[go: up one dir, main page]

JP2018079432A - Iron compound-supported titanium oxide photocatalyst - Google Patents

Iron compound-supported titanium oxide photocatalyst Download PDF

Info

Publication number
JP2018079432A
JP2018079432A JP2016223952A JP2016223952A JP2018079432A JP 2018079432 A JP2018079432 A JP 2018079432A JP 2016223952 A JP2016223952 A JP 2016223952A JP 2016223952 A JP2016223952 A JP 2016223952A JP 2018079432 A JP2018079432 A JP 2018079432A
Authority
JP
Japan
Prior art keywords
photocatalyst
titanium oxide
iron
ppm
range
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.)
Granted
Application number
JP2016223952A
Other languages
Japanese (ja)
Other versions
JP6807629B2 (en
Inventor
徹 中井
Toru Nakai
徹 中井
伊藤 久義
Hisayoshi Ito
久義 伊藤
山下 行也
Yukiya Yamashita
行也 山下
慶 石黒
Kei Ishiguro
慶 石黒
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.)
Daicel Corp
Nippon Aerosil Co Ltd
Original Assignee
Daicel Corp
Nippon Aerosil Co Ltd
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 Daicel Corp, Nippon Aerosil Co Ltd filed Critical Daicel Corp
Priority to JP2016223952A priority Critical patent/JP6807629B2/en
Priority to TW106136524A priority patent/TW201819042A/en
Priority to KR1020170151341A priority patent/KR102445141B1/en
Priority to CN201711143958.6A priority patent/CN108067269B/en
Publication of JP2018079432A publication Critical patent/JP2018079432A/en
Application granted granted Critical
Publication of JP6807629B2 publication Critical patent/JP6807629B2/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J27/00Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • B01J27/06Halogens; Compounds thereof
    • B01J27/135Halogens; Compounds thereof with titanium, zirconium, hafnium, germanium, tin or lead
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J27/00Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • B01J27/06Halogens; Compounds thereof
    • B01J27/128Halogens; Compounds thereof with iron group metals or platinum group metals
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/74General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/86Catalytic processes
    • 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
    • B01J35/30Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
    • B01J35/39Photocatalytic 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
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/30Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
    • B01J35/391Physical properties of the active metal ingredient
    • 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
    • B01J35/60Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/61Surface area
    • B01J35/612Surface area less than 10 m2/g
    • 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
    • B01J35/60Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/61Surface area
    • B01J35/61310-100 m2/g
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/02Impregnation, coating or precipitation
    • B01J37/0201Impregnation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/34Irradiation by, or application of, electric, magnetic or wave energy, e.g. ultrasonic waves ; Ionic sputtering; Flame or plasma spraying; Particle radiation
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/18Oxygen-containing compounds, e.g. metal carbonyls
    • C08K3/20Oxides; Hydroxides
    • C08K3/22Oxides; Hydroxides of metals
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09DCOATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D7/00Features of coating compositions, not provided for in group C09D5/00; Processes for incorporating ingredients in coating compositions
    • C09D7/40Additives
    • C09D7/60Additives non-macromolecular
    • C09D7/61Additives non-macromolecular inorganic
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2255/00Catalysts
    • B01D2255/80Type of catalytic reaction
    • B01D2255/802Photocatalytic
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/18Oxygen-containing compounds, e.g. metal carbonyls
    • C08K3/20Oxides; Hydroxides
    • C08K3/22Oxides; Hydroxides of metals
    • C08K2003/2237Oxides; Hydroxides of metals of titanium
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K2201/00Specific properties of additives

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Materials Engineering (AREA)
  • Health & Medical Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Plasma & Fusion (AREA)
  • Toxicology (AREA)
  • Wood Science & Technology (AREA)
  • Inorganic Chemistry (AREA)
  • Medicinal Chemistry (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Polymers & Plastics (AREA)
  • Analytical Chemistry (AREA)
  • Biomedical Technology (AREA)
  • General Chemical & Material Sciences (AREA)
  • Catalysts (AREA)
  • Epidemiology (AREA)
  • Animal Behavior & Ethology (AREA)
  • General Health & Medical Sciences (AREA)
  • Public Health (AREA)
  • Veterinary Medicine (AREA)
  • Optics & Photonics (AREA)

Abstract

【課題】可視光線及び紫外線の何れに対しても優れた応答性を有する、高活性な光触媒、及びその製造方法を提供する。【解決手段】本発明の光触媒は、酸化チタン表面に鉄化合物を担持した構成を有する光触媒であって、前記酸化チタンの比表面積(BET法測定による)が7〜55m2/gの範囲であり、前記酸化チタンがルチル型とアナターゼ型とが30/70〜95/5(前者/後者(X線回折ピーク強度比))の範囲で混在した結晶型を有することを特徴とする。前記光触媒は、ルチル型とアナターゼ型とが30/70〜95/5(前者/後者(X線回折ピーク強度比))の範囲で混在した結晶型を有し、比表面積(BET法測定による)が7〜55m2/gの範囲である酸化チタンに塩化鉄(III)を担持させる工程を経て製造することができる。【選択図】なしProvided is a highly active photocatalyst having excellent responsiveness to both visible light and ultraviolet light, and a method for producing the same. The photocatalyst of the present invention is a photocatalyst having a structure in which an iron compound is supported on the surface of titanium oxide, wherein the specific surface area of the titanium oxide (measured by a BET method) is in a range of 7 to 55 m2 / g. The titanium oxide has a crystal type in which rutile type and anatase type are mixed in a range of 30/70 to 95/5 (the former / the latter (X-ray diffraction peak intensity ratio)). The photocatalyst has a crystal type in which rutile type and anatase type are mixed in a range of 30/70 to 95/5 (the former / the latter (X-ray diffraction peak intensity ratio)), and has a specific surface area (by BET method measurement). Can be produced through a step of supporting iron (III) chloride on titanium oxide having a range of 7 to 55 m2 / g. [Selection diagram] None

Description

本発明は、鉄化合物担持酸化チタン光触媒、その製造方法、前記光触媒を含むコーティング液、並びに前記光触媒を含むコーティング層を備えた光触媒塗装体に関する。   The present invention relates to an iron compound-supported titanium oxide photocatalyst, a production method thereof, a coating liquid containing the photocatalyst, and a photocatalyst-coated body provided with a coating layer containing the photocatalyst.

酸化チタンに紫外線を照射すると強い酸化力を有するラジカルが発生して、有機化合物(例えば、汚れ、悪臭ガス等)の酸化・分解、無機化合物(例えば、NOx、NH3等)の酸化、ウィルス、細菌、カビ等の死滅、不活性化などに効果を発揮することから、近年、環境浄化、脱臭、防汚、抗菌、防カビなどに応用が進められている。しかし、酸化チタンは太陽光の照射下では優れた光触媒能を発揮できるが、白熱灯、蛍光灯等の通常の生活空間における光源に含まれる紫外線量は4%程度と少なく、大部分が可視光線と赤外線で構成されていることから、このような光源下では十分な光触媒能を発揮することができないという問題があった。 And radicals having a strong oxidizing power is irradiated with ultraviolet rays of titanium oxide is generated, an organic compound (e.g., dirt, malodorous gas, etc.) oxidation and decomposition of the oxidation of inorganic compounds (e.g., NOx, NH 3, etc.), viruses, Since it is effective in killing and inactivating bacteria and molds, it has been applied to environmental purification, deodorization, antifouling, antibacterial, and antifungal in recent years. However, although titanium oxide can exhibit excellent photocatalytic activity under sunlight, the amount of ultraviolet rays contained in light sources in ordinary living spaces such as incandescent lamps and fluorescent lamps is as low as 4%, and most of them are visible light. Therefore, there is a problem that sufficient photocatalytic ability cannot be exhibited under such a light source.

上記問題を解決する方法としては、酸化チタンに窒素や特定の金属(例えば、鉄化合物等)を担持させることにより、可視光応答性を付与する方法が知られている。特許文献1には、ルチル型とアナターゼ型が混在した結晶型を有する酸化チタン(ルチル型とアナターゼ型の混合割合(X線回折ピーク強度比)=約20/80、商品名「AEROXIDE TiO2 P25」、日本アエロジル(株)製)をFe(acac)3溶液中に浸漬させて、酸化チタン表面にFe(acac)3錯体を担持させ、その後、焼成により前記Fe(acac)3錯体を酸化鉄とすることで得られる酸化鉄担持酸化チタンは、優れた可視光応答性を有し、可視光線、紫外線の何れを照射した場合にも優れた光触媒活性を示すことが記載されている。しかし、未だ光触媒活性の点で不十分であった。 As a method for solving the above problem, a method of imparting visible light responsiveness by supporting titanium or a specific metal (for example, an iron compound) on titanium oxide is known. In Patent Document 1, titanium oxide having a crystal form in which rutile type and anatase type are mixed (mixing ratio of rutile type and anatase type (X-ray diffraction peak intensity ratio) = about 20/80, trade name “AEROXIDE TiO 2 P25”. "Japan Aerosil Co., Ltd., Ltd.) was immersed in Fe (acac) 3 solution, the surface of the titanium oxide by supporting Fe (acac) 3 complex, then, the iron oxide the Fe (acac) 3 complex by firing It is described that the iron oxide-supported titanium oxide obtained by the above has excellent visible light responsiveness and exhibits excellent photocatalytic activity when irradiated with either visible light or ultraviolet light. However, the photocatalytic activity is still insufficient.

特開2012−153591号公報JP2012-153591A

従って、本発明の目的は、可視光線及び紫外線の何れに対しても優れた応答性を有する、高活性な光触媒を提供することにある。
本発明の他の目的は、可視光線及び紫外線の何れに対しても優れた応答性を有する、高活性な光触媒の製造方法を提供することにある。
本発明の他の目的は、可視光線及び紫外線の何れに対しても優れた応答性を有する、高活性な光触媒を含むコーティング液を提供することにある。
本発明の他の目的は、可視光線及び紫外線の何れに対しても優れた応答性を有する、高活性な光触媒を含むコーティング層を備えた光触媒塗装体を提供することにある。
Accordingly, an object of the present invention is to provide a highly active photocatalyst having excellent responsiveness to both visible light and ultraviolet light.
Another object of the present invention is to provide a method for producing a highly active photocatalyst having excellent responsiveness to both visible light and ultraviolet light.
Another object of the present invention is to provide a coating liquid containing a highly active photocatalyst having excellent responsiveness to both visible light and ultraviolet light.
Another object of the present invention is to provide a photocatalyst-coated body having a coating layer containing a highly active photocatalyst having excellent responsiveness to both visible light and ultraviolet light.

本発明者等は上記課題を解決するため鋭意検討した結果、酸化チタンに鉄化合物を担持させて得られる光触媒について、ルチル型とアナターゼ型とが特定の割合で混在した結晶型を有する酸化チタンを使用すると、可視光線や紫外線の照射による光触媒活性が向上すること、更に、鉄化合物を担持する際に励起光の照射を行うと、可視光線や紫外線の照射による光触媒活性が飛躍的に向上することを見いだした。本発明はこれらの知見に基づいて完成させたものである。   As a result of diligent studies to solve the above problems, the present inventors have found that a photocatalyst obtained by supporting an iron compound on titanium oxide has a titanium oxide having a crystal type in which a rutile type and an anatase type are mixed at a specific ratio. When used, the photocatalytic activity by irradiation with visible light or ultraviolet light is improved, and further, when the excitation light is irradiated when supporting an iron compound, the photocatalytic activity by irradiation with visible light or ultraviolet light is dramatically improved. I found. The present invention has been completed based on these findings.

尚、本明細書において、「体積ppm」と記載した以外の「ppm」は「重量ppm」である。   In the present specification, “ppm” other than “volume ppm” is “ppm by weight”.

すなわち、本発明は、酸化チタン表面に鉄化合物を担持した構成を有する光触媒であって、前記酸化チタンの比表面積(BET法測定による)が7〜55m2/gの範囲であり、前記酸化チタンがルチル型とアナターゼ型とが30/70〜95/5(前者/後者(X線回折ピーク強度比))の範囲で混在した結晶型を有することを特徴とする光触媒を提供する。 That is, the present invention is a photocatalyst having a structure in which an iron compound is supported on the surface of titanium oxide, wherein the titanium oxide has a specific surface area (measured by a BET method) in the range of 7 to 55 m 2 / g, The present invention provides a photocatalyst characterized by having a crystal type in which rutile type and anatase type are mixed in a range of 30/70 to 95/5 (the former / the latter (X-ray diffraction peak intensity ratio)).

本発明は、また、反応容器(容量:200mL)の中に、当該光触媒200mgを仕込み、メタノールガス(空気希釈、800体積ppm)で前記反応容器内を満たした状態で、25℃において、24時間光照射(光源:405nmLED、照度:2.5W/m2)を行った際の前記反応容器中における二酸化炭素の生成量(濃度換算)が300体積ppm以上である、前記の光触媒を提供する。 In the present invention, 200 mg of the photocatalyst is charged in a reaction vessel (volume: 200 mL), and the reaction vessel is filled with methanol gas (air dilution, 800 ppm by volume) at 25 ° C. for 24 hours. Provided is the photocatalyst, wherein the amount of carbon dioxide produced (concentration conversion) in the reaction vessel upon light irradiation (light source: 405 nm LED, illuminance: 2.5 W / m 2 ) is 300 ppm by volume or more.

本発明は、また、酸化チタン基準での、鉄元素含有量が50〜2000ppm、塩素原子含有量が50〜1400ppmであり、鉄元素含有量/塩素原子含有量(重量比)が1.50以下である、前記の光触媒を提供する。   The present invention also has an iron element content of 50 to 2000 ppm, a chlorine atom content of 50 to 1400 ppm, and an iron element content / chlorine atom content (weight ratio) of 1.50 or less, based on titanium oxide. The above photocatalyst is provided.

本発明は、また、ルチル型とアナターゼ型とが30/70〜95/5(前者/後者(X線回折ピーク強度比))の範囲で混在した結晶型を有し、比表面積(BET法測定による)が7〜55m2/gの範囲である酸化チタンに塩化鉄(III)を担持させる工程を経て前記の光触媒を得る、光触媒の製造方法を提供する。 The present invention also has a crystal type in which rutile type and anatase type are mixed in the range of 30/70 to 95/5 (the former / the latter (X-ray diffraction peak intensity ratio)), and the specific surface area (BET method measurement) According to the present invention, there is provided a method for producing a photocatalyst, wherein the photocatalyst is obtained through a step of supporting iron (III) chloride on titanium oxide having a range of 7 to 55 m 2 / g.

本発明は、また、酸化チタンに塩化鉄(III)を担持させる際に励起光を照射する、前記の光触媒の製造方法を提供する。   The present invention also provides the method for producing the photocatalyst, wherein the excitation light is irradiated when iron (III) chloride is supported on titanium oxide.

本発明は、また、前記の光触媒を含むコーティング液を提供する。   The present invention also provides a coating liquid containing the photocatalyst.

本発明は、また、基材表面に前記の光触媒を含むコーティング層を備えた光触媒塗装体を提供する。   The present invention also provides a photocatalyst-coated body provided with a coating layer containing the above-mentioned photocatalyst on the surface of a substrate.

本発明の光触媒は、紫外線域から可視光線域の広い波長範囲の光を吸収することにより、価電子帯にホール、伝導帯に励起電子を生成し、光触媒表面に付着した種々の物質を酸化、或いは還元して、環境浄化、脱臭、防汚、抗菌、又は防カビ効果を発現する。そのため、本発明の光触媒は、太陽光だけでなく、白熱灯、蛍光灯、及びLEDライト等の通常の生活空間における紫外線量の少ない光源を利用して優れた光触媒能を発揮することができ、車内や屋内等の従来は光触媒能を十分に発揮することが困難であった空間において環境浄化等に好適に使用することができる。   The photocatalyst of the present invention absorbs light in a wide wavelength range from the ultraviolet region to the visible light region, thereby generating holes in the valence band, excited electrons in the conduction band, and oxidizing various substances attached to the surface of the photocatalyst. Or it reduces and expresses environmental purification, deodorization, antifouling, antibacterial, or antifungal effect. Therefore, the photocatalyst of the present invention can exhibit excellent photocatalytic ability using not only sunlight but also a light source with a small amount of ultraviolet light in a normal living space such as an incandescent lamp, a fluorescent lamp, and an LED light, Conventionally, it can be suitably used for environmental purification or the like in a space where it has been difficult to sufficiently exhibit the photocatalytic activity, such as in a car or indoors.

実施例及び比較例で得られた光触媒の光触媒活性を示す図である。It is a figure which shows the photocatalytic activity of the photocatalyst obtained by the Example and the comparative example. 実施例及び比較例で得られた光触媒の光触媒活性を示す図である。It is a figure which shows the photocatalytic activity of the photocatalyst obtained by the Example and the comparative example.

[光触媒]
本発明の光触媒は、酸化チタン表面に鉄化合物を担持した構成を有する光触媒であって、前記酸化チタンの比表面積(BET法測定による)が7〜55m2/gの範囲であり、前記酸化チタンがルチル型とアナターゼ型とが30/70〜95/5(前者/後者(X線回折ピーク強度比))の範囲で混在した結晶型を有することを特徴とする。
[photocatalyst]
The photocatalyst of the present invention is a photocatalyst having a structure in which an iron compound is supported on the surface of titanium oxide, wherein the titanium oxide has a specific surface area (measured by BET method) in the range of 7 to 55 m 2 / g, Is characterized in that the rutile type and the anatase type have a crystal type mixed in a range of 30/70 to 95/5 (the former / the latter (X-ray diffraction peak intensity ratio)).

本発明における酸化チタンは、ルチル型とアナターゼ型とが混在した結晶型を有する。本発明における酸化チタンは、更にその他の型(例えば、ブルッカイト型等)も含んでいても良いが、全酸化チタンのX線回折ピーク強度におけるルチル型のX線回折ピーク強度とアナターゼ型のX線回折ピーク強度の合計の占める割合は、例えば60%以上、好ましくは70%以上、特に好ましくは80%以上、最も好ましくは90%以上である。尚、上限は100%である。すなわち、その他の型の含有割合(2種以上含有する場合はその合計含有割合)は、例えば40%以下、好ましくは30%以下、特に好ましくは20%以下、最も好ましくは10%以下である。   The titanium oxide in the present invention has a crystal type in which a rutile type and an anatase type are mixed. The titanium oxide in the present invention may further include other types (for example, brookite type), but the rutile X-ray diffraction peak intensity and the anatase type X-ray in the X-ray diffraction peak intensity of all titanium oxides. The proportion of the total diffraction peak intensity is, for example, 60% or more, preferably 70% or more, particularly preferably 80% or more, and most preferably 90% or more. The upper limit is 100%. That is, the content ratio of other types (when two or more types are included, the total content ratio) is, for example, 40% or less, preferably 30% or less, particularly preferably 20% or less, and most preferably 10% or less.

前記酸化チタンにおけるルチル型とアナターゼ型の混合割合(前者/後者(X線回折ピーク強度比))は30/70〜95/5であり、触媒活性がより向上する観点から、好ましくは35/65〜90/10、特に好ましくは40/60〜85/15、最も好ましくは50/50を超え、85/15以下、とりわけ好ましくは50/50を超え、80/20以下である。ルチル型とアナターゼ型の混合割合が上記範囲を外れると、触媒活性が低下するため好ましくない。   The mixing ratio (the former / the latter (X-ray diffraction peak intensity ratio)) of the rutile type and the anatase type in the titanium oxide is 30/70 to 95/5, and preferably 35/65 from the viewpoint of further improving the catalytic activity. ~ 90/10, particularly preferably 40/60 to 85/15, most preferably more than 50/50, 85/15 or less, particularly preferably more than 50/50 and 80/20 or less. If the mixing ratio of the rutile type and the anatase type is out of the above range, the catalytic activity is lowered, which is not preferable.

尚、本発明において、酸化チタンにおけるルチル型とアナターゼ型の混合割合は、X線回折ピーク強度比によって示される。そして、X線回折ピーク強度比はルチル型結晶およびアナターゼ型結晶の最強回折線の強度比から算出することができ、例えば、X線回折装置としてCuの管球を用いた場合は、2θ=25.3°付近と2θ=27.4°付近に見られる両者の回折線のピークトップの比から算出することができる。   In the present invention, the mixing ratio of rutile type and anatase type in titanium oxide is indicated by the X-ray diffraction peak intensity ratio. The X-ray diffraction peak intensity ratio can be calculated from the intensity ratio of the strongest diffraction lines of the rutile type crystal and the anatase type crystal. For example, when a Cu tube is used as the X-ray diffractometer, 2θ = 25. It can be calculated from the ratio of the peak tops of both diffraction lines seen at around 3 ° and around 2θ = 27.4 °.

ルチル型とアナターゼ型とが上記範囲で混在した結晶型を有する酸化チタンの比表面積(BET法測定による)は7〜55m2/gの範囲であり、好ましくは7m2/g以上、50m2/g未満、より好ましくは10〜45m2/g、特に好ましくは10〜30m2/g、最も好ましくは10m2/g以上、30m2/g未満である。比表面積が上記範囲の酸化チタンは、高活性面の露出量が多く、優れた光触媒能を発揮することができる。尚、酸化チタンの比表面積は、窒素吸着法によって求められる。 The specific surface area of titanium oxide and rutile type and anatase type has a crystal form mixed in the above range (by BET method measurement) in the range of 7~55m 2 / g, preferably 7m 2 / g or more, 50 m 2 / g, more preferably 10 to 45 m 2 / g, particularly preferably 10 to 30 m 2 / g, most preferably 10 m 2 / g or more and less than 30 m 2 / g. Titanium oxide having a specific surface area in the above range has a large amount of exposure of the highly active surface and can exhibit excellent photocatalytic ability. The specific surface area of titanium oxide is determined by a nitrogen adsorption method.

酸化チタンの比表面積が上記範囲を下回ると、反応物質を吸着する能力が低下して光触媒能が低下する傾向がある。一方、酸化チタンの比表面積が上記範囲を上回ると、励起電子とホールの分離性が低下し、光触媒能が低下する傾向がある。   When the specific surface area of titanium oxide is less than the above range, the ability to adsorb reactants tends to decrease and the photocatalytic ability tends to decrease. On the other hand, when the specific surface area of titanium oxide exceeds the above range, the separability between excited electrons and holes tends to decrease, and the photocatalytic ability tends to decrease.

本発明の光触媒において、酸化チタン表面に担持する鉄化合物は、鉄イオン、鉄単体、鉄塩、鉄酸化物、鉄水酸化物、鉄錯体等のいずれの状態であってもよい。   In the photocatalyst of the present invention, the iron compound supported on the titanium oxide surface may be in any state such as iron ion, iron simple substance, iron salt, iron oxide, iron hydroxide, iron complex and the like.

本発明の光触媒における、酸化チタン基準での鉄元素含有量は、例えば50〜2000ppmであり、上限は、好ましくは1500ppm、より好ましくは1000ppm、更に好ましくは800ppm、特に好ましくは500ppm、最も好ましくは400ppm、とりわけ好ましくは300ppmである。また、下限は、好ましくは100ppm、更に好ましくは150ppm、特に好ましくは200ppmである。鉄元素含有量が上記範囲を上回ると、励起電子が有効に作用せず、光触媒能が低下する傾向がある。一方、鉄元素含有量が上記範囲を下回ると、可視光応答性が低下する傾向がある。   In the photocatalyst of the present invention, the content of iron element based on titanium oxide is, for example, 50 to 2000 ppm, and the upper limit is preferably 1500 ppm, more preferably 1000 ppm, still more preferably 800 ppm, particularly preferably 500 ppm, and most preferably 400 ppm. Particularly preferred is 300 ppm. The lower limit is preferably 100 ppm, more preferably 150 ppm, and particularly preferably 200 ppm. When the iron element content exceeds the above range, excited electrons do not act effectively, and the photocatalytic ability tends to decrease. On the other hand, when the iron element content is below the above range, the visible light responsiveness tends to decrease.

また、本発明の光触媒における、酸化チタン基準での塩素原子含有量は、例えば50〜1400ppmであり、上限は、好ましくは1200ppm、より好ましくは1000ppm、更に好ましくは900ppm、特に好ましくは800ppm、最も好ましくは750ppm、とりわけ好ましくは700ppmである。また、下限は、好ましくは100ppm、より好ましくは200ppm、更に好ましくは400ppm、特に好ましくは500ppm、最も好ましくは550ppm、とりわけ好ましくは600ppmである。塩素原子含有量が上記範囲を外れると、触媒活性が低下する傾向がある。   Further, the chlorine atom content on the basis of titanium oxide in the photocatalyst of the present invention is, for example, 50 to 1400 ppm, and the upper limit is preferably 1200 ppm, more preferably 1000 ppm, still more preferably 900 ppm, particularly preferably 800 ppm, and most preferably. Is 750 ppm, particularly preferably 700 ppm. The lower limit is preferably 100 ppm, more preferably 200 ppm, still more preferably 400 ppm, particularly preferably 500 ppm, most preferably 550 ppm, particularly preferably 600 ppm. When the chlorine atom content is outside the above range, the catalytic activity tends to decrease.

更に、本発明の光触媒における、酸化チタン基準での鉄元素含有量/塩素原子含有量(重量比)は、例えば1.50以下、好ましくは1.40以下、更に好ましくは1.0以下、より好ましくは0.8以下、特に好ましくは0.6以下、最も好ましくは0.5以下、とりわけ好ましくは0.4以下である。尚、下限は、例えば0.05、好ましくは0.1、特に好ましくは0.2、最も好ましくは0.25、とりわけ好ましくは0.3である。   Furthermore, in the photocatalyst of the present invention, the iron element content / chlorine atom content (weight ratio) based on titanium oxide is, for example, 1.50 or less, preferably 1.40 or less, more preferably 1.0 or less, and more. It is preferably 0.8 or less, particularly preferably 0.6 or less, most preferably 0.5 or less, and particularly preferably 0.4 or less. The lower limit is, for example, 0.05, preferably 0.1, particularly preferably 0.2, most preferably 0.25, and particularly preferably 0.3.

更に、本発明の光触媒は鉄化合物以外の遷移金属化合物を担持していても良いが、酸化チタンに担持される遷移金属化合物全量に占める鉄化合物の割合(金属元素換算)は、例えば80重量%以上、好ましくは90重量%以上、特に好ましくは95重量%以上である。すなわち、酸化チタンに担持される遷移金属化合物全量に占める、鉄化合物以外の遷移金属化合物の割合(金属元素換算)は、例えば20重量%以下、好ましくは10重量%以下、特に好ましくは5重量%以下である。他の遷移金属化合物の担持量が上記範囲を上回ると、本発明の効果が得られにくくなる傾向がある。   Furthermore, although the photocatalyst of the present invention may carry a transition metal compound other than the iron compound, the ratio of the iron compound to the total amount of the transition metal compound supported on the titanium oxide (in terms of metal element) is, for example, 80% by weight. Above, preferably 90% by weight or more, particularly preferably 95% by weight or more. That is, the ratio of the transition metal compound other than the iron compound to the total amount of the transition metal compound supported on titanium oxide (in terms of metal element) is, for example, 20% by weight or less, preferably 10% by weight or less, particularly preferably 5% by weight. It is as follows. If the amount of other transition metal compound supported exceeds the above range, the effect of the present invention tends to be difficult to obtain.

[光触媒の製造方法]
本発明の光触媒は、例えば、ルチル型とアナターゼ型とが30/70〜95/5(前者/後者(X線回折ピーク強度比))の範囲で混在した結晶型を有し、酸化チタンの比表面積(BET法測定による)は7〜55m2/gの範囲である酸化チタンに塩化鉄(III)を担持させる工程を経て製造することができる。
[Method for producing photocatalyst]
The photocatalyst of the present invention has, for example, a crystal type in which rutile type and anatase type are mixed in a range of 30/70 to 95/5 (the former / the latter (X-ray diffraction peak intensity ratio)), and the ratio of titanium oxide The surface area (according to the BET method measurement) can be produced through a step of supporting iron (III) chloride on titanium oxide having a range of 7 to 55 m 2 / g.

本発明の光触媒の製造に使用する酸化チタンは、ルチル型とアナターゼ型とが混在した結晶型を有し、ルチル型とアナターゼ型の混合割合(前者/後者(X線回折ピーク強度比))は30/70〜95/5であり、好ましくは35/65〜90/10、特に好ましくは40/60〜85/15、最も好ましくは50/50を超え、85/15以下、とりわけ好ましくは50/50を超え、80/20以下である。   The titanium oxide used for the production of the photocatalyst of the present invention has a crystal type in which rutile type and anatase type are mixed, and the mixing ratio of the rutile type and the anatase type (the former / the latter (X-ray diffraction peak intensity ratio)) is 30/70 to 95/5, preferably 35/65 to 90/10, particularly preferably 40/60 to 85/15, most preferably more than 50/50 and not more than 85/15, particularly preferably 50 / It exceeds 50 and is 80/20 or less.

ルチル型とアナターゼ型とが混在した結晶型を有する酸化チタンは、例えば、四塩化チタンをバーナー中で燃焼させる方法(気相法)にて製造することができる。また、気相法で製造されたルチル型とアナターゼ型とが混在した結晶型を有する酸化チタンをさらに高温で焼成して、アナターゼ型の一部をルチル型へ変換させることにより、ルチル型とアナターゼ型の混合割合を調整することができる。   Titanium oxide having a crystal type in which a rutile type and an anatase type are mixed can be produced, for example, by a method (gas phase method) in which titanium tetrachloride is burned in a burner. In addition, the rutile type and the anatase are produced by further baking a titanium oxide having a crystal type mixed with a rutile type and an anatase type produced by a vapor phase method at a high temperature to convert a part of the anatase type into a rutile type. The mixing ratio of the mold can be adjusted.

その他、アナターゼ型酸化チタンを気相にて500℃以上の温度で燃焼させてその一部をルチル型へ変換することにより製造することができ、燃焼時間を調整することでルチル型とアナターゼ型の割合をコントロールすることができる。尚、アナターゼ型酸化チタンは、周知慣用の方法(例えば、下記(I)〜(III)の方法)で製造することができる。
(I)チタンテトライソプロポキシドを600〜800℃の温度での熱分解反応に付す方法(気相法)
(II)ゾル−ゲル法で得られた非晶質酸化チタンを、300〜600℃の温度で焼成する方法(液相法)
(III)オートクレーブ中、チタンアルコキシドを250〜300℃で水熱処理する方法(水熱法)
In addition, it can be manufactured by burning anatase-type titanium oxide in the gas phase at a temperature of 500 ° C. or higher and converting a part thereof to the rutile type. By adjusting the combustion time, the rutile type and the anatase type can be produced. The ratio can be controlled. In addition, anatase type titanium oxide can be manufactured by a well-known and commonly used method (for example, methods (I) to (III) below).
(I) Method of subjecting titanium tetraisopropoxide to a thermal decomposition reaction at a temperature of 600 to 800 ° C. (gas phase method)
(II) A method of firing amorphous titanium oxide obtained by a sol-gel method at a temperature of 300 to 600 ° C. (liquid phase method)
(III) Method of hydrothermally treating titanium alkoxide at 250 to 300 ° C. in an autoclave (hydrothermal method)

酸化チタンに塩化鉄(III)を担持させる方法としては、例えば、酸化チタンに塩化鉄(III)を含浸させる含浸法により行うことができる。   As a method of supporting iron (III) chloride on titanium oxide, for example, an impregnation method in which titanium oxide is impregnated with iron (III) chloride can be performed.

含浸は、具体的には、酸化チタンの水懸濁液中に塩化鉄(III)水溶液を添加することにより行うことができる。塩化鉄(III)水溶液中の塩化鉄(III)濃度は、例えば10〜80重量%程度である。含浸時間としては、例えば1〜48時間程度、好ましくは3〜24時間、特に好ましくは3〜12時間である。塩化鉄(III)水溶液濃度や含浸時間を調整することにより、得られる光触媒の鉄元素含有量や塩素原子含有量をコントロールすることができる。   Specifically, the impregnation can be performed by adding an aqueous iron (III) chloride solution to an aqueous suspension of titanium oxide. The iron (III) chloride concentration in the iron (III) chloride aqueous solution is, for example, about 10 to 80% by weight. The impregnation time is, for example, about 1 to 48 hours, preferably 3 to 24 hours, and particularly preferably 3 to 12 hours. By adjusting the iron (III) chloride aqueous solution concentration and the impregnation time, the iron element content and chlorine atom content of the resulting photocatalyst can be controlled.

さらに、本発明においては、酸化チタンに塩化鉄(III)を含浸させる際、系内に犠牲剤を添加することが好ましい。犠牲剤を添加することにより、酸化チタンの表面に効率よく鉄化合物を担持させることができる。犠牲剤としては、それ自体が電子を放出しやすい有機化合物を使用することが好ましく、例えば、メタノール、エタノール等のアルコール;酢酸等のカルボン酸;エチレンジアミン四酢酸(EDTA)、トリエタノールアミン(TEA)等のアミン等を挙げることができる。   Furthermore, in the present invention, it is preferable to add a sacrificial agent to the system when impregnating titanium oxide with iron (III) chloride. By adding the sacrificial agent, the iron compound can be efficiently supported on the surface of the titanium oxide. As the sacrificial agent, it is preferable to use an organic compound that easily emits electrons. For example, alcohols such as methanol and ethanol; carboxylic acids such as acetic acid; ethylenediaminetetraacetic acid (EDTA) and triethanolamine (TEA) And the like.

犠牲剤の添加量は適宜調整することができ、例えば、酸化チタンの0.5〜20.0重量%程度、好ましくは1.0〜5.0重量%である。犠牲剤は過剰量を使用してもよい。   The addition amount of the sacrificial agent can be adjusted as appropriate, and is, for example, about 0.5 to 20.0% by weight of titanium oxide, preferably 1.0 to 5.0% by weight. An excessive amount of the sacrificial agent may be used.

本発明においては、酸化チタン表面に塩化鉄(III)を担持(若しくは、吸着)させる際に励起光を照射することが好ましい。励起光を照射すると、酸化チタンの表面の特定部位に担持された鉄イオンが選択的に剥がれることにより、酸化反応と還元反応の反応場が空間的に大きく引き離され、励起電子とホールの分離性が高められ、励起電子とホールの再結合及び逆反応の進行が極めて低く抑制されるためか、より一層優れた光触媒能を発揮することができる光触媒が得られる。   In the present invention, it is preferable to irradiate excitation light when iron (III) chloride is supported (or adsorbed) on the titanium oxide surface. When irradiated with excitation light, iron ions supported on specific sites on the surface of titanium oxide are selectively peeled off, so that the reaction field of oxidation and reduction is spatially separated and the separation between excited electrons and holes This is because the recombination of excited electrons and holes and the progress of the reverse reaction are suppressed to be extremely low, so that a photocatalyst capable of exhibiting a further excellent photocatalytic ability can be obtained.

励起光の照射は、例えば、紫外線等の、バンドギャップエネルギー以上のエネルギーを有する光を照射することにより行うことができる。紫外線を照射する場合は、例えば、中・高圧水銀灯、UVレーザー、UV−LED、ブラックライト等の紫外線露光装置を使用することができる。励起光の照射量としては、例えば0.1〜300mW/cm2程度、好ましくは0.5〜100mW/cm2である。励起光の照射時間としては、例えば1〜48時間程度、好ましくは3〜36時間、特に好ましくは6〜36時間である。 Irradiation with excitation light can be performed by irradiating light having energy equal to or higher than the band gap energy, such as ultraviolet rays. In the case of irradiating ultraviolet rays, for example, an ultraviolet exposure device such as a medium / high pressure mercury lamp, a UV laser, a UV-LED, or a black light can be used. The irradiation amount of the excitation light is, for example, about 0.1 to 300 mW / cm 2 , preferably 0.5 to 100 mW / cm 2 . The irradiation time of the excitation light is, for example, about 1 to 48 hours, preferably 3 to 36 hours, and particularly preferably 6 to 36 hours.

上記工程を経て得られた本発明の光触媒は、周知慣用の方法で精製することが好ましいく、特に、上記工程を経て得られた本発明の光触媒を、水懸濁液の上澄み液の電気伝導度が300μS/cm以下(例えば0.5〜300μS/cm)、好ましくは250μS/cm以下、特に好ましくは200μS/cm以下となるまで繰り返し水洗することが好ましい。水懸濁液の電気伝導度が上記範囲となるまで水洗することにより、光触媒に含まれる不純物[例えば、酸化チタンに含まれる未反応原料(チタン化合物)、鉄化合物(例えば、塩化鉄(III)、硝酸鉄(III)、硫酸鉄(III)等の3価の鉄化合物等)、反応中間体(例えば、2価の鉄化合物等)]を分離・除去することができ、光触媒能を一層向上させることができる。   The photocatalyst of the present invention obtained through the above steps is preferably purified by a well-known and commonly used method. In particular, the photocatalyst of the present invention obtained through the above steps is used for the electrical conduction of the supernatant liquid of the aqueous suspension. It is preferable to repeatedly wash with water until the degree becomes 300 μS / cm or less (for example, 0.5 to 300 μS / cm), preferably 250 μS / cm or less, particularly preferably 200 μS / cm or less. By washing with water until the electrical conductivity of the aqueous suspension is within the above range, impurities contained in the photocatalyst [for example, unreacted raw material (titanium compound) contained in titanium oxide, iron compound (for example, iron (III) chloride) , Iron (III) nitrate, trivalent iron compounds such as iron (III) sulfate), and reaction intermediates (for example, divalent iron compounds)] can be separated and removed, further improving the photocatalytic performance. Can be made.

上記水洗に使用する水としては、例えば、精製水、蒸留水、イオン交換水、純水等を挙げることができる。   Examples of water used for the water washing include purified water, distilled water, ion exchange water, and pure water.

水洗処理方法としては、例えば、水に分散−水洗−遠心分離を、遠心分離後の上澄み液の電気伝導度が上記範囲となるまで繰り返し行う方法や、濾過膜を使用して濾過液(若しくは透過液)の電気伝導度が上記範囲になるまで繰り返し膜濾過する方法が挙げられる。膜濾過には、全量ろ過方式とクロスフロー方式(濾過膜面に平行に被処理水を流し、流れの側方で濾過する方式)が含まれる。本発明においては、特に、クロスフロー方式により膜濾過することが、本発明の光触媒の結晶構造及び分散性を維持しつつ、イオン性不純物の含有量を低減することができる点で好ましい。   As the washing treatment method, for example, dispersion in water, washing in water, and centrifugation are repeated until the electrical conductivity of the supernatant after centrifugation is within the above range, or a filtrate (or permeation through a filtration membrane) is used. Examples of the method include repeated membrane filtration until the electrical conductivity of the liquid reaches the above range. Membrane filtration includes a total amount filtration method and a cross flow method (a method in which water to be treated is flowed parallel to the filtration membrane surface and filtered on the side of the flow). In the present invention, it is particularly preferable to perform membrane filtration by the crossflow method in that the content of ionic impurities can be reduced while maintaining the crystal structure and dispersibility of the photocatalyst of the present invention.

上記方法により得られる本発明の光触媒は非常に優れた光触媒活性を有し、反応容器(容量:200mL)の中に、当該光触媒200mgを仕込み、メタノールガス(空気希釈、800体積ppm)で前記反応容器内を満たした状態で、25℃において、24時間光照射(光源:405nmLED、照度:2.5W/m2)を行った際の前記反応容器中における二酸化炭素の生成量(濃度換算)は、例えば300体積ppm以上、好ましくは400体積ppm以上、より好ましくは500体積ppm以上、特に好ましくは650体積ppm以上、最も好ましくは700体積ppm以上、とりわけ好ましくは760体積ppm以上である。尚、上限は1000ppm程度である。 The photocatalyst of the present invention obtained by the above method has a very excellent photocatalytic activity, and 200 mg of the photocatalyst is charged in a reaction vessel (volume: 200 mL), and the reaction is performed with methanol gas (air dilution, 800 ppm by volume). The amount of carbon dioxide produced (concentration conversion) in the reaction vessel when irradiated with light (light source: 405 nm LED, illuminance: 2.5 W / m 2 ) for 24 hours at 25 ° C. with the inside of the vessel filled. For example, it is 300 volume ppm or more, preferably 400 volume ppm or more, more preferably 500 volume ppm or more, particularly preferably 650 volume ppm or more, most preferably 700 volume ppm or more, and particularly preferably 760 volume ppm or more. The upper limit is about 1000 ppm.

本発明の光触媒は紫外線域から可視光線域までの広い波長範囲において優れた応答性を有し、上述の通り優れた光触媒能を発揮することができるため、屋外だけでなく、屋内や車内等の紫外線量が低い環境下において、環境浄化や家電製品の高機能化等に応用が可能である。   The photocatalyst of the present invention has excellent responsiveness in a wide wavelength range from the ultraviolet region to the visible light region, and can exhibit excellent photocatalytic activity as described above, so that it can be used not only outdoors but also indoors and in vehicles. In an environment where the amount of ultraviolet rays is low, it can be applied to environmental purification and enhancement of functions of home appliances.

[コーティング液]
本発明のコーティング液は、任意の塗布対象物に塗布することで、当該塗布対象物表面に上記光触媒を含むコーティング層を形成する用途に用いられるものであり、少なくとも上記光触媒を含む。本発明のコーティング液は、上記光触媒の他に、例えば、バインダー樹脂、着色顔料、分散媒等を必要に応じて適宜含有することができる。
[Coating solution]
The coating liquid of this invention is used for the use which forms the coating layer containing the said photocatalyst on the said application | coating object surface by apply | coating to arbitrary application | coating objects, and contains the said photocatalyst at least. In addition to the photocatalyst, the coating liquid of the present invention can appropriately contain, for example, a binder resin, a color pigment, a dispersion medium, and the like as necessary.

本発明のコーティング液を、例えば、スプレー、刷毛、ローラー、グラビア印刷等を使用して塗布し、その後、乾燥及び/又は硬化させることによってコーティング層を形成することができる。   The coating liquid of the present invention can be applied by using, for example, spraying, brushing, roller, gravure printing, etc., and then dried and / or cured to form a coating layer.

[光触媒塗装体]
本発明の光触媒塗装体は、基材表面に前記光触媒を含むコーティング層を1層又は2層以上備えることを特徴とする。
[Photocatalyst coated body]
The photocatalyst-coated body of the present invention is characterized by comprising one or more coating layers containing the photocatalyst on the substrate surface.

コーティング層の厚み(2層以上有する場合はその総厚み)としては、例えば0.1〜1μm程度である。   The thickness of the coating layer (the total thickness when it has two or more layers) is, for example, about 0.1 to 1 μm.

素材からみた前記基材としては、例えば、各種プラスチック材料[例えば、ポリエチレン、ポリプロピレン、エチレン−プロピレン共重合体、エチレン−酢酸ビニル共重合体等のα−オレフィンをモノマー成分とするオレフィン系樹脂;ポリエチレンテレフタラート、ポリエチレンナフタレート、ポリブチレンテレフタラート等のポリエステル系樹脂;ポリ塩化ビニル;酢酸ビニル系樹脂;ポリフェニレンスルフィド;ポリアミド(ナイロン)、全芳香族ポリアミド(アラミド)等のアミド系樹脂;ポリイミド系樹脂;ポリエーテルエーテルケトン等]、ゴム材料(例えば、天然ゴム、合成ゴム、シリコンゴム等)、金属材料(例えば、アルミニウム、銅、鉄、ステンレス等)、紙質材料(例えば、紙、紙類似物質等)、木質材料(例えば、木材、MDF等の木質ボード、合板等)、繊維材料(例えば、不織布、織布等)、革材料、無機材料(例えば、石、コンクリート等)、ガラス材料、磁器材料等の各種の素材を挙げることができる。   Examples of the base material from the viewpoint of materials include various plastic materials [for example, olefin-based resins containing α-olefin as a monomer component such as polyethylene, polypropylene, ethylene-propylene copolymer, ethylene-vinyl acetate copolymer; polyethylene Polyester resins such as terephthalate, polyethylene naphthalate, polybutylene terephthalate; polyvinyl chloride; vinyl acetate resin; polyphenylene sulfide; amide resins such as polyamide (nylon) and wholly aromatic polyamide (aramid); polyimide resin Polyetheretherketone, etc.], rubber materials (eg, natural rubber, synthetic rubber, silicon rubber, etc.), metal materials (eg, aluminum, copper, iron, stainless steel, etc.), paper materials (eg, paper, paper-like substances, etc.) ), Woody materials (eg, Materials, wood boards such as MDF, plywood, etc.), fiber materials (eg, non-woven fabric, woven fabric, etc.), leather materials, inorganic materials (eg, stone, concrete, etc.), glass materials, porcelain materials, etc. be able to.

用途からみた前記基材としては、例えば、レンズ(例えば、眼鏡やカメラのレンズ等)、プリズム、自動車や鉄道車両等の乗物部材(窓ガラス、照明灯カバー、バックミラー等)、建築部材(例えば、外壁材、内壁材、窓枠、窓ガラス等)、機械構成部材、交通標識等の各種表示装置、広告塔、遮音壁(道路用、鉄道用等)、橋梁、ガードレール、トンネル、碍子、太陽電池カバー、太陽熱温水器集熱カバー、照明器具、浴室用品、浴室部材(例えば、鏡、浴槽等)、台所用品、台所部材(例えば、キッチンパネル、流し台、レンジフード、換気扇等)、空調、トイレ用品、トイレ部材(例えば、便器等)等の抗菌、防カビ、脱臭、大気浄化、水質浄化、防汚効果が期待される物品や、前記物品表面に貼着させるためのフィルム、シート、シール等を挙げることができる。   Examples of the base material from the viewpoint of use include lenses (for example, glasses and camera lenses), prisms, vehicle members such as automobiles and railway vehicles (window glass, illumination lamp covers, rearview mirrors, etc.), building members (for example, , Outer wall materials, inner wall materials, window frames, window glass, etc.), machine components, various display devices such as traffic signs, advertising towers, sound insulation walls (for roads, railways, etc.), bridges, guardrails, tunnels, insulators, solar cells Covers, solar water heater heat collection covers, lighting fixtures, bathroom items, bathroom components (eg, mirrors, bathtubs, etc.), kitchen appliances, kitchen components (eg, kitchen panels, sinks, range hoods, exhaust fans, etc.), air conditioning, toilet articles , Articles such as toilet members (for example, toilets), antibacterial, antifungal, deodorizing, air purification, water purification, antifouling effects, and films, sheets, paper Mention may be made of the Le and the like.

本発明の光触媒塗装体は、上記光触媒を含むコーティング層を有するため、太陽光の照射環境下はもちろん、白熱灯、蛍光灯等の通常の生活空間の低照度環境下でも、優れた抗菌、防カビ、脱臭、大気浄化、水質浄化、防汚等の効果を発揮することができる。   The photocatalyst-coated body of the present invention has a coating layer containing the above-mentioned photocatalyst, so that it has excellent antibacterial and antibacterial properties not only in the sunlight irradiation environment but also in a low-light environment such as an incandescent lamp and a fluorescent lamp. Effects such as mold, deodorization, air purification, water purification, and antifouling can be exhibited.

以下、実施例により本発明をより具体的に説明するが、本発明はこれらの実施例により限定されるものではない。   EXAMPLES Hereinafter, although an Example demonstrates this invention more concretely, this invention is not limited by these Examples.

調製例1
四塩化チタンをバーナー中で燃焼させ、酸化チタン(30)[比表面積:45m2/g、ルチル型とアナターゼ型の混合割合(X線回折ピーク強度比):30/70)が混在した結晶型を有する]を製造した。
Preparation Example 1
Crystalline form in which titanium tetrachloride is burned in a burner and mixed with titanium oxide (30) [specific surface area: 45 m 2 / g, mixing ratio of rutile type and anatase type (X-ray diffraction peak intensity ratio): 30/70) Has been manufactured.

調製例2
四塩化チタンをバーナー中で燃焼させ、酸化チタン(50)[比表面積:30m2/g、ルチル型とアナターゼ型の混合割合(X線回折ピーク強度比):50/50]を製造した。
Preparation Example 2
Titanium tetrachloride was burned in a burner to produce titanium oxide (50) [specific surface area: 30 m 2 / g, mixing ratio of rutile type and anatase type (X-ray diffraction peak intensity ratio): 50/50].

調製例3
調製例1で得られた酸化チタン(30)を大気中、電気炉で1000℃で90分加熱することにより、酸化チタン(71)[比表面積:20m2/g、ルチル型とアナターゼ型の混合割合(X線回折ピーク強度比):71/29]を製造した。
Preparation Example 3
Titanium oxide (30) obtained in Preparation Example 1 was heated in the electric furnace at 1000 ° C. for 90 minutes in the atmosphere to obtain titanium oxide (71) [specific surface area: 20 m 2 / g, mixed rutile type and anatase type. Ratio (X-ray diffraction peak intensity ratio): 71/29].

実施例1
調製例1で得られた酸化チタン(30)10gとイオン交換水90gを撹拌混合して懸濁液を得た。
得られた懸濁液に、塩化鉄(III)水溶液(塩化鉄(III)濃度:38重量%)0.15gを添加し、25℃にて30分間撹拌した。その後、メタノール2.3g(酸化チタンの23重量%に相当)を添加し、更に6時間撹拌した。
その後、懸濁液を、上澄み液の電気伝導度が200μS/cm以下となるまで水洗を行う粉体洗浄に付し、高速遠心沈降機(遠心力:20000G、遠心時間:10〜20分)を用いて粉体を沈降させた。
沈降した粉体を分取し、真空乾燥機を用いて60℃で乾燥を行って乾燥粉体を得た。
得られた乾燥粉体を乳鉢ですり潰して、光触媒(1)(Fe/酸化チタン(30)、酸化チタンに対して、鉄元素含有量:1820ppm、塩素原子含有量:1310ppm、鉄元素含有量/塩素原子含有量:1.39)を得た。
Example 1
10 g of titanium oxide (30) obtained in Preparation Example 1 and 90 g of ion-exchanged water were stirred and mixed to obtain a suspension.
To the obtained suspension, 0.15 g of an aqueous iron (III) chloride solution (iron (III) chloride concentration: 38% by weight) was added, and the mixture was stirred at 25 ° C. for 30 minutes. Thereafter, 2.3 g of methanol (corresponding to 23% by weight of titanium oxide) was added, and the mixture was further stirred for 6 hours.
Thereafter, the suspension is subjected to powder washing in which the supernatant is washed with water until the electric conductivity of the supernatant becomes 200 μS / cm or less, and a high-speed centrifugal sedimentator (centrifugal force: 20000 G, centrifugation time: 10 to 20 minutes) is used. Used to settle the powder.
The settled powder was collected and dried at 60 ° C. using a vacuum dryer to obtain a dry powder.
The obtained dry powder was ground in a mortar, and with respect to the photocatalyst (1) (Fe / titanium oxide (30), titanium oxide, iron element content: 1820 ppm, chlorine atom content: 1310 ppm, iron element content / Chlorine atom content: 1.39) was obtained.

実施例2
調製例1で得られた酸化チタン(30)に代えて、調製例3で得られた酸化チタン(71)を使用した以外は実施例1と同様にして、光触媒(2)(Fe/酸化チタン(71)、酸化チタンに対して、鉄元素含有量:1740ppm、塩素原子含有量:1270ppm、鉄元素含有量/塩素原子含有量:1.37)を得た。
Example 2
The photocatalyst (2) (Fe / titanium oxide) was prepared in the same manner as in Example 1 except that the titanium oxide (71) obtained in Preparation Example 3 was used instead of the titanium oxide (30) obtained in Preparation Example 1. (71), with respect to titanium oxide, iron element content: 1740 ppm, chlorine atom content: 1270 ppm, iron element content / chlorine atom content: 1.37).

実施例3
懸濁液に、塩化鉄(III)水溶液とメタノールを添加した後、10Wのブラックライトを用いて紫外線(UV)を6時間照射(UV照射量:10mW/cm2)した以外は実施例1と同様にして、光触媒(3)(Fe/酸化チタン(30)(UV)、酸化チタンに対して、鉄元素含有量:230ppm、塩素原子含有量:650ppm、鉄元素含有量/塩素原子含有量:0.35)を得た。
Example 3
Example 1 except that an aqueous solution of iron (III) chloride and methanol were added to the suspension, followed by irradiation with ultraviolet rays (UV) for 6 hours using a 10 W black light (UV irradiation amount: 10 mW / cm 2 ). Similarly, with respect to photocatalyst (3) (Fe / titanium oxide (30) (UV), titanium oxide), iron element content: 230 ppm, chlorine atom content: 650 ppm, iron element content / chlorine atom content: 0.35) was obtained.

実施例4
調製例1で得られた酸化チタン(30)に代えて、調製例2で得られた酸化チタン(50)を使用して懸濁液を得、得られた懸濁液に、塩化鉄(III)水溶液とメタノールを添加した後、10Wのブラックライトを用いて紫外線(UV)を6時間照射(UV照射量:10mW/cm2)した以外は実施例1と同様にして、光触媒(4)(Fe/酸化チタン(50)(UV)、酸化チタンに対して、鉄元素含有量:220ppm、塩素原子含有量:630ppm、鉄元素含有量/塩素原子含有量:0.35)を得た。
Example 4
Instead of the titanium oxide (30) obtained in Preparation Example 1, a suspension was obtained using the titanium oxide (50) obtained in Preparation Example 2, and the resulting suspension was subjected to iron chloride (III ) Photocatalyst (4) (4) (Addition of aqueous solution and methanol in the same manner as in Example 1 except that ultraviolet rays (UV) were irradiated for 6 hours using a 10 W black light (UV irradiation amount: 10 mW / cm 2 ). With respect to Fe / titanium oxide (50) (UV) and titanium oxide, iron element content: 220 ppm, chlorine atom content: 630 ppm, iron element content / chlorine atom content: 0.35) were obtained.

実施例5
調製例1で得られた酸化チタン(30)に代えて、調製例3で得られた酸化チタン(71)を使用して懸濁液を得、得られた懸濁液に、塩化鉄(III)水溶液とメタノールを添加した後、10Wのブラックライトを用いて紫外線(UV)を6時間照射(UV照射量:10mW/cm2)した以外は実施例1と同様にして、光触媒(5)(Fe/酸化チタン(71)(UV)、酸化チタンに対して、鉄元素含有量:210ppm、塩素原子含有量:620ppm、鉄元素含有量/塩素原子含有量:0.34)を得た。
Example 5
Instead of the titanium oxide (30) obtained in Preparation Example 1, a suspension was obtained using the titanium oxide (71) obtained in Preparation Example 3, and the resulting suspension was subjected to iron chloride (III ) Photocatalyst (5) in the same manner as in Example 1 except that after adding an aqueous solution and methanol, ultraviolet rays (UV) were irradiated for 6 hours using a 10 W black light (UV irradiation amount: 10 mW / cm 2 ). With respect to Fe / titanium oxide (71) (UV) and titanium oxide, iron element content: 210 ppm, chlorine atom content: 620 ppm, iron element content / chlorine atom content: 0.34) were obtained.

比較例1
調製例1で得られた酸化チタン(30)に代えて、酸化チタン(20)(ルチル型とアナターゼ型が混在した結晶型を有する酸化チタン、ルチル型とアナターゼ型の混合割合(X線回折ピーク強度比):20/80、比表面積:50m2/g、商品名「AEROXIDE TiO2 P25」、日本アエロジル(株)製)を使用した以外は実施例1と同様にして、光触媒(7)(Fe/酸化チタン(20)、酸化チタンに対して、鉄元素含有量:2120ppm、塩素原子含有量:1500ppm、鉄元素含有量/塩素原子含有量:1.41)を得た。
Comparative Example 1
Instead of the titanium oxide (30) obtained in Preparation Example 1, titanium oxide (20) (titanium oxide having a crystal form in which rutile type and anatase type are mixed, mixing ratio of rutile type and anatase type (X-ray diffraction peak) Intensity ratio): 20/80, specific surface area: 50 m 2 / g, trade name “AEROXIDE TiO 2 P25” manufactured by Nippon Aerosil Co., Ltd.), and photocatalyst (7) (7) With respect to Fe / titanium oxide (20) and titanium oxide, iron element content: 2120 ppm, chlorine atom content: 1500 ppm, iron element content / chlorine atom content: 1.41).

<鉄元素含有量の測定方法>
光触媒の鉄元素含有量は、以下の方法で測定した。
光触媒約20mgを精秤し、硫酸1mLを加えた後、砂浴上で加熱溶解した。溶解後、少量の超純水を加えてリフラックスした後、これをIWAKI製PP容器にて20mLにメスアップし、更に0.2μmフィルター処理を施してサンプルを調製し、これをICP発光分析(ICP発光分析装置:(株)リガク製、CIROS)に付した。
また、光触媒を加えなかった以外は前記と同様にして得られたサンプルをブランクとして使用した。検量線用の標準液は、SPEX社製ICP−MS用混合標準液XSTC−22を同濃度の硫酸水溶液にて希釈調整したものを使用した。
<Measurement method of iron element content>
The iron element content of the photocatalyst was measured by the following method.
About 20 mg of the photocatalyst was precisely weighed, 1 mL of sulfuric acid was added, and then dissolved by heating on a sand bath. After dissolution, a small amount of ultrapure water is added and refluxed, and this is made up to 20 mL in an IWAKI PP container, further 0.2 μm filtered to prepare a sample, and this is analyzed by ICP emission spectrometry ( ICP emission analyzer: manufactured by Rigaku Corporation, CIROS).
Moreover, the sample obtained by carrying out similarly to the above except having not added a photocatalyst was used as a blank. As the standard solution for the calibration curve, a solution prepared by diluting a mixed standard solution XSTC-22 for ICP-MS manufactured by SPEX with an aqueous sulfuric acid solution having the same concentration was used.

<塩素原子含有量の測定方法>
光触媒の塩素原子含有量は、下記条件で測定した。
燃焼条件
使用機器:ダイアインスツルメンツ製AQF−100
サンプル:約20mg
燃焼プログラム:2
吸収液:H22150ppm
内部標準液:酒石酸5ppm
吸収液量:10mL
イオンクロマト条件
使用機器:DIONEX ICS−2000(低濃度分析モード)
本カラム:AS−12
プレカラム:AG−12
溶離液:3.0mM K2CO3+0.3mM EPM
サプレッサー:ASRS(リサイクルモード)
流速:1.2mL/分
検出器:電気伝導度検出器
カラム温度:35℃
注入量:100μL
<Method for measuring chlorine atom content>
The chlorine atom content of the photocatalyst was measured under the following conditions.
Combustion conditions Equipment used: AQF-100 manufactured by Dia Instruments
Sample: about 20mg
Combustion program: 2
Absorbent: H 2 O 2 150 ppm
Internal standard solution: Tartaric acid 5ppm
Absorbing liquid volume: 10mL
Ion chromatography conditions Equipment used: DIONEX ICS-2000 (low concentration analysis mode)
This column: AS-12
Precolumn: AG-12
Eluent: 3.0 mM K 2 CO 3 +0.3 mM EPM
Suppressor: ASRS (recycle mode)
Flow rate: 1.2 mL / min Detector: Conductivity detector Column temperature: 35 ° C
Injection volume: 100 μL

<光触媒活性評価方法(メタノール酸化法)>
光触媒(1)〜(7)、及び酸化チタン(20)の光触媒活性は、メタノールを酸化し、生成するCO2量を測定することによりで光触媒活性を評価した。
すなわち、光触媒約200mgをガラス製皿に広げ、反応容器(容量:200mL、ANALYTIC−BARRIER、ジーエルサイエンス(株)製)の中に入れ、真空状態にした後、メタノールガス(空気希釈;800体積ppm)125mLを反応容器内に吹き込んだ。メタノールガスの光触媒への吸着が平衡に達した後、25℃で光照射(光源:405nmLED、照度:2.5W/m2)を行った。
光照射開始24時間後における反応容器内のCO2濃度をメタナイザー(商品名「MT221」、GLサイエンス(株)製)が付属した水素炎イオン化検出器付きガスクロマトグラフ(商品名「GC−14B」、島津製作所製)を使用して測定し、光照射開始前における反応用器内のCO2濃度を差し引いた値を、CO2の生成量とした。結果を図1、2に示す。
<Photocatalytic activity evaluation method (methanol oxidation method)>
The photocatalytic activities of the photocatalysts (1) to (7) and titanium oxide (20) were evaluated by oxidizing methanol and measuring the amount of CO 2 produced.
That is, about 200 mg of photocatalyst was spread on a glass dish, placed in a reaction vessel (capacity: 200 mL, ANALYTIC-BARRIER, manufactured by GL Sciences Inc.), evacuated, and then methanol gas (air diluted; 800 volume ppm) ) 125 mL was blown into the reaction vessel. After the adsorption of methanol gas to the photocatalyst reached equilibrium, light irradiation (light source: 405 nm LED, illuminance: 2.5 W / m 2 ) was performed at 25 ° C.
A gas chromatograph with a flame ionization detector (trade name “GC-14B”) attached with a methanizer (trade name “MT221”, manufactured by GL Science Co., Ltd.) for the CO 2 concentration in the reaction vessel 24 hours after the start of light irradiation, A value obtained by subtracting the CO 2 concentration in the reactor before the start of light irradiation was defined as the amount of CO 2 produced. The results are shown in FIGS.

図1、2より、ルチル型とアナターゼ型とが30/70〜95/5(前者/後者(X線回折ピーク強度比))の範囲で混在した結晶型を有する酸化チタンに鉄化合物を担持してなる本発明の光触媒は、ルチル型とアナターゼ型の混合割合が前記範囲を外れる酸化チタンに鉄化合物を担持してなる光触媒に比べて、触媒活性に優れることが分かる。
また、ルチル型とアナターゼ型の混合割合は、前記範囲内においてルチル型の含有割合が上がると、触媒活性が向上する傾向があることが分かる。
更に、鉄化合物担持の際に励起光を照射して得られる光触媒は、励起光を照射することなく得られた光触媒に比べて飛躍的に触媒活性が向上することが分かる。
1 and 2, an iron compound is supported on titanium oxide having a crystal type in which rutile type and anatase type are mixed in a range of 30/70 to 95/5 (the former / the latter (X-ray diffraction peak intensity ratio)). It can be seen that the photocatalyst of the present invention is superior in catalytic activity compared to a photocatalyst obtained by supporting an iron compound on titanium oxide in which the mixing ratio of the rutile type and the anatase type is outside the above range.
Moreover, it can be seen that the mixing ratio of the rutile type and the anatase type tends to improve the catalytic activity when the content ratio of the rutile type is increased within the above range.
Furthermore, it can be seen that the photocatalyst obtained by irradiating the excitation light when the iron compound is supported has dramatically improved catalytic activity compared to the photocatalyst obtained without irradiating the excitation light.

Claims (7)

酸化チタン表面に鉄化合物を担持した構成を有する光触媒であって、前記酸化チタンの比表面積(BET法測定による)が7〜55m2/gの範囲であり、前記酸化チタンがルチル型とアナターゼ型とが30/70〜95/5(前者/後者(X線回折ピーク強度比))の範囲で混在した結晶型を有することを特徴とする光触媒。 A photocatalyst having a structure in which an iron compound is supported on a titanium oxide surface, wherein the titanium oxide has a specific surface area (measured by a BET method) in a range of 7 to 55 m 2 / g, and the titanium oxide has a rutile type and an anatase type. Having a crystal type mixed in a range of 30/70 to 95/5 (the former / the latter (X-ray diffraction peak intensity ratio)). 反応容器(容量:200mL)の中に、当該光触媒200mgを仕込み、メタノールガス(空気希釈、800体積ppm)で前記反応容器内を満たした状態で、25℃において、24時間光照射(光源:405nmLED、照度:2.5W/m2)を行った際の前記反応容器中における二酸化炭素の生成量(濃度換算)が300体積ppm以上である、請求項1に記載の光触媒。 In a reaction vessel (capacity: 200 mL), 200 mg of the photocatalyst was charged, and the reaction vessel was filled with methanol gas (air dilution, 800 ppm by volume). Light irradiation was performed at 25 ° C. for 24 hours (light source: 405 nm LED). , Illuminance: 2.5 W / m 2 ) The photocatalyst according to claim 1, wherein the amount of carbon dioxide produced (concentration conversion) in the reaction vessel is 300 ppm by volume or more. 酸化チタン基準での、鉄元素含有量が50〜2000ppm、塩素原子含有量が50〜1400ppmであり、鉄元素含有量/塩素原子含有量(重量比)が1.50以下である、請求項1又は2に記載の光触媒。   The iron element content on the basis of titanium oxide is 50 to 2000 ppm, the chlorine atom content is 50 to 1400 ppm, and the iron element content / chlorine atom content (weight ratio) is 1.50 or less. Or the photocatalyst of 2. ルチル型とアナターゼ型とが30/70〜95/5(前者/後者(X線回折ピーク強度比))の範囲で混在した結晶型を有し、比表面積(BET法測定による)が7〜55m2/gの範囲である酸化チタンに塩化鉄(III)を担持させる工程を経て請求項1〜3の何れか1項に記載の光触媒を得る、光触媒の製造方法。 The rutile type and anatase type have crystal types mixed in the range of 30/70 to 95/5 (the former / the latter (X-ray diffraction peak intensity ratio)), and the specific surface area (according to BET method measurement) is 7 to 55 m. A method for producing a photocatalyst, wherein the photocatalyst according to any one of claims 1 to 3 is obtained through a step of supporting iron (III) chloride on titanium oxide in a range of 2 / g. 酸化チタンに塩化鉄(III)を担持させる際に励起光を照射する、請求項4に記載の光触媒の製造方法。   The method for producing a photocatalyst according to claim 4, wherein the excitation light is irradiated when iron (III) chloride is supported on titanium oxide. 請求項1〜3の何れか1項に記載の光触媒を含むコーティング液。   The coating liquid containing the photocatalyst of any one of Claims 1-3. 基材表面に請求項1〜3の何れか1項に記載の光触媒を含むコーティング層を備えた光触媒塗装体。   The photocatalyst coating body provided with the coating layer containing the photocatalyst of any one of Claims 1-3 on the base-material surface.
JP2016223952A 2016-11-17 2016-11-17 Iron compound-supported titanium oxide photocatalyst Active JP6807629B2 (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
JP2016223952A JP6807629B2 (en) 2016-11-17 2016-11-17 Iron compound-supported titanium oxide photocatalyst
TW106136524A TW201819042A (en) 2016-11-17 2017-10-24 Titanium dioxide photocatalyst carrying iron compounds with excellent reactivity to both visible light and ultraviolet rays
KR1020170151341A KR102445141B1 (en) 2016-11-17 2017-11-14 Iron compound supported titanium oxide photocatalyst
CN201711143958.6A CN108067269B (en) 2016-11-17 2017-11-17 Titanium oxide photocatalyst having iron compound supported thereon

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2016223952A JP6807629B2 (en) 2016-11-17 2016-11-17 Iron compound-supported titanium oxide photocatalyst

Publications (2)

Publication Number Publication Date
JP2018079432A true JP2018079432A (en) 2018-05-24
JP6807629B2 JP6807629B2 (en) 2021-01-06

Family

ID=62157226

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2016223952A Active JP6807629B2 (en) 2016-11-17 2016-11-17 Iron compound-supported titanium oxide photocatalyst

Country Status (4)

Country Link
JP (1) JP6807629B2 (en)
KR (1) KR102445141B1 (en)
CN (1) CN108067269B (en)
TW (1) TW201819042A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3984623A4 (en) * 2019-06-13 2023-08-23 Liwei Huang NITRIC OXIDE ABSORBING SLURRY, MANUFACTURING METHOD THEREOF AND USE THEREOF

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR102089987B1 (en) * 2019-08-05 2020-03-18 주식회사 제이치글로벌 Air dome comprising visible light active photocatalyst

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001287996A (en) * 2000-04-03 2001-10-16 Toho Titanium Co Ltd Anatase-type titanium oxide single crystal
JP2006341250A (en) * 2000-12-28 2006-12-21 Showa Denko Kk High activity photo-catalyst
JP2011063473A (en) * 2009-09-16 2011-03-31 Toho Titanium Co Ltd Method for producing metal oxide-containing titanium oxide compound
JP2012153591A (en) * 2011-01-28 2012-08-16 Nippon Shokubai Co Ltd Composite oxide
WO2014046020A1 (en) * 2012-09-19 2014-03-27 株式会社ダイセル Transition metal compound-loaded titanium oxide
JP6010718B1 (en) * 2016-07-01 2016-10-19 株式会社ダイセル Iron compound-supported titanium oxide photocatalyst

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1243555B1 (en) * 1999-09-27 2007-11-14 Showa Denko K.K. Fine particulate titanium oxide and method for producing the same
CN101293669B (en) * 2008-06-20 2011-01-19 南开大学 Preparation method of nano titanium dioxide powder with controllable phase ratio of anatase and rutile
US9248432B2 (en) * 2011-06-27 2016-02-02 The University Of Tokyo Titanium oxide photocatalyst having copper compounds supported thereon, and method for producing same
EP2974793A4 (en) * 2013-03-15 2016-11-30 Daicel Corp Titanium oxide liquid dispersion, titanium oxide liquid coating, and photocatalyst coating film

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001287996A (en) * 2000-04-03 2001-10-16 Toho Titanium Co Ltd Anatase-type titanium oxide single crystal
JP2006341250A (en) * 2000-12-28 2006-12-21 Showa Denko Kk High activity photo-catalyst
JP2011063473A (en) * 2009-09-16 2011-03-31 Toho Titanium Co Ltd Method for producing metal oxide-containing titanium oxide compound
JP2012153591A (en) * 2011-01-28 2012-08-16 Nippon Shokubai Co Ltd Composite oxide
WO2014046020A1 (en) * 2012-09-19 2014-03-27 株式会社ダイセル Transition metal compound-loaded titanium oxide
JP6010718B1 (en) * 2016-07-01 2016-10-19 株式会社ダイセル Iron compound-supported titanium oxide photocatalyst

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
RIYAS, S. ET AL., BRITISH CERAMIC TRANSACTIONS, vol. 103, JPN6020018221, 2004, GB, pages 23 - 28, ISSN: 0004273972 *
SUN, Q. ET AL., JOURNAL OF HAZARDOUS MATERIALS, vol. Vol.229-230, JPN6020018222, 5 June 2012 (2012-06-05), NL, pages 224 - 232, ISSN: 0004273971 *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3984623A4 (en) * 2019-06-13 2023-08-23 Liwei Huang NITRIC OXIDE ABSORBING SLURRY, MANUFACTURING METHOD THEREOF AND USE THEREOF

Also Published As

Publication number Publication date
CN108067269B (en) 2022-09-16
JP6807629B2 (en) 2021-01-06
CN108067269A (en) 2018-05-25
TW201819042A (en) 2018-06-01
KR20180055719A (en) 2018-05-25
KR102445141B1 (en) 2022-09-21

Similar Documents

Publication Publication Date Title
KR101868192B1 (en) Photocatalytic coating film and method for producing same
JP6231550B2 (en) Titanium oxide dispersion, titanium oxide coating solution, and photocatalytic coating
JP6010718B1 (en) Iron compound-supported titanium oxide photocatalyst
CN104640631B (en) It is loaded with the titanium oxide of transistion metal compound
KR102445141B1 (en) Iron compound supported titanium oxide photocatalyst
TWI580469B (en) A method for producing a titanium oxide suspension containing a transition metal compound and a method for producing titanium oxide containing a transition metal compound
JP5986799B2 (en) Method for adjusting amount of transition metal compound supported on transition metal compound supported titanium oxide
KR20060013181A (en) Method for preparing sol for visible light responsive photocatalyst coating
JP2008043848A (en) Optical semiconductor fine particle
JP6315791B2 (en) Iron compound-supported titanium oxide particles
Bondarenko The Synthesis and Study of TiO2/Aluminosilicate Composites as Components of Building Finishing Materials for Improvement of the Indoor Air Quality
Chan Gaseous phase photocatalytic degradation of volatile organic compounds by titanium dioxide

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20190924

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20200520

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20200602

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20200730

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: 20201201

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20201204

R150 Certificate of patent or registration of utility model

Ref document number: 6807629

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313117

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250