JP2007190767A - Exhaust method of high-density volume-reducing molding machine of waste plastic - Google Patents
Exhaust method of high-density volume-reducing molding machine of waste plastic Download PDFInfo
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- JP2007190767A JP2007190767A JP2006010176A JP2006010176A JP2007190767A JP 2007190767 A JP2007190767 A JP 2007190767A JP 2006010176 A JP2006010176 A JP 2006010176A JP 2006010176 A JP2006010176 A JP 2006010176A JP 2007190767 A JP2007190767 A JP 2007190767A
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- 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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/62—Plastics recycling; Rubber recycling
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Abstract
Description
本発明は、廃プラスチックを圧縮・混練してペレットを製造する廃プラスチック高密度減容成形機の排気方法に関するものである。 The present invention relates to a method for exhausting a waste plastic high-density volume reducing machine that compresses and kneads waste plastic to produce pellets.
容器包装リサイクル法によって自治体より排出される廃プラスチックをコークス原料としてリサイクルする設備において、廃プラスチックは粗破砕・選別・二次破砕によりペレット化に適した成分および形状のフラフとなり、減容成形機により減容されペレットが製造される。減容成形機で発生する排ガスは水封式真空ポンプを使用して抜き取られて集じん機へ送られる。 In equipment that recycles waste plastic discharged from local governments by the Containers and Packaging Recycling Law as raw materials for coke, the waste plastic becomes a fluff with components and shapes suitable for pelletization by rough crushing, sorting, and secondary crushing. The volume is reduced to produce pellets. The exhaust gas generated in the volume reduction molding machine is extracted using a water ring vacuum pump and sent to a dust collector.
図4は従来の廃プラスチック減容成形機の概略を示す概略図である。 FIG. 4 is a schematic view showing an outline of a conventional waste plastic volume reduction molding machine.
シリンダー1a内に回転するスクリュー1bが配置された高密度減容成形機1に供給されたフラフは、スクリュー1bの回転により移動しながらヒータによる加熱とフラフの自己の摩擦熱により溶融、混練されてダイス1cから押し出される。廃プラスチック減容成形機にはベントが設けられ、ベントから減容成形機内で発生した水蒸気や揮発分が真空ポンプにより抜き取られる。押し出された混練物は回転刃2により切断されてペレットとなる(特許文献1参照)。
The fluff supplied to the high-density volume
高密度減容成形機1ではヒータによる加熱とフラフの自己の摩擦熱により180〜220℃に昇温し、ペレット単体比重を高密度にする。高密度減容成形では、減容くずが発生しないためにハンドリング製が向上し、またコークス生産量、コークス品質を向上させることが可能となる。
従来の高密度減容成形機では、フラフに同伴される空気、付着した水分の蒸発により発生した水蒸気、溶融物から発生する揮発分などの気体を減容の過程で抜き取らないと、気体がペレット内部に残留し、膨張して空洞が大きくなって比重が低下してしまう。そのため、水蒸気及び揮発分などの気体をまとめて一つのベントから真空ポンプで高密度減容成形機内から抜くため、大きな能力を有する真空ポンプでないと十分に気体を抜くことができず、さらに、溶融物内部に存在する気体を十分に吸引することができなかった。そのため、ペレットの比重を高密度にできない場合があった。さらに、フラフが溶融する前に吸引されて飛散するだけでなく、後工程の集じんラインの影響を受けて安定した排気吸引ができない場合があった。 In a conventional high-density volume-reduction molding machine, if the gas such as air entrained by the fluff, water vapor generated by evaporation of attached water, volatile matter generated from the melt is not extracted during the volume reduction process, the gas will be pelletized. It remains inside, expands, and the cavity becomes larger, reducing the specific gravity. For this reason, gas such as water vapor and volatile matter is collectively extracted from a single vent from the inside of the high-density volume reduction molding machine using a vacuum pump. The gas present inside the object could not be sufficiently sucked. Therefore, the specific gravity of the pellet may not be high. Further, not only the fluff is sucked and scattered before melting, but there are cases where stable exhaust suction cannot be performed due to the influence of the dust collection line in the subsequent process.
そこで、本発明は、高密度減容成形機内の気体を効率よく排出するとともに、溶融物内部の気体を効率よく吸引することにより、ペレットの比重を向上させることができる廃プラスチック高密度減容成形機の排気方法を提供するものである。 Therefore, the present invention efficiently discharges the gas in the high-density volume reduction molding machine and efficiently sucks the gas inside the melt, thereby improving the specific gravity of the waste plastic. A method for exhausting the aircraft is provided.
本発明は、投入されたフラフを回転するスクリュで移動させながら圧縮溶融し、溶融物を押し出してペレットを製造する廃プラスチック高密度減容成形機の排気方法において、排気を第1段階と第2段階で行い、前記第1段階で廃プラスチック高密度減容成形機に投入されたフラフの一部が溶融し始める領域に配設された第1ベントからフラフより蒸発した水蒸気を排気し、次いで前記第2段階で原料の溶融が進行した領域に配設された第2ベントから溶融物の揮発分を真空ポンプで吸引することを特徴とする。 The present invention relates to an exhaust method of a waste plastic high-density volume molding machine that compresses and melts a thrown fluff while moving it with a rotating screw, and extrudes the melt to produce pellets. The steam evaporated from the fluff is exhausted from a first vent disposed in a region where a part of the fluff charged into the waste plastic high-density volume reduction molding machine in the first step begins to melt, It is characterized in that the volatile matter of the melt is sucked by a vacuum pump from the second vent arranged in the region where the melting of the raw material has progressed in the second stage.
前記第1段階の第1ベントからの排気は、(1)トラップを介してブロアで吸引する、(2)第1ベントからの排気を一旦大気開放した後、フードを介してブロアで吸引する、(3)前記ブロアで吸引した気体を一旦大気開放した後、フードを介して集じんラインのブロアで吸引する、(4)第1ベントからの排気を減速塔で減速した後、ブロワで吸引することができる。 The exhaust from the first vent in the first stage is (1) sucked with a blower through a trap, (2) the exhaust from the first vent is once released to the atmosphere, and then sucked with a blower through a hood. (3) The gas sucked by the blower is once released to the atmosphere, and then sucked by a dust collection line blower via a hood. (4) The exhaust from the first vent is decelerated by a reduction tower and then sucked by a blower. be able to.
本発明は、高密度減容成形機の排気を2段階で行い、まず、第1段階で、原料の一部が溶融し始める領域に配設された第1ベントで蒸発する水蒸気を自発的に排気することにより、フラフの飛散を抑えながら、後工程の集じんラインの変動による影響を受けずに安定した排気ができる。 The present invention performs the exhaust of the high-density volume reduction molding machine in two stages. First, in the first stage, the vapor that evaporates in the first vent disposed in the region where a part of the raw material starts to melt is spontaneously generated. By exhausting, stable exhaust can be achieved without being affected by fluctuations in the dust collection line in the subsequent process while suppressing scattering of fluff.
次ぎに、第2段階で、更に原料の溶融が進行した領域に配設された第2ベントから真空ポンプで吸引することで、溶融物内部に存在する気体を積極的に吸引することで、ペレットの比重を向上させることができる。 Next, in the second stage, the pellets are obtained by actively sucking the gas present in the melt by sucking with a vacuum pump from the second vent disposed in the region where the melting of the raw material has proceeded. The specific gravity can be improved.
また、2段階では、主として溶融物の揮発分を排気するので、第2段階では大きい能力の真空ポンプを使用することなく、且つ集じんラインの影響を受けずに安定した排気吸引が可能となる。 In the second stage, the volatile component of the melt is mainly exhausted. In the second stage, stable exhaust suction is possible without using a vacuum pump having a large capacity and without being affected by the dust collection line. .
図1は本発明の脱気方法に使用する廃プラスチック高密度成形機の概略図、図2は第2ベントの吸引ラインを示す図である。 FIG. 1 is a schematic view of a waste plastic high-density molding machine used in the degassing method of the present invention, and FIG. 2 is a view showing a suction line of a second vent.
シリンダー1a内に回転するスクリュー1bが配置された高密度減容成形機1に供給されたフラフは、スクリュー1bの回転により移動しながらヒータによる加熱と原料の自己の摩擦熱により溶融、混練されてダイス1cから押し出される。押し出された混練物は回転刃2により切断されてペレット3となる。
The fluff supplied to the high-density volume
本発明では、高密度減容成形機内で発生する気体を2段階で排気する。まず、第1段階で、原料の一部が溶融し始める領域に配設された第1ベント4から原料に付着した水分の蒸発により発生した水蒸気が排出され、排気は集じん機へ送られる。
In the present invention, the gas generated in the high-density volume reduction molding machine is exhausted in two stages. First, in the first stage, water vapor generated by evaporation of water adhering to the raw material is discharged from the
次ぎに第2段階で、さらに原料の溶融が進行した領域に配設された第2ベント5から排気を真空ポンプで吸引し、溶融物内部に存在する気体を積極的に吸引し、溶融物の比重を向上させるための脱気を行う。図2に示すように、第2ベント5の排気は、トラップ6を介して真空ポンプ7で吸引される。
Next, in the second stage, exhaust gas is sucked with a vacuum pump from the
図3は本発明の第1段階の排気行程を示す図である。 FIG. 3 is a diagram showing an exhaust stroke in the first stage of the present invention.
図3(a)において、高密度減容成形機1の、原料の一部が溶融し始める領域に第1ベント4が配設され、この第1ベント4から原料に付着した水分の蒸発により発生した水蒸気を排気し、一旦大気開放し、次いで集じん配管に設けたブロア8によりフード9から吸引しトラップ6を介して集じん機へ送る。水蒸気の発生が一定していない場合、排気を一旦大気開放することによりブロア8は排気と大気を吸引するので、排気量が変動しても一定量のガスを吸引することができ、また、集じんラインの変動に伴う影響を受けることなく安定して排気を処理することができる。
In FIG. 3A, the
なお、原料に付着している水分がほぼ一定し水蒸気の発生が一定している場合は、図3(b)に示すように、排気を大気開放することなく、第1ベントの排気を集じん配管に設けたブロアブ8で吸引し集じん配管を経て集じん機へ送ってもよい。
If the moisture adhering to the raw material is almost constant and the generation of water vapor is constant, the exhaust from the first vent is collected without opening the exhaust to the atmosphere as shown in FIG. You may suck | suck with the
また、図3(c)に示すように、集じんラインの変動に伴う影響を受けないように、ブロア8で吸引した気体を一旦大気開放した後、フード10を介して集じんラインのブロア(図示せず)で吸引してもよい。
Further, as shown in FIG. 3C, the gas sucked by the
また、図3(d)に示すように、第1ベント4からの排気を減速塔12で減速させることによりフラフの飛散を抑えることができる。
Moreover, as shown in FIG.3 (d), the scattering of a fluff can be suppressed by decelerating the exhaust_gas | exhaustion from the
〈実施例〉
高密度減容成形機にフラフを4.2t/h投入して2段階で排気した。第1ベントを図3(a)に示す大気開放により排気し、溶融温度190〜200℃、第2ベントのガス温度150℃、真空ポンプの吸引圧力100Torrで吸引した。ペレットの比重は、0.9であった。
<Example>
A fluff was introduced into a high-density volume reduction molding machine at 4.2 t / h and exhausted in two stages. The first vent was evacuated by opening to the atmosphere shown in FIG. 3A, and suctioned at a melting temperature of 190 to 200 ° C., a gas temperature of the second vent of 150 ° C., and a vacuum pump suction pressure of 100 Torr. The specific gravity of the pellet was 0.9.
〈従来技術〉
第1ベントを塞ぎ、実施例1の条件で、第2ベントのみから真空ポンプで吸引した。ペレットの比重は0.7であった。
<Conventional technology>
The first vent was closed, and suction was performed with a vacuum pump only from the second vent under the conditions of Example 1. The specific gravity of the pellet was 0.7.
本発明に従って2段階で排気することにより、ペレットの比重が第2ベントのみで吸引するよりもペレットの比重を向上させることができた。また、フラフの飛散が抑えられて安定した運転ができた。 By exhausting in two stages according to the present invention, the specific gravity of the pellet could be improved as compared with the case where the specific gravity of the pellet was sucked only by the second vent. In addition, scattering of fluff was suppressed and stable operation was possible.
1:高密度減容成形機
1a:シリンダー
1b:スクリュー
1c:ダイス
2:回転刃
3:ペレット
4:第1ベント
5:第2ベント
6:トラップ
7:真空ポンプ
8:ブロア
9:フード
10:フード
11:ブロア
12:減速塔
1: High density volume
2: Rotating blade 3: Pellet 4: First vent 5: Second vent
6: Trap 7: Vacuum pump 8: Blower 9: Hood 10: Hood 11: Blower 12: Reduction tower
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Cited By (3)
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---|---|---|---|---|
JP2007331305A (en) * | 2006-06-16 | 2007-12-27 | Nippon Steel Corp | Exhaust method of high density volume reducing molding machine of waste plastic |
JP2007331304A (en) * | 2006-06-16 | 2007-12-27 | Nippon Steel Corp | High density volume reducing molding machine of waste plastic and exhaust method therefor |
KR101346291B1 (en) | 2013-05-20 | 2013-12-31 | 한국기계연구원 | Asr molding apparatus with superior moldability |
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JP2007331304A (en) * | 2006-06-16 | 2007-12-27 | Nippon Steel Corp | High density volume reducing molding machine of waste plastic and exhaust method therefor |
JP4653699B2 (en) * | 2006-06-16 | 2011-03-16 | 新日本製鐵株式会社 | Exhaust method of waste plastic high density volume reduction molding machine and waste plastic high density volume reduction molding machine |
KR101346291B1 (en) | 2013-05-20 | 2013-12-31 | 한국기계연구원 | Asr molding apparatus with superior moldability |
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