JPH04141069A - Fibrous formed texture material of fish and shellfish - Google Patents

Fibrous formed texture material of fish and shellfish

Info

Publication number
JPH04141069A
JPH04141069A JP2265579A JP26557990A JPH04141069A JP H04141069 A JPH04141069 A JP H04141069A JP 2265579 A JP2265579 A JP 2265579A JP 26557990 A JP26557990 A JP 26557990A JP H04141069 A JPH04141069 A JP H04141069A
Authority
JP
Japan
Prior art keywords
raw material
fish
low
seafood
twin
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
JP2265579A
Other languages
Japanese (ja)
Other versions
JPH0646929B2 (en
Inventor
Toshikatsu Takahashi
高橋 敏勝
Isamu Sasaki
勇 佐々木
Kazuto Majima
真島 和登
Masahiko Terajima
寺嶋 正彦
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.)
Nissui Corp
Fuji Oil Co Ltd (fka Fuji Oil Holdings Inc)
Original Assignee
Fuji Oil Co Ltd
Nippon Suisan Kaisha 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 Fuji Oil Co Ltd, Nippon Suisan Kaisha Ltd filed Critical Fuji Oil Co Ltd
Priority to JP2265579A priority Critical patent/JPH0646929B2/en
Publication of JPH04141069A publication Critical patent/JPH04141069A/en
Publication of JPH0646929B2 publication Critical patent/JPH0646929B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

PURPOSE:To obtain the title product having good flavor and soft texture of feeling of fiber free from change of color such as browning and a smell by forming a kneaded meat raw material of fish and shellfish containing a low- saccharide vegetable protein by a twin-screw extruder and making into a fibrous state. CONSTITUTION:A kneaded meat raw material of fish and shellfish containing a low-saccharide vegetable protein is formed by a twin-screw extruder and made into a fibrous state to give the objective product. A low-saccharide vegetable protein having >=0.4wt.% low saccharide content is preferable as the low- saccharide vegetable protein component and the amount thereof in the kneaded meat raw material of fish and shellfish is preferably 0.5-20wt.%.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は魚介類の繊維状成型組織化物に係り、詳しくは
、低糖植物蛋白質を含む魚介類練り肉原料を2軸エクス
トルーダにより成形して得られるIll状状組織化物が
色調、フレーバー等に優れた魚介類のliW状成型成型
組織化物る。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a fibrous molded tissue of fish and shellfish, and more specifically, to a fibrous tissue obtained by molding a fish paste raw material containing low-sugar plant protein using a twin-screw extruder. The textured product is a LIW-shaped molded textured product of seafood that has excellent color tone, flavor, etc.

従  来  の  技  術 従来から、魚介類のすり身や落し身などの魚介類練り肉
を原料として製造された練り製品のうちで、カマボコ、
竹輪若しくは魚肉ソーセージ等が知られ、これら練り製
品が最も多く市販され食用に供されている。これら練り
製品は魚介類の可食部に食塩のほかに適当な添加物や調
味料を添加して混練痛潰して、所謂すり身などの練り肉
を形成し、この練り肉を成型加熱して弾力性のある組織
に形成したものである。しかし、最近、生活の洋風化、
多様化に伴って食品の嗜好が変化し、この変化に対応す
べく、カマボコ、竹輪若しくは魚介類ソーセージ等の魚
介類練り製品も改善されているが、必ずしも、本質的改
善ははかられていない。更に、w唐土の要請から、なる
べく塩分が少ないか、あるいは、塩分を含まないことが
要求されるのにも拘らず、魚介類可食部から練り肉をつ
くるときに、どうしても比較的多量の食塩を添加しであ
る程度の粘着性を持たせなければならず、健康上ではこ
の点が好ましくない。
Conventional technology Traditionally, fish paste products, such as kamaboko,
Chikuwa or fish sausages are known, and these paste products are the most commercially available and edible products. These paste products are made by adding appropriate additives and seasonings in addition to salt to the edible parts of seafood, kneading and crushing them to form paste such as surimi, and molding and heating this paste to make it elastic. It was formed by a certain organization. However, recently, the westernization of life,
Food preferences are changing with diversification, and in order to respond to these changes, seafood paste products such as kamaboko, chikuwa, and seafood sausage have been improved, but essential improvements have not always been made. Furthermore, despite the demands of Karado that it should contain as little or no salt as possible, when making paste from edible parts of seafood, it is inevitable to use a relatively large amount of salt. must be added to give it a certain degree of stickiness, which is not desirable from a health standpoint.

例えば、特公昭64−27号公報ならびに特R[62−
259565号公報には、魚介類すり身を原料とし、こ
れに食塩のほかに添加物、調味料を添加して混5trv
tし、この練り肉を帯状に成型してから加熱してすわら
せ、−旦所謂カマボコの如き練り製品をつくってから、
この製品を更に例えばナイフなどで切断して多数の細長
いフィラメントを形成し、その後、これらフィラメント
を所望に応じてバインダを添加して一体化し、ホタテ貝
柱もどき食品や、たらばかに足間もどき食品を製造する
方法が記載されている。しかしながら、これら食品は、
通常のカマボコ組織の練り製品を機械的に切断して、か
に足間などに近いIIN状組織組織成するため、天然の
ホタテ貝柱やたらばかに足間と区別できないほど近似し
ている外観は得られるが、各フィラメントは細く小径に
構成されていても、フィラメントそのものは蛋白質が立
体的に網状に結合した網状構造、つまり、所謂カマボコ
組織がそのまま残り、組織の上では天然のホタテ貝柱や
たらばかに足間とは本質的に異なるものであり、更に、
カマポコ組織の練り製品中には多口の塩分を含むため、
健康上からも好ましくない。
For example, Japanese Patent Publication No. 64-27 and Special Publication No. R [62-
Publication No. 259565 discloses that minced seafood is used as a raw material, and additives and seasonings are added to it in addition to salt.
Then, this paste is formed into a belt shape, heated and cooled, and a paste product like so-called kamaboko is made.
This product is further cut, for example, with a knife, to form a large number of long and thin filaments, and then these filaments are integrated by adding a binder as desired to produce foods that resemble scallops or foods that resemble kingfish. A method of manufacturing is described. However, these foods
By mechanically cutting a regular kamaboko tissue paste product to form an IIN-like tissue similar to that of a crab's legs, an appearance that is indistinguishably similar to that of a natural scallop or a crab's legs can be obtained. However, even though each filament is thin and has a small diameter, the filament itself has a network structure in which proteins are connected in a three-dimensional network, that is, a so-called cylindrical structure. It is essentially different from between, and furthermore,
Kamapoko tissue paste products contain a large amount of salt,
It's not good from a health standpoint.

これに対し、練り製品の組織自体をかに足間や、えび肉
組織に近づ(ブるために、蛋白質を直線状に配向した魚
介類練り製品、つまり、直線方向性繊維状練り製品の製
造方法が特開昭6368059号公報や特開昭63−6
8060号公報に提案されている。これら方法は、従来
からパン生地の混線製造過程に2軸エクストルダが適用
されていることを利用して開発されたもので、すり身等
の魚介類原料に添加物や調味料を添加して混練したゾル
化状態のものを加熱又は高粘度に調整してゲル化したも
のを2軸エクストルーダ中で混線、加熱、溶融し、この
加熱溶融物を2軸エクストルーダのせん所作用を利用し
て直線方向に蛋白質分子を配向させて押出し、その後、
これを水中で解繊後、食塩を含む魚介類すり身を添加混
合してから、所望形状に成型し、これをすわらせてから
蒸煮又は加熱するものである。このように得られた練り
肉製品は、従前のカマボコ組織とは相違し、蛋白質分子
が一つの方向に配向された線状のフィラメントを無差別
に結合して一体化した組織から成るもので、この組織は
えび肉やかに足間の組織に近似し、洋風化、多様化の目
的にある程度適合する。しかしながら、これら方法は、
2軸エクストルーダで混線処理してパン生地、つまり、
ドウを製造することをそのまま利用して、パン生地の代
りに魚介類原料を2軸エクストルーダで混練処理して、
方向性を持ったフィラメントを形成するが、これを解繊
して方向性なく無差別に結合する。すなわち、これら方
法で2軸エクストルーダで魚介類原料を処理するには、
この原料の特性をパン生地に近づけるために、予め、加
熱したり、澱粉、塩分などを添加して高粘度に調整して
いる。しかしながら、塩分などを含まないものが要請さ
れるのにも拘らず、塩分を添加しないとパン生地のよう
な粘着性が生じないため、これを対象とするものが製造
できない。また、高粘度の原料であるため、従来例の構
造の2軸エクストルーダがそのまま使用できるが、蛋白
質分子の配向性が損なわれ、配向性が不完全な組織のも
の、つまり、製品化できないものしか製造できない。こ
のために、2軸エクストルーダでの処理後、更に、水中
で攪拌解繊し、この解繊物にバインダとして塩分を含む
すり身を添加し混練成型してから、蒸成又は蒸煮して練
り製品を製造している。従って、これらの方法では、2
軸エクストルーダ処理後に仕上処理が8要であり、この
ため、製造工程が煩雑となり、仕上処理の際に、やや不
完全であるが配向された組織をわざわざ解繊し、この解
繊物を混線してから成型するため、蛋白質分子が結合し
たフィラメントが直線状に一つの方向に配向された製品
が得られない。
On the other hand, in order to make the structure of the paste product closer to the structure between crab legs or shrimp meat, there is a method for manufacturing seafood paste products in which proteins are oriented in a linear manner, that is, a linearly oriented fibrous paste product. JP-A-6368059 and JP-A-63-6
This is proposed in Japanese Patent No. 8060. These methods were developed by taking advantage of the fact that a twin-screw extruder has traditionally been applied to the mixed wire manufacturing process of bread dough. The gelatinized product is heated or adjusted to a high viscosity and then mixed, heated, and melted in a twin-screw extruder, and this heated melt is used to extrude proteins in a straight direction using the thrust action of the twin-screw extruder. The molecules are oriented and extruded, then
This is defibrated in water, mixed with salt-containing ground seafood, molded into a desired shape, allowed to sit, and then steamed or heated. The paste product obtained in this way is different from the conventional kamaboko structure, and consists of a structure in which linear filaments in which protein molecules are oriented in one direction are indiscriminately bonded and integrated. This tissue closely resembles the tissue between the legs of a shrimp, and is suitable to some extent for the purpose of Westernization and diversification. However, these methods
Bread dough is processed using a two-axis extruder, that is,
Utilizing the process of manufacturing dough, instead of bread dough, seafood ingredients are kneaded using a twin-screw extruder.
It forms directional filaments, which are then unraveled and bonded indiscriminately without any direction. In other words, in order to process seafood raw materials with a twin-screw extruder using these methods,
In order to bring the properties of this raw material closer to those of bread dough, it is heated or added with starch, salt, etc. to make it highly viscous. However, although there is a demand for products that do not contain salt, products that do not contain salt cannot be produced because they do not become sticky like bread dough. In addition, since the raw material is highly viscous, a biaxial extruder with a conventional structure can be used as is, but the orientation of the protein molecules is impaired, and only those with incomplete orientation can be used as products. Cannot be manufactured. For this purpose, after processing with a twin-screw extruder, it is further stirred and defibrated in water, and the defibrated product is added with salt-containing surimi as a binder, kneaded and molded, and then steamed or steamed to produce a paste product. are doing. Therefore, in these methods, 2
Eight finishing treatments are required after the shaft extruder treatment, which makes the manufacturing process complicated.During the finishing treatment, the slightly imperfectly oriented structure is defibrated, and this defibrated material is mixed with wires. Because the process is then molded, it is not possible to obtain a product in which the filaments to which protein molecules are bonded are linearly oriented in one direction.

更に詳しく説明すると、例えば、パンドウの如く、パン
生地その他の小麦粉を主成分とする生地の製造用として
使用されている従来例の工クストルーダは主として円筒
状バレルとその内部で回転するスクリュウ軸とから成っ
ている。
To explain in more detail, a conventional dough truder, which is used for manufacturing bread dough or other flour-based dough such as bread dough, mainly consists of a cylindrical barrel and a screw shaft that rotates inside the barrel. ing.

このスクリュウ軸上にはスクリ]つが設けられ、このス
クリュウの作用によって主として小麦粉から成る原料が
搬送され、この間に各成分が混練されて所謂トウが形成
される。円筒状バレル内の原料は加熱することができ、
この加熱は、通常、円筒状バレル自体を蒸気又は電気ヒ
ータによって加熱したり、原料中に蒸気などを注入混合
して行なわれる。円筒状バしルの先端は絞られてノズル
又はオリフィスが形成され、このように先端が絞られて
いるため、原料がスクリュウ羽根によって搬送される間
に、原料は加圧され圧力が上社する。エクストルーダと
しては、円筒状バレル内に1つのスクリュウ軸を回転自
在に収納した型式、つまり、1軸エクストルーダが用い
られていたが、近年、1軸エクストルーダに比べて高い
原料搬送能力を持っている2軸エクストルーダが用いら
れるようになっている。この2軸エクストルーダは原料
特性ならびに加工処理目的に応じてスクリュウ軸の組換
ができ、鳥油脂分の多い原料も処理できることから、パ
ン生地、つまり、パンドウの製造用として用いられてい
る。
A screw is provided on the shaft of the screw, and the action of this screw transports the raw material mainly consisting of wheat flour, during which time the ingredients are kneaded to form a so-called tow. The raw material inside the cylindrical barrel can be heated,
This heating is usually carried out by heating the cylindrical barrel itself with steam or an electric heater, or by injecting and mixing steam into the raw materials. The tip of the cylindrical bulb is constricted to form a nozzle or orifice, and because the tip is constricted in this way, the raw material is pressurized and the pressure increases while it is being conveyed by the screw blade. . As an extruder, a type in which one screw shaft is rotatably housed in a cylindrical barrel, that is, a single-screw extruder, was used, but in recent years, extruders have been used that have a higher raw material conveyance capacity than single-screw extruders2. Axial extruders are now used. This twin-screw extruder is used for manufacturing bread dough, that is, bread dough, because the screw shaft can be rearranged depending on the characteristics of the raw material and the purpose of processing, and it can also process raw materials with a high content of bird fat.

この同方向回転型2軸■クストルーダの代表例の一部を
示すと、第7図の通りであって、円筒状バレル1内には
2つのスクリュウ軸2.3が互いに同方向に回転するよ
う配置されている。
A typical example of this co-rotating two-screw screwtruder is shown in Fig. 7, in which two screw shafts 2.3 are arranged inside the cylindrical barrel 1 so as to rotate in the same direction. It is located.

これらスクリュウ軸2.3のスクリュウ21.31はn
いにかみ合って回転し、各スクリュウ軸2.3の先端に
はフロックナツト22.32が設けられている。フロッ
クナツト22.32に近接してバレルダイ4が設けられ
、バレルダイ4の略々中心部にはオリフィス若しくはノ
ズル状の吐出口41が形成されている。円筒状バレル1
内において2つのスクリュウ軸2.3が同方向に回転し
、この回転によって原料が各スクリュウ21.31によ
って搬送される間に混練、圧縮されると共に、円筒状バ
レル1内の加熱素子(図示せず1と各スクリュウ21.
31による剪断の際の内部熱とによって加熱され、原I
N図示せす)はフロックナツト22.32とバレルダイ
4との間隙に入って、バレルダイ4の吐出口41から吐
出される。従って、バレルダイ4によって円筒状バレル
]の先端は絞られているため、原料は搬送の間に加圧さ
れ、この圧力は2軸エクストルーダであると、蒸気圧力
以上の高い圧力に高められるため、円筒状バレル1内で
は蒸気の、5=つとつや、スプラッシュが起こらない。
The screws 21.31 of these screw shafts 2.3 are n
A flocking nut 22.32 is provided at the tip of each screw shaft 2.3. A barrel die 4 is provided adjacent to the flock nut 22, 32, and an orifice or nozzle-shaped discharge port 41 is formed approximately at the center of the barrel die 4. Cylindrical barrel 1
The two screw shafts 2.3 rotate in the same direction within the barrel 1, and this rotation kneads and compresses the raw material while being conveyed by each screw 21.31, as well as heating elements (not shown) in the cylindrical barrel 1. 1 and each screw 21.
31 and the internal heat during shearing, the original I
N (not shown) enters the gap between the flock nut 22, 32 and the barrel die 4 and is discharged from the discharge port 41 of the barrel die 4. Therefore, since the tip of the cylindrical barrel is squeezed by the barrel die 4, the raw material is pressurized during conveyance, and with a twin-shaft extruder, this pressure is increased to a pressure higher than the steam pressure, so the cylindrical barrel In the shaped barrel 1, no steam, 5=gloss, or splash occurs.

しかし、バレルダイ4の吐出口41から大気中に原料が
押出されると、原料が膨化・し、高圧蒸気が発生するた
め、原料が飛び散り、細かい細片状になり易い、つまり
、フラッシュ現象が発生し、製品の成形性が損なわれ、
とくに、高粘度で湿分の少ない原料であると、この傾向
は助長され、配向性が損なわれて整った繊状構造のもの
が得られない。
However, when the raw material is extruded into the atmosphere from the discharge port 41 of the barrel die 4, the raw material expands and generates high-pressure steam, so the raw material tends to scatter and become fine pieces, that is, a flash phenomenon occurs. However, the moldability of the product is impaired,
In particular, if the raw material has high viscosity and low moisture content, this tendency will be exacerbated, and the orientation will be impaired, making it impossible to obtain a well-ordered fibrous structure.

この現象をさけるために、バレルダイ4の吐出口41の
ところで冷部することも行なわれている。しかし、この
ように冷却してもフラッシュ現象は完全には回避できず
、かえって、吐出口41のところで局部的に冷却される
と、バレルダイ4の吐出口41で目詰りが発生して円筒
状バレル1内の圧力が変動し、時には爆発的に原料が吐
出しすることもあって、吐出量が制御することができな
いほか、所望形状に成型できない。
In order to avoid this phenomenon, cooling is also performed at the discharge port 41 of the barrel die 4. However, even with such cooling, the flash phenomenon cannot be completely avoided.On the contrary, if the discharge port 41 is locally cooled, the discharge port 41 of the barrel die 4 will become clogged, causing the cylindrical barrel to become clogged. The pressure inside the mold fluctuates, and sometimes the raw material is discharged explosively, making it impossible to control the discharge amount and making it impossible to mold it into a desired shape.

また、フラッシュ現象の回避のために、魚介類原料を処
理する場合に、円筒状バレルの先端に長い管状のノズル
を連結し、このノズルの前半では原料を溶融状態に保持
するのに反し、ノズルの後半では100℃以下まで冷却
して、組織の繊状化を達成する方法が、米国特許第4、
816278号公報に記載されている。しかし、この長
いノズルによって一部フラッシュ現象は回避できるが、
冷却ゾーンが良いノズルの半分であって短かく、直線状
の配向性を持たすのには不十分である。長いノズルは前
半の加熱又は溶融ゾーンと後半の冷却ゾーンとを加える
と、良さは長くなり、その接触抵抗が太きくなることも
あって、2軸エクストルーダの押出力のみによっては長
いノズル内に原料を連続かつ安定して送ることができな
い。
In addition, in order to avoid the flash phenomenon, when processing seafood raw materials, a long tubular nozzle is connected to the tip of the cylindrical barrel. In the latter half of the process, a method of cooling the tissue to below 100°C to achieve fibrillation of the tissue is disclosed in U.S. Patent No. 4,
It is described in No. 816278. However, although this long nozzle can partially avoid the flash phenomenon,
The cooling zone is half as short as a good nozzle and is insufficient to provide linear orientation. When a long nozzle has a heating or melting zone in the first half and a cooling zone in the second half, the quality becomes longer and the contact resistance becomes thicker. cannot be sent continuously and stably.

そこで、円筒状バレルの吐出口の先端と長いノズルとの
間にポンプを設けたところ、2軸エクストルーダのバレ
ル1から長いノズル内に原料を連続かつ安定して送るこ
とが可能である口とがわかった。
Therefore, when a pump was installed between the tip of the discharge port of the cylindrical barrel and the long nozzle, it was possible to continuously and stably feed the raw material from the barrel 1 of the twin-shaft extruder into the long nozzle. Understood.

しかしながら、上記の2軸エクストルーダにより^湯処
理し、魚介類原料を繊維状成形組織化物とする際には各
種の添加物を添加することが行なわれているが、その添
加物の種類によっては食品として好ましくない問題を生
ずる。例えば、澱粉では食感、乾燥卵白では臭気、高糖
大豆蛋白質では着色等に問題があり、口れらの特性をバ
ランスよ(保持した良好な繊維状の成型組織化物の出現
が要望されている。
However, various additives are added when processing fish and shellfish raw materials into fibrous structured materials by hot water treatment using the above-mentioned twin-screw extruder. This may cause undesirable problems. For example, starch has problems with texture, dried egg whites have problems with odor, and high-sugar soybean proteins have problems with coloring, etc., and it is desired to create a well-balanced fibrous textured structure that maintains the properties of the palate. .

発明が解決しようとする課題 本発明は上記問題解決を目的とし、具体的には、引張強
度、色調、フレーバー、食感等が良好で、しかも、各種
物性がバランスより保持した魚介類の繊維状成形組織化
物を提案することを目的とする。
Problems to be Solved by the Invention The purpose of the present invention is to solve the above-mentioned problems. Specifically, the present invention aims to provide a fibrous fish and shellfish material that has good tensile strength, color tone, flavor, texture, etc., and also maintains a good balance of various physical properties. The purpose of this paper is to propose a molded structure.

課題を解決するための 手段ならびにその作用 すなわら、本発明は、低糖植物蛋白質を含む魚介類練り
肉原料を2軸エクストルーダにより成形し、IIN状と
したものから成ることを特徴とする。
As a means for solving the problem and its function, the present invention is characterized in that it consists of a raw material for fish and shellfish paste containing low-sugar plant protein that is molded using a twin-screw extruder to form an IIN shape.

以下、本発明の手段たる構成ならびにその作用について
説明すると、次の通りである。
Hereinafter, the configuration and operation of the means of the present invention will be explained as follows.

本発明者等は添加物を含む魚介類の練り肉原料を2軸エ
クストルーダによりIll状の成形組織化物とする際に
、200℃前後の高温に加熱処理すると添加物が熱分解
し悪臭が発生し、組織化物が着色したりまたは硬いもの
となり食感を害するため、これを防止する方法について
検討を行なったところ、低糖植物蛋白を含む魚介類練り
肉原料を用いればよいということがわかった。
The present inventors have discovered that when making fish and shellfish paste raw materials containing additives into an Ill-shaped textured product using a twin-screw extruder, if the additives were heat-treated to a high temperature of around 200°C, the additives would thermally decompose and produce a bad odor. The textured product becomes colored or hard, which impairs the texture, so we investigated ways to prevent this and found that it would be best to use a seafood paste material containing low-sugar plant protein.

そこで、更に進んで研究開発を行ない、この研究に基づ
いて本発明は成立したものである。
Therefore, we conducted further research and development, and the present invention was established based on this research.

本発明に用いられる魚介類練り肉原料として用いられる
魚介類の種類としては、例えばスケソーダラ、ホキ、イ
トヨリ等の白身魚類、イワシ、サバ、アジ等の赤身魚類
、イカ、タコ等の軟体類、エビ、カニ等の甲殻類等があ
げられ、これらの中色調の点から白身間の魚介類が好適
である。
Examples of the types of seafood used as raw materials for the seafood paste used in the present invention include white fish such as pollock cod, hoki, and stickleback; red fish such as sardines, mackerel, and horse mackerel; molluscs such as squid and octopus; and shrimp. , crustaceans such as crabs, etc., and fish and shellfish with white flesh are preferred from the viewpoint of medium color tone.

魚介類練り肉原料は例えば魚介類の可食部から採肉し、
水晒し脱水して脱水肉とし、これにソルビットならびに
リン酸塩を加えて無塩すり身としたもの若しくは脱水肉
に食塩を加えて嬬凄し加塩すり身としたもので生又は凍
結したものであれば良い。このすり身を単品若しくは数
種類を組合せて混練して使用する。
Raw materials for seafood paste include, for example, meat harvested from the edible parts of seafood,
If the meat is exposed to water and dehydrated to make dehydrated meat, then sorbitol and phosphate are added to it to make unsalted surimi, or if salted surimi is made by adding salt to the dehydrated meat, and it is raw or frozen. good. This surimi can be used singly or in combination.

この魚介類練り肉原料からII帷状状成形組織化物製造
するには、重量比で低糖植物蛋白を0.5〜20%を含
み、必要に応じて他の添加剤例えば澱粉0.5〜5%、
食塩O〜3%を含有させた魚介類練り肉原料を2軸■ク
ストルダにより混線、加熱、溶融、加圧、押出、冷却す
ることにより得られる。
In order to produce a textured tissue in the shape of II from this raw material for fish and shellfish paste, it contains 0.5 to 20% by weight of low sugar vegetable protein, and if necessary, other additives such as starch 0.5 to 5%. %,
It is obtained by mixing a raw material for seafood paste containing 0 to 3% of common salt in a two-screw xtruder, heating, melting, pressurizing, extruding, and cooling.

本発明に用いられる低糖植物蛋白質は乾燥重量で蛋白質
92.5%以上、少糖類成分0.4%以下を含み、残部
が灰分から成るものである。
The low-sugar plant protein used in the present invention contains 92.5% or more of protein, 0.4% or less of oligosaccharide components, and the remainder consists of ash.

この製造法の一例をあげると、脱脂大豆を水抽出し、水
不溶性画分と水溶性画分とに分離し、この水溶性画分を
等電点沈澱させ、水不溶性画分と水溶性画分に分離し、
口の水不溶性画分を温水により次層を1回若しくは2回
以上くり返し、中和する方法によって得られる。この具
体例としては不二製油株式会社製低糖植物蛋白質商品名
「ニューフジブロー5t−IJがある。
To give an example of this production method, defatted soybeans are extracted with water, separated into a water-insoluble fraction and a water-soluble fraction, and this water-soluble fraction is subjected to isoelectric point precipitation to separate the water-insoluble and water-soluble fractions. separated into minutes,
It is obtained by a method in which the water-insoluble fraction of the mouth is neutralized by repeating the next layer once or twice or more with warm water. A specific example of this is the low-sugar plant protein manufactured by Fuji Oil Co., Ltd. under the trade name "New Fuji Blow 5t-IJ."

本発明において、魚介類練り肉原料に低糖植物蛋白質を
重量比で0.5〜20%含有さゼる理由は、2軸エクス
トルーダにより加熱処理する際に繊維状の成形組織化物
の色調変化を防止するためであり、多量に糖類成分を含
む高糖植物蛋白質は高温で糖成分が熱分解し、白色度に
優れたものが轡られないからである。また、添加量が0
65%未満では十分な効果が得られず20%超えても色
調が更に向上することがないがらである。
In the present invention, the reason why the raw material for seafood paste contains 0.5 to 20% by weight of low-sugar plant protein is to prevent color change of the fibrous molded structure during heat treatment using a twin-screw extruder. This is because the sugar components of high-sugar plant proteins containing a large amount of sugar components are thermally decomposed at high temperatures, and those with excellent whiteness will not be washed away. Also, the amount added is 0
If it is less than 65%, a sufficient effect cannot be obtained, and if it exceeds 20%, the color tone will not be further improved.

また、上記以外の副原料の他に着色剤、可塑剤、糊剤、
油脂等通常成形組織化物に添加される凌加剤を用いるこ
とができる。
In addition to the above-mentioned auxiliary materials, we also use colorants, plasticizers, adhesives,
It is possible to use additives such as fats and oils that are usually added to molded textured products.

次に、これら魚介類の練り肉を2軸エクストルーダによ
り繊維状の成形組織化物とする方法について図面により
詳しく説明する。
Next, a method for forming the fish paste into a fibrous structured material using a twin-screw extruder will be described in detail with reference to the drawings.

第1図は本発明を実施する際に用いられる装置の一例を
示す縦断面図であり、第2図は本発明方法によって製造
された魚介類の繊維状成形組織化物の一例の斜視図であ
り、第3図は第2図の矢印A−八へ向から切断した縦断
面を示す断面図であり、第4図は第3図に示す繊維状角
fr類練り製品のうちのフィラメントを一つの方向に引
き裂いたときを示す説明図であり、第5図は本発明の他
の実施例に係る魚介類の繊維状成形組織化物の断面図で
あり、第6図は本発明を実PI!する際に用いられる装
置の一例を示す縦断面図であり、第7図は従来例に係る
2軸エクストルーダの一部を示す断面図である。
FIG. 1 is a longitudinal cross-sectional view showing an example of an apparatus used in carrying out the present invention, and FIG. 2 is a perspective view of an example of a fibrous molded tissue of seafood produced by the method of the present invention. , FIG. 3 is a cross-sectional view showing a longitudinal section taken in the direction of arrow A-8 in FIG. 2, and FIG. FIG. 5 is a cross-sectional view of a fibrous molded structure of fish and shellfish according to another embodiment of the present invention, and FIG. 6 is an explanatory diagram showing the present invention when it is torn into pieces. FIG. 7 is a longitudinal cross-sectional view showing an example of a device used in the extrusion process, and FIG. 7 is a cross-sectional view showing a part of a conventional biaxial extruder.

第1図に示す本発明を実施する際に用いられる装置にお
いては、先端に送りポンプ71を介して長い冷却ゾーン
8が接続される2軸エクストルーダ50後端に低糖大豆
蛋白を含む魚介類原料を投入し、この投入された魚介類
原料を2軸エクストルーダ5中で混線、加圧ならびに加
熱溶融した後に、この加熱溶融原料を冷却シン8中に押
出し、この冷Wゾーン8の全長にわたって冷却し、とく
に、2軸エクストルーダ5の先端で温度150〜260
℃に保つ一方、冷却ゾーン8内においては、その長さ方
向にわたり、0.05〜0.35℃ 1の温度勾配をつ
けて、加熱溶融原料を60〜110℃まで冷却する。こ
のため、上記魚介類原料を予め加熱又は蒸煮してグツし
化状態にしておくと、冷却ゾーン8において蛋白質など
の成分が中心軸と平行な直線方向に配向して各フィラメ
ントが形成され、これらフィラメントから成る第2図、
第3図ならびに第4図に示すI!緒状状成形組織化物得
られる。また、上記魚介類原料がゾル化したままで処理
すると、冷却ゾーンにおいては2軸エクストルーダ5の
先端の加熱条件ならびに冷却シン8の冷却条件を変える
と、タンパク質などの成分が斜め半径方向に指向してフ
ィラメントが形成され、これらフィラメントから成る第
5図に示す繊維状成形組織化物も得られる。上記の繊維
状成形組織化物は引張強度、食感、フレーバーならびに
色調が従来例のものに比べてバランスよく優れたもので
ある。
In the apparatus shown in FIG. 1 used to carry out the present invention, a seafood raw material containing low sugar soybean protein is placed at the rear end of a two-shaft extruder 50, to which a long cooling zone 8 is connected via a feed pump 71. After the input seafood raw material is cross-wired, pressurized, and heated and melted in the twin-screw extruder 5, the heated and molten raw material is extruded into the cooling sink 8 and cooled over the entire length of the cold W zone 8, In particular, the temperature at the tip of the two-shaft extruder 5 is 150 to 260.
While maintaining the heated molten raw material at a temperature of 60 to 110°C, a temperature gradient of 0.05 to 0.35°C is applied in the cooling zone 8 along its length. For this reason, if the above-mentioned seafood raw material is heated or steamed in advance to make it into a chewy state, components such as proteins are oriented in a straight line direction parallel to the central axis in the cooling zone 8 to form each filament. Figure 2, consisting of filaments;
I! shown in FIGS. 3 and 4! A cord-like molded structure is obtained. Furthermore, if the above-mentioned seafood raw materials are processed in a sol state, in the cooling zone, if the heating conditions of the tip of the twin-shaft extruder 5 and the cooling conditions of the cooling sink 8 are changed, components such as proteins will be oriented diagonally in the radial direction. Thus, filaments are formed, and a fibrous shaped structure made of these filaments as shown in FIG. 5 is also obtained. The above-mentioned fibrous molded structure has a well-balanced and excellent tensile strength, texture, flavor, and color tone compared to conventional products.

また、本発明を実施する際に用いられる他の装置として
第6図に示すように、同方向に回転する2本のスクリュ
ウ21.31を有し、このスクリュウ21.31によっ
て圧送される魚介類練り肉原料をRIll、加圧ならひ
に加熱溶融して先端から押出す2軸エクストルーダ5と
、口の2軸エクストルーダ5の先端に連結されて複数個
に分岐された分岐チューブ61.62と、これら各分岐
チューブ61.62の先端にそれぞれ連結されて2軸エ
クストルーダ5からの原料を加熱溶融状態のままで定量
的に送出す送給ポンプ71.72と、これら各送給ポン
プ71.72の吐出口に個別的に連結され、しかも、前
記各送給ポンプ71.72から連続的に送られてかつ加
熱溶融状態にある原料をその周囲から徐々に冷却する冷
却ゾーン8.9とを臭える。
In addition, as shown in FIG. 6, another device used in carrying out the present invention has two screws 21.31 that rotate in the same direction, and seafood is fed under pressure by these screws 21.31. A twin-screw extruder 5 that heats and melts the meat paste raw material under pressure and extrudes it from the tip, and a branch tube 61,62 that is connected to the tip of the two-screw extruder 5 and branched into a plurality of pieces. Feed pumps 71.72 are connected to the ends of each of these branch tubes 61.62 and quantitatively feed the raw material from the twin-shaft extruder 5 in a heated and molten state, and each of these feed pumps 71.72 Cooling zones 8.9 which are individually connected to the discharge ports and which are continuously fed from each of the feed pumps 71, 72 and which gradually cool the heated and molten raw material from its surroundings are provided. .

従って、魚介類原料の水分量、粘度にかかわらす、つま
り、ゲル化又はゾル化のいかんにかかわらず、魚介類原
料は定常的に一定量づつ断続することなく送ることがで
き、更に、送りポンプ71.72の回転数の調整によっ
て長い冷却ゾーン8.9の冷却条件を変化させて各フィ
ラメントを一つの方向に配向させたII雑状状成形組織
化物容易に得られ、この繊維状成形組織化物は前記した
ものと同様に各物性をバランスよく保持した優れたもの
である。
Therefore, regardless of the moisture content and viscosity of the seafood raw material, that is, regardless of whether it is gelled or sol-formed, the seafood raw material can be constantly fed in a fixed amount without interruption, and furthermore, the feed pump A II miscellaneous molded structure in which each filament is oriented in one direction is easily obtained by changing the cooling conditions of the long cooling zone 8.9 by adjusting the rotational speed of 71.72, and this fibrous molded structure is obtained. Similar to the above-mentioned materials, these are excellent materials that maintain a good balance of physical properties.

実施例1゜ スケソウタラの可食部を採取し、これを水晒し、脱水し
、これに重量比で6部のソルビットを加え、よく混練i
潰した後凍結した。この冷凍すり身を解凍した後、この
すり身に重量比で0.5部の食塩、1部の澱粉、3部の
低糖植物蛋白(不二製油製商品名「ニューフジブロー5
HJ)を加え、サイレントカッターでよく混練した。こ
の得られたゾル状物を出発原料として第6図に示す製造
装置において、その2軸エクストルーダに投入し、次の
条件で処理して、棒状の成型組織化物(径181IIl
内外)を得た。
Example 1 Collect the edible part of pollock cod, expose it to water, dehydrate it, add 6 parts by weight of sorbitol, and knead well.
It was crushed and then frozen. After thawing this frozen surimi, add 0.5 parts of salt, 1 part of starch, and 3 parts of low-sugar vegetable protein (product name: New Fuji Blow 5 manufactured by Fuji Oil Co., Ltd.) to this surimi by weight.
HJ) was added and thoroughly kneaded with a silent cutter. The obtained sol-like material was used as a starting material to be introduced into a twin-screw extruder in the manufacturing apparatus shown in FIG.
obtained (inside and outside).

2軸エクストルーダの原料供給量 50〜60kg h 2軸エクストルーダのスクリュウ軸回転数150〜20
Orpm 2軸エクストルーダの円筒状バレル温度(中間)   
  170℃ (先端の吐出口) 220℃ 冷却ゾーンの寸法、内径15閣X長さ1m×2基この際
、送給ポンプとしてのギヤーポンプの回転数を制御する
ことにより、原料の供給ならびに流れは安定し円滑な運
転ができた。口のとき原料は2軸■クストルーダで完全
に溶融混練し、各分岐チューブを通る間に加熱溶融物の
温度は170°Cまで低下し、冷却ゾーンでは95Cま
で冷却し、冷却時の温度勾配は0.255℃・lであっ
た。棒状の成型組織化物の表面には滑動性のある薄い表
面皮膜におおわれて、これの縦断面をみると、第3図に
示す通り、各フィラメントが中心軸と平行方向に整った
繊維状の組織になっていた。これを食べたところ、風味
、食感に優れ、これを第3図に示す通りに棒状成型組織
化物の一部をとって切り裂いたところ、フィラメントの
配ダ1方向に全長にわたって切り裂きができ、途中で切
れることはなかった。
2-screw extruder raw material supply amount 50-60 kg h 2-screw extruder screw shaft rotation speed 150-20
Orpm 2-screw extruder cylindrical barrel temperature (intermediate)
170℃ (discharge port at tip) 220℃ Cooling zone dimensions: inner diameter 15mm x length 1m x 2 units At this time, the supply and flow of raw materials are stabilized by controlling the rotation speed of the gear pump as a feed pump. I was able to drive smoothly. At the time of melting, the raw materials are completely melted and kneaded in a two-screw xtruder, and the temperature of the heated melt drops to 170°C while passing through each branch tube, and then cools to 95°C in the cooling zone, and the temperature gradient during cooling is It was 0.255°C·l. The surface of the rod-shaped molded structure is covered with a thin, sliding surface film, and when viewed in longitudinal section, as shown in Figure 3, it is a fibrous structure in which each filament is aligned parallel to the central axis. It had become. When I ate this, I found that it had excellent flavor and texture, and when I cut it into pieces as shown in Figure 3, I found that it was torn along the entire length in one direction of the filament distribution, and in the middle. It never broke.

得られた成型組織化物は褐変等の変色はなく、また、高
温加熱時に発生する特有の異臭も少なく、mmsのある
ソフトな食感を有し、優れた加工食品素材であった。
The obtained molded textured product had no discoloration such as browning, had little peculiar odor generated during high-temperature heating, had a soft texture with mms, and was an excellent processed food material.

実施例1と同様にして、低糖植物蛋白質の代りに澱粉、
乾燥卵白、高糖大豆蛋白を同配合量を添加した組織化物
を得た。かくして得られた組織化物について比較した結
果を第1表に示した。低糖大豆蛋白添加量は色、フレー
バー、食実施例2゜ スケソウタラの代りに魚介類のうちで、甲殻類に属する
オキアミ、軟体動物に属するイカの各可食部を上記の如
く水晒し、脱水、混線、温潤してすり身をつくり、これ
に実施例1と同様に食塩、澱粉、低糖植物蛋白を添加し
てゾル化し、ごれを加熱してゲル化してから、チョッパ
径2.0■を用いて粒状物にくだいた。
In the same manner as in Example 1, starch and
A textured product was obtained by adding dried egg white and high sugar soybean protein in the same amounts. Table 1 shows the results of a comparison of the structured products thus obtained. The amount of low-sugar soy protein added is determined by color, flavor, and food.Example 2゜In place of pollock cod, among seafood, krill, which belongs to crustaceans, and squid, which belongs to molluscs, are exposed to water as described above, dehydrated, Mix and heat to make surimi, add salt, starch, and low-sugar vegetable protein as in Example 1 to form a sol, heat the dirt to gel, and then use a chopper with a diameter of 2.0 mm. It was crushed into granules.

これを実施例1と同じ条件で第6図に示す製造装置で処
理したところ、第3図に示す成型組織化物が得られた。
When this was processed using the manufacturing apparatus shown in FIG. 6 under the same conditions as in Example 1, a molded structured product shown in FIG. 3 was obtained.

得られた繊維状成型組織化物は実施例1と全(変らず褐
変等の変色は殆んどなく優れた加工食品素材であった。
The obtained fibrous molded textured product was the same as Example 1, and was an excellent processed food material with almost no discoloration such as browning.

実施例3゜ イトヨリの可食部を採取し、この可食部を実施例1と同
様に水晒し、脱水し、これに重量比で5部のソルビット
と0.2部のりんI!Ij!を加えてから混練信潰して
すり身をつくり凍結した。この冷凍すり身を解凍した後
このすり身に重量比で0.5部のfi塩と1部の澱粉と
3部の低糖植物蛋白(実施例1と同じもの)を加え。
Example 3 The edible part of the Japanese stickleback was collected, and the edible part was exposed to water and dehydrated in the same manner as in Example 1, and to this was added 5 parts of sorbitol and 0.2 parts of phosphorus I! in a weight ratio. Ij! After adding , the mixture was kneaded and crushed to make surimi and frozen. After thawing the frozen surimi, 0.5 part of fi salt, 1 part of starch, and 3 parts of low-sugar vegetable protein (same as in Example 1) were added to the surimi by weight.

サイレントカッターでよく混練してゾル化した。このゾ
ル化物は水分が73重量%も含有するものであったが、
このゾル状物をそのまま第6図に示す製造装置の2軸エ
クストルーダに供給し、原料供給量35kg・′h、ス
クリュウ軸の回転数175rpm、円筒状のバレルの中
間温度170℃、先端のバレル吐出口の温度220℃の
条件で処理し冷却ゾーンにおいては温度勾配0.325
℃・′mで95℃まで冷却した。
The mixture was thoroughly kneaded with a silent cutter to form a sol. This sol contained 73% by weight of water, but
This sol-like material was fed as it was to the two-screw extruder of the manufacturing equipment shown in Fig. 6, with a raw material supply amount of 35 kg·'h, a rotation speed of the screw shaft of 175 rpm, an intermediate temperature of the cylindrical barrel of 170°C, and a barrel discharge at the tip. Processed under the condition of outlet temperature 220℃, temperature gradient 0.325 in cooling zone
The mixture was cooled to 95°C at ℃·'m.

この結果、第2図に示す如き、棒状成型組織化物が得ら
れ、この成型組織化物の表面には実施例1と同様に滑動
性のある薄い表面皮膜におおわれていたが、縦断面をみ
ると、第5図に示す各フィラメントが半径方向斜めに指
向した成型組織化物であった。この棒状成型組織化物に
おいて、一部をもって引き裂いたとごろ、フィラメント
の指向方向、つまり、斜めの半径方向にフィラメントが
引き裂かれた。得られた成型組織化物は褐変等の変色は
なく、また、異臭もなく繊維感のあるソフトな食感を有
する優れた加工食品素材であった。
As a result, a rod-shaped molded textured product was obtained as shown in FIG. 2, and the surface of this molded textured product was covered with a thin surface film with sliding properties as in Example 1, but when viewed in longitudinal section, , each filament shown in FIG. 5 was a molded structure in which the filaments were oriented obliquely in the radial direction. When this rod-shaped textured product was partially torn, the filaments were torn in the direction in which the filaments were oriented, that is, in the diagonal radial direction. The obtained molded textured product was an excellent processed food material with no discoloration such as browning, no off-odor, and a soft texture with a fibrous feel.

また、上記の通りに得られたすり身に食塩を添加するこ
となく3部の澱粉のみを添加混練してゾル化し、これを
上記のところと同様に処理したところ、同様な成型組織
化物が得られた。
In addition, when the surimi obtained as above was added with only 3 parts of starch without adding salt and kneaded to form a sol, and this was treated in the same manner as above, a similar shaped structured product was obtained. Ta.

実施例4゜ 脱皮されたいかをチョッパー挽きし、これに0.5部の
食塩、1部の1119j、3部の低糖植物蛋白(実施例
1と同じもの)を添加してゾル化したものと、食塩を添
加せずにゾル化したものとをつくり、これを実施例1と
同様にしてバレル中間温度165℃、先端のバレル吐出
口の温度200℃の条件で処理したところ、第5図に示
す成型組織化物が得られた。この成型組織化物も実施例
1と同様のものであった。
Example 4 Dehulled squid was ground using a chopper, and 0.5 parts of common salt, 1 part of 1119J, and 3 parts of low sugar vegetable protein (same as in Example 1) were added to form a sol. , and a sol without adding salt were prepared and treated in the same manner as in Example 1 under the conditions of a barrel intermediate temperature of 165°C and a barrel outlet temperature of 200°C, as shown in Fig. 5. The molded tissue shown in the figure was obtained. This molded textured product was also similar to Example 1.

〈発明の効果7) 以上詳しく説明した通り、本発明は、低糖植物蛋白質を
含む魚介類練り肉原料を2軸エクストルーダにより成形
し、繊維状としたものから成ることを特徴とする。
<Effect 7 of the Invention> As explained in detail above, the present invention is characterized by forming a raw material for fish and shellfish paste containing low-sugar plant protein into a fibrous form using a twin-screw extruder.

従って、am!l植物蛋白質を魚介類練り肉に含有させ
た原料を2軸エクストルーダ処理して繊維状成型組織化
物としたため、褐変等の変色や臭気がなく、良好なフレ
ーバーを有し、all<H感のあるソフトな食感を有す
る加工食品素材が提供される。
Therefore, am! l The raw material, which contains vegetable protein in seafood paste, is treated with a twin-screw extruder to form a fibrous molded structure, so there is no discoloration such as browning, no odor, a good flavor, and a feeling of all < H. A processed food material having a soft texture is provided.

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

第1図は本発明を実施する際に用いられる装置の一例を
示す縦断面図、第2図は本発明方法によって製造された
魚介類の繊維状成形組織化物の一例の斜視図、第3図は
第2図の矢印△A力方向ら切断した縦断面を示す断面図
、第4図は第3図に示す繊維状魚介類練り製品のうちの
フィラメントを一つの方向に引き裂いたときを示す説明
図、第5図は本発明の他の実施例に係る魚介類のlll
1t状成形組織成形の断面図、第6図は本発明を実施す
る際に用いられる装置の例を示す縦断面図、第7図は従
来例に係る2軸エクストルーダの一部を示す断面図であ
る。 符号1・・・・・・バレル 2.3・・・・・・スクリュウ 4・・・・・・バレルダイ 5・・・・・・2軸エクストルーダ 8.9・・・・・・冷却ゾーン 21.31・・・・・・スクリュウ 22.32・・・・・・フロックナツト41・・・・・
・吐出口 61.62・・・・・・分岐チューブ 71.72・・・・・・送給ポンプ 84.94・・・・・・給水管 85.95・・・・・・排水管
FIG. 1 is a longitudinal cross-sectional view showing an example of an apparatus used in carrying out the present invention, FIG. 2 is a perspective view of an example of a fibrous molded tissue of seafood produced by the method of the present invention, and FIG. 3 is a cross-sectional view showing a longitudinal section taken from the force direction of arrow △A in Fig. 2, and Fig. 4 is an explanatory view showing the filament of the fibrous seafood paste product shown in Fig. 3 being torn in one direction. , FIG. 5 shows lll of seafood according to another embodiment of the present invention.
FIG. 6 is a longitudinal sectional view showing an example of an apparatus used in carrying out the present invention, and FIG. 7 is a sectional view showing a part of a conventional biaxial extruder. be. Code 1: Barrel 2.3: Screw 4: Barrel die 5: 2-shaft extruder 8.9: Cooling zone 21. 31...Screw 22.32...Flock nut 41...
・Discharge port 61.62... Branch tube 71.72... Feed pump 84.94... Water supply pipe 85.95... Drain pipe

Claims (1)

【特許請求の範囲】 1)低糖植物蛋白質を含む魚介類練り肉原料を2軸エク
ストルーダにより成形し、繊維状としたものから成るこ
とを特徴とする魚介類の繊維状成型組織化物。 2)前記低糖植物蛋白質が低糖成分、0.4重量%以下
のものからなり、かつ魚介類の練り肉原料中に0.5〜
20%含むものである請求項1記載の魚介類の繊維状成
型組織化物。
[Scope of Claims] 1) A fibrous molded tissue of seafood, characterized in that it consists of a fish paste material containing low-sugar vegetable protein that is molded into a fibrous form using a twin-screw extruder. 2) The low-sugar plant protein consists of a low-sugar component of 0.4% by weight or less, and is present in the raw material for fish paste from 0.5 to 0.5% by weight.
The fibrous molded tissue of seafood according to claim 1, which contains 20%.
JP2265579A 1990-10-03 1990-10-03 Method for producing fibrous molded seafood Expired - Fee Related JPH0646929B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2265579A JPH0646929B2 (en) 1990-10-03 1990-10-03 Method for producing fibrous molded seafood

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2265579A JPH0646929B2 (en) 1990-10-03 1990-10-03 Method for producing fibrous molded seafood

Publications (2)

Publication Number Publication Date
JPH04141069A true JPH04141069A (en) 1992-05-14
JPH0646929B2 JPH0646929B2 (en) 1994-06-22

Family

ID=17419085

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2265579A Expired - Fee Related JPH0646929B2 (en) 1990-10-03 1990-10-03 Method for producing fibrous molded seafood

Country Status (1)

Country Link
JP (1) JPH0646929B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20140287124A1 (en) * 2011-10-26 2014-09-25 Nippon Suisan Kaisha, Ltd. Method for producing feed or food

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4930557A (en) * 1972-07-14 1974-03-19
JPS5548353A (en) * 1978-10-02 1980-04-07 Ajinomoto Co Inc Production of soybean protein
JPS62171657A (en) * 1986-01-22 1987-07-28 Tech Res Assoc Extru Cook Food Ind Production of protein processed food ingredient

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4930557A (en) * 1972-07-14 1974-03-19
JPS5548353A (en) * 1978-10-02 1980-04-07 Ajinomoto Co Inc Production of soybean protein
JPS62171657A (en) * 1986-01-22 1987-07-28 Tech Res Assoc Extru Cook Food Ind Production of protein processed food ingredient

Also Published As

Publication number Publication date
JPH0646929B2 (en) 1994-06-22

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