JPS6129767B2 - - Google Patents

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Publication number
JPS6129767B2
JPS6129767B2 JP7837878A JP7837878A JPS6129767B2 JP S6129767 B2 JPS6129767 B2 JP S6129767B2 JP 7837878 A JP7837878 A JP 7837878A JP 7837878 A JP7837878 A JP 7837878A JP S6129767 B2 JPS6129767 B2 JP S6129767B2
Authority
JP
Japan
Prior art keywords
impeller
water
negative pressure
pressure chamber
scum
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
JP7837878A
Other languages
Japanese (ja)
Other versions
JPS555726A (en
Inventor
Katsumi Nagasaki
Yoshihiro Inoe
Osao Nakade
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.)
Kubota Corp
Original Assignee
Kubota 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 Kubota Corp filed Critical Kubota Corp
Priority to JP7837878A priority Critical patent/JPS555726A/en
Publication of JPS555726A publication Critical patent/JPS555726A/en
Publication of JPS6129767B2 publication Critical patent/JPS6129767B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】 本発明は、高温の吸引物を吸引気流路から分離
する装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an apparatus for separating hot suction matter from a suction air flow path.

吸引気流路から吸引物を分離する場合、吸引気
流路の負圧を破らずに吸引物を分離する装置とし
て、本出願人は先に、吸引装置に連通した負圧室
と、該負圧室に連通した液体槽と、該液体槽と負
圧室との連通部に設けたインペラからなる分離装
置を提案した。かかる装置においては、上記連通
部を液体槽内の水で封鎖し、この水が負圧室内に
流入するのをインペラの遠心作用により防止しな
がら、該インペラを介して負圧室から液体槽へ吸
引物の排出がなされる。しかし、高温の吸引物の
分離に上記分離装置を適用したところ、次のよう
に水封作用に問題があつた。すなわち、溶湯表面
のスカムを吸引し、吸引したスカムに水を噴射し
て冷却固化し、この固化したスカムと、噴射した
水と、この水から発生した水蒸気とを含む吸引気
流からスカムと水を分離する場合に上記分離装置
を使用した。ところが、短時間にインペラ部に到
達するため、液体槽へ放出されるスカムは粒子内
部が赤熱状態であることから、連続運転の間に液
体槽内の水は90゜〜95℃の高温となり、このよう
な高温の水内に赤熱したスカムがインペラから放
出されると、インペラの近傍で瞬間に沸騰が生じ
て多量の蒸気が発生する。そして、この蒸気によ
つてインペラの出口部が気体雰囲気での運転状態
となり、そのため、水封能力が不足となりインペ
ラ周辺の高温の水が気泡および蒸気分と共に負圧
室内に逆流する。しかもこの逆流した水と赤熱ス
カムとの接触によつて吸引気流路内で多量の蒸気
が発生し、コンデンサーでの復水能力以上の蒸気
が管路に流れこれによつて負圧が低下して溶湯表
面からのスカムの吸引能力が弱められる。又この
様にインペラ羽根部で多量の蒸気を発生するため
連通部4aをスカムが落下せずに負圧室1にスカ
ムがたまるか又は吸引装置連通口2へ流れてい
き、スカム排出が不能となる。
When separating the aspirate from the suction air flow path, the applicant has previously developed a device that separates the aspirate without breaking the negative pressure in the suction air flow path, including a negative pressure chamber that communicates with the suction device, and the negative pressure chamber. proposed a separation device consisting of a liquid tank that communicates with a vacuum chamber, and an impeller that is installed in a communication section between the liquid tank and a negative pressure chamber. In such a device, the communication portion is sealed with water in the liquid tank, and the water is prevented from flowing into the negative pressure chamber by the centrifugal action of the impeller, and the water is transferred from the negative pressure chamber to the liquid tank via the impeller. The aspirate is evacuated. However, when the above-mentioned separation device was applied to the separation of high-temperature suction materials, the following problems occurred in the water sealing effect. That is, the scum on the surface of the molten metal is sucked, water is injected onto the scum, the scum is cooled and solidified, and the scum and water are removed from the suction airflow containing the solidified scum, the injected water, and the steam generated from this water. In the case of separation, the above separation apparatus was used. However, since the scum reaches the impeller in a short period of time, the inside of the particles of the scum released into the liquid tank is red-hot, so during continuous operation, the water in the liquid tank reaches a high temperature of 90° to 95°C. When red-hot scum is discharged from the impeller in such high-temperature water, boiling occurs instantaneously near the impeller and a large amount of steam is generated. This steam causes the outlet of the impeller to operate in a gas atmosphere, resulting in insufficient water sealing ability and the high temperature water around the impeller flowing back into the negative pressure chamber along with bubbles and steam. Moreover, a large amount of steam is generated in the suction air flow path due to the contact between this backflowing water and the red-hot scum, and steam that exceeds the condensation capacity of the condenser flows into the pipe, thereby reducing the negative pressure. The ability to attract scum from the surface of the molten metal is weakened. In addition, since a large amount of steam is generated in the impeller blades, the scum does not fall through the communication section 4a, but accumulates in the negative pressure chamber 1 or flows to the suction device communication port 2, making it impossible to discharge the scum. Become.

本発明は、上述のような高温吸引物で生じる沸
騰により負圧室の液体封鎖作用が低下すること
を、液体噴射ノズルの附設によつて防止したもの
である。
The present invention prevents the deterioration of the liquid sealing effect of the negative pressure chamber due to boiling caused by the high-temperature suction as described above, by providing a liquid injection nozzle.

以下、上述の溶湯表面から吸引したスカムの分
離に本発明を適用した実施例につき、図面と共に
説明する。
Hereinafter, an embodiment in which the present invention is applied to the separation of scum sucked from the surface of the molten metal will be described with reference to the drawings.

1は負圧状態に保持される負圧室であり、同筒
状の側壁1aと、漏斗状の底壁1bと、側壁1a
に蓋をする上壁1cとを有している。側壁1aに
は真空ポンプ等の吸引装置と接続する吸引装置連
通口2が開口している。上壁1cには吸引物流入
口3が設けられ、該吸引物流入口3は、溶湯表面
に対向配置されてスカムを吸引すると共に吸引し
たスカムに水を噴射するサクシヨンヘツドと連通
している。底壁1bは円筒状の排出口部4と連な
り、排出口部4は液体槽5の液面下で開口して、
負圧室1と液体槽5との連通部4aを形成してい
る。連通部4aにはインペラ6が配置されて、該
インペラ6は液体槽5の側壁を貫通する筒体7内
の駆動軸8の一端に固定されており、駆動軸8の
他端のプーリ9を介して駆動装置により回転駆動
される。筒体7は液体槽5の側壁の支持板部10
に固定され、駆動軸8は軸受11を介して筒体7
に回転自在に支持されている。駆動軸8の筒体7
からの突出部分には、支持板部10に固定された
環状の水密壁12が外嵌され、水密壁12と駆動
軸8との間にシール材13が介装されている。イ
ンペラ6は、駆動軸8の一端のねじ部8aに螺着
された底板14と、該底板14に対向配置され排
出口部4に外嵌する環状の上板15と、底板14
と上板15との間に放射状に配置された翼板16
からなる。上板15の内周縁と排出口部4との間
にはラビリンス等のシール材17が介装されてい
る。インペラ6の上方および下方には該インペラ
6と隣接して環状のノズル18,19を形成する
環状室20,21が設けられている。上方の環状
室20は、排出口部4の外周に固定されたL形断
面の壁体22と、インペラ6の上板15とで形成
され、ノズル18は上板15の外周縁と壁体22
の下端縁とで形成されている。下方の環状室21
は、液体槽5の支持板部10に固定された壁体2
3と、インペラ6の底板14と、水密壁12とで
形成され、ノズル19は底板14の外周縁と、壁
体23の上縁との間で形成されている。両環状室
20,21は、排出口部4の外周に環状に設けら
れた分配管24に、周方向適当間隔おきの位置で
接続管25を介して接続されており、環状室2
0,21内には、給水装置26から分配管24を
介して水が供給される。
1 is a negative pressure chamber maintained in a negative pressure state, and includes a cylindrical side wall 1a, a funnel-shaped bottom wall 1b, and a side wall 1a.
It has an upper wall 1c that covers the. A suction device communication port 2, which is connected to a suction device such as a vacuum pump, is opened in the side wall 1a. A suction flow inlet 3 is provided in the upper wall 1c, and the suction flow inlet 3 communicates with a suction head which is disposed opposite to the surface of the molten metal and which sucks scum and injects water onto the sucked scum. The bottom wall 1b is connected to a cylindrical discharge port 4, and the discharge port 4 opens below the liquid surface of the liquid tank 5.
A communication portion 4a between the negative pressure chamber 1 and the liquid tank 5 is formed. An impeller 6 is disposed in the communication portion 4a, and the impeller 6 is fixed to one end of a drive shaft 8 in a cylinder 7 that penetrates the side wall of the liquid tank 5, and is fixed to a pulley 9 at the other end of the drive shaft 8. It is rotationally driven by a drive device through it. The cylindrical body 7 is a support plate portion 10 on the side wall of the liquid tank 5.
The drive shaft 8 is fixed to the cylindrical body 7 via a bearing 11.
is rotatably supported. Cylindrical body 7 of drive shaft 8
An annular watertight wall 12 fixed to the support plate portion 10 is fitted onto the protruding portion from the support plate portion 10 , and a sealing material 13 is interposed between the watertight wall 12 and the drive shaft 8 . The impeller 6 includes a bottom plate 14 screwed onto a threaded portion 8a at one end of the drive shaft 8, an annular upper plate 15 disposed opposite to the bottom plate 14 and externally fitted into the discharge port 4, and a bottom plate 14.
and a vane plate 16 arranged radially between the upper plate 15 and the upper plate 15
Consisting of A sealing material 17 such as a labyrinth is interposed between the inner peripheral edge of the upper plate 15 and the discharge port 4. Annular chambers 20 and 21 are provided above and below the impeller 6 and adjacent to the impeller 6 to form annular nozzles 18 and 19. The upper annular chamber 20 is formed by a wall 22 with an L-shaped cross section fixed to the outer periphery of the discharge port 4 and the upper plate 15 of the impeller 6, and the nozzle 18 is formed between the outer periphery of the upper plate 15 and the wall 22.
It is formed by the lower edge of. Lower annular chamber 21
is the wall body 2 fixed to the support plate part 10 of the liquid tank 5
3, the bottom plate 14 of the impeller 6, and the watertight wall 12, and the nozzle 19 is formed between the outer peripheral edge of the bottom plate 14 and the upper edge of the wall body 23. Both the annular chambers 20 and 21 are connected to a distribution pipe 24 provided annularly around the outer periphery of the discharge port 4 via connection pipes 25 at appropriate intervals in the circumferential direction.
0 and 21, water is supplied from a water supply device 26 via a distribution pipe 24.

つぎに作用につき説明する。スカムと水と水蒸
気を含む吸引気流が吸引物流入口3から負圧室1
内に流入すると、該吸引気流は流路断面の増大に
より減速し、これにより比重の軽い水蒸気および
空気のみが吸引装置連通口2へ吸引される。スカ
ムおよび水は吸引気流から分離されて排出口部4
へ落下し、この落下したスカムおよび水は、イン
ペラ6の遠心作用により負圧室1内の負圧を破る
ことなく、該インペラ6を介して液体槽5内に放
出される。このようにして、スカムおよび水の吸
引気流からの分離排出がなされる。ところで、イ
ンペラ6から放出されるスカムは赤熱状態であ
り、液体槽5内に放出されたときに液体槽5内の
水を沸騰させる。しかし、インペラ6の上下のノ
ズル18,19からは常時もしくは適時に高速で
水が噴出させてあり、この噴射水で生起される水
流により、上記の沸騰でインペラ6の周辺で生じ
た気泡ないし蒸気分は、インペラ6から遠く離れ
た所へ運び去られる。同時にインペラ6の上方お
よび下方で生じた気泡や蒸気分がインペラ6へ近
ずくことも、上記水流によつて防止される。その
ため、インペラ6の出口周辺が沸騰によつて気体
雰囲気での回転がなくインペラ内の負圧に勝つ遠
心水封ができ、水や気泡や水蒸気等がインペラ6
から負圧室1内に逆流することが防止される。し
たがつて、負圧室1内で不用意に沸騰が生じて吸
引力を低下させる問題もなくスカムの逆流も生じ
ない。ノズル18,19から噴出させる水に、液
体槽5内の水よりも低温の水を用いれば、インペ
ラ6の周辺での沸騰が緩和されることから、負圧
室1の水封効果がさらに向上する。このような低
温の水として、例えば吸引装置接続口2と吸引装
置との間で配置される複水器で生じた水を用いれ
ば有効である。
Next, the effect will be explained. A suction airflow containing scum, water, and steam flows from the suction flow inlet 3 to the negative pressure chamber 1.
When flowing into the suction device, the suction airflow is decelerated due to the increase in the cross section of the flow path, so that only water vapor and air with light specific gravity are suctioned into the suction device communication port 2. Scum and water are separated from the suction air stream at the outlet section 4
The fallen scum and water are discharged into the liquid tank 5 through the impeller 6 without breaking the negative pressure in the negative pressure chamber 1 due to the centrifugal action of the impeller 6. In this way, scum and water are separated and discharged from the suction air stream. By the way, the scum discharged from the impeller 6 is in a red-hot state, and when discharged into the liquid tank 5, it boils the water in the liquid tank 5. However, water is ejected at high speed from the nozzles 18 and 19 on the upper and lower sides of the impeller 6 at all times or at appropriate times. The components are transported away from the impeller 6. At the same time, the water flow prevents bubbles and steam generated above and below the impeller 6 from approaching the impeller 6. Therefore, the area around the outlet of the impeller 6 does not rotate in a gas atmosphere due to boiling, creating a centrifugal water seal that overcomes the negative pressure inside the impeller, and water, bubbles, water vapor, etc. are removed from the impeller 6.
This prevents the liquid from flowing back into the negative pressure chamber 1. Therefore, there is no problem of inadvertent boiling occurring in the negative pressure chamber 1 and lowering the suction force, and no backflow of scum occurs. If water at a lower temperature than the water in the liquid tank 5 is used for the water spouted from the nozzles 18 and 19, boiling around the impeller 6 is alleviated, which further improves the water sealing effect of the negative pressure chamber 1. do. As such low-temperature water, it is effective to use, for example, water produced in a double water device disposed between the suction device connection port 2 and the suction device.

なお、上記実施例では、インペラ6に隣接して
ノズル18,19を設けたが、ノズル18,19
の位置はインペラ6の近傍であればよい。またノ
ズル18,19は上記のように環状に形成する代
りに、インペラ6の周方向適当間隔おきに設けて
もよい。
In the above embodiment, the nozzles 18 and 19 were provided adjacent to the impeller 6, but the nozzles 18 and 19
The position may be in the vicinity of the impeller 6. Further, the nozzles 18 and 19 may be provided at appropriate intervals in the circumferential direction of the impeller 6 instead of being formed in an annular shape as described above.

以上説明したように、本発明によれば、インペ
ラから遠ざかる方向へ液体を噴射するノズルをイ
ンペラの近傍に設けたから、赤熱したような高温
の吸引物の分離排出に用いても、該吸引物の熱に
よる沸騰で生じた気泡や蒸気分はインペラの周辺
から運び去られ、そのため負圧室への水や蒸気の
逆流が生じることがなく、負圧室内の負圧の低下
を防止することができる。
As explained above, according to the present invention, since the nozzle that injects the liquid in the direction away from the impeller is provided near the impeller, even if the nozzle is used for separating and discharging hot aspirated materials such as red-hot materials, the aspirated materials can be Bubbles and steam generated by boiling due to heat are carried away from the area around the impeller, so there is no backflow of water or steam to the negative pressure chamber, and a drop in negative pressure in the negative pressure chamber can be prevented. .

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

図面は本発明の一実施例を示し、第1図は分離
装置の断面図、第2図は同部分拡大断面図であ
る。 1……負圧室、2……吸引装置連通口、3……
吸引物流入口、4……排出口部、4a……連通
部、5……液体槽、6……インペラ、8……駆動
軸、18,19……ノズル、20,21……環状
室。
The drawings show one embodiment of the present invention, with FIG. 1 being a sectional view of a separation device, and FIG. 2 being an enlarged sectional view of the same portion. 1... Negative pressure chamber, 2... Suction device communication port, 3...
Suction flow inlet, 4...Discharge port part, 4a...Communication part, 5...Liquid tank, 6...Impeller, 8...Drive shaft, 18, 19...Nozzle, 20, 21...Annular chamber.

Claims (1)

【特許請求の範囲】[Claims] 1 吸引装置に連通した負圧室と、該負圧室に連
通した液体槽と、該液体槽と負圧室との連通部に
設けられたインペラと、該インペラの近傍に配置
されインペラから遠ざかる方向へ液体を噴射する
ノズルとを具備した分離装置。
1. A negative pressure chamber that communicates with the suction device, a liquid tank that communicates with the negative pressure chamber, an impeller that is provided in the communication section between the liquid tank and the negative pressure chamber, and an impeller that is arranged near the impeller and moves away from the impeller. A separation device equipped with a nozzle that injects liquid in a direction.
JP7837878A 1978-06-27 1978-06-27 Separator Granted JPS555726A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7837878A JPS555726A (en) 1978-06-27 1978-06-27 Separator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7837878A JPS555726A (en) 1978-06-27 1978-06-27 Separator

Publications (2)

Publication Number Publication Date
JPS555726A JPS555726A (en) 1980-01-16
JPS6129767B2 true JPS6129767B2 (en) 1986-07-09

Family

ID=13660347

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7837878A Granted JPS555726A (en) 1978-06-27 1978-06-27 Separator

Country Status (1)

Country Link
JP (1) JPS555726A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6490404A (en) * 1987-10-01 1989-04-06 Tomoegawa Paper Co Ltd Production of antidazzle filter

Also Published As

Publication number Publication date
JPS555726A (en) 1980-01-16

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