JPS6260445B2 - - Google Patents
Info
- Publication number
- JPS6260445B2 JPS6260445B2 JP54109085A JP10908579A JPS6260445B2 JP S6260445 B2 JPS6260445 B2 JP S6260445B2 JP 54109085 A JP54109085 A JP 54109085A JP 10908579 A JP10908579 A JP 10908579A JP S6260445 B2 JPS6260445 B2 JP S6260445B2
- Authority
- JP
- Japan
- Prior art keywords
- furnace
- gas
- preheating chamber
- combustion
- chamber
- 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
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21D—MODIFYING THE PHYSICAL STRUCTURE OF FERROUS METALS; GENERAL DEVICES FOR HEAT TREATMENT OF FERROUS OR NON-FERROUS METALS OR ALLOYS; MAKING METAL MALLEABLE, e.g. BY DECARBURISATION OR TEMPERING
- C21D1/00—General methods or devices for heat treatment, e.g. annealing, hardening, quenching or tempering
- C21D1/74—Methods of treatment in inert gas, controlled atmosphere, vacuum or pulverulent material
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Crystallography & Structural Chemistry (AREA)
- Mechanical Engineering (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Tunnel Furnaces (AREA)
- Furnace Details (AREA)
Description
【発明の詳細な説明】 本発明は無酸化熱処理炉に関するものである。[Detailed description of the invention] The present invention relates to a non-oxidizing heat treatment furnace.
熱処理たとえばろう付け作業を無酸化性(還元
性)の炉気を用いて行つた場合には、母材および
ろう材の酸化防止効果により品質寸法など諸特性
のすぐれた光輝製品が得られる。このようなこと
から、ろう付けや焼鈍などの熱処理用として無酸
化炉が汎用され、ことに生産性や省力化の面など
から、第1図のようにトンネル炉50とコンベア
ベルト51とを組合せた連続炉が用いられている
が、従来のこの種連続炉ではその操業方法とし
て、炉の外方にこれと別個独立した雰囲気ガス発
生機52を設置し、被処理物を炉中で発熱機構5
3により予熱及び加熱しつつ、前記雰囲気ガス発
生機52の燃焼装置54で原料ガスと空気とを混
合燃焼させて雰囲気ガスを作り、これを炉内に導
入する方法がとられていた。 When heat treatment, such as brazing, is performed using non-oxidizing (reducing) furnace air, a bright product with excellent quality, dimensions and other properties can be obtained due to the oxidation-preventing effect of the base material and brazing material. For this reason, non-oxidizing furnaces are widely used for heat treatments such as brazing and annealing, and in particular, from the viewpoint of productivity and labor saving, a tunnel furnace 50 and a conveyor belt 51 are combined as shown in Fig. 1. A conventional continuous furnace of this type is operated by installing a separate atmospheric gas generator 52 outside the furnace, and moving the workpiece inside the furnace through a heat-generating mechanism. 5
3, the raw material gas and air are mixed and burned in the combustion device 54 of the atmospheric gas generator 52 to create an atmospheric gas, and this is introduced into the furnace.
しかしこのような方法では、雰囲気ガスの生成
と被処理物の加熱とが別個の設備と工程で行わ
れ、とくに原料と空気の高温燃焼で生じた熱が雰
囲気ガス発生機の燃焼室内でいたずらに消費さ
れ、その消費量も炉の処理能力の向上に比例して
増大する傾向にあるため、所期する熱処理の実施
に全体として大量のエネルギーを要するという問
題があり、また、燃焼装置54は燃焼室、散水機
構、熱交換部材、ポンプなどを必須の構成とする
複雑な装置であるため全体的に設備が高価とな
り、かつ容積が大きく雰囲気発生装置に占める割
合が高いため据付面積も広きを要するという不具
合があつたものである。 However, in this method, the generation of atmospheric gas and the heating of the material to be processed are performed in separate equipment and processes, and in particular, the heat generated from the high-temperature combustion of the raw material and air can be wasted in the combustion chamber of the atmospheric gas generator. Since the consumption amount tends to increase in proportion to the improvement in the processing capacity of the furnace, there is a problem that a large amount of energy is required as a whole to carry out the intended heat treatment. Because it is a complex device that requires a chamber, a water sprinkling mechanism, a heat exchange member, a pump, etc., the equipment as a whole is expensive, and it also requires a large installation area because it has a large volume and occupies a high proportion of the atmosphere generation device. There was this problem.
本発明は前記した実情に鑑み研究を重ねて創案
されたもので、雰囲気ガス発生機を別設する要な
く効率よく無酸化熱処理を行うことができる省エ
ネルギー型の連続炉を提供せんとするものであ
る。 The present invention was devised after repeated research in view of the above-mentioned circumstances, and aims to provide an energy-saving continuous furnace that can efficiently perform non-oxidation heat treatment without the need for a separate atmospheric gas generator. be.
この目的のため本発明は連続炉内で直接還元炎
燃焼を起させることでその燃焼熱により被処理物
を予熱し、しかも燃焼排ガスを精製して炉内に導
入することでこれを炉気に利用し効果的な無酸化
熱処理を行うようにしたものである。 For this purpose, the present invention causes direct reducing flame combustion in a continuous furnace to preheat the material to be treated using the combustion heat, and also purifies the combustion exhaust gas and introduces it into the furnace. This method allows effective non-oxidation heat treatment to be carried out.
すなわち本発明は、前後に入口部と出口部を連
設した炉本体に、仕切壁を介して予熱室と加熱室
を形成し、前記予熱室に還元炎形成用のバーナと
燃焼排ガスの吸引排出部を設け、前記吸引排出部
を炉外のガス精製装置を介して出口部に接続した
ことを特徴とするものである。 That is, in the present invention, a preheating chamber and a heating chamber are formed through a partition wall in a furnace main body having an inlet and an outlet connected to each other in the front and rear, and a burner for forming a reducing flame and a suction/discharge of combustion exhaust gas are provided in the preheating chamber. The apparatus is characterized in that the suction and discharge part is connected to the outlet part through a gas purification device outside the furnace.
以下本発明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2図ないし第4図は本発明に係る無酸化熱処
理炉を示すもので、1は耐火物で作られた炉本体
であり、該炉本体1の前側には入口部2が連設さ
れると共に、後側には外周に水冷ボツクス4を囲
繞した出口部3が連設されている。 Figures 2 to 4 show the non-oxidizing heat treatment furnace according to the present invention, in which 1 is a furnace body made of refractory material, and an inlet portion 2 is connected to the front side of the furnace body 1. At the same time, an outlet section 3 surrounding a water-cooled box 4 on the outer periphery is connected to the rear side.
5は被処理物を前記入口部2と炉本体1および
出口部3に順次移動させるための移送機構で、本
実施例ではメツシユベルトのようなコンベアベル
トを用いている。 Reference numeral 5 denotes a transfer mechanism for sequentially moving the material to be treated to the inlet section 2, the furnace main body 1, and the outlet section 3. In this embodiment, a conveyor belt such as a mesh belt is used.
このような構成は従前の加熱炉と同様である
が、本発明は、炉本体1の内側中間部に被処理物
の通過を許す限度で下る仕切壁6を設け、この仕
切壁6により炉内に予熱室7と加熱室8とを区画
形成し、加熱室8には内壁に加熱機構(本実施例
では電気ヒータ)9を配設すると共に、予熱室7
には原料(たとえばプロパンガス)と空気との混
合物で予熱室内に還元炎燃焼を得るためのバーナ
10,10′を挿設している。そして予熱室7の
他所には還元炎燃焼排ガスを強制的に取出すため
の吸引排出部11を設け、一方前記炉本体1の支
持フレーム12には、冷却器14a,14b,1
4cとフイルタ15とドライヤ16a,16bお
よびブロワー17とを配管で直列状に結んだガス
精製装置13を設置し、このガス精製装置13の
冷却器14aに前記吸引排出部11を接続すると
共に、炉本体1の出口部3には精製ガスの挿入部
19を設け、このガス挿入部19とブロワー17
の吐出側とを流量計18を介して接続している。
なおガス精製装置13には、冷凍器やCO2除去装
置を設けてもよいのは勿論である。 Such a configuration is similar to the conventional heating furnace, but in the present invention, a partition wall 6 is provided at the inner middle part of the furnace body 1 and descends to the extent that allows the passage of the material to be processed. A preheating chamber 7 and a heating chamber 8 are divided into a preheating chamber 7 and a heating chamber 8, and a heating mechanism (an electric heater in this embodiment) 9 is disposed on the inner wall of the heating chamber 8.
Burners 10 and 10' are inserted in the preheating chamber to obtain reducing flame combustion with a mixture of raw material (eg, propane gas) and air. A suction/discharge section 11 for forcibly taking out reducing flame combustion exhaust gas is provided elsewhere in the preheating chamber 7, while coolers 14a, 14b, 1
4c, a filter 15, dryers 16a, 16b, and a blower 17 are connected in series with piping. A purified gas insertion part 19 is provided at the outlet part 3 of the main body 1, and the gas insertion part 19 and the blower 17 are connected to each other.
The discharge side of the flowmeter is connected via a flowmeter 18.
Note that the gas purification device 13 may of course be provided with a refrigerator or a CO 2 removal device.
ここで、前記予熱室7は、バーナ10,10′
から噴出される還元炎燃焼熱が室内に均一に行き
渡り被処理物に充分な熱量を与え得るよう、上側
のバーナ10の噴出口下方域に支持部材20を介
して耐熱製の多孔板21を張設し、また下側のバ
ーナ10′の噴出口上方域には被処理物の移送レ
ベルと同じ高さ位置に耐熱製の多孔板22を装着
している。 Here, the preheating chamber 7 includes burners 10 and 10'.
A heat-resistant perforated plate 21 is placed in the area below the spout of the upper burner 10 via a support member 20 so that the combustion heat of the reducing flame emitted from the burner can be uniformly distributed throughout the room and provide a sufficient amount of heat to the object to be treated. In addition, a heat-resistant perforated plate 22 is mounted above the spout of the lower burner 10' at the same height as the transfer level of the object to be treated.
その他図面において23は加熱室8に内設した
炉芯管であるが、これは加熱機構9がガスバーナ
の如きである場合には必要であるが、電気ヒータ
の場合には必ずしも必要としない。 In addition, in the drawings, 23 is a furnace core tube installed inside the heating chamber 8, which is necessary when the heating mechanism 9 is a gas burner, but not necessarily when it is an electric heater.
なお、場合によれば、炉本体1に近い出口部3
の適所に置換用ガスの導入部を設けて始業時に内
部空気を追出すようにしてもよいのは勿論であ
り、さらに仕切壁6にガスカーテン又はシヤツタ
ーを設け、これにより始業時に予熱室7を加熱室
8と独立させ、還元炎形成と排ガスの吸引排出を
促進させるようにしてもよい。 In addition, depending on the case, the outlet part 3 near the furnace main body 1
Of course, it is also possible to provide an inlet for replacement gas at an appropriate location to expel the internal air at the start of work.Furthermore, a gas curtain or shutter may be provided on the partition wall 6, so that the preheating chamber 7 can be expelled at the start of work. It may be made independent of the heating chamber 8 to promote the formation of a reducing flame and the suction and discharge of exhaust gas.
本発明は上記のような構成からなるので、ろう
付け、燃鈍および燃結などの無酸化熱処理を行う
にあたつては、移送機構5を駆動して被処理物を
入口部2から出口部3に向かつて順次移動させる
と共に、加熱機構9およびバーナ10,10′を
作動させ、バーナ10,10′に対し空燃比が原
料過剰の混合物を供給するものであり、こうする
ことにより予熱室内にはバーナ10,10′によ
る還元炎が形成され、還元性の燃焼ガスがバーナ
10,10′から予熱室中に連続噴出するので、
予熱室7を通る被処理物は前記燃焼ガスによつて
直接かつ急速に加熱され昇温する。 Since the present invention has the above-described configuration, when performing non-oxidizing heat treatment such as brazing, annealing, and sintering, the transfer mechanism 5 is driven to transfer the workpiece from the inlet section 2 to the outlet section. At the same time, the heating mechanism 9 and the burners 10, 10' are operated to supply the burner 10, 10' with a mixture with an air-fuel ratio in excess of the raw material. A reducing flame is formed by the burners 10 and 10', and reducing combustion gas is continuously ejected from the burners 10 and 10' into the preheating chamber.
The object to be processed passing through the preheating chamber 7 is directly and rapidly heated by the combustion gas, and its temperature rises.
一方予熱室7にはガス吸引排出部11が設けら
れブロワー17による強制吸引力が働いているの
で、還元炎燃焼排ガスは被処理物に熱量を与えた
後直ちにガス吸引排出部11から炉外に導かれ、
冷却器14a,14b,14cを通る間に水分が
凝縮除去され、続いてフイルタ15により夾雑物
類が除去され、最後にドライヤ16a,16bに
より所定の露点に調整され、こうした過程で高純
度の還元性ガスに変成されて出口部3に供給され
るものである。そして出口部3に供給された還元
性ガスは、加熱室8の熱に引かれたガス流とな
り、出口部3を通る間に被処理物との熱交換でこ
れを冷却すると共にガス自体は適度に昇温し加熱
室8に連続供給される。そのため、被処理物は予
熱室7で還元炎により急速加熱されるのに続き、
加熱室8では予熱排ガスを精製した還元性雰囲気
により所定温度に効率よく加熱され、さらに出口
部3で同雰囲気ガス流による室冷効果と外周の水
冷効果により無酸化条件で効率よく冷却され連続
的に取り出されるものである。 On the other hand, the preheating chamber 7 is provided with a gas suction/discharge section 11 and a forced suction force is applied by the blower 17, so that the reducing flame combustion exhaust gas is immediately discharged from the gas suction/discharge section 11 to the outside of the furnace after imparting heat to the object to be treated. guided by,
Moisture is condensed and removed while passing through coolers 14a, 14b, 14c, impurities are removed by filter 15, and finally the dew point is adjusted to a predetermined dew point by dryers 16a, 16b. In this process, high purity reduction is achieved. It is converted into a sexual gas and supplied to the outlet section 3. The reducing gas supplied to the outlet section 3 becomes a gas flow attracted by the heat of the heating chamber 8, and while passing through the outlet section 3, it is cooled by heat exchange with the object to be treated, and the gas itself is moderately The temperature is raised to , and the heat is continuously supplied to the heating chamber 8 . Therefore, the object to be treated is rapidly heated by the reducing flame in the preheating chamber 7, and then
In the heating chamber 8, the preheated exhaust gas is efficiently heated to a predetermined temperature by a purified reducing atmosphere, and furthermore, at the outlet section 3, it is efficiently cooled under non-oxidizing conditions by the room cooling effect due to the gas flow in the same atmosphere and the water cooling effect on the outer periphery, and is continuously cooled. It is something that is taken out.
以上説明した本発明によるときには、前後に入
口部2と出口部3を連設した炉本体1に仕切壁6
を介して予熱室7と加熱室8を形成し、前記予熱
室7に還元炎形成用のバーナ10,10′と燃焼
排ガスの吸引排出部11を設け、前記吸引排出部
11を炉外のガス精製装置13を介して出口部3
に接続したので次のようなすぐれた効果が得られ
る。 According to the present invention explained above, the partition wall 6
A preheating chamber 7 and a heating chamber 8 are formed through the preheating chamber 7, and the preheating chamber 7 is provided with burners 10, 10' for forming a reducing flame and a combustion exhaust gas suction and discharge section 11, and the suction and discharge section 11 is connected to the gas outside the furnace. Outlet section 3 via purifier 13
By connecting it to , you can get the following excellent effects.
炉本体内で原料と空気との混合物を直接還元
炎燃焼させ、その燃焼熱エネルギーを利用して
被処理物を急速加熱し、予熱後の排ガスを精製
して無酸化性の炉気に用いるので、エネルギー
の無駄がなく、加熱室における加熱機構の電力
等を節減できることや、加熱後の冷却効果を向
上できることと相まち総合的に大幅な省エネル
ギー化を達成することができる。 The mixture of raw materials and air is directly combusted with a reducing flame in the furnace body, and the combustion heat energy is used to rapidly heat the material to be processed. After preheating, the exhaust gas is purified and used as non-oxidizing furnace air. There is no wastage of energy, the electric power of the heating mechanism in the heating chamber can be saved, and the cooling effect after heating can be improved, so that it is possible to achieve overall significant energy savings.
雰囲気発生装置の枢要をなしボリユームも大
きい燃焼装置が不要になり、残余の構成物も炉
本体の支持フレーム中に納めることができるの
で、この種無酸化熱処理炉としてコンパクトで
据付面積の小さい設備とすることができる。 This eliminates the need for a large-volume combustion device, which is a key part of the atmosphere generation device, and the remaining components can be housed in the support frame of the furnace body, making this type of non-oxidation heat treatment furnace compact and requiring only a small installation area. can do.
構成が複雑で高価な燃焼装置が不要になり、
また炉長の短縮と加熱機構の減少を図ることが
できるので設備費および運転費を安価なものに
することができる。 Eliminates the need for complex and expensive combustion equipment,
Further, since the length of the furnace can be shortened and the number of heating mechanisms can be reduced, equipment costs and operating costs can be reduced.
第1図は従来の無酸化熱処理炉を示す説明図、
第2図は本発明に係る無酸化熱処理炉の一実施例
を示す縦断側面図、第3図は第1図−線にそ
う断面図、第4図は第1図−線にそう断面図
である。
1……炉本体、2……入口部、3……出口部、
6……仕切壁、7……予熱室、8……加熱室、1
1……吸引排出部、13……ガス精製装置、19
……精製ガスのガス挿入部。
Figure 1 is an explanatory diagram showing a conventional non-oxidation heat treatment furnace;
FIG. 2 is a longitudinal sectional side view showing an embodiment of the non-oxidation heat treatment furnace according to the present invention, FIG. 3 is a sectional view along the line shown in FIG. 1, and FIG. 4 is a sectional view taken along the line shown in FIG. 1. be. 1...Furnace body, 2...Inlet part, 3...Outlet part,
6... Partition wall, 7... Preheating chamber, 8... Heating chamber, 1
1... Suction discharge unit, 13... Gas purification device, 19
...Gas insertion part for purified gas.
Claims (1)
1に仕切壁6を介して予熱室7と加熱室8を形成
し、前記予熱室7に還元炎形成用のバーナ10,
10′と燃焼排ガスの吸引排出部11を設け、前
記吸引排出部11を炉外のガス精製装置13を介
して出口部3に接続したことを特徴とする無酸化
熱処理炉。1. A preheating chamber 7 and a heating chamber 8 are formed through a partition wall 6 in the furnace body 1, which has an inlet section 2 and an outlet section 3 connected in the front and rear, and a burner 10 for forming a reducing flame in the preheating chamber 7,
10' and a combustion exhaust gas suction/discharge section 11, the suction/discharge section 11 being connected to an outlet section 3 via a gas purification device 13 outside the furnace.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10908579A JPS5635715A (en) | 1979-08-29 | 1979-08-29 | Nonoxidizing heat treatment furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10908579A JPS5635715A (en) | 1979-08-29 | 1979-08-29 | Nonoxidizing heat treatment furnace |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5635715A JPS5635715A (en) | 1981-04-08 |
| JPS6260445B2 true JPS6260445B2 (en) | 1987-12-16 |
Family
ID=14501211
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP10908579A Granted JPS5635715A (en) | 1979-08-29 | 1979-08-29 | Nonoxidizing heat treatment furnace |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5635715A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS58212862A (en) * | 1982-06-04 | 1983-12-10 | Honda Motor Co Ltd | Continuous furnace brazing method |
| JPH0726147B2 (en) * | 1986-03-19 | 1995-03-22 | 大同特殊鋼株式会社 | Circulation method of atmospheric gas in heat treatment |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS51115211A (en) * | 1975-04-02 | 1976-10-09 | Daido Steel Co Ltd | Continuous heat treatment equipment |
-
1979
- 1979-08-29 JP JP10908579A patent/JPS5635715A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5635715A (en) | 1981-04-08 |
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