JPS5932945A - Granular deoxidizing agent - Google Patents

Granular deoxidizing agent

Info

Publication number
JPS5932945A
JPS5932945A JP14229282A JP14229282A JPS5932945A JP S5932945 A JPS5932945 A JP S5932945A JP 14229282 A JP14229282 A JP 14229282A JP 14229282 A JP14229282 A JP 14229282A JP S5932945 A JPS5932945 A JP S5932945A
Authority
JP
Japan
Prior art keywords
ascorbic acid
granular
water
deoxidizing agent
alkali metal
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
Application number
JP14229282A
Other languages
Japanese (ja)
Other versions
JPS625010B2 (en
Inventor
Hideyuki Takahashi
秀之 高橋
Toshio Komatsu
小松 俊夫
Yoshiaki Inoue
井上 義彰
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Gas Chemical Co Inc
Original Assignee
Mitsubishi Gas Chemical Co Inc
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Mitsubishi Gas Chemical Co Inc filed Critical Mitsubishi Gas Chemical Co Inc
Priority to JP14229282A priority Critical patent/JPS5932945A/en
Priority to US06/521,167 priority patent/US4524015A/en
Publication of JPS5932945A publication Critical patent/JPS5932945A/en
Publication of JPS625010B2 publication Critical patent/JPS625010B2/ja
Granted legal-status Critical Current

Links

Abstract

PURPOSE:To provide a granular deoxidizing agent good in flowability and capable of being filled and packed continuously and automatically for a long time, obtained by coating a deoxidizing agent containing ascorbic acid, alkali metal carbonate, an iron compound, carbon black and water with a fine powder. CONSTITUTION:A deoxidizing agent obtained by mixing about 10-500pts.wt. alkali metal carbonate, about 1-200pts.wt. iron compound, 10-500pts.wt. carbon black and a proper amount of water in 100pts.wt. ascorbic acid and/or a salt thereof is coated with a fine powder with a particle size of about 100 mesh or less comprising, for example, activated carbon or gypsum to be formed into a granular shape. As ascorbic acid, L-ascorbic acid is used and, as alkali metal carbonate, Na2CO3 is used while, as the iron compound, FeCl2 or FeC>3 is used and, as carbon black, any carbon blac can be used. The particle size thereof is about 100 mesh or less and water is added after other components are mixed therein.

Description

【発明の詳細な説明】 本発明は粒状脱酸素剤に関する。更に詳しくはアスコル
ビン酸および/またはその塩、アルカリ金属の炭酸塩、
鉄化合物、カーボンブラックおよび水を含有する脱酸素
剤を微細フィラーで被覆してなることを特徴とする粒状
脱酸素剤に関する発明である。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to particulate oxygen scavengers. More specifically, ascorbic acid and/or its salts, alkali metal carbonates,
This invention relates to a granular oxygen absorber characterized in that the oxygen absorber containing an iron compound, carbon black, and water is coated with a fine filler.

近年、食品のカビ防止、酸化防止、変色防止等を目的と
する脱酸素剤として鉄系のもの、またはアスコルビン酸
類な用いたもの等各棟の脱酸素剤が知られている。
In recent years, various types of oxygen absorbers, such as iron-based ones or those using ascorbic acids, have become known as oxygen absorbers for the purpose of preventing mold, oxidation, and discoloration of foods.

従来の7スコルビン酸類を用いた脱酸素剤はアスコルビ
ン酸類と共に炭酸アルカリまたは水酸化アルカリ、鉄化
合物、水および活)ニド炭等の充填剤を含有するもので
あった。
Conventional oxygen scavengers using 7 scorbic acids contain fillers such as alkali carbonates or alkali hydroxides, iron compounds, water, and active carbon charcoal, along with ascorbic acids.

しかし従来の7スコルビン酸系の脱r1タ素即ロ↓流動
性が悪く、実用上、次の様な欠点があった0脱酸素剤は
酸素吸収組成物を通気(’lの包材に充填包装し、これ
を食品と共に密封系内に封入して用いるが、酸素吸収組
成物を通気性包材に光3fi包装するためにはダイロー
ル方式や)(−シール)5式の自動光」A包装機が用い
られ℃いる。しかし自H1jノ包装の場合は脱酸素剤が
粉体としての流動性カーよくないと、自動包装の際に、
正確な計量を行なうことが困難であり、しかも包装材料
をシールしたf!5分に酸素吸収組成物が一諸にシール
される欠点力tあった0 この様な欠点を改良する為に、上d己組a !l勿をI
n粒化する試みもあるが、活性炭等σ〕充填斉1jをJ
fl 1.・る為、大量のバインダーを用(・なけれ(
1n粒イヒできす、大量のバインダーを用(・ると酸*
の吸1区力を阻害される欠点があった。
However, the conventional 7-scorbic acid-based deoxidizers have poor fluidity and have the following drawbacks in practical use. This is used by sealing it in a sealed system with food, but in order to package the oxygen-absorbing composition in a breathable packaging material, a die-roll method or ) (-Seal) Type 5 automatic light "A packaging" is used. The machine is used at ℃. However, in the case of self-packaging, the flowability of the oxygen absorber as a powder is not good, so during automatic packaging,
It is difficult to measure accurately and the packaging material is sealed. There was a drawback that the oxygen-absorbing composition was sealed all together in 5 minutes.In order to improve this drawback, the upper management group a! l of course
There are attempts to reduce the particle size to n particles, but if activated carbon, etc.
fl 1.・To avoid this, a large amount of binder is required.
If you use 1n grains, you can use a large amount of binder.
There was a drawback that the suction force was inhibited.

発明者等は、以上の様な欠点を改良するために椙々の研
究を行なった結果、充填剤としてカーボンブラックを用
いる事により容易に自動充填包装が可能な流動性の良い
顆粒状の脱酸素剤を製造することが可能なことを見出し
た。
As a result of extensive research to improve the above-mentioned drawbacks, the inventors have developed a granular deoxidizer with good fluidity that can be easily filled and packaged automatically by using carbon black as a filler. It has been found that it is possible to produce a drug.

しかしながら、高速自動充填包装機を用いて、上記原末
を連続充填する場合、1〜2時間程度の短時間であれば
問題なく製造出来るが、更に長時間原末が空気にふれる
と時間経過と共に原末が反応して発熱−1湿潤した顆粒
となって包装機への原末付着が増加し絶境不可能となる
欠点があった。
However, when continuously filling the above bulk powder using a high-speed automatic filling and packaging machine, it can be manufactured for a short time of about 1 to 2 hours without any problems, but if the bulk powder is exposed to air for a longer period of time, it will gradually change over time. There was a drawback that the bulk powder reacted and became moist granules that generated heat and increased adhesion of the bulk powder to the packaging machine, making it impossible to do so.

本発明者等はこれらの欠点を改良するため更に、研究を
進めた結果アスコルビン酸および/またはその塩、アル
カリ金属の炭酸塩、鉄化合物、カーボンブラックおよび
水を含右する脱酸素^りを水に難溶性の微粉末で被覆す
ることによって、容易に長時間連続自動充填包装が可能
な流動性の良い粒状の脱酸素剤を作ることによって本発
明を完成するに至った。
In order to improve these shortcomings, the present inventors further conducted research and found that ascorbic acid and/or its salts, carbonates of alkali metals, iron compounds, carbon black, and deoxidizing agents containing water were used as deoxidizers containing ascorbic acid and/or its salts. The present invention was completed by creating a granular oxygen scavenger with good fluidity that can be easily and continuously filled and packaged automatically over a long period of time by coating it with a poorly soluble fine powder.

は七の塩としてはL−7スフルビン腟、L−7ス   
1本発明におい壬、7スコルビノ酸および/まだコルビ
ン酸ナトリウムまたはa−−−iso−アスコル   
□ビン酸ナトリウム等単独あイ)いはこれらの混合物が
用いられる。
The seven salts are L-7 sfulvin vaginalis, L-7 sulfur
1. According to the present invention, 7. Scorbino acid and/or sodium corbate or a---iso-ascol.
□ Sodium birate etc. alone or a mixture of these can be used.

アルカリ金属の炭酸塩としてはNa、CO3、NaHC
U、。
Alkali metal carbonates include Na, CO3, and NaHC.
U.

8、。o3f ?、、 1−1− KH9゜3ニア、I
I 1,161.4.71、Ch ”i (’)   
1塩は単独または混合物が用いられる。
8. o3f? ,, 1-1- KH9゜3 Near, I
I 1,161.4.71, Ch ”i (')
1 Salts may be used alone or in mixtures.

アルカリ金属の炭酸塩のhiはアスコルビン酸および/
またはその塩100重)、1部にzjシて一般的に  
 □は10〜500重損部であり、好ましくは30〜 
 1250ThjJi部である。          
      しなお、本発明において、アルカリ金属の
炭酸塩   :としCNaHCO3またはKHCO3を
用いた場合、またはNa2CO3またはに、 CO,で
あってもRLが少い場合には、本発明の脱酸素剤はO7
の吸収と共にCO,を発生する。
hi of alkali metal carbonates is ascorbic acid and/or
or its salt (100 parts), 1 part is commonly used
□ is 10 to 500 severely damaged parts, preferably 30 to 500
1250ThjJi part.
However, in the present invention, when alkali metal carbonate: CNaHCO3 or KHCO3 is used, or when RL is small even if Na2CO3 or CO, the oxygen scavenger of the present invention is O7.
As CO is absorbed, CO is generated.

本発明におい壬、鉄化合物としては第−鉄基および第二
鉄塩はともに好適に用いられる。具体的にはFeCl2
 、 FeC1,、Fe50.  またはFez (8
04)3    :。
In the present invention, both ferrous groups and ferric salts are preferably used as iron compounds. Specifically, FeCl2
, FeC1,, Fe50. or Fez (8
04)3:.

および結晶水を有する塩が用いられるが、これらの中で
結晶水を有する塩が特に好ましい。
and salts having water of crystallization are used, among which salts having water of crystallization are particularly preferred.

鉄化合物の犠はアスコルビン酸および/またはまた、カ
ーボンシラツクとしてはゴム用、カラー用または電池用
等いずれのカーボンブラックをも用いることが可能であ
る。
As the iron compound, ascorbic acid and/or as the carbon black, any carbon black for rubber, color or battery use can be used.

カーボンシラツクのlはアスコルビン酸および/または
七Ω塩100重漬部に対し一般的には10〜500 i
ff、’−111部であり、好ましくは50〜200@
量部である。
Generally, l of carbon silicon is 10 to 500 l per 100 parts soaked in ascorbic acid and/or 7Ω salt.
ff, '-111 parts, preferably 50 to 200@
It is a quantity part.

なおり−ボンブランクの粒子の大きさは1001ノシ二
以下のものが好ましい。
The particle size of the Naori-bon blank is preferably 1001 noshi2 or less.

本発明において脱酸素剤を被値するための微粉末として
は粒度が100メソシユ以下の水に離溶性の微粉末、例
えば活性炭、石膏、炭酸カルシウム、ゼオライト、パー
ライト、シリカ微粉末または酸化鉄等が用いられる。
In the present invention, as the fine powder for applying the oxygen scavenger, water-soluble fine powder having a particle size of 100 mesosinus or less, such as activated carbon, gypsum, calcium carbonate, zeolite, perlite, fine silica powder, or iron oxide, is used. It will be done.

本発明において被覆とは、粒状もしくは顆粒状物と微粉
末とな混合しまぶすことを示し、披偵後   □□ の顆粒に付着した微粉末が全面付7・l、か、部分重付
   1着か等でノリ、定されるものではない。
In the present invention, coating refers to sprinkling of granules or a mixture of granules and fine powder. It is not something that is determined by these things.

本発明において、微粉末を19)澹すイ)t”+ilの
粒状の脱酸素剤を製造するには、一般的には混紳潰粒1
.贋、押出造粒1幾、流動層造粒4μ、転ipH+青粒
機、:i;、 It’造□ 粒1幾または解砕造粒機が用いられるが、これらの中で
押出造粒ぜトまたは転lvb造粒(練が好ましい。また
この、用台の各成分の配合方法は特に限冒されるもので
はないが、水は他成分をilL合板iC1173合する
こと、または鉄化合物をあらかじめ水に1611+イし
た   1後に添加することが好ましい。
In the present invention, in order to produce a granular oxygen absorber with a fine powder of 19) t"+il, generally mixed crushed granules 1
.. False, extrusion granulation 1 size, fluidized bed granulation 4 μ, transfer ipH + blue granulation machine, :i;, It' granulation 1 size or crushing granulator are used, but among these, extrusion granulation Granulation or rolling lvb granulation (kneading is preferred.Also, there are no particular restrictions on the method of blending each component in this table, but for water, other components may be combined with ILL plywood iC1173, or iron compounds may be mixed in advance. It is preferably added after 1611+ hours in water.

なお本発明に1+5いて、粒状の脱・′伎素剤は+1t
なる粒状のものだけでなく、顆粒状の説請諮剤なも格味
する。
In addition, the present invention has 1+5, and the granular de-removal agent has +1 t.
Not only the granular ones, but also the granular ones are great.

本発明において微粉末を粒状の脱・−P素剤に破積する
方法としては一般的には18字ブレンター、   □v
字ブレンダー、ナウターミキ・ター、コーチイン   
1グバン、コンクリートミキサー等に粒状物を入れ粒粉
末を添IJD混合してiするl、Rな方法メ1tとらt
t    lるが好ましくはコーティングパン、コンク
リートミキザー等で破Ijシする様な方法でありまた、
転動造粒機等に微粉末を添加し被覆する様な方法も好ま
しい。
In the present invention, the method for stacking fine powder into granular de-P base material is generally carried out using an 18-character blender, □v
Aji blender, nauta miki ta, coachin
1.Put the granules in a concrete mixer, etc., add the granular powder, and mix.
However, it is preferable to use a method such as breaking with a coating pan, concrete mixer, etc.
A method in which fine powder is added to a rolling granulator or the like and coated is also preferred.

以下実施例により更に詳しく説明する。This will be explained in more detail below with reference to Examples.

実施例 アスコルビン酸ナトリウム  1(lHjtitf15
カーボンブラック      1O Na、Co、             5NaHC0
312 硫酸第一鉄プ水塩       2 から成る組成物をコニーダーで5分間混合後、水6重量
部を添加し更に5分間混練した。
Example Sodium Ascorbate 1 (lHjtitf15
Carbon black 1O Na, Co, 5NaHC0
After mixing the composition consisting of 312 ferrous sulfate salt 2 for 5 minutes in a co-kneader, 6 parts by weight of water was added and kneaded for an additional 5 minutes.

混練後、円筒式押出し造粒機(網目の径z%)を用い顆
粒状脱酸素剤組成物を得た。
After kneading, a granular oxygen scavenger composition was obtained using a cylindrical extrusion granulator (mesh diameter: z%).

上記顆粒をコーティングパンに入れ、シリカ微粉末を顆
粒Zoo重員部に対し5重曾部晧加、5分間被覆し、流
動性良好な脱酸素組成物を得た。
The above-mentioned granules were placed in a coating pan, and the silica fine powder was coated on the weight part of the granules for 5 minutes to obtain a deoxidizing composition with good fluidity.

これを自動充填包装機を用い、開孔ポリエチレンを純白
紙にラミネートした通気性包材で連続充填を行なったと
ころイOJら間i・117エく充」」“1可能でまンっ
だ。
When this was continuously filled using an automatic filling and packaging machine with a breathable packaging material made of open-pore polyethylene laminated to pure white paper, the result was 117 times.

上記組成物5gを充填した脱r俊素剤を空気250−と
共に、塩化ビニリデンツー1ポリエチレン製の袋に封入
し、1日後に袋内の酸素a度を分析した結果、0.1チ
以下であり、炭酸カスのTa IIは22.1%であっ
た。
A desaturation agent filled with 5 g of the above composition was sealed in a vinylidene chloride-1 polyethylene bag with 250 g of air, and after one day, the oxygen a degree in the bag was analyzed and found to be less than 0.1 g. The Ta II of the carbonate residue was 22.1%.

特許出願人 三菱瓦斯化学株式会社 代表者 J之 野 和 吉Patent applicant: Mitsubishi Gas Chemical Co., Ltd. Representative: Kazukichi Nono

Claims (1)

【特許請求の範囲】[Claims] アスコルビン酸および/またはその塩アルカリ金属の炭
酸塩、鉄化合物、カーボン7゛ラツクおよび水を含有す
る脱酸素剤を微粉末で被覆してなることを特徴とする粒
状脱酸素剤。
A granular oxygen absorber comprising an oxygen absorber containing ascorbic acid and/or its salt alkali metal carbonate, an iron compound, carbon chloride, and water, coated with fine powder.
JP14229282A 1982-08-09 1982-08-17 Granular deoxidizing agent Granted JPS5932945A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP14229282A JPS5932945A (en) 1982-08-17 1982-08-17 Granular deoxidizing agent
US06/521,167 US4524015A (en) 1982-08-09 1983-08-05 Oxygen absorbent

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14229282A JPS5932945A (en) 1982-08-17 1982-08-17 Granular deoxidizing agent

Publications (2)

Publication Number Publication Date
JPS5932945A true JPS5932945A (en) 1984-02-22
JPS625010B2 JPS625010B2 (en) 1987-02-03

Family

ID=15311983

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14229282A Granted JPS5932945A (en) 1982-08-09 1982-08-17 Granular deoxidizing agent

Country Status (1)

Country Link
JP (1) JPS5932945A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0371702A2 (en) * 1988-11-30 1990-06-06 Pfizer Inc. Oxygen removal with carbon catalyzed erythorbate or ascorbate
JPH0480869U (en) * 1990-11-22 1992-07-14
JPH04215842A (en) * 1990-05-16 1992-08-06 Ueno Seiyaku Oyo Kenkyusho:Kk Oxygen absorbent
JP2017225953A (en) * 2016-06-24 2017-12-28 凸版印刷株式会社 Oxygen scavenger and manufacturing method thereof

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS53140292A (en) * 1977-05-02 1978-12-07 Toyo Ink Mfg Co Ltd Oxygen absorbent composition
JPS54132246A (en) * 1978-04-04 1979-10-15 Toppan Printing Co Ltd Freshness preserving agent
JPS56133027A (en) * 1980-03-21 1981-10-17 Mitsubishi Gas Chem Co Inc Deoxidizer and preservation of coffee by using the same

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS53140292A (en) * 1977-05-02 1978-12-07 Toyo Ink Mfg Co Ltd Oxygen absorbent composition
JPS54132246A (en) * 1978-04-04 1979-10-15 Toppan Printing Co Ltd Freshness preserving agent
JPS56133027A (en) * 1980-03-21 1981-10-17 Mitsubishi Gas Chem Co Inc Deoxidizer and preservation of coffee by using the same

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0371702A2 (en) * 1988-11-30 1990-06-06 Pfizer Inc. Oxygen removal with carbon catalyzed erythorbate or ascorbate
JPH04215842A (en) * 1990-05-16 1992-08-06 Ueno Seiyaku Oyo Kenkyusho:Kk Oxygen absorbent
JPH0480869U (en) * 1990-11-22 1992-07-14
JP2017225953A (en) * 2016-06-24 2017-12-28 凸版印刷株式会社 Oxygen scavenger and manufacturing method thereof

Also Published As

Publication number Publication date
JPS625010B2 (en) 1987-02-03

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