JPS59232078A - Production of granular agent to preserve freshness - Google Patents

Production of granular agent to preserve freshness

Info

Publication number
JPS59232078A
JPS59232078A JP8820383A JP8820383A JPS59232078A JP S59232078 A JPS59232078 A JP S59232078A JP 8820383 A JP8820383 A JP 8820383A JP 8820383 A JP8820383 A JP 8820383A JP S59232078 A JPS59232078 A JP S59232078A
Authority
JP
Japan
Prior art keywords
alkali
hydroxide
salt
granulation
carbonate
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
JP8820383A
Other languages
Japanese (ja)
Other versions
JPH0321148B2 (en
Inventor
Kiyotaka Omote
清隆 表
Ryukichi Matsuo
龍吉 松尾
Kenji Saishiyo
最所 研次
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.)
Toppan Inc
Original Assignee
Toppan Printing Co Ltd
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 Toppan Printing Co Ltd filed Critical Toppan Printing Co Ltd
Priority to JP8820383A priority Critical patent/JPS59232078A/en
Publication of JPS59232078A publication Critical patent/JPS59232078A/en
Publication of JPH0321148B2 publication Critical patent/JPH0321148B2/ja
Granted legal-status Critical Current

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  • Food Preservation Except Freezing, Refrigeration, And Drying (AREA)

Abstract

PURPOSE:To obtain the titled agent granulated uniformly and surely, and resistant to the secondary agglomeration, by mixing an L-ascorbic acid compound, an alkali hydroxide and an alkali carbonate at least one of which is hydrated salt, a ferrous salt, and a porous substance for a definite time interval, and granulating the mixture. CONSTITUTION:(A) An L-ascorbic acid compound, (B) two or more alkaline compounds composed of an alkali metal or alkaline earth metal hydroxide or an alkali metal or alkaline earth metal (bi)carbonate at least one of which is a hydrated salt, (C) a ferrous salt, and (D) a porous substance (e.g. a substance having uniform fine pores, e.g. activated carbon, zeolite, activated alumina, etc.) are mixed with each other for a definite time interval, and granulated with a granulator. The water of crystal existing in the hydrated salt of the alkaline compound is isolated by the heat of mixing and dispersed among the powdery mixture to effect the uniform moistening of the composition. Consequently, the granulation can be carried out without using a binder, and solid granules can be obtained.

Description

【発明の詳細な説明】 本発明は食品等と共に包装体内に封入し、包装体内の酸
素を吸収し、食品を長期保存可能にする鮮度保持剤で、
顆粒状の鮮度保持剤の製造方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention is a freshness-preserving agent that is enclosed in a package together with food, etc., absorbs oxygen in the package, and enables food to be stored for a long time.
The present invention relates to a method for producing a granular freshness-preserving agent.

食品類の品質の劣化は、殆んどが酸素が関与しており、
それを改善するため従来から真空包装、ガス置換包装方
法とがとられてきた。
Oxygen is responsible for most of the deterioration in food quality.
In order to improve this problem, vacuum packaging and gas exchange packaging methods have been used.

そして近年食品類と共に酸素を吸収する脱酸素剤を包装
体内に封入する包装方法がとられつつある。
In recent years, a packaging method has been adopted in which an oxygen absorber that absorbs oxygen is enclosed in the package together with foods.

この脱酸素剤は、酸素の吸収速度を高めるため、各成分
は微粉末化されているため、この脱酸素剤を通気性材料
からなる袋に充填する際、計量誤差、粉末の舞い上がり
が生じ、高速充填が不可能であった。そこで従来におい
ても造粒加工を行々うことが行なわれており、その工程
は、まず各成分を一定量ずつ均一に混合し、この混合し
たものに水を加え加湿後、押出し造粒様により行なって
いた。
In order to increase the oxygen absorption rate, each component of this oxygen absorber is finely powdered, so when filling this oxygen absorber into a bag made of breathable material, measurement errors and powder flying up may occur. High-speed filling was not possible. Therefore, in the past, granulation processing has been carried out, and the process involves first uniformly mixing a certain amount of each component, then adding water to the mixture, humidifying it, and then extruding it into granules. I was doing it.

しかしながら上記の工程で製造された顆粒は、加湿時の
水分の均一分散が困難で、水分の少ない部分は、造粒さ
れず、また水分が多い場合は、顆粒は柔かく、多少の圧
力により2次疑集をおこしてしまい均一粒径の顆粒が得
られないばかりか、表面積が低下して反応速度の低下を
きたしてしまっていた。
However, in the granules produced by the above process, it is difficult to uniformly disperse the moisture during humidification, and areas with low moisture are not granulated, and if there is a lot of moisture, the granules are soft and become secondary due to some pressure. Not only does this cause agglomeration, making it impossible to obtain granules of uniform particle size, but the surface area decreases, resulting in a decrease in the reaction rate.

本発明は、これらの欠点を解消し、顆粒状にしても2次
疑集のおこらない顆粒状の鮮度保持剤の製造方法である
The present invention is a method for producing a granular freshness-preserving agent that eliminates these drawbacks and does not cause secondary condensation even when it is made into granules.

以下本発明について詳細に説明する。The present invention will be explained in detail below.

本発明で製造する鮮度保持剤の成分は、L−アスコルビ
ン酸、L−アスコルビン酸異性体、またはこれらの塩か
らなるL−アスコルビン酸系化合物、少なくとも1つが
含水塩である水酸化アルカリまたは炭酸アルカリからな
る2種以上のアルカリ性化合物、第一鉄塩および多孔質
物質からなる。
The components of the freshness-preserving agent produced in the present invention are L-ascorbic acid, L-ascorbic acid isomers, or L-ascorbic acid-based compounds consisting of salts thereof, and alkali hydroxide or alkali carbonate in which at least one is a hydrated salt. consisting of two or more alkaline compounds, a ferrous salt, and a porous substance.

L−アメコルビン酸系化合物は、L−アスコルビン酸、
D −i 5cy−アスコルビン酸またはこれらのナト
リウム塩が適当である。
L-amecorbic acid compounds include L-ascorbic acid,
D-i 5cy-ascorbic acid or their sodium salts are suitable.

またアルカリ性化合物で水酸化アルカリは、アルカリ金
属またはアルカリ土類金属の水酸化物であり具体的には
、水酸化リチウム、水酸化ナトリウム、水酸化カリウム
、水酸化ルビジウム、水酸化セシウム、水酸化ベリラム
、水酸化マグネシウム、水酸化カルシウム、水酸化スト
ロンチウム、水酸化ラジウムであり、一方炭酸アルカリ
は、炭、   @lJf′)”・1+“″”・1”″″
・炭酸マグネシウム、炭酸カリウム、炭酸水素カリウム
、炭酸水素ナトリウム、炭酸水素リチウムのアルカリ金
属またはアルカリ土類金属の炭酸塩、炭酸水素塩または
これらの含水塩である。
Alkali hydroxides are alkaline metal or alkaline earth metal hydroxides, specifically lithium hydroxide, sodium hydroxide, potassium hydroxide, rubidium hydroxide, cesium hydroxide, berylum hydroxide. , magnesium hydroxide, calcium hydroxide, strontium hydroxide, and radium hydroxide, while alkali carbonate is charcoal, @lJf′)”・1+“″”・1”″″
・Alkali metal or alkaline earth metal carbonates, hydrogen carbonates, or hydrated salts thereof, such as magnesium carbonate, potassium carbonate, potassium hydrogen carbonate, sodium hydrogen carbonate, and lithium hydrogen carbonate.

第一鉄塩は、硫酸第一鉄、塩化第一鉄、水酸化第一鉄、
炭酸第一鉄の第一鉄の無水塩または含水塩である。
Ferrous salts include ferrous sulfate, ferrous chloride, ferrous hydroxide,
Ferrous carbonate is an anhydrous or hydrated salt of ferrous iron.

多孔質物質は、活性炭、ゼオライト、ベントナイト、活
性アルミナ、活性白土のように均一な細孔を有する物質
である。
Porous materials are materials with uniform pores, such as activated carbon, zeolite, bentonite, activated alumina, and activated clay.

上記成分の大きさで、硫酸第一鉄・7水塩は、10メツ
シー以上、アルカリ性化合物は、粉末または10メツシ
ュ以上、その他の成分は80メツシュ以上細かい粉末状
である。
Regarding the size of the above components, ferrous sulfate heptahydrate is in the form of a fine powder of 10 mesh or more, the alkaline compound is a powder or 10 mesh or more, and the other components are in the form of a fine powder of 80 mesh or more.

上記成分の具体的−例は、下記のとおりである。Specific examples of the above components are as follows.

前記具体的成分の鮮度保持剤に基づいて製造方法につい
て説明する。
The manufacturing method will be explained based on the freshness preserving agent as the specific ingredient.

前記各成分を同時に密封可能な混合器中で十分に混合し
た後、押出し造粒する顆粒状鮮度保持剤の製造方法であ
る。
This is a method for producing a granular freshness-preserving agent, in which the above-mentioned components are sufficiently mixed together in a sealable mixer, and then extruded and granulated.

本発明においては、混合中に炭酸ナトリウム、10水塩
等の含水塩からなるアルカリ性化合物が混合時の熱によ
り結晶水が遊離し、混合粉体中に分散し、鮮度保持剤全
体に均一に湿気を付与することができ、造粒が確実にか
つ均一に行なうことができる。
In the present invention, water of crystallization is liberated from an alkaline compound consisting of hydrated salts such as sodium carbonate and decahydrate during mixing due to the heat during mixing, and is dispersed in the mixed powder, distributing moisture evenly throughout the freshness-preserving agent. can be applied, and granulation can be performed reliably and uniformly.

この含水塩からなるアルカリ性化合物の量は、全体の2
0〜80重量%の範囲が好ましく、20重量%以下であ
ると造粒が行なわれず、粉末状態のままで、また80重
量%以上であると造粒時に糸状となってしまい好ましく
ない。
The amount of alkaline compound consisting of this hydrated salt is 2
The range of 0 to 80% by weight is preferable, and if it is less than 20% by weight, granulation will not take place and it will remain in a powder state, and if it is more than 80% by weight, it will become filamentous during granulation, which is not preferable.

またこの含水塩からなるアルカリ性化合物は、造粒のみ
ならず酸素吸収反応を促進する働きもする。
Moreover, this alkaline compound consisting of a hydrous salt functions not only to granulate but also to promote oxygen absorption reaction.

ここで本発明の成分を一度に混合しても、鮮度保持剤に
湿気は与えられず造粒は不可能であった。
Even if the components of the present invention were mixed at once, moisture was not imparted to the freshness-preserving agent, making granulation impossible.

このようにして得られた顆粒状の鮮度保持剤は、顆粒が
硬く、多少の圧力下においても2次疑集をおこさず、従
来の粉末状のものと比較して、表面積が小さくなるが酸
素吸収能力の低下はなかった。
The granular freshness-preserving agent obtained in this way has hard granules, does not cause secondary aggregation even under some pressure, and has a smaller surface area compared to conventional powder, but is free from oxygen. There was no decrease in absorption capacity.

また粒径分布が狭く、充填時の計量誤差が極めて小さい
範囲で行なうことができる。
In addition, the particle size distribution is narrow, and filling can be carried out within an extremely small range of measurement errors.

さらに、本発明の製造方法によれば、従来のように造粒
時にアラビアゴム、ポリビニルアルコール、アルギン酸
ンーダー、グリセリン、ゼラチン等の結合剤を用いなく
とも、造粒可能で、前述のように硬い顆粒が得られた。
Furthermore, according to the production method of the present invention, granulation is possible without using binders such as gum arabic, polyvinyl alcohol, alginate underlayer, glycerin, gelatin, etc. during granulation as in the past, and hard granules can be obtained as described above. was gotten.

本発明において使用する混合機は、密封構造を有するも
のであればよく、同筒型、■型等の容器回転型混合機及
びリボン型、水平スクリュー型、パドル型、遊星運動型
等の容器固定型混合機の使用が可能である。
The mixer used in the present invention may be one having a sealed structure, such as a container rotating type mixer such as a cylindrical type or a type, or a container fixed type mixer such as a ribbon type, horizontal screw type, paddle type, or planetary motion type. It is possible to use a mold mixer.

また造粒は、短時間で行なうことができる押出し造粒方
法が適当である。
Furthermore, extrusion granulation is suitable for granulation because it can be carried out in a short time.

この押出し造粒方法は、スクリュー回転の円滑性及びス
クリーンからの吐出性を保有するため、被造粒物は、粘
性のあるものまたは湿気を有するものにかぎられていた
が、本発明においては薬剤に含む結晶水を利用するため
このように粉体のままで、その他の湿気を付与するため
の助剤を添加するととなく造粒可能であった。
In this extrusion granulation method, the material to be granulated has been limited to viscous or moist materials in order to ensure smooth screw rotation and ejectability from the screen. Since the water of crystallization contained in the powder is used, it is possible to granulate the powder as it is by adding other auxiliary agents for imparting moisture.

さらに造粒において使用される孔径ば、得ようとする粒
径によって異なるが、08〜2.8 mnφ及びスクリ
ーン開孔率は、20〜40%の範囲が適当である。
Further, the pore size used in granulation varies depending on the particle size to be obtained, but the appropriate range is 08 to 2.8 mnφ and the screen porosity is 20 to 40%.

次に本発明の実施例について説明する。Next, examples of the present invention will be described.

〈実施例1〉 下記表の配合の薬剤をそれぞれ3 kgずつ、空容積2
0石、回転速度30回/分のV型混合機で60分間、2
0〜25°Cの条件下で密封状態で混合した。この混合
した薬剤をスクリーン孔径1.5配φ、開孔率225%
のスクリーンを設けた押出し造粒j、  機により造粒
した結果、64の配合の薬剤は、顆粒状の鮮度保持剤が
得られ、3ば、一部粉末が混入した顆粒が、6は、一部
系状のものが混入した顆粒が得られた。
<Example 1> 3 kg of each drug with the formulation shown in the table below, 2 empty volumes
0 stone, 60 minutes with a V-type mixer at a rotation speed of 30 times/min, 2
The mixture was mixed in a sealed state at a temperature of 0 to 25°C. This mixed chemical was applied to the screen with a hole diameter of 1.5 mm and an opening rate of 225%.
As a result of granulation using an extrusion granulation machine equipped with a screen of Granules containing particulate matter were obtained.

しかし、1,2は、湿気が不足し、造粒が刀能であった
However, in Nos. 1 and 2, the moisture was insufficient and the granulation was poor.

また7の配合の薬剤は、湿気に十分であったが、造粒時
にスクリーンから糸状に押出され、顆粒状の鮮度保持剤
は得られなかった。
In addition, although the chemical in the formulation No. 7 had sufficient moisture, it was extruded into threads from the screen during granulation, and a granular freshness-preserving agent could not be obtained.

そして顆粒状と々った6、4の鮮度保持剤の粒度分布は
、表2の通りであった。
The particle size distribution of the granular freshness-preserving agents 6 and 4 was as shown in Table 2.

表1 上記表1の数値はいずれも重量部を示す。Table 1 All numerical values in Table 1 above indicate parts by weight.

7− 表2 〈実施例2〉 実゛施例1の表1に示した1〜7の薬剤を実施例1で用
いた混合機20〜25℃の条件下で5分間混合後、さら
に全体を40℃に加温し、30分放置後、実施例1と同
じ造粒機により造粒を行なった。
7- Table 2 <Example 2> After mixing the drugs 1 to 7 shown in Table 1 of Example 1 in the mixer used in Example 1 for 5 minutes at 20 to 25°C, the whole was further mixed. After heating to 40° C. and leaving for 30 minutes, granulation was performed using the same granulator as in Example 1.

この結果3〜6の薬剤は、実施例1と同様造粒されたが
、1,2および7の薬剤は造粒不可能であった。
As a result, drugs 3 to 6 were granulated in the same manner as in Example 1, but drugs 1, 2, and 7 could not be granulated.

特許出願人 凸版印刷株式会社 代表者鈴木和夫 8−patent applicant Toppan Printing Co., Ltd. Representative Kazuo Suzuki 8-

Claims (1)

【特許請求の範囲】[Claims] (1)L−アスコルビン酸系化合物、少なくとも1つが
含水塩である水酸化アルカリまたは炭酸アルカリからな
る少々くとも2種以上のアルカリ性化合物、第一鉄塩お
よび多孔質物質からなる薬剤を一定時間混合した後、造
粒機により造粒する顆粒状鮮度保持剤の製造方法。
(1) A drug consisting of an L-ascorbic acid compound, at least two or more alkaline compounds consisting of an alkali hydroxide or alkali carbonate, at least one of which is a hydrated salt, a ferrous salt, and a porous substance is mixed for a certain period of time. A method for producing a granular freshness-preserving agent, which is then granulated using a granulator.
JP8820383A 1983-05-19 1983-05-19 Production of granular agent to preserve freshness Granted JPS59232078A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8820383A JPS59232078A (en) 1983-05-19 1983-05-19 Production of granular agent to preserve freshness

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8820383A JPS59232078A (en) 1983-05-19 1983-05-19 Production of granular agent to preserve freshness

Publications (2)

Publication Number Publication Date
JPS59232078A true JPS59232078A (en) 1984-12-26
JPH0321148B2 JPH0321148B2 (en) 1991-03-22

Family

ID=13936338

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8820383A Granted JPS59232078A (en) 1983-05-19 1983-05-19 Production of granular agent to preserve freshness

Country Status (1)

Country Link
JP (1) JPS59232078A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61260198A (en) * 1985-05-14 1986-11-18 株式会社新来島どっく Hydrothermal solidifying treating method of inorganic group waste
JPS61293375A (en) * 1985-06-21 1986-12-24 Nippon Chem Ind Co Ltd:The Freshness preservative
WO2007046449A1 (en) * 2005-10-21 2007-04-26 Mitsubishi Gas Chemical Company, Inc. Solid oxygen scavenger composition and process for producing the same
JP2008264665A (en) * 2007-04-19 2008-11-06 Mitsubishi Gas Chem Co Inc Method for manufacturing deoxidizer composition

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5682831B2 (en) * 2009-11-24 2015-03-11 三菱瓦斯化学株式会社 Atmospheric conditioner composition

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61260198A (en) * 1985-05-14 1986-11-18 株式会社新来島どっく Hydrothermal solidifying treating method of inorganic group waste
JPS61293375A (en) * 1985-06-21 1986-12-24 Nippon Chem Ind Co Ltd:The Freshness preservative
JPH043191B2 (en) * 1985-06-21 1992-01-22
WO2007046449A1 (en) * 2005-10-21 2007-04-26 Mitsubishi Gas Chemical Company, Inc. Solid oxygen scavenger composition and process for producing the same
US8017033B2 (en) 2005-10-21 2011-09-13 Mitsubishi Gas Chemical Company, Inc. Solid oxygen scavenger composition and process for producing the same
US8168079B2 (en) 2005-10-21 2012-05-01 Mitsubishi Gas Chemical Company, Inc. Solid oxygen scavenger composition and process for producing the same
JP5413790B2 (en) * 2005-10-21 2014-02-12 三菱瓦斯化学株式会社 Solid oxygen scavenger composition and method for producing the same
JP2008264665A (en) * 2007-04-19 2008-11-06 Mitsubishi Gas Chem Co Inc Method for manufacturing deoxidizer composition

Also Published As

Publication number Publication date
JPH0321148B2 (en) 1991-03-22

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