Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JP7533710B2 - Self-cleaning agent - Google Patents
[go: Go Back, main page]

JP7533710B2 - Self-cleaning agent - Google Patents

Self-cleaning agent Download PDF

Info

Publication number
JP7533710B2
JP7533710B2 JP2023108711A JP2023108711A JP7533710B2 JP 7533710 B2 JP7533710 B2 JP 7533710B2 JP 2023108711 A JP2023108711 A JP 2023108711A JP 2023108711 A JP2023108711 A JP 2023108711A JP 7533710 B2 JP7533710 B2 JP 7533710B2
Authority
JP
Japan
Prior art keywords
titanium oxide
copper
ratio
self
cleaning agent
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
JP2023108711A
Other languages
Japanese (ja)
Other versions
JP2023130423A5 (en
JP2023130423A (en
Inventor
幸介 藤田
俊介 河中
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
DIC Corp
Original Assignee
DIC Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by DIC Corp filed Critical DIC Corp
Publication of JP2023130423A publication Critical patent/JP2023130423A/en
Publication of JP2023130423A5 publication Critical patent/JP2023130423A5/ja
Application granted granted Critical
Publication of JP7533710B2 publication Critical patent/JP7533710B2/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D7/00Compositions of detergents based essentially on non-surface-active compounds
    • C11D7/02Inorganic compounds
    • C11D7/20Water-insoluble oxides
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/72Copper
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/76Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/84Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/847Vanadium, niobium or tantalum or polonium
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2235/00Indexing scheme associated with group B01J35/00, related to the analysis techniques used to determine the catalysts form or properties
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2235/00Indexing scheme associated with group B01J35/00, related to the analysis techniques used to determine the catalysts form or properties
    • B01J2235/15X-ray diffraction
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2235/00Indexing scheme associated with group B01J35/00, related to the analysis techniques used to determine the catalysts form or properties
    • B01J2235/30Scanning electron microscopy; Transmission electron microscopy
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/70Catalysts, in general, characterised by their form or physical properties characterised by their crystalline properties, e.g. semi-crystalline

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Wood Science & Technology (AREA)
  • Materials Engineering (AREA)
  • Catalysts (AREA)
  • Paints Or Removers (AREA)

Description

本発明は、汚れ分解機能を有するセルフクリーニング剤に関する。 The present invention relates to a self-cleaning agent that has dirt-decomposing properties.

防汚加工は、シミや汚れを付着しにくくしたり、汚れたものを洗濯、拭き取り等で除去しやすくするための加工である。前記防汚加工の手法としては、例えば、撥水撥油系と吸水吸油系とに大別され、撥水撥油系はフッ素化合物を含むものや、また汚れを分解する手法としては、光触媒酸化チタンを用いる方法が知られている(例えば、特許文献1を参照。)。 Anti-soiling processing is processing that makes it difficult for stains and dirt to adhere and makes it easier to remove stains by washing, wiping, etc. The methods of anti-soiling processing are roughly divided into water- and oil-repellent systems and water- and oil-absorbing systems, and the water- and oil-repellent systems include those that contain fluorine compounds, and a method that uses photocatalytic titanium oxide to break down dirt is known (see, for example, Patent Document 1).

しかしながら、前記光触媒酸化チタンは、紫外光という強いエネルギー源が必要である点と、その強い酸化作用により、加工物や基材自体の劣化を招いてしまうという課題を有していた。 However, the photocatalytic titanium oxide requires a strong energy source, namely ultraviolet light, and has the problem that its strong oxidizing effect can cause deterioration of the processed material or the base material itself.

特開2014-163030号公報JP 2014-163030 A

本発明が解決しようとする課題は、室内光の下で汚れ成分を分解できるセルフクリーニング剤を提供することである。 The problem that this invention aims to solve is to provide a self-cleaning agent that can break down dirt components under indoor light.

本発明は、可視光応答型光触媒を含有することを特徴とするセルフクリーニング剤を提供するものである。 The present invention provides a self-cleaning agent that contains a visible light responsive photocatalyst.

本発明のセルフクリーニング剤によれば、実用的な室内光の下で、汚れ成分を分解することができる。また、前記可視光応答型光触媒として、特定のものを用いることで、更に抗菌性、及び、抗ウイルス性にも優れたセルフクリーニング剤を得ることができる。また、前記可視光応答型光触媒は、特定のものを用いると、酸化チタンの濃度を高めても取扱いが良好である。 The self-cleaning agent of the present invention can decompose dirt components under practical indoor light. In addition, by using a specific visible light responsive photocatalyst, a self-cleaning agent with even better antibacterial and antiviral properties can be obtained. In addition, when a specific visible light responsive photocatalyst is used, the agent is easy to handle even when the titanium oxide concentration is increased.

本発明のセルフクリーニング剤は、本発明の課題を解決するうえで、可視光応答型光触媒を含有することが好ましい。 The self-cleaning agent of the present invention preferably contains a visible light responsive photocatalyst in order to solve the problems of the present invention.

前記可視光応答型光触媒としては、例えば、酸化チタン(a)を含む組成物が挙げられ、より一層優れた抗ウイルス性が得られる点から、酸化チタン(a)に金属化合物が担持されたものが好ましく挙げられる。 The visible light responsive photocatalyst may be, for example, a composition containing titanium oxide (a), and preferably a composition in which a metal compound is supported on titanium oxide (a) because it provides even more excellent antiviral properties.

前記酸化チタン(a)としては、例えば、ルチル型酸化チタン(a1)、アナターゼ型酸化チタン、ブルッカイト型酸化チタン等を用いることができる。これらの酸化チタンは単独で用いても2種以上を併用してもよい。これらの中でも、優れた可視光領域での光触媒活性を有する点から、ルチル型酸化チタン(a1)を含むことが好ましい。 As the titanium oxide (a), for example, rutile type titanium oxide (a1), anatase type titanium oxide, brookite type titanium oxide, etc. can be used. These titanium oxides may be used alone or in combination of two or more. Among these, it is preferable to include rutile type titanium oxide (a1) because it has excellent photocatalytic activity in the visible light region.

前記前記ルチル型酸化チタン(a1)の含有率(ルチル化率)としては、より一層優れた明所及び暗所における抗ウイルス性、明所における有機化合物分解性、及び、可視光応答性が得られる点から、15モル%以上であることが好ましく、50モル%以上あることがより好ましく、90モル%以上が更に好ましい。 The content (rutilated rate) of the rutile-type titanium oxide (a1) is preferably 15 mol% or more, more preferably 50 mol% or more, and even more preferably 90 mol% or more, in order to obtain even better antiviral properties in bright and dark places, organic compound decomposition properties in bright places, and visible light responsiveness.

前記酸化チタン(a)の製造方法としては、一般的に、液相法と気相法とが知られている。前記液相法とは、イルメナイト鉱などの原料鉱石を溶解した液から得られる硫酸チタニルを、加水分解又は中和して酸化チタンを得る方法である。また、気相法とは、ルチル鉱などの原料鉱石を塩素化して得られる四塩化チタンと、酸素との気相反応により酸化チタンを得る方法である。なお、両方法により製造された酸化チタンを区別する方法としては、蛍光X線分析装置などを用いてチタン(Ti)含有量と金属元素の含有量を比較分析することが挙げられる。 The liquid phase method and the gas phase method are generally known as methods for producing the titanium oxide (a). The liquid phase method is a method in which titanium oxide is obtained by hydrolyzing or neutralizing titanyl sulfate obtained from a liquid in which raw ore such as ilmenite is dissolved. The gas phase method is a method in which titanium oxide is obtained by a gas phase reaction between oxygen and titanium tetrachloride obtained by chlorinating raw ore such as rutile. Note that one method for distinguishing between titanium oxides produced by both methods is to comparatively analyze the titanium (Ti) content and the metal element content using a fluorescent X-ray analyzer or the like.

前記液相法により製造された酸化チタンは、その生成物にイルメナイト鉱石に由来するジルコニウム、ニオブなどの金属元素が含まれている。前記液相法により製造された酸化チタンにおけるチタン100に対するジルコニウムの含有比(Zr/Ti比)は、0.03以上でもよく、0.04以上でもよく、0.05以上でもよく、また、0.8以下でもよく、0.5以下でもよく、0.3以下でもよい。これらの上限及び下限はいずれの組み合わせでもよい。酸化チタンにおけるチタン100に対するジルコニウムの含有比(Zr/Ti比)は、0.03~0.8でもよく、0.04~0.5でもよく、0.05~0.3でもよい。前記液相法により製造された酸化チタンにおけるチタン100に対するニオブの含有比(Nb/Ti比)は、0.05以上でもよく、0.08以上でもよく、0.1以上でもよく、また、0.8以下でもよく、0.5以下でもよく、0.3以下でもよい。これらの上限及び下限はいずれの組み合わせでもよい。酸化チタンにおけるチタン100に対するニオブの含有比(Nb/Ti比)は、0.05~0.8でもよく、0.08~0.5でもよく、0.10~0.3でもよい。上記範囲内の酸化チタンであれば、溶媒への分散性が高く酸化チタンの濃度を高めても取扱いの良好な混合液ができる。上記範囲内の酸化チタンで得られた可視光応答型光触媒は、可視光応答型光触媒におけるチタン100に対する金属元素(ジルコニウム及び/又はニオブ)の含有比が上記範囲と同じになる。 The titanium oxide produced by the liquid phase method contains metal elements such as zirconium and niobium derived from ilmenite ore in the product. The zirconium content ratio (Zr/Ti ratio) to titanium 100 in the titanium oxide produced by the liquid phase method may be 0.03 or more, 0.04 or more, 0.05 or more, 0.8 or less, 0.5 or less, or 0.3 or less. Any combination of these upper and lower limits may be used. The zirconium content ratio (Zr/Ti ratio) to titanium 100 in the titanium oxide may be 0.03 to 0.8, 0.04 to 0.5, or 0.05 to 0.3. The content ratio of niobium to titanium 100 (Nb/Ti ratio) in the titanium oxide produced by the liquid phase method may be 0.05 or more, 0.08 or more, 0.1 or more, 0.8 or less, 0.5 or less, or 0.3 or less. Any combination of these upper and lower limits is acceptable. The content ratio of niobium to titanium 100 (Nb/Ti ratio) in the titanium oxide may be 0.05 to 0.8, 0.08 to 0.5, or 0.10 to 0.3. If the titanium oxide is within the above range, it is highly dispersible in the solvent and a mixture liquid that is easy to handle can be produced even if the titanium oxide concentration is increased. The visible light responsive photocatalyst obtained from the titanium oxide within the above range has the same content ratio of metal elements (zirconium and/or niobium) to titanium 100 in the visible light responsive photocatalyst as the above range.

これに対し、気相法では四塩化チタンを精製するため、酸化チタン中には、これらの金属元素(ジルコニウム及び/又はニオブ)は実質的に含まれない。ここで酸化チタンが金属元素を実質的に含まないとは、酸化チタンにおける金属元素の含有比がチタン100に対して0.02未満であることを意味する。逆に酸化チタンが金属元素(ジルコニウム及び/又はニオブ)を実質的に含むとは、酸化チタンにおける金属元素の含有比がチタン100に対して0.02以上であることを意味する。金属元素(ジルコニウム及び/又はニオブ)を実質的に含む酸化チタンで得られた可視光応答型光触媒は、金属元素(ジルコニウム及び/又はニオブ)を実質的に含む。 In contrast, in the gas phase method, titanium tetrachloride is refined, so these metal elements (zirconium and/or niobium) are not substantially contained in the titanium oxide. Here, "titanium oxide substantially does not contain metal elements" means that the content ratio of metal elements in titanium oxide is less than 0.02 per 100 titanium. Conversely, "titanium oxide substantially contains metal elements (zirconium and/or niobium)" means that the content ratio of metal elements in titanium oxide is 0.02 or more per 100 titanium. A visible light responsive photocatalyst obtained from titanium oxide that substantially contains metal elements (zirconium and/or niobium) substantially contains metal elements (zirconium and/or niobium).

前記気相法により製造された酸化チタンは、均一な粒子径を生成可能な利点があるものの、2次凝集体は生成しにくいため、見かけの比表面積が高くなることにより反応工程時における混合液の粘度が高くなると考えられる。これに対し、液相法により製造された酸化チタン(a)は、焼成工程において緩やかな2次凝集体を生成することが考えられ、1次粒子に起因する比表面積(BET値)に対して、凝集力は少なく混合液の粘度を抑制することが可能である。以上の理由より、前記酸化チタン(a)としては、セルフクリーニング剤の生産性をより一層向上できる点から、液相法により製造された酸化チタンが好ましい。 Although titanium oxide produced by the gas phase method has the advantage of being able to produce uniform particle diameters, it is thought that secondary aggregates are difficult to produce, and therefore the apparent specific surface area is high, which increases the viscosity of the mixed liquid during the reaction process. In contrast, titanium oxide (a) produced by the liquid phase method is thought to produce gentle secondary aggregates in the firing process, and has low cohesive force compared to the specific surface area (BET value) caused by the primary particles, making it possible to suppress the viscosity of the mixed liquid. For these reasons, titanium oxide (a) produced by the liquid phase method is preferable because it can further improve the productivity of the self-cleaning agent.

前記酸化チタン(a)のBET比表面積としては、より一層優れた抗ウイルス性、及び、可視光応答性が得られる点から、1~200m/gの範囲が好ましく、3~100m/gの範囲がより好ましく、4~70m/gの範囲がより好ましく、8~50m/gの範囲が更に好ましく、セルフクリーニング剤の生産性をより一層高めることができる点から、7.5~9.5m/gの範囲であることが好ましい。なお、前記ルチル型酸化チタン(a1)のBET比表面積の測定方法は、後述する実施例にて記載する。 The BET specific surface area of the titanium oxide (a) is preferably in the range of 1 to 200 m 2 /g, more preferably in the range of 3 to 100 m 2 /g, more preferably in the range of 4 to 70 m 2 /g, and even more preferably in the range of 8 to 50 m 2 /g, from the viewpoint of obtaining even better antiviral properties and visible light responsiveness, and is preferably in the range of 7.5 to 9.5 m 2 /g from the viewpoint of further increasing the productivity of the self-cleaning agent. The method for measuring the BET specific surface area of the rutile titanium oxide (a1) will be described in the Examples below.

前記酸化チタン(a)の1次粒子径としては、より一層優れた抗ウイルス性、及び、可視光応答性が得られる点から、0.01~0.5μmの範囲が好ましく、0.06~0.35μmの範囲がより好ましい。なお、前記酸化チタン(a)の1次粒子径の測定方法は、透過型電子顕微鏡(TEM)を使用して、電子顕微鏡写真から一次粒子の大きさを直接計測する方法で測定した値を示す。具体的には、個々の酸化チタンの1次粒子の短軸径と長軸径を計測し、平均をその1次粒子の粒子径とし、次に100個以上の酸化チタン粒子について、それぞれの粒子の体積(重量)を、求めた粒子径の立方体と近似して求め、体積平均粒径を平均1次粒子径とした。 The primary particle diameter of the titanium oxide (a) is preferably in the range of 0.01 to 0.5 μm, more preferably in the range of 0.06 to 0.35 μm, in order to obtain even better antiviral properties and visible light responsiveness. The primary particle diameter of the titanium oxide (a) is measured by a method in which a transmission electron microscope (TEM) is used to directly measure the size of the primary particles from an electron microscope photograph. Specifically, the minor axis diameter and major axis diameter of each primary particle of titanium oxide are measured, and the average is taken as the particle diameter of the primary particle. Next, the volume (weight) of each particle is calculated for 100 or more titanium oxide particles by approximating it to the cube of the calculated particle diameter, and the volume average particle diameter is taken as the average primary particle diameter.

また、前記可視光応答型光触媒としては、可視光領域における光触媒活性を一層向上し、実用的な室内光の下で、汚れ成分を分解できる適度な活性を発現しやすい点から、酸化チタン(a)に金属化合物が担持されたもの(酸化チタン組成物)を用いることが好ましい。 In addition, as the visible light responsive photocatalyst, it is preferable to use a titanium oxide (a) carrying a metal compound (titanium oxide composition) since this further improves the photocatalytic activity in the visible light region and is likely to exhibit a suitable activity capable of decomposing dirt components under practical indoor light.

前記金属化合物としては、例えば、銅化合物、鉄化合物、タングステン化合物等を用いることができる。これらの中でも、より一層優れた抗菌性、及び、抗ウイルス性が得られる点から、銅化合物が好ましく、2価銅化合物がより好ましい。前記酸化チタン(a)への金属化合物の担持方法としては、公知の手法を用いることができる。 As the metal compound, for example, a copper compound, an iron compound, a tungsten compound, etc. can be used. Among these, a copper compound is preferred, and a divalent copper compound is more preferred, in that it provides even more excellent antibacterial and antiviral properties. A known method can be used to support the metal compound on the titanium oxide (a).

次に、最も好ましい態様である、酸化チタン(a)に2価銅化合物を担持する方法について説明する。 Next, we will explain the most preferred method of supporting a divalent copper compound on titanium oxide (a).

前記酸化チタン(a)に2価銅化合物を担持する方法としては、例えば、ルチル型酸化チタン(a1)を含む酸化チタン(a)、2価銅化合物原料(b)、水(c)、及び、アルカリ性物質(d)の混合工程(i)を有する方法が挙げられる。 As an example of a method for supporting a divalent copper compound on the titanium oxide (a), there can be mentioned a method having a mixing step (i) of titanium oxide (a) including rutile-type titanium oxide (a1), a divalent copper compound raw material (b), water (c), and an alkaline substance (d).

前記混合工程(i)における前記酸化チタン(a)の濃度としては、3~40質量%の範囲が好ましい。なお、本発明においては、液相法により製造された酸化チタン(a)を用いた場合には、酸化チタン(a)の濃度を高めても取扱いの良好な混合工程を行うことができ、具体的には、前記酸化チタン(a)の濃度が、25質量%を超えて40質量%以下の範囲でも良好に混合工程を行うことができる。 The concentration of the titanium oxide (a) in the mixing step (i) is preferably in the range of 3 to 40% by mass. In the present invention, when titanium oxide (a) produced by a liquid phase method is used, the mixing step can be carried out with good handling even if the concentration of titanium oxide (a) is increased. Specifically, the mixing step can be carried out well even if the concentration of titanium oxide (a) is in the range of more than 25% by mass to 40% by mass or less.

前記2価銅化合物原料(b)としては、例えば、2価銅無機化合物、2価銅有機化合物等を用いることができる。 As the divalent copper compound raw material (b), for example, a divalent copper inorganic compound, a divalent copper organic compound, etc. can be used.

前記2価銅無機化合物としては、例えば、硫酸銅、硝酸銅、沃素酸銅、過塩素酸銅、シュウ酸銅、四ホウ酸銅、硫酸アンモニウム銅、アミド硫酸銅、塩化アンモニウム銅、ピロリン酸銅、炭酸銅等の2価銅の無機酸塩;塩化銅、フッ化銅、臭化銅等の2価銅のハロゲン化物;酸化銅、硫化銅、アズライト、マラカイト、アジ化銅などを用いることができる。これらの化合物は単独で用いても2種以上を併用してもよい。 Examples of the divalent copper inorganic compound that can be used include inorganic acid salts of divalent copper such as copper sulfate, copper nitrate, copper iodate, copper perchlorate, copper oxalate, copper tetraborate, ammonium copper sulfate, copper amidosulfate, ammonium copper chloride, copper pyrophosphate, and copper carbonate; divalent copper halides such as copper chloride, copper fluoride, and copper bromide; copper oxide, copper sulfide, azurite, malachite, and copper azide. These compounds may be used alone or in combination of two or more.

前記2価銅有機化合物としては、例えば、蟻酸銅、酢酸銅、プロピオン酸銅、酪酸銅、吉草酸銅、カプロン酸銅、エナント酸銅、カプリル酸銅、ペラルゴン酸銅、カプリン酸銅、ミスチン酸銅、パルミチン酸銅、マルガリン酸銅、ステアリン酸銅、オレイン酸銅、乳酸銅、リンゴ酸銅、クエン酸銅、安息香酸銅、フタル酸銅、イソフタル酸銅、テレフタル酸銅、サリチル酸銅、メリト酸銅、シュウ酸銅、マロン酸銅、コハク酸銅、グルタル酸銅、アジピン酸銅、フマル酸銅、グリコール酸銅、グリセリン酸銅、グルコン酸銅、酒石酸銅、アセチルアセトン銅、エチルアセト酢酸銅、イソ吉草酸銅、β-レゾルシル酸銅、ジアセト酢酸銅、ホルミルコハク酸銅、サリチルアミン酸銅、ビス(2-エチルヘキサン酸)銅、セバシン酸銅、ナフテン酸銅、オキシン銅、アセチルアセトン銅、エチルアセト酢酸銅、トリフルオロメタンスルホン酸銅、フタロシアニン銅、銅エトキシド、銅イソプロポキシド、銅メトキシド、ジメチルジチオカルバミン酸銅等を用いることができる。これらの化合物は単独で用いても2種以上を併用してもよい。 Examples of the divalent copper organic compounds include copper formate, copper acetate, copper propionate, copper butyrate, copper valerate, copper caproate, copper enanthate, copper caprylate, copper pelargonate, copper caprate, copper myristic acid, copper palmitate, copper margarate, copper stearate, copper oleate, copper lactate, copper malate, copper citrate, copper benzoate, copper phthalate, copper isophthalate, copper terephthalate, copper salicylate, copper mellitic acid, copper oxalate, copper malonate, copper succinate, copper glutarate, copper adipic acid, copper fumarate, and glycol. Examples of compounds that can be used include copper glycerate, copper gluconate, copper tartrate, copper acetylacetonate, copper ethylacetoacetate, copper isovalerate, copper β-resorcylate, copper diacetoacetate, copper formylsuccinate, copper salicylamine, copper bis(2-ethylhexanoate), copper sebacate, copper naphthenate, copper oxine, copper acetylacetonate, copper ethylacetoacetate, copper trifluoromethanesulfonate, copper phthalocyanine, copper ethoxide, copper isopropoxide, copper methoxide, and copper dimethyldithiocarbamate. These compounds may be used alone or in combination of two or more.

前記2価銅化合物原料(b)としては、前記したものの中でも、下記一般式(1)で示されるものを用いることが好ましい。
CuX (1)
(式(1)において、Xは、ハロゲン原子、CHCOO、NO、又は、(SO1/2を示す。)
As the divalent copper compound raw material (b), among those mentioned above, it is preferable to use one represented by the following general formula (1).
CuX2 (1)
(In formula (1), X represents a halogen atom, CH 3 COO, NO 3 , or (SO 4 ) 1/2 .)

前記式(1)におけるXとしては、ハロゲン原子であることがより好ましく、塩素原子が更に好ましい。 In the formula (1), X is more preferably a halogen atom, and even more preferably a chlorine atom.

前記混合工程(i)における前記2価銅化合物原料(b)の使用量としては、前記酸化チタン(a)100質量部に対して、0.01~20質量部の範囲であることが好ましく、0.1~15質量部の範囲がより好ましく、0.3~10質量部の範囲が更に好ましい。 The amount of the divalent copper compound raw material (b) used in the mixing step (i) is preferably in the range of 0.01 to 20 parts by mass, more preferably in the range of 0.1 to 15 parts by mass, and even more preferably in the range of 0.3 to 10 parts by mass, per 100 parts by mass of the titanium oxide (a).

前記水(c)は、混合工程(i)における溶媒であり、水単独が好ましいが、必要に応じてその他の溶媒を含んでいてもよい。前記その他の溶媒としては、例えば、メタノール、エタノール、1-プロパノール、2-プロパノール、1-ブタノール等のアルコール溶媒;メチルエチルケトン、メチルイソブチルケトン等のケトン溶媒;ジメチルホルムアミド、テトラヒドロフラン等を用いることができる。これらの溶媒は単独で用いても2種以上を併用してもよい。 The water (c) is a solvent in the mixing step (i), and although water alone is preferred, other solvents may be included as necessary. Examples of the other solvents that can be used include alcohol solvents such as methanol, ethanol, 1-propanol, 2-propanol, and 1-butanol; ketone solvents such as methyl ethyl ketone and methyl isobutyl ketone; dimethylformamide, tetrahydrofuran, and the like. These solvents may be used alone or in combination of two or more.

前記アルカリ性物質(d)としては、例えば、水酸化ナトリウム、水酸化カリウム、テトラメチルアンモニウムハイドロオキサイド、テトラブチルアンモニウムヒドロキシド、トリエチルアミン、トリメチルアミン、アンモニア、塩基性界面活性剤等を用いることができ、水酸化ナトリウムを用いることが好ましい。 Examples of the alkaline substance (d) that can be used include sodium hydroxide, potassium hydroxide, tetramethylammonium hydroxide, tetrabutylammonium hydroxide, triethylamine, trimethylamine, ammonia, and basic surfactants, and it is preferable to use sodium hydroxide.

前記アルカリ性物質(d)は、反応を制御しやすい点から、溶液として添加するのが好ましく、添加するアルカリ溶液の濃度としては、0.1~5mol/Lの範囲であることが好ましく、0.3~4mol/Lの範囲がより好ましく、0.5~3mol/Lの範囲が更に好ましい。 The alkaline substance (d) is preferably added as a solution in order to facilitate control of the reaction, and the concentration of the alkaline solution added is preferably in the range of 0.1 to 5 mol/L, more preferably in the range of 0.3 to 4 mol/L, and even more preferably in the range of 0.5 to 3 mol/L.

前記混合工程(i)は、前記酸化チタン(a)、2価銅化合物原料(b)、水(c)、及び、アルカリ性物質(d)を混合すればよく、例えば、まず水(c)に酸化チタン(a)を混合するとともに必要に応じて撹拌し、次いで、2価銅化合物原料(b)を混合し、撹拌し、その後、アルカリ性物質(d)を添加して撹拌する方法が挙げられる。この混合工程(i)により、前記2価銅化合物原料(b)由来の2価銅化合物が前記酸化チタン(a)に担持することとなる。 In the mixing step (i), the titanium oxide (a), the divalent copper compound raw material (b), the water (c), and the alkaline substance (d) may be mixed. For example, the titanium oxide (a) may be mixed with the water (c) and stirred as necessary, the divalent copper compound raw material (b) may then be mixed and stirred, and the alkaline substance (d) may then be added and stirred. By this mixing step (i), the divalent copper compound derived from the divalent copper compound raw material (b) is supported on the titanium oxide (a).

前記混合工程(i)における全体の撹拌時間としては、例えば、5~120分間が挙げられ、好ましくは10~60分間である。混合工程(i)時における温度としては、例えば、室温~70℃の範囲が挙げられる。 The total stirring time in the mixing step (i) is, for example, 5 to 120 minutes, and preferably 10 to 60 minutes. The temperature during the mixing step (i) is, for example, in the range of room temperature to 70°C.

酸化チタン(a)への2価銅化合物の担持が良好である点から、前記酸化チタン(a)、2価銅化合物原料(b)、及び、水(c)を混合・撹拌し、その後アルカリ性物質(d)を混合・撹拌した後の混合物のpHとしては、好ましくは8~11の範囲であり、より好ましくは9.0~10.5の範囲である。 In order to ensure good support of the divalent copper compound on the titanium oxide (a), the titanium oxide (a), the divalent copper compound raw material (b), and water (c) are mixed and stirred, and then the alkaline substance (d) is mixed and stirred to produce a mixture having a pH value preferably in the range of 8 to 11, and more preferably in the range of 9.0 to 10.5.

前記混合工程(i)が終了した後には、混合液を固形分として分離することができる。前記分離を行う方法としては、例えば、濾過、沈降分離、遠心分離、蒸発乾燥等が挙げられるが、濾過が好ましい。分離した固形分は、その後必要に応じて、水洗、解砕、分級等を行ってもよい。 After the mixing step (i) is completed, the mixture can be separated as a solid content. Methods for the separation include, for example, filtration, sedimentation, centrifugation, and evaporation and drying, with filtration being preferred. The separated solid content may then be washed with water, crushed, classified, etc., as necessary.

前記固形分を得た後には、前記酸化チタン(a)上に担持された前記2価銅化合物原料(b)由来の2価銅化合物を、より強固に結合することができる点から、固形分を熱処理することが好ましい。熱処理温度としては、好ましくは150~600℃の範囲であり、より好ましくは250~450℃の範囲である。また、熱処理時間は、好ましくは1~10時間であり、より好ましくは、2~5時間である。 After obtaining the solid content, it is preferable to heat treat the solid content in order to more firmly bond the divalent copper compound derived from the divalent copper compound raw material (b) supported on the titanium oxide (a). The heat treatment temperature is preferably in the range of 150 to 600°C, more preferably in the range of 250 to 450°C. The heat treatment time is preferably 1 to 10 hours, more preferably 2 to 5 hours.

以上の方法によって、酸化チタン(a)に2価銅化合物が担持した酸化チタンを含有する酸化チタン組成物が得られる。前記酸化チタン(a)に担持された2価銅化合物の担持量としては、酸化チタン(a)100質量部に対して、0.01~20質量部の範囲であることが、抗ウイルス性を含む光触媒活性の点から好ましい。前記2価銅化合物の担持量は、前記混合工程(i)における前記2価銅化合物原料(b)の使用量によって調整することができる。なお、前記2価銅化合物の担持量の測定方法は、後述する実施例にて記載する。 By the above method, a titanium oxide composition containing titanium oxide in which a divalent copper compound is supported on titanium oxide (a) can be obtained. The amount of the divalent copper compound supported on the titanium oxide (a) is preferably in the range of 0.01 to 20 parts by mass per 100 parts by mass of titanium oxide (a) from the viewpoint of photocatalytic activity including antiviral activity. The amount of the divalent copper compound supported can be adjusted by the amount of the divalent copper compound raw material (b) used in the mixing step (i). The method for measuring the amount of the divalent copper compound supported will be described in the Examples below.

次に、本発明のセルフクリーニング剤が使用される具体的な態様について説明する。 Next, we will explain specific aspects of how the self-cleaning agent of the present invention is used.

前記態様としては、繊維等への練りこみ、スプレー剤、コーティング剤が挙げられる。 Examples of the above include kneading the material into fibers, spraying it, and using it as a coating agent.

前記繊維等への練りこみを行う方法としては、例えば、ポリエステル等の繊維と、前記セルフクリーニング剤とを、押出機等を使用して練りこみ、紡糸する方法が挙げられる。 As a method for kneading the self-cleaning agent into the fibers, for example, a method in which the self-cleaning agent is kneaded into fibers such as polyester using an extruder or the like, and then spun into yarn can be given.

前記スプレー剤としては、例えば、前記セルフクリーニング剤、及び、水、アルコール等の溶剤の混合物などが挙げられる。 Examples of the spray agent include a mixture of the self-cleaning agent and a solvent such as water or alcohol.

前記コーティング剤としては、例えば、前記セルフクリーニング剤、水、アルコール等の溶剤、及び、バインダー樹脂の混合物などが挙げられる。前記バインダー樹脂としては、例えば、アクリル樹脂、ウレタン樹脂、フェノール樹脂、ポリエステル樹脂、エポキシ樹脂等を用いることができる。これらのバインダー樹脂は単独で用いても2種以上を併用してもよい。 The coating agent may be, for example, a mixture of the self-cleaning agent, a solvent such as water or alcohol, and a binder resin. The binder resin may be, for example, an acrylic resin, a urethane resin, a phenolic resin, a polyester resin, or an epoxy resin. These binder resins may be used alone or in combination of two or more kinds.

以上、本発明のセルフクリーニング剤によれば、繊維等の有機系素材、スレート板等の無機系素材の態様において、実用的な室内光の下で、汚れ成分を分解することができる。また、前記可視光応答型光触媒として、特定のものを用いることで、更に抗菌性、及び、抗ウイルス性にも優れたセルフクリーニング剤を得ることができる。 As described above, the self-cleaning agent of the present invention can decompose dirt components under practical indoor light in the form of organic materials such as fibers and inorganic materials such as slate boards. In addition, by using a specific visible light responsive photocatalyst, a self-cleaning agent with even better antibacterial and antiviral properties can be obtained.

また、本発明によるセルフクリーニング剤は、抗ウイルス性、抗菌性、人体への安全性、耐熱性、耐候性、及び、耐水性に優れるものである。 The self-cleaning agent according to the present invention also has excellent antiviral and antibacterial properties, safety to the human body, heat resistance, weather resistance, and water resistance.

以下、実施例を用いて、本発明をより詳細に説明する。 The present invention will be explained in more detail below using examples.

[調製例1]
(1)酸化チタン
a)結晶性ルチル型酸化チタン
b)製法:液相法(硫酸法)
c)物性値
・BET比表面積:9.0m/g
・ルチル化率:95.4%
・1次粒子径:0.18μm
・Zr/Ti比:0.05
・Nb/Ti比:0.17
[Preparation Example 1]
(1) Titanium oxide a) Crystalline rutile titanium oxide b) Manufacturing method: Liquid phase method (sulfuric acid method)
c) Physical properties: BET specific surface area: 9.0 m 2 /g
- Rutile rate: 95.4%
・Primary particle size: 0.18μm
・Zr/Ti ratio: 0.05
・Nb/Ti ratio: 0.17

(2)製造工程
a)混合工程(反応工程)
前記酸化チタン600質量部、塩化銅(ii)二水和物8質量部、水900質量部をステンレス容器中に混合した。次いで、混合物を撹拌機(特殊機化工業株式会社製「ロボミクス」)で撹拌し、1mol/Lの水酸化ナトリウム水溶液を混合液のpHが10になるまで滴下した。
b)脱水工程
定性濾紙(5C)により減圧濾過をおこない、混合液から固形分を分離し、更にイオン交換水で洗浄を実施した。次いで、洗浄後の固形物を120℃で12時間乾燥し、水分を除去した。乾燥後、ミル(イワタニ産業株式会社製「ミルサー」)で粉状の酸化チタン組成物を得た。
c)熱処理工程
精密恒温器(ヤマト科学株式会社製「DH650」)を用いて酸素存在下で450℃、3時間熱処理し、2価銅化合物が担持された酸化チタンを含有する酸化チタン組成物を得た。
(2) Manufacturing process a) Mixing process (reaction process)
600 parts by mass of the titanium oxide, 8 parts by mass of copper (II) chloride dihydrate, and 900 parts by mass of water were mixed in a stainless steel container. The mixture was then stirred in a stirrer ("Robomix" manufactured by Tokushu Kika Kogyo Co., Ltd.). The mixture was stirred at RT, and a 1 mol/L aqueous solution of sodium hydroxide was added dropwise until the pH of the mixture reached 10.
b) Dehydration step: The mixture was filtered under reduced pressure using a qualitative filter paper (5C) to separate the solid matter from the mixture, and then washed with ion-exchanged water. The washed solid matter was then dried at 120° C. for 12 hours. The water was removed, and after drying, a powdered titanium oxide composition was obtained using a mill (Miller, manufactured by Iwatani Sangyo Co., Ltd.).
c) Heat Treatment Step: The mixture was heat-treated at 450° C. for 3 hours in the presence of oxygen using a precision incubator (DH650 manufactured by Yamato Scientific Co., Ltd.) to obtain a titanium oxide composition containing titanium oxide carrying a divalent copper compound. Got it.

(3)混合工程における混合物の酸化チタン濃度の変更
前記(2)製造工程a)混合工程(反応工程)において、酸化チタンの濃度を変更し、各配合率で撹拌可能な状態を判定した。具体的には、容器内で混合液が均一に撹拌される状態であれば「T」、混合液がゲル状となり、撹拌軸周辺のみの不十分な撹拌状態であれば「F」とした。
(3) Changing the titanium oxide concentration of the mixture in the mixing step In the above (2) manufacturing process a) mixing step (reaction step), the titanium oxide concentration was changed, and the stirrable state was judged for each blend ratio. Specifically, if the mixture was stirred uniformly in the container, it was rated as "T," and if the mixture became gel-like and only the stirring around the stirring shaft was insufficient, it was rated as "F."

[調製例2]
調製例1において、塩化銅(ii)二水和物の使用量を、8質量部から3.3質量部に変更した以外は、実施例1と同様にして、酸化チタン組成物を得た。また、調製例1と同様にして、酸化チタン濃度の変更試験を行った。
[Preparation Example 2]
A titanium oxide composition was obtained in the same manner as in Example 1, except that the amount of copper(II) chloride dihydrate used in Preparation Example 1 was changed from 8 parts by mass to 3.3 parts by mass. In addition, a test for changing the titanium oxide concentration was conducted in the same manner as in Preparation Example 1.

[調製例3]
(1)酸化チタン
a)結晶性ルチル型酸化チタン
b)製法:液相法
c)物性値
・BET比表面積:37.2m/g
・ルチル化率:99.6%
・1次粒子径:0.04μm
・Zr/Ti比:0.05
・Nb/Ti比:0.26
[Preparation Example 3]
(1) Titanium oxide a) Crystalline rutile titanium oxide b) Manufacturing method: Liquid phase method c) Physical properties BET specific surface area: 37.2 m 2 /g
- Rutile rate: 99.6%
・Primary particle size: 0.04μm
・Zr/Ti ratio: 0.05
・Nb/Ti ratio: 0.26

調製例1において、酸化チタンの種類を前記酸化チタンに変更した以外は、調製例1と同様にして、酸化チタン組成物を得た。また、調製例1と同様にして、酸化チタン濃度の変更試験を行った。 A titanium oxide composition was obtained in the same manner as in Preparation Example 1, except that the type of titanium oxide in Preparation Example 1 was changed to the titanium oxide described above. In addition, a test for changing the titanium oxide concentration was conducted in the same manner as in Preparation Example 1.

[調製例4]
(1)酸化チタン
a)結晶性ルチル型酸化チタン
b)製法:液相法
c)物性値
・BET比表面積:6m/g
・ルチル化率:87.2%
・Zr/Ti比:0.17
・Nb/Ti比:0.20
[Preparation Example 4]
(1) Titanium oxide a) Crystalline rutile titanium oxide b) Manufacturing method: Liquid phase method c) Physical properties BET specific surface area: 6 m 2 /g
- Rutile rate: 87.2%
・Zr/Ti ratio: 0.17
・Nb/Ti ratio: 0.20

調製例1において、酸化チタンの種類を前記酸化チタンに変更した以外は、調製例1と同様にして、酸化チタン組成物を得た。また、調製例1と同様にして、酸化チタン濃度の変更試験を行った。 A titanium oxide composition was obtained in the same manner as in Preparation Example 1, except that the type of titanium oxide in Preparation Example 1 was changed to the titanium oxide described above. In addition, a test for changing the titanium oxide concentration was conducted in the same manner as in Preparation Example 1.

[調製例5]
(1)酸化チタン
a)結晶性ルチル型酸化チタン
b)製法:気相法
c)物性値
・BET比表面積:13m/g
・ルチル化率:95.6%
・1次粒子径:0.15μm
・Zr/Ti比:0.00
・Nb/Ti比:0.01
[Preparation Example 5]
(1) Titanium oxide a) Crystalline rutile titanium oxide b) Manufacturing method: Gas phase method c) Physical properties BET specific surface area: 13 m 2 /g
- Rutile rate: 95.6%
・Primary particle size: 0.15μm
・Zr/Ti ratio: 0.00
・Nb/Ti ratio: 0.01

調製例1において、酸化チタンの種類を前記酸化チタンに変更し、水の使用量を900質量部から4,000質量部に変更した以外は、調製例1と同様にして、酸化チタン組成物を得た。また、調製例1と同様にして、酸化チタン濃度の変更試験を行った。 A titanium oxide composition was obtained in the same manner as in Preparation Example 1, except that the type of titanium oxide was changed to the titanium oxide described above and the amount of water used was changed from 900 parts by mass to 4,000 parts by mass. In addition, a test for changing the titanium oxide concentration was conducted in the same manner as in Preparation Example 1.

[調製例6]
調製例5において、塩化銅(ii)二水和物の使用量を8質量部から3.3質量部に変更した以外は、調製例5と同様にして、酸化チタン組成物を得た。また、調製例1と同様にして、酸化チタン濃度の変更試験を行った。
[Preparation Example 6]
A titanium oxide composition was obtained in the same manner as in Preparation Example 5, except that the amount of copper(II) chloride dihydrate used was changed from 8 parts by mass to 3.3 parts by mass in Preparation Example 5. In addition, a test for changing the titanium oxide concentration was conducted in the same manner as in Preparation Example 1.

[調製例7]
(1)酸化チタン
a)結晶性ルチル型酸化チタン
b)製法:気相法
c)物性値
・BET比表面積:6.8m/g
・ルチル化率:99.6%
・1次粒子径:0.25μm
・Zr/Ti比:0.01
・Nb/Ti比:0.01
[Preparation Example 7]
(1) Titanium oxide a) Crystalline rutile titanium oxide b) Manufacturing method: Gas phase method c) Physical properties BET specific surface area: 6.8 m 2 /g
- Rutile rate: 99.6%
・Primary particle size: 0.25μm
・Zr/Ti ratio: 0.01
・Nb/Ti ratio: 0.01

調製例5において、酸化チタンの種類を前記酸化チタンに変更した以外は、調製例5と同様にして、酸化チタン組成物を得た。また、調製例1と同様にして、酸化チタン濃度の変更試験を行った。 A titanium oxide composition was obtained in the same manner as in Preparation Example 5, except that the type of titanium oxide in Preparation Example 5 was changed to the titanium oxide described above. In addition, a test for changing the titanium oxide concentration was conducted in the same manner as in Preparation Example 1.

[調製例8]
(1)酸化チタン
a)結晶性ルチル型酸化チタン
b)製法:気相法
c)物性値
・BET比表面積:13.5m/g
・ルチル化率:76.5%
・1次粒子径:0.13μm
・Zr/Ti比:0.00
・Nb/Ti比:0.01
[Preparation Example 8]
(1) Titanium oxide a) Crystalline rutile titanium oxide b) Manufacturing method: Gas phase method c) Physical properties BET specific surface area: 13.5 m 2 /g
- Rutile ratio: 76.5%
・Primary particle size: 0.13μm
・Zr/Ti ratio: 0.00
・Nb/Ti ratio: 0.01

調製例5において、酸化チタンの種類を前記酸化チタンに変更した以外は、調製例5と同様にして、酸化チタン組成物を得た。また、調製例1と同様にして、酸化チタン濃度の変更試験を行った。 A titanium oxide composition was obtained in the same manner as in Preparation Example 5, except that the type of titanium oxide in Preparation Example 5 was changed to the titanium oxide described above. In addition, a test for changing the titanium oxide concentration was conducted in the same manner as in Preparation Example 1.

[調製例9]
(1)酸化チタン
a)結晶性ルチル型酸化チタン
b)製法:気相法
c)物性値
・BET比表面積:20m/g
・ルチル化率:53%
・1次粒子径:0.07μm
・Zr/Ti比:0.00
・Nb/Ti比:0.01
[Preparation Example 9]
(1) Titanium oxide a) Crystalline rutile titanium oxide b) Manufacturing method: Gas phase method c) Physical properties BET specific surface area: 20 m 2 /g
- Rutile rate: 53%
・Primary particle size: 0.07μm
・Zr/Ti ratio: 0.00
・Nb/Ti ratio: 0.01

調製例5において、酸化チタンの種類を前記酸化チタンに変更した以外は、調製例5と同様にして、酸化チタン組成物を得た。また、調製例1と同様にして、酸化チタン濃度の変更試験を行った。 A titanium oxide composition was obtained in the same manner as in Preparation Example 5, except that the type of titanium oxide in Preparation Example 5 was changed to the titanium oxide described above. In addition, a test for changing the titanium oxide concentration was conducted in the same manner as in Preparation Example 1.

[酸化チタン(a)のBET比表面積の測定方法]
株式会社マウンテック製全自動BET比表面積測定装置「MacSORBHM model-1208」を使用して、比表面積測定(BET1点法)による測定を行った。
[Method for measuring the BET specific surface area of titanium oxide (a)]
The specific surface area was measured (BET single point method) using a fully automatic BET specific surface area measuring device "MacSORBHM model-1208" manufactured by Mountech Co., Ltd.

[酸化チタン(a)のルチル化率の測定方法]
島津製作所株式会社製X線回折装置「XRD-6100」を使用して、ルチル型結晶に対応するピーク高さ割合を酸化チタン全体の結晶(ルチル型、ブルッカイト型、アナターゼ型)に対応するピーク高さから算出した。
[Method for measuring the rutile content of titanium oxide (a)]
Using an X-ray diffractometer "XRD-6100" manufactured by Shimadzu Corporation, the peak height ratio corresponding to rutile crystals was calculated from the peak heights corresponding to the entire titanium oxide crystals (rutile, brookite, and anatase types).

[酸化チタン(a)のZr/Ti比、Nb/Ti比の算出方法]
セイコーインスツル株式会社製蛍光X線分析装置「SEA1200VX」を使用して、バルクファンダメンタルパラメータ(バルクFP)法による金属元素組成分析を行った。酸化チタン(a)試料を測定して得られた、ジルコニウムまたはニオブの蛍光強度(cps:count per second)とチタンの蛍光強度(cps)との強度比を、それぞれZr/Ti比、またはNb/Ti比として算出した。
[Method of calculating Zr/Ti ratio and Nb/Ti ratio of titanium oxide (a)]
Metal element composition analysis was performed by the bulk fundamental parameter (bulk FP) method using a fluorescent X-ray analyzer "SEA1200VX" manufactured by Seiko Instruments Inc. The intensity ratio of the fluorescence intensity (cps: counts per second) of zirconium or niobium to the fluorescence intensity (cps) of titanium obtained by measuring the titanium oxide (a) sample was calculated as the Zr/Ti ratio or the Nb/Ti ratio, respectively.

[酸化チタン(a)への2価銅化合物の担持量の測定方法]
調製例1~9で得られた酸化チタン組成物を、フッ酸溶液で全溶解し、抽出液をICP発光分光分析装置により分析して、酸化チタン(a)に対する2価銅化合物の担持量(2価銅化合物の担持量(質量部)/酸化チタン(a)(質量部))を定量した。なお、前記担持量の測定まで行わなかったものは「-」とした。
[Method for measuring the amount of divalent copper compound supported on titanium oxide (a)]
The titanium oxide compositions obtained in Preparation Examples 1 to 9 were completely dissolved in a hydrofluoric acid solution, and the extract was analyzed by an ICP atomic emission spectrometer to quantify the amount of divalent copper compound supported on titanium oxide (a) (amount of divalent copper compound supported (parts by mass)/titanium oxide (a) (parts by mass)). Note that the cases where the amount supported was not measured were marked with "-".

[抗ウイルス性]
JIS R 1756:2013に準拠して、抗ウイルス性試験を行った。抗ウイルス性はソーダライムガラス板上に実施例及び比較例で得られた酸化チタン組成物を1g/mを均一に塗布し、N-113フィルターで400nm以下の波長をカットした光源を用いて、4時間照射後の試料について以下の式により求めた値、不活化度で評価した。
不活化度=log(N/N
N:反応後のサンプルの感染価 、N:接種ファージの感染価。
不活化度-1が90%、不活化度-2が99%、不活化度-3 が99.9%不活化していることを示す。
なお、抗ウイルス性試験まで行わなかったものは「-」とした。
[Antiviral]
Antiviral tests were conducted in accordance with JIS R 1756: 2013. The antiviral properties were evaluated by uniformly applying 1 g/ m2 of the titanium oxide compositions obtained in the Examples and Comparative Examples onto a soda-lime glass plate, irradiating the sample for 4 hours with a light source that cuts off wavelengths of 400 nm or less with an N-113 filter, and calculating the value (degree of inactivation) from the following formula.
Inactivation degree = log (N/N 0 )
N: infectious titer of the sample after the reaction, N 0 : infectious titer of the inoculated phage.
Inactivation degree-1 indicates 90% inactivation, inactivation degree-2 indicates 99%, and inactivation degree-3 indicates 99.9% inactivation.
In addition, those for which antiviral tests were not performed were marked "-".

Figure 0007533710000001
Figure 0007533710000001

調製例1~4に示す通り、酸化チタンを液相法で得れば、混合工程(i)中における混合物中の酸化チタン(a)の濃度を高めても安定的に混合でき、抗ウイルス性に優れる抗ウイルス剤が効率よく生産できることが分かった。 As shown in Preparation Examples 1 to 4, it was found that if titanium oxide is obtained by a liquid phase method, the titanium oxide (a) can be mixed stably even if the concentration in the mixture during the mixing step (i) is increased, and an antiviral agent with excellent antiviral properties can be efficiently produced.

一方、調製例5~9はいずれも、酸化チタン(a)に代えて、気相法により製造されたルチル型酸化チタンを用いた態様であるが、混合工程(i)における酸化チタン濃度が20質量%を超えると、混合液の粘度が極めて高くなり、取扱いが困難であり、生産性に劣ることが分かった。 On the other hand, all of Preparation Examples 5 to 9 use rutile-type titanium oxide produced by a gas phase method instead of titanium oxide (a), but it was found that when the titanium oxide concentration in the mixing step (i) exceeds 20 mass%, the viscosity of the mixture becomes extremely high, making it difficult to handle and resulting in poor productivity.

特に、調製例5~9では、酸化チタンのBET比表面積の幅を振った実験を行ったものの、その値が小さい調製例7においても酸化チタン濃度が上がると混合液の粘度が極めて高くなり、生産性の改善効果は見られなかった。 In particular, in Preparation Examples 5 to 9, experiments were conducted with varying ranges of the BET specific surface area of titanium oxide, but even in Preparation Example 7, where the value was small, the viscosity of the mixed liquid became extremely high as the titanium oxide concentration increased, and no improvement in productivity was observed.

[実施例1]
調整例1で得られた酸化チタン組成物25質量部、水73.5質量部、分散剤(ビックケミー社製「DISPERBIK 190」)1.5質量部をサンドグラインダーにて分散し、水性スラリーを得た。
得られた水性スラリー35質量部、アクリル樹脂バインダー(DIC株式会社製「RYUDYE-W FIXER 254PK」)5質量部、O/W型エマルジョン(DIC株式会社製「RYUDYE-W REDUCER CONC 720ENF」5部、水45部、ミネラルスピリット50部の乳化物)60質量部を混合し、綿ブロード生地(122.5g/m)上にオートスクリーン捺染機(辻井染機工業株式会社製)を用いて乾燥前塗布量が100g/mとなるようにプリントを実施し、熱風循環式乾燥機にて150℃で2分間乾燥させ、評価用試料を得た。
[Example 1]
25 parts by mass of the titanium oxide composition obtained in Preparation Example 1, 73.5 parts by mass of water, and 1.5 parts by mass of a dispersant (DISPERBIK 190 manufactured by BYK-Chemie) were dispersed in a sand grinder to obtain an aqueous slurry.
35 parts by mass of the obtained aqueous slurry, 5 parts by mass of an acrylic resin binder ("RYUDYE-W FIXER 254PK" manufactured by DIC Corporation), and 60 parts by mass of an O/W type emulsion (an emulsion of 5 parts of "RYUDYE-W REDUCER CONC 720ENF" manufactured by DIC Corporation, 45 parts of water, and 50 parts of mineral spirits) were mixed and printed on a cotton broadcloth (122.5 g/ m2 ) using an auto screen printing machine (manufactured by Tsujii Senki Kogyo Co., Ltd.) so that the coating amount before drying was 100 g/ m2 , and the mixture was dried for 2 minutes at 150°C in a hot air circulation dryer to obtain a sample for evaluation.

得られた試料に、汚れ成分(A)(オイルレッド0.5質量部、エタノール49.75質量部、及び、オレイン酸49.75質量部)30μLを、マイクロピペットを用いて滴下し、500ルクスの室内に放置し、滴下後1時間後(0日後)、1日後、2日後に色彩計(コニカミノルタ株式会社製「CR-200 D65光源」)にてa*値を測定した。 30 μL of stain component (A) (0.5 parts by mass of oil red, 49.75 parts by mass of ethanol, and 49.75 parts by mass of oleic acid) was dripped onto the obtained sample using a micropipette and left in a room at 500 lux. The a* value was measured 1 hour (0 days), 1 day, and 2 days after dripping using a colorimeter (Konica Minolta, Inc. "CR-200 D65 light source").

[実施例2]
実施例1において、汚れ成分(A)を、汚れ成分(B)(S&B株式会社製ラー油)に変更した以外は、実施例1と同様にして、a*値を測定した。なお、Δa*は、比較例4との差分によって求めた。
[Example 2]
In Example 1, the a* value was measured in the same manner as in Example 1, except that the stain component (A) was changed to the stain component (B) (chili oil manufactured by S&B Co., Ltd.). The Δa* was calculated by the difference from Comparative Example 4.

[実施例3]
実施例1において、汚れ成分(A)を、汚れ成分(C)(エスビーカレーパウダー顆粒1質量部、及び、エタノール99質量部)に変更した以外は、実施例1と同様にして、
a*値を測定した。なお、Δa*は、比較例6との差分によって求めた。
[Example 3]
The same procedure as in Example 1 was repeated, except that the stain component (A) in Example 1 was changed to stain component (C) (1 part by mass of SB curry powder granules and 99 parts by mass of ethanol).
The a* value was measured. Note that Δa* was determined by the difference from Comparative Example 6.

[実施例4]
実施例1において、綿ブロード生地に代えて、スレート板(ノザワ株式会社製)に変更した以外は、実施例1と同様にして、a*値を測定した。なお、Δa*は、比較例8との差分によって求めた。
[Example 4]
The a* value was measured in the same manner as in Example 1, except that a slate board (manufactured by Nozawa Co., Ltd.) was used instead of the cotton broadcloth in Example 1. The a* value was determined by the difference from Comparative Example 8.

[比較例1]
実施例1で用いた綿ブロード生地に直接汚れ成分(A)を滴下した以外は、実施例1と同様にして、a*値を測定した。また、このa*値を、実施例1、比較例2、及び比較例3の色変化量(Δa*)の基準とした。
[Comparative Example 1]
The a* value was measured in the same manner as in Example 1, except that the stain component (A) was dropped directly onto the cotton broadcloth used in Example 1. The a* value was used as the standard for the color change (Δa*) in Example 1, Comparative Example 2, and Comparative Example 3.

[比較例2]
アクリル樹脂バインダー(DIC株式会社製「RYUDYE-W FIXER 254PK」)5質量部、O/W型エマルジョン(DIC株式会社製「RYUDYE-W REDUCER CONC 720ENF」5部、水45部、ミネラルスピリット50部の乳化物)95質量部を混合し、実施例1で用いた綿ブロード生地に、オートスクリーン捺染機(辻井染機工業株式会社製)を用いて乾燥前塗布量が100g/mとなるようにプリントを実施し、熱風循環式乾燥機にて150℃で2分間乾燥させ、評価用試料を得た。これに汚れ成分(A)を滴下した以外は、実施例1と同様にして、a*値を測定した。
[Comparative Example 2]
5 parts by weight of an acrylic resin binder ("RYUDYE-W FIXER 254PK" manufactured by DIC Corporation) and 95 parts by weight of an O/W type emulsion (an emulsion of 5 parts of "RYUDYE-W REDUCER CONC 720ENF" manufactured by DIC Corporation, 45 parts of water, and 50 parts of mineral spirits) were mixed, and printed on the cotton broadcloth used in Example 1 using an auto screen printing machine (manufactured by Tsujii Senki Kogyo Co., Ltd.) so that the coating amount before drying was 100 g/ m2 , and dried in a hot air circulation dryer at 150°C for 2 minutes to obtain a sample for evaluation. The a* value was measured in the same manner as in Example 1, except that the stain component (A) was dropped onto the sample.

[比較例3]
調整例1の酸化チタン組成物に代えて、紫外光応答型光触媒(石原産業株式会社製「ST-41」)25質量部、水73.5質量部、分散剤(ビックケミー社製「DISPERBIK 190」)1.5質量部をサンドグラインダーにて分散し、水性スラリーを得た。
得られた水性スラリー35質量部、アクリル樹脂バインダー(DIC株式会社製「RYUDYE-W FIXER 254PK」)5質量部、O/W型エマルジョン(DIC株式会社製「RYUDYE-W REDUCER CONC 720ENF」5部、水45部、ミネラルスピリット50部の乳化物)60質量部を混合し、綿ブロード生地(122.5g/m)上にオートスクリーン捺染機(辻井染機工業株式会社製)を用いて乾燥前塗布量が100g/mとなるようにプリントを実施し、熱風循環式乾燥機にて150℃で2分間乾燥させ、評価用試料を得た。これに汚れ成分(A)を滴下した以外は、実施例1と同様にして、a*値を測定した。
[Comparative Example 3]
Instead of the titanium oxide composition of Preparation Example 1, 25 parts by mass of an ultraviolet light responsive photocatalyst ("ST-41" manufactured by Ishihara Sangyo Kaisha, Ltd.), 73.5 parts by mass of water, and 1.5 parts by mass of a dispersant ("DISPERBIK 190" manufactured by BYK-Chemie) were dispersed in a sand grinder to obtain an aqueous slurry.
35 parts by weight of the obtained aqueous slurry, 5 parts by weight of an acrylic resin binder ("RYUDYE-W FIXER 254PK" manufactured by DIC Corporation), and 60 parts by weight of an O/W type emulsion (an emulsion of 5 parts of "RYUDYE-W REDUCER CONC 720ENF" manufactured by DIC Corporation, 45 parts of water, and 50 parts of mineral spirits) were mixed, and printed on a cotton broadcloth (122.5 g/m 2 ) using an auto screen printing machine (manufactured by Tsujii Senki Kogyo Co., Ltd.) so that the coating amount before drying was 100 g/m 2 , and dried in a hot air circulation dryer at 150° C. for 2 minutes to obtain a sample for evaluation. The a* value was measured in the same manner as in Example 1, except that the stain component (A) was dropped onto the sample.

[比較例4]
比較例1において、汚れ成分(A)を、汚れ成分(B)に変更した以外は、比較例1と同様にして、a*値を測定した。また、このa*値を、実施例2、及び比較例5の色変化量(Δa*)の基準とした。
[Comparative Example 4]
The a* value was measured in the same manner as in Comparative Example 1, except that the stain component (A) in Comparative Example 1 was changed to the stain component (B). This a* value was used as the standard for the color change (Δa*) in Example 2 and Comparative Example 5.

[比較例5]
比較例2において、汚れ成分(A)を、汚れ成分(B)に変更した以外は、比較例2と同様にして、a*値を測定した。
[Comparative Example 5]
The a* value was measured in the same manner as in Comparative Example 2, except that the stain component (A) in Comparative Example 2 was changed to the stain component (B).

[比較例6]
比較例1において、汚れ成分(A)を、汚れ成分(C)に変更した以外は、比較例1と同様にして、a*値を測定した。また、このa*値を、実施例3、及び比較例7の色変化量(Δa*)の基準とした。
[Comparative Example 6]
The a* value was measured in the same manner as in Comparative Example 1, except that the stain component (A) in Comparative Example 1 was changed to the stain component (C). This a* value was used as the standard for the color change (Δa*) in Example 3 and Comparative Example 7.

[比較例7]
比較例2において、汚れ成分(A)を、汚れ成分(C)に変更した以外は、比較例2と同様にして、a*値を測定した。
[Comparative Example 7]
The a* value was measured in the same manner as in Comparative Example 2, except that the stain component (A) in Comparative Example 2 was changed to the stain component (C).

[比較例8]
比較例1の綿ブロード生地に代えて、スレート板(ノザワ株式会社製)を用いた以外は、比較例1と同様にして、a*値を測定した。また、このa*値を、実施例4、及び比較例9の色変化量(Δa*)の基準とした。
[Comparative Example 8]
The a* value was measured in the same manner as in Comparative Example 1, except that a slate board (manufactured by Nozawa Co., Ltd.) was used instead of the cotton broadcloth of Comparative Example 1. This a* value was used as the standard for the color change (Δa*) of Example 4 and Comparative Example 9.

[比較例9]
比較例2において、綿ブロード生地に代えて、スレート板(ノザワ株式会社製)を用いた以外は、比較例2と同様にして、a*値を測定した。
[Comparative Example 9]
The a* value was measured in the same manner as in Comparative Example 2, except that a slate board (manufactured by Nozawa Co., Ltd.) was used instead of the cotton broadcloth.

[汚れ分解性の評価]
汚れを滴下した評価用試料を日中11時間(照度500~550ルクス、照度計「YOKOGAWA3281A」)で日中11時間、夜間(照度10ルクス以下)13時間静置し、滴下後1時間後(0日後)、n日後に、色彩色差計(コニカミノルタ株式会社製「CR-200」を使用して、汚れ滴下部分の測色を実施した。
汚れの分解効果は、基材(綿ブロード生地、スレート板)に汚れ成分のみを滴下した比較例のa*値を基準として差分Δa*により求めた。n日後のΔa*と初期(0日後)のΔa*から色変化量を評価し、色変化量がマイナス側になればなるほど、汚れ成分である色素が分解していることを示す。
[Evaluation of dirt decomposition ability]
The evaluation sample onto which the dirt was dropped was left to stand for 11 hours during the day (illuminance 500 to 550 lux, illuminance meter "YOKOGAWA 3281A") and for 13 hours at night (illuminance 10 lux or less), and the color of the portion onto which the dirt was dropped was measured using a color difference meter ("CR-200" manufactured by Konica Minolta, Inc.) 1 hour after dropping (0 days) and n days later.
The stain decomposition effect was calculated from the difference Δa* with the a* value of the comparative example in which only the stain component was dropped onto the substrate (cotton broadcloth, slate board) as the standard. The color change was evaluated from Δa* after n days and the initial value (0 days), and the more negative the color change, the more the stain component pigment was decomposed.

Figure 0007533710000002
Figure 0007533710000002

Figure 0007533710000003
Figure 0007533710000003

Figure 0007533710000004
Figure 0007533710000004

Figure 0007533710000005
Figure 0007533710000005

本発明のセルフクリーニング剤は、室内光の下で、優れた汚れ分解機能を有することが分かった。 The self-cleaning agent of the present invention was found to have excellent dirt-decomposing properties under indoor light.

一方、比較例1~9はいずれも、可視光応答型光触媒を含有しない態様であるが、室内光の下での汚れ分解性に劣っていた。 On the other hand, all of the comparative examples 1 to 9, which do not contain a visible light responsive photocatalyst, were inferior in dirt decomposition under indoor light.

Claims (6)

可視光応答型光触媒を含有し、前記可視光応答型光触媒が、酸化チタン(a)に金属化合物が担持されたものであり、
前記酸化チタン(a)が、ルチル型酸化チタン(a1)を含むものであって、前記酸化チタン(a)における前記ルチル型酸化チタン(a1)の含有率が50モル%以上であり、
前記可視光応答型光触媒におけるチタン100に対するジルコニウムの含有比(Zr/Ti比)が、0.03~0.8であり、前記可視光応答型光触媒におけるチタン100に対するニオブの含有比(Nb/Ti比)が、0.05~0.8であることを特徴とするセルフクリーニング剤。
The visible light responsive photocatalyst is a titanium oxide (a) having a metal compound supported thereon,
the titanium oxide (a) contains rutile-type titanium oxide (a1), and the content of the rutile-type titanium oxide (a1) in the titanium oxide (a) is 50 mol % or more;
The self-cleaning agent is characterized in that the content ratio of zirconium to titanium 100 in the visible light responsive photocatalyst (Zr/Ti ratio) is 0.03 to 0.8, and the content ratio of niobium to titanium 100 in the visible light responsive photocatalyst (Nb/Ti ratio) is 0.05 to 0.8.
前記酸化チタン(a)における前記ルチル型酸化チタン(a1)の含有率が90モル%以上である、請求項1記載のセルフクリーニング剤。 2. The self-cleaning agent according to claim 1, wherein the content of the rutile-type titanium oxide (a1) in the titanium oxide (a) is 90 mol % or more. 前記金属化合物が、2価銅化合物である請求項1又は2記載のセルフクリーニング剤。 The self-cleaning agent according to claim 1 or 2, wherein the metal compound is a divalent copper compound. 前記酸化チタン(a)のBET比表面積が、1~200m/gである請求項1~3のいずれか1項に記載のセルフクリーニング剤。 The self-cleaning agent according to any one of claims 1 to 3, wherein the titanium oxide (a) has a BET specific surface area of 1 to 200 m 2 /g. 前記可視光応答型光触媒におけるチタン100に対するジルコニウムの含有比(Zr/Ti比)が、0.05~0.3である請求項1~4のいずれか1項に記載のセルフクリーニング剤。 The self-cleaning agent according to any one of claims 1 to 4, wherein the content ratio of zirconium to titanium 100 (Zr/Ti ratio) in the visible light responsive photocatalyst is 0.05 to 0.3. 前記可視光応答型光触媒におけるチタン100に対するニオブの含有比(Nb/Ti比)が、0.1~0.3である請求項1~5のいずれか1項に記載のセルフクリーニング剤。 The self-cleaning agent according to any one of claims 1 to 5, wherein the content ratio of niobium to titanium 100 (Nb/Ti ratio) in the visible light responsive photocatalyst is 0.1 to 0.3.
JP2023108711A 2019-12-23 2023-06-30 Self-cleaning agent Active JP7533710B2 (en)

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
JP2019231480 2019-12-23
JP2019231480 2019-12-23
JP2021567469A JPWO2021132206A1 (en) 2019-12-23 2020-12-22
PCT/JP2020/047823 WO2021132206A1 (en) 2019-12-23 2020-12-22 Self-cleaning agent

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP2021567469A Division JPWO2021132206A1 (en) 2019-12-23 2020-12-22

Publications (3)

Publication Number Publication Date
JP2023130423A JP2023130423A (en) 2023-09-20
JP2023130423A5 JP2023130423A5 (en) 2023-12-25
JP7533710B2 true JP7533710B2 (en) 2024-08-14

Family

ID=76574132

Family Applications (2)

Application Number Title Priority Date Filing Date
JP2021567469A Pending JPWO2021132206A1 (en) 2019-12-23 2020-12-22
JP2023108711A Active JP7533710B2 (en) 2019-12-23 2023-06-30 Self-cleaning agent

Family Applications Before (1)

Application Number Title Priority Date Filing Date
JP2021567469A Pending JPWO2021132206A1 (en) 2019-12-23 2020-12-22

Country Status (3)

Country Link
JP (2) JPWO2021132206A1 (en)
CN (1) CN114829007B (en)
WO (1) WO2021132206A1 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP7809935B2 (en) * 2021-09-16 2026-02-03 Dic株式会社 Resin composition, coating agent, and article

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004082088A (en) 2001-10-15 2004-03-18 Jfe Steel Kk Photocatalysts and photocatalytic materials
JP2004322052A (en) 2003-04-28 2004-11-18 Toagosei Co Ltd Visible light-responsive photocatalyst
JP2004344863A (en) 2003-05-19 2004-12-09 Masanori Hirano Photocatalyst support porous gel and manufacturing method therefor
JP2007196182A (en) 2006-01-30 2007-08-09 Toray Ind Inc Bag cloth and bag filter
WO2008146711A1 (en) 2007-05-25 2008-12-04 Ishihara Sangyo Kaisha, Ltd. Complex, method for production of the same, and composition comprising the same
JP2011020033A (en) 2009-07-14 2011-02-03 Ishihara Sangyo Kaisha Ltd Visible light-responsive photocatalyst, method for producing the same and photocatalyst coating agent and photocatalyst dispersion obtained by using the same
WO2013094573A1 (en) 2011-12-22 2013-06-27 昭和電工株式会社 Copper-and-titanium-containing composition and production method therefor
JP2017155368A (en) 2016-03-03 2017-09-07 Dic株式会社 Resin composition for fiber processing and fabric using the same

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005138008A (en) * 2003-11-05 2005-06-02 National Institute For Materials Science Visible light responsive titanium oxide composite photocatalyst and process for producing the same
EP2491956A4 (en) * 2009-10-19 2013-11-20 Univ Tokyo METHOD FOR INACTIVATION OF A VIRUS AND ARTICLE PROVIDED WITH ANTIVIRAL PROPERTIES
JP5567828B2 (en) * 2009-11-30 2014-08-06 パナソニック株式会社 Visible light responsive photocatalyst coating material, coated product and allergen inactivation method
JP6040021B2 (en) * 2012-12-13 2016-12-07 昭和電工株式会社 Antibacterial antiviral composition and method for producing the same
KR20150074071A (en) * 2013-03-15 2015-07-01 쇼와 덴코 가부시키가이샤 Antibacterial, antiviral photocatalytic titanium oxide, and antibacterial, antiviral photocatalytic titanium oxide slurry dispersed in a neutral area, as well as method for manufacturing same
CN103852481B (en) * 2014-03-12 2016-03-02 攀钢集团攀枝花钢铁研究院有限公司 A kind of method measuring elemental composition in coating titanium white
JP7238877B2 (en) * 2020-11-10 2023-03-14 Dic株式会社 Aqueous composition of titanium oxide supporting metal compound
JP7235162B2 (en) * 2020-12-22 2023-03-08 Dic株式会社 Titanium oxide composition

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004082088A (en) 2001-10-15 2004-03-18 Jfe Steel Kk Photocatalysts and photocatalytic materials
JP2004322052A (en) 2003-04-28 2004-11-18 Toagosei Co Ltd Visible light-responsive photocatalyst
JP2004344863A (en) 2003-05-19 2004-12-09 Masanori Hirano Photocatalyst support porous gel and manufacturing method therefor
JP2007196182A (en) 2006-01-30 2007-08-09 Toray Ind Inc Bag cloth and bag filter
WO2008146711A1 (en) 2007-05-25 2008-12-04 Ishihara Sangyo Kaisha, Ltd. Complex, method for production of the same, and composition comprising the same
JP2011020033A (en) 2009-07-14 2011-02-03 Ishihara Sangyo Kaisha Ltd Visible light-responsive photocatalyst, method for producing the same and photocatalyst coating agent and photocatalyst dispersion obtained by using the same
WO2013094573A1 (en) 2011-12-22 2013-06-27 昭和電工株式会社 Copper-and-titanium-containing composition and production method therefor
JP2017155368A (en) 2016-03-03 2017-09-07 Dic株式会社 Resin composition for fiber processing and fabric using the same

Also Published As

Publication number Publication date
CN114829007A (en) 2022-07-29
JPWO2021132206A1 (en) 2021-07-01
JP2023130423A (en) 2023-09-20
CN114829007B (en) 2024-03-12
WO2021132206A1 (en) 2021-07-01

Similar Documents

Publication Publication Date Title
JP5343176B1 (en) Copper and titanium-containing composition and method for producing the same
JP6040021B2 (en) Antibacterial antiviral composition and method for producing the same
DE102004027549A1 (en) Carbonaceous titania photocatalyst and process for its preparation
US8298979B2 (en) Zirconium oxalate sol
JP7533710B2 (en) Self-cleaning agent
WO2015125367A1 (en) Antiviral composition, antiviral agent, photocatalyst and virus inactivation method
JP2007091574A (en) Method for producing highly active anatase-type titanium dioxide sol using metatitanic acid as a precursor
JP4436910B2 (en) Photocatalyst containing titanium oxide, its production method and use
JP2015059089A (en) Antiviral composition, method for preparing the same, and method for inactivating virus
JP5510521B2 (en) Photocatalyst particle dispersion and process for producing the same
JP2011079713A (en) Copper ion-modified titanium oxide, method for producing the same, and photocatalyst
JP7235162B2 (en) Titanium oxide composition
KR20230079058A (en) Composition for coating
JP5407549B2 (en) Photocatalyst particle dispersion and process for producing the same
JP6368926B2 (en) Photocatalyst coating composition
JP6485464B2 (en) Photocatalyst material, method for producing photocatalyst material, antiviral agent, antibacterial agent, photocatalyst coating composition, and photocatalyst-coated body
JP2020182918A (en) Method for producing titanium oxide composition
JP2015205254A (en) Photocatalyst composition, antiviral agent and antibacterial agent
JP2015134726A (en) Antiviral composition, production method thereof and virus inactivation method
JP5644877B2 (en) Method for producing dispersion of photocatalyst particles
JP2007314418A (en) Low halogen-low rutile type ultrafine-grained titanium oxide and production method thereof
JP3641269B1 (en) Method for producing titania solution
JP2023006883A (en) Copper-carrying titanium oxide slurry, method for producing copper-carrying titanium oxide slurry, and method for producing coating composition
JP2008246303A (en) Photocatalyst dispersion and method for producing the same
TW201300168A (en) The preparation of nano-metal supported on photocatalyst from wastewater

Legal Events

Date Code Title Description
A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20231215

A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20231215

A871 Explanation of circumstances concerning accelerated examination

Free format text: JAPANESE INTERMEDIATE CODE: A871

Effective date: 20231228

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20240326

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20240425

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20240702

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20240715

R150 Certificate of patent or registration of utility model

Ref document number: 7533710

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150