JPH05131200A - Sea water purification device - Google Patents

Sea water purification device

Info

Publication number
JPH05131200A
JPH05131200A JP3294106A JP29410691A JPH05131200A JP H05131200 A JPH05131200 A JP H05131200A JP 3294106 A JP3294106 A JP 3294106A JP 29410691 A JP29410691 A JP 29410691A JP H05131200 A JPH05131200 A JP H05131200A
Authority
JP
Japan
Prior art keywords
water
bacteria
seawater
seawater purification
purification device
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP3294106A
Other languages
Japanese (ja)
Inventor
Keiko Nakanishi
圭子 中西
Masao Maki
正雄 牧
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP3294106A priority Critical patent/JPH05131200A/en
Publication of JPH05131200A publication Critical patent/JPH05131200A/en
Pending legal-status Critical Current

Links

Classifications

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

Landscapes

  • Biological Treatment Of Waste Water (AREA)
  • Treatment Of Biological Wastes In General (AREA)
  • Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
  • Physical Water Treatments (AREA)
  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
  • Farming Of Fish And Shellfish (AREA)

Abstract

PURPOSE:To obtain a compact sea water purification device capable of increasing the activity of water-purifying microbe by using an air feed technique which does not allow physical stimulation in a domestic or a commercial sea water purification device for purifying water in a brine aquarium. CONSTITUTION:The subject sea water purification device is equipped with a pressurized water feed means 4, a brine purification module 6, an air feed means 7 for feeding air to water-purifying microbe in the brine purification module so as to minimize physical stimulation, and an ultraviolet emission device 10. Thus it is possible to enhance the activity of aerophilic microbe which decomposes harmful ammonia secreted by fish by oxygen to harmless nitric acid. In addition, pathogenic bacteria proliferated in the water tank for fish can be exterminated using the ultraviolet emission device.

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、観賞魚用水槽の水、魚
の養殖用水などの海水を浄化する家庭用もしくは業務用
海水浄化装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a domestic or commercial seawater purification device for purifying seawater such as water in an aquarium for aquarium or water for fish culture.

【0002】[0002]

【従来の技術】従来この種の海水浄化装置は図9のよう
な構造になっている。図9において、水槽16内の水は
オーバーフローパイプ17を経由して海水浄化槽18で
ろ材19によって水の浄化を行い、ポンプ20で水槽1
6に戻される。なお21は水槽16とポンプ20を接続
するパイプである。なお、酸素補給など水浄化槽でのバ
クテリア活性を増進させる手段や病原菌等の殺菌手段が
備えられていない。
2. Description of the Related Art Conventionally, this type of seawater purifying apparatus has a structure as shown in FIG. In FIG. 9, the water in the water tank 16 is purified by the seawater purifying tank 18 by the filter medium 19 through the overflow pipe 17, and the water in the water tank 1 by the pump 20.
Returned to 6. Reference numeral 21 is a pipe connecting the water tank 16 and the pump 20. It should be noted that there is no means for enhancing the bacterial activity in the water purification tank, such as supplementing oxygen, or sterilizing means for pathogenic bacteria.

【0003】[0003]

【発明が解決しようとする課題】一般に、観賞魚水槽に
おいて、水槽水中には魚の代謝作用と食べ残しの餌の分
解と排泄物等が原因でアンモニアや汚れの発生、病原菌
の繁殖等の課題がある。さらにアンモニア等の窒素化合
物が分解する過程で発生する亜硝酸も魚毒性があり、大
きな課題であった。
Generally, in an aquarium fish tank, there are problems such as generation of ammonia and stains and propagation of pathogenic bacteria in the aquarium water due to the metabolic action of fish, decomposition of uneaten food and excrement. is there. Furthermore, nitrous acid generated in the process of decomposing nitrogen compounds such as ammonia has fish toxicity, which is a big problem.

【0004】これらの課題を一部解決しようとしたもの
として従来例に示すようにオーバーフロー式の下置海水
浄化槽が提案されている。
As an attempt to partially solve these problems, an overflow-type subsea water purification tank has been proposed as shown in a conventional example.

【0005】しかしながら、従来例において海水を浄化
する海水浄化槽でのろ材としてはカキの貝殻、サンゴ砂
等があるがこれらを用いた場合では効率が悪く、その結
果、海水浄化槽の大きさが大きくなるという課題と海水
浄化用のバクテリアは物理的な刺激に弱く、好気性細菌
には物理的刺激のない酸素供給が必要とされるという課
題があった。
However, in the conventional example, as a filter medium in a seawater purification tank for purifying seawater, there are oyster shells, coral sand, etc., but when these are used, the efficiency is low and, as a result, the size of the seawater purification tank becomes large. However, there is a problem that bacteria for seawater purification are weak against physical stimulation, and aerobic bacteria require oxygen supply without physical stimulation.

【0006】本発明では、コンパクトな海水浄化装置を
提供することを第1の目的としている。
The first object of the present invention is to provide a compact seawater purification device.

【0007】第2の目的は物理的刺激の少ない酸素供給
手段を用い、海水浄化槽の好気性細菌を効果的に繁殖さ
せ浄化性能をより高めることとする。
A second object is to use oxygen supplying means with less physical irritation to effectively propagate aerobic bacteria in the seawater purification tank and further improve the purification performance.

【0008】[0008]

【課題を解決するための手段】上記目的を達成するため
に、本発明は、塩基性物質が主成分とする鉱物質から成
る海水浄化モジュルと、海水浄化モジュル中の好気性へ
の空気供給手段と、紫外線照射装置を水の強制循環流路
に配置し、さらに前記海水浄化モジュルに人工培養した
好気性細菌と嫌気性細菌を大量に繁殖させたものであ
る。
In order to achieve the above object, the present invention provides a seawater purification module comprising a mineral substance containing a basic substance as a main component, and a means for supplying aerobic air in the seawater purification module. An ultraviolet irradiation device is arranged in the forced circulation channel of water, and a large amount of artificially cultivated aerobic bacteria and anaerobic bacteria are further propagated in the seawater purification module.

【0009】[0009]

【作用】本発明の海水浄化装置は、海水浄化モジュルに
内蔵する個々のセラミックを塩基性物質を主成分とする
材料で構成するとともに、最初から前記のセラミックに
人工培養した好気性細菌と嫌気性細菌を大量に繁殖させ
ており、好気性細菌への物理的刺激の少ない空気供給手
段を用いているので、魚の排泄する有害なアンモニアを
無害な硝酸に酸化分解する好気性細菌の活性を高めるこ
とができる。しかも硝酸が蓄積しても、セラミックの塩
基性成分によりPHの低下がなく、また、セラミックの
形状を断面トユ状とするとともに弓状に湾曲させかつ略
一定の寸法としたので、水流がセラミックのどの面に当
たっても水流方向に流れるのでセラミックによる抵抗が
極めて少なくなるとともに水流の抵抗値のバラツキが少
なくなる。また、水槽中で繁殖した魚の病原菌は、紫外
線照射装置により死滅する。
In the seawater purification apparatus of the present invention, the individual ceramics contained in the seawater purification module are made of a material containing a basic substance as a main component, and the aerobic bacteria and anaerobic bacteria artificially cultured on the ceramics from the beginning. Since a large amount of bacteria are propagated and an air supply means that does not cause physical irritation to aerobic bacteria is used, the activity of aerobic bacteria that oxidize and decompose harmful ammonia excreted by fish into harmless nitric acid is enhanced. You can Moreover, even if nitric acid accumulates, the PH does not decrease due to the basic component of the ceramic, and since the shape of the ceramic is a tow-shaped cross section and is curved in an arc shape and has a substantially constant size, the water flow of the ceramic is Since any surface will flow in the water flow direction, the resistance of the ceramic will be extremely small and the variation in the resistance value of the water flow will be small. In addition, the pathogenic bacteria of the fish propagated in the aquarium are killed by the ultraviolet irradiation device.

【0010】このように、水槽中の水は殺菌浄化され常
に正常な状態に保たれる。
As described above, the water in the water tank is sterilized and purified, and is always kept in a normal state.

【0011】[0011]

【実施例】以下、本発明の一実施例を添え付け図面に基
づいて説明する。図1は本発明の海水浄化装置を応用し
た観賞魚水槽の外観図、図2は同観賞魚用水槽の構成原
理図である。図1、図2において、1は水槽、2は水槽
の台で、内部に海水浄化ユニット3が内蔵されている。
海水浄化ユニット3は水圧送手段である循環ポンプ4、
鉱物質5からなる微生物固定担体を内蔵した海水浄化モ
ジュル6、イジェクター作用により外部空気を流水中に
導入する空気供給手段7、ヒータ8、紫外線ランプ9が
取り付けられた紫外線照射装置10とこれらをつなぐ強
制循環流路11を基本構成要素としている。強制循環流
路11からの清浄化された海水は、水槽1へ送られる。
12はエアセパレータで、空気供給手段で吸引された微
細な気泡を分離するものである。
An embodiment of the present invention will be described below with reference to the accompanying drawings. FIG. 1 is an external view of an aquarium fish tank to which the seawater purification apparatus of the present invention is applied, and FIG. 2 is a structural principle diagram of the aquarium fish tank. In FIGS. 1 and 2, reference numeral 1 is a water tank, 2 is a base of the water tank, and a seawater purification unit 3 is incorporated therein.
The seawater purification unit 3 is a circulation pump 4 which is a water pressure feeding means,
A seawater purification module 6 containing a microbial immobilization carrier made of a mineral substance 5, an air supply means 7 for introducing outside air into running water by an ejector action, a heater 8, and an ultraviolet irradiation device 10 to which an ultraviolet lamp 9 is attached, and these are connected. The forced circulation flow path 11 is a basic constituent element. The purified seawater from the forced circulation channel 11 is sent to the aquarium 1.
An air separator 12 separates fine air bubbles sucked by the air supply means.

【0012】図3は空気供給手段7の断面図である。図
3において、13は循環流を高速化する供給ノズル、1
4は高速ジェット流の吸引作用により空気が流入する空
気流入口、15は吸引された空気と循環流との混合流が
流出する流出路である。この混合流には酸素が多く溶け
こみ、水槽1の海水や水浄化モジュル6に流入する海水
の溶存酸素は常に飽和状態になる。水槽1の海水の溶存
酸素は飽和状態なので、従来の水槽で行われている空気
ポンプによるエアレーションが不必要になる。また海水
浄化モジュル6に流入する海水の溶存酸素は飽和状態と
なり鉱物質5の表面に繁殖している好気性細菌は物理的
刺激のない状態で酸素を取り入れることが出来るため、
好気性細菌の活性が高くなる。好気性細菌の働きにより
水中のアンモニアは魚に無害な硝酸塩にまで酸化分解さ
れる。アンモニアの硝酸塩への酸化分解反応を次に示
す。
FIG. 3 is a sectional view of the air supply means 7. In FIG. 3, 13 is a supply nozzle for speeding up the circulation flow, and 1
Reference numeral 4 is an air inlet through which air flows in by the suction action of the high-speed jet stream, and 15 is an outflow passage through which a mixed flow of the sucked air and the circulation flow out. A large amount of oxygen is dissolved in this mixed flow, and the dissolved oxygen in the seawater in the water tank 1 or the seawater flowing into the water purification module 6 is always saturated. Since the dissolved oxygen in the seawater in the water tank 1 is saturated, the aeration by the air pump, which is performed in the conventional water tank, becomes unnecessary. Further, the dissolved oxygen of seawater flowing into the seawater purification module 6 becomes saturated, and aerobic bacteria growing on the surface of the mineral matter 5 can take in oxygen without physical stimulation.
Increases the activity of aerobic bacteria. Due to the action of aerobic bacteria, ammonia in water is oxidatively decomposed into nitrate, which is harmless to fish. The oxidative decomposition reaction of ammonia into nitrate is shown below.

【0013】 NH4 + +1.5O2 →NO2 - +H2 O+2H+ …………… NO2 - +0.5O2 →NO3 - ………………………………… 図4は、本発明の海水浄化モジュル6に内蔵する鉱物質
5の側面図、図5は、図4のa−b断面図である。本発
明の鉱物質5は、図4に示すように断面トユ状としてい
るとともに図4に示すように弓状に湾曲させている。し
たがって鉱物質5が重なり合い水に接触しない部分が生
じる事がなく、海水浄化モジュル内での水との接触面積
も最も広くでき、また微生物の培養できる面積も最も広
くできる。
NH 4 + + 1.5O 2 → NO 2 + H 2 O + 2H + ………… NO 2 + 0.5O 2 → NO 3 ……………………………………… FIG. 5 is a side view of the mineral substance 5 contained in the seawater purification module 6 of the present invention, and FIG. 5 is a sectional view taken along line ab of FIG. As shown in FIG. 4, the mineral substance 5 of the present invention has a tow-shaped cross section and is curved in an arc shape as shown in FIG. Therefore, there is no part where the mineral matter 5 overlaps and does not come into contact with water, the contact area with water in the seawater purification module can be maximized, and the area where microorganisms can be cultured can also be maximized.

【0014】図6は、上記鉱物質5の斜視図であり、こ
の形状から見ても水がどの方向から当たっても水流方向
に向かう。したがって、海水浄化モジュル内の鉱物質5
による抵抗が極めて少なくなる。上記海水浄化モジュル
6に内蔵する個々の鉱物質5は、高炉水砕を原料として
用いた。この高炉水砕は、製鉄所の溶鉱炉から溶鉄1ト
ン当たり0.5トン発生するスラグを急冷して製造さ
れ、主にセメントの原料や土壌改良材として使用されて
いるものである。高炉水砕は、多孔質のガラス室に焼成
され(表1)に示すようにCaO、SiO2 、Al2
3 、MgOなどが主成分である。
FIG. 6 is a perspective view of the above-mentioned mineral matter 5, and in view of this shape, no matter which direction water hits, it goes in the water flow direction. Therefore, 5 minerals in the seawater purification module
The resistance due to is extremely reduced. As for the individual mineral substances 5 contained in the seawater purification module 6, blast furnace water granulation was used as a raw material. This blast furnace granulation is produced by rapidly cooling slag generated from a blast furnace of an iron mill at a rate of 0.5 ton per 1 ton of molten iron, and is mainly used as a raw material for cement and a soil improving material. Water-granulated blast furnace is, CaO as shown in calcined in a glass chamber of the porous (Table 1), SiO 2, Al 2 O
3 and MgO are the main components.

【0015】[0015]

【表1】 [Table 1]

【0016】このようにCaOが主成分であるので、前
述の反応式でNO3 - が生成してもPHの低下がおこ
らない。また、各地のPHの低い水を使用しても前述の
CaOで中和できるので水を浄化する微生物の活性を向
上させることができる。
As described above, since CaO is the main component, the pH does not decrease even if NO 3 is produced in the above reaction formula. Further, even if water with low pH is used in various places, it can be neutralized with CaO described above, so that the activity of microorganisms for purifying water can be improved.

【0017】さらに、CaOなどが主成分である鉱物質
5の表面には、水のなかでカルシウムなどの2価のプラ
スイオンが沢山存在する。一方、微生物は、マイナスに
荷電されているので水を浄化する微生物が鉱物質5に付
着しやすいので、鉱物質5は微生物の固定床として最適
である。
Further, on the surface of the mineral substance 5 containing CaO or the like as a main component, many divalent positive ions such as calcium exist in the water. On the other hand, since the microorganisms are negatively charged and water-purifying microorganisms easily attach to the mineral matter 5, the mineral matter 5 is most suitable as a fixed bed of microorganisms.

【0018】また、水槽1中に繁殖した魚の病原菌は前
記紫外線照射装置10の紫外線で殺菌される。更に、前
記紫外線照射装置10の紫外線は遊離塩素を除去する作
用も有し、魚の飼育環境をより高める働きをしている。
The pathogenic bacteria of the fish propagated in the aquarium 1 are sterilized by the ultraviolet rays of the ultraviolet irradiation device 10. Further, the ultraviolet rays of the ultraviolet irradiation device 10 also have a function of removing free chlorine, and have a function of further enhancing the environment for raising fish.

【0019】次に、観賞魚用水槽の水を循環する強制循
環流路11に塩基性物質を主成分とする鉱物質から成る
海水浄化モジュルと、空気供給手段と、紫外線照射装置
を配置した海水の殺菌浄化システムに海水浄化用バクテ
リアの人工培養菌とバクテリア活性化物質を使用した海
水浄化装置における海水浄化モジュル中の鉱物質表面に
繁殖した好気性細菌へ物理的刺激のない酸素供給法を用
いた本発明の海水浄化装置の効果を下記の実験で判定し
た。
Next, in the forced circulation channel 11 for circulating the water in the aquarium for aquarium fish, seawater purification module composed of a mineral substance containing a basic substance as a main component, air supply means, and seawater in which an ultraviolet irradiation device is arranged. The oxygen supply method without physical irritation to the aerobic bacteria propagated on the surface of the minerals in the seawater purification module in the seawater purification device using the artificial culture bacteria of seawater purification bacteria and the bacteria activator for the sterilization and purification system of The effect of the present seawater purifying apparatus of the present invention was determined by the following experiment.

【0020】実験は50lの水槽水(27℃)を2.5
ml/minの循環流量で流し、アンモニア態窒素を1
1mg/日で添加した。海水浄化モジュルには3lの前
記鉱物質に海水浄化用バクテリアの人工培養菌を繁殖さ
せておいた。空気供給手段を海水浄化モジュルの上流に
配置した場合と、下流に配置した場合の水槽水中のアン
モニア態窒素、亜硝酸態窒素、硝酸態窒素の濃度変化を
測定した。
The experiment was conducted using 50 l of aquarium water (27 ° C.) for 2.5 hours.
Flow at a circulating flow rate of ml / min, and add ammonia nitrogen to 1
Added at 1 mg / day. In the seawater purification module, an artificial culture of seawater purification bacteria was propagated in 3 liters of the above mineral substances. Changes in the concentrations of ammonia nitrogen, nitrite nitrogen, and nitrate nitrogen in the aquarium water were measured when the air supply means was placed upstream and downstream of the seawater purification module.

【0021】空気供給手段を海水浄化モジュルの上流に
配置した場合の水槽水中のアンモニア態窒素、亜硝酸態
窒素、硝酸態窒素の濃度変化を図7に示す。
FIG. 7 shows changes in the concentrations of ammonia nitrogen, nitrite nitrogen and nitrate nitrogen in the aquarium water when the air supply means is arranged upstream of the seawater purification module.

【0022】空気供給手段を海水浄化モジュルの下流に
配置した場合(本発明の海水浄化装置)の水槽水中のア
ンモニア態窒素、亜硝酸態窒素、硝酸態窒素の濃度変化
を図8に示す。
FIG. 8 shows changes in the concentrations of ammonia nitrogen, nitrite nitrogen and nitrate nitrogen in the aquarium water when the air supply means is arranged downstream of the seawater purification module (seawater purification apparatus of the present invention).

【0023】図7より空気供給手段を海水浄化モジュル
の上流に配置した場合の水槽水中のアンモニア態窒素は
15日で検出されなくなり、亜硝酸態窒素は30日目で
も増加している。
As shown in FIG. 7, when the air supply means is arranged upstream of the seawater purification module, ammonia nitrogen in the aquarium water is not detected in 15 days, and nitrite nitrogen is increased even in 30 days.

【0024】図8より空気供給手段を海水浄化モジュル
の下流に配置した場合の水槽水中のアンモニア態窒素は
初日から検出されず、亜硝酸態窒素は15日で検出され
なくなっている。
As shown in FIG. 8, when the air supply means is arranged downstream of the seawater purification module, ammonia nitrogen in the aquarium water is not detected from the first day, and nitrite nitrogen is not detected in 15 days.

【0025】[0025]

【発明の効果】以上本発明の海水浄化装置を用いると次
の効果を用いることが出来る。 (1)空気供給手段を海水浄化モジュルの下流に設けて
いるため、海水浄化モジュルに内蔵されている鉱物質の
表面に繁殖している好気性細菌が物理的刺激の少ない状
態で酸素を取り入れる事ができるので、細菌の活性が高
くなる。 (2)一般に鉱物質の形状としては、球形とか円筒状と
か板状とかが考えられるが、同じ鉱物質の体積で表面積
が最も広いのは板状である。しかしながら板状のものを
海水浄化モジュルに内蔵した場合は、鉱物質が重なり合
い水に接触しない部分が生じる可能性がある。本発明の
鉱物質は、板状の物をトユ状とし、かつ弓状に湾曲させ
ているので重なり合うことがなく、海水浄化モジュル内
での水との接触面積も最も広くできる。また、水流が鉱
物質のどの面に当たっても水流方向に流れるので鉱物質
による抵抗が極めて少なくなるので、強制循環用のポン
プの出力が小型でよく、また消費電力の少ない海水浄化
装置が得られる。さらに、個々の鉱物質の端部で接触し
て積み重ねられるので部分部分による水流の抵抗値のバ
ラツキが少なく、海水浄化モジュル内の水の流れが均一
化する。したがって浄化モジュル内で微生物が広い面積
で均一に培養できるので効率の良い水浄化装置とするこ
とができる。その結果小型コンパクトにすることができ
る。
The following effects can be obtained by using the seawater purifying apparatus of the present invention. (1) Since the air supply means is provided downstream of the seawater purification module, the aerobic bacteria that propagate on the surface of the minerals contained in the seawater purification module must take in oxygen with little physical irritation. Therefore, the activity of bacteria is increased. (2) Generally, the shape of the mineral matter may be spherical, cylindrical, or plate-like, but the plate-like one has the largest surface area with the same volume of mineral matter. However, when a plate-shaped one is built into the seawater purification module, there is a possibility that some minerals may overlap and some parts may not come into contact with water. The mineral substance of the present invention has a toy-like plate-like material and is curved in an arc shape so that it does not overlap with each other, and the contact area with water in the seawater purification module can be maximized. Moreover, since the resistance of the mineral matter is extremely small because the water stream flows in the direction of the water stream regardless of which surface of the mineral matter hits, the output of the pump for forced circulation can be small, and a seawater purification device with low power consumption can be obtained. Furthermore, since the end portions of the individual minerals are stacked in contact with each other, variations in the resistance value of the water flow due to the partial portions are small, and the water flow in the seawater purification module is made uniform. Therefore, the microorganisms can be uniformly cultivated in a wide area in the purification module, so that an efficient water purification device can be obtained. As a result, it can be made compact and compact.

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

【図1】本発明の一実施例における海水浄化装置の外観
斜視図
FIG. 1 is an external perspective view of a seawater purification device according to an embodiment of the present invention.

【図2】同海水浄化装置の構成断面図FIG. 2 is a sectional view of the structure of the seawater purification device.

【図3】図2の空気供給手段の断面図FIG. 3 is a sectional view of the air supply means of FIG.

【図4】本発明の海水浄化装置の水浄化モジュルに内蔵
する鉱物質の側面図
FIG. 4 is a side view of mineral substances contained in the water purification module of the seawater purification device of the present invention.

【図5】図4のa−b断面図5 is a sectional view taken along the line ab of FIG.

【図6】鉱物質の斜視図FIG. 6 is a perspective view of mineral matter.

【図7】空気供給手段を海水浄化モジュル上流に設けた
ときの濃度変化図
FIG. 7: Concentration change diagram when air supply means is provided upstream of the seawater purification module

【図8】空気供給手段を海水浄化モジュル下流に設けた
ときの濃度変化図
FIG. 8 is a concentration change diagram when an air supply unit is provided downstream of the seawater purification module.

【図9】従来の海水浄化装置の構成図FIG. 9 is a block diagram of a conventional seawater purification device.

【符号の説明】[Explanation of symbols]

3 海水浄化ユニット 4 水圧送手段 5 鉱物質 6 海水浄化モジュル 7 空気供給手段 10 紫外線照射装置 3 Sea Water Purification Unit 4 Water Pressure Feeding Means 5 Minerals 6 Sea Water Purification Module 7 Air Supply Means 10 Ultraviolet Irradiation Device

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.5 識別記号 庁内整理番号 FI 技術表示箇所 C02F 3/10 Z 6647−4D 3/20 Z 3/34 101 D 7158−4D ─────────────────────────────────────────────────── ─── Continuation of front page (51) Int.Cl. 5 Identification code Office reference number FI technical display location C02F 3/10 Z 6647-4D 3/20 Z 3/34 101 D 7158-4D

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】水槽の水を循環する強制循環流路に、塩基
性物質を主成分とする鉱物質から成る海水浄化モジュル
と、空気供給手段と、紫外線照射装置を順次配置し、海
水殺菌浄化モジュルに海水浄化用バクテリアの人工培養
菌とバクテリア活性化物質を使用した海水浄化装置。
1. A seawater sterilizing and purifying apparatus, in which a seawater purification module composed of a mineral substance containing a basic substance as a main component, an air supply means, and an ultraviolet irradiation device are sequentially arranged in a forced circulation passage for circulating water in a water tank. A seawater purification device that uses artificially cultured bacteria of seawater purification bacteria and a bacteria activator as a module.
【請求項2】バクテリアとして好気性細菌、嫌気性細菌
の人工培養菌と、バクテリア活性化物質として非イオン
系界面活性剤を使用した請求項1記載の海水浄化装置。
2. The seawater purification apparatus according to claim 1, wherein artificial cultures of aerobic bacteria and anaerobic bacteria are used as bacteria, and a nonionic surfactant is used as a bacteria activating substance.
【請求項3】鉱物質は、カルシウムもしくはマグネシウ
ムの酸化物、ケイ酸塩、アルミン酸塩、炭酸塩の群より
選択した少なくとも一種を含むセラミックで、その形状
を断面トユ状とするとともに弓状に湾曲させかつ略一定
の寸法とした請求項1記載の海水浄化装置。
3. The mineral substance is a ceramic containing at least one selected from the group consisting of oxides of calcium or magnesium, silicates, aluminates, and carbonates, and its shape is cross-section touy and arcuate. The seawater purification device according to claim 1, which is curved and has a substantially constant size.
JP3294106A 1991-11-11 1991-11-11 Sea water purification device Pending JPH05131200A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3294106A JPH05131200A (en) 1991-11-11 1991-11-11 Sea water purification device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3294106A JPH05131200A (en) 1991-11-11 1991-11-11 Sea water purification device

Publications (1)

Publication Number Publication Date
JPH05131200A true JPH05131200A (en) 1993-05-28

Family

ID=17803369

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3294106A Pending JPH05131200A (en) 1991-11-11 1991-11-11 Sea water purification device

Country Status (1)

Country Link
JP (1) JPH05131200A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2002068345A1 (en) * 2001-02-26 2002-09-06 Fukuda, Hatsuo Oxygen-enriched water purifying plant
JP2004261698A (en) * 2003-02-28 2004-09-24 Ebara Corp Cleaning method for seawater and brackish water and apparatus therefor

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2002068345A1 (en) * 2001-02-26 2002-09-06 Fukuda, Hatsuo Oxygen-enriched water purifying plant
JP2004261698A (en) * 2003-02-28 2004-09-24 Ebara Corp Cleaning method for seawater and brackish water and apparatus therefor

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