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JP2009125063A - Vacuum heating equipment with defoaming function, and superheated steam generator - Google Patents

Vacuum heating equipment with defoaming function, and superheated steam generator Download PDF

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JP2009125063A
JP2009125063A JP2007307138A JP2007307138A JP2009125063A JP 2009125063 A JP2009125063 A JP 2009125063A JP 2007307138 A JP2007307138 A JP 2007307138A JP 2007307138 A JP2007307138 A JP 2007307138A JP 2009125063 A JP2009125063 A JP 2009125063A
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heating
liquid
kettle
steam
superheated steam
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Setsuo Shinkai
節夫 新開
Kenji Shinkai
健司 新開
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a manufacturing equipment for a safe product having flavor and body, stabilizing a component concentration without adding a defoaming agent, and completely removing uncomfortable odor, in view of the point that a heating method of slurry-like, emulsion-like, or liquid treatment liquid cannot stabilize a component concentration, completely remove uncomfortable odor, or make flavor and body satisfactory. <P>SOLUTION: This manufacturing equipment for the stable product having flavor and body includes bringing slurry-like, emulsion-like, or liquid treatment liquid into contact with superheated steam of 100°C-550°C, and lessening generation of bubbles to make a component concentration unchanged, with a heating boiler which is attached with a decompressable and compressable sealing-type cover, and in which a stirrer and a suction apparatus exist. Furthermore, the manufacturing equipment includes setting a ripening process in a final stage through jetting superheated steam and bringing the treatment liquid into contact directly therewith in a short time with a sealing-type heating jacket double boiler attached with a stirrer and a suction apparatus. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

本発明は、一般に前記処理液を加熱する場合には、泡が発生して、溶液に含有するために品質が劣化することがある。そのために前記処理液を加熱する場合に消泡剤を添加せずに、成分濃度を安定化して、しかも殺菌作用を施して食品衛生上で解決している前記処理液の加熱における装置に関する。   In general, in the present invention, when the treatment liquid is heated, bubbles are generated, and the quality may deteriorate due to inclusion in the solution. Therefore, the present invention relates to an apparatus for heating the processing liquid which is stabilized in food hygiene by stabilizing the component concentration without adding an antifoaming agent when heating the processing liquid and applying a bactericidal action.

例えば豆乳は健康食品であることから、最近需要が伸びている。その為、消費者から安全性、衛生面等が厳しくなり出来るだけ添加物を使用しない方が良いとの声も強く、消費者、あるいは生活協同組合等でも無添加を望まれている。
従来の加熱方法においては、開放型では泡が吹き出す為又、吹き出さない様にするには、複雑な構造で能力も少量で作業効率が悪いものであった(特許文献1参照)。
For example, soy milk is a health food, so demand has recently increased. For this reason, there is a strong voice from consumers that it is better not to use additives as much as possible in terms of safety, hygiene, and the like, and consumers or consumer cooperatives are demanding no additives.
In the conventional heating method, bubbles are blown out in the open type, and in order not to blow out, the work efficiency is poor with a complicated structure and a small capacity (see Patent Document 1).

スラリー状、乳液状、液状等の処理液を高温で処理する上で一番の問題は、前記処理液をどのようにして焦げ付かせることなしに、また、前記処理液の有効成分に影響を与えることなしに完全に不快臭を除去するとともに、香ばしさと深いコクを付与することができるかということである。さらに前記処理液の加熱においては泡の発生があり、気泡などが製品に混入するために、消泡剤などを使用することが多い。しかし添加物の含有という点で好まれない。   The biggest problem in processing a slurry, emulsion, liquid, etc. at high temperature is that the process liquid is not burned and the active ingredients of the process liquid are affected. It is whether it is possible to completely remove the unpleasant odor without giving it, and to add fragrance and deep body. Furthermore, in the heating of the treatment liquid, bubbles are generated, and bubbles and the like are mixed into the product. Therefore, an antifoaming agent is often used. However, it is not preferred in terms of inclusion of additives.

この問題を解決するため、加熱釜に攪拌機を使用することで解決策が検討されて来たが、十分な解決方法をもたらしていない。また豆乳等の製品においても、香ばしさと深いコクを十分に与えることができる処理法はなお満足すべきものが得られていないのが現状である。したがって、消泡剤の添加がなされているのが現状である。
またスラリー状、乳液状、液状等の処理液の加熱装置として、ジャケット付き、あるいは蒸気噴射装置付き又、泡を吸引して羽根車による消泡が提案されているが、泡の発生、あるいは原料本来の味を引き出し、高温での温度の均一化については問題を残している(特許文献3,4,5,7参照)
In order to solve this problem, a solution has been studied by using a stirrer in a heating kettle, but it does not provide a sufficient solution. In addition, even in products such as soy milk, there is not yet a satisfactory treatment method that can provide sufficient aroma and deep body. Therefore, the present condition is that an antifoaming agent is added.
In addition, as a heating device for processing liquid such as slurry, emulsion, liquid, etc., a jacket or a steam injection device has been proposed. Also, defoaming by impellers by sucking bubbles has been proposed. The original taste is drawn out, and there remains a problem with temperature uniformity at high temperatures (see Patent Documents 3, 4, 5, and 7).

又、温度の均一化の為にジャケット付二重釜が使用されているがジャケット部の間接加熱のみでは時間が掛かり、作業性が悪く、製品によっては長時間加熱の場合には使用できない。特に呉汁の場合、長時間になるとこげを生じる為、間接加熱のみでは不適当である。(特許文献6参照)   In addition, a double hook with a jacket is used to make the temperature uniform, but it takes time only by indirect heating of the jacket portion, the workability is poor, and some products cannot be used when heating for a long time. In particular, in the case of kure soup, indirect heating alone is inappropriate because it causes burns over a long period of time. (See Patent Document 6)

特開2000−228970号JP 2000-228970 A 特開平11−89722号JP-A-11-89722 特開平5−268900号JP-A-5-268900 特開昭58−1936668号JP 58-19936668 特開2001−054364号JP 2001-054364 A 特開昭63−141557号JP-A-63-141557 特開2003−235489号JP 2003-235490 A

従来、豆乳などの製造においてスラリー状、乳液状、液状等の処理液を加熱する際に、泡発生に対して多くの消泡剤(品質改良剤)等を使用している。そのために原料本来の味を引き出すことが困難である。
また豆乳と卯の花の製造装置において呉汁を加熱する釜が提案されているが、呉汁の泡の発生を防ぐこと、豆乳濃度が不安定で不快臭(青臭み)を、なお完全に除去出来なかったことと、香ばしさとコクを満足できずにいた点に鑑み、また一般におから卯の花は豆腐製造のお荷物となり、産業廃棄物として処分されていたが、近年用途の見直しなどによって卯の花の需要の伸びが期待されるようになってきた。しかし卯の花の本来の特性である腐敗に対する懸念があり、卯の花として製品の安定、日持ちのよい装置を開発することが要請されている。さらに加熱時に泡が発生しないような装置も期待されている。
Conventionally, many antifoaming agents (quality improving agents) or the like are used for foam generation when heating a slurry, emulsion, liquid, or other treatment liquid in the production of soymilk or the like. Therefore, it is difficult to bring out the original taste of the raw material.
In addition, a kettle that heats kure soup in the soy milk and camellia flower production apparatus has been proposed, but the generation of boiled soup bubbles was prevented, and the concentration of soy milk was unstable and unpleasant odor (blue odor) could not be completely removed In view of the fact that the fragrance and richness could not be satisfied, and in general, the okara camellia flowers were used as luggage for tofu production and were disposed of as industrial waste. Has come to be expected. However, there is concern about the spoilage that is the original characteristic of camellia flowers, and there is a need to develop a device that is stable and has a long shelf life. Furthermore, an apparatus that does not generate bubbles during heating is also expected.

本発明は成分濃度を安定させ、スラリー状、乳液状、液状等の処理液の加熱の際に通常使用されている消泡剤を添加せずに、泡の発生を少なくする装置によって、製品から完全に不快臭を除去するとともに、香ばしさとコクのある安全な製品の製造装置を提供することを課題としている。   The present invention stabilizes the component concentration and removes bubbles from the product by adding an antifoaming agent that is usually used when heating a treatment liquid such as slurry, emulsion, or liquid. An object of the present invention is to provide an apparatus for producing a safe product that completely removes an unpleasant odor and is fragrant and rich.

消泡剤等を使用せず、調味たれや飲料水や醤油、乳製品や発酵製品などスラリー状、乳液状、液状等の処理液を加熱する為には、温度を上げ前記処理液中の泡と処理液を分離し易くし、空気と不快臭を加熱釜より排出しながら炊き上げ設定温度より圧力をかけて、発生した泡成分を完全加熱して消去することである。それによって安全な原料本来の美味しく、コクのある製品が得られる加熱装置を提案するものである。
本発明では、前記処理液を加熱釜に入れて直接加熱と間接加熱(ジャケット部より)をし、同時に撹拌機を回し、吸引装置により吸引を始める。そのとき釜を密閉にして真空状態で加熱する。設定温度になると吸引装置を止めて熟成を(1分から10分前後)行う。
同じように前記処理液を加熱釜に入れて直接加熱と間接加熱(ジャケット部より)をし、同時に撹拌機を回し、設定温度(80℃前後)になるまで開放炊きをする。その後加熱のみを止め、密閉にし、吸引装置により真空引きを始める。設定時間後、再び加熱を始め、設定温度2になると吸引装置を止め、開放又は密閉にて熟成(煮込み)を(1分から10分前後)行う。
In order to heat processing liquids such as seasonings, drinking water, soy sauce, dairy products and fermentation products without using an antifoaming agent, etc., the temperature is increased and bubbles in the processing liquid are increased. And the processing liquid is easily separated, and pressure is applied from the set temperature while discharging air and unpleasant odor from the heating kettle, and the generated foam component is completely heated and erased. By doing so, we propose a heating device that provides a safe and delicious raw material.
In the present invention, the treatment liquid is put into a heating kettle and directly heated and indirectly heated (from the jacket portion), and at the same time, the agitator is turned and suction is started by a suction device. At that time, the kettle is sealed and heated in a vacuum state. When the set temperature is reached, the suction device is stopped and aging is carried out (around 1 to 10 minutes).
Similarly, the treatment liquid is put into a heating kettle and directly heated and indirectly heated (from the jacket portion), and at the same time, the stirrer is turned and cooked open until the set temperature (around 80 ° C.) is reached. Thereafter, only heating is stopped, the container is sealed, and evacuation is started by a suction device. After the set time, heating is started again, and when the set temperature reaches 2, the suction device is stopped, and aging (simmering) is performed by opening or closing (around 1 to 10 minutes).

本発明では、前記処理液は、間接的、及び直接的な加熱できる加熱釜にて、撹拌と真空吸引の操作を行いながら100℃から550℃の過熱蒸気で直接に接した後、加温の最終段階で熟成する時間を1分から20分間設ける。とくに前記処理液を密閉式の加熱ジャケット付二重釜にて、密閉状態で100℃から550℃の過熱蒸気に直接に接し、最終段階で熟成工程を設けている。特に撹拌と真空吸引の操作をすることが重要である。最終の熟成工程は75℃から130℃で、1分から10分間程度が望ましい。   In the present invention, the treatment liquid is heated directly after being contacted with superheated steam at 100 ° C. to 550 ° C. while performing stirring and vacuum suction operations in a heating kettle that can be heated indirectly and directly. Allow 1 to 20 minutes for aging at the final stage. In particular, the treatment liquid is brought into direct contact with superheated steam at 100 ° C. to 550 ° C. in a sealed state in a sealed double jacket with a heating jacket, and an aging process is provided at the final stage. It is particularly important to perform the operations of stirring and vacuum suction. The final aging step is 75 ° C. to 130 ° C., and preferably about 1 to 10 minutes.

スラリー状、乳液状、液状等の処理液入口より二重加熱釜内に入れ終わると、蒸気管よりジャケット部へ入り間接加熱し、さらに発射管を通じ直接加熱すると同時に、撹拌機を回転させ、上部に浮いている泡を巻き込み、処理液と泡を一緒に加熱する。設定温度に達すると撹拌と同時に釜内部の不快臭等を吸引装置により真空引きをする。そのことにより泡と処理液とが分離し易くなり、泡が消滅していく。
設定温度(85℃から98℃)になる迄、充分空気及び不快臭を排出した後、吸引装置を止め吸引口を閉じて密閉にして圧力をかける。それにより、完全に炊けてない部分の泡に加熱熟成を充分にさせて、安定均一な処理液にして、加熱用蒸気と撹拌機を停止する。その後処理液排出弁を開いて処理液は、排出される。
消泡剤無添加の加熱熟成された安全均一な処理液になり原料本来の美味しい製品を得ることが出来る。
When the slurry is filled into the double heating kettle from the treatment liquid inlet such as emulsion, liquid, liquid, etc., it enters the jacket part from the steam pipe and indirectly heats, further heats directly through the launch pipe, and at the same time rotates the stirrer, Entrain the floating bubbles in and heat the treatment liquid and the bubbles together. When the set temperature is reached, an unpleasant odor inside the kettle is evacuated by a suction device simultaneously with stirring. As a result, the bubbles and the processing liquid are easily separated, and the bubbles disappear.
Air and unpleasant odor are sufficiently discharged until the set temperature (85 ° C. to 98 ° C.) is reached, the suction device is stopped, the suction port is closed, and the pressure is applied. Thereby, the heat aging is sufficiently performed on the foam which is not completely cooked to obtain a stable and uniform treatment liquid, and the heating steam and the stirrer are stopped. Thereafter, the processing liquid discharge valve is opened to discharge the processing liquid.
It becomes a safe and uniform treatment liquid that has been heat-aged without the addition of an antifoaming agent, and the original delicious product can be obtained.

本発明では、消泡対応の安定した製品の製造装置において、過熱蒸気噴射管を内部に設置した撹拌機と吸引装置付加熱二重加熱釜(ジャケット付)と、100℃から550℃の過熱蒸気を発生させる過熱蒸気発生装置とからなる製造装置である。
過熱蒸気噴射管を内部に設置した撹拌機と吸引装置付加熱釜は、過熱蒸気噴射管を底部位置に設置しており、100℃から550℃の過熱蒸気を発生させる過熱蒸気発生装置は、低圧の水蒸気をパイプ式配管内に通して、外部から加熱装置によって100℃から550℃の過熱蒸気にすることができる装置である。
高温水蒸気発生装置は低圧の水蒸気を配管内に通して外部からの高温加熱であって、当該の配管内で低圧水蒸気を所定温度の蒸気になるようにしている外部加熱装置による高温蒸気を発生させる。
According to the present invention, in a stable product manufacturing apparatus capable of defoaming, an agitator with a superheated steam injection pipe installed therein, a suction device additional heat double heating kettle (with a jacket), and a superheated steam at 100 ° C. to 550 ° C. It is a manufacturing apparatus which consists of a superheated steam generator which produces | generates.
The stirrer and suction device additional heat kettle with the superheated steam injection pipe installed inside has the superheated steam injection pipe installed at the bottom position, and the superheated steam generator that generates superheated steam from 100 ° C to 550 ° C is low pressure This is a device that can pass the water vapor into a pipe-type pipe and convert it from 100 ° C. to 550 ° C. by using a heating device from the outside.
The high-temperature steam generator is a high-temperature heating from outside by passing low-pressure steam through a pipe, and generates high-temperature steam by an external heating device that makes the low-pressure steam into a steam at a predetermined temperature in the pipe .

本発明では、香ばしさとコクのある安定した製品の製造装置において、過熱蒸気噴射管を内部に設置した撹拌機吸引装置付加熱二重加熱釜(ジャケット付)と、100℃から550℃の過熱蒸気を発生させる過熱蒸気噴射装置とからなる製造装置である。
過熱蒸気噴射管を内部に設置した撹拌機と吸引装置付加熱二重加熱釜(ジャケット付)は、外部から加熱可能な水蒸気加熱用の加熱釜であって、内部100℃から550℃の過熱蒸気を発生させることのできる過熱蒸気噴射管を底部位置に設置しており、又、撹拌機吸引装置付で100℃から550℃の過熱蒸気を発生させる過熱蒸気発生装置は、低圧の水蒸気をパイプ式配管内に通して、外部から加熱装置によって100℃から550℃の過熱蒸気にすることができるような装置である。
According to the present invention, in a stable product manufacturing apparatus with aroma and richness, an agitator suction device additional heat double heating kettle (with a jacket) having a superheated steam injection pipe installed therein, and superheated steam at 100 to 550 ° C It is a manufacturing apparatus which consists of a superheated steam injection device which generates.
A stirrer with a superheated steam injection pipe installed inside and a suction device additional heating double heating kettle (with jacket) is a heating kettle for steam heating that can be heated from the outside, and superheated steam with an internal temperature of 100 ° C. to 550 ° C. The superheated steam injection pipe that can generate steam is installed at the bottom position, and the superheated steam generator that generates superheated steam from 100 ° C to 550 ° C with a stirrer suction device is a pipe type It is an apparatus that can be passed through a pipe and can be converted into superheated steam at 100 ° C. to 550 ° C. by a heating device from the outside.

低圧の水蒸気を通すパイプ配管としては限定しないが、蛇管もしくは直管の形状のものが使用される。さらに加熱装置は通常使用されている燃焼バーナーによるか、あるいは電気加熱によって行うことができる。一般には燃焼バーナーを使用することができる。
製品の製造方法における前記した課題を解決する為、本発明は処理液を100℃から550℃の超高温に所定時間保持して不快臭を除去するとともに原料の成分を引出し香ばしさとコクのある製品、日持ちのよい製品の製造装置を提供する。
Although it does not limit as pipe piping which lets low-pressure water vapor | steam pass, the thing of the shape of a snake pipe or a straight pipe is used. Further, the heating device can be performed by a commonly used combustion burner or by electric heating. In general, a combustion burner can be used.
In order to solve the above-mentioned problems in the manufacturing method of the product, the present invention is to remove the unpleasant odor by holding the treatment liquid at an ultrahigh temperature of 100 ° C. to 550 ° C. for a predetermined time and to extract the ingredients of the raw material and to have a fragrant and rich Providing equipment for producing long-lasting products.

本発明によるスラリー状、乳液状、液状等の処理液の加熱方法においては、前記処理液を100℃から550°Cの超高温に所定時間保持する処理を行うが、その高温の程度とその高温への保持時間を適正に選定することにより、原料の焦げ付きを適度に抑えて所望の香ばしさやコクを付与することができる。   In the method for heating a slurry, emulsion, liquid or the like treatment liquid according to the present invention, the treatment liquid is treated at a super high temperature of 100 ° C. to 550 ° C. for a predetermined time. By appropriately selecting the holding time, it is possible to moderately suppress the burning of the raw material and to impart a desired fragrance and richness.

本発明によるスラリー状、乳液状、液状等の処理液の加熱方法において、前記処理液を100℃から550℃の過温に保持するための熱源として、過熱水蒸気を採用すると、過熱蒸気の熱量の顕熱は僅かであるため、原料の焦げ付きは一部生ずるにすぎない。この一部の焦げ付きと高温加熱での接触処理が製品へ好ましい香ばしさとしての味覚を付与し深いコクを感ずる、日持ちのよい製品となるのである。   In the method for heating a slurry, emulsion, liquid or the like treatment liquid according to the present invention, when superheated steam is used as a heat source for maintaining the treatment liquid at an overtemperature of 100 ° C. to 550 ° C., the amount of heat of the superheated steam is increased. Since the sensible heat is negligible, only part of the raw material is burnt. This partial burning and contact treatment with high-temperature heating give the product a favorable aroma and give it a long-lasting product that feels deep and rich.

加熱方法は図4の装置図に示した様に、加熱釜内部に設置した蒸気噴射管より最初低温蒸気で加熱し、その後設定温度より過熱蒸気(高温熱媒体)に切り替え設定時間及び設定温度まで加熱及び蒸し炊きをすることにより、香ばしさとコクのある製品を得ることが出来る。   As shown in the device diagram of FIG. 4, the heating method is to first heat with low-temperature steam from the steam injection pipe installed inside the heating kettle, then switch from the set temperature to superheated steam (high-temperature heat medium) until the set time and set temperature. By heating and steaming, a product with aroma and richness can be obtained.

本発明の実施例について具体的に説明する
図2に示すように、直径600mm、高さ600mmの容積170リットルの二重加熱釜(ジャケット付)に、上部からプロペラ式攪拌機と吸引装置を取り付け、上部の蓋の密閉型容器に、原料の生呉汁50kgを入れ、図4に示すような外部に1インチのステンレスのパイプ500mm径の蛇管にしたものをオイル燃焼による外部加熱バーナーで低圧水蒸気を高温加熱する加熱装置によって550℃まで過熱蒸気(550℃ 0.5Mpa)を1インチの配管を通して釜内部に設置した直径400mmに2mmの穴を下部に開けた1インチの円形パイプの図4に示すような過熱蒸気噴射管より過熱蒸気で加熱し、並行して二重加熱釜ジャケット部に水蒸気(120℃ 0.1Mpa)を入れて所定の温度98℃に加温した後、2分間蒸し炊きを行い、分離機にて豆乳と卯の花に分離した。
上記の方法で加熱された豆乳と卯の花は均一で、安定した香ばしいコクのある高品質の豆乳と卯の花を得ることが出来る
The embodiment of the present invention will be described in detail. As shown in FIG. 2, a propeller-type stirrer and a suction device are attached to the double heating kettle (with a jacket) having a diameter of 600 mm and a height of 600 mm from the top, In a sealed container with an upper lid, 50 kg of raw raw soup is put, and a 1-inch stainless steel pipe with a 500 mm diameter snake pipe is externally heated as shown in FIG. As shown in FIG. 4, a 1-inch circular pipe having a hole of 400 mm in diameter and 2 mm in the bottom is installed inside the kettle by superheated steam (550 ° C., 0.5 MPa) up to 550 ° C. through a 1-inch pipe. Heated with superheated steam from a superheated steam injection pipe, and in parallel, water vapor (120 ° C. 0.1 MPa) was put into the double heating kettle jacket portion to give a predetermined temperature of 98 After warming to perform the steamed cooked 2 minutes to separate soybean milk and UNOHANA at separator.
Soy milk and strawberries heated by the above method are uniform, and you can obtain high-quality soy milk and straw flowers with a stable and fragrant richness.

二重加熱釜(ジャケット付)に、浸積大豆20kgと水30リットルを配合し、グラインダーにて粉砕した生呉汁を生呉入口3より二重加熱釜2内にポンプ又は圧力により送り込む。設定した量を送り終ると釜を密閉にし、加熱を開始する。配管6より蒸気(熱媒体)が二重加熱釜2の内部の蒸気噴射管より生呉汁に直接加熱し、同時に配管5より蒸気(熱媒体)が二重加熱釜のジャケット部13に入り周囲より間接加熱する。
同時に撹拌機にて低速撹拌し真空吸引を始める。98℃の設定温度に到達すると、吸引を停止し、蒸気の供給量を少なくする。3分前後蒸し炊き状態にして、絞り機(分離機)で豆乳と卯の花に分離した。
A double heating kettle (with a jacket) is mixed with 20 kg of soaked soybeans and 30 liters of water, and raw koji juice pulverized by a grinder is fed into the double heating kettle 2 from the raw Kure inlet 3 by a pump or pressure. When the set amount is finished, close the kettle and start heating. Steam (heat medium) from pipe 6 is directly heated to raw soup from the steam spray pipe inside double heating kettle 2, and at the same time, steam (heat medium) enters pipe jacket section 13 from pipe 5 from the surroundings. Indirect heating.
At the same time, low-speed stirring is performed with a stirrer and vacuum suction is started. When the set temperature of 98 ° C. is reached, the suction is stopped and the supply amount of steam is reduced. Steamed for about 3 minutes, and separated into soy milk and camellia flowers with a squeezer (separator).

二重加熱釜(ジャケット付)に50kgの生呉汁を入れ、過熱蒸気(550℃ 0.5Mpa)を釜内部に設置した過熱蒸気噴射管より加熱し、並行して二重加熱釜ジャケット部に水蒸気(120℃ 0.1Mpa)を入れて98℃に加熱する。
特に詳細には、生呉汁を生呉汁入口3より二重加熱釜2内に入れ終わると蒸気管5より
ジャケット部へ入り間接加熱し、又6よりも発射管を通じ直接加熱すると同時に撹拌泡巻
込機7を回転させ、上部に浮いている泡を巻き込み呉と泡を一緒に加熱する。又、同時に吸引装置により不快臭を10−1より排出する。
Put 50kg raw soup in a double heating kettle (with jacket) and heat superheated steam (550 ° C 0.5Mpa) from the superheated steam injection pipe installed inside the kettle. (120 ° C 0.1 Mpa) is added and heated to 98 ° C.
In particular, when raw raw soup is put into the double heating kettle 2 from the raw raw soup inlet 3, it enters the jacket from the steam pipe 5 and indirectly heats it, and is heated directly through the launch pipe rather than 6 and at the same time entrains the stirring bubbles. The machine 7 is rotated, the bubbles floating at the top are entrained, and the kure and the bubbles are heated together. At the same time, the unpleasant odor is discharged from 10-1 by the suction device.

設定温度(85℃から98℃)になる迄、充分空気及び不快臭を出した後、開放弁10と吸引口10−1を閉じて圧力をかける。密閉にして、圧力をかける事により完全に炊けてない部分の泡を加熱して、さらに熟成を充分させて安定均一な煮呉にする。その後撹拌泡巻込機7を止め、呉出弁4を開き煮呉は、分離機にて豆乳とオカラに分離される。消泡剤無添加の加熱熟成された安全均一な煮呉により大豆本来の美味しい豆乳、卯の花を得る事が出来る。
二重加熱釜(ジャケット付)に50kgの生呉汁を入れ、過熱蒸気(550℃ 0.5Mpa)を釜内部に設置した過熱蒸気噴射管より加熱し、並行して二重加熱釜ジャケット部に水蒸気(120℃ 0.1Mpa)を入れて同時に撹拌機を回し、80度になるまで開放炊きをする。
その後加熱のみを止め、密閉にし、吸引装置により真空引きを始める。不快臭及び泡を排出した後、再度加熱を始め、98℃になると吸引装置を止め、開放にし、蒸気の供給量を少なくして熟成(煮込み)を3分ほどして絞り機にて豆乳、卯の花に分離した。消泡剤無添加の加熱熟成された安全均一な煮呉により大豆本来の美味しい豆乳、卯の花を得る事が出来る。
「比較例1」
Air and unpleasant odor are sufficiently produced until the set temperature (85 ° C. to 98 ° C.) is reached, and then the open valve 10 and the suction port 10-1 are closed to apply pressure. Seal and heat the part of the foam that is not fully cooked by applying pressure to further ripen it into a stable and uniform boiled rice. Thereafter, the stirring bubble wrapping machine 7 is stopped, the Kure outlet valve 4 is opened, and the boiled Kure is separated into soy milk and okara by a separator. Delicious soy milk and cocoon blossoms of soybeans can be obtained with a safe and uniform boiled rice that has been heat-aged without the addition of an antifoaming agent.
Put 50kg raw soup in a double heating kettle (with jacket) and heat superheated steam (550 ° C 0.5Mpa) from the superheated steam injection pipe installed inside the kettle. (120 ° C 0.1Mpa) is put in and the stirrer is turned at the same time, and cooked open until it reaches 80 degrees.
Thereafter, only heating is stopped, the container is sealed, and evacuation is started by a suction device. After discharging the unpleasant odor and foam, start heating again, stop the suction device when it reaches 98 ° C, open it, reduce the supply amount of steam and ripen (simmer) for about 3 minutes, Isolated on camellia flower. Delicious soy milk and cocoon blossoms of soybeans can be obtained with a safe and uniform boiled rice that has been heat-aged without the addition of an antifoaming agent.
"Comparative Example 1"

図6に示すように、直径600mm、高さ600mmの容積170リットルの加熱釜(ジャケットと撹拌機なし)に、上部の蓋の開放型容器に、原料の生呉汁50kgを入れ、図4に示すような外部に1インチのステンレスのパイプを500mm径の蛇管にしたものをオイル燃焼による外部加熱バーナーで低圧水蒸気を高温加熱する加熱装置によって500℃の過熱蒸気(550℃ 0.5Mpa)を1インチの配管を通して釜内部に設置した直径400mmに2mmの穴を下部に開けた1インチの円形パイプの図4に示すような過熱蒸気噴射管より過熱蒸気で温度98℃に加熱し呉汁の処理を行った。   As shown in FIG. 6, 50 kg of raw raw soup stock is placed in an open-type container with an upper lid in a heating pot (without a jacket and a stirrer) having a diameter of 600 mm and a height of 600 mm, and is shown in FIG. A 1-inch stainless steel pipe made into a 500 mm diameter serpentine tube is heated by a heating device that heats low-pressure steam at a high temperature with an external heating burner by oil combustion, and 500 ° C superheated steam (550 ° C 0.5Mpa) is 1 inch. A 1-inch circular pipe with a diameter of 400 mm installed in the bottom of the kettle installed in the inside of the kettle through the pipe is heated to 98 ° C with superheated steam from a superheated steam injection pipe as shown in Fig. 4 to treat the soup stock. It was.

上記の装置によって、浸積大豆20kgと水30リットルを配合し、グラインダーにて粉砕した 生呉汁を生呉入口3より攪拌機の無い加熱釜1内にポンプ又は圧力により送り込む。設定した量を送り終ると加熱を開始する。配管6より蒸気(熱媒体)が加熱釜1の内部の蒸気噴射管より生呉汁に直接加熱して98℃の設定温度に到達すると過熱蒸気の供給量を少なくし、2分前後熟成して、絞り機(分離機)で豆乳と卯の花に分離した。   Using the above apparatus, 20 kg of soaked soybeans and 30 liters of water are blended and crushed with a grinder, and the raw koji soup is fed into the heating kettle 1 without a stirrer from the ginger inlet 3 by a pump or pressure. When the set amount has been sent, heating starts. When the steam (heat medium) is heated directly from the steam injection pipe inside the heating pot 1 to the raw koji juice through the pipe 6 and reaches a set temperature of 98 ° C., the supply amount of superheated steam is reduced, and it is aged for about 2 minutes. Using a squeezer (separator), the soy milk and camellia flowers were separated.

加熱釜に50kgの生呉汁を入れ、過熱蒸気を釜内部に設置した過熱蒸気噴射管より 加熱し、並行して加熱釜部に水蒸気(120℃ 0.1Mpa)を入れて98℃に加熱する。その後、過熱蒸気の供給量を少なくし、2分前後熟成して、絞り機(分離機)で豆乳と卯の花に分離した。
本結果では、釜より泡が吹き出す。又、むら炊きになり不快臭が残る。消泡剤を使用しないと豆乳、卯の花は出来なかった。
Put 50 kg of raw koji soup in the heating kettle, heat the superheated steam from the superheated steam spray pipe installed inside the kettle, and in parallel add steam (120 ° C 0.1Mpa) to the heating kettle and heat to 98 ° C. Thereafter, the supply amount of superheated steam was reduced, and the mixture was aged for about 2 minutes and separated into soybean milk and camellia flowers with a squeezer (separator).
In this result, bubbles blow out from the kettle. In addition, it is cooked unevenly and an unpleasant odor remains. Soy milk and camellia flowers could not be made without using antifoam.

加熱釜(密閉式・ジャケットなし)攪拌機吸引装置付側面図Side view of heating kettle (sealed, without jacket) with agitator suction device 二重加熱釜(密閉式・ジャケット付)攪拌機吸引装置付側面図Double heating kettle (sealed, with jacket) Side view with agitator suction device 二重加熱釜(水蒸気と過熱蒸気の切替え)攪拌機吸引装置付側面図Double heating kettle (switching between steam and superheated steam) Side view with agitator suction device 過熱蒸気噴射部(A側面図・B平面図)Superheated steam injection section (A side view, B plan view) 過熱蒸気発生機Superheated steam generator 加熱釜(開放式・ジャケットなし)攪拌機なし側面図Heating kettle (open type, without jacket) Side view without a stirrer

符号の説明Explanation of symbols

1 加熱釜(密閉式)
2 二重加熱釜(密閉式)
3 処理液入口
4 処理液出口
5 水蒸気(熱媒体)
5-1 水蒸気入口
6 高温蒸気(熱媒体)
6-1 高温蒸気入口
7 撹拌機
8 温度センサー
9 スチームトラップ
10 開放弁
10−1吸引口
10−2吸引装置
11 過熱蒸気発生装置
12 バーナー取付口
13 二重加熱釜ジャケット部
14 加熱釜(開放式)
1 Heating pot (sealed)
2 Double heating kettle (sealed)
3 Treatment liquid inlet 4 Treatment liquid outlet 5 Water vapor (heat medium)
5-1 Steam inlet 6 High temperature steam (heat medium)
6-1 High temperature steam inlet 7 Stirrer 8 Temperature sensor 9 Steam trap 10 Release valve 10-1 Suction port 10-2 Suction device 11 Superheated steam generator 12 Burner mounting port 13 Double heating kettle jacket 14 Heating kettle (open type )

Claims (5)

調味たれや飲料水や醤油、乳製品や発酵製品などスラリー状、乳液状、液状等の処理液の加熱において、処理液の加熱装置は、真空と加圧可能な密封式開閉蓋と、液温を均一にして、液中の泡を減少させるための攪拌機と釜内を真空状態にする吸引装置を取り付けている加熱ジャケット付加熱密閉釜で、二重加熱釜内部の蒸気噴射管よりの直接加熱と二重ジャケット部よりの間接加熱することができることを特徴とする加熱処理方法。   In the heating of processing liquids such as seasoning, drinking water, soy sauce, dairy products and fermentation products, such as slurry, emulsion, liquid, etc., the processing liquid heating device includes a sealed opening / closing lid capable of applying vacuum and pressure, liquid temperature A heating jacket-added heat-sealed kettle equipped with a stirrer to reduce the bubbles in the liquid and a suction device that evacuates the kettle, and directly heated from the steam injection pipe inside the double-heating kettle And a heat treatment method characterized in that indirect heating from the double jacket portion is possible. 調味たれや飲料水や醤油、乳製品や発酵製品などスラリー状、乳液状、液状等の処理液の加熱において、処理液の加熱装置は、真空と加圧可能な密封式開閉蓋と、液温を均一にして、液中の泡を減少させるための攪拌機と釜内を真空状態にする吸引装置を取り付けている加熱ジャケット付加熱密閉釜で、二重加熱釜内部の蒸気噴射管よりの直接加熱と二重ジャケット部よりの間接加熱することができることを特徴とする消泡機能付き加熱装置。   In the heating of processing liquids such as seasoning, drinking water, soy sauce, dairy products and fermentation products, such as slurry, emulsion, liquid, etc., the processing liquid heating device includes a sealed opening / closing lid capable of applying vacuum and pressure, liquid temperature A heating jacket-added heat-sealed kettle equipped with a stirrer to reduce the bubbles in the liquid and a suction device that evacuates the kettle, and directly heated from the steam injection pipe inside the double-heating kettle A heating device with a defoaming function, characterized in that it can be indirectly heated from the double jacket portion. 請求項2において直接加熱と間接加熱が出来、釜内の前記処理液を撹拌機により撹拌しながらの吸引装置による真空引きが出来、又真空引きをしながらの加熱が出来ることを特徴とする消泡機能付き加熱装置。   In claim 2, direct heating and indirect heating can be performed, vacuuming can be performed by a suction device while stirring the processing liquid in the kettle with a stirrer, and heating while vacuuming can be performed. Heating device with foam function. 調味たれや飲料水や醤油、乳製品や発酵製品などスラリー状、乳液状、液状等の処理液の加熱において、前記処理液の加熱装置は、真空と加圧可能な密封式開閉蓋と、液温を均一にして、液中の泡を減少させるための攪拌機と釜内を真空状態にする吸引装置を取り付けている加熱ジャケット付二重密閉釜と、100℃から550℃の水蒸気を噴射させることのできる高温水蒸気発生装置とからなることを特徴とする消泡機能付き加熱装置。   In heating of processing liquids such as seasoning, drinking water, soy sauce, dairy products and fermented products, such as slurry, emulsion, liquid, etc., the processing liquid heating device comprises a sealed opening / closing lid capable of applying vacuum and pressure, liquid Injecting steam from 100 ° C to 550 ° C with a double sealed kettle with a heating jacket, equipped with a stirrer to reduce the bubbles in the liquid, and a suction device for vacuuming the kettle A heating device with a defoaming function, characterized in that it comprises a high-temperature steam generator capable of performing defoaming. 請求項4において、高温水蒸気発生装置は低圧の水蒸気を配管内に通して外部からの高温加熱であって、当該の配管内で低圧水蒸気を所定温度の蒸気になるようにしている外部加熱装置による高温蒸気を発生させることを特徴とする消泡機能付き加熱装置。
5. The high-temperature steam generator according to claim 4, wherein the low-pressure steam is passed through the pipe and is heated from outside, and the low-pressure steam is converted into steam at a predetermined temperature in the pipe. A heating device with a defoaming function, characterized by generating high-temperature steam.
JP2007307138A 2007-11-28 2007-11-28 Vacuum heating equipment with defoaming function, and superheated steam generator Pending JP2009125063A (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103654468A (en) * 2012-09-07 2014-03-26 福库电子株式会社 Electronic food processor
CN106551614A (en) * 2015-09-25 2017-04-05 佛山市顺德区美的电热电器制造有限公司 The control method of cooking apparatus
CN106580053A (en) * 2015-10-16 2017-04-26 佛山市顺德区美的电热电器制造有限公司 Low-temperature vacuum cooking equipment
CN107897690A (en) * 2017-10-20 2018-04-13 福州永乐食品有限公司 A kind of upper thread raw material stirring and dissolving fermentation equipment integrating

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103654468A (en) * 2012-09-07 2014-03-26 福库电子株式会社 Electronic food processor
CN106551614A (en) * 2015-09-25 2017-04-05 佛山市顺德区美的电热电器制造有限公司 The control method of cooking apparatus
CN106551614B (en) * 2015-09-25 2018-11-23 佛山市顺德区美的电热电器制造有限公司 The control method of cooking apparatus
CN106580053A (en) * 2015-10-16 2017-04-26 佛山市顺德区美的电热电器制造有限公司 Low-temperature vacuum cooking equipment
CN107897690A (en) * 2017-10-20 2018-04-13 福州永乐食品有限公司 A kind of upper thread raw material stirring and dissolving fermentation equipment integrating

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