JP2005049058A - Heat treatment equipment - Google Patents

Heat treatment equipment Download PDF

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JP2005049058A
JP2005049058A JP2003283361A JP2003283361A JP2005049058A JP 2005049058 A JP2005049058 A JP 2005049058A JP 2003283361 A JP2003283361 A JP 2003283361A JP 2003283361 A JP2003283361 A JP 2003283361A JP 2005049058 A JP2005049058 A JP 2005049058A
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outside air
heat treatment
exhaust pipe
cyclone cylinder
sublimate
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Oudo Fujita
翁堂 藤田
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JTEKT Thermo Systems Corp
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Koyo Thermo Systems Co Ltd
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    • 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
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
    • Y02A50/2351Atmospheric particulate matter [PM], e.g. carbon smoke microparticles, smog, aerosol particles, dust
    • 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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/25Process efficiency

Abstract

<P>PROBLEM TO BE SOLVED: To solve problems in conventional heat treatment equipment that environmental pollution is caused when the recovery of an atmospheric sublimate generated by the heat treatment equipment is not necessarily good, the man-hour for maintenance of factory internal piping is increased by desorption and coagulation of the sublimate in the middle of exhaust system piping, and the atmospheric sublimate of the heat treatment equipment cannot be efficiently recovered. <P>SOLUTION: This heat treatment equipment comprises a primary exhaust pipe 2 communicating with the internal space 1a of a heat treatment tank 1; an outside air intake port 3 combined with the middle of the primary exhaust pipe 2; a sprinkler nozzle 4 for injecting water at the vicinity of a combined point P between the primary exhaust pipe 2 and the outside air intake port 3; a cyclone cylinder 5 for receiving a mixture of exhaust gas, outside air, and sprayed water; an exhaust sucking blower 8 for sucking the exhaust gas in the cyclone cylinder through a secondary exhaust pipe 6; and a water tank 7 for receiving the water sprayed from the sprinkler nozzle 4 which contains the sublimate. The inflow quantity of the outside air is adjusted by the flow regulating valve 9 of the outside air intake port 3. The sprinkler nozzle 3 may not be used. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

本発明は、液晶パネルなどの電子部品を加熱処理する際、周囲の雰囲気中に放出されるバインダ等主として有機物の蒸発物の昇華物を除去してクリーンな排気ガスとして処理する熱処理装置に関する。   The present invention relates to a heat treatment apparatus for removing mainly sublimates of organic evaporants such as a binder released into the surrounding atmosphere and treating it as a clean exhaust gas when heat-treating an electronic component such as a liquid crystal panel.

液晶パネル等の電子部品の製造時には、熱処理装置により加熱処理する工程があり、液晶パネル面に塗布された顔料(レジスト)やバインダ等が加熱されることにより蒸発し、昇華物として処理室内の雰囲気中に放出される。熱処理室は、通常、不純物の付着や混入を防止するためクリーンな空間に保つ必要があり、熱処理室内の雰囲気の空気は、排気ダクトを通して排気装置により排出される。しかし、このような排気ガス中の昇華物は、高温時は蒸発して雰囲気ガス中に存在するが、排気ガスの温度が一定温度以下に低下すると、雰囲気ガス中から離脱、凝固する。このように途中で離脱、凝固した昇華物が排気ガス配管途中のフィルタや管通路に付着し、フィルタ機能を低下させたり配管内を汚染するという問題がある。また、凝固せずに屋外に排出された場合、周囲の生活環境に悪影響を及ぼす、という問題もある。   When manufacturing electronic components such as liquid crystal panels, there is a process of heat treatment using a heat treatment device, and the pigment (resist) or binder applied to the liquid crystal panel surface evaporates when heated, and the atmosphere in the treatment chamber is formed as a sublimated product. Released into. The heat treatment chamber usually needs to be kept in a clean space in order to prevent adhesion and mixing of impurities, and air in the atmosphere in the heat treatment chamber is exhausted by an exhaust device through an exhaust duct. However, although the sublimate in the exhaust gas evaporates at a high temperature and exists in the atmospheric gas, when the temperature of the exhaust gas falls below a certain temperature, the sublimate is separated from the atmospheric gas and solidifies. Thus, there is a problem that the sublimate that has been detached and solidified in the middle adheres to a filter or a pipe passage in the middle of the exhaust gas pipe, thereby lowering the filter function or contaminating the inside of the pipe. In addition, there is a problem that when discharged to the outdoors without solidifying, it adversely affects the surrounding living environment.

上記するように、熱処理装置の稼働によって生じる昇華物の混入している雰囲気ガスを排出する従来の熱処理装置としては、熱処理室内の雰囲気(気体)を吸引する排気系として、熱処理室と外部との間に設けた開口部から処理室内の空気を所定の圧力で吸引するガスラインと、外気を吸引する外気ラインと、外気吸入量を調整するダンパと、駆動装置付の吸気フアンと、隣接する機械室と処理室との差圧を一定となるように構成した制御装置と、吸引した気体を昇華物が固形化する温度まで冷却する接触式水冷却器、等より構成される昇華物除去機能付熱処理装置が提案されている(特許文献1)。   As described above, as a conventional heat treatment apparatus that discharges atmospheric gas mixed with sublimates generated by the operation of the heat treatment apparatus, as an exhaust system that sucks the atmosphere (gas) in the heat treatment chamber, A gas line that sucks air in the processing chamber at a predetermined pressure from an opening provided therebetween, an outside air line that sucks outside air, a damper that adjusts the outside air intake amount, an intake fan with a drive device, and an adjacent machine With sublimation removal function composed of a control device configured to maintain a constant differential pressure between the chamber and the processing chamber, a contact water cooler that cools the sucked gas to a temperature at which the sublimation solidifies, etc. A heat treatment apparatus has been proposed (Patent Document 1).

特開平07−242412JP 07-242412 A

熱処理装置で発生する昇華物の除去に際しては、熱処理装置に隣接した位置で素早く除去した方が昇華物の捕集効率はよい。しかし従来のものは比較的配管が長く捕集効率が必ずしも良いとは言えないものも多い。また、差圧の測定制御装置を用いる場合、構成が複雑で相当のスペースを必要とし、操作も煩雑で且つ高価となりやすい。また、昇華物には冷却水を必ずしも必要としないものもあり、冷却水を使用しないで昇華物の効率的回収ができれば後の処理が比較的容易となる。更に、高速且つ高効率の昇華物の回収ができれば環境汚染の度合いもより一層低下する。   When removing the sublimate generated in the heat treatment apparatus, the collection efficiency of the sublimate is better when it is quickly removed at a position adjacent to the heat treatment apparatus. However, many of the conventional ones have relatively long pipes and the collection efficiency is not necessarily good. Further, when using a differential pressure measurement control device, the configuration is complicated and requires a considerable space, and the operation is complicated and tends to be expensive. Some sublimates do not necessarily require cooling water, and if the sublimates can be efficiently recovered without using cooling water, the subsequent processing becomes relatively easy. Furthermore, if the sublimate can be collected at high speed and high efficiency, the degree of environmental pollution is further reduced.

本発明は、熱処理装置によって発生する雰囲気中の昇華物の回収が必ずしも良くない場合に生じる環境汚染、また、工場内における昇華物によるフィルタの目詰まりや排気系配管途中での昇華物の離脱、凝固により生じる工場内配管のメインテナンス工数の増大、熱処理装置の雰囲気中の昇華物の高効率的回収ができない、という問題を解決しようとするものである。   The present invention is environmental pollution that occurs when recovery of sublimates in the atmosphere generated by the heat treatment device is not necessarily good, filter clogging due to sublimates in the factory and the removal of sublimates during the exhaust system piping, An object of the present invention is to solve the problems that the maintenance man-hours of the piping in the factory caused by solidification and the high-efficiency recovery of sublimates in the atmosphere of the heat treatment apparatus cannot be performed.

請求項1の発明は、熱処理装置が、熱処理槽の内部空間に通じる一次排気管と、該一次排気管の途中で合流する外気吸入用ポートと、これらの排気管と外気吸入用ポートからの排気ガスを導入口より受け入れるサイクロン筒と、該サイクロン筒から排気ガスを排出する二次排気管と、該二次排気管を通じてサイクロン筒内の排気ガスを吸引する排気吸引用ブロワと、サイクロン筒内で分離された昇華物を収容する昇華物収納容器と、を備えてなることを特徴とする。   According to the first aspect of the present invention, the heat treatment apparatus includes a primary exhaust pipe that communicates with the internal space of the heat treatment tank, an outside air intake port that joins in the middle of the primary exhaust pipe, and an exhaust from the exhaust pipe and the outside air intake port. A cyclone cylinder for receiving gas from an inlet, a secondary exhaust pipe for discharging exhaust gas from the cyclone cylinder, an exhaust suction blower for sucking exhaust gas in the cyclone cylinder through the secondary exhaust pipe, and a cyclone cylinder And a sublimate storage container for storing the separated sublimate.

請求項2の発明は、熱処理装置が、熱処理槽の内部空間に通じる一次排気管と、該一次排気管の途中で合流する外気吸入用ポートと、前記一次排気管と外気吸入用ポートとの合流点近傍で水を噴射する散水ノズルと、これらの一次排気管と外気吸入用ポートから排気ガスと外気と散水混合物を受け入れるサイクロン筒と、該サイクロン筒からの排気ガスを吸引する二次排気管と、該二次排気管を通じてサイクロン筒内の排気ガスを吸引する排気吸引用ブロワと、前記サイクロン筒の下部に配置され、散水ノズルより散水され昇華物を含んだ水分を受け入れる水槽と、を備えたことを特徴とする。   The invention of claim 2 is characterized in that the heat treatment apparatus has a primary exhaust pipe that communicates with the internal space of the heat treatment tank, an outside air suction port that joins in the middle of the primary exhaust pipe, and a joining of the primary exhaust pipe and the outside air suction port. A water spray nozzle for injecting water in the vicinity of the point, a cyclone cylinder for receiving the exhaust gas, the outside air and the water spray mixture from the primary exhaust pipe and the outside air intake port, and a secondary exhaust pipe for sucking the exhaust gas from the cyclone cylinder; An exhaust suction blower that sucks exhaust gas in the cyclone cylinder through the secondary exhaust pipe, and a water tank that is disposed at a lower portion of the cyclone cylinder and that receives water containing water and sublimated water sprayed from a water spray nozzle. It is characterized by that.

請求項3の発明は、前記外気吸入用ポートには、途中に外気流量調節バルブを設けて成ることを特徴とする。   The invention of claim 3 is characterized in that the outside air intake port is provided with an outside air flow rate adjusting valve in the middle.

本発明の熱処理装置によれば、加熱処理によって発生する昇華物の含まれた雰囲気ガスを排気する場合、高い効率で昇華物を離脱、凝固させ分離回収することができる。よって排気系統(装置内、工場内)における昇華物の目詰まりや途中での付着を大幅に抑制、防止してメインテナンス工数を削減することができる。また、昇華物の回収効率が良いことから有害物排気による周囲の環境影響負荷を抑制、防止することができる。更に、本発明の熱処理装置は、気体での昇華物を固化して離脱、凝固させ冷却水を利用したり、固体という形で排出させることにより廃棄物としての取り扱いが容易となる。更に、排気温度を低下させて処理することができるので工場内排気系統の耐熱性を従来のように考慮する必要性がなくなる。更にまた、外気を吸入し風量が増大しサイクロン円筒内での旋回風速が大きくなり、遠心力も大きくなるので捕集効率が大幅に向上する。   According to the heat treatment apparatus of the present invention, when exhausting the atmospheric gas containing the sublimate generated by the heat treatment, the sublimate can be separated, solidified and separated and recovered with high efficiency. Therefore, clogging of sublimates in the exhaust system (inside the apparatus and in the factory) and adhesion on the way can be greatly suppressed and prevented, and maintenance man-hours can be reduced. In addition, since the sublimate collection efficiency is high, it is possible to suppress or prevent the environmental impact load of the surroundings due to the exhaust of harmful substances. Further, the heat treatment apparatus of the present invention makes it easy to handle as waste by solidifying and sublimating and solidifying the gas sublimate and using cooling water or discharging it in the form of a solid. Furthermore, since the exhaust gas can be processed at a reduced temperature, there is no need to consider the heat resistance of the exhaust system in the factory as in the prior art. Furthermore, since the outside air is sucked and the air volume is increased, the swirling wind speed in the cyclone cylinder is increased and the centrifugal force is increased, so that the collection efficiency is greatly improved.

以下、本発明を実施するための最良の形態について図面を参照しながら説明する。   The best mode for carrying out the present invention will be described below with reference to the drawings.

図1は、この発明の熱処理装置の第1の実施の形態である。この熱処理装置は、熱処理槽1の内部空間1aに通じる一次排気管2と、該一次排気管2の途中で合流する冷却用外気を取り入れる外気吸入用ポート3と、これら一次排気管2と外気吸入用ポート3からの排気ガスを導入口5aより受け入れるサイクロン筒5と、該サイクロン筒5から排気ガスを排出する二次排気管6と、該二次排気管6を通じてサイクロン筒5内で昇華物を離脱、凝固させて除去処理された排気ガスを吸引する排気吸引用ブロワ8と、サイクロン筒5内で分離された昇華物の固化物を収容する昇華物収納容器10と、で構成される。尚、前記外気吸入用ポート3には途中に流量調節バルブ9が設けられ、外気の流入量が調節される。   FIG. 1 shows a first embodiment of the heat treatment apparatus of the present invention. The heat treatment apparatus includes a primary exhaust pipe 2 that communicates with the internal space 1a of the heat treatment tank 1, an outside air intake port 3 that takes in outside air for cooling that merges in the middle of the primary exhaust pipe 2, and the primary exhaust pipe 2 and the outside air intake. A cyclone cylinder 5 for receiving the exhaust gas from the port 3 through the introduction port 5 a, a secondary exhaust pipe 6 for exhausting the exhaust gas from the cyclone cylinder 5, and a sublimation product in the cyclone cylinder 5 through the secondary exhaust pipe 6. An exhaust suction blower 8 that sucks exhaust gas that has been separated and solidified and removed, and a sublimate storage container 10 that stores solidified sublimate separated in the cyclone cylinder 5. The outside air intake port 3 is provided with a flow rate adjusting valve 9 in the middle to adjust the inflow amount of outside air.

以上のように構成された本発明の熱処理装置の第1の実施の形態は、次の動作により昇華物を除去する。
前記熱処理槽1の内部空間1aに通じる一次排気管2から排出された排気ガスは高温であり、熱処理時に発生したレジスト等の主として有機物の蒸発ガスが昇華物として排気ガス中に含まれている。この高温の昇華物混合の排気ガスは、一次排気管と外気吸入用ポート3との合流点近傍Pで、外気吸入用ポート3から導入される冷たい外気と合流し、急速に冷却される。こうして前記一次排気管2を通過した排気ガスは、固化温度まで低下し、該排気ガス中の昇華物は分離、凝固され粉粒状の固化物となり、排気ガスと共にサイクロン筒5内へ吸引される。この場合、合流点近傍Pは外気により冷却されるので昇華物の分離、凝固が促進される。
1st Embodiment of the heat processing apparatus of this invention comprised as mentioned above removes a sublimation by the following operation | movement.
The exhaust gas discharged from the primary exhaust pipe 2 communicating with the internal space 1a of the heat treatment tank 1 is high in temperature, and mainly organic evaporating gas such as resist generated during the heat treatment is contained in the exhaust gas as a sublimation product. The high-temperature sublimate mixed exhaust gas joins the cold outside air introduced from the outside air suction port 3 in the vicinity of the junction point P between the primary exhaust pipe and the outside air suction port 3, and is rapidly cooled. Thus, the exhaust gas that has passed through the primary exhaust pipe 2 is lowered to the solidification temperature, and the sublimate in the exhaust gas is separated and solidified to become a powdery solidified product, which is sucked into the cyclone cylinder 5 together with the exhaust gas. In this case, since the vicinity P of the junction is cooled by the outside air, the separation and solidification of the sublimate are promoted.

前記サイクロン筒5の内部へ排出された排気ガスと昇華物の粉粒状化した固化物との混合物は、排気ブロワ8の吸引力により、前記サイクロン筒5に設けた導入口5aより該サイクロン筒5の円周方向に大きな流速をもって排出される。そして、サイクロン筒5内に、強制渦流が生じると共に遠心力が発生し、混合物中の昇華物の粉粒状の固化物Mは、サイクロン筒5の内壁5bへ当り、下方へ落下する。こうして昇華物の固化物は、サイクロン筒5の排出口5cに設けた昇華物収納容器10の中へ排出される。   The mixture of the exhaust gas discharged into the cyclone cylinder 5 and the sublimated powdered solidified product is introduced into the cyclone cylinder 5 from the inlet 5 a provided in the cyclone cylinder 5 by the suction force of the exhaust blower 8. Is discharged with a large flow velocity in the circumferential direction. Then, a forced vortex flow is generated in the cyclone cylinder 5 and a centrifugal force is generated. The sublimate powder solidified product M in the mixture hits the inner wall 5b of the cyclone cylinder 5 and falls downward. Thus, the solidified product of the sublimate is discharged into the sublimate storage container 10 provided in the discharge port 5c of the cyclone cylinder 5.

図2は、本発明の熱処理装置の第2の実施の形態の構成概要を示す図である。この熱処理装置は、熱処理槽1の内部空間1aに通じる一次排気管2と、該一次排気管2の途中で合流する冷却用外気を取り入れる外気吸入用ポート3と、前記一次排気管2と外気吸入用ポート3との合流点近傍Pで水を噴射する散水ノズル4と、これらの一次排気管2と外気吸入用ポート3からの排気ガスと外気と散水混合物を導入口5aより受け入れるサイクロン筒5と、該サイクロン筒5から排気ガスを排出する二次排気管6と、該二次排気管6を通じてサイクロン筒内で昇華物除去処理のされた排気ガスを吸引する排気吸引用ブロワ8と、散水ノズル4より散水され昇華物を含んだ水分を受け入れる水槽7と、で構成される。尚、前記外気吸入用ポート3には途中に流量調節バルブ9が設けられ、外気の流入量が調節される。   FIG. 2 is a diagram showing an outline of the configuration of the second embodiment of the heat treatment apparatus of the present invention. The heat treatment apparatus includes a primary exhaust pipe 2 that communicates with the internal space 1a of the heat treatment tank 1, an outside air intake port 3 that takes in cooling outside air that joins in the middle of the primary exhaust pipe 2, and the primary exhaust pipe 2 and the outside air intake. A water spray nozzle 4 for injecting water in the vicinity of a junction P with the working port 3, and a cyclone cylinder 5 for receiving the exhaust gas, the outside air and the water sprinkled mixture from the primary exhaust pipe 2 and the outside air suction port 3 from the inlet 5 a A secondary exhaust pipe 6 that exhausts exhaust gas from the cyclone cylinder 5, an exhaust suction blower 8 that sucks exhaust gas that has been subjected to sublimation removal processing in the cyclone cylinder through the secondary exhaust pipe 6, and a water spray nozzle 4 and a water tank 7 for receiving water that has been sprinkled with water and containing sublimation. The outside air intake port 3 is provided with a flow rate adjusting valve 9 in the middle to adjust the inflow amount of outside air.

以上のように構成された昇華物除去機能付熱処理装置は、次の動作により昇華物を除去する。
前記熱処理槽1の内部空間1aに通じる一次排気管2から排出された排気ガスは高温であり、熱処理時に発生したレジスト等の蒸発物が昇華物として排気ガス中に含まれている。この高温の昇華物混合の排気ガスは、一次排気管と外気吸入用ポート3との合流点近傍Pで、外気吸入用ポート3から導入される冷たい外気と合流し、更に散水ノズル4からの散水による水分で急速に冷却される。こうして前記一次排気管2を通過した排気ガスは、固化温度まで低下し、該排気ガス中の昇華物は分離、凝固され粉粒物状の固化物となり、熱処理槽1からの排気ガス、外気、水分の混合物と共にサイクロン筒5内へ吸引される。この場合、合流点近傍Pは外気と冷却水により冷却されるので昇華物の分離、凝固が一層促進される。
The heat treatment apparatus with a sublimate removal function configured as described above removes the sublimate by the following operation.
The exhaust gas discharged from the primary exhaust pipe 2 communicating with the internal space 1a of the heat treatment tank 1 is at a high temperature, and evaporates such as resist generated during the heat treatment are contained in the exhaust gas as sublimates. The exhaust gas of the high-temperature sublimate mixture merges with the cold outside air introduced from the outside air intake port 3 in the vicinity P of the junction point between the primary exhaust pipe and the outside air intake port 3, and further the water spray from the water spray nozzle 4. Cools quickly with moisture. Thus, the exhaust gas that has passed through the primary exhaust pipe 2 is lowered to the solidification temperature, and the sublimate in the exhaust gas is separated and solidified to become a powdery solidified product. The exhaust gas from the heat treatment tank 1, the outside air, It is sucked into the cyclone cylinder 5 together with the water mixture. In this case, since the vicinity P of the junction is cooled by the outside air and the cooling water, the separation and solidification of the sublimate are further promoted.

前記サイクロン筒5の内部へ排出された排気ガス、昇華物の粉粒状の固化物と水分の混合物は、排気ブロワ8の吸引力により、前記サイクロン筒5に設けた導入口5aより該サイクロン筒5の円周方向に大きな流速をもって排出される。この排出によりサイクロン筒5内に、強制渦流が生じると共に遠心力が発生し、混合物中の昇華物の固化物Mは、分離され、サイクロン筒5の内壁5bへ当り、落下する。そして水分と共に該サイクロン筒5の下部へ落下して排出口5cより水槽7の中へ排出される。   The exhaust gas discharged into the cyclone cylinder 5, the mixture of the sublimated powdery solidified substance and the water is supplied to the cyclone cylinder 5 from the inlet 5 a provided in the cyclone cylinder 5 by the suction force of the exhaust blower 8. Is discharged with a large flow velocity in the circumferential direction. By this discharge, a forced vortex is generated in the cyclone cylinder 5 and a centrifugal force is generated. The sublimated solidified substance M in the mixture is separated, hits the inner wall 5b of the cyclone cylinder 5 and falls. And it falls to the lower part of this cyclone cylinder 5 with a water | moisture content, and is discharged | emitted in the water tank 7 from the discharge port 5c.

上記構成とした本発明の熱処理装置は、いずれの実施の形態においても、特に吸引用の排気ブロワ8は、サイクロン筒5の内部に発生する遠心力を最大限に大きくするため、その排気能力を向上させることが出来る。そして、サイクロン筒5内での旋回速度を上昇させても熱処理槽1からの排気量は変動せず、外気吸入用ポート3内に配置した流量調節バルブ9により外気の吸引のみを大きくすることができる。従って、処理後の排気を工場外部へ排出しても、外部の環境への影響が無く、調整の自由度を非常に高くすることが可能となる。   In any embodiment of the heat treatment apparatus of the present invention having the above-described configuration, in particular, the exhaust blower 8 for suction has its exhaust capability in order to maximize the centrifugal force generated in the cyclone cylinder 5. Can be improved. And even if the turning speed in the cyclone cylinder 5 is increased, the exhaust amount from the heat treatment tank 1 does not fluctuate, and only the intake of the outside air can be increased by the flow rate adjusting valve 9 disposed in the outside air intake port 3. it can. Therefore, even if the exhaust after treatment is discharged to the outside of the factory, there is no influence on the external environment, and the degree of freedom of adjustment can be greatly increased.

尚、吸引用の排気ブロワ8は、サイクロン筒5の内部に発生する遠心力を最大限に大きくして、その排気能力を向上させることが出来ること、サイクロン筒5内での旋回速度を上昇させても熱処理槽1からの排気量は変動せず、外気の吸引のみを大きくすることができること、処理後の排気を工場外部へ排出しても、外部の環境への影響が無く、調整の自由度を非常に高くすることが可能であること等は第1の実施の形態と同様である。   The suction exhaust blower 8 can maximize the centrifugal force generated in the cyclone cylinder 5 to improve its exhaust capacity, and increase the turning speed in the cyclone cylinder 5. However, the amount of exhaust from the heat treatment tank 1 does not fluctuate, it is possible to increase only the suction of outside air, and even if the exhaust after treatment is discharged to the outside of the factory, there is no influence on the external environment and adjustment is free It is possible to make the degree extremely high as in the first embodiment.

以上詳述したように、本発明の熱処理装置によれば、熱処理槽で蒸気として発生した昇華物を高い効率で分離、凝固化して回収することができるので、排気ガスをクリーン化して外部へ排出することができる。従って、工場周辺の環境を悪化させることない。また、産業廃棄物処理としても水槽排水のフィルタで回収し、交換のみですむため大幅な工数削減となる。装置自身もスペースを取らずコンパクト化することができる。   As described above in detail, according to the heat treatment apparatus of the present invention, the sublimate generated as vapor in the heat treatment tank can be separated, solidified and recovered with high efficiency, so the exhaust gas is cleaned and discharged to the outside. can do. Therefore, the environment around the factory is not deteriorated. In addition, industrial waste can be collected with a tank drain filter and only replaced, which greatly reduces man-hours. The device itself can be made compact without taking up space.

尚、本発明の実施の形態においては、サイクロン筒5がいずれも1つの場合について説明したが、図3に示すように、先ず一次排気管2と外気吸入用ポート3からの排気ガスと冷たい外気との合流した混合ガス及びその際凝固し粉粒状となった昇華物の固化物等の混合物を第1のサイクロン筒5へ導入し、昇華物を分離、除去してから更に排気管11を介して第2のサイクロン筒5へ導入するよう二連接続或いはそれ以上の多連接続のサイクロン筒を配置するようにしても良い。このようにサイクロン筒5を多連接続とすれば固化された昇華物をより一層高い収率で分離・除去することができる。   In the embodiment of the present invention, the case where there is only one cyclone cylinder 5 has been described. However, as shown in FIG. 3, first, the exhaust gas from the primary exhaust pipe 2 and the outside air intake port 3 and the cold outside air are cooled. And a mixture of solidified sublimate that has been solidified and powdered at that time are introduced into the first cyclone cylinder 5, and after the sublimate is separated and removed, the mixture is further passed through the exhaust pipe 11. Thus, a cyclonic cylinder having two or more multiple connections may be arranged so as to be introduced into the second cyclone cylinder 5. Thus, if the cyclone cylinder 5 is made into a multiple connection, the solidified sublimate can be separated and removed with a higher yield.

本発明は、液晶パネル、その他の電子部品等の製作等の過程で熱処理によって生じる昇華物を除去し、環境負荷を軽減することが可能な熱処理装置の製造及び電子機器類の産業の分野に適用することができる。   The present invention is applied to the field of manufacturing of a heat treatment apparatus capable of reducing the environmental burden by removing sublimates generated by heat treatment in the process of manufacturing liquid crystal panels and other electronic components, and the industrial field of electronic equipment. can do.

本発明の熱処理装置の第1の実施の形態の構成概要図である。BRIEF DESCRIPTION OF THE DRAWINGS It is a structure schematic diagram of 1st Embodiment of the heat processing apparatus of this invention. 本発明の熱処理装置の第2の実施の形態の構成概要図である。It is a structure schematic diagram of 2nd Embodiment of the heat processing apparatus of this invention. 本発明の熱処理装置を構成するサイクロン筒を2連とした場合の実施の形態の構成概要図である。It is a structure schematic diagram of embodiment at the time of making the cyclone cylinder which comprises the heat processing apparatus of this invention into 2 stations.

符号の説明Explanation of symbols

1 熱処理槽
2 一次配管
3 外気吸入用ポート
4 散水ノズル
5 サイクロン筒
6 二次配管
7 水槽
8 吸引用排気ブロワ
9 流量調節バルブ
10 昇華物収納容器
P 合流点近傍
1 Heat treatment tank
2 Primary piping 3 Outside air intake port 4 Sprinkling nozzle 5 Cyclone cylinder 6 Secondary piping 7 Water tank 8 Suction exhaust blower 9 Flow control valve 10 Sublimation storage container P Near junction

Claims (3)

熱処理槽の内部空間に通じる一次排気管と、該一次排気管の途中で合流する外気吸入用ポートと、これらの排気管と外気吸入用ポートからの排気ガスを導入口より受け入れるサイクロン筒と、該サイクロン筒から排気ガスを排出する二次排気管と、該二次排気管を通じてサイクロン筒内の排気ガスを吸引する排気吸引用ブロワと、サイクロン筒内で分離された昇華物を収容する昇華物収納容器と、を備えてなることを特徴とする熱処理装置。   A primary exhaust pipe that communicates with the internal space of the heat treatment tank, an outside air intake port that joins in the middle of the primary exhaust pipe, a cyclone cylinder that receives exhaust gas from these exhaust pipe and the outside air intake port from an inlet, A secondary exhaust pipe that exhausts exhaust gas from the cyclone cylinder, an exhaust suction blower that sucks exhaust gas in the cyclone cylinder through the secondary exhaust pipe, and a sublimate storage that stores the sublimate separated in the cyclone cylinder A heat treatment apparatus comprising: a container; 熱処理槽の内部空間に通じる一次排気管と、該一次排気管の途中で合流する外気吸入用ポートと、前記一次排気管と外気吸入用ポートとの合流点近傍で水を噴射する散水ノズルと、これらの一次排気管と外気吸入用ポートから排気ガスと外気と散水混合物を受け入れるサイクロン筒と、該サイクロン筒からの排気ガスを吸引する二次排気管と、該二次排気管を通じてサイクロン筒内の排気ガスを吸引する排気吸引用ブロワと、前記サイクロン筒の下部に配置され、散水ノズルより散水され昇華物を含んだ水分を受け入れる水槽と、を備えたことを特徴とする熱処理装置。   A primary exhaust pipe that communicates with the internal space of the heat treatment tank, an outside air suction port that joins in the middle of the primary exhaust pipe, and a water spray nozzle that jets water in the vicinity of the junction of the primary exhaust pipe and the outside air suction port; A cyclone cylinder that receives the exhaust gas, the outside air, and the sprinkled mixture from the primary exhaust pipe and the outside air intake port, a secondary exhaust pipe that sucks the exhaust gas from the cyclone cylinder, and the cyclone cylinder in the cyclone cylinder through the secondary exhaust pipe A heat treatment apparatus comprising: an exhaust suction blower that sucks exhaust gas; and a water tank that is disposed at a lower portion of the cyclone cylinder and receives water containing water that is sublimated and sprayed from a water spray nozzle. 前記外気吸入用ポートには、途中に外気流量調節バルブを設けて成ることを特徴とする請求項1または請求項2に記載の熱処理装置。 The heat treatment apparatus according to claim 1 or 2, wherein the outside air intake port is provided with an outside air flow rate adjustment valve in the middle thereof.
JP2003283361A 2003-07-31 2003-07-31 Heat treatment equipment Pending JP2005049058A (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008185284A (en) * 2007-01-31 2008-08-14 Furukawa Electric Co Ltd:The Treatment method for exhaust gas, and treatment facility for exhaust gas
JP2009236471A (en) * 2008-03-28 2009-10-15 Espec Corp Heat treatment device
CN101585665A (en) * 2008-05-21 2009-11-25 爱斯佩克株式会社 Heat treatment equipment

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008185284A (en) * 2007-01-31 2008-08-14 Furukawa Electric Co Ltd:The Treatment method for exhaust gas, and treatment facility for exhaust gas
JP2009236471A (en) * 2008-03-28 2009-10-15 Espec Corp Heat treatment device
CN101585665A (en) * 2008-05-21 2009-11-25 爱斯佩克株式会社 Heat treatment equipment

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