JPH07328319A - Dilution-injection system for emulsion type polymer coagulant - Google Patents

Dilution-injection system for emulsion type polymer coagulant

Info

Publication number
JPH07328319A
JPH07328319A JP14854694A JP14854694A JPH07328319A JP H07328319 A JPH07328319 A JP H07328319A JP 14854694 A JP14854694 A JP 14854694A JP 14854694 A JP14854694 A JP 14854694A JP H07328319 A JPH07328319 A JP H07328319A
Authority
JP
Japan
Prior art keywords
conduit
dilution
emulsion polymer
coagulant
polymer flocculant
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
JP14854694A
Other languages
Japanese (ja)
Other versions
JP2745106B2 (en
Inventor
Hideaki Tanaka
秀明 田中
Kosei Umeda
耕生 梅田
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.)
Taki Chemical Co Ltd
Original Assignee
Taki Chemical Co Ltd
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 Taki Chemical Co Ltd filed Critical Taki Chemical Co Ltd
Priority to JP14854694A priority Critical patent/JP2745106B2/en
Publication of JPH07328319A publication Critical patent/JPH07328319A/en
Application granted granted Critical
Publication of JP2745106B2 publication Critical patent/JP2745106B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PURPOSE:To provide a compact automatic supply system for diluting and injecting an emulsion type polymer coagulant. CONSTITUTION:In a system for diluting and injecting a coagulant, a dilution water supply apparatus 1 and an emulsion type high molecular coagulant supply apparatus 4 are connected electrically through a ratio setting device 3, the two supply apparatus are connected to a T-shaped conduit tube 6, a valve is attached at a position which makes the volume of the conduit tube 6 from an opening of the tube 6 to the position 500ml or less, and a conduit tube is connected between the other opening of the conduit tube 6 and a line mixer 10. The system is more compact than a conventional apparatus for diluting an emulsion type high molecular coagulant and easy of handling since the system can easily be operated automatically.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は高分子凝集剤、特にエマ
ルジョン高分子凝集剤の自動希釈注入システムに関す
る。
FIELD OF THE INVENTION The present invention relates to a self-diluting injection system for polymeric flocculants, particularly emulsion polymeric flocculants.

【0002】[0002]

【従来の技術】水処理凝集剤、特に粉末高分子水処理凝
集剤は年々厳しくなる排水規制に対応して、その需要量
は年々増加している。この粉末高分子凝集剤は、水を入
れた溶解槽に設定濃度になるように粉末高分子凝集剤を
添加し、攪拌溶解することによって使用しているが、粉
末の攪拌溶解に長時間を要するばかりでなく、この粉末
が極めて微粉であるため溶解槽への投入時に粉立ちがあ
り、環境を汚染するという問題がある。
2. Description of the Related Art Demand for water treatment coagulants, particularly powdery polymer water treatment coagulants, has been increasing year by year in response to stricter wastewater regulations. This powdery polymer flocculant is used by adding the powdery polymer flocculant to a dissolution tank containing water to a set concentration and stirring and dissolving it, but it takes a long time to dissolve the powder with stirring. Not only that, but since this powder is extremely fine powder, there is a problem that when it is charged into the melting tank, it will stand up and pollute the environment.

【0003】そこでこのような粉末高分子凝集剤に代え
て、近年エマルジョン高分子凝集剤が注目され使用され
るようになった。現在市販されているエマルジョン高分
子凝集剤は、樹脂分濃度が大略20〜40%であり、使用に
際してはこれを希釈して使用する。エマルジョン高分子
凝集剤の出現により粉立ち問題は解消され溶解時間も改
善されたが、いずれにしても粉末高分子凝集剤と同様攪
拌機を備えた希釈槽が必要である。しかし、このような
希釈槽の設置は、依然として設備規模、設置面積を大き
くし、エマルジョン高分子凝集剤の利便性を滅殺するも
のである。そこで設備規模、設置面積を小さくするため
の希釈水とエマルジョン高分子凝集剤を同一ポンプに吸
入し、ポンプ内で混合する方法も提案されているが、運
転中に希釈比率が変動し安定操業が困難である。
Therefore, emulsion polymer flocculants have recently been noticed and used in place of such powder polymer flocculants. The emulsion polymer flocculants currently on the market have a resin content of approximately 20 to 40%, and are diluted before use. With the advent of the emulsion polymer flocculant, the powdering problem was solved and the dissolution time was also improved, but in any case, a diluting tank equipped with a stirrer is required as with the powder polymer flocculant. However, the installation of such a diluting tank still increases the facility scale and installation area, and destroys the convenience of the emulsion polymer coagulant. Therefore, a method has been proposed in which dilution water and emulsion polymer flocculant are sucked into the same pump to reduce the equipment scale and installation area, and mixed in the pump, but the dilution ratio fluctuates during operation and stable operation is possible. Have difficulty.

【0004】[0004]

【発明が解決しようとする課題】そこで、本発明者らは
エマルジョン高分子凝集剤の希釈注入システムについて
検討を重ねた結果、希釈溶解槽を必要とせず、従って設
備規模、設置面積が小さく、更に自由に希釈倍率を設定
でき、希釈混和性に優れた希釈注入システムを完成した
ものである。
Therefore, as a result of repeated studies on the dilution injection system of the emulsion polymer coagulant, the present inventors did not need a dilution dissolution tank, and therefore the equipment scale and the installation area were small. We have completed a dilution injection system with excellent dilution and miscibility that allows the dilution ratio to be set freely.

【0005】[0005]

【課題を解決するための手段】即ち、本発明は希釈水供
給装置に連結した希釈水流量計とエマルジョン高分子凝
集剤供給装置とが比率設定器を介して電気的に接続され
ており、T字型導管の垂直方向の導管にバルブが装着さ
れており、そのバルブ装着位置がT字型導管開口部から
バルブ装着部までの導管容量が500ml以下の位置であっ
て、T字型導管の一方の水平方向の導管には希釈水供給
導管が連結され、垂直方向の導管にはエマルジョン高分
子凝集剤供給導管が連結されており、他方の水平方向導
管にはラインミキサーが連結されているエマルジョン高
分子凝集剤希釈注入システムに関する。
That is, according to the present invention, a dilution water flow meter connected to a dilution water supply device and an emulsion polymer flocculant supply device are electrically connected via a ratio setting device. A valve is mounted on the vertical conduit of the T-shaped conduit, and the valve mounting position is such that the conduit capacity from the T-shaped conduit opening to the valve mounting part is 500 ml or less, and one of the T-shaped conduits The horizontal conduit is connected to the dilution water supply conduit, the vertical conduit is connected to the emulsion polymer flocculant supply conduit, and the other horizontal conduit is connected to the line mixer. Molecular coagulant dilution injection system.

【0006】尚、特開平5-169067号公報には、凝集剤の
希釈方法に於いて、希釈された無機凝集剤と被処理水と
をラインミキサーで混合する方法が開示されているが本
発明とは概念を基本的に異にするものである。
Japanese Patent Laid-Open No. 5-169067 discloses a method of diluting a coagulant, in which a diluted inorganic coagulant and water to be treated are mixed by a line mixer. Is basically different in concept.

【0007】[0007]

【作用】以下に本発明を図1のフローシートに基づいて
更に詳細に説明する。図1のフローシートに於いて、1
は希釈水供給装置を、2は流量計を示す。流量計2は、
比率設定器3を介して電気的にエマルジョン高分子凝集
剤供給装置4に接続されている。従って、希釈倍率を変
更する場合、比率設定器3を所望する倍率に設定する
と、例えば同回路に組み込まれているインバーター12
が作動し、エマルジョン高分子凝集剤供給装置4、例え
ば定量ポンプの回転数が変動し、エマルジョン高分子凝
集剤供給量が設定量に変動する。
The present invention will be described in more detail below with reference to the flow sheet of FIG. 1 in the flow sheet of FIG.
Is a dilution water supply device, and 2 is a flow meter. Flow meter 2
It is electrically connected to the emulsion polymer flocculant supply device 4 via the ratio setting device 3. Therefore, when changing the dilution ratio, if the ratio setter 3 is set to a desired ratio, for example, the inverter 12 incorporated in the same circuit will be used.
Is activated, the rotation number of the emulsion polymer coagulant supply device 4, for example, the metering pump is changed, and the emulsion polymer coagulant supply amount is changed to a set amount.

【0008】さて、5は希釈水導管を示し、希釈水導管
5はT字型導管6の一方の水平方向の導管6aに連結さ
れている。T字型導管6の垂直方向の導管6bにはエマ
ルジョン高分子凝集剤導管7が連結され、T字型導管6
の他方の水平方向の導管6cは、ラインミキサー導管8
に連結されている。T字型導管6の垂直方向の導管6b
には、バルブ9が装着されている。このバルブ9の装着
位置は、T字型導管6の部分拡大図である図2に示すT
字型導管開口部Aからバルブ装着部Bまでの導管容量が
500ml以下の位置である。
Reference numeral 5 denotes a dilution water conduit, which is connected to one horizontal conduit 6a of the T-shaped conduit 6. An emulsion polymer flocculant conduit 7 is connected to the vertical conduit 6b of the T-shaped conduit 6,
The other horizontal conduit 6c of the line mixer conduit 8
Are linked to. Vertical conduit 6b of T-shaped conduit 6
A valve 9 is attached to the. The mounting position of the valve 9 is T shown in FIG. 2, which is a partially enlarged view of the T-shaped conduit 6.
The conduit volume from the A-shaped conduit opening A to the valve mounting part B is
The position is 500 ml or less.

【0009】本発明者らは、エマルジョン高分子凝集剤
希釈注入システムを検討する過程に於いて、極めて困難
な問題に遭遇した。エマルジョン高分子凝集剤の希釈注
入運転を中止した場合、即ちエマルジョン高分子凝集剤
供給装置4及び希釈水供給装置1の運転を停止した場
合、エマルジョン高分子凝集剤導管7に残留していたエ
マルジョン高分子凝集剤が、T字型導管の水平方向の導
管6cに次第に溢流し、これがT字型導管中に残留して
いる希釈水により次第に膨潤し、水平方向の導管6cあ
るいはラインミキサー10を閉塞していた。従って、運
転再開にあたってはT字型導管6の部分を分解し、高分
子凝集剤膨潤物を取り除く必要があった。そこで、T字
型導管6の垂直方向の導管6bの開口部Aの形状を変更
したり、エマルジョン高分子凝集剤供給装置4を停止し
た後、希釈水供給装置1のみを稼働し、残留エマルジョ
ン高分子凝集剤の汲み上げ、同伴等を試みたが、いずれ
も成功しなかった。
The inventors have encountered a very difficult problem in the process of investigating an emulsion polymer flocculant dilution injection system. When the operation of diluting and injecting the emulsion polymer coagulant is stopped, that is, when the operations of the emulsion polymer coagulant supply device 4 and the dilution water supply device 1 are stopped, the emulsion high-pressure agent remaining in the emulsion polymer coagulant conduit 7 is increased. The molecular flocculant gradually overflows into the horizontal conduit 6c of the T-shaped conduit, which gradually swells due to the dilution water remaining in the T-shaped conduit, and blocks the horizontal conduit 6c or the line mixer 10. Was there. Therefore, when restarting the operation, it was necessary to decompose the portion of the T-shaped conduit 6 and remove the polymer coagulant swelling material. Therefore, after changing the shape of the opening A of the vertical conduit 6b of the T-shaped conduit 6 or stopping the emulsion polymer coagulant supply device 4, only the dilution water supply device 1 is operated and the residual emulsion height is increased. Attempts were made to pump up and accompany the molecular flocculant, but none succeeded.

【0010】そこで、更に種々の運転条件、エマルジョ
ン高分子凝集剤の種類、例えばエマルジョンの一種であ
るディスパージョン高分子凝集剤等について検討を重ね
た結果、T字型導管開口部Aからバルブ装着部Bまでの
導管容量が500ml以下の位置にバルブ9を装着すれば、
若干のエマルジョン高分子凝集剤膨潤物は生成するもの
の、支障無く運転再開可能なることを確認した。
Therefore, as a result of further studies on various operating conditions, types of emulsion polymer coagulants, for example, dispersion polymer coagulants, which are a type of emulsion, as a result, from the T-shaped conduit opening A to the valve mounting portion. If the valve 9 is installed at a position where the conduit volume up to B is 500 ml or less,
Although some emulsion polymer flocculant swelling was generated, it was confirmed that the operation could be restarted without any trouble.

【0011】本発明に於いて特に好ましい態様は、T字
型導管6の垂直方向の導管6bの内径が2〜10mmφであ
ることである。この管径よりも小さいと、圧力損失の上
昇および導管の閉塞を生じ易くなり、またこの管径より
も大きいと、希釈水と高分子凝集剤との接触面積が大き
くなり、凝集剤の膨潤現象を生起するために圧力損失が
上昇するだけでなく、溶解不良が発生し易くなる。更
に、T字型導管6の水平方向、即ち6aから6cの方向
への導管の管径は、上記6bと同径若しくは6bの4倍
程度である。また、このT字型導管内の水平方向への希
釈水の流速は、0.2m/s以上であることが必要である。こ
の流速以下では、T字型導管内に凝集剤の膨潤物が滞留
し易くなり、導管を閉塞したり圧力損失が増大したり、
あるいはラインミキサー10内での溶解が不充分となり
好ましくない。
In a particularly preferred embodiment of the present invention, the vertical inner diameter of the T-shaped conduit 6 is 6 to 10 mmφ. If it is smaller than this pipe diameter, the pressure loss is likely to increase and the conduit is apt to be blocked. If it is larger than this pipe diameter, the contact area between the diluting water and the polymeric flocculant becomes large, and the swelling phenomenon of the flocculant occurs. As a result, not only the pressure loss increases, but also defective dissolution easily occurs. Further, the pipe diameter of the T-shaped conduit 6 in the horizontal direction, that is, in the direction from 6a to 6c is the same as the above 6b or about 4 times as large as 6b. Further, the flow velocity of the dilution water in the T-shaped conduit in the horizontal direction needs to be 0.2 m / s or more. Below this flow rate, the swelling material of the coagulant is likely to stay in the T-shaped conduit, clogging the conduit and increasing the pressure loss,
Alternatively, it is not preferable because the dissolution in the line mixer 10 is insufficient.

【0012】さて、ラインミキサー導管8はラインミキ
サー10に連結され、エマルジョン高分子凝集剤は、ラ
インミキサー10を通過中に溶解、希釈される。ライン
ミキサー10で溶解、希釈されたエマルジョン高分子凝
集剤は、注入導管11を経て凝集沈降槽等へ導かれる。
尚、流量計2とT字型導管6との間には、希釈水流量調
節バルブ13を設けることにより、処理対象水の種類、
処理量に対応して自由に凝集剤の添加量を調節すること
ができる。
The line mixer conduit 8 is connected to the line mixer 10, and the emulsion polymer flocculant is dissolved and diluted while passing through the line mixer 10. The emulsion polymer coagulant dissolved and diluted by the line mixer 10 is introduced into a coagulation sedimentation tank or the like via an injection conduit 11.
In addition, by providing a dilution water flow rate control valve 13 between the flow meter 2 and the T-shaped conduit 6, the type of water to be treated,
The addition amount of the coagulant can be freely adjusted according to the treatment amount.

【0013】本発明のエマルジョン高分子凝集剤希釈注
入システムの運転方法は次の通りである。先ず運転の開
始は、希釈水供給装置1を始動後、希釈水流量調節バル
ブ13によって最適流量を調節する。次いでバルブ9を
開口した後、エマルジョン高分子凝集剤供給装置4を始
動する。また運転の停止は、この一連の操作を逆に行え
ば良いが、このような操作は、一般に用いられているシ
ーケンシャル制御プログラム等を介して自動化すればよ
い。また、希釈水流量調節バルブ13による最適流量
は、凝集沈降槽に導入される処理対象水の種類、流量に
応じて調整し、比率設定器3により希釈倍率を設定す
る。尚、希釈水流量調節バルブ13による流量調整は、
処理対象水の流量に連動するように自動化することもで
きる。
The operation method of the emulsion polymer coagulant dilution injection system of the present invention is as follows. First, the operation is started by starting the dilution water supply device 1 and then adjusting the optimum flow rate by the dilution water flow rate adjusting valve 13. Next, after opening the valve 9, the emulsion polymer flocculant supply device 4 is started. Further, the stop of the operation may be performed by reversing this series of operations, and such an operation may be automated through a generally used sequential control program or the like. The optimum flow rate by the dilution water flow rate control valve 13 is adjusted according to the type and flow rate of the water to be treated introduced into the coagulation sedimentation tank, and the ratio setting device 3 sets the dilution ratio. In addition, the flow rate adjustment by the dilution water flow rate control valve 13 is
It can also be automated so as to be linked to the flow rate of the water to be treated.

【0014】[0014]

【実施例】以下に本発明の実施例を挙げて更に説明す
る。図1のフローシートに示したように、本発明のシス
テム実験装置を組み立てた。希釈水供給ポンプ1(能力:
揚程30m,吐出量50L/min)を稼働し、10L/min の速度とな
るように希釈水流量調節バルブ13を開口し、流量計2
を通して希釈水を連続的にT字型導管6に供給すると共
に、バルブ9を開口後、エマルジョン高分子凝集剤供給
ポンプ4(能力:揚程50m,吐出量250ml/min)を稼働し、連
続的にエマルジョン高分子凝集剤(ハイモ(株)製,商品名
ハイモロックE-395,樹脂分濃度20%,粘度150cps)をT字型導管
6に供給した。この場合の比率設定器3(渡辺電機工業
(株)製)の設定値、即ち希釈倍率は100倍とし、この電気
的回路にインバーター((株)安川電機製)を使用した。ま
た、バルブ9の接着位置は450ml位置とし、T字型導管
6の6bの管径を4mmφ、6aから6cの方向への管径
を16mmφとし、ラインミキサー10(ノリタケ(株)製,商品
名:スタティックミキサー)を2連接続して使用した。
EXAMPLES The present invention will be further described below with reference to examples. The system experimental apparatus of the present invention was assembled as shown in the flow sheet of FIG. Dilution water supply pump 1 (Capacity:
(Height: 30 m, Discharge rate: 50 L / min), and the dilution water flow rate control valve 13 is opened so that the speed is 10 L / min.
The dilution water is continuously supplied to the T-shaped conduit 6 through the valve, the valve 9 is opened, and the emulsion polymer flocculant supply pump 4 (capacity: head 50 m, discharge rate 250 ml / min) is operated continuously. An emulsion polymer flocculant (manufactured by Hymo Co., Ltd., trade name Hymolok E-395, resin content concentration 20%, viscosity 150 cps) was supplied to the T-shaped conduit 6. Ratio setter 3 in this case (Watanabe Electric Industry
The setting value of (manufactured by Co., Ltd.), that is, the dilution ratio was 100 times, and an inverter (manufactured by Yasukawa Electric Co., Ltd.) was used for this electric circuit. In addition, the adhesion position of the valve 9 is set to 450 ml, the diameter of 6b of the T-shaped conduit 6 is 4 mmφ, and the diameter of the tube from 6a to 6c is 16 mmφ. : Static mixer) was connected in series and used.

【0015】3時間の連続運転を行い、1時間毎に注入
水の濃度測定を行ったが、極めてよく設定値と一致し、
エマルジョン高分子凝集剤は完全に溶解していた。ま
た、3時間連続運転後、2時間停止し運転を再開した
が、支障無く運転を再開することができた。比較のため
に、バルブ9の接着位置を、T字型導管開口部からバル
ブ装着部までの導管容量が600mlの位置に変更し、上記
と同様の運転を行ったところ、運転中は全く問題を生じ
なかった。しかし、2時間停止し運転を再開したとこ
ろ、注入水の出が悪いために運転を停止した。この時、
T字型導管6を取り外したところ、エマルジョン高分子
凝集剤の膨潤物が導管内に詰まっていた。
Continuous operation was carried out for 3 hours, and the concentration of the injected water was measured every 1 hour.
The emulsion polymer flocculant was completely dissolved. Further, after continuous operation for 3 hours, the operation was restarted after stopping for 2 hours, but the operation could be restarted without any trouble. For comparison, the bonding position of the valve 9 was changed to a position where the conduit volume from the T-shaped conduit opening to the valve mounting part was 600 ml, and the same operation as above was performed, but there was no problem during operation. Did not happen. However, when the operation was restarted after stopping for 2 hours, the operation was stopped because the amount of injected water was poor. At this time,
When the T-shaped conduit 6 was removed, the swollen material of the emulsion polymer coagulant was found to be clogged in the conduit.

【0016】[0016]

【発明の効果】本発明システムは以上詳記したように極
めてコンパクトなエマルジョン高分子凝集剤希釈注入シ
ステムであるから、従来のような大きな設備設置面積を
必要とせず、またエマルジョン高分子凝集剤の膨潤によ
るトラブルも回避されているから、運転の開始、停止も
極めて簡単であり、しかも比率設定器3を介して流量計
2とエマルジョン高分子凝集剤供給装置4とを電気的に
接続しているから、工業廃水、し尿、下水など被処理水
の濁質の種類、濃度などに対応して自由にエマルジョン
高分子凝集剤の注入量、濃度を変更設定することがで
き、従来の希釈装置に比べて頗る簡便であり、産業の発
展に寄するところは甚だ大きいものである。
As described in detail above, the system of the present invention is an extremely compact emulsion polymer flocculant diluting injection system, so that it does not require a large installation area as in the conventional system, and the emulsion polymer flocculant Since troubles due to swelling are also avoided, the operation can be started and stopped very easily, and the flow meter 2 and the emulsion polymer coagulant supply device 4 are electrically connected via the ratio setting device 3. Therefore, the injection amount and concentration of the emulsion polymer flocculant can be freely changed and set according to the type and concentration of suspended solids in the treated water such as industrial wastewater, human waste and sewage. It is extremely simple and convenient, and the area that contributes to the development of industry is enormous.

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

【図1】本発明のエマルジョン高分子凝集剤希釈注入シ
ステムのフローシート図である。
FIG. 1 is a flow sheet diagram of the emulsion polymer flocculant dilution injection system of the present invention.

【図2】本発明のエマルジョン高分子凝集剤希釈注入シ
ステムのT字型導管の部分拡大図である。
FIG. 2 is a partial enlarged view of the T-shaped conduit of the emulsion polymer flocculant dilution injection system of the present invention.

【符号の説明】[Explanation of symbols]

1 希釈水供給装置 2 流量計 3 比率設定器 4 エマルジョン高分子凝集剤供給装置 5 希釈水導管 6 T字型導管 7 エマルジョン高分子凝集剤導管 8 ラインミキサー導管 9 バルブ 10 ラインミキサー 11 注入導管 12 インバーター 13 希釈水流量調節バルブ 1 Diluting Water Supply Device 2 Flow Meter 3 Ratio Setting Device 4 Emulsion Polymer Flocculant Supply Device 5 Dilution Water Conduit 6 T-shaped Conduit 7 Emulsion Polymer Flocculant Conduit 8 Line Mixer Conduit 9 Valve 10 Line Mixer 11 Injection Conduit 12 Inverter 13 Dilution water flow control valve

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 希釈水供給装置に連結した希釈水流量計
とエマルジョン高分子凝集剤供給装置とが比率設定器を
介して電気的に接続されており、T字型導管の垂直方向
の導管にバルブが装着されており、そのバルブ装着位置
がT字型導管開口部からバルブ装着部までの導管容量が
500ml以下の位置であって、T字型導管の一方の水平方
向の導管には希釈水供給導管が連結され、垂直方向の導
管にはエマルジョン高分子凝集剤供給導管が連結されて
おり、他方の水平方向導管にはラインミキサーが連結さ
れているエマルジョン高分子凝集剤希釈注入システム。
1. A dilution water flow meter connected to a dilution water supply device and an emulsion polymer flocculant supply device are electrically connected via a ratio setting device, and are connected to a vertical conduit of a T-shaped conduit. The valve is installed and the valve installation position is such that the conduit volume from the T-shaped conduit opening to the valve installation part is
At a position of 500 ml or less, a dilution water supply conduit is connected to one horizontal conduit of the T-shaped conduit, an emulsion polymer flocculant supply conduit is connected to the vertical conduit, and the other is connected to the vertical conduit. Emulsion polymer flocculant dilution injection system with line mixer connected to horizontal conduit.
JP14854694A 1994-06-06 1994-06-06 Emulsion polymer coagulant dilution injection system Expired - Fee Related JP2745106B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14854694A JP2745106B2 (en) 1994-06-06 1994-06-06 Emulsion polymer coagulant dilution injection system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14854694A JP2745106B2 (en) 1994-06-06 1994-06-06 Emulsion polymer coagulant dilution injection system

Publications (2)

Publication Number Publication Date
JPH07328319A true JPH07328319A (en) 1995-12-19
JP2745106B2 JP2745106B2 (en) 1998-04-28

Family

ID=15455187

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14854694A Expired - Fee Related JP2745106B2 (en) 1994-06-06 1994-06-06 Emulsion polymer coagulant dilution injection system

Country Status (1)

Country Link
JP (1) JP2745106B2 (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100336865B1 (en) * 1999-04-15 2002-05-16 종 현 김 Auto Mixing and Diffusing System of Liquid Chemicals for Water Treatment Plant
JP2011167651A (en) * 2010-02-22 2011-09-01 Hymo Corp Treatment method of sewage sludge
JP2011183314A (en) * 2010-03-09 2011-09-22 Kurita Water Ind Ltd Chemical injection apparatus and operation method for the same
JP2018134625A (en) * 2017-03-31 2018-08-30 メタウォーター株式会社 Waste water treatment system
JP2018202330A (en) * 2017-06-05 2018-12-27 メタウォーター株式会社 Dispersion device and processing system for processing object water

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100336865B1 (en) * 1999-04-15 2002-05-16 종 현 김 Auto Mixing and Diffusing System of Liquid Chemicals for Water Treatment Plant
JP2011167651A (en) * 2010-02-22 2011-09-01 Hymo Corp Treatment method of sewage sludge
JP2011183314A (en) * 2010-03-09 2011-09-22 Kurita Water Ind Ltd Chemical injection apparatus and operation method for the same
JP2018134625A (en) * 2017-03-31 2018-08-30 メタウォーター株式会社 Waste water treatment system
JP2018202330A (en) * 2017-06-05 2018-12-27 メタウォーター株式会社 Dispersion device and processing system for processing object water

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