JP4710501B2 - Foreign matter sorter - Google Patents

Foreign matter sorter Download PDF

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JP4710501B2
JP4710501B2 JP2005266519A JP2005266519A JP4710501B2 JP 4710501 B2 JP4710501 B2 JP 4710501B2 JP 2005266519 A JP2005266519 A JP 2005266519A JP 2005266519 A JP2005266519 A JP 2005266519A JP 4710501 B2 JP4710501 B2 JP 4710501B2
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glass powder
flow path
glass
unit
powder group
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JP2007075721A (en
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弥彦 酒井
弘光 杉浦
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Panasonic Corp
Panasonic Holdings Corp
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Panasonic Corp
Matsushita Electric Industrial Co Ltd
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本発明は、テレビやコンピュータのディスプレイなどに用いるブラウン管のガラス材を再資源として回収するための異物選別機に関するものである。   The present invention relates to a foreign material sorter for collecting glass material of a cathode ray tube used for a television or a computer display as a resource.

従来より、テレビやコンピュータのディスプレイなどに用いるブラウン管のガラス材を再資源化するための方法は、いろいろなものが提案されている。   Conventionally, various methods have been proposed for recycling glass materials of cathode ray tubes used for televisions and computer displays.

主な作業手順は、以下のとおりである。   The main work procedure is as follows.

まず、テレビやディスプレイを手作業にて解体し、筐体内部からブラウン管を取り出す。   First, the TV and display are dismantled manually, and the cathode ray tube is taken out from the inside of the housing.

次に、ブラウン管を構成するガラスの特性の違いから、ブラウン管をパネルとファンネルに分割する。   Next, the cathode ray tube is divided into a panel and a funnel due to the difference in the characteristics of the glass constituting the cathode ray tube.

分割後、ファンネルは次工程である破砕機にて破砕し、小さなガラス片にする。   After the division, the funnel is crushed by a crusher, which is the next process, into small glass pieces.

一方、パネルはブラウン管の内面に塗布していた蛍光材を除去した後、次工程である破砕機にて破砕する。   On the other hand, after removing the fluorescent material applied to the inner surface of the cathode ray tube, the panel is crushed by a crusher as the next step.

破砕は、ダブルロールクラッシャーやジョークラッシャーなどに代表される破砕機で行う。   The crushing is performed by a crusher represented by a double roll crusher or a jaw crusher.

そして、破砕されたガラス片は、次工程である洗浄工程にて乾式洗浄を施される。   And the crushed glass piece is dry-cleaned in the washing | cleaning process which is a next process.

この洗浄工程については、ガラスパウダーを用いてブラスト洗浄を施すものや、ドラムシェイカーのように容器内にガラス片を入れ、この容器を回転させることで内容物であるガラス片同士を擦り合わせる、というものがよく知られた方法である。   About this cleaning process, it is said that glass blasting is performed using glass powder, glass pieces are put in a container like a drum shaker, and the glass pieces that are the contents are rubbed together by rotating this container Things are a well-known method.

そして、洗浄工程にてガラス片表面の異物を除去した後、混在するほこりや金属くずをふるい機や磁選機を用いて除去することで、有価物としてのガラス片が回収できる。(例えば、特許文献1、特許文献2参照)
なお、上記ブラスト洗浄で発生したガラス粉体には、蛍光材やほこり、金属くずなどの異物が多く混在するため、再資源化が困難であり廃棄していた。
特開平10−137732号公報 特開2000−233170号公報
And after removing the foreign material on the surface of a glass piece by a washing | cleaning process, the glass piece as valuables can be collect | recovered by removing the mixed dust and metal waste using a sieving machine or a magnetic separator. (For example, see Patent Document 1 and Patent Document 2)
Note that the glass powder generated by the blast cleaning contains many foreign materials such as fluorescent materials, dust, and metal scraps, so that it is difficult to recycle and was discarded.
JP-A-10-137732 JP 2000-233170 A

しかしながら、近年の社会的要望により、更に、ブラウン管のガラス材の回収率を向上しようとした場合、従来廃棄していた粒径1mmに満たないガラス粉体を再資源化する必要性が高くなってくる。   However, due to social demands in recent years, the need to recycle glass powder with a particle size of less than 1 mm, which has been disposed of in the past, has been increased when trying to improve the recovery rate of CRT glass materials. come.

つまり、上記廃棄していたガラス粉体はテレビセットの重量比で5%程度を占めるため、更に改善する必要性がある。   In other words, the discarded glass powder occupies about 5% by weight of the television set, and thus needs to be further improved.

また、上記従来の技術に記載のガラス再処理装置を活用するためには、設備に見合った処理台数が必要となる。   Moreover, in order to utilize the glass reprocessing apparatus described in the above-mentioned conventional technology, the number of treatments corresponding to the equipment is required.

つまり、大都市近郊では、その装置が有する能力を最適な状態で稼動できるブラウン管の処理台数が得られるものの、人工が少ない地域や、離島などでは過剰な設備投資となるという課題があった。   In other words, in the suburbs of large cities, although the number of CRTs that can be operated in the optimum state of the equipment can be obtained, there has been a problem of excessive capital investment in areas where there are few man-made areas or remote islands.

そこで本発明は、このような課題を解決するものであり、大規模施設で発生するガラス粉体を再資源化し、処理台数が少ない地域に適した小型の異物選別機を提供するものである。   Therefore, the present invention solves such problems, and recycles the glass powder generated in a large-scale facility, and provides a small foreign matter sorter suitable for an area where the number of treatments is small.

本発明は、上記目的を達成するために、投入するガラス粉体群に応じて、投入部に投入したガラス粉体群が流れる流路を第1の通路と第2の通路とのいずれかに切り換えるというものである。   In order to achieve the above object, according to the present invention, depending on the glass powder group to be charged, the flow path through which the glass powder group charged into the charging portion flows is either the first path or the second path. It is to switch.

さらに本発明は、投入部と流路切換部との間にガラス粉体群がこの流路切換部に与える衝撃を緩める緩衝部を設けるというものである。   Further, according to the present invention, a buffer part is provided between the charging part and the flow path switching part to relax the impact of the glass powder group on the flow path switching part.

本構成により、ガラス粉体、塗布材、ほこりや金属くず等が混在するガラス粉体群より、粒径1mmに満たないガラス粉体を取り出すことが可能となる。   With this configuration, it is possible to take out glass powder having a particle size of less than 1 mm from a glass powder group in which glass powder, coating material, dust, metal scraps, and the like are mixed.

また本構成により、ガラス粉体群が流路切換部に衝突する際の衝撃を小さくすることができる。   Also, with this configuration, the impact when the glass powder group collides with the flow path switching unit can be reduced.

本発明によれば、従来、再資源として顧みられることがなかったガラス粉体をガラス材の再生資源として用いることができるため、廃ブラウン管から得る再使用可能なガラス材の回収率が向上する。   According to the present invention, since glass powder that has not been considered as a resource for recycling can be used as a recycling resource for glass material, the recovery rate of the reusable glass material obtained from the waste cathode ray tube is improved.

また、本発明によれば、投入部と流路切換部との間にガラス粉体群がこの流路切換部に与える衝撃を緩める緩衝部を設けることで、流路切換部の磨耗の進行を抑制することが可能となり、異物選別機をメンテナンスする割合を抑制できる。   In addition, according to the present invention, by providing a buffering part that relaxes the impact of the glass powder group on the flow path switching part between the input part and the flow path switching part, the wear of the flow path switching part is progressed. It becomes possible to suppress, and the ratio which maintains a foreign material sorter can be suppressed.

さらに、パネルとファンネルの処理工程を一つの装置内に収めたため、装置全体が小型となり、ブラウン管の処理台数が少ない地域においても過剰な設備投資とならない規模の異物選別機を得ることができる。   Furthermore, since the panel and funnel processing steps are housed in one apparatus, the entire apparatus can be reduced in size, and a foreign material sorter with a scale that does not require excessive capital investment even in an area where the number of CRTs processed is small.

本発明の実施の形態は、投入するガラス粉体群に応じて投入部に投入したガラス粉体群が流れる流路を第1の通路と第2の通路とのいずれかに切り換えるというものである。   In the embodiment of the present invention, the flow path through which the glass powder group charged into the charging section flows is switched between the first path and the second path according to the glass powder group to be charged. .

このように小型の一体型装置にて、ガラス粉体群に混在する塗布材、ほこりや金属くずを選別、除去することができるため、細かなガラス粉体を再資源として回収できる。   As described above, since the coating material, dust and metal scrap mixed in the glass powder group can be selected and removed by the small integrated apparatus, fine glass powder can be recovered as a resource.

その結果、ブラウン管で用いられたガラス材料の再利用率が向上する。   As a result, the reuse rate of the glass material used in the cathode ray tube is improved.

また、本発明の他の実施の形態は、投入部と流路切換部との間にガラス粉体群がこの流路切換部に与える衝撃を緩衝する緩衝部を設けるというものである。   In another embodiment of the present invention, a buffer unit is provided between the input unit and the channel switching unit to buffer the impact of the glass powder group on the channel switching unit.

このようにすることで、ガラス粉体が流れる流路を切り換える流路切換部の衝突による磨耗を低減するとともに、ガラス粉体同士の研磨を促進することが可能となる。   By doing in this way, it becomes possible to reduce the abrasion by the collision of the flow-path switching part which switches the flow path through which glass powder flows, and to accelerate | stimulate grinding | polishing of glass powder.

特に、ガラス粉体は粒径が細かいために、流路切換部の摺動部の隙間に入り込むことが多く、摺動部分を研磨するために流路切換部を構成する部品の寿命が短くなっていたが、緩衝部を設けることにより、摺動部の隙間にガラス粉体が入り込むことが少なくなるので、メンテナンスを行う機会を抑制することが可能となる。   In particular, since glass powder has a small particle size, it often enters the gap of the sliding part of the flow path switching part, and the life of the parts constituting the flow path switching part is shortened to polish the sliding part. However, by providing the buffer portion, the glass powder is less likely to enter the gap between the sliding portions, so that the opportunity for maintenance can be suppressed.

その結果、異物選別機の稼動率の低下を抑制することができる。   As a result, it is possible to suppress a decrease in the operating rate of the foreign matter sorter.

以下、本発明の実施例について図面を参照しながら説明する。   Embodiments of the present invention will be described below with reference to the drawings.

(実施例1)
まず、図1に本発明の異物選別機1の側面図、図2に流路切換部2の要部拡大図を示す。
Example 1
First, FIG. 1 shows a side view of the foreign matter sorter 1 of the present invention, and FIG.

図中3は、ブラスト洗浄などの洗浄作業を行うことで発生するガラス粉体、蛍光材を中心とする塗布材、金属くずやほこりからなるガラス粉体群4を投入する投入部である。また、図中5は、ガラス粉体群4から上述した異物やカーボンなどを除去し、ガラス粉体を選別するための塗布材除去部であり、ふるい機や風力選別機を用いることで実現できる。   In the figure, reference numeral 3 denotes an input unit for supplying glass powder generated by performing a cleaning operation such as blast cleaning, a coating material mainly made of a fluorescent material, and a glass powder group 4 made of metal scrap or dust. Reference numeral 5 in the figure denotes a coating material removing unit for removing the above-mentioned foreign matters and carbon from the glass powder group 4 and sorting the glass powder, and can be realized by using a sieve or a wind sorter. .

次に、図中6は磁石を用いて金属くずを除去する磁力選別部であり、用いる磁石は、電磁石でも、永久磁石でもよい。   Next, reference numeral 6 in the figure denotes a magnetic force selection unit that removes metal scraps using a magnet, and the magnet used may be an electromagnet or a permanent magnet.

これら各部を図1に示すように接続する。   These parts are connected as shown in FIG.

すなわち、第1の通路7を用いて、投入部3の下方に位置する流路切換部2と磁力選別部6とを接続する。 That is, the flow path switching unit 2 and the magnetic force sorting unit 6 located below the input unit 3 are connected using the first passage 7.

また、第2の通路8を用いて、投入部3の下方に位置する流路切換部2と塗布材除去部5とを接続し、塗布材除去部5と磁力選別部6とを第3の通路9にて接続する。 Also, using the second passage 8, the flow path switching unit 2 positioned below the charging unit 3 and the coating material removing unit 5 are connected, and the coating material removing unit 5 and the magnetic force sorting unit 6 are connected to the third channel 8. Connect through passage 9.

上記した構成において、投入するガラス粉体群4に応じて、流路切換部2を切り換える。すなわち、投入するガラス粉体群4が、ファンネルをブラスト洗浄やドラムシェイカーなどを用いて乾式洗浄した際に発生するガラス粉体群の場合、塗布材の混入が皆無なので、図2に示すように、流路切換板20をA位置に設定し、投入したガラス粉体群4が第1の通路7を経由して磁力選別部6へ流れるようにする。   In the above configuration, the flow path switching unit 2 is switched according to the glass powder group 4 to be charged. That is, in the case where the glass powder group 4 to be introduced is a glass powder group generated when the funnel is dry-cleaned using a blast cleaning or a drum shaker or the like, since there is no mixing of the coating material, as shown in FIG. The flow path switching plate 20 is set to the A position so that the charged glass powder group 4 flows to the magnetic force sorting unit 6 via the first passage 7.

一方、投入するガラス粉体群4が、パネルを乾式洗浄した際に発生するガラス粉体群の場合、蛍光材などの塗布材や、洗浄時に発生したほこりなどが多量に混在しているため、図2に点線にて示すB位置に流路切換板20を設定し、投入したガラス粉体群が第2の通路8を経由して塗布材除去部5に至るようにする。 On the other hand, when the glass powder group 4 to be added is a glass powder group that is generated when the panel is dry-cleaned, since there are a large amount of coating materials such as fluorescent materials and dust generated during the cleaning, A flow path switching plate 20 is set at a position B indicated by a dotted line in FIG. 2 so that the charged glass powder group 4 reaches the coating material removing unit 5 via the second passage 8.

塗布材除去部5には、ふるい機や風力選別機(いずれも図示せず)が設けてあり、ガラス粉体群4に混入していた塗布材やほこりなどの異物13aがガラス粉体4aと分離され、ダスト排気口10より排除される。そして、再利用できるガラス粉体4aについては、第3の通路9を経由して磁力選別部6へと送付される。   The coating material removing unit 5 is provided with a sieving machine and a wind power sorter (both not shown), and the foreign material 13a such as coating material and dust mixed in the glass powder group 4 is separated from the glass powder 4a. It is separated and removed from the dust exhaust port 10. The reusable glass powder 4 a is sent to the magnetic force sorting unit 6 via the third passage 9.

上述したように、異なる経路を辿って磁力選別部6に送り込まれたガラス粉体(図示せず)から、磁石(図示せず)による磁力を用いて金属くずを除去する。   As described above, scrap metal is removed from the glass powder (not shown) sent to the magnetic force sorting unit 6 along different paths by using the magnetic force of a magnet (not shown).

以上の工程を経たガラス粉体4bは、ガラス粉体回収口11から回収できる。   The glass powder 4b having undergone the above steps can be recovered from the glass powder recovery port 11.

その後、磁力選別部6から磁石を取り除いた後、金属くず回収口12から除去された金属くず13bを回収する。   Then, after removing the magnet from the magnetic sorting unit 6, the metal scrap 13b removed from the metal scrap recovery port 12 is recovered.

次に、図2を用いて、流路切換部2について説明する。   Next, the flow path switching unit 2 will be described with reference to FIG.

図中、20は流路切換板であり、この流路切換板20を図2中、A位置、B位置に設置することにより、投入されたガラス粉体群4を第1の通路7、第2の通路8へと導くことができる。   In the figure, reference numeral 20 denotes a flow path switching plate. By installing this flow path switching plate 20 at positions A and B in FIG. To the second passage 8.

ところで、ガラス粉体は粒径が小さく研磨作用があるため、流路切換板20で頻繁にガラス粉体が衝突する場所は損傷が激しく、部品の交換頻度が高くなる。   By the way, since the glass powder has a small particle size and has a polishing action, the place where the glass powder frequently collides with the flow path switching plate 20 is severely damaged, and the frequency of replacement of parts becomes high.

特に、流路切換板20がA位置からB位置へと摺動する摺動部は、ガラス粉体が集まりやすく、しかも、その隙間にガラス粉体が入り込みやすいために、部品の磨耗が加速され、損傷が激しい。   In particular, the sliding portion where the flow path switching plate 20 slides from the A position to the B position tends to collect glass powder, and the glass powder easily enters the gap, so that the wear of parts is accelerated. The damage is severe.

さらに、ガラス粉体群4が固まりすぎると、ガラス粉体群4同士の分離が進まないという課題がある。   Furthermore, if the glass powder group 4 is too hard, there is a problem that the separation between the glass powder groups 4 does not proceed.

ここで、投入部3と流路切換部2との間に緩衝部21を設置する。   Here, the buffer unit 21 is installed between the input unit 3 and the flow path switching unit 2.

緩衝部21には、図に示すように格子状の板が設けてあり、ガラス粉体群4を適度に拡散することができる。   As shown in the figure, the buffer portion 21 is provided with a lattice-like plate, and the glass powder group 4 can be appropriately diffused.

その結果、流路切換板20の特定部位へのガラス粉体群4の衝突が発生しなくなり、局部の磨耗発生を抑制することができるので、異物選別機1のメンテナンス頻度を抑制することができる。   As a result, the collision of the glass powder group 4 with the specific part of the flow path switching plate 20 does not occur, and the occurrence of local wear can be suppressed, so that the maintenance frequency of the foreign matter sorter 1 can be suppressed. .

また、ガラス粉体群4を適度に拡散することで、ガラス粉体とほこりや塗布材などの異物との分離が加速し、塗布材除去部5や磁力選別部6での異物除去効果が高くなる。   Further, by appropriately diffusing the glass powder group 4, the separation of the glass powder from foreign matters such as dust and coating material is accelerated, and the foreign matter removing effect in the coating material removing unit 5 and the magnetic force sorting unit 6 is high. Become.

すなわち、回収されるガラス粉体4bの異物付着や異物混入率が低下するため、再資源としてのガラス粉体の品質が向上する。   That is, since the foreign matter adhesion and the foreign matter mixing rate of the collected glass powder 4b are reduced, the quality of the glass powder as a resource is improved.

なお、上述したように、一体型の装置にてパネル、ファンネルの両方のガラスを処理できる異物選別機を実現したが、取り扱う処理量によっては、第1の通路8を取り外し、第2の通路、第3の通路のみの簡単な構成とすることも可能である。   In addition, as described above, a foreign material sorter capable of processing both panel and funnel glass with an integrated apparatus has been realized, but depending on the amount of processing, the first passage 8 is removed, the second passage, It is also possible to have a simple configuration with only the third passage.

つまり、ファンネルに用いていたガラス粉体は塗布材除去部5を経由する必要ないが、作業工数を増やすことで異物選別機1をシンプルな構成とするができ、設備の初期投資をより抑制することが可能となる。 That is, although glass powder was used in the funnel is not necessary to go through the coating material removing unit 5, can but a foreign matter sorter 1 with simple configuration by increasing the number of working steps, more suppress initial investment capital It becomes possible to do.

つまり、過大な設備投資を必要とすることなく、ガラスの再資源化に取り組むことができるようになる。   In other words, it becomes possible to tackle the recycling of glass without requiring excessive capital investment.

本発明は、食品に用いる粉体など、あらゆる粉体と金属くずとの選別に用いることができる。   INDUSTRIAL APPLICABILITY The present invention can be used for sorting all kinds of powders such as powders used for foods and scrap metal.

本発明の一実施例における異物選別機の側面図The side view of the foreign material sorter in one example of the present invention 本発明の一実施例における流路切換部の要部拡大図The principal part enlarged view of the flow-path switching part in one Example of this invention.

符号の説明Explanation of symbols

1 異物選別機
2 流路切換部
3 投入部
4 ガラス粉体群
4a、4b ガラス粉体
5 塗布材除去部
6 磁力選別部
7 第1の通路
8 第2の通路
9 第3の通路
10 ダスト排気口
11 ガラス粉体回収口
12 金属くず回収口
13a 異物
13b 金属くず
20 流路切換板
21 緩衝部
DESCRIPTION OF SYMBOLS 1 Foreign material sorter 2 Flow path switching part 3 Input part 4 Glass powder group 4a, 4b Glass powder 5 Coating material removal part 6 Magnetic force selection part 7 1st path 8 2nd path 9 3rd path 10 Dust exhaust Port 11 Glass powder recovery port 12 Metal scrap recovery port 13a Foreign matter 13b Metal scrap 20 Channel switching plate 21 Buffer

Claims (3)

ブラウン管ガラスを破砕して得られる小さなガラス片の洗浄作業により発生するガラス粉体群を投入する投入部と、ガラス粉体に塗布された塗布材を除去する塗布材除去部と、前記ガラス粉体群に混入している金属くずを選別する磁力選別部と、前記投入部と前記塗布材除去部および前記磁力選別部との間に流路切換部と、一端を前記流路切換部と接続し他端を前記磁力選別部と接続する第1の通路と、一端を前記流路切換部と接続し他端を前記塗布材除去部と接続する第2の通路と、一端を前記塗布材除去部と接続し他端を前記磁力選別部と接続する第3の通路とを具備し、前記流路切換部は、前記ブラウン管ガラスのファンネルの洗浄作業により発生するガラス粉体群前記投入部投入する場合にこのガラス粉体群が流れる流路を前記第1の通路とし、前記ブラウン管ガラスのパネルの洗浄作業により発生するガラス粉体群を前記投入部へ投入する場合にこのガラス粉体群が流れる流路を前記第2の通路と切り換えることを特徴とする異物選別機。 An input part for introducing a glass powder group generated by a cleaning operation of a small glass piece obtained by crushing a cathode ray tube glass, an application material removing part for removing an application material applied to the glass powder, and the glass powder A magnetic force sorting part for sorting metal scraps mixed in the group, a flow path switching part between the charging part, the coating material removing part and the magnetic force sorting part, and one end connected to the flow path switching part. A first passage connecting the other end to the magnetic force sorting unit, a second passage connecting one end to the flow path switching unit and the other end to the coating material removal unit, and one end to the coating material removal unit the connection to the other end; and a third passage connecting said magnetic separation unit and the flow path switching section is turned on the glass powder group generated by the cleaning operation of the funnel of the cathode ray tube glass into the insertion portion wherein a flow path through which the glass powder group when A first passage, characterized in that the flow path through which the glass powder group when introducing the glass powder group generated by the cleaning operation of the panel of the cathode ray tube glass into the insertion portion switches and the second passage Foreign matter sorter. さらに、前記投入部と前記流路切換部との間に前記ガラス粉体群がこの流路切換部に与える衝撃を緩める緩衝部を設けたことを特徴とする請求項1に記載の異物選別機。 The foreign matter sorter according to claim 1, further comprising a buffer unit that relaxes an impact of the glass powder group on the channel switching unit between the charging unit and the channel switching unit. . 前記ガラス粉体群は、粒径1mm未満のガラス粉体からなることを特徴とする請求項1または2に記載の異物選別機。The foreign matter sorter according to claim 1 or 2, wherein the glass powder group is made of glass powder having a particle size of less than 1 mm.
JP2005266519A 2005-09-14 2005-09-14 Foreign matter sorter Expired - Fee Related JP4710501B2 (en)

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Citations (4)

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Publication number Priority date Publication date Assignee Title
JPH10137732A (en) * 1996-11-12 1998-05-26 Matsushita Seiko Eng Kk Regeneration pretreating system for television picture tube
JP2000135450A (en) * 1998-10-30 2000-05-16 Mitsubishi Electric Corp Crusher, classifier, crushing and classification
JP2000233170A (en) * 1999-02-12 2000-08-29 Matsushita Electric Ind Co Ltd Method and apparatus for recycling cathode ray tube
JP2004525744A (en) * 2000-10-27 2004-08-26 フオルクスヴアーゲン アクチエンゲゼルシヤフト Apparatus and method for treating shredder residue and use of the resulting fiber waste fraction

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH10137732A (en) * 1996-11-12 1998-05-26 Matsushita Seiko Eng Kk Regeneration pretreating system for television picture tube
JP2000135450A (en) * 1998-10-30 2000-05-16 Mitsubishi Electric Corp Crusher, classifier, crushing and classification
JP2000233170A (en) * 1999-02-12 2000-08-29 Matsushita Electric Ind Co Ltd Method and apparatus for recycling cathode ray tube
JP2004525744A (en) * 2000-10-27 2004-08-26 フオルクスヴアーゲン アクチエンゲゼルシヤフト Apparatus and method for treating shredder residue and use of the resulting fiber waste fraction

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