JPH0639388A - Apparatus and method for circulation cleaning of water - Google Patents

Apparatus and method for circulation cleaning of water

Info

Publication number
JPH0639388A
JPH0639388A JP9598593A JP9598593A JPH0639388A JP H0639388 A JPH0639388 A JP H0639388A JP 9598593 A JP9598593 A JP 9598593A JP 9598593 A JP9598593 A JP 9598593A JP H0639388 A JPH0639388 A JP H0639388A
Authority
JP
Japan
Prior art keywords
water
filter medium
filter
activated carbon
filter cylinder
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
JP9598593A
Other languages
Japanese (ja)
Inventor
Masayoshi Ketayama
正吉 桁山
Hiroyoshi Miyahara
浩嘉 宮原
Junko Fukuda
純子 福田
Shingo Sato
信吾 佐藤
Shintarou Harite
伸太郎 播手
Emika Ogawa
恵美香 小川
Tamon Kimura
太門 木村
Takao Imasaka
卓男 今坂
Takao Teraoka
高生 寺岡
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.)
Toto Ltd
Original Assignee
Toto 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 Toto Ltd filed Critical Toto Ltd
Priority to JP9598593A priority Critical patent/JPH0639388A/en
Publication of JPH0639388A publication Critical patent/JPH0639388A/en
Pending 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

  • Biological Treatment Of Waste Water (AREA)
  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
  • Water Treatment By Sorption (AREA)
  • Bathtub Accessories (AREA)
  • Details Of Fluid Heaters (AREA)

Abstract

PURPOSE:To avoid wasting water by cleaning the hot water in a bathtub without discarding by returning it into the bathtub after heating. CONSTITUTION:Filter medium cartridges 21 are piled into three stages from top to bottom in a filter cylinder 5 and in each filter medium cartridge 21, a structural body 31 consisting of the filter medium is set. The structural body 31 has a plurality of penetrating holes 32 in a definite direction and these penetrating holes 32 are positioned so as to bring these penetrating holes in parallel (in the top to bottom direction) with the passing direction of hot water. The structural body 31 is obtd. by extrusion-molding of the filter material and as the filter material, those which have a large specific area such as activated carbon, boiled rice and 'BAKUHAN SEKI' or sanitary clay are used. When the activated carbon is used, as the specific area is larger in comparison with others, a filter apparatus being compact and having high performance is obtd.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は浴水槽内の水を浄化して
再び浴水槽内に戻す装置と方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus and method for purifying water in a bath water tank and returning it to the bath water tank again.

【0002】[0002]

【従来の技術】浴水槽内の汚れた水(湯)を浄化し、加
熱して再び浴水槽内に戻すようにした装置が特開昭62
−160116号に提案されている。この装置は浴水槽
内の水をパイプを介してポリウレタン等の濾過布を入れ
た濾過タンクに通して水中の夾雑物を捕捉し、夾雑物を
除去した水を加熱部で加熱した後に麦飯石等の活性石を
充填した活性槽を通してミネラル等の有効成分を水中に
溶解せしめ、この後オゾン殺菌して浴水槽内に戻すよう
にしている。
2. Description of the Related Art An apparatus for purifying dirty water (hot water) in a bath water tank, heating it, and returning it to the bath water tank again is disclosed in Japanese Unexamined Patent Publication No. Sho 62-62.
-160116. This device passes the water in the bath water tank through a pipe to a filtration tank containing a filter cloth such as polyurethane to trap impurities in the water, and the water from which the impurities have been removed is heated in the heating unit, then boiled stone, etc. The active ingredients such as minerals are dissolved in water through the active tank filled with the activated stones, and then ozone sterilization is performed to return them to the bath water tank.

【0003】一方、最近では24時間使用可能な浴槽シ
ステムが提案されている。このシステムは浴水槽内の水
を捨てることなく浄化し、加熱して浴水槽内に戻し、浴
水槽には洗い場で使用して減った分だけ補給し、水の無
駄使いを完全になくそうというものである。
On the other hand, recently, a bathtub system that can be used for 24 hours has been proposed. This system purifies the water in the bath water tank without throwing it away, heats it up and returns it to the bath water tank, and uses it at the washing place to replenish it by the amount that has been reduced to completely eliminate the waste of water. It is a thing.

【0004】[0004]

【発明が解決しようとする課題】上述したシステムに特
開昭62−160116号に提案された装置を適用する
と、継続性の面で問題が生じる。即ち、この装置は濾過
タンクでは夾雑物を捕捉するだけで、また活性槽内の活
性石は水中にミネラル等を放出することを主目的として
おり、水中の有機物を吸着したり分解するには量的に不
十分である。また麦飯石等の活性石を充填した活性槽で
水中の有機物を除去するには活性槽の容量を極めて大き
なものにしなければならない。
When the device proposed in Japanese Patent Laid-Open No. 62-160116 is applied to the above-mentioned system, a problem occurs in terms of continuity. That is, the main purpose of this device is to capture impurities in the filtration tank, and the main purpose of the activated stone in the active tank is to release minerals into the water. Is insufficient. Further, in order to remove organic matter in water in an active tank filled with activated stone such as barley stone, the capacity of the active tank must be extremely large.

【0005】そこで、麦飯石等の活性石の代りに特開平
3−69575号に示されるような、多孔質ハニカムを
タールピッチにドブ浸けして得られる構造体を濾過筒内
にセットすることが考えられるが、この構造体では循環
浄化運転の初期において有機物の除去が有効に行なえな
い。
Therefore, instead of an activated stone such as barley stone, a structure obtained by immersing a porous honeycomb in a tar pitch as shown in Japanese Patent Laid-Open No. 3-69575 can be set in a filter cylinder. It is conceivable that this structure cannot effectively remove organic matter in the early stage of the circulation purification operation.

【0006】[0006]

【課題を解決するための手段】上記課題を解決すべく本
願の第1発明は、プールや浴槽等の浴水槽内の水を浄化
する濾過筒内に、一定方向に複数の貫通孔を有する濾材
からなる構造体を、当該貫通孔が水の通過方向と平行に
なるように配置し、更に構造体の表面には有機物を分解
する微生物層を形成せしめた。また本願の第2発明は、
循環浄化運転の初期には濾過筒内の濾材表面に水中の有
機物を吸着せしめて物理的に除去し、一定の期間経過後
は濾材表面に形成された微生物層によって水中の有機物
を化学的に分解除去するようにした。
In order to solve the above problems, a first invention of the present application is a filter medium having a plurality of through holes in a certain direction in a filter cylinder for purifying water in a bath water tank such as a pool or a bath. The structure made of was arranged such that the through holes were parallel to the passage direction of water, and a microbial layer that decomposes organic substances was formed on the surface of the structure. The second invention of the present application is
At the beginning of the circulation purification operation, the organic substances in the water are adsorbed on the surface of the filter medium inside the filter to physically remove them, and after a certain period of time, the organic substances in the water are chemically decomposed by the microbial layer formed on the surface of the filter medium. I tried to remove it.

【0007】[0007]

【作用】ハニカム状等の構造体を活性炭等の比表面積の
大きな濾材自体で形成したので、濾過筒内での水の流れ
を阻害することなく、しかも循環浄化運転の開始直後か
ら有機物の除去が行なえる。
[Function] Since the honeycomb-like structure is formed by the filter medium itself having a large specific surface area such as activated carbon, it is possible to remove organic substances immediately after the start of the circulation purification operation without obstructing the flow of water in the filter cylinder. I can do it.

【0008】[0008]

【実施例】以下に本発明の実施例を添付図面に基づいて
説明する。ここで、図1は本発明に係る水の循環浄化装
置を適用したシステムの全体図、図2は循環浄化装置を
構成する濾過筒の縦断面図であり、循環浄化装置は浴槽
1の下部に循環ポンプ2を備えた循環ライン3の取水口
を接続し、浴水槽1の上部に循環ライン3の吐水口を接
続している。そして、循環ライン3の途中には上流側か
ら順にヘアキャッチャ4、濾過筒5、紫外線もしくはオ
ゾンまたはこれら両者を利用した殺菌装置6、加熱装置
7及びエジェクタ8を設けている。
Embodiments of the present invention will be described below with reference to the accompanying drawings. Here, FIG. 1 is an overall view of a system to which the water circulation purifying apparatus according to the present invention is applied, and FIG. 2 is a vertical cross-sectional view of a filter cylinder constituting the circulation purifying apparatus. The water intake of the circulation line 3 provided with the circulation pump 2 is connected, and the water discharge outlet of the circulation line 3 is connected to the upper part of the bath water tank 1. In the middle of the circulation line 3, a hair catcher 4, a filter cylinder 5, a sterilizer 6 using ultraviolet rays or ozone, or both of them, a heating device 7 and an ejector 8 are provided in this order from the upstream side.

【0009】濾過筒5の構造は縦断面図である図2に示
すように、円筒状ケース20内に濾材カートリッジ21
を上下に3段重ねて構成される。円筒状ケース20は上
端開口に蓋体22を載せた状態でナット部材23により
固定され、また円筒状ケース20の上部側面には水の入
口部24、底面には水の出口部25及び逆洗用の開口2
6、蓋体22にはガス抜き穴27をそれぞれ形成してい
る。
As shown in FIG. 2, which is a vertical cross-sectional view, the structure of the filter cylinder 5 includes a filter medium cartridge 21 in a cylindrical case 20.
It is configured by stacking three layers vertically. The cylindrical case 20 is fixed by a nut member 23 with the lid 22 placed on the upper end opening, and the water inlet 24 is provided on the upper side surface of the cylindrical case 20 and the water outlet 25 and backwash is provided on the bottom surface. Opening 2
6, the lid 22 is formed with a gas vent hole 27, respectively.

【0010】濾材カートリッジ21は図3に示すよう
に、バケツ状の収納ケース28の上端部の内径を下端部
の外形に略等しくして、上下に重ねた際にぐらつかない
ようにし、また収納ケース28の底面には多数の穴29
を開口させ、上縁部には把持部30を取り付け、内部に
は濾材からなる構造体31をセットしている。また構造
体31の貫通孔32の大きさは有機物を分解する微生物
(好気性菌、嫌気性菌等)が成育するのに適したものと
する。
As shown in FIG. 3, the filter medium cartridge 21 has an inner diameter at the upper end of a bucket-shaped storage case 28 that is substantially equal to the outer diameter at the lower end to prevent wobbling when stacked one above the other. Many holes 29 on the bottom of 28
Is opened, a grip 30 is attached to the upper edge, and a structure 31 made of a filter medium is set inside. The size of the through hole 32 of the structure 31 is set to be suitable for the growth of microorganisms (aerobic bacteria, anaerobic bacteria, etc.) that decompose organic substances.

【0011】構造体31は一定方向に複数の貫通孔32
を有し、この貫通孔32が水の通過方向と平行(上下方
向)になるように配置されている。また構造体31は濾
材カートリッジ21内でその上下端をストッパリング3
3で保持されている。このようにストッパリング33で
保持することで、構造体31外周と濾材カートリッジ2
1内周との間の流路断面積が大きな流路を水が通過しな
いようにしている。
The structure 31 has a plurality of through holes 32 in a certain direction.
The through holes 32 are arranged so as to be parallel to the water passage direction (vertical direction). In addition, the structure 31 has a stopper ring 3 at the upper and lower ends in the filter medium cartridge 21.
Holds at 3. By holding the stopper ring 33 in this way, the outer periphery of the structure 31 and the filter cartridge 2
Water is prevented from passing through a flow passage having a large flow passage cross-sectional area between the inner circumference and the inner circumference.

【0012】ところで、構造体31は濾材を押出し成形
することで得るが、濾材としては活性炭、麦飯石或いは
坏土などの比表面積(単位体積当りの表面積)の大きな
ものを用いる。活性炭を用いる場合には他のものに比べ
て微細孔も含めた比表面積が大きいため、コンパクトで
高性能の濾過装置が得られる。
By the way, the structure 31 is obtained by extruding a filter medium, and as the filter medium, activated carbon, barley stone, kneaded clay or the like having a large specific surface area (surface area per unit volume) is used. When activated carbon is used, it has a large specific surface area including fine pores as compared with other types, and thus a compact and high-performance filtration device can be obtained.

【0013】一方、杯土の場合には廃物利用が図れる。
即ち、衛生陶器やタイル等の陶磁器を加圧成形する際に
排出されるスラリーを集め、このスラリーに凝集剤を添
加して沈殿せしめ、沈澱物をフィルタプレスにかけて脱
水せしめて粘土とし、この粘土を押出し成形し、最終的
に焼成することで構造体31を得る。
On the other hand, in the case of clay, waste can be used.
That is, a slurry discharged during pressure molding of ceramics such as sanitary ware and tiles is collected, a coagulant is added to the slurry to cause precipitation, and the precipitate is dehydrated by applying a filter press to obtain clay. The structure 31 is obtained by extrusion molding and finally firing.

【0014】以上において、循環ポンプ2を駆動して循
環浄化運転を開始すると、濾過筒5の入口部24から入
った汚れた水は、各濾材カートリッジ21内の構造体3
1の貫通孔32内を流れ、出口部25から下流側の殺菌
装置6へ送られる。そして、循環浄化運転の初期段階に
おいては、水中の有機物は構造体31の表面に物理的に
吸着されて補足され、下流側には殆ど出て行かない。
In the above, when the circulation pump 2 is driven to start the circulation purification operation, the dirty water that has entered from the inlet portion 24 of the filter cylinder 5 is the structure 3 in each filter medium cartridge 21.
It flows through the through hole 32 of No. 1 and is sent from the outlet part 25 to the sterilization device 6 on the downstream side. Then, in the initial stage of the circulation purification operation, the organic matter in the water is physically adsorbed on the surface of the structure 31 and captured, and hardly exits to the downstream side.

【0015】そして、構造体31の表面に物理的に吸着
された有機物は好気性菌や嫌気性菌等の微生物の栄養源
となり、一定期間(約1週間)経過後には構造体31表
面には微生物層が形成される。
The organic matter physically adsorbed on the surface of the structure 31 serves as a nutrient source for microorganisms such as aerobic bacteria and anaerobic bacteria, and the surface of the structure 31 remains on the surface of the structure 31 after a certain period (about 1 week). A microbial layer is formed.

【0016】このように、構造体31表面には微生物層
が形成された後は、水中の有機物は主として微生物によ
って化学的に分解除去される。このように構造体31の
比表面積、濾過筒5の容量、水の処理量、構造体の材質
等を適切に設定することによって、運転の開始直後から
継続して効果的な有機物の除去が行なえる。
As described above, after the microbial layer is formed on the surface of the structure 31, organic matter in the water is chemically decomposed and removed mainly by the microorganism. In this way, by appropriately setting the specific surface area of the structure 31, the capacity of the filter cylinder 5, the amount of water to be treated, the material of the structure, etc., effective removal of organic substances can be performed immediately after the start of operation. It

【0017】また、構造体31(ハニカム)を活性炭に
て構成する場合には以下の条件が好ましいことが実験の
結果判明した。
Experiments have also revealed that the following conditions are preferable when the structure 31 (honeycomb) is made of activated carbon.

【0018】構造体中の活性炭の含有量は30重量%以
上65重量%以下が好ましい。即ち、構造体を製作する
場合には活性炭をバインダと混練して成形するが、この
時活性炭の割合が多ければ比表面積は大きくなって浄化
性能は向上するが、反面強度的に弱くなり端部に欠けや
ひびが生じ易くなる。これらを考慮すると、活性炭の含
有量は30重量%以上65重量%以下が好ましく、特に
製作時の成形性を考慮して35重量%以上45重量%以
下が好ましい。
The content of activated carbon in the structure is preferably 30% by weight or more and 65% by weight or less. That is, when manufacturing a structure, the activated carbon is kneaded and molded with a binder. At this time, if the ratio of the activated carbon is large, the specific surface area is increased and the purification performance is improved, but on the other hand, the strength is weakened and the end portion is weakened. Chips and cracks are likely to occur. Taking these into consideration, the content of the activated carbon is preferably 30% by weight or more and 65% by weight or less, and particularly preferably 35% by weight or more and 45% by weight or less in consideration of moldability during production.

【0019】構造体の流路径は0.6mm以上5.0m
m以下が好ましい。ここで、流路径とは、例えばセルの
形状が正方形の場合には一辺の長さであり、六角形の場
合には対角線の長さであり、円の場合には直径を表わ
す。このように流路径を0.6mm以上5.0mm以下
とするのは以下の理由による。即ち、構造体の流路表面
に付着する生物層はその厚みが厚くなると酸素が流路表
面まで透過できなくなって流路表面の生物が死滅して剥
離する。そして実験の結果、剥離が生じない最大厚さは
0.3mm程度であることが判明した。したがって、流
路表面に付着した生物層によって流路の目詰りを生じさ
せないためには流路径は0.6mm以上必要である。ま
た、流路径をあまり大きくすると単位体積当りの表面積
が小さくなって浄化性能が低下するので、流路径は5.
0mm以下とするのが好ましい。そして、実験結果から
流路径の最適範囲は1.0mm以上2.0mm以下であ
った。
The flow path diameter of the structure is from 0.6 mm to 5.0 m
m or less is preferable. Here, the flow path diameter is, for example, the length of one side in the case of a square cell shape, the length of a diagonal line in the case of a hexagon, and the diameter in the case of a circle. The reason why the flow path diameter is set to 0.6 mm or more and 5.0 mm or less is as follows. That is, when the thickness of the biological layer attached to the flow channel surface of the structure increases, oxygen cannot permeate to the flow channel surface, and organisms on the flow channel surface die and peel off. As a result of experiments, it was found that the maximum thickness at which peeling did not occur was about 0.3 mm. Therefore, in order to prevent the clogging of the channel due to the biological layer attached to the channel surface, the channel diameter must be 0.6 mm or more. Further, if the flow path diameter is made too large, the surface area per unit volume becomes small and the purification performance deteriorates.
It is preferably 0 mm or less. From the experimental results, the optimum range of the channel diameter was 1.0 mm or more and 2.0 mm or less.

【0020】また、構造体のセル壁の厚さは0.2mm
以上1.0mm以下とするのが好ましい。0.2mm以
上とするのは処理水の濾過通水時や洗浄水の通水時に加
わる機械的衝撃によってセル壁表面の欠けや脱落、割れ
等を生じないためであり、1.0mm以下とするのは、
これ以上厚くするとセルの本数が少なくなって単位体積
当りの表面積が小さくなることによる。
The thickness of the cell wall of the structure is 0.2 mm.
It is preferably not less than 1.0 mm. The thickness of 0.2 mm or more is used to prevent chipping, dropping, cracking, etc. of the cell wall surface due to mechanical shock applied during filtration of treated water or passage of washing water, and is set to 1.0 mm or less. Is
This is because if the thickness is made thicker than this, the number of cells decreases and the surface area per unit volume decreases.

【0021】[0021]

【発明の効果】以下の(表1)は循環浄化装置によって
49日間運転した後、浴水槽の水を総入替えし、その後
24時間経過した後に得たE260、TOC、色度及び
濁度の除去率と各濾材との関係を示すものであり、図5
は有機物(TOC)の経時変化、図6は有機物(TO
C)の除去と運転開始からの日数との関係を各濾材につ
いて実験した結果を示すものである。(表1)及び図5
からは濾材自体にてハニカム構造体を形成したものが、
他の濾材を用いた場合に比較して、TOC等の除去効果
において大幅に優れていることが分る。また(表1)及
び図6からは活性炭ハニカムとすることで運転の立上が
り特性に顕著な効果が現れることが分る。
The following (Table 1) shows the removal of E260, TOC, chromaticity, and turbidity obtained after 24 hours have elapsed after total replacement of the water in the bath water tank after operating for 49 days with a circulation purifier. FIG. 5 shows the relationship between the ratio and each filter medium.
Is the change of organic matter (TOC) with time, and Fig. 6 is the organic matter (TOC).
The result of having experimented about each filter medium about the relationship between the removal of C) and the number of days from the start of operation is shown. (Table 1) and FIG.
From the one that formed the honeycomb structure with the filter medium itself,
It can be seen that the effect of removing TOC and the like is significantly superior to the case of using other filter media. Further, it can be seen from (Table 1) and FIG. 6 that the activated carbon honeycomb has a remarkable effect on the startup characteristics of the operation.

【0022】[0022]

【表1】 [Table 1]

【0023】図7は、単位体積当りの表面積とKv値
(浴水槽水中のTOCの減少速度をTOC濃度の2乗で
割った値(K値)を体積当りの浄化性能に換算した値)
との関係を示すグラフであり、このグラフからも明らか
なように活性炭ハニカム(AC)とした場合にはKv値
が大巾に高くなり、高い浄化性能を有していることが分
る。
FIG. 7 shows the surface area per unit volume and the Kv value (the value obtained by dividing the reduction rate of TOC in the bath water by the square of the TOC concentration (K value) converted into the purification performance per volume).
It is a graph showing the relationship with, and as is clear from this graph, when the activated carbon honeycomb (AC) is used, the Kv value becomes extremely high, and it can be seen that it has a high purification performance.

【0024】以上に説明した如く本発明によれば、水の
循環浄化装置を構成する濾過筒内に、濾過材からなるハ
ニカム状等の構造体を所定の向きで配置したので、水の
流れを阻害することなく、しかも効率よく水中の有機物
を除去することができる。特に循環浄化運転の初期には
濾過筒内の濾材表面に水中の有機物を吸着せしめて除去
し、この後は濾材表面に形成した微生物層によって水中
の有機物を分解除去するようにしたので、運転の立上が
り性能が向上する。
As described above, according to the present invention, since the honeycomb-like structure made of the filtering material is arranged in a predetermined direction in the filter cylinder constituting the water circulation purifying apparatus, the flow of water is prevented. Organic substances in water can be efficiently removed without any inhibition. In particular, at the beginning of the circulation purification operation, the organic matter in the water is adsorbed and removed on the surface of the filter medium in the filter cylinder, and thereafter, the organic matter in the water is decomposed and removed by the microbial layer formed on the surface of the filter medium. The start-up performance is improved.

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

【図1】本発明に係る水の循環浄化装置を適用したシス
テムの全体図
FIG. 1 is an overall view of a system to which a water circulation purification device according to the present invention is applied.

【図2】本発明に係る水の循環浄化装置を構成する濾過
筒の縦断面図
FIG. 2 is a vertical cross-sectional view of a filter cylinder that constitutes the water circulation purification device according to the present invention.

【図3】濾過筒内にセットされる濾材カートリッジの断
面図
FIG. 3 is a cross-sectional view of a filter medium cartridge set in a filter cylinder.

【図4】濾材カートリッジ内に収納される構造体の斜視
FIG. 4 is a perspective view of a structure housed in a filter medium cartridge.

【図5】有機物の経時変化を示すグラフFIG. 5 is a graph showing changes over time in organic substances.

【図6】有機物の除去率と運転開始からの日数との関係
を示すグラフ
FIG. 6 is a graph showing the relationship between the removal rate of organic matter and the number of days from the start of operation.

【図7】単位体積当りの表面積とKv値との関係を示す
グラフ
FIG. 7 is a graph showing the relationship between the surface area per unit volume and the Kv value.

【符号の説明】[Explanation of symbols]

1…浴槽、5…濾過筒、21…濾材カートリッジ、31
…濾材からなる構造体、32…貫通孔。
1 ... Bathtub, 5 ... Filter cylinder, 21 ... Filter medium cartridge, 31
... A structure made of a filter material, 32 ... Through holes.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.5 識別記号 庁内整理番号 FI 技術表示箇所 C02F 1/68 3/10 Z 3/28 B F24H 9/00 W (72)発明者 福田 純子 福岡県北九州市小倉北区中島2丁目1番1 号 東陶機器株式会社内 (72)発明者 佐藤 信吾 福岡県北九州市小倉北区中島2丁目1番1 号 東陶機器株式会社内 (72)発明者 播手 伸太郎 福岡県北九州市小倉北区中島2丁目1番1 号 東陶機器株式会社内 (72)発明者 小川 恵美香 福岡県北九州市小倉北区中島2丁目1番1 号 東陶機器株式会社内 (72)発明者 木村 太門 福岡県北九州市小倉北区中島2丁目1番1 号 東陶機器株式会社内 (72)発明者 今坂 卓男 福岡県北九州市小倉北区中島2丁目1番1 号 東陶機器株式会社内 (72)発明者 寺岡 高生 福岡県北九州市小倉北区中島2丁目1番1 号 東陶機器株式会社内─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 5 Identification number Reference number within the agency FI Technical display location C02F 1/68 3/10 Z 3/28 B F24H 9/00 W (72) Inventor Junko Fukuda Fukuoka 2-1-1, Nakajima, Kokurakita-ku, Kitakyushu, Tochigi Co., Ltd. (72) Inventor Shingo Sato, 2-1-1, Nakajima, Kokurakita-ku, Kitakyushu, Kitakyushu, Fukuoka Prefecture (72) Invention Shintaro Harite, 2-1-1 Nakajima, Kokurakita-ku, Kitakyushu, Fukuoka Prefecture Totoki Equipment Co., Ltd. (72) Inventor Emika Ogawa 2-1-1, Nakajima, Kokurakita-ku, Kitakyushu, Kitakyushu, Fukuoka Prefecture In-house (72) Inventor Taimon Kimura 2-1-1 Nakajima, Kokurakita-ku, Kitakyushu, Fukuoka Prefecture Totoki Equipment Co., Ltd. (72) In-house Takuo Imasaka 2-1-1, Nakajima, Kokurakita-ku, Kitakyushu, Fukuoka Issue TOTO within Co., Ltd. (72) inventor Teraoka high school students Kitakyushu, Fukuoka Prefecture Kokura-ku Nakajima 2-chome No. 1 No. 1 TOTO within Co., Ltd.

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 浴水槽内の水を濾過筒内を通して再び浴
水槽内に戻すようにした水の循環浄化装置において、前
記濾過筒内には一定方向に複数の貫通孔を有する構造体
が当該貫通孔が水の通過方向と平行になるように配置さ
れ、この構造体は比表面積の大きな濾材を成形してなる
とともにその表面には有機物を分解する微生物層が形成
されていることを特徴とする水の循環浄化装置。
1. A water circulation purifying device in which water in a bath water tank is returned to the bath water tank through the inside of a filter cylinder, wherein a structure having a plurality of through holes in a certain direction is provided in the filter cylinder. The through holes are arranged so as to be parallel to the passage direction of water, and this structure is formed by molding a filter medium having a large specific surface area, and a microbial layer that decomposes organic substances is formed on the surface. Circulating water purification device.
【請求項2】 前記構造体は、陶磁器の製造工程で排出
されるスラリーを凝集沈澱させ、これを脱水して得られ
た粘土を成形し焼成して得ることを特徴とする請求項1
に記載の水の循環浄化装置。
2. The structure is obtained by coagulating and precipitating a slurry discharged in a ceramics manufacturing process, dehydrating the slurry, and molding and firing clay.
The water circulation purification device described in 1.
【請求項3】 前記構造体は活性炭から構成されること
を特徴とする請求項1に記載の水の循環浄化装置。
3. The water circulation purifier according to claim 1, wherein the structure is made of activated carbon.
【請求項4】 前記活性炭の含有量は30重量%以上6
5重量%以下であることを特徴とする請求項3に記載の
水の循環浄化装置。
4. The content of the activated carbon is 30% by weight or more and 6
The water circulation purifying apparatus according to claim 3, wherein the content is 5% by weight or less.
【請求項5】 浴水槽内の水を濾過筒内を通して再び浴
水槽内に戻すようにした水の循環浄化方法において、循
環浄化運転の初期には濾過筒内の濾材表面に水中の有機
物を吸着せしめて除去し、これと並行して濾材表面には
吸着した有機物を栄養源とする微生物の層を形成させ、
一定の期間経過後は濾材表面に形成した微生物層によっ
て水中の有機物を分解除去するようにしたことを特徴と
する水の循環浄化方法。
5. A method for circulating purification of water in which water in a bath tank is returned to the bath tank through the inside of the filter cylinder, wherein organic substances in water are adsorbed on the surface of the filter medium in the filter cylinder at the initial stage of the circulation cleaning operation. At the very least, in parallel with this, a layer of microorganisms with adsorbed organic matter as a nutrient source is formed on the surface of the filter medium,
A method for circulating and purifying water, characterized in that after a certain period of time, organic matter in water is decomposed and removed by a microbial layer formed on the surface of the filter medium.
JP9598593A 1992-04-28 1993-04-22 Apparatus and method for circulation cleaning of water Pending JPH0639388A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9598593A JPH0639388A (en) 1992-04-28 1993-04-22 Apparatus and method for circulation cleaning of water

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP4-136127 1992-04-28
JP13612792 1992-04-28
JP9598593A JPH0639388A (en) 1992-04-28 1993-04-22 Apparatus and method for circulation cleaning of water

Publications (1)

Publication Number Publication Date
JPH0639388A true JPH0639388A (en) 1994-02-15

Family

ID=26437140

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9598593A Pending JPH0639388A (en) 1992-04-28 1993-04-22 Apparatus and method for circulation cleaning of water

Country Status (1)

Country Link
JP (1) JPH0639388A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100799651B1 (en) * 2006-12-15 2008-01-30 여인봉 Apparatus for purifying sewer overflows and storm water
JP2015047523A (en) * 2013-08-30 2015-03-16 トクラス株式会社 Water purification cartridge and water purifier
US9969097B2 (en) 2014-09-29 2018-05-15 Yuan-Chi Hsu Cutting tool

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100799651B1 (en) * 2006-12-15 2008-01-30 여인봉 Apparatus for purifying sewer overflows and storm water
JP2015047523A (en) * 2013-08-30 2015-03-16 トクラス株式会社 Water purification cartridge and water purifier
CN104418402A (en) * 2013-08-30 2015-03-18 托客乐思股份有限公司 Water purifying cartridge and water purifier
US9969097B2 (en) 2014-09-29 2018-05-15 Yuan-Chi Hsu Cutting tool
USRE48804E1 (en) 2014-09-29 2021-11-02 Yuan-Chi Hsu Cutting tool

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