JPH0611219B2 - Method for producing protein food material - Google Patents
Method for producing protein food materialInfo
- Publication number
- JPH0611219B2 JPH0611219B2 JP62181871A JP18187187A JPH0611219B2 JP H0611219 B2 JPH0611219 B2 JP H0611219B2 JP 62181871 A JP62181871 A JP 62181871A JP 18187187 A JP18187187 A JP 18187187A JP H0611219 B2 JPH0611219 B2 JP H0611219B2
- Authority
- JP
- Japan
- Prior art keywords
- protein
- food material
- containing mixture
- extruder
- die
- 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 - Fee Related
Links
Description
【発明の詳細な説明】 [産業上の利用分野] この発明は、肉的食感に優れた蛋白食品素材の製造方法
に係り、蛋白食品素材を2軸のスクリューを有する押出
機(二軸エクストルーダ)を用いて製造するにあたり、
製品が実質的には膨化しているが、その膨化を抑えて緻
密な組織を持つ蛋白食品素材を製造する方法に関するも
のである。Description: TECHNICAL FIELD The present invention relates to a method for producing a protein food material having an excellent meat texture, and relates to an extruder having a twin screw for the protein food material (a twin screw extruder). ) Is used for manufacturing,
The present invention relates to a method for producing a protein food material having a dense structure by suppressing the swelling although the product is substantially swelled.
[従来技術とその問題点] 従来、加工食品等を製造するにあたっては、一軸のエク
ストルーダが用いられていたが、近年、2軸のスクリュ
ーを持つ二軸エクストルーダが開発され、これを用いて
各種の加工食品を製造する方法が提供されるようになっ
た。[Prior art and its problems] Conventionally, in manufacturing processed foods and the like, a single-screw extruder has been used, but in recent years, a twin-screw extruder having a twin-screw has been developed and various extruders have been developed. There is now provided a method of manufacturing processed foods.
本出願人も先の出願の特開昭60−221041号にお
いて、二軸エクストルーダを用い、油糧種子蛋白、小麦
グルテン及び水を主成分とする蛋白含有混合物から蛋白
食品素材を製造する方法を開示した。The applicant of the present application also discloses a method for producing a protein food material from a protein-containing mixture containing oil seed protein, wheat gluten and water as a main component, using a biaxial extruder in Japanese Patent Application Laid-Open No. 60-221041. did.
ここで、二軸エクストルーダを用いて蛋白食品素材を製
造する場合は、蛋白含有混合物をエクストルーダのバレ
ル内に供給し、バレルを加熱すると共にバレル内に設け
られた各スクリューを回転させ、蛋白含有混合物を高温
・高圧下において混練し、その剪断力や摩擦力等の作用
によって蛋白含有混合物を組織化し、エクストルーダの
先端に設けられたダイ等の口金から押し出すようになっ
ている。Here, when a protein food material is produced using a twin-screw extruder, the protein-containing mixture is supplied into the barrel of the extruder, and each screw provided in the barrel is heated while the barrel is heated to rotate the protein-containing mixture. Is kneaded under high temperature and high pressure, the protein-containing mixture is organized by the action of shearing force and frictional force, and the mixture is extruded from a die such as a die provided at the tip of the extruder.
しかし、蛋白含有混合物を細い口金から押し出す等、蛋
白含有混合物を押出口において高圧の状態で押し出した
場合、圧力の変化により蛋白含有混合物に内蔵された高
温・高圧の水がフラッシュして蛋白食品素材が膨化して
しまい、緻密な組織を持ち、肉的食感に優れた蛋白食品
素材を、連続的に安定して製造し難い問題がある。However, when the protein-containing mixture is extruded at a high pressure at the extrusion port, such as when the protein-containing mixture is extruded through a thin die, the high temperature and high pressure water contained in the protein-containing mixture is flushed by the change in pressure and the protein food material Is swelled and has a problem that it is difficult to continuously and stably manufacture a protein food material having a dense structure and an excellent meat texture.
ここで、このような膨化を抑制する手段としては、従
来、原料となる蛋白含有混合物に油や水を多く加えるこ
とが知られている。Here, as a means for suppressing such swelling, it has been conventionally known to add a large amount of oil or water to a protein-containing mixture as a raw material.
しかし、原料に油を過剰に加えると、バレル内において
滑りが生じ、スクリューの回転による混練が安定して行
われず、剪断力等の作用による蛋白含有混合物の組織化
が不十分で安定した組織が得られないという問題があ
る。However, if too much oil is added to the raw material, slippage occurs in the barrel, kneading by rotation of the screw is not stable, and the organization of the protein-containing mixture due to the action of shearing force is insufficient and a stable structure is obtained. There is a problem that you cannot get it.
また、水を多く加える場合も、バレル内の温度が充分に
上がらず、蛋白含有混合物の組織化が低下すると共に、
製造された蛋白食品素材中に多くの水が含まれ、簡単に
乾燥して保存することができず、フリーズドライ等の特
別の保存方法が必要になる等の問題がある。Also, when adding a large amount of water, the temperature in the barrel does not rise sufficiently, and the organization of the protein-containing mixture is reduced,
Since the protein food material produced contains a large amount of water, it cannot be easily dried and stored, and there is a problem that a special storage method such as freeze-drying is required.
[問題点を解決するための手段および作用] この発明は、上記のような問題を解決せんとしてなされ
たものであり、油や水を多く加えた場合のように、蛋白
含有混合物の組織化を低下させたりすることがなく、蛋
白食品素材の膨化を効果的に抑制し、実質的に膨化して
いるものの緻密な組織を持つ蛋白食品素材を安定して製
造できる方法を提供するものである。[Means and Actions for Solving Problems] The present invention has been made as a solution to the above-mentioned problems, and it is possible to organize a protein-containing mixture as in the case of adding a large amount of oil or water. It is intended to provide a method capable of effectively suppressing swelling of a protein food material without lowering it, and stably producing a protein food material having a dense structure although it is substantially swelled.
すなわち、この発明においては、油糧種子蛋白と小麦グ
ルテンとを主原料として用い、これに水を加えた蛋白含
有混合物を、2軸をスクリューを有する押出機内におい
て加熱・加圧下において混練した後、この蛋白含有混合
物を押出機の先端に設けられた口金より押し出すにあた
り、口金に押し出す直前の圧力を30〜80kg/cm2にす
ると共に、押出機先端の口金を冷却させてその表面温度
を80〜110℃にして実質的に膨化させその程度を抑
制するようにしたのである。That is, in the present invention, oil seed protein and wheat gluten are used as main raw materials, and a protein-containing mixture obtained by adding water thereto is kneaded under heating and pressure in an extruder having a twin screw, When the protein-containing mixture is extruded from the die provided at the tip of the extruder, the pressure immediately before being extruded into the die is set to 30 to 80 kg / cm 2 , and the die at the tip of the extruder is cooled to bring the surface temperature to 80 to The temperature was set to 110 ° C. to substantially swell and suppress the degree.
ここで、原料に用いる油糧種子としては、大豆、菜種、
綿実、落花生、ゴマ、向日葵、コーン等の食用に利用で
きる蛋白を含むものを用いることができるが、特性や入
手の容易性および経済性等の観点から大豆を用いること
が好ましい。また、油糧種子蛋白としては、分離大豆蛋
白のように油糧種子から蛋白部分を分離させたものだけ
ではなく、オカラのような大豆の繊維質部分や、コスト
面から脱脂大豆等を組合わせて用いることも可能であ
る。Here, soybeans, rapeseed,
Although it is possible to use edible protein, such as cottonseed, peanut, sesame, sunflower, corn, etc., it is preferable to use soybean from the viewpoints of characteristics, easy availability and economical efficiency. In addition, as oil seed protein, not only soybean protein such as isolated soybean protein from which the protein portion is separated, but soybean fibrous portion such as okara, and defatted soybean etc. are combined in terms of cost. It is also possible to use.
また、小麦グルテンを用いたのは、小麦グルテンが製造
される蛋白食品素材に繊維状の配向性を付与する作用を
持つためである。Wheat gluten is used because it has a function of imparting fibrous orientation to the protein food material from which wheat gluten is produced.
ここで、油糧種子蛋白と小麦グルテンとの配合比率は、
製造する蛋白食品素材の種類によって異なるが、通常は
これらの重量比を95:5〜20:80の範囲で適宜選
択するようにしている。ただし、蛋白含量が高いほど歯
応えのある蛋白食品素材が得られるため、蛋白含有混合
物中における蛋白含量が、乾物換算で50重量%以上に
なるように調整することが好ましい。Here, the blending ratio of oil seed protein and wheat gluten is
Although it varies depending on the type of protein food material to be produced, these weight ratios are usually selected appropriately within the range of 95: 5 to 20:80. However, the higher the protein content, the more chewy the protein food material is obtained. Therefore, it is preferable to adjust the protein content in the protein-containing mixture to 50% by weight or more in terms of dry matter.
次に、これらの原料に加える水の量は、これを多くし過
ぎると、蛋白含有混合物の実質的膨化による組織化が低
下する一方、これを少なくし過ぎると、原料の水和が不
十分となり、組織が脆くなるため、好ましくは20〜5
0重量%、より好ましくは30〜40重量%に調整す
る。Next, if the amount of water added to these raw materials is too large, the organization due to substantial expansion of the protein-containing mixture is reduced, while if it is too small, the hydration of the raw materials becomes insufficient. Since the structure becomes brittle, it is preferably 20 to 5
It is adjusted to 0% by weight, more preferably 30 to 40% by weight.
また、蛋白含有混合物にはこれらの材料の他に、蛋白食
品素材の用途等に応じてその他の材料を加えることがで
き、例えば、蛋白食品素材がソフトで滑らかな食感を持
つように澱粉を加えたり、蛋白食品素材自体が味を持つ
ように各種の調味料を加えることも可能である。なお、
調味料を加えて蛋白食品素材に予め味付けを行った場合
には、蛋白食品素材に後で味付けを行った場合のように
味が簡単に抜けるということがなく、長い間味が残るよ
うになる。In addition to these materials, other materials can be added to the protein-containing mixture depending on the use of the protein food material. For example, starch is added so that the protein food material has a soft and smooth texture. In addition, it is also possible to add various seasonings so that the protein food material itself has a taste. In addition,
When a protein food material is seasoned in advance by adding a seasoning, the taste will not be easily lost as in the case where the protein food material is seasoned later, and the taste will remain for a long time. .
そして、このような蛋白含有混合物を2軸のスクリュー
を持つ押出機内において、押出機のバレルを加熱すると
共に、バレル内に設けられた各スクリューを回転させ、
高温・高圧下において混練し、剪断力等の作用によって
組織化させるのである。Then, such a protein-containing mixture is heated in an extruder having a twin screw, while heating the barrel of the extruder, and rotating each screw provided in the barrel,
It is kneaded at high temperature and high pressure and organized by the action of shearing force.
ここで、バレルを加熱するにあたっては、通常、蛋白含
有混合物が供給されたバレル前半部の温度が60〜10
0℃、バレル中央の加熱部の温度が90〜170℃、口
金に押し出す直前の先端熔融部の温度が140〜180
℃になるように調整し、また圧力は、口金に押し出す直
前の圧力が30〜80kg/cm2となるように調整する。ま
た、スクリューとしては、蛋白含有混合物に対する剪断
力を高めて組織化を充分にするため、パイナップルスク
リューやニーディングディスクを、単独もしくは組合わ
せて使用することが好ましい。Here, when heating the barrel, the temperature of the first half of the barrel to which the protein-containing mixture is supplied is usually 60 to 10
0 ° C., the temperature of the heating part in the center of the barrel is 90 to 170 ° C., the temperature of the melting part of the tip immediately before extrusion into the die is 140 to 180
The pressure is adjusted so that it becomes 30 ° C., and the pressure is adjusted so that the pressure immediately before extrusion into the die is 30 to 80 kg / cm 2 . Further, as the screw, it is preferable to use a pineapple screw or a kneading disk alone or in combination in order to enhance the shearing force for the protein-containing mixture and to sufficiently organize the screw.
このようにして蛋白含有混合物を高温・高圧下において
混練して組織化させた後、上記押出機の先端に設けた口
金の押出口から押し出す場合、そのままの状態では口金
の表面温度が通常1.20〜140℃に達しており、蛋白含有
混合物内の高温・高圧の水がフラッシュするため、口金
の表面温度が80〜110℃程度となるように口金を冷
却する。そして、この口金部分において蛋白含有混合物
を冷却し、実質的に膨化するがその程度を抑制させて、
口金の押出口から押し出すのである。In this way, after the protein-containing mixture is kneaded under high temperature and high pressure to be organized, and when extruded from the extrusion port of the die provided at the tip of the extruder, the surface temperature of the die is usually 1.20 to Since the temperature has reached 140 ° C and the high-temperature, high-pressure water in the protein-containing mixture flashes, the die is cooled so that the surface temperature of the die becomes about 80 to 110 ° C. Then, the protein-containing mixture is cooled in the mouthpiece portion and substantially swells, but the degree is suppressed,
It is pushed out from the extrusion port of the die.
このように口金を冷却する場合、口金に直接水をかけて
冷却することも可能であるが、安定した冷却を行うため
には、口金内部の押出口近傍にジャケットを設け、この
ジャケットに冷媒を流して冷却することが望ましい。ま
た、ジャケットに冷媒を流して冷却する場合、一つのジ
ャケットでは冷媒の入口と出口とにおける温度差が大き
くなり、均一な冷却が困難になるため、ジャケットを複
数に分割し、各ジャケットに個別に冷媒を流して冷却さ
せるようにすることが好ましい。When cooling the mouthpiece in this way, it is possible to directly cool the mouthpiece with water, but in order to perform stable cooling, a jacket is provided in the vicinity of the extrusion opening inside the mouthpiece, and a refrigerant is put in this jacket. It is desirable to run and cool. In addition, when cooling the refrigerant by flowing it into the jacket, the temperature difference between the inlet and the outlet of the refrigerant becomes large in one jacket, and uniform cooling becomes difficult.Therefore, divide the jacket into multiple jackets and separate each jacket individually. It is preferable to allow a cooling medium to flow to cool it.
ここで、口金としては、蛋白含有混合物を徐々に冷却さ
せて固めていくために、その押出口の断面積に比べ、押
し出し方向の長さの長いものを使用することが好まし
く、またその押出口の形状は、製造する蛋白食品素材の
用途等に応じて、丸形、スリット形等の任意の断面形状
のものを使用することができる。なお、円形の押出口の
場合は、通常その直径dを1〜5mm、長さlを5〜15
0mmとし、l/dが5〜30程度になるようにする。Here, as the die, in order to gradually cool and solidify the protein-containing mixture, it is preferable to use one having a longer length in the extrusion direction than the cross-sectional area of the extrusion port. As for the shape, any cross-sectional shape such as a round shape or a slit shape can be used depending on the intended use of the protein food material to be produced. In the case of a circular extrusion port, the diameter d is usually 1 to 5 mm and the length l is 5 to 15
It is 0 mm and l / d is about 5 to 30.
このようにして得られる蛋白食品素材は、実質的には膨
化しているが、その膨化度は冷却しない場合を100と
して断面比で表すと80以下であり、通常、口金の径の
面積の2倍未満の断面積のものが得られる。The protein food material thus obtained is substantially swelled, but its swelling degree is 80 or less in terms of a cross-sectional ratio, assuming that it is not cooled, and is usually 2 or less of the area of the diameter of the die. A cross-sectional area of less than double is obtained.
[実施例] 以下、この発明の実施例について詳述する。[Examples] Examples of the present invention will be described in detail below.
この実施例において、蛋白食品素材の製造に使用する2
軸のスクリュー(11)を持つ押出機(10)としては、直径D
が約50mm、長さLが約75mm(L/D≒15)のスク
リュー(11)を2本噛み合うようにしてバレル(12)内に並
設したものを用いた(第1図参照)。また、バレル(12)
の先端に設ける口金(13)には、長さlが40mmで、直径
dが2.5mmの円形の押出口(14)が周方向に多数設けら
れ、さらにその外周側に冷水を通すジャケット(15)が2
つに分割されて設けられたものを用いた(第2図参
照)。In this example, 2 used to make protein food ingredients
For an extruder (10) with a shaft screw (11), the diameter D
Of approximately 50 mm and length L of approximately 75 mm (L / D≈15) were used, and two screws (11) were arranged side by side in the barrel (12) so that they meshed with each other (see FIG. 1). Also barrel (12)
A large number of circular extrusion ports (14) with a length l of 40 mm and a diameter d of 2.5 mm are provided in the circumferential direction on a mouthpiece (13) provided at the tip of the jacket, and a jacket ( 15) is 2
The one divided into two parts was used (see FIG. 2).
また、原料としては、下記第1表に示すような配合比率
からなるA〜Dの4種類の原料を使用した。As the raw materials, four types of raw materials A to D having the mixing ratios shown in Table 1 below were used.
そして、これらA〜Dの原料それぞれについて、上記押
出機(10)を用いて蛋白食品素材を製造した。 Then, for each of these raw materials A to D, a protein food material was manufactured using the above extruder (10).
ここで、上記押出機(10)を用いて蛋白食品素材を製造す
るにあたっては、各原料を上記押出機(10)のバレル(12)
内に35kg/Hrの割合で供給し、これに水を加え、原料
に対する水の量が30重量%となるようにした。Here, in producing a protein food material using the extruder (10), each raw material is barrel (12) of the extruder (10)
It was supplied at a rate of 35 kg / Hr and water was added to this so that the amount of water relative to the raw material was 30% by weight.
そして、蛋白含有混合物が供給されたバレル前半部の温
度が60〜100℃、バレル中央の加熱部の温度が90
〜170℃、口金に押し出す直前の先端熔融部の温度が
140〜180℃になるようにバレル(12)を加熱すると
共に、各スクリュー(11)を同方向に300rpmの回転
数で回転させ、蛋白含有混合物を混練した。The temperature of the first half of the barrel to which the protein-containing mixture was supplied was 60 to 100 ° C., and the temperature of the heating part in the center of the barrel was 90.
The barrel (12) is heated so that the temperature of the tip melting part immediately before being extruded into the die is 140 to 180 ° C at ~ 170 ° C, and each screw (11) is rotated in the same direction at a rotation speed of 300 rpm to remove the protein. The containing mixture was kneaded.
一方、バレル(12)の先端に設けた口金(13)においては、
口金(13)に設けた各ジャケット(15)の供給口(15a)から
冷水をジャケット(15)内に供給し、ジャケット(15)内を
循環させて排出口(15b)から排水し、口金(13)をその表
面温度が80〜110℃程度となるように冷却した。On the other hand, in the base (13) provided at the tip of the barrel (12),
Cold water is supplied into the jacket (15) from the supply port (15a) of each jacket (15) provided in the base (13), circulates in the jacket (15) and is discharged from the discharge port (15b), and the base ( 13) was cooled so that the surface temperature was about 80 to 110 ° C.
そして、上記のようにバレル(12)内において高温・高圧
下で混練された蛋白含有混合物を、この口金(13)部分に
おいて冷却させながら押出口(14)から連続して押し出
し、これを適当な長さに切断して蛋白食品素材を得た。Then, the protein-containing mixture kneaded in the barrel (12) under high temperature and high pressure as described above is continuously extruded from the extrusion port (14) while being cooled in this die (13) portion, and this is appropriately cooled. The protein food material was obtained by cutting into length.
このようにして各原料から得られた蛋白食品素材は、そ
の直径が約3.5mmであり、膨化が少なく緻密な多孔状
構造を持つものであった。The protein food material thus obtained from each raw material had a diameter of about 3.5 mm and had a dense porous structure with little swelling.
このようにして得られた各蛋白食品素材を湯戻しした
後、これにビーフエキス等の調味料を用いて味付けし調
理すると、肉的食感に優れ、青椒肉絲等における薄肉の
代用として好適に使用できるものであった。なお、調味
料を加えた原料Dから製造された蛋白食品素材は、味が
簡単に抜けるということがなく、長い間味が残った。After each protein food material thus obtained is reconstituted with hot water, and seasoned with a seasoning such as beef extract and cooked, it has an excellent meat texture and is suitable as a substitute for thin meats such as green pepper meat roe. It was something that could be used. The protein food material produced from the raw material D to which the seasoning was added did not easily lose its taste, and the taste remained for a long time.
[発明の効果] 以上詳述したように、この発明に係る蛋白食品素材の製
造方法においては、油糧種子蛋白と小麦グルテンとを主
原料とし、これに水を加えた蛋白含有混合物を、2軸を
スクリューを有する押出機内において加熱・加圧下にお
いて混練し、押出機の先端に設けた口金より押し出すに
あたり、口金に押し出す直前の圧力を30〜80kg/cm2
にすると共に、押出機先端の口金を冷却させてその表面
温度を80〜110℃にして実質的に膨化させその程度
を抑制するようにした。[Effects of the Invention] As described in detail above, in the method for producing a protein food material according to the present invention, a protein-containing mixture obtained by adding water to oil seed protein and wheat gluten as main materials is added to When the shaft is kneaded in an extruder having a screw under heating and pressure and extruded from a die provided at the tip of the extruder, the pressure immediately before extruding into the die is 30 to 80 kg / cm 2
In addition, the die at the tip of the extruder was cooled to bring the surface temperature to 80 to 110 ° C. to substantially swell and suppress the degree.
この結果、従来のように蛋白含有混合物を口金から押し
出した場合に、蛋白含有混合物に内蔵された高温・高圧
の水がフラッシュするということが少なくなり、上記蛋
白食品素材を実質的に膨化させながらもその程度を抑制
するということができ、また油や水を多く加えた場合の
ように蛋白含有混合物の組織化が低下する等の問題もな
く、緻密な組織を持ち、肉的食感に優れた蛋白食品素材
を連続的に安定して製造できるようになった。As a result, when the protein-containing mixture is extruded from the mouthpiece as in the conventional case, the high temperature and high pressure water contained in the protein-containing mixture is less likely to be flushed, and the protein food material is substantially expanded while It can be controlled to a lesser degree, and there is no problem that the organization of the protein-containing mixture is reduced, such as when adding a lot of oil or water. It has become possible to continuously and stably produce protein food materials.
また、上記の蛋白含有混合物中における水の量を20〜
50重量%にすると、この蛋白含有混合物を押出機内に
おいて混練した後、これを押出機の先端に設けられた口
金より押し出す際に、この蛋白含有混合物における実質
的な膨化が適切に行われ、緻密な組織を持ち、肉的食感
に優れた蛋白食品素材がより安定して得られるようにな
った。Further, the amount of water in the above protein-containing mixture is 20 to
When it is 50% by weight, when the protein-containing mixture is kneaded in the extruder and then extruded from the die provided at the tip of the extruder, substantial expansion of the protein-containing mixture is appropriately performed and the dense mixture is obtained. It has become possible to more stably obtain a protein food material having a different texture and an excellent meat texture.
さらに、蛋白含有混合物中に澱粉等の炭水化物を混入さ
せた場合には、蛋白食品素材をソフトで滑らかな食感を
持つように調整することができ、さらに調味料を混入さ
せて蛋白食品素材に予め味付けを行った場合には、後で
味付けを行った場合のように味が簡単に抜けるというこ
とがなく、長い間味が残るようになった。Furthermore, when a carbohydrate such as starch is mixed in the protein-containing mixture, the protein food material can be adjusted to have a soft and smooth texture, and a seasoning is further mixed to the protein food material. When seasoning was performed in advance, the taste did not easily come off as in the case where the seasoning was performed later, and the taste remained for a long time.
第1図はこの発明の実施例において使用した押出機の先
端部分の横断面図、第2図は同実施例で使用した口金の
縦断面図である。 符号の説明 (10)……押出機、(11)……スクリュー (13)……口金FIG. 1 is a cross-sectional view of the tip portion of the extruder used in the embodiment of the present invention, and FIG. 2 is a vertical cross-sectional view of the die used in the embodiment. Explanation of symbols (10) …… Extruder, (11) …… Screw (13) …… Mouthpiece
Claims (3)
して用い、これに水を加えた蛋白含有混合物を、2軸の
スクリューを有する押出機内において加熱・加圧下にお
いて混練した後、この蛋白含有混合物を押出機の先端に
設けられた口金より押し出すにあたり、口金に押し出す
直前の圧力を30〜80kg/cm2にすると共に、押出機先
端の口金を冷却させてその表面温度を80〜110℃に
して実質的に膨化させその程度を抑制することを特徴と
する蛋白食品素材の製造方法。1. A protein-containing mixture obtained by using oil seed protein and wheat gluten as main raw materials, and adding water thereto, after kneading under heating and pressurization in an extruder having a twin screw. When extruding the containing mixture from the die provided at the tip of the extruder, the pressure immediately before being extruded into the die is set to 30 to 80 kg / cm 2 , and the die at the tip of the extruder is cooled to make the surface temperature 80 to 110 ° C. A method for producing a protein food material, which comprises substantially swelling and suppressing the degree thereof.
0〜50重量%であることを特徴とする特許請求の範囲
第1項記載の蛋白食品素材の製造方法。2. The amount of water in the protein-containing mixture is 2.
The method for producing a protein food material according to claim 1, wherein the content is 0 to 50% by weight.
せたことを特徴とする特許請求の範囲第1項または第2
項記載の蛋白食品素材の製造方法。3. The method according to claim 1 or 2, wherein a carbohydrate such as starch is mixed in the raw material.
A method for producing the protein food material according to the item.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62181871A JPH0611219B2 (en) | 1987-07-20 | 1987-07-20 | Method for producing protein food material |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62181871A JPH0611219B2 (en) | 1987-07-20 | 1987-07-20 | Method for producing protein food material |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6423856A JPS6423856A (en) | 1989-01-26 |
| JPH0611219B2 true JPH0611219B2 (en) | 1994-02-16 |
Family
ID=16108306
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62181871A Expired - Fee Related JPH0611219B2 (en) | 1987-07-20 | 1987-07-20 | Method for producing protein food material |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0611219B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP4520185A1 (en) * | 2023-09-07 | 2025-03-12 | FUJIFILM Corporation | Method of producing protein food material, protein food material, and molded meat alternative |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0698686A (en) * | 1992-09-22 | 1994-04-12 | Nisshin Oil Mills Ltd:The | Meat-like protein food having improved taste and flavor |
| WO2023171304A1 (en) | 2022-03-11 | 2023-09-14 | 富士フイルム株式会社 | Production method for protein food ingredient, and protein food ingredient |
| WO2023171303A1 (en) * | 2022-03-11 | 2023-09-14 | 富士フイルム株式会社 | Protein food material and alternative molded meat |
| WO2024202702A1 (en) * | 2023-03-29 | 2024-10-03 | 富士フイルム株式会社 | Protein food material and alternative molded meat |
| WO2024202703A1 (en) * | 2023-03-29 | 2024-10-03 | 富士フイルム株式会社 | Protein food material and molded meat alternative |
| CN121925181A (en) | 2023-09-29 | 2026-04-24 | 富士胶片株式会社 | Alternative shaped meat |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5716655A (en) * | 1981-05-26 | 1982-01-28 | Ajinomoto Co Inc | Production of food material |
| JPS61224940A (en) * | 1985-03-29 | 1986-10-06 | Kibun Kk | Production of textured food |
| JPS6261544A (en) * | 1985-09-12 | 1987-03-18 | Fuji Oil Co Ltd | Production of laminated food |
| JPS6296045A (en) * | 1985-10-22 | 1987-05-02 | Kowa Kogyo:Kk | Production of soybean-processed food |
| JPS62186752A (en) * | 1986-02-12 | 1987-08-15 | Tech Res Assoc Extru Cook Food Ind | Production of tissual vegetable protein |
| JPH0642B2 (en) * | 1987-07-20 | 1994-01-05 | 不二製油株式会社 | Method for producing high-moisture protein food material |
-
1987
- 1987-07-20 JP JP62181871A patent/JPH0611219B2/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP4520185A1 (en) * | 2023-09-07 | 2025-03-12 | FUJIFILM Corporation | Method of producing protein food material, protein food material, and molded meat alternative |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6423856A (en) | 1989-01-26 |
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