JPS62244444A - Oxygen scavenger - Google Patents
Oxygen scavengerInfo
- Publication number
- JPS62244444A JPS62244444A JP8889486A JP8889486A JPS62244444A JP S62244444 A JPS62244444 A JP S62244444A JP 8889486 A JP8889486 A JP 8889486A JP 8889486 A JP8889486 A JP 8889486A JP S62244444 A JPS62244444 A JP S62244444A
- Authority
- JP
- Japan
- Prior art keywords
- powder
- oxygen
- weight
- electrolyte
- water
- 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
- 229940123973 Oxygen scavenger Drugs 0.000 title claims abstract description 42
- 239000000843 powder Substances 0.000 claims abstract description 82
- 239000001301 oxygen Substances 0.000 claims abstract description 42
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 42
- 229910052751 metal Inorganic materials 0.000 claims abstract description 40
- 239000002184 metal Substances 0.000 claims abstract description 40
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 39
- 239000003792 electrolyte Substances 0.000 claims abstract description 35
- 229920000642 polymer Polymers 0.000 claims abstract description 27
- 238000006243 chemical reaction Methods 0.000 claims abstract description 25
- 230000002000 scavenging effect Effects 0.000 claims abstract description 8
- 239000006096 absorbing agent Substances 0.000 claims description 27
- 230000008961 swelling Effects 0.000 claims description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 29
- 239000002245 particle Substances 0.000 abstract description 24
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 abstract description 15
- 239000000203 mixture Substances 0.000 abstract description 11
- 229910052742 iron Inorganic materials 0.000 abstract description 5
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 abstract description 4
- 229920002239 polyacrylonitrile Polymers 0.000 abstract description 4
- 229920002472 Starch Polymers 0.000 abstract description 3
- 239000008107 starch Substances 0.000 abstract description 3
- 235000019698 starch Nutrition 0.000 abstract description 3
- 229920002134 Carboxymethyl cellulose Polymers 0.000 abstract description 2
- 229910001508 alkali metal halide Inorganic materials 0.000 abstract description 2
- 150000008045 alkali metal halides Chemical class 0.000 abstract description 2
- 229910001615 alkaline earth metal halide Inorganic materials 0.000 abstract description 2
- 239000001768 carboxy methyl cellulose Substances 0.000 abstract description 2
- 235000010948 carboxy methyl cellulose Nutrition 0.000 abstract description 2
- 239000008112 carboxymethyl-cellulose Substances 0.000 abstract description 2
- 229910017052 cobalt Inorganic materials 0.000 abstract description 2
- 239000010941 cobalt Substances 0.000 abstract description 2
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 abstract description 2
- 229910052759 nickel Inorganic materials 0.000 abstract description 2
- 108010009736 Protein Hydrolysates Proteins 0.000 abstract 1
- 229940105329 carboxymethylcellulose Drugs 0.000 abstract 1
- 238000013329 compounding Methods 0.000 abstract 1
- 238000010008 shearing Methods 0.000 abstract 1
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 14
- 239000007789 gas Substances 0.000 description 14
- XTEGARKTQYYJKE-UHFFFAOYSA-M Chlorate Chemical compound [O-]Cl(=O)=O XTEGARKTQYYJKE-UHFFFAOYSA-M 0.000 description 10
- 230000009257 reactivity Effects 0.000 description 10
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 8
- OSVXSBDYLRYLIG-UHFFFAOYSA-N dioxidochlorine(.) Chemical compound O=Cl=O OSVXSBDYLRYLIG-UHFFFAOYSA-N 0.000 description 8
- -1 inorganic acid salts Chemical class 0.000 description 8
- 239000011148 porous material Substances 0.000 description 8
- 235000002639 sodium chloride Nutrition 0.000 description 8
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 5
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 5
- 239000000460 chlorine Substances 0.000 description 5
- 229910052801 chlorine Inorganic materials 0.000 description 5
- 235000013305 food Nutrition 0.000 description 5
- BAUYGSIQEAFULO-UHFFFAOYSA-L iron(2+) sulfate (anhydrous) Chemical compound [Fe+2].[O-]S([O-])(=O)=O BAUYGSIQEAFULO-UHFFFAOYSA-L 0.000 description 5
- 239000004570 mortar (masonry) Substances 0.000 description 5
- 239000000047 product Substances 0.000 description 5
- UKLNMMHNWFDKNT-UHFFFAOYSA-M sodium chlorite Chemical compound [Na+].[O-]Cl=O UKLNMMHNWFDKNT-UHFFFAOYSA-M 0.000 description 5
- 229960002218 sodium chlorite Drugs 0.000 description 5
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- 239000004155 Chlorine dioxide Substances 0.000 description 4
- 230000002378 acidificating effect Effects 0.000 description 4
- 239000007864 aqueous solution Substances 0.000 description 4
- 235000019398 chlorine dioxide Nutrition 0.000 description 4
- 229920001577 copolymer Polymers 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 229910000359 iron(II) sulfate Inorganic materials 0.000 description 4
- 150000007524 organic acids Chemical class 0.000 description 4
- 229920003023 plastic Polymers 0.000 description 4
- 239000004033 plastic Substances 0.000 description 4
- 150000003839 salts Chemical class 0.000 description 4
- DWAQJAXMDSEUJJ-UHFFFAOYSA-M Sodium bisulfite Chemical compound [Na+].OS([O-])=O DWAQJAXMDSEUJJ-UHFFFAOYSA-M 0.000 description 3
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 3
- LSNNMFCWUKXFEE-UHFFFAOYSA-N Sulfurous acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 description 3
- 239000002253 acid Substances 0.000 description 3
- OSGAYBCDTDRGGQ-UHFFFAOYSA-L calcium sulfate Chemical compound [Ca+2].[O-]S([O-])(=O)=O OSGAYBCDTDRGGQ-UHFFFAOYSA-L 0.000 description 3
- 239000003795 chemical substances by application Substances 0.000 description 3
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- 239000011790 ferrous sulphate Substances 0.000 description 3
- 235000003891 ferrous sulphate Nutrition 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 150000002926 oxygen Chemical class 0.000 description 3
- 239000011780 sodium chloride Substances 0.000 description 3
- 229940079827 sodium hydrogen sulfite Drugs 0.000 description 3
- 235000010267 sodium hydrogen sulphite Nutrition 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- WCLKSQYCWXZMGX-UHFFFAOYSA-N 1,2,3,4-tetrabromo-5,6-dimethoxybenzene Chemical compound COC1=C(Br)C(Br)=C(Br)C(Br)=C1OC WCLKSQYCWXZMGX-UHFFFAOYSA-N 0.000 description 2
- 239000004154 Calcium bromate Substances 0.000 description 2
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 2
- 229920000742 Cotton Polymers 0.000 description 2
- IMROMDMJAWUWLK-UHFFFAOYSA-N Ethenol Chemical compound OC=C IMROMDMJAWUWLK-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- TWRXJAOTZQYOKJ-UHFFFAOYSA-L Magnesium chloride Chemical compound [Mg+2].[Cl-].[Cl-] TWRXJAOTZQYOKJ-UHFFFAOYSA-L 0.000 description 2
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 2
- CSNNHWWHGAXBCP-UHFFFAOYSA-L Magnesium sulfate Chemical compound [Mg+2].[O-][S+2]([O-])([O-])[O-] CSNNHWWHGAXBCP-UHFFFAOYSA-L 0.000 description 2
- 229910021536 Zeolite Inorganic materials 0.000 description 2
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 2
- 238000009825 accumulation Methods 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
- VSCWAEJMTAWNJL-UHFFFAOYSA-K aluminium trichloride Chemical compound Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 description 2
- 229910021529 ammonia Inorganic materials 0.000 description 2
- 150000003863 ammonium salts Chemical class 0.000 description 2
- 239000002585 base Substances 0.000 description 2
- 235000019397 calcium bromate Nutrition 0.000 description 2
- 239000001110 calcium chloride Substances 0.000 description 2
- 229910001628 calcium chloride Inorganic materials 0.000 description 2
- 229910001919 chlorite Inorganic materials 0.000 description 2
- 229910052619 chlorite group Inorganic materials 0.000 description 2
- QBWCMBCROVPCKQ-UHFFFAOYSA-N chlorous acid Chemical compound OCl=O QBWCMBCROVPCKQ-UHFFFAOYSA-N 0.000 description 2
- 229910052802 copper Inorganic materials 0.000 description 2
- 239000010949 copper Substances 0.000 description 2
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 230000001771 impaired effect Effects 0.000 description 2
- FBAFATDZDUQKNH-UHFFFAOYSA-M iron chloride Chemical compound [Cl-].[Fe] FBAFATDZDUQKNH-UHFFFAOYSA-M 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 235000005985 organic acids Nutrition 0.000 description 2
- 229920000058 polyacrylate Polymers 0.000 description 2
- 239000000377 silicon dioxide Substances 0.000 description 2
- JHJLBTNAGRQEKS-UHFFFAOYSA-M sodium bromide Chemical compound [Na+].[Br-] JHJLBTNAGRQEKS-UHFFFAOYSA-M 0.000 description 2
- JQWHASGSAFIOCM-UHFFFAOYSA-M sodium periodate Chemical compound [Na+].[O-]I(=O)(=O)=O JQWHASGSAFIOCM-UHFFFAOYSA-M 0.000 description 2
- 150000003467 sulfuric acid derivatives Chemical class 0.000 description 2
- ZSUXOVNWDZTCFN-UHFFFAOYSA-L tin(ii) bromide Chemical compound Br[Sn]Br ZSUXOVNWDZTCFN-UHFFFAOYSA-L 0.000 description 2
- 239000010457 zeolite Substances 0.000 description 2
- 229910052725 zinc Inorganic materials 0.000 description 2
- 239000011701 zinc Substances 0.000 description 2
- WHQOKFZWSDOTQP-UHFFFAOYSA-N 2,3-dihydroxypropyl 4-aminobenzoate Chemical compound NC1=CC=C(C(=O)OCC(O)CO)C=C1 WHQOKFZWSDOTQP-UHFFFAOYSA-N 0.000 description 1
- BZSXEZOLBIJVQK-UHFFFAOYSA-N 2-methylsulfonylbenzoic acid Chemical compound CS(=O)(=O)C1=CC=CC=C1C(O)=O BZSXEZOLBIJVQK-UHFFFAOYSA-N 0.000 description 1
- 239000005995 Aluminium silicate Substances 0.000 description 1
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 1
- ZKQDCIXGCQPQNV-UHFFFAOYSA-N Calcium hypochlorite Chemical compound [Ca+2].Cl[O-].Cl[O-] ZKQDCIXGCQPQNV-UHFFFAOYSA-N 0.000 description 1
- 229920000298 Cellophane Polymers 0.000 description 1
- 229910021589 Copper(I) bromide Inorganic materials 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- 229910021575 Iron(II) bromide Inorganic materials 0.000 description 1
- 239000005909 Kieselgur Substances 0.000 description 1
- CERQOIWHTDAKMF-UHFFFAOYSA-M Methacrylate Chemical compound CC(=C)C([O-])=O CERQOIWHTDAKMF-UHFFFAOYSA-M 0.000 description 1
- 229910020108 MgCu2 Inorganic materials 0.000 description 1
- 239000007832 Na2SO4 Substances 0.000 description 1
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- 229910019142 PO4 Inorganic materials 0.000 description 1
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 1
- 239000005708 Sodium hypochlorite Substances 0.000 description 1
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 description 1
- GFZPUGCMGGUPHH-UHFFFAOYSA-N [I].[Na] Chemical compound [I].[Na] GFZPUGCMGGUPHH-UHFFFAOYSA-N 0.000 description 1
- 239000002250 absorbent Substances 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 229940048053 acrylate Drugs 0.000 description 1
- BAPJBEWLBFYGME-UHFFFAOYSA-N acrylic acid methyl ester Natural products COC(=O)C=C BAPJBEWLBFYGME-UHFFFAOYSA-N 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 235000012211 aluminium silicate Nutrition 0.000 description 1
- SWLVFNYSXGMGBS-UHFFFAOYSA-N ammonium bromide Chemical compound [NH4+].[Br-] SWLVFNYSXGMGBS-UHFFFAOYSA-N 0.000 description 1
- 235000011114 ammonium hydroxide Nutrition 0.000 description 1
- 229910052925 anhydrite Inorganic materials 0.000 description 1
- 229910001620 barium bromide Inorganic materials 0.000 description 1
- NKQIMNKPSDEDMO-UHFFFAOYSA-L barium bromide Chemical compound [Br-].[Br-].[Ba+2] NKQIMNKPSDEDMO-UHFFFAOYSA-L 0.000 description 1
- 239000011324 bead Substances 0.000 description 1
- 239000000440 bentonite Substances 0.000 description 1
- 229910000278 bentonite Inorganic materials 0.000 description 1
- SVPXDRXYRYOSEX-UHFFFAOYSA-N bentoquatam Chemical compound O.O=[Si]=O.O=[Al]O[Al]=O SVPXDRXYRYOSEX-UHFFFAOYSA-N 0.000 description 1
- YALMXYPQBUJUME-UHFFFAOYSA-L calcium chlorate Chemical compound [Ca+2].[O-]Cl(=O)=O.[O-]Cl(=O)=O YALMXYPQBUJUME-UHFFFAOYSA-L 0.000 description 1
- 150000007942 carboxylates Chemical class 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 229910052570 clay Inorganic materials 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 239000013256 coordination polymer Substances 0.000 description 1
- 239000008151 electrolyte solution Substances 0.000 description 1
- NPERTKSDHFSDLC-UHFFFAOYSA-N ethenol;prop-2-enoic acid Chemical compound OC=C.OC(=O)C=C NPERTKSDHFSDLC-UHFFFAOYSA-N 0.000 description 1
- 229910052736 halogen Inorganic materials 0.000 description 1
- 150000002367 halogens Chemical class 0.000 description 1
- 239000005457 ice water Substances 0.000 description 1
- 229910010272 inorganic material Inorganic materials 0.000 description 1
- 239000011147 inorganic material Substances 0.000 description 1
- 229910000358 iron sulfate Inorganic materials 0.000 description 1
- GYCHYNMREWYSKH-UHFFFAOYSA-L iron(ii) bromide Chemical compound [Fe+2].[Br-].[Br-] GYCHYNMREWYSKH-UHFFFAOYSA-L 0.000 description 1
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 description 1
- 229910001629 magnesium chloride Inorganic materials 0.000 description 1
- 239000000395 magnesium oxide Substances 0.000 description 1
- 229910052943 magnesium sulfate Inorganic materials 0.000 description 1
- 235000019341 magnesium sulphate Nutrition 0.000 description 1
- WPBNNNQJVZRUHP-UHFFFAOYSA-L manganese(2+);methyl n-[[2-(methoxycarbonylcarbamothioylamino)phenyl]carbamothioyl]carbamate;n-[2-(sulfidocarbothioylamino)ethyl]carbamodithioate Chemical compound [Mn+2].[S-]C(=S)NCCNC([S-])=S.COC(=O)NC(=S)NC1=CC=CC=C1NC(=S)NC(=O)OC WPBNNNQJVZRUHP-UHFFFAOYSA-L 0.000 description 1
- 150000001247 metal acetylides Chemical class 0.000 description 1
- 229910001507 metal halide Inorganic materials 0.000 description 1
- 150000005309 metal halides Chemical class 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- NALMPLUMOWIVJC-UHFFFAOYSA-N n,n,4-trimethylbenzeneamine oxide Chemical compound CC1=CC=C([N+](C)(C)[O-])C=C1 NALMPLUMOWIVJC-UHFFFAOYSA-N 0.000 description 1
- 239000011368 organic material Substances 0.000 description 1
- 239000010451 perlite Substances 0.000 description 1
- 235000019362 perlite Nutrition 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 235000021317 phosphate Nutrition 0.000 description 1
- 150000003013 phosphoric acid derivatives Chemical class 0.000 description 1
- 239000002985 plastic film Substances 0.000 description 1
- 229920006255 plastic film Polymers 0.000 description 1
- VKJKEPKFPUWCAS-UHFFFAOYSA-M potassium chlorate Chemical compound [K+].[O-]Cl(=O)=O VKJKEPKFPUWCAS-UHFFFAOYSA-M 0.000 description 1
- SATVIFGJTRRDQU-UHFFFAOYSA-N potassium hypochlorite Chemical compound [K+].Cl[O-] SATVIFGJTRRDQU-UHFFFAOYSA-N 0.000 description 1
- JLKDVMWYMMLWTI-UHFFFAOYSA-M potassium iodate Chemical compound [K+].[O-]I(=O)=O JLKDVMWYMMLWTI-UHFFFAOYSA-M 0.000 description 1
- 239000001230 potassium iodate Substances 0.000 description 1
- 235000006666 potassium iodate Nutrition 0.000 description 1
- 229940093930 potassium iodate Drugs 0.000 description 1
- VISKNDGJUCDNMS-UHFFFAOYSA-M potassium;chlorite Chemical compound [K+].[O-]Cl=O VISKNDGJUCDNMS-UHFFFAOYSA-M 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 229940047670 sodium acrylate Drugs 0.000 description 1
- XUXNAKZDHHEHPC-UHFFFAOYSA-M sodium bromate Chemical compound [Na+].[O-]Br(=O)=O XUXNAKZDHHEHPC-UHFFFAOYSA-M 0.000 description 1
- SUKJFIGYRHOWBL-UHFFFAOYSA-N sodium hypochlorite Chemical compound [Na+].Cl[O-] SUKJFIGYRHOWBL-UHFFFAOYSA-N 0.000 description 1
- 239000011697 sodium iodate Substances 0.000 description 1
- 235000015281 sodium iodate Nutrition 0.000 description 1
- 229940032753 sodium iodate Drugs 0.000 description 1
- BAZAXWOYCMUHIX-UHFFFAOYSA-M sodium perchlorate Chemical compound [Na+].[O-]Cl(=O)(=O)=O BAZAXWOYCMUHIX-UHFFFAOYSA-M 0.000 description 1
- 229910001488 sodium perchlorate Inorganic materials 0.000 description 1
- 229910052938 sodium sulfate Inorganic materials 0.000 description 1
- 235000011152 sodium sulphate Nutrition 0.000 description 1
- CRWJEUDFKNYSBX-UHFFFAOYSA-N sodium;hypobromite Chemical compound [Na+].Br[O-] CRWJEUDFKNYSBX-UHFFFAOYSA-N 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 150000003871 sulfonates Chemical class 0.000 description 1
- 229910052723 transition metal Inorganic materials 0.000 description 1
- 150000003624 transition metals Chemical class 0.000 description 1
- 239000010455 vermiculite Substances 0.000 description 1
- 229910052902 vermiculite Inorganic materials 0.000 description 1
- 235000019354 vermiculite Nutrition 0.000 description 1
Abstract
Description
【発明の詳細な説明】 〔技術分野〕 本発明は脱酸素剤に関するものである。[Detailed description of the invention] 〔Technical field〕 The present invention relates to an oxygen scavenger.
従来、鉄粉、銅、亜鉛等の被酸化性金属の粉末を主剤と
する脱酸素剤は種々提案されており、それらの中で、金
属粉末成分と電解質成分との乾燥状態混合物からなる脱
酸素剤が知らている(特開昭56−17633号公報)
。このような脱酸素剤は、乾燥空気中や、低湿度の空気
中ではその脱酸素反応は抑制され、安定であるが、高湿
度の空気中では、空気中水分を吸湿して脱酸素反応を開
始し、空気中酸素を吸収する。しかしながら、このよう
な脱酸素剤は、高湿度下においては、良好な脱酸素反応
を示すものの、それに用いた電解質の作用により、比較
的短期間で過剰の水分を吸湿して、その脱酸素反応が著
しく抑制されたり、あるいは脱酸素反応が停止するとい
う欠点があることが判明した。例えば、前記した脱酸素
剤(鉄粉100重量部と食塩10重量部との混合物を通
気性小袋に充填したもの)を、水分活性の高い食品(例
えば、切もち等)と共にプラスチック袋に入れて封止し
た場合、その袋内の相対湿度は100%になることから
、脱酸素剤は円滑に脱酸素反応を開始し、そのプラスチ
ック袋内の酸素濃度は12時間以内に1%以下に低下す
るが、1力月以」二経過すると、脱酸素剤は、脱酸素反
応に対して過剰の水分を吸湿し、その結果、脱酸素反応
は実質的に停止してしまい、脱酸素剤はその機能を実質
的に失う。特に、この傾向は、脱酸素剤を充填した小袋
が水分活性の高い食品と接触した時に著しい。一方、商
品は、製造から消費者の手にわたるまでに1力月以上も
要する場合もあり、従って、それに適用した脱酸素剤は
、その流通の間十分に脱酸素機能を保持することが要求
される。Conventionally, various oxygen scavengers based on powders of oxidizable metals such as iron powder, copper, and zinc have been proposed. agent is known (Japanese Unexamined Patent Publication No. 17633/1983)
. The deoxidizing reaction of such oxygen absorbers is suppressed and stable in dry air or low humidity air, but in high humidity air, they absorb moisture in the air and perform the deoxidizing reaction. Start and absorb oxygen from the air. However, although such oxygen scavengers exhibit a good deoxidation reaction under high humidity, due to the action of the electrolyte used in them, they absorb excess moisture in a relatively short period of time, causing the deoxidation reaction to deteriorate. It has been found that there are disadvantages in that the deoxidizing reaction is significantly inhibited or the deoxidizing reaction is stopped. For example, the above-mentioned oxygen absorber (a mixture of 100 parts by weight of iron powder and 10 parts by weight of common salt filled in a breathable pouch) may be placed in a plastic bag along with foods with high water activity (for example, cut rice cakes, etc.). When sealed, the relative humidity inside the bag will be 100%, so the oxygen absorber will smoothly start the deoxidizing reaction, and the oxygen concentration inside the plastic bag will drop to 1% or less within 12 hours. However, after one month or two has passed, the oxygen scavenger absorbs excess moisture relative to the oxygen scavenging reaction, and as a result, the oxygen scavenging reaction substantially stops, and the oxygen scavenger stops functioning. substantially lost. This tendency is particularly noticeable when sachets filled with oxygen scavengers come into contact with foods with high water activity. On the other hand, it may take more than a month for a product to reach the consumer from its manufacture, so the oxygen scavenger applied to it is required to maintain its oxygen scavenging function sufficiently during distribution. Ru.
本発明は、従来の脱酸素剤に見られる前記欠点を克服し
、高湿度下において、長期間にわたってその脱酸素反応
を継続し得る脱酸素剤を提供することを目的とする。The present invention aims to overcome the above-mentioned drawbacks of conventional oxygen scavengers and to provide an oxygen scavenger that can continue its oxygen scavenging reaction over a long period of time under high humidity.
本発明によれば、被酸化性金属粉末成分と電解質成分と
の組合せからなる高湿度下で脱酸素反応を示す脱酸素剤
において、該脱酸素剤中に水吸収膨潤性高分子粉末を含
有させたことを特徴とする脱酸素剤が提供される。According to the present invention, in an oxygen scavenger that exhibits a deoxidizing reaction under high humidity and is made of a combination of an oxidizable metal powder component and an electrolyte component, the oxygen scavenger contains a water-absorbing swelling polymer powder. An oxygen scavenger is provided.
本発明においては、従来の金属粉末と電解質成分との組
合せからなる実質状乾燥混合物状態にあり、高湿度下で
脱酸素反応を示す脱酸素剤に見られる前記欠点を克服す
るために、水吸収膨潤性高分子粉末を添加することを特
徴とする。この場合、水吸収膨潤性高分子は、電解質に
よって吸湿される脱酸素反応に過剰の水分を吸収し、脱
酸素剤系の水分を所要範囲に保持し、高湿度下において
も長期間にわたって円滑に脱酸素反応を進行させる作用
を示す。In the present invention, in order to overcome the above-mentioned drawbacks of oxygen scavengers that are in the form of a substantially dry mixture consisting of a combination of metal powder and electrolyte components and exhibit oxygen scavenging reactions under high humidity, we have developed It is characterized by adding swellable polymer powder. In this case, the water-absorbing swelling polymer absorbs excess water in the deoxidation reaction caused by the electrolyte, maintains the moisture in the oxygen scavenger system within the required range, and smoothly maintains the moisture content for long periods of time even under high humidity. Shows the action of advancing the deoxidizing reaction.
本発明で用いる金属の粉末は、被酸化性金属の粉末であ
ればよく、従来公知の種々のものが使用され、このよう
なものとしては、例えば、鉄、コバルト、ニッケル、マ
ンガン、亜鉛、銅等の遷移金属の粉末の他、それらの合
金及び炭化物等が挙げられるが、一般には、鉄粉が使用
される。この場合、鉄粉は、純鉄である必要はなく、鉄
を主成分とすればよく、例えば、イオウやリン酸分等の
不純物を含むものや、フェロニッケル、炭化鉄等の合金
であってもよい。また、この鉄粉は種々の方法で製造さ
れたものであってよく1例えば、還元粉、電解粉、噴霧
粉、破砕粉等であることができる。被酸化性金属粉末の
粒径は、一般には、1.50μm以下、好ましくけ10
0〜10μmの範囲である。The metal powder used in the present invention may be any oxidizable metal powder, and various conventionally known metal powders may be used, such as iron, cobalt, nickel, manganese, zinc, copper, etc. In addition to powders of transition metals such as, alloys and carbides thereof, iron powders are generally used. In this case, the iron powder does not need to be pure iron, but only needs to have iron as its main component. Good too. Further, this iron powder may be manufactured by various methods, such as reduced powder, electrolytic powder, spray powder, crushed powder, etc. The particle size of the oxidizable metal powder is generally 1.50 μm or less, preferably 10 μm or less.
It is in the range of 0 to 10 μm.
本発明で用いる電解質としては、種々の有機酸又は無機
酸の塩が用いられ、このようなものとしでは、例えば、
NaCQ 、 KCfl 、 NaBr、にBrなどの
アルカリ金属ハロゲン化物、MgCu 2、CaCn2
、CaBr2MgBr2、BaBr2などのアルカリ土
類金属のハロゲン化物の他、AgCQ 2、ZnCQ
2、AQCQ3、SnCQ 2゜MnCQ 2、FeC
l13. CaCO2、NxCQ 2、CuCQ 、Z
nBr2、SnBr2、CuBr、 FeBr2などの
各種金属ハロゲン化物、さらにNa2SO4、K2S0
.、CaSO4、MgSO4、Al12(SO4)aN
j、SO−、FeSO4などの各種硫酸塩、NH4CQ
、 NH4Br、(Ni1. )2SO4などの各種
アンモニウム塩、過塩素酸ナトリウム、過塩素酸カルシ
ウム、過ヨウ素酸ナトリウム、塩素酸ナトリウム、塩素
酸カリウム、塩素酸カルシウム、臭素酸ナトリウム、臭
素酸カルシウム、ヨウ素酸ナトリウム、臭素酸カルシウ
ム、ヨウ素酸ナトリウム、ヨウ素酸カリウム、亜塩素酸
ナトリウム、亜塩素酸カリウム、次亜塩素酸ナトリウム
、次亜塩素酸カリウム、次亜塩素酸カルシウム、次亜臭
素酸ナトリウム等のハロゲン含有酸素酸塩等が挙げられ
る。電解質粉末の粒径は、一般には、1.50μm以下
、好ましくは100〜10μmの範囲である。このよう
な電解質粉末は、金属酸分100重量部に対し、0.0
1〜10重量部、好ましくは0.1〜2重量%の割合で
用いられる。As the electrolyte used in the present invention, various organic or inorganic acid salts are used, such as, for example,
Alkali metal halides such as NaCQ, KCfl, NaBr, and Br, MgCu2, CaCn2
In addition to alkaline earth metal halides such as CaBr2MgBr2 and BaBr2, AgCQ2, ZnCQ
2, AQCQ3, SnCQ 2゜MnCQ 2, FeC
l13. CaCO2, NxCQ2, CuCQ, Z
Various metal halides such as nBr2, SnBr2, CuBr, FeBr2, as well as Na2SO4, K2S0
.. , CaSO4, MgSO4, Al12(SO4)aN
j, SO-, various sulfates such as FeSO4, NH4CQ
, NH4Br, various ammonium salts such as (Ni1.)2SO4, sodium perchlorate, calcium perchlorate, sodium periodate, sodium chlorate, potassium chlorate, calcium chlorate, sodium bromate, calcium bromate, iodine sodium acid, calcium bromate, sodium iodate, potassium iodate, sodium chlorite, potassium chlorite, sodium hypochlorite, potassium hypochlorite, calcium hypochlorite, sodium hypobromite, etc. Examples include halogen-containing oxyacid salts. The particle size of the electrolyte powder is generally 1.50 μm or less, preferably in the range of 100 to 10 μm. Such electrolyte powder has a content of 0.0 parts by weight per 100 parts by weight of metal acid.
It is used in an amount of 1 to 10 parts by weight, preferably 0.1 to 2% by weight.
本発明において、脱酸素反応開始の早い脱酸素剤を得る
には、電解質としては、例えば、塩化カルシウム、塩化
マグネシウム、塩化鉄、塩化アルミニウム、粗製食塩等
のような潮解性を有するものあるいはこれを含む電解質
の使用が好ましい。In the present invention, in order to obtain an oxygen scavenger that starts the oxygen scavenging reaction quickly, the electrolyte should be one that has deliquescent properties such as calcium chloride, magnesium chloride, iron chloride, aluminum chloride, crude common salt, etc. The use of electrolytes containing is preferred.
本発明で用いる水吸収膨潤性高分子粒子とは、水を吸収
し、膨潤する性質を有する高分子粒子を意味し、カルボ
ン酸塩、スルホン酸塩、リン酸塩5あるいはアンモニウ
ム塩等のイオン性基を高分子中に有するものである。こ
のような高分子は従来公知であり、例えば、高分子基材
別で分類すると、カルボキシメチルセルロース系、デン
プン/ポリアクリロニトリル加水分解物系、デンプン/
ポリアクリル酸塩架橋物系、酢酸ビニル/アクリル酸メ
チル共重合体ケン化物系、ポリアクリロニトリル加水分
解物系、ポリアクリル酸すトリウム架橋物系、ビニルア
ルコール/アクリル酸塩共重合体系、エチレン/メタク
リル酸塩共重合体系のもの等がある。これらの吸水膨潤
性高分子粒子は、その自重の200倍以上、高吸水性の
ものでは1000倍程度0水分を吸収する。本発明にお
いては、一般的には、自重の20倍以上、好ましくは5
0倍0」−の吸水性を示すものであれば使用可能である
。The water-absorbing and swelling polymer particles used in the present invention refer to polymer particles that have the property of absorbing water and swelling, and include ionic salts such as carboxylates, sulfonates, phosphates, or ammonium salts. It has a group in the polymer. Such polymers are conventionally known, and for example, when classified by polymer base material, there are carboxymethyl cellulose, starch/polyacrylonitrile hydrolyzate, and starch/polyacrylonitrile hydrolyzate.
Polyacrylate crosslinked product system, saponified vinyl acetate/methyl acrylate copolymer system, polyacrylonitrile hydrolyzate system, polyacrylate crosslinked product system, vinyl alcohol/acrylate copolymer system, ethylene/methacrylate There are acid-acid copolymer types, etc. These water-absorbing and swelling polymer particles absorb water at least 200 times their own weight, and in the case of highly water-absorbent particles, about 1000 times their own weight. In the present invention, generally 20 times or more of its own weight, preferably 5
Any material that exhibits a water absorbency of 0 times 0'' can be used.
本発明で用いる吸水膨潤性高分子粒子は、微粉末状のも
のであればよく、一般には、100μm〜1mm程度の
粒径を有するものが用いられる。この吸水膨潤性高分子
粒子の使用割合は、被酸化性金属成分100重量部に対
し、0.1〜10重量部、好ましくは0.5〜5重量部
の範囲である。その使用割合が多すぎると、得られる脱
酸素剤の反応性が悪くなる傾向を示し、少なすぎると有
効な水分吸収を行うことができなくなる。脱酸素剤を水
分活性の高い食品と接触させた場合、その脱酸素剤を被
包する通気性の袋を介して水分が浸透してくるが、本発
明の脱酸素剤はこのようにして浸透してくる水分によっ
てもその脱酸素反応は阻害されない。本発明者らによれ
ば、金属粉末と電解質との混合物からなる脱酸素剤の場
合、その重量の20%以」ユもの水分が脱酸素剤中に混
入してくると、もはや脱酸素剤としての使用が不可能に
なることが見出されたが、本発明の脱酸素剤では、それ
に添加した小吸収膨潤性高分子粒子の作用により、20
%以上もの水分が混入しても、その脱酸素反応性は損わ
れない。The water-absorbing and swelling polymer particles used in the present invention may be in the form of fine powder, and generally have a particle size of about 100 μm to 1 mm. The proportion of water-absorbing and swelling polymer particles to be used is in the range of 0.1 to 10 parts by weight, preferably 0.5 to 5 parts by weight, per 100 parts by weight of the oxidizable metal component. If the proportion used is too high, the reactivity of the oxygen scavenger obtained tends to deteriorate, and if the proportion is too small, effective moisture absorption cannot be carried out. When an oxygen absorber is brought into contact with foods with high water activity, moisture permeates through the air-permeable bag that encloses the oxygen absorber. The deoxidizing reaction is not inhibited by the moisture that comes in. According to the present inventors, in the case of an oxygen scavenger made of a mixture of metal powder and electrolyte, if more than 20% of the weight of water is mixed into the oxygen scavenger, it can no longer be used as an oxygen scavenger. However, in the oxygen scavenger of the present invention, due to the action of the small absorbing and swelling polymer particles added to it, the use of 20
Even if more than 30% of water is mixed in, its deoxidizing reactivity is not impaired.
本発明の脱酸素剤を製造するには、前記した被酸化性金
属粉末、電解質粉末及び水吸収膨潤性高分子粉末を混合
すればよい。この場合、混合機としては、各成分相互の
接触を緊密にさせるために、マサツ円板ミルや、ヘンセ
ルミキサー等のマ勺ツカ及び/又は剪断力を作用させる
混合装置を用いるのが好ましい。In order to produce the oxygen scavenger of the present invention, the above-described oxidizable metal powder, electrolyte powder, and water-absorbing swelling polymer powder may be mixed. In this case, as the mixer, in order to bring each component into close contact with each other, it is preferable to use a mixing device that applies a force and/or shear force, such as a Masatsu disk mill or a Hensel mixer.
本発明の脱酸素剤においては種々の変更が可能であり、
電解質は、あらかじめ、被酸化性金属粉末表面に被覆さ
せることも有効である。このような表面に電解質を被覆
した金属粉末は、電解質の水溶液と金属粉末とを混合し
、乾燥することによって製造し得る他、塩酸、硫酸ある
いは有機酸等の酸性物質の水溶液と金属粉末とを混合し
、金属粉末表面に酸性物質を反応させた後、乾燥する方
法等がある。このような表面に電解質の被覆された金属
粉は、前記した金属粉末と電解質との混合物と同様に、
高湿度下において空気中酸素と反応する。また、このよ
うな表面に電解質の被覆された金属粉末も、長時間高湿
度下に保持すると、脱酸素反応に適する以上の水分を吸
湿し、その脱酸素反応が阻害されるようになる。本発明
の原理は、このような表面に電解質の被覆された金属粉
末からなる脱酸素剤に対しても適用し得るものである。Various changes are possible in the oxygen scavenger of the present invention,
It is also effective to coat the surface of the oxidizable metal powder with the electrolyte in advance. Such metal powder whose surface is coated with electrolyte can be produced by mixing an aqueous electrolyte solution and metal powder and drying it, or by mixing an aqueous solution of an acidic substance such as hydrochloric acid, sulfuric acid, or an organic acid with metal powder. There is a method of mixing, reacting an acidic substance on the surface of the metal powder, and then drying. Such metal powder whose surface is coated with electrolyte is similar to the above-mentioned mixture of metal powder and electrolyte,
Reacts with atmospheric oxygen under high humidity. Further, if such a metal powder whose surface is coated with an electrolyte is kept under high humidity for a long time, it will absorb more moisture than is suitable for the deoxidation reaction, and the deoxidation reaction will be inhibited. The principles of the present invention can also be applied to such an oxygen scavenger made of metal powder whose surface is coated with an electrolyte.
この場合、表面に被覆される電解質成分の割合量は、金
属粉末100重量部に対し、0.01〜10重量部、好
ましくは、0.1〜1重量部程度である。In this case, the proportion of the electrolyte component coated on the surface is about 0.01 to 10 parts by weight, preferably about 0.1 to 1 part by weight, based on 100 parts by weight of the metal powder.
また、本発明の脱酸素剤においては、必要に応じ、多孔
性物質粉末を適量、例えば、金属粉末100重量部に対
し、0.05〜5重量部、好ましくは0.01〜2重量
部程度加えることができる。この場合、多孔性物質粉末
の粒径は、一般には、150μm以下、好ましくは、1
00μm〜1μmの範囲であり、またこの多孔性物質粉
末には、電解質を担持させるのが好ましい。この電解質
の担持は、電解質の水溶液と多孔質物質粉末とを混合し
、水分15%以下程度に乾燥することによって実施され
る。前記多孔性物質としては、種々の有機又は無機系の
ものが用いられ、例えば、油性カーボン、活性炭、石炭
粉末、コークス、ゼオライト、パーライト、バーミキュ
ライト、黄土、ケイソウ土、ベントナイト、カオリン、
セピオライl−1白土、シリカ、アルミナ、マグネシア
、シリカ/アルミナ等が挙げられる。In addition, in the oxygen scavenger of the present invention, if necessary, an appropriate amount of porous material powder is added, for example, about 0.05 to 5 parts by weight, preferably about 0.01 to 2 parts by weight, per 100 parts by weight of metal powder. can be added. In this case, the particle size of the porous material powder is generally 150 μm or less, preferably 1
The porous material powder preferably supports an electrolyte. This electrolyte support is carried out by mixing an electrolyte aqueous solution and porous material powder, and drying the mixture to a moisture content of about 15% or less. Various organic or inorganic materials are used as the porous material, such as oily carbon, activated carbon, coal powder, coke, zeolite, perlite, vermiculite, loess, diatomaceous earth, bentonite, kaolin,
Examples include sepiolyte 1-1 clay, silica, alumina, magnesia, silica/alumina, and the like.
本発明の好ましい態様によれば、粒径150μm以下、
好ましくは100μm以下の金属粉末100重量部に対
し、粒径11007z以下、好ましくは50μm以下の
電解質粉末0.05〜5重景部、好ましくは0.1〜4
重量部及び粒径500μm以下、好ましくは200μm
以下の水吸収膨潤性高分子粉末0.1〜10重量部、好
ましくは0.5〜5重量ff1lからなる脱酸素剤が提
供される。According to a preferred embodiment of the present invention, the particle size is 150 μm or less,
Preferably, per 100 parts by weight of metal powder with a particle size of 100 μm or less, 0.05 to 5 parts of electrolyte powder with a particle size of 11007z or less, preferably 50 μm or less, preferably 0.1 to 4 parts by weight.
Part by weight and particle size 500 μm or less, preferably 200 μm
An oxygen scavenger consisting of 0.1 to 10 parts by weight, preferably 0.5 to 5 parts by weight of the following water-absorbing swelling polymer powder is provided.
本発明のさらに好ましい他の実施態様によれば、前記し
た本発明の脱酸素剤において、電解質粉末の少なくとも
一部として含塩素酸塩を用いたものが提供される。この
ような脱酸素剤は、高湿度下において水分を吸湿して脱
酸素反応を開始すると共に、さらに、添加した含塩素酸
塩から微量の殺菌性の塩素系ガスを発生する。例えば、
含塩素酸塩として亜塩素酸ナトリウム(NthCβ02
)を用いる時には、二酸化塩素ガス(c QO7)が発
生する。また、この含塩素酸塩に代えて、亜硫酸水素ナ
トリウムや亜硫酸す1ヘリウム等の亜硫酸塩を用いる時
には、亜硫酸ガスが発生する。従って、このような脱酸
素剤は、食品と共にプラスチック袋に密封封入した場合
、その袋内は脱酸素されると同時に、食品の表面殺菌も
行われる。According to another preferred embodiment of the present invention, there is provided an oxygen scavenger of the present invention described above, in which a chlorate is used as at least a portion of the electrolyte powder. Such an oxygen absorber absorbs moisture under high humidity and starts a deoxidizing reaction, and also generates a small amount of sterilizing chlorine-based gas from the added chlorate. for example,
Sodium chlorite (NthCβ02
), chlorine dioxide gas (cQO7) is generated. Furthermore, when a sulfite such as sodium hydrogen sulfite or monohelium sulfite is used in place of the chlorate, sulfur dioxide gas is generated. Therefore, when such an oxygen absorber is sealed together with food in a plastic bag, the inside of the bag is deoxidized and the surface of the food is sterilized at the same time.
このような塩素系ガスや亜硫酸ガスの発生は、酸性物質
、例えば、塩化鉄、塩化カルシウム、硫酸鉄、硫酸カル
シウム等の硫酸塩や固体状の有機酸又はその塩、硫酸や
有機酸を担持させた多孔性物質粉末等を加えることによ
って促進させることができる。このような脱酸素剤にお
いて、含塩素酸塩又は亜硫酸塩の使用量は、金属粉末1
00重量部に対し、通常、0.05〜10重量部、好ま
しくは0,1〜5重量部である。The generation of chlorine-based gas and sulfur dioxide gas is caused by acidic substances such as sulfates such as iron chloride, calcium chloride, iron sulfate, and calcium sulfate, solid organic acids or their salts, sulfuric acid, and organic acids supported. This can be promoted by adding porous material powder or the like. In such an oxygen scavenger, the amount of chlorate or sulfite used is 1
The amount is usually 0.05 to 10 parts by weight, preferably 0.1 to 5 parts by weight.
本発明において、含塩素酸塩や亜硫酸塩を金属粉末の存
在下で吸湿させて塩素系ガスや亜硫酸ガスを発生させる
ことは、その金属粉末の作用により過剰の塩素系ガスや
亜硫酸ガスの発生が抑制され、微量の塩素系ガスや亜硫
酸ガスが長期間にわたって安定的に発生することから非
常に有利である。In the present invention, generating chlorine-based gas or sulfur dioxide gas by absorbing moisture from chlorate or sulfite in the presence of metal powder means that excessive chlorine-based gas or sulfur dioxide gas is generated due to the action of the metal powder. This is very advantageous because trace amounts of chlorine-based gas and sulfur dioxide gas are generated stably over a long period of time.
本発明の脱酸素剤は、実質的に乾燥状態の混合物からな
るもので、乾燥空気中や低湿度空気中では安定であるが
、高湿度空気中では、空気中水分を吸湿し、脱酸素反応
を円滑に開始する。本発明の脱酸素剤は、水分5重量%
以下、好ましくは1重量%以下の乾燥状態で、通気性の
小袋に充填され、この脱酸素剤充填小袋は、非通気性の
プラスチック袋に密封保存される。The oxygen scavenger of the present invention consists of a mixture in a substantially dry state and is stable in dry air or low humidity air, but in high humidity air it absorbs moisture in the air and undergoes a deoxidizing reaction. Start smoothly. The oxygen scavenger of the present invention has a water content of 5% by weight.
Thereafter, the oxygen absorber is filled in a dry state, preferably at a concentration of 1% by weight or less, into a breathable pouch, and the oxygen scavenger-filled pouch is sealed and stored in a non-breathable plastic bag.
本発明の脱酸素剤は、前記構成であり、電解質を含む金
属粉末に対し、水吸収膨潤性高分子粒子を混合させたこ
とにより、電解質の過剰水分の吸湿によって、金属粉末
の表面がその水分によって湿潤されることが防止され、
高湿度空気中において、長期間にわたって、その脱酸素
反応を継続させることができる。The oxygen scavenger of the present invention has the above-mentioned structure, and by mixing water-absorbing and swelling polymer particles with a metal powder containing an electrolyte, the surface of the metal powder absorbs excess water from the electrolyte, causing the surface of the metal powder to absorb the water. is prevented from being wetted by
The deoxidizing reaction can be continued for a long period of time in high humidity air.
次に本発明を実施例によってさらに詳細に説明する。 Next, the present invention will be explained in more detail with reference to Examples.
実施例1
(1)脱N!素剤C1)の製造
(イ)金属粉末〔F〕:
金属粉末としては、150メツシュ通過量65重量%、
200メツシュ通過量50重量%の鉄粉を用いた。Example 1 (1) Get rid of N! Production of base material C1) (a) Metal powder [F]: As metal powder, the amount passing through 150 mesh is 65% by weight,
Iron powder having an amount of 50% by weight passing through 200 meshes was used.
(ロ)水吸収膨潤性高分子粉末〔P〕:市販のビニルア
ルコール/アクリル酸ナトリウム共重合体ビーズ(粒径
約0.5mm、住人化学社製、「スミカゲル」)を用い
た・
(ハ)電解質粉末〔E〕:
市販食塩(50メツシュ通過量4.5重量%、28メツ
シュ通過量80.5重量%)を乾燥し、粒度350メツ
シユ以下に微粉砕化したものを用いた。(b) Water-absorbing swelling polymer powder [P]: Commercially available vinyl alcohol/sodium acrylate copolymer beads (particle size approximately 0.5 mm, manufactured by Sumikagaku Co., Ltd., "Sumikagel") were used. (c) Electrolyte powder [E]: Commercially available salt (4.5% by weight passing through 50 meshes, 80.5% by weight passing through 28 meshes) was dried and pulverized to a particle size of 350 meshes or less.
(ニ)前記金属粉末[F]100重量部に対し、前記水
=12−
吸収膨潤性高分子(+)31重量部、電解質粉末[E]
0.6重量部を加え、乳鉢で均一に混合して脱酸素剤[
1]を製造した。(d) 100 parts by weight of the metal powder [F], the water = 12-31 parts by weight of the absorption-swelling polymer (+), and the electrolyte powder [E]
Add 0.6 parts by weight and mix uniformly in a mortar to prepare the oxygen absorber [
1] was manufactured.
(ホ)比較のために、前記金属粉末(F)1.00重量
部に対し、前記電解質粉末(IE〕0.6重量部のみを
加え、乳鉢で均一に混合し、脱酸素剤(n)を製造した
。(E) For comparison, only 0.6 parts by weight of the electrolyte powder (IE) was added to 1.00 parts by weight of the metal powder (F), mixed uniformly in a mortar, and oxygen scavenger (n) was manufactured.
(2)脱酸素剤の反応性テスト
前記そ得た各説aS剤(1)及び〔旧の2.7gを、小
袋〔通気性プラスチックフィルム(商品名:タイペック
)を重ねて3方をシールして形成した寸法5αX5an
の小袋〕にその開口部から充填し、開口部を封止した。(2) Reactivity test of oxygen scavenger 2.7 g of each of the above-obtained aS agents (1) and [old] were placed in a sachet [overlaid with breathable plastic film (product name: Typec) and sealed on three sides. Dimensions 5αX5an
sachet] was filled through its opening, and the opening was sealed.
この脱酸素剤充填袋を空間約500ccの容器に入れ、
さらに、水5ccを含ませた脱脂綿をその脱酸素剤充填
小袋の上に接触載置し、セロテープで固定し、全体を密
封し、所定時間間隔で密封空間の酸素濃度を測定し、そ
の酸素濃度の低下を測定した。Place this oxygen absorber filling bag in a container with a space of about 500cc,
Furthermore, absorbent cotton soaked with 5 cc of water was placed in contact with the oxygen absorber-filled sachet, fixed with cellophane tape, and sealed, and the oxygen concentration in the sealed space was measured at predetermined time intervals. We measured the decrease in
この結果を表−1に示す。また、この反応性テスト(第
1回反応性テスト)を15日間継続した後、容器から脱
酸素剤充填袋を取出し、その充填袋の−端を開口し、そ
の内部を観察したところ、比較品(脱酸素剤[rl)の
袋内部には水が溜り、全体がビショビショに濡れてもは
や脱酸素剤としての使用は不可能であった。これに対し
、本発明品(脱酸素剤〔I〕は、そのようなことはなく
、添加した高分子粒子〔P〕が水分を吸収し、膨潤して
いることが確認され、また良好な脱酸素反応を示すこと
が確認された。表−2にこの脱酸素剤(1)について、
これを2時間大気中に放置した後、再び前記と同様の反
応性テスト(第2回反応性テスト)を繰返した結果を示
す。The results are shown in Table-1. After continuing this reactivity test (first reactivity test) for 15 days, we removed the oxygen absorber filling bag from the container, opened the lower end of the filling bag, and observed the inside. (Water accumulated inside the oxygen absorber [rl] bag, and the entire bag became soaked and could no longer be used as an oxygen absorber. On the other hand, with the product of the present invention (oxygen scavenger [I], it was confirmed that the added polymer particles [P] absorbed moisture and swelled, and that the oxygen scavenger [I] had good deoxidation properties. It was confirmed that the oxygen absorber (1) exhibits an oxygen reaction.Table 2 shows the oxygen absorber (1).
After this was left in the air for 2 hours, the same reactivity test as above (second reactivity test) was repeated, and the results are shown below.
第一1 (第1回反応性テスト)
表−2(第2回反応性テスト)
以上のことから、本発明の脱酸素剤は、多水分中におい
ても長時間にわたって円滑な脱酸素反応を示すことがわ
かる。11 (First reactivity test) Table 2 (Second reactivity test) From the above, the oxygen absorber of the present invention exhibits a smooth deoxidation reaction over a long period of time even in high moisture environments. I understand that.
実施例2
金属粉末(F)100重量部に対し、電解質粉末〔E〕
0.6重量部と、水吸収膨潤性高分子(P)0.1〜1
0重量部と、活性炭微粉末0.5重量部とを加え、乳鉢
で均一に混合して脱M素剤を得た。Example 2 Electrolyte powder [E] to 100 parts by weight of metal powder (F)
0.6 parts by weight and water-absorbing swelling polymer (P) 0.1-1
0 parts by weight and 0.5 parts by weight of activated carbon fine powder were added and mixed uniformly in a mortar to obtain a de-Ming agent.
この脱酸素剤を、その金属粉末含量が2.5gとなるよ
うに実施例1で示した小袋に充填した。この脱酸素剤充
填小袋を空間約500ccの容器に入れさらに水5cc
を含ませた脱酸綿をその脱酸素剤充填袋とは接触しない
ように隔離して入れ、全体を密封し2所定時間間隔で密
封空間の酸素濃度を測定し、その酸素濃度の低下を測定
した。その結果を表−3に示す。表−3の結果から、水
吸収膨潤性粒子の添加量が多くなりすぎると脱酸素剤の
反応性が損われるようになることがわかる。This oxygen scavenger was filled into the sachet shown in Example 1 so that the metal powder content was 2.5 g. Place this oxygen absorber filled pouch in a container with a space of about 500cc and add 5cc of water.
Place the absorbent cotton soaked in the oxygen absorber in a separate manner so that it does not come into contact with the oxygen absorber-filled bag, seal the entire bag, and measure the oxygen concentration in the sealed space at two predetermined time intervals to measure the decrease in the oxygen concentration. did. The results are shown in Table-3. From the results in Table 3, it can be seen that when the amount of water-absorbing swelling particles added is too large, the reactivity of the oxygen scavenger is impaired.
表−3
実施例3
水100ccに対し、食塩12g、硫酸(濃度95%)
3ccを添加して水溶液を作り、この水溶液25ccを
粒径約0.7mmのゼオライト粉末100gと均一に混
合した後、得られた混合物を加熱乾燥して多孔性物質粗
粉末[T−]、]を作った。次に、この粗粉末[T−1
]を微粉砕し、粒度150メツシユ以下の微粉末〔T〜
2〕を得た。Table 3 Example 3 12g of common salt and sulfuric acid (concentration 95%) per 100cc of water
After adding 3 cc of this aqueous solution and uniformly mixing 25 cc of this aqueous solution with 100 g of zeolite powder having a particle size of about 0.7 mm, the resulting mixture was heated and dried to obtain a porous material coarse powder [T-]. made. Next, this coarse powder [T-1
] is finely pulverized to produce a fine powder with a particle size of 150 mesh or less [T~
2] was obtained.
次に、前記金属粉末(F) 100重量部に対し前記電
解質粉末(E)0.6重量部、亜塩素酸ナトリウム0.
2重量部、高分子粉末〔P〕1重量部及び前記多孔質物
質微粉末(T−2)0.5重量部を加え、乳鉢で均一に
混合して脱酸素剤を得た。この脱酸素剤3gを小袋に入
れ、この小袋に水Iceを加えたところ、高分子粉末〔
P〕の作用によりその水分は吸収され、小袋の底に遊離
水が溜ることはなかった。また、この水分の添加により
、亜塩素酸塩から遊離した二酸化塩素ガスの臭気が見ら
れ、二酸化塩素の発生が確認された。Next, 0.6 parts by weight of the electrolyte powder (E) and 0.6 parts by weight of sodium chlorite were added to 100 parts by weight of the metal powder (F).
2 parts by weight, 1 part by weight of polymer powder [P], and 0.5 parts by weight of the porous material fine powder (T-2) were added and mixed uniformly in a mortar to obtain an oxygen absorber. When I put 3g of this oxygen scavenger into a small bag and added ice water to this bag, the polymer powder [
The water was absorbed by the action of P], and free water did not accumulate at the bottom of the sachet. Furthermore, due to the addition of water, the odor of chlorine dioxide gas liberated from chlorite was observed, and the generation of chlorine dioxide was confirmed.
比較のために、高分子粉末CP)を添加しない以外は同
様にして得た脱酸素剤の場合には、前記と同様のテスト
を行ったところ、小袋の底に遊離水が溜ることが確認さ
れた。For comparison, in the case of an oxygen absorber obtained in the same manner except that polymer powder CP) was not added, the same test as above was conducted, and it was confirmed that free water accumulated at the bottom of the sachet. Ta.
実施例4
実施例3において、亜塩素酸塩の代りに、亜硫酸水素ナ
トリウム(NalISO3)を用いた以外は同様にして
脱酸素剤を作り、これに水を同様にして添加したところ
、小袋の開口部に保持した水を含ませたp)l試験紙の
色が酸性域の色に変色し、亜硫酸ガスの発生が確認され
た。また、小袋の底には遊離水の溜りは見られなかった
。Example 4 An oxygen absorber was prepared in the same manner as in Example 3 except that sodium hydrogen sulfite (NalISO3) was used instead of chlorite, and water was added to it in the same manner. The color of the p)l test paper impregnated with the water retained in the sample changed to a color in the acidic range, and the generation of sulfur dioxide gas was confirmed. Furthermore, no free water accumulation was observed at the bottom of the sachet.
実施例5
前記金属粉末[F] 100重量部に対し、前記電解質
粉末[E]0.6重量部、高分子粉末〔P〕1重量部及
び亜塩素酸ナトリウム0.2重量部を加えて、乳鉢で均
一に混合した。この混合物の場合にも、同様の水の添加
により二酸化塩素の発生が確認された。また、この実験
において、亜塩素酸ナトリウムの代りに、亜硫酸水素ナ
トリウムを用いたところ、亜硫酸ガスの発生が確認され
た。なお、これらの実験においても、同様に、小袋の底
には遊離水の溜りは見られなかった。Example 5 To 100 parts by weight of the metal powder [F], 0.6 parts by weight of the electrolyte powder [E], 1 part by weight of polymer powder [P], and 0.2 parts by weight of sodium chlorite were added, Mixed evenly in a mortar. In the case of this mixture as well, generation of chlorine dioxide was confirmed by the addition of water in a similar manner. Furthermore, in this experiment, when sodium hydrogen sulfite was used instead of sodium chlorite, generation of sulfur dioxide gas was confirmed. In addition, in these experiments as well, no accumulation of free water was observed at the bottom of the sachet.
実施例6
実施例3において、硫酸3ccの代りに、硫酸第1鉄・
71(2015gとクエン酸5gを用いた以外は同様に
して脱酸素剤を得た。この脱酸素剤3gを小袋に入れ、
この袋にアンモニア水1滴を加え、その小袋内の臭気を
調べたところ、硫酸第1鉄がアンモニアと反応し、アン
モニア臭は感じられなかった。Example 6 In Example 3, ferrous sulfate/ferrous sulfate was used instead of 3 cc of sulfuric acid.
An oxygen absorber was obtained in the same manner except that 71 (2015 g) and 5 g of citric acid were used. 3 g of this oxygen absorber was placed in a sachet,
When one drop of ammonia water was added to this bag and the odor inside the bag was examined, ferrous sulfate reacted with ammonia and no ammonia odor was detected.
Claims (1)
らなる高湿度下で脱酸素反応を示す脱酸素剤において、
該脱酸素剤中に水吸収膨潤性高分子粉末を含有させたこ
とを特徴とする脱酸素剤。(1) In an oxygen scavenger that exhibits an oxygen scavenging reaction under high humidity and is made of a combination of an oxidizable metal powder component and an electrolyte component,
An oxygen absorber characterized in that the oxygen absorber contains a water-absorbing swelling polymer powder.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61088894A JPH0716600B2 (en) | 1986-04-16 | 1986-04-16 | Oxygen absorber |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61088894A JPH0716600B2 (en) | 1986-04-16 | 1986-04-16 | Oxygen absorber |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS62244444A true JPS62244444A (en) | 1987-10-24 |
JPH0716600B2 JPH0716600B2 (en) | 1995-03-01 |
Family
ID=13955675
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP61088894A Expired - Fee Related JPH0716600B2 (en) | 1986-04-16 | 1986-04-16 | Oxygen absorber |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0716600B2 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH05115776A (en) * | 1991-04-02 | 1993-05-14 | W R Grace & Co | Mixture, product and method for scavenging oxygen |
US8017033B2 (en) | 2005-10-21 | 2011-09-13 | Mitsubishi Gas Chemical Company, Inc. | Solid oxygen scavenger composition and process for producing the same |
CN113508836A (en) * | 2021-07-01 | 2021-10-19 | 大连果真鲜供应链管理有限公司 | Composite deoxidizing fresh-keeping powder for figs and fresh-keeping powder bag |
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JPS5588844A (en) * | 1978-12-28 | 1980-07-04 | Toyo Ink Mfg Co Ltd | Oxygen absorbing structure |
JPS565132A (en) * | 1979-06-28 | 1981-01-20 | Daishiro Fujishima | Deoxidizing agent and preparation thereof |
JPS5620450A (en) * | 1979-07-30 | 1981-02-26 | Mitsubishi Rayon Co | Exothermic composition |
JPS5624473U (en) * | 1979-07-31 | 1981-03-05 | ||
JPS5660642A (en) * | 1979-10-25 | 1981-05-25 | Teijin Ltd | Oxygen absorptive sheet structure |
JPS5678630A (en) * | 1980-11-17 | 1981-06-27 | Mitsubishi Gas Chem Co Inc | Oxygen absorbent |
JPS58193678A (en) * | 1982-05-04 | 1983-11-11 | Kao Corp | Method of keeping vegetable and food fresh |
JPS61200835A (en) * | 1985-03-04 | 1986-09-05 | Sumitomo Chem Co Ltd | Desiccant |
-
1986
- 1986-04-16 JP JP61088894A patent/JPH0716600B2/en not_active Expired - Fee Related
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5588844A (en) * | 1978-12-28 | 1980-07-04 | Toyo Ink Mfg Co Ltd | Oxygen absorbing structure |
JPS565132A (en) * | 1979-06-28 | 1981-01-20 | Daishiro Fujishima | Deoxidizing agent and preparation thereof |
JPS5620450A (en) * | 1979-07-30 | 1981-02-26 | Mitsubishi Rayon Co | Exothermic composition |
JPS5624473U (en) * | 1979-07-31 | 1981-03-05 | ||
JPS5660642A (en) * | 1979-10-25 | 1981-05-25 | Teijin Ltd | Oxygen absorptive sheet structure |
JPS5678630A (en) * | 1980-11-17 | 1981-06-27 | Mitsubishi Gas Chem Co Inc | Oxygen absorbent |
JPS58193678A (en) * | 1982-05-04 | 1983-11-11 | Kao Corp | Method of keeping vegetable and food fresh |
JPS61200835A (en) * | 1985-03-04 | 1986-09-05 | Sumitomo Chem Co Ltd | Desiccant |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH05115776A (en) * | 1991-04-02 | 1993-05-14 | W R Grace & Co | Mixture, product and method for scavenging oxygen |
US8017033B2 (en) | 2005-10-21 | 2011-09-13 | Mitsubishi Gas Chemical Company, Inc. | Solid oxygen scavenger composition and process for producing the same |
US8168079B2 (en) | 2005-10-21 | 2012-05-01 | Mitsubishi Gas Chemical Company, Inc. | Solid oxygen scavenger composition and process for producing the same |
CN113508836A (en) * | 2021-07-01 | 2021-10-19 | 大连果真鲜供应链管理有限公司 | Composite deoxidizing fresh-keeping powder for figs and fresh-keeping powder bag |
Also Published As
Publication number | Publication date |
---|---|
JPH0716600B2 (en) | 1995-03-01 |
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