JPH0440248A - Solid-liquid separating method - Google Patents

Solid-liquid separating method

Info

Publication number
JPH0440248A
JPH0440248A JP2141336A JP14133690A JPH0440248A JP H0440248 A JPH0440248 A JP H0440248A JP 2141336 A JP2141336 A JP 2141336A JP 14133690 A JP14133690 A JP 14133690A JP H0440248 A JPH0440248 A JP H0440248A
Authority
JP
Japan
Prior art keywords
liquid
matters
magnetic powder
magnetic
coagulating
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
Application number
JP2141336A
Other languages
Japanese (ja)
Inventor
Toshihito Kondo
敏仁 近藤
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.)
Fujita Corp
Original Assignee
Fujita Corp
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 Fujita Corp filed Critical Fujita Corp
Priority to JP2141336A priority Critical patent/JPH0440248A/en
Publication of JPH0440248A publication Critical patent/JPH0440248A/en
Pending legal-status Critical Current

Links

Landscapes

  • Water Treatment By Electricity Or Magnetism (AREA)
  • Separation Of Suspended Particles By Flocculating Agents (AREA)
  • Treatment Of Sludge (AREA)

Abstract

PURPOSE:To facilitate solid-liquid separation of a liquid containing suspended matters hard to precipitate easy by mixing a magnetic powder and a coagulant to a liquid to form coagulating matters which are the suspended matters and the magnetic powder combined each other and drawing and concentrating the coagulating matters in a specified position owing to the magnetic force and then separating them from the liquid. CONSTITUTION:A magnetic powder and a coagulant are mixed with a liquid to produce coagulating matters which are suspended matters and the magnetic powder combined each other and the coagulating matters are drawn and concentrated in a specified position owing to the magnetic force and then they are separated from the liquid. As the magnetic powder to be used, iron powder, iron sand, ferrite, etc. with 0.01-100mum grain size are suitable. The addition amount of the magnetic powder is preferably 0.1-10wt.% of the suspended solid matter. The magnetic force is generated by a permanent magnet or an electromagnet. In this way, organic suspended matters which are hard to precipitate by normal gravity precipitation precipitate extremely quickly.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、凝集剤を用いて液体中の懸濁物を分離する方
法の改良に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to an improvement in a method for separating suspended matter in a liquid using a flocculant.

〔従来の技術〕[Conventional technology]

沈降性の悪い微細な固形物を懸濁状態で含有する液体に
ついて固液分離を行う場合は、凝集剤を用いて微細な固
形物を粗大な凝集物に変えることにより沈殿し易いもの
とし、これを静置状態で、または遠心力等の作用下に、
沈殿させて分離することが多い。
When solid-liquid separation is performed on a liquid containing suspended fine solids that have poor settling properties, a flocculant is used to convert the fine solids into coarse aggregates that make them easier to settle. in a stationary state or under the action of centrifugal force, etc.
Often separated by precipitation.

しかしながら、凝集剤を用いても、形成される凝集物が
軟弱な場合や液体との比重差が小さい場合には沈降速度
はあまり大きくならず、沈降分離された凝集物の脱水も
困難である。
However, even if a flocculant is used, if the flocculates formed are soft or have a small difference in specific gravity from the liquid, the sedimentation rate will not be very high, and it will be difficult to dehydrate the flocculates that have been sedimented and separated.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

そこで本発明は、単なる凝集剤の使用によっては沈降分
離が困難な微細固形物を速やかに液体から分離可能にす
る手段を提供し、難沈降性懸濁物を含む液体の固液分離
を容易にしようとするものである。
Therefore, the present invention provides a means for quickly separating fine solids that are difficult to settle and separate from a liquid by simply using a flocculant, and facilitates solid-liquid separation of liquids containing difficult-to-settle suspensions. This is what I am trying to do.

〔課題を解決するための手段〕[Means to solve the problem]

上記目的を達成することに成功した本発明は、微細な懸
濁物を含有する液体の固液分離を行うに当たり、液体に
磁性体粉末および凝集剤を混合して懸濁物と磁性体粉末
とが合体した凝集物を生成させ、該凝集物を磁力により
特定の位置に誘引濃縮し、次いで液体より分離すること
を特徴とするものである。
The present invention, which has succeeded in achieving the above object, involves mixing magnetic powder and a flocculant with the liquid to separate the suspension and magnetic powder when performing solid-liquid separation of a liquid containing fine suspensions. The method is characterized in that agglomerates are formed by coalescing, the aggregates are attracted to a specific position by magnetic force, concentrated, and then separated from the liquid.

この固液分離方法において使用する磁性体粉末としては
、粒径が0.0l−100u程度の鉄粉、砂鉄、フェラ
イトなどが適当である。
As the magnetic powder used in this solid-liquid separation method, iron powder, iron sand, ferrite, etc. having a particle size of about 0.0 l to 100 u are suitable.

磁性体粉末の添加量は、分離しようとする懸濁物の種類
によっても異なるが、懸濁固形物あたり0.1〜lO重
量%程度が適当である。
The amount of magnetic powder added varies depending on the type of suspended matter to be separated, but is suitably about 0.1 to 10% by weight per suspended solid matter.

磁力は、永久磁石または電磁石により発生させる。Magnetic force is generated by a permanent magnet or an electromagnet.

磁性体を含む懸濁物凝集物は、磁性体を添加しない場合
に形成される凝集物よりも重いので、重力のみによる沈
降も加速される傾向がある。したがって、静置分離にお
いては、磁力も重力による沈降を加速するように作用さ
せるのが有利である。すなわち、非鉄金属またはプラス
チックで作られた沈降槽の底板直下に磁石を置いて凝集
物中の磁性体に磁力を作用させることにより凝集物を下
方に誘引し、重力による沈降を加速する。しかしながら
、凝集物の性質によっては底板方向とは別の方向に磁力
による誘引を行うほうが存利な場合もあり、静置分離に
おいても誘引方向は限定されるものではない。静置によ
らない分離たとえば遠心分離を行う場合においては、遠
心力作用方向前方に磁石を配置して磁性体含有凝集物を
誘引する。
Suspension aggregates containing magnetic material are heavier than aggregates formed without the addition of magnetic material, so sedimentation due to gravity alone also tends to be accelerated. Therefore, in static separation, it is advantageous that magnetic force also acts to accelerate sedimentation due to gravity. That is, a magnet is placed directly under the bottom plate of a settling tank made of non-ferrous metal or plastic, and a magnetic force is applied to the magnetic material in the aggregates, thereby attracting the aggregates downward and accelerating the sedimentation due to gravity. However, depending on the nature of the aggregates, it may be more advantageous to attract them by magnetic force in a direction other than the direction of the bottom plate, and the direction of attraction is not limited even in static separation. When performing separation that does not involve standing still, such as centrifugation, a magnet is placed forward in the direction of centrifugal force to attract magnetic substance-containing aggregates.

いずれの場合も、凝集物は磁性体を添加しない場合より
も速やかに、かつ高度に、磁石膜置部付近に濃縮される
。スラリー状ないしケーク状に濃縮された凝集物は、任
意の方法で上溝部分と分離する。
In either case, the aggregates are concentrated near the magnet film placement part more quickly and to a higher degree than in the case where no magnetic material is added. The aggregates concentrated into a slurry or cake are separated from the upper groove portion by any method.

磁性体粉末を含むことにより、濃縮された凝集物は軟質
の有機性懸濁物の場合においても濾過、乾燥等、その後
の処理における取り扱いが容易である。
By containing the magnetic powder, the concentrated aggregate can be easily handled in subsequent processing such as filtration and drying even in the case of a soft organic suspension.

〔寮施例〕[Dormitory example]

沈降性のきわめて悪い有機性懸濁物を含む消化汚泥の固
液分離処理に本発明の方法を実施した。供試消化汚泥は
都市下水処理場で採取したもので、懸濁物含有量はO,
S%である。
The method of the present invention was applied to solid-liquid separation treatment of digested sludge containing organic suspended matter with extremely poor settling properties. The sample digested sludge was collected from a municipal sewage treatment plant, and the suspended solids content was O,
It is S%.

容量11のトールビーカーに消化汚泥10100Oを取
り、これに、高分子凝集剤・IKフロック(市川毛織株
式会社製品)10%溶液5011と鉄粉0,5gを同時
に添加し、マグネチックスターラーで5分間撹拌した。
Take 10,100 O of digested sludge in a tall beaker with a capacity of 11, add 10% solution of polymer flocculant/IK floc (product of Ichikawa Keori Co., Ltd.) 5011 and 0.5 g of iron powder at the same time, and stir with a magnetic stirrer for 5 minutes. Stirred.

次いでビーカー底部に永久磁石(45x30x10m+
*;3500ガウス)を固定し、以後、撹拌することな
く静置し、ビーカー底部の沈澱物の体積と上澄液の濁度
を経時的に測定した。なお、濁度は分光光度計を用いて
波長620 +nで測定した。
Next, place a permanent magnet (45x30x10m+) at the bottom of the beaker.
*; 3,500 Gauss) was fixed, and then allowed to stand without stirring, and the volume of the precipitate at the bottom of the beaker and the turbidity of the supernatant were measured over time. Note that turbidity was measured at a wavelength of 620 +n using a spectrophotometer.

比較のため、鉄粉を添加せず磁石も使用しないほかは上
記と同様にした試験(比較例1)、および鉄粉も高分子
凝集剤も添加しないほかは同様にした試験(比較例2)
を実施した。
For comparison, a test was conducted in the same manner as above except that no iron powder was added and no magnet was used (Comparative Example 1), and a test was conducted in the same manner as above except that neither iron powder nor polymer flocculant was added (Comparative Example 2).
was carried out.

測定結果を表1に示す。The measurement results are shown in Table 1.

表1 〔発明の効果〕 上述のように、本発明によれば通常の重力沈降ではなか
なか沈降しない有機性懸濁物もきわめて迅速に沈降させ
ることができる。さらに、本発明によれば任意の位置に
高密度で凝集物を集めることができから、従来よりも能
率のよい固液分離が可能になるだけでなく、従来は沈降
分離が不可能であったような難沈降性懸濁物の分離も可
能になる。
Table 1 [Effects of the Invention] As described above, according to the present invention, even organic suspended matter that does not easily settle by normal gravity sedimentation can be sedimented very quickly. Furthermore, according to the present invention, it is possible to collect aggregates at a high density at any location, which not only enables more efficient solid-liquid separation than before, but also allows for sedimentation separation, which was previously impossible. It also becomes possible to separate suspended substances that do not easily settle.

Claims (1)

【特許請求の範囲】[Claims] 微細な懸濁物を含有する液体の固液分離を行うに当たり
、液体に磁性体粉末および凝集剤を混合して懸濁物と磁
性体粉末とが合体した凝集物を生成させ、該凝集物を磁
力により特定の位置に誘引濃縮し、次いで液体より分離
することを特徴とする固液分離方法。
When performing solid-liquid separation of a liquid containing fine suspensions, magnetic powder and a flocculant are mixed with the liquid to form aggregates in which the suspensions and magnetic powders are combined, and the aggregates are A solid-liquid separation method characterized by attracting concentration to a specific position by magnetic force and then separating it from a liquid.
JP2141336A 1990-06-01 1990-06-01 Solid-liquid separating method Pending JPH0440248A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2141336A JPH0440248A (en) 1990-06-01 1990-06-01 Solid-liquid separating method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2141336A JPH0440248A (en) 1990-06-01 1990-06-01 Solid-liquid separating method

Publications (1)

Publication Number Publication Date
JPH0440248A true JPH0440248A (en) 1992-02-10

Family

ID=15289586

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2141336A Pending JPH0440248A (en) 1990-06-01 1990-06-01 Solid-liquid separating method

Country Status (1)

Country Link
JP (1) JPH0440248A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002177997A (en) * 2000-12-11 2002-06-25 Asahi Tec Corp Sludge thickening method
JP2006513851A (en) * 2003-02-26 2006-04-27 デグレマン ソシエテ アノニム Method and system for the treatment of liquid effluents, especially containing suspended contaminants
JP2008012530A (en) * 1996-06-07 2008-01-24 Roche Diagnostics Gmbh Dry polymer bead preparation
JP2011002679A (en) * 2009-06-19 2011-01-06 Konica Minolta Business Technologies Inc Developing device and image forming apparatus
JP2013126640A (en) * 2011-12-19 2013-06-27 Toshiba Corp Oil-containing waste water treatment apparatus
CN103524015A (en) * 2013-10-22 2014-01-22 秦广山 Mud curing agent and preparation method thereof

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4920948A (en) * 1972-06-15 1974-02-23
JPS5182459A (en) * 1975-01-14 1976-07-20 Miura Eng Int Jujiseifuntono kyogyoshuoryosuru haisuishorihoho
JPS51103361A (en) * 1975-03-08 1976-09-11 Miura Eng Int
JPS5561979A (en) * 1978-11-02 1980-05-10 Daido Steel Co Ltd Treatment method for solid in raw water
JPS55132684A (en) * 1979-04-02 1980-10-15 Hitachi Plant Eng & Constr Co Ltd Magnetic treatment of waste water
JPS59139910A (en) * 1983-01-27 1984-08-11 Daido Steel Co Ltd Magnetic separation method

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4920948A (en) * 1972-06-15 1974-02-23
JPS5182459A (en) * 1975-01-14 1976-07-20 Miura Eng Int Jujiseifuntono kyogyoshuoryosuru haisuishorihoho
JPS51103361A (en) * 1975-03-08 1976-09-11 Miura Eng Int
JPS5561979A (en) * 1978-11-02 1980-05-10 Daido Steel Co Ltd Treatment method for solid in raw water
JPS55132684A (en) * 1979-04-02 1980-10-15 Hitachi Plant Eng & Constr Co Ltd Magnetic treatment of waste water
JPS59139910A (en) * 1983-01-27 1984-08-11 Daido Steel Co Ltd Magnetic separation method

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008012530A (en) * 1996-06-07 2008-01-24 Roche Diagnostics Gmbh Dry polymer bead preparation
JP2002177997A (en) * 2000-12-11 2002-06-25 Asahi Tec Corp Sludge thickening method
JP2006513851A (en) * 2003-02-26 2006-04-27 デグレマン ソシエテ アノニム Method and system for the treatment of liquid effluents, especially containing suspended contaminants
JP2011002679A (en) * 2009-06-19 2011-01-06 Konica Minolta Business Technologies Inc Developing device and image forming apparatus
JP2013126640A (en) * 2011-12-19 2013-06-27 Toshiba Corp Oil-containing waste water treatment apparatus
CN103524015A (en) * 2013-10-22 2014-01-22 秦广山 Mud curing agent and preparation method thereof

Similar Documents

Publication Publication Date Title
US4089779A (en) Clarification process
US8399239B2 (en) Compositions and methods for continuous harvesting of suspension growth cultures
US4741838A (en) Flocculation of high solids mineral slurries
JPH0440248A (en) Solid-liquid separating method
US2232294A (en) Process for treating liquids
JPH08267075A (en) Method for using new high solid polymer composition as flocculating auxiliary
KR100345405B1 (en) Method for treating waste water with steel slag
CN111039515A (en) Flocculation-magnetic separation process for treating non/weak magnetic sewage
JPH06507573A (en) liquid handling
US4225426A (en) Magnetic beneficiation of clays utilizing magnetic particulates
JPS6359759B2 (en)
KR101269045B1 (en) Disposal apparatuse of waste water comprising magnetic nanoparticles
JPH06344000A (en) Dehydration process for sludge
JP3478321B2 (en) Activated sludge settling promoter and activated sludge treatment method for wastewater using the same
US4383928A (en) Treatment of water contaminated with dispersed resin
CA1114080A (en) Method and an agent for chemical purification of water by means of chemical precipitation and magnetic sludge separation
KR940000550B1 (en) Process for separating suspended solid particles from liquids
JP2016159210A (en) Treatment method and treatment device of incineration ash
Wu et al. Magnetic seeding sedimentation (MSS) of coal slimes
JP4353584B2 (en) Sand-added coagulating sedimentation equipment
Sengul et al. Determination of the factors affecting the efficiency of the polymer in solid–liquid separation with synthetic polymers
Das, B.*, Prakash, S.**, Biswal, SK** & Reddy Settling characteristics of coal washery tailings using synthetic polyelectrolytes with fine magnetite
JP2538006B2 (en) Wastewater treatment agent and wastewater treatment method using the same
Krishnan et al. Floc characteristics in selective flocculation of fine particles.
JPS624197B2 (en)