A METHOD FOR PREPARING A COMPOSITE FILTER MEDIUM AND THE COMPOSITE FILTER MEDIUM OBTAINED WITH THIS METHOD

Abstract

A method for preparing a composite filter medium, which involves a step of forming a first filter medium by depositing nanofibers on a base fabric by means of an electrospinning process, a subsequent step of forming the filter medium through plasma deposition of a coating on the first filter medium and a step of forming irregularities on the surface of the coating, through plasma treatment of the filter medium obtained in the previous plasma deposition step. With respect to the known filter media, that of the invention offers the advantage of maintaining the desired level of water and oil repellency, without interfering with the secure adhesion of the filter medium to the body on which is located the opening to be protected against liquid infiltration.

Claims

1. A method for preparing a composite filter medium, a step of forming a first filter medium by depositing nanofibers on a base fabric, by means of an electrospinning process, a step of covering said first filter medium by plasma deposition of a coting on said first filter medium, wherein said step of covering said first filter medium is performed after said step of forming said first filter medium, and a step of forming irregularities on the surface of said coating, through plasma treatment of the first filter medium obtained in the plasma deposition step, wherein said step of forming irregularities is performed after said step of covering said first filter medium.

2. The method according to claim 1, wherein the electrospinning process involves extrusion of polymer dissolved in a suitable solvent, by means of a nozzle, and subsequent stretching of fibers between the nozzle and an electrode, thus obtaining a deposition of nanometric fibers on the base fabric, suitably interposed between the nozzle and the electrode, wherein the filter medium thus obtained is subsequently subjected to a surface treatment through plasma deposition of a polymeric layer of nanometric thickness on exposed surfaces of the base fabric and of the nanofiber layer, obtaining the composite filter medium in which external surfaces of monofilaments of the base fabric and of the nanofibers are coated with said polymeric layer, the filter medium thus obtained being subsequently subjected to an additional plasma treatment step in the presence of a carrier gas and without any polymer-containing gas.

3. The method according to claim 2, wherein the plasma deposition treatment comprises creation of a vacuum of 10-50 mTorr, an electrode power of 150-350 W and an exposure time of 0.5-6 minutes.

4. The method according to claim 2, wherein the additional plasma treatment step comprises creation of a vacuum of 10-400 mTorr, an electrode power of 100-2000 W and an exposure time between 5 seconds and 5 minutes.

5. The method according to claim 2, wherein the carrier gas is selected from nitrogen, helium, argon and oxygen.

6. A composite filter medium comprising: a base fabric; and nanofiber deposited on the base fabric, wherein said base fabric and said nanofibers are covered with a nanometric coating layer, applied by means of a plasma process, said coating layer having nanogrooves obtained through plasma treatment in the presence of a carrier gas and without any polymer-containing gas.

7. A filter medium according to claim 6, wherein the coating layer is formed by a film having a thickness of up to 500 nm.

8. A filter medium according to claim 6, wherein the coating layer is a coating based on fluorocarbon acrylates with water- and oil-repelling properties.

9. A filter medium according to claim 6, wherein said monofilaments are made starting from a monofilament of polyester, polyamide, polypropylene, polyether sulfone, polyimide, polyamide imide, polyphenylene sulfide, polyether ether ketone, polyvinylidene fluoride, polytetrafluoroethylene, aramid.

10. A filter medium according to claim 6, wherein the base fabric has a mesh opening of 2500-5 microns.

11. A filter medium according to claim 6, wherein the base fabric has a textile construction of 4-300 threads/cm, thread diameter of 10-500 microns, weave with a weight of 15-300 g/m.sup.2 and thickness of 18-1000 microns.

12. A filter medium according to claim 6, wherein the nanofibers are nanofibers of polyester, polyurethane, polyamide, polyimide, polypropylene, polysulfone, polyether sulfone, polyamide imide, polyphenylene sulfide, polyether ether ketone, polyvinylidene fluoride, polytetrafluoroethylene, alginate, polycarbonate, PVA (polyvinyl alcohol), PLA (polylactic acid), PAN (polyacrylonitrile), PEVA (polyethylene vinyl acetate), PMMA (polymethyl methacrylate), PEO (polyethylene oxide), PE (polyethylene), PVC, PI or polystyrene.

13. A filter medium according to claim 6, wherein said nanofibers have a diameter of between 50 nm and 700 nm.

14. A mobile phone comprising: a body including an opening therein; and a filter medium provided on the body to protect the opening, wherein the filter medium comprises: a base fabric; and nanofibers deposited on the base fabric, wherein said base fabric and said nanofibers are covered with a nanometric coating layer, applied by means of a plasma process, said coating layer having nanogrooves obtained through plasma treatment in the presence of a carrier gas and without any polymer-containing gas.

15. A filter medium according to claim 6, wherein the coating layer is formed by a film having a thickness in the range of 15-60 nm.

16. A filter medium according to claim 6, wherein said nanofibers are PVDF (polyvinylidene fluoride) nanofibers with a diameter ranging from 75 to 200 nm.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0011] These and other objects, advantages and features will be apparent from the following description of a preferred embodiment of the method and the filter medium according to the invention illustrated by way of a non-limiting example in the figures in the attached drawings.

[0012] In these:

[0013] FIG. 1 is a sectional and schematic view of an example of a composite filter medium of the invention;

[0014] FIG. 2 shows a detailed drawing of the nanofibers deposited by electrospinning on a corresponding thread of base fabric, in which both the nanofibers and the threads of the base fabric are all coated with a nanometric layer of water- and oil-repellent polymer, applied by plasma treatment;

[0015] FIG. 3 illustrates the electrospinning method for making a layer of nanofibers in the filter medium of the invention;

[0016] FIG. 4 schematically illustrates the plasma treatment of the filter medium of the invention, obtained by depositing the nanofiber layer made by an electrospinning process on a base fabric;

[0017] FIG. 5 illustrates the relationship between the flow rate and the pressure measured across the filter medium for the dry sample and the wet sample;

[0018] FIG. 6 illustrates the relationship between the emptying pressure and the corresponding pressure drop for the declogging test carried out on two different samples.

DESCRIPTION OF THE PREFERRED EMBODIMENTS

[0019] The composite filter medium of the invention, indicated as a whole by the number 1 in FIG. 1, comprises a support formed by a base fabric 2 of the warp and weft type, preferably a monofilament fabric, on the surface of which nanofibers 4 are deposited by electrospinning. Suitable for the invention are the monofilaments 3 made starting from monofilaments of polyester, polyamide, polypropylene, polyether sulfone, polyimide, polyamide imide, polyphenylene sulfide, polyether ether ketone, polyvinylidene fluoride, polytetrafluoroethylene, aramid, with a mesh opening of the base fabric 2 in a range from 2500 microns to 5 microns.

[0020] The base fabric used in the preparation of the composite filter medium of the invention is selected from a wide range of synthetic monofilament fabrics, which differ in the chemical nature of the monofilament used for weaving, such as polyester, polyamide, polypropylene, polyether sulfone, polyimide, polyamide imide, polyphenylene sulfide, polyether ether ketone, polyvinylidene fluoride, polytetrafluoroethylene, aramid. Also suitable for the invention are base fabrics with textile construction of 4-300 threads/cm, thread diameter of 10-500 microns, weave with a weight of 15-300 g/m.sup.2 and thickness of 18-1000 microns. For finishing and further surface treatments, in addition to metallization, use can be made of washed and heat-set “white” fabric, colored fabric, fabric subjected to plasma treatment, hydrophobic, hydrophilic, antibacterial, antistatic fabric and the like. Preferred for the invention is a polyester monofilament fabric, with 48 threads/cm, diameter 55 μm, mesh opening of the base fabric of 153 μm.

[0021] Suitable for the invention are nanofibers 4 of polyester, polyurethane, polyamide, polyimide, polypropylene, polysulfone, polyether sulfone, polyamide imide, polyphenylene sulfide, polyether ether ketone, polyvinylidene fluoride, polytetrafluoroethylene, alginate, polycarbonate, PVA (polyvinyl alcohol), PLA (polylactic acid), PAN (polyacrylonitrile), PEVA (polyethylene vinyl acetate), PMMA polymethyl methacrylate), PEO (polyethylene oxide), PE (polyethylene), PVC, PEI, PUR and polystyrene. These nanofibers can have a diameter of between 50 nm and 700 nm. PVDF (polyvinylidene fluoride) nanofibers with a diameter ranging from 75 to 200 nm are preferred.

[0022] As illustrated in FIG. 3, the electrospinning process for the formation of the nanofibers 4 and their subsequent deposition on the base fabric 2, consists in injecting the material for the formation of the nanofibers 4, dissolved in a suitable solvent, through a nozzle 5 in order to spread it on an electrode 6. Due to the difference in potential between the nozzle 5 and the electrode 6, the nanofibers 4 are formed through evaporation of the solvent, due to the electric field and stretching of the polymer deposited on the electrode, by means of the nozzle. The nanofibers thus formed are then stretched and subsequently deposited on the base fabric 2.

[0023] The composite filter medium obtained in this way is then subjected to a surface treatment by plasma deposition of a polymeric layer 7 of nanometric thickness on the exposed surfaces of the fabric 2 and of the nanofiber layer 4, completely covering the external surfaces of the monofilaments 3 of the base fabric 2 and of the aforementioned nanofibers 4 (FIG. 2).

[0024] As shown in FIG. 4, the composite filter medium 8, obtained from the previous electrospinning process of FIG. 3, is arranged inside a plasma treatment chamber 9, in the presence of a gas forming the aforementioned coating 7 so as to cover the composite filter medium 1 of the invention.

[0025] Preferred for the invention are gases based on fluorocarbon acrylates, in particular, heptadecafluorodecyl acrylate, perfluorooctylacrylate and the like. Advantageous for the invention are the gases forming by plasma treatment a deposit of fluorocarbon acrylates, due to their water- and oil-repellent properties.

[0026] In the plasma treatment described above, a carrier gas is also used, for example the type described in WO2011089009A1.

[0027] The aforementioned plasma treatment involves the creation of a vacuum of 10-50 mTorr, an electrode power of 150-350 W and an exposure time of 0.5-6 minutes.

[0028] The coating deposited by means of plasma technology can have a thickness of up to 500 nm and, due to the particular technology used, has the structure of a continuous film, capable of coating even 3D surfaces like those of a fabric. Depending on the chemical compound used, the aforementioned coating can have various peculiar characteristics, such as hydrophobicity, oleophobicity, hydrophilicity and antistaticity.

[0029] Preferred for the invention are the coatings obtained starting from the following chemical compounds in the starting gases:

[0030] 1H,1H,2H,2H-HEPTADECAFLUORODECYL ACRYLATE (CAS #27905-45-9, H.sub.2C═CHCO.sub.2CH.sub.2CH.sub.2(CF.sub.2).sub.7CF.sub.3)

[0031] 1H,1H,2H,2H-PERFLUOROOCTYL ACRYLATE (CAS #17527-29-6, H.sub.2C═CHCO.sub.2CH.sub.2CH.sub.2(CF.sub.2).sub.5CF.sub.3)

[0032] The thickness of the coating 7 is 15-60 nm, suitable to prevent it from excessively narrowing the pores that the composite filter medium 1 forms in both the fabric 2 and the nanofibers 4, which would hinder the free passage of sound.

[0033] Tests were carried out on composite filter medium 8, as obtained from the electrospinning process of FIG. 3, compared with the analogous composite filter medium 1 that was subjected to the subsequent plasma treatment of FIG. 4.

[0034] In particular, the aforementioned filter medium 8 is formed by a weft and warp fabric made of synthetic monofilament 3 (for example of polyester), on which nanofibers 4, also made of synthetic material (for example polyester), have been deposited, in order to obtain an acoustic impedance of 25 MKS Rayls, measured with the Textest instrument or similar for measuring the acoustic impedance/air permeability.

[0035] After plasma treatment of the filter medium 8, it can be observed, on the composite filter medium 1 of the invention, that the acoustic impedance remains unchanged at values of 25 MKS Rayls. The air permeability value of 5,200 I/m.sup.2s at a pressure of 200 Pa and the filtration efficiency also remain unchanged.

[0036] On the other hand, a considerable increase is observed both in the angle of contact with water (from 50° to 130°), and in the angle of contact with oil (from 50° to 120° for an oil with corn oil having a surface tension of 32 mN/m), where the angle of contact is measured on a drop of water or oil with the nanofibers 4, using the sessile method with Kruss instruments (drop deposition and measurement of the angle of contact by means of high resolution camera).

[0037] Declogging Test

[0038] In order to provide evidence of the observations set out above, a test method was developed with a view to numerically quantifying the energy necessary to remove the oil deposited on the surface of the composite filter medium of the invention.

[0039] This test was carried out with a porometer (PMI 1200, manufactured by PMI), an instrument that uses capillary flow porometry to determine the bubble point, the minimum pore size and the distribution of the pore size on the sample tested. Capillary flow porometry, or simply porometry, is based on an extremely simple principle: measuring the pressure of a gas necessary to force the passage of a wetting liquid through the pores of the material. The pressure at which the pores empty is inversely proportional to the size of the pores themselves. Large pores require low pressures while small pores require high pressures.

[0040] The test consists in cutting the sample to be analyzed and placing it inside the test chamber. Subsequently the sample is held in position by means of O-rings, in such a way as to be sure there are no lateral air leaks. Once the chamber is closed, the air permeability of the filter medium is measured, obtaining a curve that puts the air flow through the sample in relation with the pressure drop measured across the filter medium (dry curve in the graph in FIG. 5). Once the dry curve has been obtained, the test chamber is opened and, leaving the sample in position, its surface is covered with a test liquid having a low surface tension (typically <20 mN/m). The test chamber is then closed and the air permeability of the material is measured again. As the material is occluded by the test liquid, the pressure will increase, but no air flow will be measured downstream, until the pressure is high enough to force the liquid to pass through the pores. From this moment on, the pores of decreasing size will be emptied with increasing pressure values until the sample (previously wet) is completely dry and the two curves of FIG. 5 overlap. Without going into analytical details, on a qualitative level, from the difference between the two curves, the bubble point value (largest pore), the size of the smallest pore and the distribution of the pore size can be determined.

[0041] In the specific case, in order to determine the oil repellency/removal call) pacity, this test was carried out but using corn oil (surface tension 32 mN/m) in place of the test liquid.

[0042] The graph in FIG. 6 shows the emptying pressure and the corresponding pressure drop (energy required for emptying). The samples considered in the graph in FIG. 6 are the filter medium 8 from electrospinning treatment (curve 10) and the filter medium 1 of the invention (curve 11). It can be seen that with the filter medium 1 of the invention, the oil can be removed at decidedly lower pressures or, at the same pressure, a decidedly larger amount of oil is removed than with the composite filter medium 8, which has not undergone the plasma treatment.

[0043] According to the invention, it has now surprisingly been discovered that, by adding to the method described above a further step of plasma treatment of the composite filter medium 1 coated with the polymeric layer 7, this time, however, in the presence of the carrier gas only and therefore without the gas forming the aforementioned polymeric coating 7, the same filter medium exhibits not only the desired degree of repellency to water and oily liquids but also an excellent level of adhesion to the PSA layer.

[0044] In fact, the method of the invention comprises an additional step of plasma treatment of the filter medium 1 provided with polymeric coating 7, that is, after the described deposition of said coating, but this time without the polymer-containing gas.

[0045] During this additional step, a suitable working pressure is set inside the plasma treatment chamber 9 (10-400 mTorr), an electrode power of 100-2000 W and an exposure time of 5 seconds to 5 minutes, within which a carrier gas is injected, preferably selected from nitrogen, helium, argon and oxygen.

[0046] In this step and given the inert nature of the gas used, the material constituting the filter medium does not undergo any further coating process. The ions of the carrier gas that are formed during the plasma treatment impact, with some energy, on the surface of the coating 7 deposited in the previous step, thus reactivating the latter and creating surface irregularities, for example in the form of microcorrugations or nanogrooves that favor the adhesion of the polymeric coating 7 to the PSA adhesive layer.

[0047] Although, on the one hand, the action undergone by this coating affects its integrity and continuity, consequently modifying its surface energy value and reducing, though not significantly, the level of water and oil repellency of the filter medium, on the other, the adhesive strength of the filter medium to the PSA layer is considerably increased, reaching a satisfactory compromise between the water/oil repellency and workability of the filter medium.

[0048] In fact, the filtering system obtained using the described method of the invention ensures a very large angle of contact with oil (130-135°), with which the known technique normally associates a very low value of adhesion with the PSA, thus jeopardizing the correct seal and the ease of assembly of the “die cut parts”.

[0049] The results offered by the filter medium prepared with the method of the invention are shown in the following table, the values of which were measured on a filter medium having a layer 7 of polymeric material, subsequently subjected to a plasma treatment carried out in the presence of helium as a carrier gas, with a vacuum of 100 mTorr, an electrode power of 700 W and an exposure time of 2 minutes:

TABLE-US-00001 Minimum angle of Angle contact Minimum of required Adhesion level of contact for the level to adhesion with application PSA required oil (°) (°) (gf/20 mm) (gf/20 mm) Electrospinning 130-135 110  20 100 process + plasma deposition Electrospinning 115 110 220 100 process + plasma deposition + plasma treatment of the coating deposited in the previous step
where “gf/20 mm” represents the value in gram-force of adhesion of the filter medium on a 20 mm wide PSA sample.

[0050] From these results it can be observed that, after the additional step of plasma reactivation of the polymer coating 7 formed in the previous step, the filter medium thus obtained achieves both very large angles of contact with oil (>110°), and a much higher adhesion level with PSA than the minimum required, i.e. 100 gf/mm.