FLOW METER DEVICE ACCORDING TO THE VORTEX MEASURING PRINCIPLE, MEASURING TUBE FOR SAME, AND METHOD FOR MEASURING THE FLOW RATE OR THE FLOW SPEED OF A MEDIUM

Abstract

The invention relates to: a measuring tube (10) for guiding a fluid for a flow meter device (1) according to the vortex measuring principle, wherein the measuring tube has an inflow-side opening in an inflow-side end face and an outflow-side opening in an outflow-side end face, between which the measuring tube extends in the axial direction; a bluff body (15) which is arranged in the measuring tube (10), wherein the bluff body functions to bring about a Krmn vortex street with a flow-rate-dependent vortex frequency when a fluid flows through the measuring tube; and at least one vortex detector (16) for detecting vortexes of the vortex street and for providing vortex-dependent signals; characterized in that the measuring tube (10) has a control valve (14), between the vortex detector (16) and the outflow-side end face and axially spaced apart from the vortex detector, which annularly constricts the flow cross-section of the measuring tube (10).

Claims

1. Measuring tube (10; 110; 210) for guiding a fluid, for a flow meter device (1; 100; 200) according to the vortex measuring principle, wherein the measuring tube has an inflow-side opening in an inflow-side end face and an outflow-side opening in an outflow-side end face, between which the measuring tube extends in the axial direction; a bluff body (15; 115; 215) which is arranged in the measuring tube (10; 110; 210), wherein the bluff body functions to bring about a Krmn vortex street with a flow-rate-dependent vortex frequency when a fluid flows through the measuring tube; at least one vortex detector (16; 116, 117; 216, 217) for detecting vortexes of the vortex street and for providing vortex-dependent signals; characterized in that the measuring tube (10; 110; 210) has a control valve (14; 114; 214), between the vortex detector (16; 116, 117; 216, 217) and the outflow-side end face and axially spaced apart from the vortex detector, which annularly constricts the flow cross-section of the measuring tube (10; 110; 210).

2. Measuring tube (10) according to claim 1, wherein the control valve has a flow resistance which is not less than 50%, for example not less than 75%, further for example less than 90%, especially, not less than 95%, of the flow resistance of the measuring tube between the inflow-side end face and the vortex detector.

3. Measuring tube (10) according to claim 1 or 2, wherein the control valve (14) has a minimum flow cross-sectional area which is not more than one and a half times, for example not more than one and one-fourth times and, especially, not more than one and one-tenth times the minimum flow cross-sectional area in the region of the bluff body.

4. Measuring tube (10) according to claim 1, 2, or 3, wherein the measuring tube has a first diameter (d1) between the vortex detector and the control valve at a first axial position, wherein at a second axial position, the control valve has a second diameter (d2) which is smaller than the first diameter by at least one tenth, wherein a quotient formed from the difference between the first diameter and the second diameter on the one hand and the difference between the first axial position and the second axial position is not less than two, for example is not less than four and, especially, is not less than eight, wherein the diameter transition is, especially, abrupt.

5. Measuring tube (10) according to any one of the preceding claims, wherein the control valve (14) is axially spaced apart from the vortex detector (16), wherein the the axial distance is, for example, not less than half the diameter (d1) of the measuring tube between the vortex detector and the control valve, especially, not less than one diameter (d1).

6. Flow meter device (100) according to the vortex measuring principle, comprising: a measuring tube (10) according to any one of the preceding claims, and an evaluation unit which is configured to determine a vortex frequency on the basis of the signals of the vortex detector and a flow rate measurement value as a function of the vortex frequency.

7. Method for measuring the flow rate or the flow speed of a medium with a flow meter device (1; 101) according to the vortex measuring principle, which flow meter device comprises: a measuring tube (10) for guiding a fluid, wherein the measuring tube has an inflow-side opening in an inflow-side end face and an outflow-side opening in an outflow-side end face, between which the measuring tube extends in the axial direction; a bluff body (15) which is arranged in the measuring tube (10), wherein the bluff body functions to bring about a Krmn vortex street with a flow-rate-dependent vortex frequency when a fluid flows through the measuring tube; at least one vortex detector (16) for detecting vortexes of the vortex street and for providing vortex-dependent signals; an operating and evaluation circuit which is configured to determine a vortex frequency on the basis of the signals and a flow rate measurement value as a function of the vortex frequency; wherein the flow meter device has a control valve, between the vortex detector and the outflow-side end face of the flow meter device, which annularly constricts the flow cross section of the measuring tube; wherein a difference between the static pressure at the inflow-side end face and the static pressure at an axial position halfway between the bluff body and the control valve is not more than two thirds, especially, not more than half the difference between the static pressure at the inflow-side end face and the static pressure downstream of the control valve at the outflow-side end face.

8. Method according to claim 7, wherein the medium has a vapor pressure, wherein the the static pressure at the axial position halfway between the bluff body and the control valve is not less than one and a half times the vapor pressure of the medium.

9. Method according to claim 7 or 8, wherein the difference between the static pressure at the inflow-side end face and the static pressure at the outflow-side end face is not less than 20% of the static pressure at the outflow-side end face.

Description

[0017] The invention will now be explained on the basis of the exemplary embodiments shown in the drawings. Shown are:

[0018] FIG. 1: a schematic longitudinal view through a first exemplary embodiment of a flow meter device according to the invention in a top view;

[0019] FIG. 2: a schematic longitudinal view through a second exemplary embodiment of a flow meter device according to the invention in a side view; and

[0020] FIG. 3: a schematic longitudinal view through a third exemplary embodiment of a flow meter device according to the invention.

[0021] The first exemplary embodiment of a flow meter device 1 according to the invention shown in FIG. 1 comprises a measuring tube 10 which has a first flange 11 on the inflow side and a second flange 12 on the outflow side for installation in a pipeline. The measuring tube 10 has on the inflow side a first cylindrical section 13 with a first inner diameter d1 and a on the outflow side a second cylindrical section 14 with a second inner diameter d2, wherein the transition between the first cylindrical section and the second section is designed as a radial step or radial jump. The flow meter device 1 furthermore has a bluff body 15 which is arranged in the first cylindrical section 13 and extends through the measuring tube perpendicularly to the longitudinal axis of the measuring tube 10 in order to generate a Krmn vortex street an a medium flowing through the measuring tube 10. In the flow direction below the bluff body 15, the flow meter device 1 has a vortex detector in the form of a sensor vane 16 which projects from the measuring tube wall into the measuring tube. The bluff body 15 and the sensor vane 16 are mirror-symmetrical with respect to a common measuring tube longitudinal plane in which the measuring tube longitudinal axis runs. The sensor vane 16 is mounted, for example, in a membrane, and deflections of the sensor vane caused by the vortexes are detected, for example, by means of (piezo)resistive or piezoelectric sensors or capacitive sensors (not shown here), especially, with a differential capacitor, wherein their signals are processed by an evaluation unit in order to ascertain a flow-rate-dependent vortex frequency and to calculate a flow rate value. Suitable holders for the sensor vane and signal evaluations are described, for example, in published patent applications DE10 2013 013 476 A1, DE 10 2013 105 363 A1, and WO 1998 031 988 A1.

[0022] The aforementioned reduction of the diameter between the first cylindrical section 13 and the second cylindrical section 14 achieves a throttling effect which, in a flowing medium, causes the static pressure in the first cylindrical section 13 in the region of the sensor vane 16 to be kept at a higher level than the static pressure in a pipeline which is connected to the measuring tube on the outflow side and has the diameter of the first pipeline section. In this way, the static pressure in the region of the sensor vane 16 can still be kept at a higher level, especially, above the vapor pressure of a component of a medium flowing in the pipe, despite a pressure drop at the bluff body 15 caused by the measuring principle. In this way, the outgassing of the component or cavitation is prevented, as a result of which a measurement continues to be possible and damage to the flow meter device 1 is avoided, even though the vapor pressure would be undershot, for example, in a pipeline connected to the measuring tube 10 on the outflow side with the first diameter or the diameter of an inflow-side pipeline. The diameter jump between the first cylindrical section and the second cylindrical section can be designed relative to the bluff body 15 such that a difference between the static pressure at the inflow-side end face and the static pressure at an axial position halfway between the bluff body 15 and the control valve 14 is not more than two thirds, especially, not more than half the difference between the static pressure at the inflow-side end face and the static pressure at the outflow-side end face downstream of the control valve when a pipeline with the first diameter is connected there again.

[0023] The second exemplary embodiment of a flow meter device 100 according to the invention shown in FIG. 2 comprises a measuring tube 110 with a first flange 111 on the inflow side and a second flange 112 on the outflow side for installation in a pipeline. The measuring tube 110 has a central first cylindrical section 113 having a first inner diameter and a second cylindrical section 114 on the outflow side having a second inner diameter, wherein the transition between the first cylindrical section and the second section is designed as a radial step or radial jump. On the inflow side, a conical section 118 is also connected upstream of the first cylindrical section 113 and reduces the diameter of the measuring tube continuously from a diameter of a pipeline connected on the inflow side to the diameter of the first cylindrical section 113 in order to increase the flow speed of a medium. This reduction in diameter should take place with as little energy loss as possible for the flowing medium. The flow meter device 100 furthermore has a bluff body 115 which is arranged in the first cylindrical section 113 and which extends through the measuring tube perpendicularly to the longitudinal axis of the measuring tube 110 in order to generate a Krmn vortex street an a medium flowing through the measuring tube 110. The measuring tube 110 has two wall regions which are thinned in a membrane-like manner and function as membranes of pressure sensors 116, 117 with electrical transducers, wherein the membranes are influenced differently by the Krmn vortex street. The pressure sensors 116, 117 together form a vortex detector, wherein a fluctuation of the difference between their sensor signals is evaluated by an operating and evaluation circuit 120 in order to determine a vortex frequency and thus the flow rate.

[0024] The aforementioned reduction of the diameter between the first cylindrical section 113 and the second cylindrical section 114 achieves a throttling effect which, in a flowing medium, causes the static pressure in the first cylindrical section 113 in the region of the membranes of the pressure sensors 116, 117 to be kept at a higher level than the static pressure in a pipeline which is connected to the measuring tube on the outflow side and has the diameter of the measuring tube on the inflow-side end face. In this way, the static pressure in the region of the membranes of the pressure sensors 116, 117 can still be kept, for example, above the vapor pressure of a component of a medium flowing in the pipe, despite a pressure drop at the bluff body 15 caused by the measuring principle.

[0025] The third exemplary embodiment of a flow meter device 200 according to the invention shown in FIG. 3 comprises a measuring tube 210 which a first flange 211 on the inflow side and a second flange 212 on the outflow side for installation in a pipeline. The measuring tube 210 has a central cylindrical section 213 having a first inner diameter. On the inflow side, a conical section 218 is connected upstream of the cylindrical section 213 and reduces the diameter of the measuring tube continuously from a diameter of a pipeline connected on the inflow side to the diameter of the first cylindrical section 213 in order to increase the speed of the flowing medium. On the outflow side, a conical section 219 is also connected downstream of the cylindrical section 213 and continuously increases the diameter of the measuring tube 210 in the direction of the outflow-side end face, wherein the measuring tube 210 has an annular disk-shaped control valve 214 on the outflow-side end face, the inner diameter of which control valve is abruptly reduced relative to the adjacent diameter of the conical section, especially, to the diameter of the central cylindrical section 213.

[0026] The flow meter device 200 furthermore has a bluff body 215 which is arranged in the first cylindrical section 213 and extends through the measuring tube perpendicularly to the longitudinal axis of the measuring tube 210 in order to generate a Krmn vortex street an a medium flowing through the measuring tube 210. The measuring tube 210 has two wall regions which are thinned in a membrane-like manner and function as membranes of pressure sensors 216, 217 with electrical transducers, wherein the membranes are influenced differently by the Krmn vortex street. The pressure sensors 216, 217 together form a vortex detector, wherein a fluctuation of the difference between their sensor signals is evaluated by an operating and evaluation circuit 120 in order to determine a vortex frequency and thus the flow rate.

[0027] The diameter jump at the annular disk-shaped control valve 214 has the effect that, in a flowing medium, the static pressure in the central cylindrical section 213 in the region of the membranes of the pressure sensors is kept at a higher level than the static pressure in a pipeline which is connected to the measuring tube on the outflow side and has the diameter on the inflow-side end face. In this way, the static pressure at the location of the pressure sensors can still be kept at a higher level, especially, above the vapor pressure of a component of a medium flowing in the pipe, despite a pressure drop at the bluff body 215 caused by the measuring principle.