JP3387423B2 - Method for producing soy protein with excellent flavor and gel properties - Google Patents
Method for producing soy protein with excellent flavor and gel propertiesInfo
- Publication number
- JP3387423B2 JP3387423B2 JP24742198A JP24742198A JP3387423B2 JP 3387423 B2 JP3387423 B2 JP 3387423B2 JP 24742198 A JP24742198 A JP 24742198A JP 24742198 A JP24742198 A JP 24742198A JP 3387423 B2 JP3387423 B2 JP 3387423B2
- Authority
- JP
- Japan
- Prior art keywords
- neutralization
- treatment
- soybean protein
- curd
- solution
- 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 - Lifetime
Links
Description
【0001】[0001]
【発明の属する技術分野】この発明は、風味が良く、ゲ
ル物性に優れた大豆蛋白質の製造法に関するものであ
る。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing soybean protein having a good flavor and excellent gel properties.
【0002】[0002]
【従来の技術】一般的に、高分子の水和の場合、例えば
多糖類あるいはゼラチンの水和にみられるように、水温
が室温乃至それより少し高い温度域では、水和速度が遅
いことが知られている。大豆蛋白質も高分子であり、水
和・中和に、時間がかかるのが通常である。大豆蛋白質
の中和液は、酸性凝集物(カード)にアルカリ液を添加
して調製される。その際、カード中の大豆蛋白質は不溶
化しており、アルカリ添加により、大豆蛋白質が水和溶
解しつつ、pHが中性に徐々におちついていくと考えら
れる。この操作で、加熱して水和を促進させようとする
と大豆蛋白質は変性し、不溶化が起こるので高温処理は
避けなければならない。大豆蛋白の変性温度以下の温度
で時間をかけて、水和・中和を行う必要があった。2. Description of the Related Art Generally, in the case of hydration of polymers, the hydration rate is slow in the temperature range of room temperature or slightly higher than room temperature, as seen in the hydration of polysaccharides or gelatin. Are known. Soy protein is also a high polymer, and it usually takes time to hydrate and neutralize. The soybean protein neutralization solution is prepared by adding an alkaline solution to the acidic aggregate (curd). At that time, the soybean protein in the curd is insolubilized, and it is considered that the addition of alkali causes the soybean protein to be hydrated and dissolved, and the pH gradually decreases to neutral. In this operation, soybean protein is denatured and insolubilized when heated to accelerate hydration, so high temperature treatment must be avoided. It was necessary to perform hydration / neutralization at a temperature below the denaturation temperature of soybean protein for a long time.
【0003】本発明者らの知見では、上記のように中和
で時間がかかることによって、以下のような欠点が生じ
ると考えられる。即ち、菌の増殖と酸化による風味の劣
化である。菌は、原料とする大豆に付着する土壌菌が多
く存在し、工程中で低く抑えているが中和工程で増加す
る傾向がある。また酸化についても中和液中に存在する
残存脂質が攪拌により空気と混ざる等して、さらに酸化
され、悪風味の生成を促進する傾向がある。このことか
ら、中和時間を短くすることで風味の悪化が防げると考
えられた。実際、中和時間を短くするとこれらは改善さ
れる。しかし蛋白質の水和が不十分な場合、中和液の溶
解度が低くなり、その中和液で調製した分離大豆蛋白質
のゲル物性が著しく低下する問題が生じた。According to the knowledge of the present inventors, it is considered that the following disadvantages occur due to the time required for neutralization as described above. That is, it is the deterioration of flavor due to the growth and oxidation of bacteria. Many fungi are soil fungi that adhere to soybeans, which are the raw material, and are kept low during the process, but they tend to increase during the neutralization process. Regarding the oxidation, the residual lipids present in the neutralized solution are mixed with air by stirring, and are further oxidized, which tends to promote the production of bad taste. From this, it was considered that the deterioration of flavor could be prevented by shortening the neutralization time. In fact, shortening the neutralization time improves them. However, when the hydration of the protein is insufficient, the solubility of the neutralization solution becomes low, and the gel properties of the isolated soybean protein prepared with the neutralization solution remarkably deteriorates.
【0004】しかしながら、本発明者らは種々検討の結
果、カードを予備攪拌してカードスラリーにした後、中
和に要する量のアルカリ溶液を密閉下で注入しながら一
気に高エネルギー処理を施すことにより、溶解度の高い
中和液を瞬時に連続的に調製することが可能であること
を見いだした。さらに難しいと思われる高濃度での短時
間中和も可能であることを見いだして、この発明に到達
した。However, as a result of various investigations, the present inventors have found that after curd is preliminarily stirred into a curd slurry, a high energy treatment is carried out all at once while pouring an alkaline solution in an amount required for neutralization in a sealed manner. It was found that it is possible to instantaneously and continuously prepare a neutralizing solution having high solubility. The inventors have reached the present invention by discovering that neutralization at a high concentration, which seems to be more difficult, can be performed for a short time.
【0005】本発明者らはまた、該処理の際、カードス
ラリーを予め脱気しておくことで、風味及びゲル強度が
さらに改善されることも見い出した。The present inventors have also found that by degassing the curd slurry in advance during the treatment, the flavor and gel strength are further improved.
【0006】[0006]
【本発明が解決しようとする課題】この発明は、効率よ
く大豆蛋白質のカードを水和・中和及び加熱殺菌するこ
とで、風味・ゲル物性に優れた大豆蛋白を製造方法を提
供することにある。DISCLOSURE OF THE INVENTION The present invention provides a method for producing soybean protein excellent in flavor and gel properties by efficiently hydrating, neutralizing and heat sterilizing soybean protein curd. is there.
【0007】[0007]
【課題を解決するための手段】本発明者らは、上記のよ
うに、大豆蛋白質の酸性凝集物を予備攪拌したカードス
ラリーに、中和に要する量のアルカリを密閉下で注入し
ながら、一気に高エネルギー処理し、短時間で連続的に
大豆蛋白質の水和・中和を完了させる。さらに、この中
和液を直ちに加熱殺菌後噴霧乾燥することを特徴とする
大豆蛋白の製造法である。[Means for Solving the Problems] As described above, the present inventors suddenly injected a quantity of alkali required for neutralization into a curd slurry prepared by pre-stirring an acidic aggregate of soybean protein in a sealed manner while High energy treatment is performed to continuously complete hydration and neutralization of soybean protein in a short time. Furthermore, the soybean protein production method is characterized in that the neutralized solution is immediately sterilized by heating and then spray-dried.
【0008】[0008]
【発明の実施の形態】本発明にいう大豆蛋白質の酸性凝
集物とは、大豆蛋白質が酸添加により凝集沈澱したもの
ならどのような態様でもよいが、具体的には、大豆蛋白
質の水性抽出液から酸性沈降性画分を生じさせるもので
あるか、または大豆あるいは脱脂大豆に酸を添加して酸
沈澱大豆蛋白からホエー画分を除去したもの、といった
態様が挙げられる。BEST MODE FOR CARRYING OUT THE INVENTION The acidic aggregate of soybean protein referred to in the present invention may be any form as long as soybean protein is aggregated and precipitated by the addition of an acid, and specifically, an aqueous extract of soybean protein is used. From the acid-precipitated soybean protein by removing the whey fraction from acid-precipitated soybean protein by adding an acid to soybean or defatted soybean.
【0009】また、本発明にいう「一気に高エネルギー
処理」でないと短時間中和処理であっても大豆蛋白質の
水和・中和が不十分であり、加熱殺菌後噴霧乾燥して調
製した大豆蛋白質のゲル物性に悪影響を及ぼす。Further, unless the "high energy treatment at once" according to the present invention, hydration / neutralization of soybean protein is insufficient even with a short-time neutralization treatment, and soybean prepared by spray drying after heat sterilization is prepared. It adversely affects the gel properties of proteins.
【0010】用いる高エネルギー処理というのは、ライ
ン中で強攪拌する装置や超音波処理、高速度循環装置等
が考えられるが、最も適切なのは高圧ホモゲナイザーで
ある。この圧力を50kg/cm2 以上,好ましくは1
50kg/cm2 以上の圧力で1パスすることで目的と
する中和液の作製が可能である。また、インライン高速
攪拌機処理でも1パスで可能である。The high-energy treatment to be used may be a strong stirring device in a line, ultrasonic treatment, a high-speed circulation device, etc., but the most suitable is a high-pressure homogenizer. This pressure is 50 kg / cm 2 or more, preferably 1
The target neutralization liquid can be prepared by making one pass at a pressure of 50 kg / cm 2 or more. Further, in-line high-speed agitator treatment can be performed in one pass.
【0011】この発明において、目的とする水和・中和
の程度の目安は、後述する蛋白質の溶解度で決める。即
ち、中和液固形分10重量%,大豆蛋白質濃度9重量%
に中和液濃度を調整し、1万G,10分間遠心分離し、
沈澱しない液重量の全体の重量に対する割合を%に換算
した値を溶解度とした。その尺度で中和液の溶解度を求
め、中和液を加熱殺菌(130℃,15秒)後噴霧乾燥
した粉末状分離大豆蛋白質のゲル物性と中和液の溶解度
との関係を調べると、中和液の溶解度が80を越えると
著しくゲル値が向上し、溶解度が90をこえるとさらに
ゲル値が向上する。通常の攪拌装置(インラインホモミ
キサー)では、繰り返しを行わないで1パスした場合中
和液の溶解度は71で、ゲル値は極端に低く30であっ
た。それに対してライン中にインライン高速攪拌機(荏
原製作所製、「マイルダー」)を装備し、1パスで処理
した場合の中和液の溶解度は88であり、高圧ホモゲナ
イザー(150kg/cm2 )で1パス処理した場合で
は中和液の溶解度が95であった。In the present invention, the target degree of hydration / neutralization is determined by the protein solubility described below. That is, solid content of neutralization solution 10% by weight, soybean protein concentration 9% by weight
Adjust the concentration of the neutralizing solution to 10,000 G, centrifuge for 10 minutes,
The value obtained by converting the ratio of the weight of the liquid that did not precipitate to the total weight into% was taken as the solubility. The solubility of the neutralization solution was determined on that scale, and the relationship between the gel properties of the powdery soybean protein powder separated by spray sterilization (130 ° C, 15 seconds) and spray drying and the solubility of the neutralization solution was determined. When the solubility of the Japanese solution exceeds 80, the gel value remarkably improves, and when the solubility exceeds 90, the gel value further improves. With a normal stirrer (in-line homomixer), the solubility of the neutralization solution was 71 and the gel value was extremely low, 30 when one pass was performed without repeating. On the other hand, when the in-line high-speed stirrer (Ebara Corporation, "Milder") is installed in the line and the solubility of the neutralizing solution is 88 when processed in 1 pass, it is processed in 1 pass with a high pressure homogenizer (150 kg / cm2). In that case, the neutralization solution had a solubility of 95.
【0012】特に、密閉下で短時間にインライン高速攪
拌機、高圧ホモゲナイザーで水和・中和を行うことによ
り、カード調製から中和、殺菌、乾燥までの間の時間を
大幅に短縮してもゲル値の高い中和液を調製できる。ま
た、カードを脱気処理し、ライン中で、即ち密閉下連続
的に水和・中和処理することで、中和処理中の酸素濃度
も抑えられる。これらの結果、菌の増殖が抑えられ、酵
素的な酸化も抑制された風味の良い中和液が調製可能と
なる。In particular, by performing hydration / neutralization with an in-line high-speed stirrer and a high-pressure homogenizer for a short time in a sealed state, even if the time from card preparation to neutralization, sterilization, and drying is greatly shortened, gel A high-value neutralizing solution can be prepared. Further, by degassing the curd and continuously performing hydration / neutralization treatment in the line, that is, under closed condition, the oxygen concentration during the neutralization treatment can be suppressed. As a result, it is possible to prepare a neutralizing liquid with a good taste in which the growth of bacteria is suppressed and the enzymatic oxidation is suppressed.
【0013】この様な処理をした中和液のpHは、好まし
くは6.5 以上、さらに好ましくは7.0 以上の中性乃至微
アルカリ性であるが、目的に応じて調整出来る。The pH of the neutralized solution treated as described above is preferably 6.5 or more, more preferably 7.0 or more neutral to slightly alkaline, but can be adjusted according to the purpose.
【0014】更に、水和・中和後直ちに加熱殺菌、噴霧
乾燥することにより、工程中での酸化を抑制し、風味が
良好な大豆蛋白質を得ることができる。Furthermore, by heating and sterilizing immediately after hydration / neutralization and spray-drying, oxidation in the process can be suppressed, and soybean protein having a good flavor can be obtained.
【0015】[0015]
【実施例】以下、実施例により本発明の実施様態を具体
的に説明するが、本発明がこれらによってその技術範囲
が限定されるものではない。EXAMPLES Hereinafter, the embodiments of the present invention will be specifically described with reference to Examples, but the technical scope of the present invention is not limited by these.
【0016】実施例1
不二製油(株)製の低変性脱脂大豆フレーク(NSI 9
0)10kgに15倍の40℃の温水を加え、1NのNa
OH溶液でpH7.5 に調整した。これを3時間攪拌抽出を行
ったのち、遠心分離機によりオカラ成分を除去し、脱脂
豆乳を得た。これに1Nの塩酸を加え、pHを4.5に
調整し、大豆蛋白質成分を沈澱させ、遠心分離機にて回
収し、分離大豆蛋白カード(以下「カード」という。)
を得た。このカードの固形分は約40重量%であり、こ
の固形分中における粗蛋白質純度は95重量%であっ
た。Example 1 Low-denaturation defatted soybean flakes (NSI 9 manufactured by Fuji Oil Co., Ltd.)
0) Add 15N of 40 ℃ warm water to 10kg and add 1N Na
The pH was adjusted to 7.5 with an OH solution. This was stirred and extracted for 3 hours, and then the okara component was removed by a centrifuge to obtain defatted soymilk. To this, 1N hydrochloric acid was added to adjust the pH to 4.5, the soybean protein component was precipitated, collected by a centrifuge, and separated soybean protein curd (hereinafter referred to as "curd").
Got The solid content of this curd was about 40% by weight, and the crude protein purity in this solid content was 95% by weight.
【0017】カードに水を加えて予備攪拌し、固形分1
5重量%のカードスラリーを調整した。このカードスラ
リーに、中和に要するアルカリ量を算出し、1NのNaOH
溶液を密閉下(空気に触れること無く)連続的に注入し
ながら高圧ホモゲナイザーに送液した。高圧ホモゲナイ
ザーの圧力は150kg/cm2 で1パス処理を行っ
た。この中和液を直ちに加熱殺菌(130℃,15秒)
し、噴霧乾燥して粉末状分離大豆蛋白質を得た。Water is added to the curd and preliminarily stirred to obtain a solid content of 1
A 5 wt% curd slurry was prepared. Calculate the amount of alkali needed for neutralization in this curd slurry, and add 1N NaOH
The solution was sent to a high-pressure homogenizer while continuously injecting it closed (without touching air). The pressure of the high-pressure homogenizer was 150 kg / cm @ 2 and one pass treatment was performed. Immediately heat sterilize this neutralized solution (130 ° C, 15 seconds)
And spray-dried to obtain powdery soybean protein isolate.
【0018】[0018]
【実施例2】実施例1と同様に調製したカードスラリー
を、実施例1と同じ方法でアルカリを密閉下連続的に注
入しながらインライン高速攪拌機(荏原製作所製、「マ
イルダー」)に送液し、1パス処理を行った。この中和
液を直ちに加熱殺菌(130℃,15秒)し、噴霧乾燥
して粉末状分離大豆蛋白質を得た。Example 2 The curd slurry prepared in the same manner as in Example 1 was fed to an in-line high-speed stirrer (“Milder” manufactured by EBARA CORPORATION) while continuously injecting an alkali in a sealed manner in the same manner as in Example 1. One pass processing was performed. This neutralized solution was immediately sterilized by heating (130 ° C., 15 seconds) and spray-dried to obtain powdered soybean protein isolate.
【0019】[0019]
【実施例3】実施例1と同様に調製したカードスラリー
を、脱気装置にかけ、脱気処理を行った。この脱気カー
ドスラリーを、実施例1と同じ方法でアルカリを密閉下
連続的に注入しなが高圧ホモゲナイザーに送液し、1パ
ス処理を行った。この中和液を直ちに加熱殺菌(130
℃,15秒)し、噴霧乾燥して粉末状分離大豆蛋白質を
得た。Example 3 The curd slurry prepared in the same manner as in Example 1 was put into a deaerator and deaerated. This degassed card slurry was fed to a high-pressure homogenizer while continuously injecting an alkali in a sealed manner in the same manner as in Example 1 to perform a one-pass treatment. Immediately heat sterilize this neutralized solution (130
(15 ° C., 15 seconds) and spray-dried to obtain powdery soybean protein isolate.
【0020】[0020]
【比較例1】実施例1と同様に調製したカードスラリー
を、タンクに入れ、中和に要するアルカリ量を添加後、
インラインホモミキサーで液をタンクの底面から液面へ
循環させることにより、徐々に水和・中和を行い2時間
かけて中和した。これを加熱殺菌(130℃,15秒)
し、噴霧乾燥して粉末状分離大豆蛋白質を得た。Comparative Example 1 A curd slurry prepared in the same manner as in Example 1 was placed in a tank, and after adding an alkali amount required for neutralization,
By circulating the liquid from the bottom surface of the tank to the liquid surface with an in-line homomixer, hydration and neutralization were gradually performed, and neutralization was performed over 2 hours. Heat sterilize this (130 ℃, 15 seconds)
And spray-dried to obtain powdery soybean protein isolate.
【0021】[0021]
【比較例2】実施例1と同様に調製したカードスラリー
を、比較例1と同じ方法でアルカリを添加後、20分間
循環させ、中和した液をさらに、高圧ホモゲナイザーに
送液した。高圧ホモゲナイザーの圧力は150kg/c
m2 で1パス処理を行った。この液を加熱殺菌(130
℃,15秒)し、噴霧乾燥して粉末状分離大豆蛋白質を
得た。Comparative Example 2 A curd slurry prepared in the same manner as in Example 1 was circulated for 20 minutes after adding an alkali in the same manner as in Comparative Example 1, and the neutralized solution was further fed to a high pressure homogenizer. High pressure homogenizer pressure is 150kg / c
One pass treatment was performed at m2. Heat sterilize this solution (130
(15 ° C., 15 seconds) and spray-dried to obtain powdery soybean protein isolate.
【0022】[0022]
【比較例3】実施例1と同様に調製したカードスラリー
を、実施例1と同じ方法でアルカリを密閉下連続的に注
入しながらインラインホモミキサーに送液し、1パス処
理を行った。この中和液を直ちに加熱殺菌(130℃,
15秒)し、噴霧乾燥して粉末状分離大豆蛋白質を得
た。[Comparative Example 3] The curd slurry prepared in the same manner as in Example 1 was fed to an in-line homomixer while continuously injecting an alkali in a sealed manner in the same manner as in Example 1 to perform one-pass treatment. Immediately heat sterilize this neutralized solution (130 ° C,
15 seconds) and spray-dried to obtain a powdery soybean protein isolate.
【0023】各種調製粉末状大豆蛋白質の官能評価によ
る風味(5%溶液)と溶解度、ゲル値(20%溶液を9
0℃で20分加熱後、カードメータで測定)を以下の表
に示す。風味の官能評価は10点満点で点数が多い方が
風味が良いとし、24人のパネラーの平均値である。
−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−
カ−ド 短時間 中 和 溶解度 ゲル値 官 能
脱 気 中 和 機 械 評 価
−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−
実施例 1 × ○ 高圧ホモ 95 80 6.2
実施例 2 × ○ 高速攪拌機 88 75 6.0
実施例 3 ○ ○ 高圧ホモ 95 82 7.5
比較例 1 × × インライン ミキサー 92 80 3.0
比較例 2 × × インライン ミキサー+高圧ホモ 95 80 4.6
比較例 3 × ○ インライン ミキサー 71 30 5.8
−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−Sensory evaluation of various prepared powdery soybean proteins (5% solution) in flavor and solubility, gel value (20% solution was 9%).
After heating at 0 ° C. for 20 minutes, measurement with a card meter) is shown in the table below. Regarding the sensory evaluation of flavor, the larger the score, the better the flavor, and the average value of 24 panelists. −−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−− Solubility / Gel value Machinery Evaluation ----------------------------------------- Example 1 × ○ High pressure homo 95 80 6.2 Example 2 × ○ High-speed stirrer 88 75 6.0 Example 3 ○○ High-pressure homo 95 2 82 7.5 Comparative example 1 ×× in-line mixer 92 80 3.0 Comparative example 2 ×× in-line mixer + high-pressure homo 95 80 4. 6 Comparative Example 3 × ○ In-line Mixer 71 30 5.8 ---------------------------------------------------------------------------------------------------------------------------------------------------
【0024】ここで示すように風味に関しては、密閉下
短時間で連続的に中和すると風味が良い。また、カード
で脱気する方がさらに良い。また、例え高圧ホモゲナイ
ザー処理をしても、中和時に開放系で数十分の時間をか
けて水和・中和したものは風味が良くない(比較例
2)。ゲル物性は高圧ホモゲナイザー処理、インライン
高速攪拌機処理及び長時間をかけて中和したものが良
い。従って、風味が良く、ゲル物性の優れた大豆蛋白質
を得る為には、密閉下短時間で攪拌能力が高い高圧ホモ
ゲナイザー処理、インライン高速攪拌機処理して中和液
を調製したものが有効であることがわかる。As shown here, the flavor is good if it is neutralized continuously in a short time under sealing. It is even better to degas with a card. In addition, even if a high-pressure homogenizer treatment is carried out, the one which is hydrated and neutralized in an open system for several tens of minutes at the time of neutralization does not have a good flavor (Comparative Example 2). The physical properties of the gel are preferably those treated with a high pressure homogenizer, treated with an in-line high speed stirrer and neutralized for a long time. Therefore, in order to obtain a soybean protein having a good flavor and excellent gel properties, it is effective to prepare a neutralized liquid by high pressure homogenizer treatment with high stirring ability in a short time under sealing, in-line high speed agitator treatment. I understand.
【0025】[0025]
【発明の効果】以上説明したとおり、本願発明によって
風味がよく且つゲル物性に優れた大豆蛋白質が調製可能
であり、さらに中和機が高圧ホモゲナイザー、インライ
ン高速攪拌機である場合は高濃度の中和液を短時間で連
続的に調製できる利点がある。As described above, according to the present invention, a soybean protein having a good taste and excellent gel properties can be prepared, and when the neutralizer is a high pressure homogenizer or an in-line high speed stirrer, a high concentration of neutralization is obtained. There is an advantage that the liquid can be continuously prepared in a short time.
フロントページの続き (72)発明者 山瀬 慶子 大阪府泉佐野市住吉町1番地 不二製油 株式会社阪南事業所内 (72)発明者 澤村 紀夫 大阪府泉佐野市住吉町1番地 不二製油 株式会社阪南事業所内 (72)発明者 足立 朋彦 兵庫県神戸市兵庫区浜中町2丁目18番24 号 不二製油株式会社神戸工場内 (56)参考文献 特開 昭53−62850(JP,A) 特公 昭55−23058(JP,B1) (58)調査した分野(Int.Cl.7,DB名) A23J 1/14 - 3/16 Front page continuation (72) Keiko Yamase, 1 Sumiyoshi-cho, Izumisano-shi, Osaka Prefecture Fuji Oil Co., Ltd. Hannan Works (72) Inventor Norio Sawamura, 1 Sumiyoshi-cho, Izumisano City, Osaka Fuji Oil Co., Ltd. Hannan Works (72) Inventor Tomohiko Adachi 2-18-24 Hamanaka-cho, Hyogo-ku, Kobe-shi, Hyogo Fuji Oil Co., Ltd. Kobe factory (56) Reference JP-A-53-62850 (JP, A) JP-B-55- 23058 (JP, B1) (58) Fields surveyed (Int.Cl. 7 , DB name) A23J 1/14-3/16
Claims (4)
する量のアルカリを密閉下で注入しながら、一気に高エ
ネルギー処理し、短時間で連続的に大豆蛋白質の水和・
中和を完了させ、さらにこの中和液を直ちに加熱殺菌、
噴霧乾燥することを特徴とする大豆蛋白の製造法。1. A soy protein curd slurry is subjected to a high-energy treatment at a stretch while pouring an amount of alkali required for neutralization in a sealed manner, and continuously soaking the soy protein in a short time.
Neutralization is completed, and the neutralized solution is immediately sterilized by heating.
A method for producing soybean protein, which comprises spray drying.
モゲナイザー処理である請求項1記載の製造法。2. The method according to claim 1, wherein the high energy treatment for neutralization is a high pressure homogenizer treatment.
イン高速攪拌機処理である請求項1記載の製造法。3. The production method according to claim 1, wherein the high energy treatment for neutralization is an in-line high speed agitator treatment.
脱気処理する請求項2および3記載の製造法。4. The method according to claim 2, wherein the acidic aggregate (curd) before the neutralization treatment is degassed.
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JP24742198A JP3387423B2 (en) | 1998-09-01 | 1998-09-01 | Method for producing soy protein with excellent flavor and gel properties |
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JP24742198A JP3387423B2 (en) | 1998-09-01 | 1998-09-01 | Method for producing soy protein with excellent flavor and gel properties |
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JP2000069914A JP2000069914A (en) | 2000-03-07 |
JP3387423B2 true JP3387423B2 (en) | 2003-03-17 |
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JP5320344B2 (en) * | 2010-06-04 | 2013-10-23 | 日清オイリオグループ株式会社 | Processed livestock meat and production method thereof |
JP6061118B1 (en) * | 2015-03-18 | 2017-01-18 | 不二製油株式会社 | Chocolate-like food |
FR3065623B1 (en) * | 2017-04-28 | 2021-07-09 | Roquette Freres | IMPROVED PEA ALBUMINS, PROCESS FOR OBTAINING THEIR APPLICATIONS |
CN113080396A (en) * | 2021-04-22 | 2021-07-09 | 广西北部湾海岳农业科技有限公司 | Self-heating meat crab pot |
CN114468116A (en) * | 2022-02-22 | 2022-05-13 | 克东禹王大豆蛋白食品有限公司 | Production method of soy protein isolate with high hydration gel whiteness |
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