JPS633645B2 - - Google Patents

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Publication number
JPS633645B2
JPS633645B2 JP56009652A JP965281A JPS633645B2 JP S633645 B2 JPS633645 B2 JP S633645B2 JP 56009652 A JP56009652 A JP 56009652A JP 965281 A JP965281 A JP 965281A JP S633645 B2 JPS633645 B2 JP S633645B2
Authority
JP
Japan
Prior art keywords
water
dome
collection
pit
guide plate
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
JP56009652A
Other languages
Japanese (ja)
Other versions
JPS57127434A (en
Inventor
Yukio Takahashi
Rokuro Komagine
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 JP965281A priority Critical patent/JPS57127434A/en
Publication of JPS57127434A publication Critical patent/JPS57127434A/en
Publication of JPS633645B2 publication Critical patent/JPS633645B2/ja
Granted legal-status Critical Current

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  • Curing Cements, Concrete, And Artificial Stone (AREA)
  • Manufacture Of Iron (AREA)
  • Furnace Details (AREA)
  • Glanulating (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は水砕製造設備に関するものである。 高炉より出滓した溶融スラグを原料として水砕
を製造することは既知である。この製造方式の一
つに、例えば第1図に示すものがある。 即ち溶滓鍋1を転回して溶融スラグ2を溶滓処
理シユート3を介して回転ドラム4へ供給し、飛
散させる。これによつて粒状化したスラグ(水
砕)5は、捕集ピツト6の冷却水中へ落下し、冷
却されて水砕となる。 なお7は粒状化スラグ(以下水砕という)を回
収し搬送するためのコンベア、8は貯蔵ホツパ
ー、9は飛散する粒状化スラグ5を捕集するため
の捕集ドーム、10は冷却水を貯留清浄化するた
めの循環ピツトである。 しかしこの水砕製造設備では、捕集ドーム9の
雰囲気温度および/または冷却水の温度が上昇す
るため、冷却能が適正に維持され難く、水砕の品
質を悪くし、スラグと水蒸気が反応して生成する
硫化水素の発生量が増大する問題があつた。 この冷却水の温度上昇は、該冷却水を循環使用
する方式を採用しなければならない以上、回避で
きないものである。すなわち冷却水には、粒状化
スラグ5より溶出するイオウ化合物、アルカリ等
のため直接系外へ排出することは環境上、問題発
生の要因となる。従つて必ず循環ピツト10へ順
次流出させ、これらのピツトの系の中で冷却水
が、循環使用させるように水砕製造設備は構成さ
れているのである。 このため上記問題点の他に長期に亘る使用にお
いて、捕集ドーム9は変形をきたし、熱損傷を起
す場合もある。 さらに捕集ピツト6の冷却水の水位は、ガイド
板の内側(コンベア7のある方)と、外側との水
位バランスがとり難く、これが原因となつて粒状
化スラグ(水砕)5がコンベア7より流出(漏
出)し、捕集ピツト6へ堆積してコンベア7の稼
働を停止させる操業上致命的欠点を有する。 またこれによつて水砕の製造歩留の低下、捕集
ピツト内の冷却水温度の適正管理ができなくなる
問題もある。 本発明は上記問題を解決する目的で、回転ドラ
ムの前方の捕集ピツトを包囲する如く捕集ドーム
を設け、該ドームの天井および/または側壁方向
へ指向する散水ノズルを配設し、該ドームの側壁
の下端をコンベア方向へ傾斜し水位調整口を有す
るガイド板に形成すると共に、該ガイド板へ指向
する散水ノズルを配設し、且つ上記側壁の鉛直方
向へ開口するスリツト状の通気孔を複数列設けて
構成したことを特徴とする水砕製造設備を提供せ
んとするものである。 以下本発明の実施例を図面について説明する。 第2図は平面図、第3図は第2図のA−A矢視
図、第4図は第3図のB−B矢視図、第5図は第
2図のC−C矢視図、第6図は要部拡大説明図で
ある。 図において1は溶滓鍋、3は溶滓処理シユー
ト、4は回転ドラム、6は捕集ピツト、7はコン
ベア、8は貯蔵ホツパー、12は沈澱処理ピツ
ト、13は開溝で、沈澱処理ピツト12へ捕集ピ
ツト6より使用済みの冷却水を導くためのもので
ある。沈澱処理ピツト12は若干深く構成されて
おり、冷却水に含有されてくる粉塵その他を清浄
化する。14は沈澱処理ピツト12に引続く循環
ピツトであり、清浄になつた冷却水を貯留する。
15は循環ポンプで、循環ピツト14の清浄化さ
れている冷却水を供給するためのものであり、1
6は冷却水導管である。9は捕集ドームであり、
排気孔17を有し、概ね捕集ピツト6を包囲する
如く配設されている。 捕集ドームは第4図に示すように密閉状で、底
部を捕集ピツト6に浸漬され、開口域30が形成
され、開口域30にコンベア7が付設されてい
る。又捕集ドーム9の側壁19にガイド板22が
連設される。 捕集ドーム9は、天井18および/または側壁
19の方向へ指向する散水ノズル20を配設し、
且つ側壁19にはスリツト状の通気孔21を複数
列設けている。これによつて循環ポンプ15より
供給される冷却水は、冷却水導管16を経由し
て、散水ノズル20より天井18および/または
側壁19の稼働面に水膜を形成しつつ稼働面を濡
らし捕集ピツト6に至る。 上記冷却水が側壁19の稼働面に水膜を形成し
ているとき、複数列のスリツト状の通気孔21
は、大気を通過させているので、これにより冷却
水は適正温度に維持されつつ捕集ピツト6へ至
る。これに基づき、冷却水の冷却能は常に維持さ
れるので、品質のよい水砕を製造することができ
る。 また回転ドラム4により飛散する粒状化スラグ
5−1は天井18、側壁19に付着しても、水膜
を形成しつつ流れる冷却水に洗われて、捕集ピツ
ト6へ容易に捕集できる。さらに捕集ドーム9の
側壁19に複数列設けたスリツト状の通気孔21
は、捕集ドーム9内の大気の通過を図り、排気孔
17は捕集ドーム9内の雰囲気を大気へ排気す
る。 これによつて捕集ドーム9内の雰囲気温度は、
目標温度に維持することができ、冷却水の昇温を
防止することもできる。 22は水砕をコンベア7へ導く役目を果すガイ
ド板で、捕集ドーム9の側壁19の下端より、コ
ンベア7方向へ傾斜している。而してガイド板2
2の適正位置には、水位調整口23を設け、また
ガイド板22へ指向する散水ノズル20−2を配
設している。上記水位調整口23は特に構成上の
制約はなく、例えば第6図に拡大図示する構造の
ものでもよい。図中24は水砕漏出抑制板、25
は取付部材、26は冷却水流出入口を示す。 このようにガイド板22は、コンベア7の方向
へ傾斜し且つ該ガイド板22へ指向する散水ノズ
ル20−2を配設しているので、水砕5−2をコ
ンベア7へ容易に導くことができ捕集率を向上で
きる。またガイド板22の適正位置には、水位調
整口23を設けているので、第5図に例示するガ
イド板22の内側(コンベア7が存在する方)の
水位Hと外側の水位hとを選択的にH=h、H<
h又はH>hに調整できる。 即ち、H=hの場合はH及びh部の水圧バラン
スがとれているため捕集ビツトへのスラグ流出が
ない。H<hの場合はh部の水圧が大となり、冷
却水がH部の方へ流れるため、第5図l部からの
スラグ流出は起らない。又H>hの場合は第2図
に示す如く、H部の水圧が大となり、冷却水がh
部の方へ流れるため、l部からのスラグ流出が発
生する。 このことから通常操業においては、H=h又は
H<hの方向に水位を調整することにより、ガイ
ド板22とコンベア7との間隔lより漏出(流
出)するのを抑制でき、コンベア7の直下や近傍
に堆積してコンベア7の稼働停止を起すことはな
く、また捕集率も向上できる。 上述の水位Hと水位hを適正に調整するには、
例えばガイド板22に複数設けた水位調整口23
を適宜開度調整し、又は閉塞することで対処でき
る。 さてこの水砕製造設備30によつて水砕を製造
するには次のように行う。 溶滓鍋1を転回して溶融スラグ2を溶滓処理シ
ユート3へ展開しつつ回転ドラム4へ導き飛散さ
せる。これによつて粒状化されつつ捕集ドーム9
内へ飛散し、一部は捕集ピツト6の水中へ落下
し、他の一部は捕集ドーム9の天井18、側壁1
9へ飛散し付着するが、既述の如く冷却能を維持
された冷却水で洗い流されて、捕集ピツト6の水
中へ落下し冷却される。特にガイド板22へ指向
させた散水ノズル20−2は、粒状スラグ5をコ
ンベア7へ導き捕集を容易にする。コンベア7は
水中に滞在する水砕5−2を貯蔵ホツパー8へ搬
送し水砕製品とする。 捕集ピツト6の冷却水は、開溝13を通り、沈
澱処理ピツト12へ至り、清浄化された冷却水
は、循環ピツト14へ流れ、順次上述の系内で循
環使用される。このとき捕集ドーム9内は、スリ
ツト状の通気孔21、排気孔17、散水ノズル2
0による天井18および/または側壁19の冷却
水による水膜形成などの相互作用により雰囲気温
度は適正に維持されているので、捕集ピツト6も
冷却水温度は適正に維持されることになり、水砕
の品質向上に寄与する。 以上の如く本発明は、回転ドラム4と捕集ピツ
ト6を概ね包囲する如く捕集ドーム9を設け、該
ドーム9の天井18および/または側壁19の方
向へ指向する散水ノズル20を配設し、該ドーム
9の側壁19の下端をコンベア7の方向へ傾斜
し、水位調整口23を有するガイド板22に形成
すると共に、該ガイド板22へ指向する散水ノズ
ル20−2を配設し、且つ上記側壁19の鉛直方
向へ開口するスリツト状の通気孔21を複数列設
けて構成したことにより、次の第1表に示す効果
が得られる。
The present invention relates to granulation manufacturing equipment. It is known to produce granulated water using molten slag from a blast furnace as a raw material. One of these manufacturing methods is shown in FIG. 1, for example. That is, the slag ladle 1 is rotated to supply the molten slag 2 to the rotating drum 4 via the slag treatment chute 3 and scatter it. The slag (crushed water) 5 thus granulated falls into the cooling water of the collection pit 6, is cooled, and becomes granulated water. In addition, 7 is a conveyor for collecting and conveying granulated slag (hereinafter referred to as granulated slag), 8 is a storage hopper, 9 is a collection dome for collecting the scattered granulated slag 5, and 10 is a storage for cooling water. This is a circulation pit for cleaning. However, in this granulated water production equipment, the atmospheric temperature of the collection dome 9 and/or the temperature of the cooling water rises, making it difficult to maintain proper cooling capacity, which deteriorates the quality of the granulated water and causes the slag and steam to react. There was a problem in that the amount of hydrogen sulfide generated increased. This increase in the temperature of the cooling water cannot be avoided as long as a method of circulating the cooling water has to be adopted. That is, since the cooling water contains sulfur compounds, alkalis, etc. eluted from the granulated slag 5, direct discharge to the outside of the system may cause environmental problems. Therefore, the granulation production equipment is constructed so that the cooling water is always flowed sequentially into the circulation pits 10 and is circulated within the system of these pits. For this reason, in addition to the above-mentioned problems, the collection dome 9 may become deformed and thermally damaged during long-term use. Furthermore, the water level of the cooling water in the collection pit 6 is difficult to balance between the inside of the guide plate (the side where the conveyor 7 is located) and the outside, and this causes the granulated slag (crushed water) 5 to be transferred to the conveyor 7. This has a fatal drawback in terms of operation, as it flows out (leaks) and accumulates in the collection pit 6, causing the conveyor 7 to stop operating. This also causes problems such as a decrease in the production yield of granulated water and an inability to properly control the temperature of the cooling water in the collection pit. In order to solve the above problems, the present invention provides a collection dome so as to surround the collection pit in front of the rotating drum, and provides a water spray nozzle directed toward the ceiling and/or side wall of the dome. The lower end of the side wall is formed into a guide plate that is inclined toward the conveyor and has a water level adjustment port, and a water spray nozzle directed toward the guide plate is disposed, and a slit-shaped ventilation hole that opens in the vertical direction of the side wall is provided. It is an object of the present invention to provide a water granulation manufacturing equipment characterized by having a plurality of rows. Embodiments of the present invention will be described below with reference to the drawings. Fig. 2 is a plan view, Fig. 3 is a view taken along the line A-A in Fig. 2, Fig. 4 is a view taken along the line B-B in Fig. 3, and Fig. 5 is a view taken along the line C-C in Fig. 2. 6 are enlarged explanatory views of main parts. In the figure, 1 is a slag pan, 3 is a slag processing chute, 4 is a rotating drum, 6 is a collection pit, 7 is a conveyor, 8 is a storage hopper, 12 is a sedimentation treatment pit, 13 is an open groove, and is a sedimentation treatment pit. This is for guiding used cooling water from the collection pit 6 to 12. The settling pit 12 is constructed to be somewhat deep and cleans dust and other particles contained in the cooling water. Reference numeral 14 denotes a circulation pit following the precipitation treatment pit 12, and stores purified cooling water.
15 is a circulation pump for supplying purified cooling water to the circulation pit 14;
6 is a cooling water conduit. 9 is a collection dome;
It has an exhaust hole 17 and is arranged so as to generally surround the collection pit 6. As shown in FIG. 4, the collecting dome has a closed shape, the bottom part of which is immersed in a collecting pit 6, an open area 30 is formed, and a conveyor 7 is attached to the open area 30. Further, a guide plate 22 is provided continuously on the side wall 19 of the collection dome 9. The collection dome 9 is provided with a water spray nozzle 20 directed toward the ceiling 18 and/or side wall 19,
In addition, a plurality of rows of slit-shaped ventilation holes 21 are provided in the side wall 19. As a result, the cooling water supplied from the circulation pump 15 passes through the cooling water conduit 16 and from the water spray nozzle 20 forms a water film on the working surface of the ceiling 18 and/or side wall 19, wetting the working surface and capturing it. It reaches the collection pit 6. When the cooling water forms a water film on the working surface of the side wall 19, a plurality of rows of slit-shaped ventilation holes 21
Since the cooling water is passed through the atmosphere, the cooling water reaches the collection pit 6 while being maintained at an appropriate temperature. Based on this, the cooling ability of the cooling water is always maintained, so that high-quality granulated water can be produced. Further, even if the granulated slag 5-1 scattered by the rotating drum 4 adheres to the ceiling 18 and side walls 19, it is washed away by the flowing cooling water while forming a water film, and can be easily collected in the collecting pit 6. Furthermore, multiple rows of slit-shaped ventilation holes 21 are provided in the side wall 19 of the collection dome 9.
The exhaust hole 17 allows the atmosphere inside the collection dome 9 to pass through, and the exhaust hole 17 exhausts the atmosphere inside the collection dome 9 to the atmosphere. As a result, the atmospheric temperature inside the collection dome 9 is
It is possible to maintain the target temperature and also prevent the temperature of the cooling water from rising. Reference numeral 22 denotes a guide plate that serves to guide the crushed water to the conveyor 7, and is inclined toward the conveyor 7 from the lower end of the side wall 19 of the collection dome 9. Then guide plate 2
A water level adjustment port 23 is provided at the appropriate position of No. 2, and a water spray nozzle 20-2 directed toward the guide plate 22 is provided. There are no particular restrictions on the structure of the water level adjustment port 23, and it may have the structure shown in an enlarged view in FIG. 6, for example. In the figure, 24 is a granulated water leakage suppression plate, 25
26 indicates a mounting member, and 26 indicates a cooling water inlet. In this way, the guide plate 22 is inclined in the direction of the conveyor 7 and has the water nozzle 20-2 directed toward the guide plate 22, so that the granulated water 5-2 can be easily guided to the conveyor 7. It is possible to improve the collection rate. In addition, since the water level adjustment port 23 is provided at the appropriate position of the guide plate 22, the water level H on the inside (the side where the conveyor 7 is present) and the water level h on the outside of the guide plate 22 illustrated in FIG. 5 are selected. H=h, H<
It can be adjusted to h or H>h. That is, when H=h, the water pressures in the H and h sections are balanced, so that no slag flows out to the collection bit. When H<h, the water pressure in the h section becomes high and the cooling water flows toward the H section, so that slag does not flow out from the l section in Fig. 5. In addition, when H > h, as shown in Figure 2, the water pressure in the H section increases and the cooling water reaches h
Since the slag flows toward the 1 section, slag flows out from the 1 section. Therefore, in normal operation, by adjusting the water level in the direction of H=h or H<h, it is possible to suppress leakage (outflow) from the distance l between the guide plate 22 and the conveyor 7, and directly below the conveyor 7. There is no possibility that the conveyor 7 will stop operating due to accumulation in the surrounding area, and the collection rate can also be improved. To properly adjust the water level H and h mentioned above,
For example, multiple water level adjustment ports 23 provided on the guide plate 22
This can be dealt with by adjusting the opening or closing it appropriately. Now, in order to manufacture granulated water using this granulated water production equipment 30, the following procedure is performed. The slag ladle 1 is rotated to spread the molten slag 2 to a slag treatment chute 3 while guiding it to a rotating drum 4 and scattering it. As a result, the collection dome 9 is granulated.
Some of it falls into the water of the collection pit 6, and the other part hits the ceiling 18 and side wall 1 of the collection dome 9.
However, as described above, it is washed away with cooling water that maintains its cooling ability, and falls into the water in the collection pit 6, where it is cooled. In particular, the water spray nozzle 20-2 directed toward the guide plate 22 guides the granular slag 5 to the conveyor 7 and facilitates its collection. The conveyor 7 conveys the granulated water 5-2 remaining in the water to the storage hopper 8 to produce a granulated product. The cooling water in the collection pit 6 passes through the open groove 13 and reaches the precipitation treatment pit 12, and the purified cooling water flows into the circulation pit 14 and is sequentially circulated within the above-mentioned system. At this time, inside the collection dome 9, there are a slit-shaped ventilation hole 21, an exhaust hole 17, and a water spray nozzle 2.
Since the atmospheric temperature is maintained appropriately through interactions such as the formation of a water film by the cooling water on the ceiling 18 and/or side walls 19, the cooling water temperature in the collection pit 6 is also maintained appropriately. Contributes to improving the quality of granulated water. As described above, the present invention provides the collection dome 9 so as to generally surround the rotating drum 4 and the collection pit 6, and the water spray nozzle 20 directed toward the ceiling 18 and/or side wall 19 of the dome 9. , the lower end of the side wall 19 of the dome 9 is inclined in the direction of the conveyor 7, formed into a guide plate 22 having a water level adjustment port 23, and is provided with a water spray nozzle 20-2 directed toward the guide plate 22; By providing a plurality of rows of slit-shaped ventilation holes 21 opening in the vertical direction of the side wall 19, the effects shown in Table 1 below can be obtained.

【表】 また第7図に捕集ピツト内の冷却水温度を示
す。実線は本発明例、点線は従来例によるもので
ある。 この図より明らかな如く、本発明に係る水砕製
造設備は、水砕の品質および硫化水素の発生に影
響を与える温度が適正に維持されることがわか
る。 以上の如く本発明は、従来の水砕製造設備では
得られない顕著な効果を発揮する。
[Table] Figure 7 also shows the temperature of the cooling water in the collection pit. The solid line represents the example of the present invention, and the dotted line represents the conventional example. As is clear from this figure, it can be seen that the granulated water manufacturing equipment according to the present invention maintains an appropriate temperature that affects the quality of granulated water and the generation of hydrogen sulfide. As described above, the present invention exhibits remarkable effects that cannot be obtained with conventional water granulation production equipment.

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

第1図は従来の水砕製造設備の全体概要図、第
2図は本発明に係る水砕製造設備の平面図、第3
図は第2図のA−A矢視図、第4図は第3図のB
−B矢視図、第5図は第2図のC−C矢視図、第
6図は第5図の要部拡大斜視図、第7図は捕集ド
ーム内の雰囲気温度、捕集ピツト内の冷却水温度
を示すグラフである。 1……溶滓鍋、2……溶融スラグ、3……溶滓
処理シユート、4……回転ドラム、5……粒状化
スラグ(水砕)、6……捕集ピツト、7……コン
ベア、8……貯蔵ホツパー、9……捕集ドーム、
11……補助ガイド板、12……沈澱処理ピツ
ト、13……開溝、14……循環ピツト、15…
…循環ポンプ、16……冷却水導管、17……排
気孔、18……天井、19……側壁、20……散
水ノズル、21……スリツト状の通気孔、22…
…ガイド板、23……水位調整口、24……水砕
漏出抑制板、25……取付部材、26……冷却水
流出入口、30……水砕製造設備。
FIG. 1 is an overall schematic diagram of a conventional granulated water production facility, FIG. 2 is a plan view of a granulated water production facility according to the present invention, and FIG.
The figure is the A-A arrow view in Figure 2, and Figure 4 is B in Figure 3.
-B arrow view, Figure 5 is a C-C arrow view in Figure 2, Figure 6 is an enlarged perspective view of the main part of Figure 5, Figure 7 is the atmospheric temperature inside the collection dome, and the collection pit. 3 is a graph showing the temperature of cooling water in the interior of the vehicle. 1... Slag pot, 2... Molten slag, 3... Slag processing chute, 4... Rotating drum, 5... Granulated slag (crushed water), 6... Collection pit, 7... Conveyor, 8... Storage hopper, 9... Collection dome,
11... Auxiliary guide plate, 12... Sedimentation treatment pit, 13... Open groove, 14... Circulation pit, 15...
... Circulation pump, 16 ... Cooling water conduit, 17 ... Exhaust hole, 18 ... Ceiling, 19 ... Side wall, 20 ... Water nozzle, 21 ... Slit-shaped ventilation hole, 22 ...
... Guide plate, 23 ... Water level adjustment port, 24 ... Granule leakage suppression plate, 25 ... Mounting member, 26 ... Cooling water inlet, 30 ... Granule manufacturing equipment.

Claims (1)

【特許請求の範囲】[Claims] 1 溶融スラグを回転ドラムで飛散させて粒状化
し、粒状スラグを捕集ピツトに捕集する水砕製造
設備において、捕集ピツトを包囲する密閉状捕集
ドームを設け、該ドームの底部を捕集ピツトに浸
漬して開口域を形成し、該開口域にコンベアを付
設し、該ドームの天井および/または側壁に指向
する散水ノズルを配設し、該ドームの側壁の下端
を、コンベア方向に傾斜するガイド板に形成し、
該ガイド板に指向する散水ノズルを配設し、該ガ
イド板に開度調整可能な水位調整口を穿設し、か
つ前記側壁の鉛直方向に開口するスリツト状の通
気孔を複数列設けたことを特徴とする水砕製造設
備。
1 In a granulated slag production facility that scatters molten slag with a rotating drum and collects the granular slag in a collection pit, a closed collection dome surrounding the collection pit is provided, and the bottom of the dome is collected. The dome is immersed in a pit to form an opening area, a conveyor is attached to the opening area, a water spray nozzle is provided pointing toward the ceiling and/or side wall of the dome, and the lower end of the side wall of the dome is inclined toward the conveyor. formed into a guide plate to
A water spray nozzle directed toward the guide plate is provided, a water level adjustment port whose opening degree can be adjusted is provided in the guide plate, and a plurality of rows of slit-shaped ventilation holes opening in the vertical direction of the side wall are provided. Water granulation manufacturing equipment featuring:
JP965281A 1981-01-27 1981-01-27 Producing facilities for granulated slag Granted JPS57127434A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP965281A JPS57127434A (en) 1981-01-27 1981-01-27 Producing facilities for granulated slag

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP965281A JPS57127434A (en) 1981-01-27 1981-01-27 Producing facilities for granulated slag

Publications (2)

Publication Number Publication Date
JPS57127434A JPS57127434A (en) 1982-08-07
JPS633645B2 true JPS633645B2 (en) 1988-01-25

Family

ID=11726139

Family Applications (1)

Application Number Title Priority Date Filing Date
JP965281A Granted JPS57127434A (en) 1981-01-27 1981-01-27 Producing facilities for granulated slag

Country Status (1)

Country Link
JP (1) JPS57127434A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01259656A (en) * 1988-04-11 1989-10-17 Hitachi Commun Syst Inc Optical receiver

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101914643A (en) * 2010-09-13 2010-12-15 北京慧德盛节能科技有限公司 Adjustable expanded slag bead chute
CN101914641B (en) * 2010-09-13 2014-08-20 北京慧德盛节能科技有限公司 Expansion slag bead casting drum
CN101914642B (en) * 2010-09-13 2015-04-08 北京慧德盛节能科技有限公司 Waste heat recovery device for expanded slag balls
CN101914640B (en) * 2010-09-13 2014-04-16 北京慧德盛节能科技有限公司 Dry granulation and afterheat recovery system of blast-furnace slag

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5319991A (en) * 1976-08-10 1978-02-23 Nippon Steel Corp Granulating apparatus for molten slag

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5319991A (en) * 1976-08-10 1978-02-23 Nippon Steel Corp Granulating apparatus for molten slag

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01259656A (en) * 1988-04-11 1989-10-17 Hitachi Commun Syst Inc Optical receiver

Also Published As

Publication number Publication date
JPS57127434A (en) 1982-08-07

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