JP2002206868A - Superheated steam treating furnace - Google Patents

Superheated steam treating furnace

Info

Publication number
JP2002206868A
JP2002206868A JP2000403192A JP2000403192A JP2002206868A JP 2002206868 A JP2002206868 A JP 2002206868A JP 2000403192 A JP2000403192 A JP 2000403192A JP 2000403192 A JP2000403192 A JP 2000403192A JP 2002206868 A JP2002206868 A JP 2002206868A
Authority
JP
Japan
Prior art keywords
superheated steam
heater
tube
superheater
processing
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP2000403192A
Other languages
Japanese (ja)
Other versions
JP3897276B2 (en
Inventor
Kunio Tsurumaki
國夫 鶴巻
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to JP2000403192A priority Critical patent/JP3897276B2/en
Publication of JP2002206868A publication Critical patent/JP2002206868A/en
Application granted granted Critical
Publication of JP3897276B2 publication Critical patent/JP3897276B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/12Heat utilisation in combustion or incineration of waste

Abstract

PROBLEM TO BE SOLVED: To provide a superheated steam treating furnace good in energy efficiency upon raising the temperature of a treating vessel. SOLUTION: The superheated steam treating furnace comprises a superheating heater 20 for generating superheated steam and the treating vessel 10 for carrying out a thermal treatment by the superheated steam generated by the superheating heater 20. The superheating heater 20 is a pipe member generating heat upon turning on a power. The pipe member 20 is bent in the treating vessel 10 to surround an accommodated part P of a member to be treated. The superheating heater 20 has one end 21 of the pipe member connected to the treating vessel 10 and the other end 23 of the pipe member connected to a terminal 24a insulated from the treating vessel 10. At an intermediate part, a spiral part 22 is provided for allowing the steam to flow downward from an upper part. The superheating heater 20 has a jet port 23 for jetting the steam upward from the lower part of the treating vessel 10.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、食品加工、ゴミ焼
却等を行うことの可能な過熱水蒸気処理炉に関するもの
である。さらに詳しくは、過熱水蒸気を発生させる過熱
ヒーターと、この過熱ヒーターにより発生した過熱水蒸
気により熱処理を行う処理容器とを備えた過熱水蒸気処
理炉に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a superheated steam processing furnace capable of performing food processing, refuse incineration, and the like. More specifically, the present invention relates to a superheated steam processing furnace provided with a superheated heater for generating superheated steam and a processing vessel for performing a heat treatment using the superheated steam generated by the superheated heater.

【0002】[0002]

【従来の技術】従来、上述のような過熱水蒸気処理炉と
しては、例えば実開昭57−92763号、特開平3−
83547号、特開平6−90677号公報に記載のも
のが知られている。これらはいずれも過熱炉外で過熱水
蒸気を発生し、これを過熱炉に供給している。
2. Description of the Related Art Conventionally, as a superheated steam treatment furnace as described above, for example, Japanese Utility Model Laid-Open No. 57-92763,
No. 83547 and JP-A-6-90677 are known. All of these generate superheated steam outside the superheating furnace and supply it to the superheating furnace.

【0003】しかし、一旦高温に過熱された過熱水蒸気
であっても、過熱炉に供給した途端、放熱により過熱炉
内の温度上昇は抑制され、十分な処理温度を得ることが
できなかった。また、上記第一の公報記載の技術では、
過熱炉近傍に別途ヒーターを設けて温度制御を行ってい
るが、電力が余分に必要でエネルギー効率がよいとはい
えない。
[0003] However, even if the superheated steam is once heated to a high temperature, as soon as it is supplied to the superheat furnace, the temperature rise in the superheat furnace is suppressed by heat radiation, and a sufficient processing temperature cannot be obtained. In the technology described in the first publication,
Although a separate heater is provided in the vicinity of the superheater to control the temperature, extra power is required and energy efficiency is not high.

【0004】[0004]

【発明が解決しようとする課題】かかる従来の実状に鑑
みて、本発明の目的は、処理容器内の温度を昇温させる
際のエネルギー効率が良い過熱水蒸気処理炉を提供する
ことにある。
SUMMARY OF THE INVENTION In view of such a conventional situation, an object of the present invention is to provide a superheated steam treatment furnace having good energy efficiency when increasing the temperature in a processing vessel.

【0005】[0005]

【課題を解決するための手段】上記目的を達成するた
め、本発明に係る過熱水蒸気処理炉の特徴は、過熱水蒸
気を発生させる過熱ヒーターと、この過熱ヒーターによ
り発生した過熱水蒸気により熱処理を行う処理容器とを
備えた構成において、前記過熱ヒーターが通電により発
熱する管体であり、この管体を前記処理容器内で屈曲さ
せて被処理体の収納部を囲んだことにある。
In order to achieve the above object, a superheated steam processing furnace according to the present invention is characterized by a superheater for generating superheated steam, and a process for performing heat treatment using superheated steam generated by the superheated heater. In the configuration provided with the container, the overheater is a tube that generates heat when energized, and this tube is bent in the processing container to surround the storage section of the object to be processed.

【0006】前記管体は螺旋状に屈曲させることが望ま
しい。この場合、前記過熱ヒーターが前記管体を同方向
に巻回させた一対の螺旋体となるように構成し、各螺旋
体に加える過熱用の電流の向きを互いに異ならせると、
電磁波の発生を抑制できる。
[0006] It is desirable that the tube be bent spirally. In this case, the superheater is configured to be a pair of spirals wound around the tube in the same direction, and the directions of the superheating currents applied to the spirals are different from each other.
Generation of electromagnetic waves can be suppressed.

【0007】前記過熱ヒーターが前記管体の一端を前記
処理容器に接続し、前記管体の他端に前記処理容器と絶
縁された端子を接続してもよい。
[0007] The overheating heater may connect one end of the tube to the processing container, and connect a terminal insulated from the processing container to the other end of the tube.

【0008】前記過熱ヒーターが上から下に向かって水
蒸気を流通させる管体部分と、前記処理容器の下部から
上方に向かって水蒸気を噴出する噴出口とを有していれ
ば、水蒸気を管体内に効率的に滞留させて過熱を十分に
行うことができる。
[0008] If the superheater has a pipe portion through which steam is circulated from top to bottom, and a jet port for jetting steam upward from a lower portion of the processing vessel, the steam is transferred into the pipe. Overheating can be carried out sufficiently.

【0009】被処理体の収納部が前記管体に囲まれると
共に駆動回転される筒状体であり、この筒状体内に前記
過熱ヒーターからの過熱水蒸気を導入してもよい。
[0009] The accommodating portion of the object to be processed may be a cylindrical body that is driven and rotated by being surrounded by the tube, and superheated steam from the superheater may be introduced into the cylindrical body.

【0010】[0010]

【発明の効果】このように、上記本発明に係る過熱水蒸
気処理炉の特徴によれば、管体を処理容器内で屈曲させ
て被処理体の収納部を囲んだので、当該収納部が予熱さ
れた状態で過熱水蒸気を受け入れる。その結果、収納部
を十分に過熱することができ、また、余熱に過熱ヒータ
ー自身の熱を利用しているので、エネルギー効率も非常
に良好となった。本発明の他の目的、構成及び効果につ
いては、以下に示す発明の実施の形態の欄で明らかにな
るであろう。
As described above, according to the characteristics of the superheated steam processing furnace according to the present invention, the tube is bent in the processing vessel to surround the storage section of the object to be processed. Accept superheated steam in the condition. As a result, the storage section could be sufficiently heated, and the heat efficiency of the superheater itself was used for the residual heat, so that the energy efficiency was also very good. Other objects, configurations and effects of the present invention will be apparent in the following embodiments of the present invention.

【0011】[0011]

【発明の実施の形態】次に、添付図面を参照しながら、
本発明をさらに詳細に説明する。図2は、本発明に係る
過熱水蒸気処理装置1のブロック図である。本発明の過
熱水蒸気処理装置1は、食品の焼き加工、焙煎加工、工
業製品の加工、ゴミの焼却、炭化加工等の用途に用いる
ことができる。この過熱水蒸気処理装置1は、浄水導入
管2から取り込んだ水をボイラ3で水蒸気とし、この水
蒸気をヒーター20で加熱することにより過熱水蒸気を
発生させる。処理容器10の中には被処理物が収納され
ており、この処理容器10内にヒーター20から過熱水
蒸気を導入し、熱処理を行う。本発明ではヒーター20
が処理容器10内に収納され、全体として過熱水蒸気処
理炉4を構成する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Next, referring to the attached drawings,
The present invention will be described in more detail. FIG. 2 is a block diagram of the superheated steam processing apparatus 1 according to the present invention. The superheated steam treatment apparatus 1 of the present invention can be used for applications such as baking of food, roasting, processing of industrial products, incineration of garbage, and carbonization. The superheated steam processing apparatus 1 converts water taken in from a purified water introduction pipe 2 into steam in a boiler 3, and heats the steam with a heater 20 to generate superheated steam. An object to be processed is stored in the processing container 10, and superheated steam is introduced from the heater 20 into the processing container 10 to perform heat treatment. In the present invention, the heater 20
Are housed in the processing vessel 10 to constitute the superheated steam processing furnace 4 as a whole.

【0012】排気は高温排気処理装置6により処理され
て不純物が取り除かれた状態で排気管8から排出され
る。但し、処理容器10での処理温度が比較的低く排気
にタール分等が多い場合は、処理容器10の排気をさら
に後過熱ヒーター5により過熱してタール分を分解さ
せ、高温排気処理装置6による処理を行うことが望まし
い。なお、ヒーター20の加熱長さを十分とることによ
って、ボイラ3を省略することも可能である。
The exhaust gas is discharged from the exhaust pipe 8 in a state where the exhaust gas is processed by the high-temperature exhaust processing device 6 to remove impurities. However, when the processing temperature in the processing vessel 10 is relatively low and the exhaust has a large amount of tar, etc., the exhaust of the processing vessel 10 is further heated by the post-heating heater 5 to decompose the tar, and the high-temperature exhaust treatment device 6 It is desirable to perform processing. Note that the boiler 3 can be omitted by making the heating length of the heater 20 sufficient.

【0013】図1に示すように、処理容器10は、円筒
状の容器本体11の上部に開閉自在な蓋体12を嵌合さ
せてあり、複数のボルト13により閉じられる。容器本
体11上部のフランジ11aには網状容器18の上部が
係止し、この網状容器18内部が被処理体の収納部Pと
なる。容器本体11の中央下部に位置する排出部23か
ら過熱蒸気Vが上方に向かって収納部Pに供給される。
また、処理に用いられた排気は排気管14を介して外部
に排出される。
As shown in FIG. 1, the processing container 10 has a lid 12 that is openable and closable fitted on the upper part of a cylindrical container body 11 and is closed by a plurality of bolts 13. The upper portion of the mesh container 18 is engaged with the flange 11a on the upper portion of the container body 11, and the inside of the mesh container 18 becomes a storage portion P for the object to be processed. Superheated steam V is supplied to the storage section P upward from the discharge section 23 located at the lower center of the container body 11.
Further, the exhaust gas used for the processing is exhausted to the outside through the exhaust pipe 14.

【0014】ヒーター20はステンレス製等により構成
された管体を螺旋状に巻回したもので、導入部21から
取り込んだ水蒸気を螺旋部22により過熱しながら下方
に向かって誘導し、容器本体11の下部中央に位置する
排出部23から過熱水蒸気Vを噴出する。螺旋部22は
網状容器18の周りを取り囲み、螺旋部22の熱は網状
容器18内の収納部Pに輻射される。
The heater 20 is formed by spirally winding a tube made of stainless steel or the like. The heater 20 guides the steam taken in from the introduction portion 21 downward while heating the steam with the spiral portion 22. The superheated steam V is ejected from the discharge part 23 located at the lower center of the container. The spiral portion 22 surrounds the mesh container 18, and the heat of the spiral portion 22 is radiated to the storage portion P in the mesh container 18.

【0015】ヒーター20の導入部21側は容器本体1
1に対して直接導電状態で取り付けられ、この導入部2
1側がアースとなる。また、螺旋部22は複数の碍子1
5や下碍子16により容器本体11と絶縁された状態で
その位置を固定される。端子ねじ24aは容器本体11
に形成した孔に筒碍子17を介して挿通され、2つのナ
ット24b、24bに締め付けられて絶縁状態で容器本
体11に固定される。この電極24の一端は端子板24
cにより排出部23側と接続され、電源30の陽極が端
子ねじ24aを介して排出部23に接続される。
The introduction portion 21 side of the heater 20 is the container body 1
1 is mounted directly in a conductive state with respect to
One side is grounded. In addition, the spiral portion 22 includes a plurality of insulators 1.
The position is fixed while being insulated from the container main body 11 by the lower insulator 5 and the lower insulator 16. The terminal screw 24a is connected to the container body 11
Is fixed to the container body 11 in an insulated state by being inserted through the hole formed through the cylindrical insulator 17 and tightened by the two nuts 24b, 24b. One end of this electrode 24 is a terminal plate 24
The terminal c is connected to the discharge unit 23 side, and the anode of the power supply 30 is connected to the discharge unit 23 via the terminal screw 24a.

【0016】図示省略するが、処理容器10の周囲には
グラスウール等の断熱材料を巻き付けることが望まし
い。また、容器本体11は二重構造としても構わない。
Although not shown, it is desirable to wind a heat insulating material such as glass wool around the processing vessel 10. Further, the container body 11 may have a double structure.

【0017】例えば、ヒーター20にステンレスの管体
を使用した場合、電源30としては数十ボルトの直流又
は交流電源を用いればよい。200〜300A等の大電
流を通電させることで、少なくとも800℃程度にまで
収納部Pを昇温することができる。
For example, when a stainless steel tube is used for the heater 20, a DC or AC power supply of several tens of volts may be used as the power supply 30. By energizing a large current such as 200 to 300 A, the temperature of the storage section P can be raised to at least about 800 ° C.

【0018】ところで、ヒーター20は螺旋部22を有
し、大電流を流すことにより強力な磁場が発生するの
で、シールドを施さねば電磁気障害の発生源となる。そ
こで、図3〜6に示すように、ヒーター20として第一
ヒーター20a,第二ヒーター20bという二つの同方
向に巻回された螺旋体を組合せ、電源30により互いに
逆極性の電流を通電させることで逆磁場を発生させ、ト
ータルの磁束を減少させることが可能である。なお、こ
れらの図において、電源30は極性の説明のために直流
電源として表示するが、極性を逆に設定した交流電源を
用いても勿論構わない。
The heater 20 has a helical portion 22 and generates a strong magnetic field when a large current flows. Therefore, if the heater 20 is not shielded, it becomes a source of electromagnetic interference. Therefore, as shown in FIGS. 3 to 6, two spiral bodies wound in the same direction, that is, a first heater 20 a and a second heater 20 b, are combined as the heater 20, and currents having opposite polarities are supplied by the power supply 30. It is possible to generate a reverse magnetic field and reduce the total magnetic flux. In these figures, the power source 30 is shown as a DC power source for the sake of explanation of the polarity, but an AC power source with the polarity set in reverse may of course be used.

【0019】図3では、第一ヒーター20aと第二ヒー
ター20bとが上部の連結部20cで結合されている。
低温水蒸気は第一ヒーター20aの下部に位置する導入
部21から導入され、第二ヒーター20bの下部に位置
する排出部23から上方に向かって過熱水蒸気を噴出す
る。電源30は導入部21,排出部23間に接続され
る。図4におけるヒーター20は図3と同様であるが、
電源30、30をそれぞれ導入部21と連結部20c
間、及び排出部23と連結部20c間に接続している点
が異なる。
In FIG. 3, the first heater 20a and the second heater 20b are connected by an upper connecting portion 20c.
The low-temperature steam is introduced from an inlet 21 located below the first heater 20a, and ejects superheated steam upward from an outlet 23 located below the second heater 20b. The power supply 30 is connected between the introduction section 21 and the discharge section 23. The heater 20 in FIG. 4 is the same as in FIG.
The power supplies 30, 30 are connected to the introduction section 21 and the connection section 20c, respectively.
The difference is that the connection is made between the discharge part 23 and the connecting part 20c.

【0020】図5では、第一ヒーター20aと第二ヒー
ター20bとが並行に巻回され、低温水蒸気は双方の上
部に位置する導入部21、21からそれぞれ導入され、
双方の下部に位置する排出部23,23からそれぞれ上
方に向かって過熱水蒸気を噴出する。第一ヒーター20
a、第二ヒーター20bそれぞれの導入部21,21と
排出部23,23間には互いに逆極性の関係で電源3
0,30が接続される。図6におけるヒーター20は図
5と同様であるが、排出部23,23同士を短絡部31
で導通し、電源30をそれぞれの導入部21,21間に
接続している点が異なる。
In FIG. 5, the first heater 20a and the second heater 20b are wound in parallel, and the low-temperature steam is introduced from the inlets 21 located above both, respectively.
Superheated steam is spouted upward from discharge sections 23, 23 located at both lower portions. First heater 20
a, the power supply 3 is connected between the inlets 21 and 21 and the outlets 23 and 23 of the second heater 20b in opposite polarities.
0 and 30 are connected. The heater 20 in FIG. 6 is the same as that in FIG. 5 except that the discharge portions 23 are short-circuited to each other.
And the power supply 30 is connected between the introduction sections 21 and 21.

【0021】次に、過熱水蒸気処理炉4の異なる実施形
態として、図7を参照しながら焙煎機40について説明
する。なお、上述の実施形態と同様の部材については同
様の符号を付してある。
Next, as another embodiment of the superheated steam treatment furnace 4, a roasting machine 40 will be described with reference to FIG. The same members as those in the above-described embodiment are denoted by the same reference numerals.

【0022】本実施形態の焙煎機40は、例えばコーヒ
ー豆を焙煎するものであって、外容器41内にヒーター
20が収納され、さらにそのヒーター20の螺旋部22
内に回転する内容器42が収納されている。内容器42
は両端の軸受43a,43aで外容器41に支持され、
軸43周りで回転する。軸43はモーター45によりチ
エン46を介して駆動回転される。
The roasting machine 40 of the present embodiment roasts, for example, coffee beans. The heater 20 is housed in an outer container 41, and the helical portion 22 of the heater 20 is provided.
A rotating inner container 42 is housed therein. Inner container 42
Is supported by the outer container 41 by bearings 43a at both ends,
It rotates around the axis 43. The shaft 43 is driven and rotated by a motor 45 via a chain 46.

【0023】本実施形態のヒーター20では、下方に位
置する導入部21から低温水蒸気が導入され、螺旋部2
2を上方に向かって通過しながら昇温し、排出部23か
ら図示省略する回転継手を介して中筒44内に導入され
る。中筒44は内容器42を貫通し、多数の小孔44a
から供給された過熱水蒸気を内容器42内の収納部Pに
噴出し、蒸気加工を行う。内容器42内には複数の羽4
2aが突出し、収納部P内のコーヒー豆等を攪拌する。
なお、使用に際しては、焙煎機40全体が傾斜状態で回
転動作を行うこととなる。本装置はコーヒー豆以外の焙
煎や、その他工業製品の過熱水蒸気処理にも用いること
ができる。
In the heater 20 of the present embodiment, low-temperature steam is introduced from an introduction portion 21 located below, and
2 rises while passing upward, and is introduced into the middle cylinder 44 from the discharge section 23 via a rotary joint (not shown). The middle cylinder 44 penetrates the inner container 42 and has many small holes 44a.
Superheated steam supplied from the container is ejected into the storage section P in the inner container 42 to perform steam processing. In the inner container 42, a plurality of feathers 4
2a protrudes and stirs the coffee beans and the like in the storage section P.
In use, the entire roasting machine 40 performs a rotating operation in an inclined state. This apparatus can be used for roasting other than coffee beans and for superheated steam treatment of other industrial products.

【0024】最後に、本発明のさらに他の実施形態の可
能性について説明する。上記実施形態では、ヒーター2
0を構成する管体を螺旋状に巻回させることで、収納部
Pを囲むように構成した。しかし、ヒーター20の管体
を上下や左右に蛇行させて収納部Pをヒーター20によ
り囲んでも構わない。但し、処理容器10内の水平方向
に対する温度分布を均質にする点で、螺旋状の管体配置
が優れている。
Finally, the possibility of another embodiment of the present invention will be described. In the above embodiment, the heater 2
0 was spirally wound so as to surround the storage portion P. However, the housing P may be surrounded by the heater 20 by meandering the tube of the heater 20 up and down or left and right. However, the spiral tube arrangement is excellent in that the temperature distribution in the horizontal direction in the processing container 10 is made uniform.

【0025】上記実施形態では、ヒーター20の管体と
してステンレス等を用いた。しかし、ヒーター20の管
体としては電気抵抗発熱体に用いられるような抵抗値の
高い部材を用いても良く、この場合、電源30として1
00V、200V等の商用電源を使用することも可能で
ある。
In the above embodiment, stainless steel or the like is used for the tube of the heater 20. However, a member having a high resistance value, such as that used for an electric resistance heating element, may be used as the tube of the heater 20.
It is also possible to use a commercial power supply such as 00V or 200V.

【0026】上記実施形態では、ヒーター20に排出部
23を一つのみ設けた。しかし、排出部23は複数あっ
てもよく、ヒーター20の構成により適宜変更が可能で
ある。
In the above embodiment, the heater 20 is provided with only one discharge section 23. However, a plurality of discharge units 23 may be provided, and the discharge units 23 can be appropriately changed depending on the configuration of the heater 20.

【0027】なお、上記各実施形態は相互に組み合わせ
て実施することができる。また、特許請求の範囲の項に
記入した符号は、あくまでも図面との対照を便利にする
ためのものにすぎず、該記入により本発明は添付図面の
構成に限定されるものではない。
The embodiments described above can be implemented in combination with each other. Further, reference numerals written in the claims are merely for convenience of comparison with the drawings, and the present invention is not limited to the configuration of the attached drawings by the writing.

【図面の簡単な説明】[Brief description of the drawings]

【図1】過熱水蒸気処理炉における処理容器の断面図で
ある。
FIG. 1 is a sectional view of a processing vessel in a superheated steam processing furnace.

【図2】過熱水蒸気処理装置のブロック図である。FIG. 2 is a block diagram of a superheated steam processing apparatus.

【図3】過熱ヒーターの第一の別実施形態を示す斜視図
である。
FIG. 3 is a perspective view showing a first alternative embodiment of the superheater.

【図4】過熱ヒーターの第二の別実施形態を示す斜視図
である。
FIG. 4 is a perspective view showing a second alternative embodiment of the superheater.

【図5】過熱ヒーターの第三の別実施形態を示す斜視図
である。
FIG. 5 is a perspective view showing a third alternative embodiment of the superheater.

【図6】過熱ヒーターの第四の別実施形態を示す斜視図
である。
FIG. 6 is a perspective view showing a fourth alternative embodiment of the superheater.

【図7】過熱水蒸気処理炉の別実施形態を示す断面図で
ある。
FIG. 7 is a sectional view showing another embodiment of the superheated steam processing furnace.

【符号の説明】[Explanation of symbols]

1 過熱水蒸気処理装置 2 浄水導入管 3 ボイラ 4 過熱水蒸気処理炉 5 後過熱ヒーター 6 高温排気処理装置 8 排気管 10 処理容器 11 容器本体 11a フランジ 12 蓋体 13 ボルト 14 排気管 15 碍子 16 下碍子 17 筒碍子 18 網状容器 20 ヒーター 20a、b 第一、第二ヒーター 20c 連結部 21 導入部 22 螺旋部 23 排出部 24 電極 24a 端子ねじ 24b ナット 24c 端子板 30 電源 31 短絡部 40 焙煎機 41 外容器 42 内容器 42a 羽根 43 軸 43a 軸受 44 中筒 44a 小孔 45 モーター 46 チエン E アース P 収納部 DESCRIPTION OF SYMBOLS 1 Superheated steam processing apparatus 2 Purified water introduction pipe 3 Boiler 4 Superheated steam processing furnace 5 Post-superheater 6 High temperature exhaust processing apparatus 8 Exhaust pipe 10 Processing vessel 11 Container body 11a Flange 12 Lid 13 Bolt 14 Exhaust pipe 15 Insulator 16 Lower insulator 17 Cylindrical insulator 18 Reticulated container 20 Heater 20a, b First and second heaters 20c Connecting portion 21 Introducing portion 22 Spiral portion 23 Discharging portion 24 Electrode 24a Terminal screw 24b Nut 24c Terminal plate 30 Power supply 31 Short-circuit portion 40 Roasting machine 41 Outer container 42 inner container 42a blade 43 shaft 43a bearing 44 middle cylinder 44a small hole 45 motor 46 chain E ground P storage section

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) F23G 5/46 ZAB F23G 5/46 ZABZ ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ゛ (Reference) F23G 5/46 ZAB F23G 5/46 ZABZ

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 過熱水蒸気を発生させる過熱ヒーター
(20)と、この過熱ヒーター(20)により発生した
過熱水蒸気により熱処理を行う処理容器(10)とを備
えた過熱水蒸気処理炉であって、前記過熱ヒーター(2
0)が通電により発熱する管体であり、この管体(2
0)を前記処理容器(10)内で屈曲させて被処理体の
収納部(P)を囲んである管過熱水蒸気処理炉。
1. A superheated steam processing furnace comprising: a superheater (20) for generating superheated steam; and a processing vessel (10) for performing heat treatment by the superheated steam generated by the superheated heater (20). Superheater (2
0) is a tube that generates heat when energized, and this tube (2)
0) a tube superheated steam treatment furnace which bends the inside of the processing container (10) to surround the storage section (P) of the object to be processed.
【請求項2】 前記管体(20)を螺旋状に屈曲させて
ある請求項1に記載の過熱水蒸気処理炉。
2. A superheated steam treatment furnace according to claim 1, wherein said tube (20) is spirally bent.
【請求項3】 前記過熱ヒーター(20)が前記管体を
同方向に巻回させた一対の螺旋体(20a、20b)で
あり、各螺旋体(20a、20b)に加える過熱用の電
流の向きを互いに異ならせてある請求項2に記載の過熱
水蒸気処理炉。
3. The superheater (20) is a pair of spiral bodies (20a, 20b) obtained by winding the tubular body in the same direction, and determines the direction of a current for superheating applied to each spiral body (20a, 20b). 3. The superheated steam treatment furnace according to claim 2, wherein the furnaces are different from each other.
【請求項4】 前記過熱ヒーター(20)が前記管体の
一端(21)を前記処理容器(10)に接続し、前記管
体の他端(23)に前記処理容器(10)と絶縁された
端子(24a)を接続してある請求項1〜3のいずれか
に記載の過熱水蒸気処理炉。
4. The superheater (20) connects one end (21) of the tube to the processing vessel (10), and the other end (23) of the tube is insulated from the processing vessel (10). The superheated steam treatment furnace according to any one of claims 1 to 3, further comprising a terminal (24a) connected thereto.
【請求項5】 前記過熱ヒーター(20)が上から下に
向かって水蒸気を流通させる管体部分(22)と、前記
処理容器(10)の下部から上方に向かって水蒸気を噴
出する噴出口(23)とを有している請求項2〜4のい
ずれかに記載の過熱水蒸気処理炉。
5. A pipe section (22) through which the superheater (20) circulates steam from top to bottom, and a jet port (20) for jetting steam upward from a lower portion of the processing vessel (10). The superheated steam treatment furnace according to any one of claims 2 to 4, comprising:
【請求項6】 被処理体の収納部(P)が前記管体(2
0)に囲まれると共に駆動回転される筒状体(42)で
あり、この筒状体(42)内に前記過熱ヒーター(2
0)からの過熱水蒸気を導入してある請求項1〜5のい
ずれかに記載の過熱水蒸気処理炉。
6. A storage section (P) for an object to be processed is provided in said tubular body (2).
0) is a cylindrical body (42) that is driven and rotated while being surrounded by the superheater (2).
The superheated steam treatment furnace according to any one of claims 1 to 5, wherein superheated steam from (0) is introduced.
JP2000403192A 2000-12-28 2000-12-28 Superheated steam treatment furnace Expired - Fee Related JP3897276B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000403192A JP3897276B2 (en) 2000-12-28 2000-12-28 Superheated steam treatment furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000403192A JP3897276B2 (en) 2000-12-28 2000-12-28 Superheated steam treatment furnace

Publications (2)

Publication Number Publication Date
JP2002206868A true JP2002206868A (en) 2002-07-26
JP3897276B2 JP3897276B2 (en) 2007-03-22

Family

ID=18867362

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
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Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007143550A (en) * 2005-11-04 2007-06-14 Fuji Koki:Kk Roasting apparatus, roasting method, smoke remover and method for removing smoke
JP2007178089A (en) * 2005-12-28 2007-07-12 Fuji Electric Systems Co Ltd Induction heating type steam generating device
KR100828095B1 (en) 2007-02-22 2008-05-08 주식회사 씨엔엘에너지 A gas humidifier for a fuel cell
JP2009192184A (en) * 2008-02-17 2009-08-27 Thermo Electron Kk Aluminum melting furnace, heat treatment apparatus, and casting system
CN102297583A (en) * 2011-07-26 2011-12-28 浙江省长兴精工电炉制造有限公司 Steam oxidation well furnace
CN102727071A (en) * 2011-04-15 2012-10-17 松下电器产业株式会社 Electric cooker
CN113165939A (en) * 2018-12-13 2021-07-23 奥林巴斯株式会社 Heating furnace
JP2021135023A (en) * 2020-02-28 2021-09-13 株式会社吉野家ホールディングス Heating cooker using superheated steam

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007143550A (en) * 2005-11-04 2007-06-14 Fuji Koki:Kk Roasting apparatus, roasting method, smoke remover and method for removing smoke
JP2007178089A (en) * 2005-12-28 2007-07-12 Fuji Electric Systems Co Ltd Induction heating type steam generating device
JP4552851B2 (en) * 2005-12-28 2010-09-29 富士電機システムズ株式会社 Induction heating steam generator
KR100828095B1 (en) 2007-02-22 2008-05-08 주식회사 씨엔엘에너지 A gas humidifier for a fuel cell
JP2009192184A (en) * 2008-02-17 2009-08-27 Thermo Electron Kk Aluminum melting furnace, heat treatment apparatus, and casting system
CN102727071A (en) * 2011-04-15 2012-10-17 松下电器产业株式会社 Electric cooker
CN102297583A (en) * 2011-07-26 2011-12-28 浙江省长兴精工电炉制造有限公司 Steam oxidation well furnace
CN102297583B (en) * 2011-07-26 2014-02-19 浙江省长兴精工电炉制造有限公司 Steam oxidation well furnace
CN113165939A (en) * 2018-12-13 2021-07-23 奥林巴斯株式会社 Heating furnace
JP2021135023A (en) * 2020-02-28 2021-09-13 株式会社吉野家ホールディングス Heating cooker using superheated steam
JP7377742B2 (en) 2020-02-28 2023-11-10 株式会社吉野家ホールディングス Food cooking device using superheated steam

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