JPH101712A - Brick structure of degassing equipment - Google Patents

Brick structure of degassing equipment

Info

Publication number
JPH101712A
JPH101712A JP14704396A JP14704396A JPH101712A JP H101712 A JPH101712 A JP H101712A JP 14704396 A JP14704396 A JP 14704396A JP 14704396 A JP14704396 A JP 14704396A JP H101712 A JPH101712 A JP H101712A
Authority
JP
Japan
Prior art keywords
brick
uppermost
parts
uppermost step
circulating flow
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.)
Withdrawn
Application number
JP14704396A
Other languages
Japanese (ja)
Inventor
Tadashi Aso
正 麻生
Ikuo Irie
入江郁夫
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
Nippon 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 Nippon Steel Corp filed Critical Nippon Steel Corp
Priority to JP14704396A priority Critical patent/JPH101712A/en
Publication of JPH101712A publication Critical patent/JPH101712A/en
Withdrawn legal-status Critical Current

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  • Treatment Of Steel In Its Molten State (AREA)
  • Furnace Housings, Linings, Walls, And Ceilings (AREA)

Abstract

PROBLEM TO BE SOLVED: To reduce erosion speed of bricks in a circulating flow tube by dividing a brick at uppermost step into an upper and the lower parts at the uppermost part of the circulating flow tube in at least the center side of a vessel and inclining downward the boundary surface of both brick parts to molten steel flowing passage side. SOLUTION: The lower vessel 1 has cylindrical circulating flow tubes 3, 4. The circulating flow tube 3 lines the bricks at three or four steps, and each boundary surface between brick 5a at the uppermost step and a brick 5b just below the brick at the uppermost step has the inclination so that the friction force becomes large because the boundary area becomes larger than a horizatal boundary area. Direction of the inclination is formed as downward to the molten steel flowing passage side. The reason for dividing the brick at the uppermost step into two parts, is that the division into small parts is more profitable to restrain the crack caused by structural spalling, etc., progressed from the apparatus. The eroding speed of the brick at the uppermost step is reduced and the service life of the lower vessel 1 is improved.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は真空脱ガス装置とく
にRH脱ガス装置のレンガ構造の改良に関するものであ
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a vacuum degassing apparatus, and more particularly to an improvement in a brick structure of an RH degassing apparatus.

【0002】[0002]

【従来の技術】溶鋼の真空精練に使用するRH脱ガス設
備は、槽内を真空にして、溶鋼を一方の浸漬管から吸い
込み、他方の浸漬管から吐出し、鍋内溶鋼を槽内に循環
させ、溶鋼全体を主に脱ガス処理する設備である。その
中で浸漬管に接続する下部槽の環流管は、溶鋼およびス
ラグによる溶損が大きいため下部槽の寿命を決定する主
な部位となる点で重要である。この部分のレンガ積み
は、従来図2のようにレンガの境界面が全て水平だっ
た。
2. Description of the Related Art RH degassing equipment used for vacuum refining of molten steel is a method in which the inside of a tank is evacuated, the molten steel is sucked in from one dipping pipe, discharged from the other dipping pipe, and the molten steel in the pot is circulated in the tank. This is a facility for mainly degassing the entire molten steel. Among them, the recirculation pipe of the lower tank connected to the immersion pipe is important in that it is a main part that determines the life of the lower tank because the molten steel and the slag are largely melted. In the brickwork of this part, the boundary surfaces of the bricks were all horizontal as shown in FIG.

【0003】図中1はRH下部槽、2は側壁レンガ、
3,4は環流管、5cは従来の環流管最上段レンガ、6
は環流管二段目レンガ、7は環流管最下端レンガ、8は
敷レンガ、9はフランジを示す。
In the figure, 1 is an RH lower tank, 2 is a side wall brick,
3 and 4 are reflux pipes, 5c is a top brick of a conventional reflux pipe, 6
Denotes a second-stage brick of the reflux pipe, 7 denotes a lowermost brick of the reflux pipe, 8 denotes a brick, and 9 denotes a flange.

【0004】[0004]

【本発明が解決しようとする課題】従来技術によるレン
ガ積み構造では、環流管最上段レンガがある程度溶損す
ると、溶鋼の激しい流動により最上段レンガは浮上して
しまい、結果的に他の部位より溶損速度が大きくなるた
め、下部槽の寿命を低耐用で律速する要因となってい
た。
In the brick structure according to the prior art, when the uppermost brick of the reflux pipe is eroded to some extent, the uppermost brick floats by violent flow of molten steel, and as a result, the uppermost brick is lifted from other parts. Since the erosion rate is increased, the service life of the lower tank is limited with low durability.

【0005】[0005]

【問題を解決するための手段】本願発明は前記問題点を
有利に解決するものであって、その主旨は、RH脱ガス
設備の環流管レンガ構造において、少なくとも槽中心側
の環流管最上段レンガを上下に分割し、その分割した上
レンガと下レンガとの境界面がレンガとの境界面が溶鋼
流路側に下向きに傾斜させたことを特徴とするレンガ構
造である。
Means for Solving the Problems The present invention advantageously solves the above-mentioned problems, and the gist of the present invention is to provide a reflux pipe brick structure for RH degassing equipment, in which at least the uppermost brick of the reflux pipe at the center of the tank. Is divided into upper and lower parts, and a boundary surface between the divided upper brick and lower brick has a boundary surface with the brick inclined downward toward the molten steel channel side.

【0006】以下、図によって、本発明を詳細に説明す
る。
Hereinafter, the present invention will be described in detail with reference to the drawings.

【0007】図1は本発明のRH下部槽レンガ構造を示
す正面断面図である。図1において下部槽1は円筒状の
環流管3,4を有している。環流管3はレンガが三ない
し四段積みで、その最上段レンガ5aとその最上段下レ
ンガ5bの境界面は傾斜をつけており、境界面が水平で
ある場合よりも境界面積が大きく摩擦力が大きくなるよ
うにしてある。傾斜の向きは、溶鋼流路側が下になるよ
うに傾斜をもたす。傾斜の向きが逆であると、図3のよ
うに最上段レンガの溶損が進むにつれて境界面積が小さ
くなり、摩擦力も小さくなる。従来の最上段レンガ5c
を二つに割った理由は、小割りにした方が、上部から進
行する構造スポーリング等による亀裂の伝播を抑えられ
るためである。図3中5a’は境界面の傾斜が本発明と
逆の環流管最上段上レンガ、5b’は境界面の傾斜が本
発明と逆の最上段下レンガを示す。
FIG. 1 is a front sectional view showing the RH lower tank brick structure of the present invention. In FIG. 1, the lower tank 1 has cylindrical reflux pipes 3 and 4. The reflux pipe 3 has three or four levels of bricks, and the boundary between the uppermost brick 5a and the lowermost brick 5b is inclined, so that the boundary area is larger than when the boundary is horizontal and the frictional force is larger. Is set to be large. The direction of the inclination is inclined so that the molten steel channel side is downward. When the direction of the inclination is reversed, as shown in FIG. 3, as the erosion of the uppermost brick progresses, the boundary area decreases, and the frictional force decreases. Conventional top brick 5c
The reason for dividing into two is that, when divided into small parts, the propagation of cracks due to structural spalling or the like that proceeds from above can be suppressed. In FIG. 3, 5a 'indicates the uppermost brick of the reflux pipe whose inclination of the boundary surface is opposite to the present invention, and 5b' indicates the uppermost lower brick whose inclination of the boundary surface is opposite to the present invention.

【0008】このことから、環流管最上段レンガを上下
に分割し、分割した上レンガと下レンガとの境界面が溶
融流路側に下向きに傾斜させたことを特徴とする本願発
明のレンガ構造が有効である。
Accordingly, the brick structure according to the present invention is characterized in that the uppermost brick of the reflux pipe is divided into upper and lower parts, and a boundary surface between the divided upper and lower bricks is inclined downward toward the melting channel. It is valid.

【0009】[0009]

【発明の実施の形態】BEST MODE FOR CARRYING OUT THE INVENTION

【0010】[0010]

【実施例】本願発明を実際に300tRHに適用した例
を下記に示す。
An example in which the present invention is actually applied to 300 tRH is shown below.

【0011】本願発明を適用した下部槽は鋼浴部内径が
約2200mm、浸漬管内径650mmである。環流管
全体高さは830mmである。環流管レンガのサイズは
幅250mmで、高さは約180mmから380mm、
円周方向では28分割している。従来の環流管最上段レ
ンガの高さは350mmで本願発明の環流管最上段レン
ガは従来品を溶鋼流路側が下になるように約12°の傾
斜でほぼ中央位置で分割した(5a,5b)。傾斜角度
は大きすぎるとレンガに鋭角部分が発生し、亀裂が入り
やすくなるため、30°以下にするのが望ましい。
The lower tank to which the present invention is applied has a steel bath inner diameter of about 2200 mm, and an immersion pipe inner diameter of 650 mm. The total height of the reflux tube is 830 mm. The size of the reflux tube brick is 250 mm in width and the height is about 180 mm to 380 mm,
It is divided into 28 parts in the circumferential direction. The height of the top brick of the conventional reflux tube is 350 mm, and the top brick of the reflux tube of the present invention is obtained by dividing the conventional product at a substantially central position with an inclination of about 12 ° so that the molten steel channel side is downward (5a, 5b). ). If the inclination angle is too large, an acute angle portion is generated in the brick and a crack is easily formed. Therefore, the inclination angle is desirably 30 ° or less.

【0012】本願発明のレンガ構造にてRH操業をおこ
なったところ、環流管レンガの溶損速度が減少し、下部
槽寿命が従来の400chから10〜20%向上した。
When the RH operation was performed with the brick structure of the present invention, the erosion rate of the reflux pipe brick was reduced, and the lower tank life was improved by 10 to 20% from the conventional 400 ch.

【0013】[0013]

【発明の効果】従来のレンガ積み構造では、環流管最上
段レンガが溶損するにつれ、溶鋼の激しい流動により最
上段レンガは浮上してしまい、結果的に他の部位より溶
損速度が大きくなるため、下部槽の寿命を低耐用で律速
する要因となっていたが、本発明のレンガ構造により、
環流管最上段レンガの溶損速度が低減され、下部槽寿命
が従来の10〜20%向上し、脱ガス工程の稼動率、コ
スト面の向上に大きく寄与した。
In the conventional brickwork structure, as the uppermost brick in the reflux pipe is eroded, the uppermost brick floats due to the strong flow of molten steel, and as a result, the erosion speed becomes higher than in other parts. , Had become a factor limiting the service life of the lower tank with low durability, but with the brick structure of the present invention,
The erosion rate of the uppermost brick in the reflux pipe was reduced, the service life of the lower tank was improved by 10 to 20%, and the operating rate and cost of the degassing process were greatly improved.

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

【図1】本願発明による脱ガス設備の環流管レンガ構造
を示す正面断面図。
FIG. 1 is a front sectional view showing a reflux pipe brick structure of a degassing facility according to the present invention.

【図2】従来の脱ガス設備の環流管レンガ構造を示す正
面断面図。
FIG. 2 is a front sectional view showing a reflux pipe brick structure of a conventional degassing facility.

【図3】環流管レンガの境界面の傾斜が本願発明と逆の
状態を示す一部断面図。
FIG. 3 is a partial sectional view showing a state in which the inclination of the boundary surface of the reflux pipe brick is opposite to that of the present invention.

【符号の説明】[Explanation of symbols]

1…RH下部槽 2…側壁レンガ 3,4…環流管 5a…環流管最上段
上レンガ 5b…環流管最下段下レンガ 5a’…境界面の傾斜が本発明と逆の環流管最上段上レ
ンガ 5b’…境界面の傾斜が本発明と逆の環流管最上段下レ
ンガ 5c…従来の環流管最上段レンガ 6…環流管二段目レンガ 7…環流管最下端レ
ンガ 8…敷レンガ 9…フランジ
DESCRIPTION OF SYMBOLS 1 ... RH lower tank 2 ... Side wall brick 3, 4 ... Reflux pipe 5a ... Reflux pipe uppermost step upper brick 5b ... Reflux pipe lowermost step lower brick 5a '... Boundary surface inclination reverse to that of the present invention, upper level pipe upper brick 5b ': Uppermost lower brick of the reflux pipe whose inclination of the boundary surface is opposite to that of the present invention 5c: Conventional uppermost brick of the reflux pipe 6 ... Second brick of the reflux pipe 7 ... Lowermost brick of the reflux pipe 8 ... Brick 9 ... Flange

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 RH脱ガス設備の環流管レンガ構造にお
いて、少なくとも槽中心側の環流管最上部のレンガ構造
において、最上段レンガを上下に分割し、その分割した
上レンガと下レンガとの境界面が溶鋼流路側に下向きに
傾斜させたことを特徴とするレンガ構造。
In a reflux pipe brick structure of an RH degassing facility, at least in a brick structure at an uppermost part of a reflux pipe on a tank center side, an uppermost brick is vertically divided, and a boundary between the divided upper brick and lower brick. A brick structure characterized in that the surface is inclined downward toward the molten steel channel.
JP14704396A 1996-06-10 1996-06-10 Brick structure of degassing equipment Withdrawn JPH101712A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14704396A JPH101712A (en) 1996-06-10 1996-06-10 Brick structure of degassing equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14704396A JPH101712A (en) 1996-06-10 1996-06-10 Brick structure of degassing equipment

Publications (1)

Publication Number Publication Date
JPH101712A true JPH101712A (en) 1998-01-06

Family

ID=15421226

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14704396A Withdrawn JPH101712A (en) 1996-06-10 1996-06-10 Brick structure of degassing equipment

Country Status (1)

Country Link
JP (1) JPH101712A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110885913A (en) * 2019-10-24 2020-03-17 包头钢铁(集团)有限责任公司 Method for controlling length of tubular brick at steel tapping hole and improving steel tapping rate

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110885913A (en) * 2019-10-24 2020-03-17 包头钢铁(集团)有限责任公司 Method for controlling length of tubular brick at steel tapping hole and improving steel tapping rate

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Legal Events

Date Code Title Description
A300 Withdrawal of application because of no request for examination

Free format text: JAPANESE INTERMEDIATE CODE: A300

Effective date: 20030902