JPS58128145A - oxygen absorber - Google Patents
oxygen absorberInfo
- Publication number
- JPS58128145A JPS58128145A JP1130582A JP1130582A JPS58128145A JP S58128145 A JPS58128145 A JP S58128145A JP 1130582 A JP1130582 A JP 1130582A JP 1130582 A JP1130582 A JP 1130582A JP S58128145 A JPS58128145 A JP S58128145A
- Authority
- JP
- Japan
- Prior art keywords
- iron powder
- powder
- packaging
- parts
- oxygen
- 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
Landscapes
- Food Preservation Except Freezing, Refrigeration, And Drying (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は酸素吸収剤に関する。更に詳しくは鉄粉と電解
質を含有する組成物(2)と活性炭(至)とをあらかじ
め混合することなく、包装時K(A)と−とを一緒に包
装してなることを特徴とする酸素徴収剤Kr1jする発
明である。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an oxygen absorbent. More specifically, the oxygen is characterized in that the composition (2) containing iron powder and an electrolyte and activated carbon (1) are not mixed in advance, but K (A) and - are packaged together at the time of packaging. This is an invention that uses a collection agent Kr1j.
近年、脱酸素剤を応用した食品の鮮度保持方法が急速に
広まりつへある。In recent years, methods of keeping food fresh using oxygen absorbers have been rapidly gaining popularity.
脱酸素剤としては種々のものが知られているが。Various oxygen scavengers are known.
これらの中で鉄粉を主剤とした脱酸素剤は酸素吸収能力
および酸素吸収速度が共に大き(、安全性も優れている
ので、最も実用性が高く、多量に使用されている。Among these, oxygen scavengers based on iron powder have a high oxygen absorption capacity and oxygen absorption rate (and are also excellent in safety), so they are the most practical and are used in large quantities.
鉄粉を主剤とした脱酸素剤は通常は鉄粉の他K。Oxygen absorbers based on iron powder usually contain K in addition to iron powder.
ハロゲン化物をはじめとする電解質、フィラー。Electrolytes and fillers including halides.
場合にようては水等を温合してなるものであるが。In some cases, it is made by heating water, etc.
この鳩舎、鉄が特有の臭気を発するので1通常はこれに
活性炭等の脱臭性吸収剤を温合して用いている。しかし
鉄系脱噴素剤虻活性炭を含有させるために混合する場合
、微粉末の活性炭を用いると混合時およびこれらの混合
物を紙袋ドパツクする際に、黒い粉塵が着しく尭生ずる
ため1作業環境が悪化すると共に、バッタした紙袋にも
付着する等の好ましくない影響があられれる。この様な
影響を防ぐために、粗粒状または顆粒状の活性炭を用い
ることが行なわれるが、この場合は他の組成物との均一
混合が難しく、活性炭と他の組成物とが分級するために
混合に続く、紙袋へのバッキングにおいて活性炭が脱酸
素剤中に均一に分布することが必ずしもうまく行なわれ
ないので、鉄虻よる異臭を完全に除去することが出来な
い製品が得られる場合があった。Since the iron in this pigeon house emits a peculiar odor, it is usually mixed with a deodorizing absorbent such as activated carbon. However, when mixing to contain activated carbon, which is an iron-based deoxidizing agent, if fine powder activated carbon is used, a lot of black dust will be generated during mixing and when the mixture is packed in a paper bag, making the work environment difficult. Not only does it get worse, but it also causes undesirable effects such as adhesion to paper bags that have fallen apart. In order to prevent such effects, activated carbon in the form of coarse particles or granules is used, but in this case it is difficult to mix it uniformly with other compositions, and the activated carbon and other compositions are classified, so it is difficult to mix them. Subsequently, in the backing of the paper bag, it is not always possible to ensure that the activated carbon is evenly distributed in the oxygen scavenger, resulting in a product that cannot completely remove the odor caused by iron flies.
本発明者等は以上の様な欠点を有しない脱酸素剤につい
て鋭意研究を行なりた結果、脱酸素剤に含まれる各成分
のうち、活性炭■を除く他の成分(2)と活性炭(至)
とを包装前にあらかじめ拠金することなく、包装時にお
いて、■または■のいずれかを先に充填すれば活性炭に
よる粉塵の発生もなく。As a result of intensive research into oxygen scavengers that do not have the above-mentioned drawbacks, the present inventors found that among the components contained in oxygen scavengers, other components (2) except activated carbon )
If you fill either (■) or (■) first at the time of packaging without having to pre-deposit (1) and (2) before packaging, there will be no dust generation due to activated carbon.
また分級もおこらないので、好適な脱酸素剤を得ること
が出来ることを見出して本発明を完成するに至った。Furthermore, since classification does not occur, the present invention was completed based on the discovery that a suitable oxygen scavenger can be obtained.
本発114において、鉄粉としては還元鉄11、電湊鉄
粉、噴磐鉄粉、切削くずなどの種々のものが使用できる
が、酸素との接触を良好とするために表面積比をできる
だけ大赦くすることが好ましい。In this invention 114, various types of iron powder can be used, such as reduced iron 11, Denminato iron powder, Fukiwa iron powder, cutting waste, etc., but the surface area ratio should be as large as possible in order to improve contact with oxygen. It is preferable to
たとえば、s末では10メッシ為以下、とくに50メツ
シエ以下の粒子として用いるのが適廟である。For example, it is appropriate to use S powder as particles of 10 mesh or less, particularly 50 mesh or less.
本発明において、電解質としては例えばハロゲン化金属
が使用されるが、ハロゲン化金属における金属成分とし
てはアルカリ金属、アルカリ土類金属、鋼、亜鉛、アル
ξニク^、スズ、マンガン。In the present invention, for example, a metal halide is used as the electrolyte, and the metal components in the metal halide include alkali metals, alkaline earth metals, steel, zinc, aluminum, tin, and manganese.
鉄、コバルトおよびニッケルからなる群から選ばれる少
なくとも一種の金属があげられるが、水素の発生を考慮
すればアルカリ金属、アルカリ土類金属が好ましく、リ
チウム、ナトリウム、カリウム、マダネシウム、カルシ
ウム、バリウムが好ましい、また、ハロゲン化金属にお
けるハロゲン成分としては塩素、臭素、llつ素があげ
られる。これらは単独または二種以上の混合で用いる。At least one metal selected from the group consisting of iron, cobalt, and nickel is mentioned, but in consideration of hydrogen generation, alkali metals and alkaline earth metals are preferable, and lithium, sodium, potassium, madanesium, calcium, and barium are preferable. Further, examples of the halogen component in the metal halide include chlorine, bromine, and chlorine. These may be used alone or in combination of two or more.
ハロゲン化金属の鉄との混合方法には、単なる添加混合
や、ハロゲン化金属水**と鉄を謳合し、次いで乾燥す
ることKよりハロゲン化金属を鉄褒爾を被覆する方法な
どがある。ハロゲン化金属の単なる混合では鉄100部
あたりハーグン化金属α1部以上、好ましくは10g以
上が適当である。ハロゲン化金属を多量に用いすぎるこ
とは単位重量あたりの酸素吸収量を減少させるので好ま
しくない、ハロゲン化金属水溶筐と鉄を混合し1次いで
空気中などで乾燥し、バーダン化金属で鉄を被覆する場
合の使用量は鉄lOe部あたり、ハロゲン化金属α00
1〜10 @、好ましく、はQ、01〜3部である。い
ずれの添加方法の場合も、下限未満では酸素吸収能力が
低下する。Methods for mixing metal halides with iron include simple addition and mixing, and methods such as mixing metal halide water** and iron, then drying, and coating metal halides on iron. . If the metal halide is simply mixed, it is appropriate that the amount of metal hagnide α is 1 part or more, preferably 10 g or more, per 100 parts of iron. It is undesirable to use too much metal halide because it reduces the amount of oxygen absorbed per unit weight. Mix the aqueous metal halide casing with iron, then dry in air, etc., and coat the iron with bardanized metal. In this case, the amount used is per 1Oe part of iron, metal halide α00
1 to 10 @, preferably Q, 01 to 3 parts. In either addition method, below the lower limit, the oxygen absorption capacity decreases.
本発明の酸素吸収剤による酸素吸収は鉄の水醗化物生成
反応を利用したものであり、したがりて酸素吸収剤が水
を含有するか、または酸素徴収剤が使用される系内に水
蒸気が存在することが必須である。酸素吸収剤が水を含
有する場合はこの水は自由水、結晶水などのいかなる形
であってもよい。水を自由水として用いる場合は、鉄1
00部あたり111以上、好ましくは5部以上を用いる
。Oxygen absorption by the oxygen absorbent of the present invention utilizes the water fluoride formation reaction of iron. Therefore, the oxygen absorbent contains water or water vapor is present in the system in which the oxygen scavenger is used. It is essential to exist. When the oxygen absorbent contains water, this water may be in any form such as free water or crystal water. When water is used as free water, iron 1
111 parts or more, preferably 5 parts or more per 00 parts.
また自由水KかえてNa180. ・IOH,O,Na
、80.・7H,0゜Na、CO,・)OH,0なとの
結晶水をもった化合物を用いる場合は、鉄100mあた
り2部以上、好ましくは10i1以上用いるのが適当で
ある。自由水または結晶水をもった化合物の使用量は、
酸素1lIIL剤の単位重量当りの酸素徴収量などを考
慮して適宜決定する。ここで1食品が水分を含んでおり
密閉系内に水蒸気を発生するものであれば、鉄粉とハロ
ゲン化金属塩の二成分を適用する事によって、十分酸素
吸収剤として役割をはたす。Also, instead of free water K, Na180.・IOH, O, Na
, 80. When using a compound having water of crystallization such as 7H, 0° Na, CO, .)OH, 0, it is appropriate to use 2 parts or more per 100 m of iron, preferably 10i1 or more. The amount of compounds with free water or water of crystallization is
It is determined as appropriate by taking into account the amount of oxygen collected per unit weight of the oxygen 1lIIL agent. Here, if a food contains water and generates water vapor in a closed system, the application of two components, iron powder and metal halide salt, will sufficiently serve as an oxygen absorber.
また1本発明においては組成物(AKは通常フィラーを
含有させるが、この場合のフィラートシては、活性アル
ミナ、活性白土、ケイソウ土、パーライト、セルロース
、ゼオライト、微粉シリカゲル、アルカリ土類金属の硫
酸塩、カオリン、窒化ケイ素、ブロイダルシリカ、タル
ク、ベントナイト、シリカアルミナゲル、無水シリカ、
ケイ酸カルシウム、水酸化マグネシウム、酸化マグネシ
ウム、水酸化アルにラム、酸化鉄などの有機もしくは無
機の水難溶性フィラーがあげられるつこれらのフィラー
の粒度は混合物を均一化する為通常200メツシ為以下
のものが用いられる。In addition, in the present invention, the composition (AK usually contains a filler, but the filler material in this case includes activated alumina, activated clay, diatomaceous earth, perlite, cellulose, zeolite, fine powder silica gel, alkaline earth metal sulfate). , kaolin, silicon nitride, broidal silica, talc, bentonite, silica alumina gel, anhydrous silica,
Examples include organic or inorganic water-insoluble fillers such as calcium silicate, magnesium hydroxide, magnesium oxide, aluminum hydroxide, rum, and iron oxide.The particle size of these fillers is usually 200 mesh or less in order to homogenize the mixture. things are used.
また、フィラーの添加量は、a合物に水を用いた場合に
は水1部に対して好ましくは0.2部以上。Further, when water is used in compound a, the amount of filler added is preferably 0.2 parts or more per 1 part of water.
更に好ましくはα5部以上であり、結晶水含有化合物を
用いた場合には、曽晶水會化合物1001IK対して、
好ましくは1部以上、更に好ましくは3部以上であり、
酸素吸収剤の単位重量当りの酸素吸収量等を勘案して適
宜決定される。More preferably, it is α5 parts or more, and when a crystal water-containing compound is used, it is
Preferably 1 part or more, more preferably 3 parts or more,
It is appropriately determined by taking into consideration the amount of oxygen absorbed per unit weight of the oxygen absorbent.
m*炭としては粒状のものを用いるが、破砕炭造粒縦い
ずれでもよ(,150メッシェ以上、好まL〈はlOO
メッシ纂以上の粒度のものが好適に用いられる。Granular charcoal is used as m*charcoal, but crushed charcoal granulated vertically may be used (150 mesh or more, preferably L< is lOO
Particles with a particle size of mesh or larger are preferably used.
活性炭の使用量は鉄粉100部に対して0.1部〜lO
部が好ましく、更に好ましくは0.3部〜5部である。The amount of activated carbon used is 0.1 part to lO per 100 parts of iron powder.
1 part, more preferably 0.3 parts to 5 parts.
鉄粉100時に20−食塩水5−と200メツシユ以下
のタルク5−を大気下”tlL合し、乾燥して、I!質
的に水分のない粉体(2)を得た。At 100 hrs of iron powder, 20-saline solution 5- and 200 mesh or less of talc 5- were combined in the atmosphere and dried to obtain a powder (2) that was qualitatively free of water.
■4fと50メツシエの粒状活性炭30.02 Fを各
々計量し、2種温合自動充填機にて5儂×5cmの有孔
ポリエチレンフィルムをラミ半−Fした紙袋に二段に充
填り、(こ〜でいう二段充填とは釦と−とを色装前にあ
らかじめ接触させることなく、一つの通気性包材K(2
)または0を入れ1次ka1または^を入れて一緒に包
装することをいう)脱酸素剤を得た。充填中の験膓は認
められず、好適に包装する事が出来た。■ Weighed 30.02F of 4F and 50Metsushie granular activated carbon, and filled them in two layers into a paper bag laminated with a 5F x 5cm perforated polyethylene film using a two-type heating automatic filling machine. The two-stage filling referred to here means that one breathable packaging material K (2
) or 0 and primary ka1 or ^ and packaged together) to obtain an oxygen absorber. No condensation was observed during filling, and packaging was possible.
得られた脱Il素剤を空気50G嵯の密閉系内で。The obtained de-Il agent was placed in a closed system with 50 G of air.
RH10691!5℃下で放置したところ、2日後には
系内酸素鏝度はαO憾となり、系内の臭気も認められな
かった。RH10691! When left at 5°C, the oxygen concentration in the system became αO after 2 days, and no odor was observed in the system.
又、上記充填包装して得られた脱酸素剤10個中の活性
炭含有量を分析したところ、0.018f〜0.023
tの範囲内であった。In addition, when the activated carbon content in the 10 oxygen absorbers obtained by filling and packaging the above was analyzed, it was found to be 0.018f to 0.023
It was within the range of t.
特許出願人 三菱瓦斯化学株式金社 代表者長野和吉patent applicant Mitsubishi Gas Chemical Co., Ltd. Representative Kazuyoshi Nagano
Claims (1)
らかじめ混合することなく、包装時K(A)と・とを−
緒虻包装してなることを特徴とする酸素吸収剤。Without pre-mixing the composition (2) containing iron powder and electrolyte with the activated carbon ■, K(A) and - are mixed at the time of packaging.
An oxygen absorber characterized by being packaged in Oogi packaging.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1130582A JPS58128145A (en) | 1982-01-27 | 1982-01-27 | oxygen absorber |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1130582A JPS58128145A (en) | 1982-01-27 | 1982-01-27 | oxygen absorber |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS58128145A true JPS58128145A (en) | 1983-07-30 |
| JPH0351392B2 JPH0351392B2 (en) | 1991-08-06 |
Family
ID=11774288
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1130582A Granted JPS58128145A (en) | 1982-01-27 | 1982-01-27 | oxygen absorber |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS58128145A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0768165A (en) * | 1993-09-01 | 1995-03-14 | Toagosei Co Ltd | Oxygen absorber |
| US5725795A (en) * | 1991-11-13 | 1998-03-10 | Mitsubishi Gas Chemical Company, Inc. | Oxygen absorber and method for producing same |
| JP2008221983A (en) * | 2007-03-12 | 2008-09-25 | Lecip Corp | Luminaire for vehicle |
| WO2023022220A1 (en) * | 2021-08-20 | 2023-02-23 | 三菱瓦斯化学株式会社 | Package for fruits and vegetables, and method for maintaining freshness of fruits and vegetables |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5522318A (en) * | 1978-08-04 | 1980-02-18 | Mitsubishi Gas Chem Co Inc | Oxygen absorber |
| JPS5581742A (en) * | 1978-12-15 | 1980-06-20 | Teijin Ltd | Preserving method of oxygen trapping composition |
-
1982
- 1982-01-27 JP JP1130582A patent/JPS58128145A/en active Granted
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5522318A (en) * | 1978-08-04 | 1980-02-18 | Mitsubishi Gas Chem Co Inc | Oxygen absorber |
| JPS5581742A (en) * | 1978-12-15 | 1980-06-20 | Teijin Ltd | Preserving method of oxygen trapping composition |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5725795A (en) * | 1991-11-13 | 1998-03-10 | Mitsubishi Gas Chemical Company, Inc. | Oxygen absorber and method for producing same |
| JPH0768165A (en) * | 1993-09-01 | 1995-03-14 | Toagosei Co Ltd | Oxygen absorber |
| JP2008221983A (en) * | 2007-03-12 | 2008-09-25 | Lecip Corp | Luminaire for vehicle |
| WO2023022220A1 (en) * | 2021-08-20 | 2023-02-23 | 三菱瓦斯化学株式会社 | Package for fruits and vegetables, and method for maintaining freshness of fruits and vegetables |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0351392B2 (en) | 1991-08-06 |
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