JPH07323295A - Water purifier - Google Patents

Water purifier

Info

Publication number
JPH07323295A
JPH07323295A JP6117904A JP11790494A JPH07323295A JP H07323295 A JPH07323295 A JP H07323295A JP 6117904 A JP6117904 A JP 6117904A JP 11790494 A JP11790494 A JP 11790494A JP H07323295 A JPH07323295 A JP H07323295A
Authority
JP
Japan
Prior art keywords
water
raw water
membrane
biological treatment
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
JP6117904A
Other languages
Japanese (ja)
Other versions
JP3345732B2 (en
Inventor
Koichi Anraku
幸一 安楽
Tetsuji Inoue
哲次 井上
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.)
Maezawa Industries Inc
Original Assignee
Maezawa Industries Inc
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 Maezawa Industries Inc filed Critical Maezawa Industries Inc
Priority to JP11790494A priority Critical patent/JP3345732B2/en
Publication of JPH07323295A publication Critical patent/JPH07323295A/en
Application granted granted Critical
Publication of JP3345732B2 publication Critical patent/JP3345732B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Landscapes

  • Separation Using Semi-Permeable Membranes (AREA)
  • Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
  • Biological Treatment Of Waste Water (AREA)

Abstract

PURPOSE:To reduce the space for the purifier and shorten the treating time by setting the biological treating device, membrane filter and concentrator in a single treating tank and continuously conducting discrete operations in one stage. CONSTITUTION:A biological treating device 2 for bringing raw water into contact with a contact material on which microorganisms are immobilized to purify the raw water, a membrane filter 3 for permeating the biologically treated water through a filter membrane, separating solid and liq. and discharging the treated water outside the system and a concentrator 4 placed below the biological treating device 2 and membrane filter 3 and separating the solid and precipitate contained in the raw water are set in a single treating tank 1. The raw water ascends in the tank 1 by the air 5a injected from an air injection pipe 5, flows toward the membrane filter 3 in direction of the arrow C and returns toward the biological treating device 2. A so-called circulating current is generated in this case. The treated water as a filtrate is discharged outside the system, the solid and precipitate in the raw water are separated by the concentrator 4, and the concentrated precipitate is periodically discharged outside the system from the lower part of the tank 1.

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、原水を生物処理した
後、膜濾過により固液分離を行い、分離された濁質を濃
縮する浄水装置に係り、特に、小スペース化および処理
能力の増大を図った浄水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 water purification apparatus for concentrating separated turbidity by subjecting raw water to biological treatment and then performing solid-liquid separation by membrane filtration, and in particular, reduction of space and increase of treatment capacity. The present invention relates to a water purification device.

【0002】[0002]

【従来の技術】水処理設備、特に上水設備において、原
水中に含まれるアンモニア性窒素,かび臭,藻類,マン
ガン等を生物処理により除去した後、膜濾過により固液
分離を行う浄水処理は、従来、図5に示す処理工程を経
て行われている。沈砂池51に取り入れられた原水は、
大型の浮遊物、懸濁物が取り除かれた後、着水井52に
貯留される。貯留された原水は、凝集,沈殿,濾過等通
常の浄水処理の前処理として、生物処理設備53におい
て送られ生物処理が行われる。そして、凝集沈殿池54
でフロックの沈殿除去を行った後、濾過池55で濾過さ
れ、処理水は、次工程56へと送られるものである。な
お、凝集沈殿池54で沈殿させたフロックは、濃縮装置
57で濃縮された後、排出される。
2. Description of the Related Art In a water treatment facility, particularly in a water supply facility, a water purification treatment in which solid-liquid separation is carried out by membrane filtration after removing ammoniacal nitrogen, musty odor, algae, manganese, etc. contained in raw water by biological treatment, Conventionally, it is performed through the processing steps shown in FIG. The raw water taken into the sand basin 51
After the large suspended matter and suspended matter are removed, they are stored in the landing well 52. The stored raw water is sent to the biological treatment facility 53 for biological treatment as a pretreatment for ordinary water purification treatment such as coagulation, precipitation, and filtration. And the coagulating sedimentation basin 54
After the flocs are removed by sedimentation in (1), the treated water is filtered in the filter basin 55 and the treated water is sent to the next step 56. The flocs precipitated in the coagulation sedimentation tank 54 are concentrated by the concentrating device 57 and then discharged.

【0003】[0003]

【発明が解決しようとする課題】上記した従来の浄水設
備では、次のような問題点がある。原水は、生物処理設
備53において生物処理が行われ、凝集沈殿池54でフ
ロックの沈殿除去を行った後、次の工程である濾過池5
5で濾過されるようになっている。したがって、生物処
理設備53と凝集沈殿池54と濾過池55とが、それぞ
れ別々に設置されており、特に、これらは浄水施設の中
でも夫々設置スペースを多くとるものであることから、
両者が占める面積の割合はかなり大きなものとなる。こ
のように、設備の設置面積によって処理能力が決まって
しまい、小スペースでは処理能力を大きくすることがで
きない。また、生物処理、沈殿処理の後に濾過処理を行
うため、処理時間がかかる。
The above-mentioned conventional water purification equipment has the following problems. The raw water is subjected to biological treatment in the biological treatment facility 53, and flocs are removed by sedimentation in the coagulation sedimentation basin 54, and the next step is the filtration basin 5
It is designed to be filtered at 5. Therefore, the biological treatment facility 53, the coagulation sedimentation basin 54, and the filtration basin 55 are separately installed, and in particular, these occupy a large installation space in each water purification facility,
The ratio of the area occupied by both parties will be quite large. Thus, the processing capacity is determined by the installation area of the equipment, and the processing capacity cannot be increased in a small space. Moreover, since the filtration process is performed after the biological treatment and the precipitation process, it takes a long time.

【0004】本発明は、従来技術の有する上記の問題点
を解決し、小スペース化が図れると共に、処理時間を短
縮できる浄水装置を提供することを目的とする。
SUMMARY OF THE INVENTION It is an object of the present invention to solve the above-mentioned problems of the prior art, to provide a water purifying apparatus which can reduce the space and can shorten the processing time.

【0005】[0005]

【課題を解決するための手段】上記の目的を達成するた
めに、本発明は、微生物を付着させた接触材に原水を接
触させて浄化を行う生物処理装置と、この生物処理され
た原水を濾過膜に透過させて固液分離を行い処理水を系
外に取り出す膜濾過装置とを、単一の処理槽内に配設し
たことを特徴とする浄水装置を構成した。また、本発明
は、微生物を付着させた接触材に原水を接触させて浄化
を行う生物処理装置と、この生物処理された原水を濾過
膜に透過させて固液分離を行い処理水を系外に取り出す
膜濾過装置と、前記生物処理装置および膜濾過装置の下
方に位置し、原水中に含まれている固形物および沈殿物
を分離する濃縮装置とを、単一の処理槽内に配設したこ
とを特徴とする浄水装置を構成した。
In order to achieve the above-mentioned object, the present invention provides a biological treatment apparatus for purifying by contacting raw water with a contact material having microorganisms attached thereto, and a raw water treated with this biological treatment. A water purifying device was constructed by arranging a membrane filtration device that permeates through a filtration membrane to perform solid-liquid separation and takes out treated water to the outside of the system in a single treatment tank. Further, the present invention is a biological treatment apparatus for purifying by contacting raw water with a contact material to which microorganisms are adhered, and this biologically treated raw water is permeated through a filtration membrane for solid-liquid separation and treated water outside the system. The membrane filtration device that is taken out to the above and the concentrating device that is located below the biological treatment device and the membrane filtration device and that separates solids and precipitates contained in raw water are provided in a single treatment tank. A water purification device characterized by the above was constructed.

【0006】[0006]

【作用】原水は、処理槽内において、生物処理装置と膜
濾過装置との間を循環しつつ浄化され、処理水は、系外
に取り出される。また、原水中に含まれている固形物お
よび沈殿物は、同一処理槽内の濃縮装置により分離され
て系外に排出される。
In the treatment tank, the raw water is purified while circulating between the biological treatment device and the membrane filtration device, and the treated water is taken out of the system. Further, the solid matter and the precipitate contained in the raw water are separated by the concentrating device in the same treatment tank and discharged out of the system.

【0007】[0007]

【実施例】以下に、本発明の実施例を図面について説明
する。図1は、本発明を実施した浄水装置の一例を示す
断面図である。図中、符号1は、生物処理装置および膜
濾過装置、更には濃縮装置をそれぞれ内部に収める処理
槽であって、望ましくは下部を狭めたホッパ形状に形成
される。処理槽1の内部には、その上部側に仕切板7を
隔てて生物処理装置2および膜濾過装置3を並設してお
り、処理されるべき原水10が処理槽1に導入される。
Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is a cross-sectional view showing an example of a water purification device embodying the present invention. In the figure, reference numeral 1 is a treatment tank for accommodating a biological treatment device, a membrane filtration device, and a concentrating device, and is preferably formed in a hopper shape with a narrowed lower part. Inside the treatment tank 1, a biological treatment device 2 and a membrane filtration device 3 are arranged side by side with a partition plate 7 on the upper side thereof, and raw water 10 to be treated is introduced into the treatment tank 1.

【0008】生物処理方式には、水中に固定したプラス
チックの小筒の集合体によるハニコーム方式(浸漬濾床
法),回転する円板による回転円板方式,粒状の濾材に
よる生物接触濾過方式等が従来知られており、いずれの
方式を用いてもよいが、本実施例では、生物処理装置2
として、図2に示す浸漬濾床法を採用したので、その具
体例について説明する。処理槽1内に、充填材21とし
て、塩化ビニルシートを蜂の巣状(均一な六角形)に成
型した小筒21aの集合体を浸している。充填材21に
は、その表面に生物膜が付着しており、図中下方から上
方に向け充填材21に原水を通過させ、生物膜と接触さ
せることにより、原水中のアンモニア性窒素,藻類,か
び臭,陰イオン界面活性剤,マンガン等を有効に除去し
得る。
The biological treatment method includes a Hanikomeu method (an immersion filter bed method) using an assembly of small plastic tubes fixed in water, a rotating disk method using a rotating disk, and a biological contact filtration method using a granular filter material. Although any known method may be used, in the present embodiment, the biological treatment device 2 is used.
As the above, the immersion filter bed method shown in FIG. 2 was adopted, and a specific example thereof will be described. An aggregate of small cylinders 21 a formed by molding a vinyl chloride sheet into a honeycomb shape (uniform hexagonal shape) as a filler 21 is immersed in the processing tank 1. A biofilm adheres to the surface of the packing material 21, and raw water is passed through the packing material 21 from the bottom to the top in the figure to bring it into contact with the biofilm, whereby ammonia nitrogen in the raw water, algae, Musty odor, anionic surfactant, manganese, etc. can be effectively removed.

【0009】生物処理装置2の下部側には、エアー噴出
管5を配設し、処理槽1外に設けたエアー供給源からエ
アー5aを連続的または間欠的に送給している。微生物
による有機物の酸化・分解反応や、アンモニア性窒素の
酸化には、溶存酸素の存在が不可欠である。したがっ
て、原水中の酸素が不足するおそれがある場合は、エア
ーを吹き込み、酸素を補給する必要がある。
An air jet pipe 5 is provided on the lower side of the biological treatment apparatus 2, and air 5a is continuously or intermittently fed from an air supply source provided outside the treatment tank 1. The presence of dissolved oxygen is essential for the oxidation / decomposition reaction of organic substances by microorganisms and the oxidation of ammonia nitrogen. Therefore, when there is a risk of lack of oxygen in the raw water, it is necessary to blow air to supplement oxygen.

【0010】また、エアー噴出管5から噴出するエアー
5aにより、原水は、処理槽1内を上昇し、図1の矢印
Cで示すように、膜濾過装置3側に流れ、再び生物処理
装置2側に還流する、いわゆる循環流を発生させる。し
たがって、生物膜と水の接触頻度を増加させ、処理効果
を高めることができる。また、エアー噴出管5から噴出
するエアー5aにより循環流を起こさせるので、循環用
ポンプを別途設ける必要がなく、エネルギーの有効利用
を図ることができる。肥厚した生物膜は、循環流により
生じる剪弾力により脱落し、同時に新しい微生物が増加
し、常に活性度の高い生物膜が保持される。
Further, the raw water rises in the treatment tank 1 by the air 5a ejected from the air ejection pipe 5, flows toward the membrane filtration device 3 side as shown by an arrow C in FIG. A so-called circulating flow is generated that returns to the side. Therefore, the contact frequency of the biofilm and water can be increased, and the treatment effect can be enhanced. Further, since the circulation flow is caused by the air 5a ejected from the air ejection pipe 5, it is not necessary to separately provide a circulation pump, and the energy can be effectively used. The thickened biofilm is shed by the shearing force generated by the circulation flow, and at the same time, new microorganisms are increased, and the biofilm having high activity is always retained.

【0011】次に、膜濾過装置3について説明する。本
実施例においては、膜濾過装置3として、図3に示す外
圧式のクロスフロー濾過装置を採用した。処理槽1内に
配設した中空糸膜モジュール31は、例えばセルロース
アセテートを良溶媒に溶解した後これに金属塩と添加溶
媒を加えたポリマー溶液を紡糸した多孔膜中空糸であっ
て、膜槽31aと中空部31bとから構成される。原水
10は、膜層31aの外側を、図中上方から下方に、膜
層31aに平行に流され、膜層31aをこれに直交する
方向(矢印方向)から透過する。このクロスフロー濾過
により、固液分離され、膜層31aの内側、つまり中空
部31bに透過された濾液である処理水20が、系外に
取り出されるものである。中空糸膜モジュール31の膜
層31aの外側には、固液分離された濁質8が付着して
いる。
Next, the membrane filtration device 3 will be described. In the present embodiment, as the membrane filtration device 3, the external pressure type cross flow filtration device shown in FIG. 3 was adopted. The hollow fiber membrane module 31 arranged in the treatment tank 1 is a porous membrane hollow fiber obtained by, for example, dissolving cellulose acetate in a good solvent and spinning a polymer solution obtained by adding a metal salt and an additional solvent to the good solvent. 31a and a hollow portion 31b. The raw water 10 is flown outside the membrane layer 31a from the upper side to the lower side in the drawing in parallel with the membrane layer 31a, and permeates the membrane layer 31a in a direction (arrow direction) orthogonal to the membrane layer 31a. By this cross-flow filtration, the treated water 20, which is a filtrate that has been solid-liquid separated and has been permeated to the inside of the membrane layer 31a, that is, the hollow portion 31b, is taken out of the system. On the outside of the membrane layer 31a of the hollow fiber membrane module 31, the suspended matter 8 that has been solid-liquid separated is attached.

【0012】膜濾過装置3の下部側には、エアー噴出管
6を配設し、処理槽1外に設けたエアー供給源からエア
ー6aを間欠的に送給することにより、前記膜層31a
の外側に付着した濁質8を除去する。処理槽1の下部に
溜まった沈殿物は、定期的に系外に排出される。
An air jetting pipe 6 is provided on the lower side of the membrane filtration device 3 and the air 6a is intermittently fed from an air supply source provided outside the processing tank 1 to thereby form the membrane layer 31a.
The suspended matter 8 adhering to the outside of the is removed. The precipitate accumulated in the lower part of the processing tank 1 is regularly discharged out of the system.

【0013】上記のように、生物処理装置2および膜濾
過装置3を単一の処理槽1内に収容したので、生物処
理,膜濾過の両装置をそれぞれ別々に設置するものに比
較して小スペース化を図ることができ、同時に、処理時
間を短縮することができる。
As described above, since the biological treatment device 2 and the membrane filtration device 3 are housed in the single treatment tank 1, the biological treatment device and the membrane filtration device are smaller than those separately installed. The space can be increased, and at the same time, the processing time can be shortened.

【0014】次に、図1を参照して、生物処理装置2と
膜濾過装置3の下方に位置させて濃縮装置4を配設した
例について説明する。濃縮装置4は、図4の(a)にそ
の具体例を示すように、鉛直方向に対して60度の傾斜
角度をもつ傾斜板41を所定の間隔で所要数並設した傾
斜板沈降装置や、図4の(b)のように、六角形状(円
形でもよい)の管42を鉛直方向に対して60度の傾斜
角度をもつように密接させて所要数配設した傾斜管沈降
装置が用いられ、原水中に含まれている固形物および沈
殿物を分離する。濃縮された沈殿物は、処理槽1の下部
から定期的に系外に排出される。
Next, an example in which the concentrating device 4 is arranged below the biological treatment device 2 and the membrane filtration device 3 will be described with reference to FIG. As shown in a specific example of FIG. 4A, the concentrating device 4 includes a slant plate settling device in which a required number of slant plates 41 having a slant angle of 60 degrees with respect to the vertical direction are juxtaposed at predetermined intervals. As shown in FIG. 4 (b), a slant pipe settling device is used in which a required number of hexagonal (or circular) pipes 42 are arranged in close contact with each other at an inclination angle of 60 degrees with respect to the vertical direction. To separate solids and precipitates contained in the raw water. The concentrated precipitate is regularly discharged from the lower part of the processing tank 1 to the outside of the system.

【0015】上記のように、生物処理装置2,膜濾過装
置3および濃縮装置4を単一の処理槽1内に収容した浄
水装置では、生物処理,膜濾過,濃縮の各装置をそれぞ
れ別々に設置するものに比較して小スペース化を図るこ
とができ、同時に、処理時間を短縮することができる。
As described above, in the water purification apparatus in which the biological treatment device 2, the membrane filtration device 3 and the concentrating device 4 are housed in the single treatment tank 1, the biological treatment device, the membrane filtration device and the concentrating device are separately provided. The space can be reduced as compared with the installed one, and at the same time, the processing time can be shortened.

【0016】[0016]

【発明の効果】以上説明したように、本発明の浄水装置
によれば、生物処理装置および膜濾過装置、更には濃縮
装置をそれぞれ単一の処理槽に収容し、処理槽内に原水
の循環流を起こし、生物処理および膜濾過を行い、濃縮
装置で濃縮する各処理を一工程で連続処理することがで
きるので、従来の装置のように各処理工程を個別に行う
ものに比較して、設置スペースを小さくすることがで
き、また、処理時間を大幅に短縮できる効果がある。
As described above, according to the water purification apparatus of the present invention, the biological treatment apparatus, the membrane filtration apparatus, and the concentrating apparatus are housed in a single treatment tank, and the raw water is circulated in the treatment tank. Flowing, performing biological treatment and membrane filtration, each process of concentrating with a concentrating device can be continuously processed in one step, so compared to a conventional device that performs each processing step individually, The installation space can be reduced, and the processing time can be significantly shortened.

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

【図1】本発明を実施した浄水装置の一例を示す断面図
である。
FIG. 1 is a cross-sectional view showing an example of a water purifier according to the present invention.

【図2】本発明の浄水装置に用いられる生物処理装置の
一例を示す斜視図である。
FIG. 2 is a perspective view showing an example of a biological treatment apparatus used in the water purification apparatus of the present invention.

【図3】本発明の浄水装置に用いられる膜濾過装置の一
例を示す斜視図である。
FIG. 3 is a perspective view showing an example of a membrane filtration device used in the water purification device of the present invention.

【図4】本発明の浄水装置に用いられる濃縮装置の一例
を示す斜視図である。
FIG. 4 is a perspective view showing an example of a concentrating device used in the water purifying device of the present invention.

【図5】従来の浄水装置の処理工程を示すフロー図であ
る。
FIG. 5 is a flow chart showing a treatment process of a conventional water purifier.

【符号の説明】[Explanation of symbols]

1 …処理槽 2 …生物処理装置 3 …膜濾過装置 4 …濃縮装置 5 …エアー噴出管 6 …エアー噴出管 10 …原水 1 ... Treatment tank 2 ... Biological treatment device 3 ... Membrane filtration device 4 ... Concentration device 5 ... Air jet pipe 6 ... Air jet pipe 10 ... Raw water

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 微生物を付着させた接触材に原水を接触
させて浄化を行う生物処理装置と、この生物処理された
原水を濾過膜に透過させて固液分離を行い処理水を系外
に取り出す膜濾過装置とを、単一の処理槽内に配設した
ことを特徴とする浄水装置。
1. A biological treatment apparatus for purifying by contacting raw water with a contact material to which microorganisms are adhered, and a biological treatment raw water which is permeated through a filtration membrane to perform solid-liquid separation to bring the treated water out of the system. A water purifier characterized in that a membrane filtration device to be taken out is arranged in a single treatment tank.
【請求項2】 微生物を付着させた接触材に原水を接触
させて浄化を行う生物処理装置と、この生物処理された
原水を濾過膜に透過させて固液分離を行い処理水を系外
に取り出す膜濾過装置と、前記生物処理装置および膜濾
過装置の下方に位置し、原水中に含まれている固形物お
よび沈殿物を分離する濃縮装置とを、単一の処理槽内に
配設したことを特徴とする浄水装置。
2. A biological treatment apparatus for purifying by contacting raw water with a contact material on which microorganisms are adhered, and a biological treatment raw water which is permeated through a filtration membrane to perform solid-liquid separation to bring the treated water out of the system. A membrane filtration device for taking out and a concentrating device located below the biological treatment device and the membrane filtration device for separating solids and precipitates contained in raw water were arranged in a single treatment tank. A water purification device characterized by that.
【請求項3】 前記生物処理装置は、水槽内に生物の付
着しやすい充填剤を浸漬し、この充填剤の表面に生物膜
を形成させ、原水を接触させて浄化する浸漬濾床装置で
ある請求項1または請求項2に記載の浄水装置。
3. The biological treatment apparatus is an immersion filter apparatus for immersing a filler to which organisms are likely to adhere in a water tank, forming a biological film on the surface of the filler, and contacting with raw water to purify it. The water purifier according to claim 1 or 2.
【請求項4】 前記膜濾過装置は、処理水を中空糸膜の
外側に膜に平行に流し、膜の内側に透過させ、固液分離
を行う外圧式クロスフロー濾過装置である請求項1また
は請求項2に記載の浄水装置。
4. The membrane filtration device is an external pressure type cross-flow filtration device which causes treated water to flow to the outside of the hollow fiber membrane in parallel with the membrane and permeate to the inside of the membrane for solid-liquid separation. The water purifier according to claim 2.
【請求項5】 前記生物処理装置に対しエアーを吹き込
み、原水中に酸素を補給するためのエアー噴出管を設け
てなる請求項1または請求項2に記載の浄水装置。
5. The water purifier according to claim 1 or 2, wherein air is blown into the biological treatment apparatus to provide an air jet pipe for supplying oxygen to the raw water.
【請求項6】 前記濃縮装置は、所定間隔で所要数配設
された傾斜板または密接させて所要数配設された傾斜管
である請求項2に記載の浄水装置。
6. The water purifier according to claim 2, wherein the concentrating device is an inclined plate provided in a required number at predetermined intervals or an inclined pipe provided in a required number in close contact with each other.
JP11790494A 1994-05-31 1994-05-31 Water purification equipment Expired - Fee Related JP3345732B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11790494A JP3345732B2 (en) 1994-05-31 1994-05-31 Water purification equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11790494A JP3345732B2 (en) 1994-05-31 1994-05-31 Water purification equipment

Publications (2)

Publication Number Publication Date
JPH07323295A true JPH07323295A (en) 1995-12-12
JP3345732B2 JP3345732B2 (en) 2002-11-18

Family

ID=14723079

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11790494A Expired - Fee Related JP3345732B2 (en) 1994-05-31 1994-05-31 Water purification equipment

Country Status (1)

Country Link
JP (1) JP3345732B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005279408A (en) * 2004-03-29 2005-10-13 Hanshin Water Supply Authority Media and membrane filtration combined filter equipment
WO2007066471A1 (en) * 2005-12-09 2007-06-14 Tsukishima Kikai Co., Ltd. Filtration unit
CN104874211A (en) * 2015-04-29 2015-09-02 南京梅山冶金发展有限公司 Anti-blocking method used for diameter-height-ratio thickener

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005279408A (en) * 2004-03-29 2005-10-13 Hanshin Water Supply Authority Media and membrane filtration combined filter equipment
JP4672993B2 (en) * 2004-03-29 2011-04-20 阪神水道企業団 Media and membrane filtration combined filtration equipment
WO2007066471A1 (en) * 2005-12-09 2007-06-14 Tsukishima Kikai Co., Ltd. Filtration unit
US8142655B2 (en) 2005-12-09 2012-03-27 Tsukishima Kikai Co., Ltd. Filtration unit
CN104874211A (en) * 2015-04-29 2015-09-02 南京梅山冶金发展有限公司 Anti-blocking method used for diameter-height-ratio thickener

Also Published As

Publication number Publication date
JP3345732B2 (en) 2002-11-18

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