JP2767690B2 - Filtration machine and filtration method - Google Patents

Filtration machine and filtration method

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Publication number
JP2767690B2
JP2767690B2 JP7017500A JP1750095A JP2767690B2 JP 2767690 B2 JP2767690 B2 JP 2767690B2 JP 7017500 A JP7017500 A JP 7017500A JP 1750095 A JP1750095 A JP 1750095A JP 2767690 B2 JP2767690 B2 JP 2767690B2
Authority
JP
Japan
Prior art keywords
filter medium
hollow
filtrate
container
hollow filter
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 - Fee Related
Application number
JP7017500A
Other languages
Japanese (ja)
Other versions
JPH08187407A (en
Inventor
忠 桐澤
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
NIPPON ENBAIRO KOGYO KK
Original Assignee
NIPPON ENBAIRO KOGYO KK
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by NIPPON ENBAIRO KOGYO KK filed Critical NIPPON ENBAIRO KOGYO KK
Priority to JP7017500A priority Critical patent/JP2767690B2/en
Publication of JPH08187407A publication Critical patent/JPH08187407A/en
Application granted granted Critical
Publication of JP2767690B2 publication Critical patent/JP2767690B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Description

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

【0001】[0001]

【産業上の利用分野】 本発明は被処理液から固形分を
分離するために使用される濾過機および該濾過機を使用
する濾過方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a filter used for separating a solid content from a liquid to be treated and a filtration method using the filter.

【0002】[0002]

【従来の技術】 従来、図6に示すように容器(2) と、
該容器(2) 内に回転可能に差渡されている中空回転軸
(3) と、該中空回転軸(3) に取付けられている複数個の
中空濾材(4) とからなり、該容器(2) には被処理液導入
口(5) とドレン排出口(6) とが設けられ、該中空濾材
(4) 内部は導通孔(7) を介して該中空回転軸(3) 内部に
形成されている濾液流路(3A)に連絡し、該中空回転軸
(3) の端部(3B)には濾液排出口(8) が設けられ、更に該
端部(3B)は該容器(2) の端部から延設されている被覆筒
(9) によって被覆され、該被覆筒(9) には濾液排出路(1
0)が接続され、該中空回転軸(3) の末端にはプーリー(1
1)が取付けられ、該プーリー(11)はベルト(12)を介して
図示しないモーターに接続している濾過機(1) が提供さ
れている(特開昭53−37950号、特開昭56−5
6772号、特開昭56−77270号)。
2. Description of the Related Art Conventionally, as shown in FIG.
A hollow rotary shaft rotatably provided in the container (2)
(3) and a plurality of hollow filter media (4) attached to the hollow rotary shaft (3), and the container (2) has a liquid inlet (5) and a drain outlet (6). And the hollow filter medium
(4) The inside communicates with the filtrate flow path (3A) formed inside the hollow rotary shaft (3) through the conduction hole (7),
The end (3B) of (3) is provided with a filtrate outlet (8), and the end (3B) is further provided with a coating tube extending from the end of the container (2).
(9), and a filtrate discharge passage (1)
0) is connected, and a pulley (1) is provided at the end of the hollow rotary shaft (3).
1), and a filter (1) is provided in which the pulley (11) is connected to a motor (not shown) via a belt (12) (Japanese Patent Application Laid-Open Nos. 53-37950 and 56-56). -5
No. 6772, JP-A-56-77270).

【0003】 上記濾過機(1) を使用して濾過を行なう
には、該容器(2) 内に被処理液導入口(5) から被処理液
を圧入し、該中空濾材(4) によって該被処理液を濾過
し、濾液を該中空濾材(4) 内部から導通孔(7) を介して
該中空回転軸(3) の濾液流路(3A)に導入し、そして該濾
液を該中空回転軸(3)の濾液排出口(8) から被覆筒(9)
を介して濾液排出路(10)へ排出する。上記濾過工程にお
いて、該濾過機(1) の中空濾材(4) 表面に該被処理液に
含まれている固形分(ケーキ)が蓄積したら、該被処理
液の圧入を停止し、該被覆筒(9) に接続している濾液排
出路(10)から逆に洗滌液あるいは濾液を該中空回転軸
(3) の濾液流路(3A)を介して中空濾材(4) 内に圧入し、
該濾液を該中空濾材(4) の内側から外側に通過させつゝ
モーターによって該中空回転軸(3) を介して該中空濾材
(4) を回転させる。このようにして該中空濾材(4) 表面
に蓄積したケーキを該中空濾材(4) の内側から洗滌液あ
るいは濾液で押して剥離させ、かつ該中空濾材(4) の回
転による遠心力によって該ケーキを該中空濾材(4) 表面
から振り落とすことによって該中空濾材(4) 表面に蓄積
したケーキを除去する。
In order to perform filtration using the above-mentioned filter (1), the liquid to be treated is pressed into the vessel (2) from the liquid inlet (5), and is filtered by the hollow filter medium (4). The liquid to be treated is filtered, the filtrate is introduced from the inside of the hollow filter medium (4) into the filtrate flow path (3A) of the hollow rotary shaft (3) through the through-hole (7), and the filtrate is rotated in the hollow rotary medium (3). From the filtrate outlet (8) of the shaft (3), coat the cylinder (9)
To the filtrate discharge passage (10). In the above-mentioned filtration step, when solids (cake) contained in the liquid to be treated accumulate on the surface of the hollow filter medium (4) of the filter (1), press-in of the liquid to be treated is stopped, and Conversely, the washing liquid or the filtrate is discharged from the filtrate discharge path (10) connected to (9) to the hollow rotary shaft.
Press-fit into the hollow filter medium (4) through the filtrate channel (3A) of (3),
The filtrate is passed from the inside to the outside of the hollow filter medium (4), and the hollow filter medium is passed through the hollow rotary shaft (3) by a motor.
(4) Rotate. The cake thus accumulated on the surface of the hollow filter medium (4) is separated from the inside of the hollow filter medium (4) by pressing with a washing solution or a filtrate, and the cake is separated by centrifugal force caused by the rotation of the hollow filter medium (4). The cake accumulated on the surface of the hollow filter medium (4) is removed by shaking off the surface of the hollow filter medium (4).

【0004】[0004]

【発明が解決しようとする課題】 しかしながら上記従
来の濾過機では、該中空濾材表面に蓄積したケーキを洗
滌液あるいは濾液の押圧力と該中空濾材(4) の回転によ
る遠心力とによって除去するため、該ケーキが粘着性の
大きなものであると該中空濾材(4) の表面に多量残留す
ると言う問題点があった。
However, in the above conventional filter, the cake accumulated on the surface of the hollow filter medium is removed by the pressing force of the washing liquid or the filtrate and the centrifugal force caused by the rotation of the hollow filter medium (4). However, there is a problem that a large amount of the cake remains on the surface of the hollow filter medium (4) if the cake has a high tackiness.

【0005】[0005]

【課題を解決するための手段】 本発明は上記従来の課
題を解決する手段として、容器(22)と、該容器(22)内に
回転可能に差渡され濾液流路(23F) を有する回転軸(23)
と、該回転軸(23)に取付けられている一個または二個以
上の中空濾材(24)と、該容器(22)内に取付けられ該中空
濾材(24)表面に接触するブラシ(25)とからなり、該容器
(22)には被処理液導入口(26)とドレン排出口(27)とが設
けられ、該中空濾材(24)は濾枠(24A) と該濾枠(24A) に
被覆さ れている濾布(24B) とからなり、該中空濾材(24)
内部は該回転軸(23)の濾液流路(23F) に連絡し、該回転
軸(23)の濾液流路(23F) は濾液排出路(33)に連絡し、該
中空濾材(24)内には該濾液排出路(33)を介して流体圧を
及ぼすこと が可能にされている濾過機(21)を提供するも
のであり、更に該濾過機(21)を用い該濾過機(21)の容器
(22)内に被処理液導入口(26)から被処理液を圧送し、該
中空濾材(24)において該被処理液を濾過し、濾液は該
濾材(24)内部から該回転軸(23)の濾液排出路(33)へ導
入し、該回転軸(23)の濾液排出口(23D) から排出し、
中空濾材(24)表面に蓄積したケーキCは該中空濾材(24)
を回転軸(23)を介して回転させると共に該濾液排出路(3
3)を介して該中空濾 材(24)内に流体圧を導入し、該流体
圧によって該中空濾材(24)の濾布(24B) を押して該ブラ
シ(25)に圧接せしめることによってブラシ(25)によって
掻落す濾過方法を提供するものである。
According to the present invention, as a means for solving the above-mentioned conventional problems, there is provided a container (22) and a rotatable pump (23F) rotatably provided in the container (22). Shaft (23)
When the brush in contact with the one or the two or more hollow filter medium (24), said hollow <br/> filter medium (24) attached to the container (22) in the surface attached to the rotating shaft (23) (25)
(22) is provided with a liquid to be treated inlet (26) and a drain outlet (27), and the hollow filter medium (24) is connected to a filter frame (24A) and the filter frame (24A).
Coated with which the filter cloth becomes from the (24B), the hollow filter medium (24)
Internal contact filtrate flow path of the rotary shaft (23) (23F), the filtrate channel of the rotary shaft (23) (23F) is to contact the filtrate discharge channel (33), said
Fluid pressure is set in the hollow filter medium (24) through the filtrate discharge passage (33).
To provide a filter (21) that is capable of exerting the same , further using the filter (21) and a container of the filter (21).
The liquid to be treated is pressure-fed from the liquid introduction port (26) into (22),
The該被treatment solution was filtered in a hollow filter medium (24), the filtrate is in the
It is introduced into the filtrate discharge passage (33) of the rotary shaft (23) from the inside of the empty filter medium (24), and discharged from the filtrate discharge port (23D) of the rotary shaft (23).
Cake accumulated on the hollow filter medium (24) surface C is the hollow filter medium (24)
Is rotated through the rotary shaft (23) Rutotomoni filtrate discharge channel (3
3) through the introducing fluid pressure into the hollow filtration material (24) within the fluid
The filter cloth (24B) of the hollow filter medium (24) is pressed by pressure to
The present invention provides a filtration method in which the brush (25) is scraped off by being pressed against the cloth (25).

【0006】[0006]

【作用】 被処理液導入口(26)から容器(22)内に被処理
液を圧入し、該被処理液を中空濾材(24)によって濾過す
る。濾液は該中空濾材(24)から回転軸(23)の濾液流路(2
3F) に流入し、更に該濾液流路(23F) に連絡する濾液排
出路(33)から排出され、該被処理液中に含まれている固
形分はケーキとして該中空濾材(24)の表面に蓄積する。
該中空濾材(24)が目詰まりして濾過効率が低下して来た
ら該回転軸(23)を介して該中空濾材(24)を回転させる
共に該中空濾材(24)の内部に濾液排出 路(33)を介して流
体圧を及ぼす。そうすると該中空濾材(24)の濾布(24B)
該流体圧によって該中空濾材(24)の内側から押されて
該ブラシ(25)に均一に 圧接し、同時に該濾布(24B) 表面
に付着しているケーキCは該圧力によって 濾布(24B) か
ら剥がれ易くなり、この状態で該中空濾材(24)の濾布(2
4B) の表面に接触しているブラシ(25)が該濾布(24B)
表面を擦過するので、該 布(24B) 表面に蓄積している
ケーキは該ブラシ(25)によって効率良くこすり落され
る。
The liquid to be treated is pressed into the container (22) through the liquid inlet (26), and the liquid to be treated is filtered by the hollow filter medium (24). The filtrate flows from the hollow filter medium (24) to the filtrate channel (2) on the rotating shaft (23).
3F), and is further discharged from a filtrate discharge path (33) communicating with the filtrate flow path (23F), and solids contained in the liquid to be treated are converted into cakes on the surface of the hollow filter medium (24). To accumulate.
When the hollow filter medium (24) rotates the hollow filter medium (24) through the rotary shaft After filtration efficiency comes reduced clogged (23)
Both flow through the filtrate discharge passage (33) inside the hollow filter medium (24).
Exerts body pressure. Then the filter cloth (24B) of the hollow filter medium (24)
Is pushed from the inside of the hollow filter medium (24) by the fluid pressure.
The brush (25) is evenly pressed against the surface of the filter cloth (24B).
The cake C adhered to the filter cloth (24B)
Easily peeled al, filter cloth of the hollow filter medium (24) in this state (2
Since the brush in contact with the surface of the 4B) (25) is abraded surface of the filter cloth (24B), the cake that accumulated in the filtration fabric (24B) surfaces rubbing efficiently by the brush (25) Dropped.

【0007】[0007]

【実施例】 本発明を図1〜図3に示す一実施例によっ
て説明すれば、濾過機(21)は容器(22)と、該容器(22)内
に回転可能に差渡されている回転軸(23)と、該回転軸(2
3)に取付けられている複数個の中空濾材(24)と、該中空
濾材(24)の表面に接触するブラシ(25)とからなり、該中
空濾材(24)は図2に示すように濾枠(24A) と該濾枠(24
A) に被覆されている濾布(24B) とからなる。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described with reference to an embodiment shown in FIGS. 1 to 3. A filter (21) includes a container (22) and a rotatable rotatably provided in the container (22). Shaft (23) and the rotating shaft (2
3) a plurality of hollow filter media (24) attached to the filter, and a brush (25) in contact with the surface of the hollow filter media (24). The hollow filter media (24) has a filter as shown in FIG. Frame (24A) and the filter frame (24
A) and a filter cloth (24B) coated thereon.

【0008】 該容器(22)にはバルブ(26A) を有する被
処理液導入口(26)とバルブ(27A) を有するドレン排出口
(27)とが設けられており、該回転軸(23)は断面三股状で
あり、先端部(23A) は丸棒状にされ、該容器(22)前端の
軸受部(28)に回転可能に軸支され、該回転軸(23)の後端
部(23B) は円筒状にされ、更に該後端部(23B) の端末か
らは丸棒状の根端部(23C) が差出され、該根端部(23C)
は該容器(22)後端から延設され該回転軸(23)の後端部(2
3B)を被覆する被覆筒(22A) の端末の軸受部(29)に回転
可能に軸支され、該回転軸(23)の根端部(23C) は該被覆
筒(22A) から外出し、外出端にはプーリー(30)が取付け
られ、該プーリー(30)はベルト(31)を介してモーター(3
2)と連絡しており、更に被覆筒(22A) にはバルブ(33A)
を有する濾液排出路(33)が連絡している。そして該被覆
筒(22A) 内において該回転軸(23)の後端部(23B)には濾
液排出口(23D) が設けられている。該回転軸(23)には複
数個の中空濾材(24)が取付けられているが、該中空濾材
(24)は図2に示すように濾枠(24A) と該濾枠(24A) に被
覆されている濾布(24B) とからなり、該濾布(24B) は好
ましくはポリエステル繊維、ポリ塩化ビニリデン繊維、
ポリプロピレン繊維、ポリアミド繊維等の熱可塑性繊維
の織物からなり、表面に付着するケーキの剥離を容易に
するために表面はカレンダー加工によって平滑にされて
いることが望ましい。そして該中空濾材(24)は中心孔(2
4C) を介して回転軸(23)に取付けられているが、該中空
濾材(24)間にはリング状のスペーサー(34)が介在し、先
端部においてフランジ(35)によって固定され、後端部は
該回転軸(23)の後端部(23B) のフランジ(23E) およびス
ペーサー(36)によって固定されている。このようにして
該中空濾材(24)は回転軸(23)に固定されているが、該回
転軸(23)は断面三股状であるので該中空濾材(24)の中心
孔(24C) と回転軸(23)との間は中空状態になって濾液流
路(23F) が形成されている。
The container (22) has a liquid inlet (26) having a valve (26A) and a drain outlet having a valve (27A).
(27), the rotating shaft (23) has a trifurcated cross section, the tip (23A) is a round bar, and the container (22) is rotatable with the bearing (28) at the front end. The rear end (23B) of the rotary shaft (23) is cylindrically supported, and a round bar-shaped root end (23C) is protruded from the end of the rear end (23B). End (23C)
Extends from the rear end of the container (22) and extends to the rear end (2
3B) is rotatably supported by a bearing (29) at the end of a coating cylinder (22A) that covers the coating cylinder (22A), and the root end (23C) of the rotating shaft (23) is out of the coating cylinder (22A), A pulley (30) is attached to the outside end, and the pulley (30) is connected to a motor (3) via a belt (31).
2), and a valve (33A)
The filtrate discharge path (33) having the following is connected. A filtrate outlet (23D) is provided at the rear end (23B) of the rotating shaft (23) in the coating tube (22A). A plurality of hollow filter media (24) are attached to the rotating shaft (23).
As shown in FIG. 2, (24) comprises a filter frame (24A) and a filter cloth (24B) coated on the filter frame (24A), and the filter cloth (24B) is preferably made of polyester fiber or polychlorinated fiber. Vinylidene fiber,
It is preferably made of a woven fabric of a thermoplastic fiber such as a polypropylene fiber or a polyamide fiber, and the surface is desirably smoothed by calendering in order to facilitate peeling of the cake adhering to the surface. The hollow filter medium (24) has a central hole (2
4C), the ring-shaped spacer (34) is interposed between the hollow filter media (24), and is fixed at the front end by a flange (35). The part is fixed by a flange (23E) of a rear end (23B) of the rotating shaft (23) and a spacer (36). In this way, the hollow filter medium (24) is fixed to the rotating shaft (23), but since the rotating shaft (23) has a forked cross section, the hollow filter medium (24) rotates with the center hole (24C) of the hollow filter medium (24). The filtrate flow path (23F) is formed hollow between the shaft (23).

【0009】 該ブラシ(25)は基板(25A) と該基板(25
A) の表裏面の片側に形成されている植毛層(25B) とか
らなり、該基板(25A) の頭部(25C) の孔(25D) を介して
該容器(22)内の上部に差渡されている固定棒(37)に支持
されている。そして該ブラシ(25)の植毛層(25B) の長さ
は該中空濾材(24)の濾布(24B) 表面に接触するように設
定されている。
The brush (25) includes a substrate (25A) and the substrate (25A).
A) A flocking layer (25B) formed on one side of the front and back surfaces of the substrate (25A), and is inserted into the upper portion of the container (22) through the hole (25D) of the head (25C) of the substrate (25A). It is supported by the fixed bar (37) being passed. The length of the flocked layer (25B) of the brush (25) is set so as to be in contact with the surface of the filter cloth (24B) of the hollow filter medium (24).

【0010】 上記濾過機(21)において濾過を行なうに
は、先ずドレン排出口(27)のバルブ(27A) を閉じ、被処
理液導入口(26)のバルブ(26A) を開き、更に濾液排出路
(33)のバルブ(33A) を開いて、該被処理液導入口(26)か
ら容器(22)内に被処理液を圧入する。該被処理液は該容
器(22)内において中空濾材(24)によって濾過され、濾液
は図1矢印に示すように回転軸(23)の濾液流路(23F) に
沿って該回転軸(23)の後端部(23B) へ流れ、該後端部(2
3B)の濾液排出口(23D) から容器(22)の被覆筒(22A) 内
に排出され、そして濾液排出路(33)から外部へ排出され
る。
To perform filtration in the filter (21), first, the valve (27A) of the drain outlet (27) is closed, the valve (26A) of the liquid inlet (26) is opened, and the filtrate is further discharged. Road
The valve (33A) of (33) is opened, and the liquid to be treated is pressed into the container (22) from the liquid inlet (26). The liquid to be treated is filtered through the hollow filter medium (24) in the vessel (22), and the filtrate is passed along the filtrate flow path (23F) of the rotating shaft (23) as shown by the arrow in FIG. ) To the rear end (23B).
The filtrate is discharged from the filtrate discharge port (23D) of 3B) into the coating tube (22A) of the container (22), and discharged to the outside from the filtrate discharge passage (33).

【0011】 上記濾過工程中該被処理液中の固形分は
ケーキCとして該中空濾材(24)の濾布(24B) の表面に付
着するので、次第に該濾布(24B) は目詰りして濾過効率
が低下して来る。したがって適当な時期に被処理液導入
口(26)のバルブ(26A) を閉じて被処理液の容器(22)内へ
の圧送を停止し、モーター(32)を作動させて回転軸(23)
を介して図3に示すように中空濾材(24)を矢印方向に回
転させると共に該濾液排出路(33)から濾液を中空濾材(2
4)内 に逆送して中空濾材(24)内に流体圧を及ぼす。そう
すると該中空濾材(24)の 濾布(24B) は該流体圧によって
該中空濾材(24)の内側から押されて該ブラシ (25)の植毛
層(25B) に均一に圧接し、かつケーキCは該圧力によっ
て濾布(2 4B) から剥がれ易くなり、この状態で該中空濾
材(24)の濾布(24B) の表面を該ブラシ(25)の植毛層(25
B) が擦過し、図3に示すように該濾布(24B) の表面に
付着しているケーキCは該植毛層(25B) によって効率良
こすり落とされる。この場合の中空濾材(24)の回転数
は通常3〜5rpm とし、2〜4回程度回転させる。
During the above-mentioned filtration step, the solid content in the liquid to be treated adheres to the surface of the filter cloth (24B) of the hollow filter medium (24) as cake C, so that the filter cloth (24B) gradually becomes clogged. Filtration efficiency decreases. Therefore, at an appropriate time, the valve (26A) of the liquid to be treated inlet (26) is closed to stop the pumping of the liquid to be treated into the container (22), and the motor (32) is operated to rotate the rotating shaft (23).
A hollow filter medium (24) is rotated in the arrow direction as shown in FIG. 3 through Rutotomoni filtrate discharge channel (33) filtrate hollow filter medium (2
The fluid is fed back into 4) to exert fluid pressure in the hollow filter medium (24). so
Then, the filter cloth (24B) of the hollow filter medium (24 ) is caused by the fluid pressure.
Flooding of the brush (25) by being pushed from the inside of the hollow filter medium (24)
The layer (25B) is pressed uniformly to the layer (25B), and the cake C is pressed by the pressure.
Easily peeled off from the filter cloth (2 4B) Te, flocked layer of filter cloth surface of (24B) said brush (25) of the hollow filter medium (24) in this state (25
B) is abraded, efficiency good by the filter cloth as shown in FIG. 3 (cake C is plant hair layer adhering to the surface of 24B) (25B)
Ku is scraped off. In this case, the rotation speed of the hollow filter medium (24) is usually 3 to 5 rpm, and it is rotated about 2 to 4 times.

【0012】 このようにして中空濾材(24)の濾布(24
B) 表面に付着しているケーキCをブラシ(25)で除去し
た後、ドレン排出口(27)のバルブ(27A) を開いて、容器
(22)内に残留していた被処理液と共に中空濾材(24)の濾
(24B) 表面から除去されたケーキCを外部へ排出し、
その後は再び濾過工程に移る。上記ケーキ除去工程の
、容器(22)内の被処理液を洗滌水に入替えておいても
よい。
In this way, the filter cloth (24 ) of the hollow filter medium (24)
B) After removing cake C adhering to the surface with a brush (25), open the valve (27A) of the drain outlet (27), and
Filtration of the hollow filter medium (24) together with the liquid to be treated remaining in (22)
The cake C removed from the cloth (24B) surface is discharged to the outside,
Thereafter, the process returns to the filtration step. During the cake removal process, it may have been replaced the liquid to be treated in the container (22) to the wash water.

【0013】 上記実施例以外、図4に示すようにブラ
シ(45)の基板として二分割した基板(45A,45B) を用い、
該基板(45A,45A) 間にスペーサー(45C) を挟んでもよ
い。このような構造のブラシ(45)を用いると、該ブラシ
(45)の植毛層(45D) が摩耗して中空濾材(24)の濾布(24
B) 表面に圧接しなくなった場合、該スペーサー(45C)
をより厚いものに代えると、該植毛層(45D)は再び該中
空濾材(24)の濾布(24B) 表面に圧接するようになる。ま
たブラシ(45)の植毛層(45D) は基板(45A,45A) の表面全
面に形成されてもよいが、前実施例および本実施例のよ
うに片側のみに形成すれば植毛層の材料を節約すること
が出来る。
In addition to the above embodiment, as shown in FIG. 4, a substrate (45A, 45B) divided into two is used as a substrate of the brush (45).
A spacer (45C) may be interposed between the substrates (45A, 45A). When a brush (45) having such a structure is used, the brush
The flocked layer (45D) of (45) wears out and the filter cloth (24
B) If no longer press against the surface, the spacer (45C)
When is replaced with a thicker one, the flocked layer (45D) comes into pressure contact with the surface of the filter cloth (24B) of the hollow filter medium (24) again. The flocked layer (45D) of the brush (45) may be formed on the entire surface of the substrate (45A, 45A), but if formed on only one side as in the previous embodiment and this embodiment, the material of the flocked layer is reduced. You can save.

【0014】 更に上記実施例以外、中空濾材は濾枠
と、該濾枠に被覆されている金網からなる構成でもよい
し、またプラスチックビーズ、セラミック粉、金属粉等
の焼結体等を材料としてもよい。また回転軸(43)は内部
に濾液流路(43A) を形成した中空軸としてもよい。この
場合は該回転軸(43)の中空濾材(24)取付け位置に濾液導
通孔(43B) を設ける。しかし本実施例では中空濾材(24)
と濾液導通孔(43B) との位置合わせを行なう必要があ
り、前実施例の断面三股状の回転軸(23)の場合はこのよ
うな位置合わせの手間が不要である。更に本発明の濾過
機においては濾過工程中に濾材を回転させることによっ
てケーキを除去することも可能である。
Further, in addition to the above embodiments, the hollow filter medium may be formed of a filter frame and a wire mesh coated on the filter frame, or may be made of a sintered body such as plastic beads, ceramic powder, metal powder, or the like. Is also good. The rotating shaft (43) may be a hollow shaft having a filtrate flow path (43A) formed therein. In this case, a filtrate passage hole (43B) is provided in the rotary shaft (43) at a position where the hollow filter medium (24) is attached. However, in this embodiment, the hollow filter medium (24)
It is necessary to perform the alignment between the rotary shaft and the filtrate passage hole (43B), and in the case of the rotating shaft (23) having a three-pronged cross section of the previous embodiment, such a labor of alignment is unnecessary. Further, in the filter of the present invention, the cake can be removed by rotating the filter medium during the filtration step.

【0015】[0015]

【発明の効果】 したがって本発明においては中空濾材
の濾布を内側から 流体圧によってブラシに押付けるの
で、該濾布は該ブラシに均一に圧接し、 その結果該
に付着したケーキを略完全に効率良く除去することが出
来、中空濾材洗滌の頻度や中空濾材交換の頻度を大巾に
減少させることが出来、また濾布の損傷やブラシの不規
則な摩耗も回避出来、極めて合理的に濾過工程を行なう
ことが出来る。
Accordingly, in the present invention, the hollow filter medium is used.
Press the filter cloth against the brush from inside with fluid pressure
In, filtrate cloth uniformly pressed against the brush, the frequency of the result can be substantially completely removed efficiently cake adhered to the filtration fabric <br/>, the frequency of the hollow filter medium washing and hollow filter medium exchange Can be greatly reduced, and filter cloths can be damaged
Regular abrasion can be avoided , and the filtration step can be performed very reasonably.

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

図1〜図3は本発明の一実施例を示すものである。 1 to 3 show one embodiment of the present invention.

【図1】 側断面図FIG. 1 is a side sectional view

【図2】 中空濾材取付部分斜視図FIG. 2 is a perspective view of a hollow filter medium mounting portion.

【図3】 中空濾材正面図FIG. 3 is a front view of a hollow filter medium.

【図4】 ブラシの他の実施例の斜視図FIG. 4 is a perspective view of another embodiment of the brush.

【図5】 回転軸の他の実施例の部分断面図FIG. 5 is a partial sectional view of another embodiment of the rotating shaft.

【図6】 従来例の説明図FIG. 6 is an explanatory view of a conventional example.

【符号の説明】[Explanation of symbols]

21 濾過機 22 容器 23,43 回転軸 23D 濾液排出口 23F,43A 濾液流路 24 中空濾材24A 濾枠 24B 濾布 25,45 ブラシ 26 被処理液導入口 27 ドレン排出口 33 濾液排出路21 Filtration machine 22 Container 23,43 Rotating shaft 23D Filtrate outlet 23F, 43A Filtrate flow path 24 Hollow filter medium 24A Filter frame 24B Filter cloth 25,45 Brush 26 Liquid to be treated inlet 27 Drain outlet 33 Filtrate outlet

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】容器と、該容器内に回転可能に差渡され濾
液流路を有する回転軸と、該回転軸に取付けられている
一個または二個以上の中空濾材と、該容器内に取付けら
れ該中空濾材表面に接触するブラシとからなり、該容器
には被処理液導入口とドレン排出口とが設けられ、該中
空濾材は濾枠と該濾枠 に被覆されている濾布とからな
り、該中空濾材内部は該回転軸の濾液流路に連絡し、該
回転軸の濾液流路は濾液排出路に連絡し、該中空濾材内
には該濾 液排出路を介して流体圧を及ぼすことが可能に
されていることを特徴とする濾過機
1. A container, a rotating shaft rotatably inserted into the container and having a filtrate flow path, one or more hollow filter media mounted on the rotating shaft, and mounted in the container. is composed of a brush in contact with the hollow filter medium surface, the container is provided with the liquid to be treated inlet and drain outlet, intermediate
The empty filter medium comprises a filter frame and a filter cloth coated on the filter frame.
The inside of the hollow filter medium communicates with the filtrate flow path of the rotating shaft, the filtrate flow path of the rotating shaft communicates with the filtrate discharge path, and the inside of the hollow filter medium
Can apply fluid pressure through the filtrate discharge path
Filter characterized by the fact that
【請求項2】容器と、該容器内に回転可能に差渡され濾
液流路を有する回転軸と、該回転軸に取付けられている
一個または二個以上の中空濾材と、該容器内に取付けら
れ該中空濾材表面に接触するブラシとからなり、該容器
には被処理液導入口とドレン排出口とが設けられ、該中
空濾材は濾枠と該濾枠 に被覆されている濾布とからな
り、該中空濾材内部は該回転軸の濾液流路に連絡し、該
回転軸の濾液流路は濾液排出路に連絡し、該中空濾材内
には該濾 液排出路を介して流体圧を及ぼすことが可能に
されている濾過機を使用し、該濾過機の容器内に被処理
液導入口から被処理液を圧送し、該中空濾材において該
被処理液を濾過し、濾液は該中空濾材内部から該回転軸
の濾液排出路へ導入し、該回転軸の濾液排出口から排出
し、該中空濾材表面に蓄積したケーキは該中空濾材を回
転軸を介して回転させると共に該濾液排出路を介して
中空濾材内に流体圧を導入し、該流体圧によって該中空
濾材の濾布を押し て該ブラシに圧接せしめることによっ
ブラシによって掻落すことを特徴とする濾過方法
2. A container, a rotating shaft rotatably passed through the container and having a filtrate flow path, one or more hollow filter media mounted on the rotating shaft, and mounted in the container. is composed of a brush in contact with the hollow filter medium surface, the container is provided with the liquid to be treated inlet and drain outlet, intermediate
The empty filter medium comprises a filter frame and a filter cloth coated on the filter frame.
The inside of the hollow filter medium communicates with the filtrate flow path of the rotating shaft, the filtrate flow path of the rotating shaft communicates with the filtrate discharge path, and the inside of the hollow filter medium
Can apply fluid pressure through the filtrate discharge path
Using the filter machine which is the liquid to be treated is pumped from the treated liquid inlet port into the container of the filter machine and filtered該被processing solution in said hollow filter medium, the filtrate is the rotating from inside the hollow filter medium introduced into the axial filtrate discharge passage, and discharged from the filtrate outlet of the rotary shaft, the hollow filter medium surface on the accumulated cake through Rutotomoni filtrate discharge passage is rotated through the rotation axis of said hollow filter medium the
A fluid pressure is introduced into the hollow filter medium, and the fluid pressure causes the hollow
By pressing the filter medium filter cloth and pressing it against the brush,
Method characterized by scraping off with a brush
JP7017500A 1995-01-06 1995-01-06 Filtration machine and filtration method Expired - Fee Related JP2767690B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7017500A JP2767690B2 (en) 1995-01-06 1995-01-06 Filtration machine and filtration method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7017500A JP2767690B2 (en) 1995-01-06 1995-01-06 Filtration machine and filtration method

Publications (2)

Publication Number Publication Date
JPH08187407A JPH08187407A (en) 1996-07-23
JP2767690B2 true JP2767690B2 (en) 1998-06-18

Family

ID=11945720

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7017500A Expired - Fee Related JP2767690B2 (en) 1995-01-06 1995-01-06 Filtration machine and filtration method

Country Status (1)

Country Link
JP (1) JP2767690B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107684769A (en) * 2017-09-29 2018-02-13 威孔过滤科技(苏州)有限公司 Quickly press dry filter and its filter method

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6018202B2 (en) * 1976-10-09 1985-05-09 アイドレツクス・インコ−ポレ−テツド Furnace filtration device
US4608169A (en) * 1985-07-15 1986-08-26 Arvanitakis Kostas S Filter brush
JPS62225214A (en) * 1986-03-27 1987-10-03 Miura Eng Internatl Kk Method for obtaining low-liquid content cake

Also Published As

Publication number Publication date
JPH08187407A (en) 1996-07-23

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