JPS6210626B2 - - Google Patents

Info

Publication number
JPS6210626B2
JPS6210626B2 JP7483878A JP7483878A JPS6210626B2 JP S6210626 B2 JPS6210626 B2 JP S6210626B2 JP 7483878 A JP7483878 A JP 7483878A JP 7483878 A JP7483878 A JP 7483878A JP S6210626 B2 JPS6210626 B2 JP S6210626B2
Authority
JP
Japan
Prior art keywords
protein
interface
aqueous liquid
layer
proteins
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
Application number
JP7483878A
Other languages
Japanese (ja)
Other versions
JPS553732A (en
Inventor
Makoto Utena
Kazuhisa Yamada
Eiki Kamata
Kaoru Inagami
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.)
Asahi Soft Drinks Co Ltd
Original Assignee
Calpis Food Industry 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 Calpis Food Industry Co Ltd filed Critical Calpis Food Industry Co Ltd
Priority to JP7483878A priority Critical patent/JPS553732A/en
Publication of JPS553732A publication Critical patent/JPS553732A/en
Publication of JPS6210626B2 publication Critical patent/JPS6210626B2/ja
Granted legal-status Critical Current

Links

Description

【発明の詳細な説明】 本発明は植物系蛋白質から層状構造をもつ組織
化蛋白質を製造することに係わるものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to the production of an organized protein having a layered structure from a plant-based protein.

本発明の目的とするところは、網状で且つ層状
の組織を有し、さらに植物系蛋白質原料が持つ特
有の臭気が充分に除かれた、畜肉様の食感を持つ
た組織化蛋白質を得ることにある。
The object of the present invention is to obtain a structured protein having a reticular and layered structure, which is sufficiently free from the characteristic odor of plant-based protein raw materials, and which has a meat-like texture. It is in.

植物系蛋白質を組織化する方法については、既
に多くのものが知られている。例えばスピニング
法といわれるもので、蛋白質のアルカリ解膠液を
強制的に細口から押出し、凝固剤を含む浴中で凝
固させ、繊維状とする方法がある。この方法は、
原料由来の臭いを除去すること、及び繊維に組織
化することにおいては優れているが、工程上数種
の薬品を使い、且つ工程が複雑なため、経済的な
方法とはいえない。最もよく知られている方法と
しては、所謂エクストルーダー法といわれている
ものがある。これは高温に加熱され加圧された蛋
白質原料が放出され、そのときの膨化で組織化さ
れる方法で、これの改良法も数多く開発されてい
る。この方法は、工程が簡単で安価に生産できる
利点を有するが、原料由来の臭気成分の大部分は
残存し、また繊維性に欠ける等、生成物の品質の
点ではなお問題点を残している。
Many methods for organizing plant proteins are already known. For example, there is a method called spinning, in which an alkaline peptizing solution for protein is forcibly extruded through a narrow opening and coagulated in a bath containing a coagulant to form a fiber. This method is
Although this method is excellent in removing odors originating from raw materials and organizing it into fibers, it is not an economical method because several types of chemicals are used in the process and the process is complicated. The most well-known method is the so-called extruder method. This is a method in which a protein raw material is heated to a high temperature and pressurized, and is then released and organized by swelling, and many improved methods have been developed. This method has the advantage of a simple process and low cost production, but there are still problems with the quality of the product, such as most of the odor components derived from the raw materials remaining and lack of fibrous properties. .

さらに最近、水蒸気を利用して網状組織化する
方法が開発されている。例えば特開昭52―15853
は、処理区域内において非組織化蛋白質を水蒸気
で組織化する発明である。この発明はエクストル
ーダー法より品質的に優れ、スピニング法より経
済的な方法である。しかし生成物は拡大鏡下で判
別できる程度の微細網状構造を有しているが、巨
視的には粒子状であり、生成物の利用は限定され
るものである。また特公昭49―6665も非組織化蛋
白質と水蒸気を急激に流動せしめて蛋白質を組織
化する方法であるが、この生成物も拡大鏡下にお
いては網状構造を有しているが、水蒸気気流によ
り細片化されているものである。またこれらの水
蒸気法では脱臭の点でも充分とはいえない。
Furthermore, recently, a method of forming a network using water vapor has been developed. For example, Japanese Patent Publication No. 52-15853
is an invention that uses water vapor to organize unorganized proteins within a processing zone. This invention is superior in quality to the extruder method and more economical than the spinning method. However, although the product has a fine network structure that can be discerned under a magnifying glass, macroscopically it is particulate, so the use of the product is limited. In addition, Japanese Patent Publication No. 49-6665 is a method of organizing proteins by rapidly flowing unorganized proteins and water vapor, but this product also has a network structure when viewed under a magnifying glass, but due to the flow of water vapor, It is fragmented. Furthermore, these steam methods are not sufficient in terms of deodorization.

またJ.Food Sci.39 777(1974)で報告されて
いる斎尾らの研究は、大豆蛋白質をカルシウム塩
又は酸で凝固せしめカードを造り、更に脱水して
凝集物とし、この凝集物を水又は緩衝液中に投
じ、次にそれをそのまま加圧釜に入れ100℃以上
で加熱処理しているものである。この方法は蛋白
質を組織化するのに複数回の工程が必要なため経
済的方法とは言えず、更に得られる生成物は油揚
状又は凍豆腐状の多孔質構造である。
In addition, research by Saio et al. reported in J.Food Sci. 39 777 (1974) involved coagulating soybean protein with calcium salts or acids to make curd, then dehydrating it to form aggregates, and watering the aggregates. Alternatively, it is poured into a buffer solution, then placed directly in a pressure cooker and heated at 100°C or higher. This method is not an economical method because multiple steps are required to organize the protein, and furthermore, the resulting product has a porous structure similar to fried tofu or frozen tofu.

この種の研究の最終目的とするところは、畜肉
様の組織を有する素材を得ることにあり、そのた
めに得られる素材は、(1)微細構造としては網状構
造を有しており、(2)巨視的にはある程度の層状構
造をもち且つ横への拡がりを有しており、(3)充分
な脱臭が行なわれたものであることが必要であ
り、なお更に、(4)その製造方法は経済的方法であ
ることが肝要である。
The ultimate goal of this type of research is to obtain a material with a tissue similar to meat, and the material obtained for this purpose has (1) a net-like microstructure; (2) Macroscopically, it has a certain degree of layered structure and spreads horizontally, (3) it must be sufficiently deodorized, and (4) its manufacturing method is It is essential that the method be economical.

本発明者らは上記の目的を達すべく研究を進
め、蛋白質の組織化と同一の工程で植物系蛋白質
原料に混在する非消化性炭水化物や臭気成分等を
除去するとともに、微細構造は網状で巨視的大き
さにおいては層状の組織化蛋白質を得るという。
従来なされなかつた経済的方法を確立し、本発明
を完成した。
The present inventors have conducted research to achieve the above objectives, and have removed indigestible carbohydrates, odor components, etc. mixed in plant protein raw materials in the same process as protein organization, and the microstructure is reticular and macroscopic. It is said that at the target size, a layered organized protein is obtained.
The present invention was completed by establishing an economical method that had not been done before.

本発明は、酸性条件下で熱変性せしめて組織化
蛋白質を得る方法において、下層が水性液体で上
層が気体又は非水性液体又は固体からなる界面が
形成されている装置内へ、植物系蛋白質含有液を
細口を通じて注入し、蛋白質を界面に集積させつ
つ網状で且つ層状の組織化蛋白質を得るものであ
り、このとき同時に植物系蛋白質原料に混在する
非消化性炭水化物や臭気成分等は水性液体層に逸
散して除去され、生成した網状で且つ層状の組織
化蛋白質は蛋白質純度の高いものとなる。以上の
ように本発明は、特定の薬品や添加物を使うこと
なく、組織の優れた品質のよい生成物が簡易に得
られ、上記の4つの目的を達成した方法である。
The present invention provides a method for obtaining an assembled protein by heat denaturation under acidic conditions, in which a plant protein-containing protein is placed into an apparatus in which an interface is formed in which the lower layer is an aqueous liquid and the upper layer is a gas, a non-aqueous liquid, or a solid. The liquid is injected through a narrow opening, and proteins are accumulated at the interface to obtain a reticular and layered organized protein. At the same time, indigestible carbohydrates and odor components mixed in the vegetable protein raw material are removed from the aqueous liquid layer. The resulting reticular and layered organized protein has high protein purity. As described above, the present invention is a method in which a product with excellent tissue quality can be easily obtained without using specific chemicals or additives, and the above four objects have been achieved.

蛋白質が界面部において変性し、特有の生成物
を造る現象は所謂「ユバ」においてみられる。こ
の現象は加熱された豆乳液の液面で蛋白質が変性
する際、独特の膜を形成することである。このユ
バ膜の形成には長時間の加熱を要し、また生成物
の組織は網状且つ層状の組織でないので、畜肉様
組織から程遠いものである。
A phenomenon in which proteins denature at interfaces and produce unique products is observed in so-called "Yuba". This phenomenon occurs when proteins denature on the surface of heated soybean milk, forming a unique film. The formation of this membrane requires long heating times, and the structure of the product is not a reticulated or layered structure, so it is far from a meat-like structure.

しかし本発明者らは、この界面における蛋白質
変性の現象に着目し、新たな方法を見出すことを
計画し研究を進めた。当初、無加圧条件で水性液
体と空気(気体)との界面を造り、等電点に近い
PH条件下で蛋白質含有液を細口より注入した場
合、蛋白質は界面において熱変性を起したが、網
状且つ層状の組織化蛋白質は得られなかつた。次
に更に温度を高め、加圧下で110℃以上の加熱を
行い蛋白質を細口より注入した場合、それまでと
は全く異なる現象が起ることが判明した。即ち界
面に集積した蛋白質から非消化性炭水化物や臭気
成分等が逸散し、水性液体層に移行しており、蛋
白質は純度が高くなるとともに、蛋白質は充分熱
変性を受け、3次元的網状構造を形成し、最終的
には網状にして且つ層状の形態を有する組織化蛋
白質が得られることが明らかになつた。
However, the present inventors focused on the phenomenon of protein denaturation at this interface, and proceeded with research with a plan to find a new method. Initially, an interface between aqueous liquid and air (gas) was created under no pressure conditions, and the interface was close to the isoelectric point.
When a protein-containing solution was injected through the narrow opening under PH conditions, the protein was thermally denatured at the interface, but a network-like and layer-like organized protein was not obtained. Next, it was discovered that when the temperature was further increased to 110°C or higher under pressure and the protein was injected through the narrow opening, a completely different phenomenon occurred. In other words, indigestible carbohydrates and odor components escape from the protein accumulated at the interface and move to the aqueous liquid layer, and the purity of the protein increases.The protein also undergoes sufficient thermal denaturation to form a three-dimensional network structure. It was revealed that an organized protein having a reticular and layered morphology was finally obtained.

次に本発明の構成について詳しく説明する。 Next, the configuration of the present invention will be explained in detail.

本発明でいうところの植物系蛋白質とは、大
豆、落花生、麦類、綿等の種子から得られるもの
である。そして異なる植物系蛋白質が2種以上混
合使用されても差支えない。またミルクカゼイ
ン、卵白等の動物系蛋白質や微生物系蛋白質を本
発明を損なわない程度に適宜添加することは可能
であり、最終生成物の使用目的によつては好まし
いことがある。
Plant-based proteins as used in the present invention are those obtained from seeds of soybeans, peanuts, wheat, cotton, and the like. There is no problem even if two or more different plant-based proteins are used in combination. It is also possible to appropriately add animal proteins such as milk casein and egg white, and microbial proteins to the extent that they do not impair the present invention, and this may be preferable depending on the intended use of the final product.

また本発明でいう界面に蛋白質をより能率的に
集積せしめ収量を高めるためと、生成物の組織を
変える目的でグアガム、キサンタンガム、アラビ
アガム、寒天、コンニヤクマンナン等の増粘剤又
は油脂類を加えることは有効であるが、その添加
量は植物系蛋白質に対し3W/W%以下で充分で
ある。植物系蛋白質含有物は水に分散させて蛋白
質含有液として使用されるが、蛋白質含有液中の
蛋白質含量は1〜30W/W%が好ましい。より好
ましくは3〜20W/W%である。蛋白質含量が
1W/W%未満の場合は網状で且つ層状組織の生
成が不充分となり、30W/W%以上となると蛋白
質含有液は流動性が乏しくなり操作に困難を伴な
う。
In addition, thickeners such as guar gum, xanthan gum, gum arabic, agar, konjac mannan, etc. or fats and oils are added in order to more efficiently accumulate proteins at the interface in the present invention and increase the yield, and to change the structure of the product. Although it is effective to add it, it is sufficient to add it in an amount of 3W/W% or less based on the vegetable protein. A plant-based protein-containing material is used as a protein-containing liquid by dispersing it in water, and the protein content in the protein-containing liquid is preferably 1 to 30 W/W%. More preferably, it is 3 to 20 W/W%. protein content
If it is less than 1 W/W%, the formation of a network and layered structure will be insufficient, and if it is more than 30 W/W%, the protein-containing liquid will have poor fluidity and will be difficult to operate.

上記蛋白質含有液は下層が水性液体で、上層が
気体又は非水性液体又は固体からなる界面が形成
されている装置に細口を通じて注入される。この
装置は圧力に耐える容器でよい。生成物はロータ
リーバルブ等を取りつけて連続的に系外に取り出
すことが可能である。
The protein-containing liquid is injected through a narrow port into a device in which an interface is formed in which the lower layer is an aqueous liquid and the upper layer is a gas, non-aqueous liquid, or solid. This device may be a pressure resistant container. The product can be continuously taken out of the system by attaching a rotary valve or the like.

本発明でいうところの界面は次の3つの何れか
である。
The interface referred to in the present invention is any of the following three.

(1) 水性液体層と水蒸気又は水蒸気、空気からな
る気体層との界面。
(1) An interface between an aqueous liquid layer and a gas layer consisting of water vapor or water vapor or air.

(2) 水性液体層と油脂等の非水性液体層との界
面。
(2) Interface between an aqueous liquid layer and a non-aqueous liquid layer such as oil or fat.

(3) 水性液体層と固体層との界面、例えば水性液
体中に金属板、金網類、その他ベルト類等を設
ける場合がこの態様に相当する。
(3) This embodiment corresponds to the interface between the aqueous liquid layer and the solid layer, for example, when a metal plate, wire mesh, or other belt is provided in the aqueous liquid.

なお水性液体中に、沸点調整物質であるグリセ
リン、プロピレングリコール、塩類、又は蛋白質
変性調整物質であるPH調整剤、アルカリ土類金属
塩等が適宜加えられていてもよい。
Incidentally, boiling point adjusting substances such as glycerin, propylene glycol, salts, protein denaturation adjusting substances such as PH adjusting agents, alkaline earth metal salts, etc. may be appropriately added to the aqueous liquid.

さらに本発明を成就するための界面は、界面に
集積した蛋白質が相互に結着し大きな構造物にな
るのを妨げない程度の静止状態が保たれることが
必要である。なお公知の水蒸気を使用する組織化
法、例えば前述した特開昭52―15853、特公昭49
―6665も蛋白質を熱変性によつて組織化させる方
法であるが、流動的環境下すなわち動的状態で蛋
白質の変性が進行するため、本発明で得られるよ
うな大きな構造物ができず、粒状のものや細片化
されたものしかできない。ゆえにこのような方法
は本発明でいう界面を利用したものとは言えな
い。
Furthermore, in order to achieve the present invention, the interface needs to remain stationary to the extent that proteins accumulated at the interface do not bind to each other and form a large structure. In addition, there are known organization methods using water vapor, such as the above-mentioned Japanese Patent Application Publication No. 52-15853 and Japanese Patent Publication No. 1989-1999.
-6665 is also a method of organizing proteins by thermal denaturation, but since the denaturation of proteins proceeds in a fluid environment, that is, in a dynamic state, large structures such as those obtained with the present invention cannot be formed, and particles are formed. I can only do things that are made up of pieces or fragmented pieces. Therefore, such a method cannot be said to utilize the interface as defined in the present invention.

上記の蛋白質含有液は細口を通じてこの装置に
注入されるが、(1)の水性液体層と気体層からなる
界面を有する装置においては、界面に近い水性液
体層中に細口の位置を設置してもよく、また界面
に近い気体層中に細口の位置を設置して注入して
もよい。なお界面に近い部位とは、注入された蛋
白質含有液が界面に集積することを大きく妨げな
い程度に界面から離れたところをいう。水性液体
層中に細口の位置を設置して蛋白質含有液を水性
液体層中に注入する場合は、蛋白質が界面に集積
していくとともに、蛋白質含有液の不純物、例え
ば非消化性炭水化物や臭気成分等が水性液体層に
逸散していき、純度の高い蛋白質が界面に残存、
集積し、逐次充分なる熱変性を受けて網状にして
且つ層状の組織化蛋白質が造られる。一方、注入
細口の位置を気体層中に設置して、蛋白質含有液
を気体層から注入する場合は、不純物の除去は前
者に劣る。すなわち必要に応じ、適宜蛋白質含有
液の注入位置を選ぶことができるが、水性液体層
中に細口の位置を設置する方が気体層中に設置す
るよりも臭気成分等の不純物の除去が充分行われ
且つ所望の組織化蛋白質が得られるので好まし
い。(2)の水性液体層と非水性液体層からなる界面
が造られている場合は、蛋白質含有液を水性液体
層又は非水性液体層又はその上部の気体層中の何
れに注入してもよいが、生成物の性状および非消
化性炭水化物や臭気成分等の不純物の除去におい
て、水性液体層中に細口の位置を設置して注入し
たものが最も優れている。また(3)の水性液体層と
固体層からなる界面においては蛋白質含有液は界
面の下部に細口の位置を設置して注入することに
なる。なお(1)の水性液体層と気体層との界面にお
いて造られた生成物が、他の界面(2),(3)において
造られたものより口当りが優れている。
The protein-containing liquid mentioned above is injected into this device through the narrow port, but in the device (1) having an interface consisting of an aqueous liquid layer and a gas layer, the narrow port is located in the aqueous liquid layer near the interface. Alternatively, a narrow opening may be placed in the gas layer near the interface for injection. Note that the site close to the interface refers to a site that is far enough away from the interface to not significantly prevent the injected protein-containing liquid from accumulating at the interface. When a protein-containing liquid is injected into an aqueous liquid layer by setting a narrow opening in the aqueous liquid layer, proteins accumulate at the interface and impurities in the protein-containing liquid, such as indigestible carbohydrates and odor components, etc. dissipate into the aqueous liquid layer, and highly pure proteins remain at the interface.
The protein is accumulated and successively subjected to sufficient heat denaturation to produce a reticular and layered organized protein. On the other hand, when the injection port is located in the gas layer and the protein-containing liquid is injected from the gas layer, the removal of impurities is inferior to the former method. In other words, the injection position of the protein-containing liquid can be selected as needed, but impurities such as odorous components can be removed more effectively if the narrow opening is placed in the aqueous liquid layer than if it is placed in the gas layer. This method is preferable because the desired organized protein can be obtained. If an interface consisting of an aqueous liquid layer and a non-aqueous liquid layer is created in (2), the protein-containing liquid may be injected into either the aqueous liquid layer, the non-aqueous liquid layer, or the gas layer above it. However, in terms of the properties of the product and the removal of impurities such as indigestible carbohydrates and odor components, the best method is to inject it into the aqueous liquid layer through a narrow opening. Furthermore, at the interface between the aqueous liquid layer and the solid layer (3), the protein-containing liquid is injected by setting a narrow opening at the bottom of the interface. Note that the product produced at the interface between the aqueous liquid layer and the gas layer (1) has a better mouthfeel than those produced at the other interfaces (2) and (3).

上記の何れの形の界面の場合も、また注入の位
置も、注入された蛋白質が界面に集積するように
適宜操作すればよい。
In the case of any of the above-mentioned forms of the interface, the injection position may be appropriately manipulated so that the injected protein accumulates at the interface.

装置内への蛋白質含有液の注入には、加圧され
た装置内へ押出すことのできる充分な圧力が必要
である。一般には加圧ポンプが使用できる。蛋白
質含有液を通じる細口のサイズは装置の容量、押
出ポンプの性能や蛋白質含有液の粘度等の諸条件
によつて異なる。なお細口の形は円形、環状、長
方形等が使用でき、また細口の数は1個である必
要はなく複数個でも差し支えない。蛋白質含有液
の装置内への注入速度も装置の大きさ等の諸条件
によつて異なるが、獲得したい組織化蛋白質の性
質に応じて、適宜速度を選べばよい。
Injecting the protein-containing liquid into the device requires sufficient pressure to force it into the pressurized device. Generally, a pressure pump can be used. The size of the narrow opening through which the protein-containing liquid passes varies depending on various conditions such as the capacity of the device, the performance of the extrusion pump, and the viscosity of the protein-containing liquid. Note that the shape of the narrow opening can be circular, annular, rectangular, etc., and the number of narrow openings does not have to be one, but may be more than one. Although the rate of injection of the protein-containing liquid into the apparatus also varies depending on various conditions such as the size of the apparatus, the rate may be selected as appropriate depending on the properties of the assembled protein desired to be obtained.

なお蛋白質含有液を装置内に注入し、蛋白質を
熱変性せしめ、界面において網状且つ層状構造を
有する組織化蛋白質を得るには、熱変性を受ける
ときに酸性条件下で110℃以上であることが必要
である。110℃以上に加熱するには加圧条件下で
行い、その方法としては直接加熱法、加熱水蒸気
を装置内に注入する方法、又は熱媒体による間接
加熱法のいずれでもよい。温度が110℃以下に下
がれば、粒子状の生成物が生じる割合が多くな
る。温度の上限は特に限定されないが、エネルギ
ー損失および生成物の褐変等を考えると200℃以
下が好ましい。加熱時間は加熱温度及び求められ
る生成物の組織の性状等により異なる。例えば高
温度ほどまた生成物を長時間高温に放置しておく
ほど組織は硬く強固になつてくる。また本発明の
酸性条件とはPH4.0〜6.5の範囲であり、好ましく
はPH4.5〜5.5である。PH4.0以下やPH6.5以上で
は、たとえ温度が110℃以上でも所望の組織化が
起らない。PH調整は注入する蛋白質含有液のPHを
注入前に調整するか、装置内の水性液体層のPHを
調整するか、あるいは両者を組み合せることによ
り行う。なお注入する蛋白質含有液を前以つてPH
調整する方が操作が容易な点で優れている。PH調
整には酸および塩基が使用でき、例えば塩酸、リ
ン酸、クエン酸、水酸化ナトリウム、重炭酸ナト
リウム等を用いればよい。
Note that in order to inject a protein-containing solution into the device and thermally denature the protein to obtain an organized protein having a network and layered structure at the interface, the temperature must be 110°C or higher under acidic conditions during thermal denaturation. is necessary. Heating to 110° C. or higher is performed under pressurized conditions, and the method may be a direct heating method, a method of injecting heated steam into the apparatus, or an indirect heating method using a heat medium. As the temperature decreases below 110°C, the proportion of particulate products increases. The upper limit of the temperature is not particularly limited, but in consideration of energy loss and browning of the product, it is preferably 200°C or less. The heating time varies depending on the heating temperature and the desired structure of the product. For example, the higher the temperature, and the longer the product is left at high temperature, the harder and stronger the structure becomes. Further, the acidic conditions of the present invention are in the range of PH4.0 to 6.5, preferably PH4.5 to 5.5. If the pH is below 4.0 or above 6.5, the desired organization will not occur even if the temperature is above 110°C. PH adjustment is performed by adjusting the PH of the protein-containing liquid to be injected before injection, by adjusting the PH of the aqueous liquid layer within the device, or by a combination of both. The pH of the protein-containing solution to be injected must be adjusted in advance.
Adjustment is superior in that it is easier to operate. Acids and bases can be used to adjust the pH, such as hydrochloric acid, phosphoric acid, citric acid, sodium hydroxide, sodium bicarbonate, and the like.

また収率よく組織化蛋白質を得るためには次の
方法が有効である。蛋白質含有液において、蛋白
質と炭水化物等の混在成分とをなるべく遊離した
状態におくこと、会合している蛋白質をサブユニ
ツトに近い状態にしておくこと、あるいは蛋白質
を疎水型にすること等の処理を施せばよい。この
処理方法としては蛋白質含有液を前以つて加熱処
理するか、強アルカリ性に保持したのち酸を用い
て等電点近くのPHに調整するか、あるいは強酸性
下に保持したのちアルカリを用いて等電点近くの
PHに調整する等の方法で容易に目的を達成するこ
とができる。その他、前述したようにガム類等の
増粘剤を蛋白質含有液に加えておけば、蛋白質が
水性液体層へ逸散するのを妨ぐ効果がある。水性
液体層についてはそのPHを等電点に近いものとす
るとか、蛋白質の溶解を防止するような塩類を加
えておく等の方法も効果的である。
Furthermore, the following method is effective for obtaining assembled proteins in good yield. In a protein-containing solution, treatments such as keeping proteins and mixed components such as carbohydrates in a free state as much as possible, keeping associated proteins in a state similar to subunits, or making proteins in a hydrophobic form should be applied. Bye. This treatment method is to heat the protein-containing solution in advance, to maintain it in a strongly alkaline state and then use an acid to adjust the pH to near the isoelectric point, or to maintain it in a strongly acidic state and then use an alkali. near the isoelectric point
The purpose can be easily achieved by adjusting the pH. In addition, as mentioned above, adding a thickener such as a gum to the protein-containing liquid has the effect of preventing the protein from escaping into the aqueous liquid layer. For the aqueous liquid layer, methods such as adjusting the pH to be close to the isoelectric point or adding salts to prevent protein dissolution are also effective.

蛋白質含有液のうち110℃以上の温度の水性液
体に溶解し易い成分又は親水性の高い成分は水性
液体層に逸散していき、それとともに蛋白質の純
化が進行する。したがつて好ましくない非消化性
炭水化物や臭気成分等が極めて効率よく除かれ
る。例えば蛋白質含量57W/W%(乾物重量比)
位の原料を使用した場合は最終生成物の蛋白質含
量は約90W/W%近くに上昇することがこのこと
を証明している。このように簡単な操作で蛋白質
の純化が行なわれることが本発明の特徴の一つで
ある。
In the protein-containing liquid, components that are easily soluble in the aqueous liquid at a temperature of 110° C. or higher or highly hydrophilic components dissipate into the aqueous liquid layer, and the purification of the protein progresses accordingly. Therefore, undesirable indigestible carbohydrates, odor components, etc. are removed extremely efficiently. For example, protein content 57W/W% (dry weight ratio)
This is evidenced by the fact that the protein content of the final product increases to nearly 90 W/W% when using approximately 90% raw material. One of the features of the present invention is that proteins can be purified with such simple operations.

また本発明は蛋白質を界面に集積させつつ組織
化蛋白質を得る方法であるので、界面の形や広が
りをいろいろに変えて実施できる。例えば細長い
形態のものや、円形のものや、大きな厚いシート
状のもの等各種製造できる。このことも本発明の
特徴の一つである。
Furthermore, since the present invention is a method for obtaining an organized protein while accumulating proteins at an interface, the method can be carried out by changing the shape and extent of the interface in various ways. For example, various types of products can be manufactured, such as elongated ones, circular ones, and large thick sheet-like ones. This is also one of the features of the present invention.

蛋白質含有液が水性液体層に導入されると、非
消化性炭水化物や臭気成分等は水性液体層に逸散
し、一方蛋白質は熱変性を受けつつ逐次界面に集
積され、熱変性の進行に伴いそれらが充分からみ
合い、結着し、最終的には網状にして且つ層状の
組織化蛋白質を得ることができる。
When a protein-containing liquid is introduced into the aqueous liquid layer, indigestible carbohydrates and odor components escape into the aqueous liquid layer, while proteins undergo thermal denaturation and gradually accumulate at the interface. They are sufficiently intertwined and bound together, and finally, a reticular and layered organized protein can be obtained.

ゆえに本発明は、経済的な工程で、非消化性炭
水化物や臭気成分等の除去を行いつつ、蛋白質の
純化が起り、微細構造としては網状構造を有し、
巨視的には層状構造を有する組織化蛋白質を生産
できるわけである。
Therefore, the present invention purifies the protein while removing indigestible carbohydrates, odor components, etc. in an economical process, and has a network structure as a fine structure.
Macroscopically, an organized protein with a layered structure can be produced.

なお本発明によつて得られる組織化蛋白質を使
用目的によつては、更に炭酸ナトリウム水溶液、
アンモニア水溶液やアンモニアガス等で処理し
て、組織をソフトにしたり水とのなじみを高める
ことも適宜工夫することができる。
Depending on the purpose of use of the structured protein obtained by the present invention, it may be further mixed with an aqueous sodium carbonate solution,
It is also possible to treat the tissue with an aqueous ammonia solution, ammonia gas, or the like to soften the tissue or improve its compatibility with water.

本発明で得られる組織化蛋白質はコンビーフ、
つくだに、ハンバーク、シユーマイ等の畜肉製品
に対して畜肉の代替として使用できる。従来の植
物系組織化蛋白質は植物臭を充分に除去できず、
また組織の面においても畜肉に比べて繊維性に乏
しいため、畜肉含有食品の製造において、畜肉の
約30W/W%以上を組織化蛋白質で代替すること
は味覚および食感に異和感を生じむずかしかつ
た。しかしながら本発明の組織化蛋白質は植物臭
が極めて少なく、組織の面においても畜肉に近い
ものであることから、畜肉に対して約50W/W%
代替しても味覚および食感において、100W/W
%畜肉のものに比べて遜色のないものを得ること
ができる。また本発明によれば、粒状のように小
さな形態ではなく、大小さまざまな大きさ(厚さ
や広がり)の層状形態を有するものが得られるの
で、ひき肉の代替だけではなく、ほし肉やつくだ
に等の代替にも使用できる。また単独でも適宜調
味料を施すことにより食品とすることができる。
すなわち本発明で得られる組織化蛋白質は従来の
組織化蛋白質に比べて用途を広範囲に拡げること
ができるものである。
The structured protein obtained by the present invention is corned beef,
It can be used as a substitute for meat products such as meatballs, hamburgers, and shumai. Conventional plant-based organizing proteins cannot sufficiently remove plant odors;
In addition, in terms of structure, it is less fibrous than livestock meat, so in the production of livestock meat-containing foods, replacing approximately 30W/W% or more of livestock meat with textured protein may result in an unpleasant taste and texture. It was difficult. However, the structured protein of the present invention has very little vegetable odor and is similar to livestock meat in terms of structure, so it is approximately 50W/W% compared to livestock meat.
Even when substituted, the taste and texture are 100W/W.
You can obtain products that are comparable to those made using % livestock meat. Furthermore, according to the present invention, it is possible to obtain a layered product of various sizes (thickness and spread) rather than a small granular form, so it can be used not only as a substitute for minced meat, but also as a substitute for starch meat, meatballs, etc. It can also be used as an alternative. Moreover, it can be used alone as a food by adding seasoning as appropriate.
That is, the assembled protein obtained by the present invention can be used in a wider range of applications than conventional assembled proteins.

実施例 1 市販生大豆を常法によりn―ヘキサンで処理
し、低変性脱脂大豆を得た。この脱脂大豆1部に
水9部を加え、常法によりオカラ部分を除去し、
乾燥固形分6.4W/W%、蛋白質含量が4.2W/W
%である脱脂豆乳を得た。この脱脂豆乳1000gに
1規定の塩酸水を添加し、PH5.10の蛋白質含有液
を調製した。次いで、この蛋白質含有液を、圧力
3.0Kg/cm2、温度126℃に保持された熱水7を有
する、第1図の様な直径20cm、長さ30cm、内容量
9.4のステンレス製の円筒型密閉容器1へ、水
面下3cmより口径1.0mmの細口2を通じ、圧力3.5
Kg/cm2、速度100ml/minの条件において圧入し
た。圧入された蛋白質含有液は水層3と水蒸気層
4とが成す界面5に集積しつつ網状且つ層状の組
織化蛋白質を形成した。蛋白質含有液注入終了約
3分後、常法により容器1を冷却し組織化蛋白質
を得た。本方法によつて得られた組織化蛋白質は
横25cm、縦10cm、厚さ0.5cmの、大豆臭を有さ
ず、白色度の高い畜肉に類似した組織化蛋白質で
あり、その重量は92.6g(乾物重量32.4g)、乾
物あたり88.4W/W%の蛋白質を含有していた。
したがつて脱脂豆乳中の蛋白質は、乾燥固形分比
65.6W/W%が組織化蛋白質では88.4W/W%に
向上していた。また脱脂豆乳に対する組織化蛋白
質の収率は、68%であつた。
Example 1 Commercially available raw soybeans were treated with n-hexane in a conventional manner to obtain low-denatured defatted soybeans. Add 9 parts of water to 1 part of this defatted soybean, remove the okara part by the usual method,
Dry solid content 6.4W/W%, protein content 4.2W/W
% skimmed soy milk was obtained. 1N hydrochloric acid water was added to 1000 g of this skimmed soymilk to prepare a protein-containing solution with a pH of 5.10. Next, this protein-containing liquid is heated under pressure.
3.0Kg/cm 2 , with hot water 7 maintained at a temperature of 126℃, diameter 20cm, length 30cm, and internal capacity as shown in Figure 1.
9.4 into a stainless steel cylindrical airtight container 1 from 3 cm below the water surface through a narrow opening 2 with a diameter of 1.0 mm, and a pressure of 3.5
It was press-fitted at a rate of Kg/cm 2 and a speed of 100 ml/min. The injected protein-containing liquid accumulated at the interface 5 between the water layer 3 and the water vapor layer 4, forming a network and layered structured protein. Approximately 3 minutes after the injection of the protein-containing solution was completed, the container 1 was cooled by a conventional method to obtain a structured protein. The structured protein obtained by this method is 25 cm wide, 10 cm long, and 0.5 cm thick, has no soy odor, has a high white color, and is similar to livestock meat, and its weight is 92.6 g. (dry weight: 32.4 g), and contained 88.4 W/W% protein per dry weight.
Therefore, the protein in skim soy milk is
65.6W/W% was improved to 88.4W/W% for organized protein. Furthermore, the yield of structured protein from skim soy milk was 68%.

実施例 2 市販脱脂豆乳粉末(日清製油〓ソルピーNY:
蛋白質含量60.0W/W%)を塩酸水溶液中に投
じ、PH5.5、蛋白質含量が1.5W/W%である蛋白
質含有液を得た。この蛋白質含有液を実施例1に
記載の装置において水層と水蒸気層との界面の2
cm上方から圧力5.5Kg/cm2、速度70ml/minの条
件において圧入した。この時装置の圧力及び温度
は5.0Kg/cm2、150℃であつた。注入された蛋白質
含有液は界面に集積し、層状構造が緻密な組織化
蛋白質を生成した。蛋白質含有液注入終了後、装
置を冷却し、組織化蛋白質を得た。本方法によつ
て得られた組織化蛋白質は、乾物あたり85W/W
%の蛋白質を含有し、充分なる畜肉様食感を有す
るものであつた。
Example 2 Commercially available skim soy milk powder (Nissin Oil Co., Ltd. Solpy NY:
(Protein content: 60.0 W/W%) was poured into an aqueous hydrochloric acid solution to obtain a protein-containing solution having a pH of 5.5 and a protein content of 1.5 W/W%. This protein-containing liquid was added to the interface between the water layer and the water vapor layer in the apparatus described in Example 1.
It was press-fitted from above at a pressure of 5.5 kg/cm 2 and a speed of 70 ml/min. At this time, the pressure and temperature of the apparatus were 5.0 Kg/cm 2 and 150°C. The injected protein-containing solution accumulated at the interface, producing an organized protein with a dense layered structure. After the injection of the protein-containing liquid was completed, the apparatus was cooled to obtain an assembled protein. The structured protein obtained by this method is 85W/W per dry matter.
% protein and had a sufficient meat-like texture.

実施例 3 市販脱脂豆乳粉末(日本タンパク〓プロトン
MA―1:蛋白質含量60.0W/W%)1部を
0.2W/W%寒天ゲルをつくりこれを撹拌により
破砕したもの9部に投入し、PH6.5、蛋白質含量
が6.0W/W%である蛋白質含有液を得た。次い
でこの蛋白質含有液を圧力0.6Kg/cm2、温度113℃
に保持された0.1M酢酸―酢酸ナトリウム緩衝液
(PH4.50)7を有する実施例1に記載の装置中
に、圧力0.7Kg/cm2、速度70ml/minの条件によ
つて圧入した。緩衝液面下3cmより口径1.0mmの
細口を通じて圧入された蛋白質含有液は、水層と
気層の界面に集積し組織化蛋白質を生成した。本
方法によつて得られた組織化蛋白質は乾物あたり
93W/W%の蛋白質を含有し、繊維性の強いスジ
肉様の食感を有するものであつた。
Example 3 Commercially available skim soy milk powder (Nippon Protein Proton)
MA-1: Protein content 60.0W/W%) 1 part
A 0.2 W/W% agar gel was prepared, crushed by stirring, and added to 9 parts to obtain a protein-containing solution having a pH of 6.5 and a protein content of 6.0 W/W%. Next, this protein-containing liquid was heated at a pressure of 0.6 Kg/cm 2 and a temperature of 113°C.
The mixture was pressurized into the apparatus described in Example 1 containing a 0.1M acetic acid-sodium acetate buffer (PH4.50) maintained at a pressure of 0.7 Kg/cm 2 and a speed of 70 ml/min. The protein-containing solution, which was injected from 3 cm below the surface of the buffer solution through a narrow opening with a diameter of 1.0 mm, accumulated at the interface between the water layer and the air layer to form organized proteins. The structured protein obtained by this method is
It contained 93 W/W% protein and had a texture similar to that of highly fibrous tendon meat.

実施例 4 実施例2で使用した脱脂豆乳粉末1部をクエン
酸水溶液9部に投入し、PH5.0、蛋白質含量が
6.0W/W%である蛋白質含有液を得た。実施例
1の蛋白質組織化装置に水6と食用油1を入
れ、水と油による水性液体層と非水性液体層との
界面を形成せしめた後、圧力3.0Kg/cm2、温度128
℃に加熱した。次いで上記蛋白質含有液を口径
1.0mmの細口より水中に圧入し、水と油の界面に
組織化蛋白質を集積せしめた。本方法によつて得
られる組織化蛋白質は繊維間に油が適度に分布
し、油漬畜肉様の食感を有するものであつた。
Example 4 1 part of the defatted soy milk powder used in Example 2 was added to 9 parts of citric acid aqueous solution, and the pH was 5.0 and the protein content was
A protein-containing solution having a concentration of 6.0 W/W% was obtained. Water 6 and edible oil 1 were put into the protein assembly apparatus of Example 1, and after forming an interface between an aqueous liquid layer and a non-aqueous liquid layer made of water and oil, the pressure was 3.0 Kg/cm 2 and the temperature was 128 kg/cm 2 .
heated to ℃. Next, the above protein-containing solution was poured into a caliber.
It was injected into water through a 1.0 mm narrow opening, and organized proteins were accumulated at the water-oil interface. The structured protein obtained by this method had oil appropriately distributed between the fibers and had a texture similar to oil-soaked meat.

実施例 5 市販低変性脱脂大豆ミール(日清製油〓ソルピ
ーA)に水を加え、常法により蛋白質含量
6.5W/W%の脱脂豆乳を得た。次いでこの脱脂
豆乳を80℃達温加熱処理をした後、塩酸水溶液を
用いPH5.3の蛋白質含有液を調製した。実施例1
において使用した蛋白質組織化装置の製造タンク
内部に、ステンレス製ネツトを設置し、ネツトの
下方に蛋白質含有液圧入細口(口径1.0mm)を設
置した。次いで圧力3.5Kg/cm2、温度140℃の加熱
水をネツト面が水面下になるように圧入し、タン
ク内部で水性液体層と固体層との界面を形成させ
た。この装置内に圧力4.0Kg/cm2、速度100ml/
minで圧入された蛋白質含有液はステンレス製ネ
ツトにそつて集積し、組織化蛋白質を形成した。
本方法によつて得た組織化蛋白質は乾物あたり
90W/W%の蛋白質を含有する保水性良好な蛋白
質繊維からなり、肉様充填材料に適するものであ
つた。
Example 5 Water was added to a commercially available low-denatured defatted soybean meal (Nissin Oil Co., Ltd. Sorpy A), and the protein content was determined by a conventional method.
Skimmed soy milk with a concentration of 6.5 W/W% was obtained. Next, this defatted soymilk was heat-treated to reach a temperature of 80°C, and then a protein-containing solution with a pH of 5.3 was prepared using an aqueous hydrochloric acid solution. Example 1
A stainless steel net was installed inside the production tank of the protein assembly apparatus used in , and a narrow opening (diameter 1.0 mm) for press-in the protein-containing liquid was installed below the net. Next, heated water at a pressure of 3.5 kg/cm 2 and a temperature of 140° C. was injected into the tank so that the net surface was below the water surface to form an interface between an aqueous liquid layer and a solid layer inside the tank. The pressure inside this device is 4.0Kg/cm 2 and the speed is 100ml/cm 2 .
The protein-containing solution injected at 10 min accumulated along the stainless steel net to form an organized protein.
The structured protein obtained by this method is
It was made of protein fibers containing 90W/W% protein and having good water retention properties, and was suitable for meat-like filling materials.

実施例 6 市販落化生を常法によりn―ヘキサンで処理し
低変性脱脂落花生を得た。この脱脂落花生1部に
水9部を加え、常法により蛋白質含量4.0W/W
%の脱脂落化生乳を得た。この脱脂落化生乳に増
粘安定剤としてキサンタンガムを0.2W/W%添
加し、次いで塩酸水溶液を用いPH5.2の蛋白質含
有液を調製した。この蛋白質含有液を実施例1と
同様に、圧力3.0Kg/cm2、温度130℃において組織
化した。本方法により得られた組織化蛋白質は畜
肉様食感を有し、かつ弾力性に富むものであつ
た。
Example 6 Commercially available peanuts were treated with n-hexane in a conventional manner to obtain low-modified defatted peanuts. Add 9 parts of water to 1 part of this defatted peanut and use the usual method to obtain a protein content of 4.0W/W.
% defatted raw milk was obtained. 0.2% W/W xanthan gum was added as a thickening stabilizer to this skimmed and converted raw milk, and then a protein-containing liquid with a pH of 5.2 was prepared using an aqueous hydrochloric acid solution. This protein-containing liquid was organized in the same manner as in Example 1 at a pressure of 3.0 Kg/cm 2 and a temperature of 130°C. The structured protein obtained by this method had a meat-like texture and was highly elastic.

実施例 7 市販の分離大豆蛋白質(日本タンパク〓、プロ
トンNA―2・90、蛋白質含量90.0W/W%)を
水に溶解し、次いで塩酸水溶液によりPH2.0の蛋
白質含有液を得た。この蛋白質含有液を30分間室
温に放置し、低PH処理を施した後水酸化ナトリウ
ム水溶液を添加し、PH4.2に調整した。この時蛋
白質含有液の蛋白質含量は12.0W/W%であつ
た。この蛋白質含有液を実施例1と同様に、圧力
2.0Kg/cm2、温度120℃において組織化した。本方
法によつて得られた組織化蛋白質は、乾物あたり
94W/W%の蛋白質を含有し、畜肉の筋肉組織に
類似する性状を有するものであつた。
Example 7 Commercially available isolated soybean protein (Nippon Protein Co., Ltd., Proton NA-2.90, protein content 90.0 W/W%) was dissolved in water, and then a protein-containing solution with a pH of 2.0 was obtained with an aqueous hydrochloric acid solution. This protein-containing solution was left at room temperature for 30 minutes, subjected to pH-lowering treatment, and then an aqueous sodium hydroxide solution was added to adjust the pH to 4.2. At this time, the protein content of the protein-containing solution was 12.0 W/W%. This protein-containing liquid was heated under pressure in the same manner as in Example 1.
It was organized at 2.0Kg/cm 2 and a temperature of 120°C. The structured protein obtained by this method is
It contained 94 W/W% protein and had properties similar to muscle tissue of livestock meat.

実施例 8 実施例1と同様の処理によつて得た脱脂豆乳に
水酸化ナトリウム水溶液を添加しPH12.0に調整し
た。30分間室温に放置して高アルカリ処理を行な
つた後、塩酸水溶液によつてPH6.0の蛋白質含有
液を得た。そしてこの時の蛋白質含量は4.0W/
W%であつた。この蛋白質含有液を実施例1と同
様に、圧力6.5Kg/cm2、温度162℃において組織化
した。本方法によつて得られた組織化蛋白質は、
乾物あたり91W/W%の蛋白質を含有し充分なる
畜肉様食感を有していた。
Example 8 A sodium hydroxide aqueous solution was added to defatted soymilk obtained by the same treatment as in Example 1 to adjust the pH to 12.0. After being left at room temperature for 30 minutes to perform a high alkaline treatment, a protein-containing solution with a pH of 6.0 was obtained with an aqueous hydrochloric acid solution. And the protein content at this time is 4.0W/
It was W%. This protein-containing liquid was organized in the same manner as in Example 1 at a pressure of 6.5 kg/cm 2 and a temperature of 162°C. The assembled protein obtained by this method is
It contained 91 W/W% protein per dry matter and had a sufficient meat-like texture.

実施例 9 実施例7で使用した分離大豆蛋白質を塩酸水溶
液中に投入し、PH4.5、蛋白質含量20W/W%の
蛋白質含有液を調製した。この蛋白質含有液を実
施例1と同様に、圧力2.0Kg/cm2、温度120℃にお
いて組織化した。本方法によつて得られた組織化
蛋白質は、乾物あたり92W/W%の蛋白質を含有
していた。
Example 9 The isolated soybean protein used in Example 7 was poured into an aqueous hydrochloric acid solution to prepare a protein-containing solution with a pH of 4.5 and a protein content of 20 W/W%. This protein-containing liquid was organized in the same manner as in Example 1 at a pressure of 2.0 Kg/cm 2 and a temperature of 120°C. The structured protein obtained by this method contained 92% W/W protein on a dry matter basis.

実施例 10 実施例3で使用した脱脂豆乳粉末と市販のカゼ
インナトリウム(オルガノ〓)の等量混合物1部
を酢酸水9部に投入し、PH5.20、蛋白質含量
7.0W/W%の蛋白質含有液を調製した。この蛋
白質含有液を実施例1と同様に、圧力3.0Kg/
cm2、温度126℃において組織化した。本方法によ
つて得られた組織化蛋白質は、乾物あたり89W/
W%の蛋白質を含み大豆蛋白質単独のものに比し
弾性に富み、高い咀嚼性を有するものであつた。
Example 10 1 part of a mixture of equal amounts of the defatted soy milk powder used in Example 3 and commercially available sodium caseinate (Organo) was added to 9 parts of acetic acid water, and the mixture was adjusted to pH 5.20 and protein content.
A solution containing 7.0 W/W% protein was prepared. This protein-containing liquid was heated at a pressure of 3.0 kg/kg in the same manner as in Example 1.
cm 2 and textured at a temperature of 126°C. The assembled protein obtained by this method is 89W/dry matter.
It contained W% protein and had higher elasticity and chewability compared to soybean protein alone.

実施例 11 実施例1と同様の処理をして得たPH5.1、蛋白
質含量約4.2W/W%である蛋白質含有液(大豆
蛋白質)3部と、市販活性グルテン粉末(江崎グ
リコ栄養〓、A―グルK、蛋白質含量70W/W
%)を0.01N酢酸水溶液に10W/W%となるよう
に懸濁させた懸濁液1部とを混合し、PH5.0、蛋
白質含量4.9W/W%の蛋白質含有液を得た。こ
の蛋白質含有液を実施例1と同様に、圧力3.0
Kg/cm2、温度131℃において組織化した。本方法
によつて得られた組織化蛋白質は、乾物あたり
88W/W%の蛋白質を含み、大豆蛋白質単独のも
のに比し、より高い柔軟性と結着性を有するもの
であつた。
Example 11 Three parts of a protein-containing liquid (soy protein) with a pH of 5.1 and a protein content of approximately 4.2 W/W% obtained by the same treatment as in Example 1, and commercially available active gluten powder (Ezaki Glico Nutrition Co., Ltd.) A-Glu K, protein content 70W/W
%) in a 0.01N acetic acid aqueous solution to give a concentration of 10 W/W %, and mixed with 1 part of a suspension of 10 W/W %) to obtain a protein-containing solution with a pH of 5.0 and a protein content of 4.9 W/W %. This protein-containing liquid was heated at a pressure of 3.0 as in Example 1.
Kg/cm 2 and a temperature of 131°C. The structured protein obtained by this method is
It contained 88W/W% protein and had higher flexibility and binding properties than soybean protein alone.

実施例 12 実施例2で使用した市販脱脂豆乳粉末(日清製
油〓、ソルピーNY:蛋白質含量60.0W/W%)
1部を増粘安定剤としてグアガムを0.2W/W%
添加した塩酸水溶液9部に投入し、PH5.2の蛋白
質含有液を調製した。この蛋白質含有液2000g
を、加圧ポンプにより圧力3.5Kg/cm2、速度100
ml/minで、あらかじめ3.0Kg/cm2、130℃の加熱
水30を含む製造タンク(直径31cm、高さ56cm、
内容量42からなる円柱型容器)の水層中に口径
1.0mmの細口を通して水面下10cmから圧入した。
圧入された蛋白質は、水蒸気と加熱水との界面に
そつて集積し、組織化蛋白質を生成した。組織化
終了後、冷却水を用い製造タンクを冷却し、常圧
に戻した後、組織化蛋白質を取り出した。本方法
により直径30cm、厚さ1cm、重量389gで大豆臭
を有さない組織化蛋白質が得られた。この組織化
蛋白質は、乾燥固形分30W/W%を含み、乾燥固
形分中の蛋白質含量は92.5W/W%と高かつた。
また本方法による原料蛋白質に対する組織化蛋白
質の収率は90%に達した。本方法によつて得られ
た組織化蛋白質は異味異臭を伴わず畜肉様の組織
を有し、畜肉製品に肉の代替物として利用できる
ものであつた。
Example 12 Commercially available skim soy milk powder used in Example 2 (Nissin Oil Co., Ltd., Sorpy NY: protein content 60.0W/W%)
0.2W/W% of guar gum with 1 part as thickening stabilizer
The solution was poured into 9 parts of the added hydrochloric acid aqueous solution to prepare a protein-containing solution with a pH of 5.2. 2000g of this protein-containing liquid
, the pressure is 3.5Kg/cm 2 and the speed is 100 by the pressure pump.
ml/ min , a production tank (diameter 31cm, height 56cm,
caliber in the water layer of a cylindrical container with an internal capacity of 42
It was press-fitted from 10 cm below the water surface through a 1.0 mm narrow opening.
The injected proteins accumulated along the interface between steam and heated water, producing organized proteins. After the texturing was completed, the production tank was cooled using cooling water and returned to normal pressure, and then the texturized protein was taken out. By this method, a structured protein having a diameter of 30 cm, a thickness of 1 cm, and a weight of 389 g and having no soy odor was obtained. This structured protein contained a dry solid content of 30 W/W%, and the protein content in the dry solid content was as high as 92.5 W/W%.
Moreover, the yield of assembled protein based on the raw material protein by this method reached 90%. The structured protein obtained by this method had a meat-like structure without any off-taste or odor, and could be used as a meat substitute in livestock meat products.

実施例 13 実施例12で得た組織化蛋白質をカラメル及びモ
ナスカラーを用いて肉様に着色した。この着色組
織化蛋白質を繊維方向にほぐし、食塩3W/W%
を添加後冷塩蔵した。一方、市販牛肉に3W/W
%の食塩を加え乾塩蔵したものを、121℃で30分
間高圧蒸煮し、蒸煮後繊維方向にほぐした。繊維
方向にほぐした着色組織化蛋白質及び牛肉を各々
250gとり、牛脂100g、コシヨウ1.5g、グルタ
ミン酸ソーダ0.75g、オールスパイス0.5gを添
加し、ミキサーを用いて混合撹拌しコンビーフベ
ースを調製した。このコンビーフベース125gを
レトルトパウチに充填し真空包装の後、110℃で
30分間加熱殺菌した。本方法により得られた組織
化蛋白質50%置換コンビーフは牛肉100%のもの
に比し、風味、食感ともに何等遜色のないもので
あつた。
Example 13 The structured protein obtained in Example 12 was colored to resemble meat using caramel and Monas color. This colored structured protein is loosened in the direction of the fibers, and salted at 3W/W%.
After addition, the mixture was cold-salted. On the other hand, 3W/W for commercially available beef
% of common salt was added and dry-salted, then high-pressure steamed at 121°C for 30 minutes, and after steaming, it was loosened in the direction of the fibers. Colored structured protein and beef loosened in the fiber direction
250 g was taken, 100 g of beef tallow, 1.5 g of koshiyo, 0.75 g of sodium glutamate, and 0.5 g of allspice were added, and the mixture was mixed and stirred using a mixer to prepare a corned beef base. Fill 125g of this corned beef base into a retort pouch, vacuum pack it, and store it at 110℃.
Heat sterilized for 30 minutes. The corned beef substituted with 50% structured protein obtained by this method was comparable in flavor and texture to 100% beef.

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

第1図は実施例1で使用した本発明の組織化蛋
白質の製造装置の説明図である。1……密閉容
器、2……細口、3……水層、4……水蒸気層、
5……界面。 第2図は実施例1で得られた組織化蛋白質の上
から見た図である。 第3図は実施例1で得られた組織化蛋白質をほ
ぐして、繊維性を示した図である。 第4図は実施例1で得られた組織化蛋白質の断
面で、層状を示す図である。
FIG. 1 is an explanatory diagram of the apparatus for producing an assembled protein of the present invention used in Example 1. 1...Airtight container, 2...Narrow mouth, 3...Water layer, 4...Water vapor layer,
5... Interface. FIG. 2 is a top view of the assembled protein obtained in Example 1. FIG. 3 is a diagram showing the fibrous properties of the organized protein obtained in Example 1. FIG. 4 is a cross section of the assembled protein obtained in Example 1, showing the layered structure.

Claims (1)

【特許請求の範囲】 1 酸性条件下で熱変性せしめて組織化蛋白質を
得る方法において、下層が水性液体で上層が気体
又は非水性液体又は固体からなる界面が形成され
ている装置内へ、植物系蛋白質含有液を細口を通
じて注入し、蛋白質を界面に集積させつつ組織化
させることを特徴とする、組織化蛋白質の製造方
法。 2 蛋白質含有液を装置内に注入するための細口
を水性液体中に位置しておくことを特徴とする特
許請求の範囲第1項記載の方法。 3 下層が水性液体、上層が気体からなる界面を
使用することを特徴とする特許請求の範囲第1項
又は第2項記載の方法。
[Claims] 1. In a method for obtaining an organized protein by heat denaturation under acidic conditions, a plant is placed into an apparatus in which an interface is formed in which the lower layer is an aqueous liquid and the upper layer is a gas, a non-aqueous liquid, or a solid. 1. A method for producing an assembled protein, which comprises injecting a solution containing a system protein through a narrow opening and assembling the protein while accumulating it at an interface. 2. The method according to claim 1, characterized in that a narrow opening for injecting the protein-containing liquid into the device is located in the aqueous liquid. 3. The method according to claim 1 or 2, characterized in that an interface is used in which the lower layer is an aqueous liquid and the upper layer is a gas.
JP7483878A 1978-06-22 1978-06-22 Preparation of organized protein Granted JPS553732A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7483878A JPS553732A (en) 1978-06-22 1978-06-22 Preparation of organized protein

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7483878A JPS553732A (en) 1978-06-22 1978-06-22 Preparation of organized protein

Publications (2)

Publication Number Publication Date
JPS553732A JPS553732A (en) 1980-01-11
JPS6210626B2 true JPS6210626B2 (en) 1987-03-07

Family

ID=13558868

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7483878A Granted JPS553732A (en) 1978-06-22 1978-06-22 Preparation of organized protein

Country Status (1)

Country Link
JP (1) JPS553732A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6212976U (en) * 1985-07-08 1987-01-26
JPH033289A (en) * 1989-05-30 1991-01-09 Gurafuiko:Kk Twisted printed wiring

Also Published As

Publication number Publication date
JPS553732A (en) 1980-01-11

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