AU594362B2 - Fluid flowmeter - Google Patents

Description

_i 1 v AU-AI-62288/86 WOVRLD INTELLETIL P ERTYPRO aATIO P CT I tio I ra INTERNATIONAL APPLICATION PUI3LISHE N R THf 4 T AINTET PT (51) International Patent Classification 4 International Publication Number: WO 88/ 01369 GOlF 1/10, 1/50 Al International Publication Date: 25 February 1988 (25.02.88) (21) Interrnational Application Number: PCT/US86/01719 Published Withi international search report.

(22) International Filing Date: 20 August 1986 (20.08.86) (71) Applicant: AMETEK, INC. [US/US]; McCrometer Division, 3255 West Stetson Avenue, H-emet, CA 92343

(US).

(72) Inventor: McCALL,' Floyd 26031 Dumond Road, This (1O~cumcflt Conta~the I Hemet, CA 92344 anencti 9an s corrcec)t £,in (74) Agent: VERBECK, Bruno, 110 West C Street, Suiteprnig 12.12, San Diego, CA 92101-3907 (US).

(81) Designated States: AT (European patent), AU, BE (Eu- A. O.J.P. 3 1 MIAR 1988 ropean patent), CH- (European patent), DE (European patent), FR (European patent), GB (European patent), IT (European patent), JP, KP, LU (European patent), NL (European patent), SE (European patent).

AUSTRALIAN

-8 MAR 1988 PATENT OFFICE (54)Title: FLUID FLOWMETER _t4 i

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(57) Abstract A fluid flowmcter which includes a fluid displacement member (10) positioned in the fluid flow to substantially linearize the velocity profile associated therewith. In one form or the Invention the pressure differential in the fluid extisting across the fluid displacement member (10) Is advantageously exploited, and several embodiments thereof are disclosed. In another form of the invention the fluid digplaccment member (10A) is utilized to produce trailing vortices.

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DESCRIPTION

FLUID FLOWMETER Technical Field The present invention relates in general to flowmeters, and in particular to flowmeters of the fluid displacement type.

Background Art A particularly troublesome problem associated with flowmeter design and implementation derives from the inherent non-linearity of the velocity profile of fluid as it courses through a section of pipe. Thus, the interaction between the fluid and the pipe wall results in a curved velocity profile wherein the fluid velocity in the vicinity of the pipe center .is greater than the fluid velocity adjacent the pipe wall. Compounding this problem is the fact that altering the fluid flow rate results in a non-linear alteration of the velocity profile.

For virtually any flow condition the non-linearity of the velocity profile can be converted into a mean velocity of the fluid and an associated mean crosssectional area. This does not, however, overcome the problem of non-linearity since changes in fluid flow conditions result in non-linear changes to the mean velocity and its associated cross-sectional area.

Hitherto, the aforementioned non-linear characteristics of the fluid velocity profile have been accepted as an uncontrolled variable in flowmeter design with 1

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-2the knowledge that such non-linearity would necessarily detract from the range of flow rate conditions over which the flowmeter could operate within acceptable error limits. This range is referred to as a flowmeter's linear rangeability and, until the present invention, has been generally quite limited. For example, flowmeters employing conventional orifice plates typically exhibit a linear rangeability in the order of only about 3:1.

The problem of non-linearity also manifests itself with another type of flowmeter known as a vortexmeter.

Very briefly, it is well known that an object placed in a moving fluid sheds vortices from the edges thereof, and that the rate of vortex production is in part a function of the fluid velocity about the object.

Exemplary embodiments of such vortex flowmeters can be found in U.S. Patent Nos. 4,404,858 and 4,416,159.

These vortexmeters, like the orifice plate, are also quite limited in their linear rangeability because of the non-linearity of the fluid velocity profile, as previously discussed.

In view of the foregoing drawbacks existing in the prior art, it would be highly desirable and beneficial to provide a flowmeter with some mechanism for reducing the non-linearity of the fluid velocity profile. In this regard, the ability to reduce such non-linearity would result in a flowmeter having increased linear rangeability. To the extent that the non-linearity can be reduced over a relatively large range of flow conditions, then in that event such a flowmeter. would have a linear rangeability rendering it particularly useful for measuring flow under widely varying flow conditions and in widely varying industrial applications.

i i *tftA -3- In one broad form there is provided a fluid flow apparatus comprising a main tubular conduit of uniform internal configuration for conducting a fluid the;'ethrough in a predetermined direction, and a fluid displacement member mounted with a supporting member In said main conduit to deflect the fluid through a region defined by the periphery of said fluid displacement member and the interior surface portion of said main conduit proximate said periphery, said fluid displacement member including a first sloped wall portion on the side thereof facing upstream in the direction of fluid flow, and a second sloped wall portion on the side thereof facing downstream in the direction of fluid flow, said first sloped wall portion being effective to linearize the velocity profile of the fluid in said region over a predetermined range of fluid flow rates through said main conduit, said second sloped wall portion being effective to optimize the return velocity of the fluid as it reassumes free stream conditions in said conduit downstream from said displacement member.

In a further broad form there is provided an apparatus for measuring fluid flow comprising a main tubular conduit for conducting a fluid therethrough in a predetermined direction, a fluid displacement member mounted in said main conduit to deflect the fluid to flow through a region defined by S the periphery of said fluid displacement member and the interior surface portion of said main conduit proximate said periphery said fluid displacement S, member being effective to substantially linearize the velocity profile of said fluid in at least said region over a predetermined range of fluid flow rates through said main conduit, a smaller tubular conduit for diverting a portion of the fluid passing through said main conduit along an auxiliary flowpath having one end positioned upstream of said fluid displacement member and its opposite end positioned downstream of said region, and means connected with said auxiliary flowpath effective to measure fluid flow therethrough.

0 In yet a further broad form there is provided a fluid flow apparatus comprising a main tubular conduit of uniform internal configuration for conducting a fluid therethrough in a predetermined direction, a smaller tubular conduit in said main conduit having a downstream end centered axially within said main conduit, such that the center lines of the main conduit and the downstream end of the smaller conduit are substan- tlally coaxial, a fluid displacement member mounted on the downstream end of said smaller conduit c within said main conduit such that the axis of symmetry of said fluid displacement member is substantially coaxial with the axes of said main conduit and the downstream end of said smaller conduit, said fluid VAL 148z 4/ -ort 9 3a displacement member being smaller than said main conduit and larger than the smaller conduit and being mounted in said main conduit substantially perpendicular to the direction of fluid flow through said main conduit, said fluid displacement member having sloped wall means facing in the upstream direction for deflecting the fluid to flow through a region defined by the periphery of said fluid displacement member and the interior surface portion of said main conduit proximate said periphery, said sloped wall means being effective to substantially linearize the velocity profile of said fluid in said region, said fluid displacement member having sloped wall means facing in the downstream direction effective to substantially optimize the return velocity of the fluid as it reassumes free stream conditions in said main conduit downstream of said displacement member, the sloped wall means facing in the upstream direction extending at an angle in the order of at least about 390 to the plane defined by the periphery of said fluid displacement member and the sloped wall means facing in the downstream direction extending at an angle in order of about 220 to said plane.

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_7r -9 :ii m lfg l WO 88/01369 PCT/US86/01719 -4- The inventor herein has discovered that a flowmeter with increased linear rangeability can be produced by the placement of a substantially flat disc in a position as above-described. The disc operates to reduce the non-linearity of the fluid velocity profile in the aforementioned region over a determinable range of flow rate conditions such that the pressure differential across the region can be taken as a relatively accurate indicator of fluid velocity through the region. With the fluid velocity'profile tending towards linearization, and with the area of the region being fixed, it then becomes clear that a greater linear correspondence 'is achieved through the region in terms of changes in both fluid velocity and fluid flow rate. This linearization of the fluid flow has equal import with respect to measuring flow using vortexmeters of the type previously discussed.

While the use of merely a flat disc as the fluid displacement member results in a flowmeter of enhanced linear rangeability, even greater linear rangeability can be realized by providing the disc on the upstream side thereof with a sloped wall extending outwardly from the disc. Empirical and theoretical studies have revealed that such a sloped wall interacts with the fluid in such a manner that a very high degree of linearity in the fluid velocity profile is achieved as the fluid passes through the region between the disc periphery and the inner surface of the pipe or conduit, and that this very high degree of linearity holds true for an unusually and unexpectedly large range of fluid flow rates, thus resulting in a flowmeter. having an unusually and unexpectedly large linear rangeability. i f WO 88/01369 PCT/US86/01719 The extent to which the sloped wall extends upstream from the disc, i.e. its slope, is limited primarily by practical considerations. Generally speaking, the greater the extension, then the greater the linearization of the velocity profile in the aforementioned region. A drawback associated with a large extension is, however, that the pressure differential across the region is correspondingly reduced and consequently becomes more difficult to measure with a high degree of confidence as to its accuracy. Thus, the ability of available equipment to measure pressure represents a practical limitation, with the ultimate objective being to maximize the linearity of the fluid velocity profile in the region while maintaining a sufficiently large pressure differential across the region to ensure accurate measurement.

While not critical of the invention, the fluid displacement member may also include a sloped wall extending outwardly from the downstream side thereof for minimizing the line pressure drop across the fluid displacement member and for optimizing the return velocity of the fluid as it once again reassumes free stream conditions in the pipe or conduit.

By virtue of its ability to effect substantial linearization of the fluid velocity profile, the fluid displacement member above-described may be incorporated Sinto any one of a plurality of flowmeter systems. In one such system conduit means are provided for diverting a portion of the fluid communicating through the pipe or conduit along an auxiliary or secondary flowpath having one end positioned upstream of the fluid displacement member and its opposite end positioned just downstream

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WO 88/01369 PCT/US86/01719 -6of the aforementioned region. The pressure differential across the region manifests itself as a pressure differential between the two ends of the auxiliary flowpath.

The dimensions of the auxiliary flowpath are selected such that a.constant of proportionality exists between the fluid diverted along the auxiliary flowpath and the remainder of the fluid flowing through the conduit or pipe, and this relationship holds true throughout the entire linear range of the flowmeter system. Totalizer means, which may take the form of a relatively small turbine, are disposed in the auxiliary flowpath for measuring the total volume of fluid passing therethrough, and this measurement is multiplied by a predetermined constant of proportionality to determine the total volume of fluid flowing through the pipe or conduit.

In a variant form of the above flow meter system, the totalizer means is replaced by a rate-of-flow means, which may take the form of a conventional rotometer, for measuring the rate of fluid flow through the auxiliary flowpath. This measurement may likewise be multiplied by a predetermined constant of proportionality to yield fluid flow rate through the pipe or conduit.

Yet another variant form of the foregoing flowmeter systems includes positioning a pressure transducer across the auxiliary flowpath. In this flowmeter system fluid would not flow along the auxiliary flowpath; however, a pressure differential would be established across the pressure transducer by virtue of the different pressures S0 existing at each end of the auxiliary flowpath. This pressure differential, coupled with knowledge that the non-linearity of the fluid velocity profile through the region has been reduced, enables one to determine with a high degree of confidence as to its accuracy either total

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!L i r .a r- WO 88/01369 PCT/US86/01719 -7volume, rate of flow, or both.

In yet another embodiment of the present invention, a flowmeter system is provided wherein a plurality of pressure transducers are positioned downstream of the region in order to sense pressure fluctuations in the fluid resulting from the vortices shed from the periphery of the fluid displacement member. These pressure transducers are coupled to a processor which converts the frequency of the pressure fluctuations into either total volume, rate of flow, or both.

Brief Description of the Drawings The above-mentioned and other objects and features of this invention and the manner of attaining them will become apparent, and the invention itself will be best understood, by reference to the following description of the invention taken in conjunction with the accompanying drawings, wherein: Figure 1 is a partial, cross-sectional view of the preferred embodiment of a fluid displacement member constructed in accordance with the disclosure herein and as mounted in a section of conduit or pipe through which fluid is communicating from left to right; Figure 2 is a partial, crbss-sectional view of a differential pressure-type flowmeter system employing the fluid displacement member shown in Figure 1; Figure 3 is a partial, cross-sectional view of a vortexmeter system employing a. fluid displacement member similar to that shown in Figure 1; Figure 4 is a side view of a specific embodiment of the fluid displacement member shown in Figure 1; and h h Ii e 741 WO 88/01369 PCT/US86/01719 -8- Figure 5 is a front view of the fluid displacement member shown in Figure 4 as 'taken in the direction of line Best Mode for Carrying Out the Invention Referring now to the drawings, and in particular to Figure i, therein is shown the preferred embodiment of a fluid displacement member 10 constructed in accordance with the preferred practice of the present invention. Stated in greater detail, fluid displacement member 10 comprises a substantially circular disc 11 having a bore 12 extending transversely therethrough and defining an aperture 13 on the rear or downstream side thereof. Bore 12 is dimensioned to receive the distal end portion of a hollow support arm 14, with the inward extension of support arm 14 being limited by an integral shoulder 15. Removable fastening means, such as the illustrated set screw 16, are provided for securing disc 11 to support arm 14.

Disc 11 is mounted on support arm 14 in substantially coaxial alignment with the longitudinal axis of a section of pipe 20 and is positioned therein such that the plane defined by the edge or periphery 17 of disc 11 is oriented substantially perpendicular to the direction of fluid flow through pipe 20. Defined between periphery 17 and the inner surface 21 of pipe 20 is a substantially annular ri space or region 17A of fixed cross-sectional area through which fluid coursing along pipe 20 must flow in order to pass around the obstruction formed by disc 11.

Means for linearizing the velocity profile of the fluid, i.e. reducing the non-linearity associated therewith, as it passes through the aforementioned 7* i' tt WO 88/01369 PCT/US86/01719 -9region are included by providing disc 11 with a sloped wall portion 18 extending outwardly from the plane of periphery 17 on the side thereof facing upstream. A sloped wall portion 19 is also provided on the opposite side of the plane, the outward extension of sloped wall portion 19 preferably being less than that of sloped wall portion 18.

The above-described fluid displacement member may be employed to produce a plurality of flowmeter systems, and the form of several such systems will be more fully understood by now referring to Figure 2. More particularly, Figure 2 illustrates a flowmeter system having hollow support arm 14 in fluid communication with a conduit 22 extending through pipe 20 a distance sufficient to position its inlet 23 in the fluid flow at a location upstream'of fluid displacement member 10. In this manner an auxiliary fluid flowpath is defined between inlet 23 and aperture 13 on the rear of disc 11.

By virtue of the pressure differential existing between inlet 23 and aperture 13, a plurality of conventional flow measurement devices can be positioned in the auxiliary flowpath to measure fluid flow through pipe These devices are illustrated in schematic form and generally referred to by reference numeral 24.

One flowmeter system of the type shown in Figure 2 comprises a by-pass flowmeter wherein reference numeral 24 signifies a small turbine mounted in the auxiliary flowpath for measuring the total volume of fluid communicating along the auxiliary flowpath -'i from inlet 23 to aperture 13. Fluid through the auxiliary flowpath bears a fixed relationship to the fluid through pipe 20 and, therefore, one is thus able to determine total fluid flow through the by-pass flowmeter system.

WO 88/01369 PCT/US86/01719 A variant form of the above-described flowmeter system substitutes a conventional rotometer for the turbine to thereby yield the rate of fluid flow through pipe In yet another variant form a differential pressure transducer is mounted across the auxiliary flowpath to directly sense and measure the pressure differential between inlet 23 and aperture 13. The output from the pressure transducer is connected to a microprocessor (not shown) for determining either total flow, flow rate, or both.

Figure 3 illustrates yet another practical application of the present invention as adapted to produce a vortexmeter. More particularly, a fluid displacement member 10A, which is substantially identical to the fluid displacement member 10 of Figures 1 and 2 except that it is preferably a solid body not having an aperture on the rear thereof, is substantially coaxially supported within a section of pipe 20 by a support arm 14A. A plurality of pressure sensors 25 are mounted on the downstream side of fluid displacement member 10A at a position enabling them to sense pressure fluctuations in the fluid resulting from vortices shed from the periphery 17. Pressure sensors 25 are connected via electrical leads 26 to. a processor 27 which measures the frequency of the pressure fluctuations and converts that frequency into either total fluid flow, fluid flow rate, or both.

S While the precise mechanism by which the present SIinvention interacts with the fluid flow through a pipe to reduce the non-linearity associated with the fluid velocity profile is not altogether completely understood, it is believed that the fluid displacement member creates I /1 r Ai WO 88/01369 PCT/US86/01719 -lla turbulent zone in the pipe extending upstream from the disc which expands and contracts in response to changing flow conditions. As a consequence, a flowmeter embodying the present invention exhibits an unusually and unexpectedly large linear rangeability.

An even greater understanding of this invention can be obtained by now referring to Figures 4 and which illustrate a specific embodiment that was constructed and subjected to empirical s.tudies in order to ascertain its linear rangeability within a given section of pipe. All dimensions shown in the figures, except for angles, are in inches.

A test rig was constructed by mounting the disc shown in Figures 4 and 5 within an elongated section of pipe having a nominal inner dameter of 10.156 inches.

A plurality of taps were spaced axially, along the pipe to permit a pressure probe to be inserted into the fluid flow for pressure measurements at various positions upstream, about, and downstream from the disc. With water flowing through the pipe, pressure measurements Swere taken at each of the taps for different flow rate conditions, and those measurements were then correlated to develop pressure profiles along the length of the pipe for each flow condition. A study of those pressure profiles revealed that the point at which the free stream pressure of the fluid began to drop was a function of the flow rate, and as the flow rate increased that point 3 shifted further upstream from the disc.

The pressure measurements also yielded pressure drop across the disc for each flow rate condition, and a.graph was prepared plotting pressure drop on i one axis and the square of the fluid flow rate on the WO 88/0 1369 PCT/US86/031719 -12other axis, The plotted data produced a line of substantially constant slope and demonstrated that the test rig had an unusually and unexpectedly large linear rangeability within the range of about 500 to 4,500 jallons per minute of water, In view of the foregoing it will be understood that disclosed herein is an invention, useful for nwasuring both liquid and gas flows, which emrbraces each of the general objects therefor earlier stated. In this regard it should be noted that the invention is of quite simple construction and, except for the devices included to measure flow along the auxiliary flowpath, includes no moving parts. Thus, the invention is particularly useful in fluid environments containing solids that cause breakdowns in conventional flowmeter systems.

While various particular embodiments of the present invention have been disclosed herein, it will be understood that various changes, rearrangements, and modifications can be made thereto without departing from the essence and scope of the invention as defined in the appended claims. For example, Figures 4 and 5 each include specific details concerning values associated with the component parts of a particular embodiment.

Those values are considered to be merely illustrative of that particular embodiment of the invention. Therefore, it is intended that the present disclosure not be interpreted in a limiting senge and that obvious vartants of the invention are comprehended to be within its essence and scope.

Claims (22)

1. Fluid flow apparatus comprising a main tubular conduit of uniform internal configuration for conducting a fluid therethrough in a predetermined direction, and a fluid displacement member mounted with a supporting member in said main conduit to deflect the fluid through a region defined by the periphery of said fluid displacement member and the interior surface portion of said main conduit proximate said periphery, said fluid displacement member including a first sloped wall portion on the side thereof facing upstream in the direction of fluid flow, and a second sloped wall portion on the side thereof facing downstream in the direction ,f fluid flow, said first sloped wall portion being effective to linearize the velocity profile of the fluid in said region over a predetermined range of fluid flow rates through said main conduit, said second sloped wall portion being effective to optimize the return velocity of the fluid as it reassumes free stream conditions in said conduit downstream from said displacement member.

2. Fluid flow apparatus as set forth in claim 1, wherein the outward extension of said first sloped wall portion is not less than the outward extension of said second sloped wall portion.

3. Fluid flow apparatus as set forth in claim 2, the sloped wall means facing in the upstream direction extending at an angle in the order of at least about 390 to the plane defined by the periphery of said fluid displacement member and the sloped wall means facing in the downstream 0: direction extending at an angle in order of about 220 to said plane.

4. Fluid flow apparatus as set forth in any one of claims 1 to 3, wherein said supporting member is a smaller tubular conduit having a downstream end centered axially within said main conduit, such that the center lines of said main conduit, the downstream end of said smaller tubular conduit and the axis of symmetry of said fluid displacement member are substantially coaxial. 50

5. Fluid flow apparatus as set forth in claim 4, wherein said smaller ,e tubular conduit enters through and is secured to the wall of said main conduit upstream from said fluid displacement member and turns in the downstream direction of fluid flow through a bend to its said downstream end.

6. Apparatus as set forth in any one of claims 1 to 5, further comprising 35 sensor means positioned downstream of said region for sensing pressure fluctuations in said fluid resulting from the vortices shed from the periphery of said fluid displacement member, and processing means coupled to said sensor means for determining fluid flow through said conduit as a function of said pressure fluctuations. .r/148z 55r S **SS S f 14

7. Apparatus for measuring fluid flow comprising a main tubular conduit for conducting a fluid therethrough in a predetermined direction, a fluid displacement member mounted in said main conduit to deflect the fluid to flow through a region defined by the periphery of said fluid displacement member and the interior surface portion of said main conduit proximate said periphery, said fluid displacement member being effective to substantially linearize the velocity profile of said fluid in at least said region over a predetermined range of fluid flow rates through said main conduit, a smaller tubular conduit for diverting a portion of the fluid passing through said main conduit along an auxiliary flowpath having one end positioned upstream of said fluid displacement member and its opposite end positioned downstream of said region, and means connected with said auxiliary flowpath effective to measure fluid flow therethrough.

8. Apparatus as set forth in claim 7, wherein said fluid displacement member includes sloped wall means for deflecting the fluid to flow through said region.

9. Apparatus as set forth in claim 7 or 8, wherein said measuring means comprises totalizer means in said auxiliary flowpath for determining the total fluid flow therethrough.

10. Apparatus as set forth in claim 7 or 8, wherein said measuring means comprising rate-of-flow means in said auxiliary flowpath for determining the rate of fluid flow through.

11. Apparatus as set forth in claim 7 or 8, wherein said measuring means d a 5 comprises means for measuring the pressure differential across said region.

12. Apparatus as set forth in claim 7 or 8, wherein said measuring means comprises transducer means mounted across said auxiliary flowpath for measuring the pressure differential between the said ends of said auxiliary flowpath. 3.

13. Apparatus as set forth in claim 8, wherein said fluid displacement member Includes a first sloped wall portion on the side thereof facing upstream in the direction of fluid flow and a second sloped wall portion on the side thereof facing downstream in the direction of fluid flow,, said first I' r sloped wall portion being effective to linearize the velocity profile of the fluid in said region and said second sloped wall portion being effective to S optimize the return velocity of the fluid as it reassumes free stream conditions in said conduit downstream from said displacement member. 0

14. Apparatus as set forth in claim 13, wherein the outward extension of said first sloped wall portion is not less than the outward extension of gr/148z N 07r C-) said second sloped wall portion.

Apparatus as set forth in claim 14, wherein said sloped wall pcrtion facing in the upstream direction extends at an angle in the order of ac least about 390 to the plane defined by the periphery of said fluid displacement member and the sloped wall portion facing in the downstream direction extends at an angle in the order of about 220 to said plane.

16. Fluid flow apparatus comprising a main tubular conduit of uniform internal configuration for conducting a fluid therethrough in a predetermined direction, a smaller tubular conduit in said main conduit having a downstream end centered axially within said main conduit, such that the center lines of the main conduit and the downstream end of the smaller conduit are substan- tially coaxial, a fluid displacement member mounted on the downstream end of said smaller conduit within said main conduit such that the axis of symmetry of said fluid displacement member is substantially coaxial with the axes of said main conduit and the downstream end of said smaller conduit, said fluid displacement member being smaller than said main conduit and larger than the smaller conduit and being mounted in said main conduit substantially perpen- dicular to the direction of fluid flow through said main conduit, said fluid displacement member having sloped wall means facing in the upstream direction for deflecting the fluid to flow through a region defined by the periphery of said fluid displacement member and the interior surface portion of said main conduit proximate said periphery, said sloped wall means being effective to substantially linearize the velocity profile of said fluid in said region, said fluid displacement member having sloped wall means facing in the downstream direction effective to substantially optimize the return velocity of the fluid as it reassumes free stream conditions in said main conduit downstream of said displacement member, the sloped wall means facing in the upstream direction extending at an angle in the order of at least about 390 to 0 the plane defined by the periphery of said fluid displacement member and the *6 0 so o sloped wall means facing in the downstream direction extending at an angle in order of about 220 to said plane.

17. Fluid flow apparatus as set forth in claim 9, whereln said smaller *ee tubular conduit enters through and is secured to the wall of said main conduit upstream from said fluid displacement member and turns In the downstream S direction of fluid flow through a bend to its said donwstream end.

18. Fluid flow apparatus as set forth in claim 9, wherein said smaller tubular conduit extends through said displacement member for diverting a portion of the fluid passing through said main conduit along an auxiliary r./I 1 48z U, 16 flowpath having one end positioned upstream of said fluid displacement member and its opposite end positioned downstream of said region, and including means connected with said auxiliary flowpath for effectively measuring flow therethrough.

19. Apparatus as set forth in claim 9, further comprising sensor means positioned downstream of said region for sensing pressure fluctuations in said fluid resulting from the vortices shed from the periphery of said fluid displacement member, and processing means coupled to said sensor means for determining fluid flow through said conduit as a function of said pressure fluctuations.

Apparatus as hereinbefore particularly described with reference to what is shown in Fig. 1.

21. Apparatus as hereinbefore particularly described with reference to what is shown in Fig. 2.

22. Apparatus as hereinbefore particularly described with reference to what is shown in Figs. 4 and DATED this FIFTEENTH day of DECEMBER 1989 Ametek, Inc S a Patent Attorneys for the Applicant SPRUSON FERGUSON S* .5 33 S S S 0 gr/148z