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JPS6018728B2 - Non-oxidizing atmosphere annealing furnace - Google Patents
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JPS6018728B2 - Non-oxidizing atmosphere annealing furnace - Google Patents

Non-oxidizing atmosphere annealing furnace

Info

Publication number
JPS6018728B2
JPS6018728B2 JP327478A JP327478A JPS6018728B2 JP S6018728 B2 JPS6018728 B2 JP S6018728B2 JP 327478 A JP327478 A JP 327478A JP 327478 A JP327478 A JP 327478A JP S6018728 B2 JPS6018728 B2 JP S6018728B2
Authority
JP
Japan
Prior art keywords
furnace
gas
inner cover
air
oxidizing 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
JP327478A
Other languages
Japanese (ja)
Other versions
JPS5496408A (en
Inventor
武一 関谷
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
JFE Steel Corp
Original Assignee
Kawasaki Steel Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Kawasaki Steel Corp filed Critical Kawasaki Steel Corp
Priority to JP327478A priority Critical patent/JPS6018728B2/en
Publication of JPS5496408A publication Critical patent/JPS5496408A/en
Publication of JPS6018728B2 publication Critical patent/JPS6018728B2/en
Expired legal-status Critical Current

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  • Heat Treatment Of Strip Materials And Filament Materials (AREA)

Description

【発明の詳細な説明】 本発明は無酸化雰囲気暁鈍炉に関するものである。[Detailed description of the invention] The present invention relates to a non-oxidizing atmosphere cold furnace.

連続炉およびバッチ炉で焼鈍を行うに際しては、比を含
む雰囲気ガスを用いることが多く、通常は被焼鈍物を炉
のインナーカバー内へ装入し、次いで、インナーカバー
内へ比を含む雰囲気ガスを供給し、さらにインナーカバ
ーをその外側から電熱ヒータまたはラジアントチュープ
で加熱することにより無酸化暁鎚を行う。
When annealing is performed in a continuous furnace or a batch furnace, an atmospheric gas containing a ratio is often used. Usually, the object to be annealed is charged into the inner cover of the furnace, and then an atmospheric gas containing a ratio is introduced into the inner cover. The inner cover is further heated from the outside with an electric heater or a radiant tube to perform oxidation-free oxidation.

この場合、雰囲気ガスの多くは燐錨作業中にインナーカ
バーのシール部から炉内へ洩出するため、インナーカバ
ー外の炉内雰囲気はインナーカバー内の雰囲気とほぼ同
一のガス組成となり、この結果、爆発の危険性が生ずる
ことはもちろん、炉壁の断熱性が低下し、さらに、炉の
構造が複雑になるなどの問題生じる。
In this case, most of the atmospheric gas leaks into the furnace from the seal part of the inner cover during phosphorus anchoring work, so the atmosphere inside the furnace outside the inner cover has almost the same gas composition as the atmosphere inside the inner cover. This not only poses the risk of explosion, but also causes other problems such as a reduction in the heat insulation of the furnace wall and a complicated furnace structure.

たとえば、第1図に示す従来のバッチ式燐鈍炉は、炉底
壁1上にインナーカバー2を載層し、このインナーカバ
ー2の下端部をサンドシールまたはセラミックファイバ
ーシール3によって炉底壁上にシールし、さらにインナ
ーカバー2の外側に、電熱ヒータ4を有し、かつ炉の側
壁および頂壁を形成する炉横5を被せることにより構成
されており、そしてここでの暁鈍は、まず被焼鈍物6を
インナーカバー2内に配置し、次いで、比ガス供聯合管
7によってインナーカバー内の空気8内へ日2ガスを含
む雰囲気ガスを供給し、さらに、ヒータ4を作動させる
ことにより行い、この暁鈍中に、雰囲気ガスはシール3
を経てインナーカバー外の空間9へ流出し、その後排出
筒10から大気中へ排出される。
For example, in the conventional batch type phosphor annealing furnace shown in FIG. It is constructed by sealing the inner cover 2, and then covering the outside of the inner cover 2 with a furnace side 5 having an electric heater 4 and forming the side wall and top wall of the furnace. By arranging the object 6 to be annealed in the inner cover 2, then supplying an atmospheric gas containing 2 gas into the air 8 in the inner cover through the specific gas supply pipe 7, and further activating the heater 4. During this dawn, the atmospheric gas is sealed 3
It flows out into the space 9 outside the inner cover through the air, and is then discharged into the atmosphere from the exhaust pipe 10.

このため、空間8,9内の雰囲気ガスの組成はほぼ等し
くなり、たとえば、耐火断熱レンガあるいはセラミック
ファイバーなどの炉構内張りの断熱性が著しく低下する
こととなる。
For this reason, the compositions of the atmospheric gases in the spaces 8 and 9 become approximately equal, and the insulation properties of the furnace lining, such as fireproof insulation bricks or ceramic fibers, are therefore significantly reduced.

すなわち、4ガスの熱伝導率と空気もしくは燃焼ガスの
熱伝導率との差異に起因して炉壁の熱的性質は第1表に
表わされるようになり、第1表 比雰囲気中での熱伝導率は空気中のそれより非常に高く
、2〜2.7倍にもなる。
In other words, due to the difference between the thermal conductivity of the four gases and that of air or combustion gas, the thermal properties of the furnace wall are as shown in Table 1. The conductivity is much higher than that in air, 2 to 2.7 times higher.

この結果、炉体の放散熱量が増加して凝鎚作業中の損失
熱量が増加する。また、第2図に示す従来の連続式脇錨
炉においては、台車11上に被焼銘物6を配贋し、この
被焼錨物6の外側をインナーカバーで被い、その台車1
1を順次炉内へ移動させるとともに、インナーカバー2
内へ日2ガスを供給し、そしてその後炉内から取り出す
競錨サイクルを繰り返すに際して、空間8,9はともに
Qガス雰囲気となっており、かつ炉内温度は600℃以
上に維持されているので、炉内の日2ガスが炉外へ噴出
して空気と接触することによる爆発を防止するため、炉
の入口および出口に扉12,13および14,15を配
置してそれぞれ入口室16および出口室17を区画し、
台車の袋入、取り出し時にこれらの各室をN2等の不活
性ガスで満たして仏と炉外空気が直接接触することのな
いよう各扉を順次に操作する。
As a result, the amount of heat dissipated from the furnace body increases, and the amount of heat lost during the coagulating operation increases. In addition, in the conventional continuous type side anchor furnace shown in FIG.
1 into the furnace one after another, and the inner cover 2
When repeating the racing anchor cycle in which gas is supplied into the furnace twice a day and then taken out from the furnace, both spaces 8 and 9 are in a Q gas atmosphere, and the temperature inside the furnace is maintained at 600°C or higher. In order to prevent an explosion caused by gas inside the furnace blowing out of the furnace and coming into contact with air, doors 12, 13 and 14, 15 are placed at the inlet and outlet of the furnace to close the inlet chamber 16 and the outlet, respectively. compartmentalize room 17,
When loading and unloading bags from the trolley, each of these chambers is filled with an inert gas such as N2, and each door is operated in sequence to prevent direct contact between the Buddha and the air outside the furnace.

このため、炉の構造および運転操作が極めて複雑になり
、またN2ガスなどの不活性ガスが必要となる他、冷却
帯城a内における低温度日2ガスの爆発の危険性を確実
に除去するためには、高精度で作動が完全な安全装置が
必要となる。
For this reason, the structure and operation of the furnace are extremely complicated, and inert gas such as N2 gas is required.In addition, it is necessary to reliably eliminate the risk of explosion of low-temperature gas in the cooling zone a. This requires a safety device with high precision and perfect operation.

本発明はこれらの問題を有利に解決するものである。The present invention advantageously solves these problems.

以下に本発明の実施例を図面に基いて詳細に説明する。Embodiments of the present invention will be described in detail below with reference to the drawings.

図中1は炉底壁、2はインナーカバー、5は耐火断熱レ
ンガあるいはセラミックファイバーなどを内張りした炉
横であり、この炉構の入口端および出口端にはそれぞれ
1個ずつの扉12,15を設ける。また、この例では炉
底壁1に複数個の空気導入口16を設けるとともに、炉
礎5の頂壁に複数個の排出口17を設け、各空気導入口
16を空気供給管18によって送出装置19に接続する
。一方、排出口17を排気筒20‘こよって煙突21に
接続する。さらに排気筒20と空気供給管18で熱交換
器22を構成して排気ガスの熱で供給空気を加熱する。
なお、図中1 1は台車であり、この台車上には被焼鈍
物6を戦遣するとともに、インナーカバー2を被せて炉
内を移動させる。また、インナー力バー2と台車11と
の間のシールは、第1図について述べたと同様にして行
なわれているので、後述するようにしてインナーカバー
2内へ供給された日2ガスは、焼錨中に従来の装置のよ
うにインナーカバー外へ流出する。さらに、図中23は
第2図に示すと同様の冷却帯域a内に配置した点じに手
段、手は暁鈍炉の加熱帯城である。第4図は日2ガス配
管系統例を示す説明図であり、台車11に日2ガス供給
管7を固定し、この供聯合管7を炉壁下方の地下室内へ
突出させるとともに、その先端にカプラー24を取り付
ける。
In the figure, 1 is the bottom wall of the furnace, 2 is the inner cover, and 5 is the side of the furnace lined with fireproof and insulating bricks or ceramic fibers.There are doors 12 and 15 at the inlet and outlet ends of the furnace structure, respectively. will be established. In addition, in this example, a plurality of air inlets 16 are provided in the furnace bottom wall 1, and a plurality of exhaust ports 17 are provided in the top wall of the furnace foundation 5, and each air inlet 16 is connected to a delivery device by an air supply pipe 18. Connect to 19. On the other hand, the exhaust port 17 is connected to the chimney 21 through the exhaust pipe 20'. Further, the exhaust pipe 20 and the air supply pipe 18 constitute a heat exchanger 22 to heat the supply air with the heat of the exhaust gas.
In the figure, reference numeral 11 denotes a truck, on which the object 6 to be annealed is transported, and the object 6 is covered with an inner cover 2 and moved inside the furnace. Furthermore, since the seal between the inner force bar 2 and the truck 11 is performed in the same manner as described with reference to FIG. During the anchorage, it flows out of the inner cover like in the conventional device. Furthermore, the reference numeral 23 in the figure is a means placed within the cooling zone a similar to that shown in FIG. FIG. 4 is an explanatory diagram showing an example of a daily gas piping system, in which a daily gas supply pipe 7 is fixed to a trolley 11, this joint pipe 7 is projected into the basement below the furnace wall, and its tip is Attach coupler 24.

また、日2ガス本管25とりガス分岐管26とをフレキ
シブルチューブ27で接続し、分岐管26をその両端に
接続したシリンダー28で進退可能ならしめ、さらに、
炉内に位置決めした比ガス供給管7と対応する位置で分
岐管26に枝管29を突出させ、これらの枝管の先端に
前述のカプラ−24と頚脱するカプラー30を取り付け
る。このような構成の炉を操業するに際しては、まず、
送出装置19を作動させて炉内へ空気を供聯合し、次い
で、炉内温度を760qo以上に上昇させ、そして冷却
帯城aの点火手段23をON‘こする。その後、扉12
,15を開いて台車11上の被焼鈍材を炉内へ装入して
各扉12,15を閉止する。この状態において、シリン
ダー28の作動の下に、カプラー24とカブラー29を
掛合ごせてインナーカバー2内へ比ガスを供給する。こ
こで、インナーカバー2から洩れた比ガスは、炉内で加
熱された空気と接触して直ちに、または点火手段23の
作動に塞いて燃焼する。これは、比ガスの着火温度57
0℃であり、加熱帯城bにおける炉内温度が760℃以
上であるから、ここでは比ガスは空気との接触によって
直ちに燃焼し、また、日2ガスの着火温度以下の温度を
有し、かつ日2ガスの爆発範囲4〜74%の混合比(空
気中)を有する冷却帯域aでは点火手段の介在によって
日2ガスが燃焼することに起因する。
In addition, the daily gas main 25 and the gas branch pipe 26 are connected by a flexible tube 27, and the branch pipe 26 is made to be movable forward and backward by a cylinder 28 connected to both ends thereof, and further,
Branch pipes 29 are made to protrude from the branch pipe 26 at positions corresponding to the specific gas supply pipe 7 positioned in the furnace, and the above-mentioned coupler 24 and a coupler 30 that can be retracted from the neck are attached to the tips of these branch pipes. When operating a furnace with such a configuration, first,
The delivery device 19 is operated to feed air into the furnace, and then the temperature inside the furnace is raised to 760 qo or more, and the ignition means 23 of the cooling zone a is turned on. After that, door 12
, 15 are opened, the material to be annealed on the cart 11 is charged into the furnace, and each door 12, 15 is closed. In this state, under the operation of the cylinder 28, the coupler 24 and the coupler 29 are engaged to supply specific gas into the inner cover 2. Here, the specific gas leaking from the inner cover 2 comes into contact with the heated air in the furnace and burns immediately or when the ignition means 23 is activated. This is the specific gas ignition temperature 57
0°C, and the temperature inside the furnace in the heating zone b is 760°C or higher, so here the specific gas burns immediately upon contact with air, and also has a temperature below the ignition temperature of the gas, This is due to the fact that in the cooling zone a, which has a mixture ratio (in air) of 4 to 74% of the explosive range of the 2 gas, the 2 gas is combusted with the intervention of the ignition means.

なお、図示例では炉内へ供給される空気は、炉内温度が
−旦760午0以上に上昇した後は、熱交換器22の機
能に基いて20000以上に子熱されるので、冷えた空
気を直接炉内へ供給する場合よりも炉の所要加熱エネル
ギーを低減させることができる。
In the illustrated example, the air supplied into the furnace is heated to 20,000 ℃ or more based on the function of the heat exchanger 22 after the temperature inside the furnace rises to 760 pm or higher. The required heating energy for the furnace can be reduced compared to the case where the gas is directly supplied into the furnace.

その後、同様にして暁錨材を順次炉内へ菱入する。Thereafter, Akatsuki anchor materials are sequentially introduced into the furnace in the same manner.

この装入に際しては、その都度シリンダー28を作動さ
せてカプラー30と順次に掛合するカブラー24を介し
てインナーカバー2内へ間欠的に弘ガスを供V給する。
各被焼鎚材を炉内の加熱帯城bおよび冷却帝城aを通過
させた後、扉15から炉外へ取り出して燐鈍を終了する
During this charging, the cylinder 28 is actuated each time to intermittently supply hydrogen gas into the inner cover 2 through the coupler 24 which is sequentially engaged with the coupler 30.
After each material to be hammered passes through the heating belt b and the cooling belt a in the furnace, it is taken out of the furnace through the door 15 and the phosphor annealing process is completed.

このような4ガスの燃焼によってインナーカバー外の空
間1川こはN2と、燃焼生成物である比0と、もし余剰
空気が供給された場合にはそのQとが充満し、そして排
気筒20および煙突21を経て大気へ排出される。
Through the combustion of these four gases, the space outside the inner cover 1 is filled with N2, the combustion product 0, and if excess air is supplied, the Q, and the exhaust pipe 20 is filled with and is discharged into the atmosphere through the chimney 21.

空間1 0内がN2,日20,02で満たされる結果、
扉12または15を開放して炉内ガスを炉外空気と直接
接触させても燃焼、爆発のおそれは全くなくなり、この
ため扉12,15を同時に開放して被焼鈍物の装入・取
り出しを同時に行うことができ、炉の構造および操作が
極めて単純になる。
As a result, space 10 is filled with N2, day 20,02,
Even if the door 12 or 15 is opened to bring the gas inside the furnace into direct contact with the air outside the furnace, there is no risk of combustion or explosion. Therefore, the doors 12 and 15 can be opened at the same time to load and remove the objects to be annealed. They can be carried out simultaneously, making the structure and operation of the furnace extremely simple.

また、炉壁の放散熱量も増加しないので、炉墜を厚くす
ることなく所要の断熱性を得ることができ、熱経済的に
もまた炉設備的にも有利である。さらに、この際の熱勘
定を行うと第2表に示すようになる。
Furthermore, since the amount of heat dissipated from the furnace wall does not increase, the required heat insulation can be obtained without increasing the thickness of the furnace wall, which is advantageous in terms of thermoeconomics and furnace equipment. Furthermore, when the heat is counted at this time, the results are shown in Table 2.

第2表 空間10内へ流出する日2ガス量 loゆれr供給
空気量 262め化r供給空
気予熱温度 350℃排出ガス温度
loo0℃排出ガス量
312林竹rこのため、本発明によれ
ば日2ガスの燃焼によって175900(Kcal/h
r)の熱量が炉温の上昇に寄与することとなり、さらに
熱経済上の大なる利益がある。
Second table Amount of gas flowing out into the space 10 lo Sway r Supply air amount 262nd supply air preheating temperature 350°C Exhaust gas temperature
loo0℃ exhaust gas amount
Therefore, according to the present invention, by burning 2 gas per day, 175,900 (Kcal/h
The amount of heat in r) contributes to an increase in the furnace temperature, and there is also a large thermoeconomic benefit.

従って本発明によれば、安全な炉の操業を行い得ること
はもちろん、炉の構造および操作を単純化することがで
き、さらに炉の放散熱量を低下させて熱効率を高めるこ
とができる。
Therefore, according to the present invention, not only can the furnace be operated safely, but also the structure and operation of the furnace can be simplified, and furthermore, the amount of heat dissipated by the furnace can be reduced and the thermal efficiency can be increased.

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

第1図は従来のバッチ式焼鎚炉を示す断面図、第2図は
従来の連続式焼鎚炉を示す断面図、第3図は本発明の実
施例を示す部分断面図、第4図は比ガスの配管系統をを
示す部分断面図、である。 1…・・・炉底壁、2・・・・・・インナーカバー、5
…・・・炉構、16・・・・・・空気導入口、17・・
・・・・排気口、19・・・・・・送出装置。 鎌1図 第2図 鎌3図 範4図
FIG. 1 is a sectional view showing a conventional batch-type pounding furnace, FIG. 2 is a sectional view showing a conventional continuous-type pounding furnace, FIG. 3 is a partial sectional view showing an embodiment of the present invention, and FIG. 4 is a partial sectional view showing a specific gas piping system. 1... Furnace bottom wall, 2... Inner cover, 5
...Furnace structure, 16...Air inlet, 17...
...Exhaust port, 19... Delivery device. Sickle 1 figure 2 sickle 3 figure 4 figure

Claims (1)

【特許請求の範囲】[Claims] 1 断熱性耐性火物で構成した炉壁の内側にインナーカ
バーを配置し、このインナーカバー内へH_2を含むガ
スを供給する無酸化雰囲気焼鈍炉において、炉壁に複数
個の空気導入口を開口させるとともに、排気口を開口さ
せ、前記空気導入口を送出装置に接続したことを特徴と
する無酸化雰囲気焼鈍炉。
1 In a non-oxidizing atmosphere annealing furnace where an inner cover is placed inside the furnace wall made of heat-insulating and resistant fireworks and a gas containing H_2 is supplied into the inner cover, multiple air inlets are opened in the furnace wall. A non-oxidizing atmosphere annealing furnace characterized in that the air inlet is opened and the air inlet is connected to a delivery device.
JP327478A 1978-01-18 1978-01-18 Non-oxidizing atmosphere annealing furnace Expired JPS6018728B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP327478A JPS6018728B2 (en) 1978-01-18 1978-01-18 Non-oxidizing atmosphere annealing furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP327478A JPS6018728B2 (en) 1978-01-18 1978-01-18 Non-oxidizing atmosphere annealing furnace

Publications (2)

Publication Number Publication Date
JPS5496408A JPS5496408A (en) 1979-07-30
JPS6018728B2 true JPS6018728B2 (en) 1985-05-11

Family

ID=11552855

Family Applications (1)

Application Number Title Priority Date Filing Date
JP327478A Expired JPS6018728B2 (en) 1978-01-18 1978-01-18 Non-oxidizing atmosphere annealing furnace

Country Status (1)

Country Link
JP (1) JPS6018728B2 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61154829U (en) * 1985-03-19 1986-09-25
JPS6339327U (en) * 1986-09-01 1988-03-14
JPS63121023U (en) * 1987-01-31 1988-08-05
JPS63123232U (en) * 1987-02-04 1988-08-10

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57104630A (en) * 1980-12-19 1982-06-29 Kawasaki Steel Corp Operating method for continuous heat treatment furnace for metallic strip coil

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61154829U (en) * 1985-03-19 1986-09-25
JPS6339327U (en) * 1986-09-01 1988-03-14
JPS63121023U (en) * 1987-01-31 1988-08-05
JPS63123232U (en) * 1987-02-04 1988-08-10

Also Published As

Publication number Publication date
JPS5496408A (en) 1979-07-30

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