JPH03296496A - Water purifying apparatus - Google Patents
Water purifying apparatusInfo
- Publication number
- JPH03296496A JPH03296496A JP2101377A JP10137790A JPH03296496A JP H03296496 A JPH03296496 A JP H03296496A JP 2101377 A JP2101377 A JP 2101377A JP 10137790 A JP10137790 A JP 10137790A JP H03296496 A JPH03296496 A JP H03296496A
- Authority
- JP
- Japan
- Prior art keywords
- water
- module
- ammonia
- flange
- water tank
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 91
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 22
- 239000001301 oxygen Substances 0.000 claims abstract description 22
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 22
- 238000000746 purification Methods 0.000 claims description 26
- 229910052500 inorganic mineral Inorganic materials 0.000 claims description 15
- 239000011707 mineral Substances 0.000 claims description 15
- 239000000463 material Substances 0.000 claims description 11
- 239000000758 substrate Substances 0.000 claims description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 abstract description 36
- 241000251468 Actinopterygii Species 0.000 abstract description 20
- 229910021529 ammonia Inorganic materials 0.000 abstract description 18
- 230000001954 sterilising effect Effects 0.000 abstract description 12
- 241001148470 aerobic bacillus Species 0.000 abstract description 7
- 241001148471 unidentified anaerobic bacterium Species 0.000 abstract description 7
- 229910002651 NO3 Inorganic materials 0.000 abstract description 6
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 abstract description 6
- 238000010438 heat treatment Methods 0.000 abstract description 6
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 abstract description 4
- 238000006864 oxidative decomposition reaction Methods 0.000 abstract description 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 abstract description 2
- 239000001257 hydrogen Substances 0.000 abstract description 2
- 229910052739 hydrogen Inorganic materials 0.000 abstract description 2
- 229910052757 nitrogen Inorganic materials 0.000 abstract description 2
- 239000000356 contaminant Substances 0.000 abstract 1
- 230000029142 excretion Effects 0.000 abstract 1
- 241000894006 Bacteria Species 0.000 description 11
- 238000004659 sterilization and disinfection Methods 0.000 description 11
- 238000009395 breeding Methods 0.000 description 10
- 230000001488 breeding effect Effects 0.000 description 10
- 239000005416 organic matter Substances 0.000 description 9
- 244000005700 microbiome Species 0.000 description 5
- 150000002823 nitrates Chemical class 0.000 description 5
- 244000052616 bacterial pathogen Species 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 238000000354 decomposition reaction Methods 0.000 description 3
- 235000013305 food Nutrition 0.000 description 3
- 230000000813 microbial effect Effects 0.000 description 3
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 2
- 102000004190 Enzymes Human genes 0.000 description 2
- 108090000790 Enzymes Proteins 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 2
- 239000012190 activator Substances 0.000 description 2
- 238000005273 aeration Methods 0.000 description 2
- 239000000919 ceramic Substances 0.000 description 2
- 239000000460 chlorine Substances 0.000 description 2
- 229910052801 chlorine Inorganic materials 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000008187 granular material Substances 0.000 description 2
- 238000005469 granulation Methods 0.000 description 2
- 230000003179 granulation Effects 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- 229910017604 nitric acid Inorganic materials 0.000 description 2
- 239000008213 purified water Substances 0.000 description 2
- 238000011144 upstream manufacturing Methods 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- 241000195493 Cryptophyta Species 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- IOVCWXUNBOPUCH-UHFFFAOYSA-M Nitrite anion Chemical compound [O-]N=O IOVCWXUNBOPUCH-UHFFFAOYSA-M 0.000 description 1
- IOVCWXUNBOPUCH-UHFFFAOYSA-N Nitrous acid Chemical compound ON=O IOVCWXUNBOPUCH-UHFFFAOYSA-N 0.000 description 1
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- -1 ammonia Chemical class 0.000 description 1
- 230000001580 bacterial effect Effects 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 201000010099 disease Diseases 0.000 description 1
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 1
- 210000003608 fece Anatomy 0.000 description 1
- 238000002513 implantation Methods 0.000 description 1
- 230000006698 induction Effects 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 230000002503 metabolic effect Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 229910017464 nitrogen compound Inorganic materials 0.000 description 1
- 150000002830 nitrogen compounds Chemical class 0.000 description 1
- 244000052769 pathogen Species 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 230000001902 propagating effect Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 239000011435 rock Substances 0.000 description 1
- 229910052814 silicon oxide Inorganic materials 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 230000002747 voluntary effect Effects 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
- Farming Of Fish And Shellfish (AREA)
- 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、観賞魚用水槽の水や魚の養殖用水、風呂水な
どの水を浄化する家庭用もしくは業務用水浄化装置、ま
た生ごみを砕き水に混ぜて汚泥水を浄化する水浄化装置
に関するものである。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a household or commercial water purification device for purifying water such as ornamental fish tank water, fish culture water, bath water, etc. This relates to a water purification device that purifies sludge water by mixing it.
従来の技術
従来この種の水浄化装置は、例えば、実開昭58−19
5697号公報に示されるように、第5図のような構造
になっている。即ち、紫外線ランプ31を内部に具えた
紫外線照射槽32、微生物着床体を具えた第1微生物処
理槽33第2微生物処理槽34が直列に接続されている
。各種間は、魚類飼育水槽(図示せず)ないし前記処理
水槽からの被処理水を前記処理水槽に導入するための導
入口35.36.37と被処理水を次の処理水槽、ない
し前記魚類飼育水槽へ送出するための吐出口38.39
.40とはホースで接続されている。また、各生物処理
槽の活性を増進させる手段が備えられていない。2. Description of the Related Art Conventionally, this type of water purification device was developed by, for example,
As shown in Japanese Patent No. 5697, it has a structure as shown in FIG. That is, an ultraviolet irradiation tank 32 equipped with an ultraviolet lamp 31 therein, a first microorganism treatment tank 33 and a second microorganism treatment tank 34 each equipped with a microorganism implantation body are connected in series. Each space has an inlet 35, 36, 37 for introducing treated water from a fish breeding tank (not shown) or the treated water tank into the treated water tank, and an inlet 35, 36, 37 for introducing the treated water from the fish breeding tank (not shown) or the treated water tank into the treated water tank, and a port 35, 36, 37 for introducing the treated water from the fish breeding tank (not shown) or the treated water tank into the treated water tank. Outlet port 38.39 for sending out to breeding tank
.. 40 is connected with a hose. Furthermore, there is no means for increasing the activity of each biological treatment tank.
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は、水槽中の水は魚の代謝
作用と食べ残しの餅の分解と排泄物などが原因でアンモ
ニアや汚れの発生、病原菌の繁殖などの課題がある。Problems to be Solved by the Invention In general, in aquarium fish tanks, the water in the tank has problems such as the generation of ammonia and dirt and the growth of pathogenic bacteria due to the metabolic effects of the fish, the decomposition of leftover rice cakes, and excreta. be.
さらに、アンモニアなどの窒素化合物が分解する過程で
発生する亜硝酸や硝酸も大きな課題であった。Furthermore, nitrous acid and nitric acid, which are generated during the decomposition process of nitrogen compounds such as ammonia, were also a major issue.
これらの課題を一部解決しようとしたものとして、最近
上記従来例に示すように微生物を利用した浄化フィルタ
ーや紫外線による殺菌手段が提案され始めている。In an attempt to partially solve these problems, recently, purification filters using microorganisms and sterilization means using ultraviolet rays have begun to be proposed, as shown in the above-mentioned conventional examples.
上記従来の単に微生物処理槽を直列接続に接続した構成
では、微生物処理槽内を好気性菌の最適繁殖状態に維持
することができないという課題を有していた。The above-mentioned conventional configuration in which microbial treatment tanks are simply connected in series has a problem in that the interior of the microbial treatment tank cannot be maintained in an optimal breeding state for aerobic bacteria.
本発明では、好気性菌、嫌気性菌等繁殖状態が変わる複
数の細菌を効果的に繁殖させ浄化性能をより高めること
と、従来構成にみられた処理水槽間の接続配管を省き水
漏れ等の品質問題を解消することを目的とする。The present invention improves purification performance by effectively propagating a plurality of bacteria with varying breeding states, such as aerobic bacteria and anaerobic bacteria, and eliminates the need for connecting piping between treated water tanks, which was seen in conventional configurations, and eliminates water leaks. The aim is to resolve quality issues.
さらに、細菌の固定床に鉱物質を用い浄化処理装置の浄
化性能を高めることを目的とする。Furthermore, the purpose is to improve the purification performance of the purification treatment equipment by using minerals as a fixed bed for bacteria.
課題を解決するための手段
上記課題を解決するために本発明は、水槽の水を循環す
る強制循環流路に鉱物質からなる第1モジュル、第2モ
ジュルと前記各モジエル間を接続するフランジと前記フ
ランジ内に設けた酸素供給手段とで水浄化部を構成し、
又、酸素供給手段は第1モジュルと連通ずる供給口、噴
流を形成する供給ノズル、前記供給ノズルの下流端壁に
形成された空気唆引口、噴流を受ける出力路と前記第2
モジュルへ連通する出力口とからなる流路パターンを形
成するフランジ基板と空気吸引流路を形成するフランジ
カバーとで構成されている。Means for Solving the Problems In order to solve the above problems, the present invention provides a forced circulation flow path for circulating water in an aquarium, and a flange connecting the first module, the second module, and each of the modules made of mineral material. A water purification unit is constituted by an oxygen supply means provided in the flange,
Further, the oxygen supply means includes a supply port communicating with the first module, a supply nozzle forming a jet, an air induction port formed in a downstream end wall of the supply nozzle, an output path for receiving the jet, and the second
It is composed of a flange substrate that forms a flow path pattern consisting of an output port communicating with the module, and a flange cover that forms an air suction flow path.
更に、細菌を繁殖させる固定床は、CaO1Si○z
、Alz Os 、MgO1Fe○が主成分とするアル
カリ成分を多く含んだ鉱物質で構成されている。Furthermore, the fixed bed for breeding bacteria is CaO1Si○z
, AlzOs , and MgO1Fe○ are minerals containing a large amount of alkaline components.
作用
本発明は、上記構成によって、まず、さかなの排泄物や
食べ残しの餌などの有機物、及び有機物から発生するア
ンモニアや硝酸塩を含んだ水槽水は、嫌気性細菌群
入し、モジュルの中の鉱物質の表面に膜状に付着した人
工的に培養された嫌気性細菌群と細菌活性化物質により
、硝酸塩は分解される。この硝酸塩が分解除去され、ア
ンモニアを含んだ水槽水は酸素供給手段で吸引された酸
素を含んだ空気と供に、第2モジュルへ流入する。ここ
で水槽水中に含まれるアンモニアはモジュルの中の鉱物
質の表面に膜状に付着した人工的に培養された好気性細
菌群と細菌活性化物質により、酸素の多い雰囲気で効率
よく硝酸塩に酸化分解され、水は浄化される。Effect of the present invention With the above-mentioned configuration, first, aquarium water containing organic matter such as fish excrement and uneaten food, as well as ammonia and nitrates generated from the organic matter, enters the anaerobic bacteria group, and Nitrates are decomposed by artificially cultivated anaerobic bacteria and bacterial activators attached to the surface of minerals in a film form. The nitrates are decomposed and removed, and the ammonia-containing aquarium water flows into the second module together with the oxygen-containing air sucked in by the oxygen supply means. Here, the ammonia contained in the aquarium water is efficiently oxidized to nitrate in an oxygen-rich atmosphere by an artificially cultured aerobic bacteria group and bacteria activator that adheres to the surface of the mineral material in the module in the form of a film. It is decomposed and the water is purified.
また、水槽中で繁殖した魚の病原菌類は、第1モジュル
、第2モジュルから流出した後、紫外線殺菌ユニットに
流入し紫外線により死滅する。In addition, pathogenic bacteria of fish that have grown in the aquarium flow out from the first module and the second module, and then flow into the ultraviolet sterilization unit where they are killed by ultraviolet rays.
このような浄化、殺菌作用により、水槽中の水は常に清
浄な状態に保たれる。Such purification and sterilization effects keep the water in the aquarium clean at all times.
実施例
以下、本発明の一実施例を添付図面に基づいて説明する
。第1図は、本発明の水浄化装置を応用した観賞魚用水
槽の外観図、第2図は同観賞魚用水槽の構成原理図であ
る。第1図、第2図において1は水槽、2は水槽1の台
で内部に水浄化ユニット3が内蔵されている。水浄化ユ
ニット3は鉱物質から成る微生物固定床が封入、直列に
配設された第1モジュル4、第2モジエル5と、前記各
モジエル間を接合し、イジェクタ−作用により外部空気
を流水中に導入する酸素供給手段6を内設する接合フラ
ンジよりなる接合フランジユニット7、前記第1モジュ
ル4の上流側に設けた温水加熱ユニット8、前記第2モ
ジュル5の下流側に設けた紫外線殺菌ユニット9及び、
循環ポンプ10を基本要素として構成されている。第1
モジュル4には嫌気性細菌、第2モジュル5には好気性
細菌が培養されている。循環ポンプ10の流入路11は
電磁弁12を介し、水槽1の底へ連通している。紫外線
殺菌ユニット9には流出路13が取りつけられ、清浄化
された水は前記流出路13を通り水槽1へ送られる。1
4はエアセパレータで、酸素供給手段6で吸引され、微
細化された気泡を分離するものである、15は空気用電
磁弁で空気導入管16中に取り付けられている。17は
水槽1、水浄化ユニット2からの漏水を検知する漏水セ
ンサである。°18は制御回路を内蔵した制御ボックス
である。EXAMPLE Hereinafter, an example of the present invention will be described based on the accompanying drawings. FIG. 1 is an external view of an aquarium fish tank to which the water purification device of the present invention is applied, and FIG. 2 is a diagram showing the principle of construction of the aquarium fish tank. In FIGS. 1 and 2, 1 is a water tank, and 2 is a stand for the water tank 1, which has a water purification unit 3 built therein. The water purification unit 3 has a fixed bed of microorganisms made of mineral substances sealed therein, and connects the first module 4 and the second module 5 arranged in series between each module, and uses an ejector action to draw outside air into the flowing water. A joint flange unit 7 consisting of a joint flange in which the oxygen supply means 6 to be introduced is installed, a hot water heating unit 8 provided upstream of the first module 4, and an ultraviolet sterilization unit 9 provided downstream of the second module 5. as well as,
It is constructed using a circulation pump 10 as a basic element. 1st
Anaerobic bacteria are cultured in module 4, and aerobic bacteria are cultured in second module 5. An inflow path 11 of the circulation pump 10 communicates with the bottom of the water tank 1 via a solenoid valve 12 . An outflow path 13 is attached to the ultraviolet sterilization unit 9, and purified water is sent to the aquarium 1 through the outflow path 13. 1
4 is an air separator that separates fine air bubbles sucked in by the oxygen supply means 6; 15 is an air solenoid valve installed in the air introduction pipe 16; 17 is a water leakage sensor that detects water leakage from the water tank 1 and the water purification unit 2. °18 is a control box containing a control circuit.
第3図は水浄化ユニット3の外観斜視回である。FIG. 3 is a perspective view of the water purification unit 3.
図において、温水加熱ユニット8には温水加熱ヒータ1
9の他に、湯温サーモ20、フロートセンサ21、湯温
過昇防止サーモ22が取りつけられている。紫外線殺菌
ユニット9には紫外線ランプ23が取りつけられている
。接合フランジユニット7はフランジ基板24、フラン
ジカバー25、との分割構成となっている。In the figure, the hot water heating unit 8 includes a hot water heater 1.
In addition to 9, a hot water temperature thermostat 20, a float sensor 21, and a hot water temperature overrise prevention thermostat 22 are installed. An ultraviolet lamp 23 is attached to the ultraviolet sterilization unit 9. The joining flange unit 7 is divided into a flange substrate 24 and a flange cover 25.
第4図はフランジカバー25の水路構成を示す。FIG. 4 shows the water channel configuration of the flange cover 25.
図中26は第1モジュル4へ連通する供給口、27は噴
流を形成する供給ノズル、28は前記供給ノズル27の
下流端壁に形成された空気吸引口、29は噴流を受ける
出力路、30は前記第2モジュル5へ連通する出力口で
ある。In the figure, 26 is a supply port communicating with the first module 4, 27 is a supply nozzle that forms a jet stream, 28 is an air suction port formed on the downstream end wall of the supply nozzle 27, 29 is an output path that receives the jet stream, 30 is an output port communicating with the second module 5.
鉱物質として高炉水砕を原料としたサドルロック型セラ
ミックスを用いた。この高炉水砕は製鉄所の溶鉱炉から
溶鉄1.0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
質でCab、SiOx。Saddle rock type ceramics made from blast furnace granulation was used as the mineral material. This granulated blast furnace is produced by rapidly cooling 0.5 tons of slag generated per 1.0 tons of molten iron from blast furnaces in steel plants, and is mainly used as a raw material for cement and as a soil improvement material. Blast furnace granules are porous and glassy, with Cab and SiOx.
A11a3を主成分とし、このほかMgO,FeOなど
を含んでいる。The main component is A11a3, and also contains MgO, FeO, etc.
上記構成において、循環ポンプIOを運転する。In the above configuration, the circulation pump IO is operated.
水槽1中のさかなの排泄物や食べ残しの餌などの有機物
、及び有機物から発生するアンモニアや硝酸塩を含んだ
水槽水は、水槽1の底部から流入路11を経由し循環ポ
ンプ10に入り、ポンプで加圧され、温水加熱ユニット
8で加熱されてから、第1モジュル4、第2モジュル5
、紫外線殺菌ユニット9を通り水槽1へと循環する。こ
の循環系において、まず第2モジュル5で前記水槽中の
さかなの排泄物や食べ残しの餌などの有機物、及び有機
物から発生するアンモニアは、鉱物質の表面に最初から
付着している人工的に培養された好気性細菌、随意性細
菌、およびそれらの活性化物質と酸素供給手段6で吸引
された空気中に含まれる酸素とにより酸化分解され硝酸
塩になる。このアンモニアの硝酸塩への酸化分解反応は
次に示す反応式%式%
つぎに、この硝酸塩に分解された成分を含んだ水は、紫
外線殺菌ユニット9から水槽1に戻り、水槽1中で発生
した有機物やアンモニアと共に、第1モジュル4へ循環
し、ここで鉱物質の表面に最初から付着している人工的
に培養された前記嫌気性細菌群によって循環水中の有機
物から発生する水素の作用により、窒素と水とに分解さ
れる。The aquarium water containing organic matter such as fish excrement and uneaten food in the aquarium tank 1, as well as ammonia and nitrates generated from the organic matter, enters the circulation pump 10 from the bottom of the aquarium 1 via the inflow channel 11, and is pumped After being pressurized by the hot water heating unit 8 and heated by the hot water heating unit 8, the first module 4 and the second module 5 are heated.
, passes through the ultraviolet sterilization unit 9 and circulates to the aquarium 1. In this circulation system, first, in the second module 5, organic matter such as fish excrement and uneaten food in the aquarium, as well as ammonia generated from organic matter, are removed from artificial substances that are attached to the surface of mineral materials from the beginning. It is oxidized and decomposed into nitrates by cultured aerobic bacteria, voluntary bacteria, their activated substances, and oxygen contained in the air sucked in by the oxygen supply means 6. This oxidative decomposition reaction of ammonia to nitrate is expressed by the following reaction formula% formula%Next, the water containing the components decomposed to nitrate returns from the ultraviolet sterilization unit 9 to the aquarium 1, and the water generated in the aquarium 1 Together with organic matter and ammonia, it circulates to the first module 4, where, due to the action of hydrogen generated from the organic matter in the circulating water by the artificially cultured anaerobic bacteria group that is originally attached to the surface of the mineral material, Decomposes into nitrogen and water.
この分解反応は次の式で表される。This decomposition reaction is expressed by the following formula.
Noff−+AH−+H,+O,・・・・・・ ■又
、水槽1の中に繁殖した魚の病原菌は前記紫外線殺菌ユ
ニット9の紫外線で殺菌される。更に、前記紫外線殺菌
ユニット9は循環水中の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。Noff-+AH-+H, +O, . . . ■Also, pathogenic bacteria on fish that have grown in the aquarium 1 are sterilized by the ultraviolet rays of the ultraviolet sterilization unit 9. Furthermore, the ultraviolet sterilization unit 9 also has the function of removing free chlorine from the circulating water, thereby further improving the fish breeding environment.
以上のように、原水中に含まれている遊離塩素や、水槽
lの中に発生した有機物やアンモニア、魚の病原菌など
は、鉱物質の表面に付着した人工的に培養した細菌群と
酵素により分解されたり、紫外線ランプ23で殺菌され
る。きれいになった水は、流出路13を通りエアセパレ
ータ14に入り、そこで混入している極微細気泡が成長
して水槽1に戻る。As mentioned above, free chlorine contained in raw water, organic matter and ammonia generated in the aquarium, fish pathogens, etc. are decomposed by artificially cultured bacteria and enzymes attached to the surface of mineral materials. or sterilized with an ultraviolet lamp 23. The purified water passes through the outflow path 13 and enters the air separator 14, where the ultrafine bubbles mixed therein grow and return to the water tank 1.
一方、前述の酸素供給手段6は供給ノズル27で形成さ
れたジェット噴流により空気吸引口28より大気を吸引
、空気を循環水中に送りこむ。ここで、吸引された空気
中の酸素の量を■、■式のアンモニアの酸化分解に必要
な量より多くすれば、酸素を多く含んだ水が水槽1に戻
る。その結果、従来の水槽のように散気管を入れて空気
ポンプで常にエアレーシッンをする必要がなくなる。On the other hand, the above-mentioned oxygen supply means 6 sucks atmospheric air through the air suction port 28 using a jet stream formed by the supply nozzle 27, and sends the air into the circulating water. Here, if the amount of oxygen in the sucked air is made larger than the amount required for oxidative decomposition of ammonia in formulas (1) and (2), water containing a large amount of oxygen returns to the water tank 1. As a result, unlike conventional aquariums, there is no need to install an aeration pipe and constantly use an air pump to air the tank.
鉱物質として使用される高炉水砕は多孔質のガラス質で
表に示すようにCab、5ift、Altosを主成分
とし、このほかMgO,FeOなどを含んでいる。この
主成分であるCaOは、前述の第2モジュル5でのアン
モニアの酸化分解時に発生するH’ (反応式■、■
)に対し中和反応をおこない、水槽1内の水のPH値の
低下を押さえる働きをする。Granulated blast furnace granules used as mineral materials are porous and glassy, and as shown in the table, contain Cab, 5ift, and Altos as main components, as well as MgO, FeO, and the like. This main component, CaO, is generated during the oxidative decomposition of ammonia in the second module 5 described above.
) to carry out a neutralization reaction and work to suppress a decrease in the pH value of the water in the aquarium 1.
表 高炉水砕の組成(%)
更に、CaOなどを主成分とする鉱物質の表面には、水
中でカルシウム等の2価のプラスイオンが沢山存在する
。これは、細菌群が一般にはマイナスに帯電されている
ことから、プラスイオンで表面が覆われる前記鉱物質は
、人工的に培養した細菌群や酵素の最適な固定床となる
。Table Composition (%) of blast furnace granulated water In addition, on the surface of mineral substances whose main component is CaO etc., there are many divalent positive ions such as calcium in water. This is because bacteria are generally negatively charged, so the mineral material whose surface is covered with positive ions serves as an optimal fixed bed for artificially cultured bacteria and enzymes.
発明の効果
(1)直列に接続された水浄化モジュルの一方は嫌気性
細菌、他方は好気性細菌と異なる働きをする細菌を効率
よく繁殖させることにより、魚の飼育時に発生するアン
モニア、亜硝酸、硝酸等多数の汚れ成分を効率よく分解
することができる。その結果、魚飼育水槽に使用した場
合水の交換回数が激減し、水槽内の藻の繁殖を防ぐこと
ができる。Effects of the invention (1) One of the water purification modules connected in series is an anaerobic bacteria, and the other is an aerobic bacteria. By efficiently breeding bacteria that have different functions, ammonia, nitrite, and It can efficiently decompose many dirt components such as nitric acid. As a result, when used in a fish tank, the number of water changes is drastically reduced, and the growth of algae in the tank can be prevented.
(2)各水浄化モジエル間には配管接続がなく、そのた
め構成部品の数が削減されると共に、組立工数も少なく
なってコストが低減される。(2) There are no piping connections between each water purification module, which reduces the number of component parts and reduces assembly man-hours, reducing costs.
(3)各水浄化モジュル内に配設される細菌の固定床と
して、CaOを多く含んだ高炉水砕のサドル型セラミッ
クが使用されているので、水槽中の水はアンモニアが分
解し酸が生成しても、PHが減少し酸性側に移ることが
ない、したがって、従来のように、水槽水中へアルカリ
を加えて水を中和することが不必要となる。(3) As a fixed bed of bacteria installed in each water purification module, a saddle-shaped ceramic made of blast furnace granulation containing a large amount of CaO is used, so ammonia decomposes in the water in the water tank and acid is generated. However, the pH does not decrease and shift to the acidic side. Therefore, it is no longer necessary to neutralize the water by adding alkali to the aquarium water as in the past.
(4)水浄化モジュルの上流にイジェクタ−作用で大気
を吸引する酸素供給手段を配設し、前記浄化モジエルで
必要とされる酸素量よりも多くの酸素量が供給されるよ
うに吸引空気量を設定することにより、水槽中の水は酸
素が十分溶存された状態となっている。そのため、従来
のように水槽中へ散気管を挿入し、空気ポンプで常にエ
ア細菌群は死滅することがなく、水槽中に発生する育機
物やアンモニアを運転開始時から分解することができる
。また、紫外線は魚の病原菌を殺菌するので、魚が病気
で死ぬのを防止することができる。(4) An oxygen supply means for suctioning atmospheric air by an ejector action is arranged upstream of the water purification module, and the suction air amount is adjusted so that a larger amount of oxygen is supplied than the amount of oxygen required by the purification module. By setting , the water in the aquarium has enough oxygen dissolved in it. Therefore, instead of inserting an aeration pipe into the aquarium and using an air pump to constantly kill the air bacteria group as in the past, it is possible to decompose the breeding materials and ammonia generated in the aquarium from the start of operation. In addition, UV rays can kill pathogenic bacteria in fish, which can prevent fish from dying from disease.
第1図は本発明の一実施例を示す水浄化装置の外観斜視
図、第2図は同装置の構成原理図、第3図は同装置の浄
化ユニットの外観斜視図、第4図は同装置の接続フラン
ジの水路構成図、第5図は従来の水浄化用微生物処理槽
の外観斜視図である。
3・・・・・・水浄化ユニット、4・・・・・・第1モ
ジュル、5・・・・・・第2モジュル、6・・・・・・
酸素供給手段、7・・・・・・接合フランジユニット、
8・・・・・・温水加熱ユニット、9・・・・・・紫外
線殺菌ユニット。Fig. 1 is an external perspective view of a water purification device showing an embodiment of the present invention, Fig. 2 is a diagram showing the principle of construction of the device, Fig. 3 is an external perspective view of a purification unit of the same device, and Fig. 4 is the same. FIG. 5 is an external perspective view of a conventional microbial treatment tank for water purification. 3... Water purification unit, 4... First module, 5... Second module, 6...
Oxygen supply means, 7... joint flange unit,
8... Hot water heating unit, 9... Ultraviolet sterilization unit.
Claims (3)
なる第1モジュル、第2モジュルと、前記第1モジュル
、前記第2モジュル間を接続するフランジと、前記フラ
ンジ内に設けた酸素供給手段とからなる水浄化装置。(1) A forced circulation channel that circulates water in the aquarium includes a first module and a second module made of a mineral, a flange connecting the first module and the second module, and a flange provided in the flange. A water purification device consisting of an oxygen supply means.
噴流を形成する供給ノズル、前記供給ノズルの下流端壁
に形成された空気吸引口、噴流を受ける出力路と前記第
2モジュルへ連通する出力口とからなる流路パターンを
形成するフランジ基板と空気吸引流路を形成するフラン
ジカバーとで構成される特許請求の範囲第1項記載の水
浄化装置。(2) the oxygen supply means is a supply port communicating with the first module;
A flange substrate and air forming a flow path pattern consisting of a supply nozzle that forms a jet, an air suction port formed on a downstream end wall of the supply nozzle, an output path that receives the jet, and an output port that communicates with the second module. The water purification device according to claim 1, comprising a flange cover forming a suction flow path.
MgO、FeOが主成分である特許請求の範囲第1項記
載の水浄化装置。(3) Mineral materials are CaO, SiO_2, Al_2O_3,
The water purification device according to claim 1, wherein the main components are MgO and FeO.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2101377A JPH03296496A (en) | 1990-04-17 | 1990-04-17 | Water purifying apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2101377A JPH03296496A (en) | 1990-04-17 | 1990-04-17 | Water purifying apparatus |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH03296496A true JPH03296496A (en) | 1991-12-27 |
Family
ID=14299111
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2101377A Pending JPH03296496A (en) | 1990-04-17 | 1990-04-17 | Water purifying apparatus |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH03296496A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20120091058A1 (en) * | 2010-10-15 | 2012-04-19 | Derek Byrd | Modular bioreactor system |
-
1990
- 1990-04-17 JP JP2101377A patent/JPH03296496A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20120091058A1 (en) * | 2010-10-15 | 2012-04-19 | Derek Byrd | Modular bioreactor system |
US8778184B2 (en) * | 2010-10-15 | 2014-07-15 | Derek Byrd | Modular bioreactor system |
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