JPH0581218B2 - - Google Patents
Info
- Publication number
- JPH0581218B2 JPH0581218B2 JP59281690A JP28169084A JPH0581218B2 JP H0581218 B2 JPH0581218 B2 JP H0581218B2 JP 59281690 A JP59281690 A JP 59281690A JP 28169084 A JP28169084 A JP 28169084A JP H0581218 B2 JPH0581218 B2 JP H0581218B2
- Authority
- JP
- Japan
- Prior art keywords
- protein
- membrane
- film
- tgase
- casein
- 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
Landscapes
- Medicinal Preparation (AREA)
- Manufacture Of Macromolecular Shaped Articles (AREA)
- Peptides Or Proteins (AREA)
Description
【発明の詳細な説明】 本発明は強化蛋白質膜の製造法に関する。[Detailed description of the invention] The present invention relates to a method for producing reinforced protein membranes.
高分子学において、cast膜という概念がある。
これは、液状物質を型の中に流し込み、固化させ
溶媒を蒸発させてフイルムとする流延成形を
castingといい、得られるフイルムをcast膜と称
している。食品分野においても日本の伝統食品で
ある湯葉は、豆乳を加熱して得られるゲル状皮膜
を風乾して製造され、cast膜の範疇に入るものと
考えられる。このような食品蛋白を用いたcast膜
形成に関する報告は、蛋白溶液に20〜30%のグリ
セロールやソルビトールを添加したり、アルデヒ
ドや重金属を作用させフイルム化するなどといつ
たものが多く過激な条件で製造するものが多く、
生分解性や安全性に問題がある。 In polymer science, there is a concept called cast film.
This is a casting process in which a liquid substance is poured into a mold, solidified, and the solvent is evaporated to form a film.
This is called casting, and the resulting film is called cast film. Yuba, which is a traditional Japanese food in the food field, is produced by air-drying a gel-like film obtained by heating soy milk, and is considered to fall under the category of cast film. Reports on the formation of cast films using food proteins often involve extreme conditions such as adding 20-30% glycerol or sorbitol to a protein solution, or adding aldehydes or heavy metals to form a film. Many products are manufactured in
There are problems with biodegradability and safety.
本発明者らは、上記のような欠点を補い、天然
系素材を用いて温和な条件でcastingして得られ
る強靱で、かつ、安全性の高い蛋白質膜の製造法
を開発しようと種々研究を行なつた結果、高濃度
蛋白含有溶液にトランスグルタミナーゼを作用さ
せ、cast膜化することによつて、強靱で安定な蛋
白質膜を製造しうることを発見し、本発明を完成
した。 The present inventors have carried out various studies in an attempt to compensate for the above-mentioned drawbacks and develop a method for manufacturing a strong and highly safe protein membrane that can be obtained by casting natural materials under mild conditions. As a result, they discovered that a tough and stable protein film could be produced by applying transglutaminase to a solution containing a high concentration of protein and forming a cast film, thereby completing the present invention.
即ち、本発明は、蛋白質濃度2重量%以上の蛋
白含有溶液にアシル転移酵素トランスグルタミナ
ーゼ(EC2,3,2,13、以下「TGase」と略
す)を蛋白質1gに対して適宜量、好ましくは1
ユニツト以上添加し、型枠に流し込み、10ないし
60°にて、水分率が20%以下になるまで乾燥する
ことを特徴とする蛋白質膜の製造法である。 That is, in the present invention, an appropriate amount of acyltransferase transglutaminase (EC2, 3, 2, 13, hereinafter abbreviated as "TGase") is added to a protein-containing solution with a protein concentration of 2% by weight or more, preferably 1 g of protein.
Add at least 1 unit, pour into the formwork,
This method of producing a protein film is characterized by drying at 60° until the moisture content is 20% or less.
本発明で利用可能なトランスグルタミナーゼは
天然物から抽出分離したものはもちろん、トラン
スグルタミナーゼを生産する微生物を培養してそ
れらの菌体外又は菌体内に蓄積されたものでもよ
い。また遺伝子工学的手法や細胞工学的手法など
の生物工学的手法を用いて得られたものでもよ
い。 The transglutaminase that can be used in the present invention may not only be extracted and separated from natural products, but also be accumulated outside or inside the cells of microorganisms that produce transglutaminase by culturing them. Alternatively, it may be obtained using bioengineering techniques such as genetic engineering techniques and cell engineering techniques.
本発明に用いられる膜化用蛋白質は、その起源
に制約されず、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(脱脂大豆など)及びそれ
らより分離した蛋白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。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%
ないし15重量%であればよい。 The membrane-forming protein used in the present invention is not limited by 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, etc.) and proteins separated from them. Furthermore, examples of animal proteins include milk protein, gelatin, and collagen. A protein-containing solution containing 2% by weight or more of these proteins is prepared. It is desirable that the concentration of the protein-containing solution is relatively high, usually 2% by weight or more, preferably 5% by weight.
The amount may be between 15% and 15% by weight.
この高濃度蛋白含有溶液に、特開昭58−149645
号に記載されている方法で調製したTGaseを蛋
白質1gに対して、1ユニツト/g・蛋白以上添
加し、直ちに、平板型枠(例えば、メタアクリル
樹脂製)に流し込み、10ないし60℃にて、水分率
20%以下となるまで(通常、3ないし5時間)、
風乾または送風乾燥すると型枠より容易に剥離す
る強靱な蛋白質膜が得られる。蛋白質濃度が2重
量%未満の場合、TGase量が基質蛋白質1gに
対して1U未満の場合、乾燥温度が10℃未満や60
℃以上の場合は、各れも剥離性が悪く、本発明の
特徴を有する蛋白質膜は得られない。 In this highly concentrated protein-containing solution, JP-A-58-149645
Add at least 1 unit/g of TGase to 1 g of protein, prepared by the method described in the above issue, immediately pour into a flat mold (for example, made of methacrylic resin), and heat at 10 to 60°C. ,Moisture percentage
Until it becomes 20% or less (usually 3 to 5 hours).
Air drying or blast drying yields a tough protein film that is easily peeled off from the mold. When the protein concentration is less than 2% by weight, when the amount of TGase is less than 1U per 1g of substrate protein, the drying temperature is less than 10℃ or 60℃.
If the temperature is above .degree. C., the releasability is poor and a protein film having the characteristics of the present invention cannot be obtained.
上記のようにして得られる蛋白質膜は、
TGaseを作用させずに同様の条件でcastingして
得られる蛋白質膜が水や塩類溶液で容易に溶解す
るのに比して、それらに対して安定で不溶であ
り、約2倍の引張強度と伸度を有している。さら
に、TGaseによる蛋白質膜は、水中では、22
ml/g蛋白質膜程度の吸水力を示し、有機溶媒中
では、分子篩効果を有する蛋白質膜である。ま
た、沸盪浴水中でも安定であり、全PH領域におい
ても不溶である。TGaseによる蛋白質膜が、こ
のような性質を有するのは、TGaseの触媒作用
によるε−(γ−グルタミル)リジン架橋形成に
基づいた蛋白質重合物であることに由来する。そ
れは、1)各種蛋白質変性剤(2−メルカプトエ
タノール、ドデシル硫酸ナトリウム、塩酸グアニ
ジン、尿素等)に対して安定であること。2)
TGaseの反応部位であるLys残基を完全にアセチ
ル化された蛋白質を用いて同様にcast膜化しても
水に対して可溶であること。3)TGaseによる
蛋白質膜形成途中で、高分子化された蛋白質が
SDS−ポリアクリルアミドゲル電気泳動で検出さ
れること。等から証明される。また、この
TGaseによる蛋白質膜をプロテアーゼ処理すれ
ば、加水分解され、溶液となる。従つて、生分解
性を有し、かつ、結合剤も酵素であるから、本発
明によつて得られる蛋白質膜は、生体に対する影
響が少ない。 The protein membrane obtained as above is
Compared to protein films obtained by casting under similar conditions without the action of TGase, which easily dissolve in water and salt solutions, it is stable and insoluble in water and salt solutions, and has approximately twice the tensile strength. It has elongation. Furthermore, protein membranes formed by TGase can be formed in water by 22
It is a protein film that exhibits a water absorption capacity comparable to that of a ml/g protein film, and has a molecular sieve effect in organic solvents. It is also stable in boiling water and insoluble in all pH ranges. The reason why a protein film produced by TGase has such properties is that it is a protein polymer based on the formation of ε-(γ-glutamyl)lysine crosslinks by the catalytic action of TGase. 1) It must be stable against various protein denaturants (2-mercaptoethanol, sodium dodecyl sulfate, guanidine hydrochloride, urea, etc.). 2)
Even if the Lys residue, which is the reaction site of TGase, is made into a cast film using a completely acetylated protein, it is soluble in water. 3) During protein film formation by TGase, polymerized proteins are
Detected by SDS-polyacrylamide gel electrophoresis. It is proven from etc. Also, this
When a protein membrane is treated with protease using TGase, it is hydrolyzed and becomes a solution. Therefore, since it is biodegradable and the binding agent is an enzyme, the protein membrane obtained by the present invention has little effect on living organisms.
以上のような性質を利用すれば、可食性フイル
ムとしてばかりでなく、包装材料、生分解性膜、
医用高分子膜素材、固定化酵素膜基材等が製造可
能である。 By utilizing the above properties, it can be used not only as an edible film but also as a packaging material, biodegradable membrane,
Medical polymer membrane materials, immobilized enzyme membrane substrates, etc. can be manufactured.
以下、実施例を挙げて本発明を説明するが、本
発明はこれら実施例によつて何ら制限されるもの
ではない。 The present invention will be described below with reference to Examples, but the present invention is not limited to these Examples in any way.
実施例 1
αs1−カゼインの5重量%溶液を0.1Mトリス−
塩酸緩衝液(5mM CaCl2,20mMジチオスレイ
トール0.1% グリセロール含有、PH8.0)で調製
した。これに、αs1−カゼイン1mg当り0.002ユニ
ツトのTGaseを添加し、激しく撹拌後、直ちに
メタアクリル樹脂板(あるいは、硬質ビニル板)
上の20×50×1.5mmの型枠に流し込み、40℃で5
時間送風乾燥し、αs1−カゼイン膜を得た。得ら
れたαs1−カゼイン膜は、水分率11.2%、膜厚
47μm、引張強度104.7g/cm2、伸度82%を有し、
水に不溶な蛋白質となつた。それに比して、
TGaseを使用させず他は同様の条件で、αs1−カ
ゼイン膜を調製すると、水分率10.5%、膜厚
49μm、引張強度40.6g/cm2、伸度38%を有する
蛋白質が得られた。引張強度と伸度が、TGase
を作用させた場合の0.5倍弱であるばかりでなく、
水に容易に溶解する膜であつた。Example 1 A 5% by weight solution of α s1 -casein was added to 0.1M Tris-
It was prepared with a hydrochloric acid buffer (5mM CaCl 2 , 20mM dithiothreitol, 0.1% glycerol, pH 8.0). Add 0.002 units of TGase per 1 mg of α s1 -casein to this, stir vigorously, and immediately transfer to a methacrylic resin plate (or hard vinyl plate).
Pour into the 20 x 50 x 1.5 mm mold above and heat at 40℃ for 5 minutes.
After drying with air for a period of time, an α s1 -casein film was obtained. The obtained α s1 -casein film had a moisture content of 11.2% and a film thickness of
47μm, tensile strength 104.7g/cm 2 , elongation 82%,
It became a water-insoluble protein. Compared to that,
When α s1 -casein membrane was prepared under the same conditions without using TGase, the moisture content was 10.5% and the membrane thickness was
A protein having a diameter of 49 μm, a tensile strength of 40.6 g/cm 2 and an elongation of 38% was obtained. Tensile strength and elongation are TGase
Not only is it less than 0.5 times that when
The film was easily soluble in water.
実施例 2
実施例1で得られるαs1−カゼイン膜80mgを、
脱イオン水100ml中に入れ、経時的に、この膜の
増加重量分を測定し、吸水量(gwater/g膜)
として表現した。結果は第1図に示すようにな
り、αs1−カゼイン膜1gあたり22g程度の水を
吸収した。Example 2 80 mg of α s1 -casein membrane obtained in Example 1 was
The increase in weight of this membrane was measured over time by placing it in 100 ml of deionized water, and the water absorption amount (gwater/g membrane) was calculated.
Expressed as. The results are shown in FIG. 1, and approximately 22 g of water was absorbed per gram of α s1 -casein membrane.
実施例 3
実施例1と同様の方法によつて、ゼラチンの10
重量%溶液から調製したゼラチン膜と、TGase
のみ添加せず、あとは全く同一条件で調製したゼ
ラチン膜を、各々10mgを1cm光路長の石英セル中
に入れ、脱イオン水3mlを加え電子冷熱式温度コ
ントローラー(島津製作所(株)製)を用いて20°よ
り35℃まで5℃おきに、10分間加温し、その時の
280nmの吸光度を測定し、溶解している蛋白質量
を測定した。結果は第2図に示すように、
TGase処理していないゼラチン膜は、28℃位か
ら吸光度が急激に増加し徐々に溶解してくる。こ
れに比して、TGase処理した膜は、吸光度の上
昇の割合がゆつくりとしており、かなり熱に対し
て安定であることが示唆される。これは、
TGase処理しない場合は、水素結合等の二次的
結合を主体とした膜のため、加熱で結合が切れ、
次第に溶解するのに比してTGase処理すれば、
ε−(γ−Glu)Lys架橋が生じ、共有結合を主体
とした膜となるために、熱に対しても比較的安定
になつたと考えられた。また、両者を沸盪浴水中
に浸漬すると、TGase処理膜は溶解しなかつた
が、TGase無添加膜は溶解した。Example 3 By the same method as in Example 1, gelatin 10
Gelatin membrane prepared from wt% solution and TGase
10 mg of each gelatin film prepared under exactly the same conditions without adding any additives was placed in a 1 cm optical path length quartz cell, 3 ml of deionized water was added, and an electronic cooling temperature controller (manufactured by Shimadzu Corporation) was used. Heat the temperature from 20° to 35°C every 5°C for 10 minutes using
Absorbance at 280 nm was measured to determine the amount of dissolved protein. The results are shown in Figure 2.
For gelatin membranes that have not been treated with TGase, the absorbance increases rapidly from around 28°C and gradually dissolves. In contrast, the rate of increase in absorbance of the TGase-treated film was slow, suggesting that it was fairly stable against heat. this is,
If TGase treatment is not performed, the film is mainly composed of secondary bonds such as hydrogen bonds, so the bonds will be broken by heating.
If treated with TGase, it will gradually dissolve.
It was thought that ε-(γ-Glu)Lys crosslinking occurred, resulting in a film mainly composed of covalent bonds, making it relatively stable against heat. Furthermore, when both were immersed in boiling water, the TGase-treated membrane did not dissolve, but the TGase-free membrane did.
実施例 4
Senらの方法(J.Agric.Food Chem.,29,348
(1981))に習つて、実施例1で得られるαs1−カ
ゼイン膜とαs1−カゼイン粉末の消化性を比較し
た。即ち、各々5mgを、0.1Mリン酸緩衝液(PH
8.0)2mlを加え、さらにキモトリプシン0.1mgを
添加、37℃でインキユベートした。適時反応溶液
を100℃、3分間加熱することによつて、キモト
リプシンを失活させ、反応を止めた。この反応溶
液中のアミノ基量をFields法(Biochem.J.,124,
581(1971))を用いて定量し、各時間における消
化率を次式の様に定義した。Example 4 Sen et al.'s method (J.Agric.Food Chem., 29 , 348
(1981)), the digestibility of the α s1 -casein membrane obtained in Example 1 and the α s1 -casein powder was compared. That is, 5 mg of each was added to 0.1M phosphate buffer (PH
8.0), 0.1 mg of chymotrypsin was added, and the mixture was incubated at 37°C. Chymotrypsin was inactivated and the reaction was stopped by heating the reaction solution at 100° C. for 3 minutes. The amount of amino groups in this reaction solution was determined by the Fields method (Biochem.J., 124 ,
581 (1971)), and the digestibility at each time was defined as follows.
消化率=観測時のアミノ基量/24時間後のアミノ基量
×100(%)
結果は第3図に示す。24時間後には、両者のア
ミノ基量はほぼ同一であり、膜化しても、充分消
化しえた。しかし、120分後までの消化率を比較
すると、αs1−カゼイン粉末では100%消化されて
いるのに比して、TGaseを作用させて得られる
cast膜では約60%と、かなり制御されていた。従
つて、TGaseによる蛋白質膜は、消化可能でか
つ、その分解速度をある程度制御しえる。 Digestibility = amount of amino groups at the time of observation/amount of amino groups after 24 hours x 100 (%) The results are shown in Figure 3. After 24 hours, the amounts of amino groups in both were almost the same, and even if they were formed into a membrane, they could be sufficiently digested. However, when comparing the digestibility up to 120 minutes, α s1 -casein powder is 100% digested, whereas α s1 -casein powder is digested at 100%.
With the cast film, it was approximately 60%, which was quite controlled. Therefore, protein membranes can be digested by TGase, and the rate of degradation can be controlled to some extent.
実施例 5
実施例1にて得られるαs1−カゼイン膜は、有
機溶媒中で安定で不溶である。そこで、有機溶媒
中で、このαs1−カゼイン膜がどのような透過性
を示すかを、メチレンブルー(MW.373.90,νnax
660nm)、クマシーブリリアントブルー
(MW.695.61,νnax590nm)、ビタミンB12
(MW.1355.42,νnax560nm)を用いて観察した。
3種類の化合物を各各小試験管に入れ、TGase
作用によつて得られたαs1−カゼインcast膜で密
封し、大量のエタノール中に浸漬した。もし、こ
れらの化合物がcast膜を介して放出されるなら、
外液(エタノール)が各化合物特有の色がつき、
その最大吸収波長を観察すれば、膜を介してどの
くらい透過されているのか知ることができる。15
℃から40℃へ5℃/分の割で昇温し、次に5℃/
分の割で40℃から15℃へと冷却する操作を繰り返
し行ない、60分間、外液に放出される上記3種類
の化合物の透過率を求めて第4図に示した。メチ
レンブルーでは、浸漬すると比較的速やかに透過
され、40分後には、完全に透過された。それに比
して、クマシーブリリアントブルーは、60分後に
約20%が透過し、ビタミンB12では、ほとんど透
過されないことが観察された。従つて、60分後の
透過率を比較すると、
メチレンブルー>クマシーブリリアントブルー
>ビタミンB12
の順となつた。即ち、分子量の大きさによつて透
過性に大小が生じていた。従つて分子量が大きい
程、透過しずらくなつており、分子篩効果がある
ことが示めされた。Example 5 The α s1 -casein membrane obtained in Example 1 is stable and insoluble in organic solvents. Therefore, we investigated the permeability of this α s1 -casein membrane in organic solvents using methylene blue (MW.373.90, ν nax
660nm), Coomassie Brilliant Blue (MW.695.61, ν nax 590nm), Vitamin B 12
(MW.1355.42, ν nax 560 nm).
Place the three compounds in each small test tube and add TGase.
The resulting α s1 -casein cast membrane was sealed and immersed in a large amount of ethanol. If these compounds are released through the cast membrane,
The external solution (ethanol) takes on a color unique to each compound,
By observing the maximum absorption wavelength, it is possible to determine how much light is being transmitted through the film. 15
℃ to 40℃ at a rate of 5℃/min, then 5℃/min.
The operation of cooling from 40°C to 15°C in portions was repeated, and the transmittance of the above three types of compounds released into the external liquid for 60 minutes was determined and is shown in Figure 4. Methylene blue was penetrated relatively quickly after immersion, and completely penetrated after 40 minutes. In comparison, it was observed that about 20% of Coomassie Brilliant Blue penetrated after 60 minutes, and almost no penetration of vitamin B12 . Therefore, when comparing the transmittance after 60 minutes, the order was methylene blue>Coomassie brilliant blue>vitamin B12 . That is, the permeability varies depending on the molecular weight. Therefore, it was shown that the larger the molecular weight, the more difficult it is to permeate, and that there is a molecular sieve effect.
第1,2,3および4図はそれぞれ実施例2,
3,4および5の実験結果を示す。第1図の図
中、横軸は浸漬時間(分)、縦軸は吸水量(g
water/gcast膜)を示す。第2図の図中、横軸
は温度(℃)、縦軸は280nmにおける吸光度を示
す。●はTGase添加ゼラチン膜、○はTGase無
添加ゼラチン膜の値を示す。第3図の図中、横軸
は消化時間(分)、縦軸は消化率(%)を示す。
●はTGase添加αs1カゼイン膜、○はαs1カゼイン
粉末の値を示す。第4図の図中、横軸は浸漬時間
(分)、縦軸は透過率(%)を示す。△はメチレン
ブルー、●はクマシーブリリアントブルー、○は
ビタミンB12の値を示す。
Figures 1, 2, 3 and 4 are Example 2, respectively.
The experimental results of 3, 4 and 5 are shown. In Figure 1, the horizontal axis is immersion time (minutes), and the vertical axis is water absorption amount (g
water/gcast film). In the diagram of FIG. 2, the horizontal axis shows temperature (°C), and the vertical axis shows absorbance at 280 nm. ● indicates the value for the gelatin membrane with TGase added, and ○ indicates the value for the gelatin membrane without the addition of TGase. In the diagram of FIG. 3, the horizontal axis shows the digestion time (minutes), and the vertical axis shows the digestibility (%).
● indicates the value of TGase-added α s1 casein membrane, and ○ indicates the value of α s1 casein powder. In FIG. 4, the horizontal axis represents immersion time (minutes), and the vertical axis represents transmittance (%). △ indicates methylene blue, ● indicates Coomassie brilliant blue, and ○ indicates the value of vitamin B12 .
Claims (1)
ランスグルタミナーゼを蛋白1gに対して1ユニ
ツト以上添加し、型枠に流し込み10ないし60℃に
て水分を20%以下にまで乾燥することを特徴とす
る蛋白質膜。1. Adding 1 unit or more of transglutaminase per 1 g of protein to a protein-containing solution with a protein concentration of 2% by weight or more, pouring into a mold, and drying at 10 to 60°C until the moisture content is 20% or less. protein membrane.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP28169084A JPS61152247A (en) | 1984-12-26 | 1984-12-26 | Production of protein membrane |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP28169084A JPS61152247A (en) | 1984-12-26 | 1984-12-26 | Production of protein membrane |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61152247A JPS61152247A (en) | 1986-07-10 |
| JPH0581218B2 true JPH0581218B2 (en) | 1993-11-11 |
Family
ID=17642621
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP28169084A Granted JPS61152247A (en) | 1984-12-26 | 1984-12-26 | Production of protein membrane |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS61152247A (en) |
Families Citing this family (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2705024B2 (en) * | 1987-07-02 | 1998-01-26 | マルハ株式会社 | Food manufacturing method |
| JPH02107163A (en) * | 1988-10-15 | 1990-04-19 | Suntory Ltd | Production of novel gelatinous food |
| JP2782849B2 (en) * | 1988-12-08 | 1998-08-06 | 味の素株式会社 | Vegetable protein powder and method for producing tofu using the same |
| NZ522071A (en) * | 2002-10-18 | 2005-07-29 | Patrick Joseph Silcock | Hydrolysed casein phosphoprotein preparations for bioactive metal ion delivery and teeth remineralisation |
| EP1645907A1 (en) * | 2004-10-07 | 2006-04-12 | N-Zyme BioTec GmbH | Protein-coated substrates and their preparation |
| DE102006033167A1 (en) | 2006-07-10 | 2008-01-24 | Gelita Ag | Use of gelatin and a crosslinking agent for the preparation of a crosslinking medical adhesive |
| DE102006033168A1 (en) | 2006-07-10 | 2008-01-17 | Gelita Ag | Use of gelatin and a crosslinking agent for the preparation of a crosslinking therapeutic composition |
| JP5562042B2 (en) * | 2008-01-15 | 2014-07-30 | 株式会社 資生堂 | Microparticle film composition |
| JP7445378B2 (en) * | 2017-09-29 | 2024-03-07 | 大日本印刷株式会社 | Packaging films and packaging containers |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS521057A (en) * | 1975-06-24 | 1977-01-06 | Shiyokuhin Kougiyou Hatsuten K | Continuous production of apparatus for film like protein food |
| DE3263869D1 (en) * | 1981-06-19 | 1985-07-04 | Ciba Geigy Ag | Aminoalkyl-substituted aromatic amines and process for their preparation |
| JPS58149645A (en) * | 1982-03-01 | 1983-09-06 | Ajinomoto Co Inc | Preparation of gelatinized material |
| JPS5959151A (en) * | 1982-09-29 | 1984-04-04 | Ajinomoto Co Inc | Preparation of novel gelatinous food |
-
1984
- 1984-12-26 JP JP28169084A patent/JPS61152247A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61152247A (en) | 1986-07-10 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US5834232A (en) | Cross-linked gelatin gels and methods of making them | |
| Li et al. | Ultrasonic irradiation in the enzymatic extraction of collagen | |
| JPH0581218B2 (en) | ||
| JPH0411254B2 (en) | ||
| JP2004534137A (en) | Keratin-based product and method for producing the same | |
| WO2005079879A1 (en) | Collagen gel and process for producing the same | |
| JPH05285374A (en) | Microcapsules using recycled natural keratin as wall material and method for producing the same | |
| CN104449587A (en) | Preparation method of paraffin microcapsules | |
| JP2619933B2 (en) | Method for producing high polymerization degree gelatin | |
| CN106946987B (en) | High concentration acid-soluble collagen solution and preparation method of water-soluble collagen solution | |
| JPH03259928A (en) | Production of highly polymeric gelatin | |
| US3057782A (en) | Cross-linked gelatin plasma substitute and production thereof | |
| US20060078962A1 (en) | Polysaccharide-based polymers and methods of making the same | |
| EP3921372B1 (en) | Protein hydrogel, preparation method and use thereof | |
| US5856120A (en) | Method of preparing a biological material for use in ophthalmology | |
| JPH02240165A (en) | Aqueous silk fibroin solution with excellent storage stability and preparation thereof | |
| CN102558589B (en) | Preparation method of formaldehyde cross-linked gelatin/polyvinyl alcohol(PVA) composite membrane | |
| US6037144A (en) | Method of preparing a biological material for use in ophthalmology | |
| CN113416320B (en) | A degradable protein hydrogel based on the regulation of mechanical signals and its preparation method and application | |
| WO2005092960A1 (en) | Biocompatible porous material and process for producing the same | |
| JPS6058056A (en) | Production of transparent egg white gel material | |
| US3536587A (en) | Enzyme resin and a process for the preparation thereof | |
| CN110498932A (en) | Casein-pectin-protocatechuic acid ternary compound, its preparation method and application | |
| JP2671226B2 (en) | Silk fibroin aqueous solution having excellent storage stability and method for producing the same | |
| JPS61227783A (en) | Production of immobilized enzyme membrane |