JPH0440248A - Solid-liquid separating method - Google Patents
Solid-liquid separating methodInfo
- 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
Links
- 239000007788 liquid Substances 0.000 title claims abstract description 26
- 238000000034 method Methods 0.000 title description 5
- 239000006247 magnetic powder Substances 0.000 claims abstract description 13
- 238000000926 separation method Methods 0.000 claims abstract description 13
- 239000000725 suspension Substances 0.000 claims description 7
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 abstract description 9
- 230000005484 gravity Effects 0.000 abstract description 6
- 239000007787 solid Substances 0.000 abstract description 6
- 229910052742 iron Inorganic materials 0.000 abstract description 2
- 238000002156 mixing Methods 0.000 abstract description 2
- 239000002244 precipitate Substances 0.000 abstract description 2
- 238000001556 precipitation Methods 0.000 abstract description 2
- 239000004576 sand Substances 0.000 abstract description 2
- 229910000859 α-Fe Inorganic materials 0.000 abstract description 2
- 230000001112 coagulating effect Effects 0.000 abstract 4
- 239000000701 coagulant Substances 0.000 abstract 2
- 238000004062 sedimentation Methods 0.000 description 6
- 239000000696 magnetic material Substances 0.000 description 4
- 239000010802 sludge Substances 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- 230000003068 static effect Effects 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
Landscapes
- Water Treatment By Electricity Or Magnetism (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
- Treatment Of Sludge (AREA)
Abstract
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.
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.
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.
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.
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)
、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.
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)
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)
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 |
-
1990
- 1990-06-01 JP JP2141336A patent/JPH0440248A/en active Pending
Patent Citations (6)
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)
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 |
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