JPH0512003B2 - - Google Patents
Info
- Publication number
- JPH0512003B2 JPH0512003B2 JP63253248A JP25324888A JPH0512003B2 JP H0512003 B2 JPH0512003 B2 JP H0512003B2 JP 63253248 A JP63253248 A JP 63253248A JP 25324888 A JP25324888 A JP 25324888A JP H0512003 B2 JPH0512003 B2 JP H0512003B2
- Authority
- JP
- Japan
- Prior art keywords
- mud
- tank
- filtrate
- dewatering
- filter cloth
- 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 - Lifetime
Links
- 239000000706 filtrate Substances 0.000 claims description 43
- 239000004744 fabric Substances 0.000 claims description 30
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 19
- 230000018044 dehydration Effects 0.000 claims description 11
- 238000006297 dehydration reaction Methods 0.000 claims description 11
- 239000000463 material Substances 0.000 claims description 8
- 238000007599 discharging Methods 0.000 claims description 7
- 238000005192 partition Methods 0.000 claims 1
- 208000005156 Dehydration Diseases 0.000 description 10
- 238000000034 method Methods 0.000 description 9
- 238000004140 cleaning Methods 0.000 description 7
- 238000003756 stirring Methods 0.000 description 5
- 230000002093 peripheral effect Effects 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 239000000654 additive Substances 0.000 description 2
- 230000006835 compression Effects 0.000 description 2
- 238000007906 compression Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 239000003595 mist Substances 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- 230000032258 transport Effects 0.000 description 2
- 230000000996 additive effect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000008394 flocculating agent Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Filtration Of Liquid (AREA)
- Treatment Of Sludge (AREA)
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は、例えば港湾、河川、糊沼等において
浚渫した泥土の脱水を行なう脱水装置に関するも
のである。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a dewatering device for dewatering dredged mud in, for example, ports, rivers, swamps, etc.
[従来の技術]
近年、河川、糊沼等の浚渫工事において、浚渫
した泥土を陸地や埋立地に投棄する際、浚渫泥土
は水分を含んでいることから、これを直接投棄す
ると天日による乾燥にかなりの日数を要したり、
また投棄場所まで例えばダンプカー等の車両を使
用する場合には、本来必要としない水を相当量運
搬することになり、その分無駄となるばかりでな
く、運搬の途中で泥土が跳ね出るといつた2次公
害を引き起こすことがある。[Conventional technology] In recent years, during dredging work for rivers, swamps, etc., when dredged mud is dumped onto land or reclaimed land, the dredged mud contains water, so if it is directly dumped, it will dry out in the sun. It may take a considerable number of days to
In addition, if a vehicle such as a dump truck is used to reach the dumping site, a considerable amount of water that is not originally needed is transported, which not only results in waste, but also causes problems such as mud being thrown out during transportation. May cause secondary pollution.
そこで、浚渫した泥土を投棄する前や、運搬す
る前に、脱水装置により脱水することが近年行な
われている。 Therefore, in recent years, dredged mud has been dewatered using a dewatering device before being dumped or transported.
[発明が解決しようとする課題]
従来のこの種の脱水装置は、泥土を圧縮する方
式、真空吸着方式、比重分離方式が採用されてい
るが、これらの方式は高分子凝集剤等の添加を必
要とすることから、ランニングコストが高くなる
ばかりでなく、添加剤の種類によつては投棄場所
が限定される産業廃棄物となる場合がある。[Problem to be solved by the invention] Conventional dewatering equipment of this type employs a mud compression method, a vacuum adsorption method, and a specific gravity separation method, but these methods require the addition of polymer flocculants, etc. Not only does running cost become high because of the need for additives, but depending on the type of additive, it may become industrial waste for which there are limited places to dispose of it.
また、泥土を圧縮したり、真空を利用したり、
比重の違いを利用する方式では、泥土の脱水性能
に限界があり、高効率の脱水が難しいとういう欠
点があつた。 In addition, we can compress mud, use vacuum,
Methods that utilize differences in specific gravity have the disadvantage that there are limits to the dewatering performance of muddy soil, making it difficult to achieve highly efficient dewatering.
本発明の目的は、高分子凝集剤等を添加するこ
となく、泥土中の水分を高効率に脱水できる脱水
装置を提供するものである。 An object of the present invention is to provide a dehydration device that can highly efficiently dewater water in mud without adding a polymer flocculant or the like.
[課題を解決するための手段]
本発明の目的を達成するための手段の一例は、
泥土供給手段からの泥土が供給される泥土供給開
口部及び脱水処理した泥土を排出する処理泥土排
出開口部を有し、胴部の下部部分に濾布材を仕切
り壁として外側板との間に濾液貯槽が形成された
密閉可能な横長形式の圧力タンクと、脱水処理時
には該泥土供給開口部を閉じ、泥土の供給時には
該泥土供給開口部を開く泥土取り入れ弁と、脱水
処理時には該泥土排出開口部を閉じ、処理泥土の
排出時には該泥土排出開口部を開く泥土吐出弁
と、該圧力タンク内にその軸方向に沿つて配置さ
れ、圧縮空気が軸内を通して多数のノズルから噴
出すると共に、脱水処理時には正逆回転により該
圧力タンク内の泥土を撹拌し、脱水処理の終了時
には一方向回転により脱水泥土を処理泥土排出開
口部に向けて移送するスクリユー軸と、該圧力タ
ンクに形成された濾液貯槽内の濾液をタンク外に
廃液するための濾液弁とを有し、脱水処理時には
該圧力タンク内に密閉状態に保持して該スクリユ
ー軸内に圧縮空気を供給し、圧縮空気の加圧によ
り該濾布材を通して泥土の水分を該濾液貯槽に排
出することを特徴とする脱水装置にある。[Means for Solving the Problems] An example of means for achieving the object of the present invention is as follows:
It has a mud supply opening through which mud is supplied from the mud supply means and a treated mud discharge opening through which dehydrated mud is discharged. A sealable horizontal pressure tank in which a filtrate storage tank is formed, a mud intake valve that closes the mud supply opening during dewatering processing and opens the mud supply opening when mud is supplied, and the mud discharge opening during dewatering processing. A mud discharge valve is arranged along the axial direction in the pressure tank, and compressed air is ejected from a number of nozzles through the shaft, and the mud discharge opening is opened when discharging the treated mud. A screw shaft that stirs the mud in the pressure tank by forward and reverse rotation during processing, and transports the dehydrated mud toward the treated mud discharge opening by rotating in one direction when the dewatering process is completed, and a filtrate formed in the pressure tank. It has a filtrate valve for discharging the filtrate in the storage tank outside the tank, and during dehydration processing, the pressure tank is kept in a sealed state and compressed air is supplied into the screw shaft, and by pressurizing the compressed air. The dewatering device is characterized in that water in mud is discharged into the filtrate storage tank through the filter cloth material.
[作用]
上記のごとく構成した脱水装置は、加圧タンク
内に一定量の泥土を収容すると密閉され、スクリ
ユー軸の正逆回転により泥土をまんべんなく撹拌
しつつ、スクリユー軸から供給された圧縮空気に
より、泥土を圧脱水し、濾布材を通して泥土の水
分を該濾液貯槽に排出し、その後濾液弁を開弁し
て加圧タンク外に廃液する。[Function] The dewatering device configured as described above is sealed when a certain amount of mud is stored in the pressurized tank, and while the mud is evenly stirred by the forward and reverse rotation of the screw shaft, the dewatering device is heated by the compressed air supplied from the screw shaft. , the mud is dehydrated under pressure, the water in the mud is discharged into the filtrate storage tank through the filter cloth material, and then the filtrate valve is opened to drain the fluid out of the pressurized tank.
また、脱水処理された泥土は、脱水処理後にス
クリユー軸の一方向回転により、泥土排出開口に
向け移送され、加圧タンク外に排出されることに
なる。 Further, the dewatered mud is transferred toward the mud discharge opening by rotating the screw shaft in one direction after the dewatering treatment, and is discharged outside the pressurized tank.
[実施例]
以下本発明を図面に示す実施例に基づいて詳細
に説明する。[Example] The present invention will be described in detail below based on an example shown in the drawings.
実施例 1
第1図は本発明による脱水装置の実施例1の一
部切欠き側面図、第2図はそのA−A線に沿つた
断面図、第3図はその要部断面図、第4図は泥土
中における水分の分布状態を示す図である。Embodiment 1 FIG. 1 is a partially cutaway side view of Embodiment 1 of the dewatering device according to the present invention, FIG. 2 is a sectional view taken along line A-A, FIG. Figure 4 is a diagram showing the distribution of water in mud.
1は上部が開口したホツパーで、上部開口面に
格子状に形成された不図示のスクリーンが取り付
けられ、例えばバツクホー等の土木機械により掘
削された泥土(以下未脱水処理の泥土を源泥と称
す)が該スクリーンを通して投入される。ホツパ
ー1内に投入される源泥はこのスクリーンにより
粗大ゴミ等が取り除かれたり、またスクリーンを
加振器(不図示)を介して振動させることで格子
部分に引つ掛かつている大塊状の源泥を後段で脱
水するのに適する大きさに砕いて落下させる。2
は円筒横長の両端が閉塞したタンクで、断面略半
円弧状の下タンク部4′には水分を通過させるた
めの後記する多孔ケーシングが取り付けられ、こ
の下タンク部4′の外周部に取り付けられた濾液
受タンク3に溜められる。そしてこの濾液受タン
ク3はジヨイント部材5を介して上タンク部4に
連結され、濾液タンク開閉シリンダー21を駆動
させることで、濾液受タンク3を上タンク部4に
対し第2図に示す如く開閉させるようになつてお
り、ジヨイントピン6により閉位置にロツクされ
るようになつている。 1 is a hopper with an open top, and a screen (not shown) formed in a lattice pattern is attached to the top opening surface of the hopper, which is used to collect mud excavated by a civil engineering machine such as a backhoe (hereinafter undehydrated mud is referred to as source mud). ) is injected through the screen. The screen removes bulky dirt from the source mud that is introduced into the hopper 1, and the screen is vibrated via an exciter (not shown) to remove large chunks of dirt that are caught on the grid. The mud is crushed into a size suitable for dehydration later on and then dropped. 2
is a horizontally elongated cylindrical tank with both ends closed, and a porous casing (to be described later) for passing moisture is attached to a lower tank portion 4' having a substantially semicircular cross section, and is attached to the outer periphery of this lower tank portion 4'. The filtrate is stored in the filtrate receiving tank 3. The filtrate receiving tank 3 is connected to the upper tank section 4 via the joint member 5, and by driving the filtrate tank opening/closing cylinder 21, the filtrate receiving tank 3 can be opened and closed relative to the upper tank section 4 as shown in FIG. It is designed to be locked in the closed position by a joint pin 6.
上タンク部4の他端部は濾液受タンク3の延長
上まで延び、該他端部の下部に脱水処理された泥
土を吐出させる泥土吐出管16が取り付けられ、
空気又は油圧シリンダ16bにより泥土吐出弁1
6aを開放させることで泥土を泥土吐出管16か
ら排出させる。 The other end of the upper tank section 4 extends to an extension of the filtrate receiving tank 3, and a mud discharge pipe 16 for discharging dehydrated mud is attached to the lower part of the other end.
Mud discharge valve 1 by air or hydraulic cylinder 16b
Mud is discharged from the mud discharge pipe 16 by opening 6a.
また上タンク部4は頂部にタンク2内に収容さ
れる泥土のレベルを検知するレベルセンサー2
2、空気又は油圧シリンダ17bの駆動制御で開
閉する大気開放弁17aを有する大気開放管17
が設けられている。 In addition, the upper tank part 4 has a level sensor 2 at the top that detects the level of mud contained in the tank 2.
2. An atmosphere release pipe 17 having an atmosphere release valve 17a that opens and closes under drive control of an air or hydraulic cylinder 17b.
is provided.
下タンク部4′は、内周面に多孔ケーシング9
が設けられ、この多孔ケーシング9の外周面に濾
布10が添設され、この濾布10を多孔濾布カバ
ー11を介して多孔ケーシング9に取り外し可能
に固定している。 The lower tank part 4' has a porous casing 9 on its inner peripheral surface.
A filter cloth 10 is attached to the outer peripheral surface of the porous casing 9, and the filter cloth 10 is removably fixed to the porous casing 9 via a porous filter cloth cover 11.
また、濾液受タンク3は、一端部の下部に濾液
放出管18が取り付けられ、濾液受タンク3の内
部に溜つた濾液を濾液放出管18を通してタンク
外に放出させるようになつており、空気又は油圧
シリンダ18bの駆動で濾液放出弁18aの開閉
を行なうことで濾液放出管18の開閉が行なわれ
る。また、濾液受タンク3の一端壁部には内周面
と多孔濾布カバー11との間に濾布洗浄管19が
取り付けられ、空気又は油圧シリンダー19bに
より開閉制御される濾布洗浄弁19aを開放させ
ることで、洗浄空気を濾布洗浄管19を通してタ
ンク2内に供給し、濾布10の洗浄を行なう。 In addition, the filtrate receiving tank 3 has a filtrate discharge pipe 18 attached to the lower part of one end, and the filtrate accumulated inside the filtrate receiving tank 3 is discharged to the outside of the tank through the filtrate discharge pipe 18. The filtrate discharge pipe 18 is opened and closed by opening and closing the filtrate discharge valve 18a by driving the hydraulic cylinder 18b. In addition, a filter cloth cleaning pipe 19 is attached to one end wall of the filtrate receiving tank 3 between the inner circumferential surface and the porous filter cloth cover 11, and a filter cloth cleaning valve 19a is controlled to open and close by an air or hydraulic cylinder 19b. By opening it, cleaning air is supplied into the tank 2 through the filter cloth cleaning pipe 19 and the filter cloth 10 is cleaned.
また、タンク2の長さ方向一端部の上部には泥
土取入れ弁15を介してホツパー1の下部が取り
付けられ、この泥土取入れ弁15を空気又は油圧
シリンダ15a介して開放させることにより、ホ
ツパー1内の源泥が落下供給される。 Further, the lower part of the hopper 1 is attached to the upper part of one longitudinal end of the tank 2 via a mud intake valve 15, and by opening this mud intake valve 15 via air or a hydraulic cylinder 15a, the inside of the hopper 1 can be opened. The source mud is supplied by falling.
このタンク2内には、源泥の撹拌、移送及び脱
水用の圧縮空気の供給を兼ねる中空のスクリユー
軸12が長さ方向に沿つて回転可能に設けられ、
一方の貫通端部はロータリーシール13に接続さ
れ、他方の貫通端部にはスクリユー軸駆動モータ
7にチエーン8aを介して連結されるスクリユー
軸チエーンホイール8が固定され、このモータ7
の駆動力により回転する。なお、軸の回転は油圧
モータ等で行なつても良い。 Inside this tank 2, a hollow screw shaft 12, which also serves to stir and transport the source mud and supply compressed air for dewatering, is provided so as to be rotatable along the length direction.
One through end is connected to the rotary seal 13, and the other through end is fixed with a screw shaft chain wheel 8 connected to the screw shaft drive motor 7 via a chain 8a.
It rotates due to the driving force of. Note that the shaft may be rotated by a hydraulic motor or the like.
このスクリユー軸12は中空部がロータリーシ
ール13との接続端まで延び(他端部は閉塞され
ている)、また周壁12aに該中空部に連通する
多数のエアーノズル12bが形成されていて、加
圧弁20を開放すると不図示の圧縮空気源からの
圧縮空気がロータリーシール13、中空部を通し
てエアーノズル12bからタンク2内に噴出され
る。また、スクリユー軸12の外周には螺旋状に
スクリユー羽根14が形成され、スクリユー軸1
2の回転に応じてタンク2内の泥土を一端側から
他端側に向け撹拌しながら移送する。 The screw shaft 12 has a hollow portion extending to the connecting end with the rotary seal 13 (the other end is closed), and a number of air nozzles 12b communicating with the hollow portion are formed on the peripheral wall 12a. When the pressure valve 20 is opened, compressed air from a compressed air source (not shown) is ejected into the tank 2 from the air nozzle 12b through the rotary seal 13 and the hollow portion. Further, screw blades 14 are formed in a spiral shape on the outer periphery of the screw shaft 12.
According to the rotation of the tank 2, the mud in the tank 2 is transferred from one end to the other end while being stirred.
以上が本実施例1の構造であるが、その動作を
以下に説明する。 The structure of the first embodiment has been described above, and its operation will be explained below.
ホツパー1内の源泥をタンク2内に供給する
際、取入れ弁15、大気開放弁17a、濾液放出
弁18aは開弁状態とし、他の弁は閉状態にして
おく。なお、スクリユー軸12は常に回転駆動さ
れ、脱水処理中には時計方向及び反時計方向に適
当に回転されてタンク2内の一部分に泥土が溜ら
ないようにしており、脱水処理の終了時には泥土
吐出管16に向けて泥土を移送するように回転す
る。 When supplying the source mud in the hopper 1 into the tank 2, the intake valve 15, the atmosphere release valve 17a, and the filtrate discharge valve 18a are kept open, and the other valves are kept closed. The screw shaft 12 is always driven to rotate, and is appropriately rotated clockwise and counterclockwise during the dewatering process to prevent mud from accumulating in a part of the tank 2. At the end of the dewatering process, the mud is discharged. It rotates to transfer mud toward the pipe 16.
レベルセンサー22によりタンク2内の泥土が
満杯となつたことを検知すると、取入れ弁15、
大気開放弁17aを閉じ、タンク2内を密閉状態
にし、加圧弁20を開弁して、回転しているスク
リユー軸12のエアーノズル12aから圧縮空気
をタンク2内に圧気する。ここで、タンク2内に
収容されている源泥は、第4図に示すように、泥
土固形質の周囲に表面付着水、割れ目に割れ目毛
細管結合水、楔状毛細管結合水、間隙水、自由水
があり、また内部には内部水がある。そして、ス
クリユー軸12のエアーノズル12aから圧縮空
気がタンク2内に圧気されると、第3図に示すよ
うに、源泥を通して空気が多孔ケーシング9→濾
布10→多孔濾布カバーの順に通過し、圧縮空気
の通過に伴い源泥の水分が濾布10を通し、霧状
濾液となつて濾液受タンク3内に溜る。その際、
圧縮空気は第3図に示すように、固形質間に空気
が貫通して固形質内の内部水まで除去され、また
源泥はスクリユー軸により万べんに撹拌されてい
ることから一様に脱水されることとなる。 When the level sensor 22 detects that the tank 2 is full of mud, the intake valve 15,
The atmosphere release valve 17a is closed to seal the inside of the tank 2, and the pressurizing valve 20 is opened to supply compressed air into the tank 2 from the air nozzle 12a of the rotating screw shaft 12. As shown in Fig. 4, the source mud stored in the tank 2 includes surface adhesion water, crack capillary bound water, wedge-shaped capillary bound water, interstitial water, and free water around the solid mud. There is also internal water inside. When compressed air is pressurized into the tank 2 from the air nozzle 12a of the screw shaft 12, the air passes through the source mud in the order of the porous casing 9 → filter cloth 10 → porous filter cloth cover, as shown in FIG. As the compressed air passes through, water in the source mud passes through the filter cloth 10 and becomes a mist of filtrate, which accumulates in the filtrate receiving tank 3. that time,
As shown in Figure 3, the compressed air penetrates between the solids and even the internal water within the solids is removed, and the source mud is thoroughly stirred by the screw shaft, so it is uniformly mixed. It will be dehydrated.
圧縮空気をタンク2内に供給する時間、すなわ
ち脱水時間は、収容される源泥の量、源泥の含水
率、圧縮空気圧等に基づき、目標含水率に応じて
不図示のタイマーにより設定され、圧縮時間に達
すると、加圧弁20を開弁してタンク2内への圧
気を停止し、大気開放弁17aを開弁してタンク
2内を大気開放する。大気開放弁17aは、大気
開放弁開タイマーにより開弁時間が制御され、大
気開放弁開タイマーのタイムアツプで吐出弁16
aを開弁し、タンク2内の脱水処理された処理泥
をタンク外に吐出する。 The time for supplying compressed air into the tank 2, that is, the dewatering time, is set by a timer (not shown) according to the target moisture content based on the amount of source mud contained, the moisture content of the source mud, the compressed air pressure, etc. When the compression time is reached, the pressurizing valve 20 is opened to stop supplying pressurized air into the tank 2, and the atmosphere release valve 17a is opened to release the inside of the tank 2 to the atmosphere. The opening time of the atmosphere release valve 17a is controlled by an atmosphere release valve open timer, and the discharge valve 16 is closed when the atmosphere release valve open timer times up.
Open the valve a and discharge the dehydrated treated mud in the tank 2 to the outside of the tank.
吐出弁16aの開弁と同時に、濾液放出弁18
aを閉弁、濾布洗浄弁19aを開弁して、多孔ケ
ーシング9、濾布10、多孔濾布カバー11を空
気洗浄する。吐出弁16aの開弁時間は吐出弁タ
イマーにより制御され、吐出弁タイマーのタイム
アツプで吐出弁16a、濾布洗浄弁19a、大気
開放弁17aが閉弁、取入れ弁15、濾液放出弁
18aを開弁して再び源泥をタンク2内に取入れ
る。 Simultaneously with the opening of the discharge valve 16a, the filtrate discharge valve 18
Close the valve a, open the filter cloth cleaning valve 19a, and clean the porous casing 9, filter cloth 10, and porous filter cloth cover 11 with air. The opening time of the discharge valve 16a is controlled by a discharge valve timer, and when the discharge valve timer times up, the discharge valve 16a, the filter cloth cleaning valve 19a, and the atmosphere release valve 17a are closed, and the intake valve 15 and the filtrate discharge valve 18a are opened. Then, the source mud is taken into tank 2 again.
なお、本実施例1は、1つのホツパー1に対し
て、1台のタンク2を取り付けているが、例えば
2台以上のタンク2を取付け、連続に脱水処理を
行なうようにすれば、一層脱水処理能力が向上す
る。 In the first embodiment, one tank 2 is attached to one hopper 1, but if two or more tanks 2 are attached and dehydration is performed continuously, the dehydration can be further improved. Processing power is improved.
実施例 2 第5図は実施例2の概略断面図である。Example 2 FIG. 5 is a schematic cross-sectional view of the second embodiment.
本実施例は、ホツパー1に下部開口を2つ形成
し、各開口に設けた取入れ弁31,32を介して
竪配置された共に同一構造の2つのタンク33,
34に夫々接続されている。 In this embodiment, two lower openings are formed in the hopper 1, and two tanks 33, both having the same structure, are arranged vertically through intake valves 31 and 32 provided in each opening.
34, respectively.
このタンク33,34は、下部が開口した不図
示のタンク側板内に、筒状の多孔ケーシング35
の外周面に濾布36を添設し、この濾布36を外
側から多孔濾布カバー37で多孔ケーシング35
に取り外し可能に固定した構造で、下端には脱水
処理された泥土を排出させる吐出弁38,39が
取り付けられ、内部中央には多数のエアーノズル
40が形成された圧気管41,42が上下方向に
設けられ、夫々加圧弁43,44を開弁すること
により不図示の圧縮空気源からの圧縮空気がタン
ク内に供給されるようになつている。 The tanks 33 and 34 have a cylindrical porous casing 35 inside a tank side plate (not shown) that is open at the bottom.
A filter cloth 36 is attached to the outer peripheral surface of the porous casing 35, and this filter cloth 36 is attached to the porous casing 35 from the outside with a porous filter cloth cover 37.
It has a structure that is removably fixed to the bottom end, and discharge valves 38 and 39 for discharging dehydrated mud are attached to the lower end, and air pressure pipes 41 and 42 in which a number of air nozzles 40 are formed in the center of the interior are installed in the vertical direction. Compressed air from a compressed air source (not shown) is supplied into the tank by opening pressurizing valves 43 and 44, respectively.
一方、タンク33,34は、そのタンク側板下
端が多孔ケーシング35の下端よりも上方に位置
し、下端に濾液を受ける濾液皿45が設けられ、
不図示の濾液管を通して濾液皿45内の濾液が排
出される。 On the other hand, the lower ends of the tank side plates of the tanks 33 and 34 are located above the lower end of the porous casing 35, and a filtrate tray 45 for receiving the filtrate is provided at the lower end.
The filtrate in the filtrate dish 45 is discharged through a filtrate pipe (not shown).
43′,44′はタンク33,34に夫々設けら
れた大気開放弁である。 43' and 44' are atmospheric release valves provided in the tanks 33 and 34, respectively.
なお、各弁は夫々空気シリンダ等により開閉制
御される。 The opening and closing of each valve is controlled by an air cylinder or the like.
以上が本実施例の構造であるが、以下にその動
作を説明する。 The structure of this embodiment has been described above, and its operation will be explained below.
本実施例の脱水装置は、ホツパー1内の源泥を
タンク33,34に交互に供給して脱水処理を行
なうもので、例えば取入れ弁31を開弁してタン
ク33内に源泥を取入れる場合、取入れ弁32を
閉弁、また加圧弁44を開弁してタンク34内に
圧縮空気を供給し収容された源泥の脱水処理を行
なう。脱水処理は前述実施例と同様に圧縮空気が
源泥を通し、多孔ケーシング35→濾布36→多
孔濾布カバー37を通過する際に、霧状濾液とし
て脱水され、濾液皿45に溜る。そして、タンク
34の脱水処理が終了すると、加圧弁44を閉
弁、大気開放弁44′を開弁した後、吐出弁39
を開弁し、タンク34内の処理泥を自重により落
下排出させ、また取入れ弁31を閉弁してタンク
33への源泥の供給を停止し、タンク33に供給
された源泥の脱水処理を開始可能な状態にする。
タンク34内の処理泥の排出が完了すると、吐出
弁39、取入れ弁32を開弁してタンク34内へ
源泥を供給し、また大気開放弁43′を閉弁し加
圧弁43を開弁してタンク33内の源泥の脱水処
理を開始する。 The dewatering device of this embodiment performs dewatering by alternately supplying the source mud in the hopper 1 to the tanks 33 and 34. For example, the intake valve 31 is opened and the source mud is introduced into the tank 33. In this case, the intake valve 32 is closed and the pressurizing valve 44 is opened to supply compressed air into the tank 34 to dewater the stored source mud. In the dewatering process, as in the previous embodiment, when compressed air passes through the source mud and passes through the porous casing 35 → filter cloth 36 → porous filter cloth cover 37, water is dehydrated as a mist of filtrate, which accumulates in the filtrate tray 45. When the dehydration process of the tank 34 is completed, the pressurizing valve 44 is closed, the atmosphere release valve 44' is opened, and the discharge valve 39 is opened.
The valve is opened to allow the treated mud in the tank 34 to fall and discharge under its own weight, and the intake valve 31 is closed to stop supplying the source mud to the tank 33, and the source mud supplied to the tank 33 is dehydrated. Make it ready to start.
When the discharge of the treated mud in the tank 34 is completed, the discharge valve 39 and the intake valve 32 are opened to supply the source mud into the tank 34, and the atmosphere release valve 43' is closed and the pressurizing valve 43 is opened. Then, dewatering of the source mud in the tank 33 is started.
そして、この動作を繰り弁すことで、略連続し
た脱水処理が行なえることになる。 By repeating this operation, substantially continuous dehydration processing can be performed.
この用に構成した本実施例は、前述の実施例1
と同様に高率の脱水処理ができる他、実施例1の
ように回転部分がないので、構造が簡単になると
いつた効果もある。 This embodiment configured for this purpose is similar to the embodiment 1 described above.
In addition to being able to carry out high-rate dehydration treatment in the same manner as in Example 1, there is also the effect of simplifying the structure since there are no rotating parts as in Example 1.
なお、本実施例では脱水処理されさ泥土を自重
によりタンク内から落下させるようにしているの
で、タンクの内形状(多孔ケーシング35の内形
状)を下方が拡がる截頭錐形状とすると処理泥の
自重落下性が向上する。 In addition, in this embodiment, since the dewatered mud is allowed to fall from the tank by its own weight, if the internal shape of the tank (the internal shape of the porous casing 35) is a truncated cone shape that widens at the bottom, the treated mud will fall. Improves self-weight falling properties.
また、タンクを2基用いて交互運転を行なつて
いるが、実施例1と同様に1基であつてもよく、
又3基以上設けて連続運転してもよい。 Also, although two tanks are used for alternate operation, it is also possible to use only one tank as in Example 1.
Moreover, three or more units may be provided and operated continuously.
[発明の効果]
以上説明してきたように、本発明は加圧タンク
内に一定量収容された泥土を圧縮空気により脱水
するバツチ式の脱水装置であり、泥土を撹拌を撹
拌しながら脱水処理を行うので、一様な脱水が行
え、効率の良い脱水処理が実現できる。[Effects of the Invention] As explained above, the present invention is a batch-type dewatering device that dewaters a certain amount of mud stored in a pressurized tank using compressed air, and dewaters the mud while stirring the mud. As a result, uniform dehydration can be performed and efficient dehydration processing can be achieved.
また、スクリユー軸は、圧縮空気の供給、泥土
の撹拌及び脱水処理された泥土を移送する機能を
有するため、加圧タンク内の構造等を簡素化する
ことができる効果もある。 Further, since the screw shaft has the functions of supplying compressed air, stirring the mud, and transporting the dehydrated mud, it also has the effect of simplifying the structure inside the pressurized tank.
さらに、泥土の撹拌機能を備えたスクリユー軸
から脱水処理を行うための圧縮空気を噴出させる
ため、すなわち処理泥土を濾布材に押しつけたよ
うな状態での脱水処理が行えるため、脱水効率が
向上する。 Furthermore, since compressed air for dewatering is ejected from the screw shaft, which has a mud stirring function, dewatering can be performed while the treated mud is pressed against the filter material, improving dewatering efficiency. do.
第1図は本発明による脱水装置の実施例1を示
す一部切欠き側面図、第2図は第1図のA−A線
に沿つた断面図、第3図は脱水状態を説明第1図
の要部断面図、第4図は泥土中の水分の挙動を説
明する図、第5図は実施例2の脱水装置の概略断
面図である。
1……ホツパー、2,33,34……タンク、
3……下タンク部、4……上タンク部、5……ジ
ヨイント部材、6……ジヨイントピン、7……ス
クリユー軸駆動モータ、8……スクリユー軸チエ
ーンホイール、9,35……多孔ケーシング、1
0,36……濾布、11,37……多孔濾布カバ
ー、12……スクリユー軸エアーノズル、13…
…ロータリーシール、14……スクリユー羽根、
15,31,32……取入れ弁、16……吐出
管、17……大気開放管、18……濾液放出管、
19……濾布洗浄管、20,43,44……加圧
弁、21……濾液タンク開閉シリンダ。
FIG. 1 is a partially cutaway side view showing Embodiment 1 of the dewatering device according to the present invention, FIG. FIG. 4 is a diagram illustrating the behavior of water in mud, and FIG. 5 is a schematic sectional view of the dewatering device of Example 2. 1... Hopper, 2, 33, 34... Tank,
3...Lower tank part, 4...Upper tank part, 5...Joint member, 6...Joint pin, 7...Screw shaft drive motor, 8...Screw shaft chain wheel, 9, 35...Porous casing, 1
0,36...Filter cloth, 11,37...Porous filter cloth cover, 12...Screw shaft air nozzle, 13...
...Rotary seal, 14...Screw blade,
15, 31, 32...Intake valve, 16...Discharge pipe, 17...Atmospheric release pipe, 18...Filtrate discharge pipe,
19... Filter cloth cleaning pipe, 20, 43, 44... Pressure valve, 21... Filtrate tank opening/closing cylinder.
Claims (1)
給開口部及び脱水処理した泥土を排出する処理泥
土排出開口部を有し、胴部の下部部分に濾布材を
仕切り壁として外側板との間に濾液貯槽が形成さ
れた密閉可能な横長形式の圧力タンクと、脱水処
理時には該泥土供給開口部を閉じ、泥土の供給時
には該泥土供給開口部を開く泥土取り入れ弁と、
脱水処理時には該泥土排出開口部を閉じ、処理泥
土の排出時には該泥土排出開口部を開く泥土吐出
弁と、該圧力タンク内にその軸方向に沿つて配置
され、圧縮空気が軸内を通して多数のノズルから
噴出すると共に、脱水処理時には正逆回転により
該圧力タンク内の泥土を撹拌し、脱水処理の終了
時には一方向回転により脱水泥土を処理泥土排出
開口部に向けて移送するスクリユー軸と、該圧力
タンクに形成された濾液貯槽内の濾液をタンク外
に廃液するための濾液弁とを有し、脱水処理時に
は該圧力タンク内に密閉状態に保持して該スクリ
ユー軸内に圧縮空気を供給し、圧縮空気の加圧に
より該濾布材を通して泥土の水分を該濾液貯槽に
排出することを特徴とする脱水装置。 2 前記加圧タンクの胴部の略下半部分は、開閉
可能に構成したことを特徴とする請求項1に記載
の脱水装置。 3 上部に泥土供給手段からの泥土が供給される
泥土供給開口部を有すると共に、下部に処理泥土
排出用の泥土排出開口部を有し、周面に濾布材を
有する竪型筒状の加圧タンクと、泥土供給時には
該泥土供給開口部を開口し、脱水処理時には閉じ
る泥土取り入れ弁と、泥土排出時には該泥土排出
部を開口し、脱水処理時には閉じる泥土吐出弁
と、脱水処理時に圧縮空気が管内を通して多数の
ノズルから噴出する該加圧タンク内に配置された
圧気管と、該タンクの濾布材を通した濾液を受け
る濾液受け手段とを備え、該圧気管から噴出する
圧気により泥土から出た水分を該濾布材を通して
濾液受け手段に廃液することを特徴とする脱水装
置。[Scope of Claims] 1. It has a mud supply opening through which mud is supplied from the mud supply means and a treated mud discharge opening through which dehydrated mud is discharged, and a filter cloth material is attached to the lower part of the body as a partition wall. a sealable horizontal pressure tank with a filtrate storage tank formed between it and an outer plate; a mud intake valve that closes the mud supply opening during dewatering processing and opens the mud supply opening when mud is supplied;
A mud discharge valve that closes the mud discharge opening during dewatering processing and opens the mud discharge opening when discharging the treated mud; A screw shaft that ejects from a nozzle, agitates the mud in the pressure tank by forward and reverse rotation during dewatering processing, and transfers the dehydrated mud toward a treated mud discharge opening by rotating in one direction when dewatering processing is completed; It has a filtrate valve for discharging the filtrate in the filtrate storage tank formed in the pressure tank to the outside of the tank, and during dehydration processing, the pressure tank is kept in a sealed state and compressed air is supplied into the screw shaft. A dewatering device characterized in that water in the mud is discharged into the filtrate storage tank through the filter cloth material by pressurizing compressed air. 2. The dewatering device according to claim 1, wherein substantially the lower half of the body of the pressurized tank is configured to be openable and closable. 3 A vertical cylindrical filter having a mud supply opening in the upper part for supplying mud from the mud supply means, a mud discharge opening for discharging treated mud in the lower part, and having a filter cloth material on the circumference. A pressure tank, a mud intake valve that opens the mud supply opening during mud supply and closes it during dewatering, a mud discharge valve that opens the mud discharge port when mud is discharged and closes it during dewatering, and compressed air during dewatering. The pressurized air pipe is disposed in the pressurized tank through which water is ejected from a number of nozzles through the pipe, and the filtrate receiving means receives the filtrate that has passed through the filter cloth material of the tank. A dewatering device characterized in that water released from the filter is drained into a filtrate receiving means through the filter cloth material.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63253248A JPH02102706A (en) | 1988-10-07 | 1988-10-07 | Dehydrator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63253248A JPH02102706A (en) | 1988-10-07 | 1988-10-07 | Dehydrator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH02102706A JPH02102706A (en) | 1990-04-16 |
| JPH0512003B2 true JPH0512003B2 (en) | 1993-02-17 |
Family
ID=17248625
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP63253248A Granted JPH02102706A (en) | 1988-10-07 | 1988-10-07 | Dehydrator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH02102706A (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH07111064B2 (en) * | 1990-12-07 | 1995-11-29 | 日立造船株式会社 | Dredged material transport device |
| DE102006037169A1 (en) * | 2006-08-09 | 2008-02-14 | Robert Bosch Gmbh | Method for producing a coil, in particular an ignition coil for a motor vehicle |
| CN105668980B (en) * | 2016-03-02 | 2018-08-07 | 普利资环境科技(苏州)有限公司 | A kind of sludge heat drying device |
-
1988
- 1988-10-07 JP JP63253248A patent/JPH02102706A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPH02102706A (en) | 1990-04-16 |
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