JP2006249801A - Asphalt recycling plant - Google Patents

Asphalt recycling plant Download PDF

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JP2006249801A
JP2006249801A JP2005068736A JP2005068736A JP2006249801A JP 2006249801 A JP2006249801 A JP 2006249801A JP 2005068736 A JP2005068736 A JP 2005068736A JP 2005068736 A JP2005068736 A JP 2005068736A JP 2006249801 A JP2006249801 A JP 2006249801A
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exhaust
dryer
exhaust gas
flue
temperature
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JP4677255B2 (en
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Hideto Horai
秀人 蓬莱
Hideki Okada
英輝 岡田
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Nikko Co Ltd
Nikko KK
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Nikko Co Ltd
Nikko KK
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Abstract

<P>PROBLEM TO BE SOLVED: To provide an asphalt recycling plant for preventing the occurrence of a fire by preventing the vaporized asphalt content in exhaust gas from sticking in a flue. <P>SOLUTION: A deodorizing furnace 11 is arranged on the downstream of the exhaust flue 7 of a drier 1, and a waste material is heated by supplying high temperature gas of the deodorizing furnace 11 to the drier 1 via a high temperature gas supply duct 5. A branch duct 14 formed by branching off the high temperature gas supply duct 5, is connected to the exhaust flue 7 on the downstream of the drier 1, so as not to condense the vaporized asphalt content in the exhaust gas by heightening the exhaust gas temperature in the exhaust flue 7 by introducing the high temperature gas into the exhaust flue 7. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

本発明は、道路工事等により発生するアスファルト舗装廃材を加熱再生するアスファルトリサイクルプラントに関する。   The present invention relates to an asphalt recycle plant that heats and recycles asphalt pavement waste material generated by road construction and the like.

アスファルト舗装廃材(以下「廃材」という)を加熱再生するアスファルトリサイクルプラントのドライヤにて廃材を加熱すると、アスファルト分が気化してドライヤの排気煙道下流に導出されるが、排ガス温度が200℃程度であるため、排ガス中の気化したアスファルト分が煙道内壁付近では更に温度低下して凝縮し、排気煙道の内壁に付着することがある。そして、排ガスが一時的に高温になれば発火し、また火種が飛んでくると引火するなどして火災の原因となることがある。このアスファルト分の排気煙道への付着防止の一手段として、排気煙道内に石粉を混入し、アスファルト分を石粉で被覆して非粘着性として排気煙道内に付着しないようにする方法も考えられる(特許文献1参照)。
特開昭60−230407号公報
When waste material is heated in an asphalt recycle plant dryer that heats and recycles asphalt pavement waste material (hereinafter referred to as “waste material”), the asphalt content is vaporized and led to the exhaust flue downstream of the dryer, but the exhaust gas temperature is around 200 ° C. Therefore, the vaporized asphalt content in the exhaust gas may be further condensed at the temperature near the flue inner wall, and may adhere to the inner wall of the exhaust flue. And, if the exhaust gas becomes temporarily high temperature, it may ignite, and if a fire is flying, it may ignite and cause a fire. As a means to prevent this asphalt from adhering to the exhaust flue, it is also possible to mix stone powder into the exhaust flue and coat it with stone powder so that it does not stick to the exhaust flue. (See Patent Document 1).
JP 60-230407 A

しかしながら、前記のように、石粉でアスファルト分を非粘着性とするには多量の石粉が必要であって、維持管理も厄介であるという問題を有しており、もう少し簡単にアスファルト分の煙道付着を防止できる方法の出現を要望されていた。   However, as mentioned above, there is a problem that a large amount of stone powder is required to make the asphalt content non-sticky with stone powder, and maintenance is troublesome, and the flue for asphalt is a little easier. There has been a demand for the appearance of a method capable of preventing adhesion.

本発明は上記の点に鑑み、排ガス中の気化したアスファルト分が煙道内に付着しないようにして火災の発生を防止するようにしたアスファルトリサイクルプラントを提供することを課題とする。   This invention makes it a subject to provide the asphalt recycle plant which prevented generation | occurrence | production of a fire by preventing the vaporized asphalt part in waste gas from adhering in a flue in view of said point.

本発明は上記の課題を解決するために、請求項1記載のアスファルトリサイクルプラントにあっては、廃材加熱用のドライヤの排気煙道下流に排ガス中の臭気成分を加熱分解する脱臭炉を配設し、該脱臭炉から導出される高温ガスを高温ガス供給ダクトを介して前記ドライヤに供給して廃材を加熱する一方、前記高温ガス供給ダクトを分岐して形成した分岐ダクトの末端をドライヤ出口の排気煙道に連結し、高温排ガスの一部をドライヤ出口の排気煙道内へと導くようにしたことを特徴としている。   In order to solve the above problems, the present invention provides an asphalt recycle plant according to claim 1, wherein a deodorizing furnace for thermally decomposing odorous components in exhaust gas is disposed downstream of an exhaust flue of a dryer for heating waste materials. The high-temperature gas derived from the deodorizing furnace is supplied to the dryer via a high-temperature gas supply duct to heat the waste material, while the end of the branch duct formed by branching the high-temperature gas supply duct is connected to the dryer outlet. It is connected to the exhaust flue and is characterized in that a part of the high temperature exhaust gas is led into the exhaust flue at the outlet of the dryer.

また、請求項2記載のアスファルトリサイクルプラントにあっては、前記分岐ダクトに開度調整用ダンパーを配設し、ドライヤの出口の排気煙道に配設した排ガス温度検出計にて検出する排ガス温度に基づいて前記開度調整用ダンパーの開度調整制御を行うことを特徴としている。   Further, in the asphalt recycle plant according to claim 2, an exhaust gas temperature detected by an exhaust gas temperature detector disposed in the exhaust flue at the outlet of the dryer, wherein an opening adjusting damper is disposed in the branch duct. The opening adjustment control of the opening adjustment damper is performed based on the above.

本発明の請求項1記載のアスファルトリサイクルプラントによれば、廃材加熱用のドライヤの排気煙道下流に排ガス中の臭気成分を加熱分解する脱臭炉を配設し、該脱臭炉から導出される高温ガスを高温ガス供給ダクトを介して前記ドライヤに供給して廃材を加熱する一方、前記高温ガス供給ダクトを分岐して形成した分岐ダクトの末端をドライヤ出口の排気煙道に連結し、高温排ガスの一部をドライヤ出口の排気煙道内へと導くようにしたので、ドライヤ下流の排気煙道内の排ガス温度を高くできて排ガス中の気化したアスファルト分が凝縮しにくくなり、排気煙道へのアスファルト分の付着を抑えて火災の発生を防止できる。   According to the asphalt recycle plant of claim 1 of the present invention, a deodorizing furnace for thermally decomposing odorous components in the exhaust gas is disposed downstream of the exhaust flue of the waste material heating dryer, and a high temperature derived from the deodorizing furnace. Gas is supplied to the dryer via a high-temperature gas supply duct to heat the waste material, while the end of the branch duct formed by branching the high-temperature gas supply duct is connected to an exhaust flue at the dryer outlet, Since a part of the exhaust flue is led into the exhaust flue at the outlet of the dryer, the exhaust gas temperature in the exhaust flue downstream of the dryer can be increased, making it difficult for the vaporized asphalt content in the exhaust gas to condense. Prevents the occurrence of fire by suppressing the adhesion of.

本発明の請求項2記載のアスファルトリサイクルプラントによれば、前記分岐ダクトに開度調整用ダンパーを配設し、ドライヤの出口の排気煙道に配設した排ガス温度検出計にて検出する排ガス温度に基づいて前記開度調整用ダンパーの開度調整制御を行うので、排気煙道内の排ガス温度をコントロールしてアスファルト分の凝縮しにくいガス温度に維持でき、排気煙道へのアスファルト分の付着を抑えて火災の発生を防止できる。   According to the asphalt recycle plant of claim 2 of the present invention, an exhaust gas temperature detected by an exhaust gas temperature detector disposed in the exhaust flue at the outlet of the dryer, wherein an opening adjusting damper is disposed in the branch duct. Because the opening adjustment control of the opening adjustment damper is performed based on the above, the exhaust gas temperature in the exhaust flue can be controlled and maintained at a gas temperature that is difficult to condense asphalt, and the asphalt adheres to the exhaust flue. It can be suppressed and fire can be prevented.

本発明の請求項1記載のアスファルトリサイクルプラントにあっては、廃材加熱用のドライヤの排気煙道下流に排ガス中の臭気成分を加熱分解する脱臭炉を配設すると共に、ドライヤの廃材加熱の熱源として脱臭炉から排出される750℃程度の高温ガスを高温ガス供給ダクトを介してドライヤに供給する。また、前記高温ガス供給ダクトを分岐して形成した分岐ダクトをドライヤ出口の排気煙道に連結する。これによって、ドライヤから排気される200℃程度の排ガスと750℃程度の高温ガスとを合流させて350℃程度の排ガスがドライヤ下流の排気煙道内を流れるようになり、排ガス中の気化したアスファルト分も凝縮しにくくなり、排気煙道へのアスファルト分の付着を抑えて火災の発生を防止できる。   In the asphalt recycle plant according to claim 1 of the present invention, a deodorizing furnace for thermally decomposing odorous components in exhaust gas is disposed downstream of the exhaust flue of the dryer for heating the waste material, and a heat source for heating the waste material of the dryer. The high temperature gas of about 750 ° C. discharged from the deodorizing furnace is supplied to the dryer through the high temperature gas supply duct. A branch duct formed by branching the hot gas supply duct is connected to an exhaust flue at the outlet of the dryer. As a result, the exhaust gas of about 200 ° C. exhausted from the dryer and the high temperature gas of about 750 ° C. are combined so that the exhaust gas of about 350 ° C. flows in the exhaust flue downstream of the dryer, and the vaporized asphalt content in the exhaust gas It becomes difficult to condense, and it can prevent the occurrence of fire by suppressing the attachment of asphalt to the exhaust flue.

本発明の請求項2記載のアスファルトリサイクルプラントにあっては、ドライヤの排気煙道内へと高温ガスを導く分岐ダクトに開度調整用ダンパーを配設すると共に、ドライヤの出口の排気煙道に排ガス温度検出計を配設している。そして、排ガス温度検出計にて検出する排ガス温度をダンパー開度調整器に取り込み、該ダンパー開度調整器にて予め設定した基準値と比較し、その差値量に基づいて前記開度調整用ダンパーの開度調整制御を行う。これによって、排気煙道内の排ガス温度をコントロールして排ガス中の気化したアスファルト分が凝縮しないような温度とし、排気煙道へのアスファルト分の付着を抑えて火災の発生を防止できる。   In the asphalt recycle plant according to claim 2 of the present invention, an opening adjusting damper is disposed in a branch duct for introducing a high temperature gas into the exhaust flue of the dryer, and an exhaust gas is disposed in the exhaust flue at the outlet of the dryer. A temperature detector is provided. Then, the exhaust gas temperature detected by the exhaust gas temperature detector is taken into the damper opening adjuster, compared with a reference value preset by the damper opening adjuster, and based on the difference value, the opening adjustment Perform damper opening adjustment control. As a result, the temperature of the exhaust gas in the exhaust flue is controlled so that the vaporized asphalt content in the exhaust gas does not condense, and the occurrence of a fire can be prevented by suppressing the attachment of the asphalt content to the exhaust flue.

以下、本発明の実施例を図面に基づいて説明する。   Embodiments of the present invention will be described below with reference to the drawings.

図中の1は、廃材を加熱する公知のドライヤであって、内周部に多数の掻き上げ羽根(図示せず)を周設した円筒状のドラム2を機台3上に回転自在に傾斜支持し、駆動装置(図示せず)により所定の速度で回転させるようにしている。そして、後述する脱臭炉4からの高温ガスを高温ガス供給ダクト5を介してドラム2内に送り込むと共に、ドラム2の他端部の排出ホッパ6に連結した排気煙道7の下流に介在させた排風機8によって排ガスを吸引してドラム2内を通過する高温ガス流を維持する一方、図示しない骨材ホッパから払い出した廃材をベルトコンベヤ9を介してドラム2内に供給し、廃材がドラム2内を転動流下する間に所望の温度まで加熱している。   1 in the figure is a known dryer for heating waste materials, and a cylindrical drum 2 having a large number of scraping blades (not shown) around its inner periphery is inclined on a machine base 3 in a freely rotatable manner. It is supported and rotated at a predetermined speed by a driving device (not shown). And the hot gas from the deodorizing furnace 4 mentioned later is sent in in the drum 2 via the hot gas supply duct 5, and was interposed downstream of the exhaust flue 7 connected with the discharge hopper 6 of the other end part of the drum 2. While the exhaust gas is sucked by the exhaust fan 8 and the high temperature gas flow passing through the drum 2 is maintained, the waste material discharged from the aggregate hopper (not shown) is supplied into the drum 2 via the belt conveyor 9. It is heated to the desired temperature while rolling down.

また、前記排気煙道7の下流には排ガス中のダストを捕捉する集塵機10を配設すると共に、集塵機10の下流には排ガス中に含まれるアスファルト分を燃焼分解するための脱臭炉4を配設している。そして、脱臭炉4を通過した排ガスは清浄なガスとなって煙突11から大気中に放出される。   A dust collector 10 that captures dust in the exhaust gas is disposed downstream of the exhaust flue 7, and a deodorization furnace 4 is disposed downstream of the dust collector 10 for burning and decomposing asphalt contained in the exhaust gas. Has been established. The exhaust gas that has passed through the deodorizing furnace 4 becomes a clean gas and is released from the chimney 11 into the atmosphere.

前記脱臭炉4は、一端に炉内温度を所定値に維持するためのバーナ12を備えており、炉内に導入する排ガスを高温雰囲気にさらし、排ガス中に含まれるアスファルト分を燃焼分解している。なお、脱臭炉4はアスファルト分が完全に燃焼分解できるように、炉内温度を例えば、略750℃以上の高温を維持するようにバーナ12の燃焼量をコントロールすると共に、排ガスが炉内を通過するのに少なくとも1乃至2秒以上かかる程度の滞留室4aを備えていることが好ましい。   The deodorizing furnace 4 is provided with a burner 12 for maintaining the furnace temperature at a predetermined value at one end, exposing the exhaust gas introduced into the furnace to a high temperature atmosphere, and burning and decomposing asphalt contained in the exhaust gas. Yes. The deodorizing furnace 4 controls the combustion amount of the burner 12 so that the temperature inside the furnace is maintained at a high temperature of, for example, approximately 750 ° C. or more so that the asphalt can be completely burned and decomposed, and the exhaust gas passes through the furnace. It is preferable to have a staying chamber 4a that takes at least 1 to 2 seconds or more to do so.

脱臭炉4を通過する高温ガスは、ダンパー13の開閉度の制御によって所定量が高温ガス供給ダクト5を介してドライヤ1に供給される。また、高温ガス供給ダクト5を分岐して形成した分岐ダクト14の末端をドライヤ1出口の排気煙道7に連結し、高温ガスの一部を分岐ダクト14を経由してドライヤ1出口の排気煙道7内へと導き、ドライヤ1の排ガスと合流するようにしている。   A predetermined amount of the hot gas passing through the deodorizing furnace 4 is supplied to the dryer 1 through the hot gas supply duct 5 by controlling the degree of opening and closing of the damper 13. Further, the end of the branch duct 14 formed by branching the high temperature gas supply duct 5 is connected to the exhaust flue 7 at the outlet of the dryer 1, and a part of the high temperature gas passes through the branch duct 14 and is exhausted at the outlet of the dryer 1. It is led into the road 7 so as to merge with the exhaust gas of the dryer 1.

前記分岐ダクト14には風量調整用ダンパー15を配設すると共に、ドライヤ1の出口付近の排気煙道7には排ガス温度検出計16を備えている。また、排ガス温度検出計16の検出値を取り込むダンパー開度調整器17を配設し、該ダンパー開度調整器17にて取り込んだ排ガス検出値と予め設定した基準値とを比較し、その差値量に基づいて風量調整用ダンパー15の開度調整制御を行うようにしている   An air volume adjusting damper 15 is disposed in the branch duct 14, and an exhaust gas temperature detector 16 is provided in the exhaust flue 7 near the outlet of the dryer 1. Further, a damper opening adjuster 17 for taking in the detection value of the exhaust gas temperature detector 16 is arranged, and the exhaust gas detection value taken in by the damper opening adjuster 17 is compared with a preset reference value, and the difference therebetween The opening adjustment control of the air volume adjusting damper 15 is performed based on the value amount.

また、18、19は熱交換器であって、脱臭炉4から排出される750℃程度の高温の排ガスが保有する排ガス熱を有効利用するためのものであり、熱交換器18は排気煙道7から脱臭炉4に導入される排ガスを昇温させるものであり、また熱交換器19は燃焼用空気供給ファン20から脱臭炉4のバーナ12へ供給する燃焼用空気の予熱を図るものである。   Reference numerals 18 and 19 denote heat exchangers for effectively using the exhaust gas heat of the exhaust gas having a high temperature of about 750 ° C. discharged from the deodorizing furnace 4, and the heat exchanger 18 is an exhaust flue. 7 raises the temperature of the exhaust gas introduced into the deodorizing furnace 4, and the heat exchanger 19 preheats the combustion air supplied from the combustion air supply fan 20 to the burner 12 of the deodorizing furnace 4. .

しかして、廃材を加熱するときには、先ず、ベルトコンベヤ9を介して廃材をドライヤ1に供給する一方、脱臭炉4から高温ガス供給ダクト5を介して高温ガスをドライヤ1内に供給して廃材を所定温度まで加熱する。このとき、高温ガスの供給量はドラム2から排出される加熱廃材の温度または排ガス温度が予め設定された値となるようにダンパー13の開閉度を調整してコントロールされる。   Thus, when heating the waste material, first, the waste material is supplied to the dryer 1 via the belt conveyor 9, while the high temperature gas is supplied from the deodorizing furnace 4 to the dryer 1 via the high temperature gas supply duct 5. Heat to predetermined temperature. At this time, the supply amount of the high-temperature gas is controlled by adjusting the degree of opening and closing of the damper 13 so that the temperature of the heated waste material discharged from the drum 2 or the exhaust gas temperature becomes a preset value.

また、風量調整用ダンパー15の開度を適宜調整し、脱臭炉4から排出される750℃程度の高温ガスを分岐ダクト14を経由してドライヤ1出口の排気煙道7に導き、ドライヤ1から排出される200℃程度の排ガスと合流させる。このとき、ダンパー開度調整器17を備えたものでは、ガス温度検出計16によって検出する排気煙道7内の排ガス温度をダンパー開度調整器17に取り込み、予め設定した基準値、例えば350℃と比較し、その差値量に基づいて風量調整用ダンパー15の開度制御を行い、ドライヤ1下流の排気煙道7内の温度を350℃程度に維持する。   Further, the opening degree of the air volume adjusting damper 15 is appropriately adjusted, and a high temperature gas of about 750 ° C. discharged from the deodorizing furnace 4 is led to the exhaust flue 7 at the outlet of the dryer 1 through the branch duct 14. Combine with the exhaust gas at about 200 ° C. At this time, in the case where the damper opening adjuster 17 is provided, the exhaust gas temperature in the exhaust flue 7 detected by the gas temperature detector 16 is taken into the damper opening adjuster 17, and a preset reference value, for example, 350 ° C. And the opening degree of the air volume adjusting damper 15 is controlled based on the difference value, and the temperature in the exhaust flue 7 downstream of the dryer 1 is maintained at about 350 ° C.

そして、ドライヤ1から導出される排ガスを集塵機10へと導き、集塵機10にて排ガス中のダスト分を捕捉する一方、集塵機10を通過した排ガスを脱臭炉4へと導いて炉内の750℃程度の高温雰囲気にさらし、排ガス中に残るアスファルト分を完全に燃焼分解する。脱臭炉4から排出される高温排ガスは熱交換器18、19を経て400℃程度まで低下して煙突11より大気中に放出される。   Then, the exhaust gas derived from the dryer 1 is guided to the dust collector 10, and the dust content in the exhaust gas is captured by the dust collector 10, while the exhaust gas that has passed through the dust collector 10 is guided to the deodorizing furnace 4 and about 750 ° C. in the furnace. The asphalt remaining in the exhaust gas is completely burned and decomposed by exposure to a high temperature atmosphere. The high-temperature exhaust gas discharged from the deodorizing furnace 4 is lowered to about 400 ° C. through the heat exchangers 18 and 19 and discharged from the chimney 11 to the atmosphere.

このように、脱臭炉4から排出される高温ガスを分岐ダクト14を介してドライヤ1下流の排気煙道7内に供給することによって、排気煙道7内の排ガス温度を350℃程度の高温とすることができ、排ガス中の気化したアスファルト分が凝縮しにくくなり、排気煙道7内へのアスファルト分の付着を抑えて火災の発生を防止できる。   In this way, by supplying the high-temperature gas discharged from the deodorizing furnace 4 into the exhaust flue 7 downstream of the dryer 1 through the branch duct 14, the exhaust gas temperature in the exhaust flue 7 is set to a high temperature of about 350 ° C. As a result, the vaporized asphalt content in the exhaust gas becomes difficult to condense, and the asphalt content in the exhaust flue 7 can be suppressed to prevent the occurrence of a fire.

本発明に係るアスファルトリサイクルプラントの一実施例を示す概略説明図である。It is a schematic explanatory drawing which shows one Example of the asphalt recycle plant which concerns on this invention.

符号の説明Explanation of symbols

1…ドライヤ 4…脱臭炉
5…高温ガス供給ダクト 7…排気煙道
8…排風機 10…集塵機
12…バーナ 14…分岐ダクト
15…風量調整用ダンパー 16…排ガス温度検出計
17…ダンパー開度調整器 18、19…熱交換器
DESCRIPTION OF SYMBOLS 1 ... Dryer 4 ... Deodorizing furnace 5 ... High temperature gas supply duct 7 ... Exhaust flue 8 ... Exhaust fan 10 ... Dust collector 12 ... Burner 14 ... Branch duct 15 ... Damper for air volume adjustment 16 ... Exhaust gas temperature detector 17 ... Damper opening adjustment 18, 19 ... heat exchanger

Claims (2)

廃材加熱用のドライヤの排気煙道下流に排ガス中の臭気成分を加熱分解する脱臭炉を配設し、該脱臭炉から導出される高温ガスを高温ガス供給ダクトを介して前記ドライヤに供給して廃材を加熱する一方、前記高温ガス供給ダクトを分岐して形成した分岐ダクトの末端をドライヤ出口の排気煙道に連結し、高温排ガスの一部をドライヤ出口の排気煙道内へと導くようにしたことを特徴とするアスファルトリサイクルプラント。   A deodorizing furnace for thermally decomposing odor components in the exhaust gas is disposed downstream of the exhaust flue of the dryer for heating the waste material, and the high-temperature gas derived from the deodorizing furnace is supplied to the dryer via the high-temperature gas supply duct. While the waste material is heated, the end of the branch duct formed by branching the high temperature gas supply duct is connected to the exhaust flue at the outlet of the dryer so that a part of the high temperature exhaust gas is led into the exhaust flue at the outlet of the dryer. An asphalt recycle plant characterized by that. 前記分岐ダクトに開度調整用ダンパーを配設し、ドライヤの出口の排気煙道に配設した排ガス温度検出計にて検出する排ガス温度に基づいて前記開度調整用ダンパーの開度調整制御を行うことを特徴とする請求項1記載のアスファルトリサイクルプラント。   An opening adjustment damper is disposed in the branch duct, and the opening adjustment control of the opening adjustment damper is performed based on the exhaust gas temperature detected by the exhaust gas temperature detector disposed in the exhaust flue at the outlet of the dryer. The asphalt recycle plant according to claim 1, which is performed.
JP2005068736A 2005-03-11 2005-03-11 Asphalt recycle plant Active JP4677255B2 (en)

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Cited By (1)

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KR102642895B1 (en) * 2022-12-21 2024-03-04 케이씨브이씨에스 주식회사 The ascon manufacturing equipment

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Publication number Priority date Publication date Assignee Title
KR102632275B1 (en) * 2021-10-29 2024-02-01 케이씨브이씨에스 주식회사 The ascon manufacturing equipment

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JPH07166510A (en) * 1993-12-15 1995-06-27 Nikko Co Ltd Recycling plant for asphalt pavement waste
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KR102642895B1 (en) * 2022-12-21 2024-03-04 케이씨브이씨에스 주식회사 The ascon manufacturing equipment

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