JPH08229591A - Method for circulative filtration of water and device therefor - Google Patents

Method for circulative filtration of water and device therefor

Info

Publication number
JPH08229591A
JPH08229591A JP7353499A JP35349995A JPH08229591A JP H08229591 A JPH08229591 A JP H08229591A JP 7353499 A JP7353499 A JP 7353499A JP 35349995 A JP35349995 A JP 35349995A JP H08229591 A JPH08229591 A JP H08229591A
Authority
JP
Japan
Prior art keywords
water
container
filter
tank
filled
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
JP7353499A
Other languages
Japanese (ja)
Other versions
JP3827100B2 (en
Inventor
Tsutomu Nishimura
勤 西村
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Individual
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Individual
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Priority to JP35349995A priority Critical patent/JP3827100B2/en
Publication of JPH08229591A publication Critical patent/JPH08229591A/en
Application granted granted Critical
Publication of JP3827100B2 publication Critical patent/JP3827100B2/en
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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

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  • Filtration Of Liquid (AREA)
  • Water Treatment By Sorption (AREA)
  • Biological Treatment Of Waste Water (AREA)
  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)

Abstract

PURPOSE: To effectively circulate and filter the withdrawn water or sucked water by passing the water through a filter device in which useful bacterium spore-contg. compds., silica sources and magnesium sources are packed in the case the waste materials included in the water in a tank is subjected to a cleaning treatment and is cyclically used. CONSTITUTION: The withdrawn water or sucked water is passed through the filter device in which the useful bacterium spore-contg. compds., silica sources and magnesium sources are packed, by which the water is circulated and filtered in the case the waste materials included in the water in the tank is subjected to the cleaning treatment and is cyclically used. A net container 5 is housed in a cylindrical container 4 provided with a withdrawn water introducing port 2 in its bottom and a filtered water delivery port 3 in its cap part, respectively, of, for example, a small-sized filter 1 to be built in a thermostatic purifying device, etc., for home baths. Calcite, zeolite, ceramic balls, granite porphyry and non-woven fabric filter are packed successively from below into the net container 5. Useful bacteria, etc., are implanted on the surfaces of the respective packing materials and the water is thereby filtered.

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、水の循環濾過方法及び
装置の改良に係わり、浴湯やプール、温水プールの水、
水棲動物の飼育槽の水などの中に含まれる老廃物質や排
泄物を長期間にわたり安定的且つ確実に清浄化処理する
新規な方法及び装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to improvement of a method and apparatus for circulating and filtering water, including bath water, pool water and hot water pool water.
The present invention relates to a novel method and apparatus for stably and reliably purifying waste substances and excrements contained in water of aquariums for aquatic animals over a long period of time.

【0002】[0002]

【従来の技術】公衆浴場やホテル・旅館等不特定多数が
入浴する浴槽の管理には、浴湯の入れ替え、浴槽の洗
浄、ストレーナーの清掃等が必須のこととして毎日行わ
れている。更に、入浴者がある度に浴槽からオーバーフ
ローする温湯は無為に放流され、その都度冷水を追加し
て適温になるまで加温される。これは、入浴者が持ち込
む皮膚老廃物その他の汚物により浴湯が汚濁汚染される
のを防止するために必要避くべからざることであるが、
これら入れ替えや放流による熱損失、労力消費は極めて
大きなものである。
2. Description of the Related Art In managing bathtubs in which public baths, hotels, and inns are open to the public, it is essential to replace bathtubs, wash bathtubs, clean strainers, etc. every day. Furthermore, every time a bather takes a bath, the hot water overflowing from the bath is discharged randomly, and cold water is added each time to warm the bath to an appropriate temperature. This must be avoided in order to prevent the bath water from becoming polluted and contaminated by skin waste and other contaminants brought in by the bather.
The heat loss and labor consumption due to replacement and discharge are extremely large.

【0003】そこで従来から、浴湯の汚染や汚濁を少し
でも低減させて、追加水の削減をしたり、或いは連続使
用する努力が続けられている。例えば、単純な濾材によ
る濾過、吸着材を濾材に用いた濾過、濾材に微生物を着
床させた生物濾過、更にはこれらとミネラル溶出濾材の
併用等が各種提案され、また実用化されている。
Therefore, conventionally, efforts have been made to reduce the contamination and pollution of the bath water as much as possible to reduce the additional water or continuously use the bath water. For example, various filtrations using a simple filter medium, filtrations using an adsorbent as a filter medium, biological filtrations in which microorganisms are implanted on the filter medium, and combinations of these and mineral elution filter mediums have been proposed and put into practical use.

【0004】更に、近来では家庭用の小型濾過器が市場
に出回り始めている。これには、ヒーターを内蔵して2
4時間入浴可能とするものや、バブルジエットと称して
濾過水を空気とともに噴射する機能を内蔵したものなど
各種のものが提供されている。
Further, recently, small-sized home filters have begun to appear on the market. It has a built-in heater for 2
Various things such as those that can be bathed for 4 hours and those that have a function called a bubble jet that has a function of spraying filtered water with air are provided.

【0005】尚、プールの水の場合も、浴湯と同様に人
間の老廃物その他の汚濁物質により汚染されるので、浴
湯と同様に水を循環濾過処理している。更に、次亜塩素
酸ソーダ等の塩素剤による殺菌が行われている。しか
し、殺菌剤の濃度が低いと殺菌効果が少なく、高くする
と目や皮膚を傷める欠点があり、濃度管理が難しいし、
排水を生物処理することも困難である。
Since water in the pool is also contaminated with human wastes and other pollutants like the bath water, the water is circulated and filtered as in the bath water. Furthermore, sterilization is performed with a chlorine agent such as sodium hypochlorite. However, if the concentration of the bactericide is low, the bactericidal effect is low.
Biological treatment of wastewater is also difficult.

【0006】また、鑑賞魚や水族館における水棲動物の
飼育槽の場合、魚等の排泄物や腐敗した残り餌によって
飼育槽内の水は常時汚染されている。そのため槽内の水
を循環し、その過程においてグラスウールによる濾過や
ゼオライト、活性炭による吸着濾過が行われている。し
かし、水中の窒素分などの栄養分を完全に除去すること
は難しく、富栄養化によって植物性プランクトンが繁殖
し、ガラス面等に付着する。そのために、残った餌の回
収や月に数度のガラス面の清掃などかなり面倒な手入れ
を必要とする。しかも塩素剤による殺菌はできないの
で、魚が一匹でも病原性の黴やバクテリアに侵される
と、またたくまに広がって水槽内の魚が全滅する現象も
良く見られるところである。
In addition, in the case of a breeding tank for ornamental fish and aquatic animals in an aquarium, the water in the breeding tank is constantly polluted by excretions such as fish and rotten residual food. Therefore, the water in the tank is circulated, and in the process, filtration by glass wool and adsorption filtration by zeolite and activated carbon are performed. However, it is difficult to completely remove nutrients such as nitrogen in water, and eutrophication causes phytoplankton to propagate and adhere to glass surfaces. For this reason, it requires considerable care such as collecting the remaining food and cleaning the glass surface several times a month. Moreover, since it is not possible to sterilize with a chlorine agent, it is often seen that even if one fish is infested with pathogenic fungi or bacteria, it will spread to the fish again and the fish in the aquarium will be wiped out.

【0007】[0007]

【発明が解決しようとする課題】以下、主として浴湯の
清浄化の場合を主として例にとって、本発明について説
明する。浴湯を処理する従来の濾材の多くは、業務用
(浴場用)、家庭用を問わず、雑菌類特に腐敗菌の繁殖
が生じたり、生物濾過や生物活性化ミネラルによる有効
化や温泉効果を主張しながら、何ら生物処理が行われず
単なる物理濾過に止まっていた。甚だしくは、生物膜処
理を標榜しながら有効な菌体の増殖が皆無なものや、悪
性菌と呼ばれる各種の腐敗菌を増殖させているものもの
もある。本発明者が濾材やフイルターに付着したバクテ
リアを培養実験をしたところ、濾材等に付着している栄
養分を分解するバクテリアの存在は多くの場合殆どみと
められなかった。逆に、大腸菌や、球菌、ブドウ状球菌
がかなりの例で存在していた。更に、生物処理を行ない
ながら紫外線殺菌(紫外線は、微生物組織を破壊するば
かりでなく酸素をオゾン化する)やオゾン殺菌を併用す
る全く矛盾した装置も市販されている。従って、これら
の器具や装置を用いた浴場の長期にわたる水質維持は困
難で、少なくとも1〜2月に1回程度は器具、配管、濾
材等の洗浄や解体洗浄(メンテナンス)が必要であり、
設置者にとって大きな負担となっていた。
The present invention will be described below, taking the case of cleaning bath water as an example. Many conventional filter media for treating bath water, whether for commercial use (bathhouse use) or household use, cause the propagation of various bacteria, especially spoilage bacteria, and have the effects of biofiltration and bioactivated minerals and hot spring effects. As he insisted, no biological treatment was carried out, and it was merely physical filtration. There are also those that advocate biofilm treatment and have no effective bacterial growth, or those that grow various spoilage bacteria called malignant bacteria. When the present inventor conducted a culturing experiment on bacteria adhering to the filter media and filters, the presence of bacteria decomposing nutrients adhering to the filter media etc. was hardly found in many cases. On the contrary, E. coli, cocci, and staphylococci were present in a considerable number of cases. Furthermore, a completely contradictory device is also commercially available that is used in combination with ultraviolet sterilization (ultraviolet rays not only destroy microbial tissue but also ozone-oxygenate) and ozone sterilization while performing biological treatment. Therefore, it is difficult to maintain long-term water quality in a bathhouse using these instruments and devices, and it is necessary to wash and dismantle the instruments, pipes, filter media, etc. at least once every 1-2 months.
It was a heavy burden on the installer.

【0008】他方機構上の問題として、浴槽内における
汚物やバクテリアの死骸の沈降を防ぎ、目視的に浴槽水
の清浄感を求めるところから過大な循環水量を求め、そ
の結果として濾過器での流速は過大なものとなり、濾材
接触時間、生物接触時間は極めて短いものであって、生
物処理効果を求められない器具、装置となっていた。ま
た、濾過水をジェット噴流(バブルジェット)として使
用する場合も多く、そのためにも大量の循環水量が要求
されている。しかも、この流量の確保は、多くの装置に
おいて濾材や生物膜と流湯が接触することなくパス(短
絡)によって行われているのが実情である。
On the other hand, as a mechanical problem, an excessive amount of circulating water is obtained from a place where filth and dead carcass of bacteria are prevented from settling in the bathtub and a feeling of cleanliness of the bath water is visually obtained, and as a result, a flow velocity in the filter is obtained. Was too large, and the contact time of the filter media and the contact time of the organisms were extremely short, resulting in an instrument or device that is not required to have the biological treatment effect. In addition, filtered water is often used as a jet jet (bubble jet), which requires a large amount of circulating water. Moreover, in many devices, the flow rate is ensured by a pass (short circuit) without contact between the filter medium or the biofilm and the running water in many devices.

【0009】上記したことは、以下に述べる現状調査か
らも明らかである。 (1)現状濾過筒内のバクテリア調査 現在実動中の生物濾過筒(浴湯用)内に充填されていた
セラミックボール、麦飯石、繊維フィルター等に付着し
ているバクテリアを調査するため、寒天培地にそれらの
一定量を植えて32℃で7日間培養してみた。その結
果、これらの濾材には1,700〜2,000個/mlもの
球菌、300〜500個/mlものブドウ状球菌が付着
していることが判明した。尚、老廃物(有機物)の分解
除去に有効な有用細菌(以下に詳述)は、麦飯石にのみ
僅か50個/ml程度付着しているに過ぎない。即ち、
これらには生物処理に関わるべき有用細菌が殆どいない
こと、そして大腸菌、球菌、ブドウ状球菌等が付着菌類
の主体を占めていることが判明した。かかる事態は甚だ
しい危険を内包しており、速やかに改善せねばならな
い。尚、有用細菌の優先化により、それらは消滅する
(以下に詳述)。従って、これらの濾材は物理的な濾過
を行っているに過ぎないことも明らかとなった。但し、
ミネラル溶出は行っている。
The above is clear from the current situation survey described below. (1) Survey of bacteria in the current filtration cylinder To investigate the bacteria adhering to the ceramic balls, barley stones, fiber filters, etc. filled in the biological filtration cylinder (for bath water) currently in operation, agar is used. A fixed amount of them was planted in a medium and cultured at 32 ° C. for 7 days. As a result, it was found that 1,700 to 2,000 cocci / ml and 300 to 500 staphylococci / coccus adhered to these filter media. Note that useful bacteria (detailed below) effective for decomposing and removing waste products (organic substances) are attached only to bakuhanishi in an amount of only about 50 / ml. That is,
It was found that there are few useful bacteria that should be involved in biological treatment, and that Escherichia coli, cocci, staphylococci, etc. occupy the majority of adherent fungi. Such a situation entails great danger and must be improved promptly. In addition, by prioritizing useful bacteria, they disappear (detailed below). Therefore, it became clear that these filter media only perform physical filtration. However,
Mineral elution is done.

【0010】(2)濾過筒内滞留時間 業務用濾過筒の場合、濾過筒内滞留時間は1分前後のも
のが多い。これは、濾過筒通過水量(濾過水量)が極め
て大きいことによる。例えば、図8に示すものはかなり
優れた浄化能力を示す装置であるが、それでも濾過筒内
滞留時間は1.2分程度である(濾過筒aの外筒容積60
0リットル、濾過筒通過水量500リットル/分)。し
かも、濾材bは大きな通過水量を確保するために、図8
のように3本の小さな濾材充填筒cに充填されたタイプ
のものが多い。従って濾材の抵抗を考えると、濾材充填
筒の表面接触、それも極めて短い時間の通過であり、生
物処理が充分に行われているとは考えられない。また家
庭用小型濾過器の場合には、濾過筒内容積が小さいうえ
に業務用同様濾過水をバブルジェットにすることが多い
ため、濾過筒内滞留時間は極めて短く数十秒程度であ
る。従って、業務用同様或いはそれ以上に生物処理は困
難である。
(2) Residence time in filtration cylinder In the case of a commercial filtration cylinder, the retention time in the filtration cylinder is often around 1 minute. This is because the amount of water passing through the filter cylinder (the amount of filtered water) is extremely large. For example, although the device shown in FIG. 8 is a device having a considerably excellent purification capacity, the residence time in the filtration cylinder is still about 1.2 minutes (the outer cylinder volume 60 of the filtration cylinder a).
(0 liter, 500 liters / min passing through the filter cylinder). Moreover, in order to secure a large amount of passing water, the filter medium b is
There are many types in which the three small filter medium filling cylinders c are filled. Therefore, considering the resistance of the filter medium, the surface contact of the filter medium-filled cylinder and the passage of the filter medium for a very short time are not considered to be sufficient for biological treatment. Further, in the case of a small-sized filter for home use, since the volume inside the filter cylinder is small and the filtered water is often used as a bubble jet as in the case of commercial use, the residence time inside the filter cylinder is extremely short, about several tens of seconds. Therefore, biological treatment is more difficult than for commercial use.

【0011】[0011]

【課題を解決するための手段】そこで本発明者は、まず
濾材について研究を進めた。得られた結論として、浴湯
の理想的な濾材、濾過システムは以下の要件を満たすも
のである。 (1)有用細菌胞子を高濃度に濾材中に内包している濾
材(有用細菌胞子含有物)を用いること。 (2)濾過筒内で、生物処理を行なうのに必要な菌体
(有用細菌)の増殖や再胞子化に必要なミネラル(シリ
カ及びマグネシウム)の供給を行ない、菌体の培養と維
持を行なう濾材を用いること。更に望ましくは、 (3)短い時間で汚染物質を吸着し、以後の生物栄養を
供給する濾材を併用すること。 (4)ミネラルを供給したり菌体を着床して増殖させる
他の接触濾材を併用すること。 (5)更に、着床より離脱したバクテリアの流失を防止
するために、最終段階でフイルターを使用するとよい。
Therefore, the present inventor first proceeded with research on filter media. In conclusion, the ideal filter material and filtration system for bath water satisfy the following requirements. (1) Use of a filter medium (useful bacterial spores-containing material) containing useful bacterial spores in a high concentration in the filter medium. (2) In the filtration cylinder, the growth of bacterial cells (useful bacteria) necessary for biological treatment and the supply of minerals (silica and magnesium) necessary for re-spore formation are carried out to culture and maintain the bacterial cells. Use filter media. More preferably, (3) a filter medium that adsorbs pollutants in a short time and supplies biological nutrients thereafter is also used. (4) To use together with other contact filter media that supplies minerals or implants and grows bacterial cells. (5) Further, a filter may be used at the final stage in order to prevent the washout of the bacteria detached from the implantation.

【0012】尚、本発明で言う有用細菌とは、芽胞(胞
子)を形成する好気性ないし通性嫌気性のグラム陽性桿
菌(バチルス属)に属する、澱粉分解、蛋白質分解、脂
肪分解に優れた能力を示す複数種のバクテリアのことで
ある。
The useful bacterium referred to in the present invention is a spore-forming aerobic or facultative anaerobic gram-positive bacillus (bacillus genus), which is excellent in starch degradation, protein degradation and lipolysis. It refers to multiple species of bacteria that exhibit potency.

【0013】これらのバクテリアは、以下のようにして
得られた。枯草菌を代表とするバチルス属のバクテリア
は、土壌、枯れ草など自然界に広く分布しており、一般
の屎尿処理場の槽内にも低濃度ではあるが存在してい
る。そこで、ある既設の屎尿処理場の消化槽において、
硅酸イオン(SiO2 :シリカ成分)及びマグネシウム
イオンの存在下で長期間(少なくとも6ケ月以上)にわ
たって好気処理し、生成した汚泥を抜き出し、平面寒天
培地にこの汚泥を植菌し、32℃で6時間培養して菌株
を単離した。得られた菌株は30余種であったが、その
90%以上がバチルス属であり、そのうち澱粉を分解資
化するもの、蛋白質(カゼイン)を分解資化するもの、
その両者を分解資化するものがほぼ等分含まれていた。
脂肪は殆どの菌株が分解資化した。また、アンモニアは
半数以上の菌株が、硫化水素は全ての菌株が分解資化す
る能力を有している。
These bacteria were obtained as follows. Bacteria belonging to the genus Bacillus represented by Bacillus subtilis are widely distributed in nature such as soil and dead grass, and they are present in the tank of a general human waste treatment plant, although the concentration is low. Therefore, in a digestive tank at an existing human waste treatment plant,
Aerobic treatment was carried out for a long time (at least 6 months or more) in the presence of silicate ion (SiO 2 : silica component) and magnesium ion, the sludge produced was extracted, and the sludge was inoculated on a flat agar medium at 32 ° C. The strain was isolated by culturing for 6 hours. The obtained strains were more than 30 species, 90% or more of which belong to the genus Bacillus, of which those that decompose and assimilate starch, those that decompose and assimilate proteins (casein),
The materials that decompose and assimilate both of them were included in almost equal parts.
Most strains decomposed and assimilated fat. Further, more than half of the strains of ammonia have the ability to decompose and assimilate hydrogen sulfide by all strains.

【0014】更に、バクテリアの分解資化能力を増大さ
せるために、以下の操作を行なった。まず、上記と同じ
汚泥(MLSS5,400)の4リットルを5リットル瓶
に採り、クリーンベンチ内で曝気を続ける。これに、生
物試験用のジャガイモ澱粉、クックドミート、牛肉エキ
ス、コーン油を1:1:1:1の割合で、初期は少量を
加え、糸状体を形成しない範囲で徐々に増量し、70日
経過後より総量40gとなるように添加量を増して与え
つづけた。尚、モノマーシリカ20mg、マグネシウム
イオン20mgを微酸性水溶液として毎日添加し、更に
蒸発水分の補充は適時蒸留水を添加して調整した。この
操作を6ケ月続けたのち、養分の投入を停止し更に曝気
を5日続けて(胞子化のため)から汚泥を抜き出し、同
様にして菌株毎の澱粉分解、蛋白質分解、脂肪分解挙動
を調査した。
Further, the following operations were carried out in order to increase the ability of the bacteria to decompose and assimilate. First, 4 liters of the same sludge (MLSS5,400) as described above is put in a 5 liter bottle, and aeration is continued in a clean bench. To this, potato starch for biological tests, cooked meat, beef extract, and corn oil were added at a ratio of 1: 1: 1: 1 in a small amount at the beginning, and gradually increased until a filament was not formed. After 70 days, The addition amount was increased so that the total amount became 40 g, and the addition was continued. Incidentally, 20 mg of monomer silica and 20 mg of magnesium ion were added every day as a slightly acidic aqueous solution, and further evaporation water was supplemented by adding distilled water at appropriate times. After this operation was continued for 6 months, the feeding of nutrients was stopped, and aeration was continued for 5 days (for sporulation), sludge was extracted, and similarly, the starch decomposition, protein decomposition, and lipolysis behavior of each strain was investigated. did.

【0015】その結果、As a result,

【表1】 に示すように、澱粉と蛋白質の両者を分解する菌株が増
え、また分解能もそれぞれ増大しており、菌体の太さに
も変化が見られ。即ち、菌の馴化或いは変成が生じたも
のと思われる。尚、菌体の太さが1.2μmを境に、それ
よりも太い菌体は澱粉を分解し、それよりも細い菌体は
蛋白質を分解することが判る。また、1〜15の菌株(バ
チルス属)が全体の90%以上を占有しており、これらが
有機物分解に関与している。グラム陰性桿菌や酵母に
は、直接栄養分解を行なう力がないことも明らかとなっ
た。このように、適正範囲内で最大の負荷を細菌に与え
ることにより、細菌機能が向上したり、複合機能を有す
る菌株が増し、変成を示すことが明らかとなった。これ
らの変成菌は有機物分解能が高く、高負荷の処理に適し
た機能をもつものである。本発明では、上記汚泥由来の
菌株、更に分解資化能力増強タイプの菌株の何れも使用
できるが、後者の方が処理能力は優れている。更にこれ
らの汚泥を脱水後、共存する原生動物の死骸を分解資化
するとともにバチルス属バクテリアをさらに増殖させる
ため、発酵処理を加えて完熟させることにより、胞子濃
度を1010個/mlから1011〜1012個/mlにまで
高濃度化することができる。
[Table 1] As shown in, the number of strains that decompose both starch and protein is increasing, and the resolution is also increasing. That is, it seems that the acclimation or denaturation of the bacterium has occurred. It should be noted that, when the thickness of the bacterial cells is 1.2 μm as a boundary, the bacterial cells thicker than that decompose starch and the bacterial cells thinner than that decompose protein. Further, 1 to 15 strains (genus Bacillus) occupy 90% or more of the whole, and these are involved in the decomposition of organic matter. It was also revealed that Gram-negative bacilli and yeasts do not have the ability to directly decompose nutrients. Thus, it was clarified that by giving the maximum load to the bacteria within the proper range, the bacterial function was improved or the number of strains having a combined function was increased to show the metamorphosis. These metamorphic bacteria have a high ability to decompose organic substances and have a function suitable for high-load treatment. In the present invention, any of the above-mentioned sludge-derived strains and strains of enhanced digestion and assimilation capacity can be used, but the latter has better treatment capacity. Furthermore, after dehydrating these sludges, in order to decompose and assimilate the carcasses of the coexisting protozoa and to further grow the bacteria of the genus Bacillus, fermentation treatment is added to complete maturation, and the spore concentration is from 10 10 cells / ml to 10 11 The concentration can be increased up to 10 12 cells / ml.

【表1】[Table 1]

【0016】バチルス属のバクテリアは、発芽、増殖す
るために栄養分とともに酸素、シリカ、及びマグネシウ
ムを必要とする。これらの条件が満たされれば、貪欲に
栄養分を消費して優先化し、他のバクテリア例えば球菌
やブドウ状球菌を消滅させる能力を有している。また、
貧栄養状態になれば胞子化し、栄養分の供給で発芽す
る。シリカは、有用細菌の細胞液や細胞膜、胞子膜を構
成する重要な物質であり、これが不足すると有用細菌の
増殖ができなくなる。またマグネシウムは、この有用細
菌の世代時間(増殖サイクル)を極端に短縮させる作用
を有している。このシリカ及びマグネシウム働きは、本
発明者らが初めて見いだしたものである。また一定範囲
の温度にコントロールすると、増殖速度が早くなる。好
ましい温度の上限は有用細菌の種類により異なり、62
℃或いは45℃程度であるが、浴湯の場合40〜42℃
であるので、特に問題はない。また酸素は浴槽内でバブ
ルジェットにより供給される程度で十分である。但し、
本発明の場合濾過筒内滞留時間を長くするために濾過筒
通過水量を少なくするので、バブルジェットは別系統に
することが好ましい。
Bacteria of the genus Bacillus require oxygen, silica, and magnesium along with nutrients for germination and growth. If these conditions are satisfied, it has the ability to greedily consume and prioritize nutrients to eliminate other bacteria such as cocci and staphylococci. Also,
When it becomes oligotrophic, it sporulates and germinates by supplying nutrients. Silica is an important substance that constitutes the cell fluid, cell membrane, and spore membrane of useful bacteria, and if this is insufficient, the useful bacteria cannot grow. Further, magnesium has an action of extremely shortening the generation time (growth cycle) of this useful bacterium. This function of silica and magnesium was first discovered by the present inventors. Further, if the temperature is controlled within a certain range, the growth rate becomes faster. The preferable upper limit of the temperature varies depending on the type of useful bacteria.
℃ or 45 ℃, but in the case of bath water 40-42 ℃
Therefore, there is no particular problem. Further, it is sufficient that oxygen is supplied by a bubble jet in the bath. However,
In the case of the present invention, since the amount of water passing through the filter cylinder is reduced in order to prolong the residence time in the filter cylinder, it is preferable to use a separate system for the bubble jet.

【0017】そして、各種濾材について検討した結果、
上記(1)と(2)については、方形石の破砕品または
該粉末の造粒品を使用することが最も好ましいと結論さ
れた。即ち、方形石はクリストバライト形シリカを主成
分(90%以上)とし、500Å〜数μmの空隙を全体
に有する極めて高度な多孔質形態を持ち、嵩比重1.1〜
1.6(採取地により変動)のポーラスな鉱物である。し
かも、その空隙には無数の有用細菌胞子を天然的に内包
しており(この現象は本発明者により初めて確認され
た)、水と加温により胞子が活性化されて発芽直前の状
態とすることができる。更に栄養分(人間の老廃物等)
が供給されると、たちまち発芽して栄養分を分解し、そ
の胞子化に必要なミネラル存在下で、貧栄養状態の出現
とともに再び胞子化する性質を有している。従って、浴
湯の浄化処理には欠かせない自然界で得られる生物濾材
である。但し、方形石が高温に晒されると、内包してい
る有用細菌の胞子が死滅する(121℃の恒温箱内では
死滅しなかった)。従って、破砕品の形で使用するか、
加工する場合には121℃、好ましくは100℃程度以
下の低温で処理する必要がある。尚、方形石の破砕品に
有用細菌胞子を植菌したり、方形石の粉末に有用細菌胞
子やこれを高濃度に含有する汚泥を混合して成型したも
のも、濾材として使用できる。
Then, as a result of examining various filter media,
Regarding the above (1) and (2), it was concluded that it is most preferable to use a crushed product of square stone or a granulated product of the powder. In other words, square stone has cristobalite-type silica as the main component (90% or more), has an extremely highly porous morphology with voids of 500 Å to several μm throughout, and has a bulk specific gravity of 1.1 to 1.
It is a porous mineral of 1.6 (varies depending on the sampling site). Moreover, innumerable useful bacterial spores are naturally included in the void (this phenomenon was first confirmed by the present inventor), and the spores are activated by water and heating to bring them into a state just before germination. be able to. Further nutrients (human waste, etc.)
When it is supplied, it immediately germinates and decomposes nutrients, and in the presence of minerals necessary for its sporulation, it has the property of sporulation again with the appearance of an oligotrophic state. Therefore, it is a biological filter material obtained in the natural world which is indispensable for the purification treatment of bath water. However, when the square stone is exposed to a high temperature, the spores of the useful bacteria contained therein are killed (it was not killed in the 121 ° C constant temperature box). Therefore, use it in the form of crushed products,
When processing, it is necessary to process at a low temperature of 121 ° C., preferably about 100 ° C. or less. In addition, a crushed product of square stones may be inoculated with useful bacterial spores, or a powder of square stones may be mixed with useful bacterial spores or sludge containing a high concentration thereof and molded to form a filter medium.

【0018】或いは、(1)として有用細菌の胞子を多
数内包させた繊維製品を用いてもよい。これは例えば、
有用細菌を液体培地で培養してその胞子を単離したのち
更に希液体培地で培養して胞子化した菌体を、糸、紐、
ロープ等の繊維製品(好ましくは化学繊維)を繰り返し
浸漬−引き上げ(水切り)して繊維空間に植え付けたの
ち、乾燥して得る。繊維としては、からみの多い繊維、
例えばアクリル繊維等が適している。
Alternatively, as (1), a fiber product containing a large number of useful bacterial spores may be used. This is for example
A useful bacterium is cultured in a liquid medium to isolate its spores, and then further cultured in a dilute liquid medium to sporulate the microbial cells into a thread, a string,
A fiber product (preferably a chemical fiber) such as a rope is repeatedly dipped and pulled up (drained) to be planted in a fiber space, and then dried. As fibers, there are many entangled fibers,
For example, acrylic fiber is suitable.

【0019】更に(1)として、シリカとマグネシウム
に富んだ排水処理場等で本発明と同様に有用細菌を増殖
処理して得られる有用細菌高濃度胞子汚泥(活性汚泥:
有用細菌の胞子を少なくとも106 〜109 個/ml程度
以上含んでいるものが好ましい)を、乾燥或いは発酵乾
燥して成形したものも使用可能である。繊維製品や汚泥
成形品の場合には、有用細菌の増殖や再胞子化に必要な
ミネラルが欠如している。この場合には、方形石や麦飯
石その他ミネラルを含む鉱物を併用するとよい。尚、マ
グネシウム分に富むドロマイトを使用することも好まし
い。
Further, as (1), a useful bacterial high-concentration spore sludge (active sludge: obtained by multiplying useful bacteria in a wastewater treatment plant rich in silica and magnesium in the same manner as in the present invention.
Those containing at least about 10 6 to 10 9 spores of a useful bacterium are preferable) and those formed by drying or fermentation drying can also be used. Textiles and sludge moldings lack the minerals needed for the growth and re-sporification of useful bacteria. In this case, square stone, barley stone, and other minerals containing minerals may be used together. It is also preferable to use dolomite rich in magnesium.

【0020】次に(3)については、浴湯中の汚染物質
の内、特に大きなウエートを占めるアンモニア性窒素の
吸着力が強いゼオライト鉱物を用いる。特に、高品位の
天然ゼオライト粉末を使用した造粒品が有効であるが、
通常のゼオライト粉末の造粒品や破砕品も使用可能であ
る。また(4)については、麦飯石や適度のミネラル溶
出をする安山岩系鉱物や火山性軽石等が用いられる。こ
れらは、従来浴用濾材とて用いられてきたもので、いず
れも容易に入手することが可能であり、バクテリアの着
床になるとともにミネラル(シリカ、マグネシウム、カ
ルシウム、ナトリウム、鉄その他)を溶出する働きをす
る。更に(5)としては、ポリエステル綿やアクリル綿
などの合成繊維製綿状のフィルターを用いるとよい。分
厚い不織布状のものも使用できる。セルロース系のもの
は分解される可能性があるので、椰子繊維等強靱なもの
を除いては好ましくない。尚、本発明の濾材としては上
記(1)及び(2)の要件が充足されれば、それだけで
かなりの効果を発揮する。ただ、これにゼオライトを併
用すれば、濾過筒内滞留時間が多少短くても浴湯中のア
ンモニア系老廃物の除去がより効果的に行なえる。高品
位の天然ゼオライト粉末(粘土分を低減除去したもの)
の造粒品は吸着速度や吸着容量が大きいため、その効果
は更に増大する。これに更に麦飯石その他の濾材を併用
ば、濾過清浄化工程が長くなり、より優れた効果を発揮
する。
In regard to (3), among the pollutants in the bath water, a zeolite mineral having a strong adsorbing power for ammoniacal nitrogen, which occupies a particularly large weight, is used. In particular, granulated products using high-quality natural zeolite powder are effective,
Ordinary zeolite powder granulated products or crushed products can also be used. As for (4), barley stone, andesite minerals and volcanic pumice, which elute moderate minerals, are used. These are conventionally used as bath filter media, and all of them can be easily obtained, and they become the implantation of bacteria and elute minerals (silica, magnesium, calcium, sodium, iron, etc.). Work. Further, as (5), it is preferable to use a cotton-like filter made of synthetic fiber such as polyester cotton or acrylic cotton. Thick non-woven fabric can also be used. Cellulosic materials are likely to be decomposed, so it is not preferable except for strong materials such as palm fibers. As long as the requirements (1) and (2) are satisfied, the filter material of the present invention exhibits a considerable effect by itself. However, if zeolite is used in combination with this, the ammonia-based waste products in the bath water can be more effectively removed even if the residence time in the filtration cylinder is somewhat short. High quality natural zeolite powder (reduced and removed clay content)
Since the granulated product of No. 2 has a large adsorption speed and adsorption capacity, its effect is further enhanced. If boiled stone or other filter material is used in combination with this, the filter cleaning step becomes longer and more excellent effect is exhibited.

【0021】(実験例) 1. 方形石中の有用細菌の確認 a 方形石を乳鉢で微粉砕し、その1gを液体培地(グ
ルコース0.8%、ニュートロエレトクロース0.8%、食
塩0.6%)10mlをシャーレに取り、その上に散布し
たのち、32℃で7日間培養した。その結果、無数に近
い有用細菌の発芽と胞子化コロニーの出現を確認した。 b 更に、aより有用細菌胞子を単離し、1/10に希
釈した液体培地300mlに移植し、50mlの散気を
行いながら32℃で3日間培養して増殖させたところ、
この培地溶液中に極めて高い有用細菌のコロニーが出現
し、有用細菌濃度=5×109 個/mlとなった。計測
は、バイオ−プロッターにより行なった。 c 方形石表面を、電子顕微鏡走査像により観察したと
ころ、その空隙に大量の有用細菌胞子の存在を確認し
た。
(Experimental example) 1. Confirmation of useful bacteria in square stone a Square stone was finely crushed in a mortar and 1 g of the fine stone was pulverized in a liquid medium (glucose 0.8%, Neutroeletochrose 0.8%, salt 0) (6%) was placed in a petri dish, sprayed on the dish, and then cultured at 32 ° C. for 7 days. As a result, it was confirmed that a myriad of useful bacteria germinated and sporulated colonies appeared. b Further, useful bacterial spores were isolated from a, transplanted to 300 ml of a liquid medium diluted to 1/10, and cultured and grown at 32 ° C. for 3 days while aerating 50 ml,
Very high useful bacteria colonies appeared in this medium solution, and the concentration of useful bacteria was 5 × 10 9 cells / ml. The measurement was performed by a bio-plotter. c The surface of the square stone was observed by an electron microscope scanning image, and it was confirmed that a large amount of useful bacterial spores were present in the void.

【0022】2. 繊維製品中の有用細菌の確認 前述した有用細菌の胞子を繊維空間に植え付けたアクリ
ル製紐を、ステンレスドラム(60mmφ)の外周に巻
付ける。1リットルビーカーに純水を1リットル採り3
2℃に加温しながらこのステンレスドラムを浸漬し、1
00ml/分×60分の散気を行い、顕微鏡観察したとこ
ろ、各有用細菌胞子は発芽寸前(桿菌を内包)の状態と
なっていた(活性化)。次いで、先の希釈液体培地に浸
漬し、シリカ溶液1ml(シリカ10mg、MgO3mg
相当)を加え、同様の散気と加温を行ったところ、一斉
に発芽増殖し、1日後には栄養分解が完了して高濃度胞
子コロニーとなった。(稀液体培地はグルコース0.2
%、ニュートロエレトクロース0.2%、食塩0.1%を用
いた)。よって、本方法によっても、有用細菌の種菌を
供与できることも明らかとなった。尚、一般に麦飯石、
安山岩、セラミックボール(多孔質)等には、有用細菌
胞子を含んでおらず、浴湯中に進入してくる有用細菌が
余りにも少ないため、既に述べてきた有用細菌の高濃度
化は生起せず、種菌、特に高濃度化された胞子を種とし
て与えない限り、浴湯の生物処理は行えないと言える。
2. Confirmation of Useful Bacteria in Textile Products An acrylic cord in which the spores of the useable bacteria described above are planted in the fiber space is wound around the outer circumference of a stainless drum (60 mmφ). Take 1 liter of pure water in a 1 liter beaker 3
Immerse this stainless steel drum while heating to 2 ° C and
When air was diffused at 00 ml / min × 60 min and observed under a microscope, each useful bacterial spore was in a state of being on the verge of germination (including bacilli) (activation). Then, it is immersed in the diluted liquid medium described above, and 1 ml of silica solution (10 mg of silica, 3 mg of MgO).
(Equivalent) was added and the same aeration and heating were carried out. As a result, germination and growth occurred all at once, and one day later, nutrient decomposition was completed and high concentration spore colonies were formed. (Rare liquid medium is glucose 0.2
%, Neutroeletoclaus 0.2%, and sodium chloride 0.1%). Therefore, it was also clarified that this method can also provide a useful bacterial inoculum. In addition, generally
Since andesite, ceramic balls (porous), etc. do not contain useful bacterial spores, and there are too few useful bacteria that enter the bath water, the high concentration of useful bacteria already mentioned can occur. Therefore, it cannot be said that the biological treatment of the bath water cannot be carried out unless seed bacteria, especially highly concentrated spores are given as seeds.

【0023】3. 活性汚泥成形品中の有用細菌の確認 有用細菌による処理を行っている屎尿処理場の引き抜き
汚泥を脱水し、これにシリカ溶液の適量(50ml/K
g)を加えて混合し発酵処理後に、成形し自然乾燥して
活性汚泥成形品とした。この活性汚泥成形品を粉砕し、
その1gを分取して500mlの純水に溶解し、その適
量を分取して予め準備してある寒天培地(可溶性澱粉、
蛋白質含有)上に散布し、32℃で3日間培養し発芽さ
せた。その結果、この汚泥中には5×1010〜1×10
11個/gの有用細菌胞子が存在したことが確認された。
尚、その他酵母菌や球菌が僅かに存在したが、有用細菌
の優先率は96%に達した。
3. Confirmation of Useful Bacteria in Activated Sludge Molded Article Dewatered sludge from a human waste treatment plant, where treatment with useful bacteria is performed, is dehydrated, and an appropriate amount of silica solution (50 ml / K is added thereto).
g) was added and mixed, and after fermentation treatment, it was molded and air-dried to obtain an activated sludge molded product. Crush this activated sludge molded product,
An aliquot of 1 g was dissolved in 500 ml of pure water, and an appropriate amount was aliquoted to prepare an agar medium (soluble starch,
(Containing protein), and cultured at 32 ° C. for 3 days to germinate. As a result, this sludge contained 5 × 10 10 to 1 × 10 5.
It was confirmed that there were 11 useful bacteria spores / g.
Although other yeasts and cocci were slightly present, the priority rate of useful bacteria reached 96%.

【0024】4. 窒素吸着濾材の検討 硫酸アンモニウム溶液(1.0w/w%)を作成し、各種
濾材50gをコンデンサーに充填し、5ml/分で硫酸
アンモニウム溶液を流下させ、その濾過液中のアンモニ
ア性窒素をネスラー法により定量した。その結果を、表
2に示すす。 表 2 ゼオライト製品 残留アンモニア性窒素(ppm ) 天然ゼオライト破砕品5mm径 3.6 ゼオライト粉末造粒品(ペレット)3mmφ 2.1 ゼオライト粉末造粒品(球形)5mm径 1.3 高純度ゼオライト粉末造粒品(ペレット)4mmφ 0.6 表2から判るように、高純度ゼオライト造粒品が最も適
していることが明らかとなった。また、これらゼオライ
ト造粒品は、その多孔質性状により、有用細菌の担体と
なるとともに、シリカやマグネシウムを溶出して有用細
菌の高濃度化に資することを考えると、大変有効と言え
る。
4. Examination of Nitrogen-Adsorbing Filter Material An ammonium sulfate solution (1.0 w / w%) was prepared, 50 g of various filtering materials were filled in a condenser, and the ammonium sulfate solution was allowed to flow down at 5 ml / min, so that the filtrate was ammoniacal. Nitrogen was quantified by the Nessler method. The results are shown in Table 2. Table 2 Zeolite products Residual ammonia nitrogen (ppm) Natural zeolite crushed product 5 mm diameter 3.6 Zeolite powder granulated product (pellet) 3 mm φ 2.1 Zeolite powder granulated product (spherical) 5 mm diameter 1.3 High-purity zeolite powder manufacturing Granular product (pellet) 4 mm φ 0.6 As can be seen from Table 2, it was revealed that the high-purity zeolite granulated product is most suitable. Further, these zeolite granules can be said to be very effective, considering that they serve as a carrier for useful bacteria due to their porous nature and contribute to high concentration of useful bacteria by eluting silica and magnesium.

【0025】5. 有効ミネラル供給濾材の選択 各種濾材100gを秤取し、1リットルビーカーに採
り、純水900mlを加えて超音波槽(50KHz)で
30分間溶出させた結果は表3(その1)、(その2)
の通りであり、材毎にその適量を決めて使用する。
5. Selection of Effective Mineral Supply Filter Material 100 g of each filter material was weighed out, placed in a 1 liter beaker, added with 900 ml of pure water and eluted in an ultrasonic bath (50 KHz) for 30 minutes. The results are shown in Table 3 (No. 1). ), (Part 2)
The appropriate amount is determined for each material and used.

【表3】 上記より、また物理濾材効果も勘案して、濾材としては
方形石、ゼオライト、麦飯石、セラミックボール(Si
2 ・Al2 3 )等が適しているが、特に限定される
ことはない。尚、表3中、方形石(クリストバル石)は
5〜8mmの破砕品、他の石は5〜20mmの破砕品、
セラミックボールと麦飯セラミックは5mmの球形品を
使用した。
[Table 3] From the above, in consideration of the effect of the physical filter medium, the filter medium is square stone, zeolite, barley stone, ceramic balls (Si
O 2 · Al 2 O 3 ) and the like are suitable, but are not particularly limited. In Table 3, square stones (Cristobal stones) are crushed products of 5 to 8 mm, other stones are crushed products of 5 to 20 mm,
As the ceramic balls and the boiled rice ceramics, spherical products of 5 mm were used.

【0026】(本発明処理方法のまとめ) 1. 濾過筒内に有用細菌胞子を持つ濾材(方形石)また
は種胞子を植えた糸、紐、ロープ等の繊維製品或いは活
性汚泥成形品を内装又は別途生物処理層内に充填し、生
物処理に関わる有用細菌を高濃度に保持して、流入する
栄養分を高速度的に分解する。この場合、方形石、ロー
プ種菌或いは汚泥成形品を単独で採用してもよく、複合
で採用してもよい。 2. 栄養分の高速吸着による高濃度化と、その有用細菌
による分解と言う全く新しい生物濾過方式を採用する。 3. 有用細菌を活性化、高濃度化するために、ミネラル
特にシリカ、マグネシウムの適量を溶出する濾材であっ
て、物理濾過にも働く濾材を用いる。 4. 水中の微生物と接触時間を長くとるように濾過水流
量の圧縮と、パス(短絡)の起こらない、又は浴槽内水
流を得るに必要な最低限のパス水量となるように工夫す
る。 5. 従って、浴槽の場合のバブルジェットは濾過系とは
別の経路で行なう。更に、生物処理の害になるオゾン曝
気や紫外線照射は併用しない。
(Summary of the Treatment Method of the Present Invention) 1. A filter material (square stone) having useful bacterial spores or a fiber product such as a thread, string, rope or the like in which a useful spore is planted or an activated sludge molded product is internally provided in a filtration cylinder or Separately filled in the biological treatment layer, the useful bacteria involved in biological treatment are maintained at a high concentration, and the inflowing nutrients are decomposed at high speed. In this case, the square stone, the inoculum of rope, or the sludge molded product may be used alone or in combination. 2. Adopt a completely new biological filtration method called high concentration of nutrients by high-speed adsorption and its decomposition by useful bacteria. 3. To activate and increase the concentration of useful bacteria, use a filter medium that elutes an appropriate amount of minerals, especially silica and magnesium, and that also works for physical filtration. 4. Make arrangements so that the flow rate of filtered water is compressed so that the contact time with microorganisms in the water is long, and that a pass (short circuit) does not occur or the minimum pass water amount necessary to obtain the water flow in the bathtub. 5. Therefore, in the case of a bathtub, bubble jet should be routed separately from the filtration system. Furthermore, neither ozone aeration nor ultraviolet irradiation, which is harmful to biological treatment, is used together.

【0027】(本発明装置のまとめ) 1. 濾過流速を大幅に減速し、濾過筒内滞留時間を最低
2〜3分以上とする。プールや魚の飼育槽等水温が低い
場合は3〜10分以上対流させることが好ましい。 2. 有用細菌を活性化するミネラル溶出を確保する。 3. 着床より離脱したバクテリアの流出を防止する単純
濾材又はミネラル溶出濾材を用いる。更に最終段階でフ
イルターを使用する。 4. 更に、濾過筒に各種濾材を充填する関係から、メン
テナンスが容易にできる機構で、充分な処理効果を発現
できる機構を採用する。 5. オゾン発生器や紫外線照射を排除する。生物膜処理
を行なう上で、水中にオゾンを吹き込んで溶解させるこ
とは、全く甚だしい矛盾であると言わざるを得ない。オ
ゾンは、悪性細菌ばかりか良性細菌(有用細菌)までも
殺菌するし、人間にとっても有害である。 6. 有用細菌を優先化(90%以上)しておけば、腐敗
菌等の悪性菌は消滅する。よって、その優先処理を講ず
る。 7. 浴槽の場合、ジエット水流システムについては、そ
の吸水を循環濾過水を用いないで、浴槽から別途単独で
導きだし、ポンプ圧送またはエア圧送を行いながら、ア
スピレーター効果によりジエット水流を浴槽内に造らせ
る方式を採用する。これにより、濾過筒内流速は、任意
に設定できる。大型浴槽の場合、溜水抵抗が大きいた
め、複数設置することが望ましい。 8. 浴槽よりオーバーフローした湯(表面水)は、回収
して循環使用する。この場合、浴槽から引き抜いた湯と
合流させて処理してもよいが、オーバーフロー水を受け
る溝内において、方形石とゼオライトに接触させ、その
後タンクに溜めてから引き抜いた湯と合流させるように
してもよい。この場合、有用細菌はここで発芽して栄養
分解と油分凝集を行わせるとともに、ゼオライト石によ
りアンモニア、硫化水素(ゼオライトは硫化水素は殆ど
吸着せず)を吸着させ、二次的に方形石表面に発芽した
有用細菌によりこれを分解させるようにしてもよい。
(Summary of the device of the present invention) 1. The filtration flow rate is significantly reduced so that the retention time in the filtration cylinder is at least 2 to 3 minutes. When the water temperature is low, such as in a pool or a fish breeding tank, it is preferable to convection for 3 to 10 minutes or longer. 2. Ensure mineral elution that activates useful bacteria. 3. Use a simple filter medium or mineral elution filter medium to prevent the outflow of bacteria that have detached from the implantation. Further, a filter is used in the final stage. 4. Furthermore, due to the fact that the filter cylinder is filled with various types of filter media, a mechanism that can be easily maintained and that exhibits a sufficient treatment effect will be adopted. 5. Eliminate ozone generators and UV irradiation. In carrying out biofilm treatment, blowing ozone into water to dissolve it must be said to be a serious contradiction. Ozone kills not only malignant bacteria but also benign bacteria (useful bacteria) and is harmful to humans. 6. By prioritizing useful bacteria (90% or more), malignant bacteria such as spoilage bacteria disappear. Therefore, the priority process is taken. 7. In the case of a bathtub, as for the jet water flow system, the water absorption is guided separately from the bathtub without using circulating filtered water, and the jet water flow is created in the bathtub by the aspirator effect while pumping or air pumping. Adopt a method that allows Thereby, the flow velocity in the filtration cylinder can be set arbitrarily. In the case of a large tub, it is desirable to install multiple tubs because of the large water resistance. 8. Collect the hot water (surface water) that overflows from the bathtub and reuse it. In this case, the treatment may be performed by combining with the hot water drawn from the bath, but in the groove for receiving the overflow water, the square stone and the zeolite are brought into contact with each other, and then the hot water extracted from the tank is joined. Good. In this case, the useful bacteria germinate here to cause nutrient decomposition and oil aggregation, and at the same time, adsorb ammonia and hydrogen sulphide (zeolite hardly adsorbs hydrogen sulphide) by the zeolite stone, and secondary You may make it decompose | disassemble by the useful bacteria which germinated.

【0028】(水棲動物の飼育槽の場合)鑑賞魚の飼育
槽や水族館の水槽の場合、浴湯に比べて水温が低いの
で、微生物の活性が低くなって処理速度が遅くなる。従
って、濾過装置の大形化によって、装置内での水の滞留
時間を少なくとも3〜10分以上と長くする必要があ
る。従来は、フイルターによる濾過とともに活性炭等に
よるアンモニア等の吸着が行なわれていたが、これだけ
では病原菌を排除することは不可能であった。本発明の
採用により、大腸菌、球菌、ブドウ状球菌等の病原菌を
殺菌できるのみならず、定期的な活性炭の交換に要する
手間を省くことができる。
(In the case of aquariums for aquatic animals) In the case of fish tanks for appreciating fish and aquariums, the water temperature is lower than that of bath water, so that the activity of microorganisms becomes low and the treatment speed becomes slow. Therefore, it is necessary to lengthen the residence time of water in the apparatus to at least 3 to 10 minutes or more by increasing the size of the filtering apparatus. Conventionally, adsorption of ammonia and the like by activated carbon and the like was carried out along with filtration by a filter, but it was not possible to eliminate pathogenic bacteria by this alone. By adopting the present invention, it is possible not only to sterilize pathogenic bacteria such as Escherichia coli, cocci, and staphylococci, but also to save the time and labor required for regular replacement of activated carbon.

【0029】(プール、温水プールの場合)プールや温
水プールの場合、水中の汚れ物質は浴湯の場合と殆ど同
じであり、本発明が適用できる。但し、温水プールの場
合はまだしも冷水プールの場合は、水温が低いため、水
棲動物の飼育槽の場合と同様の問題が生じる。更に、プ
ールの場合は塩素消毒がされているので、引き抜いた水
をそのまま本発明装置に通すと、有用細菌が死滅する。
従って、本発明濾過装置を通す前に、活性炭等による脱
塩素処理を行なう必要がある。尚、充分な処理能力を持
った本発明装置で処理すれば、塩素滅菌は不要か或いは
塩素濃度を著しく逓減しても、問題は生じない。
(In the case of pools and hot water pools) In the case of pools and hot water pools, the contaminants in water are almost the same as in the case of bath water, and the present invention can be applied. However, in the case of the hot water pool, the water temperature is still low in the case of the cold water pool, so the same problem as in the case of the aquarium for aquatic animals occurs. Further, since the pool is sterilized with chlorine, if the extracted water is directly passed through the device of the present invention, useful bacteria are killed.
Therefore, it is necessary to perform dechlorination treatment with activated carbon or the like before passing through the filtration device of the present invention. If the treatment is performed by the device of the present invention having a sufficient treatment capacity, chlorine sterilization is not necessary, or even if the chlorine concentration is remarkably reduced, no problem will occur.

【0030】[0030]

【実施例】次に、実施例により本発明を更に詳細に説明
する。 実施例 1 図1は、家庭風呂用の恒温浄化装置等に組み込まれる小
型濾過器の一例を示す。この小型濾過器1は、底部に引
抜き水導入口2、蓋部に濾過水送出口3を備えた筒型容
器4の内部に網容器5を収納し、この網容器5内に方形
石、ゼオライト、セラミックボール、麦飯石及び不織布
フイルターを順次下方から充填したものである。方形石
の代わりに上記した有用細菌胞子を含む繊維製品や汚泥
成形品を使用してもよいし、セラミックボールや麦飯石
の代わりに軽石その他の鉱物を使用してもよい。尚、網
容器5は浴湯の短絡を防ぐために、筒型容器4の内部下
方に設けた環状金具6で支持され、容器内壁に内接した
状態で収納されている。網容器5と環状金具6の間にパ
ンキングを介挿させてもよい。この筒型容器の内容量は
3.1リットル、循環水量は1リットル/分である。従っ
て、濾過筒内滞留時間は約3分である。
Next, the present invention will be described in more detail by way of examples. Example 1 FIG. 1 shows an example of a compact filter incorporated in a home bath constant temperature purification device or the like. This small-sized filter 1 contains a net container 5 inside a cylindrical container 4 having a drawing water inlet 2 at the bottom and a filtered water outlet 3 at the lid, and the net container 5 contains square stones and zeolite. , Ceramic balls, barley stones, and a non-woven fabric filter are sequentially filled from below. Instead of the square stone, a fiber product or a sludge molded product containing the above-mentioned useful bacterial spores may be used, and instead of the ceramic ball or the barley stone, pumice or other minerals may be used. The mesh container 5 is supported by an annular metal member 6 provided below the inside of the cylindrical container 4 in order to prevent a short circuit of the bath water, and is stored in a state of being inscribed in the inner wall of the container. Punking may be inserted between the mesh container 5 and the annular metal member 6. The content of this cylindrical container is
3.1 liters, circulating water volume is 1 liter / min. Therefore, the residence time in the filtration cylinder is about 3 minutes.

【0031】この小型濾過器(循環濾過装置)を組み込
んだ恒温浄化装置を、容量250リットル槽(家庭用2
人用風呂)に設置して平成5年3月1日より連続運転テ
ストを行った(平成6年8月末まで)ところ、浴湯の清
浄度、透明度に変化もなく、悪臭の発生も全くなかった
(もっとも、洗い湯分は追加した)。更に濾過器内部の
点検を行ったところ、方形石表面は全て有用細菌及びそ
の胞子コロニーで覆われており、ゼオライト層にも有用
細菌の付着が認められた。更に、その上部のセラミック
ボールや麦飯石濾材の凹凸部には有用細菌の着床が見ら
れた。また、繊維フィルターには、担体を離脱したバク
テリアが引っ掛かっており、生物処理が充分に行われた
ことを示した。これは、方形石、ゼオライトに付着した
有用細菌及び同胞子の高濃度化(1×1010個/ml)
が認められ、それらによる処理効果が発現したものと考
えられる。また、1年6ケ月使用後の浴湯水質は、表4
(その1)、(その2)に示す通りの優れたものであっ
た。
A constant temperature purification device incorporating this small-sized filter (circulation filtration device) was used in a 250-liter tank (2 for household use).
It was installed in a bath for people) and a continuous operation test was carried out from March 1, 1993 (until the end of August 1994). The cleanliness and transparency of the bath water did not change, and no foul odor was generated. (However, I added the hot water for washing.) Further, when the inside of the filter was inspected, all the surface of the square stone was covered with useful bacteria and its spore colonies, and the adherence of useful bacteria was also found in the zeolite layer. Further, the implantation of useful bacteria was observed on the ceramic balls and the uneven portion of the barley stone filter material on the upper part thereof. In addition, bacteria detached from the carrier were caught on the fiber filter, indicating that the biological treatment was sufficiently performed. This is a high concentration of square stone, useful bacteria attached to zeolite, and spores (1 × 10 10 cells / ml)
Was observed, and it is considered that the treatment effect by them was exhibited. In addition, Table 4 shows the quality of bath water after 1 year and 6 months of use.
It was excellent as shown in (1) and (2).

【表4】 上記の通り、大変優れた水質、清澄度を有しており、特
に有用細菌の活性化、高濃度化に必要なミネラル分を溶
解していることは、大きな特徴であり、充分な生物処理
効果を示した。また浴湯中のミネラル分は、SiO2
2.0ppm 、MgO22.1ppm 、CaO32.6ppm であっ
た。尚、表4中の金属は全て酸化物である。
[Table 4] As mentioned above, it has a very good water quality and clarity, and it is a major feature that it dissolves the minerals necessary for activating and increasing the concentration of useful bacteria. showed that. The mineral content in the bath water is SiO 2 7
The amounts were 2.0 ppm, MgO2.1 ppm and CaO32.6 ppm. All the metals in Table 4 are oxides.

【0032】比較例 1 実施例1に使用したものと略同様の筒型容器(内容量3.
1リットル)に、周囲が透けた状態で網容器を挿入し、
この網容器に実施例1と同様の麦飯石とセラミックボー
ルを充填した。この小型濾過器を、循環水量が41リッ
トル/分(濾過筒内滞留時間は約4.5秒)にした以外は
実施例1と同様に使用し、1年6ケ月使用後の浴湯水質
を分析した。その結果を表4に示す。尚、従来使用され
ている多くの濾過器は、比較例品と同様に濾過筒内滞留
時間が極めて短いものである。
Comparative Example 1 A cylindrical container (content of 3.
1 liter), insert a mesh container with the surroundings transparent,
This net container was filled with the same barley stone and ceramic balls as in Example 1. This small-sized filter was used in the same manner as in Example 1 except that the circulating water flow rate was 41 liters / minute (retention time in the filter cylinder was about 4.5 seconds), and the bath water quality after 1 year and 6 months was used. analyzed. The results are shown in Table 4. It should be noted that many of the conventionally used filters have extremely short residence time in the filter cylinder, as in the comparative example.

【0033】実施例 2 図2は、業務用の浴湯循環濾過装置の一例を示す。この
循環濾過装置7は、底部に引抜き水導入口8、蓋部に濾
過水送出口9を備えた筒型容器10の内部に、下方から
順に方形石と胞子含有汚泥及びドロマイトを充填した網
容器11、ゼオライトを充填した網容器12、セラミッ
クボールと活性炭を充填した網容器13、麦飯石を充填
した網容器14及び繊維質フイルター15を収納したも
のである。なお、各網容器は鉄板で枠組みし、その底面
及び側面に金網を張設したもので、その下部が筒型容器
10に内接するよう構成されている。筒型容器10の内
面下部には網容器11を支える環状金具16が固設さ
れ、環状金具16の下方は湯溜まり用の空間になってい
る。また、図中符号17は該空間部分に設けられた拡散
・減速板、符号18は洗浄水用ドレイン、符号19はフ
イルター押さえ用の金網、符号20は引抜き水導入用ポ
ンプ、符号21は濾過水送出口用ポンプである。
Embodiment 2 FIG. 2 shows an example of a bath water circulation filtration device for business use. This circulation filtration device 7 is a net container in which a square stone, a spore-containing sludge and dolomite are sequentially filled from the bottom inside a cylindrical container 10 having a drawing water inlet 8 at the bottom and a filtered water outlet 9 at the lid. 11, a net container 12 filled with zeolite, a net container 13 filled with ceramic balls and activated carbon, a net container 14 filled with barley stone, and a fiber filter 15. Each mesh container is framed by an iron plate, and a wire mesh is stretched on the bottom surface and side surfaces of the mesh container, and the lower part of the mesh container is inscribed in the cylindrical container 10. An annular metal fitting 16 for supporting the mesh container 11 is fixedly provided on the lower portion of the inner surface of the cylindrical container 10, and a space for storing a hot water is provided below the annular metal fitting 16. Further, in the figure, reference numeral 17 is a diffusion / deceleration plate provided in the space portion, reference numeral 18 is a drain for cleaning water, reference numeral 19 is a wire mesh for pressing the filter, reference numeral 20 is a pump for introducing drawing water, and reference numeral 21 is filtered water. It is a pump for the delivery port.

【0034】この循環濾過装置7は内容積が340リッ
トルの筒型容器10に、50Kg(15〜30mm粒)
の方形石と10Kgの胞子含有汚泥と10Kgのドロマ
イト、95Kgの高純度ゼオライト造粒品、80kg(S
iO2 とAl2 3 、7mm粒)のセラミックボール、
40Kgの造粒活性炭(3〜5mm)、120kg(5〜
15mm)の麦飯石粒をそれぞれ充填し、最上部にアク
リル綿フイルター板を設置したものである。そして容量
5m2 の浴槽に組み込み、濾過筒通過水量150リット
ル/分で1年以上の長期にわたって連続使用した。従っ
て、この循環濾過装置7における濾過筒内滞留時間は約
2.3 分である。夜間は保温ヒータを使用して24時間運
転を行なった。また、浴槽内ジェット水流を噴射し、エ
ア70リットル/分の導入も併せて運転した。このテス
ト期間中に、濾材の洗浄を行なわず、浴湯の入れ替え、
浴槽の洗浄も全く行なわず、体の洗い湯と蒸発による損
水のみの補給を行なったに過ぎなかったが、テスト終了
時点においても、表4に示すように濁度や透視度に優れ
しかも大腸菌が皆無な清浄な湯の状態であった。
This circulating filtration device 7 has a cylindrical container 10 having an internal volume of 340 liters, and 50 kg (15 to 30 mm particles).
Square stone, 10Kg spore-containing sludge, 10Kg dolomite, 95Kg high-purity zeolite granulated product, 80kg (S
Ceramic balls of iO 2 and Al 2 O 3 , 7 mm particles,
40 kg of granulated activated carbon (3-5 mm), 120 kg (5-
15 mm) of boiled rice stone particles are filled in each, and an acrylic cotton filter plate is installed on the top. Then, it was installed in a bath with a capacity of 5 m 2 and continuously used for a long term of 1 year or more at a water flow rate of 150 liters / minute through a filter cylinder. Therefore, the residence time in the filtration cylinder in this circulation filtration device 7 is about
2.3 minutes. At night, the heater was used to operate for 24 hours. In addition, the jet water flow in the bathtub was jetted, and the operation was performed with the introduction of air at 70 l / min. During this test period, do not wash the filter medium, replace the bath water,
The bathtub was not washed at all, and only body water was supplied and only water that was damaged by evaporation was replenished, but even at the end of the test, as shown in Table 4, the turbidity and the transparency were excellent, and E. coli was used. There was nothing but clean water.

【0035】尚、オーバーフローした浴湯は、図5に一
例を示すような浴湯回収処理槽33で生物処理して浴槽
に戻すようにして、循環濾過装置7の負担を軽減するよ
うにするとよい。この浴湯回収処理槽33は、被処理水
(オーバーフロー浴湯)導入パイプ34と処理水が流出
する越流パイプ35を備えた槽36内に、方形石濾材3
7を充填した網フィルター38を複数段設置したもので
ある。方形石濾材37に加えて、循環濾過装置7に充填
している他の濾材を充填すると、更に処理効率があが
る。尚、負荷が小さい場合は、循環濾過装置7の代わり
にこの浴湯回収処理槽33にオーバーフロー水とともに
循環水を導入して処理するようにしてもよい。
The overflowed bath water may be biologically treated in a bath bath recovery treatment tank 33 as shown in FIG. 5 and returned to the bath to reduce the load on the circulation filtration device 7. . The bath hot water recovery treatment tank 33 includes a square stone filter medium 3 in a tank 36 provided with a treated water (overflow bath hot water) introduction pipe 34 and an overflow pipe 35 through which the treated water flows out.
A plurality of mesh filters 38 filled with 7 are installed. In addition to the square stone filter medium 37, when another filter medium filled in the circulation filter device 7 is filled, the treatment efficiency is further improved. When the load is small, the circulating hot water may be introduced into the bath hot water collecting and treating tank 33 together with the overflow water instead of the circulating filtration device 7 for treatment.

【0036】比較例 2 図8に示す業務用濾過筒(外筒容量600リットル、濾
材は麦飯石及びセラミックボールで濾材容量は28.3リ
ットル×3本)を実施例2と同様の条件で使用した。但
し、濾過筒通過水量500リットル/分であるため、濾
過筒内滞留時間は約1.2分である。その結果を表4に示
す。
Comparative Example 2 A commercial-use filtration cylinder shown in FIG. 8 (outer cylinder capacity: 600 liters, filter media: barley stone and ceramic balls, filter media capacity: 28.3 liters × 3) was used under the same conditions as in Example 2. did. However, since the amount of water passing through the filter cylinder is 500 liters / minute, the residence time in the filter cylinder is about 1.2 minutes. The results are shown in Table 4.

【0037】表4から明らかなように、本発明(実施
例)では長時間使用後の浴湯に病原菌が見られずBO
D、CODも低く、清浄度の高い結果となった。尚、シ
リカ及びマグネシウム濃度が高いが、これは有用細菌が
活性化されていることの査証となる。これに対し従来装
置(比較例)は、病原菌や雑菌も多く、またBODやC
ODも高いし清浄性に欠けるものである。
As is clear from Table 4, in the present invention (Example), no pathogenic bacteria were found in the bath water after long-term use
The D and COD were also low, resulting in high cleanliness. It should be noted that the silica and magnesium concentrations are high, which serves as a voucher that useful bacteria are activated. On the other hand, the conventional device (comparative example) has many pathogenic bacteria and miscellaneous bacteria, and BOD and C
It has a high OD and lacks cleanliness.

【0038】実施例 3 循環濾過装置22として、図2のものに代えて図3に示
すように網容器23の外周に外筒24を設けて槽25と
し、積み重ねた槽25の各外筒24により筒型容器26
を構成するようにしてもよい。この場合、各外筒24は
連結具27で水密に連結されるようになっており、濾材
の手入れが簡単にできる利点がある。尚、図3の循環濾
過装置22の濾材は、有用細菌及びミネラル供給槽25
Aとして有用細菌胞子を含む繊維製品と汚泥成形品、吸
着槽25Bとしてゼオライト破砕品を充填しているが、
必要に応じて槽の数を増やせばよい。他は、実施例2と
同様である。
Example 3 As the circulation filtration device 22, instead of the one shown in FIG. 2, as shown in FIG. 3, an outer cylinder 24 is provided on the outer circumference of a mesh container 23 to form a tank 25, and each outer cylinder 24 of the stacked tanks 25 is provided. Due to the cylindrical container 26
May be configured. In this case, the outer cylinders 24 are water-tightly connected by the connection tool 27, which has an advantage that the filter media can be easily maintained. The filter material of the circulation filtration device 22 of FIG. 3 is a useful bacteria and mineral supply tank 25.
A is filled with a fiber product containing useful bacterial spores and a sludge molded product, and a crushed zeolite product is used as the adsorption tank 25B.
If necessary, increase the number of tanks. Others are the same as in the second embodiment.

【0039】実施例 4 図4の循環濾過装置28は、複数(図では3個)の筒型
容器29にそれぞれ方形石30、ゼオライト31、麦飯
石32を充填し、これを連結したものである。この装置
は、設置面積は大きくなるが濾過材の手入れが容易に行
なえる利点がある。尚、上記した各循環濾過装置は、浴
湯以外にプールの水や水族館の飼育水の清浄化処理にそ
のまま使用できる。ただ、水温が低いために滞留時間を
長くするため容量を大きくするとか、脱塩素処理装置を
接続するなど、設計変更を加える必要がある。
Example 4 The circulation filtration device 28 of FIG. 4 is one in which a plurality of (three in the figure) cylindrical vessels 29 are filled with square stones 30, zeolite 31, and barley stones 32, respectively, and they are connected. . This device has a large installation area, but has an advantage that the filter medium can be easily maintained. In addition to the bath water, each of the above-described circulation filtration devices can be used as it is for the purification treatment of pool water and aquarium breeding water. However, since the water temperature is low, it is necessary to make design changes such as increasing the capacity to increase the residence time and connecting a dechlorination treatment device.

【0040】実施例 5 図6は、鑑賞魚用の水槽39の水を循環濾過する濾過装
置40の一例を示す。この濾過装置40は、処理槽41
を3枚の仕切り板42で4室に仕切り、中央の2つの濾
過室43に有用細菌胞子含有物やシリカ源、マグネシウ
ム源等の濾材44を充填したものである。水槽の水はポ
ンプPで引き抜かれ、被処理水導入パイプ45から曝気
室46に送り込まれる。水は自然流下している間に処理
され、越流パイプ47から放流室48へ越流してフィル
ター49を通して水槽39に戻される。符号50、51
は散気具である。
Embodiment 5 FIG. 6 shows an example of a filtration device 40 for circulating and filtering the water in the water tank 39 for ornamental fish. The filtering device 40 includes a processing tank 41.
Is divided into four chambers by three partition plates 42, and the two central filtration chambers 43 are filled with a filter medium 44 containing a useful bacterial spore-containing material, a silica source, a magnesium source or the like. The water in the water tank is drawn out by the pump P and fed into the aeration chamber 46 from the treated water introduction pipe 45. The water is treated while naturally flowing down, overflows from the overflow pipe 47 into the discharge chamber 48, and is returned to the water tank 39 through the filter 49. Reference numerals 50 and 51
Is an air diffuser.

【0041】実施例 6 図7は、同じく鑑賞魚用の水槽の水を循環濾過する濾過
装置の他の例を示す。この濾過装置52は水槽内に設置
されるもので、透水構造の容器53の内部に、有用細菌
胞子含有物やシリカ源、マグネシウム源等の濾材54を
充填し、処理水を容器外に吸引する吸引口55を設けて
いる。吸引は、ポンプで行っても良いが、図のように散
気による対流を利用してもよい。ここに透水構造とは、
容器に多数のスリット孔や丸孔を設けたり、網で構成し
て水が容器内に入る構造のことを言う。容器の外周はス
ポンジ等で被覆してもよい。符号56は散気管、57は
散気具である。
Embodiment 6 FIG. 7 shows another example of a filtering device for circulating and filtering water in an aquarium for ornamental fish. The filtration device 52 is installed in a water tank, and a filter medium 54 such as a useful bacterial spore-containing material, a silica source, a magnesium source is filled in a water-permeable container 53, and the treated water is sucked out of the container. A suction port 55 is provided. The suction may be performed by a pump, but convection due to air diffusion may be used as shown in the figure. The permeable structure here is
It means a structure in which a large number of slit holes or round holes are provided in the container, or a net is used to allow water to enter the container. The outer circumference of the container may be covered with sponge or the like. Reference numeral 56 is an air diffuser, and 57 is an air diffuser.

【0042】[0042]

【発明の効果】以上詳述したように本発明の水の循環濾
過方法は、槽から引き抜いた水を有用細菌胞子含有物と
シリカ源、マグネシウム源の層、更にはゼオライトの層
や麦飯石その他の濾材の層を時間をかけてゆっくり且つ
確実に通過させるものである。また、従来広く行われて
いる紫外線照射やオゾン添加、処理湯のバブルジェット
化を排除するものである。従って、有用細菌の優先化が
起こり、大腸菌その他の病原菌の繁殖が押さえられて極
めて衛生的である。また有用細菌の活発な栄養活動によ
り浴湯中の老廃物が完全に除去され、循環使用する浴湯
の清浄化が、長期に渡って維持される。低温の水棲動物
の飼育槽水の場合も、引抜きいた水を濾過装置内で充分
な時間濾材と接触させれば、水中の排泄物や餌残渣が除
去され、水の清浄化が十分に行なえる。冷水や温水プー
ルの場合、塩素滅菌やオゾン殺菌を廃止し、十分な能力
のある大形の濾過装置を使用すれば、浴湯の場合と同様
に水中に含まれる老廃物その他の汚れ成分が完全に除去
できる。温水プールの方が、水温が高い分だけ装置がよ
り小型のもので済む。塩素滅菌やオゾン殺菌を行なって
いる場合は、本発明の濾過装置に掛ける前に、活性炭に
よる塩素吸着や、特定波長の紫外線によるオゾンの消去
等の前処理をおこなえばよい。
As described in detail above, the method of circulating filtration of water according to the present invention uses the water drawn from the tank as a layer containing useful bacterial spores, a silica source, a magnesium source, a zeolite layer, barley stone, etc. It slowly and surely passes through the layer of the filter medium described above. Further, it eliminates ultraviolet irradiation, addition of ozone, and formation of bubble jet of treated hot water, which have been widely performed in the past. Therefore, useful bacteria are prioritized, and the propagation of Escherichia coli and other pathogenic bacteria is suppressed, which is extremely hygienic. Moreover, waste products in the bath water are completely removed by the active nutritional activity of the useful bacteria, and the cleanliness of the bath water used for circulation is maintained for a long period of time. Even in the case of low-temperature aquatic animal breeding tank water, if the extracted water is contacted with the filter medium for a sufficient time in the filter device, excrements and food residues in the water will be removed and the water will be sufficiently purified. . In the case of cold water and hot water pools, chlorine sterilization and ozone sterilization will be abolished, and if a large-capacity filtration device with sufficient capacity is used, waste products and other contaminants contained in the water will be completely removed as in the case of bath water. Can be removed. The warm water pool requires a smaller device because the water temperature is higher. When chlorine sterilization or ozone sterilization is performed, pretreatment such as adsorption of chlorine by activated carbon or elimination of ozone by ultraviolet rays of a specific wavelength may be carried out before application to the filtration device of the present invention.

【0043】また本発明の水の循環濾過装置は、濾過筒
通過水量を抑えしかも短絡が生じないように濾材を収納
した網容器が濾過筒に内接されている。従って、引き抜
いた水が十分な浄化作用、ミネラル溶出作用を受けて循
環する。しかも、濾材として有用細菌胞子含有物とシリ
カ源、マグネシウム源、更にはゼオライト等を使用して
いるので、従来増殖がみられた病原菌が皆無になり、長
期に渡って衛生的且つ安全に使用できるものである。
尚、本発明においては濾過筒等浄化に関わる部分につい
てのみ説明したが、家庭風呂用の恒温浄化装置の場合、
従来品同様ヒーターや浴湯温度調節機能を組み込んで使
用できることは当然である。
Further, in the water circulation filter of the present invention, the mesh container containing the filter medium is inscribed in the filter cylinder so as to suppress the amount of water passing through the filter cylinder and to prevent a short circuit. Therefore, the extracted water circulates with a sufficient purification action and mineral elution action. Moreover, since a bacterial spore-containing material useful as a filter medium, a silica source, a magnesium source, and further a zeolite etc. are used, there is no pathogenic bacterium that has been conventionally grown, and it can be used hygienically and safely for a long period of time. It is a thing.
In the present invention, only the part related to purification such as the filter cylinder has been described, but in the case of a home bath constant temperature purification device,
As with conventional products, it is of course possible to incorporate a heater and bath water temperature adjustment function into the product.

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

【図1】本発明に関わる家庭用の小型濾過器の一例を示
す縦断面図である。
FIG. 1 is a vertical cross-sectional view showing an example of a home-use compact filter according to the present invention.

【図2】本発明に関わる業務用の循環濾過装置の一例を
示す縦断面図である。
FIG. 2 is a vertical sectional view showing an example of a commercial circulation filtration device according to the present invention.

【図3】循環濾過装置の他の例を示す縦断面図である。FIG. 3 is a vertical cross-sectional view showing another example of the circulation filtration device.

【図4】循環濾過装置の更に異なる他の例を示す一部断
面した側面図である。
FIG. 4 is a partially sectional side view showing still another example of the circulation filtration device.

【図5】オーバーフロー水の処理槽の一例を示す断面図
である。
FIG. 5 is a cross-sectional view showing an example of a treatment tank for overflow water.

【図6】鑑賞魚用の循環濾過装置の一例を示す断面図で
ある。
FIG. 6 is a cross-sectional view showing an example of a circulation filtration device for appreciation fish.

【図7】鑑賞魚用の循環濾過装置の他の例を示す断面図
である。
FIG. 7 is a cross-sectional view showing another example of the circulation filtering device for ornamental fish.

【図8】従来の業務用浴湯濾過筒の一例を示す概略斜視
図である。
FIG. 8 is a schematic perspective view showing an example of a conventional commercial bath hot water filter cylinder.

【符号の説明】[Explanation of symbols]

1 小型濾過器 2 引抜き水導入口 3 濾過水送出口 4 筒型容器 5 網容器 7 循環濾過装置 10 筒型容器 11〜15 網容器 20 引抜き水導入用ポンプ 21 濾過水送出用ポンプ 22 循環濾過装置 23 網容器 24 外筒 25 槽 28 循環濾過装置 29 筒型容器 33 浴湯回収処理槽 36 槽 38 網フィルター 39 鑑賞魚用の水槽 40 濾過装置 41 処理槽 52 濾過装置 53 透水構造の容器 54 濾材 55 吸引口 1 Small Filter 2 Extraction Water Inlet 3 Filtered Water Outlet 4 Cylindrical Container 5 Mesh Container 7 Circulating Filtration Device 10 Cylindrical Container 11-15 Mesh Container 20 Extraction Water Introducing Pump 21 Filtered Water Delivery Pump 22 Circulation Filtering Device 23 Net Container 24 Outer Cylinder 25 Tank 28 Circulating Filtration Device 29 Cylindrical Container 33 Bath Hot Water Recovery Treatment Tank 36 Tank 38 Mesh Filter 39 Water Tank for Appreciating Fish 40 Filtration Device 41 Treatment Tank 52 Filtration Device 53 Water-permeable Container 54 Filter Media 55 Suction port

フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 B01D 35/027 C02F 1/28 E C02F 1/28 3/06 ZAB 3/06 ZAB 3/10 Z 3/10 3/34 Z 3/34 B01D 35/02 J E04H 4/12 C E04H 3/20 B Continuation of front page (51) Int.Cl. 6 Identification number Office reference number FI technical display location B01D 35/027 C02F 1/28 E C02F 1/28 3/06 ZAB 3/06 ZAB 3/10 Z 3/10 3/34 Z 3/34 B01D 35/02 J E04H 4/12 C E04H 3/20 B

Claims (11)

【特許請求の範囲】[Claims] 【請求項1】 槽内の水中に含まれる老廃物質を清浄化
処理して循環使用をする場合において、引き抜いた水又
は吸い込んだ水を有用細菌胞子含有物とシリカ源、マグ
ネシウム源を充填した濾過装置を通過させることを特徴
とする水の循環濾過方法。
1. When the waste substance contained in the water in the tank is purified and used for circulation, the extracted water or the sucked water is filled with useful bacterial spore-containing material, silica source, and magnesium source for filtration. A method of circulating filtration of water, which comprises passing through a device.
【請求項2】 濾過装置には、更にゼオライト、他の接
触濾材の少なくとも一方を充填したものである請求項1
記載の水の循環濾過方法。
2. The filter device is further filled with at least one of zeolite and another contact filter medium.
A method for circulating filtration of water as described.
【請求項3】 槽が、浴槽、プール又は温水プールであ
る請求項1又は請求項2記載の水の循環濾過方法。
3. The water circulation filtration method according to claim 1, wherein the tank is a bath, a pool, or a hot water pool.
【請求項4】 槽が、水棲動物の飼育槽である請求項1
又は請求項2記載の水の循環濾過方法。
4. The tank is an aquatic animal breeding tank.
Alternatively, the method of circulating filtration of water according to claim 2.
【請求項5】 濾過装置内における水の滞留時間を、少
なくとも2〜3分以上にするとともに、バブルジェット
は別系統とするものである請求項3又は請求項4記載の
水の循環濾過方法。
5. The water circulation filtration method according to claim 3, wherein the residence time of water in the filtration device is at least 2 to 3 minutes or more and the bubble jet is a separate system.
【請求項6】 下部に引抜き水導入口、上部に濾過水送
出口を備えた筒型容器の内部に、有用細菌胞子含有物と
シリカ源、マグネシウム源を充填した網容器を収納した
ことを特徴とする水の循環濾過装置。
6. A net container filled with a useful bacterial spore-containing material, a silica source, and a magnesium source is housed in a cylindrical container having a drawing water inlet at the bottom and a filtered water outlet at the top. A circulating filtration device for water.
【請求項7】 下部に引抜き水導入口、上部に濾過水送
出口を備えた筒型容器の内部に、下方から順に有用細菌
胞子含有物とシリカ源、マグネシウム源を充填した網容
器、ゼオライトを充填した網容器及び接触濾材を充填し
た網容器を収納したことを特徴とする水の循環濾過装
置。
7. A tubular container having a drawing water inlet at the bottom and a filtered water outlet at the top, and a net container filled with useful bacterial spore-containing material, silica source, magnesium source, and zeolite in this order from the bottom. A water circulation filtration device, characterized in that a filled mesh container and a mesh container filled with a contact filter medium are housed.
【請求項8】 下部に引抜き水導入口、上部に濾過水送
出口を備えた筒型容器の内部に網容器を収納したものを
複数連結し、各網容器に有用細菌胞子含有物とシリカ
源、マグネシウム源、ゼオライト、及び接触濾材を収納
したことを特徴とする水の循環濾過装置。
8. A cylindrical container having a drawing water inlet at the bottom and a filtered water outlet at the top is connected to a plurality of net containers, and each net container contains a useful bacterial spore-containing material and a silica source. , A magnesium source, zeolite, and a contact filter medium are housed in a water circulation filtration device.
【請求項9】 上部に引抜き水導入口、下部に濾過水送
出口を備えた筒型容器の内部に、少なくともその一部が
容器内壁に内接した状態で網容器を収納し、且つ網容器
内には下方から順に有用細菌胞子含有物とシリカ源やマ
グネシウム源、ゼオライト、及び接触濾材を充填したこ
とを特徴とする水の循環濾過装置。
9. A mesh container is housed inside a cylindrical container having a drawing water inlet at the top and a filtered water outlet at the bottom, at least a portion of which is inscribed in the inner wall of the container. A circulating filtration device for water, which is filled with useful bacterial spore-containing material, silica source, magnesium source, zeolite, and contact filter medium in this order from the bottom.
【請求項10】 被処理水導入パイプと処理水が流出す
る越流パイプを備えた処理槽内部に、有用細菌胞子含有
物とシリカ源、マグネシウム源を充填したことを特徴と
する水の循環装置。
10. A water circulating device characterized in that a useful tank spore-containing material, a silica source, and a magnesium source are filled in a treatment tank equipped with a treated water introduction pipe and an overflow pipe for letting out treated water. .
【請求項11】 槽中に設置されるもので、透水構造の
容器内に有用細菌胞子含有物とシリカ源、マグネシウム
源を充填し、処理水を容器外に吸引する吸引口を設けた
ことを特徴とする水の循環濾過装置。
11. A device installed in a tank, wherein a container having a water-permeable structure is filled with a useful bacterial spore-containing material, a silica source, and a magnesium source, and a suction port for sucking treated water outside is provided. Characteristic water circulation filtration device.
JP35349995A 1994-12-30 1995-12-31 Water circulating filtration method and apparatus Expired - Fee Related JP3827100B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP35349995A JP3827100B2 (en) 1994-12-30 1995-12-31 Water circulating filtration method and apparatus

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP33975494 1994-12-30
JP6-339754 1994-12-30
JP35349995A JP3827100B2 (en) 1994-12-30 1995-12-31 Water circulating filtration method and apparatus

Publications (2)

Publication Number Publication Date
JPH08229591A true JPH08229591A (en) 1996-09-10
JP3827100B2 JP3827100B2 (en) 2006-09-27

Family

ID=26576526

Family Applications (1)

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Country Link
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JP2010247137A (en) * 2009-04-16 2010-11-04 Takahashi Setsubi:Kk Water cleaner and method of using the same
JP2012024762A (en) * 2011-09-22 2012-02-09 Chugoku Electric Power Co Inc:The Microorganism-immobilized carrier, dhs reactor, biological nitrification and denitrification apparatus, and method for using the apparatus
CN104907027A (en) * 2015-06-18 2015-09-16 成都衔石科技有限公司 Reaction equipment capable of preparing straw cellulose food materials conveniently
CN107096202A (en) * 2016-02-22 2017-08-29 汪俊石 A kind of swimming machine
CN108249664A (en) * 2018-03-08 2018-07-06 湖州南浔超联水产养殖有限公司 A kind of water purification installation used for aquiculture
KR20190101816A (en) * 2018-02-23 2019-09-02 농업회사법인 에파솔 주식회사 Adsorption apparatus of chloride ion on storm water for supply into roadside tree rhizosphere
JP2021049527A (en) * 2015-03-17 2021-04-01 ドナルドソン カンパニー,インコーポレイティド Hydrocarbon-in-water purification system
KR102331902B1 (en) * 2021-05-27 2021-12-01 주식회사 거양링커스 Selective filteration apparatus for waste water
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JP2002102876A (en) * 2000-10-02 2002-04-09 Nippon Kenki:Kk Water cleaning apparatus equipped with active chips
JP4502492B2 (en) * 2000-10-02 2010-07-14 株式会社日本建機 Water purification device with active chip
JP2009220075A (en) * 2008-03-18 2009-10-01 Chugoku Electric Power Co Inc:The Microorganism-immobilized carrier, biological nitrification and denitrification apparatus, and method for using the apparatus
JP2010247137A (en) * 2009-04-16 2010-11-04 Takahashi Setsubi:Kk Water cleaner and method of using the same
JP2012024762A (en) * 2011-09-22 2012-02-09 Chugoku Electric Power Co Inc:The Microorganism-immobilized carrier, dhs reactor, biological nitrification and denitrification apparatus, and method for using the apparatus
JP2021049527A (en) * 2015-03-17 2021-04-01 ドナルドソン カンパニー,インコーポレイティド Hydrocarbon-in-water purification system
CN104907027B (en) * 2015-06-18 2017-03-08 姚立东 It is easy to the reaction unit of stalk cellulose food materials preparation
CN104907027A (en) * 2015-06-18 2015-09-16 成都衔石科技有限公司 Reaction equipment capable of preparing straw cellulose food materials conveniently
CN107096202A (en) * 2016-02-22 2017-08-29 汪俊石 A kind of swimming machine
KR20190101816A (en) * 2018-02-23 2019-09-02 농업회사법인 에파솔 주식회사 Adsorption apparatus of chloride ion on storm water for supply into roadside tree rhizosphere
CN108249664A (en) * 2018-03-08 2018-07-06 湖州南浔超联水产养殖有限公司 A kind of water purification installation used for aquiculture
CN114053464A (en) * 2020-08-04 2022-02-18 山东福洋生物科技股份有限公司 Method for reducing corn starch microbial indexes
KR102331902B1 (en) * 2021-05-27 2021-12-01 주식회사 거양링커스 Selective filteration apparatus for waste water
CN116138208A (en) * 2022-09-07 2023-05-23 郑志灿 Internal circulation aquaculture purifying equipment and use method thereof

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