JP3430892B2 - Method and apparatus for recovering metal in pyrolysis residue - Google Patents
Method and apparatus for recovering metal in pyrolysis residueInfo
- Publication number
- JP3430892B2 JP3430892B2 JP34555297A JP34555297A JP3430892B2 JP 3430892 B2 JP3430892 B2 JP 3430892B2 JP 34555297 A JP34555297 A JP 34555297A JP 34555297 A JP34555297 A JP 34555297A JP 3430892 B2 JP3430892 B2 JP 3430892B2
- Authority
- JP
- Japan
- Prior art keywords
- inclined plate
- pyrolysis residue
- particles
- metal
- specific gravity
- 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 - Fee Related
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Landscapes
- Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
- Manufacture And Refinement Of Metals (AREA)
Description
【0001】[0001]
【発明の属する技術分野】本発明は、廃自動車、廃家電
品等の廃棄物からのシュレッダダスト等を熱処理するこ
とにより得られる熱分解残渣中の金属を回収する方法お
よび装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and an apparatus for recovering metal in a pyrolysis residue obtained by heat-treating shredder dust and the like from waste such as waste automobiles and waste home electric appliances.
【0002】[0002]
【従来の技術】自動車、家電品などを廃棄処理する際、
内装部品などは他の部分から取り外されて粉砕され、い
わゆるシュレッダダストとされる。このシュレッダダス
トは、通常、熱処理により減容化され、いわゆる熱分解
残渣とされた後、廃棄処理されている。この熱分解残渣
は、通常、電気部品等、例えば銅線などに由来するC
u、Fe、Pb、Znなどの金属からなる金属粒子と、
合成樹脂などに由来する炭化物などからなる比較的低比
重の粒子との混合物となっている。この熱分解残渣の具
体例としては、Cuを3〜15重量%、Feを3〜20
重量%、その他の金属を1〜7重量%、炭化物を30〜
70重量%、その他の非金属を10〜30重量%含み、
その平均粒径が0.1mm〜10cmであるものを挙げ
ることができる。2. Description of the Related Art When disposing of automobiles, home appliances, etc.,
Interior parts and the like are removed from other parts and crushed to form so-called shredder dust. This shredder dust is usually volume-reduced by heat treatment to be a so-called pyrolysis residue and then disposed of. This thermal decomposition residue is usually C derived from an electric component or the like, such as a copper wire.
metal particles made of a metal such as u, Fe, Pb, and Zn;
It is a mixture with particles having a relatively low specific gravity, such as carbides derived from synthetic resins. As a specific example of this thermal decomposition residue, Cu is 3 to 15% by weight, and Fe is 3 to 20%.
% By weight, 1 to 7% by weight of other metals, 30 to 30% of carbides
70% by weight, including 10 to 30% by weight of other non-metals,
The thing with the average particle diameter of 0.1 mm-10 cm can be mentioned.
【0003】[0003]
【発明が解決しようとする課題】上述のように、上記熱
分解残渣には、電気部品等に由来するCu、Fe、P
b、Zn等の有価金属が含まれている場合が多いが、従
来、この金属を回収する技術は確立されておらず、上記
熱分解残渣中の金属を効率よく回収することができる技
術が要望されていた。本発明は、上記事情に鑑みてなさ
れたもので、熱分解残渣中の金属を効率よく回収するこ
とができる方法および装置を提供することを目的とす
る。As described above, the thermal decomposition residue contains Cu, Fe, P derived from electric parts and the like.
In many cases, valuable metals such as b and Zn are contained, but a technique for recovering this metal has not been established so far, and a technique for efficiently recovering the metal in the thermal decomposition residue is desired. It had been. The present invention has been made in view of the above circumstances, and an object of the present invention is to provide a method and an apparatus capable of efficiently recovering a metal in a thermal decomposition residue.
【0004】[0004]
【課題を解決するための手段】上記課題は、金属粒子と
これより比重の低い物質からなる低比重粒子とを含む熱
分解残渣中の金属粒子を傾斜板を用いて回収する方法で
あって、傾斜板として、その上面に、熱分解残渣中の金
属粒子を傾斜板上に留める選別溝が傾斜方向に交わる方
向に沿って形成されたものを用い、熱分解残渣を傾斜板
上の選別溝より傾斜方向上部側に供給するとともに流下
水を傾斜板上に流し、熱分解残渣中の低比重粒子を傾斜
方向下部側に押し流し傾斜板から流出させつつ、傾斜板
を選別溝の溝方向に沿って揺動させ、この際、溝方向一
端部側に向けた傾斜板の移動速度を、他端部側に向けた
傾斜板の移動速度に対し高く設定する熱分解残渣中金属
の回収方法によって解決される。傾斜板としては、選別
溝が、傾斜方向上部側から下部側にかけて複数形成さ
れ、これら選別溝が、これらのうち傾斜方向最下部側に
形成されたものの他端部がこれ以外の選別溝の他端部に
比べてより溝方向他端部側に位置するように形成された
ものを用いるのが好ましい。本発明の熱分解残渣中金属
の回収装置は、傾斜板と、この傾斜板上に、金属粒子と
これより比重の低い物質からなる低比重粒子とを含む熱
分解残渣を供給する熱分解残渣供給手段と、熱分解残渣
中の低比重粒子を傾斜方向下部側に押し流す流下水を傾
斜板上に流す流下水供給手段とを備え、傾斜板上に、熱
分解残渣中の金属粒子を傾斜板上に留める選別溝を傾斜
方向に交わる方向に沿って形成したことを特徴とするも
のである。選別溝の深さは、0.5〜5mmとするのが
好ましく、幅は5〜10mmとするのが好ましい。The above object is a method of recovering metal particles in a thermal decomposition residue containing metal particles and low specific gravity particles made of a substance having a lower specific gravity than the metal particles by using an inclined plate, As the inclined plate, the one on the upper surface of which the sorting groove for retaining the metal particles in the thermal decomposition residue on the inclined plate is formed along the direction intersecting the inclination direction, the thermal decomposition residue is separated from the sorting groove on the inclined plate. The slant plate is fed along the groove direction of the sorting groove while being supplied to the upper side in the slanting direction and flowing down the water onto the slanting plate, pushing the low specific gravity particles in the pyrolysis residue to the lower side in the slanting direction and flowing out from the slanting plate. swung, this time, the groove direction one-
The moving speed of the inclined plate toward the end side, is solved by the method of recovering the pyrolysis residue metal is set higher relative to the moving speed of the inclined plate toward the other end side. As the inclined plate, a plurality of selection grooves are formed from the upper side to the lower side in the inclination direction. Among these selection grooves, those formed on the lowermost side in the inclination direction have the other end other than this. It is preferable to use the one formed so as to be located closer to the other end portion side in the groove direction than the end portion . The apparatus for recovering metal in pyrolysis residue according to the present invention supplies a pyrolysis residue containing a tilted plate and low-density particles made of a substance having a lower specific gravity than the tilted plate. And a means for supplying effluent that causes the low-gravity particles in the pyrolysis residue to flow downward in the inclination direction on the inclined plate, and the metal particles in the pyrolysis residue on the inclined plate. It is characterized in that the selection groove to be fastened to is formed along the direction intersecting the inclination direction. The depth of the sorting groove is preferably 0.5 to 5 mm, and the width thereof is preferably 5 to 10 mm.
【0005】[0005]
【発明の実施の形態】図1および図2は、本発明の熱分
解残渣中金属の回収装置(以下、金属回収装置という)
の一実施形態を示すもので、ここに示す金属回収装置1
は、傾斜板2と、熱分解残渣を傾斜板2上に供給する熱
分解残渣供給手段となる熱分解残渣供給部3と、傾斜板
2上の熱分解残渣中の低比重粒子を傾斜方向下部側に押
し流す流下水を傾斜板2上に流す流下水供給手段となる
流下水供給管4とから概略構成されている。1 and 2 show a device for recovering metal in a pyrolysis residue of the present invention (hereinafter referred to as a metal recovery device).
1 shows an embodiment of a metal recovery device 1 shown here.
Is a slant plate 2, a pyrolysis residue supply unit 3 that serves as a pyrolysis residue supply unit that supplies the pyrolysis residue onto the slope plate 2, and a low specific gravity particle in the pyrolysis residue on the slope plate 2 in the slanting direction. The effluent water supply pipe 4 serves as a effluent water supply means for causing the effluent water to be pushed to the side to flow on the inclined plate 2.
【0006】傾斜板2は、矩形状に形成され、その上面
には、傾斜方向に対しほぼ垂直な方向に沿う複数の突条
5が形成されている。これら突条5は傾斜板2の傾斜方
向上部側から下部側にかけて多段に形成されている。こ
れら突条5同士の隙間を、以下選別溝6という。これら
突条5は、傾斜板2上に選別溝6を形成し、これにより
熱分解残渣中の金属粒子が流下水によって押し流される
のを防ぎ金属粒子を傾斜板2上に留めるためのもので、
傾斜板2の一端部を基点として他端方向に延びるよう形
成され、その長さが傾斜板2の傾斜方向にかけて徐々に
長くなり、最長となる傾斜方向最下部のものの他端部
が、傾斜板2の他端部付近に至るように形成されてい
る。The inclined plate 2 is formed in a rectangular shape, and a plurality of protrusions 5 are formed on the upper surface thereof along a direction substantially perpendicular to the inclination direction. These ridges 5 are formed in multiple stages from the upper side to the lower side of the inclined plate 2 in the inclination direction. The gap between the ridges 5 will be referred to as a selection groove 6 hereinafter. These ridges 5 form a sorting groove 6 on the inclined plate 2 to prevent the metal particles in the pyrolysis residue from being swept away by the flowing water and to keep the metal particles on the inclined plate 2.
The inclined plate 2 is formed so as to extend in the other end direction from one end of the inclined plate 2, and the length gradually increases in the inclination direction of the inclined plate 2, and the other end of the longest lower portion in the inclination direction is the inclined plate. It is formed so as to reach near the other end of No. 2.
【0007】上記突条5の高さ、すなわち選別溝6の深
さは、大きすぎれば回収した金属中への低比重粒子混入
量が増加し、小さすぎれば流下水により傾斜板2上を押
し流され傾斜板2から流出する金属粒子量が増大し金属
回収率が低下するため、0.5〜5mmとするのが好ま
しい。また突条5同士の間隔、すなわち選別溝6の幅は
5〜10mmとするのが好ましい。If the height of the ridges 5, that is, the depth of the sorting groove 6 is too large, the amount of low specific gravity particles mixed into the recovered metal increases, and if it is too small, the sludge plate 2 is washed away by the falling water. Since the amount of metal particles flowing out from the inclined plate 2 increases and the metal recovery rate decreases, it is preferably 0.5 to 5 mm. Further, it is preferable that the interval between the protrusions 5, that is, the width of the selection groove 6 is 5 to 10 mm.
【0008】傾斜板2の水平面に対する傾斜角度、すな
わち図2に示す傾斜角度αは、2〜10度とするのが好
ましい。これは、この傾斜角度が2度未満であると、回
収した金属中への低比重粒子混入量が増加し、10度を
越えると、流下水により傾斜板2上を押し流され傾斜板
から流出する金属粒子量が増大し金属回収率が低下する
ためである。傾斜板2には、図示せぬ揺動装置が取り付
けられており、傾斜板2を選別溝6の溝方向に沿って揺
動させることができるようになっている。The inclination angle of the inclined plate 2 with respect to the horizontal plane, that is, the inclination angle α shown in FIG. 2, is preferably 2 to 10 degrees. This is because when the inclination angle is less than 2 degrees, the amount of low-density particles mixed into the recovered metal increases, and when it exceeds 10 degrees, the falling water pushes the inclined plate 2 and flows out from the inclined plate. This is because the amount of metal particles increases and the metal recovery rate decreases. A swinging device (not shown) is attached to the inclined plate 2, so that the inclined plate 2 can be swung along the groove direction of the selection groove 6.
【0009】傾斜板2の他端側には、傾斜方向上部側か
ら下部側にかけて、選別溝6内に残留した粒子を残留粒
子として回収するための残留粒子受け8が設けられ、下
縁部には、一端側から他端側にかけて、流下水により押
し流され傾斜板2から流出した粒子を流出粒子として回
収するための流出粒子受け9が設けられている。At the other end of the inclined plate 2, there is provided a residual particle receiver 8 for recovering the particles remaining in the selection groove 6 as residual particles from the upper side to the lower side in the inclination direction, and at the lower edge thereof. Is provided with an outflow particle receiver 9 for collecting, as outflow particles, particles that have been washed away by the falling water and flowed out of the inclined plate 2 from one end side to the other end side.
【0010】熱分解残渣供給部3は、傾斜板2の一端側
であり、かつ選別溝6より傾斜方向上部側である位置に
設けられている。流下水供給管4は、傾斜板2上の選別
溝6より傾斜方向上部側に、傾斜板2の一端側から他端
側にかけて設けられており、この流下水供給管4には、
その長さ方向に間隔をおいて複数の流下水供給孔7が設
けられ、流下水を傾斜板2上の一端側から他端側にわた
る広い範囲に流すことができるようになっている。The thermal decomposition residue supply unit 3 is provided at a position on one end side of the inclined plate 2 and on the upper side of the selection groove 6 in the inclination direction. The falling water supply pipe 4 is provided above the sorting groove 6 on the inclined plate 2 in the inclination direction from one end side to the other end side of the inclined plate 2, and the flowing water supply pipe 4 includes:
A plurality of downflow water supply holes 7 are provided at intervals in the lengthwise direction so that the downflow water can flow in a wide range from one end side to the other end side on the inclined plate 2.
【0011】次に、上記装置を用いた場合を例として、
本発明の熱分解残渣中金属の回収方法の一実施形態を説
明する。まず熱分解残渣を、熱分解残渣供給部3を通し
て傾斜板2上に供給する。この熱分解残渣としては、予
め粉砕処理および篩い分けを施し、その平均粒径を2m
m以下としたものを用いると、回収した金属の不純物含
有量を低く抑えることができるため好ましい。また熱分
解残渣は、水中に懸濁した状態、すなわちスラリー状と
して傾斜板2上に供給するのが好ましい。同時に、流下
水供給管4を用いて、流下水を傾斜板2上に流す。な
お、流下水を、流下水供給管4からだけでなく熱分解残
渣供給部3から傾斜板2上に流すことも可能である。Next, taking the above-mentioned device as an example,
An embodiment of the method for recovering the metal in the thermal decomposition residue of the present invention will be described. First, the thermal decomposition residue is supplied onto the inclined plate 2 through the thermal decomposition residue supply unit 3. The thermal decomposition residue is pulverized and sieved in advance to give an average particle size of 2 m.
It is preferable to use one having a thickness of m or less because the impurity content of the recovered metal can be suppressed to a low level. Further, it is preferable that the thermal decomposition residue is suspended in water, that is, supplied as a slurry on the inclined plate 2. At the same time, the falling water is supplied onto the inclined plate 2 by using the falling water supply pipe 4. In addition, it is possible to flow the spilled water not only from the spilled water supply pipe 4 but also from the thermal decomposition residue supply unit 3 onto the inclined plate 2.
【0012】また同時に、傾斜板2を選別溝6の溝方向
に沿って揺動させる。この際、選別溝6一端方向(残留
粒子受け8方向に対し逆の方向)への傾斜板2の移動速
度を、他端方向(残留粒子受け8方向)への傾斜板2の
移動速度に対し高く設定する。傾斜板2の揺動条件は特
に限定されないが、具体例としては、傾斜板2の揺動回
数を1分間当たり230〜280回とした場合を挙げる
ことができる。At the same time, the inclined plate 2 is swung along the groove direction of the selection groove 6. At this time, the moving speed of the inclined plate 2 in one direction of the sorting groove 6 (the direction opposite to the residual particle receiving direction 8) is relative to the moving speed of the inclined plate 2 in the other direction (remaining particle receiving direction 8). Set higher. The rocking condition of the tilt plate 2 is not particularly limited, but a specific example is a case where the tilt plate 2 is rocked 230 to 280 times per minute.
【0013】傾斜板2上に供給された熱分解残渣中の金
属粒子および低比重粒子は流下水に押し流され、傾斜板
2の傾斜方向に向かって移動し、選別溝6内に入る。上
述のように、傾斜板2は、選別溝6一端方向(残留粒子
受け8方向に対し逆の方向)への傾斜板2の移動速度
が、他端方向(残留粒子受け8方向)への傾斜板2の移
動速度に対し高くなるように揺動するため、選別溝6内
の金属粒子および低比重粒子は、傾斜板2が他端方向へ
移動する際に傾斜板2と共にこの方向へ移動しやすく、
かつ傾斜板2が一端方向へ移動する際に慣性力によりこ
の方向へ移動しにくくなり、これにより選別溝6の他端
方向に向けて徐々に移動する。The metal particles and low specific gravity particles in the pyrolysis residue supplied onto the inclined plate 2 are swept away by the flowing water, move in the inclination direction of the inclined plate 2 and enter the sorting groove 6. As described above, in the inclined plate 2, the moving speed of the inclined plate 2 in the one end direction (direction opposite to the residual particle receiving 8 direction) of the sorting groove 6 is inclined in the other end direction (remaining particle receiving 8 direction). The metal particles and the low specific gravity particles in the sorting groove 6 move in this direction together with the inclined plate 2 when the inclined plate 2 moves in the other end direction because the metal particles and the low specific gravity particles in the sorting groove 6 move so as to be higher than the moving speed of the plate 2. Easy,
In addition, when the inclined plate 2 moves toward one end, it becomes difficult to move in this direction due to inertial force, and thus gradually moves toward the other end of the selection groove 6.
【0014】この際、熱分解残渣のうち、合成樹脂等に
由来する炭化物等からなる低比重粒子は、低比重である
ため流下水によって突条5を乗り越えて傾斜方向に押し
流されやすい。このため、大部分の低比重粒子は、傾斜
板傾斜方向への移動速度が傾斜板他端方向への移動速度
より大きくなり、選別溝6の他端部に達する以前に傾斜
板2の傾斜方向下部側から流出し流出粒子受け9上に集
まる。At this time, among the pyrolysis residues, low specific gravity particles made of carbide or the like derived from synthetic resin have a low specific gravity, so that they are easily swept in the inclined direction by running water over the ridges 5. Therefore, most of the low specific gravity particles have a moving speed in the tilting direction of the tilting plate that is higher than a moving speed in the other end direction of the tilting plate, and the tilting direction of the tilting plate 2 before reaching the other end of the sorting groove 6. It flows out from the lower side and collects on the outflow particle receiver 9.
【0015】これに対し銅線等に由来する金属粒子は、
高比重であるため流下水によって流されにくく、選別溝
6内に留まりやすい。このため、大部分の金属粒子は、
傾斜板他端方向への移動速度が傾斜板傾斜方向への移動
速度より大きくなり、傾斜板2の傾斜方向最下部に達す
る以前に選別溝6の他端から出ることとなる。On the other hand, metal particles derived from copper wire, etc.
Since it has a high specific gravity, it is hard to be washed away by the falling water and easily stays in the sorting groove 6. Therefore, most metal particles are
The moving speed in the other direction of the inclined plate becomes faster than the moving speed in the inclined direction of the inclined plate, and the inclined plate 2 exits from the other end of the sorting groove 6 before reaching the lowermost portion in the inclined direction.
【0016】上述のように、突条5は、傾斜板2の一端
部を基点とし、長さが傾斜板2の傾斜方向にかけて徐々
に長くなるように形成されているため、選別溝6は、傾
斜方向最下部側のものの他端部が、これ以外の選別溝6
の他端部に比べてより溝方向他端側に位置するものとな
っている。As described above, since the ridge 5 is formed such that the one end of the inclined plate 2 serves as a base point and the length thereof gradually increases in the inclination direction of the inclined plate 2, the selection groove 6 is The other end of the lowermost one in the tilt direction is the other sorting groove 6
Is located on the other end side in the groove direction as compared with the other end.
【0017】このため、傾斜方向最下部側に位置する選
別溝6以外の選別溝6から出た金属粒子は、流下水によ
って傾斜方向に流れ、下方側に隣接する選別溝6内に至
り、最終的には上記最下部側の選別溝6内に至ることと
なる。上記最下部側の選別溝6は、その他端部が傾斜板
2の他端部付近に位置するように設けられているため、
その内部の金属粒子は、この選別溝6の他端部から出た
後、傾斜板2の他端部に設けられた残留粒子受け8上に
集まる。Therefore, the metal particles that come out of the sorting grooves 6 other than the sorting groove 6 located on the lowermost side in the tilt direction flow in the tilting direction by the flowing water, reach the inside of the sorting groove 6 adjacent to the lower side, and finally reach the final position. Specifically, it reaches the inside of the sorting groove 6 on the lowermost side. Since the sorting groove 6 on the lowermost side is provided so that the other end is located near the other end of the inclined plate 2,
The metal particles in the inside exit from the other end of the sorting groove 6 and then collect on the residual particle receiver 8 provided at the other end of the inclined plate 2.
【0018】また、熱分解残渣中に塩素化合物が含まれ
ている場合には、この塩素化合物が流下水中に溶け込ん
で傾斜板2から流出するため、残留粒子受け8および流
出粒子受け9上に集められた金属粒子および低比重粒子
中の塩素含有量は低下する。なお上記操作を行うにあた
り、傾斜板2から流れ落ちた流下水はそのまま排出して
もよいが、流下水供給管4に戻し、流下水供給管4を通
して再び傾斜板2上に流すのが運転コスト抑制の観点か
ら好ましい。When the thermal decomposition residue contains a chlorine compound, the chlorine compound dissolves in the flowing water and flows out from the inclined plate 2. Therefore, the chlorine compound is collected on the residual particle receiver 8 and the outflow particle receiver 9. The content of chlorine in the obtained metal particles and low specific gravity particles decreases. In performing the above operation, the spilled water that has flowed down from the sloping plate 2 may be discharged as it is, but it is necessary to return it to the spilling water supply pipe 4 and to flow it again on the sloping plate 2 through the spilling water supply pipe 4 to reduce the operating cost. From the viewpoint of.
【0019】残留粒子受け8上に集められた金属粒子
は、金属製品原材料として再資源化することができる。
一方、流出粒子受け9上に集められた低比重粒子は、炭
化物を多く含むものであるため、燃料等として再利用す
ることができる。The metal particles collected on the residual particle receiver 8 can be recycled as a metal product raw material.
On the other hand, since the low specific gravity particles collected on the outflow particle receiver 9 contain a large amount of carbide, they can be reused as fuel or the like.
【0020】上記金属回収方法にあっては、熱分解残渣
を、選別溝6を有する傾斜板2上に供給するとともに傾
斜板2上に流下水を流し、熱分解残渣中の低比重粒子を
傾斜方向下部側に押し流し傾斜板2から流出させ、傾斜
板2の選別溝6内に残留した金属粒子を残留粒子受け8
に集めて回収するので、熱分解残渣中の低比重粒子を効
率よく金属粒子から分離し、不純物含有量の少ない金属
粒子を効率よくかつ容易に回収することができる。In the above metal recovery method, the pyrolysis residue is supplied onto the inclined plate 2 having the sorting groove 6 and the flowing water is caused to flow over the inclined plate 2 to incline the low specific gravity particles in the pyrolysis residue. The metal particles remaining in the sorting groove 6 of the inclined plate 2 are washed away by the residual particle receiver 8
Since the low specific gravity particles in the thermal decomposition residue are efficiently separated from the metal particles, the metal particles having a low impurity content can be efficiently and easily recovered.
【0021】また、傾斜板2として、複数の選別溝6
が、最下部側のものの他端部がこれ以外の選別溝6の他
端部に比べてより溝方向他端側に位置するように形成さ
れたものを用いることによって、すべての選別溝6内の
金属粒子を最終的に最下部側の選別溝6の他端部を経由
させた後に残留粒子受け8上に集めることができる。従
って、選別溝6内の金属粒子を容易に一カ所に集めるこ
とができ、金属回収操作を容易化することができる。As the inclined plate 2, a plurality of sorting grooves 6 are provided.
However, by using the one formed so that the other end of the lowermost one is located closer to the other end in the groove direction than the other ends of the other sorting grooves 6, Finally, the metal particles can be collected on the residual particle receiver 8 after passing through the other end of the sorting groove 6 on the lowermost side. Therefore, the metal particles in the sorting groove 6 can be easily collected in one place, and the metal recovery operation can be facilitated.
【0022】また、残留粒子および流出粒子として得ら
れた金属粒子および低比重粒子はそれぞれ再利用可能と
なるため、廃棄処理コスト削減を図ることができる。ま
た、熱分解残渣中のCu、Pb等の重金属が廃棄処理に
より環境中へ放出されるのを防ぐことができ、環境保全
の観点からも好適である。さらに、熱分解残渣中に塩素
化合物が含まれている場合でも、この塩素化合物を流下
水で洗い流し、回収した金属粒子または低比重粒子を、
塩素含有量が少なく、加熱時に塩化物ガスなどの有害ガ
スを発することがなく安全性の高いものとすることがで
きる。Further, the residual particles and the metal particles and the low specific gravity particles obtained as the outflow particles can be reused, respectively, so that the disposal cost can be reduced. Further, it is possible to prevent heavy metals such as Cu and Pb in the thermal decomposition residue from being released into the environment due to the waste treatment, which is also preferable from the viewpoint of environmental protection. Furthermore, even if a chlorine compound is contained in the thermal decomposition residue, the chlorine compound is washed away with running water, and the recovered metal particles or low specific gravity particles are
The chlorine content is low, and no harmful gas such as chloride gas is emitted during heating, so that the safety can be improved.
【0023】また上記金属回収装置1にあっては、傾斜
板2と、この傾斜板2上に熱分解残渣を供給する熱分解
残渣供給部3と、熱分解残渣中の低比重粒子を傾斜方向
下部側に押し流し傾斜板2から流出させる流下水を供給
する流下水供給管4とを備え、傾斜板2上に、熱分解残
渣中の金属粒子を傾斜板上に留める選別溝6を形成した
ので、熱分解残渣中の低比重粒子を効率よく分離し、不
純物含有量の少ない金属粒子を効率よくかつ容易に回収
することができる。Further, in the metal recovery device 1, the inclined plate 2, the thermal decomposition residue supply unit 3 for supplying the thermal decomposition residue onto the inclined plate 2, and the low specific gravity particles in the thermal decomposition residue in the inclination direction. Since there is a falling water supply pipe 4 for supplying the falling water that flows to the lower side and flows out from the inclined plate 2, a sorting groove 6 for retaining the metal particles in the pyrolysis residue on the inclined plate 2 is formed on the inclined plate 2. The low specific gravity particles in the thermal decomposition residue can be efficiently separated, and the metal particles having a low impurity content can be efficiently and easily recovered.
【0024】なお、本発明の金属回収方法は上記実施形
態のものに限らず、上記操作によって回収した残留粒子
を、再び同様の工程に供することも可能であり、これに
より不純物含有量がより低い金属を回収することができ
る。この場合には、2度目以降の回収操作で用いる傾斜
板2の傾斜角度を、1度目の回収操作で用いる傾斜板2
の傾斜角度よりも大きくし、1度目の操作で金属粒子中
に混入した不純物となる低比重粒子が分離除去されやす
くするのが好ましい。The metal recovery method of the present invention is not limited to that of the above embodiment, and the residual particles recovered by the above operation can be subjected to the same step again, whereby the impurity content is lower. The metal can be recovered. In this case, the inclination angle of the inclined plate 2 used in the second and subsequent recovery operations is set to the inclination plate 2 used in the first recovery operation.
It is preferable to make it larger than the inclination angle of No. 1 to make it easier to separate and remove the low specific gravity particles as impurities mixed in the metal particles by the first operation.
【0025】[0025]
【実施例】以下、具体例を示して本発明の効果を明確化
する。
(実施例1〜4)図1に示す金属回収装置1を用いて熱
分解残渣試料中金属の回収試験を行った。ここで用いた
金属回収装置1は、傾斜板2の幅(傾斜方向長さ)が4
6.6cm、長さ(傾斜方向に対し垂直な方向の長さ)
が84.4cmであり、傾斜板2上に傾斜方向にかけて
22本の突条5が形成され、これら突条5の幅が6m
m、高さ(選別溝6深さ)が0.6〜3.4mmである
ものとした。突条5間の選別溝6の幅は8mmとした。
傾斜板2の傾斜角度は、3〜7度とした。EXAMPLES Hereinafter, the effects of the present invention will be clarified by showing concrete examples. (Examples 1 to 4) A recovery test of metal in the pyrolysis residue sample was conducted using the metal recovery apparatus 1 shown in FIG. In the metal recovery device 1 used here, the width of the inclined plate 2 (the length in the inclination direction) is 4
6.6 cm, length (length perpendicular to the tilt direction)
Is 84.4 cm, 22 protrusions 5 are formed on the inclined plate 2 in the inclination direction, and the width of these protrusions 5 is 6 m.
m, and the height (the depth of the selection groove 6) was 0.6 to 3.4 mm. The width of the selection groove 6 between the protrusions 5 was 8 mm.
The inclination angle of the inclined plate 2 was 3 to 7 degrees.
【0026】熱分解残渣試料としては、家電品由来のシ
ュレッダダストを熱処理した後、粉砕機により粒度が約
2mmとなるまで粉砕したものを用いた。この熱分解残
渣92.8gを、50mlの水に懸濁させた状態とし、
これを上記回収装置1の熱分解残渣供給部3から傾斜板
2上に供給した。同時に、流下水を流下水供給管4およ
び熱分解残渣供給部3を通して流量3300ml/mi
nで傾斜板2上に供給した。また傾斜板2を選別溝6に
沿う方向に揺動させ、この際、傾斜板2の一端方向への
移動速度を他端方向への移動速度に対し高くなるように
設定した。上記操作により、選別溝6内に残留した粒
子、および流下水により押し流された粒子を、それぞれ
残留粒子受け8および流出粒子受け9上に回収した。As the pyrolysis residue sample, a shredder dust derived from home electric appliances was heat-treated and then pulverized by a pulverizer to a particle size of about 2 mm. 92.8 g of this thermal decomposition residue was suspended in 50 ml of water,
This was supplied onto the inclined plate 2 from the thermal decomposition residue supply unit 3 of the recovery device 1. At the same time, the flow rate of the flowing water is 3300 ml / mi through the flowing water supply pipe 4 and the pyrolysis residue supply unit 3.
n on the inclined plate 2. Further, the inclined plate 2 was swung in the direction along the selection groove 6, and at this time, the moving speed of the inclined plate 2 in one end direction was set to be higher than the moving speed in the other end direction. By the above operation, the particles remaining in the sorting groove 6 and the particles washed away by the falling water were collected on the residual particle receiver 8 and the outflow particle receiver 9, respectively.
【0027】(実施例5)実施例1〜4と同様の操作に
より金属回収操作を行い、続いて、残留粒子受け8上に
集められた残留粒子を再び50mlの水に懸濁させた状
態で傾斜板2上に供給し、上記過程に従って再び金属回
収操作を行った。傾斜板2の傾斜角度は、1回目の回収
操作時には2度、2回目の回収操作時には3.5度とし
た。上記実施例1〜5によって回収された残留粒子およ
び流出粒子中の金属分および非金属分の含有率(重量基
準)、および残留粒子中に回収された金属分の回収率
(重量基準)を測定した。試験結果を表1および表2に
示す。(Embodiment 5) A metal recovery operation is carried out in the same manner as in Embodiments 1 to 4, and then the residual particles collected on the residual particle receiver 8 are suspended again in 50 ml of water. It was supplied onto the inclined plate 2 and the metal recovery operation was performed again according to the above process. The inclination angle of the inclined plate 2 was 2 degrees during the first recovery operation and 3.5 degrees during the second recovery operation. The contents of metal and non-metal components in the residual particles and outflow particles collected by the above Examples 1 to 5 (weight basis), and the recovery of the metal components recovered in residual particles (weight basis) were measured. did. The test results are shown in Tables 1 and 2.
【0028】[0028]
【表1】 [Table 1]
【0029】[0029]
【表2】 [Table 2]
【0030】表1より、熱分解残渣試料中の金属成分と
して最も多く含まれるCuは、残留粒子中の含有率が、
熱分解残渣試料中の含有率に比べ遥かに高く、実施例1
〜5の回収方法によって、不純物含有量が少ない金属粒
子を回収することができたことがわかる。また、表2よ
り、実施例1〜5の回収方法によって、熱分解残渣試料
中の金属粒子を高い効率で回収することができたことが
わかる。From Table 1, Cu, which is the most contained as a metal component in the pyrolysis residue sample, has a content rate in the residual particles of
The content is much higher than that in the pyrolysis residue sample,
It can be seen that the metal particles having a low impurity content could be collected by the collection methods of ~ 5. Further, it can be seen from Table 2 that the metal particles in the pyrolysis residue sample could be recovered with high efficiency by the recovery methods of Examples 1 to 5.
【0031】[0031]
【発明の効果】以上説明したように、本発明の熱分解残
渣中金属の回収方法にあっては、熱分解残渣中の低比重
粒子を効率よく分離し、不純物含有量の少ない金属粒子
を効率よくかつ容易に回収することができる。また、得
られた金属粒子および低比重粒子はそれぞれ再利用可能
となるため、廃棄処理コスト削減を図ることができる。
また、熱分解残渣中の重金属が廃棄処理により環境中へ
放出されるのを防ぐことができ、環境保全の観点からも
好適である。As described above, in the method for recovering metal in the pyrolysis residue of the present invention, the low specific gravity particles in the pyrolysis residue are efficiently separated, and the metal particles having a low impurity content are efficiently separated. It can be collected well and easily. Further, the obtained metal particles and low specific gravity particles can be reused, respectively, so that the disposal cost can be reduced.
Further, it is possible to prevent the heavy metal in the thermal decomposition residue from being released into the environment due to the waste treatment, which is also preferable from the viewpoint of environmental protection.
【図1】 本発明の金属回収装置の一実施形態を示す平
面図である。FIG. 1 is a plan view showing an embodiment of a metal recovery device of the present invention.
【図2】 図1に示す回収装置の側面図である。FIG. 2 is a side view of the recovery device shown in FIG.
1・・・金属回収装置、 2・・・傾斜板、3・・・熱分解残渣
供給部(熱分解残渣供給手段)、4・・・流下水供給管
(流下水供給手段)、6・・・選別溝DESCRIPTION OF SYMBOLS 1 ... Metal recovery device, 2 ... Inclined plate, 3 ... Pyrolysis residue supply part (pyrolysis residue supply means), 4 ... Flowing water supply pipe (flowing water supply means), 6 ...・ Selection groove
───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) B03B 1/00 - 13/06 ─────────────────────────────────────────────────── ─── Continuation of front page (58) Fields surveyed (Int.Cl. 7 , DB name) B03B 1/00-13/06
Claims (3)
なる低比重粒子とを含む熱分解残渣中の金属粒子を傾斜
板を用いて回収する方法であって、 傾斜板として、その上面に、熱分解残渣中の金属粒子を
傾斜板上に留める選別溝が傾斜方向に交わる方向に沿っ
て形成されたものを用い、 熱分解残渣を傾斜板上の選別溝より傾斜方向上部側に供
給するとともに流下水を傾斜板上に流し、熱分解残渣中
の低比重粒子を傾斜方向下部側に押し流し傾斜板から流
出させつつ、傾斜板を選別溝の溝方向に沿って揺動さ
せ、この際、溝方向一端部側に向けた傾斜板の移動速度
を、他端部側に向けた傾斜板の移動速度に対し高く設定
することを特徴とする熱分解残渣中金属の回収方法。1. A method for recovering metal particles in a pyrolysis residue containing metal particles and low specific gravity particles made of a substance having a lower specific gravity than that using an inclined plate, wherein the inclined plate has an upper surface, Using a sorting groove that holds metal particles in the pyrolysis residue on the inclined plate along the direction that intersects the inclination direction, the pyrolysis residue is supplied to the upper side in the inclination direction from the selection groove on the inclined plate. Flowing water is flown on the inclined plate, the low specific gravity particles in the pyrolysis residue are pushed to the lower side in the inclined direction and flowed out from the inclined plate, while the inclined plate is swung along the groove direction of the selection groove. A method for recovering metal in a pyrolysis residue, characterized in that the moving speed of the inclined plate toward one end side in the direction is set higher than the moving speed of the inclined plate toward the other end side .
側から下部側にかけて複数形成され、これら選別溝が、
これらのうち傾斜方向最下部側に形成されたものの他端
部がこれ以外の選別溝の他端部に比べてより溝方向他端
部側に位置するように形成されたものを用いることを特
徴とする請求項1記載の熱分解残渣中金属の回収方法。2. As the inclined plate, a plurality of selection grooves are formed from the upper side to the lower side in the inclination direction, and these selection grooves are
More groove direction end than the other end portion of the other end portion but is formed in the inclined direction bottom side of these other sorting groove
The method for recovering the metal in the pyrolysis residue according to claim 1, wherein a metal formed so as to be located on the side of the section is used.
これより比重の低い物質からなる低比重粒子とを含む熱
分解残渣を供給する熱分解残渣供給手段と、熱分解残渣
中の低比重粒子を傾斜方向下部側に押し流す流下水を傾
斜板上に流す流下水供給手段とを備え、 傾斜板上に、熱分解残渣中の金属粒子を傾斜板上に留め
る選別溝を傾斜方向に交わる方向に沿って形成したこと
を特徴とする熱分解残渣中金属の回収装置。3. A slant plate, a pyrolysis residue supply means for supplying a pyrolysis residue containing metal particles and low specific gravity particles made of a substance having a specific gravity lower than that to the slope plate, and Equipped with a sewage supply means for flowing the sewage that pushes the low specific gravity particles to the lower side in the tilt direction on the tilt plate, and in the tilt direction, a sorting groove that holds the metal particles in the pyrolysis residue on the tilt plate. A device for recovering metal in a pyrolysis residue, which is formed along the intersecting direction.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP34555297A JP3430892B2 (en) | 1997-12-15 | 1997-12-15 | Method and apparatus for recovering metal in pyrolysis residue |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP34555297A JP3430892B2 (en) | 1997-12-15 | 1997-12-15 | Method and apparatus for recovering metal in pyrolysis residue |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH11169744A JPH11169744A (en) | 1999-06-29 |
| JP3430892B2 true JP3430892B2 (en) | 2003-07-28 |
Family
ID=18377375
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP34555297A Expired - Fee Related JP3430892B2 (en) | 1997-12-15 | 1997-12-15 | Method and apparatus for recovering metal in pyrolysis residue |
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| Country | Link |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
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| JP4953254B2 (en) * | 2008-08-05 | 2012-06-13 | シャープ株式会社 | Processing methods for LED products |
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1997
- 1997-12-15 JP JP34555297A patent/JP3430892B2/en not_active Expired - Fee Related
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| Publication number | Publication date |
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