JPS58143806A - Solid-liquid separation method - Google Patents
Solid-liquid separation methodInfo
- Publication number
- JPS58143806A JPS58143806A JP2568182A JP2568182A JPS58143806A JP S58143806 A JPS58143806 A JP S58143806A JP 2568182 A JP2568182 A JP 2568182A JP 2568182 A JP2568182 A JP 2568182A JP S58143806 A JPS58143806 A JP S58143806A
- Authority
- JP
- Japan
- Prior art keywords
- liquid
- treated
- coagulant
- ionicity
- dehydrating
- 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
Abstract
Description
【発明の詳細な説明】
本発明け、被処理液に電解質の凝集剤全添加して凝集混
相処理した後に固液分離処理する固液分離方法に関する
。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a solid-liquid separation method in which an electrolyte flocculant is completely added to a liquid to be treated, a coagulation multiphase treatment is performed, and then a solid-liquid separation treatment is performed.
上記方法に、微粒状の固形分全大径のフロックにしてそ
の固形分の回収効率を同上せんとfるものであるが、凝
集処理を良好に行うことにもちろんの事、薬剤使用量を
少なくしてランニングコスト全低減する上から凝集剤を
過不足無く供給fゐ必要がある。 −f:こて、従来で
は・被処理液の汚濁濃/fを測定し、その測定濃1wπ
応じて凝集剤の添加量を調節している。 ところが、現
状で(1、汚濁濃度の検出稍jWが低く、又、微粒状の
固形分の混入度合いが貧化してもそれが汚濁7禰度の変
化として現われない場合がある等、未だ改善の故地があ
り之。In the above method, the solid content is made into flocs with a large diameter in the form of fine particles, and the recovery efficiency of the solid content is the same as that of the above method. In order to reduce running costs, it is necessary to supply just the right amount of flocculant. -f: Trowel, conventionally - Measure the contamination density/f of the liquid to be treated, and the measured density 1wπ
The amount of flocculant added is adjusted accordingly. However, at present (1) the detection level of the pollution concentration is low, and even if the degree of incorporation of fine particulate solids becomes poor, it may not appear as a change in the pollution level. There is a hometown.
本発明に、上記の点に鑑み、被処理液に対する凝集剤の
添加量分、被処理液の性状VC応じて梢度艮〈調節でき
るようVc〒ることを目体]とfる。In the present invention, in view of the above points, the degree of concentration (Vc) is adjusted according to the amount of flocculant added to the liquid to be treated and the property VC of the liquid to be treated.
次に、本発明方法実施の態様全例示図に基いて説明する
。Next, embodiments of the method of the present invention will be explained based on all illustrative drawings.
′粥/貯留槽(11力・ら供給びハ、る、し尿や都市1
;水あるいは産業廃水等の各種の水処理に伴って発生さ
れる汚泥等の被処理液と、第J貯留槽(2)から供給き
れる電解質凝集剤とを、混和機13)において凝集混相
処理する。'Porridge/storage tank (11 power, supply, human waste and city 1
The liquid to be treated such as sludge generated in the treatment of various types of water such as water or industrial wastewater, and the electrolyte flocculant completely supplied from the J storage tank (2) are subjected to coagulation multiphase treatment in the mixer 13). .
凝集され^被処理液をベルトプレス型脱水機(4)に供
給し、縦力脱水部(5)においてろ逸脱水処理すると共
に、直線状経路の轄圧脱水ゾーン(A)大径円弧状経路
り〕匝縮脱水/−ンLBI、及び、蛇行状経路の剪断脱
水ゾーン(C)からなる強制脱水部ill icおいて
、重力脱水部(5)から第1回幼ろ布(7)に載って送
り出されてくるケーキを第2回動ろ布(8)によって挟
圧脱水処理する。The flocculated liquid to be treated is supplied to the belt press type dehydrator (4), where the filtration water is treated in the vertical force dewatering section (5), and at the same time, the concentrated pressure dewatering zone (A) is a linear path, and the large diameter arc path is In the forced dehydration section (Illic), which consists of a collapse dehydration/-LBI and a shear dehydration zone (C) with a meandering path, the water is transferred from the gravity dehydration section (5) to the first child's cloth (7). The cake sent out is subjected to pressure dehydration treatment using a second rotating filter cloth (8).
脱水処理後のケーキをスクレーパ(9)によってろ布(
7)・(8)から剥離除去する。After the dehydration process, the cake is passed through a filter cloth (
7) Peel and remove from (8).
分離液、および、ケーキ剥離後のろ布(7)・(8)紫
洸浄するためにノズル(10]から噴出され之洗浄排水
倉集合排水路(ul VC回収させる。The separated liquid and the filter cloths (7) and (8) after removing the cake are ejected from the nozzle (10) for purification and are collected in the cleaning drainage tank collecting drain (ul VC).
111記果合排水路(11)に連ねて設けられた滞留槽
(14に分離液を一時的に滞wびぜ、その滞留分離液の
イオン性を測定装置nにより設定時間おきに測定し、そ
の測′尼されたイオン性を判別機構(I41に入力し、
曲記判別機構圓における判別結果に基いて、前記・躬2
貯留槽(2)から混和機(3)への凝集剤供給用の、吐
出容置if父型ボング(10全自切的Vc操作し、凝集
剤を過不足無く供給する。111 The separated liquid is temporarily retained in the retention tank (14) provided in series with the water drainage channel (11), and the ionicity of the retained separated liquid is measured at set time intervals by a measuring device n. The measured ionicity is input to the discrimination mechanism (I41,
Based on the discrimination results of the songwriting discrimination mechanism, the above-mentioned
For supplying flocculant from the storage tank (2) to the mixer (3), the discharge container if father-type bong (10 fully automatic Vc operation is used to supply just the right amount of flocculant.
即ち、分離液中のイオン性がプラスであるかマイナスで
あるか、あるいは零(以下中和状態と称する)であるか
を判別し1例えば、電解質凝集剤として陽イオン性のも
のケ用いる場合に、測定されたイオン性がプラスであれ
ば、凝集剤の添加量を設定量減少させ、逆にマイナスで
あれば凝集剤の添加量を設定量増加させ、そして中和状
態の場合Kにその寸筺の状惑全維持ざぜル(7)である
。 従って、被処理液の性状いかんにかかわらず、測定
イオン性が交互にプラスとマイナス分水す、中和状晧に
近い状態が、あるいに零を示す中和状態で安定し、凝集
剤の添加量を必要最小限の量に自助的に調節するのであ
る。That is, it is determined whether the ionicity in the separated liquid is positive, negative, or zero (hereinafter referred to as the neutralized state). If the measured ionicity is positive, the amount of flocculant added is decreased by the set amount, and if the measured ionicity is negative, the amount of flocculant added is increased by the set amount. This is Zazeru (7), which maintains the entire state of the box. Therefore, regardless of the properties of the liquid to be treated, the measured ionicity alternates between positive and negative water, a state close to a neutralized state, or a stable state in a neutralized state where it shows zero, and the flocculant They adjust the amount added to the minimum necessary amount on their own.
前記電解質凝集剤として汀、ポリアクリルアンドやポリ
アクリル酸エステル、あるいに、有機質に対するカチオ
ン系凝集剤、無機質に対するアニオン系#集剤等各種の
ものが使用さnるtのである。As the electrolyte flocculant, various kinds of coagulants such as slag, polyacrylate, polyacrylic acid ester, cationic flocculants for organic substances, anionic coagulants for inorganic substances, etc. are used.
本発明とじてに、1iTI記ベルトプレス型脱水機14
iVC代えて凝集沈澱槽とか遠心濃縮機等、各種の固液
分離処理手段が採用できるものである。According to the present invention, 1iTI belt press type dehydrator 14
Instead of iVC, various solid-liquid separation treatment means such as a coagulation sedimentation tank or a centrifugal concentrator can be used.
以上要f、6K、本発明に、胃記した固液分離力法にお
いて、分離液のイオン性を測定し、その測定イオン性金
中和あるい汀そAに近い状態K Tるように凝集剤の添
加量を調節する事會特徴とする。In the solid-liquid separation force method described above, in the present invention, the ionicity of the separated liquid is measured, and the ionicity of the gold is neutralized or aggregated so that it is in a state close to A. The feature is that the amount of the agent added is adjusted.
凝集処理し7′j結果である、分離液のイオン性に基き
、電解質凝集剤が有−rるイオン性と比較して、測定イ
オン性が同じである事により添加量が過剰である4!を
、逆である事により添加量が不足している事を、そして
、中和状態にある事により適量である事を夫々判別する
から、その凝集処理が適量の凝集剤によって行われてい
るかどうかを適量に判別でき、し力・も、その判別結果
に応じて凝集剤の添加量を調節するから、被処理液の性
状に応じ、凝集剤の添加量を精度良〈調節できるように
なつ迄。Based on the ionicity of the separated liquid as a result of flocculation treatment, the amount added is excessive as the measured ionicity is the same compared to the ionicity of the electrolyte flocculant.4! If the opposite is true, it is determined that the amount added is insufficient, and if it is in a neutralized state, it is determined that the amount is appropriate, so whether the flocculation process is being performed with the appropriate amount of flocculant. It is possible to determine the appropriate amount of coagulant and adjust the amount of coagulant added according to the determination result, so the amount of coagulant added can be adjusted with high precision according to the properties of the liquid to be treated. .
Claims (1)
した後に固液分離処理する固液分離方法であって、分離
液のイオン性全測疋し、その測定イオン性を中和あるい
はそれに近い状諮に丁ゐ工うVc凝集剤の添加量を調節
する事を特徴とfる固液分離方法。A solid-liquid separation method in which the liquid to be treated Vc1 is subjected to a coagulation-mixing treatment by adding a solute flocculant, and then subjected to solid-liquid separation treatment, in which the total ionicity of the separated liquid is measured, and the measured ionicity is neutralized or A solid-liquid separation method characterized in that the amount of Vc flocculant added is adjusted according to the situation.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2568182A JPS58143806A (en) | 1982-02-18 | 1982-02-18 | Solid-liquid separation method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2568182A JPS58143806A (en) | 1982-02-18 | 1982-02-18 | Solid-liquid separation method |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS58143806A true JPS58143806A (en) | 1983-08-26 |
Family
ID=12172522
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2568182A Pending JPS58143806A (en) | 1982-02-18 | 1982-02-18 | Solid-liquid separation method |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58143806A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4932513A (en) * | 1985-09-02 | 1990-06-12 | The Brook Club, Inc. | Hopper for continuously and automatically drawing out tires through a water tank |
JPH04263480A (en) * | 1991-02-18 | 1992-09-18 | Nippon Telegr & Teleph Corp <Ntt> | Oxide superconductor single crystal thin film forming board and manufacture thereof |
JPH04137708U (en) * | 1991-06-19 | 1992-12-22 | 株式会社スイレイ | Coagulant injection control device for solid-liquid separation systems for raw water such as sludge water |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5721985A (en) * | 1980-07-11 | 1982-02-04 | Hitachi Ltd | Controlling method for chlorine injection |
-
1982
- 1982-02-18 JP JP2568182A patent/JPS58143806A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5721985A (en) * | 1980-07-11 | 1982-02-04 | Hitachi Ltd | Controlling method for chlorine injection |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4932513A (en) * | 1985-09-02 | 1990-06-12 | The Brook Club, Inc. | Hopper for continuously and automatically drawing out tires through a water tank |
JPH04263480A (en) * | 1991-02-18 | 1992-09-18 | Nippon Telegr & Teleph Corp <Ntt> | Oxide superconductor single crystal thin film forming board and manufacture thereof |
JPH04137708U (en) * | 1991-06-19 | 1992-12-22 | 株式会社スイレイ | Coagulant injection control device for solid-liquid separation systems for raw water such as sludge water |
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