JPS63287447A - Production of milk protein conjugated material - Google Patents

Production of milk protein conjugated material

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Publication number
JPS63287447A
JPS63287447A JP62122728A JP12272887A JPS63287447A JP S63287447 A JPS63287447 A JP S63287447A JP 62122728 A JP62122728 A JP 62122728A JP 12272887 A JP12272887 A JP 12272887A JP S63287447 A JPS63287447 A JP S63287447A
Authority
JP
Japan
Prior art keywords
milk protein
chitosan
weight
complex
protein complex
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP62122728A
Other languages
Japanese (ja)
Other versions
JPH0648955B2 (en
Inventor
Koji Kikuchi
菊地 幸治
Mitsuhisa Kin
金 光永
Itaru Yamamoto
格 山本
Naoki Yagi
直樹 八木
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
MINAMINIHON RAKUNOU KYODO KK
Minami Nihon Rakuno Kyodo Co Ltd
Original Assignee
MINAMINIHON RAKUNOU KYODO KK
Minami Nihon Rakuno Kyodo Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by MINAMINIHON RAKUNOU KYODO KK, Minami Nihon Rakuno Kyodo Co Ltd filed Critical MINAMINIHON RAKUNOU KYODO KK
Priority to JP62122728A priority Critical patent/JPH0648955B2/en
Publication of JPS63287447A publication Critical patent/JPS63287447A/en
Publication of JPH0648955B2 publication Critical patent/JPH0648955B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

PURPOSE:To obtain the titled conjugated material having excellent heat resistance, processing properties and cooking properties inexpensively and readily, comprising milk protein and chitosan, by using extruder processing method and adjusting pH. CONSTITUTION:The aimed conjugated material which consists of (A) milk protein and (B) 0.5-7wt.% based on the component A of chitosan, is in a state of a solid substance having 30-90wt.% water content or of emulsion, shows pH5.0-7.5 and is obtained by extruder processing method. Further the conjugated material preferably contains (C) 20-100wt.% based on the component A of a saccharide or (D) <=40wt.% based on the component A of fats and oils or (E) 10-40wt.% based on the component A of protein except the component A or (F) 100-250wt.% based on the component A of raw meat or processed meat or a mixture thereof.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は乳蛋白質複合体の製法、さらに詳しくは耐熱性
、加工性および調理性に優れた乳蛋白質−キトサン複合
体のエクストルーダ加工法による製法に関する。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a method for producing a milk protein complex, and more particularly to a method for producing a milk protein-chitosan complex having excellent heat resistance, processability, and cookability using an extruder processing method.

発明の背景 カゼインは乳中に含まれる蛋白質の大部分を占めるもの
であり、その優れた栄養性(アミノ酸バランス、消化吸
収性など)と機能性(保水性、乳化性、風味など)によ
り食品素材として幅広く使用されている。
Background of the Invention Casein makes up the majority of the protein contained in milk, and is used as a food material due to its excellent nutritional properties (amino acid balance, digestibility, etc.) and functionality (water retention, emulsifying properties, flavor, etc.) It is widely used as.

このカゼインを利用して組織状や繊維状の組織化物を得
ようとする試みは古くからあるが(特公昭49−110
856号、特公昭51−1788号など)、それらの試
みは、調理時におけるカゼインの加熱溶融性のためにあ
らかじめ付与しておいたテキスチャーが失われてしまう
;製造工程が複雑であるという欠点を有しており、実用
性に乏しいものであった。
Attempts to obtain textured or fibrous structured products using this casein have been made for a long time (Special Publication No. 49-110
856, Japanese Patent Publication No. 51-1788, etc.), these attempts had the disadvantage that the texture imparted in advance was lost due to the heat-melting nature of casein during cooking; the manufacturing process was complicated. However, it lacked practicality.

発明が解決しようとする問題点 従って、前記カゼインの加熱溶融性を克服し、かつ工程
が簡単であるカゼイン組織化物の製法の出現が望まれて
いる。
Problems to be Solved by the Invention Accordingly, it is desired to develop a method for producing a structured casein product that overcomes the heat-melting property of casein and has a simple process.

発明者らはかかる状況に鑑みて鋭意研究に励んだ結果、
カゼインの加熱溶融性を克服するものとして乳蛋白質と
カチオン系高分子化合物であるキトサンより成る新規な
乳蛋白質複合体を提供する発明を完成するに至り、既に
特許出願した(特願昭62−645号)。該出願の明細
書においては、該乳蛋白質複合体の製造に関し、乳蛋白
質とキトサンを混合し、pH1l!整し、加熱するとい
う旨の開示しかなされていないが、発明者らはその後ら
鋭意研究を続行した結果、エクストルーダ加工法が該乳
蛋白質複合体の製造について有効であり、かつ優れた組
織性を有する乳蛋白質複合体が得られること、さらには
乳蛋白質とキトサン以外に糖類、油脂、乳蛋白質以外の
蛋白質または生肉もしくは加工肉をも添加して同様に優
れた組織性を有する乳蛋白質複合体が得られることを見
い出し、本発明を完成するに至った。
In view of this situation, the inventors worked diligently on research, and as a result,
We have completed an invention to provide a novel milk protein complex consisting of milk protein and chitosan, a cationic polymer compound, which overcomes the heat-melting property of casein, and have already filed a patent application (Japanese Patent Application No. 62-645). issue). In the specification of the application, regarding the production of the milk protein complex, milk protein and chitosan are mixed and the pH is adjusted to 11! Although the disclosure only states that the milk protein complex is prepared and heated, the inventors continued their intensive research and found that the extruder processing method is effective for producing the milk protein complex and provides excellent texture. Furthermore, in addition to milk protein and chitosan, sugars, fats and oils, proteins other than milk protein, or raw meat or processed meat can be added to obtain a milk protein complex having similar excellent texture. The present inventors have discovered that the present invention can be obtained, and have completed the present invention.

問題点を解決するための手段 本発明は、エクストルーダ加工法を用いて、乳蛋白質と
乳蛋白質に対し0.5〜7重量%のキトサンとより成る
乳蛋白質複合体であって水分30〜90%を含む固形物
または懸濁物の状態でPH5,0〜7,5を示す乳蛋白
質複合体を得ることを特徴とする乳蛋白質複合体の製法
を提供するものである。
Means for Solving the Problems The present invention uses an extruder processing method to produce a milk protein complex consisting of milk protein and chitosan in an amount of 0.5 to 7% by weight based on the milk protein, with a water content of 30 to 90%. The present invention provides a method for producing a milk protein complex, which is characterized by obtaining a milk protein complex exhibiting a pH of 5.0 to 7.5 in the form of a solid or suspension containing the following.

乳蛋白質複合体の原料として用いる乳蛋白質としては、
主として、乳中のカゼインおよびその塩であるカゼイン
ソーダ、カゼインカリウムが挙げられる。また、ホエー
アルブミンおよびポエーグロプリンもカゼインと同様な
効果があり、単独であるいはカゼインまたはカゼイネー
トと組合せて用いることができる。
Milk proteins used as raw materials for milk protein complexes include:
Main examples include casein found in milk and its salts, caseinate soda and caseinate potassium. Whey albumin and poeglopurin also have similar effects to casein and can be used alone or in combination with casein or caseinate.

一方、もう1つの原料であるキトサンは、主としてエビ
、カニ等の甲殻類の組織中に含まれるキチンを脱アセチ
ル化処理したものであり、通常、フレーク状または粉末
状である。このものは、近年、医薬・食品あるいは水処
理への応用が注目されており、商業的に入手可能である
か、または常法により容易に調製される。
On the other hand, chitosan, which is another raw material, is obtained by deacetylating chitin mainly contained in the tissues of crustaceans such as shrimp and crabs, and is usually in the form of flakes or powder. This product has recently attracted attention for its application to medicines, foods, and water treatment, and is either commercially available or easily prepared by conventional methods.

本発明の乳蛋白質複合体の製法においては、前記原料を
エクストルーダに供給してエクストルーダ加工を行う。
In the method for producing a milk protein complex of the present invention, the raw materials are supplied to an extruder and subjected to extruder processing.

供給する形態としては、キトサンの場合、常法に従って
1〜25重量%乳酸水溶液の如き有機酸の水溶液に溶解
せしめて溶液とする。この場合、キトサン濃度は0.5
〜25重量%、好ましくは3〜IO重量%とする。なお
、6〜25重量%の高濃度域ではキトサン溶解物がゲル
性を呈するようになり、通常の撹拌機を用いる溶解工程
での溶解が困難となるため、サイレントカッターや、望
ましくは脱気装置付きのバッチ式カッター、または本発
明で用いる如きエクストルーダを用いて溶解させる必要
がある。
In the case of chitosan, it is supplied as a solution by dissolving it in an aqueous solution of an organic acid such as a 1 to 25% by weight aqueous lactic acid solution according to a conventional method. In this case, the chitosan concentration is 0.5
-25% by weight, preferably 3-IO% by weight. In addition, in the high concentration range of 6 to 25% by weight, the chitosan solution becomes gelatinous and difficult to dissolve in the dissolution process using a normal stirrer, so a silent cutter or preferably a degassing device is used. It is necessary to melt using a batch type cutter with a holder or an extruder such as the one used in the present invention.

一方、乳蛋白質の供給形態については、塩酸カゼインま
たは乳酸カゼインの場合、炭酸ソーダ、炭酸カリウム、
炭酸水素カリウムまたは炭酸水素ナトリウムの如き粉末
状アルカリ剤と粉末混合しておくか、あるいは水酸化ナ
トリウム、水酸化カリウムの如き潮解性アルカリの水溶
液に5〜30重量%の高濃度にて溶解させておく。後者
の場合には前記の如きサイレントカッター、バッチ式カ
ッターまたはエクストルーダを用いて溶解させるが、カ
ゼインはこの時アルカリ塩となる。カゼインjこ対する
アルカリ剤の添加量は、10重量%のカゼイン溶液とし
たとき、pHが6.θ〜9.0の範囲内となるように選
択する。p■(が9.0を超える添加量だと、80℃以
上に加熱すると蛋白質の分解が促進されてアンモニアが
発生するので好ましくない。また、p)lが6.0未満
となる添加量だと、カゼインが十分にアルカリ塩になら
ず未溶解のままなので不適当である。カゼインソーダま
たはカゼインカリウムの如きアルカリ塩の形のものはそ
のまま単独で用いる。
On the other hand, regarding the supply form of milk protein, in the case of casein hydrochloride or casein lactate, soda carbonate, potassium carbonate,
Either by mixing the powder with a powdered alkaline agent such as potassium hydrogen carbonate or sodium hydrogen carbonate, or by dissolving it at a high concentration of 5 to 30% by weight in an aqueous solution of a deliquescent alkali such as sodium hydroxide or potassium hydroxide. put. In the latter case, the casein is dissolved using a silent cutter, a batch type cutter, or an extruder as described above, and the casein becomes an alkali salt at this time. The amount of alkaline agent added to casein j is such that when the casein solution is 10% by weight, the pH is 6. It is selected so that it is within the range of θ to 9.0. If the amount of p■( exceeds 9.0), heating above 80°C will promote protein decomposition and generate ammonia, which is undesirable.Also, the amount of addition that makes p)l less than 6.0 is undesirable. This is inappropriate because the casein is not sufficiently converted into an alkaline salt and remains undissolved. Alkaline salts such as caseinate soda or caseinate potassium are used alone.

本発明において用いることができるエクストルーダには
一軸エクストルーダ、二軸エクストルーダなどのタイプ
があるが、通常、カゼインソーダの製造などに用いられ
ているものならばいずれも使用でき、特に限定されるも
のではない。
There are several types of extruders that can be used in the present invention, such as a single-screw extruder and a twin-screw extruder, but any type that is normally used in the production of casein soda can be used, and there are no particular limitations. .

以下、第1図のフロー・シートを参照して説明する。第
1図において、Aはフードカッター、Bはフィーダー、
Cはバレル、Dはグイ、Eはもう1つのフィーダーを表
わす。
This will be explained below with reference to the flow sheet shown in FIG. In Figure 1, A is a food cutter, B is a feeder,
C stands for barrel, D stands for goo, and E stands for another feeder.

前記の如き粉末または濃厚溶液の供給形態とした乳蛋白
質原料とキトサン溶液とをあらかじめAのフードカッタ
ーにて混合し、次いでBのフィーダーで定量的にバレル
Cに供給する。別法として、乳蛋白質原料とキトサン原
料とをB%Eの別のフィーダーで供給することもできる
The milk protein raw material in the form of a powder or concentrated solution as described above and the chitosan solution are mixed in advance using a food cutter A, and then quantitatively fed to barrel C using a feeder B. Alternatively, the milk protein raw material and the chitosan raw material can be fed in separate feeders at B%E.

いずれの場合においても、バレルC中での混合時に乳蛋
白質に対するキトサンの割合が0.5〜7重量%となる
ように各原料の供給量を選択するか、あるいは予備混合
する。また、該バレル中での混合時に、pHは5.0〜
7.5となるようにする。
In either case, the amount of each raw material to be supplied is selected or premixed so that the ratio of chitosan to milk protein is 0.5 to 7% by weight during mixing in barrel C. Also, during mixing in the barrel, the pH is 5.0~
Make it 7.5.

これらの原料がバレルに供給されると、例えばスクリュ
ー回転数30 Orpm、バレル温度110℃の条件で
エクストルーダを運転する。乳蛋白質の熱変性の関係で
温度は約140℃の上限が要請されるが、他の条件はエ
クストルーダの機種、原料などにより適宜選択される。
When these raw materials are supplied to the barrel, the extruder is operated under conditions such as a screw rotation speed of 30 Orpm and a barrel temperature of 110°C. Due to thermal denaturation of milk protein, an upper limit of about 140° C. is required for the temperature, but other conditions are appropriately selected depending on the extruder model, raw materials, etc.

かくして、定量的にバレルに供給された原料ばバレル中
のスクリューにより混合、撹拌されながら出口側に進行
し、その間にゲル化し、粘着性の高い塊状の乳蛋白質−
キトサン複合体となってエクストルーダの出口に導かれ
、ダイDの形に応じた組織化物として系外に排出される
。通常、エクストルーダ中での滞留時間は15〜60秒
とするが、バレルを60〜140℃に加熱すると複合体
生成反応が促進され、短時間で組織化が起こることかわ
かった。なお、吐出物はpH5,0〜7.5の範囲とな
ることが確認できた。
In this way, the raw materials quantitatively supplied to the barrel proceed to the exit side while being mixed and stirred by the screw in the barrel, during which time they gel and form highly sticky lumps of milk protein.
The chitosan complex is guided to the exit of the extruder, and is discharged from the system as a structured material according to the shape of the die D. Usually, the residence time in the extruder is 15 to 60 seconds, but it has been found that heating the barrel to 60 to 140° C. accelerates the complex formation reaction and causes organization in a short time. In addition, it was confirmed that the pH of the discharged material was in the range of 5.0 to 7.5.

また、本発明は、エクストルーダ加工法を用いて、乳蛋
白質と乳蛋白質に対し0.5〜7重量%のキトサンと乳
蛋白質に対し20〜!00重量%の糖類とより成る乳蛋
白質複合体であって水分30〜90%を含む固形物また
は懸濁物の状態でpH5,0〜7.5を示す乳蛋白質複
合体を得ることを特徴とする乳蛋白質複合体の製法を提
供するものである。
In addition, the present invention uses an extruder processing method to obtain chitosan of 0.5 to 7% by weight for milk protein and 20% for milk protein. 00% by weight of saccharides and exhibiting a pH of 5.0 to 7.5 in the form of a solid or suspension containing 30 to 90% water. The present invention provides a method for producing a milk protein complex.

前記の乳蛋白質−キトサン複合体の製法において、乳蛋
白質とキトサン以外に、乳糖、デキストリン、グルコー
ス、蔗糖、デンプン、化エデンブン、マルトース、プル
ラン、異性化糖(クルコース、フラクトース混合液)、
ラフィノース、マルチトール、ソルビトール、グリセロ
ールの如き糖類(本明細書中でいう糖類には糖アルコー
ルを含めるものとする)あるいはこれらの混合物を原料
として、乳蛋白質に対し20〜!00重量%、好ましく
は30〜70重猷%加えて、同様にエクストルーダ加工
を行うと膨化状組織化物が得られる。
In the method for producing the milk protein-chitosan complex, in addition to milk protein and chitosan, lactose, dextrin, glucose, sucrose, starch, edenbane, maltose, pullulan, isomerized sugar (a mixture of crucose and fructose),
Sugars such as raffinose, maltitol, sorbitol, and glycerol (saccharides in this specification include sugar alcohols) or mixtures thereof are used as raw materials to give milk proteins a 20~! If 00% by weight, preferably 30 to 70% by weight is added and extruder processing is performed in the same manner, a swollen structured product is obtained.

これらの糖類は粉末として別系統でバレルに供給しても
よく、または乳蛋白質原料と混合してから供給してもよ
く、あるいは乳蛋白質原料、キトサン原料と混合してか
ら供給してもよい。いずれの場合においても、バレル中
にて乳蛋白質に対しキトサンが0.5〜7重量%、pH
5,0〜7.5となるように行う。また、エクストルー
ダの運転条件は前記と同様、適宜選択できる。
These saccharides may be supplied to the barrel as a powder in a separate system, or may be supplied after being mixed with the milk protein raw material, or may be supplied after being mixed with the milk protein raw material or chitosan raw material. In either case, chitosan was added at a pH of 0.5 to 7% by weight based on the milk protein in the barrel.
Do this so that the ratio is between 5.0 and 7.5. Further, the operating conditions of the extruder can be selected as appropriate, as described above.

さらに、本発明は、エクストルーダ加工法を用いて、乳
蛋白質と乳蛋白質に対し0.5〜7重量%のキトサンと
乳蛋白質に対し40重量%以下の油脂゛とより成る乳蛋
白質複合体であって水分30〜90%を含む固形物また
は懸濁物の状態でpH5,0〜7.5を示す乳蛋白質複
合体を得ることを特徴とする乳蛋白質複合体の製法、エ
クストルーダ加工法を用いて、乳蛋白質と乳蛋白質に対
し0゜5〜7重量%のキトサンと乳蛋白質に対し10〜
40重量%の乳蛋白質以外の蛋白質とより成る乳蛋白質
複合体であって水分30〜90%を含む固形物または懸
濁物の状態でpH5,0〜7.5を示す乳蛋白質複合体
を得ることを特徴とする乳蛋白質複合体の製法、ならび
にエクストルーダ加工法を用いて、乳蛋白質と乳蛋白質
に対し0.5〜7重量%のキトサンと乳蛋白質に対し1
00〜250重量%の生肉もしくは加工肉またはそれら
の混合物とより成る乳蛋白質複合体であって水分30〜
90%を含む固形物または懸濁物の状態でpH5,0〜
7.5を示す乳蛋白質複合体を得ることを特徴とする乳
蛋白質複合体の製法を提供するものである。
Furthermore, the present invention provides a milk protein complex consisting of milk protein, chitosan in an amount of 0.5 to 7% by weight based on the milk protein, and oil and fat in an amount of 40% by weight or less based on the milk protein, using an extruder processing method. A method for producing a milk protein complex, characterized by obtaining a milk protein complex exhibiting a pH of 5.0 to 7.5 in the form of a solid or suspension containing 30 to 90% water, using an extruder processing method. , 0° for milk protein and 5-7% by weight of chitosan and 10-10% for milk protein.
Obtaining a milk protein complex consisting of 40% by weight of proteins other than milk protein and exhibiting a pH of 5.0 to 7.5 in the form of a solid or suspension containing 30 to 90% water. Using a method for producing a milk protein complex and an extruder processing method characterized by
A milk protein complex consisting of 00 to 250% by weight of raw meat or processed meat or a mixture thereof, with a water content of 30 to 250% by weight.
pH 5.0~ in solid form or suspension containing 90%
The present invention provides a method for producing a milk protein complex, which is characterized by obtaining a milk protein complex exhibiting a molecular weight of 7.5.

前記の乳蛋白質−キトサン複合体の製法において、乳蛋
白質とキトサン以外に、各々、乳蛋白質に対し40重量
%以下、好ましくは10〜30重量%のサラダ油、ラー
ド、ヘッド、バター、バターオイル、植物性硬化油脂の
如き動植物性油脂またはこれらの混合物、乳蛋白質に対
し10〜40重量%、好ましくは20〜30重量%の卵
白、大豆蛋白質、ホエー蛋白質濃縮物、グルテン、コラ
ーゲンの如き乳蛋白質以外の蛋白質またはこれらの混合
物、あるいは乳蛋白質に対し100〜250重量%、好
ましくは150〜200重量%の魚肉すり身、畜肉の如
き生肉もしくは加工肉またはそれらの混合物を原料とし
て加えてエクストルーダ加工を行うと、各々、油脂を乳
化した組織化物、第2図に一例として添加物濃度とゲル
強度の関係を示す如く耐熱性・ゲル強度が異なる組織化
物、あるいは耐熱性に優れ、方向性のある繊維性組織化
物が得られる。いずれの場合においても、前記乳蛋白質
−キトサン−糖類複合体の場合と同様に第3原料は種々
の方法で供給できるが、バレル中で乳蛋白質に対しキト
サンが0.5〜7重量%、PH5、0〜7.5となるよ
うに行い、また、エクストルーダの運転条件は適宜選択
できる。
In the above-mentioned method for producing a milk protein-chitosan complex, in addition to milk protein and chitosan, salad oil, lard, head, butter, butter oil, and vegetable oil are each added in an amount of 40% by weight or less, preferably 10 to 30% by weight based on the milk protein. Animal and vegetable oils and fats such as hydrogenated fats and oils, or mixtures thereof, 10 to 40% by weight, preferably 20 to 30% by weight of milk protein, other than milk proteins such as egg white, soybean protein, whey protein concentrate, gluten, and collagen. When extruder processing is performed by adding protein or a mixture thereof, or milk protein in an amount of 100 to 250% by weight, preferably 150 to 200% by weight of raw meat such as minced fish meat, raw meat such as livestock meat, processed meat, or a mixture thereof as a raw material, These are structured products that emulsify fats and oils, structured products that have different heat resistance and gel strength as shown in Figure 2, which shows the relationship between additive concentration and gel strength, or structured fibrous products that have excellent heat resistance and directionality. is obtained. In either case, the third raw material can be supplied in various ways as in the case of the milk protein-chitosan-saccharide complex, but the third raw material can be supplied in a barrel with 0.5 to 7% by weight of chitosan based on the milk protein and a pH of 5. , 0 to 7.5, and the operating conditions of the extruder can be selected as appropriate.

本発明の製法によるエクストルーダ加工物は種々に利用
できる。
The extruder processed product produced by the manufacturing method of the present invention can be used in various ways.

乳蛋白質−キトサン複合体ならびにさらにホエーアルブ
ミン、ホエーグロブリン、卵白、大豆蛋白質等をも成分
とする組織化物である複合体は、押出物を繊維状、板状
、粒状に加工し、ハンバーグや中華スープ等の他の食材
と組み合せて食用とすることができる。あるいは、押出
物をドラム乾燥法、流動層乾燥法、棚式乾燥法または凍
結乾燥法等により乾燥し、細粒化・粉末化し、または微
繊維化して他の食材と共に調理することもできる。
The complex, which is a structured product containing milk protein-chitosan complex as well as whey albumin, whey globulin, egg white, soybean protein, etc., is produced by processing the extrudate into fibers, plates, and granules, and making it into hamburgers and Chinese soups. It can be made edible by combining with other ingredients such as. Alternatively, the extrudate can be dried by a drum drying method, a fluidized bed drying method, a shelf drying method, a freeze drying method, etc., and then pulverized, powdered, or microfiberized and cooked together with other foods.

乳糖をも成分とする膨化組織化物のような糖類をも成分
とする複合体は、湯もどり性がよく、ハンバーグ等の組
織状増量材として利用できる。
Complexes that also contain sugars, such as puffed textured products that also contain lactose, have good rehydration properties and can be used as textured fillers for hamburger steaks and the like.

魚肉、畜肉のような肉をも成分とする配向性のある組織
化物である複合体は、調味料と組み合せて調味すること
により珍味とすることができる。
A complex, which is an oriented structured material containing meat such as fish or livestock meat, can be made into a delicacy by being seasoned in combination with seasonings.

油脂をも成分とする複合体は、糖類をも成分とする複合
体と同様に、ハンバーグ等への増量材に利用できる。
A complex containing fats and oils as a component can be used as a filler for hamburgers and the like, similar to a complex containing sugars as a component.

発明の効果 本発明の製法により得られる乳蛋白質複合体は、一般に
、30〜60%の水分を含有する凝集物として得られ、
このものあるいは粉末化物をもどしたものは熱ゲル化性
に優れており、従来のカゼインの加熱溶融性を克服する
ものであって耐熱性を有する。また、保水性および復水
性も良好である。
Effects of the Invention The milk protein complex obtained by the production method of the present invention is generally obtained as an aggregate containing 30 to 60% water,
This product or the reconstituted powdered product has excellent heat gelling properties, overcomes the heat-melting property of conventional casein, and has heat resistance. In addition, water retention and water condensation properties are also good.

従って、調理性、加工性にも優れたものである。Therefore, it has excellent cooking properties and processability.

さらに、乳蛋白質、キトサン以外の第3成分を加えて得
られる乳蛋白質複合体は前記の如く種々の機能を付与さ
れたものであって多様な使用が可能である。
Furthermore, the milk protein complex obtained by adding a third component other than milk protein and chitosan is endowed with various functions as described above, and can be used in a variety of ways.

このような優れた特性を有する乳蛋白質複合体が、本発
明のエクストルーダ加工法による製法によって簡単な工
程で製造でき、安価に供給される。
A milk protein complex having such excellent properties can be produced in a simple process by the extruder processing method of the present invention, and can be supplied at low cost.

また、エクストルーダ加工法によると反応系の水分が3
0〜60%という低水分系で加工できるので、吐出物か
ら粉末化物を得る際の水分蒸発量が低く押さえられ、省
エネルギーの観点からも有利である。
Also, according to the extruder processing method, the water content in the reaction system is 3.
Since it can be processed with a low moisture system of 0 to 60%, the amount of moisture evaporated when obtaining a powdered product from the discharged material can be kept low, which is also advantageous from the viewpoint of energy saving.

以下に実施例を挙げて本発明をさらに詳しく説明する。The present invention will be explained in more detail with reference to Examples below.

各実施例において、エクストルーダはウニルナ−フライ
ド社製Continua  37 / 27 Pを用い
た。なお、エクストルーダを用いる場合のフロー・シー
トは第1図に示した。
In each example, the extruder used was Continua 37/27P manufactured by Unirnafried. The flow sheet for using an extruder is shown in FIG.

実施例1 カゼインソーダ5に9をフードカッターAに入れ、5%
キトサン−乳酸水溶液5に9を加えて分散させた。この
分散物を110℃に加熱したバレルに150g/分の供
給速度で供給した。スクリュー回転300 rpo+で
運転し、乳蛋白質−キトサン複合体8に9をダイDより
吐出した。該複合体は透明なソフトなゲル状のプラスチ
ック組織を有する組織化物であって、42.0%の水分
を含み、pF[は5゜5であった。
Example 1 Put 5 and 9 of casein soda into food cutter A, and add 5%
9 was added to chitosan-lactic acid aqueous solution 5 and dispersed. This dispersion was fed into a barrel heated to 110° C. at a feed rate of 150 g/min. The system was operated at a screw rotation of 300 rpo+, and 9 was discharged from the die D onto the milk protein-chitosan complex 8. The composite was a textured material having a transparent soft gel-like plastic structure, contained 42.0% water, and had a pF of 5.5.

該組織化物をpH6,8の0.02Mリン酸緩衝液中、
95℃にて5分間加熱した場合の乳蛋白質溶出率は4.
5%であった。
The assembled product was placed in a 0.02M phosphate buffer at pH 6.8.
The milk protein elution rate when heated at 95°C for 5 minutes was 4.
It was 5%.

実施例2 カゼインソーダ5に9および乳糖2に9をフードカッタ
ーAに入れ、5%キトサン−乳酸水溶液5に9を分散さ
せた。この分散物を110℃に加熱したバレルに150
9/分の供゛給速度で供給した。スクリュー回転300
 rpmで運転し、出口温度100〜105℃にて均一
に膨化した乳蛋白質−キトサン−乳糖複合体の組織化物
10に9をダイDより吐出した。この組織化物は31.
0%の水分を含み、pl−1は5.5であった。
Example 2 9 in 5 parts of casein soda and 9 in 2 parts of lactose were placed in food cutter A, and 9 was dispersed in 5% chitosan-lactic acid aqueous solution. This dispersion was placed in a barrel heated to 110°C for 150°C.
The feed rate was 9/min. Screw rotation 300
9 was discharged from die D onto the uniformly expanded milk protein-chitosan-lactose complex structure 10 at an outlet temperature of 100 to 105° C. while operating at rpm. This organized material is 31.
It contained 0% water and had a pl-1 of 5.5.

該組織化物を棚式乾燥法により50℃にて乾燥した後場
もどし試験を行うと、第3図に示す如く、15分間の加
熱で十分湯もどりすることが判明した。また、実施例1
と同じ条件で溶出試験を行うと、乳蛋白質溶出率は4.
6%であった。
When the structured product was dried at 50° C. using a shelf drying method and then subjected to a reconstitution test, it was found that heating for 15 minutes was sufficient to reconstitute the product, as shown in FIG. In addition, Example 1
When performing a dissolution test under the same conditions as above, the milk protein dissolution rate was 4.
It was 6%.

実施例3 カゼインソーダ5に9および5%キトサン−乳酸水溶液
5に9をフードカッターAに入れ、ラード2に9を分散
させた。この分散物を110℃に加熱したバレルに15
09/分の供給速度で供給した。。
Example 3 Casein soda 5 and 9 and 5% chitosan-lactic acid aqueous solution 5 and 9 were placed in food cutter A, and 9 was dispersed in lard 2. This dispersion was placed in a barrel heated to 110°C for 15 minutes.
The feed rate was 0.09/min. .

スクリュー回転300 rpmで運転し、組織化物11
に9を得た。
The screw rotation was operated at 300 rpm, and the textured material 11
I got a 9.

この組織化物を走査型電子顕微鏡で観察すると、第4図
に示す如く、1〜100μの分散した油滴が見られた。
When this structured product was observed with a scanning electron microscope, dispersed oil droplets of 1 to 100 μm in size were observed as shown in FIG.

第4図は;走査型電子顕微鏡による840倍拡大の、本
発明の製法による乳蛋白質複合体0組織構造を示す一耐
°代わる写真である・実施例4 カゼインソーダ5に9および5%キトサン−乳酸水溶液
2に9をフードカッターAに入れ、牛肉ミンチ7kgを
加え、撹拌・混合した。この混合物をフィーダーBより
100℃に加熱したバレルに1309/分の供給速度で
供給した。スクリュー回転250 rpmにて運転し、
配向性のある組織化物13に9を得た。
FIG. 4 is a photograph taken with a scanning electron microscope magnified 840 times and showing the structure of the milk protein complex produced by the production method of the present invention. Example 4 Casein soda 5 with 9 and 5% chitosan. 9 was put into lactic acid aqueous solution 2 in food cutter A, 7 kg of minced beef was added, and the mixture was stirred and mixed. This mixture was fed from feeder B to a barrel heated to 100° C. at a feed rate of 1309/min. Operating the screw at 250 rpm,
9 was obtained for oriented textured material 13.

この組織化物は95℃の湯中で5分間加熱しても組織の
分散はなく、十分な耐熱性を有するものと認められた。
Even when this structured product was heated in hot water at 95° C. for 5 minutes, the structure did not disperse, and it was recognized that it had sufficient heat resistance.

実施例5 カゼイン5に9および炭酸ソーダ132gの割合の粉末
原料を809/分の供給速度でフィーダーBから、同時
に5%キトサン・乳酸水溶液5に9の液状原料を809
/分の供給速度でフィーダーEから110℃に加熱した
バレルCに供給した。スクリュー回転300rp−で運
転し、乳蛋白質−キトサン複合体8klをダイDより吐
出した。
Example 5 Powder raw materials in a ratio of 9 to 5 casein and 132 g of soda carbonate were fed from feeder B at a feed rate of 809/min, and at the same time, a liquid raw material of 5 to 9 in a 5% chitosan/lactic acid aqueous solution was fed at a rate of 809/min.
The mixture was fed from feeder E to barrel C heated to 110°C at a feed rate of 1/min. The screw was operated at 300 rpm, and 8 kl of the milk protein-chitosan complex was discharged from die D.

得られた複合体は透明なソフトなゲル状のプラスチック
組織を有する組織化物であって、43jO%の水分を含
み、pHは5.5であった。該組織化物をpH6、8の
0.02Mリン酸緩衝液中、95℃にて5分間加熱した
場合の乳蛋白質溶出率は6.5%であった。
The obtained composite was a structured material having a transparent soft gel-like plastic structure, contained 43JO% water, and had a pH of 5.5. When the structured product was heated at 95° C. for 5 minutes in 0.02M phosphate buffer at pH 6 and 8, the milk protein elution rate was 6.5%.

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

第1図はエクストルーダを用いる本発明の製法における
フロー・シートである。 第2図は第3成分として種々の蛋白質を加えた場合の乳
蛋白質複合体において、第3成分添加濃度と乳蛋白質複
合体ゲル強度との関係を示すグラフである。 第3図は実施例2で得られた乳蛋白質複合体において、
加熱時間とゲル強度との関係を示すグラフである。 第4図は走査型電子顕微鏡による840倍拡大の、本発
明の製法による乳蛋白質複合体の組織構造を示す図面に
代わる写真である。 特許出願人南日本酪農協同株式会社 代 理 人 弁理士 青 山  葆 はが2名第1図 第2図 冥季i長by何トカロA吟 (5ら) 第3図 ηD熱時間(ケ) 第4図
FIG. 1 is a flow sheet of the manufacturing method of the present invention using an extruder. FIG. 2 is a graph showing the relationship between the concentration of the third component added and the gel strength of the milk protein complex in milk protein complexes in which various proteins are added as the third component. Figure 3 shows the milk protein complex obtained in Example 2.
It is a graph showing the relationship between heating time and gel strength. FIG. 4 is a photograph taken with a scanning electron microscope, magnified 840 times, in place of a drawing, showing the tissue structure of the milk protein complex produced by the production method of the present invention. Patent applicant Minami Nippon Dairy Kyodo Co., Ltd. Agent Patent attorney Haga Aoyama 2 people Figure 1 Figure 2 Meiji I length by He Tokaro Agin (5 et al.) Figure 3 ηD heat time (ke) No. Figure 4

Claims (5)

【特許請求の範囲】[Claims] (1)エクストルーダ加工法を用いて、乳蛋白質と乳蛋
白質に対し0.5〜7重量%のキトサンとより成る乳蛋
白質複合体であって水分30〜90%を含む固形物また
は懸濁物の状態でpH5.0〜7.5を示す乳蛋白質複
合体を得ることを特徴とする乳蛋白質複合体の製法。
(1) Using the extruder processing method, a milk protein complex consisting of milk protein and 0.5 to 7% by weight of chitosan based on the milk protein, and a solid or suspension containing 30 to 90% water, is produced. A method for producing a milk protein complex, characterized by obtaining a milk protein complex exhibiting a pH of 5.0 to 7.5.
(2)エクストルーダ加工法を用いて、乳蛋白質と乳蛋
白質に対し0.5〜7重量%のキトサンと乳蛋白質に対
し20〜100重量%の糖類とより成る乳蛋白質複合体
であって水分30〜90%を含む固形物または懸濁物の
状態でpH5.0〜7.5を示す乳蛋白質複合体を得る
ことを特徴とする乳蛋白質複合体の製法。
(2) Using an extruder processing method, a milk protein complex consisting of milk protein, 0.5 to 7% by weight of chitosan based on the milk protein, and saccharides of 20 to 100% by weight based on the milk protein, with a moisture content of 30% A method for producing a milk protein complex, characterized in that the milk protein complex exhibiting a pH of 5.0 to 7.5 is obtained in the form of a solid or suspension containing ~90%.
(3)エクストルーダ加工法を用いて、乳蛋白質と乳蛋
白質に対し0.5〜7重量%のキトサンと乳蛋白質に対
し40重量%以下の油脂とより成る乳蛋白質複合体であ
って水分30〜90%を含む固形物または懸濁物の状態
でpH5.0〜7.5を示す乳蛋白質複合体を得ること
を特徴とする乳蛋白質複合体の製法。
(3) Using an extruder processing method, a milk protein complex consisting of milk protein, chitosan of 0.5 to 7% by weight based on the milk protein, and oil and fat of 40% by weight or less based on the milk protein, and a moisture content of 30 to 30% 1. A method for producing a milk protein complex, which comprises obtaining a milk protein complex exhibiting a pH of 5.0 to 7.5 in the form of a solid or suspension containing 90%.
(4)エクストルーダ加工法を用いて、乳蛋白質と乳蛋
白質に対し0.5〜7重量%のキトサンと乳蛋白質に対
し10〜40重量%の乳蛋白質以外の蛋白質とより成る
乳蛋白質複合体であって水分30〜90%を含む固形物
または懸濁物の状態でpH5.0〜7.5を示す乳蛋白
質複合体を得ることを特徴とする乳蛋白質複合体の製法
(4) Using an extruder processing method, a milk protein complex consisting of milk protein, 0.5 to 7% by weight of chitosan based on the milk protein, and 10 to 40% by weight of proteins other than milk protein based on the milk protein is produced. 1. A method for producing a milk protein complex, which comprises obtaining a milk protein complex exhibiting a pH of 5.0 to 7.5 in the form of a solid or suspension containing 30 to 90% water.
(5)エクストルーダ加工法を用いて、乳蛋白質と乳蛋
白質に対し0.5〜7重量%のキトサンと乳蛋白質に対
し100〜250重量%の生肉もしくは加工肉またはそ
れらの混合物とより成る乳蛋白質複合体であって水分3
0〜90%を含む固形物または懸濁物の状態でpH5.
0〜7.5を示す乳蛋白質複合体を得ることを特徴とす
る乳蛋白質複合体の製法。
(5) Using an extruder processing method, milk protein is made of milk protein, chitosan in an amount of 0.5 to 7% by weight based on the milk protein, and raw meat or processed meat or a mixture thereof in an amount of 100 to 250% by weight based on the milk protein. complex and water 3
pH 5.0 in solid form or suspension containing 0-90%.
1. A method for producing a milk protein complex, characterized by obtaining a milk protein complex exhibiting a pH of 0 to 7.5.
JP62122728A 1987-05-20 1987-05-20 Milk protein complex manufacturing method Expired - Lifetime JPH0648955B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62122728A JPH0648955B2 (en) 1987-05-20 1987-05-20 Milk protein complex manufacturing method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62122728A JPH0648955B2 (en) 1987-05-20 1987-05-20 Milk protein complex manufacturing method

Publications (2)

Publication Number Publication Date
JPS63287447A true JPS63287447A (en) 1988-11-24
JPH0648955B2 JPH0648955B2 (en) 1994-06-29

Family

ID=14843116

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62122728A Expired - Lifetime JPH0648955B2 (en) 1987-05-20 1987-05-20 Milk protein complex manufacturing method

Country Status (1)

Country Link
JP (1) JPH0648955B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH05255596A (en) * 1991-06-07 1993-10-05 Snow Brand Milk Prod Co Ltd Spongy gel and its production
WO1998037775A2 (en) * 1997-02-28 1998-09-03 Societe Des Produits Nestle S.A. Gelled emulsion products containing chitosan

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH05255596A (en) * 1991-06-07 1993-10-05 Snow Brand Milk Prod Co Ltd Spongy gel and its production
WO1998037775A2 (en) * 1997-02-28 1998-09-03 Societe Des Produits Nestle S.A. Gelled emulsion products containing chitosan
WO1998037775A3 (en) * 1997-02-28 1998-12-10 Nestle Sa Gelled emulsion products containing chitosan
US6238720B1 (en) 1997-02-28 2001-05-29 Nestec S.A. Gelled emulsion products containing chitosan
AU740568B2 (en) * 1997-02-28 2001-11-08 Societe Des Produits Nestle S.A. Gelled emulsion products containing chitosan
EP1295532A3 (en) * 1997-02-28 2003-06-18 Société des Produits Nestlé S.A. Gelled emulsion products containing chitosan

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Publication number Publication date
JPH0648955B2 (en) 1994-06-29

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