JPS58149645A - Preparation of gelatinized material - Google Patents
Preparation of gelatinized materialInfo
- Publication number
- JPS58149645A JPS58149645A JP57031978A JP3197882A JPS58149645A JP S58149645 A JPS58149645 A JP S58149645A JP 57031978 A JP57031978 A JP 57031978A JP 3197882 A JP3197882 A JP 3197882A JP S58149645 A JPS58149645 A JP S58149645A
- Authority
- JP
- Japan
- Prior art keywords
- protein
- transglutaminase
- gel
- solution
- gelatin
- 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
Links
Landscapes
- Jellies, Jams, And Syrups (AREA)
Abstract
Description
【発明の詳細な説明】 本発明は新規なゲル化物の製造法に関する。[Detailed description of the invention] The present invention relates to a novel method for producing a gelled product.
既存蛋白資源の中には、生物価が低い、機能特性が乏し
い等の理由から利用が制限されているものが多い。これ
らの蛋白資源を意図的に組織化食品會こ適するような機
能性、栄養性を有する蛋白素材に改質する技術が確立さ
れるなら、その利用度が増加するだけでなく、高品質の
蛋白食品を作りうる。改質技術の一つとして酵素修飾t
こよる改質があるが、現状では加水分解酵素tこよる改
質が主なものであり、他の酵素の利用例は少ない。Among existing protein resources, the use of many of them is restricted due to reasons such as low biological value and poor functional properties. If a technology were established to intentionally modify these protein resources into functional and nutritious protein materials suitable for organized food, it would not only increase their utilization but also produce high-quality proteins. Can make food. Enzyme modification as one of the modification techniques
Although there are other types of modification, currently the main modification is based on hydrolase t, and there are few examples of the use of other enzymes.
本発明者らはアシル転移酵素の一つであるトランスグル
タミナーゼ會こ着目し、食品蛋白中に含tの多いグルタ
ミン(Ginと略す)残基とリジン(Lysと略す)残
基開会こ架橋を形成させ、ゲル状物質を製造できること
を発見し、本発明を完成した。The present inventors focused on transglutaminase, which is one of the acyltransferases, and formed crosslinks by opening glutamine (abbreviated as Gin) residues and lysine (abbreviated as Lys) residues, which have a high T content in food proteins. They discovered that it was possible to produce a gel-like substance, and completed the present invention.
即ち、本発明は蛋白質濃度2重量%以上の蛋白含有溶液
に、トランスグルタミナーゼを蛋白If1こ対して1ユ
ニット以上、添加してゲル化させることを特徴とするゲ
ル化物の製造法である。That is, the present invention is a method for producing a gelled product, which is characterized by adding 1 unit or more of transglutaminase to 1 protein If to a protein-containing solution having a protein concentration of 2% by weight or more to form a gel.
本発明1こ用いられる蛋白質は、その起源tこ制約され
るものではなく植物性蛋白質、動物性蛋白質などいかな
るものでも使用できる。植物性蛋白質としては油糧種子
の脱脂物(脱脂大豆)及びそれらより分離した蛋白質を
挙げることができる。また、動物性蛋白質としては乳蛋
白質、ゼラチン、コラーゲン等を例示することができる
。The protein used in the present invention is not limited in its origin, and any protein such as vegetable protein or animal protein can be used. Examples of vegetable proteins include defatted oilseed products (defatted soybeans) and proteins separated from them. Furthermore, examples of animal proteins include milk protein, gelatin, and collagen.
これらの蛋白質の2重量%以上の蛋白含有溶液を調製す
る。蛋白含有溶液の濃度は比較的高いことが望ましく通
常2重量%以上、好ましくは5重量チないし15重量%
であればよい。この場合、澱粉、多糖類、調味料、着色
料、香辛料などの食品添加物を配合することができる。A protein-containing solution containing 2% by weight or more of these proteins is prepared. The concentration of the protein-containing solution is desirably relatively high, usually 2% by weight or more, preferably 5% to 15% by weight.
That's fine. In this case, food additives such as starch, polysaccharides, seasonings, colorants, and spices can be added.
これらの使用量は、後のトランスグルタミナーゼによる
ゲル化を阻害しない範囲で適宜選択して添加すればよい
。These amounts may be selected and added as appropriate within a range that does not inhibit subsequent gelation by transglutaminase.
蛋白溶液の濃度が2重量俤より少ない場合には、溶液状
態のまま、もしくは沈澱を生じゲル化しない。また、蛋
白含有溶液のpHは6ないし9であれば好ましい。When the concentration of the protein solution is less than 2 weights, it remains in a solution state or precipitates and does not gel. Further, the pH of the protein-containing solution is preferably 6 to 9.
この蛋白含有溶液にトランスグルタミナーゼを蛋白If
に対して1ユニツト以上添加してゲル化させる。このト
ランスグルタミナーゼはConnellanらの方法(
Journal of BiologicalChem
istry、 246(4)、 1093(1971
) )に従って、モルモットの肝臓より調製される。即
ち、モルモットの肝臓をシヅ糖溶液に分散させたものを
遠心分離し、上清液を回収し、これにジエチルアミノエ
チルセルロースカラムにて分画することtこよって、粗
製トランスグルコシダーゼを得る。Transglutaminase was added to this protein-containing solution.
1 unit or more is added to the gel to form a gel. This transglutaminase was prepared using the method of Connellan et al. (
Journal of Biological Chem
istry, 246(4), 1093 (1971
) Prepared from guinea pig liver according to ). That is, guinea pig liver is dispersed in a sucrose solution, centrifuged, the supernatant is collected, and this is fractionated using a diethylaminoethyl cellulose column to obtain crude transglucosidase.
これを1%硫酸プロタミンで沈澱させ、沈澱物を回収す
る。さらにこの沈澱物を0.2 M Tris−酢酸
緩衝液で洗浄後、0.05 M硫安−5mM Tris
−HCI緩衝液(2mMエチレンジアミン4酢酸(以下
EDTAと略す)を含む)を用いて抽出し、得られた抽
出液をカルポキシメチルセルロース力うムテフロタミン
を除去し、口液に硫酸アンモニウム溶液(IM ED
TAを含む)を添加し遠心分離を行ない、沈澱物を回収
する。沈澱物を10mM Trim−酢酸緩衝液(1m
M EDTA 。This is precipitated with 1% protamine sulfate and the precipitate is collected. Further, this precipitate was washed with 0.2 M Tris-acetate buffer, and then washed with 0.05 M ammonium sulfate-5 mM Tris.
-Extraction using HCI buffer (containing 2mM ethylenediaminetetraacetic acid (hereinafter abbreviated as EDTA)), extracting the resulting extract using carpoxymethylcellulose to remove muteflotamine, and adding ammonium sulfate solution (IMED) to the oral fluid.
(contains TA) and centrifugation is performed to collect the precipitate. The precipitate was diluted with 10mM Trim-acetate buffer (1m
MEDTA.
0.16 M KCIを含む)で溶解し、遠心分離した
上清液を10%アガロース(Bio Get A −0
,5M )でゲル濾過し、得られた高活性画分を限外濾
過で濃縮し、精製されたトランスグルタミナーゼを得る
。The supernatant was dissolved in 10% agarose (Bio Get A-0) and centrifuged.
, 5M), and the resulting highly active fraction is concentrated by ultrafiltration to obtain purified transglutaminase.
他のトランスグルタミナーゼの調製法としては、C1a
rkeらの方法(Archives of Bioch
emistryand Biophysics+ 79
+ 338 (1959) )がある。即ち、モル
モット肝30097こ、0.25 Mシヨ糖溶液600
−を加え、ホモゲナイズする。Other methods for preparing transglutaminase include C1a
rke et al.'s method (Archives of Bioch
emistryand biophysics+ 79
+338 (1959)). That is, 30097 pieces of guinea pig liver, 600 pieces of 0.25 M sucrose solution.
- and homogenize.
これを遠心分離し、上清を得る。Centrifuge this to obtain a supernatant.
0.01 Mとなるよう一一■■■■■■■■−酢酸ナ
トリウムを加え、酢酸にてpH,5,Or−調整し、遠
心分離する。得られた沈澱に0.06 M !Jン酸緩
衝液(pH6,5)30m添加しホモゲナイズする。Add sodium acetate to a concentration of 0.01 M, adjust the pH to 5, Or- with acetic acid, and centrifuge. 0.06 M in the resulting precipitate! Add 30 m of J acid buffer (pH 6,5) and homogenize.
この懸濁液を遠心分離し、その上清を0.001 Mリ
ン酸緩衝液(pH7,5)に対して透析し、これを粗ト
ランスグルタミナーゼ溶液として用いる方法である。This suspension is centrifuged, the supernatant is dialyzed against 0.001 M phosphate buffer (pH 7.5), and this is used as a crude transglutaminase solution.
これらの方法は、操作順序を変化させたり、添加量、濃
度、pH値分離装置などを若干変えても差しつかえない
。このようにして得たトランスグルタミナーゼの蛋白濃
度をpつ見z法(Journalof Biologi
cal Chemistry+ 193 、 266
(1951))で、酵素活性なN−カルボベンゾキシ−
し−グルタミニルグリシンとヒドロキシアミンを用いた
ヒドロキサム酸法(Journal ofBiolog
ical Chemistry、 241 (23)
+ 5618(1966))で測定すれば、調製し
た酵素溶液の比活性は6.0ないし13.0の範囲の値
を示す。また、電気泳動によって分子量を測゛定すると
8.0万ないし9,0万の範囲の値である。このトラン
スグルタミナーゼ溶液は一3071’程度の低温にて保
存し、適時解凍して使用することができる。In these methods, the order of operations may be changed or the amount added, concentration, pH value separation device, etc. may be slightly changed. The protein concentration of transglutaminase obtained in this way was measured using the p-z method (Journal of Biology).
cal Chemistry+ 193, 266
(1951)), the enzymatically active N-carbobenzoxy-
Hydroxamic acid method using glutaminylglycine and hydroxyamine (Journal of Biolog
ical Chemistry, 241 (23)
+5618 (1966)), the specific activities of the prepared enzyme solutions range from 6.0 to 13.0. Furthermore, when the molecular weight is measured by electrophoresis, the value is in the range of 80,000 to 90,000. This transglutaminase solution can be stored at a low temperature of about -3071' and thawed for use.
このようにして得られるトランスグルタミナーゼを蛋白
1tr一対して1ユニツト以上、添加してゲル化させる
。添加量が1ユニツトより少ない場合には、高粘性の溶
液となる0、また、2000ユニツトより多く添加して
も効果はそれほど変わらない。One or more units of transglutaminase thus obtained is added to each protein to form a gel. If the amount added is less than 1 unit, the solution becomes highly viscous, and even if more than 2000 units is added, the effect does not change much.
トランスグルタミナーゼで蛋白分子にGlu −Lya
架橋が生じることは知られている( J、 E、 Fo
lkAnfinsen+ J、 T、 Edsall
and F、 M、 Richards+Academ
ic Pre6Tn1.、 New York、 N、
y、+ 11J7Lp、L ) カ、i%い蛋白溶液
にトランスグルタミナーゼを作用させた時に生成される
ゲルがGlu −Lys架橋によるものである事は、以
下の実験データから推察された。Glu-Lya is added to protein molecules by transglutaminase.
It is known that crosslinking occurs (J, E, Fo
lkAnfinsen+ J, T, Edsall
and F, M, Richards+Academ
ic Pre6Tn1. , New York, N.
It was inferred from the following experimental data that the gel generated when transglutaminase is applied to a protein solution is due to Glu-Lys crosslinking.
■ トランスグルタ“ミナーゼの反応部位となるLys
残基をアセチル化及びサクシニル化したαs1カゼイン
にトランスグルタミナーゼを作用させてもゲル化しなか
った。■ Lys serves as the reaction site for transglutaminase
Even when transglutaminase was applied to αs1 casein with acetylated and succinylated residues, no gelation occurred.
■ 反応溶液中C15−S還元剤であるジチオスレイト
ールを共存させて反応を行なわせているので、S−S結
合を主体とするゲルではないO
■ 加熱・冷却して得られる通常のゼラチンゲルとトラ
ンスグルタミナーゼでゲル化させたゼラチンゲルの各々
の弾性率を測定したところ、通常のゼラチンゲルは温度
が高くなるにつれ、著しく弾性率が低下した。これはゲ
ルの網目構造をつくる架橋が共有結合などのような強い
結合でなく、二次的結合であるため、温度上昇とともに
この弱い結合が切れるためであると考えられる。とれに
比してトランスグルタミナーゼによるゲルは温度が変化
しても、その変化量は少なく、共有結合性の強いゲルで
ある事が示唆された。事実両方のゲルを4喝v上にさら
すとトランスグルタミナーゼによるゲルは、そのままで
あるが通常のゼラチンゲルは溶融した。■ Because the reaction is carried out in the coexistence of dithiothreitol, a C15-S reducing agent, in the reaction solution, it is not a gel mainly composed of S-S bonds. ■ A normal gelatin gel obtained by heating and cooling. When we measured the elastic modulus of each gelatin gel gelated with gelatin and transglutaminase, we found that the elastic modulus of normal gelatin gel decreased significantly as the temperature increased. This is thought to be because the crosslinks that form the gel network structure are secondary bonds, rather than strong bonds such as covalent bonds, and these weak bonds break as the temperature rises. Compared to this gel, the amount of change in the transglutaminase gel was small even when the temperature changed, suggesting that it is a gel with strong covalent bonds. In fact, when both gels were exposed to 4 volts, the transglutaminase gel remained intact, but the normal gelatin gel melted.
以上ヨ’) 、Glu −Lys架橋によってゲルが生
成されており、S−sの架橋tこよるゲルではないと考
えられる。As mentioned above, the gel is generated by Glu-Lys crosslinking, and it is thought that the gel is not due to S-s crosslinking.
このようにして得られたゲル化物は、比較的短時間、即
ち、1分以内、長くとも30分以内tこてゲル化し、し
かも一般のゲル化物と同等のゲル物性を備えたものであ
る。The thus obtained gelled product gels in a relatively short time, that is, within 1 minute, and within 30 minutes at the most, and has gel properties equivalent to those of general gelled products.
また、本発明で用いる蛋白含有溶液は単に蛋白質と水と
の混合物Vこ限らず、蛋白質、水及び油脂を混合したエ
マルジョンであってもよい。Furthermore, the protein-containing solution used in the present invention is not limited to a simple mixture of protein and water, but may also be an emulsion containing a mixture of protein, water, and oil.
更にこのゲル化物は加熱することにより、強度のより強
いゲルを作ることができる。Furthermore, by heating this gelled product, a stronger gel can be made.
本発明のゲル化物は、従来のゲル状食品と同様にヨーグ
ルト、ゼリーなどとして用いることはもちろん、未加熱
で製造でき、熱tこ安定なゲルであるため、マイクロカ
プセルの素材、固定化酵素の素材などとしても用いるこ
とができるものである。The gelled product of the present invention can be used as yogurt, jelly, etc. in the same way as conventional gelled foods, and can be produced without heating and is a heat-stable gel, so it can be used as a material for microcapsules or as an immobilized enzyme. It can also be used as a material.
実施例1
以下の方法會こよりトランスグルタミナーゼを調製した
。モルモット肝800fC冷0.26 Mシロ糖溶液約
2を加え、20000rpm、2分でホモゲイズし、遠
心分離(106,0OOXf、5 C11時間)を行な
い上清を得た。Example 1 Transglutaminase was prepared by the following method. Approximately 2 ounces of a cold 0.26 M guinea pig liver solution at 800 fC was added, homogenized at 20,000 rpm for 2 minutes, and centrifuged (106,0 OOXf, 5 C for 11 hours) to obtain a supernatant.
これを5mM*)jjスψ塩酸緩衝液(2mMEDTA
含有、pH7,5)で平衡化しであるDEAE セルロ
ールカラムに添加・吸着させた後、上記緩衝液の食塩濃
度なOMから1.0Mまで変化させる勾配溶離法で分画
し、酵素活性の高い両分を得た。Add this to 5mM*)jjsuψHCl buffer (2mM EDTA
After adding and adsorbing DEAE to a cellulose column equilibrated with pH 7.5), fractionation was performed using a gradient elution method in which the saline concentration of the above buffer was varied from 0M to 1.0M. I got both.
これをゆっくりと攪拌しながら1チ硫酸プロタミン40
jI/を添加し、遠心分離(14,600Xf。While stirring this slowly, add 40% of protamine monothiosulfate.
Add jI/ and centrifuge (14,600Xf.
15分、SC)で沈澱を集め、これを0.2 M )リ
ス・酢酸緩衝液(pH6,0)r−懸濁、ホモゲイズし
て洗い、遠心分離(2,600Xf、1分、5t’)で
、沈澱を集めた。Collect the precipitate (SC) for 15 minutes, suspend it in 0.2 M) Lis-acetate buffer (pH 6,0), homogenize, wash, and centrifuge (2,600Xf, 1 minute, 5t'). Then, the precipitate was collected.
この沈澱より、0.05M硫安を含む5mM)!jス塩
酸緩衡液(2mM EDTA含有、pH7,5)を添加
し、ホモゲイズするととtこよって、トランスグルタミ
ナーゼを抽出した。これを3度繰り返し、集めた抽出液
を5mM)リス・コハク酸緩衝液(2mM EDTA含
有、p)(6,0)で平衡化したカルボキシメチル・セ
ルロースカラムに添加し、プロタミンを除去し、濾液に
I M EDTA (p)18.0 ) 2.4 wi
tと硫安47.4 fを加え、よく攪拌した後に、遠心
分離(!5,000Xf、10分、5C)で沈澱を集め
た。From this precipitate, 5mM containing 0.05M ammonium sulfate)! A hydrochloric acid buffer solution (containing 2mM EDTA, pH 7.5) was added, homogenized, and transglutaminase was extracted. This was repeated three times, and the collected extract was added to a carboxymethyl cellulose column equilibrated with 5mM) lis-succinate buffer (containing 2mM EDTA, p) (6,0) to remove protamine, and the filtrate was IM EDTA (p)18.0) 2.4 wi
After adding t and 47.4 f of ammonium sulfate and stirring well, the precipitate was collected by centrifugation (!5,000Xf, 10 minutes, 5C).
これを10mM)!JスΦ酢酸緩衝液(1mMEDTA
0.16 M KCI 含有、pH6,0)tこ
溶解し、遠心分離(27,0ooxr、3o分、SC)
で難溶物を除いた後、上清を同じ緩衝液で平衡化してい
る1(1%アガロース(Bio Gcl A −0,5
M)でゲル濾過を行ない、活性の高い画分な集め、これ
を10〜20冨9/−の濃度となるよう限外濾過(UM
−10,アミコン社製)で濃縮し、トランスグルタミナ
ーゼ溶液とした。この溶液を一30C以下で凍結保存し
、適時溶解し使用した(尚、これは常時5Cで操作し調
製した。)。This is 10mM)! JS Φ acetate buffer (1mM EDTA
Contains 0.16 M KCI, pH 6,0) and centrifugation (27,000xr, 30 minutes, SC)
After removing poorly soluble substances, the supernatant was equilibrated with the same buffer solution (1% agarose (Bio Gcl A-0,5
Gel filtration is performed with M), the highly active fraction is collected, and this is subjected to ultrafiltration (UM) to a concentration of 10 to 20 m
-10, manufactured by Amicon) to prepare a transglutaminase solution. This solution was stored frozen at -30C or below, dissolved and used at appropriate times (this solution was prepared by constantly operating at 5C).
表1r:示した基質蛋白にトランスグルタミナーゼを作
用させ、ゲル化物を得た。Table 1r: Transglutaminase was allowed to act on the indicated substrate proteins to obtain gelled products.
表 1
※I C,As Zittle et al
、J、Diary Sci、+ 46 +1183(
+963)
※2 V、H,Thanh et al、J、
Agric、FoodChem、+ 24(6)、
+117(1976)実施例2
α カゼイン、Na−カゼイネート、大豆蛋白1
11Sグロブリン、水抽出大豆蛋白、各々500mgを
0.1 M )リス塩酸緩衝液(5m M CaC1,
,20mMジチオスレイトール含有、pH7,6)3.
5d?こ溶解し、これに大豆油1.5dを加えて200
00 rpmで3分間ホモゲナイズして乳化並を得た。Table 1 *I C, As Zittle et al.
, J, Diary Sci, +46 +1183(
+963) *2 V, H, Thanh et al, J,
Agric, FoodChem, +24(6),
+117 (1976) Example 2 α-casein, Na-caseinate, soybean protein 1 11S globulin, water-extracted soybean protein, 500mg each were mixed with 0.1M) Lis-HCl buffer (5mM CaC1,
, containing 20mM dithiothreitol, pH 7,6)3.
5d? Dissolve this and add 1.5 d of soybean oil to it for 200 min.
Homogenization was performed for 3 minutes at 0.00 rpm to obtain a homogenized emulsion.
これにトランスグルタミナーゼを蛋白1■に対して0.
09ユニット加えると即座にゲルイ)物を得た。To this, transglutaminase was added at 0.00% per 1 kg of protein.
When 09 units were added, gelatin was obtained immediately.
実施例3
α、l−カゼイン、大豆蛋白115グロブリン及び大豆
蛋白7Sグリプリンの2.5.10重量%溶液を0.1
M )リス・塩酸緩衝液(5mM CaC11,20
mMジチオスレイトール含有pH7,6)で0.5d作
成し、37Cで各々にトランスグルタミナーゼを蛋白1
m91C対して0.1ユニツトの割合で加えて、ゲル化
するか否を判定し、表2の結果を得た。Example 3 A 2.5.10% by weight solution of α, l-casein, soybean protein 115 globulin, and soybean protein 7S glypurin was added to 0.1
M) Lis-HCl buffer (5mM CaC11,20
Transglutaminase was added to each protein at 37C for 0.5 d at pH 7.6) containing mM dithiothreitol.
It was added at a ratio of 0.1 unit to m91C to determine whether gelation occurred, and the results shown in Table 2 were obtained.
表 2
0ニゲル化
△:弱いゲル
×:溶液のまま
実施例4
αal カゼインの5重量係溶液と大豆蛋白I!Sグ
ロブリンの10重量%溶液を0.1 M )リス−塩酸
緩衝液(5mM CaCIQ120 mMジチオスレ
イトール含有、pH7,6)で調整し、これら溶液0.
8−r一対して、トランスグルタミナーゼを蛋白1 m
gあたり5×10〜2.0ユニット添加してゲル化する
か否かを観察したところ、表3tこ示すような結果を得
た。Table 2 0 gelatinization △: weak gel ×: remain as solution Example 4 5 weight ratio solution of αal casein and soybean protein I! A 10% by weight solution of S globulin was prepared with 0.1 M) Lis-HCl buffer (containing 5mM CaCIQ120mM dithiothreitol, pH 7.6), and these solutions were diluted with 0.1M (containing 5mM CaCIQ120mM dithiothreitol, pH 7.6).
For each 8-r pair, add transglutaminase to 1 m of protein.
When 5 x 10 to 2.0 units per gram were added and it was observed whether gelation occurred or not, the results shown in Table 3t were obtained.
表 3
■=即座にゲル化した
。:1時間以上にゲル化
Δニゲルするが弱いゲル
×:溶液のまま
実施例5
5 mM Ca11gと20mMジチオスレイトールを
含んだpH7,0〜pH9,0のトリス−塩酸緩衝液を
調整し、それを用いて、5重量%α8.カゼイン溶液と
10重量%大豆蛋白115グロブリン溶液を各0.8−
ずつ作成し、トランスグルタミナーゼを蛋白11gに対
して0.1ユニツト添加してゲル化するか否かを観察し
た。結果を表4tこ示す。Table 3 ■ = Immediate gelation. : Gelled for over 1 hour, but weak gel ×: Still in solution Example 5 A Tris-HCl buffer solution containing 11 g of 5 mM Ca and 20 mM dithiothreitol at pH 7.0 to pH 9.0 was prepared, and using 5% by weight α8. Casein solution and 10 wt% soy protein 115 globulin solution were each mixed with 0.8-
0.1 unit of transglutaminase was added to 11 g of protein, and it was observed whether gelation occurred. The results are shown in Table 4t.
表 4
@:即座にゲル化
○:ややゲル化に時間を要した
×:溶液のまま
実施例6
直径9.3tts、高さ1.5d?のテストピース作成
容器に試料溶液1mを流し込み、下記tこ示す様1こゲ
ル化させて円筒ゲルを作成し、これをレオログラム(東
洋精機製作所■、CV−100)tこて、18から25
cまで昇温させ、各温度の貯蔵弾性率を測定した。Table 4 @: Immediately gelled ○: Slightly required time for gelation ×: Still in solution Example 6 Diameter 9.3tts, height 1.5d? Pour 1 m of the sample solution into a test piece preparation container, gel it as shown below to create a cylindrical gel, and apply it using a rheogram (Toyo Seiki Seisakusho ■, CV-100) with a 18 to 25 trowel.
The storage elastic modulus at each temperature was measured.
■ ゼラチン冷却ゲル
10重量%溶液となるようtこ、ゼラチンtこ水を加え
、60211’、3分で完全にゼラチンを溶解後、lT
111をテストピース作成容器に流し込み、3Cr−て
20分放置し、ゲル化させ室温に戻して測定した。■ Add water to the gelatin to make a 10% gelatin cooling gel solution, completely dissolve the gelatin in 60211' for 3 minutes, and then add 1T.
111 was poured into a test piece preparation container and left to stand for 20 minutes in 3Cr-coated water to gel and return to room temperature for measurement.
■ ゼラチンTGa@eゲル
ゼラチンに10重量%溶液となるように0.1Mトリス
塩酸溶液(5mM CaCl、、20mMジチオスレイ
トール含有、pH7,6)を加え、60r、3分で完全
にゼラチンを溶解し、テストピース作成容器に流し込み
、すばやくトランスグルタミナーゼをゼラチンl璽gに
対して0.1ユニツトの割合で加え、室温1n1時間放
置しゲル化させ、測定した。■ Gelatin TGa@e Gel Add 0.1M Tris-HCl solution (contains 5mM CaCl, 20mM dithiothreitol, pH 7.6) to gelatin to make a 10% solution by weight, and completely dissolve gelatin at 60r for 3 minutes. Then, the mixture was poured into a test piece preparation container, and immediately transglutaminase was added at a ratio of 0.1 unit to 1 g of gelatin, and the gelatin was left to gel for 1 hour at room temperature, followed by measurement.
結果を回目こ示す。ゼラチン冷却ゲルは温度が増加する
とともに貯蔵弾性率が著しく低下するが、それに比して
ゼラチンTGaseゲルは温度変化の影響が少なかった
。I will show you the results for the second time. The storage modulus of gelatin cooled gel decreases significantly as the temperature increases, but in comparison, gelatin TGase gel was less affected by temperature changes.
実施例7
α5、カゼインについては5重量%、大豆115グロブ
リンについては10重量%となるように0.1 M )
リス・塩酸緩衝液(5mM CaCl、、20mMジチ
オスレイトール含有、pH7,6)で1 mlを調製し
、これtこトランスグルタミナーゼを蛋白IQE対して
0.1ユニツトを加えゲルを得た。このゲルを、さらt
こ100rに20分間保った後、室温まで冷却した。Example 7 α5, 5% by weight for casein and 10% by weight for soybean 115 globulin (0.1 M)
1 ml of lysate-hydrochloric acid buffer (containing 5mM CaCl, 20mM dithiothreitol, pH 7.6) was prepared, and 0.1 unit of transglutaminase was added to the protein IQE to obtain a gel. Add this gel to
After maintaining the temperature at 100 rpm for 20 minutes, it was cooled to room temperature.
ゲル化させた直後のゲルと、加熱処理したゲルについて
レオメータ−(不動工業■、NRM−2002J)で、
プランジャー(5Φ、ポール型)を侵入させた時の最高
荷重を測定し、ゲル強度とした。結果を表5に示す。The gel immediately after gelation and the heat-treated gel were measured using a rheometer (Fudou Kogyo ■, NRM-2002J).
The maximum load when a plunger (5Φ, pole type) was inserted was measured and defined as gel strength. The results are shown in Table 5.
表 5
上表かられかるようケこいずれの場合も加熱処理した方
がゲル強度が増加した。Table 5 As can be seen from the above table, in both cases, the gel strength increased with heat treatment.
図1は実施例6の結果を示す。図中、横軸は温度(r)
、縦軸は貯蔵弾性率(dyn/d )であり、実線は
本発明のゼラチンTGa@eゲルを、破線はゼラチン冷
却ゲルを示す。
特許出願人□ 味の素株式会社
11
ン)底 C°Cノ
手続補正書
昭和57年10月らl
特許庁長官若杉和夫殿
1、事件の表示
昭和57年特許願31978号
2、発明の名称
ゲル化物の製造法
3、補正をする者
事件との関係 特許出願人
住 所 東京都中央区京橋−丁目5番8号7、補正の
内容
(1) 明細−第6頁第12行の「p rotecnJ
をrProteinJに補正する。
(2) 明細書第9頁第7行のr511M・トリス」を
「5Il1M トリス」に補正する。
(3) 明細書第10頁第14行のrGcIJをrGe
lJに補正する。
(4) 明細書第11頁表1の牛乳蛋白■Na−カゼイ
ネートの欄の「化学■及び」を「化学■)及び」に補正
する。
(5) 明細書第11頁表1の牛乳蛋白■Na−カゼイ
ネートの欄のrDacryJをrDairyJに補正す
る。
(6) 明細書第11頁表1の牛乳蛋白■Na−カゼイ
ネートの欄の「兵器■))」を「共益■)」に補正する
。
(7) 明細書第12頁表1の大豆蛋白11Sグロブリ
ンの欄の「フレーク」を「フレーク」に補正する。
(8) 明細書第16頁下から第5行のF調整Jを「調
製Jに補正する。
(9ン 明細59@17頁表3欄外のU△ニゲルするJ
を「△ニゲル化する」に補正する。
(10) 明細書第17頁−トから第7行のrcal
12 JをrCaCリ 」に補正する。
(11) 明細書第17真下から第5行の「調整」を
rlllJに補正する。
(12) 明細書第18頁下から第9行の[高さ1.
5111114を[高さ15111]に補正する。FIG. 1 shows the results of Example 6. In the figure, the horizontal axis is temperature (r)
, the vertical axis is the storage modulus (dyn/d), the solid line shows the gelatin TGa@e gel of the present invention, and the broken line shows the gelatin cooling gel. Patent Applicant□ Ajinomoto Co., Inc. 11 N) Bottom C°C Procedural Amendment October 1980 et al. Kazuo Wakasugi, Commissioner of the Japan Patent Office 1, Indication of the Case, Patent Application No. 31978, 1982, 2, Title of Invention: Gelified Product Manufacturing method 3, relationship with the case of the person making the amendment Patent applicant address 5-8-7, Kyobashi-chome, Chuo-ku, Tokyo Contents of amendment (1) Specification - "protecnJ" on page 6, line 12
is corrected to rProteinJ. (2) Correct "r511M Tris" on page 9, line 7 of the specification to "5Il1M Tris." (3) rGcIJ on page 10, line 14 of the specification is replaced by rGe
Correct to lJ. (4) In Table 1 on page 11 of the specification, "Chemistry ■ and" in the milk protein column "Na-caseinate" is corrected to "Chemistry ■) and". (5) Correct rDacryJ to rDairyJ in the column of milk protein ■Na-caseinate in Table 1 on page 11 of the specification. (6) In Table 1 on page 11 of the specification, "weapon ■))" in the milk protein ■Na-caseinate column is corrected to "common benefit ■)." (7) "Flake" in the column for soybean protein 11S globulin in Table 1 on page 12 of the specification is corrected to "flake". (8) F Adjustment J in the 5th line from the bottom of page 16 of the specification is corrected to ``Preparation J.''
is corrected to "△nigelization". (10) rcal on page 17 of the specification, line 7 from
Correct 12 J to rCaC. (11) Correct “adjustment” in the 5th line from the bottom of No. 17 of the specification to rllllJ. (12) [Height 1.
Correct 5111114 to [height 15111].
Claims (1)
ルタミナーゼを蛋白!fに対してlユニット以上、添加
してゲル化させることを特徴とするゲル化物の製造法。Add transglutaminase to a protein-containing solution with a protein concentration of 2% by weight or more! A method for producing a gelled product, which comprises adding 1 unit or more to f to cause gelation.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57031978A JPS58149645A (en) | 1982-03-01 | 1982-03-01 | Preparation of gelatinized material |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57031978A JPS58149645A (en) | 1982-03-01 | 1982-03-01 | Preparation of gelatinized material |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS58149645A true JPS58149645A (en) | 1983-09-06 |
JPH0150382B2 JPH0150382B2 (en) | 1989-10-30 |
Family
ID=12346027
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP57031978A Granted JPS58149645A (en) | 1982-03-01 | 1982-03-01 | Preparation of gelatinized material |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58149645A (en) |
Cited By (24)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61152247A (en) * | 1984-12-26 | 1986-07-10 | Ajinomoto Co Inc | Production of protein membrane |
WO1989000011A1 (en) * | 1987-07-02 | 1989-01-12 | Taiyo Fishery Co., Ltd. | Process for producing food |
JPH02257831A (en) * | 1988-12-08 | 1990-10-18 | Ajinomoto Co Inc | Vegetable protein powder and production of bean curd using the same |
US5023024A (en) * | 1987-04-16 | 1991-06-11 | Suntory Limited | Process for producing microcapsules |
US5037664A (en) * | 1988-10-15 | 1991-08-06 | Suntory Limited | Process for producing novel gel-like food articles |
FR2659352A1 (en) * | 1990-03-09 | 1991-09-13 | Nippi Gelatine Ind Ltd | Process for the production of highly polymerised gelatin |
US5531795A (en) * | 1992-12-10 | 1996-07-02 | Novo Nordisk A/S | Method for casein finishing of leather |
EP0800771A2 (en) * | 1996-04-10 | 1997-10-15 | Ajinomoto Co., Inc. | Process for producing chocolate |
EP0815742A2 (en) * | 1996-07-01 | 1998-01-07 | Ajinomoto Co., Ltd. | Binding composition comprising transglutaminase and collagen, and process for producing bound food products |
EP0956778A1 (en) * | 1993-03-19 | 1999-11-17 | Novo Nordisk A/S | Method of preparing a meat product using a transglutaminase containing milk product |
US6039901A (en) * | 1997-01-31 | 2000-03-21 | Givaudan Roure Flavors Corporation | Enzymatically protein encapsulating oil particles by complex coacervation |
EP1074592A1 (en) * | 1999-08-05 | 2001-02-07 | F. Hoffmann-La Roche Ag | Process for preparing beadlets containing fat-soluble substances |
CN1066925C (en) * | 1994-03-04 | 2001-06-13 | 泰特拉·雷沃金融控股公司 | Process for producing protein gel |
US6399117B1 (en) | 1998-04-08 | 2002-06-04 | Nutreco Aquaculture Research Centre A/S | Method for the modification of protein structure in finish shaped feed pellets, balls or the like in order to achieve shape stability, and feed mass made in accordance with the method |
US6716461B2 (en) | 2000-10-10 | 2004-04-06 | Ajinomoto Co., Inc. | Method for modifying raw material milk and dairy product prepared by using the modified raw material milk |
US6749873B2 (en) | 2000-08-31 | 2004-06-15 | Ajinomoto Co., Inc. | Cheese yield enhancing method |
US6908634B2 (en) | 2003-03-20 | 2005-06-21 | Solae, Llc | Transglutaminase soy fish and meat products and analogs thereof |
JP2007277217A (en) * | 2006-03-17 | 2007-10-25 | Fujifilm Corp | Biodegradable matrix homogeneously encapsulating medicament |
WO2009060678A1 (en) * | 2007-11-08 | 2009-05-14 | Fuji Oil Company, Limited | Soy protein gel and method of producing the same |
JP2009106271A (en) * | 2007-10-11 | 2009-05-21 | Aoba Kasei Kk | Method for preparing food quality improver, method for producing paste product, food color fading inhibitor, method for producing fading-inhibited food, hot taste development retarder, and method for producing hot taste development-retarded food |
US7727629B2 (en) | 2002-04-11 | 2010-06-01 | Ocean Nutrition Canada Limited | Encapsulated agglomeration of microcapsules and method for the preparation thereof |
US9056058B2 (en) | 2006-06-05 | 2015-06-16 | Dsm Nutritional Products | Microcapsules with improved shells |
US9968120B2 (en) | 2006-05-17 | 2018-05-15 | Dsm Nutritional Products Ag | Homogenized formulations containing microcapsules and methods of making and using thereof |
US10166196B2 (en) | 2007-01-10 | 2019-01-01 | Dsm Nutritional Products Ag | Vegetarian microcapsules |
Families Citing this family (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE69533606T2 (en) * | 1994-01-28 | 2006-03-02 | Ajinomoto Co., Inc. | TRANSGLUTAMINASE FROM JAPANESE EYES |
JP3545148B2 (en) | 1996-01-08 | 2004-07-21 | 味の素株式会社 | Edible microcapsules and foods containing the same |
JPH10276695A (en) | 1997-04-11 | 1998-10-20 | Ajinomoto Co Inc | Production of noodle |
JP5257067B2 (en) | 2006-04-18 | 2013-08-07 | 味の素株式会社 | Method for producing stirred fermented milk with enhanced whey protein |
CN101646356B (en) | 2007-03-29 | 2013-09-25 | 味之素株式会社 | Enzyme preparation for adhesion and method of producing adhesion-molded food product |
DK2251421T3 (en) | 2008-02-13 | 2017-02-06 | Amano Enzyme Inc | Stabilized transglutaminase and process for its preparation |
TW200942616A (en) | 2008-03-14 | 2009-10-16 | Ajinomoto Kk | Method of denaturing protein with enzymes |
PL2253229T3 (en) | 2008-03-17 | 2012-03-30 | Ajinomoto Kk | Method of producing fish paste product and enzyme preparation for fish paste products |
TWI444146B (en) | 2008-09-25 | 2014-07-11 | Ajinomoto Kk | Enzyme preparations for bound and formed foods and methods for producing bound and formed foods |
EP2382875B1 (en) | 2008-12-26 | 2015-11-11 | Ajinomoto Co., Inc. | Enzyme preparation for single-ingredient meat product and method for producing single-ingredient meat product |
WO2012026618A1 (en) | 2010-08-27 | 2012-03-01 | 味の素株式会社 | Process for production of fish paste product, and enzyme preparation for modifying fish paste product |
US20140186492A1 (en) | 2011-08-25 | 2014-07-03 | Amano Enzyme Inc. | Composition having improved head stability and use thereof |
WO2016210395A1 (en) | 2015-06-26 | 2016-12-29 | Dupont Nutrition Biosciences Aps | Aminopeptidases for protein hydrlyzates |
JPWO2023058616A1 (en) | 2021-10-04 | 2023-04-13 |
-
1982
- 1982-03-01 JP JP57031978A patent/JPS58149645A/en active Granted
Non-Patent Citations (7)
Title |
---|
ADVANCES IN PROTEIN CHEMISTRY=1948 * |
AGRIC BIOL CHEM=1980 * |
METHODS IN ENZYMOLOGY=1970 * |
NEW FOOD INDUSTRY=S55 * |
PROC NAT ACAD SCI USA=1972 * |
PROTEIN FUNCTIONALITY IN FOODS=1981 * |
THE JORNAL OF BIOLOGICAL CHEMISTRY=1971 * |
Cited By (38)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61152247A (en) * | 1984-12-26 | 1986-07-10 | Ajinomoto Co Inc | Production of protein membrane |
JPH0581218B2 (en) * | 1984-12-26 | 1993-11-11 | Ajinomoto Kk | |
US5023024A (en) * | 1987-04-16 | 1991-06-11 | Suntory Limited | Process for producing microcapsules |
US4917904A (en) * | 1987-07-02 | 1990-04-17 | Taiyo Fishery Co., Ltd. | Process for the production of transglutaminase-containing food having improved texture |
GB2227154A (en) * | 1987-07-02 | 1990-07-25 | Taiyo Fishery Co Ltd | Process for producing food |
GB2227154B (en) * | 1987-07-02 | 1992-03-18 | Taiyo Fishery Co Ltd | Method of treating food material |
JPS6410949A (en) * | 1987-07-02 | 1989-01-13 | Taiyo Fishery Co Ltd | Preparation of food |
WO1989000011A1 (en) * | 1987-07-02 | 1989-01-12 | Taiyo Fishery Co., Ltd. | Process for producing food |
US5037664A (en) * | 1988-10-15 | 1991-08-06 | Suntory Limited | Process for producing novel gel-like food articles |
JPH02257831A (en) * | 1988-12-08 | 1990-10-18 | Ajinomoto Co Inc | Vegetable protein powder and production of bean curd using the same |
FR2659352A1 (en) * | 1990-03-09 | 1991-09-13 | Nippi Gelatine Ind Ltd | Process for the production of highly polymerised gelatin |
US5531795A (en) * | 1992-12-10 | 1996-07-02 | Novo Nordisk A/S | Method for casein finishing of leather |
EP0956778A1 (en) * | 1993-03-19 | 1999-11-17 | Novo Nordisk A/S | Method of preparing a meat product using a transglutaminase containing milk product |
CN1066925C (en) * | 1994-03-04 | 2001-06-13 | 泰特拉·雷沃金融控股公司 | Process for producing protein gel |
US6063408A (en) * | 1996-04-10 | 2000-05-16 | Ajinomoto Co., Inc. | Process for producing chocolate |
EP0800771A3 (en) * | 1996-04-10 | 1998-03-04 | Ajinomoto Co., Inc. | Process for producing chocolate |
EP0800771A2 (en) * | 1996-04-10 | 1997-10-15 | Ajinomoto Co., Inc. | Process for producing chocolate |
EP0815742A3 (en) * | 1996-07-01 | 1999-06-30 | Ajinomoto Co., Inc. | Binding composition comprising transglutaminase and collagen, and process for producing bound food products |
EP0815742A2 (en) * | 1996-07-01 | 1998-01-07 | Ajinomoto Co., Ltd. | Binding composition comprising transglutaminase and collagen, and process for producing bound food products |
US6039901A (en) * | 1997-01-31 | 2000-03-21 | Givaudan Roure Flavors Corporation | Enzymatically protein encapsulating oil particles by complex coacervation |
US6325951B1 (en) | 1997-01-31 | 2001-12-04 | Givaudan Roure Flavors Corporation | Enzymatically protein-encapsulating oil particles by complex coacervation |
US6399117B1 (en) | 1998-04-08 | 2002-06-04 | Nutreco Aquaculture Research Centre A/S | Method for the modification of protein structure in finish shaped feed pellets, balls or the like in order to achieve shape stability, and feed mass made in accordance with the method |
US6528100B1 (en) | 1998-04-08 | 2003-03-04 | Nutreco Aquaculture Research Centre As | Feed mass having a modified protein structure for carnivorous animals |
EP1074592A1 (en) * | 1999-08-05 | 2001-02-07 | F. Hoffmann-La Roche Ag | Process for preparing beadlets containing fat-soluble substances |
KR100794846B1 (en) * | 1999-08-05 | 2008-01-15 | 디에스엠 아이피 어셋츠 비.브이. | Process for preparing beadlets containing fat-soluble substances |
US6749873B2 (en) | 2000-08-31 | 2004-06-15 | Ajinomoto Co., Inc. | Cheese yield enhancing method |
US6716461B2 (en) | 2000-10-10 | 2004-04-06 | Ajinomoto Co., Inc. | Method for modifying raw material milk and dairy product prepared by using the modified raw material milk |
US7727629B2 (en) | 2002-04-11 | 2010-06-01 | Ocean Nutrition Canada Limited | Encapsulated agglomeration of microcapsules and method for the preparation thereof |
US6908634B2 (en) | 2003-03-20 | 2005-06-21 | Solae, Llc | Transglutaminase soy fish and meat products and analogs thereof |
JP2007277217A (en) * | 2006-03-17 | 2007-10-25 | Fujifilm Corp | Biodegradable matrix homogeneously encapsulating medicament |
US9968120B2 (en) | 2006-05-17 | 2018-05-15 | Dsm Nutritional Products Ag | Homogenized formulations containing microcapsules and methods of making and using thereof |
US9056058B2 (en) | 2006-06-05 | 2015-06-16 | Dsm Nutritional Products | Microcapsules with improved shells |
US10166196B2 (en) | 2007-01-10 | 2019-01-01 | Dsm Nutritional Products Ag | Vegetarian microcapsules |
JP2009106271A (en) * | 2007-10-11 | 2009-05-21 | Aoba Kasei Kk | Method for preparing food quality improver, method for producing paste product, food color fading inhibitor, method for producing fading-inhibited food, hot taste development retarder, and method for producing hot taste development-retarded food |
WO2009060678A1 (en) * | 2007-11-08 | 2009-05-14 | Fuji Oil Company, Limited | Soy protein gel and method of producing the same |
JPWO2009060678A1 (en) * | 2007-11-08 | 2011-03-17 | 不二製油株式会社 | Soy protein gel and method for producing the same |
US8304522B2 (en) | 2007-11-08 | 2012-11-06 | Fuji Oil Company, Limited | Soy protein gel and method of producing the same |
JP5577702B2 (en) * | 2007-11-08 | 2014-08-27 | 不二製油株式会社 | Soy protein gel and method for producing the same |
Also Published As
Publication number | Publication date |
---|---|
JPH0150382B2 (en) | 1989-10-30 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JPS58149645A (en) | Preparation of gelatinized material | |
Jaros et al. | Transglutaminase in dairy products: chemistry, physics, applications | |
Stainsby | Proteinaceous gelling systems and their complexes with polysaccharides | |
Hou et al. | Edible double-network gels based on soy protein and sugar beet pectin with hierarchical microstructure | |
EP0379606B1 (en) | Novel transglutaminase | |
JPS60176549A (en) | Preparation of protein hydrolyzate | |
US3974294A (en) | Process for the production of protein-containing food additives | |
Li et al. | Effect of partial hydrolysis with papain on the characteristics of transglutaminase‐crosslinked tofu gel | |
AU670370B2 (en) | Method for production of a not acidified edible gel on milk basis, and use of such gel | |
Wang et al. | High‐pressure processing‐induced conformational changes during heating affect water holding capacity of myosin gel | |
Kiosseoglou et al. | Physical characterization of thermally induced networks of lupin protein isolates prepared by isoelectric precipitation and dialysis | |
JPH09208A (en) | Manufacture of meat patty | |
US4636388A (en) | Preparing protein for hydrolysis and product | |
JPH03259928A (en) | Production of highly polymeric gelatin | |
CN112167543B (en) | Oxidative damage protein gel performance repairing method based on lysine-glutamine transaminase | |
JP2572716B2 (en) | Novel transglutaminase | |
JP2958801B2 (en) | Method for producing debittered functional peptide | |
JP2021504463A (en) | Method for preparing gelatin hydrolyzate with low endotoxin content | |
Benguigui et al. | Study of junction zones in gelatin gels through selective enzymatic digestion | |
US5856120A (en) | Method of preparing a biological material for use in ophthalmology | |
JPH08224063A (en) | Gelatinized composition of protein | |
US6037144A (en) | Method of preparing a biological material for use in ophthalmology | |
TAKAHASHI et al. | Edible Meat Casing from Reconstruction of Collagen‐Elastin Matrix | |
Cronlund et al. | Effect of microbial rennets on meat protein fractions | |
JP2927076B2 (en) | New protein food ingredients |