JP3453129B2 - Water purification promoter and water purification method and purification system using this purification promoter - Google Patents

Water purification promoter and water purification method and purification system using this purification promoter

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Publication number
JP3453129B2
JP3453129B2 JP2001233134A JP2001233134A JP3453129B2 JP 3453129 B2 JP3453129 B2 JP 3453129B2 JP 2001233134 A JP2001233134 A JP 2001233134A JP 2001233134 A JP2001233134 A JP 2001233134A JP 3453129 B2 JP3453129 B2 JP 3453129B2
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JP
Japan
Prior art keywords
water
purification
powder
shell
filter medium
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.)
Expired - Fee Related
Application number
JP2001233134A
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Japanese (ja)
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JP2003039086A (en
Inventor
則一 小泉
斉 小泉
Original Assignee
斉 小泉
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Application filed by 斉 小泉 filed Critical 斉 小泉
Priority to JP2001233134A priority Critical patent/JP3453129B2/en
Publication of JP2003039086A publication Critical patent/JP2003039086A/en
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Publication of JP3453129B2 publication Critical patent/JP3453129B2/en
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Expired - Fee Related legal-status Critical Current

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Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage
    • 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
    • Y02W10/30Wastewater or sewage treatment systems using renewable energies
    • Y02W10/37Wastewater or sewage treatment systems using renewable energies using solar energy

Landscapes

  • Immobilizing And Processing Of Enzymes And Microorganisms (AREA)
  • Micro-Organisms Or Cultivation Processes Thereof (AREA)
  • Biological Treatment Of Waste Water (AREA)
  • Treatment Of Biological Wastes In General (AREA)
  • Activated Sludge Processes (AREA)
  • Apparatus Associated With Microorganisms And Enzymes (AREA)

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、カキ類、アコヤ貝
等の二枚貝の貝殻や活性汚泥法等による水の接触浄化法
おいて、前記の濾材中の微生物に接触させて水の浄化を
促進する浄化促進剤と、この浄化促進剤を使用した水の
浄化方法及び浄化システムに関する。
TECHNICAL FIELD The present invention relates to a method for contact purification of water by bivalve shells such as oysters and pearl oysters, and an activated sludge method, which promotes purification of water by contacting with microorganisms in the filter medium. The present invention relates to a purification accelerator, and a method and system for purifying water using the purification accelerator.

【0002】[0002]

【従来の技術】従来、生活排水、河川や湖沼などの水処
理に、活性汚泥法が広く利用されているが、活性汚泥法
は、処理後に汚泥が多量に生成してバルキング現象を起
こし、その処理が煩わしいこと、汚水の流入量の変動や
BOD濃度の変動に対応し難い場合があること、活性の
維持や装置の維持管理が面倒であること、海水と淡水の
両方に併用することが困難であること、などの問題点を
有している。そこで、本願発明者は、前記の問題点を解
消すべく、カキ殻接触浄化法及びカキ殻接触浄化装置に
関する発明について先に特許出願した(特願昭62−7
1768)。
2. Description of the Related Art Conventionally, the activated sludge method has been widely used for the treatment of domestic wastewater, rivers and lakes, but the activated sludge method causes a large amount of sludge after the treatment to cause a bulking phenomenon. The treatment is complicated, it may be difficult to deal with the fluctuation of the inflow of wastewater and the fluctuation of the BOD concentration, the maintenance of the activity and the maintenance of the equipment are troublesome, and it is difficult to use it for both seawater and freshwater. There are problems such as being. Therefore, in order to solve the above problems, the inventor of the present application has previously filed a patent application for an invention relating to an oyster shell contact purification method and an oyster shell contact purification apparatus (Japanese Patent Application No. 62-7).
1768).

【0003】前記の特許出願に係るカキ殻接触浄化法に
よれば、前記の活性汚泥法に伴う問題点が概ね解消され
る。しかし、活性汚泥法やカキ殻接触浄化法などの微生
物処理の浄化装置を初めて稼動する際に、微生物群が浄
化作用を呈するに至る期間、即ち浄化装置を立ち上げる
までの期間として、一般に、3ヶ月乃至6ヶ月以上を要
し、この間は未処理水が放出されることとなり無駄であ
るだけでなく、特に大型処理槽の場合には、微生物の所
謂種付け(Seeding)に長年の経験が要求され、
一部の経験者や専門業者に任せ切りになり、工期遅延の
原因となるなどの弊害が多いことから、もっと簡単に種
付けができて、装置を立ち上げるまでの期間を短縮でき
る方法の開発についての要望があった。
According to the oyster shell contact purification method according to the above-mentioned patent application, the problems associated with the activated sludge method are almost solved. However, when the purification apparatus for microbial treatment such as the activated sludge method and the oyster shell contact purification method is first operated, the period until the microbial group exhibits the purification action, that is, the period until the purification apparatus is started up is generally 3 It takes 6 months to 6 months or more, and untreated water is discharged during this period, which is wasteful. In particular, in the case of a large treatment tank, many years of experience are required for so-called seeding of microorganisms. ,
Since there are many negative effects such as leaving the work to some experienced persons and specialists and causing a delay in the construction period, we will develop a method that can more easily seed and shorten the time until the equipment starts up. Was requested.

【0004】[0004]

【発明が解決しようとする課題】そこで、本願発明者
は、更に鋭意研究した結果、カキ殻等の浄化能力は、カ
キ殻等の表面の付着物中に生息する微生物類に由来する
ものであり、この付着物中に含まれるバクテリア等の微
生物群が、ある条件のもとで乾燥すると休眠状態に入
り、この休眠状態の微生物群を富栄養化溶液中に投入す
ると、蘇生して濾材中の微生物群を活性化する機能を有
することを知見して、本願発明に到ったものである。本
願発明は、活性汚泥法やカキ殻接触浄化法などの微生物
処理の浄化装置を初めて稼動する際に浄化作用を発揮す
るまでの立ち上げ期間を大幅に短縮でき、且つ、カキな
どの貝殻などに付着する微生物群が本来有する浄化能力
を助長することによって、大腸菌等の細菌に対する滅菌
効果を併せ有する水の浄化促進剤と、この浄化促進剤を
使用した水の浄化方法及び浄化システムを提供すること
を目的とする。
Therefore, as a result of further studies, the present inventor has found that the ability to purify oyster shells and the like is derived from microorganisms inhabiting the adherents on the surface of oyster shells and the like. , Microorganisms such as bacteria contained in this adhered substance enter a dormant state when dried under a certain condition, and when the dormant microorganisms are put into an eutrophication solution, they are revived and contained in the filter medium. The inventors of the present invention have reached the present invention by finding that they have a function of activating a microbial group. INDUSTRIAL APPLICABILITY The present invention can greatly shorten the start-up period until the purifying action is exhibited when the purifying apparatus for microbial treatment such as the activated sludge method and the oyster shell contact purification method is operated for the first time, and can be applied to shells such as oysters. To provide a water purification accelerator having a sterilizing effect on bacteria such as Escherichia coli, and a water purification method and a purification system using the purification accelerator by promoting the original purification ability of the attached microorganism group. With the goal.

【0005】[0005]

【課題を解決するための手段】前記の課題を解決するた
めに、本発明は、カキ類、アコヤ貝よりなる群から選択
される二枚貝の一種又はニ種以上からなる二枚貝の貝殻
の表面に付着している微生物を含む付着物を乾燥させる
ことによって微生物を休眠状態にした前記付着物の粉体
と無機質粉体との混合物を含むことを特徴とする水の浄
化促進剤とする(請求項1)。
[Means for Solving the Problems] In order to solve the above-mentioned problems, the present invention is directed to the surface of the shell of a bivalve shell consisting of one or two or more species of bivalves selected from the group consisting of oysters and pearl oysters. A purification agent for water, comprising a mixture of a powder of the adhering matter in which the microorganisms are in a dormant state by drying the adhering matter containing the microorganisms and an inorganic powder (claim 1). ).

【0006】また、前記の課題を解決するために、本発
明は、カキ類、アコヤ貝よりなる群から選択される二枚
貝の一種又はニ種以上からなる二枚貝の貝殻の表面に付
着している微生物を含む付着物を乾燥させることによっ
て微生物を休眠状態にした前記付着物の粉体と、無機質
粉体と、フミン酸及び/又はフルボ酸と、鉄及び/又は
鉄の化合物と、海藻類を含む栄養源と、の混合物を含む
ことを特徴とする水の浄化促進剤とする(請求項2)。
In order to solve the above-mentioned problems, the present invention provides a microorganism attached to the surface of the shell of a bivalve shell consisting of one or two or more species of bivalve selected from the group consisting of oysters and pearl oysters. A powder of the deposit in which the microorganisms are put into a dormant state by drying the deposit containing the substance, an inorganic powder, humic acid and / or fulvic acid, iron and / or a compound of iron, and seaweed A water purification accelerator comprising a mixture of a nutrient source and the nutrient source (claim 2).

【0007】また、前記の課題を解決するために、本発
明は、前記の無機質粉体が、ベントナイト粉、モンモリ
ロナイト粉、ドロマイト粉、珪藻土粉、カオリン粉及び
これらの何れかと実質的に同一の成分からなる土粉の群
から選択される何れか一種又はニ種以上からなることを
特徴とする前記の水の浄化促進剤とすることが好ましい
(請求項3)。
In order to solve the above-mentioned problems, according to the present invention, the above-mentioned inorganic powder is bentonite powder, montmorillonite powder, dolomite powder, diatomaceous earth powder, kaolin powder and any of these substantially the same components. It is preferable that the water purification accelerator is composed of any one kind or two or more kinds selected from the group of soil powder consisting of (3).

【0008】また、前記の課題を解決するために、本発
明は、前記の微生物を含む付着物と無機質粉体の混合比
が、重量比で0.1:99.9〜10:90であること
を特徴とする前記の水の浄化促進剤とすることが好まし
い(請求項4)。
In order to solve the above-mentioned problems, according to the present invention, the mixing ratio of the deposit containing the microorganisms and the inorganic powder is 0.1: 99.9 to 10:90 by weight. It is preferable that the water purification promoter is characterized in that (claim 4).

【0009】また、前記の課題を解決するために、本発
明は、活性汚泥法やカキ殻を含む貝殻濾材を用いた接触
浄化法などの微生物による水の浄化方法において、前記
の何れかに記載された浄化促進剤を予め水に分散させた
ものを処理槽中に投入して、前記の活性汚泥乃至貝殻濾
材に浄化促進剤を接触させるとともに、係る活性汚泥乃
至貝殻濾材に汚水などの原水を接触通過させて浄化する
ことを特徴とする水の浄化方法とすることが好ましい
(請求項5)。
In order to solve the above-mentioned problems, the present invention provides a method for purifying water by microorganisms, such as an activated sludge method or a contact purification method using a shell filter medium containing oyster shells. The purified purification agent is dispersed in water in advance into a treatment tank, and the purification accelerator is brought into contact with the activated sludge or the shell filter medium, and raw water such as sewage is fed to the activated sludge or the shell filter medium. It is preferable to use a water purification method characterized in that the water is brought into contact with and purified.

【0010】また、前記の課題を解決するために、本発
明は、前記の浄化促進剤を処理水に対して10〜100
0ppm投入することを特徴とする前記の水の浄化方法
とすることが好ましい(請求項6)。
In order to solve the above-mentioned problems, the present invention provides the purification accelerator as described above with respect to the treated water in an amount of 10 to 100.
It is preferable that the water purification method is characterized in that 0 ppm is added (claim 6).

【0011】また、前記の課題を解決するために、本発
明は、水産食品加工などで発生する高濃度汚水浄化シス
テムであって、水中に混在する挟雑物を除去する前処理
手段と、カキ殻を含む貝殻濾材を充填した処理槽中に前
記の何れかに記載された浄化促進剤を投入する投入手段
と、前記の処理槽中に空気を吹き込んで汚水などの原水
を曝気するとともに、前記貝殻濾材に浄化促進剤を接触
させつつ係る貝殻濾材に汚水などの原水を接触通過させ
て浄化する濾過手段と、汚泥を水と分離して取り除く汚
泥分離手段と、を備えた水の浄化システムとすることが
好ましい(請求項7)。
In order to solve the above-mentioned problems, the present invention is a high-concentration sewage purification system that occurs in the processing of aquatic foods, which comprises pretreatment means for removing contaminants mixed in water and oysters. A charging means for charging the purification accelerator described in any one of the above into a treatment tank filled with a shell filter medium containing a shell, and aeration of raw water such as sewage by blowing air into the treatment tank, A water purification system provided with a filtering means for bringing raw water such as sewage into contact with and purifying the shell filter medium while bringing a purification accelerator into contact with the shell filter medium, and a sludge separation means for separating sludge from water and removing the sludge. It is preferable to do so (claim 7).

【0012】また、前記の課題を解決するために、本発
明は、河川や湖沼などの水浄化システムであって、河川
や湖沼などの水に前記の何れかに記載された浄化促進剤
を投入する投入手段と、カキ殻を含む貝殻濾材を充填し
た処理槽中において、前記の貝殻濾材に接触する状態で
前記のカキ殻浄化促進剤を添加した水を通過させる濾過
手段と、前記の処理槽中を通過した水の一部を処理槽の
前段階にもどして循環させ、残余の水を河川や湖沼など
に放流する放流手段と、を備えた水の浄化システムとす
ることが好ましい(請求項8)。
In order to solve the above problems, the present invention is a water purification system for rivers, lakes and marshes, in which the purification accelerator described in any one of the above is added to the water for rivers, lakes and marshes. In a treatment tank filled with a shell filter medium containing oyster shells, a filtering means for passing water containing the oyster shell purification promoter in a state of being in contact with the shell filter medium, and the treatment tank It is preferable that the water purification system is provided with a discharge means that circulates a part of the water that has passed through the inside of the treatment tank and circulates it, and discharges the remaining water into a river or lake. 8).

【0013】[0013]

【作用】本発明に係る水の浄化促進剤に関する浄化促進
作用のメカニズムは必ずしも明確ではないが、浄化促進
剤中には、カキ類、アコヤ貝等の貝殻表面に付着してい
る微生物類が乾燥によって休眠状態で粘土状の粉体中に
存在している。活性汚泥法やカキ殻を含む貝殻濾材を用
いた接触浄化法などにおいて、浄化処理槽中に前記の浄
化促進剤を投入すると、休眠状態の前記微生物群が蘇生
し、これらの微生物群自体が汚水に含まれる有機物を捕
食して汚水を浄化する作用を呈するとともに、活性汚泥
乃至貝殻濾材に含まれる浄化に寄与する微生物群を活性
化し、この活性化された微生物群が連鎖的に他の濾材に
含まれる微生物群を次々に活性化することによって、前
記の微生物処理の浄化槽を初めて稼動する際に浄化作用
を発揮するまでの立ち上がり時間を大幅に短縮でき、且
つ、浄化能力を助長する作用を有すると考えられる。
The mechanism of the purification promoting action of the water purification promoting agent according to the present invention is not always clear, but in the purification promoting agent, microorganisms attached to the surface of shells such as oysters and pearl oysters are dried. It exists in a clay-like powder in a dormant state. In the activated sludge method and the contact purification method using a shell filter medium containing oyster shells, when the purification accelerator is added to the purification treatment tank, the dormant microorganism groups are revived, and these microorganism groups themselves are sewage. While exhibiting the action of precipitating the organic matter contained in to purify the sewage, activate the microbial group that contributes to the purification contained in the activated sludge or shell filter medium, this activated microbial group is chained to other filter medium By successively activating the contained microorganisms, it is possible to significantly shorten the start-up time until the purifying action is exhibited when the above-mentioned septic tank for microbial treatment is operated for the first time, and to promote the purifying ability. It is thought that.

【0014】また、フミン酸及び/又はフルボ酸と、鉄
及び/又は鉄の化合物と、海藻類を含む栄養源とを含む
浄化促進剤においては、休眠状態の前記微生物群が蘇生
した時に前記の海藻類などの栄養源を捕食して、微生物
群の蘇生を助長するとともに、フミン酸やフルボ酸乃至
可溶性のフルボ酸鉄が微生物の細胞中に取り込まれる結
果、硝酸塩等の栄養源を還元して栄養分を吸収し易くし
て微生物を活性化させる作用を有することから、浄化促
進剤中の微生物と他の濾材中の微生物をより積極的に活
性化させる作用を有する。
Further, in a purification promoter containing humic acid and / or fulvic acid, iron and / or an iron compound, and a nutrient source containing seaweed, the above-mentioned microbial groups in a dormant state are resuscitated when they are revived. Prey on nutrients such as seaweed to promote revitalization of microbial communities, and as a result of humic acid, fulvic acid or soluble iron fulvic acid being taken into the cells of microorganisms, it reduces nutrients such as nitrates. Since it has the effect of facilitating the absorption of nutrients and activating the microorganisms, it has the effect of more actively activating the microorganisms in the purification accelerator and the microorganisms in other filter media.

【0015】また、ベントナイト粉、モンモリロナイト
粉、ドロマイト粉、珪藻土粉、カオリン粉などの粘土状
粉体は多孔質体で、PH値が中性に近いので、カキ殻等
の表面に付着している微生物を含む付着物からなる粉体
をその多孔質体の中に取り込んで微生物を休眠状態のま
ま固定することができる。また、前記の粘土状粉体、特
にベントナイト粉等は水分を包含し水中で膨潤が著し
く、乾燥状態においては、微生物への水分を遮断する作
用がある反面、水中においては、その内部に水分を取り
込み、その水分に含まれる有機物を捕食することによっ
て、休眠状態の微生物を蘇生する補助的な作用をなすと
考えられる。
Clay-like powders such as bentonite powder, montmorillonite powder, dolomite powder, diatomaceous earth powder, and kaolin powder are porous bodies and have a PH value close to neutral, so they adhere to the surface of oyster shells and the like. It is possible to immobilize the microorganisms in a dormant state by incorporating a powder made of a deposit containing microorganisms into the porous body. Further, the clay-like powder, especially bentonite powder, etc., contains water and significantly swells in water, and in a dry state, it has an effect of blocking water to microorganisms, while in water, water is contained therein. It is considered that by taking up and precipitating the organic matter contained in the water, it has an auxiliary effect of reviving the dormant microorganisms.

【0016】また、浄化促進剤中の微生物を含む付着物
の混合比が大き過ぎると、乾燥時の休眠状態において僅
かの水分条件によって蘇生状態になり安定性を欠き、逆
に付着物の混合比が小さ過ぎると、蘇生時の浄化促進の
効率が低下することから、混合比が重量比で0.1:9
9.9〜10:90であることが好ましい。また、カキ
殻などの殻表は好気性と嫌気性の多種多様な微生物群が
生息するのでバランスのとれた浄化作用がなされる。
Further, if the mixing ratio of the deposits containing microorganisms in the purification accelerator is too large, a slight water condition in the dormant state during drying causes resuscitation and lacks stability. If the ratio is too small, the efficiency of purification promotion during resuscitation decreases, so the mixing ratio is 0.1: 9 by weight.
It is preferably 9.9 to 10:90. In addition, the shell surface such as oyster shells is inhabited by a wide variety of aerobic and anaerobic microbial groups, and therefore has a well-balanced purification action.

【0017】[0017]

【発明の実施の形態】次に、この発明の実施の形態につ
いて以下に説明する。先ず、本発明の実施の形態に係る
浄化促進剤の原料となるカキは、イタボガキ科の二枚貝
の総称であり、マガキ、イタボガキ、スミノエガキ等の
種類があり、貝殻の表面は薄い板状の成長脈が発達して
いる。また、アコヤ貝は、昔、阿古屋の浦(愛知県半田
市付近の古地名)に多く産したと言われる二枚貝の一種
であり、殻表は雲母状の殻片に覆われ、養殖真珠の母貝
とされ、本州中部以南に広く分布する。前記のカキ類や
アコヤ貝などの二枚貝の貝殻の表面は、雲母状の殻片に
覆われ、ここに太陽虫、脱窒菌、一般菌などの水の浄化
に関与するといわれる微生物が生息している。
BEST MODE FOR CARRYING OUT THE INVENTION Next, embodiments of the present invention will be described below. First, oysters, which are the raw material of the purification promoter according to the embodiment of the present invention, are a general term for bivalve molluscs of the family Itapidae, and there are types such as oysters, velvet oysters, and oyster oysters, and the surface of the shell is a thin plate-shaped growth pulse. Is developing. In addition, pearl oysters are a type of bivalve that is said to have often been found in Akoya-no-ura (an ancient place name near Handa City, Aichi Prefecture) in the past. The shell surface is covered with mica-shaped shell pieces, and cultured pearls It is considered to be a mother oyster and is widely distributed south of central Honshu. The surface of the shell of bivalve such as the above-mentioned oysters and pearl oysters is covered with micaceous shell pieces, where microorganisms that are said to be involved in the purification of water such as solar insects, denitrifying bacteria, and general bacteria inhabit. There is.

【0018】次に、本発明の実施の形態に係る浄化促進
剤の製造方法について以下に説明する。先ず、前記のカ
キやアコヤ貝等の貝殻を日陰で1週間乃至数週間乾燥さ
せる。太陽光に当てた場合、貝殻表面に生息する微生物
は、紫外線の影響を受け約80℃以上で死滅する虞があ
るので、日陰で乾燥させるのが好ましい。乾燥後に、殻
表の微生物を含む付着物を落し、これを集めて篩にかけ
て粉体を得る。この粉体をベントナイト粉、モンモリロ
ナイト粉、ドロマイト粉、珪藻土粉、カオリン粉等の粘
土状粉体やゼオライトなどの多孔質粉体に、前記の付着
物と無機質粉体の混合比が、重量比で0.1:99.9
〜10:90になるようにブレンダーなどで攪拌混合し
て所望の浄化促進剤を得る。
Next, a method for producing the purification accelerator according to the embodiment of the present invention will be described below. First, the shells such as the oysters and pearl oysters are dried in the shade for 1 week to several weeks. When exposed to sunlight, microorganisms that inhabit the surface of the shell may be affected by ultraviolet rays and die at about 80 ° C. or higher, so it is preferable to dry in the shade. After drying, the deposits containing the microorganisms on the shell surface are removed, and the collected deposits are sieved to obtain a powder. This powder is bentonite powder, montmorillonite powder, dolomite powder, diatomaceous earth powder, kaolin powder or other clay-like powder or porous powder such as zeolite, the mixing ratio of the above-mentioned adherent and inorganic powder is a weight ratio. 0.1: 99.9
A desired purification accelerator is obtained by stirring and mixing with a blender or the like so that the ratio becomes 10:90.

【0019】前記のベントナイト乃至モンモリロナイト
は、火山灰が海底や湖底に堆積して地熱や地圧や海水の
続成作用を受けて結晶化した含水層状珪酸塩で、スメク
タイト系粘土の一種と言われる。ベントナイトの結晶
は、4面体と4面体の間に8面体が入る3層構造をな
し、水中においては各層間に水分子が入ってきて膨潤
し、体積が数倍から10数倍に膨れる。前記ベントナイ
トに対してドロマイト(白雲石(CaCO・MgCO
))、珪藻土(SiO・Fe・Al
)、カオリン(カオリナイト(Al・2S
iO・2HO))は、何れも堆積岩であって、特
に、カオリンはベントナイトと同様に層状珪酸塩である
が水によって膨潤することは殆どないが、水分を包含す
る機能を有する。
The above-mentioned bentonite or montmorillonite is a hydrous layered silicate that is crystallized by volcanic ash deposited on the seabed or lakebed and subjected to geothermal heat, geopressure and diagenesis of seawater, and is said to be a kind of smectite clay. Bentonite crystals have a three-layer structure in which octahedra are inserted between tetrahedra and tetrahedra, and in water, water molecules enter between the layers and swell, and the volume swells from several times to several ten times. Dolomite (white dolomite (CaCO 3 · MgCO) for the bentonite
3 )), diatomaceous earth (SiO 2 · Fe 2 O 3 · Al)
2 O 3 ), kaolin (kaolinite (Al 2 O 3 .2S
iO 2 .2H 2 O)) is a sedimentary rock, and in particular, kaolin is a layered silicate like bentonite, but it hardly swells with water, but has a function of including water.

【0020】また、フミン酸やフルボ酸は、腐植物質か
ら分離して得られ、特にフルボ酸は鉄と結合して水に溶
け易く、微生物を活性化する作用がある。海藻類を含む
栄養源としては、例えば、乾燥した昆布の粉末を添加混
合することが好ましい。この他に、鉄、鉄の化合物、例
えば塩化第2鉄の微粉末を添加混合することが好まし
く、併せて落葉樹の粉末などの腐植物質を添加混合して
もよい。
Further, humic acid and fulvic acid are obtained by separating them from humic substances, and in particular, fulvic acid binds iron and is easily dissolved in water, and has an action of activating microorganisms. As a nutrient source containing seaweeds, for example, dry kelp powder is preferably added and mixed. In addition to this, it is preferable to add and mix iron and iron compounds, for example, fine powder of ferric chloride, and humic substances such as deciduous tree powder may also be added and mixed.

【0021】前記のようにして得られた浄化促進剤は、
乾燥状態下、冷暗所において微生物が休眠状態のまま略
半永久的に保管することができる。そして、前記で得ら
れた浄化促進剤を中性の水に解かし、浄化促進剤を処理
水に対して約10〜1000ppmの割合になるように
貝殻濾材を用いた浄化槽に投入することによって、休眠
状態の前記微生物が蘇生して貝殻濾材の微生物群を活性
化するとともに、浄化作用を助長する。カキ殻濾材は3
年間生育した貝殻を使用することが歩留まりの点で好ま
しい。そして、カキ殻濾材は、浄化槽の容積の50%以
上充填することが好ましい。
The purification accelerator obtained as described above is
Under dry conditions, microorganisms can be stored semi-permanently in a dormant state in a cool and dark place. Then, the purification accelerator obtained in the above is dissolved in neutral water, and the purification accelerator is put into a septic tank using a shell filter medium so as to be in a ratio of about 10 to 1000 ppm with respect to treated water, thereby giving a dormancy. The above-mentioned microorganisms in the state are revived to activate the microorganism groups of the shell filter medium and promote the purifying action. Oyster shell filter material is 3
From the viewpoint of yield, it is preferable to use shells that have been grown for a year. The oyster shell filter medium is preferably filled in 50% or more of the volume of the septic tank.

【0022】前記の浄化促進剤は、例えばBOD換算5
000〜6000mg/lの高濃度な富栄養化液(汚
水)中や動植物油脂のnヘキサン200〜600mg/
lの溶液中でも問題なく蘇生し、活性化能を発揮する。
本発明の浄化促進剤を使用した水の浄化処理において
は、浄化対象となる原水の種類や浄化設備によって効果
に差が生じることもあるが、通常、BOD(生物化学的
酸素要求量)は約80〜99%、COD(化学的酸素要
求量)は約60〜90%、全窒素(T−N)は約20〜
80%、全燐(T−P)は約30〜65%、大腸菌は約
90〜95%を削減できる。とりわけ、大腸菌を大幅に
削減できることから、通常の浄化設備に要求される公共
水域での排出基準の1ml当り3000MPN以内を満
足し、塩素殺菌が不要となる。
The above-mentioned purification accelerator is, for example, 5 in terms of BOD.
000-6000 mg / l in high-concentration eutrophication liquid (sewage) or n-hexane of animal and vegetable oils 200-600 mg /
It can be revived without any problems in the solution of 1 and exerts its activation ability.
In the purification treatment of water using the purification accelerator of the present invention, the effect may vary depending on the type of raw water to be purified and the purification equipment, but normally the BOD (biochemical oxygen demand) is about 80-99%, COD (chemical oxygen demand) is about 60-90%, total nitrogen (TN) is about 20-
80%, total phosphorus (TP) can be reduced by about 30 to 65%, and E. coli can be reduced by about 90 to 95%. In particular, since Escherichia coli can be significantly reduced, it satisfies the discharge standard of 3000 MPN per ml in public water bodies required for ordinary purification equipment, and chlorine sterilization is unnecessary.

【0023】また、淡水は言うまでもなく、塩分が海水
の3倍以上の溶液中でも前記機能が低下することはな
い。更に、微生物処理の浄化槽を初めて稼動する際に浄
化能力を発揮するまでの立ち上がり時間は、浄化促進剤
を使用しない従来法では、3ヶ月乃至6ヶ月以上を要す
るのに比較して、本発明の実施の形態に係る浄化促進剤
を使用すると、何と24時間乃至48時間以内に濾材の
微生物群が浄化作用を発揮し、処理水の水質が設計値に
達することが分かった。
Further, not to mention fresh water, the above-mentioned function does not deteriorate even in a solution having a salt content three times or more that of seawater. Furthermore, the rise time until the purification performance is exhibited when the septic tank for microbial treatment is operated for the first time requires 3 to 6 months or more in the conventional method that does not use the purification accelerator. It was found that when the purification accelerator according to the embodiment is used, the microorganism group of the filter medium exerts a purification action within 24 to 48 hours, and the quality of treated water reaches the design value.

【0024】[0024]

【実施例】以下に、前記の発明の実施の形態で説明した
浄化促進剤を作成する実施例と、この浄化促進剤を貝殻
濾材を用いた浄化槽に投入して使用する使用例について
図に基づいて説明する。
[Examples] Examples for producing the purification accelerators described in the embodiments of the present invention and usage examples in which the purification accelerators are put into a septic tank using a shell filter medium and used are described below with reference to the drawings. Explain.

【0025】実施例(浄化促進剤の作成) カキ類及びアコヤ貝の貝殻の表面に付着している休眠状
態の微生物を含む乾燥付着物の篩かけ粉体0.1〜10
重量部、フミン酸0.1〜1.0重量部、フルボ酸0.
1〜1.0重量部、海藻類を含む栄養源(昆布の粉体)
0.1〜1.0重量部、鉄、鉄の化合物(塩化第2鉄の
粉体)0.05〜1.0重量部、無機質粉体(モンモリ
ロナイト粉)99.9〜90重量部を攪拌器で10分間
攪拌混合して、所望の浄化促進剤を得た。
Example (Preparation of Purification Accelerator) Sifted powder of dried deposits containing dormant microorganisms adhering to the surface of oysters and pearl oyster shells 0.1 to 10
Parts by weight, humic acid 0.1 to 1.0 parts by weight, fulvic acid 0.
1 to 1.0 parts by weight, nutrient source containing seaweed (kelp powder)
Stir 0.1 to 1.0 parts by weight, iron, iron compound (ferric chloride powder) 0.05 to 1.0 parts by weight, inorganic powder (montmorillonite powder) 99.9 to 90 parts by weight The mixture was stirred and mixed in a vessel for 10 minutes to obtain the desired purification promoter.

【0026】使用例1 図1は、水産食品加工などで発生する塩分高濃度汚水の
浄化システムを例示した説明図である。図において1a
は、浄化システムであって、原水10を遊水槽11に一
旦溜めておき、この原水10をスクリーン乃至フィルタ
ー12を通過させて原水中に混在する油分や挟雑物26
を除去する前処理手段と、前処理後の水を貯留槽13に
導いて散気孔14から空気を吹き込む曝気手段と、曝気
後の水を流量計21を経て、カキ殻とアコヤ貝を含む貝
殻濾材15を充填したシェルタッチ槽16に導き、シェ
ルタッチ槽16において、前記の浄化促進剤の含水液1
7を投入する投入手段と、下方の散気孔14から空気を
吹き込んで前記貝殻濾材15に浄化促進剤乃至水を接触
させる濾過手段と、分離槽18底部の汚泥引抜管19か
ら汚泥20を水と分離して引き抜いて取り除く汚泥分離
手段と、放流手段23を備えてなる。貝殻濾材15に水
を接触させる滞留時間は約12時間位であった。
Example of Use 1 FIG. 1 is an explanatory view illustrating a purification system of salty high-concentration sewage generated in processing of seafood. In the figure, 1a
Is a purification system, in which the raw water 10 is temporarily stored in a water tank 11, and the raw water 10 is passed through a screen or a filter 12 to mix oil and foreign matters 26 in the raw water.
Means for removing water, aeration means for guiding the water after pretreatment to the storage tank 13 and blowing air from the diffuser holes 14, and water after aeration through the flowmeter 21 for oyster shells and shellfish containing pearl oysters It is led to the shell touch tank 16 filled with the filter medium 15, and in the shell touch tank 16, the water-containing liquid 1 of the above-mentioned purification accelerator.
7, charging means for blowing air from the lower air diffuser 14 to bring the purification filter or water into contact with the shell filter medium 15, and a sludge extraction pipe 19 at the bottom of the separation tank 18 for converting sludge 20 into water. It comprises a sludge separating means for separating and withdrawing, and a discharge means 23. The residence time for contacting water with the shell filter medium 15 was about 12 hours.

【0027】[0027]

【表1】 [Table 1]

【0028】表1は、前記の使用例1に記載された高濃
度汚水の浄化システムを水産、食品加工関係の4社で実
験して得られた処理水4点を水質検査して、その結果を
表示したものである。表中の排出基準は総理府令で定め
る許容限度であり、同欄の下方の数値はそれぞれの項目
の平均除去率を表す(以下同じ)。この表から、BOD
は、除去率97.7〜98.7%(平均除去率98.1
%)で何れも排出基準の120mg/lをクリアして安
定している。CODは除去率37.5〜95.6%(平
均除去率72.2%)で全点が基準値をクリアし、SS
は、除去率42.1〜98.9%(平均除去率73.4
%)で全点が基準値をクリアしている。Nヘキサンは、
除去率が98%で極めて高い。大腸菌は1件のデータで
あるが除去率86%であり、通常の浄化設備に要求され
る公共水域での排出基準3000MPN/1mlを満足
し、塩素系殺菌が不要となる。また、前記の4点の使用
例とも1〜2日のならし運転で表1に示す浄化作用を呈
することが確認された。これに対して、浄化促進剤を使
用しない比較例は、6ヶ月以上の立上げ期間を要した。
Table 1 shows the results of water quality inspection of 4 points of treated water obtained by experimenting with the high-concentration wastewater purification system described in the above-mentioned Use Example 1 by four companies involved in fisheries and food processing. Is displayed. The emission standards in the table are the permissible limits specified by the Prime Minister's Ordinance, and the numbers below this column indicate the average removal rate for each item (the same applies below). From this table, BOD
Shows a removal rate of 97.7 to 98.7% (average removal rate of 98.1).
%), Both of which have cleared the emission standard of 120 mg / l and are stable. COD has a removal rate of 37.5 to 95.6% (average removal rate of 72.2%), and all the points clear the standard value.
Shows a removal rate of 42.1 to 98.9% (average removal rate of 73.4).
%), All points clear the standard value. N hexane is
The removal rate is extremely high at 98%. Escherichia coli has one data, but the removal rate is 86%, which satisfies the emission standard of 3000 MPN / 1 ml in public water bodies required for ordinary purification equipment, and chlorine-based sterilization is unnecessary. In addition, it was confirmed that all of the above four use examples exhibited the cleaning action shown in Table 1 in the 1- to 2-day break-in operation. On the other hand, the comparative example that did not use the purification accelerator required a startup period of 6 months or more.

【0029】使用例2 図2は、自然の河川や湖沼などを想定して、愛媛県県民
環境局の援助によって愛媛県南宇和郡御荘町平城に設け
られた水浄化システムシステムの実験装置を例示したも
のである。図において1bは、浄化システムであって、
長さ170cm、幅160cm、深さ90cmの箱を複
数個に区分けし、その中を水が蛇行して通過するように
し、その各々に愛媛県産のカキ殻とアコヤ貝からなる貝
殻濾材15を充填した処理槽22中において、湖沼や河
川24などからポンプ26によって汲み上げた水に前記
の浄化促進剤の含水液17を投入する投入手段と、前記
の貝殻濾材に接触する状態で水を通過させる濾過手段
と、前記の処理槽22中を通過した水の一部(全体の約
20%)を処理槽の前段階にもどす循環手段25と、残
余の水を河川や湖沼などに放流する放流手段23と、を
備えてなる。
Example 2 of Use FIG. 2 illustrates an experimental apparatus of a water purification system system provided in Heijo, Miso-cho, Minamiuwa-gun, Ehime Prefecture, with the assistance of the Ehime Prefectural Citizens' Environment Department, assuming natural rivers and lakes. It is a thing. In the figure, 1b is a purification system,
A 170 cm long, 160 cm wide, and 90 cm deep box is divided into a plurality of boxes, through which water meanders and passes through, and each has a shell filter material 15 consisting of oyster shells and pearl oysters from Ehime prefecture. In the filled treatment tank 22, the water is pumped from the lake or river 24 by the pump 26, and the charging means for charging the water containing liquid 17 of the purification promoter and the water passing through the shell filter medium in contact with the charging means. A filtering means, a circulation means 25 for returning a part (about 20% of the whole) of the water that has passed through the treatment tank 22 to the previous stage of the treatment tank, and a discharge means for discharging the residual water to rivers, lakes and marshes. 23, and.

【0030】濾材に水が接触する滞留時間は5〜6時間
であった。また、処理槽22中にバイオアッセイ用の魚
を泳がせておき、処理水の安全性を確認できるようにし
た。前記の浄化促進剤の投入は、浄化装置を立ち上げる
ときに1回行い、その後は、濾材のカキ殻に付着する微
生物が浄化作用を呈し、このカキ殻が減った時を見計ら
って追加補充すればよい。
The residence time of contacting the filter medium with water was 5 to 6 hours. In addition, the fish for bioassay was allowed to swim in the treatment tank 22 so that the safety of the treated water could be confirmed. The purification accelerator is added once when the purifying device is started up, and thereafter, the microorganisms adhering to the oyster shell of the filter medium exert a purifying action, and when the oyster shell is depleted, additional supplementation is required. Good.

【0031】[0031]

【表2】 [Table 2]

【0032】表2は、前記の使用例2に記載された浄化
システムを平成12年9月から平成13年2月末まで試
験し、処理して得られた処理水を、愛媛県県民環境局が
愛媛県保健衛生協会に依頼して、経時的に水質検査をし
た結果を表示したものである。この表から、BOD(生
物化学的酸素要求量)は1点を除き除去率75〜95%
(平均除去率88%)、COD(化学的酸素要求量)は
1点を除き除去率62〜76%(平均除去率70.5
%)、SS(懸濁物質)は除去率75〜99%(平均除
去率92%)、全窒素(T−N)は除去率12〜55%
(平均除去率33%)、全燐(T−P)は除去率11〜
43%(平均除去率26%)、大腸菌は除去率82〜9
9.9%(平均除去率93%)、一般細菌は除去率86
〜99.9%(平均除去率96%)であって、極めて良
好な結果が得られた。前記の数値が国の定める公共水域
排出基準を満足することは言うまでもない。
Table 2 shows the treated water obtained by testing the purification system described in Use Example 2 from September 2000 to the end of February 2001, and treating the treated water by the Ehime Prefectural Environmental Bureau. This is a display of the results of water quality inspection over time requested by the Ehime Prefectural Health and Hygiene Association. From this table, BOD (Biochemical Oxygen Demand) is 75-95% removal rate except 1 point
(Average removal rate 88%), COD (chemical oxygen demand) except for one point, removal rate 62-76% (average removal rate 70.5
%), SS (suspended substance) removal rate 75-99% (average removal rate 92%), total nitrogen (TN) removal rate 12-55%
(Average removal rate 33%), total phosphorus (TP) removal rate 11-
43% (average removal rate 26%), E. coli removal rate 82-9
9.9% (average removal rate 93%), general bacteria removal rate 86
It was ˜99.9% (average removal rate 96%), and extremely good results were obtained. It goes without saying that the above figures satisfy the national standards for discharge of public water bodies.

【0033】大腸菌と一般細菌の除去率が高いので、塩
素系の殺菌剤を使用しなくてもよい。SSの除去率が高
いのでクリプトスポリジウムの発生を抑制できる。BO
DやCODの最終の除去率が低いのは、水温が10℃以
下に低下したために微生物の機能低下によるものと考え
られる。また、前記の使用例2では、1〜2日のならし
運転で表2に示す浄化作用を呈することが確認された。
これに対して、浄化促進剤を使用しない別の実験による
比較例では、6ヶ月以上の立上げ期間を要した。
Since the removal rate of Escherichia coli and general bacteria is high, it is not necessary to use a chlorine-based bactericide. Since the removal rate of SS is high, the generation of Cryptosporidium can be suppressed. BO
It is considered that the final removal rate of D and COD is low because the function of microorganisms is deteriorated because the water temperature is lowered to 10 ° C or lower. In addition, it was confirmed that, in the above-mentioned usage example 2, the cleaning action shown in Table 2 was exhibited in the 1- to 2-day break-in operation.
On the other hand, the comparative example by another experiment which did not use the purification accelerator required a startup period of 6 months or more.

【0034】[0034]

【発明の効果】本発明に係る水の浄化促進剤は、前記の
ように構成したことによって、活性汚泥法やカキ殻接触
浄化法などの微生物処理の浄化装置を初めて稼動する際
に浄化作用を発揮するまでの立ち上げ期間を大幅に短縮
できるばかりでなく、カキなどの貝殻に付着する微生物
群が本来有する浄化能力を助長し、大腸菌等の細菌に対
する滅菌効果を併せ有することよって、殺菌剤などの化
学物質を使用することによる良性の微生物を阻害するこ
となく、微生物や付着生物の食物連鎖を応用し、自然界
における自浄効果を促進且つ効率化して、肥沃な土壌を
つくり、河川や海域を清浄化する。海水、淡水である河
川及び川の水が入りこむ汽水域(海水と淡水が混じり合
った海域)の何れにおいても有効であり、しかも、一
旦、浄化装置が立ち上がった後は、維持管理のための手
間が殆ど不用であって、極めて経済的に優れた効果を奏
する。
EFFECTS OF THE INVENTION The water purification accelerator according to the present invention, having the above-mentioned constitution, has a purification action when the purification apparatus for microbial treatment such as the activated sludge method and the oyster shell contact purification method is operated for the first time. Not only can the start-up period until it takes effect be drastically shortened, but it also contributes to the original purifying ability of the microbial group that adheres to shells such as oysters, and also has a sterilizing effect against bacteria such as Escherichia coli. Applying the food chain of microorganisms and adhering organisms without promoting benign microorganisms by using these chemical substances, promoting and improving the self-cleaning effect in the natural world, creating fertile soil, cleaning rivers and sea areas Turn into. It is effective in both seawater, rivers that are freshwater, and brackish water areas where river water enters (sea areas where seawater and freshwater are mixed). In addition, once the purification device has been started up, it takes time and effort for maintenance. Is almost unnecessary and has an extremely economically excellent effect.

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

【図1】使用例1に係る水産食品加工などで発生する高
濃度汚水の浄化システムを例示した説明図である。
FIG. 1 is an explanatory diagram exemplifying a purification system for highly-concentrated sewage generated in processing of seafood, etc. according to Use Example 1.

【図2】(a)は、使用例2に係る自然の河川や湖沼な
どを想定した実験装置による水の浄化システムを例示し
た縦断面図であり、(b)は、処理槽の平面図である。
FIG. 2 (a) is a vertical cross-sectional view illustrating a water purification system using an experimental device assuming natural rivers and lakes according to Use Example 2, and FIG. 2 (b) is a plan view of a treatment tank. is there.

【符号の説明】[Explanation of symbols]

1a,1b:水の浄化システム、10:原水、11:遊
水槽、12:スクリーン乃至フィルター、13:貯留
槽、14:散気孔、15:貝殻濾材、16:シェルタッ
チ槽、17:浄化促進剤の含水液、18:分離槽、1
9:汚泥引抜管、20:汚泥、21:流量計、22:処
理槽、23:放流手段、24:河川、25:循環手段、
26:挟雑物、26:ポンプ
1a, 1b: Water purification system, 10: Raw water, 11: Water tank, 12: Screen or filter, 13: Storage tank, 14: Air diffuser hole, 15: Shell filter material, 16: Shell touch tank, 17: Purification accelerator Water-containing liquid, 18: separation tank, 1
9: sludge drawing pipe, 20: sludge, 21: flow meter, 22: treatment tank, 23: discharge means, 24: river, 25: circulation means,
26: Foreign matter, 26: Pump

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI C12N 11/14 C12N 11/14 (58)調査した分野(Int.Cl.7,DB名) C02F 3/00 C02F 3/06 C02F 3/12 ─────────────────────────────────────────────────── ─── Continuation of front page (51) Int.Cl. 7 identification code FI C12N 11/14 C12N 11/14 (58) Fields investigated (Int.Cl. 7 , DB name) C02F 3/00 C02F 3/06 C02F 3/12

Claims (8)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】カキ類、アコヤ貝よりなる群から選択され
る二枚貝の一種又はニ種以上からなる二枚貝の貝殻の表
面に付着している微生物を含む付着物を乾燥させること
によって微生物を休眠状態にした前記付着物の粉体と無
機質粉体との混合物を含むことを特徴とする水の浄化促
進剤。
1. A diapause state of microorganisms by drying a deposit containing microorganisms attached to the surface of a bivalve shell of one or two or more species of bivalve selected from the group consisting of oysters and pearl oysters. A water purification accelerator, comprising a mixture of the powder of the adhered substance as described above and an inorganic powder.
【請求項2】カキ類、アコヤ貝よりなる群から選択され
る二枚貝の一種又はニ種以上からなる二枚貝の貝殻の表
面に付着している微生物を含む付着物を乾燥させること
によって微生物を休眠状態にした前記付着物の粉体と、
無機質粉体と、フミン酸及び/又はフルボ酸と、鉄及び
/又は鉄の化合物と、海藻類を含む栄養源と、の混合物
を含むことを特徴とする水の浄化促進剤。
2. A dormant state of microorganisms by drying a deposit containing microorganisms attached to the surface of a bivalve shell of one or two or more species of bivalve selected from the group consisting of oysters and pearl oysters. The powder of the adhered substance,
A water purification accelerator comprising a mixture of an inorganic powder, humic acid and / or fulvic acid, iron and / or an iron compound, and a nutrient source containing seaweed.
【請求項3】前記の無機質粉体が、ベントナイト粉、モ
ンモリロナイト粉、ドロマイト粉、珪藻土粉、カオリン
粉及びこれらの何れかと実質的に同一の成分からなる土
粉の群から選択される何れか一種又はニ種以上からなる
ことを特徴とする請求項1記載の水の浄化促進剤。
3. The inorganic powder is any one selected from the group consisting of bentonite powder, montmorillonite powder, dolomite powder, diatomaceous earth powder, kaolin powder, and soil powder consisting essentially of the same components as any of these. Alternatively, the water purification accelerator according to claim 1, comprising two or more species.
【請求項4】前記の微生物を含む付着物と無機質粉体の
混合比が、重量比で0.1:99.9〜10:90であ
ることを特徴とする請求項1記載の水の浄化促進剤。
4. The purification of water according to claim 1, wherein the mixing ratio of the deposit containing the microorganism and the inorganic powder is 0.1: 99.9 to 10:90 by weight. Accelerator.
【請求項5】活性汚泥法やカキ殻を含む貝殻濾材を用い
た接触浄化法などの微生物による水の浄化方法におい
て、請求項1〜4の何れかに記載された浄化促進剤を予
め水に分散させたものを処理槽中に投入して、前記の活
性汚泥乃至貝殻濾材に浄化促進剤を接触させるととも
に、係る活性汚泥乃至貝殻濾材に汚水などの原水を接触
通過させて浄化することを特徴とする水の浄化方法。
5. A method for purifying water by microorganisms, such as an activated sludge method or a contact purification method using a shell filter medium containing oyster shells, wherein the purification accelerator according to any one of claims 1 to 4 is previously added to water. The dispersion is put into a treatment tank, and a purification accelerator is brought into contact with the activated sludge or the shell filter medium, and raw water such as sewage is passed through the activated sludge or the shell filter medium for purification. How to purify water.
【請求項6】前記の浄化促進剤を処理水に対して10〜
1000ppm投入することを特徴とする請求項5記載
の水の浄化方法。
6. The purified water is added to the treated water in an amount of 10 to 10.
The method for purifying water according to claim 5, wherein 1000 ppm is added.
【請求項7】水産食品加工などで発生する高濃度汚水浄
化システムであって、水中に混在する挟雑物を除去する
前処理手段と、カキ殻を含む貝殻濾材を充填した処理槽
中に請求項1〜4の何れかに記載された浄化促進剤を投
入する投入手段と、前記の処理槽中に空気を吹き込んで
汚水などの原水を曝気するとともに、前記貝殻濾材に浄
化促進剤を接触させつつ係る貝殻濾材に汚水などの原水
を接触通過させて浄化する濾過手段と、汚泥を水と分離
して取り除く汚泥分離手段と、を備えた水の浄化システ
ム。
7. A high-concentration sewage purification system generated in the processing of aquatic foods, the pretreatment means for removing contaminants mixed in water, and a treatment tank filled with a shell filter medium containing oyster shells. Item 1. A charging means for charging the purification accelerator described in any one of 1 to 4 and aeration of raw water such as sewage by blowing air into the treatment tank and bringing the purification filter into contact with the shell filter medium. A water purification system comprising: a filtration means for bringing raw water such as sewage into contact with the shell filter medium to purify it, and a sludge separation means for separating and removing sludge from water.
【請求項8】河川や湖沼などの水浄化システムであっ
て、河川や湖沼などの水に請求項1〜4の何れかに記載
された浄化促進剤を投入する投入手段と、カキ殻を含む
貝殻濾材を充填した処理槽中において、前記の貝殻濾材
に接触する状態で前記のカキ殻浄化促進剤を添加した水
を通過させる濾過手段と、前記の処理槽中を通過した水
の一部を処理槽の前段階にもどして循環させ、残余の水
を河川や湖沼などに放流する放流手段と、を備えた水の
浄化システム。
8. A water purification system for rivers, lakes and marshes, which includes an oyster shell for charging the water for rivers, lakes and marshes with the purification promoter according to any one of claims 1 to 4. In a treatment tank filled with a shell filter medium, a filtering means for passing water containing the oyster shell purification promoter in a state of being in contact with the shell filter medium, and a part of the water passing through the treatment tank. A water purification system equipped with a discharge means that circulates it back to the previous stage of the treatment tank and discharges the remaining water to rivers and lakes.
JP2001233134A 2001-08-01 2001-08-01 Water purification promoter and water purification method and purification system using this purification promoter Expired - Fee Related JP3453129B2 (en)

Priority Applications (1)

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JP3453129B2 true JP3453129B2 (en) 2003-10-06

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3659591B2 (en) * 2001-10-12 2005-06-15 永和国土環境株式会社 Sewage purification equipment
JP2005290767A (en) * 2004-03-31 2005-10-20 Kazuo Nakamura Coastal zone fertilizing system
JP4945742B2 (en) * 2004-08-06 2012-06-06 国立大学法人広島大学 Bottom quality improving material and bottom quality improving method using the same
JP4390804B2 (en) * 2004-11-25 2009-12-24 敏明 楠 Method for suppressing activated sludge generation and method for treating sewage
KR101091077B1 (en) * 2008-12-12 2011-12-09 김선구 Method for purification processing waste-water contaminated with arsenic using natural biosorbents made of persimmon skin and the like, and the apparatus therefor
JP2022036699A (en) * 2020-08-24 2022-03-08 阿部化学 株式会社 Microbial activator and method for producing microbial activator

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