JPS61253327A - Method for decreasing dew point of heating furnace - Google Patents

Method for decreasing dew point of heating furnace

Info

Publication number
JPS61253327A
JPS61253327A JP9449285A JP9449285A JPS61253327A JP S61253327 A JPS61253327 A JP S61253327A JP 9449285 A JP9449285 A JP 9449285A JP 9449285 A JP9449285 A JP 9449285A JP S61253327 A JPS61253327 A JP S61253327A
Authority
JP
Japan
Prior art keywords
furnace
dew point
gas
heating
heating furnace
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
JP9449285A
Other languages
Japanese (ja)
Inventor
Shogo Hamachi
濱地 省吾
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 JP9449285A priority Critical patent/JPS61253327A/en
Publication of JPS61253327A publication Critical patent/JPS61253327A/en
Pending legal-status Critical Current

Links

Landscapes

  • Heat Treatment Of Strip Materials And Filament Materials (AREA)
  • Tunnel Furnaces (AREA)
  • Furnace Details (AREA)
  • Coating With Molten Metal (AREA)

Abstract

PURPOSE:To reduce the time required for decreasing the dew point of a heating furnace and to improve the operating efficiency thereof by heating the inside of the furnace while injecting an inert gas or reducing gas of a low dew point into the spacing between the outside wall of the furnace body and refractories of the heating furnace. CONSTITUTION:The inside of the heating furnace A for heating treatment of a material C to be heated conveyed by means of rollers B is heated up while the inert gas or reducing gas of <=-40 deg.C dew point is introduced from a gas feed main pipe 4 through a branch pipe 5 and a gas feed hole 6 into the spacing 3 between the outside wall 2 of the body of the furnace A and the retractories 1 lined on the inside thereof and is discharged from a discharge hole 9 to a discharge pipe 11 prior to the operation of the above-mentioned furnace. The gaseous N2 having -78 deg.C dew point is suitable as the above-mentioned inert gas and the gaseous Ax (N2+H2) or the like having -70 deg.C dew point is adequate as the reducing gas. The gas is preferably preheated to about 250-300 deg.C to maintain the pressure in the spacing 3 slightly higher than the pressure in the furnace. The moisture of the refractories 1 is thereby absorbed and the decrease of the dew point in the furnace is accelerated.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、加熱炉の露点をその操業に先だって低下させ
る方法に関する。
DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a method for lowering the dew point of a heating furnace prior to its operation.

(従来技術) 連続圧延工程や連続メッキ工程等には、目的に応じて種
々の加熱炉(熱処理炉も含む)が設置される。たとえば
連続溶融亜鉛メッキ工程ではメッキ前の材料に、焼鈍と
清浄化とを目的とした熱処理を施すことが不可欠の条件
である。このような加熱炉において炉を新築、改築した
場合、耐火物は多量の水分を含有しておシ、また修理等
のため、炉を長期間停止した場合にも耐火物は水分を吸
収する。このような状態の炉はいわゆる露点が高く、た
とえば連続メッキ工程の場合はメッキの密着性を悪化さ
せる原因になるので、炉操業を開始する前には必ず露点
を所定の値以下に低下させるための乾燥作業を行わなけ
ればならない。
(Prior Art) Various heating furnaces (including heat treatment furnaces) are installed in continuous rolling processes, continuous plating processes, etc. depending on the purpose. For example, in a continuous hot-dip galvanizing process, it is essential that the material be subjected to heat treatment for annealing and cleaning purposes before plating. In such heating furnaces, when the furnace is newly built or renovated, the refractories contain a large amount of moisture, and the refractories also absorb moisture when the furnace is stopped for a long period of time for repairs or the like. Furnaces in such conditions have a high dew point, which can cause deterioration of plating adhesion in continuous plating processes, so be sure to lower the dew point to a predetermined value or less before starting furnace operation. drying work must be carried out.

(発明が解決しようとする問題点) 上記の乾燥作業は加熱炉を内部から加熱しながら炉内に
露点の低いNuガスやHJガスを注入して、水分を含ん
だ耐火物を乾燥させることによシ行われるが、連続溶融
亜鉛メッキ工程の場合、操業中の安定露点は一40℃〜
−50℃とされておシ、ここまで露点を低下させるのに
5日以上を要することも少なくない。そこで通常は露点
が一15℃程度になった時点で操業を開始し、安定露点
に至るまでの間は、ツイン速度を抑えてメッキの密着性
を確保しながら操業を行っているが、それでも−15℃
の露点に到達させるのに平均40時間以上を要する。
(Problem to be solved by the invention) The above drying work involves injecting Nu gas or HJ gas with a low dew point into the furnace while heating it from the inside to dry the refractories containing moisture. However, in the case of a continuous hot-dip galvanizing process, the stable dew point during operation is -40℃~
It is assumed that the dew point is -50°C, and it often takes 5 days or more to lower the dew point to this extent. Therefore, we normally start operations when the dew point reaches around 115 degrees Celsius, and until the dew point reaches a stable dew point, we operate by reducing the twin speed to ensure plating adhesion, but even then - 15℃
It takes an average of 40 hours or more to reach the dew point of .

本発明の目的はこの露点低下に要する時間を短縮し、炉
操業開始期を早めて操業効率の大巾向上を図る露点低下
方法を提供することにある。
An object of the present invention is to provide a dew point lowering method that shortens the time required for lowering the dew point, advances the start of furnace operation, and greatly improves operational efficiency.

(問題点を解決するための手段ならびに作用)ところで
、加熱炉の構造を見たとき、炉体外壁とその内側の耐火
物との間に両者の熱膨張の差により生じる間隙のあるの
が分かる。そしてこの間隙は炉の規模、種類にもよって
異なるが通常10原程度の値である。本発明者は、この
既存の間隙部に着目し、露点低下作業時にこの部分に露
点の低いNuガス、HJガス等を同時進行的に流通させ
れば、露点低下作業に要する時間が短縮されると考え、
種々の実地試験を行った。その結果、この4ム 間隙部へのガス流通の併用によシ露点を下作業の所要時
間が従来の約%程度に短縮され得ることを知見した。
(Means and actions for solving the problem) By the way, when we look at the structure of the heating furnace, we can see that there is a gap between the outer wall of the furnace body and the refractory inside it due to the difference in thermal expansion between the two. . Although this gap varies depending on the scale and type of furnace, it is usually a value of about 10 mm. The present inventor focused on this existing gap, and if Nu gas, HJ gas, etc. with a low dew point is simultaneously introduced into this part during dew point lowering work, the time required for dew point lowering work can be shortened. I thought,
Various field tests were conducted. As a result, it was found that the time required for lowering the dew point can be reduced to approximately % of the conventional time by using gas flow to the 4-mm gap.

本発明は、この知見に基づいてなされたもので、加熱炉
の炉体外壁と耐火物との間隙部内に、露点が一40℃以
下の不活性ガスまたは還元性ガスを注入しながら炉内を
加熱することを特徴とする加熱炉の露点低下方法を要旨
とする。
The present invention was made based on this knowledge, and the inside of the heating furnace is heated while injecting an inert gas or reducing gas with a dew point of 140°C or less into the gap between the outer wall of the furnace body and the refractory. The gist is a method for lowering the dew point of a heating furnace, which is characterized by heating.

以下、図面を参照して本発明の方法を更に具体的に説明
する。第1図において(3)は加熱炉で、短体外壁(1
)(鉄皮)の内側に間隙部(3)ヲおいて耐火物(21
(レンガ)がライニングされた構造となっている。■は
加熱炉(2)の内部に設置した、被加熱物(Qを搬送す
るためのローラーである。
Hereinafter, the method of the present invention will be explained in more detail with reference to the drawings. In Figure 1, (3) is the heating furnace, and the outer wall of the short body (1
) (iron shell) with a gap (3) inside the refractory (21
The structure is lined with (brick). (2) is a roller installed inside the heating furnace (2) for conveying the object to be heated (Q).

加熱炉(4)の外側には炬に平行に2本の送気母管(4
)が配設されている。この母管(4)から分岐した複数
の送気枝管(5)は、外壁(1)の下部に適当間隔で接
続され、上記間隙部(3)とは送気孔(6)を介して連
通している。各送気枝管にはバルブ(7)および圧力計
(8)が設けられている。一方、炉頂部の外壁(1)に
は排気孔(9)が1個もしくはそれ以上設けられており
、これにバルブQQを介して排気管αυが接続されてい
る。(イ)は上記間隙部(3〕内のガス圧力測定用の圧
力計で、必要に応じて1個もしくはそれ以上装着される
On the outside of the heating furnace (4), there are two air supply main pipes (4) parallel to the furnace.
) are provided. A plurality of air supply branch pipes (5) branched from this main pipe (4) are connected to the lower part of the outer wall (1) at appropriate intervals, and communicate with the gap (3) through air supply holes (6). are doing. Each air supply branch pipe is provided with a valve (7) and a pressure gauge (8). On the other hand, one or more exhaust holes (9) are provided in the outer wall (1) at the top of the furnace, and an exhaust pipe αυ is connected to this through a valve QQ. (A) is a pressure gauge for measuring the gas pressure in the gap (3), and one or more pressure gauges are installed as necessary.

送気母管(4)には露点が一40℃以下の不活性ガスま
たは還元性ガスが送給されるが、具体的には不活性ガス
としてはたとえばNuガス(露点−78℃)などであシ
、還元性ガスとしてはたとえばAxガス(Nコ+Hコ)
(露点−70℃)などである。
An inert gas or reducing gas with a dew point of 140 degrees Celsius or less is supplied to the air supply main pipe (4). As a reducing gas, for example, Ax gas (N+H)
(dew point -70°C), etc.

上記加熱炉設備において本発明の露点低下方法を実施す
るには、加熱炉(8)内に従来通シネ活性ガスまたは還
元性ガスを通じながら炉内を加熱すると同時に、送気母
管(4)から送気枝管(5)を介して送給される露点−
40℃以下の不活性ガスまたは還元性ガスを、パルプ(
7)を開放して吸気孔(6)から炉の間隙部(3)に導
入する。
In order to carry out the method of lowering the dew point of the present invention in the heating furnace equipment described above, it is necessary to heat the inside of the heating furnace (8) while passing conventional cine active gas or reducing gas into the heating furnace (8), and at the same time The dew point supplied via the air supply branch pipe (5) -
Pulp (
7) is opened and introduced into the gap (3) of the furnace through the intake hole (6).

この際、圧力計02を測定しながらバルブ(7)の開度
を調節して、間隙部(3)内のガス圧が炉内・外圧より
高目になるようにする。これは外気の侵入防止、及びパ
ージ効果を高めるためである。また導入ガスは露点低下
効果を促進するため、250℃〜800℃程度に加熱し
ておく方がよい。
At this time, the opening degree of the valve (7) is adjusted while measuring the pressure gauge 02 so that the gas pressure in the gap (3) is higher than the pressure inside and outside the furnace. This is to prevent outside air from entering and to enhance the purging effect. Further, in order to promote the effect of lowering the dew point, the introduced gas is preferably heated to about 250°C to 800°C.

以上のようにして間隙部(3)に注入されたガスはいわ
ゆるキャリアガスとなって耐火レンガ(1)に吸湿され
ていた湿分を逆に吸収した上、排気孔(9)から排気管
01)を介して炉外へ排除され、炬自体の加熱と相俟っ
て、炉内の露点の低下を促進する。
The gas injected into the gap (3) as described above becomes a so-called carrier gas and reversely absorbs the moisture absorbed by the refractory brick (1), and then passes through the exhaust hole (9) to the exhaust pipe 01. ), which, together with the heating of the kettle itself, promotes a lowering of the dew point inside the furnace.

不活性ガスまたは還元性ガスの送給量は、加熱炉の規模
によっても異なるが、100Nn1/Hr以上が望まし
い。
The amount of inert gas or reducing gas to be fed varies depending on the scale of the heating furnace, but is preferably 100 Nn1/Hr or more.

(実施例) 次の第1表に諸元を示す連続式溶融亜鉛メッキ用の加熱
炉において、定期修理後、加熱炉内に、Coガス(流量
30ON→りr)を通じながら炉内を800℃に加熱す
るとともに、炉壁と耐火物との間の間隙部に露点が一7
8℃の乾燥Ax Cアンモニア分解ガス(NJ+Hコ)
)i260℃に加熱して、+8011mAqの圧力、1
2ONtrI/Hrノ流量テ連続的に送給した。送給開
始時(立上り時)の露点は+10℃〜20℃であった。
(Example) In a heating furnace for continuous hot-dip galvanizing whose specifications are shown in Table 1 below, after regular repairs, the inside of the furnace was heated to 800°C while Co gas (flow rate 30ON → RIr) was passed through the furnace. At the same time, the dew point in the gap between the furnace wall and the refractory reaches 17.
Dry Ax C ammonia decomposition gas (NJ+H) at 8℃
) i Heated to 260°C, +8011 mAq pressure, 1
A flow rate of 2ONtrI/Hr was continuously fed. The dew point at the start of feeding (startup) was +10°C to 20°C.

炉内露点の経時変化を第2図に実線で示す。また比較の
ため同一種、同一規模の加熱炉において、炉内加熱およ
び炉内ガス送給のみを行った場合の結果を、従来方法と
して同図に破線で示す。
Figure 2 shows the change in furnace dew point over time as a solid line. For comparison, the results obtained when only in-furnace heating and in-furnace gas feeding were performed in a heating furnace of the same type and size are shown by a broken line in the figure as a conventional method.

第   1   表 第2図から明らかなように、炉内温度を一15℃まで下
げるのに従来方法では40Hrを要していたが、本発明
方法に、よれば80Hrと発に短縮できた。
As is clear from Table 1 and Figure 2, the conventional method required 40 hours to lower the furnace temperature to -15°C, but the method of the present invention reduced the time to 80 hours.

また、−15℃に低下させるまでの使用ガス総量は、従
来方法では120 N”/HrX 40 Hr −48
0ONn?であったが、本発明方法では作業期間中は余
分にガスを必要とするものの、期間が大巾に短縮される
結果、全体では4600 NINIIとなり、4.2%
の削減を達成できた。その結果総使用エネルギー量(炉
内加熱エネルギーとガス加熱エネルギーとガス送給エネ
ルギーとの和)も9600万Kcatから770075
 Kcalへ、19.8%の低減を図ることができた。
In addition, the total amount of gas used to lower the temperature to -15°C is 120 N"/HrX 40 Hr -48 in the conventional method.
0ONn? However, although the method of the present invention requires extra gas during the working period, the working period is greatly shortened, resulting in a total of 4,600 NINII, which is a reduction of 4.2%.
achieved a reduction in As a result, the total amount of energy used (the sum of furnace heating energy, gas heating energy, and gas feeding energy) decreased from 96 million Kcat to 770,075.
We were able to achieve a 19.8% reduction in Kcal.

(発明の効果) 以上の説明から明らかなように、本発明は加熱炉の露点
低下速度を速め、炉の操業開始時を早めて、操業効率の
向上に大きな効果を発揮するのみならず、露点低下に要
するエネルギーの節減も可能となシ、更に既存の空隙部
を利用するため、実施容易で、経済的に著しい効果を有
するものである。
(Effects of the Invention) As is clear from the above description, the present invention not only accelerates the dew point reduction rate of the heating furnace and brings the furnace into operation earlier, and has a great effect on improving operational efficiency, but also It is possible to save the energy required for lowering, and furthermore, since the existing void is used, it is easy to implement and has a significant economic effect.

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

第1図は本発明に係る露点低下方法を実施するための加
熱炉の断面図、第2図は従来技術と本発明方法とにおけ
る炉内露点の経時的変化を、比較対照して図示したもの
である。 1:炉体外壁(鉄皮)、2:耐火物(レンガ)、3:間
隙部、4:送気母管、5:送気枝管、6:吸気孔、7、
lO:パルプ、8.12:圧力計、9:排気孔、11:
排気管
Fig. 1 is a cross-sectional view of a heating furnace for carrying out the dew point lowering method according to the present invention, and Fig. 2 is a diagram comparing and contrasting the change in the furnace dew point over time between the conventional technology and the method of the present invention. It is. 1: Furnace outer wall (iron shell), 2: Refractory (brick), 3: Gap, 4: Air supply main pipe, 5: Air supply branch pipe, 6: Air intake hole, 7,
lO: Pulp, 8.12: Pressure gauge, 9: Exhaust hole, 11:
Exhaust pipe

Claims (1)

【特許請求の範囲】[Claims] (1)加熱炉の炉体外壁と耐火物との間隙部内に、露点
が−40%以下の不活性ガスまたは還元性ガスを注入し
ながら炉内を加熱することを特徴とする加熱炉の露点低
下方法。
(1) The dew point of a heating furnace characterized by heating the inside of the furnace while injecting an inert gas or reducing gas with a dew point of -40% or less into the gap between the outer wall of the furnace body and the refractory. How to lower.
JP9449285A 1985-04-30 1985-04-30 Method for decreasing dew point of heating furnace Pending JPS61253327A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9449285A JPS61253327A (en) 1985-04-30 1985-04-30 Method for decreasing dew point of heating furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9449285A JPS61253327A (en) 1985-04-30 1985-04-30 Method for decreasing dew point of heating furnace

Publications (1)

Publication Number Publication Date
JPS61253327A true JPS61253327A (en) 1986-11-11

Family

ID=14111795

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9449285A Pending JPS61253327A (en) 1985-04-30 1985-04-30 Method for decreasing dew point of heating furnace

Country Status (1)

Country Link
JP (1) JPS61253327A (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01285783A (en) * 1988-05-13 1989-11-16 Kawasaki Steel Corp Wall structure of heat treatment furnace
JPH0347923A (en) * 1989-04-05 1991-02-28 Nippon Yakin Kogyo Co Ltd Bright annealing furnace
JPH0413817A (en) * 1990-05-07 1992-01-17 Nippon Yakin Kogyo Co Ltd Bright annealing furnace
JPH04116127A (en) * 1990-09-04 1992-04-16 Nippon Yakin Kogyo Co Ltd Bright annealing furnace
JP2012111995A (en) * 2010-11-25 2012-06-14 Jfe Steel Corp Method for adjusting furnace atmosphere of continuous annealing furnace
CN103438700A (en) * 2013-08-02 2013-12-11 浙江吉利汽车研究院有限公司 Heating furnace used for hot forming production line
JP2015160975A (en) * 2014-02-26 2015-09-07 Jfeスチール株式会社 Continuous annealing furnace start-up method
WO2022234701A1 (en) * 2021-05-06 2022-11-10 Jfeスチール株式会社 Method for controlling dew point of continuous annealing furnace, continuous annealing method for steel sheets, method for producing steel sheet, continuous annealing furnace, continuous hot dip galvanization facility and alloyed hot dip galvanization facility

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01285783A (en) * 1988-05-13 1989-11-16 Kawasaki Steel Corp Wall structure of heat treatment furnace
JPH0347923A (en) * 1989-04-05 1991-02-28 Nippon Yakin Kogyo Co Ltd Bright annealing furnace
JPH0413817A (en) * 1990-05-07 1992-01-17 Nippon Yakin Kogyo Co Ltd Bright annealing furnace
JPH04116127A (en) * 1990-09-04 1992-04-16 Nippon Yakin Kogyo Co Ltd Bright annealing furnace
JP2012111995A (en) * 2010-11-25 2012-06-14 Jfe Steel Corp Method for adjusting furnace atmosphere of continuous annealing furnace
CN103438700A (en) * 2013-08-02 2013-12-11 浙江吉利汽车研究院有限公司 Heating furnace used for hot forming production line
JP2015160975A (en) * 2014-02-26 2015-09-07 Jfeスチール株式会社 Continuous annealing furnace start-up method
WO2022234701A1 (en) * 2021-05-06 2022-11-10 Jfeスチール株式会社 Method for controlling dew point of continuous annealing furnace, continuous annealing method for steel sheets, method for producing steel sheet, continuous annealing furnace, continuous hot dip galvanization facility and alloyed hot dip galvanization facility
JPWO2022234701A1 (en) * 2021-05-06 2022-11-10

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