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JPH1118687A - Manufacturing method of soy protein material with excellent solubility - Google Patents

Manufacturing method of soy protein material with excellent solubility

Info

Publication number
JPH1118687A
JPH1118687A JP17822197A JP17822197A JPH1118687A JP H1118687 A JPH1118687 A JP H1118687A JP 17822197 A JP17822197 A JP 17822197A JP 17822197 A JP17822197 A JP 17822197A JP H1118687 A JPH1118687 A JP H1118687A
Authority
JP
Japan
Prior art keywords
protein
soybean protein
caseinate
solution
soy protein
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
JP17822197A
Other languages
Japanese (ja)
Other versions
JP3381558B2 (en
Inventor
Masahiko Samoto
将彦 佐本
Masami Fukase
真美 深瀬
Takeshi Akasaka
武志 赤坂
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.)
Fuji Oil Co Ltd (fka Fuji Oil Holdings Inc)
Original Assignee
Fuji Oil 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 Fuji Oil Co Ltd filed Critical Fuji Oil Co Ltd
Priority to JP17822197A priority Critical patent/JP3381558B2/en
Publication of JPH1118687A publication Critical patent/JPH1118687A/en
Application granted granted Critical
Publication of JP3381558B2 publication Critical patent/JP3381558B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

(57)【要約】 【課題】水或いは塩水に対し、高い溶解性及びその保存
性を示す粉末状大豆タンパク質を製造すること。 【解決手段】大豆タンパク質にカゼイネート、炭水化物
を加えた溶液に、好ましくはリン酸塩を加えて、加熱処
理し、均質化処理し、乾燥することにより上記の課題を
解決したものである。この粉末状大豆タンパク質は、乾
燥物として粉末の重量基準で、大豆タンパク質50〜80重
量% 、カゼイネート5 〜50重量% 、炭水化物 0〜45重量
% 、及び燐酸塩 0〜20重量% を含有することを特徴とす
る粉末状大豆タンパク質である。
(57) [Problem] To produce a powdery soybean protein having high solubility and storage stability in water or salt water. SOLUTION: This problem is solved by adding a phosphate to a solution obtained by adding a caseinate and a carbohydrate to a soybean protein, heating, homogenizing, and drying the solution. This powdered soy protein is 50 to 80% by weight of soy protein, 5 to 50% by weight of caseinate, and 0 to 45% of carbohydrate on a dry basis based on the weight of the powder.
% Soybean protein, and 0 to 20% by weight of a phosphate.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、加工及び保存に対
して水または塩水に対して高い溶解性を保持する大豆タ
ンパク質素材の製造法に関する。
[0001] The present invention relates to a method for producing a soybean protein material having high solubility in water or salt water for processing and storage.

【0002】[0002]

【従来の技術】従来、市販の分離大豆タンパク質等、粉
末状大豆タンパク質は、動物タンパク質であるカゼイネ
ート、卵白、ホエータンパク質、プラズマタンパク質等
の粉末製剤に比べて、水、特に塩水に対する溶解性が低
い傾向にある。すなわち、市販の分離大豆タンパク質
は、殺菌のために、加熱され、スプレードライによって
乾燥され、パウダーとして保存されるが、この際、加熱
・スプレードライ時のタンパク質濃度に依存した、ある
いは、保存条件( 温度・湿度・時間)に依存した重合が
原因となり、タンパク質粒子が巨大化し、水、特に塩水
に対する溶解性が減少すると考えられる。特に6%以上
の高濃度タンパク質溶液をスプレードライしたり、粉末
化後の保存が高温、高湿下に長時間行われるとこの傾向
が顕著になる。
2. Description of the Related Art Conventionally, powdery soybean protein such as commercially available isolated soybean protein has lower solubility in water, particularly in salt water, than powdered preparations of animal proteins such as caseinate, egg white, whey protein and plasma protein. There is a tendency. That is, commercially available isolated soybean protein is heated for sterilization, dried by spray-drying, and stored as a powder.In this case, depending on the protein concentration during heating and spray-drying, or under storage conditions ( It is considered that the polymerization depending on (temperature / humidity / time) causes the protein particles to become large and the solubility in water, particularly in salt water, to decrease. In particular, this tendency becomes remarkable when a protein solution having a high concentration of 6% or more is spray-dried or stored after powdering for a long time under high temperature and high humidity.

【0003】特に塩水に対する溶解性が低い大豆タンパ
ク質を、塩を含んだ練り生地や溶液(例えばソーセージ
やハムピックル液)に対して添加すると沈澱物の発生や
最終製品の滑らかさが低下することがある。また、大豆
タンパク質に求められる機能として、ゲル形成性、結着
性、保水性等が上げられるが、溶解性が悪いと少なから
ずこれらの性質の低下が起こるという問題がある。
[0003] In particular, when a soybean protein having low solubility in salt water is added to a dough or solution containing salt (eg, sausage or ham pickle solution), precipitates may be generated and the smoothness of the final product may be reduced. . In addition, functions required for soybean protein include gel-forming property, binding property, water retention, and the like, but there is a problem that if the solubility is poor, these properties are considerably reduced.

【0004】本発明では、大豆タンパク質に対してカゼ
イネートを加配し、均質化溶液にして、加熱後、乾燥す
ることにより、加工工程・保存中の溶解性低下が防止で
きる知見を得た。本出願人は、大豆タンパク質にカゼイ
ネートあるいはカゼインを加配することで溶解性を高め
ることを提案していた( 特開昭62−6656号) 。しかし、
カゼイネートだけで加工中・保存中の溶解性低下を防止
するためには、大豆タンパク質に対してかなりの量が必
要であり、大豆タンパク質のゲル形成性が活かせない可
能性があった。そこで、大豆タンパク質に対する非大豆
タンパク質成分を少ない量で充分な溶解性の改善・維持
を実現させる為に種々検討した結果、カゼイネートある
いはカゼインをデキストリン等の炭水化物と併用するこ
と、好ましくは、更に均質化処理を施すことが有効であ
る知見を得た。
In the present invention, it has been found that a caseinate is added to a soybean protein to form a homogenized solution, which is then heated and dried to prevent a decrease in solubility during processing and storage. The present applicant has proposed increasing the solubility by adding caseinate or casein to soybean protein (Japanese Patent Application Laid-Open No. 62-6656). But,
In order to prevent a decrease in solubility during processing or storage with caseinate alone, a considerable amount is required for soy protein, and the gel-forming properties of soy protein may not be utilized. Therefore, as a result of various studies for realizing a sufficient improvement and maintenance of the solubility of the non-soy protein component with respect to the soy protein in a small amount, caseinate or casein was used in combination with a carbohydrate such as dextrin, and more preferably, We found that it is effective to apply treatment.

【0005】その他、大豆タンパク質と他成分を併用
し、均質化される乾燥粉末素材としては、コーヒーホワ
イトナーの起泡剤として大豆タンパク質を少量用いるこ
とが知られており、その際大豆タンパク質とカゼイネー
トを併用することにより起泡性と泡の保持性を向上させ
ること等は知られている( 特開平6-30698 号) が、コー
ヒーホワイトナーは脂肪や炭水化物を圧倒的成分とする
もので、ゲル形成性、結着性、保水性を求められるタン
パク質素材とは凡そ異なるものであった。
[0005] In addition, as a dry powder material that is used in combination with soy protein and other components, it is known that a small amount of soy protein is used as a foaming agent for coffee whitener, in which case the soy protein and caseinate are used. It is known to improve the foaming property and the foam retention property by using in combination (Japanese Unexamined Patent Publication No. 6-30698) .However, coffee whitener uses fat and carbohydrate as overwhelming components, It was almost different from a protein material required for formability, binding property and water retention.

【0006】また、豆乳又は分離大豆タンパク質の水溶
液にリン酸塩と、カゼイン、カゼイン塩、或いはカゼイ
ン主体複合物を併用添加した後、均質化処理と凝固剤添
加をいずれかの順で添加して充填容器に充填し、密封後
加熱凝固させる充填豆腐の製造法が知られている( 特開
昭61-19463号) が、充填豆腐は、ゲル形成性、結着性、
保水性を求められるタンパク質素材を得ること、或いは
その溶解性を改善することと何の関係も無い。
Further, a phosphate and a casein, a caseinate, or a casein-based complex are added to an aqueous solution of soymilk or an isolated soybean protein in combination, followed by homogenization and addition of a coagulant in any order. A method for producing a filled tofu, which is filled in a filling container, and then heat-coagulated after sealing, is known (Japanese Patent Application Laid-Open No. 61-19463), but filled tofu is gel-forming, binding,
It has nothing to do with obtaining a protein material that requires water retention or improving its solubility.

【0007】[0007]

【発明が解決しようとする課題】この発明は、ゲル形成
性、結着性、保水性といった大豆タンパク質に求められ
る機能を基本的に保持したままで水または塩水に対する
溶解性が改善・維持される乾燥タンパク質素材を得るこ
とを課題とする。従来の方法では解決されていない課
題、即ち6%以上の高濃度のタンパク質溶液を殺菌加熱
後、スプレードライして製造した粉末状大豆タンパク質
を高温・高湿度下に保存すると、水、特に塩水に対して
溶解しないか或いは溶解しずらい現象を大幅に改善する
ことが課題である。
SUMMARY OF THE INVENTION According to the present invention, the solubility in water or salt water is improved and maintained while basically maintaining the functions required for soybean proteins such as gel-forming properties, binding properties and water retention. It is an object to obtain a dried protein material. Problems that have not been solved by the conventional method, namely, sterilizing and heating a protein solution having a high concentration of 6% or more and then spray-drying the powdered soybean protein produced at high temperature and high humidity, the water, especially salt water, On the other hand, it is an object to greatly improve the phenomenon of not dissolving or hardly dissolving.

【0008】[0008]

【課題を解決するための手段】本発明は、大豆タンパク
質にカゼイン或いはカゼイネート、炭水化物を混合し、
殺菌のための加熱、その前後の均質化、その後にスプレ
ードライすることで、課題の溶解性が高くなり改善され
る。但し、この際の粉末状大豆タンパク質の持つゲル形
成性や結着性、保水性等の機能性の発揮を目的とした場
合、大豆タンパク質以外の物質の添加量が多過ぎると逆
に機能の低下を招くので、大豆タンパク質以外の物質の
添加量は、乾燥重量当たり、大豆たん白質の同量以下が
好ましい。
SUMMARY OF THE INVENTION The present invention provides a method for mixing soybean protein with casein, caseinate, or carbohydrate,
Heating for sterilization, homogenization before and after that, and then spray-drying increase and improve the problem of solubility. However, when the purpose is to exhibit the gel-forming properties, binding properties, and water retention properties of the powdery soy protein at this time, if the amount of the substance other than the soy protein is too large, the function will be deteriorated. Therefore, the amount of the substance other than the soy protein is preferably equal to or less than the amount of the soy protein per dry weight.

【0009】分離大豆タンパク質の原料として使用する
形態は豆乳、酸沈カード、カードの中和液など大豆たん
白質の含有量を高めたものであれば特に限定しない。但
し、7S、11Sグロブリンの純度( 通常分離大豆タン
パク質の70%)が高く、大豆のマイナーなタンパク質やタ
ンパク質以外の不純物の含有量が低い方が粉末状大豆タ
ンパク質の機能上、より好ましい。
The form used as the raw material of the isolated soybean protein is not particularly limited as long as the content of soybean protein such as soymilk, acid precipitated curd, and a neutralized solution of curd is increased. However, the higher the purity of 7S and 11S globulin (usually 70% of the isolated soy protein) and the lower the content of minor proteins and impurities other than proteins are more preferable from the viewpoint of the function of the powdery soy protein.

【0010】蒸気吹き込みによる直接加熱方式である
か、間接加熱方式であるかといった加熱の形式は特に限
定しない。温度は50〜160 ℃、1 時間〜5 秒の間で行
い、加熱殺菌が行われればよい。上記の温度下で高圧ホ
モゲナイザーによる均質化の処理(以下、単に均質化又
は均質化処理と言う)を行うことが重要であり、場合に
よっては、加熱の前、あるいは加熱中、あるいは加熱
後、あるいはこれらを組合せて行うことができる。
There is no particular limitation on the type of heating, such as whether it is a direct heating system by steam injection or an indirect heating system. The temperature may be 50 to 160 ° C. for 1 hour to 5 seconds, and heat sterilization may be performed. It is important to perform the homogenization treatment with the high-pressure homogenizer at the above temperature (hereinafter, simply referred to as homogenization or homogenization treatment). In some cases, before or during heating, or after heating, or These can be performed in combination.

【0011】大豆タンパク質の変性温度を越える80℃
以上の温度を維持して均質化を行うことで、タンパク質
間の相互作用が起こりやすい為か、少ないカゼイネート
の量でも溶解性の向上・保持に効果がある。均質化の圧
力は50〜500kg/cm2 で1パス〜3パス(通過
させること。以下、同じ)の処理を行うのが好ましい。
80 ° C. above the denaturation temperature of soy protein
Performing homogenization while maintaining the above temperature is likely to cause an interaction between proteins, and is effective in improving and maintaining solubility even with a small amount of caseinate. The homogenizing pressure is preferably 50 to 500 kg / cm 2 , and it is preferable to perform 1 to 3 passes (passing; the same applies hereinafter).

【0012】カゼイネート或いはカゼインの添加量は、
大豆タンパク質に対し、5〜50%、好ましくは10〜
30%を使用する。少なすぎると効果が無く、多すぎる
とゲル形成能などの低下を招く。
The amount of caseinate or casein added is as follows:
5 to 50%, preferably 10 to 50% of soy protein
Use 30%. If the amount is too small, there is no effect, and if the amount is too large, the gel forming ability and the like are lowered.

【0013】一方、炭水化物とりわけ糖類の添加量は、
大豆タンパク質に対し、5〜100%好ましくは15〜
50%であり、種類は特に限定しないが、DE=20〜
40のデキストリンが好ましい。DEとはデキストロー
ズエキーバレントの意味で以下、DEと略称する。
On the other hand, the amount of carbohydrates, especially saccharides,
5 to 100%, preferably 15 to 100%
50%, the type is not particularly limited, but DE = 20 to
Forty dextrins are preferred. DE means Dextrose Equivalent, and is abbreviated as DE hereinafter.

【0014】リン酸塩を使用する場合は、大豆タンパク
質に対し、1〜30%好ましくは5〜10%、種類は特
に限定しないが、ヘキサメタリン酸塩、ピロリン酸塩、
ポリリン酸塩等が良い。効果としては、保存中の経時的
溶解性の悪化防止の助長効果と微酸性側の溶解性向上効
果を発揮する。
When a phosphate is used, it is 1-30%, preferably 5-10%, based on soybean protein, and the type thereof is not particularly limited, but hexametaphosphate, pyrophosphate,
Polyphosphate and the like are good. As effects, it has the effect of promoting the deterioration of solubility over time during storage and the effect of improving solubility on the slightly acidic side.

【0015】これらの大豆タンパク質に加配する物質
は、均質化後の大豆タンパク質溶液を噴霧乾燥した後に
加えたのでは、溶解性の向上や保持に関して効果は無
い。互いに溶解した状態で、加熱・均質化処理すること
で、何らかの相互作用が起こり、溶解性の低下が防止さ
れると考えられる。
If these substances added to soybean protein are added after the soybean protein solution after homogenization is spray-dried, there is no effect on the improvement and retention of solubility. It is considered that by performing the heating and homogenizing treatment in a state of being dissolved in each other, some kind of interaction occurs and a decrease in solubility is prevented.

【0016】[0016]

【実施例】以下、実施例により本発明の実施様態を具体
的に説明する。ただし、本発明はこれらの実施例にその
技術範囲が限定されるものではない。
The embodiments of the present invention will be specifically described below with reference to examples. However, the technical scope of the present invention is not limited to these examples.

【0017】実施例1 脱脂大豆に15重量倍の水を加え、水酸化ナトリウムで中
性にpHを調整し、攪拌抽出した豆乳を、塩酸でpH4.8 に
して大豆タンパク質を沈殿させ、遠心分離後、沈殿物で
ある大豆タンパク質(酸沈カードとも言う)を回収し
た。これを水酸化ナトリウムで中和して、8%の大豆タ
ンパク質中和液を調製した。この溶液に大豆タンパク質
100 部に対し、20部のカゼイネート、及び30部のデキス
トリン( DE=25 )を加え、混合溶解し、120 ℃で30秒の
加熱を行った後、均質化を300kg/cm2の圧力で2 パスで
行い、スプレードライした。
Example 1 To 15% by weight of water was added to defatted soybeans, the pH was adjusted to neutrality with sodium hydroxide, and the soymilk extracted with stirring was adjusted to pH 4.8 with hydrochloric acid to precipitate soybean proteins and centrifuged. Thereafter, the soybean protein (also referred to as acid precipitation curd) as a precipitate was recovered. This was neutralized with sodium hydroxide to prepare an 8% soybean protein neutralized solution. Soy protein in this solution
100 parts, 20 parts of caseinate, and 30 parts of dextrin (DE = 25) was added, mixed and dissolved, 2 after the heat for 30 seconds at 120 ° C., homogenized at a pressure of 300 kg / cm 2 Performed by pass and spray dried.

【0018】実施例2 実施例1で調製された大豆タンパク質中和液に大豆タン
パク質100 部(重量部。以下も同じ)に対し、20部のカ
ゼイネート、及び30部のデキストリン( DE=25 )、及び
10部のヘキサメタリン酸ナトリウムを加え、混合溶解
し、120 ℃、30秒の加熱を行った後、均質化を300kg/cm
2 の圧力で2 パスで行い、スプレードライした。
Example 2 20 parts of caseinate, 30 parts of dextrin (DE = 25), and 100 parts of soy protein (parts by weight; the same applies hereinafter) were added to the soy protein neutralized solution prepared in Example 1. as well as
Add 10 parts of sodium hexametaphosphate, mix and dissolve, heat at 120 ° C for 30 seconds, and homogenize to 300 kg / cm
This was performed in two passes at a pressure of 2 and spray dried.

【0019】実施例3 実施例1で調製された大豆タンパク質中和液に大豆タン
パク質100 部に対し、10部のカゼイネート、及び30部の
デキストリン( DE=36 )及び10部のヘキサメタリン酸ナ
トリウムを加え、混合溶解し、120 ℃, 30秒の加熱を行
った後、スプレードライした。
Example 3 10 parts of caseinate, 30 parts of dextrin (DE = 36) and 10 parts of sodium hexametaphosphate were added to 100 parts of soy protein to the soy protein neutralized solution prepared in Example 1. After mixing and dissolving, the mixture was heated at 120 ° C. for 30 seconds and spray-dried.

【0020】実施例4 実施例1で調製された大豆タンパク質中和液に大豆タン
パク質100 部に対し、10部のカゼイネート、30部のデキ
ストリン( DE=36 )、及び10部のヘキサメタリン酸ナト
リウムを加え、混合溶解し、90℃に加熱後、均質化を30
0kg/cm2 の圧力で3 パスで行い、その後120 ℃、30秒の
加熱を行った後、スプレードライした。
Example 4 To 100 parts of soybean protein, 10 parts of caseinate, 30 parts of dextrin (DE = 36) and 10 parts of sodium hexametaphosphate were added to 100 parts of soybean protein neutralized solution prepared in Example 1. Dissolve, mix and heat to 90 ° C, homogenize 30
This was performed in three passes at a pressure of 0 kg / cm 2 , followed by heating at 120 ° C. for 30 seconds, followed by spray drying.

【0021】比較例1 実施例1で調製された大豆タンパク質中和液に大豆タン
パク質を120 ℃、30秒の加熱を行った後、スプレードラ
イした。
Comparative Example 1 The soybean protein neutralized liquid prepared in Example 1 was heated at 120 ° C. for 30 seconds and then spray-dried.

【0022】比較例2 実施例1で調製された大豆タンパク質中和液に大豆タン
パク質を90℃に加熱後、均質化を300kg/cm2 の圧力で3
パスで行い、その後、120 ℃、30秒の加熱を与えた後、
スプレードライした。
Comparative Example 2 After heating the soybean protein neutralized solution prepared in Example 1 to 90 ° C., homogenization was carried out at a pressure of 300 kg / cm 2 for 3 hours.
Pass, and then give a heating of 120 ℃ for 30 seconds,
Spray dried.

【0023】比較例3 実施例1で調製された大豆タンパク質中和液に大豆タン
パク質100 部に対し、10部のデキストリン( DE=25 )、
及び10部のヘキサメタリン酸ナトリウムを加え、混合溶
解し、90℃に加熱後、均質化を300kg/cm2 の圧力で3 パ
スで行い、その後の120 ℃, 30秒の加熱後、スプレード
ライした。
Comparative Example 3 In the soybean protein neutralized solution prepared in Example 1, 10 parts of dextrin (DE = 25) was added to 100 parts of soybean protein.
Then, 10 parts of sodium hexametaphosphate were added, mixed and dissolved, heated to 90 ° C., homogenized at a pressure of 300 kg / cm 2 for 3 passes, and then heated at 120 ° C. for 30 seconds, followed by spray drying.

【0024】比較例4 実施例1で調製された大豆タンパク質中和液に於いて大
豆たん白質100 部に対し、30部のカゼイネートを加え混
合溶解させ、120 ℃で30秒間の加熱を行った後、スプレ
ードライした。
Comparative Example 4 In the soybean protein neutralized solution prepared in Example 1, 30 parts of caseinate was added to 100 parts of soybean protein, mixed and dissolved, and heated at 120 ° C. for 30 seconds. , Spray dried.

【0025】各調製パウダーを相対湿度60%、温度4
0℃で0日〜5日間保存した。溶解率は2%食塩水に1
%濃度(W/W)でパウダーを分散させ、「ポリトロン
・ホモジナイザー」(スイス・KINEMATICA社製) で5,
000r. p. m. で攪拌し、遠心分離(10, 000
G 、10分)して、上清液に残るタンパク質の百分比で
求めた。
Each prepared powder was subjected to a relative humidity of 60% and a temperature of 4%.
Stored at 0 ° C for 0-5 days. Dissolution rate is 1% in 2% saline
% (W / W) and dispersed with a "Polytron Homogenizer" (KINEMATICA, Switzerland).
000 rpm and centrifugation (10,000).
G, 10 minutes) and the percentage of protein remaining in the supernatant was determined.

【0026】[0026]

【表1】大豆タンパク質への添加物質量、均一化処理が
粉末状大豆タンパク質の食塩水への溶解性に及ぼす影
響。 ─────────────────────────────────── 大豆タンパク質100 部への添加量 2%NaCl 水への溶解率 カゼイ デキス ヘキサメタ 均質化 0日後 2日後 5日後 ネート トリン リン酸 Na 処理 ─────────────────────────────────── 部 部 部 % % % 実施例 1 20 30 0 有り 88 83 75 実施例 2 20 30 10 有り 88 85 83 実施例 3 10 30 10 無し 86 68 66 実施例 4 10 30 10 有り 86 82 82 比較例 1 0 0 0 無し 68 43 33 比較例 2 0 0 0 有り 75 51 35 比較例 3 0 10 10 有り 78 55 38 比較例 4 30 0 0 無し 85 44 42 ─────────────────────────────────── 実施例の結果として、カゼイネートとデキストリンの併
用は、効果が高く、リン酸塩や高圧ホモゲナイザーによ
る均質化の処理はその効果を助長した。一方比較例で、
何も添加しない場合や均質化処理のみを行った場合、添
加量が低い場合、あるいは、カゼイネートのみでその添
加量が低い場合など、いずれの場合も溶解率は著しく低
下した。
[Table 1] Effect of the amount of added substances to soy protein and the homogenization treatment on the solubility of powdered soy protein in saline.添加Addition to 100 parts of soybean protein 2% NaCl Dissolution in water Rate Casei dex Hexameta Homogenization 0 days 2 days 5 days After treatment with sodium trin triphosphate phosphate ──────────────────────────────── ─── Part Part%%% Example 1 20 30 0 Yes 88 83 75 Example 2 20 30 10 Yes 88 85 83 Example 3 10 30 10 None 86 68 66 Example 4 10 30 10 Yes 86 82 82 Compare Example 1 0 0 0 None 68 43 33 Comparative example 2 0 0 0 Present 75 51 35 Comparative example 3 0 10 10 Present 78 55 38 Comparative example 4 30 0 0 None 85 44 42 ───────────と し て As a result of the examples, the combined use of caseinate and dextrin is highly effective, homogenizing with phosphate or high pressure homogenizer. Processing promotes its effect did. On the other hand, in the comparative example,
The dissolution rate was significantly reduced in all cases, such as when nothing was added, when only the homogenization treatment was performed, when the amount added was low, or when only the caseinate was used and the amount added was low.

【0027】[0027]

【発明の効果】本発明によれば、大豆タンパク質にカゼ
イネート、炭水化物を加えた溶液に、好ましくはリン酸
塩を加えて、加熱処理し、均質化処理し、乾燥すること
により、水或は塩水に対し高い溶解性及びその保存性を
有する粉末状大豆タンパク質が得られた。
According to the present invention, a solution obtained by adding a caseinate and a carbohydrate to a soybean protein, preferably a phosphate is added, and the mixture is heated, homogenized, and dried to obtain water or saline. , A powdery soybean protein having high solubility and storage stability was obtained.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 赤坂 武志 茨城県筑波郡谷和原村絹の台4丁目3番地 不二製油株式会社つくば研究開発センタ ー内 ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Takeshi Akasaka 4-3 Kinokudai, Yawahara-mura, Tsukuba-gun, Ibaraki Pref.

Claims (9)

【特許請求の範囲】[Claims] 【請求項1】大豆タンパク質に対してカゼイネートもし
くはカゼイン及び炭水化物を加配した溶液を調製し、加
熱処理し、乾燥することを特徴とするタンパク質素材の
製造法。
1. A method for producing a protein material, comprising preparing a solution in which caseinate or casein and carbohydrate are added to soybean protein, heat-treating and drying.
【請求項2】大豆タンパク質に対するカゼイネートもし
くはカゼインの量が 5〜50重量%である請求項1記載の
製造法。
2. The method according to claim 1, wherein the amount of caseinate or casein is 5 to 50% by weight based on the soybean protein.
【請求項3】大豆タンパク質に対する炭水化物の量が 5
〜100 重量%である請求項1記載の製造法。
3. The method according to claim 1, wherein the amount of carbohydrate to soybean protein is 5%.
The method according to claim 1, wherein the amount is from 100 to 100% by weight.
【請求項4】タンパク質溶液を加熱の前または後、もし
くは加熱しながら均質化する請求項1記載の製造法。
4. The method according to claim 1, wherein the protein solution is homogenized before or after heating or while heating.
【請求項5】均質化溶液中の非水・非油成分中の大豆タ
ンパク質含有量が50重量%以上である請求項4記載の製
造法。
5. The method according to claim 4, wherein the soybean protein content in the non-water / non-oil component in the homogenized solution is 50% by weight or more.
【請求項6】均質化溶液中の大豆タンパク質濃度が6%
以上である請求項4記載の製造法。
6. The soybean protein concentration in the homogenized solution is 6%.
The method according to claim 4, which is the above.
【請求項7】均質化溶液中にリン酸塩が含有される請求
項4記載の製造法。
7. The method according to claim 4, wherein the homogenized solution contains a phosphate.
【請求項8】均質化溶液を調製する均質化圧力が50〜50
0kg/cm2 である請求項4記載の製造法。
8. The homogenization pressure for preparing a homogenization solution is 50 to 50.
5. The method according to claim 4, wherein the amount is 0 kg / cm 2 .
【請求項9】加熱処理が、50〜160 ℃、1 時間〜5 秒間
の範囲で実施される請求1記載の製造法。
9. The method according to claim 1, wherein the heat treatment is carried out at 50 to 160 ° C. for 1 hour to 5 seconds.
JP17822197A 1997-07-03 1997-07-03 Manufacturing method of soy protein material with excellent solubility Expired - Fee Related JP3381558B2 (en)

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Publication number Priority date Publication date Assignee Title
US7179499B2 (en) * 2002-01-15 2007-02-20 Kabushiki Kaisha Kyowashokuhin Method of producing soy milk products
WO2005055735A1 (en) * 2003-12-11 2005-06-23 Fuji Oil Company, Limited Improved soybean 7s protein and process for producing the same
US7635756B2 (en) 2003-12-11 2009-12-22 Fuji Oil Company, Limited Soybean 7S protein and process for producing the same
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