JPS5814812B2 - Foaming agent manufacturing method - Google Patents
Foaming agent manufacturing methodInfo
- Publication number
- JPS5814812B2 JPS5814812B2 JP51134434A JP13443476A JPS5814812B2 JP S5814812 B2 JPS5814812 B2 JP S5814812B2 JP 51134434 A JP51134434 A JP 51134434A JP 13443476 A JP13443476 A JP 13443476A JP S5814812 B2 JPS5814812 B2 JP S5814812B2
- Authority
- JP
- Japan
- Prior art keywords
- foaming agent
- alcohol
- foaming
- present
- hours
- 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
Links
Landscapes
- Confectionery (AREA)
- General Preparation And Processing Of Foods (AREA)
- Emulsifying, Dispersing, Foam-Producing Or Wetting Agents (AREA)
Description
【発明の詳細な説明】
本発明は大豆たん白より起泡性および気泡安定性にすぐ
れ、保存性ならびに風味上も好ましい起泡剤の製造法に
関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing a foaming agent that has better foaming properties and foam stability than soybean protein, and is also preferable in terms of storage stability and flavor.
更に詳しくは、従来の起泡剤に比し極めて気泡安定性に
優れたものを簡便な操作で製造する方法に関する。More specifically, the present invention relates to a method for producing a foaming agent with extremely superior foam stability compared to conventional foaming agents using a simple operation.
従来より大豆たん白等の植物たん白を酵素で加水分解し
て起泡性物質を得る方法は知られており、たとえば米国
特許第2,489,173、同3,814,816等が
ある。Methods for obtaining foamable substances by hydrolyzing plant proteins such as soybean proteins with enzymes have been known, for example, as disclosed in US Pat. No. 2,489,173 and US Pat. No. 3,814,816.
すなわち、脱脂大豆をアルカリ抽出、次いで酸沈澱して
分離たん白を得、この酸沈澱カードを水に分散させペプ
シンで加水分解したのち濾過し、濾液を噴霧乾燥する等
の方法である。That is, defatted soybeans are extracted with alkali, followed by acid precipitation to obtain separated proteins, the acid-precipitated curd is dispersed in water, hydrolyzed with pepsin, filtered, and the filtrate is spray-dried.
これらの方法に基づいて得られる起泡性物質は気泡の安
定性、溶解性に問題がありまた呈味をかなり有するとい
う欠点があり、満足すべきものではない。Foamable substances obtained based on these methods have problems with foam stability and solubility, and have the disadvantage of having a considerable taste, and are therefore unsatisfactory.
また、これらの改良法もいくつか見られるがかならずし
も充分とはいゝがたい。In addition, although some of these improvement methods have been seen, they are not always sufficient.
従来、上記の如き欠点を有しつつも大豆蛋白より得られ
る起泡剤は、フラッペ、ヌガー、スポンジケーキ、メレ
ンゲ等の菓子製造用素材として広く利用されて来たが、
その改善が強く要望されてきた。Conventionally, foaming agents obtained from soybean protein have been widely used as materials for the production of confectionery such as frappes, nougat, sponge cakes, and meringues, although they have the drawbacks mentioned above.
There has been a strong demand for improvement.
本発明者は大豆たん白の起泡性に関し研究を鋭意行った
結果、従来の如くして得た起泡剤をアルコール処理し、
アルコール可溶部を除去することにより気泡安定性が大
巾に改善されること、および起泡剤として要求される他
特性についても改善されることを知見し本発明を完成す
るに至った。As a result of intensive research into the foaming properties of soybean protein, the present inventors treated foaming agents obtained in the conventional manner with alcohol,
The present invention was completed based on the finding that the foam stability is greatly improved by removing the alcohol-soluble portion, and that other properties required as a foaming agent are also improved.
アルコール処理によりこのように起泡剤の物性が大巾に
改善される機構は明確ではないが、共存するある種の低
分子量物質が気泡安定性等を阻害しており、これがアル
コール処理にて除去されるためと考えられる。The mechanism by which the physical properties of the foaming agent are greatly improved by alcohol treatment is not clear, but certain low molecular weight substances that coexist inhibit foam stability, etc., and these can be removed by alcohol treatment. It is thought that this is because the
即ち、本発明は脱脂大豆、あるいはそれから得られる太
豆たん白または同含有物をたん白分解酵素にて部分加水
分解し、不溶物を除去した後乾燥し、次いで室温にて0
.5乃至20時間アルコール処理することによる高品質
起泡剤の製法である。That is, the present invention partially hydrolyzes defatted soybeans, or fat soybean protein obtained therefrom, or a substance containing the same with a proteolytic enzyme, removes insoluble matters, and then dries the defatted soybean at room temperature.
.. This is a method for producing high quality foaming agents by treating with alcohol for 5 to 20 hours.
本発明方法に於いて用いる大豆たん白としては特に制限
はなく、脱脂大豆、あるいはそれから得られる濃縮たん
白或いは分離たん白等の大豆たん白または同含有物が用
いられる。The soybean protein used in the method of the present invention is not particularly limited, and soybean proteins such as defatted soybeans, concentrated proteins or isolated proteins obtained therefrom, or products containing the same can be used.
その形態はどのようなものであってもよく、例えば熱変
性或いはアルコール変性したものでもよい。It may be in any form; for example, it may be heat-denatured or alcohol-denatured.
一方、使用酵素としては、ペプシン、パパイン、モルミ
ン等如何なるものでもよく、動物、植物、或いは微生物
起源のたん白分解酵素が用いられる。On the other hand, the enzyme used may be any enzyme such as pepsin, papain, mormin, etc., and proteolytic enzymes derived from animals, plants, or microorganisms are used.
本発明方法の第1段は、上記大豆たん白または同含有物
を水性溶媒中にてたん白分解酵素にて部分加水分解する
にある。The first step of the method of the present invention is to partially hydrolyze the soybean protein or its containing material in an aqueous solvent with a proteolytic enzyme.
加水分解はAPL(平均ペプチド鎖長)が4〜25程度
になる様に行うのがよい。Hydrolysis is preferably carried out so that the APL (average peptide chain length) is about 4 to 25.
また、加水分解条件は特に従来と変るところはなく、p
Hに関しては使用酵素の至適領域であり、反応温度につ
いても最も効率的に酵素が作用する領域を原料の腐販を
考慮しつつ決定すればよく、通常5°乃至60℃、好ま
しくは20°〜50℃が選択される。In addition, the hydrolysis conditions are not particularly different from conventional ones, and p
Regarding H, it is the optimum range for the enzyme used, and the reaction temperature can be determined by taking into consideration the spoilage of raw materials, and the range where the enzyme acts most efficiently, usually 5° to 60°C, preferably 20°C. ~50°C is selected.
加水分解時間は使用量により変化するが、24時間以内
をなるよう設定するのが収率並らびに製品品質上好まし
い。Although the hydrolysis time varies depending on the amount used, it is preferable to set it within 24 hours in terms of yield and product quality.
本加水分解中にpHが至適域より大巾に変化する場合に
はpHの調整を反応中に行うのが有効である。If the pH changes more widely than the optimum range during the main hydrolysis, it is effective to adjust the pH during the reaction.
次いで、一般の酵素反応と同じく酵素活性を失活せしめ
反応を停止するのであるが、これには加熱失活が有効で
ある。Next, the reaction is stopped by inactivating the enzyme activity as in general enzymatic reactions, and heat inactivation is effective for this purpose.
通常70℃以上に5分乃至30分加熱することにより失
活は完了する。Deactivation is usually completed by heating at 70° C. or higher for 5 to 30 minutes.
次いで、酵素たん白、未反応のたん白等の分子量の大き
いたん白性不溶物を除去するのであるが、使用原料が脱
脂大豆等の所謂オカラと呼ばれる繊維性物質が存在する
場合には、反応液よりまずそれら物質を除去するのが望
ましく、それには反応液のpHを7〜8に調整し不溶物
を除去するのが有利である。Next, protein insoluble substances with large molecular weights such as enzyme proteins and unreacted proteins are removed. However, if the raw material used contains fibrous substances called okara such as defatted soybeans, the reaction It is desirable to remove these substances first from the liquid, and for this purpose, it is advantageous to adjust the pH of the reaction liquid to 7 to 8 and remove insoluble matter.
次いで先述のたん白性不溶物を除去するのであるが、こ
れは反応液のpHを4〜5に調整し、濾過、遠心、デカ
ンテーション等の通常の固液分離手段にて達成すること
ができる。Next, the aforementioned proteinaceous insoluble matter is removed, which can be achieved by adjusting the pH of the reaction solution to 4 to 5 and using conventional solid-liquid separation methods such as filtration, centrifugation, and decantation. .
斯くして得られた清澄液を必要に応じpHを調整(好ま
しくはpH4〜7)した後凍結乾燥、噴霧乾燥等の方法
で乾燥することにより従来の起泡剤となるのであるが、
先述した通り本発明方法の特徴はこの乾燥品のアルコー
ル処理にある。A conventional foaming agent is obtained by adjusting the pH of the clarified liquid thus obtained (preferably to pH 4 to 7) as necessary and then drying it by a method such as freeze drying or spray drying.
As mentioned above, the feature of the method of the present invention lies in the alcohol treatment of this dried product.
すなわち、上記乾燥品をアルコールと接触せしめアルコ
ール可溶物を抽出除去するのが本発明の第二段である。That is, the second step of the present invention is to bring the dried product into contact with alcohol to extract and remove alcohol-soluble substances.
使用アルコールとしては、メタノール、エタノール、n
−プロパノール等の低級アルカノールが使用可能である
が、本発明に係る起泡剤は食品用として応用することが
多いのでエタノールが最も好ましく、その含水量は10
%未満好ましくは5%未満が望ましい。The alcohol used is methanol, ethanol, n
- Lower alkanols such as propanol can be used, but since the foaming agent according to the present invention is often used for food, ethanol is most preferred, and its water content is 10
%, preferably less than 5%.
90%未満のアルコールであっても充分効果を挙げるこ
とは可能であるが、残留固形分の吸水が多く塊状となり
やすく操作性の悪化を来し、且つ収率の低下をも免れな
いのでその使用は勧められない。Although it is possible to achieve a sufficient effect even with less than 90% alcohol, its use is not recommended because the residual solid content absorbs a lot of water and tends to form lumps, resulting in poor operability and a decrease in yield. is not recommended.
アルコールと上記乾燥品との接触方法はいかなる方式で
あってもよく、通常のバッチ式攪拌法、或いは連続抽出
法にて行うことができ、接触温度としては室温であって
も加温状態であってもよく、通常5℃乃至60’C程度
が採用される。Any method may be used to bring the alcohol and the dried product into contact with each other, and it can be carried out by a normal batch stirring method or a continuous extraction method, and the contact temperature may be room temperature or heated. Generally, a temperature of about 5° C. to 60° C. is adopted.
また、アルコールの使用量および時間は接触方式および
温度により異ってくるが、通常乾燥品に対し2倍量乃至
100倍、好ましくは5倍乃至50倍量(重量比)にて
0.5乃至20時間、一般的には1乃至10時間接触さ
せることにより抽出は完了する。The amount and time of alcohol used vary depending on the contact method and temperature, but it is usually 0.5 to 100 times the amount of the dry product, preferably 5 to 50 times the amount (weight ratio). Extraction is completed after 20 hours of contact, typically 1 to 10 hours.
アルコールおよびその抽出物は遠心分離等の方法により
除き、更に残留アルコールは加熱或いは減圧下の留去等
により完全に除去しそのまゝ乾燥するか、或いは一度水
に溶解した後噴霧乾燥、凍結乾燥等の手段にて乾燥する
ことにより製品とすることができる。Alcohol and its extracts are removed by methods such as centrifugation, and residual alcohol is completely removed by heating or distillation under reduced pressure and then dried as is, or once dissolved in water and then spray-dried or freeze-dried. It can be made into a product by drying by means such as.
本品はアルコール処理しないものに比し起泡性、気泡安
定性、特に気泡安定性に優れ、しかも呈味もほとんどな
く、所謂大豆臭や苦味を感じさせない優れたものである
。This product has excellent foaming properties and foam stability, especially foam stability, compared to products that are not treated with alcohol, and has almost no taste, with no so-called soybean odor or bitter taste.
また、吸湿性も少なく優れた保存性を有する。It also has low hygroscopicity and excellent storage stability.
以上の説明に明らかな通り、本発明に係る起泡剤は起泡
剤に要求される諸特性を高度に具備しており、またその
製法も極めて容易である。As is clear from the above explanation, the foaming agent according to the present invention has various properties required for a foaming agent to a high degree, and its manufacturing method is also extremely easy.
従って本発明は起泡剤使用分野に大いに貢献するもので
ある。Therefore, the present invention makes a significant contribution to the field of foaming agent use.
以下に実施例をあげ本発明をより詳しく説明する。The present invention will be explained in more detail with reference to Examples below.
尚、実施例における起泡性および気泡安定性の測定法は
次の通りである。The methods for measuring foamability and foam stability in Examples are as follows.
起泡性:濃度1%の試料溶液100mlを起泡性測定用
シリンダー(内径82mm、容量
1000ml)にとり定速攪拌器(東京理化社製Che
my Stirrer B−1 0 0、回転数280
0rpm)を用いて泡だたせ10分後に回転をとめ5分
後に泡の体積(A)を測定する。Foaming property: 100 ml of a sample solution with a concentration of 1% was placed in a foaming property measurement cylinder (inner diameter 82 mm, capacity 1000 ml) using a constant speed stirrer (Che manufactured by Tokyo Rika Co., Ltd.).
my Stirrer B-1 0 0, rotation speed 280
After 10 minutes, the rotation was stopped and the foam volume (A) was measured after 5 minutes.
この体積(A)とはじめの溶液の液量(100ml)と
の比を起泡性とする。The ratio between this volume (A) and the initial volume of the solution (100 ml) is defined as the foaming property.
気泡安定性:上の方法で起泡性を測定したのちそのま′
>2時間放置しふたゝび泡の体積(B)を測定する。Foam stability: After measuring the foaming property using the above method,
> Leave to stand for 2 hours and measure the volume of bubbles (B) again.
この体積(B)と起泡性測定時の泡の体積低)から求め
た泡の減少率(A−B/A×100)をもって気泡安定
性とする。The foam stability is defined as the foam reduction rate (A-B/A×100) determined from this volume (B) and the foam volume (low volume at the time of foaming property measurement).
実施例 1
醸造用脱脂大豆(窒素含有率13.8%)100gを1
0倍量の水に分散させ塩酸でpH1.5に調整した。Example 1 100g of defatted soybeans for brewing (nitrogen content 13.8%)
It was dispersed in 0 times the amount of water and adjusted to pH 1.5 with hydrochloric acid.
これにペプシン(1:10000)を脱脂大豆に対して
1%(w/w)添加し40℃にて4時間加水分解したの
ち70℃ 30分加熱して酵素を失活させた。To this was added pepsin (1:10000) at 1% (w/w) based on defatted soybean, hydrolyzed at 40°C for 4 hours, and then heated at 70°C for 30 minutes to inactivate the enzyme.
その後水酸化ナトIJウムで溶液のpHを70に調整し
遠心分離により不溶物を除去し上清は塩酸でpH4.5
にし生ずるたん白性沈澱を遠心分離によりのぞき清澄液
を得た。After that, the pH of the solution was adjusted to 70 with sodium hydroxide, insoluble matter was removed by centrifugation, and the supernatant was diluted with hydrochloric acid to pH 4.5.
The resulting proteinaceous precipitate was removed by centrifugation to obtain a clear solution.
この溶液を凍結乾燥し従来の起泡剤を得た。This solution was freeze-dried to obtain a conventional foaming agent.
上記凍結乾燥品に10倍量の95%エタノールを加え室
温で2時間可溶部を抽出し、その後遠心分離によりエタ
ノール区分を除去した。A 10-fold amount of 95% ethanol was added to the freeze-dried product to extract the soluble portion at room temperature for 2 hours, and then the ethanol fraction was removed by centrifugation.
残渣は減圧下に処理しエタノールを留去し、次いで凍結
乾燥し、改良起泡剤30gを得た。The residue was treated under reduced pressure to remove ethanol and then freeze-dried to obtain 30 g of improved foaming agent.
両起泡剤の起泡性、気泡安定性、呈味性を測定したとこ
ろ下記の通りであり、本発明による改質起泡剤の優秀性
が確認された。The foaming properties, foam stability, and taste properties of both foaming agents were measured and were as follows, confirming the superiority of the modified foaming agent according to the present invention.
Claims (1)
たは同含有物をたん白分解酵素にて部分加水分解し、分
解液より不溶物を除去した後乾燥し、次いで得られた乾
燥品とアルコールとを室温にて0.5乃至20時間接触
せしめアルコール可溶部を抽出除去することを特徴とす
る起泡剤の製造法。1 Partially hydrolyze defatted soybeans, soybean proteins obtained from them, or their contents using proteolytic enzymes, remove insoluble matter from the decomposition solution, and then dry, then mix the obtained dried product with alcohol at room temperature. A method for producing a foaming agent, which comprises contacting the foaming agent for 0.5 to 20 hours and extracting and removing the alcohol-soluble portion.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP51134434A JPS5814812B2 (en) | 1976-11-09 | 1976-11-09 | Foaming agent manufacturing method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP51134434A JPS5814812B2 (en) | 1976-11-09 | 1976-11-09 | Foaming agent manufacturing method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5358981A JPS5358981A (en) | 1978-05-27 |
| JPS5814812B2 true JPS5814812B2 (en) | 1983-03-22 |
Family
ID=15128272
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP51134434A Expired JPS5814812B2 (en) | 1976-11-09 | 1976-11-09 | Foaming agent manufacturing method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5814812B2 (en) |
-
1976
- 1976-11-09 JP JP51134434A patent/JPS5814812B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5358981A (en) | 1978-05-27 |
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