JP3457015B2 - Production method of fried food - Google Patents
Production method of fried foodInfo
- Publication number
- JP3457015B2 JP3457015B2 JP15432992A JP15432992A JP3457015B2 JP 3457015 B2 JP3457015 B2 JP 3457015B2 JP 15432992 A JP15432992 A JP 15432992A JP 15432992 A JP15432992 A JP 15432992A JP 3457015 B2 JP3457015 B2 JP 3457015B2
- Authority
- JP
- Japan
- Prior art keywords
- fried
- dough
- gas
- soymilk
- parts
- 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 - Lifetime
Links
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- Beans For Foods Or Fodder (AREA)
Description
【発明の詳細な説明】
【0001】
【産業上の利用分野】本発明は、従来から知られる丸大
豆からの油揚げの欠点(乾燥品の湯戻り復元性が悪く、
組織も粗い)や分離大豆蛋白と油脂の組み合わせによる
油揚げの欠点(乾燥品でも容易に湯戻りするものの丸大
豆からの油揚げのような張りや風味がない)を解決した
丸大豆からの油揚げ(乾燥品であっても湯戻りに優れ、
組織が細かく、風味に優れる)を製造する方法を提供す
るものである。
【0002】
【従来技術】油揚げの製造方法には大きく2つの方法が
知られている。ひとつは丸大豆から豆腐生地を得、これ
を成形しフライするいわゆる伝統工法である。もうひと
つは、分離大豆蛋白と油脂のエマルジョン生地を成形し
フライする新工法である。得られた油揚げを比較する
と、伝統工法によって得られた油揚げは乾燥品が湯戻り
しないことと、組織的に内部に空隙を有する海綿状の組
織を有し外皮はガラス状の硬い表皮膜である特徴があ
る。一方、新工法により得られる油揚げは湯戻りが容易
なのでインスタント食品等に最適であり、組織的にも内
外部共均一に細かなスポンジ状組織である特徴を有す
る。
【0003】
【発明が解決しようとする問題】伝統工法による油揚げ
は湯戻りしない欠点を有するものの大豆由来の風味が豊
富である。一方、新工法による油揚げは湯戻りが容易で
ある反面大豆由来の風味に乏しい欠点を有する。そこ
で、本発明者等は湯戻りしやすく且つ大豆由来の風味を
有する油揚げを目的とした。
【0004】
【問題を解決する為の手段】前記目的達成のアプローチ
として伝統工法の湯戻り性を解決するか、新工法の大豆
由来の風味を追求するかのいずれかが考えられるが、ま
ず前者を目的とした。本発明者等は伝統工法の油揚げと
新工法の油揚げの湯戻り性の違いを組織的に研究するな
かで、伝統工法によって得られた油揚げが内部に空隙を
有する海綿状のポーラスな組織とガラス状の硬い表皮膜
の外皮を有するのに比べ、新工法により得られる油揚げ
は内外部共均一に細かなスポンジ状組織を有する知見を
得た。そこで、組織的に伝統工法による油揚げを新工法
による油揚げに近づける多くの研究を行った。そのなか
の一つに豆乳に含気させた状態で凝固させた豆腐生地を
作成しこれを成形フライすれば、その乾燥品が湯戻り性
に優れる知見を得た。その組織をみても伝統工法の油揚
げや新工法のそれとも異なる組織、即ち、内部は均一に
細かなスポンジ状組織で外皮はきめの細かな柔らかい表
皮組織を有する知見を得た。本発明はこれらの知見に基
づいて完成したものである。
【0005】即ち、本発明は、丸大豆から油揚げを製造
する工程において、豆乳に含気させて凝固し油揚げ生地
を調製する油揚げの製造法である。一般に丸大豆からの
油揚げの製造工程は水に浸漬した丸大豆に水を加え磨砕
し、必要により消泡剤等を加えて呉を得、加熱処理した
後加水しおからを分離して豆乳を得、凝固剤を加えて豆
腐状のカードとなしこれを割砕し脱水プレス成形しフラ
イして油揚げを得る。本発明に用いる丸大豆は産地、種
類、新旧を問わず公知のものを用いることができる。そ
の他リポキシゲナーゼ欠損大豆等遺伝子的に改質したも
のも用いることができる。又、本発明に於いては丸大豆
を圧偏した全脂大豆も権利範囲に含むが、脱脂した脱脂
大豆は大豆由来の風味に劣る為権利外である。丸大豆の
水浸漬は充分な水に大豆が膨潤するに充分な時間、例え
ば一昼夜程度浸漬すればよい。浸漬して膨潤した丸大豆
は加水して磨砕して呉となすことが出来る。呉は加熱・
戻し水加水して後オカラを不溶物として分離除去して豆
乳を得ることができる。
【0006】本発明は得られた豆乳に含気させて凝固し
油揚げ生地を調製するところに特徴を有する。即ち、気
体がミクロ状に分散し(一部は溶解して)豆乳中に含気
されることによって油揚げ生地の組織や油揚げの乾燥品
の湯戻り復元性を向上させるものである。含気割合の計
測や算出は含気装置や用いる気体の種類により規定が困
難であるが次に例示相当量の気体をミクロ状に分散ある
いは溶存状態で含むことができる。管内連続混合撹拌装
置を用いて空気を含気させる場合、豆乳100重量部に
対し0.6−1.7容量部(好ましくは0.8−1.6
容量部)の気体を吹き込むことが適当である。尚、重量
部に対する容量部は、kgに対してはリットル、gに対
してはcc或いはミリリットルを意味する。別の指標を
用いて表現すれば、含気された後の豆乳の溶酸素量が
3.0mg/リットル−5.8mg/リットル(好ましくは
3.1mg/リットル−5.7mg/リットル)が適当であ
る。V=W*22.4*Mの式から計算すると、溶酸素
量が2.1ミリリットル/リットル−4.0ミリリット
ル/リットル(好ましくは2.2ミリリットル/リット
ル−3.9ミリリットル/リットル)が適当である。空
気を含気させたときの溶存酸素量は前記の値のときが適
当であるが、空気成分として溶存窒素等溶存する空気量
の合計はこの値以上となる。もしミクロ的に分散して存
在する割合が多ければ含まれる空気量は溶存酸素量のほ
ぼ5倍であるおよそ10.5ミリリットル/リットル−
20.0ミリリットル/リットル(好ましくは11.0
ミリリットル/リットル−19.5ミリリットル/リッ
トル)が適当となるし、溶存状態の割合が大きい場合は
窒素の溶解割合が関与してこれよりも小さい値になるこ
ともある。その他の気体を用いる場合でも、炭酸ガスの
ように水に対する溶解度の高い気体ほどこれを考慮して
前記空気量より多めに含気させる(例えば管内連続混合
撹拌装置等を用いて)ことがミクロ的に分散した含気状
態の形成に有効である。
【0007】含気量が多くなるほど生地をフライして油
揚げとなす際の生地の伸びが制限され伸びが少なくなる
反面得られる油揚げの組織は空隙のある粗い海綿状組織
から空隙がないきめ細かなスポンジ状組織となる。含気
割合が少ないと生地が伸びすぎ、反対に含気割合が多す
ぎると生地の伸びが悪くなり不適である。含気させる気
体の種類は空気、窒素ガス、炭酸ガス、不活ガス等毒性
がない限り特に制限するものではない。含気手段は豆乳
を気体存在下に激しく撹拌すればよい。公知の気液混合
装置であればバッチ式でも連続式でも用いることができ
るが、工業的に一定量の気体を含気させるには連続装置
が好ましい。バッチ式では例えばキャビッテーション等
のような高速撹拌により容易に多量の空気を含ませるこ
とができるが、含気割合を一定に保つように調製するこ
とは容易ではない。連続式では管内に豆乳を流しながら
気体を吹き込み撹拌・混合して含気させることができ
る。いわゆる管内連続混合撹拌が好ましく、豆乳の濃
度、温度等を調節し流量を一定に保ち吹き込む気体の量
を調整することにより容易に含気割合を調節することが
できる。通常、管内に流れる豆乳100重量部に対し
0.6−1.7容量部(好ましくは0.8−1.6容量
部)の気体を吹き込むことが適当である。豆乳中に気体
が均一に細かく分散して含まれるには管内に流れる豆乳
に気体を吹き込み分割し、反転し、転換しながら管内連
続混合撹拌することがより好ましい。
【0008】本発明の含気豆乳を凝固させるには公知の
凝固剤を用いることも出来るが、なかでも塩化Mgを用
いると食感の柔らかい油揚げを得ることが出来好まし
い。より好ましくは塩化Mgと塩化Caを併用すること
により脱水プレス成形する油揚げ生地の水切れがよく得
られる油揚げのの食感もソフトで好ましい。例えば、塩
化Caを用いると脱水プレス後の生地が硬くなるので水
切れは良くなるが得られる油揚げの食感が硬いものにな
ったり、表面が硬くなるなどして湯戻り復元性が悪化す
る傾向が見られる。塩化Mgだけではソフトな食感の油
揚げが得られが、作業性の点で脱水生地の水切れが悪く
なり生産効率が低下する傾向にある。塩化Mgと塩化C
aの組み合わせが適当であり、塩化Mgと塩化Caの組
み合わせにより食感のソフトな油揚げが得られるととも
に脱水生地の水切れもよく生産効率も向上する。又、必
要に応じ豆乳中へ炭酸Caを添加することができる。炭
酸Caを加えることにより得られる油揚げの伸びが促進
される傾向にある。凝固した豆腐状カードを割砕して脱
水プレスしてホエー成分を除去するとともに成形する。
【0009】割砕手段はカードをこわして脱水しやすく
する為であり公知の手段を用いることができる。成形は
目的の油揚げにあわせ伸びを考慮して条件を設定するこ
とができる。脱水成形物の水分は凝固剤の量や製造工程
条件(加熱等)により異なるが生地が成形できればよ
い。脱水成形物はフライする。フライは通常工業的には
公知のフライヤーを用いることができ、フライヤーへの
導入部に分配手段等の装置を用いることは自由である。
フライ条件は成形生地のサイズにより異なるが生地が適
度に伸びきめ細かなスポンジ状組織を形成する条件であ
れば特に制限するものではない。市販インスタント食品
用の油揚げ程度の大きさであれば通常220℃以下が適
当である。フライ態様は1段よりも2段以上の多段フラ
イによる温度勾配(例えば、60℃−180℃)を設け
たほうが好ましい。通常、工業的には得られた油揚げは
目的により冷却、凍結、レトルト処理、着味あるいは乾
燥等適宜組み合わせる等し、選別、包装等されて製品と
することができる。
【0010】
【実施例】以下実施例により本発明の実施態様を説明す
る。
実施例1(含気量の検討)
丸大豆100重量部(以下部)を充分量の水に20時間
浸漬し、水切りして220部の浸漬大豆を得た。この浸
漬大豆15.6部に35部の水を加え、グラインダー
(ナガサキ機械(株)製)を用いて磨砕して呉を得た。
この呉を生蒸気で加熱(96℃で40秒)し、戻し水3
6部を加えて、おから絞り機(高井製作所(株)製:1
20メッシュ)を用いておからを分離して豆乳(濃度4
Bx、品温71℃)21.3部を得た。この豆乳100
部当たり空気混入量が表1となるようにスタティックミ
キサーN30型(ノリタケ(株)製)を用いて空気を豆
乳に均一に含気させ、ついで塩化Mg5.63部を加
え、凝固した豆乳を割砕してこわし、連続油揚げ生地成
形装置(ソーエーマシーン(株)製)を用いてプレスし
てホエーを分離脱水すると同時に成形(62mm*49
mm*7mm)しフライヤー(ソーエーマシーン(株)
製)に入れ1段目60℃、2段目120℃の条件で2段
フライし、品温20℃まで冷却して油揚げを得た。得ら
れた油揚げの伸びと組織の状態を表1に合わせて示す。
又、空気混合後の豆乳の含気割合を測定する為に、大和
環境分析センター(株)に溶存酸素(単位はmg/リッ
トル)の測定を依頼した。結果を表1に合わせて示す。
溶存酸素の豆乳1リットルに対する重量割合(W)と容
量割合(V)の関係は、V=W*22.4*Mである。
Mは気体の分子量であり酸素は32とした。
【0011】
【表1】
──────────────────────────────────
空気量 揚げの伸び 組織 溶存酸素量
──────────────────────────────────
0 伸び過ぎ 空隙を有する 2.6 1.86
(容量部) 粗い海綿状組織 (mg/l) (ml/l )
表面はガラス状
の硬い組織
──────────────────────────────────
0.54 伸び過ぎ 空隙を有する 2.9 2.08
(容量部) 海綿状組織 (mg/l) (ml/l )
──────────────────────────────────
1.08 若干伸び スポンジ状組織 3.4 2.44
(容量部) 過ぎ (mg/l) (ml/l )
--------------------------------------------------------------
1.53 良好な伸び スポンジ状組織 4.2 3.01
(容量部) (mg/l) (ml/l )
──────────────────────────────────
1.80 伸び不足 スポンジ状組織 5.7 4.09
(容量部) (mg/l) (ml/l )
──────────────────────────────────
【0012】表1の結果よりわかるように含気量が少な
すぎると伸びすぎ組織も空隙が生じて粗い海綿状組織と
なり、湯戻り復元性も悪化した。反対に含気量が多くな
りすぎると組織は細かなスポンジ状となるものの生地の
伸びが不足した。豆乳(4Bx)100部に対して通気
量が0.54容量部を越え、1.80容量部未満の範囲
のとき得られる生地をフライした油揚げ生地は伸びも適
当で組織もスポンジ状の細かなもので、これを乾燥した
油揚げの湯戻り復元性も優れていた。このときの溶存酸
素量は2.08ミリリットル/リットルを越え、4.0
9ミリリットル/リットルを越えていた。含気量は窒素
等の溶存割合にもよるが100%と仮定すれば約5倍程
度と予測された。
【0013】実施例2(凝固剤の検討)
実施例1と同様にして得た豆乳100部当たり空気混入
量を表1の1.53部に設定し実施例1と同様に含気さ
せ、実施例1の塩化Mgの代わりに表2に示すように凝
固剤の種類の組み合わせ及び量(実施例1と同様豆乳に
対する添加量)を変えて、後の工程は実施例1と同様に
して油揚げを得た。結果を合わせて表2に示す。
【0014】
【表2】
──────────────────────────────────
塩化Ca 塩化Mg 脱水生地及び油揚げの状態
---------------------------------------------------------------
5.63部 0 脱水プレス後の生地の水切り良好なれど
油揚げの食感が硬い。
──────────────────────────────────
2.81部 2.82部 脱水プレス後の水切れも良好で
油揚げの食感もソフトであった
──────────────────────────────────
0 5.63部 脱水プレス後の生地の水切り悪いが
油揚げの食感がソフトであった
──────────────────────────────────
【0015】表2からわかるように、塩化Caだけでは
脱水プレスした生地が硬く水切れは良いが、得られた油
揚げが硬く(特に表面が硬い)ソフトな食感が得られな
かった。一方、塩化Mgだけでも食感がソフトで良好で
あったが、脱水プレス後の生地が柔らかく水切れが悪く
なる傾向にあった。塩化Caと塩化Mgを併用すること
により脱水プレス後の生地の硬さも適当になり水切れも
良く食感がソフトな油揚げが得られた。
【0016】
【発明の効果】本発明により、丸大豆からの油揚げであ
りながら湯戻りが容易できめ細かな組織を有し大豆由来
の風味に優れ、生地の伸びが十分な油揚げが可能になっ
たものである。更に、湯戻り復元性に優れた乾燥油揚げ
が可能になったものである。 Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a drawback of conventionally known frying from whole soybeans (recovery property of dried products is poor,
Frying from dried soybean (drying) which solved the drawbacks of fried food due to the combination of isolated soybean protein and oils and fats (the dried product easily returns to hot water but has no tension or flavor like fried from whole soybean) It is excellent in hot water return even if it is a product,
Which has a fine structure and excellent flavor). [0002] There are roughly two known methods for producing fried food. One is the so-called traditional method of obtaining tofu dough from whole soybeans, shaping it and frying it. The other is a new method of forming and frying emulsion dough of isolated soy protein and oil and fat. Comparing the obtained fried products, the fried products obtained by the traditional method have no sponge-dried product, and have a spongy structure with voids inside, and the outer skin is a glassy hard surface film. There are features. On the other hand, the deep-fried fried food obtained by the new method is suitable for instant foods and the like because of easy hot water replenishment, and also has a feature that the inside and outside are uniformly fine sponge-like structures. [0003] The deep-fried oil fried by the traditional method has a disadvantage that it does not return to hot water, but has a rich flavor derived from soybeans. On the other hand, the deep-fried oil fried by the new method has a drawback in that the hot water is easily returned, but the flavor derived from soybean is poor. Therefore, the present inventors aimed to fry oil having a soybean-derived flavor that easily returns to hot water. Means for solving the problems [0004] As an approach for achieving the above-mentioned object, either one of solving the hot water reversibility of the traditional method or pursuing a soybean-derived flavor of the new method is considered. Aimed at. The present inventors have systematically studied the difference between the refrigerating property of the deep-fried oil of the traditional method and the new method of refrigerating, and found that the deep-fried oil obtained by the traditional method has a spongy porous structure with voids inside and glass. It was found that the deep-fried fried food obtained by the new method had a fine sponge-like structure both inside and outside, compared to having a hard outer skin with a slab shape. Therefore, a lot of research was conducted to systematically make the deep-frying by the traditional method approach the deep-frying by the new method. When one of them produced tofu dough coagulated in a state in which the soymilk was aerated and formed and fried, the obtained dried product was found to be excellent in hot water recyclability. Looking at the structure, it was found that the structure was different from that of the traditional method of fried or the new method, that is, the inside had a fine sponge-like structure and the outer skin had a fine-grained soft skin structure. The present invention has been completed based on these findings. [0005] That is, the present invention is a method for producing fried food in which in the step of producing fried food from whole soybeans, soymilk is aerated and coagulated to prepare fried dough. Generally, the production process of fried soybeans from whole soybeans involves adding water to the soybeans immersed in water, grinding them, adding an antifoaming agent, etc., if necessary, to obtain go, and heat-treating the water to separate soy milk from soymilk. And a coagulant is added to make a tofu-like curd, which is crushed, dewatered press-molded and fried to obtain oil fried. As the whole soybean used in the present invention, known ones can be used irrespective of the place of origin, kind, and new or old. In addition, genetically modified products such as lipoxygenase-deficient soybeans can also be used. In the present invention, whole fat soybeans in which whole soybeans are pressed are included in the scope of right, but defatted defatted soybeans are inferior in flavor due to soybeans and thus are out of the right. The water soak of the whole soybean may be soaked in sufficient water for a sufficient time for the soybean to swell, for example, about one day and night. The soybeans swelled by immersion can be mashed with water to make a go. Kure is heated
After adding water back, the okara is separated and removed as an insoluble matter to obtain soy milk. The present invention is characterized in that the soymilk obtained is aerated and coagulated to prepare fried dough. That is, the gas is dispersed in a micro shape (partially dissolved) and is contained in the soymilk to improve the texture of the fried dough and the hot water restoring property of the dried fried product. It is difficult to determine the measurement or calculation of the gas content depending on the gas containing device and the type of gas used. Next, however, a substantial amount of gas can be microscopically dispersed or dissolved. When air is aerated using a continuous mixing and stirring apparatus in a tube, 0.6 to 1.7 parts by volume (preferably 0.8 to 1.6 parts) is added to 100 parts by weight of soymilk.
It is appropriate to blow the gas of the volume part). In addition, weight
Parts by volume are liters for kg and gram for g
Means cc or milliliter. Expressed using another index, the amount of dissolved oxygen in soymilk after aeration is 3.0 mg / l to 5.8 mg / l (preferably 3.1 mg / l to 5.7 mg / l) is appropriate. It is. When calculated from the equation of V = W * 22.4 * M, the dissolved oxygen amount is 2.1 ml / liter-4.0 ml / liter (preferably 2.2 ml / liter-3.9 ml / liter). Appropriate. The amount of dissolved oxygen when air is included is suitably the above value, but the total amount of dissolved air such as dissolved nitrogen as an air component is more than this value. If the ratio of microscopically dispersed components is large, the amount of air contained is approximately 5 times the amount of dissolved oxygen, approximately 10.5 ml / liter-
20.0 ml / liter (preferably 11.0
(Milliliter / liter-19.5 milliliter / liter) is appropriate, and when the ratio of the dissolved state is large, the value may be smaller than this due to the dissolution ratio of nitrogen. Even when other gases are used, a gas having a higher solubility in water, such as carbon dioxide gas, is taken into consideration to contain more gas than the air amount (for example, using a continuous mixing and stirring device in a tube). This is effective for forming an air-containing state dispersed in the air. [0007] As the air content increases, the dough elongates when the dough is fried and fried, the elongation of the dough is limited and the elongation is reduced. It becomes like a tissue. If the air content is too low, the dough is too stretched. On the other hand, if the air content is too high, the dough elongates poorly and is unsuitable. The type of gas to be aerated is not particularly limited as long as there is no toxicity such as air, nitrogen gas, carbon dioxide gas, and inert gas. What is necessary is just to agitate the soy milk vigorously in the presence of gas as the aeration means. A known gas-liquid mixing apparatus can be used in a batch system or a continuous system, but a continuous system is preferable for industrially containing a certain amount of gas. In a batch system, for example, a large amount of air can be easily contained by high-speed stirring such as cavitation, but it is not easy to adjust the mixture so as to keep the air content constant. In the continuous type, a gas can be blown while stirring and mixing while flowing soymilk in the tube to be aerated. The so-called continuous mixing and stirring in a tube is preferable, and the air content can be easily adjusted by adjusting the concentration and temperature of the soymilk and adjusting the amount of gas to be blown while keeping the flow rate constant. Usually, it is appropriate to blow 0.6-1.7 volume parts (preferably 0.8-1.6 volume parts) of gas to 100 parts by weight of soymilk flowing in the tube. In order for the gas to be evenly and finely dispersed and contained in the soymilk, it is more preferable that the gas is blown into the soymilk flowing into the tube, divided, inverted, and continuously mixed and stirred while being inverted. For coagulating the aerated soy milk of the present invention, a known coagulant can be used, but among them, Mg chloride is preferred because soft fried food can be obtained. More preferably, the combined use of Mg chloride and Ca chloride has a soft and preferable texture of the fried food, which allows the fried dough to be dewatered to be formed well by dehydration press molding. For example, when Ca chloride is used, the dough after dehydration pressing becomes harder, so the drainage becomes better, but the texture of the fried food obtained becomes harder, or the surface becomes harder, and the hot water restorability tends to deteriorate. Can be seen. With Mg chloride alone, fried food with a soft texture can be obtained, but in terms of workability, the drainage of the dewatered dough tends to be poor and the production efficiency tends to decrease. Mg chloride and C chloride
The combination of “a” is appropriate, and the combination of Mg chloride and Ca chloride can provide a deep-fried fried food with a good texture, and the dewatered dough drains well to improve production efficiency. In addition, Ca carbonate can be added to soymilk as required. The addition of Ca carbonate tends to promote the fried food obtained. The solidified tofu curd is crushed and dewatered and pressed to remove whey components and to form. The crushing means is used for breaking the card to facilitate dehydration, and any known means can be used. Molding conditions can be set in consideration of elongation according to the desired frying. Although the moisture content of the dehydrated molded product differs depending on the amount of the coagulant and the manufacturing process conditions (heating, etc.), it is sufficient that the dough can be molded. The dewatered molding is fried. A fryer generally known in the industry can be used for frying, and it is free to use a device such as a distributing means at an introduction portion to the fryer.
The frying conditions vary depending on the size of the molded dough, but are not particularly limited as long as the dough is appropriately stretched and forms a fine sponge-like structure. 220 ° C. or less is usually appropriate if the size is of the order of fried for commercial instant foods. In the frying mode, it is preferable to provide a temperature gradient (for example, 60 ° C.-180 ° C.) by two or more stages of fry than one stage. Usually, the fried product obtained industrially can be cooled, frozen, retorted, seasoned or dried, etc. as appropriate according to the purpose, and can be sorted, packaged, etc. to obtain a product. An embodiment of the present invention will be described below with reference to an example. Example 1 (Study of air content) 100 parts by weight (hereinafter referred to as "part") of soybeans were immersed in a sufficient amount of water for 20 hours, and drained to obtain 220 parts of immersed soybeans. 35 parts of water was added to 15.6 parts of the immersed soybeans, and ground using a grinder (manufactured by Nagasaki Kikai Co., Ltd.) to obtain go.
This go is heated with live steam (40 seconds at 96 ° C.),
After adding 6 parts, okara squeezing machine (manufactured by Takai Manufacturing Co., Ltd .: 1)
Separate the okara using 20 mesh) soy milk (concentration 4
(Bx, product temperature 71 ° C.) 21.3 parts were obtained. This soy milk 100
Using a static mixer N30 type (manufactured by Noritake Co., Ltd.), air is evenly introduced into the soymilk so that the amount of air mixed per part becomes as shown in Table 1. Then, 5.63 parts of MgCl 2 is added, and the solidified soymilk is split. Crushed, crushed and pressed using a continuous fried dough forming apparatus (manufactured by So-A Machine Co., Ltd.) to separate and dehydrate whey and simultaneously form (62 mm * 49)
mm * 7mm) and flyer (Soae Machine Co., Ltd.)
The first stage was fried at 60 ° C. and the second stage at 120 ° C., and cooled to a product temperature of 20 ° C. to obtain oil fried. Table 1 shows the obtained elongation of frying and the state of the structure.
In addition, in order to measure the air content of the soymilk after air mixing, we asked Daiwa Environmental Analysis Center Co., Ltd. to measure the dissolved oxygen (unit: mg / liter). The results are shown in Table 1.
The relationship between the weight ratio (W) of dissolved oxygen per liter of soy milk and the volume ratio (V) is V = W * 22.4 * M.
M is the molecular weight of gas and oxygen is 32. [Table 1] 空 気 Air volume Frying elongation Tissue Dissolved oxygen content ────────────────────────────────── 0 Excessive elongation with voids 2.6 1.86 (capacity part) Coarse spongy tissue (mg / l) (ml / l) Hard glassy surface. ───── 0.54 Excessive elongation with voids 2.9 2.08 (volume) spongy tissue (mg / l) (ml / l) ────────────── 1.0 1.08 Slightly stretched Sponge-like tissue 3.4 2.44 (Volume) Past (mg / l) (ml / l)- -------------------------------------------------- ----------- 1.53 Good elongation sponge 4.2.01 (volume part) (mg / l) (ml / l) ──────────────────────────── ────── 1.80 Insufficient elongation Sponge-like tissue 5.7 4.09 (volume part) (mg / l) (ml / l) ──────────────── [0012] As can be seen from the results in Table 1, if the air content is too small, the structure is too elongated and voids are formed, resulting in a coarse spongy structure. The hot water restoration property also deteriorated. On the other hand, if the air content is too large, the structure becomes fine sponge, but the elongation of the dough is insufficient. When the air permeability exceeds 100 parts by volume of soy milk (4Bx) and exceeds 0.54 parts by volume, the fried dough obtained by frying the obtained dough has an appropriate elongation and a fine sponge-like structure. It was also excellent in restoring hot water after drying it. The dissolved oxygen amount at this time exceeds 2.08 ml / liter and is 4.0
It was over 9 milliliters / liter. Although the air content depends on the dissolved ratio of nitrogen and the like, it was predicted to be about 5 times assuming 100%. Example 2 (Study of coagulant) The amount of air mixed per 100 parts of soymilk obtained in the same manner as in Example 1 was set to 1.53 parts in Table 1 and aerated as in Example 1. As shown in Table 2, the combination and amount of coagulant (the amount added to soymilk as in Example 1) was changed in place of Mg chloride in Example 1, and the subsequent steps were fried as in Example 1. Obtained. The results are shown in Table 2. [Table 2] Ca Ca chloride Mg chloride Dehydrated dough and fried Status------------------------------------------------- -------------- 5.63 parts 0 The drainage of the dough after dehydration pressing is good, but the texture of the fried food is hard. ────────────────────────────────── 2.81 parts 2.82 parts Good drainage after dewatering press The texture of the fried food was also soft. 0 5.63 parts Dehydration press The texture of the fried food was soft, although the draining of the dough was poor. As can be seen from Table 2, the dough dehydrated and pressed with Ca chloride alone was hard and drained well, but the obtained deep-fried fried food was hard (particularly a hard surface) and a soft texture was not obtained. On the other hand, the texture was soft and good even with Mg chloride alone, but the dough after dehydration pressing was soft and the drainage tended to be poor. By using Ca chloride and Mg chloride in combination, the hardness of the dough after the dehydration press became appropriate, the drainage was good, and the fried food with a soft texture was obtained. According to the present invention, it is possible to fry the soybean-derived soybean with a fine structure, which has a fine structure, is excellent in soybean-derived flavor, and has a sufficient elongation of the dough . Things. In addition, dry oil fried food with excellent hot water recovery
Is made possible.
───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 昭52−38052(JP,A) ────────────────────────────────────────────────── ─── Continuation of front page (56) References JP-A-52-38052 (JP, A)
Claims (1)
いて、豆乳100Kgに対し0.6〜1.7リットルの
気体を吹き込んで含気させて凝固した油揚生地を調製し
フライ後乾燥することを特徴とする乾燥油揚げの製造
法。(57) [Claims 1] In the step of producing dried oil fried from whole soybeans, 0.6-1.7 liters of gas is blown into 100 kg of soymilk to aerate and coagulate . the frying dough preparation
A method for producing dried oil fried, comprising drying after frying.
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JP15432992A JP3457015B2 (en) | 1992-05-20 | 1992-05-20 | Production method of fried food |
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JP3457015B2 true JP3457015B2 (en) | 2003-10-14 |
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KR100320091B1 (en) * | 1999-06-03 | 2002-01-10 | 최효광 | Soft fried bean curd and processing method thereof |
KR100335156B1 (en) * | 1999-06-04 | 2002-05-04 | 최경문 | Raw fried bean curd and processing method thereof |
JP4789736B2 (en) * | 2006-07-27 | 2011-10-12 | 株式会社高井製作所 | Fried dough regeneration method and continuous production equipment for fried dough |
JP5615662B2 (en) * | 2010-10-19 | 2014-10-29 | 株式会社小菱屋 | Method for producing fried tofu products |
JP5604364B2 (en) * | 2011-04-28 | 2014-10-08 | 株式会社高井製作所 | Fried dough remanufacturing method and fried dough continuous manufacturing device |
JP5750678B2 (en) * | 2013-03-06 | 2015-07-22 | 株式会社高井製作所 | Continuous production method of fried dough and continuous production apparatus of fried dough |
JP7207953B2 (en) * | 2018-11-02 | 2023-01-18 | 日清食品ホールディングス株式会社 | Method for producing dried fried tofu |
JP7207988B2 (en) * | 2018-12-19 | 2023-01-18 | 日清食品ホールディングス株式会社 | Deep-fried dried whole soybeans |
CN112006111A (en) * | 2020-09-27 | 2020-12-01 | 山东冠珍轩豆制食品有限公司 | Preparation process of fried bean curd |
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