 21.7 37.1 2.6 0.961 62.29 997.7 17.58 5.36 3.85E+05 0.5627 2 693.5 157.5 175.69 436.8 71.2 21.8 37.2 2.6 0.960 62.29 997.7 17.23 5.25 3.78E+05 0.5611 3 647.0 146.9 152.07 378.1 71.2 21.8 37.4 2.6 0.959 62.29 997.7 16.07 4.90 3.53E+05 0.5627 4 655.3 148.8 156.14 388.2 71.2 21.8 37.3 2.6 0.960 62.29 997.7 16.28 4.96 3.57E+05 0.5625 5 602.7 136.9 132.19 328.7 71.2 21.8 37.6 2.6 0.959 62.29 997.7 14.97 4.56 3.28E+05 0.5623 6 603.2 137.0 132.56 329.6 71.2 21.8 37.6 2.6 0.960 62.29 997.7 14.99 4.57 3.29E+05 0.5619 7 556.4 126.4 113.12 281.3 71.2 21.8 37.8 2.6 0.960 62.29 997.7 13.82 4.21 3.03E+05 0.5611 8 546.7 124.2 108.96 270.9 71.2 21.8 37.8 2.6 0.960 62.29 997.7 13.58 4.14 2.98E+05 0.5617 9 500.9 113.8 91.46 227.4 71.2 21.8 38.0 2.6 0.960 62.29 997.7 12.44 3.79 2.73E+05 0.5618 10 497.4 113.0 90.12 224.1 71.2 21.8 38.0 2.6 0.960 62.29 997.7 12.36 3.77 2.71E+05 0.5620 11 454.1 103.1 75.19 187.0 71.2 21.8 38.2 2.6 0.960 62.29 997.7 11.28 3.44 2.47E+05 0.5617 12 451.8 102.6 74.31 184.8 71.1 21.7 37.7 2.6 0.961 62.29 997.7 11.23 3.42 2.46E+05 0.5622 13 399.5 90.7 58.12 144.5 71.1 21.7 38.3 2.6 0.961 62.29 997.7 9.92 3.03 2.17E+05 0.5621 14 399.2 90.7 58.06 144.3 71.1 21.7 38.1 2.6 0.961 62.29 997.7 9.92 3.02 2.17E+05 0.5620 15 349.4 79.3 44.53 110.7 71.1 21.7 38.0 2.6 0.961 62.29 997.7 8.68 2.65 1.90E+05 0.5615 16 350.4 79.6 44.85 111.5 71.1 21.7 37.6 2.6 0.961 62.29 997.7 8.71 2.65 1.91E+05 0.5612 17 298.5 67.8 32.37 80.5 71.1 21.7 38.1 2.6 0.961 62.29 997.7 7.41 2.26 1.62E+05 0.5627 18 301.3 68.4 33.07 82.2 71.1 21.7 37.6 2.6 0.962 62.29 997.7 7.48 2.28 1.64E+05 0.5618 19 248.8 56.5 22.49 55.9 71.1 21.7 37.9 2.6 0.962 62.29 997.7 6.18 1.88 1.35E+05 0.5629 20 249.6 56.7 22.65 56.3 71.1 21.7 38.1 2.6 0.961 62.29 997.7 6.20 1.89 1.36E+05 0.5627 21 704.7 160.0 180.36 448.5 71.0 21.6 37.1 2.6 0.963 62.29 997.8 17.51 5.34 3.83E+05 0.5628 22 692.6 157.3 174.37 433.5 71.0 21.6 37.1 2.6 0.963 62.29 997.8 17.21 5.24 3.76E+05 0.5626 23 645.8 146.7 151.80 377.4 71.0 21.6 37.3 2.6 0.963 62.29 997.8 16.04 4.89 3.51E+05 0.5622 24 654.0 148.5 155.60 386.9 71.0 21.6 37.3 2.6 0.963 62.29 997.8 16.25 4.95 3.55E+05 0.5623 25 600.4 136.4 130.97 325.6 71.0 21.6 37.5 2.6 0.963 62.29 997.8 14.92 4.55 3.26E+05 0.5627 26 609.1 138.3 134.66 334.8 71.0 21.7 37.5 2.6 0.963 62.29 997.8 15.13 4.61 3.31E+05 0.5630 27 556.3 126.4 113.48 282.2 71.0 21.7 37.8 2.6 0.963 62.29 997.8 13.82 4.21 3.02E+05 0.5601 28 545.4 123.9 108.99 271.0 71.0 21.7 37.8 2.6 0.963 62.29 997.8 13.55 4.13 2.96E+05 0.5603 29 502.3 114.1 92.11 229.0 71.0 21.7 38.0 2.6 0.962 62.29 997.8 12.48 3.80 2.73E+05 0.5613 30 491.9 111.7 88.35 229.0 71.0 21.7 38.1 2.6 0.962 62.29 997.8 12.22 3.72 2.67E+05 0.5613 31 450.1 102.2 74.22 184.5 71.0 21.6 37.5 2.6 0.963 62.29 997.8 11.18 3.41 2.44E+05 0.5604 32 447.6 101.7 73.39 182.5 71.0 21.7 38.0 2.6 0.963 62.29 997.8 11.12 3.39 2.43E+05 0.5604 33 398.1 90.4 57.93 144.0 71.0 21.7 37.7 2.6 0.963 62.29 997.8 9.89 3.01 2.16E+05 0.5609 34 411.7 93.5 62.06 154.3 71.0 21.7 37.9 2.6 0.963 62.29 997.8 10.23 3.12 2.24E+05 0.5605 35 348.1 79.1 44.37 110.3 71.0 21.7 37.9 2.6 0.963 62.29 997.8 8.65 2.64 1.89E+05 0.5605 36 349.6 79.4 44.64 111.0 71.0 21.7 37.5 2.6 0.963 62.29 997.8 8.68 2.65 1.90E+05 0.5612 37 298.0 67.7 32.42 80.6 71.0 21.7 37.9 2.6 0.962 62.29 997.8 7.40 2.26 1.62E+05 0.5614 38 300.7 68.3 32.98 82.0 71.0 21.7 37.7 2.6 0.963 62.29 997.8 7.47 2.28 1.63E+05 0.5616 39 248.9 56.5 22.55 56.1 71.0 21.7 38.2 2.6 0.962 62.29 997.8 6.18 1.88 1.35E+05 0.5621 40 249.3 56.6 22.64 56.3 71.0 21.6 37.6 2.6 0.963 62.29 997.8 6.19 1.89 1.35E+05 0.5621

Flow Rate

GPM m3/h inH2O mbar °F °C psig bar g cP lb/ft3kg/m3ft/s m/s

Differential

Pressure

Fluid

Temperature

Fluid

Pressure

Fluid

Viscosity

Fluid Density Fluid Velocity

Pipe

Reynolds

Number

5-30

Page 53

Reference Manual

00821-0100-4809, Rev BA July 2009

Sensor Size: 11 Fluid: Water Sensor Serial Number: 585-11-1 Pipe Size: 4-in. S40 Test Spool: DS-879

Rosemount Annubar

Flow Test Data Book

Test Laboratory: Rosemount - Boulder, Colorado Flow Lab

Test Date: September 29, 2007 Test Pipe Dia.: 4.055-in (103 mm) Blockage: 25.12% K

: 0.5633

pub

Average K: 0.5621 Calibration ID: 18249

5-31

Page 54

Rosemount Annubar Flow Test Data Book

Reference Manual

00821-0100-4809, Rev BA

July 2009

Data

Point

Number

1 706.1 160.4 182.33 453.3 70.7 21.5 37.1 2.6 0.967 62.29 997.8 17.54 5.35 3.82E+05 0.5609 2 644.0 146.3 151.28 376.1 70.7 21.5 37.4 2.6 0.967 62.29 997.8 16.00 4.88 3.48E+05 0.5616 3 601.7 136.7 131.94 328.1 70.7 21.5 37.5 2.6 0.967 62.29 997.8 14.95 4.56 3.26E+05 0.5619 4 556.9 126.5 113.29 281.7 70.7 21.5 37.7 2.6 0.966 62.29 997.8 13.84 4.22 3.01E+05 0.5612 5 506.2 115.0 93.37 232.2 70.7 21.5 37.9 2.6 0.967 62.29 997.8 12.58 3.83 2.74E+05 0.5619 6 454.8 103.3 75.51 187.7 70.7 21.5 38.2 2.6 0.966 62.29 997.8 11.30 3.44 2.46E+05 0.5614 7 396.7 90.1 57.50 143.0 70.6 21.4 37.6 2.6 0.967 62.29 997.8 9.85 3.00 2.15E+05 0.5611 8 349.1 79.3 44.44 110.5 70.7 21.5 37.8 2.6 0.967 62.29 997.8 8.67 2.64 1.89E+05 0.5617 9 299.4 68.0 32.60 81.0 70.7 21.5 38.4 2.6 0.966 62.29 997.8 7.44 2.27 1.62E+05 0.5624 10 249.4 56.6 22.58 56.2 70.7 21.5 37.6 2.6 0.967 62.29 997.8 6.19 1.89 1.35E+05 0.5628 11 710.7 161.4 183.35 455.9 70.6 21.4 37.1 2.6 0.968 62.29 997.8 17.66 5.38 3.84E+05 0.5630 12 644.9 146.5 151.37 376.4 70.6 21.4 37.4 2.6 0.968 62.29 997.8 16.02 4.88 3.49E+05 0.5622 13 601.0 136.5 131.39 326.7 70.6 21.4 37.6 2.6 0.968 62.29 997.8 14.93 4.55 3.25E+05 0.5624 14 557.0 126.5 113.13 281.3 70.6 21.4 37.7 2.6 0.967 62.29 997.8 13.84 4.22 3.01E+05 0.5617 15 505.2 114.7 93.09 231.5 70.6 21.4 37.7 2.6 0.968 62.29 997.8 12.55 3.83 2.73E+05 0.5616 16 455.2 103.4 75.45 187.6 70.6 21.4 38.2 2.6 0.967 62.29 997.8 11.31 3.45 2.46E+05 0.5621 17 396.8 90.1 57.22 142.3 70.6 21.4 38.0 2.6 0.967 62.29 997.8 9.86 3.00 2.14E+05 0.5626 18 349.7 79.4 44.42 110.4 70.6 21.4 37.8 2.6 0.968 62.29 997.8 8.69 2.65 1.89E+05 0.5628 19 298.6 67.8 32.36 80.5 70.6 21.4 37.7 2.6 0.967 62.29 997.8 7.42 2.26 1.61E+05 0.5630 20 249.5 56.7 22.59 56.2 70.7 21.5 38.6 2.7 0.967 62.29 997.8 6.20 1.89 1.35E+05 0.5631

Flow Rate

GPM m3/h inH2O mbar °F °C psig bar g cP lb/ft3kg/m3ft/s m/s

Differential

Pressure

Fluid

Temperature

Fluid

Pressure

Fluid

Viscosity

Fluid Density Fluid Velocity

Pipe

Reynolds

Number

5-32

Page 55

Reference Manual

00821-0100-4809, Rev BA July 2009

Sensor Size: 11 Fluid: Water Sensor Serial Number: 585-11-7 Pipe Size: 10-in. S40 Test Spool: DS-878

Rosemount Annubar

Flow Test Data Book

Test Laboratory: Rosemount - Boulder, Colorado Flow Lab

Test Date: January 7, 2008 Test Pipe Dia.: 10.083-in (256 mm) Blockage: 10.10% K

: 0.6351

pub

Average K: 0.6390 Calibration ID: 18964

Data

Point

Number

1 499.4 113.4 1.86 4.6 71.5 21.9 37.6 2.6 0.957 62.28 997.7 2.01 0.61 1.10E+05 0.6355 2 1006.8 228.7 7.41 18.4 71.5 21.9 34.6 2.4 0.957 62.28 997.7 4.05 1.23 2.21E+05 0.6417 3 1503.3 341.4 16.57 41.2 71.5 22.0 31.4 2.2 0.956 62.28 997.7 6.04 1.84 3.31E+05 0.6405 4 2003.2 455.0 29.57 73.5 71.6 22.0 28.6 2.0 0.955 62.28 997.7 8.05 2.45 4.41E+05 0.6390 5 2491.7 565.9 45.89 114.1 71.7 22.1 25.5 1.8 0.953 62.28 997.7 10.01 3.05 5.50E+05 0.6380 6 3025.1 687.1 67.75 168.4 71.9 22.1 21.1 1.5 0.951 62.28 997.6 12.15 3.70 6.69E+05 0.6375 8 1003.8 228.0 7.37 18.3 72.2 22.3 34.9 2.4 0.948 62.28 997.6 4.03 1.23 2.23E+05 0.6412 9 1503.5 341.5 16.60 41.3 72.2 22.3 31.4 2.2 0.947 62.28 997.6 6.04 1.84 3.34E+05 0.6401 10 2008.6 456.2 29.80 74.1 72.3 22.4 28.6 2.0 0.946 62.28 997.6 8.07 2.46 4.46E+05 0.6382 11 2499.7 567.7 46.27 115.0 72.4 22.4 25.4 1.8 0.945 62.28 997.6 10.04 3.06 5.56E+05 0.6374 12 3030.2 688.2 67.72 168.4 72.5 22.5 21.1 1.5 0.943 62.28 997.6 12.18 3.71 6.76E+05 0.6387 13 497.8 113.1 1.81 4.5 72.8 22.7 38.0 2.6 0.939 62.27 997.5 2.00 0.61 1.11E+05 0.6411 14 1007.3 228.8 7.45 18.5 72.8 22.7 34.8 2.4 0.940 62.27 997.5 4.05 1.23 2.25E+05 0.6403 15 1500.0 340.7 16.55 41.2 72.9 22.7 31.3 2.2 0.939 62.27 997.5 6.03 1.84 3.36E+05 0.6395 16 2008.9 456.3 29.77 74.0 73.0 22.8 28.5 2.0 0.938 62.27 997.5 8.07 2.46 4.50E+05 0.6386 17 2499.6 567.7 46.16 114.8 73.1 22.8 25.3 1.7 0.937 62.27 997.5 10.04 3.06 5.61E+05 0.6381 18 3025.7 687.2 67.76 168.5 73.2 22.9 21.1 1.5 0.935 62.27 997.5 12.16 3.71 6.80E+05 0.6375

Flow Rate

GPM m3/h inH2O mbar °F °C psig bar g cP lb/ft3kg/m3ft/s m/s

Differential

Pressure

Fluid

Temperature

Fluid

Pressure

Fluid

Viscosity

Fluid Density F luid Velocity

Pipe

Reynolds

Number

5-33

Page 56

Rosemount Annubar Flow Test Data Book

Test Laboratory: Rosemount - Boulder, Colorado Flow Lab

Sensor Size: 11 Fluid: Water Sensor Serial Number: 585-11-6 Pipe Size: 8-in. S40 Test Spool: DS-859

Test Date: January 17, 2008 Test Pipe Dia.: 7.990-in (203 mm) Blockage: 12.75% K

: 0.6238

pub

Average K: 0.6186 Calibration ID: 19057

Reference Manual

00821-0100-4809, Rev BA

July 2009

Data

Point

Number

1 2661.5 604.5 141.50 351.8 78.5 25.8 24.2 1.7 0.874 62.22 996.7 17.03 5.19 8.07E+05 0.6178 2 2537.2 576.3 128.89 320.5 78.5 25.8 25.0 1.7 0.874 62.22 996.7 16.23 4.95 7.69E+05 0.6171 3 2011.1 456.8 80.71 200.7 78.5 25.8 28.4 2.0 0.874 62.22 996.7 12.87 3.92 6.10E+05 0.6181 4 1510.7 343.1 45.59 113.3 78.5 25.8 31.1 2.1 0.874 62.22 996.7 9.67 2.95 4.58E+05 0.6178 5 1000.0 227.1 19.79 49.2 78.5 25.8 34.8 2.4 0.874 62.22 996.7 6.40 1.95 3.03E+05 0.6206 6 499.0 113.3 4.95 12.3 78.6 25.9 37.9 2.6 0.873 62.22 996.7 3.19 0.97 1.52E+05 0.6191 7 2659.6 604.1 141.10 350.8 78.4 25.8 24.2 1.7 0.875 62.23 996.8 17.02 5.19 8.06E+05 0.6182 8 2535.7 575.9 128.79 320.2 78.4 25.8 25.0 1.7 0.875 62.23 996.8 16.23 4.95 7.68E+05 0.6170 9 2012.7 457.1 80.60 200.4 78.4 25.8 28.4 2.0 0.875 62.23 996.8 12.88 3.93 6.10E+05 0.6190 10 1502.7 341.3 44.89 111.6 78.4 25.8 30.9 2.1 0.875 62.23 996.8 9.62 2.93 4.55E+05 0.6192 11 1003.2 227.9 19.72 49.0 78.4 25.8 34.7 2.4 0.874 62.22 996.7 6.42 1.96 3.04E+05 0.6237 12 500.5 113.7 4.95 12.3 78.5 25.8 37.9 2.6 0.874 62.22 996.7 3.20 0.98 1.52E+05 0.6209 13 2661.4 604.4 141.99 353.0 78.3 25.7 24.1 1.7 0.876 62.23 996.8 17.03 5.19 8.05E+05 0.6167 14 2532.4 575.2 128.47 319.4 78.3 25.7 25.0 1.7 0.876 62.23 996.8 16.20 4.94 7.66E+05 0.6169 15 2009.3 456.3 80.82 200.9 78.3 25.7 28.4 2.0 0.876 62.23 996.8 12.86 3.92 6.08E+05 0.6171 16 1505.2 341.9 45.13 112.2 78.3 25.7 30.9 2.1 0.876 62.23 996.8 9.63 2.94 4.56E+05 0.6187 17 1001.9 227.6 20.07 49.9 78.3 25.7 34.5 2.4 0.875 62.23 996.8 6.41 1.95 3.03E+05 0.6175 18 497.4 113.0 4.91 12.2 78.4 25.8 37.9 2.6 0.874 62.22 996.7 3.18 0.97 1.51E+05 0.6200

5-34

Flow Rate

GPM m3/h inH2O mbar °F °C psig bar g cP lb/ft3kg/m3ft/s m/s

Differential

Pressure

Fluid

Temperature

Fluid

Pressure

Fluid

Viscosity

Fluid Density F luid Velocity

Pipe

Reynolds

Number

Page 57

Reference Manual

00821-0100-4809, Rev BA July 2009

Sensor Size: 11 Fluid: Water Sensor Serial Number: 585-11-5 Pipe Size: 6-in. S40 Test Spool: DS-1003

Rosemount Annubar

Flow Test Data Book

Test Laboratory: Rosemount - Boulder, Colorado Flow Lab

Test Date: January 28, 2008 Test Pipe Dia.: 6.123-in (156 mm) Blockage: 16.64% K

: 0.6063

pub

Average K: 0.6085 Calibration ID: 19219

Data

Point

Number

1 1791.3 406.8 193.93 482.2 70.7 21.5 29.5 2.0 0.966 62.29 997.8 19.52 5.95 6.42E+05 0.6051 2 1485.7 337.4 133.24 331.3 70.7 21.5 31.2 2.2 0.966 62.29 997.8 16.19 4.93 5.32E+05 0.6055 3 1201.6 272.9 86.30 214.6 70.7 21.5 32.9 2.3 0.966 62.29 997.8 13.09 3.99 4.31E+05 0.6085 4 902.8 205.0 48.68 121.0 70.7 21.5 35.2 2.4 0.966 62.29 997.8 9.84 3.00 3.24E+05 0.6087 5 594.4 135.0 20.59 51.2 70.8 21.5 37.3 2.6 0.965 62.29 997.8 6.48 1.97 2.13E+05 0.6162 6 298.9 67.9 5.36 13.3 70.8 21.6 38.0 2.6 0.964 62.29 997.8 3.26 0.99 1.07E+05 0.6076 7 1846.6 419.4 206.73 514.0 70.6 21.5 28.7 2.0 0.967 62.29 997.8 20.12 6.13 6.61E+05 0.6042 8 1482.4 336.7 132.69 329.9 70.6 21.5 30.9 2.1 0.967 62.29 997.8 16.15 4.92 5.31E+05 0.6054 9 1200.9 272.8 86.14 214.2 70.6 21.5 32.3 2.2 0.967 62.29 997.8 13.09 3.99 4.30E+05 0.6087 10 903.0 205.1 48.31 120.1 70.7 21.5 34.9 2.4 0.967 62.29 997.8 9.84 3.00 3.24E+05 0.6112 11 592.2 134.5 20.57 51.1 70.7 21.5 37.1 2.6 0.966 62.29 997.8 6.45 1.97 2.12E+05 0.6143 12 299.3 68.0 5.39 13.4 70.8 21.5 37.9 2.6 0.965 62.29 997.8 3.26 0.99 1.07E+05 0.6065 13 1849.0 419.9 206.51 513.5 70.6 21.4 28.6 2.0 0.968 62.29 997.8 20.15 6.14 6.62E+05 0.6053 14 1510.0 342.9 137.12 340.9 70.6 21.4 30.3 2.1 0.968 62.29 997.8 16.45 5.01 5.40E+05 0.6066 15 1201.7 272.9 86.61 215.4 70.6 21.4 32.6 2.2 0.968 62.29 997.8 13.09 3.99 4.30E+05 0.6074 16 900.9 204.6 47.89 119.1 70.6 21.5 35.1 2.4 0.967 62.29 997.8 9.82 2.99 3.23E+05 0.6125 17 595.3 135.2 20.94 52.1 70.7 21.5 37.2 2.6 0.967 62.29 997.8 6.49 1.98 2.13E+05 0.6120 18 299.2 68.0 5.36 13.3 70.7 21.5 38.2 2.6 0.966 62.29 997.8 3.26 0.99 1.07E+05 0.6082

Flow Rate

GPM m3/h inH2O mbar °F °C psig bar g cP lb/ft3kg/m3ft/s m/s

Differential

Pressure

Fluid

Temperature

Fluid

Pressure

Fluid

Viscosity

Fluid Density F luid Velocity

Pipe

Reynolds

Number

5-35

Page 58

Rosemount Annubar Flow Test Data Book

Test Laboratory: Rosemount - Boulder, Colorado Flow Lab

Sensor Size: 11 Fluid: Water Sensor Serial Number: 585-11-5 Pipe Size: 6-in. S40 Test Spool: DS-1003

Test Date: January 29, 2008 Test Pipe Dia.: 6.123-in (156 mm) Blockage: 16.64% K

: 0.6063

pub

Average K: 0.6085 Calibration ID: 19232

Reference Manual

00821-0100-4809, Rev BA

July 2009

Data

Point

Number

1 1800.4 408.9 196.67 489.0 70.7 21.5 29.3 2.0 0.967 62.29 997.8 19.62 5.98 6.45E+05 0.6039 2 1485.4 337.4 132.27 328.9 70.8 21.6 31.3 2.2 0.965 62.29 997.8 16.18 4.93 5.33E+05 0.6076 3 1205.5 273.8 86.97 216.2 70.9 21.6 33.0 2.3 0.963 62.29 997.8 13.14 4.00 4.33E+05 0.6081 4 902.4 204.9 48.46 120.5 71.1 21.7 35.1 2.4 0.962 62.29 997.7 9.83 3.00 3.25E+05 0.6098 5 593.9 134.9 20.77 51.7 71.2 21.8 37.2 2.6 0.960 62.29 997.7 6.47 1.97 2.14E+05 0.6130 6 299.1 67.9 5.38 13.4 71.4 21.9 38.2 2.6 0.958 62.28 997.7 3.26 0.99 1.08E+05 0.6065 7 1833.1 416.3 202.34 503.1 71.3 21.8 29.0 2.0 0.959 62.29 997.7 19.97 6.09 6.62E+05 0.6062 8 1488.9 338.2 133.54 332.0 71.4 21.9 31.1 2.1 0.958 62.28 997.7 16.22 4.94 5.38E+05 0.6061 9 1200.6 272.7 86.20 214.3 71.5 21.9 33.0 2.3 0.956 62.28 997.7 13.08 3.99 4.35E+05 0.6083 10 903.0 205.1 48.30 120.1 71.6 22.0 35.4 2.4 0.955 62.28 997.7 9.84 3.00 3.28E+05 0.6112 11 596.1 135.4 20.94 52.1 71.7 22.1 37.4 2.6 0.953 62.28 997.7 6.49 1.98 2.17E+05 0.6128 12 299.6 68.1 5.36 13.3 71.9 22.2 38.1 2.6 0.951 62.28 997.6 3.26 1.00 1.09E+05 0.6086 13 1842.8 418.5 206.15 512.6 71.8 22.1 28.7 2.0 0.953 62.28 997.7 20.08 6.12 6.70E+05 0.6037 14 1488.0 338.0 133.62 332.2 71.9 22.1 31.4 2.2 0.952 62.28 997.6 16.21 4.94 5.41E+05 0.6055 15 1201.5 272.9 85.99 213.8 71.9 22.2 33.0 2.3 0.951 62.28 997.6 13.09 3.99 4.38E+05 0.6095 16 899.4 204.3 47.97 119.3 72.0 22.2 35.7 2.5 0.950 62.28 997.6 9.80 2.99 3.28E+05 0.6108 17 590.9 134.2 20.69 51.4 72.0 22.2 37.5 2.6 0.949 62.28 997.6 6.44 1.96 2.15E+05 0.6110 18 300.9 68.3 5.38 13.4 72.1 22.3 38.5 2.7 0.948 62.28 997.6 3.28 1.00 1.10E+05 0.6101

5-36

Flow Rate

GPM m3/h inH2O mbar °F °C psig bar g cP lb/ft3kg/m3ft/s m/s

Differential

Pressure

Fluid

Temperature

Fluid

Pressure

Fluid

Viscosity

Fluid Density F luid Velocity

Pipe

Reynolds

Number

Page 59

Reference Manual

00821-0100-4809, Rev BA July 2009

Sensor Size: 11 Fluid: Water Sensor Serial Number: 585-11-3 Pipe Size: 4-in. S80 Test Spool: DS-889

Rosemount Annubar

Flow Test Data Book

Test Laboratory: Rosemount - Boulder, Colorado Flow Lab

Test Date: March 27, 2008 Test Pipe Dia.: 3.800-in (97 mm) Blockage: 26.80% K

: 0.5539

pub

Average K: 0.5500 Calibration ID: 19766

Data

Point

Number

1 657.7 149.4 213.14 530.0 68.7 20.4 37.4 2.6 0.992 62.30 998.0 18.60 5.67 3.70E+05 0.5502 2 563.4 127.9 157.18 390.8 68.8 20.4 37.8 2.6 0.992 62.30 998.0 15.94 4.86 3.17E+05 0.5489 3 456.4 103.7 103.02 256.2 68.8 20.4 38.2 2.6 0.991 62.30 998.0 12.91 3.94 2.57E+05 0.5493 4 349.1 79.3 60.07 149.4 68.8 20.4 38.4 2.6 0.991 62.30 998.0 9.88 3.01 1.97E+05 0.5502 5 248.5 56.4 30.40 75.6 68.8 20.4 37.8 2.6 0.991 62.30 998.0 7.03 2.14 1.40E+05 0.5505 6 149.3 33.9 10.92 27.2 68.8 20.4 38.2 2.6 0.991 62.30 998.0 4.22 1.29 8.41E+04 0.5517 7 662.1 150.4 216.23 537.6 68.7 20.4 37.4 2.6 0.992 62.30 998.0 18.73 5.71 3.73E+05 0.5500 8 563.6 128.0 157.14 390.7 68.8 20.4 37.8 2.6 0.992 62.30 998.0 15.94 4.86 3.17E+05 0.5492 9 454.8 103.3 102.15 254.0 68.8 20.4 38.0 2.6 0.992 62.30 998.0 12.87 3.92 2.56E+05 0.5496 10 348.4 79.1 59.90 148.9 68.8 20.4 38.1 2.6 0.991 62.30 998.0 9.86 3.00 1.96E+05 0.5499 11 248.4 56.4 30.51 75.9 68.8 20.4 37.9 2.6 0.992 62.30 998.0 7.03 2.14 1.40E+05 0.5494 12 149.5 34.0 10.94 27.2 68.8 20.4 38.1 2.6 0.991 62.30 998.0 4.23 1.29 8.42E+04 0.5522 13 658.9 149.7 214.65 533.7 68.7 20.4 37.4 2.6 0.992 62.30 998.0 18.64 5.68 3.71E+05 0.5494 14 562.8 127.8 156.57 389.3 68.7 20.4 37.8 2.6 0.992 62.30 998.0 15.92 4.85 3.17E+05 0.5494 15 456.3 103.6 102.86 255.8 68.8 20.4 38.2 2.6 0.992 62.30 998.0 12.91 3.93 2.57E+05 0.5495 16 348.9 79.2 60.38 150.1 68.8 20.4 38.1 2.6 0.992 62.30 998.0 9.87 3.01 1.96E+05 0.5485 17 248.4 56.4 30.45 75.7 68.8 20.4 37.7 2.6 0.992 62.30 998.0 7.03 2.14 1.40E+05 0.5498 18 149.1 33.9 10.89 27.1 68.8 20.4 38.0 2.6 0.991 62.30 998.0 4.22 1.29 8.39E+04 0.5518

Flow Rate

GPM m3/h inH2O mbar °F °C psig bar g cP lb/ft3kg/m3ft/s m/s

Differential

Pressure

Fluid

Temperature

Fluid

Pressure

Fluid

Viscosity

Fluid Density F luid Velocity

Pipe

Reynolds

Number

5-37

Page 60

Rosemount Annubar Flow Test Data Book

Sensor Size: 11 Fluid: Air Sensor Serial Number: 585-11-1 Pipe Size: 4-in. S40 Test Spool: DS-879

Test Laboratory: CEESI - Nunn, Colorado

Test Date: April 7, 2008 Test Pipe Dia.: 4.055-in (103 mm) Blockage: 25.12% K

: 0.5633

pub

Average K: 0.5628 Calibration ID: 07DSC-0009

Reference Manual

00821-0100-4809, Rev BA

July 2009

Data

Point

Number

1 14.9 6.8 162.88 405.0 405.0 507.2 281.8 299.0 0.999 1.61 25.8 103.15 31.44 4.84E+06 0.5618 2 14.9 6.8 163.09 405.5 405.5 507.3 281.8 299.0 0.999 1.61 25.8 103.19 31.45 4.84E+06 0.5616 3 10.6 4.8 81.96 203.8 203.8 508.3 282.4 299.0 0.999 1.61 25.7 73.45 22.39 3.43E+06 0.5631 4 10.6 4.8 81.97 203.8 203.8 508.6 282.6 299.0 0.999 1.61 25.7 73.46 22.39 3.43E+06 0.5631 5 6.6 3.0 31.63 78.7 510.2 283.4 283.4 299.0 1.000 1.60 25.6 45.70 13.93 2.12E+06 0.5625 6 6.6 3.0 31.46 78.2 510.7 283.7 283.7 299.0 1.000 1.60 25.6 45.75 13.94 2.12E+06 0.5644 7 7.0 3.2 36.69 91.2 517.2 287.3 287.3 299.0 1.000 1.58 25.3 49.61 15.12 2.24E+06 0.5630 8 7.0 3.2 36.71 91.3 517.1 287.3 287.3 299.0 1.000 1.58 25.3 49.59 15.12 2.24E+06 0.5628 9 3.1 1.4 7.10 17.7 516.4 286.9 286.9 299.0 1.000 1.58 25.3 21.82 6.65 9.89E+05 0.5628 10 3.1 1.4 7.10 17.7 516.5 286.9 286.9 299.0 1.000 1.58 25.3 21.83 6.65 9.89E+05 0.5632

5-38

Flow Rate

GPM m3/h inH2O mbar °R °C psia bar a lb/ft3kg/m3ft/s m/s

Differential

Pressure

Fluid

Temperature

Fluid Pressure

Gas Exp.

Factor

Fluid Density Fluid Velocity

Pipe

Reynolds

Number

Page 61

Reference Manual

00821-0100-4809, Rev BA July 2009

Rosemount Annubar

Flow Test Data Book

585 SENSOR SIZE 22

Table 5-17. Flow Coefficient Data Summary: Sensor 22

Calibration

Number

18248 DSI 6" S40 DS-897 6.075 25.2% 0.5550 0.5569 18242 DSI 6" S40 DS-897 6.075 25.2% 0.5548 0.5569 19413 DSI 10" S40 DS-878 10.080 15.2% 0.6115 0.6091 19805 DSI 10" S40 DS-878 10.080 15.2% 0.6120 0.6091 19807 DSI 10" S40 DS-878 10.080 15.2% 0.6124 0.6091 19998 DSI 5" S40 DS-943 5.110 29.9% 0.5332 0.5285 19999 DSI 5" S40 DS-943 5.110 29.9% 0.5332 0.5285

08DSC-0002 CEESI-CO 8" S10 DS-995 8.350 18.3% 0.5890 0.5938

LAB Pipe Size Spool No ID Blockage

Calibrated Average K

Published K

5-39

Page 62

Rosemount Annubar Flow Test Data Book

Test Laboratory: Rosemount - Boulder, Colorado Flow Lab

Sensor Size: 22 Fluid: Water Sensor Serial Number: 585-22-1 Pipe Size: 6-in. S80 Test Spool: DS-897

Test Date: September 28, 2007 Test Pipe Dia.: 6.075-in (154 mm) Blockage: 25.15% K

: 0.5569

pub

Average K: 0.5544 Calibration ID: 18242

Reference Manual

00821-0100-4809, Rev BA

July 2009

5-40

Page 63

Reference Manual

00821-0100-4809, Rev BA July 2009

Rosemount Annubar

Flow Test Data Book

Data

Point

Number

1 1591.2 361.4 189.70 471.7 70.0 21.1 30.8 2.1 0.975 62.29 997.9 17.61 5.37 5.70E+05 0.5521 2 1395.5 316.9 146.50 364.2 70.1 21.1 32.1 2.2 0.975 62.29 997.9 15.45 4.71 5.00E+05 0.5510 3 1194.3 271.2 106.83 265.6 70.1 21.2 33.5 2.3 0.974 62.29 997.9 13.22 4.03 4.28E+05 0.5522 4 1004.5 228.2 75.20 187.0 70.1 21.1 34.1 2.3 0.974 62.29 997.9 11.12 3.39 3.60E+05 0.5536 5 799.0 181.5 47.38 117.8 70.1 21.2 36.6 2.5 0.974 62.29 997.9 8.84 2.70 2.86E+05 0.5547 6 593.6 134.8 26.07 64.8 70.2 21.2 37.6 2.6 0.973 62.29 997.9 6.57 2.00 2.13E+05 0.5556 7 401.3 91.1 11.88 29.5 70.2 21.2 38.1 2.6 0.973 62.29 997.8 4.44 1.35 1.44E+05 0.5563 8 199.5 45.3 2.89 7.2 70.2 21.2 38.1 2.6 0.972 62.29 997.8 2.21 0.67 7.16E+04 0.5606 9 200.4 45.5 2.90 7.2 70.2 21.2 38.2 2.6 0.972 62.29 997.8 2.22 0.68 7.20E+04 0.5622 10 399.3 90.7 11.81 29.4 70.2 21.2 38.0 2.6 0.973 62.29 997.8 4.42 1.35 1.43E+05 0.5552 11 591.2 134.3 25.85 64.3 70.2 21.2 37.2 2.6 0.973 62.29 997.9 6.54 1.99 2.12E+05 0.5556 12 797.5 181.1 47.32 117.7 70.1 21.2 36.0 2.5 0.974 62.29 997.9 8.83 2.69 2.86E+05 0.5540 13 1005.5 228.4 75.18 186.9 70.1 21.1 34.2 2.4 0.974 62.29 997.9 11.13 3.39 3.60E+05 0.5542 14 1205.7 273.8 108.60 270.0 70.0 21.1 32.8 2.3 0.975 62.29 997.9 13.35 4.07 4.32E+05 0.5529 15 1415.9 321.6 150.57 374.4 70.0 21.1 31.5 2.2 0.975 62.30 997.9 15.67 4.78 5.07E+05 0.5515 16 1621.0 368.2 196.87 489.5 70.0 21.1 30.2 2.1 0.975 62.30 997.9 17.94 5.47 5.80E+05 0.5521 17 1579.4 358.7 186.95 464.8 70.0 21.1 30.4 2.1 0.975 62.29 997.9 17.48 5.33 5.66E+05 0.5521 18 1391.9 316.1 145.27 361.2 70.1 21.1 31.5 2.2 0.975 62.29 997.9 15.41 4.70 4.99E+05 0.5519 19 1195.7 271.6 107.04 266.1 70.1 21.2 32.8 2.3 0.974 62.29 997.9 13.24 4.03 4.28E+05 0.5523 20 1005.4 228.4 75.29 187.2 70.1 21.2 34.1 2.4 0.974 62.29 997.9 11.13 3.39 3.60E+05 0.5537 21 801.5 182.0 47.79 118.8 70.1 21.2 36.3 2.5 0.973 62.29 997.9 8.87 2.70 2.87E+05 0.5541 22 593.9 134.9 26.31 65.4 70.2 21.2 37.4 2.6 0.973 62.29 997.9 6.57 2.00 2.13E+05 0.5533 23 401.8 91.3 11.90 29.6 70.2 21.2 38.2 2.6 0.972 62.29 997.8 4.45 1.36 1.44E+05 0.5566 24 199.8 45.4 2.90 7.2 70.2 21.2 38.1 2.6 0.972 62.29 997.8 2.21 0.67 7.17E+04 0.5610 25 199.9 45.4 2.92 7.3 70.2 21.2 38.2 2.6 0.972 62.29 997.8 2.21 0.67 7.18E+04 0.5593 26 400.5 91.0 11.85 29.5 70.2 21.2 38.3 2.6 0.972 62.29 997.8 4.43 1.35 1.44E+05 0.5559 27 591.4 134.3 26.00 64.6 70.2 21.2 37.2 2.6 0.973 62.29 997.9 6.55 2.00 2.12E+05 0.5542 28 798.1 181.3 47.65 118.5 70.1 21.2 35.9 2.5 0.974 62.29 997.9 8.83 2.69 2.86E+05 0.5525 29 1003.6 227.9 75.10 186.7 70.1 21.2 34.1 2.4 0.974 62.29 997.9 11.11 3.39 3.60E+05 0.5535 30 1209.6 274.7 109.66 272.6 70.1 21.1 32.8 2.3 0.975 62.29 997.9 13.39 4.08 4.33E+05 0.5520 31 1412.5 320.8 149.09 370.7 70.0 21.1 31.9 2.2 0.975 62.30 997.9 15.63 4.77 5.06E+05 0.5529 32 1615.8 367.0 196.30 488.1 70.0 21.1 30.5 2.1 0.975 62.30 997.9 17.89 5.45 5.78E+05 0.5512 33 1592.8 361.8 190.48 473.6 70.0 21.1 30.6 2.1 0.975 62.30 997.9 17.63 5.37 5.70E+05 0.5515 34 1390.1 315.7 144.61 359.6 70.0 21.1 32.0 2.2 0.975 62.29 997.9 15.39 4.69 4.98E+05 0.5525 35 1201.2 272.8 107.66 267.7 70.1 21.1 33.2 2.3 0.974 62.29 997.9 13.30 4.05 4.30E+05 0.5532 36 1002.3 227.6 74.82 186.0 70.1 21.2 34.1 2.4 0.974 62.29 997.9 11.09 3.38 3.59E+05 0.5538 37 801.3 182.0 47.80 118.8 70.1 21.2 36.3 2.5 0.974 62.29 997.9 8.87 2.70 2.87E+05 0.5539 38 594.0 134.9 26.45 65.8 70.2 21.2 37.4 2.6 0.973 62.29 997.9 6.58 2.00 2.13E+05 0.5520 39 402.7 91.5 11.95 29.7 70.2 21.2 38.3 2.6 0.972 62.29 997.8 4.46 1.36 1.45E+05 0.5567 40 199.4 45.3 2.89 7.2 70.2 21.2 38.0 2.6 0.973 62.29 997.8 2.21 0.67 7.16E+04 0.5605

Flow Rate

GPM m3/h inH2O mbar °F °C psig bar g cP lb/ft3kg/m3ft/s m/s

Differential

Pressure

Fluid

Temperature

Fluid

Pressure

Fluid

Viscosity

Fluid Density F luid Velocity

Pipe

Reynolds

Number

5-41

Page 64

Rosemount Annubar Flow Test Data Book

Test Laboratory: Rosemount - Boulder, Colorado Flow Lab

Sensor Size: 22 Fluid: Water Sensor Serial Number: 585-22-1 Pipe Size: 6-in. S80 Test Spool: DS-897

Test Date: September 29, 2007 Test Pipe Dia.: 6.075-in (154 mm) Blockage: 25.15% K

: 0.5569

pub

Average K: 0.5545 Calibration ID: 18248

Reference Manual

00821-0100-4809, Rev BA

July 2009

Data

Point

Number

1 1604.1 364.3 193.20 480.4 70.7 21.5 30.4 2.1 0.966 62.29 997.8 17.76 5.41 5.80E+05 0.5515 2 1391.4 316.0 144.90 360.3 70.8 21.6 31.8 2.2 0.964 62.29 997.8 15.40 4.69 5.04E+05 0.5524 3 1194.5 271.3 106.77 265.5 70.9 21.6 33.1 2.3 0.963 62.29 997.8 13.22 4.03 4.33E+05 0.5524 4 1004.8 228.2 75.14 186.8 71.1 21.7 34.7 2.4 0.962 62.29 997.7 11.12 3.39 3.65E+05 0.5539 5 800.4 181.8 47.57 118.3 71.2 21.8 36.5 2.5 0.960 62.29 997.7 8.86 2.70 2.91E+05 0.5546 6 595.6 135.3 26.36 65.5 71.2 21.8 37.7 2.6 0.959 62.29 997.7 6.59 2.01 2.17E+05 0.5544 7 399.5 90.7 11.85 29.5 71.3 21.8 38.0 2.6 0.959 62.29 997.7 4.42 1.35 1.45E+05 0.5545 8 199.0 45.2 2.86 7.1 71.3 21.8 38.3 2.6 0.959 62.29 997.7 2.20 0.67 7.24E+04 0.5619 9 1617.7 367.4 196.58 196.58 488.8 21.7 30.4 2.1 0.962 62.29 997.7 17.91 5.46 5.87E+05 0.5514 10 1393.0 316.4 145.83 145.83 362.6 21.7 31.9 2.2 0.962 62.29 997.7 15.42 4.70 5.06E+05 0.5512 11 1195.4 271.5 107.04 107.04 266.1 21.7 33.5 2.3 0.962 62.29 997.7 13.23 4.03 4.34E+05 0.5521 12 1005.2 228.3 75.18 75.18 186.9 21.7 34.6 2.4 0.962 62.29 997.7 11.13 3.39 3.65E+05 0.5540 13 801.2 182.0 47.73 47.73 118.7 21.7 36.6 2.5 0.961 62.29 997.7 8.87 2.70 2.91E+05 0.5542 14 594.0 134.9 26.11 26.11 64.9 21.7 37.6 2.6 0.961 62.29 997.7 6.57 2.00 2.16E+05 0.5555 15 398.9 90.6 11.73 11.73 29.2 21.7 37.7 2.6 0.961 62.29 997.7 4.41 1.35 1.45E+05 0.5565 16 199.2 45.2 2.87 2.87 7.1 21.8 38.2 2.6 0.960 62.29 997.7 2.20 0.67 7.24E+04 0.5618

5-42

Flow Rate

GPM m3/h inH2O mbar °F °C psig bar g cP lb/ft3kg/m3ft/s m/s

Differential

Pressure

Fluid

Temperature

Fluid

Pressure

Fluid

Viscosity

Fluid Density Fluid Velocity

Pipe

Reynolds

Number

Page 65

Reference Manual

00821-0100-4809, Rev BA July 2009

Sensor Size: 22 Fluid: Water Sensor Serial Number: 585-22-5 Pipe Size: 10-in. S40 Test Spool: DS-878

Rosemount Annubar

Flow Test Data Book

Test Laboratory: Rosemount - Boulder, Colorado Flow Lab

Test Date: February 20, 2008 Test Pipe Dia.: 10.080-in (256 mm) Blockage: 15.16% K

: 0.6091

pub

Average K: 0.6110 Calibration ID: 19413

Data

Point

Number

1 3009.6 683.5 73.99 184.0 71.0 21.7 21.1 1.5 0.963 62.29 997.8 12.10 3.69 6.58E+05 0.6073 2 2504.8 568.9 51.03 126.9 71.1 21.7 25.2 1.7 0.961 62.29 997.7 10.07 3.07 5.48E+05 0.6086 3 2006.9 455.8 32.32 80.4 71.2 21.8 28.4 2.0 0.960 62.29 997.7 8.07 2.46 4.40E+05 0.6127 4 1503.2 341.4 17.97 44.7 71.3 21.8 30.8 2.1 0.959 62.29 997.7 6.04 1.84 3.30E+05 0.6154 5 998.3 226.7 8.02 19.9 71.4 21.9 34.4 2.4 0.957 62.28 997.7 4.01 1.22 2.19E+05 0.6119 6 496.3 112.7 1.96 4.9 71.6 22.0 37.7 2.6 0.955 62.28 997.7 2.00 0.61 1.09E+05 0.6158 7 3010.1 683.6 74.27 184.7 71.6 22.0 20.7 1.4 0.955 62.28 997.7 12.10 3.69 6.63E+05 0.6062 8 2503.8 568.7 50.69 126.0 71.7 22.0 25.3 1.7 0.954 62.28 997.7 10.07 3.07 5.52E+05 0.6104 9 2010.6 456.6 32.68 81.3 71.8 22.1 28.5 2.0 0.953 62.28 997.7 8.08 2.46 4.44E+05 0.6105 10 1504.6 341.7 18.33 45.6 71.9 22.2 31.2 2.2 0.951 62.28 997.6 6.05 1.84 3.33E+05 0.6099 11 1002.3 227.6 8.12 20.2 72.0 22.2 34.8 2.4 0.950 62.28 997.6 4.03 1.23 2.22E+05 0.6104 12 498.7 113.3 1.98 4.9 72.1 22.3 37.9 2.6 0.949 62.28 997.6 2.00 0.61 1.11E+05 0.6143 13 3013.8 684.5 74.33 184.8 71.9 22.2 21.2 1.5 0.951 62.28 997.6 12.12 3.69 6.66E+05 0.6067 14 2501.5 568.1 50.83 126.4 71.9 22.2 25.1 1.7 0.951 62.28 997.6 10.06 3.07 5.53E+05 0.6089 15 2008.5 456.2 32.75 81.4 71.9 22.2 28.5 2.0 0.951 62.28 997.6 8.07 2.46 4.44E+05 0.6091 16 1503.8 341.5 18.09 45.0 71.9 22.2 31.2 2.2 0.951 62.28 997.6 6.05 1.84 3.33E+05 0.6137 17 997.4 226.5 7.91 19.7 72.0 22.2 34.3 2.4 0.950 62.28 997.6 4.01 1.22 2.21E+05 0.6156 18 498.8 113.3 2.02 5.0 72.1 22.3 37.9 2.6 0.949 62.28 997.6 2.01 0.61 1.11E+05 0.6098

Flow Rate

GPM m3/h inH2O mbar °F °C psig bar g cP lb/ft3kg/m3ft/s m/s

Differential

Pressure

Fluid

Temperature

Fluid

Pressure

Fluid

Viscosity

Fluid Density F luid Velocity

Pipe

Reynolds

Number

5-43

Page 66

Rosemount Annubar Flow Test Data Book

Test Laboratory: Rosemount - Boulder, Colorado Flow Lab

Sensor Size: 22 Fluid: Water Sensor Serial Number: 585-22-5 Pipe Size: 10-in. S40 Test Spool: DS-878

Test Date: April 1, 2008 Test Pipe Dia.: 10.080-in (256 mm) Blockage: 15.16% K

: 0.6091

pub

Average K: 0.6118 Calibration ID: 19805

Reference Manual

00821-0100-4809, Rev BA

July 2009

Data

Point

Number

1 3019.5 685.8 74.35 184.9 68.9 20.5 21.1 1.5 0.990 62.30 998.0 12.14 3.70 6.42E+05 0.6079 2 2582.8 586.6 54.09 134.5 68.9 20.5 24.7 1.7 0.990 62.30 998.0 10.38 3.17 5.49E+05 0.6096 3 2015.3 457.7 33.11 82.3 68.9 20.5 28.5 2.0 0.990 62.30 998.0 8.10 2.47 4.28E+05 0.6080 4 1506.0 342.0 18.29 45.5 68.9 20.5 31.3 2.2 0.989 62.30 998.0 6.05 1.85 3.20E+05 0.6113 5 1001.7 227.5 8.10 20.1 69.0 20.6 34.8 2.4 0.988 62.30 998.0 4.03 1.23 2.13E+05 0.6109 6 499.6 113.5 1.97 4.9 69.1 20.6 37.9 2.6 0.987 62.30 998.0 2.01 0.61 1.06E+05 0.6174 7 3010.2 683.7 73.67 183.2 68.9 20.5 21.4 1.5 0.990 62.30 998.0 12.10 3.69 6.40E+05 0.6088 8 2576.1 585.1 53.72 133.6 68.9 20.5 24.9 1.7 0.989 62.30 998.0 10.36 3.16 5.48E+05 0.6102 9 2012.2 457.0 32.58 81.0 68.9 20.5 28.6 2.0 0.989 62.30 998.0 8.09 2.47 4.28E+05 0.6120 10 1504.4 341.7 18.08 44.9 69.0 20.5 31.3 2.2 0.989 62.30 998.0 6.05 1.84 3.20E+05 0.6142 11 1002.6 227.7 8.08 20.1 69.0 20.6 35.0 2.4 0.988 62.30 998.0 4.03 1.23 2.14E+05 0.6122 12 499.2 113.4 1.99 5.0 69.1 20.6 38.1 2.6 0.987 62.30 998.0 2.01 0.61 1.06E+05 0.6140 13 3012.7 684.2 73.21 182.0 68.9 20.5 21.2 1.5 0.989 62.30 998.0 12.11 3.69 6.41E+05 0.6112 14 2583.7 586.8 53.63 133.4 69.0 20.5 24.9 1.7 0.989 62.30 998.0 10.39 3.17 5.50E+05 0.6124 15 2012.4 457.1 32.86 81.7 69.0 20.5 28.6 2.0 0.989 62.30 998.0 8.09 2.47 4.28E+05 0.6095 16 1503.4 341.4 18.17 45.2 69.0 20.6 31.4 2.2 0.988 62.30 998.0 6.04 1.84 3.20E+05 0.6122 17 1000.1 227.1 7.98 19.8 69.1 20.6 35.0 2.4 0.988 62.30 998.0 4.02 1.23 2.13E+05 0.6146 18 499.7 113.5 1.98 4.9 69.2 20.6 38.1 2.6 0.986 62.30 998.0 2.01 0.61 1.07E+05 0.6158 19 3011.3 683.9 73.51 182.8 69.0 20.5 21.1 1.5 0.989 62.30 998.0 12.11 3.69 6.41E+05 0.6097

5-44

Flow Rate

GPM m3/h inH2O mbar °F °C psig bar g cP lb/ft3kg/m3ft/s m/s

Differential

Pressure

Fluid

Temperature

Fluid

Pressure

Fluid

Viscosity

Fluid Density F luid Velocity

Pipe

Reynolds

Number

Page 67

Reference Manual

00821-0100-4809, Rev BA July 2009

Sensor Size: 22 Fluid: Water Sensor Serial Number: 585-22-5 Pipe Size: 10-in. S40 Test Spool: DS-878

Rosemount Annubar

Flow Test Data Book

Test Laboratory: Rosemount - Boulder, Colorado Flow Lab

Test Date: April 1, 2008 Test Pipe Dia.: 10.080-in (256 mm) Blockage: 15.16% K

: 0.6091

pub

Average K: 0.6120 Calibration ID: 19807

Data

Point

Number

1 3040.9 690.7 75.43 187.6 69.4 20.8 21.3 1.5 0.983 62.30 997.9 12.23 3.73 6.51E+05 0.6078 2 2570.9 583.9 53.89 134.0 69.5 20.8 25.3 1.7 0.982 62.30 997.9 10.34 3.15 5.51E+05 0.6079 3 2010.1 456.5 32.65 81.2 69.6 20.9 28.9 2.0 0.980 62.30 997.9 8.08 2.46 4.31E+05 0.6106 4 1501.7 341.1 17.99 44.7 69.7 21.0 31.7 2.2 0.979 62.30 997.9 6.04 1.84 3.23E+05 0.6145 5 1003.2 227.8 8.06 20.0 69.8 21.0 35.4 2.4 0.978 62.30 997.9 4.03 1.23 2.16E+05 0.6135 6 495.4 112.5 1.93 4.8 69.8 21.0 38.1 2.6 0.978 62.30 997.9 1.99 0.61 1.07E+05 0.6186 7 3008.1 683.2 73.65 183.1 69.7 20.9 21.5 1.5 0.980 62.30 997.9 12.09 3.69 6.46E+05 0.6085 8 2579.4 585.8 53.73 133.6 69.7 20.9 25.1 1.7 0.980 62.30 997.9 10.37 3.16 5.54E+05 0.6108 9 2009.0 456.3 32.50 80.8 69.7 20.9 28.9 2.0 0.980 62.30 997.9 8.08 2.46 4.31E+05 0.6117 10 1505.2 341.9 18.16 45.2 69.7 20.9 31.7 2.2 0.979 62.30 997.9 6.05 1.84 3.23E+05 0.6131 11 999.9 227.1 8.02 19.9 69.8 21.0 35.1 2.4 0.979 62.30 997.9 4.02 1.23 2.15E+05 0.6129 12 497.6 113.0 1.99 4.9 69.8 21.0 38.4 2.6 0.977 62.30 997.9 2.00 0.61 1.07E+05 0.6130 13 3011.3 683.9 73.50 182.8 69.7 20.9 21.6 1.5 0.980 62.30 997.9 12.11 3.69 6.47E+05 0.6097 14 2578.5 585.6 53.83 133.8 69.7 20.9 25.2 1.7 0.980 62.30 997.9 10.37 3.16 5.54E+05 0.6101 15 2011.3 456.8 32.60 81.1 69.7 20.9 28.9 2.0 0.980 62.30 997.9 8.09 2.46 4.32E+05 0.6115 16 1506.5 342.2 18.27 45.4 69.7 20.9 31.6 2.2 0.979 62.30 997.9 6.06 1.85 3.24E+05 0.6117 17 1003.2 227.8 8.20 20.4 69.7 21.0 34.6 2.4 0.979 62.30 997.9 4.03 1.23 2.16E+05 0.6083 18 497.6 113.0 1.93 4.8 69.9 21.0 38.3 2.6 0.977 62.30 997.9 2.00 0.61 1.07E+05 0.6216

Flow Rate

GPM m3/h inH2O mbar °F °C psig bar g cP lb/ft3kg/m3ft/s m/s

Differential

Pressure

Fluid

Temperature

Fluid

Pressure

Fluid

Viscosity

Fluid Density F luid Velocity

Pipe

Reynolds

Number

5-45

Page 68

Rosemount Annubar Flow Test Data Book

Test Laboratory: Rosemount - Boulder, Colorado Flow Lab

Sensor Size: 22 Fluid: Water Sensor Serial Number: 585-22-2 Pipe Size: 5-in. S40 Test Spool: DS-943

Test Date: April 18, 2008 Test Pipe Dia.: 5.100-in (130 mm) Blockage: 29.96% K

: 0.5281

pub

Average K: 0.5328 Calibration ID: 19998

Reference Manual

00821-0100-4809, Rev BA

July 2009

Data

Point

Number

1 1211.1 275.1 237.71 591.0 68.7 20.4 34.7 2.4 0.993 62.31 998.0 19.02 5.80 5.07E+05 0.5327 2 1008.7 229.1 164.93 410.1 68.8 20.4 36.9 2.5 0.991 62.30 998.0 15.84 4.83 4.23E+05 0.5327 3 813.5 184.8 107.37 267.0 68.9 20.5 38.4 2.6 0.990 62.30 998.0 12.78 3.89 3.42E+05 0.5324 4 592.9 134.7 56.91 141.5 69.0 20.5 38.8 2.7 0.989 62.30 998.0 9.31 2.84 2.49E+05 0.5330 5 404.3 91.8 26.61 66.2 69.0 20.6 38.2 2.6 0.988 62.30 998.0 6.35 1.94 1.70E+05 0.5314 6 199.4 45.3 6.39 15.9 69.1 20.6 37.7 2.6 0.987 62.30 998.0 3.13 0.95 8.40E+04 0.5350 7 1219.1 276.9 240.43 597.8 69.2 20.7 36.1 2.5 0.986 62.30 998.0 19.15 5.84 5.14E+05 0.5331 8 1013.9 230.3 166.20 413.2 69.3 20.7 37.5 2.6 0.985 62.30 998.0 15.92 4.85 4.28E+05 0.5333 9 804.9 182.8 105.03 261.1 69.3 20.7 37.5 2.6 0.984 62.30 998.0 12.64 3.85 3.40E+05 0.5326 10 587.6 133.5 56.00 139.2 69.4 20.8 38.8 2.7 0.983 62.30 997.9 9.23 2.81 2.49E+05 0.5325 11 403.0 91.5 26.31 65.4 69.5 20.8 37.8 2.6 0.982 62.30 997.9 6.33 1.93 1.71E+05 0.5328 12 199.3 45.3 6.44 16.0 69.6 20.9 38.3 2.6 0.981 62.30 997.9 3.13 0.95 8.45E+04 0.5325 13 1215.8 276.1 239.05 594.4 69.6 20.9 36.6 2.5 0.980 62.30 997.9 19.09 5.82 5.16E+05 0.5332 14 1002.5 227.7 162.78 404.7 69.6 20.9 37.3 2.6 0.980 62.30 997.9 15.74 4.80 4.25E+05 0.5328 15 803.7 182.5 104.93 260.9 69.6 20.9 37.9 2.6 0.980 62.30 997.9 12.62 3.85 3.41E+05 0.5321 16 591.8 134.4 56.97 141.6 69.6 20.9 39.1 2.7 0.980 62.30 997.9 9.29 2.83 2.51E+05 0.5317 17 404.2 91.8 26.53 66.0 69.6 20.9 38.2 2.6 0.980 62.30 997.9 6.35 1.93 1.71E+05 0.5322 18 199.2 45.2 6.40 15.9 69.6 20.9 37.8 2.6 0.981 62.30 997.9 3.13 0.95 8.45E+04 0.5340

5-46

Flow Rate

GPM m3/h inH2O mbar °F °C psig bar g cP lb/ft3kg/m3ft/s m/s

Differential

Pressure

Fluid

Temperature

Fluid

Pressure

Fluid

Viscosity

Fluid Density F luid Velocity

Pipe

Reynolds

Number

Page 69

Reference Manual

00821-0100-4809, Rev BA July 2009

Sensor Size: 22 Fluid: Water Sensor Serial Number: 585-22-2 Pipe Size: 5-in. S40 Test Spool: DS-943

Rosemount Annubar

Flow Test Data Book

Test Laboratory: Rosemount - Boulder, Colorado Flow Lab

Test Date: April 19, 2008 Test Pipe Dia.: 5.100-in (130 mm) Blockage: 29.96% K

: 0.5281

pub

Average K: 0.5328 Calibration ID: 19999

Data

Point

Number

1 1199.6 272.4 232.60 578.3 69.2 20.6 34.5 2.4 0.986 62.30 998.0 18.84 5.74 5.06E+05 0.5334 2 1011.0 229.6 165.68 412.0 69.3 20.7 36.6 2.5 0.985 62.30 998.0 15.88 4.84 4.27E+05 0.5326 3 806.1 183.1 105.33 261.9 69.4 20.8 37.0 2.6 0.984 62.30 998.0 12.66 3.86 3.41E+05 0.5326 4 591.7 134.4 56.73 141.1 69.4 20.8 38.7 2.7 0.983 62.30 997.9 9.29 2.83 2.50E+05 0.5327 5 404.3 91.8 26.56 66.0 69.5 20.9 39.1 2.7 0.981 62.30 997.9 6.35 1.94 1.71E+05 0.5319 6 199.6 45.3 6.43 16.0 69.6 20.9 37.8 2.6 0.981 62.30 997.9 3.13 0.96 8.46E+04 0.5338 7 1214.1 275.8 238.28 592.5 69.7 20.9 37.7 2.6 0.980 62.30 997.9 19.07 5.81 5.15E+05 0.5334 8 1006.8 228.7 164.33 408.6 69.6 20.9 36.7 2.5 0.980 62.30 997.9 15.81 4.82 4.27E+05 0.5326 9 802.9 182.3 104.62 260.1 69.7 20.9 38.4 2.6 0.980 62.30 997.9 12.61 3.84 3.41E+05 0.5323 10 587.5 133.4 56.06 139.4 69.7 20.9 38.7 2.7 0.980 62.30 997.9 9.23 2.81 2.49E+05 0.5321 11 404.0 91.8 26.47 65.8 69.6 20.9 37.7 2.6 0.980 62.30 997.9 6.35 1.93 1.71E+05 0.5326 12 198.3 45.0 6.36 15.8 69.6 20.9 38.0 2.6 0.980 62.30 997.9 3.11 0.95 8.41E+04 0.5335 13 1215.4 276.1 239.22 594.8 69.6 20.9 37.1 2.6 0.980 62.30 997.9 19.09 5.82 5.16E+05 0.5329 14 1010.3 229.5 165.62 411.8 69.6 20.9 36.7 2.5 0.980 62.30 997.9 15.87 4.84 4.29E+05 0.5323 15 805.0 182.8 105.20 261.6 69.6 20.9 37.5 2.6 0.980 62.30 997.9 12.64 3.85 3.41E+05 0.5322 16 590.7 134.2 56.66 140.9 69.6 20.9 39.0 2.7 0.980 62.30 997.9 9.28 2.83 2.51E+05 0.5321 17 402.9 91.5 26.25 65.3 69.6 20.9 37.7 2.6 0.980 62.30 997.9 6.33 1.93 1.71E+05 0.5333 18 198.8 45.2 6.38 15.9 69.6 20.9 38.0 2.6 0.980 62.30 997.9 3.12 0.95 8.44E+04 0.5337

Flow Rate

GPM m3/h inH2O mbar °F °C psig bar g cP lb/ft3kg/m3ft/s m/s

Differential

Pressure

Fluid

Temperature

Fluid

Pressure

Fluid

Viscosity

Fluid Density F luid Velocity

Pipe

Reynolds

Number

5-47

Page 70

Rosemount Annubar Flow Test Data Book

Sensor Size: 22 Fluid: Air Sensor Serial Number: 585-22-5 Pipe Size: 8-in. S10 Test Spool: DS-995

Test Laboratory: CEESI - Nunn, Colorado

Test Date: July 18, 2008 Test Pipe Dia.: 8.350-in (212 mm) Blockage: 18.30% K

: 0.5938

pub

Average K: 0.5862 Calibration ID: 08DSC-0002

Reference Manual

00821-0100-4809, Rev BA

July 2009

Data

Point

Number

1 36.3 16.4 52.81 131.3 523.0 290.6 301.5 20.8 0.999 1.51 24.2 62.99 19.20 5.49E+06 0.5840 2 36.3 16.5 52.55 130.7 523.0 290.6 301.5 20.8 0.999 1.52 24.3 62.94 19.18 5.50E+06 0.5854 3 30.4 13.8 35.29 87.7 523.0 290.6 301.5 20.8 1.000 1.59 25.4 50.41 15.37 4.63E+06 0.5845 4 32.4 14.7 40.95 101.8 523.0 290.6 301.5 20.8 1.000 1.55 24.8 55.07 16.79 4.96E+06 0.5855 5 30.0 13.6 34.68 86.2 523.0 290.6 301.5 20.8 1.000 1.56 25.0 50.58 15.42 4.63E+06 0.5867 6 26.5 12.0 26.46 65.8 523.0 290.6 301.5 20.8 1.000 1.61 25.7 43.34 13.21 4.09E+06 0.5843 7 28.5 12.9 30.88 76.8 523.0 290.6 301.5 20.8 1.000 1.56 25.1 47.88 14.59 4.42E+06 0.5897 8 22.8 10.3 19.87 49.4 523.0 290.6 301.5 20.8 1.000 1.58 25.3 37.90 11.55 3.54E+06 0.5847 9 22.6 10.3 19.52 48.5 523.0 290.6 301.5 20.8 1.000 1.59 25.5 37.40 11.40 3.52E+06 0.5842 10 20.9 9.5 16.57 41.2 523.0 290.6 301.5 20.8 1.000 1.58 25.3 34.84 10.62 3.26E+06 0.5887 11 17.4 7.9 11.57 28.8 523.0 290.6 301.5 20.8 1.000 1.59 25.4 28.86 8.80 2.71E+06 0.5845 12 13.6 6.2 7.02 17.4 523.0 290.6 301.5 20.8 1.000 1.60 25.7 22.35 6.81 2.12E+06 0.5847 13 13.4 6.1 6.90 17.1 523.0 290.6 301.5 20.8 1.000 1.56 25.0 22.48 6.85 2.05E+06 0.5855 14 11.4 5.2 4.97 12.4 523.0 290.6 301.5 20.8 1.000 1.56 25.0 19.18 5.85 1.75E+06 0.5879 15 7.3 3.3 2.04 5.1 523.0 290.6 301.5 20.8 1.000 1.55 24.8 12.37 3.77 1.11E+06 0.5896 16 7.3 3.3 2.05 5.1 523.0 290.6 301.5 20.8 1.000 1.55 24.8 12.38 3.77 1.11E+06 0.5887

5-48

Flow Rate

GPM m3/h inH2O mbar °F °C psig bar g cP lb/ft3kg/m3ft/s m/s

Differential

Pressure

Fluid

Temperature

Fluid Pressure

Fluid

Viscosity

Fluid Density Fluid Velocity

Pipe

Reynolds

Number

Page 71

Reference Manual

00821-0100-4809, Rev BA July 2009

Rosemount Annubar

Flow Test Data Book

585 SENSOR SIZE 44

Table 5-18. Flow Coefficient Data Summary: Sensor 22

Calibration

Number

1864a UTAH 16" STD N/A 15.300 19.0% 0.5900 0.5844 1864b UTAH 24" STD N/A 23.326 12.4% 0.6148 0.6187

08DSC-0010 CEESI-IA 12" STD DS-1040 12.066 24.1% 0.5516 0.5544

1926 UTAH 12" STD DS-1040 12.066 24.1% 0.5489 0.5544

LAB Pipe Size Spool No ID Blockage

Calibrated Average K

Published K

5-49

Page 72

Rosemount Annubar Flow Test Data Book

Test Laboratory: Utah Water Research Lab - Logan, Utah

Sensor Size: 44 Fluid: Water Sensor Serial Number: 585-44-1 Pipe Size: 16-in. STD Test Spool: UWRL Spool

Test Date: May 27, 2008 Test Pipe Dia.: 15.300-in (389 mm) Blockage: 18.97% K

: 0.5844

pub

Average K: 0.5900 Calibration ID: 01864a

Reference Manual

00821-0100-4809, Rev BA

July 2009

Data

Point

Number

1 1738.0 394.7 4.95 12.3 44.5 6.9 22.0 1.5 1.000 62.42 999.9 3.03 0.92 2.55E+05 0.5892 2 3186.3 723.7 16.47 41.0 44.5 6.9 22.0 1.5 1.000 62.42 999.9 5.56 1.69 4.67E+05 0.5921 3 4229.9 960.7 28.94 72.0 44.5 6.9 22.0 1.5 1.000 62.42 999.9 7.38 2.25 6.21E+05 0.5930 4 5652.9 1283.9 52.25 129.9 44.5 6.9 22.0 1.5 1.000 62.42 999.9 9.86 3.01 8.29E+05 0.5898 5 6905.3 1568.3 77.50 192.7 44.5 6.9 22.0 1.5 1.000 62.42 999.9 12.05 3.67 1.01E+06 0.5916 6 8159.3 1853.1 108.13 268.9 44.5 6.9 22.0 1.5 1.000 62.42 999.9 14.24 4.34 1.20E+06 0.5918 7 9122.4 2071.9 136.72 339.9 44.5 6.9 22.0 1.5 1.000 62.42 999.9 15.92 4.85 1.34E+06 0.5884 8 10168.5 2309.5 170.63 424.3 44.5 6.9 22.0 1.5 1.000 62.42 999.9 17.74 5.41 1.49E+06 0.5871 9 11246.8 2554.4 208.28 517.9 44.5 6.9 22.0 1.5 1.000 62.42 999.9 19.63 5.98 1.65E+06 0.5877 10 12170.8 2764.2 242.66 603.3 44.5 6.9 22.0 1.5 1.000 62.42 999.9 21.24 6.47 1.69E+06 0.5893

5-50

Flow Rate

GPM m3/h inH2O mbar °F °C psig bar g cP lb/ft3kg/m3ft/s m/s

Differential

Pressure

Fluid

Temperatur

Fluid

Pressure

Fluid

Viscosity

Fluid Density Fluid Velocity

Pipe

Reynolds

Number

Page 73

Reference Manual

00821-0100-4809, Rev BA July 2009

Sensor Size: 44 Fluid: Water Sensor Serial Number: 585-44-1 Pipe Size: 24-in. STD Test Spool: UWRL Spool

Rosemount Annubar

Flow Test Data Book

Test Laboratory: Utah Water Research Lab - Logan, Utah

Test Date: May 27, 2008 Test Pipe Dia.: 23.326-in (592 mm) Blockage: 12.45% K

: 0.6187

pub

Average K: 0.6148 Calibration ID: 1864b

Data

Point

Number

1 4384.4 995.8 5.25 13.1 44.5 6.9 22.0 1.5 1.000 62.42 999.9 3.29 1.00 2.55E+05 0.6209 2 7083.8 1608.9 13.84 34.4 44.5 6.9 22.0 1.5 1.000 62.42 999.9 5.32 1.62 4.67E+05 0.6179 3 9984.7 2267.7 27.25 67.8 44.5 6.9 22.0 1.5 1.000 62.42 999.9 7.50 2.28 6.21E+05 0.6206 4 12646.9 2872.4 44.06 109.6 44.5 6.9 22.0 1.5 1.000 62.42 999.9 9.49 2.89 8.29E+05 0.6182 5 15200.4 3452.3 64.84 161.2 44.5 6.9 22.0 1.5 1.000 62.42 999.9 11.41 3.48 1.01E+06 0.6125 6 18149.3 4122.1 92.50 230.0 44.5 6.9 22.0 1.5 1.000 62.42 999.9 13.63 4.15 1.20E+06 0.6123 7 20767.7 4716.8 120.63 299.9 44.5 6.9 22.0 1.5 1.000 62.42 999.9 15.59 4.75 1.34E+06 0.6135 8 23873.1 5422.1 161.72 402.1 44.5 6.9 22.0 1.5 1.000 62.42 999.9 17.92 5.46 1.49E+06 0.6091 9 26484.9 6015.3 197.19 490.3 44.5 6.9 22.0 1.5 1.000 62.42 999.9 19.88 6.06 1.65E+06 0.6120 10 29116.7 6613.0 237.97 591.7 44.5 6.9 22.0 1.5 1.000 62.42 999.9 21.86 6.66 1.65E+06 0.6124 11 20753.4 4713.5 120.94 300.7 44.5 6.9 22.0 1.5 1.000 62.42 999.9 15.58 4.75 1.65E+06 0.6123 12 23959.8 5441.7 162.03 402.9 44.5 6.9 22.0 1.5 1.000 62.42 999.9 17.99 5.48 1.65E+06 0.6108 13 12787.2 2904.2 45.31 112.7 44.5 6.9 22.0 1.5 1.000 62.42 999.9 9.60 2.93 1.65E+06 0.6164 14 7217.6 1639.3 14.34 112.7 44.5 6.9 22.0 1.5 1.000 62.42 999.9 5.42 1.65 6.57E+05 0.6184

Flow Rate

GPM m3/h inH2O mbar °F °C psig bar g cP lb/ft3kg/m3ft/s m/s

Differential

Pressure

Fluid

Temperature

Fluid

Pressure

Fluid

Viscosity

Fluid Density Fluid Velocity

Pipe

Reynolds

Number

5-51

Page 74

Rosemount Annubar Flow Test Data Book

Test Laboratory: Utah Water Research Lab - Logan, Utah

Sensor Size: 44 Fluid: Water Sensor Serial Number: 585-44-1 Pipe Size: 12-in. STD Test Spool: DS-1040

Test Date: November 12, 2008 Test Pipe Dia.: 12.060-in (306 mm) Blockage: 24.07% K

: 0.5543

pub

Average K: 0.5496 Calibration ID: 1926

Reference Manual

00821-0100-4809, Rev BA

July 2009

Data

Point

Number

1 2089.9 474.7 21.25 52.8 44.5 6.9 22.0 1.5 1.000 62.42 999.9 5.87 1.79 2.83E+05 0.5503 2 2090.9 474.9 21.31 53.0 44.5 6.9 22.0 1.5 1.000 62.42 999.9 5.87 1.79 2.83E+05 0.5498 3 2410.4 547.5 28.31 70.4 44.5 6.9 22.0 1.5 1.000 62.42 999.9 6.77 2.06 3.27E+05 0.5499 4 2416.4 548.8 28.50 70.9 44.5 6.9 22.0 1.5 1.000 62.42 999.9 6.79 2.07 3.28E+05 0.5494 5 2912.1 661.4 41.31 102.7 44.5 6.9 22.0 1.5 1.000 62.42 999.9 8.18 2.49 3.95E+05 0.5500 6 2909.6 660.8 41.44 103.0 44.5 6.9 22.0 1.5 1.000 62.42 999.9 8.17 2.49 3.94E+05 0.5487 7 3298.6 749.2 53.19 132.3 44.5 6.9 22.0 1.5 1.000 62.42 999.9 9.26 2.82 4.47E+05 0.5490 8 3297.4 748.9 53.00 131.8 44.5 6.9 22.0 1.5 1.000 62.42 999.9 9.26 2.82 4.47E+05 0.5498 9 3724.0 845.8 67.69 168.3 44.5 6.9 22.0 1.5 1.000 62.42 999.9 10.46 3.19 5.05E+05 0.5494 10 3717.9 844.4 67.31 167.4 44.5 6.9 22.0 1.5 1.000 62.42 999.9 10.44 3.18 5.04E+05 0.5501 11 4342.0 986.2 91.75 228.1 44.5 6.9 22.0 1.5 1.000 62.42 999.9 12.20 3.72 5.88E+05 0.5502 12 4348.1 987.5 92.19 229.2 44.5 6.9 22.0 1.5 1.000 62.42 999.9 12.21 3.72 5.89E+05 0.5497 13 4658.3 1058.0 105.75 262.9 44.5 6.9 22.0 1.5 1.000 62.42 999.9 13.08 3.99 6.31E+05 0.5499 14 4660.7 1058.5 106.13 263.9 44.5 6.9 22.0 1.5 1.000 62.42 999.9 13.09 3.99 6.32E+05 0.5492 15 6228.9 1414.7 189.00 469.9 44.5 6.9 22.0 1.5 1.000 62.42 999.9 17.49 5.33 8.44E+05 0.5500 16 6237.3 1416.6 190.13 472.7 44.5 6.9 22.0 1.5 1.000 62.42 999.9 17.52 5.34 8.45E+05 0.5491 17 7132.9 1620.0 248.44 617.7 44.5 6.9 22.0 1.5 1.000 62.42 999.9 20.03 6.11 9.67E+05 0.5493 18 7138.9 1621.4 249.19 619.6 44.5 6.9 22.0 1.5 1.000 62.42 999.9 20.05 6.11 9.68E+05 0.5490 19 5489.6 1246.8 146.63 364.6 44.5 6.9 22.0 1.5 1.000 62.42 999.9 15.42 4.70 7.44E+05 0.5503 20 5484.8 1245.7 146.81 365.0 44.5 6.9 22.0 1.5 1.000 62.42 999.9 15.40 4.70 7.43E+05 0.5495

5-52

Flow Rate

GPM m3/h inH2O mbar °F °C psig bar g cP lb/ft3kg/m3ft/s m/s

Differential

Pressure

Fluid

Temperature

Fluid Pressure

Fluid

Viscosity

Fluid Density Fluid Velocity

Pipe

Reynolds

Number

Page 75

Reference Manual

00821-0100-4809, Rev BA July 2009

Sensor Size: 44 Fluid: Natural Gas Sensor Serial Number: 585-44-10 Pipe Size: 12-in. STD Test Spool: DS-1040

Test Laboratory: CEESI - Garner, Iowa

Test Date: September 16, 2008 Test Pipe Dia.: 12.060-in (306 mm) Blockage: 24.07% K

: 0.5543

pub

Average K: 0.5521 Calibration ID: 08DSC-0010

Rosemount Annubar

Flow Test Data Book

Data

Point

Number

1 147.7 67.0 91.62 227.8 536.2 297.9 1111.6 76.6 1.000 3.71 59.4 50.18 15.30 2.04E+07 0.5525 2 147.6 67.0 91.64 227.9 536.2 297.9 1111.6 76.6 1.000 3.71 59.4 50.17 15.29 2.04E+07 0.5522 3 135.0 61.2 76.50 190.2 536.2 297.9 1112.4 76.6 1.000 3.71 59.4 45.85 13.98 1.87E+07 0.5525 4 134.7 61.1 76.30 189.7 536.2 297.9 1112.5 76.7 1.000 3.71 59.5 45.75 13.94 1.86E+07 0.5520 5 123.1 55.8 63.60 158.1 536.2 297.9 1113.3 76.7 1.000 3.71 59.5 41.78 12.73 1.70E+07 0.5524 6 122.7 55.6 63.31 157.4 536.2 297.9 1113.4 76.7 1.000 3.71 59.5 41.63 12.69 1.70E+07 0.5517 7 110.5 50.1 51.19 127.3 536.2 297.9 1112.2 76.6 1.000 3.71 59.4 37.57 11.45 1.53E+07 0.5531 8 110.6 50.2 51.26 127.5 536.2 297.9 1112.3 76.6 1.000 3.71 59.4 37.61 11.46 1.53E+07 0.5534 9 98.9 44.8 41.07 102.1 536.2 297.9 1113.2 76.7 1.000 3.71 59.4 33.60 10.24 1.37E+07 0.5524 10 98.9 44.9 41.10 102.2 536.2 297.9 1113.2 76.7 1.000 3.71 59.4 33.61 10.24 1.37E+07 0.5524 11 85.4 38.7 30.63 76.2 536.2 297.9 1114.1 76.8 1.000 3.71 59.5 29.01 8.84 1.18E+07 0.5525 12 85.5 38.8 30.64 76.2 536.2 297.9 1114.2 76.8 1.000 3.71 59.5 29.05 8.86 1.18E+07 0.5532 13 73.1 33.2 22.50 55.9 536.3 297.9 1115.2 76.8 1.000 3.71 59.5 24.82 7.57 1.01E+07 0.5517 14 72.9 33.1 22.28 55.4 536.3 297.9 1115.3 76.8 1.000 3.71 59.5 24.74 7.54 1.01E+07 0.5526 15 58.4 26.5 14.35 35.7 536.4 298.0 1116.3 76.9 1.000 3.71 59.5 19.81 6.04 8.07E+06 0.5515 16 58.3 26.4 14.27 35.5 536.4 298.0 1116.6 76.9 1.000 3.71 59.6 19.76 6.02 8.07E+06 0.5518 17 47.2 21.4 9.37 23.3 536.4 298.0 1117.5 77.0 1.000 3.71 59.6 15.99 4.87 6.52E+06 0.5514 18 47.3 21.4 9.39 23.3 536.4 298.0 1117.5 77.0 1.000 3.71 59.6 16.01 4.88 6.53E+06 0.5515 19 38.3 17.3 6.18 15.4 536.4 298.0 1118.2 77.0 1.000 3.71 59.7 12.95 3.95 5.28E+06 0.5499 20 38.3 17.4 6.17 15.3 536.4 298.0 1118.2 77.0 1.000 3.71 59.7 12.97 3.95 5.29E+06 0.5514

Flow Rate

GPM m3/h inH2O mbar °F °C psig bar g cP lb/ft3kg/m3ft/s m/s

Differential

Pressure

Fluid

Temperature

Fluid Pressure

Fluid

Viscosity

Fluid Density Fluid Velocity

Pipe

Reynolds

Number

5-53

Page 76

Rosemount Annubar Flow Test Data Book

Reference Manual

00821-0100-4809, Rev BA

July 2009

5-54

Page 77

Reference Manual

00821-0100-4809, Rev BA July 2009

Section 6 References

ASME, Fluid Meters, Sixth Edition 1971, ASME, New York, pages 47-111.

Achenbach, E. Distribution of Local Pressure & Skin Friction Around a

Circular Cylinder in Cross-Flow Up to RE = 5 x 10

1968, Volume 34, Part 4, pages 625 - 639.

Schlichting, H., Boundary Layer Theory, Fourth Edition 1960, McGraw-Hill Book Co., New York, pages 1 - 40.

Daugherty, R., Fluid Mechanics with Engineering Applications, Eight Edition 1985, McGraw-Hill Book Co., New York, Chapter 10.

Rosemount 485 Annubar

Flow Test Data Book

, J. Fluid Mechanics, March

Hamli, D., Practical Guide to the Evaluation of the Metering Performance of Differential Producers, J., Fluids Engineering, March 1973, V o lume 95, Series

1, Number 1, pages 127 - 141.

Hoerner, Sighard F., Fluid-Dynamic Drag, 1965: Great Britain. Produced in the United States.

Schneider, W. Experimental Investigations on Bodies With Non-Circular Sections in Compressible Flow (Pressure Distributions), Viscous and Interacting Flow Field Effects, May 9 - 10, 1984, pages 132 - 153.

www.rosemount.com

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Rosemount 485 Annubar Flow Test Data Book

Reference Manual

00821-0100-4809, Rev BA

July 2009

6-2

Page 79

Reference Manual

00821-0100-4809, Rev BA July 2009

Index

Rosemount Annubar

Flow Test Data Book

Annubar strengths . . . . . . . . . . 1-1

Derivation

Blockage Equation

Flow Equation . . . . . . . . . . 4-2

Design and Performance . . . . . 2-2

High Pressure Measurement Low Pressure Measurement 2-4

sensor design . . . . . . . . . . 2-2

surface texture

Drawings

Frontal slot design . . . . . . . 2-3

sensor cross-section

Velocity Graph . . . . . . . . . . 2-4

Flow Coefficient . . . . . . . . . . . . 3-1

Benefits

Overview . . . . . . . . . . . . . . 3-1

Reynolds Number Ranges 3-2

Flow Theory

Blockage Equation Derivation 4-3

Conclusion . . . . . . . . . . . . . 4-5

Flow Equation Derivation

. . . . . . . . . . . . . . . 3-1

. . . . . . . . . . . . . . . 4-1

. . . . . . 4-3

2-3

. . . . . . . . . . 2-4

. . . . . 2-2

. . 4-2

Testing . . . . . . . . . . . . . . . . . . .1-1

Independent Laboratory . . .1-2 In-House Performance

Laboratories . . . . . . . . . . . .5-1

Rosemount . . . . . . . . . 5-1

. . . . . . . . . . . . . .5-1

SwRI

Mechanical . . . . . . . . . . . . .1-2

On-Site Performance . . . . . 1-2

Sensor Size 1

Fl-210 . . . . . . . . . . . . .5-4

Fl-260 . . . . . . . . . . . . .5-6

Fl-261

Sensor Size 2 . . . . . . . . .5-10

Fl-156 . . . . . . . . . . . .5-10

Fl-162

Fl-163 . . . . . . . . . . . .5-14

Fl-169 . . . . . . . . . . . .5-16

Fl-178

Fl-179 . . . . . . . . . . . .5-20

Fl-180 . . . . . . . . . . . .5-22

Fl-181

Sensor Size 3 . . . . 5-26, 5-49

Fl-307 . . . . . . . . . . . .5-26

Structural

. . . . . . . . . . 5 -4

. . . . . . . . . . . . .5-8

. . . . . . . . . . . .5-12

. . . . . . . . . . . .5-18

. . . . . . . . . . . .5-24

. . . . . . . . . . . . . .1-2

. . . . 1-2

Gravimetric Procedure . . . . . . . 5-2

High Pressure Measurement . . 2-3 How the Annubar Works

Low Pressure Measurement . . . 2-4

Nomenclature . . . . . . . . . . . . . . 4-1

References . . . . . . . . . . . . . . . . 6-1

Sensor Design . . . . . . . . . . . . . 2-2

Surface Texture

. . . . . . . . . . . . 2-4

. . . . . . 2-1

Index-1

Page 80

Rosemount Annubar Flow Test Data Book

Reference Manual

00821-0100-4809, Rev BA

July 2009

Index-2

Page 81

Page 82

Reference Manual

00821-0100-4809, Rev BA

July 2009

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Rosemount Annubar Primary Flow Element Flow Test Data Book Manuals & Guides

Specifications and Main Features

Frequently Asked Questions

User Manual

Table of Contents

Section 1 Annubar Technology

ROSEMOUNT ANNUBAR PRIMARY FLOW ELEMENT

ROSEMOUNT ANNUBAR FLOW ELEMENT TEST ADVANTAGES

Section 2 How the Annubar Works

OVERVIEW The Rosemount Annubar primary flow element is a device used to measure

DESIGN AND PERFORMANCE

FLOW COEFFICIENT OVERVIEW

BENEFITS The K-factor of an Annubar is a function of the blockage the probe present s to

ROSEMOUNT ANNUBAR REYNOLDS NUMBER RANGES

NOMENCLATURE The following symbols are used in the derivation of the flow equation and the

FLOW EQUATION DERIVATION

BLOCKAGE EQUATION DERIVATION

CONCLUSION While empirical testing of a flowmeter is the most accurate means of

Section 5 Test Facilities and Procedures

OVERVIEW The following descriptions of tests and testing methods are abbreviated

TESTING LABORATORIES

GRAVIMETRIC PROCEDURE

TESTING PERFORMED BY SENSOR SIZE

485 SENSOR SIZE 1

485 SENSOR SIZE 2

485 SENSOR SIZE 3

585 SENSOR SIZE 11

585 SENSOR SIZE 22

585 SENSOR SIZE 44

Section 6 References

Index