JP2007312768A - Roast processing method and apparatus for marine alga, using superheated steam - Google Patents

Roast processing method and apparatus for marine alga, using superheated steam Download PDF

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JP2007312768A
JP2007312768A JP2006346223A JP2006346223A JP2007312768A JP 2007312768 A JP2007312768 A JP 2007312768A JP 2006346223 A JP2006346223 A JP 2006346223A JP 2006346223 A JP2006346223 A JP 2006346223A JP 2007312768 A JP2007312768 A JP 2007312768A
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superheated steam
seaweed
roasting
moving
temperature
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Keiji Otsuka
啓治 大塚
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OOTSUKA GAS ENGINEERING KK
Kyuken Corp
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Kyuken Corp
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a roast processing method for effectively roasting marine algae to bring into a good item, using superheated steam. <P>SOLUTION: This roast processing method for marine algae, using superheated steam comprises roasting while moving marine algae in forced flow atmosphere of superheated steam. <P>COPYRIGHT: (C)2008,JPO&INPIT

Description

この発明は、焼のり加工など、海藻類を焙焼加工することを目的として焙焼に際し、過熱水蒸気を用いた海藻類の焙焼加工方法及び装置に関する。   The present invention relates to a method and apparatus for roasting seaweeds using superheated steam for the purpose of roasting seaweeds such as grilling.

従来焼のりその他海藻類の焙焼加工は、炭火、電気熱、ガス熱を用い、近来は遠赤外線による焙焼が多く採用されている。   Conventional roasting of seaweed and other seaweeds uses charcoal fire, electric heat, and gas heat, and far-infrared roasting is widely used.

また過熱水蒸気は、食品加工の分野で、乾燥、洗浄、炭化、減容などに使用できることが知られているが、海藻類の乾燥は低温(40℃〜50℃)がよいとされていた為に、100℃以上の高温となる焙焼には使用されていなかった。
特許第3535062号 特公平5−74340号
It is known that superheated steam can be used for drying, washing, carbonization, volume reduction, etc. in the field of food processing, but low temperature (40 ° C to 50 ° C) is good for drying seaweeds. In addition, it was not used for roasting at a high temperature of 100 ° C. or higher.
Japanese Patent No. 3535062 Japanese Patent Publication No. 5-74340

近来高含水有機物(例えば海藻)の温風乾燥が考えられており、ボイラーによる過熱水蒸気を使用して乾燥空気を生成し、この乾燥空気を用いて海苔を乾燥させる提案がある(特許文献1)。   Recently, warm air drying of highly water-containing organic matter (for example, seaweed) has been considered, and there is a proposal of generating dry air using superheated steam from a boiler and drying the laver using this dry air (Patent Document 1). .

また乾海苔原料を、搬送装置により連続的に遠赤外線加熱装置内を通過させて焙焼する発明が提案されている(特許文献2)。   Moreover, the invention which passes the inside of a far-infrared heating apparatus continuously by a conveying apparatus and roasts it is proposed (patent document 2).

前記乾燥については、温度の均一化と乾燥速度の短縮化を達成する為に、過熱水蒸気を用いて生成した乾燥空気を使用したとされている。前記によれば生海苔の表面、裏面に乱流が発生することを抑制し、乾燥むらをなくし、品質を向上すると共に、乾燥効率のアップ、エネルギー損失を抑えて乾燥時間を短縮できるとされている。また前記乾燥空気を生海苔に接触させて乾燥することにしている。   For the drying, it is said that dry air generated using superheated steam is used in order to achieve uniform temperature and shorten drying speed. According to the above, the occurrence of turbulent flow on the front and back surfaces of fresh seaweed is suppressed, drying unevenness is eliminated, quality is improved, drying efficiency is increased, energy loss is reduced, and drying time can be shortened. Yes. The dry air is brought into contact with fresh seaweed and dried.

前記のように、生海苔の乾燥においては、温度が40℃〜50℃の温風(乾燥空気)を用いる為に、過熱水蒸気は専ら温風を得る為の熱媒体である。従って、過熱水蒸気を直接海藻類に接触させる焙焼加工とは技術分野を異にするものである。例えば生海苔の焙焼加工には、乾海苔を遠赤外線により焙焼加工する技術が提案されている(特許文献2)。   As described above, since hot air (dry air) having a temperature of 40 ° C. to 50 ° C. is used for drying fresh seaweed, superheated steam is a heat medium exclusively for obtaining hot air. Therefore, the technical field is different from roasting processing in which superheated steam is brought into direct contact with seaweed. For example, a technique for roasting dry seaweed with far infrared rays has been proposed for roasting raw seaweed (Patent Document 2).

前記のように海藻の焙焼加工に遠赤外線が用いられているが、遠赤外線の場合には、直線的照射であるから、一枚の乾燥の処理に有効であるけれども、複数枚重ねた場合には、上下不均一処理になり易く、かつ遠赤外線の照射量の不均一により、焙焼むらを生じる問題点があるので、特別の工夫を要する。また乾燥は40℃〜50℃の低温でなければならないので、過熱水蒸気を直接使用することができない問題点があった。何故ならば、過熱水蒸気は本来的に100℃の蒸気を更に過熱して生成するので、100℃以上の温度となるからである。   As mentioned above, far-infrared rays are used for seaweed roasting, but in the case of far-infrared rays, since it is a linear irradiation, it is effective for a single drying process, but when multiple sheets are stacked However, there is a problem in that uneven baking tends to occur due to unevenness in the amount of far-infrared radiation, which tends to be a non-uniform treatment in the vertical direction. Further, since drying must be performed at a low temperature of 40 ° C. to 50 ° C., there is a problem that the superheated steam cannot be used directly. This is because superheated steam is inherently generated by further heating steam at 100 ° C., resulting in a temperature of 100 ° C. or higher.

この発明は、過熱水蒸気の温度、加工時間、海藻類と過熱水蒸気との接触状態などを調整することにより、過熱水蒸気による海藻類の焙焼を良質でかつ効率よく実施することに成功したのである。   This invention succeeded in efficiently and efficiently carrying out roasting of seaweed with superheated steam by adjusting the temperature of superheated steam, processing time, contact state between seaweed and superheated steam, and the like. .

即ちこの発明は、過熱水蒸気の強制流動雰囲気内で海藻類を移動しつつ焙焼することを特徴とした過熱水蒸気を用いた海藻類の焙焼加工方法であり、110℃〜300℃の過熱水蒸気の強制流動雰囲気内で海藻類を移動しつつ焙焼することを特徴とした過熱水蒸気を用いた海藻類の焙焼加工方法であり、110℃〜300℃の過熱水蒸気の強制流動雰囲気内で海藻類を定速移動させると共に、遠赤外線を照射して焙焼することを特徴とした過熱水蒸気を用いた海藻類の焙焼加工方法である。   That is, the present invention is a method for roasting seaweed using superheated steam, which is characterized by roasting while moving seaweed in a forced flow atmosphere of superheated steam. Is a roasting method of seaweed using superheated steam characterized by roasting while moving seaweed in a forced fluid atmosphere of seawater, and seaweed in a forced fluid atmosphere of 110 ° C to 300 ° C superheated steam This is a method for roasting seaweeds using superheated steam, which is characterized in that it is moved at a constant speed and fired by irradiating far infrared rays.

次に、下記の条件により過熱水蒸気で海藻類を焙焼することを特徴とした過熱水蒸気を用いた海藻類の焙焼加工方法である。   Next, a seaweed roasting method using superheated steam characterized by roasting seaweed with superheated steam under the following conditions.

(1)過熱水蒸気の温度を110℃〜300℃とすること
(2)焼き時間を5秒〜300秒とすること
(3)海藻類の移動速度を0.5m/分〜5m/分とすること
また他の発明は、請求項1記載の方法を実施する装置であって、海藻類を焙焼する焙焼室と、該焙焼室内を通過する海藻類に向けて過熱水蒸気を吹き出す過熱水蒸気の加圧吹出手段と、前記過熱水蒸気の供給手段と、前記焙焼室内に海藻類を移動させる移動手段と、前記各手段の制御手段とを組み合わせたことを特徴とする過熱水蒸気による海藻類の焙焼加工装置であり、請求項1記載の方法を実施する装置であって、焙焼室内の中間部へ、海藻類を移動させるメッシュコンベアを横に架設すると共に、該メッシュコンベアの上方及び下方に過熱水蒸気の吹出し口を設け、前記焙焼室に、過熱水蒸気の排出口と、海藻類の供給口及び取出し口を設けたことを特徴とする過熱水蒸気による海藻類の焙焼加工装置である。
(1) The temperature of the superheated steam is set to 110 ° C. to 300 ° C. (2) The baking time is set to 5 seconds to 300 seconds (3) The moving speed of the seaweed is set to 0.5 m / min to 5 m / min. According to another aspect of the present invention, there is provided an apparatus for carrying out the method according to claim 1, wherein a roasting chamber for roasting seaweeds, and superheated steam for blowing out superheated steam toward seaweeds passing through the roasting chamber. A combination of pressure blowing means, superheated steam supply means, moving means for moving seaweeds into the roasting chamber, and control means for each means. It is a roasting processing apparatus and is an apparatus for carrying out the method according to claim 1, wherein a mesh conveyor for moving seaweed is horizontally installed in an intermediate portion of the roasting chamber, and above and below the mesh conveyor. Provided with a superheated steam outlet, An apparatus for roasting seaweed with superheated steam, characterized in that a superheated steam discharge port and a seaweed supply / extraction port are provided in the roasting chamber.

また、請求項1記載の方法を実施する装置であって、焙焼室内の中間部へ、海藻類を移動させるメッシュコンベアを横に架設すると共に、該メッシュコンベアの上方及び下方に過熱水蒸気の吹出し口を設け、前記焙焼室に、過熱水蒸気の排出口と、海藻類の供給口及び取出し口を設け、前記過熱水蒸気及び海藻類の加工条件を制御する制御器を付設したことを特徴とする過熱水蒸気による海藻類の焙焼加工装置であり、焙焼室内に、過熱水蒸気の温度を検出するセンサーを設置し、該センサーの出力を制御器に接続したものであり、過熱水蒸気の供給手段は、過熱水蒸気の供給管に給送ファンを介装したものである。   The apparatus for carrying out the method according to claim 1, wherein a mesh conveyor for moving seaweed is horizontally installed in an intermediate portion of the roasting chamber, and superheated steam is blown out above and below the mesh conveyor. Provided with a controller for controlling the processing conditions of the superheated steam and seaweed, and provided with a discharge port for superheated steam, a supply port for seaweed and a discharge port for seaweed. It is a seaweed roasting processing device using superheated steam, a sensor for detecting the temperature of superheated steam is installed in the roasting chamber, and the output of the sensor is connected to a controller. The superheated steam supply pipe is provided with a feed fan.

前記発明においては、過熱水蒸気を使用する為に、海藻類の積み重ね2枚〜数枚でも均一焙焼できるが、過不足なく焙焼する為には、温度、時間を制御する必要がある。そこで海藻類の状態に応じて、温度と時間を制御する。この場合に制御器で設定すれば、最良の状態で制御できる。温度を一定にすれば、時間制御だけであるから、操作が容易となり、容易に均質焙焼製品が期待できる。但し焙焼室の容量2m〜5mの時に、0.1L/分〜0.19L/分の過熱空気を用いて、十分の焙焼ができた。 In the invention, since superheated steam is used, even two to several seaweed stacks can be uniformly roasted, but in order to roast without excess or deficiency, it is necessary to control temperature and time. Therefore, temperature and time are controlled according to the state of seaweeds. In this case, if it is set by the controller, it can be controlled in the best state. If the temperature is kept constant, only time control is performed, so that the operation becomes easy and a homogeneous roasted product can be easily expected. However when the volume of the roasting chamber 2m 3 ~5m 3, using a 0.1 L / min ~0.19L / min superheated air, could well roasting.

この発明の方法によれば、過熱水蒸気の温度は110℃〜300℃、好ましくは120℃〜200°で自由に選定することができる。   According to the method of the present invention, the temperature of the superheated steam can be freely selected at 110 ° C. to 300 ° C., preferably 120 ° C. to 200 °.

この発明で使用するコンベアは、メッシュコンベアであって、低温(例えば150℃以下)の場合には、耐熱合成樹脂繊維よりなるメッシュを用い、高温(例えば150℃以上)になれば、ステンレスメッシュを用いる。   The conveyor used in the present invention is a mesh conveyor. When the temperature is low (for example, 150 ° C. or lower), a mesh made of heat-resistant synthetic resin fiber is used. Use.

この発明で使用する過熱水蒸気は、飽和蒸気に圧力を加えることなく加熱することにより得られる100℃以上の水蒸気のことであって、食品加工、環境設備、各種熱処理などに使用されている。然し乍ら海藻類(例えば生海苔)の加工については使用されていない。   The superheated steam used in the present invention is steam of 100 ° C. or higher obtained by heating saturated steam without applying pressure, and is used for food processing, environmental equipment, various heat treatments and the like. However, it is not used for processing seaweeds (for example, fresh seaweed).

その理由は、生海苔は、温度変化によって変質し易く、通常乾燥用の加温空気は40℃〜50℃が常識とされていた。事実上も、60℃以上の加熱は考えられなかった。また焙焼については、通常乾燥海苔が焙焼され、熱源としては電熱、炭火など輻射熱が考えられ、過熱水蒸気は考慮外であった。   The reason for this is that raw laver is easily altered by temperature changes, and it has been common knowledge that warm air for drying is usually 40 ° C to 50 ° C. In fact, heating above 60 ° C. could not be considered. As for roasting, usually dried laver was roasted, and radiant heat such as electric heat or charcoal fire was considered as a heat source, and superheated steam was not considered.

然し乍ら、過熱水蒸気(100℃以上)を使用した場合であっても、短時間の処理においては、品質を損することなく、かつ多量に処理する場合にも条件の変化が少ない状態の加工処理方法を開発し、この発明を完成したのである。   However, even when superheated steam (100 ° C. or higher) is used, a processing method in which the change in conditions is small even when processing in a large amount without damaging the quality in a short time processing. It was developed and the invention was completed.

即ちメッシュコンベアに敷き詰めて供給するような多量(一定時間内の処理量が多い)の海藻類であっても、移動中に過熱水蒸気を吹き出す雰囲気内を通過させることにより、全部同一条件の加工がされると共に、過熱水蒸気の熱容量が大きいので(図4)、同一場所における海藻類に与える熱量がほぼ一定である。従って使用過熱水蒸気の温度変化が少なく、かつ海藻類から発生する蒸気の混入により、過熱水蒸気の影響が緩和されるなど、未解明の部分も含めて好影響を与えるものと推定される。その結果一枚一枚管理して焙焼した製品以上の良質な焙焼製品(色彩、品質共に良好)ができる。   In other words, even a large amount of seaweed that is supplied on a mesh conveyor (a large amount of processing within a certain period of time) can be processed under the same conditions by passing it through an atmosphere in which superheated steam is blown during movement. In addition, since the heat capacity of superheated steam is large (FIG. 4), the amount of heat given to seaweeds in the same place is almost constant. Therefore, it is presumed that the temperature change of the superheated steam used is small, and the influence of the superheated steam is mitigated by the mixing of steam generated from seaweed, including unexplained parts. As a result, a higher quality roasted product (both color and quality is better) than products that are managed and roasted one by one.

前記発明において、過熱水蒸気の温度を110℃〜300℃とし、好ましくは120℃〜200℃としたのは、比較的短時間に、所定の品質の焙焼製品を得る為である。例えば過熱水蒸気の温度が110℃未満では、焙焼時間が長くなり、焙焼条件の均一性を失うおそれがあり、前記焙焼温度が300℃を越えると、焙焼時間が短すぎるので、均一性を害するおそれがあり、120℃〜200℃で安定しているからである。海藻類のような熱に対して敏感に変化するおそれのある材質に対しては、温度と時間に厳しく配慮する必要がある。   In the invention, the temperature of the superheated steam is set to 110 ° C. to 300 ° C., preferably 120 ° C. to 200 ° C., in order to obtain a roasted product having a predetermined quality in a relatively short time. For example, if the temperature of the superheated steam is less than 110 ° C., the roasting time becomes long, and the uniformity of the roasting conditions may be lost. If the roasting temperature exceeds 300 ° C., the roasting time is too short, so It is because there is a possibility of harming the property, and it is stable at 120 to 200 ° C. For materials that can change sensitively to heat, such as seaweeds, it is necessary to carefully consider temperature and time.

この発明によれば、過熱水蒸気を使用して加工するので、熱の伝達が良好であり、40℃〜50℃の温度の空気利用に比し、2倍〜5倍の効率が認められた。また焙焼製品は、緑色勝ちの鮮明な色彩となり、品質を向上できる効果がある。   According to this invention, since processing is performed using superheated steam, heat transfer is good, and an efficiency of 2 to 5 times as high as that of using air at a temperature of 40 ° C. to 50 ° C. is recognized. In addition, the roasted product has a clear green color and has the effect of improving quality.

またガスバーナーの先端部で水を霧化する為に、効率よく霧化すると共に、過熱し、過熱水蒸気を高い効率で製造し得る効果がある。   In addition, since the water is atomized at the tip of the gas burner, the water can be efficiently atomized and overheated to produce superheated steam with high efficiency.

この発明は主として過熱水蒸気の温度制御と、これに伴う各部の制御により、連続、かつ自動の焙焼ができる効果がある。   The present invention has an effect that continuous and automatic roasting can be performed mainly by temperature control of superheated steam and control of each part associated therewith.

この発明は、焙焼室内の中央部において、海藻類をメッシュコンベアに乗せて一方から他方へ横移動させる際に、上下から120℃〜200℃の過熱水蒸気を吹きつけて、30秒〜150秒間焙焼する。前記において、120℃ならば150秒位、200℃ならば30秒位焙焼を継続する。   In the center of the roasting chamber, when the seaweed is placed on a mesh conveyor and laterally moved from one side to the other, superheated steam at 120 ° C. to 200 ° C. is blown from above and below for 30 seconds to 150 seconds. Roast. In the above, roasting is continued for about 150 seconds at 120 ° C. and for about 30 seconds at 200 ° C.

前記方法を実施する装置は、焙焼室内へネットコンベアを横架し、該ネットコンベアの上下に、過熱水蒸気吹出しパイプを架設したものである。前記過熱水蒸気の量は、例えば0.1L/分〜0.18L/分であって、焙焼温度は120℃〜200℃を保つようにする。   In the apparatus for carrying out the method, a net conveyor is horizontally installed in the roasting chamber, and superheated steam blowing pipes are installed on the top and bottom of the net conveyor. The amount of the superheated steam is, for example, 0.1 L / min to 0.18 L / min, and the roasting temperature is maintained at 120 ° C. to 200 ° C.

この発明の実施例を図1に基づいて説明すると、焙焼すべき生海苔をメッシュコンベアにのせて焙焼室に入れると、メッシュコンベアの上下から150℃の過熱水蒸気を吹き出し、前記生海苔をメッシュコンベアに乗せたまま焙焼する。この場合に焙焼室には、センサーが設置してあって、このセンサーにより焙焼室内の過熱水蒸気の温度を検出し、その出力を制御器に入力し、この制御器で設定温度と比較する。例えば設定温度が150℃であり、センサーの検出温度が145℃の場合には、制御器によりバーナーのバルブ(図示してない)を若干開いてガスの供給量を多くして温度を高くさせる。   An embodiment of the present invention will be described with reference to FIG. 1. When raw nori to be roasted is placed on a mesh conveyor and placed in a roasting chamber, 150 ° C. superheated steam is blown out from above and below the mesh conveyor, Roast it on the mesh conveyor. In this case, a sensor is installed in the roasting chamber, the temperature of the superheated steam in the roasting chamber is detected by this sensor, the output is input to the controller, and this controller compares it with the set temperature. . For example, when the set temperature is 150 ° C. and the detected temperature of the sensor is 145 ° C., the controller increases the temperature by slightly opening the burner valve (not shown) to increase the gas supply amount.

前記に反し、設定温度が150℃であるのに対し、センサーの検出温度が160℃を示した場合には、制御器を介して、ガスバーナーのバルブを若干締めて、ガスの供給量を少なくし、燃焼エネルギーの低下から、過熱水蒸気の温度低下を図る。   Contrary to the above, when the set temperature is 150 ° C. and the detected temperature of the sensor indicates 160 ° C., the gas burner valve is slightly tightened via the controller to reduce the gas supply amount. Then, the temperature of the superheated steam is decreased due to a decrease in combustion energy.

前記はガス量を制御したが、生成過熱水蒸気の量を増減させる為に、水量を増減しても、或いは廃棄過熱水蒸気の循環量を変える(循環ファン又は煙突のダンパーによる)ことにより、混合比を変えても、前記と同様に過熱水蒸気の温度を調節することができる。   The above controls the amount of gas, but to increase or decrease the amount of superheated steam produced, the mixing ratio can be increased by increasing or decreasing the amount of water or by changing the circulation rate of waste superheated steam (by a circulation fan or chimney damper). Even if it changes, the temperature of superheated steam can be adjusted similarly to the above.

前記のように過熱水蒸気の温度制御の外に、メッシュコンベアの速度を変えて焙焼時間を調節し、最良の焙焼時間を得ることもできる。   In addition to the temperature control of superheated steam as described above, the best roasting time can be obtained by adjusting the roasting time by changing the speed of the mesh conveyor.

前記のように、所定時間焙焼すれば、水分3%以下の製品となる。また焙焼室内の過熱水蒸気は、生海苔から発生する水蒸気を含み、排気管を経てダンパー、循環ファンで過熱水蒸気と混合し、再び焙焼室へ入る。また他の場合には、焙焼排気の一部は過熱水蒸気に混合し、他部は煙突から外界へ放出される。前記割合は専らセンサーの検出値により制御器で自動制御する。   As described above, when roasted for a predetermined time, the product has a moisture content of 3% or less. The superheated steam in the roasting chamber contains steam generated from the raw laver, is mixed with the superheated steam with a damper and a circulation fan through the exhaust pipe, and enters the roasting chamber again. In other cases, part of the roasting exhaust is mixed with superheated steam, and the other part is discharged from the chimney to the outside. The ratio is automatically controlled by the controller exclusively by the detection value of the sensor.

前記において、同一条件の生海苔を同一条件で焙焼する場合は、条件が一定となるので、必ずしもセンサーを利用しなくてもよい場合もある。   In the above, when raw nori under the same conditions is roasted under the same conditions, the conditions are constant, so there is a case where it is not always necessary to use a sensor.

この発明の装置の実施例を図2、3について説明すると、焙焼室1の下部へメッシュコンベア2を水平方向に架設する。前記メッシュコンベア2の上下に過熱水蒸気の吹出パイプ3、3aを、前記メッシュコンベア2を横切る方向へ架設する。前記焙焼室1の一側上部に排気管4の基端を接続し、排気管4の先端は循環ファン5の吸入側へ接続し、循環ファン5の吸入側へは過熱水蒸気の生成室6の吐出管7も接続してある。前記過熱水蒸気の生成室6には、バーナー8の火焔が吹き込まれ、前記生成室6の上部両側に、噴霧管9が架設されている。図中19、19aは連結管、10は生海苔である。図中18は遠赤外線照射球、20は実施装置である。   2 and 3, the mesh conveyor 2 is installed in the horizontal direction below the roasting chamber 1. Superheated steam blowing pipes 3, 3 a are installed above and below the mesh conveyor 2 in a direction crossing the mesh conveyor 2. The base end of the exhaust pipe 4 is connected to one upper side of the roasting chamber 1, the tip of the exhaust pipe 4 is connected to the suction side of the circulation fan 5, and the superheated steam generation chamber 6 is connected to the suction side of the circulation fan 5. The discharge pipe 7 is also connected. A flame of a burner 8 is blown into the superheated steam generation chamber 6, and spray tubes 9 are installed on both sides of the upper portion of the generation chamber 6. In the figure, 19 and 19a are connecting pipes, and 10 is fresh seaweed. In the figure, 18 is a far-infrared irradiation sphere, and 20 is an implementation apparatus.

前記において、図3(b)中、噴霧管9から矢示11のように噴霧すると共に、バーナー8から火焔を矢示12のように吹き出すと、噴霧が瞬時に蒸発して過熱水蒸気となり、吐出管7を矢示13のように通過して、循環ファン5に入り、その吐出口から、矢示14のように連結管19を経て矢示15、15のように吹出しパイプ3、3aから上下方向へ吹出し、メッシュコンベア2上の生海苔10を焙焼する。この場合に、生海苔10は、数枚積み上げてあっても、過熱水蒸気が間に吹き込まれるので焙焼に支障なく、均等に焙焼される。   In FIG. 3 (b), when spraying is performed from the spray tube 9 as indicated by an arrow 11 and a flame is blown from the burner 8 as indicated by an arrow 12, the spray is instantaneously evaporated to become superheated steam. It passes through the pipe 7 as shown by arrow 13 and enters the circulation fan 5, and from its outlet, passes through the connecting pipe 19 as shown by arrow 14 and goes up and down from the outlet pipes 3 and 3 a as shown by arrows 15 and 15. It blows out in the direction and roasts the raw nori 10 on the mesh conveyor 2. In this case, even if several sheets of fresh seaweed 10 are stacked, superheated steam is blown in between, so that roasting is performed without any problem.

前記焙焼室1の排気は、矢示17のように、排気管4から取出され、循環ファン5に入り、再び連結管19を経て焙焼室1へ送られる。前記において、温度低下、風量不足の際は過熱水蒸気の混入量を調節する。   The exhaust of the roasting chamber 1 is taken out from the exhaust pipe 4 as shown by an arrow 17, enters the circulation fan 5, and is sent again to the roasting chamber 1 through the connecting pipe 19. In the above, the amount of superheated steam mixed is adjusted when the temperature drops or the air volume is insufficient.

前記過熱水蒸気の温度制御、供給の有無、循環ファン5の作動などは、総て制御器16の制御によるものとする。例えば、タイマー(設定できる)の出力によって、循環ファン5をON、OFFし、又はダンパー22の開閉度を定める。   The temperature control of the superheated steam, the presence / absence of supply, the operation of the circulation fan 5 and the like are all controlled by the controller 16. For example, the circulation fan 5 is turned ON / OFF or the opening / closing degree of the damper 22 is determined by the output of a timer (which can be set).

この発明の実施例を図4について説明すると、焙焼室1の中間部へメッシュコンベア2を水平方向に架設する。前記メッシュコンベア2を横切る方向(メッシュコンベア2の進行方向と直角の方向)の上下に、過熱水蒸気の吹出しパイプ3、3aを架設する。   An embodiment of the present invention will be described with reference to FIG. 4. A mesh conveyor 2 is installed in the horizontal direction on the intermediate portion of the roasting chamber 1. Superheated steam blowing pipes 3 and 3a are installed above and below the direction crossing the mesh conveyor 2 (the direction perpendicular to the traveling direction of the mesh conveyor 2).

前記焙焼室1の上部へ排気管4の基端を接続し、前記焙焼室1の上部一側へ、循環ファン5を設置し、該循環ファン5の吸入筒5aは、前記焙焼室1の上部へ水平方向に突出し、前記循環ファン5の吐出側は、前記吹出しパイプ3、3aの連結管19aに連結してある。   The base end of the exhaust pipe 4 is connected to the upper part of the roasting chamber 1, and a circulation fan 5 is installed on the upper side of the roasting chamber 1, and the suction cylinder 5a of the circulation fan 5 is connected to the roasting chamber. 1, the discharge side of the circulation fan 5 is connected to the connection pipe 19a of the outlet pipes 3 and 3a.

前記焙焼室1の外側壁に、過熱水蒸気の生成室6を設置し、該生成室6の吐出口6aを、前記連結管19aに開口させる。また前記生成室6の一側に、噴霧管9を有する高圧給水管9aと、ガスバーナー8とを近接して設置し、生成室6の下側に、給気ファン24の吐出口24aを開口し、装置20を構成する。図中25は点火プラグ、26、27はモータである。   A superheated steam generation chamber 6 is installed on the outer wall of the roasting chamber 1, and a discharge port 6a of the generation chamber 6 is opened to the connecting pipe 19a. Further, a high-pressure water supply pipe 9 a having a spray pipe 9 and a gas burner 8 are installed close to one side of the generation chamber 6, and a discharge port 24 a of an air supply fan 24 is opened below the generation chamber 6. The apparatus 20 is configured. In the figure, 25 is a spark plug, and 26 and 27 are motors.

前記実施例において、高圧給水管9aから加圧水を給送し、噴霧管9から矢示11のように噴霧すると共に、ガスバーナー8の火焔を矢示12のように吹き出すと、生成室6内では、過熱水蒸気が生成され、矢示13、13のように連結管19aを介し、吹出しパイプ3、3aに給送され、吹出しパイプ3、3aから、焙焼室1内へ矢示15、15のようにメッシュコンベア2の上下部に向かって吹き出される。一方メッシュコンベア2上には生海苔10が配列されているので、生海苔10は前記過熱水蒸気によって急速に焙焼される。   In the above embodiment, when pressurized water is fed from the high pressure water supply pipe 9a and sprayed from the spray pipe 9 as shown by arrow 11, and the flame of the gas burner 8 is blown out as shown by arrow 12, in the generation chamber 6 Then, superheated steam is generated and fed to the blowing pipes 3 and 3a through the connecting pipe 19a as indicated by arrows 13 and 13, and from the blowing pipes 3 and 3a to the roasting chamber 1 as indicated by arrows 15 and 15 Thus, it blows out toward the upper and lower parts of the mesh conveyor 2. On the other hand, since the raw nori 10 is arranged on the mesh conveyor 2, the raw nori 10 is rapidly roasted by the superheated steam.

前記過熱水蒸気の温度は、例えば150℃(予め設定し、センサー23、23aにより制御する)であって、焙焼時間100秒とする。前記のように、吹出し管3、3aから吹き出された過熱水蒸気は、矢示28、29のように煙突21から排出され、その一部は吸入管5aに矢示30のように吸入され、循環ファン5より、矢示17のように連結管19aへ吹き込まれて、前記生成された過熱水蒸気と混合して、吹出しパイプ3、3aから吹き出される。   The temperature of the superheated steam is, for example, 150 ° C. (preliminarily set and controlled by the sensors 23 and 23a), and the baking time is 100 seconds. As described above, the superheated steam blown out from the blow-out pipes 3 and 3a is discharged from the chimney 21 as indicated by arrows 28 and 29, and a part thereof is sucked into the suction pipe 5a as indicated by the arrow 30 and circulated. The fan 5 is blown into the connecting pipe 19a as indicated by an arrow 17, mixed with the generated superheated steam, and blown out from the blowing pipes 3 and 3a.

前記における循環ファン5の送気量により過熱水蒸気の温度は低下するが、その温度はセンサー23、23a、23bで検出し、制御器16に伝えられて、制御器16の指示により循環ファン5及び生成室6内で生成される過熱水蒸気の温度が制御される。即ち生海苔10に吹き出される過熱水蒸気の温度を設定値(例えば150℃)に保つべく循環ファン5及び生成過熱水蒸気の温度が制御される。また温度を高く設定した場合には、生海苔の移動速度を速くして加工時間を短縮する。   Although the temperature of the superheated steam is lowered by the amount of air supplied from the circulation fan 5 in the above, the temperature is detected by the sensors 23, 23 a, 23 b and transmitted to the controller 16. The temperature of superheated steam generated in the generation chamber 6 is controlled. That is, the temperature of the circulating fan 5 and the generated superheated steam is controlled so as to keep the temperature of the superheated steam blown to the raw laver 10 at a set value (for example, 150 ° C.). When the temperature is set high, the moving time of raw nori is increased to shorten the processing time.

この発明の実施例のブロック図。The block diagram of the Example of this invention. 同じく焙焼装置の斜視図。The perspective view of a roasting apparatus similarly. (a)同じく焙焼装置の概念図、(b)同じく過熱水蒸気生成装置の概念図、(c)同じくダンパーの作用を示す一部断面拡大図。(A) The conceptual diagram of a roasting apparatus, (b) The conceptual diagram of a superheated steam production apparatus, (c) The partial cross-sectional enlarged view which similarly shows the effect | action of a damper. 同じく他の実施例の概念図。Similarly, the conceptual diagram of another Example. 同じく過熱水蒸気の熱容量を示す図。The figure which similarly shows the heat capacity of superheated steam.

符号の説明Explanation of symbols

1 焙焼室
2 メッシュコンベア
3 吹出しパイプ
4 排気管
5 循環ファン
6 生成室
7 吐出管
8 バーナー
9 噴霧管
10 生海苔
16 制御器
DESCRIPTION OF SYMBOLS 1 Roasting room 2 Mesh conveyor 3 Blowing pipe 4 Exhaust pipe 5 Circulating fan 6 Generation room 7 Discharge pipe 8 Burner 9 Spraying pipe 10 Fresh seaweed 16 Controller

Claims (9)

過熱水蒸気の強制流動雰囲気内で海藻類を移動しつつ焙焼することを特徴とした過熱水蒸気を用いた海藻類の焙焼加工方法。   A seaweed roasting method using superheated steam, characterized in that the seaweed is roasted while moving in a forced flow atmosphere of superheated steam. 110℃〜300℃の過熱水蒸気の強制流動雰囲気内で海藻類を移動しつつ焙焼することを特徴とした過熱水蒸気を用いた海藻類の焙焼加工方法。   A seaweed roasting method using superheated steam, wherein the seaweed is roasted while moving in a forced flow atmosphere of superheated steam at 110 ° C to 300 ° C. 110℃〜300℃の過熱水蒸気の強制流動雰囲気内で海藻類を定速移動させると共に、遠赤外線を照射して焙焼することを特徴とした過熱水蒸気を用いた海藻類の焙焼加工方法。   A seaweed roasting method using superheated steam, characterized in that seaweed is moved at a constant speed in a forced flow atmosphere of superheated steam at 110 ° C to 300 ° C and is irradiated with far-infrared rays for roasting. 下記の条件により過熱水蒸気で海藻類を焙焼することを特徴とした過熱水蒸気を用いた海藻類の焙焼加工方法。
(1)過熱水蒸気の温度を110℃〜300℃とすること
(2)焼き時間を5秒〜300秒とすること
(3)海藻類の移動速度を0.5m/分〜5m/分とすること
A seaweed roasting method using superheated steam, characterized in that seaweed is roasted with superheated steam under the following conditions.
(1) The temperature of the superheated steam is set to 110 ° C. to 300 ° C. (2) The baking time is set to 5 seconds to 300 seconds (3) The moving speed of the seaweed is set to 0.5 m / min to 5 m / min. thing
請求項1記載の方法を実施する装置であって、海藻類を焙焼する焙焼室と、該焙焼室内を通過する海藻類に向けて過熱水蒸気を吹き出す過熱水蒸気の加圧吹出手段と、前記過熱水蒸気の供給手段と、前記焙焼室内に海藻類を移動させる移動手段と、前記各手段の制御手段とを組み合わせたことを特徴とする過熱水蒸気による海藻類の焙焼加工装置。   An apparatus for carrying out the method according to claim 1, wherein a roasting chamber for roasting seaweed, and a superheated steam pressure blowing means for blowing superheated steam toward the seaweed passing through the roasting chamber; An apparatus for roasting seaweed with superheated steam, wherein the superheated steam supply means, a moving means for moving seaweed into the roasting chamber, and a control means for each means are combined. 請求項1記載の方法を実施する装置であって、焙焼室内の中間部へ、海藻類を移動させるメッシュコンベアを横に架設すると共に、該メッシュコンベアの上方及び下方に過熱水蒸気の吹出し口を設け、前記焙焼室に、過熱水蒸気の排出口と、海藻類の供給口及び取出し口を設けたことを特徴とする過熱水蒸気による海藻類の焙焼加工装置。   An apparatus for carrying out the method according to claim 1, wherein a mesh conveyor for moving seaweed is horizontally installed in an intermediate portion of the roasting chamber, and a superheated steam outlet is provided above and below the mesh conveyor. An apparatus for roasting seaweed with superheated steam, wherein the roasting chamber is provided with a discharge port for superheated steam and a supply port and a take-out port for seaweed. 請求項1記載の方法を実施する装置であって、焙焼室内の中間部へ、海藻類を移動させるメッシュコンベアを横に架設すると共に、該メッシュコンベアの上方及び下方に過熱水蒸気の吹出し口を設け、前記焙焼室に、過熱水蒸気の排出口と、海藻類の供給口及び取出し口を設け、前記過熱水蒸気及び海藻類の加工条件を制御する制御器を付設したことを特徴とする過熱水蒸気による海藻類の焙焼加工装置。   An apparatus for carrying out the method according to claim 1, wherein a mesh conveyor for moving seaweed is horizontally installed in an intermediate portion of the roasting chamber, and a superheated steam outlet is provided above and below the mesh conveyor. The superheated steam provided with a controller for controlling the processing conditions of the superheated steam and the seaweed is provided in the roasting chamber, provided with a superheated steam discharge port, a seaweed supply port and a discharge port. Seaweed roasting processing equipment. 焙焼室内に、過熱水蒸気の温度を検出するセンサーを設置し、該センサーの出力を制御器に接続したことを特徴とする請求項5又は6記載の過熱水蒸気による海藻類の焙焼加工装置。   The apparatus for roasting seaweed with superheated steam according to claim 5 or 6, wherein a sensor for detecting the temperature of superheated steam is installed in the roasting chamber, and the output of the sensor is connected to a controller. 過熱水蒸気の供給手段は、過熱水蒸気の供給管に給送ファンを介装したことを特徴とする請求項5記載の過熱水蒸気による海藻類の焙焼加工装置。   6. The apparatus for roasting seaweed by superheated steam according to claim 5, wherein the superheated steam supply means includes a feed fan in a superheated steam supply pipe.
JP2006346223A 2006-04-28 2006-12-22 Roast processing method and apparatus for marine alga, using superheated steam Pending JP2007312768A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2017077738A1 (en) * 2015-11-04 2017-05-11 小浅商事株式会社 Method for producing roasted nori

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2017077738A1 (en) * 2015-11-04 2017-05-11 小浅商事株式会社 Method for producing roasted nori
JP6200105B1 (en) * 2015-11-04 2017-09-20 小浅商事株式会社 Method for producing grilled seaweed
KR20180006461A (en) 2015-11-04 2018-01-17 코아사 쇼지 가부시키가이샤 How to make roasted steaming
CN107613788A (en) * 2015-11-04 2018-01-19 小浅商事株式会社 The manufacture method of roasting sea sedge
KR101909856B1 (en) * 2015-11-04 2018-10-18 코아사 쇼지 가부시키가이샤 How to make roasted steaming

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