JPS58215298A - Supply device of sludge to solid-liquid separator - Google Patents

Supply device of sludge to solid-liquid separator

Info

Publication number
JPS58215298A
JPS58215298A JP57096212A JP9621282A JPS58215298A JP S58215298 A JPS58215298 A JP S58215298A JP 57096212 A JP57096212 A JP 57096212A JP 9621282 A JP9621282 A JP 9621282A JP S58215298 A JPS58215298 A JP S58215298A
Authority
JP
Japan
Prior art keywords
sludge
conveyance
solid
granulation
downstream side
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
JP57096212A
Other languages
Japanese (ja)
Other versions
JPS6025238B2 (en
Inventor
Masatsuki Shirakawa
正月 白川
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.)
SEKISUI ENBAIROMENTO KK
Original Assignee
SEKISUI ENBAIROMENTO 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 SEKISUI ENBAIROMENTO KK filed Critical SEKISUI ENBAIROMENTO KK
Priority to JP57096212A priority Critical patent/JPS6025238B2/en
Publication of JPS58215298A publication Critical patent/JPS58215298A/en
Publication of JPS6025238B2 publication Critical patent/JPS6025238B2/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B30PRESSES
    • B30BPRESSES IN GENERAL
    • B30B9/00Presses specially adapted for particular purposes
    • B30B9/02Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material
    • B30B9/24Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material using an endless pressing band

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Structure Of Belt Conveyors (AREA)
  • Filling Or Emptying Of Bunkers, Hoppers, And Tanks (AREA)
  • Filtration Of Liquid (AREA)
  • Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)

Abstract

PURPOSE:To economize the amt. of the flocculating agent to be used, by connecting a conveyance and granulation mechanism having a conveyance screw mounted with plural spiral conveyance pieces at prescribed intervals to a revolving shaft to the downstream side of a charging tank for the flocculating agent and providing a scooping up mechanism on the downstream side of the conveyance and granulation mechanism. CONSTITUTION:A supply device of sludge to a solid-liquid separator 30 is constituted of a conveyance and granulation mechanism 1 having a conveyance screw 12 mounted with spiral conveyance pieces 10 at prescribed intervals D to a revolving shaft 9 connected to the downstream side of a charging tank 4 for a flocculating agent, a scooping up mechanism 20 of a long transverse width having scooping up pieces 26 which moves along the bottom part on the downstream of said mechanism 1, and a sludge discharge port 29 at the top edge in the bottom part of the mechanism 20. Thus the flocculating agent charged into the sludge is diffused uniformly thereon, whereby the effect of granulation is provided fully and the sepn. efficiency of the separator 30 is improved. Therefore, the amt. of the flocculating agent to be used in the tank 4 is economized.

Description

【発明の詳細な説明】 この発明は、固液分離装置に汚泥などのスラッジを供給
するスラッジ供給装置に関するもので、スラッジに混合
した凝集剤の拡散効果及び造粒効果を十分に高めること
で固液分離しやすいようにしたことを特徴とする。
Detailed Description of the Invention The present invention relates to a sludge supply device that supplies sludge such as sludge to a solid-liquid separator. It is characterized by easy liquid separation.

泥水等に凝集剤を投入することによυ泥の分子f凝集し
、固液分離効果において固液分離効果を高めることは従
来から行われている。しかし、従来は、単に凝集剤を投
入するだけであるため、凝集剤が本来有している凝集効
果を十分に発揮させることが困難であり、とのか、め所
期の凝集効果を得るためには多量の凝集剤を投入しなけ
ればならない。
It has been conventional practice to add a flocculant to muddy water or the like to cause the molecules f of mud to flocculate, thereby enhancing the solid-liquid separation effect. However, in the past, because the flocculant was simply added, it was difficult to fully utilize the flocculant's inherent flocculating effect. requires a large amount of flocculant to be added.

本発明は上記に鑑み提案されたもので、回転軸に複数の
螺旋状搬送片を所定の間隔で取付けた搬送スクリューと
、該搬送スクリューを収納するケースとからなる搬送造
粒機構を凝集剤投入槽の下流側に接続し、搬送造粒機構
の下流側には底部に沿って移動する抄い上げ片を有する
抄い上げ機構を設けることによシ、凝集剤拡散効果を高
め、かつ造粒効果を十分に発揮させることができる固液
分離装置へのスラッジ供給装置を提供しようとするもの
である。
The present invention has been proposed in view of the above, and includes a conveying granulation mechanism consisting of a conveying screw in which a plurality of spiral conveying pieces are attached to a rotating shaft at predetermined intervals, and a case that houses the conveying screw. By providing a scooping mechanism connected to the downstream side of the tank and having a scooping piece that moves along the bottom on the downstream side of the transport granulation mechanism, it is possible to enhance the flocculant diffusion effect and improve the granulation process. The present invention aims to provide a sludge supply device to a solid-liquid separator that can fully exhibit its effects.

以下本発明の構成を実施例の図面にもとづいて説明する
The configuration of the present invention will be explained below based on drawings of embodiments.

本発明に係るスラッジ供給装置/は、I@1図で示すよ
うに、パイブスから流出するスラッジを受は入れる定量
41!3の隣りに凝集剤投入槽qをIF!l!け、該凝
集剤投入槽qの上方にはタンクjからn[定量の高分子
凝集剤を投入する凝集剤投入W6の出口を臨ませ、凝集
剤投入槽ダの内部には攪拌機7を臨ませである。したか
つて宇量惰3から凝集剤投入槽qにスラッジが流、入す
ると、凝集剤投入管すからルT定量の斤隼剤を投入し、
攪拌機りにより攪拌することができる。
As shown in Figure I@1, the sludge supply device/according to the present invention has a flocculant input tank q adjacent to the metering unit 41!3 that receives the sludge flowing out from the pipes. l! Above the flocculant input tank q, the outlet of the flocculant input W6, into which a fixed amount of polymer flocculant is inputted, faces from tank j to n, and the agitator 7 faces inside the flocculant input tank d. It is. When the sludge flows into the flocculant input tank q from the coagulant input tank q, a fixed amount of flocculant is introduced into the flocculant input pipe.
Stirring can be performed using a stirrer.

凝集剤投入槽qの下流側には凝集剤を拡散させるととも
に、スラッジ中の固形分子を凝集して造粒する搬送造粒
機at gを接続する。701邸jで示す搬送造粒機構
gは、柄長な回転軸9に複数の蜘旋状搬送片io・・・
全所定の間隔りで取付けるとともに、回転軸デとl′り
丁平行に複数の埒拌杆//・・・を各を送片10に通ブ
ように設けた搬送スクリュー/2と、該搬送スクリュー
/2を収納する断面略U字状の横長なケース/3と、ト
11記搬送スクリュー/2をロー11転するN IIJ
源とからなり、該駆動源としては例えば減速機/’Jを
有するモータ/まである。
A transport granulator atg is connected to the downstream side of the flocculant input tank q to diffuse the flocculant and to aggregate and granulate solid molecules in the sludge. The conveyance granulation mechanism g shown at 701 house j has a plurality of spider-shaped conveyance pieces io...
A conveying screw /2 is installed at predetermined intervals, and is provided with a plurality of stirring rods parallel to the rotation axis D so as to pass through the conveying piece 10, and the conveying screw /2. A horizontally elongated case /3 with a substantially U-shaped cross section that houses the screw /2, and a NIIJ that rotates the transport screw /2 in the row direction.
The drive source includes, for example, a motor with a speed reducer/'J.

しだがって、前1、凝集剤投入管1ダからスラッジをケ
ース/3に流入すると、計スラッジは回転軸9の回転げ
より授拌杆//で十分に攪拌ネf]て凝集剤が十分に拡
散し、オだ、第1搬送片10αによりケース/3内を移
動する。第1搬送片10aの下流側部分は第1搬送片1
0Qと第2搬送片lObとが間隔りだけ一旺れているの
で、移動するスラッジが第1搬送片10aと第2搬送片
10hとの間F!#α内に貿オる。スラッジが留まると
、スラッジ中の固形分子が託隼して粒状となり、造粒効
果が発揮される。
Therefore, when the sludge flows into the case 3 from the flocculant input pipe 1, the sludge is sufficiently stirred by the stirring rod from the rotation of the rotating shaft 9, and the flocculant is mixed. After being sufficiently diffused, it is moved within the case/3 by the first conveyance piece 10α. The downstream portion of the first conveying piece 10a is the first conveying piece 1
Since 0Q and the second conveyance piece lOb are separated by the distance F!, the moving sludge is between the first conveyance piece 10a and the second conveyance piece 10h. Trade within #α. When the sludge remains, the solid molecules in the sludge are dispersed and become granular, producing a granulation effect.

そして第1搬送片/IQにより凝集剤投入管qか(のス
ラッジを1次間隙/6α内に送ると、先に送られたスラ
ッジが祷から送られてくるスラッジにより押圧され、下
流側に移動する。間隙/lの下流側には第2搬送片10
hがあるので、間隙16αから押し出略れたスラッジは
第2搬送片tohの回転によシ該搬送片10hの下流側
に送られる。そして第2搬送片iohの下流側部分には
間隙/bbがあるので、第2搬送片tabにより移動す
るスラッジは該間隙/4h内に溜まる。スラッジが溜ま
ると、前記と同様に凝集剤により固形分子がすでに凝集
した塊に次々に付着したり、或いは浮遊する固形分子同
志が凝集して新たな粒状となる。
Then, when the sludge from the coagulant input pipe q or ( is sent into the primary gap /6α by the first conveyor piece /IQ, the sludge sent earlier is pressed by the sludge sent from the pipe and moves downstream. On the downstream side of the gap/l, there is a second conveying piece 10.
h, the sludge pushed out from the gap 16α is sent to the downstream side of the second conveying piece 10h by the rotation of the second conveying piece toh. Since there is a gap /bb on the downstream side of the second conveyance piece ioh, the sludge moved by the second conveyance piece tab accumulates in the gap /4h. When sludge accumulates, solid molecules adhere to already aggregated lumps one after another due to the flocculant, or floating solid molecules aggregate to form new particles, as described above.

そして第2搬送片tohが同転し紗、けてこの間隙/6
b内にスラッジを順次送ると、先に送られて溜っていた
スラッジが後から送られてくるスラッジにより押圧され
、下流側に移動する。
Then, the second conveyor piece toh rotates at the same time and the gap between the gauze and the grate is /6.
When the sludge is sent sequentially into b, the sludge that was sent first and accumulated is pressed by the sludge sent later and moves to the downstream side.

この様に1ケース/3内のスラッジは、回転軸tの回転
で各搬送片10tl、 10h、 10c・・・により
移動したシ貯溜するのを繰シ返しながら下流側に搬送さ
れ、終局的には下流端の開口部/7から流下樋1g内に
流下する。なお、スラッジは搬送造粒機構g内を移動す
る間、各搬送片10・・・によシ混練されるとともに、
攪拌杆/2により継続して攪拌されるので、凝集剤の拡
散効果が著しく高められる。したがって前記造粒効果を
確実に且つ十分に発揮することができる。
In this way, the sludge in 1 case/3 is transferred to the downstream side while being moved and accumulated by each transfer piece 10tl, 10h, 10c, etc. by the rotation of the rotation axis t, and finally flows down into the downflow gutter 1g from the opening /7 at the downstream end. In addition, while the sludge moves within the transport granulation mechanism g, it is kneaded by each transport piece 10...
Since the mixture is continuously stirred by the stirring rod/2, the diffusion effect of the flocculant is significantly enhanced. Therefore, the granulation effect can be reliably and sufficiently exerted.

流下樋/gは、第3図で示すように、下方に向って横幅
を広く形成した縦方向の樋であり、内部には幅方向の拡
散板/q・・・を上下多段に有し、下端開口部/g’に
抄い上げ機構20を設けである。拡散板/qは、造粒機
構gから流下するスラッジを横方向に広く分散するもの
で、基端を流下樋/gの対向内面に互い違いに固定し、
上面を先端に向けて僅かに下シ傾斜させた棚板状である
。したがって搬送造粒機構gからスラッジが流下樋1g
内に流入すると、このスラッジは流下する途中で各拡散
板/り・・・に当って横方向に拡がり、拡散板19の先
端と流下樋/ざの内面との間隙内を流下して抄い上げ機
構コOに流下する。なお、拡散板/qの上面を左右端部
に向けて僅かに下り傾斜させると、横方向の分散効果を
著しく高めることができる。
As shown in Fig. 3, the downflow gutter /g is a vertical gutter whose width is widened toward the bottom, and inside thereof there are multiple diffusion plates /q in the upper and lower directions. A scooping mechanism 20 is provided at the lower end opening /g'. The diffusion plates /q widely disperse the sludge flowing down from the granulation mechanism g in the horizontal direction, and their base ends are fixed alternately to the opposing inner surface of the downflow gutter /g.
It has a shelf-like shape with the top surface slightly tilted downward toward the tip. Therefore, 1 g of sludge flows down from the transport granulation mechanism g.
As the sludge flows down, it hits each diffuser plate and spreads laterally, and flows down in the gap between the tip of the diffuser plate 19 and the inner surface of the downflow gutter. It flows down to the lifting mechanism KO. Note that if the upper surface of the diffuser plate /q is slightly inclined downward toward the left and right ends, the lateral dispersion effect can be significantly enhanced.

抄い上げ機構20は、底部コ/の断面が半円弧状であっ
て横幅が流下樋/Ifの下端開口部ig’の幅に等しい
貯留槽、22と、該貯留槽、22の内部に設けた抄い上
げ車23とからなυ、貯留摺コニの底部2/に溜ったス
ラッジを固液分離装置に供給するものである。抄い上げ
車23は、第4図で示すように、回転@λダの左右に十
字状の支持杆、1!r、 2!を設け、左右の支持杆2
S。
The scooping mechanism 20 includes a storage tank 22 whose bottom part has a semicircular cross section and whose width is equal to the width of the lower end opening ig' of the downflow trough /If, and is provided inside the storage tank 22. The sludge collected at the bottom 2/ of the storage slider is supplied to the solid-liquid separator. As shown in FIG. 4, the scooping wheel 23 has cross-shaped support rods, 1! r, 2! , and left and right support rods 2
S.

、2!rの先端間隔に断面り字状の横長な抄い上げ片コ
ロ・・・を回転軸2≠とほぼ平行にして設けたもので、
回転軸2ダを中心にして対向する抄い上げ片ユ6,2乙
の間に空隙部27を有する。
, 2! Horizontally long paper-cutting rollers with a cross-section shaped like a letter r are provided at intervals between the tips of r, almost parallel to the rotation axis 2≠.
A gap 27 is provided between the papermaking pieces 6 and 2 that face each other around the rotating shaft 2.

したがって、この抄い上げ車、23を躯動源2gにより
第1図矢印方向に回転すると、各抄い上げ片コロ・・・
が底部、2/に沿って回動し、底部、2/に溜ったスラ
ッジだけを抄い上げ、底部、2/上縁に形成した横長な
スラッジ排出口29から固液分離装置30に供給するこ
とができる。なお抄い上げ車ユ3を回転しても空隙部2
7内に存在するスラッジは・抄い上げ片、2乙により抄
い上げられることがないので、固液分離装置3゜に供給
されることはない。したがって流下樋/gから貯留槽2
2内に流下したスラッジは、抄い上げ車23の空隙部コ
ク内に溜っている間、凝集剤の効果により凝集する。そ
して空隙部27内のスラッジが凝集し、次第に沈殿して
底部2/に溜まると抄い上げ片コロにより抄い上げられ
固液分離装置30に供給される。この様に抄い上げ機構
、20は、空隙部27を有するため、凝集剤の効果を一
層高袷ることかできるとともに、横長な抄い上げ片2乙
が底部2/に溜ったスラッジだけを抄い上げるので、固
液分11!a装置30のr布上にスラッジを均一に供給
できる。
Therefore, when this papermaking wheel 23 is rotated in the direction of the arrow in Fig. 1 by the rotating source 2g, each papermaking piece roller...
rotates along the bottom, 2/, scoops up only the sludge accumulated on the bottom, 2/, and supplies it to the solid-liquid separator 30 from an oblong sludge discharge port 29 formed at the upper edge of the bottom, 2/. be able to. Note that even if the scooping wheel 3 is rotated, the void 2
The sludge present in the solid-liquid separator 3 is not scooped up by the scooping piece 2, so it is not supplied to the solid-liquid separator 3. Therefore, from the downflow gutter/g to the storage tank 2
The sludge that has flowed down into the sludge 2 is coagulated by the effect of the coagulant while it remains in the cavity of the scooping vehicle 23. Then, the sludge in the cavity 27 coagulates, gradually precipitates, and accumulates at the bottom 2/, whereupon it is scooped up by a scraping roller and supplied to the solid-liquid separator 30. As described above, since the scooping mechanism 20 has the cavity 27, the effect of the flocculant can be further enhanced, and the horizontally long scooping piece 2B can only remove the sludge accumulated at the bottom 2/. Since it is made by papermaking, the solid-liquid content is 11! Sludge can be uniformly supplied onto the r cloth of the a device 30.

固液分離装置3θは、一般に、回転駆動されるr布上に
スラッジを供給してBP布土に固形物を残し、液分はP
布を通過させて一次的な固液分離を行い、更に固形物を
加圧脱水して二次的に固液分離するという基本構成を有
している。
Generally, the solid-liquid separator 3θ supplies sludge onto a rotatably driven cloth, leaving solids on the BP cloth, and liquids are P
The basic structure is to perform primary solid-liquid separation by passing through a cloth, and then dehydrate the solid material under pressure to perform secondary solid-liquid separation.

第1図で示す固液分離装置30ば、複数のローラ31・
・・に張設されて回転する下P布3:1と、該下P布3
.2上にスラッジを供給するスラッジ供給ボックス33
と、下戸布3コ上のスラッジの水分を吸引して分離する
バキュームホッパー3ダと、下f布32上のスラッジを
挟入つける上f布、7 kと、両1布32,3!fによ
って挾持したスラッジを加圧脱水するメーンローラ36
及び加圧ベルト37などからなる。
The solid-liquid separator 30 shown in FIG.
The lower P cloth 3:1 that is stretched on and rotates, and the lower P cloth 3
.. Sludge supply box 33 that supplies sludge onto 2
, a vacuum hopper 3 da that sucks and separates the moisture from the sludge on the lower f cloth 3, an upper f cloth that pinches the sludge on the lower f cloth 32, 7k, and both cloths 32, 3! The main roller 36 pressurizes and dewaters the sludge held by f.
and a pressure belt 37.

したがってスラツジイjE給装備“lにより排出口2q
から排出するスラッジは、スラッジ供給ボックス33に
より下P布32の表面に幅方向に均一厚さで供給され、
バキュームホッパー3’1によυ−一次的固液分離が行
われ、メーンローラ36と加圧ベルト3りにより加圧脱
水され、排出口(図示せず)から水分含有率の少ない脱
水ケーキ3g・・・とじて排出される。
Therefore, the discharge port 2q is
The sludge discharged from the sludge is supplied to the surface of the lower P cloth 32 with a uniform thickness in the width direction by the sludge supply box 33,
υ-primary solid-liquid separation is performed by the vacuum hopper 3'1, dehydrated under pressure by the main roller 36 and the pressure belt 3, and 3 g of dehydrated cake with a low moisture content is discharged from the discharge port (not shown). ...It is closed and discharged.

以上説明したように本発明によれば、回転軸に複数の噂
旋状搬送片をル1定の間隔で取付けた搬送スクリューを
有する搬送造粒機構を凝集剤投入槽の下流側に接続し、
搬送造粒機構の下流側に;は底部に沿って回動する抄い
上げ片を有する抄い上げ機構を設けであるので、スラッ
ジ中に投入した凝集剤投入槽lく拡散し、造粒効果を十
分に発揮させることができる。したがって固液分明装置
における固液分離効果を従来以上に高めることができる
As explained above, according to the present invention, a conveying granulation mechanism having a conveying screw in which a plurality of spiral conveying pieces are attached to a rotating shaft at regular intervals is connected to the downstream side of a coagulant charging tank,
On the downstream side of the transport granulation mechanism, there is a scouring mechanism with a sifting piece that rotates along the bottom, so that the flocculant introduced into the sludge is diffused into the tank and the granulation effect is improved. can be fully demonstrated. Therefore, the solid-liquid separation effect in the solid-liquid spectrometer can be improved more than ever.

また本発明によれば、凝集剤が本来有している凝集効果
を十分に発揮させることができるので、凝集剤の使用量
を従来よυも少なくすることができる。
Further, according to the present invention, since the flocculant's inherent flocculating effect can be fully exhibited, the amount of the flocculant used can be reduced by υ compared to the conventional method.

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

図面は本発明の一実施例を示すもので、第1図は縦断正
面図、第2図は搬送スクリューの断面図、第5[imは
流下樋の一部欠截側面図、第4図は抄い上げ車の一部欠
截斜視図である。 /・・・スラッジ供給装置、グ・・・凝集剤投入槽、g
・・・搬送造粒機構、デ・・・回転軸、IO・・・搬送
片、lユ・・・搬送スクリュー、13・・・ケース、2
0・・・抄い上げ機構、コ/・・・底部、26・・・抄
い上げ片、ユデ・・・スラッジ排出口、30・・・固液
分明装置。
The drawings show an embodiment of the present invention, in which Fig. 1 is a longitudinal sectional front view, Fig. 2 is a sectional view of the conveying screw, Fig. 5 is a partially cutaway side view of the downflow gutter, and Fig. 4 is a partially cutaway side view of the downflow gutter. FIG. 2 is a partially cutaway perspective view of the paper-lifting vehicle. /...sludge supply device, g...flocculant charging tank, g
... Conveyance granulation mechanism, De... Rotating shaft, IO... Conveyance piece, lU... Conveyance screw, 13... Case, 2
0... Paper-picking mechanism, /... Bottom, 26... Paper-picking piece, Yude... Sludge discharge port, 30... Solid-liquid separation device.

Claims (1)

【特許請求の範囲】[Claims] 回転軸に複数の螺旋状搬送片を所定の間隔で取付けた搬
送スクリューと、該搬送スクリューを収納するケースと
からなる搬送造粒機構を凝集剤投入−の下流側に接続し
、搬送造粒(2)構の下流側には底部に沿って移動する
抄い上げ片を有する横幅の長い抄い上げ機構を接続し、
該抄い上げ機構の底部上縁にスラクジ排田口を形成して
なる固液分*qtへのスラッジ供給装置。
A conveyance granulation mechanism consisting of a conveyance screw in which a plurality of spiral conveyance pieces are attached at predetermined intervals to a rotating shaft and a case that houses the conveyance screw is connected to the downstream side of the flocculant input, and conveyance granulation ( 2) Connect to the downstream side of the mechanism a long raking mechanism with a raking piece that moves along the bottom,
A sludge supply device for solid-liquid *qt comprising a sludge discharge port formed at the upper edge of the bottom of the scooping mechanism.
JP57096212A 1982-06-07 1982-06-07 Sludge supply device to solid-liquid separator Expired JPS6025238B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57096212A JPS6025238B2 (en) 1982-06-07 1982-06-07 Sludge supply device to solid-liquid separator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57096212A JPS6025238B2 (en) 1982-06-07 1982-06-07 Sludge supply device to solid-liquid separator

Publications (2)

Publication Number Publication Date
JPS58215298A true JPS58215298A (en) 1983-12-14
JPS6025238B2 JPS6025238B2 (en) 1985-06-17

Family

ID=14158933

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57096212A Expired JPS6025238B2 (en) 1982-06-07 1982-06-07 Sludge supply device to solid-liquid separator

Country Status (1)

Country Link
JP (1) JPS6025238B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60261694A (en) * 1984-06-11 1985-12-24 Nippon Kokan Kk <Nkk> Dehydrating method of sludge
JP2014193441A (en) * 2013-03-29 2014-10-09 Kubota Kankyo Service Kk Sludge dehydration apparatus

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01196907A (en) * 1988-02-02 1989-08-08 Fujitsu Ten Ltd Low-pass and high-pass filter
JPH01309408A (en) * 1988-06-07 1989-12-13 Fujitsu Ten Ltd Active filter circuit
JP2008000769A (en) * 2006-06-21 2008-01-10 Ishigaki Co Ltd High dewatering mechanism-fitted screw press

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60261694A (en) * 1984-06-11 1985-12-24 Nippon Kokan Kk <Nkk> Dehydrating method of sludge
JP2014193441A (en) * 2013-03-29 2014-10-09 Kubota Kankyo Service Kk Sludge dehydration apparatus

Also Published As

Publication number Publication date
JPS6025238B2 (en) 1985-06-17

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