JPS60199349A - Preparation of protein - Google Patents

Preparation of protein

Info

Publication number
JPS60199349A
JPS60199349A JP59054758A JP5475884A JPS60199349A JP S60199349 A JPS60199349 A JP S60199349A JP 59054758 A JP59054758 A JP 59054758A JP 5475884 A JP5475884 A JP 5475884A JP S60199349 A JPS60199349 A JP S60199349A
Authority
JP
Japan
Prior art keywords
soybean
protein
solvent
organic solvent
odor
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
JP59054758A
Other languages
Japanese (ja)
Other versions
JPH0331415B2 (en
Inventor
Masaya Watanabe
渡辺 正弥
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
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 JP59054758A priority Critical patent/JPS60199349A/en
Publication of JPS60199349A publication Critical patent/JPS60199349A/en
Publication of JPH0331415B2 publication Critical patent/JPH0331415B2/ja
Granted legal-status Critical Current

Links

Abstract

PURPOSE:To prepare a protein having excellent taste and flavor, and extremely low oil seed smell, by extracting pressed oil seed with an organic solvent under specific condition, and removing the solvent from the product to effect the deodoization. CONSTITUTION:An oil seed such as soybean is pressed at a water-content of <=10%, and extracted with an organic solvent such as hexane/etchanol, etc. at <=70 deg.C. The residual organic solvent is removed from the extracted oil seed at a temperature above the boiling point of said organic solvent. The obtained solvent-free pressed oil seed is extracted with water preferably having a pH excluding the region near the isoelectric point of the protein. The objective protein can be extracted by this procedure.

Description

【発明の詳細な説明】 本発明は油糧種子臭の極めて少ない、風味の優れた蛋白
の製造法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing a protein with very little oilseed odor and excellent flavor.

(従来技術) 油種種子蛋白の一つである大豆蛋白は、植物性の優れた
蛋白でありながら独特の風味(通称大豆臭と呼ばれる)
を有するが故に、食品への利用用途及びその量が制限さ
れている。
(Prior art) Soybean protein, which is one of the oilseed proteins, is an excellent vegetable protein but has a unique flavor (commonly known as soybean odor).
Therefore, its use in food and its amount are limited.

この問題を解決する為の研究は多くの研究者により連綿
と続けられておりその量は厖大な数にのぼる。
Many researchers are continuing to conduct research to solve this problem, and the amount of research is enormous.

その思想を大別するとta+大豆臭の発生原因を究明し
これをなくす、tb+発生した大豆臭を取り除く、(C
)マスキングして感知できなくする等となる。
The ideas can be roughly divided into ta+investigate the cause of soybean odor and eliminate it, tb+remove the soybean odor (C
) masking to make it undetectable, etc.

叉その具体的な手段としては■加熱処理によりリポキシ
ゲナーゼ等の大豆臭発生に関与する酵素を失活する物理
化学的手段、■炭酸ナトリウム等の利用による化学的手
段、■乳酸菌、酵母等の微生物を利用する生物学的手段
、■アルデヒドデヒドロゲナーゼ等の酵素を利用する生
化学的手段、■これらの組合せ等を挙げることができる
Specific methods include: ■ Physicochemical means of inactivating enzymes involved in soybean odor generation such as lipoxygenase through heat treatment; ■ Chemical means using sodium carbonate, etc.; ■ Microorganisms such as lactic acid bacteria and yeast. Examples include biological means utilizing, (2) biochemical means utilizing enzymes such as aldehyde dehydrogenase, and (2) combinations thereof.

しかし、今日に至るまで無臭の大豆蛋白は得られていな
い。それは、大豆臭の発生機構が複雑なこと、大豆臭が
単一成分でなく複合された臭でありその実体が明確につ
かめないこと、大豆臭が大豆蛋白の複雑な高次構造とあ
いまって除去が極めて困難なこと等に由来する。
However, to date, odorless soybean protein has not been obtained. This is because the mechanism by which soybean odor is generated is complex, soybean odor is not a single component but a compound odor and its substance cannot be clearly grasped, and soybean odor is removed due to the complex higher-order structure of soybean protein. This is due to the fact that it is extremely difficult.

例えば、特開昭52−120149 F大豆の酸抽出た
ん白及びその製造法」には大豆蛋白の等電点以下(pH
1,6〜3.5 )で水抽出し且つNSI (Nitr
ogenSoluble Index )の関係からシ
ビアーな条件で中和する方法が開示されている。しかし
、この場合もリポキシゲナーゼが失活している訳ではな
く、大豆臭の問題は残る。
For example, in Japanese Patent Application Laid-Open No. 52-120149 "F Soybean Acid Extracted Protein and Method for Producing the Same,"
1,6-3.5) and NSI (Nitr
A method of neutralizing under severe conditions has been disclosed based on the relationship of (ogenSolble Index). However, even in this case, lipoxygenase is not inactivated, and the problem of soybean odor remains.

本発明者は、過去の技術をトレースする範囲のなかごは
大豆蛋白の物性を1員なうことなく脱臭することが如何
に困難なことであるか痛感し、残念ながら充分満足のい
く大豆蛋白を得ることはできなかった。しかし、試行錯
誤の末、まず原料の大豆の大豆臭発生要因を無くし且つ
もともと大豆が有している大豆臭を極力除去した圧扁大
豆を用い、大豆蛋白抽出工程でそれでもなお発生する可
能性のある大豆臭の発生を所望により極力抑えることに
より従来品に比べ大豆臭の極めて少ない大豆蛋白を得る
ことができたのである。
The present inventor was acutely aware of how difficult it was to deodorize soybean protein without losing its physical properties, and unfortunately, it was discovered that a sufficiently satisfactory soybean protein was obtained. I couldn't get it. However, after much trial and error, we first eliminated the causes of soybean odor in the soybean raw material and used compressed soybeans that removed as much of the soybean odor as possible, which could still occur during the soybean protein extraction process. By suppressing the generation of certain soybean odor as much as possible, we were able to obtain soybean protein with extremely less soybean odor compared to conventional products.

(目的) 本発明者は、油糧種子具の極めて少ない、風味の優れた
蛋白を得ることを目的とし、油種種子の一つである大豆
に関し大豆臭の極めて少ない、風味の優れた大豆蛋白を
得ることを検討した。
(Purpose) The present inventor has aimed to obtain a protein with excellent flavor that has very little oilseed ingredients, and has made a soybean protein that has very little soy odor and has an excellent flavor using soybean, which is one of the oilseeds. I considered getting it.

通常、大豆蛋白は以下の工程で得られる。Soybean protein is usually obtained through the following steps.

大豆−(圧扁)=(脱脂)−説脂大豆一(水抽出)−(
脱オカラ)→豆乳−(酸沈銀)−(脱ホエー)−酸沈澱
カード−(中和)−分離大豆蛋白溶液−(乾燥)−分離
大豆蛋白 本発明者は目的達成の為、まず第一に大豆臭の発生する
工程のチェックと発生防止を目的として研究した結果、
主に■大豆−(圧扁)段階及び■脱脂大豆=(水抽出)
段階で大豆臭が発生ずることを見いだし、ごれを防止す
るには■圧扁時の大豆の水分を低(保ち、要ずれば低温
で圧扁ずればよいこと、■(水抽出)をリポキシゲナー
ゼ作用pH域外で行えばよいこと、を見出した。
Soybeans - (pressing) = (defatting) - defatted soybeans (water extraction) - (
In order to achieve the objective, the inventors first of all As a result of research aimed at checking and preventing the production of soy odor,
Mainly ■ Soybean - (pressing) stage and ■ Defatted soybean = (water extraction)
We discovered that a soybean odor occurs during the process, and in order to prevent stains, we need to keep the soybean moisture at a low level during pressing, and if necessary, press at a low temperature. It has been found that the process can be carried out outside the working pH range.

しかし、いくら大豆臭の防止をしても限界のあることに
気付いた。そこで更に研究を進めた結果、もともと大豆
自体が大豆臭をある程度有していることに由来すること
が分かった。
However, I realized that no matter how much I tried to prevent soy odor, there was a limit. As a result of further research, it was discovered that soybeans themselves originally have a certain degree of soybean odor.

そこで本発明者は、第二に(脱臭)について検討した。Therefore, the present inventors secondly investigated (deodorization).

その結果、■(圧扁)=(脱脂)工程において、有機溶
剤による抽出及び脱溶剤をある条件下に行うことにより
、もともと大豆自体が有している大豆臭を除去できるの
みならず大豆臭発生原因も防止できる知見を得た。
As a result, by performing extraction with an organic solvent and desolvation under certain conditions in the (pressing) = (defatting) process, it is possible to not only remove the soy odor that the soybean itself originally has, but also to generate soy odor. We have obtained knowledge that can prevent the cause.

以上の知見を有機的に組み合わせることにより、従来の
単一または複合工程で限界のあった大豆臭を大幅になく
すことができた。また、このことは大豆を含め広く油糧
種子について応用することができる知見を得て本発明を
完成するに至った。
By organically combining the above knowledge, we were able to largely eliminate soybean odor, which was a limitation with conventional single or combined processes. Furthermore, this knowledge has led to the completion of the present invention, which can be applied to a wide range of oilseeds including soybeans.

(構成) 本発明は、(1)油in +i子を水分10%以下で圧
扁する第1工程、圧扁油糧種子を70℃以下で有機溶剤
を用いて抽出する第2工程、有機溶剤抽出後の圧扁油糧
種子から、残存有機溶剤を該有機溶剤の沸点以上の温度
で脱溶剤する第3工程、脱溶剤圧扁油糧種子から、水系
下(好ましくは等電点にJ近を除く)に蛋白を抽出する
第4工程を含むことを特徴とする蛋白の製造法である。
(Structure) The present invention comprises (1) a first step of compressing oil in +i seeds with a moisture content of 10% or less; a second step of extracting the compressed oil seeds at a temperature of 70° C. or lower using an organic solvent; The third step is to remove residual organic solvent from the extracted pressed oil seeds at a temperature higher than the boiling point of the organic solvent. This is a method for producing a protein characterized by including a fourth step of extracting the protein.

油糧種子は大豆、菜種、綿実、落花生、ゴマ、向日葵、
コーン等その蛋白を食用に利用できるものが好ましく、
その特性、入手の容易性及び経済性より大豆が好適であ
る。以下油糧種子に関し大豆を例にして説明する。
Oilseeds include soybean, rapeseed, cottonseed, peanut, sesame, sunflower,
Preferably, those whose protein can be used as food, such as corn.
Soybeans are preferred because of their characteristics, availability, and economy. Below, oilseeds will be explained using soybeans as an example.

大豆は公知の種類のものを用いることができ、剥皮して
もよいが大豆の組織が損なわれていないほうが好ましい
。組織の破壊により酵素等が作用して大豆臭発生の原因
となるからである。
Known types of soybeans can be used, and although they may be peeled, it is preferable that the soybean structure is intact. This is because the destruction of the tissue causes enzymes and the like to act, causing soybean odor.

圧扁する際、大豆の水分は10%以下、好ましくは5%
以下が適当である。10%をこえて圧扁されると大豆の
組織内の酵素等が作用し易く大豆臭が発生し易い。公知
の乾燥手段を用い°ζ該水分を減少することができ、熱
風乾燥が好ましい。また要すれば、低温で圧扁すること
が好ましい。雷温以下が好ましく、特に好ましくは0℃
以下が適当である。
When compressing, the moisture content of soybeans is 10% or less, preferably 5%.
The following are appropriate. When the soybean is compressed by more than 10%, enzymes in the soybean tissue are likely to act on the soybean, and a soybean odor is likely to occur. The moisture content can be reduced using known drying means, with hot air drying being preferred. Moreover, if necessary, it is preferable to press at a low temperature. Preferably below lightning temperature, particularly preferably 0°C
The following are appropriate.

圧扁大豆は公知の有機溶剤或いはこれら有機溶剤を組み
合わせた混合物を用いて溶剤溶解成分を抽出することが
できる。抽出温度は大豆蛋白が変性し難い温度以下即ち
70°C以下が好ましい。有機溶剤はエチルアルコール
等のアルコール類、アセトン等のケトン類、エチルエー
テル等のエーテル類等が挙げられる。叉アセトン、エタ
ノール等の極性溶剤は脱臭効果のみならず脱色効果も有
り好ましい。特に好ましくはヘキサン/エタノール等に
代表される非極性溶剤/極性溶剤の混合物が脱臭効果が
最も強く適当である。抽出方法は公知の方法を用いるこ
とができる。脱溶剤(60°C)後の圧扁大豆の脱臭効
果を次表に例示する。
The solvent-soluble components of the pressed soybean can be extracted using a known organic solvent or a mixture of these organic solvents. The extraction temperature is preferably below a temperature at which soybean protein is difficult to denature, that is, below 70°C. Examples of the organic solvent include alcohols such as ethyl alcohol, ketones such as acetone, and ethers such as ethyl ether. Polar solvents such as acetone and ethanol are preferred because they have not only a deodorizing effect but also a decolorizing effect. Particularly preferred is a mixture of a non-polar solvent/polar solvent represented by hexane/ethanol etc., which has the strongest deodorizing effect. A known extraction method can be used. The deodorizing effect of compressed soybeans after solvent removal (60°C) is illustrated in the following table.

尚、大豆臭は訓練された40名のパネラ−によりにおい
、風味を官能検査し、全く大豆臭を感じない・・・0〜
5、はとんど大豆臭を感しない・・・6〜15、若干大
豆臭を感じる・・・16〜25、大豆臭を感しる・・・
26〜35、大豆臭を強く感じる・・・36以上として
評価し上限及び下限の値を除いて相加平均した。以下同
様である。
In addition, the smell and flavor of soybeans were sensory tested by 40 trained panelists, and the results showed that there was no soybean smell at all...0~
5. I don't really notice a soybean odor... 6-15, I feel a slight soybean odor... 16-25, I notice a soybean odor...
26-35, strong soybean odor...Evaluated as 36 or higher, and arithmetic averaged excluding the upper and lower limits. The same applies below.

ヘキサン 39 アセトン 33 エタノール 38 エーテル 25 ヘキサン/エタノール(2/1)23 有機溶剤抽出後、該有831溶剤は濾過等により除去さ
れ、残存有機溶剤は蒸気等を用いて該有機溶剤の沸点以
上の温度で脱溶剤することができる。
Hexane 39 Acetone 33 Ethanol 38 Ether 25 Hexane/ethanol (2/1) 23 After organic solvent extraction, the 831 solvent is removed by filtration, etc., and the remaining organic solvent is heated to a temperature higher than the boiling point of the organic solvent using steam or the like. The solvent can be removed with

このときの温度は大豆蛋白の変性に大きく関与し高くし
ないほうが好ましいとされてきた。本発明においては、
該温度は63〜95℃が適当であり、好ましくは68℃
以上、特に好ましくは78℃以上が適当である。該温度
が高い程脱臭効果が顕著であり好ましいが95℃を越え
ると脱溶剤時間にもよるが蛋白の変性が著しく第四工程
における蛋白の抽出におりる収率の低下をきたし好まし
くない。尚、脱溶剤の手段として乾燥蒸気を用いる方法
と飽和水蒸気を用いる方法があるが、後者のほうが脱臭
効果が大きく打ましい。以下n−へキサンを用いて圧扁
大豆を抽出した後の脱溶剤温度(雰囲気温度)による脱
臭効果を次表に例示する。
It has been said that it is preferable not to raise the temperature at this time, as it greatly affects the denaturation of soybean protein. In the present invention,
The temperature is suitably 63 to 95°C, preferably 68°C.
Above, a temperature of 78° C. or higher is particularly preferred. The higher the temperature, the more pronounced the deodorizing effect is, which is preferable; however, if the temperature exceeds 95°C, the protein will be significantly denatured, depending on the desolvation time, and the yield of the protein extraction in the fourth step will decrease, which is not preferable. There are two methods for removing the solvent, one using dry steam and the other using saturated steam, but the latter method has a greater deodorizing effect. The following table illustrates the deodorizing effect depending on the solvent removal temperature (ambient temperature) after extracting compressed soybeans using n-hexane.

表−2 脱溶剤温度 脱溶剤圧扁大豆の大豆臭 60℃ 39 65℃ 29 70’C21 75℃ 13 80’C10 90℃ 9 100℃ 5 70℃以下の場合適宜減圧した。Table-2 Solvent removal temperature: Soybean odor from solvent-free pressed soybeans 60℃ 39 65℃ 29 70’C21 75℃ 13 80’C10 90℃ 9 100℃ 5 When the temperature was 70°C or lower, the pressure was appropriately reduced.

脱溶剤した圧扁大豆を用いて大豆蛋白を水抽出すること
ができる。しかし大豆蛋白の等電点付近部ちpl+3.
6〜5.4では蛋白の抽出効率が下がるのみならず大豆
臭が強くなり好ましくない。従って中性域或いはpl+
3.5以下が好ましい。あまりpHを低くすると抽出後
の分離大豆蛋白溶液の中和に酸を多く用いる為生成され
る塩が多くなるので得られた蛋白の用途が制限される。
Soybean protein can be extracted with water using compressed soybeans that have been subjected to solvent removal. However, the area near the isoelectric point of soybean protein is pl+3.
6 to 5.4 is not preferable because not only the protein extraction efficiency decreases but also the soybean odor becomes strong. Therefore, the neutral range or pl+
3.5 or less is preferable. If the pH is too low, a large amount of acid will be used to neutralize the isolated soybean protein solution after extraction, resulting in a large amount of salt produced, which will limit the uses of the resulting protein.

次表に各抽出ρ1;域のときの大豆臭の程度を示す。The following table shows the degree of soybean odor for each extraction in the ρ1 range.

脱溶剤温度による効果が著しい。これは、脱溶剤温度が
酵素等の失活等にも作用し、脱臭効果とあいまって大豆
臭の減少に効を奏したものとlIl、察される。
The effect of desolvation temperature is significant. This is thought to be due to the fact that the desolvent temperature also acts to deactivate enzymes and the like, which, combined with the deodorizing effect, was effective in reducing soybean odor.

表−3 0,67279 1,03147 1,58146 3,3147 3,43158 4,53617 6、、II 2G 13 7.0 25 12 以上、油糧種子として大豆を例にして詳述したように、
(11油糧種子を水分10%以下で圧扁する第1工程、
圧扁部i1種子を70℃以下で有機溶剤を用いて抽出す
る第2工程、有機溶剤抽出後の圧扁油糧種子から、残存
有ta溶剤を該有機溶剤の沸点以上の温度で脱溶剤する
第3工程、脱溶剤圧扁油糧種子から、水系下(好ましく
は等電点付近を除く)に蛋白を抽出する第4工程を有機
的に組合せることにより、従来の単独或いは公知の組合
せでは得られなかった油糧種子具の極めて少ない、風味
の優れた蛋白を得ることが可能になったものである。 
(実施例) 以下実施例により本発明の実施態様を説明する。
Table-3 0,67279 1,03147 1,58146 3,3147 3,43158 4,53617 6,, II 2G 13 7.0 25 12 As explained above using soybean as an example of oilseed,
(11 The first step of compressing oilseeds with a moisture content of 10% or less,
A second step of extracting the compressed part i1 seeds using an organic solvent at 70°C or lower, removing residual ta solvent from the compressed oil seeds after organic solvent extraction at a temperature above the boiling point of the organic solvent. By organically combining the third step and the fourth step of extracting protein from solvent-free and pressed oil seeds in an aqueous system (preferably excluding the area near the isoelectric point), it is possible to It has now become possible to obtain protein with excellent flavor and with very little amount of unobtainable oilseed ingredients.
(Example) Embodiments of the present invention will be described below with reference to Examples.

実施例1 大豆(米国イリノイ産)(水分7%)を約2ml11厚
に圧扁してフレークとし、n−ヘキサンを10倍(−/
誓)量の割合で用いて50℃で溶剤抽出し、溶剤を濾別
し、残存溶剤をデソルベンタイザー(水蒸気(4kg 
/−ゲージ圧))を用い雰囲気温度を75℃にして脱溶
剤して脱脂フレークを得た。この脱脂フレーク10部に
対し、piを酸性に調整した水100部を加え、水抽出
した後オカラを除き豆乳を得た。尚、水抽出時のpl+
はそれぞれ第11頁の表−3の通りであった。次に塩酸
を用いてpH4,5に調整し、ホエーを除き水酸化ナト
リウムを用いて中和し、蛋白溶液を得た。但しpl+4
.5では抽出困難であった為、まずpl(4゜5でホエ
ーを除いた後、中和してオカラを除いて蛋白溶液を得た
。各々の蛋白溶液をスプレードライして分離大豆蛋白と
した。
Example 1 Soybean (produced in Illinois, USA) (moisture 7%) was pressed into flakes to a thickness of about 2 ml, and n-hexane was added 10 times (-/
Extract the solvent at 50°C using the same amount as
/-gauge pressure)) at an ambient temperature of 75° C. to remove the solvent and obtain degreased flakes. To 10 parts of the defatted flakes, 100 parts of water whose pi was adjusted to be acidic was added, and after water extraction, okara was removed to obtain soybean milk. In addition, pl+ during water extraction
were as shown in Table 3 on page 11. Next, the pH was adjusted to 4.5 using hydrochloric acid, whey was removed, and the mixture was neutralized using sodium hydroxide to obtain a protein solution. However, pl+4
.. Since it was difficult to extract with 5, we first removed the whey using pl (4°5) and then neutralized it to remove okara to obtain a protein solution. Each protein solution was spray dried to obtain isolated soybean protein. .

該分離大豆蛋白の10%水溶液について、訓練された4
0名のパネラ−によりにおい、風味を官能検査し、全く
大豆臭を感じない・・・O〜5、はとんど大豆臭を感じ
ない・・・6〜15、若干大豆臭を感じる・・・16〜
25、大豆臭を感じる・・・26〜35、大豆臭を強く
感じる・・・36以上として評価し上限及び下限の値を
除いて相加平均した。以下同様である。
4 trained on the 10% aqueous solution of isolated soy protein.
A sensory test of smell and flavor was carried out by 0 panelists: No soy odor at all...O~5: Almost no soy odor...6~15: Slight soy odor...・16~
25, I feel a soybean odor...26-35, I feel a strong soybean odor...Evaluated as 36 or higher, and the arithmetic average was calculated excluding the upper and lower limits. The same applies below.

叉、同様にしてデソルベンタイザー雰囲気温度を60℃
にして脱溶剤して得た分離大豆蛋白にっても同様に官能
検査した。
Similarly, the desolventizer atmosphere temperature was set to 60°C.
The isolated soybean protein obtained by removing the solvent was also subjected to the same sensory test.

結果を第11頁の表−3に示した。The results are shown in Table 3 on page 11.

75℃脱溶剤して得た分離大豆蛋白は殆ど大豆臭を感ぜ
ず極めて風味の良いものであった。
The isolated soybean protein obtained by removing the solvent at 75°C had an extremely good flavor with almost no soybean odor.

実施例2 大豆(米国イリノイ産)を熱風乾燥し、水分を3%に調
整し、約2mm厚に圧扁してフレークとし、n−ヘキサ
ン/98%エタノール=20/10 (V /V)を1
0倍(W /W ) M用いて50℃で溶剤抽出した後
、溶剤を濾別し、残存溶剤をデソルヘンタイザ−(水蒸
気(4kg /−ゲージ圧))を用い雰囲気温度を75
℃にして脱溶剤して脱脂フレークを得た。この脱脂フレ
ーク10部に水100部を加え、実施例1と同様にして
中性で蛋白を抽出して分離大豆蛋白を得た。実施例1と
同様にして官能検査の結果、評価の値は8で、極めて風
味の良いものであった。
Example 2 Soybeans (produced in Illinois, USA) were dried with hot air, the moisture content was adjusted to 3%, and the flakes were pressed to a thickness of about 2 mm. N-hexane/98% ethanol = 20/10 (V/V) was prepared. 1
After solvent extraction at 50°C using 0x (W/W) M, the solvent was filtered and the remaining solvent was removed using a desolventizer (steam (4 kg/-gauge pressure)) at an ambient temperature of 75°C.
℃ and the solvent was removed to obtain defatted flakes. 100 parts of water was added to 10 parts of the defatted flakes, and protein was extracted under neutral conditions in the same manner as in Example 1 to obtain isolated soybean protein. As a result of the sensory test in the same manner as in Example 1, the evaluation value was 8, indicating that the flavor was extremely good.

(効果) 以上詳述したように、本発明の方法は広く油糧種子(大
豆、菜種、綿実、落花生、ゴマ、向日葵、コーン等)等
に応用することができ、油糧種子具の極めて少ない、風
味の優れた蛋白を提供するものである。また、本発明に
おいて、その中間溶剤抽出産物(脱溶剤したもの)につ
いても風味のすぐれたものを得ることができる。これら
風味の榎れた蛋白或いは中間溶剤抽出産物(脱溶剤した
もの)は食品素材としての利用用途及びその量の拡大に
大いに寄与するものである。
(Effects) As detailed above, the method of the present invention can be widely applied to oilseeds (soybeans, rapeseed, cottonseed, peanuts, sesame, sunflowers, corn, etc.), and is extremely useful for oilseeds. It provides protein with excellent flavor. In addition, in the present invention, the intermediate solvent extraction product (solvent removed) can also be obtained with excellent flavor. These flavorful proteins or intermediate solvent extraction products (solvent removed) greatly contribute to the expansion of their use and quantity as food materials.

手続禎正書(自発) 1.事件の表示 昭和59年3月21日付特許出願(A)3、補正をする
者 4、代理人 大阪市淀用区東三国1丁目32番12号(■532)5
、?di正により増加する発明の数 なし6、’sNi
正の対象 明細書第12頁12行[・・・蒸気(4kg /cal
ゲージ圧))を用い・・・」とあるを「・・・蒸気(4
kg/cnlゲージ圧)を調整して用いた)を用い・・
・」と訂正する。
Procedural formalities (spontaneous) 1. Case description Patent application dated March 21, 1980 (A) 3, person making the amendment 4, agent 1-32-12 Higashi Mikuni, Yodoyou-ku, Osaka (■532) 5
,? Number of inventions increases due to di positive None 6,'sNi
Positive target specification page 12, line 12 [...steam (4kg/cal
Gauge pressure)) is used..." instead of "...steam (4
kg/cnl gauge pressure) was adjusted and used...
・” I corrected it.

明細書第14頁3行「・・・蒸気(4kg/adケージ
圧))を用い・・・」とあるを「・・・蒸気(4kg 
/c+aゲージ圧)を8111して用いた)を用い・・
・」と訂正する。
Page 14 of the specification, line 3, ``...steam (4kg/ad cage pressure)...'' was replaced with ``...steam (4kg/ad cage pressure)...''
/c+a gauge pressure) was 8111 and used)...
・” I corrected it.

Claims (4)

【特許請求の範囲】[Claims] (1)油糧種子を水分10%以下で圧扁する第1工程、
圧扁油糧種子を70℃以下で有機溶剤を用いて抽出する
第2工程、有機溶剤抽出後の圧扁油糧種子から、残存有
機溶剤を該有ta溶剤の沸点以上の温度で脱溶剤する第
3工程、脱溶剤圧扁油糧種子から、水系下(好ましくは
等重点付近を除く)に蛋白を抽出する第4工程を含むこ
とを特徴とする蛋白の製造法。
(1) The first step of compressing oilseeds with a moisture content of 10% or less,
A second step of extracting the compressed oil seeds using an organic solvent at a temperature of 70°C or lower, removing the remaining organic solvent from the compressed oil seeds after extraction with the organic solvent at a temperature equal to or higher than the boiling point of the ta-containing solvent. A method for producing protein, comprising a third step, and a fourth step of extracting protein from solvent-free and pressed oil seeds in an aqueous system (preferably excluding the vicinity of the iso-point).
(2)油iM種子が大豆である特許請求の範囲第(1)
項記載の製造法。
(2) Claim No. (1) in which the oil iM seeds are soybeans.
Manufacturing method described in section.
(3)自機溶剤の沸点以上の温度が70℃以上である特
許請求の範囲第(1)項又は第(2)項記載の製造法。
(3) The manufacturing method according to claim (1) or (2), wherein the temperature above the boiling point of the organic solvent is 70° C. or higher.
(4)等電点付近がPII3.6〜5.4である特許請
求の範囲第(2)項又は第(3)項に記載の製造法。
(4) The manufacturing method according to claim (2) or (3), wherein the isoelectric point has a PII of 3.6 to 5.4.
JP59054758A 1984-03-21 1984-03-21 Preparation of protein Granted JPS60199349A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59054758A JPS60199349A (en) 1984-03-21 1984-03-21 Preparation of protein

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59054758A JPS60199349A (en) 1984-03-21 1984-03-21 Preparation of protein

Publications (2)

Publication Number Publication Date
JPS60199349A true JPS60199349A (en) 1985-10-08
JPH0331415B2 JPH0331415B2 (en) 1991-05-07

Family

ID=12979667

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59054758A Granted JPS60199349A (en) 1984-03-21 1984-03-21 Preparation of protein

Country Status (1)

Country Link
JP (1) JPS60199349A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6022453A (en) * 1997-09-05 2000-02-08 Fried. Krupp Ag Hoesch Krupp Apparatus for the distillation of oil-seed extracts
JP2004504863A (en) * 2000-08-11 2004-02-19 ナチュラ・ホールディングス・プロプライエタリー・リミテッド Processing of oilseed
US7090875B2 (en) 2000-12-19 2006-08-15 Kabushiki Kaisha Yakult Honsha External skin preparations and process for producing the same

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA2400121C (en) 2000-02-16 2010-09-21 Nichia Corporation Nitride semiconductor laser device
US8845831B2 (en) 2009-02-02 2014-09-30 Denki Kogyo Co., Ltd. Heat treatment method

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS53142555A (en) * 1977-05-17 1978-12-12 Akzo Nv Production of soybean residue of which bitter substance removed as much as possible by extracting soybean

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS53142555A (en) * 1977-05-17 1978-12-12 Akzo Nv Production of soybean residue of which bitter substance removed as much as possible by extracting soybean

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6022453A (en) * 1997-09-05 2000-02-08 Fried. Krupp Ag Hoesch Krupp Apparatus for the distillation of oil-seed extracts
JP2004504863A (en) * 2000-08-11 2004-02-19 ナチュラ・ホールディングス・プロプライエタリー・リミテッド Processing of oilseed
US7090875B2 (en) 2000-12-19 2006-08-15 Kabushiki Kaisha Yakult Honsha External skin preparations and process for producing the same

Also Published As

Publication number Publication date
JPH0331415B2 (en) 1991-05-07

Similar Documents

Publication Publication Date Title
JP4596006B2 (en) Fractionated soybean protein material, processed soybean suitable for the same, and production method thereof
Wolf Lipoxygenase and flavor of soybean protein products
JP2012518990A (en) Protein preparation obtained from sunflower seeds and method for producing the same
US20060099325A1 (en) Vegetable protein preparations and use thereof
US3168406A (en) Process for treating soybean flour to improve its flavor
JP2006204266A (en) Roasted soybean oil and method for producing the same
JPS60199349A (en) Preparation of protein
JP2016146753A (en) Method for producing defatted soybean milk
US7122216B2 (en) Vegetable oil extraction methods
JP7375745B2 (en) Method for producing tissue-based vegetable protein material
KR100897450B1 (en) An Improved Process for the Preparation of Soy Protein Concentrate with Improved Functional Properties
JPS59132865A (en) Preparation of soya milk
Pudel et al. Vegetable oil-biorefinery
Sarv A comparative study of camelina, canola and hemp seed processing and products
JPS59140845A (en) Production of deodorized whole fat soybean flour
US5023104A (en) Defatted soybeans and soybean protein obtained from the same
JPS62502864A (en) Method of manufacturing food in an oxygen-free environment
JP2668480B2 (en) Processing method of soybean hypocotyl
JPS63219343A (en) Product of soybean protein
JPH04207158A (en) Modification of soybean protein food
Li et al. Soy Protein Flavours
Langyan et al. Lauren Viana and Marcia English
JPS5830024B2 (en) Manufacturing method for deodorized soybean flour
JPH06240287A (en) Oxidation-resistant fat or oil powder and its preparation
CN114304501A (en) Vegetable protein meat puffing process for reducing beany flavor by controlling temperature of forming section and vegetable protein meat