JP2000191694A - Fragmentation and preparation of subunit from 11s globulin of soybean, and its product - Google Patents

Fragmentation and preparation of subunit from 11s globulin of soybean, and its product

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Publication number
JP2000191694A
JP2000191694A JP10372899A JP37289998A JP2000191694A JP 2000191694 A JP2000191694 A JP 2000191694A JP 10372899 A JP10372899 A JP 10372899A JP 37289998 A JP37289998 A JP 37289998A JP 2000191694 A JP2000191694 A JP 2000191694A
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JP
Japan
Prior art keywords
subunit
globulin
steam
reducing agent
basic
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
JP10372899A
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Japanese (ja)
Other versions
JP3644283B2 (en
Inventor
Mitsutaka Kono
光登 河野
Motohiko Hirotsuka
元彦 広塚
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
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Fuji Oil Co Ltd
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Priority to JP37289998A priority Critical patent/JP3644283B2/en
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Publication of JP3644283B2 publication Critical patent/JP3644283B2/en
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Abstract

PROBLEM TO BE SOLVED: To provide a method for readily and efficiently fractionating and preparing an acidic subunit and a basic subunit, safe in food sanitation without using a reducing agent on 11S globulin. SOLUTION: An acidic subunit fraction and a basic subunit fraction are fractionated by bringing 11S globulin which is a major component of the soybean protein into contact with steam at a temp. of >=150 deg.C (under about 4 kgf/cm2 gage pressure of the steam). The fractionation is carried out under one of conditions that no reducing agent is used at all at the time of the contact with the steam, a centrifugal separation or a filtration is carried out after the contact with the steam, the temperature is kept at a temp. of >=120 deg.C for >=1 min after the contact with the steam, and the contact with the steam is performed at >=10% concentration of the protein, and the like. As the result, the cost of the reducing agent becomes unnecessary, and the method enables the cost for the removing operation, the treating expense, etc., of the remaining sulfurous acid by the conventional technique to be reduced compared to the conventional technique. The method can contribute to mass production, etc.

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】本発明は大豆タンパク質の主
要成分である11Sグロブリン(グリシニンとも言う)
から、その構成成分である酸性サブユニットと塩基性サ
ブユニットを、還元剤を使用することなく、簡便な方法
で取得するための分画方法に関する。
TECHNICAL FIELD The present invention relates to 11S globulin (also referred to as glycinin) which is a main component of soybean protein.
Accordingly, the present invention relates to a fractionation method for obtaining acidic subunits and basic subunits as constituents by a simple method without using a reducing agent.

【0002】[0002]

【従来の技術】大豆タンパク質は植物性タンパク質の中
で栄養性が優れているだけに止まらず、近年では様々な
生理活性効果が見い出され、生理機能剤としても注目さ
れる食品素材である。それら生理機能は大豆タンパク質
の中のある特定の部位から発現され、その部位を含む大
豆タンパク質成分を効率よく分画する技術を確立するこ
とは、大豆タンパク質を食品素材だけでなく、医薬品素
材として利用する上で重要な因子である。
2. Description of the Related Art Soybean protein is not only excellent in nutritional properties among vegetable proteins, but has recently been found to have various physiologically active effects, and is a food material that has attracted attention as a physiologically functional agent. Their physiological functions are expressed from a specific site in soy protein, and establishing technology to efficiently fractionate the soy protein component containing that site is necessary to use soy protein not only as a food material but also as a pharmaceutical material Is an important factor in

【0003】大豆タンパク質の各サブユニットは加熱に
よる変性過程において、解離されることが報告されてい
る。例えば、Wolf W.J. and Tamura T. (Cereal Chem.
46, 331,1969) は、大豆11Sグロブリンの熱変性につ
いて検討し、加熱により11Sグロブリンが酸性サブユ
ニットと塩基性サブユニットに解離されることを明らか
にした。その解離条件の詳細について、森 友彦(New
Food Industry, 24 (6), 53 ,1982 ) によると、低濃度
(0.5 %程度)の11Sグロブリン溶液は加熱により可
溶性会合体を経た上で、可溶性の酸性サブユニットと不
溶性の塩基性サブユニットに解離し、高濃度(5%以
上)では、そのような解離は起こらず、可溶性会合体か
ら可溶性巨大会合体を経て、ゲル化するとしている。し
かし、その後の研究によると、Hermansson, A.M., (JAO
CS, 63 (5), 658,1986)は蛋白濃度に関わらず、酸性サ
ブユニットと塩基性サブユニットに解離し、その後のゲ
ル化の有無のみが蛋白濃度に依存するとしている。ただ
し、何れにしても溶液状態での酸性サブユニットと塩基
性サブユニットの分画には、超遠心分離のような実用性
に乏しい手段でしか分画出来ない。
[0003] It has been reported that each subunit of soy protein is dissociated during denaturation by heating. For example, Wolf WJ and Tamura T. (Cereal Chem.
46, 331, 1969) studied the thermal denaturation of soybean 11S globulin and revealed that 11S globulin is dissociated into an acidic subunit and a basic subunit by heating. For details of the dissociation conditions, see Tomohiko Mori (New
According to Food Industry, 24 (6), 53, 1982), a low-concentration (about 0.5%) 11S globulin solution is converted into a soluble acidic subunit and an insoluble basic subunit after passing through a soluble aggregate by heating. Dissociation, and at a high concentration (5% or more), such dissociation does not occur, and the gel is formed from a soluble aggregate through a soluble giant aggregate. However, subsequent studies show that Hermansson, AM, (JAO
CS, 63 (5), 658, 1986) dissociates into acidic and basic subunits regardless of protein concentration, and states that only subsequent gelation depends on protein concentration. However, in any case, the acidic subunit and the basic subunit in the solution state can be fractionated only by means of low practicality such as ultracentrifugation.

【0004】以上の様に加熱だけでは分画が困難である
塩基性サブユニットであるが、その凝集性について、Ya
magishi T. et al.,(Agric. Biol. Chem., 44, 1575,19
80)は、11Sグロブリンの酸性サブユニットと塩基性
サブユニットが還元剤の存在下での加熱により比較的明
確に解離されることを明らかにした。この還元剤添加に
よる酸性サブユニットと塩基性サブユニットの解離効果
については、Damodaran,S. and Kinsella, E.(J. Agri
c. Food Chem., 30, 812,1982 )らは90℃で30分間
の加熱による酸性サブユニットと塩基性サブユニットの
解離後、還元剤によりシスチン間の再架橋に基づく酸性
サブユニットと塩基性サブユニットのジスルフィド結合
を介した再会合や、それから派生する複雑な重合を防止
し、塩基性サブユニットだけが疎水性凝集体を作り、分
離容易な白濁沈殿を生じるとしている。ただし、ここで
使用されている還元剤である2−メルカプトエタノール
は、食品加工には使用出来ないものである。そこで菊池
らは、食品加工上使用し得る還元剤として亜硫酸ソーダ
(Na2SO3)を用いて、この還元剤の使用による塩基性サブ
ユニットの凝集効果を利用し、120℃・1気圧(ゲー
ジ圧)で10〜20分間加熱することで酸性サブユニッ
トと塩基性サブユニットの分離・調製方法を見い出した
(特開昭63-36748号公報)。
As described above, it is a basic subunit which is difficult to fractionate only by heating.
magishi T. et al., (Agric. Biol. Chem., 44, 1575, 19
80) revealed that the acidic and basic subunits of 11S globulin are relatively clearly dissociated by heating in the presence of a reducing agent. The dissociation effect of acidic and basic subunits by the addition of this reducing agent is described in Damodaran, S. and Kinsella, E. (J. Agri
c. Food Chem., 30, 812, 1982) dissociate the acidic subunit and the basic subunit by heating at 90 ° C for 30 minutes, and then reduce the acidic subunit and the basic subunit based on the re-crosslinking between cystine with a reducing agent. The subunits are prevented from reassociating via disulfide bonds and the resulting complex polymerization, and only the basic subunits form hydrophobic aggregates, resulting in an easily separable cloudy precipitate. However, the reducing agent used here, 2-mercaptoethanol, cannot be used for food processing. Kikuchi et al. Have proposed sodium sulfite as a reducing agent that can be used in food processing.
Using (Na2SO3), the acidic subunit and the basic subunit are heated at 120 ° C. and 1 atm (gauge pressure) for 10 to 20 minutes by utilizing the aggregation effect of the basic subunit by using this reducing agent. Was found (Japanese Patent Application Laid-Open No. 63-36748).

【0005】しかし、この食品加工上使用し得る還元剤
である亜硫酸ソーダ(Na2SO3)を用いた上記の方法でも、
その添加量(0.5モル)は食品中での残存許容量(3
0ppm)を大幅に上回るもので、酸性サブユニットと
塩基性サブユニットの分離後、残存亜硫酸を煩雑な操作
を経て除去する必要がある。亜硫酸ソーダには人の摂取
量によっては急性毒性、慢性毒性のおそれがあることが
知られており、例え除去操作を加えるとは言え、これを
大量に使用することには食品衛生上に問題があると言え
る。以上の背景から、大豆タンパク質の主要成分である
11Sグロブリンから、その構成成分である酸性サブユ
ニットと塩基性サブユニットを分画・調製する場合に、
食品衛生の点からも、還元剤を使用することなく、簡便
な方法で取得するための方法が待望されていた。以上の
従来技術は、加熱方法として間接加熱(湯浴、オートク
レーブなど)であり、さらに還元剤(2−メルカプトエ
タノール又はNa2SO3など)使用による方法であり、本発
明の構成要件である直接加熱(水蒸気接触、吹き込みな
ど)及び還元剤不使用とは異なるものである。
However, the above method using sodium sulfite (Na2SO3), which is a reducing agent that can be used in food processing,
The added amount (0.5 mol) is the remaining allowable amount (3
0 ppm), and it is necessary to remove the remaining sulfurous acid through a complicated operation after separating the acidic subunit and the basic subunit. It is known that sodium sulfite may have acute or chronic toxicity depending on human intake.Thus, even if removal operation is added, using it in large quantities poses a problem in food hygiene. It can be said that there is. From the above background, when fractionating and preparing acidic subunits and basic subunits as constituents thereof from 11S globulin which is a main component of soybean protein,
From the viewpoint of food hygiene, a method for obtaining the compound by a simple method without using a reducing agent has been desired. The prior art described above uses indirect heating (hot water bath, autoclave, etc.) as a heating method, and further uses a reducing agent (2-mercaptoethanol or Na2SO3, etc.). Contact, blowing, etc.) and no reducing agent.

【0006】[0006]

【発明が解決しようとする課題】本発明は、11Sグロ
ブリンに還元剤を使用することなく食品衛生上安全で、
簡便かつ効率よく、酸性サブユニットと塩基性サブユニ
ットを分画・調製する方法及びその製品を提供すること
を課題とする。
DISCLOSURE OF THE INVENTION The present invention provides a food safe and safe product without using a reducing agent for 11S globulin.
It is an object of the present invention to provide a method for simply and efficiently fractionating and preparing an acidic subunit and a basic subunit and a product thereof.

【0007】[0007]

【課題を解決するための手段】本発明は、大豆タンパク
質の主要成分である11Sグロブリンを、150℃( 飽
和水蒸気圧のゲージ圧で約4 kgf/ cm2 で、以下、
「ゲージ圧で約4 kgf/ cm2 」と略称する。なお、
絶対圧では約5 kgf/ cm2 に相当するが、以下に特
記しない場合はゲージ圧を意味する。)以上の水蒸気と
接触させることを特徴とする、酸性サブユニット画分と
塩基性サブユニット画分を分画する方法である。更に詳
しくは、水蒸気との接触時に還元剤を全く使用しないこ
と、水蒸気と接触後に遠心分離或いは濾別すること、水
蒸気と接触後に120℃以上で1分間以上の温度保持を
行うこと、水蒸気との接触をタンパク質濃度10%以上
で行うこと、などの内何れか1つ以上の条件を用いるこ
とによる方法である。本発明は、高濃度の11Sグロブ
リン溶液を水蒸気と直接接触させる加熱方法を採用する
ことにより、酸性サブユニットと塩基性サブユニットを
解離させ、実用性のある低回転数の遠心分離やろ過によ
り、二者を分画出来ることを見い出し、本発明を達成し
た。
According to the present invention, 11S globulin which is a main component of soybean protein is prepared at 150 ° C. (at a saturated steam pressure gauge pressure of about 4 kgf / cm 2).
Abbreviated as "about 4 kgf / cm @ 2 in gauge pressure". In addition,
Absolute pressure corresponds to about 5 kgf / cm 2, but unless otherwise specified, it means gauge pressure. A) a method for fractionating an acidic subunit fraction and a basic subunit fraction, which is characterized by contacting with water vapor as described above. More specifically, no reducing agent is used at the time of contact with steam, centrifugation or filtration is performed after contact with steam, temperature is maintained at 120 ° C. or more for 1 minute or more after contact with steam, This is a method by using any one or more conditions such as performing the contact at a protein concentration of 10% or more. The present invention employs a heating method in which a high-concentration 11S globulin solution is brought into direct contact with water vapor to dissociate an acidic subunit and a basic subunit, and by centrifugation and filtration at a practically low rotational speed, The inventors have found that the two can be fractionated, and have achieved the present invention.

【0008】[0008]

【発明の実施の形態】以下、本発明を詳細に説明する。
本発明は大豆タンパク質の主要成分である11Sグロブ
リンから、還元剤を添加することなく加熱方法を工夫す
るだけで、塩基性サブユニットを分画可能なまでに凝集
させ、効率よく酸性サブユニットと塩基性サブユニット
を分画・調製する方法である。
BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, the present invention will be described in detail.
The present invention uses 11S globulin, which is a main component of soybean protein, by simply devising a heating method without adding a reducing agent, by aggregating a basic subunit to a fractionable level, and efficiently combining an acidic subunit with a base. This is a method for fractionating and preparing a sex subunit.

【0009】先ず、本発明の用語を説明する。11Sグ
ロブリンとは、一般に可溶性の球状タンパク質の総称で
あるグロブリンの中、分子量の超遠心沈降係数が11S
に相当するものを言う。グロブリンの分子量分布で2
S、7S、11S、15Sが存在し、その内、7Sと1
1Sが大豆の様な豆科植物の貯蔵タンパク質には多量に
含まれていることが知られている。なお、大豆の11S
グロブリンはグリシニンとも言われている。酸性サブユ
ニットとは、上記の11Sグロブリンの構成成分の一つ
で、酸性アミノ酸に富んでいる。塩基性サブユニットと
は、11Sグロブリンの構成成分の他の一つで、塩基性
アミノ酸に富んでいる。この塩基性サブユニットと上記
の酸性サブユニットとは、1個のジスルフィド(S−
S)結合により結合し、中間サブユニットを形成してい
る。11Sグロブリンはこの中間サブユニットが6個会
合したものである。
First, terms of the present invention will be described. 11S globulin is a globulin that is generally a generic name of soluble globular proteins, and has an ultracentrifugal sedimentation coefficient of molecular weight of 11S.
Say the equivalent of 2 in molecular weight distribution of globulin
S, 7S, 11S, and 15S exist, of which 7S and 1S
It is known that 1S is contained in large amounts in storage proteins of legumes such as soybeans. In addition, 11S of soybean
Globulin is also called glycinin. The acidic subunit is one of the components of the above 11S globulin, and is rich in acidic amino acids. The basic subunit is another component of the 11S globulin and is rich in basic amino acids. This basic subunit and the above-mentioned acidic subunit consist of one disulfide (S-
S) linked by a bond to form an intermediate subunit. 11S globulin is a combination of six of these intermediate subunits.

【0010】150℃以上の水蒸気とは、気体状態にあ
る水すなはち水蒸気のうち、その飽和水蒸気圧が約4 k
gf/ cm2 (ゲージ圧。絶対圧では約5 kgf/ cm
2 )以上あるものを言う。還元剤とは、化学において還
元反応を起こさせる試薬で、種々の金属、金属の水素化
合物、低原子価の金属イオン(Fe++、Sn++、Ti+3
など)、低い酸化状態の陰イオン(S--、SO3 --、S
2 O3 --など)、水素、炭素、一酸化炭素、ケイ素、イ
オウ、ヨウ化水素などが代表的還元剤である。なお、食
品の生産においては物質名、品質規格、使用基準などの
条件つきで限定的に使用が認可されている。例示とし
て、亜硫酸ナトリウム(使用基準:限定食品以外の一般
食品に対してSO2 として30ppm以下)、二硫化硫
黄(使用基準:限定食品以外の一般食品に対してSO2
として30ppm以下)などがある。
[0010] The water vapor of 150 ° C or higher is defined as a gas, ie, a water vapor having a saturated vapor pressure of about 4 k.
gf / cm2 (gauge pressure. Absolute pressure is about 5 kgf / cm2)
2) Say what you have. Reducing agents are reagents that cause a reduction reaction in chemistry, and include various metals, metal hydrides, and low-valent metal ions (Fe ++, Sn ++, Ti + 3).
), Low oxidation state anions (S--, SO3-, S
2 O3-), hydrogen, carbon, carbon monoxide, silicon, sulfur, hydrogen iodide and the like are typical reducing agents. In the production of food, limited use is approved with conditions such as substance names, quality standards, and use standards. For example, sodium sulfite (standard of use: 30 ppm or less as SO2 for general foods other than limited foods), sulfur disulfide (standard of use: SO2 for general foods other than limited foods)
30 ppm or less).

【0011】分画するとは、固体と液体を分けることを
指し、これが出来る方法・装置であれば何れでも良く、
例示として遠心分離やろ別などがある。遠心分離とは、
液体中にある固体の粒子を、遠心力を利用して密度の差
により分離・分画する方法を指し、本発明ではこの遠心
分離が出来る方法であれば限定せず用いることが出来
る。ろ別とは、多孔質の物体であるフィルターを通過さ
せることによって、液体とその中に含まれる固体とを分
離する操作を言う。フィルターとしては、工業的には濾
布、砂、海綿状金属等の多孔質体等が用いられる。タン
パク質濃度は、一定量の供試物を公知のケルダール法又
はそれに準じる方法により窒素を定量し窒素係数(6.
25)を乗じて算出する。
The term "fractionation" refers to the separation of a solid and a liquid.
Examples include centrifugation and filtration. What is centrifugation?
It refers to a method of separating and fractionating solid particles in a liquid by a difference in density using centrifugal force. In the present invention, any method capable of performing this centrifugation can be used without limitation. Filtration refers to an operation of separating a liquid and a solid contained therein by passing through a filter which is a porous object. As the filter, a filter cloth, sand, a porous body such as spongy metal or the like is industrially used. The protein concentration is determined by quantifying nitrogen by a known Kjeldahl method or a method analogous thereto using a constant amount of the test substance, and determining the nitrogen coefficient (6.
25).

【0012】実質的に還元剤を含まない画分とは、原料
大豆由来によらない還元剤を大豆の11Sグロブリンの
水蒸気との接触時に用いずに分画・調製した画分で、還
元剤の残存が不検出又は30ppm以下程度、好ましく
は10ppm以下のものを意味している。その分析測定
方法は、例示として亜硫酸塩ではSO2 としてアルカリ
滴定法(試験法A)又は比色法(試験法B。試験法A、
Bとも厚生省食品化学課編の「食品中の食品添加物分析
法)による。
The fraction containing substantially no reducing agent is a fraction fractionated and prepared without using a reducing agent not derived from the raw material soybean at the time of contact with steam of 11S globulin of soybean. It means that the residue is not detected or about 30 ppm or less, preferably 10 ppm or less. The analytical measurement method is, for example, an alkali titration method (test method A) or a colorimetric method (test method B.
B is based on "Food Additive Analysis Method in Food" edited by Food Chemistry Division, Ministry of Health and Welfare.

【0013】本発明者らの検討によれば、次のことが判
った。 1)120℃以下の温度で酸性サブユニットと塩基性サ
ブユニットを分画させるには、亜硫酸ソーダを最低35
ミリモルは添加しなければならない。 2)この場合、分離された酸性サブユニットと塩基性サ
ブユニットには、約4,000〜5,000ppmもの
亜硫酸が残存していた。 3)その残存亜硫酸の除去操作すなはち、食品中での残
存許容量以下にまで低減させるには、酸性サブユニット
の場合、5%水溶液を80℃以上で10分間加熱し、p
H4.0〜5.0に調整して酸性サブユニットを沈澱さ
せ、遠心分離にて回収する操作を3回以上繰り返す必要
がある。 4)同じく塩基性サブユニットの場合は、5%懸濁液を
80℃以上で10分間加熱し、遠心分離にて塩基性サブ
ユニットを回収する操作を3回以上繰り返す必要があ
る。以上のことが判った。
According to the study by the present inventors, the following has been found. 1) To fractionate the acidic subunit and the basic subunit at a temperature of 120 ° C. or lower, sodium sulfite must be at least 35%.
Mmol must be added. 2) In this case, about 4,000 to 5,000 ppm of sulfurous acid remained in the separated acidic subunit and basic subunit. 3) An operation of removing the residual sulfurous acid, that is, in order to reduce the residual sulfurous acid to below the allowable amount in food, in the case of an acidic subunit, a 5% aqueous solution is heated at 80 ° C. or more for 10 minutes,
It is necessary to repeat the operation of adjusting the H to 4.0 to 5.0 to precipitate the acidic subunit and recovering by centrifugation three times or more. 4) In the case of the basic subunit, it is necessary to repeat the operation of heating the 5% suspension at 80 ° C. or higher for 10 minutes and collecting the basic subunit by centrifugation at least three times. The above was found.

【0014】そこで、本発明者らは鋭意検討の結果、次
のことを見い出した。 5)酸性サブユニットと塩基性サブユニットは還元剤を
添加せずとも、100℃以上で10分間以上加熱するこ
とで分離する。 6)しかし、100℃で10分間程度の加熱では、塩基
性サブユニットが凝集沈澱せず、加熱後の溶液を酸性サ
ブユニットと塩基性サブユニットに分画するのは容易で
はない。 7)塩基性サブユニットの凝集沈澱が、150℃(ゲー
ジ圧で約4 kgf/ cm2)の水蒸気と1分間、直接に接
触(該水蒸気を吹き込むなどの方法で)させて得られ
た。。 以上のことを見い出した。従って、酸性サブユニットと
塩基性サブユニットの分画の際に、還元剤を添加するこ
となく加熱方法を工夫するだけで、塩基性サブユニット
を分画可能なまでに凝集させ、効率よく酸性サブユニッ
トと塩基性サブユニットを分画・調製する方法を見い出
し、残存する還元剤濃度が実質的に含まない、ないしは
30ppm以下、多くの場合に10ppm以下の酸性サ
ブユニットと塩基性サブユニットを得ることが出来た。
上記の150℃(ゲージ圧約4Kgf/cm2 )以上
は、11Sグロブリン溶液の品温が150℃以上に達せ
られる温度であれば良く、実用上は150℃〜275℃
(約60Kgf/cm2 )、効率的に好ましくは150
℃〜214℃(約20Kgf/cm2 )であっても良
い。直接の接触時間は、11Sグロブリン溶液の品温が
150℃以上に達せられる時間であれば良く、実用上は
瞬間的な2〜3秒以上から1時間程度であろうが、生産
効率的に好ましくは2秒以上から10分間程度でも良
い。従来技術の間接加熱(湯浴、オートクレーブなど)
に比べて、本発明の直接加熱(水蒸気接触、吹き込みな
ど)の効果の差は塩基性サブユニットの凝集沈澱化と分
画化であり、意外な発見であった。この効果差のメカニ
ズムは未解明であるが、11Sグロブリン水溶液にノズ
ルなどから吹き込まれる水蒸気による急速な攪拌力・剪
断力などや、急激な加熱により11Sグロブリンの構造
変化による塩基性サブユニットの解離と沈澱化が生じる
のではないかと推察される。
The present inventors have assiduously studied and found the following. 5) The acidic subunit and the basic subunit are separated by heating at 100 ° C. or more for 10 minutes or more without adding a reducing agent. 6) However, when heated at 100 ° C. for about 10 minutes, the basic subunit does not aggregate and precipitate, and it is not easy to fractionate the heated solution into an acidic subunit and a basic subunit. 7) An aggregate precipitate of the basic subunit was obtained by direct contact (eg, by blowing the steam) with steam at 150 ° C. (about 4 kgf / cm 2 at a gauge pressure) for 1 minute. . We have found the above. Therefore, when the acidic subunit and the basic subunit are fractionated, the basic subunit is aggregated to the extent that it can be fractionated by simply devising a heating method without adding a reducing agent, and the acidic subunit is efficiently separated. To find a method for fractionating / preparing units and basic subunits, to obtain acidic subunits and basic subunits substantially free of residual reducing agent concentration, or 30 ppm or less, and often 10 ppm or less. Was completed.
The above 150 ° C. (gauge pressure of about 4 kgf / cm 2) or higher may be any temperature at which the product temperature of the 11S globulin solution can reach 150 ° C. or higher.
(About 60 Kgf / cm @ 2), preferably 150
C. to 214.degree. C. (about 20 kgf / cm @ 2). The direct contact time may be any time during which the temperature of the 11S globulin solution can reach 150 ° C. or higher. In practice, it will be about 2 to 3 seconds or more in an instant, but about 1 hour is preferable in terms of production efficiency. May be from 2 seconds or more to about 10 minutes. Conventional indirect heating (hot water bath, autoclave, etc.)
The difference in the effect of the direct heating (water vapor contact, blowing, etc.) of the present invention, compared with that of the present invention, was agglomeration precipitation and fractionation of the basic subunit, which was an unexpected finding. The mechanism of this effect difference has not been elucidated. It is presumed that precipitation occurs.

【0015】本発明のために用いる大豆11Sグロブリ
ンは、脱脂大豆をタン・シバサキのpH分画法(Thanh,
V.H., and Shibasaki, K., J. Agric. Food Chem., 2
4, 117,1976 )での沈殿画分としても得られるが、この
文献に記載された還元剤を含む緩衝液を用いなくても、
脱脂大豆から水によって抽出された脱脂豆乳のpHを、
11Sグロブリンの等電点であるpH6.4 に調整し、冷却
するだけでも11Sグロブリンを得ることが出来る。
[0015] The soybean 11S globulin used for the present invention is prepared by converting defatted soybean to a pH-fractionation method of Tan Shibasaki (Thanh,
VH, and Shibasaki, K., J. Agric. Food Chem., 2
4, 117,1976), but without using the buffer containing a reducing agent described in this document.
The pH of defatted soy milk extracted with water from defatted soybeans,
It is possible to obtain 11S globulin simply by adjusting to pH 6.4, which is the isoelectric point of 11S globulin, and cooling.

【0016】本発明は、上記により調製した10重量%
以上、好ましくは約13〜16%にまで濃縮された11Sグ
ロブリン水溶液に、直接、水蒸気と接触させることで、
酸性サブユニットと塩基性サブユニットに分離させるも
ので、その際、タンパク質濃度、温度、加熱時間等の条
件を設定する。発明者らの実験結果によると、タンパク
質濃度10%以上、好ましくは 13.5 〜15.2% 、pHを
中性域、例示として7.0 〜8.0 に調整した11Sグロブ
リン水溶液に150 ℃(水蒸気圧のゲージ圧で約4 kgf
/ cm2)以上の水蒸気を吹き込み、その後液温を120
℃以上、例示として好ましくは120 〜150 ℃程度の高温
に1分間以上保持することが、酸性サブユニットと塩基
性サブユニットを効率よく分画する上で最適条件である
ことを見い出したので、実際にはこの条件を基準として
加熱条件を設定すると良い。
The present invention relates to 10% by weight prepared as described above.
As described above, preferably, the 11S globulin aqueous solution concentrated to about 13 to 16% is brought into direct contact with water vapor,
The acidic subunit and the basic subunit are separated from each other. At this time, conditions such as protein concentration, temperature, and heating time are set. According to the experimental results of the inventors, a protein concentration of 10% or more, preferably 13.5 to 15.2%, and a pH of 11S globulin aqueous solution adjusted to a neutral region, for example, 7.0 to 8.0, were added at 150 ° C. 4 kgf
/ cm2) or more, and then the liquid temperature is set to 120
It has been found that holding at a high temperature of at least 120 ° C., for example, preferably at a temperature of about 120 to 150 ° C. for at least 1 minute is the optimal condition for efficient fractionation of acidic subunits and basic subunits. It is preferable to set heating conditions based on these conditions.

【0017】本発明では、上記条件に基づいて11Sグ
ロブリンを加熱して得られた反応液を遠心分離あるい
は、ろ別により上澄と沈殿に分画し、上澄画分はそのま
ま噴霧乾燥あるいは凍結乾燥し、沈殿画分も水に懸濁
後、噴霧乾燥あるいは凍結乾燥して、上澄画分を酸性サ
ブユニットとして、沈殿画分を塩基性サブユニットとし
て得ることが出来る。
In the present invention, the reaction solution obtained by heating 11S globulin under the above conditions is separated into a supernatant and a precipitate by centrifugation or filtration, and the supernatant fraction is directly spray-dried or frozen. After drying, the precipitate fraction is also suspended in water and then spray-dried or freeze-dried to obtain the supernatant fraction as an acidic subunit and the precipitate fraction as a basic subunit.

【0018】こうして得られる各画分にはそれぞれのサ
ブユニットの混入がなく、還元剤を使用していないの
で、加熱後の煩雑な脱還元剤操作が不要である。
The fractions thus obtained do not contain the respective subunits and do not use a reducing agent, so that a complicated operation of the reducing agent after heating is unnecessary.

【0019】[0019]

【実施例】以下に、本発明の有効性を実施例と共に示す
が、これらの例示によって本発明の技術思想が限定され
るものではない。
EXAMPLES The effectiveness of the present invention will be described below together with examples, but the technical idea of the present invention is not limited by these examples.

【0020】[0020]

【実施例1】11Sグロブリンの調製 脱脂大豆に1:10の重量割合で水を加え、随時pHを7.0
に調整しながら1時間撹拌し、この混合物を遠心分離
(4,000 r.p.m., 20℃で10分間) し、得られた上澄液
をpH6.4 に調整して、4 ℃にて一晩放置して、遠心分離
(4,000 r.p.m., 4℃にて10分間) して得られた沈殿物を
11Sグロブリンとした。このようにして得られた11
SグロブリンをSDS-ポリアクリルアミドゲル電気泳動に
供し、その後染色された蛋白質のバンドの染色度の測定
から、純度として80%以上あり、以下の検討に十分耐
えうる純度であることを確認した。
Example 1 Preparation of 11S globulin Water was added to defatted soybean at a weight ratio of 1:10, and the pH was adjusted to 7.0 as needed.
Stir for 1 hour while adjusting the mixture to centrifuge.
(4,000 rpm, 20 ° C for 10 minutes), adjust the resulting supernatant to pH 6.4, leave at 4 ° C overnight, and centrifuge
(4,000 rpm, 4 ° C. for 10 minutes), and the obtained precipitate was defined as 11S globulin. 11 obtained in this way
S-globulin was subjected to SDS-polyacrylamide gel electrophoresis, and thereafter, the degree of staining of the stained protein band was measured. From the result, it was confirmed that the purity was 80% or more, and the purity was sufficient to withstand the following examination.

【0021】[0021]

【実施例2】11Sグロブリンより各サブユニットの分
離・分画 上記により得られた14.2% 濃度の11Sグロブリン溶液
を、吹き込み水蒸気圧6kgf/cm2の水蒸気殺菌装置に供
し、2秒間の水蒸気吹き込み後、140 ℃にて1分間の高
温を保持した。溶液が50℃程度にまで冷却されてから、
遠心分離(8,000 r.p.m.,20℃前後にて10分間) して上
澄と沈殿に分画した。上澄はそのまま凍結乾燥し、沈殿
には沈殿の重量とほぼ等量の水を加えて懸濁した後、凍
結乾燥した。この様にして得られた各サブユニットをSD
S-ポリアクリルアミドゲル電気泳動に供してそのパター
ンを調べた。その結果、上澄画分はその大部分が酸性サ
ブユニットから成り、塩基性サブユニットの混入は認め
られなかった。また、沈殿画分は塩基性サブユニットが
占め、酸性サブユニットは検出されなかった。
Example 2 Separation and fractionation of each subunit from 11S globulin The 14.2% concentration 11S globulin solution obtained above was supplied to a steam sterilizer having a steam pressure of 6 kgf / cm2, and steam was blown for 2 seconds. The high temperature was maintained at 140 ° C. for 1 minute. After the solution has cooled to around 50 ° C,
The mixture was centrifuged (8,000 rpm, about 20 ° C. for 10 minutes) to fractionate into a supernatant and a precipitate. The supernatant was freeze-dried as it was. The precipitate was suspended by adding water in an amount substantially equal to the weight of the precipitate, and then freeze-dried. Each subunit obtained in this way is
The pattern was examined by subjecting to S-polyacrylamide gel electrophoresis. As a result, most of the supernatant fraction was composed of acidic subunits, and no contamination with basic subunits was observed. The precipitated fraction was occupied by basic subunits, and no acidic subunit was detected.

【0022】[0022]

【発明の効果】本発明により、11Sグロブリンから、
還元剤を使用しない、水蒸気吹き込み加熱などの食品衛
生の点で安全で、簡便かつ効率よく酸性サブユニットと
塩基性サブユニットを提供することが出来る様になっ
た。
According to the present invention, from 11S globulin,
It is possible to provide an acidic subunit and a basic subunit safely, easily and efficiently in terms of food hygiene such as steam blowing heating without using a reducing agent.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明により分離された酸性サブユニット(
3)と塩基性サブユニット( 4)のSDS-ポリアクリルア
ミドゲル電気泳動による泳動パターンを、精製の各ステ
ップのサンプルも含めて示したものである。
FIG. 1 shows an acidic subunit separated according to the present invention (
The electrophoresis pattern of SDS-polyacrylamide gel electrophoresis of 3) and basic subunit (4) is shown, including the sample of each purification step.

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】大豆タンパク質の主要成分である11Sグ
ロブリンを、150℃(飽和水蒸気圧のゲージ圧で約4
kgf/ cm2)以上の水蒸気と接触させることを特徴と
する、酸性サブユニット画分と塩基性サブユニット画分
を分画する方法。
(1) 11S globulin which is a main component of soybean protein is prepared at 150 ° C. (at a saturated steam pressure gauge pressure of about 4 ° C.).
A method for fractionating an acidic subunit fraction and a basic subunit fraction, which is carried out by contacting water vapor of not less than KGf / cm2).
【請求項2】11Sグロブリンを水蒸気と接触させる時
に還元剤を添加すること無く、実質的に還元剤を含まな
い画分である請求項1に記載の方法。
2. The method according to claim 1, wherein the fraction is substantially free of a reducing agent without adding a reducing agent when contacting 11S globulin with water vapor.
【請求項3】水蒸気と接触後、塩基性サブユニット画分
である沈澱と酸性サブユニット画分である上澄液とを分
画する請求項1又は2に記載の方法。
3. The method according to claim 1, wherein after contacting with water vapor, a precipitate as a basic subunit fraction and a supernatant as an acidic subunit fraction are fractionated.
【請求項4】水蒸気と接触後、120℃以上の温度で1
分間以上保持する請求項1から3のいずれかに記載の方
法。
4. After contact with water vapor, the temperature of the
The method according to any one of claims 1 to 3, wherein the method is held for at least one minute.
【請求項5】水蒸気との接触を11Sグロブリンのタン
パク質濃度10重量%以上にし、中性域のpHで行う請
求項1から4のいずれかに記載の方法。
5. The method according to claim 1, wherein the contact with the water vapor is carried out at a protein concentration of 11S globulin of 10% by weight or more and at a neutral pH.
【請求項6】請求項1から請求項5のいずれかに記載の
方法によって得られる製品。
6. A product obtained by the method according to claim 1.
JP37289998A 1998-12-28 1998-12-28 Method for fractionating and preparing subunits from soybean 11S globulin and its product Expired - Fee Related JP3644283B2 (en)

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WO2002028198A1 (en) * 2000-10-02 2002-04-11 Fuji Oil Company, Limited Fractionated soybean protein and process for producing the same
JP2007116961A (en) * 2005-10-27 2007-05-17 Fuji Oil Co Ltd Method for producing gel, and food utilizing the gel
JP2007518409A (en) * 2004-01-20 2007-07-12 バーコン ニュートラサイエンス (エムビー) コーポレイション Novel canola protein isolate
EP1905312A1 (en) * 2005-05-30 2008-04-02 Fuji Oil Company, Ltd. Fractionated soybean protein material, processed soybean suitable for the material, and processes for production of the soybean protein material and the processed soybean

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2002028198A1 (en) * 2000-10-02 2002-04-11 Fuji Oil Company, Limited Fractionated soybean protein and process for producing the same
AU2001292291B2 (en) * 2000-10-02 2006-03-02 Fuji Oil Company, Limited Fractionated soybean protein and process for producing the same
US7226633B2 (en) 2000-10-02 2007-06-05 Fuji Oil Company, Limited Fractionated soybean proteins and method for producing the same
KR100754051B1 (en) * 2000-10-02 2007-08-31 후지 세이유 가부시키가이샤 Fractionated soybean protein and process for producing the same
JP2007518409A (en) * 2004-01-20 2007-07-12 バーコン ニュートラサイエンス (エムビー) コーポレイション Novel canola protein isolate
EP1905312A1 (en) * 2005-05-30 2008-04-02 Fuji Oil Company, Ltd. Fractionated soybean protein material, processed soybean suitable for the material, and processes for production of the soybean protein material and the processed soybean
EP1905312A4 (en) * 2005-05-30 2011-01-12 Fuji Oil Co Ltd Fractionated soybean protein material, processed soybean suitable for the material, and processes for production of the soybean protein material and the processed soybean
US9107428B2 (en) 2005-05-30 2015-08-18 Fuji Oil Company, Limited Fractionated soybean protein material, processed soybean suitable for the material, and processes for production of the soybean protein material and the processed soybean
JP2007116961A (en) * 2005-10-27 2007-05-17 Fuji Oil Co Ltd Method for producing gel, and food utilizing the gel

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