JPS5882902A - Continuous separating storing device for solid matter - Google Patents

Continuous separating storing device for solid matter

Info

Publication number
JPS5882902A
JPS5882902A JP18046881A JP18046881A JPS5882902A JP S5882902 A JPS5882902 A JP S5882902A JP 18046881 A JP18046881 A JP 18046881A JP 18046881 A JP18046881 A JP 18046881A JP S5882902 A JPS5882902 A JP S5882902A
Authority
JP
Japan
Prior art keywords
solids
storage tank
separator
gas
solid matter
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.)
Pending
Application number
JP18046881A
Other languages
Japanese (ja)
Inventor
保彦 西村
佐野 次生
茂 鎌田
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.)
Fujicar Manufacturing Co Ltd
Original Assignee
Fujicar Manufacturing Co Ltd
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 Fujicar Manufacturing Co Ltd filed Critical Fujicar Manufacturing Co Ltd
Priority to JP18046881A priority Critical patent/JPS5882902A/en
Publication of JPS5882902A publication Critical patent/JPS5882902A/en
Pending legal-status Critical Current

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Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 この発明は、塵芥、穀類などの被輸送固形物を気流で輸
送するシステムに用いる連続分離貯留装置に関する・も
のである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a continuous separation and storage device used in a system for transporting solid materials such as garbage and grains by air current.

このようなシステムの場合、固形物は気体とともに輸送
されるため、終端では気体と固形物を分離して、気体が
空気の場合は大気へ放出し、固形物は貯留槽に捕集して
その後の処理を行なう必要かある。
In such systems, the solids are transported together with the gas, so the gas and solids are separated at the end, and if the gas is air, they are released to the atmosphere, and the solids are collected in a storage tank and then disposed of. Is it necessary to perform some processing?

F記のような分離貯留を行なうためには、従来では第1
!¥1乃至第4図のような装置が必要となる。
In order to perform separation and storage as described in F, conventionally, the first
! A device like the one shown in Figure 4 is required.

これらの図において、1はサイクロン型分離器で、2は
混合流の入口、3は気体の出口であり、下端には、接続
部4を介して貯留槽5を連結する。
In these figures, 1 is a cyclone type separator, 2 is an inlet for a mixed flow, 3 is an outlet for gas, and a storage tank 5 is connected to the lower end via a connection 4.

この貯留槽5は第1図の例では横置回転式、第2図乃至
第4図の例は縦向き固定式で、接続部4は第1図のシュ
ート式、第2図の環状、第3図のフランジ式、第4図の
コンベヤ式のように種々の型式がある。
The storage tank 5 is a horizontal rotating type in the example shown in Fig. 1, and a vertically fixed type in the examples shown in Figs. There are various types, such as the flange type shown in Figure 3 and the conveyor type shown in Figure 4.

また、各貯留槽5の排出口に設ける蓋6も各種の方式が
ある。
Furthermore, there are various types of lids 6 provided at the discharge ports of each storage tank 5.

しかし、上記の何れの場合も貯留槽5の上にサイクロン
型分離器1があるため、全高が非常に大きくなり、建物
内に設ける場合は容量を大きくすると、建物の2階3階
分のフロア−を貫通させなければならない場合が生じ、
建築−Fの諸問題が発生するおそれかある。
However, in both of the above cases, since the cyclone separator 1 is placed above the storage tank 5, the total height becomes very large. - may have to be penetrated,
There is a risk that various problems related to Architecture-F may occur.

また、現地において、組立てる必要があるため、現地工
事費が高くなり、高所作業となるから危険性も大きくな
る。さらに高所設置のため、大きな架台も必要となり、
従って全体の重量が大きくなると吉もに価格も高くなる
などの欠点がある。
Furthermore, since it is necessary to assemble on-site, the cost of on-site construction increases, and work at heights increases the risk. Furthermore, since it is installed at a high place, a large mount is also required.
Therefore, as the overall weight increases, the price also increases.

この発明の目的は上記のような従来の分離貯留装置の欠
点を解決することである。
The purpose of the present invention is to overcome the drawbacks of conventional separation and storage devices as described above.

すなわち、この発明は横置式の回転貯留槽の後部内にサ
イクロン型分離器を内蔵させて、この分離器内で分離さ
れて下部の開口から排出される固形物を貯留槽の後部内
周のかき上羽根によりかき上げて、分離器の上部および
両側のシュートから貯留槽へと排出するようにした固形
物の連続分離貯留装置を提供するものである。
That is, the present invention incorporates a cyclone separator in the rear part of a horizontal rotating storage tank, and collects the solids separated in the separator and discharged from the opening at the bottom by scraping the inner periphery of the rear part of the storage tank. The present invention provides a continuous separation and storage device for solids that is scraped up by upper blades and discharged into a storage tank through chutes at the top and both sides of the separator.

′1 第5図1乃至′第8図において、11はサイクロン型分
離器で、基台12の後部に設けた支持枠13に固定され
たものである。
1 to 8, reference numeral 11 denotes a cyclone separator, which is fixed to a support frame 13 provided at the rear of a base 12. In FIGS.

14は横置式の回転貯留槽で、この槽14の後 ′部は
第6図のように分離器11に被さるとともに支持枠13
内にベアリング15を介して回動自在に支承されている
。また、この槽14の前部附近の外周には全周に亘るタ
イヤ16を固定し、このタイヤ16を基台12の前端上
部両側の一対のローラ17により支承せしめ、この両ロ
ーラ17の何れかまたは両方を図示省略しであるモータ
や減速機などの駆動装置により駆動して貯留槽14を第
θシ・の矢印方向に回転させるように樒成しである。
14 is a horizontal rotating storage tank, and the rear part of this tank 14 covers the separator 11 as shown in FIG.
It is rotatably supported therein via a bearing 15. Further, a tire 16 is fixed around the entire circumference of the tank 14 near the front part, and this tire 16 is supported by a pair of rollers 17 on both sides of the upper front end of the base 12. Alternatively, both may be driven by a drive device such as a motor or a speed reducer (not shown) to rotate the storage tank 14 in the direction of the θ-th arrow.

前記分離器11の上部外側には気体と固形物の混合流の
入口18を設け、分離器11の上端には分離された気体
の出口19を設けて、これらの入口18と出口19を*
 6 fR+のように後方へ向けである。また、分離器
11の下端には第6図、第8し、のように固形物の排出
口20が設けである。
An inlet 18 for a mixed flow of gas and solids is provided on the outside of the upper part of the separator 11, and an outlet 19 for the separated gas is provided at the upper end of the separator 11.
6 It is directed towards the rear like fR+. Further, a solid material discharge port 20 is provided at the lower end of the separator 11 as shown in FIGS. 6 and 8.

21は貯留槽14の後端部内周に固定した複数のかき上
羽根で、第7図、第8し1のようl断面となっている。
Reference numeral 21 denotes a plurality of blades fixed to the inner periphery of the rear end of the storage tank 14, which have an L cross section as shown in FIGS. 7 and 8.

また、分離器11の左右の外側には第6図に示すように
後上方から前下方へと傾斜するシュート22が設けであ
るが、このシュート22の外周から後111iの部分は
第8り1のようにかき上羽根21の内側に沿う円弧状の
ガイド板23を設けて、羽根21てかき上げた固形物が
シュート22の後側に落ちないようにしである。
Further, on the left and right outer sides of the separator 11, as shown in FIG. An arc-shaped guide plate 23 is provided along the inside of the scraping blade 21 to prevent the solids scraped up by the blade 21 from falling to the rear side of the chute 22.

さらに分離器11の上端に突出した出口19の屈曲部2
3″には突6タ1ないし第8図のように両側と前方へ傾
斜するシュー)24.25を設けてかき上羽根21で上
方までかき上げられて分離器11の上部に落下した固形
物が両側と前部のシュート24.25から、前方の貯留
槽14内に落下するようにしである。
Furthermore, the bent portion 2 of the outlet 19 protrudes from the upper end of the separator 11.
3'' is provided with protrusions 1 to 24 and 25 that slope forward on both sides as shown in FIG. from the chutes 24, 25 on both sides and the front into the storage tank 14 at the front.

前記の貯留槽14の前部は第6図1のように前部 −が
窄まったテーパ状となり、この部が基台12Φ前端の枠
26内から前方に突出している。
The front portion of the storage tank 14 has a tapered shape with a narrowed front portion as shown in FIG. 6, and this portion protrudes forward from within the frame 26 at the front end of the base 12Φ.

27は貯留槽14の前端の排出口を開閉する蓋で、この
蓋27は枠26上に軸28で揺動自在に取付けた腕29
の端部に回動自在に取付けたもので、腕29は油圧また
はエアシリンダなどで駆動される。また、蓋27が貯留
槽14の排出口を閉釦したとき、蓋27の回転中心は槽
14の回転中心と同心となり、共に回転する。
Reference numeral 27 denotes a lid for opening and closing the discharge port at the front end of the storage tank 14, and this lid 27 is attached to an arm 29 that is swingably attached to the frame 26 with a shaft 28.
The arm 29 is rotatably attached to the end of the arm 29, and the arm 29 is driven by hydraulic pressure or an air cylinder. Further, when the lid 27 closes the outlet of the storage tank 14, the rotation center of the lid 27 becomes concentric with the rotation center of the tank 14, and rotates together.

なお、貯留槽14内には1条あるいは複数条の螺旋羽根
30を設けて、槽14の回転に伴って槽14内の固形物
が前方に送られるようにしである。
Note that one or more spiral blades 30 are provided in the storage tank 14 so that the solids in the tank 14 are sent forward as the tank 14 rotates.

こ□の発明の装置は上記の構成であ′す、以下にその使
戸例を説明する。
The device of this invention has the above-mentioned configuration, and an example of its use will be explained below.

第5図において、不定期的に発生する塵芥などの固形物
をコンベヤ31で運搬して一次貯留槽32に貯留し、こ
の槽32が満杯になると、ロータリフィーダ33が回転
を始め、気流による輸送システムが起動し、同時にこの
発明の装置も起動して貯留槽14が回転を始める。
In FIG. 5, solid matter such as garbage that is generated irregularly is transported by a conveyor 31 and stored in a primary storage tank 32. When this tank 32 is full, a rotary feeder 33 starts rotating and is transported by air current. When the system is activated, the device of the present invention is also activated and the storage tank 14 begins to rotate.

このため、輸送管34内を気体とと′もに輸送された固
形物は人品18から分離器11内に向って接線方間に流
入するので、分離器11内において固形物と気体とは第
5図の矢印のように旋回して固形物は遠心力により分離
器11の周壁内面に沿って旋回しつつ気体と分離して下
降し、下部の排出口20から排出される。
Therefore, the solids transported along with the gas in the transport pipe 34 flow tangentially from the goods 18 into the separator 11, so that the solids and gas are separated in the separator 11. The solids rotate as indicated by the arrows in FIG. 5, and while rotating along the inner surface of the peripheral wall of the separator 11 due to centrifugal force, the solids are separated from the gas, descend, and are discharged from the discharge port 20 at the bottom.

一方、出口19には第5図のように2次フィルタ35を
有する排気筒36が連結され、その端部には排気用のブ
ロワ−37を連結しであるがら、分離器11内において
、固形物と分離した気体は出口19から流出し、フィル
タ35によって気体中の微粉塵が除去され、清浄となっ
た気体が空気の場合はブロワ−37によって大気中に放
出される。
On the other hand, an exhaust pipe 36 having a secondary filter 35 is connected to the outlet 19 as shown in FIG. The gas separated from the substances flows out from the outlet 19, fine dust in the gas is removed by the filter 35, and if the purified gas is air, it is discharged into the atmosphere by the blower 37.

一方、排出口20から排出された固形物は第7図、第8
図の矢印方向に回転している貯留槽14内のかき上羽根
21によりかき上げられていく。
On the other hand, the solid matter discharged from the discharge port 20 is
It is raked up by the raking blade 21 in the storage tank 14, which is rotating in the direction of the arrow in the figure.

こうして、羽根21でかき上げられる固形物はガイド板
23に沿って上昇していくが、その途中でシュート22
上へ固形物が出るとシュート22上へこほれてシュート
22上を螺旋羽根30の位置まで滑り落ちる。
In this way, the solid matter scraped up by the blades 21 rises along the guide plate 23, but along the way, the solid matter is raised by the chute 22.
When the solid material comes out upward, it crumbles onto the chute 22 and slides down on the chute 22 to the position of the spiral blade 30.

また、途中でこぼれなかった固形物は分離器11の上方
まで移動して醒下し、シュート24.25上を滑り落ち
てシュート22上あるいは螺旋羽根3゜の部分に落下し
、最終的には全ての固形物が貯留槽14とともに回転す
る螺旋羽根30により貯留槽14内の前方へ送られてい
く。
In addition, the solids that did not spill out on the way move to the upper part of the separator 11 and fall down, slide down on the chute 24, 25, fall on the chute 22 or on the 3° part of the spiral blade, and finally All the solids are sent forward into the storage tank 14 by the spiral blades 30 that rotate together with the storage tank 14.

上記の作用により貯留槽14内の固形物は満杯になるか
、それ以後も運転を続けると、さらに圧縮されて貯留さ
れる。
As a result of the above action, the solids in the storage tank 14 become full or if the operation continues thereafter, the solids are further compressed and stored.

こうして貯留槽14内に固形物が十分に圧縮貯留された
状態で−たん全ての運転を停止し、蓋27を開き、貯留
槽14のみを回転させると、螺旋羽根30の作用によっ
て貯留槽14内の固形物が前端の排出口から排出される
ので、この固形物を第5図のように運搬用自動車3 B
 i−C積み込んで所望の場所へ運搬する。
When the solids are sufficiently compressed and stored in the storage tank 14 in this way, all operations are stopped, the lid 27 is opened, and only the storage tank 14 is rotated. This solid material is discharged from the discharge port at the front end, and the solid material is transferred to the transportation vehicle 3B as shown in Fig. 5.
Load the i-C and transport it to the desired location.

こ、の発明の装置は上記のように空気などの気体ととも
に輸送されてきた固形物を遠心作用により気体から分離
するサイクロン型分離器11を横置型の回転式貯留槽1
4の後部内に取付けたものであるから、第1図乃至第4
図に示す従来の装置に比較してきわめて小型で軽量な分
離貯留槽が得られる。
As described above, the device of this invention includes a cyclone separator 11 that separates solids transported together with a gas such as air from the gas by centrifugal action, and a horizontal rotary storage tank 1.
Since it is installed in the rear part of Figure 4, Figures 1 to 4
A separation storage tank that is extremely small and lightweight compared to the conventional device shown in the figure is obtained.

また、この発明はサイクロン分離器11と、横置型の貯
留槽14を単に組合せただけでなく、貯留槽14の後部
内周にかき上羽根21を設けてこ、れにより排出口20
から排出された固形物をがき上げるようにし、こうして
かき上げた固形物は分離器11の両側と上側のシュー)
2.2,24.25によって全て、分離器11より前の
貯留槽14内に落すようにしたから、分離器11内で分
離した固形物が円滑かつ連続的に貯留槽14内に充填貯
留されるので気体で輸送されてきた固形物の分離と貯留
がきわめて能率よく行なえるなどの効果がある。
In addition, the present invention not only combines the cyclone separator 11 and the horizontal storage tank 14, but also provides scraping blades 21 on the inner periphery of the rear part of the storage tank 14, thereby increasing the discharge port 20.
The solids discharged from the separator 11 are scraped up, and the solids thus scraped are disposed of on both sides and upper shoes of the separator 11).
2.2, 24.25, all solids are dropped into the storage tank 14 before the separator 11, so the solids separated in the separator 11 are smoothly and continuously filled and stored in the storage tank 14. As a result, the separation and storage of solids transported in gas can be carried out extremely efficiently.

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

第1図乃至第4図は従来の分離貯留設備の各側を示す略
図、第5図はこの発明の分離貯留装置の使用状態を示す
略図、第6図はこの発明の分離貯留装置の一部縦断側面
図、第7図は第6図I−4線の縦断正面りI、第8図は
第6図rr−n線の′縦断正面図である。 11・・・サイクロン型分離器、14・・・回転貯留槽
、18・・・入口、19・・・出口、20・・・排出口
、21・・・かき上羽根、22 、24 、25・・・
シュート、23・・・案内板。 特許出願人  富士車輌株式会社
1 to 4 are schematic diagrams showing each side of a conventional separation and storage facility, FIG. 5 is a schematic diagram showing the usage state of the separation and storage device of the present invention, and FIG. 6 is a part of the separation and storage device of the present invention. 7 is a vertical sectional front view I taken along line I-4 in FIG. 6, and FIG. 8 is a vertical sectional front view taken along line rr-n in FIG. 6. DESCRIPTION OF SYMBOLS 11... Cyclone type separator, 14... Rotating storage tank, 18... Inlet, 19... Outlet, 20... Discharge port, 21... Scraping blade, 22, 24, 25.・・・
Shoot, 23...information board. Patent applicant Fuji Sharyo Co., Ltd.

Claims (1)

【特許請求の範囲】[Claims] 気体を媒体として固形物を輸送するシステムにおいて、
輸送されてきた固形物と気体を分離するサイクロン型分
離器を、横置式の回転貯留槽の後部内に静止状に取付け
るとともに、分離器の混合流の入口および分離気体の出
口を後方へ突出させ、貯留槽の後部内周には、分離器の
下端の排出口から排出される固形物を分離器の上方へか
き上げる複数のかき上羽根を設け、分離器の上部と両弁
側にはかき上げられた固形物を分離器の前方の貯留槽内
に滑り落すシュートを設けた固形物の連続分離貯留装置
In systems that transport solids using gas as a medium,
A cyclone separator that separates transported solids and gas is installed stationary in the rear of a horizontal rotating storage tank, and the separator's mixed flow inlet and separated gas outlet protrude rearward. , A plurality of scraping vanes are installed on the rear inner circumference of the storage tank to scrape up the solids discharged from the discharge port at the bottom end of the separator to the top of the separator. A continuous separation and storage device for solids that is equipped with a chute that allows the lifted solids to slide down into a storage tank in front of the separator.
JP18046881A 1981-11-09 1981-11-09 Continuous separating storing device for solid matter Pending JPS5882902A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18046881A JPS5882902A (en) 1981-11-09 1981-11-09 Continuous separating storing device for solid matter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18046881A JPS5882902A (en) 1981-11-09 1981-11-09 Continuous separating storing device for solid matter

Publications (1)

Publication Number Publication Date
JPS5882902A true JPS5882902A (en) 1983-05-18

Family

ID=16083743

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18046881A Pending JPS5882902A (en) 1981-11-09 1981-11-09 Continuous separating storing device for solid matter

Country Status (1)

Country Link
JP (1) JPS5882902A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010280462A (en) * 2009-06-03 2010-12-16 Mitsubishi Heavy Industries Environment & Chemical Engineering Co Ltd Vacuum-corresponding rotary storage device

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS49128562A (en) * 1973-04-13 1974-12-09

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS49128562A (en) * 1973-04-13 1974-12-09

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010280462A (en) * 2009-06-03 2010-12-16 Mitsubishi Heavy Industries Environment & Chemical Engineering Co Ltd Vacuum-corresponding rotary storage device

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