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JPH0115644B2 - - Google Patents
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JPH0115644B2 - - Google Patents

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Publication number
JPH0115644B2
JPH0115644B2 JP16973781A JP16973781A JPH0115644B2 JP H0115644 B2 JPH0115644 B2 JP H0115644B2 JP 16973781 A JP16973781 A JP 16973781A JP 16973781 A JP16973781 A JP 16973781A JP H0115644 B2 JPH0115644 B2 JP H0115644B2
Authority
JP
Japan
Prior art keywords
waste material
dryer
particle size
asphalt waste
recycling
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
Application number
JP16973781A
Other languages
Japanese (ja)
Other versions
JPS5869906A (en
Inventor
Terutaka Onoe
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Osaka Gas Co Ltd
Original Assignee
Osaka Gas Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Osaka Gas Co Ltd filed Critical Osaka Gas Co Ltd
Priority to JP16973781A priority Critical patent/JPS5869906A/en
Publication of JPS5869906A publication Critical patent/JPS5869906A/en
Publication of JPH0115644B2 publication Critical patent/JPH0115644B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】 本発明は、アスフアルト道路面の修復工事や道
路下埋設の導管工事等に伴なつて発生するアスフ
アルト廃材を加熱合材として再生する技術で、詳
しくは、道路工事等によつて発生するアスフアル
ト廃材を破砕機に通して粒度調整したのち、その
粒度調整済みのアスフアルト廃材をドライヤーに
投入して再生所要温度まで加熱するアスフアルト
廃材の再生方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention is a technology for recycling asphalt waste material generated during asphalt road surface repair work, conduit work buried under roads, etc. as a heating mixture. This invention relates to a method for recycling asphalt waste material, in which the asphalt waste material thus generated is passed through a crusher to adjust its particle size, and then the asphalt waste material whose particle size has been adjusted is put into a dryer and heated to the required temperature for recycling.

上記の再生方法において従来一般には、前記破
砕機で破砕され、粒度調整済みのアスフアルト廃
材の全てを粒度選別等することなく、ドライヤー
内に投入して加熱していたが、これによる場合
は、廃材中の小粒度のもの(0〜5mm粒径範囲の
細粒子)が急激に温度上昇して軟化し、ドライヤ
ー内壁面に付着し、その結果、加熱効率が経時的
に低下するのみならず、付着粒子の除去などドラ
イヤーの整備に手間取る不都合があり、加えて、
全廃材が再生所要温度に達するべく加熱すると、
前記の細粒分が燃えたり、或いは、劣化温度以上
に過加熱され、もつて、排ガス中に多くの不純物
が含まれて公害問題を提起したり、再生合材の品
質低下を招くといつた欠点があつた。
Conventionally, in the above-mentioned recycling method, all of the asphalt waste that has been crushed by the crusher and whose particle size has been adjusted is placed in a dryer and heated without particle size sorting. Small particles in the middle (fine particles in the particle size range of 0 to 5 mm) soften due to a sudden rise in temperature and adhere to the inner wall surface of the dryer. As a result, not only does the heating efficiency decrease over time, but also the adhesion There is an inconvenience in that it takes time to maintain the dryer such as removing particles, and in addition,
When all waste materials are heated to reach the required temperature for recycling,
If the fine particles are burned or overheated above the deterioration temperature, many impurities will be included in the exhaust gas, causing pollution problems and deteriorating the quality of the recycled composite material. There were flaws.

また、上記のような不都合、欠点を除去又は抑
制する手段として、従来 ○イ ドライヤーの中途箇所から小粒度のものを投
入する方法、 ○ロ 小粒度のものに事前散水してドライヤー内で
の昇温速度を抑える方法、 等が知られているが、これらの方法による時は、
全廃材量に対する細粒分量の比の変動に応じてド
ライヤー中途箇所への投入量や散水量を厳密に調
整する要がある。若し、その投入量が散水量の調
整が行なわれない場合や調整が不良であると、前
述したような不都合、欠点を除去又は抑制できな
いばかりか、却つて、熱効率のロスや品質低下を
助長する結果になりかねないのである。従つて、
上記の対策方法をもつて実効を挙げるには、投入
量や散水量の高精度自動調整のための設備、及
び、その運転費を要し、これが再生コストの著し
い増加要因になる難点があつた。
In addition, as a means to eliminate or suppress the above-mentioned inconveniences and drawbacks, there are conventional methods such as ○I, which introduces small particles from the middle of the dryer, and ○B, which involves pre-spraying small particles with water and allowing them to rise in the dryer. Methods of suppressing the temperature rate are known, but when these methods are used,
It is necessary to strictly adjust the amount of water added to the midway point of the dryer and the amount of water sprinkled depending on the fluctuation of the ratio of the amount of fine particles to the amount of total waste material. If the water input amount is not adjusted or is improperly adjusted, not only will the above-mentioned inconveniences and drawbacks not be eliminated or suppressed, but it will even promote loss of thermal efficiency and deterioration of quality. This could result in Therefore,
In order for the above countermeasures to be effective, equipment for high-precision automatic adjustment of the input amount and watering amount, as well as operating costs, are required, which has the disadvantage of causing a significant increase in regeneration costs. .

本発明は、かかる実情に鑑み、設備的に比較的
簡単でコスト面でも有利に実現可能な工程追加を
もつて、加熱効率の向上を図るとともに、品質の
良い合材を再生できる方法を提案する点に目的を
有する。
In view of these circumstances, the present invention proposes a method that improves heating efficiency and regenerates high-quality composite material by adding a process that is relatively simple in terms of equipment and can be realized advantageously in terms of cost. Have a purpose in mind.

上記目的を指向して提案した本発明によるアス
フアルト廃材の再生方法は、冒頭詳記の方法にお
いて、前記ドライヤーに投入する前の粒度調整済
みアスフアルト廃材を造粒機に通して、その廃材
中の小粒度のものを団粒化することを特徴とす
る。
The method for recycling asphalt waste according to the present invention proposed with the above object in mind is that in the method detailed at the beginning, the asphalt waste whose particle size has been adjusted before being put into the dryer is passed through a granulator, and the small particles in the waste are passed through a granulator. It is characterized by agglomerating particles of a certain size.

即ち、破砕によつて粒度調整されたアスフアル
ト廃材中の小粒度のものを、造粒手段といつた設
備的に比較的簡単でかつ経済的な手段をもつて団
粒化して見掛けの粒度を大きくすることにより、
全ての廃材を同時にかつ同一箇所からドライヤー
に投入しながら、細粒分のドライヤー内壁面への
付着、及び、それに伴なう加熱効率の低下、ドラ
イヤー整備の煩わしさといつた不都合を極力回避
することができるばかりでなく、ドライヤー内の
加熱対象全廃材の粒度がほぼ揃えられているた
め、一部のものが燃えたり、劣化温度以上に過加
熱される憂いがなく、排ガス中の不純物含有量の
減少に伴なう公害対策の容易化、及び再生合材の
品質向上、並びに、合材再生率の増大化の諸効果
を、破砕に伴なう細粒分量の変動に拘わらず、確
実に達成できるに至つた。
That is, the small particles in asphalt waste whose particle size has been adjusted by crushing are aggregated using relatively simple and economical equipment such as granulation means to increase the apparent particle size. By doing so,
To avoid as much as possible the inconvenience of fine particles adhering to the inner wall surface of the dryer, the resulting reduction in heating efficiency, and the troublesome maintenance of the dryer, while all waste materials are fed into the dryer at the same time and from the same location. Not only is it possible to reduce the amount of impurities in the exhaust gas, but because the particle size of all the waste materials to be heated in the dryer is almost the same, there is no risk of some materials burning or being overheated above the deterioration temperature, and the impurity content in the exhaust gas can be reduced. Reliably achieves the effects of facilitating pollution countermeasures due to reduction in pollution, improving the quality of recycled composite material, and increasing the composite material recycling rate, regardless of fluctuations in the fine particle content due to crushing. I was able to do it.

以下本発明の実施の態様を例示図に基づいて工
程順に詳述する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, embodiments of the present invention will be described in detail in order of steps based on illustrative drawings.

第1工程 道路工事等によつて発生するアスフアルト廃材
Aをホツパー1aを介して破砕機1に供給し粗砕
したのち、フルイ3にかけてフルイ上廃材A1
互いに粒度の異なる二種のフルイ中間廃材A2
A3、及び、フルイ下廃材A4の四種類のものに分
級する。尚、分級されたフルイ上廃材A1は前記
とは別の破砕機1にかけて破砕したのち前記フル
イ3にフイードバツクすることにより、合材再生
率の増大を図つている。
First step Asphalt waste material A generated from road construction etc. is supplied to the crusher 1 through the hopper 1a and coarsely crushed, and then passed through the sieve 3 to produce waste material A 1 on the sieve.
Two types of sieve intermediate waste material A 2 with different particle sizes,
It is classified into four types: A 3 and sieve waste material A 4 . The classified waste material A1 on the sieve is crushed by a crusher 1 different from the one described above, and then fed back to the sieve 3, thereby increasing the composite material regeneration rate.

第2工程 第1工程において分級された廃材のうち、最も
粒度が小さいフルイ下廃材A4を造粒機4に通し
て団粒化することにより、見掛け粒度を大きく
し、その見掛け粒度を大きくした廃材A′4及び二
種のフルイ中間廃材A2,A3を各別にホツパー5
に収容する。
2nd process Out of the waste materials classified in the 1st process, the waste material under the sieve A 4 , which has the smallest particle size, was passed through the granulator 4 to aggregate it, thereby increasing the apparent particle size. Waste material A′ 4 and two types of sieve intermediate waste materials A 2 and A 3 are each placed in the hopper 5.
to be accommodated.

第3工程 前記ホツパー5内に収容された各廃材A′4
A2,A3を適当な配合割合(規定の骨材の真粒度
範囲に入るように調合)で、ドラムドライヤー2
に投入し、そのドライヤー2軸線方向に沿つて高
温燃焼ガスを併流する状態で螺旋状に移送するこ
とにより、再生所要温度にまで加熱する。このと
き、燃焼排ガスは集塵機6を通し、その排ガス中
に含まれている固形分を除去して大気に放出され
る。
Third step Each waste material A′ 4 accommodated in the hopper 5,
Mix A 2 and A 3 in an appropriate ratio (mixed so that it falls within the specified aggregate true particle size range), and then dry it in a drum dryer 2.
The dryer is heated to the required regeneration temperature by spirally transferring the high-temperature combustion gas along the two axial directions of the dryer. At this time, the combustion exhaust gas passes through the dust collector 6 to remove solids contained in the exhaust gas, and is released into the atmosphere.

第4工程 加熱された廃材をミキサー7に供給するととも
に、その加熱廃材に所定量のストレートアスフア
ルトA5及び適量の軟化剤Bを加え、適当時間に
亘つて混合することにより、再生合材とする。こ
の再生合材は例えば保温されたサイロ8内に貯蔵
され、必要に応じて搬出される。
Fourth step: The heated waste material is supplied to the mixer 7, and a predetermined amount of straight asphalt A 5 and an appropriate amount of softener B are added to the heated waste material and mixed for an appropriate period of time to produce a recycled composite material. . This recycled composite material is stored, for example, in a heat-insulated silo 8, and is carried out as needed.

尚、本発明方法において、前記フルイ3による
分級は必ずしも必要ではなく、破砕された全ての
廃材を造粒機4にかけて全廃材をほぼ均等で見掛
け粒度を大きくしても良い。
Incidentally, in the method of the present invention, classification using the sieve 3 is not necessarily necessary, and all the crushed waste materials may be passed through a granulator 4 so that all the waste materials are approximately uniform and the apparent particle size is increased.

【図面の簡単な説明】[Brief explanation of drawings]

図面は本発明に係るアスフアルト廃材の再生方
法の実施の態様を例示するフローシートである。 1…破砕機、2…ドライヤー、3…フルイ、4
…造粒機。
The drawing is a flow sheet illustrating an embodiment of the method for recycling asphalt waste according to the present invention. 1...Crusher, 2...Dryer, 3...Sieve, 4
...granulator.

Claims (1)

【特許請求の範囲】 1 道路工事等によつて発生するアスフアルト廃
材を破砕機1に通して粒度調整したのち、その粒
度調整済みのアスフアルト廃材をドライヤー2に
投入して再生所要温度まで加熱するアスフアルト
廃材の再生方法において、前記ドライヤー2に投
入する前の粒度調整済みアスフアルト廃材を造粒
機4に通して、その廃材中の小粒度のものを団粒
化することを特徴とするアスフアルト廃材の再生
方法。 2 前記破砕機1により破砕されたアスフアルト
廃材は、フルイ3を介して複数種類のものに分級
され、そのうち、小粒度のもののみが前記造粒機
4に通されるものである特許請求の範囲第1項に
記載のアスフアルト廃材の再生方法。
[Scope of Claims] 1. Asphalt waste material generated from road construction, etc. is passed through a crusher 1 to adjust its particle size, and then the asphalt waste material whose particle size has been adjusted is put into a dryer 2 and heated to the required temperature for recycling. The asphalt waste recycling method is characterized in that the asphalt waste material whose particle size has been adjusted before being input into the dryer 2 is passed through a granulator 4 to aggregate small particles in the waste material. Method. 2. The asphalt waste crushed by the crusher 1 is classified into a plurality of types through a sieve 3, of which only small particles are passed through the granulator 4. The method for recycling asphalt waste material according to item 1.
JP16973781A 1981-10-22 1981-10-22 Regeneration of asphalt waste material Granted JPS5869906A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16973781A JPS5869906A (en) 1981-10-22 1981-10-22 Regeneration of asphalt waste material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16973781A JPS5869906A (en) 1981-10-22 1981-10-22 Regeneration of asphalt waste material

Publications (2)

Publication Number Publication Date
JPS5869906A JPS5869906A (en) 1983-04-26
JPH0115644B2 true JPH0115644B2 (en) 1989-03-20

Family

ID=15891906

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16973781A Granted JPS5869906A (en) 1981-10-22 1981-10-22 Regeneration of asphalt waste material

Country Status (1)

Country Link
JP (1) JPS5869906A (en)

Also Published As

Publication number Publication date
JPS5869906A (en) 1983-04-26

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