JPS6242708B2 - - Google Patents
Info
- Publication number
- JPS6242708B2 JPS6242708B2 JP57095807A JP9580782A JPS6242708B2 JP S6242708 B2 JPS6242708 B2 JP S6242708B2 JP 57095807 A JP57095807 A JP 57095807A JP 9580782 A JP9580782 A JP 9580782A JP S6242708 B2 JPS6242708 B2 JP S6242708B2
- Authority
- JP
- Japan
- Prior art keywords
- furnace
- gas
- brazing
- section
- cooling
- 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
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B23—MACHINE TOOLS; METAL-WORKING NOT OTHERWISE PROVIDED FOR
- B23K—SOLDERING OR UNSOLDERING; WELDING; CLADDING OR PLATING BY SOLDERING OR WELDING; CUTTING BY APPLYING HEAT LOCALLY, e.g. FLAME CUTTING; WORKING BY LASER BEAM
- B23K1/00—Soldering, e.g. brazing, or unsoldering
- B23K1/008—Soldering within a furnace
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Tunnel Furnaces (AREA)
Description
【発明の詳細な説明】
本発明はベルトコンベアによつてワークを搬送
しつつ加熱し、ロー付を行ない、更には冷却する
ようにした連続式の炉中ロー付方法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a continuous furnace brazing method in which a workpiece is conveyed by a belt conveyor, heated, brazed, and further cooled.
一般に連続式の炉中ロー付炉にあつては、プロ
パン、ブタン等の変成ガス或いはアンモニア分解
ガスなどを雰囲気ガスとして炉内に導入し、炉内
を無酸化雰囲気としてロー付処理を行なうように
している。 Generally, in a continuous type brazing furnace, a modified gas such as propane or butane or decomposed ammonia gas is introduced into the furnace as an atmospheric gas to create a non-oxidizing atmosphere in the furnace for brazing. ing.
また、変成炉によつて製造した雰囲気ガスは、
水分を除去するため、一旦冷凍機において10℃以
下に冷却した後、炉の加熱部に直接投入するよう
にしている。したがつて、低温の雰囲気ガスは加
熱炉において、例えば銅ロー付炉にあつては1100
℃以上に昇温せしめられることとなる。そして斯
る温度まで低温の雰囲気ガスを昇温せしめるには
雰囲気ガス1m3あたり300kcal以上のエネルギー
を必要とする。したがつて一般に100m3/hr程度
の雰囲気ガスが加熱部内に供給されるので毎時
30000kcalのエネルギーが雰囲気ガスを昇温させ
るために消費されることとなり、ロー付に直接関
与しないエネルギーが多量に使用されている。 In addition, the atmospheric gas produced by the conversion furnace is
In order to remove moisture, the material is first cooled to below 10 degrees Celsius in a refrigerator and then placed directly into the heating section of the furnace. Therefore, low-temperature atmospheric gas is used in a heating furnace, for example in a copper brazing furnace, at a temperature of 1100
The temperature will be raised above ℃. In order to raise the temperature of the low-temperature atmospheric gas to such a temperature, more than 300 kcal of energy is required per 1 m 3 of the atmospheric gas. Therefore, generally about 100m 3 /hr of atmospheric gas is supplied into the heating section, so
30,000 kcal of energy is consumed to raise the temperature of the atmospheric gas, and a large amount of energy that is not directly involved in brazing is used.
更に、雰囲気ガスはH2或いはCO等の可燃成分
を含んでおり、ロー付炉を通過してワークの還元
に寄与した変成ガスは炉から燃焼して放出するよ
うにしているが、例えば雰囲気ガスをプロパン変
成ガスとした場合、毎時100m3放出するとすれば
毎時60000kcalのエネルギーが有効利用されずに
放出されることとなる。 Furthermore, the atmospheric gas contains combustible components such as H 2 or CO, and the metamorphosed gas that has passed through the brazing furnace and contributed to the reduction of the workpiece is burned and released from the furnace. If 100 m 3 of gas is released per hour, 60,000 kcal of energy will be released without being used effectively.
本発明は上記の如き従来の炉中ロー付炉におけ
るエネルギーの無駄な使用を極力排除し、エネル
ギーの有効利用を図り得る連続式炉中ロー付炉を
提供することを目的とし、この目的を達成すべく
本発明は、連続式炉中ロー付炉のワーク搬入口又
は搬出口の少くとも一方の炉外近傍に雰囲気ガス
の吸引部を設け、この吸引部につながる排気ダク
ト内に、炉の加熱部内に雰囲気ガスを供給する供
給パイプを配設したことをその要旨としている。 The purpose of the present invention is to provide a continuous type brazing furnace that can effectively utilize energy by eliminating as much as possible the wasteful use of energy in the conventional brazing furnace, and has achieved this object. In order to achieve this, the present invention provides a suction section for atmospheric gas near the outside of at least one of the workpiece inlet or outlet of a continuous brazing furnace, and provides a suction section for the atmospheric gas in the exhaust duct connected to this suction section. The gist of this is that a supply pipe was installed to supply atmospheric gas into the unit.
以下に本発明の実施の一例を添付図面に基いて
詳述する。 An example of the implementation of the present invention will be explained in detail below based on the accompanying drawings.
第1図は本発明方法を実施するための連続式炉
中ロー付炉の側断面図、第2図は同ロー付炉の冷
却部の平面図であり、連続式炉中ロー付炉1はそ
の上流側の端部に前部テーブル2を配置し、この
前部テーブル2上にワークの搬入口3を形成して
いる。そして前部テーブル2に連続して予熱部4
を設け、この予熱部4内にワークの温度をある程
度上昇するためのヒータ5a……を配設してい
る。そして予熱部4に連続して加熱部6を配し、
この加熱部6内にもワークをロー付処理温度例え
ば銅ロー付する場合には1100℃以上に昇温せしめ
るためのヒータ5b……を配設している。また、
この加熱部6の下流には徐冷部7、更にこの徐冷
部7の下流には冷却部8を配している。 Fig. 1 is a side sectional view of a continuous brazing furnace for carrying out the method of the present invention, and Fig. 2 is a plan view of the cooling section of the brazing furnace. A front table 2 is arranged at the upstream end, and a work entry port 3 is formed on the front table 2. Then, the preheating section 4 is connected to the front table 2.
The preheating section 4 is provided with heaters 5a for raising the temperature of the workpiece to a certain extent. Then, a heating section 6 is arranged continuously to the preheating section 4,
Heaters 5b for raising the temperature of the workpiece to a brazing treatment temperature, for example, 1100° C. or higher in the case of copper brazing, are also provided within the heating section 6. Also,
A slow cooling section 7 is disposed downstream of the heating section 6, and a cooling section 8 is further downstream of the slow cooling section 7.
上記徐冷部7及び冷却部8を構成する壁部には
ウオータジヤケツト9が形成され、また冷却部8
の天井にはワークの搬送方向に沿つて4個の冷却
フアン10a,10b,10c,10dを取り付
けている。これら冷却フアン10a,10b,1
0c,10dは第2図に示す如く冷却部8の外側
壁に固定したモータ11a,11bによつて回転
せしめられ、特に冷却フアン10a,10cはモ
ータ11aによつて、また冷却フアン10b,1
0dはモータ11bによつて回転せしめられ、
夫々のモータ11a,11bの回転方向は逆にな
つているので冷却フアン10a,10b,10
c,10dも夫々交互に回転方向が逆になり、冷
却部8内の雰囲気ガスが冷却部8内で旋回して循
環し、冷却効果を高めるとともに加熱部6内の雰
囲気ガスを乱さず、且つ外気の引き込みもないよ
うにしている。尚、各冷却フアン10a,10
b,10c,10dの回転方向を同一にし、冷却
フアン10a,10cと冷却フアン10b,10
dの羽根の向きを逆にしても上記同様の旋回流を
得ることができる。 A water jacket 9 is formed on the walls constituting the slow cooling section 7 and the cooling section 8.
Four cooling fans 10a, 10b, 10c, and 10d are installed on the ceiling of the workpiece along the transport direction of the workpiece. These cooling fans 10a, 10b, 1
0c and 10d are rotated by motors 11a and 11b fixed to the outer wall of the cooling section 8 as shown in FIG.
0d is rotated by the motor 11b,
Since the rotation directions of the respective motors 11a, 11b are reversed, the cooling fans 10a, 10b, 10
The rotation directions of c and 10d are alternately reversed, so that the atmospheric gas in the cooling part 8 swirls and circulates in the cooling part 8, increasing the cooling effect and not disturbing the atmospheric gas in the heating part 6. It also prevents outside air from being drawn in. In addition, each cooling fan 10a, 10
The rotation directions of cooling fans 10a, 10c and cooling fans 10b, 10 are made the same.
Even if the direction of the blade d is reversed, the same swirling flow as described above can be obtained.
また、冷却部8に連続して後部テーブル12を
配置し、この後部テーブル12上にワークの搬出
口13を形成している。 Further, a rear table 12 is arranged continuously to the cooling section 8, and a workpiece export port 13 is formed on the rear table 12.
また、炉1のワーク搬入口3及び搬出口13の
外側には夫々ローラ14,15を設け、このロー
ラ14,15間にメツシユベルト16を架設し、
このメツシユベルト16上にワークを載置し、メ
ツシユベルト16の移動によつてワークを予熱部
4、加熱部6、徐冷部7及び冷却部8に順次送り
込むようにしている。 Further, rollers 14 and 15 are provided outside the workpiece inlet 3 and outlet 13 of the furnace 1, respectively, and a mesh belt 16 is installed between the rollers 14 and 15.
A workpiece is placed on the mesh belt 16, and as the mesh belt 16 moves, the workpiece is sequentially sent to the preheating section 4, the heating section 6, the slow cooling section 7, and the cooling section 8.
更に上記ワーク搬入口3及び搬出口13の炉外
近傍には吸引部17,18を設け、この吸引部1
7,18に排気ダクト19,20を接続し、これ
ら排気ダクト19,20を途中で合流して一本の
排気ダクト21とし、搬入口3及び搬出口13か
ら流出する高温の雰囲気ガスを吸引排出するよう
にしている。この吸引された雰囲気ガスはH2、
CO等の可燃性成分を含んでいるため、吸引部に
おいて外気と接触した際に燃焼する。 Furthermore, suction parts 17 and 18 are provided near the outside of the furnace at the workpiece loading port 3 and the unloading port 13, and the suction parts 1
Exhaust ducts 19 and 20 are connected to 7 and 18, and these exhaust ducts 19 and 20 are merged in the middle to form one exhaust duct 21, and the high temperature atmospheric gas flowing out from the carry-in port 3 and the carry-out port 13 is sucked and discharged. I try to do that. This sucked atmospheric gas is H2 ,
Since it contains flammable components such as CO, it will burn when it comes into contact with outside air at the suction part.
一方炉1の近傍には変成ガス発生装置22が設
置され、この変成ガス発生装置22で発生した変
成ガスを装置22に付設した冷却装置23に導入
し、10℃以下に冷却して水分を除去し、これを炉
1内に雰囲気ガスとして供給するようにしてい
る。即ち、冷却装置23から雰囲気ガス供給パイ
プ24を導出し、この供給パイプ24を途中で枝
分かれせしめ、一方のパイプ25はそのまま冷却
部8の近くまで延ばし、ここで4本に分枝せし
め、夫々のパイプ25a……を冷却フアン10
a,10b,10c,10dの軸の近くに穿設し
た導入孔26……に挿入し、低温の雰囲気ガスを
冷却部8内に供給するようにしている。また他方
のパイプ27は前記合流した排気ダクト21内を
通して予熱部4加熱部6の近くまで延ばして2分
のパイプ28,29に分枝し、一方のパイプ28
を予熱部4の天井に穿設した導入孔30に挿入
し、他方のパイプ29を加熱部6の天井に穿設し
た導入孔31に挿入している。 On the other hand, a metamorphic gas generator 22 is installed near the furnace 1, and the metamorphic gas generated by the metamorphic gas generator 22 is introduced into a cooling device 23 attached to the device 22, where it is cooled to below 10°C and moisture is removed. This is then supplied into the furnace 1 as an atmospheric gas. That is, an atmospheric gas supply pipe 24 is led out from the cooling device 23, and this supply pipe 24 is branched in the middle, and one pipe 25 is extended as it is to the vicinity of the cooling section 8, where it is branched into four pipes. The pipe 25a... is connected to the cooling fan 10
They are inserted into introduction holes 26 . The other pipe 27 passes through the merged exhaust duct 21 and extends to near the preheating section 4 heating section 6, and branches into two pipes 28 and 29.
is inserted into an introduction hole 30 formed in the ceiling of the preheating section 4, and the other pipe 29 is inserted into an introduction hole 31 formed in the ceiling of the heating section 6.
而して、加熱部6或いは予熱部4に供給される
雰囲気ガスは排気ダクト21内において約500℃
にまで加熱された後、予熱部4、加熱部6内に供
給される。もちろん、排気ダクト19,20内に
パイプ27を配設してもよい。 Therefore, the atmospheric gas supplied to the heating section 6 or the preheating section 4 has a temperature of about 500°C in the exhaust duct 21.
After being heated to , it is supplied into the preheating section 4 and the heating section 6. Of course, the pipe 27 may be provided within the exhaust ducts 19 and 20.
したがつて、例えば加熱部6の温度が1100℃で
あるとすると、従来は1000℃以上雰囲気ガスを昇
温せしめなければならなかつたが、600℃程度昇
温せしめるだけで済み、毎時100m3のプロパン変
成ガスを雰囲気ガスとして供給するとすれば、約
15000kcalのエネルギーが節約できることとな
る。 Therefore, if the temperature of the heating section 6 is 1100°C, for example, whereas conventionally it was necessary to raise the temperature of the atmospheric gas by 1000°C or more, it is only necessary to raise the temperature by about 600°C, and the temperature of 100m3 /hour is increased. If propane converted gas is supplied as atmospheric gas, approximately
This means that 15,000 kcal of energy can be saved.
以上の説明で明らかな如く本発明によれば、連
続式の炉中ロー付炉において、ワークの搬入口或
いは搬出口の少くとも一方の炉外近傍に吸引部を
設け、炉内に供給された変成ガスを炉外に吸引
し、変成ガスと外気とを接触せしめ、変成ガス中
の可燃成分を燃焼せしめて高温にし、この吸引部
につながる排気ダクト内に、加熱炉内に雰囲気ガ
スを供給するための供給パイプを配設したので、
従来、そのまま放出していた使用済みの雰囲気ガ
スの熱を利用して、供給途中の低温の雰囲気ガス
を昇温せしめることとなり、エネルギーの有効利
用が図れ、コストダウンにもつながる等多大の効
果を発揮する。 As is clear from the above description, according to the present invention, in a continuous type brazing furnace, a suction section is provided near the outside of the furnace at least on one of the workpiece inlet and outlet, and the workpiece is supplied into the furnace. The metamorphic gas is sucked outside the furnace, the metamorphic gas is brought into contact with the outside air, the combustible components in the metamorphic gas are combusted to a high temperature, and atmospheric gas is supplied into the heating furnace into the exhaust duct connected to this suction section. Since we have installed a supply pipe for
Conventionally, the heat of the used atmospheric gas, which was released as is, is used to raise the temperature of the low-temperature atmospheric gas that is being supplied, which allows for effective use of energy and has many benefits, including cost reduction. Demonstrate.
図面は本発明の実施の一例を示すものであり、
第1図は本発明に係る連続式炉中ロー付炉の側断
面図、第2図は同炉中ロー付炉の冷却部の平面図
である。
尚、図面中1は連続式炉中ロー付炉、3はワー
クの搬入口、6は加熱部、13はワークの搬出
口、17,18は雰囲気ガスの吸引部、19,2
0,21は排気ダクト、22は変成ガス発生装
置、23は冷却装置、27は供給パイプである。
The drawings show an example of the implementation of the present invention,
FIG. 1 is a side sectional view of a continuous brazing furnace according to the present invention, and FIG. 2 is a plan view of a cooling section of the brazing furnace. In the drawing, 1 is a continuous brazing furnace, 3 is a workpiece loading port, 6 is a heating section, 13 is a workpiece loading port, 17 and 18 are atmospheric gas suction sections, 19 and 2
0 and 21 are exhaust ducts, 22 is a modified gas generator, 23 is a cooling device, and 27 is a supply pipe.
Claims (1)
装置に通して水分を除去した後に炉内に導入する
ようにした連続式炉中ロー付方法において、前記
冷却装置から導出した変成ガスの一部をロー付炉
の加熱部に、残部をロー付炉の冷却部に導入する
ようにし、またロー付炉から排出される変成ガス
を外気と接触せしめて燃焼させ、この燃焼によつ
て高温となつた排気ガスと前記冷却装置からロー
付炉の加熱部に向う変成ガスとを熱交換させて変
成ガスを昇温せしめ、更に前記冷却装置からロー
付炉の冷却部へ向う変成ガスについてはそのまま
の温度で導入するようにしたことを特徴とする連
続式炉中ロー付方法。1. In a continuous furnace brazing method in which the modified gas generated in the modified gas generator is passed through a cooling device to remove moisture and then introduced into the furnace, a part of the modified gas drawn out from the cooling device is The remaining part was introduced into the heating part of the brazing furnace and the remaining part was introduced into the cooling part of the brazing furnace, and the metamorphosed gas discharged from the brazing furnace was brought into contact with the outside air and combusted, and the combustion became high temperature. Heat exchange is performed between the exhaust gas and the transformed gas flowing from the cooling device to the heating section of the brazing furnace to raise the temperature of the transformed gas, and the temperature of the transformed gas flowing from the cooling device to the cooling section of the brazing furnace remains unchanged. A continuous furnace brazing method characterized in that it is introduced in.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9580782A JPS58212862A (en) | 1982-06-04 | 1982-06-04 | Continuous furnace brazing method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9580782A JPS58212862A (en) | 1982-06-04 | 1982-06-04 | Continuous furnace brazing method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS58212862A JPS58212862A (en) | 1983-12-10 |
| JPS6242708B2 true JPS6242708B2 (en) | 1987-09-09 |
Family
ID=14147692
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP9580782A Granted JPS58212862A (en) | 1982-06-04 | 1982-06-04 | Continuous furnace brazing method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS58212862A (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS62252671A (en) * | 1986-04-25 | 1987-11-04 | Hitachi Techno Eng Co Ltd | Vapor reflow soldering equipment |
| JPS62252670A (en) * | 1986-04-25 | 1987-11-04 | Hitachi Techno Eng Co Ltd | Vapor reflow soldering equipment |
| JPH01181965A (en) * | 1988-01-13 | 1989-07-19 | Matsushita Electric Ind Co Ltd | Substrate heating device |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5178719A (en) * | 1974-12-30 | 1976-07-08 | Kawasaki Heavy Ind Ltd | KANETSUSOCHI |
| JPS5746554Y2 (en) * | 1979-01-11 | 1982-10-13 | ||
| JPS5635715A (en) * | 1979-08-29 | 1981-04-08 | Yamazaki Denki Kogyo Kk | Nonoxidizing heat treatment furnace |
-
1982
- 1982-06-04 JP JP9580782A patent/JPS58212862A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS58212862A (en) | 1983-12-10 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN214172902U (en) | High-efficiency energy-saving tunnel kiln | |
| JPH10185139A (en) | Method and apparatus for generating and utilizing gas from waste material | |
| RU2131934C1 (en) | Installation for heat treatment of materials | |
| JPS59225277A (en) | Hot-air purifying circulating device for treating cloth | |
| JP2007247922A (en) | Exhaust gas treatment system | |
| JPS6242708B2 (en) | ||
| CN107081497A (en) | Production line without glue aluminum cellular board | |
| GB1068059A (en) | A method and apparatus for stabilizing strip work | |
| JPS6219265B2 (en) | ||
| JPS6320885B2 (en) | ||
| CN222514238U (en) | Firing furnace | |
| GB958731A (en) | Means for supplying heated air to blast furnaces | |
| CN210624543U (en) | Organic waste gas incineration treatment device for automobile coating and drying | |
| JP3877878B2 (en) | Heat treatment furnace | |
| JP3839910B2 (en) | Copper product heat treatment equipment | |
| CN110423881B (en) | A long-range roller hearth type solution annealing furnace | |
| JPS57143444A (en) | Continuous heat treating furnace having convection type preheating zone | |
| CN121163193A (en) | Air inlet pipe, heat exchange pipeline and paint drying device | |
| JPS6347770B2 (en) | ||
| RU2032851C1 (en) | Method of joint operation of power-generating boiler and drying unit | |
| JPS62112982A (en) | Fiber calciner | |
| JPS6141360A (en) | Heat treatment apparatus for dyeing | |
| JPS5841433B2 (en) | Yakitsuke Kansourosouchi | |
| SU1615109A1 (en) | System for feeding heat-transfer agent to garage for defreezing loose materials in railway gondola cars | |
| CN118670143A (en) | Application of flue gas of annealing furnace in surface drying furnace |