JPH0725797B2 - Twain manufacturing method - Google Patents

Twain manufacturing method

Info

Publication number
JPH0725797B2
JPH0725797B2 JP1691087A JP1691087A JPH0725797B2 JP H0725797 B2 JPH0725797 B2 JP H0725797B2 JP 1691087 A JP1691087 A JP 1691087A JP 1691087 A JP1691087 A JP 1691087A JP H0725797 B2 JPH0725797 B2 JP H0725797B2
Authority
JP
Japan
Prior art keywords
zein
extract
extraction
adjusted
added
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 - Fee Related
Application number
JP1691087A
Other languages
Japanese (ja)
Other versions
JPS63185999A (en
Inventor
高伸 河本
史生 福井
隆 八木
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.)
Showa Sangyo Co Ltd
Original Assignee
Showa Sangyo Co Ltd
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Filing date
Publication date
Application filed by Showa Sangyo Co Ltd filed Critical Showa Sangyo Co Ltd
Priority to JP1691087A priority Critical patent/JPH0725797B2/en
Publication of JPS63185999A publication Critical patent/JPS63185999A/en
Publication of JPH0725797B2 publication Critical patent/JPH0725797B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Peptides Or Proteins (AREA)
  • Paints Or Removers (AREA)
  • Adhesives Or Adhesive Processes (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、とうもろこしまたはコーングルテンミールか
ら、エタール可溶性の大きいツェインを製造する方法に
関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method for producing highly etal-soluble zein from corn or corn gluten meal.

〔従来の技術〕[Conventional technology]

ツェインは、とうもろこし蛋白質の主要成分であり、ア
ルコールに可溶で、接着力及びフィルムや繊維の形成能
を有し、そのアルコールあるいはアルカリ溶液を噴霧,
塗布,浸漬等の適宜の手段で被処理物の表面に付着さ
せ、これを乾燥することによって、耐水性,耐酸性,耐
熱性,電気絶縁性等に優れた被膜をつくることが知られ
ている。
Zein, which is the main component of corn protein, is soluble in alcohol, has adhesiveness and the ability to form films and fibers, and can be sprayed with alcohol or alkaline solutions.
It is known that a film excellent in water resistance, acid resistance, heat resistance, electric insulation, etc. is formed by adhering it to the surface of the object to be treated by an appropriate means such as coating or dipping and drying it. .

このような性質から、ツェインは製紙加工用塗布剤,木
材製品の表面塗装,合板等の接着剤,防湿剤,食品・錠
剤等のコーティング剤として利用されている。
Due to these properties, zein is used as a coating agent for papermaking, surface coating of wood products, an adhesive agent for plywood, a moistureproof agent, and a coating agent for foods, tablets and the like.

ツェインの製造法については特開昭61−167700号公報や
「シード・プロテインス バイオケミストリー,ジェネ
ティックス,ニュートリティブ バリュー(Seed Prote
ins Bichemistry,Genetics,Nutritive Value)」(W.Go
ttschalk,H.P.Muller編、Martinus Nijhoff/Dr.W.Junk
Publishers,1983)第275〜287頁に概説されているよう
に、一般にコーングルテンミール等の原料を70〜90%
(v/v)エタール,90%(v/v)前後のイソプロパール等
の含水低級アルコールで抽出し、得られたアルコール溶
液から溶剤を溜去する、あるいは同溶液を水または塩類
溶液中に投入してツェインを沈澱させる等の方法により
製造される。
Regarding the manufacturing method of zein, JP-A-61-167700 and “Seed Proteins Biochemistry, Genetics, Nutritive Value (Seed Prote
ins Bichemistry, Genetics, Nutritive Value) "(W.Go
ttschalk, HP Muller, Martinus Nijhoff / Dr.W.Junk
Publishers, 1983) 70-90% of raw materials such as corn gluten meal are generally used as outlined on pages 275-287.
(V / v) Ethal, 90% (v / v) About 90% (v / v) Isopropal and other hydrous lower alcohols are extracted, and the solvent is distilled off from the resulting alcohol solution, or the solution is poured into water or a salt solution. Then, it is produced by a method such as precipitating zein.

〔発明が解決しようとする問題点〕[Problems to be solved by the invention]

食品・錠剤等のコーティング材等の用途において、ツェ
インに要求される性質としては、エタノール可溶性、す
なわち種々の濃度のエタールに溶解し、ある程度の期間
安定していることが最も重要視される。しかるに、ツェ
インの製造に関する従来法は、原料からのツェインの回
収率を高めることを第一の目的としたものであり、これ
までの製品にはエタール可溶性において、満足できるも
のはなかった。すなわち、ツェインの標品を20倍量の6
0,80及び90%(v/v)の各エタール溶液に分散・溶解さ
せて観察した場合、従来法で製造したものは、よく分散
したように見えても一日放置すると沈澱が折出する等、
いずれも溶解性に乏しいものであった。用途にもよるが
薬剤コーティング用に使用するものであっては、そのア
ルコール溶液が少なくとも一昼夜完全に清澄な状態を維
持することが望まれている。
In applications such as coating materials for foods and tablets, zein is most importantly required to be soluble in ethanol, that is, dissolved in various concentrations of etal and stable for a certain period of time. However, the conventional method for producing zein has the first purpose of increasing the recovery rate of zein from the raw materials, and no etal-soluble products have been satisfactory so far. In other words, the standard of zein is 20 times the amount of 6
When observed by dispersing and dissolving in 0,80 and 90% (v / v) of each etal solution, the product produced by the conventional method appears to be well dispersed, but the precipitates appear when left for a day. etc,
All had poor solubility. For use as a drug coating, depending on the application, it is desired that the alcohol solution be kept completely clear for at least one day and night.

〔問題点を解決するための手段〕[Means for solving problems]

本発明は、ツェインの原料からの回収率を高水準に維持
し、かつ、エタールへの溶解性が極めて良好なツェイン
を取得する方法を提供するものである。
The present invention provides a method for maintaining a high level of recovery of zein from a raw material and obtaining zein having extremely good solubility in etal.

本発明は、とうもろこしまたはコーングルテンミールか
ら含水エタノールを用いてツェインを抽出、分離するツ
ェインの製造法において、抽出液のpHを8〜10に維持し
つつ抽出を行うことを特徴とするツェインの製造法であ
る。また、上記による抽出液を固形物濃度20〜50%にま
で濃縮し、これを水に加えて沈澱するツェインを分離、
回収するときは、特に臭い,色調の良好な製品が得られ
る。
The present invention is a method for producing zein in which zein is extracted and separated from corn or corn gluten meal using hydrous ethanol, and the zein is extracted while maintaining the pH of the extract at 8 to 10. Is the law. In addition, the extract according to the above is concentrated to a solid concentration of 20 to 50%, and this is added to water to separate precipitated zein,
When recovered, a product with particularly good odor and color tone is obtained.

本発明の出発原料の一つであるコーングルテンミールと
は、とうもろこしから通常の湿式処理法によりコーンス
ターチを分離製造する工程で副産物として得られるもの
である。出発原料にとうもろこしを使用する場合は、80
〜100メッシュ以下に粉砕して用いるのがよい。
Corn gluten meal, which is one of the starting materials of the present invention, is obtained as a by-product in the process of separating and producing corn starch from corn by a conventional wet treatment method. 80 if using corn as the starting material
It is recommended to pulverize to 100 mesh or less before use.

本発明においては、まず、これらの原料を60〜90%(v/
v)の含水エタールを用いて抽出する。該抽出工程は、
原料の3〜10倍相当量の上記含水エタールを用い、50〜
65℃で30〜180分間、攪拌しつつ行うが、抽出の全過程
を通して抽出液のpHを8〜10に維持することが必須であ
る。例えばグルテンミールを5倍量の90%(v/v)の含
水エタノールを用いて60℃で2時間抽出すると、抽出液
のpHは初発の6.4から5.2程度にまで、また当初の抽出液
を水酸化ナトリウム等のアルカリ剤でpH8に調整してお
いても、同様に5.2程度にまで低下する。
In the present invention, first, 60 to 90% (v /
Extract with the hydrous etal of v). The extraction step is
Using the water-containing etal in an amount equivalent to 3 to 10 times that of the raw material,
It is carried out at 65 ° C. for 30 to 180 minutes with stirring, but it is essential to maintain the pH of the extract at 8 to 10 throughout the whole extraction process. For example, when gluten meal is extracted with 5 times the volume of 90% (v / v) hydrous ethanol at 60 ° C for 2 hours, the pH of the extract is from the initial 6.4 to 5.2, and the initial extract is water. Even if the pH is adjusted to 8 with an alkaline agent such as sodium oxide, it will also drop to about 5.2.

本発明ではpHの自動測定機構とこれに連動するアルカリ
剤自動添加機構を備えたpHスタット装置を作動させる等
の方法を適宜適用して、抽出液のpHを絶えず8〜10に維
持して行うものである。抽出液のpHが8以下に低下する
と、それから調製したツェインのエタールへの溶解性が
著しく低下し、しかも原料に対するツェインの収率も低
下することとなる。また、抽出液のpHを10以上に高めて
も、抽出率の上昇は殆どなく、かえってツェインの好ま
しくない分解反応等を引き起こす可能性もあり、不利で
ある。
In the present invention, a method such as operating a pH stat device equipped with an automatic pH measuring mechanism and an alkaline agent automatic adding mechanism that works in conjunction with the method is appropriately applied to continuously maintain the pH of the extract at 8-10. It is a thing. When the pH of the extract is lowered to 8 or less, the solubility of zein prepared from it in etal is remarkably lowered, and further, the yield of zein with respect to the raw materials is lowered. Further, even if the pH of the extract is increased to 10 or higher, the extraction rate hardly increases, which may cause an undesirable decomposition reaction of zein, which is disadvantageous.

所定時間抽出を行った後、遠心分離,加圧濾過等の適宜
の手段により抽出液を得る。
After extraction for a predetermined time, an extract is obtained by an appropriate means such as centrifugation or pressure filtration.

上記により得られた抽出液からは、エタールを蒸留して
除去する、必要に応じ濃縮した後、水または中性の塩類
溶液中に滴下してツェインを沈澱させる等の公知の方法
によりツェインを回収することができる。
From the extract obtained as described above, zein is recovered by a known method such as removing etal by distillation, concentrating it if necessary, and then dropping it into water or a neutral salt solution to precipitate zein. can do.

ツェインの回収手段として、上記抽出液を固形物濃度20
〜50%程度にまで濃縮し、これを水(濃縮液の概ね6倍
量以上)に加えて生じた沈澱を採取するならば、臭いや
着色の少ない高品位のツェインが取得できるので特に有
利である。なお、この方法により臭いや着色の少ないツ
ェインを得るには、前段の抽出段階で抽出液のpHを8〜
10に維持しつつ行うことが必要であり、他の方法による
抽出液からは、かかる高品位のツェインを取得すること
ができない。
As a means of recovering zein, the above-mentioned extract was added to the solids concentration 20
It is especially advantageous if it is concentrated to about 50% and the precipitate formed by adding this to water (approximately 6 times the amount of the concentrated solution or more) is obtained because high-quality zein with little odor or coloration can be obtained. is there. In order to obtain zein with little odor and coloration by this method, the pH of the extract is adjusted to 8 ~
It is necessary to maintain the temperature at 10, and it is not possible to obtain such high-quality zein from an extract obtained by another method.

〔実施例〕〔Example〕

例1 グルテンミール100gに90%(v/v)含水エタノール500ml
を加え、60℃で2時間抽出した。抽出液のpHはpHスタッ
ト装置を用いて1N水酸化ナトリウムを間歇的に添加し、
抽出の全期間を通じ8.0〜8.5の範囲となるよう調整し
た。経時後、遠心分離により抽出液を得、これを濃縮、
乾燥して蛋白純度88.2%のツェインを24.8%(W)(対
原料%)の収率で得る。
Example 1 500 g of 90% (v / v) hydrous ethanol in 100 g of gluten meal
Was added and the mixture was extracted at 60 ° C. for 2 hours. The pH of the extract is intermittently added with 1N sodium hydroxide using a pH stat device,
Adjusted to be in the range of 8.0-8.5 throughout the extraction period. After a lapse of time, an extract was obtained by centrifugation and concentrated,
By drying, zein having a protein purity of 88.2% is obtained with a yield of 24.8% (W) (% of raw material).

例2 グルテンミール100gに90%(v/v)含水エタノール500ml
を加え、60℃で2時間抽出し、この抽出液のpHはpHスタ
ット装置を用いて1N水酸化ナトリウムを間歇的に添加
し、抽出の全期間を通じて9.0〜9.5の範囲となるよう調
整した。経時後、遠心分離により抽出液を得、これを濃
縮、乾燥して蛋白純度88.1%のツェインを24.7%(W)
(対原料%)の収率で得る。
Example 2 500 ml of 90% (v / v) hydrous ethanol in 100 g of gluten meal
Was added for 2 hours at 60 ° C., and the pH of this extract was adjusted to 9.0-9.5 throughout the entire extraction period by intermittently adding 1N sodium hydroxide using a pH stat device. After the passage of time, an extract was obtained by centrifugation, concentrated and dried to give 24.7% (W) of zein with a protein purity of 88.1%.
Obtained in a yield of (% of raw material).

例3 グルテンミール100gに80%(v/v)含水エタノール500ml
を加え、60℃で2時間抽出した。抽出液のpHはpHスタッ
ト装置を用いて1N水酸化ナトリウムを間歇的に添加し、
抽出の全期間を通じて8.0〜8.5の範囲となるよう調整し
た。経時後、遠心分離により抽出液を得、これを濃縮、
乾燥して蛋白純度87.2%のツェインを27.2%(W)(対
原料%)の収率で得る。
Example 3 100 ml of gluten meal 500 ml of ethanol containing 80% (v / v)
Was added and the mixture was extracted at 60 ° C. for 2 hours. The pH of the extract is intermittently added with 1N sodium hydroxide using a pH stat device,
It was adjusted to be in the range of 8.0 to 8.5 throughout the extraction period. After a lapse of time, an extract was obtained by centrifugation and concentrated,
By drying, zein having a protein purity of 87.2% is obtained in a yield of 27.2% (W) (% of raw material).

例4 グルテンミール100gに70%(v/v)含水エタノール500ml
を加え、60℃で2時間抽出した。抽出液のpHはpHスタッ
ト装置を用いて1N水酸化ナトリウムを間歇的に添加し、
抽出の全期間を通じ8.0〜8.5の範囲となるよう調整し
た。経時後、遠心分離により抽出液を得、これを濃縮、
乾燥して蛋白純度87.3%のツェインを27.3%(W)(対
原料%)の収率で得る。
Example 4 500 ml of 70% (v / v) hydrous ethanol in 100 g of gluten meal
Was added and the mixture was extracted at 60 ° C. for 2 hours. The pH of the extract is intermittently added with 1N sodium hydroxide using a pH stat device,
Adjusted to be in the range of 8.0-8.5 throughout the extraction period. After a lapse of time, an extract was obtained by centrifugation and concentrated,
By drying, zein having a protein purity of 87.3% is obtained with a yield of 27.3% (W) (% of raw material).

例5 グルテンミール100gに60%(v/v)含水エタノール500ml
を加え、60℃で2時間抽出した。抽出液のpHはpHスタッ
ト装置を用いて1N水酸化ナトリウムを間歇的に添加し、
抽出の全期間を通じ8.0〜8.5の範囲となるよう調整し
た。経時後、遠心分離により抽出液を得、これを濃縮、
乾燥して蛋白純度87.2%のツェインを29.2%(W)(対
原料%)の収率で得る。
Example 5 Gluten meal 100 g, 60% (v / v) hydrous ethanol 500 ml
Was added and the mixture was extracted at 60 ° C. for 2 hours. The pH of the extract is intermittently added with 1N sodium hydroxide using a pH stat device,
Adjusted to be in the range of 8.0-8.5 throughout the extraction period. After a lapse of time, an extract was obtained by centrifugation and concentrated,
By drying, zein having a protein purity of 87.2% is obtained with a yield of 29.2% (W) (% of raw material).

例6 グルテンミール100gに90%(v/v)含水エタノール500ml
を加え、60℃で2時間抽出した。抽出液のpHはpHスタッ
ト装置を用いて1N水酸化ナトリウムを間歇的に添加し、
抽出の全期間を通じ8.0〜8.5の範囲となるよう調整し
た。経時後、遠心分離により抽出液を得、これを固形分
20%になるよう濃縮縮する。この濃縮液を10倍量の冷水
中に滴下してツェインを沈澱させ、遠心分離により回収
し、真空乾燥すると蛋白純度97.8%のツェインを15.7%
(W)(対原料%)の収率で得る。
Example 6 500g of 90% (v / v) hydrous ethanol in 100g of gluten meal
Was added and the mixture was extracted at 60 ° C. for 2 hours. The pH of the extract is intermittently added with 1N sodium hydroxide using a pH stat device,
Adjusted to be in the range of 8.0-8.5 throughout the extraction period. After a lapse of time, an extract was obtained by centrifugation,
Concentrate and shrink to 20%. This concentrate was added dropwise to 10 times the amount of cold water to precipitate zein, which was recovered by centrifugation and dried in vacuum to give 15.7% zein with a protein purity of 97.8%.
Obtained in a yield of (W) (% of raw material).

例7 グルテンミール100gに90%(v/v)含水エタノール500ml
を加え、60℃で2時間抽出した。抽出液のpHはpHスタッ
ト装置を用いて1N水酸化ナトリウムを間歇的に添加し、
抽出の全期間を通じ9.0〜9.5の範囲となるよう調整し
た。経時後、遠心分離により抽出液を得、これを固形分
20%になるよう濃縮する。この濃縮液を10倍量の冷水中
に滴下してツェインを沈澱させ、遠心分離により蛋白純
度98.2%のツェインを16.3%(W)(対原料%)の収率
で得る。
Example 7 Gluten meal 100 g, 90% (v / v) hydrous ethanol 500 ml
Was added and the mixture was extracted at 60 ° C. for 2 hours. The pH of the extract is intermittently added with 1N sodium hydroxide using a pH stat device,
It was adjusted to be in the range of 9.0 to 9.5 throughout the extraction period. After a lapse of time, an extract was obtained by centrifugation,
Concentrate to 20%. This concentrated solution was added dropwise to 10 times the amount of cold water to precipitate zein, and zein having a protein purity of 98.2% was obtained by centrifugation at a yield of 16.3% (W) (% of raw material).

例8 グルテンミール100gに80%(v/v)含水エタノール500ml
を加え、60℃で2時間抽出した。抽出液のpHはpHスタッ
ト装置を用いて1N水酸化ナトリウムを間歇的に添加し、
抽出の全期間を通じ8.0〜8.5の範囲となるよう調整し
た。経時後、遠心分離により抽出液を得、これを固形分
20%になるよう濃縮する。この濃縮液を10倍量の冷水中
に滴下してツェインを沈澱させ、遠心分離により回収
し、真空乾燥すると蛋白純度96.8%のツェインを17.1%
(W)(対原料%)の収率で得る。
Example 8 500 ml of 80% (v / v) hydrous ethanol in 100 g of gluten meal
Was added and the mixture was extracted at 60 ° C. for 2 hours. The pH of the extract is intermittently added with 1N sodium hydroxide using a pH stat device,
Adjusted to be in the range of 8.0-8.5 throughout the extraction period. After a lapse of time, an extract was obtained by centrifugation,
Concentrate to 20%. This concentrate was added dropwise to 10 times the amount of cold water to precipitate zein, which was recovered by centrifugation and dried in vacuum to give 17.1% zein with 96.8% protein purity.
Obtained in a yield of (W) (% of raw material).

例9 グルテンミール100gに70%(v/v)含水エタノール500m
を加え、60℃で2時間抽出した。抽出液のpHはpHスタッ
ト装置を用いて1N水酸化ナトリウムを間歇的に添加し、
抽出の全期間を通じ8.0〜8.5の範囲となるよう調整し
た。経時後、遠心分離により抽出液を得、これを固形分
20%になるよう濃縮する。この濃縮液を10倍量の冷水中
に滴下してツェインを沈澱させ、遠心分離により蛋白純
度97.2%のツェインを18.2%(W)(対原料%)の収率
で得る。
Example 9 Gluten meal 100 g, 70% (v / v) hydrous ethanol 500 m
Was added and the mixture was extracted at 60 ° C. for 2 hours. The pH of the extract is intermittently added with 1N sodium hydroxide using a pH stat device,
Adjusted to be in the range of 8.0-8.5 throughout the extraction period. After a lapse of time, an extract was obtained by centrifugation,
Concentrate to 20%. This concentrated solution was dropped into 10 times the amount of cold water to precipitate zein, and zein having a protein purity of 97.2% was obtained by centrifugation at a yield of 18.2% (W) (% of raw material).

例10 グルテンミール100gに60%(v/v)含水エタノール500ml
を加え、60℃で2時間抽出した。抽出液のpHはpHスタッ
ト装置を用いて1N水酸化ナトリウムを間歇的に添加し、
抽出の全期間を通じ8.0〜8.5の範囲となるよう調整し
た。経時後、遠心分離により抽出液を得、これを固形分
20%になるよう濃縮する。この濃縮液を10倍量の冷水中
に滴下してツェインを沈澱させ、遠心分離により回収
し、真空乾燥すると蛋白純度96.5%のツェインを19.5%
(W)(対原料%)の収率で得る。
Example 10 500 g of water containing 60% (v / v) water in 100 g of gluten meal
Was added and the mixture was extracted at 60 ° C. for 2 hours. The pH of the extract is intermittently added with 1N sodium hydroxide using a pH stat device,
Adjusted to be in the range of 8.0-8.5 throughout the extraction period. After a lapse of time, an extract was obtained by centrifugation,
Concentrate to 20%. This concentrate was added dropwise to 10 times the amount of cold water to precipitate the zein, which was recovered by centrifugation and vacuum dried to yield 19.5% zein with a protein purity of 96.5%.
Obtained in a yield of (W) (% of raw material).

本発明の製法により得られたツェインは極めてアルコー
ル溶解性が優れていて、長時間放置しても安定な清澄状
態を維持し、更に着色,臭いの発生も生じない。
The zein obtained by the production method of the present invention has extremely excellent alcohol solubility, maintains a stable clear state even when left standing for a long time, and does not cause coloring or odor.

次に、これを明らかにする試験例を示す。Next, a test example for clarifying this will be shown.

試験例 1.供試試料 実施例1〜10の本発明の製法により得られたツェイン、
対照として下記製造例にり得られたツェインを用いた。
Test Example 1. Test sample Zein obtained by the manufacturing method of the present invention of Examples 1 to 10,
As a control, the zein obtained in the following production example was used.

製造例1 グルテンミール100gに90%(v/v)含水エタノール500ml
を加え、60℃で2時間抽出した。抽出液のpHは初発の6.
4から抽出末期には5.2まで低下した。経時後、遠心分離
により抽出液を得、これを濃縮、乾燥して蛋白純度87%
のツェインを得る。
Production Example 1 500g of 90% (v / v) hydrous ethanol in 100g of gluten meal
Was added and the mixture was extracted at 60 ° C. for 2 hours. The pH of the extract is 6.
It decreased from 4 to 5.2 at the end of extraction. After a lapse of time, an extract was obtained by centrifugation, concentrated and dried to a protein purity of 87%.
Get the zein of.

製造例2 製造例1と同様の原料を用い、60℃で2時間抽出した。
抽出液のpHはpHスタット装置を用いて1N水酸化ナトリウ
ムを間歇的に添加し、全期間を通じ7.0〜7.5の範囲とな
るよう調整して行って蛋白純度87.5%のツェインを得
る。
Production Example 2 Using the same raw material as in Production Example 1, extraction was performed at 60 ° C. for 2 hours.
The pH of the extract is intermittently added with 1N sodium hydroxide using a pH stat device and adjusted to be in the range of 7.0 to 7.5 throughout the period to obtain zein with a protein purity of 87.5%.

製造例3 製造例1と同様の原料を用い、抽出を80%(v/v)含水
エタノールを用い、抽出液のpHを抽出の全期間を通じ7.
0〜7.5の範囲となるよう調整した他は製造例2と同様の
操作で行い、蛋白純度87.0%のツェインを得る。
Production Example 3 The same raw material as in Production Example 1 was used, extraction was performed with 80% (v / v) hydrous ethanol, and the pH of the extract was adjusted throughout the entire extraction period.
A zein having a protein purity of 87.0% is obtained by the same procedure as in Production Example 2 except that the zein is adjusted to a range of 0 to 7.5.

製造例4 製造例1と同様の原料を用い、抽出を70%(v/v)含水
エタノールを用い、抽出液のpHを抽出の全期間を通じ7.
0〜7.5の範囲となるよう調整した他は製造例2と同様の
操作で行い、蛋白純度86.8%のツェインを得る。
Production Example 4 The same raw material as in Production Example 1 was used, extraction was performed with 70% (v / v) hydrous ethanol, and the pH of the extract was adjusted throughout the entire extraction period.
A zein having a protein purity of 86.8% is obtained by the same procedure as in Production Example 2 except that the zein is adjusted to a range of 0 to 7.5.

製造例5 製造例1と同様の原料を用い、抽出を60%(v/v)含水
エタノールを用い、抽出液のpHを抽出の全期間を通じ7.
0〜7.5の範囲となるよう調整した他は製造例2と同様の
操作で行い、蛋白純度86.9%のツェインを得る。
Production Example 5 The same raw material as in Production Example 1 was used, extraction was carried out with 60% (v / v) hydrous ethanol, and the pH of the extract was adjusted throughout the entire extraction period.
A zein having a protein purity of 86.9% is obtained by the same procedure as in Production Example 2 except that the zein is adjusted to have a range of 0 to 7.5.

製造例6 グルテンミール100gに90%(v/v)含水エタノール500ml
を加え、60℃で2時間抽出した。抽出液のpHは初発の6.
4から抽出末期には5.2まで低下した。経時後、遠心分離
により抽出液を得、これを固形分20%になるよう濃縮す
る。この濃縮液を10倍量の冷水中に滴下してツェインを
沈澱させ、真空乾燥すると蛋白純度91.3%のツェインを
得る。
Production Example 6 500 ml of 90% (v / v) hydrous ethanol in 100 g of gluten meal
Was added and the mixture was extracted at 60 ° C. for 2 hours. The pH of the extract is 6.
It decreased from 4 to 5.2 at the end of extraction. After a lapse of time, an extract is obtained by centrifugation and concentrated to a solid content of 20%. The concentrate is added dropwise to 10 times the amount of cold water to precipitate the zein, and dried in vacuum to obtain zein with a protein purity of 91.3%.

製造例7 製造例6と同様の原料を用い、60℃で2時間抽出した。
抽出液のpHはpHスタット装置を用いて1N水酸化ナトリウ
ムを間歇的に添加し、抽出の全期間を通じ7.0〜7.5の範
囲となるよう調整して行って蛋白純度92.1%のツェイン
を得る。
Production Example 7 Using the same raw material as in Production Example 6, extraction was performed at 60 ° C. for 2 hours.
The pH of the extract is intermittently added with 1N sodium hydroxide using a pH stat device and adjusted so as to be in the range of 7.0 to 7.5 throughout the extraction period to obtain zein having a protein purity of 92.1%.

製造例8 製造例6と同様の原料を用い、抽出を80%(v/v)含水
エタノールを用い、製造例7に準じて抽出液のpHを抽出
の全期間を通じ7.0〜7.5の範囲となるよう調整して行っ
て蛋白純度91.6%のツェインを得る。
Production Example 8 The same raw material as in Production Example 6 was used, extraction was performed with 80% (v / v) hydrous ethanol, and the pH of the extract was adjusted to 7.0 to 7.5 throughout the entire extraction period according to Production Example 7. Zein with a protein purity of 91.6% is obtained.

製造例9 製造例6と同様の原料を用い、抽出を70%(v/v)含水
エタノールを用い、抽出液のpHを抽出の全期間を通じ7.
0〜7.5の範囲となるよう調整した他は製造例7と同様の
操作で行い、蛋白純度90.3%のツェインを得る。
Production Example 9 The same raw material as in Production Example 6 was used, extraction was performed with 70% (v / v) hydrous ethanol, and the pH of the extract was adjusted throughout the entire extraction period.
A zein having a protein purity of 90.3% is obtained by the same procedure as in Production Example 7, except that the zein is adjusted to have a range of 0 to 7.5.

2.試験方法 上記各供試試料1gを20倍量の60%(v/v),80%(v/v),
90%(v/v)の各含水エタノールに分散、溶解し、その
直後と25℃で24時間経過後の状態を観察した。
2. Test method 1 g of each sample above is 20% volume 60% (v / v), 80% (v / v),
It was dispersed and dissolved in 90% (v / v) water-containing ethanol, and the state immediately after that and after 24 hours at 25 ° C was observed.

なお、実施例6〜10で得られたツェイン、製造例6〜9
で得られたツェインについては、色,臭いについても観
察した。
In addition, zein obtained in Examples 6 to 10 and Production Examples 6 to 9
The zein obtained in 1. was also observed for color and odor.

3.試験結果 試験結果を下記表により示す。3. Test results The test results are shown in the table below.

表1に明らかなように、本発明によりツェインを抽出液
のpHを8〜10に維持しつつ抽出したものでは、抽出エタ
ールの濃度が60〜90%(v/v)の範囲のいずれもが、60,
80および90%(v/v)の試験した総ての濃度のエタール
に対して優れた溶解性を示し、薬剤コーティング等の用
途に適するものであった。これに対し、pH調整を行わな
かったもの、および抽出をpH8以下で行ったものでは、
いずれも溶解性が劣っており、上記目的に適合するもの
ではなかった。
As is clear from Table 1, in the case where zein was extracted according to the present invention while maintaining the pH of the extract at 8 to 10, the concentration of the extracted etal was in the range of 60 to 90% (v / v). , 60,
It showed excellent solubility for all tested concentrations of etal at 80 and 90% (v / v), making it suitable for applications such as drug coating. On the other hand, in those without pH adjustment and with extraction at pH 8 or less,
All of them had poor solubility and were not suitable for the above purpose.

表2より明らかなように、本発明によりツェインを抽出
液のpHを8〜10に維持しつつ抽出したものでは前項同様
に含水エタノールに対する優れた溶解性を有するととも
に、水による沈澱時に色素や有臭成分等の不純物が水に
溶解して除去されるので、色相が淡く臭いも少ない高品
位のツェインを得ることができる。これに対しpH調整を
行なわなかったもの、および抽出をpH8以下で行ったも
のでは、溶解性ばかりでなく、色素や有臭成分の除去で
も劣るものであった。
As is clear from Table 2, zein extracted according to the present invention while maintaining the pH of the extract at 8 to 10 has excellent solubility in hydrous ethanol as in the previous section, and also has no dye or pigment during precipitation with water. Since impurities such as odor components are dissolved and removed in water, it is possible to obtain high-quality zein having a light hue and a small odor. On the other hand, in the case where the pH was not adjusted and the case where the extraction was performed at a pH of 8 or less, not only the solubility but also the removal of the pigment and the odorous component were poor.

〔発明の効果〕〔The invention's effect〕

本発明によれば、薬剤・食品等のコーティング剤として
好適な、特にエタールへの溶解性が大きく、かつ、着
色,臭いのないツェインを経済的に製造することができ
る。もちろん、本発明によるツェインは、他にも工業用
材料,製菓材料等としても使用可能な、利用用途の広い
ものである。
According to the present invention, it is possible to economically produce zein, which is suitable as a coating agent for medicines, foods, etc., has particularly high solubility in etal, and has no coloration or odor. Of course, the zein according to the present invention can be used as an industrial material, a confectionery material, etc., and has a wide range of applications.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】とうもろこしまたはコーングルテンミール
から含水エタノールを用いてツェインを抽出、分離する
ツェインの製造法において、抽出液のpHを8〜10に維持
しつつ抽出を行うことを特徴とするツェインの製造法。
1. A method for producing zein in which zein is extracted and separated from corn or corn gluten meal using hydrous ethanol, wherein the zein is extracted while maintaining the pH of the extract at 8 to 10. Manufacturing method.
【請求項2】とうもろこしまたはコーングルテンミール
から含水エタノールで抽出液のpHを8〜10に維持しつつ
抽出して得た抽出液を固形物濃度が20〜50%となるまで
濃縮し、これを水に加えて沈澱したツェインを分離、回
収する特許請求の範囲第1項記載のツェインの製造法。
2. An extract obtained by extraction from corn or corn gluten meal with hydrous ethanol while maintaining the pH of the extract at 8 to 10 is concentrated to a solid concentration of 20 to 50%. The method for producing zein according to claim 1, wherein the zein precipitated in addition to water is separated and recovered.
JP1691087A 1987-01-26 1987-01-26 Twain manufacturing method Expired - Fee Related JPH0725797B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1691087A JPH0725797B2 (en) 1987-01-26 1987-01-26 Twain manufacturing method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1691087A JPH0725797B2 (en) 1987-01-26 1987-01-26 Twain manufacturing method

Publications (2)

Publication Number Publication Date
JPS63185999A JPS63185999A (en) 1988-08-01
JPH0725797B2 true JPH0725797B2 (en) 1995-03-22

Family

ID=11929292

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1691087A Expired - Fee Related JPH0725797B2 (en) 1987-01-26 1987-01-26 Twain manufacturing method

Country Status (1)

Country Link
JP (1) JPH0725797B2 (en)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3091515B2 (en) * 1991-04-23 2000-09-25 昭和産業株式会社 Processing method for materials containing zein
JP3153311B2 (en) * 1992-01-16 2001-04-09 昭和産業株式会社 Purification method of zein
JP2772213B2 (en) * 1992-12-25 1998-07-02 昭和産業株式会社 How to make Zein
JP6507561B2 (en) * 2014-10-22 2019-05-08 株式会社サタケ Method of recovering protein contained in rice
CA3018218C (en) 2016-03-24 2024-01-09 Cargill, Incorporated Corn protein product having decreased free sulfite levels & method for manufacturing same
CA3037843A1 (en) 2016-09-23 2018-03-29 Cargill, Incorporated Corn protein retention during extraction
MX2020001301A (en) 2017-08-02 2020-03-12 Cargill Inc Extruded corn protein material.
CN111132557B (en) 2017-09-21 2023-06-30 嘉吉公司 Corn protein retention during extraction

Also Published As

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