JP2004141474A - Heat treatment equipment - Google Patents

Heat treatment equipment Download PDF

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Publication number
JP2004141474A
JP2004141474A JP2002311099A JP2002311099A JP2004141474A JP 2004141474 A JP2004141474 A JP 2004141474A JP 2002311099 A JP2002311099 A JP 2002311099A JP 2002311099 A JP2002311099 A JP 2002311099A JP 2004141474 A JP2004141474 A JP 2004141474A
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Prior art keywords
processing chamber
heat treatment
steam
superheated steam
rotary joint
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JP2002311099A
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JP4036725B2 (en
Inventor
Kotaro Hirayama
平山 鋼太郎
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Dai Ichi High Frequency Co Ltd
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Dai Ichi High Frequency Co Ltd
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  • Incineration Of Waste (AREA)
  • Commercial Cooking Devices (AREA)
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Abstract

<P>PROBLEM TO BE SOLVED: To eliminate treatment temperature restriction in a rotary type heat treatment using superheated steam. <P>SOLUTION: A steam superheating mechanism 3b for feeding superheated steam to a treatment chamber 1 operated while rotating is directly disposed in the treatment chamber 1 and is operated while rotating along with the treatment chamber 1. This constitution can dispense with a rotary joint from a superheated steam feed route and dissolve the treatment temperature restriction derived from the heat resistance of the rotary joint. <P>COPYRIGHT: (C)2004,JPO

Description

【0001】
【発明の属する技術分野】
本発明は、被処理物を収容して又は通過させながら回転する処理室を備え、過熱水蒸気をこの処理室に送給して被処理物を加熱処理する回転式の加熱処理装置に関し、詳しくは、この加熱処理を処理温度に係る適用限界なしに行えるようにしたものである。
【0002】
【従来の技術】
従来、この種の加熱処理は、例えば、廃油,廃プラスチック,食材,生ごみ等の被処理物を対象として、乾燥,減容,調理,焼却等の目的で行われる。この加熱処理を行う装置の基本構成を模式的に示せば、図1のようになる。
【0003】
図1において、1は、ターニングローラ2によって支持・回転駆動される処理室である。ターニングローラ2は、変速機構(図示略)を介してモータ(図示略)に接続されている。3は過熱水蒸気発生機構であって、水を加熱して100℃を越えない水蒸気を発生させるための水蒸気発生機構(ボイラ)3aと、この水蒸気を100℃を越える目的温度に加熱するための水蒸気過熱機構3bとを備えている。そして、過熱水蒸気発生機構3から出力された過熱水蒸気は、ロータリージョイント4を介して処理室1に送給されて加熱処理に与ったのち、排気管5から系外に排出される。
【0004】
図1の基本構成に類する装置の一例が、下記特許文献1,2に開示されている。このような、過熱水蒸気を熱源とする回転式の加熱処理装置によれば、熱含量が大で加熱能力に優れ且つクリーンな過熱水蒸気を被処理物に均等に作用させて加熱処理が行える。すなわち、下記特許文献1,2に記載されているように、食品調理のような被処理物の汚染が許されない加熱処理を高能率に且つ均一な処理品質を以て行うことができるのである。
【0005】
【特許文献1】特開2000−135061(第(8)ページ、図1,             図2)
【特許文献2】特開2000−135167(第(7)ページ、図2,             図3)
【0006】
【発明が解決しようとする課題】
過熱水蒸気を熱源とする回転式の加熱処理装置は、上述のような際立った利点を有する。しかしながら、この加熱処理装置には適用上の限界があった。それは、過熱水蒸気発生機構3から処理室1への過熱水蒸気の送給が前記ロータリージョイント4を介して行われることから、ロータリージョイントの耐熱性によって加熱処理温度が制限されてしまうという限界である。因みに、市販のロータリージョイントの使用可能上限温度は、連続使用の場合、200℃台に過ぎない。例えば前記特許文献1,2の実施例には、最高で350℃に及ぶ過熱水蒸気による加熱処理が開示されているが、その処理時間は30秒といった短時間であるから、ロータリージョイントのシール部材の熱劣化は少なく、シール部材の交換をやや頻度高く行う程度の負荷を以て実施可能であろう。
【0007】
ところが、300℃以上の連続加熱を要するような高熱加熱処理となると、過熱水蒸気が単なる高温ガス(窒素ガスなど)よりも熱劣化作用が更に強い高露点ガスであることも相まって、実用可能なロータリージョイントの入手が適わず、ついては、このような加熱処理には、過熱水蒸気による回転式の加熱処理が適用できない。
【0008】
すなわち、300℃以上の連続加熱といった高熱加熱処理にも適用できるような、過熱水蒸気利用の回転式加熱処理装置の提供が課題となっていた。
【0009】
【課題を解決するための手段】
本発明はこのような課題を解決するためになされたものであって、本発明加熱処理装置は、被処理物を収容して又は通過させながら回転する処理室を備え、この処理室に、水蒸気発生機構と水蒸気過熱機構とを備えた過熱水蒸気発生機構から過熱水蒸気を送給して前記被処理物を加熱処理する加熱処理装置において、前記水蒸気過熱機構は、前記処理室に直結接続されていて、前記処理室と共に回転しながら稼働するようにした構成を特徴とする。
【0010】
この構成によれば、処理室に過熱水蒸気を送給する経路上には、ロータリージョイントが存在せず、従って、前記ロータリージョイントの耐熱性に係る加熱処理装置の適用限界が解消して前記高熱加熱処理にも適用可能となっており、前記本発明の課題は解決されたのである。
【0011】
【発明の実施の形態】
次に、本発明による加熱処理装置の一実施形態について説明する。
【0012】
図2(a)は本実施形態による加熱処理装置の概略部分断面図であって、そのA−A線矢視正面図を図2(b)に示す。
【0013】
図2において、1は処理室,3bは水蒸気過熱機構であって、両者は直結一体化されており、複数のターニングローラ2により支持・駆動されて一緒に回転する。この回転は、処理室1内で行う加熱処理の内容に応じて一方向のみへの回転にしたり、往方向と復方向に代わる代わる回転させる揺動的回転にしたりする。ターニングローラ2は変速器付きモータ(図示略)により駆動される。1aは、処理室1に被処理物を出し入れするための有蓋口である。なお、処理室1等を支持して回転させる手段は、上記ターニングローラ方式に限定されるものではなく、例えば、処理室1等を軸心付きアームで支持して軸心を中心に回転させるといった、他の手段によってもよい。
【0014】
3aは、水蒸気発生機構(ボイラ)であって、使用可能上限温度が150℃の緊密シール式のロータリージョイント4Aを介して水蒸気過熱機構3bに接続されており、両機構3a,3bで前記過熱水蒸気発生機構3(図1参照)を構成している。すなわち、本発明によって、水蒸気過熱機構3bと処理室1を結ぶロータリージョイント(図1の4)は排除されたものの、その代償として上記ロータリージョイント4Aが必要になっている。しかしながら、このロータリージョイント4Aを流れるのは、水蒸気発生機構3aから送給される高々100℃の水蒸気であるから、上記150℃耐用のロータリージョイント4A用いれば何ら支障は生じない。
【0015】
5Aは煙突であって、ラビリンス(迷路)シール式の簡易ロータリージョイント4Bと排気管5とを順次介して処理室1に接続されており、加熱処理の排気を系外上方に導いている。すなわち、回転しない静置状態の煙突5Aを配備するために、水蒸気温度が処理室1内よりさほど低下していない排気部にロータリージョイント4Bの配備を要している。しかしながら、ここに配備するロータリージョイントは、排気放出口間近であって、ラビリンス程度の簡易シールでも水蒸気の洩れは防止できるため、上記簡易ロータリージョイント4Bで事足りる。そして、ラビリンスシール部は金属材料のみで構成されており、前述のような耐熱性に係る支障は何ら生じない。なお、この煙突5Aは処理室1内で行われる加熱処理の内容によっては省略されてよい。
【0016】
図2の装置では、処理室1,水蒸気過熱機構3b,煙突5Aのそれぞれに、流体(水蒸気や飛沫水など)の通路7A,7B,7Cを誘導加熱するための誘導コイル6A,6B,6Cが配備されており、これらの誘導コイル6A,6B,6Cに、高周波電源装置(図示略)から高周波通電を行うことで、処理室1等の被入熱部となる通路7A,7B,7Cに誘導電流(渦電流)を生じさせて、被加熱部を誘導加熱する構成としている。ついては、上記通路7A,7B,7Cを構成する管状体の材質は金属や導電性セラミックスのような導電性材料である必要があり、この実施形態では、上記管状体を非磁性のオーステナイトステンレス鋼製としている。このように、非磁性の導電性管状体を用いると、図2(a)の装置に類する別実施形態の加熱処理装置のA−A線矢視正面図として同図(c)に示す水蒸気過熱部のように、複数の管状体3baaを外縁領域から内奥領域に亘って輻輳配置した場合でも、誘導コイル6Bによる電磁誘導作用が内奥領域の管状体3baaにまで均等に及んで、各管状体3baaを均等に誘導加熱することが出来る。なお、上記導電性管状体がフェライト系ステンレスなどの強磁性材であっても、その磁気変態点を超える温度で稼働させるケースでは、非磁性材としたことによる上記作用が同様に奏される。
【0017】
ここで、誘導コイル6A,6B,6Cのそれぞれについて、配備の目的や作用について説明すると次の通りである。
【0018】
まず、処理室1の誘導コイル6Aは、処理室1内の温度分布を調整するための加熱手段として配したものである。例えば、この誘導コイル6Aに高周波通電して処理室1の器壁1bを誘導加熱し、過熱水蒸気と同等の温度に昇温させることにより、処理室1内の温度を器壁1b近傍に亘って均一にできる。この施策は、処理温度の空間的な均一化もさることながら、時間的な均一化をもたらす作用において更に重要である。例えば、器壁1bを上記温度に昇温させてから過熱水蒸気を送給すれば、温度の上がっていない器壁1bにおいて起こるはずの結露が防止されるし、処理温度への立ち上がりを速くできる。更には、上記誘導加熱を、処理室1内の被処理物も予熱されるように行うことで、処理温度への立ち上がりが一層速くなって、処理温度の終始一定した加熱処理が行える。被処理物の加熱を、上記予熱や加熱処理中の補熱のために器壁1b側からも行うという指向に対しては、器壁1bの内壁面1baに、温度上昇に伴う赤外線放射の放射率を高める表面処理を施しておく施策が有用である。この実施形態では、上記表面処理は、器壁1bを予め過熱水蒸気で酸化させて含水酸化物被膜を形成しておく処理である。この被膜は黒色であり、その材質と色調が相まって、器壁面1baの赤外線放射率は、裸金属面と比べて10倍以上高くなり、これによる赤外線放射の増大によって、被処理物の放射加熱(輻射加熱)作用が顕著になる。
【0019】
以上、誘導加熱による処理室器壁1bの加熱について述べたが、この加熱は、誘導加熱以外の加熱手段、例えば、直線状に炎口が設けられたガスバーナを用いて、回転している処理室1の器壁1bを加熱する構成も、安価な高能率加熱手段として有用である。また、この器壁1bの加熱は、本発明装置の望ましい構成要件であるものの、加熱処理の内容によっては省略されることもある。
【0020】
次に、水蒸気過熱機構3bの誘導コイル6Bは、この水蒸気過熱機構3bにおいて、被加熱物である水蒸気を100℃超の温度に加熱するための加熱手段として配したものである。この実施形態では、水蒸気を加熱するための釜体を、図2に示すように、小径(機構全体の外径に比して十分小さい径)の管状体3baaの複数本を並列配置した水蒸気通路群3baを以て構成しており、この水蒸気通路群3baを、その包括的外周囲に配した誘導コイル6Bによって誘導加熱する構成としている。そして、各小径管状体3baの内部には、ジグザグ状に折り曲げ加工されたステンレス鋼板製の条片(図示略)が配備されており、この条片の配備によって、小径管状体3ba内の水蒸気の流れが乱されて(乱流化を含む)、誘導加熱により入熱された小径管状体3baの管壁の熱の内部の水蒸気への伝達効率が顕著に向上する。なお、この水蒸気過熱機構については上述のような外部からの加熱が必須であるが、そのための加熱手段は上記誘導加熱に限定されない。例えばガス炎加熱で行うようにしてもよい。
【0021】
水蒸気過熱機構3bと同様に、水蒸気発生機構3aにも外部からの加熱が必須であり、その加熱手段として、上記水蒸気過熱機構3bの誘導加熱に準じた形態の誘導加熱を採用することもできる。
【0022】
次いで、煙突5Aの誘導コイル6Cは、煙突5Aから排出される、加熱処理で副生する熱分解ガス等を含んだ水蒸気系排気を急速高温加熱して無害化するためのものである。ついては、この加熱における煙突管壁から排気への伝熱を効率よく行うために、前記水蒸気過熱機構3bの実施形態に準じて煙突5Aを複数本の小径管状体を並列配置して構成(図示略)するとともに各小径管状体内に邪魔体を配備(図示略)している。そして、この邪魔体としては、スチール繊維製の束子(たわし)のスチール繊維表面に触媒機能を有する表面処理(ニッケル系のメッキなど)を施したものを用いている。すなわち、上記邪魔体には、伝熱効率を向上させるばかりでなく、排気中の有害成分の熱分解無害化を促進する機能を果たさせるのである。また、上記熱分解無害化が有害成分の酸化を伴うケースもあることを考慮して、酸化用の空気を煙突5A内に流入させるための開閉自在な小穴等を煙突5Aに設けておくのもよい。なお、誘導コイル6Cは、ガス炎加熱など他の排気加熱手段で代替可能である。また、加熱処理の内容によっては、排気加熱手段そのものを、あるいは、前述のように煙突5Aまでもを省略することが出来る。
【0023】
上述のように、処理室1等に誘導コイル6A等を配して誘導加熱を行う施策は、前記処理室1内の温度分布や時系列的温度プログラムの調整を精度高く且つ迅速に行うのに極めて有用である。
【0024】
誘導コイル6A等は、これに投入を要する電力に応じて冷却の要否が分かれる。冷却が不要な場合には、誘導コイル6A等を、リッツ線(絶縁被覆付き銅細線を縒り合わせた導線)や通常の縒り導線あるいは所要外径の銅単線や銅帯板を巻回して構成すればよい。特にリッツ線は、高周波電流が断面内に行き亘って流れるため、高い周波数での通電における実効抵抗増が少なく、銅損が小さい。ついては、他の線材より細い線外径を以て冷却の要らない通電が可能であり、軽便性,電力効率の両面において好ましい。次に、冷却が必要な場合には、誘導コイル6A等を、銅チューブや真鍮チューブあるいは銅や真鍮の帯板に同材質のチューブを添わせてろう接した導体を巻回して構成し、上記チューブの中空部を冷却水路として利用すればよい。更には、前記リッツ線をプラスチックチューブ等の可撓鞘体の中空部に挿入し、この中空部を冷却水路とした複合導体も有用である。この複合導体は可撓性であり、その場巻回にも適する。ここで、上記冷却水路を流れて誘導コイル6A等の冷却を終えた冷却水は、前記水蒸気発生機構3aに入力し、水蒸気原料水として再利用することが望ましい。これは、冷却を終えた冷却水を、水資源としてばかりではなく、冷却時に蓄積された顕熱を含めて再利用できて、本発明装置に係る水・電力原単位の低減、ひいては環境負荷の低減に資するからである。
【0025】
なお、図2には、誘導コイル6A等として、ソレノイド型(蔓巻き型)のコイルを用いる実施形態を示しているが、回転しながら稼働する処理室1や水蒸気過熱機構3bには、図3,図4にそれぞれ模式的に示すような鞍型コイル61やヘアピン型コイル62を配して誘導加熱するようにしてもよい。両コイルは、共に、被加熱部に沿って位置する部分61a,62aが誘導作用導体として機能し、これらが対向する線状領域を誘導加熱する。そして処理室1等の回転により、処理室1等の器壁が全周に亘って加熱される。因みに、ソレノイド型コイルは誘導加熱効率に優れており、一方、鞍型コイルやヘアピン型コイルによれば、本発明装置における処理室1等に対する操作(被加熱物の出し入れや全体の着脱)が容易になる。
【0026】
誘導コイル6A等あるいは61等により誘導加熱される処理室1等の外周側には、誘導コイル6A,61等との間を隔てる形で絶縁材料(ケイ酸カルシウム・ガラス・アルミナなどの繊維を集結させたマットやアルミナ成形体等)による断熱層8A,8B,8Cを配して、処理室1等からの放熱を防止することが望ましい。こうすることで、より少ない消費電力で所期の誘導加熱が行えるからである。
【0027】
以上、被処理物の加熱処理をバッチ形式(被処理物を処理室内に閉じこめて行う形式)の実施形態を例にとって説明したが、本発明装置の実施形態はこれに限定されず、連続形式(処理室内に被処理物を連続的に順次送給して通過させながら処理する形式)で加熱処理する形態の装置としてもよい。
【0028】
【発明の効果】
本発明加熱処理装置は、回転しながら稼働する処理室内にて被処理物を過熱水蒸気で加熱処理する装置において、処理室に過熱水蒸気を送給するための過熱水蒸気発生機構の後段機能を受け持つ水蒸気過熱機構を、処理室に直結接続する形で配して処理室と共に回転しながら稼働させるようにした構成を特徴とする。
【0029】
従来の過熱水蒸気による回転式加熱処理装置では、過熱水蒸気発生機構から処理室への過熱水蒸気の送給がロータリージョイントを介して行われており、このため、ロータリージョイントの耐熱温度に起因して、上記過熱処理の行える温度が制限され、ついては、適用用途にも制約が生じていた。
【0030】
本発明装置においては、ロータリージョイントを構成する有機物資材の劣化が激しい過熱水蒸気出力部にロータリージョイントを配置する必要が無くなり、その結果、上記加熱処理の適用温度の限界に起因する用途制約は完全に解消された。過熱水蒸気による加熱処理の適用用途の拡大は、処理技術の益々の向上が望まれている、廃棄物のリサイクルや有害物の無害化、各種資源の高価値資材化といった種々の要請にとって好ましいことである。
【図面の簡単な説明】
【図1】従来の回転式の加熱処理装置の概略構成を示す図である。
【図2】(a)は本発明の一実施形態による回転式の加熱処理装置の概略構成を示す図、(b)は(a)に示す水蒸気過熱部のA−A線矢視正面図、(c)は水蒸気過熱部の別形態のA−A線矢視正面図である。
【図3】本発明の一実施形態による回転式の加熱処理装置に用いられる誘導加熱コイルの第1の他の例を示す図である。
【図4】本発明の一実施形態による回転式の加熱処理装置に用いられる誘導加熱コイルの第2の他の例を示す図である。
【符号の説明】
1…処理室
1a…有蓋口
1b…処理室1の器壁
1ba…器壁1bの内壁面
2…ターニングローラ
3…過熱水蒸気発生機構
3a…水蒸気発生機構(ボイラ)
3b…水蒸気過熱機構
3ba…水蒸気通路群
3baa…管状体
4A,4B…ロータリージョイント
5…排気管
5A…煙突
6A,6B,6C…誘導コイル
7A,7B,7C…流体通路
8A,8B,8C…断熱層
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a rotary heat treatment apparatus that includes a treatment chamber that rotates while containing or passing a workpiece, and that heats the workpiece by supplying superheated steam to the treatment chamber. This heat treatment can be performed without an application limit related to the treatment temperature.
[0002]
[Prior art]
Conventionally, this type of heat treatment is performed for the purpose of drying, volume reduction, cooking, incineration, and the like, for example, to-be-treated objects such as waste oil, waste plastic, food materials, and garbage. If the basic structure of the apparatus which performs this heat processing is shown typically, it will become like FIG.
[0003]
In FIG. 1, reference numeral 1 denotes a processing chamber supported and rotated by a turning roller 2. The turning roller 2 is connected to a motor (not shown) via a speed change mechanism (not shown). 3 is a superheated steam generating mechanism, a steam generating mechanism (boiler) 3a for heating water to generate steam not exceeding 100 ° C, and steam for heating this steam to a target temperature exceeding 100 ° C. And an overheating mechanism 3b. Then, the superheated steam output from the superheated steam generation mechanism 3 is supplied to the processing chamber 1 through the rotary joint 4 and subjected to heat treatment, and then discharged from the exhaust pipe 5 to the outside of the system.
[0004]
An example of an apparatus similar to the basic configuration of FIG. 1 is disclosed in Patent Documents 1 and 2 below. According to such a rotary heat treatment apparatus using superheated steam as a heat source, heat treatment can be performed by applying evenly superheated steam having a large heat content, excellent heating capability, and clean treatment to the workpiece. That is, as described in Patent Documents 1 and 2 below, heat treatment such as food cooking that does not allow contamination of an object to be processed can be performed with high efficiency and uniform processing quality.
[0005]
[Patent Document 1] Japanese Patent Application Laid-Open No. 2000-135061 (Page (8), FIGS. 1 and 2)
Japanese Patent Laid-Open No. 2000-135167 (Page (7), FIGS. 2 and 3)
[0006]
[Problems to be solved by the invention]
A rotary heat treatment apparatus using superheated steam as a heat source has the outstanding advantages as described above. However, this heat treatment apparatus has a limit in application. This is the limit that the heat treatment temperature is limited by the heat resistance of the rotary joint because the superheated steam is fed from the superheated steam generation mechanism 3 to the processing chamber 1 through the rotary joint 4. Incidentally, the maximum usable temperature of a commercially available rotary joint is only 200 ° C. in the case of continuous use. For example, the examples of Patent Documents 1 and 2 disclose heat treatment with superheated steam up to 350 ° C., but the treatment time is as short as 30 seconds. There is little thermal deterioration, and the seal member can be replaced with a load that is slightly more frequent.
[0007]
However, in the case of high-temperature heat treatment that requires continuous heating at 300 ° C. or higher, the superheated steam is a high-dew point gas that has a stronger thermal degradation effect than a simple high-temperature gas (nitrogen gas, etc.). A joint cannot be obtained, and therefore, a rotary heat treatment with superheated steam cannot be applied to such a heat treatment.
[0008]
That is, it has been a problem to provide a rotary heat treatment apparatus using superheated steam that can be applied to a high heat treatment such as continuous heating at 300 ° C. or higher.
[0009]
[Means for Solving the Problems]
The present invention has been made to solve such a problem, and the heat treatment apparatus of the present invention includes a processing chamber that rotates while containing or passing an object to be processed. In a heat treatment apparatus that heats the workpiece by supplying superheated steam from a superheated steam generation mechanism that includes a generation mechanism and a steam superheat mechanism, the steam superheat mechanism is directly connected to the processing chamber. The structure is configured to operate while rotating together with the processing chamber.
[0010]
According to this configuration, there is no rotary joint on the path for supplying superheated steam to the processing chamber. Therefore, the application limit of the heat treatment apparatus related to the heat resistance of the rotary joint is eliminated, and the high heat heating is performed. The present invention has been solved because the present invention can be applied to processing.
[0011]
DETAILED DESCRIPTION OF THE INVENTION
Next, an embodiment of the heat treatment apparatus according to the present invention will be described.
[0012]
FIG. 2A is a schematic partial cross-sectional view of the heat treatment apparatus according to the present embodiment, and FIG.
[0013]
In FIG. 2, reference numeral 1 denotes a processing chamber, and 3 b a steam superheating mechanism, both of which are directly connected and integrated, and are supported and driven by a plurality of turning rollers 2 to rotate together. This rotation is a rotation in only one direction according to the content of the heat treatment performed in the processing chamber 1, or a swinging rotation that is rotated in place of the forward direction and the backward direction. The turning roller 2 is driven by a motor with a transmission (not shown). Reference numeral 1 a denotes a lid opening for taking a processing object into and out of the processing chamber 1. The means for supporting and rotating the processing chamber 1 and the like is not limited to the above-mentioned turning roller system. For example, the processing chamber 1 and the like are supported by an arm with an axis and rotated around the axis. Other means may be used.
[0014]
3a is a steam generation mechanism (boiler), which is connected to the steam superheater mechanism 3b via a tightly sealed rotary joint 4A having a usable upper limit temperature of 150 ° C., and the mechanism 3a, 3b The generating mechanism 3 (see FIG. 1) is configured. That is, although the rotary joint (4 in FIG. 1) connecting the steam superheating mechanism 3b and the processing chamber 1 is eliminated by the present invention, the rotary joint 4A is required as a compensation. However, since the water flowing through the rotary joint 4A is at most 100 ° C. fed from the water vapor generating mechanism 3a, there is no problem if the 150 ° C. rotary joint 4A is used.
[0015]
A chimney 5A is connected to the processing chamber 1 through a labyrinth (maze) seal-type simple rotary joint 4B and an exhaust pipe 5 in order, and guides the exhaust of the heat treatment to the upper part of the system. That is, in order to deploy the stationary chimney 5 </ b> A that does not rotate, the rotary joint 4 </ b> B needs to be disposed in the exhaust portion where the water vapor temperature is not so much lower than in the processing chamber 1. However, the rotary joint provided here is close to the exhaust discharge port, and even with a simple seal of the labyrinth level, the leakage of water vapor can be prevented. Therefore, the simple rotary joint 4B is sufficient. And the labyrinth seal part is comprised only with the metal material, and the trouble concerning the heat resistance as mentioned above does not arise at all. The chimney 5A may be omitted depending on the content of the heat treatment performed in the processing chamber 1.
[0016]
In the apparatus of FIG. 2, induction coils 6A, 6B, and 6C for induction heating the passages 7A, 7B, and 7C of fluid (water vapor, splashed water, and the like) are provided in the processing chamber 1, the steam heating mechanism 3b, and the chimney 5A, respectively. The induction coils 6A, 6B, and 6C are provided with high-frequency energization from a high-frequency power supply device (not shown), so that the induction coils 6A, 6B, and 6C are guided to the passages 7A, 7B, and 7C serving as heat input portions of the processing chamber 1 and the like. An electric current (eddy current) is generated to heat the heated part by induction. Therefore, the material of the tubular body constituting the passages 7A, 7B, and 7C needs to be a conductive material such as metal or conductive ceramics. In this embodiment, the tubular body is made of nonmagnetic austenitic stainless steel. It is said. In this way, when a nonmagnetic conductive tubular body is used, the steam superheating shown in FIG. 2C is a front view of the heat treatment apparatus of another embodiment similar to the apparatus of FIG. Even when a plurality of tubular bodies 3baa are convergingly arranged from the outer edge region to the inner back region as in the section, the electromagnetic induction action by the induction coil 6B extends evenly to the tubular body 3baa in the inner back region, The body 3baa can be uniformly induction-heated. Even when the conductive tubular body is a ferromagnetic material such as ferritic stainless steel, the above-described effect due to the non-magnetic material is similarly exhibited in a case where the conductive tubular body is operated at a temperature exceeding its magnetic transformation point.
[0017]
Here, the purpose and function of deployment of each of the induction coils 6A, 6B, 6C will be described as follows.
[0018]
First, the induction coil 6 </ b> A of the processing chamber 1 is arranged as a heating means for adjusting the temperature distribution in the processing chamber 1. For example, the induction coil 6A is energized with high frequency to inductively heat the vessel wall 1b of the processing chamber 1 and raise the temperature to a temperature equivalent to that of superheated steam, thereby increasing the temperature in the processing chamber 1 over the vicinity of the vessel wall 1b. Can be uniform. This measure is more important in the operation that brings about temporal uniformity as well as spatial uniformity of the processing temperature. For example, if superheated steam is supplied after raising the temperature of the device wall 1b to the above temperature, condensation that should occur on the device wall 1b where the temperature has not increased can be prevented, and the rise to the processing temperature can be accelerated. Furthermore, by performing the induction heating so that the object to be processed in the processing chamber 1 is also preheated, the rise to the processing temperature is further accelerated, and a heat treatment with a constant processing temperature can be performed. In response to directing that the workpiece is also heated from the side of the vessel wall 1b for preheating or supplementary heat during the heating process, the inner wall surface 1ba of the vessel wall 1b is radiated with infrared radiation as the temperature rises. It is useful to have a surface treatment that increases the rate. In this embodiment, the surface treatment is a treatment in which the vessel wall 1b is previously oxidized with superheated steam to form a hydrous oxide film. This coating is black, and its material and color tone combine to make the infrared emissivity of the vessel wall surface 1ba more than 10 times higher than that of the bare metal surface. (Radiation heating) action becomes remarkable.
[0019]
Although the heating of the processing chamber wall 1b by induction heating has been described above, this heating is performed by using a heating means other than induction heating, for example, a rotating processing chamber using a gas burner having a straight flame opening. The structure that heats one wall 1b is also useful as an inexpensive high-efficiency heating means. Moreover, although the heating of the container wall 1b is a desirable component of the apparatus of the present invention, it may be omitted depending on the content of the heat treatment.
[0020]
Next, the induction coil 6B of the steam superheating mechanism 3b is arranged as a heating means for heating the steam, which is an object to be heated, to a temperature higher than 100 ° C. in the steam superheating mechanism 3b. In this embodiment, as shown in FIG. 2, a steam passage for heating steam is a steam passage in which a plurality of tubular bodies 3baa having a small diameter (a diameter sufficiently smaller than the outer diameter of the entire mechanism) are arranged in parallel. The group 3ba is configured, and the water vapor passage group 3ba is induction-heated by an induction coil 6B disposed around the outer periphery thereof. Each small-diameter tubular body 3ba is provided with a strip (not shown) made of a stainless steel plate that is bent in a zigzag shape. By the provision of this strip, the water vapor in the small-diameter tubular body 3ba When the flow is disturbed (including turbulent flow), the efficiency of transmission of the heat of the tube wall of the small-diameter tubular body 3ba, which has been input by induction heating, to the water vapor inside is significantly improved. In addition, although the above-mentioned heating from the outside is indispensable about this steam superheating mechanism, the heating means for that purpose is not limited to the induction heating. For example, it may be performed by gas flame heating.
[0021]
Similarly to the steam superheating mechanism 3b, the steam generating mechanism 3a is also required to be heated from the outside. As the heating means, induction heating in a form according to the induction heating of the steam superheating mechanism 3b can be employed.
[0022]
Next, the induction coil 6 </ b> C of the chimney 5 </ b> A is for detoxifying the steam-based exhaust gas containing the pyrolysis gas and the like by-produced by the heat treatment discharged from the chimney 5 </ b> A at a high temperature. Therefore, in order to efficiently transfer heat from the chimney tube wall to the exhaust in this heating, the chimney 5A is configured by arranging a plurality of small-diameter tubular bodies in parallel according to the embodiment of the water vapor superheating mechanism 3b (not shown). And a baffle is provided (not shown) in each small-diameter tubular body. As the baffle, a steel fiber surface of a steel fiber bundle that has been subjected to a surface treatment having a catalytic function (such as nickel plating) is used. That is, the baffle not only improves the heat transfer efficiency but also has a function of promoting the thermal decomposition and detoxification of harmful components in the exhaust gas. In consideration of the fact that the thermal decomposition and detoxification may involve oxidation of harmful components, an openable small hole or the like for allowing the air for oxidation to flow into the chimney 5A may be provided in the chimney 5A. Good. The induction coil 6C can be replaced by other exhaust heating means such as gas flame heating. Further, depending on the content of the heat treatment, the exhaust heating means itself or the chimney 5A as described above can be omitted.
[0023]
As described above, the measure of performing induction heating by arranging the induction coil 6A or the like in the processing chamber 1 or the like is used to accurately and quickly adjust the temperature distribution in the processing chamber 1 or the time-series temperature program. Very useful.
[0024]
Whether the induction coil 6A or the like needs to be cooled depends on the power required to be input. When cooling is not required, the induction coil 6A, etc. can be constructed by winding a litz wire (conducting wire with a copper thin wire with insulation coating), a normal twisted conducting wire, a copper single wire with a required outer diameter or a copper strip. That's fine. In particular, since a high-frequency current flows through the cross section of the litz wire, the increase in effective resistance when energized at a high frequency is small, and the copper loss is small. Therefore, it is possible to energize without cooling with a thinner wire outer diameter than other wires, which is preferable in terms of both convenience and power efficiency. Next, when cooling is necessary, the induction coil 6A and the like are formed by winding a copper tube, a brass tube, or a copper or brass strip with a tube made of the same material and brazed to the conductor, What is necessary is just to utilize the hollow part of a tube as a cooling water channel. Furthermore, a composite conductor in which the litz wire is inserted into a hollow portion of a flexible sheath such as a plastic tube and the hollow portion is used as a cooling water channel is also useful. This composite conductor is flexible and suitable for in-situ winding. Here, the cooling water that has flowed through the cooling water channel and finished cooling the induction coil 6A and the like is preferably input to the steam generation mechanism 3a and reused as steam raw material water. This is because cooling water that has been cooled can be reused not only as a water resource but also including sensible heat accumulated during cooling. This is because it contributes to reduction.
[0025]
FIG. 2 shows an embodiment in which a solenoid type (bend type) coil is used as the induction coil 6A or the like, but the processing chamber 1 or the steam superheater 3b that operates while rotating is shown in FIG. 4, a saddle type coil 61 and a hairpin type coil 62 as schematically shown in FIG. In both coils, the portions 61a and 62a located along the heated portion function as induction working conductors, and induction heating is performed on the linear regions facing each other. Then, due to the rotation of the processing chamber 1 etc., the wall of the processing chamber 1 etc. is heated over the entire circumference. Incidentally, the solenoid type coil is excellent in induction heating efficiency. On the other hand, according to the saddle type coil and hairpin type coil, the operation of the processing chamber 1 etc. in the apparatus of the present invention (inserting / removing the object to be heated and the entire attachment / detachment) are easy. become.
[0026]
Insulating materials (calcium silicate, glass, alumina, etc.) are gathered on the outer peripheral side of the treatment chamber 1 etc. that is induction-heated by the induction coil 6A etc. or 61 etc. so as to be separated from the induction coils 6A, 61 etc. It is desirable to prevent heat radiation from the processing chamber 1 or the like by disposing the heat insulating layers 8A, 8B, and 8C made of a mat or an alumina molded body. This is because the desired induction heating can be performed with less power consumption.
[0027]
As mentioned above, although the heat processing of the to-be-processed object was demonstrated taking the example of embodiment of the batch type (form to which a to-be-processed object is enclosed in a process chamber) as an example, embodiment of this invention apparatus is not limited to this, Continuous type ( It is good also as an apparatus of the form which heat-processes by the form which carries out a process, supplying a to-be-processed object sequentially in a processing chamber, and letting it pass.
[0028]
【The invention's effect】
The heat treatment apparatus of the present invention is a device for heat-treating an object to be treated with superheated steam in a processing chamber that operates while rotating, and is a steam having a subsequent function of a superheated steam generation mechanism for supplying superheated steam to the processing chamber. The overheating mechanism is arranged in a form that is directly connected to the processing chamber and is operated while rotating together with the processing chamber.
[0029]
In the conventional rotary heat treatment apparatus using superheated steam, the superheated steam is supplied from the superheated steam generation mechanism to the processing chamber via the rotary joint. Therefore, due to the heat-resistant temperature of the rotary joint, The temperature at which the above heat treatment can be performed is limited, and there are restrictions on the application.
[0030]
In the apparatus of the present invention, it is not necessary to arrange the rotary joint in the superheated steam output section where the organic material constituting the rotary joint is severely deteriorated. It was solved. The expansion of the application of heat treatment with superheated steam is desirable for various demands such as recycling of waste, detoxification of harmful substances, and the creation of high-value materials for various resources. is there.
[Brief description of the drawings]
FIG. 1 is a diagram showing a schematic configuration of a conventional rotary heat treatment apparatus.
2A is a diagram showing a schematic configuration of a rotary heat treatment apparatus according to an embodiment of the present invention, FIG. 2B is a front view of the steam superheater shown in FIG. (C) is an AA arrow front view of another form of a water vapor superheated part.
FIG. 3 is a diagram showing a first other example of the induction heating coil used in the rotary heat treatment apparatus according to the embodiment of the present invention.
FIG. 4 is a diagram showing a second other example of the induction heating coil used in the rotary heat treatment apparatus according to the embodiment of the present invention.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 ... Processing chamber 1a ... Covered opening 1b ... Unit wall 1ba of processing chamber 1 ... Inner wall surface 2 of unit wall 1b ... Turning roller 3 ... Superheated steam generation mechanism 3a ... Steam generation mechanism (boiler)
3b ... Steam overheating mechanism 3ba ... Steam passage group 3baa ... Tubular bodies 4A, 4B ... Rotary joint 5 ... Exhaust pipe 5A ... Chimneys 6A, 6B, 6C ... Induction coils 7A, 7B, 7C ... Fluid passages 8A, 8B, 8C ... Thermal insulation layer

Claims (4)

被処理物を収容して又は通過させながら回転する処理室を備え、この処理室に、水蒸気発生機構と水蒸気過熱機構とを備えた過熱水蒸気発生機構から過熱水蒸気を送給して前記被処理物を加熱処理する加熱処理装置において、
前記水蒸気過熱機構は、前記処理室に直結接続されていて、前記処理室と共に回転しながら稼働することを特徴とする加熱処理装置。
A processing chamber is provided that rotates while containing or passing a workpiece, and the processing chamber is configured to supply superheated steam from a superheated steam generation mechanism including a steam generation mechanism and a steam superheating mechanism. In the heat treatment apparatus for heat treatment,
The water vapor superheating mechanism is directly connected to the processing chamber and operates while rotating together with the processing chamber.
前記水蒸気発生機構は、ロータリージョイントを介して前記水蒸気過熱機構に接続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。The heat treatment apparatus according to claim 1, wherein the water vapor generating mechanism is connected to the water vapor superheating mechanism via a rotary joint. 前記処理室には、ロータリージョイントを介して、前記処理室の排気を上方に排出させるための煙突が配備され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 heat treatment apparatus according to claim 1 or 2, wherein a chimney for discharging the exhaust of the processing chamber upward is provided in the processing chamber via a rotary joint. 前記処理室,水蒸気発生機構,水蒸気過熱機構,煙突の少なくとも1つは、水蒸気の通路が導電性の管状体を用いて構成されており、この管状体の外側に、この管状体を誘導加熱するための誘導コイルが配備されていることを特徴とする請求項3に記載の加熱処理装置。At least one of the processing chamber, the steam generation mechanism, the steam superheating mechanism, and the chimney is configured by using a conductive tubular body in the steam passage, and the tubular body is induction-heated outside the tubular body. The heat treatment apparatus according to claim 3, wherein an induction coil is provided.
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JP2006043767A (en) * 2004-06-30 2006-02-16 Dai Ichi High Frequency Co Ltd Method for hot-bending metallic tube
JP2008060026A (en) * 2006-09-04 2008-03-13 Nippon Steel Corp In-furnace installed induction heating device
JP2012107492A (en) * 2010-10-29 2012-06-07 Taiheiyo Material Kk Injection system
JP2013086028A (en) * 2011-10-18 2013-05-13 Kansai Electric Power Co Inc:The Food waste treatment apparatus
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