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JP4809066B2 - Exhaust method of waste plastic high density volume reduction molding machine - Google Patents
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JP4809066B2 - Exhaust method of waste plastic high density volume reduction molding machine - Google Patents

Exhaust method of waste plastic high density volume reduction molding machine Download PDF

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Publication number
JP4809066B2
JP4809066B2 JP2006010176A JP2006010176A JP4809066B2 JP 4809066 B2 JP4809066 B2 JP 4809066B2 JP 2006010176 A JP2006010176 A JP 2006010176A JP 2006010176 A JP2006010176 A JP 2006010176A JP 4809066 B2 JP4809066 B2 JP 4809066B2
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molding machine
vent
waste plastic
fluff
volume reduction
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JP2007190767A (en
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泰彦 森
正治 中村
司 柴田
昭啓 市江
孝志 佐藤
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Nippon Steel Corp
Nippon Steel Engineering Co Ltd
Nippon Steel Plant Designing Corp
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Nittetsu Plant Designing Corp
Nippon Steel Corp
Nippon Steel Engineering Co Ltd
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    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/62Plastics recycling; Rubber recycling

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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 reduction molding 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 reduction molding machine 1 in which the rotating screw 1b is disposed in the cylinder 1a is melted and kneaded by heating by the heater and the frictional heat of the fluff while moving by the rotation of the screw 1b. Extruded from the die 1c. The waste plastic volume reduction molding machine is provided with a vent, and water vapor and volatile matter generated in the volume reduction molding machine are extracted from the vent by a vacuum pump. The extruded kneaded product is cut into pellets by the rotary blade 2 (see Patent Document 1).

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。
特開平6−293021号公報
In the high-density volume reduction molding machine 1, the temperature is raised to 180 to 220 ° C. by the heating by the heater and the frictional heat of the fluff itself, so that the specific gravity of the single pellet is increased. In high-density volume reduction molding, volume reduction waste does not occur, so that the handling can be improved, and the coke production and coke quality can be improved.
Japanese Patent Laid-Open No. 6-293021

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ブロアで排気し、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し、前記第1ベントからの排気を減速させることによりフラフの飛散を抑えてブロワ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 reduction molding machine that compresses and melts the introduced fluff while moving it with a rotating screw and extrudes the melt to produce pellets. The steam evaporated from the fluff is exhausted by the blower from the first vent disposed in the region where a part of the fluff charged into the waste plastic high-density volume reduction molding machine in the first stage starts to melt, The volatile matter of the melt is sucked with a vacuum pump from the second vent disposed in the region where the melting of the raw material has progressed in the second stage, and the exhaust from the first vent is decelerated to suppress fluff scattering. And sucking with a blower .

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 reduction molding machine 1 in which the rotating screw 1b is disposed in the cylinder 1a is melted and kneaded by heating with the heater and the frictional heat of the raw material while moving by the rotation of the screw 1b. Extruded from the die 1c. The extruded kneaded material is cut into the pellets 3 by the rotary blade 2.

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 first vent 4 disposed in a region where a part of the raw material begins to melt, and the exhaust gas is sent to a dust collector.

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 second vent 5 disposed in the region where the melting of the raw material has further progressed, and the gas existing inside the melt is actively sucked, Perform deaeration to improve specific gravity. As shown in FIG. 2, the exhaust from the second vent 5 is sucked by the vacuum pump 7 through the trap 6.

図3は第1段階の排気行程を示し、(a)〜(c)は参考例、(d)は本発明の実施例を示す図である。 FIG. 3 shows the exhaust stroke of the first stage, (a) to (c) are reference examples , and ( d) is a diagram showing an embodiment 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 first vent 4 is disposed in a region of the raw material of the high-density volume reduction molding machine 1 where a part of the raw material starts to melt, and is generated by evaporation of water adhering to the raw material from the first vent 4. The steam is exhausted, once released into the atmosphere, and then sucked from the hood 9 by the blower 8 provided in the dust collection pipe and sent to the dust collector through the trap 6. If the generation of water vapor is not constant, the blower 8 sucks the exhaust gas and the air by releasing the exhaust gas to the atmosphere. Therefore, even if the exhaust gas amount fluctuates, a constant amount of gas can be sucked. The exhaust gas can be processed stably without being affected by the fluctuation of the dust line.

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 blower 8 provided in piping, and may send to a dust collector through dust collection piping.

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 blower 8 is once released to the atmosphere so as not to be affected by the fluctuation of the dust collection line, and then the blower ( (Not shown) may be used.

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 1st vent 4 with the reduction tower 12. FIG.

参考例〉
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。
< Reference 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、参考例の条件で、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 the reference example. 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.

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である。It is the schematic of the waste plastics high density molding machine used for the deaeration method of this invention. 第2ベントの吸引ラインを示す図である。It is a figure which shows the suction line of a 2nd vent. 第1ベントの排気方法を示し、(a)〜(c)は参考例、(d)は本発明の実施例を示す図である。The exhaust method of a 1st vent is shown, (a) -(c) is a reference example , ( d) is a figure which shows the Example of this invention. 従来の廃プラスチック高密度成形機の概略図である。It is the schematic of the conventional waste plastics high density molding machine.

符号の説明Explanation of symbols

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 reduction molding machine 1a: Cylinder 1b: Screw 1c: Die
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

Claims (1)

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ブロアで排気し、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し、前記第1ベントからの排気を減速させることによりフラフの飛散を抑えてブロアで吸引することを特徴とする廃プラスチック高密度減容成形機の排気方法。 In the exhaust method of the waste plastic high-density volume molding machine that compresses and melts the introduced fluff while moving it with a rotating screw and extrudes the melt to produce pellets, exhausting is performed in the first stage and the second stage, Water vapor evaporated from the fluff is exhausted by a blower from a first vent disposed in a region where a part of the fluff charged into the waste plastic high-density reduction molding machine in the first stage starts to melt, and then the second The volatile matter of the melt is sucked with a vacuum pump from the second vent arranged in the region where the melting of the raw material has progressed in stages, and the blowout of the fluff is suppressed by slowing down the exhaust from the first vent. An exhaust method for a waste plastic high-density volume reduction molding machine characterized by suction .
JP2006010176A 2006-01-18 2006-01-18 Exhaust method of waste plastic high density volume reduction molding machine Expired - Lifetime JP4809066B2 (en)

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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
JP4847800B2 (en) * 2006-06-16 2011-12-28 新日本製鐵株式会社 Waste plastic high density volume reduction molding machine and its exhaust method
KR101346291B1 (en) * 2013-05-20 2013-12-31 한국기계연구원 Asr molding apparatus with superior moldability

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JPS609710A (en) * 1983-06-29 1985-01-18 Japan Steel Works Ltd:The Manufacture of reclaimed pellet
JPS62151317A (en) * 1985-12-26 1987-07-06 Teijin Eng Kk Melting and extruding method for plastic resin and its device
JPS6397515U (en) * 1986-12-12 1988-06-24
JPH0727131Y2 (en) * 1989-10-03 1995-06-21 宇部興産株式会社 Extruder
JPH03190709A (en) * 1989-12-21 1991-08-20 Diafoil Co Ltd Extrusion molding of thermoplastic resin
JP2895714B2 (en) * 1993-06-24 1999-05-24 新日本製鐵株式会社 Extruder structure in waste plastic recycling facility
JPH08120284A (en) * 1994-10-27 1996-05-14 Nippon Steel Corp Extruder structure in waste plastic recycling facility
JPH10180761A (en) * 1996-12-25 1998-07-07 Matsushita Electric Ind Co Ltd Waste plastic material reduction equipment
JP3905253B2 (en) * 1999-06-09 2007-04-18 株式会社日本製鋼所 Waste plastic dehydrochlorination equipment
JP3895103B2 (en) * 2000-10-13 2007-03-22 株式会社日本製鋼所 Waste plastic dechlorination equipment
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