JPS6238730Y2 - - Google Patents
Info
- Publication number
- JPS6238730Y2 JPS6238730Y2 JP15665584U JP15665584U JPS6238730Y2 JP S6238730 Y2 JPS6238730 Y2 JP S6238730Y2 JP 15665584 U JP15665584 U JP 15665584U JP 15665584 U JP15665584 U JP 15665584U JP S6238730 Y2 JPS6238730 Y2 JP S6238730Y2
- Authority
- JP
- Japan
- Prior art keywords
- drainage
- pressure
- chute
- water
- air
- 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
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 24
- 239000008187 granular material Substances 0.000 claims description 18
- 239000007788 liquid Substances 0.000 claims description 13
- 230000018044 dehydration Effects 0.000 claims description 10
- 238000006297 dehydration reaction Methods 0.000 claims description 10
- 238000000926 separation method Methods 0.000 claims description 5
- 239000002245 particle Substances 0.000 description 10
- 239000007787 solid Substances 0.000 description 6
- 238000010586 diagram Methods 0.000 description 3
- 230000002265 prevention Effects 0.000 description 3
- 239000010419 fine particle Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- NJPPVKZQTLUDBO-UHFFFAOYSA-N novaluron Chemical compound C1=C(Cl)C(OC(F)(F)C(OC(F)(F)F)F)=CC=C1NC(=O)NC(=O)C1=C(F)C=CC=C1F NJPPVKZQTLUDBO-UHFFFAOYSA-N 0.000 description 2
- 238000005192 partition Methods 0.000 description 2
- 101150054854 POU1F1 gene Proteins 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
Landscapes
- Drying Of Solid Materials (AREA)
- Centrifugal Separators (AREA)
Description
【考案の詳細な説明】
産業上の利用分野
本考案は、水分を含む砂利、砕石、砂、土或い
はこれらの混合物等の含水粒体を乾燥等の加熱手
段を伴わずに機械的に固液分離して脱水させる脱
水装置に関するものである。[Detailed description of the invention] Industrial application field The invention is a method for mechanically converting water-containing particles such as gravel, crushed stone, sand, soil, or mixtures thereof into solid-liquid without drying or other heating means. This relates to a dehydration device that separates and dehydrates the water.
従来の技術
この種脱水装置の基本的構成は本出願人に係る
特公昭55−24029号で示されている。この脱水装
置は長筒状の脱水筒(圧送筒)に投入された含水
粒体をその一端側から導入される空気により他端
開口(放出口)から射出し、放出口に対向する回
転板に衝突させることにより粒体と水分とを分離
し、水分を回転板の周囲に固設した金網からなる
仕切板(固液分離板)より透過させて液体シユー
トから排出すると共に、粒体を固体シユートより
回収している。Prior Art The basic structure of this type of dewatering device is shown in Japanese Patent Publication No. 55-24029 filed by the present applicant. This dehydration device uses air introduced from one end of the water-containing granules put into a long cylindrical dehydration cylinder (pressure-feeding cylinder) to eject them from an opening at the other end (discharge port) and onto a rotating plate facing the discharge port. The granules and water are separated by collision, and the moisture is passed through a partition plate (solid-liquid separation plate) made of a wire mesh fixed around the rotating plate and discharged from the liquid chute, and the granules are separated from the solid chute. We are collecting more.
考案が解決しようとする問題点
圧送筒に導入された空気によつて含水粒体を装
置内に送り込み、かつ、固液分離しているが、上
記構造の脱水装置における脱水処理能力は空気流
によつて決まる。そして、処理能力の向上を図る
ためには空気の排出量を多くする必要があるが、
従来の脱水装置ではシユートの断面積が小さく空
気の排出量に限界があるので、送風量が増えず、
含水粒体の単位時間当たりの送り込み量を増大さ
せることができない。その為含水粒体を脱水する
のに時間が掛り、作業能率が悪いという欠点があ
つた。Problems that the invention aims to solve Water-containing particles are fed into the device by air introduced into the pressure cylinder and solid-liquid separation is carried out, but the dehydration processing capacity of the dehydration device with the above structure is limited by the air flow. It's decided by then. In order to improve processing capacity, it is necessary to increase the amount of air discharged.
In conventional dehydration equipment, the cross-sectional area of the chute is small and there is a limit to the amount of air discharged, so the amount of air blown cannot be increased.
It is not possible to increase the amount of water-containing granules fed per unit time. As a result, it took time to dehydrate the water-containing granules, resulting in poor working efficiency.
問題点を解決するための手段
本考案は、圧送筒3に投入された含水粒体を、
圧送筒3の一端側の送風口3aより導入される空
気により他端側の放出口3bから射出させ、圧送
筒3の放出口3bと対向位置に配設された回転板
6に衝突させ、該回転板6の周囲に配されて回転
板6と1体となつて回転し、かつ、上記圧送筒3
側にラツパ状に拡開した脱水篭11を介して固液
分離し、粒体より分離された水分を排水シユート
15を介して排水ピツト16に排出するようにし
た脱水装置において、上記排水シユート15から
空気を強制的に吸引するためのサイクロン20
に、吸引ダクト22,26或いは30の一端を接
続開口し、かつ、該ダクト22の他端を排水シユ
ート15或いは排水ピツト16の少なくとも一方
に接続開口したものである。Means for Solving the Problems The present invention allows the water-containing granules charged into the pressure feeding tube 3
The air introduced from the air outlet 3a at one end of the pressure-feeding tube 3 is injected from the outlet 3b at the other end, and is caused to collide with the rotary plate 6 disposed opposite the outlet 3b of the pressure-feeding tube 3. It is arranged around the rotary plate 6 and rotates as one body with the rotary plate 6, and the pressure feeding cylinder 3
In the dewatering apparatus, solid-liquid separation is carried out through a dewatering basket 11 which is expanded in a lattice shape on the side, and water separated from the granules is discharged into a drainage pit 16 through a drainage chute 15. Cyclone 20 for forcibly sucking air from
One end of the suction duct 22, 26 or 30 is opened for connection, and the other end of the duct 22 is opened for connection to at least one of the drainage chute 15 or the drainage pit 16.
実施例
以下本考案を図示の実施例に基づいて説明する
と次の通りである。Embodiments The present invention will be described below based on illustrated embodiments.
第1図および第2図において、1はケーシング
で、架台2上に設置されている。3はケーシング
1内にその側方より全長の略半分を水平状態にし
て挿入した円筒状の圧送筒で、この圧送筒3の外
端には送風機4に接続される送風口3aが開設さ
れ、同内端には放出口3bが開口している。5は
圧送筒3の後部に配置したホツパーで、圧送筒3
内への投下位置直前で空気流速が増大して含水粒
体の堆積残留を防止するように、開口縁5aが圧
送筒3の中心付近まで突入して放出口3b側へ向
くように傾斜して開口している。また圧送筒3の
放出口3b側の外周囲には、回転板6と対向する
小径な第1の飛散防止板7と、その後方に位置す
る大径な第2の飛散防止板8とが圧送筒3に対し
直立して固設されている。上記回転板6は、回転
軸9の内端に固着されて放出口3bと対向するよ
うにケーシング1内に配され、かつ、該回転軸9
のケーシング1外に突出した先端に取付けたプー
リー10を介してモータ(図示省略)等の駆動装
置により回転駆動するように構成されている。1
1は回転板6と一体回転する脱水篭で、これは飛
散防止板7,8の外周端に対して所定間隔を有す
るように圧送筒3の送風口3a側へ拡開した形状
を備えており、粒体は通過不能で水分のみを透過
させる固液分離機能を有している。12は脱水さ
れた粒体が流入するケーシング1内の固体集合
室、13は固体集合室12の下方に設けた固体シ
ユート、14は粒体から分離した水分が流入する
液体集合室、15は液体集合室14の下方に設け
た排水シユートである。 In FIGS. 1 and 2, 1 is a casing, which is installed on a pedestal 2. Reference numeral 3 denotes a cylindrical pressure tube inserted into the casing 1 from the side with approximately half of its total length in a horizontal state, and an air outlet 3a connected to a blower 4 is provided at the outer end of the pressure tube 3. A discharge port 3b is opened at the inner end. 5 is a hopper placed at the rear of the pressure-feeding tube 3;
The opening edge 5a extends to the vicinity of the center of the pressure-feeding tube 3 and is inclined toward the discharge port 3b so that the air flow velocity increases just before the position of dropping into the container and prevents the accumulation and residual of water-containing particles. It's open. Further, around the outer periphery of the discharge port 3b side of the pressure-feeding cylinder 3, there is a first scattering prevention plate 7 with a small diameter facing the rotary plate 6, and a second scattering prevention plate 8 with a large diameter located behind it. It is fixed upright to the cylinder 3. The rotary plate 6 is fixed to the inner end of the rotary shaft 9 and is disposed within the casing 1 so as to face the discharge port 3b.
It is configured to be rotated by a drive device such as a motor (not shown) via a pulley 10 attached to the tip protruding outside the casing 1 of the casing 1. 1
Reference numeral 1 designates a dewatering basket that rotates integrally with the rotary plate 6, and has a shape that expands toward the air outlet 3a side of the pressure-feeding tube 3 so as to have a predetermined distance from the outer circumferential ends of the scattering prevention plates 7 and 8. , the granules have a solid-liquid separation function that allows only water to pass through and not allow them to pass through. 12 is a solid collecting chamber in the casing 1 into which dehydrated granules flow, 13 is a solid chute provided below the solid collecting chamber 12, 14 is a liquid collecting chamber into which water separated from the granules flows, and 15 is a liquid collecting chamber. This is a drainage chute provided below the gathering room 14.
16は地面下に密封して設けた排水ピツトで、
この排水ピツト16に上記の排水シユート15の
先端を接続開口する。17は排水ピツト16内に
設置した水中ポンプ、18は水中ポンプ17に接
続した排水パイプ、19は排水ピツト16内を区
画するように立設した金網からなる濾材、20は
上記排水シユート15から空気を強制的に吸引す
るためのサイクロンで、このサイクロン20は架
台21上に設置されている。22は吸引ダクト
で、このダクト22の一端をサイクロン20の上
部20aに接続開口し、かつ、他端を排水ピツト
16に接続開口する。そして、排水ピツト16内
に浮遊する微細な粒体を空気と共に吸引ダクト2
2を介してサイクロン20に吸引し、かつ、遠心
分離し、これら粒体が大気中に飛散するのを防止
する。23は両端を排水ピツト16及びサイクロ
ン20の下部20bにそれぞれ接続開口した接続
パイプで、この接続パイプ23により、遠心分離
されてサイクロン20の下部20bに集められた
粒体を排水ピツト16に戻す。24,25は排水
シユート15及び吸引ダクト22内にそれぞれ設
けたダンパーである。 16 is a drainage pit sealed under the ground.
The distal end of the drain chute 15 is connected to the drain pit 16 and opened. 17 is a submersible pump installed in the drainage pit 16, 18 is a drainage pipe connected to the submersible pump 17, 19 is a filter material made of a wire mesh installed upright to partition the inside of the drainage pit 16, and 20 is an air source from the drainage chute 15. This cyclone 20 is installed on a pedestal 21. A suction duct 22 has one end connected to the upper part 20a of the cyclone 20 and the other end connected to the drainage pit 16. The fine particles floating in the drainage pit 16 are then sucked into the suction duct 2 along with the air.
2 into a cyclone 20 and centrifuged to prevent these particles from scattering into the atmosphere. Reference numeral 23 denotes a connecting pipe whose both ends are connected to the drainage pit 16 and the lower part 20b of the cyclone 20, respectively, and the granules centrifuged and collected in the lower part 20b of the cyclone 20 are returned to the drainage pit 16 through this connecting pipe 23. 24 and 25 are dampers provided in the drainage chute 15 and the suction duct 22, respectively.
而して、上記構成の脱水装置により含水粒体の
脱水処理を行うには、回転板6および脱水篭11
を一体回転すると共に、送風機4によつて圧送筒
3内に送風口3aから空気を所定流量で送りなが
ら、ホツパー5より含水粒体を圧送筒3内へ投入
し、空気流により放出口3b側へ圧送する。これ
と同時にサイクロン20を作動させ、排水ピツト
16内の空気を吸引して減圧し、該排水ピツト1
6と連通する排水シユート15に吸引力を作用さ
せる。この吸引力によつて排水シユート15から
空気が強制的に吸引されるので、空気の排出量が
多くなると共に、それだけ圧送筒3への送風量が
増え、含水粒体の単位時間当たりの送り込み量が
大幅に増大する。そうして、空気流の圧送によつ
て放出口3bから射出された含水粒体は回転板6
に衝突して跳ね返り、更に第1飛散防止板7に衝
突して再び回転板6に衝突し、この衝突を繰る返
す過程で粒体と水分とが完全に分離し、粒体は第
1飛散防止板7と脱水篭11との間隙より次第に
外周方向へ移動し、更に回転している脱水篭11
の遠心力により傾斜内面に誘導されて脱水篭11
前方のケーシング1内の固体集合室12に入り、
その下方の固体シユート13から脱水された状態
で回収される。他方粒体から分離して飛散した水
分は脱水篭11を通過してその背面側の液体集合
室に入り、その下方の排水シユート15を介して
排水ピツト16に送られる。 Therefore, in order to dehydrate the water-containing granules using the dehydrating device having the above configuration, the rotating plate 6 and the dehydrating basket 11 are required.
At the same time, while the blower 4 is sending air at a predetermined flow rate from the air outlet 3a into the pressure tube 3, the water-containing granules are introduced into the pressure tube 3 from the hopper 5, and the air flow causes the water-containing particles to be transferred to the discharge port 3b side. to be pumped to. At the same time, the cyclone 20 is activated to suck the air inside the drain pit 16 and reduce the pressure.
A suction force is applied to the drainage chute 15 communicating with the drain chute 6. Since air is forcibly sucked from the drainage chute 15 by this suction force, the amount of air discharged increases, and the amount of air blown to the pressure feeding tube 3 increases accordingly, resulting in the amount of water-containing granules fed per unit time. increases significantly. Then, the water-containing particles ejected from the discharge port 3b by the air flow are transferred to the rotary plate 6.
The particles collide with the first anti-scattering plate 7, and then again the rotating plate 6. In the process of repeating this collision, the particles and water are completely separated, and the particles are bounced off the first anti-scattering plate 7. The dehydration basket 11 gradually moves toward the outer circumference from the gap between the plate 7 and the dehydration basket 11 and is further rotated.
The dewatering basket 11 is guided to the inclined inner surface by the centrifugal force of
Enter the solid collection chamber 12 in the front casing 1,
It is recovered in a dehydrated state from the solid chute 13 below. On the other hand, the water separated and scattered from the granules passes through the dehydration basket 11, enters the liquid collection chamber on the back side thereof, and is sent to the drainage pit 16 via the drainage chute 15 below.
上記排水ピツト16はサイクロン20の吸引力
によつて減圧され、排水シユート15に吸引力が
作用しているので、該排水シユート15或いは排
水ピツト16内に浮遊する微細な粒体は空気と共
に吸引ダクト21を介してサイクロン20に吸引
され、かつ、遠心分離され、該サイクロン20の
下部に集められた後、接続パイプ23を介して排
水ピツト16に戻される。尚、上記排水ピツト1
6の減圧度の調整は上記ダンパー24,25によ
り行えばよい。 The drainage pit 16 is depressurized by the suction force of the cyclone 20, and since the suction force is acting on the drainage chute 15, the fine particles floating in the drainage chute 15 or the drainage pit 16 are sucked into the suction duct along with the air. The water is sucked into the cyclone 20 via the cyclone 21, centrifuged and collected at the bottom of the cyclone 20, and then returned to the drainage pit 16 via the connecting pipe 23. In addition, the above drainage pit 1
The degree of pressure reduction in step 6 may be adjusted using the dampers 24 and 25.
第3図は本考案の他の実施例を示したもので、
上記実施例と同一部分は同一符号で示し、その説
明は省略する。すなわち、本実施例は、サイクロ
ン20の上部に連通する吸引ダクト26の先端を
排水シユート15の基部15aに接続開口したも
のである。尚、27は排風ダクト28を介してサ
イクロン20の上面部に接続した撹拌機で、この
撹拌機27はさらにダクト27を介して湿式集塵
装置(図示省略)に接続される。30は吸引ダク
ト28内に設けたダンパーである。 Figure 3 shows another embodiment of the present invention.
The same parts as in the above embodiment are indicated by the same reference numerals, and the explanation thereof will be omitted. That is, in this embodiment, the tip of the suction duct 26 communicating with the upper part of the cyclone 20 is connected to the base 15a of the drainage chute 15. Note that 27 is an agitator connected to the upper surface of the cyclone 20 via an exhaust duct 28, and this agitator 27 is further connected to a wet dust collector (not shown) via the duct 27. 30 is a damper provided within the suction duct 28.
第4図は本考案のさらに他の実施例を示したも
ので、本実施例は、サイクロン20の上部に連通
する吸引ダクト31を分岐させ、一方の分岐ダク
ト31aを排水シユート15の基部15aに又他
方の分岐ダクト31bを前記排水ピツト16に接
続開口したものである。32,33は各分岐ダク
ト31a,31b内に設けたダンパーである。 FIG. 4 shows still another embodiment of the present invention, in which the suction duct 31 communicating with the upper part of the cyclone 20 is branched, and one branch duct 31a is connected to the base 15a of the drainage chute 15. The other branch duct 31b is connected to the drainage pit 16 and opened. 32 and 33 are dampers provided in each branch duct 31a and 31b.
尚、前記圧送筒3に送られた空気の送風量を増
大させる手段として、上記実施例の外に排水シユ
ート15の一部に大気に開放した分岐ダクトを固
設してもよいし、或いは排水シユート15の断面
積を大きくしてもよい。 As a means for increasing the amount of air sent to the pressure tube 3, in addition to the above embodiment, a branch duct open to the atmosphere may be fixed in a part of the drainage chute 15, or a branch duct open to the atmosphere may be installed. The cross-sectional area of the chute 15 may be increased.
また、前記圧送筒3の下面には第5図に示すよ
うにケーシング1内外の各数ケ所にスリツト板3
4を斜めに装着し、ケーシング1外のスリツト板
34の下方には第1の液体シユート35を配設
し、ケーシング1内のスリツト板34の下方には
第2の液体シユート36を配設し、両液体シユー
ト35,36をケーシング1外で合流させてもよ
い。 Furthermore, on the lower surface of the pressure-feeding cylinder 3, there are slit plates 3 at several locations inside and outside the casing 1, as shown in FIG.
4 is installed diagonally, a first liquid chute 35 is arranged below the slit plate 34 outside the casing 1, and a second liquid chute 36 is arranged below the slit plate 34 inside the casing 1. , both liquid chute 35 and 36 may be combined outside the casing 1.
考案の効果
本考案によれば、空気の排出量が多くなり、そ
れだけ送風量が増えるから、含水粒体の単位時間
当たりの圧送筒への送り込み量が大幅に増大す
る。その結果、大量の含水粒体を短時間で脱水す
ることが可能となり、作業能率の大幅な向上を図
ることができる。Effects of the invention According to the invention, the amount of air discharged increases and the amount of air blown increases accordingly, so the amount of water-containing particles sent into the pressure tube per unit time increases significantly. As a result, it becomes possible to dehydrate a large amount of water-containing granules in a short time, and work efficiency can be greatly improved.
第1図は本考案に係る脱水装置の第1の実施例
を示した一部断面説明図、第2図は脱水装置の一
部省略縦断面図、第3図は脱水装置の第2の実施
例を示した一部断面説明図、第4図は脱水装置の
第3実施例を示した一部断面説明図、第5図は圧
送筒にスリツト板を装着した脱水装置の一部省略
縦断面図である。
3……圧送筒、3a……送風口、3b……放出
口、6……回転板、11……脱水篭、15……排
水シユート、16……排水ピツト、20……サイ
クロン、22,26,30……吸引ダクト。
Fig. 1 is a partially cross-sectional explanatory diagram showing a first embodiment of the dehydrating device according to the present invention, Fig. 2 is a partially omitted vertical sectional view of the dehydrating device, and Fig. 3 is a second embodiment of the dehydrating device. FIG. 4 is a partial cross-sectional explanatory diagram showing a third embodiment of the dewatering device; FIG. 5 is a partially omitted vertical cross-section of the dewatering device in which a slit plate is attached to the pressure tube. It is a diagram. 3... Pressure tube, 3a... Air outlet, 3b... Discharge port, 6... Rotating plate, 11... Dewatering basket, 15... Drain chute, 16... Drain pit, 20... Cyclone, 22, 26 , 30... Suction duct.
Claims (1)
端側の送風口より導入される空気により他端側の
放出口から射出させ、圧送筒の放出口と対向位置
に配設された回転板に衝突させ、該回転板の周囲
に配されて回転板と1体となつて回転し、且つ、
上記圧送筒側にラツパ状に拡開した脱水篭を介し
て固液分離し、粒体より分離された水分を排水シ
ユートを介して排水ピツトに排出するようにした
脱水装置において、上記排水シユートから空気を
強制的に吸引するためのサイクロンに、吸引ダク
トの一端を接続開口し、かつ、該ダクトの他端を
排水シユート或いは排水ピツトの少なくとも一方
に接続開口したことを特徴とする脱水装置。 The water-containing granules put into the pressure-feeding cylinder are injected from the outlet at the other end by air introduced from the air outlet at one end of the pressure-feeding cylinder, and the rotating collides with the plate, is arranged around the rotating plate and rotates as one with the rotating plate, and
In the dehydration device, solid-liquid separation is carried out through a dewatering cage that expands in a shape of a bulge on the side of the pressure-feeding cylinder, and the water separated from the granules is discharged into a drainage pit through a drainage chute. A dewatering device characterized in that one end of a suction duct is connected to a cyclone for forcibly sucking air, and the other end of the duct is connected to at least one of a drainage chute and a drainage pit.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15665584U JPS6238730Y2 (en) | 1984-10-17 | 1984-10-17 |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15665584U JPS6238730Y2 (en) | 1984-10-17 | 1984-10-17 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6171212U JPS6171212U (en) | 1986-05-15 |
| JPS6238730Y2 true JPS6238730Y2 (en) | 1987-10-02 |
Family
ID=30714660
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP15665584U Expired JPS6238730Y2 (en) | 1984-10-17 | 1984-10-17 |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6238730Y2 (en) |
-
1984
- 1984-10-17 JP JP15665584U patent/JPS6238730Y2/ja not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6171212U (en) | 1986-05-15 |
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