The invention relates to an acoustic phase mask for the spatial manipulation of acoustic wavefronts, for example an acoustic lens for focusing an acoustic wave.
The spatial manipulation of acoustic wavefronts, and particularly the focusing of acoustic waves, is typically carried out using metamaterial devices, notably in a frequency range corresponding to audible and/or ultrasonic frequencies.
Zhu et al. (Zhu, H., & Semperlotti, F. (2015), Improving the performance of structure-embedded acoustic lenses via gradient-index local inhomogeneities, International Journal of Smart and Nano Materials, 6(1), 1-13.) describes for example a device for focusing an ultrasonic wave propagating in an aluminum plate. Inhomogeneities or inclusions are formed by openings in the aluminum plate so as to form a waveguide, making it possible to focus an initially radial ultrasonic wave. This method is difficult to transpose industrially to the manipulation of acoustic waves in three dimensions, and in other acoustic wave propagation media in which it is not possible to create openings.
Martin et al. (Martin, T. P., Naify, C. J., Skerritt, E. A., Layman, C. N., Nicholas, M., Calvo, D. C., . . . . & Sánchez-Dehesa, J. (2015), Transparent gradient-index lens for underwater sound based on phase advance, Physical Review Applied, 4(3), 034003.) describes a device comprising an anisotropic array of hollow aluminum cylinders arranged to form an acoustic index gradient n in the device. An incident sound acoustic wave, passing through the array of cylinders, is focused in predefined regions of space. The manufacture of such a device requires precise and expensive mechanical assembly, limiting its industrial application.
One goal of the invention is to produce an acoustic phase mask that is easier to implement or to manufacture than the devices of the prior art.
These goals are achieved in the present invention by virtue of an acoustic phase mask, the mask having a variation in the acoustic index n, characterized in that the phase mask comprises a body comprising:
The invention can be advantageously complemented by the following features, taken individually or in any one of their technically possible combinations:
Another aspect of the invention relates to a process for manipulating acoustic wavefronts, comprising a step of installing an acoustic phase mask described above in the propagation space of an incident plane acoustic wave having a wavelength λ.
The phase mask can advantageously have a thickness d in one direction of propagation of the incident acoustic wave, the thickness d being strictly less than the wavelength λ.
Another aspect of the invention relates to a process for manufacturing a phase mask described above, the method comprising steps of:
The invention can be advantageously complemented by the following features, taken individually or in any one of their technically possible combinations:
Other features and advantages will become further apparent in the following description, which is purely illustrative and non-limiting, and should be read in relation to the appended figures, among which:
The “porosity” of a porous material is defined the ratio of the pore volume of the porous material to the total volume of the porous material (i.e. the sum of the pore volume of the porous material and the volume of solid material extending between the pores).
“Manipulation” of an acoustic wave (or of the acoustic wavefront) means any deliberate and controlled modification of said front (local phase, amplitude and/or polarization), for example the deflection or focusing of an acoustic wave.
A “phase mask” is defined as any device that allows the phase of an incident wave passing through it to be modified locally. Preferably, the phase mask is a planar device.
An “emulsion” is defined as a mixture of two immiscible liquid substances, one being homogeneously dispersed in the form of drops in the other.
The body 2 comprises at least one matrix 3, formed in a deformable solid material, and pores 4 formed in the matrix 3. The majority of the pores 4 are filled with gas, allowing the body 2 to be compressible (compressibility is comprised between 109 Pa−1 for the non-porous body 2 to 10−6 Pa1 for the body 2 having 40% gas-filled pores). The deformable solid material extends between the pores 4. This material has a shear modulus preferentially less than 10 MPa.
The pores 4 give the body 2 a local porosity φ. The body 2 has a porosity of less than 50%, i.e. the local porosity at any point in the body 2 is less than 50%. In other words, the maximum porosity of the body 2 is less than 50%.
The body 2 has a porosity φ gradient. This porosity gradient in the body 2 is controlled and leads to a spatial variation of the acoustic index n in the body 2. The variation of the acoustic index n, or the acoustic index n gradient, leads to a modulation of the incident wavefront during its passage through the phase mask 1, allowing for example to focus an incident wave, particularly an incident plane wave.
The body 2 is at least partly made of porous material, i.e. a material comprising the matrix 3 of deformable solid material, and the pores 4, the deformable solid material of the matrix 3 extending between the pores 4. The porous material is manufactured by polymerization of an aqueous emulsion in a polymerizable solvent, for example thermally or by UV irradiation and subsequent drying.
The solid deformable material includes elastomeric polymers. These polymers have glass transition temperatures below room temperature. In particular, the polymers of the deformable solid material have a glass transition temperature below −50° C., preferably below −80° C., and preferably below −100° C.
Due to the high porosity of the porous material, the filling of the pores 4 mostly with gas, and the deformability of the solid material, the body 2 may have a higher compressibility than known porous materials.
The acoustic index n of a material can be defined by the formula (1):
n=c
ref
/c
mat (1)
where cref and cmat are respectively the propagation velocities (or celerities) of the longitudinal acoustic waves in a reference material, i.e. water in the invention, for which cref=1500 m·s−1, and in the material under consideration. As the propagation velocity of an acoustic wave in a material depends on the porosity of the material, the acoustic index n depends on the porosity. A porosity gradient of the porous material thus leads to an acoustic index gradient n in the body 2 of the phase mask 1.
The porous material can have a wide range of propagation velocities. Indeed, the propagation speed of sound in a material can be written as follows cmat=(M/ρ)1/2 where ρ is the density of the material and M is the compressive elastic modulus of the material. The velocity of an acoustic wave in the porous material decreases when both the compressive elastic modulus of the porous material decreases and the density of the porous material increases.
Thus, the porosity of the porous material can be adjusted to exhibit propagation velocities between typically 10 m·s1 and 1000 m·s1. Known devices do not allow variations in propagation velocities with such a high amplitude.
With reference to
a) forming a plurality of emulsions 12, each emulsion 12 having, on the one hand, a first liquid phase 13 and, on the other hand, a second phase 14 comprising monomers and at least one type of surfactant, so as to form drops of the first liquid phase 13 in the second phase 14.
At least two emulsions 12 have different fractions in the first phase 13. The step of forming an emulsion is illustrated in
b) cross-linking the monomers of the emulsions 12 so as to form a deformable solid material 3 defining the matrix or matrices 3 and the pores 4 containing the first liquid phase 13.
The cross-linking step is illustrated in
c) drying the porous material obtained in step b) to remove the first liquid phase 13 so as to mostly fill the pores 4 with gas.
The drying step is illustrated by
During step a), each inverse emulsion 12 is made between, on the one hand, a second phase 14 comprising monomers and a suitable surfactant, and on the other hand a first aqueous phase 13. The emulsion 12 can be made using a shearing device (for example Rayneri, Ultraturrax, or any mechanical device allowing sufficient shearing of the two phases). The emulsion can also be formed by exposing the first phase 13 and the second phase 14 to ultrasonic waves. The “stock emulsion” is defined as the emulsion 12 thus obtained. The volume fraction of the stock emulsion 12 in the first phase 13 can be between 0% and 90%. The choice of surfactant is adapted to the monomers chosen in the second phase 14. Generally, the surfactant has an HLB number less than or equal to about 8. Thus, an inverse emulsion 12, i.e. comprising drops of aqueous first phase 13 in a lipidic second phase 14, is favored. The diameter of the first phase 13 drops formed in the second phase 14 is typically comprised between 0.1 and 100 μm.
During step b), the emulsions 12 are deposited in one or more containers. At least two emulsions 12 have different fractions in the first phase 13. The first phase 13 fraction may also vary in a controlled manner during the deposition of one emulsion 12 in a container, forming a plurality of emulsions 12 continuously. The container can be, for example, a mold or a honeycomb. A container wall can be formed by an already cross-linked emulsion 12. Once deposited, the monomers of the second phase 14 of the emulsion 12 are cross-linked to form a deformable solid material. The cross-linking of the monomers can preferentially be carried out by exposing the monomers to ultraviolet radiation or to heating. At the end of step b), one or more matrices 3 of deformable solid material are obtained. Pores 4 are formed by the matrix or matrices 3, which are filled with the first phase 13.
During step c), the matrix or matrices 3 is/are dried. This step makes it possible to replace, at least in majority and preferentially completely, the first liquid phase 13 contained in the pores 14 by the gas. Typically, the drying of the first phase 13 is carried out by pervaporation of the first liquid phase 13 through the polymer matrix 3.
In known drying methods, a drying front propagates in the matrix 3, and more particularly at the interface between the matrix 3 and the pores 4. The matrix 3 is then subjected to a drying pressure Pdrying equal to twice the surface tension □ of the first phase liquid 13 with air, divided by the radius r of the micropores through which the first phase 13 escapes during pervaporation, i.e. Pdrying=2γ/r. Although it is difficult to know the exact value of r, it can be estimated that r is typically less than or equal to 1 nm. Thus, for a first phase 13 of water (□=72 mN/m), Pdrying≈144 MPa. This value, indicative, is higher than the typical shear modulus of the deformable solid material, in elastomeric polymers. Consequently, pore collapse is observed when using known drying methods, and the porosity of a porous material is thus limited because no gas replaces the disappearance of first phase 13 in the pores 4.
According to one aspect of the invention, the drying step is a step of supercritical drying of the porous material to remove the first liquid phase 13. The supercritical drying method is known for drying brittle porous materials such as aerogels. It is for example described by Marre et al. (Mane, S., & Aymonier, C. (2016), Preparation of Nanomaterials in Flow at Supercritical Conditions from Coordination Complexes. In Organometallic Flow Chemistry (pp. 177-211). Springer, Cham.). During supercritical drying, a liquid phase contained in the pores 4 is transformed into a gaseous phase, without phase transition, by imposing temperature and pressure conditions that allow to bypass the critical point of the compound(s) contained in the pores 4. The absence of passage through a phase transition line avoids a drying front between a liquid and a gaseous phase. Thus, the drying pressure is decreased or equal to zero, and it is possible to avoid the crushing of the porous material on itself during drying.
The drying fluid used for supercritical drying can be CO2. CO2 has a critical point corresponding to a pressure PC=73.9 atm and a temperature TC=31° C. These temperature and pressure conditions are easy and economical to implement.
The ethanol is then extracted by CO2. Extraction is carried out by placing the porous material soaked in pure ethanol in a high-pressure reactor, in which the pressure and temperature conditions can be adjusted by means of injection pumps and an outlet pressure regulator. The reactor temperature is first adjusted above the theoretical critical temperature of the CO2/ethanol mixture (i.e. between 45 and 50° C. for a 90/10 molar composition) while the reactor is slowly pressurized with CO2, up to a value above the critical pressure of the CO2/ethanol mixture (i.e. 110 bar). These variations in pressure and temperature correspond to the trajectory illustrated by dotted lines from point A to point B in
The CO2 is then continuously pumped through the porous material at a constant flow rate (11 g/min), while the operating conditions are kept constant (the pressure is controlled by an outlet pressure controller). The CO2 mixes with ethanol and forms a single-phase supercritical mixture. During this mixing phase, the ethanol contained in the pores 4 is gradually replaced by a supercritical CO2/ethanol mixture which is gradually enriched with CO2. At the same time, the fluid ethanol/CO2 mixture is extracted from the reactor in order to maintain a constant internal fluid volume. Once all the ethanol has been replaced by CO2, the pressure in the system is slowly reduced to 1 bar, for example in one hour, so as to return the CO2 to the gaseous phase without returning to the liquid state. This pressure change corresponds to the dashed line from point B to point I in
Finally, the temperature is lowered to room temperature. This temperature variation corresponds to the trajectory illustrated by dotted lines from point I to point A in
According to another aspect of the invention, the first liquid phase 3 comprises a liquid compound adapted to spontaneously decompose at room temperature into a gas and a liquid. The kinetics of decomposition of the liquid into a gas and a liquid product can be determined by the proportion of liquid that can decompose in the dispersed phase. This kinetics can be adjusted so that the characteristic time for the appearance of gas bubbles is typically slower (i.e. typically more than 30 minutes) than the time required for emulsification. During the drying step, the liquid compound is allowed to decompose to form a gas phase in the pores 4. The compound 1 can be hydrogen peroxide H2O2. Hydrogen peroxide decomposes at constant ambient temperature and pressure into water (liquid) and gaseous oxygen. The proportion of H2O2 in the first liquid phase 13 may be preferentially ⅓ by total mass of the first phase 13. For a proportion of H2O2 in water of ⅓, the characteristic time of appearance of the gas bubbles is about 30 minutes. This kinetics can be slowed or accelerated by adjusting this proportion or by adding a catalyst in controlled concentration in the dispersed phase (for example iodide ions I which are known to catalyze the decomposition reaction of H2O2 into oxygen and water). This method makes it possible to compensate for the pressure potentially exerted, during drying, by contact lines in the pores 4 by an increase in gas pressure caused by the decomposition of the compound. It is thus possible to avoid the collapse of the pores 4 on themselves during the drying of the porous material. This method does not require external control of the pressure and/or temperature imposed on the porous material. Thus, the use of the compound makes it possible to dry the porous material using a simpler and less expensive material than in supercritical drying. Drying by introduction of the compound is for example achieved by placing the porous material in an oven, in which the temperature is controlled at 40° C., under ambient atmosphere.
The two drying processes described above (supercritical drying and introduction of a compound in the first liquid phase 13) make it possible to obtain a porosity of the porous material substantially equal to the volume fraction in the first phase 13 obtained during step a) of the process.
The second phase 14 comprises Silcolease UV poly 200 silicone oil from Bluestar Silicones, 4% by mass Silcolease UV cata 211 catalyst from Bluestar Silicones, 0.4% by mass surfactant (2-octyl-1-dodecanol) and 200 ppm Genocure ITX from Rahn. The first phase 13 comprises 1.5% by mass sodium chloride. The amount of aqueous phase incorporated into the organic phase is dependent on the desired porosity of the porous material. The formation of an emulsion is achieved in a mortar by adding the first phase 13 dropwise during shearing, and then it is refined either with paddle tools (such as Rayneri or Ultraturrax) or by ultrasound. The cross-linking step is carried out by exposing the emulsion to ultraviolet radiation with the BlueWave 200 lamp from Dymax. The porous material is then dried by supercritical drying or by introducing a compound, as described above.
The second phase 14 consists of 64% by mass ethylhexyl acrylate, 5.5% by mass Styrene, 10.5% by mass divinylbenzene and 20% by mass SPAN 80 surfactant. The aqueous phase has sodium chloride concentrations of 25.10−3 mol/L and potassium peroxodisulfate concentrations of 5.10−3 mol/L. The amount of first phase 13 incorporated into the organic phase is dependent on the desired porosity of the final material. The formation of an emulsion is achieved with a Rayneri type paddle tool by adding the first phase 13 dropwise during shearing. Cross-linking of the monomers is achieved by heating to a temperature of 60° C. The porous material is then dried by supercritical drying or by introducing a compound as described above.
A deformable silicone-based solid material (denoted SiVi/SiH) can be obtained by thermal polymerization of PDMS via a hydrosilylation reaction. The second phase 14 comprises 8.8 g of PDMS-vinyl (BLUESIL FLD 621V1500), 1.8 g of PDMS-silane (BLUESIL FLD 626V30H2.5) and 0.352 g of platinum catalyst (SCLS CATA11091M), (BlueStar Silicones). In order to be able to prepare the emulsions 12 before the cross-linking of the monomers, 4.4 mg of polymerization retarder (1-ethynyl-1-cyclohexanol, ECH from Sigma Aldrich) is added. To stabilize the emulsion, 2-octyl-1-dodecanol or Silube J208-812 can be used. The emulsions 12 are prepared by introducing a first aqueous phase 13 comprising 1.5% by mass NaCl under stirring. The emulsion is then poured into a Teflon mold and heated at 60° C. for 24 hours. The porous material is then dried by supercritical drying or by the introduction of a compound, as described above.
Due to the presence of a porosity gradient leading to a spatial variation of the acoustic index n in the body 2, it is possible to locally control the velocity of acoustic waves and thus to custom bend acoustic rays by mirage effect (3D version of the gradient medium) or to control phase delays/advances at wavefronts (2D version of these media, for example a phase mask 1). Thus, it is for example possible to concentrate the acoustic beams, i.e. focus them, to deflect the acoustic beams and/or to separate the acoustic beams. “Manipulation” of the acoustic wavefront means at least one of the effects previously described on a plane incident acoustic wave.
With reference to
Generally, so that the output pressure field is as close as possible to the target field (chosen by a user), the phase mask 1 is manufactured so that the transmission of an incident plane wave 6 by the phase mask 1 reproduces exactly at the output of the phase mask 1 the chosen target field, i.e. in z=0, and preferentially on a larger surface of the plane defined by the x and z axes.
The target pressure field can, for example, be a pulsating harmonic field w. The target pressure can be written
where A is the amplitude of the pressure, Φc the target phase, and t the time. The acoustic field pm immediately at the output of the phase mask 1 is equal to
The phase mask 1 makes it possible to impose the phase of the wave transmitted directly at the output of the phase mask 1, which makes it possible to establish the relation Φm (x, y)=Φc (x, y, z=0). It is possible to consider that the phase mask 1 has an acoustic index n variable in the plane xy and constant in its thickness d, assumed to be small with respect to λ, that is to say, to consider that n depends on x and y. The phase mask locally shifts the incident field by a quantity ein(x,y)k
n(x,y)=Φc(x,y,z=0)/k0d (2)
to be adapted to generate the target field pc. The porosity distribution in the phase mask 1 is thus chosen so as to produce a phase mask 1 with an acoustic index n satisfying formula (2).
With reference to
With reference to
With reference to
With reference to
With reference to
The different layers 9 can be dried before each application of a new emulsion.
With reference to
The deposited layers 9 have a height h smaller than the wavelength λ of the incident acoustic wave 6. For example, for a frequency of 100 kHz, the wavelength λ of an incident plane acoustic wave 6 is 15 mm. The layers 9 have a height equal to 8 mm (i.e. about λ/2), which is sufficient for the acoustic index gradient n to be effectively perceived as continuous for the incident plane acoustic wave 6. It is of course possible to reduce the width of the bands, for example to about 1 mm.
With reference to
With reference to
With reference to
With reference to
The phase mask 1 may comprise a succession of strips or layers 9, as described above.
With reference to
is thus transformed into a transmitted or deflected plane wave 19, of the target field
The spatial distribution of n verifies n(x)=n0+sin θx/d, n0=n (x=0) being the index at the center of the phase mask 1. The gradient is preferentially constant, which corresponds to a linear change in the porosity of the body 2 in space. In this case, it is equal to sin θ/d and oriented along the x axis.
With reference to
is thus transformed into a convergent cylindrical wave at the focusing point of coordinate z=F with respect to the phase mask 1 whose output face corresponds to the coordinate z=0. Using a far-field approximation, the target field is expressed in the form
with r=√{square root over (x2+(z−F)2)}. The spatial distribution of the index n in the phase mask 1 is thus given by n(x)=n0−(√{square root over (x2+F2)}−F)/d. With reference to
In all the embodiments, it is possible to make the porosity of the body 2 correspond to a determined index n, as described previously, by using the measured relation between the velocity of the acoustic wave and the porosity of the material through which the acoustic wave passes, illustrated in
With reference to
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With reference to
Number | Date | Country | Kind |
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1852569 | Mar 2018 | FR | national |
Filing Document | Filing Date | Country | Kind |
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PCT/EP2019/057427 | 3/25/2019 | WO | 00 |