JP2001120911A - Rotary filtering device with filter medium cleaning function - Google Patents

Rotary filtering device with filter medium cleaning function

Info

Publication number
JP2001120911A
JP2001120911A JP30963099A JP30963099A JP2001120911A JP 2001120911 A JP2001120911 A JP 2001120911A JP 30963099 A JP30963099 A JP 30963099A JP 30963099 A JP30963099 A JP 30963099A JP 2001120911 A JP2001120911 A JP 2001120911A
Authority
JP
Japan
Prior art keywords
liquid
filter medium
suspended substance
tank
liquid tank
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
JP30963099A
Other languages
Japanese (ja)
Inventor
Katsumi Mogi
克己 茂木
Akira Ueda
晃 上田
Koichi Kato
耕一 加藤
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.)
Mitsubishi Materials Corp
Original Assignee
Mitsubishi Materials 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 Mitsubishi Materials Corp filed Critical Mitsubishi Materials Corp
Priority to JP30963099A priority Critical patent/JP2001120911A/en
Publication of JP2001120911A publication Critical patent/JP2001120911A/en
Pending legal-status Critical Current

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  • Filtration Of Liquid (AREA)

Abstract

PROBLEM TO BE SOLVED: To efficiently catch and recover suspended material contained in a liquid. SOLUTION: A supply means 14 supplies the liquid 12 containing the suspended material 11 into a liquid tank 13 and a double cylindrical body 16 is provided in the liquid tank 13 rotatably around an axial line with a part of an outer cylinder 17 and a part of an inner cylinder 18 projected from a liquid surface. Filter medium 21 is accommodated in a filtration space 19 so as to be able to flow and not to be able to leak therefrom and the filter medium catches the suspended material. A rotating means 43 rotating-drives the double cylindrical body and a draining means 46 discharges the liquid passed through the filter medium from inside of the inner cylinder to outside of the liquid tank. Partition plates partition the filtration space into small spaces, a cleaning nozzle 54 above the outer cylinder sprays a cleaning liquid 60 onto the filter medium in the small space above the liquid surface to remove the suspended material from the filter medium. A liquid collecting vessel 63, which is located inside the inner cylinder and is fixed to the liquid tank 13, collects the cleaning liquid sprayed from the cleaning nozzle together with the suspended material and a guiding tube 64 guides the cleaning liquid containing the suspended material in the liquid collecting vessel 63 to an unfiltered liquid outside the double cylindrical body.

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、地熱熱水等の液体
中に含まれる過飽和シリカ等の懸濁物質を捕捉・回収す
る回転濾過装置に関する。更に詳しくは懸濁物質を捕捉
した濾過材を洗浄する機能を有する回転濾過装置に関す
るものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a rotary filtration device for capturing and recovering suspended substances such as supersaturated silica contained in a liquid such as geothermal hot water. More specifically, the present invention relates to a rotary filtration device having a function of washing a filtering material having captured suspended substances.

【0002】[0002]

【従来の技術】本出願人は、この種の濾過装置として、
略円筒状の流体流通性容器がその軸心を中心として周方
向に回転可能に配設され、この容器の内部に外部から流
入する流体中の懸濁物質を捕捉分離する濾過材が流動可
能に収容され、更に流動撹拌補助手段により濾過材の流
動が促進されるように構成された流体濾過装置を特許出
願した(特開平11−90116号)。この流体濾過装
置では、流動撹拌補助手段が流体流通性容器内に周方向
に所定の間隔をあけて設けられた板状の掻き上げ板、或
いは撹拌用飯給剤及び撹拌用棒部材である。また流体流
通性容器の外周面又は上方には付着物排除部材、或いは
流体噴出洗浄機構が設けられる。付着物排除部材として
は、流体流通性容器の外周面に接触するブラシ部材が挙
げられ、流体噴出洗浄機構としては、流体の上方に流体
流通性容器の外周面に向けて配設された噴射ノズルと、
流体を上記噴射ノズルに圧送するポンプとを有するもの
が挙げられる。
2. Description of the Related Art The present applicant has proposed a filter device of this type,
A substantially cylindrical fluid circulating container is disposed so as to be rotatable in the circumferential direction around its axis, and a filtering material for capturing and separating suspended substances in a fluid flowing in from the outside into the container is allowed to flow. A patent has been filed for a fluid filtration device that is accommodated and configured so that the flow of the filter medium is promoted by the flow stirring assisting means (Japanese Patent Application Laid-Open No. H11-90116). In this fluid filtration device, the flow-stirring assisting means is a plate-shaped scraping plate provided at a predetermined interval in the circumferential direction in the fluid-flowable container, or a stirring rice feed and a stirring rod member. An adhering matter removing member or a fluid ejection cleaning mechanism is provided on the outer peripheral surface or above the fluid circulating container. As the attached matter removing member, a brush member that comes into contact with the outer peripheral surface of the fluid circulating container may be mentioned, and as the fluid ejection cleaning mechanism, an injection nozzle disposed above the fluid and directed toward the outer peripheral surface of the fluid circulating container. When,
A pump having a pump for pumping a fluid to the spray nozzle.

【0003】このように構成された流体濾過装置では、
流体流通性容器の回転時に濾過材が流動撹拌補助手段に
接触してその流動が促進されるので、濾過材間や濾過材
表面に付着した異物や汚泥が流体流通性容器外に排出さ
れると同時に、濾過材の一部が摩滅して流体中に溶出し
拡散される。濾過材が摩滅すると、その物理化学的機能
が回復され、また濾過材の粒径が小さくなると、微少な
懸濁物質を捕捉可能になり、更に濾過材が流体流通性容
器の目開きより小さくなると、この容器から排出され
る。一方、流体流通性容器の外周面に付着した異物や汚
泥等の付着物は付着物排除部材や流体噴出洗浄機構によ
り除去される。この結果、流体中の懸濁物質を濾過分離
することができるとともに、濾過材により捕捉分離され
た濾過材とともに流体中に排出することができる。
[0003] In the fluid filtration device configured as described above,
During rotation of the fluid-flow container, the filter medium comes into contact with the flow-stirring assisting means to promote the flow, so that foreign matter or sludge adhering between the filter materials or on the filter medium surface is discharged out of the fluid-flow container. At the same time, a portion of the filter material is worn and eluted and diffused into the fluid. When the filter media is worn, its physicochemical function is restored, and when the particle size of the filter media becomes smaller, it becomes possible to capture fine suspended substances, and when the filter media becomes smaller than the opening of the fluid-flowable container. Is discharged from this container. On the other hand, extraneous matter such as foreign matter and sludge adhering to the outer peripheral surface of the fluid circulating container is removed by the extraneous matter removing member or the fluid ejection cleaning mechanism. As a result, the suspended substance in the fluid can be separated by filtration, and can be discharged into the fluid together with the filter medium captured and separated by the filter medium.

【0004】[0004]

【発明が解決しようとする課題】しかし、上記従来の特
開平11−90116号に記載された流体濾過装置で
は、流動撹拌補助手段だけでは濾過材の流動を十分に促
進させることができず、濾過材による懸濁物質の捕捉能
力が低下するおそれがあった。本発明の目的は、懸濁物
質を捕捉した濾過材を順次洗浄することにより、濾過材
による懸濁物質の捕捉能力を低下させることなく、液体
に含まれる懸濁物質を濾過材により効率良く捕捉するこ
とができる濾過材洗浄機能付回転濾過装置を提供するこ
とにある。本発明の別の目的は、濾過材から離脱した懸
濁物質を効率良く回収することができる濾過材洗浄機能
付回転濾過装置を提供することにある。
However, in the conventional fluid filtration apparatus described in Japanese Patent Application Laid-Open No. H11-90116, the flow of the filtration material cannot be sufficiently promoted only by the flow stirring assist means. There is a possibility that the ability of the material to capture suspended substances may be reduced. An object of the present invention is to efficiently capture suspended substances contained in a liquid with a filter medium without decreasing the ability of the filter medium to capture suspended substances by sequentially washing the filter medium that has captured the suspended substances. It is an object of the present invention to provide a rotary filtration device with a filtering material washing function. Another object of the present invention is to provide a rotary filtration device with a filtration material washing function that can efficiently collect suspended substances separated from the filtration material.

【0005】[0005]

【課題を解決するための手段】請求項1に係る発明は、
図1及び図2に示すように、懸濁物質11を含む液体1
2が貯留される液槽13と、液槽13に液体12を供給
する供給手段14と、通液性外筒17とこの外筒17に
略同心の通液性内筒18を有し軸線を略水平方向にかつ
外筒17と内筒18の一部を液体12の液面から突出さ
せて液体12中を軸線を中心に周方向に回転可能に液槽
13内に設けられた二重筒体16と、外筒17と内筒1
8により囲まれた濾過空間19に流動可能にかつ濾過空
間19から漏出不能に収容され懸濁物質11を捕捉して
液体12から分離する濾過材21と、二重筒体16を回
転駆動する回転手段43と、液槽13内の液面を一定に
保ちながら液槽13に供給されかつ濾過材21を通った
液体12を内筒18の内部から液槽13の外部に排出す
る排液手段46とを備えた回転濾過装置である。その特
徴ある構成は、軸線を中心に放射状に設けられ濾過空間
19を複数の小空間19bに区画する複数の仕切り板1
9aと、外筒17の上方又は内筒18の内部に設けられ
液面の上方に位置する小空間19b内の濾過材21に洗
浄液60を噴射して濾過材21が捕捉した懸濁物質11
を濾過材21から離脱させる洗浄ノズル54と、内筒1
8の内部に液面の上方に位置する小空間19bに対向し
て設けられかつ液槽13に固定され洗浄ノズル54から
噴射された洗浄液60を濾過材21から離脱した懸濁物
質11とともに集液する集液容器63と、集液容器63
に貯留された懸濁物質11を含む洗浄液60を二重筒体
16外部の未濾過液体12に導く誘導管64とを備えた
ところにある。
The invention according to claim 1 is
As shown in FIG. 1 and FIG.
A liquid tank 13 for storing the liquid 2, a supply means 14 for supplying the liquid 12 to the liquid tank 13, a liquid-permeable outer cylinder 17, and a liquid-permeable inner cylinder 18 substantially concentric with the outer cylinder 17. A double cylinder provided in the liquid tank 13 so as to be substantially horizontal and part of the outer cylinder 17 and the inner cylinder 18 protruding from the liquid surface of the liquid 12 so as to be rotatable in the liquid 12 in the circumferential direction about the axis. Body 16, outer cylinder 17 and inner cylinder 1
A filter medium 21 that is housed in a filtration space 19 surrounded by the filter 8 so as to be able to flow and cannot leak from the filtration space 19 and captures the suspended substance 11 and separates it from the liquid 12, and a rotation that rotationally drives the double cylinder 16. Means 43 and a drainage means 46 for discharging the liquid 12 supplied to the liquid tank 13 and passing through the filter medium 21 from the inside of the inner cylinder 18 to the outside of the liquid tank 13 while keeping the liquid level in the liquid tank 13 constant. And a rotary filtration device comprising: The characteristic configuration is that a plurality of partition plates 1 are provided radially about the axis to partition the filtration space 19 into a plurality of small spaces 19b.
9a and the suspended substance 11 captured by the filter medium 21 by injecting the cleaning liquid 60 into the filter medium 21 in the small space 19b provided above the outer cylinder 17 or inside the inner cylinder 18 and located above the liquid level.
Cleaning nozzle 54 for removing air from filter medium 21 and inner cylinder 1
The cleaning liquid 60 fixed to the liquid tank 13 and sprayed from the cleaning nozzle 54 is collected together with the suspended substance 11 separated from the filter medium 21 and provided in the interior of the nozzle 8 so as to face the small space 19b located above the liquid surface. Liquid collecting container 63 and liquid collecting container 63
And a guide tube 64 for guiding the washing liquid 60 containing the suspended substance 11 stored in the non-filtration liquid 12 outside the double cylinder 16.

【0006】この請求項1に記載された濾過材洗浄機能
付回転濾過装置では、供給手段14により液体12を液
槽13に供給すると、液槽13内の液体12の液面は徐
々に上昇し、その液面が二重筒体16に達すると、液体
12が通液性外筒17から濾過空間19に流入し、液体
12中の懸濁物質11が濾過材21により捕捉されて分
離し、更に濾過された液体12は通液性内筒18の内部
に流入する。液槽13に供給された液体12の液面が二
重筒体16の軸線近傍まで達すると、内筒18の内部の
濾過された液体12は排液手段43により液槽13の外
部に排出される。一方、回転手段43により二重筒体1
6を回転させることにより、液体12の液面より上方に
出現する小空間19b内の濾過材21が洗浄ノズル54
から噴射される洗浄液60により洗浄され、濾過材21
から離脱した懸濁物質11が洗浄液60とともに集液容
器63内に溜る。集液容器63に溜った懸濁物質11を
含む洗浄液60は誘導管64を通って二重筒体16外の
液槽13内に導かれ、洗浄液60中の懸濁物質11は液
槽13の底部に堆積する。
[0006] In the rotary filtration device with the filter material washing function according to the first aspect, when the supply means 14 supplies the liquid 12 to the liquid tank 13, the liquid level of the liquid 12 in the liquid tank 13 gradually rises. When the liquid level reaches the double cylinder 16, the liquid 12 flows from the liquid-permeable outer cylinder 17 into the filtration space 19, and the suspended substance 11 in the liquid 12 is captured and separated by the filter medium 21, Further, the filtered liquid 12 flows into the liquid-permeable inner cylinder 18. When the liquid level of the liquid 12 supplied to the liquid tank 13 reaches near the axis of the double cylinder 16, the filtered liquid 12 inside the inner cylinder 18 is discharged to the outside of the liquid tank 13 by the drainage means 43. You. On the other hand, the double cylinder 1
6, the filter medium 21 in the small space 19b appearing above the liquid level of the liquid 12 is removed from the cleaning nozzle 54.
The filter medium 21 is cleaned by the cleaning liquid 60 injected from the
The suspended substance 11 released from the reservoir collects together with the washing liquid 60 in the liquid collecting container 63. The cleaning liquid 60 containing the suspended substance 11 stored in the liquid collecting container 63 is guided into the liquid tank 13 outside the double cylinder 16 through the guide tube 64, and the suspended substance 11 in the cleaning liquid 60 is transferred to the liquid tank 13. Deposits on the bottom.

【0007】請求項2に係る発明は、請求項1に係る発
明であって、更に図1及び図2に示すように、回転手段
43が二重筒体16を小空間19b単位で間欠的に回転
駆動するように構成されたことを特徴とする。この請求
項2に記載された濾過材洗浄機能付回転濾過装置では、
液槽13に液体12を供給して所定時間毎に小空間19
b単位で二重筒体16を回転駆動すると、懸濁物質11
を捕捉した濾過材21が収容された小空間19bが順
次、液体12の液面より上方に出現するので、液槽13
への液体12の供給を停止することなく、懸濁物質11
を捕捉した濾過材21を順次洗浄することができ、集液
容器63により洗浄液60を濾過材21から離脱した懸
濁物質11とともに確実に集液することができる。
The invention according to claim 2 is the invention according to claim 1, and as shown in FIGS. 1 and 2, the rotating means 43 intermittently moves the double cylinder 16 in small space 19b units. It is configured to be driven to rotate. In the rotary filtration device with a filter material washing function according to claim 2,
The liquid 12 is supplied to the liquid tank 13 and the small space 19 is supplied every predetermined time.
When the double cylinder 16 is rotationally driven in units of b, the suspended substance 11
The small space 19b accommodating the filter medium 21 that has captured the liquid 12 appears sequentially above the liquid level of the liquid 12, so that the liquid tank 13
Without stopping the supply of liquid 12 to the
Can be sequentially washed, and the washing solution 60 can be surely collected by the collecting container 63 together with the suspended substance 11 separated from the filtering material 21.

【0008】請求項3に係る発明は、請求項1又は2に
係る発明であって、更に図1及び図2に示すように、洗
浄液60が液槽13に供給される懸濁物質11を含む液
体12又は懸濁物質11が除去された液体12であるこ
とを特徴とする。この請求項3に記載された濾過材洗浄
機能付回転濾過装置では、洗浄液60が液槽13に供給
される液体12又は濾過材21にて濾過された液体12
と同一であるので、洗浄液60を新たに用意せずに済
む。
[0008] The invention according to claim 3 is the invention according to claim 1 or 2, further comprising a suspended substance 11 in which a cleaning liquid 60 is supplied to a liquid tank 13 as shown in FIGS. The liquid 12 or the liquid 12 from which the suspended substance 11 has been removed is characterized. In the rotary filtration device with a filter material cleaning function according to the third aspect, the cleaning liquid 60 is supplied to the liquid tank 13 or the liquid 12 filtered by the filter material 21.
Therefore, it is not necessary to newly prepare the cleaning liquid 60.

【0009】請求項4に係る発明は、請求項1ないし3
いずれかに係る発明であって、更に図1及び図2に示す
ように、上端が液槽13内の液面より上方に位置するよ
うに集液容器63が設けられたことを特徴とする。この
請求項4に記載された濾過材洗浄機能付回転濾過装置で
は、濾過材21により濾過された液体12と、濾過材2
1から離脱した懸濁物質11を含む洗浄液60とが混ざ
るのを防止できる。
The invention according to claim 4 is the invention according to claims 1 to 3
The invention according to any of the above aspects, further characterized in that a liquid collecting container 63 is provided so that an upper end is located above a liquid level in the liquid tank 13 as shown in FIGS. 1 and 2. In the rotary filtration device with a filtration material washing function according to the fourth aspect, the liquid 12 filtered by the filtration material 21 and the filtration material 2
It is possible to prevent the washing liquid 60 containing the suspended substance 11 separated from 1 from being mixed.

【0010】請求項5に係る発明は、請求項1ないし4
いずれかに係る発明であって、更に図1に示すように、
外筒17の両端面にこの両端面をそれぞれ閉止する一対
の閉止板37,38が設けられたことを特徴とする。こ
の請求項5に記載された濾過材洗浄機能付回転濾過装置
では、濾過材21により濾過された液体12と、二重筒
体16の外部の液槽13内の未濾過の液体12とが混ざ
るのを防止できる。
[0010] The invention according to claim 5 is the invention according to claims 1 to 4.
The invention according to any of the above, further as shown in FIG.
It is characterized in that a pair of closing plates 37 and 38 for closing the both end surfaces respectively are provided on both end surfaces of the outer cylinder 17. In the rotary filtration device with a filtering material washing function according to the fifth aspect, the liquid 12 filtered by the filtering material 21 and the unfiltered liquid 12 in the liquid tank 13 outside the double cylinder 16 are mixed. Can be prevented.

【0011】請求項6に係る発明は、請求項1ないし5
いずれかに係る発明であって、更に図1に示すように、
懸濁物質11を含む液体12が地熱熱水であることを特
徴とする。この請求項6に記載された濾過材洗浄機能付
回転濾過装置では、地熱熱水12に含まれる過飽和シリ
カ(懸濁物質11)を濾過材21により効率良く捕捉し
て分離することができる。
The invention according to claim 6 is the invention according to claims 1 to 5
The invention according to any of the above, further as shown in FIG.
The liquid 12 containing the suspended substance 11 is geothermal hot water. In the rotary filtration device with a filtration material washing function according to the sixth aspect, the supersaturated silica (suspension substance 11) contained in the geothermal hot water 12 can be efficiently captured and separated by the filtration material 21.

【0012】請求項7に係る発明は、請求項1ないし6
いずれかに係る発明であって、更に図1に示すように、
液槽13の底部に懸濁物質11が沈殿して生成されたス
ラリーを排出するための排出手段68が設けられたこと
を特徴とする。この請求項7に記載された濾過材洗浄機
能付回転濾過装置では、液槽13底部に沈殿して堆積し
た懸濁物質11のスラリーは液体12の液槽13への供
給を停止せずに、排出手段68により液槽13から排出
される。
The invention according to claim 7 is the invention according to claims 1 to 6
The invention according to any of the above, further as shown in FIG.
Discharge means 68 is provided at the bottom of the liquid tank 13 for discharging a slurry produced by precipitation of the suspended substance 11. In the rotary filtration device with a filter material washing function according to the seventh aspect, the slurry of the suspended substance 11 settled and deposited at the bottom of the liquid tank 13 does not stop the supply of the liquid 12 to the liquid tank 13. The liquid is discharged from the liquid tank 13 by the discharging means 68.

【0013】[0013]

【発明の実施の形態】次に本発明の第1の実施の形態を
図面に基づいて説明する。図1及び図2に示すように、
回転濾過装置10は懸濁物質11を含む液体12が貯留
される液槽13と、液槽13に液体12を供給する供給
手段14と、通液性外筒17とこの外筒17に略同心の
通液性内筒18を有する二重筒体16と、外筒17と内
筒18により囲まれた濾過空間19に収容された濾過材
21とを備える。液槽13はこの実施の形態では四角筒
状に形成された上槽部13aと、上槽部13aの下端に
連設され四角錐状に形成された下槽部13bとを有す
る。また液体12はこの実施の形態では地熱熱水であ
り、懸濁物質11は地熱熱水12に含まれる過飽和シリ
カである。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Next, a first embodiment of the present invention will be described with reference to the drawings. As shown in FIGS. 1 and 2,
The rotary filtration device 10 includes a liquid tank 13 in which a liquid 12 containing a suspended substance 11 is stored, a supply unit 14 for supplying the liquid 12 to the liquid tank 13, a liquid-permeable outer cylinder 17, and substantially concentric with the outer cylinder 17. And a filter medium 21 housed in a filtration space 19 surrounded by the outer cylinder 17 and the inner cylinder 18. In this embodiment, the liquid tank 13 has an upper tank portion 13a formed in a square tubular shape, and a lower tank portion 13b formed in a quadrangular pyramid shape and connected to the lower end of the upper tank portion 13a. In this embodiment, the liquid 12 is geothermal hot water, and the suspended substance 11 is supersaturated silica contained in the geothermal hot water 12.

【0014】供給手段14は図1に詳しく示すように、
一端が地中から噴出した地熱熱水12に浸され他端が下
槽部13bに挿入された供給管22と、この供給管22
に設けられた供給ポンプ23とを有する。また供給ポン
プ23より下流側の供給管22にはシード供給管24及
び薬液供給管26を介してシードタンク27及び薬液タ
ンク28がそれぞれ接続される。上記シードタンク27
には懸濁物質11の結晶粒の成長を促進する結晶核成長
促進材又は懸濁物質11の結晶粒の凝集沈殿を促進する
凝集沈殿材のいずれか一方又は双方が貯留される。結晶
核成長促進材は比表面積が1m2/g以上に設定された
二酸化珪素又は珪酸塩化合物であることが好ましい。上
記二酸化珪素又は珪酸塩化合物を地熱熱水に添加するの
は、これらが核(シード)となって懸濁物質11である
過飽和シリカの結晶核成長をより促進するためである。
The supply means 14 is, as shown in detail in FIG.
A supply pipe 22 having one end immersed in the geothermal hot water 12 spouted from the ground and the other end inserted into the lower tank portion 13b;
And a supply pump 23 provided at A seed tank 27 and a chemical tank 28 are connected to the supply pipe 22 downstream of the supply pump 23 via a seed supply pipe 24 and a chemical supply pipe 26, respectively. The above-mentioned seed tank 27
One or both of a crystal nucleus growth promoting material for promoting the growth of the crystal grains of the suspended substance 11 and a coagulated sedimentation material for promoting the coagulated precipitation of the crystal grains of the suspended substance 11 are stored. It is preferable that the crystal nucleus growth promoting material is silicon dioxide or a silicate compound having a specific surface area of 1 m 2 / g or more. The reason why the silicon dioxide or the silicate compound is added to the geothermal hot water is that they serve as nuclei (seeds) to further promote the crystal nucleus growth of the supersaturated silica as the suspended substance 11.

【0015】また凝集沈殿材はアルミニウム,マグネシ
ウム,鉄,カルシウム,銅若しくはマンガンを含む金属
化合物、又は含窒素カチオン化合物の群より選ばれた1
種又は2種以上の混合物であることが好ましい。上記金
属化合物や含窒素カチオン化合物を添加するのは、これ
らの化合物が地熱熱水12中に溶在して、多価陽イオン
や二次的に生成された物質によって懸濁物質11である
過飽和シリカをより凝集し易くするためである。更に薬
液タンク28には地熱熱水12のpHを調整する硫酸
(H2SO4),苛性ソーダ(NaOH)等のpH調整剤
が貯留される。図1の符号29及び31はシードポンプ
及び流量計であり、符号32及び33は薬液ポンプ及び
流量計である。また符号34及び36は供給管22を流
れる地熱熱水12の圧力及び流量をそれぞれ計測する圧
力計及び流量計である。
The coagulated sedimentation material is selected from the group consisting of metal compounds containing aluminum, magnesium, iron, calcium, copper or manganese, and nitrogen-containing cation compounds.
It is preferably a species or a mixture of two or more species. The above-mentioned metal compound and nitrogen-containing cation compound are added because these compounds are dissolved in the geothermal hot water 12 and the supersaturated substance 11 is suspended by polyvalent cations or substances generated secondarily. This is because silica is easily aggregated. Further, the chemical liquid tank 28 stores a pH adjuster such as sulfuric acid (H 2 SO 4 ) or caustic soda (NaOH) for adjusting the pH of the geothermal hot water 12. Reference numerals 29 and 31 in FIG. 1 are a seed pump and a flow meter, and reference numerals 32 and 33 are a chemical pump and a flow meter. Reference numerals 34 and 36 denote a pressure gauge and a flow meter for measuring the pressure and flow rate of the geothermal hot water 12 flowing through the supply pipe 22, respectively.

【0016】二重筒体16の外筒17及び内筒18の軸
線は略水平方向にかつ外筒17と内筒18の一部を地熱
熱水12の液面から突出させて、地熱熱水12中を上記
軸線を中心に周方向に回転可能に液槽13内に設けられ
る(図1及び図2)。具体的には内筒18は外筒17に
軸線を一致させて収容され、外筒17及び内筒18の両
端面には一対の閉止板37,38が取付けられる(図
1)。一対の閉止板37,38の中心には上記軸線上に
沿って延びる第1及び第2回転軸41,42がそれぞれ
突設され、これらの回転軸41,42は上槽部13aの
互いに対向する一対の側壁13c,13dに回転可能に
取付けられる(図1,図3及び図4)。第1回転軸41
は一方の側壁13cの第1透孔13eに遊挿され、一方
の側壁13cに取付けられた第1ブラケット41aによ
り第1軸受41bを介して回転可能に保持される(図
3)。また第2回転軸42は他方の側壁13dの第2透
孔13fに遊挿され、他方の側壁13dに取付けられた
第2ブラケット42aにより第2軸受42bを介して回
転可能に保持される(図4)。
The axis of the outer cylinder 17 and the inner cylinder 18 of the double cylinder 16 is substantially horizontal, and a part of the outer cylinder 17 and the inner cylinder 18 is made to protrude from the liquid surface of the geothermal hot water 12. 12 is provided in the liquid tank 13 so as to be rotatable in the circumferential direction around the axis (FIGS. 1 and 2). More specifically, the inner cylinder 18 is accommodated in the outer cylinder 17 so as to have the same axis, and a pair of closing plates 37 and 38 are attached to both end surfaces of the outer cylinder 17 and the inner cylinder 18 (FIG. 1). First and second rotating shafts 41 and 42 extending along the axis are projected from centers of the pair of closing plates 37 and 38, respectively, and these rotating shafts 41 and 42 are opposed to each other of the upper tank portion 13a. It is rotatably attached to the pair of side walls 13c and 13d (FIGS. 1, 3 and 4). First rotating shaft 41
Is loosely inserted into the first through hole 13e of the one side wall 13c, and is rotatably held via the first bearing 41b by the first bracket 41a attached to the one side wall 13c (FIG. 3). Further, the second rotating shaft 42 is loosely inserted into the second through hole 13f of the other side wall 13d, and is rotatably held by the second bracket 42a attached to the other side wall 13d via the second bearing 42b (FIG. 4).

【0017】内筒18及び外筒17は図示しないがそれ
ぞれ2枚のステンレス鋼製の網を重ねて形成されること
が好ましく、一方の網は線径が比較的細くかつ目開きが
1mm程度と小さく形成され、他方の網は線径が比較的
太くかつ目開きが5mm程度と比較的大きく形成されて
上記一方の網の変形を防止するように構成される。更に
外筒17,内筒18及び一対の閉止板37,38により
囲まれた濾過空間19は軸線を中心に放射状に設けられ
た複数の仕切り板19aにより複数の小空間19bに区
画される(図2)。この実施の形態では、濾過空間19
を12枚の仕切り板19aにより12個の小空間19b
に区画したが、これらの数に限定されるものではない。
Although not shown, the inner cylinder 18 and the outer cylinder 17 are preferably formed by superposing two stainless steel nets, one of which has a relatively small wire diameter and an opening of about 1 mm. The other mesh is formed to have a relatively large wire diameter and a relatively large mesh size of about 5 mm to prevent deformation of the one mesh. Further, the filtration space 19 surrounded by the outer cylinder 17, the inner cylinder 18, and the pair of closing plates 37, 38 is divided into a plurality of small spaces 19b by a plurality of partition plates 19a provided radially around the axis (FIG. 2). In this embodiment, the filtering space 19
Is divided into twelve small spaces 19b by twelve partition plates 19a.
, But is not limited to these numbers.

【0018】濾過材21は濾過空間19の各小空間19
b内で流動可能にかつ濾過空間19から漏出不能な大き
さ、例えば粒径が2〜5mmの範囲に形成され、地熱熱
水12中の懸濁物質11を捕捉して地熱熱水12から分
離する機能を有する。また濾過材21の材質は従来から
濾過処理に使用されているものでよいが、含水珪酸塩鉱
物(ゼオライト族)を主成分とする土壌成分,天然若し
くは人工の珪酸塩鉱物(軽量発泡コンクリート(AL
C)等)の塊粒状物質,高分子材料の顆粒状物質,高分
子材料の立体網目構造状塊粒物質,高分子材料のブラシ
状団塊物質、無機材料若しくは有機材料の中空円柱状物
質,無機材料若しくは有機材料の中空球状体物質等を用
いることが好ましく、これらを単独又は混合状態で使用
することができる。特に濾過材21として比重が1以下
の軽量のものを用いれば、濾過材21自体の自己浮揚力
により濾過材21が容易に流動撹拌されるとともに、濾
過材21自体の取扱い・運搬が容易になる。更に濾過材
21は小空間19bの容積に対して一定の空間容積を持
たせて収容される。これにより濾過材21は各小空間1
9b内で流動でき、かつ相互に接触できる状態になる。
なお、濾過材21に水酸化鉄を混合すれば、地熱熱水1
2に含まれるヒ素が濾過材21中に蓄積され、地熱熱水
12から除去できる。
The filtering material 21 is provided in each small space 19 of the filtering space 19.
b, it is formed in a size that can flow and cannot leak from the filtration space 19, for example, the particle size is in the range of 2 to 5 mm, and captures the suspended matter 11 in the geothermal hot water 12 and separates it from the geothermal hot water It has a function to do. The material of the filter material 21 may be a material conventionally used for the filtration treatment, but may be a soil component mainly composed of a hydrous silicate mineral (zeolite group), a natural or artificial silicate mineral (lightweight foamed concrete (AL
C) etc.) Agglomerated and granular materials, granular materials of polymeric materials, 3D network aggregates of polymeric materials, brush-like aggregates of polymeric materials, hollow cylindrical materials of inorganic or organic materials, inorganic It is preferable to use a hollow sphere material of a material or an organic material, and these can be used alone or in a mixed state. In particular, if a light-weight material having a specific gravity of 1 or less is used as the filter medium 21, the filter medium 21 is easily flow-stirred by the self-buoyancy of the filter medium 21 itself, and the handling and transport of the filter medium 21 itself is facilitated. . Further, the filter medium 21 is accommodated so as to have a certain space volume with respect to the volume of the small space 19b. As a result, the filter medium 21 is placed in each small space 1
9b so that they can flow and come into contact with each other.
In addition, if iron hydroxide is mixed with the filter material 21, geothermal hot water 1
2 is accumulated in the filter medium 21 and can be removed from the geothermal hot water 12.

【0019】二重筒体16は回転手段43により回転駆
動される。回転手段43は図3に詳しく示すように、上
槽部13aの一方の側壁13c外面に取付けられた筒体
駆動モータ43aと、このモータ43aの出力軸43b
に嵌着された駆動歯車43cと、駆動歯車43cに噛合
しかつ第2回転軸42に嵌着された従動歯車43dとを
有する。筒体駆動モータ43aとしてはステッピングモ
ータやサーボモータ等の電動モータや、油圧や空気圧を
利用した流体圧モータ等が用いられる。また回転手段4
3は二重筒体16を小空間19b単位で間欠的に回転駆
動するように構成される。図3の符号44は液槽13の
地熱熱水12が漏れるのを防止するためのシール部材で
ある。
The double cylinder 16 is driven to rotate by a rotation means 43. As shown in detail in FIG. 3, the rotating means 43 includes a cylindrical drive motor 43a mounted on the outer surface of one of the side walls 13c of the upper tank portion 13a, and an output shaft 43b of the motor 43a.
, And a driven gear 43d meshed with the drive gear 43c and fitted to the second rotating shaft 42. As the cylinder driving motor 43a, an electric motor such as a stepping motor or a servomotor, a fluid pressure motor using hydraulic pressure or air pressure, or the like is used. Rotating means 4
Numeral 3 is configured to intermittently drive the double cylinder 16 in small space 19b units. Reference numeral 44 in FIG. 3 denotes a seal member for preventing the geothermal hot water 12 in the liquid tank 13 from leaking.

【0020】上槽部13aの一方の側壁13c外面には
液槽13内に供給された地熱熱水12の液面を一定に保
つ排液手段46が取付けられる(図1及び図3)。排液
手段46は図3に詳しく示すように、一方の側壁13c
外面に取付けられた排液タンク46aと、排液タンク4
6a内に挿通されたオーバフローパイプ46bとを有す
る。第1回転軸41は中空に形成され、かつ第1回転軸
41の先端は排液タンク46aの下部に挿入される。こ
れにより内筒18の内部と排液タンク46aとが第1回
転軸41を通して連通するように構成され、液槽13に
供給されかつ濾過材21を通って濾過された地熱熱水1
2が内筒18の内部から液槽13の外部に排出されるよ
うになっている。またオーバフローパイプ46bの上端
は排液タンク46aの上端近傍まで延び、このパイプ4
6bの上端の位置により液槽13内の地熱熱水12の液
面が決定される。図3の符号53は第1回転軸41を第
3軸受53aを介して回転可能に保持しかつ排液タンク
46aに取付けられた第3ブラケットであり、符号51
は排液タンク46a内の地熱熱水12が漏れるのを防止
するためのシール部材である。
A drainage means 46 for keeping the level of the geothermal hot water 12 supplied into the liquid tank 13 constant is attached to the outer surface of one side wall 13c of the upper tank 13a (FIGS. 1 and 3). As shown in detail in FIG. 3, the drainage means 46 has one side wall 13c.
A drainage tank 46a mounted on the outer surface;
6a and an overflow pipe 46b inserted into the inside. The first rotating shaft 41 is formed to be hollow, and the tip of the first rotating shaft 41 is inserted into a lower part of the drainage tank 46a. Thereby, the inside of the inner cylinder 18 and the drainage tank 46 a are configured to communicate with each other through the first rotation shaft 41, and the geothermal hot water 1 supplied to the liquid tank 13 and filtered through the filter medium 21 is formed.
2 is discharged from the inside of the inner cylinder 18 to the outside of the liquid tank 13. The upper end of the overflow pipe 46b extends to near the upper end of the drainage tank 46a.
The liquid level of the geothermal hot water 12 in the liquid tank 13 is determined by the position of the upper end of 6b. Reference numeral 53 in FIG. 3 denotes a third bracket that rotatably holds the first rotary shaft 41 via a third bearing 53a and is attached to the drainage tank 46a.
Is a seal member for preventing the geothermal hot water 12 in the drainage tank 46a from leaking.

【0021】外筒17の上方には洗浄ノズル54が設け
られ、この洗浄ノズル54はノズル搬送手段56により
二重筒体16の軸線方向に沿って往復動可能に設けられ
る(図1及び図2)。ノズル搬送手段56は液槽13の
上端に立設された一対の支持部材56a,56aと、一
対の支持部材56a,56aにより回転可能に支持され
たねじ棒56bと、両端が一対の支持部材56a,56
aにより支持されかつねじ棒56bと平行に配設された
一対のガイド棒56c,56cと、ねじ棒56bに螺合
しかつ一対のガイド棒56c,56cに摺動可能に嵌入
されたノズルホルダ56dと、ねじ棒56bを回転駆動
するノズル駆動モータ56eとを有する。洗浄ノズル5
4はノズルホルダ56dの下面に連結部材55を介して
取付けられかつ外筒17の外周面に相応するように湾曲
して形成されたノズル本体54aと、複数の小空間19
bのうち地熱熱水12の液面の上方に位置する小空間1
9bに向って形成された複数の噴射孔54bとを有す
る。
A washing nozzle 54 is provided above the outer cylinder 17, and the washing nozzle 54 is provided so as to be able to reciprocate along the axial direction of the double cylinder 16 by the nozzle conveying means 56 (FIGS. 1 and 2). ). The nozzle transfer means 56 includes a pair of support members 56a, 56a erected at the upper end of the liquid tank 13, a screw rod 56b rotatably supported by the pair of support members 56a, 56a, and a pair of support members 56a at both ends. , 56
a, and a pair of guide rods 56c, 56c arranged in parallel with the screw rod 56b, and a nozzle holder 56d screwed to the screw rod 56b and slidably fitted in the pair of guide rods 56c, 56c. And a nozzle drive motor 56e that rotationally drives the screw rod 56b. Cleaning nozzle 5
Reference numeral 4 denotes a nozzle main body 54a which is attached to the lower surface of the nozzle holder 56d via the connecting member 55 and which is curved so as to correspond to the outer peripheral surface of the outer cylinder 17, and a plurality of small spaces 19.
b, the small space 1 located above the liquid level of the geothermal hot water 12
9b, and a plurality of injection holes 54b formed toward 9b.

【0022】また供給ポンプ23より上流側の供給管2
2には洗浄管57の一端が分岐して接続され、この洗浄
管57の他端はノズル駆動モータ56e近傍まで延びて
設けられる(図1)。ノズルホルダ56d及び連結部材
55には噴射孔56fに連通する連通孔56f,55a
が形成され(図2)、洗浄管57の他端とノズルホルダ
56dの連通孔56fとは可撓性を有するホース58に
より連通接続される(図1及び図2)。またホース58
はホース保持手段59により保持される。このホース保
持手段59はねじ棒56bの上方に架設されたレール5
9aと、このレール59aに摺動可能に嵌入された複数
のフック59bとを有し、ホース58はこれらのフック
59bにより所定の間隔をあけて保持される。これによ
りホース58がねじ棒56b等に接触することなく、ノ
ズルホルダ56dにスムーズに追従するように構成され
る。噴射孔54bから噴射される洗浄液60は濾過空間
19を通過する前の地熱熱水12である。また図1の符
号61は洗浄管57を開閉する開閉バルブであり、符号
62は洗浄液60を洗浄ノズル54に圧送する洗浄ポン
プである。
The supply pipe 2 upstream of the supply pump 23
2, one end of a cleaning pipe 57 is branched and connected, and the other end of the cleaning pipe 57 is provided so as to extend to the vicinity of a nozzle drive motor 56e (FIG. 1). The nozzle holder 56d and the connecting member 55 have communicating holes 56f, 55a communicating with the injection holes 56f.
Is formed (FIG. 2), and the other end of the cleaning pipe 57 and the communication hole 56f of the nozzle holder 56d are connected by a flexible hose 58 (FIGS. 1 and 2). Also hose 58
Is held by the hose holding means 59. The hose holding means 59 is a rail 5 provided above the screw rod 56b.
9a and a plurality of hooks 59b slidably fitted to the rail 59a, and the hose 58 is held at a predetermined interval by the hooks 59b. Thereby, the hose 58 is configured to smoothly follow the nozzle holder 56d without coming into contact with the threaded rod 56b or the like. The cleaning liquid 60 injected from the injection holes 54 b is the geothermal hot water 12 before passing through the filtration space 19. Reference numeral 61 in FIG. 1 denotes an opening / closing valve for opening and closing the cleaning pipe 57, and reference numeral 62 denotes a cleaning pump for pumping the cleaning liquid 60 to the cleaning nozzle 54.

【0023】内筒18の内部には地熱熱水12の液面の
上方に位置する小空間19bに対向して集液容器63が
設けられ、この集液容器63はその上端が内筒18から
所定の間隔をあけかつ上端が液槽13内の地熱熱水12
の液面より上方に位置するように設けられる(図1〜図
4)。この集液容器63の一端は第1ステー71及び排
液タンク46aを介して液槽13に固定され(図3)、
他端は第2ステー72及び第2ブラケット42aを介し
て液槽13に固定される(図4)。第1ステー71は略
L字状に形成され、第1回転軸41内を通って排液タン
ク46aの内側面に固定される(図3)。また第2ステ
ー72は逆L字状に形成され、第2回転軸42内を通っ
て第2ブラケット42aに固定される(図4)。集液容
器63は洗浄ノズル54から噴射された洗浄液60を濾
過材21から離脱した懸濁物質11とともに集液するよ
うに構成される。第2ステー72は集液容器63に貯留
された懸濁物質11を含む洗浄液60を二重筒体16の
外部の未濾過の地熱熱水12に導く誘導管64としての
機能も有する(図4)。即ち、第2ステー72は鉛直方
向に延びる鉛直部72aと、水平方向に延びる鉛直部7
2bとを有し、第2ステー72には鉛直部72aの上端
から水平部72bの先端近傍まで延びる誘導穴72cが
形成される。鉛直部72aの上端に対向する集液容器6
3の底部には第1通孔63aが形成され、水平部72b
の中央には第2通孔72dが形成され、更に第2回転軸
42には第3通孔42cが形成される。図4の符号66
は内筒18内部の濾過された地熱熱水12と二重筒体1
6外部の未濾過の地熱熱水12が混ざるのを防止するシ
ール部材であり、符号67は第2回転軸42内の地熱熱
水12が漏れるのを防止するシール部材である。
A liquid collecting container 63 is provided inside the inner cylinder 18 so as to face the small space 19 b located above the liquid level of the geothermal hot water 12. The geothermal hot water 12 in the liquid tank 13 with a predetermined interval
(FIGS. 1 to 4). One end of the liquid collecting container 63 is fixed to the liquid tank 13 via the first stay 71 and the drain tank 46a (FIG. 3).
The other end is fixed to the liquid tank 13 via the second stay 72 and the second bracket 42a (FIG. 4). The first stay 71 is formed in a substantially L-shape, passes through the inside of the first rotating shaft 41, and is fixed to the inner surface of the drainage tank 46a (FIG. 3). The second stay 72 is formed in an inverted L-shape, passes through the inside of the second rotating shaft 42, and is fixed to the second bracket 42a (FIG. 4). The liquid collecting container 63 is configured to collect the cleaning liquid 60 sprayed from the cleaning nozzle 54 together with the suspended substance 11 separated from the filter medium 21. The second stay 72 also has a function as a guide tube 64 for guiding the cleaning liquid 60 containing the suspended substance 11 stored in the liquid collecting container 63 to the unfiltered geothermal hot water 12 outside the double cylinder 16 (FIG. 4). ). That is, the second stay 72 includes a vertical portion 72a extending in the vertical direction and a vertical portion 7 extending in the horizontal direction.
2b, and a guide hole 72c is formed in the second stay 72 and extends from the upper end of the vertical portion 72a to near the tip of the horizontal portion 72b. Liquid collection container 6 facing the upper end of vertical portion 72a
3, a first through hole 63a is formed at the bottom of the horizontal portion 72b.
A second through-hole 72d is formed in the center of the second rotary shaft 42, and a third through-hole 42c is further formed in the second rotating shaft 42. Reference numeral 66 in FIG.
Represents the filtered geothermal hot water 12 inside the inner cylinder 18 and the double cylinder 1
Reference numeral 67 denotes a seal member for preventing the unfiltered geothermal hot water 12 outside from being mixed, and reference numeral 67 denotes a seal member for preventing the geothermal hot water 12 in the second rotating shaft 42 from leaking.

【0024】液槽13の底部には排出手段68が設けら
れる(図1及び図2)。この排出手段68は一端が液槽
13の底部に接続された排出管68aと、排出管68a
に設けられこの排出管68aを開閉可能な開閉バルブ6
8bと、開閉バルブ68bの下流側の排出管68aに設
けられたスラリー排出ポンプ68cとを有する。このス
ラリー排出ポンプ68cにより液槽13の底部に堆積し
た懸濁物質11のスラリーが排出されるように構成され
る。排出管68aの他端には図示しないが上記スラリー
を固形物にして回収するフィルタプレスや、上記スラリ
ーを粉体として回収するスプレードライヤ等が接続され
る。
A discharge means 68 is provided at the bottom of the liquid tank 13 (FIGS. 1 and 2). The discharge means 68 includes a discharge pipe 68a having one end connected to the bottom of the liquid tank 13, and a discharge pipe 68a.
Opening / closing valve 6 provided at the
8b and a slurry discharge pump 68c provided in a discharge pipe 68a downstream of the on-off valve 68b. The slurry discharge pump 68c is configured to discharge the slurry of the suspended substance 11 deposited on the bottom of the liquid tank 13. To the other end of the discharge pipe 68a, a filter press (not shown) for collecting the slurry as a solid and a spray dryer for collecting the slurry as a powder are connected.

【0025】このように構成された回転濾過装置の動作
を説明する。供給ポンプ23を始動すると、地熱熱水1
2が供給管22を通って液槽13の下部に供給される。
このときシードポンプ29を始動すると、シードタンク
27内の結晶核成長促進材や凝集沈殿材が地熱熱水に混
合されて液槽13に供給されるので、結晶核成長促進材
が核(シード)となって懸濁物質11である過飽和シリ
カの結晶核成長が促進され、凝集沈殿材により懸濁物質
11である過飽和シリカが凝集する。この結果、懸濁物
質11である過飽和シリカの粒径が大きくなる。また薬
液ポンプ32を始動すると、薬液タンク28内のpH調
整剤が地熱熱水12に混合されて液槽13に供給される
地熱熱水12のpHが調整される。
The operation of the rotary filter constructed as above will be described. When the supply pump 23 is started, the geothermal hot water 1
2 is supplied to the lower part of the liquid tank 13 through the supply pipe 22.
At this time, when the seed pump 29 is started, the crystal nucleus growth promoting material and the coagulated sedimentation material in the seed tank 27 are mixed with geothermal hot water and supplied to the liquid tank 13, so that the crystal nucleus growth promoting material is nucleated (seed). As a result, the crystal nucleus growth of the supersaturated silica as the suspended substance 11 is promoted, and the supersaturated silica as the suspended substance 11 is aggregated by the coagulating sedimentation material. As a result, the particle size of the supersaturated silica as the suspended substance 11 increases. When the chemical pump 32 is started, the pH adjusting agent in the chemical tank 28 is mixed with the geothermal water 12 to adjust the pH of the geothermal water 12 supplied to the liquid tank 13.

【0026】液槽13内の地熱熱水12の液面は徐々に
上昇し、その液面が二重筒体16に達すると、地熱熱水
12が外筒17から濾過空間19に流入し、濾過材21
間の間隙を通過する際に地熱熱水12中の懸濁物質11
が濾過材21により捕捉されて分離し、更に濾過された
地熱熱水12は内筒18の内部に流入する。地熱熱水1
2に含まれる懸濁物質11の粒径は濾過材21間の間隙
より大きいため、その間隙を通過できずに濾過材21に
より捕捉される。また上記間隙を通過した微少な懸濁物
質11はこの懸濁物質11と地熱熱水12との質量差に
基づく慣性力の相違により濾過材21に衝突してその流
速が低下することにより、或いは濾過材21表面の地熱
熱水12の表面張力により捕捉される。液槽13に供給
された地熱熱水12の液面が二重筒体16の軸線近傍ま
で達すると、内筒18の内部の濾過された地熱熱水12
は第1回転軸41内を通って排液タンク46aに貯留さ
れ、液槽13に供給された地熱熱水12の液面がオーバ
フローパイプ46bの上端に達すると、濾過された地熱
熱水12はオーバフローパイプ46bを通り、更に地熱
発電用の地下還元井を通って地中に戻される。
The liquid level of the geothermal hot water 12 in the liquid tank 13 gradually rises, and when the liquid level reaches the double cylinder 16, the geothermal hot water 12 flows from the outer cylinder 17 into the filtration space 19, Filter material 21
Suspended matter 11 in the geothermal hot water 12 when passing through the gap between
Are captured and separated by the filter material 21, and the filtered geothermal hot water 12 flows into the inner cylinder 18. Geothermal hot water 1
Since the particle size of the suspended substance 11 contained in 2 is larger than the gap between the filter media 21, the suspended substance 11 cannot be passed through the gap and is captured by the filter media 21. Further, the minute suspended substance 11 that has passed through the gap collides with the filter medium 21 due to a difference in inertial force based on a difference in mass between the suspended substance 11 and the geothermal hot water 12, and the flow velocity thereof decreases, or It is captured by the surface tension of the geothermal hot water 12 on the surface of the filter medium 21. When the liquid level of the geothermal hot water 12 supplied to the liquid tank 13 reaches the vicinity of the axis of the double cylinder 16, the filtered geothermal hot water 12
When the liquid level of the geothermal hot water 12 supplied to the liquid tank 13 reaches the upper end of the overflow pipe 46b, the filtered geothermal hot water 12 is stored in the drain tank 46a through the first rotary shaft 41. The water is returned to the ground through the overflow pipe 46b and further through an underground reduction well for geothermal power generation.

【0027】このとき地下還元井を通る地熱熱水12に
は懸濁物質11である過飽和シリカが含まれていないた
め、この過飽和シリカがシリカスケールとして地下還元
井の内壁に付着することはなく、地下還元井の流動減少
が発生することはない。なお、供給ポンプ23による地
熱熱水11の吐出量は液槽13内及び排液タンク46a
内の地熱熱水12の液面がオーバフローパイプ46bの
上端に略一致するように調整される。また排液タンク4
6a内の濾過後の地熱熱水12を調べることにより、地
下還元井に戻される地熱熱水12の水質をチェックする
ことができる。
At this time, since the geothermal hot water 12 passing through the underground reduction well does not contain supersaturated silica as the suspended substance 11, this supersaturated silica does not adhere to the inner wall of the underground reduction well as silica scale. No flow reduction of underground return wells will occur. The discharge amount of the geothermal hot water 11 by the supply pump 23 is determined in the liquid tank 13 and the drain tank 46a.
The liquid level of the geothermal hot water 12 is adjusted so as to substantially coincide with the upper end of the overflow pipe 46b. Drainage tank 4
By examining the filtered geothermal hot water 12 in 6a, the quality of the geothermal hot water 12 returned to the underground reduction well can be checked.

【0028】供給ポンプ23を始動して所定時間経過す
ると、筒体駆動モータ43aを始動して二重筒体16を
所定の角度だけ(小空間19b単位:この実施の形態で
は30度)回転させた後に停止させる。筒体駆動モータ
43aの停止後に、開閉バルブ61を開いて洗浄ポンプ
62を始動すると、洗浄液60が洗浄ノズル54の噴射
孔54bから地熱熱水12の液面より上方に位置する小
空間19b内の濾過材21に向って噴射され、濾過材2
1が捕捉した懸濁物質11が濾過材21から離脱して洗
浄液60とともに集液容器63内に溜る。ここでノズル
駆動モータ43aを始動すると、洗浄ノズル54がノズ
ルホルダ56dとともに上記小空間19bの全長にわた
って往復動するので、上記小空間19b内の濾過材21
全てを洗浄することができる。集液容器63に溜った懸
濁物質11を含む洗浄液60は集液容器63の第1通孔
63a,第2ステー72の誘導穴72c,第2ステー7
2の第2通孔72d及び第2回転軸42の第3通孔42
cを通って二重筒体16外の液槽13内に導かれ、洗浄
液60中の懸濁物質11は液槽13の底部に堆積する。
When a predetermined time elapses after the supply pump 23 is started, the cylinder driving motor 43a is started to rotate the double cylinder 16 by a predetermined angle (in units of the small space 19b: 30 degrees in this embodiment). Stop after When the opening and closing valve 61 is opened and the cleaning pump 62 is started after the cylinder driving motor 43a is stopped, the cleaning liquid 60 is discharged from the injection hole 54b of the cleaning nozzle 54 into the small space 19b located above the liquid level of the geothermal hot water 12. Injected toward the filter medium 21, the filter medium 2
The suspended substance 11 captured by 1 is separated from the filter medium 21 and accumulates together with the cleaning liquid 60 in the liquid collecting container 63. Here, when the nozzle drive motor 43a is started, the cleaning nozzle 54 reciprocates with the nozzle holder 56d over the entire length of the small space 19b.
Everything can be washed. The cleaning liquid 60 containing the suspended substance 11 stored in the liquid collecting container 63 is supplied to the first through hole 63a of the liquid collecting container 63, the guide hole 72c of the second stay 72, and the second stay 7.
The second through hole 72d of the second rotary shaft 42 and the third through hole 42 of the second rotary shaft 42
The liquid 11 is guided into the liquid tank 13 outside the double cylinder 16 through c, and the suspended substance 11 in the cleaning liquid 60 is deposited on the bottom of the liquid tank 13.

【0029】筒体駆動モータ43aを停止してから所定
時間経過すると、再びこのモータ43aを始動して二重
筒体16を小空間19b単位で間欠的に回転駆動し、上
記と同様に地熱熱水12の液面より上方に位置する小空
間19b内の濾過材21を洗浄する。更に液槽13底部
に沈殿して堆積した懸濁物質11のスラリーは液槽13
への地熱熱水12の供給を停止することなく、開閉バル
ブ68b及びスラリー排出ポンプ68cを開くことによ
り液槽13から排出され、フィルタプレスやスプレード
ライヤ等に導かれる。上記操作を繰返すことにより、液
槽13への地熱熱水12の供給を停止することなく、懸
濁物質11を捕捉した濾過材21を順次洗浄することが
できる。この結果、濾過材21による懸濁物質11の捕
捉能力を低下させることなく、地熱熱水12に含まれる
懸濁物質11を濾過材21により効率良く捕捉すること
ができる。なお、上記操作はコントローラにて供給ポン
プ23,筒体駆動モータ43a,ノズル駆動モータ56
e,洗浄ポンプ62等を制御することにより、自動的に
行われることが好ましい。
When a predetermined time elapses after stopping the cylinder driving motor 43a, the motor 43a is started again to rotate the double cylinder 16 intermittently in small space 19b units. The filter medium 21 in the small space 19b located above the level of the water 12 is washed. Further, the slurry of the suspended substance 11 precipitated and deposited on the bottom of the liquid tank 13 is supplied to the liquid tank 13.
Without stopping the supply of the geothermal hot water 12 to the tank, the gas is discharged from the liquid tank 13 by opening the on-off valve 68b and the slurry discharge pump 68c, and is guided to a filter press, a spray dryer, or the like. By repeating the above operation, it is possible to sequentially wash the filter medium 21 capturing the suspended substances 11 without stopping the supply of the geothermal hot water 12 to the liquid tank 13. As a result, the suspended substance 11 contained in the geothermal hot water 12 can be efficiently captured by the filter medium 21 without reducing the ability of the filter medium 21 to capture the suspended substance 11. The above operations are performed by the controller using the supply pump 23, the cylinder drive motor 43a, the nozzle drive motor 56a.
e, It is preferable that the cleaning is automatically performed by controlling the cleaning pump 62 and the like.

【0030】図5は本発明の第2の実施の形態を示す。
図5において図2と同一符号は同一部品を示す。この実
施の形態では、洗浄ノズル94が内筒18の内部に設け
られ、地熱熱水12の液面の上方に位置する小空間19
b内の濾過材21に洗浄液60を噴射するように構成さ
れる。洗浄ノズル94は集液容器63内に位置し上記小
空間19bの幅より僅かに小さくかつ集液容器63の全
長より僅かに短く形成されたノズル本体94aと、ノズ
ル本体94aの上面に形成された多数の噴射孔94bと
を有する。ノズル本体94aは集液容器63に固定さ
れ、噴射孔94bは図示しないがホースにより洗浄管に
連通接続される。上記以外は第1の実施の形態と同一に
構成される。このように構成された回転濾過装置では、
洗浄ノズル94の噴射孔94bから吹上げるように噴射
した洗浄液60により、濾過材21が捕捉した懸濁物質
を濾過材21から離脱させ、懸濁物質を含む洗浄液60
が集液容器63に貯留されることを除いて、動作は第1
の実施の形態とほぼ同様であるので、繰返しの説明を省
略する。
FIG. 5 shows a second embodiment of the present invention.
5, the same reference numerals as those in FIG. 2 indicate the same parts. In this embodiment, a cleaning nozzle 94 is provided inside the inner cylinder 18 and a small space 19 located above the liquid level of the geothermal hot water 12.
It is configured to inject the cleaning liquid 60 to the filter medium 21 in b. The cleaning nozzle 94 is located in the liquid collecting container 63 and is formed on the upper surface of the nozzle body 94a, which is formed slightly smaller than the width of the small space 19b and slightly shorter than the entire length of the liquid collecting container 63. It has a large number of injection holes 94b. The nozzle body 94a is fixed to the liquid collecting container 63, and the injection hole 94b is connected to the washing pipe by a hose (not shown). Except for the above, the configuration is the same as that of the first embodiment. In the rotary filter configured as described above,
With the cleaning liquid 60 sprayed so as to blow up from the injection holes 94b of the cleaning nozzle 94, the suspended substance trapped by the filter medium 21 is separated from the filter medium 21, and the cleaning liquid 60 containing the suspended substance is removed.
The operation is the first except that is stored in the collection container 63.
Since the third embodiment is almost the same as the first embodiment, the description thereof will not be repeated.

【0031】なお、上記第1及び第2の実施の形態で
は、液体として地熱熱水を挙げたが、有機物,無機物等
の懸濁物質を含む液体であれば、湖沼の水,河川の水,
汚水,泥水等でもよい。また、上記第1及び第2の実施
の形態では、洗浄ノズルから噴射される洗浄液として液
槽に供給される懸濁物質を含む液体を用いたが、濾過空
間19を通過した後の地熱熱水、即ち濾過材により濾過
されて懸濁物質が除去された地熱熱水を用いてもよく、
更に河川の水又はその他の液体を用いてもよい。
In the first and second embodiments, geothermal hot water is used as the liquid. However, if the liquid contains a suspended substance such as an organic substance or an inorganic substance, water from a lake or marsh, water from a river,
Sewage, muddy water, etc. may be used. Further, in the first and second embodiments, the liquid containing the suspended substance supplied to the liquid tank is used as the cleaning liquid sprayed from the cleaning nozzle, but the geothermal hot water after passing through the filtration space 19 is used. That is, geothermal hot water from which suspended matter has been removed by filtration with a filter material may be used,
Further, river water or other liquids may be used.

【0032】[0032]

【発明の効果】以上述べたように、軸性を中心に回転可
能な二重筒体の通液性外筒と通液性内筒により囲まれた
濾過空間に液体に含まれる懸濁物質を捕捉する濾過材を
収容し、軸線を中心に放射状に設けられた複数の仕切り
板が濾過空間を複数の小空間に区画し、外筒上方又は内
筒内部に設けられた洗浄ノズルが液面上方に位置する小
空間内の濾過材に洗浄液を噴射して懸濁物質を濾過材か
ら離脱させ、内筒内部に位置しかつ液槽に固定された集
液容器が洗浄ノズルから噴射された洗浄液を懸濁物質と
ともに集液し、更に集液容器に貯留された懸濁物質を含
む洗浄液を誘導管が二重筒体外部の未濾過液体に導くよ
うに構成したので、供給手段により液槽に供給された液
体は通液性外筒から濾過空間に流入し、液体に含まれる
懸濁物質は濾過材により捕捉されて分離し、更に濾過さ
れた液体は通液性内筒の内部に流入して、排液手段によ
り液槽の外部に排出される。一方、二重筒体は回転手段
により回転するので、液体の液面より上方に出現する小
空間内の濾過材が洗浄ノズルから噴射される洗浄液によ
り洗浄され、濾過材が捕捉した懸濁物質は濾過材から離
脱して洗浄液とともに集液容器内に溜り、誘導管を通っ
て二重筒体外の液槽に導かれ、更に洗浄液中の懸濁物質
は液槽の底部に沈殿して堆積しスラリーとなる。この結
果、液槽への液体の供給を停止することなく、懸濁物質
を捕捉した濾過材を洗浄することができ、また濾過材に
よる懸濁物質の捕捉能力を低下させることなく、液体に
含まれる懸濁物質を濾過材により効率良く捕捉すること
ができる。
As described above, the suspended substance contained in the liquid is contained in the filtration space surrounded by the liquid-permeable outer cylinder and the liquid-permeable inner cylinder which are rotatable about the axis. The filter medium to be captured is accommodated, and a plurality of partition plates radially provided around the axis divide the filtration space into a plurality of small spaces, and the washing nozzle provided above the outer cylinder or inside the inner cylinder is above the liquid surface. The cleaning liquid is sprayed onto the filter medium in the small space located at the position to separate suspended substances from the filter medium, and the liquid collecting container located inside the inner cylinder and fixed to the liquid tank discharges the cleaning liquid sprayed from the cleaning nozzle. The liquid is collected together with the suspended substance, and further the washing liquid containing the suspended substance stored in the liquid collecting container is configured to be guided to the unfiltered liquid outside the double cylinder by the guide tube, and is supplied to the liquid tank by the supply means. The liquid that has flowed into the filtration space from the liquid-permeable outer cylinder, Separated are more captured and further discharged filtered fluid then flows into the liquid permeability inner cylinder, the outside of the liquid tank by drainage means. On the other hand, since the double cylinder is rotated by the rotating means, the filtering material in the small space that appears above the liquid level of the liquid is washed by the washing liquid ejected from the washing nozzle, and the suspended matter captured by the filtering material is After being separated from the filter material, it collects in the liquid collecting container together with the washing liquid, is guided to the liquid tank outside the double cylinder through the guide tube, and the suspended solids in the washing liquid precipitate and deposit on the bottom of the liquid tank to form a slurry. Becomes As a result, it is possible to wash the filter medium that has captured the suspended substance without stopping the supply of the liquid to the liquid tank, and to reduce the ability of the filter medium to capture the suspended substance without decreasing the ability to capture the suspended substance. Suspended substances can be efficiently captured by the filter material.

【0033】また回転手段が二重筒体を小空間単位で間
欠的に回転駆動するように構成すれば、懸濁物質を捕捉
した濾過材を収容した小空間が順次、液体の液面より上
方に出現するので、液槽への液体の供給を停止すること
なく、懸濁物質を捕捉した濾過材を順次洗浄することが
でき、集液容器により洗浄液を濾過材から離脱した懸濁
物質とともに確実に集液することができる。また洗浄液
が液槽に供給される懸濁物質を含む液体又は懸濁物質が
除去された液体であれば、洗浄液が液槽に供給される液
体又は濾過材により濾過された液体と同一であるので、
洗浄液を新たに用意せずに済む。また集液容器の上端が
液槽内の液面より上方に位置するように設ければ、濾過
材により濾過された液体と、濾過材から離脱した懸濁物
質を含む洗浄液とが混ざるのを防止できる。
Further, if the rotating means is configured to intermittently drive the double cylinder in small space units, the small spaces containing the filter medium capturing the suspended matter are sequentially raised above the liquid level. Therefore, the filter medium capturing the suspended substance can be sequentially washed without stopping the supply of the liquid to the liquid tank, and the washing liquid is surely removed by the collecting container together with the suspended substance separated from the filter medium. Can be collected. Further, if the cleaning liquid is a liquid containing a suspended substance to be supplied to the liquid tank or a liquid from which the suspended substance has been removed, the cleaning liquid is the same as the liquid supplied to the liquid tank or the liquid filtered by the filter material. ,
There is no need to prepare a new cleaning solution. In addition, if the upper end of the liquid collecting container is provided above the liquid level in the liquid tank, the liquid filtered by the filter medium and the washing liquid containing suspended substances separated from the filter medium are prevented from being mixed. it can.

【0034】また外筒の両端面にこの両端面をそれぞれ
閉止する一対の閉止板を設ければ、濾過材により濾過さ
れた液体と、二重筒体の外部の液槽内の未濾過の液体と
が混ざるのを防止できる。また懸濁物質を含む液体が地
熱熱水であれば、地熱熱水に含まれる過飽和シリカ(懸
濁物質)を濾過材により効率良く捕捉して分離すること
ができる。更に液槽の底部に懸濁物質が沈殿して生成さ
れたスラリーを排出するための排出手段を設ければ、液
槽底部に沈殿して堆積した懸濁物質のスラリーを液槽へ
の液体の供給を停止せずに、排出手段により液槽から排
出することができる。
Further, if a pair of closing plates for closing the both end surfaces are provided on both end surfaces of the outer cylinder, the liquid filtered by the filtering material and the unfiltered liquid in the liquid tank outside the double cylinder are provided. Can be prevented from being mixed. If the liquid containing the suspended substance is geothermal hot water, supersaturated silica (suspended substance) contained in the geothermal hot water can be efficiently captured and separated by the filter material. Further, if a discharging means is provided at the bottom of the liquid tank for discharging the slurry generated by the precipitation of the suspended substance, the slurry of the suspended substance deposited and deposited at the bottom of the liquid tank can be used to transfer the slurry to the liquid tank. The liquid can be discharged from the liquid tank by the discharging means without stopping the supply.

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

【図1】本発明第1実施形態の濾過材洗浄機能付回転濾
過装置を示す図2のA−A線縦断面図。
FIG. 1 is a longitudinal sectional view taken along the line AA of FIG. 2, showing a rotary filtration device with a filter material washing function according to a first embodiment of the present invention.

【図2】図1のB−B線断面図。FIG. 2 is a sectional view taken along line BB of FIG. 1;

【図3】図1のC部拡大断面図。FIG. 3 is an enlarged sectional view of a portion C in FIG. 1;

【図4】図1のD部拡大断面図。FIG. 4 is an enlarged sectional view of a portion D in FIG. 1;

【図5】本発明の第2実施形態の二重筒体の上部,洗浄
ノズル及び集液容器を含む要部断面図。
FIG. 5 is a sectional view of a main part including an upper portion of a double cylinder, a washing nozzle, and a liquid collecting container according to a second embodiment of the present invention.

【符号の説明】[Explanation of symbols]

10 回転濾過装置 11 懸濁物質 12 地熱熱水(液体) 13 液槽 14 供給手段 16 二重筒体 17 通液性外筒 18 通液性内筒 19 濾過空間 19a 仕切り板 19b 小空間 21 濾過材 37,38 閉止板 43 回転手段 46 排液手段 54,94 洗浄ノズル 60 洗浄液 63 集液容器 64 誘導管 68 排出手段 Reference Signs List 10 Rotary filtration device 11 Suspended substance 12 Geothermal hot water (liquid) 13 Liquid tank 14 Supply means 16 Double cylinder 17 Liquid-permeable outer cylinder 18 Liquid-permeable inner cylinder 19 Filtration space 19a Partition plate 19b Small space 21 Filter material 37, 38 Closing plate 43 Rotating means 46 Drainage means 54, 94 Cleaning nozzle 60 Cleaning liquid 63 Liquid collecting container 64 Guide tube 68 Discharge means

フロントページの続き (72)発明者 加藤 耕一 埼玉県大宮市北袋町1丁目297番地 三菱 マテリアル株式会社総合研究所内 Fターム(参考) 4D026 BA01 BB01 BC22 BC24 BC29 BD03 Continued on the front page (72) Inventor Koichi Kato 1-297 Kitabukuro-cho, Omiya-shi, Saitama F-term in Mitsubishi Materials Corporation Research Laboratory 4D026 BA01 BB01 BC22 BC24 BC29 BD03

Claims (7)

【特許請求の範囲】[Claims] 【請求項1】 懸濁物質(11)を含む液体(12)が貯留され
る液槽(13)と、 前記液槽(13)に前記液体(12)を供給する供給手段(14)
と、 通液性外筒(17)とこの外筒(17)に略同心の通液性内筒(1
8)を有し軸線を略水平方向にかつ前記外筒(17)と前記内
筒(18)の一部を前記液体(12)の液面から突出させて前記
液体(12)中を前記軸線を中心に周方向に回転可能に前記
液槽(13)内に設けられた二重筒体(16)と、 前記外筒(17)と前記内筒(18)により囲まれた濾過空間(1
9)に流動可能にかつ前記濾過空間(19)から漏出不能に収
容され前記懸濁物質(11)を捕捉して液体(12)から分離す
る濾過材(21)と、 前記二重筒体(16)を回転駆動する回転手段(43)と、 前記液槽(13)内の液面を一定に保ちながら前記液槽(13)
に供給されかつ濾過材(21)を通った液体(12)を前記内筒
(18)の内部から前記液槽(13)の外部に排出する排液手段
(46)とを備えた回転濾過装置であって、 前記軸線を中心に放射状に設けられ前記濾過空間(19)を
複数の小空間(19b)に区画する複数の仕切り板(19a)と、 前記外筒(17)の上方又は前記内筒(18)の内部に設けられ
前記液面の上方に位置する小空間(19b)内の濾過材(21)
に洗浄液(60)を噴射して前記濾過材(21)が捕捉した懸濁
物質(11)を前記濾過材(21)から離脱させる洗浄ノズル(5
4)と、 前記内筒(18)の内部に前記液面の上方に位置する小空間
(19b)に対向して設けられかつ前記液槽(13)に固定され
前記洗浄ノズル(54)から噴射された洗浄液(60)を前記濾
過材(21)から離脱した懸濁物質(11)とともに集液する集
液容器(63)と、 前記集液容器(63)に貯留された懸濁物質(11)を含む洗浄
液(60)を前記二重筒体(16)外部の未濾過液体(12)に導く
誘導管(64)とを備えたことを特徴とする濾過材洗浄機能
付回転濾過装置。
1. A liquid tank (13) for storing a liquid (12) containing a suspended substance (11), and a supply means (14) for supplying the liquid (12) to the liquid tank (13).
And a liquid-permeable outer cylinder (17) and a liquid-permeable inner cylinder (1
8) having an axis in a substantially horizontal direction and projecting a part of the outer cylinder (17) and the inner cylinder (18) from the liquid surface of the liquid (12) to move the axis in the liquid (12). A double cylindrical body (16) provided in the liquid tank (13) so as to be rotatable in the circumferential direction around the center, and a filtration space (1) surrounded by the outer cylinder (17) and the inner cylinder (18).
9) a filter medium (21) housed so as to be able to flow and not leak from the filtration space (19) and trapping the suspended substance (11) to separate it from the liquid (12); Rotating means (43) for rotating and driving the 16), and the liquid tank (13) while keeping the liquid level in the liquid tank (13) constant.
Liquid (12) supplied to the inner cylinder
Drainage means for discharging from the inside of (18) to the outside of the liquid tank (13)
(46), and a plurality of partition plates (19a) radially provided around the axis and dividing the filtration space (19) into a plurality of small spaces (19b), Filtering material (21) in a small space (19b) provided above the outer cylinder (17) or inside the inner cylinder (18) and located above the liquid level
The washing nozzle (5) which injects the washing liquid (60) into the filter medium (21) to separate the suspended substance (11) captured by the filter medium (21) from the filter medium (21).
4); and a small space located above the liquid level inside the inner cylinder (18).
The cleaning liquid (60) provided opposite to (19b) and fixed to the liquid tank (13) and jetted from the cleaning nozzle (54) together with the suspended substance (11) separated from the filter medium (21). A liquid collecting container (63) for collecting liquid, and a washing liquid (60) containing the suspended substance (11) stored in the liquid collecting container (63) is supplied with an unfiltered liquid (12) outside the double cylinder (16). ), And a guide pipe (64) leading to the filter material washing function.
【請求項2】 回転手段(43)が二重筒体(16)を小空間(1
9b)単位で間欠的に回転駆動するように構成された請求
項1記載の濾過材洗浄機能付回転濾過装置。
2. The rotating means (43) moves the double cylinder (16) into a small space (1).
The rotary filtration device with a filter material washing function according to claim 1, wherein the rotary filtration device is configured to intermittently drive in units of 9b).
【請求項3】 洗浄液(60)が液槽(13)に供給される懸濁
物質(11)を含む液体(12)又は前記懸濁物質(11)が除去さ
れた液体(12)である請求項1又は2記載の濾過材洗浄機
能付回転濾過装置。
3. The cleaning liquid (60) is a liquid (12) containing a suspended substance (11) supplied to a liquid tank (13) or a liquid (12) from which the suspended substance (11) has been removed. Item 3. A rotary filtration device with a filter material washing function according to item 1 or 2.
【請求項4】 上端が液槽(13)内の液面より上方に位置
するように集液容器(63)が設けられた請求項1ないし3
いずれか記載の濾過材洗浄機能付回転濾過装置。
4. A liquid collecting container (63) having an upper end located above a liquid level in the liquid tank (13).
The rotary filtration device with a filter material washing function according to any one of the above.
【請求項5】 外筒(17)の両端面にこの両端面をそれぞ
れ閉止する一対の閉止板(37,38)が設けられた請求項1
ないし4いずれか記載の濾過材洗浄機能付回転濾過装
置。
5. A pair of closing plates (37, 38) for closing both end surfaces of the outer cylinder (17), respectively.
5. The rotary filtration device with a filter material washing function according to any one of items 4 to 4.
【請求項6】 懸濁物質(11)を含む液体(12)が地熱熱水
である請求項1ないし5いずれか記載の濾過材洗浄機能
付回転濾過装置。
6. The rotary filtration device with a filter material washing function according to claim 1, wherein the liquid (12) containing the suspended substance (11) is geothermal hot water.
【請求項7】 液槽(13)の底部に懸濁物質(11)が沈殿し
て生成されたスラリーを排出するための排出手段(68)が
設けられた請求項1ないし6いずれか記載の濾過材洗浄
機能付回転濾過装置。
7. A discharge means (68) for discharging a slurry produced by precipitation of a suspended substance (11) at the bottom of a liquid tank (13). Rotary filtration device with filter material washing function.
JP30963099A 1999-10-29 1999-10-29 Rotary filtering device with filter medium cleaning function Pending JP2001120911A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP30963099A JP2001120911A (en) 1999-10-29 1999-10-29 Rotary filtering device with filter medium cleaning function

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP30963099A JP2001120911A (en) 1999-10-29 1999-10-29 Rotary filtering device with filter medium cleaning function

Publications (1)

Publication Number Publication Date
JP2001120911A true JP2001120911A (en) 2001-05-08

Family

ID=17995356

Family Applications (1)

Application Number Title Priority Date Filing Date
JP30963099A Pending JP2001120911A (en) 1999-10-29 1999-10-29 Rotary filtering device with filter medium cleaning function

Country Status (1)

Country Link
JP (1) JP2001120911A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2009122614A1 (en) 2008-03-31 2009-10-08 株式会社テクノサポート Rotary filtration device
KR101055627B1 (en) * 2009-04-10 2011-08-09 대한민국 Mobile Manure and Sewage Aeration System
CN114146459A (en) * 2021-12-15 2022-03-08 鹰潭市钲旺科技有限公司 Multi-stage filtering device for copper-clad copper wire cleaning solution

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2009122614A1 (en) 2008-03-31 2009-10-08 株式会社テクノサポート Rotary filtration device
JP2009240892A (en) * 2008-03-31 2009-10-22 Techno Support Ltd Rotary filter
JP4537468B2 (en) * 2008-03-31 2010-09-01 株式会社テクノサポート Rotary filtration device
KR101055627B1 (en) * 2009-04-10 2011-08-09 대한민국 Mobile Manure and Sewage Aeration System
CN114146459A (en) * 2021-12-15 2022-03-08 鹰潭市钲旺科技有限公司 Multi-stage filtering device for copper-clad copper wire cleaning solution

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