JPH047506Y2 - - Google Patents

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Publication number
JPH047506Y2
JPH047506Y2 JP6185489U JP6185489U JPH047506Y2 JP H047506 Y2 JPH047506 Y2 JP H047506Y2 JP 6185489 U JP6185489 U JP 6185489U JP 6185489 U JP6185489 U JP 6185489U JP H047506 Y2 JPH047506 Y2 JP H047506Y2
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JP
Japan
Prior art keywords
furnace
core tube
ceramic
furnace core
atmosphere
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP6185489U
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Japanese (ja)
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JPH033698U (en
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Priority to JP6185489U priority Critical patent/JPH047506Y2/ja
Publication of JPH033698U publication Critical patent/JPH033698U/ja
Application granted granted Critical
Publication of JPH047506Y2 publication Critical patent/JPH047506Y2/ja
Expired legal-status Critical Current

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  • Manufacturing Of Printed Wiring (AREA)

Description

【考案の詳細な説明】 〔産業上の利用分野〕 本考案はコンベア式焼成炉の改良に関するもの
である。
[Detailed Description of the Invention] [Field of Industrial Application] The present invention relates to an improvement of a conveyor type kiln.

〔従来の技術とその技術的課題〕[Conventional technology and its technical issues]

電子部品搭載用のセラミツク基板やエンジニア
リング用フアインセラミツクス類の仮焼成や本焼
成を行う手段として、コンベア式焼成炉が汎用さ
れている。この焼成工程は、セラミツクの高品質
化の要求から、1000℃を越える高温条件下で非常
にクリーンな状態すなわち、炉内ガス純度が高
く、ゴミ等の微粒子の存在の少ない雰囲気である
こと、精密な温度条件を得るため、被処理物の搬
送が安定して行われることが要求されている。
Conveyor-type firing furnaces are commonly used as means for pre-firing and final firing of ceramic substrates for mounting electronic components and fine ceramics for engineering. This firing process requires high-temperature conditions of over 1000°C to meet the demands for high quality ceramics, and is performed under very clean conditions, i.e., with high purity gas in the furnace and an atmosphere with little dust and other fine particles. In order to obtain suitable temperature conditions, it is required that the objects to be processed be transported stably.

しかしながら、従来のこの種コンベア式焼成炉
は、耐熱金属製の炉芯管に耐熱金属製のメツシユ
ベルトを通し、炉芯管の入口側と出口側部位で雰
囲気ガスを供給し、自然なフローにより前筒と後
筒の開口から流出させる構造であつたため、外気
の侵入やカセスの淀みにより炉内雰囲気を低い酸
素濃度に保つことができず、また、金属同士の摺
動接触により炉内に金属質のゴミが多量に持ち込
まれるという問題があつた。
However, in conventional conveyor-type firing furnaces, a mesh belt made of heat-resistant metal is passed through a furnace core tube made of heat-resistant metal, and atmospheric gas is supplied at the inlet and outlet sides of the furnace core tube, allowing the natural flow to proceed. Because the structure allows the flow to flow through the openings in the cylinder and rear cylinder, the atmosphere inside the furnace cannot be maintained at a low oxygen concentration due to intrusion of outside air and stagnation in the case.Also, sliding contact between metals makes it impossible to maintain a low oxygen concentration inside the furnace. There was a problem with large amounts of trash being brought in.

また、ベルトが直接炉芯管の底を摺動し、その
炉芯管が熱疲労により変形しやすいため、搬送抵
抗が大きいと共に経時的にベルト蛇行が生じやす
くなり、これにより所期の温度曲線を得るための
被処理物の搬送速度が許容範囲から逸脱したり、
被処理物を傷つけたり、煩雑なメンテナンスを必
要とするという不具合があつた。
In addition, since the belt slides directly on the bottom of the furnace core tube, and the furnace core tube is easily deformed due to thermal fatigue, conveyance resistance is large and belt meandering tends to occur over time. If the conveyance speed of the processed material to obtain the
There were problems such as damaging the objects to be processed and requiring complicated maintenance.

本考案は前記のような問題点を解消するために
考案されたもので、その目的とするところは、高
温条件下で良好な雰囲気を形成できると共に異物
やゴミの発生が少なく、かつ被処理物の搬送も安
定かつスムーズに行え、クリーンな条件下での精
密な焼成に適したコンベア式焼成炉を提供するこ
とにある。
The present invention was devised to solve the above-mentioned problems, and its purpose is to be able to form a good atmosphere under high-temperature conditions, to generate less foreign matter and dust, and to reduce the amount of material to be treated. Our objective is to provide a conveyor-type kiln that allows for stable and smooth conveyance and is suitable for precise kiln under clean conditions.

〔課題を解決するための手段〕[Means to solve the problem]

上記目的を達成するため本考案は、炉芯管を内
蔵した炉体の前後に前筒と後筒を連設し、それら
にコンベアベルトを通した形式の焼成炉におい
て、炉芯管内に全長に渡り天井および側面から被
処理物に雰囲気ガスを吹き付ける機構を設ける一
方、炉芯管入口域と出口域には炉内雰囲気を炉外
に排出する吸引管を挿設し、前筒と後筒には端部
の開口と炉芯管開口とのあいだに、雰囲気ガスを
開口側かつ下向きに吹き出す整流用雰囲気吹出し
機構を横設し、炉芯管と前筒及び後筒の内底には
セラミツクチエーンベルトのローラを転接させる
セラミツク系レールを敷設したものである。
In order to achieve the above object, the present invention is a firing furnace in which a front cylinder and a rear cylinder are installed in front and behind a furnace body with a built-in furnace core tube, and a conveyor belt is passed between them. A mechanism is provided to blow atmospheric gas onto the workpiece from the floating ceiling and side surfaces, while suction pipes are inserted in the inlet and outlet areas of the furnace core tube to exhaust the atmosphere inside the furnace to the outside of the furnace. A rectifying atmosphere blowing mechanism is installed horizontally between the end opening and the furnace core tube opening to blow out the atmospheric gas toward the opening and downward, and a ceramic chain is installed at the inner bottom of the furnace core tube, front tube, and rear tube. It is equipped with ceramic rails that make contact with the belt rollers.

〔実施例〕〔Example〕

以下本考案の実施例を添付図面に基いて説明す
る。
Embodiments of the present invention will be described below with reference to the accompanying drawings.

第1図ないし第6図は本考案によるコンベア式
焼成炉の一実施例を示している。1は耐火物で作
られたトンネル状の炉体、2は炉体1を貫く炉芯
管であり、ステンレス等の耐熱金属材料で作られ
ている。3は前筒(入口筒)、4は後筒(出口筒)
であり、それぞれフランジを介して炉芯管2の前
後に連結されている。5は炉体1に内設された発
熱体、6は張り側が前筒3から後筒4にわたるセ
ラミツクチエーンベルトである。
1 to 6 show an embodiment of a conveyor type kiln according to the present invention. Reference numeral 1 denotes a tunnel-shaped furnace body made of a refractory material, and 2 a furnace core tube passing through the furnace body 1, which is made of a heat-resistant metal material such as stainless steel. 3 is the front cylinder (inlet cylinder), 4 is the rear cylinder (outlet cylinder)
and are connected to the front and rear of the furnace core tube 2 via flanges, respectively. Reference numeral 5 designates a heating element installed inside the furnace body 1, and reference numeral 6 designates a ceramic chain belt whose tension side extends from the front cylinder 3 to the rear cylinder 4.

前記炉芯管2は、第3図ないし第5図のよう
に、底部外側がSiCなどの耐火物からなる炉床板
20で支持される一方、底部内側にはムライトな
どの耐火物からなるレール板21が全長にわたり
敷設され、前筒3と後筒4にはレール板21とレ
ベルを同じくして石英などのセラミツク系からな
るレール板22が敷設されている。さらに、炉体
1と前筒3及び後筒4の下方位置にも同じ材質か
らなるレール板23が敷設されている。少なくと
も前記レール材21は第5図のごとく両側の突条
24,24により炉幅方向のズレが止められてい
る。そして、各レール板21,22,23の上部
には長手方向に走る複数条のレール部25が設け
られている。
As shown in FIGS. 3 to 5, the hearth tube 2 is supported by a hearth plate 20 made of a refractory such as SiC on the outside of the bottom, and a rail plate made of a refractory such as mullite on the inside of the bottom. A rail plate 21 is laid over the entire length, and a rail plate 22 made of ceramic such as quartz is laid on the front tube 3 and the rear tube 4 at the same level as the rail plate 21. Further, rail plates 23 made of the same material are installed below the furnace body 1, the front cylinder 3, and the rear cylinder 4. At least the rail material 21 is prevented from shifting in the furnace width direction by the protrusions 24, 24 on both sides, as shown in FIG. A plurality of rail portions 25 running in the longitudinal direction are provided at the top of each rail plate 21, 22, 23.

前記セラミツクチエーンベルト6は複数列から
なつており、それぞれが左右1組をなす複数組の
セラミツクリンク板60,60をセラミツクロー
ラ61のはまつたピン62で連結してなり、セラ
ミツクローラ61はピン62の回りで回転できる
ように構成されている。その前記セラミツクロー
ラ61は張り側が前記レール板21,22の各レ
ール部25により転接自在に支持され、緩み側も
レール板23のレール部25により転接自在に支
持されている。そして、セラミツクチエーンベル
ト6は入口側に設けた従動スプロケツト63に噛
合わされ、出口側は可変速駆動装置64で回転さ
れる駆動スプロケツト65に噛合わされている。
それら両スプロケツト63,65はセラミツクチ
エーンベルト6と非メタルタツチの構造となつて
おり、すなわち全体がセラミツク質で作られる
か、又は耐熱金属質の表面にセラミツク被覆が施
されている。
The ceramic chain belt 6 consists of a plurality of rows, each of which is made up of a plurality of sets of ceramic link plates 60, 60, one on the left and one on the left, connected by a pin 62 of a ceramic roller 61. It is configured to be able to rotate around 62. The ceramic roller 61 is supported on its tight side by the rail portions 25 of the rail plates 21 and 22 so as to be freely in contact with each other, and its loose side is also supported in such a manner as to be freely in contact with the rail portion 25 of the rail plate 23. The ceramic chain belt 6 is meshed with a driven sprocket 63 provided on the inlet side, and meshed with a drive sprocket 65 rotated by a variable speed drive device 64 on the exit side.
Both sprockets 63 and 65 have a non-metallic construction with the ceramic chain belt 6, that is, they are entirely made of ceramic or have a heat-resistant metal surface coated with ceramic.

一方、炉芯管2には全長に渡り雰囲気ガスを被
処理物Wに吹き付ける機構が設けられている。具
体的には、入口側と出口側から炉長方向中央部に
到る天井側雰囲気導入管7,7′がそれぞれ数条
ずつ挿入されると共に、両側壁部分にも入口側と
出口側から炉長方向中央部に到る側面側雰囲気導
入管8,8′,9,9′がそれぞれ数条ずつ挿入さ
れている。
On the other hand, the furnace core tube 2 is provided with a mechanism for spraying atmospheric gas onto the workpiece W over its entire length. Specifically, several ceiling-side atmosphere introduction pipes 7 and 7' are inserted from the inlet and outlet sides to the central part in the furnace length direction. Several side atmosphere introduction pipes 8, 8', 9, and 9' are each inserted to reach the central portion in the longitudinal direction.

それら各雰囲気導入管7,7′,8,8′,9,
9′は、第5図に示すように、Uボルトの金具1
0により一定間隔ごとに炉芯管2に支持されてお
り、各導入管の先端は閉じられ、周面に細かいピ
ツチで噴孔70,80,90が配設されている。
第5図のように、天井側雰囲気導入管7,7′の
噴孔70は斜め下向きに開けられ、側面側雰囲気
導入管8,8′,9,9′の噴孔89は炉芯管中心
に向く方向に開けられている。
Each of these atmosphere introduction pipes 7, 7', 8, 8', 9,
9' is the U-bolt fitting 1, as shown in Figure 5.
0, and are supported by the furnace core tube 2 at regular intervals, the tip of each introduction tube is closed, and nozzle holes 70, 80, and 90 are arranged at fine pitches on the circumferential surface.
As shown in Fig. 5, the nozzle holes 70 of the ceiling-side atmosphere introduction pipes 7, 7' are opened diagonally downward, and the nozzle holes 89 of the side-side atmosphere introduction pipes 8, 8', 9, 9' are at the center of the furnace core tube. It is opened in the direction facing.

そして、炉芯管2の入口側と出口側には、天井
側雰囲気導入管7,7′と平行状に太径の吸引管
11,11′が挿設されており、この吸引管11,
11′は、第3図と第4図のように、先端付近に
吸引口110が設けられ、後端側は炉外の排気ダ
クトに導かれている。必要に応じ、第3図〜第5
図の仮想線で示すように、炉芯管2の入口部と出
口部に、天井域に近く幅方向を横断するごとく吸
引ガイド用雰囲気導管12,12′を設け、これ
に配設した噴孔120から吸引口110の方向に
雰囲気ガスを吹出させてもよい。吸引ガイド用雰
囲気導入管12,12′は炉芯管2に回転可能に
支持され、炉外のハンドルなどの調整手段13に
より吹出し角度が可変となつている。
Large-diameter suction pipes 11, 11' are inserted into the inlet and outlet sides of the furnace core tube 2 in parallel with the ceiling-side atmosphere introduction pipes 7, 7'.
11', as shown in FIGS. 3 and 4, has a suction port 110 near its tip, and its rear end is led to an exhaust duct outside the furnace. Figures 3 to 5 as necessary
As shown by the imaginary lines in the figure, suction guide atmosphere conduits 12 and 12' are provided at the inlet and outlet of the furnace core tube 2 so as to cross the width direction near the ceiling area, and the nozzle holes arranged therein are provided. Atmospheric gas may be blown out from 120 in the direction of suction port 110 . The suction guide atmosphere introducing tubes 12, 12' are rotatably supported by the furnace core tube 2, and the blowing angle is made variable by adjusting means 13 such as a handle outside the furnace.

一方、前筒3は、第2図のように入口に向かう
ほど断面積の縮少したテーパ状に構成され、入口
シヤツタ30の近くにはノレン状の外気流入抵抗
体31が吊設されると共に、これと炉芯管入口と
の間の天井域には、炉幅方向に整流用雰囲気吹出
し管14が横架されている。この整流用雰囲気吹
出し管14には、第3図のごとく吹出し角度を入
口方向斜め下方にとつた噴孔140が所定ピツチ
で配設されている。
On the other hand, the front cylinder 3 has a tapered shape with a cross-sectional area that decreases toward the inlet as shown in FIG. In the ceiling area between this and the furnace core tube inlet, a rectifying atmosphere blow-off tube 14 is horizontally suspended in the furnace width direction. As shown in FIG. 3, nozzle holes 140 are arranged at a predetermined pitch in the rectifying atmosphere blowout pipe 14, and the blowout angle is diagonally downward toward the inlet.

後筒4も同様であり、すなわち第2図のように
出口に向かうほど断面積の縮少するテーパ状に構
成され、出口シヤツタ40の近くには、ノレン状
の外気流入抵抗体41が吊設され、これと炉芯管
との間の天井域に、幅方向を横断するように整流
用雰囲気吹出し管14′が設けられ、これに吹出
し角度を出口方向斜め下向きにとつた噴孔14
0′が所定ピツチで配設されている。そして、後
筒4の外周には空冷機構15が設けられている。
The rear cylinder 4 is similar, that is, it has a tapered shape with a cross-sectional area that decreases toward the outlet as shown in FIG. A rectifying atmosphere blow-off pipe 14' is provided in the ceiling area between this and the furnace core tube so as to cross the width direction.
0' are arranged at a predetermined pitch. An air cooling mechanism 15 is provided on the outer periphery of the rear cylinder 4.

第7図は本考案の別の実施例を前筒で代表して
示しており、前記外気流入抵抗体31と整流用雰
囲気吹出し管14の間の前筒のまわりに均圧ボツ
クス160を備えたガスカーテン機構16を設け
ている。後筒4についても同じ構造を採り得るの
は勿論である。
FIG. 7 shows another embodiment of the present invention using a front cylinder as a representative, and a pressure equalizing box 160 is provided around the front cylinder between the outside air inflow resistor 31 and the rectifying atmosphere blowout pipe 14. A gas curtain mechanism 16 is provided. Of course, the same structure can be adopted for the rear cylinder 4 as well.

第6図は雰囲気供給系を示しており、この例で
はN2ガスを用いている。170はドライN2ガス
の供給源であり、メイン配管171がウエツト装
置172に接続され、その出口側が分岐されてガ
ス加熱器173に挿入され、枝配管174a,1
74bが天井側雰囲気導入管7,7′に、枝配管
174c,174dが入口側の側面用雰囲気導入
管8,9、枝配管174e,174fが出口側の
側面用雰囲気導入管8′,9′にそれぞれ接続さ
れ、加湿ウエツトガスを供給するようになつてい
る。また、メイン配管171はウエツト装置17
2の上流側から分岐配管175が分岐され、枝管
176a,176bにより入口側と出口側の整流
用雰囲気吹出し装置14,14′に接続されるこ
とでドライガスを供給するようになつている。
FIG. 6 shows an atmosphere supply system, in which N2 gas is used in this example. 170 is a dry N 2 gas supply source, a main pipe 171 is connected to a wet device 172, the outlet side thereof is branched and inserted into a gas heater 173, and branch pipes 174a, 1
74b is the ceiling side atmosphere introduction pipe 7, 7', the branch pipes 174c, 174d are the inlet side side atmosphere introduction pipes 8, 9, and the branch pipes 174e, 174f are the outlet side side atmosphere introduction pipes 8', 9'. and are connected to each other to supply humidifying wet gas. In addition, the main pipe 171 is connected to the wet device 17.
A branch pipe 175 is branched from the upstream side of 2, and connected to the rectifying atmosphere blowing devices 14, 14' on the inlet and outlet sides through branch pipes 176a and 176b, thereby supplying dry gas.

〔実施例の作用〕[Effect of the embodiment]

被処理物Wは入口作業台でセラミツクチエーン
ベルト6に乗せられる。セラミツクチエーンベル
ト6は入口側の従動スプロケツト63と出口側の
駆動スプロケツト65が噛合つており、駆動スプ
ロケツト65が駆動回転されることにより所要の
速度で移動する。
The workpiece W is placed on the ceramic chain belt 6 at the entrance workbench. The ceramic chain belt 6 has a driven sprocket 63 on the inlet side and a drive sprocket 65 on the outlet side meshing with each other, and moves at a required speed by driving and rotating the drive sprocket 65.

このときセラミツクチエーンベルト6の構成要
素の各ローラ61が、前筒32と炉芯管2及び後
筒4の底に敷設したセラミツク系レール板21,
22のレール部25に転接し、緩み側についても
炉体下側のレール板23のレール部25に転接す
るため、走行抵抗が少ない。また、リンク板6
0,60の間のローラ61がレール部25にはま
つたかたちで走行し、レール板21,22も突条
24,24によりズレが止められるため、蛇行が
生じない。そのうえ、炉芯管2は1000℃を越える
高温にさらされるが、底部厚さ方向を炉床板20
とレール板21で挟まれているため、熱による変
形や歪みが発生しにくく、通路形態が良好に維持
される。これらにより搬送を非常にスムーズに行
え、精密な加熱温度カーブを得ることができる。
また、コンベアベルトの支持がころがり摩擦であ
ることに加え、ベルトと支持手段がともに耐摩耗
性の良好なセラミツク系材質であるため、搬送に
伴うゴミの発生がきわめて少なく、これによる炉
内汚損や被処理物への付着による品質劣化を防止
できる。
At this time, each roller 61 of the ceramic chain belt 6 is connected to the ceramic rail plate 21 installed at the bottom of the front tube 32, the furnace core tube 2, and the rear tube 4.
Since the loose side also comes into rolling contact with the rail portion 25 of the rail plate 23 on the lower side of the furnace body, there is little running resistance. Also, link board 6
Since the rollers 61 between 0 and 60 run in a tight manner on the rail portion 25, and the rail plates 21 and 22 are also prevented from shifting by the protrusions 24 and 24, meandering does not occur. Moreover, although the hearth tube 2 is exposed to high temperatures exceeding 1000°C, the thickness direction of the bottom part is connected to the hearth plate 20.
Since it is sandwiched between the rail plate 21 and the rail plate 21, deformation or distortion due to heat is difficult to occur, and the shape of the passage is maintained well. These allow for extremely smooth conveyance and a precise heating temperature curve.
In addition to the fact that the conveyor belt is supported by rolling friction, both the belt and the support means are made of a ceramic material with good wear resistance, so there is very little dust generated during conveyance, and there is no risk of contamination in the furnace. It is possible to prevent quality deterioration due to adhesion to objects to be processed.

セラミツクチエーンベルト6の移動により、被
処理物Wは入口シヤツタ30から前筒3に入り、
次いで炉芯管2内を移動する間に雰囲気加熱さ
れ、後筒4を通る間に冷却され、入口シヤツタ4
0を介して出口作業台へと送られる。この間、炉
芯管2においては、全長にわたり天井側雰囲気導
入管7,7′と側面側雰囲気導入管8,8′,9,
9′かの各噴孔70,80,90からウエツトガ
スが吹出され、被処理物Wの上からと左右からき
め細かく吹付けられる。それと同時に入口ゾーン
と出口ゾーンでは天井部に配置されている太径の
吸引管11,11′により吸気が働いており、被
処理物Wに含まれている揮発性成分(バインダ)
等で汚れた雰囲気はここで補集されて炉外へと排
出される。
Due to the movement of the ceramic chain belt 6, the workpiece W enters the front cylinder 3 from the inlet shutter 30,
Next, the atmosphere is heated while moving through the furnace core tube 2, cooled while passing through the rear tube 4, and the inlet shutter 4 is heated.
0 to the exit workbench. During this time, over the entire length of the furnace core tube 2, the ceiling side atmosphere introduction tubes 7, 7', the side side atmosphere introduction tubes 8, 8', 9,
Wet gas is blown out from each of the nozzle holes 70, 80, and 90 at 9', and is finely sprayed from above and from the left and right sides of the object W to be processed. At the same time, in the inlet zone and outlet zone, suction air is working through large-diameter suction pipes 11 and 11' arranged on the ceiling, and volatile components (binder) contained in the processed material W are being sucked in.
The atmosphere polluted by such substances is collected here and discharged to the outside of the furnace.

上記導入管で炉内に導入されたガスは加熱され
ることにより体積を増し、炉芯管2の入口側と出
口側に流れる。しかし、その流れは必ずしも一様
ではなく、全体によどみを生じたり、炉幅方向で
の流れ分布が片寄つたりする。これにより前筒3
や後筒4の開口から外気が侵入し、炉中酸素濃度
を増加させる。しかし本考案では、前筒3と後筒
4の天井域に炉長方向と直角に整流用雰囲気吹出
し管14,14′を設けており、それらに配設し
た多数の噴孔140,140′からドライガスが
開口側でかつ下向きシヤワー状に吹出されてい
る。このため、炉芯管2内からガスの流出が促進
されると同時に炉幅方向で流れが均等となるよう
に整流され、かつ、底側に押し込まれ気味、すな
わち開口断面に正対する状態となつて流れる。し
かも前筒3と後筒4はその幅が開口部に向かうほ
どすぼまつていることからガスの流速が増す。そ
のため、これらの相乗効果により炉内への外気の
侵入が確実に防止され、トンネル炉でありながら
炉内酸素濃度をきわめて低い値に保つことができ
る。
The gas introduced into the furnace through the introduction tube increases in volume by being heated, and flows to the inlet and outlet sides of the furnace core tube 2. However, the flow is not necessarily uniform, and stagnation may occur throughout the furnace, or the flow distribution in the width direction of the furnace may be uneven. This allows the front cylinder 3
Outside air enters through the opening of the rear cylinder 4 and increases the oxygen concentration in the furnace. However, in the present invention, rectifying atmosphere blow-off pipes 14, 14' are provided in the ceiling areas of the front cylinder 3 and rear cylinder 4 at right angles to the furnace length direction, and a large number of nozzle holes 140, 140' arranged in these are provided. Dry gas is blown out from the opening side in a downward shower. Therefore, the outflow of gas from inside the furnace core tube 2 is promoted, and at the same time, the flow is rectified so that it becomes uniform in the width direction of the furnace, and the gas is pushed toward the bottom side, that is, directly facing the opening cross section. It flows. Furthermore, since the widths of the front cylinder 3 and the rear cylinder 4 become narrower toward the opening, the gas flow rate increases. Therefore, these synergistic effects reliably prevent outside air from entering the furnace, and the oxygen concentration inside the furnace can be maintained at an extremely low value even though it is a tunnel furnace.

〔考案の効果〕[Effect of idea]

以上説明した本考案によれば、高温条件下で安
定したスムーズな被処理物搬送を行え、また搬送
に伴うゴミの発生を少なくすることができると共
に、雰囲気ガスの流れが良くなるため、炉内の雰
囲気を高い純度に保つことができ、従つてクリー
ンで精密な焼成工程を実現することができる。さ
らに、炉芯管の変形が少なく、ベルトもころがり
摩擦のためいたみが少ないため耐久性も良好でメ
ンテナンスも容易化することができるなどのすぐ
れた効果が得られる。
According to the present invention explained above, it is possible to carry out stable and smooth transport of the workpiece under high-temperature conditions, reduce the generation of dust during transport, and improve the flow of atmospheric gas inside the furnace. The atmosphere can be maintained at a high level of purity, and a clean and precise firing process can therefore be achieved. Furthermore, the furnace core tube is less deformed and the belt is less likely to be damaged due to rolling friction, resulting in excellent durability and easy maintenance.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本考案によるコンベア式連続焼成炉の
一実施例を示す縦断側面図、第2図同じくその一
部切欠平面図、第3図は第1図の前半部分の拡大
図、第4図は第1図の後半部分の拡大図、第5図
は第1図V−V線に沿う断面図、第6図は本考案
における雰囲気ガスの系統図、第7図は本考案の
別の実施例を示す。 1……炉体、2……炉芯管、3……前筒、4…
…後筒、5……発熱体、6……セラミツクチエー
ンベルト、7,7′……天井側雰囲気導入管、8,
8′,9,9′……側面側雰囲気導入管、11,1
1′……吸引管、14,14′……整流用雰囲気導
入管、20……炉床板、21,22,23……レ
ール板、25……レール部、31,41……外気
流入抵抗体。
Fig. 1 is a vertical sectional side view showing an embodiment of the conveyor type continuous firing furnace according to the present invention, Fig. 2 is a partially cutaway plan view of the same, Fig. 3 is an enlarged view of the first half of Fig. 1, and Fig. 4 is an enlarged view of the latter half of FIG. 1, FIG. 5 is a sectional view taken along line V-V in FIG. 1, FIG. 6 is a system diagram of atmospheric gas in the present invention, and FIG. 7 is another implementation of the present invention Give an example. 1...Furnace body, 2...Furnace core tube, 3...Front cylinder, 4...
... Rear cylinder, 5 ... Heating element, 6 ... Ceramic chain belt, 7, 7' ... Ceiling side atmosphere introduction pipe, 8,
8', 9, 9'...Side side atmosphere introduction pipe, 11, 1
1'... Suction pipe, 14, 14'... Rectifying atmosphere introduction pipe, 20... Hearth plate, 21, 22, 23... Rail plate, 25... Rail part, 31, 41... Outside air inflow resistor .

Claims (1)

【実用新案登録請求の範囲】 (1) 炉芯管を内蔵した炉体の前後に前筒と後筒を
連設し、それらにコンベアベルトを通した形式
の焼成炉において、炉芯管内に全長に渡り天井
および側面から被処理物に雰囲気ガスを吹き付
ける機構を設ける一方、炉芯管入口域と出口域
には炉内雰囲気を炉外に排出する吸引管を挿設
し、前筒と後筒には端部の開口と炉芯管開口と
のあいだに、雰囲気ガスを開口側かつ下向きに
吹き出す整流用雰囲気吹出し機構を横設し、炉
芯管と前筒及び後筒の内底にはセラミツクチエ
ーンベルトのローラを転接させるセラミツク系
レールを敷設したことを特徴とするコンベア式
焼成炉。 (2) 炉芯管内に全長に渡り天井および側面から被
処理物に雰囲気ガスを吹き付ける機構が、多数
の噴孔を有し炉芯管天井部に沿つて配設した雰
囲気導入管と、多数の噴孔を有し炉芯管両側部
に沿つて配設された雰囲気導入管からなつてお
り、整流用雰囲気吹出し機構が、前筒および後
筒の天井域炉幅方向を横に貫く管からなり、そ
の管に多数の噴孔が配設され、かつ前筒および
後筒が開口に向かうほど断面積が減少している
実用新案登録請求の範囲第1項記載のコンベア
式焼成炉。 (3) セラミツク系レールが板からなり、これと炉
床板とで炉芯管の底部がはさまれている実用新
案登録請求の範囲第1項記載のコンベア式焼成
炉。 (4) セラミツクチエーンベルトが出口側の駆動ス
プロケツトにより噛み合い駆動され、緩み側が
セラミツク系レールを転接するようになつてい
る実用新案登録請求の範囲第1項記載のコンベ
ア式焼成炉。 (5) 幅方向に数組のリンク板とそれらの間の可転
ローラを有し、セラミツク系レールの突条で可
転ローラを受けている実用新案登録請求の範囲
第1項記載のコンベア式焼成炉。
[Scope of Claim for Utility Model Registration] (1) In a firing furnace of the type in which a front cylinder and a rear cylinder are connected in front and behind a furnace body with a built-in furnace core tube, and a conveyor belt is passed between them, A mechanism is installed to blow atmospheric gas onto the workpiece from the ceiling and sides, while suction pipes are installed in the inlet and outlet areas of the furnace core tube to exhaust the atmosphere inside the furnace to the outside of the furnace. A rectifying atmosphere blowing mechanism is installed horizontally between the opening at the end and the opening of the furnace core tube to blow out the atmospheric gas toward the opening and downward, and the inner bottoms of the furnace core tube, front cylinder, and rear cylinder are made of ceramic. A conveyor-type kiln characterized by a ceramic rail that connects the rollers of a chain belt. (2) The mechanism that blows atmospheric gas onto the workpiece from the ceiling and sides over the entire length of the furnace core tube consists of an atmosphere introduction tube that has many nozzle holes and is arranged along the ceiling of the furnace core tube, and a large number of It consists of an atmosphere introduction pipe that has nozzle holes and is arranged along both sides of the furnace core tube, and the rectifying atmosphere blowing mechanism consists of a tube that runs horizontally through the ceiling area of the front and rear cylinders in the width direction of the furnace. A conveyor-type kiln according to claim 1, wherein the pipe is provided with a large number of nozzle holes, and the cross-sectional area of the front cylinder and the rear cylinder decreases toward the opening. (3) The conveyor type kiln according to claim 1, wherein the ceramic rail is made of a plate, and the bottom of the hearth tube is sandwiched between the ceramic rail and the hearth plate. (4) The conveyor-type kiln according to claim 1, wherein the ceramic chain belt is meshed and driven by a drive sprocket on the outlet side, and the loose side makes rolling contact with the ceramic rail. (5) The conveyor type according to claim 1 of the utility model registration, which has several sets of link plates in the width direction and a rotatable roller between them, and the rotatable roller is supported by a protrusion of a ceramic rail. Firing furnace.
JP6185489U 1989-05-30 1989-05-30 Expired JPH047506Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6185489U JPH047506Y2 (en) 1989-05-30 1989-05-30

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6185489U JPH047506Y2 (en) 1989-05-30 1989-05-30

Publications (2)

Publication Number Publication Date
JPH033698U JPH033698U (en) 1991-01-16
JPH047506Y2 true JPH047506Y2 (en) 1992-02-27

Family

ID=31590475

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6185489U Expired JPH047506Y2 (en) 1989-05-30 1989-05-30

Country Status (1)

Country Link
JP (1) JPH047506Y2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102017121224A1 (en) 2017-09-13 2019-03-14 Eisenmann Se Apparatus and method for thermal or thermo-chemical treatment of material

Also Published As

Publication number Publication date
JPH033698U (en) 1991-01-16

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