JPH0363303A - Device for recycling scrapped asphalt pavement material - Google Patents
Device for recycling scrapped asphalt pavement materialInfo
- Publication number
- JPH0363303A JPH0363303A JP19993089A JP19993089A JPH0363303A JP H0363303 A JPH0363303 A JP H0363303A JP 19993089 A JP19993089 A JP 19993089A JP 19993089 A JP19993089 A JP 19993089A JP H0363303 A JPH0363303 A JP H0363303A
- Authority
- JP
- Japan
- Prior art keywords
- drum
- exhaust gas
- combustion chamber
- flue
- asphalt pavement
- 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.)
- Granted
Links
- 239000010426 asphalt Substances 0.000 title claims abstract description 20
- 238000004064 recycling Methods 0.000 title claims description 10
- 239000000463 material Substances 0.000 title abstract 2
- 238000002485 combustion reaction Methods 0.000 claims abstract description 24
- 239000002699 waste material Substances 0.000 claims description 23
- 239000000428 dust Substances 0.000 abstract description 7
- 238000010438 heat treatment Methods 0.000 abstract description 7
- 230000009965 odorless effect Effects 0.000 abstract description 6
- 230000007613 environmental effect Effects 0.000 abstract description 2
- 239000004615 ingredient Substances 0.000 abstract 2
- 238000003912 environmental pollution Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 abstract 1
- 238000004321 preservation Methods 0.000 abstract 1
- 238000003303 reheating Methods 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 34
- 239000000779 smoke Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 230000001172 regenerating effect Effects 0.000 description 2
- 239000002918 waste heat Substances 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 230000001877 deodorizing effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000007790 scraping Methods 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
Landscapes
- Road Paving Machines (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は既設アスファルト舗装の打ち換え、補修、更に
は既設アスファルト舗装下に埋設される設備の工事に伴
って発生するアスファルト舗装廃材の再生装置に関する
ものである。[Detailed Description of the Invention] [Field of Industrial Application] The present invention relates to an apparatus for recycling asphalt pavement waste generated during replacement and repair of existing asphalt pavement, and furthermore, construction of equipment buried under the existing asphalt pavement. It is related to.
[従来の技術]
道路工事等によって掘り起こしたアスファルト舗装廃材
(以下「廃材」という)は加熱装置であるドライヤによ
って加熱再生され、有効利丹されるようになってきた。[Prior Art] Asphalt pavement waste material (hereinafter referred to as "waste material") dug up during road construction, etc. has come to be heated and regenerated using a dryer, which is a heating device, and to be effectively recycled.
[発明が解決しようとする課題]
しかしながら、アスファルト分を含む廃材を加熱する際
に悪臭が発生し、この悪臭が近隣に放散される可能性が
あり、このため環境保全面から悪臭対策が必要となって
きている。[Problem to be solved by the invention] However, when waste materials containing asphalt are heated, a bad odor is generated, and this bad odor may be radiated into the neighborhood. Therefore, from the perspective of environmental conservation, countermeasures against the bad odor are necessary. It has become to.
そこで本発明は上記の点に鑑み、大型の脱臭装置を使用
せずに低コストで脱臭することができるアスファルト舗
装廃材再生装置を提案することを目的とするものである
。Therefore, in view of the above points, the present invention aims to propose an asphalt pavement waste recycling device that can deodorize at low cost without using a large-sized deodorizing device.
[課題を解決するための手段]
本考案は上記目的を達成するために、アスファルト舗装
廃材を加熱再生するドラムの一端部のホットホッパ側に
燃焼室を備えたバーナを配設する一方、ドラム他端部の
コールドホッパに連結した循環煙道の途中に排風機を介
在させるとともに循環煙道端部を前記燃焼室に連結し、
前記ホットホッパにはドラム内のガスの一部を外部に放
出する放出煙道を配設したことを特徴とするアスファル
ト舗装廃材再生装置を提供するものである。[Means for Solving the Problems] In order to achieve the above object, the present invention provides a burner equipped with a combustion chamber on the hot hopper side of one end of the drum for heating and regenerating asphalt pavement waste, while An exhaust fan is interposed in the middle of the circulation flue connected to the cold hopper at the end, and the end of the circulation flue is connected to the combustion chamber,
The present invention provides an apparatus for recycling asphalt pavement waste material, characterized in that the hot hopper is provided with a discharge flue for discharging part of the gas in the drum to the outside.
[作 用]
本発明に係るアスファルト舗装廃材再生装置にあっては
、ドラムのコールドホッパ側から導出する排ガスの全量
をホットホッパ側に配設した燃焼室に戻し、該燃焼室で
排ガスを燃焼させて炭酸ガスと水蒸気に分解して無臭処
理する。モーして、燃焼室で再加熱した高温の排ガスを
再びドラム内に送り込んでドラム内の廃材を加熱するの
である。[Function] In the asphalt pavement waste recycling device according to the present invention, the entire amount of exhaust gas led out from the cold hopper side of the drum is returned to the combustion chamber disposed on the hot hopper side, and the exhaust gas is combusted in the combustion chamber. It decomposes into carbon dioxide gas and water vapor, making it odorless. The high-temperature exhaust gas reheated in the combustion chamber is sent into the drum again to heat the waste material inside the drum.
この時ドラム内の全ガス量の内、バーナから取り込む燃
焼用空気やドラム隙間より侵入する空気及び加熱廃材か
ら発生する水蒸気により漸次増加していくガス量はホッ
トホッパに配設した放出煙道から放出されていく。At this time, out of the total amount of gas in the drum, the amount of gas that gradually increases due to the combustion air taken in from the burner, the air that enters through the drum gap, and the steam generated from the heated waste materials is released from the exhaust flue installed in the hot hopper. It is being released.
[実施例] 以下本発明の実施例を図面に基いて説明する。[Example] Embodiments of the present invention will be described below based on the drawings.
lは廃材を加熱再生するドライヤであって、内部に多数
の掻き上げ羽根2を周設した円筒状のドラム3を機台4
上に回転自在に傾斜枢支し、駆動装置(図示せず)によ
り所定の速度で回転させている。5はドラム3の一端部
に配設したホットホッパであって、該ホットホッパ5側
にはバーナ6が配設してあり、バーナ6の前方には火炎
を形成する燃焼室7を備えている。8はドラム3の他端
部に配設したコールドホッパであって、該コールドホッ
パ8にはドラム3の排ガスを導出させる循環煙道9を連
結してあり、該循環煙道9の途中にはドラム3から導出
する排ガスを吸引排気する排風機lOと排ガス中の飛散
粉塵を捕集する集□塵機1)とを配設しである。前記循
環煙道9の他端部は燃焼室7に連結されており、ドラム
3より導出された排ガスは燃焼室7へと導かれれる。1
2は排風機lOの吸い込み側の循環煙道9に配設した風
量調整用ダンパであって、該風量調整用ダンパ12は燃
焼室7の適宜位置に挿入した温度センサ13によって検
出する燃焼室7内の温度に応答して動作させ、燃焼室7
内の温度が約800℃程度となるように排ガスの吸引量
を制御するものである。1 is a dryer for heating and regenerating waste materials, and a cylindrical drum 3 with a large number of scraping blades 2 arranged around it is mounted on a machine base 4.
It is rotatably tilted upwardly and rotated at a predetermined speed by a drive device (not shown). 5 is a hot hopper disposed at one end of the drum 3, a burner 6 is disposed on the side of the hot hopper 5, and a combustion chamber 7 for forming a flame is provided in front of the burner 6. . Reference numeral 8 denotes a cold hopper disposed at the other end of the drum 3. A circulation flue 9 is connected to the cold hopper 8 for discharging the exhaust gas from the drum 3. An exhaust fan 10 that sucks and exhausts the exhaust gas led out from the drum 3 and a dust collector 1) that collects scattered dust in the exhaust gas are provided. The other end of the circulation flue 9 is connected to the combustion chamber 7, and the exhaust gas discharged from the drum 3 is guided to the combustion chamber 7. 1
Reference numeral 2 denotes an air volume adjustment damper disposed in the circulation flue 9 on the suction side of the exhaust fan 1O, and the air volume adjustment damper 12 has a temperature sensor 13 inserted into the combustion chamber 7 at an appropriate position to detect the temperature of the combustion chamber 7. The combustion chamber 7 is operated in response to the temperature within the combustion chamber 7.
The amount of suction of exhaust gas is controlled so that the temperature inside is approximately 800°C.
14はホットホッパ5に連結した放出煙道であって、該
放出煙道14はバーナ6によって取り込む燃焼用空気や
ドライヤ1の各シール部より侵入する空気及びドラム3
内で加熱廃材から発生する水蒸気によって漸次増加して
いく余剰ガスをドラム3外に放出するものであり、ドラ
ム内のプラス圧による自然通風によって余剰ガスは外部
に放出される。なお放出煙道に排風機を設けて強制排気
するようにしても良い。14 is a discharge flue connected to the hot hopper 5, and the discharge flue 14 collects combustion air taken in by the burner 6, air entering from each seal part of the dryer 1, and the drum 3.
Excess gas that gradually increases due to water vapor generated from heated waste materials inside the drum is released to the outside of the drum 3, and the excess gas is released to the outside by natural ventilation due to positive pressure inside the drum. Note that an exhaust fan may be provided in the discharge flue to forcefully exhaust the air.
前記放出煙道14から放出されるガスは高温であり、こ
の高温ガスを有効に利用するために放出煙道14と循環
煙道9との間に熱交換器15を配設し、放出煙道14側
の高温ガスによって循環煙道9側のガスの温度を上昇さ
せてから燃焼室7に送り込むようにし、熱の回収を図っ
ている。The gas discharged from the discharge flue 14 has a high temperature, and in order to effectively utilize this high temperature gas, a heat exchanger 15 is disposed between the discharge flue 14 and the circulation flue 9. The temperature of the gas on the circulation flue 9 side is raised by the high temperature gas on the 14 side, and then the gas is sent into the combustion chamber 7 to recover heat.
しかして、ドライヤ1により廃材を加熱再生する場合に
は、ベルトコンベヤ16によってドラム3内に廃材を供
給し、廃材がドラム3内を転勤流下する間に廃材を所望
の温度まで加熱する。この時、ドラム3内で発生した臭
気やブルースモーク及び粉塵を伴う排ガスは排風機10
によって吸引排気され、循環煙道9途中に設けた集塵機
1)によって粉塵が除去され、燃焼室7に還元される。When the waste material is heated and regenerated by the dryer 1, the waste material is supplied into the drum 3 by the belt conveyor 16, and the waste material is heated to a desired temperature while flowing down the drum 3. At this time, the exhaust gas accompanied by odor, blue smoke, and dust generated in the drum 3 is removed by the exhaust fan 10.
is suctioned and exhausted, dust is removed by a dust collector 1) provided in the middle of the circulation flue 9, and returned to the combustion chamber 7.
燃焼室7に還元された排ガスはバーナ6の火炎によって
高温度に加熱され、排ガス中の臭気成分やブルースモー
クは加熱分解されて無臭となるのである。脱臭された高
温の排ガスは再度ドラム3内に送り込まれて廃材の加熱
に再利用される。排ガス循環によってバーナ6の燃焼に
必要な空気量とドラム3の各シール部より侵入する空気
量及び廃材の加熱に伴って発生する水蒸気量に見合った
ガス量が余剰ガスとなって漸次増加していくが、これら
の余剰ガスはネットホッパ5のプラス圧によって放出煙
道14から外部に放出される。このように排ガスの全量
を循環させているためにバーナの燃焼に際しては必要最
小限の空気量で燃焼させることが好ましい。The exhaust gas returned to the combustion chamber 7 is heated to a high temperature by the flame of the burner 6, and the odor components and blue smoke in the exhaust gas are thermally decomposed and become odorless. The deodorized high-temperature exhaust gas is sent into the drum 3 again and reused to heat the waste material. Through exhaust gas circulation, the amount of gas corresponding to the amount of air required for combustion in the burner 6, the amount of air entering from each seal part of the drum 3, and the amount of water vapor generated as the waste material is heated becomes surplus gas and gradually increases. However, these surplus gases are discharged to the outside from the discharge flue 14 by the positive pressure of the net hopper 5. Since the entire amount of exhaust gas is circulated in this way, it is preferable to use the minimum amount of air necessary for combustion in the burner.
なお、放出煙道14から放出する高温ガスを有効利用す
るために熱交換器15を配設し循環煙道9中の排ガスを
加熱して熱を回収するようにしたが、放出煙道14から
放出する高温ガスを熱交換器15に通さずに併設した公
知のアスファルトプラントの新規骨材加熱用ドライヤの
ホットホッパ側に送り込むようにしても良い。この場合
には約800℃程度の熱風を新規骨材加熱用ドライヤに
送り込むこととなり、新規骨材の加熱に有効に利用でき
る。Note that in order to effectively utilize the high-temperature gas discharged from the discharge flue 14, a heat exchanger 15 is provided to heat the exhaust gas in the circulation flue 9 and recover heat. The high-temperature gas to be released may not be passed through the heat exchanger 15, but may be sent to the hot hopper side of a dryer for heating new aggregates in a known asphalt plant. In this case, hot air of about 800° C. will be sent to the new aggregate heating dryer, and can be effectively used for heating the new aggregate.
[発明の効果]
以上のように本発明に係るアスファルト廃材再生装置に
よれば、ドラム3から導出する排ガス全量を燃焼室7に
還元して再加熱し、排ガス中に含まれる臭気成分やブル
ースモークを加熱分解して無臭とすることができ、嫌臭
気で周囲環境を害するのを完全に防止できるのである。[Effects of the Invention] As described above, according to the asphalt waste recycling apparatus according to the present invention, the entire amount of exhaust gas derived from the drum 3 is returned to the combustion chamber 7 and reheated, and odor components and blue smoke contained in the exhaust gas are removed. It can be thermally decomposed to make it odorless, completely preventing it from harming the surrounding environment with its unpleasant odor.
また放出煙道14から導出される高温ガスを熱交換器1
5を介して回収したり、公知のアスファルトプラントの
ドライヤのホットホッパ側に供給して新規骨材を加熱す
るようにすれば排熱を有効に利用することができて経済
的である。In addition, the high temperature gas led out from the discharge flue 14 is transferred to the heat exchanger 1
If the waste heat is recovered through a dryer (5) or supplied to the hot hopper side of a dryer in a known asphalt plant to heat new aggregate, the waste heat can be effectively used and it is economical.
第1図は本発明に係るアスファルト舗装廃材再生装置の
一実施例の一部縦断した概略説明用図である。FIG. 1 is a partially longitudinally sectional schematic explanatory diagram of an embodiment of the asphalt pavement waste recycling apparatus according to the present invention.
Claims (3)
端部のホットホッパ側に燃焼室を備えたバーナを配設す
る一方、ドラム他端部のコールドホッパ側に連結した循
環煙道の途中に排風機を介在させるとともに循環煙道端
部を前記燃焼室に連結し、前記ホットホッパにはドラム
内のガスの一部を外部に放出する放出煙道を配設したこ
とを特徴とするアスファルト舗装廃材再生装置。(1) A burner with a combustion chamber is installed on the hot hopper side at one end of the drum that heats and regenerates asphalt pavement waste, while an exhaust fan is installed in the middle of the circulation flue connected to the cold hopper side at the other end of the drum. an asphalt pavement waste recycling device, characterized in that the end of the circulation flue is connected to the combustion chamber, and the hot hopper is provided with a discharge flue for releasing a part of the gas in the drum to the outside. .
部に放出煙道の高温ガスによって循環煙道内の排ガスを
加熱する熱交換器を配設したことを特徴とする請求項1
記載のアスファルト舗装廃材再生装置。(2) The circulation flue and the discharge flue intersect, and a heat exchanger is disposed at the crossing point to heat the exhaust gas in the circulation flue with the high temperature gas of the discharge flue.
The asphalt pavement waste recycling device described.
ーナ側に連結したことを特徴とする請求項1記載のアス
ファルト舗装廃材再生装置。(3) The asphalt pavement waste recycling apparatus according to claim 1, wherein the discharge flue is connected to a burner side of a dryer that heats the new aggregate.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1199930A JPH07107249B2 (en) | 1989-07-31 | 1989-07-31 | Asphalt pavement waste material recycling device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1199930A JPH07107249B2 (en) | 1989-07-31 | 1989-07-31 | Asphalt pavement waste material recycling device |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0363303A true JPH0363303A (en) | 1991-03-19 |
JPH07107249B2 JPH07107249B2 (en) | 1995-11-15 |
Family
ID=16415962
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1199930A Expired - Lifetime JPH07107249B2 (en) | 1989-07-31 | 1989-07-31 | Asphalt pavement waste material recycling device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH07107249B2 (en) |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1993010952A1 (en) * | 1991-11-27 | 1993-06-10 | Cyclean, Inc. | Method and apparatus for producing hot mix asphalt |
US5303999A (en) * | 1989-07-31 | 1994-04-19 | Cyclean, Inc. | Apparatus for control of recycled asphalt production |
US5322367A (en) * | 1989-07-31 | 1994-06-21 | Cyclean, Inc. | Process control for recycled asphalt pavement drum plant |
JPH06207403A (en) * | 1991-10-03 | 1994-07-26 | Niigata Eng Co Ltd | Deodorization type recycle plant for asphalt pavement waste |
US5344229A (en) * | 1989-07-31 | 1994-09-06 | Cyclean, Inc. | Angle and velocity adjustment of a hot mix asphalt drum when output gas temperatures are uneven |
US5556197A (en) * | 1994-11-04 | 1996-09-17 | Gentec Equipment Company | Asphalt plant for both continuous and batch operation |
US5579587A (en) * | 1995-12-15 | 1996-12-03 | Jat Enterprises Inc. Of Indiana | Recycle moisture evaporation system |
CN117166319A (en) * | 2023-11-03 | 2023-12-05 | 知行良知实业股份有限公司 | Production device and process of large-proportion hot-recycled asphalt mixture |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS56139301A (en) * | 1980-03-31 | 1981-10-30 | Tokyo Koki Kk | Method and apparatus for heat treating asphalt and aggregate or asphalt pavement waste material or asphalt pavement waste material and aggregate |
JPS61159407U (en) * | 1985-03-26 | 1986-10-02 |
-
1989
- 1989-07-31 JP JP1199930A patent/JPH07107249B2/en not_active Expired - Lifetime
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS56139301A (en) * | 1980-03-31 | 1981-10-30 | Tokyo Koki Kk | Method and apparatus for heat treating asphalt and aggregate or asphalt pavement waste material or asphalt pavement waste material and aggregate |
JPS61159407U (en) * | 1985-03-26 | 1986-10-02 |
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5303999A (en) * | 1989-07-31 | 1994-04-19 | Cyclean, Inc. | Apparatus for control of recycled asphalt production |
US5322367A (en) * | 1989-07-31 | 1994-06-21 | Cyclean, Inc. | Process control for recycled asphalt pavement drum plant |
US5344229A (en) * | 1989-07-31 | 1994-09-06 | Cyclean, Inc. | Angle and velocity adjustment of a hot mix asphalt drum when output gas temperatures are uneven |
JPH06207403A (en) * | 1991-10-03 | 1994-07-26 | Niigata Eng Co Ltd | Deodorization type recycle plant for asphalt pavement waste |
WO1993010952A1 (en) * | 1991-11-27 | 1993-06-10 | Cyclean, Inc. | Method and apparatus for producing hot mix asphalt |
US5556197A (en) * | 1994-11-04 | 1996-09-17 | Gentec Equipment Company | Asphalt plant for both continuous and batch operation |
US5579587A (en) * | 1995-12-15 | 1996-12-03 | Jat Enterprises Inc. Of Indiana | Recycle moisture evaporation system |
US5737849A (en) * | 1995-12-15 | 1998-04-14 | Jat Enterprise Inc. Of Indiana | Recycle moisture evaporation system |
CN117166319A (en) * | 2023-11-03 | 2023-12-05 | 知行良知实业股份有限公司 | Production device and process of large-proportion hot-recycled asphalt mixture |
CN117166319B (en) * | 2023-11-03 | 2024-01-05 | 知行良知实业股份有限公司 | Production device and process of large-proportion hot-recycled asphalt mixture |
Also Published As
Publication number | Publication date |
---|---|
JPH07107249B2 (en) | 1995-11-15 |
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