JPH08131720A - Method and apparatus for concentrating muddy water - Google Patents
Method and apparatus for concentrating muddy waterInfo
- Publication number
- JPH08131720A JPH08131720A JP6273358A JP27335894A JPH08131720A JP H08131720 A JPH08131720 A JP H08131720A JP 6273358 A JP6273358 A JP 6273358A JP 27335894 A JP27335894 A JP 27335894A JP H08131720 A JPH08131720 A JP H08131720A
- Authority
- JP
- Japan
- Prior art keywords
- water
- muddy water
- filtrate
- passage
- concentrating
- 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
Links
Landscapes
- Filtering Materials (AREA)
- Filtration Of Liquid (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、河川湖沼等自然界にお
ける泥水等、又は産業活動によって生ずる低濃度の泥水
等を、沈殿槽や固形分分離装置等に導入する前に予備処
理的に中程度の濃度まで簡易に濃縮する方法及びその装
置の改善に関する。[Field of Industrial Application] The present invention is a preliminary treatment of mud in nature such as rivers and lakes, or mud of low concentration generated by industrial activities, before introducing it into a sedimentation tank or a solid content separation device. The present invention relates to a method for simply concentrating to a concentration of 1 and improvement of the apparatus.
【0002】[0002]
【従来の技術】本発明者らはさきに固形分3〜5%程度
を含む低濃度の泥水を筒状布帛内を通過させ泥水から連
続的に濾液を浸出させ、低濃度泥水を高濃度泥水にし、
濃縮によって泥水の量を減少し、泥水のハンドリングを
容易にする技術を開発した(特願平6−95195号出
願)。2. Description of the Related Art The present inventors previously passed a low-concentration muddy water containing a solid content of about 3 to 5% through a tubular cloth to continuously leach the filtrate from the muddy water to transform the low-concentration muddy water into a high-concentration muddy water. West,
We have developed a technology to reduce the amount of muddy water by concentration and facilitate handling of muddy water (Japanese Patent Application No. 6-95195).
【0003】その技術は、浸透性壁を有する筒状布帛か
らなる通水路内に泥水を通水し、この浸透性壁から濾液
を通水路外に浸出させ、通路内の泥水の濃度を高めるこ
とを特徴とする泥水の濃縮方法である。この通水路を濾
液タンク中に浸漬しておくと、通水を停止した場合、筒
状布帛の壁を浸透して通水路内に濾液が逆に侵入し、通
水路内の泥水の濃度が低くなり、通水路内で固形分によ
る閉塞が生じない。The technique is to increase the concentration of muddy water in a passage by passing muddy water through a water passage made of a tubular cloth having a permeable wall and allowing the filtrate to leach out of the water passage through the permeable wall. Is a method of concentrating muddy water. If this water passage is immersed in the filtrate tank, if the water passage is stopped, it penetrates through the wall of the tubular fabric and the filtrate enters the water passage in the opposite direction, and the concentration of muddy water in the water passage becomes low. Therefore, clogging due to solid content does not occur in the water passage.
【0004】その装置は、筒状布帛からなる通水路を濾
液タンク内に水没させ、この通水路に泥水を通水させる
ポンプを備えている。The apparatus is provided with a pump for submerging a water passage made of a tubular cloth in the filtrate tank and for passing muddy water through the water passage.
【0005】[0005]
【発明が解決しようとする課題】この装置では、上記の
ように、筒状布帛の内壁に泥分などによる閉塞は生じな
いとはいうものの、筒状布帛の内壁に泥分などの固形分
が堆積する傾向があることは避けることができない。そ
こでこの泥分の堆積を積極的に除去することが好まし
い。In this device, although it is said that the inner wall of the tubular cloth is not clogged by mud or the like as described above, the inner wall of the tubular cloth is not covered by solid matter such as mud. The tendency to deposit is unavoidable. Therefore, it is preferable to positively remove the accumulation of mud.
【0006】本発明は上記技術の改良に関するもので、
筒状布帛の内面に付着する泥分を剥離させ、又は、堆積
を防止し、泥水処理能力の低下を防止する技術を提供す
ることを目的とする。本発明の別の目的は、筒状布帛か
ら浸出した清水中に含まれる微量の泥分をさらに沈降除
去する装置を提供することにある。The present invention relates to an improvement of the above technique,
It is an object of the present invention to provide a technique for peeling off mud adhered to the inner surface of a tubular cloth or preventing accumulation of the mud, thereby preventing a decrease in muddy water treatment capacity. Another object of the present invention is to provide an apparatus for further sedimenting and removing a minute amount of mud contained in clear water leached from a tubular cloth.
【0007】[0007]
【課題を解決するための手段】本発明は、浸透性壁を有
する筒状布帛から成る通水路内に泥水を通水し、この浸
透性壁から濾液を通水路外に浸出させ、通路内の泥水の
濃度を高める泥水の濃縮方法において、筒状布帛の外面
側を内面側より高圧にする加圧工程を設けたことを特徴
とする泥水の濃縮方法である。この加圧工程を設けるこ
とにより、筒状布帛からなる通水路内面に付着した泥分
を除去することができる。この方法を好適に実施するこ
とができる装置は、濾液タンク内に水没した筒状布帛か
らなる通水路と、この通水路に泥水を通水させるポンプ
とを備えた泥水の濃縮装置であって、濾液タンクを密閉
自在な構造にすると共に濾液タンク内に加圧媒体を供給
する供給口を設けたことを特徴とする泥水の濃縮装置で
ある。ここで、加圧媒体としては例えば圧縮空気又は高
圧水等を用いることができる。この濃縮装置では、筒状
布帛として合成繊維糸をたて糸に、針金又は剛直な線状
体と合成繊維糸とを横糸として交互に織り込んで織成し
た筒状布帛を用いれば、加圧工程において筒状布帛が断
面を円形に保ち、つぶれないので好適である。さらに、
この筒状布帛の構造は、泥水圧に対して耐圧性のたて糸
および横糸を織成した筒状体の内側に、たて糸および横
糸に合成繊維のマルチフィラメントを用いて密に織成し
た筒状体を内嵌させた構造の筒状布帛を用いてもよい。
なお、泥水圧力の低いときには内筒だけでも用いること
ができる。According to the present invention, muddy water is passed through a water passage made of a tubular fabric having a permeable wall, and the filtrate is leached out of the water passage from the permeable wall to prevent the passage of the water inside the passage. In the method of concentrating muddy water, the method of concentrating muddy water is characterized in that a pressure step of making the outer surface side of the tubular cloth higher than the inner surface side is provided. By providing this pressurizing step, it is possible to remove the mud adhered to the inner surface of the water passage made of the tubular cloth. A device capable of suitably carrying out this method is a muddy water concentrating device comprising a water passage made of a tubular cloth submerged in a filtrate tank, and a pump for making muddy water pass through this water passage, It is a device for concentrating muddy water, characterized in that the filtrate tank has a structure capable of being sealed, and a supply port for supplying a pressurized medium is provided in the filtrate tank. Here, for example, compressed air or high-pressure water can be used as the pressurizing medium. In this concentrating device, if a tubular cloth that is woven by alternately weaving a synthetic fiber thread into a warp thread and a wire or a rigid linear body and a synthetic fiber thread as a weft is used as the tubular cloth It is preferable because the cloth keeps its cross section circular and does not collapse. further,
The structure of this tubular fabric is such that inside a tubular body woven of warp threads and weft threads that is resistant to mud pressure, a densely woven tubular body is prepared by using multifilaments of synthetic fibers for the warp threads and weft threads. A tubular cloth having a fitted structure may be used.
When the muddy water pressure is low, the inner cylinder alone can be used.
【0008】次に、本発明の泥水の濃縮方法において、
固形分の堆積を防止する手段として泥水とともに空気泡
を筒状布帛内に送入することを特徴とする泥水の濃縮方
法を提供する。この方法を実現する装置は上記泥水の濃
縮装置において、ポンプの出口側の通水路に空気吹き込
み装置を備えたことを特徴とする泥水の濃縮装置であ
る。空気吹き込み装置としては、圧縮空気を吹き込むノ
ズルを通水路に設けるとよい。Next, in the muddy water concentrating method of the present invention,
Provided is a method for concentrating muddy water, which comprises feeding air bubbles together with muddy water into a tubular cloth as a means for preventing the accumulation of solids. An apparatus for realizing this method is the above-mentioned muddy water concentrating apparatus, characterized in that an air blowing device is provided in the water passage on the outlet side of the pump. As the air blowing device, a nozzle for blowing compressed air may be provided in the water passage.
【0009】次に別の方法は、濾液タンク内に浸漬し浸
透性壁を有する通水路内に泥水を通水し、この浸透性壁
から濾液を濾液タンク内に浸出させ、通水路内の泥水の
濃度を高める泥水の濃縮方法において、通水路又は濾液
に振動を付与することを特徴とする泥水の濃縮方法であ
る。この方法を実施する装置は、上記泥水の濃縮装置に
おいて、濾液タンク内の濾液中に浸漬するバイブレータ
を備えたことを特徴とする泥水の濃縮装置である。バイ
ブレータは、筒状布帛に取付けて筒状布帛に振動を与え
るものでもよく、また、筒状布帛に接触させることなく
濾液タンク内の濾液中に浸漬して、清水に振動を付与す
るものでもよい。Next, another method is to immerse the muddy water in a water passage having a permeable wall by immersing it in the filtrate tank, to leach the filtrate from the permeable wall into the filtrate tank, and to make the muddy water in the water passage. In the method of concentrating muddy water for increasing the concentration of, the method for concentrating muddy water is characterized by applying vibration to a water passage or a filtrate. An apparatus for carrying out this method is the above-mentioned muddy water concentrating apparatus, which is equipped with a vibrator immersed in the filtrate in the filtrate tank. The vibrator may be attached to a tubular cloth to give vibration to the tubular cloth, or it may be immersed in the filtrate in the filtrate tank without contacting the tubular cloth to give vibration to fresh water. .
【0010】また、本発明の別の手段は、浸透性壁を有
する通水路内に泥水を通水し、この浸透性壁から濾液を
通水路外に浸出させ、通路内の泥水の濃度を高める泥水
の濃縮方法において、泥水の流れに脉動を与えることを
特徴とする泥水の濃縮方法である。脈動を与える手段と
しては脈動発生装置を通水路に取付けることでもよく、
また、ポンプの出口側に設けた通水路のバルブを急速に
開閉する装置を取付けてもよい。Another means of the present invention is to pass mud water through a water passage having a permeable wall and allow the filtrate to leach out of the water passage from the permeable wall to increase the concentration of the mud water in the passage. A method for concentrating muddy water, which comprises fluctuating the flow of muddy water. As a means for giving pulsation, a pulsation generator may be attached to the water passage,
A device for rapidly opening and closing the valve of the water passage provided on the outlet side of the pump may be attached.
【0011】次に、上記の泥水を濃縮する装置におい
て、筒状布帛から浸出した濾液中に含まれる微量の泥分
をさらに沈降除去する装置として、濾液タンクに濾液が
低速で上昇する空間を設け、濾液タンクの上部より濾液
をオーバーフローさせると共に前記空間内に傾斜板を配
設し、濾液タンク底部に排泥口を備えたことを特徴とす
る泥水の濃縮装置を提供する。Next, in the above-mentioned device for concentrating muddy water, as a device for further sedimenting and removing a small amount of mud contained in the filtrate leached from the tubular cloth, a space in which the filtrate rises at a low speed is provided in the filtrate tank. Provided is a mud concentrating device, characterized in that a filtrate is overflowed from an upper portion of a filtrate tank, an inclined plate is arranged in the space, and a mud discharge port is provided at a bottom portion of the filtrate tank.
【0012】[0012]
【作用】本発明は、浸透性壁を有する通水路内に泥水を
通水することによって、浸透性壁から濾液を通水路外に
浸出させ、通水路内の泥水の濃度を高め、比較的低濃度
の泥水を濃縮する技術の改善に係るもので、筒状布帛の
内面に固形物が付着して濃縮性能が低下するのを防止す
る。具体的な手段としては、筒状布帛に圧力流体による
外圧を加えて濾液を逆浸透させて筒状布帛の内面の固形
物を除去する手段、筒状布帛内に空気泡を吹き込んで泥
水に撹拌を与えることにより固形物の附着を防止する手
段、筒状布帛を機械的に振動させて固形物の附着を防止
する手段、筒状布帛内の流れに脈動を与える手段等を採
用する。According to the present invention, the mud water is passed through the water passage having the permeable wall so that the filtrate can be leached out of the water passage through the permeable wall to increase the concentration of the mud water in the water passage, thereby reducing the water concentration to a relatively low level. The present invention relates to an improvement in the technique for concentrating concentrated mud water, and prevents solid substances from adhering to the inner surface of a tubular fabric and degrading the concentration performance. Specific means include applying external pressure from a pressure fluid to the tubular fabric to reversely permeate the filtrate to remove solid matter on the inner surface of the tubular fabric, blowing air bubbles into the tubular fabric and stirring it in muddy water. Means for preventing sticking of solids by applying a pressure, means for mechanically vibrating the tubular cloth to prevent sticking of solids, means for pulsating the flow in the tubular cloth, and the like.
【0013】また、本発明の装置は上記手段を実現する
加圧装置、空気吹き込み装置、バイブレータ、脈動発生
装置を備えることにより、筒状布帛の詰り等の問題を完
全に解決する。脈動発生装置として、通水路の泥水入口
のバルブを急に開閉する装置により、筒状布帛内に圧力
変動を起こすことができ、ウォーターハンマーに類似す
るような現象によって、筒状布帛内面に付着している泥
土が洗い流される。Further, the apparatus of the present invention is provided with a pressurizing device, an air blowing device, a vibrator, and a pulsation generating device which realize the above means, thereby completely solving the problems such as clogging of the tubular cloth. As a pulsation generator, a device that suddenly opens and closes the valve at the muddy water inlet of the water passage can cause pressure fluctuations inside the tubular fabric, and due to a phenomenon similar to a water hammer, it adheres to the inner surface of the tubular fabric. Muddy soil is washed away.
【0014】一方、濾液タンクに濾液が低速で上昇する
空間を設け、濾液タンクの上部より濾液をオーバーフロ
ーさせると共にこの空間内に傾斜板を配設し、微粒の固
形分粒子を傾斜板に沿って沈降させ濾液タンク底部に排
泥口を備えることにより、濾液中に少量の微粒の泥土が
含まれた場合でも、この泥土がタンク内で沈降し、濾液
は清浄水となってタンク外に排出される。On the other hand, a space in which the filtrate rises at a low speed is provided in the filtrate tank, the filtrate is overflowed from the upper part of the filtrate tank, and an inclined plate is arranged in this space, and fine solid particles are distributed along the inclined plate. Even if a small amount of fine mud is included in the filtrate, the mud is settled in the tank and the filtrate becomes clean water and is discharged to the outside of the tank. It
【0015】[0015]
【実施例】図1に本発明の実施例装置の(a)平面図、
(b)側面図を示した。ポンプ2は、泥水を管5、バル
ブ11を経て吸入し、これをバルブ12、管7を通っ
て、濾液タンク3内の筒状布帛22内に連続的に圧送す
る。圧送された泥水は、筒状布帛22の浸透性壁から濾
液が濾液タンク3内に排水され、泥水自身は濃縮され
て、管4を経て泥水タンクに還流するか又は次の工程に
送られる。濾液は濾液タンク3からオーバーフローす
る。泥水を濃縮する通常運転時には、バルブ11、12
は開、バルブ13、14は閉とする。1 is a plan view of an apparatus according to an embodiment of the present invention, FIG.
(B) The side view was shown. The pump 2 sucks muddy water through the pipe 5 and the valve 11, and continuously pumps the muddy water into the tubular cloth 22 in the filtrate tank 3 through the valve 12 and the pipe 7. The pressure-fed mud water is filtrated from the permeable wall of the tubular cloth 22 into the filtrate tank 3, and the mud water itself is concentrated and returned to the mud water tank via the pipe 4 or sent to the next step. The filtrate overflows from the filtrate tank 3. During normal operation of concentrating muddy water, valves 11 and 12
Is open and valves 13 and 14 are closed.
【0016】濾液タンク3内には、筒状布帛22が多重
螺旋状に収納されている。濾液タンクの外壁21の内側
に格子状の壁をもつ網目円筒23が内装されており、筒
状布帛22が濾液タンクの壁に密着して濾布面積が縮小
するのを防止するようになっている。筒状布帛22の壁
を通過した微粒子は濾液タンク3の下部のホッパ状円錐
筒9内に沈降堆積する。堆積した微粒子はポンプ2によ
り再濃縮するか又は貯泥する。再濃縮する場合は、バル
ブ11、14を閉、バルブ12、13を開にして行う。
貯泥する場合は、バルブ11、12を閉、バルブ13、
14を開にして行う。 〔実施例−1〕上記装置において、筒状布帛22として
は、従来、たて糸20番手のポリエステル紡績糸を4本
寄り合わせた糸条を424本使用し、よこ糸として15
00dのポリエステル長繊維糸を4本撚合せした糸条
(打込み数10cm当たり30本)を用い、平織りにし
た口径25mmの円筒体を用いていた。A tubular cloth 22 is housed in the filtrate tank 3 in a multiple spiral shape. A mesh cylinder 23 having a lattice-shaped wall is provided inside the outer wall 21 of the filtrate tank, and the tubular cloth 22 is prevented from adhering to the wall of the filtrate tank and reducing the filter cloth area. There is. The fine particles that have passed through the wall of the tubular cloth 22 settle and accumulate in the hopper-shaped conical cylinder 9 below the filtrate tank 3. The accumulated fine particles are re-concentrated by the pump 2 or stored. When reconcentrating, the valves 11 and 14 are closed and the valves 12 and 13 are opened.
When storing mud, close valves 11 and 12, valve 13,
Open with 14. [Example-1] In the above-mentioned apparatus, as the tubular cloth 22, 424 yarns in which four polyester spun yarns having a warp yarn count of 20 are conventionally used are used.
A cylindrical body having a diameter of 25 mm, which was plain-woven, was used by using a yarn in which four polyester long fiber yarns of 00d were twisted (30 yarns per 10 cm of the number of threads).
【0017】本発明の実施例としては、合成繊維糸をた
て糸に、針金又は剛直な線状体と合成繊維糸とを横糸と
して交互に織り込んで織成した筒状布帛を用いた。具体
的には、次のとおりである。 (1)図2に実施例の筒状布帛の織物構造を例示した。
図2(a)は平面図、図2(b)は側面図である。図2
において、たて糸61として20番手のポリエステル紡
績糸を4本寄り合わせた糸条を424本使用し、よこ糸
63として1500デニール(d)のポリエステル長繊
維を4本撚合せした糸条(打込み数10cm当たり26
本)を用い、さらによこ糸である線状体62として97
50dのナイロンモノフィラメント(打込み数10cm
当たり26本)を用いた。そして図2に示すように、上
記たて糸61(61a、61b)とよこ糸63および線
状体62とを平織りに交織した。このように織成した口
径25mmの円筒体からなる筒状布帛である。As an embodiment of the present invention, a tubular fabric is used in which a synthetic fiber yarn is woven by alternately weaving a wire or a rigid linear body and a synthetic fiber yarn into a warp yarn as a weft yarn. Specifically, it is as follows. (1) FIG. 2 illustrates the woven structure of the tubular cloth of the example.
2A is a plan view and FIG. 2B is a side view. Figure 2
In the above, as the warp yarn 61, 424 yarns in which four 20th count polyester spun yarns are twisted together are used, and as the weft yarns 63, four yarns of 1500 denier (d) polyester long fibers are twisted (per 10 cm of driving number). 26
97) as a linear body 62 which is a weft thread.
50d nylon monofilament
26 pieces were used. Then, as shown in FIG. 2, the warp yarn 61 (61a, 61b), the weft yarn 63, and the linear body 62 were woven in a plain weave. It is a tubular cloth made of a cylindrical body having a diameter of 25 mm woven in this way.
【0018】(2)図3に実施例の筒状布帛の織物構造
を例示した。図3(a)は平面図、図3(b)は側面図
である。たて糸61として20番手のポリエステル紡績
糸を4本寄り合わせた糸条を424本使用し、よこ糸6
3として1500デニール(d)のポリエステル長繊維
を4本撚合せした糸条(打込み数10cm当たり28
本)及び線状体64として直径1.5mmの鋼線(打込
み数10cm当たり28本)を用い、上記たて糸61と
よこ糸63および線状体64とを、図3に示すように、
2分の1綾織りに交織した。このような構造の布帛を口
径25mmの円筒体に成形した筒状布帛である。(2) FIG. 3 illustrates the woven structure of the tubular cloth of the embodiment. 3A is a plan view and FIG. 3B is a side view. As the warp yarn 61, 424 yarns in which four 20th count polyester spun yarns are put together are used.
The number of yarns obtained by twisting four polyester filaments of 1500 denier (d) as 3 (28 per 10 cm of the number of driving)
3) and a steel wire having a diameter of 1.5 mm (28 wires per 10 cm of the number of threads) as the linear body 64 and the warp thread 61, the weft thread 63, and the linear body 64, as shown in FIG.
Weaved in a half twill weave. It is a tubular cloth formed by forming the cloth having such a structure into a cylindrical body having a diameter of 25 mm.
【0019】(3)また、別の実施例としては、たて糸
61にポリエステル長繊維1100d/2×2×104
本を用い、よこ糸63にポリエステル繊維1100d/
5×27本/10cm、線状体62としてナイロンフィ
ラメント9750d×27本/10cmで織布した筒状
体の内部に、直径40μmのポリエステルのマルチフィ
ラメントをたて糸及びよこ糸に使用し、1cm当たり1
00本使用して、織布した筒状体構造の円筒体である。(3) In another embodiment, the warp yarn 61 is made of polyester filament 1100d / 2 × 2 × 104.
Using a book, weft 63 polyester fiber 1100d /
5 × 27 filaments / 10 cm, linear filaments of nylon filament 9750 d × 27 filaments / 10 cm were woven into a tubular body, and a polyester multifilament with a diameter of 40 μm was used for warp and weft threads.
It is a cylindrical body having a tubular body structure which is woven by using 00 pieces.
【0020】次の条件で泥水の脱水試験を行った。 泥水条件 泥土:ミクロサンド−D(シリカ分を主成分としたパウ
ダに無機質成分を加え材料分離をなくした粒度ほぼ74
μm以下の市販材料) 比重:1.06 流量:60リットル/min 泥水圧:0.8kg/cm2 筒状布帛A: たて糸:20番手のポリエステル紡績糸を4本より合わ
せた糸条(20/4)を424本。よこ糸:1500デ
ニールのポリエステル長繊維を4本より合わせた糸条
(打ち込み数10cm当り28本)。A muddy water dehydration test was conducted under the following conditions. Mud conditions Mud: Micro Sand-D (Particle size of 74 with powder composed mainly of silica with inorganic components added to eliminate material separation)
Commercially available material of μm or less) Specific gravity: 1.06 Flow rate: 60 liters / min Mud pressure: 0.8 kg / cm 2 Cylindrical fabric A: Warp yarn: A yarn formed by combining four polyester spun yarns of 20 count (20 / 4) 424. Weft yarn: A yarn in which four polyester filaments of 1500 denier are combined (28 yarns per 10 cm).
【0021】筒状布帛B: たて糸:20/6×2×129本。よこ糸:1500d
/1×60本。 口径25mmφの筒状布帛A,Bそれぞれ10mを水中
に浸漬し2時間泥水を通水した。1分間当りの脱水量は
5.4〜2.1リットル/minに漸次低下したが、筒
状布帛Bは筒状布帛Aより10〜20%脱水量が多かっ
た。また2時間経過後0.5kg/cm2 の水圧を筒状
布帛の外部に10分間かけ、再度試験を行ったところ、
当初能力の約90%の脱水能力に回復した。Cylindrical fabric B: Warp yarn: 20/6 × 2 × 129 yarns. Weft: 1500d
/ 1 x 60 pieces. 10 m of each of the tubular fabrics A and B having a diameter of 25 mmφ was immersed in water to pass mud water for 2 hours. The dehydration amount per minute gradually decreased to 5.4 to 2.1 liters / min, but the tubular fabric B had a 10 to 20% more dehydration amount than the tubular fabric A. After 2 hours, a water pressure of 0.5 kg / cm 2 was applied to the outside of the tubular fabric for 10 minutes, and the test was conducted again.
The dehydration capacity was restored to about 90% of the initial capacity.
【0022】また上記泥水条件でモノフィラメントのネ
ット状の筒状布帛について試験を行ったところ表1に示
すように開目86μmまでは筒状布帛を通って濾液が脱
水していたが、開目が114μm以上では筒状布帛から
全水漏れを生じた。これは、ミクロンサンドがほぼ74
μm以下なので開目を通り抜けることによるものと考え
られる。When the monofilament net-shaped tubular cloth was tested under the above-mentioned muddy water conditions, as shown in Table 1, the filtrate was dehydrated through the tubular cloth up to the opening of 86 μm. At 114 μm or more, total water leakage occurred from the tubular cloth. This is about 74 microns
Since it is less than μm, it is thought to be due to passing through the opening.
【0023】[0023]
【表1】 [Table 1]
【0024】〔実施例−2〕実施例装置は濾液タンク3
に密閉蓋31を設けて濾液タンク3を密閉できるように
し、濾液タンク3内に圧力媒体を供給して加圧できるよ
うになっている。筒状布帛内に泥水を圧送循環させる
と、経過時間にともない筒状布帛内面に泥が付着し、脱
水量が減少してくる。この時点でポンプ2の運転を一時
停止して、泥水の通水を停止させ、濾液のオーバーフロ
ー管34、36に設けたバルブ35を閉止し、加圧媒体
導入管32のバルブ33を開き、タンク内の水に圧力を
一定時間かける。加圧媒体としては、圧縮空気、圧力水
等を用いることができる。[Embodiment 2] The apparatus of the embodiment is a filtrate tank 3
A sealing lid 31 is provided on the filter tank 3 so that the filtrate tank 3 can be sealed, and a pressure medium can be supplied into the filtrate tank 3 for pressurization. When the muddy water is pumped and circulated in the tubular cloth, the mud adheres to the inner surface of the tubular cloth with the passage of time and the amount of dehydration decreases. At this time, the operation of the pump 2 is temporarily stopped to stop the passage of muddy water, the valve 35 provided in the filtrate overflow pipes 34, 36 is closed, the valve 33 of the pressurized medium introduction pipe 32 is opened, and the tank is closed. Apply pressure to the water inside for a certain period of time. As the pressurizing medium, compressed air, pressurized water or the like can be used.
【0025】濾液タンク3内の水は筒状布帛22の壁を
通ってその内部に浸透し、筒状布帛22の内壁に付着し
ている固形分を除去し、筒状布帛内の水は管4を通って
図示しない泥水タンクに排出される。次いで加圧媒体導
入管32のバルブ33を閉止し、バルブ35を開放し、
次いでポンプ2を再運転する。たて糸として20番手の
ポリエステル紡績糸を6本より合わせた糸を2本引き揃
えた糸状を324本使用し、よこ糸として1000dの
ポリエステル長繊維を4本より合わせた糸状(打ち込み
数10cm当たり50本)を用いた筒状布帛(芦森工業
株式会社製のエーワンホース)で、直径65mmφ、長
さ10mを濾液タンク中にスパイラル状に埋没した実施
例装置を用い、原泥水比重1.1のボーリング掘削水を
濃縮した。泥水流量は135リットル/min、泥水圧
力1.3〜1.4kg/cm2 で濃縮した。この時濾液
は、8リットル/min、脱水効率(対全濾液)約6%
で推移した。濾液の濁度は約1時間は20〜40mg/
lであったが、その後1〜2mg/lとなった。約30
時間経過した時、濾液量は次第に低下し、約50時間後
には5リットル/minまで低下した。そこで、ポンプ
を一時停止し、濾液タンクに蓋を取付け、濾液タンク内
に圧力2kg/cm 2 の圧力水を2時間注入した。その
後、再びポンプを運転し泥水の循環濃縮を行った。濾液
量は7リットル/minに復活した。 〔実施例−3〕図1に示すように、ポンプ2の吐出管7
に空気吹き込み管41を取付け、泥水中に空気泡を吹き
込むようにした。実施例−2と同様の装置を用いて、原
泥水比重1.1のボーリング掘削水を濃縮した。泥水流
量は155リットル/min、泥水圧力1.35〜1.
4kg/cm2 で濃縮しながら、2kg/cm2 の空気
を注入した。この時濾液は、8.5〜11リットル/m
in、脱水効率(対全濾液)約5.3〜7.3%で推移
した。濾液の量が変動が大きくまた濾液の濁度がが、頭
初140mg/lと高かったが、約1時間経過後、35
〜40mg/lに低下した。約20時間後に濾液の量が
4リットル/minまで低下したので空気泡吹き込み運
転を停止した。空気泡吹き込みは、濾液の濁度がやや高
いが処理量が増加するという効果が顕著である。 〔実施例−4〕図4は別の実施例を示すもので、濾液タ
ンク3内にバイブレータ51を装着したものである。バ
イブレータ51は次の仕様のものである。The water in the filtrate tank 3 flows through the wall of the tubular cloth 22.
It penetrates through and penetrates the inside and adheres to the inner wall of the tubular fabric 22.
The solid content is removed, and the water in the tubular fabric passes through the pipe 4.
It is discharged to a muddy water tank (not shown). Then pressurizing medium
Close the valve 33 of the inlet pipe 32, open the valve 35,
Then, the pump 2 is restarted. 20th as warp thread
Align 2 polyester yarns from 6 yarns
Using 324 of the obtained threads, weft of 1000d
Filament shape made by combining four polyester filaments
Cylindrical cloth (Ashimori Industry Co., Ltd.) using 50 pieces per several 10 cm
A one hose manufactured by Co., Ltd.), diameter 65mmφ, long
Conducted by spirally burying 10m in the filtrate tank
Using the example equipment, drilling water with a specific gravity of raw mud water of 1.1
Concentrated. Mud flow rate is 135 liters / min, mud pressure
Force 1.3-1.4kg / cm2 Concentrated in. At this time the filtrate
Is 8 liters / min, dehydration efficiency (vs total filtrate) about 6%
Remained the same. The turbidity of the filtrate is 20-40 mg / for about 1 hour.
It was 1, but then became 1-2 mg / l. About 30
After a lapse of time, the amount of filtrate gradually decreases, and after about 50 hours
To 5 liters / min. So the pump
Temporarily stop, attach the lid to the filtrate tank, and
Pressure of 2 kg / cm 2 Was injected for 2 hours. That
After that, the pump was operated again to circulate and concentrate the muddy water. Filtrate
The volume was restored to 7 liters / min. Example 3 As shown in FIG. 1, the discharge pipe 7 of the pump 2
Attach the air blowing pipe 41 to the and blow air bubbles into the muddy water.
I tried to put it in. Using the same device as in Example-2,
The drilling water with a specific gravity of muddy water of 1.1 was concentrated. Mud flow
The amount is 155 liters / min, the muddy water pressure is 1.35 to 1.
4 kg / cm2 2kg / cm while concentrating with2 The air
Was injected. At this time, the filtrate is 8.5-11 liters / m
in, dehydration efficiency (relative to total filtrate) remained at about 5.3-7.3%
did. The amount of filtrate varies greatly and the turbidity of the filtrate is
It was high at 140 mg / l for the first time, but after about 1 hour, 35
-40 mg / l. After about 20 hours, the amount of filtrate
Since it has dropped to 4 liters / min
Stopped rolling. Blowing air bubbles causes the turbidity of the filtrate to be slightly high.
However, the effect of increasing the throughput is remarkable. [Embodiment 4] FIG. 4 shows another embodiment.
A vibrator 51 is mounted in the link 3. Ba
The evaporator 51 has the following specifications.
【0026】 形式:棒状電気バイブレータ 外径32mmφ×長さ488mm 振動:振動数12,000〜14,000v.p.m、
最大振幅1.8mm 出力:280W 電圧:100V 電流:5A 重量:4.9kg 実施例−2と同じ条件で濃縮を行い、2時間運転したと
ころ、濾液の量の低下は20〜30%改善された。 〔実施例−5〕図5は濾液タンク3の外周に濾液の上昇
空間70を別に設けた実施例を示すもので、この上昇空
間内に傾斜板71を設けた。濾液は上昇空間70内を極
めて緩やかな上昇速度で上昇し、オーバーフローする。
この時、濾液中に混入した固形の微粒子は、自然沈降
し、傾斜板の作用により、傾斜板の面に沿って効率よく
沈降する。沈降した微粒子はホッパ72に集められ、そ
こから排出される。Type: Rod-shaped electric vibrator Outer diameter 32 mmφ × Length 488 mm Vibration: Vibration frequency 12,000 to 14,000 v. p. m,
Maximum amplitude 1.8 mm Output: 280 W Voltage: 100 V Current: 5 A Weight: 4.9 kg Concentrating under the same conditions as in Example-2 and operating for 2 hours, the decrease in the amount of filtrate was improved by 20 to 30%. . [Embodiment 5] FIG. 5 shows an embodiment in which a filtrate raising space 70 is separately provided on the outer periphery of the filtrate tank 3, and an inclined plate 71 is provided in this raising space. The filtrate rises in the rising space 70 at an extremely slow rising speed and overflows.
At this time, the solid fine particles mixed in the filtrate spontaneously settle, and due to the action of the inclined plate, they efficiently settle along the surface of the inclined plate. The settled fine particles are collected in the hopper 72 and discharged from there.
【0027】[0027]
【発明の効果】本発明によれば、浸透性壁を有する筒状
布帛から成る通水路内に泥水を通水し、この浸透性壁か
ら濾液を通水路外に浸出させ、通路内の泥水の濃度を高
める泥水の濃縮方法において、筒状布帛の内面に固形分
が付着し、濾液排出能力が低下するのを効果的に防止す
ることができる。この防止方法の1つとして筒状布帛の
外面側を内面側より高圧にする加圧工程を設けることに
より、機能を回復することができるが、この加圧工程に
おいて、本発明の筒状布帛を用いることによって、筒状
布帛のつぶれ等を効果的に防止することができる。EFFECTS OF THE INVENTION According to the present invention, muddy water is passed through a water passage made of a tubular cloth having a permeable wall, and the filtrate is leached from the permeable wall to the outside of the water passage, so that the muddy water in the passage is leached. In the method of concentrating the muddy water for increasing the concentration, it is possible to effectively prevent the solid content from adhering to the inner surface of the tubular cloth and lowering the filtrate discharge capacity. As one of the methods for preventing this, a function can be restored by providing a pressurizing step in which the outer surface side of the tubular cloth is made higher than the inner surface side, but in this pressurizing step, the tubular cloth of the present invention is By using it, it is possible to effectively prevent the tubular cloth from being crushed.
【0028】また、筒状布帛内に空気泡を吹き込む手
段、筒状布帛を機械的に振動させる手段、筒状布帛内の
流れに脈動を与える手段等を採用することによって、筒
状布帛の内面に固形分が付着するのを防止することがで
きる。The inner surface of the tubular cloth can be obtained by employing means for blowing air bubbles into the tubular cloth, means for mechanically vibrating the tubular cloth, means for pulsating the flow in the tubular cloth, and the like. It is possible to prevent the solid content from adhering to.
【図1】実施例装置の(a)平面図、(b)側面図であ
る。FIG. 1A is a plan view and FIG. 1B is a side view of an apparatus according to an embodiment.
【図2】実施例の筒状布帛の織物構造を示す説明図であ
る。FIG. 2 is an explanatory view showing the woven structure of the tubular cloth of the example.
【図3】実施例の筒状布帛の織物構造を示す説明図であ
る。FIG. 3 is an explanatory view showing the woven structure of the tubular cloth of the example.
【図4】実施例装置の(a)平面図、(b)側面図であ
る。FIG. 4A is a plan view and FIG. 4B is a side view of the apparatus according to the embodiment.
【図5】実施例装置の(a)平面図、(b)側面図であ
る。5 (a) is a plan view and FIG. 5 (b) is a side view of the embodiment apparatus.
1 泥水タンク 2 ポンプ 3 濾液タンク 4、5、6、7、
8 管 11、12、13、14 バルブ 21 外壁 22 筒状布帛 23 網目円筒 24 円筒形螺旋
形維持部材 25 蛇腹管 31 蓋 32 加圧媒体導入管 33 バルブ 34、36 オーバーフロー管 35 バルブ 41 空気管 42 バルブ 51 バイブレータ 61 たて糸 62 線状体 63 よこ糸 64 線状体 70 上昇空間 71 傾斜板 72 ホッパ1 Muddy water tank 2 Pump 3 Filtrate tank 4, 5, 6, 7,
8 pipes 11, 12, 13, 14 valve 21 outer wall 22 tubular cloth 23 mesh cylinder 24 cylindrical helical maintenance member 25 bellows pipe 31 lid 32 pressurized medium introduction pipe 33 valve 34, 36 overflow pipe 35 valve 41 air pipe 42 Valve 51 Vibrator 61 Warp thread 62 Linear body 63 Weft thread 64 Linear body 70 Ascending space 71 Inclined plate 72 Hopper
───────────────────────────────────────────────────── フロントページの続き (72)発明者 上垣 潔志 大阪府摂津市千里丘7丁目11番7号 芦森 エンジニアリング株式会社内 (72)発明者 瀬下 雅博 大阪府摂津市千里丘7丁目11番7号 芦森 エンジニアリング株式会社内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Kiyoshi Uegaki 7-11-7 Senrioka, Settsu-shi, Osaka Ashimori Engineering Co., Ltd. (72) Inventor Masahiro Seshita 7-11-7 Senri-oka, Settsu-shi, Osaka Ashi Mori Engineering Co., Ltd.
Claims (10)
路内に泥水を通水し、この浸透性壁から濾液を通水路外
に浸出させ、通路内の泥水の濃度を高める泥水の濃縮方
法において、筒状布帛の外面側を内面側より圧力を高め
る加圧工程を設けたことを特徴とする泥水の濃縮方法。1. Concentration of muddy water for increasing the concentration of muddy water in the passage by allowing muddy water to pass through the water passage made of a tubular fabric having a permeable wall and allowing the filtrate to leach out of the water passage from the permeable wall. A method for concentrating muddy water, which comprises a step of increasing the pressure on the outer surface side of the tubular cloth from the inner surface side.
る通水路と、この通水路に泥水を通水させるポンプとを
備えた泥水の濃縮装置において、濾液タンクを密閉自在
にすると共に該濾液タンク内に加圧媒体を供給する供給
口を設けたことを特徴とする泥水の濃縮装置。2. In a muddy water concentrating device comprising a water passage made of a tubular cloth submerged in a filtrate tank and a pump for letting muddy water pass through the water passage, the filtrate tank can be sealed and the filtrate can be sealed. A muddy water concentrating device having a supply port for supplying a pressurized medium in a tank.
又は剛直な線状体と合成繊維糸とを横糸として交互に織
り込んで織成した筒状布帛であることを特徴とする請求
項2記載の泥水の濃縮装置。3. The tubular fabric is a tubular fabric formed by weaving synthetic fiber yarns into warp yarns by alternately weaving wire or rigid linear bodies and synthetic fiber yarns as weft yarns. The described muddy water concentrator.
織成した筒状体の内側に、たて糸および横糸に合成繊維
のマルチフィラメントを用いて密に織成した筒状体を内
嵌した構造の筒状布帛であることを特徴とする請求項2
記載の泥水の濃縮装置。4. A structure in which a tubular cloth is tightly woven by using a synthetic fiber multifilament in the warp threads and the weft threads inside a tubular body in which pressure-resistant warp threads and weft threads are woven. A tubular cloth, wherein the cloth is a tubular cloth.
The described muddy water concentrator.
し、この浸透性壁から濾液を通水路外に浸出させ、通路
内の泥水の濃度を高める泥水の濃縮方法において、泥水
とともに空気泡を通水路内に送入することを特徴とする
泥水の濃縮方法。5. A method for concentrating muddy water in which mud is passed through a water passage having a permeable wall, and filtrate is leached from the permeable wall to the outside of the water passage to increase the concentration of the muddy water in the passage. A method for concentrating muddy water, which comprises feeding air bubbles into a water passage.
筒状布帛からなる通水路と、この通水路に泥水を通水さ
せるポンプとから成る泥水の濃縮装置において、ポンプ
の出口側の通水路に空気吹き込み装置を備えたことを特
徴とする泥水の濃縮装置。6. A muddy water concentrating device comprising a water passage made of a tubular cloth submerged in a filtrate tank and having a permeable wall, and a pump for letting muddy water pass through the water passage. A mud concentrating device having an air blowing device in a waterway.
通水路内に泥水を通水し、この浸透性壁から濾液を濾液
タンク内に浸出させ、通水路内の泥水の濃度を高める泥
水の濃縮方法において、通水路又は濾液に振動を付与す
ることを特徴とする泥水の濃縮方法。7. A muddy water which is immersed in a filtrate tank to pass mud water through a water passage having a permeable wall, from which the filtrate is leached into the filtrate tank to increase the concentration of the muddy water in the water passage. In the method for concentrating muddy water, vibration is applied to a water passage or a filtrate, and
る通水路と、この通水路に泥水を通水させるポンプとか
ら成る泥水の濃縮装置において、濾液タンクの濾液中に
浸漬するバイブレータを備えたことを特徴とする泥水の
濃縮装置。8. A muddy water concentrating device comprising a water passage made of a tubular cloth submerged in a filtrate tank and a pump for letting the muddy water pass through the water passage, comprising a vibrator immersed in the filtrate in the filtrate tank. A muddy water concentrator that is characterized by
し、この浸透性壁から濾液を通水路外に浸出させ、通路
内の泥水の濃度を高める泥水の濃縮方法において、泥水
の流れに脉動を与えることを特徴とする泥水の濃縮方
法。9. A method for concentrating muddy water in which muddy water is passed through a water passage having a permeable wall and filtrate is leached from the permeable wall to the outside of the water passage to increase the concentration of the muddy water in the passage. A method for concentrating muddy water, characterized by pulsating the flow.
路を水没させて該通水路内に泥水を通水し、濾液タンク
内に濾液を浸出させて泥水を濃縮する装置において、濾
液タンクに濾液が低速で上昇する空間を設け、濾液タン
クの上部より濾液をオーバーフローさせると共に該空間
内に傾斜板を配設し、濾液タンク底部に排泥口を備えた
ことを特徴とする泥水の濃縮装置。10. An apparatus for submerging a tubular cloth-made water passage in a filtrate tank to pass muddy water into the water passage, leaching the filtrate into the filtrate tank and concentrating the muddy water into the filtrate tank. A muddy water concentrating device characterized by providing a space in which the filtrate rises at a low speed, overflowing the filtrate from the upper part of the filtrate tank, and arranging an inclined plate in the space, and providing a sludge discharge port at the bottom of the filtrate tank. .
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP27335894A JP3522856B2 (en) | 1994-11-08 | 1994-11-08 | Mud concentrator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP27335894A JP3522856B2 (en) | 1994-11-08 | 1994-11-08 | Mud concentrator |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH08131720A true JPH08131720A (en) | 1996-05-28 |
JP3522856B2 JP3522856B2 (en) | 2004-04-26 |
Family
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JP27335894A Expired - Fee Related JP3522856B2 (en) | 1994-11-08 | 1994-11-08 | Mud concentrator |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7456103B2 (en) * | 2003-02-28 | 2008-11-25 | Fujitsu Limited | Etch-resistant film, forming method thereof, surface-modified resist pattern, forming method thereof, semiconductor device and manufacturing method thereof |
-
1994
- 1994-11-08 JP JP27335894A patent/JP3522856B2/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7456103B2 (en) * | 2003-02-28 | 2008-11-25 | Fujitsu Limited | Etch-resistant film, forming method thereof, surface-modified resist pattern, forming method thereof, semiconductor device and manufacturing method thereof |
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JP3522856B2 (en) | 2004-04-26 |
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