WO2023054012A1 - ガス吸着剤ならびにそれを用いたガス吸着シート、濾材およびエアフィルター - Google Patents
ガス吸着剤ならびにそれを用いたガス吸着シート、濾材およびエアフィルター Download PDFInfo
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- WO2023054012A1 WO2023054012A1 PCT/JP2022/034719 JP2022034719W WO2023054012A1 WO 2023054012 A1 WO2023054012 A1 WO 2023054012A1 JP 2022034719 W JP2022034719 W JP 2022034719W WO 2023054012 A1 WO2023054012 A1 WO 2023054012A1
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- WO
- WIPO (PCT)
- Prior art keywords
- activated carbon
- acid
- impregnated activated
- gas
- adsorbent
- Prior art date
Links
- 239000003463 adsorbent Substances 0.000 title claims abstract description 183
- 238000001179 sorption measurement Methods 0.000 title claims abstract description 61
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 394
- 125000002485 formyl group Chemical class [H]C(*)=O 0.000 claims abstract description 68
- 239000011148 porous material Substances 0.000 claims description 115
- 238000000034 method Methods 0.000 claims description 68
- 239000002245 particle Substances 0.000 claims description 49
- 239000004745 nonwoven fabric Substances 0.000 claims description 25
- 230000007774 longterm Effects 0.000 abstract description 5
- 239000007789 gas Substances 0.000 description 154
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 83
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 57
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 51
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 36
- 235000019645 odor Nutrition 0.000 description 36
- 238000003795 desorption Methods 0.000 description 19
- 239000002253 acid Substances 0.000 description 18
- 239000010954 inorganic particle Substances 0.000 description 17
- 238000004519 manufacturing process Methods 0.000 description 16
- 239000000463 material Substances 0.000 description 16
- 238000005259 measurement Methods 0.000 description 16
- 229910021529 ammonia Inorganic materials 0.000 description 15
- 239000002585 base Substances 0.000 description 13
- 239000000126 substance Substances 0.000 description 13
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 description 12
- 229920006395 saturated elastomer Polymers 0.000 description 11
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 9
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 8
- UIIMBOGNXHQVGW-UHFFFAOYSA-M Sodium bicarbonate Chemical compound [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 description 8
- 239000000835 fiber Substances 0.000 description 8
- 238000006386 neutralization reaction Methods 0.000 description 8
- 241000208125 Nicotiana Species 0.000 description 7
- 235000002637 Nicotiana tabacum Nutrition 0.000 description 7
- 239000003795 chemical substances by application Substances 0.000 description 7
- 230000002378 acidificating effect Effects 0.000 description 6
- 239000000853 adhesive Substances 0.000 description 6
- 230000001070 adhesive effect Effects 0.000 description 6
- IBVAQQYNSHJXBV-UHFFFAOYSA-N adipic acid dihydrazide Chemical compound NNC(=O)CCCCC(=O)NN IBVAQQYNSHJXBV-UHFFFAOYSA-N 0.000 description 6
- 230000000052 comparative effect Effects 0.000 description 6
- 230000001877 deodorizing effect Effects 0.000 description 6
- 229940079593 drug Drugs 0.000 description 6
- 239000003814 drug Substances 0.000 description 6
- 230000000694 effects Effects 0.000 description 6
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Chemical compound [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 description 6
- 238000010521 absorption reaction Methods 0.000 description 5
- 230000001186 cumulative effect Effects 0.000 description 5
- 230000007423 decrease Effects 0.000 description 5
- 239000004744 fabric Substances 0.000 description 5
- IKHGUXGNUITLKF-UHFFFAOYSA-N Acetaldehyde Chemical compound CC=O IKHGUXGNUITLKF-UHFFFAOYSA-N 0.000 description 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 4
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
- 238000001035 drying Methods 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- 235000011007 phosphoric acid Nutrition 0.000 description 4
- 239000000843 powder Substances 0.000 description 4
- 230000009257 reactivity Effects 0.000 description 4
- 229920005989 resin Polymers 0.000 description 4
- 239000011347 resin Substances 0.000 description 4
- 239000000377 silicon dioxide Substances 0.000 description 4
- 229910000030 sodium bicarbonate Inorganic materials 0.000 description 4
- 235000017557 sodium bicarbonate Nutrition 0.000 description 4
- 238000003860 storage Methods 0.000 description 4
- 230000001629 suppression Effects 0.000 description 4
- -1 tertiary amine compounds Chemical class 0.000 description 4
- 238000012360 testing method Methods 0.000 description 4
- 239000012855 volatile organic compound Substances 0.000 description 4
- MUBZPKHOEPUJKR-UHFFFAOYSA-N Oxalic acid Chemical compound OC(=O)C(O)=O MUBZPKHOEPUJKR-UHFFFAOYSA-N 0.000 description 3
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 3
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 230000009471 action Effects 0.000 description 3
- 235000019504 cigarettes Nutrition 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 229960003975 potassium Drugs 0.000 description 3
- 229910052700 potassium Inorganic materials 0.000 description 3
- 239000011591 potassium Substances 0.000 description 3
- 229910000027 potassium carbonate Inorganic materials 0.000 description 3
- 235000011181 potassium carbonates Nutrition 0.000 description 3
- 238000000746 purification Methods 0.000 description 3
- 238000009423 ventilation Methods 0.000 description 3
- 235000013162 Cocos nucifera Nutrition 0.000 description 2
- 244000060011 Cocos nucifera Species 0.000 description 2
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 2
- MJNIWUJSIGSWKK-UHFFFAOYSA-N Riboflavine 2',3',4',5'-tetrabutanoate Chemical compound CCCC(=O)OCC(OC(=O)CCC)C(OC(=O)CCC)C(OC(=O)CCC)CN1C2=CC(C)=C(C)C=C2N=C2C1=NC(=O)NC2=O MJNIWUJSIGSWKK-UHFFFAOYSA-N 0.000 description 2
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- 238000010669 acid-base reaction Methods 0.000 description 2
- 150000007513 acids Chemical class 0.000 description 2
- 230000004913 activation Effects 0.000 description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 2
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 230000003247 decreasing effect Effects 0.000 description 2
- 239000002781 deodorant agent Substances 0.000 description 2
- 230000006866 deterioration Effects 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- 239000011521 glass Substances 0.000 description 2
- 238000010030 laminating Methods 0.000 description 2
- 239000004750 melt-blown nonwoven Substances 0.000 description 2
- WSFSSNUMVMOOMR-NJFSPNSNSA-N methanone Chemical compound O=[14CH2] WSFSSNUMVMOOMR-NJFSPNSNSA-N 0.000 description 2
- 150000007522 mineralic acids Chemical class 0.000 description 2
- 230000007935 neutral effect Effects 0.000 description 2
- 229910017604 nitric acid Inorganic materials 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- 229910021426 porous silicon Inorganic materials 0.000 description 2
- 239000011736 potassium bicarbonate Substances 0.000 description 2
- 229910000028 potassium bicarbonate Inorganic materials 0.000 description 2
- 235000015497 potassium bicarbonate Nutrition 0.000 description 2
- TYJJADVDDVDEDZ-UHFFFAOYSA-M potassium hydrogencarbonate Chemical compound [K+].OC([O-])=O TYJJADVDDVDEDZ-UHFFFAOYSA-M 0.000 description 2
- 229940086066 potassium hydrogencarbonate Drugs 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 235000012239 silicon dioxide Nutrition 0.000 description 2
- 239000000779 smoke Substances 0.000 description 2
- 238000005507 spraying Methods 0.000 description 2
- 239000012209 synthetic fiber Substances 0.000 description 2
- 229920002994 synthetic fiber Polymers 0.000 description 2
- BJEPYKJPYRNKOW-REOHCLBHSA-N (S)-malic acid Chemical compound OC(=O)[C@@H](O)CC(O)=O BJEPYKJPYRNKOW-REOHCLBHSA-N 0.000 description 1
- KXGFMDJXCMQABM-UHFFFAOYSA-N 2-methoxy-6-methylphenol Chemical compound [CH]OC1=CC=CC([CH])=C1O KXGFMDJXCMQABM-UHFFFAOYSA-N 0.000 description 1
- HVBSAKJJOYLTQU-UHFFFAOYSA-N 4-aminobenzenesulfonic acid Chemical compound NC1=CC=C(S(O)(=O)=O)C=C1 HVBSAKJJOYLTQU-UHFFFAOYSA-N 0.000 description 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-M Bicarbonate Chemical class OC([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-M 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 239000004113 Sepiolite Substances 0.000 description 1
- UIIMBOGNXHQVGW-DEQYMQKBSA-M Sodium bicarbonate-14C Chemical compound [Na+].O[14C]([O-])=O UIIMBOGNXHQVGW-DEQYMQKBSA-M 0.000 description 1
- 229910021536 Zeolite Inorganic materials 0.000 description 1
- YKTSYUJCYHOUJP-UHFFFAOYSA-N [O--].[Al+3].[Al+3].[O-][Si]([O-])([O-])[O-] Chemical compound [O--].[Al+3].[Al+3].[O-][Si]([O-])([O-])[O-] YKTSYUJCYHOUJP-UHFFFAOYSA-N 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 1
- 239000002156 adsorbate Substances 0.000 description 1
- 229910001413 alkali metal ion Inorganic materials 0.000 description 1
- 150000001340 alkali metals Chemical class 0.000 description 1
- 229910001420 alkaline earth metal ion Inorganic materials 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 238000005452 bending Methods 0.000 description 1
- KGBXLFKZBHKPEV-UHFFFAOYSA-N boric acid Chemical compound OB(O)O KGBXLFKZBHKPEV-UHFFFAOYSA-N 0.000 description 1
- 239000004327 boric acid Substances 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- HCOMFAYPHBFMKU-UHFFFAOYSA-N butanedihydrazide Chemical compound NNC(=O)CCC(=O)NN HCOMFAYPHBFMKU-UHFFFAOYSA-N 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-N carbonic acid Chemical class OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 239000011300 coal pitch Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- GRGBENNNGZARRZ-UHFFFAOYSA-N dodecanedihydrazide Chemical compound NNC(=O)CCCCCCCCCCC(=O)NN GRGBENNNGZARRZ-UHFFFAOYSA-N 0.000 description 1
- 230000008030 elimination Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000000499 gel Substances 0.000 description 1
- 239000003365 glass fiber Substances 0.000 description 1
- 239000012943 hotmelt Substances 0.000 description 1
- 150000004679 hydroxides Chemical class 0.000 description 1
- YAMHXTCMCPHKLN-UHFFFAOYSA-N imidazolidin-2-one Chemical compound O=C1NCCN1 YAMHXTCMCPHKLN-UHFFFAOYSA-N 0.000 description 1
- 239000012784 inorganic fiber Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 235000005985 organic acids Nutrition 0.000 description 1
- 235000006408 oxalic acid Nutrition 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 229920001568 phenolic resin Polymers 0.000 description 1
- 239000005011 phenolic resin Substances 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 229920000728 polyester Polymers 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920000098 polyolefin Polymers 0.000 description 1
- 229920005672 polyolefin resin Polymers 0.000 description 1
- 235000011118 potassium hydroxide Nutrition 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 229910052624 sepiolite Inorganic materials 0.000 description 1
- 235000019355 sepiolite Nutrition 0.000 description 1
- 208000008842 sick building syndrome Diseases 0.000 description 1
- 239000000741 silica gel Substances 0.000 description 1
- 229910002027 silica gel Inorganic materials 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 229910000029 sodium carbonate Inorganic materials 0.000 description 1
- 235000017550 sodium carbonate Nutrition 0.000 description 1
- 235000011121 sodium hydroxide Nutrition 0.000 description 1
- 229950000244 sulfanilic acid Drugs 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
- 229920005992 thermoplastic resin Polymers 0.000 description 1
- LENZDBCJOHFCAS-UHFFFAOYSA-N tris Chemical compound OCC(N)(CO)CO LENZDBCJOHFCAS-UHFFFAOYSA-N 0.000 description 1
- 229910021642 ultra pure water Inorganic materials 0.000 description 1
- 239000012498 ultrapure water Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 239000002759 woven fabric Substances 0.000 description 1
- 239000010457 zeolite Substances 0.000 description 1
- 229910000166 zirconium phosphate Inorganic materials 0.000 description 1
- LEHFSLREWWMLPU-UHFFFAOYSA-B zirconium(4+);tetraphosphate Chemical compound [Zr+4].[Zr+4].[Zr+4].[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O LEHFSLREWWMLPU-UHFFFAOYSA-B 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
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/20—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising free carbon; comprising carbon obtained by carbonising processes
-
- 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
- A61L9/014—Deodorant compositions containing sorbent material, e.g. activated carbon
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D39/00—Filtering material for liquid or gaseous fluids
- B01D39/14—Other self-supporting filtering material ; Other filtering material
-
- 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
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/22—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
-
- 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
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical 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
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28014—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their form
-
- 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
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28054—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their surface properties or porosity
-
- 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
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28054—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their surface properties or porosity
- B01J20/28057—Surface area, e.g. B.E.T specific surface area
- B01J20/28064—Surface area, e.g. B.E.T specific surface area being in the range 500-1000 m2/g
-
- 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
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28054—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their surface properties or porosity
- B01J20/28057—Surface area, e.g. B.E.T specific surface area
- B01J20/28066—Surface area, e.g. B.E.T specific surface area being more than 1000 m2/g
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B32/00—Carbon; Compounds thereof
- C01B32/30—Active carbon
- C01B32/354—After-treatment
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B33/00—Silicon; Compounds thereof
- C01B33/113—Silicon oxides; Hydrates thereof
- C01B33/12—Silica; Hydrates thereof, e.g. lepidoic silicic acid
- C01B33/18—Preparation of finely divided silica neither in sol nor in gel form; After-treatment thereof
Definitions
- the present invention relates to gas adsorbents and gas adsorption sheets, filter media and air filters using the same.
- Air purifiers are used to remove dust and odorous gas components in the home.
- deodorizing performance against volatile organic compounds (VOC) generated in the living environment where the air purifier is used is required as a performance requirement for the deodorizing function of the air purifier for home use.
- VOCs such as formaldehyde have been shown to have an undesirable effect on the human body, and laws and ordinances of each country stipulate that indoor environmental concentrations should be controlled below a certain level.
- Air purifiers are expected to have performance as removal equipment for this VOC.
- there is a demand for high efficiency in removing formaldehyde which is at risk of being released from building materials such as wallpaper, which is thought to cause sick house syndrome, and for a long service life.
- a high deodorizing efficiency means that the operation time of the air purifier required to lower the gas concentration in a predetermined space is short. Longer life means that the above deodorizing efficiency is maintained even after a predetermined amount of gas is adsorbed.
- the deodorizing efficiency is shown as the space purification capacity (CADR: Clean Air Delivery Rate), and the lifetime is shown as the cumulative clean mass (CCM: Cumulate Clean Mass) with evaluation criteria such as GB/T 18801 2015 (Chinese national standard).
- the present invention is capable of maintaining the ability to remove odorous components such as formaldehyde for a long period of time and suppressing the desorption of gas components adsorbed during use from the air filter. To provide an adsorbent effective in suppressing secondary odor generation.
- the gas adsorbent of the present invention that solves the above problems includes (A1) acid-impregnated activated carbon, (A2) base-impregnated activated carbon and (B) aldehyde adsorbent.
- the gas adsorbent of the present invention preferably satisfies the following (1) to (4).
- the ratio of the pore volume of pores with a pore diameter of 0.4 to 2.0 nm calculated by the MP method of (A1) acid-impregnated activated carbon is 75 to 100% of the pore volume of pores with a calculated pore diameter of 0.4 nm or more, and/or (A2) the pore diameter of the base-impregnated activated carbon calculated by the MP method is 0.4 to 2.0 nm is 75 to 100% of the pore volume of pores having a pore diameter of 0.4 nm or more calculated by the MP method and BJH method of (A2) base-impregnated activated carbon.
- the specific surface area of (A1) acid-impregnated activated carbon and/or (A2) base-impregnated activated carbon is 400 to 1300 m 2 /g.
- the gas adsorption sheet of the present invention contains the gas adsorbent of the present invention.
- the filter medium of the present invention holds the gas adsorbent of the present invention in at least one of one or more layers formed by two or more layers of nonwoven fabric.
- the air filter of the present invention includes the filter medium of the present invention.
- the present invention it is possible to suppress desorption from the air filter of gas components such as aldehyde, ammonia, and acetic acid adsorbed on the air filter. It is possible to provide a gas adsorbent that is effective in suppressing and prolonging the life of formaldehyde gas removal performance.
- the present invention solves the above problem, that is, it is possible to suppress detachment from the air filter of odorous components such as aldehyde, ammonia, and acetic acid once adsorbed on the air filter.
- odorous components such as aldehyde, ammonia, and acetic acid
- the gas adsorbent of the present invention includes (A1) acid-impregnated activated carbon, (A2) base-impregnated activated carbon and (B) aldehyde adsorbent.
- activated carbon to which no acid or base is impregnated has only a so-called physical adsorption action, in which the pore structure allows gas to be adsorbed on the pore surfaces by intermolecular force generated by contact with gas in the air. Therefore, when a gas exceeding the physical adsorption capacity of activated carbon is adsorbed, the same component as the adsorbed gas is released again.
- Acid-impregnated activated carbon is an unimpregnated activated carbon impregnated with an acid agent to make the acid exist on the pore surface of the activated carbon. It is an activated carbon imparted with a so-called chemisorption effect, which is a neutralization reaction that converts to a non-volatile component different from that before adsorption.
- the acid of the acid-impregnated activated carbon (A1) used in the gas adsorbent of the present invention is not particularly limited, and inorganic acids such as phosphoric acid, hydrochloric acid, sulfuric acid, nitric acid and boric acid, citric acid, oxalic acid and apple acid. acid, and other organic acids.
- inorganic acids such as phosphoric acid, hydrochloric acid, sulfuric acid, nitric acid and boric acid, citric acid, oxalic acid and apple acid. acid, and other organic acids.
- an inorganic acid selected from phosphoric acid, hydrochloric acid, sulfuric acid and nitric acid is more preferable in terms of deodorizing effect.
- Base-impregnated activated carbon impregnates unimpregnated activated carbon with a chemical consisting of a base, and by making the base exist on the pore surface of the activated carbon, in addition to the physical adsorption action inherent to activated carbon, acid gases such as acetic acid can be removed. It is an activated carbon imparted with a so-called chemisorption effect, which is a neutralization reaction that changes the components into non-volatile components different from those before adsorption.
- the base of the base-impregnated activated carbon (A2) used in the gas adsorbent of the present invention is not particularly limited, and hydroxides or salts of alkali metal and alkaline earth metal ions such as potassium, calcium, sodium and magnesium are used.
- alkali metal and alkaline earth metal ions such as potassium, calcium, sodium and magnesium are used.
- Examples include potassium hydroxide, sodium hydroxide, potassium carbonate, sodium carbonate, potassium hydrogen carbonate, sodium hydrogen carbonate, and the like.
- hydrogencarbonates such as potassium hydrogencarbonate and sodium hydrogencarbonate are preferable because they hardly clog pores of activated carbon due to deliquescence.
- the method for impregnating the acid or base drug is not particularly limited, but an aqueous solution or dispersion of the acid or base is sprayed onto the activated carbon and dried to remove moisture, thereby allowing the drug component to adhere to the pores of the activated carbon. A method is preferred.
- (A1) acid-impregnated activated carbon and/or (A2) base-impregnated activated carbon in the present invention preferably have the following pore structure. That is, (A1) the ratio of the pore volume of pores with a pore diameter of 0.4 to 2.0 nm calculated by the MP method of acid-impregnated activated carbon is calculated by (A1) the MP method and BJH method of acid-impregnated activated carbon. and (A2) the pore diameter calculated by the MP method of the base-impregnated activated carbon is 0.4 to 2.0 nm.
- the ratio of the pore volume of the pores of (A2) is 75 to 100% of the pore volume of pores having a pore diameter of 0.4 nm or more calculated by the MP method and the BJH method of the base-impregnated activated carbon. It is preferable to satisfy at least one of
- the ratio of the pore volume of pores with a pore diameter of 0.4 to 2 nm is 0.4 to 2 nm.
- the adsorbent with activated carbon exhibits physical adsorption of organic gas components such as toluene and chemisorption performance of acidic or basic gases. Furthermore, re-release of gas components once adsorbed from the adsorbent is further suppressed.
- the mechanism by which this effect is obtained is as follows. That is, among the pores provided in (A1) the acid-impregnated activated carbon and (A2) the base-impregnated activated carbon, the pores having a pore diameter of 0.4 to 2 nm impregnated with an acid or a base contain an acid gas such as acetic acid. Alternatively, since the molecular size is close to that of a basic gas such as ammonia, it has excellent physical adsorption performance, and furthermore, it is said that odorous components once adsorbed in the pores are difficult to desorb from the pores. It has characteristics.
- Methods for analyzing the pore diameter and pore volume of activated carbon include the MP (MICROPORE) method and the BJH (Barrett-Joyner-Halenda) method.
- the MP method was adopted for the analysis of micropores with a pore diameter of 0.4 to 2 nm, in which capillary condensation does not occur, among the pores of activated carbon.
- the BJH method was adopted for the analysis of macropores having a pore diameter of 2 nm or more among the pores of activated carbon.
- the pore volume of pores having a pore diameter of 0.4 nm or more calculated by the MP method and the BJH method of activated carbon in the present invention means the value of the pore volume obtained by the MP method and the pore volume obtained by the BJH method. It refers to the total value of the pore volume values obtained.
- the specific surface area of (A1) acid-impregnated activated carbon and/or (A2) base-impregnated activated carbon is preferably in the range of 400 to 1300 m 2 /g, more preferably in the range of 600 to 1000 m 2 /g.
- the specific surface area referred to here is determined by the BET multipoint method specified in JIS R 1626-1996. measurement.).
- the amount of acid or base impregnated to obtain the above specific surface area is preferably 2 to 40% by mass, more preferably 5 to 25% by mass, based on the entire impregnated activated carbon.
- Activated carbon having a pore structure as described above can be arbitrarily selected as a raw material from known materials such as coconut shells, charcoal, coal pitch, and phenolic resin. It is obtained by adjusting the activation conditions that form pores by Among them, it is more preferable to use coconut shells as a raw material and select the activation method with steam, because it is easy to obtain activated carbon with a smaller pore size.
- Aldehyde adsorbent is a chemical adsorbent in which inorganic particles are used as a carrier and agents having chemical reactivity with aldehyde components such as acetaldehyde and formaldehyde are added thereto.
- inorganic particles inorganic particles that react less with the attached drug are preferable.
- the specific surface area of the inorganic particles employed in the present invention is preferably 50-1200 m 2 /g, more preferably 100-1000 m 2 /g.
- the specific surface area of the inorganic particles is measured according to the BET multi-point method specified in JIS R 1626-1996 (constant volume method described in 6.1 Volume method, preheating, N 2 as adsorbate, and measurement by the constant volume method). can.
- the inorganic particles preferably have a pore volume of 0.3 to 2.5 cc/g, more preferably 1.0 to 2.0 cc/g.
- a pore volume of the inorganic particles By setting the pore volume of the inorganic particles to 0.3 to 2.5 cc/g, it is possible to increase the amount of the chemical to be impregnated while retaining pores that are excellent in reacting with aldehyde gas in the air. It is preferable because it can increase the adsorption efficiency and adsorption capacity as an adsorbent.
- the pore volume referred to here can be measured by the BJH method described above.
- the inorganic particles preferably have pores with an average diameter of 0.5 to 100 nm, more preferably 2 to 50 nm.
- the average diameter of the pores of the inorganic particles is 0.5 to 100 nm, it is possible to secure a large specific surface area for supporting the drug while ensuring mechanical strength even in a porous body, and This is preferable because it facilitates penetration of the drug into the pores.
- pores with a diameter of 2 to 50 nm are called mesopores, and particles having mesopores are excellent in efficiently advancing the reaction between the attached drug and acetaldehyde.
- Inorganic particles employed in the present invention include porous silicon dioxide (silica), zeolite, sepiolite, activated alumina, aluminum silicate, silica gel, alumina gel, activated clay, layered compounds such as zirconium phosphate and ammonium polytriphosphate, porous
- porous silicon dioxide (silica) has the above-mentioned preferred average pore diameter, specific surface area, and pore size. It is possible to procure a large volume at a low cost, which is preferable.
- tertiary amine compounds can be used as agents having chemical reactivity with aldehyde components employed in the present invention, and hydrazide compounds such as adipic acid dihydrazide, dodecanedioic acid dihydrazide, and succinic acid dihydrazide are preferred. , p-aminobenzenesulfonic acid, ethylene urea condensates, tris(hydroxymethyl)aminomethane and the like. Among them, adipic acid dihydrazide is preferable in terms of adsorption performance of aldehydes.
- the amount of adipic acid dihydrazide used in the present invention is preferably 7 mg to 120 mg, more preferably 35 to 90 mg, per 1 g of inorganic particles.
- the gas adsorbent of the present invention is composed of the above two types of drug-impregnated activated carbon and aldehyde adsorbent.
- the first point is that when a gas adsorbent is used as an air filter, the gas in the air is composed of an extremely large number of components, among which are basic gases typified by ammonia, acidic gases typified by acetic acid, acetaldehyde, Aldehyde gases, such as formaldehyde, have a low concentration threshold at which humans perceive them as odors, and chemisorption by acids, bases, and aldehyde adsorbents are all used as a means of suppressing the re-emission of these gases from adsorbents.
- the second point is that many of the chemicals that react with the aldehyde component impregnated on the inorganic particles are highly reactive with the aldehyde gas in the air when the pH is weakly acidic to near neutral.
- activated carbon or base-impregnated activated carbon alone, by using both together with an aldehyde adsorbent, it is possible to maintain an appropriate pH. can be exhibited, and its performance can be maintained even after long-term storage.
- the gas adsorbent By blending the gas adsorbent within this range, the re-release amount of the adsorbed gas when used as a filter is reduced, and (A1) the acid-impregnated activated carbon and (A2) the base-impregnated activated carbon come into contact with each other, resulting in a decrease in the performance of each other. can be suppressed.
- the ratio of (M A ) By setting the ratio of (M A ) to 95 or less, it is possible to reduce the neutralization reaction due to contact between (A1) the acid-impregnated activated carbon and (A2) the base-impregnated activated carbon in the gas adsorbent, and the mutual chemisorption performance It is preferable because it is possible to suppress the decrease in On the contrary, by setting the ratio of (M A ) to 25 or more, the adsorption performance of acidic and basic gases in the air becomes more sufficient, and (B) these gas components adhering to the surface of the aldehyde adsorbent are chemisorbed. It is preferable because it can suppress the generation of unpleasant odors.
- the pH of the gas adsorbent of the present invention is preferably 3-7, more preferably 5-7.
- a pH of 3 to 7 is preferable because the absorption-desorption characteristics of acid gases, basic gases, and non-polar gases such as formaldehyde are not biased.
- the pH of the gas adsorbent 0.3 g of the gas adsorbent is put into 5 g of ultrapure water at a temperature of 20° C., and the pH in the water can be measured with a glass electrode type pH meter.
- the average particle size of (A1) acid-impregnated activated carbon used in the gas adsorbent of the present invention is preferably 40 to 500 ⁇ m, and the average particle size of (A2) base-impregnated activated carbon is preferably 40 to 500 ⁇ m.
- (B) the average particle diameter of the aldehyde adsorbent is preferably 100, and (A1) the average particle diameter of the acid-impregnated activated carbon is preferably 95 to 600.
- the average particle size of the base-impregnated activated carbon is preferably 95-600.
- the average particle size of the acid-impregnated activated carbon is 40 ⁇ m or more, preferably 50 ⁇ m or more. Since the frequency of contact between (A1) the acid-impregnated activated carbon and (A2) the base-impregnated activated carbon is reduced, deterioration in performance can be suppressed.
- (A1) the average particle size of the acid-impregnated activated carbon is 500 ⁇ m or less, preferably 400 ⁇ m or less
- (A2) the average particle size of the base-impregnated activated carbon is 500 ⁇ m or less, preferably 400 ⁇ m or less. Since the degree of contact with the activated carbon particles can be reduced, deterioration in performance can be suppressed.
- the ratio of the average particle size of (A1) acid-impregnated activated carbon to the average particle size of (A2) base-impregnated activated carbon is preferably close.
- the average particle size of the base-impregnated activated carbon is preferably 80-120.
- the average particle size of the aldehyde adsorbent is 100, and (A1) the average particle size of the acid-impregnated activated carbon is 95 or more, preferably 100 or more, (B) the average particle size of the aldehyde adsorbent is 100, and (A2) a base
- the average particle size of the impregnated activated carbon is 95 or more, preferably 100 or more, the air permeability after forming into a sheet can be made more sufficient.
- (A1) the average particle size of the acid-impregnated activated carbon is 600 or less, preferably 500 or less;
- (B) the average particle size of the aldehyde adsorbent is 100;
- the average particle size referred to here means the particle size distribution measured according to JIS-Z-8815 (1994), and the granular (A1) acid-impregnated activated carbon, (A2) base-impregnated activated carbon and (B) aldehyde adsorbent. For each of the particles, the particle size is determined to correspond to the size of the sieve through which 50% by mass of the total mass passes.
- the shape of (A1) acid-impregnated activated carbon, (A2) base-impregnated activated carbon, and (B) aldehyde adsorbent can be arbitrarily selected from known shapes such as spherical, crushed, and columnar shapes.
- the gas adsorbent of the present invention is preferably used in the form of a sheet. That is, the gas adsorbent of the present invention is suitable for use in gas adsorption sheets.
- the gas adsorbent is formed in the form of a sheet, which means a method of forming a sheet by dispersing the gas adsorbent particles between the fibers of the fabric, or a method of connecting the surface of the composite gas adsorbent with an adhesive or the like. and forming it into a sheet.
- the form of the fabric is not particularly limited, and can be arbitrarily selected from woven fabrics, knitted fabrics, molded nets, non-woven fabrics, and the like.
- nonwoven fabrics are preferable because the desired physical properties can be easily obtained by arbitrarily selecting the fiber diameter, fiber length, etc. of the fibers to be used and combining them.
- nonwoven fabrics include chemical bond nonwoven fabrics, wet stamp nonwoven fabrics, spunbond nonwoven fabrics, meltblown nonwoven fabrics, spunlace nonwoven fabrics and air-laid nonwoven fabrics.
- the basis weight of the gas adsorbent is preferably in the range of 15 to 400 g/m 2 . Furthermore, the range of 30 to 300 g/m 2 is more preferable because the gas adsorption capacity is high and the obtained sheet-like filter material is excellent in pleating (bending) workability when processed into an air filter.
- the gas adsorbent is preferably particulate, and the shape can be arbitrarily selected from known ones such as spherical, crushed, and columnar.
- the gas adsorbent of the present invention is suitable for use as a filter medium.
- the filter medium comprises two or more layers of nonwoven fabric and the gas adsorbent of the present invention. At least one of the layers formed by two or more layers of nonwoven fabric holds the gas adsorbent of the present invention.
- the amount of the gas adsorbent used in the filter medium of the present invention is preferably in the range of 40 to 400 g/ m2 , more preferably 100 to 200 g/m2, from the viewpoint of obtaining gas removal efficiency and adsorption capacity when used as the filter medium. 2 .
- the nonwoven fabric included in the filter material is preferably an electret nonwoven fabric.
- the electret nonwoven fabric is preferable because the filter medium can collect dust in the air with higher efficiency.
- gas adsorbent particles and powdery heat-bonding resin particles are uniformly dispersed on one non-woven fabric, and after heating and melting the heat-bonding resin particles with a heater, the other non-woven fabric is produced.
- a method of integrating by laminating and pressure bonding, and a method of integrating by laminating and pressure bonding the other nonwoven fabric after spraying gas adsorbent particles on one nonwoven fabric while spraying a heated molten resin is not limited to these.
- the thickness of the nonwoven fabric is preferably 0.08 to 0.60 mm from the viewpoint of having a certain strength and increasing the area that can be accommodated in a certain volume when pleated, and the lower limit is 0.15 mm or more. More preferably, the upper limit is 0.50 mm or less.
- the filter medium has two or more layers of nonwoven fabric, the thickness of these nonwoven fabrics may be the same or different.
- fibers used in the above nonwoven fabric natural fibers, synthetic fibers, or inorganic fibers such as glass fibers or metal fibers can be used.
- thermoplastic resin synthetic fibers that can be melt-spun are preferable.
- the air filter of the present invention comprises the gas adsorption sheet of the present invention or the filter material and outer frame of the present invention. It is preferable that the four sides of the filter medium are fixed to the outer frame.
- the gas adsorption sheet or filter medium may be used as a sheet, or may be pleated to form a three-dimensional shape having ridges and valleys.
- a gas adsorbent and a polyethylene adhesive powder (Abifor 1200 manufactured by Abifor AG) (hereinafter referred to as an adhesive powder) are blended at a mass ratio of 2 gas adsorbents: 1 adhesive powder, and a spunbond nonwoven fabric made of polyester fibers (Toray Axter (registered trademark) H2070-1S manufactured by Co., Ltd., thickness 0.27 mm) is uniformly dispersed in a predetermined amount, and the adhesive powder is melted by heating to 110 ° C. to 130 ° C.
- melt-blown nonwoven fabric (basis weight: 30 g/m 2 , thickness: 0.25 mm)
- pressure is applied by nip rolls to obtain a sheet-like filter medium with a predetermined thickness.
- the mass (g) of the filter material taken out from the desiccator was measured with an electronic balance. The obtained measured value was defined as m2 (g).
- the toluene concentration (ppm) of the air on the downstream side of the filter medium sample was measured using an infrared absorption gas concentration meter (Nippon Thermo Co., Ltd. The passage of the gas was stopped after 25 minutes of measurement at 10-second intervals using the MIRAN Apphl Re). was calculated .
- the ammonia concentration (ppm) in the air on the downstream side of the filter medium sample was measured using an infrared absorption gas concentration meter (manufactured by Nippon Thermo Co., Ltd. MIRAN ApphlRe) was used to measure for 60 minutes at 10 second intervals until the ammonia gas concentration on the downstream side of the sample reached 9 ppm, that is, the ammonia adsorption efficiency of the filter material reached 10%.
- the cumulative adsorption amount (g/m 2 ) of ammonia per (1 m 2 ) was calculated and taken as the saturated adsorption amount.
- a relative humidity of 50% was passed from one side of the filter medium sample to the other side at a wind speed of 20 cm/sec. . 120 seconds after passing acetic acid gas through the filter medium sample, the acetic acid concentration (ppm) of the air on the downstream side of the filter medium sample (the other side of the filter medium sample) was measured using an infrared absorption gas concentration meter (Nippon Thermo Co., Ltd. The passage of the gas was stopped after 25 minutes of measurement at 10-second intervals using a MIRAN Apphl Re), and the concentration of acetic acid in the air detected from the downstream side until then was determined to be acetic acid per unit area (1 m 2 ) of the filter medium. was calculated .
- Acetic acid _ _ The desorption rate (%) was calculated.
- Acetic acid desorption rate (%) [accumulated desorption amount of acetic acid per unit area (1 m 2 ) (g/m 2 )/accumulated adsorption amount of acetic acid per unit area (1 m 2 ) (g/m 2 ) ] ⁇ 100.
- Polyolefin adhesive (Hitachi Kasei Polymer Hibon YH450-1 manufactured by Co., Ltd.) was attached to the four sides of the pleated filter medium to obtain an air filter with a frontage size of 372 mm long, 291 mm wide, and 60 mm high.
- the air purifier after collecting the tobacco combustion smoke is left in a test room with a volume of 30 m 3 for 24 hours without being operated, and then the air purifier is operated, and the odor intensity and comfort level of the discharged air were scored by five panelists according to the criteria shown in Tables 1 and 2, and the average value was obtained.
- Pore volume of activated carbon pores Put 0.10 g of activated carbon in a glass cell, degassed at 150 ° C. for 5 hours, and then, using a device BELSORP-18PLUS manufactured by Bell Japan Co., Ltd., liquid nitrogen temperature 77 K, Activated carbon was put into the apparatus under the condition that the temperature inside the apparatus was set to 35° C. and the saturated vapor pressure was set to 101.3 kPa, and the isothermal adsorption and desorption processes of nitrogen were measured. From the measurement results, the pore volume of pores with a pore diameter of 0.4 to 2 nm was calculated by the MP method, and the pore volume of pores with a pore diameter of 0.4 nm or more was calculated by the BJH method.
- Example 1 As the acid-impregnated activated carbon, granular activated carbon (MNC30/60-O manufactured by Manei Kogyo Co., Ltd., average particle size 300 ⁇ m according to JIS Z8815 method, specific surface area 1200 m 2 /g measured by BET multipoint method) was added with 40 mass of citric acid. and an impregnated activated carbon having a specific surface area of 450 m 2 /g impregnated so as to have a specific surface area of 450 m 2 /g.
- MNC30/60-O manufactured by Manei Kogyo Co., Ltd., average particle size 300 ⁇ m according to JIS Z8815 method, specific surface area 1200 m 2 /g measured by BET multipoint method was added with 40 mass of citric acid.
- an impregnated activated carbon having a specific surface area of 450 m 2 /g impregnated so as to have a specific surface area of 450 m 2 /g.
- the acid-impregnated activated carbon was 30 g/m 2
- the base-impregnated activated carbon was 30 g/m 2
- the aldehyde adsorbent was 90 g/m 2
- total impregnated activated carbon: aldehyde adsorbent A mass ratio of 40:60 was obtained.
- the thickness of this filter medium was 1.1 mm.
- the gas adsorbent was 80 g/m 2
- the acid-impregnated activated carbon was 36 g/m 2
- the base-impregnated activated carbon was 36 g/m 2
- the aldehyde adsorbent was 8 g/m 2
- total impregnated activated carbon: aldehyde adsorbent A mass ratio of 90:10 was obtained.
- the thickness of this filter medium was 0.7 mm.
- Example 4 As the acid-impregnated activated carbon, granular activated carbon (MNC30/60-O manufactured by Manei Kogyo Co., Ltd., average particle size 300 ⁇ m according to JIS Z8815 method, specific surface area 1200 m 2 /g measured by BET multipoint method) was added with 20 mass of orthophosphoric acid. and an impregnated activated carbon having a specific surface area of 700 m 2 /g impregnated so as to have a specific surface area of 700 m 2 /g.
- MNC30/60-O manufactured by Manei Kogyo Co., Ltd., average particle size 300 ⁇ m according to JIS Z8815 method, specific surface area 1200 m 2 /g measured by BET multipoint method was added with 20 mass of orthophosphoric acid.
- an impregnated activated carbon having a specific surface area of 700 m 2 /g impregnated so as to have a specific surface area of 700 m 2 /g.
- the acid-impregnated activated carbon was 30 g/m 2
- the base-impregnated activated carbon was 30 g/m 2
- the aldehyde adsorbent was 90 g/m 2
- total impregnated activated carbon: aldehyde adsorbent A mass ratio of 40:60 was obtained.
- the thickness of this filter medium was 1.2 mm.
- Example 5 The same acid-impregnated activated carbon and base-impregnated activated carbon as in Example 4, and as an aldehyde adsorbent, porous silica particles (pore volume 1.0 cc/g measured by BJH method, specific surface area 500 m measured by BET multipoint method 2 / g, average particle size 280 ⁇ m according to JISZ8815 method), and an adsorbent in which adipic acid dihydrazide (manufactured by Nippon Kasei Co., Ltd.) is impregnated so that it becomes 7% by mass of the total.
- porous silica particles pore volume 1.0 cc/g measured by BJH method, specific surface area 500 m measured by BET multipoint method 2 / g, average particle size 280 ⁇ m according to JISZ8815 method
- adipic acid dihydrazide manufactured by Nippon Kasei Co., Ltd.
- Acid-impregnated activated carbon base-impregnated activated carbon: aldehyde adsorption
- a gas adsorbent blended at a mass ratio of agent 30:30:90 was used.
- a filter medium having a gas adsorbent was produced by the method described in the above [Method for producing filter medium using gas adsorbent].
- the acid-impregnated activated carbon was 30 g/m 2
- the base-impregnated activated carbon was 30 g/m 2
- the aldehyde adsorbent was 90 g/m 2
- total impregnated activated carbon: aldehyde adsorbent A mass ratio of 40:60 was obtained.
- the thickness of this filter medium was 1.1 mm.
- Example 6 As the acid-impregnated activated carbon, granular activated carbon (Kuraray Co., Ltd., Kuraray Coal (registered trademark) GW30/60D, average particle size 300 ⁇ m according to JIS Z8815 method, specific surface area 950 m 2 /g measured by BET multipoint method) was added with orthorin in the same manner as in Example 4. Impregnated activated carbon having a specific surface area of 600 m 2 /g impregnated with an acid of 20% by mass of the whole, and sodium hydrogen carbonate similar to that of Example 4 as the base-impregnated activated carbon and the same granular activated carbon as the above-mentioned impregnated activated carbon.
- Kuraray Co., Ltd., Kuraray Coal (registered trademark) GW30/60D average particle size 300 ⁇ m according to JIS Z8815 method, specific surface area 950 m 2 /g measured by BET multipoint method
- Impregnated activated carbon with a specific surface area of 850 m 2 /g impregnated so as to be 5% by mass, and the same adsorbent as in Example 5 as an aldehyde adsorbent, acid-impregnated activated carbon: base-impregnated activated carbon: aldehyde adsorbent 20 : A gas adsorbent blended at a mass ratio of 40:90 was used. Using this gas adsorbent, a filter medium having a gas adsorbent was produced by the method described in the above [Method for producing filter medium using gas adsorbent].
- the gas adsorbent was 150 g/m 2
- the acid-impregnated activated carbon was 20 g/m 2
- the base-impregnated activated carbon was 40 g/m 2
- the aldehyde adsorbent was 90 g/m 2
- total impregnated activated carbon: aldehyde adsorbent A mass ratio of 40:60 was obtained.
- the thickness of this filter medium was 1.2 mm.
- Example 1 Without using the base-impregnated activated carbon, the same citric acid-impregnated granular activated carbon as in Example 1 was used as the acid-impregnated activated carbon, and the same adsorbent as in Example 5 was used as the aldehyde adsorbent. A gas adsorbent blended at a mass ratio was used. Using 150 g/m 2 of this gas adsorbent, a filter medium having a gas adsorbent was produced by the method described in the above [Method for producing filter medium using gas adsorbent].
- the acid-impregnated activated carbon was 60 g/m 2 and the aldehyde adsorbent was 90 g/m 2 , so the mass ratio of the total impregnated activated carbon: aldehyde adsorbent was 40:60. .
- the thickness of this filter medium was 1.0 mm.
- Example 2 Without using acid-impregnated activated carbon, the same potassium carbonate-impregnated granular activated carbon as in Example 1 was used as the base-impregnated activated carbon, and the same adsorbent as in Example 5 was used as the aldehyde adsorbent. A gas adsorbent blended at a mass ratio was used. Using 150 g/m 2 of this gas adsorbent, a filter medium having a gas adsorbent was produced by the method described in the above [Method for producing filter medium using gas adsorbent].
- the base-impregnated activated carbon was 60 g/m 2 and the aldehyde adsorbent was 90 g/m 2 , so the mass ratio of the total impregnated activated carbon: aldehyde adsorbent was 40:60. .
- the thickness of this filter medium was 1.0 mm.
- the thickness of this filter medium was 1.0 mm.
- Tables 3 and 4 show the gas adsorbents of Examples 1 to 6 and the filter media and air filters using the gas adsorbents of Examples 1 to 6.
- Tables 5 and 6 summarize the filter media and air filters using adsorbents.
- Example 1 a gas adsorbent that combines acid-impregnated activated carbon, base-impregnated activated carbon, and an aldehyde adsorbent is used, so the desorption rate after adsorption is low.
- citric acid used as an acid adsorbs ammonia gas in the air through an acid-base reaction, so it has excellent adsorption capacity for ammonia
- potassium carbonate used as a base adsorbs acetic acid gas in the air through an acid-base reaction. Therefore, the desorption rate after adsorption of acetic acid is low.
- the neutralization reaction due to the contact of citric acid and potassium carbonate, which are the impregnated components of the activated carbon is suppressed by the inclusion of inorganic particles, so that the adsorption performance of ammonia gas and acetic acid gas was maintained even after long-term storage.
- the formaldehyde cleanability (F-CADR) performance is also good, and the odor intensity of the secondary odor after adsorption of tobacco odor is small. It was a long-life air filter that made it difficult to perceive unpleasant odors.
- Example 4 the activated carbon impregnated with orthophosphoric acid, which has better reactivity with ammonia gas in the air than in Example 1, was used, so the saturated adsorption amount of ammonia was improved.
- the obtained filter material is processed into a filter and installed in an air purifier, the odor intensity of the secondary odor after adsorbing the tobacco odor is small, and the user does not feel uncomfortable, that is, it is a long-life air filter. there were.
- Example 5 the average particle size of the aldehyde adsorbent composed of inorganic particles was approximately the same as the average particle size of the acid-impregnated activated carbon and the base-impregnated activated carbon. Since the neutralization reaction due to contact between acid and sodium bicarbonate is suppressed, the adsorption performance of ammonia gas and acetic acid gas was maintained even after long-term storage. In addition, when the obtained filter material is processed into a filter and mounted in an air purifier, the formaldehyde cleanability (F-CADR) performance is also good, and the odor intensity of the secondary odor after adsorption of tobacco odor is small. It was a long-life air filter that made it difficult to perceive unpleasant odors.
- F-CADR formaldehyde cleanability
- Example 6 compared with Examples 1 to 5, the ratio of the pore volume due to pores having a pore diameter of 0.4 to 2 nm to the pore volume of all pores of acid-impregnated activated carbon and base-impregnated activated carbon was Since the higher one is used, the desorption rate after adsorption of toluene and acetic acid was decreased as compared with Examples 1-5.
- the formaldehyde cleanability (F-CADR) performance is also good, and the odor intensity of the secondary odor after adsorption of tobacco odor is small. It was a long-life air filter that made it difficult to perceive unpleasant odors.
- Comparative Example 1 does not contain base-impregnated activated carbon, all acetic acid gas in the air is adsorbed by the physical adsorption properties of activated carbon, and the desorption rate after adsorption is remarkably high. Therefore, after processing it into a filter and installing it in an air purifier, the odor intensity of the secondary odor emitted after adsorption of tobacco odor was high, and the odor was felt to be highly unpleasant.
- Comparative Example 2 did not contain acid-impregnated activated carbon, so the saturated adsorption capacity for ammonia was remarkably low. Therefore, it was processed into a filter and installed in an air purifier, and the odor intensity of the secondary odor after adsorption of the cigarette odor containing a high concentration of ammonia component was high, and the odor was felt to be highly unpleasant. In addition, it is thought that the pH of the entire gas adsorbent changed to the alkaline side due to the influence of the base-impregnated activated carbon, causing a decrease in the formaldehyde adsorption performance, and a decrease in the formaldehyde detergency (F-CADR) was observed.
- F-CADR formaldehyde detergency
- Comparative Example 3 does not use an aldehyde chemical adsorbent, so when processed into a filter and installed in an air purifier, the formaldehyde cleanability (F-CADR) performance is low.
- F-CADR formaldehyde cleanability
- acid-impregnated activated carbon and base-impregnated activated carbon adhere to each other, and the neutralization reaction of the impregnating agent reduces the adsorption performance of ammonia and acetic acid. The amount of re-released was increased, the intensity of the secondary odor was strong, and the odor was felt to be highly unpleasant.
- the gas adsorbent according to the present invention is mainly installed in household air purifiers and used in air filters and filtering materials for cleaning indoor air.
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Abstract
Description
(1)(A1)酸添着活性炭および(A2)塩基添着活性炭の合計質量(MA)と、(B)アルデヒド吸着剤の質量(MB)の比率が、(MA):(MB)=95:5~25:75である。
(2)(A1)酸添着活性炭の平均粒子径が40~500μm、(A2)塩基添着活性炭の平均粒子径が40~500μmであり、
(B)アルデヒド吸着剤の平均粒子径を100として(A1)酸添着活性炭の平均粒子径が95~600、(B)アルデヒド吸着剤の平均粒子径を100として(A2)塩基添着活性炭の平均粒子径が95~600である。
(3)(A1)酸添着活性炭のMP法により算出される細孔径が0.4~2.0nmの細孔の細孔容積の割合が、(A1)酸添着活性炭のMP法およびBJH法により算出される細孔径が0.4nm以上の細孔の細孔容積に対し75~100%、および/または(A2)塩基添着活性炭のMP法により算出される細孔径が0.4~2.0nmの細孔の細孔容積の割合が、(A2)塩基添着活性炭のMP法およびBJH法により算出される細孔径が0.4nm以上の細孔の細孔容積に対し75~100%である。
(4)(A1)酸添着活性炭および/または(A2)塩基添着活性炭の比表面積が、400~1300m2/gである。
D=4 V/S
本発明で採用する無機粒子としては、多孔質二酸化ケイ素(シリカ)、ゼオライト、セピオライト、活性アルミナ、ケイ酸アルミニウム、シリカゲル、アルミナゲル、活性白土、リン酸ジルコニウムやポリトリリン酸アンモニウム等の層状化合物、多孔性粘土鉱物といった中から目的に応じて選択できるが、薬剤との反応が小さい無機粒子が好ましく、中でも多孔質二酸化ケイ素(シリカ)は、上記の好ましい細孔の平均直径や比表面積、および細孔容積を有するものを安価に調達可能であり好ましい。
ガス吸着剤とポリエチレン系接着パウダー(AbiforAG社製 Abifor1200)(以下、接着パウダーとする)を、ガス吸着剤2:接着パウダー1の質量割合でブレンドし、それをポリエステル繊維からなるスパンボンド不織布(東レ株式会社製 アクスター(登録商標)H2070-1S、厚み0.27mm)上に所定量均一に散布し、加熱炉内で110℃~130℃に加熱することにより接着パウダーを溶融させ、その散布面にエレクトレットメルトブロー不織布(目付30g/m2、厚み0.25mm)を積層後、ニップロールによって加圧し、所定の厚みのシート状の濾材を得る。
(1)トルエンの飽和吸着量(g/m2)
上記[ガス吸着剤を用いた濾材の製造方法]で得られたガス吸着剤を用いたシート状濾材を10cm×10cmの四角形に採取し、それを80℃に加熱した乾燥機内に入れ、2時間乾燥処理し、取り出した濾材の質量(g)を電子天秤で測定した。得られた測定値をm1(g)とした。次に、湿度を50%RHに管理した10Lのデシケーター内にトルエンを飽和させ、そこに質量測定した後の濾材を投入し、24時間放置した。そして、上記のデシケーター内から取り出した後の濾材の質量(g)を電子天秤で測定した。得られた測定値をm2(g)とした。次に、下記計算式より、濾材の単位面積当たりのトルエン飽和吸着容量を算出した。
・トルエン飽和吸着容量=(m2-m1)/(0.1×0.1) (g/m2)。
上記[ガス吸着剤を用いた濾材の製造方法]で得られたガス吸着剤を用いたシート状濾材から、直径6cmの円径の濾材サンプル(面積28.3cm2)を採取し、それを80℃に加熱した乾燥機内に入れ、2時間乾燥処理後に取り出した。次に通風直径4cm、および胴部長さ15cmからなる円筒形風洞を2つ用意し、それぞれを濾材サンプルの一方の面側と他方の面側とに取り付けた。次に、濾材サンプルの一方の面側から他方の面側の方向に、温度を20℃、相対湿度を50%に調整した濃度80ppmのトルエンガスを含む空気を、風速20cm/secで通過させた。濾材サンプルにトルエンガスを通過させた120秒後から、濾材サンプルの下流側(濾材サンプルの他方の面側)の空気のトルエン濃度(ppm)を、赤外吸光式ガス濃度計(日本サーモ株式会社製 MIRANSapphlRe)を用いて10秒間隔で25分間測定したところでガスの通過を停止し、そこまでに下流側から検出された空気中のトルエンの濃度から、濾材の単位面積(1m2)あたりのトルエンの積算吸着量(g/m2)を計算した。
トルエンの脱離率(%)=単位面積(1m2)あたりのトルエンの積算脱離量(g/m2)/単位面積(1m2)あたりのトルエンの積算吸着量(g/m2)×100。
上記[ガス吸着剤を用いた濾材の製造方法]で得られたガス吸着剤を用いたシート状濾材から、直径6cmの円径の濾材サンプル(面積28.3cm2)を採取し、それを80℃に加熱した乾燥機内に入れ、2時間乾燥処理後に取り出した。次に通風直径4cm、および胴部長さ15cmからなる円筒形風洞を2つ用意し、それぞれを濾材サンプルの一方の面側と他方の面側とに取り付けた。次に、濾材サンプルの一方の面側から他方の面側の方向に、温度を20℃、相対湿度を50%に調整した濃度10ppmのアンモニアガスを含む空気を、風速20cm/secで通過させた。濾材サンプルにアンモニアを通過させた120秒後から、濾材サンプルの下流側(濾材サンプルの他方の面側)の空気のアンモニア濃度(ppm)を、赤外吸光式ガス濃度計(日本サーモ株式会社製 MIRANSapphlRe)を用いて10秒間隔で60分間測定し、サンプル下流側のアンモニアガス濃度が9ppm、すなわち濾材のアンモニア吸着効率が10%に到達するまで測定し、得られた測定結果から濾材の単位面積(1m2)あたりのアンモニアの積算吸着量(g/m2)を計算し、飽和吸着量とした。
上記[ガス吸着剤を用いた濾材の製造方法]で得られたガス吸着剤を用いたシート状濾材から、直径6cmの円径の濾材サンプル(面積28.3cm2)を採取し、それを80℃に加熱した乾燥機内に入れ、2時間乾燥処理後に取り出した。次に通風直径4cm、および胴部長さ15cmからなる円筒形風洞を2つ用意し、それぞれを濾材サンプルの一方の面側と他方の面側とに取り付けた。次に、濾材サンプルの一方の面側から他方の面側の方向に、温度を20℃、相対湿度を50%に調整した濃度80ppmの酢酸ガスを含む空気を、風速20cm/secで通過させた。濾材サンプルに酢酸ガスを通過させた120秒後から、濾材サンプルの下流側(濾材サンプルの他方の面側)の空気の酢酸濃度(ppm)を、赤外吸光式ガス濃度計(日本サーモ株式会社製 MIRANSapphlRe)を用いて10秒間隔で25分間測定したところでガスの通過を停止し、そこまでに下流側から検出された空気中の酢酸の濃度から、濾材の単位面積(1m2)あたりの酢酸の積算吸着量(g/m2)を計算した。
酢酸の脱離率(%)=[単位面積(1m2)あたりの酢酸の積算脱離量(g/m2)/単位面積(1m2)あたりの酢酸の積算吸着量(g/m2)]×100。
上記[ガス吸着剤を用いた濾材の製造方法]で得られたガス吸着剤を用いたシート状濾材を巾方289mm、長さ7.8m分作製し、レシプロプリーツ加工機(ホップテック株式会社製 W650)を用いて濾材の長さ方向に対し折高さ58mmで66山分プリーツ加工した後、その濾材を一度展開し、濾材表裏の各面上に、ホットメルトアプリケーター(ITWダイナテック株式会社製 Dynamelt)を用いて180℃に加熱し溶融させたポリオレフィン系樹脂(日立化成ポリマー(株)製 ハイボン9500)を、圧空ノズルを用いて太さ3mm、濾材巾方向に対し5cm間隔で計6本連続で塗布した後、再度プリーツ加工の折り目に合わせて折り畳み、隣接するプリーツ山同士の間隔が5.6mmとなるよう、線状のホットメルト樹脂同士を接着固定させ、略直方体のプリーツ形状の濾材を得た。
上記(5)と同様の方法で得られたエアフィルターを温度60℃、相対湿度60%RHの環境下で30日間放置後、上記(5)と同様の空気清浄機に搭載し、上記(5)と同様の試験方法でホルムアルデヒドのCADR(m3/hr)を測定した。
上記(5)と同様の方法で得られたエアフィルターを市販の空気清浄機(定格風量450m3/時)に搭載した。次に、この空気清浄機を容積1m3の透明アクリル製の試験室内に設置し、その試験室内でタバコ(メビウス10mg)5本を燃焼させた後、空気清浄機を稼働させ、燃焼煙をエアフィルターに30分間捕集させた。この作業を10回繰り返し、計50本分のタバコ燃焼煙を捕集させた。
活性炭0.10gをガラスセルに入れて、150℃で5時間脱気したのち、日本ベル株式会社製の装置BELSORP-18PLUSを用い、液体窒素温度77K、装置内温度を35℃、飽和蒸気圧は101.3kPaに設定した条件にて、活性炭を装置に投入して、窒素の等温吸着、脱着過程を測定した。測定結果から、MP法で細孔径0.4~2nmの細孔の細孔容積を計算し、BJH法で細孔径0.4nm以上の細孔の細孔容積を計算した。
酸添着活性炭として、粒状活性炭(満栄工業株式会社製 MNC30/60-O、JISZ8815法による平均粒子径300μm、BET多点法で測定された比表面積1200m2/g)にクエン酸を全体の40質量%となるよう添着処理した、比表面積が450m2/gの添着活性炭と、塩基添着活性炭として、上記添着活性炭と同じ粒状活性炭に炭酸カリウムを全体の7質量%となるよう添着した、比表面積が800m2/gの添着活性炭と、アルデヒド吸着剤として、多孔質シリカ粒子(BJH法により測定された細孔容積1.0cc/g、BET多点法で測定された比表面積500m2/g、JISZ8815法 による平均粒子径400μm)にアジピン酸ジヒドラジド(日本化成株式会社製)を全体の7質量%となるよう添着させた吸着剤とを、酸添着活性炭:塩基添着活性炭:アルデヒド吸着剤=10:10:80の質量比率で配合したガス吸着剤を用いた。このガス吸着剤を用い、上記の[ガス吸着剤を用いた濾材の製造方法]に記載の方法で、ガス吸着剤を有する濾材を製造した。ガス吸着剤を100g/m2用いたので、酸添着活性炭が10g/m2、塩基添着活性炭が10g/m2、アルデヒド吸着剤が80g/m2となるから、添着活性炭合計:アルデヒド吸着剤=20:80の質量比率となった。またこの濾材の厚みは0.9mmであった。
実施例1と同じ酸添着活性炭、塩基添着活性炭、およびアルデヒド吸着剤を酸添着活性炭:塩基添着活性炭:アルデヒド吸着剤=30:30:90の質量比率で配合したガス吸着剤を用いた。このガス吸着剤を用い、上記の[ガス吸着剤を用いた濾材の製造方法]に記載の方法で、ガス吸着剤を有する濾材を製造した。ガス吸着剤を150g/m2用いたので、酸添着活性炭が30g/m2、塩基添着活性炭が30g/m2、アルデヒド吸着剤が90g/m2となるから、添着活性炭合計:アルデヒド吸着剤=40:60の質量比率となった。またこの濾材の厚みは1.1mmであった。
実施例1と同じ酸添着活性炭、塩基添着活性炭、およびアルデヒド吸着剤を酸添着活性炭:塩基添着活性炭:アルデヒド吸着剤=36:36:8の質量比率で配合したガス吸着剤を用いた。このガス吸着剤を用い、上記の[ガス吸着剤を用いた濾材の製造方法]に記載の方法で、ガス吸着剤を有する濾材を製造した。ガス吸着剤を80g/m2用いたので、酸添着活性炭が36g/m2、塩基添着活性炭が36g/m2、アルデヒド吸着剤が8g/m2となるから、添着活性炭合計:アルデヒド吸着剤=90:10の質量比率となった。またこの濾材の厚みは0.7mmであった。
酸添着活性炭として、粒状活性炭(満栄工業株式会社製 MNC30/60-O、JISZ8815法による平均粒子径300μm、BET多点法で測定された比表面積1200m2/g)にオルソリン酸を全体の20質量%となるよう添着処理した、比表面積が700m2/gの添着活性炭と、塩基添着活性炭として、上記添着活性炭と同じ粒状活性炭に炭酸水素ナトリウムを全体の5質量%となるよう添着した、比表面積が950m2/gの添着活性炭と、アルデヒド吸着剤として、実施例1と同様の吸着剤とを、酸添着活性炭:塩基添着活性炭:アルデヒド吸着剤=30:30:90の質量比率で配合したガス吸着剤を用いた。このガス吸着剤を用い、上記の[ガス吸着剤を用いた濾材の製造方法]に記載の方法で、ガス吸着剤を有する濾材を製造した。ガス吸着剤を150g/m2用いたので、酸添着活性炭が30g/m2、塩基添着活性炭が30g/m2、アルデヒド吸着剤が90g/m2となるから、添着活性炭合計:アルデヒド吸着剤=40:60の質量比率となった。またこの濾材の厚みは1.2mmであった。
実施例4と同じ酸添着活性炭、塩基添着活性炭と、アルデヒド吸着剤として、多孔質シリカ粒子(BJH法により測定された細孔容積1.0cc/g、BET多点法で測定された比表面積500m2/g、JISZ8815法 による平均粒子径280μm)にアジピン酸ジヒドラジド(日本化成株式会社製)を全体の7質量%となるよう添着させた吸着剤とを、酸添着活性炭:塩基添着活性炭:アルデヒド吸着剤=30:30:90の質量比率で配合したガス吸着剤を用いた。このガス吸着剤を用い、上記の[ガス吸着剤を用いた濾材の製造方法]に記載の方法で、ガス吸着剤を有する濾材を製造した。ガス吸着剤を150g/m2用いたので、酸添着活性炭が30g/m2、塩基添着活性炭が30g/m2、アルデヒド吸着剤が90g/m2となるから、添着活性炭合計:アルデヒド吸着剤=40:60の質量比率となった。またこの濾材の厚みは1.1mmであった。
酸添着活性炭として、粒状活性炭(株式会社クラレ製 クラレコール(登録商標)GW30/60D、JISZ8815法による平均粒子径300μmBET多点法で測定された比表面積950m2/g)に実施例4同様のオルソリン酸を全体の20質量%となるよう添着処理した、比表面積が600m2/gの添着活性炭と、塩基添着活性炭として、上記添着活性炭と同じ粒状活性炭に実施例4同様の炭酸水素ナトリウムを全体の5質量%となるよう添着した、比表面積が850m2/gの添着活性炭と、アルデヒド吸着剤として、実施例5と同様の吸着剤とを、酸添着活性炭:塩基添着活性炭:アルデヒド吸着剤=20:40:90の質量比率で配合したガス吸着剤を用いた。このガス吸着剤を用い、上記の[ガス吸着剤を用いた濾材の製造方法]に記載の方法で、ガス吸着剤を有する濾材を製造した。ガス吸着剤を150g/m2用いたので、酸添着活性炭が20g/m2、塩基添着活性炭が40g/m2、アルデヒド吸着剤が90g/m2となるから、添着活性炭合計:アルデヒド吸着剤=40:60の質量比率となった。またこの濾材の厚みは1.2mmであった。
塩基添着活性炭を用いず、酸添着活性炭として実施例1と同様のクエン酸添着粒状活性炭、アルデヒド吸着剤として実施例5と同様の吸着剤とを、酸添着活性炭:アルデヒド吸着剤=60:90の質量比率で配合したガス吸着剤を用いた。このガス吸着剤を150g/m2用い、上記の[ガス吸着剤を用いた濾材の製造方法]に記載の方法で、ガス吸着剤を有する濾材を製造した。ガス吸着剤を150g/m2用いたので、酸添着活性炭が60g/m2、アルデヒド吸着剤が90g/m2となるから、添着活性炭合計:アルデヒド吸着剤=40:60の質量比率となった。またこの濾材の厚みは1.0mmであった。
酸添着活性炭を用いず、塩基添着活性炭として実施例1と同様の炭酸カリウム添着粒状活性炭、アルデヒド吸着剤として実施例5と同様の吸着剤とを、塩基添着活性炭:アルデヒド吸着剤=60:90の質量比率で配合したガス吸着剤を用いた。このガス吸着剤を150g/m2用い、上記の[ガス吸着剤を用いた濾材の製造方法]に記載の方法で、ガス吸着剤を有する濾材を製造した。ガス吸着剤を150g/m2用いたので、塩基添着活性炭が60g/m2、アルデヒド吸着剤が90g/m2となるから、添着活性炭合計:アルデヒド吸着剤=40:60の質量比率となった。またこの濾材の厚みは1.0mmであった。
アルデヒド吸着剤を用いず、酸添着活性炭として実施例1と同様のクエン酸添着粒状活性炭、塩基添着活性炭として実施例1と同様の炭酸カリウム添着粒状活性炭とを酸添着活性炭:塩基添着活性炭=50:100の質量比率で配合したガス吸着剤を用いた。このガス吸着剤を計150g/m2用い、上記の[ガス吸着剤を用いた濾材の製造方法]に記載の方法と同様の方法で濾材を製造した。ガス吸着剤を150g/m2用いたので、酸添着活性炭が50g/m2、塩基添着活性炭が100g/m2となるから、添着活性炭合計:アルデヒド吸着剤=100:0の質量比率となった。またこの濾材の厚みは1.0mmであった。
Claims (8)
- (A1)酸添着活性炭、(A2)塩基添着活性炭および(B)アルデヒド吸着剤を含むガス吸着剤。
- (A1)酸添着活性炭および(A2)塩基添着活性炭の合計質量(MA)と、(B)アルデヒド吸着剤の質量(MB)の比率が、(MA):(MB)=95:5~25:75である請求項1に記載のガス吸着剤。
- (A1)酸添着活性炭の平均粒子径が40~500μm、(A2)塩基添着活性炭の平均粒子径が40~500μmであり、(B)アルデヒド吸着剤の平均粒子径を100として(A1)酸添着活性炭の平均粒子径が95~600、(B)アルデヒド吸着剤の平均粒子径を100として(A2)塩基添着活性炭の平均粒子径が95~600である請求項1または2に記載のガス吸着剤。
- (A1)酸添着活性炭のMP法により算出される細孔径が0.4~2.0nmの細孔の細孔容積の割合が、(A1)酸添着活性炭のMP法およびBJH法により算出される細孔径が0.4nm以上の細孔の細孔容積に対し75~100%であること、および(A2)塩基添着活性炭のMP法により算出される細孔径が0.4~2.0nmの細孔の細孔容積の割合が、(A2)塩基添着活性炭のMP法およびBJH法により算出される細孔径が0.4nm以上の細孔の細孔容積に対し75~100%であること、の少なくともいずれか一方を満たす請求項1~3のいずれかに記載のガス吸着剤。
- (A1)酸添着活性炭の比表面積が、400~1300m2/gである、および/または、(A2)塩基添着活性炭の比表面積が、400~1300m2/gである請求項1~4のいずれかに記載のガス吸着剤。
- 請求項1~5のいずれかに記載のガス吸着剤を含む、ガス吸着シート。
- 2層以上の不織布およびガス吸着剤を含む濾材であって、該ガス吸着剤が請求項1~5のいずれかに記載のガス吸着剤であり、2層以上の不織布により形成される1つ以上の層間の少なくとも1つに該ガス吸着剤が保持されている、濾材。
- 請求項7に記載の濾材を備える、エアフィルター。
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JP2008148804A (ja) | 2006-12-15 | 2008-07-03 | Suminoe Textile Co Ltd | たばこ臭の除去性能に優れた消臭剤 |
JP2010260045A (ja) * | 2009-04-09 | 2010-11-18 | Toyota Boshoku Corp | 表皮材 |
JP2016171875A (ja) | 2015-03-17 | 2016-09-29 | 三菱製紙株式会社 | 脱臭剤封入濾材 |
JP2017064048A (ja) * | 2015-09-30 | 2017-04-06 | 住江織物株式会社 | 消臭剤及び該消臭剤を備えた消臭フィルター |
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JPH0810315A (ja) * | 1994-06-28 | 1996-01-16 | Midori Anzen Co Ltd | 空気浄化剤およびこれを用いた空気清浄機用脱臭フィルター |
JP2008148804A (ja) | 2006-12-15 | 2008-07-03 | Suminoe Textile Co Ltd | たばこ臭の除去性能に優れた消臭剤 |
JP2010260045A (ja) * | 2009-04-09 | 2010-11-18 | Toyota Boshoku Corp | 表皮材 |
JP2016171875A (ja) | 2015-03-17 | 2016-09-29 | 三菱製紙株式会社 | 脱臭剤封入濾材 |
JP2017064048A (ja) * | 2015-09-30 | 2017-04-06 | 住江織物株式会社 | 消臭剤及び該消臭剤を備えた消臭フィルター |
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