JPH0346182B2 - - Google Patents
Info
- Publication number
- JPH0346182B2 JPH0346182B2 JP1254383A JP1254383A JPH0346182B2 JP H0346182 B2 JPH0346182 B2 JP H0346182B2 JP 1254383 A JP1254383 A JP 1254383A JP 1254383 A JP1254383 A JP 1254383A JP H0346182 B2 JPH0346182 B2 JP H0346182B2
- Authority
- JP
- Japan
- Prior art keywords
- magnetic
- raw water
- magnetic separation
- magnetite powder
- powder particles
- 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.)
- Expired
Links
- 230000005291 magnetic effect Effects 0.000 claims description 18
- 238000007885 magnetic separation Methods 0.000 claims description 17
- 239000007788 liquid Substances 0.000 claims description 12
- 239000000696 magnetic material Substances 0.000 claims description 7
- 239000000126 substance Substances 0.000 claims description 5
- 239000000701 coagulant Substances 0.000 claims description 4
- 238000003672 processing method Methods 0.000 claims 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 26
- SZVJSHCCFOBDDC-UHFFFAOYSA-N iron(II,III) oxide Inorganic materials O=[Fe]O[Fe]O[Fe]=O SZVJSHCCFOBDDC-UHFFFAOYSA-N 0.000 description 20
- 239000002245 particle Substances 0.000 description 19
- 239000000843 powder Substances 0.000 description 17
- 238000000034 method Methods 0.000 description 9
- 238000007796 conventional method Methods 0.000 description 8
- 239000006185 dispersion Substances 0.000 description 5
- 238000010586 diagram Methods 0.000 description 4
- 238000011001 backwashing Methods 0.000 description 2
- 239000006247 magnetic powder Substances 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 125000000129 anionic group Chemical group 0.000 description 1
- 230000001112 coagulating effect Effects 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003302 ferromagnetic material Substances 0.000 description 1
- 239000008394 flocculating agent Substances 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 239000012258 stirred mixture Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C1/00—Magnetic separation
- B03C1/005—Pretreatment specially adapted for magnetic separation
- B03C1/01—Pretreatment specially adapted for magnetic separation by addition of magnetic adjuvants
Landscapes
- Water Treatment By Electricity Or Magnetism (AREA)
- Physical Water Treatments (AREA)
Description
本発明は磁気分離処理方法、更に詳しくは、液
中の非磁性懸濁物質を磁性体及び凝集剤等の存在
下、共凝集して磁性フロツクとなした後にこれを
磁気分離処理するに当たり、超音波で均一分散せ
しめた磁性体を用いることによつて、液中から該
非磁性懸濁物質を効果的に且つ充分に分離除去す
ることができる磁気分離処理方法に関する。
都市下水、産業排水、各種の製造工程廃液更に
はこれらの活性汚泥処理水等の液中には有機系又
は無機系の非磁性懸濁物質(以下、これを単に
SSと略記する)が混在していることが多い。こ
れらはそのまま環境へ放出すると公害源となるた
め何らかの手段で処理される必要がある。
近年、かかるSSを含む液(以下、これを単に
原水と略記する)を処理するに磁気分離処理が行
われている。この場合の磁気分離処理は、原水中
のSSを適当な磁性体及び凝集剤等の存在下に共
凝集して磁気分離処理し得る形態の磁性フロツク
となし、しかる後にこれを磁気分離するもので、
代表的には例えば、磁気分離装置として電磁フイ
ルタが、また磁性体として強磁性体であるマグネ
タイトの粉粒が各々用いられている。
ところが、このような場合における従来の磁気
分離処理は一般に、羽根式撹拌機等で機械的に撹
拌して得た磁性体粉粒の撹拌混合液を原水に投入
し、凝集剤を加え、該原水中のSSを磁性体粉粒
とともに共凝集して磁性フロツクとなし、しかる
後にこれを磁気分離装置へ供する方法であるが、
実際上、かかる従来法によると処理水中に依然と
して無視できない程度のSSが浮遊していて、特
にSSの除去が質的及び量的に極めて高度に要求
される今日においてはなお充分といえず、磁気分
離処理によるSSのより効率的なそしてより充分
な分離除去が望まれているのである。
本発明は、叙上の如き観点において、原水中の
SSを効率的に且つ充分に分離除去することがで
きる磁気分離処理方法を提供するものである。
以下、磁気分離装置として電磁フイルタを、ま
た磁性体としてマグネタイト粉粒を各々例にと
り、図面に基づいて従来法と比較しつつ本発明の
構成を詳細に説明する。
第1図は従来法の処理手順を例示する概略系統
図である。原水をポンプ11で送液する配管途中
において、羽根式撹拌機21によるマグネタイト
粉粒の撹拌混合液31及び羽根式撹拌機22によ
る凝集剤の希釈溶解液44が各々ポンプ12,1
3で加えられ、次いで電磁フイルタ51に供され
て、処理水が得られている。電磁フイルタ51で
は、凝集剤により共凝集したSSとマグネタイト
粉粒との磁性フロツクが捕捉蓄積され、これらは
例えば一定時間の連続処理後に常法の逆洗で系外
へ排出される。
かかる従来法には、図面で例示する場合の他
に、別途、原水とマグネタイト粉粒との混合槽
や、凝集剤による共凝集槽等を設けたり、また原
水にマグネタイト粉粒と凝集剤とを同時に加える
場合等もあるが、いずれの方法でも実際に磁気分
離処理すると、処理水中に依然として無視できな
い程度のSSが浮遊してくるのである。
本発明者らは、この原因を追求すると、従来法
では原水中に投入するマグネタイト粉粒が一様な
均一分散状態になく、マグネタイト粉粒相互間で
凝集していて、マグネタイト粉粒の一つ一つが原
水中のSSを吸着するような状態になつていない
ため、該SSは磁性フロツクを形成することなく
凝集剤により単なるフロツクの状態で電磁フイル
タに供給されるか、又は磁性フロツクを形成した
としても、SSとマグネタイト粉粒との緊密度が
弱い磁性フロツクのままで電磁フイルタに供給さ
れ、このようなフロツクのSSが電磁フイルタに
捕捉されることなく処理水中に同伴されてしまう
ことが判つた。
そこで本発明者らは、このような問題を解消す
るべく更に鋭意研究した結果、原水中に投入する
マグネタイト粉粒を予め超音波で液中分散させる
と、該マグネタイト粉粒はあたかもその一つ一つ
がバラバラになつた均一分散状態となり、しかも
その表面に付着していることの多い塵埃等が同時
に除去された活性状態となつて、このような状態
のマグネタイト粉粒を原水に投入すれば、原水中
のSSがマグネタイト粉粒のあたかも一つ一つに
効率的且つ緊密強固に吸着され、これらが凝集剤
によつて磁性フロツクを形成し、かかる磁性フロ
ツクが電磁フイルタに確実に捕捉されることを見
出し、本発明を完成するに至つた。
第2図と第3図とは本発明の各別の一実施例を
示す概略系統図である。第2図の場合、原水をポ
ンプ14で送液する配管途中において、超音波発
振器61によるマグネタイト粉粒の均一分散液7
1及び羽根式撹拌機23による凝集剤の希釈溶解
液42が各々ポンプ15,16で加えられ、次い
で電磁フイルタ52に供されて、処理水が得られ
ている。第3図の場合、原水をポンプ17で送液
する配管途中において、羽根式撹拌機24による
マグネタイト粉粒の撹拌混合液32を超音波発振
器62を備える分散容器81内にて前述の如き均
一分散液72としたもの及び羽根式撹拌機25に
よる凝集剤の希釈溶解液43が各々ポンプ18,
19で加えられ、次いで電磁フイルタ53に供さ
れて、処理水が得られている。
図示した実施例はいずれも、マグネタイト粉粒
を前述のごとくあたかも一つ一つバラバラにした
活性状態の均一分散液71,72として原水に加
えており、電磁フイルタ52,53で捕捉された
磁性フロツクの系外への排出は従来法と同様逆洗
による。
本発明において、マグネタイト粉粒は磁性体
の、また電磁フイルタは磁気分離装置のそれぞれ
代表例であり、既によく知られている他の磁性体
や磁気分離装置が使用され得る。そして凝集剤
は、対象となる原水の性状に応じて適宜選択され
る1種又は2種以上のもので、通常アニオン系や
ノニオン系の高分子凝集剤等、例えばポリ塩化ア
ルミニウム、が使用され得る。
以上説明した本発明の効果をより具体的にする
ため、次の第1表を例示する。表中、従来例は第
1図に、実施例1は第2図に、また実施例2は第
3図に、各々したがつて処理したものである。
The present invention relates to a magnetic separation treatment method, and more specifically, a method for coagulating non-magnetic suspended matter in a liquid into a magnetic floc in the presence of a magnetic substance, a flocculant, etc., and then subjecting the same to magnetic separation treatment. The present invention relates to a magnetic separation treatment method that can effectively and sufficiently separate and remove non-magnetic suspended matter from a liquid by using a magnetic material uniformly dispersed by sound waves. Municipal sewage, industrial wastewater, various manufacturing process waste liquids, and activated sludge treated water, etc., contain organic or inorganic non-magnetic suspended substances (hereinafter simply referred to as
(abbreviated as SS) are often mixed together. If these are released into the environment as they are, they become a source of pollution, so they must be disposed of by some means. In recent years, magnetic separation processing has been used to treat liquids containing such SS (hereinafter simply referred to as raw water). In this case, the magnetic separation treatment involves co-agglomerating the SS in the raw water in the presence of an appropriate magnetic material and coagulant to form a magnetic floc that can be subjected to magnetic separation treatment, and then magnetically separating this. ,
Typically, for example, an electromagnetic filter is used as the magnetic separation device, and powder particles of magnetite, which is a ferromagnetic material, are used as the magnetic material. However, in conventional magnetic separation treatment in such cases, generally, a stirred mixture of magnetic powder particles obtained by mechanically stirring with a blade stirrer etc. is poured into raw water, a flocculant is added, and the raw material is separated. This method coagulates SS in water with magnetic powder particles to form magnetic flocs, which is then sent to a magnetic separation device.
In reality, according to such conventional methods, a non-negligible amount of SS is still suspended in the treated water, and it is still insufficient, especially in today's world where removal of SS is extremely demanding in terms of quality and quantity. There is a desire for more efficient and sufficient separation and removal of SS through separation treatment. From the above-mentioned viewpoint, the present invention provides
The present invention provides a magnetic separation treatment method that can efficiently and sufficiently separate and remove SS. Hereinafter, the structure of the present invention will be explained in detail by using an electromagnetic filter as a magnetic separation device and magnetite powder as an example of the magnetic material, and comparing it with a conventional method based on the drawings. FIG. 1 is a schematic system diagram illustrating the processing procedure of the conventional method. In the middle of the piping through which raw water is sent by the pump 11, a mixed liquid 31 of magnetite powder particles stirred by a blade-type stirrer 21 and a diluted solution 44 of flocculant by a blade-type stirrer 22 are pumped to the pumps 12 and 1, respectively.
3, and then passed through an electromagnetic filter 51 to obtain treated water. The electromagnetic filter 51 captures and accumulates magnetic flocs of SS and magnetite powder coagulated by a flocculant, and these are discharged from the system by backwashing in a conventional manner after continuous treatment for a certain period of time, for example. In addition to the examples shown in the drawings, such conventional methods include separately providing a mixing tank for raw water and magnetite powder, a co-flocculating tank using a coagulant, or adding magnetite powder and a coagulant to raw water. In some cases, SS is added at the same time, but in actual magnetic separation treatment using either method, a non-negligible amount of SS still floats in the treated water. When the present inventors investigated the cause of this problem, they found that in the conventional method, the magnetite powder particles introduced into raw water were not uniformly dispersed, and that the magnetite powder particles were agglomerated between each other. Since one of the SS is not in a state where it can adsorb SS in the raw water, the SS is either supplied to the electromagnetic filter in the form of a floc by a flocculant without forming a magnetic floc, or the SS is supplied to the electromagnetic filter in the form of a floc without forming a magnetic floc. However, it has been found that the tightness between SS and magnetite powder particles is weak and the magnetic flocs are supplied to the electromagnetic filter, and the SS in such flocs is not captured by the electromagnetic filter and is entrained in the treated water. Ivy. Therefore, the inventors of the present invention conducted further intensive research in order to solve this problem, and found that if the magnetite powder particles to be introduced into raw water are dispersed in the liquid using ultrasonic waves in advance, each magnetite powder particle will appear as if it were a single particle. When the magnetite particles are in a uniformly dispersed state, and the dust that often adheres to the surface is removed at the same time, the magnetite particles in this state are put into raw water. It was confirmed that SS in water is efficiently, tightly and strongly adsorbed to each magnetite powder particle, and these form magnetic flocs by the flocculant, and these magnetic flocs are reliably captured by an electromagnetic filter. This finding led to the completion of the present invention. 2 and 3 are schematic system diagrams showing different embodiments of the present invention. In the case of FIG. 2, a uniform dispersion of magnetite powder particles 7 is generated by an ultrasonic oscillator 61 in the middle of the piping where raw water is sent by the pump 14.
1 and a diluted solution 42 of the flocculant produced by the blade stirrer 23 are added by pumps 15 and 16, respectively, and then passed through an electromagnetic filter 52 to obtain treated water. In the case of FIG. 3, a mixed liquid 32 of magnetite particles is stirred by a blade-type stirrer 24 in the middle of a pipe for feeding raw water by a pump 17, and is uniformly dispersed as described above in a dispersion container 81 equipped with an ultrasonic oscillator 62. The liquid 72 and the diluted flocculant solution 43 produced by the blade stirrer 25 are pumped into the pumps 18 and 43, respectively.
19, and then passed through an electromagnetic filter 53 to obtain treated water. In all of the illustrated embodiments, magnetite powder particles are added to raw water as uniform dispersion liquids 71 and 72 in an activated state as if they had been separated one by one as described above, and magnetic flocs captured by electromagnetic filters 52 and 53 are added to the raw water. is discharged out of the system by backwashing as in the conventional method. In the present invention, the magnetite powder particles are typical examples of a magnetic material, and the electromagnetic filter is a typical example of a magnetic separation device, and other well-known magnetic materials and magnetic separation devices can be used. The flocculant is one or more types selected as appropriate depending on the properties of the target raw water, and usually anionic or nonionic polymer flocculants, such as polyaluminum chloride, may be used. . In order to make the effects of the present invention explained above more concrete, the following Table 1 is illustrated. In the table, the conventional example is shown in FIG. 1, Example 1 is shown in FIG. 2, and Example 2 is shown in FIG. 3, respectively.
【表】【table】
【表】
第1表の結果からも明らかなように、各実施例
はいずれも、従来例に比べて処理水中のSS濃度
が著るしく低くなつており、使用したマグネタイ
ト粉粒が超音波によつて効率的に且つ充分に機能
していることが判る。
本発明によると、磁気分離処理において原水中
のSSをより効率的且つ充分に分離除去すること
ができ、従来法において生じるマグネタイト粉粒
のタンクや配管途中への付着堆積現象もない。[Table] As is clear from the results in Table 1, in each example, the SS concentration in the treated water was significantly lower than in the conventional example, and the magnetite powder particles used were exposed to ultrasonic waves. Therefore, it can be seen that it is functioning efficiently and satisfactorily. According to the present invention, SS in raw water can be separated and removed more efficiently and sufficiently in the magnetic separation process, and there is no phenomenon of adhesion and accumulation of magnetite powder particles in a tank or in the middle of piping, which occurs in the conventional method.
第1図は従来法の処理手順を例示する概略系統
図、第2図と第3図とは本発明の各別の一実施例
を示す概略系統図である。
11〜19……ポンプ、21〜25……羽根式
撹拌機、31,32……撹拌混合液、41〜43
……希釈溶解液、51〜53……電磁フイルタ、
61,62……超音波発振器、71,72……均
一分散液、81……分散容器。
FIG. 1 is a schematic system diagram illustrating the processing procedure of the conventional method, and FIGS. 2 and 3 are schematic system diagrams illustrating different embodiments of the present invention. 11-19...Pump, 21-25...Blade type stirrer, 31,32...Stirring mixed liquid, 41-43
... Diluted solution, 51-53 ... Electromagnetic filter,
61, 62... Ultrasonic oscillator, 71, 72... Uniform dispersion liquid, 81... Dispersion container.
Claims (1)
剤等を適宜に加えて該非磁性懸濁物質を磁性フロ
ツクとなした後にこれを磁気分離処理するに当た
り、超音波で均一分散せしめた磁性体を加えるこ
とを特徴とする磁気分離処理方法。1. When a magnetic substance and a coagulant are appropriately added to a liquid containing a non-magnetic suspended substance to form a magnetic floc from the non-magnetic suspended substance, and when this is subjected to magnetic separation treatment, the magnetic material is uniformly dispersed by ultrasonic waves. A magnetic separation processing method characterized by adding a body.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1254383A JPS59139910A (en) | 1983-01-27 | 1983-01-27 | Magnetic separation processing method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1254383A JPS59139910A (en) | 1983-01-27 | 1983-01-27 | Magnetic separation processing method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS59139910A JPS59139910A (en) | 1984-08-11 |
| JPH0346182B2 true JPH0346182B2 (en) | 1991-07-15 |
Family
ID=11808246
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1254383A Granted JPS59139910A (en) | 1983-01-27 | 1983-01-27 | Magnetic separation processing method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS59139910A (en) |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| AU601386B2 (en) * | 1985-12-20 | 1990-09-13 | Syntex (U.S.A.) Inc. | Particle separation method |
| JPH0295594U (en) * | 1988-07-27 | 1990-07-30 | ||
| JPH0440248A (en) * | 1990-06-01 | 1992-02-10 | Fujita Corp | Solid-liquid separating method |
| KR100918373B1 (en) | 2008-12-01 | 2009-09-21 | 충남대학교산학협력단 | Hybrid water treatment device and method using electromagnet and membrane |
| CN106391302A (en) * | 2016-11-10 | 2017-02-15 | 江苏省冶金设计院有限公司 | High-intensity magnetic disperse magnetic separation device and method for low-intensity magnetic separation tailings containing magnetic mica |
| CN110655290B (en) * | 2019-09-26 | 2022-04-22 | 安徽恒源煤电股份有限公司 | Coal mine wastewater treatment method |
-
1983
- 1983-01-27 JP JP1254383A patent/JPS59139910A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS59139910A (en) | 1984-08-11 |
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