GB2026704A - Device for Measuring Fluid Flow in Tubing - Google Patents
Device for Measuring Fluid Flow in Tubing Download PDFInfo
- Publication number
- GB2026704A GB2026704A GB7924820A GB7924820A GB2026704A GB 2026704 A GB2026704 A GB 2026704A GB 7924820 A GB7924820 A GB 7924820A GB 7924820 A GB7924820 A GB 7924820A GB 2026704 A GB2026704 A GB 2026704A
- Authority
- GB
- United Kingdom
- Prior art keywords
- orifice
- flow
- section
- cross
- tubing
- 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.)
- Granted
Links
- 239000012530 fluid Substances 0.000 title claims abstract description 7
- 238000011144 upstream manufacturing Methods 0.000 description 3
- 239000007788 liquid Substances 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 238000010079 rubber tapping Methods 0.000 description 2
- 230000035945 sensitivity Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
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
- G01F1/20—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 by detection of dynamic effects of the flow
- G01F1/22—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 by detection of dynamic effects of the flow by variable-area meters, e.g. rotameters
-
- 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
- G01F1/34—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 by measuring pressure or differential pressure
- G01F1/36—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 by measuring pressure or differential pressure the pressure or differential pressure being created by the use of flow constriction
- G01F1/363—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 by measuring pressure or differential pressure the pressure or differential pressure being created by the use of flow constriction with electrical or electro-mechanical indication
-
- 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
- G01F1/34—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 by measuring pressure or differential pressure
- G01F1/36—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 by measuring pressure or differential pressure the pressure or differential pressure being created by the use of flow constriction
- G01F1/40—Details of construction of the flow constriction devices
- G01F1/42—Orifices or nozzles
-
- 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
- G01F1/34—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 by measuring pressure or differential pressure
- G01F1/50—Correcting or compensating means
Landscapes
- Physics & Mathematics (AREA)
- Fluid Mechanics (AREA)
- General Physics & Mathematics (AREA)
- Measuring Volume Flow (AREA)
- Flow Control (AREA)
Abstract
A device for measuring the flow rate of a fluid travelling along tubing comprises a flow orifice (40, 50) of continuously variable cross-section formed by a multiple orifice valve (2), a servo-mechanism (60) connected to vary the cross-section of the said flow orifice by means of a moving component (5), a unit (6) sensitive to the loss of head caused by the flow orifice, and calculating means (9) for calculating the flow rate as a function of the said head loss and the cross- section of the said orifice, the servo- mechanism being arranged to keep the head loss within a predetermined range. The cross-section of the orifice is monitored by a cursor (71) attached to the moving component (5) and co- operating with a position sensor (8). <IMAGE>
Description
SPECIFICATION
Device for Measuring Fluid Flow in Tubing
The present invention relates to a device for measuring the flow rate of a fiuidtravelling under pressure in tubing.
Usually, the flow rate through tubing is measured by means of apparatus including a head loss unit, e.g. of the diaphragm type, i.e. having a predetermined fixed flow cross-section.
A major drawback with this type of apparatus lies in its small dynamic range. For exampie, if the flow should drop from 1 to 0.1 the head loss would pass from 1 to 0.01 which generally tends to make low flow rate measurements inaccurate.
Indeed, supposing that a particular tube conveys a flow rate that may vary from a maximum rate OM to a minimum rate Qm, a minimum head loss, AP1, must be created to obtain an adequate measurement taking into account the sensitivity of the instruments, the fluctuations in flow rate and the Reynolds number of the flow. There is a maximum tolerable head loss, AP2. Generally speaking, the difference between API and AP2 is small. It is thus only possible to use apparatus of the head-loss type if means are provided to maintain the pressure in the rangeAPi,AP2.
This drawback can be mitigated by using different diaphragms for different flow rates, the diaphragms being placed in an arrangement for facilitating selection of the most appropriate diaphragm, but this makes for a complex and bulky assembly.
Preferred embodiments of the present invention provide a measuring device adequately adapted to measure all rates of flow to be expected in a particular situation.
The present invention provides a device for measuring the flow rate of a fluid travellling along tubing, the device comprising a flow orifice of continuously variable cross-section, a servomechanism connected to vary the cross-section of the said flow orifice by means of a moving component, a unit sensitive to the loss of head caused by the flow orifice, and calculating means for calculating the flow rate as a function of the said head loss and the cross-section of the said orifice, the servo-mechanism being arranged to keep the head loss within a predetermined range and the orifice of variable cross-section being provided by a multiple orifice valve. The head loss may be maintained substantially constant.
The unit sensitive to the head loss may comprise a differential pressure sensor arranged across the variable section orifice, and the unit sensitive to the flow cross-section to the orifice may comprise a cursor fixed to move with the moving component. The calculating means may be electronic.
An embodiment of the invention is described by way of example with reference to the sole figure of the accompanying drawing which is a diagrammatic view of a device for measuring liquid flow through tubing under the control of a multiple orifice valve.
In the figure, the reference 1 designates as a whole tubing for fluid flowing in the direction of the arrow F situated between a length of upstream tubing 11 and a- length of downstream tubing 12. A multiple orifice valve 2 analogous to that described in French patent application nO 76 17956 published under the nO 2355237 is disposed between the flange 1 3 of the upstream length and the flange 14 of the downstream length.
The valve 2 comprises an annular body 3 having an annular recess 20 in which a fixed plate 4 and a moving plate 5 are disposed. The moving plate 5 is controlled by a motor unit of conventional type and not shown. The fixed plate 4 comprises a set of orifices 40 of identical crosssection and the moving plate 5 also comprises a set of orifices 50 of identical cross-section.
Depending the position of the moving plate 5, the orifices 50 of the fixed plate 4 may face solid parts of the moving plate 5, which corresponds to the valve being totally closed, or else they may be partially uncovered by adjacent orifices 40, or eise they may be in coincidence with the orifices 40, which corresponds to the fully opened position of the valve.
The flow of liquid in the tubing causes a head loss proportional to the square of the flow, but also inversely proportional to a function of the free flow cross-section offered by the orifices as a result of the greater or lesser coincidence of each of the orifices 40 with a corresponding orifice 50.
Under these conditions, the head loss obtained makes it possible to measure over a very wide dynamic range with fair accuracy.
The head loss is detected by a sensor 6 connected to an upstream tapping 61 and a downstream tapping 62 disposed on either side of the flow orifices of the valve.
Indeed, the degree of opening of the valve may be obtained satisfactorily provided it is free from play and vibrations.
As a function of a head loss measured between the orifices 40 and 50, the sensor 6 controls a servo-mechanism 60 which continuously varies the free cross-section of the orifices 40 and 50 by moving a controlled rod 7 in such a manner as to maintain the head loss substantially constant and predetermined and lying in the previously defined range AP1, AP2.
The end of the rod 7 that is connected to the moving plate 5 and which moves therewith, includes a cursor 71 cooperating with a position sensor 8.
The sensors 6 and 8 thus transmit data concerning the loss of head across the orifices 40 and 50 of the valve and the position of the valve to calculation means 9.
The function of the calculation means 9 is to translate the position of the valve into an effective free-flow cross-section of the orifices and then to calculate the flow rate as a function of this flow section and of the head loss. The result is then displayed on a display 90 attached to the calculation means 9.
Claims (6)
1. A device for measuring the flow rate of a fluid travelling along tubing, the device comprising a flow orifice of continuously variable cross-section, a servo-mechanism connected to vary the cross-section of the said flow orifice by means of a moving component, a unit sensitive to the loss of head caused by the flow orifice, and calculating means for calculating the flow rate as a function of the said head loss and the crosssection of the said orifice, the servo-mechanism being arranged to keep the head loss within a predetermined range and the orifice of variable cross-section being provided by a multiple orifice valve.
2. A device according to claim 1, wherein the multiple orifice valve is a valve controlling the flow in the tubing.
3. A device according to claim 1 or 2, wherein the unit sensitive to head loss comprises a differential pressure sensor arranged about the variable section orifice.
4. A device according to claim 1,2 or 3, wherein the flow cross-section of the orifice is sensed by a sensor operated by a cursor moving with the moving component.
5. A device according to any preceding claim, wherein the calculating means is electronic.
6. A device for measuring the flow rate of a fluid travelling along tubing, substantially as herein described with reference to the accompanying drawing.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR7822258A FR2432160A1 (en) | 1978-07-27 | 1978-07-27 | DEVICE FOR MEASURING THE FLOW OF A PIPELINE |
Publications (2)
Publication Number | Publication Date |
---|---|
GB2026704A true GB2026704A (en) | 1980-02-06 |
GB2026704B GB2026704B (en) | 1982-11-10 |
Family
ID=9211255
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB7924820A Expired GB2026704B (en) | 1978-07-27 | 1979-07-17 | Device for measuring fluid flow in tubing |
Country Status (9)
Country | Link |
---|---|
JP (1) | JPS6015001B2 (en) |
BE (1) | BE877571A (en) |
DE (1) | DE2929471A1 (en) |
ES (1) | ES482911A1 (en) |
FR (1) | FR2432160A1 (en) |
GB (1) | GB2026704B (en) |
GR (1) | GR69642B (en) |
IT (1) | IT1118918B (en) |
MA (1) | MA18531A1 (en) |
Cited By (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0025576A2 (en) * | 1979-09-14 | 1981-03-25 | Giuseppe Torresin | Turbulence conveyor flowmeter for medical use |
EP0086259A2 (en) * | 1981-11-13 | 1983-08-24 | Hamilton Bonaduz AG | Process and device to determine a gas flow |
US4581707A (en) * | 1980-05-30 | 1986-04-08 | John Millar (U.K.) Limited | Microprocessor controlled valve flow indicators |
EP0223300A2 (en) * | 1985-11-20 | 1987-05-27 | EMS Holland BV | Gas meter |
FR2594541A1 (en) * | 1986-02-14 | 1987-08-21 | Air Liquide | METHOD FOR CONTROLLING THE FLOW RATE IN A VALVE AND APPARATUS FOR IMPLEMENTING SAID METHOD |
US4801245A (en) * | 1986-05-02 | 1989-01-31 | Borsig Gmbh | Method of damping surges in recirpocating compressors |
US4918994A (en) * | 1987-05-21 | 1990-04-24 | Ems Holland B.V. | Gas meter |
EP0392271A1 (en) * | 1989-04-03 | 1990-10-17 | Landis & Gyr Business Support AG | Measuring device for fluid flow and/or quantities of heat |
EP0392272A1 (en) * | 1989-04-03 | 1990-10-17 | Landis & Gyr Technology Innovation AG | Measuring and/or controlling device for fluid flow and/or quantities of heat |
US5016468A (en) * | 1988-04-06 | 1991-05-21 | T. A. Jennings Associates, Inc. | Method and apparatus for the determination of moisture in materials |
EP0565485A1 (en) * | 1992-04-08 | 1993-10-13 | EMILE EGGER & CO. AG | Method and device to measure the flow of a medium and application of the method |
NL1003973C2 (en) * | 1996-09-06 | 1998-03-09 | Berkin Bv | Method for instantaneous identification of a gas or liquid flow and device for carrying out the method. |
GB2497321A (en) * | 2011-12-06 | 2013-06-12 | Senico Ltd | Multi-phase metering of fluid flows |
Families Citing this family (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5992313A (en) * | 1982-11-18 | 1984-05-28 | Kansai Electric Power Co Inc:The | Flow rate detector |
JPS6138517U (en) * | 1984-08-10 | 1986-03-11 | 株式会社 武藤電機 | flow measuring device |
JPS6197721U (en) * | 1985-12-04 | 1986-06-23 | ||
JPS6329210Y2 (en) * | 1986-05-15 | 1988-08-05 | ||
JPH02297023A (en) * | 1989-05-11 | 1990-12-07 | Kubota Konpusu Kk | Water distribution controller |
JPH0349101U (en) * | 1989-09-22 | 1991-05-13 | ||
CN106052774A (en) * | 2016-06-21 | 2016-10-26 | 成都国光电子仪表有限责任公司 | Differential pressure type flow meter |
CN106123975A (en) * | 2016-06-21 | 2016-11-16 | 成都国光电子仪表有限责任公司 | A kind of multi-functional effusion meter of nozzle-type |
CN106153129A (en) * | 2016-06-21 | 2016-11-23 | 成都国光电子仪表有限责任公司 | Natural gas flowmeter |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE869421C (en) * | 1951-12-25 | 1953-03-05 | Bopp & Reuther Gmbh | Adjustable throttle measuring device with segment aperture |
DE1295254B (en) * | 1958-03-03 | 1969-05-14 | Sulzer Ag | Arrangement for controlling the amount of medium flowing through a line with a throttle element per unit of time |
FR1340463A (en) * | 1962-11-21 | 1963-10-18 | Siemens Ag | Device for regulating a flow |
US3640307A (en) * | 1970-02-24 | 1972-02-08 | Allied Thermal Corp | Apparatus for balancing fluid distribution systems |
FR2355237A1 (en) * | 1976-06-14 | 1978-01-13 | Alsthom Cgee | ORGAN WITH ADJUSTABLE PRESSURE DROP |
-
1978
- 1978-07-27 FR FR7822258A patent/FR2432160A1/en active Granted
-
1979
- 1979-07-09 BE BE1/9461A patent/BE877571A/en not_active IP Right Cessation
- 1979-07-17 MA MA18728A patent/MA18531A1/en unknown
- 1979-07-17 GB GB7924820A patent/GB2026704B/en not_active Expired
- 1979-07-18 GR GR59631A patent/GR69642B/el unknown
- 1979-07-20 DE DE19792929471 patent/DE2929471A1/en not_active Ceased
- 1979-07-26 IT IT68557/79A patent/IT1118918B/en active
- 1979-07-27 ES ES482911A patent/ES482911A1/en not_active Expired
- 1979-07-27 JP JP54096625A patent/JPS6015001B2/en not_active Expired
Cited By (23)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0025576A2 (en) * | 1979-09-14 | 1981-03-25 | Giuseppe Torresin | Turbulence conveyor flowmeter for medical use |
EP0025576A3 (en) * | 1979-09-14 | 1983-04-13 | Giuseppe Torresin | Turbulence conveyor flowmeter for medical use |
US4581707A (en) * | 1980-05-30 | 1986-04-08 | John Millar (U.K.) Limited | Microprocessor controlled valve flow indicators |
EP0086259A2 (en) * | 1981-11-13 | 1983-08-24 | Hamilton Bonaduz AG | Process and device to determine a gas flow |
EP0086259A3 (en) * | 1981-11-13 | 1985-06-12 | Hamilton Bonaduz AG | Process and device to determine a gas flow |
EP0223300A2 (en) * | 1985-11-20 | 1987-05-27 | EMS Holland BV | Gas meter |
EP0223300A3 (en) * | 1985-11-20 | 1988-05-18 | EMS Holland BV | Gas meter |
FR2594541A1 (en) * | 1986-02-14 | 1987-08-21 | Air Liquide | METHOD FOR CONTROLLING THE FLOW RATE IN A VALVE AND APPARATUS FOR IMPLEMENTING SAID METHOD |
EP0237390A1 (en) * | 1986-02-14 | 1987-09-16 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Method for controlling fluid flow through a valve and apparatus for carrying out this method |
US4763681A (en) * | 1986-02-14 | 1988-08-16 | L'air Liquide | Process for controlling the flow of a fluid in a valve and apparatus for carrying out said process |
US4801245A (en) * | 1986-05-02 | 1989-01-31 | Borsig Gmbh | Method of damping surges in recirpocating compressors |
US4918994A (en) * | 1987-05-21 | 1990-04-24 | Ems Holland B.V. | Gas meter |
US5016468A (en) * | 1988-04-06 | 1991-05-21 | T. A. Jennings Associates, Inc. | Method and apparatus for the determination of moisture in materials |
EP0392271A1 (en) * | 1989-04-03 | 1990-10-17 | Landis & Gyr Business Support AG | Measuring device for fluid flow and/or quantities of heat |
EP0392272A1 (en) * | 1989-04-03 | 1990-10-17 | Landis & Gyr Technology Innovation AG | Measuring and/or controlling device for fluid flow and/or quantities of heat |
US5125753A (en) * | 1989-04-03 | 1992-06-30 | Landis & Gyr Betriebs Ag | Device to measure flow-through and/or quantity of heat |
EP0565485A1 (en) * | 1992-04-08 | 1993-10-13 | EMILE EGGER & CO. AG | Method and device to measure the flow of a medium and application of the method |
US5987981A (en) * | 1996-06-09 | 1999-11-23 | Berkin B.V. | Method for momentarily identifying a gas or liquid flow, and device for carry out the method |
NL1003973C2 (en) * | 1996-09-06 | 1998-03-09 | Berkin Bv | Method for instantaneous identification of a gas or liquid flow and device for carrying out the method. |
EP0829793A1 (en) * | 1996-09-06 | 1998-03-18 | Berkin B.V. | Method for momentarily identifying a gas or liquid flow, and device for carrying out the method |
GB2497321A (en) * | 2011-12-06 | 2013-06-12 | Senico Ltd | Multi-phase metering of fluid flows |
GB2497321B (en) * | 2011-12-06 | 2014-06-18 | Senico Ltd | Multi-phase metering of fluid flows |
US9671793B2 (en) | 2011-12-06 | 2017-06-06 | Senico Limited | Multi-phase metering of fluid flows |
Also Published As
Publication number | Publication date |
---|---|
JPS6015001B2 (en) | 1985-04-17 |
GR69642B (en) | 1982-07-06 |
ES482911A1 (en) | 1980-04-16 |
FR2432160B1 (en) | 1982-04-02 |
JPS5522188A (en) | 1980-02-16 |
IT1118918B (en) | 1986-03-03 |
BE877571A (en) | 1980-01-09 |
FR2432160A1 (en) | 1980-02-22 |
GB2026704B (en) | 1982-11-10 |
IT7968557A0 (en) | 1979-07-26 |
DE2929471A1 (en) | 1980-02-07 |
MA18531A1 (en) | 1980-04-01 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PCNP | Patent ceased through non-payment of renewal fee |