JPS5831182B2 - Kashyokusei Film no Seizouhouhou - Google Patents
Kashyokusei Film no SeizouhouhouInfo
- Publication number
- JPS5831182B2 JPS5831182B2 JP50036079A JP3607975A JPS5831182B2 JP S5831182 B2 JPS5831182 B2 JP S5831182B2 JP 50036079 A JP50036079 A JP 50036079A JP 3607975 A JP3607975 A JP 3607975A JP S5831182 B2 JPS5831182 B2 JP S5831182B2
- Authority
- JP
- Japan
- Prior art keywords
- film
- amylose
- weight
- casein
- 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.)
- Expired
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- General Preparation And Processing Of Foods (AREA)
- Food Preservation Except Freezing, Refrigeration, And Drying (AREA)
Description
【発明の詳細な説明】
本発明はアミロース、カゼインのアルカリ金属塩および
低分子可食性可塑剤から構成される成形材料組成物を、
押出機バレル内に導入し混練して流動性の均質塊状体と
成して後、ダイスを介して押出すことを特徴とする可食
性押出しフィルムの製造方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention provides a molding material composition comprising amylose, an alkali metal salt of casein, and a low molecular edible plasticizer.
The present invention relates to a method for producing an edible extruded film, which comprises introducing the film into an extruder barrel, kneading it to form a fluid homogeneous mass, and extruding it through a die.
従来よりアミロースフィルムを得る方法としては、該物
質の水溶液を用いて水を蒸発させて製品を得る謂ゆるキ
ャストフィルム法(湿式)が行なわれていた。Conventionally, as a method for obtaining an amylose film, a so-called cast film method (wet method) has been used in which a product is obtained by evaporating water using an aqueous solution of the substance.
しかしながら得られるシート若しくはフィルムが特徴あ
る性質を有するにも拘らず製法自体に致命的欠点を有す
るため、他プラスチック類生産量の驚異的伸びに比較し
て全く伸び悩みの状態にあるのが現状である。However, despite the unique properties of the resulting sheet or film, the manufacturing method itself has fatal flaws, and as a result, the production of other plastics is currently at a completely sluggish rate compared to the phenomenal growth in production of other plastics. .
即ちこれら致命的欠点とは、(1)アミロースの溶媒と
して適当な工業用溶媒がなく水を用いざるを得ないため
、水を除去して製品を得るためには莫大な熱量が必要と
なり、経済的に高価なものとなる。In other words, these fatal drawbacks are: (1) There is no suitable industrial solvent as a solvent for amylose, so water has to be used; therefore, a huge amount of heat is required to remove water and obtain the product, making it uneconomical. It becomes expensive.
(2)キャストフィルム法であるため一般には肉厚製品
しか得られず、工程的にシート。(2) Since it is a cast film method, generally only thick products can be obtained, and the process requires sheets.
フィルム等に製品が限定されてしまう。Products are limited to films, etc.
(3)得られたフィルムは低湿度下で脆く、これを避け
るためグリセリンの如き低分子可塑剤を多量に混合する
と高湿度下でのブリード現象が生ずる。(3) The obtained film becomes brittle under low humidity conditions, and if a large amount of a low-molecular plasticizer such as glycerin is mixed in to avoid this, a bleed phenomenon will occur under high humidity conditions.
(4)高度の製造技術及び精度の高い設備が要求される
。(4) Advanced manufacturing technology and highly accurate equipment are required.
等である。etc.
一方これらの欠点を除くために押出機を用いる所謂乾式
の製造法b′−提案されているが、この方法はアミロー
スを化学的に誘導体と成し、加工性を附与し、これに各
種可塑剤を添加して成形材料組成物となし成形せんとす
るものであり、キャスト法による製造法を簡略化せしめ
たという点でその意義は大きい。On the other hand, in order to eliminate these drawbacks, a so-called dry production method b' using an extruder has been proposed, but this method involves chemically derivatizing amylose, giving it processability, and adding various plasticizers to it. This method is significant in that it simplifies the manufacturing method by casting, which is made into a molding material composition by adding a molding agent.
しかしながらアミロースを誘導体とすることは本質的に
アミロース本来の性質を損うといった欠点がある。However, using amylose as a derivative has the disadvantage that the original properties of amylose are essentially impaired.
即ち加工性を向上させるために未処理アミロースの高結
晶性(強固な水素結合)に由来する機械的性質、耐湿耐
水性が犠牲にされるとか、誘導体化することにより可食
性であるという他のプラスチックの追随を許さない性能
が犠牲にされるといった欠点を有する。In other words, the mechanical properties derived from the high crystallinity (strong hydrogen bonding) of untreated amylose and the moisture and water resistance may be sacrificed to improve processability, or other properties such as edibility may be sacrificed by derivatization. The drawback is that the unrivaled performance of plastics is sacrificed.
更にこの方法の改良方法として未処理アミロースに水及
びグリセリン、エチレングリコール、プロビレ/グリコ
ール、ジメチルホルムアミド等の100℃においてlQ
Qmm以下の蒸気圧を有する有機可塑剤を混じ、高剪断
力をかげて得られる高温均質流動体をダイスを介して押
出成形する方法が提案されている。Furthermore, as an improvement to this method, untreated amylose is treated with water and glycerin, ethylene glycol, probilene/glycol, dimethylformamide, etc. at 100°C.
A method has been proposed in which a high-temperature homogeneous fluid obtained by mixing an organic plasticizer having a vapor pressure of Qmm or less and applying a high shear force is extruded through a die.
しかしながらこれら低分子有機可塑剤を単独で添加する
方法は致命点欠点を有していることが実験の結果判明し
た。However, as a result of experiments, it has been found that the method of adding these low-molecular-weight organic plasticizers alone has a fatal drawback.
即ち(1)低分子可塑剤であるためアミロースとの相溶
性に限界があり、アミロース100部に対して40部以
上の可塑剤を添加すると、加熱押出し時粘性の少ない柔
かくて脆い物質となるため、巻き取りのためのテンショ
ンをかげることが出来ず、引張りによる薄膜化カ非常に
困難になる。That is, (1) since it is a low-molecular plasticizer, its compatibility with amylose is limited, and if more than 40 parts of plasticizer is added to 100 parts of amylose, it becomes a soft and brittle substance with low viscosity during hot extrusion. In this case, the tension for winding cannot be lowered, making it extremely difficult to thin the film by pulling.
(2)アミロース製品は衆知の如く乾燥時固くもろいた
め多量の可塑剤が必要となるが、多量の可塑剤を添加し
た場合、製品にした後謂ゆるブリージング現象を生じ製
品として使用に耐えず、特に本現象は高湿下に製品をさ
らした場合著じるしい。(2) As is well known, amylose products are hard and brittle when dry, so they require a large amount of plasticizer, but if a large amount of plasticizer is added, a so-called breathing phenomenon will occur after the product is made, making it unusable as a product. This phenomenon is particularly noticeable when the product is exposed to high humidity.
(3)可食性といった観点から考えた場合、低分子有機
可塑剤のうち未処理アミロースと相溶性を有するものの
数は限定され、わずかに水、グリセリ/、ンルビトール
、マルチトール、マンニット程度のものである。(3) When considered from the perspective of edibility, the number of low-molecular organic plasticizers that are compatible with untreated amylose is limited, and only a few include water, glycerin, nrubitol, maltitol, and mannitol. It is.
これらの可塑剤は低湿度下での可塑化効果にとぼしく又
高湿下でのブリードを生じ易い。These plasticizers have poor plasticizing effect under low humidity conditions and are prone to bleed under high humidity conditions.
(4)更にポリビニルアルコール等の水溶性高分子を水
との組合せで添加することが提案されているが、ブリー
ジング現象および熱時に際しての引張り、伸び強度とい
う観点からは良好であるが、可食性という点では全く問
題外である。(4) Furthermore, it has been proposed to add a water-soluble polymer such as polyvinyl alcohol in combination with water, but this is good from the viewpoint of breathing phenomenon and tensile and elongation strength when heated, but it is not edible. In that sense, it is completely out of the question.
等である。我々はこれらの現状に対し可食性を有し、高
温押出しフィルム化時に延伸可能であり、且つブロッキ
ング現象を起さず、製品にした場合の乾燥時柔軟性が良
好で且つ高湿下でのブリージング現象の生じない経済性
のある押出フィルムを得るといった目標の画期的研究を
重ね、これら条件を満たす発明を成すに至った。etc. In response to these current circumstances, we have developed a product that is edible, can be stretched during high-temperature extrusion, does not cause blocking, has good flexibility when dried, and is breathable under high humidity. Through ground-breaking research aimed at obtaining an economical extruded film that does not cause any phenomenon, the inventors achieved an invention that satisfies these conditions.
即ち未処理アミロースに可食性低分子可塑剤を作業に支
障のない程度混合し、更にこれに加えてカゼインのアル
カリ金属塩を併用混合することにより、従来の未処理ア
ミロース単独フィルムシートの欠点をすべて解消すると
(・つた画期的製品を得る方法を確立するに至った。In other words, by mixing untreated amylose with an edible low-molecular-weight plasticizer to an extent that does not interfere with the work, and further adding an alkali metal salt of casein, all the drawbacks of conventional untreated amylose-only film sheets can be overcome. Once the problem was resolved, a method was established to obtain an epoch-making product.
即ち下表の如きアミロースとカゼイノのアルカリ金属塩
の併用混合に帰因する効果を見い出すに至った。That is, we have discovered effects resulting from the combination of amylose and caseino alkali metal salts as shown in the table below.
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.
本発明において用いられるアミロースとは、とうもろこ
しでんぷん、馬鈴薯でんぷん、タヒオヵでんぷん、米で
んぷん等の種々のでんぷんの分画により得られた分画ア
ミロースおよび品種改良により得られたアミロース含有
量50%以上の謂ゆるパイアミロースでんぷん、および
一般のでんぷんもしくはアミロペクチンと分画アミロー
スとの混合物であってアミロース含有量が50%以上の
組成物である。The amylose used in the present invention refers to fractionated amylose obtained by fractionating various starches such as corn starch, potato starch, Tahioka starch, and rice starch, and so-called amylose with an amylose content of 50% or more obtained through breeding. It is a composition of loose pie amylose starch, and a mixture of general starch or amylopectin and fractionated amylose, and has an amylose content of 50% or more.
また本発明に用いられるカゼインのアルカリ金属塩とは
、ナトリウムカゼイネート、カリウムカゼイネート等で
あって、カゼインを構成するカルボキシル基とアルカリ
金属の塩はすべて包含される。Further, the alkali metal salt of casein used in the present invention includes sodium caseinate, potassium caseinate, etc., and includes all salts of a carboxyl group and an alkali metal constituting casein.
またその反応程塵は適宜選択出来るが、望ましくはカゼ
イン中のカルボキシル基と略々当量のアルカリ金属化合
物で処理されたカゼイネートが望ましい。Although the reaction mixture can be selected as appropriate, caseinate treated with an alkali metal compound in an amount approximately equivalent to the carboxyl group in casein is preferable.
しかしながら耐水性の要求される用途には一部のみアル
カリ金属塩化されたカゼインを用いるのが望ましい。However, for applications requiring water resistance, it is preferable to use casein in which only a portion of the casein is chlorinated with an alkali metal.
またカゼインのアルカリ金属塩はソジウムカゼイネート
の如き市販品を用いることが望ましいが、経済性を重視
する場合においては、市販カゼインにかんすい等の食添
用アルカリ物質の水溶液を少量添加して押出機バレル内
でカゼイネート化を行うことも、一段でカゼイネート化
とフィルム化を行う上で有効な方法である。Furthermore, it is desirable to use a commercially available alkali metal salt of casein such as sodium caseinate, but if economic efficiency is important, it is preferable to add a small amount of an aqueous solution of an alkaline food additive such as kansui to commercially available casein and extrude it. Forming caseinate in the machine barrel is also an effective method for forming caseinate and film in one step.
また本発明者らはカゼインのアルカリ金属塩を選定する
に際して、類似物質としてカゼイン、ニカワ、ゼラチン
、大豆蛋白、コラーゲ/、各種酵母類より抽出された蛋
白等の各種蛋白のアルカリ金属塩およびアルギン酸ソー
ダー等の適用検討も実施したが、夫々一長一短があり、
カゼインのアルカリ金属塩が特に優れていることを見い
出したものである。In addition, when selecting an alkali metal salt of casein, the present inventors used similar substances such as casein, glue, gelatin, soybean protein, collagen, alkali metal salts of various proteins such as proteins extracted from various yeasts, and sodium alginate. We have also examined the application of
It has been discovered that alkali metal salts of casein are particularly excellent.
またその使用量はアミロース100重量部に対して、1
0重量部から1000重量部の範囲で適宜選択可能であ
る。The amount used is 1 for 100 parts by weight of amylose.
It can be appropriately selected within the range of 0 parts by weight to 1000 parts by weight.
また本発明に用いられる可食性低分子可塑剤とは、アミ
ロース及びカゼインのアルカリ金属塩に対する膨潤可塑
化能を有する物質であって且つ可食性の低分子有機化合
物および水に限定される。Furthermore, the edible low-molecular-weight plasticizer used in the present invention is limited to edible low-molecular organic compounds and water that are substances that have the ability to swell and plasticize amylose and alkali metal salts of casein.
代表例として水、グリセリン、ソルビトール、マンニッ
ト、マルチトール、またはグリセリンのモノ脂肪酸エス
テル類、蔗糖のアルキルエステル類等がある。Typical examples include monofatty acid esters of water, glycerin, sorbitol, mannitol, maltitol, or glycerin, and alkyl esters of sucrose.
この中で特にアミロースへの相溶性という点で水および
グリセリンもしくは両者の併用が好ましい。Among these, water and glycerin, or a combination of both, are particularly preferred from the viewpoint of compatibility with amylose.
上述の如きアミロース、カゼインのアルカリ金属塩、低
分子可食性有機可塑剤、必要ならば水を均質に混合して
成形材料組成物となして後押出機内に導入するが、この
混合方法には種々の方法がある。Amylose as described above, an alkali metal salt of casein, a low-molecular edible organic plasticizer, and water if necessary are homogeneously mixed to form a molding material composition and then introduced into the extruder, but there are various methods for this mixing. There is a method.
即ち攪拌混合機を用いて単にブレンドする方法、混練ロ
ール、加圧ニーター−1押出機等の加熱混練装置を用(
・て混線した後、これを冷却して粉砕若しくは造粒して
得られた粉末もしくは粒状成形材料組成物を用いるとか
の方法がある。That is, a method of simply blending using a stirring mixer, a method of simply blending using a stirring mixer, a method of blending using a heating kneading device such as a kneading roll, a pressure kneader-1 extruder, etc.
・There is a method of using a powder or granular molding material composition obtained by mixing the wires by cooling and pulverizing or granulating the mixture.
特に後者の方法を用いる場合、押出機ホッパーかもの均
一チャージ性、押出し混線条件の緩和、押出しフィルム
の均一複合化という観点からは望ましい。In particular, when using the latter method, it is desirable from the viewpoints of uniform charging of the extruder hopper, relaxation of extrusion cross-wire conditions, and uniform composite formation of the extruded film.
次に押出機内に該組成物をチャージし、100℃以上に
設定された押出機内で加熱混練しダイスを介してフィル
ム、シートを得る。Next, the composition is charged into an extruder, heated and kneaded in the extruder set at 100° C. or higher, and passed through a die to obtain a film or sheet.
なお押出しを行う場合は、ベント式押出機を用い、圧縮
比が1.5〜4.5のタ′ルメージ型スクリューを選択
し、ホッパー下水冷、バレル内温度80〜170℃、T
ダイもしくはコートハンガーダイ温度80乃至120℃
といった条件での実施が好ましい。When extruding, use a vented extruder, select a talmage type screw with a compression ratio of 1.5 to 4.5, use water cooling under the hopper, a barrel temperature of 80 to 170°C, and T.
Die or coat hanger die temperature 80 to 120℃
It is preferable to carry out the test under these conditions.
また押出しフィルム化に際して長時間運転性、押出量の
安定性を計る上で、チャージ物質100重量部に対し、
0.1〜3.0重量部のグリセリン脂肪酸エステル、蔗
糖の脂肪酸エステル等の可食性脂肪酸エステル類をトラ
イブレンドすることにより可食性を損うことなく効果を
示すことを見い出している。In addition, in order to measure long-term operability and stability of extrusion amount during extrusion film production, for 100 parts by weight of charge material,
It has been found that tri-blending 0.1 to 3.0 parts by weight of edible fatty acid esters such as glycerin fatty acid ester and sucrose fatty acid ester produces an effect without impairing edibility.
謂ゆる可食性滑剤である。この様にして押出しフィルム
を得る方法においてアミロースを単独で用いる場合、乾
燥時にも柔軟性を維持出来る迄の量の低分子可塑剤のみ
を添加すると混練流動塊状体は非常に柔かく脆いものと
なってしまうため、成形性が著しるしく減じフィルム、
シート等の場合無数の亀裂を生じてしまう。It is a so-called edible lubricant. When amylose is used alone in this method for obtaining an extruded film, if only an amount of low-molecular plasticizer is added to maintain flexibility during drying, the kneaded fluidized mass becomes extremely soft and brittle. Due to storage, the formability of the film is significantly reduced.
In the case of sheets, etc., countless cracks occur.
また全く熱時粘性がないため延伸不可能となり延伸によ
る薄膜化(工全く出来ない。In addition, since it has no viscosity when heated, it cannot be stretched and cannot be made into a thin film by stretching.
発明者らの見解によると乾燥アミロース100重量部に
対して、40重量部以上のグリセリンの如き低分子可塑
剤の添加は実用上不可能である。According to the inventors' opinion, it is practically impossible to add 40 parts by weight or more of a low-molecular plasticizer such as glycerin to 100 parts by weight of dry amylose.
また可能だとしても高湿下のフリージングの問題は解決
出来ない。Even if it were possible, the problem of freezing under high humidity cannot be solved.
これに対して本発明において規定されたカゼインのアル
カリ金属塩を併用することによりこの問題は一挙に解決
されるという画期的事実を見い出すに至るとともに、前
表の如き種々の効果をも見い出すに至った。On the other hand, we have discovered the revolutionary fact that this problem can be solved at once by using the alkali metal salt of casein specified in the present invention, and we have also discovered various effects as shown in the table above. It's arrived.
必要ならば押出しにより得られたフィルムシートを更に
カレンター−加工を行なって商品価値を高めるといった
手法も適宜利用可能であるし、また得られたシートを所
望の含水量まで調湿して包装するといった手法も適宜利
用可能である。If necessary, the film sheet obtained by extrusion can be further calender-processed to increase its commercial value, or the obtained sheet can be moistened to a desired moisture content and then packaged. Methods can also be used as appropriate.
かくして得られたフィルムは巻き取った状態でもフロラ
キング現象が全くなく、高湿下でも低分子可塑剤のプリ
ージング現象がなく、低湿度下においても強靭であり、
ヒートシール性を有し、酸素バリヤー性を有し、且つ経
済性を有する従来にない優れたフィルムであった。The film obtained in this way has no floraking phenomenon even when rolled up, no precipitating phenomenon of low-molecular plasticizers even under high humidity, and is strong even under low humidity.
It was an unprecedented film that had heat-sealing properties, oxygen barrier properties, and economic efficiency.
本フィルムは食用油脂類、固形食品添加物等の可食包装
用フィルムとして最適なものであり用途は非常に広い。This film is ideal as a film for edible packaging of edible oils and fats, solid food additives, etc., and has a wide range of uses.
以下に本発明の具体的実施例を挙げる。Specific examples of the present invention are listed below.
実施例 1
ハイアミロースとうもろこしでんぷん
(アミロース含有量60%含水量8%)
50重量部
ソジウム力ゼイネート 50重量部食添用グ
リセリン 40重量部食添用ソルビトー
ル 10重量部上記配合物を表面温度12
0℃に設定された混練ロールにて混練し、水を蒸発せし
めながらシート状と成し、得られたシートを冷却扇衝撃
式粉砕機を用いて粉砕し粒状成形材料組成物を得た。Example 1 High amylose corn starch (amylose content 60% water content 8%) 50 parts by weight Sodium zeinate 50 parts by weight Glycerin for food additives 40 parts by weight Sorbitol for food additives 10 parts by weight The above formulation was heated to a surface temperature of 12
The mixture was kneaded using a kneading roll set at 0°C to form a sheet while evaporating water, and the resulting sheet was pulverized using a cooling fan impact type pulverizer to obtain a granular molding material composition.
その後グリセリン脂肪酸エステルを粉砕粒状物100重
量部に対して1重量部添加しトライブレンドを行った。Thereafter, 1 part by weight of glycerin fatty acid ester was added to 100 parts by weight of the pulverized granules to perform triblending.
その后多湿下で調湿を行った。次に上記組成物を圧縮比
18のダルメージ型スクリューを内蔵する押出機内に導
入し、60回転の回転速度、シリノダー内温度120〜
160”C1り゛イス温度420℃、ダイスリップ間隔
0.1 mmの条件で押出し、引取装置で延伸して60
ミクロンのフィルムを得た。After that, humidity was adjusted under high humidity conditions. Next, the above composition was introduced into an extruder equipped with a Dullmage screw with a compression ratio of 18, and the rotation speed was 60 revolutions, and the internal temperature of the cylinder was 120~
160" C1 was extruded under the conditions of a die temperature of 420°C and a die slip interval of 0.1 mm, and stretched with a drawing device to 60"
A micron film was obtained.
得られたフィルムは淡褐色半透明の優れた物性のフィル
ムであり、20℃、関係湿i20%の条件下でも柔軟性
を有し且つ25℃、80悌の高湿下でも全くブリージン
グ現象を生じなかった。The obtained film was a light brown translucent film with excellent physical properties, and was flexible even under conditions of 20°C and relative humidity of 20%, and did not exhibit any bleeding phenomenon even under high humidity conditions of 25°C and 80 °C. There wasn't.
実施例 2
ハイアミロースと5もろこしでんぷん
(アミロース含有量75優、含水量10%)60重量部
カゼイン 40重量部食添用グ
リセリン 50重量部かんすい(オリエ
ンタル酵母工業株
式会社製、商品名飛竜印粉末かんす
い)の20悌水溶液 20重量部グリセリ
ンモノ脂肪酸エステル 1重量部上記組成物をヘン
シェルミキサーを用いて12QOr、p、mの高速攪拌
を行い、混合造粒を行ないかんすいによりカゼイン分子
中の主にカルボキシル基が完全にアルカリ金属塩化され
たカゼインを含む粒状成形材料組成物を得た。Example 2 High amylose and 5 sorghum starch (amylose content 75%, water content 10%) 60 parts by weight Casein 40 parts by weight Glycerin for food additives 50 parts by weight Kansui (manufactured by Oriental Yeast Co., Ltd., trade name Hiryujirushi powder) 20 parts by weight of an aqueous solution of 20 parts by weight of glycerin monofatty acid ester 1 part by weight The above composition was stirred at a high speed of 12Q Or, p, m using a Henschel mixer, and mixed and granulated. A granular molding material composition was obtained containing casein in which the groups were completely alkali metal chlorinated.
得られた粒状組成物を実施例1と同様の条件で押出し4
0ミクロンのフィルムを得た。The obtained granular composition was extruded under the same conditions as in Example 1.
A 0 micron film was obtained.
ただし引取り速度を実施例1より早くし薄膜化を計った
。However, the take-up speed was made faster than in Example 1 to achieve a thinner film.
得られたフィルムは淡黄色半透明の優れた物性のフィル
ムであり、関係湿度65%の条件下でもブロッキング、
ブリージングが全くなく、20φの低湿度下でも柔軟な
フィルムであった。The obtained film is a pale yellow, translucent film with excellent physical properties, and has excellent blocking properties even under conditions of relative humidity of 65%.
There was no breathing at all, and the film remained flexible even under low humidity conditions of 20φ.
このフィルムで熱封着法により袋を作成し、内部にマー
ガリンを詰めたところ良好な包装体が得られた。When a bag was made from this film by heat sealing and margarine was stuffed inside, a good package was obtained.
Claims (1)
可食性可塑剤を主成分とする配合組成物を均一に混合ま
たは混練して成形材料組成物を得、該組成物を押出機に
投入し押出機内で混練して流動性の均質塊状体となし、
ダイスを介してフィルム状にこれを押出してフィルムを
得ることを特徴とする可食性フィルムの製造方法。1. A blended composition containing amylose, an alkali metal salt of caseino, and a low-molecular edible plasticizer as main components is uniformly mixed or kneaded to obtain a molding material composition, and the composition is charged into an extruder. Knead to form a fluid homogeneous mass,
1. A method for producing an edible film, which comprises obtaining a film by extruding it into a film through a die.
Priority Applications (7)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP50036079A JPS5831182B2 (en) | 1975-03-27 | 1975-03-27 | Kashyokusei Film no Seizouhouhou |
| 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 |
|---|---|---|---|
| JP50036079A JPS5831182B2 (en) | 1975-03-27 | 1975-03-27 | Kashyokusei Film no Seizouhouhou |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS51112533A JPS51112533A (en) | 1976-10-05 |
| JPS5831182B2 true JPS5831182B2 (en) | 1983-07-04 |
Family
ID=12459722
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP50036079A Expired JPS5831182B2 (en) | 1974-11-22 | 1975-03-27 | Kashyokusei Film no Seizouhouhou |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5831182B2 (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS584538B2 (en) * | 1975-04-16 | 1983-01-26 | 住友ベークライト株式会社 | casein oak film |
| JPS59187765A (en) * | 1983-04-07 | 1984-10-24 | Maruka:Kk | Preparation of tidbit |
| JPS6296060A (en) * | 1985-06-06 | 1987-05-02 | Unie Koroido Kk | Glucomannan composition |
| JP2013138350A (en) | 2011-12-28 | 2013-07-11 | D & M Holdings Inc | Headphones and ear pads |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS584537B2 (en) * | 1974-11-22 | 1983-01-26 | 住友ベークライト株式会社 | Method for producing edible extruded product |
-
1975
- 1975-03-27 JP JP50036079A patent/JPS5831182B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS51112533A (en) | 1976-10-05 |
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