JP3660884B2 - Deep-fried dough manufacturing equipment - Google Patents

Deep-fried dough manufacturing equipment Download PDF

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JP3660884B2
JP3660884B2 JP2001025064A JP2001025064A JP3660884B2 JP 3660884 B2 JP3660884 B2 JP 3660884B2 JP 2001025064 A JP2001025064 A JP 2001025064A JP 2001025064 A JP2001025064 A JP 2001025064A JP 3660884 B2 JP3660884 B2 JP 3660884B2
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coagulant
soymilk
air
soy milk
pipe
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JP2002223716A (en
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正 安田
穂 江崎
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Ako Kasei Co Ltd
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Ako Kasei Co Ltd
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Description

【0001】
【発明の属する技術分野】
本発明は、経済的に油揚げ用生地を製造できる製造装置に関する。
また、本発明は、得られた油揚げの品質が、豆乳の製造方法及び豆乳の品質に影響されない油揚げ用生地の製造装置に関する。
さらに、本発明は、凝固剤の種類等に影響されず、木目が細かく、生地に対して均一に膨張する油揚げを効率よく製造するための油揚げ用生地の製造装置に関する。
【0002】
【従来の技術】
一般に油揚げは、豆乳に凝固剤を加えて蛋白質を不溶凝集させた後、圧搾して水を切り油揚げ用生地とし、これを先ず低温の油で揚げて充分に膨張させ、高温の油で水分を蒸発させて製造される。
生地を低温で揚げる際に起こる膨張は、豆乳製造における豆乳中の溶存空気が深く係わっていることが知られている。溶存空気量が少ない場合には、生地が膨張せず、均一な組織の油揚げが製造できなかった。
そのため、豆乳の製造工程での呉汁の加熱温度を、木綿豆腐や絹ごし豆腐の場合と比べて、92℃前後と低くし、系外に逃げる空気量を少なくしたり (若炊き) 、加熱後の呉汁に加水 (戻し水) し、溶存空気量を高める等の操作が油揚げ用豆乳の製造に常用されている。しかし、加熱温度を低くした場合には、油揚げ表面 (皮) の強度が弱く、へたりやちぢみが多くみられる等の問題を生じ、戻し水を加える場合には、後工程での圧搾時間の長期化による生産性の低下、又は圧搾不足による生地強度低下による歩留まりの低下、さらには、水分のばらつきにより不均一な油揚げとなり、歩留まりが低下する等の問題があった。
【0003】
さらに、前記の方法により得た豆乳に凝固剤を加えて豆乳を凝固させるが、凝固剤を添加するまでの時間、凝固剤の添加方法、及び豆乳の撹拌方法等の豆乳の凝固条件により、豆乳の凝固状態が微妙に変化し、凝固反応が不均一となる。この結果、油ちょう時に生地は不均一な膨張を起こし、油揚げ表面 (皮) が硬くなったり、見栄えの悪い商品価値のない油揚げになり易い。
【0004】
上記問題点を解決するために、特開昭52−38052号公報では、圧縮空気を豆乳中に吹き込むと共に豆乳中に空気の泡を形成させる方法が試みられているが、この方法では均一な大きさの空気を均一に分散させることが難しく、凝固条件及び空気の泡の大きさによっては、形成された空気の泡が浮力を受け、豆乳中から減少することが起こり得る。また、特開平5−137529号公報では呉汁を高温高圧下で加熱すると共に、これにより得られた豆乳に加圧下で空気を送り込み、溶存酸素量を増加させる方法が試みられているが、この場合、溶存しない過剰の空気は豆乳中に残存する。この空気の大きさは不均一で比較的大きく、蛋白質凝固物に包含された場合、または、凝固槽等で大きな泡立ちを生じた場合には、油揚げ用生地中に大きな気泡が混入され、その生地は不均一に伸びることになり、木目の細かい油揚げは製造できない。さらに、特開平10−127248号公報では、高濃度の豆乳に空気を送給しながら凝固剤を加え、豆乳を凝固させることが試みられているが、粘度が比較的高い豆乳に空気を送給しただけでは、均一に空気を分散することができず、大きな気泡となって偏在し、上記に示したように、不均一な伸びの木目の粗い油揚げとなり易く、十分な効果は得られない。
【0005】
【発明が解決しようとする課題】
本発明は、前記のような問題点を解決すべくなされたものであって、微細な空気が均一に分散された油揚げ用生地を製造することを課題とする。
また、本発明は、得られた油揚げの品質が豆乳の製造方法及び豆乳の品質、さらには、凝固剤の種類等に影響されず、木目が細かく、生地に対して均一に膨張する油揚げ用生地を効率よく製造することを課題とする。
【0006】
【課題を解決するための手段】
本発明者は、前記課題を解決すべく鋭意研究の結果、豆乳に空気を均一に分散させる重要性に鑑み、豆乳を貯蔵する豆乳タンク、分散機、凝固剤タンク及び空気コンプレッサ−が結合された装置であって、該豆乳タンクと分散機とは、豆乳流量調節弁、豆乳供給ポンプ及び豆乳流路切換弁を有する豆乳供給管によって結合されており、該凝固剤タンクと分散機とは、凝固剤流量調節弁、凝固剤供給ポンプ及び凝固剤流路切換弁を経て分岐し、かつ分岐管には凝固剤流量調節弁及び凝固剤開閉弁を有する凝固剤供給管によって結合されており、さらに空気コンプレッサ−と分散機とは、空気流量調節弁付き空気流量計及び空気開閉弁を有する空気供給管によって結合されており、さらに豆乳凝固槽と分散機とは凝固物排出管によって結合されていることを特徴とする油揚げ用生地の製造装置によって、豆乳に空気を均一に、特に分散機中で分散した空気の径を 150μm 以下に分散させることによって上記課題を解決することができた。
【0007】
【発明の実施の形態】
以下、図1に示す本発明の油揚げ用生地の製造装置を図面を参考にして詳細に説明する。
豆乳供給部では、豆乳2は豆乳タンク1に一旦貯蔵される。次いで、この豆乳2は、豆乳を分散機3へ供給する豆乳供給管4の途中に接続された豆乳供給ポンプ5の運転により豆乳タンク1から送り出される。しかし、製造開始までは、豆乳供給ポンプ5と分散機3との間に接続された豆乳流路切換弁7により豆乳戻り管8を経て豆乳タンク1に戻される。豆乳流量は、豆乳供給管4の途中に接続された豆乳流量調節弁6により調節され、豆乳流路切換弁7を分散機3側に切り換えると、調節された流量の豆乳2が分散機3に送り出される。ここで使用される豆乳は、常法で得られる油揚げ用の豆乳が使用できるが、加熱温度、戻し水の有無等によって、制限されるものではない。
【0008】
空気供給部では、空気は、空気コンプレッサー9から豆乳供給管4に空気を供給する空気供給管10から供給され、空気供給管10の途中に接続された空気流量調節弁付き空気流量計11により、空気の流量調節を行うようにする。さらに、空気供給管10の途中には、豆乳流路切換弁7と連動する空気開閉弁12が接続されており、製造開始まで閉じた状態にある。豆乳流路切換弁7が分散機3側に切り換わると同時に空気開閉弁12は開き、予め空気流量調節弁付き空気流量計11で流量の調節がされた空気が豆乳供給管4を経て分散機3に供給される。また、豆乳流路切換弁7が豆乳戻り管8側に切り換わり、分散機3への豆乳2の供給が停止されると同時に、空気開閉弁12が閉じ、空気の分散機3への供給が停止される。空気の添加量については、乾燥豆乳固形分量100gに対して1〜100ml が好ましく、この範囲内となるように空気流量を調節する。
なお、乾燥豆乳固形分量は、豆乳を 105℃の定温乾燥機で恒量になるまで乾燥し、その残渣重量とした。
【0009】
凝固剤供給部においては、凝固剤タンク13に凝固剤溶液14が貯蔵される。凝固剤溶液14は、凝固剤タンク13から凝固剤溶液を供給する凝固剤供給管15の途中に接続された凝固剤供給ポンプ24の運転により、凝固剤タンク13から送り出されるが、製造開始までは、凝固剤供給ポンプ24と凝固剤分岐管18a及び凝固剤分岐管23bとの間に接続された凝固剤流路切換弁26により、凝固剤戻り管27を経て凝固剤タンク13に戻される。凝固剤流路切換弁26、凝固剤開閉弁17a、及び凝固剤開閉弁20bは、豆乳流路切換弁7と、連動しており、豆乳流路切換弁7が分散機3側に切り換わり、豆乳2が分散機3に送り出されると同時に、凝固剤流路切換弁26は、凝固剤分岐管18a及び凝固剤分岐管23b側に切り換わり、凝固剤開閉弁17a及び凝固剤開閉弁20bも同時に開く。凝固剤溶液14は、凝固剤分岐管18a及び/又は凝固剤分岐管23bを経て、空気供給管10と豆乳供給管4との接続部と分散機3との間の分散機3の直前の豆乳供給管4及び/又は分散機3から豆乳凝固槽21に接続する凝固物排出管22に、予め凝固剤流量調節弁25で調節された量が供給される。凝固剤分岐管18a及び凝固剤分岐管23bにそれぞれ接続された凝固剤流量調節弁16a及び凝固剤流量調節弁19bは、凝固剤分岐管18aと凝固剤分岐管23bへの凝固剤溶液の供給割合を調節するもので、凝固剤溶液の種類によって異なるようにするのが適当である。
【0010】
例えば、比較的凝固速度が遅い油脂及び/又はグリセリン脂肪酸エステル等を含む乳化型又は分散型凝固剤では、凝固剤分岐管18aからの供給が好ましく、粗製海水塩化マグネシウム、塩化マグネシウム、硫酸カルシウム、塩化カルシウム、硫酸マグネシウム、グルコノデルタラクトン、有機酸等及びこれらを2種以上複合させたものでは、凝固剤分岐管18a及び凝固剤分岐管23bの一方又は両方から供給できるが、凝固速度が比較的速い粗製海水塩化マグネシウム、塩化マグネシウム、塩化カルシウム、硫酸マグネシウム、有機酸及びこれらを多く含む複合剤については、後のプレス工程での圧搾、脱水時間を短縮する点から、凝固剤分岐管23bからの供給割合を多くするほうが好ましい。
【0011】
分散機3では、豆乳供給管4から供給される豆乳2に空気供給管10から供給される空気を 150μm 以下の大きさに分散させることが重要な要件であり、これを越える大きさの場合には、分散された空気はその浮力によって豆乳から減少し、木目の粗い不均一な油揚げとなりやすい。分散機としては、例えば、TKパイプラインホモミクサー(特殊機化工業 (株) 製)、マイルダー((株)荏原製作所製)等が使用できる。
【0012】
【実施例】
本発明の好適な一実施例を図面に従って説明する。
先ず、豆乳供給部から説明すると、豆乳製造装置により製造された豆乳2は、豆乳タンク1に供給され、一旦貯蔵される。次いで、豆乳タンク1の豆乳2は、豆乳供給管4に接続された豆乳流路切換弁7の切り換えにより、分散機3へ供給されるか、又は、豆乳戻り管8を経て豆乳タンク1に戻されるかが選択される。豆乳流路切換弁7と豆乳タンク1の間の豆乳供給管4には、豆乳タンク1から豆乳2を送り出すための豆乳供給ポンプ5と、豆乳2の流量を調節するための豆乳流量調節弁6が接続されている。
【0013】
凝固剤供給部について説明すると、凝固剤溶液14は凝固剤タンク13に貯蔵され、凝固剤タンク13の凝固剤溶液14は、凝固剤供給管15を経て凝固剤供給管15から分岐した凝固剤分岐管18a、凝固剤分岐管23bの一方又は両方から、凝固剤供給管15の途中に接続された凝固剤供給ポンプ24によって供給され、凝固剤流量調節弁25によってその流量が調節される。
凝固剤供給ポンプ24と凝固剤分岐管18a及び凝固剤分岐管23bの間の凝固剤供給管15には、豆乳流路切換弁7と連動する凝固剤流路切換弁26が接続されており、凝固剤分岐管18a、凝固剤分岐管23bの一方又は両方から、凝固剤溶液14を供給するのか、又は凝固剤溶液14を凝固剤戻り管27を経て凝固剤タンク13へ戻すのかを切り換える。
【0014】
凝固剤流路切換弁26は、豆乳流路切換弁7が分散機3側に切り換わり、豆乳2が分散機3に供給されると同時に、凝固剤分岐管18a及び凝固剤分岐管23b側に切り換わり、豆乳に凝固剤溶液14が供給される。凝固剤分岐管18aは、空気供給管10が接続する豆乳供給管4との接点と分散機3の間の分散機3の直前に接続され、その途中に凝固剤流量調節弁16aと凝固剤開閉弁17aが接続されている。
凝固剤分岐管23bは、分散機3と豆乳凝固槽21を接続する凝固物排出管22に接続され、凝固剤流量調節弁19bと凝固剤開閉弁20bが接続されている。
【0015】
凝固剤開閉弁17a及び凝固剤開閉弁20bは、豆乳流路切換弁7と連動しており、豆乳流路切換弁7が分散機3側に切り換わり、豆乳2が分散機3に供給されると同時に開き、豆乳に凝固剤溶液14を供給できる。凝固剤流量調節弁16aと凝固剤流量調節弁19bとは、それらを調節することによって、凝固剤溶液の添加位置と供給量を任意の割合で変えることができる。
分散機は、豆乳供給管4と凝固物排出管22の間に接続され、豆乳供給管4から供給された豆乳と空気供給管10から供給された空気とを、又は、豆乳供給管4から供給された豆乳と空気供給管10から供給された空気と凝固剤分岐管18aから供給された凝固剤溶液とを分散し、豆乳中の空気の径を 150μm 以下にさせるものである。
【0016】
上記装置における豆乳供給部、空気供給部、凝固剤供給部及び分散機の各弁の開閉関係は、凝固剤流路切換弁26、空気開閉弁12、凝固剤開閉弁17a、及び凝固剤開閉弁20bが、豆乳流路切換弁7と連動している。豆乳流路切換弁7を分散機3側に切り換えると、豆乳2は、豆乳供給管4を経て分散機3に供給され、同時に空気開閉弁12が開き、豆乳に空気が供給される。さらに、同時に凝固剤供給部では、凝固剤流路切換弁26は、凝固剤分岐管18a及び凝固剤分岐管23b側に切り換わり、凝固剤開閉弁17a及び凝固剤開閉弁20bは開いた状態となり、凝固剤溶液14が豆乳に供給される。分散機3に供給される豆乳と空気、又は豆乳と空気と凝固剤溶液は、分散機3内で分散された後、場合によっては、凝固剤分岐管23bから凝固剤溶液がさらに供給され、凝固物排出管22から豆乳凝固槽21に排出される。
【0017】
豆乳凝固槽21に所望量の凝固物が注がれた時点で、豆乳流路切換弁7は豆乳戻り管8側に切り換わり、これと連動した凝固剤流路切換弁26、空気開閉弁12、凝固剤開閉弁17a、及び凝固剤開閉弁20bは製造開始前の待機状態に戻る。この動作を繰り返すと、バッチ運転で製造でき、豆乳流路切換弁7を分散機3側に切換えたままで運転を行い、適当な豆乳凝固槽を使用する場合には、連続運転で製造できる。
なお、分散機3で分散された空気の径の測定は、以下の方法により行った。
図1の装置を使用し、凝固物排出管22から排出される空気の分散された豆乳を目盛り(1mm 100等分) の刻まれたスライドガラス上に採取し、採取直後にカバーガラスで覆った後、位相差顕微鏡 (オリンパス株式会社製) で分散された空気の径を測定した。
位相差顕微鏡での測定によれば、分散された空気の径が150 μm 以下の場合に、木目が細かく、生地に対して均一に膨張する油揚げを製造することができた。
【0018】
【発明の効果】
本発明によれば、油揚げの品質が豆乳の製造方法及びその品質、また、凝固剤の種類等に影響されず、木目が細かく、生地に対して均一に膨張する油揚げを効率よく製造することができ、さらに、バッチ運転及び連続運転の両方に使用でき、現行設備に容易に組み込めるという経済的利点がある。
【図面の簡単な説明】
【図1】油揚げ用生地の製造法に用いる装置の一例を示す。
【符号の説明】
1 豆乳タンク
2 豆乳
3 分散機
4 豆乳供給管
5 豆乳供給ポンプ
6 豆乳流量調節弁
7 豆乳流路切換弁
8 豆乳戻り管
9 空気コンプレッサー
10 空気供給管
11 空気流量調節弁付き空気流量計
12 空気開閉弁
13 凝固剤タンク
14 凝固剤溶液
15 凝固剤供給管
16a 凝固剤流量調節弁
17a 凝固剤開閉弁
18a 凝固剤分岐管
19b 凝固剤流量調節弁
20b 凝固剤開閉弁
21 豆乳凝固槽
22 凝固物排出管
23b 凝固剤分岐管
24 凝固剤供給ポンプ
25 凝固剤流量調節弁
26 凝固剤流路切換弁
27 凝固剤戻り管
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a manufacturing apparatus that can economically manufacture a fried dough.
The present invention also relates to a method for producing soymilk and a device for producing fried dough that does not affect the quality of the soymilk.
Furthermore, the present invention relates to a deep-fried dough manufacturing apparatus for efficiently manufacturing deep-fried fried food that is not affected by the type of coagulant and the like and has a fine grain and expands uniformly with respect to the dough.
[0002]
[Prior art]
Generally, frying is done by adding a coagulant to soy milk to insoluble agglomerate proteins, then pressing to drain water to make dough for frying, first fry it with low temperature oil and fully expand it, and then heat it with hot oil. Manufactured by evaporation.
It is known that the expansion that occurs when the dough is fried at low temperatures is deeply related to the dissolved air in the soymilk during soymilk production. When the amount of dissolved air was small, the dough did not expand, and it was impossible to produce a fried chicken with a uniform structure.
Therefore, the heating temperature of the soup in the soy milk production process is lower than around 92 ° C compared to the case of cotton tofu and silken tofu, reducing the amount of air escaping outside the system (cooking young), Operations such as hydrating (returning water) to the soup and increasing the amount of dissolved air are commonly used in the production of fried soymilk. However, if the heating temperature is lowered, the fried surface (skin) strength is weak, causing problems such as a lot of sag and itchiness. There have been problems such as a decrease in yield due to a long period of time, a decrease in yield due to a decrease in dough strength due to insufficient pressing, and a non-uniform frying due to variations in moisture, resulting in a decrease in yield.
[0003]
Furthermore, the soy milk is coagulated by adding a coagulant to the soy milk obtained by the above method. Depending on the coagulation conditions of the soy milk, such as the time until the coagulant is added, the coagulant addition method, and the soy milk agitation method, the soy milk The coagulation state changes slightly and the coagulation reaction becomes non-uniform. As a result, the dough tends to expand unevenly when oiled, and the surface (skin) of the deep-fried food becomes hard, or it is easy to be deep-fried with no good commercial value.
[0004]
In order to solve the above problems, Japanese Patent Laid-Open No. 52-38052 has attempted a method of blowing compressed air into soy milk and forming air bubbles in the soy milk. It is difficult to uniformly disperse the air, and depending on the coagulation conditions and the size of the air bubbles, it is possible that the formed air bubbles are buoyant and reduced from the soy milk. In addition, in Japanese Patent Laid-Open No. 5-137529, a method has been attempted in which the soup is heated under high temperature and high pressure, and air is supplied under pressure to the soy milk obtained thereby to increase the amount of dissolved oxygen. Excess air that is not dissolved remains in the soy milk. The size of the air is non-uniform and relatively large, and if it is included in the protein coagulum, or if large bubbles are generated in the coagulation tank, etc., large bubbles are mixed in the dough for frying. Will grow unevenly and fine fried fish cannot be produced. Furthermore, in Japanese Patent Application Laid-Open No. 10-127248, an attempt is made to coagulate soy milk by adding a coagulant while feeding air to high-concentration soy milk. However, air is fed to soy milk having a relatively high viscosity. As a result, air cannot be uniformly dispersed, and it becomes unevenly distributed as large bubbles, and as described above, it is easy to obtain deep frying of uneven grain, and a sufficient effect cannot be obtained.
[0005]
[Problems to be solved by the invention]
The present invention has been made to solve the above-mentioned problems, and an object of the present invention is to produce a deep-fried dough for which fine air is uniformly dispersed.
In addition, the present invention provides a dough for deep-fried fry, in which the quality of the obtained fried chicken is not affected by the production method of soymilk and the quality of the soymilk, and the type of coagulant, etc. It is an object to efficiently manufacture the product.
[0006]
[Means for Solving the Problems]
As a result of diligent research to solve the above problems, the present inventor has combined a soy milk tank, a disperser, a coagulant tank, and an air compressor for storing soy milk in view of the importance of uniformly dispersing air in soy milk. The soymilk tank and the disperser are connected by a soymilk supply pipe having a soymilk flow rate adjusting valve, a soymilk supply pump and a soymilk flow path switching valve, and the coagulant tank and the disperser are coagulated. Branching through a coagulant flow control valve, a coagulant supply pump and a coagulant flow path switching valve, and the branch pipe is connected by a coagulant supply pipe having a coagulant flow rate control valve and a coagulant open / close valve, and further air The compressor and the disperser are connected by an air flow meter with an air flow control valve and an air supply pipe having an air on-off valve, and the soymilk coagulation tank and the disperser are connected by a coagulum discharge pipe. The apparatus for producing dough for fried, characterized in Rukoto, uniform air into soybean milk, it was possible to solve the above problem by causing particular dispersing diameter of dispersed air to 150μm or less in a dispersion machine.
[0007]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, the manufacturing apparatus of the deep-fried dough for this invention shown in FIG. 1 is demonstrated in detail with reference to drawings.
In the soymilk supply unit, the soymilk 2 is temporarily stored in the soymilk tank 1. Next, the soy milk 2 is sent out from the soy milk tank 1 by the operation of the soy milk supply pump 5 connected in the middle of the soy milk supply pipe 4 for supplying the soy milk to the disperser 3. However, until the start of production, the soymilk flow path switching valve 7 connected between the soymilk supply pump 5 and the disperser 3 is returned to the soymilk tank 1 via the soymilk return pipe 8. The soy milk flow rate is adjusted by a soy milk flow rate adjustment valve 6 connected in the middle of the soy milk supply pipe 4, and when the soy milk flow path switching valve 7 is switched to the disperser 3 side, the adjusted soy milk 2 is supplied to the disperser 3. Sent out. As the soy milk used here, fried soy milk obtained by a conventional method can be used, but it is not limited by the heating temperature, the presence or absence of return water, and the like.
[0008]
In the air supply unit, air is supplied from an air supply pipe 10 that supplies air from the air compressor 9 to the soymilk supply pipe 4, and is connected to the air supply pipe 10 by an air flow meter 11 with an air flow rate control valve. Adjust the air flow rate. Further, an air on-off valve 12 that is linked to the soymilk flow path switching valve 7 is connected in the middle of the air supply pipe 10 and is in a closed state until the start of manufacture. At the same time when the soymilk flow path switching valve 7 is switched to the disperser 3 side, the air on-off valve 12 is opened, and the air whose flow rate is adjusted in advance by the air flow meter 11 with an air flow rate adjusting valve passes through the soymilk supply pipe 4. 3 is supplied. Further, the soymilk flow path switching valve 7 is switched to the soymilk return pipe 8 side, the supply of the soymilk 2 to the disperser 3 is stopped, and at the same time, the air on-off valve 12 is closed and the supply of air to the disperser 3 is stopped. Stopped. The amount of air added is preferably 1 to 100 ml per 100 g of dry soymilk solid content, and the air flow rate is adjusted to be within this range.
The solid content of the dried soymilk was determined by drying the soymilk with a constant temperature dryer at 105 ° C. until the weight reached a constant weight.
[0009]
In the coagulant supply unit, the coagulant solution 14 is stored in the coagulant tank 13. The coagulant solution 14 is sent out from the coagulant tank 13 by the operation of the coagulant supply pump 24 connected in the middle of the coagulant supply pipe 15 for supplying the coagulant solution from the coagulant tank 13 until the start of production. The coagulant supply pump 24 is returned to the coagulant tank 13 through the coagulant return pipe 27 by the coagulant flow path switching valve 26 connected between the coagulant branch pipe 18a and the coagulant branch pipe 23b. The coagulant flow path switching valve 26, the coagulant open / close valve 17a, and the coagulant open / close valve 20b are linked to the soy milk flow path switching valve 7, and the soy milk flow path switching valve 7 is switched to the dispersing machine 3 side. At the same time as the soy milk 2 is fed to the disperser 3, the coagulant flow path switching valve 26 is switched to the coagulant branch pipe 18a and the coagulant branch pipe 23b side, and the coagulant open / close valve 17a and the coagulant open / close valve 20b are simultaneously switched. open. The coagulant solution 14 passes through the coagulant branch pipe 18a and / or the coagulant branch pipe 23b, and the soy milk immediately before the disperser 3 between the connection part of the air supply pipe 10 and the soymilk supply pipe 4 and the disperser 3. The amount adjusted in advance by the coagulant flow rate adjusting valve 25 is supplied from the supply pipe 4 and / or the disperser 3 to the coagulated product discharge pipe 22 connected to the soymilk coagulation tank 21. The coagulant flow control valve 16a and the coagulant flow control valve 19b connected to the coagulant branch pipe 18a and the coagulant branch pipe 23b, respectively, supply ratio of the coagulant solution to the coagulant branch pipe 18a and the coagulant branch pipe 23b. It is appropriate to vary the coagulant solution type.
[0010]
For example, in an emulsification type or dispersion type coagulant containing fats and oils and / or glycerin fatty acid ester having a relatively slow coagulation rate, supply from the coagulant branch pipe 18a is preferable, and crude magnesium chloride, magnesium chloride, calcium sulfate, chloride Calcium, magnesium sulfate, glucono delta lactone, organic acid, and the like and a combination of two or more of these can be supplied from one or both of the coagulant branch pipe 18a and the coagulant branch pipe 23b. Fast crude seawater magnesium chloride, magnesium chloride, calcium chloride, magnesium sulfate, organic acids and complex agents containing many of these, from the point of shortening the pressing and dehydration time in the subsequent press step, from the coagulant branch pipe 23b It is preferable to increase the supply ratio.
[0011]
In the disperser 3, it is an important requirement to disperse the air supplied from the air supply pipe 10 into the soymilk 2 supplied from the soymilk supply pipe 4 to a size of 150 μm or less. Dispersed air is reduced from soy milk by its buoyancy, and tends to be uneven fried with coarse grain. As the disperser, for example, a TK pipeline homomixer (manufactured by Special Machine Industry Co., Ltd.), a milder (manufactured by Ebara Corporation), or the like can be used.
[0012]
【Example】
A preferred embodiment of the present invention will be described with reference to the drawings.
First, from the soymilk supply unit, the soymilk 2 produced by the soymilk production apparatus is supplied to the soymilk tank 1 and temporarily stored. Next, the soy milk 2 in the soy milk tank 1 is supplied to the disperser 3 by switching of the soy milk flow path switching valve 7 connected to the soy milk supply pipe 4 or returned to the soy milk tank 1 through the soy milk return pipe 8. Is selected. A soymilk supply pipe 4 between the soymilk flow path switching valve 7 and the soymilk tank 1 is provided with a soymilk supply pump 5 for delivering the soymilk 2 from the soymilk tank 1 and a soymilk flow rate regulating valve 6 for adjusting the flow rate of the soymilk 2. Is connected.
[0013]
The coagulant supply unit will be described. The coagulant solution 14 is stored in the coagulant tank 13, and the coagulant solution 14 in the coagulant tank 13 is branched from the coagulant supply pipe 15 through the coagulant supply pipe 15. It is supplied from one or both of the pipe 18a and the coagulant branch pipe 23b by a coagulant supply pump 24 connected in the middle of the coagulant supply pipe 15, and its flow rate is adjusted by a coagulant flow rate adjustment valve 25.
The coagulant supply pipe 15 between the coagulant supply pump 24 and the coagulant branch pipe 18a and the coagulant branch pipe 23b is connected to a coagulant flow path switching valve 26 that is linked to the soymilk flow path switching valve 7. It is switched between supplying the coagulant solution 14 from one or both of the coagulant branch pipe 18a and the coagulant branch pipe 23b or returning the coagulant solution 14 to the coagulant tank 13 through the coagulant return pipe 27.
[0014]
The coagulant flow path switching valve 26 is switched to the side of the coagulant branch pipe 18a and the coagulant branch pipe 23b at the same time that the soy milk flow path switching valve 7 is switched to the side of the disperser 3 and the soy milk 2 is supplied to the disperser 3. The coagulant solution 14 is supplied to the soy milk. The coagulant branch pipe 18a is connected immediately before the disperser 3 between the contact with the soymilk supply pipe 4 to which the air supply pipe 10 is connected and the disperser 3, and in the middle of the coagulant flow rate adjusting valve 16a and the coagulant opening / closing. A valve 17a is connected.
The coagulant branch pipe 23b is connected to a coagulum discharge pipe 22 that connects the disperser 3 and the soy milk coagulation tank 21, and is connected to a coagulant flow rate control valve 19b and a coagulant opening / closing valve 20b.
[0015]
The coagulant opening / closing valve 17a and the coagulant opening / closing valve 20b are interlocked with the soy milk flow path switching valve 7, the soy milk flow path switching valve 7 is switched to the dispersing machine 3 side, and the soy milk 2 is supplied to the dispersing machine 3. At the same time, the coagulant solution 14 can be supplied to the soy milk. By adjusting the coagulant flow rate adjusting valve 16a and the coagulant flow rate adjusting valve 19b, the addition position and the supply amount of the coagulant solution can be changed at an arbitrary ratio.
The disperser is connected between the soymilk supply pipe 4 and the coagulum discharge pipe 22 and supplies the soymilk supplied from the soymilk supply pipe 4 and the air supplied from the air supply pipe 10 or the soymilk supply pipe 4. The soy milk, the air supplied from the air supply pipe 10 and the coagulant solution supplied from the coagulant branch pipe 18a are dispersed to reduce the diameter of the air in the soy milk to 150 μm or less.
[0016]
The open / close relationship of each of the valves of the soy milk supply unit, air supply unit, coagulant supply unit and disperser in the above apparatus is as follows: coagulant channel switching valve 26, air on / off valve 12, coagulant on / off valve 17a, and coagulant on / off valve. 20 b is linked to the soymilk flow path switching valve 7. When the soy milk flow path switching valve 7 is switched to the disperser 3 side, the soy milk 2 is supplied to the disperser 3 through the soy milk supply pipe 4, and at the same time, the air opening / closing valve 12 is opened, and air is supplied to the soy milk. At the same time, in the coagulant supply section, the coagulant flow path switching valve 26 is switched to the coagulant branch pipe 18a and the coagulant branch pipe 23b side, and the coagulant on / off valve 17a and the coagulant on / off valve 20b are opened. The coagulant solution 14 is supplied to the soy milk. The soy milk and air or the soy milk and air and the coagulant solution supplied to the disperser 3 are further dispersed in the disperser 3 and, depending on the case, the coagulant solution is further supplied from the coagulant branch pipe 23b to coagulate. The product is discharged from the product discharge pipe 22 to the soymilk coagulation tank 21.
[0017]
When a desired amount of coagulum is poured into the soymilk coagulation tank 21, the soymilk flow path switching valve 7 is switched to the soymilk return pipe 8, and the coagulant flow path switching valve 26 and the air on-off valve 12 linked to this are switched. The coagulant opening / closing valve 17a and the coagulant opening / closing valve 20b return to the standby state before the start of manufacture. If this operation is repeated, it can be manufactured in a batch operation, and when the soymilk flow path switching valve 7 is switched to the disperser 3 side and the appropriate soymilk coagulation tank is used, it can be manufactured in a continuous operation.
The diameter of the air dispersed by the disperser 3 was measured by the following method.
Using the apparatus of FIG. 1, the soy milk in which air discharged from the coagulum discharge pipe 22 is dispersed is collected on a glass slide engraved with a scale (1 mm 100 equal parts) and covered with a cover glass immediately after collection. Thereafter, the diameter of the dispersed air was measured with a phase contrast microscope (manufactured by Olympus Corporation).
According to the measurement with a phase contrast microscope, when the diameter of the dispersed air was 150 μm or less, it was possible to produce a deep-fried fried chicken that has fine grain and expands uniformly with respect to the dough.
[0018]
【The invention's effect】
According to the present invention, it is possible to efficiently produce deep-fried deep-fried fry that has a fine grain and expands uniformly with respect to the dough, regardless of the quality of the deep-fried soymilk and the quality of the soymilk and the type of coagulant. Furthermore, there is an economic advantage that it can be used for both batch operation and continuous operation, and can be easily incorporated into existing equipment.
[Brief description of the drawings]
BRIEF DESCRIPTION OF DRAWINGS FIG. 1 shows an example of an apparatus used in a method for producing fried dough.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Soymilk tank 2 Soymilk 3 Dispersing machine 4 Soymilk supply pipe 5 Soymilk supply pump 6 Soymilk flow control valve 7 Soymilk flow path switching valve 8 Soymilk return pipe 9 Air compressor 10 Air supply pipe 11 Air flow meter 12 with air flow control valve Valve 13 Coagulant tank 14 Coagulant solution 15 Coagulant supply pipe 16a Coagulant flow control valve 17a Coagulant on / off valve 18a Coagulant branch pipe 19b Coagulant flow control valve 20b Coagulant on / off valve 21 Soy milk coagulation tank 22 Coagulant discharge pipe 23b Coagulant branch pipe 24 Coagulant supply pump 25 Coagulant flow control valve 26 Coagulant flow path switching valve 27 Coagulant return pipe

Claims (3)

豆乳タンクを備えた豆乳供給部、凝固剤タンクを備えた凝固剤供給部、空気コンプレッサーを備えた空気供給部及び分散機からなる油揚げ用生地の製造装置であって、
1)該豆乳タンクと分散機とは、豆乳流量調節弁、豆乳供給ポンプ及び豆乳流路切換弁を有する豆乳供給管によって結合されており、且つ、豆乳を貯蔵する豆乳タンク1と、豆乳タンク中の豆乳2を分散機3へ供給する豆乳供給管4と、豆乳供給管4の途中に接続された豆乳供給ポンプ5及び豆乳流量調節弁6と、豆乳供給ポンプ5と分散機3の途中に接続される豆乳流路切換弁7と、豆乳流路切換弁7から豆乳タンク1に接続される豆乳戻り管8からなる豆乳供給部、
2)空気コンプレッサ−と分散機とは、空気流量調節弁付き空気流量計及び空気開閉弁を有する空気供給管によって結合されており、且つ、空気コンプレッサー9から豆乳流路切換弁7と分散機3との間の豆乳供給管4に接続され、空気を供給する空気供給管10と、空気供給管10の途中に接続された空気流量調節弁付き空気流量計11及び豆乳流路切換弁7と連動する空気開閉弁12とからなる空気供給部、
3)該凝固剤タンクと分散機とは、凝固剤流量調節弁、凝固剤供給ポンプ及び凝固剤流路切換弁を経て分岐し、かつ分岐管には凝固剤流量調節弁及び凝固剤開閉弁を有する凝固剤供給管によって結合されており、且つ、凝固剤溶液を貯蔵する凝固剤タンク13と、凝固剤タンク13から凝固剤溶液14を供給する凝固剤供給管15と、凝固剤供給管15から分岐し、凝固剤流量調節弁16a及び豆乳流路切換弁7と連動する凝固剤開閉弁17aを有し、空気供給管10と豆乳供給管4との接続部と分散機3との間の分散機3直前の豆乳供給管4に接続する凝固剤分岐管18aと、凝固剤供給管15から分岐し、凝固剤流量調節弁19b及び豆乳流路切換弁7と連動する凝固剤開閉弁20bを有し、分散機3から豆乳凝固槽21に接続する凝固物排出管22に接続する凝固剤分岐管23bと、凝固剤供給管15の途中に接続される凝固剤供給ポンプ24及び凝固剤流量調節弁25と、凝固剤供給ポンプ24と凝固剤分岐管18a及び凝固剤分岐管23bとの分岐点との間に接続される豆乳流路切換弁7と連動する凝固剤流路切換弁26と、凝固剤流路切換弁26と凝固剤タンク13を接続する凝固剤戻り管27からなる凝固剤供給部、
1)豆乳供給管4から供給される豆乳に空気供給管10から供給される空気を分散せしめ、豆乳凝固槽に凝固物排出管によって結合されており、且つ、生地中に含まれる空気の径を150μm以下になし得る分散機、
からなる油揚げ用生地の製造装置。
A soymilk supply unit comprising a soymilk tank, a coagulant supply unit comprising a coagulant tank, an air supply unit comprising an air compressor, and an apparatus for producing a frying dough comprising a disperser,
1) The soy milk tank and the disperser are connected by a soy milk supply pipe having a soy milk flow rate control valve, a soy milk supply pump, and a soy milk flow path switching valve, and the soy milk tank 1 for storing soy milk and the soy milk tank A soymilk supply pipe 4 for supplying the soymilk 2 to the disperser 3, a soymilk supply pump 5 and a soymilk flow rate control valve 6 connected in the middle of the soymilk supply pipe 4, and a soymilk supply pump 5 and a distributor 3. A soymilk flow path switching valve 7 and a soymilk supply unit comprising a soymilk return pipe 8 connected to the soymilk tank 1 from the soymilk flow path switching valve 7,
2) The air compressor and the disperser are coupled by an air flow meter with an air flow control valve and an air supply pipe having an air on / off valve, and from the air compressor 9 to the soymilk flow path switching valve 7 and the disperser 3. Connected to the soymilk supply pipe 4 between the air supply pipe 10 and the air supply pipe 10 for supplying air, and the air flow meter 11 with the air flow rate control valve and the soymilk flow path switching valve 7 connected in the middle of the air supply pipe 10. An air supply section comprising an air on-off valve 12 that
3) The coagulant tank and the disperser branch through a coagulant flow control valve, a coagulant supply pump, and a coagulant flow path switching valve, and the branch pipe is provided with a coagulant flow control valve and a coagulant opening / closing valve. A coagulant tank 13 that stores the coagulant solution, a coagulant supply pipe 15 that supplies the coagulant solution 14 from the coagulant tank 13, and a coagulant supply pipe 15. Branching and having a coagulant opening / closing valve 17a linked to the coagulant flow rate control valve 16a and the soymilk flow path switching valve 7, and the dispersion between the connection part of the air supply pipe 10 and the soymilk supply pipe 4 and the disperser 3 A coagulant branch pipe 18a connected to the soymilk supply pipe 4 immediately before the machine 3, and a coagulant on / off valve 20b branched from the coagulant supply pipe 15 and interlocked with the coagulant flow rate control valve 19b and the soymilk flow path switching valve 7. Coagulating from the disperser 3 to the soymilk coagulation tank 21 A coagulant branch pipe 23b connected to the discharge pipe 22, a coagulant supply pump 24 and a coagulant flow control valve 25 connected in the middle of the coagulant supply pipe 15, a coagulant supply pump 24, a coagulant branch pipe 18a, The coagulant flow path switching valve 26 interlocked with the soy milk flow path switching valve 7 connected between the branch point of the coagulant branch pipe 23 b and the coagulation path connecting the coagulant flow path switching valve 26 and the coagulant tank 13. A coagulant supply unit comprising an agent return pipe 27;
1) The air supplied from the air supply pipe 10 is dispersed in the soy milk supplied from the soy milk supply pipe 4, and is connected to the soy milk coagulation tank by a coagulation discharge pipe, and the diameter of the air contained in the dough is Disperser that can be made 150 μm or less,
An apparatus for producing deep-fried dough.
凝固剤が、比較的凝固速度が遅い油脂及び/又はグリセリン脂肪酸エステル等を含む乳化型又は分散型凝固剤の場合は、凝固剤分岐管18aから凝固剤を供給することを特徴とする請求項1の油揚げ用生地の製造装置。 2. The coagulant is supplied from a coagulant branch pipe 18a when the coagulant is an emulsification type or dispersion type coagulant containing fats and oils and / or glycerin fatty acid ester having a relatively low coagulation rate. Equipment for deep-fried dough. 凝固剤が、凝固速度が比較的速い粗製海水塩化マグネシウム、塩化マグネシウム、塩化カルシウム、硫酸マグネシウム、有機酸及びこれらを多く含む複合剤の場合は、凝固剤分岐管23bから凝固剤の供給割合を多くすることを特徴とする請求項1の油揚げ用生地の製造装置。 In the case where the coagulant is crude seawater magnesium chloride, magnesium chloride, calcium chloride, magnesium sulfate, organic acid and a complex containing many of these, the coagulant supply rate is increased from the coagulant branch pipe 23b. The apparatus for producing a deep-fried dough according to claim 1.
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