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JPH0619106B2 - Continuous atmosphere heat treatment equipment - Google Patents
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JPH0619106B2 - Continuous atmosphere heat treatment equipment - Google Patents

Continuous atmosphere heat treatment equipment

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Publication number
JPH0619106B2
JPH0619106B2 JP59197268A JP19726884A JPH0619106B2 JP H0619106 B2 JPH0619106 B2 JP H0619106B2 JP 59197268 A JP59197268 A JP 59197268A JP 19726884 A JP19726884 A JP 19726884A JP H0619106 B2 JPH0619106 B2 JP H0619106B2
Authority
JP
Japan
Prior art keywords
furnace
gas
pipe
collecting
heat treatment
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 - Lifetime
Application number
JP59197268A
Other languages
Japanese (ja)
Other versions
JPS6173826A (en
Inventor
正博 松本
賢治 川手
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.)
Daido Steel Co Ltd
Original Assignee
Daido Steel Co Ltd
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 Daido Steel Co Ltd filed Critical Daido Steel Co Ltd
Priority to JP59197268A priority Critical patent/JPH0619106B2/en
Publication of JPS6173826A publication Critical patent/JPS6173826A/en
Publication of JPH0619106B2 publication Critical patent/JPH0619106B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Tunnel Furnaces (AREA)

Description

【発明の詳細な説明】 [産業上の利用分野] この発明は炉内に雰囲気ガスを充満させ鋼材等の被熱物
をその雰囲気ガスの基で無酸化,還元,脱浸炭等の所期
の熱処理を行なわしめる連続雰囲気熱処理装置に関する
ものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial field of application] The present invention is intended to fill a furnace with an atmospheric gas and subject a heat-treated object such as a steel material to non-oxidation, reduction, decarburization, etc. based on the atmospheric gas. The present invention relates to a continuous atmosphere heat treatment apparatus for performing heat treatment.

[従来の技術] 周知のように連続式の雰囲気熱処理炉は、被熱物の搬送
方向に順じて複数の温度ゾーンに区画され、被熱物は各
温度ゾーンを通過することによって所定の温度曲線に従
い昇温し高温度保持され徐冷されるようにしている。そ
して炉内の雰囲気ガスの組成を調整することによって被
熱物を無酸化加熱、或いは還元,脱浸炭等所定の熱処理
を行なわしめるようにしている。この雰囲気ガスは一般
に第2図に示したようにガス発生装置から3個所程度に
分岐して炉b中へ供給し炉b中を縦貫したガスは両端部
の被熱物装入口c或いは被熱物抽出口dから排出される
ようにしている。
[Prior Art] As is well known, a continuous atmosphere heat treatment furnace is divided into a plurality of temperature zones in the conveying direction of the object to be heated, and the object to be heated passes through each temperature zone to have a predetermined temperature. The temperature is raised according to the curve, and the temperature is kept high and gradually cooled. Then, the composition of the atmosphere gas in the furnace is adjusted so that the object to be heated is subjected to a predetermined heat treatment such as non-oxidative heating, reduction, decarburization or the like. As shown in FIG. 2, this atmosphere gas is generally branched from the gas generator into about three places and supplied into the furnace b. The product is discharged from the product extraction port d.

[従来の技術の問題点] 上記従来のようにして雰囲気ガスを炉内に供給する方式
ではその雰囲気ガスが炉長方向に縦貫するために温度ゾ
ーン毎に炉内ガスの組成変化を持たせるようなことはで
きない。ところが被熱物が実際に必要とする雰囲気ガス
の濃度はその加熱温度に応じて違ってくるために、上記
のように雰囲気ガスを供給していたのでは、温度ゾーン
毎に組成変化を持たせることができないため或る温度ゾ
ーンについては過剰なまでに雰囲気ガスを供給すること
になり、従って雰囲気ガスの消費量が大きくなりランニ
ングコストを増大させるという問題点があった。
[Problems of the Prior Art] In the conventional method of supplying the atmospheric gas into the furnace as described above, since the atmospheric gas penetrates longitudinally in the furnace, the composition of the gas in the furnace should be changed for each temperature zone. I can't do anything. However, since the concentration of the atmospheric gas actually required by the object to be heated varies depending on the heating temperature, if the atmospheric gas is supplied as described above, it is possible to change the composition in each temperature zone. Since it is not possible to supply the atmospheric gas to a certain temperature zone in an excessive amount, the consumption amount of the atmospheric gas increases and the running cost increases.

[問題点を解決させるための手段] そこでこの発明の連続雰囲気熱処理装置は、被熱物の搬
送方向に順じて複数の温度ゾーンが区画形成された連続
雰囲気熱処理炉において、分配元管に複数の分配枝管を
設け、雰囲気ガスを該分配枝管を介して各温度ゾーン毎
に直接供給すると共に、該各分配枝管には雰囲気ガスの
供給量を個々に制御できるコントロールバルブを設け、
集収元管に複数の集収枝管を設け、炉内ガスを該集収枝
管を介して各温度ゾーンから直接回収すると共に、該各
集収枝管には炉内ガスの回収量を個々に制御できるコン
トロールバルブを設け、該集収枝管および集収元管によ
って回収された炉内ガスを、酸素,二酸化炭素,水蒸気
等の酸化性ガスを除去する除去装置に通して精製し、前
記分配元管および分配枝管を通して炉内の各温度ゾーン
に直接再循環させるようにしたことを特徴とするもので
ある。
[Means for Solving Problems] Therefore, in the continuous atmosphere heat treatment apparatus of the present invention, in the continuous atmosphere heat treatment furnace in which a plurality of temperature zones are formed in a division in the transport direction of the object to be heated, a plurality of distribution source tubes are provided. Distribution branch pipe is provided, and the atmospheric gas is directly supplied to each temperature zone through the distribution branch pipe, and each distribution branch pipe is provided with a control valve capable of individually controlling the supply amount of the atmospheric gas,
A plurality of collecting / branching pipes are provided in the collecting / collecting pipe, and the furnace gas can be directly recovered from each temperature zone through the collecting / branching pipe, and the collecting amount of the furnace gas can be individually controlled in each of the collecting / branching pipes. A control valve is provided, and the in-furnace gas collected by the collecting branch pipe and the collecting source pipe is purified by passing through a removing device that removes oxidizing gases such as oxygen, carbon dioxide, and steam, and the distributing source pipe and the distributing pipe. It is characterized by being directly recirculated to each temperature zone in the furnace through a branch pipe.

[実施例] 第1図に示した雰囲気熱処理炉1は被熱物2の搬送方向
に順じて炉内が3A〜3Eの5室の温度ゾーンに区画形
成され、4は装入扉、5は抽出扉である。6は雰囲気ガ
ス発生装置、7はその雰囲気ガス発生装置6に接続され
た分配元管で、該分配元管7の先端は複数の分配枝管7
A〜7Eに分岐し、該分配枝管7A〜7Eを介して雰囲
気ガスを各温度ゾーン3A〜3Eに直接供給できるよう
にしている。8A〜8Eはその各温度ゾーン3A〜3E
への雰囲気ガスの供給量を個々に制御できるように分配
枝管7A〜7Bに設けられたコントロールバルブであ
る。また、9はブロワ10の吸引側に設けられた集収元
管で、該集収元管の先端は複数の集収枝管9A〜9Eに
分岐し、該集収枝管9A〜9Eを介して各温度ゾーン3
A〜3Eから直接炉内ガスを回収できるようにしてい
る。11A〜11Eは各温度ゾーン3A〜3Eからの炉
内ガスの回収量を個々に制御できるように集収枝管9A
〜9Eに設けられたコントロールバルブである。12は
各温度ゾーン3A〜3Eから集収枝管9A〜9E,集収
元管9を介して回収された炉内ガス中の酸素および二酸
化炭素を除去する除去装置、13は水蒸気を除去するた
め前記除去装置12と直列に接続された除去装置で、該
除去装置13の二次側は前記分配元管7に接続されてい
る。
[Example] In the atmosphere heat treatment furnace 1 shown in FIG. 1, the inside of the furnace is divided into five temperature zones 3A to 3E in accordance with the transfer direction of the article to be heated 2, and 4 is a charging door and 5 is a charging door. Is the extraction door. Reference numeral 6 denotes an atmospheric gas generator, 7 denotes a distribution source pipe connected to the atmospheric gas generation device 6, and the tip of the distribution source pipe 7 has a plurality of distribution branch pipes 7.
The gas is branched into A to 7E, and the atmospheric gas can be directly supplied to the temperature zones 3A to 3E through the distribution branch pipes 7A to 7E. 8A to 8E are the respective temperature zones 3A to 3E
A control valve provided in each of the distribution branch pipes 7A to 7B so that the supply amount of the atmospheric gas can be individually controlled. Further, 9 is a collecting source pipe provided on the suction side of the blower 10, the tip of the collecting source pipe is branched into a plurality of collecting branch pipes 9A to 9E, and each temperature zone is provided via the collecting branch pipes 9A to 9E. Three
The in-furnace gas can be directly recovered from A to 3E. 11A to 11E are collecting / branching pipes 9A so that the amount of recovered gas in the furnace from each of the temperature zones 3A to 3E can be individually controlled.
9E to 9E are control valves. Reference numeral 12 is a removing device for removing oxygen and carbon dioxide in the furnace gas recovered from each of the temperature zones 3A to 3E through the collecting / branching pipes 9A to 9E and the collecting and collecting pipe 9, and 13 is the removal device for removing water vapor. The removing device is connected in series with the device 12, and the secondary side of the removing device 13 is connected to the distributor pipe 7.

しかしてこの雰囲気熱処理炉においては、集収枝管9A
〜9E,集収元管9によって炉内ガスを回収し、除去装
置12,13に通すことによってその炉内ガス中の酸化
性ガスを除去せしめ、精製されたガスを再度分配元管
7,分配枝管7A〜7Eを通して炉内へ再循環できる。
このため雰囲気ガス発生装置6は循環する雰囲気ガスの
不足分を補う程度に雰囲気ガスを生成させればよく、雰
囲気ガスの消費量は大幅に軽減できる。また、第1図
(イ)にこの雰囲気熱処理炉1内の被熱物2の昇温曲線
を表示し、第1図(ロ)にその被熱物2の還元によって
炉内に放出される酸素の量および炉外からの侵入酸素の
量を併記するが、このように被熱物2からの酸素放出量
はその温度が上昇するに従い急増する。このため被熱物
2の酸化を防ぐためには特定の温度ゾーン(この場合温
度ゾーン3C,3D)に最も多量に雰囲気ガスを供給す
る必要がある。第1図(ハ)には無酸化加熱に実際必要
な炉内ガスの組成(CO)/COを上記各温度ゾー
ン毎に表わす。この雰囲気熱処理装置では各温度ゾーン
3A〜3E毎にその雰囲気ガスの供給量をコントロール
バルブ8A〜8Eによつて制御することができるので、
このような実際に必要とする炉内雰囲気ガスの組成が達
せられるように各温度ゾーンを制御することができ、雰
囲気ガスの供給が各温度ゾーンとも過不足なくコントロ
ールでき、その点からも雰囲気ガスの消費量を低減でき
る。
However, in the atmosphere heat treatment furnace, the collecting branch pipe 9A
9E, the furnace gas is collected by the collecting and collecting pipe 9, and the oxidizing gas in the furnace gas is removed by passing the gas through the removing devices 12 and 13, and the purified gas is distributed again to the distributing pipe 7 and the distributing branch pipe. It can be recycled into the furnace through tubes 7A-7E.
Therefore, the atmospheric gas generator 6 may generate the atmospheric gas to the extent that the shortage of the circulating atmospheric gas is supplemented, and the consumption of the atmospheric gas can be greatly reduced. In addition, FIG. 1 (a) shows the temperature rise curve of the object 2 to be heated in the atmospheric heat treatment furnace 1, and FIG. 1 (b) shows the oxygen released into the furnace by the reduction of the object 2 to be heated. The amount of oxygen and the amount of oxygen invading from outside the furnace are also shown. Thus, the amount of oxygen released from the object to be heated 2 rapidly increases as the temperature rises. Therefore, it is necessary to supply the largest amount of atmospheric gas to the specific temperature zone (in this case, the temperature zones 3C and 3D) in order to prevent oxidation of the object to be heated 2. FIG. 1C shows the composition (CO) 2 / CO 2 of the furnace gas actually required for non-oxidative heating for each temperature zone. In this atmosphere heat treatment apparatus, since the supply amount of the atmosphere gas can be controlled by the control valves 8A to 8E for each of the temperature zones 3A to 3E,
It is possible to control each temperature zone so that the composition of the atmosphere gas in the furnace actually required can be reached, and the supply of the atmosphere gas can be controlled without excess or deficiency in each temperature zone. The consumption of can be reduced.

[発明の効果] このように本発明の連続雰囲気熱処理装置は、各温度ゾ
ーン毎にコントロールバルブを有する分配枝管を設けて
各温度ゾーン毎に必要とする雰囲気ガスを供給できると
共に、各温度ゾーン毎にコントロールバルブを有する集
収枝管を設けて各温度ゾーン毎に炉内ガスを必要量回収
できるようにしたので、従来のように温度ゾーンを隔て
て炉内ガスが炉長方向に縦貫することを防ぎ、各温度ゾ
ーン毎に過不足なく炉内雰囲気ガス濃度の変化を持たせ
ることができる。このため品質を損うことなく雰囲気ガ
スの消費量を大幅に少なくできランニングコストを軽減
させることができる有益な効果がある。
[Effects of the Invention] As described above, in the continuous atmosphere heat treatment apparatus of the present invention, a distribution branch pipe having a control valve is provided for each temperature zone to supply an atmosphere gas required for each temperature zone and Since a collection and collection pipe with a control valve was provided for each temperature zone so that the required amount of furnace gas could be recovered in each temperature zone, the furnace gas should be longitudinally traversed across the temperature zone as in the past. Therefore, it is possible to prevent the temperature of the gas in the furnace from changing and to change the temperature in each temperature zone without excess or deficiency. Therefore, there is a beneficial effect that the consumption amount of the atmospheric gas can be significantly reduced and the running cost can be reduced without deteriorating the quality.

【図面の簡単な説明】[Brief description of drawings]

第1図はこの発明に係る雰囲気熱処理装置の配管系統図
に温度曲線,酸素放出量および炉内ガス組成を併記した
線図、第2図は従来の雰囲気熱処理装置の配管系統図で
ある。 1……雰囲気熱処理炉、2……被熱物、3A〜3E……
温度ゾーン、6……雰囲気ガス発生装置、7……分配元
管、7A〜7E……分配枝管、8A〜8E……コントロ
ールバルブ、9……集収元管、9A〜9E……集収枝
管、11A〜11E……コントロールバルブ、12,1
3……除去装置。
FIG. 1 is a diagram in which a temperature curve, an oxygen release amount, and a gas composition in a furnace are shown together in a piping system diagram of an atmosphere heat treatment apparatus according to the present invention, and FIG. 2 is a piping system diagram of a conventional atmosphere heat treatment apparatus. 1 ... Atmosphere heat treatment furnace, 2 ... Heated object, 3A to 3E ...
Temperature zone, 6 ... Atmosphere gas generator, 7 ... Distribution pipe, 7A-7E ... Distribution branch pipe, 8A-8E ... Control valve, 9 ... Collection pipe, 9A-9E ... Collection pipe , 11A to 11E ... Control valve, 12, 1
3 ... Removal device.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】被熱物の搬送方向に順じて複数の温度ゾー
ンが区画形成された連続雰囲気熱処理炉において、分配
元管に複数の分配枝管を設け、雰囲気ガスを該分配枝管
を介して各温度ゾーン毎に直接供給すると共に、該各分
配枝管には雰囲気ガスの供給量を個々に制御できるコン
トロールバルブを設け、集収元管に複数の集収枝管を設
け、炉内ガスを該集収枝管を介して各温度ゾーンから直
接回収すると共に、該各集収枝管には炉内ガスの回収量
を個々に制御できるコントロールバルブを設け、該集収
枝管および集収元管によって回収された炉内ガスを、酸
素,二酸化炭素,水蒸気等の酸化性ガスを除去する除去
装置に通して精製し、前記分配元管および分配枝管を通
して炉内の各温度ゾーンに直接再循環させるようにした
ことを特徴とする連続雰囲気熱処理装置。
1. A continuous atmosphere heat treatment furnace in which a plurality of temperature zones are defined and formed in the conveying direction of a material to be heated, a plurality of distribution branch pipes are provided in a distribution source pipe, and an atmosphere gas is supplied to the distribution branch pipes. While directly supplying each temperature zone via each temperature zone, each distribution branch pipe is provided with a control valve capable of individually controlling the supply amount of the atmospheric gas, and a plurality of collection branch pipes are provided in the collection source pipe to supply the gas in the furnace. While directly collecting from each temperature zone through the collecting branch pipe, each collecting branch pipe is provided with a control valve capable of individually controlling the amount of the collected gas in the furnace, and is collected by the collecting branch pipe and the collection source pipe. The furnace gas is purified by passing through a removing device for removing oxidizing gases such as oxygen, carbon dioxide, and steam, and is directly recirculated to each temperature zone in the furnace through the distribution source pipe and the distribution branch pipe. Characterized by Continued atmosphere heat treatment apparatus.
JP59197268A 1984-09-20 1984-09-20 Continuous atmosphere heat treatment equipment Expired - Lifetime JPH0619106B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59197268A JPH0619106B2 (en) 1984-09-20 1984-09-20 Continuous atmosphere heat treatment equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59197268A JPH0619106B2 (en) 1984-09-20 1984-09-20 Continuous atmosphere heat treatment equipment

Publications (2)

Publication Number Publication Date
JPS6173826A JPS6173826A (en) 1986-04-16
JPH0619106B2 true JPH0619106B2 (en) 1994-03-16

Family

ID=16371643

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59197268A Expired - Lifetime JPH0619106B2 (en) 1984-09-20 1984-09-20 Continuous atmosphere heat treatment equipment

Country Status (1)

Country Link
JP (1) JPH0619106B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1830147B1 (en) * 2006-03-03 2012-04-11 Schwartz, Eva Multi-chamber continuous furnace with protective gas supply and process for the scale free heating of galvanized workpieces
JP5884171B2 (en) * 2012-03-06 2016-03-15 Jfeスチール株式会社 In-furnace atmosphere improvement method in continuous annealing furnace

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58117822A (en) * 1981-12-29 1983-07-13 Daido Steel Co Ltd Atmosphere heat treatment furnace

Also Published As

Publication number Publication date
JPS6173826A (en) 1986-04-16

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