JPH0410207Y2 - - Google Patents
Info
- Publication number
- JPH0410207Y2 JPH0410207Y2 JP17396486U JP17396486U JPH0410207Y2 JP H0410207 Y2 JPH0410207 Y2 JP H0410207Y2 JP 17396486 U JP17396486 U JP 17396486U JP 17396486 U JP17396486 U JP 17396486U JP H0410207 Y2 JPH0410207 Y2 JP H0410207Y2
- Authority
- JP
- Japan
- Prior art keywords
- slag
- trough
- separation container
- pig iron
- gutter
- 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
Links
- 239000002893 slag Substances 0.000 claims description 135
- 238000000926 separation method Methods 0.000 claims description 37
- 229910000805 Pig iron Inorganic materials 0.000 claims description 27
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 14
- 239000002184 metal Substances 0.000 description 13
- 229910052751 metal Inorganic materials 0.000 description 13
- 238000011144 upstream manufacturing Methods 0.000 description 8
- 229910052742 iron Inorganic materials 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 230000000694 effects Effects 0.000 description 4
- 230000002411 adverse Effects 0.000 description 2
- 238000005266 casting Methods 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000011819 refractory material Substances 0.000 description 2
- 238000004062 sedimentation Methods 0.000 description 2
- 239000010802 sludge Substances 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000005469 granulation Methods 0.000 description 1
- 230000003179 granulation Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 238000010079 rubber tapping Methods 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
Landscapes
- Furnace Charging Or Discharging (AREA)
- Furnace Details (AREA)
Description
【考案の詳細な説明】
(産業上の利用分野)
本考案は高炉から排出される溶滓中の粒銑を回
収する高炉溶滓の連続処理装置に関するものであ
る。[Detailed Description of the Invention] (Industrial Application Field) The present invention relates to a continuous blast furnace slag processing apparatus for recovering granular pig iron in the slag discharged from a blast furnace.
(従来の技術)
従来、この種の高炉溶滓の連続処理装置として
は、溶滓流路の中間部位に適宜段差をもつて下部
に溶銑排出口を穿設した銑滓分離容器を、前記溶
滓流路方向に対して交叉方向に傾動自在に配設し
たものが知られている。(Prior Art) Conventionally, as this type of continuous blast furnace slag processing equipment, a slag separation vessel having an appropriate step in the middle of a slag flow path and a molten metal discharge port at the bottom is used. It is known to be arranged so as to be tiltable in a direction perpendicular to the direction of the slag flow path.
(考案が解決しようとする問題点) しかしながら、上記方式は次の問題があつた。(The problem that the idea attempts to solve) However, the above method has the following problems.
(ア) 溶滓流路の樋の切替に際しては、仕切鉄板の
取付け及び片付け、あるいは整備に至るまです
べてが高熱悪環境下での人力作業により行われ
ているため、これを省くことが要求されてお
り、
(イ) 又、銑滓分離容器の取替あるいは修理などの
場合、銑滓分離容器の上方に ある溶滓樋など
が干渉して作業困難を極めるために、作業がし
易くかつ安全な場所に移動させる必要があつ
た。(a) When changing the gutter in the slag flow path, everything from installing and clearing the partition iron plate to maintenance is done manually in a high temperature and adverse environment, so it is necessary to eliminate this. (b) In addition, when replacing or repairing the pig slag separation container, the slag gutter located above the pig slag separation container interferes with the work, making the work extremely difficult. It was necessary to move it to a new location.
(問題点を解決するための手段)
本考案は上述した欠点を解決すべくなされたも
ので、高炉から排出される溶滓中の粒銑を回収す
る高炉溶滓の連続処理装置において、下部側に排
銑口を穿設し、上部側に溶滓流路方向にむかつて
複数の排滓路を形成した銑滓分離容器を溶滓流路
の中間部位に適宜段差をもつて配置し、該銑滓分
離容器を前記溶滓流路方向と交叉方向に傾動、あ
るいは走行させるように構成したことを特徴とす
る高炉溶滓の連続処理装置である。(Means for Solving the Problems) The present invention was made to solve the above-mentioned drawbacks. A slag separation vessel having a plurality of slag drainage channels formed in the upper side in the direction of the slag flow path is arranged with appropriate steps in the middle of the slag flow path. This continuous processing apparatus for blast furnace slag is characterized in that the pig slag separation container is configured to tilt or travel in a direction intersecting the direction of the slag flow path.
(作用)
本考案は溶滓処理中に銑滓分離器の傾動又は走
行において、溶滓排出路が自動的に交互に切替え
ができる作用を有する。(Function) The present invention has an effect that the slag discharge path can be automatically switched alternately when the slag separator is tilted or moved during slag processing.
(実施例)
以下、この考案の一実施例を図に基づいて説明
する。(Example) Hereinafter, an example of this invention will be described based on the drawings.
第1図は本考案による装置を設置した概略平面
図で、第2図は本装置の平面図、第3図は第2図
における本装置のA−A断面矢視図、第4図は第
1図と第2図における本装置と溶滓樋のB−B断
面矢視図を示す。 Fig. 1 is a schematic plan view of the device according to the present invention installed, Fig. 2 is a plan view of the device, Fig. 3 is a cross-sectional view taken along line A-A of the device in Fig. 2, and Fig. 4 is a schematic plan view of the device according to the present invention. FIG. 2 shows a cross-sectional view taken along line B-B of the apparatus and the slag gutter in FIGS. 1 and 2.
まず、第1図において、炉体18に連設した大
樋9の下流部にスキンマー10が設けられてお
り、スキンマー10を挾んで炉体側には溶滓樋1
と反炉体側には溶銑樋6を配設してある。 First, in FIG. 1, a skimmer 10 is provided downstream of a large gutter 9 connected to a furnace body 18, and a slag gutter 1 is provided on the furnace body side with the skinmer 10 in between.
A hot metal trough 6 is arranged on the reactor side.
また、溶滓樋1の下流側の端部には、銑滓分離
容器2を適宜段差をもつて配設し、かつ、銑滓分
離容器2の上部に定位置排滓路2a、排銑時排滓
路2bが設けられ、更にその下に適当な段差をも
つて傾注樋行樋3と水枠行き又はドライピツト行
きの樋(以下水枠行樋4と表現する)を分岐して
設けて溶滓の流路を形成している。 Further, at the downstream end of the slag trough 1, a slag separation container 2 is arranged with an appropriate level difference, and a fixed position slag discharge passage 2a is provided at the upper part of the slag separation container 2. A sludge drainage channel 2b is provided, and a tilting trough 3 and a trough for the water frame or dry pit (hereinafter referred to as water frame trough 4) are branched with an appropriate step below the sludge channel 2b. It forms a flow path for slag.
又、銑滓分離容器2には溶滓流路方向に交差し
て溶銑返送樋5が設けてあり、かつ、返送樋5は
溶銑樋6に合流する。 Further, the slag separation vessel 2 is provided with a hot metal return gutter 5 that intersects with the slag flow path direction, and the return gutter 5 merges into the hot metal gutter 6.
次に、第3図及び第4図に基づいて、本装置を
より詳細に説明する。 Next, the present device will be explained in more detail based on FIGS. 3 and 4.
銑滓分離容器2は、例えば、鋼板で内壁に耐火
物19を内張りしてあり、溶滓下流側壁部に、定
位置排滓路2a、排銑時排滓路2bの2個の排滓
路をもつ。 The slag separation container 2 has an inner wall made of, for example, a steel plate lined with a refractory material 19, and has two slag drainage channels, a fixed position slag drainage channel 2a and a slag discharge channel 2b, on the downstream side wall of the slag. have.
また、傾動側に適宜角度を付した俯仰形成部2
dを設けており、俯仰形成部2dの先端下部に排
銑口2c、排銑樋2eを持つ。 In addition, the elevation forming part 2 is provided with an appropriate angle on the tilting side.
d, and has an iron exhaust port 2c and an iron exhaust trough 2e at the lower end of the elevation forming part 2d.
銑滓分離容器2は、円弧上の傾動フレーム11
の上に載置されている。 The slag separation container 2 has a tilting frame 11 on an arc.
is placed on top.
傾動フレーム11には複数個の傾動車輪11a
が取付けられており、走行台車14上部の円弧状
の傾動レール14aの上に回動自在に載置されて
いる。 The tilting frame 11 includes a plurality of tilting wheels 11a.
is attached and rotatably placed on the arc-shaped tilting rail 14a on the upper part of the traveling carriage 14.
また、傾動フレーム11下端に取付けられたピ
ンギヤ11bに傾動駆動装置13に連接したギヤ
ー12が係合されている。 Further, a gear 12 connected to a tilting drive device 13 is engaged with a pin gear 11b attached to the lower end of the tilting frame 11.
次に、走行台車14は複数個の走行車輪14b
を持ち、浮動フレーム15又は固定フレーム15
a上部の走行レール15c上に載置されている。 Next, the traveling truck 14 has a plurality of traveling wheels 14b.
with floating frame 15 or fixed frame 15
It is placed on the running rail 15c above a.
走行車輪14bの適当数がスプロケツトホイー
ル14cを連接しており、スプロケツトホイール
14cは走行駆動装置14fと連接したスプロケ
ツトホイール14eとローラチエン14dにより
係合されている。 A suitable number of running wheels 14b are connected to a sprocket wheel 14c which is engaged by a roller chain 14d to a sprocket wheel 14e connected to a running drive 14f.
また、浮動フレームは水平方向及び垂直方向の
移動が適宜量自在にロードセル16上に載置され
ており、リンク式の接続金具15bにより固定フ
レーム15aに連結されている。 Further, the floating frame is placed on the load cell 16 so as to be freely movable in the horizontal and vertical directions by an appropriate amount, and is connected to the fixed frame 15a by a link type connecting fitting 15b.
次に、上記の如く構成した装置を用い銑滓を分
離する場合について述べる。炉体1から排出され
た溶銑は大樋9に設けたスキンマー10によつて
溶銑と溶滓に分離される。このスキンマー10で
分離されに溶滓は、上流側溶滓樋1を流送して、
銑滓分離容器2に流入して、溶滓中の粒銑を銑滓
分離容器6の下部に沈降させた後に、定位置排滓
路2a又は排銑時排滓路2bを通つて、傾注樋行
滓樋3又は水砕行滓樋4に送られる。この際に、
銑滓分離容器2の底部に沈降した粒銑は集積され
て溶銑となり、この溶銑が適宜量になれば、傾動
フレーム11下部に取付けたピンギヤー11bと
ギヤー12を傾動駆動装置を介して作動すること
により、銑滓分離容器2の俯仰形成部2d側に第
7図、第8図の如く傾動して、排銑口2c、排銑
2eを介して、溶銑返送樋5に溶銑を流送して回
収する。排銑時では溶滓は排銑時排滓路2bを通
つて下流側滓樋へと流れる。 Next, a case will be described in which the apparatus configured as described above is used to separate pig iron slag. Hot metal discharged from the furnace body 1 is separated into hot metal and molten slag by a skimmer 10 provided in a large gutter 9. The slag separated by this skimmer 10 is sent through an upstream slag gutter 1,
After flowing into the slag separation vessel 2 and settling the granulated pig iron in the slag to the lower part of the slag separation vessel 6, it passes through the fixed position slag drainage path 2a or the slag drainage path 2b during iron removal, and then flows into the tilting trough. The slag is sent to the slag 3 or the slag 4. At this time,
The granular pig iron that has settled at the bottom of the pig iron slag separation vessel 2 is accumulated and becomes hot metal, and when this hot metal reaches a suitable amount, the pin gear 11b and gear 12 attached to the lower part of the tilting frame 11 are operated via the tilting drive device. As a result, the pig iron slag separation container 2 is tilted toward the elevation forming part 2d as shown in FIGS. to recover. At the time of pig iron removal, the slag flows to the downstream side slag trough through the slag discharge path 2b during pig iron removal.
銑滓分離容器2を傾動して溜つた溶銑を排出完
了後は、反転して銑滓分離容器2を定位置に戻
す。 After tilting the pig iron slag separation container 2 and discharging the accumulated hot metal, it is reversed and the pig iron slag separation container 2 is returned to its normal position.
次に、溶滓を流送する際の樋の切替機構につい
て述べる。走行台車14を走行駆動装置14fス
プロケツト14c,14e、ローラチエン14
d、走行車輪14bを介して走行移動されること
により、銑滓分離容器2の排容路2a又は2bの
落ち口を下流側の傾注樋行滓樋3、水砕行滓樋4
に選択的に合せることにより、樋の切替を行う。 Next, we will discuss the gutter switching mechanism used to transport slag. The traveling truck 14 is driven by a driving device 14f, sprockets 14c and 14e, and a roller chain 14.
d. By running and moving via the running wheels 14b, the outlet of the discharge channel 2a or 2b of the pig iron slag separation container 2 is moved to the downstream side of the tilting slag slag 3 and the granulated slag slag 4.
Gutter switching is performed by selectively adjusting to the
次に、第5〜8図により、銑滓分離容器6の作
動と上下滓樋、溶滓返送樋5の取合関係について
説明する。第5図は定位置で溶滓を水砕行樋4に
流送している状態を示し、第6図は定位置で溶滓
を傾注樋行滓樋3へ流送している状態を示す。第
7図は排銑時で、溶滓を水砕行滓樋4へ流送して
いる状態を示し、第8図は溶滓を傾注樋行滓樋4
へ流送している状態を示す。ここで、定位置にお
ける排滓流路2aと排銑時排滓流路2bの落ち口
の位置は略一致する。 Next, with reference to FIGS. 5 to 8, the operation of the slag separation vessel 6 and the connection between the upper and lower slag troughs and the slag return trough 5 will be explained. Figure 5 shows a state in which molten slag is being flowed to the slag gutter 4 in a fixed position, and Figure 6 shows a state in which molten slag is being flowed to a tilting trough and slag trough 3 in a fixed position. . Figure 7 shows the flow of molten slag to the water crushing slag trough 4 during pig iron removal, and Figure 8 shows the state in which the molten slag is transferred to the tilting slag trough 4.
Indicates the state of being transported to. Here, the positions of the outlets of the slag exhaust flow path 2a at the regular position and the outlet of the slag exhaust flow path 2b during pig iron removal substantially coincide.
即ち第5図において上流側滓樋1と排滓口2
a、又第7図において上流側滓樋1と排滓口2b
落ち口の各中心は略一致する。 That is, in Fig. 5, the upstream slag gutter 1 and the slag discharge port 2
a, and in Fig. 7, the upstream slag gutter 1 and the slag discharge port 2b
The centers of each droplet almost coincide.
また、第6図と第8図の距離○ハは略一致する。 Moreover, the distances ○ and C in FIG. 6 and FIG. 8 are approximately the same.
これは、定位置でも排銑時でも、下流側滓樋へ
流下する滓位置はほぼ等しいことを意味する。 This means that the position of the slag flowing down to the downstream slag trough is almost the same whether it is in a fixed position or during pig removal.
なお、排銑時排滓流路2bは、第2図に示す如
く上流側が傾動方向へ屈曲している。これは、定
位置で排滓流路2bから溶滓が流出しないためで
ある。 As shown in FIG. 2, the upstream side of the slag discharge channel 2b is bent in the tilting direction. This is because the slag does not flow out from the slag discharge channel 2b at the fixed position.
第5図において銑滓分離容器2の底面がなす角
○イと樋切替走行可能距離○ロの間には、相関関係が
ある。即ち、○イが大きい程度、○ロを大きく取るこ
とが出来る。周辺設備との取合条件にもよるが、
実機設備では○イが25〜35°程度、○ロが700〜800mm
程度である。 In FIG. 5, there is a correlation between the angle ○a formed by the bottom surface of the pig iron slag separation container 2 and the gutter switching travel distance ○b. In other words, the larger ○B is, the larger ○B can be taken. It depends on the terms of arrangement with the surrounding equipment, but
In actual equipment, ○A is approximately 25 to 35 degrees, and ○B is 700 to 800 mm.
That's about it.
なお、第3図に示すように複数個ロードセルは
浮動フレーム以上の荷重を支持している。これ
は、銑滓分離容器2内の溶銑量の増加をロードセ
ルにより検知し、排銑時期を的確に把握するため
である。 Note that, as shown in FIG. 3, the plurality of load cells support a load greater than that of the floating frame. This is to detect an increase in the amount of hot metal in the pig iron slag separation vessel 2 using the load cell and to accurately determine the time to discharge the pig iron.
以上述べたように、銑滓分離容器2は定位置又
は排銑時及び傾注樋行又は水砕樋行のどの状態で
あつても、上流側溶滓樋1から溶滓を銑滓分離容
器2に流入させ、溶滓中の粒銑を沈降させて後
に、排滓流路2a又は2bを通つて下流側滓樋3
又は4に流送出来るため、溶滓の連続処理が出来
る。 As described above, whether the slag separation container 2 is in the fixed position or when the pig iron is being discharged, and whether the slag is in the tilting trough or the water crushing trough, the slag is transferred from the upstream slag trough 1 to the slag separation container 2. After the slag flows into the slag and settles the granulated pig iron in the slag, it passes through the slag discharge channel 2a or 2b to the downstream slag trough 3.
Alternatively, the molten slag can be continuously processed because it can be sent to 4.
次に、銑滓分離容器2の取替について、第3図
に基づいて説明する。 Next, replacement of the pig iron slag separation container 2 will be explained based on FIG. 3.
銑滓分離容器2を取替える際には、ます、銑滓
分離容器2が、走行移動時、上流側溶滓樋1と干
渉しない様に、容器2を傾動させ、排銑時と同じ
状態にする。その後走行台車14を2′の状態に
し、銑滓分離容器2に吊り具17を取付け、鋳床
クレーンにて、容器2を2″のように吊り上げる。
2′,2″の状態では銑滓分離容器2が上流側滓樋
1を干渉することがないため簡単に吊り上げが出
来る。銑滓分離容器2を傾動フレーム11上にセ
ツトする時は、前記取外しの逆の動作を行う。 When replacing the pig iron slag separation container 2, first, tilt the container 2 so that it does not interfere with the upstream slag gutter 1 when moving, and bring it into the same state as when discharging pig iron. . Thereafter, the traveling truck 14 is placed in the 2' position, the hanging tool 17 is attached to the pig iron slag separation container 2, and the container 2 is lifted up to the 2'' position using a casting bed crane.
In the 2', 2'' state, the pig slag separation container 2 does not interfere with the upstream slag gutter 1, so it can be easily lifted.When setting the pig slag separation container 2 on the tilting frame 11, the above removal Perform the opposite operation.
(考案の効果)
以上のように本考案は溶滓を連続して処理する
ため溶滓中の粒銑を効率よく沈降分離して回収す
ると共に、前述のような溶滓粘性及び出滓量等の
影響をうけることも少ない。又、貯溜溶銑を溶滓
連続処理中に出銑できることから、銑滓分離容器
の容量は粒銑の沈降分離効果からのみ決めること
が出来、タツプ回数等に影響されない。そして前
記の高熱悪環境内での作業等を大巾に軽減させる
ことができる。(Effects of the invention) As described above, the present invention processes the slag continuously, so that the granular pig iron in the slag can be efficiently separated by sedimentation and recovered. It is less affected by. Furthermore, since the stored hot metal can be tapped during continuous slag processing, the capacity of the slag separation vessel can be determined only from the sedimentation separation effect of the granular pig iron, and is not affected by the number of taps or the like. Further, it is possible to greatly reduce the work required in the above-mentioned high heat and adverse environment.
又銑滓分離容器を走行して溶滓流路の切替を行
なうため、滓樋切替の入力作業が省略され、銑滓
分離容器取替時の移動をも機械化しているので出
銑時の鋳床作業の省力化に大きく寄与できるなど
の極めて優れた効果を有する。 In addition, since the slag flow path is switched by traveling through the slag separation vessel, the input work for switching the slag sluice is omitted, and the movement when replacing the slag separation vessel is also mechanized, so there is no need for casting during tapping. It has extremely excellent effects, such as greatly contributing to labor savings in floor work.
第1図は本考案による装置を設置した概略平面
図で、第2図は本装置の平面図、第3図は第2図
に於けるA−A断面矢視図、第4図は第1図、第
2図のB−B断面矢視図、第5〜第8図は本装置
の銑滓分離器の作動と上下滓樋、溶銑返送樋との
取合関係を示す図面で、第5図は定位置で溶滓を
水砕側へ流している図、第6図は定位置で溶滓を
傾注樋側へ流している図、第7図は排銑時で、溶
滓を水砕側へ流している図、第8図は排銑時で溶
滓を傾注樋側へ流している図である。
1……上流側溶滓樋、2……銑滓分離容器、2
a……定位置排滓路、2b……排銑時排滓路、2
c……排銑口、2d……俯仰形成部、2e……排
銑樋、2f……溶滓レベル、3……傾注樋行滓
樋、4……水砕行滓樋、5転溶銑返送樋、6……
溶銑樋、7……傾注樋、8……水砕製造設備、9
……大樋、10……スキンマー、11……傾動フ
レーム、11a……傾動車輪、11b……ピンギ
ヤー、12……ギヤー、13……傾動駆動装置、
14……走行台車、14a……傾動用レール、1
4b……走行車輪、14c及び14e……スプロ
ケツトホイール、14d……ローラチエン、14
f……走行駆動装置、15……浮動フレーム、1
5a……固定フレーム、15b……接続金具、1
5c……走行用レール、16……ロードセル、1
7……銑滓分離容器吊り具、18……炉体、19
……耐火物、2′……交換位置にある銑滓分離容
器、2″……吊り上げ状態の銑滓分離容器。
Fig. 1 is a schematic plan view of the device according to the present invention installed, Fig. 2 is a plan view of the device, Fig. 3 is a cross-sectional view taken along line A-A in Fig. 2, and Fig. 4 is a schematic plan view of the device according to the present invention. Figure 2 is a cross-sectional view taken along line B-B in Figure 2, and Figures 5 to 8 are drawings showing the operation of the pig iron slag separator of this device and the connection relationship between the upper and lower slag gutter and the hot metal return gutter. The figure shows the molten slag flowing to the fracking side in a fixed position, Figure 6 shows the molten slag flowing to the tilting trough side in a fixed position, and Figure 7 shows the molten slag flowing to the fracking side during iron removal. Figure 8 shows the molten slag flowing to the side of the tilting trough during iron removal. 1... Upstream slag gutter, 2... Pig slag separation container, 2
a...Fixed position slag drainage path, 2b...Slag removal path during iron removal, 2
c...Pigtail outlet, 2d...Elevation formation part, 2e...Pigtail discharge trough, 2f...Slag level, 3...Tilt slag trough, 4...Water slag trough, 5-turn molten pig iron return Gutter, 6...
Hot metal trough, 7...Tilting trough, 8...Water granulation manufacturing equipment, 9
...Gutter, 10...Skinmer, 11...Tilt frame, 11a...Tilt wheel, 11b...Pin gear, 12...Gear, 13...Tilt drive device,
14...Traveling trolley, 14a...Tilt rail, 1
4b... Traveling wheel, 14c and 14e... Sprocket wheel, 14d... Roller chain, 14
f... Traveling drive device, 15... Floating frame, 1
5a...Fixed frame, 15b...Connection fittings, 1
5c...Running rail, 16...Load cell, 1
7... Pig slag separation container hanging tool, 18... Furnace body, 19
...Refractories, 2'...Pigtail slag separation container in replacement position, 2''...Pigtail slag separation container in lifted state.
Claims (1)
炉溶滓の連続処理装置において、 下部側に排銑口を穿設し、上部側に溶滓流路方
向にむかつて複数の排滓路を形成した銑滓分離容
器を溶滓流路の中間部位に適宜段差をもつて配置
し、該銑滓分離容器を前記溶滓流路方向と交叉方
向に傾動、あるいは走行させるように構成したこ
とを特徴とする高炉溶滓の連続処理装置。[Scope of Claim for Utility Model Registration] In a continuous treatment device for blast furnace slag that collects granular pig iron in slag discharged from a blast furnace, an exhaust port is bored in the lower part and the slag flows in the direction of the upper part. A slag separation container, which previously formed a plurality of slag drainage channels, is placed in the middle of the slag flow path with an appropriate step difference, and the slag separation container is tilted in a direction perpendicular to the direction of the slag flow path. Alternatively, a continuous processing device for blast furnace slag is characterized in that it is configured to run.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP17396486U JPH0410207Y2 (en) | 1986-11-14 | 1986-11-14 |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP17396486U JPH0410207Y2 (en) | 1986-11-14 | 1986-11-14 |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6381844U JPS6381844U (en) | 1988-05-30 |
JPH0410207Y2 true JPH0410207Y2 (en) | 1992-03-13 |
Family
ID=31111921
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP17396486U Expired JPH0410207Y2 (en) | 1986-11-14 | 1986-11-14 |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0410207Y2 (en) |
-
1986
- 1986-11-14 JP JP17396486U patent/JPH0410207Y2/ja not_active Expired
Also Published As
Publication number | Publication date |
---|---|
JPS6381844U (en) | 1988-05-30 |
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