JPS62244493A - Apparatus for recirculating and purifying water - Google Patents
Apparatus for recirculating and purifying waterInfo
- Publication number
- JPS62244493A JPS62244493A JP61087796A JP8779686A JPS62244493A JP S62244493 A JPS62244493 A JP S62244493A JP 61087796 A JP61087796 A JP 61087796A JP 8779686 A JP8779686 A JP 8779686A JP S62244493 A JPS62244493 A JP S62244493A
- Authority
- JP
- Japan
- Prior art keywords
- water
- reactor
- filter
- purification device
- microorganism
- 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
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 67
- 230000003134 recirculating effect Effects 0.000 title 1
- 238000000746 purification Methods 0.000 claims abstract description 14
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims abstract description 7
- 229910000323 aluminium silicate Inorganic materials 0.000 claims abstract description 6
- 241001148470 aerobic bacillus Species 0.000 claims abstract description 4
- 244000005700 microbiome Species 0.000 claims description 18
- 230000000813 microbial effect Effects 0.000 claims description 11
- 229910052751 metal Inorganic materials 0.000 claims description 2
- 239000002184 metal Substances 0.000 claims description 2
- 239000000843 powder Substances 0.000 claims description 2
- 239000007943 implant Substances 0.000 claims 1
- 239000002245 particle Substances 0.000 claims 1
- 230000001954 sterilising effect Effects 0.000 claims 1
- 239000000356 contaminant Substances 0.000 abstract description 7
- 241000894006 Bacteria Species 0.000 abstract description 4
- 238000000034 method Methods 0.000 abstract description 4
- 239000000126 substance Substances 0.000 abstract description 4
- 239000007787 solid Substances 0.000 abstract description 3
- 239000004575 stone Substances 0.000 abstract description 3
- 238000004134 energy conservation Methods 0.000 abstract description 2
- 239000000969 carrier Substances 0.000 abstract 3
- 238000009395 breeding Methods 0.000 abstract 1
- 230000001488 breeding effect Effects 0.000 abstract 1
- 230000001143 conditioned effect Effects 0.000 abstract 1
- 239000000470 constituent Substances 0.000 abstract 1
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 6
- 238000003287 bathing Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 229910052742 iron Inorganic materials 0.000 description 3
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- 229910021536 Zeolite Inorganic materials 0.000 description 2
- 229910052784 alkaline earth metal Inorganic materials 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 230000003628 erosive effect Effects 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 238000005342 ion exchange Methods 0.000 description 2
- 239000002957 persistent organic pollutant Substances 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 239000010453 quartz Substances 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 239000010457 zeolite Substances 0.000 description 2
- 241000251468 Actinopterygii Species 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 229920000742 Cotton Polymers 0.000 description 1
- 206010052804 Drug tolerance Diseases 0.000 description 1
- 241000588724 Escherichia coli Species 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 150000001342 alkaline earth metals Chemical class 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000001580 bacterial effect Effects 0.000 description 1
- 210000000476 body water Anatomy 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 230000001186 cumulative effect Effects 0.000 description 1
- 239000010840 domestic wastewater Substances 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000005485 electric heating Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 230000026781 habituation Effects 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 231100001240 inorganic pollutant Toxicity 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 230000003641 microbiacidal effect Effects 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 230000001766 physiological effect Effects 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 230000035755 proliferation Effects 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 210000002700 urine Anatomy 0.000 description 1
- 210000004885 white matter Anatomy 0.000 description 1
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Biological Treatment Of Waste Water (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は生活用水、%に浴用水の循環浄化装置に関する
。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a circulating purification device for domestic water, especially bath water.
浴用水け、体毛、生体表面の垢、脂肪、&ん白。 Bath water, body hair, dirt on living surfaces, fat, and white matter.
尿2色素類、臭気物質若しくは菌体等の有機汚染物質又
は生体に付着している塵埃、土砂若しくは設備や配管か
ら生ずるスケール、鉄錆、湯垢等の無機汚染物質の混入
によって、濁度の上昇、臭気の発生を招来し、不快感を
呈する。このため一般に多人数の入浴が行われる業務用
浴槽等では、従来から第3図に示すように、浴槽1から
ストレーナ5.循環ポンプ6、 ill過器7及び熱交
換器9を通って当該水槽1に至る経路を導管3で結合し
、浴用水2を矢印方向4に循環浄化する装置を備え、可
能な限り浴用水の交換までの期間の延長を図っているの
が実状である。Turbidity increases due to the contamination of organic pollutants such as urine pigments, odorous substances, or bacterial cells, or inorganic pollutants such as dust, dirt, scale, iron rust, and hot water adhering to living organisms such as scale, iron rust, and hot water from equipment and piping. , resulting in the generation of odor and discomfort. For this reason, in commercial bathtubs where a large number of people take a bath, conventionally, as shown in FIG. 3, a strainer 5. A path through a circulation pump 6, an ill filter 7, and a heat exchanger 9 to reach the water tank 1 is connected by a conduit 3, and a device is provided to circulate and purify the bath water 2 in the direction of the arrow 4, to purify the bath water as much as possible. The reality is that efforts are being made to extend the period until replacement.
上記従来の装置では、濾過能力に限界があり、浴用水に
溶解した汚染物質や菌体の除去効果は不十分で、水質は
次第に悪化する。したがって浴用水の長期間の使用は期
待できず、少くとも3〜10日間に1度の水の交換を余
儀なくされていた。この水の交換頻度の高さは、節水、
省エネルギー。The above-mentioned conventional devices have a limited filtration capacity, are insufficient in removing pollutants and bacteria dissolved in bath water, and water quality gradually deteriorates. Therefore, bathing water cannot be expected to be used for a long period of time, and the water must be replaced at least once every 3 to 10 days. This high frequency of water exchange saves water and
Energy Conservation.
労力の削減といった維持管理上、極めて太き表問題であ
った。This was an extremely serious issue in terms of maintenance and management, such as reducing labor.
〔問題点を解決するための手段]
本発明は上記従来の問題点を解決し、浴用水の交換を長
期間に亙って必要とせず、常に快適々入浴ができる、水
の循環浄化装置を供することを目的とする。[Means for Solving the Problems] The present invention solves the above conventional problems and provides a water circulation purification device that does not require replacing bath water for a long period of time and allows comfortable bathing at all times. The purpose is to provide
第1図は本発明に係る水の循環浄化装置を示す経路図で
、導管3で結合した、浴槽1からストレーナ5.循環ポ
ンプ6、濾過器7及び熱交換器9を通って当該浴IW1
に至る経路中、濾過器7の後に、微生物反応器旦を介在
せl−めたものである。FIG. 1 is a route diagram showing a water circulation purification device according to the present invention, from a bathtub 1 to a strainer 5, which are connected by a conduit 3. The bath IW1 passes through a circulation pump 6, a filter 7 and a heat exchanger 9.
A microbial reactor is interposed after the filter 7 during the route leading to the filter.
浴用水2中の汚染物質は、ストレーナ5において、体毛
或いは繊維物質など大きな固体混入物が除去された後、
循環ポンプ6により濾過器7に送られ、垢、土砂、鉄錆
、湯垢などの小固体混入物が除去される。濾過器7の濾
材と[7ては、綿糸或いは化学繊維を円筒上に巻回した
安価な交換フィルターの使用が有効である。ストレーナ
5及び濾過器7を経た水は、次いで微生物反応器旦に導
かれる。Contaminants in the bath water 2 are removed in a strainer 5 after large solid contaminants such as body hair or fibrous substances are removed.
It is sent to a filter 7 by a circulation pump 6, and small solid contaminants such as scale, earth and sand, iron rust, and hot water are removed. It is effective to use an inexpensive replacement filter made of cotton thread or chemical fiber wound around a cylinder as the filter material of the filter 7. The water that has passed through the strainer 5 and filter 7 is then led to the microbial reactor.
微生物反応器旦は、第2図の拡大断面図に示すように、
下部及び上部に入口10及び出口11を有する容器12
中に1アルミノ珪酸塩を主成分とする天然石から々る担
体13を充填したものである。アルミノ珪酸塩を主成分
とする天然石は、石英斑岩或いは凝灰岩(例えば沸石)
として一般に豊富に産出するものであり、具体的にはア
ルカリ及びアルカリ土類金属を含む結晶性アルミノ珪酸
塩であるゼオライト等が挙げられる。これらは水に対す
る耐侵食崩壊性が強く、物理吸着及びイオン交換能を有
する上、水中に懸濁した場合、そこかられずかに溶出し
てくる成分が微生物の生理活性に好適な場を提供し、好
気性菌から々る微生物14が相体表面に繁殖する。そし
て担体表面に着床した微生物は、自然増殖し安定した馴
養状態を維持するものである。As shown in the enlarged cross-sectional view of Figure 2, the microbial reactor is
Container 12 with an inlet 10 and an outlet 11 at the bottom and top
It is filled with a carrier 13 made of natural stone and containing 1-aluminosilicate as a main component. Natural stones mainly composed of aluminosilicate are quartz porphyry or tuff (e.g. zeolite)
It is generally produced in abundance, and specific examples include zeolite, which is a crystalline aluminosilicate containing alkali and alkaline earth metals. These materials have strong resistance to erosion and disintegration in water, and have physical adsorption and ion exchange capabilities, and when suspended in water, the components that slowly elute from the suspension provide a suitable field for the physiological activity of microorganisms. Microorganisms 14, including aerobic bacteria, proliferate on the surface of the phase body. The microorganisms that have settled on the surface of the carrier proliferate naturally and maintain a stable habituation state.
この微生物反応器中に充填された微生物固定化担体は、
吸着能及びイオン交換能によって水中の有機汚染物質を
吸着し、かつ表面に繁殖し友好気性微生物がこれを酸化
消化することによって自然増殖する、との相互依存の成
立のもとに1時間の経過とともに安定した浄化作用を生
じ、長期に亙って浄化能力を維持する。微生物反応器旦
で有機汚染物質が除去された水は、循環過程で放散した
熱量を補うため、熱交換器9に送られ、浴槽1に戻され
る。The microorganism immobilization carrier filled in this microorganism reactor is
The passage of one hour is based on the mutual dependence between organic pollutants in the water being adsorbed by adsorption capacity and ion exchange capacity, propagation on the surface, and natural proliferation as friendly microorganisms oxidize and digest them. Together with this, it produces a stable purifying effect and maintains its purifying ability over a long period of time. The water from which organic contaminants have been removed in the microbial reactor is sent to the heat exchanger 9 and returned to the bathtub 1 in order to compensate for the amount of heat dissipated during the circulation process.
なお微生物固定化相体は、水中で侵食などによる微粒化
崩壊現象がなく長期間安定して形状を維持するように、
モース硬度が3以上1粒径が4〜20111の本のが有
効である。また微生物反応器中の水流は、特定の流路を
形成することなく水が平均して充填材表面に行きわIP
:、多接触するよう、下端入口10より上端出口11に
向かう上向流とし、さらに流速は、充填材が水流で移動
することなく微生物の固定が安定に維持できること、好
気性微生物の活動に支障のない酸素供給を保つこと等の
ために、反応器の出口で〔循環水量×(2〜6)〕ダH
1の範囲に調整されると好結果が得られる。The microorganism-immobilized phase body is designed to maintain its shape stably for a long period of time without becoming atomized or disintegrating due to erosion etc. in water.
Those having a Mohs hardness of 3 or more and a grain size of 4 to 20111 are effective. In addition, the water flow in the microbial reactor is such that water reaches the surface of the filler on average without forming a specific flow path.
: The flow is upward from the lower end inlet 10 to the upper end outlet 11 to ensure multiple contact, and the flow velocity is such that the fixation of microorganisms can be stably maintained without the filling material being moved by the water flow, and that it will hinder the activity of aerobic microorganisms. In order to maintain an oxygen supply free of water, etc., at the outlet of the reactor,
Good results can be obtained if the value is adjusted within the range of 1.
容量が2−の浴槽IK、多数の円形流通孔を有する円筒
からなるストレーナ5を設け、循環用ポンプ6として1
馬力の汎用ポンプを用いた。濾過器7は、繊維を巻回し
た公称75ミクロンの交換式フィルターを濾過面積がo
、sfi”になるようにセットした吃のを設けた。微生
物反応器旦は、容器に粒径が約10箇璽の石英斑岩を5
0f充填し、有機汚染物質を消化する好気性微生物が担
体表面に自然増殖した状態とした。熱交換器9は電熱式
のものを設け、経路全体を呼び径40Aの鋼管で結んだ
。浴用水2を上記経路に循環せしめ、特に微生物反応器
、q中の水の流れは上向流とし、反応器出口の流量は4
〜12袷乍、の範囲に調整した。A bathtub IK with a capacity of 2-, a strainer 5 made of a cylinder having a large number of circular circulation holes, and a circulation pump 6 of 1
A general-purpose horsepower pump was used. The filter 7 is a replaceable filter with a nominal diameter of 75 microns and has a filtration area of o.
, sfi'' was set. At the beginning of the microbial reactor, 5 pieces of quartz porphyry with a grain size of about 10 pieces was placed in the container.
The carrier was filled with 0f to allow aerobic microorganisms that digest organic contaminants to grow naturally on the surface of the carrier. The heat exchanger 9 was of an electric heating type, and the entire path was connected with a steel pipe having a nominal diameter of 40A. The bath water 2 is circulated through the above-mentioned path, and in particular, the flow of water in the microbial reactor, q, is an upward flow, and the flow rate at the reactor outlet is 4.
It was adjusted to a range of ~12 lines.
次表に本実施例の経時水質検査結果を示す。The following table shows the results of water quality tests over time in this example.
表 浴用水の軒時分析結果
表から明らかなように、初期から2.5年における水質
は、入浴者数の累積が1,6万人を越えたにもかかわら
ずほとんど変化なく、透明度に優れ、異臭異味は全くな
かった。またpHも中性に近く、大腸菌群数は陰性であ
った。上記経過中4カ月に1度の繊維巻フィルターの交
換のみで、水道法の規準を満足する結果を得た。これら
のことから、無循環で毎日浴用水を交換した場合に比較
1.で、水及びエネルギーに要する経費を半分以下に節
減し得た。As is clear from the table showing the results of the analysis of bathing water, the water quality has hardly changed in the 2.5 years since the beginning, despite the cumulative number of bathers exceeding 160,000, with excellent transparency. There was no strange odor or taste. The pH was also close to neutral, and the coliform count was negative. During the above process, the fiber-wound filter was replaced only once every four months, and results satisfying the standards of the Water Supply Law were obtained. Based on these facts, comparison 1. This reduced water and energy costs by more than half.
本発明の浄化装置によれば、ストレーナ5及び濾過器7
を経た水が、微生物反応器旦を通過するととにより、そ
れまでの経路で捕捉され得なかった、浴用水に溶解した
汚染物質や菌体が吸着浄化され、かつとれにより好気性
微生物が自然増殖するとの作用を繰返し、常に浴用水の
清浄を維持し得るものである。したがって濾過器のフィ
ルターの定期交換及び循環ポンプの定期点検の実施によ
υ、数年に及ぶ長期に亙って浴用水の交換を必要とせず
、節水、省エネルギー、清浄労力の削減等、大き々経済
効果が得られる。本装置は、公害の発生もなく、特に水
の不足する地域に設備して効果があり、社会的貢献度の
高いものである。なお、浴用水の浄化において注意を必
要とする大腸菌の除去のため、微生物反応器旦の後に、
殺菌作用のある銅、@、ニッケルあるいはこれらの合金
等の金属の細条又は粉末の層を設けておけば、より有効
である。According to the purification device of the present invention, the strainer 5 and the filter 7
When the water passes through the microbial reactor, pollutants and bacteria dissolved in the bathing water that could not be captured by the previous route are adsorbed and purified, and aerobic microorganisms naturally proliferate due to the removal. By repeating this action, the bath water can always be kept clean. Therefore, by regularly replacing the filter of the filter and periodically inspecting the circulation pump, there is no need to replace the bath water over a long period of several years, resulting in significant water savings, energy savings, and a reduction in cleaning labor. Economic effects can be obtained. This device does not cause any pollution, is particularly effective when installed in areas with water shortages, and has a high degree of social contribution. In addition, in order to remove Escherichia coli, which requires attention when purifying bath water, after the microbial reactor is used,
It is more effective to provide a layer of microbicidal metal strips or powder, such as copper, @, nickel, or alloys thereof.
本明細書においては、浴用水の循環浄化装置圧ついて説
明したが、他に魚槽水あるいは水耕載培用水の浄化再生
、さらには産業排水、生活排水の浄化過程の二次処理、
三次処理等にも本装置を利用し得ることは勿論である。In this specification, the circulation purification system pressure for bath water has been explained, but it is also used for purification and regeneration of fish tank water or water for hydroponic cultivation, as well as secondary treatment in the purification process of industrial wastewater and domestic wastewater.
Of course, this device can also be used for tertiary processing.
第1図は本発明の水の循環浄化装置の循環経路を示す系
統図、第2図は同要部拡大断面図である。
第5図は従来装置の水の循環経路を示す系統図である。
2・・・水、5・・・ストレーナ、6・・循環ポンプ、
7・・・濾過器、旦・・・微生物反応器、9・・・熱交
換器、13・・・担体、14・・・好気性微生物。
第 1 図
第 2 図
第 3 図
手続補正書(方式)
%式%
2発明の名称
水の循環浄化装置
3、補正をする者
事件との関係 特許出願人
住所 東京都新宿区大久保1丁目6番21号電話(03
) 202−2121
のとおり(内容に変更なし)FIG. 1 is a system diagram showing a circulation path of the water circulation purification device of the present invention, and FIG. 2 is an enlarged sectional view of the same essential parts. FIG. 5 is a system diagram showing the water circulation path of the conventional device. 2...Water, 5...Strainer, 6...Circulation pump,
7... Filter, Dan... Microorganism reactor, 9... Heat exchanger, 13... Carrier, 14... Aerobic microorganism. Figure 1 Figure 2 Figure 3 Procedural amendment (method) % formula % 2 Name of the invention Water circulation purification device 3, Relationship with the person making the amendment Patent applicant address 1-6 Okubo, Shinjuku-ku, Tokyo Telephone number 21 (03
) As per 202-2121 (no change in content)
Claims (1)
って当該水槽へ水を循環浄化する装置において、上記経
路に、 (a)アルミノ珪酸塩を主成分とする担体に、好気性菌
からなる微生物を着床させ、 (b)この微生物が自然増殖し安定した馴養状態を維持
するような、 微生物固定化担体が充填された微生物反応器を介在せし
めたことを特徴とする水の循環浄化装置。 2、微生物反応器中の微生物固定化担体のモース硬度が
3以上、粒径が4〜20mmである特許請求の範囲第1
項記載の水の循環浄化装置。 3、微生物反応器中の水の流れが上向流であって、反応
器出口の流量が〔循環水量×(2〜6)〕m^3/H_
rの範囲にある特許請求の範囲第1項または第2項記載
の水の循環浄化装置。 4、微生物反応器の後に、殺菌作用のある金属の細条又
は粉末の層を設けた特許請求の範囲第1項、第2項また
は第3項記載の水の循環浄化装置。[Scope of Claims] 1. In an apparatus for circulating and purifying water from a water tank to the water tank through a strainer, a circulation pump, and a filter, the above path includes: (a) a carrier mainly composed of aluminosilicate; A microorganism reactor filled with a microorganism immobilization carrier that allows microorganisms consisting of aerobic bacteria to implant and (b) allows the microorganisms to grow naturally and maintain a stable acclimated state is interposed. Water circulation purification device. 2. Claim 1, wherein the microorganism immobilization carrier in the microorganism reactor has a Mohs hardness of 3 or more and a particle size of 4 to 20 mm.
The water circulation purification device described in section. 3. The flow of water in the microbial reactor is an upward flow, and the flow rate at the reactor outlet is [circulating water amount x (2 to 6)] m^3/H_
The water circulation purification device according to claim 1 or 2, which falls within the range of r. 4. The water circulation purification device according to claim 1, 2 or 3, wherein a layer of metal strips or powder having a sterilizing effect is provided after the microbial reactor.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61087796A JPS62244493A (en) | 1986-04-16 | 1986-04-16 | Apparatus for recirculating and purifying water |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61087796A JPS62244493A (en) | 1986-04-16 | 1986-04-16 | Apparatus for recirculating and purifying water |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS62244493A true JPS62244493A (en) | 1987-10-24 |
Family
ID=13924940
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP61087796A Pending JPS62244493A (en) | 1986-04-16 | 1986-04-16 | Apparatus for recirculating and purifying water |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS62244493A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01139186A (en) * | 1987-11-26 | 1989-05-31 | Matsushita Electric Ind Co Ltd | Sterilizing and purifying equipment for water |
JPH01189387A (en) * | 1988-01-25 | 1989-07-28 | Matsushita Electric Ind Co Ltd | Apparatus for sterilizing and purifying water |
JPH05192677A (en) * | 1990-12-18 | 1993-08-03 | Raizaa Kogyo Kk | Microorganism treating device for waste water |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5277881A (en) * | 1975-12-23 | 1977-06-30 | Toyobo Co Ltd | Catalytic oxidation |
JPS5428671A (en) * | 1977-08-05 | 1979-03-03 | Hachirou Hirota | Unbalanced log |
JPS595037A (en) * | 1982-07-02 | 1984-01-11 | Agency Of Ind Science & Technol | Manufacture of porous tetrafluoroethylene resin |
-
1986
- 1986-04-16 JP JP61087796A patent/JPS62244493A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5277881A (en) * | 1975-12-23 | 1977-06-30 | Toyobo Co Ltd | Catalytic oxidation |
JPS5428671A (en) * | 1977-08-05 | 1979-03-03 | Hachirou Hirota | Unbalanced log |
JPS595037A (en) * | 1982-07-02 | 1984-01-11 | Agency Of Ind Science & Technol | Manufacture of porous tetrafluoroethylene resin |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01139186A (en) * | 1987-11-26 | 1989-05-31 | Matsushita Electric Ind Co Ltd | Sterilizing and purifying equipment for water |
JPH01189387A (en) * | 1988-01-25 | 1989-07-28 | Matsushita Electric Ind Co Ltd | Apparatus for sterilizing and purifying water |
JPH05192677A (en) * | 1990-12-18 | 1993-08-03 | Raizaa Kogyo Kk | Microorganism treating device for waste water |
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