JP6690201B2 - Oxygen absorber composition and oxygen absorber - Google Patents
Oxygen absorber composition and oxygen absorber Download PDFInfo
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Description
本発明は、脱酸素剤組成物及び脱酸素剤に関する。詳しくは0.5以下の水分活性を示す脱酸素剤組成物及びこれを包装してなる脱酸素剤に関する。 The present invention relates to an oxygen absorber composition and an oxygen absorber. Specifically, it relates to an oxygen absorber composition having a water activity of 0.5 or less and an oxygen absorber prepared by packaging the oxygen absorber composition.
従来より、鉄粉の酸化反応を利用した脱酸素剤(以下、鉄系脱酸素剤)が提案されている。市販の脱酸素剤(例えば、商品名「エージレス」、三菱瓦斯化学株式会社製)は、食品や医薬品などの物品と共にガスバリア性容器に密封収納し容器内の酸素を除去することで、上記物品の品質や鮮度を保持するために既に広く利用されている。 Conventionally, a deoxidizer utilizing the oxidation reaction of iron powder (hereinafter referred to as an iron-based deoxidizer) has been proposed. Commercially available oxygen scavengers (for example, trade name "Ageless", manufactured by Mitsubishi Gas Chemical Co., Inc.) are used to remove the oxygen in the container by hermetically storing it in a gas barrier container together with products such as foods and pharmaceuticals. It is already widely used to maintain quality and freshness.
鉄系脱酸素剤には、被保存物等から蒸散した水分を利用して酸素吸収を開始する「水分依存型」脱酸素剤と、鉄粉の酸素吸収反応に必要な水分を予め脱酸素剤組成物に有する「自力反応型」脱酸素剤とがある。「自力反応型」脱酸素剤を含有水分量の低い食品や医薬品等に用いると、脱酸素剤組成物が予め有する水分が食品や医薬品等へ移行し被保存物の含有水分量が変化してしまう場合があった。この水分移行の課題を解決する方法として、特許文献1には水分含有量を1重量%以下とした低湿度雰囲気用脱酸素剤組成物が開示されている。 The iron-based oxygen scavengers include a "moisture-dependent" oxygen scavenger that starts absorbing oxygen by utilizing the water that has evaporated from the preserved material, and the oxygen necessary for the oxygen absorption reaction of the iron powder. There are "self-reactive" oxygen scavengers in the composition. When "self-reactive type" oxygen scavengers are used for foods and pharmaceuticals with low water content, the oxygen content of the oxygen scavenger composition is transferred to foods and pharmaceuticals, etc. There were times when it ended up. As a method for solving the problem of water migration, Patent Document 1 discloses an oxygen scavenger composition for low humidity atmosphere having a water content of 1% by weight or less.
しかしながら、特許文献1の組成物では特に50%RH以下の低湿度雰囲気においては酸素吸収性能が著しく低下するという課題があった。本発明は上記事情に鑑みなされたものであり、50%RH以下の低湿度雰囲気においても高い酸素吸収速度を有し、かつ、被保存物への水分移行が抑制された脱酸素剤組成物を提供することを目的とする。 However, the composition of Patent Document 1 has a problem that the oxygen absorption performance is remarkably reduced particularly in a low humidity atmosphere of 50% RH or less. The present invention has been made in view of the above circumstances, and provides an oxygen absorber composition having a high oxygen absorption rate even in a low humidity atmosphere of 50% RH or less, and having suppressed water transfer to a substance to be stored. The purpose is to provide.
本発明者らは、上記の課題を解決する方法を検討した結果、鉄粉、塩化カルシウム、水及び保水担体を含む脱酸素剤組成物において、水の含有量を鉄粉100質量部に対し20〜40質量部とし、塩化カルシウムの含有量を水100質量部に対し52〜61質量部とすることで、50%RH以下の低湿度雰囲気においても優れた酸素吸収性能を有し、かつ、被保存物への水分移行が抑制された脱酸素剤組成物を得られることを見出し、本発明に至った。 As a result of studying a method for solving the above problems, the present inventors have found that in a deoxidizer composition containing iron powder, calcium chloride, water and a water-retaining carrier, the content of water is 20 per 100 parts by mass of iron powder. To 40 parts by mass, and the content of calcium chloride is 52 to 61 parts by mass with respect to 100 parts by mass of water, thereby having excellent oxygen absorption performance even in a low humidity atmosphere of 50% RH or less, and The inventors have found that an oxygen scavenger composition in which water transfer to a preserved product is suppressed can be obtained, and have completed the present invention.
すなわち、本発明は、以下のとおりである。 That is, the present invention is as follows.
[1] 鉄粉、塩化カルシウム、水及び保水担体を含む脱酸素剤組成物において、前記水の含有量が前記鉄粉100質量部に対し20〜40質量部であり、前記塩化カルシウムの含有量が前記水100質量部に対し52〜61質量部である脱酸素剤組成物。 [1] In an oxygen scavenger composition containing iron powder, calcium chloride, water and a water-retaining carrier, the water content is 20 to 40 parts by mass with respect to 100 parts by mass of the iron powder, and the calcium chloride content. Is 52 to 61 parts by mass with respect to 100 parts by mass of the water.
[2] さらに活性炭を含む、[1]に記載の脱酸素剤組成物。 [2] The oxygen absorber composition according to [1], which further contains activated carbon.
[3] [1]または[2]に記載の脱酸素剤組成物を熱接着可能な樹脂層を含む複合フィルムで包装してなる、小袋状脱酸素剤の製造方法。 [3] A method for producing a pouch-shaped oxygen scavenger, which is obtained by packaging the oxygen scavenger composition according to [1] or [2] in a composite film containing a resin layer capable of heat bonding.
[4] [1]または[2]に記載の脱酸素剤組成物を、熱可塑性樹脂を含む容器に充填包装してなる、キャニスター状脱酸素剤の製造方法。 [4] A method for producing a canister-shaped oxygen absorber, which is obtained by filling and packaging the oxygen absorber composition according to [1] or [2] in a container containing a thermoplastic resin.
本発明によれば、50%RH以下の低湿度雰囲気においても優れた酸素吸収性能を有し、かつ、被保存物への水分移行が抑制された脱酸素剤組成物を提供可能となる。 ADVANTAGE OF THE INVENTION According to this invention, it becomes possible to provide the oxygen scavenger composition which has the outstanding oxygen absorption performance also in the low humidity atmosphere of 50% RH or less, and which suppressed the water transfer to the preservation object.
以下、本発明を実施するための形態(以下、単に「本実施形態」という。)について詳細に説明する。なお、以下の本実施形態は、本発明を説明するための例示であり、本発明を以下の内容に限定する趣旨ではない。本発明は、その要旨の範囲内で適宜に変形して実施できる。 Hereinafter, modes for carrying out the present invention (hereinafter, simply referred to as “the present embodiment”) will be described in detail. The following embodiments are examples for explaining the present invention, and are not intended to limit the present invention to the following contents. The present invention can be appropriately modified and implemented within the scope of the gist.
本実施形態の脱酸素剤組成物は、鉄粉、塩化カルシウム、水及び保水担体を含む脱酸素剤組成物において、前記水の含有量が前記鉄粉100質量部に対し20〜40質量部であり、前記塩化カルシウムの含有量が前記水100質量部に対し52〜61質量部である脱酸素剤組成物である。鉄粉、水及び塩化カルシウムを上記質量比とすることで、50%RH以下の低湿度雰囲気下においても優れた酸素吸収性能を示す脱酸素剤組成物を得ることができる。 The oxygen scavenger composition of the present embodiment is an oxygen scavenger composition containing iron powder, calcium chloride, water and a water-retaining carrier, and the content of water is 20 to 40 parts by mass relative to 100 parts by mass of the iron powder. And the content of the calcium chloride is 52 to 61 parts by mass with respect to 100 parts by mass of the water. By using iron powder, water and calcium chloride in the above mass ratio, it is possible to obtain an oxygen scavenger composition exhibiting excellent oxygen absorption performance even in a low humidity atmosphere of 50% RH or less.
<鉄粉>
脱酸素剤の主剤となる鉄粉は、鉄の表面が露出したものであれば特に限定されるものではなく、還元鉄粉、電解鉄粉、噴霧鉄粉などが好適に用いられる。その他、鋳鉄などの粉砕物、切削品などを用いることができる。鉄粉は、酸素との接触を良好にするために通常平均粒径1mm以下、好ましくは500μm以下、より好ましくは100μm以下の鉄粉が用いられる。ここで言う粒径とはJIS Z 8801の標準篩を用いて、5分間振動させた後の篩目のサイズによる重量分率から測定される粒径を示す。
<Iron powder>
The iron powder that is the main agent of the oxygen scavenger is not particularly limited as long as the surface of iron is exposed, and reduced iron powder, electrolytic iron powder, atomized iron powder and the like are preferably used. In addition, crushed products such as cast iron and cut products can be used. As the iron powder, iron powder having an average particle size of 1 mm or less, preferably 500 μm or less, more preferably 100 μm or less is used in order to improve the contact with oxygen. The particle size as used herein means a particle size measured from the weight fraction according to the size of the sieve mesh after being vibrated for 5 minutes using a JIS Z 8801 standard sieve.
<水及び塩化カルシウム>
鉄系脱酸素剤は酸素吸収性能を発揮するために水分が必須であるため本実施形態の脱酸素剤組成物は水を含有する。他方、脱酸素剤とした際に被保存物への水分移行抑制の観点から、本実施形態の脱酸素剤組成物は塩化カルシウムを更に含有する。塩化カルシウムは水に溶解した水溶液として含有されることが好ましい。水の含有量は液体の状態で組成物中に含有されているものの他、保水担体等の粒子表面に吸着されている水の重量及び水和物の水和水として含まれている水の重量も全て含んだ値として計算する。また、塩化カルシウムは無水塩化カルシウムの他、塩化カルシウム二水和物等市販のものを無水物、水和物の別なく用いることができる。塩化カルシウムの含有量は無水物換算として計算する。
<Water and calcium chloride>
Since the iron-based oxygen scavenger requires water in order to exert the oxygen absorption performance, the oxygen scavenger composition of the present embodiment contains water. On the other hand, the oxygen scavenger composition of the present embodiment further contains calcium chloride from the viewpoint of suppressing the migration of water to the preserved substance when it is used as the oxygen scavenger. Calcium chloride is preferably contained as an aqueous solution dissolved in water. The content of water is not only that contained in the composition in a liquid state, but also the weight of water adsorbed on the surface of particles such as water retention carrier and the weight of water contained as hydrated water of hydrate. Calculated as a value that includes all. In addition to anhydrous calcium chloride, commercially available calcium chloride such as calcium chloride dihydrate can be used regardless of whether it is anhydrous or hydrated. The content of calcium chloride is calculated as an anhydride.
脱酸素剤組成物中の水の含有量は鉄粉100質量部に対し20〜40質量部であり、25〜35質量部であることが好ましく、28〜32質量部であることが更に好ましい。水の含有量が20質量部よりも少ないと鉄粉の酸化反応が正常に進行せず酸素吸収速度低下につながり、逆に40質量部よりも多いと相対的に鉄粉の含有量が少なくなるため好ましくない。脱酸素剤組成物中の鉄粉と水の含有量比を上記好ましい範囲とすることでより優れた酸素吸収性能を有する脱酸素剤を得ることができる。 The content of water in the oxygen scavenger composition is 20 to 40 parts by mass, preferably 25 to 35 parts by mass, and more preferably 28 to 32 parts by mass with respect to 100 parts by mass of iron powder. If the content of water is less than 20 parts by mass, the oxidation reaction of the iron powder does not proceed normally, leading to a decrease in the oxygen absorption rate, and if it is more than 40 parts by mass, the content of the iron powder becomes relatively small. Therefore, it is not preferable. By setting the content ratio of iron powder and water in the oxygen scavenger composition within the above preferable range, it is possible to obtain a oxygen scavenger having more excellent oxygen absorption performance.
脱酸素剤組成物中の塩化カルシウムの含有量は前記水100質量部に対し52〜61質量部である。塩化カルシウムが52質量部よりも少ないと脱酸素剤組成物の水分活性が高くなり過ぎるため好ましくない。逆に塩化カルシウムが61質量部よりも多いと塩化カルシウムの溶解性が下がり、水溶液として添加することが困難となるため、均一な組成物を作製する観点から好ましくない。 The content of calcium chloride in the oxygen scavenger composition is 52 to 61 parts by mass with respect to 100 parts by mass of the water. If the amount of calcium chloride is less than 52 parts by mass, the water activity of the oxygen scavenger composition becomes too high, which is not preferable. On the other hand, if the amount of calcium chloride is more than 61 parts by mass, the solubility of calcium chloride decreases and it becomes difficult to add it as an aqueous solution, which is not preferable from the viewpoint of producing a uniform composition.
<保水担体>
脱酸素剤組成物としての取り扱い性を向上させる観点より、本実施形態の脱酸素剤組成物は保水担体を更に含有する。保水担体は水を担持できるものであれば特に限定されるものではなく、例えば、珪藻土、パーライト、ゼオライト、活性アルミナ、シリカゲル、砂、石等、公知のものを用いることができる。担体重量又は担体体積あたりの保水量や価格の観点から粒子形状が多孔質であるシリカ、珪藻土、ゼオライトが好ましく、沈降性湿式シリカがさらに好ましい。また、酸素吸収性能の観点から、保水担体を水スラリーとした際のpHが7に近いものが好ましい。
<Water retention carrier>
From the viewpoint of improving the handleability of the oxygen absorber composition, the oxygen absorber composition of the present embodiment further contains a water retention carrier. The water retention carrier is not particularly limited as long as it can support water, and known materials such as diatomaceous earth, perlite, zeolite, activated alumina, silica gel, sand and stone can be used. From the viewpoint of the amount of water retention per carrier weight or carrier volume and the price, silica having a porous particle shape, diatomaceous earth, and zeolite are preferable, and precipitating wet silica is more preferable. From the viewpoint of oxygen absorption performance, it is preferable that the pH of the water-retaining carrier when it is made into a water slurry is close to 7.
保水担体の性状は特に限定されないが、後述する脱酸素剤の製造時の取り扱い性の観点から流動性が高い粉体状のものが好適に用いられ、形状は球形に近いものがより好ましい。保水担体の粒径は10〜100μmであることが好ましく、30〜70μmであることがより好ましい。保水担体の粒径が大き過ぎると分級による成分の不均一化の原因となり、逆に小さすぎると取り扱い時の飛散を引き起こすため好ましくない。保水担体の粒径を上記好ましい範囲とすることで脱酸素剤を製造する際に取り扱い性の良い脱酸素剤組成物を得ることができる。保水担体の粒子は上記好ましい範囲の粒度を有するものであれば、一次粒子、凝集粒子、造粒物の別を問わず用いることができる。上記の範囲の粒度を有する保水担体は一種単独で用いることもでき、異なる粒度を有する複数種を任意の割合で混合して用いることもできる。 The property of the water-retaining carrier is not particularly limited, but a powdery one having high fluidity is preferably used from the viewpoint of handleability during production of the oxygen scavenger to be described later, and one having a shape close to a sphere is more preferred. The particle size of the water retention carrier is preferably 10 to 100 μm, more preferably 30 to 70 μm. If the particle size of the water-retaining carrier is too large, it may cause non-uniformity of the components due to classification, and if it is too small, it may cause scattering during handling, which is not preferable. By setting the particle size of the water-retaining carrier within the above-mentioned preferable range, it is possible to obtain an oxygen scavenger composition having good handleability when producing an oxygen scavenger. The water-retaining carrier particles can be used regardless of whether they are primary particles, agglomerated particles, or granulated particles, as long as they have a particle size within the above-mentioned preferred range. The water-retaining carrier having a particle size in the above range may be used alone or in combination of a plurality of kinds having different particle sizes at an arbitrary ratio.
保水担体の含有量は特に限定されないが、水100質量部に対し20〜500質量部とすることが好ましく、30〜300質量部とすることがより好ましい。 The content of the water retention carrier is not particularly limited, but is preferably 20 to 500 parts by mass, and more preferably 30 to 300 parts by mass with respect to 100 parts by mass of water.
<活性炭>
本実施形態の脱酸素剤組成物には必要に応じて活性炭を反応促進剤として加える事ができる。用いる活性炭は木質、ヤシ殻、石炭等の種類は問わない。活性炭の含有量は特に限定されないが、脱酸素剤組成物の総量に対し5質量%以下が好ましく、2質量%以下がより好ましい。活性炭を含有することにより50%RH以下の低湿度雰囲気下における脱酸素剤組成物の酸素吸収性能が一層向上する。
<Activated carbon>
Activated carbon can be added to the oxygen scavenger composition of the present embodiment as a reaction accelerator, if necessary. The activated carbon used may be wood, coconut shell, coal or the like. Although the content of the activated carbon is not particularly limited, it is preferably 5% by mass or less and more preferably 2% by mass or less with respect to the total amount of the oxygen absorber composition. By containing activated carbon, the oxygen absorbing performance of the oxygen absorber composition in a low humidity atmosphere of 50% RH or less is further improved.
<脱酸素剤組成物の製造方法>
本実施形態の脱酸素剤組成物は下記に示す工程により製造することができるが、これに限定されるものではない。下記工程とすることで均一な脱酸素剤組成物を作製することができる。
<1> 塩化カルシウムを水に溶解させる工程
<2> 工程<1>により作製した水溶液を保水担体に担持させる工程
<3> 工程<2>により作製した保水担体へ鉄粉を添加し混合する工程
<Method for producing oxygen absorber composition>
The oxygen scavenger composition of the present embodiment can be manufactured by the steps shown below, but is not limited thereto. A uniform oxygen absorber composition can be produced by the following steps.
<1> A step of dissolving calcium chloride in water <2> A step of supporting an aqueous solution prepared by the step <1> on a water retention carrier <3> A step of adding iron powder to the water retention carrier prepared by the step <2> and mixing
<脱酸素剤の包装形態>
本実施形態の脱酸素剤組成物は種々の形態に包装され、食品や医薬品等の品質、鮮度保持に用いられる。脱酸素剤の包装形態としては熱接着可能な樹脂層を含む多層フィルムによる小袋型の包装、及び熱可塑性樹脂容器への充填包装によるキャニスター形態が挙げられるが、これらに限定されない。
<Package form of oxygen absorber>
The oxygen scavenger composition of this embodiment is packaged in various forms and used for maintaining the quality and freshness of foods, pharmaceuticals and the like. Examples of the packaging form of the oxygen scavenger include, but are not limited to, a pouch-type packaging with a multilayer film including a heat-bondable resin layer, and a canister form by filling and packaging in a thermoplastic resin container.
<小袋型脱酸素剤>
本実施形態では、脱酸素剤組成物を熱接着可能な樹脂層を含む多層フィルムを用いて包装することにより、小袋型の脱酸素剤を形成することができる。上記多層フィルムとしては、脱酸素剤組成物と接する側に熱接着可能な層(以下、シーラント層)が設けられていれば特に限定されないが、内包される脱酸素剤組成物が包装袋外に漏れる恐れがなく、酸素吸収効果が十分に得られる通気性の高い多層フィルムが好適に用いられる。例えば、和紙、洋紙、レーヨン紙などの紙類、パルプ、セルロース、合成樹脂からの繊維などの各種繊維類を用いた不織布等を、開孔を施したシーラント層と積層した多層フィルム、より好ましくは更に開孔を施したポリエステル、ポリアミド、ポリ塩化ビニリデン等の耐熱性を有する樹脂フィルムをシーラント層と反対側に積層した多層フィルムが挙げられる。上記シーラント層としては熱接着した際に十分なヒートシール強度を有するものであれば特に限定されず、低密度ポリエチレン、直鎖低密度ポリエチレン(以下、LLDPE)、無延伸ポリプロピレン等のポリオレフィン樹脂フィルム;エチレン酢酸ビニル共重合体、エチレンメタクリル酸共重合体、エチレンアクリル酸共重合体、エチレンアクリル酸メチル等のコポリマーフィルム;アイオノマー(商標)等、市販のものを用いることができる。
<Pouch type oxygen absorber>
In the present embodiment, a pouch-type oxygen scavenger can be formed by packaging the oxygen scavenger composition with a multilayer film including a heat-bondable resin layer. The multilayer film is not particularly limited as long as a heat-bondable layer (hereinafter, sealant layer) is provided on the side in contact with the oxygen absorber composition, but the oxygen absorber composition to be contained is outside the packaging bag. A highly breathable multilayer film that does not leak and has a sufficient oxygen absorbing effect is preferably used. For example, a multi-layer film in which papers such as Japanese paper, western paper, rayon paper, pulp, cellulose, and non-woven fabrics using various fibers such as fibers from synthetic resin are laminated with a perforated sealant layer, and more preferably, Further, a multilayer film in which a heat-resistant resin film such as perforated polyester, polyamide, or polyvinylidene chloride is laminated on the side opposite to the sealant layer can be used. The sealant layer is not particularly limited as long as it has sufficient heat seal strength when heat-bonded, and a polyolefin resin film such as low density polyethylene, linear low density polyethylene (hereinafter, LLDPE), unstretched polypropylene and the like; Copolymer films of ethylene vinyl acetate copolymer, ethylene methacrylic acid copolymer, ethylene acrylic acid copolymer, ethylene methyl acrylate and the like; commercially available products such as Ionomer (trademark) can be used.
上記小袋型脱酸素剤の充填包装形態はピロー包装形態、三方シール包装形態、四方シール包装形態等、公知の包装形態をとることができ、各々、スティックパッカー、ロータリーパッカー、四方充填包装機等、公知の充填包装機を用いて充填包装することができる。 Filling and packaging form of the sachet-type oxygen scavenger can be a known packaging form such as pillow packaging form, three-way sealing packaging form, four-side sealing packaging form, etc., respectively, stick packer, rotary packer, four-way filling packaging machine, etc. Filling and packaging can be performed using a known filling and packaging machine.
<キャニスター型脱酸素剤>
本実施形態では、脱酸素剤組成物をキャニスター型容器に充填包装することによりキャニスター型の脱酸素剤を形成することができる。キャニスター型容器としては熱可塑性樹脂容器が好ましい。熱可塑性樹脂容器としては、低密度ポリエチレン、高密度ポリエチレン、ポリプロピレン等のポリオレフィン製容器;ポリ塩化ビニル、ポリ塩化ビニリデン等の塩素化ポリオレフィン製容器;ポリエチレンテレフタレート(以下、PET)等のポリエステル製容器;エチレン酢酸ビニル共重合体、エチレンメタクリル酸メチル共重合体、環状オレフィンコポリマー等のコポリマー製容器等公知のものを用いることができる。価格、耐衝撃性、安全性、耐熱性、加工性等の観点からポリオレフィン製容器または塩素化ポリオレフィン製容器がより好ましく、ポリプロピレン製容器またはポリ塩化ビニル製容器が更に好ましい。
<Canister type oxygen absorber>
In this embodiment, a canister type oxygen absorber can be formed by filling and packaging the oxygen absorber composition in a canister type container. As the canister type container, a thermoplastic resin container is preferable. As the thermoplastic resin container, a container made of polyolefin such as low density polyethylene, high density polyethylene or polypropylene; a container made of chlorinated polyolefin such as polyvinyl chloride or polyvinylidene chloride; a container made of polyester such as polyethylene terephthalate (hereinafter PET); A known container such as a container made of a copolymer such as an ethylene-vinyl acetate copolymer, an ethylene-methyl methacrylate copolymer, or a cyclic olefin copolymer can be used. From the viewpoints of price, impact resistance, safety, heat resistance, processability, etc., a polyolefin container or a chlorinated polyolefin container is more preferable, and a polypropylene container or a polyvinyl chloride container is further preferable.
<脱酸素剤の酸素吸収性能>
本実施形態の脱酸素剤の酸素吸収性能は、酸素吸収速度を示す指標としての脱酸素時間及び、酸素吸収量により評価される。脱酸素時間とは、ある一定容積の空気と脱酸素剤を酸素バリア袋に共封した際に、脱酸素剤が酸素バリア袋内の酸素を吸収し袋内の濃度が0.1容量%未満となるまでに要した時間を言い、酸素吸収量とは過剰量の空気と脱酸素剤を酸素バリア袋内に共封し、ある一定の期間保存した後に測定した袋内の酸素濃度より導かれる袋内酸素減少量を言う。
<Oxygen absorption performance of oxygen absorber>
The oxygen absorption performance of the oxygen scavenger of the present embodiment is evaluated by the oxygen removal time and the oxygen absorption amount as an index showing the oxygen absorption rate. The deoxidizing time means that when a certain volume of air and an oxygen scavenger are co-sealed in the oxygen barrier bag, the oxygen scavenger absorbs oxygen in the oxygen barrier bag and the concentration in the bag is less than 0.1% by volume. The oxygen absorption amount is derived from the oxygen concentration in the bag measured after enclosing the excess oxygen and oxygen scavenger in an oxygen barrier bag and storing it for a certain period of time. The amount of oxygen reduction in the bag.
<脱酸素剤からの水分移行>
本実施形態の脱酸素剤を食品や医薬品の保存に用いた際には、脱酸素剤組成物に含有される水分の保存する物品への移行を最小限に抑えることができる。上記水分移行の程度は脱酸素剤組成物の水分活性と被保存物の水分活性を測定することにより評価することができる。水分活性の測定方法は特に限定されず、露点式水分活性測定機等公知の機器を用いて測定することができる。
<Moisture migration from oxygen absorber>
When the oxygen scavenger of the present embodiment is used for storage of foods and pharmaceuticals, it is possible to minimize the transfer of water contained in the oxygen scavenger composition to the stored product. The degree of water migration can be evaluated by measuring the water activity of the oxygen absorber composition and the water activity of the stored material. The method for measuring the water activity is not particularly limited, and it can be measured using a known device such as a dew point water activity measuring device.
以下に本発明の実施例を示し、さらに具体的に説明する。なお、本発明は、これらの実施例に限定されるものではない。 Examples of the present invention will be shown below and will be described more specifically. The present invention is not limited to these examples.
以下の実施例において、鉄粉、塩化カルシウム無水物、活性炭、水酸化カルシウムは、和光純薬工業株式会社製の試薬を用いた。 In the following examples, reagents made by Wako Pure Chemical Industries, Ltd. were used for iron powder, calcium chloride anhydrous, activated carbon, and calcium hydroxide.
(実施例1)
<脱酸素剤組成物の作製>
塩化カルシウム二水和物25gを水25gへ溶解させて水溶液を調製した。これを保水担体である沈降性湿式シリカ20gへ添加混合することにより水分供与剤を得た。
上記水分供与剤全量と鉄粉100gとを混合し活性炭1.0gを添加することにより脱酸素剤組成物を得た。
(Example 1)
<Preparation of oxygen absorber composition>
An aqueous solution was prepared by dissolving 25 g of calcium chloride dihydrate in 25 g of water. This was added to and mixed with 20 g of precipitating wet silica which is a water retention carrier to obtain a moisture donor.
An oxygen absorber composition was obtained by mixing 100 g of iron powder with 100 g of iron powder and adding 1.0 g of activated carbon.
<脱酸素剤組成物の水分活性評価>
得られた脱酸素剤組成物の水分活性を、露点式水分活性測定機を用いて評価した。25℃における脱酸素剤組成物の水分活性は0.45であった。
<Evaluation of water activity of oxygen absorber composition>
The water activity of the obtained oxygen scavenger composition was evaluated using a dew point water activity measuring device. The water activity of the oxygen absorber composition at 25 ° C. was 0.45.
<小袋型脱酸素剤の作製>
LLDPE(厚み30μm)/洋紙(目付50g/m2)/PET(厚み12μm)の構成の多層シートを用いてLLDPEが内側となるように、幅20mm×ピッチ40mm、下部シール幅及び背貼りシール幅5mmの寸法のピロー包装袋を作製した。該ピロー包装袋に上記脱酸素剤組成物1.0gを充填し、上部シール幅5mmとなるようにピロー包装袋上端を熱接着し評価試料とした。
<Preparation of sachet type oxygen absorber>
Width 20 mm x pitch 40 mm, lower seal width and spine sticker width so that the LLDPE is on the inside by using a multi-layered sheet of LLDPE (thickness 30 μm) / paper (weight per unit area 50 g / m 2 ) / PET (thickness 12 μm) A pillow packaging bag having a size of 5 mm was produced. The pillow packaging bag was filled with 1.0 g of the oxygen scavenger composition, and the upper end of the pillow packaging bag was heat-bonded so as to have an upper seal width of 5 mm to obtain an evaluation sample.
<小袋型脱酸素剤の酸素吸収量評価>
上記により作製した小袋型脱酸素剤試料を1.0Lの空気とともにバリア袋に封入し、端部を熱接着し密封した。該バリア袋を25℃にて14日間保存し、袋内の酸素濃度をジルコニア式酸素濃度計により測定した。大気中酸素濃度との濃度差より酸素吸収量を計算した結果、59mLであった。
<Evaluation of oxygen absorption of sachet type oxygen absorber>
The pouch type oxygen absorber sample prepared as described above was enclosed in a barrier bag together with 1.0 L of air, and the ends were heat-bonded and sealed. The barrier bag was stored at 25 ° C. for 14 days, and the oxygen concentration in the bag was measured with a zirconia oxygen analyzer. As a result of calculating the oxygen absorption amount from the difference in concentration with the atmospheric oxygen concentration, it was 59 mL.
(実施例2及び比較例1〜4)
表1に示す組成としたこと以外は、実施例1と同様にして実験を行った。結果を表1に示す。
(Example 2 and Comparative Examples 1 to 4)
An experiment was conducted in the same manner as in Example 1 except that the composition shown in Table 1 was used. The results are shown in Table 1.
表1からも明らかなように、実施例1及び2では水分活性が0.5以下を示し、塩化カルシウム水溶液の調製が容易で、かつ、酸素吸収性能が良好な結果であることが確認された。一方、比較例1及び2では塩化カルシウム水溶液の調製が困難であること、比較例3及び4では水分活性が0.5を超えるため食品等への水分移行の観点から好ましくないことが確認された。 As is clear from Table 1, in Examples 1 and 2, the water activity was 0.5 or less, and it was confirmed that the calcium chloride aqueous solution was easily prepared and the oxygen absorption performance was good. . On the other hand, in Comparative Examples 1 and 2, it was confirmed that it was difficult to prepare an aqueous calcium chloride solution, and in Comparative Examples 3 and 4, the water activity exceeded 0.5, which was not preferable from the viewpoint of water migration to foods and the like. .
(実施例3)
<キャニスター型脱酸素剤の作製>
図1に示すポリプロピレン製容器に実施例1と同様の脱酸素剤組成物1.0gを充填し、PET(厚み12μm)/ボール紙(目付150g/m2)の構成の多層シートよりなるフタ材を紙側がキャニスター内側(原末側)となるように加締めてキャニスター形状とし、評価試料とした。
(Example 3)
<Preparation of canister type oxygen absorber>
A polypropylene container shown in FIG. 1 was filled with 1.0 g of the same oxygen scavenger composition as in Example 1, and a lid member made of a multi-layer sheet of PET (thickness 12 μm) / cardboard (weight per unit area 150 g / m 2 ). Was crimped into a canister shape so that the paper side was the inside of the canister (the bulk powder side), and this was used as the evaluation sample.
<キャニスター型脱酸素剤の酸素吸収量評価>
上記により作製したキャニスター型脱酸素剤試料の酸素吸収量を小袋型脱酸素剤の酸素吸収量評価と同様の方法にて求めた結果、56mLであった。
<Evaluation of oxygen absorption amount of canister type oxygen absorber>
The oxygen absorption amount of the canister-type oxygen absorber prepared as described above was 56 mL as a result of the same method as the evaluation of the oxygen absorption amount of the pouch-type oxygen absorber.
本発明によれば、50%RH以下の低湿度雰囲気下においても優れた酸素吸収性能を有し、かつ保存する物品への水分移行の少ない脱酸素剤組成物が提供される。特に、乾燥食品や米菓等の水分を嫌う食品や錠剤、散剤等の水分により劣化する医薬品の保存に適する脱酸素剤組成物が廉価に提供される。これにより、従来であれば水分移行の懸念から高水分活性の脱酸素剤を適用できなかった食品や医薬品に対し、優れた酸素吸収性能を有する脱酸素剤を有効に用いることができる。 According to the present invention, an oxygen scavenger composition having excellent oxygen absorption performance even in a low humidity atmosphere of 50% RH or less and having less migration of water to an article to be stored is provided. In particular, an oxygen scavenger composition suitable for storage of foods such as dried foods and rice crackers that do not like water, and medicines such as tablets and powders that deteriorate due to water is provided at a low price. This makes it possible to effectively use a deoxidizer having an excellent oxygen absorption performance for foods and pharmaceuticals to which a high water activity deoxidizer could not be applied due to the concern of water migration.
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