JP2982889B2 - Equipment for collecting ultrafine particles - Google Patents

Equipment for collecting ultrafine particles

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Publication number
JP2982889B2
JP2982889B2 JP25000694A JP25000694A JP2982889B2 JP 2982889 B2 JP2982889 B2 JP 2982889B2 JP 25000694 A JP25000694 A JP 25000694A JP 25000694 A JP25000694 A JP 25000694A JP 2982889 B2 JP2982889 B2 JP 2982889B2
Authority
JP
Japan
Prior art keywords
ultrafine particles
movable electrode
ultrafine
water tank
mud
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 - Fee Related
Application number
JP25000694A
Other languages
Japanese (ja)
Other versions
JPH0886188A (en
Inventor
光輝 炭田
武 川地
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.)
OOBAYASHIGUMI KK
Original Assignee
OOBAYASHIGUMI KK
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 OOBAYASHIGUMI KK filed Critical OOBAYASHIGUMI KK
Priority to JP25000694A priority Critical patent/JP2982889B2/en
Publication of JPH0886188A publication Critical patent/JPH0886188A/en
Application granted granted Critical
Publication of JP2982889B2 publication Critical patent/JP2982889B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、ベントナイト等の超微
粒子を泥水や濁水から回収する装置に係り、特に、泥水
掘削工法で発生した廃泥水中から超微粒子を回収する装
置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for recovering ultrafine particles such as bentonite from muddy water or turbid water, and more particularly to an apparatus for recovering ultrafine particles from waste mud generated by a mud drilling method.

【0002】[0002]

【従来の技術】地盤を掘削する方法として、連続地中壁
工法、場所打ち杭工法、泥水シールド工法等が知られて
いるが、これらの工法は、泥水を安定液として利用する
いわゆる泥水掘削工法であり、掘削孔内に泥水を満たす
ことによって掘削孔の崩壊を防止するものである。
2. Description of the Related Art A continuous underground wall method, a cast-in-place pile method, a mud shield method, and the like are known as methods for excavating the ground. These methods are so-called mud drilling methods using mud as a stable liquid. By filling the borehole with muddy water, the collapse of the borehole is prevented.

【0003】かかる工法で使用される代表的な泥水材料
としてベントナイトがある。ベントナイトは、モンモリ
ロナイトを主成分とした粘土鉱物であり、水中では表面
にマイナス電位を示して安定した懸濁液を作る。
[0003] Bentonite is a typical muddy water material used in such a method. Bentonite is a clay mineral containing montmorillonite as a main component, and exhibits a negative potential on the surface in water to form a stable suspension.

【0004】このような粘土粒子を含んだ泥水は、掘削
ずりとともにスラリ輸送によっていったん孔外へ排出さ
れるが、土砂分離装置やスクリューデカンタによってそ
れぞれ粗粒分、細粒分の土砂が取り除かれた後、再び掘
削孔内に戻され、循環使用される。
[0004] The muddy water containing such clay particles is once discharged out of the hole by slurry transport together with excavation shearing, and coarse and fine sediment are removed by a sediment separator and a screw decanter, respectively. After that, it is returned to the borehole again and used for circulation.

【0005】しかしながら、スクリューデカンタによっ
て分離可能な微粒子の大きさは、およそ10μm以上で
あって、これを下回る微粒子(超微粒子)は、除去され
ずに泥水中に増え続け、泥水を劣化させる一因となる。
However, the size of fine particles that can be separated by a screw decanter is about 10 μm or more, and fine particles (ultrafine particles) below this size are not removed and continue to increase in muddy water, which is one of the causes of deterioration of muddy water. Becomes

【0006】このため、循環使用によって劣化した泥水
は、凝集処理、ロールプレスやフィルタプレス等による
脱水処理等を経た後、廃棄物として搬出され、代わりに
新しい泥水が補給される。
For this reason, muddy water degraded by circulating use undergoes coagulation treatment, dehydration treatment by a roll press or filter press, etc., and is then carried out as waste, and new muddy water is supplied instead.

【0007】[0007]

【発明が解決しようとする課題】ここで、自然環境や生
態系を考慮すれば、廃棄物の量は、できるだけ少ない方
が望ましい。また、廃泥水中に含まれている超微粒子を
回収して再利用を図りたいという要請も高まっている。
また、このような超微粒子は、泥水掘削工法で生じる廃
泥水のみならず、採石工場で発生する濁水、コンクリー
ト用骨材等にも混入しており、超微粒子だけを分級して
回収することができれば、様々な用途に再利用できる途
が開ける。
Here, in consideration of the natural environment and ecosystem, it is desirable that the amount of waste is as small as possible. There is also a growing demand to collect and reuse ultrafine particles contained in waste mud.
In addition, such ultra-fine particles are mixed not only with waste mud generated by the mud drilling method, but also with turbid water generated at quarries, aggregate for concrete, etc., and it is possible to classify and collect only ultra-fine particles. If possible, it will be possible to reuse it for various purposes.

【0008】しかしながら、上述したようにスクリュー
デカンタを用いても10μm以下の超微粒子を分級する
ことは不可能であるため、かかる超微粒子を含む泥水や
濁水をやむをえず廃棄しているのが現状である。
However, as described above, it is impossible to classify ultrafine particles of 10 μm or less using a screw decanter, so that muddy water and turbid water containing such ultrafine particles are unavoidably discarded at present. is there.

【0009】本発明は、上述した事情を考慮してなされ
たもので、ベントナイト等の超微粒子を廃泥水等から回
収してこれを再利用することができる超微粒子を回収す
るための装置を提供することを目的とする。
The present invention has been made in view of the above circumstances, and provides an apparatus for recovering ultrafine particles such as bentonite from waste mud and the like, which can be reused. The purpose is to do.

【0010】[0010]

【課題を解決するための手段】上記目的を達成するた
め、本発明に係る超微粒子を回収するための装置は請求
項1に記載したように、ベントナイト等の超微粒子を含
む処理水が入れられる水槽内に固定電極をほぼ鉛直かつ
千鳥状に所定の間隔で配設するとともに該各固定電極の
間に無端ベルトとして構成された可動電極を対向配置し
てなる超微粒子分級装置と、前記可動電極に付着した超
微粒子を脱落させるために前記水槽の出口付近に設けら
れた機構と、該機構で脱落させた超微粒子を乾燥させる
乾燥機とからなるものである。
In order to achieve the above-mentioned object, an apparatus for recovering ultrafine particles according to the present invention contains treated water containing ultrafine particles such as bentonite. An ultrafine particle classifier in which fixed electrodes are arranged in a water tank in a substantially vertical and zigzag manner at predetermined intervals, and movable electrodes formed as endless belts are opposed to each other between the fixed electrodes; The mechanism comprises a mechanism provided near the outlet of the water tank for dropping the ultrafine particles attached to the water tank, and a dryer for drying the ultrafine particles dropped by the mechanism.

【0011】[0011]

【作用】本発明に係る超微粒子を回収するための装置に
おいては、超微粒子が含まれる処理水を水槽に入れた状
態で可動電極を循環させる。ここで、可動電極を直流電
源の正極側に接続し、固定電極を負極側に接続しておく
と、水槽内の可動電極と固定電極との間に懸濁するマイ
ナス電位の超微粒子は、電気泳動によって正極側である
可動電極に引き寄せられ、その表面に付着する。そし
て、可動電極は、その表面に超微粒子の付着塊を徐々に
成長させながら、固定電極の間を縫うようにして循環す
る。次に、水槽の出口付近に設けられた機構の作用によ
って可動電極に付着していた超微粒子を脱落させ、次い
で、機構で脱落させた超微粒子を乾燥機によって乾燥さ
せる。
In the apparatus for recovering ultrafine particles according to the present invention, the movable electrode is circulated while the treated water containing the ultrafine particles is placed in a water tank. Here, if the movable electrode is connected to the positive electrode side of the DC power supply and the fixed electrode is connected to the negative electrode side, ultra-fine particles of negative potential suspended between the movable electrode and the fixed electrode in the water tank will be electrically driven. It is attracted to the movable electrode on the positive electrode side by electrophoresis and adheres to the surface thereof. Then, the movable electrode circulates between the fixed electrodes while gradually growing an attached mass of ultrafine particles on the surface thereof. Next, the ultrafine particles attached to the movable electrode are dropped off by the action of a mechanism provided near the outlet of the water tank, and then the ultrafine particles dropped off by the mechanism are dried by a dryer.

【0012】乾燥の方法については、熱風加熱、伝熱加
熱、放射加熱、高周波加熱等の方式から適宜選択すれば
よい。
The drying method may be appropriately selected from methods such as hot air heating, heat transfer heating, radiant heating, and high frequency heating.

【0013】かくして回収された微粒子は、泥水工法の
作泥材料として再利用できるほか、陶磁器や耐火物の原
料あるいは鋳物砂、製紙添加物、各種充填剤等の用途に
再利用することができる。
The fine particles thus recovered can be reused as a mud making material in a muddy water method, and can also be reused as a raw material for porcelain and refractories, molding sand, papermaking additives, various fillers, and the like.

【0014】[0014]

【実施例】以下、本発明に係る超微粒子を回収するため
の装置の実施例について、添付図面を参照して説明す
る。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of an apparatus for recovering ultrafine particles according to the present invention will be described below with reference to the accompanying drawings.

【0015】図1は、本実施例に係る超微粒子を回収す
るための装置を示した概略図、図2は超微粒子回収方法
の手順を示したフローチャートである。図1でわかるよ
うに、本実施例に係る超微粒子を回収するための装置
は、ベントナイト等の超微粒子を含む処理水が入れられ
る水槽11内に固定電極12をほぼ鉛直かつ千鳥状に所
定の間隔で配設するとともに該各固定電極の間に無端ベ
ルトとして構成された可動電極13を対向配置してなる
超微粒子分級装置7と、可動電極13に付着した超微粒
子を振動やエアーの吹付け等によって脱落させるために
水槽11の出口付近に設けられた機構15と、該機構で
脱落させた超微粒子を乾燥させる乾燥機21とからな
る。
FIG. 1 is a schematic diagram showing an apparatus for recovering ultrafine particles according to this embodiment, and FIG. 2 is a flowchart showing a procedure of a method for recovering ultrafine particles. As can be seen from FIG. 1, the apparatus for recovering ultrafine particles according to the present embodiment is configured such that a fixed electrode 12 is substantially vertically and staggered in a water tank 11 in which treated water containing ultrafine particles such as bentonite is put. An ultrafine particle classifier 7 which is arranged at intervals and has a movable electrode 13 formed as an endless belt facing each other between the fixed electrodes, and an ultrafine particle attached to the movable electrode 13 is subjected to vibration or air blowing. The mechanism comprises a mechanism 15 provided near the outlet of the water tank 11 for dropping by ultra-fine particles and the like, and a dryer 21 for drying the ultrafine particles dropped by the mechanism.

【0016】本実施例に係る超微粒子を回収するための
装置においては、処理水として、連続地中壁工法で生じ
た廃泥水を用いる。連続地中壁工法においては、図1に
示すように、作泥装置1でつくられた泥水を掘削孔2に
満たしつつ掘削機3で掘削を行う一方、かかる泥水を掘
削ずりとともにスラリ輸送によっていったん孔外へ排出
し、土砂分離装置4で粗粒分を除去した後、沈砂槽5を
経て掘削孔2内に戻される。また、沈砂槽5に入れられ
た泥水はスクリューデカンタ6によって細粒分の土砂が
除去された後、沈砂槽5に戻して循環使用される。
In the apparatus for recovering ultrafine particles according to the present embodiment, waste mud generated by the continuous underground wall construction method is used as the treated water. In the continuous underground wall construction method, as shown in FIG. 1, while excavating with an excavator 3 while filling the excavation hole 2 with the mud created by the mud making apparatus 1, the mud is temporarily excavated by slurry transport together with the excavation. After being discharged out of the hole and coarse particles are removed by the sediment separator 4, it is returned to the excavation hole 2 through the sand settling tank 5. Further, the muddy water put in the sand settling tank 5 is returned to the sand setting tank 5 for circulating use after the fine sediment is removed by the screw decanter 6.

【0017】ここで、スクリューデカンタ6は、およそ
10μm程度の微粒子を除去するのが限界であり、これ
よりも小さな超微粒子は除去されずにオーバー泥水中に
含まれた状態でスクリューデカンタ6から出てくる。
Here, the screw decanter 6 has a limit of removing fine particles of about 10 μm, and ultrafine particles smaller than this are not removed and exit from the screw decanter 6 in a state of being contained in the over muddy water. Come.

【0018】そこで、本実施例では、図1の破線に示す
ようにスクリューデカンタ6のオーバー泥水を処理水と
して取り出す(図2、ステップ101)。なお、超微粒
子の濃度が高くなった泥水を沈砂槽5から取り出しても
よい。
Therefore, in this embodiment, as shown by the broken line in FIG. 1, the over muddy water of the screw decanter 6 is taken out as treated water (FIG. 2, step 101). In addition, the muddy water in which the concentration of the ultrafine particles is high may be taken out from the sand settling tank 5.

【0019】次いで、取り出された処理水を超微粒子分
級装置7に入れ、処理水中から超微粒子を分級する(ス
テップ102)。
Next, the extracted treated water is put into the ultra-fine particle classification device 7, and the ultra-fine particles are classified from the treated water (step 102).

【0020】ここで、超微粒子分級装置7の可動電極1
3は、水槽11の内外に多数配設されたスプロケット1
4に案内されて所定の駆動機構(図示せず)により図示
した矢印の方向に沿って水槽11の内外を循環するよう
になっている。また、固定電極12は、導電性材料で形
成された水槽11を介して直流電源のマイナス側に電気
的に接続してある。一方、可動電極13は、ブラシ等を
介して当該直流電源のプラス側に接続してある。
Here, the movable electrode 1 of the ultrafine particle classifier 7
3 is a large number of sprockets 1 arranged inside and outside the water tank 11.
4 and is circulated inside and outside the water tank 11 by a predetermined driving mechanism (not shown) in the direction of the arrow shown in the figure. The fixed electrode 12 is electrically connected to the negative side of the DC power supply via the water tank 11 formed of a conductive material. On the other hand, the movable electrode 13 is connected to the positive side of the DC power supply via a brush or the like.

【0021】[0021]

【0022】超微粒子分級装置7においては、水槽11
にスクリューデカンタ6からの処理水を入れた状態で可
動電極13をゆっくりと循環させる。ここで、可動電極
13は直流電源の正極側に接続され、固定電極12は負
極側に接続してあるので、水槽11内の可動電極13と
固定電極12との間に懸濁するマイナス電位の超微粒子
は、電気泳動によって正極側である可動電極13に引き
寄せられ、その表面に付着する。そして、可動電極13
は、その表面に超微粒子の付着塊を徐々に成長させなが
ら、固定電極12の間を縫うようにして循環する。
In the ultrafine particle classifier 7, the water tank 11
The movable electrode 13 is slowly circulated in a state in which the treated water from the screw decanter 6 is charged. Here, since the movable electrode 13 is connected to the positive electrode side of the DC power supply and the fixed electrode 12 is connected to the negative electrode side, the negative potential suspended between the movable electrode 13 and the fixed electrode 12 in the water tank 11 is The ultrafine particles are attracted to the movable electrode 13 on the positive electrode side by electrophoresis and adhere to the surface thereof. And the movable electrode 13
Circulates between the fixed electrodes 12 while gradually growing an attached mass of ultrafine particles on the surface thereof.

【0023】可動電極13が水槽11を出て機構15に
くると、当該機構15の作用によって可動電極13に付
着していた超微粒子が脱落する。
When the movable electrode 13 comes out of the water tank 11 and reaches the mechanism 15, the ultrafine particles attached to the movable electrode 13 fall off by the action of the mechanism 15.

【0024】次いで、図1の破線で示すように、機構1
5で脱落させた超微粒子を乾燥機21によって乾燥させ
る(ステップ103)。乾燥機21は、若干傾斜して回
転する円筒胴内に多数の水蒸気加熱管を配設してあり、
超微粒子を転動撹拌しながら熱風と伝導加熱によって乾
燥させることができるようになっている。
Next, as shown by the broken line in FIG.
The ultrafine particles dropped in step 5 are dried by the dryer 21 (step 103). The dryer 21 has a large number of steam heating tubes disposed in a cylindrical body that rotates slightly inclined.
The ultrafine particles can be dried by hot air and conduction heating while tumbling and stirring.

【0025】以上説明したように、本実施例に係る超微
粒子を回収するための装置によれば、廃泥水に含まれる
ベントナイト等の超微粒子を、まず電気泳動によって分
級し、次いでこれを熱風加熱等によって乾燥させること
により、廃泥水から回収するように構成したので、従来
廃棄するしかなかった泥水の量を相当量低減することが
できる。
As described above, according to the apparatus for recovering ultrafine particles according to the present embodiment, ultrafine particles such as bentonite contained in waste mud are first classified by electrophoresis and then heated with hot air. Since it is configured to be recovered from the waste mud by drying by the method such as the above, it is possible to considerably reduce the amount of the mud which has conventionally only been discarded.

【0026】また、回収された超微粒子は、再び泥水工
法の作泥材料として再利用することができるほか、れん
が、瓦等の耐火物の原料あるいは陶磁器用の高級な粘土
材料として有効利用することもできる。また、鋳物砂、
製紙添加物、各種充填剤等の用途に再利用することもで
きる。
The recovered ultrafine particles can be reused again as a mud material for a muddy water method, and can be effectively used as a raw material for refractories such as bricks and tiles or a high-grade clay material for ceramics. Can also. Also, foundry sand,
It can also be reused for applications such as papermaking additives and various fillers.

【0027】本実施例では、処理水として連続地中壁工
法で生じた廃棄泥水を用いたが、泥水シールド工法等、
他の泥水掘削工法で生じた廃泥水を利用できることはい
うまでもなく、採石場等で生じた濁水を用いてもよい。
また、コンクリートの骨材を洗浄する際、当該骨材に混
入している粘土微粒子を回収するのに用いてもよい。
In this embodiment, waste mud generated by the continuous underground wall method is used as the treated water.
Needless to say, waste mud generated by other mud drilling methods can be used, and turbid water generated at a quarry or the like may be used.
Moreover, when washing the aggregate of concrete, you may use it for collect | recovering the clay fine particle mixed in the said aggregate.

【0028】また、使用済みの鋳物砂をいったん粉砕
し、これをスラリー状にする等、あらたに処理水を作成
するようにしてもよい。
Further, the used casting sand may be once crushed and then slurried to prepare treated water.

【0029】また、本実施例では、熱風と伝熱の両方の
作用によって超微粒子を乾燥可能な乾燥機を用いたが、
かかる方式に限定されるものではなく、熱風による加
熱、伝熱による加熱、赤外線を用いた放射加熱あるいは
高周波(電磁波)を用いた加熱等のさまざまな乾燥方式
から適宜選択すればよい。また、乾燥工程を減圧下で行
ってもよい。
In this embodiment, a dryer capable of drying ultrafine particles by both the action of hot air and heat transfer is used.
The drying method is not limited to such a method, and may be appropriately selected from various drying methods such as heating by hot air, heating by heat transfer, radiant heating using infrared rays, or heating using high frequency (electromagnetic waves). Further, the drying step may be performed under reduced pressure.

【0030】また、本実施例では、可動電極に付着した
超微粒子を振動や吹き飛ばしによって当該可動電極から
脱落させるようにしたが、電極反転によってこれを脱落
させるように構成してもよい。
Further, in the present embodiment, the ultrafine particles attached to the movable electrode are dropped from the movable electrode by vibration or blow-off. However, the ultrafine particles may be dropped by electrode inversion.

【0031】[0031]

【発明の効果】以上述べたように、本発明に係る超微粒
子を回収するための装置によれば、ベントナイト等の超
微粒子を廃泥水等から回収してこれを再利用することが
できる。
As described above, according to the apparatus for recovering ultrafine particles according to the present invention, ultrafine particles such as bentonite can be recovered from waste muddy water and reused.

【0032】[0032]

【図面の簡単な説明】[Brief description of the drawings]

【図1】本実施例に係る超微粒子を回収するための装置
を示した概略図。
FIG. 1 is a schematic diagram showing an apparatus for collecting ultrafine particles according to the present embodiment.

【図2】本実施例に係る超微粒子を回収するための装置
を用いた超微粒子回収の手順を示したフローチャート。
FIG. 2 is a flowchart showing the procedure of ultra-fine particle recovery using the apparatus for recovering ultra-fine particles according to the present embodiment.

【符号の説明】[Explanation of symbols]

7 超微粒子分級装置 21 乾燥機 102 分級工程 103 乾燥工程 7 Ultrafine particle classifier 21 Dryer 102 Classification process 103 Drying process

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.6,DB名) E21D 9/06 301 B01D 57/02 ──────────────────────────────────────────────────続 き Continued on front page (58) Field surveyed (Int.Cl. 6 , DB name) E21D 9/06 301 B01D 57/02

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 ベントナイト等の超微粒子を含む処理水
が入れられる水槽内に固定電極をほぼ鉛直かつ千鳥状に
所定の間隔で配設するとともに該各固定電極の間に無端
ベルトとして構成された可動電極を対向配置してなる超
微粒子分級装置と、前記可動電極に付着した超微粒子を
脱落させるために前記水槽の出口付近に設けられた機構
と、該機構で脱落させた超微粒子を乾燥させる乾燥機と
からなることを特徴とする超微粒子を回収するための装
置。
1. A fixed electrode is disposed substantially vertically and in a staggered manner at a predetermined interval in a water tank containing treated water containing ultrafine particles such as bentonite, and an endless belt is formed between the fixed electrodes. An ultrafine particle classifier having a movable electrode opposed thereto, a mechanism provided near the outlet of the water tank for dropping the ultrafine particles attached to the movable electrode, and drying the ultrafine particles dropped by the mechanism. An apparatus for recovering ultrafine particles, comprising a dryer.
JP25000694A 1994-09-19 1994-09-19 Equipment for collecting ultrafine particles Expired - Fee Related JP2982889B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP25000694A JP2982889B2 (en) 1994-09-19 1994-09-19 Equipment for collecting ultrafine particles

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP25000694A JP2982889B2 (en) 1994-09-19 1994-09-19 Equipment for collecting ultrafine particles

Publications (2)

Publication Number Publication Date
JPH0886188A JPH0886188A (en) 1996-04-02
JP2982889B2 true JP2982889B2 (en) 1999-11-29

Family

ID=17201450

Family Applications (1)

Application Number Title Priority Date Filing Date
JP25000694A Expired - Fee Related JP2982889B2 (en) 1994-09-19 1994-09-19 Equipment for collecting ultrafine particles

Country Status (1)

Country Link
JP (1) JP2982889B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2011007820A1 (en) * 2009-07-15 2011-01-20 国立大学法人名古屋工業大学 Particle recovery method and particle recovery apparatus

Also Published As

Publication number Publication date
JPH0886188A (en) 1996-04-02

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