The present invention relates generally to the determination of the rheological parameters of fluids, regardless of their nature, and more particularly by means of a method implementing a continuous-jet droplet generator.
Determination of the rheological parameters of fluids is understood to mean, within the meaning of the present invention, the identification, for any type of fluid (whether Newtonian, shear-thinning, shear-thickening, viscoelastic or with threshold, etc.), of all the rheological properties of the fluids to be analyzed, such as, in particular, the surface tension, the density, the dynamic viscosity and the kinematic viscosity, the relaxation time, etc.
A continuous-jet droplet generator is understood to mean, within the meaning of the present invention, a continuous ink jet ejection device, usually designated by the acronym CIJ.
Understanding the flow properties of the fluids and measuring the associated rheological and physical properties are crucial both to research and industry.
The main quantities that characterize a fluid are its density, its surface tension and its rheological properties of viscosity and of elasticity. To determine these quantities, various measurement devices are necessary. Depending on the devices used, couplings or disturbances make measuring these properties difficult.
For example, the rheological properties of elasticity are disturbed by the surface tension and the inertias of the fluids and of the viscoelasticity measurement tools such as the rotational rheometers that are commonly used in research and in industry.
In order to determine the physical quantities of the fluids, the present invention relies on the development of a novel method for determining rheological parameters of fluids that implements a continuous-jet droplet generator of CIJ type and that uses a so-called “Data-Science” approach based on a dataset obtained from the CIJ method and the digital simulation of this method.
Upon the ejection of a fluid by the CIJ ejection method, three forces, inertial, viscous and interfacial (surface tension), are in competition and notably affect the morphology of the jet and of the droplets obtained. Under certain conditions, the morphology of the jet is thus unique (as illustrated by
In the present invention, the jet of fluid from the nozzle to the droplets of stabilized form will be called complete jet.
By ejecting a fluid using a suitable CIJ device, and by comparing its morphology to a dataset containing a vast range of jet morphologies through the “Data-Science” approach, it is possible to accurately determine the rheological properties of the fluid, that is to say its dynamic viscosity, its surface tension and its density.
The subject of the present invention is therefore a method for determining the rheological parameters of a fluid which comprises the following steps:
The method according to the invention is capable of determining the rheological parameters of any type of fluid, whether Newtonian or Non-Newtonian.
The first step A) of the method according to the invention consists in introducing, into a continuous-jet droplet generator, a fluid for which the rheological parameters are to be determined. The method according to the invention is suited to any type of fluid, whether Newtonian, shear-thinning, shear-thickening, viscoelastic, with threshold, etc.
The continuous-jet droplet generator used in the context of the method according to the invention (also called device of CIJ type) comprises a tank maintained at a given pressure p0 using a pump or any other pressurizing device and communicating via an inlet orifice with an ejection head, the temperature of which is controlled, as illustrated in
The second step B of the method according to the invention consists in performing a periodic stimulation, of amplitude A (in Volts) and of frequency F=1/T, of a piezoelectric actuator, such that the latter disturbs the pressurized fluid in said ejection head. The pressurizing of the fluid makes it possible to control the flowrate of the fluid on its ejection.
Advantageously, the piezoelectric actuator is immersed in the pressurized fluid in said ejection head.
The third step C) of the method according to the invention consists in ejecting out of said ejection head, via an outlet nozzle, the fluid thus disturbed in the step B, which then takes the form of a jet of given morphology.
The fourth step D) of the method according to the invention is a step of obtaining, using a stroboscope at a given instant t, of a fixed and illuminated image of the complete jet.
Image of the complete jet is understood to mean, within the meaning of the present invention, an image of the jet of fluid from the nozzle to the droplets that has a form which is stabilized.
Then, using a camera or a photographic device, one or more photographs of all or part of the image of the complete jet, the position of which appears fixed by virtue of the stroboscopic illumination of said complete jet (Step E), is or are recorded. These images are then analyzed (Step F) to extract therefrom a dataset descriptive of said jet and compared to a database in order to extract therefrom the rheological properties.
In particular, this database is composed of the morphologies of jets of fluids of different viscosity and surface tension. It is therefore necessary to obtain the morphologies of a large number of fluid jets that have different and known viscosities and/or surface tensions. Since the morphology of the jets depends also on the parameters of the CIJ device, this database must be composed in the same conditions of ejection of the CIJ device. Moreover, the number of fluids that are known (that is to say for which all the rheological parameters are known, namely the viscosity or viscosities, the surface tension and the density) and available experimentally, is not enough to constitute the dataset. So, a digital simulation approach is necessary: for a given nozzle, the jets are generated digitally and validated experimentally using a few known real fluids, including standard fluids, by comparing the digital and experimental results. A faithful prediction of the digital model is thus absolutely necessary in order to have a reliable determination of the rheological properties.
The morphologies of the jets are defined by the geometrical form taken by the free surface of the jet. It is possible to extract, from the geometrical form of the jet (as illustrated in
The measurement of the rheological properties of the ejected fluid is done by comparing the morphology of the jet to those contained in a database mapping a vast range of rheological properties.
Thus, more particularly, the last step of the method according to the invention (Step G) is a step of comparison and interpolation of the dataset descriptive of the jet obtained in the step F.
This step F of comparison and interpolation is performed using a statistical algorithm for a given outlet nozzle, pressure p0i and stimulation amplitude Ai, with i being a natural integer at least equal to 3, so as to estimate/determine the rheological parameters of said fluid.
In other words, this step F relies on the statistical algorithm which is a machine learning algorithm that makes it possible to identify, from information obtained experimentally, the fluid present using databases grouping together a large number of known fluids.
Advantageously, the dataset descriptive of the jet can be the geometrical form of the jet or data extracted from said geometrical form of all or part of the complete jet. Thus, the determination of the rheological properties of the fluids that are analyzed using the method according to the invention is based on the geometrical form taken by the jet and, in particular, on the fact that this form takes on a unique character depending on the stimulation amplitude.
Advantageously, the database can comprise information obtained with real jets and/or obtained with jets generated by digital simulation (which are previously validated experimentally using standard fluids).
According to a first variant embodiment of the step G of the method according to the invention, the statistical algorithm can be based on a model of linear regression type. The parameters of the model will be determined previously by using, as training set, the database containing the morphologies of jets of known fluids.
According to a second variant embodiment of the step G of the method according to the invention, the statistical algorithm can be based on a model of artificial neural network type.
Preferably, the model of neural network type can comprise at least one layer of neurons, which will be previously trained by using, as training set, the database containing the morphologies of jets of known fluids.
The comparison and interpolation in the step G is thus based on statistical models for which the coefficients have been determined previously.
According to a first embodiment of the method according to the invention, the procedure is as follows:
According to a second embodiment of the method according to the invention, the procedure is as follows:
Other advantages and particular features of the present invention will emerge from the following description, given as a non-limiting example and with reference to the attached figures and to the examples:
In order to determine the rheological parameters of a Newtonian fluid 1 (denoted A) with constant viscosity, a continuous-jet droplet generator 2, illustrated in
Then, the process is recommenced and the same continuous-jet droplet generator 2 is used to generate a continuous jet of droplets of a Non-Newtonian fluid 1 (denoted B), slightly shear-thinning with very high shear rate (greater than 300 000 s-1) in order also to determine therefrom its rheological parameters.
The fluids A and B have the same surface tension, the same viscosity with low shear rate and the same density. Thus, the difference between these two fluids lies solely in the shear-thinning nature of the fluid B.
The fluids A and B are ejected through the same devices of CIJ type with different stimulation amplitudes, the voltage of the piezoelectric actuator 23 varying from 2 V to 62 V. A photo of the jet 3 at the break is taken for each stimulation [
Despite the very close rheological properties, the competition between the different inertial, viscous and interfacial (surface tension) forces that come into play upon the ejection of the fluid makes it possible to discriminate the fluids and a strong difference of geometrical form of the jet is observed for the high stimulation amplitudes.
This example illustrates the determination of the viscosity of fluids using the method according to the invention, in the case where the statistical algorithm used in the step G is based on a model of artificial neural network type.
The ejection nozzle 24 is selected and identical for all the digital and experimental jets generated by a device of CIJ type 2 as represented in
In this example, the average ejection velocity, the density and the surface tension are also fixed. Only the viscosity of the fluid varies and the Reynolds number is directly linked to it.
4005 jets of Newtonian fluids are then generated using digital fluid mechanics simulation software: for a Reynolds number at the nozzle outlet varying from 100 to 900, in increments of one, five stimulation amplitudes are simulated digitally. The results of the simulations are strictly compared to a few jets of real fluids in order to ensure the relevance of the result obtained.
From the geometrical form of the 4005 jets thus obtained, the following data are extracted for each jet, in order to constitute the database:
80% of the dataset is selected randomly to constitute a training set for the training of said artificial neural network and the remaining 20% will constitute the test dataset.
This result shows that the method according to the invention makes it possible to accurately determine the rheological characteristics of the fluids.
Number | Date | Country | Kind |
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2007918 | Jul 2020 | FR | national |
Filing Document | Filing Date | Country | Kind |
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PCT/FR2021/051355 | 7/20/2021 | WO |