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JPS6037386B2 - Heat recovery device from molten slag - Google Patents
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JPS6037386B2 - Heat recovery device from molten slag - Google Patents

Heat recovery device from molten slag

Info

Publication number
JPS6037386B2
JPS6037386B2 JP54002064A JP206479A JPS6037386B2 JP S6037386 B2 JPS6037386 B2 JP S6037386B2 JP 54002064 A JP54002064 A JP 54002064A JP 206479 A JP206479 A JP 206479A JP S6037386 B2 JPS6037386 B2 JP S6037386B2
Authority
JP
Japan
Prior art keywords
trough
slag
cooling medium
stirring
shaft
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
Application number
JP54002064A
Other languages
Japanese (ja)
Other versions
JPS5594404A (en
Inventor
隆三 奥野
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.)
Kawasaki Heavy Industries Ltd
Original Assignee
Kawasaki Heavy 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 Kawasaki Heavy Industries Ltd filed Critical Kawasaki Heavy Industries Ltd
Priority to JP54002064A priority Critical patent/JPS6037386B2/en
Publication of JPS5594404A publication Critical patent/JPS5594404A/en
Publication of JPS6037386B2 publication Critical patent/JPS6037386B2/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B3/00General features in the manufacture of pig-iron
    • C21B3/04Recovery of by-products, e.g. slag
    • C21B3/06Treatment of liquid slag
    • C21B3/08Cooling slag
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B2400/00Treatment of slags originating from iron or steel processes
    • C21B2400/02Physical or chemical treatment of slags
    • C21B2400/022Methods of cooling or quenching molten slag
    • C21B2400/026Methods of cooling or quenching molten slag using air, inert gases or removable conductive bodies
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B2400/00Treatment of slags originating from iron or steel processes
    • C21B2400/02Physical or chemical treatment of slags
    • C21B2400/034Stirring or agitating by pressurised fluids or by moving apparatus
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B2400/00Treatment of slags originating from iron or steel processes
    • C21B2400/08Treatment of slags originating from iron or steel processes with energy recovery
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/25Process efficiency

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Manufacture Of Iron (AREA)
  • Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
  • Furnace Details (AREA)

Description

【発明の詳細な説明】 本発明は、溶融スラグからの熱回収装置に関する。[Detailed description of the invention] The present invention relates to an apparatus for recovering heat from molten slag.

従来から高炉や転炉などの製鋼設備から排出される高温
度の溶融スラグは、一般的にスラグピットなどで自然冷
却あるいは散水冷却した後、破砕されて埋立地に投棄さ
れており、溶スラグが保有する熱エネルギーが無駄に捨
てられていた。
Conventionally, high-temperature molten slag discharged from steelmaking equipment such as blast furnaces and converters is generally cooled naturally or with water spray in a slag pit, etc., and then crushed and dumped in a landfill. The retained thermal energy was wasted.

この技術的課題を解決する先行技術は、受皿の中に溶融
スラグを投入し、その溶融スラグに対向して受皿の上方
に伝熱管を配設し、溶融スラグから伝熱管への鏡射伝熱
によって高温度の蒸気を回収するとともに溶融スラグを
冷却するものである。この先行技術では、受皿に投入さ
れた溶融スラグは、その冷却時に、伝熱管に対向した溶
融スラグ表面付近のみが、急速に冷却されて固化する。
その理由は、溶融スラグの熱伝導率が極めて小さいため
に、溶融スラグ内部の冷却速度が溶融スラグ表面付近の
冷却速度に追随しないからである。そのため、溶融スラ
グ内部が高温度であるにもかかわらず、溶融スラグ表面
付近のみ温度が低下する現象が生じる。熔融スラグ表面
温度の低下によって伝熱管への鍵射伝熱量が低下し、溶
融スラグから有効に熱回収することが困難である。した
がって本発明の目的は、前述の技術的課題を解決して、
溶融スラグから有効に熱回収することができる熱回収装
置を提供することである。
The prior art to solve this technical problem is to charge molten slag into a saucer, arrange heat transfer tubes above the saucer to face the molten slag, and conduct mirror heat transfer from the molten slag to the heat transfer tubes. This system collects high-temperature steam and cools the molten slag. In this prior art, when the molten slag charged into the saucer is cooled, only the vicinity of the surface of the molten slag facing the heat transfer tube is rapidly cooled and solidified.
This is because the thermal conductivity of the molten slag is extremely low, so the cooling rate inside the molten slag does not follow the cooling rate near the surface of the molten slag. Therefore, although the temperature inside the molten slag is high, a phenomenon occurs in which the temperature decreases only near the surface of the molten slag. As the molten slag surface temperature decreases, the amount of radiant heat transferred to the heat transfer tube decreases, making it difficult to effectively recover heat from the molten slag. Therefore, an object of the present invention is to solve the above-mentioned technical problems and to
An object of the present invention is to provide a heat recovery device that can effectively recover heat from molten slag.

以下、図面によって本発明の実施例を説明する。第1図
は本発明の一実施例の一部を切欠いた平面図である。高
炉や転炉などから排出された高温度たとえば1500q
0程度の溶融スラグは、レール上を走行する鍋車2によ
って投入装置3の位置まで運搬され、鍋車2の鍋2aを
回動操作して、投入装置3の樋3aからトラフ4aの積
載部5に流下投入される。複数の独立したトラフ4aは
、水平面内で矩形状に配置され、トラフ駆動手段6a〜
6dによって矢符7a〜7dの橋方向に回転(移動)さ
れる。溶融スラグは、トラフ4aの回転とともに回転方
向7a〜7dに送られ、その顕熱を銭射伝熱によって後
述の伝熱12内の冷却媒体に与えて、冷却されてゆく。
そして溶融スラグは、縄枠装置24によって櫨拝されて
粒状の固形スラグとなり、排出装置44によってホツパ
45を経て回転トラフ4外に排出される。トラフ4aお
よび伝熱管12を覆うようにして炉殻8が設けられる。
Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is a partially cutaway plan view of an embodiment of the present invention. High temperature discharged from blast furnaces, converters, etc., e.g. 1500q
The molten slag of about 0 is transported to the position of the charging device 3 by the pot truck 2 running on the rails, and is transferred from the gutter 3a of the charging device 3 to the loading section of the trough 4a by rotating the pan 2a of the pan truck 2. 5 is poured into the stream. The plurality of independent troughs 4a are arranged in a rectangular shape in a horizontal plane, and the trough driving means 6a to
6d, it is rotated (moved) in the bridge direction of arrows 7a to 7d. The molten slag is sent in the rotational directions 7a to 7d as the trough 4a rotates, and is cooled by giving its sensible heat to a cooling medium in a heat transfer 12, which will be described later, by radiation heat transfer.
Then, the molten slag is crushed by the rope frame device 24 to become granular solid slag, and is discharged to the outside of the rotary trough 4 by the discharge device 44 via the hopper 45. A furnace shell 8 is provided to cover the trough 4a and the heat transfer tubes 12.

炉殻8の内壁には、その内壁全面にわたって伝熱管12
が設けれる。伝熱管12は、投入装置3も回転トラフ4
の回転方向7a〜7d前方で、トラフ4aの上方に配置
されている。伝熱管12は、トラフ4a〜4dをまたい
で鉛直面内で逆U字に延びる。伝熱管12の両端は第2
図のようにへッダ13,14に接続され、伝熱ユニット
15が構成される。伝熱ユニット15はトラフの移動方
向に複数方向に複数個設けられ、各伝熱ユニット15が
直列又は並列に接続されており、循環ポンプ又は給水ポ
ンプ等から冷却媒体が導入される。第2図は伝熱ユニッ
ト15が直列に接続された場合の例である。独立したト
ラフ4aはトラフ駆動手段6aによって矢符7aの方向
に移動され、次いでトラフ駆動手段6bによって矢符7
bの方向に移動される。
Heat exchanger tubes 12 are provided on the inner wall of the furnace shell 8 over the entire inner wall.
can be established. The heat exchanger tube 12 is connected to the charging device 3 as well as the rotating trough 4.
It is arranged above the trough 4a in front of the rotation direction 7a to 7d. The heat exchanger tubes 12 extend in an inverted U-shape in a vertical plane, straddling the troughs 4a to 4d. Both ends of the heat exchanger tube 12 are connected to the second
As shown in the figure, it is connected to headers 13 and 14 to constitute a heat transfer unit 15. A plurality of heat transfer units 15 are provided in a plurality of directions in the moving direction of the trough, and each heat transfer unit 15 is connected in series or in parallel, and a cooling medium is introduced from a circulation pump, a water supply pump, or the like. FIG. 2 shows an example in which heat transfer units 15 are connected in series. The independent trough 4a is moved in the direction of arrow 7a by trough drive means 6a and then in the direction of arrow 7 by trough drive means 6b.
is moved in the direction b.

これらトラフ4aの移動はたとえばチェーン駆動によっ
て行なわれる。本トラフ4aは二重台車構造となってい
て上部台車のみ7b方向の移動が可能となっている。7
c方向の移動はトラフ駆動手段6cによって行なわれる
These troughs 4a are moved, for example, by a chain drive. This trough 4a has a double truck structure, and only the upper truck can move in the direction 7b. 7
Movement in the c direction is performed by the trough drive means 6c.

この場合トラフ4aのみが移動する。7d方向へはトラ
フ駆動手段6dによってスラグ投入位置まで移動される
In this case, only the trough 4a moves. The slag is moved in the direction 7d to the slag charging position by the trough driving means 6d.

そして7b方向移動と同様上部台車のみで行なわれる。
没入装置3よりもトラフ4aの回転方向7a〜7c前方
で、回転トラフの周方向に間族をあげて複数の凝群装置
24が設けられる。
Similarly to the movement in the direction 7b, the movement is performed only by the upper carriage.
A plurality of agglomeration devices 24 are provided in front of the immersion device 3 in the rotational direction 7a to 7c of the trough 4a in the circumferential direction of the rotating trough.

蝿洋装層24は、トラフ4aの上方でトラフ4aの半径
方向に全幅にわたって延びて炉殻8の側壁を貫通し内部
に冷却媒体通路を有する軸部と、滋部の半径方向外方に
突出し軸部の軸線方向に間隔をあげて軸部と一体的に設
けられかつ藤都内に蓮適する冷却媒体通路27a,27
bを有する第3図〜第5図の縄梓突部28と、炉殻8の
外部に設けられ軸部をその軸線まわりに回転駆動する蝿
梓駆動手段と、冷却媒体通路27a,27bに冷却媒体
たとえば水を供給する冷却媒体供給手段とを備える。縄
梓突部28は、トラフ4aの積載部に侵入し効果的な鰻
洋が可能な長さを有する。麹部の冷却媒体通路および縄
梓突部28の冷却媒体通路27a,27bには、仕切管
31が内挿される。この仕切管31によって、冷却媒体
通路27は二重管状に仕切られて、内通路27aおよび
通路27bが形成される。仕切管31は縄梓突部28の
先端に向けて開□させており、内通路27aおよび外通
路27bが運速される。冷却媒体供給手段は、炉殻8の
外部で、回転管継手を介して軸部の内通路および外通路
に接続される給水管および排水管を備える。縄洋装層2
4は、トラフ4aの積載部5上に積載されたスラグを損
梓ないし破砕する。
The fly clothing layer 24 includes a shaft portion extending over the entire width in the radial direction of the trough 4a above the trough 4a, penetrating the side wall of the furnace shell 8, and having a cooling medium passage therein, and a shaft portion protruding outward in the radial direction of the drain portion. Cooling medium passages 27a, 27 are provided integrally with the shaft part at intervals in the axial direction of the part and are suitable for the inside of Fujito.
3 to 5, and a flywheel drive means provided outside the furnace shell 8 that rotates the shaft around its axis, and cooling medium passages 27a and 27b. A cooling medium supply means for supplying a medium such as water is provided. The rope protrusion 28 has a length that allows it to penetrate into the loading portion of the trough 4a and effectively eel. A partition pipe 31 is inserted into the coolant passage of the koji part and the coolant passages 27a and 27b of the rope ridge 28. The cooling medium passage 27 is partitioned into a double pipe shape by the partition pipe 31, forming an inner passage 27a and a passage 27b. The partition pipe 31 is opened toward the tip of the rope protrusion 28, and the inner passage 27a and the outer passage 27b are opened. The cooling medium supply means includes a water supply pipe and a drain pipe connected to the inner passage and the outer passage of the shaft portion through a rotary pipe joint outside the furnace shell 8. Western rope clothing layer 2
4 damages or crushes the slag loaded on the loading portion 5 of the trough 4a.

鯛洋装層24の蝿梓作用によって、溶融スラグ表面付近
と溶融スラグ内部とが礎拝されて、溶融スラグ表面付近
のみが急速に冷却されることを防止できる。そのため溶
融スラグから伝熱管12への頚射伝熱量が増大し効果的
な伝熱が行なわれる。また縄梓装置24の破砕作用によ
って、冷却固化したスラグが粒状に破砕される。冷却固
化したスラグは、回転トラフ4aの蝿洋装直24よりも
回転方向7a〜7c前方に設けられた排出装置44によ
って、トラフ4aから排出される。
The molten slag surface area and the interior of the molten slag are affected by the turbulent action of the sea bream coating layer 24, and it is possible to prevent only the molten slag surface area from being rapidly cooled. Therefore, the amount of radiation heat transferred from the molten slag to the heat transfer tube 12 increases, and effective heat transfer is performed. Further, the slag that has been cooled and solidified is crushed into particles by the crushing action of the rope slag device 24. The cooled and solidified slag is discharged from the trough 4a by a discharge device 44 provided ahead of the fly gear straight 24 of the rotary trough 4a in the rotation direction 7a to 7c.

糟洋装暦24の撹梓突部28は、その先端が敷捧45上
層部内に食込む長さを有するように構成することによっ
て、熔融スラグの全量が十分磯拝される。
By configuring the agitation protrusion 28 of the porcelain slag 24 so that its tip has a length that digs into the upper layer of the slag 45, the entire amount of molten slag is sufficiently absorbed.

そのため、溶融スラグがトラフ4aの内面に付着するこ
とを防止できる。排出装置44は敷盤上のスラグととも
に、敷蓬上層部の固形ススラグをも排出する。再び第1
図を参照して、投入装置3からトラフ4aの回転方向7
a〜7cに沿って、回転角範囲Aでは、高温度の溶融ス
ラグは流動状態である。
Therefore, it is possible to prevent molten slag from adhering to the inner surface of the trough 4a. The discharge device 44 discharges not only the slag on the bedding but also the solid slag in the upper layer of the bedding. 1st again
Referring to the figure, the rotation direction 7 of the trough 4a from the charging device 3
Along a to 7c, in rotation angle range A, the high temperature molten slag is in a fluid state.

次の回転角範囲Bでは、溶融スラグの流動状態から固形
状態への遷移城であって約1250〜1150ooの水
あめ状の高粘度状態である。最後の回転角範囲Cでは、
スラグは固形化されており、この範囲Cでは濃洋装暦2
4の瀦梓ないし破砕作用によってスラグは粒状となる。
回転角範囲AないしBにおいて、損杵装置24の擬伴突
部28の表面は、内通路27aから外題路27bに流れ
る水によって冷却されている。
In the next rotation angle range B, the molten slag is in a transition state from a fluid state to a solid state, and is in a starch syrup-like high viscosity state of about 1250 to 1150 oo. In the last rotation angle range C,
The slag is solidified, and in this range C, the
The slag becomes granular due to the grinding or crushing action in step 4.
In the rotation angle range A to B, the surface of the pseudo-protrusion part 28 of the punch-breaking device 24 is cooled by water flowing from the inner passage 27a to the outer passage 27b.

そのため、蝿梓突部28表面に接した溶融スラグは急冷
され、ガラス質状になって蝿洋突部28表面に第3図の
ごとく付着する。この付着したスラグ4川まガラス質で
あるので蝿枠突部28表面から剥離され易く、磯洋装瞳
24の駆動に障害となることはない。また付着スラグ4
0は健梓突部28の表面を保護する。なお、付着スラグ
40を蝿梓突部28表面から剥離し易くするために、蝿
梓突部28の表面は平滑面とする。回転角範囲Cにおい
て、粒状固化されたスラグの表面は、比較的大きな硬度
を有するので、この粒状スラグに接触する凝伴突部28
の表面が摩耗する恐れがある。
Therefore, the molten slag in contact with the surface of the fly ridge 28 is rapidly cooled, becomes glassy, and adheres to the surface of the fly ridge 28 as shown in FIG. 3. Since the adhered slag is glassy, it is easily peeled off from the surface of the fly frame protrusion 28, and does not interfere with the driving of the Iso-Western pupil 24. Also, attached slag 4
0 protects the surface of the protrusion 28. Incidentally, in order to make it easier to peel off the adhered slag 40 from the surface of the fly-cattle protrusion 28, the surface of the fly-cattle protrusion 28 is made to be a smooth surface. In the rotation angle range C, the surface of the granular solidified slag has a relatively high hardness, so the coagulation protrusion 28 that contacts the granular slag
There is a risk of surface wear.

そのため鶴梓突部28の外周表面に、第4図および第5
図のごとく円柱状の丸榛保護部材43を固着する。保護
部材41は、耐摩耗性材料たとえば高マンガン鋼で形成
される。保護部材43は、縄梓突部28の長手方向に沿
い、その鞠直角断面は円形であるので、縄杵突部28と
の溶接のための関先が形成されることになり、溶接作業
を容易に行なうことができる。なお、高炉から排出され
る溶融スラグと転炉から排出される溶融スラグとでは、
固形化する温度が異なるので、これらの処理すべき溶融
スラグに応じて回転角範囲Cが異なり、この範囲C内に
設けられる澄洋装層24の蝿梓突部28に保護部材43
を取付ける必要がある。
Therefore, on the outer circumferential surface of the crane azusa protrusion 28, as shown in FIGS.
As shown in the figure, a cylindrical round protection member 43 is fixed. The protective member 41 is made of a wear-resistant material, such as high manganese steel. Since the protective member 43 runs along the longitudinal direction of the rope punch projection 28 and has a circular cross section at right angles to the ball, a joint for welding with the rope punch projection 28 is formed, making the welding work easier. It can be done easily. In addition, molten slag discharged from a blast furnace and molten slag discharged from a converter are
Since the solidification temperature differs, the rotation angle range C differs depending on the molten slag to be treated, and the protection member 43 is attached to the flywheel protrusion 28 of the clearing layer 24 provided within this range C.
need to be installed.

回転角範囲AないしB‘こおける蝿伴装置24の冷却媒
体通路25,27には、冷却媒体として水か又は比較的
温度の低いたとえば飽和水又はポィラ水を供給すること
が好ましく、こうして溶融スラグと冷却媒体との温度差
を比較的大きくとれば、頚射伝熱量を増大させることが
できる。
The cooling medium passages 25 and 27 of the fly trap device 24 in the rotation angle range A to B' are preferably supplied with water as a cooling medium, or with relatively low temperature, for example, saturated water or boiled water, so that the molten slag By making a relatively large temperature difference between the cooling medium and the cooling medium, the amount of radiation heat transfer can be increased.

なお、高炉から排出される溶融スラグと転炉から排出さ
れる溶融スラグとでは、固形化する温度が異なるので、
これらの処理すべき溶融スラグに応じて回転角範囲Cが
異なり、この範囲C内に設けられる蝿洋装暦24の蝿梓
突部28に保護部材43を取付ける必要がある。回転角
範囲AないしBにおける凝洋装層24の冷却媒体通路2
5,27には、冷却媒体として水か又は比較的温度の低
いたとえば飽和水又はボイラを供給することが好ましく
、こうして溶融スラグと冷却媒体との温度差を比較的大
きくとれば、頚射伝熱量を増大させることができる。
Furthermore, since the solidification temperature of molten slag discharged from a blast furnace and molten slag discharged from a converter is different,
The rotation angle range C varies depending on the molten slag to be treated, and it is necessary to attach the protection member 43 to the fly azure protrusion 28 of the fly calendar 24 provided within this range C. Cooling medium passage 2 of the condenser layer 24 in the rotation angle range A to B
5 and 27, it is preferable to supply water or relatively low temperature saturated water or a boiler as a cooling medium.If the temperature difference between the molten slag and the cooling medium is made relatively large in this way, the amount of radiation heat transfer can be reduced. can be increased.

上述のごとく本発明によれば、トラフ駆動手段によって
駆動されるトラフに、投入装置によって溶融スラグを投
入し、トラフ上方に配置された伝熱管にスラグから頬射
伝熱を行なわせるようにしたので、本件熱回収装置は熔
融スラグを連続的に冷却、凝固、縄拝、粉砕して粒状化
処理をすることができる。
As described above, according to the present invention, the molten slag is charged by the charging device into the trough driven by the trough driving means, and the slag is caused to transfer heat from the slag to the heat transfer tube disposed above the trough. The heat recovery equipment of the present invention is capable of continuously cooling, solidifying, pulverizing, and pulverizing molten slag into granules.

またトラフの積載部に積載されたスラグの表面付近とス
ラグ内部とは、縄洋装層によって十分蝿拝されるので、
スラグ表面付近のみが急速に冷却されることを防止でき
、したがって伝熱管への韓射伝熱量を増大させることが
できる。しかも縄洋装直によって、溶融スラグを取扱い
の容易な粒状固形スラグとして取出すことができる。さ
らに縄梓装置の冷却媒体通路に冷却媒体を導入して蝿梓
突部を冷却するようにしたので、蝿梓突部の過熱を防止
できるとともに、冷却媒体が加熱されて熱回収量を増加
させることもできる。各トラフが独立しているため、ト
ラフの回転により、例えばホツパー内に排出することが
でき、排出装置を簡略化することができる。また、スペ
ース的に制約をうける場合には、特にコンパクトなしィ
ァゥトが可能になる。トラフは、独立しているので、保
守交換が容易である。
In addition, the vicinity of the surface of the slag loaded in the loading section of the trough and the inside of the slag are sufficiently covered by the rope layer, so
It is possible to prevent only the vicinity of the slag surface from being rapidly cooled, and therefore the amount of heat transferred to the heat transfer tube can be increased. Furthermore, the molten slag can be taken out as granular solid slag that is easy to handle. Furthermore, since a cooling medium is introduced into the cooling medium passage of the rope azusa device to cool the fly azure protrusion, it is possible to prevent the fly azure protrusion from overheating, and the cooling medium is heated to increase the amount of heat recovery. You can also do that. Since each trough is independent, the material can be discharged, for example, into a hopper by rotating the trough, and the discharge device can be simplified. In addition, especially when space is limited, a compact layout becomes possible. Since the trough is independent, maintenance and replacement are easy.

このトラフは、水平面内で矩形に移動可能であるので、
トラフを駆動するための手段の構成を簡略化することが
できる。スラグが流動状態にある範囲では、鷹梓突部の
外周は円滑であり、したがってスラグが蝿梓突部から離
脱しやすく、鷹梓突部にむやみに多量のスャグが付着し
てしまうことが防がれる。
This trough can be moved rectangularly in the horizontal plane, so
The configuration of the means for driving the trough can be simplified. In the range where the slag is in a fluid state, the outer periphery of the slag protrusion is smooth, and therefore the slag easily separates from the slag protrusion, preventing unnecessary amounts of sag from adhering to the slag protrusion. I can escape.

スラグが固形状態になる範囲では、保護部材が灘梓突部
の長手方向に沿って固着してあるので、スラグを充分に
損拝することが容易になるとともに、保護部材を櫨梓突
部との熱膨張による熱応力が緩和され、両者の変形およ
びクラックの発生が防がれる。
In the range where the slag is in a solid state, the protective member is fixed along the longitudinal direction of the Nada-azusu projection, so it is easy to sufficiently damage the slag, and the protective member is attached to the Nada-azusu projection. Thermal stress due to thermal expansion is alleviated, preventing deformation and cracking of both.

このことは特に、蝿梓突部に冷却媒体が通過される構成
になっており、この冷却媒体がスラグ中に漏出すること
を防ぐのに役立つ。しかもまた円柱状の保護部材と縄梓
部材の表面とによって溶接時の関先に通した空間が形成
され、溶接作業を容易に行なうことができる。
This especially serves to prevent the cooling medium from leaking into the slag, as the cooling medium is passed through the fly ridge. In addition, the cylindrical protection member and the surface of the rope rope member form a space through which the joint during welding can be passed, making it possible to easily perform the welding work.

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

第1図は本発明の一実施例の一部切欠き平面図、第2図
はトラフ4aの周方向への伝熱管12の簡略化した展開
図、第3図は範囲AないしB‘こおける麓梓突部28付
近の正面図、第4図は範囲Cにおける蝿梓突部28付近
の正面図、第5図は第4図のK−K線視断面図である。 3・・・・・・投入装置、4a・・・・・・トラフ、5
・・・・・・積載部、6a,6b,6c,6d…・・・
トラフ駆動手段、7a,7b,7c,7d・・・・・・
移動方向、8・・・…炉殻、12・・・・・・伝達管、
24・・・・・・蝿枠装置、27・・・・・・冷却媒体
通路、27a…・・・内通路、27b……外道路、28
……縄杵突部、31・・・・・・仕切管、44・…・・
排出装置、43・・・・・・保護部材。第2図第3図 第4図 第5図 第1図
Fig. 1 is a partially cutaway plan view of an embodiment of the present invention, Fig. 2 is a simplified developed view of the heat exchanger tubes 12 in the circumferential direction of the trough 4a, and Fig. 3 is a diagram showing the area A to B'. FIG. 4 is a front view of the vicinity of the foot azure protrusion 28, FIG. 4 is a front view of the vicinity of the foot azure protrusion 28 in range C, and FIG. 5 is a sectional view taken along the line KK in FIG. 3... Input device, 4a... Trough, 5
...Loading section, 6a, 6b, 6c, 6d...
Trough drive means, 7a, 7b, 7c, 7d...
Movement direction, 8...furnace shell, 12...transmission pipe,
24...Fly frame device, 27...Cooling medium passage, 27a...Inner passage, 27b...Outer road, 28
...Rope punch protrusion, 31...Partition pipe, 44...
Ejection device, 43... protection member. Figure 2 Figure 3 Figure 4 Figure 5 Figure 1

Claims (1)

【特許請求の範囲】 1 水平面内で矩形状に移動可能な複数の独立したトラ
フ、 前記トラフを駆動するトラフ駆動手段、 前記ト
ラフに溶融スラグを投入する投入装置、 前記投入装置
よりもトラフの移動方向前方でトラフ上方に配置された
伝熱管、 前記トラフおよび伝熱管を覆う炉殻、 トラフの上方でトラフの移動方向に直角な方向に全幅
にわたつて延びて殻数の側壁を貫通し内部に冷却媒体通
路を有する軸部、軸部の半径方向外方に突出しトラフの
積載部に侵入しうる長さを有し軸部と一体的に設けられ
かつ軸部内の前記冷却媒体通路と連通した冷却媒体通路
を有する撹拌突部、炉殻の外部に設けられ軸部をその軸
線まわりに回転駆動する撹拌駆動手段、および前記冷却
媒体通路に冷却媒体を供給する手段を備え、投入装置よ
りもトラフの移動方向前方でトラフの移動方向に間隔を
あげて設えられスラグを撹拌して伝熱管への輻射伝熱量
を増加させるための複数の撹拌装置、ならびに トラフ
の撹拌装置よりも移動方向前方に設けられ前記トラフか
らスラグを排出する排出装置を含み、 軸部と撹拌突部
との冷却媒体通路に内挿されかつ撹拌突部の先端に向け
て開口した仕切管によつて、軸部と撹拌突部とを二重管
状にそれぞれ仕切り、その二重管状通路の内または外の
いずれか一方通路に冷却媒体供給手段からの冷却媒体を
供給し、二重管状の内または外のいずれか他方通路から
排出し、 トルフに積載されたスラグが流動状態にある
トラフの移動方向範囲では撹拌突部の外周は円滑であり
、 トラフに積載されたスラグが固形状態になるトラフ
の移動方向範囲に配置された撹拌装置の前記撹拌突部の
外周に耐摩耗材料から成る円柱状の保護部材を撹拌突部
の長手方向に沿つて固着したことを特徴とする溶融スラ
グからの熱回収装置。
[Scope of Claims] 1. A plurality of independent troughs movable in a rectangular shape within a horizontal plane, trough driving means for driving the troughs, a charging device for charging molten slag into the trough, and movement of the troughs relative to the charging device. heat exchanger tubes disposed above the trough in the forward direction; a furnace shell covering the trough and the heat exchanger tubes; a shaft having a cooling medium passage; a cooling member that projects radially outward from the shaft and has a length that allows it to enter the loading area of the trough, is provided integrally with the shaft and communicates with the cooling medium passage within the shaft; It is equipped with a stirring protrusion having a medium passage, a stirring driving means provided outside the furnace shell for rotating a shaft part around its axis, and a means for supplying a cooling medium to the cooling medium passage, A plurality of stirring devices are provided at intervals in the direction of movement of the trough in front of the trough in order to stir the slag and increase the amount of radiant heat transferred to the heat transfer tube, and a plurality of stirring devices are provided in front of the stirring device of the trough in the direction of movement. The trough includes a discharge device for discharging slag from the trough, and a partition pipe inserted into a cooling medium passage between the shaft and the stirring protrusion and opening toward the tip of the stirring protrusion allows the shaft and the stirring protrusion to be separated. and are each partitioned into a double tubular shape, the cooling medium from the cooling medium supply means is supplied to either the inside or outside of the double tubular passage, and the cooling medium is discharged from either the inside or outside of the double tubular passage. However, the outer periphery of the stirring protrusion is smooth in the range of the trough movement direction where the slag loaded on the trough is in a fluid state, and the stirring protrusion is smooth in the range of the trough movement direction where the slag loaded on the trough is in a solid state. A heat recovery device from molten slag, characterized in that a cylindrical protection member made of a wear-resistant material is fixed to the outer periphery of the stirring projection of the device along the longitudinal direction of the stirring projection.
JP54002064A 1979-01-10 1979-01-10 Heat recovery device from molten slag Expired JPS6037386B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP54002064A JPS6037386B2 (en) 1979-01-10 1979-01-10 Heat recovery device from molten slag

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP54002064A JPS6037386B2 (en) 1979-01-10 1979-01-10 Heat recovery device from molten slag

Publications (2)

Publication Number Publication Date
JPS5594404A JPS5594404A (en) 1980-07-17
JPS6037386B2 true JPS6037386B2 (en) 1985-08-26

Family

ID=11518905

Family Applications (1)

Application Number Title Priority Date Filing Date
JP54002064A Expired JPS6037386B2 (en) 1979-01-10 1979-01-10 Heat recovery device from molten slag

Country Status (1)

Country Link
JP (1) JPS6037386B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102564139A (en) * 2012-03-16 2012-07-11 中国恩菲工程技术有限公司 Feeding port device for metallurgical furnace
CN104515119A (en) * 2014-10-12 2015-04-15 王志凯 High-temperature liquid slag heat energy recovery device

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102564139A (en) * 2012-03-16 2012-07-11 中国恩菲工程技术有限公司 Feeding port device for metallurgical furnace
CN104515119A (en) * 2014-10-12 2015-04-15 王志凯 High-temperature liquid slag heat energy recovery device

Also Published As

Publication number Publication date
JPS5594404A (en) 1980-07-17

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