JP2011088037A - Method for producing thermal spray material and method for producing thermally-sprayed coating film - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for producing a thermal spray material capable of exhibiting the performance of a photocatalyst satisfactorily. <P>SOLUTION: The method for producing the thermal spray material comprises steps of: mixing photocatalyst particles, which include titanium dioxide particles each having 10-1,000 nm particle size and agglomerates thereof, with water to produce slurry having 10-30 mass% photocatalyst concentration; and irradiating the slurry with the ultrasound having 28-40 kHz frequency for 2-7 hours to enlarge the particle size of the photocatalyst particles included in the slurry to 1-50 μm. <P>COPYRIGHT: (C)2011,JPO&INPIT

Description

  The present invention relates to a thermal spray material manufacturing method and a thermal spray coating manufacturing method. Specifically, for example, the present invention relates to a method for producing a thermal spray material having a photocatalytic function capable of detoxifying, antibacterial, and sterilizing contaminants, and a method for producing a thermal spray coating using such a thermal spray material.

  Due to the progress of an aging society, the proportion of elderly people with reduced immunity in the total population is increasing, and accordingly, from the viewpoint of prevention of nosocomial infections, food poisoning, etc., in the medical field, food production and processing field Strengthening hygiene management is an urgent issue. In response to this social background, various antibacterial processed products have been developed, and in recent years, the use of a photocatalytic function for antibacterial processing has attracted particular attention.

  Here, the “photocatalytic function” refers to a catalyst that is excited when irradiated with light energy larger than the band gap energy of its conduction band and valence band, and generates an electron-hole pair to cause oxidation and reduction reactions. This means the function of the substance (photosemiconductor substance).

Among photocatalysts, photocatalysts using titanium dioxide (TiO ₂ ) in particular are inexpensive, excellent in chemical stability, and have high catalytic activity. Due to their powerful organic substance decomposing activity, At the same time, it can decompose toxic substances such as endotoxin, which is an outer cell wall component of Gram-negative bacteria, and toxins produced by bacteria (for example, verotoxin produced by pathogenic E. coli), and the photocatalyst itself is harmless to the human body. Has the advantage of being.

  Therefore, research and application of photocatalysts using titanium dioxide have been performed, and titanium dioxide photocatalysts are widely used for antibacterial processing of food containers, building materials, and the like (see, for example, Patent Document 1 and Patent Document 2).

  Since titanium dioxide exhibits photocatalytic activity only under ultraviolet irradiation, it cannot exhibit sufficient catalytic activity under room light containing almost no ultraviolet component. Therefore, titanium dioxide doped with atoms such as nitrogen, carbon and sulfur in the crystal lattice has been proposed as a photocatalyst exhibiting photocatalytic activity under visible light irradiation. In particular, sulfur-doped titanium dioxide absorbs light in the visible light region. It is known that it has a high coefficient and high catalytic activity under visible light (for example, see Patent Document 3).

  Various methods have been proposed as such photocatalyst film formation methods. As a specific method for producing a titanium dioxide photocatalyst film, a solution method such as a sol-gel method, a sputtering method, an ion cluster beam method, a CVD (chemical vapor deposition) method, a thermal spraying method (for example, see Patent Document 4), and the like. A dry method can be mentioned.

  Among the photocatalyst film-forming methods described above, the thermal spraying method (1) does not require expensive vacuum equipment, (2) can form a photocatalyst having excellent adhesion strength on the surface of various substrates, and (3) It has many advantages such as being applicable to large-area film formation.

  By the way, when a photocatalyst film is formed by a thermal spraying method, if the particle size of the thermal spray material is less than 1 μm, the mass is too small, so there is a concern that the collision energy to the substrate during thermal spraying is small and the yield is lowered. Is done.

  In consideration of the case where the thermal spray material is titanium dioxide, titanium dioxide has an anatase type and rutile type crystal structure, and anatase type titanium dioxide is more preferable than rutile type titanium dioxide. However, although it is known that it exhibits a high photocatalytic function, if the particle size of the sprayed material is less than 1 μm, the heat capacity is too small, and there is a concern that the anatase content may be reduced by the heat of spraying.

  Therefore, a technique has been proposed in which a photocatalyst fine particle is mixed with a binder (binder) such as polyvinyl alcohol, and the particle diameter of the photocatalyst particle, which is a thermal spray material, is granulated to 1 μm or more. By using such a technique, 1 μm or more is proposed. The photocatalyst particles having a particle size of are granulated.

  In the following, material particles provided by a material manufacturer are referred to as “primary particles”, an aggregate of a plurality of primary particles is referred to as “secondary particles”, and primary particles and secondary particles are coarsened by granulation. The particles are referred to as “tertiary particles”.

JP 2007-51263 A JP 2006-346651 A JP 2004-143032 A JP 2006-51439 A

  However, in the granulation method in which the binder is mixed, the purity of the photocatalyst in the sprayed material decreases, the binder interferes with the contact between the photocatalyst and the harmful substance (decomposable substance), and light is emitted to the photocatalyst. It becomes difficult to hit. Furthermore, it is conceivable that the decomposition energy of the photocatalyst is used as energy for decomposing the binder.

  Thus, when a binder is mixed in the thermal spray material, the performance of the photocatalyst is degraded due to a decrease in the purity of the photocatalyst.

  The present invention was devised in view of the above points, and provides a method for producing a thermal spray material capable of sufficiently exhibiting the performance of a photocatalyst and a method for producing a thermal spray coating using such a thermal spray material. It is intended.

  In order to achieve the above object, in the method for producing a thermal spray material according to the present invention, photocatalyst particles (primary particles and secondary particles) and water are mixed to produce a slurry, and ultrasonic waves are applied to the slurry. Irradiating and coarsening the particle size of the photocatalyst particles contained in the slurry to 1 μm to 50 μm.

  In order to achieve the above object, in the method for producing a thermal spray coating according to the present invention, a step of producing a slurry by mixing photocatalyst particles (primary particles or secondary particles) and water; A step of producing a thermal spray material by irradiating a sound wave to increase the particle size of the photocatalyst particles contained in the slurry to 1 μm to 50 μm, and a step of performing thermal spraying of the thermal spray material.

  Moreover, in the manufacturing method of the sprayed coating which concerns on this invention, the aggregate (secondary particle) of the photocatalyst particle (primary particle) with a particle size of 10 nm-1000 nm or the photocatalyst particle (primary particle) with a particle size of 10 nm-1000 nm A step of mixing at least one of water and water to produce a slurry having a photocatalyst concentration of 10% by mass to 30% by mass, and irradiating the slurry with ultrasonic waves having a frequency of 28 kHz to 40 kHz for 2 hours to 7 hours. The method includes the steps of producing a thermal spray material by coarsening the particle size of the photocatalyst particles contained in the slurry to 1 μm to 50 μm, and performing the thermal spraying of the thermal spray material.

  Further, in the method for producing a thermal spray coating according to the present invention, a step of producing a slurry by mixing photocatalyst particles (primary particles or secondary particles) containing anatase-type titanium dioxide particles and water, and ultrasonicating the slurry. , The step of producing a thermal spray material by coarsening the particle size of the photocatalyst particles contained in the slurry to 1 μm to 50 μm, and controlling the transformation of the anatase type titanium dioxide into the rutile type while controlling the thermal spray material And a step of performing thermal spraying.

  In the method for producing a sprayed coating according to the present invention, photocatalyst particles (primary particles) containing anatase-type titanium dioxide particles having a particle size of 10 nm to 1000 nm or anatase-type titanium dioxide particles having a particle size of 10 nm to 1000 nm At least one of aggregates (secondary particles) of photocatalyst particles (primary particles) containing water and water to produce a slurry having a photocatalyst concentration of 10% by mass to 30% by mass, and a frequency of 28 kHz in the slurry A process of producing a thermal spray material by irradiating a ultrasonic wave of ˜40 kHz for 2 hours to 7 hours to increase the particle size of the photocatalyst particles contained in the slurry to 1 μm to 50 μm, and anatase type titanium dioxide is a rutile type And spraying the sprayed material while controlling the transformation into a heat treatment.

  Here, by irradiating the slurry with ultrasonic waves, the particle size of the photocatalyst particles contained in the slurry can be increased without reducing the purity of the photocatalyst in the thermal spray material.

  The reason why the particle size of the photocatalyst particles (tertiary particles) is 1 μm or more is that the mass is too small if the particle size is less than 1 μm, so that the collision energy to the base material at the time of thermal spraying is small and the yield decreases. This is because of concern. In consideration of the case where the thermal spray material is titanium dioxide, if the particle size of the photocatalyst particles (tertiary particles) is less than 1 μm, the heat capacity is too small, and there is a concern that the anatase content may be reduced by the thermal spray heat. It is.

  Furthermore, the particle size of the photocatalyst particles (tertiary particles) is 50 μm or less. If the particle size exceeds 50 μm, sufficient acceleration cannot be performed before the collision with the substrate, and the spray particle velocity is low. This is because the yield is reduced due to crushing in the collision with the base material and causing the dispersion to break.

  Here, when the particle diameter of the photocatalyst particles (primary particles) is less than 10 nm, it is considered that the photocatalytic function is deteriorated due to the influence of heat of spraying. For example, when the particle diameter of titanium dioxide is less than 10 nm, it is conceivable that the anatase content decreases due to the influence of thermal spraying. Accordingly, the particle diameter of the photocatalyst particles (primary particles) is preferably 10 nm or more.

  In addition, when the particle diameter of the photocatalyst particles (primary particles) is larger than 1000 nm, the specific surface area of the photocatalyst particles (primary particles) becomes small, and it is considered that the organic substance decomposition performance such as gas decomposition performance decreases. . Accordingly, the particle diameter of the photocatalyst particles (primary particles) is preferably 1000 nm or less.

  Furthermore, when the photocatalyst concentration of the slurry is less than 10% by mass, since the amount of the photocatalyst material sprayed at a time is small, it is considered that the thermal spraying efficiency is poor and the yield and the deposition efficiency are lowered. Therefore, the photocatalyst concentration of the slurry is preferably 10% by mass or more.

  Moreover, when the photocatalyst density | concentration of a slurry exceeds 30 mass%, it will be excessive with respect to a thermal spraying process capability, and it is thought that thermal spraying efficiency falls. Moreover, the risk of clogging and the like occurring when supplying the thermal spray material due to an increase in viscosity is also increased. Therefore, the photocatalytic concentration of the slurry is preferably 30% by mass or less.

  In addition, when the frequency of the ultrasonic wave applied to the slurry is less than 28 kHz, the action acts in the direction of crushing the photocatalyst particles (secondary particles) by the ultrasonic irradiation, and the photocatalyst particles (secondary particles) become coarse. It is conceivable that the device will be miniaturized without the use of this. Therefore, it is preferable that the frequency of the ultrasonic wave applied to the slurry is 28 kHz or more.

  On the other hand, if the frequency of the ultrasonic wave applied to the slurry exceeds 40 kHz, it takes a long time to coarsen the photocatalyst particles (primary particles and secondary particles), resulting in poor efficiency. Therefore, it is preferable that the frequency of the ultrasonic wave irradiated to the slurry is 40 kHz or less.

  Moreover, when the irradiation time of the ultrasonic wave to the slurry is less than 2 hours, it is considered that the effect of coarsening the photocatalyst particles (primary particles and secondary particles) cannot be obtained. Therefore, it is preferable that the ultrasonic irradiation time to the slurry is 2 hours or more.

  Further, even if the ultrasonic wave irradiation time on the slurry exceeds 7 hours, it is considered that there is no significant influence on the effect of coarsening. Therefore, it is preferable that the ultrasonic irradiation time to the slurry is 7 hours or less.

  In the thermal spray material manufacturing method to which the present invention is applied, the photocatalyst particles can be coarsened without reducing the purity of the photocatalyst in the thermal spray material. Moreover, in the manufacturing method of the thermal spraying film to which this invention is applied, the thermal spray material coarsened without reducing the purity of the photocatalyst in material is used, and a high adhesion rate and high photocatalytic performance can be obtained.

It is a flowchart for demonstrating the process of an example of the manufacturing method of the thermal spray coating to which this invention is applied. It is a graph which shows the particle size distribution of the photocatalyst microparticles | fine-particles in the slurry before and behind ultrasonic irradiation.

  Hereinafter, modes for carrying out the invention (hereinafter referred to as “embodiments”) will be described with reference to the drawings.

  FIG. 1 is a flowchart for explaining a process of an example of a manufacturing method of a thermal spray coating to which the present invention is applied. In an example of a method of manufacturing a thermal spray coating to which the present invention is applied, (1) a slurry generation process, (2) It consists of three processes: an ultrasonic irradiation process and (3) a thermal spray coating formation process. Hereinafter, each process will be described in detail.

<1. Slurry production process>
In an example of a method for producing a thermal spray coating to which the present invention is applied, first, photocatalyst fine particles comprising anatase-type titanium dioxide particles having a particle size of 10 nm to 1000 nm doped with at least one of nitrogen, carbon and sulfur atoms in the crystal lattice (Primary particles) and an aggregate of these primary particles (secondary particles) and water are mixed to produce a slurry having a photocatalyst concentration of 10% by mass to 30% by mass.

  Here, in the present embodiment, the case of using photocatalyst fine particles including titanium dioxide particles doped with at least one of nitrogen, carbon, and sulfur atoms in the crystal lattice will be described as an example. It is not necessary for at least one of carbon and sulfur atoms to be doped in the crystal lattice, and photocatalytic fine particles other than titanium dioxide may be used.

  However, considering that it is inexpensive, excellent in chemical stability, and has high catalytic activity, it is preferable to employ titanium dioxide as a photocatalyst, and it is sufficient even under room light containing almost no ultraviolet component. Considering that catalytic activity can be expressed, it is preferable that at least one of nitrogen, carbon, and sulfur atoms is doped in the crystal lattice.

  Further, in the present embodiment, the case where a slurry is formed by mixing primary particles and secondary particles with water is described as an example, but only the primary particles and water are mixed to form a slurry. It may be formed, or only secondary particles and water may be mixed to form a slurry.

[Regarding the particle size of primary particles]
Table 1 shows a case where a thermal spray coating is formed using photocatalyst fine particles (primary particles) containing titanium dioxide having a particle diameter of 7 nm (indicated by symbol a in Table 1), and titanium dioxide having a particle diameter of 200 nm. The relationship between a calcination temperature and an anatase content rate is shown about the case where a thermal spray coating is formed into a film using the photocatalyst fine particle (primary particle) containing (it shows with the code | symbol b in Table 1).

  Table 2 shows a case where a thermal spray coating is formed using photocatalyst fine particles (primary particles) containing titanium dioxide having a particle diameter of 7 nm (indicated by symbol a in Table 2), and a carbon dioxide having a particle diameter of 200 nm. The relationship between time and the concentration of a substance to be decomposed is shown for a case where a thermal spray coating is formed using photocatalyst fine particles (primary particles) containing titanium (indicated by symbol b in Table 2).

  From Table 1, it can be seen that when the particle size of the primary particles is small, it is easily affected by the heat of thermal spraying, and the anatase content decreases even if the firing temperature is the same. Also, from Table 2, when comparing the decomposition activity of “sprayed coating formed with primary particles having a particle size of 7 nm” and “sprayed coating formed with primary particles having a particle size of 200 nm” It can be seen that the decomposition activity of “a sprayed coating formed of primary particles having a particle diameter of 200 nm” is high. That is, it can be seen that the higher the anatase content, the higher the decomposition activity of the sprayed coating.

  In this way, the larger the primary particle size, the higher the anatase content and the higher the decomposition activity of the sprayed coating. Further, from the data in Table 1, when the primary particle size is 7 nm, rutile formation is remarkable. Therefore, in the present embodiment, the primary particle size is set to 10 nm or more.

  Further, Table 3 shows a case where a thermal spray coating is formed using photocatalyst fine particles (primary particles) containing titanium dioxide having a particle size of 15 nm, and the anatase content of the thermal spray coating is 89.5% (Table 3). When the thermal spray coating is formed using photocatalyst fine particles (primary particles) containing titanium dioxide having a particle size of 30 nm and the anatase content of the thermal spray coating is 98.8% In Table 3, the relationship between time and the concentration of decomposed substances (acetaldehyde concentration) is shown.

  From Table 3, even if the anatase content is high, if the difference in the anatase content is small, the smaller the primary particles, the larger the specific surface area compared to the larger primary particles. It can be seen that the degradation activity is high.

  Thus, in order to deteriorate the decomposition activity even when the primary particle size is too large, the primary particle size is set to 1000 nm or less in the present embodiment.

[Photocatalyst concentration]
Table 4 shows the anatase crystal strength and the anatase content when the sprayed coating is formed with a slurry having a photocatalyst concentration of 10% by mass and 30% by mass.

From Table 4, the “sprayed coating formed with a slurry having a photocatalyst concentration of 30% by mass” has a higher anatase crystal strength than the “sprayed coating formed with a slurry having a photocatalyst concentration of 10% by mass”. It turns out that there is much adhesion amount. And if there is much adhesion amount of a photocatalyst, it will be very advantageous from a viewpoint of lifetime or performance. In addition, when it is going to implement | achieve the adhesion amount of the same quantity as a slurry with a high photocatalyst density | concentration with a slurry with a low photocatalyst density | concentration, construction will be needed several times.
Thus, paying attention to the amount of photocatalyst attached, a slurry having a high photocatalyst concentration is preferable.

  On the other hand, when the photocatalyst concentration exceeds 30% by mass, the viscosity of the slurry is increased and the fluidity is lowered, and clogging or the like occurs when the sprayed material is supplied. It becomes physically impossible.

  Therefore, in this embodiment, the photocatalyst concentration is 10% by mass or more and 30% by mass or less.

<2. Ultrasonic irradiation process>
In an example of the manufacturing method of the thermal spray coating to which the present invention is applied, the particle size of the photocatalyst particles is subsequently set to 1 μm by irradiating ultrasonic waves of 28 kHz to 40 kHz with an output of 60 watts or more per liter of slurry for 2 hours to 7 hours. Coarse to ˜50 μm.

[About ultrasound]
First, when the output of the ultrasonic wave is less than 60 watts per liter of slurry, it takes a long time for coarsening, which is extremely inefficient. Therefore, in this embodiment, the output is 60 watts or more per liter of slurry.

  In addition, if the frequency of the ultrasonic wave is less than 28 kHz, the action works in the direction of crushing the photocatalyst fine particles (secondary particles), and there is a possibility that the particles are not coarsened and become finer. On the other hand, the frequency of the ultrasonic wave is 40 kHz. If it exceeds, it takes a long time to coarsen the particles. Therefore, in the present embodiment, the frequency of the ultrasonic wave is set to 28 kHz to 40 kHz.

  Furthermore, if the time for irradiating the ultrasonic wave is less than 2 hours, the effect of the coarsening is hardly exhibited because the time is too short. On the other hand, the effect of the coarsening is not so much developed even when the irradiation is performed for more than 7 hours. Therefore, in this embodiment, the irradiation time of ultrasonic waves is set to 2 hours to 7 hours.

  Here, FIG. 2 (a) shows the particle size distribution of the photocatalyst fine particles (primary particles and secondary particles) in the slurry before ultrasonic irradiation, and FIG. 2 (b) shows an output of 600 watts and a frequency of 28 kHz. The particle size distribution of the photocatalyst fine particles (tertiary particles) in the slurry when irradiated with ultrasonic waves for 2 hours is shown.

  As is apparent from FIGS. 2A and 2B, it can be seen that the particle diameter of the photocatalyst fine particles in the slurry is coarsened by irradiating the slurry with ultrasonic waves.

[Regarding the particle size of the tertiary particles]
If the particle size of the coarsened photocatalyst particles (tertiary particles) is less than 1 μm, the mass is too small, so that the energy of collision with the substrate during thermal spraying is small and the yield may be reduced. Moreover, since the heat capacity is small, the anatase content may be reduced by the heat of thermal spraying.

  On the other hand, when the particle size of the coarsened photocatalyst particles (tertiary particles) exceeds 50 μm, the acceleration is not sufficient before the collision with the base material, so that the spraying material speed is low, and also to the substrate. There is a risk that the yield may be reduced due to crushing in the event of a collision, and the destruction of the dispersion. Therefore, in this Embodiment, the particle size of photocatalyst particle (tertiary particle) is 1 micrometer-50 micrometers.

<3. Thermal spray coating formation process>
In an example of a method for producing a thermal spray coating to which the present invention is applied, subsequently, while controlling the transformation of anatase type titanium dioxide into a rutile type, thermal spraying of photocatalyst particles (tertiary particles) as a thermal spray material is performed, A sprayed coating is produced.

  Here, for the thermal spray coating formation process, for example, a spraying temperature variable type high-speed thermal spraying device described in JP-A-2005-68457 can be used.

  In an example of a method for producing a thermal spray coating to which the present invention is applied, the photocatalyst particles are coarsened by irradiating ultrasonic waves, that is, the photocatalyst particles are coarsened without using a binder. The purity of the photocatalyst is not lowered in the process of increasing the particle size of the photocatalyst particles. Therefore, the sprayed coating can sufficiently exhibit the function of the photocatalyst.

Table 5 shows the adhesion amount of the thermal spray coating for “in the case where ultrasonic irradiation is not performed” and “in the case where ultrasonic irradiation is performed”. Specifically, the difference in the weight of the substrate before and after thermal spraying is 9.09 mg / cm ² when “no ultrasonic irradiation is performed”, whereas “when ultrasonic irradiation is performed”. The difference in the weight of the substrate before and after thermal spraying is 14.39 mg / cm ² .

  From Table 5, the particle size of the photocatalyst particles is coarsened by irradiating with ultrasonic waves, and it is possible to sufficiently ensure the collision energy to the base material at the time of thermal spraying. You can see that

  Table 6 shows the anatase content in the thermal spray coating for “when ultrasonic irradiation is not performed” and “when ultrasonic irradiation is performed”. Specifically, when “no ultrasonic irradiation is performed”, the average particle diameter of the sprayed material is 0.565 μm, and the anatase content in the sprayed coating formed with such a sprayed material is 90.2%. In contrast, in the case of “ultrasonic irradiation”, the average particle size of the sprayed material is 1.56 μm, and the anatase content in the sprayed coating formed with such a sprayed material is 98.2%. It has become.

  Further, Table 7 shows the gas decomposition performance results of the thermal spray coating for “in the case where ultrasonic irradiation is not performed” and “in the case where ultrasonic irradiation is performed”. Specifically, the thermal spray coating (denoted by symbol e in Table 7) formed with photocatalyst particles not subjected to ultrasonic irradiation decomposed acetaldehyde gas in 180 minutes, whereas the photocatalyst subjected to ultrasonic irradiation A sprayed coating (denoted by symbol f in Table 7) formed of particles shows that acetaldehyde gas was decomposed in 90 minutes.

  From Table 6 and Table 7, the particle size of the photocatalyst particles is coarsened by performing ultrasonic irradiation, the anatase content in the sprayed coating that affects the photocatalytic function is increased, and therefore the gas decomposition performance is improved. I understand that.

Claims (10)

A step of mixing photocatalyst particles and water to produce a slurry;
A method for producing a thermal spray material, comprising: irradiating the slurry with ultrasonic waves to increase the particle size of photocatalyst particles contained in the slurry to 1 μm to 50 μm. 2. The thermal spray material according to claim 1, wherein the step of generating the slurry comprises mixing at least one of photocatalyst particles having a particle diameter of 10 nm to 1000 nm or an aggregate of photocatalyst particles having a particle diameter of 10 nm to 1000 nm with water. Production method. The manufacturing method of the thermal spray material of Claim 1 or Claim 2 which mixes a photocatalyst particle and water so that the process of producing | generating the slurry may be 10 mass%-30 mass%. The manufacturing method of the thermal spray material of Claim 1, Claim 2 or Claim 3 which irradiates the ultrasonic wave whose frequency is 28kHz-40kHz. The manufacturing method of the thermal spray material of Claim 1, Claim 2, Claim 3 or Claim 4 irradiated with an ultrasonic wave for 2 hours-7 hours. A step of mixing photocatalyst particles and water to produce a slurry;
Irradiating the slurry with ultrasonic waves, and coarsening the particle size of the photocatalyst particles contained in the slurry to 1 μm to 50 μm to produce a thermal spray material;
And a step of performing thermal spraying of the thermal spray material. A step of mixing at least one of photocatalyst particles having a particle diameter of 10 nm to 1000 nm or an aggregate of photocatalyst particles having a particle diameter of 10 nm to 1000 nm with water to produce a slurry having a photocatalyst concentration of 10% by mass to 30% by mass. When,
Irradiating the slurry with ultrasonic waves having a frequency of 28 kHz to 40 kHz for 2 hours to 7 hours, and coarsening the particle diameter of the photocatalyst particles contained in the slurry to 1 μm to 50 μm to produce a thermal spray material;
And a step of performing thermal spraying of the thermal spray material. A step of mixing a photocatalyst particle containing anatase-type titanium dioxide particles with water to produce a slurry;
Irradiating the slurry with ultrasonic waves, and coarsening the particle size of the photocatalyst particles contained in the slurry to 1 μm to 50 μm to produce a thermal spray material;
And a step of spraying the thermal spray material while controlling the transformation of anatase-type titanium dioxide into a rutile type. Mixing at least one of photocatalyst particles containing anatase-type titanium dioxide particles having a particle size of 10 nm to 1000 nm or an aggregate of photocatalyst particles containing anatase-type titanium dioxide particles having a particle size of 10 nm to 1000 nm with water. Producing a slurry having a photocatalyst concentration of 10% by mass to 30% by mass;
Irradiating the slurry with ultrasonic waves having a frequency of 28 kHz to 40 kHz for 2 hours to 7 hours, and coarsening the particle size of the photocatalyst particles contained in the slurry to 1 μm to 50 μm to produce a thermal spray material;
And a step of spraying the thermal spray material while controlling the transformation of anatase-type titanium dioxide into a rutile type. The step of generating the slurry mixes water with photocatalyst particles containing anatase-type titanium dioxide particles doped with at least one of nitrogen, carbon, and sulfur atoms in the crystal lattice. The manufacturing method of the sprayed coating as described.

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