JPH07136664A - Dephosphorization of waste water - Google Patents
Dephosphorization of waste waterInfo
- Publication number
- JPH07136664A JPH07136664A JP30857293A JP30857293A JPH07136664A JP H07136664 A JPH07136664 A JP H07136664A JP 30857293 A JP30857293 A JP 30857293A JP 30857293 A JP30857293 A JP 30857293A JP H07136664 A JPH07136664 A JP H07136664A
- Authority
- JP
- Japan
- Prior art keywords
- aeration tank
- tank
- dephosphorizing
- agent
- solidified
- 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.)
- Pending
Links
Landscapes
- Removal Of Specific Substances (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は排水処理における排水の
脱リン方法に関し、特に脱リン用薬剤の注入方法に関す
る。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for dephosphorizing wastewater in wastewater treatment, and more particularly to a method for injecting a dephosphorizing agent.
【0002】[0002]
【従来の技術】従来、排水中のリン除去には、生物学的
脱リン法、凝集剤添加法、吸着法、晶析脱リン法等が用
いられてきた。しかし、生物学的脱リン法、凝集剤添加
法、吸着法、晶析脱リン法等は、いずれも排水に負荷変
動があった場合、制御が難しく、頻繁な維持管理が必要
であるという問題点があった。2. Description of the Related Art Conventionally, a biological dephosphorization method, a coagulant addition method, an adsorption method, a crystallization dephosphorization method and the like have been used for removing phosphorus in waste water. However, the biological dephosphorization method, the coagulant addition method, the adsorption method, the crystallization dephosphorization method, etc. are all difficult to control when there is a load fluctuation in the wastewater, and frequent maintenance is required. There was a point.
【0003】また、嫌気ろ床槽、ばっ気槽、沈澱槽、汚
泥貯留タンクなどに鉄板、鋼製丸棒などを浸漬しておく
方法がある。この方法は、鉄板等の鉄分を溶解させ、排
水中のリンを鉄化合物として不溶性化し、リンを汚泥の
中に取り込み除去するものである。従って、リン除去の
ために金属塩などの薬品をその都度汚水量に比例して注
入するなどの面倒な経費がかからず、単に鉄材や鋼材を
液中に浸漬しておくだけという優れた方法である。There is also a method of immersing an iron plate, a steel round bar or the like in an anaerobic filter bed tank, an aeration tank, a settling tank, a sludge storage tank or the like. In this method, iron in a steel plate or the like is dissolved, phosphorus in waste water is made insoluble as an iron compound, and phosphorus is taken into sludge and removed. Therefore, it is an excellent method of simply immersing iron material or steel material in the liquid without incurring the troublesome expense of injecting chemicals such as metal salts in proportion to the amount of wastewater each time to remove phosphorus. Is.
【0004】[0004]
【発明が解決しようとする課題】鉄板を浸漬させる脱リ
ン方法は、維持管理が容易で経済的に安価である優れた
方法である一面、鉄分が液中に溶解する量を水量負荷に
応じて調整することが難しいという問題点があった。ま
た、鉄分の溶解速度が遅く、鉄板の比表面積が小さいた
め鉄板を相当量設置しなくてはならなかった。さらに、
鉄板浸漬後の処理日数の経過とともに、鉄板表面積に防
食性被膜がスライム状に生成し、鉄イオンの溶出が漸滅
し、リン除去率が経日的に低下する問題点があった。The dephosphorization method of immersing an iron plate is an excellent method that is easy to maintain and economically inexpensive. On the other hand, the amount of iron dissolved in the liquid depends on the water load. There was a problem that it was difficult to adjust. Further, since the dissolution rate of iron content is slow and the specific surface area of the iron plate is small, it is necessary to install a considerable amount of the iron plate. further,
There was a problem that as the number of days of treatment after immersion of the iron plate increased, a corrosion-resistant coating was formed in a slime shape on the surface area of the iron plate, the elution of iron ions gradually diminished, and the phosphorus removal rate decreased daily.
【0005】本発明は、維持管理が容易で経済的に安価
であるだけでなく、脱リン用薬剤を一定速度で必要量排
水中に添加し排水中のリンを除去する方法を提供するこ
とを目的とする。The present invention not only provides easy maintenance and economically inexpensive, but also provides a method for removing phosphorus in wastewater by adding a dephosphorizing agent to wastewater in a required amount at a constant rate. To aim.
【0006】[0006]
【課題を解決するための手段】上記目的を達成するため
に、本発明に係わる方法は、鉄板を浸漬する代りに固形
化薬剤を浸漬することとした。維持管理が容易で、経済
的に安価な方法である利点を利用したのである。しか
し、維持管理が容易で、経済的に安価であるだけでな
く、固形化薬剤が一定速度で排水中に溶解し、一定量の
薬剤が排水中に添加されなければならない。そこで、脱
リン用薬剤を溶解性結合剤により固形化することによ
り、固形化薬剤とし、排水中に単に漬けるだけで脱リン
を効率よく行えるようにした。固形化薬剤の脱リン用薬
剤は、砂鉄、繊維状鉄、石灰、アルミニウム粉末、繊維
状アルミニウム、アルミニウム箔、塩化第二鉄溶液、硫
酸アルミニウム溶液のうち、いずれか一つまたは二以上
組合せたものである。脱リン用薬剤は、溶解すると被処
理水中のリンと結合し難溶性となる。脱リン用薬剤を固
形化する溶解性結合剤は脂肪酸エステル等を配合したも
のである。この場合、脱リン用薬剤は固形化薬剤の全体
積に均等に分布するようにするが、好ましくは、固体の
中央付近は薬剤の濃度を大にする。固形化薬剤が溶解す
るに従って、排水との維持面積が小さくなるからであ
る。このような接触面積の変化の対策として、一つの保
持ネツトに数個の固形化薬剤を入れ一定時間ごとに一個
づつ取替えると、表面積が多いものと少ないものとの合
計は、一定に近くなる。In order to achieve the above object, the method according to the present invention is to immerse a solidifying agent instead of immersing an iron plate. They took advantage of the fact that they were easy to maintain and economically cheap. However, in addition to being easy to maintain and economically inexpensive, the solidifying agent must dissolve in the wastewater at a constant rate and a certain amount of the agent must be added to the wastewater. Therefore, by solidifying the dephosphorizing agent with a soluble binder, the dephosphorizing agent can be effectively solidified by simply immersing it in the waste water. The dephosphorization agent of the solidifying agent is any one or a combination of sand iron, fibrous iron, lime, aluminum powder, fibrous aluminum, aluminum foil, ferric chloride solution, and aluminum sulfate solution. Is. When dissolved, the dephosphorizing agent binds to phosphorus in the water to be treated and becomes insoluble. The soluble binder for solidifying the dephosphorization agent is a mixture of fatty acid ester and the like. In this case, the dephosphorization drug is evenly distributed in the entire volume of the solidified drug, but preferably the concentration of the drug is increased near the center of the solid. This is because the area for maintaining the drainage becomes smaller as the solidifying agent dissolves. As a countermeasure against such a change in the contact area, if several solidifying agents are put in one holding net and replaced one by one at regular time intervals, the sum of the one having a large surface area and the one having a small surface area becomes close to a constant value.
【0007】固形化薬剤の溶解速度は、溶解性結合剤の
種類と性状によって調整される。この固形化薬剤をばっ
気槽に設置し、被処理水に溶解させることにより、適正
量の薬剤の添加を行える。被処理水に前記添加方法によ
り脱リン用薬剤を添加することにより本発明の目的とす
る脱リン方法が達成できる。また、固形化薬剤の設置場
所は次のいずれでも良い。The dissolution rate of the solidified drug is controlled by the type and properties of the soluble binder. By installing this solidifying agent in the aeration tank and dissolving it in the water to be treated, an appropriate amount of the agent can be added. The dephosphorization method aimed at by the present invention can be achieved by adding the dephosphorization agent to the water to be treated by the above-mentioned addition method. Further, the installation location of the solidifying agent may be any of the following.
【0008】汚水の移送経路である嫌気ろ床槽流入配
管、嫌気ろ床槽から接触ばっ気槽への移送配管、ばっ気
槽から沈澱槽への移送配管及び沈澱槽から3次処理装置
への移送配管のいずれか一つまたは二以上の場所。[0008] The anaerobic filter bed inflow pipe, which is the transfer route of sewage, the transfer pipe from the anaerobic filter bed to the contact aeration tank, the transfer pipe from the aeration tank to the settling tank, and the settling tank to the tertiary treatment device Any one or more of the transfer pipes.
【0009】循環水の移送経路である接触ばっ気槽か
ら嫌気ろ床槽への循環配管、沈澱槽からばっ気槽への循
環配管及び3次処理装置からばっ気槽への循環配管のい
ずれか一つの場所Any of a circulation pipe from a contact aeration tank to an anaerobic filter tank, which is a transfer route of circulating water, a circulation pipe from a precipitation tank to an aeration tank, and a circulation pipe from a tertiary treatment device to an aeration tank. One place
【0010】嫌気ろ床槽、沈澱槽及び汚泥貯留槽のい
ずれか一つまたは二以上の場所。Any one or more of an anaerobic filter bed tank, a sedimentation tank, and a sludge storage tank.
【0011】[0011]
【作用】本発明に係る排水の脱リン方法は、脱リン用薬
剤を溶解性結合剤により固形化して固形化薬剤とし、該
固形化薬剤を排水中に浸漬して、脱リン用薬剤の添加を
行うことに特徴がある。このように固形化薬剤を使用す
ることにしたのは、脱リン用薬剤は通常、固体状または
液体状であり、定量的に添加するのは難しいからであ
る。脱リン用薬剤を溶解性結合剤で固形化し、溶解性結
合剤の性状を調整することにより、溶解量の制御が容易
になる。その結果、適正な薬剤量を添加できるようにな
る。溶解性結合剤により固形化された脱リン用薬剤は、
溶解性結合剤の溶解とともに、例えば、ばっ気槽に添加
される。添加された脱リン用薬剤は、ばっ気槽中でリン
酸イオンと反応し、難溶性の塩を生成する。難溶性の塩
は、ばっ気槽中で汚泥にとりこまれるか、次段の固液分
離装置で除去されるかして、被処理水中より取り除かれ
る。したがって、被処理水中のリンが除去される。溶解
性結合剤の種類は、性状は、薬剤の種類、性状、溶解の
形態、必要とされる溶解速度で選定される。The method for dephosphorizing wastewater according to the present invention comprises solidifying a dephosphorizing agent with a soluble binder to form a solidifying agent, immersing the solidifying agent in the wastewater, and adding the dephosphorizing agent. It is characterized by doing. The reason why the solidified drug is used in this way is that the dephosphorization drug is usually in a solid or liquid form and it is difficult to quantitatively add it. By solidifying the dephosphorizing agent with a soluble binder and adjusting the properties of the soluble binder, the amount of dissolution can be easily controlled. As a result, an appropriate amount of drug can be added. The dephosphorization agent solidified by the soluble binder is
Along with the dissolution of the soluble binder, for example, it is added to the aeration tank. The added dephosphorizing agent reacts with phosphate ions in the aeration tank to form a sparingly soluble salt. The sparingly soluble salt is removed from the water to be treated by being incorporated into sludge in the aeration tank or removed by the solid-liquid separation device in the next stage. Therefore, phosphorus in the water to be treated is removed. The type of the soluble binder is selected according to the type of the drug, the properties, the form of dissolution, and the required dissolution rate.
【0012】[0012]
【実施例】本発明に係る実施例について図1、図2に基
づいて説明する。Embodiments of the present invention will be described with reference to FIGS.
【0013】図1は、固形化薬剤をばっ気槽に設置した
概念縦断面図である。ばっ気槽4には、固形化薬剤1が
保持ネット6で設置されている。保持ネット6は、フツ
ク10より吊り下げる。該フツク10は、ばっ気槽4の
内面側壁であって、ばっ気槽内部液7の液面より上方に
取付けられる。ばっ気槽4の外部に設けられた送風機8
よりばっ気用空気を供給する散気管9をばっ気槽4内に
設置する。ばっ気槽内部液7は、ばっ気槽4内で一定の
液面を保持している。FIG. 1 is a conceptual vertical sectional view in which a solidified drug is installed in an aeration tank. The solidified chemical 1 is installed in the aeration tank 4 with a holding net 6. The holding net 6 is hung from the hook 10. The hook 10 is attached to the inner side wall of the aeration tank 4 and above the liquid level of the liquid 7 inside the aeration tank. Blower 8 provided outside the aeration tank 4
An air diffuser 9 for supplying more aeration air is installed in the aeration tank 4. The liquid 7 inside the aeration tank maintains a constant liquid level in the aeration tank 4.
【0014】図2は、固形化薬剤1の部分切断された斜
視図である。この実施例では、固形化薬剤1は、脱リン
用薬剤2が溶解性結合剤3で直径5cm・厚さ3cmの
寸法に固形化された構造となっている。FIG. 2 is a partially cut perspective view of the solidified drug 1. In this embodiment, the solidified drug 1 has a structure in which the dephosphorization drug 2 is solidified with a soluble binder 3 to have a diameter of 5 cm and a thickness of 3 cm.
【0015】図1の実施例において、脱リン用薬剤2は
繊維状鉄を用い、溶解性結合剤3は脂肪酸エステル等を
配合したものを用いた。固形化薬剤1を設置したばっ気
槽4に、外部に設置された送風気8によって空気を散気
管9から供給すると、ばっ気槽内部液7はばっ気撹拌さ
れる。ばっ気槽内部液7の流れ(図1で矢印で示す)に
より固形化薬剤1は徐々に溶解し、脱リン用薬剤がばっ
気槽内部液7に供給される。脱リン用薬剤は一定速度で
溶解され、ばっ気槽4中でリン酸イオンと反応し、難溶
性の塩を生成した。難溶性塩は、ばっ気槽中で汚泥にと
りかこまれ、ばっ気槽内部液7から除去された。脱リン
用薬剤として、繊維状鉄の他に、砂鉄、石灰、アルミニ
ウム粉末、繊維状アルミニウム、アルミニウム箔、塩化
第二鉄溶液及び硫酸アルミニウム溶液を用いたが、同様
な結果を得た。In the embodiment shown in FIG. 1, the dephosphorizing agent 2 was fibrous iron, and the soluble binder 3 was a mixture of fatty acid ester and the like. When air is supplied from the diffuser pipe 9 to the aeration tank 4 in which the solidification agent 1 is installed by the air blower 8 installed outside, the aeration tank internal liquid 7 is agitated. The solidified drug 1 is gradually dissolved by the flow of the aeration tank internal liquid 7 (indicated by an arrow in FIG. 1), and the dephosphorization drug is supplied to the aeration tank internal liquid 7. The dephosphorization agent was dissolved at a constant rate and reacted with phosphate ions in the aeration tank 4 to form a sparingly soluble salt. The sparingly soluble salt was contained in the sludge in the aeration tank and was removed from the liquid 7 inside the aeration tank. As the dephosphorizing agent, sand iron, lime, aluminum powder, fibrous aluminum, aluminum foil, ferric chloride solution and aluminum sulfate solution were used in addition to fibrous iron, but similar results were obtained.
【0016】[0016]
【発明の効果】本発明は以上説明したように構成されて
いるので、以下に記載されるような効果を奏する。 (1)脱リン用薬剤を一定速度で、一定量排水中に添加
できる。 (2)脱リン用薬剤の排水中への添加が安定しているた
め、排水中の脱リンが安定して、効率よく行える。 (3)脱リン用薬剤の注入方法が固形化薬剤の排水中へ
の浸漬という筒便な方法なので、本発明に係る方法は、
維持管理が容易で、経済的に安価である。 (4)脱リン用薬剤の注入場所は、固形化薬剤を浸漬で
きるところであれば良い。従って、注入場所の選択の幅
が広く、かつ複数箇所に取り付けても維持管理が容易で
経済的に安価である。Since the present invention is configured as described above, it has the following effects. (1) A dephosphorizing agent can be added to wastewater at a constant rate and in a fixed amount. (2) Since the addition of the dephosphorizing agent to the wastewater is stable, the dephosphorization in the wastewater is stable and can be performed efficiently. (3) Since the method for injecting the dephosphorizing agent is a convenient method of immersing the solidified agent in the waste water, the method according to the present invention is
It is easy to maintain and economically inexpensive. (4) The injection place of the dephosphorization drug may be any place where the solidified drug can be immersed. Therefore, a wide range of injection sites can be selected, and even if the injection sites are attached to a plurality of sites, the maintenance is easy and the cost is economical.
【図1】本発明に係わる実施例の固形化薬剤をばっ気槽
に設置した概念縦断面図である。FIG. 1 is a conceptual vertical sectional view in which a solidified drug of an example according to the present invention is installed in an aeration tank.
【図2】図形化薬剤の部分切断された斜視図である。FIG. 2 is a partially cut perspective view of a graphic drug.
1 固形化薬剤 2 脱リン用薬剤 3 溶解性結合剤 4 ばっ気槽 6 保持ネット 7 ばっ気槽内部液 8 送風機 9 ばっ気用散気管 10 フツク 1 solidifying agent 2 dephosphorizing agent 3 soluble binder 4 aeration tank 6 retention net 7 aeration tank internal liquid 8 blower 9 aeration diffuser 10 hook
Claims (6)
いて、脱リン用薬剤を溶解性結合剤により固形化して固
形薬剤とし、この固形化薬剤をばっ気槽に設置し溶解さ
せることにより、脱リン用薬剤の添加を行う排水の脱リ
ン方法。1. A wastewater treatment apparatus having a contact aeration tank, wherein a dephosphorization agent is solidified with a soluble binder to give a solid agent, and the solidification agent is placed in an aeration tank and dissolved to remove the dephosphorization agent. A method for dephosphorizing waste water by adding a chemical for phosphorus.
灰、アルミニウム粉末、繊維状アルミニウム、アルミニ
ウム箔、塩化第二鉄溶液及び硫酸アルミニウム溶液のう
ち、いずれか一つまたは二以上の組合せである請求項1
に記載の排水の脱リン方法2. The dephosphorizing agent is one or a combination of two or more of sand iron, fibrous iron, lime, aluminum powder, fibrous aluminum, aluminum foil, ferric chloride solution and aluminum sulfate solution. Claim 1
Dephosphorization of wastewater described in
嫌気ろ床槽流入配管、嫌気ろ床槽から接触ばっ気槽への
移送配管、接触ばっ気槽から沈澱槽への移送配管及び、
沈澱槽から3次処理装置への移送配管のいずれか一つま
たは二以上に配置した請求項1に記載の排水の脱リン方
法。3. An anaerobic filter bed inflow pipe, a transfer pipe from the anaerobic filter bed to a contact aeration tank, a transfer pipe from the contact aeration tank to a precipitation tank, which is a transfer path for the solidified chemical,
The method for dephosphorizing wastewater according to claim 1, wherein one or more of the transfer pipes from the settling tank to the tertiary treatment device are arranged.
る接触ばっ気槽から嫌気ろ床槽への循環配管、沈澱槽か
ら接触ばっ気槽への循環配管及び3次処理装置から接触
ばっ気槽への循環配管のいずれか一つに配置した請求項
1に記載の排水の脱リン方法。4. The solidified chemical is circulated from a contact aeration tank which is a circulating water transfer path to an anaerobic filter bed, a precipitation tank to a contact aeration tank, and a tertiary treatment device. The method for dephosphorizing wastewater according to claim 1, wherein the method is arranged in any one of circulation pipes to the air tank.
槽に配置した請求項1に記載の排水の脱リン方法。5. The method for dephosphorizing wastewater according to claim 1, wherein the solidifying agent is placed in an anaerobic filter tank or a precipitation tank.
請求項1に記載の排水の脱リン方法。6. The method for dephosphorizing wastewater according to claim 1, wherein the solidifying agent is placed in a sludge storage tank.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP30857293A JPH07136664A (en) | 1993-11-16 | 1993-11-16 | Dephosphorization of waste water |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP30857293A JPH07136664A (en) | 1993-11-16 | 1993-11-16 | Dephosphorization of waste water |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH07136664A true JPH07136664A (en) | 1995-05-30 |
Family
ID=17982647
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP30857293A Pending JPH07136664A (en) | 1993-11-16 | 1993-11-16 | Dephosphorization of waste water |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH07136664A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2000048947A1 (en) * | 1999-02-19 | 2000-08-24 | Japan Science And Technology Corporation | Method of removing phosphoric acid contained in wastewater |
JP2008055324A (en) * | 2006-08-31 | 2008-03-13 | Hitachi Housetec Co Ltd | Sewage cleaning tank |
-
1993
- 1993-11-16 JP JP30857293A patent/JPH07136664A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2000048947A1 (en) * | 1999-02-19 | 2000-08-24 | Japan Science And Technology Corporation | Method of removing phosphoric acid contained in wastewater |
US6716357B1 (en) | 1999-02-19 | 2004-04-06 | Japan Science And Technology Corporation | Method of removing phosphoric acid containting wastewater |
JP2008055324A (en) * | 2006-08-31 | 2008-03-13 | Hitachi Housetec Co Ltd | Sewage cleaning tank |
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