JPWO2017010472A1 - Odor reducing agent - Google Patents
Odor reducing agent Download PDFInfo
- Publication number
- JPWO2017010472A1 JPWO2017010472A1 JP2017528683A JP2017528683A JPWO2017010472A1 JP WO2017010472 A1 JPWO2017010472 A1 JP WO2017010472A1 JP 2017528683 A JP2017528683 A JP 2017528683A JP 2017528683 A JP2017528683 A JP 2017528683A JP WO2017010472 A1 JPWO2017010472 A1 JP WO2017010472A1
- Authority
- JP
- Japan
- Prior art keywords
- platinum
- porous silica
- freshness
- agent
- decomposing
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 239000003638 chemical reducing agent Substances 0.000 title description 3
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 claims abstract description 150
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims abstract description 99
- 239000000126 substance Substances 0.000 claims abstract description 80
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 75
- 229910052697 platinum Inorganic materials 0.000 claims abstract description 72
- 239000000377 silicon dioxide Substances 0.000 claims abstract description 49
- 238000000354 decomposition reaction Methods 0.000 claims abstract description 40
- 150000001875 compounds Chemical class 0.000 claims abstract description 29
- 150000001299 aldehydes Chemical class 0.000 claims abstract description 26
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 24
- 239000001301 oxygen Substances 0.000 claims abstract description 23
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 23
- 235000014113 dietary fatty acids Nutrition 0.000 claims abstract description 21
- 229930195729 fatty acid Natural products 0.000 claims abstract description 21
- 239000000194 fatty acid Substances 0.000 claims abstract description 21
- 150000004665 fatty acids Chemical class 0.000 claims abstract description 18
- 150000002830 nitrogen compounds Chemical class 0.000 claims abstract description 17
- 229910017464 nitrogen compound Inorganic materials 0.000 claims abstract description 16
- 150000003464 sulfur compounds Chemical class 0.000 claims abstract description 16
- 239000012298 atmosphere Substances 0.000 claims abstract description 14
- 238000000034 method Methods 0.000 claims description 33
- 239000002245 particle Substances 0.000 claims description 17
- 239000011148 porous material Substances 0.000 claims description 17
- 230000001877 deodorizing effect Effects 0.000 claims description 15
- 239000002781 deodorant agent Substances 0.000 claims description 13
- 235000013305 food Nutrition 0.000 claims description 12
- 239000003039 volatile agent Substances 0.000 claims description 11
- 238000002441 X-ray diffraction Methods 0.000 claims description 7
- 239000003755 preservative agent Substances 0.000 claims description 6
- 235000013361 beverage Nutrition 0.000 claims description 5
- 241000251468 Actinopterygii Species 0.000 abstract description 4
- 235000013372 meat Nutrition 0.000 abstract description 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 24
- LSDPWZHWYPCBBB-UHFFFAOYSA-N Methanethiol Chemical compound SC LSDPWZHWYPCBBB-UHFFFAOYSA-N 0.000 description 24
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 18
- 239000002994 raw material Substances 0.000 description 16
- GETQZCLCWQTVFV-UHFFFAOYSA-N trimethylamine Chemical compound CN(C)C GETQZCLCWQTVFV-UHFFFAOYSA-N 0.000 description 16
- 239000007789 gas Substances 0.000 description 13
- 239000000463 material Substances 0.000 description 12
- 229910052757 nitrogen Inorganic materials 0.000 description 12
- IKHGUXGNUITLKF-UHFFFAOYSA-N Acetaldehyde Chemical compound CC=O IKHGUXGNUITLKF-UHFFFAOYSA-N 0.000 description 10
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 9
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 9
- 229910021529 ammonia Inorganic materials 0.000 description 9
- 230000015556 catabolic process Effects 0.000 description 9
- 238000006731 degradation reaction Methods 0.000 description 9
- 229920006267 polyester film Polymers 0.000 description 9
- 239000012495 reaction gas Substances 0.000 description 9
- 230000000052 comparative effect Effects 0.000 description 8
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 6
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 6
- 239000002904 solvent Substances 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 238000001179 sorption measurement Methods 0.000 description 5
- 238000002336 sorption--desorption measurement Methods 0.000 description 5
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 description 4
- 239000007864 aqueous solution Substances 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 4
- -1 fatty acid salt Chemical class 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 239000000243 solution Substances 0.000 description 4
- 238000004438 BET method Methods 0.000 description 3
- 238000003775 Density Functional Theory Methods 0.000 description 3
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 3
- ZMANZCXQSJIPKH-UHFFFAOYSA-N Triethylamine Chemical compound CCN(CC)CC ZMANZCXQSJIPKH-UHFFFAOYSA-N 0.000 description 3
- IKHGUXGNUITLKF-XPULMUKRSA-N acetaldehyde Chemical compound [14CH]([14CH3])=O IKHGUXGNUITLKF-XPULMUKRSA-N 0.000 description 3
- 239000002253 acid Substances 0.000 description 3
- ZTQSAGDEMFDKMZ-UHFFFAOYSA-N butyric aldehyde Natural products CCCC=O ZTQSAGDEMFDKMZ-UHFFFAOYSA-N 0.000 description 3
- 239000001569 carbon dioxide Substances 0.000 description 3
- 229910002092 carbon dioxide Inorganic materials 0.000 description 3
- 239000003054 catalyst Substances 0.000 description 3
- 230000003197 catalytic effect Effects 0.000 description 3
- 239000002131 composite material Substances 0.000 description 3
- 230000007423 decrease Effects 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 238000005259 measurement Methods 0.000 description 3
- 239000011941 photocatalyst Substances 0.000 description 3
- 238000012643 polycondensation polymerization Methods 0.000 description 3
- 239000000843 powder Substances 0.000 description 3
- 238000000634 powder X-ray diffraction Methods 0.000 description 3
- 238000002360 preparation method Methods 0.000 description 3
- 239000004094 surface-active agent Substances 0.000 description 3
- FERIUCNNQQJTOY-UHFFFAOYSA-N Butyric acid Chemical compound CCCC(O)=O FERIUCNNQQJTOY-UHFFFAOYSA-N 0.000 description 2
- QUSNBJAOOMFDIB-UHFFFAOYSA-N Ethylamine Chemical compound CCN QUSNBJAOOMFDIB-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- 229910002651 NO3 Inorganic materials 0.000 description 2
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 2
- NBBJYMSMWIIQGU-UHFFFAOYSA-N Propionic aldehyde Chemical compound CCC=O NBBJYMSMWIIQGU-UHFFFAOYSA-N 0.000 description 2
- 239000004115 Sodium Silicate Substances 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 2
- 125000000217 alkyl group Chemical group 0.000 description 2
- 125000005211 alkyl trimethyl ammonium group Chemical group 0.000 description 2
- IXSUHTFXKKBBJP-UHFFFAOYSA-L azanide;platinum(2+);dinitrite Chemical compound [NH2-].[NH2-].[Pt+2].[O-]N=O.[O-]N=O IXSUHTFXKKBBJP-UHFFFAOYSA-L 0.000 description 2
- 239000000969 carrier Substances 0.000 description 2
- XBDQKXXYIPTUBI-UHFFFAOYSA-N dimethylselenoniopropionate Natural products CCC(O)=O XBDQKXXYIPTUBI-UHFFFAOYSA-N 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 239000001307 helium Substances 0.000 description 2
- 229910052734 helium Inorganic materials 0.000 description 2
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 2
- JARKCYVAAOWBJS-UHFFFAOYSA-N hexanal Chemical compound CCCCCC=O JARKCYVAAOWBJS-UHFFFAOYSA-N 0.000 description 2
- FUZZWVXGSFPDMH-UHFFFAOYSA-N hexanoic acid Chemical compound CCCCCC(O)=O FUZZWVXGSFPDMH-UHFFFAOYSA-N 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- BDAGIHXWWSANSR-UHFFFAOYSA-N methanoic acid Natural products OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- BSAIUMLZVGUGKX-UHFFFAOYSA-N non-2-enal Chemical compound CCCCCCC=CC=O BSAIUMLZVGUGKX-UHFFFAOYSA-N 0.000 description 2
- 239000003960 organic solvent Substances 0.000 description 2
- 238000006864 oxidative decomposition reaction Methods 0.000 description 2
- 238000006068 polycondensation reaction Methods 0.000 description 2
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 description 2
- 229910052911 sodium silicate Inorganic materials 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 2
- NQPDZGIKBAWPEJ-UHFFFAOYSA-N valeric acid Chemical compound CCCCC(O)=O NQPDZGIKBAWPEJ-UHFFFAOYSA-N 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- 239000011787 zinc oxide Substances 0.000 description 2
- OSWFIVFLDKOXQC-UHFFFAOYSA-N 4-(3-methoxyphenyl)aniline Chemical compound COC1=CC=CC(C=2C=CC(N)=CC=2)=C1 OSWFIVFLDKOXQC-UHFFFAOYSA-N 0.000 description 1
- 241000894006 Bacteria Species 0.000 description 1
- 208000031872 Body Remains Diseases 0.000 description 1
- CPELXLSAUQHCOX-UHFFFAOYSA-M Bromide Chemical compound [Br-] CPELXLSAUQHCOX-UHFFFAOYSA-M 0.000 description 1
- WKBOTKDWSSQWDR-UHFFFAOYSA-N Bromine atom Chemical compound [Br] WKBOTKDWSSQWDR-UHFFFAOYSA-N 0.000 description 1
- 102000004190 Enzymes Human genes 0.000 description 1
- 108090000790 Enzymes Proteins 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- PIICEJLVQHRZGT-UHFFFAOYSA-N Ethylenediamine Chemical compound NCCN PIICEJLVQHRZGT-UHFFFAOYSA-N 0.000 description 1
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerol Natural products OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 1
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical group [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 description 1
- 229920003171 Poly (ethylene oxide) Polymers 0.000 description 1
- BOTDANWDWHJENH-UHFFFAOYSA-N Tetraethyl orthosilicate Chemical compound CCO[Si](OCC)(OCC)OCC BOTDANWDWHJENH-UHFFFAOYSA-N 0.000 description 1
- 235000011054 acetic acid Nutrition 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- 230000000274 adsorptive effect Effects 0.000 description 1
- 125000003172 aldehyde group Chemical group 0.000 description 1
- 229910001508 alkali metal halide Inorganic materials 0.000 description 1
- 150000008045 alkali metal halides Chemical class 0.000 description 1
- 125000005210 alkyl ammonium group Chemical group 0.000 description 1
- 150000008052 alkyl sulfonates Chemical class 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 150000001412 amines Chemical class 0.000 description 1
- 125000000129 anionic group Chemical group 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- XKXHCNPAFAXVRZ-UHFFFAOYSA-N benzylazanium;chloride Chemical compound [Cl-].[NH3+]CC1=CC=CC=C1 XKXHCNPAFAXVRZ-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 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
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 description 1
- 238000007084 catalytic combustion reaction Methods 0.000 description 1
- 125000002091 cationic group Chemical group 0.000 description 1
- 239000011362 coarse particle Substances 0.000 description 1
- MLUCVPSAIODCQM-NSCUHMNNSA-N crotonaldehyde Chemical compound C\C=C\C=O MLUCVPSAIODCQM-NSCUHMNNSA-N 0.000 description 1
- MLUCVPSAIODCQM-UHFFFAOYSA-N crotonaldehyde Natural products CC=CC=O MLUCVPSAIODCQM-UHFFFAOYSA-N 0.000 description 1
- 238000004332 deodorization Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- DNJIEGIFACGWOD-UHFFFAOYSA-N ethyl mercaptane Natural products CCS DNJIEGIFACGWOD-UHFFFAOYSA-N 0.000 description 1
- 230000004133 fatty acid degradation Effects 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 235000019253 formic acid Nutrition 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 235000011187 glycerol Nutrition 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- XMBWDFGMSWQBCA-UHFFFAOYSA-N hydrogen iodide Chemical compound I XMBWDFGMSWQBCA-UHFFFAOYSA-N 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 1
- 230000005764 inhibitory process Effects 0.000 description 1
- 229910010272 inorganic material Inorganic materials 0.000 description 1
- 239000011147 inorganic material Substances 0.000 description 1
- 230000001678 irradiating effect Effects 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 239000002905 metal composite material Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- WSFSSNUMVMOOMR-NJFSPNSNSA-N methanone Chemical compound O=[14CH2] WSFSSNUMVMOOMR-NJFSPNSNSA-N 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000002736 nonionic surfactant Substances 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 235000005985 organic acids Nutrition 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- MUMZUERVLWJKNR-UHFFFAOYSA-N oxoplatinum Chemical compound [Pt]=O MUMZUERVLWJKNR-UHFFFAOYSA-N 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 150000003058 platinum compounds Chemical class 0.000 description 1
- CLSUSRZJUQMOHH-UHFFFAOYSA-L platinum dichloride Chemical compound Cl[Pt]Cl CLSUSRZJUQMOHH-UHFFFAOYSA-L 0.000 description 1
- 229910003446 platinum oxide Inorganic materials 0.000 description 1
- NFOHLBHARAZXFQ-UHFFFAOYSA-L platinum(2+);dihydroxide Chemical compound O[Pt]O NFOHLBHARAZXFQ-UHFFFAOYSA-L 0.000 description 1
- 229920000233 poly(alkylene oxides) Polymers 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 235000019260 propionic acid Nutrition 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- IUVKMZGDUIUOCP-BTNSXGMBSA-N quinbolone Chemical compound O([C@H]1CC[C@H]2[C@H]3[C@@H]([C@]4(C=CC(=O)C=C4CC3)C)CC[C@@]21C)C1=CCCC1 IUVKMZGDUIUOCP-BTNSXGMBSA-N 0.000 description 1
- 239000011541 reaction mixture Substances 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 229910052814 silicon oxide Inorganic materials 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- 235000021055 solid food Nutrition 0.000 description 1
- 239000012265 solid product Substances 0.000 description 1
- LFQCEHFDDXELDD-UHFFFAOYSA-N tetramethyl orthosilicate Chemical compound CO[Si](OC)(OC)OC LFQCEHFDDXELDD-UHFFFAOYSA-N 0.000 description 1
- ZQZCOBSUOFHDEE-UHFFFAOYSA-N tetrapropyl silicate Chemical compound CCCO[Si](OCCC)(OCCC)OCCC ZQZCOBSUOFHDEE-UHFFFAOYSA-N 0.000 description 1
- 229920000428 triblock copolymer Polymers 0.000 description 1
- 229940005605 valeric acid Drugs 0.000 description 1
- HGBOYTHUEUWSSQ-UHFFFAOYSA-N valeric aldehyde Natural products CCCCC=O HGBOYTHUEUWSSQ-UHFFFAOYSA-N 0.000 description 1
- 239000012855 volatile organic compound Substances 0.000 description 1
- DGVVWUTYPXICAM-UHFFFAOYSA-N β‐Mercaptoethanol Chemical compound OCCS DGVVWUTYPXICAM-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L3/00—Preservation of foods or foodstuffs, in general, e.g. pasteurising, sterilising, specially adapted for foods or foodstuffs
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
- A61L9/00—Disinfection, sterilisation or deodorisation of air
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
- A61L9/00—Disinfection, sterilisation or deodorisation of air
- A61L9/01—Deodorant compositions
-
- 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
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- 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
- B01J29/00—Catalysts comprising molecular sieves
- B01J29/03—Catalysts comprising molecular sieves not having base-exchange properties
- B01J29/035—Microporous crystalline materials not having base exchange properties, such as silica polymorphs, e.g. silicalites
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- 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
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- B01J35/30—
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- B01J35/60—
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B60—VEHICLES IN GENERAL
- B60H—ARRANGEMENTS OF HEATING, COOLING, VENTILATING OR OTHER AIR-TREATING DEVICES SPECIALLY ADAPTED FOR PASSENGER OR GOODS SPACES OF VEHICLES
- B60H3/00—Other air-treating devices
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65D—CONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
- B65D81/00—Containers, packaging elements, or packages, for contents presenting particular transport or storage problems, or adapted to be used for non-packaging purposes after removal of contents
- B65D81/24—Adaptations for preventing deterioration or decay of contents; Applications to the container or packaging material of food preservatives, fungicides, pesticides or animal repellants
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65D—CONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
- B65D81/00—Containers, packaging elements, or packages, for contents presenting particular transport or storage problems, or adapted to be used for non-packaging purposes after removal of contents
- B65D81/24—Adaptations for preventing deterioration or decay of contents; Applications to the container or packaging material of food preservatives, fungicides, pesticides or animal repellants
- B65D81/28—Applications of food preservatives, fungicides, pesticides or animal repellants
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65D—CONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
- B65D85/00—Containers, packaging elements or packages, specially adapted for particular articles or materials
- B65D85/50—Containers, packaging elements or packages, specially adapted for particular articles or materials for living organisms, articles or materials sensitive to changes of environment or atmospheric conditions, e.g. land animals, birds, fish, water plants, non-aquatic plants, flower bulbs, cut flowers or foliage
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B60—VEHICLES IN GENERAL
- B60H—ARRANGEMENTS OF HEATING, COOLING, VENTILATING OR OTHER AIR-TREATING DEVICES SPECIALLY ADAPTED FOR PASSENGER OR GOODS SPACES OF VEHICLES
- B60H3/00—Other air-treating devices
- B60H3/06—Filtering
- B60H2003/0675—Photocatalytic filters
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B60—VEHICLES IN GENERAL
- B60H—ARRANGEMENTS OF HEATING, COOLING, VENTILATING OR OTHER AIR-TREATING DEVICES SPECIALLY ADAPTED FOR PASSENGER OR GOODS SPACES OF VEHICLES
- B60H3/00—Other air-treating devices
- B60H3/06—Filtering
- B60H2003/0691—Adsorption filters, e.g. activated carbon
Abstract
多孔質シリカに白金又は白金含有化合物を担持させてなる臭気物質の分解剤であって、前記臭気物質が、アルデヒド類、脂肪酸類、硫黄化合物、及び窒素化合物から選択される少なくとも1種の揮発性化合物を含み、酸素の存在下、80〜−40℃の雰囲気下で使用される、分解剤。本発明は、魚や肉から放出される揮発性の臭気物質などの分解において有用である。An agent for decomposing odorous substances in which platinum or a platinum-containing compound is supported on porous silica, wherein the odorous substance is at least one volatile selected from aldehydes, fatty acids, sulfur compounds, and nitrogen compounds. A decomposition agent comprising a compound and used in an atmosphere of 80 to -40 ° C in the presence of oxygen. The present invention is useful in decomposing volatile odorous substances released from fish and meat.
Description
本発明は、臭気物質の分解剤、消臭剤、鮮度保持剤、及びこれらを備えた物品に関する。 The present invention relates to an odor substance decomposing agent, a deodorizing agent, a freshness keeping agent, and an article provided with these.
近年、硫黄化合物、窒素化合物、アルデヒド、炭化水素、低級脂肪酸など、様々な臭気物質が問題となっている。例えば、飲食品の輸送や保存に際しては、魚、肉等の鮮度低下に伴い、アセトアルデヒド、メチルメルカプタン、トリメチルアミンなどの臭気物質が発生することがある。これらの臭気物質の消臭には、活性炭等による吸着や、光触媒を利用した酸化分解などが行われている。 In recent years, various odorous substances such as sulfur compounds, nitrogen compounds, aldehydes, hydrocarbons, and lower fatty acids have become a problem. For example, when transporting and storing food and drink, odorous substances such as acetaldehyde, methyl mercaptan, and trimethylamine may be generated as the freshness of fish and meat decreases. In order to deodorize these odorous substances, adsorption by activated carbon or oxidative decomposition using a photocatalyst is performed.
特許文献1には、活性炭に、臭素、硫酸、およびアルカリ金属ハロゲン化物を均一に担持させてなる下水処理場の脱臭用吸着剤が開示されている。 Patent Document 1 discloses an adsorbent for deodorization in a sewage treatment plant, in which bromine, sulfuric acid, and alkali metal halide are uniformly supported on activated carbon.
特許文献2には、基材上に、酸化チタンおよび酸化亜鉛の少なくとも2種の光触媒粒子を含有する層が形成されており、前記酸化チタンの50%粒子径よりも酸化亜鉛の50%粒子径のほうが大きいことを特徴とする室内空間用脱臭材が開示されている。 In Patent Document 2, a layer containing at least two kinds of photocatalyst particles of titanium oxide and zinc oxide is formed on a base material, and the 50% particle diameter of zinc oxide is larger than the 50% particle diameter of the titanium oxide. An indoor space deodorizing material characterized in that is larger is disclosed.
しかしながら、特許文献1記載の発明は、吸着能が経時的に低下してしまい、長期間の使用が困難である。特許文献2記載の発明は、光を照射する装置が必要であるため、簡易にその実施をすることができず、また、臭気物質の分解能も十分なものではない。 However, in the invention described in Patent Document 1, the adsorptive capacity decreases with time and is difficult to use for a long time. The invention described in Patent Document 2 requires a device for irradiating light, and therefore cannot be easily implemented, and the resolution of odorous substances is not sufficient.
本発明の課題は、簡易に使用することができ、優れた分解能を有する、臭気物質の分解剤及び該分解剤を用いた分解方法、消臭剤及び該消臭剤を用いた消臭方法、飲食品の鮮度保持剤及び該鮮度保持剤を用いた飲食品の鮮度保持方法、並びにこれらを備えた物品を提供することである。 The subject of the present invention is an odor substance decomposing agent, a decomposing method using the decomposing agent, a deodorizing agent and a deodorizing method using the deodorizing agent, which can be used easily and has an excellent resolution. It is providing the freshness preservation agent of food-drinks, the freshness-keeping method of food-drinks using this freshness-keeping agent, and articles | goods provided with these.
本発明は、
[1]多孔質シリカに白金又は白金含有化合物を担持させてなる臭気物質の分解剤であって、前記臭気物質が、アルデヒド類、脂肪酸類、硫黄化合物、及び窒素化合物から選択される少なくとも1種の揮発性化合物を含み、酸素の存在下、80〜−40℃の雰囲気下で使用される、分解剤、
[2]臭気物質と[1]記載の分解剤とを、酸素の存在下、80〜−40℃の雰囲気下で接触させて、前記臭気物質を分解する方法であって、前記臭気物質が、アルデヒド類、脂肪酸類、硫黄化合物、及び窒素化合物から選択される少なくとも1種の揮発性化合物を含む、分解方法、
[3]多孔質シリカに白金又は白金含有化合物を担持させてなる、臭気物質を分解する消臭剤であって、前記臭気物質が、アルデヒド類、脂肪酸類、硫黄化合物、及び窒素化合物から選択される少なくとも1種の揮発性化合物を含み、酸素の存在下、80〜−40℃の雰囲気下で使用される、消臭剤、
[4]臭気物質と[3]記載の消臭剤とを、酸素の存在下、80〜−40℃の雰囲気下で接触させて、前記臭気物質を分解して消臭する方法であって、前記臭気物質が、アルデヒド類、脂肪酸類、硫黄化合物、及び窒素化合物から選択される少なくとも1種の揮発性化合物を含む、消臭方法、
[5]多孔質シリカに白金又は白金含有化合物を担持させてなる、臭気物質を分解する飲食品又は花卉の鮮度保持剤であって、前記臭気物質が、アルデヒド類、脂肪酸類、硫黄化合物、及び窒素化合物から選択される少なくとも1種の揮発性化合物を含み、酸素の存在下、80〜−40℃の雰囲気下で使用される、鮮度保持剤、
[6]臭気物質と[5]記載の鮮度保持剤とを、酸素の存在下、80〜−40℃の雰囲気下で接触させて、前記臭気物質を分解して飲食品又は花卉の鮮度を保持する方法であって、前記臭気物質が、アルデヒド類、脂肪酸類、硫黄化合物、及び窒素化合物から選択される少なくとも1種の揮発性化合物を含む、鮮度保持方法、及び
[7][1]記載の分解剤、[3]記載の消臭剤、又は[5]記載の鮮度保持剤を備える、物品、に関する。The present invention
[1] An odor substance decomposing agent comprising platinum or a platinum-containing compound supported on porous silica, wherein the odor substance is selected from aldehydes, fatty acids, sulfur compounds, and nitrogen compounds. A decomposing agent used in an atmosphere of 80 to −40 ° C. in the presence of oxygen,
[2] A method of decomposing the odorous substance by bringing the odorous substance and the decomposing agent according to [1] into contact with each other in the presence of oxygen in an atmosphere of 80 to −40 ° C. A decomposition method comprising at least one volatile compound selected from aldehydes, fatty acids, sulfur compounds, and nitrogen compounds;
[3] A deodorant for decomposing odorous substances, comprising platinum or a platinum-containing compound supported on porous silica, wherein the odorous substances are selected from aldehydes, fatty acids, sulfur compounds, and nitrogen compounds. A deodorant, which is used in an atmosphere of 80 to -40 ° C in the presence of oxygen, comprising at least one volatile compound
[4] A method of deodorizing by decomposing the odorous substance by contacting the odorous substance with the deodorant described in [3] in an atmosphere of 80 to −40 ° C. in the presence of oxygen, The deodorizing method, wherein the odor substance contains at least one volatile compound selected from aldehydes, fatty acids, sulfur compounds, and nitrogen compounds,
[5] A freshness-preserving agent for foods and beverages or flower buds that decomposes odorous substances by supporting platinum or a platinum-containing compound on porous silica, wherein the odorous substances are aldehydes, fatty acids, sulfur compounds, and A freshness-preserving agent comprising at least one volatile compound selected from nitrogen compounds and used in an atmosphere of 80 to -40 ° C in the presence of oxygen,
[6] The odorous substance and the freshness-preserving agent according to [5] are brought into contact with each other in the presence of oxygen in an atmosphere of 80 to -40 ° C to decompose the odorous substance and maintain the freshness of the food or drink or the floret. A method for maintaining freshness, wherein the odor substance includes at least one volatile compound selected from aldehydes, fatty acids, sulfur compounds, and nitrogen compounds, and
[7] An article comprising the decomposing agent according to [1], the deodorizing agent according to [3], or the freshness maintaining agent according to [5].
本発明によれば、簡易に使用することができ、優れた分解能を有する、臭気物質の分解剤及び該分解剤を用いた分解方法、消臭剤及び該消臭剤を用いた消臭方法、飲食品の鮮度保持剤及び該鮮度保持剤を用いた飲食品の鮮度保持方法、並びにこれらを備えた物品を提供することができる。 According to the present invention, an odorous substance decomposing agent that can be used easily and has an excellent resolution, a decomposing method using the decomposing agent, a deodorizing agent, and a deodorizing method using the deodorizing agent, A freshness-preserving agent for foods and beverages, a method for keeping freshness of foods and beverages using the freshness-keeping agent, and articles equipped with these can be provided.
活性炭等による吸着や、光触媒を利用した酸化分解以外の消臭方法として、白金触媒などを使用する触媒燃焼法が挙げられる。この方法により150〜350℃の高温下において、特定の臭気物質(例えば、アセトアルデヒド、メチルメルカプタン、トリメチルアミンなどの揮発性有機化合物)を酸化分解し得ることが知られている。しかし、白金触媒などを使用して、低温下においてこれらを分解する技術は知られていない。 As a deodorizing method other than adsorption by activated carbon or the like and oxidative decomposition using a photocatalyst, a catalytic combustion method using a platinum catalyst or the like can be mentioned. It is known that specific odorous substances (for example, volatile organic compounds such as acetaldehyde, methyl mercaptan, and trimethylamine) can be oxidatively decomposed at a high temperature of 150 to 350 ° C. by this method. However, a technique for decomposing these at a low temperature using a platinum catalyst or the like is not known.
ところが、前記の課題解決について検討したところ、特定の臭気物質と、多孔質シリカに白金又は白金含有化合物を担持させたものとを接触させると、驚くべきことに、150℃未満の温度(例えば、室温や、−40℃のような低温下)においても、これらの臭気物質を分解できることを新たに見出した。 However, when the above-mentioned problem solution was examined, when a specific odor substance was brought into contact with a porous silica carrying platinum or a platinum-containing compound, surprisingly, a temperature of less than 150 ° C. (for example, It has been newly found that these odorous substances can be decomposed even at room temperature or at a low temperature such as −40 ° C.
本発明者らは、かかる知見に基づき鋭意研究を重ねて、本発明を完成するに至った。 The inventors of the present invention have made extensive studies based on such knowledge and have completed the present invention.
本発明の一態様として、臭気物質の分解剤が挙げられる。この分解剤は、多孔質シリカに白金又は白金含有化合物を担持させてなる。 As one embodiment of the present invention, a decomposing agent for odorous substances can be given. This decomposing agent is formed by supporting platinum or a platinum-containing compound on porous silica.
本発明の一態様として、臭気物質と、多孔質シリカに白金又は白金含有化合物を担持させてなる分解剤とを接触させて、臭気物質を分解する方法が挙げられる。これにより、臭気物質を除去することができる。 As one embodiment of the present invention, a method of decomposing an odorous substance by bringing a odorous substance into contact with a decomposing agent obtained by supporting platinum or a platinum-containing compound on porous silica can be mentioned. Thereby, an odor substance can be removed.
この分解剤及び分解方法は、臭気物質を分解すると有益となる種々の用途に使用することができる。 This decomposing agent and decomposing method can be used in various applications where it is beneficial to decompose odorous substances.
本発明の一態様として、臭気物質を分解する消臭剤が挙げられる。この消臭剤は、多孔質シリカに白金又は白金含有化合物を担持させてなる。 As one embodiment of the present invention, a deodorant that decomposes odorous substances can be given. This deodorant is obtained by supporting platinum or a platinum-containing compound on porous silica.
本発明の一態様として、臭気物質と、多孔質シリカに白金又は白金含有化合物を担持させてなる消臭剤とを接触させて、臭気物質を分解して消臭する方法が挙げられる。これにより、臭気物質を除去することができる。 As one embodiment of the present invention, there is a method in which an odor substance is contacted with a deodorant obtained by supporting platinum or a platinum-containing compound on porous silica to decompose and deodorize the odor substance. Thereby, an odor substance can be removed.
この消臭剤及び消臭方法は、特に限定されるものではないが、例えば、飲食品の輸送や保存に際して発生する臭気物質、ゴミから発生する臭気物質、工場から発生する臭気物質、動物の遺体から発生する臭気物質などを分解して消臭することができる。 The deodorant and the deodorizing method are not particularly limited. For example, odorous substances generated during transportation and storage of food and drink, odorous substances generated from garbage, odorous substances generated from factories, animal remains Deodorize by decomposing odorous substances generated from
本発明の一態様として、臭気物質を分解する飲食品等の鮮度保持剤が挙げられる。この鮮度保持剤は、多孔質シリカに白金又は白金含有化合物を担持させてなる。 As one embodiment of the present invention, a freshness-preserving agent such as a food or drink that decomposes odorous substances can be given. This freshness-keeping agent is obtained by supporting platinum or a platinum-containing compound on porous silica.
本発明の一態様として、臭気物質と、多孔質シリカに白金又は白金含有化合物を担持させてなる鮮度保持剤とを接触させて、臭気物質を分解して飲食品又は花卉の鮮度を保持する方法が挙げられる。また、これにより、臭気物質が除去される。 As one embodiment of the present invention, a method for maintaining the freshness of a food or drink or a flower bud by decomposing the odorous substance by bringing the odorous substance into contact with a freshness-keeping agent formed by supporting platinum or a platinum-containing compound on porous silica. Is mentioned. This also removes odorous substances.
この鮮度保持剤及び鮮度保持方法は、特に限定されるものではないが、例えば、飲食品又は花卉の輸送や保存に際して発生する臭気物質を分解して鮮度を保持することができる。なお、飲食品とは、飲料と固形食品の両方を含むものを指す。 The freshness-keeping agent and the freshness-keeping method are not particularly limited. For example, the freshness can be maintained by decomposing odorous substances generated during transportation and storage of food and drink or florets. In addition, food / beverage products refer to what contains both a drink and solid food.
本発明の一態様として、これらの分解剤、消臭剤、鮮度保持剤(以下、「分解剤等」ともいう)を備える、物品が挙げられる。 As one embodiment of the present invention, an article including these decomposing agent, deodorant, and freshness-keeping agent (hereinafter, also referred to as “decomposing agent or the like”) can be given.
この物品としては、特に限定されるものではないが、例えば、袋、容器、フィルター、冷蔵庫、冷凍庫、コンテナ、空調機、車両、船舶、航空機などが挙げられる。 Although it does not specifically limit as this article | item, For example, a bag, a container, a filter, a refrigerator, a freezer, a container, an air conditioner, a vehicle, a ship, an aircraft etc. are mentioned.
例えば、冷蔵庫や冷凍庫の場合、庫内に保存される魚や肉など(被保存物)からメチルメルカプタンやトリメチルアミンなどの臭気物質が発生し、これらは庫内の臭気の原因となる。本態様の冷蔵庫や冷凍庫を使用すれば、庫内の被保存物から発生する臭気物質を分解するため、臭気を低減することができる。 For example, in the case of a refrigerator or freezer, odorous substances such as methyl mercaptan and trimethylamine are generated from fish and meat (stored objects) stored in the refrigerator, and these cause odor in the refrigerator. If the refrigerator and freezer of this aspect are used, the odor substance generated from the material to be stored in the warehouse is decomposed, so that the odor can be reduced.
また、被保存物に、臭気物質の分解時に生じる炭酸ガスを作用させるなどして被保存物の表面を弱酸性にすると、タンパク質を分解する酵素などの働きを抑えることや、細菌類の増加を抑えることにより鮮度を維持することができる。しかし、被保存物の周囲に臭気物質がある程度残存していると、被保存物に炭酸ガスを作用させることが臭気物質により阻害され、鮮度維持が困難となる。本態様の冷蔵庫や冷凍庫を使用すれば、臭気物質の分解能が高いため、この臭気物質による阻害が少なく、好適に被保存物の鮮度を維持することができる。 In addition, if the surface of the object to be preserved is made weakly acidic by, for example, causing carbon dioxide gas generated during the decomposition of odorous substances to the object to be preserved, it can suppress the action of enzymes that degrade proteins and increase the number of bacteria. The freshness can be maintained by suppressing. However, if some odorous substance remains around the object to be preserved, the action of carbon dioxide gas on the object to be preserved is inhibited by the odorous substance, making it difficult to maintain freshness. If the refrigerator or freezer of this aspect is used, since the resolution of the odorous substance is high, there is little inhibition by the odorous substance, and the freshness of the stored object can be suitably maintained.
前記の各態様は、酸素の存在下、80〜−40℃の雰囲気下で使用される。例えば、冷蔵庫の場合には15〜0℃、冷凍庫の場合には−5〜−25℃などで使用されてもよい。 Each of the above embodiments is used in an atmosphere of 80 to -40 ° C in the presence of oxygen. For example, it may be used at 15 to 0 ° C. in the case of a refrigerator and −5 to −25 ° C. in the case of a freezer.
以下、前記各態様における各要素について説明する。 Hereafter, each element in each said aspect is demonstrated.
臭気物質は、アルデヒド類、脂肪酸類、硫黄化合物、及び窒素化合物から選択される少なくとも1種の揮発性化合物を含む。 The odor substance includes at least one volatile compound selected from aldehydes, fatty acids, sulfur compounds, and nitrogen compounds.
アルデヒド類は、アルデヒド基を持つ化合物であれば特に限定するものではないが、ホルムアルデヒド、アセトアルデヒド、プロピオンアルデヒド、ブチルアルデヒド、クロトンアルデヒド、ヘキサナール、ノネナールなどが挙げられる。 The aldehyde is not particularly limited as long as it is a compound having an aldehyde group, and examples include formaldehyde, acetaldehyde, propionaldehyde, butyraldehyde, crotonaldehyde, hexanal, nonenal and the like.
脂肪酸類は、カルボキシ基を持つ鎖状の有機酸であれば特に限定するものではないが、ギ酸、酢酸、プロピオン酸、酪酸、吉草酸、カプロン酸などが挙げられる。 Fatty acids are not particularly limited as long as they are chain-like organic acids having a carboxy group, and examples include formic acid, acetic acid, propionic acid, butyric acid, valeric acid, and caproic acid.
硫黄化合物は、メチルメルカプタン,メルカプトエタノールなどが挙げられる。 Examples of the sulfur compound include methyl mercaptan and mercaptoethanol.
窒素化合物は、トリメチルアミン、トリエチルアミン、エチルアミン、エチレンジアミン、アンモニアなどが挙げられる。 Examples of the nitrogen compound include trimethylamine, triethylamine, ethylamine, ethylenediamine, and ammonia.
本明細書において多孔質シリカとは、多孔質構造を持つケイ素酸化物を主成分とする物質を意味する。 In this specification, the porous silica means a substance mainly composed of silicon oxide having a porous structure.
多孔質シリカの平均細孔直径は、分解反応の進行を促進する観点から、0.5nm以上が好ましく、白金を粒子状で担持する観点から、15nm以下が好ましい。これらの観点から、多孔質シリカの平均細孔直径は、好ましくは0.5〜15nm、より好ましくは0.5〜10nm、さらに好ましくは0.5〜7nm、さらに好ましくは0.5〜5nmである。本明細書における多孔質シリカの平均細孔直径は、窒素吸脱着によるNL−DFT法により算出することができる。 The average pore diameter of the porous silica is preferably 0.5 nm or more from the viewpoint of promoting the progress of the decomposition reaction, and preferably 15 nm or less from the viewpoint of supporting platinum in the form of particles. From these viewpoints, the average pore diameter of the porous silica is preferably 0.5 to 15 nm, more preferably 0.5 to 10 nm, still more preferably 0.5 to 7 nm, still more preferably 0.5 to 5 nm. is there. The average pore diameter of the porous silica in this specification can be calculated by the NL-DFT method by nitrogen adsorption / desorption.
多孔質シリカの比表面積は、白金の担持量を高める観点から、300m2/g以上が好ましく、製造が実現可能である観点から、2000m2/g以下が好ましい。これらの観点から、多孔質シリカの比表面積は、好ましくは300〜2000m2/g、より好ましくは600〜1500m2/gである。本明細書における多孔質シリカの比表面積は、窒素吸脱着によるBET法により算出することができる。The specific surface area of the porous silica is preferably 300 m 2 / g or more from the viewpoint of increasing the supported amount of platinum, and preferably 2000 m 2 / g or less from the viewpoint of realizing the production. From these viewpoints, the specific surface area of the porous silica is preferably 300 to 2000 m 2 / g, more preferably 600 to 1500 m 2 / g. The specific surface area of the porous silica in this specification can be calculated by the BET method based on nitrogen adsorption / desorption.
さらに、多孔質シリカは、X線回折のd間隔が2.0nmより大きい位置に少なくとも1つのピークを有することが好ましい。X線回折ピークは、そのピーク角度に相当するd値の周期構造が試料中にあることを意味する。従って、2.0nm以上のd値に相当する回折角度に1本以上のピークがあることは、細孔が2.0nm以上の間隔で規則的に配列していることを意味する。このように規則的に配列した細孔をもつ多孔質シリカを、本明細書においては、メソポーラスシリカともいう。d間隔は、好ましくは2.0〜25nm、より好ましくは3.0〜20nmである。多孔質シリカのX線回折パターンは粉末X線回折装置により測定することができる。 Furthermore, the porous silica preferably has at least one peak at a position where the d-spacing of X-ray diffraction is larger than 2.0 nm. The X-ray diffraction peak means that there is a periodic structure having a d value corresponding to the peak angle in the sample. Therefore, the presence of one or more peaks at the diffraction angle corresponding to a d value of 2.0 nm or more means that the pores are regularly arranged at intervals of 2.0 nm or more. Such porous silica having regularly arranged pores is also referred to as mesoporous silica in the present specification. The d interval is preferably 2.0 to 25 nm, more preferably 3.0 to 20 nm. The X-ray diffraction pattern of porous silica can be measured by a powder X-ray diffractometer.
多孔質シリカの製造方法としては、特に限定されるものではないが、例えば次のようにして製造できる。まず、無機原料と有機原料を混合し、反応させることにより、有機物を鋳型としてそのまわりに無機物の骨格が形成された有機物と無機物の複合体を形成させる。次いで、得られた複合体から有機物を除去することにより、多孔質シリカが得られる。 Although it does not specifically limit as a manufacturing method of porous silica, For example, it can manufacture as follows. First, an inorganic raw material and an organic raw material are mixed and reacted to form an organic matter-inorganic matter composite in which an inorganic matter skeleton is formed around the organic matter as a template. Subsequently, porous silica is obtained by removing organic substances from the obtained composite.
無機原料としては、テトラメトキシシラン、テトラエトキシシラン、テトラプロポキシシラン等のアルコキシシラン、ケイ酸ソーダ、カネマイト(kanemite、NaHSi2O5・3H2O)、シリカ、シリカ−金属複合酸化物等が挙げられる。これらの無機原料はシリケート骨格を形成する。これらは、単独で又は2種以上を混合して用いることができる。As the inorganic material, tetramethoxysilane, tetraethoxysilane, alkoxysilane, such as tetra propoxy silane, sodium silicate, kanemite (kanemite, NaHSi 2 O 5 · 3H 2 O), silica, silica - like metal composite oxide and the like It is done. These inorganic raw materials form a silicate skeleton. These can be used alone or in admixture of two or more.
鋳型として使用される有機原料は、特に限定されるものではないが、例えば界面活性剤等が挙げられる。界面活性剤は陽イオン性、陰イオン性、非イオン性のうちのいずれであってもよく、具体的には、アルキルトリメチルアンモニウム(好ましくはアルキル基の炭素数が8〜18のアルキルトリメチルアンモニウム)、アルキルアンモニウム、ジアルキルジメチルアンモニウム、ベンジルアンモニウムの塩化物、臭化物、ヨウ化物又は水酸化物の他、脂肪酸塩、アルキルスルホン酸塩、アルキルリン酸塩、ポリエチレンオキサイド系非イオン性界面活性剤、一級アルキルアミン、トリブロックコポリマー型のポリアルキレンオキサイド、グリセリン脂肪酸エステル、ポリグリセリン脂肪酸エステル等が挙げられる。これらは、単独で又は2種以上を混合して用いることができる。 Although the organic raw material used as a casting_mold | template is not specifically limited, For example, surfactant etc. are mentioned. The surfactant may be any of cationic, anionic, and nonionic, specifically, alkyltrimethylammonium (preferably alkyltrimethylammonium having an alkyl group having 8 to 18 carbon atoms). , Alkylammonium, dialkyldimethylammonium, benzylammonium chloride, bromide, iodide or hydroxide, fatty acid salt, alkylsulfonate, alkylphosphate, polyethylene oxide nonionic surfactant, primary alkyl Examples include amines, triblock copolymer type polyalkylene oxides, glycerin fatty acid esters, and polyglycerin fatty acid esters. These can be used alone or in admixture of two or more.
無機原料と有機原料を混合する場合、適当な溶媒を用いることができる。溶媒としては、特に限定されるものではないが、例えば水、有機溶媒、水と有機溶媒との混合物等が挙げられる。 When mixing an inorganic raw material and an organic raw material, a suitable solvent can be used. Although it does not specifically limit as a solvent, For example, water, an organic solvent, the mixture of water and an organic solvent, etc. are mentioned.
無機物と有機物の複合体の形成方法は、特に限定されるものではないが、例えば、有機原料を溶媒に溶解後、無機原料を添加し、所定のpHに調製した後に、反応混合物を所定の温度に保持して縮重合反応を行う方法が挙げられる。縮重合反応の反応温度は使用する有機原料や無機原料の種類や濃度によって異なるが、0〜100℃程度が好ましく、より好ましくは35〜80℃である。 The formation method of the complex of the inorganic substance and the organic substance is not particularly limited. For example, after dissolving the organic raw material in a solvent, adding the inorganic raw material and adjusting to a predetermined pH, the reaction mixture is then heated to a predetermined temperature. And a method in which the condensation polymerization reaction is carried out. The reaction temperature of the polycondensation reaction varies depending on the type and concentration of the organic raw material and inorganic raw material used, but is preferably about 0 to 100 ° C, more preferably 35 to 80 ° C.
縮重合反応の反応時間は、特に限定されるものではないが、1〜24時間が好ましい。また、前記の縮重合反応は、静置状態、撹拌状態のいずれで行ってもよく、またそれらを組み合わせて行ってもよい。 The reaction time for the condensation polymerization reaction is not particularly limited, but is preferably 1 to 24 hours. In addition, the above condensation polymerization reaction may be performed either in a stationary state or in a stirring state, or may be performed in combination.
縮重合反応後に得られる複合体から有機原料を除去することによって、多孔質シリカが得られる。有機物と無機物の複合体からの有機物の除去は、400〜800℃で焼成する方法、水やアルコール等の溶媒で処理する方法等の方法により行うことができる。 By removing the organic raw material from the composite obtained after the polycondensation reaction, porous silica can be obtained. The removal of the organic substance from the complex of the organic substance and the inorganic substance can be performed by a method such as a method of baking at 400 to 800 ° C. or a method of treating with a solvent such as water or alcohol.
多孔質シリカは、細孔容積の観点から、細孔が規則的に配列したメソポーラスシリカであることが好ましい。メソポーラスシリカは、例えば、珪酸ソーダを、界面活性剤を含む水溶液中に分散させ、加熱撹拌しながら塩酸を添加して分散液のpHを調整し、得られた固形生成物を洗浄・乾燥した後、400〜800℃程度で焼成することにより得られる。 The porous silica is preferably mesoporous silica in which pores are regularly arranged from the viewpoint of pore volume. For example, mesoporous silica is obtained by dispersing sodium silicate in an aqueous solution containing a surfactant, adding hydrochloric acid while heating and stirring to adjust the pH of the dispersion, and washing and drying the obtained solid product. It is obtained by firing at about 400 to 800 ° C.
多孔質シリカに担持される白金含有化合物としては、塩化白金、酸化白金、水酸化白金、塩化白金酸塩のほかに、その他金属との合金等が挙げられる。 Examples of the platinum-containing compound supported on the porous silica include platinum chloride, platinum oxide, platinum hydroxide, chloroplatinate, and alloys with other metals.
多孔質シリカに担持された白金又は白金含有化合物の粒子は、触媒活性の観点から、好ましくは0.5〜7nmであり、より好ましくは1〜4nmである。 From the viewpoint of catalytic activity, the particles of platinum or platinum-containing compounds supported on porous silica are preferably 0.5 to 7 nm, more preferably 1 to 4 nm.
分解剤等における白金又は白金含有化合物の含有量は、触媒活性の観点から、0.1質量%以上が好ましく、製造コストの観点から、5質量%以下が好ましい。これらの観点から、白金又は白金含有化合物の含有量は、分解剤等中、好ましくは0.1〜5質量%、より好ましくは0.1〜3質量、さらに好ましくは0.1〜2質量%である。 The content of platinum or a platinum-containing compound in the decomposing agent or the like is preferably 0.1% by mass or more from the viewpoint of catalytic activity, and preferably 5% by mass or less from the viewpoint of production cost. From these viewpoints, the content of platinum or the platinum-containing compound is preferably 0.1 to 5% by mass, more preferably 0.1 to 3% by mass, and further preferably 0.1 to 2% by mass in the decomposition agent or the like. It is.
多孔質シリカに白金又は白金含有化合物を担持させた分解剤等は、例えば、白金原子を含む白金化合物、白金錯体等の白金原料と多孔質シリカとの混合物を還元することにより得られる。具体的には、例えば、白金原料を含む水溶液を調製し、多孔質シリカを含浸させ、乾燥した後、還元して、多孔質シリカに白金又は白金含有化合物を担持させた分解剤等を得ることができる。 A decomposition agent or the like in which platinum or a platinum-containing compound is supported on porous silica can be obtained, for example, by reducing a mixture of a platinum raw material such as a platinum compound or platinum complex containing a platinum atom and porous silica. Specifically, for example, an aqueous solution containing a platinum raw material is prepared, impregnated with porous silica, dried, and then reduced to obtain a decomposition agent in which platinum or a platinum-containing compound is supported on porous silica. Can do.
白金原料としては、塩化白金酸、ジニトロジアンミン白金、硝酸テトラアンミン白金等が挙げられる。 Examples of the platinum raw material include chloroplatinic acid, dinitrodiammine platinum, and tetraammineplatinum nitrate.
白金原料を含む水溶液に含浸した多孔質シリカを乾燥させるための温度条件は、特に限定されるものではないが、50〜200℃程度が好ましい。 The temperature condition for drying the porous silica impregnated in the aqueous solution containing the platinum raw material is not particularly limited, but is preferably about 50 to 200 ° C.
還元方法としては、還元剤、熱、光等で処理する方法を用いることができ、白金原料が分解して白金粒子を生成する条件を適宜設定する。過度の処理は生成した白金粒子のシンタリングによる粒子径の増大の可能性があるため、適当な条件の設定が必要である。 As a reduction method, a method of treating with a reducing agent, heat, light, or the like can be used, and conditions for generating platinum particles by decomposition of the platinum raw material are appropriately set. Since excessive treatment may increase the particle diameter due to sintering of the generated platinum particles, it is necessary to set appropriate conditions.
例えば、塩化白金酸を用いた場合、還元剤として水素を使用し、100〜400℃の温度条件下で、処理することが好ましい。 For example, when chloroplatinic acid is used, it is preferable to use hydrogen as a reducing agent and to perform the treatment under a temperature condition of 100 to 400 ° C.
白金又は白金含有化合物は、これらが粒子成長により粗大な粒子となると触媒活性が低下するため、多孔質シリカの細孔外よりも細孔内に担持されていることが好ましい。細孔外に担持(付着)した白金又は白金粒子は、流水等により洗浄除去することができる。 Platinum or platinum-containing compounds are preferably supported in the pores rather than outside the pores of the porous silica because the catalytic activity decreases when these become coarse particles due to particle growth. Platinum or platinum particles supported (attached) outside the pores can be removed by washing with running water or the like.
前記した各態様の分解剤等によれば、従来の金属触媒による臭気物質の分解が、150℃以上の高温下で行われるのが当業者の技術常識であるのに対し、室温や、氷点を下回る温度域でも、臭気物質を分解することができる。 According to the decomposition agent of each aspect described above, the decomposition of odorous substances by a conventional metal catalyst is performed at a high temperature of 150 ° C. or higher, while the technical common knowledge of those skilled in the art is that the room temperature and freezing point are adjusted. The odorous substance can be decomposed even in a temperature range below.
分解剤の調製 実施例1、2
表1に示す担体1.0gを50mLの水に懸濁させ、Pt担持量1.0質量%になるように塩化白金酸水溶液[H2PtCl6 aq.]を滴下し、その水溶液を室温にて一晩撹拌した。エバポレータを用いて50℃に加熱して溶媒を留去し、得られた粉末を60℃で16〜18時間真空乾燥させ、水素ガスを、30mL/minで流通させながら、150℃で2時間の還元処理をすることによって担体に白金を担持させた分解剤を得た。Preparation of decomposition agents Examples 1 and 2
1.0 g of the carrier shown in Table 1 was suspended in 50 mL of water, and an aqueous chloroplatinic acid solution [H 2 PtCl 6 aq. The solution was stirred overnight at room temperature. The solvent is distilled off by heating to 50 ° C. using an evaporator, and the obtained powder is vacuum-dried at 60 ° C. for 16 to 18 hours, and hydrogen gas is circulated at 30 mL / min for 2 hours at 150 ° C. By performing the reduction treatment, a decomposition agent having platinum supported on a carrier was obtained.
分解剤の調製 実施例3
表1に示す担体1.0gを50mLの水に懸濁させ、Pt担持量1.0質量%になるようにジニトロジアンミン白金硝酸水溶液[(NO2)2(NH3)2Pt・HNO3 aq.]を滴下し、その水溶液を室温にて一晩撹拌した。エバポレータを用いて50℃に加熱して溶媒を留去し、得られた粉末を60℃で16〜18時間真空乾燥させ、水素ガスを、30mL/minで流通させながら、300℃で2時間の還元処理をすることによって担体に白金を担持させた分解剤を得た。Preparation of Decomposing Agent Example 3
1.0 g of the carrier shown in Table 1 is suspended in 50 mL of water, and a dinitrodiammineplatinum nitrate aqueous solution [(NO 2 ) 2 (NH 3 ) 2 Pt · HNO 3 aq so that the supported amount of Pt is 1.0 mass%. . The solution was stirred overnight at room temperature. The solvent is distilled off by heating to 50 ° C. using an evaporator, and the obtained powder is vacuum-dried at 60 ° C. for 16 to 18 hours, and hydrogen gas is circulated at 30 mL / min for 2 hours at 300 ° C. By performing the reduction treatment, a decomposition agent having platinum supported on a carrier was obtained.
分解剤の調製 比較例1
表1に示す担体にPtを担持させることなく、そのままのものを分解剤とした。Preparation of decomposition agent Comparative Example 1
The carrier as shown in Table 1 was used as the decomposition agent without supporting Pt.
実施例1〜3及び比較例1で使用した担体の、窒素吸脱着測定より得られた吸着等温線を用いてBET法により比表面積(SBET)及び全細孔容積(Vtot)を、NL−DFT法により平均細孔直径(Dmeso)を得た。結果を表1に示す。The specific surface area (S BET ) and total pore volume (V tot ) of the carriers used in Examples 1 to 3 and Comparative Example 1 were measured by the BET method using the adsorption isotherm obtained from the nitrogen adsorption / desorption measurement. -Average pore diameter (D meso ) was obtained by DFT method. The results are shown in Table 1.
また、各担体の粉末X線回折を行ったところ、いずれも担体も、X線回折のd間隔が実施例1、比較例1で使用した担体は9.4nm、5.8nm、4.9nmに、実施例2、3で使用した担体は4.9nm、2.9nm、2.5nm、1.9nmに、それぞれピークを有していた。 Further, when powder X-ray diffraction was performed on each carrier, the carrier used in Examples 1 and Comparative Example 1 was 9.4 nm, 5.8 nm, and 4.9 nm. The carriers used in Examples 2 and 3 had peaks at 4.9 nm, 2.9 nm, 2.5 nm, and 1.9 nm, respectively.
また、実施例1〜3で得られた分解剤に関してそれぞれ粉末X線回折及び窒素吸脱着測定を行った。粉末X線回折より得られた回折ピークからシェラー式を用いてPt粒子径(結晶子径,DPt)を算出した。また、担体と同様に、窒素吸脱着測定より得られた吸着等温線を用いてBET法により比表面積(SBET)及び全細孔容積(Vtot)を、NL−DFT法により平均細孔直径(Dmeso)を得た。結果を表1に示す。In addition, powder X-ray diffraction and nitrogen adsorption / desorption measurement were performed on the decomposition agents obtained in Examples 1 to 3, respectively. The Pt particle diameter (crystallite diameter, D Pt ) was calculated from the diffraction peak obtained by powder X-ray diffraction using the Scherrer equation. Similarly to the support, the specific surface area (S BET ) and the total pore volume (V tot ) were determined by the BET method using the adsorption isotherm obtained from the nitrogen adsorption / desorption measurement, and the average pore diameter was determined by the NL-DFT method. (D meso ) was obtained. The results are shown in Table 1.
比較例1を除き、いずれの分解剤も、白金担時前後で構造特性に大きな変化が見られなかった。また、いずれの分解剤からもXRDパターンから白金由来の回折ピークが観測された。 Except for Comparative Example 1, none of the decomposition agents showed any significant changes in structural characteristics before and after platinum loading. Moreover, the diffraction peak derived from platinum was observed from the XRD pattern from any of the decomposition agents.
試験例1 アルデヒド分解試験
実施例1〜3で得られた分解剤を用いて下記のアルデヒド分解試験を行った。表2に記載の量のアルデヒド(アセトアルデヒド)を含む反応ガス(アセトアルデヒド濃度、約100ppm;酸素、20体積%;窒素、残部:バランスガス)2.5Lを入れた「におい袋」(袋容量:3L、袋サイズ:250×250mm、材質:ポリエステルフィルム/アズワン株式会社製)に分解剤500mgを投入し、4℃で21時間静置後、におい袋内のヘッドスペースのアルデヒド(アセトアルデヒド)濃度をガス検知管(株式会社ガステック製)にて測定した。結果を表2に示す。Test Example 1 Aldehyde Decomposition Test The following aldehyde decomposition test was performed using the decomposing agents obtained in Examples 1 to 3. “Odor bag” (bag capacity: 3 L, containing 2.5 L of reaction gas (acetaldehyde concentration, about 100 ppm; oxygen, 20% by volume; nitrogen, balance: balance gas) containing aldehyde (acetaldehyde) in the amount shown in Table 2 Bag size: 250 × 250 mm, Material: Polyester film / manufactured by ASONE Co., Ltd.) 500 mg of decomposing agent was introduced and allowed to stand at 4 ° C. for 21 hours. (Measured by Gastec Co., Ltd.). The results are shown in Table 2.
試験例2 アンモニア分解試験
実施例1〜3で得られた分解剤を用いて下記のアンモニア分解試験を行った。表2に記載の量のアンモニアを含む反応ガス(アンモニア濃度、約65ppm;酸素、20体積%;窒素、残部:バランスガス)2.5Lを入れた「におい袋」(袋容量:3L、袋サイズ:250×250mm、材質:ポリエステルフィルム/アズワン株式会社製)に分解剤500mgを投入し、4℃で21時間静置後、におい袋内のヘッドスペースのアンモニア濃度をガス検知管(株式会社ガステック製)にて測定した。結果を表2に示す。Test Example 2 Ammonia decomposition test The following ammonia decomposition test was performed using the decomposition agents obtained in Examples 1 to 3. “Smell bag” (bag capacity: 3 L, bag size :) containing 2.5 L of a reaction gas (ammonia concentration, about 65 ppm; oxygen, 20 vol%; nitrogen, balance: balance gas) containing ammonia in the amount shown in Table 2 250 × 250 mm, material: polyester film / manufactured by ASONE Corporation), 500 mg of decomposing agent is added and left at 4 ° C. for 21 hours. Measured with The results are shown in Table 2.
試験例3 トリメチルアミン分解試験
実施例1〜3で得られた分解剤を用いて下記のトリメチルアミン分解試験を行った。表2に記載の量のトリメチルアミンを含む反応ガス(トリメチルアミン濃度、約3ppm;酸素、20体積%;窒素、残部:バランスガス)2.5Lを入れた「におい袋」(袋容量:3L、袋サイズ:250×250mm、材質:ポリエステルフィルム/アズワン株式会社製)に分解剤500mgを投入し、4℃で21時間静置後、におい袋内のヘッドスペースのトリメチルアミン濃度をガス検知管(株式会社ガステック製)にて測定した。結果を表2に示す。Test Example 3 Trimethylamine degradation test The following trimethylamine degradation test was performed using the degradation agents obtained in Examples 1 to 3. “Smell bag” (bag capacity: 3 L, bag size: 2.5 L) containing 2.5 L of reaction gas (trimethylamine concentration, about 3 ppm; oxygen, 20% by volume; nitrogen, balance: balance gas) containing the amount of trimethylamine described in Table 2 250 × 250 mm, material: polyester film / manufactured by ASONE Corporation), 500 mg of decomposing agent is added and left at 4 ° C. for 21 hours. Measured with The results are shown in Table 2.
試験例4 メチルメルカプタン分解試験
実施例1〜3で得られた分解剤を用いて下記のメチルメルカプタン分解試験を行った。表2に記載の量のメチルメルカプタンを含む反応ガス(メチルメルカプタン濃度、約1.5ppm;酸素、20体積%;窒素、残部:バランスガス)2.5Lを入れた「におい袋」(袋容量:3L、袋サイズ:250×250mm、材質:ポリエステルフィルム/アズワン株式会社製)に分解剤500mgを投入し、4℃で21時間静置後、におい袋内のヘッドスペースのメチルメルカプタン濃度をガス検知管(株式会社ガステック製)にて測定した。結果を表2に示す。Test Example 4 Methyl mercaptan degradation test The following methyl mercaptan degradation test was conducted using the degradation agents obtained in Examples 1 to 3. “Odor bag” (bag capacity: 3 L) containing 2.5 L of reaction gas containing methyl mercaptan in the amount shown in Table 2 (methyl mercaptan concentration, about 1.5 ppm; oxygen, 20 vol%; nitrogen, balance: balance gas) , Bag size: 250 × 250 mm, material: polyester film / manufactured by ASONE Co., Ltd.), 500 mg of decomposing agent was added and left at 4 ° C. for 21 hours. (Measured by Gastech). The results are shown in Table 2.
試験例5 アンモニア分解試験(室温)
実施例1、2で得られた分解剤を用いて下記のアンモニア分解試験を行った。表2に記載の量のアンモニアを含む反応ガス(アンモニア濃度、約50ppm;酸素、20体積%;ヘリウム、残部:バランスガス)2Lを入れた「におい袋」(袋容量:3L、袋サイズ:250×250mm、材質:ポリエステルフィルム/アズワン株式会社製)に分解剤500mgを投入し、25℃で21時間静置後、におい袋内のヘッドスペースのアンモニア濃度をガス検知管(株式会社ガステック製)にて測定した。結果を表2に示す。Test Example 5 Ammonia decomposition test (room temperature)
The following ammonia decomposition tests were conducted using the decomposition agents obtained in Examples 1 and 2. “Smell bag” (bag capacity: 3 L, bag size: 250 ×) containing 2 L of reaction gas (ammonia concentration, about 50 ppm; oxygen, 20 vol%; helium, balance: balance gas) containing ammonia in the amount shown in Table 2 250 mm, material: polyester film / manufactured by ASONE Corporation), 500 mg of decomposition agent was added and allowed to stand at 25 ° C. for 21 hours. It was measured. The results are shown in Table 2.
試験例6 メチルメルカプタン分解試験(室温)
実施例1、2及び比較例1で得られた分解剤を用いて下記のメチルメルカプタン分解試験を行った。表2に記載の量のメチルメルカプタンを含む反応ガス(メチルメルカプタン濃度、約15ppm;酸素、20体積%;ヘリウム、残部:バランスガス)2Lを入れた「におい袋」(袋容量:3L、袋サイズ:250×250mm、材質:ポリエステルフィルム/アズワン株式会社製)に分解剤400mgを投入し、25℃で21時間静置後、におい袋内のヘッドスペースのメチルメルカプタン濃度をガス検知管(株式会社ガステック製)にて測定した。結果を表2に示す。Test Example 6 Methyl mercaptan degradation test (room temperature)
Using the decomposition agents obtained in Examples 1 and 2 and Comparative Example 1, the following methyl mercaptan decomposition test was performed. “Smell bag” containing 2 L of a reaction gas (methyl mercaptan concentration, about 15 ppm; oxygen, 20% by volume; helium, balance: balance gas) containing methyl mercaptan in the amount shown in Table 2 (bag capacity: 3 L, bag size: 400 × 250 mm, material: Polyester film / manufactured by ASONE Corporation), 400 mg of decomposing agent was added and left at 25 ° C. for 21 hours. ). The results are shown in Table 2.
試験例7 脂肪酸分解試験(室温)
実施例1〜3で得られた分解剤を用いて下記の脂肪酸分解試験を行った。表2に記載の量の脂肪酸(酢酸)を含む反応ガス(酢酸濃度、約50ppm;酸素、20体積%;窒素、残部:バランスガス)2.5Lを入れた「におい袋」(袋容量:3L、袋サイズ:250×250mm、材質:ポリエステルフィルム/アズワン株式会社製)に分解剤500mgを投入し、25℃で21時間静置後、におい袋内のヘッドスペースの脂肪酸(酢酸)濃度をガス検知管(株式会社ガステック製)にて測定した。結果を表2に示す。Test Example 7 Fatty acid degradation test (room temperature)
The following fatty acid decomposition tests were performed using the decomposition agents obtained in Examples 1 to 3. “Odor bag” (bag capacity: 3 L, containing 2.5 L of reaction gas (acetic acid concentration, about 50 ppm; oxygen, 20 vol%; nitrogen, balance: balance gas) containing fatty acid (acetic acid) in the amount shown in Table 2 Bag size: 250 × 250 mm, Material: Polyester film / manufactured by ASONE Co., Ltd.), 500 mg of decomposition agent was added and left at 25 ° C. for 21 hours. (Measured by Gastec Co., Ltd.). The results are shown in Table 2.
試験例8 アルデヒド分解試験(室温)
実施例1〜3及び比較例1で得られた分解剤を用いて下記のアルデヒド分解試験を行った。表2に記載の量のアルデヒド(ホルムアルデヒド)を含む反応ガス(ホルムアルデヒド濃度、約100ppm;酸素、20体積%;窒素、残部:バランスガス)2.5Lを入れた「におい袋」(袋容量:3L、袋サイズ:250×250mm、材質:ポリエステルフィルム/アズワン株式会社製)に分解剤500mgを投入し、25℃で21時間静置後、におい袋内のヘッドスペースのアルデヒド(ホルムアルデヒド)濃度をガス検知管(株式会社ガステック製)にて測定した。結果を表2に示す。また、25℃で21時間静置後のにおい袋内のヘッドスペースの二酸化炭素の発生量をガス検知管(株式会社ガステック製)にて測定した。結果を表3に示す。Test Example 8 Aldehyde degradation test (room temperature)
The following aldehyde decomposition tests were conducted using the decomposition agents obtained in Examples 1 to 3 and Comparative Example 1. “Smell bag” (bag capacity: 3 L, containing 2.5 L of reaction gas (formaldehyde concentration, about 100 ppm; oxygen, 20% by volume; nitrogen, balance: balance gas) containing the amount of aldehyde (formaldehyde) shown in Table 2 Bag size: 250 × 250 mm, Material: Polyester film / manufactured by ASONE Co., Ltd.), 500 mg of decomposing agent was added and left at 25 ° C. for 21 hours. (Measured by Gastec Co., Ltd.). The results are shown in Table 2. Further, the amount of carbon dioxide generated in the head space in the odor bag after standing at 25 ° C. for 21 hours was measured with a gas detector tube (manufactured by Gastec Co., Ltd.). The results are shown in Table 3.
試験例9 アルデヒド分解試験(−20℃)
実施例2で得られた分解剤を用いて下記のアルデヒド分解試験を行った。表2に記載の量のアルデヒド(アセトアルデヒド)を含む反応ガス(アセトアルデヒド濃度、約50ppm;酸素、20体積%;窒素、残部:バランスガス)2.5Lを入れた「におい袋」(袋容量:3L、袋サイズ:250×250mm、材質:ポリエステルフィルム/アズワン株式会社製)に分解剤500mgを投入し、−20℃で21時間静置後、におい袋内のヘッドスペースのガスのみを別の「におい袋」に移送し、常温に戻したのちアルデヒド(アセトアルデヒド)濃度をガス検知管(株式会社ガステック製)にて測定した。結果を表2に示す。Test Example 9 Aldehyde degradation test (−20 ° C.)
The following aldehyde decomposition test was performed using the decomposition agent obtained in Example 2. “Odor bag” (bag capacity: 3 L, containing 2.5 L of reaction gas (acetaldehyde concentration, about 50 ppm; oxygen, 20% by volume; nitrogen, balance: balance gas) containing aldehyde (acetaldehyde) in the amount shown in Table 2 Bag size: 250 × 250 mm, Material: Polyester film / manufactured by AS ONE Co., Ltd.) 500 mg of decomposing agent is added and left at −20 ° C. for 21 hours. After transporting and returning to room temperature, the aldehyde (acetaldehyde) concentration was measured with a gas detector tube (manufactured by Gastec Co., Ltd.). The results are shown in Table 2.
実施例1〜3より、多孔質シリカに白金又は白金含有化合物を担持させると、臭気物質を分解できることがわかる。一方で、多孔質シリカに白金又は白金含有化合物を担持させていない比較例1においては、表3から、臭気物質の分解能がないことがわかる。なお、表2の試験例8において、比較例1のホルムアルデヒド残留濃度が初期濃度と比較して低下しているが、吸着によるものと推定される。 From Examples 1 to 3, it can be seen that odorous substances can be decomposed when platinum or a platinum-containing compound is supported on porous silica. On the other hand, in Comparative Example 1 in which platinum or a platinum-containing compound is not supported on porous silica, it can be seen from Table 3 that there is no resolution of odorous substances. In Test Example 8 of Table 2, although the formaldehyde residual concentration in Comparative Example 1 is lower than the initial concentration, it is presumed to be due to adsorption.
本発明は、前記の実施態様及び実施例によりなんら限定されるものではない。本発明の要旨を逸脱しない範囲において種々の実施態様を取り得る。 The present invention is not limited in any way by the above-described embodiments and examples. Various embodiments can be taken without departing from the scope of the present invention.
本発明は、魚や肉から放出される揮発性の臭気物質などの分解において有用である。 The present invention is useful in decomposing volatile odorous substances released from fish and meat.
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