JP2007307451A - Oxygen scavenger composition - Google Patents

Oxygen scavenger composition Download PDF

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JP2007307451A
JP2007307451A JP2006137161A JP2006137161A JP2007307451A JP 2007307451 A JP2007307451 A JP 2007307451A JP 2006137161 A JP2006137161 A JP 2006137161A JP 2006137161 A JP2006137161 A JP 2006137161A JP 2007307451 A JP2007307451 A JP 2007307451A
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carbon dioxide
oxygen
oxygen scavenger
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Koji Morishita
浩次 森下
Tomoharu Himejima
智晴 姫嶋
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Mitsubishi Gas Chemical Co Inc
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Mitsubishi Gas Chemical Co Inc
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02CCAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
    • Y02C20/00Capture or disposal of greenhouse gases
    • Y02C20/40Capture or disposal of greenhouse gases of CO2

Abstract

<P>PROBLEM TO BE SOLVED: To provide an oxygen scavenger composition which controls the amount of carbon dioxide generated and absorbed to preserve an article in a deoxygenated state under a particular carbon dioxide concentration without affecting the carbon dioxide concentration. <P>SOLUTION: The oxygen scavenger is prepared by mixing a substance obtained by immersing a porous material (c) with an unsaturated fatty acid or chain hydrocarbon polymer (a) and a catalyst (b), a hydroxide (d) of an alkaline earth metal, a moisture imparting agent (e) and a deodorant (f). The oxygen scavenger is comprised of 0.1-0.5 pts.wt. of the catalyst (b), 50-300 pts.wt. of the porous material (c), 0.3-10 pts.wt. of the hydroxide of the alkaline earth metal (d), 30-100 pts.wt. of the moisture imparting agent and 10-100 pts.wt. of the deodorant per 100 pts.wt. of the unsaturated fatty acid or chain hydrocarbon polymer. <P>COPYRIGHT: (C)2008,JPO&INPIT

Description

本発明は、炭酸ガスの発生量及び吸収量を調節した新規脱酸素剤に関する。例えば、大気組成下で脱酸素剤から実質的に炭酸ガスを発生しない事、及び、炭酸ガス濃度10%下で脱酸素剤が実質的に炭酸ガスを吸収しない事などが要求される脱酸素剤の用途に用いられる。なお、「実質的に」とは、例えば、大気組成下で脱酸素剤からの炭酸ガス発生量が1ml/g以下であり、炭酸ガス濃度10%下での脱酸素剤の炭酸ガス吸収量が5ml/g以下である事をここでは意味するものである。   The present invention relates to a novel oxygen scavenger in which the generation amount and absorption amount of carbon dioxide gas are adjusted. For example, an oxygen scavenger that requires substantially no carbon dioxide from the oxygen scavenger under atmospheric composition and that the oxygen scavenger does not substantially absorb carbon dioxide at a carbon dioxide concentration of 10%. Used for Note that “substantially” means, for example, that the amount of carbon dioxide generated from the oxygen scavenger is 1 ml / g or less under the atmospheric composition, and the amount of carbon dioxide absorbed by the oxygen absorber under a carbon dioxide concentration of 10%. It means here that it is less than 5ml / g.

従来より、食品や医薬品の酸化防止、保存性向上等の為にこれら対象物を脱酸素剤と共に容器に密閉し、密閉容器内を無酸素状態にする方法が用いられている。その対象物の中には炭酸ガスを実質的に吸収及び発生しない脱酸素剤が必要とされる場合がある。
例えば、特許文献1〜3には、制酸薬、アシドーシス治療薬等として炭酸水素ナトリウム注射薬等が薬液のpH変動を避けるためにガスバリアーフィルムで密閉され、鉄系やアスコルビン酸系の脱酸素剤と共に使用された発明が開示されている。
Conventionally, in order to prevent oxidation of foods and pharmaceuticals, improve storage stability, and the like, these objects are sealed in a container together with an oxygen scavenger, and the inside of the sealed container is made oxygen-free. Some objects require an oxygen scavenger that does not substantially absorb and generate carbon dioxide.
For example, in Patent Documents 1 to 3, sodium bicarbonate injection as an antacid, acidosis treatment, etc. is sealed with a gas barrier film to avoid pH fluctuation of the chemical solution, and iron-based or ascorbic acid-based deoxygenation The invention used with the agent is disclosed.

しかし、これらの脱酸素剤は酸素を吸収するのみではなく、炭酸ガスを吸収又は発生する反応を伴う。例えば、鉄系の脱酸素剤は鉄が酸素のみでなく炭酸ガスとも反応し炭酸鉄化合物が形成されるため、炭酸ガスを吸収する。脱酸素剤が炭酸ガスを吸収すると、薬液から炭酸ガスが放出されるため、薬効を維持するために必要な薬液のpHが維持できない問題点があった。また、鉄と炭酸ガスが反応することにより、鉄と酸素の反応が阻害されるため、脱酸素剤の酸素吸収性能が低下する問題点があった。   However, these oxygen scavengers not only absorb oxygen but also involve a reaction that absorbs or generates carbon dioxide. For example, an iron-based oxygen scavenger absorbs carbon dioxide because iron reacts not only with oxygen but also with carbon dioxide to form an iron carbonate compound. When the oxygen scavenger absorbs carbon dioxide, carbon dioxide is released from the chemical solution, so that there is a problem that the pH of the chemical solution necessary for maintaining the medicinal effect cannot be maintained. Moreover, since the reaction between iron and carbon dioxide gas inhibits the reaction between iron and oxygen, there is a problem in that the oxygen absorbing performance of the oxygen scavenger is lowered.

一方、アスコルビン酸系の脱酸素剤は、酸素吸収に伴い酸素吸収量の50%〜95%程度の炭酸ガスを発生し、発生した炭酸ガスが薬液中に溶け込むため、薬効を維持するために必要な薬液のpHが維持できない問題点があった。   On the other hand, ascorbic acid-based oxygen scavengers generate carbon dioxide that is about 50% to 95% of the amount of oxygen absorbed along with oxygen absorption, and the generated carbon dioxide dissolves in the chemical solution, so it is necessary to maintain its efficacy. However, there was a problem that the pH of various chemical solutions could not be maintained.

炭酸ガスは静菌・防虫作用があり、好気性菌、カビ、害虫などの発生を抑え、腐敗、虫害防止に効果を発揮する。炭酸ガス濃度が30%で一応の効果があり、50%以上ではカビが防止できる事が知られている。例えば、生肉、ウィンナーソーセージ、和・洋生菓子、半生菓子、豆類、穀類等では炭酸ガス置換密閉包装が用いられており、脱酸素剤が併用される場合もある。この場合、密閉容器内は特定の炭酸ガス濃度を維持することが必要であるため、炭酸ガスを吸収又は放出する脱酸素剤は使用が困難である問題点があった。   Carbon dioxide has a bacteriostatic and insecticidal action, suppresses the generation of aerobic bacteria, fungi, and insects, and is effective in preventing spoilage and insect damage. It is known that the carbon dioxide concentration is 30%, it has a temporary effect, and if it exceeds 50%, mold can be prevented. For example, fresh meat, wiener sausage, Japanese / Western confectionery, semi-fresh confectionery, beans, cereals and the like use carbon dioxide-substituted sealed packaging, and an oxygen scavenger may be used in combination. In this case, since it is necessary to maintain a specific carbon dioxide gas concentration in the sealed container, there has been a problem that it is difficult to use an oxygen scavenger that absorbs or releases carbon dioxide.

特許文献4、5および6には不飽和脂肪酸化合物又は不飽和基を有する鎖状炭化水素重合物を酸化反応物質とする脱酸素剤に関する発明が開示されている。これらの酸化反応物質は酸素吸収に伴い若干の炭酸ガスを発生するため、炭酸ガスを吸収する手段を施さなければ炭酸ガスの発生量、吸収量が調節されず、密閉容器内の特定の炭酸ガス濃度を実質的に一定に保つことができなかった。
特開平5-049675号公報 特開2001-192069 特開平8-164185号公報 特開平4-029741号公報 特開2003-128151 特開平8-282739号公報
Patent Documents 4, 5 and 6 disclose inventions relating to oxygen scavengers using an unsaturated fatty acid compound or a chain hydrocarbon polymer having an unsaturated group as an oxidation reactant. Since these oxidation reactants generate some carbon dioxide with oxygen absorption, the amount of generated carbon dioxide and the amount of carbon dioxide cannot be adjusted unless a means for absorbing carbon dioxide is applied. The concentration could not be kept substantially constant.
JP-A-5-04675 JP 2001-192069 A JP-A-8-164185 Japanese Patent Laid-Open No. 4-029741 JP 2003-128151 A JP-A-8-282737

本発明は、酸素、炭酸ガス共存下のガス組成における物品の保存において、密閉容器内及び対象物中の炭酸ガス濃度に依存しない脱酸素保存のため、大気組成下で炭酸ガスを実質的に発生せず、高濃度の炭酸ガス存在下で炭酸ガスを実質的に吸収しない脱酸素剤を提供することを目的とする。   The present invention substantially generates carbon dioxide under atmospheric composition for storage of articles in a gas composition coexisting with oxygen and carbon dioxide for deoxygenation preservation independent of the concentration of carbon dioxide in the sealed container and the object. And an oxygen scavenger that does not substantially absorb carbon dioxide in the presence of a high concentration of carbon dioxide.

本発明者らは、前記目的のため、不飽和脂肪酸系の脱酸素剤をベースとして鋭意検討した結果、大気組成下で炭酸ガスを実質的に発生せず、高濃度の炭酸ガス存在下で炭酸ガスを実質的に吸収しないものを見出し、本発明を完成させるに至った。
すなわち、本発明は、(a)不飽和脂肪酸化合物又は不飽和基を有する鎖状炭化水素重合物及び(b)触媒を(c)多孔体に含浸したもの、(d)アルカリ土類金属の水酸化物、(e)水分供与剤及び(f)脱臭剤を混合したものからなり、(a)不飽和脂肪酸化合物又は不飽和基を有する鎖状炭化水素重合物100重量部に対して、(b)触媒が0.01〜0.5重量部、(c)多孔体が50〜300重量部、(d)アルカリ土類金属の水酸化物が0.3〜10重量部、(e)水分供与剤が30〜100重量部、(f)脱臭剤が10〜100重量部である脱酸素剤である。
As a result of intensive investigations based on unsaturated fatty acid-based oxygen scavengers for the above purpose, the inventors of the present invention did not substantially generate carbon dioxide under atmospheric composition, and carbon dioxide in the presence of high-concentration carbon dioxide. The inventors have found a substance that does not substantially absorb gas and have completed the present invention.
That is, the present invention comprises (a) an unsaturated fatty acid compound or a chain hydrocarbon polymer having an unsaturated group and (b) a catalyst impregnated in (c) a porous body, (d) an alkaline earth metal water. It comprises a mixture of an oxide, (e) a moisture donor and (f) a deodorant, and (a) 100 parts by weight of an unsaturated fatty acid compound or a chain hydrocarbon polymer having an unsaturated group, ) 0.01-0.5 parts by weight of catalyst, (c) 50-300 parts by weight of porous material, (d) 0.3-10 parts by weight of alkaline earth metal hydroxide, (e) 30-100 parts by weight of water donor Part (f) is a deoxygenating agent whose deodorizing agent is 10 to 100 parts by weight.

本発明においては、大気組成下での炭酸ガス発生量が1ml/g以下であり、かつ、炭酸ガス濃度10%下での炭酸ガス吸収量が5ml/g以下であることが好ましい。また、(c)多孔体及び(e)水分供与剤の多孔体が珪藻土であること、(d)アルカリ土類金属の水酸化物が消石灰である脱酸素剤が好ましい。   In the present invention, it is preferable that the amount of carbon dioxide generated under the atmospheric composition is 1 ml / g or less, and the amount of carbon dioxide absorbed when the carbon dioxide concentration is 10% is 5 ml / g or less. Further, (c) the porous body and (e) the porous body of the moisture donor are preferably diatomaceous earth, and (d) an oxygen scavenger in which the alkaline earth metal hydroxide is slaked lime.

本脱酸素剤は、実質的に炭酸ガス濃度の変化に関与しないので、特定の炭酸ガス濃度下での保存を必要とする食品、医薬品等の物品についても、安定して長期保存することが可能となった。   Since this oxygen scavenger is not substantially involved in the change in carbon dioxide concentration, it can be stored stably for a long period of time even for foods, pharmaceuticals and other items that require storage under a specific carbon dioxide concentration. It became.

本発明における脱酸素剤の各成分の割合は、(a)不飽和脂肪酸化合物または不飽和基を有する鎖状炭化水素重合物(以下、酸化反応物質)100重量部に対して、(b)触媒が0.01〜0.5重量部、好ましくは0.01〜0.1重量部、(c)多孔体が50〜300重量部、好ましくは100〜250重量部、(d)アルカリ土類金属の水酸化物が0.3〜10重量部、好ましくは0.5〜7重量部、(e)水分供与剤が30〜100重量部、好ましくは50〜80重量部、(f)脱臭剤が10〜100重量部、好ましくは10〜80重量部である。密閉包装時の初期酸素量、包装材料の酸素透過量に応じ、各成分の使用量を最適化する。   The proportion of each component of the oxygen scavenger in the present invention is such that (a) 100 parts by weight of an unsaturated fatty acid compound or a chain hydrocarbon polymer having an unsaturated group (hereinafter referred to as an oxidation reactant) is (b) a catalyst. 0.01 to 0.5 parts by weight, preferably 0.01 to 0.1 parts by weight, (c) 50 to 300 parts by weight of porous material, preferably 100 to 250 parts by weight, and (d) 0.3 to 10 parts by weight of alkaline earth metal hydroxide. Parts by weight, preferably 0.5 to 7 parts by weight, (e) 30 to 100 parts by weight of water donor, preferably 50 to 80 parts by weight, (f) 10 to 100 parts by weight of deodorant, preferably 10 to 80 parts by weight Part. The usage amount of each component is optimized according to the initial oxygen amount during hermetic packaging and the oxygen permeation amount of the packaging material.

(b)触媒が少ない場合は酸素吸収性能が低下し、多い場合は酸素吸収速度が過剰に早くなり、大気中での取り扱い時に酸素を吸収するため酸素吸収性能が低下する。(e)多孔体が少ない場合は(a)酸化反応物質を含浸することができず酸素吸収性能が低下し、多い場合は脱酸素剤の体積が大きくなりコスト増となる。(d)アルカリ土類金属の水酸化物が少ない場合は、(a)酸化反応物質の酸化反応に伴い発生する炭酸ガスを吸収することができず、大気組成下での容器内の炭酸ガス濃度が上昇し、多い場合は過剰に炭酸ガスを吸収するため容器内の炭酸ガス濃度が低下する。(e)水分供与剤が少ない場合は(d)アルカリ土類金属の水酸化物の炭酸ガス吸収性能が低下し、多い場合は脱酸素剤の体積が大きくなりコスト増となる。(f)脱臭剤が少ない場合は酸素吸収反応に伴い副生成するカルボン酸等の臭気ガスを吸収できず臭気が強くなり、多い場合は炭酸ガス吸収量が多くなり容器内の炭酸ガス濃度が低下する。     (b) When the amount of the catalyst is small, the oxygen absorption performance is lowered. When the amount is large, the oxygen absorption rate is excessively increased, and oxygen is absorbed when handled in the air, so that the oxygen absorption performance is lowered. (e) When the porous body is small, (a) the oxygen-reactive substance cannot be impregnated, and the oxygen absorption performance is lowered. (d) When the alkaline earth metal hydroxide is low, (a) carbon dioxide gas generated by the oxidation reaction of the oxidation reactant cannot be absorbed, and the carbon dioxide concentration in the container under atmospheric composition When the amount of carbon dioxide increases, carbon dioxide is excessively absorbed, so that the concentration of carbon dioxide in the container decreases. (e) When the moisture donor is small, (d) the carbon dioxide absorption performance of the alkaline earth metal hydroxide decreases, and when it is large, the volume of the oxygen scavenger increases and the cost increases. (f) When there are few deodorizers, odorous gas such as carboxylic acid produced as a by-product in the oxygen absorption reaction cannot be absorbed and the odor becomes strong, and when there are many deodorizers, the amount of carbon dioxide absorption increases and the concentration of carbon dioxide in the container decreases. To do.

本発明における脱酸素剤の酸化反応物質は、(a)不飽和脂肪酸化合物または不飽和基を有する鎖状炭化水素重合物である。これらは、必ずしも単一物質である必要はなく、二種以上の混合物でも良い。また、これらは置換基を有していても良い。   The oxidation reaction material of the oxygen scavenger in the present invention is (a) an unsaturated fatty acid compound or a chain hydrocarbon polymer having an unsaturated group. These are not necessarily a single substance, and may be a mixture of two or more. Moreover, these may have a substituent.

不飽和脂肪酸化合物として、リノール酸、リノレン酸、アラキドン酸、パリナリン酸、ダイマー酸、植物油、動物油から得られる脂肪酸、即ち、アマニ油脂肪酸、大豆油脂肪酸、桐油脂肪酸、糠油脂肪酸、胡麻油脂肪酸、綿実油脂肪酸、菜種油脂肪酸、トール油脂肪酸、及びこれらのエステルを含有する油脂や金属塩を使用することができる。   As unsaturated fatty acid compounds, fatty acids obtained from linoleic acid, linolenic acid, arachidonic acid, parinaric acid, dimer acid, vegetable oil, animal oil, that is, linseed oil fatty acid, soybean oil fatty acid, tung oil fatty acid, coconut oil fatty acid, sesame oil fatty acid, cottonseed oil fatty acid Rapeseed oil fatty acid, tall oil fatty acid, and oils and metal salts containing these esters can be used.

不飽和基を有する鎖状炭化水素系重合物として、液状ブタジエンオリゴマー、液状イソプレンオリゴマー、スクアレン、液状アセチレンオリゴマー、液状ペンタジエンオリゴマー、液状オリゴエステルアクリレート、液状ブテンオリゴマー、液状BR、液状SBR、液状NBR、液状クロロプレンオリゴマー、液状サルファイドオリゴマー、液状イソブチレンオリゴマー、液状ブチルゴム、液状シクロペンタジエン系石油樹脂、液状オリゴスチレン、液状ヒドロキシポリオレフィンオリゴマー、液状アルキド樹脂、液状不飽和ポリエステル樹脂、天然ゴム等の液状の各種分子量のポリマーを使用することができる。   As a chain hydrocarbon polymer having an unsaturated group, liquid butadiene oligomer, liquid isoprene oligomer, squalene, liquid acetylene oligomer, liquid pentadiene oligomer, liquid oligoester acrylate, liquid butene oligomer, liquid BR, liquid SBR, liquid NBR, Liquid chloroprene oligomer, liquid sulfide oligomer, liquid isobutylene oligomer, liquid butyl rubber, liquid cyclopentadiene petroleum resin, liquid oligostyrene, liquid hydroxy polyolefin oligomer, liquid alkyd resin, liquid unsaturated polyester resin, natural rubber, etc. Polymers can be used.

本発明における酸化反応物質の酸化反応を促進する(b)触媒として、Cu、Fe、Co、Ni、Cr、Mn、Pb、Zn及びその化合物群から選ばれる少なくとも1種を使用することができる。例えば、硫酸塩、塩化物塩、硝酸塩等の無機塩、亜麻仁油、大豆油菜種油、トール油脂肪酸等の脂肪酸塩、ナフテン酸塩、オクチル酸塩、ロジン酸塩、アセチルアセトン金属塩等の有機塩、アルキル金属化合物等を使用することができる。これらCu、Fe、Co、Ni、Cr、Mn、Pb、Zn及びその化合物の中でも、酸化反応促進性能及び安全性の観点から、Fe、Co、Mn及びZnの塩が好ましい。   As the catalyst (b) for promoting the oxidation reaction of the oxidation reactant in the present invention, at least one selected from Cu, Fe, Co, Ni, Cr, Mn, Pb, Zn and a compound group thereof can be used. For example, inorganic salts such as sulfates, chloride salts, nitrates, fatty acid salts such as linseed oil, soybean oil, rapeseed oil, tall oil fatty acids, organic salts such as naphthenates, octylates, rosinates, metal salts of acetylacetone, Alkyl metal compounds and the like can be used. Among these Cu, Fe, Co, Ni, Cr, Mn, Pb, Zn, and compounds thereof, Fe, Co, Mn, and Zn salts are preferable from the viewpoint of oxidation reaction promoting performance and safety.

本発明において、(a)不飽和脂肪酸化合物または不飽和基を有する鎖状炭化水素重合物及び(b)触媒は(c)多孔体に含浸して用いることが好ましい。
(c)多孔体として、天然ゼオライト等の炭酸ガスの吸脱着量が比較的多い物質を用いた場合は、温度変化により炭酸ガスを物理的に吸脱着するため、容器内の炭酸ガス濃度が安定しない。一方、炭酸ガスの吸脱着しないか極めて少ない多孔体の場合は、温度変化による容器内の炭酸ガス濃度の変化がなく安定しており、かつ、容器内の炭酸ガス濃度に依存することなく酸素を吸収することができた。
In the present invention, (a) the unsaturated fatty acid compound or the chain hydrocarbon polymer having an unsaturated group and (b) the catalyst are preferably used by impregnating (c) the porous body.
(c) When a material with a relatively large amount of carbon dioxide adsorption / desorption, such as natural zeolite, is used as the porous body, the carbon dioxide concentration in the container is stable because the carbon dioxide is physically adsorbed / desorbed due to temperature changes. do not do. On the other hand, in the case of a porous body that does not adsorb or desorb carbon dioxide gas or has very little, there is no change in the carbon dioxide gas concentration in the container due to temperature change, and oxygen is not dependent on the carbon dioxide gas concentration in the container. Could be absorbed.

本発明における炭酸ガスを吸脱着しない(c)多孔体として、ホワイトカーボン、珪酸カルシウム、コロイダルシリカ、バーミキュライト、珪藻土などを使用することができる。これらの中でも安価で酸化反応物質の含浸率が高い珪藻土が好ましい。   In the present invention, white carbon, calcium silicate, colloidal silica, vermiculite, diatomaceous earth, or the like can be used as the porous body that does not absorb and desorb carbon dioxide gas. Among these, diatomaceous earth is preferable because it is inexpensive and has a high impregnation rate of the oxidation reaction substance.

本発明に用いる(a)不飽和脂肪酸化合物または不飽和基を有する鎖状炭化水素重合物は酸素吸収に伴い炭酸ガスを若干発生する。このため、(d)アルカリ土類金属の水酸化物により若干発生する炭酸ガスを吸収させる。
炭酸ガスを吸収する物質としては一般に、生石灰、消石灰、鉄、活性炭、モレキュラーシーブス等の合成ゼオライト、モルデナイト、エリオナイト等の天然ゼオライト等が知られている。密閉容器内の酸素濃度、炭酸ガス濃度は対象物ごとに異なるが、炭酸ガス吸収成分は容器内の炭酸ガス濃度に依存することなく一定量の炭酸ガスを吸収する必要がある。これより、炭酸ガス吸収量が炭酸ガス濃度に依存するゼオライト等の物理吸着系の物質は、本発明には不適当であり、化学反応により炭酸ガスを吸収するアルカリ土類金属の水酸化物が好ましく、これらの中でも炭酸ガス吸収速度が速い消石灰が好ましい。
The (a) unsaturated fatty acid compound or the chain hydrocarbon polymer having an unsaturated group used in the present invention generates a little carbon dioxide with oxygen absorption. For this reason, (d) carbon dioxide generated slightly by the alkaline earth metal hydroxide is absorbed.
As substances that absorb carbon dioxide, generally known are synthetic zeolites such as quick lime, slaked lime, iron, activated carbon and molecular sieves, and natural zeolites such as mordenite and erionite. Although the oxygen concentration and the carbon dioxide concentration in the sealed container vary depending on the object, the carbon dioxide absorbing component needs to absorb a certain amount of carbon dioxide gas without depending on the carbon dioxide concentration in the container. As a result, a substance of a physical adsorption system such as zeolite whose carbon dioxide absorption depends on the concentration of carbon dioxide is not suitable for the present invention, and an alkaline earth metal hydroxide that absorbs carbon dioxide by a chemical reaction is used. Among these, slaked lime having a high carbon dioxide absorption rate is preferable.

しかし、(d)アルカリ土類金属の水酸化物が、炭酸ガスを吸収するには水が必要であり、雰囲気からの水分補給の場合には相対湿度70%以上の水分が必要である事が確認された。そこで、適用する物品の水分活性や雰囲気相対湿度に依存することなく一定量の炭酸ガスを吸収させる方法について検討した結果、多孔体に水を含浸させたものなどの(e)水分供与剤を混合することにより、適用物品に依存しない方法を見出した。   However, (d) Alkaline earth metal hydroxides need water to absorb carbon dioxide, and water with a relative humidity of 70% or more is necessary when replenishing moisture from the atmosphere. confirmed. Therefore, as a result of investigating a method for absorbing a certain amount of carbon dioxide gas without depending on the water activity of the article to be applied and the relative humidity in the atmosphere, (e) mixing a water donating agent such as a porous body impregnated with water Thus, a method that does not depend on the applied article was found.

本発明の(e)水分供与剤として、水を保持(含浸)させた多孔体を用いる場合の多孔体としては、炭酸ガスを物理吸着しないもので、さらに、上記した好ましい態様である(a)酸化反応物を含浸する為に使用する(c)多孔体と同一のものが好ましい。酸素吸収剤と水分供与剤の粒径を揃え均一に混合することにより容易に機械で包装することができる。   As the porous body in the case of using a porous body in which water is retained (impregnated) as the (e) moisture donor of the present invention, the porous body does not physically adsorb carbon dioxide, and is a preferred embodiment described above (a) The same porous material (c) used for impregnation with the oxidation reaction product is preferred. It can be easily packaged by a machine by aligning the particle diameters of the oxygen absorbent and the moisture donor and mixing them uniformly.

水を多孔体に含浸してなる(e)水分供与剤の場合、各成分の割合は(d)アルカリ土類金属の水酸化物100重量部に対し、多孔体は600〜6000重量部、水は300〜4000重量部である。   (E) In the case of a moisture donor, the ratio of each component is (d) 100 to 100 parts by weight of an alkaline earth metal hydroxide, while the porous body is 600 to 6000 parts by weight of water. Is 300 to 4000 parts by weight.

本発明における(f)脱臭剤として、活性炭、活性炭素繊維、モレキュラーシービンカーボン、骨炭などから選択することができ、25℃、1/10大気圧(0.1atm)での炭酸ガス吸収量が5ml/g以下のものが好ましい。炭酸ガス吸収量が5ml/gより大きくなると炭酸ガス吸収量が多くなり、容器内の炭酸ガス濃度が低下する。   As the (f) deodorant in the present invention, it can be selected from activated carbon, activated carbon fiber, molecular sea carbon, bone charcoal, etc., and 5 ml of carbon dioxide absorption at 25 ° C. and 1/10 atmospheric pressure (0.1 atm). / g or less is preferable. When the carbon dioxide absorption is greater than 5 ml / g, the carbon dioxide absorption increases and the carbon dioxide concentration in the container decreases.

本発明に用いられる脱酸素剤は、通気性包装材料により充填包装して脱酸素剤包装体として使用することができる。その際に用いられる通気性包装材料としては、脱酸素剤用途に用いられる包装材料であれば特に制限はないが、速やかに酸素を吸収し、それに応じて発生する炭酸ガスを吸収させ、容器内のガス組成を一定に保つ為にもできるだけ通気性の高い包装材料が好ましい。   The oxygen absorber used in the present invention can be filled and packaged with a breathable packaging material and used as an oxygen absorber package. The breathable packaging material used at that time is not particularly limited as long as it is a packaging material used for an oxygen scavenger, but quickly absorbs oxygen and absorbs carbon dioxide gas generated accordingly, In order to keep the gas composition constant, a packaging material having as high a breathability as possible is preferable.

本発明が使用される容器は酸素バリア性を有した包装材料からなる。包装材料は、アルミニウム箔等の金属箔をラミネートしたフィルム、酸化珪素や酸化アルミニウム等を蒸着したフィルムをラミネートしたフィルム、バリアナイロンフィルムやKコートナイロンフィルムをラミネートしたフィルム等のガスバリアフィルム、また、HDPE、PP、PET、ポリビニルアルコール、エチレンビニルアルコール共重合体、エチレン酢酸ビニル共重合体、塩化ビニリデン重合体、Kコート樹脂、酸化ケイ素蒸着樹脂、酸化アルミ蒸着樹脂又はアルミ蒸着樹脂などを用いた容器を使用することができる。   The container in which the present invention is used is made of a packaging material having oxygen barrier properties. Packaging materials include films laminated with metal foils such as aluminum foil, films laminated with films deposited with silicon oxide, aluminum oxide, etc., gas barrier films such as films laminated with barrier nylon films and K-coated nylon films, and HDPE , PP, PET, polyvinyl alcohol, ethylene vinyl alcohol copolymer, ethylene vinyl acetate copolymer, vinylidene chloride polymer, K coat resin, silicon oxide vapor deposition resin, aluminum oxide vapor deposition resin or aluminum vapor deposition resin Can be used.

以下に本発明の具体的実施例を示し、本発明をさらに詳細に説明する。なお、本発明は実施例に限定されるものではない。   Specific examples of the present invention are shown below, and the present invention will be described in more detail. In addition, this invention is not limited to an Example.

実施例1
桐油(不飽和脂肪酸含量95 wt%)50g及びトール油脂肪酸Mn(Mn濃度4%)1.25gからなる液体混合物を珪藻土100gに加え攪拌、混合し、更に粒状活性炭37gを添加、混合し流動性のある粉粒体Aを得た。
次に水60gを上記と同種の珪藻土100gに含浸させた流動性のある粉粒体Bを得た。
最後に、粉粒体A100gに粉粒体B15gと微粉末の消石灰1.8gを均一混合し粉粒体Cを得た。
Example 1
A liquid mixture consisting of 50 g of paulownia oil (unsaturated fatty acid content 95 wt%) and 1.25 g of tall oil fatty acid Mn (Mn concentration 4%) is added to 100 g of diatomaceous earth, stirred and mixed, and 37 g of granular activated carbon is added and mixed to make it fluid. A certain granular material A was obtained.
Next, the fluid granular material B obtained by impregnating 60 g of water with 100 g of the same kind of diatomaceous earth as described above was obtained.
Finally, 100 g of powder A was mixed uniformly with 15 g of powder B and 1.8 g of fine powder of slaked lime to obtain powder C.

粉粒体C 1.9gを紙の内面に開孔したポリエチレンフィルムをラミネートした小袋(外寸;25mm×55mm、内寸25mm×38mm)に充填して開孔部をヒートシールし、脱酸素剤包装体を得た。
この脱酸素剤包装体を、炭酸ガス10%、酸素18.5%に調整した混合ガス280mlと共にアルミ箔ラミネート袋(120mm×150mm)に同封し、開口部をヒートシールして密閉し、保存用包装袋を得た。この包装袋を25℃環境下で保存した。
Filled a small bag (outer dimension: 25mm x 55mm, inner dimension 25mm x 38mm) with a polyethylene film laminated with 1.9g of powder C on the inner surface of the paper, heat-sealed the hole, and oxygen scavenger packaging Got the body.
This oxygen scavenger package is enclosed in an aluminum foil laminate bag (120 mm x 150 mm) with 280 ml of mixed gas adjusted to 10% carbon dioxide and 18.5% oxygen, and the opening is heat sealed and sealed, and a packaging bag for storage Got. This packaging bag was stored in a 25 ° C. environment.

保存開始時(初期)および5日後、保存用包装袋中のガス濃度をガスクロマトグラフィーにて測定した結果を表1に示した。
5日後においては、実質無酸素状態であることが確認された(実質無酸素状態とは酸素濃度0.1%以下の状態を意味する)。また、炭酸ガス吸収量を表1に記載した。
Table 1 shows the results of measuring the gas concentration in the storage packaging bag by gas chromatography at the start of storage (initial) and after 5 days.
After 5 days, it was confirmed that the substance was in a substantially oxygen-free state (the substance is in a state where the oxygen concentration is 0.1% or less). The carbon dioxide absorption is shown in Table 1.

実施例2、3
実施例1の25℃環境下に保存を5℃、40℃環境下へ保存する点を除き、実施例1と同様とした。
Examples 2 and 3
Example 1 was the same as Example 1 except that it was stored in a 25 ° C. environment at 5 ° C. and a 40 ° C. environment.

比較例1、2、3
実施例1の粉粒体に用いた珪藻土を天然ゼオライトに変更した点を除き、実施例1と同様として保存用包装袋を得た。比較例2、3も実施例2、3と同様に25℃環境下に保存を5℃、40℃環境下へ保存する点を除き、実施例1と同様とした。
Comparative Examples 1, 2, 3
A storage packaging bag was obtained in the same manner as in Example 1 except that the diatomaceous earth used in the granular material of Example 1 was changed to natural zeolite. Comparative Examples 2 and 3 were the same as Example 1 except that the samples were stored in a 25 ° C. environment in the same manner as in Examples 2 and 3 except that they were stored in a 5 ° C. and 40 ° C. environment.

5日後に保存用包装袋中のガス濃度は表1のとおりであり、本発明品は炭酸ガス吸収量が3.1〜4.2mlだったが、比較品は15.8〜17.8mlと多量の炭酸ガスを吸収していた。   After 5 days, the gas concentration in the storage packaging is as shown in Table 1. The carbon dioxide absorption of this product was 3.1 to 4.2 ml, but the comparative product absorbed 15.8 to 17.8 ml and a large amount of carbon dioxide. Was.

[表1]
実施例 比較例
1 2 3 1 2 3
保存温度 (℃) 25 5 40 25 5 40
初期混合ガス量 (ml) 280 ← ← ← ← ←
初期 酸素 (%) 18.90 18.45. 18.04 18.99 18.71 17.99
炭酸ガス (%) 9.74 10.50 9.21 10.26 10.11 10.91
酸素 (ml) 52.9 51.7 50.5 53.2 52.4 50.4
炭酸ガス (ml) 27.3 29.4 25.8 28.7 28.3 30.5
5日後 酸素濃度 (%) 0.07 0.03 0.03 0.07 0.02 0.05
炭酸ガス濃度(%) 10.67 11.22 10.00 5.68 5.01 6.90
酸素吸収量 (ml) 52.8 51.6 50.4 53.0 52.3 50.3
炭酸ガス吸収量(ml) 3.4 4.2 3.1 16.8 17.8 15.8
[Table 1]
Example Comparative Example
1 2 3 1 2 3
Storage temperature (℃) 25 5 40 25 5 40
Initial gas mixture volume (ml) 280 ← ← ← ← ←
Initial oxygen (%) 18.90 18.45. 18.04 18.99 18.71 17.99
Carbon dioxide (%) 9.74 10.50 9.21 10.26 10.11 10.91
Oxygen (ml) 52.9 51.7 50.5 53.2 52.4 50.4
Carbon dioxide (ml) 27.3 29.4 25.8 28.7 28.3 30.5
After 5 days Oxygen concentration (%) 0.07 0.03 0.03 0.07 0.02 0.05
Carbon dioxide concentration (%) 10.67 11.22 10.00 5.68 5.01 6.90
Oxygen absorption (ml) 52.8 51.6 50.4 53.0 52.3 50.3
Carbon dioxide absorption (ml) 3.4 4.2 3.1 16.8 17.8 15.8

実施例4、5
実施例1と同様の保存用包装袋を用い、実施例4では保存開始時(初期)および2日後、実施例5では保存開始時(初期)および6日後、保存用包装袋中のガス濃度をガスクロマトグラフィーにて測定した。結果を表2に示した。
Examples 4 and 5
Using the same storage packaging bag as in Example 1, in Example 4, the gas concentration in the storage packaging bag was measured at the start of storage (initial) and after 2 days, and in Example 5 at the start of storage (initial) and after 6 days. It was measured by gas chromatography. The results are shown in Table 2.

比較例4、5
実施例4、5に用いた粉粒体C1.9gを同等の酸素吸収量である鉄粉0.8gと水分供与剤0.6gの混合物に変更した点を除き、それぞれ実施例4、5と同様にした。結果を表2に示した。
Comparative Examples 4 and 5
As in Examples 4 and 5, except that the powder C1.9g used in Examples 4 and 5 was changed to a mixture of 0.8g of iron powder and 0.6g of water donating agent, which is equivalent to the amount of oxygen absorbed. did. The results are shown in Table 2.

本発明品は2日目で実質無酸素状態であったが、比較品は酸素が残留していた(実質無酸素状態とは酸素濃度0.1%以下の状態を意味する)。
また、炭酸ガス濃度においては本発明品が2日目、6日目共に5ml程度と安定していたが、比較品は26〜32mlと多量の炭酸ガスを吸収し、炭酸ガス吸収量が経時的に変化したことが確認された。
The product of the present invention was substantially oxygen-free on the second day, but oxygen remained in the comparative product (substantially oxygen-free means an oxygen concentration of 0.1% or less).
In addition, the carbon dioxide gas concentration of the present invention was stable at about 5 ml on both the second and sixth days, but the comparative product absorbs a large amount of carbon dioxide, 26-32 ml, and the amount of carbon dioxide gas absorbed over time. It was confirmed that the change was made.

[表2]
実施例 比較例
4 5 4 5
保存温度 (℃) 25 ← ← ←
初期混合ガス量 (ml) 280 ← ← ←
初期 酸素 (%) 18.07 18.07 18.06 18.06
炭酸ガス (%) 11.67 11.67 11.70 11.70
酸素 (ml) 50.6 50.6 50.6 50.6
炭酸ガス (ml) 32.7 32.7 32.8 32.8
保存後 (保存日数) 2日 6日 2日 6日
酸素濃度 (%) 0.04 0.04 5.22 0.03
炭酸ガス濃度(%) 12.43 12.43 3.05 0.25
酸素吸収量 (ml) 50.5 50.5 39.4 50.5
炭酸ガス吸収量(ml) 4.8 4.8 26.2 32.3
[Table 2]
Example Comparative Example
4 5 4 5
Storage temperature (℃) 25 ← ← ←
Initial gas mixture (ml) 280 ← ← ←
Initial oxygen (%) 18.07 18.07 18.06 18.06
Carbon dioxide (%) 11.67 11.67 11.70 11.70
Oxygen (ml) 50.6 50.6 50.6 50.6
Carbon dioxide (ml) 32.7 32.7 32.8 32.8
After saving (number of days to save) 2 days 6 days 2 days 6 days
Oxygen concentration (%) 0.04 0.04 5.22 0.03
Carbon dioxide concentration (%) 12.43 12.43 3.05 0.25
Oxygen absorption (ml) 50.5 50.5 39.4 50.5
Carbon dioxide absorption (ml) 4.8 4.8 26.2 32.3

実施例6
脱酸素剤包装体に用いた混合ガス280mlを空気250mlへ変更した点を除き、実施例1と同様とした。結果を表3に示した。
Example 6
The same as Example 1 except that the mixed gas 280 ml used for the oxygen scavenger package was changed to 250 ml of air. The results are shown in Table 3.

比較例6
実施例6に用いた粉粒体C1.9gから水分供与剤粉粒体B0.25gを除いた粉粒体を1.65gに変更した点を除き、実施例6と同様とした。
Comparative Example 6
Example 6 was the same as Example 6 except that the powder granules obtained by removing 0.25 g of the water donor powder granules B from the powder granules C 1.9 g used in Example 6 were changed to 1.65 g.

5日後、本発明品は炭酸ガス吸収量が0.1ml、炭酸ガス濃度0.0%であったが、比較例6の炭酸ガス発生量は1.9ml、炭酸ガス濃度0.9%と、水分供与剤がない場合は大気組成下で炭酸ガスを発生することが確認された。   After 5 days, the product of the present invention had a carbon dioxide absorption of 0.1 ml and a carbon dioxide concentration of 0.0%, but the amount of carbon dioxide generation in Comparative Example 6 was 1.9 ml and the carbon dioxide concentration was 0.9%, and there was no water donor. Was confirmed to generate carbon dioxide under atmospheric composition.

[表3]
実施例 比較例
6 6
保存温度 (℃) 25 25
初期混合ガス量(ml) 250 ←
初期 酸素 (%) 20.90 20.09
炭酸ガス (%) 0.03 0.03
酸素 (ml) 52.3 53.2
炭酸ガス (ml) 0.1 0.1
5日後 酸素濃度 (%) 0.02 0.03
炭酸ガス濃度(%) 0.0 0.9
酸素吸収量 (ml) 52.2 52.2
炭酸ガス吸収量(ml) 0.1 -1.9
[Table 3]
Example Comparative Example
6 6
Storage temperature (℃) 25 25
Initial gas mixture volume (ml) 250 ←
Initial oxygen (%) 20.90 20.09
Carbon dioxide (%) 0.03 0.03
Oxygen (ml) 52.3 53.2
Carbon dioxide (ml) 0.1 0.1
After 5 days Oxygen concentration (%) 0.02 0.03
Carbon dioxide concentration (%) 0.0 0.9
Oxygen absorption (ml) 52.2 52.2
Carbon dioxide absorption (ml) 0.1 -1.9

本発明により、酸素、炭酸ガス共存雰囲気下で物品を保存する際に、炭酸ガス濃度に影響を与えずに酸素を吸収させ、無酸素状態で物品を保存することが可能となった。これにより食品、健康食品、医薬品等を特定炭酸ガス濃度下、脱酸素状態で長期間保存することが可能となった。   According to the present invention, when storing an article in an atmosphere coexisting with oxygen and carbon dioxide, oxygen can be absorbed without affecting the concentration of carbon dioxide and the article can be stored in an oxygen-free state. As a result, foods, health foods, pharmaceuticals, etc. can be stored for a long time in a deoxygenated state under a specific carbon dioxide concentration.

Claims (5)

(a)不飽和脂肪酸化合物又は不飽和基を有する鎖状炭化水素重合物及び(b)触媒を(c)多孔体に含浸したもの、(d)アルカリ土類金属の水酸化物、(e)水分供与剤及び(f)脱臭剤を混合したものからなり、(a)不飽和脂肪酸化合物又は不飽和基を有する鎖状炭化水素重合物100重量部に対して、(b)触媒が0.01〜0.5重量部、(c)多孔体が50〜300重量部、(d)アルカリ土類金属の水酸化物が0.3〜10重量部、(e)水分供与剤が30〜100重量部、(f)脱臭剤が10〜100重量部である脱酸素剤。 (a) an unsaturated fatty acid compound or a chain hydrocarbon polymer having an unsaturated group and (b) a catalyst impregnated in (c) a porous body, (d) an alkaline earth metal hydroxide, (e) It consists of a mixture of a moisture donor and (f) a deodorant, and (b) catalyst is 0.01 to 0.5 to 100 parts by weight of (a) unsaturated fatty acid compound or chain hydrocarbon polymer having an unsaturated group. Parts by weight, (c) 50-300 parts by weight of porous material, (d) 0.3-10 parts by weight of alkaline earth metal hydroxide, (e) 30-100 parts by weight of moisture donor, (f) deodorizing An oxygen scavenger in which the agent is 10 to 100 parts by weight. 大気組成下での炭酸ガス発生量が1ml/g以下であり、炭酸ガス濃度10%下での炭酸ガス吸収量が5ml/g以下である請求項1記載の脱酸素剤。 The oxygen scavenger according to claim 1, wherein the amount of carbon dioxide generated under atmospheric composition is 1 ml / g or less, and the amount of carbon dioxide absorbed under a carbon dioxide concentration of 10% is 5 ml / g or less. (e)水分供与剤が、水を多孔体に含浸したものである請求項1記載の脱酸素剤。 2. The oxygen scavenger according to claim 1, wherein (e) the water donor is a porous body impregnated with water. (c)多孔体が、珪藻土である請求項1または3記載の脱酸素剤。 4. The oxygen scavenger according to claim 1 or 3, wherein the porous material is diatomaceous earth. (d)アルカリ土類金属の水酸化物が、消石灰である請求項1記載の脱酸素剤。 2. The oxygen absorber according to claim 1, wherein the alkaline earth metal hydroxide is slaked lime.
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WO2023074317A1 (en) * 2021-10-25 2023-05-04 三菱瓦斯化学株式会社 Oxygen scavenger

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