JPS5858062B2 - Method for producing gluten paste and gluten powder - Google Patents
Method for producing gluten paste and gluten powderInfo
- Publication number
- JPS5858062B2 JPS5858062B2 JP5077081A JP5077081A JPS5858062B2 JP S5858062 B2 JPS5858062 B2 JP S5858062B2 JP 5077081 A JP5077081 A JP 5077081A JP 5077081 A JP5077081 A JP 5077081A JP S5858062 B2 JPS5858062 B2 JP S5858062B2
- Authority
- JP
- Japan
- Prior art keywords
- gluten
- stirring
- powder
- pasty
- producing
- 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
Links
- 108010068370 Glutens Proteins 0.000 title claims description 81
- 235000021312 gluten Nutrition 0.000 title claims description 81
- 239000000843 powder Substances 0.000 title claims description 30
- 238000004519 manufacturing process Methods 0.000 title claims description 9
- 238000003756 stirring Methods 0.000 claims description 26
- 238000001035 drying Methods 0.000 claims description 21
- 238000004898 kneading Methods 0.000 claims description 17
- 235000011837 pasties Nutrition 0.000 claims description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 17
- 238000000034 method Methods 0.000 claims description 16
- 239000000203 mixture Substances 0.000 claims description 9
- 239000003921 oil Substances 0.000 claims description 9
- 239000004014 plasticizer Substances 0.000 claims description 7
- 239000003638 chemical reducing agent Substances 0.000 claims description 6
- 238000002156 mixing Methods 0.000 claims description 6
- 229920002472 Starch Polymers 0.000 claims description 5
- 239000003925 fat Substances 0.000 claims description 5
- 235000019698 starch Nutrition 0.000 claims description 5
- 239000008107 starch Substances 0.000 claims description 5
- 235000013312 flour Nutrition 0.000 claims description 4
- 241000209140 Triticum Species 0.000 claims description 2
- 235000021307 Triticum Nutrition 0.000 claims description 2
- 239000006071 cream Substances 0.000 claims description 2
- 239000003795 chemical substances by application Substances 0.000 claims 1
- 238000001694 spray drying Methods 0.000 description 8
- 230000015572 biosynthetic process Effects 0.000 description 7
- 238000010521 absorption reaction Methods 0.000 description 6
- 244000144972 livestock Species 0.000 description 6
- 235000013372 meat Nutrition 0.000 description 6
- 241000251468 Actinopterygii Species 0.000 description 5
- 239000002075 main ingredient Substances 0.000 description 5
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- 239000006185 dispersion Substances 0.000 description 3
- 239000011230 binding agent Substances 0.000 description 2
- 235000008429 bread Nutrition 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000003995 emulsifying agent Substances 0.000 description 2
- 230000001804 emulsifying effect Effects 0.000 description 2
- 239000000796 flavoring agent Substances 0.000 description 2
- 235000019634 flavors Nutrition 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 229940023462 paste product Drugs 0.000 description 2
- 239000012190 activator Substances 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 235000013339 cereals Nutrition 0.000 description 1
- 235000009508 confectionery Nutrition 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 235000014113 dietary fatty acids Nutrition 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- -1 ester fatty acid Chemical class 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 229930195729 fatty acid Natural products 0.000 description 1
- 239000000194 fatty acid Substances 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 235000015243 ice cream Nutrition 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 235000012149 noodles Nutrition 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 235000018102 proteins Nutrition 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 235000014102 seafood Nutrition 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Description
【発明の詳細な説明】
本発明はかまぼこ等の水産練製品、ハム等の畜産練製品
、うどん、パン、菓子その他の食品にバインダー等とし
て使用するペースト状グルテン及びこれを分散乾燥した
活性グルテン、所謂グルテン粉末の製造方法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to pasty gluten used as a binder in seafood paste products such as kamaboko, livestock paste products such as ham, udon noodles, bread, confectionery and other foods, and active gluten obtained by dispersing and drying the same. This invention relates to a method for producing so-called gluten powder.
小麦粉に水を加えて固く練った後、水等による洗浄法あ
るいは希酢酸等による抽出法によりデンプンを分離除去
して得られた粘着性のあるたんばく質であるグルテンは
、線状のままでは練製品等の主材料と混練し難いので、
ごく一部ヲペースト状にするほかは殆んど粉末状に分散
乾燥した状態の活性グルテン、つまりグルテン粉末とし
て製品化され、各種練製品等に添加使用されている。Gluten, which is a sticky protein obtained by adding water to wheat flour and kneading it hard, then separating and removing the starch by washing with water or extraction with dilute acetic acid, does not remain linear. Because it is difficult to mix with the main ingredients such as paste products,
With the exception of a small portion that is made into a paste, most of the active gluten is dispersed and dried into powder, which is commercialized as gluten powder, and is used as an additive to various dough products.
従来、ペースト状グルテンは単に可塑剤等によってペー
スト化したものでグルテン独特の灰褐色であるために、
練製品等の主材料、特に魚肉等とは合い難く、また畜産
練製品(例えばハム)の場合には混練温度を高くする必
要があって風味を損なうおそれがあるとともに、ペース
ト状グルテンの乳化性が低く畜肉の油分が分離するおそ
れがあるために他の乳化剤を必要とする等の欠点があり
、それがためにペースト状グルテンはパン類等のごく一
部でしか使用されていないのが実情である。Conventionally, pasty gluten was simply made into a paste using plasticizers, etc., and had a grayish brown color unique to gluten.
It is difficult to mix with main ingredients such as paste products, especially fish meat, etc., and in the case of livestock paste products (e.g. ham), the kneading temperature needs to be high, which may impair flavor, and the emulsibility of pasty gluten There are disadvantages such as the need for other emulsifiers due to the low oxidation rate and the risk of oil separation in meat, and for this reason pasty gluten is only used in a small number of breads and other products. It is.
そこでこの第1番目の発明においては、魚肉等とも合い
易い乳白色でしかも乳化性が良く、練製品の主材料と混
り合い易く、水産練製品や畜産練製品等にも汎く使用で
きるペースト状グルテンを容易かつ確実に製造、提供し
ようとするものであり、グルテンを可塑剤等とともにエ
ヤーが分散混入するように攪拌混練することにより、微
小気泡を無数に混在させてソフトクリーム状にすること
を特徴とするものである。Therefore, in this first invention, we created a paste that has a milky white color that goes well with fish meat, etc., has good emulsifying properties, is easy to mix with the main ingredients of paste products, and can be widely used for fish paste products, livestock paste products, etc. The aim is to manufacture and provide gluten easily and reliably, and by stirring and kneading gluten with plasticizer etc. so that air is dispersed, it is possible to mix countless microbubbles and make it into a soft cream-like product. This is a characteristic feature.
またグルテンを粉末状にして、つまりグルテン粉末とし
て製品化する場合は線状のグルテンを分散乾燥して粉末
にするもので、それには代表的なものとして噴霧乾燥法
(スプレードライ方式)と気流乾燥法(フラッシュドラ
イ方式)との二つの方法がある。In addition, when gluten is made into a powder, that is, when it is commercialized as gluten powder, linear gluten is dispersed and dried to make it into a powder.The typical methods are spray drying method (spray drying method) There are two methods: the flash dry method.
噴霧乾燥法は、デンプンと分離したグルテンの分散液を
熱風雰囲気中に噴霧させて乾燥しグルテン粉末を得るも
ので、これにより得られたグルテン粉末は吸水速度が速
く含水によるグルテン形成速度が速いという長所がある
反面、含有率10%程度のグルテン分散液にして乾燥す
るので熱効率が悪いという欠点がある。In the spray drying method, a dispersion of gluten separated from starch is sprayed into a hot air atmosphere and dried to obtain gluten powder.The resulting gluten powder has a high water absorption rate and is said to have a high rate of gluten formation due to water content. Although it has advantages, it has the disadvantage of poor thermal efficiency because it is dried as a gluten dispersion with a content of about 10%.
他方、気流乾燥法は、比較的固練り状のグルテンをカッ
ターにより直径2〜3m峨度のチップ状に細かく切断し
、これにグルテン粉末を添加して混練した後これをさら
に細かく粉砕して熱気流のパイプ中に送給し乾燥するも
ので、熱効率が良い反面、これにより得られたグルテン
粉末は噴霧乾燥法により得られたものより吸水速度が遅
く含水によるグルテン形成速度が遅いという欠点がある
。On the other hand, in the flash drying method, relatively hard gluten is finely cut into chips with a diameter of 2 to 3 meters using a cutter, gluten powder is added to this, kneaded, and then further finely ground to dry with hot air. The gluten powder obtained by this method has a disadvantage that it absorbs water at a slower rate than that obtained by spray drying, and the rate of gluten formation due to water content is slower than that obtained by spray drying. .
そこで、この出願の第2番目の発明においては、気流乾
燥法によって、噴霧乾燥法の場合と同様の吸水速度およ
びグルテン形成速度の速いグルテン粉末を得ようとする
ものであり、その特徴は上記第1番目の発明により得ら
れるペースト状グルテンを気流乾燥することにある。Therefore, in the second invention of this application, an attempt is made to obtain gluten powder with a high water absorption rate and gluten formation rate similar to that of the spray drying method by using a flash drying method, and its characteristics are as described in the above-mentioned No. The purpose of the present invention is to air-dry the pasty gluten obtained by the first invention.
次に本発明の実施態様を図面に基いて説明する。Next, embodiments of the present invention will be described based on the drawings.
先ず、従来と同様の方法により普通の粘稠なグルテンを
得るもので、小麦粉に水を加えて固く練り(生地形成)
、次いでこれを水等の液中に攪拌分散させてデンプンを
分離除去することにより、水分を65%前後含む粘着性
のあるグルテンを得る。First, ordinary viscous gluten is obtained using the same method as before, by adding water to flour and kneading it hard (forming dough).
Next, this is stirred and dispersed in a liquid such as water to separate and remove starch, thereby obtaining sticky gluten containing approximately 65% water.
そしてペースト状グルテンを製造するには、上記のよう
にして得られたグルテンに吸水性のよいシュガーエステ
ル等の可塑剤、還元剤、油脂等を加えてこれをエヤーが
分散混入するように攪拌混練すればよい。To produce pasty gluten, a plasticizer such as sugar ester with good water absorption, a reducing agent, fats and oils, etc. are added to the gluten obtained as described above, and the mixture is stirred and kneaded using air to disperse the mixture. do it.
この攪拌混線には、例えば第2図に略示するように、軸
11の周囲にスクリュー羽根12を固着した攪拌回転体
13a、13bを機体14内の下部において上下に並設
してなる攪拌混線機10を使用する。For example, as schematically shown in FIG. 2, this stirring mixer includes stirring rotors 13a and 13b, each having a screw blade 12 fixed around a shaft 11, arranged vertically in parallel at the lower part of the body 14. Machine 10 is used.
前記上下の攪拌回転体13a 、13bは一方のスクリ
ュー羽根12の回転域と他方のスクリュー羽根12の回
転域とがオーバーランプするように設けるのが混線効率
上望ましく、そのためスクリュー羽根12.12のらせ
ん方向をオーバーラツプ部分で同一方向、つまり一方を
他方とは逆方向のらせんにするとともに、上下の回転方
向を正逆反対にし、スクリュー羽根12.12同士が当
触しないようにする。The upper and lower stirring rotors 13a and 13b are preferably provided so that the rotation range of one screw blade 12 and the rotation range of the other screw blade 12 overlap in terms of crosstalk efficiency. The directions are made to spiral in the same direction at the overlapping part, that is, one direction is opposite to the other, and the up and down rotation directions are reversed so that the screw blades 12 and 12 do not come into contact with each other.
もちろんスクリュー羽根の構造によっては同方向のらせ
んにしたり、同一方向に回転させることも可能である。Of course, depending on the structure of the screw blades, it is possible to spiral in the same direction or to rotate in the same direction.
上記のような攪拌混練機10内に所定量のグルテンを入
れ、さらに可塑剤、還元剤、油脂等を所定量加えて攪拌
回転体13a、13bの回転により攪拌混練すると、内
部のグルテンはスクリュー羽根12による回転押動作用
によりうねり等を生じ押し合い圧し合いしながら複雑に
流動しその結果エヤーがグルテンの内部に表面部より噛
み込まれ分散混入する。When a predetermined amount of gluten is put into the stirring kneading machine 10 as described above, a predetermined amount of a plasticizer, a reducing agent, oil, etc. is added, and the mixture is stirred and kneaded by the rotation of the stirring rotors 13a and 13b, the gluten inside is mixed with the screw blades. Due to the rotational pushing action by 12, undulations and the like are generated and the gluten flows in a complex manner while pressing against each other, and as a result, air is bitten into the inside of the gluten from the surface part and dispersed.
特にグルテンは粘着性が犬でかつ比較的固練りの状態で
あるが、これに可塑剤、還元剤、油脂等を添加して攪拌
混練するので、前記可塑剤により流動性が増し、上記攪
拌混練作用およびこれに伴なうエヤー混入が不都合なく
行なわれ、また油脂の働きで泡を形成し易くエヤーが比
較的短時間で混入され、さらに還元剤により容易にペー
スト状となり、攪拌混練作用が効率よく行なわれる。In particular, gluten is sticky and in a relatively hard kneaded state, but since it is stirred and kneaded by adding plasticizers, reducing agents, fats and oils, etc., the fluidity is increased by the plasticizer, and the above-mentioned stirring and kneading. The action and the accompanying air mixing are carried out without any inconvenience, and the action of oil and fat makes it easy to form bubbles, allowing the air to be mixed in in a relatively short time.Furthermore, the reducing agent easily forms a paste, making the stirring and kneading action more efficient. It is often done.
そしてこの攪拌混練により混入したエヤーが分散し、無
数の微小気泡となって略均−に混在し、あたかもソフト
クリーム状のごときペースト状グルテンが得られるので
ある。By this stirring and kneading, the mixed air is dispersed and becomes a countless number of microbubbles that are evenly mixed together, resulting in a paste-like gluten that looks like a soft cream.
なお、上記攪拌混線の際に、油脂等とともにシュガーエ
ステル脂肪酸等の活性剤を添加しておくと、混入された
エヤーの分散が速くなる。Incidentally, if an activator such as sugar ester fatty acid is added together with oil or fat during the above-mentioned stirring and mixing, the mixed air will be dispersed more quickly.
また攪拌混練機としては、上記した形式のものが温度制
御を行ない易くかつエヤー混入作用上好適であるが、エ
ヤー混入可能な他の攪拌機を用いることもできる。Further, as for the stirring/kneading machine, the above-mentioned type is suitable for easy temperature control and air mixing, but other stirring machines capable of mixing air can also be used.
上記のごとき本発明(第1番目の発明)の方法により得
られるペースト状グルテンは、無数の微小気泡が均一に
混在してボリュームを増したソフトクリーム状をなすも
ので、灰褐色であったものがエヤー混入とともに淡くな
り結果として乳白色になっているため、練製品の主材料
特に魚肉等とも合い易く、しかも性質的には微小気泡の
混在により乳化性が非常に良く、これを畜産練製品に使
用した場合にも畜肉の油分を安定よく抱かせることがで
き、他の乳化剤を必要としない。The pasty gluten obtained by the method of the present invention (first invention) as described above is grayish brown in color and has a soft cream-like texture with increased volume due to the uniform mixture of countless microbubbles. When air is mixed in, the color becomes pale and becomes milky white, so it goes well with the main ingredients of the paste product, especially fish meat, etc. Moreover, it has very good emulsifying properties due to the presence of microbubbles, so it is used in livestock paste products. Even when used, the oil content of livestock meat can be held in a stable manner, and other emulsifiers are not required.
またこのペースト状グルテンは微小気泡が無数に混在し
ていて粒子の表面積が大きくなっているので練製品の主
材料と混り易く畜肉の場合に混練時の温度を風味を損な
うほどに上げなくても充分に混練できる。In addition, this paste-like gluten has countless microbubbles mixed in, and the surface area of the particles is large, so it easily mixes with the main ingredient of the paste product, so in the case of meat, the temperature during kneading must not be raised to the extent that it spoils the flavor. can also be thoroughly kneaded.
従って本発明により得られるペースト状グルテンは水産
練製品や畜産練製品その他の各種練製品に汎く使用でき
る。Therefore, the pasty gluten obtained by the present invention can be widely used in fish paste products, livestock paste products, and various other paste products.
このように本発明の方法によれば上記のごとき効果を有
し利用度の高い優れたペースト状グルテンを得ることが
できる。As described above, according to the method of the present invention, it is possible to obtain an excellent pasty gluten having the above-mentioned effects and being highly usable.
また、上記のようにして造られるペースト状グルテンを
、下記のごと〈従来周知の気流乾燥工程20へ供給して
分散乾燥することにより、噴霧乾燥法による場合と同様
の吸水速度およびグルテン形成速度の速い良質のグルテ
ン粉末を得ることができる(第2番目の発明)。In addition, by supplying the pasty gluten produced as described above to the conventionally well-known flash drying process 20 and dispersion drying it, the water absorption rate and gluten formation rate can be maintained at the same rate as in the case of the spray drying method. Good quality gluten powder can be obtained quickly (second invention).
このグルテン粉末の製造について説明すると上記第1番
目の発明により得られたペースト状グルテンを、第3図
に示す気流乾燥工程20における供給ホッパー21へポ
ンプ等にて送り込み、ここから攪拌コンベヤー22へ送
出させると同時にグルテン粉末を所定量添加して攪拌し
つつ徐々に送る。To explain the production of this gluten powder, the pasty gluten obtained according to the first invention is fed by a pump or the like to the supply hopper 21 in the flash drying step 20 shown in FIG. 3, and from there is sent to the stirring conveyor 22. At the same time, a predetermined amount of gluten powder is added and gradually fed while stirring.
固練りのグルテンによる従来方法ではホッパーからの送
出の際に細かαチップ状に切断し攪拌し易くしていたが
、本発明ではペースト状グルテンをそのまま送出すれば
よく、微小気泡が無数にソフトクリーム状に混在してい
るために添加グルテン粉末と混り合い易く、その攪拌が
効率よく行なわれる。In the conventional method using hardened gluten, the gluten was cut into fine α-tips to make it easier to stir when it was sent out from the hopper, but in the present invention, it is only necessary to send out the paste-like gluten as it is, and the soft serve ice cream is made up of countless microbubbles. Since they are mixed together in the same shape, they are easily mixed with the added gluten powder, and the stirring is performed efficiently.
そして前記のように攪拌コンベヤー22により徐々に送
られるグルテンを粉砕機23によりさらに細かく粉砕し
て、熱交換器z4による熱気流を生ぜしめた乾燥パイプ
25内へ送給し、熱気流により分散乾燥すればよく、こ
れに供されるグルテンが微小気泡を無数に混在して空間
が多く、そのため粉砕された細粒の表面積が大きくかつ
微小気泡を内在しているために、前記熱風気流による乾
燥が速く信実に能率よく行なわれる。Then, as mentioned above, the gluten gradually fed by the stirring conveyor 22 is further finely ground by the grinder 23, and then fed into the drying pipe 25 where a hot air flow is generated by the heat exchanger z4, and the gluten is dispersed and dried by the hot air flow. The gluten to be used for this process has a large number of microbubbles mixed in and has many spaces, so the surface area of the ground fine grains is large and contains microbubbles, so drying by the hot air flow is difficult. It is done quickly, reliably and efficiently.
なお乾燥されて粉末状になった製品所謂グルテン粉末は
乾燥パイプ25の出口にサイクロン等を設けて捕集回収
すればよい。The dried powder product, so-called gluten powder, may be collected and recovered by providing a cyclone or the like at the outlet of the drying pipe 25.
回収されたグルテン粉末の一部はホッパーからの送出部
分での添加にまわす。A portion of the recovered gluten powder is used for addition at the delivery section from the hopper.
上記のようにして得られるグルテン粉末は、微小気泡が
無数に混在してソフトクリーム状をなすペースト状グル
テンを乾燥したものであるため、粉末の粒子は乾燥前の
微小気泡の存在により変形して表面積が大きなものとな
っておりその結果従来の気流乾燥法により得られた粉末
に比し、吸水速度が速くグルテン形成速度が速く、噴霧
乾燥法により得られたものと同程度の性質を有する。The gluten powder obtained as described above is obtained by drying pasty gluten that has a soft cream-like appearance with countless microbubbles mixed in, so the powder particles are deformed by the presence of microbubbles before drying. It has a large surface area and, as a result, has a faster water absorption rate and faster gluten formation than powders obtained by conventional flash drying, and has properties comparable to those obtained by spray drying.
即ち、従来の気流乾燥法によるグルテン粉末を加水、混
練による固さ御粘弾性について特性テストを行なうと、
第4図に示すミキソグラフ〔A〕のごとくなり、グルテ
ン特有の粘弾性が生じるまでに少なくとも1分30秒以
上かかり、しかもその粘弾性が安定するのに2分以上か
かるが、本発明により得られたグルテン粉末を上記と同
条件の下で同じ特性テストを行なえば、第4図のミキソ
グラフCB)のごとくなり、20秒前後の短時間でグル
テン特有の粘弾性が生じかつその粘弾性が安定するもの
で、これによって本発明により得られるグルテン粉末は
グルテン形成速度が速く、練製品のバインダー等として
の使用に好適であることが判る。In other words, when gluten powder was mixed with water using the conventional flash drying method and tested for hardness and viscoelasticity by kneading,
The mixograph [A] shown in Fig. 4 shows that it takes at least 1 minute and 30 seconds for the viscoelasticity peculiar to gluten to occur, and moreover, it takes more than 2 minutes for the viscoelasticity to stabilize. If we perform the same characteristic test on gluten powder under the same conditions as above, it will become as shown in the mixograph CB in Figure 4, and the viscoelasticity peculiar to gluten will occur in a short time of around 20 seconds and the viscoelasticity will become stable. This shows that the gluten powder obtained by the present invention has a fast gluten formation rate and is suitable for use as a binder for dough products.
このように本願の第2番目の発明の方法によれば、微小
気泡を無数に混在せるペースト状グルテンを形成して、
これを気流乾燥に供することにより、熱効率のよい気流
乾燥法をもって吸水性が良くグルテン形成速度の速い良
質のグルテン粉末を能率よく得ることができる。In this way, according to the method of the second invention of the present application, paste-like gluten containing countless microbubbles is formed,
By subjecting this to flash drying, it is possible to efficiently obtain high-quality gluten powder with good water absorption and a fast gluten formation rate using the heat-efficient flash drying method.
第1図は本発明による工程ブロック図、第2図は攪拌混
線様部分の暗示縦断正面図、第3図は気流乾燥工程の略
示図、第4図はグルテン粉末の固さ一粘弾特性のミキソ
グラフを示す。
10・・・・・・攪拌混練機、13a 、13b・・・
・・・攪拌回転体、20・・・・・・気泡乾燥工程、2
1・・・・・・供給ホッパー、22・・・・・・攪拌コ
ンベヤー 23・・・・・・粉砕機、24・・・・・・
熱交換器、25・・・・・・パイプ。Fig. 1 is a block diagram of the process according to the present invention, Fig. 2 is a schematic vertical cross-sectional view of the stirring mixing line-like part, Fig. 3 is a schematic diagram of the flash drying process, and Fig. 4 is the hardness and viscoelastic properties of gluten powder. The mixograph is shown below. 10...Stirring and kneading machine, 13a, 13b...
... Stirring rotary body, 20 ... Bubble drying process, 2
1... Supply hopper, 22... Stirring conveyor 23... Pulverizer, 24...
Heat exchanger, 25...pipe.
Claims (1)
られたグルテンに伺塑剤、還元剤および油脂等を加えて
これをエヤーが分散混入するように攪拌混練し、微小気
泡を無数に混在させてソフトクリーム状にすることを特
徴とするペースト状グルテンの製造方法。 2 エヤーが分散混入するように攪拌混練するのに、軸
の周囲にスクリュー羽根を固設した攪拌回転体を機体内
下部において上下に並設してぼる攪拌混練機を使用する
ことを特徴とする特許請求の範囲第1項記載のペースト
状グルテンの製造方法。 3 小麦粉に水を加えて練った後デンプンと分離して得
られたグルテンに可塑剤、還元剤および油脂等を加えて
これをエヤーが分散混入するように攪拌混練し、微小気
泡を無数に混在させてソフトクリーム状にしたペースト
状グルテンを、気流乾燥法により分散乾燥することを特
徴とするグルテン粉末の製造方亀 4 ペースト状グルテンをそのまま攪拌分散させて乾燥
する特許請求の範囲第3項記載のグルテン粉末の製造方
法。[Scope of Claims] 1. After adding water to wheat flour and kneading it, a plasticizing agent, a reducing agent, fats and oils, etc. are added to the gluten obtained by separating it from starch, and the mixture is stirred and kneaded so that the mixture is dispersed with air. , a method for producing pasty gluten, which is characterized by mixing countless microbubbles into a soft cream-like product. 2 A stirring and kneading machine is used for stirring and kneading so that air is dispersed and mixed in, using a stirring and kneading machine in which stirring rotors with screw blades fixed around the shaft are arranged vertically in parallel at the lower part of the machine body. A method for producing pasty gluten according to claim 1. 3 After adding water to flour and kneading it, a plasticizer, a reducing agent, oil, etc. are added to the gluten obtained by separating it from the starch, and the mixture is stirred and kneaded using air to disperse the mixture, creating a mixture of countless microbubbles. Method for producing gluten powder, characterized by dispersing and drying pasty gluten which has been made into a soft cream form using a flash drying method.Claim 4: A method for producing gluten powder, which is characterized in that pasty gluten is dispersed and dried by a flash drying method.Claim 3 describes the process of drying the pasty gluten by stirring and dispersing it as it is. A method for producing gluten powder.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5077081A JPS5858062B2 (en) | 1981-04-03 | 1981-04-03 | Method for producing gluten paste and gluten powder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5077081A JPS5858062B2 (en) | 1981-04-03 | 1981-04-03 | Method for producing gluten paste and gluten powder |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS57166940A JPS57166940A (en) | 1982-10-14 |
| JPS5858062B2 true JPS5858062B2 (en) | 1983-12-23 |
Family
ID=12868059
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP5077081A Expired JPS5858062B2 (en) | 1981-04-03 | 1981-04-03 | Method for producing gluten paste and gluten powder |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5858062B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4211953B2 (en) * | 1998-02-19 | 2009-01-21 | アサマ化成株式会社 | Food production method and quality improver |
| JP6065209B2 (en) * | 2013-01-18 | 2017-01-25 | 日本製粉株式会社 | Noodle making method |
-
1981
- 1981-04-03 JP JP5077081A patent/JPS5858062B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS57166940A (en) | 1982-10-14 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JPH07194290A (en) | Baking improver composition | |
| JPH02502336A (en) | Method and apparatus for making batter products | |
| JP5428003B2 (en) | Processed foods using rice-based ingredients and their manufacturing methods | |
| RU2048104C1 (en) | Polycomponent food addition and method of its production | |
| JP2717226B2 (en) | Noodle manufacturing method | |
| KR20040004085A (en) | Powder or granule-form fat/oil and its production method | |
| Brennan | Mixing, emulsification and size reduction | |
| JPS5858062B2 (en) | Method for producing gluten paste and gluten powder | |
| JP4759005B2 (en) | Powdered egg, shape retention improver containing the same, and various processed foods | |
| US3290152A (en) | Method of making rehydrated gluten products | |
| JPS6283857A (en) | Production of modified wheat flour | |
| RU2281654C2 (en) | Sparkling caramel article | |
| KR900005966B1 (en) | Method of mixing or kneading food powder | |
| JP2007289089A (en) | Modified starch and noodles made from the same | |
| JPS6411329B2 (en) | ||
| AU2001237324A1 (en) | Effervescent caramel product | |
| JP2914307B2 (en) | Batter mix | |
| US3384036A (en) | Process for the continuous preparation of pastry dough | |
| JPH0419815B2 (en) | ||
| JPS632574B2 (en) | ||
| JPH0227955A (en) | Production of citron-containing noodle | |
| JPS63129956A (en) | Method for producing puffed snack confectionery containing corn grits as the main ingredient | |
| CA1300424C (en) | Method of mixing or kneading edible flour | |
| JPS6133551B2 (en) | ||
| JPS58107154A (en) | Preparation of chicken meat ball |