JP2000061266A - Deodorizing purification and catalytic water treating device using functional ceramic - Google Patents

Deodorizing purification and catalytic water treating device using functional ceramic

Info

Publication number
JP2000061266A
JP2000061266A JP10234142A JP23414298A JP2000061266A JP 2000061266 A JP2000061266 A JP 2000061266A JP 10234142 A JP10234142 A JP 10234142A JP 23414298 A JP23414298 A JP 23414298A JP 2000061266 A JP2000061266 A JP 2000061266A
Authority
JP
Japan
Prior art keywords
water
treatment
catalyst
catalytic
functional ceramic
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
JP10234142A
Other languages
Japanese (ja)
Other versions
JP3074266B2 (en
Inventor
Masami Shoji
政己 庄子
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.)
Seisui Co Ltd
Original Assignee
Seisui 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 Seisui Co Ltd filed Critical Seisui Co Ltd
Priority to JP10234142A priority Critical patent/JP3074266B2/en
Priority to KR1019990021330A priority patent/KR20000016879A/en
Publication of JP2000061266A publication Critical patent/JP2000061266A/en
Application granted granted Critical
Publication of JP3074266B2 publication Critical patent/JP3074266B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/72Treatment of water, waste water, or sewage by oxidation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/50Treatment of water, waste water, or sewage by addition or application of a germicide or by oligodynamic treatment
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/72Treatment of water, waste water, or sewage by oxidation
    • C02F1/74Treatment of water, waste water, or sewage by oxidation with air
    • 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

Abstract

PROBLEM TO BE SOLVED: To contrive the improvement of water quality in waste water treatment and the improvement of water quality of water for business use by catalytic water treatment with a simple constitution and to make effectively performable the deodorization and purification of gas. SOLUTION: This device is provided with a treating tank 1 having an air intake part 4 and a drain part 7 around the bottom thereof and having a vent part 5 and a water supply port 6 containing a water spray nozzle 14 into which water solution is introduced to perform showering around the ceiling thereof, and plural baskets 3 arranged in the treating tank 1 for housing plural granules 7 of functional ceramic in a mixed state and in which magnetic material or plural kinds of metal oxides such as iron, cobalt, and titanium are combined with ferrite-based material and sintered. A water solution, to which sodium hypochlorite or chlorine is added, is introduced from the water supply part 6 to perform showering from above the plural granules 2 of functional ceramic, and also a gas to be treated is introduced from the air intake part 4 to perform the deodorication and purification of the gas and the formation of catalytic water by utilizing catalytic action of the functional ceramic, and the catalytic water is stored up to a prescribed level from the bottom part is taken out from the drain part 7 around the bottom.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は、機能セラミックの
触媒作用を利用して気体の脱臭浄化を行うと共に触媒水
を生成し水処理を行う機能セラミックを用いた脱臭浄化
及び水触媒処理装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a deodorizing purification and water catalyst treatment apparatus using a functional ceramic that performs deodorization purification of gas by utilizing the catalytic action of a functional ceramic and produces catalytic water for water treatment.

【0002】[0002]

【従来の技術及び発明が解決しようとする課題】近年、
排気や排水による大気、河川・湖沼・海の汚染が環境破
壊として大きな問題となっている。その中で、排水によ
る河川・湖沼・海の汚染を考えると、排水には様々な種
類があり、様々な規制が設けられている。例えば農業集
落排水では、農業集落排水事業実施要綱(昭和58年4
月4日農林水産事務次官)が策定されており、その趣旨
は次のようなものである。
2. Description of the Related Art In recent years,
The pollution of the atmosphere, rivers, lakes and marshes due to exhaust and drainage has become a serious problem as environmental destruction. Among them, considering the pollution of rivers, lakes and marshes by the drainage, there are various types of drainage and various regulations are set. For example, for agricultural village drainage, the agricultural village drainage project implementation guidelines (April 1983)
The Ministry of Agriculture, Forestry and Fisheries (Secretary for Agriculture, Forestry and Fisheries) has been formulated, and the purpose is as follows.

【0003】近年の農村社会における混住化の進展、生
活様式の高度化、農業生産様式の変貌等、農業及び農村
を取り巻く状況の変化により、農業用排水の汚濁が進行
し、農作物の生育障害、土地改良施設の維持管理費の増
大、悪臭の発生等、農業生産環境及び農村生活環境の両
面に大きな問題を生じている。このため、農業用用排水
の水質保全、農業用用排水施設の機能維持又は農村生活
環境の改善を図り、併せて公共用水域の水質保全に寄与
するため、農業集落におけるし尿、生活雑排水等の汚
水、汚泥又は雨水を処理する施設を整備する、というも
のである。
Due to changes in the circumstances surrounding agriculture and rural areas such as the progress of mixed living in rural societies, the sophistication of lifestyles, changes in agricultural production styles, etc., the pollution of agricultural drainage has progressed, and the growth of agricultural crops has been impaired. There are major problems in both the agricultural production environment and the rural living environment, such as increased maintenance costs for land improvement facilities and the generation of offensive odors. Therefore, in order to maintain the water quality of agricultural drainage, maintain the functions of agricultural drainage facilities or improve the rural living environment, and contribute to the water quality conservation of public water areas, human waste in agricultural settlements, domestic wastewater, etc. The facility for treating sewage, sludge or rainwater will be developed.

【0004】排水には、このような農業集落排水の他
に、養豚等の畜産業の排水、一般家庭生活雑排水、食品
工場や半導体製造工場その他の工場排水、ゴルフ場等の
レジャー用排水その他、一定の基準以上の水質に改善す
る必要のある排水は身の回りに多岐にわたって存在して
いる。しかも、これらの排水は、それぞれし尿や化学肥
料、洗剤、家庭用油等、処理対象となる成分が異なり、
脱臭、油分解、滅菌等、水質改善の目的、効果も様々で
ある。
In addition to such agricultural village drainage, drainage from livestock such as pig farming, general household miscellaneous drainage, factory drainage from food factories, semiconductor manufacturing plants and other factories, leisure drainage from golf courses, etc. , There is a wide variety of wastewater around us that needs to be improved to above a certain standard. Moreover, these wastewaters have different components to be treated, such as human waste, chemical fertilizers, detergents, household oils, etc.
There are various purposes and effects of water quality improvement such as deodorization, oil decomposition and sterilization.

【0005】しかし、このように多様な排水に対して効
果的に水質を改善するには、それぞれの目的に応じて規
模の大きな、複雑な排水処理施設が必要となり、排水処
理にかかるコストが高くなるという問題がある。
However, in order to effectively improve the water quality for such various effluents, a large-scale and complicated effluent treatment facility is required for each purpose, and the cost of the effluent treatment is high. There is a problem of becoming.

【0006】また、排水処理や汚水処理、汚泥処理を行
う施設、畜産飼育場、食肉加工場などの施設では、硫化
水素ガス、アンモニアガスその他の悪臭成分を含有した
ガスが大量に発生するため、脱臭を行い空気の浄化を行
う装置が用いられる。脱臭のために従来用いられている
装置として、例えば悪臭成分の主体である硫化水素の含
有ガスをアルカリ水溶液と接触させることにより硫黄化
合物を吸収除去するものがある。
Further, in facilities such as wastewater treatment, sewage treatment, sludge treatment, livestock farms, meat processing plants, etc., a large amount of gas containing hydrogen sulfide gas, ammonia gas and other malodorous components is generated. A device for deodorizing and purifying air is used. As a device conventionally used for deodorization, there is, for example, a device for absorbing and removing a sulfur compound by bringing a gas containing hydrogen sulfide, which is a main component of a malodorous component, into contact with an alkaline aqueous solution.

【0007】しかし、このようなアルカリ洗浄により脱
臭しようとするものでは、アルカリ洗浄液として苛性ソ
ーダを使用すると、洗浄液に吸収された二酸化炭素が苛
性ソーダと反応して炭酸ソーダや重炭酸ソーダに変化し
て効率(除去率)が低下する。そのため、所望の効率を
維持するには、苛性ソーダの補充が必要になり、十分な
硫化水素の除去効率を維持することが難しい。また、ア
ルカリ洗浄で除去しきれない微量の硫黄化合物を除去す
る方法として、活性炭吸着法やオゾン脱臭触媒法等を組
み合わせ採用している。
However, in the case of deodorizing by such an alkali cleaning, when caustic soda is used as the alkaline cleaning liquid, carbon dioxide absorbed in the cleaning liquid reacts with caustic soda to be changed to sodium carbonate or sodium bicarbonate, resulting in efficiency (removal). Rate) decreases. Therefore, in order to maintain the desired efficiency, it is necessary to supplement the caustic soda, and it is difficult to maintain sufficient hydrogen sulfide removal efficiency. Further, as a method for removing a trace amount of sulfur compounds that cannot be completely removed by alkali cleaning, an activated carbon adsorption method, an ozone deodorizing catalyst method, or the like is employed in combination.

【0008】そこで、硫化水素等の硫黄化合物を主体と
する周期成分含有ガスから硫黄化合物を効率よく除去す
るため、アルカリ洗浄液として亜鉛塩を含む炭酸ソーダ
水溶液中に接触させ、硫黄化合物中に硫黄原子を硫化亜
鉛として分離除去する方法が提案されている(例えば特
許第2731124号)。この方法によれば、炭酸ソー
ダ水溶液中の亜鉛塩の含有量を、水溶液中に懸濁物およ
び沈殿として蓄積された硫化亜鉛に対し当量比で3倍以
上に維持することが必要であるため、亜鉛塩の含有量の
調整、維持に特別の配慮が必要になる。
Therefore, in order to efficiently remove the sulfur compound from the periodic component-containing gas mainly composed of a sulfur compound such as hydrogen sulfide, the sulfur compound is brought into contact with an aqueous solution of sodium carbonate containing zinc salt as an alkali cleaning liquid to form a sulfur atom in the sulfur compound. A method of separating and removing as zinc sulfide has been proposed (for example, Japanese Patent No. 2731124). According to this method, it is necessary to maintain the content of the zinc salt in the aqueous solution of sodium carbonate at 3 times or more as an equivalence ratio with respect to zinc sulfide accumulated in the aqueous solution as a suspension and a precipitate. Special consideration is required for adjusting and maintaining the content of zinc salt.

【0009】[0009]

【課題を解決するための手段】本発明は、上記課題を解
決するものであって、簡単な構成の水触媒処理により排
水処理における水質改善、業務用水の水質改善を図り、
かつ効率よくガスの脱臭、浄化を行えるようにするもの
である。
Means for Solving the Problems The present invention is to solve the above-mentioned problems and aims to improve the water quality in wastewater treatment and the water quality for commercial use by a water catalyst treatment having a simple structure,
In addition, it enables efficient deodorization and purification of gas.

【0010】そのために本発明は、機能セラミックの触
媒作用を利用して気体の脱臭浄化を行うと共に水処理を
行い触媒水を生成する機能セラミックを用いた脱臭浄化
及び水触媒処理装置であって、底付近に気体を導入する
給気部と触媒水を取り出す排水部とを有し、天井付近に
気体を排気する排気部と水溶液を導入しシャワリングす
る散水ノズルを含む給水部とを有する処理タンクと、バ
インダーとして樹脂やガラスを使用し、フェライト系に
少なくとも磁性体や鉄、コバルト、チタン等の複数種類
の金属酸化物を組み合わせたものを焼結してなる複数の
機能セラミックの粒体を混合して収容し前記処理タンク
内の給気部と排気部との間に配置される複数のカゴとを
備え、前記給水部より次亜塩素酸ソーダ又は塩素を添加
した水溶液を導入して前記複数の機能セラミックの粒体
の上方よりシャワリングすると共に、前記給気部より気
体を導入してそれぞれ前記複数の機能セラミックの粒体
と通過接触させることにより機能セラミックの触媒作用
を利用して気体の脱臭浄化と触媒水の生成を行い、前記
生成した触媒水を底部より所定レベルまで貯留して前記
底付近の前記排水部より取り出すように構成したことを
特徴とするものである。
To this end, the present invention provides a deodorizing purification and water catalyst treatment apparatus using a functional ceramic that uses the catalytic action of a functional ceramic to deodorize and purify gas and to treat water to generate catalytic water. A treatment tank having an air supply part for introducing gas near the bottom and a drain part for taking out catalyst water, and an exhaust part for exhausting gas near the ceiling and a water supply part including a sprinkling nozzle for introducing and showering an aqueous solution. And a mixture of a plurality of functional ceramic particles obtained by sintering ferrite and a combination of at least a magnetic material and a plurality of metal oxides such as iron, cobalt, and titanium using a resin or glass as a binder. And a plurality of baskets arranged between the air supply section and the exhaust section in the processing tank, and introduces an aqueous solution containing sodium hypochlorite or chlorine from the water supply section. And showering the particles of the functional ceramics from above, and introducing a gas from the air supply part to bring the gas into contact with the particles of the functional ceramics to utilize the catalytic action of the functional ceramics. The deodorizing purification of gas and the generation of catalytic water are performed by the gas, the generated catalytic water is stored to a predetermined level from the bottom, and is taken out from the drainage section near the bottom.

【0011】嫌気性濾床槽、好気性濾床槽、沈殿槽、汚
泥槽を備えた排水処理施設により各種排水に対する水質
改善浄化の処理を行う水処理システムにおいて、複数の
機能セラミックの粒体を混合して処理タンクに収容し、
原水に次亜塩素酸ソーダを添加した水溶液を前記処理タ
ンクに導入し該水溶液を前記機能セラミックの粒体に通
過接触させることにより触媒作用を利用した水処理を行
い触媒水を生成する水触媒処理装置と、該水触媒処理装
置により生成された触媒水を前記各種の未処理排水に混
合する混合手段と、前記水触媒処理装置の前記原水とし
て前記排水処理施設から放出される処理済排水から一部
抽出する抽出手段とを備え、前記排水処理施設から放出
される処理済排水の一部を前記水触媒処理装置に原水と
して循環させ、生成した触媒水を各種排水に混合して排
水処理を行うように構成したことを特徴とするものであ
る。
In a water treatment system for treating and improving water quality of various kinds of wastewater by a wastewater treatment facility equipped with an anaerobic filter bed tank, an aerobic filter bed tank, a settling tank, and a sludge tank, a plurality of functional ceramic particles are used. Mix and store in the processing tank,
A water-catalytic treatment for producing catalytic water by introducing an aqueous solution obtained by adding sodium hypochlorite to raw water to the treatment tank and bringing the aqueous solution into contact with the granular particles of the functional ceramic to perform catalytic water treatment to generate catalytic water. An apparatus, a mixing means for mixing catalytic water generated by the water catalyst treatment apparatus with the various untreated wastewater, and a treated wastewater discharged from the wastewater treatment facility as the raw water of the water catalyst treatment apparatus. Part of the treated wastewater discharged from the wastewater treatment facility is circulated as raw water to the water catalyst treatment device, and the generated catalyst water is mixed with various wastewater to perform wastewater treatment. It is characterized by being configured as described above.

【0012】また、触媒水使用方法としては、使用済排
水に水質改善浄化の処理を行って放流する排水処理施設
を備えた水使用施設において、複数の機能セラミックの
粒体を混合して処理タンクに収容した水触媒処理装置に
原水を導入し、該原水に次亜塩素酸ソーダを添加した水
溶液を前記機能セラミックの粒体に通過接触させること
により触媒作用を利用した水処理を行い生成される触媒
水を前記水使用施設で使用する水として供給することを
特徴とし、触媒水をグリースその他の廃油に混合して廃
油処理を行うことを特徴とするものである。
Further, as a method of using the catalytic water, in a water use facility equipped with a wastewater treatment facility for treating wastewater for water quality improvement purification and discharging the wastewater, a treatment tank is prepared by mixing a plurality of functional ceramic particles. The raw water is introduced into the water catalyst treatment apparatus housed in the raw water, and the aqueous solution obtained by adding sodium hypochlorite to the raw water is passed through and brought into contact with the granules of the functional ceramic to perform the water treatment utilizing the catalytic action. The catalyst water is supplied as water to be used in the water use facility, and the catalyst water is mixed with grease or other waste oil to perform waste oil treatment.

【0013】[0013]

【発明の実施の形態】以下、本発明の実施の形態を図面
を参照しつつ説明する。図1は本発明に係る機能セラミ
ックを用いた脱臭浄化及び水触媒処理装置の実施の形態
を示す図であり、1は処理タンク、2は機能セラミック
の粒体、3はカゴ、4は給気部、5は排気部、6は給水
部、7は排水部、8〜11はバルブ、12は排気ファ
ン、13は触媒水、14は散水ノズルを示す。
BEST MODE FOR CARRYING OUT THE INVENTION Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is a diagram showing an embodiment of a deodorizing purification and water catalyst treatment device using a functional ceramic according to the present invention, wherein 1 is a treatment tank, 2 is functional ceramic particles, 3 is a basket, and 4 is air supply. Reference numeral 5 denotes an exhaust unit, 6 a water supply unit, 7 a drainage unit, 8 to 11 valves, 12 an exhaust fan, 13 catalytic water, and 14 a water spray nozzle.

【0014】図1において、処理タンク1は、天井付近
に排気部5、排気ファン12、その下部に給水部6、散
水ノズル14を、底付近に給気部4、排水部7をそれぞ
れ有し、内部に複数の機能セラミックの粒体2を混合し
て収容したカゴ3を多段に配置したものである。給水部
6は、バルブ10で原水に点滴剤として次亜塩素酸ソー
ダ(NaClO)を点滴し、1〜3ppm程度の濃度の
次亜塩素酸ソーダ水溶液を散水ノズル14に供給し上方
から処理タンク1の中に導入するものである。排水部7
は、散水ノズル14からシャワリングされ、複数の機能
セラミックの粒体2と通過接触するときに触媒作用によ
り生成された触媒水13を取り出すものであり、バルブ
11を通して図示のように処理タンク1の底より所定の
高さレベルから取り出すようにすることにより、その所
定の高さレベルまで触媒水を処理タンク1に貯留する。
その高さレベルは、例えばカゴ3の段数の2分の1の段
数までとしてもよいし、触媒水13の中のカゴ3の段
数、触媒水13の水面より上のカゴ3の段数をそれぞれ
適宜変えても、カゴ3の段数に応じて高さレベルを調整
してもよい。給気部4は、バルブ8を通して例えば悪臭
成分含有ガスその他のガス、空気などの気体を供給し底
付近から処理タンク1の中、貯留された触媒水の中に導
入するものである。排気部5は、給気部4から導入され
た気体が複数の機能セラミックの粒体2及び触媒水と通
過接触するときに脱臭、浄化された気体をバルブ9を通
して排気するものであり、その気体を排気部5に送り込
むのが排気ファン12である。
In FIG. 1, the processing tank 1 has an exhaust unit 5, an exhaust fan 12 near the ceiling, a water supply unit 6 and a sprinkler nozzle 14 below the ceiling, and an air supply unit 4 and a drain unit 7 near the bottom. The baskets 3 each containing a plurality of functional ceramic particles 2 mixed therein are arranged in multiple stages. The water supply section 6 drips sodium hypochlorite (NaClO) as a drip agent into raw water with a valve 10 and supplies an aqueous solution of sodium hypochlorite having a concentration of about 1 to 3 ppm to the water spray nozzle 14 to feed the treatment tank 1 from above. To be introduced in. Drain 7
Is to take out the catalytic water 13 produced by the catalytic action when it is showered from the sprinkling nozzle 14 and comes into contact with the plurality of particles 2 of the functional ceramic. Through the valve 11, as shown in FIG. By taking out from the bottom at a predetermined height level, the catalytic water is stored in the treatment tank 1 up to the predetermined height level.
The height level may be, for example, half the number of stages of the basket 3, or the number of stages of the basket 3 in the catalyst water 13 and the number of stages of the basket 3 above the water surface of the catalyst water 13 may be appropriately set. Alternatively, the height level may be adjusted according to the number of steps of the basket 3. The air supply unit 4 supplies a gas such as a malodorous component-containing gas or other gas or air through a valve 8 and introduces the gas from the vicinity of the bottom into the stored catalytic water in the processing tank 1. The exhaust unit 5 exhausts the deodorized and purified gas through the valve 9 when the gas introduced from the air supply unit 4 comes into contact with the plurality of functional ceramic particles 2 and the catalytic water. The exhaust fan 12 sends the exhaust gas to the exhaust unit 5.

【0015】機能セラミックの粒体2は、バインダーと
して樹脂やガラスを使用し、フェライト系に少なくとも
磁性体や鉄、コバルト、チタン等の複数種類の金属酸化
物を組み合わせたものを焼結してなるものであり、第1
の粒体、第2の粒体、第3の粒体からなる成分濃度の異
なる複数種の粒体をカゴ3に混合して収容し、これを数
段(図示の例では4段)に重ねて着脱交換可能に配置す
る。第1の粒体は、フェライト系に少なくとも磁性体、
鉄、モリブデン、コバルト、チタン、マグネシウム、ア
ルミニウム、カリウム、ジルコニウム、珪素の金属酸化
物を組み合わせたものを焼結してなり、第2の粒体は、
フェライト系に少なくとも磁性体と鉄とマンガン、コバ
ルト、チタン、マグネシウム、アルミニウム、カリウ
ム、ジルコニウム、珪素の金属酸化物を組み合わせたも
のを焼結してなり、第3の粒体は、少なくとも酸化アル
ミニウム、ジルコニア、珪藻土、チタン酸バリウムの金
属酸化物を組み合わせたものを焼結してなる。
The functional ceramic granules 2 are obtained by using a resin or glass as a binder and sintering a ferrite-based material in which at least a magnetic material and a plurality of metal oxides such as iron, cobalt and titanium are combined. It is the first
Of the different types of particles having different component concentrations, which are composed of the above-mentioned granules, the second granules, and the third granules, are mixed and stored in the basket 3, and these are stacked in several stages (four stages in the illustrated example). It is arranged so that it can be removed and replaced. The first particles are at least a magnetic material based on ferrite,
The second granular material is formed by sintering a combination of metal oxides of iron, molybdenum, cobalt, titanium, magnesium, aluminum, potassium, zirconium, and silicon.
The ferrite-based material is a combination of at least a magnetic material and a metal oxide of iron and manganese, cobalt, titanium, magnesium, aluminum, potassium, zirconium, and silicon, and the third granular material is at least aluminum oxide, It is made by sintering a combination of metal oxides of zirconia, diatomaceous earth and barium titanate.

【0016】これらの粒体は、成分濃度を制御し、原子
パーセントを変えることにより、イオンの反応の効率を
良くすることができ、第1の粒体では、特に殺菌、脱臭
作用に顕著な効果を有し、第2の粒体では、油分解、殺
菌作用に顕著な効果を有し、第3の粒体では、油分解作
用に顕著な効果を有することが確認された。また、第1
の粒体と第2の粒体とを混合させると、第1の粒体と第
2の粒体とは、成分濃度が違うためお互いに反応しあ
い、イオンの発生の効率がよくなり、さらに、第3の粒
体を少量追加することにより、油分解がより進むことも
実証されている。しかも、第3の粒体は、凝結作用が強
く、分子をフロック状に形成し、油分を親水、親油性に
する作用がある。そのため、汚泥の沈降速度が早くなる
効果も、排水処理場で多数確認されている。つまり、有
機分解する働きがよくなるので、水質の改善に寄与し、
油の酸化臭を除去して脱臭効果をさらによくすることに
つながっている。このことは、長年の機能セラミックの
研究にわたる経験と繰り返し試験によるものであり、こ
の経験値により、脱臭、水質改善等に応用して各粒体の
比率基準が決定される。
In these granules, it is possible to improve the efficiency of the reaction of ions by controlling the component concentration and changing the atomic percentage, and the first granule has a particularly remarkable effect on the sterilization and deodorizing action. It was confirmed that the second granules had a remarkable effect on oil decomposition and bactericidal action, and the third granules had a remarkable effect on oil decomposition action. Also, the first
When the granules of No. 2 and the granules of No. 2 are mixed, the first granules and the second granules react with each other because the component concentrations are different, and the efficiency of ion generation is improved. It has also been demonstrated that by adding a small amount of a third granule, oil decomposition is more advanced. In addition, the third granules have a strong coagulation action, form molecules in the form of flocs, and have the action of making the oil content hydrophilic and lipophilic. Therefore, the effect of increasing the sedimentation speed of sludge has been confirmed in many wastewater treatment plants. In other words, since it works better for organic decomposition, it contributes to the improvement of water quality,
It is connected to the improvement of the deodorizing effect by removing the oxidative odor of oil. This is based on many years of experience in repeated studies of functional ceramics and repeated tests, and the experience value determines the ratio standard of each particle by applying it to deodorization, water quality improvement, and the like.

【0017】したがって、成分濃度を制御し、さらに第
1〜第3の粒体の混合比率を変えることにより、処理目
的に応じた効果を高めることができる。例えば養豚等の
畜産業の排水や農業集落排水、一般家庭生活雑排水に対
しては、アンモニアや硫化水素、チッソ、リン等が多
く、脱臭の効果が特に要求される。また、食品工場の排
水や食堂、レストランの排水を含む工場排水に対して
は、油、チッソ、リン等が多く、油分解の効果が特に要
求される。このようなそれぞれの要求に応じて第1〜第
3の粒体の混合比率が設定される。
Therefore, by controlling the component concentrations and changing the mixing ratio of the first to third particles, it is possible to enhance the effect according to the processing purpose. For example, a large amount of ammonia, hydrogen sulfide, nitrogen, phosphorus, etc. are contained in wastewater from livestock industries such as pig farming, wastewater from agricultural communities, and general domestic wastewater, and a deodorizing effect is particularly required. Further, with respect to factory wastewater including food factory wastewater and canteen and restaurant wastewater, a large amount of oil, nitrogen, phosphorus, etc. is required, and the effect of oil decomposition is particularly required. The mixing ratios of the first to third granules are set according to the respective requirements.

【0018】本発明に係る機能セラミックを用いた脱臭
浄化及び水触媒処理装置では、次亜塩素酸ソーダ水溶液
を散水ノズル14によりシャワリングして上段の機能セ
ラミックの粒体2から順次通過接触させ、さらに下方に
貯留して排水部7までの間に下段の機能セラミックの粒
体2と通過接触させて、触媒作用を利用した水処理を行
って触媒水を生成し、その触媒水13を底付近の排水部
7からバルブ11を通して取り出し、汚水や排水、汚泥
に添加して処理効果を改善したり、業務用水などの水質
を改善したりする触媒水として利用する。一方、次亜塩
素酸ソーダ水溶液を上記のように機能セラミックの粒体
2に通過接触させて生成された触媒水により、ガス中の
アンモニア、ダイオキシン、炭酸ガス(CO2 )、硫化
水素が除去され、脱臭、浄化を行うことができる。
In the deodorizing purification and water catalyst treatment apparatus using the functional ceramic according to the present invention, the aqueous solution of sodium hypochlorite is showered by the water spray nozzle 14 so that the granular particles 2 of the functional ceramic in the upper stage are sequentially passed and contacted. Further, it is stored below and is brought into contact with the granules 2 of the lower functional ceramic through the drainage section 7 to perform catalytic water treatment to generate catalytic water. It is taken out from the drainage section 7 through the valve 11 and added to sewage, waste water, and sludge to be used as catalytic water for improving the treatment effect or improving the quality of water such as commercial water. On the other hand, ammonia, dioxins, carbon dioxide (CO 2 ), and hydrogen sulfide in the gas are removed by the catalytic water produced by bringing the aqueous solution of sodium hypochlorite into contact with the functional ceramic granules 2 as described above. , Can be deodorized and purified.

【0019】また、上記構成の装置では、次亜塩素酸ソ
ーダ水溶液が処理タンク1の中で上方から下方に向かっ
て流れ多段配置した機能セラミックの粒体2を通過接触
して触媒水が生成され取り出されると同時に、これと全
く逆方向の下方から上方に向かってガスが流れるので、
貯留された触媒水13の中では、ガスが気泡となって機
能セラミックの粒体2の間を昇って揺動、相互接触さ
せ、機能セラミックの粒体2に付着した汚れを除去して
洗浄を行うことができる。したがって、機能セラミック
の粒体2を上方の段と下方の段で時々入れ換えることに
より、触媒水13の中のものとその上方にあるものとを
同様の状態に維持することができる。
In the apparatus having the above construction, the aqueous solution of sodium hypochlorite flows from the upper side to the lower side in the processing tank 1 and passes through the functional ceramic granules 2 arranged in multiple stages to generate catalytic water. At the same time as it is taken out, gas flows from the lower direction to the upper direction in the opposite direction,
In the stored catalyst water 13, the gas becomes bubbles and rises between the functional ceramic particles 2 so as to oscillate and contact each other, and the dirt adhering to the functional ceramic particles 2 is removed for cleaning. It can be carried out. Therefore, by replacing the functional ceramic particles 2 between the upper stage and the lower stage from time to time, it is possible to maintain the state in the catalytic water 13 and the state above it in the same state.

【0020】排水部7から取り出される触媒水は、農業
集落排水処理場や畜産業界の処理場、飼育場、食肉セン
ター、コンポスト、工場等の水として、あるいは添加混
合して使用し、また、排水に添加混合して使用すること
により、触媒効果による反応で後述するような脱臭、殺
菌、脱窒素、脱リン、水質改善、汚泥軽減、曝気省エネ
等の各種効果を高めることができる。
The catalyst water taken out from the drainage section 7 is used as water in an agricultural settlement wastewater treatment plant, a treatment plant in the livestock industry, a breeding ground, a meat center, a compost, a factory, etc., or is used as a mixture. By adding and mixing with the above, it is possible to enhance various effects such as deodorization, sterilization, denitrification, dephosphorization, water quality improvement, sludge reduction, and aeration energy saving, which will be described later, in the reaction due to the catalytic effect.

【0021】図2は本発明に係る機能セラミックを用い
た脱臭浄化及び水触媒処理装置を利用した水処理システ
ムの実施の形態を示す図であり、21は処理タンク、2
2は排水処理施設、23は次亜塩素酸ソーダ添加部、2
4は触媒水混合部、25は処理済排水抽出部を示す。
FIG. 2 is a view showing an embodiment of a water treatment system using a deodorizing purification and a water catalyst treatment apparatus using the functional ceramic according to the present invention, 21 is a treatment tank, 2
2 is a wastewater treatment facility, 23 is a sodium hypochlorite addition section, 2
Reference numeral 4 indicates a catalyst water mixing section, and 25 indicates a treated wastewater extraction section.

【0022】図2において、処理タンク21は、図1で
既に説明したものであり、バインダーとして樹脂やガラ
スを使用し、フェライト系に少なくとも磁性体や鉄、コ
バルト、チタン等の複数種類の金属酸化物を組み合わせ
たものを焼結してなる複数の機能セラミックの粒体を混
合して収容して、処理タンクに原水を導入し該原水を機
能セラミックの粒体に通過接触させることにより触媒水
を生成するものである。排水処理施設22は、養豚等の
畜産業の排水、農業集落排水、一般家庭生活雑排水、ゴ
ルフ場等のレジャー用排水その他の未処理排水を導入
し、所定の基準を満たす水質になるように水質改善浄化
の処理をする施設であり、例えば嫌気性濾床槽や好気性
濾床槽、沈殿槽、汚泥濃縮貯留槽、消毒槽等を有する。
なお、嫌気性濾床槽や汚泥濃縮貯留槽には、処理タンク
21或いは別の処理タンクで生成された触媒水を加えて
もよい。このことにより、さらに排水処理施設による処
理効果を高めることができるからである。次亜塩素酸ソ
ーダ添加部23は、処理タンク21に導入する原水に次
亜塩素酸ソーダを添加混合するものであり、触媒水混合
部24は、未処理排水に処理タンク21により生成した
触媒水を添加混合するものである。処理済排水抽出部2
5は、排水処理施設22で所定の基準を満たす水質にな
るように処理された処理済排水から処理タンク21に導
入する原水として、例えば20%程度を抽出するもので
あり、これに次亜塩素酸ソーダ添加部23で次亜塩素酸
ソーダを添加混合し処理タンク21に導入している。こ
のように処理済排水を一部抽出して還流させて触媒水を
生成することにより、無駄な水の使用をなくし排水を有
効に活用することができる。なお、通常、排水処理施設
32には、後述するように消毒槽を有するので、この消
毒槽で次亜塩素酸ソーダが添加混合される場合には、次
亜塩素酸ソーダ添加部23が省略される。
In FIG. 2, the processing tank 21 is the same as that described in FIG. 1, and resin or glass is used as a binder, and at least a magnetic material and a plurality of types of metal oxides such as iron, cobalt and titanium are added to the ferrite system. A plurality of functional ceramic granules obtained by sintering a mixture of materials are mixed and accommodated, raw water is introduced into the treatment tank, and the raw water is passed through and brought into contact with the functional ceramic granules to obtain catalytic water. To generate. The wastewater treatment facility 22 introduces wastewater from livestock industries such as pig farming, wastewater from agricultural settlements, general household wastewater, wastewater for leisure such as golf courses, and other untreated wastewater so that the quality of water meets prescribed standards. It is a facility for water quality improvement and purification treatment, and has, for example, an anaerobic filter bed tank, an aerobic filter bed tank, a sedimentation tank, a sludge concentration storage tank, a disinfection tank, and the like.
The catalytic water generated in the treatment tank 21 or another treatment tank may be added to the anaerobic filter bed tank and the sludge concentration storage tank. This is because the treatment effect of the wastewater treatment facility can be further enhanced. The sodium hypochlorite addition part 23 is for adding and mixing sodium hypochlorite to the raw water introduced into the treatment tank 21, and the catalyst water mixing part 24 is the catalyst water generated by the treatment tank 21 in the untreated wastewater. Is added and mixed. Treated wastewater extraction part 2
5 is for extracting, for example, about 20% as raw water to be introduced into the treatment tank 21 from the treated effluent treated in the effluent treatment facility 22 so as to have a water quality satisfying a predetermined standard. Sodium hypochlorite is added and mixed in the acid soda addition section 23 and introduced into the processing tank 21. In this way, by partially extracting the treated wastewater and refluxing it to generate catalyst water, it is possible to eliminate wasteful use of water and effectively utilize the wastewater. Since the wastewater treatment facility 32 usually has a disinfection tank as described later, when sodium hypochlorite is added and mixed in this disinfection tank, the sodium hypochlorite addition section 23 is omitted. It

【0023】図3は本発明に係る触媒水使用方法の実施
の形態を示す図であり、31は処理タンク、32は水使
用施設、33は排水処理施設を示す。
FIG. 3 is a diagram showing an embodiment of a method for using catalytic water according to the present invention, in which 31 is a treatment tank, 32 is a water use facility, and 33 is a wastewater treatment facility.

【0024】図3において、処理タンク31は、図1で
既に説明したものであり、バインダーとして樹脂やガラ
スを使用し、フェライト系に少なくとも磁性体や鉄、コ
バルト、チタン等の複数種類の金属酸化物を組み合わせ
たものを焼結してなる複数の機能セラミックの粒体を混
合して収容し、処理タンクに原水を導入し該原水を機能
セラミックの粒体に通過接触させることにより触媒水を
生成するものである。水使用施設32は、処理タンク3
1で生成された触媒水を利用する、例えば食品工場等で
ある。排水処理施設33は、水使用施設32から放出さ
れる排水が所定の基準を満たす水質になるように処理す
る施設であり、例えば嫌気性濾床槽や好気性濾床槽、沈
殿槽、汚泥濃縮貯留槽、消毒槽等を有する。なお、嫌気
性濾床槽や汚泥濃縮貯留槽には、処理タンク31或いは
別の処理タンクで生成された触媒水を加えてもよい。こ
のことにより、さらに排水処理施設による処理効果を高
めることができるからである。
In FIG. 3, the processing tank 31 has already been described with reference to FIG. 1, and resin or glass is used as a binder, and at least a magnetic material and a plurality of types of metal oxides such as iron, cobalt, titanium, etc. are added to the ferrite system. A plurality of functional ceramic particles formed by sintering a mixture of materials are mixed and accommodated, raw water is introduced into a treatment tank, and the raw water is passed through and contacted with the functional ceramic particles to generate catalytic water. To do. The water use facility 32 is the treatment tank 3
For example, it is a food factory or the like that uses the catalyst water generated in 1. The wastewater treatment facility 33 is a facility that treats the wastewater discharged from the water use facility 32 so that the quality of the water satisfies a predetermined standard. For example, an anaerobic filter bed tank, an aerobic filter bed tank, a sedimentation tank, and sludge concentration It has a storage tank and a disinfection tank. The catalytic water generated in the treatment tank 31 or another treatment tank may be added to the anaerobic filter bed tank and the sludge concentration storage tank. This is because the treatment effect of the wastewater treatment facility can be further enhanced.

【0025】図4は排水処理施設の構成例を示す図であ
り、41は流量調整槽、42は原水槽、43は嫌気性濾
床槽、44は好気性濾床槽、45は沈殿槽、46は汚泥
濃縮貯留槽、47は消毒槽・放流槽を示す。
FIG. 4 is a diagram showing an example of the structure of a wastewater treatment facility. 41 is a flow rate adjusting tank, 42 is a raw water tank, 43 is an anaerobic filter bed tank, 44 is an aerobic filter bed tank, 45 is a sedimentation tank, Reference numeral 46 indicates a sludge concentration storage tank, and 47 indicates a disinfection tank / discharge tank.

【0026】図4において、流量調整槽41は、例えば
触媒水を含む図2に示す水使用施設22からの放流水や
触媒水を混合した図3に示す各種放流水を未処理排水の
原水とし、その流量を調整するものであり、原水槽42
は、流量調整槽41を通して原水を貯留するものであ
る。嫌気性濾床槽43は、嫌気性微生物による嫌気性処
理を行い、好気性濾床槽・曝気槽44は、好気性微生物
による好気性処理及び曝気処理を行って、有機物を酸化
させて炭化固形物にし、さらに粉末にするものである。
沈殿槽45は、嫌気性濾床槽43及び好気性濾床槽・曝
気槽44により処理済の水に残留している汚泥を沈殿さ
せ、汚泥濃縮貯留槽46は、嫌気性濾床槽43、好気性
濾床槽・曝気槽44、沈殿槽45からの汚泥を濃縮して
貯留し、さらに必要に応じて汚泥貯留槽に移して搬出す
る。ここで、触媒水を原水だけでなく、嫌気性濾床槽4
3、汚泥濃縮貯留槽46にも必要に応じて適宜加えても
よい。このことにより、アンモニアの分解を促進してさ
らに有機物の酸化、脱臭、殺菌等の効果を高めることが
できる。また、汚泥濃縮貯留槽46から排出される余剰
水は、水質が十分改善されていないので、嫌気性濾床槽
43に戻される。消毒槽・放流槽47は、沈殿槽45で
汚泥を沈殿させた上澄みの水に次亜塩素酸ソーダを加え
て消毒して貯留し処理済排水として放流するものであ
る。
In FIG. 4, the flow rate adjusting tank 41 uses, for example, the discharge water from the water use facility 22 shown in FIG. 2 containing the catalyst water or the various discharge water shown in FIG. , For adjusting the flow rate of the raw water tank 42
Is for storing raw water through the flow rate adjusting tank 41. The anaerobic filter bed tank 43 performs anaerobic treatment with anaerobic microorganisms, and the aerobic filter bed / aeration tank 44 performs aerobic treatment and aeration treatment with aerobic microorganisms to oxidize organic matter and solidify carbonization. It is made into powder and then powdered.
The settling tank 45 precipitates the sludge remaining in the water treated by the anaerobic filter bed tank 43 and the aerobic filter bed / aeration tank 44, and the sludge concentration storage tank 46 is the anaerobic filter bed tank 43, The sludge from the aerobic filter bed / aeration tank 44 and the sedimentation tank 45 is concentrated and stored, and if necessary, transferred to a sludge storage tank and carried out. Here, the catalyst water is not limited to the raw water, but the anaerobic filter bed tank 4
3. It may be added to the sludge thickening storage tank 46 as needed. As a result, the decomposition of ammonia can be promoted and the effects of oxidizing, deodorizing, sterilizing, and the like of organic substances can be further enhanced. The surplus water discharged from the sludge concentration storage tank 46 is returned to the anaerobic filter bed tank 43 because the water quality has not been sufficiently improved. The disinfection tank / exhaust tank 47 is for adding sodium hypochlorite to the supernatant water in which sludge has been settled in the settling tank 45, disinfecting it, storing it, and discharging it as treated wastewater.

【0027】排水処理施設は、例えば上記のように構成
されたものであり、従来より採用されている各種処理施
設、例えば先に説明した農業集落排水事業要綱に対応し
て社団法人日本農業集落排水協会(JARUS)でJA
RUS型処理施設を開発しているが、これらの処理施設
も採用することができる。因みに、JARUS型処理施
設を見ても、処理対象人口等に応じ、沈殿分離と接触曝
気を組み合わせた方式のS型、1型、窒素除去を考慮し
て、嫌気性濾床と接触曝気を組み合わせた方式の2型、
流量調整槽を前置し、嫌気性濾床と接触曝気を組み合わ
せた方式の3型、窒素除去を考慮して、窒素除去を考慮
して、嫌気性濾床と接触曝気を組み合わせた方式の4
型、嫌気性濾床と接触曝気を組み合わせた方式の5型、
回分式活性汚泥方式の6型、窒素除去を考慮した回分式
活性汚泥方式の7型、7・G型、連続流入間欠曝気方式
の8型、9型のように各種型式のものがある。
The wastewater treatment facility is constructed, for example, as described above, and various treatment facilities that have been conventionally used, for example, the agricultural settlement drainage business of Japan, which corresponds to the above-mentioned outline of the agricultural settlement drainage business, is incorporated. JA at the association (JARUS)
RUS type processing facilities are being developed, but these processing facilities can also be adopted. By the way, looking at the JARUS type treatment facility, we combined the anaerobic filter bed and contact aeration in consideration of the type S and type 1 of the system that combines precipitation separation and contact aeration according to the population to be treated and nitrogen removal. Type 2 of the
Type 3 in which a flow rate control tank is installed in front, and a combination of anaerobic filter bed and contact aeration is used. Type 3 in consideration of nitrogen removal and in consideration of nitrogen removal, method 4 in which an anaerobic filter and contact aeration are combined.
Type, type 5 that combines anaerobic filter bed and contact aeration
There are various types such as batch activated sludge type 6, batch activated sludge type 7 with consideration of nitrogen removal, 7G type, continuous inflow intermittent aeration type 8 and 9.

【0028】排水処理施設によっては、嫌気性濾床槽4
3がない場合や、好気性濾床槽・曝気槽44がない場
合、沈殿槽45がない場合があるが、それぞれの構成に
応じて嫌気性濾床槽43がある場合には、先に述べたよ
うに嫌気性濾床槽43にも触媒水を加えることにより、
より水質の改善効果を高めることができる。つまり、本
発明は、排水処理施設の構成が特別に限定されるもので
はなく、様々な構成、タイプの排水処理施設に適用で
き、要するにその際に触媒水を加えることにより、より
その処理効果を高めることができるというものである。
Depending on the wastewater treatment facility, anaerobic filter bed tank 4
3 is not present, or there is no aerobic filter bed / aeration tank 44, or there may be no settling tank 45, but if there is an anaerobic filter bed tank 43 depending on each configuration, then As described above, by adding catalytic water also to the anaerobic filter bed tank 43,
The effect of improving water quality can be enhanced. That is, the present invention is not particularly limited to the configuration of the wastewater treatment facility, it can be applied to various configurations, types of wastewater treatment facility, in short, by adding catalytic water at that time, the treatment effect can be further improved. It can be raised.

【0029】これらの原水に図2や図3に示すように本
発明に係る機能セラミックを用いた脱臭浄化及び水触媒
処理装置により生成された触媒水を使用することによ
り、次亜塩素酸ソーダNaClOが水H2 Oと接触した
とき苛性ソーダNaOHに化学変化してpHをアルカリ
性にするので、そのための影響で微好気性の微生物が発
生し、エアレーション曝気がほとんど必要なくなる。し
たがって、通常の1/4の曝気で微生物の活動が活発に
なり、汚泥が軽減されるので、大きな省エネ効果が得ら
れる。しかも、好気性濾床槽・曝気槽44による処理で
は、酵素(溶酸酵素=DO)が存在するところに好んで
生息する微生物を利用することにより、有機物が酸化し
て炭化物になるので、有機物が炭化固形物になりさらに
粉末化して汚泥濃縮貯留槽から搬出される汚泥の量を少
なくすることができる。さらに、脱臭、殺菌、油分解
等、水質改善浄化の効果もあげることができ、グリース
その他の工場廃油などに本発明の触媒水を混合すること
により、油特有のドロドロがなくなり油分解が著しく促
進することが確認されている。
As shown in FIG. 2 and FIG. 3, the deodorizing purification using the functional ceramics according to the present invention and the catalyst water produced by the water catalyst treatment apparatus are used for these raw waters, so that sodium hypochlorite NaClO When it comes into contact with water H 2 O, it chemically changes into caustic soda NaOH to make the pH alkaline, so that microaerobic microorganisms are generated due to the effect, and aeration and aeration are almost unnecessary. Therefore, the aeration of 1/4 of the normal one activates the activity of the microorganisms and reduces the sludge, so that a large energy saving effect can be obtained. In addition, in the treatment by the aerobic filter bed / aeration tank 44, the organic matter is oxidized and becomes a charcoal substance by utilizing the microorganisms that prefer to live in the presence of the enzyme (hydrolytic enzyme = DO). Can be reduced to an amount of sludge that is discharged from the sludge thickening storage tank after being turned into a carbonized solid and further powdered. Furthermore, the effects of water quality improvement and purification such as deodorization, sterilization, oil decomposition, etc. can be achieved. By mixing the catalyst water of the present invention with grease and other industrial waste oil, the oil-specific mist disappears and oil decomposition is significantly promoted. It is confirmed to do.

【0030】次に、原水H2 Oに次亜塩素酸ソーダNa
ClO又は塩素Cl2 を1〜3ppm程度を添加した水
溶液が機能セラミックの粒体を通過接触するときの触媒
作用による反応について説明する。
Next, the raw water H 2 O was added to sodium hypochlorite Na.
The reaction by the catalytic action when an aqueous solution containing about 1 to 3 ppm of ClO or chlorine Cl 2 passes through and contacts the granules of the functional ceramic will be described.

【0031】[0031]

【化1】 NaClO+H2 O → HClO+NaOH Cl2 +H2 O → HCl+HClO HClO → HCl+O Cl2 +H2 O → HClO+H+ +Cl- HClO ←→ H+ +ClO- の反応により、次亜塩素酸ソーダNaClOが水H2
と接触したとき、次亜塩素酸HClOと苛性ソーダNa
OHに化学変化しアルカリ性になる。この反応はきわめ
て遅く、通常の状態では容易に右方向へは進行しない
が、機能セラミックは、右方向への作用を著しく促進す
る触媒として働く。塩素Cl2 の場合についても以下同
様である。そして、次亜塩素酸HClOは、さらに分解
して発生期の酸素を発生し、この酸素が強力な酸化作用
の働きを示す。そのため、生物の腐敗臭や排泄臭のう
ち、例えば公衆便所の不快臭は、スカトール(3メチル
インドール)が主な成分であるが、−NH−の官能基を
有するため、弱い塩基性を示し
Embedded image Reaction of NaClO + H 2 O → HClO + NaOH Cl 2 + H 2 O → HCl + HClO HClO → HCl + O Cl 2 + H 2 O → HClO + H + + Cl HClO ← → H + + ClO causes sodium hypochlorite NaClO to become water H 2. O
When in contact with hypochlorous acid HClO and caustic soda Na
It changes to OH and becomes alkaline. This reaction is extremely slow and does not easily proceed to the right under normal conditions, but the functional ceramic acts as a catalyst that significantly promotes the action to the right. The same applies to the case of chlorine Cl 2 . Then, the hypochlorous acid HClO is further decomposed to generate nascent oxygen, and this oxygen exhibits a strong oxidizing action. For this reason, among the decaying odors and excretion odors of living organisms, for example, the unpleasant odor of public toilets is mainly composed of skatole (3 methylindole), but it has a functional group of -NH- and thus shows weak basicity.

【0032】[0032]

【化2】 2C9 9 N+HCl → 2C9 9 N・HCl のように塩酸と反応してスカトール塩酸塩を生成する。
このアミンの塩は、無臭で可溶性となる。また、排泄臭
の成分であるアンモニアは、次亜塩素酸と
Embedded image It reacts with hydrochloric acid like 2C 9 H 9 N + HCl → 2C 9 H 9 N · HCl to produce skatole hydrochloride.
This amine salt becomes odorless and soluble. Ammonia, which is a component of excretion odor, is

【0033】[0033]

【化3】2NH4 + +3HClO→N2 +3H2 O+5
+ +3Cl- のように反応しアンモニアは分解され無臭化される。こ
れらは、処理タンクにおいて次亜塩素酸ソーダが加えら
れた水を機能セラミックに通過接触させるため、触媒作
用により容易に加水分解され、先の〔化1〕に示したよ
うに次亜塩素酸と苛性ソーダを生成するからである。
## STR3 ## 2NH 4 + + 3HClO → N 2 + 3H 2 O + 5
Ammonia is decomposed and deodorized by reacting like H + + 3Cl . These are hydrolyzed easily by catalytic action in order to bring water containing sodium hypochlorite into contact with the functional ceramic in the treatment tank, and thus, as shown in [Chemical Formula 1] above, This is because it produces caustic soda.

【0034】また、水中にアンモニア又はアミンが存在
すると、塩素と結合してクロレラミン(NH2 Cl)を
生じる。アンモニア含有水に塩素を注入すると、残留塩
素(Clになっていない遊離性の塩素)は次第に増加す
るが、ある点で急に減少し始めて極小点に達し次いでま
た急に増えだす。この点を不連続点といい、アンモニア
などの還元物質のなくなった点であり、ここまでに添加
された塩素量を塩素要求量という。結合残留塩素水中に
窒素化合物として、アンモニア、アミン等と結合してい
る塩素が存在する。次亜塩素酸は、4HClO → 4
HCl+4Oの反応により殺菌・脱臭・シアン酸化を行
う。
When ammonia or amine is present in water, it combines with chlorine to produce chloreramine (NH 2 Cl). When chlorine is injected into ammonia-containing water, the residual chlorine (free chlorine that has not become Cl) gradually increases, but at some point, it begins to decrease sharply, reaches a local minimum, and then increases again. This point is called a discontinuity point, which is the point at which reducing substances such as ammonia have disappeared, and the amount of chlorine added up to this point is called the required chlorine amount. Bonded residual chlorine There is chlorine bonded to ammonia, amine, etc. as a nitrogen compound in the water. Hypochlorous acid is 4HClO → 4
Performs sterilization, deodorization and cyanidation by the reaction of HCl + 40.

【0035】さらに、硫化水素は、苛性ソーダと共にFurther, hydrogen sulfide is present together with caustic soda.

【0036】[0036]

【化4】 H2 S+NaOH → NaHS+H2 O NaHS+NaOH → Na2 S+H2 O Na2 S+4NaClO → Na2 SO4 +4NaC
l Na2 S+NaClO+H2 O → NaCl+NaO
H+S のように反応して分解され無臭化される。
Embedded image H 2 S + NaOH → NaHS + H 2 O NaHS + NaOH → Na 2 S + H 2 O Na 2 S + 4NaClO → Na 2 SO 4 + 4NaC
l Na 2 S + NaClO + H 2 O → NaCl + NaO
It reacts like H + S and is decomposed and deodorized.

【0037】例えば長く使用された水道管の内部に沈着
した赤コブや赤錆といわれる化合物の成分は、主として
水酸化鉄Fe(OH)3 で、他に炭酸カルシウムCaC
、炭酸マグネシウムMgCO、酸化鉄Fe2
3 、Fe3 4 等で構成されている。本発明に係る機能
セラミックを用いた脱臭浄化及び水触媒処理装置では、
触媒水の中に、先に述べたように次亜塩素酸HClOや
塩酸HClが生成されるので、
For example, the component of a compound called red hump or red rust deposited inside a long-used water pipe is mainly iron hydroxide Fe (OH) 3 , and calcium carbonate CaC.
O 3 , magnesium carbonate MgCO 3 , iron oxide Fe 2 O
3 , Fe 3 O 4, etc. In the deodorizing purification and water catalyst treatment device using the functional ceramic according to the present invention,
Since hypochlorous acid HClO and hydrochloric acid HCl are generated in the catalyst water as described above,

【0038】[0038]

【化5】 Fe(OH)3 +3HCl → FeCl3 +3H2 O CaCO3 +2HCl → CaCl2 +H2 CO3 のように反応し、Fe(OH)3 は可溶性のFeCl3
に、そして、CaCO3は可溶性のCaCl2 に変化
し、赤コブを溶解する。
Embedded image Fe (OH) 3 + 3HCl → FeCl 3 + 3H 2 O CaCO 3 + 2HCl → CaCl 2 + H 2 CO 3 reacts like Fe (OH) 3 is soluble FeCl 3
Then, CaCO 3 is changed into soluble CaCl 2 , which dissolves red cobb.

【0039】微生物による排水処理では、酵素(溶酸酵
素=DO)が存在するところに好んで生息する好気性微
生物を利用することにより、
In the wastewater treatment with microorganisms, by utilizing aerobic microorganisms that prefer to inhabit where an enzyme (hydrolytic enzyme = DO) exists,

【0040】[0040]

【化6】(好気性酸化) 有機物(Cx y z )+O2 +好気性微生物→ CO
2 +H2 O+微生物の活動エネルギー (微生物体の増殖) 有機物(Cx y z )+N化合物+O2 +好気性微生
物→ CO2 +H2 O+エネルギー(吸熱反応) のように反応し有機物が酸化分解して、微生物の活動エ
ネルギーと生物体の増殖に使われる。そのため、有機物
が酸化して炭化物になるので、有機物が炭化固形物にな
り、さらに粉末化して汚泥濃縮貯留槽から搬出される汚
泥の量を少なくすることができる。
(Aerobic oxidation) Organic matter (C x H y O z ) + O 2 + aerobic microorganism → CO
2 + H 2 O + activity energy of microorganisms (growth of microorganisms) Organic matter (C x H y O z ) + N compound + O 2 + aerobic microorganism → CO 2 + H 2 O + energy (endothermic reaction) and organic matter is oxidized It decomposes and is used for the active energy of microorganisms and the growth of organisms. Therefore, since the organic matter is oxidized to be a carbide, the organic matter becomes a carbonized solid matter, which is further powdered to reduce the amount of sludge carried out from the sludge concentration storage tank.

【0041】次に、具体的な実施例を説明する。第5図
は処理施設における本発明に係る脱臭浄化及び水触媒処
理装置の触媒水の使用前と使用後の硫化水素濃度の比較
例を示す図、図6は処理施設における本発明に係る脱臭
浄化及び水触媒処理装置の触媒水の使用前と使用後のメ
タンガス濃度の比較例を示す図である。機能セラミック
の粒体として、第1の粒体は、25φの球で、フェライ
ト系に磁性体、鉄、モリブデン、コバルト、チタン、マ
グネシウム、アルミニウム、カリウム、ジルコニウム、
珪素を含む18種類の金属酸化物を組み合わせ、第2の
粒体は、15φの球で、フェライト系に磁性体と鉄とマ
ンガン、コバルト、チタン、マグネシウム、アルミニウ
ム、カリウム、ジルコニウム、珪素を含む18種類の金
属酸化物を組み合わせ、第3の粒体は、15φの球で、
酸化アルミニウム、ジルコニア、珪藻土、チタン酸バリ
ウムを含む金属酸化物を組み合わせ焼結して、25kg
の重量の内訳として、第1及び第2の粒体と第3の粒体
との比率を95対5、第1の粒体と第2の粒体との比率
を7対3とした。つまり、第1の粒体を約16.525
kg、第2の粒体を7.125kg、第3の粒体を1.
250kgとした。
Next, a concrete example will be described. FIG. 5 is a diagram showing a deodorizing purification according to the present invention in a treatment facility and a comparative example of hydrogen sulfide concentration before and after use of catalytic water of a water catalyst treatment device, and FIG. 6 is a deodorizing purification according to the present invention in a treatment facility. FIG. 5 is a diagram showing a comparative example of methane gas concentration before and after using catalyst water of the water catalyst treatment device. As the functional ceramic particles, the first particles are spheres of 25φ, and ferrite-based magnetic material, iron, molybdenum, cobalt, titanium, magnesium, aluminum, potassium, zirconium,
18 kinds of metal oxides containing silicon are combined, the second particle is a 15φ sphere, and the ferrite system contains magnetic material and iron and manganese, cobalt, titanium, magnesium, aluminum, potassium, zirconium and silicon. Combining kinds of metal oxides, the third particle is a 15φ sphere,
25 kg by combining and sintering metal oxides containing aluminum oxide, zirconia, diatomaceous earth and barium titanate
As a breakdown of the weights, the ratio of the first and second particles to the third particles was 95: 5, and the ratio of the first particles to the second particles was 7: 3. That is, the first granules are about 16.525
kg, the second granules 7.125 kg, the third granules 1.
It was set to 250 kg.

【0042】この機能セラミックの粒体に1ppmの次
亜塩素酸ソーダを添加混合した原水を通過接触させるこ
とにより触媒作用を利用した水処理を行い触媒水を生成
し、この触媒水を農業集落排水、一般家庭生活雑排水の
排水処理場に使用したときの硫化水素濃度を示したのが
図5〜の▲、食品加工水処理場に使用したときの硫
化水素濃度を示したのが図5の以降の▲である。これ
に対して触媒水を使用する前の硫化水素濃度が図5のそ
れぞれ●である。農業集落排水、一般家庭生活雑排水の
排水処理場に触媒水を使用したときのメタンガス濃度、
触媒水を使用する前のメタンガス濃度を示したのが図6
である。機能セラミックの粒体が1kgに対する1時間
当たりの触媒水の量は、0.041〜0.043m3
hであった。
The functional ceramic granules are mixed with raw water containing 1 ppm of sodium hypochlorite so as to pass through and contact the raw water to perform catalytic water treatment to generate catalytic water. , Figure 5 shows the hydrogen sulfide concentration when it is used in the wastewater treatment plant for general household wastewater, and Figure 5 shows the hydrogen sulfide concentration when it is used in the food processing water treatment plant. The following is ▲. On the other hand, the hydrogen sulfide concentration before using the catalyst water is represented by ● in FIG. Methane gas concentration when catalytic water is used in wastewater treatment plants for agricultural village wastewater and general household wastewater,
Figure 6 shows the concentration of methane gas before using catalytic water.
Is. The amount of catalytic water per hour for 1 kg of functional ceramic particles is 0.041 to 0.043 m 3 /
It was h.

【0043】これらの試験の結果を通して、硫化水素、
メタンガスがほとんど発生しなくなり、農業集落排水、
一般家庭生活雑排水の排水処理では、1週間〜10日間
で臭気がほとんど感じられない程度に軽減し、また、曝
気後における活性汚泥の沈降速度が短縮され、従来の汚
泥発生量より1/3以上に軽減される等の効果が認めら
れた。また、工業用水分野では、食品工場で使用する水
を触媒水に切り換えたことにより、これまでの排水処理
施設での機能が向上し、放出される水質が格段に改善さ
れ、さらに汚泥残さやスラッジが極端に軽減された。
Through the results of these tests, hydrogen sulfide,
Almost no methane gas is generated, agricultural village drainage,
In the wastewater treatment of general domestic miscellaneous wastewater, odor is reduced to a level where it is hardly felt in one week to 10 days, and the sedimentation rate of activated sludge after aeration is shortened, which is 1/3 of the conventional sludge generation amount. The effects such as the above reduction were recognized. In the industrial water field, by switching the water used in food factories to catalytic water, the functions of existing wastewater treatment facilities have been improved, the quality of the discharged water has been dramatically improved, and sludge residue and sludge have been improved. Was significantly reduced.

【0044】また、レジャー用水分野では、ゴルフ場の
貯水池(噴水池)に対して触媒水を使用することによ
り、青藻がなくなり水が透明になった。散水に使用する
ことにより、芝枯れやもん枯れ等の病気、害虫が少なく
なり無農薬化を図ることができた。
Further, in the leisure water field, the use of catalytic water for the reservoir (fountain) of the golf course has made blue water disappeared and the water became transparent. By using it for watering, it was possible to reduce pesticides by reducing diseases such as dying of grass and wilting and pests.

【0045】これまでの検査データでは、pHが6.2
→7.5、BOD濃度が160→8.3mg/l、懸濁
物質が150→17mg/l、全窒素が19→3.2m
g/lの結果や、pHが7.1→7.6、BOD濃度が
36→7.0mg/l、懸濁物質が140→27mg/
l、全窒素が17→11mg/lの結果等が得られてい
る。
According to the inspection data so far, the pH is 6.2.
→ 7.5, BOD concentration 160 → 8.3 mg / l, suspended matter 150 → 17 mg / l, total nitrogen 19 → 3.2 m
g / l result, pH 7.1 → 7.6, BOD concentration 36 → 7.0 mg / l, suspended matter 140 → 27 mg /
1 and the total nitrogen content was 17 → 11 mg / l.

【0046】また、本発明に係る機能セラミックを用い
た脱臭浄化及び水触媒処理装置により生成された触媒水
を用いると、数時間後に端末蛇口からでる水の塩素臭が
なくなり、パイプ内の赤コブは4ケ月後にほとんど除去
される。したがって、下水道に放流すると、排水処理施
設や下水管の異臭がなくなる。このことは、エマルジョ
ン作用の向上と、遊離残留塩素が赤コブに消費されるこ
とがなくなり、その分下水道に多く遊離残留塩素が流れ
るために殺菌効果が上がることによるものと考えられ
る。
Further, when the catalytic water produced by the deodorizing purification and water catalyst treatment apparatus using the functional ceramics according to the present invention is used, the chlorine odor of the water discharged from the terminal faucet disappears after a few hours, and the red cobb in the pipe disappears. Is almost eliminated after 4 months. Therefore, when discharged into the sewer, the offensive odor of the wastewater treatment facility and the sewer pipe disappears. It is considered that this is because the emulsion action is improved and the free residual chlorine is not consumed by the red cob, and a large amount of the free residual chlorine flows into the sewer, which increases the sterilization effect.

【0047】先に示した〔化1〕の反応により生成され
るClO- は、ガスとして存在する二分子塩素Cl2
次亜塩素酸HClOに比し、活性であるため殺菌能力は
高い。実際に、サウナに併設された循環風呂(1日20
00人利用)で1dl、4000,000個の一般細菌
と16個の大腸菌が検出されていたが、本発明に係る機
能セラミックを用いた脱臭浄化及び水触媒処理装置によ
り生成された触媒水を使用後10日目の水質検査では、
一般細菌が3,500個に、大腸菌が0に減少し、さら
に1ケ月後には一般細菌と大腸菌がともに0となり著し
い効果を示した。
ClO produced by the reaction of the above [Chemical formula 1] has a high sterilizing ability because it is more active than the dimolecular chlorine Cl 2 and HClO existing as gas. In fact, a circulating bath attached to the sauna (20 a day
1 person, 4,000,000 general bacteria and 16 Escherichia coli were detected in 100 people), but the catalytic water generated by the deodorizing purification and water catalyst treatment device using the functional ceramic according to the present invention was used. In the water test on the 10th day after,
The number of general bacteria decreased to 3,500 and E. coli decreased to 0, and after one month, both general bacteria and E. coli decreased to 0, showing a remarkable effect.

【0048】なお、本発明は、上記実施の形態に限定さ
れるものではなく、種々の変形が可能である。例えば上
記実施の形態では、機能セラミックの触媒水を利用した
脱臭浄化及び水触媒処理装置や水処理システム及び方法
を説明したが、排気筒や排煙筒、空気清浄器の空気導入
部を触媒水の中に導入し排気や排煙、給気を気泡にして
通したり、触媒水を排気筒や排煙筒、空気清浄器の空気
導入部に霧化して供給することにより、排気や排煙、給
気の浄化に利用するように構成してもよいし、脱臭浄化
及び水触媒処理装置に悪臭成分含有ガスではなく通常の
空気を送り込むようにして、単に触媒水を生成する装置
として用いてもよい。タンク内に貯留する触媒水のレベ
ルを中間のレベルに設定したが、ノズルのある上部のレ
ベルまで上げてもよい。また、触媒水の一部又は全部を
循環させるようにして、原水と次亜塩素酸ソーダ又は塩
素をその消耗に応じて適宜補充し、ガスの脱臭浄化装置
として用いるようにしてもよいし、さらにその一部を触
媒水として取り出して用いるようにしてもよい。
The present invention is not limited to the above embodiment, but various modifications can be made. For example, in the above-described embodiment, the deodorizing purification and water catalyst treatment device and the water treatment system and method using the catalytic water of the functional ceramic have been described, but the exhaust pipe, the smoke exhaust pipe, and the air introduction portion of the air purifier have the catalytic water. Introduce it into the exhaust and smoke, and supply air as air bubbles, or atomize the catalyst water to the exhaust pipe, smoke stack, and air inlet of the air purifier to supply exhaust, smoke, and air supply. It may be configured to be used for purification of water, or may be used as a device for simply producing catalyst water by sending normal air instead of the malodorous component-containing gas to the deodorization purification and water catalyst treatment device. Although the level of the catalyst water stored in the tank is set to the intermediate level, it may be raised to the level above the nozzle. Also, by circulating a part or all of the catalyst water, raw water and sodium hypochlorite or chlorine may be appropriately replenished according to its consumption, and may be used as a deodorizing and purifying device for gas. You may make it take out a part of it as catalyst water and use it.

【0049】その他、例えば畜産の入荷の際のボデー洗
浄、トラックの洗浄、脱臭、場内の消毒、汚物の洗浄排
出クリーンルーム化等に触媒水を使用することにより、
これらの排水の水質改善浄化の効果を高めることができ
る。また、本発明に係る触媒水は、グリストラップ(油
水分離槽)のnヘキサン改善、水道間の赤サビ赤水防
止、クーリングタワーのシリカ解消、水質改善、コンデ
ンサ冷却効果のアップ、省エネ、ボイラーの清管剤、脱
酸剤の低減、クリーンルーム化(床のヌメリ、まな板、
搬送機、洗浄殺菌等を目的として利用することができ、
アルカリ水、溶解しにくく固い、塩素臭のない製氷水、
三枚下ろし身裂きしない、ドリップ現象なしの解凍水と
して利用することができる。
In addition, for example, by using the catalyst water for body cleaning at the time of arrival of livestock, truck cleaning, deodorization, disinfection on the premises, and cleaning and discharging of filth into a clean room,
The effect of water quality improvement purification of these wastewaters can be enhanced. Further, the catalyst water according to the present invention is used to improve n-hexane in grease trap (oil / water separation tank), prevent red rust red water between water supplies, eliminate silica in cooling tower, improve water quality, improve condenser cooling effect, save energy, and clean boiler pipe. Of cleansing agent and deoxidizer, clean room (floor slimming, cutting board,
Can be used for the purpose of transporting machines, cleaning and sterilization, etc.
Alkaline water, hard to dissolve and hard, ice-making water without chlorine odor,
It can be used as thaw water without dropping the three pieces and without dripping.

【0050】[0050]

【発明の効果】以上の説明から明らかなように、本発明
によれば、バインダーとして樹脂やガラスを使用し、フ
ェライト系に少なくとも磁性体や鉄、コバルト、チタン
等の複数種類の金属酸化物を組み合わせたものを焼結し
てなる複数の機能セラミックの粒体に原水に次亜塩素酸
ソーダ又は塩素を添加した水溶液を通過接触させて、触
媒作用により次亜塩素酸を生成し、高い脱臭、殺菌、油
分解等の効果を向上させることができ、簡単な構成、シ
ステムでガスの脱臭浄化、水浄化処理の効率を向上させ
ることができる。しかも、触媒水は、そのまま水として
業務用として使用した後に排水処理施設に放流すること
により、通常の水道水等を使用水とした場合に比べて処
理効果を高めることができ、また、排水処理施設で処理
する各種雑排水、廃油などに加えることにより、触媒水
を加えない場合に比べて廃棄する際の処理効果を高める
ことができる。したがって、排水処理施設を省力化する
ことも可能となり、通常使用する水道水等から処理タン
クを通して触媒水を生成し、水質改善した使用水として
広汎な様々な用途に利用することができ、これらの利用
による水質向上、排水処理での水質向上の効果は顕著で
ある。
As is apparent from the above description, according to the present invention, a resin or glass is used as a binder, and at least a magnetic material and a plurality of kinds of metal oxides such as iron, cobalt and titanium are added to a ferrite system. An aqueous solution of sodium hypochlorite or chlorine added to the raw water is passed through contact with a plurality of functional ceramic granules obtained by sintering the combined product, and hypochlorous acid is produced by the catalytic action, resulting in high deodorization, The effects such as sterilization and oil decomposition can be improved, and the efficiency of gas deodorization purification and water purification treatment can be improved with a simple configuration and system. Moreover, the catalytic water can be used as it is for commercial use, and then discharged to a wastewater treatment facility to enhance the treatment effect compared to the case where ordinary tap water is used. By adding it to various kinds of waste water, waste oil, etc. to be treated in the facility, the treatment effect at the time of disposal can be enhanced as compared with the case where no catalytic water is added. Therefore, it becomes possible to save labor in the wastewater treatment facility, generate catalytic water from the tap water or the like that is normally used through the treatment tank, and use it for a wide variety of uses as water with improved water quality. The effect of water quality improvement by use and water quality improvement in wastewater treatment is remarkable.

【0051】本発明に係る触媒水の使用によれば、水処
理の分野では、赤コブ、赤水の除去、脱塩素臭(スイミ
ングプール)、殺菌作用の向上(大衆浴場、スイミング
プール、ゴルフ場のグリーン)、防蝕に顕著な効果があ
り、空気を媒体とした分野では、爽やかな空調(フィッ
トネスクラブ、サウナ、ホテルルーム、コンピュータル
ーム)、クリーンルームの除塵効果の向上、無菌室(手
術室、治療室、食品加工室)、冷凍庫の除霜と冷凍効率
の向上等に顕著な効果があり、廃油処理での油水分離に
顕著な効果があることが確認されている。
According to the use of the catalytic water according to the present invention, in the field of water treatment, removal of red lumps, red water, dechlorination odor (swimming pool), and improvement of bactericidal action (in public baths, swimming pools, golf courses) Green), has a remarkable effect on anticorrosion, and in the field that uses air as a medium, refreshing air conditioning (fitness club, sauna, hotel room, computer room), improvement of dust removal effect in clean room, sterile room (operating room, treatment room) , Food processing room), freezer, defrosting, and improvement of freezing efficiency are remarkable, and it is confirmed that there is a remarkable effect in oil-water separation in waste oil treatment.

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

【図1】 本発明に係る機能セラミックを用いた脱臭浄
化及び水触媒処理装置の実施の形態を示す図である。
FIG. 1 is a diagram showing an embodiment of a deodorizing purification and water catalyst treatment device using a functional ceramic according to the present invention.

【図2】 本発明に係る機能セラミックを用いた脱臭浄
化及び水触媒処理装置を利用した水処理システムの実施
の形態を示す図である。
FIG. 2 is a diagram showing an embodiment of a water treatment system utilizing a deodorizing purification and a water catalyst treatment device using a functional ceramic according to the present invention.

【図3】 本発明に係る触媒水使用方法の実施の形態を
示す図である。
FIG. 3 is a diagram showing an embodiment of a method of using catalytic water according to the present invention.

【図4】 排水処理施設の構成例を示す図である。FIG. 4 is a diagram showing a configuration example of a wastewater treatment facility.

【図5】 処理施設における本発明に係る脱臭浄化及び
水触媒処理装置の触媒水の使用前と使用後の硫化水素濃
度の比較例を示す図である。
FIG. 5 is a diagram showing a comparative example of hydrogen sulfide concentration before and after use of catalyst water of the deodorizing purification and water catalyst treatment device according to the present invention in a treatment facility.

【図6】 処理施設における本発明に係る脱臭浄化及び
水触媒処理装置の触媒水の使用前と使用後のメタンガス
濃度の比較例を示す図である。
FIG. 6 is a diagram showing a comparative example of methane gas concentration before and after use of catalyst water in the deodorizing purification and water catalyst treatment device according to the present invention in a treatment facility.

【符号の説明】[Explanation of symbols]

1…処理タンク、2…機能セラミックの粒体、3…カ
ゴ、4…給気部、5…排気部、6…給水部、7…排水
部、8〜11…バルブ、12…排気ファン、13…触媒
水、14…散水ノズル
DESCRIPTION OF SYMBOLS 1 ... Processing tank, 2 ... Functional ceramic granules, 3 ... Basket, 4 ... Air supply part, 5 ... Exhaust part, 6 ... Water supply part, 7 ... Drainage part, 8-11 ... Valve, 12 ... Exhaust fan, 13 … Catalyst water, 14… Sprinkling nozzle

─────────────────────────────────────────────────────
─────────────────────────────────────────────────── ───

【手続補正書】[Procedure amendment]

【提出日】平成11年8月2日(1999.8.2)[Submission date] August 2, 1999 (August 1999)

【手続補正1】[Procedure Amendment 1]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】発明の名称[Name of item to be amended] Title of invention

【補正方法】変更[Correction method] Change

【補正内容】[Correction content]

【発明の名称】 機能セラミックを用いた脱臭浄化及
び水触媒処理装置
Title: Deodorizing purification and water catalyst treatment device using functional ceramics

【手続補正2】[Procedure Amendment 2]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】特許請求の範囲[Name of item to be amended] Claims

【補正方法】変更[Correction method] Change

【補正内容】[Correction content]

【特許請求の範囲】[Claims]

【手続補正3】[Procedure 3]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0010[Correction target item name] 0010

【補正方法】変更[Correction method] Change

【補正内容】[Correction content]

【0010】そのために本発明は、機能セラミックの触
媒作用を利用して気体の脱臭浄化を行うと共に水処理を
行い触媒水を生成する機能セラミックを用いた脱臭浄化
及び水触媒処理装置であって、底付近に気体を導入する
給気部と触媒水を取り出す排水部とを有し、天井付近に
気体を排気する排気部と水溶液を導入しシャワリングす
る散水ノズルを含む給水部とを有する処理タンクと、バ
インダーとして樹脂やガラスを使用し、少なくともフェ
ライト系に磁性体や鉄、コバルト、チタン等の複数種類
の金属酸化物を組み合わせたものを焼結してなる複数の
機能セラミックの粒体を混合して収容し前記処理タンク
内の給気部と排気部との間に配置される複数段のカゴ
と、底付近の前記排水部より取り出す触媒水を前記カゴ
の1乃至複数段が浸されるように前記処理タンクの所定
レベルに貯留、維持させる触媒水貯留維持手段とを備
え、天井付近の前記給水部より次亜塩素酸ソーダ又は塩
素を添加した水溶液をシャワリングして前記複数の機能
セラミックの粒体と通過接触させ所内レベルに貯留して
触媒水を生成し底付近の排水部より取り出し、逆に底付
近の前記給気部より気体を導入することにより、前記触
媒水の中を気泡にしその中に浸された前記複数の機能セ
ラミックの粒体及び触媒水と通過接触させると共に、前
記触媒水の上方で前記シャワリングされた前記複数の機
能セラミック及び触媒水と通過接触させて天井付近の前
記排気部より脱臭浄化した気体を排気するように構成し
たことを特徴とするものである。
To this end, the present invention provides a deodorizing purification and water catalyst treatment apparatus using a functional ceramic that uses the catalytic action of a functional ceramic to deodorize and purify gas and to treat water to generate catalytic water. A treatment tank having an air supply part for introducing gas near the bottom and a drain part for taking out catalyst water, and an exhaust part for exhausting gas near the ceiling and a water supply part including a sprinkling nozzle for introducing and showering an aqueous solution. And, using resin or glass as a binder, mixing at least a plurality of functional ceramic particles obtained by sintering at least a ferrite-based material and a combination of multiple types of metal oxides such as iron, cobalt, titanium, etc. And a plurality of stages of baskets that are housed in the treatment tank and arranged between the air supply unit and the exhaust unit in the processing tank, and one or more stages of the baskets are filled with catalyst water taken out from the drainage unit near the bottom. As described above, the catalyst water storage / maintenance means for storing and maintaining the treatment tank at a predetermined level is provided, and the aqueous solution containing sodium hypochlorite or chlorine is showered from the water supply portion near the ceiling to perform the plurality of functions. The catalyst water is stored in the in-house level by passing it through the ceramic granules to generate catalyst water, which is taken out from the drainage section near the bottom, and conversely, by introducing gas from the air supply section near the bottom, the inside of the catalyst water is removed. Ceilings are brought into contact with the granules of the plurality of functional ceramics and the catalyst water immersed in the bubbles and the catalyst water, and are brought into contact with the plurality of showering functional ceramics and the catalyst water above the catalyst water. It is characterized in that the deodorized and purified gas is exhausted from the nearby exhaust unit.

【手続補正4】[Procedure amendment 4]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0011[Correction target item name] 0011

【補正方法】削除[Correction method] Delete

【手続補正5】[Procedure Amendment 5]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0012[Correction target item name] 0012

【補正方法】削除[Correction method] Delete

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) C02F 1/50 550 C02F 1/50 550C 560 560Z 560H 3/06 3/06 3/12 3/12 U Fターム(参考) 4D003 AA01 AA08 BA02 CA03 CA07 CA08 CA10 EA30 EA38 EA40 4D028 AA03 AB01 AB03 AC03 AC05 AC09 BD06 4D048 AA21 AA22 AB01 AB02 AB03 BA01X BA01Y BA03X BA03Y BA06X BA06Y BA07X BA07Y BA08X BA08Y BA09X BA09Y BA10X BA10Y BA12X BA12Y BA14X BA14Y BA15X BA15Y BA26X BA26Y BA28X BA28Y BA36X BA36Y BA37X BA37Y BA41X BA41Y BA42X BA42Y BA50X BA50Y BB01 CA02 CA07 CC38 CD02 CD10 EA10─────────────────────────────────────────────────── ─── Continuation of front page (51) Int.Cl. 7 Identification code FI theme code (reference) C02F 1/50 550 C02F 1/50 550C 560 560Z 560H 3/06 3/06 3/12 3/12 UF Terms (reference) 4D003 AA01 AA08 BA02 CA03 CA07 CA08 CA10 EA30 EA38 EA40 4D028 AA03 AB01 AB03 AC03 AC05 AC09 BD06 4D048 AA21 AA22 AB01 AB02 AB03 BA01X BA01Y BA03X BA03YBAX BA15YBAX BA15YBAX BA15YBAX BA10YBAX BA08Y BA08X BA08Y BA08Y BA08Y BA08Y BA08X BA08X BA26Y BA28X BA28Y BA36X BA36Y BA37X BA37Y BA41X BA41Y BA42X BA42Y BA50X BA50Y BB01 CA02 CA07 CC38 CD02 CD10 EA10

Claims (8)

【特許請求の範囲】[Claims] 【請求項1】 機能セラミックの触媒作用を利用して気
体の脱臭浄化を行うと共に水処理を行い触媒水を生成す
る機能セラミックを用いた脱臭浄化及び水触媒処理装置
であって、底付近に気体を導入する給気部と触媒水を取
り出す排水部とを有し、天井付近に気体を排気する排気
部と水溶液を導入しシャワリングする散水ノズルを含む
給水部とを有する処理タンクと、バインダーとして樹脂
やガラスを使用し、フェライト系に少なくとも磁性体や
鉄、コバルト、チタン等の複数種類の金属酸化物を組み
合わせたものを焼結してなる複数の機能セラミックの粒
体を混合して収容し前記処理タンク内の給気部と排気部
との間に配置される複数のカゴとを備え、前記給水部よ
り次亜塩素酸ソーダ又は塩素を添加した水溶液を導入し
て前記複数の機能セラミックの粒体の上方よりシャワリ
ングすると共に、前記給気部より気体を導入してそれぞ
れ前記複数の機能セラミックの粒体と通過接触させるこ
とにより機能セラミックの触媒作用を利用して気体の脱
臭浄化と触媒水の生成を行い、前記生成した触媒水を底
部より所定レベルまで貯留して前記底付近の前記排水部
より取り出すように構成したことを特徴とする機能セラ
ミックを用いた脱臭浄化及び水触媒処理装置。
1. A deodorizing purification and water catalyst treatment apparatus using a functional ceramic that performs catalytic deodorization and purification of gas by using the catalytic action of functional ceramic, and also performs water treatment to generate catalytic water, wherein the gas is near the bottom. A treatment tank having an air supply part for introducing and a drainage part for taking out catalyst water, and an exhaust part for exhausting gas near the ceiling and a water supply part including a water spray nozzle for introducing and showering an aqueous solution, and as a binder A resin or glass is used, and a plurality of functional ceramic granules made by sintering at least a ferrite and a combination of at least a magnetic material and a plurality of types of metal oxides such as iron, cobalt, and titanium are mixed and housed. The treatment tank is provided with a plurality of baskets arranged between an air supply section and an exhaust section, and the aqueous solution containing sodium hypochlorite or chlorine is introduced from the water supply section to introduce the plurality of functional separators. De-odorizing and purifying gas by utilizing the catalytic action of functional ceramics by showering from above the Lamic particles and introducing gas from the air supply unit to bring them into contact with the granular particles of the functional ceramics. And a catalyst catalyst water is generated, and the generated catalyst water is stored from the bottom portion to a predetermined level and is taken out from the drainage portion near the bottom portion. Processing equipment.
【請求項2】 前記貯留する前記触媒水の所定レベル
は、前記複数のカゴの段数の2分の1の段数までのレベ
ルであることを特徴とする請求項1記載の機能セラミッ
クを用いた脱臭浄化及び水触媒処理装置。
2. The deodorization using a functional ceramic according to claim 1, wherein the predetermined level of the catalyst water to be stored is a level up to half the number of stages of the plurality of baskets. Purification and water catalyst treatment equipment.
【請求項3】 前記カゴは、前記機能セラミックの成分
濃度の異なる複数種の粒体を混合して収容したものであ
ることを特徴とする請求項1記載の機能セラミックを用
いた脱臭浄化及び水触媒処理装置。
3. The deodorizing purification and water using the functional ceramics according to claim 1, wherein the basket contains a plurality of types of granules having different component concentrations of the functional ceramics, which are mixed and housed. Catalyst processing equipment.
【請求項4】 前記排水部と給水部との間に触媒水を循
環させる手段を備えたことを特徴とする請求項1記載の
機能セラミックを用いた脱臭浄化及び水触媒処理装置。
4. The deodorizing purification and water catalyst treatment device using a functional ceramic according to claim 1, further comprising means for circulating catalytic water between the drainage section and the water supply section.
【請求項5】 嫌気性濾床槽、好気性濾床槽、沈殿槽、
汚泥槽を備えた排水処理施設により各種排水に対する水
質改善浄化の処理を行う水処理システムにおいて、バイ
ンダーとして樹脂やガラスを使用し、フェライト系に少
なくとも磁性体や鉄、コバルト、チタン等の複数種類の
金属酸化物を組み合わせたものを焼結してなる複数の機
能セラミックの粒体を混合して処理タンクに収容し、原
水に次亜塩素酸ソーダを添加した水溶液を前記処理タン
クに導入し該水溶液を前記機能セラミックの粒体に通過
接触させることにより触媒作用を利用した水処理を行い
触媒水を生成する水触媒処理装置と、該水触媒処理装置
により生成された触媒水を前記各種の未処理排水に混合
する混合手段とを備え、前記触媒水を前記各種の未処理
排水に混合して排水処理を行うように構成したことを特
徴とする機能セラミックを用いた水触媒処理装置利用水
処理システム。
5. An anaerobic filter bed tank, an aerobic filter bed tank, a precipitation tank,
In a water treatment system that performs water quality improvement and purification treatment on various types of wastewater with a wastewater treatment facility equipped with a sludge tank, resin or glass is used as a binder, and at least a magnetic material and a plurality of types of iron, cobalt, titanium, etc. are added to the ferrite system. A plurality of functional ceramic particles obtained by sintering a combination of metal oxides are mixed and housed in a treatment tank, and an aqueous solution obtained by adding sodium hypochlorite to raw water is introduced into the treatment tank. Water catalyst treatment apparatus for generating catalytic water by conducting water treatment utilizing catalytic action by passing and contacting with the functional ceramic granules, and the catalyst water generated by the water catalyst treatment apparatus is treated with the various untreated materials. And a mixing means for mixing with the waste water, wherein the catalyst water is mixed with the various untreated waste water to perform waste water treatment. Water catalytic treatment apparatus utilizing water treatment system using the click.
【請求項6】 水触媒処理装置は、前記原水として前記
排水処理施設から放出される処理済排水から一部抽出す
る抽出手段を有し、前記処理済排水の一部を原水として
循環させ、生成した触媒水を各種排水に混合して排水処
理を行うように構成したことを特徴とする機能セラミッ
クを用いた水触媒処理装置利用水処理システム。
6. The water catalyst treatment device has extraction means for partially extracting the treated wastewater discharged from the wastewater treatment facility as the raw water, and circulates a part of the treated wastewater as raw water to generate the raw water. A water treatment system using a water catalyst treatment device using a functional ceramic, characterized in that the catalyst water is mixed with various kinds of wastewater to perform wastewater treatment.
【請求項7】 使用済排水が排水処理施設により水質改
善浄化の処理を行って放流される水使用施設において、
バインダーとして樹脂やガラスを使用し、フェライト系
に少なくとも磁性体や鉄、コバルト、チタン等の複数種
類の金属酸化物を組み合わせたものを焼結してなる複数
の機能セラミックの粒体を混合して処理タンクに収容し
た水触媒処理装置原水を導入し、該原水に次亜塩素酸ソ
ーダを添加した水溶液を前記機能セラミックの粒体に通
過接触させることにより触媒作用を利用した水処理を行
い生成される触媒水を前記水使用施設で使用する水とし
て供給することを特徴とする触媒水使用方法。
7. A water use facility in which used wastewater is discharged after being treated by a wastewater treatment facility for water quality improvement purification.
Resin or glass is used as a binder, and a mixture of a plurality of functional ceramic particles obtained by sintering a ferrite-based material and at least a magnetic material and a combination of a plurality of types of metal oxides such as iron, cobalt, and titanium are sintered. A water catalyst treatment device housed in a treatment tank is introduced, and an aqueous solution obtained by adding sodium hypochlorite to the raw water is passed through and brought into contact with the functional ceramic granules to carry out a water treatment utilizing a catalytic action to generate the water. A method for using catalytic water, comprising supplying catalytic water as water to be used in the water use facility.
【請求項8】 バインダーとして樹脂やガラスを使用
し、フェライト系に少なくとも磁性体や鉄、コバルト、
チタン等の複数種類の金属酸化物を組み合わせたものを
焼結してなる複数の機能セラミックの粒体を混合して処
理タンクに収容した水触媒処理装置に原水を導入し、該
原水に次亜塩素酸ソーダ又は塩素を添加した水溶液を前
記機能セラミックの粒体に通過接触させることにより触
媒作用を利用した水処理を行い生成される触媒水をグリ
ースその他の廃油に混合して廃油処理を行うことを特徴
とする触媒水使用方法。
8. A resin or glass is used as a binder, and at least a magnetic material, iron, cobalt,
Raw water is introduced into a water catalyst treatment device that is mixed with a plurality of functional ceramic particles obtained by sintering a combination of a plurality of types of metal oxides such as titanium, and the raw water is introduced into the water catalyst treatment device. Performing waste oil treatment by mixing water produced by catalytic action by passing an aqueous solution containing sodium chlorate or chlorine through the functional ceramic granules and contacting the resulting catalyst water with grease or other waste oil. And a method of using catalytic water.
JP10234142A 1998-08-20 1998-08-20 Deodorizing purification and water catalyst treatment equipment using functional ceramics Expired - Fee Related JP3074266B2 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP10234142A JP3074266B2 (en) 1998-08-20 1998-08-20 Deodorizing purification and water catalyst treatment equipment using functional ceramics
KR1019990021330A KR20000016879A (en) 1998-08-20 1999-06-09 Water-Catalyst Treating Apparatus Using Function Ceramic, Liquid Discharging System Using Water-Catalyst Treating Apparatus, and Water-Catalyst Using Method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10234142A JP3074266B2 (en) 1998-08-20 1998-08-20 Deodorizing purification and water catalyst treatment equipment using functional ceramics

Related Child Applications (1)

Application Number Title Priority Date Filing Date
JP21825499A Division JP3461470B2 (en) 1999-08-02 1999-08-02 Wastewater treatment system using catalytic water of functional ceramic

Publications (2)

Publication Number Publication Date
JP2000061266A true JP2000061266A (en) 2000-02-29
JP3074266B2 JP3074266B2 (en) 2000-08-07

Family

ID=16966310

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (2)

Country Link
JP (1) JP3074266B2 (en)
KR (1) KR20000016879A (en)

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JP2002096078A (en) * 2000-09-25 2002-04-02 Suirei:Kk Purifying unit and purifying system for raw water such as polluted water, waste water or the like equipped with catalyst device
JP2008068248A (en) * 2006-08-17 2008-03-27 Hitachi Housetec Co Ltd Solid phosphorus removing agent, method for producing the same, method for dissolving the same in water, apparatus for dissolving the same and waste water cleaning tank equipped with the apparatus
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Publication number Priority date Publication date Assignee Title
JP2002085937A (en) * 2000-09-12 2002-03-26 Nagao Kk Process and equipment for deodorization
JP2002096078A (en) * 2000-09-25 2002-04-02 Suirei:Kk Purifying unit and purifying system for raw water such as polluted water, waste water or the like equipped with catalyst device
KR20010078909A (en) * 2001-05-16 2001-08-22 류성춘 Magnetic field soot purification water spray communication
JP2008068248A (en) * 2006-08-17 2008-03-27 Hitachi Housetec Co Ltd Solid phosphorus removing agent, method for producing the same, method for dissolving the same in water, apparatus for dissolving the same and waste water cleaning tank equipped with the apparatus
CN109942158A (en) * 2019-05-06 2019-06-28 湖南泰瑞医疗科技有限公司 Sewage disposal system

Also Published As

Publication number Publication date
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KR20000016879A (en) 2000-03-25

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