JPH032317A - Method for regulating atmospheric gas in bright annealing furnace - Google Patents

Method for regulating atmospheric gas in bright annealing furnace

Info

Publication number
JPH032317A
JPH032317A JP13544289A JP13544289A JPH032317A JP H032317 A JPH032317 A JP H032317A JP 13544289 A JP13544289 A JP 13544289A JP 13544289 A JP13544289 A JP 13544289A JP H032317 A JPH032317 A JP H032317A
Authority
JP
Japan
Prior art keywords
gas
amount
treated
furnace
exothermic
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.)
Pending
Application number
JP13544289A
Other languages
Japanese (ja)
Inventor
Kishio Kubo
久保 喜志夫
Seiji Tanimoto
征司 谷本
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.)
Nippon Steel Corp
Original Assignee
Sumitomo Metal Industries 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 Sumitomo Metal Industries Ltd filed Critical Sumitomo Metal Industries Ltd
Priority to JP13544289A priority Critical patent/JPH032317A/en
Publication of JPH032317A publication Critical patent/JPH032317A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To prevent the oxidation and decarburization of a material to be treated with certainty by subjecting an exothermic converted gas containing hydrocarbon by the amount corresponding to the amount of carbon contained in a material to be treated and the value of equilibrium partial pressure of oxygen in a furnace to heating up to high temp., to rapid cooling, and to dehumidification and then feeding the above gas to an annealing furnace. CONSTITUTION:A material to be treated is heat-treated and annealed in a bright annealing furnace in which an exothermic converted gas of hydrocarbon is used as heat-treatment atmosphere. In the above heat treatment method, the amount of hydrocarbon mixed into the exothermic converted gas is changed in the range of 1-20% of the amount of the exothermic converted gas according to the amount of carbon contained in the material to be treated. Simultaneously, the amount of the above hydrocarbon is further corrected according to the value of equilibrium partial pressure of oxygen in the furnace. The resulting gaseous mixture of exothermic converted gas and hydrocarbon is heated up to >=1100 deg.C, cooled rapidly, and dehumidified. By this method, the amounts of CO2 and H2O as decarburization components in the above gas are markedly reduced. By feeding the above gas after regulation as atmospheric gas into an annealing furnace, the local irregularities of atmospheric components can be prevented and the oxidation and decarburization of the material to be treated can be prevented with certainty.

Description

【発明の詳細な説明】 産業上の利用分野 この発明は、鋼管等の被処理物の酸化・脱炭を防止する
ため、炉内雰囲気を制御して熱処理する光輝焼鈍炉にあ
ける雰囲気ガスの調整方法に係り、発熱形変成ガスと炭
化水素ガスの混合ガスを高温に加熱することによって、
被処理物の酸化・脱炭を確実に防止する光輝焼鈍炉の雰
囲気ガス調整方法に関する。
[Detailed Description of the Invention] Industrial Application Field This invention is directed to the adjustment of atmospheric gas in a bright annealing furnace for heat treatment by controlling the furnace atmosphere in order to prevent oxidation and decarburization of objects to be treated such as steel pipes. By heating a mixture of exothermic gas and hydrocarbon gas to a high temperature,
The present invention relates to a method for adjusting atmospheric gas in a bright annealing furnace that reliably prevents oxidation and decarburization of a workpiece.

従来の技術 鋼管の熱処理炉として最も多く採用されている連続炉に
おいて、管内外表面の酸化・脱炭を防止するため、最近
炉内雰囲気を制御し、鋼管をラジアントチューブにより
間接的に加熱する光輝焼鈍炉の採用が目立っている。特
に、引扱管の熱処理に多く適用されている。
Conventional technology In continuous furnaces, which are most commonly used as heat treatment furnaces for steel pipes, in order to prevent oxidation and decarburization on the inner and outer surfaces of the pipes, the atmosphere inside the furnace is controlled and the steel pipes are heated indirectly using radiant tubes. The adoption of annealing furnaces is noticeable. In particular, it is often applied to heat treatment of handling pipes.

この光輝焼鈍炉では炉内雰囲気ガスに発熱形変成ガスを
用いるのが一般的であるが、発熱形変成ガスは浸炭力が
弱い(カーボンポテンシャル値0.015%)ことから
、被処理鋼管のカーボン含有最(通常0.1〜1.0%
C)において脱炭の可能性がある。また、露点温度が比
較的高いことから、炉況の変動によりスケールが発生し
易い。
In this bright annealing furnace, it is common to use an exothermic transformed gas as the atmosphere gas in the furnace, but since the exothermic transformed gas has a weak carburizing power (carbon potential value 0.015%), the carbon in the steel pipe to be treated is Contains maximum (usually 0.1-1.0%
There is a possibility of decarburization in C). Furthermore, since the dew point temperature is relatively high, scale is likely to occur due to fluctuations in furnace conditions.

一方、最近の製品の動向から、脱炭や鋼管表面性状等の
品質に対する要求が厳しくなってきており、これに対処
すべく無脱炭・無酸化熱処理への取組みが必要となって
きた。
On the other hand, recent product trends have led to stricter quality requirements such as decarburization and surface properties of steel pipes, and in order to meet these demands, it has become necessary to work on non-decarburization and non-oxidation heat treatment.

このため、例えば実公昭63−13242号公報には、
炭化水素変成ガスや窒素ガスに炭化水素を添加して熱処
理炉へ送気する方法が提案されている。
For this reason, for example, in Utility Model Publication No. 63-13242,
A method has been proposed in which hydrocarbons are added to hydrocarbon converted gas or nitrogen gas and the mixture is fed to a heat treatment furnace.

しかしながら、光輝焼鈍炉の熱処理雰囲気に炭化水素変
成ガスと窒素ノJス等に炭化水素ガスを混合したものを
用いる方法では、炉内吹込口付近で炭化水素の分解反応
が起り、局部的な雰囲気成分の乱れが生じるという問題
がある。
However, in the method of using a mixture of hydrocarbon gas, nitrogen gas, etc., in the heat treatment atmosphere of a bright annealing furnace, a decomposition reaction of hydrocarbons occurs near the inlet of the furnace, and the local atmosphere There is a problem in that the ingredients become disordered.

したがって、単に炭化水素変成ガスや窒素ガスに炭化水
素を添加して送気するだけは、炉内被処理物の酸化・脱
炭を十分に防止することができない。
Therefore, simply adding hydrocarbons to hydrocarbon converted gas or nitrogen gas and supplying the gas cannot sufficiently prevent oxidation and decarburization of the material to be treated in the furnace.

発明が解決しようとする課題 この発明は、前に述べたような実情よりみて、雰囲気ガ
スに発熱形変成ガスと炭化水素を混合して用いる光輝焼
鈍炉において、局部的な雰囲気成分の乱れを防止し、被
処理物の酸化・脱炭を確実に防止し得る雰囲気カス調整
方法を提案しようとするものでおる。
Problems to be Solved by the Invention In view of the above-mentioned actual situation, this invention aims to prevent local disturbance of atmospheric components in a bright annealing furnace that uses a mixture of an exothermic modified gas and a hydrocarbon in the atmospheric gas. However, this paper attempts to propose a method for adjusting the atmospheric scum that can reliably prevent oxidation and decarburization of the treated material.

課題を解決するための手段 この発明は、発熱形変成ガスに炭化水素を混合して光輝
焼鈍炉に送気する方法において、被処理物の含有カーボ
ン量に応じて発熱形変成ガスに混合する炭化水素量を、
発熱形変成ガス足の1〜20%の範囲で変化させるとと
もに、当該炭化水素量を炉内の平衡酸素分圧値に応じて
補正し、この発熱形変成ガスと炭化水素との混合ガスを
1100°C以上の温度に加熱した後、急冷・除湿する
ことを要旨とするものでおる。
Means for Solving the Problems This invention provides a method for mixing hydrocarbons with exothermic gas and sending the mixture to a bright annealing furnace. The amount of hydrogen,
The amount of hydrocarbons is varied in the range of 1 to 20% of the exothermic gas foot, and the amount of hydrocarbons is corrected according to the equilibrium oxygen partial pressure value in the furnace, and the mixed gas of this exothermic gas and hydrocarbons is The gist is to rapidly cool and dehumidify after heating to a temperature of °C or higher.

作   用 被処理物の含有カーボン最に応じて発熱形変成ガスに混
合する炭化水素量を、発熱形変成ガス最の1〜20%の
範囲で変化させることとしたのは、1%以下では充分な
脱炭防止効果が得られない。
The reason why we decided to vary the amount of hydrocarbons mixed into the exothermic modified gas in the range of 1 to 20% of the exothermic modified gas depending on the carbon content of the object to be treated is that 1% or less is sufficient. No decarburization prevention effect can be obtained.

また、被処理物の含有カーボン量から20%以下で充分
な脱炭防止効果が1qられる。
Further, a sufficient decarburization prevention effect of 1q can be obtained when the amount of carbon contained in the object to be treated is 20% or less.

上記炭化水素ガス量を炉内の平衡酸素分圧値に応じて補
正することとしたのは、被処理物のカーボン含有量に応
じたカーボンポテンシャルを得るためでおる。
The reason why the amount of hydrocarbon gas is corrected according to the equilibrium oxygen partial pressure value in the furnace is to obtain a carbon potential corresponding to the carbon content of the object to be treated.

発熱形変成ガスと炭化水素の混合ガスを1100’C以
上の高温に加熱した後、急冷・除湿するのは、次に示す
理由による。
The reason why the mixed gas of exothermic gas and hydrocarbon is heated to a high temperature of 1100'C or higher and then rapidly cooled and dehumidified is as follows.

発熱形変成ガスと炭化水素の混合ガスを高温に加熱する
と、以下に示す反応が生じる。
When a mixed gas of an exothermic gas and a hydrocarbon is heated to a high temperature, the following reaction occurs.

4H20十C4)1+o −4CO+9824CO2十
C4HID −) aco+ 5822CO2+H2→
C○十H20 したがって、上記混合ガスを急冷し、さらに除湿するこ
と(こよって、1党を束成分でおるCO2、H2Oの低
減がはかられるのである。
4H2010C4)1+o -4CO+9824CO20C4HID -) aco+ 5822CO2+H2→
C○1H20 Therefore, the above-mentioned mixed gas is rapidly cooled and further dehumidified (thereby, CO2 and H2O, which are bundle components of one gas, are reduced).

なお、発熱形変成ガスと炭化水素の混合ガスの加熱温度
を1100°C以上に限定したのは、CO2成分の低減
を促進するためである。
Note that the heating temperature of the mixed gas of exothermic gas and hydrocarbon was limited to 1100° C. or higher in order to promote the reduction of the CO2 component.

実  施  例 第1図はこの発明方法を実施するための装置溝成例を示
すブロック図であり、(1)は発熱形変成ガス発生器、
(2)は脱湿器、(3)はガス混合器、(4)は炭化水
素ガス供給器、(5)は加熱機能付ガス変成装置、(6
)はガス急冷・除湿装置、(7)は光輝焼鈍炉、(8)
は酸素分圧計、(9)はカーボンポテンシャル演算制御
器、 Vlは流量調節弁である。
Embodiment FIG. 1 is a block diagram showing an example of the configuration of an apparatus for carrying out the method of this invention, and (1) shows an exothermic modified gas generator;
(2) is a dehumidifier, (3) is a gas mixer, (4) is a hydrocarbon gas supply device, (5) is a gas conversion device with heating function, (6
) is a gas quenching/dehumidifying device, (7) is a bright annealing furnace, (8)
is an oxygen partial pressure meter, (9) is a carbon potential calculation controller, and Vl is a flow rate control valve.

すなわち、発熱形変成ガス発生器(1)を出た発熱形変
成ガスは脱湿器(2)を経てガス混合器(3)へ導入さ
れ、ここで炭化水素ガス供給器(4)より流量調節弁V
1を介して供給される炭化水素ガスと混合される。
That is, the exothermic converted gas that exits the exothermic converted gas generator (1) is introduced into the gas mixer (3) via the dehumidifier (2), where the flow rate is adjusted by the hydrocarbon gas supplier (4). Valve V
1 and mixed with hydrocarbon gas supplied via 1.

この時、光輝焼鈍炉(7)内の被処理物に対して無酸化
・無税成性の雰囲気ガスに調整すべく、被処理物の含有
カーボン量に応じて混合する炭化水素量を、カーボンポ
テンシャル演算制御器(9)にて発熱形変成ガス量の1
〜20%の範囲内とするとともに、酸素分圧計(8)に
て測定される炉内の酸素分圧値に応じて適正量に補正し
、流量調節弁v1を操作してその適正量をガス混合器(
3)へ供給する。
At this time, in order to adjust the atmosphere gas to be non-oxidizing and tax-free for the workpiece in the bright annealing furnace (7), the amount of hydrocarbons to be mixed is adjusted according to the amount of carbon contained in the workpiece. The calculation controller (9) determines the amount of heat-generating transformed gas.
~20%, correct the amount to an appropriate amount according to the oxygen partial pressure value in the furnace measured with the oxygen partial pressure meter (8), and operate the flow rate control valve v1 to adjust the appropriate amount of gas. mixer (
3).

ガス混合器(3)にて混合された発熱形変成ガスと炭化
水素の混合ガスは、加熱感能付ガス変成装置(5)にて
1100’C以上の温度に加熱され、急冷・除湿装置(
6)を経て光輝焼鈍炉(7)へ供給される。
The mixed gas of exothermic converted gas and hydrocarbon mixed in the gas mixer (3) is heated to a temperature of 1100'C or higher in the heat-sensing gas converter (5), and then passed through the quenching/dehumidifying device (
6) and is supplied to the bright annealing furnace (7).

次に、上記装置を使用し、光輝焼鈍炉にて炭素鋼鋼管(
0,15%C)の熱処理を行なった結果を、従来法と比
較して第1表に示す。
Next, using the above equipment, carbon steel pipe (
Table 1 shows the results of the heat treatment (0.15% C) in comparison with the conventional method.

本実施例では、発熱形変成ガスに対し5%の割合で炭化
水素を混合し、この混合ガスを1100°Cの温度に加
熱し、急冷・除湿したガスを雰囲気ガスとして用いた。
In this example, hydrocarbons were mixed at a ratio of 5% to the exothermic modified gas, and this mixed gas was heated to a temperature of 1100° C., and the gas that was rapidly cooled and dehumidified was used as the atmospheric gas.

なお、本実施例における熱処理パターンを第2図に示す
Note that the heat treatment pattern in this example is shown in FIG.

第1表より明らかなごとく、本発明法により、脱炭に有
害な成分であるCO2、H2Ota度は大幅に低下し、
被処理鋼管に脱炭およびスケールの発生は見られなかっ
た。
As is clear from Table 1, the method of the present invention significantly reduces CO2 and H2Ota, which are components harmful to decarburization.
No decarburization or scale formation was observed in the treated steel pipe.

以下余白 第  1 表 発明の詳細 な説明したごとく、この発明方法によれば、発熱形変成
ガスと炭化水素の混合ガスを高温に加熱し、かつ急冷・
除湿することによって脱炭に有害なCO2、8208度
を大幅に低下させることができるので、光輝焼鈍炉内の
被処理物の酸化・脱炭を確実に防止することでき、特に
高品質が要求される機械構造用鋼管等の製造に大なる効
果を奏するものである。
As described in detail in Table 1 below, according to the method of this invention, a mixed gas of an exothermic gas and a hydrocarbon is heated to a high temperature, and then rapidly cooled.
By dehumidifying, CO2, which is harmful to decarburization, can be significantly lowered by 8,208 degrees, so it is possible to reliably prevent oxidation and decarburization of the processed material in the bright annealing furnace, which requires particularly high quality. This is highly effective in manufacturing steel pipes for machine structures, etc.

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

第1図はこの発明方法を実施するための装置構成例を示
すブロック図、第2図は熱処理パターンを示す図である
。 1・・・発熱形変成ガス発生器 3・・・ガス混合器 4・・・炭化水素ガス供給器 5・・・加熱機能付ガス変成装置 6・・・ガス急冷・除湿装置 7・・・光輝焼鈍炉 8・・・酸素分圧h1 9・・・カーボンポテンシャル演算制御器出願人  住
友金屈工業株式会社
FIG. 1 is a block diagram showing an example of the configuration of an apparatus for carrying out the method of the present invention, and FIG. 2 is a diagram showing a heat treatment pattern. 1... Exothermic transformed gas generator 3... Gas mixer 4... Hydrocarbon gas supplier 5... Gas converter with heating function 6... Gas quenching/dehumidifying device 7... Kouki Annealing furnace 8...Oxygen partial pressure h1 9...Carbon potential calculation controller Applicant: Sumitomo Kinkuta Industries, Ltd.

Claims (1)

【特許請求の範囲】[Claims] 熱処理雰囲気に炭化水素の発熱形変成ガス(以下単に発
熱形変成ガス)を用いる光輝焼鈍炉において、炉内被処
理物に対して無酸化・無脱炭性の雰囲気ガスに調整する
方法であつて、被処理物の含有カーボン量に応じて発熱
形変成ガスに混合する炭化水素量を、発熱形変成ガス量
の1〜20%の範囲で変化させるとともに、当該炭化水
素量を炉内の平衡酸素分圧値に応じて補正し、この発熱
形変成ガスと炭化水素との混合ガスを1100℃以上の
温度に加熱した後、急冷・除湿して焼鈍炉へ送気するこ
とを特徴とする光輝焼鈍炉の雰囲気ガス調整方法。
A method of adjusting the atmosphere gas to be non-oxidizing and non-decarburizing for objects to be treated in the furnace in a bright annealing furnace using exothermic modified gas of hydrocarbons (hereinafter simply referred to as exothermic modified gas) in the heat treatment atmosphere. , the amount of hydrocarbons mixed into the exothermic modified gas is varied in the range of 1 to 20% of the amount of exothermic modified gas according to the amount of carbon contained in the workpiece, and the amount of hydrocarbons is adjusted to the equilibrium oxygen level in the furnace. Bright annealing characterized by correcting according to the partial pressure value and heating the mixed gas of the exothermic modified gas and hydrocarbon to a temperature of 1100°C or higher, followed by rapid cooling and dehumidification and sending the air to an annealing furnace. How to adjust the furnace atmosphere gas.
JP13544289A 1989-05-29 1989-05-29 Method for regulating atmospheric gas in bright annealing furnace Pending JPH032317A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13544289A JPH032317A (en) 1989-05-29 1989-05-29 Method for regulating atmospheric gas in bright annealing furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13544289A JPH032317A (en) 1989-05-29 1989-05-29 Method for regulating atmospheric gas in bright annealing furnace

Publications (1)

Publication Number Publication Date
JPH032317A true JPH032317A (en) 1991-01-08

Family

ID=15151817

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13544289A Pending JPH032317A (en) 1989-05-29 1989-05-29 Method for regulating atmospheric gas in bright annealing furnace

Country Status (1)

Country Link
JP (1) JPH032317A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005120448A (en) * 2003-10-17 2005-05-12 Chugai Ro Co Ltd Method for controlling bright annealing furnace
WO2013146520A1 (en) 2012-03-27 2013-10-03 関東冶金工業株式会社 Method for heat treatment and heat treatment apparatus, and heat treatment system
WO2014007046A1 (en) 2012-07-04 2014-01-09 関東冶金工業株式会社 Heat treatment method, heat treatment device, and heat treatment system

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005120448A (en) * 2003-10-17 2005-05-12 Chugai Ro Co Ltd Method for controlling bright annealing furnace
WO2013146520A1 (en) 2012-03-27 2013-10-03 関東冶金工業株式会社 Method for heat treatment and heat treatment apparatus, and heat treatment system
US9581389B2 (en) 2012-03-27 2017-02-28 Kanto Yakin Kogyo Co., Ltd. Method for heat treatment, heat treatment apparatus, and heat treatment system
WO2014007046A1 (en) 2012-07-04 2014-01-09 関東冶金工業株式会社 Heat treatment method, heat treatment device, and heat treatment system

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