JP6552090B2 - Photocatalyst composite material and method for producing the same - Google Patents
Photocatalyst composite material and method for producing the same Download PDFInfo
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- JP6552090B2 JP6552090B2 JP2015095761A JP2015095761A JP6552090B2 JP 6552090 B2 JP6552090 B2 JP 6552090B2 JP 2015095761 A JP2015095761 A JP 2015095761A JP 2015095761 A JP2015095761 A JP 2015095761A JP 6552090 B2 JP6552090 B2 JP 6552090B2
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- 239000011941 photocatalyst Substances 0.000 title claims description 111
- 239000002131 composite material Substances 0.000 title claims description 48
- 238000004519 manufacturing process Methods 0.000 title claims description 13
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims description 69
- 239000010457 zeolite Substances 0.000 claims description 69
- 229910021536 Zeolite Inorganic materials 0.000 claims description 68
- 230000001699 photocatalysis Effects 0.000 claims description 66
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 49
- 239000002689 soil Substances 0.000 claims description 41
- 229910052742 iron Inorganic materials 0.000 claims description 29
- 229910044991 metal oxide Inorganic materials 0.000 claims description 28
- 150000004706 metal oxides Chemical class 0.000 claims description 28
- QGLKJKCYBOYXKC-UHFFFAOYSA-N nonaoxidotritungsten Chemical compound O=[W]1(=O)O[W](=O)(=O)O[W](=O)(=O)O1 QGLKJKCYBOYXKC-UHFFFAOYSA-N 0.000 claims description 25
- 229910001930 tungsten oxide Inorganic materials 0.000 claims description 25
- 239000000463 material Substances 0.000 claims description 21
- 239000004065 semiconductor Substances 0.000 claims description 20
- -1 iron cation Chemical class 0.000 claims description 16
- 238000005341 cation exchange Methods 0.000 claims description 15
- 229910052902 vermiculite Inorganic materials 0.000 claims description 14
- 239000010455 vermiculite Substances 0.000 claims description 14
- 235000019354 vermiculite Nutrition 0.000 claims description 14
- VMQMZMRVKUZKQL-UHFFFAOYSA-N Cu+ Chemical group [Cu+] VMQMZMRVKUZKQL-UHFFFAOYSA-N 0.000 claims description 13
- 239000011259 mixed solution Substances 0.000 claims description 12
- 238000002156 mixing Methods 0.000 claims description 11
- 150000003839 salts Chemical class 0.000 claims description 10
- 239000002904 solvent Substances 0.000 claims description 10
- 239000002253 acid Substances 0.000 claims description 9
- 229910052797 bismuth Inorganic materials 0.000 claims description 9
- JCXGWMGPZLAOME-UHFFFAOYSA-N bismuth atom Chemical compound [Bi] JCXGWMGPZLAOME-UHFFFAOYSA-N 0.000 claims description 9
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 8
- 239000003415 peat Substances 0.000 claims description 8
- 229910052751 metal Inorganic materials 0.000 claims description 7
- 239000002184 metal Substances 0.000 claims description 7
- 230000033116 oxidation-reduction process Effects 0.000 claims description 6
- FJOLTQXXWSRAIX-UHFFFAOYSA-K silver phosphate Chemical compound [Ag+].[Ag+].[Ag+].[O-]P([O-])([O-])=O FJOLTQXXWSRAIX-UHFFFAOYSA-K 0.000 claims description 6
- 239000011734 sodium Substances 0.000 claims description 6
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 claims description 5
- 239000011575 calcium Substances 0.000 claims description 5
- 229910052791 calcium Inorganic materials 0.000 claims description 5
- 239000005909 Kieselgur Substances 0.000 claims description 4
- 238000010438 heat treatment Methods 0.000 claims description 4
- 229910000275 saponite Inorganic materials 0.000 claims description 4
- 229910052712 strontium Inorganic materials 0.000 claims description 4
- CIOAGBVUUVVLOB-UHFFFAOYSA-N strontium atom Chemical compound [Sr] CIOAGBVUUVVLOB-UHFFFAOYSA-N 0.000 claims description 4
- 239000010451 perlite Substances 0.000 claims description 3
- 235000019362 perlite Nutrition 0.000 claims description 3
- 238000003756 stirring Methods 0.000 claims description 3
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 claims description 2
- 150000001621 bismuth Chemical class 0.000 claims description 2
- 239000004927 clay Substances 0.000 claims description 2
- 229910052708 sodium Inorganic materials 0.000 claims description 2
- 239000000306 component Substances 0.000 claims 1
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 65
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 44
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 36
- 239000000126 substance Substances 0.000 description 35
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 33
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 29
- 229910052680 mordenite Inorganic materials 0.000 description 23
- 239000001569 carbon dioxide Substances 0.000 description 22
- 229910002092 carbon dioxide Inorganic materials 0.000 description 22
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 18
- 238000000034 method Methods 0.000 description 17
- 229910052760 oxygen Inorganic materials 0.000 description 17
- 239000001301 oxygen Substances 0.000 description 17
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 16
- 230000000052 comparative effect Effects 0.000 description 15
- 239000010949 copper Substances 0.000 description 15
- 230000000694 effects Effects 0.000 description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 15
- 239000000843 powder Substances 0.000 description 14
- 239000007789 gas Substances 0.000 description 13
- 238000013032 photocatalytic reaction Methods 0.000 description 13
- 238000006243 chemical reaction Methods 0.000 description 12
- 238000000354 decomposition reaction Methods 0.000 description 10
- 238000007254 oxidation reaction Methods 0.000 description 10
- 229910052802 copper Inorganic materials 0.000 description 9
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 9
- 238000006722 reduction reaction Methods 0.000 description 9
- 230000031700 light absorption Effects 0.000 description 8
- 239000005416 organic matter Substances 0.000 description 8
- 239000000725 suspension Substances 0.000 description 8
- 239000010936 titanium Substances 0.000 description 8
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 7
- 150000001768 cations Chemical class 0.000 description 7
- 239000004570 mortar (masonry) Substances 0.000 description 7
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 6
- MWUXSHHQAYIFBG-UHFFFAOYSA-N Nitric oxide Chemical compound O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 6
- 239000007864 aqueous solution Substances 0.000 description 6
- 230000001965 increasing effect Effects 0.000 description 6
- 230000009257 reactivity Effects 0.000 description 6
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 5
- 238000010521 absorption reaction Methods 0.000 description 5
- 229910052739 hydrogen Inorganic materials 0.000 description 5
- 239000001257 hydrogen Substances 0.000 description 5
- 239000002245 particle Substances 0.000 description 5
- 229910052697 platinum Inorganic materials 0.000 description 5
- 238000001179 sorption measurement Methods 0.000 description 5
- 230000007423 decrease Effects 0.000 description 4
- 230000007613 environmental effect Effects 0.000 description 4
- 230000007246 mechanism Effects 0.000 description 4
- 238000005215 recombination Methods 0.000 description 4
- 230000006798 recombination Effects 0.000 description 4
- 239000000758 substrate Substances 0.000 description 4
- 229910052715 tantalum Inorganic materials 0.000 description 4
- JPVYNHNXODAKFH-UHFFFAOYSA-N Cu2+ Chemical compound [Cu+2] JPVYNHNXODAKFH-UHFFFAOYSA-N 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- 239000003054 catalyst Substances 0.000 description 3
- 230000002950 deficient Effects 0.000 description 3
- 238000003795 desorption Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 229910052757 nitrogen Inorganic materials 0.000 description 3
- 238000002360 preparation method Methods 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- VTLYFUHAOXGGBS-UHFFFAOYSA-N Fe3+ Chemical compound [Fe+3] VTLYFUHAOXGGBS-UHFFFAOYSA-N 0.000 description 2
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 2
- 239000000969 carrier Substances 0.000 description 2
- 125000002091 cationic group Chemical group 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 239000003153 chemical reaction reagent Substances 0.000 description 2
- 239000011248 coating agent Substances 0.000 description 2
- 229910001431 copper ion Inorganic materials 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 229910001657 ferrierite group Inorganic materials 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 239000000543 intermediate Substances 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- 239000003921 oil Substances 0.000 description 2
- 239000000376 reactant Substances 0.000 description 2
- PNYYBUOBTVHFDN-UHFFFAOYSA-N sodium bismuthate Chemical compound [Na+].[O-][Bi](=O)=O PNYYBUOBTVHFDN-UHFFFAOYSA-N 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 241000195493 Cryptophyta Species 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- VCUFZILGIRCDQQ-KRWDZBQOSA-N N-[[(5S)-2-oxo-3-(2-oxo-3H-1,3-benzoxazol-6-yl)-1,3-oxazolidin-5-yl]methyl]-2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidine-5-carboxamide Chemical compound O=C1O[C@H](CN1C1=CC2=C(NC(O2)=O)C=C1)CNC(=O)C=1C=NC(=NC=1)NCC1=CC(=CC=C1)OC(F)(F)F VCUFZILGIRCDQQ-KRWDZBQOSA-N 0.000 description 1
- 241001122767 Theaceae Species 0.000 description 1
- 241000700605 Viruses Species 0.000 description 1
- VNSWULZVUKFJHK-UHFFFAOYSA-N [Sr].[Bi] Chemical compound [Sr].[Bi] VNSWULZVUKFJHK-UHFFFAOYSA-N 0.000 description 1
- 238000000862 absorption spectrum Methods 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 150000001299 aldehydes Chemical class 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 229910001854 alkali hydroxide Inorganic materials 0.000 description 1
- 150000008044 alkali metal hydroxides Chemical class 0.000 description 1
- 229910000272 alkali metal oxide Inorganic materials 0.000 description 1
- 150000004703 alkoxides Chemical class 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 150000001412 amines Chemical class 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 230000000844 anti-bacterial effect Effects 0.000 description 1
- 150000001491 aromatic compounds Chemical class 0.000 description 1
- 239000003212 astringent agent Substances 0.000 description 1
- 239000011324 bead Substances 0.000 description 1
- PMVFCJGPQOWMTE-UHFFFAOYSA-N bismuth calcium Chemical compound [Ca].[Bi] PMVFCJGPQOWMTE-UHFFFAOYSA-N 0.000 description 1
- FSAJRXGMUISOIW-UHFFFAOYSA-N bismuth sodium Chemical compound [Na].[Bi] FSAJRXGMUISOIW-UHFFFAOYSA-N 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 150000004649 carbonic acid derivatives Chemical class 0.000 description 1
- 150000001735 carboxylic acids Chemical class 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 239000007806 chemical reaction intermediate Substances 0.000 description 1
- 238000005229 chemical vapour deposition Methods 0.000 description 1
- 150000001805 chlorine compounds Chemical class 0.000 description 1
- 229910001430 chromium ion Inorganic materials 0.000 description 1
- 239000003426 co-catalyst Substances 0.000 description 1
- 238000000975 co-precipitation Methods 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000003750 conditioning effect Effects 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- ORTQZVOHEJQUHG-UHFFFAOYSA-L copper(II) chloride Chemical compound Cl[Cu]Cl ORTQZVOHEJQUHG-UHFFFAOYSA-L 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
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- 239000005556 hormone Substances 0.000 description 1
- 229940088597 hormone Drugs 0.000 description 1
- 238000007602 hot air drying Methods 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 238000001027 hydrothermal synthesis Methods 0.000 description 1
- 229910001872 inorganic gas Inorganic materials 0.000 description 1
- 239000002917 insecticide Substances 0.000 description 1
- FBAFATDZDUQKNH-UHFFFAOYSA-M iron chloride Chemical compound [Cl-].[Fe] FBAFATDZDUQKNH-UHFFFAOYSA-M 0.000 description 1
- 239000010977 jade Substances 0.000 description 1
- 229910052640 jadeite Inorganic materials 0.000 description 1
- 150000002576 ketones Chemical class 0.000 description 1
- 230000004298 light response Effects 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 201000005299 metal allergy Diseases 0.000 description 1
- 229910001510 metal chloride Inorganic materials 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
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- 229910017464 nitrogen compound Inorganic materials 0.000 description 1
- 150000002830 nitrogen compounds Chemical class 0.000 description 1
- 229910000510 noble metal Inorganic materials 0.000 description 1
- 229910052755 nonmetal Inorganic materials 0.000 description 1
- 150000002896 organic halogen compounds Chemical class 0.000 description 1
- 150000002903 organophosphorus compounds Chemical class 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 229910052763 palladium Inorganic materials 0.000 description 1
- KDLHZDBZIXYQEI-UHFFFAOYSA-N palladium Substances [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 1
- 229910001562 pearlite Inorganic materials 0.000 description 1
- 239000000575 pesticide Substances 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 239000010970 precious metal Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 238000006479 redox reaction Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
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- 239000000344 soap Substances 0.000 description 1
- 238000003980 solgel method Methods 0.000 description 1
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- 229910052719 titanium Inorganic materials 0.000 description 1
Landscapes
- Catalysts (AREA)
- Disinfection, Sterilisation Or Deodorisation Of Air (AREA)
Description
本発明は、光が照射されることを利用して、有害な物質を酸化分解して無害化する光触媒複合体材料およびその製造方法に関する。 The present invention relates to a photocatalyst composite material that uses a light irradiation to oxidize and decompose harmful substances to make them harmless, and a method for producing the same.
光触媒複合体材料は、光が照射されることで、バンド間吸収により光を吸収しその光エネルギーを利用して、電子とホールを生成し、特にそのホールおよびホールと大気中成分と反応してできる化合物により、有害な物質を酸化分解して、より無害にするもので、例えば酸化チタンが知られている。
酸化チタンは紫外光が照射されている状況下で、光触媒特性を示し、有害な有機物質を酸化分解し、二酸化炭素にまで分解することができる。しかし、屋内など、紫外光が少ない場所では、その活性が抑えられ、うまく機能しないという課題がある。
The photocatalyst composite material is irradiated with light, absorbs light by interband absorption, and uses the light energy to generate electrons and holes, and particularly reacts with the holes and holes and atmospheric components. Depending on the compounds that can be used, the harmful substances are oxidatively decomposed to make them harmless, for example, titanium oxide is known.
Titanium oxide exhibits photocatalytic properties in the presence of ultraviolet light, and can oxidize and decompose harmful organic substances into carbon dioxide. However, there is a problem that in places where there is little ultraviolet light, such as indoors, its activity is suppressed and it does not work well.
そこで、室内により豊富に存在する可視光線を吸収する可視光応答型光触媒に関する研究がさかんになってきた。酸化チタンに窒素をドープした材料は、窒素をドープすることで可視光に吸収を持つようになる（非特許文献１）が、合成時に有害なアンモニアなどを用いる必要があるため、環境にやさしい方法ではなく、望ましい材料ではない。 Therefore, research on visible light responsive photocatalysts that absorb visible light that is more abundant in the room has become increasingly popular. A material in which titanium oxide is doped with nitrogen comes to have absorption in visible light by doping nitrogen (Non-Patent Document 1), but it is necessary to use harmful ammonia and the like at the time of synthesis, so an environmentally friendly method Not a desirable material.
一方、酸化タングステンはそのバンドギャップが約２．８ｅＶと可視光を吸収し、光触媒特性を示す材料である。しかし、耐久性に問題があり、光触媒として利用するとすぐに活性が低下し、失活してしまう。そのため、酸化タングステンのみで可視光光触媒材料として、実用上、利用することができないという課題がある。 On the other hand, tungsten oxide is a material which absorbs visible light with a band gap of about 2.8 eV and exhibits photocatalytic properties. However, there is a problem in the durability, and when it is used as a photocatalyst, the activity is immediately reduced and the catalyst is inactivated. Therefore, there is a problem that tungsten oxide alone can not be used practically as a visible light photocatalyst material.
それゆえ、酸化タングステンと各種金属などを複合化させることで、その光触媒特性の耐久性の向上が図られてきている。
酸化タングステンをプラチナに担持することで、酸化タングステンの光触媒活性を上昇させるという報告もなされている（非特許文献２）。しかし、プラチナの採掘可能な量は、鉄との比較では４桁から５桁少なく、非常に微量である。また、プラチナの単位重量当たりの価格は、鉄との比較では４桁から５桁高価であるため、汎用的に利用することはなかなか難しい。それゆえ、高価な金属を使わない材料の開発が期待されてきている。
Therefore, the durability of the photocatalytic properties has been improved by combining tungsten oxide with various metals and the like.
It is also reported that supporting tungsten oxide on platinum increases the photocatalytic activity of tungsten oxide (Non-patent Document 2). However, the extractable amount of platinum is very small, four to five orders of magnitude less than iron. Also, the price per unit weight of platinum is 4 to 5 digits more expensive than iron, so it is difficult to use for general purposes. Therefore, development of materials that do not use expensive metals has been expected.
さらには、銅イオンと酸化チタン、酸化タングステンを組み合わせた光触媒が報告されている（特許文献１）。この光触媒は、可視光により光触媒特性を示す。しかし、この表面修飾された銅イオンは水溶性であり、コーティング剤として利用した場合、溶媒に水やアルコールなどを用いると酸化チタン、酸化タングステン光触媒から遊離や偏析するおそれが発生する。そこで、水などの溶媒により溶けにくい助触媒が必要とされている。また、遊離した銅イオンは抗菌性などが高すぎ、用途が限られ、また、金属アレルギー源にもなりえる。 Furthermore, photocatalysts in which copper ions, titanium oxide, and tungsten oxide are combined have been reported (Patent Document 1). The photocatalyst exhibits photocatalytic properties by visible light. However, this surface-modified copper ion is water-soluble, and when used as a coating agent, there is a possibility of liberation or segregation from titanium oxide or tungsten oxide photocatalyst when water, alcohol or the like is used as the solvent. Therefore, a cocatalyst that is hardly dissolved by a solvent such as water is required. In addition, the liberated copper ion is too high in antibacterial properties, has limited applications, and can be a metal allergy source.
また、Ｆｅ２Ｏ３をＷＯ３に担持した光触媒材料も報告されている（非特許文献３）。しかし、Ｆｅ２Ｏ３をＷＯ３に担持すると、却って可視光光触媒活性が低下し、ＷＯ３単独より可視光照射下の有機物分解活性が低下する。このことから、酸化鉄をＷＯ３に担持させることは、酸化タングステン光触媒に対しては適当ではないといいえる。 Also, photocatalytic material carrying Fe 2 O 3 in WO 3 has also been reported (Non-Patent Document 3). However, when Fe 2 O 3 is supported on WO 3 , the visible light photocatalytic activity is lowered, and the organic substance decomposing activity under irradiation with visible light is lower than that of WO 3 alone. From this, it can be said that supporting iron oxide on WO 3 is not suitable for a tungsten oxide photocatalyst.
一方、比表面積を増大させて、酸化タングステンの光触媒活性を向上させることを目的として、酸化タングステンに酸化チタン並びに／若しくは比表面積の大きなＮａ型ゼオライト、Ｈ型ゼオライト及び／又はＮＨ４型ゼオライトと混合した例も報告されている（特許文献２）。しかし、酸化チタンや３種のゼオライトは白色であり、それらを混ぜることで触媒中の有色成分の比率が減少し、光触媒材料の色が薄くなる。その結果として光触媒自身が十分に可視光線を吸収できず、光触媒活性が不十分となるという課題がある。 On the other hand, for the purpose of increasing the specific surface area and improving the photocatalytic activity of tungsten oxide, titanium oxide is mixed with titanium oxide and / or Na type zeolite, H type zeolite and / or NH 4 type zeolite having a large specific surface area. An example is also reported (Patent Document 2). However, titanium oxide and three kinds of zeolites are white, and by mixing them, the proportion of colored components in the catalyst decreases and the color of the photocatalytic material becomes lighter. As a result, there is a problem that the photocatalyst itself can not sufficiently absorb visible light and the photocatalytic activity becomes insufficient.
一方、銅カチオン交換型ゼオライトは窒素酸化物除去触媒として利用され、その活性はＮａ型ゼオライトよりも非常に高活性であることが知られている（非特許文献４）。このことは、換言するとゼオライトがカチオンの特性によってその特性、特に触媒活性が異なってくることを示している。しかし、銅カチオン交換型ゼオライトによる窒素酸化物除去は３５０℃以上の高温でしか機能せず、光触媒反応が実施されるような室温では、このゼオライトを単独で用いても有害物質を除去することはできないという課題がある。 On the other hand, copper cation exchange type zeolite is used as a nitrogen oxide removal catalyst, and its activity is known to be much higher than that of Na type zeolite (Non-patent Document 4). This indicates that, in other words, the properties of the zeolite, in particular its catalytic activity, differ depending on the properties of the cation. However, nitrogen oxide removal by copper cation exchange type zeolite functions only at high temperature of 350 ° C or higher, and at room temperature where photocatalytic reaction is carried out, it is possible to remove harmful substances even if this zeolite is used alone There is a problem that it can not do.
以上示したように、従来の可視光応答型光触媒は、活性が非常に高く、安価で、コーティングの際の安定性、より環境にやさしいという４つの条件が整った材料はなく、様々な課題が山積していた。 As shown above, conventional visible light responsive photocatalysts have very high activity, are inexpensive, and do not have materials that meet the four conditions of stability in coating and environmental friendliness, and there are various issues I was piled up.
本発明は安価でかつ、高い光触媒活性を持つ可視光応答型の光触媒材料を提供することを目的とする。 An object of the present invention is to provide a visible light responsive photocatalytic material which is inexpensive and has high photocatalytic activity.
本特許の発明者らは、上記の課題を解決するために有色の土壌成分などの優れた環境調和性に着目し、これを酸化タングステンなどの可視光応答型光触媒と複合化させるなど、鋭意研究開発を行った。その結果、高活性、安価かつ安定な可視光応答型光触媒複合材料の発明に至ったのである。 The inventors of the present patent focused on excellent environmental harmony such as colored soil component to solve the above-mentioned problems, and intensively researched such as combining this with visible light responsive photocatalyst such as tungsten oxide. Developed. As a result, the invention of a highly active, inexpensive and stable visible light responsive photocatalytic composite material has been achieved.
これらの土壌成分は園芸や住宅の内壁に使われるように環境調和性に秀で、吸湿、放湿の調湿効果に代表されるように気体の吸着・脱離効果に優れており、さらに茶色を帯びるなど有色であるため、可視光を十分に吸収できる。
一方、価電子帯のボトムの位置が０〜＋０．７Ｖに相当する可視光応答型光触媒は光照射により、ホールと電子を生成し、生成したホールは有機物質を酸化分解する。この可視光応答型光触媒単独で用いた場合、電子は酸素を還元して、過酸化水素を生成するが、過酸化水素の反応性は低濃度では著しく低いため、過酸化水素が蓄積し、その結果、電子が消費しづらくなり、電子とホールの再結合が起きやすくなり、活性が著しく低下してしまう。しかし、前述の有色の土壌成分および沸石成分と接合すると、土壌および沸石成分特有の優れた吸着脱離能により、光触媒表面に生成した過酸化水素も土壌並びに沸石成分の表面および界面へとあふれ出し、光触媒表面への過度の過酸化水素の蓄積を防ぎ、光触媒活性を維持できる。また、土壌および沸石成分は光触媒と比較して非常に吸着能に優れるため、表面に一部あふれ出した過酸化水素もその表面で濃縮され、濃縮された有機ガスとの反応性が増す。さらに、有色の土壌および沸石成分を用いることで、可視光を大幅に吸収することができ、その光吸収による局所的な熱的効果は高められ、その結果、濃縮された過酸化水素と有機物の反応性が飛躍的に増すことになり、土壌および沸石成分に吸着した有機物をも酸化分解されていくことになる。その結果、非常に高効率に有機物を分解することできるようになる。また、沸石中にカチオン交換またはドープした鉄および銅は混合原子価であり、複数の価数をとることができるため、過酸化水素と電子のやり取りができ、過酸化水素がより分解しやすくラジカルも作りやすく、さらに反応性が高くなり、有機物を分解することを促進する手助けをする。
These soil components are excellent in environmental harmony as used for gardening and inner walls of houses, and are excellent in gas adsorption and desorption effects, as represented by moisture conditioning effects of moisture absorption and desorption. Because it is colored, it can absorb visible light sufficiently.
On the other hand, a visible light responsive photocatalyst having a valence band bottom position corresponding to 0 to +0.7 V generates holes and electrons by light irradiation, and the generated holes oxidatively decompose organic substances. When this visible light responsive photocatalyst is used alone, the electrons reduce oxygen to produce hydrogen peroxide. However, hydrogen peroxide accumulates because the reactivity of hydrogen peroxide is extremely low at low concentrations. As a result, electrons are less likely to be consumed, recombination between electrons and holes is likely to occur, and the activity is significantly reduced. However, when combined with the colored soil components and zeolite components mentioned above, hydrogen peroxide generated on the photocatalytic surface also overflows to the surface and interface of the soil and zeolite components due to the excellent adsorption and desorption ability unique to the soil and zeolite components. It is possible to prevent excessive hydrogen peroxide accumulation on the photocatalyst surface and maintain photocatalytic activity. In addition, since the soil and zeolite components are very excellent in adsorption capacity compared to the photocatalyst, hydrogen peroxide partially overflowing on the surface is also concentrated on the surface, and the reactivity with the concentrated organic gas is increased. In addition, the use of colored soil and zeolite components can significantly absorb visible light, enhancing the local thermal effect of the light absorption, resulting in the concentration of concentrated hydrogen peroxide and organic matter. The reactivity will increase dramatically, and the organic matter adsorbed on the soil and zeolite components will also be oxidatively decomposed. As a result, it becomes possible to decompose the organic matter very efficiently. In addition, iron and copper cation exchanged or doped in zeolite have mixed valences and can take multiple valences, so that hydrogen and electrons can be exchanged, and hydrogen peroxide is more easily decomposed and radicals. Makes it easier to make, more responsive, and helps promote the decomposition of organic matter.
また、これらの土壌成分はプラチナなどの貴金属とは異なり、地球上に豊富に存在し、価格も非常に廉価であるという特長も持つ。その結果、本発明は、安価でかつ、高い光触媒活性を持つ可視光応答型の光触媒材料を提供するという前記の課題を解決することができる。
そして、本発明は、以下の構成を有する。
In addition, unlike precious metals such as platinum, these soil components are abundant on the earth and are also very inexpensive. As a result, the present invention can solve the above-mentioned problem of providing an inexpensive and light-responsive photocatalytic material having high photocatalytic activity.
And this invention has the following structures.
本発明の光触媒複合体材料は、可視光応答型光触媒と、可視光応答型光触媒の表面に担持した可視光を吸収する有色の土成分または有色になるよう加工された沸石成分を含有し、可視光応答型光触媒が、バンドギャップが１．４ｅＶ以上３．１ｅＶ以下であり、かつ、伝導帯のボトムのエネルギー準位から換算した酸化還元電位が０Ｖ以上＋０．７Ｖ以下（ｖｓ．ＳＨＥ，ｐＨ＝０）の金属酸化物半導体であることを特徴とする。ここで、『ＳＨＥ』は標準水素電極のことで、Ｓｔａｎｄａｒｄ ｈｙｄｒｏｇｅｎ ｅｌｅｃｔｒｏｄｅの略である。本発明の光触媒複合体材料には、添加物として、シリカ、アルミナ、セメント、酸化チタン等を適宜添加しても良い。酸化チタンを加えることで、紫外光に対する光触媒特性を高めることができる。 The photocatalyst composite material of the present invention contains a visible light responsive photocatalyst, and a colored earth component or a zeolite component processed to become colored which absorbs visible light supported on the surface of the visible light responsive photocatalyst, The photoresponsive photocatalyst has a band gap of 1.4 eV or more and 3.1 eV or less, and a redox potential of 0 V or more and 0.7 V or less calculated from the energy level of the bottom of the conduction band (vs. SHE, pH = It is characterized by being a metal oxide semiconductor of 0). Here, “SHE” is a standard hydrogen electrode, and is an abbreviation for Standard hydrogen electrode. In the photocatalyst composite material of the present invention, silica, alumina, cement, titanium oxide or the like may be appropriately added as an additive. By adding titanium oxide, the photocatalytic properties for ultraviolet light can be enhanced.
本発明の光触媒複合体材料において、好ましくは、金属酸化物半導体が、酸化タングステン、リン酸銀(Ａｇ３ＰＯ４)、ビスマス酸塩、チタン酸化物のいずれか１つまたは２つ以上からなるとよい。
本発明の光触媒複合体材料において、好ましくは、チタン酸化物は、Ｆｅ２ＴｉＯ５、ドープ型酸化チタン（ＦｅとＴａの両方をドープした酸化チタン若しくはＴｉ３＋及び／又はＴｉ４＋を格子間位置（ｉｎｔｅｒｓｔｉｔｉａｌ ｓｉｔｅ）にドープした酸化チタン）のいずれか１つまたは２つ以上からなるとよい。
また、ビスマス酸塩は、好ましくは、ビスマス酸ナトリウム（ＮａＢｉＯ３）、ビスマス酸カルシウム、ビスマス酸ストロンチウムのいずれか１つまたは２つ以上からなるとよい。ビスマス酸カルシウムは、例えばＣａＢｉ２Ｏ４であるが、他の化学式で表記される物でも良い。
In the photocatalytic composite material of the present invention, preferably, the metal oxide semiconductor is made of any one or more of tungsten oxide, silver phosphate (Ag 3 PO 4 ), bismuth acid salt, and titanium oxide. .
In the photocatalyst composite material of the present invention, preferably, the titanium oxide is Fe 2 TiO 5 , doped titanium oxide (titanium oxide doped with both Fe and Ta or Ti 3+ and / or Ti 4+ in an interstitial position ( It may be composed of any one or more of titanium oxide doped in interstitial site).
The bismuth acid salt is preferably composed of one or more of sodium bismutate (NaBiO 3 ), calcium bismutate, and strontium bismuthate. Calcium bismuthate is, for example, CaBi 2 O 4 , but may be one represented by another chemical formula.
本発明の光触媒複合体材料において、好ましくは、土壌成分がバーミキュライト、パーライト、ピートモス、ミックスピートモス、ココソイル、珪藻土、サポナイト又は赤土のいずれか１つまたは２つ以上を含むとよい。
本発明の光触媒複合体材料において、好ましくは、沸石成分が銅カチオン交換型ゼオライト、銅カチオンドープ型ゼオライト、鉄カチオン交換型ゼオライトまたは鉄カチオンドープ型ゼオライトの群から選択されるいずれか１種または２種以上からなるとよい。
In the photocatalyst composite material of the present invention, preferably, the soil component may include one or more of vermiculite, perlite, peat moss, mixed peat moss, coco soy, diatomaceous earth, saponite or red soil.
In the photocatalyst composite material of the present invention, preferably, the zeolite component is any one or two selected from the group consisting of a copper cation exchange type zeolite, a copper cation dope type zeolite, an iron cation exchange type zeolite, and an iron cation dope type zeolite. It is good to consist of more than seeds.
本発明の光触媒複合体材料において、好ましくは、銅または鉄カチオンが沸石成分に対して、質量比で０．０１％以上１００％以下であるとよい。
本発明の光触媒複合体材料において、好ましくは、土壌または沸石成分の光触媒に対する質量比が、０．０１％以上５００％以下であるとよい。
In the photocatalyst composite material of the present invention, preferably, the copper or iron cation is 0.01% or more and 100% or less by mass ratio with respect to the zeolite component.
In the photocatalyst composite material of the present invention, the mass ratio of the soil or zeolite component to the photocatalyst is preferably 0.01% or more and 500% or less.
本発明の光触媒複合体材料の製造方法は、例えば図２に示すように、可視光を吸収する有色の土壌成分、有色の金属交換沸石成分、または有色の金属ドープ沸石成分のいずれか１つまたは２つ以上を含む可視光吸収成分を準備する工程（Ｓ１００）と、バンドギャップが１．４ｅＶ以上３．１ｅＶ以下であり、かつ、伝導帯のボトムのエネルギー準位から換算した酸化還元電位が０Ｖ以上＋０．７Ｖ以下（ｖｓ．ＳＨＥ，ｐＨ＝０）の金属酸化物半導体からなる光触媒を準備する工程（Ｓ１０２）と、前記可視光吸収成分と前記光触媒の比が０．０１質量％以上５００質量％以下となるようにして、混合溶液を調製する工程（Ｓ１０４）と、前記混合溶液を加熱して、光触媒複合体材料を作製する工程（Ｓ１０６）とを有することを特徴とする。
本発明の光触媒複合体材料の製造方法において、好ましくは、前記混合溶液を調製する工程は、前記光触媒を溶媒中に分散させて、混合してから、攪拌する工程を含むとよい。
For example, as shown in FIG. 2, the method for producing the photocatalyst composite material of the present invention includes any one of a colored soil component that absorbs visible light, a colored metal exchange zeolite component, or a colored metal doped zeolite component, or A step (S100) of preparing a visible light absorption component including two or more, a band gap of 1.4 eV or more and 3.1 eV or less, and an oxidation-reduction potential converted from the energy level of the bottom of the conduction band is 0 V A step (S102) of preparing a photocatalyst composed of a metal oxide semiconductor of +0.7 V or less (vs. SHE, pH = 0), and a ratio of the visible light absorbing component to the photocatalyst of 0.01 mass% to 500 mass. % Or less, and preparing a photocatalyst composite material by heating the mixed solution (S106). .
In the method for producing a photocatalyst composite material of the present invention, preferably, the step of preparing the mixed solution may include a step of dispersing the photocatalyst in a solvent, mixing, and stirring.
本発明の光触媒複合体材料によれば、水溶液に懸濁させても材料の遊離を生じさせず、安定、安全に使用でき、可視光照射下で長寿命な光触媒活性を示し、廉価で高活性な光触媒複合体材料を提供できる。また、本発明の光触媒複合体材料を用いて、様々な有害な有機物質、非金属無機ガスを効率よく酸化又は還元して分解できる。
また、本発明の光触媒複合体材料の製造方法によれば、水溶液に懸濁させても材料の遊離を生じさせず、安定、安全に使用でき、可視光照射下で長寿命な光触媒活性を示し、低価格な光触媒複合体材料を効率よく製造できる。
According to the photocatalyst composite material of the present invention, the material is not liberated even when suspended in an aqueous solution, can be used stably and safely, exhibits long-lived photocatalytic activity under visible light irradiation, is inexpensive and highly active A photocatalytic composite material can be provided. In addition, various harmful organic substances and non-metallic inorganic gases can be efficiently oxidized or reduced and decomposed using the photocatalyst composite material of the present invention.
Further, according to the method for producing a photocatalyst composite material of the present invention, even when suspended in an aqueous solution, the material is not released, can be used stably and safely, and exhibits long-lived photocatalytic activity under visible light irradiation. The low cost photocatalyst composite material can be efficiently produced.
（光触媒複合体材料）
可視光応答型光触媒は、金属酸化物半導体であり、伝導帯のボトムと価電子帯のトップの差であるバンドギャップが１．４ｅＶ以上３．１ｅＶ以下である。これにより、可視光及び紫外光下で光触媒活性を示すことができる。なお、バンドギャップが３．１ｅＶ超では、４００ｎｍ以上の波長をもつ光が吸収できなくなり、すなわち、４００ｎｍ以上の波長の可視光線を吸収できないこととなる。逆に、バンドギャップが１．４ｅＶ未満では、安定な光触媒活性を生じさせることができなくなる。標準水素生成電位と標準酸素生成電位の差は１．２３Ｖであり、過電圧も考慮に入れると、有色の土成分担持前の光触媒のバンドギャップが１．４ｅＶ以上必要となるためである。
(Photocatalyst composite material)
The visible light responsive photocatalyst is a metal oxide semiconductor, and has a band gap of 1.4 eV or more and 3.1 eV or less, which is the difference between the bottom of the conduction band and the top of the valence band. Thereby, photocatalytic activity can be exhibited under visible light and ultraviolet light. If the band gap exceeds 3.1 eV, light having a wavelength of 400 nm or more cannot be absorbed, that is, visible light having a wavelength of 400 nm or more cannot be absorbed. Conversely, when the band gap is less than 1.4 eV, stable photocatalytic activity cannot be produced. The difference between the standard hydrogen generation potential and the standard oxygen generation potential is 1.23 V, and taking the overvoltage into consideration, the band gap of the photocatalyst before supporting the colored soil component needs to be 1.4 eV or more.
金属酸化物半導体の伝導帯のボトムのエネルギー準位は、酸化還元電位で換算することができ、換算した酸化還元電位は０Ｖ以上＋０．７Ｖ以下（ｖｓ．ＳＨＥ，ｐＨ＝０）となる。可視光応答型光触媒である金属酸化物の伝導帯のボトムのエネルギー準位から換算した酸化還元電位を０Ｖ（ｖｓ．ＳＨＥ，ｐＨ＝０）より大きくすることにより、電子は酸素の１電子還元反応で消費されないが、土壌または沸石成分担持により過酸化水素が担持成分または担持成分と光触媒界面へあふれだし、その部分での過酸化水素濃度、有機物濃度を濃縮することができる。その結果、過酸化水素及び有機物質の反応性が増し、その両者が徐々に分解されることになり、結果として、光触媒活性を低下させる過酸化水素の蓄積を防ぎ、光触媒活性を向上させることができる。また、沸石にカチオン交換またはドープした鉄および銅は過酸化水素などを不安定化させ、ラジカルを生じやすくし、有機物の分解の手助けをする。 The energy level of the bottom of the conduction band of the metal oxide semiconductor can be converted by the redox potential, and the converted redox potential is 0 V or more and +0.7 V or less (vs. SHE, pH = 0). The electron is a one-electron reduction reaction of oxygen by making the redox potential converted from the energy level at the bottom of the conduction band of the metal oxide that is a visible light responsive photocatalyst greater than 0 V (vs. SHE, pH = 0) Although it is not consumed at this time, hydrogen peroxide can overflow to the supported component or supported component and the photocatalyst interface by the soil or zeolite component loaded, and the concentration of hydrogen peroxide and the concentration of organic substances in that portion can be concentrated. As a result, the reactivity of the hydrogen peroxide and the organic substance is increased, and both of them are gradually decomposed. As a result, the accumulation of hydrogen peroxide which reduces the photocatalytic activity is prevented, and the photocatalytic activity is improved. it can. In addition, iron and copper cation exchanged or doped in zeolite destabilize hydrogen peroxide and the like, make radicals easily generated, and help decompose organic substances.
伝導帯のボトムのエネルギー準位から換算した酸化還元電位が０Ｖ（ｖｓ．ＳＨＥ，ｐＨ＝０）より小さくなると、酸素の１電子還元反応や水からの水素生成反応が起き、助触媒を担持しないでも可視光応答型光触媒から生じた電子が素早く消費されてしまう可能性がある。
逆に、伝導帯のボトムのエネルギー準位から換算した酸化還元電位が＋０．７Ｖ（ｖｓ．ＳＨＥ，ｐＨ＝０）より大きくなると、２電子酸素還元反応も起こりづらくなり、電子の消費が起こりづらい。２電子酸素還元反応が起こるように、伝導帯のボトムのエネルギー準位から換算した酸化還元電位が＋０．７Ｖ（ｖｓ．ＳＨＥ，ｐＨ＝０）より小さくなる必要がある。
When the redox potential converted from the energy level at the bottom of the conduction band is less than 0 V (vs. SHE, pH = 0), a one-electron reduction reaction of oxygen or a hydrogen generation reaction from water occurs, and no promoter is supported. However, electrons generated from the visible light responsive photocatalyst may be consumed quickly.
Conversely, when the oxidation-reduction potential converted from the energy level at the bottom of the conduction band is greater than +0.7 V (vs. SHE, pH = 0), the two-electron oxygen reduction reaction is difficult to occur and the electron consumption is difficult to occur. . The redox potential converted from the energy level at the bottom of the conduction band needs to be smaller than +0.7 V (vs. SHE, pH = 0) so that the two-electron oxygen reduction reaction occurs.
金属酸化物半導体としては、酸化タングステン、リン酸銀(Ａｇ３ＰＯ４)、ビスマス酸塩、チタン酸化物のいずれか１つまたは２つ以上からなる材料を挙げることができる。また、チタン酸化物としては、Ｆｅ２ＴｉＯ５、ＦｅとＴａの両方をドープした酸化チタン若しくはＴｉ３＋及び／又はＴｉ４＋を格子間位置にドープした酸化チタンを挙げることができる。また、ビスマス酸塩は、ビスマス酸ナトリウム（NaBiO3）、CaBi2O4をはじめとするビスマス酸カルシウム、ビスマス酸ストロンチウムを挙げることができる。 Examples of the metal oxide semiconductor include a material made of any one or more of tungsten oxide, silver phosphate (Ag 3 PO 4 ), bismuth acid salt, and titanium oxide. As the titanium oxide, Fe 2 TiO 5, Fe and Ta titanium oxide doped or Ti 3+ and / or Ti 4+ both can be mentioned titanium oxide doped interstitial position. Further, examples of the bismuth acid salt include calcium bismuthate including sodium bismuthate (NaBiO 3 ) and CaBi 2 O 4 , and strontium bismuthate.
これらの金属の酸化物は、試薬メーカーなどで販売される試薬をそのまま利用してもよいし、加工して用いてもよい。これらの金属の酸化物を加工して用いる場合としては、例えば、これらの可視光応答型光触媒の金属酸化物に、窒素やクロムイオン等の非金属イオン又は金属イオンを添加して、イオンドープ型にして、金属酸化物として利用してもよい。 As these metal oxides, reagents sold by reagent manufacturers and the like may be used as they are or may be processed and used. In the case of processing and using these metal oxides, for example, ion doping type by adding non-metal ions or metal ions such as nitrogen and chromium ions to the metal oxides of these visible light responsive photocatalysts. And may be used as a metal oxide.
上記の金属酸化物半導体は、バンドギャップが１．４ｅＶ以上３．１ｅＶ以下、伝導帯のボトムのエネルギー準位から換算した酸化還元電位が０Ｖ以上＋０．７Ｖ以下（ｖｓ．ＳＨＥ，ｐＨ＝０）の条件を満たす半導体であるので、可視光応答型光触媒として用いることができる。 The above metal oxide semiconductor has a band gap of 1.4 eV or more and 3.1 eV or less, and an oxidation reduction potential of 0 V or more and 0.7 V or less calculated from the energy level of the bottom of the conduction band (vs. SHE, pH = 0) Therefore, it can be used as a visible light responsive photocatalyst.
また、金属酸化物半導体は、結晶性がよいことが望ましい。これにより、光を有効に利用できる。また、比表面積は０．１ｍ２ｇ−１以上であることがよく、好ましくは１ｍ２ｇ−１以上であり、より好ましくは１０ｍ２ｇ−１以上である。これにより、光をより有効に利用できる。 In addition, it is preferable that the metal oxide semiconductor has high crystallinity. Thereby, light can be used effectively. The specific surface area is preferably 0.1 m 2 g −1 or more, preferably 1 m 2 g −1 or more, and more preferably 10 m 2 g −1 or more. This enables more effective use of light.
金属酸化物半導体としては、酸素欠損型酸化チタンを用いることもできるが、他の金属酸化物半導体を酸素欠損型にして用いてもよい。例えば、酸素欠損型のＷＯ３系としては、マグネリ相に相当するＷ１９Ｏ４９やＷ２０Ｏ５８などを挙げることができる。 As the metal oxide semiconductor, oxygen-deficient titanium oxide can be used, but other metal oxide semiconductors may be used in an oxygen-deficient type. For example, examples of the oxygen deficient WO 3 system include W 19 O 49 and W 20 O 58 corresponding to the magnetic phase.
金属酸化物半導体は、金属アルコキシドや金属塩を原料として、ゾルーゲル法、共沈法、錯体重合法、スパッタリング法、化学蒸着法、又は水熱合成法のいずれかの方法によって調製することができる。これにより、金属酸化物半導体の光触媒材活性をより高く、粒径を小さくでき、ナノ材料の作製もできる。 A metal oxide semiconductor can be prepared by any of sol-gel method, coprecipitation method, complex polymerization method, sputtering method, chemical vapor deposition method, or hydrothermal synthesis method using metal alkoxide or metal salt as a raw material. Thus, the photocatalytic material activity of the metal oxide semiconductor can be further increased, the particle diameter can be reduced, and the nanomaterial can be manufactured.
更にまた、金属酸化物半導体に熱処理を行い、還元又は酸化したものを、可視光応答型光触媒として利用してもよい。
例えば、上記いずれかの方法で調整した原料を焼成して利用することもできる。このときの焼成温度は、原料物質が分解して酸化物に転換され、酸化物からなる焼結体が得られる温度であればよく、具体的には１００℃以上１２００℃以下の温度範囲がよく、より好ましくは３００℃以上９００℃以下である。
Furthermore, a metal oxide semiconductor subjected to heat treatment and reduced or oxidized may be used as a visible light responsive photocatalyst.
For example, the raw material prepared by any of the above methods can be fired and used. At this time, the firing temperature may be a temperature at which the raw material is decomposed and converted into an oxide to obtain a sintered body made of the oxide, specifically, a temperature range of 100 ° C. or more and 1200 ° C. or less is good More preferably, the temperature is 300 ° C. or more and 900 ° C. or less.
可視光応答型光触媒が表面に担持された有色の土壌成分、または有色のカチオン交換型またはドープ型沸石成分は可視光を吸収することができる。それにより、可視光応答型光触媒が十分に吸収しきれなかった光をも吸収でき、照射された光を有効に利用することができる。すなわち、光触媒反応で生成した過酸化水素と有機物成分を土壌成分由来の吸着脱離特性により土壌成分内または土壌成分と光触媒の界面で濃縮し、光吸収による光熱効果により、過酸化水素及び有機物質の除去に寄与することができる。その結果、光触媒全体の光吸収能力が向上し、全体の光触媒活性も向上する。有色の土壌成分としては赤土、バーミキュライトが、有色の沸石成分としては、銅カチオン交換型ゼオライト、銅カチオンドープ型ゼオライト、鉄カチオン交換型ゼオライトまたは鉄カチオンドープ型ゼオライトを用いることができる。 A colored soil component having a visible light responsive photocatalyst supported on its surface, or a colored cation exchange or doped zeolite component can absorb visible light. As a result, it is possible to absorb light that the visible light responsive photocatalyst has not sufficiently absorbed, and to effectively use the irradiated light. That is, hydrogen peroxide and organic matter components generated by photocatalytic reaction are concentrated in the soil components or at the interface between soil components and photocatalysts by the adsorption / desorption characteristics derived from the soil components, and hydrogen peroxide and organic substances are produced by the photothermal effect by light absorption. Can contribute to the removal of As a result, the light absorption capability of the entire photocatalyst is improved, and the overall photocatalytic activity is also improved. Red soil can be used as the colored soil component, and vermiculite can be used as the colored zeolite component, and copper cation exchange zeolite, copper cation doped zeolite, iron cation exchange zeolite or iron cation doped zeolite can be used.
これらの土壌成分は市販のまま用いてもよいが、粉砕して粒子の大きさを細かくしてから用いた方がより望ましい。また、赤土が水分などを多く含む場合は、７０℃以上で、望ましくは１５０℃以上で、より望ましくは３００℃以上で焼成し、水分などを取り除くほうが望ましい。 These soil components may be used as they are on the market, but it is more desirable to use them after pulverizing and reducing the size of the particles. In addition, when red soil contains a lot of moisture, it is desirable to remove the moisture by baking at 70 ° C. or higher, preferably 150 ° C. or higher, more preferably 300 ° C. or higher.
沸石成分は、沸石に銅や鉄をドープしたり、また、沸石のカチオンを鉄や銅でカチオン交換したりすることで有色化することができる。また、ドープまたはカチオン交換後、３００℃以上で焼成して用いることもできる。さらには、土成分の可視光吸収能力をさらに高めて活性を向上させるために、土成分に銅や鉄をドープやカチオン交換することができる。 The zeolite component can be colored by doping the zeolite with copper or iron, or by exchanging the cation of the zeolite with iron or copper. Moreover, after dope or cation exchange, it can also be used by baking at 300 ° C. or higher. Furthermore, in order to further enhance the activity of the soil component by absorbing visible light, copper or iron can be doped or cation exchanged with the soil component.
さらには、これらの材料を単独で利用するだけでなく、電子の消費速度を上昇させる第２の助触媒として、Ｐｔ、Ｐｄといった貴金属、塩化銅、塩化鉄など塩化金属化合物やアルカリ水酸化物、アルカリ酸化物、アルカリ炭酸塩の１種以上と組み合わせて利用することができる。 Furthermore, not only these materials are used alone, but also as a second co-catalyst that increases the consumption rate of electrons, noble metals such as Pt and Pd, metal chloride compounds such as copper chloride and iron chloride, alkali hydroxides, It can be used in combination with one or more of alkali oxides and alkali carbonates.
土または沸石成分の可視光応答型光触媒に対する質量比は、０．０１質量％以上５００質量％以下であることが好ましく、０．１質量％以上から１００質量％以下がより好ましい。
質量比が０．０１質量％より小さい場合には、土または沸石成分の担持量が少なすぎ、可視光応答型光触媒が生成した電子を消費した際に生じた過酸化水素を始めとする活性酸素をうまく消費できにくくなり、光触媒活性を十分に発揮できなくなる。
逆に、質量比が５００％より大きい場合には、土または沸石成分が光触媒表面を覆い尽くし、光触媒本体まで光が届きづらくなり、光触媒活性の低下をもたらす。
The mass ratio of the soil or zeolite component to the visible light responsive photocatalyst is preferably 0.01% by mass to 500% by mass, and more preferably 0.1% by mass to 100% by mass.
When the mass ratio is smaller than 0.01% by mass, the amount of supported earth or zeolite component is too small, and active oxygen such as hydrogen peroxide generated when the electrons generated by the visible light responsive photocatalyst are consumed. Can not be consumed properly, and the photocatalytic activity can not be sufficiently exhibited.
Conversely, if the mass ratio is greater than 500%, the soil or zeolite component covers the photocatalyst surface, making it difficult for light to reach the photocatalyst body, leading to a decrease in photocatalytic activity.
銅カチオン交換型成分、銅カチオンドープ型成分、鉄カチオン交換型成分、または鉄カチオンドープ型成分の沸石に対する質量比は、０．０１質量％以上１００質量％以下であることが好ましい。
上記の銅または鉄カチオン量の沸石に対する質量比が０．０１質量％より小さい場合には、銅または鉄カチオン量が少なすぎ、沸石自体の色が薄くなりすぎ、光の吸収が少なくなるので、沸石担持効果が得られづらい。
逆に、この質量比が１００％より大きい場合には、沸石成分の可視光吸収が多くなりすぎ、光触媒本体まで光が届きづらくなり、光触媒活性の低下をもたらす。
The mass ratio of the copper cation exchange type component, copper cation dope type component, iron cation exchange type component, or iron cation dope type component to zeolite is preferably 0.01% by mass or more and 100% by mass or less.
If the mass ratio of the amount of copper or iron cation to zeolite is less than 0.01% by mass, the amount of copper or iron cation is too small, the zeolite itself becomes too light in color, and light absorption is reduced. Zeolite loading effect is difficult to obtain.
On the other hand, when the mass ratio is larger than 100%, the visible light absorption of the zeolite component is excessive, and it becomes difficult for light to reach the photocatalyst body, resulting in a decrease in photocatalytic activity.
（光触媒複合体材料の光触媒機構）
図１は、本発明の一実施の形態による可視光応答型光触媒による有機物質の分解メカニズムを説明する構造模式図である。
可視光が可視光応答型光触媒の粒子に照射されると、可視光応答型光触媒のバンドギャップ以上の光が照射されることとなるので、可視光応答型光触媒の価電子帯の電子が伝導帯に励起して、伝導帯に励起電子ｅ−を形成するとともに、価電子帯にホールｈ＋を形成する。
(Photocatalytic mechanism of photocatalytic composite materials)
FIG. 1 is a structural schematic diagram illustrating a decomposition mechanism of an organic substance by a visible light responsive photocatalyst according to an embodiment of the present invention.
When visible light is irradiated onto the particles of the visible light responsive photocatalyst, light exceeding the band gap of the visible light responsive photocatalyst is irradiated, so the electrons in the valence band of the visible light responsive photocatalyst are in the conduction band. To form excited electrons e − in the conduction band and holes h + in the valence band.
ホールｈ＋は酸化力を持っており、有機物質を酸化することができる。一方、励起電子ｅ−は酸素の還元反応によって消費される。そのため、離別した励起電子ｅ−とホールｈ＋が粒子表面付近に移動すると、励起電子が反応物（酸素や水）を還元し、過酸化水素を生成し、ホールｈ＋が別の反応物（有機物）を酸化し、二酸化炭素にまで分解する光触媒反応を行う。 Hole h + has oxidizing power and can oxidize organic substances. On the other hand, excited electrons e − are consumed by the reduction reaction of oxygen. Therefore, when the separated excited electrons e − and holes h + move to the vicinity of the particle surface, the excited electrons reduce reactants (oxygen and water) to generate hydrogen peroxide, and the holes h + are separated from other reactants ( The organic matter is oxidized and photocatalytic reaction which decomposes to carbon dioxide is performed.
反応の主体となる離別した励起電子ｅ−とホールｈ＋は、光触媒反応をしないと、再結合反応する。励起電子ｅ−の酸素還元反応がうまく進行しないと、励起電子ｅ−の消費が進まず、励起電子ｅ−とホールｈ＋の再結合が増え、光触媒活性が大きく低下する。または失活してしまう。その結果、再結合反応に対する光触媒反応の発生確率が相対的に低くなり、光触媒反応の発生効率が低くなる。 The separated excited electrons e − and holes h + that are the main components of the reaction recombine if they are not photocatalytically reacted. If the oxygen reduction reaction does not proceed well, the excited electrons e - - excited electrons e consumption does not proceed, the excited electrons e - and holes h + recombination increases the photocatalytic activity decreases significantly. Or it will be deactivated. As a result, the probability of occurrence of the photocatalytic reaction to the recombination reaction becomes relatively low, and the generation efficiency of the photocatalytic reaction becomes low.
また、可視光応答型光触媒を単独で用いた場合には、空気中の水と酸素を反応させて、過酸化水素を生成する反応を生じさせ、生成した過酸化水素（Ｈ２Ｏ２）が粒子表面の一部または全部を覆う場合を生じさせる。表面がＨ２Ｏ２で覆われているので、還元反応及び酸化反応を行うことができない。
これにより、光触媒反応の発生効率をより低減させる。
In addition, when the visible light responsive photocatalyst is used alone, water in the air reacts with oxygen to generate hydrogen peroxide, and the generated hydrogen peroxide (H 2 O 2 ) The case of covering part or all of the particle surface is generated. Since the surface is covered with H 2 O 2 , the reduction reaction and the oxidation reaction cannot be performed.
Thereby, the generation efficiency of the photocatalytic reaction is further reduced.
しかし、可視光応答型光触媒１１を担体１２（土成分や沸石成分）に担持すると、図１（分解メカニズム）に示すように励起電子によって生成した過酸化水素が担体表面や担体と光触媒との界面へ拡散し濃縮され、また、有機物質１３も吸着能に優れる担体上に濃縮される。この濃縮により過酸化水素と有機物質１３の反応性が高まり、そこに可視光による局所的な熱が加えられることで、劇的に過酸化水素と有機物質が反応し分解されることになり、光触媒表面を覆う可能性のある過酸化水素の量を削減できる。その結果、光触媒表面での電子消費を阻害していた過酸化水素が減り、高い光触媒活性を示すことができるようになる。また、沸石成分中の鉄や銅カチオンは過酸化水素などが不安定化させ、ラジカルが生成しやすくし、有機物分解の手助けをする。 However, when the visible light responsive photocatalyst 11 is supported on the carrier 12 (earth component or zeolite component), hydrogen peroxide generated by excited electrons is an interface between the carrier surface and the carrier and photocatalyst as shown in FIG. 1 (decomposition mechanism). The organic substance 13 is also concentrated on the carrier having excellent adsorption ability. By this concentration, the reactivity of hydrogen peroxide and organic substance 13 is increased, and by adding local heat by visible light, hydrogen peroxide and organic substance are dramatically reacted and decomposed, The amount of hydrogen peroxide that may cover the surface of the photocatalyst can be reduced. As a result, hydrogen peroxide that has hindered electron consumption on the surface of the photocatalyst is reduced, and high photocatalytic activity can be exhibited. In addition, iron and copper cations in the zeolite components destabilize hydrogen peroxide and the like, making it easy to generate radicals and helping decompose organic substances.
本発明の実施形態である光触媒複合体材料を光触媒として使用する際には、光触媒複合体材料を室温で用いてもよいが、過酸化水素をより速く消費するために、２０〜５００℃までの範囲のいずれかの温度に加温することもできる。これにより、可視光応答型光触媒反応を効率的に行うことができ、有害有機物質をより速やかに浄化できる。 When the photocatalyst composite material according to the embodiment of the present invention is used as a photocatalyst, the photocatalyst composite material may be used at room temperature. It can also be heated to any temperature in the range. Thereby, the visible light responsive photocatalytic reaction can be efficiently performed, and the harmful organic substance can be cleaned more quickly.
（光触媒複合体材料の製造方法）
次に、本発明の実施形態である光触媒複合体材料の製造方法について説明する。図２は、本発明の一実施の形態による光触媒複合体材料の製造方法を説明する流れ図である。
本発明の製造方法では、まず、可視光吸収成分を準備する（Ｓ１００）。可視光吸収成分とは、有色の土壌成分、有色の沸石又はそれらの混合体からなる担体をいう。有色の土壌成分としては、赤玉土で代表される赤土、バーミキュライト、サポナイト、パーライト、ピートモス、ミックスピートモス、ココソイル、珪藻土を利用することができる。また、有色の沸石成分としては、１価、２価の銅や２価、３価の鉄をドープまたはカチオン交換した沸石を利用することができる。
(Method for producing photocatalyst composite material)
Next, a method of producing the photocatalyst composite material according to the embodiment of the present invention will be described. FIG. 2 is a flowchart illustrating a method for producing a photocatalyst composite material according to an embodiment of the present invention.
In the manufacturing method of the present invention, first, a visible light absorbing component is prepared (S100). The visible light absorbing component refers to a carrier comprising a colored soil component, a colored zeolite or a mixture thereof. As colored soil components, red soil, vermiculite, saponite, pearlite, peat moss, mixed peat moss, coco soy, and diatomaceous earth typified by red jade soil can be used. Further, as the colored zeolite component, a zeolite obtained by doping or cation-exchanged monovalent, divalent copper, divalent, or trivalent iron can be used.
次に、光触媒を準備する（Ｓ１０２）。光触媒は、バンドギャップが１．４ｅＶ以上３．１ｅＶ以下であり、かつ、伝導帯のボトムのエネルギー準位から換算した酸化還元電位が０Ｖ以上＋０．７Ｖ以下（ｖｓ．ＳＨＥ，ｐＨ＝０）の金属酸化物半導体からなるものをいう。金属酸化物半導体としては、酸化タングステン、リン酸銀(Ａｇ３ＰＯ４)、ビスマス酸塩、チタン酸化物のいずれか１つまたは２つ以上からなる材料を用いることができる。また、前記チタン酸化物としては、Ｆｅ２ＴｉＯ５、ドープ型酸化チタン（ＦｅとＴａの両方をドープした酸化チタン若しくはＴｉ３＋及び／又はＴｉ４＋を格子間位置にドープした酸化チタン）を用いることが可能である。また、ビスマス酸塩は、ビスマス酸ナトリウム（ＮａＢｉＯ３）、ＣａＢｉ２Ｏ４をはじめとするビスマス酸カルシウム、ビスマス酸ストロンチウムを用いることができる。 Next, a photocatalyst is prepared (S102). The photocatalyst has a band gap of 1.4 eV or more and 3.1 eV or less, and an oxidation-reduction potential converted from the energy level at the bottom of the conduction band of 0 V or more and +0.7 V or less (vs. SHE, pH = 0). The thing which consists of a metal oxide semiconductor. As the metal oxide semiconductor, a material made of any one or more of tungsten oxide, silver phosphate (Ag 3 PO 4 ), bismuth acid salt, and titanium oxide can be used. Further, as the titanium oxide, Fe 2 TiO 5 , doped titanium oxide (titanium oxide doped with both Fe and Ta, or titanium oxide doped with Ti 3+ and / or Ti 4+ at interstitial positions) is used. Is possible. As the bismuth acid salt, calcium bismuth and strontium bismuth including sodium bismuth (NaBiO 3 ) and CaBi 2 O 4 can be used.
次の工程では、混合溶液を調製する（Ｓ１０４）。混合溶液の成分は、担体と可視光応答型光触媒の比が０．０１質量％以上５００質量％以下となるように調製したものである。この調整では、担体と可視光応答型光触媒を溶媒中に分散して、混合してから、攪拌して、混合溶液を調製するとよい。
また、乳鉢などで十分に分散できる場合は、溶媒を用いずに混合撹拌して本発明の光触媒複合材料を作製することもできる。
混合の際には、乳鉢の代わりにビーズミルやボールミルを利用して、材料を分散させることもできる。また、磁気撹拌子とスターラ―を用いて分散させることもできる。なお、担体を水溶液に分散させず、固体のまま、金属酸化物と混ぜ合わせてもよい。
In the next step, a mixed solution is prepared (S104). The components of the mixed solution are prepared so that the ratio of the carrier to the visible light responsive photocatalyst is 0.01% by mass or more and 500% by mass or less. In this preparation, the carrier and the visible light responsive photocatalyst may be dispersed in a solvent, mixed, and then stirred to prepare a mixed solution.
Moreover, when it can fully disperse | distribute with a mortar etc., it can also carry out mixing stirring without using a solvent, and can also produce the photocatalyst composite material of this invention.
At the time of mixing, in place of a mortar, a bead mill or a ball mill may be used to disperse the material. It can also be dispersed using a magnetic stirrer and a stirrer. The carrier may be mixed with the metal oxide as it is without being dispersed in the aqueous solution.
次の工程では、混合溶液を加熱して、光触媒複合体材料を作製する（Ｓ１０６）。加熱して、乾燥させて、溶媒を除去することで、金属酸化物を有色の土または沸石担体に担持できる。
混合溶液は、例えば、乾燥機等を用いて、乾燥させることが好ましい。これにより、残存した溶媒が気化して、溶媒とともに溶媒中の不純物等を取り除くことができる。好ましくは、混合溶液を４０℃以上１００℃未満の温度で加熱して、乾燥を早めても良い。
In the next step, the mixed solution is heated to produce a photocatalyst composite material (S106). The metal oxide can be supported on a colored earth or zeolite support by heating and drying to remove the solvent.
The mixed solution is preferably dried using, for example, a drier or the like. Thereby, the remaining solvent is vaporized, and impurities and the like in the solvent can be removed together with the solvent. Preferably, the mixed solution may be heated at a temperature of 40 ° C. or higher and lower than 100 ° C. to accelerate drying.
なお、混合溶液の加熱を１２０℃以上１０００℃以下の高温で行えば、光触媒材料を焼成処理できる。これにより、光触媒材料中の不純物を取り除くことができるとともに、結晶性を向上させることができる。１０００℃は、通常の耐熱性を有する電気炉の使用上限温度であり、電気炉の使用規格に応じて６００℃や１２００℃等の各種の値を用いることができる。
以上の工程により、有色の土または沸石の表面に金属酸化物光触媒を担持でき、本発明の実施形態にかかる光触媒複合体材料を作製できる。
In addition, if the mixed solution is heated at a high temperature of 120 ° C. or higher and 1000 ° C. or lower, the photocatalytic material can be fired. Thereby, impurities in the photocatalytic material can be removed and the crystallinity can be improved. 1000 ° C. is a use upper limit temperature of an electric furnace having normal heat resistance, and various values such as 600 ° C. and 1200 ° C. can be used according to the use standard of the electric furnace.
By the above steps, the metal oxide photocatalyst can be supported on the surface of colored soil or zeolite, and the photocatalyst composite material according to the embodiment of the present invention can be manufactured.
なお、基板上に膜として形成すれば、安定、安全に使用でき、可視光照射下で長寿命な光触媒活性を示し、低価格な光触媒複合体材料を膜状の配置した基板を、光触媒処理面形状に合わせて容易に配置できる。 In addition, if it forms as a film on a substrate, it can be used stably and safely, shows long-lived photocatalytic activity under visible light irradiation, and the substrate on which a low cost photocatalyst composite material is arranged in a film form is treated with photocatalyst. It can be easily arranged according to the shape.
また、本発明の実施形態である光触媒複合体材料の光触媒特性に基づく分解反応、酸化反応、または還元反応により除去できる有害物質としては、環境ホルモン、農薬、殺虫剤、カビ、細菌、ウィルス、藻類、環境汚染物質、フロンガス、炭化水素、アルコール、アルデヒド、ケトン、カルボン酸、一酸化炭素、アミン、油、芳香族化合物、有機ハロゲン化合物、窒素化合物、硫黄化合物、有機リン化合物、タンパク質などを挙げることができる。さらに身の回りの汚れの原因となる石鹸や油、手垢、茶渋、台所のシンクのぬめりなども、この可視光応答型光触媒の光触媒反応により分解することができる。 In addition, as harmful substances that can be removed by the decomposition reaction, oxidation reaction or reduction reaction based on the photocatalytic properties of the photocatalyst composite material according to the embodiment of the present invention, environmental hormones, pesticides, insecticides, molds, bacteria, viruses, algae Environmental pollutants, fluorocarbons, hydrocarbons, alcohols, aldehydes, ketones, carboxylic acids, carbon monoxide, amines, oils, aromatic compounds, organic halogen compounds, nitrogen compounds, sulfur compounds, organic phosphorus compounds, proteins, etc. Can. Furthermore, soaps and oils, hand stains, tea astringents, and kitchen sink slimes that cause personal contamination can be decomposed by the photocatalytic reaction of the visible light responsive photocatalyst.
本発明の実施形態である光触媒複合体材料は、金属酸化物半導体が、酸化タングステン、リン酸銀(Ａｇ３ＰＯ４)、ビスマス酸塩、チタン酸化物（Ｆｅ２ＴｉＯ５、ドープ型酸化チタン（ＦｅとＴａの両方をドープした酸化チタン、若しくはＴｉ３＋、Ｔｉ４＋を格子間位置にドープした酸化チタン））のいずれか１つ以上である構成なので、これらの材料を主触媒として、水溶液に懸濁させても材料の遊離を生じさせず、安定、安全に使用でき、可視光照射下で長寿命な光触媒活性を示し、低価格な光触媒複合体材料を提供できる。また、ビスマス酸塩は、ビスマス酸ナトリウム（ＮａＢｉＯ３）、ＣａＢｉ２Ｏ４をはじめとするビスマス酸カルシウム、ビスマス酸ストロンチウムを挙げることができる。 In the photocatalytic composite material according to the embodiment of the present invention, the metal oxide semiconductor is made of tungsten oxide, silver phosphate (Ag 3 PO 4 ), bismuth salt, titanium oxide (Fe 2 TiO 5 , doped titanium oxide ( It is configured to be one or more of titanium oxide doped with both Fe and Ta, or titanium oxide doped with Ti 3+ and Ti 4+ at interstitial positions)). Even if turbid, it does not cause liberation of the material, can be used stably and safely, exhibits a long-life photocatalytic activity under visible light irradiation, and can provide a low-cost photocatalyst composite material. Further, examples of the bismuth acid salt include calcium bismuthate including sodium bismuthate (NaBiO 3 ) and CaBi 2 O 4 , and strontium bismuthate.
本発明の実施形態である光触媒複合体材料及びその製造方法は、上記実施形態に限定されるものではなく、本発明の技術的思想の範囲内で、種々変更して実施することができる。表１は、実施例１−６と比較例１−４における光触媒名称と約１日経過後のＣＯ２生成量を載せたものである。
（実施例１）
１０ｗｔ％バーミキュライト−ＷＯ３を以下に示す方法を用いて作製した。
まず、バーミキュライト（南アフリカ産）を乳鉢で粉砕後、純水中でよく撹拌し、懸濁液（スラリー）を作った。次に、その懸濁液と酸化タングステンＷＯ３（和光純薬社製）を十分な時間撹拌し、粉末を得た。粉末の混合比は重量比でバーミキュライト：ＷＯ３＝１０：１００であった。
次に、それを７０℃で４〜５時間乾燥させて、粉末試料（実施例１試料）を得た。
Example 1
10 wt% vermiculite-WO 3 was made using the method shown below.
First, vermiculite (produced in South Africa) was ground in a mortar and then thoroughly stirred in pure water to form a suspension (slurry). Next, the suspension and tungsten oxide WO 3 (manufactured by Wako Pure Chemical Industries, Ltd.) were stirred for a sufficient time to obtain a powder. The mixing ratio of the powder was vermiculite: WO 3 = 10: 100 by weight.
Next, it was dried at 70 ° C. for 4 to 5 hours to obtain a powder sample (Example 1 sample).
まず、この粉末試料（実施例１試料）の担体であるバーミキュライトの光吸収特性を測定した（図３）。４００ｎｍ以上の可視光線を吸収していることが見られる。酸化タングステンの吸収端は約４７０ｎｍであり、バーミキュライトはそれより長波長の可視光・赤外光を熱エネルギーとして、反応に有効に使用できることを示唆している。 First, the light absorption characteristics of vermiculite, which is the carrier of this powder sample (sample of Example 1), were measured (FIG. 3). It can be seen that it absorbs visible light of 400 nm or more. The absorption edge of tungsten oxide is about 470 nm, which suggests that vermiculite can be effectively used for the reaction by using visible light / infrared light having a longer wavelength as thermal energy.
次に、この粉末試料（実施例１試料）の光触媒活性評価を、２−プロパノール（ＩＰＡ）ガスの分解試験により実施した。
粉末試料（実施例１試料）０．４ｇを５００ｍＬの反応容器内部に、約８ｃｍ２になるように置き、その後、純空気で反応容器内を置換した。
次に、反応容器内の２−プロパノールガスの濃度が約６００〜９００ｐｐｍになるようにガスを注入した。光源には３００ＷのＸｅランプを用い、反応容器の上部面に設けた窓部を通して、カットオフフィルター、水フィルターを用いて、４００ｎｍ〜５３０ｎｍの可視光線を約１ｍＷｃｍ−２で反応容器の粉末試料（実施例１試料）に室温で照射した。
Next, the photocatalytic activity evaluation of this powder sample (example 1 sample) was carried out by a decomposition test of 2-propanol (IPA) gas.
In a 500 mL reaction vessel, 0.4 g of a powder sample (example 1 sample) was placed to be about 8 cm 2 , and then the inside of the reaction vessel was replaced with pure air.
Next, the gas was injected so that the concentration of 2-propanol gas in the reaction vessel became about 600 to 900 ppm. Using a 300 W Xe lamp as the light source, through a window provided on the upper surface of the reaction vessel, using a cut-off filter and a water filter, visible light from 400 nm to 530 nm at about 1 mWcm −2 (powder sample of the reaction vessel) Example 1 sample) was irradiated at room temperature.
２−プロパノールガスは、光触媒酸化反応により酸化分解され、反応中間体であるアセトンを経由して、最終的には二酸化炭素が生成した。実施例１の試料を利用した実験では、反応初期はアセトンが選択的に生成した。図４に実施例１に示した試料の中間体アセトンの生成量の時間変化を示す。反応初期では時間にほぼ比例して、アセトンが生成することが見られ、１２０分後のアセトン量は約１８０ｐｐｍであった。また、さらに光照射するとアセトンが分解して二酸化炭素が生成し、約１日間の光照射後の二酸化炭素の量は約７１０ｐｐｍとなった。このことは光触媒反応により有機物である２−プロパノールが最終的には無機物である二酸化炭素にまで分解されたことを意味する。 The 2-propanol gas was oxidatively decomposed by a photocatalytic oxidation reaction, and finally carbon dioxide was produced via acetone as a reaction intermediate. In the experiment using the sample of Example 1, acetone was selectively generated at the beginning of the reaction. FIG. 4 shows the change over time in the amount of intermediate acetone produced in the sample shown in Example 1. In the initial stage of the reaction, it was observed that acetone was generated almost in proportion to the time, and the amount of acetone after 120 minutes was about 180 ppm. Further, when the light was further irradiated, acetone was decomposed to generate carbon dioxide, and the amount of carbon dioxide after the light irradiation for about 1 day was about 710 ppm. This means that 2-propanol which is an organic substance is finally decomposed into carbon dioxide which is an inorganic substance by a photocatalytic reaction.
（実施例２）
１ｗｔ％バーミキュライト−ＷＯ３は実施例１と同様の方法を用いて作製された。その作製した試料を実施例１と同様の方法で光触媒活性を評価した。
２−プロパノールガスは、光触媒酸化反応により酸化分解され、最終的には二酸化炭素が生成した。約１日間の光照射後の二酸化炭素の量は約１５００ｐｐｍとなった。
(Example 2)
1 wt% vermiculite-WO 3 was produced using the same method as in Example 1. The photocatalytic activity of the prepared sample was evaluated in the same manner as in Example 1.
The 2-propanol gas was oxidatively decomposed by a photocatalytic oxidation reaction, and finally carbon dioxide was generated. The amount of carbon dioxide after light irradiation for about 1 day was about 1500 ppm.
（実施例３）
赤土の１つである赤玉土を利用した光触媒複合体１０ｗｔ％赤玉土−ＷＯ３を以下に示す方法で作製した。
まず、３００℃で熱風乾燥処理した赤玉土を乳鉢で粉砕後、純水を５ｃｃ入れ、懸濁させた。その後、酸化タングステンＷＯ３（和光純薬社製）を添加し、十分な時間撹拌し、粉末を得た。粉末の混合比は重量比で赤玉土：ＷＯ３＝１０：１００であった。
図３に担体赤玉土の吸収スペクトルを示す。赤玉土は４００ｎｍ以上の可視光・赤外光を吸収し、照射される光エネルギーを有効に分解反応に利用できることを示している。そして、その作製した試料を実施例１と同様の方法で光触媒活性を評価した。
２−プロパノールガスは、光触媒酸化反応により酸化分解され、最終的には二酸化炭素が生成した。約１日間の光照射後の二酸化炭素の量は約９２０ｐｐｍとなった。
(Example 3)
A photocatalyst complex 10 wt% Akatama-Wo 3 using red jadeite which is one of the red soils was produced by the method shown below.
First, red egg clay subjected to hot air drying at 300 ° C. was crushed in a mortar, and then 5 cc of pure water was added and suspended. Thereafter, tungsten oxide WO 3 (manufactured by Wako Pure Chemical Industries, Ltd.) was added and stirred for a sufficient time to obtain a powder. The mixing ratio of the powder was red ball soil: WO 3 = 10: 100 in weight ratio.
The absorption spectrum of carrier red egg soil is shown in FIG. Akadama soil absorbs visible light and infrared light of 400 nm or more, and shows that the irradiated light energy can be used effectively for the decomposition reaction. And the photocatalytic activity was evaluated by the method similar to Example 1 to the produced sample.
The 2-propanol gas was oxidatively decomposed by a photocatalytic oxidation reaction, and finally carbon dioxide was generated. The amount of carbon dioxide after light irradiation for about 1 day was about 920 ppm.
（実施例４）
１０ｗｔ％Ｃｕ（ＩＩ）カチオン交換型モルデナイト−ＷＯ３を以下に示す方法を利用して作製した。まず、Ｃｕ（ＮＯ３）２を純水に溶かし、約０．０１２ｍｏｌ／ＬのＣｕ（ＮＯ３）２水溶液を作製した。この水溶液２５０ｍＬに３ｇのＮａ型モルデナイトを入れ撹拌した。その後、純水で十分に洗浄後７０〜８０℃で乾燥させ、Ｃｕ（ＩＩ）カチオン型モルデナイトを得た。なお、Ｃｕカチオンとモルデナイトの仕込み比は重量比で６．３：１００であった。
その後、Ｃｕ（ＩＩ）カチオン型モルデナイトを純水中で撹拌し、懸濁させ、懸濁液を作製した。この懸濁液にＷＯ３を添加し、乳鉢で十分撹拌、担持し、試料を得た。粉末の混合比は重量比でＣｕ（ＩＩ）カチオン型モルデナイト：ＷＯ３＝１０：１００であった。
そして、その作製した試料を実施例１と同様の方法で光触媒活性を評価した。
２−プロパノールガスは、光触媒酸化反応により酸化分解され、最終的には二酸化炭素が生成した。約１日間の光照射後の二酸化炭素の量は約７９０ｐｐｍとなった。
(Example 4)
10 wt% Cu (II) cation exchange mordenite-WO 3 was prepared using the method shown below. First, Cu (NO 3 ) 2 was dissolved in pure water to prepare an about 0.012 mol / L Cu (NO 3 ) 2 aqueous solution. 3 g of Na-type mordenite was added to 250 mL of this aqueous solution and stirred. Then, after thoroughly washing with pure water, it was dried at 70-80 ° C. to obtain Cu (II) cationic mordenite. In addition, the preparation ratio of Cu cation and mordenite was 6.3: 100 by weight ratio.
Thereafter, Cu (II) cation mordenite was stirred in pure water and suspended to prepare a suspension. WO 3 was added to this suspension and sufficiently stirred and supported in a mortar to obtain a sample. The mixing ratio of the powder was Cu (II) cationic mordenite: WO 3 = 10: 100 by weight.
Then, the photocatalytic activity of the produced sample was evaluated in the same manner as in Example 1.
The 2-propanol gas was oxidatively decomposed by a photocatalytic oxidation reaction, and finally carbon dioxide was generated. The amount of carbon dioxide after light irradiation for about 1 day was about 790 ppm.
（実施例５）
１０ｗｔ％Ｆｅ（ＩＩＩ）カチオン交換型モルデナイト−ＷＯ３を以下に示す方法を利用して作製した。まず、０．４０５ｇのＦｅＣｌ３を２５０ｍＬの純水に溶かし、ＦｅＣｌ３水溶液を作製した。これに３ｇのＮａ型モルデナイトを入れ、十分な時間撹拌した。その後、純水で十分に洗浄後７０〜８０℃で乾燥させ、Ｆｅ（ＩＩＩ）カチオン型モルデナイトを得た。なお、Ｆｅカチオンとモルデナイトの仕込み比は重量比で４．６：１００であった。
その後、Ｆｅ（ＩＩＩ）カチオン型モルデナイトを純水中で撹拌し、懸濁させ、懸濁液を作製した。この懸濁液にＷＯ３を添加し、乳鉢で十分撹拌、担持し、粉末試料を得た。
粉末の混合比は重量比でＦｅ（ＩＩＩ）カチオン型モルデナイト：ＷＯ３＝１０：１００であった。そして、その作製した試料を実施例１と同様の方法で光触媒活性を評価した。２−プロパノールガスは、光触媒酸化反応により酸化分解され、最終的には二酸化炭素が生成した。約１日間の光照射後の二酸化炭素の量は約１６００ｐｐｍとなった。
(Example 5)
10 wt% Fe (III) cation exchange mordenite-WO 3 was prepared using the method shown below. First, 0.405 g of FeCl 3 was dissolved in 250 mL of pure water to prepare an FeCl 3 aqueous solution. To this, 3 g of Na-type mordenite was added and stirred for a sufficient time. Then, after thoroughly washing with pure water, it was dried at 70-80 ° C. to obtain Fe (III) cationic mordenite. In addition, the preparation ratio of Fe cation and mordenite was 4.6: 100 by weight ratio.
Thereafter, the Fe (III) cation mordenite was stirred in pure water and suspended to prepare a suspension. WO 3 was added to this suspension and sufficiently stirred and supported in a mortar to obtain a powder sample.
The mixing ratio of the powder was Fe (III) cationic mordenite: WO 3 = 10: 100 in weight ratio. And the photocatalytic activity was evaluated by the method similar to Example 1 to the produced sample. The 2-propanol gas was oxidatively decomposed by a photocatalytic oxidation reaction, and finally carbon dioxide was generated. The amount of carbon dioxide after light irradiation for about 1 day was about 1600 ppm.
（実施例６）
１００ｗｔ％Ｆｅ（ＩＩＩ）カチオン交換型モルデナイト−ＷＯ３は実施例５と同様の方法で作製された。そして、その作製した試料を実施例１と同様の方法で光触媒活性を評価した。２−プロパノールガスは、光触媒酸化反応により酸化分解され、最終的には二酸化炭素が生成した。約１日間の光照射後の二酸化炭素の量は約６００ｐｐｍとなった。
(Example 6)
100 wt% Fe (III) cation exchange mordenite-WO 3 was prepared in the same manner as Example 5. Then, the photocatalytic activity of the produced sample was evaluated in the same manner as in Example 1. The 2-propanol gas was oxidatively decomposed by a photocatalytic oxidation reaction, and finally carbon dioxide was generated. The amount of carbon dioxide after light irradiation for about 1 day was about 600 ppm.
（比較例１）
次に、酸化タングステン（和光純薬社製）を比較例１試料として単独で用いた。酸化タングステン（比較例１試料）の光触媒活性評価を実施例１で示した方法と同じ方法で行った。さらに、約１日間の光照射後の二酸化炭素の量は約０ｐｐｍとなった。つまり、光触媒反応が遅く実施例１〜６に比べて光触媒活性が顕著に劣っていることを示している。
(Comparative example 1)
Next, tungsten oxide (manufactured by Wako Pure Chemical Industries, Ltd.) was used alone as a comparative example 1 sample. The photocatalytic activity of tungsten oxide (comparative example 1 sample) was evaluated in the same manner as the method described in Example 1. Furthermore, the amount of carbon dioxide after light irradiation for about 1 day was about 0 ppm. That is, it shows that the photocatalytic reaction is slow and the photocatalytic activity is significantly inferior to Examples 1 to 6.
酸化タングステンの単独（比較例１）の場合は光触媒活性の低下を招いた。
酸化タングステン（比較例１）の光触媒反応では、ホールによってＩＰＡなどの有機物を酸化し、電子は、最初は酸素の２電子還元反応によって酸素を過酸化水素にまで還元することで消費された。また、酸化タングステンは過酸化水素を分解または消費する能力に劣るため、酸化タングステン表面に過酸化水素が蓄積してしまった。その結果、過酸化水素の消費速度が極端に遅いため、光触媒反応で生成した電子が有効に消費されづらくなり、ホールと電子の再結合が非常に起こりやすくなる。また、実施例１では擬０次反応で光触媒反応が進行しアセトンの生成濃度が時間に比例して増加するが、逆に比較例１では、４０分以降のアセトンの生成速度が顕著に低下し、４０分以降光触媒活性が低下してしまった（図４）。
In the case of tungsten oxide alone (Comparative Example 1), the photocatalytic activity was lowered.
In the photocatalytic reaction of tungsten oxide (Comparative Example 1), organic substances such as IPA were oxidized by holes, and electrons were initially consumed by reducing oxygen to hydrogen peroxide by a two-electron reduction reaction of oxygen. Further, since tungsten oxide is inferior in ability to decompose or consume hydrogen peroxide, hydrogen peroxide has accumulated on the surface of tungsten oxide. As a result, since the consumption rate of hydrogen peroxide is extremely slow, the electrons generated by the photocatalytic reaction are hardly consumed effectively, and the recombination of holes and electrons is very likely to occur. In addition, in Example 1, the photocatalytic reaction proceeds in the pseudo 0th order reaction, and the formation concentration of acetone increases in proportion to time. Conversely, in Comparative Example 1, the formation rate of acetone after 40 minutes is significantly reduced. After 40 minutes, the photocatalytic activity decreased (FIG. 4).
一方、優れた吸着特性を持ち、可視光にも吸収を持つバーミキュライトを始めとする前記酸化物を利用すると、光触媒の還元反応で生じた過酸化水素と有機物がバーミキュライトを始めとする担体上または担体と光触媒との界面で濃縮される。そして、バーミキュライトを始めとする担体は可視光を吸収し、熱エネルギーとして利用できるため、過酸化水素と有機物の分解反応を促進することができる。また、混合原子価をとりやすい鉄カチオンを含むゼオライトを始めとする前記沸石を用いると、過酸化酸素の反応性がさらに増し、より過酸化水素が分解されやすくかつラジカルも発生しやすくなり、有機物の分解反応も促進されることになる。その結果、有色の土または沸石成分を担持させた可視光応答型光触媒の電子の消費が進み、表１の実施例１で示すように高い光触媒活性を示した。 On the other hand, when using the oxides such as vermiculite which has excellent adsorption characteristics and also absorbs visible light, hydrogen peroxide and organic substances generated by the reduction reaction of the photocatalyst are on or on the carrier such as vermiculite. Concentrated at the interface between Since carriers such as vermiculite absorb visible light and can be used as thermal energy, the decomposition reaction of hydrogen peroxide and organic matter can be promoted. In addition, when using the above zeolite including zeolite containing iron cation which easily takes mixed valence, the reactivity of oxygen peroxide is further increased, hydrogen peroxide is easily decomposed and radicals are more easily generated, and organic substances The decomposition reaction of is also promoted. As a result, the consumption of electrons of the visible light responsive photocatalyst carrying colored soil or zeolite components progressed, and high photocatalytic activity was exhibited as shown in Example 1 of Table 1.
（比較例２）
次に、１ｗｔ％Ｎａ型モルデナイト−ＷＯ３を以下に示す方法を利用して比較例として作製した。Ｎａ型モルデナイトを純水中で撹拌し、懸濁させ、懸濁液を作製した。この懸濁液にＷＯ３を添加し、乳鉢で十分撹拌、担持し、試料を得た。粉末の混合比は重量比でＮａ型モルデナイト：ＷＯ３＝１：１００であった。そして、その作製した試料を実施例１と同様の方法で光触媒活性を評価した。
２−プロパノールガスは、光触媒酸化反応により酸化分解され、最終的には二酸化炭素が生成した。約１日間の光照射後の二酸化炭素の量は約２５ｐｐｍとなった。
(Comparative example 2)
Next, 1 wt% Na-type mordenite-WO 3 was produced as a comparative example using the method shown below. Na-type mordenite was stirred in pure water and suspended to prepare a suspension. WO 3 was added to this suspension and sufficiently stirred and supported in a mortar to obtain a sample. The mixing ratio of the powder was Na-type mordenite: WO 3 = 1: 100 in weight ratio. Then, the photocatalytic activity of the produced sample was evaluated in the same manner as in Example 1.
The 2-propanol gas was oxidatively decomposed by a photocatalytic oxidation reaction, and finally carbon dioxide was generated. The amount of carbon dioxide after light irradiation for about one day was about 25 ppm.
（比較例３）
次に、１００ｗｔ％Ｎａ型モルデナイト−ＷＯ３を以下に示す方法を利用して比較例として比較例２と同様の方法で作製した。粉末の混合比は重量比でＮａ型モルデナイト：ＷＯ３＝１００：１００であった。そして、その作製した試料を実施例１と同様の方法で光触媒活性を評価した。２−プロパノールガスは、光触媒酸化反応により酸化分解され、最終的には二酸化炭素が生成した。約１日間の光照射後の二酸化炭素の量は約８１ｐｐｍとなった。
(Comparative example 3)
Were then prepared in the same manner as in Comparative Example 2 As a comparative example a 100 wt% Na-type mordenite -WO 3 using the method described below. The mixing ratio of the powder was Na-type mordenite: WO 3 = 100: 100 by weight. Then, the photocatalytic activity of the produced sample was evaluated in the same manner as in Example 1. The 2-propanol gas was oxidatively decomposed by a photocatalytic oxidation reaction, and finally carbon dioxide was generated. The amount of carbon dioxide after light irradiation for about 1 day was about 81 ppm.
このようにＮａ型モルデナイトを用いると、ＷＯ３単独よりも活性が高くなる。しかし、Ｎａモルデナイトは図３に示すように、可視光域に吸収を持たないため、照射された光エネルギーを熱に変えることができなく、有機物と過酸化水素の分解反応が促進されづらい。その結果、比較例２、３のようにＮａ型モルデナイトＷＯ３は実施例１−６のバーミキュライトを始めとする担体に担持されたＷＯ３よりも活性が低くなった。 When Na-type mordenite is used in this way, the activity is higher than that of WO 3 alone. However, as shown in FIG. 3, Na mordenite has no absorption in the visible light region, so that the irradiated light energy cannot be changed to heat, and it is difficult to promote the decomposition reaction between the organic matter and hydrogen peroxide. As a result, as in Comparative Examples 2 and 3, Na-type mordenite WO 3 was less active than WO 3 supported on a carrier such as vermiculite of Example 1-6.
（比較例４）
鉄カチオン型モルデナイトは実施例５と同じ方法で作製した。
そして、その作製した試料を実施例１と同様の方法で光触媒活性を評価した。
その結果、一部の２−プロパノールは分解して、二酸化炭素を生成するが、その二酸化炭素は約７．４ｐｐｍと非常に低く、活性は実施例１を始めとする前記光触媒担持有色土または沸石複合体の活性（実施例１から６）よりも大幅に低く、鉄カチオン型モルデナイトを単独で用いても、有機物を分解する能力が不足していることが分かった。
(Comparative example 4)
The iron cation mordenite was prepared in the same manner as in Example 5.
Then, the photocatalytic activity of the produced sample was evaluated in the same manner as in Example 1.
As a result, some 2-propanol decomposes to produce carbon dioxide, which is very low at about 7.4 ppm, and the activity is the above-mentioned photocatalyst-supported colored earth or zeolite including Example 1. It was significantly lower than the activity of the composite (Examples 1 to 6), and it was found that the ability to decompose organic substances was insufficient even when iron cation mordenite was used alone.
なお、本発明は上記の実施例に限定されるものではなく、光触媒の技術分野における通常の知識を有するものにとって自明事項の範囲内で、各種の組成物の取捨選択を含むものである。例えば、上記の実施例ではゼオライトとしてモルデナイトを用いる場合を示しているが、ゼオライトとしては２００種類程度の細区分が存在しており、モルデナイトと同程度の範囲の他の細区分に含まれるものを用いても良い。例えば、ゼオライトの骨格構造は、国際ゼオライト学会（International Zeolite Association）によりデータベース化されており、アルファベット大文字３個からなる構造コードが与えられている（http://www.iza-structure.org/databases/）。この構造コードは骨格の幾何構造のみを指定するものであり、組成や格子定数が異なっても幾何構造が等しければ同じ構造コードに含まれる。代表的な構造コードとしては、ＬＴＡ、ＦＥＲ（フェリエライト）、ＭＷＷ、ＭＦＩ、ＭＯＲ（モルデナイト）、ＬＴＬ、ＦＡＵ、ＢＥＡがある。 In addition, this invention is not limited to said Example, The selection of various compositions is included in the range of an obvious matter for the person who has the normal knowledge in the technical field of a photocatalyst. For example, although the case of using mordenite as the zeolite is shown in the above-mentioned example, there are about 200 types of fine divisions as the zeolite, and those contained in other fine divisions in the same range as mordenite You may use. For example, the framework structure of the zeolite is databased by the International Zeolite Association and given a structure code consisting of 3 capital letters (http://www.iza-structure.org/databases /). This structure code designates only the geometric structure of the skeleton, and even if the composition and lattice constant are different, they are included in the same structure code if the geometric structures are the same. Typical structure codes include LTA, FER (ferrierite), MWW, MFI, MOR (mordenite), LTL, FAU, and BEA.
本発明の光触媒複合体材料は、これを基板の一面に塗布して、光触媒複合体材料膜とすることで、安定、安全に使用でき、可視光照射下で長寿命な光触媒活性を示す。そこで、光触媒複合体材料を膜状の配置した基板を、光触媒処理面形状に合わせて容易に配置することで、有機物や非金属の無機物を効率よく酸化または還元することができ、例えば室内に存在するシックハウス症候群等を引き起こす有害な有機物質も分解することができる。 The photocatalyst composite material of the present invention is applied to one surface of a substrate to form a photocatalyst composite material film, so that it can be used stably and safely, and exhibits long-lived photocatalytic activity under visible light irradiation. Therefore, organic substances and nonmetallic inorganic substances can be efficiently oxidized or reduced by arranging the substrate on which the photocatalytic composite material is arranged in a film shape in accordance with the shape of the surface treated with the photocatalyst, for example, indoors Harmful organic substances that cause sick house syndrome etc. can also be decomposed.
１１ 可視光応答型光触媒
１２ 担体
１３ 有機物質
11 Visible light responsive photocatalyst 12 Carrier 13 Organic substance
Claims (7)
前記可視光応答型光触媒が、バンドギャップが１．４ｅＶ以上３．１ｅＶ以下であり、かつ、伝導帯のボトムのエネルギー準位から換算した酸化還元電位が０Ｖ以上＋０．７Ｖ以下（ｖｓ．ＳＨＥ，ｐＨ＝０）の金属酸化物半導体であり、
前記金属酸化物半導体が、酸化タングステン、リン酸銀(Ａｇ３ＰＯ４)またはビスマス酸塩のいずれか１つまたは２つ以上からなり、
前記土成分は、バーミキュライト、パーライト、ピートモス、ミックスピートモス、ココソイル、サポナイト、珪藻土又は赤土のいずれか１つまたは２つ以上を含むことを特徴とする光触媒複合体材料。 A visible light responsive photocatalyst, and a supported on the surface of the visible light responsive photocatalyst, and containing a colored earth component that absorbs visible light or a zeolite component that is processed to be colored,
The visible light responsive photocatalyst has a band gap of 1.4 eV or more and 3.1 eV or less, and an oxidation-reduction potential converted from the energy level of the bottom of the conduction band of 0 V or more and +0.7 V or less (vs. SHE, a metal oxide semiconductor of pH = 0),
Wherein the metal oxide semiconductor, tungsten oxide, silver phosphate (Ag 3 PO 4) or Ri Do from any one or more of bismuth salt,
The soil component, vermiculite, perlite, peat moss, mixed peat moss, Kokosoiru, saponite, photocatalytic composite material characterized in it to contain one or more either diatomaceous earth or red clay.
バンドギャップが１．４ｅＶ以上３．１ｅＶ以下であり、かつ、伝導帯のボトムのエネルギー準位から換算した酸化還元電位が０Ｖ以上＋０．７Ｖ以下（ｖｓ．ＳＨＥ，ｐＨ＝０）の金属酸化物半導体からなる光触媒を準備する工程であって、前記金属酸化物半導体は酸化タングステン、リン酸銀(Ａｇ３ＰＯ４)またはビスマス酸塩のいずれか１つまたは２つ以上からなる、工程と、
前記可視光吸収成分と前記光触媒の比が０．０１質量％以上５００質量％以下となるようにして、混合溶液を調製する工程と、
前記混合溶液を加熱して、光触媒複合体材料を作製する工程とを有することを特徴とする、請求項１〜５のいずれかに記載の光触媒複合体材料の製造方法。 Soil component of colored absorbing visible light, there is enough engineering to prepare a visible light absorbing component comprising any one or more of the metal-exchanged zeolite components of colored or metal doped zeolite component of the color, the soil The step comprises one or more of vermiculite, perlite, peat moss, mixed peat moss, coco soil, saponite, diatomaceous earth or red earth, and
Metal oxide having a band gap of 1.4 eV or more and 3.1 eV or less and an oxidation-reduction potential converted from the energy level at the bottom of the conduction band of 0 V or more and +0.7 V or less (vs. SHE, pH = 0) A step of preparing a photocatalyst comprising a semiconductor, wherein the metal oxide semiconductor comprises at least one of tungsten oxide, silver phosphate (Ag 3 PO 4 ) and bismuth acid salt;
Preparing a mixed solution such that the ratio of the visible light absorbing component to the photocatalyst is 0.01% by mass or more and 500% by mass or less;
The method for producing a photocatalyst composite material according to any one of claims 1 to 5 , further comprising the steps of: heating the mixed solution to produce a photocatalyst composite material.
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| CN103212392B (en) * | 2013-04-07 | 2015-04-22 | 昆明理工大学 | A kind of method for preparing TiO2/diatomite composite photocatalytic material by sol-gel method |
| JP6342225B2 (en) * | 2014-06-09 | 2018-06-13 | 国立研究開発法人物質・材料研究機構 | Photocatalyst composite material and method for producing the same |
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