• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    The invention relates to a system for measuring time-resolved flow processes of fluids with an inlet (12), an outlet (14) and a flow meter (10) arranged between the inlet (12) and the outlet (14). In order to be able to additionally provide further values for the chemical and physical states of the pumped fluid, it is proposed that a line section (18) of the flowmeter (10) can be bypassed via a bypass line (16), in which a pump (48) and a sensor (50) arranged in series for measuring a physical or chemical property of the delivered fluid.
    公开号:AT516622A4
    申请号:T168/2015
    申请日:2015-03-24
    公开日:2016-07-15
    发明作者:Heribert Kammerstetter；Christian Thomas Berger；Otfried Dipl Ing Derschmidt；Manfred Dipl Ing Pross (Fh)；Martin Dr Dürrwächter；Othmar Bernhard；Herwig Breitwieser
    申请人:Avl List Gmbh；
    IPC主号:
    专利说明:

    System for measuring time-resolved flow processes of fluids
    The invention relates to a system for measuring time-resolved flow processes of fluids having an inlet, an outlet and a flow meter arranged between the inlet and the outlet and a system for measuring time-resolved flow processes of fluids with an inlet, an outlet, via a main conduit is fluidly connected to the inlet, a driven displacer disposed in the main conduit, a bypass conduit branching from the main conduit between the inlet and the displacer and opening into the main conduit between the displacer and the outlet, a pressure differential receiver disposed in the bypass conduit and an evaluation and control unit, via which the drivable displacer can be regulated as a function of the pressure difference applied to the translatory pressure difference sensor.
    Such systems have been known for many years and are used, for example, for injection quantity measurement
    Internal combustion engines used.
    Thus, DE-AS 1 798 080 describes an electronically controlled flowmeter with an inlet and an outlet, between which a rotary displacer in the form of a gear pump and in a line parallel to the displacer a piston is arranged in a measuring chamber. To determine the flow rate, the deflection of the piston in the measuring chamber is measured by means of an optical sensor. The speed of the gear pump is continuously readjusted due to this signal via an evaluation and control unit in such a way that the piston is always returned to its original position, so that only small currents arise in the bypass line. From the number of revolutions or partial revolutions of the gear pump measured via an encoder as well as the known delivery volume of the gear pump in one revolution, the flow is calculated within a predetermined period of time,
    Such a constructed flow meter is also described in DE 103 31 228 B3. To determine the precise injection flow rates, the gear pump is set to a constant speed before the start of injection, so that subsequently the movement of the piston is measured and used to determine the injection curves. In addition, a pressure sensor and a temperature sensor are arranged in the measuring chamber, the measured values of which are likewise fed to the arithmetic unit for calculating and correcting the injection quantity profiles.
    However, it has turned out that the determination of the injection-gas flow courses continues to be subject to small errors, which are due to hitherto unnoticed fluctuations in the viscosity or the density of the measured fluid.
    It is therefore the object to provide a system for measuring time-resolved flow processes of fluids, with which the flow characteristics can be calculated even more accurately. In particular, this should be considered additional information regarding the respective physical properties of the fluid without affecting the actually measured with the flowmeter results negative, which would be to be feared if, for example, a
    Density sensor in the main line or the bypass line of the meter would be installed.
    This object is achieved by a system for measuring time-resolved flow processes of a fluid having the features of claim 1 or claim 2.
    Characterized in that a line section of the flowmeter is bypassed via a bypass line in which a pump and a sensor for measuring a physical or chemical property of the pumped fluid are arranged in series, for a flow meter, an additional physical quantity, such as the density or viscosity be taken into account in the determination of the flow of the measured fluid. For this purpose, a flow is ensured by the sensor by means of the pump. The arrangement in the bypass line prevents repercussions on the flowmeter.
    When using a system with a flow meter with a parallel to a displacer Druckdifferenzaufnehmer the object is achieved in that branches off from the main line or the bypass line of the flow meter, a bypass line and on the same side of the displacer and Druckdifferenzaufnehmers bypassing a line section of the main line or the bypass line opens, from which the bypass line is branched off, wherein in the bypass line, a pump and a sensor for measuring a physical or chemical property of the pumped fluid are arranged in series. Thus, regardless of a flow in the main line or the bypass line a flow in the bypass line is provided, the correct operation of the in the
    Bypass line arranged sensor ensures. Above all, sufficient flow through the sensor is ensured, which would have to be provided by external energy supply when installing the sensor in the main line or the bypass line, which would lead to a retroactive effect on the measured data of the flowmeter. In particular, density sensors require such a flow to provide correct readings. The values of the corresponding sensor can either serve only for evaluation or as an additional control variable. By using this system according to the invention even more accurate measurement results of such a flowmeter can be achieved.
    Preferably, the bypass line branches off from the bypass line between the inlet and the Druckdifferenzaufnehmer and empties there. This position is on the one hand very easily accessible, so that short connecting lines sufficient and on the other hand, an influence on the measurement is prevented, since the medium can be performed directly in a circle, without a flow is generated at the measuring chamber.
    In particular, it is advantageous if the sensor is a density sensor or a viscosity sensor, so that their measured values provide additional information which can be taken into account in the results of the flowmeter for improving the calculated flow. These sensors can be designed, for example, as MEMS sensors, which operate on the Coriolis principle.
    In a particularly preferred embodiment according to the invention, the pump is a pulsation-free pump. By a complete freedom from pulsation is an influence of the
    Druckdifferenzaufnehmers and thus the measurement results of the flowmeter completely excluded. In addition, erroneous measurements of the density sensors are avoided, which, in particular if they are designed as MEMS sensors, would be excited even by the vibrations of the measurement fluid to vibrate, which would falsify their measurement results.
    It is particularly advantageous if the pulsation-free pump is a Tesla pump. Teslapumpen promote a fluid without using blades, but only because of the existing viscosity of the fluid using the adhesion forces. For this purpose, a plurality of discs arranged side by side, between which the fluid is centrally introduced, are rotated by an electric motor, whereby the fluid is conveyed tangentially in the direction of rotation and radially outwards due to the viscosity and the adhesion with outwardly increasing speed. This leads to a pulsation-free promotion with good efficiencies. Such a pump can be made very compact and yet withstand the relatively high system pressure of the displacement meter of about 20 bar and temperatures of up to 150 ° C. In addition, such a pump operates without valves, so that the system remains open when the flowmeter is stopped. Since the manufacturing tolerances are low, such a pump is inexpensive h erstelIbar.
    In a further embodiment, the Tesla pump is arranged in the conveying direction of the fluid in the bypass line in front of the sensor, whereby air inclusions do not reach the pump during commissioning in the region of the sensor. Such air bubbles can from a Tesla pump due to low adhesion forces of the
    Medium are not promoted, otherwise the efficiency of the pump would be extremely reduced.
    Accordingly, it is advantageous if an inlet to a flow space of the Tesla pump, in which a rotor of the Tesla pump is arranged geodetically below the branch of the bypass line, since air from the region of the inlet rise in the direction of the bypass line and can be discharged from there , whereby the function of the Tesla pump is ensured.
    In a further advantageous embodiment of the invention, the bypass line section between the junction of the bypass line and the inlet to the flow chamber of the pump is continuously sloping towards the inlet of the pump, air bubbles in this bypass line section leading to the pump rise accordingly along the bypass line section in the direction the bypass line and can be reliably dissipated there, whereby the function of the pump is ensured.
    It has proven to be particularly advantageous if the inclination of the bypass line section between the branch and the inlet of the Tesla pump is between 9 ° and 12 °. As a result, an increase of air bubbles is ensured and it can be maintained at the same time a compact design.
    Preferably, an outlet of the Tesla pump is arranged geodetically above the flow space of the Tesla pump. Air bubbles arranged in the flow space during the initial startup rise correspondingly to the outlet and leave the outlet
    Flow space, so that a pump delivery is ensured when switching.
    In addition, it is advantageous if an outlet channel of the Tesla pump in the flow direction formed rising, whereby a return flow of the air bubbles from the outlet to the rotor is prevented.
    In order to provide a compact and well-sealed unit, the system has a solid body which is connected to the body in which the bypass line is formed and in which a flow space of the pump, the inlet of the pump, the outlet of Pump and a Bypassleitungsabsehnitt between the outlet of the pump and an inlet of the sensor and a bypass line section between the outlet of the sensor and the mouth are formed in the bypass line at least partially. The hydraulic line sections are all easy to make as thin holes in the solid body, additional flexible lines can be omitted.
    Preferably, the flow cross-section of the bypass line is smaller than the flow cross-section of the main line and the bypass line, in particular about 4 mm. This minimizes the effects on the flows in the bypass, while still providing a sufficient pressure difference to
    Density measurement is provided. Since there is theoretically no flow with optimum control of the displacer in the bypass line, a flow must be avoided by excessively high pressure differences relative to the flow cross section of the bypass line. This is achieved by the present bypass line without too high
    To generate pressure losses in the bypass line.
    Thus, a system is provided for measuring time-resolved fluid flow events that can be used to time resolved flow events with high accuracy and continuously. In this case, additional data are provided for controlling the system or for evaluating the measurement results, in particular with regard to the physical quantities density or viscosity of the fluid, without adversely affecting the actual measurement, for example, by pulsations occurring. The additional space required is very small. This is a high pressure and
    Temperature resistance of the used achieved,
    The system according to the invention for measuring temporally resolved flow processes of fluids is described below with reference to a non-limiting exemplary embodiment illustrated in the figures below.
    FIG. 1 shows a diagram of the basic structure of a system according to the invention for measuring time-resolved flow processes of fluids.
    Figure 2 shows a perspective view of a section of a test setup of the system according to the invention with partially cut bodies shown.
    The inventive system shown in Figure 1 for the measurement of temporally resolved flow processes of fluids consists of a flow meter 10 with an inlet 12 and an outlet 14 and a bypass line 16 through which a line section 18 of the flowmeter 10 can be bypassed. Via the inlet 12, a fluid to be measured, in particular a fuel, flows from a flow-generating device, in particular a high-pressure fuel pump, and at least one injection valve, into a main line 20 of the main flow meter 10. In this main line 20, a rotary displacer 22 in the form of a Double gear pump arranged. Downstream of the displacer 22, the main line 20 terminates at the outlet 14. The gear pump 22 is driven by a drive motor 24 via a clutch or a transmission.
    From the main line 20 branches off between the inlet 12 and the rotary displacer 22 from a bypass line 26 which opens downstream of the rotary displacer 22 between this and the outlet 14 back into the main line 20 and corresponding to the main line 20 fluidly with the inlet 12 and Outlet 14 is connected. In this bypass line 26, a translational Druckdifferenzaufnehmer 28 is arranged, which consists of a measuring chamber 30 and a freely displaceable in the measuring chamber 30 arranged piston 32 which has the same specific gravity as the measuring fluid, so the fuel and how the measuring chamber 30 is cylindrically shaped ; the measuring chamber 30 thus has an inner diameter which substantially corresponds to the outer diameter of the piston 32. When a pressure difference between the front and the back of the piston 32 concerns a deflection of the piston 32 takes place from its rest position. Accordingly, the deflection of the piston 32 is a measure of the applied pressure difference. At the measuring chamber 30, a displacement sensor 34 is arranged, which is in operative connection with the piston 32 and in which by the deflection of the piston 32 a dependent on the size of the deflection of the piston 32 voltage is generated. This at the
    Measuring chamber 30 fixed displacement sensor 34 is in particular a magnetoresistive sensor, via which the field strength of a magnet 36 acting on it is converted into a voltage. For this purpose, the magnet 36 is fixed in the center of gravity of the piston 32. As displacement sensors and light sensors can be used.
    The displacement sensor 34 is connected to an evaluation and control unit 38, which receives the values of this displacement sensor 34 and transmits corresponding control signals to the drive motor 24, which is possibly controlled such that the piston 32 is always in a defined starting position, ie the gear pump 22 the resulting due to the injected fluid at the piston 32 pressure difference is constantly compensated by promotion This means that upon deflection of the piston 32 to the right depending on the size of this deflection, the pump speed is increased and vice versa. For this purpose, the deflection of the piston 32 or the volume displaced by it in the measuring chamber 30 by means of a transfer function in a desired delivery volume of the gear pump 22 and a rotational speed of the drive motor 24 is converted and the drive motor 24 energized accordingly
    In the measuring chamber 30, a pressure sensor 40 and a temperature sensor 42 are arranged, which continuously measure the pressures and temperatures occurring in this area and in turn the evaluation and control unit 38 perform to account for changes in density in the calculation can.
    The sequence of the measurements is such that when calculating a total flow to be determined in the evaluation and
    Control unit 38 both in the bypass line 26 caused by the movement or position of the piston 32 and the displaced volume in the measuring chamber 30 flow as well as an actual flow of the gear pump 22 are taken into account in a fixed time interval and adds both flows together to determine the total flow become.
    The flow rate on the piston 32 is determined, for example, by differentiating in the evaluation and control unit 38, which is connected to the displacement sensor 34, the deflection of the piston 32 and subsequently multiplying it by the base area of the piston 32, so that a volumetric flow rate is obtained in the bypass line 26 in this time interval.
    The flow through the gear pump 22 and thus in the main line 20 can either be determined from the determined control data for controlling the gear pump 22 or calculated via the speed, if this directly on the gear pump 22 or on the drive motor 24, for example via optical encoder or magnetoresistive sensors is measured.
    According to the invention branches off in the present embodiment between the inlet 12 and the measuring chamber 30 from the bypass line 26 from the bypass line 16, which opens before the measuring chamber 30, bypassing the line section 18 again in the bypass line 26. It would also be possible to branch off this bypass line 16 at any other position of the main line 20 or the bypass line 26 and let it open again, wherein the bypass line 16 is not allowed to bypass the displacer 22 or the Druckdifferenzaufnehmer 28.
    Between the branch 44 and the mouth 46, a pulsation-free pump 48 in the form of a Tesla pump and a sensor 50 for measuring a chemical or physical property of the pumped fluid connected in series are arranged in series in the bypass line 16. This sensor 50 is in particular a density sensor or a viscosity sensor, which is designed, for example, as a Coriolis-type measuring MEMS sensor. The tesla pump 48 and the sensor 50 are both electrically connected to the evaluation and control unit 38, so that the measured values of the sensor 50 can be used in order to be able to improve the calculated flow values by the additional information on the density or viscosity and to control the Tesla pump 48 , This pump 48 is necessary to ensure a flow over the sensor 50, the readings of which could otherwise deviate from the actual values to be measured due to a flow stoppage. The pulsation-free promotion of the Tesla pump 48 also prevents the measured values of the sensor 50 from being falsified, since these sensors 50 also tend to pulsate during pulsating flows. Accordingly, the evaluation and control unit 38 are supplied with correct additional information which can be used both in the control of the displacer 22 and in the calculation of the flow rates, in order to additionally improve the results.
    The Tesla pump 48 consists essentially of an electric motor 52, which may be embodied, for example, as an electronically commutated DC motor and a rotor 54, which consists of a plurality of disks 56 which are arranged one behind the other but with small distances from each other in a flow space 58 of the Tesla 48 and over the electric motor 52 are driven. When current of the electric motor 52, the rotor 54 is rotated.
    In the figure 2 is based on a test setup in which a part of the bypass line 26 and in particular the line section 18 is simulated by a separate cylindrical line shown, as well as the real flow meter 10, the bypass line 16 and the pump 48 and the sensor 50 in the Bypass line 16 are connected to the here simulated bypass line 26. The Tesiapumpe 48 has a central inlet 60, via which the fluid can flow into the flow space 58 between the discs 56. For this purpose, the discs 56 in the inner region openings. Due to its viscosity, the rotation of the disks 56 accelerates the fluid in the tangential direction as well as radially outward between the disks 56. Accordingly, a flow of the fluid leaves the flow chamber 58 of the pump 48 via an outlet 62, which is arranged geodetically above the flow space 58. An outlet channel 64 extending from the outlet 62 runs tangentially to the flow space in order to avoid pressure losses. The fact that this pump 48 has no blades, creates a pulsation-free flow in the direction of the sensor 50. Furthermore, the flow characteristic of the Tesla pump 48 increases substantially linearly to the speed of the rotor 54, so that the pump 48 is easy to control.
    The flow cross section of the bypass line 26 of the flowmeter 10 is significantly larger than the cross section of the bypass line 16 whose diameter is for example about 4 mm, so that relatively small flow rates are required to produce a necessary pressure difference.
    The pulsation freedom of the pump 48 as well as these lower flow rates ensure that a retroactive effect on the control loop of the displacer 22 and the Druckdifferenzaufnehmers 28 due to undesirable flows or pulsations is virtually absent. Furthermore, this diameter has proven to be advantageous in order to remove air pockets, which arise in particular during initial commissioning.
    To prevent measurement errors due to air inclusions in the system, further measures are taken. A bypass line section 16.1, which leads from the branch 44 to the inlet 60 into the flow space 58 and thus to the rotor 54 of the pump 48, is inclined in the direction of the inlet 60 at an angle of approximately 11 °. This has the result that trapped air in this bypass line section 16.1 ascend to the bypass line 26 and can be discharged there, Also, the execution of the outlet channel 64 of the pump 48, which is arranged in the geodesic upper region and further upwards, leads to an upgrade of Air bubbles from the flow chamber 58 of the pump 48. Accordingly, the flow chamber 58 is filled at standstill of the pump 48 with fluid, whereby a promotion of the pump 48 is sjchergestellt in which would otherwise collect non-dischargeable air inside the rotor 54.
    The flow and wiring is performed such that first of the bypass line 26 at the junction 44, the first to the inlet 60 of the Tesla 48 leading bypass line section 16.1 branches at an angle of 11 ° down leading. This bypass line section 16, 1 is formed in a body 66 in which a portion of the bypass line 26 is also formed. At this body 66, a solid body 68 is fixed, in which the inlet 60 to the Tesla pump 48 and the
    In addition, branches from the flow chamber 58 in this solid body 68 of the outlet channel 64 of the pump 48 from. This opens into a further approximately horizontally extending bypass line section 16.2, which merges into a leading to the sensor 50 bypass line section 16.3 in the form of a connecting pipe, which is curved downward such that an inlet 70 is disposed geodetically below the sensor 50. A following bypass line section 16.4 leads approximately perpendicularly through the sensor to its outlet 72 arranged at the top. From the outlet 72 extends a bypass line section 16.5, which is initially formed by a curved tube 74, the connecting piece 76 of which is fixed geodetically below the flow space 58 on the solid body 68, and continues inside the solid body 68 as well as the body 66 to the mouth 46, which is arranged corresponding geodetically below the branch.
    It can be seen that the line section 18 of the bypass line 26 is bypassed by the bypass line 16, wherein when conveyed by the Tesla pump 48, a circulation flow over the line section 18 from the mouth 46 of the bypass line 16 to the junction 44 is formed, in particular, since in the ideal case Gear pump 22 a pressure difference across the piston 32 completely compensates, whereby in the bypass line 26 in the ideal case no flow occurs.
    A flow, which is generated by a rotation of the rotor 54 of the Tesla pump 48 in the bypass line 16, takes place correspondingly along these bypass line sections 16.1-16.5, the line section 18 and through the sensor 50, whose measured values are then transmitted to the evaluation and control unit , Thus, the flowmeter calculates temporally high-resolution flow processes with high accuracy and continuously, provided in comparison to known designs, additional data for controlling the system or for the evaluation of the measurement results, in particular with respect to the physical sizes density or viscosity of the fluid; become. In this case, both a sufficient flow to ensure the function of the density sensor is provided as well as repercussions on the flowmeter avoided because too large flow rates and occurring pulsations are excluded. The system is very compact and has a high pressure and temperature resistance of up to 20 bar and 150 ° C. In addition, provision was made for ensuring the function of the pump by removing disturbing air bubbles. The density sensor and the pump can be operated both continuously and at defined time intervals and pass on their data to the evaluation and control unit
    It should be understood that the invention is not limited to the embodiment described, but various modifications are possible within the scope of the main claim. In principle, other continuous flowmeters can be used or the bypass line can bypass the corresponding line section at another position of the flowmeter,
    权利要求:
    Claims (14)
    [1]
    A system for measuring time-resolved flow processes of fluids having an inlet (12), an outlet (14) and a flow meter (IQ) arranged between the inlet (12) and the outlet (14), characterized in that a line section ( 18) of the flowmeter (10) via a bypass line (16) is flowed around, in which a pump (48) and a sensor (50) for measuring a physical or chemical property of the pumped fluid are arranged in series.
    [2]
    2, system for measuring time-resolved flow processes of fluids having an inlet (12), an outlet (14), which is fluidically connected via a main line (20) to the inlet (12), a drivable arranged in the main line (20) Displacer (22), a bypass line (26), which branches off between the inlet (12) and the displacer (22) from the main line (20) and between the displacer (22) and the outlet (14) in the main line (20). opens, a Druckdifferenzaufnehmer (28) which is arranged in the bypass line (26), and an evaluation and control unit (38) via which the i drivable displacer (22) in dependence on the Druckdifferenzaufnehmer (28) applied pressure difference is adjustable characterized in that from the main line (20) or the bypass line (26) branches off a bypass line (16) and on the same side of the displacer (22) and the Druckdifferenzaufnehmers (28), bypassing a line section (18) of the main line (20) or the bypass line (26) opens, from which the bypass line (16) is branched off, wherein in the bypass line (16) comprises a pump (48) and a sensor (50) for measuring a physical or chemical Property of the pumped fluid are arranged in series.
    [3]
    3. A system for measuring time-resolved flow processes of fluids according to claim 2, characterized in that the bypass line (16) branches off from the bypass line (26) between the inlet (12) and the Druckdifferenzaufnehmer (28) and opens.
    [4]
    4. A system for measuring time-resolved flow processes of fluids according to any one of the preceding claims, characterized in that the sensor (50) is a density sensor or a viscosity sensor.
    [5]
    5. A system for measuring time-resolved flow processes of fluids according to claim 4, characterized in that the pump (48) is a pulsation-free pump.
    [6]
    6. A system for measuring time-resolved flow processes of fluids according to claim 5, characterized in that the puisationsfrei demanding pump (48) is a Tesla pump.
    [7]
    7. A system for measuring time-resolved flow processes of fluids according to claim 6, characterized in that the Tesla pump (48) is arranged in Förderriehtung in front of the sensor (50).
    [8]
    8. A system for measuring time-resolved flow processes of fluids according to one of the preceding claims, characterized in that an inlet (60) to a flow space (58) of the Tesla pump (48), in which a rotor (54) of the Tesla pump (48). is arranged geodetically below the branch (44) of the bypass line (16) is arranged.
    [9]
    A system for measuring time-resolved flow processes of fluids according to claim 8, characterized in that the bypass line section (16.1) between the branch (44) and the inlet (60) to the flow space (58) of the Tesla pump (48) steadily in the direction of Inlet (60) of the Tesla pump (48) is designed sloping.
    [10]
    10. A system for measuring time-resolved flow processes of fluids according to claim 9, characterized in that the inclination of the bypass line section (16.1) between the branch (44) and the inlet (60) of the Tesla pump (48) is between 9 ° and 12 ° ,
    [11]
    11. A system for measuring time-resolved flow processes of fluids according to one of claims 8 to 10, characterized in that an outlet (62) of the Tesla pump (48) geodetically above the flow space (58) of the Tesla pump (48) is arranged.
    [12]
    12. A system for measuring temporally resolved flow processes of fluids according to claim 11, characterized in that an outlet channel (64) of the Tesla pump (48) is formed rising in the conveying direction.
    [13]
    A fluid flow rate measurement system according to any one of claims 8 to 12, characterized in that the system comprises a solid body (68) provided with a body (66) in which the bypass (26) is formed. and in which a flow space (58) of the pump (48), the inlet (60) of the pump (48), the outlet channel (64) of the pump (48) and a bypass line section (16.2) between the outlet channel (64) Pump (48) and an inlet (70) of the sensor (50) and a bypass line portion (16,5) between the outlet (72) of the sensor (50) and the mouth (46) in the bypass line (26) are at least partially formed .
    [14]
    14. A system for measuring time-resolved flow processes of fluids according to one of claims 2 to 13, characterized in that the flow cross-section of the bypass line (16) is smaller than the flow cross-section of the main line (20) and the bypass line (26).
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    同族专利:
    公开号 | 公开日
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    US20160281708A1|2016-09-29|
    CN106092216B|2021-04-20|
    JP2016180756A|2016-10-13|
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    KR20160114528A|2016-10-05|
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    ATA168/2015A|AT516622B1|2015-03-24|2015-03-24|System for measuring time-resolved flow processes of fluids|ATA168/2015A| AT516622B1|2015-03-24|2015-03-24|System for measuring time-resolved flow processes of fluids|
    EP16161104.1A| EP3073228B1|2015-03-24|2016-03-18|System for measuring time-resolved flow processes of fluids|
    US15/075,207| US10094378B2|2015-03-24|2016-03-21|System for measuring temporally resolved through-flow processes of fluids|
    KR1020160034496A| KR20160114528A|2015-03-24|2016-03-23|System for measuring temporally resolved through-flow processes of fluids|
    JP2016060619A| JP6695184B2|2015-03-24|2016-03-24|System for time-resolved measurement of fluid flow processes|
    CN201610363987.2A| CN106092216B|2015-03-24|2016-03-24|System for measuring a time-resolved flow process of a fluid|
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