JP2001281044A - Level measuring device for reverse washing fluid - Google Patents

Level measuring device for reverse washing fluid

Info

Publication number
JP2001281044A
JP2001281044A JP2000095067A JP2000095067A JP2001281044A JP 2001281044 A JP2001281044 A JP 2001281044A JP 2000095067 A JP2000095067 A JP 2000095067A JP 2000095067 A JP2000095067 A JP 2000095067A JP 2001281044 A JP2001281044 A JP 2001281044A
Authority
JP
Japan
Prior art keywords
backwashing
metal powder
level
liquid
powder
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.)
Pending
Application number
JP2000095067A
Other languages
Japanese (ja)
Inventor
Katsuhiko Kato
克彦 加藤
Kazumitsu Sanbondake
一光 三本竹
Koji Kawashima
浩治 川島
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.)
JFE Steel Corp
Original Assignee
Kawasaki 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 Kawasaki Steel Corp filed Critical Kawasaki Steel Corp
Priority to JP2000095067A priority Critical patent/JP2001281044A/en
Publication of JP2001281044A publication Critical patent/JP2001281044A/en
Pending legal-status Critical Current

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  • Measurement Of Levels Of Liquids Or Fluent Solid Materials (AREA)
  • Filtration Of Liquid (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a level measuring device that can continuously use for a long time by preventing the clogging the device. SOLUTION: The level measuring device, which measures the level of the reverse washing fluid 7 in a reverse washing fluid tank 8, is provided with a level gauge 10 and a conduction passage 12 that communicates the fluid of the lower part of the tank 8 to the level gage 10. A metal powder retaining part that precipitate the metal powder is installed on the way of the passage 12. A powder exhausting pipe that communicates a position above an opening and closing valve 21, which opens and closes an exhausting pipe 9 on the exhausting pipe 9, to an iron powder precipitation part of the metal powder retaining part is placed. The passage of the part, on which the exhaust pipe is communicated on the exhausting pipe 9, is throttled.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、電磁フィルタなど
の金属粉除去フィルタを、逆洗液タンクに収容されてい
る逆洗液で逆洗して、当該逆洗液タンクに当該金属粉フ
ィルタに捕捉されている金属粉を回収する循環式の逆洗
装置で使用されて、上記逆洗液タンク内の逆洗液のレベ
ルを計測するレベル計測装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for backwashing a metal powder removing filter such as an electromagnetic filter with a backwashing liquid contained in a backwashing liquid tank, and to apply the metal powder filter to the backwashing liquid tank. The present invention relates to a level measuring device that is used in a circulation type backwashing device that collects captured metal powder and that measures the level of the backwashing solution in the backwashing solution tank.

【0002】[0002]

【従来の技術】例えば、冷間圧延後の鋼帯1には鉄粉が
付着しているので、図1に示すように、当該圧延後の鋼
帯1をクリーニング液2で洗浄する洗浄工程を経た後
に、当該鋼帯1を焼鈍工程に送っている。上記クリーニ
ング液2による洗浄は、鋼帯1を、クリーニング液2を
収容したクリーニング槽3に浸漬したり、クリーニング
液2を鋼帯1表面に吹き付けることで行われる。図1で
は浸漬による場合のみが例示されている。
2. Description of the Related Art For example, since iron powder is adhered to a steel strip 1 after cold rolling, a cleaning step of cleaning the steel strip 1 after rolling with a cleaning liquid 2 as shown in FIG. After passing, the steel strip 1 is sent to an annealing step. The cleaning with the cleaning liquid 2 is performed by immersing the steel strip 1 in a cleaning tank 3 containing the cleaning liquid 2 or spraying the cleaning liquid 2 on the surface of the steel strip 1. FIG. 1 illustrates only the case of immersion.

【0003】上記クリーニング槽3内のクリーング液2
は、プロセス液タンク4内に送られると共にプロセス液
タンク4のきれいなクリーニング液2がクリーニング槽
3に送られることで循環する。また、プロセス液タンク
4のクリーニング液2は、連続的に若しくは間欠的に鉄
粉除去フィルタ5(例えば、電磁フィルタなど)内を濾
過方向に循環してクリーニング液2内に混在する鉄粉を
除去している。符号6は圧送のための濾過ポンプであ
る。なお、上記クリーニング液2は一般に油を含まない
アルカリ液である。
The cleaning liquid 2 in the cleaning tank 3
Is circulated by being sent into the process liquid tank 4 and at the same time the clean liquid 2 in the process liquid tank 4 is sent to the cleaning tank 3. Further, the cleaning liquid 2 in the process liquid tank 4 continuously or intermittently circulates in an iron powder removing filter 5 (for example, an electromagnetic filter) in a filtering direction to remove iron powder mixed in the cleaning liquid 2. are doing. Reference numeral 6 denotes a filtration pump for pressure feeding. The cleaning liquid 2 is generally an alkaline liquid containing no oil.

【0004】そして、鉄粉除去フィルタ5が目詰まりし
たら、プロセス液タンク4からの濾過のための循環を一
時的に停止して、鉄粉除去フィルタ5の逆洗が行われ
る。逆洗とは、洗浄液を濾過方向とは逆方向に流してフ
ィルタを洗浄することを言い、図1では逆洗は、鉄粉除
去フィルタ5内を、出口側から入口側に向けて、つまり
濾過方向Aとは逆方向Bに温水からなる逆洗液7をフィ
ルタ5内に圧送し、フィルタ5の入口側から排出された
鉄粉を含む逆洗液7を捨てることで行われている。この
とき、図1に示す逆洗装置では、逆洗液7を経済的に使
用するために、逆洗液タンク8に収容した逆洗液7を循
環使用し、逆洗が完了した時点で、逆洗液タンク8の底
部に設けられた排出管9を開いて、逆洗液タンク8内の
逆洗液7及び鉄粉を全部排出している。その排出が完了
したら、逆洗液供給用の弁11を開いて逆洗液タンク8
内に逆洗液7を所定レベルまで充填する。このとき、充
填する逆洗液7のレベルを計測するために、レベル計測
装置が使用されて、上記充填する逆洗液7の量を制御し
ている。
When the iron powder removing filter 5 is clogged, the circulation for filtration from the process liquid tank 4 is temporarily stopped, and the iron powder removing filter 5 is backwashed. Backwashing refers to washing a filter by flowing a washing liquid in a direction opposite to a filtration direction. In FIG. 1, backwashing moves the inside of an iron powder removal filter 5 from an outlet side to an inlet side, that is, the filtration. This is performed by feeding backwash liquid 7 made of warm water into filter 5 in the direction B opposite to direction A, and discarding backwash liquid 7 containing iron powder discharged from the inlet side of filter 5. At this time, in the backwashing device shown in FIG. 1, in order to use the backwashing solution 7 economically, the backwashing solution 7 contained in the backwashing solution tank 8 is circulated and used, and when the backwashing is completed, The drain pipe 9 provided at the bottom of the backwash liquid tank 8 is opened to discharge all the backwash liquid 7 and iron powder in the backwash liquid tank 8. When the discharge is completed, the backwash liquid supply valve 11 is opened and the backwash liquid tank 8 is opened.
The inside is filled with a backwash liquid 7 to a predetermined level. At this time, in order to measure the level of the backwash liquid 7 to be filled, a level measuring device is used to control the amount of the backwash liquid 7 to be filled.

【0005】レベル計測装置は、逆洗液タンク8下部と
レベル計10との間を導通路12によって連通させるこ
とで、逆洗液タンク8下部での逆洗液7の圧をレベル計
10に伝達し、レベル計10でその圧に基づき逆洗液7
のレベルを計測している。レベル計10は、例えば水圧
計から構成される。
The level measuring device communicates the pressure of the backwashing liquid 7 at the lower part of the backwashing tank 8 to the levelmeter 10 by connecting the lower part of the backwashing liquid tank 8 and the level meter 10 by a conduction path 12. The backwash liquid 7 is transmitted by the level meter 10 based on the pressure.
Is measuring the level. The level meter 10 is composed of, for example, a water pressure gauge.

【0006】[0006]

【発明が解決しようとする課題】上記構成のレベル計測
装置にあっては、経時的に、逆洗液7中の鉄粉の移動に
よってレベル計10や導通路12が目詰まりして、レベ
ル計10による計測値が実際の値よりも低くなってしま
い計測精度が悪くなる。このため、レベル計測装置の洗
浄を定期的に行う必要がある。
In the level measuring apparatus having the above-mentioned structure, the level meter 10 and the conduction path 12 are clogged with the movement of the iron powder in the backwashing liquid 7 with the passage of time. The measured value by 10 becomes lower than the actual value, and the measurement accuracy is deteriorated. Therefore, it is necessary to periodically clean the level measuring device.

【0007】また、レベル計測装置の洗浄を行うとき
は、逆洗液タンク8中の逆洗液7のレベル制御ができな
くなるので、その期間は逆洗ができなくなるという問題
がある。本発明は、上記のような問題点に着目してなさ
れたもので、レベル計測装置の目詰まりを防止して長期
に亘ってレベル計測が可能なレベル計測装置を提供する
ことを課題としている。
When the level measuring device is cleaned, the level of the backwashing liquid 7 in the backwashing liquid tank 8 cannot be controlled, so that the backwashing cannot be performed during that period. SUMMARY OF THE INVENTION The present invention has been made in view of the above problems, and has as its object to provide a level measurement device capable of preventing a level measurement device from being clogged and capable of measuring a level over a long period of time.

【0008】[0008]

【課題を解決するための手段】上記課題を解決するため
に、本発明のうち請求項1に記載した発明は、逆洗液タ
ンク内の逆洗液を、濾過方向とは逆方向に金属粉除去フ
ィルタ内に循環させることで、金属粉除去フィルタに捕
捉されている金属粉を、逆洗液と共に上記逆洗液タンク
内に回収した後、上記逆洗液タンクの底部に接続する排
出管を開いて逆洗液及び金属粉を逆洗液タンクから排出
する逆洗装置で使用されて、上記逆洗液タンク内の逆洗
液のレベルを計測するレベル計と、上記逆洗液タンクの
下部の液を上記レベル計に連通させる導通路とを備えた
レベル計測装置において、上記導通路の途中に、金属粉
を捕捉して沈殿させる金属粉溜まりを介装したことを特
徴とするものである。
In order to solve the above-mentioned problems, the present invention as set forth in claim 1 of the present invention is directed to a method in which a backwashing liquid in a backwashing liquid tank is washed with metal powder in a direction opposite to a filtration direction. By circulating in the removal filter, the metal powder captured by the metal powder removal filter is recovered together with the backwash liquid in the backwash liquid tank, and then a discharge pipe connected to the bottom of the backwash liquid tank is provided. Used in a backwashing device that opens and discharges the backwashing solution and metal powder from the backwashing solution tank, a level meter that measures the level of the backwashing solution in the backwashing solution tank, and a lower part of the backwashing solution tank. A conductive path for communicating the liquid with the level meter, wherein a metal powder reservoir for capturing and precipitating metal powder is interposed in the middle of the conductive path. .

【0009】次に、請求項2に記載した発明は、請求項
1に記載した構成に対し、上記排出管における当該排出
管を開閉する開閉弁よりも上流側位置と、上記金属粉溜
まりの金属粉沈殿部とを連通する粉体排出路を設けると
共に、当該排出管における粉体排出路が連通する部分の
流路を絞ったことを特徴とするものである。
Next, according to a second aspect of the present invention, in the configuration according to the first aspect, a position of the discharge pipe on the upstream side of an opening / closing valve for opening and closing the discharge pipe and a metal in the metal powder reservoir are provided. A powder discharge path communicating with the powder sedimentation section is provided, and a flow path of a portion of the discharge pipe communicating with the powder discharge path is narrowed.

【0010】[0010]

【発明の実施の形態】次に、本発明の実施形態について
図面を参照して説明する。なお、上記従来例と同一の装
置などについては、同一の符号を付して説明する。ま
た、本実施形態では、上記従来例で説明した、鉄粉除去
フィルタ5を逆洗する逆洗装置の逆洗液タンク8で使用
されるレベル計測装置で例示する。
Next, embodiments of the present invention will be described with reference to the drawings. It should be noted that the same devices and the like as those in the above-described conventional example are denoted by the same reference numerals and described. In the present embodiment, a level measuring device used in the backwashing liquid tank 8 of the backwashing device for backwashing the iron powder removing filter 5 described in the above-described conventional example will be exemplified.

【0011】本実施形態のレベル計測装置は、図2に示
すように、水位計からなるレベル計10と、導通路12
と、金属粉溜まり部である鉄粉溜まり20と、粉体排出
路を構成する粉体排出管22とを備える。導通路12
は、逆洗液タンク8の下部とレベル計10とを連通し
て、逆洗液7の圧をレベル計10に伝達するものであ
る。
As shown in FIG. 2, the level measuring device of the present embodiment includes a level
And an iron powder reservoir 20, which is a metal powder reservoir, and a powder discharge tube 22 forming a powder discharge passage. Conduction path 12
Communicates the pressure of the backwash liquid 7 to the level meter 10 by communicating the lower part of the backwash liquid tank 8 with the level meter 10.

【0012】鉄粉溜まり20は、導通路12の途中に介
装されていている。その鉄粉溜まり20は、図3に示す
ように、2つの室20a、20bが隔壁20cで画成さ
れると共に上部で連通して構成され、該第1室20a側
が逆洗液タンク8に連通し、第2室20b側がレベル計
10に連通している。そして、タンク側の第1室20a
から液体だけがレベル側の第2室20bに移動して、比
重の大きい鉄粉は第1室20aにトラップされて沈殿し
堆積するようになっている。なお、鉄粉溜まり20は、
鉄粉をトラップして沈殿できるものであれば上記構成に
限定されない。
The iron powder reservoir 20 is interposed in the conduction path 12. As shown in FIG. 3, the iron powder reservoir 20 has two chambers 20a and 20b defined by a partition wall 20c and communicates with an upper portion thereof, and the first chamber 20a communicates with the backwash liquid tank 8. The second chamber 20b communicates with the level meter 10. And the first chamber 20a on the tank side
, Only the liquid moves to the second chamber 20b on the level side, and the iron powder having a large specific gravity is trapped in the first chamber 20a to precipitate and deposit. In addition, the iron powder pool 20
The configuration is not limited to the above configuration as long as it can trap and precipitate iron powder.

【0013】また、上記第1室20aの底部に粉体排出
管22の一端が連通し、当該粉体排出管22の端部は、
逆洗液タンク8に連通する排出管9に接続されている。
その接続位置は開閉弁21よりも上流側で有ればよい
が、本実施形態では開閉弁21上流側のフランジ部23
に接続している。そのフランジ部23の位置における排
出管9の流路は、図4に示すように絞られていて流速が
速くなるように、つまり負圧によって粉体排出管22側
からの吸い込みを促進するようにしている。
One end of a powder discharge pipe 22 communicates with the bottom of the first chamber 20a.
It is connected to a discharge pipe 9 communicating with the backwash liquid tank 8.
The connection position may be on the upstream side of the on-off valve 21, but in the present embodiment, the flange portion 23 on the upstream side of the on-off valve 21
Connected to The flow path of the discharge pipe 9 at the position of the flange portion 23 is narrowed as shown in FIG. 4 so that the flow velocity is high, that is, suction from the powder discharge pipe 22 side is promoted by negative pressure. ing.

【0014】上記構成のレベル計測装置を備えた逆洗液
タンク8にあっては、逆洗液タンク8内の逆洗液7中の
鉄粉が導通路12側に移動しても鉄粉溜まり20の第1
室20aにトラップされてレベル計10に移動すること
が防止される。第1室20aにトラップされた鉄粉は、
第1室20aの底に沈殿すると共に、当該底に連通する
粉体排出管22内を落下していく。
In the backwash liquid tank 8 provided with the level measuring device having the above structure, the iron powder accumulates even if the iron powder in the backwash liquid 7 in the backwash liquid tank 8 moves to the conduction path 12 side. 20 first
It is prevented from being trapped in the chamber 20a and moving to the level meter 10. The iron powder trapped in the first chamber 20a
The particles settle on the bottom of the first chamber 20a and fall in the powder discharge pipe 22 communicating with the bottom.

【0015】これによって、鉄粉の目詰まりによってレ
ベル計10の計測精度が劣化することが、防止される。
また、鉄粉除去フィルタ5の逆洗を循環式で実施後、逆
洗液タンク8内に、フィルタ5に捕捉されていた鉄粉を
捕捉したら、開閉弁21を開いて排出管9を通じて逆洗
液タンク8内の逆洗液7及び鉄粉を下方に落下して排出
する。
This prevents the measurement accuracy of the level meter 10 from deteriorating due to the clogging of the iron powder.
After the backwashing of the iron powder removing filter 5 is performed in a circulating manner, and after the iron powder captured by the filter 5 is captured in the backwashing liquid tank 8, the on-off valve 21 is opened and the backwashing is performed through the discharge pipe 9. The backwash liquid 7 and the iron powder in the liquid tank 8 fall down and are discharged.

【0016】このとき、フランジ部23、つまり粉体排
出管22の接続部は絞られているため、負圧となって粉
体排出管22内の鉄粉が吸引されて、排出管9及び第1
室20aに堆積していた鉄粉及び当該導通路12内の液
抜きが、自動的に行われる。以上の結果、自動的に導通
路12の洗浄が行われる結果、レベル計測装置は、長期
間連続して使用可能となる。
At this time, since the flange portion 23, that is, the connection portion of the powder discharge tube 22 is narrowed, a negative pressure is applied and the iron powder in the powder discharge tube 22 is sucked, so that the discharge tube 9 and the powder 1
The iron powder deposited in the chamber 20a and the liquid in the passage 12 are automatically drained. As a result, the cleaning of the conduction path 12 is performed automatically, so that the level measuring device can be used continuously for a long time.

【0017】ここで、本実施形態では、鉄粉溜まり20
の第1室20aを排出管9に連通させているが、これに
限定されない。例えば、上記第1室20aに弁を設け
て、適宜弁を開いて液抜きを行い、第1室20aに沈殿
した鉄粉の除去を行うようにしても良い。また、上記実
施形態では、金属粉として鉄粉を例示しているがアルミ
ニウム粉などの他の金属粉を除去するフィルタ5に対す
る逆洗用のタンクにも適用可能である。
In this embodiment, the iron powder pool 20
Although the first chamber 20a is communicated with the discharge pipe 9, the present invention is not limited to this. For example, a valve may be provided in the first chamber 20a, the valve may be opened as appropriate, and the liquid may be drained to remove the iron powder precipitated in the first chamber 20a. In the above embodiment, iron powder is exemplified as the metal powder, but the present invention is also applicable to a tank for backwashing the filter 5 for removing other metal powder such as aluminum powder.

【0018】[0018]

【発明の効果】以上説明してきたように、本発明の逆洗
液のレベル計測装置では、逆洗液タンク内の逆洗液のレ
ベル検出が長期間安定して可能となるという効果があ
る。特に、請求項2に係る発明を採用すると、逆洗液タ
ンク内に逆洗液を排出する際にレベル計測装置の導通路
の洗浄が行われるという効果がある。
As described above, the backwash liquid level measuring apparatus of the present invention has an effect that the level of the backwash liquid in the backwash liquid tank can be stably detected for a long period of time. In particular, when the invention according to claim 2 is adopted, there is an effect that the conduction path of the level measurement device is cleaned when the backwash liquid is discharged into the backwash liquid tank.

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

【図1】フィルタによる濾過と当該フィルタの循環式の
逆洗について説明する構成図である。
FIG. 1 is a configuration diagram illustrating filtration by a filter and circulating backwashing of the filter.

【図2】本発明に基づく実施形態に係るレベル計測装置
を示す図である。
FIG. 2 is a diagram showing a level measuring device according to an embodiment based on the present invention.

【図3】本発明に基づく実施形態に係る鉄粉溜まりを示
す図である。
FIG. 3 is a diagram showing an iron powder pool according to an embodiment according to the present invention.

【図4】本発明に基づく実施形態に係る粉体排出管を接
続する排出管部分を示す図である。
FIG. 4 is a view showing a discharge pipe portion connecting a powder discharge pipe according to an embodiment according to the present invention.

【符号の説明】[Explanation of symbols]

1 鋼帯 2 クリーニング液 3 クリーニング槽 4 プロセス液タンク 5 鉄粉除去フィルタ 6 濾過用ポンプ 7 逆洗液 8 逆洗液タンク 9 排出管 10 レベル計 11 弁 12 導通路 20 鉄粉溜まり 20a 第1室 20b 第2室 20c 隔壁 21 開閉弁 22 粉体排出管 23 フランジ部 A 濾過方向 B 逆洗方向 C レベル計測装置 DESCRIPTION OF SYMBOLS 1 Steel strip 2 Cleaning liquid 3 Cleaning tank 4 Process liquid tank 5 Iron powder removal filter 6 Filtration pump 7 Backwash liquid 8 Backwash liquid tank 9 Discharge pipe 10 Level meter 11 Valve 12 Conduction path 20 Iron powder pool 20a First chamber 20b Second chamber 20c Partition wall 21 Open / close valve 22 Powder discharge pipe 23 Flange part A Filtration direction B Backwash direction C Level measurement device

───────────────────────────────────────────────────── フロントページの続き (72)発明者 川島 浩治 千葉県千葉市中央区川崎町1番地 川崎製 鉄株式会社千葉製鉄所内 Fターム(参考) 2F014 AA17 AB01 4D066 BB12 EA06 EA12 FA02  ──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Koji Kawashima 1 Kawasaki-cho, Chuo-ku, Chiba-shi, Chiba F-term in the Chiba Works, Chiba Works (reference) 2F014 AA17 AB01 4D066 BB12 EA06 EA12 FA02

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 逆洗液タンク内の逆洗液を、濾過方向と
は逆方向に金属粉除去フィルタ内に循環させることで、
金属粉除去フィルタに捕捉されている金属粉を、逆洗液
と共に上記逆洗液タンク内に回収した後、上記逆洗液タ
ンクの底部に接続する排出管を開いて逆洗液及び金属粉
を逆洗液タンクから排出する逆洗装置で使用されて、上
記逆洗液タンク内の逆洗液のレベルを計測するレベル計
と、上記逆洗液タンクの下部の液を上記レベル計に連通
させる導通路とを備えたレベル計測装置において、 上記導通路の途中に、金属粉を捕捉して沈殿させる金属
粉溜まりを介装したことを特徴とする逆洗液のレベル計
測装置。
1. A backwash liquid in a backwash liquid tank is circulated through a metal powder removal filter in a direction opposite to a filtration direction,
After collecting the metal powder trapped in the metal powder removal filter in the above-mentioned backwashing liquid tank together with the backwashing liquid, open the discharge pipe connected to the bottom of the above-mentioned backwashing liquid tank to remove the backwashing liquid and the metal powder. Used in a backwashing device that discharges from the backwashing liquid tank, a level meter for measuring the level of the backwashing liquid in the backwashing liquid tank, and a liquid at a lower portion of the backwashing liquid tank communicates with the level meter. A level measuring device having a conduction path, wherein a metal powder reservoir for capturing and precipitating metal powder is interposed in the middle of the conduction path.
【請求項2】 上記排出管における当該排出管を開閉す
る開閉弁よりも上流側位置と、上記金属粉溜まりの金属
粉沈殿部とを連通する粉体排出路を設けると共に、当該
排出管における粉体排出路が連通する部分の流路を絞っ
たことを特徴とする請求項1に記載した逆洗液のレベル
計測装置。
2. A powder discharge path communicating between a position of the discharge pipe upstream of an on-off valve for opening and closing the discharge pipe and a metal powder sedimentation section of the metal powder reservoir, and a powder discharge passage in the discharge pipe. 2. The level measuring device for a backwash liquid according to claim 1, wherein a flow passage at a portion where the body discharge passage communicates is narrowed.
JP2000095067A 2000-03-30 2000-03-30 Level measuring device for reverse washing fluid Pending JP2001281044A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000095067A JP2001281044A (en) 2000-03-30 2000-03-30 Level measuring device for reverse washing fluid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000095067A JP2001281044A (en) 2000-03-30 2000-03-30 Level measuring device for reverse washing fluid

Publications (1)

Publication Number Publication Date
JP2001281044A true JP2001281044A (en) 2001-10-10

Family

ID=18610018

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000095067A Pending JP2001281044A (en) 2000-03-30 2000-03-30 Level measuring device for reverse washing fluid

Country Status (1)

Country Link
JP (1) JP2001281044A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101416428B1 (en) * 2013-12-23 2014-07-10 한국지질자원연구원 Reactor for Recovering Metal, System for Recovering Metal and Method for Recovering Metal
KR101416429B1 (en) * 2014-01-08 2014-07-10 한국지질자원연구원 Reactor for Recovering Metal and System for Recovering Metal
KR101461502B1 (en) * 2013-03-18 2014-11-18 (주)다남이엔이 System for Recovering Metal using Electrolysis Apparatus and Method for Recovering Metal using Electrolysis Apparatus
WO2015099383A1 (en) * 2013-12-23 2015-07-02 한국지질자원연구원 Metal recovery reactor and metal recovery system
GB2585373A (en) * 2019-07-04 2021-01-13 Linde Ag Measurement instrumentation for a process vessel and process vessel and process vessel system

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101461502B1 (en) * 2013-03-18 2014-11-18 (주)다남이엔이 System for Recovering Metal using Electrolysis Apparatus and Method for Recovering Metal using Electrolysis Apparatus
KR101416428B1 (en) * 2013-12-23 2014-07-10 한국지질자원연구원 Reactor for Recovering Metal, System for Recovering Metal and Method for Recovering Metal
WO2015099383A1 (en) * 2013-12-23 2015-07-02 한국지질자원연구원 Metal recovery reactor and metal recovery system
CN105849318A (en) * 2013-12-23 2016-08-10 韩国地质资源研究院 Metal recovery reactor and metal recovery system
KR101416429B1 (en) * 2014-01-08 2014-07-10 한국지질자원연구원 Reactor for Recovering Metal and System for Recovering Metal
GB2585373A (en) * 2019-07-04 2021-01-13 Linde Ag Measurement instrumentation for a process vessel and process vessel and process vessel system

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