JPS6320490B2 - - Google Patents
Info
- Publication number
- JPS6320490B2 JPS6320490B2 JP52053222A JP5322277A JPS6320490B2 JP S6320490 B2 JPS6320490 B2 JP S6320490B2 JP 52053222 A JP52053222 A JP 52053222A JP 5322277 A JP5322277 A JP 5322277A JP S6320490 B2 JPS6320490 B2 JP S6320490B2
- Authority
- JP
- Japan
- Prior art keywords
- viscous material
- product
- tray
- viscosity
- starch
- 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
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- Meat, Egg Or Seafood Products (AREA)
- Formation And Processing Of Food Products (AREA)
- Dairy Products (AREA)
- Freezing, Cooling And Drying Of Foods (AREA)
- Grain Derivatives (AREA)
- Bakery Products And Manufacturing Methods Therefor (AREA)
- Seeds, Soups, And Other Foods (AREA)
Description
【発明の詳細な説明】
本発明は熱凝固性蛋白とでん粉類、例えば卵蛋
白と小麦でん粉を主原料とし、高周波乾燥して水
の浸透性が早く復元性のよい即席食品用具を製造
する方法に関するものである。[Detailed Description of the Invention] The present invention is a method for producing instant food utensils that have high water permeability and good restorability by using heat-coagulable proteins and starches, such as egg protein and wheat starch, as main raw materials and drying them using high frequency. It is related to.
従来より卵蛋白、乳蛋白、大豆分離蛋白、魚肉
蛋白の如き熱凝固性蛋白は、即席食品の具の製造
には好適なものとされ、これを調理乾燥して具と
することは広く行なわれている。従来このような
乾燥具を製造する場合は、卵蛋白質等とでん粉等
を適当比率で配合し、比較的粘度の高い粘稠物と
なし、これをそのままトレイ上に垂落下せしめ、
高周波又はその他の加熱手段により加熱調理、乾
燥して乾燥具とするものである。このとき加熱に
高周波を採用すると、水に溶解したり、混合中に
混入した気泡が膨張するので、体積比膨化倍率2
〜3倍の肉厚で、外見は乳白色の麩状あるいはカ
ステラ状の多孔性膨化食品となる。 Conventionally, heat-coagulable proteins such as egg protein, milk protein, soy protein isolate, and fish protein have been considered suitable for producing ingredients for instant foods, and it is widely practiced to cook and dry them to make ingredients. ing. Conventionally, when manufacturing such a drying tool, egg protein, etc. and starch, etc. are mixed in an appropriate ratio to form a viscous substance with relatively high viscosity, and this is allowed to drip onto a tray.
It is cooked and dried using high frequency or other heating means to form a dry tool. If high frequency is used for heating at this time, air bubbles dissolved in water or mixed in during mixing will expand, resulting in a volume expansion ratio of 2.
It is a porous puffed food that is ~3 times as thick and has a milky white, gluten-like or castella-like appearance.
これは前記配合の粘稠物の一定量をトレイに垂
落下させる際に粘度が高いので周囲に展開せず含
気泡も多いのでそのままの形態で加熱膨化固定さ
れるので芯部が肉厚となり、その結果表面積が少
さいため製品特に芯部の復元性が悪くなり、更に
は多孔質のため原料本来の食感とは異なる等の欠
点が生じる。これを解決するため前記配合物に加
水し、粘度を下げて加熱することも考えられる
が、この場合、垂落下した配合物は流動して不定
形となつたり、辺縁の加熱が最初に起り順次芯部
に及ぶため芯部は既熱変形の縁部に妨げられて漏
斗状に膨化固定するが、縁部が裂けてしまうかす
るので平円盤状に膨化しない欠点がみられる。 This is because when a certain amount of the above-mentioned viscous material is dropped onto a tray, the viscosity is high, so it does not spread around, and there are many air-containing bubbles, so it is heated and expanded and fixed in its original form, resulting in a thick core. As a result, the surface area of the product is small, resulting in poor restorability of the product, especially the core, and furthermore, the porous nature of the product results in disadvantages such as a texture different from the original texture of the raw material. To solve this problem, it may be possible to add water to the mixture to lower its viscosity and then heat it, but in this case, the dripping mixture may flow and become an amorphous shape, or the edges may be heated first. Since the core is successively reached, the core is blocked by the heated deformed edge and expands and fixes in a funnel shape, but the edge is torn or not, so it does not expand into a flat disk shape.
従来、このような卵蛋白質とでん粉質を配合し
て高周波により加熱、乾燥を行う場合、膨化する
のが当り前とされ、これにより前記欠点が生じて
もそれは当然のこととして解決する研究は全く行
なわれなかつた。 Conventionally, when such a mixture of egg protein and starch is heated and dried using high frequency waves, it has been assumed that swelling occurs, and even if this causes the above-mentioned drawbacks, no research has been conducted to resolve them. I couldn't.
本発明者は、前述のような欠点を除去し原料本
来の食感を生かした乾燥具を製造するために研究
を進めた結果、卵蛋白質等の熱凝固性蛋白質にで
ん粉類等を配合して重粘稠物を作り、これを一定
量トレイ上に垂落下させた後、減圧装置内で減圧
して膨化脱気せしめ、次いで減圧を解除して常圧
に戻して収縮させ、収縮したものを高周波で加熱
乾燥することにより解決できた。 As a result of conducting research to eliminate the above-mentioned drawbacks and to produce a drying tool that takes advantage of the original texture of the raw material, the inventor of the present invention has developed a drying tool that combines heat-coagulable proteins such as egg protein with starch, etc. After making a heavy viscous material and dropping a certain amount onto a tray, it is depressurized in a decompression device to cause it to expand and degas, then the decompression is released and the pressure is returned to normal pressure to cause it to contract, and the deflated material is The problem was solved by heating and drying with high frequency.
これを詳細説明すると、熱凝固性蛋白としては
主として卵蛋白、大豆蛋白、魚肉蛋白を用いるも
ので、これに水及び馬鈴薯でんぷん、小麦でんぷ
ん、とうもろこしでん粉等のでん粉類又はそれ等
を含む穀豆根菜類の粉末を配合し、通常のミキサ
ーで混合する。(第一工程)このときの配合割合
は混合後の粘度を決定する重要な因子であり、こ
の粘度により脱気の際の膨張倍率が左右される。 To explain this in detail, egg protein, soybean protein, and fish protein are mainly used as heat-coagulable proteins, and water and starches such as potato starch, wheat starch, and corn starch, or grains, beans, and root vegetables containing these are used as heat-coagulable proteins. Blend the powders and mix with a regular mixer. (First step) The blending ratio at this time is an important factor that determines the viscosity after mixing, and this viscosity affects the expansion ratio during degassing.
しかし、この粘度管理はα−でん粉、水その他
の粘度調整剤によつて調整するのが好ましくその
粘度は5000〜40000センチポイズとするものであ
る。 However, the viscosity is preferably controlled by α-starch, water or other viscosity modifiers, such that the viscosity is between 5,000 and 40,000 centipoise.
上記粘稠物は第二工程として、トレイ上に移
し、減圧脱気を行つて膨張した後は急速に常圧に
戻す操作を行つて収縮させる。トレイ上に移す場
合は上記粘稠物の一定量を垂落下行なうとよい。
次いでこれを減圧室に搬入し、好ましくは常温に
おいて真空度150〜5torrの減圧下で脱気する。脱
気により粘稠物は膨張し、10〜30倍の膨張倍率に
到達する。脱気後急速に減圧を解き常圧に戻す
と、粘稠物は収縮するがもとの状態とならず、最
初の面積に対し2〜10倍程度のほぼ円形に展開し
たまゝ薄物となる。この状態は前記垂落下の際、
高しぼりとしても、低しぼりとしても厚さの差の
如何を問わずほぼ均一の厚さの円形となる。 In the second step, the viscous material is transferred onto a tray, expanded by degassing under reduced pressure, and then rapidly returned to normal pressure to deflate. When transferring onto a tray, it is preferable to drop a certain amount of the above viscous material onto the tray.
Next, this is carried into a vacuum chamber and degassed under reduced pressure, preferably at room temperature and a degree of vacuum of 150 to 5 torr. Degassing causes the viscous material to expand, reaching an expansion factor of 10 to 30 times. When the pressure is quickly released after degassing and the pressure is returned to normal, the viscous material contracts but does not return to its original state, and remains a thin material that develops into an approximately circular shape with an area 2 to 10 times larger than its original area. . In this state, during the above-mentioned drooping,
Regardless of the difference in thickness, whether high or low, the circular shape is approximately uniform in thickness.
減圧により調合構成物質間の結びつきが強くな
り、また調合物内部に内蔵する空気の液内移動よ
りその表面に内蔵する空気の粘稠液相外への脱気
が僅かに早く、したがつて表面層が脱気のため気
密な層となり、内部から空気の移動を困難にし、
移動困難な空気の膨張により膨張倍率を高くして
薄物の成型を容易にする。 The reduced pressure strengthens the bonds between the constituents of the formulation, and the air contained on the surface of the formulation is degassed out of the viscous liquid phase slightly faster than the air contained within the formulation moves into the liquid, thus reducing the The layer becomes airtight due to degassing, making it difficult for air to move from inside,
By expanding air, which is difficult to move, the expansion magnification is increased to facilitate the molding of thin objects.
このようにして得た薄物は、第三工程として高
周波により内部加熱する。この工程は通常の高周
波誘電加熱手段によるものであるが、加熱により
原料は熱変性して凝固し、生地内部に発生した蒸
気の逃げ場が少いため、激しく震動しつつ水分を
失つて乾燥する。得られた乾燥製品は膨化がきわ
めて少く印加中止後起つた収縮により表面に多数
のしわを生じた円形薄膜となる。 The thin product thus obtained is internally heated by high frequency as a third step. This process uses ordinary high-frequency dielectric heating means, but the raw material is thermally denatured and solidified by heating, and since there is little room for the steam generated inside the dough to escape, it vibrates violently, loses moisture, and dries. The dried product obtained had very little swelling and became a circular thin film with many wrinkles on the surface due to shrinkage that occurred after the application was stopped.
本発明は上述の如くしてなるものであるが原料
の配合に際し、前記α−でん粉の外アルギン酸等
を使用することができ、更に油脂食塩、砂糖、化
学調味料等を添加し、生地粘度及び製品の味を改
良する。又牛肉、豚肉、鳥肉等の鳥獣類の肉類、
鮭、鱒、鯖、すりみ、えび、貝、青のり等の魚貝
藻類、又は、キヤベツ、玉葱、人参等の野菜類等
又はそれらの加工品等を小片となし、前記粘稠物
の混合時に混合するとよい。得られた乾燥製品は
小片が薄膜で被覆され小片の形状に応じた凹凸に
よつて明瞭に識別できる製品となる。この製品は
従来の製品に比べて見場がよく、優れたものとな
る。 The present invention is made as described above, but when blending the raw materials, alginic acid, etc. outside of the α-starch can be used, and further oil and fat salts, sugar, chemical seasonings, etc. are added, and the viscosity of the dough is adjusted. Improve the taste of the product. Also, poultry and animal meat such as beef, pork, and poultry;
Small pieces of fish and shellfish algae such as salmon, trout, mackerel, surimi, shrimp, shellfish, and seaweed, or vegetables such as cabbage, onions, and carrots, or processed products thereof, are used when mixing the viscous material. Good to mix. The resulting dried product is a product in which the small pieces are covered with a thin film and can be clearly identified by the unevenness corresponding to the shape of the small pieces. This product has a better appearance and is superior to conventional products.
本発明の方法により得られた製品は、上記利点
を有する外、表面積が大きく、ほぼ均一な薄物で
あるため水の浸透性がよく、復元がきわめて容易
であり、原料個有の食感を有する等の利点を有す
るものである。 In addition to the above-mentioned advantages, the product obtained by the method of the present invention has a large surface area, is almost uniformly thin, has good water permeability, is extremely easy to reconstitute, and has a texture unique to the raw material. It has the following advantages.
本発明の製品はそのまゝ食用に供しても差支え
ないが、即席食品の具として混合すると極めてそ
の効果を発揮するものである。 Although the product of the present invention may be used for consumption as is, it exhibits its effects extremely well when mixed as an ingredient for instant foods.
以下実施例により本発明の態様を説明する。 Aspects of the present invention will be explained below with reference to Examples.
実施例 1
全卵粉1.6Kgに対しとうもろこしでん粉0.4Kg水
2.96を加え5容ケーキミキサーで5分間混合
し粘度7500センチポイスの重粘稠物を調製した。
この重粘稠物を縦20cm、横30cmのトレイ上に高し
ぼりで垂落下し、直径5cm高さ3mm重さ15gの調
合物を多数作つた。次いでこのトレイを縦形棚式
減圧器に入れ、密閉し50秒間で20torrの減圧に達
せしめ体積膨張倍率がほぼ9倍に達するのを確認
の上、急速に減圧を破り常圧に戻した。これを取
出して測定した所直径9.5cm高さ2.4mmの円形薄物
となつた。Example 1 Whole egg powder 1.6Kg, corn starch 0.4Kg water
2.96 was added and mixed for 5 minutes using a 5 volume cake mixer to prepare a heavy viscous material with a viscosity of 7500 centipoise.
This heavy viscous material was dropped onto a tray measuring 20 cm in length and 30 cm in width using a high squeezer to make a number of preparations each having a diameter of 5 cm, a height of 3 mm, and a weight of 15 g. Next, this tray was placed in a vertical shelf-type pressure reducer, sealed, and a reduced pressure of 20 torr was achieved in 50 seconds. After confirming that the volumetric expansion ratio had reached approximately 9 times, the reduced pressure was rapidly broken to return to normal pressure. When this was taken out and measured, it was a circular thin object with a diameter of 9.5 mm and a height of 2.4 mm.
次いで2450メガヘルツ定格出力1K.W.のコンベ
ア式高周波加熱装置に前記トレイを入れ15gあた
り30秒の条件で加熱乾燥して水分10%、1ケの重
さ9.5gの製品330枚を得た。得られた製品はほぼ
均一な厚さで表面はしわ状を呈し、95℃の熱湯を
注いで3分間で吸水復元しその食感は即席食品の
具として使用して好適であつた。 Next, the tray was placed in a conveyor-type high-frequency heating device with a 2450 MHz rated output of 1 K.W., and heated and dried for 30 seconds per 15 g to obtain 330 products with a moisture content of 10% and a weight of 9.5 g each. The obtained product had a substantially uniform thickness and a wrinkled surface, and when boiling water at 95°C was poured over it, it absorbed water and recovered in 3 minutes, and its texture was suitable for use as an ingredient in instant foods.
実施例 2
実施例1の原料に小えび350g、化学調味料45
g、食塩188g、砂糖470gを加え、ケーキミキサ
ーで10分間混合し粘度15000センチポイスの生地
とした。その他の条件は実施例1と同様に行い、
水分10%で1ケの重量が7.9gのえび玉子400枚を
得た。この製品はえびが薄膜で被覆されて浮き出
し、その形状が見別け可能で見映えが良好であつ
た。この製品はそのまゝ食しても美味であつたが
即席食品の具として吸水復元すればさらに好適で
あつた。Example 2 The raw materials used in Example 1 were 350g of small shrimp and 45g of chemical seasoning.
g, 188 g of salt, and 470 g of sugar were added and mixed for 10 minutes using a cake mixer to form a dough with a viscosity of 15,000 centipoise. Other conditions were the same as in Example 1,
400 shrimp eggs with a moisture content of 10% and a weight of 7.9 g each were obtained. In this product, the shrimp were covered with a thin film and stood out, and the shape was distinguishable and had a good appearance. This product was delicious when eaten as is, but it was even more suitable when it was reconstituted by water absorption as an ingredient in instant foods.
Claims (1)
粘稠物を調整する第一工程と、第一工程の粘稠物
をトレイ上に移し、真空脱気を行つた後常圧に戻
して、膨張収縮する第二工程と、第二工程の収縮
物を高周波加熱する第三工程よりなる即席食品用
円形薄もの具の製造法。 2 特許請求の範囲第1項に於て、第一工程の重
粘稠物に粘度調製剤、調味料又は鳥獣魚介肉類、
野菜類等の小片の一つ又は二つ以上を混合するこ
とを特徴とする即席食品用円形薄もの具の製造
法。[Claims] 1. A first step in which a viscous material is prepared by using thermocoagulable protein and starch alone or in a mixture, and the viscous material in the first step is transferred onto a tray and vacuum degassed. A method for producing a circular thin filling for instant food, which comprises a second step of expanding and contracting after returning to normal pressure, and a third step of heating the contracted product of the second step with high frequency. 2 In claim 1, the heavy viscous material in the first step contains a viscosity modifier, a seasoning, or a bird, animal, seafood, or meat product.
A method for producing a circular thin filling for instant food, characterized by mixing one or more small pieces of vegetables, etc.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5322277A JPS53139737A (en) | 1977-05-11 | 1977-05-11 | Production of circular thin filling for instant food |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5322277A JPS53139737A (en) | 1977-05-11 | 1977-05-11 | Production of circular thin filling for instant food |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS53139737A JPS53139737A (en) | 1978-12-06 |
| JPS6320490B2 true JPS6320490B2 (en) | 1988-04-27 |
Family
ID=12936787
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP5322277A Granted JPS53139737A (en) | 1977-05-11 | 1977-05-11 | Production of circular thin filling for instant food |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS53139737A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2004187639A (en) * | 2002-12-13 | 2004-07-08 | Taiyo Kagaku Co Ltd | Process for making dried food |
| US7279398B2 (en) | 2003-09-17 | 2007-10-09 | Micron Technology, Inc. | Microfeature workpiece processing apparatus and methods for controlling deposition of materials on microfeature workpieces |
-
1977
- 1977-05-11 JP JP5322277A patent/JPS53139737A/en active Granted
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2004187639A (en) * | 2002-12-13 | 2004-07-08 | Taiyo Kagaku Co Ltd | Process for making dried food |
| US7279398B2 (en) | 2003-09-17 | 2007-10-09 | Micron Technology, Inc. | Microfeature workpiece processing apparatus and methods for controlling deposition of materials on microfeature workpieces |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS53139737A (en) | 1978-12-06 |
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