JPH0780251A - Micro-filtering apparatus - Google Patents

Micro-filtering apparatus

Info

Publication number
JPH0780251A
JPH0780251A JP25234593A JP25234593A JPH0780251A JP H0780251 A JPH0780251 A JP H0780251A JP 25234593 A JP25234593 A JP 25234593A JP 25234593 A JP25234593 A JP 25234593A JP H0780251 A JPH0780251 A JP H0780251A
Authority
JP
Japan
Prior art keywords
filter medium
filter
granular
cylinder
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.)
Granted
Application number
JP25234593A
Other languages
Japanese (ja)
Other versions
JP3082538B2 (en
Inventor
Eiichi Ishigaki
栄一 石垣
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.)
Ishigaki Mechanical Industry Co Ltd
Original Assignee
Ishigaki Mechanical Industry Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Ishigaki Mechanical Industry Co Ltd filed Critical Ishigaki Mechanical Industry Co Ltd
Priority to JP05252345A priority Critical patent/JP3082538B2/en
Publication of JPH0780251A publication Critical patent/JPH0780251A/en
Application granted granted Critical
Publication of JP3082538B2 publication Critical patent/JP3082538B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

PURPOSE:To provide a micro-filtering apparatus using a ceramic membrane and capable of simply washing and regenerating a filter medium. CONSTITUTION:A floatable granular filter medium is supplied in a filter tank 1 and a filter cylinder 3 using a ceramic membrane is embedded in the filter medium bed formed by the granular filter medium so that a filtrate is taken out of the hollow part of the filter cylinder 3 and the stirrer 4 of the granular filter medium is installed under the filter medium bed 2. A supplied raw soln. is passed through the granular filter medium to separate impurities in the raw soln, and the fine solid in the raw soln. is further removed by the filter cylinder 3. When the granular filter medium and the filter cylinder 3 are clogged, by stirring the granular filter medium, the clogging substance of the granular filter medium and the filter cylinder can be removed at a stroke.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】この発明は、セラミック膜を用い
た精密ろ過装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a microfiltration device using a ceramic membrane.

【0002】[0002]

【従来の技術】従来、セラミック膜を用いた精密ろ過装
置はよく知られている。すなわち、図2に示すように砂
ろ過機でろ過したろ液を中空外圧式のセラミック膜を多
数垂下したろ過槽内に導入してろ過する精密ろ過装置が
一般に用いられている。そして、セラミック膜が目詰り
したときには、これを洗浄再生するには、図3に示すよ
うにセラミック膜の表面を逆洗空気や逆洗水を流動させ
ている。
2. Description of the Related Art Conventionally, a microfiltration device using a ceramic membrane is well known. That is, as shown in FIG. 2, a microfiltration device is generally used in which a filtrate filtered by a sand filter is introduced into a filtration tank in which a large number of hollow external pressure type ceramic membranes are suspended and filtered. Then, when the ceramic membrane is clogged, in order to wash and regenerate it, backwash air or backwash water is made to flow over the surface of the ceramic membrane as shown in FIG.

【0003】[0003]

【発明が解決しようとする課題】然しながら、上述のよ
うな従来の精密ろ過装置では、精密ろ過をする前段に砂
ろ過装置等のろ過装置を必要とし、また、これらろ過装
置のろ材が目詰りしたときには、それぞれ洗浄再生が必
要である。また、上述のようなセラミック膜の洗浄再生
では、セラミック膜の表面を逆洗水あるいは逆洗空気の
流体を流動させるのみであるので、完全な洗浄は困難で
ある。
However, the conventional microfiltration apparatus as described above require a filtration apparatus such as a sand filtration apparatus before the microfiltration, and the filter media of these filtration apparatuses are clogged. Occasionally, cleaning and regeneration are required for each. Further, in the above-described cleaning and regeneration of the ceramic membrane, the surface of the ceramic membrane is simply made to flow a fluid of backwash water or backwash air, so that complete washing is difficult.

【0004】[0004]

【課題を解決するための手段】この発明は、上述のよう
な課題を一挙に解決し得るものであって、前処理用のろ
過装置を設けることなく、一つのろ過槽内で一挙に精密
ろ過が可能であるとともに、ろ材が目詰りしたときに
も、簡単に再生できるもので、その要旨とするところ
は、浮上性の粒状ろ材を充填したろ過槽内に、その粒状
ろ材が形成するろ材層に埋没させてセラミック膜よりな
るろ過筒を垂下し、そのろ過筒の中空部からろ液を槽外
に取り出すようにするとともに、上記ろ材層の下方に
は、ろ材層の撹拌装置を設置したものである。
SUMMARY OF THE INVENTION The present invention can solve the above-mentioned problems all at once, and does not require a pretreatment filtration device to perform microfiltration at once in one filtration tank. It is possible to regenerate even when the filter medium is clogged, and the main point is that the filter medium layer formed by the granular filter medium is formed in the filtration tank filled with the floating granular filter medium. A filter tube made of ceramic membrane that is buried in the filter, and the filtrate is taken out of the tank from the hollow part of the filter tube, and a stirring device for the filter layer is installed below the filter layer. Is.

【0005】[0005]

【作用】この発明に係る装置は、上述のように構成して
あり、ろ過槽に供給された原液は、先ず、粒状ろ材層に
よって夾雑物が捕捉除去された上でろ過筒で微少な固形
物が除去され、そのろ液は、ろ過筒の中空部を経て槽外
に取り出すことができる。そして、粒状のろ材層および
ろ過筒が目詰りしたときには、撹拌装置によって、粒状
ろ材層を撹拌することによって、粒状ろ材層がほぐさ
れ、その粒子間に詰まった夾雑物が分離されるととも
に、撹乱する粒状ろ材がろ過筒の膜面に衝突して付着し
た固形物を剥離し、ろ過筒も同時に再生することができ
る。尚、分離した夾雑物および固形物は、ろ過槽に設け
た排出手段によって、粒状ろ材とは分離して槽外に排出
するものである。以下、図面に基づいてこの発明を具体
的に説明する。
The apparatus according to the present invention is constructed as described above. First, the undiluted solution supplied to the filtration tank is subjected to trapping and removal of impurities by the granular filter medium layer, and then the fine solids are filtered by the filter tube. Is removed, and the filtrate can be taken out of the tank through the hollow portion of the filtration cylinder. Then, when the granular filter medium layer and the filter tube are clogged, the granular filter medium layer is loosened by stirring the granular filter medium layer by the agitator, and the foreign substances clogged between the particles are separated and disturbed. The granular filter medium collides with the membrane surface of the filter cylinder to remove the adhered solid matter, and the filter cylinder can be regenerated at the same time. The separated contaminants and solids are separated from the granular filter medium by the discharging means provided in the filtration tank and discharged outside the tank. Hereinafter, the present invention will be specifically described with reference to the drawings.

【0006】[0006]

【実施例】図1において、符号1はろ過槽、2は充填し
た粒状ろ材が形成したろ材層、3は、ろ材層2中に埋没
させて垂下したセラミック膜よりなるろ過筒、4はろ過
槽1の底部に設けた撹拌翼、5は原液の供給管、6はろ
液の取出管、7は洗浄水の排出管である。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS In FIG. 1, reference numeral 1 is a filter tank, 2 is a filter medium layer formed by a filled granular filter medium, 3 is a filter cylinder made of a ceramic membrane suspended in the filter medium layer 2, and 4 is a filter tank. A stirring blade provided at the bottom of 1 is a supply pipe for the stock solution, 6 is a discharge pipe for the filtrate, and 7 is a discharge pipe for washing water.

【0007】この発明に係る装置は、上述のように構成
してあり、粒状のろ材は、原液を供給することで、ろ過
槽内で浮上し、ろ過筒3を包むようにその周辺でろ材層
2を形成する。供給管5からろ過槽1内に供給された原
液は、このろ材層2を通過する間に夾雑物が捕捉された
のち、ろ過筒3のセラミック膜によってさらに微少な固
形物が捕捉され、清浄なろ液を取出管6から得ることが
できる。
The apparatus according to the present invention is constructed as described above, and the granular filter medium is floated in the filter tank by supplying the undiluted solution, and the filter medium layer 2 is provided around the filter cylinder 3 so as to wrap it. To form. In the undiluted solution supplied from the supply pipe 5 into the filtration tank 1, impurities are captured while passing through the filter medium layer 2, and then a fine solid matter is further captured by the ceramic membrane of the filtration cylinder 3 to obtain a clean filter. The liquid can be obtained from the discharge pipe 6.

【0008】このような運転をして、ろ材層2およびろ
過筒3のセラミック膜が目詰りしたときには、原液の供
給およびろ液の取り出しを停止し、撹拌翼4を駆動する
ことによってその流動水流でろ材層2がほぐされ、粒状
ろ材間に詰まった夾雑物が剥離するとともに、流動する
ろ材がセラミック膜の表面に衝突することによってろ過
筒3のセラミック膜の表面に付着した微少固形物を剥離
することができる。すなわち、浮上ろ材で形成されるろ
材層2とセラミック膜を同時に更新できるものである。
尚、上述のようにして分離された夾雑物や固形物は排出
管7より槽外に取り出すので、この場合排水管7のバル
ブ7aを開くことによって、粒状ろ材よりも重い夾雑物
や固形物が先にピット7b内に沈降し、粒状ろ材は流失
することはないものである。
When the ceramic membranes of the filter medium layer 2 and the filter cylinder 3 are clogged in such an operation, the supply of the undiluted solution and the withdrawal of the filtrate are stopped, and the stirring blade 4 is driven to drive the flowing water flow. Then, the filter medium layer 2 is loosened, the foreign substances clogged between the granular filter media are peeled off, and the flowing filter medium collides with the surface of the ceramic membrane to peel off the minute solid matter adhering to the surface of the ceramic membrane of the filtration cylinder 3. can do. That is, the filter medium layer 2 formed of the floating filter medium and the ceramic film can be renewed at the same time.
Since the contaminants and solids separated as described above are taken out of the tank through the discharge pipe 7, in this case, by opening the valve 7a of the drain pipe 7, the contaminants and solids heavier than the granular filter medium are removed. The granular filter medium does not flow away because it settles into the pit 7b first.

【0009】また、撹拌翼4による槽内水流を垂下する
ろ過筒3の表面のセラミック膜に有効的に作用させるた
めには、上下水流が最適であり、このためには、撹拌翼
4自体の形状を上下水流が生じるようにしてもよいが、
図4に示すように案内筒4aを設けてもよい。さらに、
粒状ろ材は、セラミック膜に衝突して目詰り物を剥離す
るものであるので、浮上性のろ材機能を備えていること
は必要であるが、できる限り重くて慣性力の強いものが
よい。
Further, in order to effectively act the water flow in the tank by the stirring blade 4 on the ceramic membrane on the surface of the filtering cylinder 3 which depends, the up and down water flow is optimum. For this purpose, the stirring blade 4 itself Although the shape may be such that a vertical water flow occurs,
A guide tube 4a may be provided as shown in FIG. further,
Since the granular filter medium collides with the ceramic film to remove the clogging, it is necessary to have a floating filter medium function, but it is preferable that the granular filter medium be as heavy and strong in inertia as possible.

【0010】[0010]

【発明の効果】このように、この発明に係る装置は、従
来のこの種精密ろ過装置に比較して、一つのろ過槽内で
一次ろ過と二次ろ過とを同時にして、精密ろ過が可能で
あり、そして、ろ材が目詰りしたときには、これら二段
階ろ過用のろ材を一挙に洗浄再生できるもので、製作コ
ストおよび運転操作等のランニングコスト面でも、従来
の課題を解決し得たものである。
As described above, the device according to the present invention can perform the microfiltration by simultaneously performing the primary filtration and the secondary filtration in one filtration tank as compared with the conventional microfiltration device of this type. And, when the filter medium becomes clogged, it is possible to wash and regenerate the filter medium for these two-stage filtration all at once, and it is possible to solve the conventional problems in terms of production cost and running cost such as operation. is there.

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

【図1】この発明に係る精密ろ過装置の模式縦断側面図
である。
FIG. 1 is a schematic vertical sectional side view of a microfiltration device according to the present invention.

【図2】従来のこの種精密ろ過装置の模式縦断側面図で
ある。
FIG. 2 is a schematic vertical sectional side view of a conventional microfiltration device of this type.

【図3】同じく、その精密ろ過機部分の模式縦断側面図
である。
FIG. 3 is likewise a schematic vertical cross-sectional side view of the precision filter part.

【図4】この発明に係る精密ろ過装置におけるろ材の洗
浄流を説明するためのろ過槽の概略縦断面図である。
FIG. 4 is a schematic vertical cross-sectional view of a filtration tank for explaining a cleaning flow of a filter medium in the microfiltration device according to the present invention.

【符号の説明】[Explanation of symbols]

1 ろ過槽 2 ろ材層 3 ろ過筒 4 撹拌翼 1 Filter Tank 2 Filter Material Layer 3 Filter Cylinder 4 Stirrer

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 浮上性の粒状ろ材を充填したろ過槽1内
に、その粒状ろ材が形成するろ材層2に埋没させてセラ
ミック膜よりなるろ過筒3を垂下し、そのろ過筒3の中
空部からろ液を槽外に取り出すようにするとともに、上
記ろ材層の下方には、ろ材層2の撹拌装置4を設置して
なる精密ろ過装置。
1. A filter cylinder (3) made of a ceramic membrane is suspended in a filter tank (1) filled with a buoyant granular filter medium so as to be buried in a filter medium layer (2) formed by the granular filter medium, and a hollow portion of the filter cylinder (3). A microfiltration device in which the filtrate is removed from the tank and a stirring device 4 for the filter material layer 2 is installed below the filter material layer.
JP05252345A 1993-09-13 1993-09-13 Precision filtration equipment Expired - Fee Related JP3082538B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP05252345A JP3082538B2 (en) 1993-09-13 1993-09-13 Precision filtration equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP05252345A JP3082538B2 (en) 1993-09-13 1993-09-13 Precision filtration equipment

Publications (2)

Publication Number Publication Date
JPH0780251A true JPH0780251A (en) 1995-03-28
JP3082538B2 JP3082538B2 (en) 2000-08-28

Family

ID=17235992

Family Applications (1)

Application Number Title Priority Date Filing Date
JP05252345A Expired - Fee Related JP3082538B2 (en) 1993-09-13 1993-09-13 Precision filtration equipment

Country Status (1)

Country Link
JP (1) JP3082538B2 (en)

Also Published As

Publication number Publication date
JP3082538B2 (en) 2000-08-28

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