JP2512420B2 - Water treatment method, treatment agent and treatment equipment - Google Patents

Water treatment method, treatment agent and treatment equipment

Info

Publication number
JP2512420B2
JP2512420B2 JP60124920A JP12492085A JP2512420B2 JP 2512420 B2 JP2512420 B2 JP 2512420B2 JP 60124920 A JP60124920 A JP 60124920A JP 12492085 A JP12492085 A JP 12492085A JP 2512420 B2 JP2512420 B2 JP 2512420B2
Authority
JP
Japan
Prior art keywords
water
pipe
rotary
contaminated
sludge
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 - Lifetime
Application number
JP60124920A
Other languages
Japanese (ja)
Other versions
JPH01310790A (en
Inventor
康之 桜田
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP60124920A priority Critical patent/JP2512420B2/en
Publication of JPH01310790A publication Critical patent/JPH01310790A/en
Priority to CN91102048A priority patent/CN1065644A/en
Priority to CN91102047A priority patent/CN1065643A/en
Application granted granted Critical
Publication of JP2512420B2 publication Critical patent/JP2512420B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A40/00Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
    • Y02A40/10Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
    • Y02A40/20Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses

Landscapes

  • Separation Of Suspended Particles By Flocculating Agents (AREA)
  • Treatment Of Sludge (AREA)
  • Fertilizers (AREA)

Description

【発明の詳細な説明】Detailed Description of the Invention 【産業上の利用分野】[Industrial applications]

この発明は、極めて短時間に汚濁水、屎尿処理排水、
青子、赤潮又は機械油含有排水を透明に浄化する汚濁水
の浄化処理方法又は処理装置に関するものである。
This invention is a very short time polluted water, human waste treatment wastewater,
The present invention relates to a method or apparatus for purifying polluted water for purifying blue water, red tide, or wastewater containing machine oil transparently.

【従来の技術】[Prior art]

従来、汚濁水その他の水処理には硫酸アルミニウムを
混合し、時間をかけて沈殿槽を通過させて重力によって
水に含まれていた砂や不純物等を沈殿分離し、バクテリ
ヤで処理し、これに化学薬品を混入して攪拌処理し、更
にこの薬品を中和してから放水させていたが、更にその
後の浄化処理を必要とする程度にしか浄化できなかっ
た。
Conventionally, for the treatment of contaminated water and other water, aluminum sulfate is mixed, and over a period of time it is allowed to pass through a settling tank to precipitate and separate the sand and impurities contained in the water by gravity, and then treated with bacteria. The chemicals were mixed and stirred, and the chemicals were neutralized and then water was released, but the purification could only be performed to the extent necessary for the subsequent purification.

【発明が解決しようとする課題】[Problems to be Solved by the Invention]

しかし、その間の処理に18時間以上もの長時間を要し
て水を滞留させるために膨大な敷地と設備と費用とを必
要とするという問題点があったので、国の援助なしに市
町村や地方自治体の資金だけではこのような大規模の水
処理施設を建設することができなかった。そこで、小規
模で合理的な方法、装置及び薬品等による汚濁水処理の
開発が国の内外から強く求められていたが、今日まで尚
これを解決する技術は未開発であった。そこで、本発明
は、これらの問題点を解決するために開発されたもので
ある。
However, there was a problem that it took a long time of 18 hours or more to process water during that time and required enormous amount of site, equipment and cost to retain water. It was not possible to construct such a large-scale water treatment facility with the funds of the local government alone. Therefore, there has been a strong demand from Japan and abroad for the development of small-scale, rational methods, devices, chemicals, and the like for polluted water treatment, but to date, no technology has yet been developed. Therefore, the present invention was developed to solve these problems.

【課題を解決するための手段】[Means for Solving the Problems]

本発明は、汚濁水を浄化するために、凝集剤として石
灰、生石灰等のカルシウム含有物を使用し、その他の薬
剤として塩化鉄、硫酸アルミニウム、明礬、硫酸鉄、ポ
リ塩化アルミニウム、珪酸ナトリウム等の化合物を使用
し、又はこれらを適宜組合せて1回以上浄化を繰り返し
て使用することにより汚濁水を浄化処理する方法又は装
置に関するものである。実際には、石灰を基準としてこ
れに明礬、塩化鉄(III)又はポリ塩化アルミニウム等
を加えて汚濁水に添加し、又はこれらを予め混合してか
ら汚濁水に添加した後、これらを良く攪拌して汚濁水中
溶解したり浮遊して含まれた泥や砂や不純物等をこれら
の薬品の相乗作用によって急速に凝集沈殿させることに
より、数分以内で浄化された透明な水を分離することが
できる。重金属等も95%除去することができ、又屎尿処
理工程の残留アンモニアと窒素とを中和させて消滅させ
ることができる。なお、処理される汚濁水に油や石鹸類
が含まれていてもこれらの薬剤を添加混合することによ
り油も石鹸類も除去されることができる。 石灰又は生石灰等のカルシウム含有物質と明礬又は塩
化鉄とを適量ずつ交互にその量を増減して汚濁水に混入
して良く攪拌すると、各物質の凝集作用及び反応作用の
相乗効果によって1分以内に汚濁水からその泥が底に沈
殿し、3分以内に水が上水の様に透明に浄化される。こ
のカルシウム含有物質と明礬又は塩化鉄等との使用は、
汚濁水だけでなく青子又は赤潮に対しても沈殿分離効果
があり、更に、この汚濁水、青子又は赤潮に対して、カ
ルシウム含有物質を多く加えるか、又はこれに加えて過
マンガン酸カリ、ClO2及び/又は塩素類の殺菌剤を同時
に使用すると、凝集沈殿処理に加えて殺菌、消臭、脱色
する効果も発揮する。凝集剤としては、石灰、生石灰の
他に、ライポン(ライオン油脂KK製の陰イオン活性剤の
商品名);貝化石;貝類若しくは甲殻類の粉末;サン
ゴ、サンゴショウの粉末;魚類動植物類若しくはプラン
クトンのカルシウム含有死骸、又はカルシウム含有岩石
等、CaOを多量に含有する物質等は凝集効果を発揮す
る。又、CaO 15−100%、Co2 20−40%、SiO2 10−3
0%、MgO 1−5%、Fe2O3 1−3%、P2O2 0.1−10
%、Mn 1−5%等を含む物質、CaOを98%含有する物
質等のカルシウムを含有する物質に明礬、塩化鉄等の化
学反応作用物質を適宜混合して、上水、下水、屎尿、汚
濁水、青子又赤潮等の水処理に使用する時には、これら
凝集剤中にCaOの含有量が多い程凝集効果が大きく、又
その使用量も少なくてすむという効果を発揮する。 カルシウム含有物質以外の添加混合薬剤としては、無
機系凝集補助剤として、明礬(硫酸アルミニウム他)、
塩化鉄(III)、硫酸鉄(II)、(III)、塩化コッパラ
ス、硫酸カリウム、ポリ塩化アルミニウム等がある。
又、有機系凝集補助剤としては、その陰イオン系として
ポリアクリル酸ナトリウム、ポリアクリルアミドの部分
加水分解塩等があり、その非イオン系としてポリアクリ
ルアミド、ポリオキシエチレン等があり、又その陽イオ
ン系としてはポリエチレンイミン、第4級アンモニウム
塩類又はその他の高分子凝集剤等がある。これらの補助
剤は、単体及び/又はそれらの混合物として、石灰、生
石灰等のカルシウム含有物質と混合して使用され、更に
これに殺菌剤としてClO2、過マンガン酸カリウム、及び
/又は塩素を適宜混合して使用されるか、又は浄化菌を
混合攪拌して使用される。 本発明の浄化処理対象物は、上水、下水、屎尿、汚
水、濁水、工業排水、青子又赤潮、食品工場排水、食肉
加工場排水、魚肉加工場排水、畜産排水、生活排水であ
り、又河川工事、ダム工事、隧道工事、トンネル工事、
高圧力水噴射式切断工事、鑿岩工事、ビル工事、地下道
工事等からの排水又はリサイクル水である。このような
排水の浄化処理において、本発明は適宜の装置、機械又
は浄化槽等を組み合わせて実施すると極めて短時間で大
量の汚濁排水を浄化することができる。 カルシウム含有物質と一緒に塩化鉄、塩化アルミニウ
ム、炭酸カルシウム、硫酸第2鉄、硫酸アルミニウム、
炭酸ナトリウム、硫酸、塩酸、ゼオライト、硅藻土、硅
酸ナトリウム等の単体又はその混合物を汚濁水中に添加
して混合攪拌すると、水は完全に透明になり、汚濁水中
の泥は急速に分離されて水底に沈殿する。そこで、これ
らの物質も適宜混合して使用すると便利である。 これらの無機物質の中には土壌改良剤として使用され
るものも含まれており、又植物の栄養素(凝集剤、凝集
補助剤等)としても有効であるものも含まれており、更
に又これらの中には消臭効果(酸、アルカリ等)を有す
るものもふくまれているので、これらの物質を使用して
沈殿堆積された汚泥は、そのまま肥料として使用でき
る。又汚濁水の浄化時や屎尿や動物の蓄血液や各種廃棄
物の水処理途中や処理完了後の廃棄物に上記栄養素を含
有する物質を添加して混合し、これにアゾートバクター
菌(トーマス菌)やその他の発酵菌を添加して良く攪拌
すると汚濁水の浄化を促進するとともに、発酵して完熟
肥料が得られるので、これを野菜、果物、稲、その他の
植物の施肥として使用する場合には、通常肥料の2倍の
収穫を得ることができる。 次に、大量の汚濁水に凝集剤として石灰、生石灰等の
カルシウム含有物質及びその他の薬剤として明礬や塩化
鉄(III)等を添加するか、或いは更にその他の凝集剤
を適宜に組み合わせて添加使用するか、又カルシウム含
有物質、カルシウム分を含まない凝集剤及び凝集補助剤
等を2種以上適宜に組み合わせて汚濁水に混入して良く
攪拌することにより、泥と透明な水とに急速に分離する
ことのできる本発明の装置の1例を図を用いて説明す
る。 第1図に示すように汚濁水が導入される導水管1内に
外部モーター2に連結するシャフト3によって回転する
スクリュー4を取り付けるか、第2図に示すように導水
管内に水の流れによって回転するスクリュー5を取り付
けるか、又は第3図に示すように導水管3の内壁に、突
起した螺旋状の適数の帯板又はヒダ6等を取り付けるこ
とにより導水管中で水流を回転させる。この導水管の上
方に、凝集剤やその他の薬剤等を水量に比例して常に一
定量供給するための計量器付投入装置7を設置する。こ
の装置からパイプ8を通して導水管中に、汚濁水1トン
に対してカルシウム含有物質及び塩化鉄、明礬又はポリ
塩化アルミニウム等を適量投入して導入管中に流れる汚
濁水に攪拌混合して反応させ、汚濁水中に含まれる泥や
不純物等を水より凝集させる。その後回転式分離沈殿濾
過装置、シックナー、クラリファイヤー、沈殿槽、濾過
槽、その他適当な分離沈殿濾過装置を使用して汚濁水か
ら泥と水とを分離して浄化された水を回収する。 この一方法としては、凝集剤等が混入された後、導水
管より出た汚濁水を第4図に示すパイプ10から適宜形状
の汚水浄化兼汚泥回収装置11に導入して汚泥を沈殿分離
させ、分離された水を更にフィルター12で濾過したり、
或いはサイクロンを設けて更に分離する。又、第5図に
示されるにサイクロンのような形状の攪拌回転式分離濾
過装置9を設け、これに導水管1から凝集剤が混入され
た汚濁水を導入し、その中段に装置内の水を回転させる
複数の攪拌機13を設置してこれにより水を回転させて分
離処理を行う。又、第5図に示されるように、他の噴射
回転式分離濾過装置25の壁に、それに沿って水を回転さ
せるための複数の噴射水管18を設け、この管より装置内
の壁に沿って水を噴射させて容器内の水を回転させなが
ら、その下方において導水管1′の先端を装置9より装
置25に向かって斜め下に向けて装着し、これから導入さ
れた混合液を装置25内で回転させ、泥や汚物を下に沈殿
させ、透明な水を急速に上昇させ、これを更に濾過する
必要がある場合には網、フィルター又は蛭石の入ったフ
ィルター19を通して濾過処理する。 分離された泥は装置9、25の底に堆積するので、装置
の底に連通する排泥管22を設け、この管の元と先にそれ
ぞれ1個以上のバルブ又はバタフライバルブ23を設けて
これを交互に開閉することにより、排泥管中に泥水を取
り入と取り出とを行う。更に排泥管に他の装置を連結し
て薬品やバクテリヤを混入したり、又は他の装置中に移
行させて攪拌して発酵させながら汚泥を取り出すことが
できる。
In order to purify polluted water, the present invention uses calcium-containing substances such as lime and quicklime as a coagulant, and iron chloride, aluminum sulfate, alum, iron sulfate, polyaluminum chloride, sodium silicate and the like as other agents. The present invention relates to a method or an apparatus for purifying polluted water by using a compound, or by appropriately combining these and repeating the purification once or more. In practice, add alum, iron (III) chloride, polyaluminum chloride, etc. to lime based on lime and add it to the polluted water, or mix these in advance and add to the polluted water, then stir them well. It is possible to separate the purified clear water within a few minutes by rapidly coagulating and sedimenting the mud, sand, impurities, etc. that are dissolved or suspended in the polluted water by the synergistic action of these chemicals. it can. 95% of heavy metals can be removed, and residual ammonia and nitrogen in the human waste treatment process can be neutralized and eliminated. Even if the treated polluted water contains oil or soap, the oil and soap can be removed by adding and mixing these chemicals. If calcium-containing substances such as lime or quick lime and alum or iron chloride are alternately adjusted in appropriate amounts and mixed in polluted water and stirred well, within 1 minute due to the synergistic effect of the agglomeration and reaction of each substance The mud settles to the bottom from the polluted water, and the water is purified to clear water like clean water within 3 minutes. The use of this calcium-containing substance and alum or iron chloride,
It has a precipitation separation effect not only on polluted water but also on blue water or red tide.In addition, a large amount of a calcium-containing substance is added to this polluted water, blue water or red tide, or in addition to this, potassium permanganate, ClO. When 2 and / or chlorine type bactericides are used at the same time, in addition to the coagulation-sedimentation treatment, bactericidal, deodorant and decolorizing effects are exhibited. As flocculants, in addition to lime and quicklime, lypon (trade name of anion activator manufactured by Lion Oil & Fat KK); fossil shell; powder of shellfish or shellfish; powder of coral, coral ginger; fish, animals and plants or plankton Calcium-containing carcasses, or calcium-containing rocks, and other substances that contain large amounts of CaO exhibit a cohesive effect. Also, CaO 15-100%, Co 2 20-40%, SiO 2 10-3
0%, MgO 1-5%, Fe 2 O 3 1-3%, P 2 O 2 0.1-10
%, Mn 1-5%, etc., CaO 98%, etc., calcium-containing substances, etc., and alum, iron chloride and other chemical reaction substances are appropriately mixed to obtain tap water, sewage, human waste, When it is used for treating water such as polluted water, algae or red tide, the greater the content of CaO in these aggregating agents, the greater the aggregating effect, and the smaller the amount used. As an additive mixed agent other than the calcium-containing substance, alum (aluminum sulfate etc.)
There are iron (III) chloride, iron (II) sulfate, (III), copper chloride, potassium sulfate, polyaluminum chloride and the like.
The organic coagulant aids include sodium polyacrylate, partially hydrolyzed salts of polyacrylamide, etc. as its anionic system, polyacrylamide, polyoxyethylene, etc. as its nonionic system, and its cations. Examples of the system include polyethyleneimine, quaternary ammonium salts, and other polymer flocculants. These auxiliaries are used as a simple substance and / or a mixture thereof by mixing with a calcium-containing substance such as lime and quicklime, and further, ClO 2 , potassium permanganate, and / or chlorine as a bactericide are appropriately used. It is used as a mixture, or the bacterium is mixed and stirred. The purification treatment object of the present invention is tap water, sewage, human waste, sewage, turbid water, industrial drainage, Aoko or Akashio, food factory drainage, meat processing plant drainage, fish processing plant drainage, livestock drainage, domestic drainage, and River construction, dam construction, tunnel construction, tunnel construction,
It is drainage or recycled water from high pressure water jet cutting work, chisel work, building work, underpass work, etc. In the purification treatment of such wastewater, the present invention can purify a large amount of polluted wastewater in an extremely short time when combined with an appropriate device, machine or septic tank. Iron chloride, aluminum chloride, calcium carbonate, ferric sulfate, aluminum sulfate, together with calcium-containing substances,
When simple substances such as sodium carbonate, sulfuric acid, hydrochloric acid, zeolite, diatomaceous earth, sodium silicate, etc. or a mixture thereof are added to the polluted water and mixed and stirred, the water becomes completely transparent and the mud in the polluted water is rapidly separated. Settles on the bottom of the water. Therefore, it is convenient to use these substances by appropriately mixing them. Some of these inorganic substances are used as soil conditioners, and some are also effective as plant nutrients (flocculants, flocculants, etc.). Since some of them have deodorant effects (acid, alkali, etc.), sludge precipitated and deposited using these substances can be used as it is as a fertilizer. In addition, the substances containing the above nutrients are added to and mixed with wastewater during purification of contaminated water, blood collection of human waste, blood storage of animals, and water treatment of various wastes, and mixed with this. ) And other fermenting bacteria are added and well stirred to promote purification of polluted water and ferment to obtain fully fertilized fertilizer, so when using this as fertilizer for vegetables, fruits, rice, and other plants. Can get twice as much harvest as normal fertilizer. Next, add a calcium-containing substance such as lime or quick lime as a coagulant to a large amount of polluted water and alum or iron (III) chloride as another agent, or add another coagulant in an appropriate combination. Or, by mixing two or more kinds of calcium-containing substances, calcium-free flocculants, coagulant aids, etc. into the polluted water and stirring well, the mud and clear water are rapidly separated. An example of a device of the present invention that can be used will be described with reference to the drawings. As shown in FIG. 1, a screw 4 which is rotated by a shaft 3 connected to an external motor 2 is installed in the water conduit 1 into which polluted water is introduced, or as shown in FIG. The water flow is rotated in the water guiding pipe by attaching a screw 5 or by attaching a suitable number of protruding spiral strips or folds 6 to the inner wall of the water guiding pipe 3 as shown in FIG. Above the water conduit, a metering device-equipped device 7 for constantly supplying a constant amount of a coagulant or other chemicals in proportion to the amount of water is installed. From this device, through a pipe 8, an appropriate amount of a calcium-containing substance and iron chloride, alum, polyaluminum chloride or the like is added to 1 ton of contaminated water, and the contaminated water flowing in the introduction pipe is stirred and mixed for reaction. , Coagulate mud and impurities contained in polluted water from water. Thereafter, a rotary separation settling filter, thickener, clarifier, settling tank, filtration tank, and other suitable separation settling filter are used to separate mud and water from the contaminated water to recover purified water. As one of the methods, after the coagulant and the like are mixed, the polluted water discharged from the water pipe is introduced from the pipe 10 shown in FIG. , Further filter the separated water with filter 12,
Alternatively, a cyclone is provided for further separation. Further, as shown in FIG. 5, a stirring rotary type separation / filtration device 9 having a cyclone-like shape is provided, into which polluted water mixed with a coagulant is introduced from a water pipe 1, and the water inside the device is introduced in the middle stage thereof. A plurality of stirrers 13 for rotating are installed to rotate water to perform a separation process. Further, as shown in FIG. 5, a plurality of jet water pipes 18 for rotating water along the wall of another jet rotary separation / filtration device 25 are provided along the wall inside the device. While spraying water to rotate the water in the container, the tip of the water conduit 1'is installed downwardly from the device 9 toward the device 25 obliquely downward, and the mixed liquid introduced from this is installed in the device 25. Rotate in to settle mud and debris down and rapidly raise clear water, which is filtered through a net, filter or vermiculite filter 19 if further filtration is required. Since the separated mud deposits on the bottoms of the devices 9 and 25, a drainage mud pipe 22 communicating with the bottoms of the devices is provided, and one or more valves or butterfly valves 23 are provided at the base and the tip of the pipe, respectively. By alternately opening and closing, the mud water is taken in and taken out from the mud discharge pipe. Further, the sludge can be taken out by connecting another device to the sludge pipe to mix chemicals or bacteria, or by transferring to another device and stirring to ferment it.

【実施例】【Example】

次に本発明をその実施例に基づいて説明する。 Next, the present invention will be described based on its embodiments.

【実施例1】 1リットルの汚濁水中に石灰1gと塩化鉄(III)0.33g
とを投入して良く攪拌すると20秒以内に沈殿が始まり、
1分以内に水に含まれた泥は沈殿し、3分以内に水は透
明になる。
Example 1 1 g of lime and 0.33 g of iron (III) chloride in 1 liter of polluted water
Add and and stir well, precipitation will start within 20 seconds,
The mud contained in the water settles within 1 minute, and the water becomes transparent within 3 minutes.

【実施例2】 1リットルの汚濁水中に石灰1.5gと塩化鉄(III)0.3
3gとを投入して良く攪拌すると20秒以内に沈殿が始ま
り、1分以内に水に含まれた泥は沈殿し、2分半後には
水は上水の様に透明になり、この水をガラス容器に入れ
ると水を通して反対側の景色が良く見える。
Example 2 1.5 g of lime and 0.3 iron (III) chloride in 1 liter of polluted water
Add 3 g and stir well, precipitation will start within 20 seconds, mud contained in water will settle within 1 minute, and after 2 and a half minutes the water will become clear like tap water. If you put it in a glass container, you can see the scenery on the other side through the water.

【実施例3】 1リットルの汚濁水中に石灰1.3gと明礬0.66gとを投
入して良く攪拌すると20秒以内に沈殿が始まり、1分以
内に水に含まれた泥は沈殿し、2分半後には水は上水の
様に透明になり、この水をガラス容器に入れると水を通
して反対側の景色が良く見える。
[Example 3] When 1.3 g of lime and 0.66 g of alum were added to 1 liter of polluted water and well stirred, precipitation started within 20 seconds, and mud contained in water precipitated within 1 minute, followed by 2 minutes. After half a year, the water becomes clear like tap water, and when you put this water in a glass container, you can see the scenery on the other side through the water.

【実施例4】 1リットルの汚濁水中に石灰1gと塩化鉄(III)0.33g
と明礬0.33gとを同時に投入して良く攪拌すると20秒以
内に沈殿が始まり、1分以内に水に含まれた泥は沈殿
し、3分以内に水は上水の様に透明になり、この水をガ
ラス容器に入れると水を通して反対側の景色が良く見え
る。
Example 4 1 g of lime and 0.33 g of iron (III) chloride in 1 liter of polluted water
When 0.33 g of alum and alum are added at the same time and well stirred, the precipitation starts within 20 seconds, the mud contained in the water precipitates within 1 minute, and the water becomes clear like tap water within 3 minutes. If you put this water in a glass container, you can see the scenery on the other side through the water.

【実施例5】 1リットルの汚濁水中に石灰0.33と塩化鉄(III)0.3
3gと明礬1gとを同時に投入して良く攪拌すると20秒以内
に沈殿が始まり、1分以内に水に含まれた泥は沈殿し、
3分以内に水は上水の様に透明になり、この水をガラス
容器に入れると水を通して反対側の景色が良く見える。
Example 5 0.33 of lime and 0.3 of iron (III) chloride in 1 liter of polluted water
If 3 g and 1 g of alum are added at the same time and well stirred, precipitation starts within 20 seconds, and mud contained in water precipitates within 1 minute,
Within 3 minutes, the water becomes clear like tap water, and when this water is put in a glass container, the scenery on the other side can be seen well through the water.

【実施例6】 0.2リットルの汚濁水中に機械油0.2gを混入攪拌し、
その油の浮いた液面に粉石鹸0.1gを混入して良く攪拌
し、これに生石灰0.4−0.5gと塩化鉄(III)0.2gと投入
して良く攪拌すると1分以内に油も泥も沈殿して油膜も
ない透明な水に浄化される。 上記実施例1乃至6で得られた透明な水に、金魚を入
れると良く泳ぎ生棲することができる。又、完全に不透
明になるまで繁殖した青子又は赤潮の汚濁水1リットル
に上記実施例1乃至6の各配合量の薬品類を混入して良
く攪拌すると2分以内に青子又は赤潮が水底に沈殿して
上水の様に水は透明になる。そこで、これにClO2を1PPM
以上、過マンガン酸カリ1/1000g以上、又は塩化鉄0.2g
以上を添加し、更にこれに適宜の量の石灰又は明礬を加
えたり、塩素等も追加使用して良く攪拌すると青子又は
赤潮は水底に沈殿したまま逐次白色に変わり3日目には
死滅して完全に白色に脱色される。
Example 6 0.2 g of mechanical oil was mixed and stirred in 0.2 liter of polluted water,
Mix 0.1g of powdered soap on the floating surface of the oil and stir well. Add 0.4-0.5g of quick lime and 0.2g of iron (III) chloride to this and stir well to get oil and mud within 1 minute. It precipitates and is purified to clear water with no oil film. When the goldfish is put into the transparent water obtained in Examples 1 to 6, it can swim and live alive. In addition, if 1 liter of polluted water of blue or red tide propagated until it became completely opaque was mixed with the chemicals of the respective compounding amounts of the above Examples 1 to 6 and stirred well, the blue or red tide settled on the bottom of the water within 2 minutes. Then, the water becomes transparent like clean water. So add 1 PPM of ClO 2 to it.
Above, potassium permanganate 1 / 1000g or more, or iron chloride 0.2g
Add the above and further add an appropriate amount of lime or alum, or use chlorine etc. additionally and stir well, and the blue or red tide will gradually turn white while precipitating on the bottom of the water and die on the third day. It is completely decolorized to white.

【発明の効果】【The invention's effect】

本発明においては、上水、下水、屎尿、汚水、濁水、
工業排水、青子又赤潮、食品工場排水、食肉加工場排
水、魚肉加工場排水、畜産排水、生活排水、更に河川工
事、ダム工事、隧道工事、トンネル工事、高圧力水噴射
式切断工事、鑿岩工事、ビル工事、地下道工事等からの
排水又はリサイクル水に、凝集剤として石灰等のカルシ
ウム含有物を使用し、その凝集補助剤として塩化鉄、塩
化アルミニウム、明礬等の化合物を使用し、又はこれら
を適宜組合せて使用することにより、更にこれに適宜の
装置、機械又は浄化槽等と組み合わせて処理を行うと極
めて短時間で汚泥を凝集沈殿させて透明な浄化水を得る
ことができる。
In the present invention, tap water, sewage, human waste, sewage, muddy water,
Industrial wastewater, Aoko or red tide, food factory wastewater, meat processing wastewater, fish processing wastewater, livestock wastewater, domestic wastewater, river construction, dam construction, tunnel construction, tunnel construction, high-pressure water jet cutting construction, chisel rock Use calcium-containing substances such as lime as a coagulant in drainage water or recycled water from construction, building construction, underpass construction, etc., and use compounds such as iron chloride, aluminum chloride, alum, etc. as coagulant aids, or When used in combination with any of the above, the sludge is coagulated and settled in an extremely short time to obtain transparent purified water when the treatment is further combined with an appropriate device, machine or septic tank.

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

第1図は、本発明における薬剤の計量投入装置付きの導
水管を示す図である。 第2図は、本発明における薬剤の計量投入装置付きの導
水管を示す図である。 第3図は、本発明における薬剤の計量投入装置付きの導
水管を示す図である。 第4図は、本発明における汚水浄化兼汚泥回収装置を示
す図である。 第5図は、本発明における回転式分離濾過装置を示す図
である。 1:導水管、2:モーター、3:シャフト、4及び5:スクリュ
ー、6:帯板、7:計量器付投入機、9又は25:攪拌又は噴
射回転式分離濾過装置、11:汚水浄化兼汚泥回収装置、1
2:フィルター、13又は18:水を回転させる装置、14:モー
ター、19:フィルター、22:排泥管、23又は23′:バルブ
又はバタフライ弁
FIG. 1 is a view showing a water conduit with a medicine metering device according to the present invention. FIG. 2 is a diagram showing a water conduit with a medicine metering device according to the present invention. FIG. 3 is a view showing a water conduit with a medicine metering device according to the present invention. FIG. 4 is a diagram showing a wastewater purifying and sludge collecting device according to the present invention. FIG. 5 is a diagram showing a rotary separation / filtration apparatus according to the present invention. 1: Water conduit, 2: Motor, 3: Shaft, 4 and 5: Screw, 6: Strip plate, 7: Charger with metering device, 9 or 25: Agitation or injection rotary separation filtration device, 11: Purification of waste water Sludge collector, 1
2: Filter, 13 or 18: Device for rotating water, 14: Motor, 19: Filter, 22: Mud pipe, 23 or 23 ': Valve or butterfly valve

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】(a) 酸化カルシウム、炭酸カルシウ
ム、水酸化カルシウム、貝化石、甲殻類若しくは貝類の
粉末、サンゴ若しくはサンゴ礁の粉末、魚類動植物類若
しくはプランクトンの死骸、又はCaOを含有する岩石か
ら選ばれた少なくとも1種のカルシウム含有凝集剤と、 (b) 明礬、硫酸アルミニウム、塩化第2鉄、硅酸ナ
トリウム、硫酸鉄(II)若しくは(III)、又はポリ塩
化アルミニウムから選ばれた少なくとも1種の無機系凝
集補助剤、及び/又は、 (c) ポリアクリル酸ナトリウム、ポリアクリルアミ
ドの部分加水分解塩、ポリアクリルアミド、ポリオキシ
エチレン、ポリエチレンイミン、又は第4級アンモニウ
ム塩から選ばれた少なくとも1種の有機系凝集補助剤と
を使用し、 これらを汚濁水中に混入攪拌して凝集反応により汚濁水
中に含まれた泥又は不純物を急速に凝集、沈殿、分離処
理して汚濁水を浄化するに当たって、 前記汚濁水を複数の回転スクリュー又は螺旋状の帯板を
内装した汚濁水用導水管に導入し、前記導水管内の汚濁
水中に前記凝集剤、凝集補助剤、並びに必要に応じて殺
菌剤及び/又は浄化菌を添加して攪拌混合した後に、得
られた混合液を導水管から汚水浄化兼汚泥回収装置、又
は回転水流発生攪拌機若しくは回転水流発生用噴射水導
入管を備えた回転式濾過装置に導入し、この装置内で混
合液を旋回回転させて汚泥及び沈殿不純物を装置下部に
凝集沈殿させ、浄化された水を装置上部に設けられたフ
ィルターを通して取り出し、前記凝集沈殿した汚泥及び
沈殿不純物を装置の底部設置された2個以上のバルブを
備えた排泥取り出し管から取り出すことからなる汚濁水
の浄化処理方法。
1. A selected from (a) calcium oxide, calcium carbonate, calcium hydroxide, shell fossil, crustacean or shellfish powder, coral or coral reef powder, carcasses of fish and animals or plankton, or rocks containing CaO. At least one selected from the group consisting of aluminium, aluminum sulfate, ferric chloride, sodium silicate, iron (II) or (III) sulfate, or polyaluminum chloride. And / or (c) sodium polyacrylate, partially hydrolyzed polyacrylamide salt, polyacrylamide, polyoxyethylene, polyethyleneimine, or quaternary ammonium salt. The organic coagulation auxiliary agent is used, and these are mixed in polluted water and stirred to carry out the coagulation reaction. In purifying the contaminated water by rapidly aggregating, precipitating, and separating the mud or impurities contained in the contaminated water, the contaminated water is introduced into a contaminated water conduit containing a plurality of rotating screws or spiral strips. After introducing and adding the aggregating agent, aggregating aid, and optionally a bactericide and / or purifying bacterium to the contaminated water in the water conduit and stirring and mixing, the resulting mixed liquid is purified from the water conduit to the wastewater. It is also introduced into a sludge recovery device or a rotary filtration device equipped with a rotary water flow generating stirrer or a rotary water flow generating injection water inlet pipe, and the mixed liquid is swirled and rotated in this device to agglomerate sludge and precipitated impurities in the lower part of the device. The precipitated and purified water is taken out through a filter provided on the upper part of the device, and the coagulated and settled sludge and the precipitated impurities are taken out from a sludge removal pipe equipped with two or more valves installed at the bottom of the device. Purification treatment method polluted water consisting of issuing Ri.
【請求項2】汚濁水用の導水管内に複数のスクリューを
備えた回転シャフト又は螺旋状の帯板を内装し、前記導
水管に投入パイプを介して凝集剤等用の計量器付投入機
を設け、この導水管を回転式濾過装置に結合し、前記装
置内の水を回転させるための回転水流発生攪拌機又は回
転水流発生用噴射水導入管をこの装置の導水管取り付け
位置の上方の位置に設け、前記装置の頂部にフィルター
を備えた浄化水の取出管を設け、前記装置の底部に2個
以上のバルブが離れて設置された排泥管を設け、前記投
入機からの凝集剤等が混入された汚濁水を前記導水管を
経て前記装置に供給して装置内で強制的に回転攪拌させ
ることにより、汚泥及び不純物を装置底部に凝集沈殿さ
せ、装置頂部に浄化水を分離する汚濁水の浄化処理装
置。
2. A charging machine equipped with a measuring device for a flocculant or the like, wherein a rotary shaft having a plurality of screws or a spiral strip is installed inside a water guiding pipe for polluted water, and the water guiding pipe is provided with a measuring device for a coagulant or the like via a feeding pipe. Provided, this water pipe is connected to a rotary filtration device, a rotary water flow generating stirrer for rotating the water in the device or a jet flow introducing pipe for rotary water flow generation is located above the water pipe mounting position of this device. A purifying water outlet pipe provided with a filter is provided at the top of the device, and a mud pipe having two or more valves separated from each other is provided at the bottom of the device. Contaminated water that supplies the contaminated contaminated water to the device via the water conduit and forcibly rotates and stirs in the device to cause sludge and impurities to coagulate and settle at the bottom of the device and to separate purified water at the top of the device. Purification equipment.
JP60124920A 1985-06-09 1985-06-09 Water treatment method, treatment agent and treatment equipment Expired - Lifetime JP2512420B2 (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
JP60124920A JP2512420B2 (en) 1985-06-09 1985-06-09 Water treatment method, treatment agent and treatment equipment
CN91102048A CN1065644A (en) 1985-06-09 1991-03-30 Effluent treatment plant
CN91102047A CN1065643A (en) 1985-06-09 1991-03-30 Effluent purification method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60124920A JP2512420B2 (en) 1985-06-09 1985-06-09 Water treatment method, treatment agent and treatment equipment

Publications (2)

Publication Number Publication Date
JPH01310790A JPH01310790A (en) 1989-12-14
JP2512420B2 true JP2512420B2 (en) 1996-07-03

Family

ID=14897406

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60124920A Expired - Lifetime JP2512420B2 (en) 1985-06-09 1985-06-09 Water treatment method, treatment agent and treatment equipment

Country Status (2)

Country Link
JP (1) JP2512420B2 (en)
CN (2) CN1065643A (en)

Families Citing this family (23)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2797234B2 (en) * 1992-12-11 1998-09-17 鎌田バイオ・エンジニアリング株式会社 Flocculant
CN100347098C (en) * 2003-10-30 2007-11-07 同济大学 Aluminium iron chloride of coagulant agent in polymorphism polymerization and preparation method
JP2009050752A (en) * 2007-08-23 2009-03-12 Shoichi Yoshizumi Flocculant
JP5172294B2 (en) * 2007-11-26 2013-03-27 佳和 福井 Muddy water purification device
JP5451323B2 (en) * 2009-11-10 2014-03-26 学校法人早稲田大学 Water treatment method
FR2966819B1 (en) * 2010-10-29 2013-12-27 Orege METHOD AND DEVICE FOR CLARIFYING WATER.
FR2966818B1 (en) * 2010-10-29 2014-02-14 Orege METHOD FOR SEPARATION BETWEEN LIQUID AND SUSPENDED MATERIAL OF A SLURRY AND DEVICE USING SUCH A METHOD
CN101973612B (en) * 2010-11-18 2012-07-18 华东交通大学 Reactive compound multi-functional water treatment agent and preparation method and application method thereof
CN102786167B (en) * 2012-07-17 2014-02-19 临沂大学 Laboratory wastewater treating device
CN104310655A (en) * 2014-11-04 2015-01-28 常熟市浩通水利工程有限公司 Sewage treatment process
JP5975130B1 (en) * 2015-03-04 2016-08-23 栗田工業株式会社 Compound treatment agent for acid gas and heavy metal, and method for treating acid gas and heavy metal
CN104709987B (en) * 2015-03-18 2016-08-24 高彬 A kind of paper-making waste water treating agent and using method thereof
CN104817151A (en) * 2015-05-23 2015-08-05 王杨 Device for accelerating sewage sedimentation
CN105776475A (en) * 2016-04-23 2016-07-20 何淑琼 Compound polysilicate aluminum water purifying agent
CN107174844B (en) * 2017-07-05 2023-03-21 中集车辆(江门市)有限公司 Washing and sweeping vehicle sewage recycling device, working method and washing and sweeping vehicle
CN107540074B (en) * 2017-08-25 2020-07-24 金川集团股份有限公司 Magnesium oxide neutralization system and method for acid wastewater produced by smelting flue gas to produce acid
CN107827218B (en) * 2017-12-08 2020-10-23 江门市崖门新财富环保工业有限公司 Unit type wastewater processor and wastewater processing method thereof
CN108246131A (en) * 2018-01-30 2018-07-06 山东佳星环保科技有限公司 Sewage disposal medicament dissolution agitating device
CN108249505A (en) * 2018-02-07 2018-07-06 中山市绿浪助剂有限公司 Environment-friendly medicament for industrial sewage treatment
CN109824179A (en) * 2019-04-08 2019-05-31 四川博渠科技有限责任公司 A kind of flood season emergency tap water production 3G flocculation precipitation method and its system
CN110642424A (en) * 2019-10-11 2020-01-03 浙江先创能源科技股份有限公司 Sewage treatment method and device
CN111943337A (en) * 2020-08-14 2020-11-17 上海中耀环保实业有限公司 Multistage crystallization precipitation treatment method and system for wastewater desalination
CN113185025A (en) * 2021-04-30 2021-07-30 江苏若焱环境设计有限公司 Method for eliminating black and odorous river channel

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5132504A (en) * 1974-09-09 1976-03-19 Toyo Soda Mfg Co Ltd 1*1*11 torikuroruetannoanteikahoho

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
産業用水調査会編「排水の物理化学的処理」第1版(昭和51年4月15日)産業用水調査会発行第76〜79頁

Also Published As

Publication number Publication date
CN1065644A (en) 1992-10-28
JPH01310790A (en) 1989-12-14
CN1065643A (en) 1992-10-28

Similar Documents

Publication Publication Date Title
JP2512420B2 (en) Water treatment method, treatment agent and treatment equipment
JP3467492B2 (en) How to purify sewage
CA1257411A (en) Apparatus for the clarification of sewage and other wastes
JP2007209886A (en) Fluorine removing agent, and method and apparatus for treating drain containing fluorine using the agent
CN106517591A (en) Reverse osmosis concentration treatment system and method
CN203922907U (en) The external dephosphorization algae removal of a kind of landscape water body purifying processing device
JP2009072769A (en) Sewage treatment system
CN207121501U (en) A kind of hardness removing device suitable for the hard waste water of high magnesium
CN103011462A (en) Device and method for treating waste residues of circulating make-up water by reutilizing lime softening method of power plant
CN101209884A (en) Method and device for comprehensive processing zero discharge and recovering commonly industrial wastewater
KR100247126B1 (en) Solid flocculant and high speed flocculation separator
JP2009056346A (en) Polluted muddy water treatment system
JPH1177094A (en) Apparatus and method for purifying treatment of dredged soil
JPH10499A (en) Method for improving dredged solid-liquid separation soil
JP2002079004A (en) Aggregation method
JPH05220500A (en) Treatment of bag-type dehydration of sludge
JPH10156391A (en) Treatment of phosphorus recovered from treated water of sewerage
JPH07108395B2 (en) Turbid water treatment method and treatment device
CN217578545U (en) High ammonia nitrogen wastewater treatment system
JPH0938414A (en) Flocculating precipitant
CN107399857A (en) A kind of circulating treating system applied to Industrial Wastewater Treatment
CN208378671U (en) Domestic sewage processing system
El Diwani et al. Bitterns as coagulants for treatment of municipal wastewater
KR100480807B1 (en) Calcium hydroxide feeding apparatus having filter, the calcium hydroxide feeding methods using the same and the water purifying methods thereof
JPH07100155B2 (en) Organic wastewater treatment method