Device for measuring the flow velocity of a fluid, System integrating at least one electrochemical probe and the measuring device Application to monitoring in bioproduction.

Abstract

Device for measuring the flow velocity of a fluid, System integrating at least one electrochemical probe and the measuring device, in particular at the free end of a pole, Application to monitoring in bioproduction. The invention relates to a device (1) for measuring the flow velocity of a non-gaseous fluid, in particular contained in a container, such as a tank, particularly one with opaque walls, comprising: - a tube (2) with longitudinal axis X; - an element (3) mounted for rotation around the tube and comprising at least one wall with a plurality of open holes (31 to 39) shaped such that the peripheral surface (300) of each hole is formed so that a flow of the fluid over the wall causes an asymmetry of the bearing forces on each peripheral surface of the hole and thus sets the element in rotation around the axis X; - a rotary encoder (5) adapted to measure the rotation of the element and thereby the flow velocity of the fluid.Figure for the abridged version: Fig.1.

Description

Title of the invention: Device for measuring the flow velocity of a fluid, System integrating at least one electrochemical probe and the measuring device Application to monitoring in bioproduction. technical field

[0001] The present invention relates to the field of speed measurement instrumentation, more particularly dedicated to knowledge of the state of a fluid.

[0002] It aims in particular to provide a reliable, precise and rapid solution for measuring the velocity of a fluid within a bioreactor.

[0003] Although described with reference to this measurement application, the invention can be considered for any application involving the measurement of the state of a fluid (liquid, gas) within a container such as a tank, particularly one with opaque walls, where the conditions of use cause the fluid to move globally or locally. For example, this could be a production or settling tank.

[0004] In the case of a fluid stirred within the tank, the invention can be used to optimize the efficiency of the stirring, in particular to adapt the speed, height and / or type of stirring turbine. Previous technique

[0005] Stirred tank reactors, like bioreactors, are widely used in many areas of the chemical industry.

[0006] In the field of bioproduction, the manufacture within bioreactors of biological products, which are living substances (vaccines, microalgae, biological pharmacological molecules, etc.) cannot be carried out by a completely pre-established protocol.

[0007] Indeed, it requires a permanent adaptation to adjust the physical parameters of the fluid, such as its viscosity, its mixing speed, its temperature, as well as its content of bubbles, gas, nutrients, etc... from imperfect measured parameters, which consist of indirect biochemical measurements, such as pH, and / or valid only locally and / or incomplete, etc....

[0008] The study of fluid flow in a bioreactor is essential in order to provide key information for choosing the best adaptation to be made in real time. In particular, viscosity and, by correlation, the Reynolds number, which defines the nature of a flow based on its velocity and also the viscosity of the flowing medium, is a parameter that must be known.

[0009] When reactor vessels have transparent walls, the flow velocity of a fluid can be measured by means of measurement by indirect observation carried out from outside. For velocity measurement, there can mainly be two optical methods, namely laser Doppler anemometry (LDA for "Laser Doppler Anemometry") and particle imaging velocimetry (PIV for "Particle Imaging Velocimetry").

[0010] Ideally, CFD (Computational Fluid Dynamics) numerical simulations should be compared with these experimental flow field data.

[0011] However, many bioreactors have opaque-walled tanks to prevent light penetration or for reasons of equipment cost or robustness. In the case of an opaque fluid, such as kerosene, the droplets are not transparent and strongly scatter light. This therefore effectively rules out the aforementioned indirect measurement methods.

[0012] Furthermore, it is generally impossible or prohibited to use in bioreactors measuring capsules that move freely with the permanent or intermittent movements of the fluid.

[0013] There is therefore a need to find a reliable and accurate measurement solution for the state of the flow velocity of a non-gaseous fluid, within a bioreactor, in particular one with opaque walls.

[0014] More generally, there is a need to find a reliable, accurate, and rapid measurement solution for the flow of a non-gaseous fluid, whether moving or not, within a volume, in particular a tank of any kind, especially a settling or production tank.

[0015] Another problem arises in bioreactors, and more generally in mixed media, which are equipped with electrochemical probes, particularly in the form of electrochemical sensors that operate primarily by voltammetry, i.e., by voltammetric and / or amperometric methods, possibly combined with other methods exploiting impedance or other electrochemical properties, to measure various parameters. Indeed, the stability of the measurement performed by these probes can be disrupted by changes in the nature of the fluid flow, which induces slow drifts that are not representative of electrochemical phenomena.

[0016] In addition, these probes can become fouled if the flow of the fluid reaching them is not sufficiently turbulent or if a layer appears covering them, also resulting in a disturbance of the measurement performed.

[0017] There is therefore also a need to find a solution to guarantee the measurement stability of electrochemical probes immersed in a non-gaseous fluid in movement or not within a volume, in particular of a tank, whatever its type, especially for decantation or production.

[0018] The object of the invention is to meet, at least in part, this need(s). Description of the invention

[0019] To this end, the invention relates to a device for measuring the flow velocity of a non-gaseous fluid, in particular contained in a container, such as a tank, especially one with opaque walls, comprising: - a tube with longitudinal axis X; - an element mounted to rotate around the tube and comprising at least one wall with a plurality of through holes made in such a way that the peripheral surface of each hole is shaped so that a flow of fluid on the wall causes an asymmetry of the support forces on each peripheral surface of the hole and thus sets the element in rotation around the X axis; - a rotary encoder adapted to measure the rotation of the element and thereby the flow velocity of the fluid.

[0020] According to an advantageous embodiment, the wall of the element is at least partly cylindrical, the holes being formed in the thickness of the cylindrical wall, each with an axis that does not intersect the axis of the cylinder of the wall. The holes are thus teardrop-shaped because their contour results from the intersection of two cylinders whose axes do not intersect.

[0021] The holes may be distributed uniformly or not on the periphery.

[0022] Advantageously, the holes are distributed in rows, preferably three or six in number, parallel to the X axis, preferably distributed uniformly angularly around the X axis, in order to improve the regularity of the rotation of the element.

[0023] Advantageously, the holes are of different diameters so as to broaden the Reynolds number range that characterizes the fluid and is capable of producing the rotation. Indeed, holes of different dimensions make it possible to adapt the rotation of the device to different ranges of fluid viscosity or turbulence effects.

[0024] The element may comprise a plurality of protrusions arranged on the external and / or internal face of the element, each adapted to create a fluid support surface, advantageously in addition to the support surfaces formed by the periphery of the holes in the wall of the element, or replacing them if the fluid is gaseous. These protrusions constitute a support surface that can be combined with the peripheral surfaces, which are the primary support surfaces. This allows for increased rotation efficiency, when the balance of added friction remains favorable.

[0025] The element is advantageously mounted for rotation around the tube by at least one bearing or ball bearing or ball cage.

[0026] According to an advantageous embodiment, the rotary encoder, also known as an electrochemical tachometer, comprises:

[0027] - an electrochemical sensor, fixed to the free end of the tube inside of the element, comprising at least one pair of electrodes, including a so-called working electrode to which an applied electrical potential (equivalent voltage or current) can be varied as a function of time and a so-called auxiliary electrode in which the electrical signal which flows, as well as in the working electrode, is measured as a function of the electrical potential;

[0028] - an electrical or hydraulic means fixed to or made entirely in the element, adapted to disrupt the electrical signal measured by the at least one pair of electrodes, so as to be able to count each complete turn, made by the element around the tube.

[0029] In other words, according to this mode the rotary encoder has a dual function, i.e. both a tachometer and an electrochemical sensor. Put another way, it can be described as an electrochemical tachometer.

[0030] The electrical means may be a rod or wire electrically conductive or made of ferromagnetic material fixed or made entirely over the height of the rotating element so as to produce an electric field or a capacitive or inductive or electromagnetic reaction detectable in the current measurement which is essentially resistive provided that this electrical component does not permanently disturb the electrochemical measurements.

[0031] By "electrochemical measurement" ("voltamperometry" or "voltammetry" or "impedance"), we mean here and within the framework of the invention an electroanalytical method based on the measurement of the electric current flow or electric potential resulting from the reduction or oxidation of the test compounds present in solution under the effect of a controlled variation of the potential difference between two specific electrodes ("voltamperometry"), or of the reduction or oxidation of the electrodes under the effect of the compounds present in solution ("voltammetry"), or of the variation of the electrical conductivity of the medium as a function of the compounds present in solution ("impedance").

[0032] The hydraulic means can be a protrusion or asperity arranged on the inner face of the element. Such a hydraulic means makes it possible to produce a vortex or the beginning of a vortex in the fluid, which will only be detected in an electrochemical measurement under specific conditions. The nature and shape of the disturbance The measured hydraulic or electrical force must be sufficient to allow for detection and recognition with a temporal accuracy that, while low, is adequate for counting. The average time elapsed between a sufficiently cumulative number of counts provides an estimate of the rotational speed of the rotating element and, consequently, the flow velocity of the fluid acting on the peripheral surfaces of the through holes, causing it to rotate through sufficiently increased tangential forces. Advantageously, the effect of a radial force is sufficiently minimized or made asymmetrical by an optimized ratio between the perforated surfaces (through holes) and the total surface area of ​​the element before perforation.

[0033] Advantageously, regardless of the presence of an electrical or hydraulic means intended to improve the temporal accuracy of the detection of each complete revolution, the precise shape of the disturbance induced by the rotating holed element is measured by a suitable configuration of the electrochemical tachometer, and in this case the observed fluctuations provide information on the turbulence of the fluid around the element, which results in rapid fluctuations of the electrical signal superimposed on the slower fluctuation rhythmic with the complete revolutions, both of which can be perceived by the detection electrode.

[0034] The invention also relates to an electrochemical measurement system and flow rate measurement system for a non-gaseous fluid, in particular contained in a container, such as a tank, especially one with opaque walls comprising: - a measuring pole forming the tube, one free end of which is intended to be immersed in the fluid; - at least one electrochemical probe, attached to the free end of the measuring pole, and adapted to measure electrochemical properties of the fluid; - a measuring device as described above, the element of which is mounted to rotate around the electrochemical probe which also acts as the rotary encoder (rev counter).

[0035] For the purposes of this invention, the term "electrochemical probe" refers to a device comprising at least one electrochemical sensor capable of converting one or more chemical quantities, such as concentration, pH, or electrochemical activity, into electrical output quantities with variable sensitivity depending on the channel and equipped with calibration relationships. This device may be single-electrode or multi-electrode and may be implemented on a PCB (Printed Card Board) or any equivalent integrated sensor. The probe may include a thin-walled, fragile capsule, e.g., made of glass, or a bare or functionalized surface in direct contact with the fluid.

[0036] Advantageously, the electrochemical sensor of the device is that of the electrochemical probe.

[0037] The invention also relates to a method of operating the measurement system as described above, comprising the steps of:

[0038] i / to carry out electrochemical measurements using the electrochemical probe for monitoring the electrochemical properties of the fluid;

[0039] ii / during or after step i / , apply electrical potential stimuli to the working electrode, located outside the useful areas of the current density characteristic curve as a function of the probe potential, and detect the measurement of current, potential or impedance perturbed by electrical or hydraulic means of the rotary encoder during the application of the potential stimuli, and deduce the measurement of fluid flow velocity.

[0040] The invention further relates to a settling, purification, or production medium or tank, particularly for a bioreactor, comprising a measuring device as described above or a system as described above. A tank can be any type of container, reservoir, bioreactor, vessel, or boiler containing a fluid. A bioreactor includes a tank used for the manufacture of drugs, pharmaceuticals, antibodies, vaccines, or other products that can be described as living.

[0041] The invention finally relates to the use of a measuring device as described above or a system as described above for monitoring bioproduction and / or for providing reference data in a digital twin.

[0042] A tank can be equipped with one or more tubes, for example, to implement means for mixing the fluid, or a means for introducing nutrients or a gas, or for any other function. Generally, the poles are fixed, but some can be mobile, rotating or translating, and driven by motors. A pole can be equipped with one or more measuring probes, including a probe capable of performing electrochemical measurements.

[0043] The invention proposes to use any one of these types of poles to carry out the measurements according to the invention, referred to for this purpose as a measuring pole.

[0044] A measuring pole can consist of a solid tube or hollow tube at least partially immersed in a fluid to be analyzed, and can be fixed or mobile in translation and / or rotation.

[0045] More generally, the invention can be implemented in certain agri-food productions and / or for applications where protection and performance improvement of already installed electrochemical probes are sought, in particular fixed probes immersed in tanks inside which the fluidic medium is likely to have adverse effects either by its Flow properties can be affected, either by fouling ("biofouling") or by the appearance of a biofilm or surface layer that impairs the quality of measurements. These can be fish farm ponds or so-called natural ponds.

[0046] The invention can also be implemented in fluidic media that are currently uninstrumented or under-instrumented due to their nature, such as excessive turbidity, significant eddies or turbulence, or excessively rapid deposition of a layer unsuitable for electrochemical measurement. These may include settling tanks, particularly for wastewater, and micro-wastewater treatment plants for private individuals.

[0047] The invention therefore essentially consists of a measuring device which can be likened to an anemometer for a non-gaseous fluid, the peripheral surface of which, mounted in rotation, is made asymmetrical by through-holes, allowing the fluid flow to produce an asymmetrical thrust which makes the element rotate and thus, thanks to the rotary encoder, to know the flow speed of the fluid.

[0048] The perforated peripheral wall of the rotating element creates sufficiently large and asymmetrical bearing surfaces to produce a torque around the axis of the tube.

[0049] In other words, the rotating element of the measuring device can be likened to a paddle wheel, with passive rotation, fully immersed in the non-gaseous fluid medium. Its bearing surfaces, defined by the perforated peripheral wall, are very compact and contained within the thickness of the element to accommodate rotation in a non-gaseous fluid. Unlike a conventional anemometer, the bearing surfaces are not convex like those of cups but are formed by the peripheral surfaces created by the perforations in the wall. The ratio of the peripheral surface area to the total surface area of ​​the rotating element is advantageously maximized to facilitate rotation by minimizing friction and to minimize the flow disturbance introduced by the presence of the rotating element. Care is, of course, taken to maintain the mechanical rigidity of the rotating element.

[0050] An advantageous variant for creating larger peripheral surfaces that are asymmetrical from the point of view of fluid flow around the drilled element is to produce the holes, either by machining or by additive manufacturing, in a perforation direction that is not directed towards the axis of symmetry of the rotating element. This promotes the accumulation of tangential forces produced by the portion of fluid flowing on one side or the other of the cylindrical surface of the rotating element, causing it to move at the fluid velocity by generating a rotational torque. The term "bearing surface" refers to the cumulative sum of all the peripheral surfaces of the drilled holes that contribute to the rotational torque. The effective bearing surface is derived from the slightly corrected geometric bearing surface of a The coefficient depends on the fluid flow conditions and can be calibrated. The diameter of the rotating element is chosen to maximize the rotational torque according to principles known to those skilled in the art. The fluid's ability to pass through the openings increases the forces exerted on the bearing surface. In turbulent flow, more numerous and smaller holes are preferable in order to sum the useful contributions and minimize the forces produced by internal turbulence orientations that are not aligned with the overall flow direction and therefore do not contribute to the rotational torque.

[0051] In fact, to minimize the equilibrium of the two supports, which are radial and antagonistic in nature, created by the flow splitting in two around the rotating element, rows of open holes are preferably created within it. In certain specific cases, a break in the symmetry of the element may suffice to generate a rotational moment corresponding to a small tangential force produced from the imbalance between the radial forces, and to obtain a slight rotation that can sometimes be regular or even stable.

[0052] But for the operation of the device to be guaranteed, more particularly in many usage configurations and fluids and Reynolds number ranges, correlated with viscosity, it is necessary to partition the liquid into two contributions around the rotation element so that the liquid enters holes that are both well organized and well made such that the summation of the fluid forces on the peripheral surfaces of the holes is tangential in nature and maximized to increase the rotational torque in the chosen direction and minimize it in the other direction.

[0053] For this reason, according to this advantageous variant, the axes of the holes do not intersect with the longitudinal axis X of the tube. Indeed, with the axes of the holes intersecting the X axis, the resulting rotational torque is less optimized, with a resultant rotation that could be irregular or, in certain turbulent fluid situations, could randomly switch from one direction of rotation to the other.

[0054] Therefore, the wall thickness of the rotating element and the number, size, drilling angle, and distribution of the plurality of holes are parameters to be precisely adjusted.

[0055] Advantageously, the element forms a protective ring for an electrochemical probe, thus providing a combined measurement system for the flow velocity of a fluid and for understanding its chemical properties.

[0056] By integrating the rotating element of the velocity flow measurement device around an electrochemical probe, the adverse effects related to the slow evolution of the flow nature are further minimized, such as highly localized microcirculations of fluid around the probe, which can generate slow drifts of The probe's measurements are not representative of electrochemical phenomena. While not limited in generality, this advantage is particularly relevant to very slow flow conditions or the effects of permanent drag induced by the probe's presence in a slow or very low-turbulence flow. Furthermore, the perforated rotating element not only facilitates the renewal of contact between the electrochemical probe and the non-gaseous fluid medium in which it is immersed, but also ensures a flow regime conducive to improving the stability of the measurement performed by the electrochemical probe.

[0057] The peripheral surface of the rotating element of the measuring device can advantageously be structured, in particular by means of grooves and / or asperities, or functionalized, in particular by a hydrophilic or hydrophobic coating to improve the operation of the device, according to methods known to those skilled in the art. This makes it possible to obtain a more linear variation of the speed of the rotating element according to the different flow regimes characterized by the Reynolds number or a more effective uniformization of the fluidic flow in contact with the electrochemical probe.

[0058] An advantageous embodiment of the invention consists of using the electrochemical probe sensor and taking advantage of its operation in volt-amperometric cycling to implement the rotary encoder (electrochemical tachometer).

[0059] Indeed, according to this mode, the operation consists of using instants within a repetitive cycling protocol of the probe to insert dedicated conditions for the rotary encoder function, i.e., electrical potential stimuli, without disturbing the primary function of cyclic voltammetry measurement of the electrochemical probe. These electrical potential stimuli are inserted outside the (temporal) segments that provide the characteristic points and slopes of the so-called "duck" curve of current density versus potential.Depending on the fluid medium and the conditions used to achieve fluid flow, these electrical potential stimuli are activated at each repetition by means of signal perturbation in the rotating element, either within an acquisition cycle or only after a canard curve acquisition and before restarting the next acquisition, in order to avoid disturbing the redox reactions occurring during canard curve acquisition or after successive canard curve acquisitions. The intercalated potential stimulus intervals may constitute a sub-part of the repeated canard curve pattern or be intercalated between repetition patterns dedicated to the electrochemical measurement of the probe.

[0060] In other words, the rotary encoder necessary to know the rotational speed of the rotating element can be implemented with only the electrodes of the electrochemical probe and its operation can be temporally intercalated into the cyclic voltammetric operation of the probe.

[0061] The electrode dedicated to acquiring the electrical signal produced by the hydraulic or electrical perturbation, fixed or fully implemented within the rotating element and active with each pass, may optionally be an independent electrode (or group of electrodes), in addition to the electrochemical probe. This can allow for a measurement protocol that is simpler to implement, optimize, and manage. An independent electrode is particularly advantageous if an electrical potential stimulus is repeated cyclically during the acquisition of the canard curve, in order to avoid any interference with the main volt-amperometric measurement or any addition of a contribution akin to noise.

[0062] The invention thus provides a reliable measurement of the flow velocity of a fluid. It can be coupled to the measurement system as described and claimed in the patent application filed on January 8, 2024 under number FR2400143 and entitled "Multi-point pressure measurement guide bearing, System for measuring the viscosity or Reynolds number of a fluid, with a pole guided by the bearing, Application to monitoring in bioproduction", to obtain an estimate of the Reynolds number and the viscosity of the fluidic medium.

[0063] For the actual analysis of the measurement data, a method for analyzing the shape of the electrical disturbance profile, which is compressed or expanded over time according to the rotational speed, can be implemented. The shortened or lengthened time between two signal signatures corresponds to accelerated or decelerated rotational speeds of the rotating element, respectively, and therefore to accelerated or decelerated fluid flow velocities, respectively, possibly after the application of at least one calibration correction.

[0064] An artificial intelligence method can also be implemented, using classification to determine and discriminate between the different velocities in the measured data. Classes can be created primarily based on flow velocity ranges. Clusters can be created to determine the nature of the flow or to estimate the local viscosity of the fluid without determining the exact (metrological) flow velocity.

[0065] As a corollary to the analysis of the data measured by the measuring device according to the invention, it is possible to dynamically control, in real time, that is to say during the execution of an industrial process using a fluid, the choice between several parameters or several configurations of a fluid condition control system, for example, a control system acting, for example, on a mixing turbine or a bubbling system. This can occur in particular due to a significant variation in flow rate, fluid viscosity, or lack of oxygenation.

[0066] This dynamic control can be implemented using a digital twin. Depending on environmental variables and information directly measured or provided by the classification method based on velocity measurement data according to the invention, the digital twin can perform new simulations. These simulations can be carried out, for example, using finite elements. The digital twin can also change its pre-defined calculation model, for example, by Model Order Reduction (MOR), a technique that reduces the computational complexity of mathematical models in numerical simulations. The information provided by the invention can lead to an evolution of the parameters of a MOR model or its replacement by another MOR model obtained for a different class, for example, a different Reynolds number range.

[0067] In conclusion, the invention offers several advantages, among which we can mention:

[0068] - a reliable estimation of the flow velocity of a fluid, advantageously around an electrochemical probe which measures its electrochemical properties, allowing to resolve an unknown on the estimation of the localized or momentary viscosity of the fluid, the other unknown being pressure induced by the same fluid at the same place and addressed in the patent application filed on January 8, 2024 under number FR2400143;

[0069] - a more precise estimation of the impact of flow physics on quality Electrochemical measurements prior to calibration, and / or on the accuracy or short-, medium-, or long-term stability of the calibration, are linked to potential changes in fluid flow properties. This helps to resolve potential ambiguities in the analysis of electrochemical dynamics based on the results measured by the probe.

[0070] Other advantages and features will become clearer upon reading the detailed description, given by way of illustration and not limitation, with reference to the following figures. Brief description of the drawings

[0071] [Fig. 1] [Fig. 1] is a schematic perspective view of the implementation at end of a pole, a first example of a speed measuring device flow of a non-gaseous fluid, according to the invention.

[0072] [Fig.2] [Fig.2] is a side view of the system according to [Fig.1].

[0073] [Fig.3] [Fig.3] is a schematic front view of a flat blank of an element rotation according to the first example in figures 1 and 2, achieved by flat additive manufacturing before being finalized.

[0074] [Fig.4] [Fig.4] illustrates the positioning of the drilling tool to produce a rotating element according to the example of figures 1 and 2.

[0075] [Fig.5] [Fig.5] is a perspective view of a second example of a device for measuring the flow velocity of a non-gaseous fluid, according to the invention.

[0076] [Fig.6] [Fig.6] is a side view of the system according to [Fig.5].

[0077] [Fig.7] [Fig.7] is a partial longitudinal cross-sectional view of the system along the [Fig.5].

[0078] [Fig.8] [Fig.8] is a schematic perspective view of a third example of a device for measuring the flow velocity of a non-gaseous fluid, according to the invention.

[0079] [Fig.9] [Fig.9] is a cyclic voltamogram, that is to say a so-called canard curve of current density as a function of potential, characteristic of a detection by cyclic voltammetry of a free oxidized species to diffuse in solution as implemented by an electrochemical probe of a system capable of measuring both the flow rate of a fluid and its electrochemical properties according to the invention. Detailed description

[0080] For the sake of clarity, the same references designating the same elements according to the invention are used for all figures 1 to 8.

[0081] The drawings and the arrangement of the different elements in relation to each other are not shown to scale.

[0082] Throughout this application, the terms "above", "below", "lower" and "upper" are to be understood by reference to the measuring system according to the invention as it is in an installation configuration with a measuring pole arranged vertically.

[0083] Figures 1 and 2 illustrate a first example of a device for measuring the flow velocity of a non-gaseous fluid contained in a vessel, such as a tank, particularly one with opaque walls. This could be the tank of a bioreactor containing a bioproduction fluid whose mixing conditions one seeks to determine and control.

[0084] The device 1 includes first of all a tube 2 with longitudinal axis X forming a measuring pole.

[0085] An element 3, mounted for rotation around the tube 2, comprises at least one wall 30 with a plurality of opening holes 31, 32, 33 made in such a way that the peripheral surface 300 of each hole is shaped so that a flow of fluid on the wall causes an asymmetry of the support forces on each peripheral surface of the hole and thus sets the element 3 in rotation around the axis X.

[0086] In other words, the surface of the wall 30 is made mechanically asymmetric about the X axis, that is to say, it can easily be subjected to a rotational torque about the X axis and with the preferred characteristic that the holes are made as small hollow cylinders in the thickness of the cylindrical wall with for each small cylinder an axis not intersecting with the X axis.

[0087] An example of the fabrication of a blank 3 of a rotating element produced flat by additive manufacturing is shown in [Fig. 3]. To finalize the rotating element 3, this blank is rolled onto itself and then sealed at its two adjoining edges. The blank 3 can be produced in several sub-parts with successive assembly of the adjoining edges.

[0088] Fig. 4 shows the presence of drilling tools PI, P2, P3 which each extend along a non-secant axis with the central axis X of the tube 2 so as to respectively make holes 31, 32, 33 with asymmetric peripheral surface.

[0089] Due to the asymmetry of each peripheral surface 300 of hole, a flow of fluid on the wall 30 causes support forces on the peripheral surfaces of the holes such that an overall rotational torque results and thus sets the element 3 in rotation around the X axis.

[0090] In the illustrated example, element 3 is in the form of a cylindrical ring, with holes 31 to 33 made in the thickness of the cylindrical wall, each with an axis that does not intersect the X-axis of the cylinder. The diameter of the ring and the thickness of its wall are chosen to maximize this torque according to rules known to those skilled in the art, and beyond this initial dimensioning, the through holes are adapted to the intended use.

[0091] This element 3 can be mounted in rotation on the measuring pole 2 by means of a ball cage 4 which can be integrated directly into the element 3 or interposed between it and the pole 2.

[0092] As can be seen in Figures 1 and 2, the holes 31 to 33 are of different diameters, for example, with the larger holes 31 on the lower and upper end portions, the intermediate-diameter holes 32 inside the wall 30, and on either side a smaller-diameter hole 33. The arrangement of these holes 31 to 33 can be symmetrical with respect to the median plane of the height of the cylindrical ring 3. As also shown, these holes 31 to 33 are arranged in rows regularly spaced at an angle of 60° around the X-axis. Having different diameters for the holes 31 to 33 allows for a wider range of Reynolds numbers that characterize the fluid, enabling the ring 3 to rotate around the X-axis.

[0093] The device 1 finally includes a rotary encoder 5, 50 adapted to measure the rotation of the element and thereby the flow velocity of the fluid.

[0094] According to an advantageous embodiment, the encoder 5 includes a volt-amperometric sensor 50 fixed to or protruding from the free end of the tube 2 inside the rotating element 3. This electrochemical sensor 50 includes a pair of electrodes, including a so-called working electrode to which an applied electrical potential can be varied as a function of time and a so-called auxiliary electrode in which the electrical signal flowing, as well as in the working electrode, is measured as a function of the electrical potential.

[0095] An electrical or hydraulic means 51 fixed to or entirely incorporated within the element allows the electrical signal measured by the pair of electrodes to be disturbed, so as to count each revolution made by the element around the tube. The rotational speed of the rotating element 3 can thus be measured, and thereby the flow velocity of a fluid over it.

[0096] As illustrated in [Fig. 7], a hydraulic disturbance means 51 can take the form of a rib 51 arranged on the inner face of the rotating ring 3, over all or part of its height. As illustrated in Figures 1 and 5, the element 51 can be projecting.

[0097] The example of device 1 according to figures 5 and 7 differs from that of figures 1 and 2 by holes 34 to 36 of larger to smaller diameter respectively which are made with a random arrangement in the peripheral wall 30 of the rotating ring 3.

[0098] Fig. 8 illustrates another example of device 1 with vertical rows of holes 37 to 39 of the same diameter, from largest to smallest respectively, arranged adjacent to each other, also being angularly separated from each other by 60°.

[0099] The volt-amperometric sensor 50 is advantageously that of an electrochemical probe which allows the electrochemical properties of the fluid to be measured. The device 1 then becomes a combined system for measuring the fluid flow velocity and its electrochemical properties. In other words, the rotary encoder 5 acts as both a tachometer and an electrochemical sensor. It can thus be described as an electrochemical tachometer.

[0100] According to an advantageous embodiment, the invention implements an operation which allows, using only the electrodes of the electrochemical probe, the measurement of the fluid flow velocity.

[0101] This advantageous operation is now described.

[0102] Fig. 9 illustrates an example of a cyclic voltamogram for an electrochemically reversible redox process obtained with electrodes of probe 5. The illustration shows the key points and portions of the so-called canard characteristic curve useful for analyzing the properties, with values ​​that are only indicative.

[0103] The scan begins at -0.4 V and progresses towards more positive oxidative potentials. Initially, the potential is insufficient to oxidize the analyte (a). When the potential approaches several kT from the standard potential, the onset (Eonset) of oxidation is reached. Following this, the current increases exponentially (b) as the analyte begins its oxidation at the surface of the working electrode. For a reversible process, the current initially increases as if there were no change in the oxidant concentration. The current is dictated by the diffusion rate of the oxidant towards the electrode, as well as by the proportion converted to the reduced form. This can be understood according to the Nernst equation. As the analysis continues, more oxidant is depleted. The concentration gradient adjusts accordingly. It is this change that causes a peak in the voltammogram.

[0104] It is observed that the decrease in current due to oxidant depletion outweighs the increase due to the change in the proportion of oxidant oxidized at the electrode. The current reaches its maximum at point c (anodic tip current (ipa) for oxidation at the anodic tip potential (Epa)). Here, more positive potentials cause an increase in current which is compensated by a decrease in analyte flux from increasingly greater distances from the electrode surface.

[0105] From this point onward, the current is limited by the massive transport of the analyte from the ground to the DDL interface, which is slow on the electrochemical timescale. This results in a decrease in current (d) as the potentials are swept more positively. This continues until a steady state is reached, where further increases in potential have no effect. Reversing the sweep to negative potentials (reductive sweep) continues to oxidize the analyte. This continues until the applied potential reaches the value at which the oxidized analyte (which has accumulated on the electrode surface) can be re-reduced (e). The reduction process mirrors that of oxidation. The only difference is that it occurs with an opposite sweep direction and a cathode peak potential (ipc) at the cathode peak potential (Epc) (f).The anodic and cathodic peak currents must be of the same amplitude but opposite sign. This is only true if the process is reversible (and if the cathodic peak is measured relative to the baseline after the anodic peak).

[0106] It is therefore the effect of the two sweeps of the electric potential that allows us to analyze a chemical equilibrium called "redox".

[0107] According to the invention, to detect the electrical signals of the disturbances generated by the means 51, electrical potential stimuli are added in time segments not used for the interpretation of the properties of the redox reaction, i.e. that is, outside the segments that provide the characteristic points and slopes of the canard curve.

[0108] In particular, with the example of [Fig. 6], the electrical potential stimuli can be incremented in the flat area at negative voltages between -0.4V and -0.3V. It is possible to use lower voltages, for example, reduced by -0.1V from the minimum useful value. The applied stimuli will preferably be rectangular pulses applied for a duration compatible with counting at least one revolution.

[0109] Preferably, where possible, continuous pulses are applied during cycling. The pulses must be of sufficient amplitude and temporal characteristics (duration and repetition) to detect the passage of the mean 51, which is sufficiently small so as not to interfere with the canard curve analyses. This implies that minor modifications or small fluctuations added to the canard curve are acceptable as long as the extraction of chemical properties is preserved.

[0110] The invention is not limited to the examples just described; in particular, features of the illustrated examples can be combined in unillustrated variants.

[0111] Other variants and improvements may be envisaged without departing from the scope of the invention.

[0112] If in the illustrated examples the holes are of circular or elliptical cross-section, any shape of through holes can very well be considered, such as triangular, square, rectangular, etc. cross-sections.

[0113] If in the illustrated examples the holes are arranged in rows regularly spaced at 60° to each other, other variants can be considered such as arrangements in pairs, in three rows at 120° to each other, etc. and / or a non-regular distribution around the X axis.

[0114] More generally, the ability of the fluid to pass through the holes instead of simply being deflected by the wall of the rotating element increases the forces exerted on the bearing surfaces defined by these peripheral walls. In turbulent flow, more numerous and smaller holes are preferable in order to sum the useful contributions and minimize the forces produced by internal turbulence orientations that are not directed in the overall flow direction.

[0115] The rotating element and the holes are designed to minimize significant frictional forces, so that the angular velocity is acquired with very low effort in order to be directly related to the free flow of the unconfined fluid. When frictional forces allow, if they are sufficiently low, it is possible to consider to increase the surface area of ​​the peripheral walls by means of protrusions arranged on the side of the external face and / or the internal face of the rotating element.

[0116] The electrode dedicated to acquiring the electrical signal produced by the perturbation means 51 and active at each pass may optionally be an independent electrode, or in addition to the electrodes of the electrochemical probe 5. An independent electrode is advantageous in particular if the stimulus is repeated cyclically during the acquisition of the canard curve in order to avoid any interference or any addition of a contribution similar to noise.

[0117] Although the advantageous method described is voltamperometry, the number and choice of electrodes, whether those for measuring current or those applying voltage, is free.

Claims

Demands

1. Device (1) for measuring the flow velocity of a non-gaseous fluid, in particular contained in a container, such as a tank, especially one with opaque walls, comprising: - a tube (2) with longitudinal axis X; - an element (3) mounted for rotation around the tube and comprising at least one wall with a plurality of through holes (31 to 39) made such that the peripheral surface (300) of each hole is shaped so that a flow of the fluid over the wall causes an asymmetry of the support forces on each peripheral surface of the hole and thus sets the element in rotation about the axis X; - a rotary encoder (5) adapted to measure the rotation of the element and thereby the flow velocity of the fluid.

2. Measuring device according to claim 1, the wall of the element (3) being at least partly cylindrical, the holes being made in the thickness of the cylindrical wall with each one having an axis not intersecting with the axis of the cylinder of the wall.

3. Measuring device according to claim 2, the holes being distributed uniformly or not on the periphery.

4. Measuring device according to claim 2 or 3, the holes being distributed in rows, preferably three or six in number, parallel to the X axis, preferably distributed uniformly angularly around the X axis.

5. A measuring device according to any one of claims 2 to 4, the holes being of different diameters so as to broaden the Reynolds number range that characterizes the fluid.

6. A measuring device according to any one of the preceding claims, the element comprising a plurality of protrusions arranged on the external face and / or the internal face of the element, each adapted to create a fluid support surface.

7. Measuring device according to any one of the preceding claims, the element being mounted for rotation around the tube by at least one bearing or ball bearing or ball cage (4).

8. A measuring device according to any one of the preceding claims, the rotary encoder (5), referred to as an electrochemical tachometer, comprising: - an electrochemical sensor (50), fixed to the free end of the tube inside the element, comprising at least one pair of electrodes, including a so-called working electrode to which an applied electrical potential can be varied as a function of time and a so-called auxiliary electrode in which the electrical signal which flows, as well as in the working electrode, is measured as a function of the electrical potential; - an electrical or hydraulic means (51) fixed to or made entirely in the element, adapted to disturb the electrical signal measured by at least one pair of electrodes, so as to be able to count each complete turn, made by the element around the tube.

9. Measuring device according to claim 8, the hydraulic means being a protrusion or asperity arranged on the inner face of the element.

10. An electrochemical and flow velocity measurement system for a non-gaseous fluid, in particular contained in a container, such as a tank, especially one with opaque walls, comprising: - a measuring pole forming the tube, one free end of which is intended to be immersed in the fluid; - at least one electrochemical probe, fixed to the free end of the measuring pole, and adapted to measure electrochemical properties of the fluid; - a measuring device according to any one of the preceding claims, the element of the device being mounted to rotate around the electrochemical probe which also acts as a rotary encoder.

11. Measurement system according to claim 10, the measurement device being according to claim 8 or 9, the electrochemical sensor of the device being the electrochemical probe.

12. A method for operating the measuring system according to claim 10 or 11, the measuring device being according to claim 8 or 9, comprising the steps of: i / performing electrochemical measurements using the electrochemical probe to monitor the electrochemical properties of the fluid; ii / during or after step i, applying electrical potential stimuli to the working electrode, located outside the useful areas

13.

14. from the characteristic curve of current density as a function of the probe potential, and detect the measurement of current, potential or impedance perturbed by the electrical or hydraulic means of the rotary encoder during the application of potential stimuli, and deduce the measurement of fluid flow velocity. Settling, purification, or production medium or tank, in particular of a bioreactor, comprising a measuring device according to one of claims 1 to 9 or a system according to one of claims 10 to 11. Use of a measuring device according to any one of claims 1 to 9 or of a system according to any one of claims 10 to 11 for monitoring bioproduction and / or for providing reference data in a digital twin.

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