USRE36401E - Tandem rotor turbine meter and field calibration module - Google Patents
Tandem rotor turbine meter and field calibration module Download PDFInfo
- Publication number
- USRE36401E USRE36401E US08/926,192 US92619297A USRE36401E US RE36401 E USRE36401 E US RE36401E US 92619297 A US92619297 A US 92619297A US RE36401 E USRE36401 E US RE36401E
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- United States
- Prior art keywords
- rotor
- gas
- flow
- module
- meter
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 238000000034 method Methods 0.000 claims abstract description 15
- 230000000694 effects Effects 0.000 claims abstract description 14
- 230000003750 conditioning effect Effects 0.000 claims description 22
- 238000005259 measurement Methods 0.000 claims description 18
- 230000000737 periodic effect Effects 0.000 claims description 6
- 230000008878 coupling Effects 0.000 claims description 5
- 238000010168 coupling process Methods 0.000 claims description 5
- 238000005859 coupling reaction Methods 0.000 claims description 5
- 238000012360 testing method Methods 0.000 claims description 2
- 238000011144 upstream manufacturing Methods 0.000 claims 23
- 230000002596 correlated effect Effects 0.000 claims 4
- 230000005540 biological transmission Effects 0.000 claims 2
- 238000009434 installation Methods 0.000 claims 2
- 238000012937 correction Methods 0.000 abstract description 11
- 230000009977 dual effect Effects 0.000 abstract description 2
- 238000012935 Averaging Methods 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 22
- 239000012530 fluid Substances 0.000 description 17
- 238000003780 insertion Methods 0.000 description 7
- 230000037431 insertion Effects 0.000 description 7
- 230000008859 change Effects 0.000 description 4
- 230000015556 catabolic process Effects 0.000 description 3
- 238000006731 degradation reaction Methods 0.000 description 3
- 230000004075 alteration Effects 0.000 description 2
- 230000002708 enhancing effect Effects 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000007664 blowing Methods 0.000 description 1
- 238000004590 computer program Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 230000008439 repair process Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Images
Classifications
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01F—MEASURING VOLUME, VOLUME FLOW, MASS FLOW OR LIQUID LEVEL; METERING BY VOLUME
- G01F1/00—Measuring the volume flow or mass flow of fluid or fluent solid material wherein the fluid passes through a meter in a continuous flow
- G01F1/05—Measuring the volume flow or mass flow of fluid or fluent solid material wherein the fluid passes through a meter in a continuous flow by using mechanical effects
- G01F1/10—Measuring the volume flow or mass flow of fluid or fluent solid material wherein the fluid passes through a meter in a continuous flow by using mechanical effects using rotating vanes with axial admission
- G01F1/12—Adjusting, correcting, or compensating means therefor
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01F—MEASURING VOLUME, VOLUME FLOW, MASS FLOW OR LIQUID LEVEL; METERING BY VOLUME
- G01F1/00—Measuring the volume flow or mass flow of fluid or fluent solid material wherein the fluid passes through a meter in a continuous flow
- G01F1/05—Measuring the volume flow or mass flow of fluid or fluent solid material wherein the fluid passes through a meter in a continuous flow by using mechanical effects
- G01F1/10—Measuring the volume flow or mass flow of fluid or fluent solid material wherein the fluid passes through a meter in a continuous flow by using mechanical effects using rotating vanes with axial admission
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01F—MEASURING VOLUME, VOLUME FLOW, MASS FLOW OR LIQUID LEVEL; METERING BY VOLUME
- G01F25/00—Testing or calibration of apparatus for measuring volume, volume flow or liquid level or for metering by volume
- G01F25/10—Testing or calibration of apparatus for measuring volume, volume flow or liquid level or for metering by volume of flowmeters
- G01F25/13—Testing or calibration of apparatus for measuring volume, volume flow or liquid level or for metering by volume of flowmeters using a reference counter
Definitions
- This invention relates to methods and an apparatus for measuring gas flow in a pipeline. More particularly, it relates to a tandem rotor turbine meter and field calibrator module which comprises a second independent metering rotor placed behind or downstream of an existing or main independent metering rotor and separated from it by flow conditioning stator vanes.
- a tandem rotor turbine meter and field calibrator module which comprises a second independent metering rotor placed behind or downstream of an existing or main independent metering rotor and separated from it by flow conditioning stator vanes.
- This apparatus There are two operation modes for this apparatus: the first being continuous operation as a tandem rotor turbine meter and the second being periodic use as a field calibrator module.
- Turbine meters provide great rangeability, compact size, and simplified maintenance when compared to alternative methods of large volume measurement.
- Single and double-rotor turbine meters as well as dual turbine meter systems are currently commercially available, each of which have drawbacks peculiar to their operation.
- single-rotor turbine meters are not well adapted to provide accurate measurement in gas flow streams with non-uniform velocity profiles or with mechanical degradation of the rotor.
- the rotor 1 operates in a manner similar to a single rotor meter because it actually measures the gas that passes through the line.
- the gas actually turns the rotor and then, through a mechanical gearing, that motion is transmitted out through a magnetic coupling to an output coupling to which the instrumentation is mounted.
- the output coupling is calibrated to represent a predetermined number of cubic feet per revolution thus generating a reading.
- rotor 1 there is a second rotor 2 whose function is to sense any change in direction of the gas velocity vector exiting from the blades of rotor 1.
- These two rotors therefore are fluidly coupled.
- the term fluid as used by those skilled in the art and as used throughout this specification shall mean both liquids and gas.
- the second or "sensing" rotor can sense this by the gas velocity vector angle change at which the flow leaves the tip of the first rotor's trailing edge and will change speed accordingly.
- the pulse output from both the rotors indicate the true flow of fluid in the pipeline. For example, if a swirl of fluid is coming down the pipeline, it may hit the blades of the first rotor at such an angle that the rotor will give a reading that may indicate a higher flow rate than the actual flow rate in the pipeline.
- the rotational speed of the rotors (rpms) is a function of the actual vector velocity of the fluid.
- the first rotor will be misled.
- the second rotor is designed to distinguish between the velocity of the fluid flowing through the pipeline and the velocity of fluid flow which comes off the trailing edges of the blades of the first rotor. Using the two rotor rotational speeds, a computer program calculates a ratio and adjusts the output at all times. Specific examples of various types of turbine meters are described in the following patents.
- an insertion type turbine meter is disclosed in U.S. Pat. No. 4,566,307 ('307 patent), entitled “Pipeline Flow Measurement Proving System”.
- an insertion turbine meter is a mechanical device used to measure the flow of gas or liquid through a pipe of known internal diameter. It has a small turbine rotor mounted on the end of a long stem. The diameter of the rotor is significantly smaller than the internal diameter of the pipe. The rotor and stem are inserted through a port in the side of the pipe. The rotor is positioned at the approximate center of the pipe and oriented in-line with the pipe axis. The speed of the gas flow causes the turbine rotor to spin.
- the rotational speed of the turbine rotor is proportional to the local velocity of the gas.
- an electronic pickup or pulse is used to sense the speed of the rotor or to count its revolutions. This output is then factored by a multiplier based on the internal diameter of the pipe to obtain a reading of total flow volume.
- the two meters used in the '307 patent are separated by a distance of about 25 feet in an attempt to eliminate the influence of one meter on the other. Such a separation requires pressure and temperature correction between the two rotors for output totalization and accuracy performance.
- insertion turbines are not as accurate as full pipeline turbine meters. Insertion turbine meters are not as accurate because they do not measure the entire flow passing through the pipeline.
- the orientation and position within the pipe is critical. This also limits the useful range of the insertion turbine meter since the location of the average flow velocity does change between laminar and turbulent flows. Also, the presence of the insertion turbine meter disturbs the flow profile. Due to their small size, the insertion turbine meter can not incorporate flow conditioners ahead of the rotor. Thus, their accuracy is affected by flow disturbances. Their calibration accuracy is also affected by the actual internal pipe diameter. Their typical accuracy is ⁇ 2% or more as compared to ⁇ 1% error for full flow turbine meters.
- U.S. Pat. No. 4,286,471 entitled “Constant Accuracy Turbine Meter” by Lee et al discloses a turbine meter in which a sensing rotor downstream from the metering rotor senses changes in the exit angle of the fluid leaving the metering rotor, the output from the sensing rotor being combined with the output from the metering rotor to produce a corrected output indicative of the flow through the meter.
- the output from the sensing rotor is utilized through a closed loop feedback system to modify the operation of the metering rotor in accordance with variations in the exit angle of the fluid leaving the metering rotor.
- the two rotors must rotate in the same direction.
- the present invention comprises methods and an apparatus for measuring gas flow in a gas pipeline.
- the apparatus includes two independent rotors, in close proximity of each other, housed in the same meter body, but isolated from the effects of each other. There are two operation modes for this apparatus, the first being continuous operation as a tandem rotor turbine meter and the second being periodic use as a field calibrator module.
- the apparatus comprises a second independent or tandem metering rotor, placed behind or downstream of an existing or main independent metering rotor.
- This second independent metering rotor in the tandem rotor/field calibrator module 61, FIG. 7B may be the same size and blade pitch as the main independent metering rotor. It rotates in either the same or opposite direction and registers the same flow.
- Flow conditioning vanes are incorporated in the module housing ahead of the second rotor, which isolates the two rotors from the effects of each other.
- the apparatus is built and calibrated as a complete double rotor meter made up of two individual measuring modules which fit into the same meter body.
- the two individual measuring modules may also be built and calibrated separately and then can be paired up later for operation.
- the tandem rotor module provides an electronic measurement output which is independent from the main rotor. This allows a direct comparison to the output of the main rotor at line conditions without the need for pressure and temperature corrections. Therefore, only simple electronics are needed for the continuous self-checking of the conditions of each rotor.
- the second rotor is more reliable than the main rotor since it is protected in its downstream location and it drives no mechanical output.
- the second rotor can run at a slower speed than the main rotor, depending upon the pitch of the blade angle, thus further enhancing its service life. Also, if desired the second rotor, without mechanical output, could be used as the electronic output totalization for billing, with the main rotor providing mechanical backup and checking.
- the output totalization of each of the two rotors can also be averaged together to lessen the effects of each rotor on accuracy degradation and provide a very reliable and accurate volume totalization.
- the tandem rotor module is independent of the main rotor module due to the stator vanes between the two rotors. Therefore, the two rotors can be repaired and recalibrated separately by the user in the shop at atmospheric conditions or in the field at operating conditions.
- the main rotor and tandem rotor module 61, 62 of FIGS. 7A, B can be interchanged with other modules without factory recalibration.
- a stator and rotor arm placed in line with an existing rotor to check its calibration and operation periodically.
- FIG. 1 is an exploded perspective view of the prior art.
- FIG. 2 is a schematic view of the two rotors and the stator vanes portions of the apparatus of the invention.
- FIG. 3 is a schematic view of the two rotors and stator vanes portion of the apparatus of the invention where the stator vanes and the second rotor are in the same housing.
- FIG. 4 is an exploded perspective view of the apparatus of the invention.
- FIG. 5 is a schematic of a totalization and self check method that can be used with the operation of the rotors.
- FIG. 5a is a schematic of a commercially available electronic device that can be used with this invention.
- FIG. 6 is a graph of the data collected by the method shown in FIG. 5.
- FIGS. 7A-C are a schematic of a turbine meter showing the single and double rotor options for Tandem rotor operation or single rotor operation with possibility of field calibration with field calibrator module.
- FIGS. 8A, B are two views of an enlarged sketch of on embodiment of the instant invention that can replace an existing single rotor turbine meter dummy housing for field calibration or for tandem rotor metering.
- the continuous mode apparats of the present invention is comprised of three essential elements, a primary rotor followed by a tandem rotor which are separated by a stator, all of which are in the same meter body.
- the tandem rotor is close enough to the primary rotor, and the stator is designed such that no temperature and pressure corrections are required.
- the stator functions to condition the fluid flow ahead of the tandem rotor enabling the tandem rotor to measure the true gas flow in the pipeline as opposed to the gas flow affected by the primary rotor blades.
- the field calibration module unit is nothing but, in its simplest terms, a module which includes a stator and a rotor adapted to be a tandem rotor when coupled to an existing single rotor measuring system already in place in a pipeline.
- two independent metering rotors 10 and 20, shown in FIGS. 2 and 4 are in close proximity of each other such that no temperature or pressure corrections are needed, and housed in the same meter body 60 of FIG. 7A and module housing 24 and 24', but isolated from the effects of each other by flow conditioning stator vanes 28 ahead of the second independent metering rotor 20.
- the first independent metering rotor 10 has spaced blades oriented to form a blade angle 41 with respect to its axis of rotation 33.
- the second independent metering rotor 20 may be the same size and blade pitch as the first or main independent metering rotor 10, or larger or smaller than first rotor; and its blade angle 44 or pitch, with respect to its axis of rotation 33 of said second independent metering rotor may be various pitch angles over a practical range of 1 to 75 degrees either in the same or opposite pitch direction.
- the second independent metering rotor 20 rotates in the same or opposite direction 32 about the same axis of rotation 33 and registers the same flow 36 as the first independent metering rotor 10.
- In between the first independent metering rotor and the second independent metering rotor are individual stator vanes 28 which are parallel to the pipeline.
- the stator vanes act to direct the flow of fluid coming off the first rotor in a straight line, parallel to the pipeline, as it flows through to the second rotor.
- the apparatus of the present invention is built and calibrated as a complete double rotor meter made up of two individual, independent measuring modules or rotors 10 and 20 and stator vanes 28 all of which fit into the same meter body and module housings 24 and 24'.
- output means 29 which is actuated by the first independent metering rotor 10.
- Output means 39 is actuated by the second independent metering rotor 20.
- the two output means 29 and 39 provide electronic output signals representative of the gas flow through their respective independent metering rotor 10 and 20.
- FIG. 5A shows a commercially available electronic package which allows the impulses generated by the instant invention to be read.
- the applicant is not claiming the electronics shown in FIG. 5A but is including them as an illustration of an available electronic devices that, with simple software changes, could be used for the Tandem Rotor and Field Calibrator Module of the instant invention.
- the second independent or tandem rotor 20 provides an electronic measurement output which is independent from the first or main independent metering rotor 10. This allows a direct comparison to the independent output of the first or main independent metering rotor 10 at line conditions without the need for pressure and temperature corrections.
- the second independent metering rotor 20 is more reliable than the first or main independent metering rotor 10 since it is protected in its downstream location and it drives no mechanical output, unlike the first or main independent metering rotor 10 which does drive a mechanical output 40 as shown in FIGS. 2 and 3. This results in the mechanical curve 42 as shown in FIG. 6.
- the protected nature of the second independent metering rotor 20 also results in a longer service life.
- the second independent metering rotor 20 can run at a speed equal to, less than or greater than the first or main independent metering rotor 10, depending upon the pitch of the blade angle or discrete angle 44, in FIGS. 2 and 3, with respect to the axis of rotation of the second independent metering rotor, thus further enhancing its service life.
- the second independent metering rotor 20, without mechanical output could be used as the electronic output totalization for billing, with the main metering rotor 10 providing mechanical backup and checking.
- the output totalization 42 and 54 of each of the two independent metering rotors can also be averaged together to lessen the effects of each rotor on accuracy degradation and to provide a very reliable volume totalization 52.
- the tandem rotor 20 is independent of the main metering rotor 10 due to the stator vanes 28 between the two rotors. Therefore, the two independent metering rotors 10 and 20 can be easily replaced and recalibrated separately by the user in the shop at atmospheric conditions or in the field at operating pressure.
- the main independent metering rotor, module 62 of FIG. 7A and tandem metering rotor module 61 can be interchanged with other modules without factory recalibration.
- the current invention allows one to check the accuracy of the main rotor of a single rotor turbine meter.
- the accuracy of the meter being tested can be defined in the field at actual operating conditions, i.e., piping, pressure, temperature, gas specific gravity, over a broad flow range, without affecting the main meter rotor performance.
- Field calibration allows the user to make on-site repairs or accuracy adjustments to a working meter. This eliminates the need for retrieving a spare module from a distant warehouse and returning the damaged module to the shop for calibration.
- the field calibrator can also be used to simplify in-shop calibration of turbine meters. No elaborate piping or proving system is required since no pressure and temperature correction is needed. A meter can be tested in its own body by simply installing the calibration module, attaching an inlet pipe, and blowing air through the meter.
- FIGS. 8A,B two views of an enlarged sketch of a flow calibration module or tandem rotor metering module 61 that can replace the dummy housing 63.
- FIG. 7C of a single rotor turbine meter.
- the dummy housing is located in the area 65.
- FIG. 7A adjacent to the main meter module 62.
- the flow or calibration module or tandem rotor metering module 61 is located in the area 65 adjacent to the main meter module 62.
- the flow calibration module or tandem rotor metering module 61 includes a housing 24', a rotor 20, flow isolation or conditioning vanes 28 and a pulser 67.
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- Physics & Mathematics (AREA)
- Fluid Mechanics (AREA)
- General Physics & Mathematics (AREA)
- Measuring Volume Flow (AREA)
Abstract
Description
Claims (20)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US08/926,192 USRE36401E (en) | 1991-11-07 | 1997-09-09 | Tandem rotor turbine meter and field calibration module |
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US78882691A | 1991-11-07 | 1991-11-07 | |
| US08/125,344 US5473932A (en) | 1991-11-07 | 1993-09-22 | Tandem rotor turbine meter and field calibration module |
| US08/926,192 USRE36401E (en) | 1991-11-07 | 1997-09-09 | Tandem rotor turbine meter and field calibration module |
Related Parent Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US78882691A Continuation | 1991-11-07 | 1991-11-07 | |
| US08/125,344 Reissue US5473932A (en) | 1991-11-07 | 1993-09-22 | Tandem rotor turbine meter and field calibration module |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| USRE36401E true USRE36401E (en) | 1999-11-23 |
Family
ID=25145685
Family Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US08/125,344 Ceased US5473932A (en) | 1991-11-07 | 1993-09-22 | Tandem rotor turbine meter and field calibration module |
| US08/926,192 Expired - Fee Related USRE36401E (en) | 1991-11-07 | 1997-09-09 | Tandem rotor turbine meter and field calibration module |
Family Applications Before (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US08/125,344 Ceased US5473932A (en) | 1991-11-07 | 1993-09-22 | Tandem rotor turbine meter and field calibration module |
Country Status (1)
| Country | Link |
|---|---|
| US (2) | US5473932A (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6555926B2 (en) * | 2001-09-28 | 2003-04-29 | Baker Hughes Incorporated | Pulser |
| US20080048142A1 (en) * | 2006-08-24 | 2008-02-28 | Robertshaw Controls Company | Valve with Inherent Enhanced Turbulent Flow Metering Device and Flow Regulation |
| US20120090406A1 (en) * | 2009-06-25 | 2012-04-19 | Stefan Etter | Flowmeter materials for a beverage machine |
| US20120247225A1 (en) * | 2011-04-01 | 2012-10-04 | Daniel Measurement And Control, Inc. | Ultrasonic flow meter having cable shroud |
| US20140102215A1 (en) * | 2012-10-15 | 2014-04-17 | Sappel | Fluid turbine flow meter |
| US8789429B2 (en) | 2009-06-25 | 2014-07-29 | Nestec S.A. | Flowmeter structure for a beverage machine |
| US20140260674A1 (en) * | 2013-03-15 | 2014-09-18 | Gilbarco, Inc. | Viscosity dependent flow meter for use in fuel dispensing environments |
Families Citing this family (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5877430A (en) * | 1997-06-13 | 1999-03-02 | M&Fc Holding Company, Inc. | Pressure measuring system for gas flow meter |
| US6267013B1 (en) | 1998-11-18 | 2001-07-31 | Stephen T. Stark | Flow anomaly detector |
| NL1022963C2 (en) * | 2003-03-18 | 2004-09-23 | Instromet Bv | Turbine meter. |
| US7155956B2 (en) * | 2004-01-23 | 2007-01-02 | Terasen Gas Inc. | Medium, method and system for proving a turbine meter |
| US20090205815A1 (en) * | 2008-02-19 | 2009-08-20 | Schlumberger Technology Corp. | Downhole tool for measuring a fluid flow rate therethrough and a well completion incorporating same |
| US8096446B2 (en) * | 2008-11-17 | 2012-01-17 | Gilbarco, S.R.L. | Turbine flow meter for use in fuel dispensing envirnoments |
| DE102013007871A1 (en) * | 2013-05-08 | 2014-11-13 | Rma Mess- Und Regeltechnik Gmbh & Co. Kg | Method and measuring device for flow measurement of a gas in a pipeline by means of a turbine wheel gas meter |
| US10788343B2 (en) * | 2019-02-12 | 2020-09-29 | Sensus Spectrum Llc | Flow meter systems and methods providing configurable functionality |
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1993
- 1993-09-22 US US08/125,344 patent/US5473932A/en not_active Ceased
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- 1997-09-09 US US08/926,192 patent/USRE36401E/en not_active Expired - Fee Related
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|---|---|---|---|---|
| US2859616A (en) * | 1955-03-07 | 1958-11-11 | Hobson Ltd H M | Apparatus for indicating the rate of a flow of a fluid |
| US3241366A (en) * | 1957-01-17 | 1966-03-22 | Rockwell Mfg Co | Fluid-flow meter |
| US3053086A (en) * | 1957-02-12 | 1962-09-11 | Granberg Corp | Turbine type meter |
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| US6555926B2 (en) * | 2001-09-28 | 2003-04-29 | Baker Hughes Incorporated | Pulser |
| US20080048142A1 (en) * | 2006-08-24 | 2008-02-28 | Robertshaw Controls Company | Valve with Inherent Enhanced Turbulent Flow Metering Device and Flow Regulation |
| US7819023B2 (en) * | 2006-08-24 | 2010-10-26 | Robertshaw Controls Company | Valve with inherent enhanced turbulent flow metering device and flow regulation |
| US20120090406A1 (en) * | 2009-06-25 | 2012-04-19 | Stefan Etter | Flowmeter materials for a beverage machine |
| US8714031B2 (en) * | 2009-06-25 | 2014-05-06 | Nestec S.A. | Flowmeter materials for a beverage machine |
| US8789429B2 (en) | 2009-06-25 | 2014-07-29 | Nestec S.A. | Flowmeter structure for a beverage machine |
| US20120247225A1 (en) * | 2011-04-01 | 2012-10-04 | Daniel Measurement And Control, Inc. | Ultrasonic flow meter having cable shroud |
| US8770042B2 (en) * | 2011-04-01 | 2014-07-08 | Daniel Measurement And Control, Inc. | Ultrasonic flow meter having cable shroud |
| US20140102215A1 (en) * | 2012-10-15 | 2014-04-17 | Sappel | Fluid turbine flow meter |
| US9074916B2 (en) * | 2012-10-15 | 2015-07-07 | Sappel | Fluid turbine flow meter |
| US20140260674A1 (en) * | 2013-03-15 | 2014-09-18 | Gilbarco, Inc. | Viscosity dependent flow meter for use in fuel dispensing environments |
| US9377332B2 (en) * | 2013-03-15 | 2016-06-28 | Gilbarco Inc. | Viscosity dependent flow meter for use in fuel dispensing environments |
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