JP5615539B2 - Continuous heat treatment method and continuous heat treatment apparatus - Google Patents

Continuous heat treatment method and continuous heat treatment apparatus Download PDF

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JP5615539B2
JP5615539B2 JP2009278614A JP2009278614A JP5615539B2 JP 5615539 B2 JP5615539 B2 JP 5615539B2 JP 2009278614 A JP2009278614 A JP 2009278614A JP 2009278614 A JP2009278614 A JP 2009278614A JP 5615539 B2 JP5615539 B2 JP 5615539B2
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小笠原 幸雄
幸雄 小笠原
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Taiyo Seisakusho Co Ltd
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本発明は、処理対象物を連続して加熱処理可能な加熱処理方法及び加熱処理装置に関し、詳しくは、この種の連続式加熱処理方法及び装置において、加熱処理室内部からの加熱媒体の流出及び加熱処理室内部への外気の混入を防止する。   The present invention relates to a heat treatment method and a heat treatment apparatus capable of continuously heat-treating an object to be treated. Specifically, in this type of continuous heat treatment method and apparatus, the outflow of a heating medium from the inside of the heat treatment chamber and Prevents outside air from entering the heat treatment chamber.

従来から食材や食品などを加熱加工処理(調理・殺菌など)するため、加熱媒体として水蒸気を用いていたものが広く知られている。特に、過熱水蒸気などの加熱媒体を用いて加熱加工処理することが昨今注目されている。
過熱水蒸気は、飽和水蒸気を更に加熱することにより、ある圧力において飽和温度以上の蒸気温度を持って発生する。過熱水蒸気は外気に触れて温度が下がっても、過熱状態を保っていれば凝縮せず、同じ圧力の飽和水蒸気よりも大きな熱量を保有している。例えば、食材の加熱において、食材の低温時には初期凝縮が発生して、飽和水蒸気同様に潜熱による凝縮伝熱が起こるが、食材の品温上昇に伴い、凝縮現象は消えて食材中水分の蒸発が始まる。この結果、食材内部への凝縮水流入が無く、味の変化や成分溶出の少ない加熱処理方法として過熱水蒸気が用いられている。
2. Description of the Related Art Conventionally, in order to heat processing (cooking, sterilization, etc.) foods, foods, etc., those using water vapor as a heating medium are widely known. In particular, attention has recently been paid to heat processing using a heating medium such as superheated steam.
Superheated steam is generated with a steam temperature higher than the saturation temperature at a certain pressure by further heating the saturated steam. Even if the superheated steam is exposed to the outside air and the temperature is lowered, the superheated steam is not condensed if the superheated state is maintained, and has a larger amount of heat than the saturated steam at the same pressure. For example, in the heating of foodstuffs, initial condensation occurs at low temperature of the foodstuffs, and condensation heat transfer due to latent heat occurs as in the case of saturated steam, but as the product temperature rises, the condensation phenomenon disappears and moisture in the foodstuffs evaporates Begins. As a result, superheated steam is used as a heat treatment method that does not cause the inflow of condensed water into the food and has little change in taste and elution of components.

また、食材や食品などを加熱処理する場合、その生産性を向上させるため、無端状に連続したコンベア等を使用して所定の長さ・形状の加熱処理室内で連続処理するのが一般的である。そこで、例えば、上述のように過熱水蒸気などの加熱媒体を用いて連続処理する装置として、特許文献1などが知られている。   In addition, when heat-treating foods and foods, in order to improve the productivity, it is common to continuously process them in a heat treatment chamber of a predetermined length and shape using an endless continuous conveyor or the like. is there. Thus, for example, Patent Document 1 is known as an apparatus that performs continuous processing using a heating medium such as superheated steam as described above.

ここで、特許文献1を含め、過熱水蒸気などの加熱媒体を用いて加熱処理する連続式の加熱処理装置について簡単に説明すると、入口側と出口側にそれぞれ処理対象物が通過可能な開口を備えた加熱処理室と、この入口側の開口と出口側の開口にわたって加熱処理室内に連続して処理対象物を搬送する無端状のコンベアと、この加熱処理室内に加熱媒体(過熱水蒸気)を噴射する加熱媒体生成噴射装置とを備えて構成されている。
この種の装置によれば、加熱処理室内にコンベアによって搬送されてきた処理対象物に加熱媒体(過熱水蒸気)を噴射することによって加熱処理していたものである。また、連続して噴射される加熱媒体(過熱水蒸気)によって加熱処理室内を所定の加熱処理雰囲気(過熱水蒸気雰囲気)に維持させようとしているものである。
Here, a brief description will be given of a continuous heat treatment apparatus that performs heat treatment using a heating medium such as superheated steam, including Patent Document 1, and an opening through which an object to be treated can pass is provided on each of an inlet side and an outlet side. A heat treatment chamber, an endless conveyor that continuously conveys the object to be processed over the opening on the inlet side and the opening on the outlet side, and a heating medium (superheated steam) is injected into the heat treatment chamber. And a heating medium generating / injecting device.
According to this kind of apparatus, it heat-processes by injecting a heating medium (superheated steam) to the process target object conveyed by the conveyor in heat processing chamber. In addition, the heat treatment chamber (superheated steam) is continuously maintained to be maintained in a predetermined heat treatment atmosphere (superheated steam atmosphere) by the heating medium (superheated steam).

しかし、コンベア等を使用して連続処理する場合、加熱処理室内を処理対象物が順次連続して搬送可能なように、加熱処理室は中空状で、かつ入口側と出口側にそれぞれ処理対象物が通過可能な程度の開口を備えた非密閉空間を採用せざるを得ない。
このように入口側と出口側に開口が開いているため、この開口から加熱処理室内の加熱媒体(過熱水蒸気)が逃げて(漏れて)しまうことがあり、また、この開口から外気(空気)が混入されてしまうこともあり、所定の加熱処理雰囲気を維持できなくなってしまうという不都合があった。
加熱処理室内からの加熱媒体の流出や加熱処理室内への外気(空気)混入は、水蒸気濃度の低下や食材表面温度の上昇速度の低下などが発生し、食材の加熱に障害がでるばかりか、殺菌効果にも大きな影響が有る。すなわち、加熱処理装置、特にこの種の連続式加熱処理装置において加熱媒体の室外への流出及び外気遮断は重要な要素となる。
However, when continuous processing is performed using a conveyor or the like, the heat treatment chamber is hollow so that the treatment objects can be sequentially conveyed in the heat treatment chamber, and the treatment objects are respectively provided on the inlet side and the outlet side. It is necessary to adopt a non-sealed space having an opening that can pass through.
Since the openings are opened on the inlet side and the outlet side in this way, the heating medium (superheated steam) in the heat treatment chamber may escape (leak) from the openings, and the outside air (air) may be discharged from the openings. May be mixed in, and a predetermined heat treatment atmosphere cannot be maintained.
Outflow of the heating medium from the heat treatment chamber and mixing of outside air (air) into the heat treatment chamber will cause a decrease in the water vapor concentration and a decrease in the rate of increase in the surface temperature of the food, and this will hinder the heating of the food. There is also a great influence on the bactericidal effect. That is, in the heat treatment apparatus, particularly in this type of continuous heat treatment apparatus, the outflow of the heating medium to the outside and the blocking of the outside air are important factors.

前記特許文献1では、このような加熱媒体の室外への流出及び外気遮断を図るための遮蔽機構を含む提案をしている。
すなわち、特許文献1では、開口している入口側と出口側にそれぞれカーテンを配設し、処理対象物が加熱処理室に入る時と加熱処理室から出る時のみ、カーテンを押し開いて開口を通過し、それ以外の時は、カーテンによってそれぞれの開口を閉じて加熱媒体の室外への流出及び外気遮断を図るものとしている。
Patent Document 1 proposes a shielding mechanism for preventing the heating medium from flowing out of the room and blocking the outside air.
That is, in Patent Document 1, curtains are provided on the entrance side and the exit side, respectively, and the curtain is pushed open when the object to be processed enters and exits the heat treatment chamber. At other times, the openings are closed by curtains so that the heating medium flows out of the room and the outside air is blocked.

また、特許文献2も特許文献1と同様の構成を有しており、開口している入口側と出口側にそれぞれのれん状の緩衝シール材を配設し、処理対象物が加熱処理室に入る時と加熱処理室から出る時のみ、前記緩衝シール材を押し開いて開口を通過し、それ以外の時は、緩衝シール材によってそれぞれの開口を閉じて加熱媒体の室外への流出・外気遮断を図るものとしている。   Further, Patent Document 2 has the same configuration as Patent Document 1, and each buffer-like cushioning seal material is disposed on the inlet side and the outlet side that are open, and the object to be processed enters the heat treatment chamber. The buffer sealant is pushed open and passed through the opening only when leaving the heat treatment chamber, and at other times, the opening is closed by the buffer sealant to block the heating medium from flowing out and outside air. It is intended.

しかし、このように入口側と出口側に配設したカーテンや緩衝シール材を処理対象物が通過する際に押し開く遮蔽機構では次のような不都合が生じてしまう。
(1)このカーテンや緩衝シール材は、処理対象物が通過する際に処理対象物によって容易に押し開くことができる程度であるため、加熱処理室内に噴射される加熱媒体の圧力によって通過時以外でも加熱処理室内の加熱媒体が室外へと流出してしまう。
(2)さらに、このように入口側と出口側に処理対象物が押し開いて通過する遮蔽機構では、加熱処理されて加熱処理室内から搬送される処理対象物(処理済対象物)にカーテンや緩衝シール材が接触するため、処理対象物(処理済対象物)に雑菌などが付着してしまう虞もあった。
However, the shielding mechanism that pushes the object to be processed when it passes through the curtain and the buffer seal material disposed on the inlet side and the outlet side as described above causes the following inconvenience.
(1) Since the curtain and the buffer seal material are such that they can be easily pushed open by the processing object when the processing object passes, the curtain and the buffer sealing material are not at the time of passing due to the pressure of the heating medium sprayed into the heat processing chamber. However, the heating medium in the heat treatment chamber flows out to the outside.
(2) Furthermore, in the shielding mechanism in which the object to be processed is pushed open to the entrance side and the outlet side in this way, a curtain or the like is added to the object to be processed (processed object) that is heated and conveyed from the heat treatment chamber. Since the buffer seal material is in contact, there is a possibility that various bacteria may adhere to the processing object (processed object).

そこで、このような機械的な遮蔽機構を使用せずに加熱媒体の室外への流出・外気遮断を図る技術的手段を提供する先行技術として特許文献3が提案されている。
特許文献3は、過熱水蒸気は空気よりも軽いという特性に着眼し、過熱水蒸気が滞留し易い機構を採用している。
具体的には、入口側と出口側にそれぞれ処理対象物が搬送して通過可能な開口(以下、開口入口と開口出口とも言う。)をそれぞれ設けた加熱処理室を使用しているが、前記開口入口と開口出口にわたって連通する加熱処理室内の処理対象物搬送空間を段差状に構成しているものである。すなわち、開口入口側と開口出口側を低位置とするとともに、加熱媒体を噴射して加熱処理する処理領域(加熱処理雰囲気領域)を高位置となるように設計している。
これによれば、空気よりも軽い過熱水蒸気は、開口入口や開口出口よりも高位置な処理領域に滞留することとなるため、処理領域よりも低位置の開口入口や開口出口から外部へと流出してしまう虞がない、というものである。したがって、この技術的手段によれば、カーテンや緩衝シール材などの機械的な遮蔽機構を別途開口入口や開口出口に備えなくとも良いということである。
Therefore, Patent Document 3 has been proposed as a prior art that provides technical means for preventing the heating medium from flowing out of the room and blocking outside air without using such a mechanical shielding mechanism.
Patent document 3 pays attention to the characteristic that superheated steam is lighter than air, and employs a mechanism in which superheated steam tends to stay.
Specifically, the heat treatment chamber provided with openings (hereinafter also referred to as opening inlets and opening outlets) through which the object to be processed can be conveyed and passed on the inlet side and the outlet side, respectively, is used. A processing object conveyance space in the heat treatment chamber communicating between the opening inlet and the opening outlet is configured in a step shape. In other words, the opening inlet side and the opening outlet side are set to low positions, and the processing region (heating treatment atmosphere region) in which the heating medium is sprayed and heat-treated is set to a high position.
According to this, superheated steam that is lighter than air stays in the processing area higher than the opening inlet and the outlet outlet, and therefore flows out from the opening inlet and outlet outlet located lower than the processing area. That is, there is no risk of doing so. Therefore, according to this technical means, it is not necessary to separately provide a mechanical shielding mechanism such as a curtain or a buffer seal material at the opening inlet or the opening outlet.

しかし、このような先行技術であっても、開口入口や開口出口にて何等外部との遮蔽を施していない状態であったため、加熱処理室内(処理領域)への外気混入を防止することが十分に成し得ておらず、加熱処理室内への外気混入により、水蒸気濃度の低下や食材表面温度の上昇速度の低下などが発生し、食材の加熱に障害が出るばかりか、殺菌効果にも大きな影響が出ている。   However, even such a prior art is in a state in which no external shielding is applied at the opening inlet or the outlet outlet, it is sufficient to prevent outside air from being mixed into the heat treatment chamber (processing area). However, the mixing of outside air into the heat treatment chamber causes a decrease in water vapor concentration and a decrease in the rate of increase in the surface temperature of the food, which not only hinders the heating of the food, but also has a great sterilizing effect. There is an impact.

そこで、本発明者は、水蒸気を使用して食材などの処理対象物を連続して加熱処理する連続式の加熱処理手段において、加熱処理室外への加熱媒体の流出防止とともに加熱処理室内(処理領域)への外気混入を防止し得る新規技術的手段を発明するに鋭意研究を重ねた。   In view of this, the present inventor, in a continuous heat treatment means for continuously heat-treating a processing object such as a foodstuff using water vapor, prevents the heating medium from flowing out of the heat treatment chamber, and in the heat treatment chamber (treatment region). ) Has intensively studied to invent a new technical means that can prevent outside air from being mixed into the air.

また、本発明者は、加熱処理する際の加熱媒体として、一般に知られている過熱水蒸気とは異なる新たな加熱媒体を提供すべく特許文献4を含む多数の出願を既にしている。具体的には、次の構成を有している。
加熱処理室内を、常圧で、かつ処理室内加熱機構によって115℃程度に加熱制御し、
加熱媒体生成機構は、水供給源から供給された水を流通させる管路を内装するとともに、前記管路内に供給された水を所定温度及び所定圧力で沸騰させることで管内に水蒸気と熱水からなる気液混合体を生成し、前記管路の先端部に備え、内圧0.19MPa以上、ノズル内部温度120℃以上、及びノズル内水量0.7gr/sec以上に制御した加熱媒体噴射ノズルを介して前記気液混合体を前記制御された加熱処理室内に噴出することにより、前記加熱処理室内を過熱水蒸気と高温微細水滴が混在する状態の加熱媒体で満たされた加熱処理雰囲気に調整している。
しかし、この種の構成を有している加熱処理装置はバッチ式のものであったため、生産性を向上させることは到底成し得なかった。このような新規な加熱媒体を用いて加熱処理するものであっても非密閉状の加熱室内で同様の効果を得ることは困難である。そこで、この種の加熱処理装置を連続式の加熱処理装置に変える要望も高いため、今般の開発において併せて行うものとした。
The present inventor has already filed a number of applications including Patent Document 4 to provide a new heating medium different from the generally known superheated steam as a heating medium for the heat treatment. Specifically, it has the following configuration.
The inside of the heat treatment chamber is heated to normal pressure and about 115 ° C. by the treatment chamber heating mechanism,
The heating medium generation mechanism includes a pipeline for circulating the water supplied from the water supply source, and boiles the water supplied in the pipeline at a predetermined temperature and a predetermined pressure so that water vapor and hot water are contained in the tube. A gas-liquid mixture comprising: a heating medium injection nozzle provided at the tip of the pipe line and controlled to have an internal pressure of 0.19 MPa or more, a nozzle internal temperature of 120 ° C. or more, and a nozzle water amount of 0.7 gr / sec or more. The gas-liquid mixture is jetted into the controlled heat treatment chamber, thereby adjusting the heat treatment chamber to a heat treatment atmosphere filled with a heating medium in which superheated steam and high-temperature fine water droplets are mixed. Yes.
However, since the heat treatment apparatus having this kind of configuration is of a batch type, it has never been possible to improve productivity. Even if heat treatment is performed using such a novel heating medium, it is difficult to obtain the same effect in a non-sealed heating chamber. Therefore, since there is a high demand for changing this type of heat treatment apparatus to a continuous heat treatment apparatus, it was decided to carry out this development together.

特開2003−310438号公報JP 2003-310438 A 特開2005−341834号公報JP-A-2005-341834 特開2006−087641号公報Japanese Patent Application Laid-Open No. 2006-087441 特開2009−091386号公報JP 2009-091386 A

本発明は、このような問題を解決するためになされており、その目的とするところは、連続して多数の処理対象物を順次加熱処理することのできる連続式加熱処理方法及び加熱処理装置であって、少なくとも入口側と出口側に、それぞれ搬送されてきた処理対象物が通過することのできる開口を備えた非密閉状の加熱処理室を使用しつつも、加熱媒体の室外への流出及び外気遮断が十分に成し得る連続式加熱処理方法及び連続式加熱処理装置を提供することである。   The present invention has been made to solve such problems, and the object of the present invention is a continuous heat treatment method and a heat treatment apparatus capable of sequentially heat-treating a large number of treatment objects in succession. In addition, while using a non-sealed heat treatment chamber having openings through which the object to be treated conveyed can pass at least on the inlet side and the outlet side, the outflow of the heating medium to the outside and It is an object of the present invention to provide a continuous heat treatment method and a continuous heat treatment apparatus that can sufficiently block outside air.

このような目的を達成するために、第1の発明は、一端側に開口した入口と、他端側に開口した出口とを設け、入口付近の入口側外気遮蔽領域と、出口付近の出口側外気遮蔽領域と、前記入口側外気遮蔽領域と出口側外気遮蔽領域との間に連続して配設される加熱処理領域とに区分けされた加熱処理室を備えており、
前記加熱処理領域内を処理室内加熱機構にて所定温度以上に加熱するとともに、前記加熱された加熱処理領域内に加熱媒体を噴射して前記加熱処理領域内を加熱処理雰囲気とする加熱媒体供給工程と、
前記加熱処理領域内に処理対象物を搬送して加熱処理する加熱処理工程と、
前記加熱処理領域内の加熱処理雰囲気の一部を加熱処理領域外へと吸い出し、所定温度以上に加熱して体積膨張した再加熱媒体を生成した後、該体積膨張した再加熱媒体を前記入口側外気遮蔽領域内及び出口側外気遮蔽領域内へとそれぞれ連続して噴射することで、前記入口側外気遮蔽領域内及び出口側外気遮蔽領域内に高温の再加熱媒体を滞留せしめる再加熱媒体生成噴射工程と、
前記入口側外気遮蔽領域の上流側と出口側外気遮蔽領域の下流側にて、入口側外気遮蔽領域と出口側外気遮蔽領域のそれぞれから溢れ出た再加熱媒体と、入口付近及び出口付近にある外気とを吸い込むことで、外気の加熱処理領域内への侵入を防ぐ室外吸い込み工程を備えていることを特徴とする加熱処理方法としたことである。
In order to achieve such an object, the first invention is provided with an inlet opening on one end side and an outlet opening on the other end side, an inlet side outside air shielding area near the inlet, and an outlet side near the outlet. A heat treatment chamber divided into an outside air shielding region and a heat treatment region continuously disposed between the inlet side outside air shielding region and the outlet side outside air shielding region;
A heating medium supply step of heating the inside of the heat treatment region to a predetermined temperature or higher by a heating mechanism inside the treatment chamber, and injecting a heating medium into the heated heat treatment region to make the inside of the heat treatment region a heat treatment atmosphere When,
A heat treatment step of carrying and heat-treating the object to be treated in the heat treatment region ;
The heating portion of the heating atmosphere of the processing area the sucked to the heat treatment outside the area, after generating the reheated medium volume expansion by heating above a predetermined temperature, said volume expanded reheated medium the inlet side Reheating medium generation injection in which a high-temperature reheating medium is retained in the inlet side outside air shielding area and the outlet side outside air shielding area by continuously injecting into the outside air shielding area and the outlet side outside air shielding area, respectively. Process,
Reheating medium overflowing from each of the inlet side outside air shielding area and the outlet side outside air shielding area on the upstream side of the inlet side outside air shielding area and the downstream side of the outlet side outside air shielding area, and in the vicinity of the inlet and the vicinity of the outlet It is a heat treatment method characterized by having an outdoor suction step for preventing outside air from entering the heat treatment region by sucking outside air .

第2の発明は、第1の発明において、加熱媒体供給工程は、
加熱処理領域内を、常圧で、かつ115℃程度に加熱制御し、
水供給源から0.7gr/sec以上で供給された水を所定温度及び所定圧力で沸騰させることで水蒸気と熱水からなる気液混合体を生成するとともに、前記気液混合体を加熱処理領域内に噴射する加熱媒体噴射ノズルを備え、
前記加熱媒体噴射ノズルは、内圧0.19MPa以上、ノズル内部温度120℃以上に制御されており、
前記加熱媒体噴射ノズルを介して、前記加熱処理領域内に気液混合体を噴射することで、前記加熱処理領域内を過熱水蒸気と高温微細水滴が混在する状態の加熱媒体で満たされた加熱処理雰囲気に調整し、
再加熱媒体は、前記加熱処理雰囲気に調整されている加熱処理領域内の加熱媒体を再加熱して生成され体積膨張した過熱水蒸気であることを特徴とする加熱処理方法としたことである。
In a second aspect based on the first aspect, the heating medium supply step comprises
The inside of the heat treatment area is controlled at normal pressure and about 115 ° C.,
The water supplied from the water supply source at a rate of 0.7 gr / sec or more is boiled at a predetermined temperature and a predetermined pressure to produce a gas-liquid mixture composed of water vapor and hot water, and the gas-liquid mixture is subjected to a heat treatment region. A heating medium spray nozzle for spraying into the inside,
The heating medium spray nozzle is controlled to have an internal pressure of 0.19 MPa or more and a nozzle internal temperature of 120 ° C. or more.
Heat treatment filled with a heating medium in a state where superheated steam and high-temperature fine water droplets are mixed in the heat treatment region by injecting a gas-liquid mixture into the heat treatment region via the heating medium injection nozzle. Adjust to the atmosphere,
The reheating medium is superheated steam produced by reheating the heating medium in the heat treatment region adjusted to the heat treatment atmosphere and volume-expanded superheated steam.

第3の発明は、第1の発明又は第2の発明において、加熱媒体は、処理対象物の加熱処理中において、連続して噴射されることを特徴とする加熱処理方法としたことである。A third invention is the heat treatment method according to the first invention or the second invention, wherein the heating medium is continuously ejected during the heat treatment of the object to be treated.

第4の発明は、第1の発明乃至第3の発明のいずれかにおいて、再加熱媒体は、入口側外気遮蔽領域内と出口側外気遮蔽領域内に向けて、拡開状に噴射されることを特徴とする加熱処理方法としたことである。According to a fourth aspect of the present invention, in any one of the first to third aspects, the reheating medium is sprayed in an expanded manner toward the inlet side outside air shielding area and the outlet side outside air shielding area. It is that it was set as the heat processing method characterized by these.

第5の発明は、一端側に開口した入口と、他端側に開口した出口とを設け、入口付近の入口側外気遮蔽領域と、出口付近の出口側外気遮蔽領域と、前記入口側外気遮蔽領域と出口側外気遮蔽領域との間に連続して配設される加熱処理領域とに区分けされた加熱処理室と
前記加熱処理室の加熱処理領域内に配し、加熱処理領域内を所定温度以上に加熱して所定の加熱処理雰囲気に調整する処理室内加熱機構と、
前記入口から前記出口に向かって処理対象物を搬送する搬送機構と、
前記加熱処理室の加熱処理領域内に加熱媒体を噴射する加熱媒体噴射ノズルを備えた加熱媒体生成機構と、
前記加熱処理室の加熱処理領域内の少なくとも一部に設けた吸込み口と、前記入口側外気遮蔽領域と前記出口側外気遮蔽領域に設けた噴き出し口と、前記吸込み口と噴き出し口とにわたって連通した連絡管と、該連絡管の所定箇所に備えられ、加熱処理領域内に噴射した前記加熱媒体を前記吸込み口から前記連絡管内へと強制的に吸い出す吸込みファンと、該吸込みファンで吸い出した加熱媒体を連絡管内で所定温度以上に加熱して体積膨張した再加熱媒体を生成する加熱部と、前記生成した再加熱媒体を、前記噴き出し口から前記入口側外気遮蔽領域内及び出口側外気遮蔽領域内へとそれぞれ噴射させる再加熱媒体噴射部を備えた再加熱媒体生成噴射機構と
入口側外気遮蔽領域の上流側と出口側外気遮蔽領域の下流側には、入口側外気遮蔽領域と出口側外気遮蔽領域のそれぞれから室外に溢れ出た再加熱媒体とともに、入口付近及び出口付近にある外気を吸い込む室外吸い込み部をそれぞれ備え、
前記入口側外気遮蔽領域と出口側外気遮蔽領域は、前記再加熱媒体噴射機構を介してそれぞれ再加熱媒体が連続して噴射されることで、高温の再加熱媒体が滞留し易い再加熱媒体の噴射・滞留領域として機能することを特徴とする加熱処理装置としたことである。
5th invention provides the inlet opened on the one end side, and the exit opened on the other end side, the inlet side external air shielding area | region near an inlet, the outlet side outdoor air shielding area | region near an outlet, and the said inlet side outdoor air shielding placed in the region and the outlet side outside air shielding the heat treatment chamber of the heat treatment zone and continuously heating chamber which is divided into a heat treatment region is disposed between the region, the predetermined temperature to a heat treatment zone A process chamber heating mechanism that heats and adjusts to a predetermined heat treatment atmosphere;
A transport mechanism for transporting the processing object from the inlet toward the outlet;
A heating medium generating mechanism including a heating medium spray nozzle that sprays the heating medium into the heat treatment region of the heat treatment chamber;
A suction port provided in at least a part of the heat treatment region of the heat treatment chamber , a blowout port provided in the inlet-side outside air shielding region and the outlet-side outside air shielding region, and the suction port and the blowout port communicated with each other. A communication pipe, a suction fan that is provided at a predetermined location of the communication pipe and forcibly sucks out the heating medium sprayed into the heat treatment region from the suction port into the communication pipe, and a heating medium sucked out by the suction fan A heating section that generates a reheat medium that has undergone volume expansion by heating to a predetermined temperature or more in the communication pipe, and the generated reheat medium from the outlet to the inside of the inlet side outside air shielding area and inside the outlet side outside air shielding area A reheating medium generating / injecting mechanism including a reheating medium injecting unit that injects each of the
On the upstream side of the inlet side outside air shielding area and the downstream side of the outlet side outside air shielding area, the reheating medium overflows from the inlet side outside air shielding area and the outlet side outside air shielding area, and near the inlet and the outlet. Each has an outdoor suction section that sucks in some outside air,
The inlet-side outside air shielding area and the outlet-side outside air shielding area are formed of a reheating medium in which a high-temperature reheating medium tends to stay by being continuously ejected through the reheating medium ejection mechanism . The heat treatment apparatus is characterized by functioning as an injection / retention area.

第6の発明は、第5の発明において、加熱処理領域は処理室内加熱機構を備え、常圧で、かつ処理室内加熱機構によって115℃程度に加熱制御されており、In a sixth aspect based on the fifth aspect, the heat treatment region includes a treatment chamber heating mechanism, and is heated to about 115 ° C. at normal pressure and by the treatment chamber heating mechanism.
加熱媒体生成機構は、加熱部と、水供給源と連絡して前記加熱部により加熱される管路と、前記管路の先端部に備えられ、加熱処理領域内に先端を臨ませてなる加熱媒体噴射ノズルを備え、前記加熱媒体噴射ノズルは、内圧0.19MPa以上、内部温度120℃以上に制御されており、  The heating medium generating mechanism includes a heating unit, a pipe line that is heated by the heating unit in communication with a water supply source, and a heating unit that is provided at a tip part of the pipe line and has a tip facing the heat treatment region. A medium injection nozzle, and the heating medium injection nozzle is controlled to have an internal pressure of 0.19 MPa or more and an internal temperature of 120 ° C. or more,
前記管路内に0.7gr/sec以上で供給された水を所定温度及び所定圧力で沸騰させることで管路内に水蒸気と熱水からなる気液混合体を生成し、  Producing a gas-liquid mixture consisting of water vapor and hot water in the pipeline by boiling water supplied at 0.7 g / sec or more into the pipeline at a predetermined temperature and pressure,
前記加熱媒体噴射ノズルを介して前記気液混合体を前記加熱処理領域内に噴出することにより、前記加熱処理領域内を過熱水蒸気と高温微細水滴が混在する状態の加熱媒体で満たされた加熱処理雰囲気に調整しており、  Heat treatment filled with a heating medium in a state where superheated steam and high-temperature fine water droplets are mixed in the heat treatment region by ejecting the gas-liquid mixture into the heat treatment region through the heating medium injection nozzle. Adjusted to the atmosphere,
再加熱媒体は、前記加熱処理雰囲気に調整されている加熱処理領域内の加熱媒体を、再加熱媒体生成噴射機構により再加熱して生成され体積膨張した過熱水蒸気であることを特徴とする加熱処理装置としたことである。  The heat treatment is characterized in that the reheat medium is superheated steam that is generated by reheating the heat medium in the heat treatment region adjusted to the heat treatment atmosphere by a reheat medium production and injection mechanism and volume-expanded. It is a device.

第7の発明は、第5の発明又は第6の発明において、加熱媒体は、処理対象物の加熱処理中において、連続して噴射されることを特徴とする加熱処理装置としたことである。A seventh invention is the heat treatment apparatus according to the fifth or sixth invention, wherein the heating medium is continuously ejected during the heat treatment of the object to be treated.

第8の発明は、第5の発明乃至第7の発明のいずれかにおいて、再加熱媒体噴射部は、吸込みファンの吹き出し口と入口側外気遮蔽領域の上方に設けた接続開口部との間、及び、吸込みファンの吹き出し口と出口側外気遮蔽領域の上方に設けた接続開口部との間にわたってそれぞれ下り傾斜の漏斗状に形成されて配設されており、In an eighth aspect based on any one of the fifth aspect to the seventh aspect, the reheating medium injection part is provided between the outlet of the suction fan and the connection opening provided above the inlet side outside air shielding area. And it is formed and arranged in a funnel shape with a downward slope between the outlet of the suction fan and the connection opening provided above the outlet side outside air shielding region,
再加熱媒体は、前記下り傾斜の漏斗状に形成されたそれぞれの再加熱媒体噴射部から、入口側外気遮蔽領域内と出口側外気遮蔽領域内に向けて、それぞれ拡開状に噴射され、Reheating medium is sprayed in an expanded manner from the respective reheating medium spraying portions formed in the descending funnel shape toward the inside of the inlet side outside air shielding area and the inside of the outlet side outside air shielding area,
前記入口側外気遮蔽領域と加熱処理領域との境界、及び、出口側外気遮蔽領域と加熱処理領域との境界には、それぞれ入口側外気遮蔽領域内と出口側外気遮蔽領域内に噴射された再加熱媒体が滞留し易い領域に形成するための境界壁を設けていることを特徴とする加熱処理装置としたことである。The boundary between the inlet side outside air shielding area and the heat treatment area and the boundary between the outlet side outside air shielding area and the heat treatment area are respectively injected into the inlet side outside air shielding area and the outlet side outside air shielding area. The heat treatment apparatus is characterized in that a boundary wall is provided for forming in a region where the heating medium is likely to stay.

第9の発明は、第5の発明乃至第8の発明のいずれかにおいて、室外吸い込み部は、入口側外気遮蔽領域の上流側と出口側外気遮蔽領域の下流側にそれぞれ連続して備えられており、In a ninth aspect based on any one of the fifth aspect to the eighth aspect, the outdoor suction portion is continuously provided on the upstream side of the inlet side outside air shielding area and the downstream side of the outlet side outside air shielding area. And
搬送機構の処理対象物載置面に向けて開口した吸い込み空間を有する箱部と、箱部と連通した吸い込みファンを含み、Including a box portion having a suction space opened toward the processing object mounting surface of the transport mechanism, and a suction fan communicating with the box portion;
前記吸い込みファンの吸い込み作動によって搬送機構の処理対象物載置面付近にある外気が強制的に吸い込まれるとともに、入口側外気遮蔽領域と出口側外気遮蔽領域から負圧により再加熱媒体が引き出されて一緒に吸い込み空間へと吸い込まれて排出されることを特徴とする加熱処理装置としたことである。  The suction operation of the suction fan forcibly sucks the outside air near the processing object mounting surface of the transport mechanism, and the reheating medium is drawn out from the inlet side outside air shielding area and the outlet side outside air shielding area by negative pressure. The heat treatment apparatus is characterized in that it is sucked into the suction space and discharged.

第10の発明は、第5の発明乃至第9の発明のいずれかにおいて、処理室内加熱機構は、加熱処理領域内の搬送方向における略中央の領域に、搬送機構の幅よりも広い間隔をもって一対で配設されているコイル状加熱部であって、According to a tenth aspect of the present invention, in any one of the fifth to ninth aspects, the processing chamber heating mechanism is paired in a substantially central region in the transport direction within the heat treatment region with an interval wider than the width of the transport mechanism. A coiled heating unit disposed at
前記一対のコイル状加熱部の間には、加熱処理領域内の加熱処理雰囲気が室内全域に行き渡るように撹拌する加熱処理室撹拌ファンを備え、Between the pair of coiled heating units, a heat treatment chamber stirring fan that stirs the heat treatment atmosphere in the heat treatment region so as to spread throughout the room,
前記加熱処理室撹拌ファンとそのファンを挟むようにして配される一対の処理室内加熱機構との間には、前記ファンの回転作動によって送風する際に、搬送機構上を移動して撹拌される気流を発生せしめるファンガードを備えたことを特徴とする加熱処理装置としたことである。Between the heat treatment chamber agitating fan and a pair of treatment chamber heating mechanisms arranged so as to sandwich the fan, an air flow that is agitated by moving on the conveyance mechanism when the fan is blown by the rotation operation of the fan. The heat treatment apparatus is characterized by including a fan guard that can be generated.

本発明によれば、少なくとも入口側と出口側に、それぞれ搬送されてきた処理対象物が通過することのできる開口を備えた非密閉状の加熱処理室を使用しつつも、加熱媒体の室外への流出及び外気遮断が十分に成し得る連続式加熱処理方法及び連続式加熱処理装置を提供できた。すなわち、非密閉状の加熱処理室を用いて行わざるを得ない連続式の加熱処理であっても、機械的な密閉機構を採用せずとも加熱処理領域を密閉に近い状態で処理し、加熱媒体の室外への流出及び外気遮断が十分に成し得ることができた。   According to the present invention, while using an unsealed heat treatment chamber provided with openings through which the object to be treated which has been conveyed can pass at least on the inlet side and the outlet side, the heating medium is moved out of the room. It is possible to provide a continuous heat treatment method and a continuous heat treatment apparatus that can sufficiently prevent the outflow of air and the blocking of outside air. That is, even if it is a continuous heat treatment that must be performed using a non-sealed heat treatment chamber, the heat treatment region is treated in a state close to hermetic sealing without using a mechanical sealing mechanism, and heating is performed. The outflow of the medium to the outside and the blocking of the outside air could be sufficiently achieved.

本発明の連続式加熱処理装置の一実施例を示す概略平面図である。It is a schematic plan view which shows one Example of the continuous heat processing apparatus of this invention. 本発明の連続式加熱処理装置の一実施例を示す概略正面図である。It is a schematic front view which shows one Example of the continuous heat processing apparatus of this invention. 本発明の連続式加熱処理装置の一実施例を示す概略側面図である。It is a schematic side view which shows one Example of the continuous heat processing apparatus of this invention. 本発明の連続式加熱処理装置の一実施例を示す概略縦断正面図である。It is a schematic longitudinal front view which shows one Example of the continuous-type heat processing apparatus of this invention. 本発明の連続式加熱処理装置の一実施例を示す概略縦断側面図である。It is a schematic longitudinal side view which shows one Example of the continuous-type heat processing apparatus of this invention. 本発明の連続式加熱処理装置に用いられる加熱媒体の実施の一形態における発生メカニズムを示す概略説明図である。It is a schematic explanatory drawing which shows the generation | occurrence | production mechanism in one Embodiment of the heating medium used for the continuous heat processing apparatus of this invention.

1 加熱処理室
2 入口
3 出口
S1 入口側外気遮蔽領域
S2 出口側外気遮蔽領域
S3 加熱処理領域
12 搬送機構
13 加熱媒体生成機構
17 加熱媒体噴射ノズル
18 再加熱媒体生成噴射機構
19 吸込み口
20 噴き出し口
21 連絡管
22 吸込みファン
23 加熱部
24,25 再加熱媒体噴射部
F 加熱処理雰囲気
H 熱水
M 水蒸気
T 処理対象物
SK 再加熱媒体
KM 過熱水蒸気
KH 高温微細水滴
DESCRIPTION OF SYMBOLS 1 Heat processing chamber 2 Inlet 3 Outlet S1 Inlet side outside air shielding area S2 Outlet side outside air shielding area S3 Heat processing area 12 Conveyance mechanism 13 Heating medium production | generation mechanism 17 Heating medium injection | spray nozzle 18 Reheating medium production | generation injection mechanism 19 Inlet 20 Outlet 21 Connecting pipe 22 Suction fan 23 Heating unit 24, 25 Reheating medium injection unit F Heat treatment atmosphere H Hot water M Steam T Process target SK Reheating medium KM Superheated steam KH High temperature fine water droplets

以下、本発明の加熱処理方法及びその加熱処理方法を使用する加熱処理装置に関する一実施形態について説明する。なお、本実施形態は本発明の一例にすぎずなんらこれに限定解釈されるものではなく、本発明の範囲内で設計変更可能である。   Hereinafter, an embodiment relating to a heat treatment method of the present invention and a heat treatment apparatus using the heat treatment method will be described. Note that this embodiment is merely an example of the present invention, and is not construed as being limited thereto, and the design can be changed within the scope of the present invention.

図1乃至図6は本発明加熱処理装置の一例を示し、加熱処理装置は、加熱処理室1と、加熱処理室1内に処理対象物Tを連続して搬送する搬送機構12と、加熱処理室1内に加熱媒体を噴射する加熱媒体生成機構13と、加熱処理室1内の加熱処理雰囲気Fの一部を吸い出して再加熱媒体SKを生成するとともに、その再加熱媒体SKを再び加熱処理室1内に噴射することで加熱媒体(加熱処理雰囲気F)の室外への流出及び外気Gの室内への侵入を防ぐ再加熱媒体生成噴射機構18とで構成されている(図1乃至図6参照。)。   1 to 6 show an example of the heat treatment apparatus of the present invention. The heat treatment apparatus includes a heat treatment chamber 1, a transport mechanism 12 that continuously conveys the processing target T into the heat treatment chamber 1, and a heat treatment. A heating medium generating mechanism 13 for injecting the heating medium into the chamber 1 and a part of the heating processing atmosphere F in the heating processing chamber 1 are sucked out to generate the reheating medium SK, and the reheating medium SK is heated again. A reheating medium generating / injecting mechanism 18 that prevents the heating medium (heat treatment atmosphere F) from flowing out of the room and preventing the outside air G from entering the room by being injected into the chamber 1 (FIGS. 1 to 6). reference.).

加熱処理室1は、一端側に開口した入口2と他端側に開口した出口3を設けた非密閉状でかつ所定長さの矩形状に形成されており、所定の架台4上に配設されている(図1乃至図4参照。)。図中5は、点検扉である。
前記加熱処理室1は、本実施例において、入口2付近の入口側外気遮蔽領域S1と、出口3付近の出口側外気遮蔽領域S2と、前記入口側外気遮蔽領域S1と出口側外気遮蔽領域S2との間の加熱処理領域S3とに区分けされている(図4参照。)。
The heat treatment chamber 1 is formed in a non-sealed rectangular shape having a predetermined length with an inlet 2 opened on one end side and an outlet 3 opened on the other end side, and is disposed on a predetermined base 4. (See FIGS. 1 to 4). In the figure, 5 is an inspection door.
In this embodiment, the heat treatment chamber 1 includes an inlet-side outside air shielding area S1 near the inlet 2, an outlet-side outside air shielding area S2 near the outlet 3, the inlet-side outside air shielding area S1, and the outlet-side outside air shielding area S2. (See FIG. 4).

なお、本発明において特に限定解釈されるものではないが、前記入口側外気遮蔽領域S1と出口側遮蔽領域S2は、加熱処理領域S3との境界部位に、後述する搬送機構12によって搬送される処理対象物Tの搬送を阻害しない程度に室内に向けて突出する境界壁6を設けている(図4に概略を示す。)。本実施例では、この境界壁6を前壁1aの内面、後壁1bの内面、天井壁1cの内面及び底面1dの内面にそれぞれ突出して備えている。
図中6aは、境界壁6に設けられている貫通した通孔である。なお、この境界壁6を備えない実施の形態であっても本発明の範囲内である。
Although not particularly limited in the present invention, the inlet-side outside air shielding area S1 and the outlet-side shielding area S2 are processed by a transfer mechanism 12 described later at a boundary portion between the heat treatment area S3. A boundary wall 6 protruding toward the room is provided so as not to hinder the conveyance of the object T (an outline is shown in FIG. 4). In this embodiment, the boundary wall 6 is provided so as to protrude from the inner surface of the front wall 1a, the inner surface of the rear wall 1b, the inner surface of the ceiling wall 1c, and the inner surface of the bottom surface 1d.
In the figure, reference numeral 6 a denotes a through hole provided in the boundary wall 6. Even an embodiment that does not include the boundary wall 6 is within the scope of the present invention.

また、本実施例では、加熱処理室1内の前記加熱処理領域S3を所定温度以上に加熱調整するため、処理室内加熱機構7を備えている。
処理室内加熱機構7は、例えば図4乃至図6に示すように、処理対象物Tの搬送方向(図4にて矢印Yで示す方向)に長尺状に形成された室内加熱ヒーターとしてのコイル状加熱部であって、このコイル状加熱部(処理室内加熱機構)7を搬送機構12と平行で、かつ搬送機構12のコンベア幅よりも広く離して前記加熱処理室1内の加熱処理領域S3の天井壁1cに一対配設している。
また、このコイル状加熱部7は、その両端部7a,7bを加熱処理室1の天井壁1cの外面に突出させるとともに、それぞれの両端部7a,7bを図示しない所定の熱源と連絡している。すなわち、本実施例のコイル状加熱部7は、加熱処理領域S3の天井壁1cの内面から領域S3内に吊り下げ状に配設されている。
本実施例では、このコイル状加熱部7によって、加熱処理室1内を、常圧で、かつ115℃程度(好ましくは、105℃〜120℃)に加熱制御している。
また、加熱処理室1は、前記所定温度以上に加熱制御するため、保温可能な材質を選定して形成するようにしている。なお、処理室内加熱機構7の形状及び構造については、適宜設計変更可能であって、何等本実施例に限定解釈されるものではない。
Further, in the present embodiment, the heating chamber 7 is provided with a heating chamber 7 for adjusting the heating area S3 in the heating chamber 1 to a predetermined temperature or higher.
The processing chamber heating mechanism 7 is, for example, as shown in FIGS. 4 to 6, a coil as an indoor heater formed in a long shape in the conveying direction of the processing target T (the direction indicated by the arrow Y in FIG. 4). A heating unit S3 in the heating processing chamber 1 that is parallel to the transport mechanism 12 and wider than the conveyor width of the transport mechanism 12. A pair of ceiling walls 1c is provided.
The coiled heating unit 7 has both end portions 7a and 7b projecting from the outer surface of the ceiling wall 1c of the heat treatment chamber 1, and the both end portions 7a and 7b communicate with a predetermined heat source (not shown). . That is, the coiled heating unit 7 of the present embodiment is disposed in a suspended manner from the inner surface of the ceiling wall 1c of the heat treatment region S3 into the region S3.
In this embodiment, the coil-shaped heating unit 7 controls the heating in the heat treatment chamber 1 at normal pressure and about 115 ° C. (preferably 105 ° C. to 120 ° C.).
In addition, the heat treatment chamber 1 is formed by selecting a material that can be kept warm in order to control heating to the predetermined temperature or higher. In addition, about the shape and structure of the process chamber heating mechanism 7, a design change is possible suitably, and it is not limitedly interpreted to a present Example at all.

本実施例では、加熱処理室1の加熱処理領域S3の天井壁1cに加熱処理室撹拌ファン8を備えている(図5及び図6参照。)図中、符号8aは加熱処理室1内に配設されるファンの羽根車、8bは加熱処理室1外に配設される駆動源(モータ)をそれぞれ示す。なお、図4では駆動源8bのみ図示し、羽根車8aについては図示を省略した。この加熱処理室撹拌ファン8によって、加熱処理室1内の加熱処理雰囲気(加熱媒体)を室内全域に行き渡る様に撹拌して加熱処理効率を高めている。
また、図中9は、羽根車8aを回転して送風する際に気流Nを発生させるための羽根車8aの絞りと、コイル状加熱部7からの輻射熱遮断の役割を有しているファンガードである。
In the present embodiment, a heat treatment chamber stirring fan 8 is provided on the ceiling wall 1c of the heat treatment region S3 of the heat treatment chamber 1 (see FIGS. 5 and 6). A fan impeller 8b and a driving source (motor) arranged outside the heat treatment chamber 1 are shown. In FIG. 4, only the drive source 8b is shown, and the illustration of the impeller 8a is omitted. The heat treatment chamber agitating fan 8 agitates the heat treatment atmosphere (heating medium) in the heat treatment chamber 1 so as to spread throughout the room, thereby improving the heat treatment efficiency.
Reference numeral 9 in the drawing denotes a fan guard having a function of blocking the radiant heat from the coiled heating unit 7 and the throttle of the impeller 8a for generating the airflow N when the impeller 8a rotates and blows air. It is.

さらに、図中10は、加熱処理室1内で発生した凝縮水等を集める排水管で、加熱処理室1の底面1dの外方にて処理対象物の搬送方向にわたって配設されており、加熱処理室1の所定箇所、本実施例では加熱処理室1の底面1dの所定位置、すなわち、例えば、加熱処理領域S3の底面1dの内面と、入口側外気遮蔽領域S1の底面1dの内面と、出口側外気遮蔽領域S2の底面1dの内面のそれぞれに、略円形状に貫通して設けられた排水口11とそれぞれ連通して配設されている。
なお、排水口11の穴形状は処理対象物の搬送方向にわたって長尺状に貫通してなるものであってもよく、また、その穴数も単数、複数限定されない。さらに、凝縮水を集めやすくするため底面1dの内面を排水口11に向けて下り傾斜状に形成するものであってもよい。
Further, in the figure, reference numeral 10 denotes a drain pipe for collecting condensed water generated in the heat treatment chamber 1, which is disposed outside the bottom surface 1d of the heat treatment chamber 1 in the conveying direction of the object to be treated. A predetermined position of the processing chamber 1, in this embodiment, a predetermined position of the bottom surface 1d of the heat treatment chamber 1, that is, for example, the inner surface of the bottom surface 1d of the heat treatment region S3, and the inner surface of the bottom surface 1d of the inlet side outside air shielding region S1, Disposed on the inner surface of the bottom surface 1d of the outlet-side outside air shielding area S2 is communicated with a drain port 11 provided in a substantially circular shape.
In addition, the hole shape of the drain port 11 may be formed in a long shape in the conveying direction of the object to be processed, and the number of holes is not limited to one or more. Further, in order to easily collect condensed water, the inner surface of the bottom surface 1d may be formed in a downward slope toward the drain port 11.

搬送機構12は、前記入口2から前記出口3に向かって処理対象物Tを順次搬送するもので、特に限定解釈はされないが、本実施例では、無端状に構成された金属製のコンベアチェーンで、所定の駆動機構Kによって入口2側から出口3側へと回転駆動する(図1乃至図6参照。)。加熱処理室1内の所定温度に耐え得る材質であれば特に本実施例の形状・材質に限定解釈されるものではない。
図中Aは、処理対象物Tを搬送するに用いた搬送籠を示す。なお、本実施例では搬送籠Aを用いたがこれに限定はされない。
The transport mechanism 12 sequentially transports the processing target T from the inlet 2 toward the outlet 3 and is not particularly limited. In this embodiment, the transport mechanism 12 is an endless metal conveyor chain. Then, it is rotationally driven from the inlet 2 side to the outlet 3 side by a predetermined drive mechanism K (see FIGS. 1 to 6). Any material that can withstand a predetermined temperature in the heat treatment chamber 1 is not particularly limited to the shape and material of this embodiment.
A in the figure indicates a transport rod used to transport the processing object T. In this embodiment, the transport rod A is used, but the present invention is not limited to this.

加熱媒体生成機構13は、本実施例では、次の構成からなる機構を採用している。
加熱媒体生成機構13は、所定長さの円筒状に形成された加熱チャンバ(加熱部)14と、該加熱チャンバ14内に一部を内装した金属製の加熱管路(管路)15と、該加熱管路15の先端側に配され、ノズルヘッダー16を介して加熱処理室1内に取り付け配置される加熱媒体噴射ノズル17とで構成されている。
In the present embodiment, the heating medium generating mechanism 13 employs a mechanism having the following configuration.
The heating medium generation mechanism 13 includes a heating chamber (heating unit) 14 formed in a cylindrical shape having a predetermined length, a metal heating pipe (pipe) 15 partially including the heating chamber 14, The heating medium spray nozzle 17 is arranged on the front end side of the heating pipe line 15 and is mounted and disposed in the heat treatment chamber 1 via the nozzle header 16.

加熱管路15は、所定の内径・長さに形成され、所定のポンプ(例えば電磁定量ポンプなどが想定される。)Pを介して内部に供給された水を前記加熱チャンバ14によって所定温度に加熱可能としている。
加熱管路15内に供給される水量は、0.7gr/sec以上、好ましくは0.7gr/sec〜25gr/secとする。なお、加熱チャンバ14の構成、加熱管路15の管径及び長さは特に限定されず本発明の範囲内において適宜設計可能である。
The heating line 15 is formed to have a predetermined inner diameter and length, and water supplied to the inside via a predetermined pump (for example, an electromagnetic metering pump) is set to a predetermined temperature by the heating chamber 14. Heating is possible.
The amount of water supplied into the heating pipe line 15 is 0.7 gr / sec or more, preferably 0.7 gr / sec to 25 gr / sec. The configuration of the heating chamber 14 and the diameter and length of the heating pipe line 15 are not particularly limited and can be appropriately designed within the scope of the present invention.

加熱媒体噴射ノズル17は、図4〜図6に示すように、加熱管路15を介して加熱処理室1の天井壁1cの外面から加熱処理室1の加熱処理領域S3内に向けて突出して配設されており、本実施例では、加熱処理領域S3の長さ方向、すなわち、加熱処理領域S3において処理対象物Tの搬送方向にわたってノズルヘッダー16を配設し、そのノズルヘッダー16を介して複数個配設されている。
本実施例における加熱媒体噴射ノズル17は、ノズル内径を0.1mm〜10mm(好ましくは0.5mm〜5mm)とし、ノズル内圧を0.19MPa以上(好ましくは、0.19MPa〜0.41MPa)、ノズル内温度:120℃以上(好ましくは120℃〜145℃)に制御されている。
本実施例では、前壁1a側と後壁1b側に沿ってそれぞれノズルヘッダー16を介して3個ずつ配設している。また、本実施例では、加熱媒体噴射ノズル17の噴射口(ノズル先端)17aは、コイル状加熱部7の上面側(天井壁1c寄りの面部)に近い位置で、かつ僅かに搬送機構12(処理対象物T)方向に向くように配設している。すなわち、前記気液混合体(水蒸気Mと熱水H)は、搬送機構12(処理対象物T)に向けて斜めに噴射されるように設計されている。なお、前記噴射方向は本実施例に限定解釈されない。
加熱処理室1内に加熱処理室撹拌ファン8を配置して加熱処理室1内を撹拌しているため、加熱媒体噴射ノズル17の噴射口17aは出来るだけ加熱処理領域S3の中央に寄せた方が効果的である。なお、加熱媒体噴射ノズル17の配設個数や配設角度などは適宜設計変更可能であって何等本実施例に限定解釈されるものではない。
前記気液混合体(水蒸気Mと熱水H)は、処理対象物Tの加熱処理中において、連続して噴射されるものとする。なお、連続とは、僅かな間隔で断続的に噴射する形態も含む概念である。
As shown in FIGS. 4 to 6, the heating medium spray nozzle 17 projects from the outer surface of the ceiling wall 1 c of the heat treatment chamber 1 toward the heat treatment region S <b> 3 of the heat treatment chamber 1 through the heating pipe 15. In this embodiment, the nozzle header 16 is arranged in the length direction of the heat treatment region S3, that is, in the heat treatment region S3 over the conveying direction of the processing target T, and the nozzle header 16 is interposed therebetween. A plurality are arranged.
The heating medium spray nozzle 17 in the present embodiment has a nozzle inner diameter of 0.1 mm to 10 mm (preferably 0.5 mm to 5 mm), a nozzle internal pressure of 0.19 MPa or more (preferably 0.19 MPa to 0.41 MPa), Nozzle temperature: controlled to 120 ° C. or higher (preferably 120 ° C. to 145 ° C.).
In this embodiment, three each are arranged via the nozzle header 16 along the front wall 1a side and the rear wall 1b side. Further, in the present embodiment, the ejection port (nozzle tip) 17a of the heating medium ejection nozzle 17 is close to the upper surface side (surface portion near the ceiling wall 1c) of the coiled heating unit 7 and slightly transport mechanism 12 ( It arrange | positions so that it may face the process target object T) direction. That is, the gas-liquid mixture (water vapor M and hot water H) is designed to be injected obliquely toward the transport mechanism 12 (processing object T). In addition, the said injection direction is not limitedly interpreted by a present Example.
Since the heat treatment chamber stirring fan 8 is disposed in the heat treatment chamber 1 and the heat treatment chamber 1 is stirred, the injection port 17a of the heating medium injection nozzle 17 is as close to the center of the heat treatment region S3 as possible. Is effective. The number of the heating medium spray nozzles 17, the angle of the heating medium 17 and the like can be appropriately changed in design, and are not limited to the present embodiment.
The gas-liquid mixture (water vapor M and hot water H) is jetted continuously during the heat treatment of the processing target T. The term “continuous” is a concept that includes a mode of intermittent injection at a slight interval.

本発明の加熱処理室1内の加熱処理雰囲気について図6に基づいて説明する。
まず、水供給源から定量ポンプPを介して加熱管路15内に0.7gr/secで水を供給し、その供給された水を、前記加熱チャンバ14によって所定温度及び所定圧力(120℃以上、0.19MPa以上)で沸騰させることで加熱管路15内には水蒸気Mと熱水Hからなる気液混合体が生成される。
そして、ノズル内圧0.19MPa以上、ノズル内部温度120℃以上に制御した加熱媒体噴射ノズル17を介し、前記したように115℃程度に加熱制御された加熱処理室1内に前記気液混合体を噴出することにより、前記加熱処理室1内が過熱水蒸気KMと高温微細水滴KHが混在する状態の加熱媒体で満たされた加熱処理雰囲気Fに調整される。
すなわち、水供給源から定量ポンプPを介して加熱管路15内に供給される水量が、加熱媒体噴射ノズル17から噴射される過熱水蒸気KMの流量を超過した場合、供給水量の超過分は、過熱水蒸気としてではなく、高温微細水滴KHとして過熱水蒸気KMとともに加熱媒体噴射ノズル17から噴射される。
The heat treatment atmosphere in the heat treatment chamber 1 of the present invention will be described with reference to FIG.
First, water is supplied from the water supply source into the heating pipe line 15 through the metering pump P at 0.7 gr / sec, and the supplied water is supplied to the heating chamber 14 at a predetermined temperature and a predetermined pressure (120 ° C. or higher). , 0.19 MPa or more), a gas-liquid mixture composed of water vapor M and hot water H is generated in the heating line 15.
Then, the gas-liquid mixture is placed in the heat treatment chamber 1 which is controlled to be heated to about 115 ° C. as described above through the heating medium spray nozzle 17 which is controlled to have a nozzle internal pressure of 0.19 MPa or more and a nozzle internal temperature of 120 ° C. or more. By ejecting, the inside of the heat treatment chamber 1 is adjusted to a heat treatment atmosphere F filled with a heating medium in which superheated steam KM and high-temperature fine water droplets KH are mixed.
That is, when the amount of water supplied from the water supply source into the heating pipe 15 via the metering pump P exceeds the flow rate of the superheated steam KM injected from the heating medium injection nozzle 17, the excess of the supply water amount is It is injected from the heating medium injection nozzle 17 together with the superheated steam KM as high temperature fine water droplets KH, not as superheated steam.

再加熱媒体生成噴射機構18は、加熱処理室1内の加熱処理雰囲気Fの一部を加熱処理室1外へと吸い出し、所定温度以上に加熱して体積膨張した再加熱媒体SKを生成した後、該体積膨張した再加熱媒体SKを加熱処理室1内に噴射する機構で、吸込み口19、噴き出し口20、連絡管21、吸込みファン(送風機)22、加熱部23、そして再加熱媒体噴射部(24,25)とで構成されている。
具体的な機構の一例について以下説明する。
After the reheating medium generation / injection mechanism 18 sucks a part of the heat treatment atmosphere F in the heat treatment chamber 1 out of the heat treatment chamber 1 and heats it to a predetermined temperature or more to generate a reheat medium SK that has undergone volume expansion. The mechanism for injecting the reheated medium SK expanded in volume into the heat treatment chamber 1 includes a suction port 19, a discharge port 20, a communication pipe 21, a suction fan (blower) 22, a heating unit 23, and a reheating medium injection unit. (24, 25).
An example of a specific mechanism will be described below.

前記加熱処理領域S3が設けられている加熱処理室1の後壁1bの所定位置(加熱処理室1の高さ方向略中央位置)に、所定の大きさで貫通した略円形状の吸込み口19を設ける(図4及び図5参照。)。
そして、入口側外気遮蔽領域S1と出口側外気遮蔽領域S2が設けられている加熱処理室1の天井壁1cの上面所定位置に、それぞれ所定の大きさで貫通した略矩形状の噴き出し口20を設ける(図1及び図4参照。)。
そして、前記吸込み口19と噴き出し口20とにわたって連通した連絡管21を配設する。
連絡管21は、単一の吸込み口19から二箇所の噴き出し口20,20へと連絡し得るように、加熱処理室1と接続される単一の接続管部21aと、該接続管部21aと連絡されて鉛直状に設けられた単一の直管部21bと、該直管部21bの上端で分岐管部21cを介して二股状に連絡される左横管部21d及び右横管部21eと、左横管部21dと左吸込みファン(左送風機)22とを連絡する左ファン接続管部21fと、右横管部21eと右吸込みファン(右送風機)22とを連絡する右接続管部21gとで構成されている(図1乃至図5参照。)。
A substantially circular suction port 19 penetrating at a predetermined size into a predetermined position (substantially central position in the height direction of the heat processing chamber 1) of the rear wall 1b of the heat processing chamber 1 in which the heat processing region S3 is provided. (See FIGS. 4 and 5).
And the substantially rectangular ejection opening 20 penetrated by the predetermined | prescribed magnitude | size at the upper surface predetermined position of the ceiling wall 1c of the heat processing chamber 1 in which the entrance side outside air shielding area | region S1 and the exit side outside air shielding area | region S2 are provided, respectively. Provided (see FIGS. 1 and 4).
Then, a communication pipe 21 communicating with the suction port 19 and the ejection port 20 is provided.
The connecting pipe 21 is connected to the heat treatment chamber 1 so that the connecting pipe 21 can communicate with the two outlets 20 and 20 from the single suction port 19, and the connecting pipe portion 21a. A single straight pipe portion 21b provided in a vertical shape in communication with the left horizontal pipe portion 21d and a right horizontal pipe portion that are bifurcated via a branch pipe portion 21c at the upper end of the straight pipe portion 21b. 21e, a left fan connecting pipe portion 21f that communicates the left lateral pipe portion 21d and the left suction fan (left blower) 22, and a right connection pipe that communicates the right lateral pipe portion 21e and the right suction fan (right blower) 22 21g (refer to FIG. 1 to FIG. 5).

連絡管21の所定箇所には、吸い出した加熱媒体(加熱処理雰囲気F)を連絡管21内で所定温度以上に加熱して体積膨張した再加熱媒体SKを生成する加熱部23が備えられている。
本実施例では、直管部21b内に加熱部23の一例として一個のコイル状加熱部(過熱水蒸気生成ヒータ)23が配設され、左横管部21d及び右横管部21eにそれぞれ一個ずつコイル状加熱部(過熱水蒸気生成ヒータ)23が配設されている(図4及び図5参照。)。
吸込みファン(送風機)22は、加熱処理室1内の加熱処理雰囲気(加熱媒体)Fを、前記吸込み口19から前記連絡管21内へと強制的に吸い出すファンで、前記左接続管部21dと左再加熱媒体噴射部24との間、及び右接続管部21eと右再加熱媒体噴射部25との間に配設されている。
再加熱媒体噴射部24,25は、前記ファン22,22の出口から噴き出し口20,20に向けて拡開状に形成されたガイド部24a,25aと前記噴き出し口20,20とで構成されており、前記生成した再加熱媒体SKを前記噴き出し口20,20から加熱処理室1内、すなわち、入口側外気遮蔽領域S1内と出口側外気遮蔽領域S2内へと連続して噴射させる。
A heating portion 23 is provided at a predetermined location of the communication tube 21 to generate the reheated medium SK that is expanded in volume by heating the sucked heating medium (heat treatment atmosphere F) to a predetermined temperature or higher in the communication tube 21. .
In the present embodiment, one coil-like heating part (superheated steam generating heater) 23 is provided as an example of the heating part 23 in the straight pipe part 21b, one for each of the left horizontal pipe part 21d and the right horizontal pipe part 21e. A coiled heating unit (superheated steam generating heater) 23 is disposed (see FIGS. 4 and 5).
The suction fan (blower) 22 is a fan that forcibly sucks the heat treatment atmosphere (heating medium) F in the heat treatment chamber 1 from the suction port 19 into the communication pipe 21, and the left connection pipe portion 21 d It is disposed between the left reheating medium ejection part 24 and between the right connection pipe part 21e and the right reheating medium ejection part 25.
The reheating medium injection units 24 and 25 are configured by guide portions 24a and 25a formed in an expanding shape from the outlets of the fans 22 and 22 toward the discharge ports 20 and 20, and the discharge ports 20 and 20, respectively. The generated reheating medium SK is continuously ejected from the ejection ports 20 and 20 into the heat treatment chamber 1, that is, into the inlet side outside air shielding area S1 and the outlet side outside air shielding area S2.

したがって、吸込み口19から吸込みファン22,22を介して強制的に吸込まれた加熱処理雰囲気(加熱媒体)Fの一部は、直管部21bと左右の横管部21d,21eに配設されているそれぞれの加熱部(コイル状加熱部)23,23,23によって、その管21内を通過する間に所定温度に加熱され、再加熱媒体SKとして前記入口側外気遮蔽領域S1と前記出口側外気遮蔽領域S2に向けてそれぞれ連続して噴射される。
例えば、再加熱媒体SKは、前記加熱処理雰囲気Fに調整されている加熱処理室1内の加熱媒体を、再加熱媒体生成噴射機構18により再加熱して生成され体積膨張した過熱水蒸気である。
再加熱媒体(過熱水蒸気)SKの温度は、例えば、加熱処理室1内の温度よりも10℃程度高く設定する。なお、加熱媒体の供給量等によっては、適宜再加熱媒体(過熱水蒸気)SKの加熱温度を上げて比容積の増加(体積膨張)を調整する必要もある。
Therefore, a part of the heat treatment atmosphere (heating medium) F forcedly sucked from the suction port 19 through the suction fans 22 and 22 is disposed in the straight pipe portion 21b and the left and right horizontal pipe portions 21d and 21e. Each of the heating sections (coiled heating sections) 23, 23, 23 is heated to a predetermined temperature while passing through the pipe 21, and serves as the reheating medium SK for the inlet side outside air shielding area S1 and the outlet side. Injected continuously toward the outside air shielding area S2.
For example, the reheating medium SK is superheated steam that is generated by reheating the heating medium in the heat treatment chamber 1 adjusted to the heat treatment atmosphere F by the reheating medium generation and injection mechanism 18 and volume-expanded.
The temperature of the reheating medium (superheated steam) SK is set, for example, about 10 ° C. higher than the temperature in the heat treatment chamber 1. Depending on the supply amount of the heating medium and the like, it is necessary to adjust the increase in the specific volume (volume expansion) by appropriately raising the heating temperature of the reheating medium (superheated steam) SK.

再加熱媒体噴射部(左再加熱媒体噴射部24,右再加熱媒体噴射部25)は、その噴射部先端を加熱処理室1の上方から入口側外気遮蔽領域S1と出口側外気遮蔽領域S2に向けて再加熱媒体SKを噴射可能に位置させている。
従って、入口側外気遮蔽領域S1と出口側外気遮蔽領域S2に連続して噴射される体積が膨張した過熱水蒸気(再加熱媒体)SKは、それぞれの領域S1,S2に滞留するとともに、相当量が加熱処理室1内に流入し、その余りが室外に流出するため、加熱媒体の室外への流出及び外気の加熱処理室1内への侵入を防ぐことができる。特に本実施例によれば、入口側外気遮蔽領域S1と加熱処理領域S3との間、及び出口側外気遮蔽領域S2と加熱処理領域S3との間に、それぞれ境界壁6を設けているため、それぞれの境界壁6によってそれぞれの遮蔽領域S1,S2には体積膨張した過熱水蒸気SKが十分に滞留し易い構成となっている。
The reheating medium ejecting units (the left reheating medium ejecting unit 24 and the right reheating medium ejecting unit 25) have their ejection unit tips from above the heat treatment chamber 1 to the inlet side outside air shielding region S1 and the outlet side outside air shielding region S2. The reheating medium SK is positioned so as to be capable of being jetted.
Accordingly, the superheated steam (reheating medium) SK having an expanded volume continuously injected into the inlet-side outside air shielding area S1 and the outlet-side outside air shielding area S2 stays in the respective areas S1 and S2 and has a considerable amount. Since it flows into the heat treatment chamber 1 and the remainder flows out of the room, the outflow of the heating medium to the outside and the entry of outside air into the heat treatment chamber 1 can be prevented. In particular, according to the present embodiment, the boundary walls 6 are provided between the inlet side outside air shielding area S1 and the heat treatment area S3 and between the outlet side outside air shielding area S2 and the heat treatment area S3, respectively. Due to the respective boundary walls 6, the volume-expanded superheated steam SK is easily retained in the respective shielding regions S <b> 1 and S <b> 2.

なお、前記吸込み口19を一箇所、噴き出し口20,20を入口側外気遮蔽領域S1と出口側外気遮蔽領域S2の二箇所に設けた実施の一形態について説明したが、吸い込み口19を複数箇所とすることも可能で本発明の範囲内である。また、噴き出し口20は少なくとも入口側外気遮蔽領域S1と出口側外気遮蔽領域S2の二箇所は必須であるが、これ以上噴き出し口を設けることを何等妨げるものではない。   In addition, although description was given of an embodiment in which the suction port 19 is provided at one location and the ejection ports 20 and 20 are provided at two locations of the inlet-side outside air shielding region S1 and the outlet-side outside air shielding region S2, a plurality of suction ports 19 are provided. And within the scope of the present invention. In addition, at least two locations of the ejection port 20 of the inlet side outside air shielding region S1 and the outlet side outside air shielding region S2 are indispensable, but this does not prevent any further provision of the ejection port.

特に限定されるものではないが、本実施例では、加熱処理室1の入口上方外部2aと出口上方外部3aには、入口側外気遮蔽領域S1と出口側外気遮蔽領域S2から室外に溢れ出た再加熱媒体SKとともに、入口付近及び出口付近にある外気Gを吸込む室外吸い込み部26,26をそれぞれ備えている。   Although not particularly limited, in the present embodiment, the inlet upper outside 2a and the outlet upper outer 3a of the heat treatment chamber 1 overflowed from the inlet side outside air shielding area S1 and the outlet side outside air shielding area S2 to the outside. In addition to the reheating medium SK, outdoor suction portions 26 and 26 for sucking outside air G near the inlet and the outlet are provided.

室外吸い込み部26は、加熱処理室1の入口2を設けている入口2側の左側壁1eと出口3を設けている出口3側の右側壁1fに配設されている。
本実施例では、入口2側と出口3側のそれぞれの室外吸い込み部26,26は同一構成を採用しているため、以下、入口2側の室外吸い込み部26をもって説明し、出口3側の室外吸い込み部26の説明は省略する。
The outdoor suction portion 26 is disposed on the left side wall 1e on the inlet 2 side where the inlet 2 of the heat treatment chamber 1 is provided and the right side wall 1f on the outlet 3 side where the outlet 3 is provided.
In this embodiment, since the outdoor suction portions 26 and 26 on the inlet 2 side and the outlet 3 side have the same configuration, the outdoor suction portion 26 on the inlet 2 side will be described below. The description of the suction part 26 is omitted.

室外吸い込み部26は、入口2側の左側壁1eに取り付けられ、入口2に向かう搬送機構12の処理対象物T載置面12aに向けて大きく開口した第一吸い込み空間26aを有する第一箱部26bと、該第一吸い込み空間26aの上面に、第一吸い込み空間26aと連通し、かつ第一吸い込み空間26aよりも小さく開口した第二吸い込み空間26cを有する第二箱部26dと、該第二箱部26dの出口側開口26eと連通して備えた吸い込みファン26fと、該吸い込みファン26fの出口側と連通した吐き出し管部26gとで構成されている。
このように構成したため、入口側外気遮蔽領域S1に噴出され、入口2から溢れ出た再加熱媒体SKは、室外吸い込み部26の吸い込みファン26fによって強制的に第一吸い込み空間26aに吸い込まれる。この時、入口2付近にある外気Gも併せて一緒に第一吸い込み空間26aに吸い込まれる。そして、吸い込まれた再加熱媒体SKと外気Gは、第二吸い込み空間26cを経由して吐き出し管部26gへと送られ、該吐き出し管部26gの先端開口26hから外気側へと排出される。
The outdoor suction portion 26 is attached to the left side wall 1e on the inlet 2 side, and has a first box portion having a first suction space 26a that opens greatly toward the processing object T placement surface 12a of the transport mechanism 12 toward the inlet 2. A second box portion 26d having a second suction space 26c that communicates with the first suction space 26a and opens smaller than the first suction space 26a on the upper surface of the first suction space 26a; The suction fan 26f is provided in communication with the outlet side opening 26e of the box part 26d, and the discharge pipe part 26g is in communication with the outlet side of the suction fan 26f.
Since it comprised in this way, the reheating medium SK which was ejected to the entrance side outside air shielding area | region S1 and overflowed from the entrance 2 is forcibly sucked into the 1st suction space 26a by the suction fan 26f of the outdoor suction part 26. FIG. At this time, the outside air G in the vicinity of the inlet 2 is also sucked together into the first suction space 26a. Then, the sucked reheating medium SK and the outside air G are sent to the discharge pipe part 26g via the second suction space 26c, and discharged from the tip opening 26h of the discharge pipe part 26g to the outside air side.

本実施例の加熱処理方法は、上述した加熱処理装置において行われる、加熱媒体供給工程と、加熱処理工程と、再加熱媒体生成噴射工程からなる。   The heat treatment method of the present embodiment includes a heating medium supply step, a heat treatment step, and a reheating medium generation jetting step that are performed in the above-described heat treatment apparatus.

「加熱媒体供給工程」
本実施例では、加熱処理室1内を上述したように所定温度以上、例えば115℃程度に加熱制御する。
そして、水供給源から定量ポンプPを介して加熱管路15内に0.7gr/sec以上で水を供給する。そして、このように供給された水を、前記加熱チャンバ14によって所定温度及び所定圧力(120℃以上、0.19MPa以上)で沸騰させることで加熱管路15内に水蒸気Mと熱水Hからなる気液混合体を生成する。
そして、ノズル内圧0.19MPa以上、ノズル内部温度120℃以上に制御した加熱媒体噴射ノズル17を介して前記加熱制御された加熱処理室1内に、前記気液混合体を噴出することにより、前記加熱処理室1内を過熱水蒸気KMと高温微細水滴KHが混在する状態の加熱媒体で満たされた加熱処理雰囲気Fに調整する。
"Heating medium supply process"
In this embodiment, the inside of the heat treatment chamber 1 is controlled to be heated to a predetermined temperature or higher, for example, about 115 ° C. as described above.
Then, water is supplied from the water supply source through the metering pump P into the heating pipe line 15 at 0.7 gr / sec or more. Then, the water supplied in this way is boiled at a predetermined temperature and a predetermined pressure (120 ° C. or higher, 0.19 MPa or higher) by the heating chamber 14, thereby comprising water vapor M and hot water H in the heating pipe line 15. A gas-liquid mixture is produced.
And, by ejecting the gas-liquid mixture into the heat-treated heat treatment chamber 1 through the heating medium spray nozzle 17 controlled to a nozzle internal pressure of 0.19 MPa or more and a nozzle internal temperature of 120 ° C. or more, The inside of the heat treatment chamber 1 is adjusted to a heat treatment atmosphere F filled with a heating medium in a state where superheated steam KM and high-temperature fine water droplets KH are mixed.

「加熱処理工程」
次に、前記所定の加熱処理雰囲気Fに調整された加熱処理室1内に、所定の処理対象物Tを搬送籠Aに載置するとともに順次搬送して連続して加熱処理する。
すなわち、搬送機構12によって加熱処理室1内に搬送された処理対象物Tは、所定の加熱処理雰囲気Fとなっている加熱処理室1内を所定の時間掛けて搬送されることで、その加熱処理室1内に充満されている加熱処理雰囲気(加熱媒体)Fによって加熱処理される。すなわち、本実施例によれば、高温微細水滴KHにより処理対象物Tの表面で凝縮伝熱が発生する。また、その周囲は過熱水蒸気KMが充満しており、凝縮伝熱により潜熱を失った微細水滴は、過熱水蒸気KM中に蒸発する。この結果、過熱水蒸気同様に処理対象物Tへの凝縮水による影響が無く、更に、蒸発による内部水分の減少もほとんどない加熱特性が得られる。
"Heat treatment process"
Next, in the heat treatment chamber 1 adjusted to the predetermined heat treatment atmosphere F, the predetermined treatment target T is placed on the conveyance rod A and sequentially conveyed to be continuously heat-treated.
That is, the processing object T transferred to the heat treatment chamber 1 by the transfer mechanism 12 is transferred in the heat treatment chamber 1 having a predetermined heat treatment atmosphere F over a predetermined time, so that the heating target T is heated. Heat treatment is performed by a heat treatment atmosphere (heating medium) F filled in the treatment chamber 1. That is, according to the present embodiment, condensation heat transfer is generated on the surface of the processing target T by the high-temperature fine water droplets KH. Further, the surrounding area is filled with superheated steam KM, and fine water droplets that have lost their latent heat due to condensation heat transfer evaporate into the superheated steam KM. As a result, like the superheated steam, there is no influence of the condensed water on the processing target T, and further, the heating characteristic is obtained in which the internal moisture is hardly reduced by evaporation.

「再加熱媒体生成噴射工程」
再加熱媒体生成噴射工程は、まず、加熱処理室1内の加熱処理雰囲気Fの一部を、吸い込みファン22,22により吸込み口19から連絡管21内へと吸い出す。そして、その連絡管21内へと吸い出した加熱媒体を、連絡管21内のコイル状加熱部23,23,23によって所定温度以上に加熱して体積膨張した再加熱媒体(過熱水蒸気)SKを生成する。
そしてその後、体積膨張した再加熱媒体(過熱水蒸気)SKを加熱処理室1内の入口側外気遮蔽領域S1と出口側外気遮蔽領域S2に、左再加熱媒体噴射部24と右再加熱媒体噴射部25のそれぞれの噴き出し口20,20を介して噴射する。
"Reheating medium generation injection process"
In the reheating medium generation and injection step, first, a part of the heat treatment atmosphere F in the heat treatment chamber 1 is sucked out from the suction port 19 into the communication pipe 21 by the suction fans 22 and 22. Then, the heating medium sucked into the connecting pipe 21 is heated to a predetermined temperature or more by the coiled heating parts 23, 23, 23 in the connecting pipe 21 to generate a reheat medium (superheated steam) SK that has undergone volume expansion. To do.
After that, the volume-expanded reheating medium (superheated steam) SK is transferred to the inlet side outside air shielding area S1 and the outlet side outside air shielding area S2 in the heat treatment chamber 1, and the left reheating medium ejection part 24 and the right reheating medium ejection part. 25 are ejected through the respective ejection ports 20 and 20.

前記噴射される体積膨張した再加熱媒体(過熱水蒸気)SKは、それぞれの領域S1,S2に滞留するとともに、相当量が加熱処理室1内に流入し、その余りが室外に流出する(溢れ出る)ため、加熱媒体の室外への流出及び外気の室内への侵入を防ぐことができる。なお、加熱処理室1内に充満している加熱処理雰囲気(加熱媒体)Fそのものが過熱水蒸気KMと高温微細水滴KHが混在する状態の加熱媒体であるため、加熱処理雰囲気Fの加熱処理室1内に過熱水蒸気(再加熱媒体)SKが流入してきても差し支えない。更に過熱水蒸気KM中を飛行する高温微細水滴KHは、距離の経過と共に粒径が更に微細化して、最後には蒸発して過熱水蒸気となる特性のため、加熱処理室1の中央領域である加熱処理領域S3に存する加熱媒体の一部を吸い出して再加熱することにより容易に高温の過熱水蒸気SKを生成する事が可能である。また、そのための費用対効果も比較的低くできる。   The ejected volume-expanded reheating medium (superheated steam) SK stays in the respective regions S1 and S2, and a considerable amount flows into the heat treatment chamber 1, and the remainder flows out of the chamber (overflows). Therefore, it is possible to prevent the heating medium from flowing out into the room and the outside air from entering the room. In addition, since the heat treatment atmosphere (heating medium) F itself that is filled in the heat treatment chamber 1 is a heating medium in which the superheated steam KM and the high-temperature fine water droplets KH are mixed, the heat treatment chamber 1 in the heat treatment atmosphere F There is no problem even if superheated steam (reheating medium) SK flows into the inside. Further, the high-temperature fine water droplets KH flying in the superheated steam KM are further refined with the passage of distance, and finally evaporate to become superheated steam. It is possible to easily generate the high-temperature superheated steam SK by sucking out a part of the heating medium existing in the processing region S3 and reheating it. In addition, the cost-effectiveness for this can be relatively low.

また、本実施例によれば、加熱処理室1の入口上方外部2aと出口上方外部3aに室外吸い込み部26,26を備える形態を採用としたため、入口側外気遮蔽領域S1と出口側外気遮蔽領域S2に噴出され、入口2及び出口3から溢れ出た再加熱媒体(過熱水蒸気)SKは、それぞれの室外吸い込み部26,26の吸い込みファン26f,26fによって強制的に第一吸い込み空間26a,26aに吸い込まれる。この時、入口2付近にある外気G及び出口3付近にある外気Gも併せて一緒に第一吸い込み空間26a,26aに吸い込まれる。そして、吸い込まれた再加熱媒体(過熱水蒸気)SKと外気Gは、第二吸い込み空間26c,26cを経由して吐き出し管部26g,26gへと送られ、該吐き出し管部26g,26gの先端開口26h,26hから外気側へと排出される。
よって、入口2付近と出口3付近にある外気Gは、加熱処理室1内へと侵入することなく室外吸い込み部26,26によって強制的に吸込まれて排出されるため、さらに加熱処理室1内への外気の侵入が阻止されるため、加熱処理室1内は、常に所定の加熱処理雰囲気Fが維持できる。
In addition, according to the present embodiment, since the configuration in which the outdoor suction portions 26 and 26 are provided in the inlet upper outside 2a and the outlet upper outer 3a of the heat treatment chamber 1, the inlet side outside air shielding region S1 and the outlet side outside air shielding region are employed. The reheating medium (superheated steam) SK ejected to S2 and overflowing from the inlet 2 and the outlet 3 is forced into the first suction spaces 26a and 26a by the suction fans 26f and 26f of the outdoor suction portions 26 and 26, respectively. Inhaled. At this time, the outside air G near the inlet 2 and the outside air G near the outlet 3 are also sucked into the first suction spaces 26a and 26a together. Then, the sucked reheating medium (superheated steam) SK and the outside air G are sent to the discharge pipe portions 26g and 26g via the second suction spaces 26c and 26c, and the leading ends of the discharge pipe portions 26g and 26g are opened. It is discharged from 26h, 26h to the outside air side.
Therefore, the outside air G in the vicinity of the inlet 2 and the outlet 3 is forcibly sucked and discharged by the outdoor suction portions 26 and 26 without entering the heat treatment chamber 1. Since the outside air is prevented from entering, the heat treatment chamber 1 can always maintain a predetermined heat treatment atmosphere F.

上述した加熱媒体供給工程、加熱処理工程、再加熱媒体生成噴射工程は、たとえば、本実施例では、加熱媒体供給工程を経て、加熱処理室1内を所定の加熱処理雰囲気Fとする必要があるため、まず加熱媒体供給工程を最初に行われなければならない。
そして、所定の加熱処理雰囲気Fとなった後、再加熱媒体生成噴射工程を経て入口側外気遮蔽領域S1と出口側外気遮蔽領域S2に体積が膨張した所定の過熱水蒸気SKを噴射して加熱処理領域S3に満たされている加熱媒体の室外への流出及び外気の室内への侵入を防ぐものとする。
このような状況が整った後、加熱処理工程を経て処理対象物を連続して加熱処理室1内に搬送し、加熱処理領域S3にて所定の加熱処理を行うものとしている。
In the present embodiment, for example, in the present embodiment, the heating medium supply process, the heat treatment process, and the reheating medium generation and injection process described above require that the inside of the heat treatment chamber 1 be a predetermined heat treatment atmosphere F through the heating medium supply process. For this reason, the heating medium supply step must be performed first.
Then, after the predetermined heat treatment atmosphere F is reached, the heat treatment is performed by injecting the predetermined superheated steam SK having a volume expanded into the inlet side outside air shielding region S1 and the outlet side outside air shielding region S2 through the reheating medium generation and injection step. It is assumed that the heating medium filled in the region S3 is prevented from flowing out of the room and from the outside air entering the room.
After such a situation is prepared, the object to be processed is continuously transferred into the heat treatment chamber 1 through the heat treatment step, and a predetermined heat treatment is performed in the heat treatment region S3.

なお、本実施例では、加熱処理室1内を所定の加熱処理雰囲気Fとするため、上述した加熱媒体構成を採用しているが、これに限定解釈はされず、例えば、一般に広く知られている過熱水蒸気を加熱媒体として採用することも可能である。
この場合、加熱処理室内に配設した複数個の噴射ノズルから大量の過熱水蒸気を処理対象物に向けて噴射し、処理対象物の周囲を過熱水蒸気雰囲気とすることとなるため、その発生量に見合うだけの再加熱媒体(再生過熱水蒸気)を生成し、入口側外気遮蔽領域S1、出口側外気遮蔽領域S2に噴射するように調整する。この場合、加熱処理室1内に処理室内加熱機構7を備えても備えなくとも良い。
In the present embodiment, the above-described heating medium configuration is adopted in order to set the inside of the heat treatment chamber 1 to a predetermined heat treatment atmosphere F. However, the present invention is not limited to this, and is widely known, for example. It is also possible to employ superheated steam as a heating medium.
In this case, a large amount of superheated steam is sprayed from the plurality of spray nozzles arranged in the heat treatment chamber toward the object to be processed, and the surroundings of the object to be processed are brought to a superheated steam atmosphere. An appropriate reheating medium (regenerated superheated steam) is generated and adjusted so as to be injected into the inlet side outside air shielding area S1 and the outlet side outside air shielding area S2. In this case, the processing chamber heating mechanism 7 may or may not be provided in the heat processing chamber 1.

Claims (10)

一端側に開口した入口と、他端側に開口した出口とを設け、入口付近の入口側外気遮蔽領域と、出口付近の出口側外気遮蔽領域と、前記入口側外気遮蔽領域と出口側外気遮蔽領域との間に連続して配設される加熱処理領域とに区分けされた加熱処理室を備えており、
前記加熱処理領域内を処理室内加熱機構にて所定温度以上に加熱するとともに、前記加熱された加熱処理領域内に加熱媒体を噴射して前記加熱処理領域内を加熱処理雰囲気とする加熱媒体供給工程と、
前記加熱処理領域内に処理対象物を搬送して加熱処理する加熱処理工程と、
前記加熱処理領域内の加熱処理雰囲気の一部を加熱処理領域外へと吸い出し、所定温度以上に加熱して体積膨張した再加熱媒体を生成した後、該体積膨張した再加熱媒体を前記入口側外気遮蔽領域内及び出口側外気遮蔽領域内へとそれぞれ連続して噴射することで、前記入口側外気遮蔽領域内及び出口側外気遮蔽領域内に高温の再加熱媒体を滞留せしめる再加熱媒体生成噴射工程と、
前記入口側外気遮蔽領域の上流側と出口側外気遮蔽領域の下流側にて、入口側外気遮蔽領域と出口側外気遮蔽領域のそれぞれから溢れ出た再加熱媒体と、入口付近及び出口付近にある外気とを吸い込むことで、外気の加熱処理領域内への侵入を防ぐ室外吸い込み工程を備えていることを特徴とする加熱処理方法。
An inlet opened on one end side and an outlet opened on the other end side are provided, an inlet-side outside air shielding area near the inlet, an outlet-side outside air shielding area near the outlet, the inlet-side outside air shielding area, and the outlet-side outside air shielding. A heat treatment chamber divided into a heat treatment region continuously disposed between the regions,
A heating medium supply step of heating the inside of the heat treatment region to a predetermined temperature or higher by a heating mechanism inside the treatment chamber, and injecting a heating medium into the heated heat treatment region to make the inside of the heat treatment region a heat treatment atmosphere When,
A heat treatment step of carrying and heat-treating the object to be treated in the heat treatment region ;
The heating portion of the heating atmosphere of the processing area the sucked to the heat treatment outside the area, after generating the reheated medium volume expansion by heating above a predetermined temperature, said volume expanded reheated medium the inlet side Reheating medium generation injection in which a high-temperature reheating medium is retained in the inlet side outside air shielding area and the outlet side outside air shielding area by continuously injecting into the outside air shielding area and the outlet side outside air shielding area, respectively. Process,
Reheating medium overflowing from each of the inlet side outside air shielding area and the outlet side outside air shielding area on the upstream side of the inlet side outside air shielding area and the downstream side of the outlet side outside air shielding area, and in the vicinity of the inlet and the vicinity of the outlet A heat treatment method characterized by comprising an outdoor suction step for preventing outside air from entering the heat treatment region by sucking outside air .
加熱媒体供給工程は、
加熱処理領域内を、常圧で、かつ115℃程度に加熱制御し、
水供給源から0.7gr/sec以上で供給された水を所定温度及び所定圧力で沸騰させることで水蒸気と熱水からなる気液混合体を生成するとともに、前記気液混合体を加熱処理領域内に噴射する加熱媒体噴射ノズルを備え、
前記加熱媒体噴射ノズルは、内圧0.19MPa以上、ノズル内部温度120℃以上に制御されており、
前記加熱媒体噴射ノズルを介して、前記加熱処理領域内に気液混合体を噴射することで、前記加熱処理領域内を過熱水蒸気と高温微細水滴が混在する状態の加熱媒体で満たされた加熱処理雰囲気に調整し、
再加熱媒体は、前記加熱処理雰囲気に調整されている加熱処理領域内の加熱媒体を再加熱して生成され体積膨張した過熱水蒸気であることを特徴とする請求項1に記載の加熱処理方法。
The heating medium supply process
The inside of the heat treatment area is controlled at normal pressure and about 115 ° C.,
The water supplied from the water supply source at a rate of 0.7 gr / sec or more is boiled at a predetermined temperature and a predetermined pressure to produce a gas-liquid mixture composed of water vapor and hot water, and the gas-liquid mixture is subjected to a heat treatment region. A heating medium spray nozzle for spraying into the inside,
The heating medium spray nozzle is controlled to have an internal pressure of 0.19 MPa or more and a nozzle internal temperature of 120 ° C. or more.
Heat treatment filled with a heating medium in a state where superheated steam and high-temperature fine water droplets are mixed in the heat treatment region by injecting a gas-liquid mixture into the heat treatment region via the heating medium injection nozzle. Adjust to the atmosphere,
2. The heat treatment method according to claim 1, wherein the reheat medium is superheated steam that is generated by reheating the heat medium in the heat treatment region adjusted to the heat treatment atmosphere and volume-expanded. 3.
加熱媒体は、処理対象物の加熱処理中において、連続して噴射されることを特徴とする請求項1又は2に記載の加熱処理方法。   The heat treatment method according to claim 1, wherein the heating medium is continuously ejected during the heat treatment of the object to be treated. 再加熱媒体は、入口側外気遮蔽領域内と出口側外気遮蔽領域内に向けて、拡開状に噴射されることを特徴とする請求項1乃至3のいずれかに記載の加熱処理方法。 4. The heat treatment method according to claim 1 , wherein the reheating medium is sprayed in an expanded manner toward the entrance-side outside air shielding area and the exit-side outside air shielding area. 一端側に開口した入口と、他端側に開口した出口とを設け、入口付近の入口側外気遮蔽領域と、出口付近の出口側外気遮蔽領域と、前記入口側外気遮蔽領域と出口側外気遮蔽領域との間に連続して配設される加熱処理領域とに区分けされた加熱処理室と
前記加熱処理室の加熱処理領域内に配し、加熱処理領域内を所定温度以上に加熱して所定の加熱処理雰囲気に調整する処理室内加熱機構と、
前記入口から前記出口に向かって処理対象物を搬送する搬送機構と、
前記加熱処理室の加熱処理領域内に加熱媒体を噴射する加熱媒体噴射ノズルを備えた加熱媒体生成機構と、
前記加熱処理室の加熱処理領域内の少なくとも一部に設けた吸込み口と、前記入口側外気遮蔽領域と前記出口側外気遮蔽領域に設けた噴き出し口と、前記吸込み口と噴き出し口とにわたって連通した連絡管と、該連絡管の所定箇所に備えられ、加熱処理領域内に噴射した前記加熱媒体を前記吸込み口から前記連絡管内へと強制的に吸い出す吸込みファンと、該吸込みファンで吸い出した加熱媒体を連絡管内で所定温度以上に加熱して体積膨張した再加熱媒体を生成する加熱部と、前記生成した再加熱媒体を、前記噴き出し口から前記入口側外気遮蔽領域内及び出口側外気遮蔽領域内へとそれぞれ噴射させる再加熱媒体噴射部を備えた再加熱媒体生成噴射機構と
入口側外気遮蔽領域の上流側と出口側外気遮蔽領域の下流側には、入口側外気遮蔽領域と出口側外気遮蔽領域のそれぞれから室外に溢れ出た再加熱媒体とともに、入口付近及び出口付近にある外気を吸い込む室外吸い込み部をそれぞれ備え、
前記入口側外気遮蔽領域と出口側外気遮蔽領域は、前記再加熱媒体噴射機構を介してそれぞれ再加熱媒体が連続して噴射されることで、高温の再加熱媒体が滞留し易い再加熱媒体の噴射・滞留領域として機能することを特徴とする加熱処理装置。
An inlet opened on one end side and an outlet opened on the other end side are provided , an inlet-side outside air shielding area near the inlet, an outlet-side outside air shielding area near the outlet, the inlet-side outside air shielding area, and the outlet-side outside air shielding. placed in a continuous heat treatment chamber which is divided into a heat treatment area are disposed with the heat treatment chamber of the heat treatment in the region between the region, the predetermined heat processing region is heated to a predetermined temperature or higher A processing chamber heating mechanism that adjusts to the heat treatment atmosphere of
A transport mechanism for transporting the processing object from the inlet toward the outlet;
A heating medium generating mechanism including a heating medium spray nozzle that sprays the heating medium into the heat treatment region of the heat treatment chamber;
A suction port provided in at least a part of the heat treatment region of the heat treatment chamber , a blowout port provided in the inlet-side outside air shielding region and the outlet-side outside air shielding region, and the suction port and the blowout port communicated with each other. A communication pipe, a suction fan that is provided at a predetermined location of the communication pipe and forcibly sucks out the heating medium sprayed into the heat treatment region from the suction port into the communication pipe, and a heating medium sucked out by the suction fan A heating section that generates a reheat medium that has undergone volume expansion by heating to a predetermined temperature or more in the communication pipe, and the generated reheat medium from the outlet to the inside of the inlet side outside air shielding area and inside the outlet side outside air shielding area A reheating medium generating / injecting mechanism including a reheating medium injecting unit that injects each of the
On the upstream side of the inlet side outside air shielding area and the downstream side of the outlet side outside air shielding area, the reheating medium overflows from the inlet side outside air shielding area and the outlet side outside air shielding area, and near the inlet and the outlet. Each has an outdoor suction section that sucks in some outside air,
The inlet-side outside air shielding area and the outlet-side outside air shielding area are formed of a reheating medium in which a high-temperature reheating medium tends to stay by being continuously ejected through the reheating medium ejection mechanism . A heat treatment apparatus that functions as an injection / retention area .
加熱処理領域は処理室内加熱機構を備え、常圧で、かつ処理室内加熱機構によって115℃程度に加熱制御されており、
加熱媒体生成機構は、加熱部と、水供給源と連絡して前記加熱部により加熱される管路と、前記管路の先端部に備えられ、加熱処理領域内に先端を臨ませてなる加熱媒体噴射ノズルを備え、前記加熱媒体噴射ノズルは、内圧0.19MPa以上、内部温度120℃以上に制御されており、
前記管路内に0.7gr/sec以上で供給された水を所定温度及び所定圧力で沸騰させることで管路内に水蒸気と熱水からなる気液混合体を生成し、
前記加熱媒体噴射ノズルを介して前記気液混合体を前記加熱処理領域内に噴出することにより、前記加熱処理領域内を過熱水蒸気と高温微細水滴が混在する状態の加熱媒体で満たされた加熱処理雰囲気に調整しており、
再加熱媒体は、前記加熱処理雰囲気に調整されている加熱処理領域内の加熱媒体を、再加熱媒体生成噴射機構により再加熱して生成され体積膨張した過熱水蒸気であることを特徴とする請求項5に記載の加熱処理装置。
The heat treatment region is provided with a treatment chamber heating mechanism, and is heated to about 115 ° C. at normal pressure and by the treatment chamber heating mechanism.
The heating medium generating mechanism includes a heating unit, a pipe line that is heated by the heating unit in communication with a water supply source, and a heating unit that is provided at a tip part of the pipe line and has a tip facing the heat treatment region . A medium injection nozzle, and the heating medium injection nozzle is controlled to have an internal pressure of 0.19 MPa or more and an internal temperature of 120 ° C. or more,
Producing a gas-liquid mixture consisting of water vapor and hot water in the pipeline by boiling water supplied at 0.7 g / sec or more into the pipeline at a predetermined temperature and pressure,
Heat treatment filled with a heating medium in a state where superheated steam and high-temperature fine water droplets are mixed in the heat treatment region by ejecting the gas-liquid mixture into the heat treatment region through the heating medium injection nozzle. Adjusted to the atmosphere,
Reheating medium, claims, characterized in that the heating medium heated in the area which is adjusted to the heat treatment atmosphere is a superheated water vapor volume is generated by reheating expanded by reheating medium generating ejection mechanism 5. The heat treatment apparatus according to 5 .
加熱媒体は、処理対象物の加熱処理中において、連続して噴射されることを特徴とする請求項5又は6に記載の加熱処理装置。   The heat treatment apparatus according to claim 5 or 6, wherein the heating medium is continuously ejected during the heat treatment of the object to be treated. 再加熱媒体噴射部は、吸込みファンの吹き出し口と入口側外気遮蔽領域の上方に設けた接続開口部との間、及び、吸込みファンの吹き出し口と出口側外気遮蔽領域の上方に設けた接続開口部との間にわたってそれぞれ下り傾斜の漏斗状に形成されて配設されており、The reheating medium injection section is provided between the suction fan outlet and the connection opening provided above the inlet side outside air shielding area, and the connection opening provided above the suction fan outlet and the outlet side outside air shielding area. It is formed and arranged in a down-tilt funnel shape between each part,
再加熱媒体は、前記下り傾斜の漏斗状に形成されたそれぞれの再加熱媒体噴射部から、入口側外気遮蔽領域内と出口側外気遮蔽領域内に向けて、それぞれ拡開状に噴射され、Reheating medium is sprayed in an expanded manner from the respective reheating medium spraying portions formed in the descending funnel shape toward the inside of the inlet side outside air shielding area and the inside of the outlet side outside air shielding area,
前記入口側外気遮蔽領域と加熱処理領域との境界、及び、出口側外気遮蔽領域と加熱処理領域との境界には、それぞれ入口側外気遮蔽領域内と出口側外気遮蔽領域内に噴射された再加熱媒体が滞留し易い領域に形成するための境界壁を設けていることを特徴とする請求項5乃至7のいずれかに記載の加熱処理装置。The boundary between the inlet side outside air shielding area and the heat treatment area and the boundary between the outlet side outside air shielding area and the heat treatment area are respectively injected into the inlet side outside air shielding area and the outlet side outside air shielding area. The heat treatment apparatus according to claim 5, further comprising a boundary wall for forming the heating medium in a region where the heating medium tends to stay.
室外吸い込み部は、入口側外気遮蔽領域の上流側と出口側外気遮蔽領域の下流側にそれぞれ連続して備えられており、The outdoor suction section is continuously provided on the upstream side of the inlet side outside air shielding area and the downstream side of the outlet side outside air shielding area, respectively.
搬送機構の処理対象物載置面に向けて開口した吸い込み空間を有する箱部と、箱部と連通した吸い込みファンを含み、Including a box portion having a suction space opened toward the processing object mounting surface of the transport mechanism, and a suction fan communicating with the box portion;
前記吸い込みファンの吸い込み作動によって搬送機構の処理対象物載置面付近にある外気が強制的に吸い込まれるとともに、入口側外気遮蔽領域と出口側外気遮蔽領域から負圧により再加熱媒体が引き出されて一緒に吸い込み空間へと吸い込まれて排出されることを特徴とする請求項5乃至8のいずれかに記載の加熱処理装置。  The suction operation of the suction fan forcibly sucks outside air near the processing object mounting surface of the transport mechanism, and the reheating medium is drawn out from the inlet side outside air shielding area and the outlet side outside air shielding area by negative pressure. The heat treatment apparatus according to claim 5, wherein the heat treatment apparatus is sucked into the suction space and discharged.
処理室内加熱機構は、加熱処理領域内の搬送方向における略中央の領域に、搬送機構の幅よりも広い間隔をもって一対で配設されているコイル状加熱部であって、The processing chamber heating mechanism is a coiled heating unit that is disposed in a pair at a distance wider than the width of the transport mechanism in a substantially central region in the transport direction within the heat treatment region,
前記一対のコイル状加熱部の間には、加熱処理領域内の加熱処理雰囲気が室内全域に行き渡るように撹拌する加熱処理室撹拌ファンを備え、Between the pair of coiled heating units, a heat treatment chamber stirring fan that stirs the heat treatment atmosphere in the heat treatment region so as to spread throughout the room,
前記加熱処理室撹拌ファンとそのファンを挟むようにして配される一対の処理室内加熱機構との間には、前記ファンの回転作動によって送風する際に、搬送機構上を移動して撹拌される気流を発生せしめるファンガードを備えたことを特徴とする請求項5乃至9のいずれかに記載の加熱処理装置。Between the heat treatment chamber agitating fan and a pair of treatment chamber heating mechanisms arranged so as to sandwich the fan, an air flow that is agitated by moving on the conveyance mechanism when the fan is blown by the rotation operation of the fan. The heat treatment apparatus according to claim 5, further comprising a fan guard that is generated.
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