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JPS6054255B2 - Water slag manufacturing method and device - Google Patents
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JPS6054255B2 - Water slag manufacturing method and device - Google Patents

Water slag manufacturing method and device

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Publication number
JPS6054255B2
JPS6054255B2 JP53034336A JP3433678A JPS6054255B2 JP S6054255 B2 JPS6054255 B2 JP S6054255B2 JP 53034336 A JP53034336 A JP 53034336A JP 3433678 A JP3433678 A JP 3433678A JP S6054255 B2 JPS6054255 B2 JP S6054255B2
Authority
JP
Japan
Prior art keywords
water
tank
slag
slurry
sedimentation
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
JP53034336A
Other languages
Japanese (ja)
Other versions
JPS54126692A (en
Inventor
正治 喜多島
和義 福本
照章 奥尾
幸典 児玉
敏雄 大薮
強 安井
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.)
Kobe Steel Ltd
Original Assignee
Kobe Steel 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 Kobe Steel Ltd filed Critical Kobe Steel Ltd
Priority to JP53034336A priority Critical patent/JPS6054255B2/en
Publication of JPS54126692A publication Critical patent/JPS54126692A/en
Publication of JPS6054255B2 publication Critical patent/JPS6054255B2/en
Expired legal-status Critical Current

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Description

【発明の詳細な説明】 本発明は水滓製造方法およびその装置に関するもので
ある。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method and apparatus for producing slag.

従来、金属製錬炉から取り出される溶滓は出滓口より
排出され、自然冷却して塊状の鉱滓とする・か加圧空気
あるいは蒸気を吹付け鉱滓綿とするか高速度で噴出する
水流上に落下させて水滓とするなどの処理をほどこして
各方面にそれぞれ利用されている。
Conventionally, slag taken out from a metal smelting furnace is discharged from a slag opening and cooled naturally to form a lumpy slag, or it is blown with pressurized air or steam to form slag fibers, or it is flowed out at high speed over a stream of water. The water is then treated by dropping it into water slag, which is then used in various ways.

従来の水滓製造装置を第1図、そのフローシートを第2
図に示す。
The conventional water slag production equipment is shown in Figure 1, and its flow sheet is shown in Figure 2.
As shown in the figure.

第1、2図よりプロセスを概述すれば、吹製装置1を出
た水滓スラリー2は水滓槽3に落下し、水滓を含有する
オーバーフロー水はオーバーフロー槽4に貯留される。
To outline the process with reference to FIGS. 1 and 2, the slag slurry 2 coming out of the blowing device 1 falls into the slag tank 3, and the overflow water containing the slag is stored in the overflow tank 4.

沈降スラリーはオーバーフロー槽4下部からスラリーポ
ンプにより脱水槽6を経て沈殿槽5に連通する系路内に
給送され、さらに沈殿槽5下部から濃縮スラリーがスラ
リーポンプにて脱水槽6へと給送、脱水されて製品水滓
となる。又吹製用圧力噴射水として沈殿槽5から清浄水
が冷却塔7に給送され、冷却水として冷水槽8に貯留さ
れる。
The settled slurry is fed from the bottom of the overflow tank 4 by a slurry pump into a system that communicates with the settling tank 5 via the dehydration tank 6, and the concentrated slurry is further fed from the bottom of the settling tank 5 to the dehydration tank 6 by a slurry pump. , dehydrated to become product slag. Also, clean water is fed from the settling tank 5 to the cooling tower 7 as pressure injection water for blowing, and is stored in the cold water tank 8 as cooling water.

又水滓槽3下部に沈降したスラリーはスラリーポンプに
て脱水槽6へ給送される。
Further, the slurry settled at the bottom of the water slag tank 3 is fed to the dewatering tank 6 by a slurry pump.

以上が従来の一般的水滓製造装置であるが、下記の様な
欠点を有していた。
The above is a conventional general water slag manufacturing apparatus, but it had the following drawbacks.

すなわち、従来装置では、起動時に必要な大量の圧力噴
射水を確保する必要があり、また稼動中においては製錬
炉から発生する溶滓量の時間的変動又は各種トラブルに
対処するため、予め高い水比(圧力噴射水量/溶滓)に
設定しており、したがつて圧力噴射水を供給する冷水槽
の容量を大きくせざるを得なかつた。
In other words, with conventional equipment, it is necessary to secure a large amount of pressure-injected water at the time of startup, and during operation, in order to deal with temporal fluctuations in the amount of slag generated from the smelting furnace or various problems, The water ratio (amount of pressure-injected water/slag) was set, so the capacity of the cold water tank that supplies the pressure-injected water had to be increased.

また他の例では特に起動時に循環径路外から圧力噴射水
用の清浄水を別途供給することも行なわれていた。また
従来装置では、各槽が独立に設置されることが多く、そ
のため各種間のスラリー、水の輸送はポンプ類に頼らざ
るを得なかつた。これらの結果、従来装置では.設備が
大規模化し、また所要電力費がかさんて水滓価格の高騰
が避け得られなかつた。本発明は、これら従来の水滓製
造装置の欠点を解消し、貯水槽の小容量化、スラリー、
水輸送の効率化を図り、しかもまた運転時の溶滓量変動
に!追従した水量自動制御の出来る水滓製造装置を提供
することを目的としてなされたものである。
In other examples, clean water for pressure injection water is separately supplied from outside the circulation path, especially at startup. In addition, in conventional equipment, each tank is often installed independently, so pumps have to be relied upon to transport slurry and water between each type. As a result, the conventional equipment. As the equipment became larger and the cost of electricity increased, it was inevitable that the price of water slag would rise. The present invention eliminates the drawbacks of these conventional water slag production devices, reduces the capacity of the water tank, and produces slurry.
Improves the efficiency of water transportation and also prevents the amount of slag from fluctuating during operation! This was done for the purpose of providing a water slag production device that can automatically control the amount of water.

次に図面に示した実施例に基づき本発明を具体的に説明
する。第3図は本発明に係る水滓製造装置の一実施例・
を示す断面図、第4図はそのフローシートである。
Next, the present invention will be specifically explained based on embodiments shown in the drawings. FIG. 3 shows an embodiment of the water slag manufacturing apparatus according to the present invention.
FIG. 4 is a cross-sectional view showing the flow sheet.

第3,4図より、適切温度の溶滓を適切温度、速度、水
量の圧力噴射水によつて微細化し得られた均一粒度の水
滓スラリーを、吹製樋9を介して水滓槽10に落下させ
、水滓槽10からの水滓スラリーを2個の水滓掻き集め
装置11を有する沈殿槽12の一端から直接流入させ一
方下部から濃縮スラリーをスラリーポンプによつて脱水
槽13に給送する。
From Figures 3 and 4, the slag slurry of uniform particle size obtained by atomizing the slag at an appropriate temperature with pressure-injected water at an appropriate temperature, speed, and water volume is passed through the blowing gutter 9 to the slag tank 10. The slag slurry from the slag tank 10 flows directly into one end of the settling tank 12 having two slag scraping devices 11, while the concentrated slurry is fed from the lower part to the dewatering tank 13 by a slurry pump. do.

沈殿槽12の清浄水を貯水槽14を構成する一方の温水
槽14bに流出せしめ、温水槽14b下部と貯水槽14
を構成する他の1つの冷水槽14ノa下部を連通状態と
する。
The clean water in the settling tank 12 is made to flow into one hot water tank 14b constituting the water storage tank 14, and the lower part of the hot water tank 14b and the water storage tank 14 are
The lower part of the other cold water tank 14a constituting the cold water tank 14 is brought into communication.

冷水槽14aは温水槽14bの温水を冷却塔15に給水
し得られた冷却水を貯留し、その下部からポンプにより
吹製装置(図示せす)に圧力噴射水用として給水するも
のである。又脱水槽13にて水滓と分離された水は沈殿
槽12に給送される。
The cold water tank 14a stores the cooled water obtained by supplying hot water from the hot water tank 14b to the cooling tower 15, and supplies water from the lower part thereof to a blowing device (shown in the figure) as pressure injection water using a pump. Further, the water separated from the water dregs in the dewatering tank 13 is fed to the settling tank 12.

ここで本発明の特徴は、水滓槽からに水滓スラリーをオ
ーバーフロー槽に貯留することなく直接沈殿槽に流入さ
せ、沈殿槽で濃縮スラリーと分離された清浄水を温水槽
に流出せしめる如くなして沈殿槽と温水槽とを同じ水位
となし、また温水槽と冷却塔からの冷却水を貯留する冷
水槽との間を連通状態としたことである。
Here, the feature of the present invention is that the water slag slurry is directly flowed from the water slag tank into the settling tank without being stored in the overflow tank, and the clean water separated from the concentrated slurry in the settling tank is flowed out to the hot water tank. The water level of the sedimentation tank and the hot water tank is the same, and the hot water tank and the cold water tank that stores cooling water from the cooling tower are connected to each other.

この様に沈殿槽と温水槽を同じ水位としかつ温水槽と冷
水槽を連通状態にする理由は下記の如くである。
The reason why the settling tank and the hot water tank are kept at the same water level and in communication with the hot water tank is as follows.

水滓製造装置における水量バランスの崩れは、起動時、
停止時、非常時等に生じ、従来の装置ではこの様な時の
対策として大容量の貯水槽を設置する等していたが、コ
ンパクトな貯水槽でもこの様な時のたとえば圧力噴射水
の水量確保を可能とするためである。
An imbalance in the amount of water in the slag production equipment occurs when starting up.
This occurs during stoppages, emergencies, etc., and with conventional equipment, a large-capacity water tank was installed as a countermeasure for such cases, but even with a compact water tank, the amount of water that is injected during such times, for example, can be reduced. This is to enable security.

一般に吹製装置内に流入する溶滓量は、高炉からの出滓
状態からも分る通り極めて不安定であり、その変動量の
最大値は平均量の2〜3倍余りにも達する。
Generally, the amount of slag flowing into the blowing device is extremely unstable, as can be seen from the state of the slag coming out of the blast furnace, and the maximum value of the fluctuation amount is more than 2 to 3 times the average amount.

こういう場合、予め設定された適切な水比を維持するた
めには、変動量に追従した圧力噴射水量が必要となり、
冷却水の確保が要求される。
In this case, in order to maintain an appropriate water ratio set in advance, it is necessary to inject water at a pressure that follows the fluctuation amount.
It is necessary to secure cooling water.

従来の装置では、変動量を見込んで予め高い水比に設定
して圧力噴射水を多量供給しており従つて変動量に応じ
た水量制御は行なわれておらず、このため大規模な冷水
槽等を設けていた。本発明では、変動量に追従した水量
制御を行なうことと共に、温水槽と冷水槽との間を連通
状態とすることにより常に必要な冷水槽水位が保たれ、
変動量に応じた圧力噴射水が供給できることとなる。
In conventional equipment, a large amount of pressure-injected water is supplied by setting a high water ratio in advance in anticipation of fluctuations.Therefore, the water volume is not controlled according to fluctuations, and as a result, large-scale cold water tanks are required. etc. were established. In the present invention, in addition to performing water flow control that follows fluctuations, the necessary cold water tank water level is always maintained by communicating between the hot water tank and the cold water tank.
Pressure injection water can be supplied according to the amount of fluctuation.

又、起動時における冷水槽水位低下の場合も温水槽から
水が自然流入し、低下によるポンプトラブルも防止する
。なお溶滓量変動の検知は後述する沈殿槽内に配置され
た水滓掻き集め装置に取り付けられたアンメーターにて
、該装置にかかる負荷の変動から行なうことができる。
Furthermore, even if the cold water tank water level drops during startup, water will naturally flow in from the hot water tank, preventing pump troubles due to the drop. Incidentally, the fluctuation in the amount of slag can be detected by using an ammeter attached to a slag scraping device disposed in the settling tank, which will be described later, from changes in the load applied to the device.

又は水滓ポンプのアンメーター変動、水滓槽水温変化、
沈殿槽水位上昇による変動から検出することも可能であ
る。更に本発明ではオーバーフロー槽を除去し直接沈殿
槽に水滓スラリーを流入させており、オーバーフロー槽
からのスラリー抜出し用のポンプが不要となるのでポン
プ台数等の削減ひいては電力費低減が可能となる。
Or ammeter fluctuation of the slag pump, change in slag tank water temperature,
It is also possible to detect from fluctuations caused by rising water level in the sedimentation tank. Further, in the present invention, the overflow tank is removed and the water slag slurry is directly flowed into the settling tank, and a pump for extracting the slurry from the overflow tank is not required, so it is possible to reduce the number of pumps, etc., and thus reduce power costs.

更に本発明では、貯水槽は温水槽と冷水槽の2つから構
成されているが、これは、循環水を圧力噴射水として使
用する場合に水温を適当な低温に維持するためである。
Furthermore, in the present invention, the water storage tank is composed of two, a hot water tank and a cold water tank, and this is to maintain the water temperature at an appropriate low temperature when the circulating water is used as pressure injection water.

すなわち、沈殿槽から温水槽に流入する温水を冷却塔に
給送して冷却した後の冷水を温水槽とは別の(但し連通
状態としている)冷水槽に貯留することにより、圧力噴
射水として使用する場合の水温を適当な低温に維持する
のてある。次に沈殿槽について図5に従つて説明する。
In other words, the hot water flowing into the hot water tank from the settling tank is sent to the cooling tower and cooled, and then the cold water is stored in a cold water tank that is separate from the hot water tank (but is in communication with it), so that it can be used as pressure injection water. It is necessary to maintain the water temperature at a suitable low temperature when using it. Next, the sedimentation tank will be explained according to FIG.

先ずその機能は先述した通り、水滓槽からの水滓スラリ
ーを沈殿槽の一端から流入させ、清浄水を右端上部から
温水槽に流出させ、一方下部から濃縮スラリーを脱水槽
に供給するものである。その形状は矩形状であり清浄水
流出方向に2個の水滓掻き集め装置を配設したものであ
る。従来の沈殿槽は、水滓スラリー供給口を中心部に設
け周辺上に清浄水排出口が有り、その形状は円もしくは
略円状であつた。かかる沈殿槽では、掻き集め装置の半
径:rは自然沈殿距離:eは等しく必然的に沈殿槽直径
はeに対して2倍となり、更に負荷が大となると複数個
の沈殿槽が設置される等不必要に沈殿槽を大ならしめて
おり設備費コストを高いものにしていた。
First, as mentioned above, its function is to allow the water slag slurry from the water slag tank to flow into one end of the settling tank, to flow clean water into the hot water tank from the upper right end, and to supply the concentrated slurry from the bottom to the dehydration tank. be. Its shape is rectangular, and two slag scraping devices are arranged in the clean water outflow direction. A conventional settling tank has a water dregs slurry supply port in the center and a clean water discharge port on the periphery, and has a circular or substantially circular shape. In such a sedimentation tank, the radius of the raking device: r is the natural sedimentation distance: e is equal, and naturally the diameter of the sedimentation tank is twice that of e, and if the load becomes even larger, multiple sedimentation tanks are installed, etc. The sedimentation tank was made unnecessarily large, resulting in high equipment costs.

したがつて沈殿槽として望ましい構造は、前述の実施例
に示したように、必要なスラリー自然沈殿距離内で掻き
集め装置の効果的利用を図つて、水滓スラリーを一端か
ら流入し他端上部から流出させ、その形状は有効面積を
十分に考慮した矩形状であり槽内には大負荷に対して能
力を2個の水滓掻き集め装置に分散させ、沈殿槽の効率
化、コンパクト化を図つたものである。
Therefore, as shown in the above-mentioned example, a desirable structure for the settling tank is to effectively utilize the scraping device within the necessary natural slurry settling distance, and to allow the water slag slurry to flow in from one end and from the top of the other end. The tank has a rectangular shape that takes into account the effective area, and the capacity to handle large loads is distributed between two slag scraping devices, making the settling tank more efficient and compact. It is something.

その他の実施例として第6図に示す通り複数個の掻き集
め装置を設けること、又用途によつては該装置なしで設
ける等がある。
Other embodiments include providing a plurality of raking devices as shown in FIG. 6, or, depending on the application, providing no such device.

以上本発明の実施例について述べたがこれら水滓槽、沈
殿槽、貯水槽は一体外枠内に共通壁を有して設置される
The embodiments of the present invention have been described above, and the slag tank, sedimentation tank, and water storage tank are installed within an integral outer frame with a common wall.

又その他の実施例として、沈殿槽と温水槽との間の側壁
を連通状態とすることも可能である。
As another embodiment, it is also possible to communicate the side wall between the settling tank and the hot water tank.

これは水滓槽と脱水槽の配管途中で管閉塞が生じた場合
、沈殿槽の水位が降下し温水槽、冷水槽の水位も合せて
降下して吹製用給水の確保が困難となる、この場合、前
述の沈殿槽と温水槽を連通にすることにより、一時的で
はあるが吹製用給水を確保することが出来る。その他の
実施例として、沈殿槽に水滓スラリーを沈降させず全て
沈殿槽にて処理することも可能であり、この場合スラリ
ーポンプは不要となつて電力費が低減される。
This is because if a pipe blockage occurs between the water slag tank and the dewatering tank, the water level in the sedimentation tank will drop, and the water levels in the hot and cold water tanks will also drop, making it difficult to secure a water supply for blowing. In this case, by communicating the above-mentioned sedimentation tank and hot water tank, water supply for blowing can be secured, albeit temporarily. As another embodiment, it is possible to treat the entire slurry in the sedimentation tank without settling it in the sedimentation tank, and in this case, a slurry pump is not required and the power cost is reduced.

もし沈殿槽の負荷が許容を越える場合は従来通り水滓槽
下部から水滓スラリーを抜き出し脱水槽へ給送しても差
しつかえない。更に他の実施例は、水滓槽下部に設けら
れたスラリーポンプにキャビテーション、閉塞が生じた
場合、冷水槽からの冷却水を水滓槽に自動的に流入させ
圧力上昇及び水量増大により、上記トラブルを速やかに
解消し回復を図ることである。
If the load on the sedimentation tank exceeds the allowable limit, the slag slurry can be extracted from the bottom of the slag tank and fed to the dewatering tank as usual. In yet another embodiment, when cavitation or blockage occurs in the slurry pump installed at the bottom of the slag tank, cooling water from the cold water tank is automatically flowed into the slag tank to increase pressure and water volume, thereby solving the above problem. The aim is to quickly resolve the problem and recover.

従来においては、手動で行なつており回復に手間取つて
いたものを自動的に検出して行なうもの.であり検出方
法は、ポンプ揚水量低下による水滓槽水位上昇もしくは
スラリー温度上昇から行なう。以上その他の実施例の効
果をまとめるど沈殿槽にて全ての水滓スラリーを処理す
ることによる電ノカ費の低減及びポンプ台数の削減、又
水滓槽下部に設けられたポンプトラブル時における速や
かな回復処置を自動制御にて行なうことがある。
In the past, this was done manually and took time to recover, but it is automatically detected and done. The detection method is based on an increase in the water level in the slag tank or an increase in the temperature of the slurry due to a decrease in the amount of pumped water. To summarize the effects of the above and other embodiments, all the water slag slurry is processed in the settling tank, which reduces electricity costs and the number of pumps. Recovery actions may be performed under automatic control.

以上本発明の実施例、その他の実施例に詳述した通り、
新規な沈殿槽及び水滓槽、沈殿槽、貯水槽、(温水槽、
冷水槽)を有機的に組み合せ、一体外枠内に設置したこ
とに依り、処理能力には無論影響を与えずコンパクトな
水滓製造装置を提供するばかりか溶滓変動量に追従した
水量自動制御、更にはポンプ台数削減による電力費低減
、コンパクト化による設備スペースの減少、水槽類建設
費の低減、更に水滓槽スラリーポンプトラブル時の水量
自動制御に依る速やかな回復処置等、これまでには見ら
れない画期的水滓製造方法およびその装置を提供するも
のであり今日の省エネ、省資源が叫ばれる中で、まさに
時代の要望に応えたものでありその価値は極めて高いと
いえよう。
As detailed above in the embodiments and other embodiments of the present invention,
New sedimentation tank and slag tank, sedimentation tank, water storage tank, (hot water tank,
By organically combining the cold water tanks) and installing them within an integral outer frame, we not only provide a compact slag production device without affecting the processing capacity, but also automatically control the water volume to follow the fluctuations in the slag amount. In addition, we have achieved reductions in electricity costs by reducing the number of pumps, reduction in equipment space by making it more compact, reduction in construction costs for water tanks, and rapid recovery by automatic water flow control in the event of trouble with the slurry pump in the water slag tank. It provides an unprecedented and innovative method and equipment for producing water slag, and in today's world where energy and resource conservation are being called for, it truly meets the demands of the times and can be said to be of extremely high value.

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

第1図は従来の水滓製造装置を示す断面図、第2図は従
来装置のフローシート、第3図は本発明の水滓製造装置
を示す断面図、第4図は本発明装置のフローシート、第
5図は従来及び本発明の沈殿槽を示す略平面図、第6図
は本発明のその他の実施例を示す略断面図である。 図中の主な符号は次のとおりである。 9:吹製樋、10:水滓槽、12:沈殿槽、13:脱水
槽、14:貯水槽、14a:冷水槽、14b:温水槽、
15:冷却塔。
Fig. 1 is a sectional view showing a conventional slag production device, Fig. 2 is a flow sheet of the conventional device, Fig. 3 is a sectional view showing the slag production device of the present invention, and Fig. 4 is a flowchart of the device of the present invention. FIG. 5 is a schematic plan view showing a conventional settling tank and a settling tank according to the present invention, and FIG. 6 is a schematic cross-sectional view showing another embodiment of the present invention. The main symbols in the figure are as follows. 9: Blown gutter, 10: Slag tank, 12: Sedimentation tank, 13: Dehydration tank, 14: Water storage tank, 14a: Cold water tank, 14b: Hot water tank,
15: Cooling tower.

Claims (1)

【特許請求の範囲】 1 溶滓に圧力水を噴射して得られた水滓スラリーを固
液分離して水滓を得る水滓の製造方法において、前記圧
力水噴射後の水滓スラリーを吹製樋を介して水滓槽に一
旦貯留した後、該水滓槽に共通壁を介して連接して矩形
状に延設されかつ該矩形状長手方向に集泥装置および集
泥室を備える沈殿部を複数個直列に配列した沈殿槽の前
記水滓槽との共通壁連接部より直接水滓スラリーを沈殿
槽内に流入せしめ、該沈殿槽内の前記複数個の沈殿部に
おいて段階的に各々沈降濃縮スラリーと浮上清浄水とに
分離し、該清浄水は流入により該沈殿槽の水位と同一の
水位になるように連接された温水槽に一旦貯留したのち
、該温水槽と連通状態に連設される冷水槽の上に設けら
れた冷却塔で冷却して前記冷水槽に貯留し、必要に応じ
て前記圧力水として供給する一方、前記沈降濃縮水滓ス
ラリーを脱水して水滓を得ることを特徴とする水滓製造
方法。 2 吹製樋からの水滓スラリーを貯留する水滓槽と、該
水滓槽に連接して矩形状に延設されかつ該矩形状長手方
向に集泥装置および集泥室を備える沈殿物を複数個直列
に配設するとともに、前記水滓槽との連接部より直接水
滓スラリーを沈殿槽内に流入せしめ、該沈殿槽内の前記
複数個の沈殿部において段階的に各々沈降濃縮スラリー
と浮上清浄水とに分離して上部から清浄水を流出し、一
方下部から濃縮スラリーを抜き出す沈殿槽と、該沈殿槽
から流出した清浄水を貯留する温水槽と冷却塔からの冷
却水を貯留する冷却槽とからなつて、該温水槽と該冷水
槽を連通状態とした貯水槽と、該温水槽の温水を冷却し
て該冷水槽に冷却水として送る冷却塔と、少なくとも該
沈殿槽の下部から抜き出された、水滓スラリーを脱水す
る脱水槽とからなるとともに前記水滓槽、沈殿槽、貯水
槽とが一体外枠内に共通壁を有して設置されることを特
徴とする水滓製造装置。
[Scope of Claims] 1. A method for producing a slag that obtains a slag by solid-liquid separation of a slag slurry obtained by injecting pressurized water onto the slag, wherein the slag slurry after the pressure water injection is sprayed. After the slag is once stored in a slag tank through a gutter, the slag is connected to the slag tank via a common wall and extends in a rectangular shape, and is provided with a sludge collection device and a sludge collection chamber in the longitudinal direction of the rectangular shape. A water slag slurry is caused to directly flow into the sedimentation tank from a common wall connecting part with the water slag tank of a sedimentation tank in which a plurality of parts are arranged in series, and the water slag slurry is made to flow into the sedimentation tank in stages in each of the plurality of sedimentation parts in the sedimentation tank. Sedimentation concentrated slurry and floating clean water are separated, and the clean water is temporarily stored in a connected hot water tank so that the water level is the same as the water level of the settling tank as it flows in, and then communicated with the hot water tank. The water is cooled in a cooling tower installed above the cold water tank, stored in the cold water tank, and supplied as the pressure water as needed, while the sedimented concentrated water slag slurry is dehydrated to obtain water slag. A water slag manufacturing method characterized by: 2. A slag tank that stores the slag slurry from the blowing gutter, and a sediment tank that is connected to the slag tank and extends in a rectangular shape, and that is equipped with a sludge collection device and a sludge collection chamber in the longitudinal direction of the rectangular shape. A plurality of them are arranged in series, and the water slag slurry is made to flow directly into the sedimentation tank from the connection part with the water slag tank, and the sedimentation and concentrated slurry are respectively mixed in stages in the plurality of settling parts in the sedimentation tank. A sedimentation tank that separates the floating clean water and drains the clean water from the upper part and extracts the concentrated slurry from the lower part, a hot water tank that stores the clean water that flows out of the sedimentation tank, and a cooling water from the cooling tower that stores it. A water storage tank comprising a cooling tank and communicating the hot water tank and the cold water tank, a cooling tower that cools the hot water in the hot water tank and sends it as cooling water to the cold water tank, and at least a lower part of the settling tank. and a dehydration tank for dewatering the water slag slurry extracted from the water slag, and the water slag tank, sedimentation tank, and water storage tank are installed in an integral outer frame with a common wall. Slag manufacturing equipment.
JP53034336A 1978-03-24 1978-03-24 Water slag manufacturing method and device Expired JPS6054255B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP53034336A JPS6054255B2 (en) 1978-03-24 1978-03-24 Water slag manufacturing method and device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP53034336A JPS6054255B2 (en) 1978-03-24 1978-03-24 Water slag manufacturing method and device

Publications (2)

Publication Number Publication Date
JPS54126692A JPS54126692A (en) 1979-10-02
JPS6054255B2 true JPS6054255B2 (en) 1985-11-29

Family

ID=12411291

Family Applications (1)

Application Number Title Priority Date Filing Date
JP53034336A Expired JPS6054255B2 (en) 1978-03-24 1978-03-24 Water slag manufacturing method and device

Country Status (1)

Country Link
JP (1) JPS6054255B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61271649A (en) * 1985-05-27 1986-12-01 Toshiba Corp Cassette holder

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5917739U (en) * 1982-07-21 1984-02-03 日立造船株式会社 Water treatment equipment for granulated slag manufacturing equipment

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS52105595A (en) * 1976-03-03 1977-09-05 Rasa Corp Water slag manufacturing process
JPS5324316A (en) * 1976-08-18 1978-03-07 Nippon Steel Corp Granulated slag production apparatus

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61271649A (en) * 1985-05-27 1986-12-01 Toshiba Corp Cassette holder

Also Published As

Publication number Publication date
JPS54126692A (en) 1979-10-02

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