JP3909078B2 - Heat treatment apparatus and heating method using heat treatment apparatus - Google Patents

Heat treatment apparatus and heating method using heat treatment apparatus Download PDF

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JP3909078B2
JP3909078B2 JP2005239442A JP2005239442A JP3909078B2 JP 3909078 B2 JP3909078 B2 JP 3909078B2 JP 2005239442 A JP2005239442 A JP 2005239442A JP 2005239442 A JP2005239442 A JP 2005239442A JP 3909078 B2 JP3909078 B2 JP 3909078B2
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JP2007054679A (en
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寛文 吹井
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有限会社 G−Labo
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この発明は、過熱水蒸気を用いて被加熱物の加熱を行う際の、この過熱水蒸気の排気を容易に行うことができ低コストとなる加熱処置装置および加熱処理装置を用いた加熱方法に関するものである。   The present invention relates to a heat treatment apparatus and a heating method using the heat treatment apparatus, which can easily exhaust the superheated steam when heating the object to be heated using the superheated steam and reduce the cost. is there.

従来の殺菌装置は、分散装置にて過熱水蒸気により被殺菌物を殺菌処理した後に、サイクロンにて被殺菌物と気体とを分離して排気するものである(例えば、特許文献1参照)。   A conventional sterilization apparatus sterilizes an object to be sterilized with superheated steam in a dispersing device, and then separates and exhausts the object to be sterilized and gas with a cyclone (for example, see Patent Document 1).

特開2002−320663号公報JP 2002-320663 A

従来の加熱処理装置は、加熱処理工程の1つである殺菌処理を行う工程と、気体を排気する工程とを別工程で行っておりそれぞれに装置が必要であり高コストとなるという問題点があった。また、殺菌処理を行う工程と排気する行程とを連続した工程にて行わなければ成らないため、殺菌処理すなわち加熱を行う時間を自由に決定することが困難であるという問題点があった。   The conventional heat treatment apparatus has a problem that a sterilization process, which is one of the heat treatment processes, and a process of exhausting gas are performed in separate processes, each of which requires an apparatus and is expensive. there were. Moreover, since the process of performing the sterilization process and the process of exhausting must be performed in a continuous process, there is a problem that it is difficult to freely determine the time for performing the sterilization process, that is, the heating.

この発明は上記のような課題を解決するためになされたものであり、排気を行いながら被加熱物の加熱処理を行うことができる加熱処理装置および加熱処理装置を用いた加熱方法を提供することを目的とする。   The present invention has been made to solve the above-described problems, and provides a heat treatment apparatus capable of performing heat treatment of an object to be heated while exhausting, and a heating method using the heat treatment apparatus. With the goal.

この発明は、被加熱物を加熱処理する加熱処理装置において、羽根部を底部に有し羽根部の回転により内部に上昇渦流気流を発生可能な本体と、本体内に過熱水蒸気を供給する過熱水蒸気供給手段と、本体の中央上部に一端が本体の所定の高さ位置まで挿入され他端が本体外に露出する中空筒にて形成され上昇渦流気流の働きにより本体内の被加熱物以外の空気および過熱水蒸気の排気を行う排気部と、本体内に被加熱物を供給する供給部と、本体内から被加熱物を排出する排出部とを備えたものである。   The present invention relates to a heat treatment apparatus for heat-treating an object to be heated, a main body capable of generating a rising vortex airflow inside by a rotation of the blade part having a blade part at the bottom, and superheated steam for supplying superheated steam into the main body Air other than the object to be heated in the main body by the action of the rising vortex airflow formed by the supply means and a hollow cylinder in which one end is inserted in the center upper part of the main body to a predetermined height position and the other end is exposed outside the main body And an exhaust unit that exhausts superheated steam, a supply unit that supplies a heated object into the main body, and a discharge unit that discharges the heated object from the main body.

この発明の加熱処理装置は、被加熱物を加熱処理する加熱処理装置において、羽根部を底部に有し羽根部の回転により内部に上昇渦流気流を発生可能な本体と、本体内に過熱水蒸気を供給する過熱水蒸気供給手段と、本体の中央上部に一端が本体の所定の高さ位置まで挿入され他端が本体外に露出する中空筒にて形成され上昇渦流気流の働きにより本体内の被加熱物以外の空気および過熱水蒸気の排気を行う排気部と、本体内に被加熱物を供給する供給部と、本体内から被加熱物を排出する排出部とを備えたので、過熱水蒸気の排気が容易となり、過熱水蒸気による被加熱物の加熱を低コストにて行うことができる。   The heat treatment apparatus of the present invention is a heat treatment apparatus for heat-treating an object to be heated. A main body capable of generating an upward vortex airflow by rotation of the blade part having a blade part at the bottom, and superheated steam in the main body Superheated steam supply means to supply and heated inside the main body by the action of the rising vortex airflow formed by a hollow cylinder with one end inserted in the center upper part of the main body to a predetermined height position and the other end exposed outside the main body Since it has an exhaust part for exhausting air other than the object and superheated steam, a supply part for supplying the object to be heated into the main body, and a discharge part for discharging the object to be heated from within the main body, the exhaust of superheated steam is It becomes easy and heating of the article to be heated by superheated steam can be performed at low cost.

実施の形態1.
以下、本願発明の実施の形態について説明する。図1はこの発明の実施の形態1における加熱処理装置の構成を示す図、図2は図1に示した加熱処理装置の本体の内部構成を説明するための部分断面斜視図、図3は図1に示した加熱処理装置の本体内における上昇渦流気流の状態を説明するための図、図4は図1に示した加熱処理装置を用いた加熱方法により行った殺菌処理の結果を示す図である。尚、本願で言う過熱水蒸気とは常圧で100℃より高い温度で、ドライで熱量が大きく、ほとんど酸素を含まない蒸気のことを示している。特に170℃以上になるとその特性が十分に発揮できものである。図において、羽根部1を底部に有し羽根部1の回転により内部に上昇渦流気流A、Bが発生可能な本体2を有する。
Embodiment 1 FIG.
Embodiments of the present invention will be described below. 1 is a diagram showing a configuration of a heat treatment apparatus according to Embodiment 1 of the present invention, FIG. 2 is a partial sectional perspective view for explaining an internal configuration of a main body of the heat treatment apparatus shown in FIG. 1, and FIG. FIG. 4 is a diagram illustrating the result of sterilization performed by the heating method using the heat treatment apparatus shown in FIG. 1. FIG. 4 is a diagram for explaining the state of the rising vortex air current in the main body of the heat treatment apparatus shown in FIG. is there. The superheated steam referred to in the present application means a steam that is dry at a temperature higher than 100 ° C. at normal pressure, has a large amount of heat, and contains almost no oxygen. In particular, when the temperature is 170 ° C. or higher, the characteristics can be sufficiently exhibited. In the figure, there is a main body 2 having a blade portion 1 at the bottom and capable of generating rising vortex air currents A and B by rotation of the blade portion 1.

上昇渦流気流A、Bとは図3に示すように、羽根部1の水平回転により中心を軸とした回転気流が上昇(A)しながらかつその上昇気流に対して中心方向に回転(B)する気流である。羽根部1は図2に示すように、例えば本体2内の底部の中心を軸として3枚の羽根10、11、12を略120度間隔にて配設させ水平方向に回転するように、一端が回転軸14に固定され、他端には本体2の壁面に沿った垂直方向部分を有している。さらに、羽根10、11、12は水平方向から上方に30度傾斜して構成されている。このように羽根10、11、12を傾斜させて形成すると、上昇渦流気流A、Bが形成されやすく、被加熱物の撹拌が容易となる。この羽根10、11、12の傾斜角度は30度に限られることはなく、20度ないし45度の範囲であれば有効である。傾斜角度が20度より小さいと上昇渦流気流A、Bが形成されにくくなり、45度より大きいと被加熱物を必要以上に破壊してしまう可能性があるために設定された値である。また、羽根部1はモータ13により本体2の底部の中心の回転軸14を回転させることにより回転するものである。また、上昇渦流気流A、Bを発生させるための羽根部1の回転速度は、羽根10、11、12の周速で3m/秒〜20m/秒程度である。3m/秒以下であると上昇渦流気流A、Bがほとんど発生しなくなり、20m/秒以上であると羽根10、11、12が被加熱物に対して空回り状態となる。   As shown in FIG. 3, the rising vortex airflows A and B rotate in the center direction with respect to the rising airflow (B) while the rotating airflow around the center ascends (A) due to the horizontal rotation of the blade portion 1. It is an airflow to do. As shown in FIG. 2, the blade portion 1 has one end so that, for example, three blades 10, 11, 12 are arranged at intervals of about 120 degrees around the center of the bottom portion in the main body 2 and rotate in the horizontal direction. Is fixed to the rotating shaft 14 and has a vertical portion along the wall surface of the main body 2 at the other end. Furthermore, the blades 10, 11, and 12 are configured to be inclined 30 degrees upward from the horizontal direction. When the blades 10, 11, and 12 are formed so as to be inclined in this manner, the rising vortex air currents A and B are easily formed, and the object to be heated is easily stirred. The inclination angle of the blades 10, 11, and 12 is not limited to 30 degrees, but is effective within a range of 20 to 45 degrees. When the inclination angle is less than 20 degrees, the rising vortex air currents A and B are difficult to be formed, and when the inclination angle is greater than 45 degrees, the heated object may be destroyed more than necessary. The blade 1 is rotated by rotating a rotating shaft 14 at the center of the bottom of the main body 2 by a motor 13. Moreover, the rotational speed of the blade | wing part 1 for generating ascending vortex | eddy_current A and B is about 3 m / sec-20 m / sec with the peripheral speed of the blade | wings 10, 11, and 12. FIG. Ascending vortex air currents A and B hardly occur when the speed is 3 m / sec or less, and when the speed is 20 m / sec or more, the blades 10, 11, and 12 are in an idle state with respect to the object to be heated.

本体2の内側壁は、下部から所定高さ位置まで略同一径に形成された垂直部20と、所定高さ位置より高い部分は中心部に向かって傾斜させて垂直部20より狭いテーパ形状にてなる傾斜部21とにてなる。これは垂直部20にて回転気流を発生させ、それを傾斜部21に沿って上昇させることにより上昇渦流気流A、Bを発生させやすくするとともに、被加熱物が傾斜部21に接触して重力により下方に落下するため、被加熱物と排気(空気および過熱水蒸気)との分離が確実となる。さらに、本体2には本体2内温度を測定するための本体内温度測定手段22と、本体2内に過熱水蒸気を配管110および流路切換手段100を介して供給するボイラ30および過熱水蒸気発生手段31にてなる過熱水蒸気供給手段3とを有する。ボイラ30にて作成された飽和水蒸気(100℃:常圧)を過熱水蒸気発生手段31にて例えば高周波誘導加熱方式(例えば、周波数20KHz)にて加熱して過熱水蒸気(100℃より高く400℃程度までの間の温度:蒸気圧力が0.05から0.18MPa)を生成している。   The inner wall of the main body 2 has a vertical portion 20 formed to have substantially the same diameter from the lower portion to a predetermined height position, and a portion higher than the predetermined height position is inclined toward the center portion so as to be narrower than the vertical portion 20. It consists of the inclined part 21. This generates a rotating airflow in the vertical portion 20 and raises it along the inclined portion 21 to facilitate the generation of ascending vortex airflows A and B, and the object to be heated comes into contact with the inclined portion 21 and gravity. Therefore, separation between the object to be heated and the exhaust (air and superheated steam) is ensured. Further, the main body 2 has a main body temperature measuring means 22 for measuring the temperature in the main body 2, a boiler 30 for supplying superheated steam into the main body 2 via the pipe 110 and the flow path switching means 100, and superheated steam generating means. And superheated steam supply means 3. Saturated steam (100 ° C .: normal pressure) created by the boiler 30 is heated by the superheated steam generation means 31 by, for example, a high-frequency induction heating method (for example, frequency 20 KHz). Until the vapor pressure is 0.05 to 0.18 MPa).

さらに、配管100の本体2の近傍には本体2内に供給される過熱水蒸気の供給温度を測定するための供給温度測定手段8と、本体2の中央上部に一端が本体2の所定の高さ位置まで挿入され、他端が本体2外に露出する中空筒にて形成され、上昇渦流気流A、Bの働きにより本体2内の被加熱物以外の空気および過熱水蒸気の排気を行う排気部4とを有する。排気部4が排気を行う場合にはバルブ103が開放され加熱処理装置外に排気される。そして、排気部4の中空筒形状の径dの大きさは、本体2の内径D(本体2の内径Dとは垂直部20における大きさを示すものである)の大きさの略2分の1にて構成されている。中空筒の径dは内径Dの大きさの略2分の1ないし略3分の1の範囲であれば有効である。これは排気部4の中空筒の径dが本体2の内径Dの2分の1より大きいと被加熱物まで一緒に排気してしまう可能性が高くなり、3分の1より小さいと上昇渦流気流A、Bの働きにより排気を行うことが難しくなるためである。   Further, in the vicinity of the main body 2 of the pipe 100, a supply temperature measuring means 8 for measuring the supply temperature of superheated steam supplied into the main body 2 and one end at a predetermined height of the main body 2 at the center upper portion of the main body 2. The exhaust part 4 is formed by a hollow cylinder that is inserted to a position and the other end is exposed to the outside of the main body 2 and exhausts air other than the heated object in the main body 2 and superheated steam by the action of the rising vortex air currents A and B. And have. When the exhaust unit 4 performs exhaust, the valve 103 is opened and exhausted out of the heat treatment apparatus. The diameter d of the hollow cylindrical shape of the exhaust part 4 is approximately half the size of the inner diameter D of the main body 2 (the inner diameter D of the main body 2 indicates the size of the vertical portion 20). 1. The diameter d of the hollow cylinder is effective if it is in the range of about one half to about one third of the size of the inner diameter D. If the diameter d of the hollow cylinder of the exhaust part 4 is larger than half of the inner diameter D of the main body 2, there is a high possibility that the object to be heated will be exhausted together. This is because it becomes difficult to perform exhaust by the action of the airflows A and B.

また、排気部4の本体2の中央上部に一端が本体2の所定の高さ位置まで挿入されている、所定高さ位置であるが、これは本体2の容量および被加熱物の容量などにより適宜設定されるものである。例えば本体2の容量の半分の容量の被加熱物を加熱処理する場合には、本体2の中央上部に一端が本体2の所定の高さ位置hは本体2の高さHの3分の1±20%の長さ分挿入され形成される。これは長すぎると、被加熱物を一緒に排気してしまう可能性があり、短すぎると効率よく排気を行うことができなくなるためである。よって、本体2の容量と被加熱物の容量とにより適宜設定する必要がある。また、排気部4の円柱筒内には簡単なフィルタ例えばバグフィルタ40が設置されており、排気部4への異物の挿入を防止している。また、排気部4には本体2の近傍に本体2内から排気(空気や過熱水蒸気など)される排気温度を測定するための排気温度測定手段9が配設されている。   Further, one end of the exhaust part 4 is inserted into the center upper portion of the main body 2 up to a predetermined height position of the main body 2, which is a predetermined height position. This depends on the capacity of the main body 2 and the capacity of the object to be heated. It is set appropriately. For example, when heating an object to be heated whose capacity is half of the capacity of the main body 2, the predetermined height position h of the main body 2 is one third of the height H of the main body 2 at the center upper portion of the main body 2. Inserted by a length of ± 20%. This is because if the length is too long, the objects to be heated may be exhausted together, and if the length is too short, the exhaust cannot be performed efficiently. Therefore, it is necessary to appropriately set the capacity of the main body 2 and the capacity of the object to be heated. In addition, a simple filter such as a bag filter 40 is installed in the cylindrical cylinder of the exhaust unit 4 to prevent foreign matter from being inserted into the exhaust unit 4. Further, an exhaust temperature measuring means 9 for measuring an exhaust temperature exhausted from the inside of the main body 2 (air, superheated steam, etc.) is disposed in the vicinity of the main body 2 in the exhaust portion 4.

さらに、本体2内に被加熱物を供給する供給部5は本体2上部に形成されている本体2の蓋体にてなる。よって、排気部4の本体2の外部の一部にフレキシブル部41を形成し供給部5の開閉に対応しているものである。また、供給部5には蓋体の一部を開口可能な予備供給部50を形成し、供給部5を開閉しなくとも、例えば少量の追加被加熱物ならば、予備供給部50から本体2内に供給することができる。さらに、本体2内から被加熱物を排出する排出部6を有している。この排出部6は本体2の下部に形成された開閉可能な排出口部60と、この排出口部60の開閉を行う例えばシリンダにてなる駆動部61と、排出口部60に連通管62にて連通して外部に曝露することのない密閉空間部63にてなる。   Further, the supply unit 5 for supplying an object to be heated into the main body 2 is a lid body of the main body 2 formed on the upper portion of the main body 2. Therefore, the flexible part 41 is formed in a part of the outside of the main body 2 of the exhaust part 4 to cope with opening and closing of the supply part 5. In addition, the supply unit 5 is provided with a preliminary supply unit 50 that can open a part of the lid, and even if the supply unit 5 is not opened and closed, for example, if there is a small amount of additional object to be heated, the preliminary supply unit 50 to the main body 2 Can be supplied within. Furthermore, it has the discharge part 6 which discharges a to-be-heated material from the inside of the main body 2. The discharge unit 6 includes an openable / closable discharge port 60 formed in the lower portion of the main body 2, a drive unit 61 formed of, for example, a cylinder that opens and closes the discharge port 60, and a communication pipe 62 connected to the discharge port 60. The sealed space portion 63 that does not communicate with the outside and is not exposed to the outside.

さらに、本体2内にドライエアを供給するドライエア供給手段7を有し、配管110および流路切換手段100を介して過熱蒸気発生手段31から過熱水蒸気を熱源として供給して空気を加熱して、100℃以下、例えば50℃〜80℃程度の温度のドライエアを作成し、配管111およびバルブ101を介して本体2内にドライエアを供給するものである。また、ドライエアを生成している際には、バルブ102が開放され加熱処理装置外に排気部4から過熱水蒸気が排気される。尚、上記にて示した各箇所において、被加熱物が接する箇所は、例えば耐腐食性に優れたステンレス材にて形成されている。   Furthermore, it has a dry air supply means 7 for supplying dry air into the main body 2, and superheated steam is supplied as a heat source from the superheated steam generation means 31 through the pipe 110 and the flow path switching means 100 to heat the air, Dry air having a temperature not higher than ° C., for example, a temperature of about 50 ° C. to 80 ° C. is created, and the dry air is supplied into the main body 2 via the pipe 111 and the valve 101. Further, when dry air is generated, the valve 102 is opened, and the superheated steam is exhausted from the exhaust unit 4 outside the heat treatment apparatus. In addition, in each location shown above, the location which a to-be-heated material contacts is formed, for example with the stainless steel material excellent in corrosion resistance.

次に上記のように構成された実施の形態1の加熱処理装置を用いた加熱方法について説明する。ここで本願発明における被加熱物の加熱処理とは、乾燥処理、殺菌処理、造粒処理など加熱により行う処理が様々存在し、適宜対応することができる。まず、過熱水蒸気供給手段3のボイラ30および過熱水蒸気供給手段3を用いて過熱水蒸気を発生させ、配管110および流路切換手段100を介して本体2内に過熱水蒸気を供給する。これとともにモータ13により回転軸14を回転させて羽根部1を本体2内を水平方向に回転させ上昇渦流気流A、Bを発生させ本体2内を予備加熱する。そして、過熱水蒸気は排気部4から羽根部1の回転により得られる上昇渦流気流A、Bにより効率よく加熱処理装置外に排気される。そしてこの加熱は本体内温度測定手段22にて測定することにより確認する。この予備加熱の際に本体2内に上昇渦流気流A、Bを発生させていないと、本体2内の過熱水蒸気がうまく排気されず、本体2内に過熱水蒸気が残存して結露の原因となることが考えられる。次に、流路切換手段100にて過熱水蒸気の流路を切り換えて過熱水蒸気供給手段3からの過熱水蒸気の供給を停止して、ドライエア供給手段7に過熱水蒸気を供給し、ドライエア供給手段7から配管111およびバルブ101を介してドライエアを例えば数分程度供給する。これは本体2の内の結露などを完全確実に防止するための工程で、仕様や環境によっては必要ない場合も存在する。また、本体2は一旦温められているため、数分程度ドライエアを供給したとしても必要以上に冷却されることはない。   Next, a heating method using the heat treatment apparatus of Embodiment 1 configured as described above will be described. Here, various heat treatments such as drying treatment, sterilization treatment, and granulation treatment exist and can be appropriately handled as the heat treatment of the object to be heated in the present invention. First, superheated steam is generated using the boiler 30 and the superheated steam supply means 3 of the superheated steam supply means 3, and the superheated steam is supplied into the main body 2 via the pipe 110 and the flow path switching means 100. At the same time, the rotating shaft 14 is rotated by the motor 13 to rotate the blade 1 in the horizontal direction in the main body 2 to generate ascending vortex air currents A and B to preheat the main body 2. Then, the superheated steam is efficiently exhausted out of the heat treatment apparatus by the rising vortex air currents A and B obtained by the rotation of the blade part 1 from the exhaust part 4. And this heating is confirmed by measuring by the body internal temperature measuring means 22. If the ascending vortex airflows A and B are not generated in the main body 2 during the preheating, the superheated steam in the main body 2 is not exhausted well, and the superheated steam remains in the main body 2 and causes condensation. It is possible. Next, the flow path switching means 100 switches the superheated steam flow path to stop the supply of superheated steam from the superheated steam supply means 3, supplies the superheated steam to the dry air supply means 7, and the dry air supply means 7 Dry air is supplied, for example, for several minutes through the pipe 111 and the valve 101. This is a process for completely preventing condensation in the main body 2 and may not be necessary depending on the specifications and environment. Moreover, since the main body 2 is once warmed, even if dry air is supplied for several minutes, it is not cooled more than necessary.

次に、予備加熱が終了した後にドライエア供給手段7からのドライエアの供給および羽根部1の回転を停止して、供給部5を開放して本体2内に被加熱物を供給する。尚、加熱処理する被加熱物の容量であるが、本体2の容量の半分程度の容量であれば、上昇渦流気流A、Bを効率よく発生させることができる。次に、被加熱物を供給した後に供給部5を閉じて、本体2内の羽根部1を回転させ、被加熱物に上昇渦流気流A、Bを発生させる。例えば、30秒程度回転すれば上昇渦流気流A、Bを発生させることができる。これは、上昇渦流気流A、Bを発生していない状態から過熱水蒸気を供給すると被加熱物の一部にのみ過熱水蒸気が接触し、不具合を生じる可能性があるためである。次に、上昇渦流気流A、Bが発生した後に、過熱水蒸気供給手段3から過熱水蒸気を所定時間供給して被加熱物を加熱処理を行う。このように上昇渦流気流A、Bが発生した状態にて加熱処理を行っているため、図3に示すように排気は上昇(A)しながら、被加熱物は回転(B)と重力とにより落下して、排気と被加熱物とは分離されて排気のみが排気部4から排気される。また、この際決定される所定時間は、例えば、供給温度測定手段8にて測定される過熱水蒸気の本体2内に供給される供給温度と、排気温度測定手段9にて測定される排気部4から排気させる排気温度とを測定し、供給温度および排気温度の差により過熱水蒸気の本体内への供給時間を設定する方法が考えられる。   Next, after the preliminary heating is completed, the supply of dry air from the dry air supply means 7 and the rotation of the blade part 1 are stopped, the supply part 5 is opened, and the object to be heated is supplied into the main body 2. In addition, although it is the capacity | capacitance of the to-be-heated material to heat-process, if it is a capacity | capacitance about a half of the capacity | capacitance of the main body 2, ascending vortex | eddy_current A and B can be generated efficiently. Next, after supplying the object to be heated, the supply part 5 is closed, and the blade part 1 in the main body 2 is rotated to generate the rising vortex air currents A and B in the object to be heated. For example, ascending vortex air currents A and B can be generated by rotating for about 30 seconds. This is because if the superheated steam is supplied from a state where the ascending vortex airflows A and B are not generated, the superheated steam may contact only a part of the object to be heated, which may cause a problem. Next, after the rising vortex airflows A and B are generated, the superheated steam is supplied from the superheated steam supply means 3 for a predetermined time to heat the object to be heated. Since the heat treatment is performed in the state where the rising vortex airflows A and B are generated in this way, as shown in FIG. 3, the heated object is rotated (B) and gravity while the exhaust gas is rising (A). It falls and the exhaust and the object to be heated are separated, and only the exhaust is exhausted from the exhaust part 4. The predetermined time determined at this time is, for example, the supply temperature supplied into the superheated steam main body 2 measured by the supply temperature measuring means 8 and the exhaust section 4 measured by the exhaust temperature measuring means 9. It is conceivable to measure the temperature of the exhaust gas discharged from the exhaust gas and set the supply time of superheated steam into the main body based on the difference between the supply temperature and the exhaust temperature.

例えば、この供給温度および排気温度の差がほぼなくなれば供給を終了する方法、供給温度および排気温度の差がほぼなくなってから所定時間供給した後に終了する方法などが考えられる。次に、過熱水蒸気の所定時間供給が終了した後に過熱水蒸気の供給を停止して、羽根部1を回転させながらドライエア供給手段7から100℃以下のドライエアを供給して被加熱物を冷却乾燥する。この際のドライエアの供給時間は数分程度が考えられる。そしてこの冷却は本体内温度測定手段22にて測定することにより確認する。ここで言う冷却とは被加熱物を100℃以下にすることを目的とするものであり、例えば80℃程度に冷却すれば、被加熱物は排出口60から排出された後に容易に室温程度まで冷却することが可能である。次に、ドライエアの供給を停止して、羽根部1を低速回転させながら被加熱物を排出部6の排出口部60を駆動部61により開放し、羽根部1の回転による遠心力により被加熱部は排出口部60から排出され連通管62を介して密閉空間部63に排出される。よって、この工程においては羽根部1は上昇渦流気流A、Bが発生しない程度に回転していることとなる。   For example, a method of terminating the supply when the difference between the supply temperature and the exhaust temperature is almost eliminated, and a method of terminating after supplying for a predetermined time after the difference between the supply temperature and the exhaust temperature is almost eliminated. Next, after the supply of the superheated steam is completed for a predetermined time, the supply of the superheated steam is stopped, and the heated object is cooled and dried by supplying dry air of 100 ° C. or less from the dry air supply means 7 while rotating the blade portion 1. . The supply time of the dry air at this time can be about several minutes. And this cooling is confirmed by measuring with the temperature measuring means 22 in a main body. The term “cooling” as used herein is intended to reduce the temperature of the object to be heated to 100 ° C. or less. It is possible to cool. Next, the supply of dry air is stopped, the object to be heated is opened by the driving unit 61 while the blade unit 1 is rotated at a low speed, and the heating unit 61 is opened by the centrifugal force generated by the rotation of the blade unit 1. The portion is discharged from the discharge port portion 60 and discharged to the sealed space portion 63 through the communication pipe 62. Therefore, in this process, the blade portion 1 is rotated to such an extent that the rising vortex air currents A and B are not generated.

上記のような加熱処理装置を用いた加熱処理方法により行った具体例を図4に示す。(但し、図4における具体例ではドライエアによる冷却乾燥工程は実施していない。)これは加熱処理として殺菌処理を目的として行った例である。図からも明らかなように、過熱水蒸気の供給時間が数十秒にて殺菌処理が十分に可能であることが確認できる。   A specific example performed by the heat treatment method using the heat treatment apparatus as described above is shown in FIG. (However, in the specific example in FIG. 4, the cooling and drying process by dry air is not performed.) This is an example in which the heat treatment is performed for the purpose of sterilization. As is apparent from the figure, it can be confirmed that the sterilization treatment is sufficiently possible in the supply time of the superheated steam within several tens of seconds.

上記のように構成された実施の形態1の加熱処理装置によれば、加熱を行う工程と排気を行う工程とを同一の装置にて行うことができるため、加熱時間を自由に調整することができるため、被加熱物を効率的な加熱処理が可能となるのはもちろんのこと、過熱水蒸気の排気を容易に行うことができる。よって被加熱物の加熱処理を低コストにて行うことができる。   According to the heat treatment apparatus of the first embodiment configured as described above, the heating process and the exhaust process can be performed in the same apparatus, so that the heating time can be freely adjusted. Therefore, it is possible not only to efficiently heat the object to be heated, but also to easily exhaust the superheated steam. Therefore, the heat treatment of the object to be heated can be performed at low cost.

尚、上記実施の形態1における予備加熱や、ドライエアにより冷却乾燥は加熱処理の仕様によっては必要がない場合も考えられる。予備加熱の工程は連続して加熱処理を行い、すでに本体が加熱されているような場合などは必要がなく、また、ドライエアによる冷却乾燥工程は、過熱水蒸気のみの乾燥であっても十分可能である仕様の場合もある。また、各温度測定手段により温度を測定して制御を行う例を示したがこれに限られることはなく、経験値や実験値などから適宜制御を行うことも可能である。   Note that preheating in the first embodiment or cooling and drying by dry air may not be necessary depending on the specifications of the heat treatment. The preheating step is not necessary when the main body is already heated by performing the heat treatment continuously, and the cooling and drying step with dry air is sufficiently possible even with drying only with superheated steam. There may be some specifications. Moreover, although the example which measures and measures temperature by each temperature measurement means was shown, it is not restricted to this, It is also possible to control suitably from an experience value, an experimental value, etc.

実施の形態2.
図5はこの発明の実施の形態2における加熱処理装置の構成を示す図、図6は図5に示した加熱処理装置の本体の内部構成を説明するための部分断面斜視図、図7は図5に示した加熱処理装置を用いた加熱方法により行った造粒処理の結果を示す図である。図において上記実施の形態1と同様の部分は同一符号を付して説明を省略する。本体2の下部側壁に、側壁近傍を撹拌する撹拌手段200を備えた。図6に示すように撹拌手段200はモータ201により本体2内を垂直方向を軸として回転する。
Embodiment 2. FIG.
5 is a diagram showing the configuration of a heat treatment apparatus according to Embodiment 2 of the present invention, FIG. 6 is a partial sectional perspective view for explaining the internal configuration of the main body of the heat treatment apparatus shown in FIG. 5, and FIG. FIG. 6 is a diagram showing the result of granulation performed by a heating method using the heat treatment apparatus shown in FIG. In the figure, the same parts as those in the first embodiment are denoted by the same reference numerals, and the description thereof is omitted. Stirring means 200 for stirring the vicinity of the side wall is provided on the lower side wall of the main body 2. As shown in FIG. 6, the stirring means 200 is rotated by the motor 201 about the vertical direction in the main body 2.

次に上記のように構成された実施の形態2の加熱処理装置を用いた加熱方法について説明する。ここで本願発明における被加熱物の加熱処理の内、特に造粒処理による場合について説明する。まず、上記実施の形態1と同様に、過熱水蒸気供給手段3のボイラ30および過熱水蒸気供給手段3を用いて過熱水蒸気を発生させ、配管110および流路切換手段100を介して本体2内に過熱水蒸気を供給する。これとともにモータ13により回転軸14を回転させて羽根部1を本体2内を水平方向に回転させ上昇渦流気流A、Bを発生させ本体2内を予備加熱する。そして、過熱水蒸気は排気部4から羽根部1の回転により得られる上昇渦流気流A、Bにより効率よく加熱処理装置外に排気される。そしてこの加熱は本体内温度測定手段22にて測定することにより確認する。次に、流路切換手段100にて過熱水蒸気の流路を切り換えて過熱水蒸気供給手段3からの過熱水蒸気の供給を停止して、ドライエア供給手段7に過熱水蒸気を供給し、ドライエア供給手段7から配管111およびバルブ101を介してドライエアを例えば数分程度供給する。   Next, a heating method using the heat treatment apparatus of the second embodiment configured as described above will be described. Here, among the heat treatments of the object to be heated in the present invention, a case by the granulation treatment will be described. First, as in the first embodiment, superheated steam is generated using the boiler 30 and the superheated steam supply means 3 of the superheated steam supply means 3, and superheated in the main body 2 via the pipe 110 and the flow path switching means 100. Supply steam. At the same time, the rotating shaft 14 is rotated by the motor 13 to rotate the blade 1 in the horizontal direction in the main body 2 to generate ascending vortex air currents A and B to preheat the main body 2. Then, the superheated steam is efficiently exhausted out of the heat treatment apparatus by the rising vortex air currents A and B obtained by the rotation of the blade part 1 from the exhaust part 4. And this heating is confirmed by measuring by the body internal temperature measuring means 22. Next, the flow path switching means 100 switches the superheated steam flow path to stop the supply of superheated steam from the superheated steam supply means 3, supplies the superheated steam to the dry air supply means 7, and the dry air supply means 7 Dry air is supplied, for example, for several minutes through the pipe 111 and the valve 101.

次に、予備加熱が終了した後にドライエア供給手段7からのドライエアの供給および羽根部1の回転を停止して、供給部5を開放して本体2内に過熱水蒸気の熱にて溶融する物質(バインダー)を含有する被加熱物を供給する。次に、被加熱物を供給した後に供給部5を閉じて、本体2内の羽根部1を回転させ、被加熱物に上昇渦流気流A、Bを発生させるとともに、モータ201により撹拌手段200にて撹拌を行う。この際の撹拌手段200における回転速度は、例えば、500rpm〜2500rpm程度である。この撹拌手段200による撹拌は本体2の外周底部でかつ羽根部1の水平方向と異なる垂直方向を軸として回転して撹拌することが望ましい。これは撹拌手段200の撹拌により、バインダーにて必要以上に固まりとなった被加熱物をほぐすことが目的であり、所望の造粒形状を得るために行うためである。次に、上昇渦流気流A、Bが発生した後に、過熱水蒸気供給手段3から過熱水蒸気を所定時間供給して被加熱物の過熱水蒸気の熱にて溶融する物質が溶融して被加熱物の造粒処理を行う。このように上昇渦流気流A、Bが発生した状態にて加熱処理を行っているため、図3に示すように排気は上昇(A)しながら、被加熱物は回転(B)と重力とにより落下して、排気と被加熱物とは分離されて排気のみが排気部4から排気される。また、この際決定される所定時間は、例えば、供給温度測定手段8にて測定される過熱水蒸気の本体2内に供給される供給温度と、排気温度測定手段9にて測定される排気部4から排気させる排気温度とを測定し、供給温度および排気温度の差により過熱水蒸気の本体内への供給時間を設定する方法が考えられる。   Next, after the preliminary heating is completed, the supply of dry air from the dry air supply means 7 and the rotation of the blade part 1 are stopped, the supply part 5 is opened, and the substance (melted by the heat of superheated steam in the main body 2) A heated object containing a binder is supplied. Next, after supplying the object to be heated, the supply unit 5 is closed and the blade part 1 in the main body 2 is rotated to generate the rising vortex air currents A and B in the object to be heated. And stir. The rotation speed in the stirring means 200 at this time is, for example, about 500 rpm to 2500 rpm. It is desirable that the stirring by the stirring means 200 is performed by rotating around the vertical direction different from the horizontal direction of the blade portion 1 at the bottom of the outer periphery of the main body 2 and stirring. This is for the purpose of loosening an object to be heated which has become harder than necessary with the binder by stirring by the stirring means 200, and is performed in order to obtain a desired granulated shape. Next, after the rising vortex airflows A and B are generated, the superheated steam is supplied from the superheated steam supply means 3 for a predetermined time, and the substance melted by the heat of the superheated steam of the heated object is melted to produce the heated object. Perform grain processing. Since the heat treatment is performed in the state where the rising vortex airflows A and B are generated in this way, as shown in FIG. 3, the heated object is rotated (B) and gravity while the exhaust gas is rising (A). It falls and the exhaust and the object to be heated are separated, and only the exhaust is exhausted from the exhaust part 4. The predetermined time determined at this time is, for example, the supply temperature supplied into the superheated steam main body 2 measured by the supply temperature measuring means 8 and the exhaust section 4 measured by the exhaust temperature measuring means 9. It is conceivable to measure the temperature of the exhaust gas discharged from the exhaust gas and set the supply time of superheated steam into the main body based on the difference between the supply temperature and the exhaust temperature.

例えば、この供給温度および排気温度の差がほぼなくなれば供給を終了する方法、供給温度および排気温度の差がほぼなくなってから所定時間供給した後に終了する方法などが考えられる。次に、過熱水蒸気の所定時間供給が終了した後に過熱水蒸気の供給を停止して、羽根部1を回転させながらドライエア供給手段7から100℃以下のドライエアを供給して被加熱物を冷却乾燥する。次に、ドライエアの供給を停止して、羽根部1を上昇渦流気流A、Bが発生しない程度の低速回転させながら被加熱物を排出部6の排出口部60を駆動部61により開放し、羽根部1の回転による遠心力により被加熱部は排出口部60から排出され連通管62を介して密閉空間部63に排出される。   For example, a method of terminating the supply when the difference between the supply temperature and the exhaust temperature is almost eliminated, and a method of terminating after supplying for a predetermined time after the difference between the supply temperature and the exhaust temperature is almost eliminated. Next, after the supply of the superheated steam is completed for a predetermined time, the supply of the superheated steam is stopped, and the heated object is cooled and dried by supplying dry air of 100 ° C. or less from the dry air supply means 7 while rotating the blade portion 1. . Next, the supply of dry air is stopped, and the discharge port portion 60 of the discharge portion 6 is opened by the drive portion 61 while rotating the blade portion 1 at a low speed that does not generate the rising vortex air currents A and B. The heated portion is discharged from the discharge port portion 60 by the centrifugal force generated by the rotation of the blade portion 1 and is discharged to the sealed space portion 63 through the communication pipe 62.

上記のような加熱処理装置を用いた加熱処理方法により行った造粒処理の具体例を図7に示す。これは造粒処理を目的として行った例である。図からも明らかなように、過熱水蒸気の供給時間が1分にて造粒処理が十分に可能であることが確認できる。   A specific example of the granulation treatment performed by the heat treatment method using the heat treatment apparatus as described above is shown in FIG. This is an example performed for the purpose of granulation treatment. As can be seen from the figure, it can be confirmed that the granulation treatment is sufficiently possible with the superheated steam supply time of 1 minute.

上記のように構成された実施の形態2の加熱処理装置によれば、上記実施の形態1と同様効果を奏するのはもちろんのこと、被加熱物を効率よく加熱処理でき、過熱水蒸気の熱にて溶融する物質(バインダー)を含有する被加熱物の場合には、容易に造粒を行うことが可能となる。よって被加熱物の加熱処理を低コストにて行うことができる。   According to the heat treatment apparatus of the second embodiment configured as described above, the same effect as that of the first embodiment can be obtained. In the case of an object to be heated containing a substance (binder) that melts, granulation can be performed easily. Therefore, the heat treatment of the object to be heated can be performed at low cost.

この発明の実施の形態1の加熱処理装置の構成を示す図である。It is a figure which shows the structure of the heat processing apparatus of Embodiment 1 of this invention. 図1に示した加熱処理装置の本体の内部構成を説明するための部分断面斜視図である。It is a fragmentary sectional perspective view for demonstrating the internal structure of the main body of the heat processing apparatus shown in FIG. 図1に示した加熱処理装置の本体内における上昇渦流気流の状態を説明するための図である。It is a figure for demonstrating the state of the rising vortex air current in the main body of the heat processing apparatus shown in FIG. 図1に示した加熱処理装置を用いた加熱方法により行った殺菌処理の結果を示す図である。It is a figure which shows the result of the sterilization process performed with the heating method using the heat processing apparatus shown in FIG. この発明の実施の形態1の加熱処理装置の構成を示す図である。It is a figure which shows the structure of the heat processing apparatus of Embodiment 1 of this invention. 図5に示した加熱処理装置の本体の内部構成を説明するための部分断面斜視図である。FIG. 6 is a partial cross-sectional perspective view for explaining the internal configuration of the main body of the heat treatment apparatus shown in FIG. 5. 図5に示した加熱処理装置を用いた加熱方法により行った造粒処理の結果を示す図である。It is a figure which shows the result of the granulation process performed with the heating method using the heat processing apparatus shown in FIG.

符号の説明Explanation of symbols

1,10,11,12 羽根部、2 本体、3 過熱水蒸気供給手段、4 排気部、
5 供給部、6 排出部、7 ドライエア供給手段、8 供給温度測定手段、
9 排気温度測定手段、20 垂直部、21 傾斜部、200 撹拌手段。
1, 10, 11, 12 blade part, 2 body, 3 superheated steam supply means, 4 exhaust part,
5 supply section, 6 discharge section, 7 dry air supply means, 8 supply temperature measurement means,
9 Exhaust temperature measuring means, 20 vertical part, 21 inclined part, 200 stirring means.

Claims (12)

被加熱物を加熱処理する加熱処理装置において、羽根部を底部に有し上記羽根部の回転により内部に上昇渦流気流を発生可能な本体と、上記本体内に過熱水蒸気を供給する過熱水蒸気供給手段と、上記本体の中央上部に一端が上記本体の所定の高さ位置まで挿入され他端が上記本体外に露出する中空筒にて形成され上記上昇渦流気流の働きにより上記本体内の上記被加熱物以外の空気および過熱水蒸気の排気を行う排気部と、上記本体内に上記被加熱物を供給する供給部と、上記本体内から上記被加熱物を排出する排出部とを備えたことを特徴とする加熱処理装置。 In a heat treatment apparatus for heat-treating an object to be heated, a main body having a blade part at the bottom and capable of generating an upward vortex air current by rotation of the blade part, and superheated steam supply means for supplying superheated steam into the main body And at the center upper part of the main body, one end is inserted up to a predetermined height position of the main body and the other end is formed by a hollow cylinder exposed outside the main body, and the heated body in the main body is operated by the rising vortex airflow. An exhaust unit that exhausts air other than the object and superheated steam, a supply unit that supplies the object to be heated into the main body, and a discharge unit that discharges the object to be heated from within the main body A heat treatment apparatus. 上記排気部の中空筒形状の径の大きさは、上記本体の内径の大きさの略2分の1ないし略3分の1の範囲にて構成されていることを特徴とする請求項1に記載の加熱処理装置。 2. The diameter of the hollow cylindrical shape of the exhaust part is configured in a range of about one half to about one third of the inner diameter of the main body. The heat treatment apparatus as described. 上記本体の内側壁は、下部から所定高さ位置まで略同一径に形成された垂直部と、上記所定高さ位置より高い部分は中心部に向かって傾斜させて上記垂直部より狭いテーパ形状にて成る傾斜部とを備えていることを特徴とする請求項1または請求項2に記載の加熱処理装置。 The inner wall of the main body has a narrower taper shape that is narrower than the vertical portion, with a vertical portion formed with substantially the same diameter from the lower portion to a predetermined height position, and a portion higher than the predetermined height position inclined toward the center portion. The heat treatment apparatus according to claim 1, wherein the heat treatment apparatus includes an inclined portion. 上記羽根部は、上記本体内の底部の中心を軸として3枚の羽根を略120度間隔にて配設されて水平方向に回転し、上記各羽根は水平方向から上方に20度ないし45度傾斜して構成されていることを特徴とする請求項1ないし請求項3のいずれかに記載の加熱処理装置。 The blades are arranged in such a manner that three blades are arranged at intervals of about 120 degrees around the center of the bottom in the main body and rotate in the horizontal direction, and each blade is 20 degrees to 45 degrees upward from the horizontal direction. The heat treatment apparatus according to any one of claims 1 to 3, wherein the heat treatment apparatus is inclined. 上記排出部は上記本体の下部に形成され、外部に曝露することのない密閉空間にて構成されていることを特徴とする請求項1ないし請求項4のいずれかに記載の加熱処理装置。 The heat treatment apparatus according to any one of claims 1 to 4, wherein the discharge portion is formed in a sealed space that is formed at a lower portion of the main body and is not exposed to the outside. 上記本体内にドライエアを供給するドライエア供給手段を備えたことを特徴とする請求項1ないし請求項5のいずれかに記載の加熱処理装置。 6. The heat treatment apparatus according to claim 1, further comprising dry air supply means for supplying dry air into the main body. 上記本体の下部側壁に、側壁近傍を撹拌する撹拌手段を備えたことを特徴とする請求項1ないし請求項6のいずれかに記載の加熱処理装置。 The heat treatment apparatus according to any one of claims 1 to 6, wherein the lower side wall of the main body is provided with stirring means for stirring the vicinity of the side wall. 請求項1ないし請求項5のいずれかに記載の加熱処理装置を用いた加熱方法において、上記本体内の過熱水蒸気の供給するとともに上記羽根部を回転させ上記上昇渦流気流を発生させながら上記本体を予備加熱する工程と、上記予備加熱終了後に上記過熱水蒸気の供給および上記羽根部の回転を停止して上記本体内に上記被加熱物を供給する工程と、上記被加熱物供給後に上記本体内の上記羽根部を回転させ上記被加熱物に上記上昇渦流気流を発生させる工程と、上記上昇渦流気流が発生した後に上記過熱水蒸気を所定時間供給して上記被加熱物を加熱処理する工程とを備えたことを特徴とする加熱処理装置を用いた加熱方法。 A heating method using the heat treatment apparatus according to any one of claims 1 to 5, wherein superheated steam in the main body is supplied and the blade portion is rotated to generate the rising vortex air current. A step of preheating; a step of supplying the superheated steam after the completion of the preheating and stopping the rotation of the blades and supplying the heated object into the main body; and after supplying the heated object, Rotating the blade portion to generate the rising vortex air current in the heated object, and supplying the superheated steam for a predetermined time after the rising vortex air current is generated to heat the heated object. The heating method using the heat processing apparatus characterized by the above-mentioned. 請求項6に記載の加熱処理装置を用いた加熱方法において、上記本体内の過熱水蒸気の供給するとともに上記羽根部を回転させ上記上昇渦流気流を発生させながら上記本体を予備加熱する工程と、上記予備加熱終了後に上記過熱水蒸気の供給および上記羽根部の回転を停止して上記本体内に上記被加熱物を供給する工程と、上記被加熱物供給後に上記本体内の上記羽根部を回転させ上記被加熱物に上記上昇渦流気流を発生させる工程と、上記上昇渦流気流が発生した後に上記過熱水蒸気を所定時間供給して上記被加熱物を加熱処理する工程と、上記過熱水蒸気を所定時間供給を終了した後に上記過熱水蒸気の供給を停止して上記羽根部を回転させ上記上昇渦流気流を発生させながら100℃以下のドライエアを供給して上記被加熱物を乾燥冷却する工程とを備えたことを特徴とする加熱処理装置を用いた加熱方法。 In the heating method using the heat treatment apparatus according to claim 6, the step of preheating the main body while supplying the superheated steam in the main body and rotating the blade portion to generate the rising vortex air current, A step of stopping the supply of the superheated steam and the rotation of the blade part after the preheating is completed and supplying the object to be heated in the main body; and the blade part in the main body is rotated after the object to be heated is supplied A step of generating the ascending vortex air current in the object to be heated; a step of supplying the superheated steam for a predetermined time after the ascending vortex air current is generated; and heating the object to be heated; and supplying the superheated steam for a predetermined time. After the completion, the supply of the superheated steam is stopped and the blades are rotated to supply the dry eddy current at 100 ° C. or less while generating the rising vortex air flow to dry and cool the heated object. Heating method using the heat treatment apparatus characterized by comprising the step of. 上記本体の下部側壁に、側壁近傍を撹拌する撹拌手段を備えた請求項6に記載の加熱処理装置を用いた加熱方法において、上記本体内の過熱水蒸気の供給するとともに上記羽根部を回転させ上記上昇渦流気流を発生させながら上記本体を予備加熱する工程と、上記予備加熱終了後に上記過熱水蒸気の供給および上記羽根部の回転を停止して上記本体内に上記過熱水蒸気の熱にて溶融する物質を含有する上記被加熱物を供給する工程と、上記被加熱物供給後に上記本体内の上記羽根部を回転させ上記被加熱物に上昇渦流気流を発生させるとともに上記撹拌手段にて撹拌を行う工程と、上記上昇渦流気流が発生した後に上記過熱水蒸気を所定時間供給して上記被加熱物を加熱して造粒を行う工程と、上記過熱水蒸気を所定時間供給を終了した後に上記過熱水蒸気の供給を停止して上記羽根部を回転させ上記上昇渦流気流を発生させながら100℃以下のドライエアを供給して上記被加熱物を乾燥冷却する工程とを備えたことを特徴とする加熱処理装置を用いた加熱方法。 The heating method using the heat treatment apparatus according to claim 6, wherein the lower side wall of the main body includes stirring means for stirring the vicinity of the side wall, and the blade is rotated while supplying the superheated steam in the main body. A step of preheating the main body while generating an ascending vortex air current, and a substance that melts in the main body by the heat of the superheated steam after the preheating is finished and the supply of the superheated steam and the rotation of the blades are stopped. Supplying the object to be heated containing, and after supplying the object to be heated, rotating the blade portion in the main body to generate a rising vortex air current in the object to be heated and stirring with the stirring means And after the generation of the rising vortex air current, the superheated steam is supplied for a predetermined time to heat the object to be granulated, and the superheated steam is supplied for a predetermined time. The method further comprises the step of stopping the supply of superheated steam and rotating the blade portion to supply the dry air at 100 ° C. or lower while generating the rising vortex air flow to dry and cool the object to be heated. A heating method using a heat treatment apparatus. 上記過熱水蒸気の上記本体内に供給される供給温度と、上記排気部から排気させる排気温度とを測定し、上記供給温度および上記排気温度の差により上記過熱水蒸気の上記本体内への供給時間を設定することを特徴とする請求項8ないし請求項10のいずれかに記載の加熱処理装置を用いた加熱方法。 The supply temperature of the superheated steam supplied into the main body and the exhaust temperature exhausted from the exhaust section are measured, and the supply time of the superheated steam into the main body is determined by the difference between the supply temperature and the exhaust temperature. The heating method using the heat treatment apparatus according to claim 8, wherein the heating method is set. 上記被加熱物の処理終了後に、上記羽根部を回転させながら上記被加熱物を上記排出口より排出する工程を備えたことを特徴とする請求項8ないし請求項11のいずれかに記載の加熱処理装置を用いた加熱方法。 The heating according to any one of claims 8 to 11, further comprising a step of discharging the heated object from the discharge port while rotating the blade portion after the treatment of the heated object. A heating method using a processing apparatus.
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