JPS594488A - Treatment of red tide - Google Patents

Treatment of red tide

Info

Publication number
JPS594488A
JPS594488A JP57109825A JP10982582A JPS594488A JP S594488 A JPS594488 A JP S594488A JP 57109825 A JP57109825 A JP 57109825A JP 10982582 A JP10982582 A JP 10982582A JP S594488 A JPS594488 A JP S594488A
Authority
JP
Japan
Prior art keywords
red tide
fine particles
magnetized
particles
ferromagnetic material
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
JP57109825A
Other languages
Japanese (ja)
Other versions
JPS625025B2 (en
Inventor
Kiichiro Fujii
藤井 喜一郎
Toru Yamauchi
徹 山内
Norio Shioji
塩地 則夫
Kiyoshi Sugata
清 菅田
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.)
UNYUSHO DAISAN KOWAN KENSETSU KYOKUCHO
Mitsubishi Heavy Industries Ltd
Original Assignee
UNYUSHO DAISAN KOWAN KENSETSU KYOKUCHO
Mitsubishi Heavy Industries 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 UNYUSHO DAISAN KOWAN KENSETSU KYOKUCHO, Mitsubishi Heavy Industries Ltd filed Critical UNYUSHO DAISAN KOWAN KENSETSU KYOKUCHO
Priority to JP57109825A priority Critical patent/JPS594488A/en
Publication of JPS594488A publication Critical patent/JPS594488A/en
Publication of JPS625025B2 publication Critical patent/JPS625025B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION 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
    • B03CMAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C1/00Magnetic separation
    • B03C1/005Pretreatment specially adapted for magnetic separation
    • B03C1/01Pretreatment specially adapted for magnetic separation by addition of magnetic adjuvants

Landscapes

  • Physical Water Treatments (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)

Abstract

PURPOSE:To recover effectively red tide planktons, by adding fine particles of a ferromagnetic material to red tidelike raw water, and subjecting the same to a centrifugal sepn. as it is when said fine particles are magnetized and after magnetizing the same when the particles are magnetized. CONSTITUTION:The raw water contg. red tide planktons from a red tide-like water area 1 is drawn through an intake line 2 and an intake device 3 into a stirring tank 5, where the raw water is stirred thoroughly with fine particles of a ferromagnetic material such as magnetite or the like from a mixing installation 4 and entangle and stick with and to each other. When the fine particles of the ferromagnetic material are magnetized with a magnetic field 7, the fine particles of the ferromagnetic material stuck with the red tide planktons are adsorbed to each other by the magnetic force of the particles themselves, thus forming flocs. The flocs are settled and separated in a settling tank 8, and are fed as a slurry through a line 10 to a centritugal separator 11, where the flocs are separated centrifugally, and are discharged as dehydrated slurry from a line 14. The desorbed water is returned to the tank 5 or the tank 8.

Description

【発明の詳細な説明】 本発明は赤潮の処理方法に関し、特に公害上問題となる
赤潮を消滅させると同時に、赤潮の原因物質である赤潮
プランクトンを遠心分離法によって濃縮状で回収する方
法を提供せん:とするものである。
[Detailed Description of the Invention] The present invention relates to a method for treating red tide, and in particular provides a method for eliminating red tide, which poses a pollution problem, and at the same time recovering red tide plankton, which is a causative agent of red tide, in a concentrated form by centrifugation. sen: means that.

一般に、赤潮プランクトンを遠心分離・する場合、無機
質凝集剤〔水に溶解した時、Fe’(oH)3゜A7(
OH)3などとなるもの〕、増量剤〔例えば0aE10
4.  CaO03,0a(OH)2あるいは粘土〕及
び高分子系凝集剤(アルギン酸ソーダなど)を加え、遠
心分離機内での滞留時間を05分以上犬体は1分程度と
して行われている。しかし、この場合、脱離水の水質が
悪((SSで100■/を以上)、しかも排出スラッジ
濃度が低い(60?/1以下)という欠点がある。
Generally, when red tide plankton is centrifuged, an inorganic flocculant [Fe'(oH) 3° A7 (when dissolved in water) is used.
OH)3, etc.], extenders [e.g. 0aE10
4. CaO03,0a(OH)2 or clay] and a polymer flocculant (sodium alginate, etc.) are added, and the residence time in the centrifuge is set to 05 minutes or more and about 1 minute for dogs. However, in this case, there are disadvantages in that the quality of the desorbed water is poor (SS: 100 .mu./1 or more) and the discharged sludge concentration is low (60 .mu./1 or less).

本発明者らは、上記の欠点を排除し、脱離水の水質が良
好であって、しかも排出スラッジ濃度が高くなるような
遠心分離法を開発し、これによって効果的に赤潮プラン
クトンを回収すると共に、公害上の問題である赤潮を消
滅させるべく鋭意研究の結果、(a)赤潮プランクトン
の表面は屈曲に富み、また粘質物の膜で覆われているも
のが多い、(b)多数の赤潮プランクトンは地磁気に感
応する性質があり強磁性体微粒子とのなじみ具合がよい
、(C)強磁性体微粒子はいったん磁化されると、微粒
子自身が相互に自分自身の磁力で吸着しあい、凝集物を
作る性質がある、(a)強磁性体微粒子はいずれも比重
が大きく遠心力の場では非常に沈降しやすい、という事
実を確認し、強磁性体微粒子に赤潮プランクトンを付着
させ、これを強磁性体微粒子自身の磁力によって凝集物
となせば、遠心分離法によシ赤潮プランクトンを濃縮状
で効率良く回収できるのではないかという知見を得、多
くの実験によシその効果を確認し、本発明を完成するに
到った。
The present inventors have developed a centrifugal separation method that eliminates the above drawbacks, has good quality of desorbed water, and has a high concentration of discharged sludge, thereby effectively recovering red tide plankton and As a result of intensive research to eliminate red tide, which is a pollution problem, we found that (a) the surface of red tide plankton is curved and many are covered with a film of mucus; (b) a large number of red tide plankton (C) Once ferromagnetic particles are magnetized, they attract each other with their own magnetic force, forming aggregates. (a) We confirmed the fact that all ferromagnetic particles have a large specific gravity and are very easy to settle in the field of centrifugal force, and we attached red tide plankton to ferromagnetic particles, We obtained the knowledge that red tide plankton could be collected efficiently in a concentrated form by centrifugation if they were made into aggregates by the magnetic force of the fine particles themselves, and after confirming this effect through many experiments, we developed the present invention. I have reached the point where I have completed the .

す々わち、本発明は赤潮状の原水から赤潮プランクトン
を分離回収する方法において、赤潮状の原水を取水し、
これに強磁性体微粒子を添加し、該強磁性体微粒子が予
め磁化されていればそのまま、磁化されていなければ上
記の添加後に磁化し、しかる後遠心分離することを特徴
とする赤潮の処理方法を要旨とするもの°である。
In short, the present invention provides a method for separating and recovering red tide plankton from red tide raw water, which includes taking red tide raw water,
A method for treating red tide, which comprises adding ferromagnetic particles to the mixture, and if the ferromagnetic particles have been magnetized in advance, they are left as is; if they are not magnetized, they are magnetized after the above addition, and then centrifuged. The gist is:

本発明は、赤潮回収船上で適用することもでき、一般に
上水(飲料水)処理における赤潮プランクトン混入トラ
ブル対策、海水、湖沼水を工業用水又は工業原料とする
場合の赤潮プランクトン混入トラブル対策に有利に適用
することができる。
The present invention can also be applied onboard a red tide collection ship, and is generally advantageous in countermeasures against red tide plankton contamination in drinking water treatment, and in countermeasures against red tide plankton contamination when seawater, lake water is used as industrial water or industrial raw material. It can be applied to

本発明の構成について詳述する前に、先ず木表1に示す
Before describing the configuration of the present invention in detail, Table 1 first shows the structure of the present invention.

以下、部側図面に沿って本発明方法を詳細に説明する。Hereinafter, the method of the present invention will be explained in detail with reference to the side drawings.

第1図は本発明方法の一実施態様例を示すフローソート
、第2図は第1図の一部変更例を示すフローシートであ
る。
FIG. 1 is a flow sorting example showing an embodiment of the method of the present invention, and FIG. 2 is a flow sheet showing a partially modified example of FIG. 1.

第1.2図において、1は赤潮状の水域、2は原水の取
水ライン、5はゴミ除去兼取水装置、4は磁化されてい
ない強磁性体微粒子の混入設備、5は攪拌槽、6は攪拌
機(空気攪拌手段としてもよい)、7は磁場(磁界゛)
で、例えば磁石で構成されたトンネル状の水路、あるい
は水路に磁石を挿入したもの等が使用され、8は沈降槽
で、例えば自然沈殿や液体サイクロン等が使用され、9
は上澄水の放流ライン、10はスラリーの抜取ライン、
11は遠心分離機、12゜16は脱離水の戻シライン、
14は脱水スラッジの排出ラインである。
In Figure 1.2, 1 is a red tide water area, 2 is a raw water intake line, 5 is a garbage removal/water intake device, 4 is equipment for mixing unmagnetized ferromagnetic particles, 5 is a stirring tank, and 6 is a water intake line. Stirrer (may be used as air stirring means), 7 is a magnetic field (magnetic field)
For example, a tunnel-shaped waterway made up of magnets or a waterway with a magnet inserted is used, 8 is a sedimentation tank, for example, natural sedimentation or a hydrocyclone is used, and 9
10 is the supernatant water discharge line, 10 is the slurry extraction line,
11 is a centrifuge, 12゜16 is a return line for desorbed water,
14 is a dewatered sludge discharge line.

第1図と第2図の相違点は、磁場7が第1図では攪拌槽
5の後にあるのに対し、第2図では強磁性体微粒子の混
入設備の後にある点だけである。
The only difference between FIG. 1 and FIG. 2 is that the magnetic field 7 is located after the stirring tank 5 in FIG. 1, whereas in FIG. 2 it is located after the equipment for mixing ferromagnetic fine particles.

第1.2図において、赤潮状の水域1よりの赤潮プラン
クトンを含む原水は、取水ライン2、取水装置3を経て
攪拌槽5に達し、混入設備4からの強磁性体微粒子〔例
えは、マグネタイト(Fe3O4)、ヘマタイト(Fe
2O3)、酸化コノ(ルト、酸化クロム等〕と共にこ\
で十分攪拌され、強磁性体微粒子と赤潮プランクトンと
は互にからみ合って何着しあう。第1図のフローでは、
この後に磁場7で強磁性体微粒子の磁化を行なうと、第
2図のフローでは強磁性体微粒子は磁化された後に攪拌
槽5に供給されるためそのま捷で、赤潮プランクトンを
付着した強磁性体微粒子は自身の磁力によシ吸着し合い
凝集物となる。この凝集物は沈降槽8にて沈降分離、し
、清浄な上澄水はライン9から放流され、凝集物はスラ
リーとしてライン10を経て遠心分離機11に送られ、
遠心分離された後、脱水スラッジとしてライン14から
排出され、脱離水はライン12.13を介して攪拌槽5
又は沈降槽8へ戻される。
In Figure 1.2, raw water containing red tide plankton from a red tide-like water area 1 reaches a stirring tank 5 via a water intake line 2 and a water intake device 3, and is mixed with ferromagnetic fine particles [for example, magnetite] from a mixing equipment 4. (Fe3O4), hematite (Fe
2O3), oxides (rut, chromium oxide, etc.)
The ferromagnetic particles and red tide plankton become entangled with each other and land on each other. In the flow shown in Figure 1,
After this, when the ferromagnetic particles are magnetized in the magnetic field 7, in the flow shown in Figure 2, the ferromagnetic particles are magnetized and then supplied to the stirring tank 5, so the ferromagnetic particles with the red tide plankton attached are left as they are. The body particles attract each other by their own magnetic force and form aggregates. The flocs are sedimented and separated in a sedimentation tank 8, clean supernatant water is discharged from a line 9, and the flocs are sent as a slurry to a centrifuge 11 via a line 10.
After being centrifuged, it is discharged as dewatered sludge through line 14, and the dehydrated water is passed through line 12.13 to stirring tank 5.
Or it is returned to the sedimentation tank 8.

第3図は本発明方法の他の実施態様例を示すフローシー
トで、該図中、第1.2図と同一符号は第1.2図と同
−機能部を示し、15は固液分離装置(例えば、凝集沈
殿処理装置)、16は無機質凝集剤(前記した一般の方
法で使用されるもの)および/′又は高分子系凝集剤(
前記した一般の方法で使用されるもの)の薬品注入装置
、17は沈降槽8をバイパスする場合のラインであシ、
磁場7a、’7bはいずれか一方のみを設備しておけば
よい。
FIG. 3 is a flow sheet showing another embodiment of the method of the present invention, in which the same reference numerals as in FIG. 1.2 indicate the same functional parts as in FIG. 1.2, and 15 indicates solid-liquid separation. equipment (e.g., coagulation-sedimentation treatment equipment), 16 is an inorganic flocculant (used in the general method described above) and/or a polymeric flocculant (
a chemical injection device (used in the general method described above); 17 is a line for bypassing the settling tank 8;
It is sufficient to install only one of the magnetic fields 7a and '7b.

第3図のものは、強磁性体微粒子を添加する前に、予め
赤潮プランクトンを含む原水を固液分離装置15で固液
分離しておき、ここで得られたスラリーに強磁性体微粒
子を添加する方式%式% 以上のように、本発明方法は、赤潮水域中では11n沈
降するのに何日というオーダーの極めて沈降しにくい赤
潮プランクトンを、磁化された強磁性体微粒子は該微粒
子1ケ1ケが磁石となっていて互に吸着しあい巨大な凝
集物を作り、しかも強磁性体微粒子はもともと比重の太
きいものが多く、沈降性は非常によい(沈降速度は数1
0 m7′Hr 〜100 m/′Hr )という性質
を示す強磁性体微粒と混合し、強磁性体微粒子が磁化さ
れていればそのitで、磁化されていなければ磁化して
、磁化された強磁性体微粒子の作る凝集物の中に赤潮プ
ランクトンを包み込み、あるいは吸着させ、あたかも1
つの巨大な比重の大きな粒子と化し、しかる後に遠心沈
降(遠心分離)させることにより、沈降しにくい赤潮プ
ランクトンを容易に遠心分離するものである。
In the case shown in Fig. 3, before adding the ferromagnetic particles, the raw water containing red tide plankton is solid-liquid separated in advance using the solid-liquid separator 15, and the ferromagnetic particles are added to the slurry obtained here. As described above, the method of the present invention allows red tide plankton, which is extremely difficult to sediment in red tide waters, to settle down to 11n, to be absorbed by magnetized ferromagnetic fine particles. The ferromagnetic particles act as magnets and attract each other, forming huge aggregates.Furthermore, many ferromagnetic fine particles originally have a high specific gravity, and have very good sedimentation properties (sedimentation speed is several 1
0 m7'Hr ~ 100 m/'Hr), and if the ferromagnetic particles are magnetized, they become magnetized, and if they are not magnetized, they become magnetized, and the magnetized Red tide plankton is engulfed or adsorbed in aggregates made by magnetic fine particles, making it look like one.
Red tide plankton, which is difficult to sediment, can be easily centrifuged by turning them into two huge particles with high specific gravity and then centrifuging them (centrifugal separation).

次に、本発明方法の実験例をあげる。Next, an experimental example of the method of the present invention will be given.

例 供試プランクトン 瀬戸内海で採取した海水に適宜栄養塩及びビタミンを添
加し、25℃前後で昼夜強い光を当てて培養したもので
、スケレトネマ(Skeleto−nema Sp、 
)及びある種の緑藻及び渦鞭毛藻を含むもの。
Example Plankton Test: Seawater collected from the Seto Inland Sea was supplemented with appropriate nutrients and vitamins, and cultured at around 25°C under strong light day and night.
) and some green algae and dinoflagellates.

強磁性体微粒子 純度98%以上のFe3O4(マグネタイト)で、真比
重5.1グ/′rnl、平均粒径0.52 p、かさ比
重約0.5 y / rn7!、磁化85.4 emu
 / ? (於7koe、 )を用゛いた。
Ferromagnetic fine particles Fe3O4 (magnetite) with a purity of 98% or more, true specific gravity 5.1 g/'rnl, average particle size 0.52 p, bulk specific gravity approximately 0.5 y/rn7! , magnetization 85.4 emu
/ ? (7koe, ) was used.

遠心分離機 デラバル型遠心分離機で、内容積t S t 、発生遠
心力8400Gのものを連続給液法で用いた。
Centrifuge: A DeLaval type centrifuge with an internal volume t S t and a generated centrifugal force of 8400 G was used in a continuous liquid supply method.

実験結果 表2に示す通シであった。Experimental result The results were as shown in Table 2.

表2中、比較例Cは強磁性体微粒子Fe3O4の磁化は
行なっておらず、本発明例A、B’は予め磁化したFe
3O4を用いた。
In Table 2, in Comparative Example C, the ferromagnetic fine particles Fe3O4 were not magnetized, and in Inventive Examples A and B', the ferromagnetic fine particles Fe3O4 were not magnetized.
3O4 was used.

表2から次のことが明らかである。The following is clear from Table 2.

(a)  本発明例A、Bは、比較例C,Dに比べ、滞
留時間が小さくても処理効果が大きい。
(a) Compared to Comparative Examples C and D, Examples A and B of the present invention have a greater treatment effect even if the residence time is shorter.

(b)  脱離水水質が約1桁本発明例A、Bが比較例
c、D’よシ良い。
(b) The quality of desorbed water is about one order of magnitude better in Examples A and B of the present invention than in Comparative Examples C and D'.

(C)  排出スラッジ濃度が本発明例Aと比較例りで
は倍近く、また、本発明例BのようにFe3O4の添加
の少ない場合でも比較例0.Dに対し有意な差を示し、
本発明例におけるスラッジの濃縮効果がみられた。
(C) The discharged sludge concentration is almost twice as high as that of the comparative example in Inventive Example A, and even when Fe3O4 is added less as in Inventive Example B, it is 0. shows a significant difference to D,
The effect of concentrating the sludge in the example of the present invention was observed.

′  以上から明らかなように、本発明方法は、極めて
有効な処理ができることが判る。
' As is clear from the above, it is clear that the method of the present invention can perform extremely effective treatment.

以上詳述した本発明方法による効果をまとめて次に示す
The effects of the method of the present invention detailed above are summarized below.

+11  小さい遠心分離機で十分な働きをなす(内容
積で前記した一般の方法に比べ3〜5倍の差がある)。
+11 A small centrifuge is sufficient (there is a difference in internal volume of 3 to 5 times compared to the general method described above).

(2)  排出スラッジ濃度が高くなる。(2) The discharged sludge concentration increases.

(3)  脱離水水質が、前記した一般の方法に比べ、
約1桁良好となる。
(3) The quality of the desorbed water is lower than that of the general method described above.
Approximately one order of magnitude better.

(4)  上記(1)〜(3)の効果を奏することによ
って、従来濃縮が困難であった赤潮プランクトンが、極
めて良好に濃縮できる。
(4) By achieving the effects (1) to (3) above, red tide plankton, which has been difficult to concentrate in the past, can be concentrated extremely well.

【図面の簡単な説明】[Brief explanation of the drawing]

第1〜6図は本発明方法の実施態様例を示すフローシー
トである。 後代理人  内 1)  明 復代理人  萩 原 亮 −
1 to 6 are flow sheets showing embodiments of the method of the present invention. Sub-agent 1) Meifuku agent Ryo Hagiwara -

Claims (1)

【特許請求の範囲】[Claims] 赤潮状の原水から赤潮プランクトンを分離回収する方法
において、赤潮状の原水を取水し、これに強磁性体微粒
子を添加し、該強磁性体微粒子が予め磁化されていれば
そのまま、磁化されていなければ上記の添加後に磁化し
、しかる後遠心分離することを管機とする赤潮の処理方
法。
In a method for separating and collecting red tide plankton from red tide raw water, red tide raw water is taken, ferromagnetic fine particles are added to it, and if the ferromagnetic fine particles are magnetized in advance, they must remain magnetized. For example, a method for treating red tide that uses a tube machine to magnetize after the above addition and then centrifuge it.
JP57109825A 1982-06-28 1982-06-28 Treatment of red tide Granted JPS594488A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57109825A JPS594488A (en) 1982-06-28 1982-06-28 Treatment of red tide

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57109825A JPS594488A (en) 1982-06-28 1982-06-28 Treatment of red tide

Publications (2)

Publication Number Publication Date
JPS594488A true JPS594488A (en) 1984-01-11
JPS625025B2 JPS625025B2 (en) 1987-02-03

Family

ID=14520162

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57109825A Granted JPS594488A (en) 1982-06-28 1982-06-28 Treatment of red tide

Country Status (1)

Country Link
JP (1) JPS594488A (en)

Also Published As

Publication number Publication date
JPS625025B2 (en) 1987-02-03

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