JP2903359B2 - Water activator and its production method - Google Patents

Water activator and its production method

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Publication number
JP2903359B2
JP2903359B2 JP5264176A JP26417693A JP2903359B2 JP 2903359 B2 JP2903359 B2 JP 2903359B2 JP 5264176 A JP5264176 A JP 5264176A JP 26417693 A JP26417693 A JP 26417693A JP 2903359 B2 JP2903359 B2 JP 2903359B2
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JP
Japan
Prior art keywords
water
treatment
hours
activator
value
Prior art date
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JP5264176A
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Japanese (ja)
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JPH0796275A (en
Inventor
倫義 杉山
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AI II RISAACHI KK
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AI II RISAACHI KK
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Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】この発明は、自然に存在している
火山礫と黒土とを用いた、水質活性剤とその製造方法に
関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a water activator using naturally occurring lapilli and black soil and a method for producing the same.

【0002】[0002]

【従来の技術】産業排水や生活排水の処理には、下水
道、浄化処理施設の建設に多額の投資が必要であるう
え、その運転、維持に多額の費用がかかっている。しか
も浄化後は、塩素ガスなどの殺菌剤を含んだままで放水
されるため、自然の生物体系を損なうおそれが多分にあ
る。
2. Description of the Related Art The treatment of industrial wastewater and domestic wastewater requires a large investment in the construction of sewage and purification facilities, and a large expense in its operation and maintenance. In addition, after purification, water is discharged while containing a germicide such as chlorine gas, so that there is a possibility that natural biological systems may be damaged.

【0003】[0003]

【発明が解決しようとする課題】この発明が解決しよう
とする課題は、天然素材を利用して自然界の食物連鎖を
急速に促進し、水槽、プ−ル、川、池、湖沼や、産業排
水、生活排水等の浄化を、自然界に限りなく近い状態
で、短時間で行なうことにある。
The problem to be solved by the present invention is to use natural materials to rapidly promote the natural food chain, and to use water tanks, pools, rivers, ponds, lakes and marshes, and industrial wastewater. Another object of the present invention is to purify domestic wastewater in a short time in a state as close as possible to the natural world.

【0004】[0004]

【課題を解決するための手段】この発明に係る水質活性
材は、酸化処理により殺菌し、吸着性と空気溶解効率と
を向上させるとともに、微生物培地に適するようにした
多孔質の火山礫と黒土との混合物から得られる礫状物、
及び又は粘土状物を粉末化した粉末物からなることに特
徴がある。
The water-active material according to the present invention is sterilized by an oxidizing treatment, and has an adsorbing property, an air dissolving efficiency and
A gravel obtained from a mixture of porous lapilli and black soil, which is suitable for a microbial medium ,
And / or a powdery material obtained by pulverizing a clay-like material.

【0005】又この水質活性剤の製造方法の特徴は、火
山礫と黒土との混合物を、80℃ないし100℃の硫酸
銅溶液中で、PH値を3.5〜5.0に維持しながら1
0〜12時間で酸化処理することにある。
[0005] The method for producing the water-active agent is characterized in that a mixture of lapilli and black clay is maintained in a copper sulfate solution at 80 ° C to 100 ° C while maintaining the PH value at 3.5 to 5.0. 1
The oxidation treatment is performed in 0 to 12 hours.

【0006】黒土は火山灰土の一種で、黒ボコ、音地
(オンジ)、ホヤとも呼ばれる、腐植質を含む黒色又は
黒褐色の肥沃土であり、火山礫とともに自然界に広く存
在する天然素材で、掘り出し、運搬以外にコストを要し
ないものである。
[0006] Black soil is a kind of volcanic ash soil and is a black or black-brown fertile soil containing humus, also known as black ash, onji, and ascidian. It is a natural material that widely exists in the natural world along with volcanic debris. It does not require any cost other than transportation.

【0007】この発明の水質活性剤の製造にあたって、
火山礫と黒土との割合はさほど重要な条件ではない。し
かし用途により火山礫を主体とする場合にあっては、容
量比で火山礫100に対して黒土20〜40を、又黒土
を主体として酸化処理後に粉末化して使用する場合は、
黒土100に対して火山礫を10〜40を混合する。又
火山礫と前記黒土粉末との混合物として使用する場合
は、容量比で火山礫100に対して黒土200〜500
の割合で混合するのが望ましい。但し何れも1例に過ぎ
ず、これら割合に限定されない。
In producing the water-activator of the present invention,
The proportion of lapilli to black soil is not a very important condition. However, in the case of mainly using lapilli depending on the application, in the case of using crushed black soil 20 to 40 with respect to lapilli 100 by volume ratio,
Mix 10 to 40 volcanic gravels with 100 black soils. When used as a mixture of lapilli and the above-mentioned black clay powder, the volume ratio of lapilli 100 to black clay 200 to 500 is used.
It is desirable to mix at a ratio of However, these are merely examples, and are not limited to these ratios.

【0008】酸化処理は次のように行なう。水10リッ
トルに硫酸銅45〜70gを溶解させた硫酸銅溶液を、
適宜割合の火山礫と黒土との混合物に、容量比で1.5
〜2.0倍程度加えて軽く攪拌し、80〜100℃で1
0〜12時間加熱して酸化処理を行なう。酸化処理中は
PH値は3.5〜5.0に維持する。
The oxidation treatment is performed as follows. A copper sulfate solution in which 45 to 70 g of copper sulfate is dissolved in 10 liters of water,
1.5 parts by volume to a mixture of lapilli and black clay in an appropriate ratio
Add about 2.0 times and stir gently.
The oxidation treatment is performed by heating for 0 to 12 hours. During the oxidation treatment, the pH value is maintained at 3.5 to 5.0.

【0009】酸化処理が完了すると、粘土状のものに覆
われた礫状物と、粘土状物質とが形成される。前者は固
形の礫状水質活性剤となり、後者は自然乾燥させると粉
末水質活性剤となる。さらに粉状物を澱粉のり、ふのり
などの結合材で固形化すると、固形化水質活性剤とな
る。結合材としては、澱粉のりなどの天然素材を用いる
のが好ましいが、化学のりも使用できる。
[0009] When the oxidation treatment is completed, a gravelly material covered with a clay-like material and a clay-like material are formed. The former becomes a solid gravel-like surfactant, and the latter becomes a powdery surfactant when air-dried. Further, when the powdery substance is solidified with a binder such as starch paste or seaweed, it becomes a solidified water activator. As the binder, it is preferable to use a natural material such as starch paste, but a chemical paste can also be used.

【0010】なお、酸化処理には特別の器具は必要でな
く、鉄鍋程度で十分である。又原料となる火山礫と黒土
とは、その地の自然状態が保たれてさえいれば産地によ
る格別の差異はない。
No special equipment is required for the oxidation treatment, and an iron pot is sufficient. In addition, there is no particular difference between the lapilli and black soil used as raw materials depending on the place of production as long as the natural state of the land is maintained.

【0011】[0011]

【作用】酸化処理により火山礫及び黒土は殺菌されると
ともに、黒土は微細な間隙を有する粘土状となる。その
ため礫状水質活性剤は、もともと有する多数の小孔と、
礫状物を覆う粘土状物とが、強い吸着性、空気溶解効率
向上性を発揮するとともに、水質浄化に有効な微生物の
極めて良好な培地となる。又粘土状物の粉末、及びこれ
を固形化したものも、どうようの作用を有する。
The oxidizing treatment sterilizes lapilli and black soil, and the black soil becomes clay-like with fine gaps. Therefore, the pebbly water surfactant has many small pores originally possessed,
The clay-like material that covers the gravel-like material exhibits a strong adsorptivity and an improvement in the efficiency of air dissolution, and provides a very good medium of microorganisms effective for water purification. In addition, clay-like powders and solidified ones have the same effect.

【0012】[0012]

【実施例1】ビ−カ−に入れた1リットルの水道水に、
容量比で火山礫100に黒土30を混合して酸化処理し
た礫状水質活性剤を、容量比で0.1%加えたものと、
対照として何も加えないものとを、72時間放置したの
ち、亜硫酸ナトリウムをそれぞれ1.6gを加えてDo
値を0とし、各ビ−カ−に0.6リットル/分のエヤを
送って、Do値の変化を調べた。
Example 1 1 liter of tap water in a beaker
A gravel water activator oxidized by mixing black clay 30 with volcanic gravel 100 by volume ratio and adding 0.1% by volume ratio;
As a control, a sample to which nothing was added was allowed to stand for 72 hours, and then 1.6 g of sodium sulfite was added, and Do was added.
The value was set to 0, and an air of 0.6 L / min was sent to each beaker, and the change in the Do value was examined.

【0013】送風開始から1時間まで急激にDo値が増
加し、送風を停止した4時間後には、前者は9.5、後
者が9に達した。そして8時間後には前者は3.4を維
持し、後者はほぼ0.9を維持した。24時間後もDo
値は2.4の差が確認された。なお野水(BOD15程
度)の場合も、ほぼどうようの変化が見られた。
The Do value rapidly increased until one hour from the start of the air supply, and reached 9.5 in the former and 9 in the latter four hours after the air supply was stopped. After 8 hours, the former maintained 3.4 and the latter maintained approximately 0.9. Do 24 hours later
A value of 2.4 was confirmed. In the case of wild water (about BOD 15), almost the same change was observed.

【0014】[0014]

【実施例2】産業排水(BOD150程度)を1リット
ルをビ−カ−に入れ、容量比で0.3%をビカ−に投入
した。対照試験として、前記産業排水のみを1リットル
をビ−カ−に入れた。両者とも約30分間曝気したのち
放置した。2時間後には対照産業排水との間にDo値で
1.5の差が生じたのち、24時間後もこの差を維持し
た。
Example 2 One liter of industrial waste water (about BOD 150) was put into a beaker, and 0.3% by volume was put into the beaker. As a control test, only 1 liter of the industrial wastewater was placed in a beaker. Both were aerated for about 30 minutes and then left. After 2 hours, a difference in Do value of 1.5 from the control industrial wastewater occurred, and this difference was maintained after 24 hours.

【0015】前記礫状水質活性剤を、生活排水、活性汚
泥(MLSS1500程度)に産業排水(BOD150
程度)を加えたものなどに投入した場合も、少なくとも
約24〜72時間を経過すれば、礫状水質活性剤を投入
しない場合に比べて、高いDo値を確保維持できる。
The gravelly water activator is converted into domestic wastewater and activated sludge (about MLSS 1500) by industrial wastewater (BOD150).
) Can be secured and maintained after at least about 24 to 72 hours, compared to a case where the pesticidal water quality activator is not added.

【0016】[0016]

【実施例3】水量約1500t、深さ約0〜5m、鯉
(平均体長約30cm)が約200匹生息し、流入水は
雨水のみの野池に、実施例1の酸化処理で得られた粉末
水質活性剤を、前記水量に対して重量比で0.01%を
散布した。散布の5日後に容量1tの循環装置を設置し
て、前記水量に対して容量比で約0.003%の実施例
1と同様の礫状水質活性剤を、循環装置内に設置した複
数段の棚に配設した。そして20リットル/分のエヤを
循環装置内に送るとともに、ポンプで270リットル/
分の池の水を循環装置内へ送った。
Example 3 About 1500 tons of water, about 0 to 5 m in depth, about 200 carps (average body length about 30 cm) inhabit, and the inflow water was a rainwater-only field pond, and the powder obtained by the oxidation treatment of Example 1 was used. The water activator was sprayed at 0.01% by weight based on the water amount. Five days after spraying, a circulation device having a capacity of 1 t was installed, and a gravel water activating agent similar to that of Example 1 having a volume ratio of about 0.003% with respect to the water amount was installed in the circulation device. On the shelf. Then, while sending 20 l / min of air into the circulation device, the pump is used to pump 270 l / min.
The water from the minute pond was sent into the circulation device.

【0017】ポンプ運転開始から30日後に、次の結果
を得た。但し括弧内は原水、単位はmg/リットルであ
る。なお透明度は原水で10cm、30日後で82cm
であった。
The following results were obtained 30 days after the start of pump operation. However, parentheses indicate raw water, and the unit is mg / liter. The transparency is 10 cm in raw water and 82 cm after 30 days.
Met.

【0018】BOD 2.2 (16) COD 3.2 (15) SS 2.4 (35) 全窒素 0.46(3.2) 全リン 0.15(0.15)BOD 2.2 (16) COD 3.2 (15) SS 2.4 (35) Total nitrogen 0.46 (3.2) Total phosphorus 0.15 (0.15)

【0019】又この池に生息する微生物の変化は以下の
とおりである。 種 類 原 水 30日後 緑藻・珪藻類 非常に多い 非常に少ない オエキスティス属 非常に多い 非常に少ない ビワクンショウモ 多い 非常に少ない セネデスチス 多い 非常に少ない スフェロティルス 多い 非常に少ない ゾウリムシ 普通 非常に少ない ボルティセラ 非常に少ない 普通 ポテリオデンドロン 非常に少ない 普通 ロタリア 非常に少ない 普通 フィロディナ 非常に少ない 普通 モノスティラ 非常に少ない 普通 輪虫類 非常に少ない 普通 ミジンコ類 少ない 普通 その他 非常に少ない 非常に多い
Changes in microorganisms inhabiting this pond are as follows. Species Raw water 30 days later Green algae and diatoms Very much Very little Oechtis genus Very much Very little Biwamushroom many Very little Senedestis Many Very little Spherotils Many Very little Paramecium Usually Very little Borticella Very little Very low Potterio dendron Very low Normal Rotalia Very low Normal Firodina Very low Normal Monostyra Very low Normal Rotifer Very low Normal Daphnia Low Normal Other Very low Very high

【0020】この発明の水質活性剤は、ペット用水槽、
営業用水槽の水の浄化にも有効であるが、池の浄化につ
いては、次のような特徴が見られた。即ち水質活性剤の
使用後24時間で、必ずボルティセラの生息が確認で
き、短期間で原生動物ないし後生動物が多種、多様に生
息する。なおペット用水槽の浄化には、固形化水質活性
剤を使用するのが便利である。
The water activator of the present invention comprises a pet aquarium,
It is also effective in purifying water in commercial aquariums, but the following characteristics were observed in pond purification. That is, 24 hours after the use of the water-active agent, the inhabitation of Balticella can be confirmed without fail, and a wide variety of protozoa or metazoans inhabit in a short period of time. It is convenient to use a solidified water activator for purification of the pet tank.

【0021】又赤潮などの発生原因といわれる微生物が
極端に減少する。そしてPH値は7.0前後で、Do値
は4〜5でいずれも安定する。さらに水環境が良好にな
るため、魚の活発な産卵状態見られ、みずすまし、その
他の小動物が確認された。
Also, the number of microorganisms that are said to be the cause of red tide and the like is extremely reduced. The PH value is around 7.0, and the Do value is 4 to 5, which are all stable. Since the water environment was further improved, active spawning conditions of fish were observed, and water spoiling and other small animals were confirmed.

【0022】[0022]

【実施例4】前処理槽の溢水が曝気槽へ、曝気槽の溢水
が沈降槽へ流入し、沈降槽から処理水が流出する処理槽
を設置する。容量はそれぞれ12リットル、60リット
ル、6リットルである。
[Embodiment 4] A treatment tank is installed in which the overflow of the pretreatment tank flows into the aeration tank, the overflow of the aeration tank flows into the settling tank, and the treated water flows out of the settling tank. The capacities are 12 liters, 60 liters and 6 liters, respectively.

【0023】まず曝気層に60リットルの活性汚泥と、
0.18リットル(活性汚泥に対して容量比0.3%)
の実施例1の礫状水質活性剤を入れ、約100時間にわ
たって、12時間毎の間歇曝気を行なう。
First, 60 liters of activated sludge was added to the aeration layer,
0.18 liter (0.3% by volume based on activated sludge)
And the intermittent aeration is performed every 12 hours for about 100 hours.

【0024】この結果、繊毛虫類、輪虫類、その他の生
物層が厚く、溶存酸素量が大きい、無臭の良好な活性汚
泥が得られた。この活性汚泥は、沈降性がよくしかもバ
ルキングなどの発生がないものである。
As a result, an activated odorless odorless sludge having a thick ciliate, rotifer, and other biological layers, a large amount of dissolved oxygen, and odor was obtained. This activated sludge has good sedimentation properties and does not generate bulking or the like.

【0025】この活性汚泥を前処理槽に約6リットル投
入し、BOD550程度の産業排水を初日の20リット
ルから次第に増やして7日目に80リットル、8日目以
降は120リットルを、それぞれ8時間かけて前処理槽
に投入する。そして前処理槽へは8リットル/分、曝気
槽へは16リットル/分のエヤを常時送る。
About 6 liters of this activated sludge is put into the pretreatment tank, and the amount of industrial wastewater having a BOD of about 550 is gradually increased from 20 liters on the first day, and 80 liters on the seventh day, and 120 liters on the 8th day and thereafter, for 8 hours each. Into the pretreatment tank. Then, 8 l / min air is always sent to the pretreatment tank and 16 l / min air is sent to the aeration tank.

【0026】8日目以降120リットルの産業排水を、
平成5年5月から6月までの2か月間毎日投入した結
果、以下のような良好な処理水が得られた。但し単位は
mg/リットルである。透視度は、原水の9cmから1
か月以降は100cm以上となった。
From the eighth day, 120 liters of industrial wastewater is
As a result of the daily charging for two months from May to June 1993, the following good treated water was obtained. However, the unit is mg / liter. Transparency is from 9cm to 1cm of raw water
After 100 months, it became 100 cm or more.

【0027】 [0027]

【0028】曝気槽の汚泥中に生息する微生物の変化
を、次に示す。 種 類 原汚泥 30日後の汚泥 アルセラ 非常に多い 少ない アスピディカ 多い 普通 ゾウリムシ 多い 非常に少ない ロタリアフィロディナ 普通 普通 ボルティセラ 普通 普通 ゾ−タニウム 普通 普通 リトノス 少ない 普通 シロクマ 少ない 普通 アメ−バ 非常に少ない 普通 ナイス 非常に少ない 普通 シヤトスピラ 非常に少ない 普通 コ−プロテス 非常に少ない 普通 プラティアス 非常に少ない 普通 リケ−ン 非常に少ない 普通 プロドトン 非常に少ない 普通 リトノス 非常に少ない 普通 その他 非常に少ない 非常に多い
The changes in microorganisms that live in the sludge in the aeration tank are as follows. Type Raw sludge Sludge after 30 days Alcera Very much Low Aspidica Many Normal Paramecium Many Very low Rotalia firodina Normal Normal Balticella Normal Normal Zo-tanium Normal Normal Litonos Low Normal Polar bear Low Normal Ameba Very low Normal Nice Very low Ordinary shyatospira Very low Ordinary co-protease Very low Ordinary plateias Very little Ordinary very little Ordinary Prodton Very little Ordinary Lithnos Very little Ordinary Other Very little Very much

【0029】さらにBOD3500程度の産業排水を、
前処理槽、曝気槽への送風量を前記の倍に、礫状水質活
性剤の投入量を3倍にした前記処理槽を用いて処理した
場合も、ほぼどうようの良好な処理水が得られた。その
結果を下に示す(単位はmg/リットル)。
[0029] Further, industrial wastewater with a BOD of about 3500
Even when the treatment is performed using the treatment tank in which the amount of air blown into the pretreatment tank and the aeration tank is doubled as described above and the input amount of the gravel-like water activator is tripled, almost how good treated water is obtained. Was done. The results are shown below (unit: mg / liter).

【0030】 [0030]

【0031】なお原水で見られなかった大腸菌は40日
後に12個/ミリリットル、透視度は原水で5cm、4
0日後は100cm以上であった。
Escherichia coli not found in the raw water was 12 cells / ml after 40 days, and the transparency was 5 cm in the raw water and 4 cm / ml.
0 days later, it was 100 cm or more.

【0032】この産業排水の処理には、以下のような特
徴が見られる。送風量は高濃度の排水及び汚泥にもかか
わらず、極端に少量で足りる。又曝気槽のPH値は、
7.5〜8.3と高めで推移するが、沈降槽では7.2
前後で安定するし、原水投入中のDo値は、8.3〜
0.5程度に推移するが、投入完了後2時間程度経過す
ると急速に回復する。
The treatment of industrial wastewater has the following characteristics. An extremely small amount of air is required despite the high concentration of wastewater and sludge. The PH value of the aeration tank is
Although it is relatively high at 7.5 to 8.3, it is 7.2 in the sedimentation tank.
It is stable before and after, and the Do value during raw water input is 8.3 ~
It changes to about 0.5, but recovers rapidly about 2 hours after the completion of charging.

【0033】しかも高濃度汚泥(MLSS10000)
にもかかわらず、沈降性はほぼ良好で、30分後に63
0cc、60分後に490cc、120分後に330c
c、180分後に300ccであった。
Moreover, high concentration sludge (MLSS10000)
Nevertheless, the sedimentation was almost good, with 63 minutes after 30 minutes.
0cc, 490cc after 60 minutes, 330c after 120 minutes
c, 300 cc after 180 minutes.

【0034】汚泥中の微生物は、原生動物から後生動物
と、多種多様に生息し、投入後約24時間経過すると、
ボルティセラの生息が確認できる。そして汚水処理中に
悪臭の発生はなく、原水の持つ臭気は前処理層で感じら
れない程除去される。
The microorganisms in the sludge inhabit a wide variety of species, from protozoa to metazoans, and when about 24 hours have passed since introduction,
We can confirm the inhabitation of Balticella. No odor is generated during the sewage treatment, and the odor of the raw water is removed so as not to be felt in the pretreatment layer.

【0035】産業排水の処理にあたって、BOD、CO
Dの高除去率を確保し、安定化した処理水を得るのは当
然であるが、従来の活性汚泥法では窒素、リンの除去は
難しいといわれてきた。しかしこの発明の水質活性剤を
投入することで、BOD、CODは勿論、窒素、リンも
高い除去率を得られることが確認できた。又大腸菌につ
いても低い値を確保でき、塩素消毒も必要としないで放
流できることが確認できた。
In the treatment of industrial wastewater, BOD, CO
Although it is natural to secure a high removal rate of D and obtain stabilized treated water, it has been said that it is difficult to remove nitrogen and phosphorus by the conventional activated sludge method. However, it was confirmed that by adding the water activator of the present invention, a high removal rate of nitrogen and phosphorus as well as BOD and COD can be obtained. Also, it was confirmed that E. coli could be released at a low value without chlorination.

【0036】なお処理槽中に沈降した余剰汚泥は、従来
は乾燥処理や脱水処理後に肥料または産業廃棄物として
処理していた。しかしこの発明の水質活性剤を使用した
余剰汚泥は、1リットルにつき6リットル/分のエヤを
送ると、5日間で約40%の減少が見られ、その処理が
容易になる。
The excess sludge settled in the treatment tank has conventionally been treated as fertilizer or industrial waste after drying treatment and dehydration treatment. However, surplus sludge using the water activator of the present invention is reduced by about 40% in 5 days when 6 l / min of air is sent per liter, which makes the treatment easier.

【0037】又生活排水、生活排水と糞尿との雑排水の
処理にもこの発明の水質活性剤は有効であることはいう
までもない。
It is needless to say that the water activator of the present invention is also effective in the treatment of domestic wastewater and miscellaneous wastewater of domestic waste and manure.

【0038】[0038]

【発明の効果】自然界にある火山礫と黒土とを酸化処理
するだけで得られ、又格別の処理装置を要しないで、水
道水、水槽、プ−ル、川、池、湖沼、生活排水、産業排
水を、効率的に極めて低コストで浄化処理できる。
The present invention can be obtained only by oxidizing lapilli and black soil in the natural world, and does not require any special treatment equipment. Tap water, water tanks, pools, rivers, ponds, lakes and marshes, domestic wastewater, Industrial wastewater can be purified efficiently and at extremely low cost.

【0039】しかも微生物を利用して処理するので、処
理後化学薬品を使って消毒する必要がなく、処理水をそ
のまま放流しても何ら自然界に悪影響を与えない。
Furthermore, since the treatment is carried out by using microorganisms, there is no need to disinfect with a chemical after the treatment, and even if the treated water is discharged as it is, there is no adverse effect on nature.

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 酸化処理により殺菌し、吸着性と空気溶
解効率とを向上させるとともに、微生物培地に適するよ
うにした多孔質の火山礫と黒土との混合物から得られる
礫状物、及び又は粘土状物を粉末化した粉末物からなる
水質活性剤。
1. Sterilization by oxidation treatment, adsorption and air solubility
It improves the dissolution efficiency and is suitable for microbial culture media.
A water activator comprising a pebble obtained from a mixture of dried porous volcanic pebble and black soil, and / or a powder obtained by pulverizing a clay-like substance.
【請求項2】 粉末物は、結合材で固形化されている請
求項1の水質活性剤。
2. The water activator according to claim 1, wherein the powder is solidified with a binder.
【請求項3】 多孔質の火山礫と黒土との混合物を、8
0℃ないし100℃の硫酸銅溶液中で、PH値を3.5
〜5.0に維持しながら10〜12時間酸化処理する水
質活性剤の製造方法。
3. A mixture of porous lapilli and black soil,
In a copper sulfate solution at 0 ° C. to 100 ° C., the pH value was 3.5.
A method for producing a water-active agent, wherein the water-active agent is subjected to an oxidation treatment for 10 to 12 hours while maintaining the same at a value of 5.0.
JP5264176A 1993-09-27 1993-09-27 Water activator and its production method Expired - Lifetime JP2903359B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5264176A JP2903359B2 (en) 1993-09-27 1993-09-27 Water activator and its production method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5264176A JP2903359B2 (en) 1993-09-27 1993-09-27 Water activator and its production method

Publications (2)

Publication Number Publication Date
JPH0796275A JPH0796275A (en) 1995-04-11
JP2903359B2 true JP2903359B2 (en) 1999-06-07

Family

ID=17399523

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5264176A Expired - Lifetime JP2903359B2 (en) 1993-09-27 1993-09-27 Water activator and its production method

Country Status (1)

Country Link
JP (1) JP2903359B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006102701A (en) * 2004-10-08 2006-04-20 Michiyoshi Sugiyama Apparatus for cleaning water

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6028814A (en) * 1983-07-25 1985-02-14 Satoo Morimoto Purifying agent of sewage or the like
JPH0523047A (en) * 1991-07-16 1993-02-02 Tanimoto Masachika Planting material for culture of horticultural plant and sewage cleaning material
JPH05169055A (en) * 1991-12-20 1993-07-09 Yoko Hirata Sewage purifier and its filter medium

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006102701A (en) * 2004-10-08 2006-04-20 Michiyoshi Sugiyama Apparatus for cleaning water
JP4502772B2 (en) * 2004-10-08 2010-07-14 倫義 杉山 Water purification device

Also Published As

Publication number Publication date
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