NANO-FUNCTIONALIZED SUPPORT AND PRODUCTION METHOD THEREOF

Abstract

A nano-functionalized support (1) comprises an application surface (2) and a photocatalytic nanoparticle coating (3) deposited on the application surface (2). The photocatalytic nanoparticle coating (3) comprises titanium dioxide doped with a nitrogen-containing doping agent.

Claims

1-13. (canceled)

14. A nano-functionalized support comprising an application surface and a photocatalytic nanoparticle coating deposited on said application surface, wherein said application surface has a honeycomb structure and said photocatalytic nanoparticle coating comprises titanium dioxide doped with nitrogen deriving from a nitrogen-containing doping agent.

15. The support according to claim 14, wherein the honeycomb structure defines a plurality of channels suitable for passage of a gaseous mixture.

16. The support according to claim 14, wherein said application surface having a honeycomb structure is characterized by a CSPI value of 40 to 120.

17. The support according to claim 14, wherein the application surface is made of a ceramic material.

18. The support according to claim 17, wherein the ceramic material is at least one selected from the group consisting of cordierite, mullite and alumina.

19. The support according to claim 14, wherein the nitrogen-containing doping agent is one selected from the group consisting of amines, amides, organic ammonium salts and inorganic ammonium salts.

20. A device for abating polluting agents in a gaseous mixture, comprising at least one nano-functionalized support according to claim 14, and a light source of visible light.

21. A method for abating polluting agents in a gaseous mixture and comprising the steps of: arranging a device for abating polluting agents according to claim 20; subjecting said device for abating polluting agents to a flow of a gaseous mixture; illuminating the at least one nano-functionalized support by means of a beam of visible light.

22. The support according to claim 16, wherein said honeycomb application surface is characterized by a CSPI value of 50 to 100.

23. The support according to claim 16, wherein said honeycomb application surface is characterized by a CSPI value of 50 to 70.

24. The support according to claim 16, wherein said honeycomb application surface is characterized by a CSPI value of 55 to 65.

25. The method of claim 21, wherein the means of the light source of visible light is contained within the device.

Description

BRIEF DESCRIPTION OF THE FIGURES

[0022] Further characteristics and advantages of the present invention will become more apparent from the indicative and thus non-limiting description of a preferred, but not exclusive, embodiment of a nano-functionalized support, as illustrated in the accompanying drawings, of which:

[0023] FIG. 1 shows a nano-functionalized support according to the present invention;

[0024] FIG. 2 shows a detail of a nano-functionalized support;

[0025] FIG. 3 is a block diagram of a method for producing a nano-functionalized support;

[0026] FIG. 4 is a graph showing the abatement trend for the polluting agents (NO, NO.sub.x, NO.sub.2) by means of irradiation of the sample prepared as per Example D, said irradiation being performed with a COOL WHITE LED with a power of 25 W;

[0027] FIG. 5 is a graph showing the abatement trend for the polluting agents (NO, NO.sub.x, NO.sub.2) by means of irradiation of the sample prepared as per Example L, said irradiation being performed with a COOL WHITE LED with a power of 25 W;

[0028] FIG. 6 is a graph showing the abatement trend for the polluting agents (NO, NOx, NO2) by means of irradiation of the sample prepared by accurately following the process of the prior art as described for Example M, said irradiation being performed with a COOL WHITE LED with a power of 25 W.

[0029] In FIG. 1, a nano-functionalized support that is installable for example inside an air filter is indicated in general by the number 1.

DETAILED DESCRIPTION OF THE INVENTION

[0030] The term nano-functionalized is used to indicate that the support has a coated surface, preferably homogeneously coated, with nanoparticles that have photocatalytic properties which are suitable for facilitating the degradation of polluting substances, principally by means of oxidation processes.

[0031] The support 1 comprises an application surface 2 and a photocatalytic nanoparticle coating 3 configured to be deposited on the application surface 2.

[0032] The nanoparticle coating 3 is realized by deposition of a suspension of photocatalytically active nanoparticles, preferably comprising nanoparticles of titanium dioxide doped with nitrogen, in which the nanoparticles are in the anatase crystalline form.

[0033] Prior to application to the support 2, the nanoparticle coating 3 is doped by means of a nitrogen-containing doping agent.

[0034] In other words, the application surface 2 is coated with titanium dioxide in the form of nanoparticles doped with nitrogen.

[0035] In particular, the precursor utilized as the nitrogen-containing doping agent is preferably selected from among: amines, amides, organic ammonium salts and inorganic ammonium salts.

[0036] The presence of nitrogen makes it possible to modify the band gap energy of the titanium dioxide, specifically to reduce it, making its photocatalytic properties activatable using a broad range of the visible light spectrum and not only with the very limited ultraviolet component as takes place for example in devices of the prior art.

[0037] Preferably, the application surface 2 is made of a ceramic material, which proves to be particularly suitable in that it provides an inert and very resistant support, thus ensuring long lifetimes for the devices in which it is used.

[0038] Even more preferably, the application surface is realized using at least one of: cordierite, mullite and/or alumina.

[0039] For the purpose of ensuring optimal filtering results and maximizing the efficiency of the support 1, the application surface 2 is realized by means of a matrix with thin ceramic walls that define a honeycomb structure constituted by a plurality of parallel channels that are open at both ends so as to enable the passage of a gaseous mixture. This honeycomb application surface (also called the honeycomb surface) is characterized by a CSPI (cells per square inch) value of 40 to 120, preferably 50 to 100, more preferably 50 to 70, even more preferably 55 to 65. In other words, the application surface 2 has a plurality of channels, each of which is coated with a nanoparticle coating 3, thus defining a plurality of oxidation sites in which, by means of the activation of the photocatalytic properties of the titanium dioxide nanoparticles doped with a nitrogen-containing doping agent, on the part of an incident photon, the environmental pollutants are adsorbed and degraded, obtaining purification of the gaseous mixture, particularly air, passing through the channels of the application surface 2.

[0040] For example, the nitrogen oxides undergo degradation to nitrates, whereas other volatile organic substances are oxidized forming carbon residues and/or carbon dioxide.

[0041] The sub-products resulting from filtration of the air can easily be washed away from the application surface 2, completely restoring the operating state thereof.

[0042] The nano-functionalized support 1 of the present invention thus proves to be particularly suited to incorporation in a device for abating polluting agents in a gaseous mixture such as air for example.

[0043] A method 10 for producing a nano-functionalized support 1 according to that which is described hereinabove also constitutes an object of the present invention.

[0044] The method 10 comprises the steps of: synthesizing 11 an aqueous suspension of nanoparticles of titanium dioxide; adding 12 a nitrogen-containing doping agent to the suspension, realizing a suspension of nanoparticles and the nitrogen-containing doping agent; applying 13 the suspension to the application surface 2, realizing a nano-functionalized support 1; subjecting 14 the support 1 to a heating cycle.

[0045] Preferably, in step 11, the aqueous suspension of the nanoparticles of titanium dioxide in anatase form is prepared according to that which is disclosed in patent WO2007088151. In particular, a titanium alkoxide is made to react under heat in water in the presence of a mineral acid and a non-ionic surfactant.

[0046] The starting material for the synthesis of the aqueous suspension of nanoparticles of titanium dioxide in anatase form is chosen from the substances of the group of titanium alkoxides. In particular, the alkoxide can be selected from among titanium methoxide, titanium ethoxide, titanium normal-propoxide, titanium isopropoxide, titanium normal-butoxide, and titanium isobutoxide. In a preferred embodiment, the titanium alkoxide selected is titanium isopropoxide (TIP) as it is less expensive and reacts more efficiently under the reaction conditions of the present synthesis.

[0047] Examples of non-ionic surfactants that can be used are: non-ionizable ethers, esters and ether esters. The use of Triton X-100 (TX-100) is particularly preferred for the present synthesis.

[0048] Mineral acid means an acid selected from among: hydrochloric acid, nitric acid, sulphuric acid, perchloric acid, hydrobromic acid and hydrogen iodide. In a preferred embodiment, the mineral acid used is selected from among hydrohalic acids, particularly hydrochloric acid.

[0049] The titanium alkoxide/mineral acid molar ratio is in the range of 0.005 to 15, preferably 5 to 6.

[0050] The reaction temperature ranges between 15 and 95° C., preferably between 45 and 55° C., and the reaction time ranges between 12 and 72 hours, and it is preferably equal to 24 hours.

[0051] The product obtained is an aqueous suspension of TiO.sub.2 nanoparticles in the anatase phase with sizes ranging between 30 and 50 nm measured with methods known in the sector, such as FEG-SEM (Field Emission Gun Scanning Electron Microscopy), TEM (Transmission Electron Microscopy) and DLS (Dynamic Light Scattering). The polydispersity index of the nanoparticles, as measured with the DLS technique, is lower than 0.3, preferably ranging between 0.21 and 0.29, and more preferably between 0.216 and 0.286. The concentration of TiO.sub.2 nanoparticles suspended in water ranges between 1 and 10% by weight, preferably between 2 and 8% by weight.

[0052] The suspension of nanoparticles is stable for very long periods of time without the appearance of coagulation and conglomeration phenomena. Subsequently, in step 12, a nitrogen-containing doping agent is added to said aqueous suspension of titanium dioxide nanoparticles, said nitrogen-containing doping agent being suitably selected from among: amines, amides, organic ammonium salts and inorganic ammonium salts.

[0053] Some possible operating parameters for realizing the doped suspension are reported below by way of non-limiting example.

[0054] Example A: 5.00 g of concentrated hydrochloric acid, 7.50 g of TX-100 and water, for a total of 750.00 g, are mixed in a 2-litre reactor and heated to 50° C. 50.00 g of titanium isopropoxide (TIP) are added and the formation of a white precipitate is observed. A stable transparent sol of titanium dioxide is formed after 24 hours.

[0055] Example B: 97.81 g of an aqueous suspension of titanium dioxide obtained as described for Example A and 2.00 g of diethanolamine are mixed in a 200 ml beaker, the temperature is set at 25° C., and after eighteen hours of mixing an opalescent white solution is obtained with a 5.87% reduction by weight of titanium dioxide and 0.27% reduction by weight of nitrogen.

[0056] Example C: 97.00 g of an aqueous suspension of titanium dioxide obtained as described for Example A and 4.07 g of diammonium citrate are mixed in a 200 ml beaker, the temperature is set at 25° C., and after twenty-four hours of mixing an opalescent white solution is formed with a 5.76% reduction by weight of titanium dioxide and a 0.49% reduction by weight of nitrogen.

[0057] Example D: 90.0 g of the suspension obtained as described for Example C were applied with the flow-coating technique on a 150×150×20 cm support of ceramic material with a honeycomb structure. Said procedure comprises the application of the suspension on the support, said suspension being drawn from a tank by a pump and said support being positioned above a rack so that the excess material can be collected and reused.

[0058] The support thus prepared was subjected to a firing cycle in a continuous electric furnace at 500° C. for three hours with the belt speed set at 4 m/h. After firing, the amount of doped titanium dioxide deposited was equal to 5.8 g. A sample with dimensions of 77×77×20 cm was obtained from this support and a pollutant abatement test (for NO, No.sub.x, NO.sub.2) was carried out with this sample (see FIG. 4), using a COOL WHITE LED with a power of 25 W as the light source.

[0059] Example E: 97.00 g of an aqueous suspension of titanium dioxide obtained as described for Example A and 4.00 g of tetrabutylammonium hydroxide are mixed in a 200 ml beaker and the temperature is set at 25° C.; after twenty-four hours of mixing an opalescent white solution is formed with a 5.76% reduction by weight of titanium dioxide and a 0.085% reduction by weight of nitrogen.

[0060] Example F: 97.00 g of an aqueous suspension of titanium dioxide obtained as described for Example A and 6.00 g of tetrabutylammonium hydroxide are mixed in a 200 ml beaker and the temperature is set at 25° C.; after twenty-four hours of mixing an opalescent white solution is formed with a 5.65% reduction by weight of titanium dioxide and a 0.125% reduction by weight of nitrogen.

[0061] Example G: 49.49 g of an aqueous suspension of titanium dioxide obtained as described for Example A and 0.53 g of urea are mixed in a 200 ml beaker and the temperature is set at 25° C.; after twenty-four hours of mixing an opalescent white solution is formed with a 5.93% reduction by weight of titanium dioxide and a 0.498% reduction by weight of nitrogen.

[0062] Example H: 49.49 g of an aqueous suspension of titanium dioxide obtained as described for Example A and 1.06 g of urea are mixed in a 200 ml beaker; the temperature is set at 25 C and after one hour of mixing an opalescent white solution is formed with a 5.87% reduction by weight of titanium dioxide and a 0.980% reduction by weight of nitrogen.

[0063] Example I: 86.21 g of an aqueous suspension of titanium dioxide obtained as described for Example A and 13.79 g of triethanolamine are mixed in a 200 ml beaker; the temperature is set at 25° C. and after four hours of mixing an opalescent white solution is formed with a 5.17% reduction by weight of titanium dioxide and a 1.29% reduction by weight of nitrogen.

[0064] Example L: 125.0 g of the suspension obtained as described for Example I were applied with the flow-coating technique on a 150×150×20 cm support of ceramic material with a honeycomb structure. Said procedure comprises the application of the suspension on the support, said suspension being drawn from a tank by a pump and said support being positioned above a rack so that the excess material can be collected and reused.

[0065] The support thus prepared was subjected to a firing cycle in a continuous electric furnace at 500° C. for 3 hours with the belt speed set at 4 m/h. After firing, the amount of doped titanium dioxide deposited was equal to 8.2 g. A sample with dimensions of 77×77×20 cm was obtained from this support and a pollutant abatement test (for NO, NO.sub.x, NO.sub.2), shown in FIG. 5, was carried out with this sample, using a COOL WHITE LED with a power of 25 W as the light source.

Example M (Comparative Experiment)

[0066] A TiO.sub.2 sol containing urea as a source of nitrogen was synthesized by accurately reproducing the steps described in section 2.1 of the paper by M. Tahir et al. (M. Tahir, B. Tahir, Applied Surface Science 377 (2016) 244-252). By means of the flow-coating technique, said sol was then applied onto a 150×150×20 cm support of ceramic material with a honeycomb structure. The support thus prepared was subjected to a firing cycle in a continuous electric furnace at 500° C. for 3 hours with the belt speed set at 4 m/h. After firing, the amount of doped titanium dioxide deposited was equal to 2.88. However, following this step, a problem was found concerning the presence of a considerable amount of loose, doped titanium dioxide powder not adhering to the surface of the support.

[0067] For this reason, prior to the analysis, washing with water had to be carried out so as to eliminate the loose powder and prevent it from spreading into the environment (which is potentially hazardous for the health of operators), as well as to ensure better handleability of the support. The washing procedure led to the elimination of a large amount of non-adherent doped titanium dioxide powder resulting in considerable losses and waste of the product. A sample with dimensions of 77×77×20 cm was obtained from this washed support and a pollutant abatement test (for NO, NO.sub.x, NO.sub.2) was carried out with this sample (see FIG. 6), using a COOL WHITE LED with a power of 25 W as the light source.

[0068] These results were compared with the results obtained with the nano-functionalized support of the present invention obtained as described for Example D, shown in FIG. 4. The graph showing the trend for the polluting agents in FIG. 6 shows a convex trend and not a concave trend as in the case of the graph in FIG. 4. It can thus be noted from the comparison of the curves in the two graphs that the photocatalytic efficiency of the washed support obtained according to the process of the prior art proves to be weaker than that of the support of the present invention. In fact, in the case of the support obtained with the prior-art process, after 50 minutes of irradiation, the concentration of NO and NO.sub.x is around the level of 300 ppbv, whereas in the case of the nano-functionalized support of the present invention, the concentration proves to be around the level of 200 ppbv.

[0069] The application step 13 comprises a first substep of applying 13a the suspension of nanoparticles of titanium dioxide and nitrogen-containing doping agent to the application surface 2, for example by means of a spraying process, and a second substep of applying 13b a flow of compressed air on the application surface 2 so as to remove excess deposited nanoparticle coating 3.

[0070] Alternatively, the doped suspension can be applied by means of dip coating or flow coating processes, or applications typical of the ceramics field such as veil-glazing, screen printing, bell-glazing, air brushing or digital injection.

[0071] In particular, after the support 1 has rested for a period of time, the heating cycle in the step of subjecting 14 the support 1 to a heating cycle is carried out, heating it to a temperature between 490° C. and 510° C.

[0072] During the heating cycle (also called the calcination step), the doping of the titanium dioxide with nitrogen from the nitrogen-containing doping agent takes place. Doping of the TiO.sub.2 with nitrogen takes place during the calcination step and the nitrogen penetrates the TiO.sub.2 nanoparticles, positioning itself in a substitutional position inside the TiO.sub.2 lattice and/or in an interstitial position, that is, inside the crystalline planes of TiO.sub.2 lattice. In the case in which a static furnace is used, the heating cycle is preferably carried out with a temperature variation coefficient of 50° C./h for a period of ten hours, reaching a maximum temperature of about 500° C. However, in the case in which a continuous run furnace is used, a 3-hour heating cycle can be implemented, with a preheating step, a 500° C. heating step and a cooling step, with a running speed of about 4 m/h.

[0073] In general, it can be noted that the heating cycle is of a duration substantially ranging from 2 to 11 hours, depending on the type of heating device used.

[0074] A further object of the present invention is a method for the abatement of polluting agents in a gaseous mixture, starting with a step of arranging a device for abating polluting agents, said device comprising at least one nano-functionalized support 1, in accordance with that which is disclosed above, and possibly a light source of visible light.

[0075] The method further comprises subjecting the device to a flow of a gaseous mixture and illuminating the at least one nano-functionalized support 1 by means of a beam of visible light.

[0076] By illuminating the support, the photocatalytic properties of the nanoparticle coating 3 present on the application surface can be activated. Owing to the particular production method used to produce the support 1, the photocatalytic properties of titanium dioxide prove to be activated by a broad range of wavelengths in the visible light spectrum and not only by the component of the ultraviolet region of the spectrum.

[0077] Therefore, when the flow of air travels through the nano-functionalized structure 1, the polluting agents contained in it are oxidized, thereby obtaining an improvement in the quality of the air exiting the device.

[0078] Advantageously, the particular method for producing a nano-functionalized support 1 makes it possible to achieve optimal doping of titanium dioxide. Furthermore, the presence of nitrogen ensures activation of the photocatalytic properties of the titanium dioxide nanoparticles also with photons having wavelengths in the visible light region, thereby making it possible to maximize the photocatalytic activity of the nano-functionalized support 1.