TW201420182A - Transition metal compound-loaded titanium oxide - Google Patents
Transition metal compound-loaded titanium oxide Download PDFInfo
- Publication number
- TW201420182A TW201420182A TW102133754A TW102133754A TW201420182A TW 201420182 A TW201420182 A TW 201420182A TW 102133754 A TW102133754 A TW 102133754A TW 102133754 A TW102133754 A TW 102133754A TW 201420182 A TW201420182 A TW 201420182A
- Authority
- TW
- Taiwan
- Prior art keywords
- titanium oxide
- transition metal
- metal compound
- membrane
- carrying
- Prior art date
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- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 title claims abstract description 307
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 title claims abstract description 263
- 150000003623 transition metal compounds Chemical class 0.000 title claims abstract description 107
- 239000013078 crystal Substances 0.000 claims abstract description 73
- 229910052723 transition metal Inorganic materials 0.000 claims description 7
- 150000003624 transition metals Chemical class 0.000 claims description 6
- 230000001699 photocatalysis Effects 0.000 abstract description 37
- 238000000034 method Methods 0.000 description 88
- 150000002506 iron compounds Chemical class 0.000 description 85
- 239000000725 suspension Substances 0.000 description 77
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 75
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 67
- 239000012528 membrane Substances 0.000 description 66
- 238000001914 filtration Methods 0.000 description 60
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 57
- 238000010408 sweeping Methods 0.000 description 40
- 230000002441 reversible effect Effects 0.000 description 34
- 239000010936 titanium Substances 0.000 description 33
- 238000007254 oxidation reaction Methods 0.000 description 32
- 238000005374 membrane filtration Methods 0.000 description 30
- 238000003860 storage Methods 0.000 description 26
- 238000005406 washing Methods 0.000 description 26
- 239000000706 filtrate Substances 0.000 description 24
- 230000003647 oxidation Effects 0.000 description 24
- 238000006243 chemical reaction Methods 0.000 description 21
- 239000007789 gas Substances 0.000 description 21
- 239000000203 mixture Substances 0.000 description 21
- 239000000463 material Substances 0.000 description 20
- 239000007788 liquid Substances 0.000 description 19
- 238000004140 cleaning Methods 0.000 description 18
- 229910052719 titanium Inorganic materials 0.000 description 17
- 239000012510 hollow fiber Substances 0.000 description 16
- 239000007864 aqueous solution Substances 0.000 description 15
- -1 halogen ion Chemical class 0.000 description 15
- 239000012535 impurity Substances 0.000 description 15
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 14
- 239000002609 medium Substances 0.000 description 12
- 238000000926 separation method Methods 0.000 description 12
- 238000000108 ultra-filtration Methods 0.000 description 12
- 239000011521 glass Substances 0.000 description 11
- 238000000746 purification Methods 0.000 description 11
- 150000003609 titanium compounds Chemical class 0.000 description 11
- XJDNKRIXUMDJCW-UHFFFAOYSA-J titanium tetrachloride Chemical compound Cl[Ti](Cl)(Cl)Cl XJDNKRIXUMDJCW-UHFFFAOYSA-J 0.000 description 11
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 10
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 10
- 239000000460 chlorine Substances 0.000 description 10
- 239000000126 substance Substances 0.000 description 10
- 230000004043 responsiveness Effects 0.000 description 9
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 8
- RBTARNINKXHZNM-UHFFFAOYSA-K iron trichloride Chemical compound Cl[Fe](Cl)Cl RBTARNINKXHZNM-UHFFFAOYSA-K 0.000 description 8
- 239000002245 particle Substances 0.000 description 8
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 7
- 229910021578 Iron(III) chloride Inorganic materials 0.000 description 7
- 238000002360 preparation method Methods 0.000 description 7
- 238000001179 sorption measurement Methods 0.000 description 7
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 6
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 6
- 238000001816 cooling Methods 0.000 description 6
- 238000004332 deodorization Methods 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 6
- 239000011941 photocatalyst Substances 0.000 description 6
- 238000006722 reduction reaction Methods 0.000 description 6
- 238000004887 air purification Methods 0.000 description 5
- 230000000844 anti-bacterial effect Effects 0.000 description 5
- 239000001569 carbon dioxide Substances 0.000 description 5
- 229910002092 carbon dioxide Inorganic materials 0.000 description 5
- 150000001875 compounds Chemical class 0.000 description 5
- 230000008021 deposition Effects 0.000 description 5
- 125000000816 ethylene group Chemical group [H]C([H])([*:1])C([H])([H])[*:2] 0.000 description 5
- 230000005284 excitation Effects 0.000 description 5
- 238000005259 measurement Methods 0.000 description 5
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 5
- 229910052753 mercury Inorganic materials 0.000 description 5
- 229920002620 polyvinyl fluoride Polymers 0.000 description 5
- 229920005989 resin Polymers 0.000 description 5
- 239000011347 resin Substances 0.000 description 5
- 239000000243 solution Substances 0.000 description 5
- 238000003756 stirring Methods 0.000 description 5
- 230000003373 anti-fouling effect Effects 0.000 description 4
- 229910052801 chlorine Inorganic materials 0.000 description 4
- 238000000354 decomposition reaction Methods 0.000 description 4
- 238000005034 decoration Methods 0.000 description 4
- 229910052739 hydrogen Inorganic materials 0.000 description 4
- 239000001257 hydrogen Substances 0.000 description 4
- 239000000047 product Substances 0.000 description 4
- 238000009281 ultraviolet germicidal irradiation Methods 0.000 description 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 3
- 239000003795 chemical substances by application Substances 0.000 description 3
- 238000010335 hydrothermal treatment Methods 0.000 description 3
- 238000005470 impregnation Methods 0.000 description 3
- 229910052742 iron Inorganic materials 0.000 description 3
- 229920003023 plastic Polymers 0.000 description 3
- 239000004033 plastic Substances 0.000 description 3
- 229920002239 polyacrylonitrile Polymers 0.000 description 3
- 238000011085 pressure filtration Methods 0.000 description 3
- 238000010298 pulverizing process Methods 0.000 description 3
- 238000007086 side reaction Methods 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- 241000195493 Cryptophyta Species 0.000 description 2
- KCXVZYZYPLLWCC-UHFFFAOYSA-N EDTA Chemical compound OC(=O)CN(CC(O)=O)CCN(CC(O)=O)CC(O)=O KCXVZYZYPLLWCC-UHFFFAOYSA-N 0.000 description 2
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 2
- 239000005977 Ethylene Substances 0.000 description 2
- LSDPWZHWYPCBBB-UHFFFAOYSA-N Methanethiol Chemical compound SC LSDPWZHWYPCBBB-UHFFFAOYSA-N 0.000 description 2
- 239000004721 Polyphenylene oxide Substances 0.000 description 2
- GSEJCLTVZPLZKY-UHFFFAOYSA-N Triethanolamine Chemical compound OCCN(CCO)CCO GSEJCLTVZPLZKY-UHFFFAOYSA-N 0.000 description 2
- 150000001412 amines Chemical class 0.000 description 2
- 125000003118 aryl group Chemical group 0.000 description 2
- 238000011001 backwashing Methods 0.000 description 2
- 125000000484 butyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 2
- 229920002301 cellulose acetate Polymers 0.000 description 2
- 239000000919 ceramic Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 238000001514 detection method Methods 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000005684 electric field Effects 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 230000001747 exhibiting effect Effects 0.000 description 2
- 238000000605 extraction Methods 0.000 description 2
- 125000005843 halogen group Chemical group 0.000 description 2
- 150000002430 hydrocarbons Chemical group 0.000 description 2
- 238000005286 illumination Methods 0.000 description 2
- VCJMYUPGQJHHFU-UHFFFAOYSA-N iron(3+);trinitrate Chemical compound [Fe+3].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O VCJMYUPGQJHHFU-UHFFFAOYSA-N 0.000 description 2
- 238000000691 measurement method Methods 0.000 description 2
- 150000002736 metal compounds Chemical class 0.000 description 2
- 230000001151 other effect Effects 0.000 description 2
- 150000002923 oximes Chemical class 0.000 description 2
- 238000010422 painting Methods 0.000 description 2
- 230000000737 periodic effect Effects 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 229920000768 polyamine Polymers 0.000 description 2
- 229920000570 polyether Polymers 0.000 description 2
- 229920002098 polyfluorene Polymers 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 230000004044 response Effects 0.000 description 2
- YONPGGFAJWQGJC-UHFFFAOYSA-K titanium(iii) chloride Chemical compound Cl[Ti](Cl)Cl YONPGGFAJWQGJC-UHFFFAOYSA-K 0.000 description 2
- 230000007704 transition Effects 0.000 description 2
- ZCYVEMRRCGMTRW-UHFFFAOYSA-N 7553-56-2 Chemical compound [I] ZCYVEMRRCGMTRW-UHFFFAOYSA-N 0.000 description 1
- 241000186361 Actinobacteria <class> Species 0.000 description 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 1
- 241000894006 Bacteria Species 0.000 description 1
- 241001674044 Blattodea Species 0.000 description 1
- WKBOTKDWSSQWDR-UHFFFAOYSA-N Bromine atom Chemical compound [Br] WKBOTKDWSSQWDR-UHFFFAOYSA-N 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- 241000233866 Fungi Species 0.000 description 1
- 229920000877 Melamine resin Polymers 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 239000002033 PVDF binder Substances 0.000 description 1
- 239000004642 Polyimide Substances 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 229920006266 Vinyl film Polymers 0.000 description 1
- 238000000862 absorption spectrum Methods 0.000 description 1
- 230000001133 acceleration Effects 0.000 description 1
- 238000004378 air conditioning Methods 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 150000001299 aldehydes Chemical class 0.000 description 1
- 125000001931 aliphatic group Chemical group 0.000 description 1
- 125000003545 alkoxy group Chemical group 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 230000000843 anti-fungal effect Effects 0.000 description 1
- 230000002924 anti-infective effect Effects 0.000 description 1
- 239000012736 aqueous medium Substances 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000004061 bleaching Methods 0.000 description 1
- 239000007844 bleaching agent Substances 0.000 description 1
- GDTBXPJZTBHREO-UHFFFAOYSA-N bromine Substances BrBr GDTBXPJZTBHREO-UHFFFAOYSA-N 0.000 description 1
- 229910052794 bromium Inorganic materials 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- 150000001735 carboxylic acids Chemical class 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000004440 column chromatography Methods 0.000 description 1
- 238000005056 compaction Methods 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 239000004035 construction material Substances 0.000 description 1
- 238000010411 cooking Methods 0.000 description 1
- 238000012937 correction Methods 0.000 description 1
- 239000002537 cosmetic Substances 0.000 description 1
- 239000006059 cover glass Substances 0.000 description 1
- 238000009295 crossflow filtration Methods 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
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- 238000009792 diffusion process Methods 0.000 description 1
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- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- 201000010099 disease Diseases 0.000 description 1
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- 239000002270 dispersing agent Substances 0.000 description 1
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- 238000001035 drying Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 230000005281 excited state Effects 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 238000000445 field-emission scanning electron microscopy Methods 0.000 description 1
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- 238000009920 food preservation Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000003673 groundwater Substances 0.000 description 1
- 150000004820 halides Chemical class 0.000 description 1
- 229910052736 halogen Inorganic materials 0.000 description 1
- 125000001183 hydrocarbyl group Chemical group 0.000 description 1
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 1
- 239000007943 implant Substances 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000012212 insulator Substances 0.000 description 1
- 238000011835 investigation Methods 0.000 description 1
- 229910052740 iodine Inorganic materials 0.000 description 1
- 239000011630 iodine Substances 0.000 description 1
- 229910000358 iron sulfate Inorganic materials 0.000 description 1
- BAUYGSIQEAFULO-UHFFFAOYSA-L iron(2+) sulfate (anhydrous) Chemical compound [Fe+2].[O-]S([O-])(=O)=O BAUYGSIQEAFULO-UHFFFAOYSA-L 0.000 description 1
- 230000001678 irradiating effect Effects 0.000 description 1
- 125000001449 isopropyl group Chemical group [H]C([H])([H])C([H])(*)C([H])([H])[H] 0.000 description 1
- 239000010806 kitchen waste Substances 0.000 description 1
- 239000002649 leather substitute Substances 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- JDSHMPZPIAZGSV-UHFFFAOYSA-N melamine Chemical compound NC1=NC(N)=NC(N)=N1 JDSHMPZPIAZGSV-UHFFFAOYSA-N 0.000 description 1
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 1
- 238000001471 micro-filtration Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- 125000004108 n-butyl group Chemical group [H]C([H])([H])C([H])([H])C([H])([H])C([H])([H])* 0.000 description 1
- QGLKJKCYBOYXKC-UHFFFAOYSA-N nonaoxidotritungsten Chemical compound O=[W]1(=O)O[W](=O)(=O)O[W](=O)(=O)O1 QGLKJKCYBOYXKC-UHFFFAOYSA-N 0.000 description 1
- 239000004745 nonwoven fabric Substances 0.000 description 1
- NJPPVKZQTLUDBO-UHFFFAOYSA-N novaluron Chemical compound C1=C(Cl)C(OC(F)(F)C(OC(F)(F)F)F)=CC=C1NC(=O)NC(=O)C1=C(F)C=CC=C1F NJPPVKZQTLUDBO-UHFFFAOYSA-N 0.000 description 1
- 239000013307 optical fiber Substances 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000005022 packaging material Substances 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 239000000546 pharmaceutical excipient Substances 0.000 description 1
- 239000002985 plastic film Substances 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 150000003058 platinum compounds Chemical class 0.000 description 1
- 239000011120 plywood Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 229920001721 polyimide Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 229920000915 polyvinyl chloride Polymers 0.000 description 1
- 239000004800 polyvinyl chloride Substances 0.000 description 1
- 229920002981 polyvinylidene fluoride Polymers 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 125000001436 propyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])[H] 0.000 description 1
- 239000008213 purified water Substances 0.000 description 1
- 230000006798 recombination Effects 0.000 description 1
- 238000005215 recombination Methods 0.000 description 1
- 238000001953 recrystallisation Methods 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 230000027756 respiratory electron transport chain Effects 0.000 description 1
- 238000001223 reverse osmosis Methods 0.000 description 1
- 238000005464 sample preparation method Methods 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 210000004761 scalp Anatomy 0.000 description 1
- 239000002453 shampoo Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 230000009182 swimming Effects 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- MTAYDNKNMILFOK-UHFFFAOYSA-K titanium(3+);tribromide Chemical compound Br[Ti](Br)Br MTAYDNKNMILFOK-UHFFFAOYSA-K 0.000 description 1
- 229910001428 transition metal ion Inorganic materials 0.000 description 1
- 229910000314 transition metal oxide Inorganic materials 0.000 description 1
- 229910001930 tungsten oxide Inorganic materials 0.000 description 1
- 238000003828 vacuum filtration Methods 0.000 description 1
- 238000007740 vapor deposition Methods 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/30—Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation 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
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/86—Catalytic processes
- B01D53/88—Handling or mounting catalysts
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/06—Silicon, titanium, zirconium or hafnium; Oxides or hydroxides thereof
- B01J21/063—Titanium; Oxides or hydroxides thereof
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/30—Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
- B01J35/39—Photocatalytic properties
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/30—Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
- B01J35/391—Physical properties of the active metal ingredient
- B01J35/393—Metal or metal oxide crystallite size
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/61—Surface area
- B01J35/613—10-100 m2/g
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B82—NANOTECHNOLOGY
- B82Y—SPECIFIC USES OR APPLICATIONS OF NANOSTRUCTURES; MEASUREMENT OR ANALYSIS OF NANOSTRUCTURES; MANUFACTURE OR TREATMENT OF NANOSTRUCTURES
- B82Y30/00—Nanotechnology for materials or surface science, e.g. nanocomposites
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01G—COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
- C01G23/00—Compounds of titanium
- C01G23/04—Oxides; Hydroxides
- C01G23/047—Titanium dioxide
- C01G23/053—Producing by wet processes, e.g. hydrolysing titanium salts
- C01G23/0536—Producing by wet processes, e.g. hydrolysing titanium salts by hydrolysing chloride-containing salts
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09C—TREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
- C09C1/00—Treatment of specific inorganic materials other than fibrous fillers; Preparation of carbon black
- C09C1/36—Compounds of titanium
- C09C1/3607—Titanium dioxide
- C09C1/3653—Treatment with inorganic compounds
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2255/00—Catalysts
- B01D2255/20—Metals or compounds thereof
- B01D2255/207—Transition metals
- B01D2255/20707—Titanium
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2255/00—Catalysts
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- B01D2255/802—Photocatalytic
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Abstract
Description
本發明係關於一種在氧化鈦載持過渡金屬化合物而得到的載有過渡金屬化合物之氧化鈦。前述載有過渡金屬化合物之氧化鈦,其對於可見光之回應性優異,並可發揮優異的光觸媒活性。 The present invention relates to a transition metal compound-loaded titanium oxide obtained by supporting a transition metal compound on titanium oxide. The above-described titanium oxide carrying a transition metal compound is excellent in response to visible light and exhibits excellent photocatalytic activity.
載有過渡金屬化合物之氧化鈦具有光觸媒活性,藉由照射可見光或紫外線等之光而發揮強的氧化力,可將有害化學物質分解至水或二氧化碳為止,且藉由塗布或混合載有過渡金屬化合物之氧化鈦的懸浮液,可對被塗布體或被混合物賦予抗菌、防黴、除臭、空氣淨化、水質淨化、及防污效果等。並且,已知在載有過渡金屬化合物之氧化鈦含有鹵素離子等之離子性雜質時,其對於紫外線及可見光的回應性會下降。 The titanium oxide carrying the transition metal compound has photocatalytic activity, and exhibits strong oxidizing power by irradiating light such as visible light or ultraviolet light, and can decompose harmful chemicals into water or carbon dioxide, and carry a transition metal by coating or mixing. The suspension of the titanium oxide of the compound imparts antibacterial, anti-mildew, deodorization, air purification, water purification, and antifouling effects to the object to be coated or the mixture to be coated. Further, it is known that when the titanium oxide carrying the transition metal compound contains an ionic impurity such as a halogen ion, the responsiveness to ultraviolet light and visible light is lowered.
載有過渡金屬化合物之氧化鈦,已知可經由下述步驟進行製造(參照專利文獻1、2等)。 The titanium oxide carrying the transition metal compound is known to be produced by the following procedure (see Patent Documents 1, 2, etc.).
1.將鈦化合物進行水熱處理(hydrothermal treatment)而得到氧化鈦懸浮液的氧化鈦製造步驟。 1. A titanium oxide production step in which a titanium compound is hydrothermally treated to obtain a titanium oxide suspension.
2.藉由在氧化鈦懸浮液添加過渡金屬化合物而得到載有過渡金屬化合物之氧化鈦懸浮液的載持過渡金屬化合物之步驟。 2. A step of supporting a transition metal compound carrying a transition metal compound-loaded titanium oxide suspension by adding a transition metal compound to a titanium oxide suspension.
3.藉由將載有過渡金屬化合物之氧化鈦懸浮液施加使用全量過濾方式之加壓或減壓過濾、或離心分離等之處理予以固液分離而減低離子性雜質之含量的精製步驟。 3. A purification step of reducing the content of ionic impurities by applying a suspension of a transition metal compound-containing titanium oxide to a titanium oxide suspension using a full filtration method, a vacuum filtration method, or a centrifugal separation treatment.
但是,前述方法中,在精製步驟中因為固液分離而使載有過渡金屬化合物之氧化鈦壓密化而高活性面之露出量下降,因此有得不到具有足夠之光觸媒活性的載有過渡金屬化合物之氧化鈦的問題。再者,一旦被壓密化的載有過渡金屬化合物之氧化鈦,即使之後施以粉碎處理等進行再分散,也還是得不到可滿足的光觸媒活性。 However, in the above-mentioned method, in the purification step, the transition metal compound-loaded titanium oxide is densified by solid-liquid separation, and the exposure amount of the high active surface is lowered, so that a transition having sufficient photocatalytic activity is not obtained. The problem of titanium oxide of metal compounds. Further, once the tungsten oxide carrying the transition metal compound, which has been densified, is redispersed after being subjected to a pulverization treatment or the like, satisfactory photocatalytic activity is not obtained.
[專利文獻1]日本特開平10-158015號公報 [Patent Document 1] Japanese Patent Laid-Open No. Hei 10-158015
[專利文獻2]日本特開昭62-235215號公報 [Patent Document 2] Japanese Laid-Open Patent Publication No. 62-235215
因此,本發明的目的在於提供一種對於可見光之回應性優異,且發揮優異之光觸媒活性的載有過渡金屬化合物之氧化鈦。 Accordingly, an object of the present invention is to provide a transition metal compound-containing titanium oxide which is excellent in response to visible light and exhibits excellent photocatalytic activity.
本案發明人為了解決前述問題而仔細探討的結果發現:棒狀的載有過渡金屬化合物之氧化鈦,藉由施加離心分離等之固液分離處理而一旦壓密化的話,之後即使藉由粉碎再分散化,棒狀之結晶結構也會被切斷 ,且因為下述1、2等之理由,可見光區域之光觸媒活性顯著下降。 As a result of intensive investigation to solve the above problems, the inventors of the present invention have found that a rod-shaped titanium oxide carrying a transition metal compound is subjected to solid-liquid separation treatment by centrifugal separation or the like, and once pulverized, even after pulverization Decentralized, rod-shaped crystal structure will also be cut off And because of the following 1, 2, etc., the photocatalytic activity in the visible light region is remarkably lowered.
1.載有過渡金屬化合物之氧化鈦的平均長寬比變小,成為更接近球狀的形狀,因此氧化反應場(field)與還原反應場的分離性下降,變得無法避免逆反應或副反應之進行。 1. The average aspect ratio of the titanium oxide carrying the transition metal compound becomes smaller and becomes closer to a spherical shape, so that the separation between the oxidation reaction field and the reduction reaction field is lowered, and the reverse reaction or side reaction cannot be avoided. Go on.
2.因為切斷棒狀之結晶結構而產生沒有載持過渡金屬化合物的氧化鈦片,該氧化鈦片變得無法發揮可見光回應性。 2. The titanium oxide sheet which does not carry a transition metal compound is produced by cutting a rod-like crystal structure, and the titanium oxide sheet becomes unable to exhibit visible light responsiveness.
並且發現:在精製步驟中,採用利用掃流過濾(cross flow filtration)方式之膜過濾處理代替離心分離等之固液分離處理的話,可不將載有過渡金屬化合物之氧化鈦壓密化,並於維持棒狀之結晶結構的狀態有效率地除去離子性雜質,得到離子性雜質之含量極低,而且為棒狀之載有過渡金屬化合物之氧化鈦。再者發現:在水熱處理時將反應系內攪拌的話,可得到平均短徑極小,且平均長寬比大的載有過渡金屬化合物之氧化鈦。並且發現:如前述進行而得到的載有過渡金屬化合物之氧化鈦,對於可見光的回應性優異,且可發揮優異的光觸媒活性。本發明係根據該等見解而完成者。 Further, it has been found that, in the purification step, if the membrane filtration treatment by the cross flow filtration method is used instead of the solid-liquid separation treatment such as centrifugation, the titanium oxide carrying the transition metal compound may not be compacted. The state in which the rod-like crystal structure is maintained is effective in removing ionic impurities, and the content of the ionic impurities is extremely low, and the rod-shaped titanium oxide carrying the transition metal compound is obtained. Further, it has been found that when the reaction system is stirred during hydrothermal treatment, a transition metal compound-containing titanium oxide having an average short diameter and a small average aspect ratio can be obtained. Further, it has been found that the transition metal compound-containing titanium oxide obtained as described above is excellent in responsiveness to visible light and exhibits excellent photocatalytic activity. The present invention has been completed in light of these findings.
亦即,本發明提供一種載有過渡金屬化合物之氧化鈦,其係在結晶性氧化鈦載持過渡金屬化合物的載有過渡金屬化合物之氧化鈦,其平均短徑為50nm以下,平均長寬比(長徑/短徑)為1.5以上。 That is, the present invention provides a transition metal compound-containing titanium oxide which is a transition metal compound-supporting titanium oxide carrying a transition metal compound in a crystalline titanium oxide, and has an average minor axis of 50 nm or less and an average aspect ratio. (long diameter / short diameter) is 1.5 or more.
作為前述結晶性氧化鈦,具有結晶面(110)及 結晶面(111)的金紅石型氧化鈦及/或具有結晶面(110)、結晶面(111)及結晶面(001)的金紅石型氧化鈦較為理想。 The crystalline titanium oxide has a crystal face (110) and The rutile-type titanium oxide of the crystal face (111) and/or the rutile-type titanium oxide having a crystal face (110), a crystal face (111), and a crystal face (001) are preferred.
比表面積為10m2/g以上較佳。 The specific surface area is preferably 10 m 2 /g or more.
本發明提供一種氧化鈦,其平均短徑為50nm以下,平均長寬比(長徑/短徑)為1.5以上。 The present invention provides a titanium oxide having an average minor axis of 50 nm or less and an average aspect ratio (long diameter/short diameter) of 1.5 or more.
本發明的載有過渡金屬化合物之氧化鈦,其平均短徑為50nm以下,而且平均長寬比(長徑/短徑)為1.5以上。因此,對可見光之回應性優異,且可吸收太陽光或白熾燈、螢光燈、LED等之通常的生活空間之光,並將有害化學物質分解至水或二氧化碳為止。亦即,本發明的載有過渡金屬化合物之氧化鈦懸浮液,可作為LED照明下用之光觸媒適當地使用。並且,可應用於各種抗菌防黴、除臭、空氣淨化、水淨化等,且可廣範圍應用於以室內的壁紙或家具為首之家庭內或病院、學校等之公共施設內的環境淨化、家電製品之高機能化等。 The transition metal compound-containing titanium oxide of the present invention has an average minor axis of 50 nm or less and an average aspect ratio (long diameter/short diameter) of 1.5 or more. Therefore, it is excellent in responsiveness to visible light, and absorbs light from ordinary living spaces such as sunlight or incandescent lamps, fluorescent lamps, and LEDs, and decomposes harmful chemicals into water or carbon dioxide. That is, the transition metal compound-containing titanium oxide suspension of the present invention can be suitably used as a photocatalyst for LED illumination. In addition, it can be applied to various antibacterial and anti-mildew, deodorization, air purification, water purification, etc., and can be widely applied to environmental purification and home appliances in public facilities such as indoor wallpapers or furniture, hospitals, schools, etc. The high functionality of the products.
001‧‧‧結晶面 001‧‧‧ Crystallized surface
110‧‧‧結晶面 110‧‧‧ Crystallized surface
111‧‧‧結晶面 111‧‧‧ Crystallized surface
第1圖為顯示利用掃流方式的膜過濾之一例的概略圖。 Fig. 1 is a schematic view showing an example of membrane filtration by a sweeping method.
第2圖為顯示利用掃流方式的膜過濾之逆清洗的一例之概略圖。 Fig. 2 is a schematic view showing an example of reverse cleaning by membrane filtration by a sweeping method.
第3圖為具有結晶面(110)(111)的棒狀金紅石型氧化鈦、及具有結晶面(110)(111)(001)的棒狀金紅石型氧化鈦之斜視圖。 Fig. 3 is a perspective view of a rod-shaped rutile-type titanium oxide having a crystal face (110) (111) and a rod-shaped rutile-type titanium oxide having a crystal face (110) (111) (001).
第4圖係使用電場發射型掃描電子顯微鏡進行攝影之實施例2所得的載有鐵化合物之氧化鈦的照片(×200000,比例尺:100nm)。 Fig. 4 is a photograph (×200000, scale: 100 nm) of the iron compound-loaded titanium oxide obtained in Example 2, which was imaged by an electric field emission type scanning electron microscope.
[載有過渡金屬化合物之氧化鈦] [Titanium oxide carrying a transition metal compound]
本發明的載有過渡金屬化合物之氧化鈦,其特徵為在結晶性氧化鈦載持過渡金屬化合物,且平均短徑為50nm以下,平均長寬比(長徑/短徑)為1.5以上。 The transition metal compound-containing titanium oxide of the present invention is characterized in that the transition metal compound is supported on the crystalline titanium oxide, and the average short diameter is 50 nm or less, and the average aspect ratio (long diameter/short diameter) is 1.5 or more.
載有過渡金屬化合物之氧化鈦的平均短徑為50nm以下,較佳為5~40nm,特佳為5~30nm,最佳為10~25nm。當平均短徑大於前述範圍時,氧化反應場與還原反應場之分離性會下降,變得無法避免逆反應或副反應之進行,且光觸媒活性下降,因此較不理想。 The titanium oxide carrying the transition metal compound has an average minor axis of 50 nm or less, preferably 5 to 40 nm, particularly preferably 5 to 30 nm, and most preferably 10 to 25 nm. When the average short diameter is larger than the above range, the separation between the oxidation reaction field and the reduction reaction field is lowered, and the reverse reaction or the side reaction is unavoidable, and the photocatalytic activity is lowered, which is not preferable.
又,載有過渡金屬化合物之氧化鈦的平均長寬比(長徑/短徑)為1.5以上,較佳為1.5~100,更佳為1.5~50,特佳為1.5~20,最佳為2~15。平均長寬比小於前述範圍的話,氧化反應場與還原反應場之分離性會下降,變得無法避免逆反應或副反應之進行,光觸媒活性下降,因此較不理想。 Further, the average aspect ratio (long diameter/short diameter) of the titanium oxide carrying the transition metal compound is 1.5 or more, preferably 1.5 to 100, more preferably 1.5 to 50, and particularly preferably 1.5 to 20, most preferably 2~15. When the average aspect ratio is less than the above range, the separation between the oxidation reaction field and the reduction reaction field is lowered, and the reverse reaction or the side reaction is unavoidable, and the photocatalytic activity is lowered, which is not preferable.
再者,本發明中平均短徑、及平均長寬比,係對於下述製備方法所得到的樣本,以下述測定方法求得的值。 Further, in the present invention, the average short diameter and the average aspect ratio are values obtained by the following measurement methods for the samples obtained by the following production methods.
<樣本製備方法> <Sample preparation method>
1.將少量(挖耳勺尺寸之刮勺的一半左右)的載有過 渡金屬化合物之氧化鈦加入9mL的玻璃製樣本瓶,並加入7mL乙醇,以超音波清洗器施加超音波5分鐘使分散至乙醇中而得到乙醇分散液。 1. Put a small amount (about half of the size of the spoon) The titanium oxide of the metal compound was added to a 9 mL glass sample vial, and 7 mL of ethanol was added thereto, and ultrasonic waves were applied for 5 minutes in an ultrasonic cleaner to disperse into ethanol to obtain an ethanol dispersion.
2.將得到的乙醇分散液以玻璃製滴管吸取1滴,使其落於SEM用之試料台上且自然乾燥後,進行30秒鐘鉑蒸鍍。 2. The obtained ethanol dispersion liquid was taken up by a glass pipette, dropped on a sample stage for SEM, and naturally dried, and then subjected to platinum vapor deposition for 30 seconds.
<測定方法> <Measurement method>
使用電場發射型掃描電子顯微鏡(商品名「FE-SEM JSM-6700F」,日本電子(股)製,加速電壓:15kV,WD:約3mm,倍率:20萬倍),隨機觀察結晶粒子,抽取代表的3處,在抽取的SEM照片整體之中,抽取外觀極端大或不小,且以平均大小之粒子為中心,輪廓分明的粒子30個,印至OHP薄片,對於該等之粒子,使用圖像解析軟體(商品名「WinROOF Version5.6」,三谷商事(股)製)求出各短徑(對最大長徑正交的寬),並將該等之值平均作為平均短徑。又,以同樣的方法求出平均長徑(最大長徑),將該等之比(平均長徑/平均短徑)作為平均長寬比。 An electric field emission type scanning electron microscope (trade name "FE-SEM JSM-6700F", manufactured by Nippon Denshi Co., Ltd., acceleration voltage: 15 kV, WD: about 3 mm, magnification: 200,000 times), random observation of crystal particles, extraction of representative In the three SEM photographs taken, the appearance of the extracted SEM photograph is extremely large or small, and 30 particles with well-defined particles centered on the average size of the particles are printed on the OHP sheet. For the particles, use the map. The analysis software (product name "WinROOF Version 5.6", manufactured by Mitani Corporation) is used to obtain each of the short diameters (widths orthogonal to the maximum long diameter), and the values are averaged as the average short diameter. Further, the average long diameter (maximum long diameter) was obtained in the same manner, and the ratio (average long diameter/average short diameter) was defined as an average aspect ratio.
作為前述結晶性氧化鈦,例如,可舉出金紅石型、銳鈦礦型、板鈦礦型氧化鈦等。本發明中,其中從露出穩定的結晶面之觀點,較理想為金紅石型或銳鈦礦型氧化鈦(從可發揮更優異的光觸媒活性之觀點,金紅石型氧化鈦更佳,特佳為具有結晶面(110)及結晶面(111)的金紅石型氧化鈦及/或具有結晶面(110)、結晶面(111)及結晶面(001)的金紅石型氧化鈦)。 Examples of the crystalline titanium oxide include a rutile type, an anatase type, and a brookite type titanium oxide. In the present invention, from the viewpoint of exposing a stable crystal surface, rutile-type or anatase-type titanium oxide is preferable (from the viewpoint of exhibiting more excellent photocatalytic activity, rutile-type titanium oxide is more preferable, particularly preferably A rutile-type titanium oxide having a crystal face (110) and a crystal face (111) and/or a rutile-type titanium oxide having a crystal face (110), a crystal face (111), and a crystal face (001).
過渡金屬化合物,例如,係以過渡金屬離子 、過渡金屬單體、過渡金屬鹽、過渡金屬氧化物、過渡金屬氫氧化物、或過渡金屬錯合物的狀態載持。作為過渡金屬化合物的載持量,例如為50ppm以上,較佳為100ppm以上,更佳為200ppm以上,特佳為300ppm以上,最佳為500ppm以上。過渡金屬化合物的載持量之上限,例如為5000ppm左右,較佳為3000ppm,特佳為2000ppm。過渡金屬化合物的載持量低於前述範圍的話,可見光回應性有下降的傾向。另一方面,過渡金屬化合物的載持量高於前述範圍的話,注入電子之反向電子轉移等造成激發電子未有效地作用,有光觸媒活性下降的傾向。 Transition metal compound, for example, a transition metal ion State loading of transition metal monomers, transition metal salts, transition metal oxides, transition metal hydroxides, or transition metal complexes. The amount of the transition metal compound supported is, for example, 50 ppm or more, preferably 100 ppm or more, more preferably 200 ppm or more, particularly preferably 300 ppm or more, and most preferably 500 ppm or more. The upper limit of the amount of the transition metal compound supported is, for example, about 5,000 ppm, preferably 3,000 ppm, and particularly preferably 2,000 ppm. When the amount of the transition metal compound supported is less than the above range, the visible light responsiveness tends to decrease. On the other hand, when the amount of the transition metal compound supported is higher than the above range, the reverse electron transfer of the injected electrons or the like causes the excited electrons to not function effectively, and the photocatalytic activity tends to decrease.
前述過渡金屬化合物,在結晶性氧化鈦之表面以面選擇性地載持,從可進一步提高氧化反應與還原反應的反應場之分離性,且藉由前述可抑制激發電子與電洞的再結合,並抑制逆反應之進行,且可飛躍地提升光觸媒活性之觀點較為理想,特別是在氧化反應面選擇性地載持過渡金屬化合物較為理想。 The transition metal compound is selectively supported on the surface of the crystalline titanium oxide, and the separation property of the reaction field between the oxidation reaction and the reduction reaction can be further improved, and the recombination of the excited electrons and the hole can be suppressed by the foregoing. It is preferable to suppress the progress of the reverse reaction and to greatly enhance the activity of the photocatalyst, and it is preferable to selectively carry the transition metal compound on the oxidation reaction surface.
再者,本發明中過渡金屬化合物以「面選擇性地」載持,係指在結晶性氧化鈦之2面以上的結晶面之中,不是全部的面,而是特定的面(例如,特定的1面或2面等)載持超過過渡金屬化合物之50%的量(較佳為70%以上,特佳為80%以上)。再者,面選擇率的上限為100%。面選擇性,可藉由使用穿透式電子顯微鏡(TEM)或能量分散型螢光X線分析裝置(EDX),確認源自各結晶面上的過渡金屬化合物之信號而判定。 In the present invention, the transition metal compound is carried in a "surface selective" manner, and refers to a specific surface (for example, a specific surface) of the crystal faces of the crystallized titanium oxide having two or more surfaces. One side or two sides, etc.) are carried in an amount exceeding 50% of the transition metal compound (preferably 70% or more, particularly preferably 80% or more). Furthermore, the upper limit of the face selection rate is 100%. The surface selectivity can be determined by confirming the signal derived from the transition metal compound on each crystal face by using a transmission electron microscope (TEM) or an energy dispersive fluorescent X-ray analyzer (EDX).
作為過渡金屬化合物,只要是在可見光區域 具有吸收光譜,且在激發狀態可注入電子至傳導帶者即可,但本發明中,週期表第3~第11族元素化合物較為理想,其中週期表第8~第11族元素化合物尤佳,特佳為鐵化合物或鉑化合物,最佳為三價的鐵化合物(Fe3+)。因為三價的鐵化合物(Fe3+)容易吸附於氧化鈦,且二價的鐵化合物(Fe2+)具有不易於吸附的特性,因此藉由利用該特性而可更容易地以面選擇性地載持。 The transition metal compound may have an absorption spectrum in the visible light region and may inject electrons into the conduction band in the excited state. However, in the present invention, the third to eleventh element compounds of the periodic table are preferred, and the periodic table is The element of the 8th to 11th element is particularly preferred, and particularly preferably an iron compound or a platinum compound, and most preferably a trivalent iron compound (Fe 3+ ). Since the trivalent iron compound (Fe 3+ ) is easily adsorbed to titanium oxide, and the divalent iron compound (Fe 2+ ) has a property of being not easily adsorbed, it is easier to use surface selectivity by utilizing this property. Ground carrying.
前述載有過渡金屬化合物之氧化鈦的比表面積,例如為10m2/g以上。比表面積的下限,較佳為30m2/g,更佳為50m2/g,特佳為60m2/g,最佳為70m2/g。比表面積的上限,例如為200m2/g,較佳為150m2/g,特佳為100m2/g。 The specific surface area of the titanium oxide carrying the transition metal compound is, for example, 10 m 2 /g or more. The lower limit of the specific surface area is preferably 30 m 2 /g, more preferably 50 m 2 /g, particularly preferably 60 m 2 /g, and most preferably 70 m 2 /g. The upper limit of the specific surface area, for example, 200m 2 / g, preferably from 150m 2 / g, particularly preferably 100m 2 / g.
前述載有過渡金屬化合物之氧化鈦的比表面積,例如為10~200m2/g,較佳為10~150m2/g,更佳為30~150m2/g,特佳為50~100m2/g,更佳為60~100m2/g,最佳為70~100m2/g。比表面積為前述範圍的載有過渡金屬化合物之氧化鈦,因為高活性面的露出量變多,所以可發揮優異的光觸媒活性。 The specific surface area of the titanium oxide contains a transition metal compound of, for example, 10 ~ 200m 2 / g, preferably 10 ~ 150m 2 / g, more preferably 30 ~ 150m 2 / g, particularly preferably 50 ~ 100m 2 / g, more preferably 60 to 100 m 2 /g, most preferably 70 to 100 m 2 /g. The titanium oxide carrying the transition metal compound having a specific surface area in the above range exhibits an excellent photocatalytic activity because the amount of exposure of the high active surface is increased.
前述比表面積,係對於將載有過渡金屬化合物之氧化鈦於100℃(真空下)脫氣60分鐘而得到的樣本,使用高速比表面積‧細孔徑分布測定裝置(商品名「NOVA-1200」,Quantachtome.Co製),在下述條件下更換樣本進行2次測定而得到的值之平均。 The specific surface area is a sample obtained by degassing a transition metal compound-containing titanium oxide at 100 ° C (under vacuum) for 60 minutes, using a high-speed specific surface area ‧ pore size distribution measuring apparatus (trade name "NOVA-1200", Quantachtome Co., Ltd., the average of the values obtained by changing the sample twice under the following conditions.
<比表面積測定條件> <Specific surface area measurement conditions>
測定原理:定容法(空白補正型) Measuring principle: constant volume method (blank correction type)
檢測法:相對壓力(利用壓力轉換器之樣本盒內的吸附平衡壓力(P)與飽和蒸氣壓(P0)之比)與吸附氣體量(藉由利用壓力轉換器之壓力檢測與利用熱敏電阻之歧管溫度檢測計算理想氣體的注入氣體量) Detection method: relative pressure (using the ratio of the adsorption equilibrium pressure (P) to the saturated vapor pressure (P 0 ) in the sample box of the pressure transducer) and the amount of adsorbed gas (by using the pressure transducer to detect and utilize the heat Manifold temperature detection of resistance calculates the amount of injected gas for an ideal gas)
吸附氣體:氮氣體 Adsorbed gas: nitrogen gas
盒尺寸:小丸粒盒(盒容量:1.8cm3,主幹外徑:9mm) Box size: small pellet box (box capacity: 1.8cm 3 , trunk outer diameter: 9mm)
測定項目:P/P0=0.1、0.2、0.3的吸附側3點 Measurement item: 3 points on the adsorption side of P/P 0 = 0.1, 0.2, 0.3
解析項目:利用BET多點法的比表面積 Analytical project: specific surface area using the BET multipoint method
本發明的載有過渡金屬化合物之氧化鈦,因為其可見光回應性佳,且藉由光照射可發揮優異的光觸媒活性,將有害化學物質分解至水或二氧化碳為止,所以可發揮抗菌、防黴、除臭、空氣淨化、水質淨化、防污等各種效果。 The transition metal compound-containing titanium oxide of the present invention exhibits excellent visible light responsiveness, and exhibits excellent photocatalytic activity by light irradiation, and decomposes harmful chemicals into water or carbon dioxide, thereby exhibiting antibacterial and antifungal properties. Deodorization, air purification, water purification, anti-fouling and other effects.
例如,使用前述載有過渡金屬化合物之氧化鈦(200mg),將甲苯氧化之際生成的CO2量,例如為300ppm以上。又,在將甲醇氧化之際生成的CO2量,例如為500ppm以上,較佳為600ppm以上,更佳為700ppm以上,特佳為750ppm以上。 For example, the amount of CO 2 produced when the toluene is oxidized by using the above-described transition metal compound-containing titanium oxide (200 mg) is, for example, 300 ppm or more. Moreover, the amount of CO 2 produced when the methanol is oxidized is, for example, 500 ppm or more, preferably 600 ppm or more, more preferably 700 ppm or more, and particularly preferably 750 ppm or more.
再者,前述在將甲苯氧化之際生成的CO2量之測定方法,係如下述。 Further, the method for measuring the amount of CO 2 produced when the toluene is oxidized is as follows.
使載有過渡金屬化合物之氧化鈦200mg廣布於玻璃製皿,並置入至反應容器(Tedlar bag,材質:氟化乙烯樹脂)之中,將100ppm的甲苯氣體125mL吹送至反應容器內。甲苯氣體之對於載有過渡金屬化合物之氧化鈦的吸附達到平衡後,在室溫(25℃)進行光照射(LED,光強度 :2.5W/cm2,光之波長:455nm),測定由光照射開始24小時後的CO2之生成量。 200 mg of titanium oxide carrying a transition metal compound was spread on a glass dish, placed in a reaction container (Tedlar bag, material: fluorinated ethylene resin), and 125 ppm of toluene gas (100 ppm) was blown into the reaction container. After the adsorption of the toluene gas to the titanium oxide carrying the transition metal compound was balanced, light irradiation (LED, light intensity: 2.5 W/cm 2 , wavelength of light: 455 nm) was carried out at room temperature (25 ° C), and the light was measured. The amount of CO 2 produced after 24 hours from the start of irradiation.
又,前述在將甲醇氧化之際生成的CO2量之測定方法,係如下述。 Further, the method for measuring the amount of CO 2 produced when the methanol is oxidized is as follows.
使載有過渡金屬化合物之氧化鈦200mg廣布於玻璃製皿,並置入至反應容器(Tedlar bag,材質:氟化乙烯樹脂)之中,將800ppm的甲醇氣體125mL吹送至反應容器內。甲醇氣體之對於載有過渡金屬化合物之氧化鈦的吸附達到平衡後,在室溫(25℃)進行光照射(LED,光強度:2.5W/m2,光之波長:455nm),測定由光照射開始24小時後的CO2之生成量。 200 mg of titanium oxide carrying a transition metal compound was spread on a glass dish, placed in a reaction container (Tedlar bag, material: fluorinated ethylene resin), and 125 ppm of methanol gas (125 mL) was blown into the reaction container. After the adsorption of the methanol gas to the titanium oxide carrying the transition metal compound is balanced, light irradiation (LED, light intensity: 2.5 W/m 2 , wavelength of light: 455 nm) is performed at room temperature (25 ° C), and the light is measured. The amount of CO 2 produced after 24 hours from the start of irradiation.
本發明的載有過渡金屬化合物之氧化鈦,如前述,可發揮極優異的光回應性,亦即具有對於由紫外線區域至可見光區域為止之廣泛的波長範圍之光的回應性,因此藉由吸收太陽光或白熾燈、螢光燈、LED等之通常的生活空間之光,發揮高觸媒活性,將有害化學物質分解至水或二氧化碳為止,可發揮抗菌(細菌、放線菌、菌類、藻類等之殺菌‧殺藻)、防黴、除臭(例如,氨、胺類、甲基硫醇、硫化氫等之含硫物質、乙酸、醛類、乙烯等之惡臭氣體之除臭)、空氣淨化、水質淨化、防污等各種效果。又,本發明的載有過渡金屬化合物之氧化鈦,視需要可藉由以混合有黏結劑、溶劑、分散劑、增黏劑、界面活性劑等之狀態進行塗布或混合,可對被塗布體或被混合物賦予前述效果。 The transition metal compound-containing titanium oxide of the present invention exhibits excellent light responsiveness as described above, that is, has responsiveness to light in a wide wavelength range from the ultraviolet region to the visible region, and thus absorbs The light of normal living space such as sunlight, incandescent lamps, fluorescent lamps, and LEDs exhibits high catalytic activity and decomposes harmful chemicals into water or carbon dioxide, and can exhibit antibacterial properties (bacteria, actinomycetes, fungi, algae, etc.) Sterilization, algae killing, mildew proofing, deodorization (for example, deodorization of sulfur-containing substances such as ammonia, amines, methyl mercaptan, hydrogen sulfide, etc., malodorous gases such as acetic acid, aldehydes, and ethylene), air purification , water purification, anti-fouling and other effects. Further, the transition metal compound-containing titanium oxide of the present invention can be applied or mixed by a state in which a binder, a solvent, a dispersant, a tackifier, a surfactant, or the like is mixed, if necessary, to coat the object to be coated. Or the mixture gives the aforementioned effects.
作為本發明的載有過渡金屬化合物之氧化鈦 的被塗布體、及被混合物,例如,可舉出建材、建物外部裝潢、建物內部裝潢、建築用塗料、牆壁、壁紙、地板、窗框、窗玻璃、結晶化玻璃、玻璃、紗窗、雨水排水槽、日照熱反射薄片、信箱、結構構件、舖裝材料、顯示板、交通號誌、道路交通標識反射板、平板顯示器、顯示器濾光片、路面顯示材、道路用裝飾板、圍籬、門、隧道用‧道路用照明裝置、隔音牆、護柵、隧道內裝、道路用鏡、塑膠布溫室頂棚內面、橋梁、橋梁之安全柵、汽車‧列車‧船之內外裝及塗裝、車輛用車輪、鐵路車輛的車體構造、車輛用零件、機械裝置或物品之外裝‧防塵罩‧塗裝、各種顯示裝置、廣告塔、絕緣體、太陽能板、太陽能電池罩、太陽能熱水器集熱罩、燃料電池、光纖、車輛用照明燈罩、漁網、繩、軟管、船底構件、防藻材、鞋子、手提包、百葉窗、窗簾、壁布、屏風、紙拉窗、塑膠拉窗、紙拉門、合成皮革、桌巾、衣類、雨衣、文具、書、筆記本、紙、紙箱、交通工具或家電等之各種塑膠體、玩具、運動用具、樂器、釣具、車內裝飾品、塑膠容器、卡片類、帳篷、木材‧柱‧天花板‧木牆等之建築用材、家具、印刷合板、內裝用板、人造花、觀葉植物、人工植物、泳池‧浴池‧河川‧海‧工廠排水‧生活排水‧地下水‧池‧人工河川等之水處理用填充劑、鏡、洗臉盆、瓷磚、瓷磚的接縫、浴缸、浴室構件、廁所用地板完工物料、院內抗感染用病院內構件、窯業系多機能材、釉藥、冰箱內外壁、台座、廚房面板、流理台、微波爐、烹調容器、換氣裝 置、空調、熱交換器、各種過濾器、便器、纖維、不織布、口罩、衣類、寢具、帽子、安全帽、門墊、絨毯、醫療器具、食品、叉子、刀、湯匙、食器、包裝材、保鮮膜、食品保存容器、食器清洗裝置、淨水器、廚餘處理裝置、三聚氰胺裝飾板、地毯、照明裝置、照明器具、照明燈、照明傘、不可見光(black light)、防污塗料、過濾器、農業用乙烯薄膜等各種薄膜‧薄片、超親水性薄膜、防草薄片、電子零件、電製品、電子機器、電暈充電裝置、電漿產生裝置、臭氧產生裝置、曝光裝置、加濕器、手乾燥機、頭皮保養裝置、吸塵器、電話機、行動電話、可攜式裝備、觸控面板顯示器、有機EL元件‧平板顯示器、噴墨記錄裝置、空氣清淨機、冷凍機器、集塵器、裝飾品、機械零件、磁碟、展示櫃、儀器用罩玻璃、相機、眼鏡、相機的鏡頭、眼鏡的鏡片、隱形眼鏡、美白劑、齒科‧口腔用材料、牙齒漂白材、植入物、口腔用器具、化妝品、洗髮精等。 Titanium oxide carrying a transition metal compound as the present invention Examples of the coated body and the mixture to be coated include building materials, exterior decoration, architectural interior decoration, architectural coatings, walls, wallpapers, floors, window frames, window glass, crystallized glass, glass, screen windows, and rainwater drainage. Sinks, sunshine heat reflective sheets, letter boxes, structural members, paving materials, display panels, traffic signs, road traffic sign reflectors, flat panel displays, display filters, road display materials, road decorative panels, fences, doors , tunnels, road lighting fixtures, soundproof walls, grilles, tunnel interiors, road mirrors, plastic sheet greenhouse roofs, bridges, bridge safety barriers, cars, trains, ships, interiors and exteriors, painting, vehicles Use wheel, railway vehicle body structure, vehicle parts, mechanical devices or articles, ‧ dust cover, painting, various display devices, advertising towers, insulators, solar panels, solar battery covers, solar water heaters, heat shields, Fuel cells, optical fibers, vehicle lighting covers, fishing nets, ropes, hoses, bottom members, anti-algae, shoes, handbags, blinds, curtains Wall coverings, screens, paper sliding windows, plastic sliding windows, paper sliding doors, synthetic leather, tablecloths, clothing, raincoats, stationery, books, notebooks, paper, cartons, vehicles or home appliances, etc. Utensils, musical instruments, fishing tackles, interior decorations, plastic containers, cards, tents, timber, columns, ceilings, wooden walls, etc., construction materials, furniture, printed plywood, interior panels, artificial flowers, foliage plants, artificial Plants, swimming pools, baths, rivers, rivers, factory drainage, living drainage, groundwater, pools, artificial rivers, water treatment fillers, mirrors, washbasins, ceramic tiles, tile joints, bathtubs, bathroom components, toilet floors Finished materials, in-house anti-infective disease internal components, kiln industry multi-function materials, glaze medicine, refrigerator inner and outer walls, pedestal, kitchen panel, flow table, microwave oven, cooking container, ventilation Installation, air conditioning, heat exchangers, various filters, toilets, fibers, non-woven fabrics, masks, clothing, bedding, hats, hard hats, door mats, carpets, medical equipment, food, forks, knives, spoons, utensils, packaging materials , plastic wrap, food preservation container, food cleaning device, water purifier, kitchen waste treatment device, melamine decorative board, carpet, lighting device, lighting fixture, lighting, lighting umbrella, black light, antifouling paint, Various films such as filters and agricultural vinyl films, sheets, super-hydrophilic films, grass-proof sheets, electronic parts, electrical products, electronic equipment, corona charging devices, plasma generating devices, ozone generating devices, exposure devices, humidification , hand dryer, scalp care device, vacuum cleaner, telephone, mobile phone, portable equipment, touch panel display, organic EL components, flat panel display, inkjet recording device, air cleaner, refrigeration machine, dust collector, Decorations, mechanical parts, disks, display cases, cover glass for instruments, cameras, glasses, lenses for cameras, lenses for glasses, Contact lenses, whitening agents, oral ‧ dental material, the dental bleaching material, implants, oral appliances, cosmetics, shampoo and the like.
(載有過渡金屬化合物之氧化鈦之製造方法) (Manufacturing method of titanium oxide carrying transition metal compound)
本發明的載有過渡金屬化合物之氧化鈦,例如,可經由下述步驟進行製造。 The transition metal compound-containing titanium oxide of the present invention can be produced, for example, by the following procedure.
(結晶性氧化鈦製造步驟) (Step of producing crystalline titanium oxide)
結晶性氧化鈦製造步驟,係由鈦化合物得到結晶性氧化鈦的步驟。作為結晶性氧化鈦之製造方法,可採用周知慣用的方法。例如,棒狀金紅石型氧化鈦,藉由將鈦化合物於水性媒體(例如,水或水與水溶性有機溶媒之混合液)中進行水熱處理[例如100~220℃、2~48小時( 較佳為2~15小時,特佳為5~15小時)]而可合成。又,在水熱處理之際添加鹵化物及/或攪拌(例如,攪拌所需動力Pv值:0.1~1500W/m3左右)的話,可調整得到的粒子之尺寸及表面積,因此較為理想。 The step of producing a crystalline titanium oxide is a step of obtaining crystalline titanium oxide from a titanium compound. As a method for producing crystalline titanium oxide, a conventionally known method can be employed. For example, bar-shaped rutile-type titanium oxide is hydrothermally treated by using a titanium compound in an aqueous medium (for example, water or a mixture of water and a water-soluble organic solvent) [for example, 100 to 220 ° C for 2 to 48 hours (more Good for 2~15 hours, especially for 5~15 hours)] but can be synthesized. Further, when a halide is added and/or stirred (for example, a power required for stirring Pv: 0.1 to 1500 W/m 3 ) during hydrothermal treatment, the size and surface area of the obtained particles can be adjusted, which is preferable.
作為前述鈦化合物,可舉出3價的鈦化合物、4價的鈦化合物。作為3價的鈦化合物,例如,可舉出三氯化鈦或三溴化鈦等之三鹵化鈦等。作為本發明之3價的鈦化合物,從廉價且容易取得的觀點,三氯化鈦(TiCl3)較為理想。 Examples of the titanium compound include a trivalent titanium compound and a tetravalent titanium compound. Examples of the trivalent titanium compound include titanium trihalide such as titanium trichloride or titanium tribromide. As the trivalent titanium compound of the present invention, titanium trichloride (TiCl 3 ) is preferred from the viewpoint of being inexpensive and easily available.
又,本發明之4價的鈦化合物,例如,可舉出下述式(1)所示之化合物等。 In addition, examples of the tetravalent titanium compound of the present invention include a compound represented by the following formula (1).
Ti(OR)tX4-t (1)(式中,R表示烴基,X表示鹵素原子。t表示0~3的整數) Ti(OR) t X 4-t (1) (wherein R represents a hydrocarbon group, and X represents a halogen atom. t represents an integer of 0 to 3)
作為式(1)中的R之烴基,例如,可舉出甲基、乙基、丙基、異丙基、正丁基、第二丁基、第三丁基等之C1-4脂肪族烴基等。 Examples of the hydrocarbon group of R in the formula (1) include a C 1-4 aliphatic group such as a methyl group, an ethyl group, a propyl group, an isopropyl group, a n-butyl group, a second butyl group, and a third butyl group. Hydrocarbyl group and the like.
作為式(1)中的X之鹵素原子,可舉出氯、溴、碘等。 Examples of the halogen atom of X in the formula (1) include chlorine, bromine, and iodine.
作為如前述之4價的鈦化合物,例如,可舉出TiCl4、TiBr4、TiI4等之四鹵化鈦;Ti(OCH3)Cl3、Ti(OC2H5)Cl3、Ti(OC4H9)Cl3、Ti(OC2H5)Br3、Ti(OC4H9)Br3等之三鹵化烷氧鈦;Ti(OCH3)2Cl2、Ti(OC2H5)2Cl2、Ti(OC4H9)2Cl2、Ti(OC2H5)2Br2等之二鹵化二烷氧鈦;Ti(OCH3)3Cl、Ti(OC2H5)3Cl、Ti(OC4H9)3Cl、Ti(OC2H5)3Br等之單鹵化三烷氧鈦等。作為本發明之4 價的鈦化合物,從廉價且容易取得的觀點,四鹵化鈦較佳,特別是四氯化鈦(TiCl4)較佳。 Examples of the tetravalent titanium compound as described above include titanium tetrahalide such as TiCl 4 , TiBr 4 , and TiI 4 ; Ti(OCH 3 )Cl 3 , Ti(OC 2 H 5 )Cl 3 , and Ti(OC). 4 H 9) Cl 3, Ti (OC 2 H 5) Br 3, Ti (OC 4 H 9) Br 3 , etc. trihalide, alkoxy titanium; Ti (OCH 3) 2 Cl 2, Ti (OC 2 H 5) Titanium dihalide dihalide such as 2 Cl 2 , Ti(OC 4 H 9 ) 2 Cl 2 , Ti(OC 2 H 5 ) 2 Br 2 or the like; Ti(OCH 3 ) 3 Cl, Ti(OC 2 H 5 ) 3 Cl, Ti(OC 4 H 9 ) 3 Cl, Ti(OC 2 H 5 ) 3 Br or the like monohalogenated titanium alkoxide. As the tetravalent titanium compound of the present invention, titanium tetrahalide is preferred from the viewpoint of being inexpensive and easily available, and particularly titanium tetrachloride (TiCl 4 ) is preferred.
利用水熱處理而得到的棒狀金紅石型氧化鈦,可利用周知慣用的方法進行精製,例如,過濾、濃縮、蒸餾、萃取、晶析、再結晶、管柱層析、或組合該等的方法。在本發明中,其中利用下述掃流方式進行膜過濾,從可維持氧化鈦的結晶結構,同時減低離子性雜質的含量,且不需要實施粉碎處理等,可直接施加載持過渡金屬化合物之步驟,並可得到高載持過渡金屬化合物的氧化鈦之觀點較為理想。 The rod-shaped rutile-type titanium oxide obtained by hydrothermal treatment can be purified by a conventionally known method, for example, filtration, concentration, distillation, extraction, crystallization, recrystallization, column chromatography, or a combination thereof. . In the present invention, the membrane filtration is carried out by the following sweeping method, and the crystal structure of the titanium oxide can be maintained, and the content of the ionic impurities can be reduced, and the pulverization treatment or the like is not required, and the transition metal compound can be directly applied. The step of obtaining a titanium oxide having a high transition metal compound is preferable.
利用前述方法得到的結晶性氧化鈦之平均短徑為50nm以下,較佳為5~40nm,特佳為5~30nm,最佳為10~25nm。 The average diameter of the crystalline titanium oxide obtained by the above method is 50 nm or less, preferably 5 to 40 nm, particularly preferably 5 to 30 nm, and most preferably 10 to 25 nm.
又,利用前述方法得到的結晶性氧化鈦之平均長寬比(長徑/短徑)為1.5以上,較佳為1.5~100,更佳為1.5~50,特佳為1.5~20,最佳為2~15。 Further, the average aspect ratio (long diameter/short diameter) of the crystalline titanium oxide obtained by the above method is 1.5 or more, preferably 1.5 to 100, more preferably 1.5 to 50, particularly preferably 1.5 to 20, most preferably It is 2~15.
再者,利用前述方法得到的結晶性氧化鈦之比表面積,例如為10m2/g以上。比表面積的下限,較佳為30m2/g,更佳為50m2/g,特佳為60m2/g,最佳為70m2/g。比表面積的上限,例如為200m2/g,較佳為150m2/g,特佳為100m2/g。 Further, the specific surface area of the crystalline titanium oxide obtained by the above method is, for example, 10 m 2 /g or more. The lower limit of the specific surface area is preferably 30 m 2 /g, more preferably 50 m 2 /g, particularly preferably 60 m 2 /g, and most preferably 70 m 2 /g. The upper limit of the specific surface area, for example, 200m 2 / g, preferably from 150m 2 / g, particularly preferably 100m 2 / g.
(載持過渡金屬化合物之步驟) (Step of carrying a transition metal compound)
載持過渡金屬化合物之步驟,係在經由前述步驟得到的結晶性氧化鈦載持過渡金屬化合物,而得到載有過渡金屬化合物之氧化鈦的步驟。過渡金屬化合物之載持 ,例如,可藉由在結晶性氧化鈦添加含有過渡金屬化合物的溶液並進行含浸而進行。例如,載持三價的鐵化合物(Fe3+)作為過渡金屬化合物之載有過渡金屬化合物之氧化鈦,可藉由在結晶性氧化鈦的懸浮液添加含有硝酸鐵(III)、硫酸鐵(III)、氯化鐵(III)等的溶液並進行含浸而得到。 The step of supporting the transition metal compound is a step of carrying a transition metal compound supported on the crystalline titanium oxide obtained through the above step to obtain a transition metal compound-containing titanium oxide. The support of the transition metal compound can be carried out, for example, by adding a solution containing a transition metal compound to the crystalline titanium oxide and impregnating it. For example, a trivalent iron compound (Fe 3+ ) is supported as a transition metal compound as a transition metal compound-containing titanium oxide, and iron (III) nitrate and iron sulfate can be added by adding a suspension of crystalline titanium oxide. III), a solution of iron (III) chloride or the like is obtained by impregnation.
包含過渡金屬化合物之溶液的濃度,例如為0.1~40重量%左右,較佳為1~40重量%。又,作為含浸時間,例如為1分鐘至24小時左右,較佳為5分鐘至10小時。 The concentration of the solution containing the transition metal compound is, for example, about 0.1 to 40% by weight, preferably 1 to 40% by weight. Further, the impregnation time is, for example, about 1 minute to 24 hours, preferably 5 minutes to 10 hours.
本發明中,在含浸過渡金屬化合物之際照射激發光,從可不需要大型設備等,並容易且有效率地在結晶性氧化鈦的特定面選擇性地載持過渡金屬化合物的觀點較為理想。照射激發光的話,結晶性氧化鈦之價電子帶的電子會激發至傳導帶,在價電子帶生成電洞,在傳導帶生成激發電子,且該等擴散至粒子表面,並依據各結晶面的特性分離激發電子與電洞,形成氧化反應面與還原反應面。在該狀態下,例如,進行三價的鐵化合物作為過渡金屬化合物之含浸時,三價的鐵化合物(Fe3+)會吸附於氧化反應面,但還原反應面中,三價的鐵化合物(Fe3+)被還原為二價的鐵化合物(Fe2+),且二價的鐵化合物(Fe2+)具有不易吸附的特性,因此溶出至溶液中,作為結果可得到在氧化反應面選擇性地載持鐵化合物(Fe3+)的載有鐵化合物之氧化鈦。 In the present invention, when the transition metal compound is impregnated, the excitation light is irradiated, and it is preferable that the transition metal compound is selectively and efficiently carried on the specific surface of the crystalline titanium oxide without requiring a large-scale facility or the like. When the excitation light is irradiated, electrons in the valence band of the crystalline titanium oxide are excited to the conduction band, and holes are generated in the valence band, and excited electrons are generated in the conduction band, and the diffusion proceeds to the surface of the particle, and according to each crystal face The characteristic separation excites electrons and holes to form an oxidation reaction surface and a reduction reaction surface. In this state, for example, when a trivalent iron compound is impregnated as a transition metal compound, a trivalent iron compound (Fe 3+ ) is adsorbed on the oxidation reaction surface, but a trivalent iron compound in the reduction reaction surface ( Fe 3+ ) is reduced to a divalent iron compound (Fe 2+ ), and the divalent iron compound (Fe 2+ ) has a property of being difficult to adsorb, and thus is eluted into the solution, and as a result, it is selectively obtained on the oxidation reaction surface. A titanium oxide carrying an iron compound supported on an iron compound (Fe 3+ ).
激發光為具有能帶隙能量以上之能量的光( 例如,紫外線)。作為激發光照射手段,例如,可使用中‧高壓水銀燈、UV雷射、UV-LED、不可見光等之具有有效地產生紫外線的光源之紫外線曝光裝置等。作為激發光的照射量,例如為0.1~300mW/cm2左右,較佳為0.5~100mW/cm2。 The excitation light is light (for example, ultraviolet light) having energy above the band gap energy. As the excitation light irradiation means, for example, an ultraviolet exposure device having a light source that efficiently generates ultraviolet light, such as a medium high pressure mercury lamp, a UV laser, a UV-LED, or an invisible light, or the like can be used. The amount of irradiation of excitation light, for example, 0.1 ~ 300mW / cm 2, and preferably 0.5 ~ 100mW / cm 2.
再者,本發明中,在含浸之際添加犠牲劑較為理想。藉由添加犠牲劑,可在結晶性氧化鈦之特定的結晶面以高選擇率載持過渡金屬化合物。作為犠牲劑,使用其本身容易放出電子的有機化合物較為理想,例如,可舉出甲醇、乙醇等之醇;乙酸等之羧酸;乙二胺四乙酸(EDTA)、三乙醇胺(TEA)等之胺等。 Further, in the present invention, it is preferred to add a sacrificial agent at the time of impregnation. By adding a cockroach, the transition metal compound can be carried at a high selectivity on the specific crystal face of the crystalline titanium oxide. As the sacrificial agent, an organic compound which easily emits electrons by itself is preferable, and examples thereof include alcohols such as methanol and ethanol; carboxylic acids such as acetic acid; ethylenediaminetetraacetic acid (EDTA) and triethanolamine (TEA). Amines, etc.
犠牲劑的添加量可適當調整,例如為結晶性氧化鈦的懸浮液之0.5~20.0重量%左右,較佳為1.0~5.0重量%左右。犠牲劑亦可使用過量。 The amount of the sacrificial agent to be added can be appropriately adjusted, and is, for example, about 0.5 to 20.0% by weight, preferably about 1.0 to 5.0% by weight, based on the suspension of the crystalline titanium oxide. Excipients can also be used in excess.
上述載持過渡金屬化合物之步驟後,實施精製處理較為理想。本發明中,實施利用掃流方式進行膜過濾的處理,從可不將載有過渡金屬化合物之氧化鈦壓密化,並於維持棒狀之結晶結構的狀態有效率地除去離子性雜質,得到離子性雜質之含量極低,而且為棒狀之載有過渡金屬化合物之氧化鈦的觀點較為理想。 After the step of carrying the transition metal compound, it is preferred to carry out the purification treatment. In the present invention, the membrane filtration treatment by the sweeping method is carried out, and the ionic impurities are efficiently removed from the state in which the titanium oxide carrying the transition metal compound is not compacted and the rod-like crystal structure is maintained. The content of the impurity is extremely low, and it is preferable that it is a rod-shaped titanium oxide carrying a transition metal compound.
(利用掃流方式的膜過濾) (filtration by membrane with sweeping method)
前述利用掃流方式的膜過濾,係使被處理水平行於過濾膜面而流動,一邊防止濾渣之沉積導致的過濾膜污染,一邊將被處理水之一部分以被處理水之流動側方向過濾的方法。藉由將上述氧化鈦或載有過渡金屬化合物 之氧化鈦的懸浮液施加利用掃流方式的膜過濾,可在過濾膜表面不形成壓密化的濾渣,並有效率地除去離子性雜質,可維持氧化鈦或載有過渡金屬化合物之氧化鈦之結晶結構,同時將離子性雜質之含量減低為極低。 In the membrane filtration by the sweeping method, the level of the treated layer flows on the surface of the filtration membrane, and while the filtration membrane is prevented from being contaminated by the deposition of the filter residue, one part of the water to be treated is filtered in the flow side direction of the water to be treated. method. By using the above titanium oxide or carrying a transition metal compound The suspension of titanium oxide is applied by membrane filtration using a sweeping method, so that no pulverized filter residue is formed on the surface of the filtration membrane, and ionic impurities are efficiently removed, and titanium oxide or a titanium oxide carrying a transition metal compound can be maintained. The crystal structure also reduces the content of ionic impurities to an extremely low level.
施加利用掃流方式的膜過濾的氧化鈦或載有過渡金屬化合物之氧化鈦的懸浮液之濃度,例如為0.1~40重量%左右(較佳為0.1~30重量%)。氧化鈦或載有過渡金屬化合物之氧化鈦的懸浮液之濃度超出上述範圍的話,離子性雜質之除去效率有下降的傾向。又,氧化鈦或載有過渡金屬化合物之氧化鈦的懸浮液之濃度高於上述範圍時,黏度變得過高,變得容易積垢(堵塞)。 The concentration of the suspension of the titanium oxide or the transition metal compound-loaded titanium oxide which is filtered by the membrane of the sweeping method is, for example, about 0.1 to 40% by weight (preferably 0.1 to 30% by weight). When the concentration of the suspension of titanium oxide or the titanium oxide carrying the transition metal compound is outside the above range, the removal efficiency of the ionic impurities tends to decrease. Moreover, when the concentration of the suspension of titanium oxide or the titanium oxide carrying the transition metal compound is higher than the above range, the viscosity becomes too high, and fouling (clogging) is likely to occur.
將氧化鈦或載有過渡金屬化合物之氧化鈦的懸浮液,施加利用掃流方式的膜過濾的話,可將離子性雜質與濾液同時分離除去,得到濃縮的氧化鈦或載有過渡金屬化合物之氧化鈦的懸浮液。 When a suspension of titanium oxide or a titanium oxide carrying a transition metal compound is applied to a membrane filtered by a sweeping method, the ionic impurities and the filtrate can be simultaneously separated and removed to obtain a concentrated titanium oxide or an oxidation carrying a transition metal compound. A suspension of titanium.
濃縮倍率調整為1~400倍左右較為理想(尤其是1~20倍,特別是1~10倍)。濃縮倍率高於上述範圍的話,有對膜面之附著物質的堆積抑制變困難,且防止氧化鈦或載有過渡金屬化合物之氧化鈦的壓密化變困難的傾向。又,由於對膜面之附著物質的堆積導致在過濾膜產生積垢(堵塞),故膜壽命變得容易降低,產生需要頻繁地進行逆清洗,產生過濾處理不能運作的情況等,且也有過濾速度變得容易下降的傾向。另一方面,濃縮倍率低於上述範圍的話,離子性雜質的分離效率下降,且清洗水的使用量有增加的傾向。 It is ideal to adjust the concentration ratio to about 1 to 400 times (especially 1 to 20 times, especially 1 to 10 times). When the concentration ratio is higher than the above range, it is difficult to suppress the deposition of the adhering substance on the film surface, and it is difficult to prevent the compaction of the titanium oxide or the titanium oxide carrying the transition metal compound. In addition, since fouling (clogging) occurs in the filtration membrane due to deposition of the adhering substance on the membrane surface, the membrane life is likely to be lowered, and it is necessary to perform reverse cleaning frequently, and the filtration treatment cannot be operated, and filtration is also performed. The tendency for speed to fall easily. On the other hand, when the concentration ratio is less than the above range, the separation efficiency of the ionic impurities is lowered, and the amount of the washing water used tends to increase.
前述濃縮倍率,例如,可藉由控制過濾壓力、氧化鈦或載有過渡金屬化合物之氧化鈦的懸浮液之膜面線速(掃流速度)等而調整。過濾壓力,例如為0.001~5.0MPa左右,較佳為0.005~3MPa,特佳為0.01~2.0MPa。 The concentration ratio can be adjusted, for example, by controlling the filtration pressure, the film surface speed (sweep speed) of the suspension of titanium oxide or the transition metal compound-loaded titanium oxide, and the like. The filtration pressure is, for example, about 0.001 to 5.0 MPa, preferably 0.005 to 3 MPa, and particularly preferably 0.01 to 2.0 MPa.
又,含有氧化鈦或載有過渡金屬化合物之氧化鈦的懸浮液之供給液的膜面線速越大,越可抑制對於膜面之附著物質的堆積,並得到高過濾流量(通量)。膜面線速(掃流速度),例如為0.02m/s以上未滿3m/s,較佳為0.05m/s以上未滿1.5m/s。 Moreover, the larger the film surface speed of the supply liquid containing the titanium oxide or the suspension of the titanium oxide carrying the transition metal compound, the more the deposition of the adhering substance to the film surface can be suppressed, and the high filtration flow rate (flux) can be obtained. The film surface line speed (sweep speed) is, for example, 0.02 m/s or more and less than 3 m/s, preferably 0.05 m/s or more and less than 1.5 m/s.
經由利用掃流方式的膜過濾而濃縮的氧化鈦或載有過渡金屬化合物之氧化鈦的懸浮液,加入水,稀釋使氧化鈦或載有過渡金屬化合物之氧化鈦的懸浮液之濃度成為上述範圍,且再度重複利用掃流方式進行膜過濾的操作較為理想。藉由前述,可減輕積垢(堵塞)等導致之過濾膜的負荷,並提升過濾膜之壽命,同時將離子性雜質之含量減低為極低。 The titanium oxide or the suspension of the titanium oxide carrying the transition metal compound, which is concentrated by membrane filtration by a sweeping method, is added with water, and the concentration of the suspension of the titanium oxide or the titanium oxide carrying the transition metal compound is diluted to the above range. And it is preferable to repeat the operation of membrane filtration by the sweeping method again. According to the above, the load of the filtration membrane due to fouling (clogging) or the like can be reduced, and the life of the filtration membrane can be increased, and the content of the ionic impurities can be reduced to an extremely low level.
第1圖為顯示氧化鈦或載有過渡金屬化合物之氧化鈦的懸浮液之利用掃流方式的膜過濾之一例(循環型膜過濾方式)的概略圖。在儲存槽儲存之含有氧化鈦或載有過渡金屬化合物之氧化鈦的懸浮液之供給液,係以掃流過濾方式進行膜過濾,可得到濃縮的氧化鈦或載有過渡金屬化合物之氧化鈦的懸浮液(濃縮液)。濃縮的氧化鈦或載有過渡金屬化合物之氧化鈦的懸浮液,再度往儲存槽進行循環,且以稀釋用的水(稀釋用水)稀釋, 並以掃流過濾方式過濾。 Fig. 1 is a schematic view showing an example of membrane filtration (circulating membrane filtration method) by means of a sweeping method of a suspension of titanium oxide or a titanium oxide carrying a transition metal compound. The supply liquid of the suspension containing titanium oxide or the titanium oxide carrying the transition metal compound stored in the storage tank is subjected to membrane filtration by a sweep filtration method to obtain concentrated titanium oxide or titanium oxide carrying a transition metal compound. Suspension (concentrate). A suspension of concentrated titanium oxide or titanium oxide carrying a transition metal compound is again circulated to the storage tank and diluted with water for dilution (diluted water). Filtered by sweeping filtration.
作為使用於利用掃流方式之膜過濾的過濾膜,例如,可舉出超過濾膜、微過濾膜、奈米過濾器、逆滲透膜等。本發明中,從分離性能佳的觀點,其中尤以使用超過濾膜較為理想。 Examples of the filtration membrane used for membrane filtration by a sweeping method include an ultrafiltration membrane, a microfiltration membrane, a nanofilter, and a reverse osmosis membrane. In the present invention, from the viewpoint of good separation performance, it is preferred to use an ultrafiltration membrane in particular.
作為超過濾膜,使用平均細孔徑為1~20nm左右(較佳為1~10nm),且可分離分子量1000~300000左右(較佳為1000~50000)、平均粒徑為1~10nm左右的物質者較為理想。 As the ultrafiltration membrane, a material having an average pore diameter of about 1 to 20 nm (preferably 1 to 10 nm) and having a molecular weight of about 1,000 to 300,000 (preferably 1,000 to 50,000) and an average particle diameter of about 1 to 10 nm can be used. The person is more ideal.
作為超過濾膜的膜形狀,例如,亦可為任何中空纖維型過濾膜、管狀膜、螺旋膜、平膜等,但從相較容易進行逆清洗的觀點,使用中空纖維型過濾膜、或管狀膜較為理想。 The film shape of the ultrafiltration membrane may be, for example, any hollow fiber filtration membrane, tubular membrane, spiral membrane, flat membrane, or the like, but a hollow fiber filtration membrane or a tubular shape is used from the viewpoint of facilitating reverse cleaning. The membrane is ideal.
從污染物質的閉塞之防止、對膜組的中空纖維填充率之提升的觀點,中空纖維型過濾膜之中空纖維膜的內徑為0.1~2.0mm左右(較佳為0.5~1.5mm)。 The inner diameter of the hollow fiber membrane of the hollow fiber type filtration membrane is about 0.1 to 2.0 mm (preferably 0.5 to 1.5 mm) from the viewpoint of prevention of clogging of the pollutants and improvement of the hollow fiber filling rate of the membrane group.
作為過濾膜的材質,例如,可舉出乙酸纖維素、聚丙烯腈、聚碸、聚醚碸(PES)、聚丙烯腈、芳香族聚醯胺、聚偏二氟乙烯、聚氯乙烯、聚乙烯、聚丙烯、聚醯亞胺、陶瓷等之一般的材質。本發明中,尤以乙酸纖維素、聚碸、聚醚碸(PES)、聚丙烯腈、芳香族聚醯胺較為理想。 Examples of the material of the filtration membrane include cellulose acetate, polyacrylonitrile, polyfluorene, polyether oxime (PES), polyacrylonitrile, aromatic polyamine, polyvinylidene fluoride, polyvinyl chloride, and poly. A general material such as ethylene, polypropylene, polyimide, or ceramics. In the present invention, cellulose acetate, polyfluorene, polyether oxime (PES), polyacrylonitrile, and aromatic polyamine are particularly preferred.
使用中空纖維型過濾膜時,作為使氧化鈦或載有過渡金屬化合物之氧化鈦的懸浮液流動之方法(過濾方式),可舉出在內側(中空纖維膜的內側)使包含氧化 鈦或載有過渡金屬化合物之氧化鈦的懸浮液之供給液流動,使濾液朝外側(中空纖維膜的外側)流動的方式(內壓過濾方式);與其相反,在外側使包含氧化鈦或載有過渡金屬化合物之氧化鈦的懸浮液之供給液流動,使濾液朝內側流動的方式(外壓過濾方式)。本發明中,從可維持高膜面流速的觀點,尤以內壓過濾方式較為理想。 When a hollow fiber type filtration membrane is used, a method of filtering a suspension of titanium oxide or a titanium oxide carrying a transition metal compound (filtration method) is oxidized on the inner side (inside of the hollow fiber membrane) a method in which a supply liquid of a suspension of titanium or a suspension of titanium oxide carrying a transition metal compound flows to the outside (the outer side of the hollow fiber membrane) (internal pressure filtration method); on the contrary, the titanium oxide or the titanium oxide is contained on the outer side. A method in which a supply liquid of a suspension of a transition metal compound titanium oxide flows and the filtrate flows inward (external pressure filtration method). In the present invention, an internal pressure filtration method is preferable from the viewpoint of maintaining a high membrane surface flow rate.
在利用掃流方式之膜過濾中,為了防止對過濾膜面之附著物質的堆積、減輕對過濾膜之負擔、並進行長時間膜過濾運作,對於過濾膜利用清洗水實施間斷的逆清洗較為理想。逆清洗係一邊控制壓力及流速,一邊以預定的週期進行較為理想。 In the membrane filtration by the sweeping method, in order to prevent the deposition of adhering substances on the membrane surface, reduce the burden on the membrane, and perform long-term membrane filtration, it is preferable to perform intermittent reverse cleaning of the membrane with washing water. . The reverse cleaning system is preferably carried out at a predetermined cycle while controlling the pressure and the flow rate.
作為逆清洗的壓力,例如為0.01~3.0MPa左右,較佳為0.01~2.0MPa,更佳為0.01~1.0MPa,特佳為0.01~0.5MPa,最佳為0.05~0.5MPa。又,作為逆清洗的流速,例如為0.01~10kg/分鐘左右,較佳為0.05~5kg/分鐘,特佳為0.1~5kg/分鐘[或者,例如為1×10-7~2×10-4m/秒左右,較佳為8×10-7~9×10-5m/秒,特佳為1×10-6~9×10-5m/秒]。作為逆清洗的頻度,例如,在0.5~3小時間進行1次左右較為理想。逆清洗的時間為0.5~10分鐘左右較佳。 The pressure for the reverse washing is, for example, about 0.01 to 3.0 MPa, preferably 0.01 to 2.0 MPa, more preferably 0.01 to 1.0 MPa, particularly preferably 0.01 to 0.5 MPa, and most preferably 0.05 to 0.5 MPa. Further, the flow rate for the reverse cleaning is, for example, about 0.01 to 10 kg/min, preferably 0.05 to 5 kg/min, particularly preferably 0.1 to 5 kg/min [or, for example, 1 × 10 -7 to 2 × 10 -4 . m/sec or so, preferably 8 × 10 -7 ~ 9 × 10 -5 m / sec, particularly preferably 1 × 10 -6 ~ 9 × 10 -5 m / sec]. The frequency of the reverse cleaning is preferably about one time in about 0.5 to 3 hours. The time for the reverse cleaning is preferably about 0.5 to 10 minutes.
再者,作為用於逆清洗的清洗水,使用水(例如,精製水、蒸餾水、純水、離子交換水等)較為理想。又,藉由逆清洗通過膜的清洗水,作為濃縮的載有過渡金屬化合物之氧化鈦的懸浮液之稀釋用水再利用較為理想(參照第2圖)。 Further, as the washing water used for the reverse washing, water (for example, purified water, distilled water, pure water, ion-exchanged water, or the like) is preferably used. Further, it is preferable to reuse the diluted water as a suspension of the concentrated transition metal compound-containing titanium oxide by backwashing the washing water passing through the membrane (see Fig. 2).
過濾氧化鈦的懸浮液時,利用掃流方式的膜過濾,重複進行直到濾液的pH成為1以上(較佳為1~7,特佳為2~6,最佳為2~5.5)為止較為理想。使利用掃流方式的膜過濾在濾液的pH成為上述範圍之前結束的話,有離子性雜質(特別是氫離子、氯離子、鈦離子)之除去變不足、過渡金屬化合物之載持變困難的情況。 When the suspension of the titanium oxide is filtered, it is repeatedly filtered by a membrane of a sweeping method until the pH of the filtrate becomes 1 or more (preferably 1 to 7, particularly preferably 2 to 6, preferably 2 to 5.5). . When the membrane filtration by the sweeping method is completed before the pH of the filtrate is in the above range, the removal of ionic impurities (especially hydrogen ions, chloride ions, and titanium ions) is insufficient, and the transition of the transition metal compound becomes difficult. .
又,過濾載有過渡金屬化合物之氧化鈦的懸浮液時,利用掃流方式的膜過濾,使濾液的電導度成為300μS/cm以下(例如為0.5~300μS/cm,較佳為0.5~250μS/cm,特佳為1~200μS/cm)為止而重複進行較為理想。使利用掃流方式的膜過濾在濾液的電導度成為上述範圍之前結束的話,有離子性雜質(特別是鐵離子、氯離子)之除去變不足的情況。 Further, when the suspension containing the transition metal compound-containing titanium oxide is filtered, the membrane has a conductivity of 300 μS/cm or less by filtration (for example, 0.5 to 300 μS/cm, preferably 0.5 to 250 μS/). It is preferable to repeat the cm, particularly preferably from 1 to 200 μS/cm. When the membrane filtration by the sweeping method is completed before the conductivity of the filtrate is within the above range, the removal of ionic impurities (especially iron ions and chloride ions) may be insufficient.
利用掃流方式進行膜過濾而得到的載有過渡金屬化合物之氧化鈦的懸浮液,之後藉由進行乾燥(例如,F.V.下(1.3kPa[A])以下),在60℃進行15小時左右;或常壓(大氣壓)下,在105℃進行1小時左右而得到載有過渡金屬化合物之氧化鈦。 a suspension of a transition metal compound-containing titanium oxide obtained by membrane filtration by a sweeping method, followed by drying (for example, FV (1.3 kPa [A]) or less), and performing at 60 ° C for about 15 hours; At a normal pressure (atmospheric pressure), the transition metal compound-containing titanium oxide is obtained at 105 ° C for about 1 hour.
以下根據實施例更具體地說明本發明,但本發明並沒有限定於該等之實施例。 Hereinafter, the present invention will be specifically described based on examples, but the present invention is not limited to the examples.
實施例1 Example 1
(結晶性氧化鈦之製備) (Preparation of crystalline titanium oxide)
在室溫(25℃),以純水將四氯化鈦水溶液(Ti濃度:16.5重量%±0.5重量%、氯離子濃度:31重量%±2重量% ,東邦鈦(股)製)稀釋,使Ti濃度成為5.6重量%。將稀釋後的四氯化鈦水溶液5650g加入至容量10L之鉭內襯的高壓釜並予以密閉。使用熱媒,花費2小時將上述高壓釜內溫度升溫至140℃。之後,以攪拌所需動力(Pv值)1360W/m3攪拌,同時在溫度:140℃、壓力:其溫度之蒸氣壓的條件下保持5小時後,藉由將熱媒予以冷卻而使高壓釜冷卻至40℃以下。之後,進一步於溫度:140℃、壓力:其溫度之蒸氣壓的條件下保持5小時後,藉由將熱媒予以冷卻而使高壓釜冷卻。確認高壓釜內溫度成為40℃以下而取出粗製氧化鈦懸浮液(1)5650g。 Diluted with titanium tetrachloride aqueous solution (Ti concentration: 16.5 wt% ± 0.5 wt%, chloride ion concentration: 31 wt% ± 2 wt%, manufactured by Toho Titanium Co., Ltd.) in pure water at room temperature (25 ° C). The Ti concentration was made 5.6% by weight. 5650 g of the diluted titanium tetrachloride aqueous solution was placed in a 10 L rug-lined autoclave and sealed. Using the heat medium, it took 2 hours to raise the temperature in the above autoclave to 140 °C. Thereafter, the mixture was stirred at a power required for stirring (Pv value) at 1,360 W/m 3 while being kept at a temperature of 140 ° C and a vapor pressure of the temperature for 5 hours, and then the autoclave was cooled by cooling the heat medium. Cool to below 40 °C. Thereafter, the mixture was further kept at a temperature of 140 ° C and a pressure of a vapor pressure of the temperature for 5 hours, and then the autoclave was cooled by cooling the heat medium. It was confirmed that the temperature in the autoclave was 40 ° C or lower, and 5650 g of the crude titanium oxide suspension (1) was taken out.
(利用掃流方式的膜過濾處理(1)) (membrane filtration treatment by sweeping method (1))
將得到的粗製氧化鈦懸浮液(1)以純水稀釋為3倍,使用中空纖維型超過濾膜(商品名「FS03-FC-FUS03C1」,材質:PES,標稱分子量(nominal molecular weight limit):3萬,Daicen Membrane Systems(股)製),於室溫(25℃)、過濾壓力0.02MPa,一邊加入與濾液量同量的純水,一邊進行利用掃流方式的過濾處理。經由過濾處理得到的濃縮液係再度於儲存槽循環,且重複施加過濾處理直到濾液的pH成為4.0為止。再者,pH係使用pH試驗紙測定。該期間中,以1小時1次的比例,以0.1MPa的壓力、2kg/分鐘的流速實施逆清洗1分鐘。藉由該逆清洗而通過膜的清洗水係於儲存槽循環。之後,停止純水之儲存,濃縮氧化鈦濃度,得到氧化鈦懸浮液(1-1)。將氧化鈦懸浮液(1-1)於常壓下、105℃乾燥1小時時,得到具有結晶面(110)及結晶面(111)之棒狀金紅石型氧化鈦與具有結晶 面(110)、結晶面(111)及結晶面(001)之棒狀金紅石型氧化鈦之混合物的氧化鈦(1)(比表面積:77m2/g,平均長寬比:6,平均短徑:18nm)525g(參照第3圖)。得到的氧化鈦(1)之以下述利用紫外線的甲苯氧化法所評價的光觸媒活性為625ppm(分解率:94%)。 The obtained crude titanium oxide suspension (1) was diluted to 3 times with pure water, and a hollow fiber type ultrafiltration membrane (trade name "FS03-FC-FUS03C1", material: PES, nominal molecular weight limit) was used. : 30,000, manufactured by Daicen Membrane Systems Co., Ltd., at room temperature (25 ° C) and a filtration pressure of 0.02 MPa, while adding the same amount of pure water as the filtrate, and performing a filtration treatment by a sweeping method. The concentrated liquid obtained by the filtration treatment was again circulated in the storage tank, and the filtration treatment was repeatedly applied until the pH of the filtrate became 4.0. Further, the pH was measured using a pH test paper. In this period, the reverse cleaning was performed for 1 minute at a pressure of 0.1 MPa and a flow rate of 2 kg/min in a ratio of one hour. The washing water that has passed through the membrane by the reverse washing is circulated in the storage tank. Thereafter, the storage of pure water was stopped, and the concentration of titanium oxide was concentrated to obtain a titanium oxide suspension (1-1). When the titanium oxide suspension (1-1) is dried at 105 ° C for 1 hour under normal pressure, a rod-shaped rutile-type titanium oxide having a crystal face (110) and a crystal face (111) is obtained and has a crystal face (110). Titanium oxide (1) of a mixture of a rod-like rutile-type titanium oxide having a crystal face (111) and a crystal face (001) (specific surface area: 77 m 2 /g, average aspect ratio: 6, average short diameter: 18 nm) 525g (refer to Figure 3). The photocatalytic activity of the obtained titanium oxide (1) evaluated by the following toluene oxidation method using ultraviolet rays was 625 ppm (decomposition rate: 94%).
(載持鐵化合物之處理) (treatment of carrying iron compounds)
在上述所得到的氧化鈦懸浮液(1-1)添加氯化鐵水溶液(35重量%)7.5g,於室溫(25℃)攪拌30分鐘。之後,添加甲醇95g(氧化鈦懸浮液的1.7重量%),使用100W的高壓水銀燈,照射紫外線(UV)3小時(UV照射量:5mW/cm2),得到粗製載有鐵化合物之氧化鈦懸浮液(1)。 To the titanium oxide suspension (1-1) obtained above, 7.5 g of an aqueous solution of ferric chloride (35 wt%) was added, and the mixture was stirred at room temperature (25 ° C) for 30 minutes. Thereafter, 95 g of methanol (1.7 wt% of the titanium oxide suspension) was added, and a 100 W high-pressure mercury lamp was irradiated with ultraviolet rays (UV) for 3 hours (UV irradiation amount: 5 mW/cm 2 ) to obtain a suspension of the titanium oxide containing the iron compound. Liquid (1).
(利用掃流方式的膜過濾處理(2)) (membrane filtration treatment by sweeping method (2))
將粗製載有鐵化合物之氧化鈦懸浮液(1)以純水稀釋為3倍,使用中空纖維型超過濾膜(商品名「FS03-FC-FUS03C1」,材質:PES,標稱分子量:3萬,Daicen Membrane Systems(股)製),於室溫(25℃)、過濾壓力0.02MPa,一邊加入與濾液量同量的純水,一邊進行利用掃流方式的過濾處理。經由過濾處理得到的濃縮液係再度於儲存槽循環,且重複施加過濾處理直到濾液的電導度成為200μS/cm為止。該期間中,以1小時1次的比例,在0.1MPa的壓力、2kg/分鐘的流速實施逆清洗1分鐘。藉由該逆清洗而通過膜的清洗水係於儲存槽循環。之後,停止純水之儲存,並濃縮載有鐵化合物之氧化鈦濃度,得到載有鐵化合物之氧化鈦懸浮液(1-1)。該期間中,以1小時1次的比例,以0.1MPa的壓力、2kg/分鐘的流 速實施逆清洗1分鐘。利用該逆清洗而通過膜的清洗水係於儲存槽循環。 The titanium oxide suspension (1) containing the iron compound is diluted to 3 times with pure water, and a hollow fiber type ultrafiltration membrane (trade name "FS03-FC-FUS03C1", material: PES, nominal molecular weight: 30,000) is used. The Daicen Membrane Systems (manufactured by Daisen Membrane Systems Co., Ltd.) was subjected to a filtration treatment by a sweeping method while adding pure water of the same amount as the filtrate at room temperature (25 ° C) and a filtration pressure of 0.02 MPa. The concentrated liquid obtained by the filtration treatment was again circulated in the storage tank, and the filtration treatment was repeatedly applied until the conductivity of the filtrate became 200 μS/cm. During this period, the reverse cleaning was carried out for 1 minute at a pressure of 0.1 MPa and a flow rate of 2 kg/min at a ratio of one hour. The washing water that has passed through the membrane by the reverse washing is circulated in the storage tank. Thereafter, the storage of pure water is stopped, and the concentration of the titanium oxide carrying the iron compound is concentrated to obtain a titanium oxide suspension (1-1) carrying the iron compound. During this period, the flow rate of 0.1 MPa and the flow of 2 kg/min are used in a ratio of one hour. Perform reverse cleaning for 1 minute. The washing water that has passed through the membrane by the reverse washing is circulated in the storage tank.
之後,在常壓下、105℃乾燥1小時,得到載有鐵化合物之氧化鈦(1)(比表面積:77m2/g,平均長寬比:6,平均短徑:18nm)。得到的載有鐵化合物之氧化鈦(1)的鐵化合物之含量為800ppm。又,根據下述利用可見光的甲醇氧化法進行評價的光觸媒活性為734ppm。再者,得到的載有鐵化合物之氧化鈦(1)為具有結晶面(110)及結晶面(111),且僅於前述結晶面(111)載有鐵化合物的棒狀金紅石型氧化鈦與具有結晶面(110)、結晶面(111)及結晶面(001),且於前述結晶面(001)及結晶面(111)載有鐵化合物的棒狀金紅石型氧化鈦之混合物。 Thereafter, the mixture was dried at 105 ° C for 1 hour under normal pressure to obtain a titanium oxide (1) (specific surface area: 77 m 2 /g, average aspect ratio: 6, average short diameter: 18 nm) carrying an iron compound. The content of the iron compound of the obtained titanium oxide (1) carrying an iron compound was 800 ppm. Further, the photocatalytic activity evaluated by the methanol oxidation method using visible light described below was 734 ppm. Further, the obtained titanium oxide (1) carrying an iron compound is a rod-shaped rutile-type titanium oxide having a crystal face (110) and a crystal face (111) and carrying only an iron compound on the crystal face (111). And a mixture of rod-shaped rutile-type titanium oxide having a crystal face (110), a crystal face (111), and a crystal face (001), and having an iron compound on the crystal face (001) and the crystal face (111).
實施例2 Example 2
(結晶性氧化鈦之製備) (Preparation of crystalline titanium oxide)
在室溫(25℃),以純水將四氯化鈦水溶液(Ti濃度:16.5重量%±0.5重量%、氯離子濃度:31重量%±2重量%,東邦鈦(股)製)稀釋,使Ti濃度成為5.6重量%。將稀釋後的四氯化鈦水溶液5650g加入至容量10L之鉭內襯的高壓釜並予以密閉。使用熱媒,花費2小時將上述高壓釜內溫度升溫至140℃。之後,以攪拌所需動力(Pv值)220W/m3攪拌,同時在溫度:140℃、壓力:其溫度之蒸氣壓的條件下保持10小時後,藉由將熱媒予以冷卻而使高壓釜冷卻。確認高壓釜內溫度成為40℃以下而取出粗製氧化鈦懸浮液(2)5650g。 The titanium tetrachloride aqueous solution (Ti concentration: 16.5 wt% ± 0.5 wt%, chloride ion concentration: 31 wt% ± 2 wt%, manufactured by Toho Titanium Co., Ltd.) was diluted with pure water at room temperature (25 ° C). The Ti concentration was made 5.6% by weight. 5650 g of the diluted titanium tetrachloride aqueous solution was placed in a 10 L rug-lined autoclave and sealed. Using the heat medium, it took 2 hours to raise the temperature in the above autoclave to 140 °C. Thereafter, the mixture was stirred at a power required for stirring (Pv value) of 220 W/m 3 while maintaining the vapor pressure at a temperature of 140 ° C and a temperature of 10 hours, and then the autoclave was cooled by cooling the heat medium. cool down. It was confirmed that the temperature in the autoclave was 40 ° C or lower, and 5650 g of the crude titanium oxide suspension (2) was taken out.
(利用掃流方式的膜過濾處理(1)) (membrane filtration treatment by sweeping method (1))
將得到的粗氧化鈦懸浮液(2)以純水稀釋為3倍,使用中空纖維型超過濾膜(商品名「FS03-FC-FUS03C1」,材質:PES,標稱分子量:3萬,Daicen Membrane Systems(股)製),於室溫(25℃)、過濾壓力0.02MPa,一邊加入與濾液量同量的純水,一邊進行利用掃流方式的過濾處理。經由過濾處理得到的濃縮液係再度於儲存槽循環,且重複施加過濾處理直到濾液的pH成為4.0為止。該期間中,以1小時1次的比例,以0.1MPa的壓力、2kg/分鐘的流速實施逆清洗1分鐘。藉由該逆清洗而通過膜的清洗水係於儲存槽循環。之後,停止純水之儲存,濃縮氧化鈦濃度,得到氧化鈦懸浮液(2-1)。將氧化鈦懸浮液(2-1)於常壓下、105℃乾燥1小時時,得到具有結晶面(110)及結晶面(111)之棒狀金紅石型氧化鈦與具有結晶面(110)、結晶面(111)及結晶面(001)之棒狀金紅石型氧化鈦之混合物的氧化鈦(2)533g。得到的氧化鈦(2)之根據下述利用紫外線的甲苯氧化法所評價的光觸媒活性為647ppm(分解率:95%)。 The obtained crude titanium oxide suspension (2) was diluted to 3 times with pure water, and a hollow fiber type ultrafiltration membrane (trade name "FS03-FC-FUS03C1", material: PES, nominal molecular weight: 30,000, Daicen Membrane) was used. The system (manufactured by Systems) was subjected to a filtration treatment by a sweeping method while adding pure water of the same amount as the filtrate at room temperature (25 ° C) and a filtration pressure of 0.02 MPa. The concentrated liquid obtained by the filtration treatment was again circulated in the storage tank, and the filtration treatment was repeatedly applied until the pH of the filtrate became 4.0. In this period, the reverse cleaning was performed for 1 minute at a pressure of 0.1 MPa and a flow rate of 2 kg/min in a ratio of one hour. The washing water that has passed through the membrane by the reverse washing is circulated in the storage tank. Thereafter, the storage of pure water was stopped, and the concentration of titanium oxide was concentrated to obtain a titanium oxide suspension (2-1). When the titanium oxide suspension (2-1) is dried at 105 ° C for 1 hour under normal pressure, a rod-shaped rutile-type titanium oxide having a crystal face (110) and a crystal face (111) is obtained and has a crystal face (110). 533 g of titanium oxide (2) of a mixture of a crystalline surface (111) and a rod-shaped rutile-type titanium oxide of a crystal surface (001). The photocatalytic activity of the obtained titanium oxide (2) evaluated by the toluene oxidation method using ultraviolet rays below was 647 ppm (decomposition rate: 95%).
(載持鐵化合物之處理) (treatment of carrying iron compounds)
在上述所得到的氧化鈦懸浮液(2-1)添加氯化鐵水溶液(35重量%)7.5g,於室溫(25℃)攪拌30分鐘。之後,添加甲醇95g(氧化鈦懸浮液的1.7重量%),使用100W的高壓水銀燈,照射紫外線(UV)3小時(UV照射量:5mW/cm2),得到粗製載有鐵化合物之氧化鈦懸浮液(2)。 7.5 g of an aqueous solution of ferric chloride (35 wt%) was added to the titanium oxide suspension (2-1) obtained above, and stirred at room temperature (25 ° C) for 30 minutes. Thereafter, 95 g of methanol (1.7 wt% of the titanium oxide suspension) was added, and a 100 W high-pressure mercury lamp was irradiated with ultraviolet rays (UV) for 3 hours (UV irradiation amount: 5 mW/cm 2 ) to obtain a suspension of the titanium oxide containing the iron compound. Liquid (2).
(利用掃流方式的膜過濾處理(2)) (membrane filtration treatment by sweeping method (2))
將粗製載有鐵化合物之氧化鈦懸浮液(2)以純水稀 釋為2倍,使用中空纖維型超過濾膜(商品名「FS03-FC-FUS03C1」,材質:PES,標稱分子量:3萬,Daicen Membrane Systems(股)製),於室溫(25℃)、過濾壓力0.02MPa,一邊加入與濾液量同量的純水,一邊進行利用掃流方式的過濾處理。經由過濾處理得到的濃縮液係再度於儲存槽循環,且重複施加過濾處理直到濾液的電導度成為200μS/cm為止。該期間中,以1小時1次的比例,以0.1MPa的壓力、2kg/分鐘的流速實施逆清洗1分鐘。藉由該逆清洗而通過膜的清洗水係於儲存槽循環。之後,停止純水之儲存,濃縮載有鐵化合物之氧化鈦濃度,得到載有鐵化合物之氧化鈦懸浮液(2-1)。該期間中,以1小時1次的比例,以0.1MPa的壓力、2kg/分鐘的流速實施逆清洗1分鐘。藉由該逆清洗而通過膜的清洗水係於儲存槽循環。 A titanium oxide suspension (2) containing a crude iron compound is diluted with pure water Released twice, using a hollow fiber type ultrafiltration membrane (trade name "FS03-FC-FUS03C1", material: PES, nominal molecular weight: 30,000, manufactured by Daicen Membrane Systems), at room temperature (25 ° C) The filtration pressure was 0.02 MPa, and the same amount of pure water as the filtrate was added, and filtration treatment by a sweeping method was performed. The concentrated liquid obtained by the filtration treatment was again circulated in the storage tank, and the filtration treatment was repeatedly applied until the conductivity of the filtrate became 200 μS/cm. In this period, the reverse cleaning was performed for 1 minute at a pressure of 0.1 MPa and a flow rate of 2 kg/min in a ratio of one hour. The washing water that has passed through the membrane by the reverse washing is circulated in the storage tank. Thereafter, the storage of pure water is stopped, and the concentration of the titanium oxide carrying the iron compound is concentrated to obtain a titanium oxide suspension (2-1) carrying the iron compound. In this period, the reverse cleaning was performed for 1 minute at a pressure of 0.1 MPa and a flow rate of 2 kg/min in a ratio of one hour. The washing water that has passed through the membrane by the reverse washing is circulated in the storage tank.
之後,在常壓下、105℃乾燥1小時,得到結晶性之載有鐵化合物之氧化鈦(2)(比表面積:78m2/g,平均長寬比:3,平均短徑:17nm)530g。得到的載有鐵化合物之氧化鈦(2)的鐵化合物之含量為830ppm。又,根據下述利用可見光的甲醇氧化法進行評價的光觸媒活性為775ppm。再者,得到的載有鐵化合物之氧化鈦(2)為具有結晶面(110)及結晶面(111),且僅於前述結晶面(111)載有鐵化合物的棒狀金紅石型氧化鈦與具有結晶面(110)、結晶面(111)及結晶面(001),且於前述結晶面(001)及結晶面(111)載有鐵化合物的棒狀金紅石型氧化鈦之混合物(第4圖)。 Thereafter, the mixture was dried at 105 ° C for 1 hour under normal pressure to obtain a crystalline iron oxide (2) (specific surface area: 78 m 2 /g, average aspect ratio: 3, average short diameter: 17 nm) 530 g of an iron compound. . The content of the obtained iron compound carrying the iron compound (2) of the iron compound was 830 ppm. Further, the photocatalytic activity evaluated by the methanol oxidation method using visible light described below was 775 ppm. Further, the obtained titanium oxide (2) carrying an iron compound is a rod-shaped rutile-type titanium oxide having a crystal face (110) and a crystal face (111) and carrying only an iron compound on the crystal face (111). a mixture of rod-shaped rutile-type titanium oxide having a crystal face (110), a crystal face (111), and a crystal face (001), and having an iron compound on the crystal face (001) and the crystal face (111) 4 picture).
實施例3 Example 3
在上述(利用掃流方式的過濾處理(2))中,重複進行直到濾液的電導度成為150μS/cm為止,此外係與實施例2同樣進行,得到結晶性的載有鐵化合物之氧化鈦(3)(比表面積:78.5m2/g,平均長寬比:3,平均短徑:16nm)530g。得到的載有鐵化合物之氧化鈦(3)的鐵化合物之含量為890ppm。又,根據下述利用可見光的甲醇氧化法所評價的光觸媒活性為795ppm。 In the above-described (filtering treatment (2) by the sweeping method), the conductivity of the filtrate was changed to 150 μS/cm, and in the same manner as in Example 2, a crystalline iron compound-loaded titanium oxide was obtained. 3) (specific surface area: 78.5 m 2 /g, average aspect ratio: 3, average short diameter: 16 nm) 530 g. The content of the iron compound of the obtained titanium oxide (3) carrying the iron compound was 890 ppm. Further, the photocatalytic activity evaluated by the methanol oxidation method using visible light described below was 795 ppm.
實施例4 Example 4
在上述(利用掃流方式的過濾處理(2))中,重複進行直到濾液的電導度成為100μS/cm為止,此外係與實施例2同樣進行,得到結晶性的載有鐵化合物之氧化鈦(4)(比表面積:79m2/g,平均長寬比:3,平均短徑:15nm)530g。得到的載有鐵化合物之氧化鈦(4)的鐵化合物之含量為950ppm。又,根據下述利用可見光的甲醇氧化法所評價的光觸媒活性為800ppm。 In the above-described (filtering treatment (2) by the sweeping method), the conductivity of the filtrate was changed to 100 μS/cm, and in the same manner as in Example 2, a crystalline iron compound-loaded titanium oxide was obtained. 4) (specific surface area: 79 m 2 /g, average aspect ratio: 3, average short diameter: 15 nm) 530 g. The content of the obtained iron compound carrying the iron compound titanium oxide (4) was 950 ppm. Further, the photocatalytic activity evaluated by the methanol oxidation method using visible light described below was 800 ppm.
實施例5 Example 5
在上述(利用掃流方式的過濾處理(2))中,重複進行直到濾液的電導度成為50μS/cm為止,此外係與實施例2同樣進行,得到結晶性的載有鐵化合物之氧化鈦(5)(比表面積:80m2/g,平均長寬比:3,平均短徑:14nm)530g。得到的載有鐵化合物之氧化鈦(5)的鐵化合物之含量為1200ppm。又,根據下述利用可見光的甲醇氧化法所評價的光觸媒活性為800ppm。 In the above-described (filtering treatment (2) by the sweeping method), the conductivity of the filtrate was changed to 50 μS/cm, and the same was carried out in the same manner as in Example 2 to obtain a crystalline iron compound-loaded titanium oxide ( 5) (specific surface area: 80 m 2 /g, average aspect ratio: 3, average short diameter: 14 nm) 530 g. The content of the iron compound of the obtained iron compound-containing titanium oxide (5) was 1200 ppm. Further, the photocatalytic activity evaluated by the methanol oxidation method using visible light described below was 800 ppm.
實施例6 Example 6
在上述(載持鐵化合物之處理)中,將氯化鐵水溶液(35重量%)的使用量由7.5g變更為6.5g,此外係與實施例2同樣進行,得到結晶性的載有鐵化合物之氧化鈦(6)(比表面積:76m2/g,平均長寬比:3,平均短徑:17nm)530g。得到的載有鐵化合物之氧化鈦(6)的鐵化合物之含量為700ppm。又,根據下述利用可見光的甲醇氧化法所評價的光觸媒活性為780ppm。 In the above (treatment of supporting the iron compound), the amount of the ferric chloride aqueous solution (35 wt%) was changed from 7.5 g to 6.5 g, and the same procedure as in Example 2 was carried out to obtain a crystalline iron-loaded compound. Titanium oxide (6) (specific surface area: 76 m 2 /g, average aspect ratio: 3, average short diameter: 17 nm) 530 g. The content of the iron compound of the obtained iron compound-containing titanium oxide (6) was 700 ppm. Further, the photocatalytic activity evaluated by the methanol oxidation method using visible light described below was 780 ppm.
實施例7 Example 7
在上述(載持鐵化合物之處理)中,將氯化鐵水溶液(35重量%)的使用量由7.5g變更為15.0g,此外係與實施例2同樣進行,得到結晶性的載有鐵化合物之氧化鈦(7)(比表面積:80m2/g,平均長寬比:3,平均短徑:16nm)530g。得到的載有鐵化合物之氧化鈦(7)的鐵化合物之含量為2000ppm。又,根據下述利用可見光的甲醇氧化法所評價的光觸媒活性為753ppm。 In the above-mentioned (treatment of supporting the iron compound), the amount of the ferric chloride aqueous solution (35 wt%) was changed from 7.5 g to 15.0 g, and the same procedure as in Example 2 was carried out to obtain a crystalline iron-loaded compound. Titanium oxide (7) (specific surface area: 80 m 2 /g, average aspect ratio: 3, average short diameter: 16 nm) 530 g. The content of the iron compound of the obtained iron compound-containing titanium oxide (7) was 2000 ppm. Further, the photocatalytic activity evaluated by the methanol oxidation method using visible light described below was 753 ppm.
實施例8 Example 8
在上述(結晶性氧化鈦之製備)中,將反應溫度(高壓釜內溫度)由140℃變更為120℃,此外係與實施例2同樣進行,得到粗製氧化鈦懸浮液(8),且對於得到的粗製氧化鈦懸浮液(8),與實施例2同樣地實施前述(利用掃流方式的膜過濾處理(1))時,得到氧化鈦懸浮液(8-1),並得到作為具有結晶面(110)及結晶面(111)之棒狀金紅石型氧化鈦與具有結晶面(110)、結晶面(111)及結晶面(001)之棒狀金紅石型氧化鈦的混合物之氧化鈦(8)530g。得到的氧化鈦(8)之根據下述利用紫外線的甲苯氧化法所評 價的光觸媒活性為600ppm(CO2產生率:90%)。 In the above (preparation of crystalline titanium oxide), the reaction temperature (temperature in the autoclave) was changed from 140 ° C to 120 ° C, and a crude titanium oxide suspension (8) was obtained in the same manner as in Example 2, and When the obtained crude titanium oxide suspension (8) was subjected to the above-described membrane filtration treatment (1) by a sweeping method in the same manner as in Example 2, a titanium oxide suspension (8-1) was obtained and obtained as crystals. Titanium oxide of a rod-shaped rutile-type titanium oxide having a surface (110) and a crystal plane (111) and a rod-shaped rutile-type titanium oxide having a crystal face (110), a crystal face (111), and a crystal face (001) (8) 530g. The photocatalytic activity of the obtained titanium oxide (8) evaluated by the toluene oxidation method using ultraviolet rays below was 600 ppm (CO 2 production rate: 90%).
之後,與實施例2同樣地實施(載持鐵化合物之處理)、(利用掃流方式的膜過濾處理(2)),得到結晶性的載有鐵化合物之氧化鈦(8)(比表面積:85m2/g,平均長寬比:2,平均短徑:10nm)。得到的載有鐵化合物之氧化鈦(8)的鐵化合物之含量為780ppm。又,根據下述利用可見光的甲醇氧化法所評價的光觸媒活性為691ppm。 Then, in the same manner as in the second embodiment, the treatment (the treatment of carrying the iron compound) and the membrane filtration treatment (2) by the sweep method are carried out to obtain a crystalline iron compound (8) carrying an iron compound (specific surface area: 85 m 2 /g, average aspect ratio: 2, average short diameter: 10 nm). The content of the iron compound of the obtained iron compound-containing titanium oxide (8) was 780 ppm. Further, the photocatalytic activity evaluated by the methanol oxidation method using visible light described below was 691 ppm.
實施例9 Example 9
在上述(結晶性氧化鈦之製備)中,將反應溫度(高壓釜內溫度)由140℃變更為160℃,此外係與實施例2同樣進行,得到粗製氧化鈦懸浮液(9),且對於得到的粗製氧化鈦懸浮液(9),與實施例2同樣地實施前述(利用掃流方式的膜過濾處理(1))時,得到氧化鈦懸浮液(9-1),並得到作為具有結晶面(110)及結晶面(111)之棒狀金紅石型氧化鈦與具有結晶面(110)、結晶面(111)及結晶面(001)之棒狀金紅石型氧化鈦的混合物之氧化鈦(9)530g。得到的氧化鈦(9)之根據下述利用紫外線的甲苯氧化法所評價的光觸媒活性為645ppm(分解率:95%)。 In the above (preparation of crystalline titanium oxide), the reaction temperature (inner autoclave temperature) was changed from 140 ° C to 160 ° C, and the same procedure as in Example 2 was carried out to obtain a crude titanium oxide suspension (9), and When the obtained crude titanium oxide suspension (9) was subjected to the above-described membrane filtration treatment (1) by a sweeping method in the same manner as in Example 2, a titanium oxide suspension (9-1) was obtained and obtained as crystals. Titanium oxide of a rod-shaped rutile-type titanium oxide having a surface (110) and a crystal plane (111) and a rod-shaped rutile-type titanium oxide having a crystal face (110), a crystal face (111), and a crystal face (001) (9) 530g. The photocatalytic activity of the obtained titanium oxide (9) evaluated by the toluene oxidation method using ultraviolet rays below was 645 ppm (decomposition rate: 95%).
之後,與實施例2同樣地實施(載持鐵化合物之處理)、(利用掃流方式的膜過濾處理(2)),得到結晶性的載有鐵化合物之氧化鈦(9)(比表面積:55m2/g,平均長寬比:12,平均短徑:25nm)。得到的載有鐵化合物之氧化鈦(9)的鐵化合物之含量為820ppm。又,根據下述利用可見光的甲醇氧化法所評價的光觸媒活性為727ppm。 Then, in the same manner as in Example 2, the treatment (the treatment of carrying the iron compound) and the membrane filtration treatment (2) by the sweep method were carried out to obtain a crystalline iron compound (9) carrying an iron compound (specific surface area: 55 m 2 /g, average aspect ratio: 12, average short diameter: 25 nm). The content of the iron compound of the obtained iron compound-containing titanium oxide (9) was 820 ppm. Further, the photocatalytic activity evaluated by the methanol oxidation method using visible light described below was 727 ppm.
實施例10 Example 10
(結晶性氧化鈦之製備) (Preparation of crystalline titanium oxide)
在室溫(25℃),以純水將四氯化鈦水溶液(Ti濃度:16.5重量%±0.5重量%、氯離子濃度:31重量%±2重量%,東邦鈦(股)製)稀釋,使Ti濃度成為5.6重量%。將稀釋後的四氯化鈦水溶液5650g加入至容量10L之鉭內襯的高壓釜並予以密閉。使用熱媒,花費2小時將上述高壓釜內溫度升溫至140℃。之後,以攪拌所需動力(Pv值)13W/m3攪拌,同時在溫度:140℃、壓力:其溫度之蒸氣壓的條件下保持10小時後,藉由將熱媒予以冷卻而使高壓釜冷卻。確認高壓釜內溫度成為40℃以下而取出粗製氧化鈦懸浮液(10)5650g。 The titanium tetrachloride aqueous solution (Ti concentration: 16.5 wt% ± 0.5 wt%, chloride ion concentration: 31 wt% ± 2 wt%, manufactured by Toho Titanium Co., Ltd.) was diluted with pure water at room temperature (25 ° C). The Ti concentration was made 5.6% by weight. 5650 g of the diluted titanium tetrachloride aqueous solution was placed in a 10 L rug-lined autoclave and sealed. Using the heat medium, it took 2 hours to raise the temperature in the above autoclave to 140 °C. Thereafter, the mixture was stirred at a power required for stirring (Pv value) of 13 W/m 3 while maintaining the vapor pressure at a temperature of 140 ° C and a pressure for 10 hours, and then the autoclave was cooled by cooling the heat medium. cool down. It was confirmed that the temperature in the autoclave was 40 ° C or lower, and 5650 g of the crude titanium oxide suspension (10) was taken out.
(利用掃流方式的膜過濾處理(1)) (membrane filtration treatment by sweeping method (1))
不以純水稀釋得到的粗製氧化鈦懸浮液(10),使用中空纖維型超過濾膜(商品名「FS03-FC-FUS03C1」,材質:PES,標稱分子量:3萬,Daicen Membrane Systems(股)製),於室溫(25℃)、過濾壓力0.02MPa,一邊加入與濾液量同量的純水,一邊進行利用掃流方式的過濾處理。經由過濾處理得到的濃縮液係再度於儲存槽循環,且重複施加過濾處理直到濾液的pH成為4.0為止。該期間中,以1小時1次的比例,以0.1MPa的壓力、2kg/分鐘的流速實施逆清洗1分鐘。藉由該逆清洗而通過膜的清洗水係於儲存槽循環。根據前述,得到氧化鈦懸浮液(10-1)5650g。將氧化鈦懸浮液(10-1)於常壓下、105℃乾燥1小時時,得到具有結晶面(110)及結晶面(111)之棒狀金紅石型氧化鈦與具有結晶面(110)、結晶面(111)及結晶面 (001)之棒狀金紅石型氧化鈦之混合物的氧化鈦(10)。得到的氧化鈦(10)之根據下述利用紫外線的甲苯氧化法所評價的光觸媒活性為647ppm(分解率:95%)。 The crude titanium oxide suspension (10) which is not diluted with pure water, uses a hollow fiber type ultrafiltration membrane (trade name "FS03-FC-FUS03C1", material: PES, nominal molecular weight: 30,000, Daicen Membrane Systems (shares) The system was subjected to a filtration treatment by a sweeping method while adding pure water of the same amount as the filtrate at room temperature (25 ° C) and a filtration pressure of 0.02 MPa. The concentrated liquid obtained by the filtration treatment was again circulated in the storage tank, and the filtration treatment was repeatedly applied until the pH of the filtrate became 4.0. In this period, the reverse cleaning was performed for 1 minute at a pressure of 0.1 MPa and a flow rate of 2 kg/min in a ratio of one hour. The washing water that has passed through the membrane by the reverse washing is circulated in the storage tank. According to the foregoing, 5650 g of a titanium oxide suspension (10-1) was obtained. When the titanium oxide suspension (10-1) is dried at 105 ° C for 1 hour under normal pressure, a rod-shaped rutile-type titanium oxide having a crystal face (110) and a crystal face (111) is obtained and has a crystal face (110). Crystalline surface (111) and crystal plane Titanium oxide (10) of a mixture of rod-shaped rutile-type titanium oxide of (001). The photocatalytic activity of the obtained titanium oxide (10) evaluated by the toluene oxidation method using ultraviolet rays below was 647 ppm (decomposition rate: 95%).
(載持鐵化合物之處理) (treatment of carrying iron compounds)
在上述所得到的氧化鈦懸浮液(10-1)添加氯化鐵水溶液(35重量%)7.5g,於室溫(25℃)攪拌30分鐘。之後,添加甲醇95g(氧化鈦懸浮液的1.7重量%),使用100W的高壓水銀燈,照射紫外線(UV)3小時(UV照射量:5mW/cm2),得到粗製載有鐵化合物之氧化鈦懸浮液(10)。 7.5 g of an aqueous ferric chloride solution (35 wt%) was added to the titanium oxide suspension (10-1) obtained above, and the mixture was stirred at room temperature (25 ° C) for 30 minutes. Thereafter, 95 g of methanol (1.7 wt% of the titanium oxide suspension) was added, and a 100 W high-pressure mercury lamp was irradiated with ultraviolet rays (UV) for 3 hours (UV irradiation amount: 5 mW/cm 2 ) to obtain a suspension of the titanium oxide containing the iron compound. Liquid (10).
(利用掃流方式的膜過濾處理(2)) (membrane filtration treatment by sweeping method (2))
不以純水稀釋粗製載有鐵化合物之氧化鈦懸浮液(10),使用中空纖維型超過濾膜(商品名「FS03-FC-FUS03C1」,材質:PES,標稱分子量:3萬,Daicen Membrane Systems(股)製),於室溫(25℃)、過濾壓力0.02MPa,一邊加入與濾液量同量的純水,一邊進行利用掃流方式的過濾處理。經由過濾處理得到的濃縮液係再度於儲存槽循環,且重複施加過濾處理直到濾液的電導度成為200μS/cm為止。該期間中,以1小時1次的比例,以0.1MPa的壓力、2kg/分鐘的流速實施逆清洗1分鐘。藉由該逆清洗而通過膜的清洗水係於儲存槽循環。根據前述,得到載有鐵化合物之氧化鈦懸浮液(10-1)。 The titanium oxide suspension (10) containing the iron compound is not diluted with pure water, and the hollow fiber type ultrafiltration membrane (trade name "FS03-FC-FUS03C1", material: PES, nominal molecular weight: 30,000, Daicen Membrane) is used. The system (manufactured by Systems) was subjected to a filtration treatment by a sweeping method while adding pure water of the same amount as the filtrate at room temperature (25 ° C) and a filtration pressure of 0.02 MPa. The concentrated liquid obtained by the filtration treatment was again circulated in the storage tank, and the filtration treatment was repeatedly applied until the conductivity of the filtrate became 200 μS/cm. In this period, the reverse cleaning was performed for 1 minute at a pressure of 0.1 MPa and a flow rate of 2 kg/min in a ratio of one hour. The washing water that has passed through the membrane by the reverse washing is circulated in the storage tank. According to the foregoing, a titanium oxide suspension (10-1) carrying an iron compound was obtained.
之後,在常壓下、105℃乾燥1小時,得到結晶性之載有鐵化合物之氧化鈦(10)(比表面積:76m2/g,平均長寬比:5,平均短徑:16nm)530g。得到的載有鐵化合物之氧化鈦(10)的鐵化合物之含量為820ppm。又, 根據下述利用可見光的甲醇氧化法進行評價的光觸媒活性為778ppm。 Thereafter, it was dried at 105 ° C for 1 hour under normal pressure to obtain a crystalline iron oxide (10) (specific surface area: 76 m 2 /g, average aspect ratio: 5, average short diameter: 16 nm) 530 g of an iron compound. . The content of the iron compound of the obtained iron compound-containing titanium oxide (10) was 820 ppm. Further, the photocatalytic activity evaluated by the methanol oxidation method using visible light described below was 778 ppm.
實施例11 Example 11
(結晶性氧化鈦之製備) (Preparation of crystalline titanium oxide)
在室溫(25℃),以純水將四氯化鈦水溶液(Ti濃度:16.5重量%±0.5重量%、氯離子濃度:31重量%±2重量%,東邦鈦(股)製)稀釋,使Ti濃度成為5.6重量%。將稀釋後的四氯化鈦水溶液560g加入至容量1L之鉭內襯的高壓釜並予以密閉。使用熱媒,花費2小時將上述高壓釜內溫度升溫至140℃。之後,以攪拌所需動力(Pv值)13W/m3攪拌,同時在溫度:140℃、壓力:其溫度之蒸氣壓的條件下保持10小時後,藉由將熱媒予以冷卻而使高壓釜冷卻。確認高壓釜內溫度成為40℃以下而取出粗製氧化鈦懸浮液(11)560g。 The titanium tetrachloride aqueous solution (Ti concentration: 16.5 wt% ± 0.5 wt%, chloride ion concentration: 31 wt% ± 2 wt%, manufactured by Toho Titanium Co., Ltd.) was diluted with pure water at room temperature (25 ° C). The Ti concentration was made 5.6% by weight. 560 g of the diluted titanium tetrachloride aqueous solution was placed in a 1 L lining autoclave and sealed. Using the heat medium, it took 2 hours to raise the temperature in the above autoclave to 140 °C. Thereafter, the mixture was stirred at a power required for stirring (Pv value) of 13 W/m 3 while maintaining the vapor pressure at a temperature of 140 ° C and a pressure for 10 hours, and then the autoclave was cooled by cooling the heat medium. cool down. It was confirmed that the temperature in the autoclave was 40 ° C or lower, and 560 g of the crude titanium oxide suspension (11) was taken out.
(利用掃流方式的膜過濾處理(1)) (membrane filtration treatment by sweeping method (1))
將得到的粗製氧化鈦懸浮液(11)以純水稀釋為10倍,使用中空纖維型超過濾膜(商品名「FS03-FC-FUS03C1」,材質:PES,標稱分子量:3萬,Daicen Membrane Systems(股)製),於室溫(25℃)、過濾壓力0.05MPa,一邊加入與濾液量同量的純水,一邊進行利用掃流方式的過濾處理。經由過濾處理得到的濃縮液係再度於儲存槽循環,且重複施加過濾處理直到濾液的pH成為2.9為止。之後,停止純水之儲存,濃縮氧化鈦濃度,得到氧化鈦懸浮液(11-1)。該期間中,以1小時1次的比例,以0.15MPa的壓力、0.1kg/分鐘的流速實施逆清洗1分鐘。藉由該逆 清洗而通過膜的清洗水係於儲存槽循環。將氧化鈦懸浮液(11-1)於減壓下、60℃乾燥15小時時,得到具有結晶面(110)及結晶面(111)之棒狀金紅石型氧化鈦與具有結晶面(110)、結晶面(111)及結晶面(001)之棒狀金紅石型氧化鈦之混合物的氧化鈦(11)。得到的氧化鈦(11)之根據下述利用紫外線的甲苯氧化法所評價的光觸媒活性為617ppm(CO2產生率:93%)。 The obtained crude titanium oxide suspension (11) was diluted 10 times with pure water, and a hollow fiber type ultrafiltration membrane (trade name "FS03-FC-FUS03C1", material: PES, nominal molecular weight: 30,000, Daicen Membrane) was used. The system (manufactured by Systems) was subjected to a filtration treatment by a sweeping method while adding pure water of the same amount as the filtrate at room temperature (25 ° C) and a filtration pressure of 0.05 MPa. The concentrated liquid obtained by the filtration treatment was again circulated in the storage tank, and the filtration treatment was repeatedly applied until the pH of the filtrate became 2.9. Thereafter, the storage of pure water was stopped, and the concentration of titanium oxide was concentrated to obtain a titanium oxide suspension (11-1). During this period, the reverse cleaning was carried out for 1 minute at a pressure of 0.15 MPa and a flow rate of 0.1 kg/min at a ratio of one hour. The washing water that has passed through the membrane by the reverse washing is circulated in the storage tank. When the titanium oxide suspension (11-1) is dried at 60 ° C for 15 hours under reduced pressure, a rod-shaped rutile-type titanium oxide having a crystal face (110) and a crystal face (111) and a crystal face (110) are obtained. A titanium oxide (11) of a mixture of a crystalline surface (111) and a rod-shaped rutile-type titanium oxide of a crystal surface (001). The photocatalytic activity of the obtained titanium oxide (11) evaluated by the toluene oxidation method using ultraviolet rays described below was 617 ppm (CO 2 production rate: 93%).
(載持鐵化合物之處理) (treatment of carrying iron compounds)
在上述所得到的氧化鈦懸浮液(11-1)添加氯化鐵水溶液(35重量%)0.3g,於室溫(25℃)攪拌30分鐘。之後,添加甲醇9.6g(氧化鈦懸浮液的1.7重量%),使用100W的高壓水銀燈,照射紫外線(UV)3小時(UV照射量:0.9mW/cm2),得到粗製載有鐵化合物之氧化鈦懸浮液(11)。 To the titanium oxide suspension (11-1) obtained above, 0.3 g of an aqueous solution of ferric chloride (35 wt%) was added, and the mixture was stirred at room temperature (25 ° C) for 30 minutes. Thereafter, 9.6 g of methanol (1.7 wt% of the titanium oxide suspension) was added, and ultraviolet rays (UV) were irradiated for 3 hours (UV irradiation amount: 0.9 mW/cm 2 ) using a 100 W high-pressure mercury lamp to obtain oxidation of the crude iron compound. Titanium suspension (11).
(利用掃流方式的膜過濾處理(2)) (membrane filtration treatment by sweeping method (2))
將粗製載有鐵化合物之氧化鈦懸浮液(11)以純水稀釋為10倍,使用中空纖維型超過濾膜(商品名「FS03-FC-FUS03C1」,材質:PES,標稱分子量:3萬,Daicen Membrane Systems(股)製),於室溫(25℃)、過濾壓力0.05MPa,一邊加入與濾液量同量的純水,一邊進行利用掃流方式的過濾處理。經由過濾處理得到的濃縮液係再度於儲存槽循環,且重複施加過濾處理直到濾液的電導度成為21μS/cm為止。之後,停止純水之儲存,濃縮載有鐵化合物之氧化鈦濃度,得到載有鐵化合物之氧化鈦懸浮液(11-1)。該期間中,以1小時1次的比例,以 0.15MPa的壓力、0.1kg/分鐘的流速實施逆清洗1分鐘。藉由該逆清洗而通過膜的清洗水係於儲存槽循環。 The titanium oxide suspension (11) containing the iron compound is diluted 10 times with pure water, and a hollow fiber type ultrafiltration membrane (trade name "FS03-FC-FUS03C1", material: PES, nominal molecular weight: 30,000) is used. The Daicen Membrane Systems (manufactured by Daisen Membrane Systems Co., Ltd.) was subjected to a filtration treatment by a sweeping method while adding pure water of the same amount as the filtrate at room temperature (25 ° C) and a filtration pressure of 0.05 MPa. The concentrated liquid obtained by the filtration treatment was again circulated in the storage tank, and the filtration treatment was repeatedly applied until the conductivity of the filtrate became 21 μS/cm. Thereafter, the storage of pure water is stopped, and the concentration of the titanium oxide carrying the iron compound is concentrated to obtain a titanium oxide suspension (11-1) carrying the iron compound. During this period, in the ratio of 1 hour and 1 time, The backwashing was carried out for 1 minute at a pressure of 0.15 MPa and a flow rate of 0.1 kg/min. The washing water that has passed through the membrane by the reverse washing is circulated in the storage tank.
之後,在減壓下、60℃乾燥15小時,得到結晶性之載有鐵化合物之氧化鈦(11)(比表面積:71m2/g,平均長寬比:9,平均短徑:20nm)40g。得到的載有鐵化合物之氧化鈦(11)的鐵化合物之含量為420ppm。又,根據下述利用可見光的甲苯氧化法進行評價的光觸媒活性為416ppm,根據下述利用可見光的甲醇氧化法進行評價的光觸媒活性為716ppm。 Thereafter, it was dried at 60 ° C for 15 hours under reduced pressure to obtain a crystalline iron oxide (11) (specific surface area: 71 m 2 /g, average aspect ratio: 9, average short diameter: 20 nm) 40 g of an iron compound. . The content of the iron compound of the obtained iron compound-containing titanium oxide (11) was 420 ppm. Further, the photocatalytic activity evaluated by the toluene oxidation method using visible light described below was 416 ppm, and the photocatalytic activity evaluated by the methanol oxidation method using visible light described below was 716 ppm.
比較例1 Comparative example 1
(結晶性氧化鈦之製備) (Preparation of crystalline titanium oxide)
在室溫(25℃),以純水將四氯化鈦水溶液(Ti濃度:16.5重量%±0.5重量%、氯離子濃度:31重量%±2重量%,東邦鈦(股)製)稀釋,使Ti濃度成為5.6重量%。將稀釋後的四氯化鈦水溶液560g加入至容量1L之鉭內襯的高壓釜並予以密閉。使用熱媒,花費2小時將上述高壓釜內溫度升溫至140℃。之後,不進行攪拌,在溫度:140℃、壓力:其溫度之蒸氣壓的條件下保持10小時後,藉由將熱媒予以冷卻而使高壓釜冷卻。確認高壓釜內溫度成為40℃以下而取出粗製氧化鈦懸浮液(12)560g。 The titanium tetrachloride aqueous solution (Ti concentration: 16.5 wt% ± 0.5 wt%, chloride ion concentration: 31 wt% ± 2 wt%, manufactured by Toho Titanium Co., Ltd.) was diluted with pure water at room temperature (25 ° C). The Ti concentration was made 5.6% by weight. 560 g of the diluted titanium tetrachloride aqueous solution was placed in a 1 L lining autoclave and sealed. Using the heat medium, it took 2 hours to raise the temperature in the above autoclave to 140 °C. Thereafter, the mixture was kept at a temperature of 140 ° C and a vapor pressure of the temperature for 10 hours, and then the autoclave was cooled by cooling the heat medium. It was confirmed that the temperature in the autoclave was 40 ° C or lower, and 560 g of the crude titanium oxide suspension (12) was taken out.
使用粗製氧化鈦懸浮液(12)代替粗製氧化鈦懸浮液(11),此外係與實施例11同樣進行,得到結晶性的載有鐵化合物之氧化鈦(12)(比表面積:9m2/g,平均長寬比:1.2,平均短徑:100nm)。得到的載有鐵化合物之氧化鈦(12)的鐵化合物之含量為30ppm。又,根據下述利 用可見光的甲醇氧化法進行評價的光觸媒活性為250ppm。 The crude titanium oxide suspension (12) was used instead of the crude titanium oxide suspension (11), and the same procedure as in Example 11 was carried out to obtain a crystalline iron compound (12) carrying an iron compound (specific surface area: 9 m 2 /g). , average aspect ratio: 1.2, average short diameter: 100 nm). The content of the iron compound of the obtained titanium oxide (12) carrying an iron compound was 30 ppm. Further, the photocatalytic activity evaluated by the methanol oxidation method using visible light described below was 250 ppm.
<光觸媒活性之評價方法> <Evaluation method of photocatalytic activity>
(利用可見光的甲苯氧化法) (Toluene oxidation using visible light)
藉由將實施例所得到的載有鐵化合物之氧化鈦作為光觸媒使用,在氣相將甲苯氧化,並測定生成的CO2量而評價光觸媒活性。 The titanium oxide carrying the iron compound obtained in the examples was used as a photocatalyst, and toluene was oxidized in the gas phase, and the amount of CO 2 produced was measured to evaluate the photocatalytic activity.
使載有鐵化合物之氧化鈦200mg廣布於玻璃製皿,並置入至反應容器(Tedlar bag,材質:氟化乙烯樹脂)之中,將100ppm的甲苯氣體125mL吹送至反應容器內。甲苯氣體之對於載有鐵化合物之氧化鈦的吸附達到平衡後,在室溫(25℃)進行光照射(LED,光強度:2.5mW/cm2,光之波長:455nm)。使用附屬於Methanizer(商品名「MT221」,GL Sciences(股)製)之附有氫火焰游離檢測器的氣體層析儀(商品名「GC-14B」,島津製作所製),測定由光照射開始24小時後的CO2之生成量(反應容器內的CO2濃度)。 200 mg of titanium oxide carrying an iron compound was spread on a glass dish, placed in a reaction container (Tedlar bag, material: fluorinated ethylene resin), and 125 ppm of toluene gas (100 ppm) was blown into the reaction container. After the adsorption of the toluene gas to the titanium oxide carrying the iron compound was balanced, light irradiation (LED, light intensity: 2.5 mW/cm 2 , wavelength of light: 455 nm) was performed at room temperature (25 ° C). Using a gas chromatograph (trade name "GC-14B", manufactured by Shimadzu Corporation) attached to a Methanizer (trade name "MT221", manufactured by GL Sciences Co., Ltd.) with a hydrogen flame free detector, the measurement starts with light irradiation. The amount of CO 2 produced after 24 hours (the concentration of CO 2 in the reaction vessel).
(利用可見光的甲醇氧化法) (Methanol oxidation method using visible light)
藉由將實施例及比較例所得到的載有鐵化合物之氧化鈦作為光觸媒使用,在氣相將甲醇氧化,並測定生成的CO2量而評價光觸媒活性。 The titanium oxide carrying the iron compound obtained in the examples and the comparative examples was used as a photocatalyst, and methanol was oxidized in the gas phase, and the amount of CO 2 produced was measured to evaluate the photocatalytic activity.
使載有鐵化合物之氧化鈦200mg廣布於玻璃製皿,並置入至反應容器(Tedlar bag,材質:氟化乙烯樹脂)之中,將800ppm的甲醇氣體125mL吹送至反應容器內。甲醇氣體之對於載有鐵化合物之氧化鈦的吸附達到平衡後 ,在室溫(25℃)進行光照射(LED,光強度:2.5W/m2,光之波長:455nm)。使用附屬Methanizer(商品名「MT221」,GL Sciences(股)製)之附有氫火焰游離檢測器的氣體層析儀(商品名「GC-14B」,島津製作所製),測定由光照射開始24小時後的CO2之生成量(反應容器內的CO2濃度)。 200 mg of titanium oxide carrying an iron compound was spread on a glass dish, placed in a reaction container (Tedlar bag, material: fluorinated ethylene resin), and 125 ppm of methanol gas (125 mL) was blown into the reaction container. After the adsorption of the methanol gas to the titanium oxide carrying the iron compound was balanced, light irradiation (LED, light intensity: 2.5 W/m 2 , wavelength of light: 455 nm) was performed at room temperature (25 ° C). Using a gas chromatograph (trade name "GC-14B", manufactured by Shimadzu Corporation) with a hydrogen flame free detector attached to the Methanizer (trade name "MT221", manufactured by GL Sciences), the measurement is started by light irradiation. The amount of CO 2 produced after the hour (the concentration of CO 2 in the reaction vessel).
(利用紫外線的甲苯氧化法) (toluene oxidation method using ultraviolet rays)
藉由將實施例所得到的氧化鈦作為光觸媒使用,在氣相將甲苯氧化,並測定生成的CO2量而評價光觸媒活性。 By using the titanium oxide obtained in the example as a photocatalyst, toluene was oxidized in the gas phase, and the amount of CO 2 produced was measured to evaluate the photocatalytic activity.
使氧化鈦200mg廣布於玻璃製皿,並置入至反應容器(Tedlar bag,材質:氟化乙烯樹脂)之中,將100ppm的甲苯氣體125mL吹送至反應容器內。甲苯氣體之對於氧化鈦的吸附達到平衡後,在室溫(25℃)進行光照射(LED,光強度:0.1mW/cm2,光之波長:365nm)。使用附屬Methanizer(商品名「MT221」,GL Sciences(股)製)之附有氫火焰游離檢測器的氣體層析儀(商品名「GC-14B」,島津製作所製),測定由光照射開始24小時後的CO2之生成量(反應容器內的CO2濃度)。 200 mg of titanium oxide was spread on a glass dish, placed in a reaction container (Tedlar bag, material: fluorinated ethylene resin), and 125 ppm of toluene gas (100 ppm) was blown into the reaction container. After the adsorption of the toluene gas to the titanium oxide was balanced, light irradiation (LED, light intensity: 0.1 mW/cm 2 , wavelength of light: 365 nm) was performed at room temperature (25 ° C). Using a gas chromatograph (trade name "GC-14B", manufactured by Shimadzu Corporation) with a hydrogen flame free detector attached to the Methanizer (trade name "MT221", manufactured by GL Sciences), the measurement is started by light irradiation. The amount of CO 2 produced after the hour (the concentration of CO 2 in the reaction vessel).
本發明的載有過渡金屬化合物之氧化鈦,其平均短徑為50nm以下,而且平均長寬比(長徑/短徑)為1.5以上。因此,對於可見光之回應性優異,且可吸收太陽光或白熾燈、螢光燈、LED等之通常的生活空間之光,並將有害化學物質分解至水或二氧化碳為止。亦即,本 發明的載有過渡金屬化合物之氧化鈦懸浮液,可作為LED照明下用之光觸媒適當地使用。並且,可應用於各種抗菌防黴除臭、空氣淨化、水淨化等,且可廣範圍應用於以室內的壁紙或家具為首之在家庭內或病院、學校等之公共施設內的環境淨化、家電製品之高機能化等。 The transition metal compound-containing titanium oxide of the present invention has an average minor axis of 50 nm or less and an average aspect ratio (long diameter/short diameter) of 1.5 or more. Therefore, it is excellent in responsiveness to visible light, and absorbs sunlight in ordinary living spaces such as sunlight or incandescent lamps, fluorescent lamps, and LEDs, and decomposes harmful chemicals into water or carbon dioxide. That is, this The titanium oxide suspension containing the transition metal compound of the invention can be suitably used as a photocatalyst for LED illumination. In addition, it can be applied to various antibacterial, anti-mildew, deodorization, air purification, water purification, etc., and can be widely applied to environmental purification, home appliances, such as indoor wallpapers or furniture, in public facilities in homes, hospitals, schools, etc. The high functionality of the products.
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