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JPS584538B2 - casein oak film - Google Patents
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JPS584538B2 - casein oak film - Google Patents

casein oak film

Info

Publication number
JPS584538B2
JPS584538B2 JP50045183A JP4518375A JPS584538B2 JP S584538 B2 JPS584538 B2 JP S584538B2 JP 50045183 A JP50045183 A JP 50045183A JP 4518375 A JP4518375 A JP 4518375A JP S584538 B2 JPS584538 B2 JP S584538B2
Authority
JP
Japan
Prior art keywords
casein
edible
weight
water
parts
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.)
Expired
Application number
JP50045183A
Other languages
Japanese (ja)
Other versions
JPS51121535A (en
Inventor
船津栄二
谷本信一
中塚隆三
鈴木節夫
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.)
Sumitomo Bakelite Co Ltd
Original Assignee
Sumitomo Bakelite 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 Sumitomo Bakelite Co Ltd filed Critical Sumitomo Bakelite Co Ltd
Priority to JP50045183A priority Critical patent/JPS584538B2/en
Priority to CA239,678A priority patent/CA1061163A/en
Priority to AU86772/75A priority patent/AU481906B2/en
Priority to DE19752552126 priority patent/DE2552126A1/en
Priority to IT52308/75A priority patent/IT1060099B/en
Priority to GB48069/75A priority patent/GB1532783A/en
Priority to FR7535857A priority patent/FR2292005A1/en
Publication of JPS51121535A publication Critical patent/JPS51121535A/en
Publication of JPS584538B2 publication Critical patent/JPS584538B2/en
Expired legal-status Critical Current

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  • Formation And Processing Of Food Products (AREA)
  • Manufacture Of Macromolecular Shaped Articles (AREA)
  • Food Preservation Except Freezing, Refrigeration, And Drying (AREA)
  • General Preparation And Processing Of Foods (AREA)

Description

【発明の詳細な説明】 本発明は蛋白系物質、特にカゼイン系物質の押出成形物
の製造方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing an extrudate of a protein-based material, particularly a casein-based material.

従来蛋白系物質の成形物としては、カゼイン、コラーゲ
ン、ゼラチン等を用いたシート、フイルム、チューブ等
がある。
Conventional molded products of protein-based materials include sheets, films, tubes, etc. made of casein, collagen, gelatin, and the like.

特に最近はコラーゲンイルムもしくはシートを用いたケ
ーシング類、ゼラチンシ一トを用いたカプセル類の生産
の伸びが著しるしい。
Particularly recently, there has been a remarkable increase in the production of casings using collagen films or sheets, and capsules using gelatin sheets.

またカゼインを用いたこれら成形物も近年見直され研究
されている。
These molded products using casein have also been reviewed and studied in recent years.

しかし従来はこれら水可溶性成形品類の製造方法は、す
べてアルカリ性水溶液から水を蒸発せしめてシート、フ
ィルムを得る謂ゆるキャスト法か、カゼイン等の場合に
見られるようにその10%前後の濃度のアルカリ性溶液
を酸性凝固浴中に押出し固化させる謂ゆる湿式方式など
である。
However, conventionally, the manufacturing methods for these water-soluble molded products have all been through the so-called casting method, in which sheets and films are obtained by evaporating water from an alkaline aqueous solution, or using an alkaline solution with a concentration of around 10%, as seen in the case of casein. This is a so-called wet method in which a solution is extruded into an acidic coagulation bath and solidified.

またカゼインに関して見ると以前よく研究されていたよ
うに製品に耐水性を附与するためにアルミニウム塩類、
カルシウム塩類の水溶液やホルムアルデヒド液中で処理
する方法が用いられるのが普通であり、水溶性の成形品
を実用化しようとするような試みは全くなされなかった
Regarding casein, as has been well researched in the past, aluminum salts are used to impart water resistance to the product.
Usually, a method of treatment in an aqueous solution of calcium salts or a formaldehyde solution is used, and no attempt has been made to put water-soluble molded products into practical use.

更に不溶化処理前の工程で形状物を得るために押出装置
を用いた例も見られる。
Furthermore, there are also examples in which extrusion equipment is used to obtain shaped objects in a step before insolubilization treatment.

しかし従来法は棒状のものを押出すにとどまり、シート
を得るためには更にプレスを用いて成形後不溶化処理を
行うといった極めて不合埋な方法であり、目的とする成
形物も水溶性、可食性を有するものとする考え方は皆無
であった。
However, the conventional method only extrudes a rod-shaped object, and in order to obtain a sheet, an insolubilization treatment is performed after forming using a press, which is an extremely unconsolidated method, and the desired molded product is also water-soluble and edible. There was no idea that it should have a

その後耐水性の優れた合成高分子の開発に伴ないこれら
蛋白系成形品は衰退の一途をたどっている。
Since then, with the development of synthetic polymers with excellent water resistance, these protein-based molded products have been in decline.

又近年公害問題等の関係から天然物を用いた水溶性、易
処理性のプラスチックが渇望されてきている。
In addition, in recent years, there has been a desire for water-soluble and easily treatable plastics made from natural products due to pollution problems and the like.

水溶性と云った観点から見るならば、ポリビニルアルコ
ール、ポリエチレンオキサイド、ポリプロピレンオキシ
ド、ポリビニルピロリドン、ポリエチレンイミン等の合
成高分子が存在する。
From the viewpoint of water solubility, there are synthetic polymers such as polyvinyl alcohol, polyethylene oxide, polypropylene oxide, polyvinylpyrrolidone, and polyethyleneimine.

しかしこれらは合成高分子であるが故にバクテリア分解
性が全くないか若しくは極めて小さいため自然のサイク
ルに組込まれず、何時までも残存するため廃棄物として
の公害問題を解決されるに至っていない。
However, since these are synthetic polymers, they have no bacterial degradability or are extremely small, so they are not incorporated into the natural cycle and remain indefinitely, so the problem of pollution as waste has not been solved.

また天然物を用いた例も多く見られ代表的な例として、
前述のカゼイン、コラーゲン、ゼラチン等の蛋白系物質
、オブラート、アミロース製品等があるが、これらはほ
とんど前述のような方法で作られているために製造にあ
たって大量の水分を蒸発させるため莫大な量のエネルギ
ーを要するとか、高度の技術を要するとか、従って経済
性が乏しいとかの大きな欠点を有している。
There are also many examples of using natural products, and a representative example is:
There are the aforementioned protein substances such as casein, collagen, and gelatin, as well as wafers and amylose products, but most of these products are made by the method described above, so a huge amount of water is evaporated during production. It has major drawbacks such as requiring energy, requiring advanced technology, and therefore being uneconomical.

本発明者らは上記の如き情勢を明確に把握し、蛋白系成
形物、特にカセイン系可食性フイルム・シートを経済的
に精度良く製造する方法を種々検討した結果、カセイン
粉末に対し、略々当量の無機アルカリ性物質、水及び親
水性可食性可塑剤並びに可食性滑剤等の各種添加物の混
合物を押出機により押出成形する新規な技術を確立する
に至った。
The present inventors have clearly grasped the situation described above, and have studied various ways to economically and precisely produce protein-based molded products, particularly casein-based edible films and sheets. A new technique has been established in which a mixture of equivalent amounts of an inorganic alkaline substance, water, and various additives such as a hydrophilic edible plasticizer and an edible lubricant is extruded using an extruder.

なおこのような方法の代りにカゼインのアルカリまたは
アルカリ上類金属塩をベースとし、これに可塑剤、滑剤
等の各種可食性添加剤を配合し加熱混練して、ペレット
状または粉塊状の成形材料組成物となして後、押出機を
用いて押出成形を行うことにより同様な特性を有するカ
ゼイン不可食フイルムを製造する方法があるが、本発明
は更に一歩進めてその工程の簡略化、原材料の低フスト
化を番キかろうとするものであり、その工業的価値は更
に高いものである。
Instead of this method, a molding material in the form of pellets or powder can be made by mixing alkali or super-alkali metal salts of casein with various edible additives such as plasticizers and lubricants and kneading them under heat. There is a method of manufacturing a casein inedible film having similar properties by forming a composition and then extruding it using an extruder, but the present invention takes it one step further by simplifying the process and reducing the amount of raw materials used. The aim is to reduce the amount of dust, and its industrial value is even higher.

以下に本発明の詳細につき述べる。The details of the present invention will be described below.

本発明に用いられるカゼインとは、カゼインを、主体と
するものであるが、その他ゼラチン、アルブミン、コラ
ーゲン、酵母抽出蛋白等の高純度蛋白、大豆蛋白、小麦
グルテン、膠等の純度の低い蛋白、ビール酵母、パン酵
母、単細胞膠母、トルラ酵母等の蛋白を30%以上含有
する物質等を組.合せて利用することも適宜可能である
The casein used in the present invention is mainly casein, but also includes high-purity proteins such as gelatin, albumin, collagen, and yeast extracted protein, and low-purity proteins such as soybean protein, wheat gluten, and glue. Contains substances containing 30% or more protein such as brewer's yeast, baker's yeast, single-cell glioma, and torula yeast. It is also possible to use them together as appropriate.

何れも乾燥品であることが望ましい。It is desirable that both be dry products.

本発明においてカセインと併用して用いる無機アル
カリとはアルカリ金属またはアルカリ土類金属の水酸化
物、炭酸塩、重炭酸塩等であり、特に苛性ソーダ、重曹
、ソーダ灰、等が適当である。
The inorganic alkali used in combination with casein in the present invention includes hydroxides, carbonates, bicarbonates, etc. of alkali metals or alkaline earth metals, and caustic soda, sodium bicarbonate, soda ash, etc. are particularly suitable.

また無機アルカリは水溶液の形で用いてもよい。Further, the inorganic alkali may be used in the form of an aqueous solution.

本発明で用いる無機アルカリの量は、カゼインに含まれ
る酸性基(主としてカルボギシル基、フェノール性水酸
基等)を略々中和するに足る量(即ち略々当量)である
ことが好ましい。
The amount of inorganic alkali used in the present invention is preferably an amount (ie, approximately an equivalent amount) sufficient to approximately neutralize the acidic groups (mainly carbogicyl groups, phenolic hydroxyl groups, etc.) contained in casein.

但しアルカリの量によって得られるフイルムシートの水
溶性の程度を変えられるので、目的に応じて適宜調節し
てもよい。
However, since the degree of water solubility of the obtained film sheet can be changed depending on the amount of alkali, it may be adjusted as appropriate depending on the purpose.

本発明の方法に於けるカゼインの乾燥品と略々当
量の無機アルカリとの混合物の代りに、カゼイン・ナト
リウム塩のように蛋白系物質のアルカリ金属またはアル
カリ土類金属塩の乾燥粉末を用いても作用効果の点では
全く同じであるが、工程の面よりは本発明の方法の方が
明らかに簡略化されており有利である。
In place of the mixture of dry casein and approximately equivalent amount of inorganic alkali in the method of the present invention, a dry powder of an alkali metal or alkaline earth metal salt of a proteinaceous substance such as casein sodium salt is used. Although they are exactly the same in terms of operation and effect, the method of the present invention is clearly simpler and more advantageous than the process.

即ち本発明の方法に於てはカゼインに無機アルカリその
他を配合した混合物の段階では殆んどは単に物理的に微
粉末状に均一にまじりあっているにすぎず、完全なカゼ
インの塩を形成するのは、押出機中での混練押出しの工
程に於て行われる。
That is, in the method of the present invention, at the stage of the mixture of casein and inorganic alkali, etc., most of the mixture is simply physically mixed uniformly in the form of fine powder, forming a complete casein salt. This is done during the kneading and extrusion process in an extruder.

このように混練押出しと同時に塩化をも一段で行わせよ
うとするのが本発明の特徴の一つである。
One of the features of the present invention is that chlorination is performed in one step simultaneously with kneading and extrusion.

また本発明に用いられる水であるが、上記カゼインは通
常の乾燥品であっても10%程度の水分を含有しており
、意識的に水を添加しなくても良い場合が大半である。
Furthermore, regarding the water used in the present invention, the above-mentioned casein contains about 10% water even if it is a normal dry product, and in most cases there is no need to consciously add water.

本発明の方法において、水分が重要な作用を行っている
ことは明確であり、完全乾燥物を用いて検討した結果、
1乃至30重量%の範囲内の水が必要であることを見い
出した。
It is clear that moisture plays an important role in the method of the present invention, and as a result of studies using completely dried products,
It has been found that water in the range of 1 to 30% by weight is required.

また本発明に用いられる可食性可塑剤としては、エチレ
ングリコール、プロピレングリコール、シエチレングリ
コール、ジプロピレングリコール、グリセリン、ソルビ
トール、マンニトール、庶糖等の多価アルコール類や含
水炭素類等の低分子化合物類があり、適宜選択して使用
される。
In addition, the edible plasticizers used in the present invention include polyhydric alcohols such as ethylene glycol, propylene glycol, diethylene glycol, dipropylene glycol, glycerin, sorbitol, mannitol, and sucrose, and low molecular compounds such as hydrated carbons. There are several options available, which can be selected and used as appropriate.

これら可食性親水性低分子可塑剤は得られる成形物に要
求される柔軟性および種々の物性、使用するカゼインの
種類、水の量、無機アルカリの種類及び量、各種添加剤
の種類及び量等により適宜その使用量は調節することが
可能であるが、カゼイン乾燥物に対し5重量%以上(外
割り、以下同じ)の添加が必要であり、これ以下の場合
では押出成形が困難となり、得られた成形品も硬く脆い
となり、実用に耐えない。
These edible hydrophilic low-molecular plasticizers are suitable for the flexibility and various physical properties required of the resulting molded product, the type of casein used, the amount of water, the type and amount of inorganic alkali, the type and amount of various additives, etc. The amount used can be adjusted as appropriate, but it is necessary to add 5% by weight or more (externally, the same applies hereinafter) to the dry casein; if it is less than this, extrusion molding becomes difficult and the obtained The resulting molded product also becomes hard and brittle, making it impractical for practical use.

また300重量部以上の添加の場合は高湿時のブリージ
ングが著じるしいとか、蛋白質の優れた性能が損なわれ
るといった欠点が生じる。
In addition, if 300 parts by weight or more is added, there will be disadvantages such as significant breathing at high humidity and loss of the excellent performance of the protein.

また本発明の可食性添加剤としては、上記可塑剤以外に
滑剤その他着色剤、防かび剤、防菌剤、老化防止剤等各
種のものを何れも適宜可食性の範囲のものであれば使用
してもよい。
In addition to the above-mentioned plasticizers, the edible additives of the present invention include lubricants, colorants, fungicides, antibacterial agents, anti-aging agents, and other various additives as long as they are within the edible range. You may.

中でも、滑剤としては可食性グレードの高級脂肪酸エス
テル類(グリセリン系または庶糖系)、レシチン等が望
ましく、滑剤の作用で押出しの長時間運転性の安定化を
はかることが出来るので本発明に於てはその添加が望ま
しい。
Among these, edible grade higher fatty acid esters (glycerin-based or sucrose-based), lecithin, etc. are preferable as lubricants, and since the action of the lubricant can stabilize long-term extrusion operation, they are used in the present invention. It is desirable to add it.

上述の如きカゼイン、無機アルカリ、水、および各種可
食性添加剤の混合物を混合して押出機内に導入するが、
この混合には種々の方法がある。
A mixture of casein, inorganic alkali, water, and various edible additives as described above is mixed and introduced into an extruder.
There are various methods for this mixing.

中でも本発明に於いては通常の攪拌混合装置(例えばヘ
ンシエル型ミキサー等)を用いて単にブレンドする方法
(所謂ドライブレンド法)が望ましい。
Among these, in the present invention, a method (so-called dry blending method) of simply blending using an ordinary stirring/mixing device (for example, a Henschel type mixer) is preferable.

この際密閉して水分が逃げないようにすることや適宜加
温することが好ましい。
At this time, it is preferable to seal the container to prevent moisture from escaping and to heat it appropriately.

また混練ロール、加圧ニーダー、押出機、コーニーダー
等の加熱混練装置を用いて材料を一且混練した後これを
冷却して粉砕もしくは粉砕後造粒して得られた粉末乃至
粒状物を用いるとかの方法があるが、工程簡略化の面で
前者の方法がすぐれている。
Alternatively, a powder or granules obtained by kneading the materials using a heating kneading device such as a kneading roll, pressure kneader, extruder, or co-kneader, cooling the mixture, and pulverizing it or pulverizing it and granulating it. There are two methods, but the former method is superior in terms of process simplification.

また前者の方法を用いる場合でも、上記の配合割合を調
整することにより押出機ホッパーからのチャージの均一
化、押出条件の緩和、押出成形品の均一性向上、押出機
投入前の材料の調湿といった点から望ましい粉塊状の成
形材料組成物を得ることが出来る。
Even when using the former method, by adjusting the above blending ratio, the charge from the extruder hopper can be made uniform, the extrusion conditions can be relaxed, the uniformity of the extruded product can be improved, and the humidity of the material can be adjusted before being fed into the extruder. From these points of view, it is possible to obtain a molding material composition in the form of a powder lump.

次に押出機バレル内に該成形材料組成物を導入し、加熱
混練しダイスを介して所望の形状物を得るための押出条
件は適宜選択出来るが、シリンダー内温度を100℃以
上に設定し、ダイス温度は100℃以下に設定するのが
水の沸とうに帰因する空洞の発生を避ける意味で望まし
い。
Next, the molding material composition is introduced into the extruder barrel, heated, kneaded, and passed through a die to obtain a desired shape. Extrusion conditions can be selected as appropriate, but the temperature inside the cylinder is set to 100 ° C. or higher, It is desirable to set the die temperature to 100° C. or less in order to avoid the formation of cavities due to boiling of water.

またこの際天然系高分子可塑剤を用いると空洞およびダ
イス内での物理的な摩擦力に帰因する亀裂を避ける土で
効果がある。
In addition, the use of a natural polymer plasticizer is effective in avoiding cracks caused by physical friction within the cavity and die.

また押出時空洞を生じた場合に更に高温カレンダー処理
するとか、得られた連続成形物を巻きとる前に調湿ゾー
ンを通過せしめるとかの方法も適宜採用可能である。
Further, if cavities are formed during extrusion, methods such as further high-temperature calender treatment or passing the obtained continuous molded product through a humidity control zone before winding it up can be adopted as appropriate.

かくして得られるシート、フィルム、チューブ等の押出
成形物は可塑剤を添加してあるため、乾燥時でも柔軟性
を有し、酸素バリアー性や高速ヒートシール性にもすぐ
れ、耐ブロッキング性のある透明若しくは半透明の優れ
た成形体であった。
The resulting extruded products, such as sheets, films, and tubes, have added plasticizers, so they remain flexible even when dry, have excellent oxygen barrier properties and high-speed heat sealing properties, and are transparent with blocking resistance. Otherwise, it was an excellent translucent molded product.

特に前述の各種添加剤のうち可食性のものを適宜選択す
れば、製品は可食性であり、ケーシング、カプセル等の
用途への適用が可能である。
In particular, if edible additives are appropriately selected from among the various additives mentioned above, the product is edible and can be applied to applications such as casings and capsules.

また本発明に得られた製品は注型法により得られたもの
と全く同等な性能を有するものであった。
Furthermore, the product obtained according to the present invention had exactly the same performance as that obtained by the casting method.

以下に本発明の実施例を挙げる。Examples of the present invention are listed below.

実施例 1 牛乳カゼイン100重量部(乾燥物換算93重量部)、
苛性ソーダ30重量部、グリセロール50重量部、水1
0重量部ステアリン酸グリセリンモノエステル2重量部
を攪拌混合し均一な分散体とした。
Example 1 100 parts by weight of milk casein (93 parts by weight in terms of dry matter),
30 parts by weight of caustic soda, 50 parts by weight of glycerol, 1 part by weight of water
0 parts by weight of stearic acid glycerin monoester and 2 parts by weight were stirred and mixed to form a uniform dispersion.

次に該分散体を110℃に設定された混練ロールを用い
て混練し、シート状として取り出した。
Next, the dispersion was kneaded using a kneading roll set at 110° C. and taken out as a sheet.

次いでこのシートを衝撃式粉砕機にて粉砕し粒状体とし
た。
This sheet was then crushed into granules using an impact crusher.

次に上記の粒状物を圧縮比1.8のダルメージ型スクリ
ューおよびベント機構を内蔵する押出機内に導入し、6
0回転の回転速度、シリンダー内温度120〜150℃
、ダイス温度100℃の条件下にダイスを介して0.3
mm厚のシートを押出した。
Next, the above granules were introduced into an extruder equipped with a Dalmage screw with a compression ratio of 1.8 and a vent mechanism.
Rotation speed of 0 rotation, cylinder temperature 120-150℃
, 0.3 through the die at a die temperature of 100°C.
A sheet with a thickness of mm was extruded.

得られたシートはわずかに褐色を帯びた透明なシートで
あった。
The obtained sheet was a slightly brownish transparent sheet.

また本シートは全くの可食性であり且つ酸素透過性が非
常に小さい上にヒートシール可能な優れた柔軟性を有す
るシートであった。
Furthermore, this sheet was completely edible, had very low oxygen permeability, and had excellent flexibility that allowed it to be heat-sealed.

実施例 2 乾燥ゼラチン100重量部(乾燥物換算91重量部)、
炭酸ソーダ30重量部、ソルビトール130重量部、大
豆レシチン3重量部、をスーパーミキサーを用いて、高
湿度下で40〜60℃に加温しつつ攪拌混合し、次に冷
却、粗砕して粉塊状の成形材料組成物を得た。
Example 2 100 parts by weight of dry gelatin (91 parts by weight in terms of dry matter),
Using a super mixer, 30 parts by weight of soda carbonate, 130 parts by weight of sorbitol, and 3 parts by weight of soybean lecithin are stirred and mixed while heating to 40 to 60°C under high humidity, then cooled and coarsely ground to form a powder. A bulk molding material composition was obtained.

次にこの成形材料をシリンダー内温度が1301〜16
0℃、ダイス温度が120℃である以外は全く実施例1
と同様な条件で、外径50mmf、肉厚2mmのテユー
プを押出した。
Next, apply this molding material to a cylinder temperature of 1301 to 16
Exactly Example 1 except that the die temperature was 0°C and the die temperature was 120°C.
Under the same conditions as above, a tube with an outer diameter of 50 mm and a wall thickness of 2 mm was extruded.

本チューブは褐色透明な柔軟性を有する巻き取り可能な
チューブであった。
This tube was a brown transparent flexible tube that could be rolled up.

実施例 3 乾燥ビール酵母100重量部(乾燥物換算89重量部)
、カゼイン50重量部(乾燥物換算45重量部)、炭酸
カリ50重量部、アルギン酸ソーダ50重量部、エチレ
ングリコール25重量部、庶糖脂肪酸エステル1重量部
を攪拌混合し実施例2と同様な条件でミキサー混練を行
い粉塊状物を得た。
Example 3 100 parts by weight of dry beer yeast (89 parts by weight in terms of dry matter)
, 50 parts by weight of casein (45 parts by weight in terms of dry matter), 50 parts by weight of potassium carbonate, 50 parts by weight of sodium alginate, 25 parts by weight of ethylene glycol, and 1 part by weight of sucrose fatty acid ester were stirred and mixed under the same conditions as in Example 2. Kneading was performed with a mixer to obtain a powder lump.

得られた粉塊状物を実施例1と同様な押出条件で0.0
4mmのシートを押出した。
The obtained powder mass was extruded under the same extrusion conditions as in Example 1.
A 4 mm sheet was extruded.

得られたシートは褐色半透明なシートであり、従来の可
食シートに比して低価格の可食性水溶性シートであった
The obtained sheet was a brown translucent sheet, and was an edible water-soluble sheet that was cheaper than conventional edible sheets.

Claims (1)

【特許請求の範囲】[Claims] 1 カゼイン、カゼインに対し略々当量の無機アルカリ
並びに水及び可食性親水性低分子可塑剤並びに可食性滑
剤よりなる可食性添加剤の混合物を、高温の押出機バレ
ル内に導入し混練して均質塊状体となして後、ダイスを
介して押出すことを特徴とするカゼイン系可食フィルム
・シートの製造方法。
1. Casein and a mixture of an edible additive consisting of an inorganic alkali and water in an approximately equivalent amount to the casein, an edible hydrophilic low-molecular plasticizer, and an edible lubricant are introduced into a high-temperature extruder barrel and kneaded to obtain a homogeneous product. A method for producing a casein-based edible film/sheet, which comprises forming into a lump and extruding it through a die.
JP50045183A 1974-11-22 1975-04-16 casein oak film Expired JPS584538B2 (en)

Priority Applications (7)

Application Number Priority Date Filing Date Title
JP50045183A JPS584538B2 (en) 1975-04-16 1975-04-16 casein oak film
CA239,678A CA1061163A (en) 1974-11-22 1975-11-14 Protein-starch binary molding composition and shaped articles obtained therefrom
AU86772/75A AU481906B2 (en) 1975-11-20 Protein-starch composition
DE19752552126 DE2552126A1 (en) 1974-11-22 1975-11-20 WATER-SOLUBLE AND EDIBLE THERMOPLASTIC MOLDING COMPOUNDS, PROCESS FOR THEIR PRODUCTION AND USE OF THE SAME FOR THE PRODUCTION OF MOLDINGS
IT52308/75A IT1060099B (en) 1974-11-22 1975-11-20 EDIBLE MOLDING COMPOSITION OF PROTEIN STARCH AND PRODUCTS OBTAINED FROM IT
GB48069/75A GB1532783A (en) 1974-11-22 1975-11-21 Edible thermoplastic moulding compositions containing starch and protein salts
FR7535857A FR2292005A1 (en) 1974-11-22 1975-11-24 BINARY MOLDING COMPOSITION CONTAINING PROTEINS AND STARCH, ITS PREPARATION PROCESS, AND ITS APPLICATIONS

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP50045183A JPS584538B2 (en) 1975-04-16 1975-04-16 casein oak film

Publications (2)

Publication Number Publication Date
JPS51121535A JPS51121535A (en) 1976-10-23
JPS584538B2 true JPS584538B2 (en) 1983-01-26

Family

ID=12712145

Family Applications (1)

Application Number Title Priority Date Filing Date
JP50045183A Expired JPS584538B2 (en) 1974-11-22 1975-04-16 casein oak film

Country Status (1)

Country Link
JP (1) JPS584538B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62126950A (en) * 1985-11-29 1987-06-09 Unie Koroido Kk Edible film containing glucomannan
JPS6339551A (en) * 1986-08-04 1988-02-20 House Food Ind Co Ltd Preparation of food raw material having fibrous texture
JP6739767B2 (en) * 2015-03-04 2020-08-12 学校法人日本大学 Protein sheet and method for producing protein sheet

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5831182B2 (en) * 1975-03-27 1983-07-04 住友ベークライト株式会社 Kashyokusei Film no Seizouhouhou

Also Published As

Publication number Publication date
JPS51121535A (en) 1976-10-23

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