JPH08117738A - Method for purifying raw water for city water - Google Patents

Method for purifying raw water for city water

Info

Publication number
JPH08117738A
JPH08117738A JP6282963A JP28296394A JPH08117738A JP H08117738 A JPH08117738 A JP H08117738A JP 6282963 A JP6282963 A JP 6282963A JP 28296394 A JP28296394 A JP 28296394A JP H08117738 A JPH08117738 A JP H08117738A
Authority
JP
Japan
Prior art keywords
basin
water
chlorine
added
pond
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP6282963A
Other languages
Japanese (ja)
Other versions
JP3232429B2 (en
Inventor
Sumio Akiyama
澄夫 秋山
Naoya Ozawa
直哉 小沢
Hiroshi Takahashi
浩 高橋
Yukio Otsubo
幸夫 大坪
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.)
NIPPON HEALTH KOGYO KK
Original Assignee
NIPPON HEALTH KOGYO KK
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 NIPPON HEALTH KOGYO KK filed Critical NIPPON HEALTH KOGYO KK
Priority to JP28296394A priority Critical patent/JP3232429B2/en
Publication of JPH08117738A publication Critical patent/JPH08117738A/en
Application granted granted Critical
Publication of JP3232429B2 publication Critical patent/JP3232429B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Water Treatment By Sorption (AREA)
  • Separation Of Suspended Particles By Flocculating Agents (AREA)
  • Filtration Of Liquid (AREA)

Abstract

PURPOSE: To purify taken-in raw water at low costs, to reduce the consumption of chlorine, and to control the generation of trihalogenomethane. CONSTITUTION: Raw water from an intake is led to a sedimentation basin 3 while being added with acid clay. The water is then added with chlorine and alkali and sent to an admixture basin 4, where polyaluminum chloride is added to the water and the mixture is stirred at a high speed. Next, the water is stirred slowly in a flock forming basin 5, and thereafter, in a chemical precipitation basin 6, a grown-up flock is precipitated and removed. Next, the water is added with chlorine and led to a rapid filtration basin 7, where residual suspended substances are filtered out by a sand layer. Finally, the water, after passing through an activated carbon adsorption tank 9, is added with chlorine and alkali and stored in a water purification basin 10.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は水道水用原水の浄化方法
に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for purifying raw water for tap water.

【0002】[0002]

【従来の技術】降水量は毎年異なるが、降水量が少ない
と河川の水量が激減する。そしてその場合には水の汚濁
が甚だしくなり、濁度と臭気がきわめて悪化する。その
ため浄水場において水道水用原水を浄化するときに、活
性炭、ポリ塩化アルミニウム(PAC)、塩素等の薬剤
を多量に必要とする。
2. Description of the Related Art The amount of rainfall varies every year, but if the amount of rainfall is low, the amount of water in the river will drastically decrease. And in that case, the water becomes extremely polluted, and the turbidity and the odor are extremely deteriorated. Therefore, a large amount of chemicals such as activated carbon, polyaluminum chloride (PAC), and chlorine is required when the raw water for tap water is purified in a water purification plant.

【0003】そして、これらの薬剤を多量に用いれば費
用が嵩み、また塩素を多量に用いるとその分発癌性物質
であるトリハロメタンの発生量も多くなる。
The use of a large amount of these agents increases the cost, and the use of a large amount of chlorine also increases the amount of trihalomethane which is a carcinogenic substance.

【0004】[0004]

【発明が解決しようとする課題】而して、従来の浄水場
における水道水用原水の浄化方法は、取水口からとり入
れた原水を沈砂池に導き、該沈砂池において活性炭粉末
を加えつつ原水中の砂等の固形物を沈澱させて除去し、
次に所要量の塩素とアルカリを加えた後混和池に導き、
該混和池においてポリ塩化アルミニウムを加えて急速攪
拌し、次にフロック形成池に導き、該フロック形成池に
おいて浮遊物がポリ塩化アルミニウムによって大きな粒
子に成長するよう緩速攪拌し、次に薬品沈澱池に導き、
該薬品沈澱池において大きく成長したフロックを沈澱さ
せて除去し、次に所要量の塩素を加えた後急速濾過池に
導き、該急速濾過池において前記薬品沈澱池で除去する
ことができない浮遊物を砂層を通して除去し、最後に活
性炭吸着槽を通し、所要量の塩素とアルカリを加えた後
浄水池に貯留するようにするものである。
Thus, the conventional method for purifying raw water for tap water in a water purification plant is to introduce raw water taken from an intake into a sand basin, and add activated carbon powder to the sand basin while the raw water is added. To remove solids such as sand by sedimentation,
Next, add the required amount of chlorine and alkali, then lead to the mixing pond,
In the mixing pond, polyaluminum chloride was added and rapidly stirred, then led to a floc formation pond, and slowly stirred in the floc formation pond so that the suspended solids grow into large particles by the polyaluminum chloride, and then the chemical precipitation pond. Lead to
Flocs that have grown greatly in the chemical sedimentation basin are precipitated and removed, and then the required amount of chlorine is added and then introduced into a rapid filtration basin to remove suspended matter that cannot be removed in the chemical sedimentation basin in the rapid filtration basin. The sand is removed through the sand layer, and finally it is passed through an activated carbon adsorption tank, and after the required amounts of chlorine and alkali have been added, it is stored in a water purification pond.

【0005】本発明は斯かる従来の浄化方法における前
記問題点を解消すべくなされたものであり、安い費用で
もって水道水用原水を浄化し且つ塩素を減らしてトリハ
ロメタンの発生量を抑制することができるようになした
浄化方法を提供せんとするものである。
The present invention has been made to solve the above-mentioned problems in the conventional purification method, and to purify raw water for tap water and reduce chlorine to suppress the amount of trihalomethane generated at a low cost. It is intended to provide a purification method that has made it possible.

【0006】[0006]

【課題を解決するための手段】本発明は上記目的を達成
すべく、前記従来の浄化方法における沈砂池で加える活
性炭粉末を酸性白土に代えるものである。
In order to achieve the above object, the present invention is to replace the activated carbon powder added in the sand basin in the conventional purification method with acid clay.

【0007】即ち、本発明は、取水口からとり入れた原
水を沈砂池に導き、該沈砂池において酸性白土を加えつ
つ原水中の砂等の固形物を沈澱させて除去し、次に所要
量の塩素とアルカリを加えた後混和池に導き、該混和池
においてポリ塩化アルミニウムを加えて急速攪拌し、次
にフロック形成池に導き、該フロック形成池において浮
遊物がポリ塩化アルミニウムによって大きな粒子に成長
するよう緩速攪拌し、次に薬品沈澱池に導き、該薬品沈
澱池において大きく成長したフロックを沈澱させて除去
し、次に所要量の塩素を加えた後急速濾過池に導き、該
急速濾過池において前記薬品沈澱池で除去することがで
きない浮遊物を砂層を通して除去し、最後に活性炭吸着
槽を通し、所要量の塩素とアルカリを加えた後浄水池に
貯留するようになした水道水用原水の浄化方法である。
That is, according to the present invention, the raw water taken in from the intake is guided to a sand basin, and in the sand basin, solid matter such as sand in the raw water is removed by precipitating and removing the solid matter while adding acid clay. After adding chlorine and alkali, lead to a mixing pond, add polyaluminum chloride in the mixing pond and rapidly stir, then lead to a floc formation pond, and in the floc formation pond, suspended solids grow into large particles by polyaluminum chloride The mixture is gently stirred so that it can be introduced into a chemical settling basin, and flocs that have grown significantly in the chemical settling basin can be precipitated and removed, and then the required amount of chlorine can be added, followed by introduction into a rapid filtration basin and the rapid filtration. In the pond, suspended solids that cannot be removed in the chemical sedimentation pond are removed through the sand layer, and finally through the activated carbon adsorption tank, after adding the required amount of chlorine and alkali, they are stored in the clean water pond. It was a method of purifying raw water for tap water.

【0008】また、用いる酸性白土は、モンモリロナイ
ト(montmorillonite)を主構成分とする粘土で、天然に
酸性環境下で活性化されて吸着性を有するものである。
そしてその成分は、SiO2、Al2O3 、Fe2O3 、CaO 、MgO
、Na2O+K2O 、Ig.Loss 等からなるものである。
The acid clay used is a clay whose main constituent is montmorillonite, which is naturally activated in an acidic environment and has adsorptivity.
And its components are SiO 2 , Al 2 O 3 , Fe 2 O 3 , CaO, MgO.
, Na 2 O + K 2 O, Ig.Loss, etc.

【0009】[0009]

【実施例】以下、本発明の実施例について図面を参照し
つつ説明する。図中、1は取水口、2は取水ポンプ棟、
3は沈砂池である。4は混和池、5はフロック形成池、
6は薬品沈澱池、7は急速濾過池、8は中間ポンプ棟、
9は活性炭吸着槽、10は浄水池である。また、その他
11は排泥排水池、12は濃縮槽、13は加圧脱水機で
ある。
Embodiments of the present invention will be described below with reference to the drawings. In the figure, 1 is the intake, 2 is the intake pump building,
3 is a sand basin. 4 is a mixing pond, 5 is a floc formation pond,
6 is a chemical sedimentation tank, 7 is a rapid filtration tank, 8 is an intermediate pump building,
9 is an activated carbon adsorption tank, and 10 is a water purification pond. In addition, 11 is a sludge drainage basin, 12 is a concentration tank, and 13 is a pressure dehydrator.

【0010】そして、本実施例による具体的な処理は次
の通りに行う。取水口1からとり入れた原水を先ず沈砂
池3に導く。そして該沈砂池3において酸性白土を加え
つつ原水中の砂等の固形物を沈澱させて除去する。次
に、所要量の塩素とアルカリを加えた後混和池4に導
き、該混和池4において凝集剤であるポリ塩化アルミニ
ウム(PAC)を加えて急速攪拌する。
The specific processing according to this embodiment is performed as follows. The raw water taken in from the intake 1 is first led to the sand basin 3. Then, in the settling basin 3, solid matter such as sand in the raw water is precipitated and removed while adding acid clay. Next, after adding required amounts of chlorine and alkali to the mixing tank 4, polyaluminum chloride (PAC) as a coagulant is added to the mixing tank 4 and rapidly stirred.

【0011】次に、フロック形成池5に導き、該フロッ
ク形成池5において浮遊物がポリ塩化アルミニウムによ
って大きな粒子に成長するよう緩速攪拌する。次に、薬
品沈澱池6に導き、該薬品沈澱池6において大きく成長
したフロックを沈澱させて除去する。
Next, it is led to the floc formation pond 5 and is slowly stirred in the floc formation pond 5 so that the suspended matter grows into large particles due to polyaluminum chloride. Next, it is guided to the chemical sedimentation pond 6, and the flocs that have grown greatly in the chemical sedimentation pond 6 are precipitated and removed.

【0012】次に、所要量の塩素を加えた後急速濾過池
7に導き、該急速濾過池7において前記薬品沈澱池6で
除去することができない浮遊物を砂層を通して除去す
る。
Next, after adding a required amount of chlorine, it is led to the rapid filtration basin 7, and in the rapid filtration basin 7, suspended matter that cannot be removed by the chemical precipitation basin 6 is removed through the sand layer.

【0013】そして最後に活性炭吸着槽9を通した後、
所要量の塩素とアルカリを加え、浄水池10に貯留する
ものである。
Finally, after passing through the activated carbon adsorption tank 9,
The required amounts of chlorine and alkali are added and stored in the water purification pond 10.

【0014】[0014]

【発明の効果】本発明は取水口からとり入れた原水を最
初に処理する沈砂池において酸性白土を加えるものであ
るから、処理する初期の段階で酸性白土の吸着作用によ
り、大半の固形物や浮遊物を吸着、除去してしまうこと
ができるものである。したがって、その後の処理工程に
おいて従来方法の如き多量の薬剤を用いなくても済む。
且つまた酸性白土は安価であるから、処理に要する費用
が従来方法よりもはるかに少なくて済むものである。
EFFECTS OF THE INVENTION Since the present invention is to add acid clay in a sand basin that first treats raw water taken in from the intake, most solids and suspended solids are suspended due to the adsorption action of acid clay in the initial stage of treatment. It can absorb and remove things. Therefore, it is not necessary to use a large amount of chemicals in the subsequent processing steps as in the conventional method.
Moreover, since the acid clay is inexpensive, the cost required for the treatment is much lower than that of the conventional method.

【0015】そしてまた、酸性白土には前記の通りアル
ミナも多量に含まれているから、凝集剤としてのポリ塩
化アルミニウムの量も従来の半分以下に減らすことがで
きるものである。
Further, since the acid clay contains a large amount of alumina as described above, the amount of polyaluminum chloride as a coagulant can be reduced to less than half of the conventional amount.

【0016】そしてまた、後処理工程においては前記の
通り原水中の固形物や浮遊物が少なくなり、且つまた酸
性白土にはマグネシウムも含まれている等のことから、
塩素の使用量も減らすことができる。そしてこのように
塩素の使用量を減らすことができるから、その分トリハ
ロメタンの発生量も少なく抑えることができるものであ
る。
Further, in the post-treatment step, as described above, the amount of solids and suspended matter in the raw water is reduced, and the acid clay also contains magnesium.
The amount of chlorine used can also be reduced. Since the amount of chlorine used can be reduced in this way, the amount of trihalomethane generated can be reduced to that extent.

【0017】以下に本発明の効果を明確にすべく試験例
を挙げる。20lポリ容器で送付されてきた取水・原水
(冷蔵庫保管)を室温に戻して、ポリ容器をよく振り、
一旦、3lのビーカーに移し、それを攪拌棒でよくかき
混ぜ500mlのトールビーカーにそれぞれ採取した。
各トールビーカーに粉末活性炭及び酸性白土をそれぞれ
に適量添加し、5分間マグネット・スターラで攪拌し、
その後それぞれにPACを適量添加して緩速攪拌を5分
間行い静置した。その後、4%NaOHを添加してpH
を7.0付近に調整して30分間静置した。その上澄液
を採取してTOC、臭気、濁度を測定した。
Test examples will be given below to clarify the effect of the present invention. Return the water intake / raw water (refrigerator storage) sent in a 20-liter plastic container to room temperature, shake the plastic container well,
Once transferred to a 3 liter beaker, it was well mixed with a stir bar and collected in a 500 ml tall beaker.
Powdered activated carbon and acid clay were added to each tall beaker in appropriate amounts and stirred for 5 minutes with a magnetic stirrer,
Thereafter, an appropriate amount of PAC was added to each of them, and the mixture was slowly stirred for 5 minutes and allowed to stand. Then add 4% NaOH and adjust the pH
Was adjusted to around 7.0 and allowed to stand for 30 minutes. The supernatant was collected and measured for TOC, odor and turbidity.

【0018】分析及び測定方法は次の通りである。 pH : 上水試験方法 8.3ガラス電極法 (堀
場 F−8 使用) TOC: 上水試験方法 72.3燃焼酸化法 (島
津 TOC-500 使用) SS : 上水試験方法 25.2濾過法 濁度 : 上水試験方法 3.3.1透過光測定法 臭気 : 上水試験方法 6.3臭気強度
The analysis and measurement methods are as follows. pH: Water supply test method 8.3 Glass electrode method (Horiba F-8 used) TOC: Water supply test method 72.3 Combustion oxidation method (Shimadzu TOC-500 used) SS: Water supply test method 25.2 Filtration method Turbid Degree: Clean water test method 3.3.1 Transmitted light measurement method Odor: Clean water test method 6.3 Odor intensity

【0019】また、取水原水は次の表のおおりである。Further, the raw water intake is the following table.

【0020】[0020]

【表1】 [Table 1]

【0021】尚、表1において*1:TOC は濾過後の測
定値、*2:臭気の強度を示す。
In Table 1, * 1: TOC is a measured value after filtration, and * 2: odor intensity.

【0022】そして、試験結果は次の通りである。The test results are as follows.

【0023】[0023]

【表2】 [Table 2]

【0024】尚、表2においてR-0 は取水原水、R-1 は
従来方法による結果、R-2 〜R-5 は本発明による結果で
ある。また、環境庁による6段階臭気強度表示は次の通
りである。
In Table 2, R-0 is the raw water intake, R-1 is the result of the conventional method, and R-2 to R-5 are the results of the present invention. The 6-level odor intensity display by the Environment Agency is as follows.

【0025】[0025]

【表3】 [Table 3]

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

【図1】本発明の一実施例の説明図である。FIG. 1 is an explanatory diagram of an embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1 取水口 3 沈砂池 4 混和池 5 フロック形成池 6 薬品沈澱池 7 急速濾過池 9 活性炭吸着槽 10 浄水池 1 Water intake 3 Settling basin 4 Mixing basin 5 Floc formation basin 6 Chemical sedimentation basin 7 Rapid filtration basin 9 Activated carbon adsorption tank 10 Purification basin

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 取水口からとり入れた原水を沈砂池に導
き、該沈砂池において酸性白土を加えつつ原水中の砂等
の固形物を沈澱させて除去し、次に所要量の塩素とアル
カリを加えた後混和池に導き、該混和池においてポリ塩
化アルミニウムを加えて急速攪拌し、次にフロック形成
池に導き、該フロック形成池において浮遊物がポリ塩化
アルミニウムによって大きな粒子に成長するよう緩速攪
拌し、次に薬品沈澱池に導き、該薬品沈澱池において大
きく成長したフロックを沈澱させて除去し、次に所要量
の塩素を加えた後急速濾過池に導き、該急速濾過池にお
いて前記薬品沈澱池で除去することができない浮遊物を
砂層を通して除去し、最後に活性炭吸着槽を通し、所要
量の塩素とアルカリを加えた後浄水池に貯留するように
なした水道水用原水の浄化方法。
1. The raw water taken in from the intake is led to a sand basin, and in the sand basin, solid matter such as sand in the raw water is removed by precipitation while adding acid clay, and then required amounts of chlorine and alkali are removed. After the addition, the mixture is introduced into a mixing pond, polyaluminum chloride is added in the mixing pond and rapidly stirred, and then the mixture is introduced into a floc formation pond, and slowly suspended in the floc formation pond to grow into large particles by the polyaluminum chloride. The mixture is stirred and then introduced into a chemical sedimentation basin, flocs that have grown greatly in the chemical sedimentation basin are precipitated and removed, and then the required amount of chlorine is added, followed by introduction into a rapid filtration basin, in which the chemical Raw water for tap water, which was stored in a clean water pond after removing suspended solids that cannot be removed in a sedimentation pond through a sand layer and finally through an activated carbon adsorption tank and adding the required amount of chlorine and alkali Purification method.
JP28296394A 1994-10-21 1994-10-21 How to purify raw water for tap water Expired - Fee Related JP3232429B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP28296394A JP3232429B2 (en) 1994-10-21 1994-10-21 How to purify raw water for tap water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP28296394A JP3232429B2 (en) 1994-10-21 1994-10-21 How to purify raw water for tap water

Publications (2)

Publication Number Publication Date
JPH08117738A true JPH08117738A (en) 1996-05-14
JP3232429B2 JP3232429B2 (en) 2001-11-26

Family

ID=17659407

Family Applications (1)

Application Number Title Priority Date Filing Date
JP28296394A Expired - Fee Related JP3232429B2 (en) 1994-10-21 1994-10-21 How to purify raw water for tap water

Country Status (1)

Country Link
JP (1) JP3232429B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012232279A (en) * 2011-05-09 2012-11-29 Tokyo Metropolitan Government Method for reusing used granular activated charcoal and purified water treating facilities
CN112939169A (en) * 2021-02-02 2021-06-11 大唐环境产业集团股份有限公司 System and method for treating high-suspended matter mine water by coal gangue sand medium

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012232279A (en) * 2011-05-09 2012-11-29 Tokyo Metropolitan Government Method for reusing used granular activated charcoal and purified water treating facilities
CN112939169A (en) * 2021-02-02 2021-06-11 大唐环境产业集团股份有限公司 System and method for treating high-suspended matter mine water by coal gangue sand medium

Also Published As

Publication number Publication date
JP3232429B2 (en) 2001-11-26

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