JPS5819337B2 - Dry solid sorting equipment - Google Patents
Dry solid sorting equipmentInfo
- Publication number
- JPS5819337B2 JPS5819337B2 JP2844580A JP2844580A JPS5819337B2 JP S5819337 B2 JPS5819337 B2 JP S5819337B2 JP 2844580 A JP2844580 A JP 2844580A JP 2844580 A JP2844580 A JP 2844580A JP S5819337 B2 JPS5819337 B2 JP S5819337B2
- Authority
- JP
- Japan
- Prior art keywords
- sorting
- trough
- separated
- separation
- granular material
- 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
- 239000007787 solid Substances 0.000 title claims description 9
- 239000008187 granular material Substances 0.000 claims description 31
- 238000000926 separation method Methods 0.000 claims description 29
- 239000000463 material Substances 0.000 claims description 28
- 239000000843 powder Substances 0.000 claims description 18
- 230000005484 gravity Effects 0.000 claims description 16
- 238000000605 extraction Methods 0.000 claims description 10
- 238000007873 sieving Methods 0.000 claims description 4
- 238000007711 solidification Methods 0.000 claims description 2
- 230000008023 solidification Effects 0.000 claims description 2
- 239000000126 substance Substances 0.000 claims 1
- 239000003562 lightweight material Substances 0.000 description 7
- 238000011084 recovery Methods 0.000 description 5
- 239000002994 raw material Substances 0.000 description 4
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 2
- 229910052802 copper Inorganic materials 0.000 description 2
- 239000010949 copper Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005188 flotation Methods 0.000 description 2
- 239000002440 industrial waste Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000001737 promoting effect Effects 0.000 description 2
- 239000000758 substrate Substances 0.000 description 2
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 description 1
- 235000010582 Pisum sativum Nutrition 0.000 description 1
- 240000004713 Pisum sativum Species 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 230000002079 cooperative effect Effects 0.000 description 1
- 230000003111 delayed effect Effects 0.000 description 1
- -1 ferrous metals Chemical class 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000696 magnetic material Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 229920003002 synthetic resin Polymers 0.000 description 1
- 239000000057 synthetic resin Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
Description
【発明の詳細な説明】
本発明は、例えば粉砕した電線や都市ゴミ等の産業廃棄
物の固体による被分離物を比重差によって重量物と軽量
物とに分離して選別する乾式固体。DETAILED DESCRIPTION OF THE INVENTION The present invention is a dry solidification method for separating and sorting solid industrial waste such as crushed electric wires and municipal waste into heavy and light materials based on the difference in specific gravity.
選別装置に係り、特に、この乾式固体選別装置の分離促
進装置に関する。The present invention relates to a sorting device, and particularly to a separation promoting device of this dry solid sorting device.
従来、この種の被分離物を重量物と軽量物との分離して
選別する装置には、液体による媒体のほかに、乾式によ
るものとして(1)、重力と風力を利用したもの、(2
)、磁石による磁気力を利用して分離選別するもの、(
3)、遠心力を利用して分離選別するものが挙げられる
。Conventionally, devices for separating and sorting this type of material into heavy and light materials include, in addition to liquid media, dry methods (1), devices that utilize gravity and wind power, and (2) devices that use gravity and wind power.
), Separation and sorting using the magnetic force of magnets, (
3) Separation and sorting using centrifugal force can be mentioned.
即ち、(1)項の重力と風力を利用した選別装置は、被
分離物から分離された重量物と軽量物との境界域の幅が
比較的に広いために、分離した選別効率が低い。That is, in the sorting device described in item (1) that uses gravity and wind power, the separation efficiency is low because the width of the boundary area between the heavy objects and the light objects separated from the objects to be separated is relatively wide.
又、(2)項の磁石による選別装置は、鉄材等の磁性体
には有効であっても、非鉄金属の分離選別をすることは
できない。Furthermore, although the magnetic sorting device described in item (2) is effective for magnetic materials such as ferrous materials, it cannot separate and sort non-ferrous metals.
さらに、(3)項の遠心分離による選別装置は、振動、
1騒音が激しく、公害の問題を生じるおそれがあり、し
かも、分離される重量物と軽量物との境界域の幅も広く
なり、分離効率を上げることが困難である。Furthermore, the sorting device using centrifugation in item (3) uses vibration,
1. The noise is intense, which may cause pollution problems, and the boundary area between the heavy and light objects to be separated becomes wide, making it difficult to increase the separation efficiency.
そこで、本出願人は、先に粉粒体(メデア)を媒体とし
た乾式比重選別手段として、傾斜した選別トラス内に被
分離物及び粉粒体を混合しながら移送し、この被分離物
の比重差及び媒介物としての上記粉粒体によって軽量物
(メデアよりも軽いため浮上物ともいう)と重量物(沈
降物ともいう)とに分離し、この軽量物と重量物とを上
記選別トラフの下端部に設けられた分離板で、上記メデ
アと共に、メデア付の軽量物とメデア付の重量物とに分
離し、この分離されたメデアと一諸の軽量物と重量物と
を傾斜して設けられた各分篩トラフ(分篩体ともいう)
に移送し、ここでメデアのみを分篩して除去し、被分離
体を重量物と軽量物とに分離して選別する乾式による選
別装置を既に提案した。Therefore, the applicant first developed a dry specific gravity sorting means using powder or granular material (medea) as a medium, in which the material to be separated and the granular material are mixed and transferred into an inclined sorting truss. Due to the difference in specific gravity and the above-mentioned granular material as a medium, light objects (also called floating objects because they are lighter than media) and heavy objects (also called sediments) are separated, and the light objects and heavy objects are passed through the sorting trough. A separating plate provided at the lower end of the media separates the media into a light object with a media and a heavy object with a media, and the separated media, one of the light objects, and the heavy object are tilted. Each dividing sieve trough provided (also called dividing sieve body)
We have already proposed a dry sorting device in which the media are transferred to a sieve, where only the media is separated and removed, and the objects to be separated are separated into heavy items and light items.
しかしながら、上述した乾式固体選別装置は、傾斜した
選別トラフ上で被分離物をメデアを媒介物とし、しかも
比重差によって重量物と軽量物とに、理論上分離選別す
ることができるのであるが、上記選別トラフの横幅が大
きくして、大型化すると、この選別トラフの略中央部に
おける被分離物の分離作用が選別トラフの両側近傍に比
較して遅延し、これに起因して分離効率を低下させる等
の難点がある。However, the above-mentioned dry solid sorting device uses media as a medium to separate the materials on an inclined sorting trough, and theoretically can separate and sort the materials into heavy and light materials based on the difference in specific gravity. When the width of the sorting trough is increased and the size of the sorting trough is increased, the separation effect of the material to be separated at the approximate center of the sorting trough is delayed compared to the vicinity on both sides of the sorting trough, resulting in a decrease in separation efficiency. There are some difficulties, such as having to
又一方、上記選別トラフの略中央部における被分離物の
流速を速くすると、上記選別トラフの両側近傍に位置す
る分離された軽量物が粉粒体(メデア)の中に混り合い
、つまり、かぶりを生じ有効な分離を妨げる等の難点が
ある。On the other hand, if the flow rate of the material to be separated in the approximate center of the sorting trough is increased, the separated lightweight materials located near both sides of the sorting trough are mixed into the powder and granular material (media). There are drawbacks such as fogging and preventing effective separation.
本発明は、上述した難点を解消するために、傾斜した選
別トラフの底板に多数の分離幇助部材を植設し、これに
より、被分離物の浮上、沈降作用を促進し、被分離物を
重量物と軽量物とに一工程で完全に分離すると共に、大
型の選別トラフにも適用し得るようにしたことを目的と
する乾式固体選別装置を提供するものである。In order to solve the above-mentioned difficulties, the present invention has a large number of separation aiding members installed on the bottom plate of the inclined sorting trough, thereby promoting the floating and settling of the objects to be separated, and weighting the objects to be separated. To provide a dry solids sorting device which is capable of completely separating solids from light objects in one step, and which is also applicable to large sorting troughs.
以下、本発明を、適当な大きさに予め粉砕した電線を被
分離物として使用した図示の一実施例について説明する
。Hereinafter, the present invention will be described with reference to an illustrated embodiment in which electric wires pre-pulverized to an appropriate size are used as objects to be separated.
第1図乃至第4図において、符号1はホッパ1aを備え
、しかも電動フィーダ1bで移送するようにした媒介物
としての粉粒体(メデア)Aを連続して供給するメデア
供給装置であって、このメデア供給装置1に近接した位
置には、例えばコンベヤによる原料供給装置2が粉砕さ
れた被服片(軽量物)と銅片(重量物)とに混合した被
分離物Bを搬送するようにして設けられている。In FIGS. 1 to 4, reference numeral 1 denotes a media supply device that is equipped with a hopper 1a and that continuously supplies powder or granular material (media) A as a medium, which is transported by an electric feeder 1b. In a position close to this media supply device 1, a raw material supply device 2 using, for example, a conveyor conveys a material to be separated B mixed with crushed clothing pieces (light objects) and copper pieces (heavy objects). It is provided.
又、上記メデア供給装置1及び原料供給装置2の下位に
は、選別トラフ3が支持枠17によって傾斜して保持さ
れ、しかも扁平な基板19上の複数のコイルばねのよう
な弾性体18で浮上状態にして設けられている。Further, below the media supply device 1 and raw material supply device 2, a sorting trough 3 is held obliquely by a support frame 17, and is floated by a plurality of elastic bodies 18 such as coil springs on a flat substrate 19. It is set up in good condition.
さらに、上記選別トラフ3の下端部3aには、分離され
た重量物Wの抽出口4及び軽量物Pの抽出口5が仕切は
機能を備えた分離板6によって水平に仕切られて設けら
れており、上記選別トラフ3の底板3cには、第1図及
び第4図に示されるように、棒状をなす多数の分離幇助
部材22が一直線状をなすように並行して植設されてい
る。Further, at the lower end 3a of the sorting trough 3, an extraction port 4 for the separated heavy items W and an extraction port 5 for the lightweight items P are horizontally partitioned by a functional separation plate 6. As shown in FIGS. 1 and 4, on the bottom plate 3c of the sorting trough 3, a large number of rod-shaped separation assisting members 22 are installed in parallel in a straight line.
なお、この分離幇助部材22は、第4図の鎖線で示され
るように、選別トラフ3の長さ方向に僅かに傾斜するよ
うに植設してもよい。Note that the separation assisting member 22 may be installed so as to be slightly inclined in the longitudinal direction of the sorting trough 3, as shown by the chain line in FIG.
一方、上記両袖出口4と5との下位には、上記粉粒体A
を分離し、しかも中仕切板16で長手方向に2分割され
た各分篩トラフ(分篩体ともいう)7と8が、一体的に
傾斜して設けられており、この各分篩トラフ7と8の各
下端部7a 、8aには重量物Wの吐出口9及び軽量物
Pの吐出口10が形成されている。On the other hand, below the above-mentioned both sleeve outlets 4 and 5, the above-mentioned granular material A
Each dividing sieve trough (also referred to as a dividing sieve body) 7 and 8, which is divided into two in the longitudinal direction by a partition plate 16, is provided integrally and inclined. A discharge port 9 for a heavy object W and a discharge port 10 for a light object P are formed in the lower end portions 7a and 8a of and 8, respectively.
さらに、この両吐出口9,10の下位には重量物の回収
容器11及び軽量物の回収容器12がそれぞれ配設され
ており、上記各分篩トラフ7.8の分篩部7b 、8b
の直下には各メデア回収トラス13及び14が傾斜して
設けられている。Furthermore, a heavy object recovery container 11 and a light object recovery container 12 are arranged below the discharge ports 9 and 10, respectively, and the dividing sieve portions 7b and 8b of each dividing sieve trough 7.8 are provided.
Immediately below the media recovery trusses 13 and 14 are provided at an angle.
又、この両メデア回収トラス13゜14はホッパ21を
介して、前記メデア供給装置1のホッパ1aにパケット
コンベヤ15によって連結されており、この両メデア回
収トラス13゜14で回収された粉粒体Aは、上記メデ
ア供給装置1へ上記パケットコンベヤ15で搬送し得る
ようになっている。Further, both media collection trusses 13° 14 are connected via a hopper 21 to the hopper 1a of the media supply device 1 by a packet conveyor 15, and the powder and granules collected by these media collection trusses 13° 14 are A can be conveyed to the media supply device 1 by the packet conveyor 15.
以下、本発明の作用について説明する。Hereinafter, the effects of the present invention will be explained.
従って、今、予めメデア供給装置1を駆動することによ
り、被分離物Bの重量物Wと軽量物Pの比重の中間的な
、例えば何秒のような乾燥した粉粒体A(比重4.7)
を傾斜した選別トラス3の上端部3bに落下して供給す
る。Therefore, by driving the media supply device 1 in advance, a dry powder A (with a specific gravity of 4.5 seconds), for example, which is intermediate in specific gravity between the heavy material W and the light material P of the material to be separated B, is prepared. 7)
falls onto the upper end 3b of the inclined sorting truss 3 and is supplied.
他方、上記基板19の中程に設置された偏心旋回装置2
0を駆動すると、この偏心旋回装置20のクランク部2
0aがこれに連続している上記支持枠17をゆっくり旋
回動作を与えるので、上記粉粒体Aは選別トラフ3内を
上記分離板6よりも高い積層をなして流下する。On the other hand, the eccentric rotation device 2 installed in the middle of the substrate 19
0, the crank part 2 of this eccentric turning device 20
Since 0a slowly rotates the support frame 17 which is continuous with it, the powder A flows down inside the sorting trough 3 in a layer higher than the separating plate 6.
次に、原料供給装置2を駆動することにより、粉砕され
た合成樹脂(比重0.92)の被服片(軽量片)Pと銅
片(比重8.96)重量物Wとを混合した被分離物Bを
上記選別トラフ3の層流をなす粉粒体Aの上面に落下す
る。Next, by driving the raw material supply device 2, the coated pieces (light pieces) P of the pulverized synthetic resin (specific gravity 0.92) and the heavy pieces W of copper pieces (specific gravity 8.96) are mixed to be separated. The material B is dropped onto the upper surface of the granular material A forming a laminar flow in the sorting trough 3.
すると、この被分離物Bの重量物Wは粉粒体A内を除々
に沈降しながら、上記選別トラフ3の底板3cに降下し
て移送され、上記選別トラフ3の重量物Wの抽出口4か
ら粉粒体Aと共に抽出され、次の分篩トラフ7に落下し
、さらに、この粉粒体Aと一諸の重量物Wは分篩部Ib
上を移動しながら、吐出口9へ送出されて重量物Wの回
収容器11に落下して貯溜される。Then, the heavy material W of the material to be separated B gradually settles inside the powder or granular material A and is transferred to the bottom plate 3c of the sorting trough 3, and is transferred to the extraction port 4 of the heavy material W of the sorting trough 3. The powder and granules A are extracted together with the granular material A, and fall into the next separating sieve trough 7, and furthermore, this powder and granular material A and various heavy objects W are extracted into the separating sieve section Ib.
While moving above, it is delivered to the discharge port 9 and falls into the recovery container 11 for heavy objects W, where it is stored.
同時に、粉粒体Aは分篩部7bで分篩されて回収トラス
13を介してホッパ21に貯溜される。At the same time, the granular material A is sieved by the sieving section 7b and stored in the hopper 21 via the collection truss 13.
他方、被分離体Bの軽量物Pは、上記粉粒体A上に落下
して沈降しようとしても、この軽量物Pの比重よりも重
い粉粒体Aに阻止されて降下することができず、粉粒体
Aの上を浮遊したまメ、この粉粒体へと共に、上記分離
板6上を通過して、軽量物Pの抽出口5から粉粒体Aと
共に分離して抽出される。On the other hand, even if the lightweight material P of the object to be separated B falls onto the powder or granular material A and attempts to settle, it is blocked by the powder or granular material A, which has a higher specific gravity than the lightweight material P, and cannot descend. The peas floating on the granular material A pass through the separating plate 6 together with the granular material A, and are separated and extracted together with the granular material A from the extraction port 5 of the lightweight material P.
次に、この粉粒体Aと一諸の軽量物Pは、分篩トラフ8
に落下し、さらに、この粉粒体Aと一諸の軽量物Pは分
篩部8b上を移動しながら、吐出口10から軽量物Pの
回収容器12へ落下して貯溜される。Next, this granular material A and one of the lightweight materials P are transferred to a separating sieve trough 8.
Further, while moving on the separating sieve section 8b, the granular material A and one of the lightweight materials P fall from the discharge port 10 into the recovery container 12 for the lightweight materials P and are stored therein.
同時に粉粒体Aは上記分篩部8bで分篩されて回収トラ
ス14を通してホッパ21に貯溜される。At the same time, the granular material A is sieved by the sieving section 8b and stored in the hopper 21 through the collection truss 14.
なお、こ5で注目すべき点は、上記選別トラス3の底板
3cに植設された各分離幇助部材22が。What should be noted here is that each separation assisting member 22 is implanted in the bottom plate 3c of the sorting truss 3.
上記選別トラス3の略中央部の近傍の被分離体Bを、媒
介物としてのメデア、つまり、粉粒体Aを介して、軽量
体Pに対して浮上作用を幇助し、他方、重量体Wに対し
て沈降作用を幇助しながら、しかも、選別トラス3の傾
斜した全体の流れ方向に整流作用を促進するようになっ
ていることである。The object B to be separated near the approximate center of the sorting truss 3 is assisted in flotation with respect to the light object P through the medium, that is, the granular material A, while the heavy object W The present invention is designed to promote a rectifying action in the entire inclined flow direction of the sorting truss 3 while assisting the settling action.
このため、大型化した選別トラス3の分離効率を一層向
上するようになっている。Therefore, the separation efficiency of the enlarged sorting truss 3 is further improved.
このようにして被分離物Bは、粉粒体Aによる媒介物と
上記各分離幇助部材22との共働作用によって、重量物
Wと軽量物Pとに一工程で完全に分離して選別すること
ができるようになっている。In this way, the material to be separated B is completely separated and sorted into heavy material W and light material P in one step by the cooperative action of the medium of powder and granular material A and the separation assisting members 22 described above. It is now possible to do so.
なお、上記両メデア回収トラフ13,14のホッパ21
に貯溜された粉粒体Aは、パケットコンベヤ15によっ
て上記メデア供給装置1のホッパ1aへの還流されるよ
うになっている。Note that the hoppers 21 of both the media collection troughs 13 and 14
The powder and granular material A stored in the granular material A is returned to the hopper 1a of the media supply device 1 by a packet conveyor 15.
次に、第5図に示される実施例は本発明の他の実施例で
あって、これは選別トラフ3の底板3cに短冊板状をな
す分離幇助部材22′を垂直方向に植設したものであり
、上述した棒状のものと実質的に同一内容をなすもので
ある。Next, the embodiment shown in FIG. 5 is another embodiment of the present invention, in which a separation assisting member 22' having a strip plate shape is vertically planted on the bottom plate 3c of the sorting trough 3. This is substantially the same content as the rod-shaped one described above.
又、第6図に示される実施例は本発明の他の実施例であ
って、これは、選別トラフ3の底板3cにねじ棒(線杆
)状をなす分離幇助部材27を植設したものであり、上
述した各承体例と同じ内容をなすものである。The embodiment shown in FIG. 6 is another embodiment of the present invention, in which a separation assisting member 27 in the shape of a threaded rod (wire rod) is implanted in the bottom plate 3c of the sorting trough 3. This is the same content as each of the above-mentioned body examples.
さらに又、上記選別トラフの底部3cに植設される多数
の分離幇助部材22は並行した一直線状をなすものばか
りでなく、千鳥状をなしたり、又は乱雑に植設しても差
支えないこと勿論である。Furthermore, the large number of separation assisting members 22 installed at the bottom 3c of the sorting trough are not limited to being arranged in parallel straight lines, but may also be installed in a staggered manner or in a random manner. It is.
又一方、本発明は、粉砕された電線を被分離物Bとして
使用した一実施例について説明したけれども、本発明の
要旨を変更しない範囲内で、例えば、粉粒体Aを何秒に
よらず、比重の異なる粉粒体を利用するこ吉により、他
の産業廃棄物等を比重差を巧みに利用して分離選別でき
るようにすることは自由である。On the other hand, although one embodiment of the present invention has been described in which a crushed electric wire is used as the material to be separated B, within the scope of the present invention, for example, the powder or granular material A may be separated for any number of seconds. By using powder and granular materials with different specific gravity, it is possible to separate and sort other industrial wastes by skillfully utilizing the difference in specific gravity.
以上述べたように本発明によれば、粉粒体Aを連続的に
供給されるようにし、しかも被分離物Bを比重差によっ
て分離する選別トラフ3を傾斜して設け、この選別トラ
フ3の底板3cに多数の分離幇助部材22を植設し、上
記選別トラフ3の下端部3aに重量物Wの抽出口4と軽
量物Pの抽出口5を分離板6によって仕切って設け、上
記両袖出口4,5の下位に上記粉粒体Aを分篩する傾斜
した各分篩トラフ7.8を配設しであるので、被分離物
Bをぬらすことなく、一工程で完全に分離選別できるば
かりでなく、上記分離幇助部材22が浮上及び沈降作用
を促進するから、選別トラフ3が大型化しても、有効ζ
こ分離効率を上げることができると共に、振動、衝撃も
少くなり、静粛に分離選別を行うことができる。As described above, according to the present invention, the sorting trough 3 that allows the powder or granular material A to be continuously supplied and separates the material to be separated B based on the difference in specific gravity is provided at an angle. A large number of separation assisting members 22 are installed on the bottom plate 3c, and an extraction port 4 for heavy materials W and an extraction port 5 for light materials P are provided at the lower end 3a of the sorting trough 3 separated by a separation plate 6, Since each slanted sieve trough 7.8 for sieving the granular material A is arranged below the outlets 4 and 5, it is possible to completely separate and sort the material B in one step without getting it wet. In addition, since the separation assisting member 22 promotes flotation and sedimentation, even if the sorting trough 3 becomes large, it will be effective.
This increases separation efficiency, reduces vibration and impact, and allows quiet separation and sorting.
第1図は本発明による乾式固体選別装置の断面図、第2
図は、第1図中の鎖線A−Aに沿う平面図、第3図は第
1図中の鎖線B−Bに沿う平面図、第4図は本発明の要
部のみを拡大して示す断面図、第5図及び第6図は本発
明の他の実施例を示す図である。
1・・・・・・メデア供給装置、2・・・・・・原料供
給装置、3・・・・・・選別トラフ、3c・・・・・・
底板、4,5・・・・・・抽出口、6・・・・・・分離
板、7,8・・・・・・分篩トラフ、9゜10・・・・
・・吐出口、11,12・・・・・・回収容器、13゜
14・・・・・・メデア回収トラフ、15・・・・・・
パケットコンベア、20・・・・・・旋回駆動装置、2
1・・・・・・ホッパ、22・・・・・・分離幇助部材
。Fig. 1 is a sectional view of a dry solid sorting device according to the present invention;
The figure is a plan view taken along the dashed line A-A in FIG. 1, FIG. 3 is a plan view taken along the dashed line B-B in FIG. 1, and FIG. 4 shows an enlarged view of only the essential parts of the present invention. The sectional views, FIGS. 5 and 6, are views showing other embodiments of the present invention. 1... Media supply device, 2... Raw material supply device, 3... Sorting trough, 3c...
Bottom plate, 4, 5... Extraction port, 6... Separation plate, 7, 8... Sieve trough, 9゜10...
...Discharge port, 11, 12... Collection container, 13゜14... Media collection trough, 15...
Packet conveyor, 20... Turning drive device, 2
1...Hopper, 22...Separation assisting member.
Claims (1)
離物を比重差によって分離する選別トラフを傾斜して設
け、この選別トラフの底板に多数の分離幇助部材を植設
し、上記選別トラフの下端部に分離された重量物の抽出
口と軽量物の抽出口とを分離板によって仕切って設け、
上記両抽出[]の下位に上記粉粒体を分篩する傾斜した
各分篩トラフを配設したことを特徴とする乾式固体選別
装置。 2 選別トラフに植設される分離幇助部材を棒体、。 短冊板体若しくはねじ棒にしたことを特徴とする特許請
求の範囲第1項記載の乾式固体選別装置。 3 選別トラフの底板上に複数の分離幇助部材を直線状
若しくは千鳥状に列設したことを特徴とする特許請求の
範囲第1項及び第2項記載の乾式固。 体選別装置。[Scope of Claims] 1. A sorting trough is provided at an angle so that the powder and granular material is continuously supplied and the substances to be separated are separated by the difference in specific gravity, and a number of separation aiding members are provided on the bottom plate of the sorting trough. planted, and a separated heavy material extraction port and a light material extraction port are provided at the lower end of the sorting trough, separated by a separation plate,
A dry solids sorting device characterized in that a slanted sieve trough for sieving the powder or granular material is arranged below the two extraction units [ ]. 2. The separation assisting member installed in the sorting trough is a rod. The dry solid sorting device according to claim 1, characterized in that it is formed into a strip plate or a threaded rod. 3. The dry solidification according to claims 1 and 2, characterized in that a plurality of separation assisting members are arranged in a linear or staggered manner on the bottom plate of the sorting trough. Body sorting device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2844580A JPS5819337B2 (en) | 1980-03-06 | 1980-03-06 | Dry solid sorting equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2844580A JPS5819337B2 (en) | 1980-03-06 | 1980-03-06 | Dry solid sorting equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS56124454A JPS56124454A (en) | 1981-09-30 |
| JPS5819337B2 true JPS5819337B2 (en) | 1983-04-18 |
Family
ID=12248866
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2844580A Expired JPS5819337B2 (en) | 1980-03-06 | 1980-03-06 | Dry solid sorting equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5819337B2 (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS59130134U (en) * | 1983-02-21 | 1984-09-01 | シャープ株式会社 | key input device |
| JPS6022228A (en) * | 1983-07-19 | 1985-02-04 | Maitemu:Kk | Corresponding method between input display and output display of computer |
| JPS6091433A (en) * | 1983-10-24 | 1985-05-22 | Gakken Co Ltd | Learning computer input method |
| JPS60134962A (en) * | 1983-12-23 | 1985-07-18 | Nippon Telegr & Teleph Corp <Ntt> | Keyboard device |
-
1980
- 1980-03-06 JP JP2844580A patent/JPS5819337B2/en not_active Expired
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS59130134U (en) * | 1983-02-21 | 1984-09-01 | シャープ株式会社 | key input device |
| JPS6022228A (en) * | 1983-07-19 | 1985-02-04 | Maitemu:Kk | Corresponding method between input display and output display of computer |
| JPS6091433A (en) * | 1983-10-24 | 1985-05-22 | Gakken Co Ltd | Learning computer input method |
| JPS60134962A (en) * | 1983-12-23 | 1985-07-18 | Nippon Telegr & Teleph Corp <Ntt> | Keyboard device |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS56124454A (en) | 1981-09-30 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US4940187A (en) | Systematic equipments for recycling raw materials from waste wires | |
| US4565624A (en) | Gravity--magnetic ore separators | |
| US4128474A (en) | Process for cleaning and dewatering fine coal | |
| US10799880B2 (en) | Method and apparatus for washing and grading silica sand for glass production | |
| RU2080933C1 (en) | Cleansing apparatus | |
| US5160035A (en) | Particle concentrator and method of operation | |
| US20050000864A1 (en) | Method and apparatus for cleaning coal | |
| US4659457A (en) | Gravity-magnetic ore separators and methods | |
| US4370225A (en) | Dry magnetic separators for increased recovery or ore at high belt speeds | |
| JPS5819337B2 (en) | Dry solid sorting equipment | |
| RU2234982C2 (en) | Screen-concentrator | |
| CA2058123A1 (en) | Method and apparatus for separation of heavy and light particles from particulate material | |
| GB2261833A (en) | Magnetic separation of materials | |
| AU739621B2 (en) | Separator | |
| RU2183999C2 (en) | Screen-concentrator | |
| NL1029022C2 (en) | Separation apparatus for mixture of different density solids with liquid, comprises fluidizing mixture above screen with pulsed flow of hutchwater | |
| CN2162297Y (en) | Rotary vibration type belt chute with weir | |
| EP1608468B1 (en) | Heavy particle separation | |
| JPS63194752A (en) | Dry type separation of solid | |
| JP3708813B2 (en) | Particle classifier | |
| Dodbiba et al. | Air tabling—a dry gravity solid–solid separation technique | |
| US12030061B2 (en) | Conveyor sluice system | |
| US2734629A (en) | menzies | |
| RU2337758C1 (en) | Vibration concentrator | |
| RU2172650C1 (en) | Screen-concentrator |