JPS60120757A - Method and apparatus for producing asphalt mixture heated by heat exchange utilizing waste bituminous paving material - Google Patents

Method and apparatus for producing asphalt mixture heated by heat exchange utilizing waste bituminous paving material

Info

Publication number
JPS60120757A
JPS60120757A JP22969683A JP22969683A JPS60120757A JP S60120757 A JPS60120757 A JP S60120757A JP 22969683 A JP22969683 A JP 22969683A JP 22969683 A JP22969683 A JP 22969683A JP S60120757 A JPS60120757 A JP S60120757A
Authority
JP
Japan
Prior art keywords
aggregate
asphalt
heat exchange
heated
waste
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
Application number
JP22969683A
Other languages
Japanese (ja)
Other versions
JPH0380922B2 (en
Inventor
Hideo Sasaki
笹木 秀雄
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.)
TAISEI DORO KK
Original Assignee
TAISEI DORO KK
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 TAISEI DORO KK filed Critical TAISEI DORO KK
Priority to JP22969683A priority Critical patent/JPS60120757A/en
Publication of JPS60120757A publication Critical patent/JPS60120757A/en
Publication of JPH0380922B2 publication Critical patent/JPH0380922B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Road Paving Machines (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Abstract

PURPOSE:To obtain a reclaimed asphalt mixture of stable quality similar to a new material, by mixing a material to be reclaimed, obtd. by crushing a waste bituminous paving material, with a new aggregate heated to a specified temp. to thereby effect heat exchange therebetween. CONSTITUTION:A waste material obtd. by cutting asphalt-paved plates with a cutter or crushed waste material obtd. by a crusher is placed in a waste material bin 8. Asphalt, an aggregate, the waste material, stone powder, etc. are weighed by metering tanks 4a, 4b, 4c and introduced into a mixer where they are mixed together in such a proportion that a mixture consisting of the asphalt, the aggregate, the stone powder, etc. accounts for 100pts.wt. The mixing ratio of these components varies according to the quality of the waste material, the particle size of the new aggregate, the purpose of use, temp. change, etc. During mixing in the mixer, the waste asphalt material, the asphalt, the stone powder, etc. are mixed with the new aggregate heated to 200-250 deg.C, whereby the temp. of the mixture approaches about 160 deg.C which is the desired temp.

Description

【発明の詳細な説明】 本発明は瀝青質舗装廃材を利用した熱交換式加熱アスフ
ァルト混合物の製造方法に係る。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing a heat exchange heated asphalt mixture using bituminous pavement waste.

既設アスファルト舗装の補修1早等で生じるアスファル
ト廃材の、熱利用はオイルショック以降、石油価格の大
幅な筒騰と不安定な石油供給の影%”&受けて、限りあ
る貿詠を有効に利用する立場から、或いは「pA果物の
処理及び清掃に関する法律」によってアスファルトm材
も産業廃檗物に指足されたことによりその処分地対策と
いう立場からも急、速に発展し、実用段階に人ってきて
いる。
Since the oil shock, the use of heat from asphalt waste generated during early repair of existing asphalt pavement has been affected by the dramatic rise in oil prices and unstable oil supply. As asphalt m materials were included as industrial waste under the ``Act on Processing and Cleaning of PA Fruits'', the development rapidly progressed from the perspective of dealing with disposal sites. It's coming.

それらの廃材の再利用合材の用途としては。What are the uses of recycled composite materials from those waste materials?

(11軽舗装の路上混合方式による再生路盤。(Recycled roadbed using road mixing method for 11 light pavement.

(2) プラント混合による再生路盤材、(3) プラ
ント混合による再生加熱合材、などで、軽舗装や簡易舗
装の表層のみにアスコンを用いる場合の代替材料的用途
か多く主流となっているのが現状である。
(2) Recycled roadbed material mixed in a plant, (3) Regenerated heated composite material mixed in a plant, etc., which are mainly used as an alternative material when Ascon is used only for the surface layer of light pavement or simple pavement. is the current situation.

また、その再生利用合材の製造方式につ(Sては、再生
加熱合材中の骨材として廃材の占める割合が80〜10
0■量−の筒車を占めるドラムドライヤー響ミキシング
方式が一般に採られており、これには、ドラムドライヤ
ー・ミキシング方式の導入その他、多額の設備費を要す
る難点、廃材中のアスファルトは相当老化しており、高
率利用においては、廃材は再加熱されるために締固め脣
性の問題等から針入度の修正に軟化剤が必袂となる難点
、供給廃材の品’Rカ5時と場所によって変動し、再生
合材としての品j葭もこれらの影響によって不安定とな
る等の難点があるため路面の最上層部分には限定使用し
力)認められていない。
In addition, regarding the manufacturing method of the recycled mixed material (S), the proportion of waste material as aggregate in the recycled heated mixed material is 80 to 10%.
The drum dryer sound mixing method, which occupies a 0.0 hour hour wheel, is generally adopted, but this method has the disadvantages of introducing a drum dryer mixing method, requiring a large amount of equipment cost, and the fact that the asphalt in the waste material ages considerably. In high-rate utilization, the waste material is reheated, so a softening agent is required to correct the penetration due to problems such as compaction flexibility, and the problem is that the waste material used is It varies depending on the location, and because of the drawbacks such as the instability of recycled composite material, such as the fact that it becomes unstable due to these influences, it is not allowed for limited use on the top layer of the road surface.

本発明はそれら難点を解消し、少額の設備費で、軟化剤
を使わす、安定した品質の再生合材を提供すると共に、
その使用範囲も新規合材と同等なものであることを目的
としている。本発明に係るアスファルト混合物の製造方
式の基本的な考え方は、アスファルト廃材を100チ使
用して合材を製造するのではな(、通常アスファルトプ
ラントで新規合材を製造1′ろ過程のミキシング時に何
割かの廃材を常温のままで混入し、新規合材の放熱によ
って間接的に加熱することにより晩材を再利用しようと
するもので、瀝青質舗装廃材を破砕して再生素材となし
、加熱した新知、骨材と再生素材を計量槽及びミキサ内
で第1次熱交換を行い、次にフィラー、加熱しり新規ア
スファルトの順にミキサに投入し、混練しその間第2次
熱交換を行なってなる熱交換式加熱アスファルト混合物
を製造するさい、該熱交侠式アスファルト混合物100
市指部に対し、前記再生素材の混合率かlO〜45jJ
Lt部であり、前記加熱した新規骨材の加熱温度は20
0〜250Cの範囲であることを特徴とする瀝青¥を個
装廃材を利用した熱交換式加熱アスファルト混合物の製
造方法に係る。上記S成により成るこの発Ijによると
、ミキシング時に何割ρ・の廃材を常温の1まで混入し
、鞠規背材の放熱によって間接的に加熱するものである
ので、ドラムドライヤー・ミキシング方式の導入を必要
とせず、単に廃刊な常温のまま自動的にミキサに投入す
る装色だけを従来のアスファルトプラントに取付けるだ
けで廃材を再生する合材製造ができるので設備投資が低
額ですみ、廃刊の混合割合が10〜45ii1部である
から剣大度の修正に軟化剤が不袈であり、廃刊の混入率
も低率であるから供給廃材の品質変動に対してもゼ)生
合材に及はす影響は極度に少なくなるなど、幾多のすぐ
れた効果がある。以下本発明の実施例を図面に基1−さ
@yl明する。第1囚はプラント概略図である。
The present invention solves these difficulties and provides a recycled composite material of stable quality using a softener with a small equipment cost.
The aim is for the scope of use to be equivalent to that of new composite materials. The basic concept of the production method of the asphalt mixture according to the present invention is that the mixed material is not manufactured using 100 pieces of asphalt waste (normally, new mixed material is manufactured in an asphalt plant during mixing during the filtration process). This method attempts to reuse late wood by mixing a percentage of waste materials at room temperature and heating them indirectly through the heat radiation of the new composite material. With this new knowledge, the aggregate and recycled material are subjected to a primary heat exchange in a measuring tank and a mixer, and then the filler and heated new asphalt are put into the mixer in that order and kneaded, during which a secondary heat exchange is performed. When producing a heat exchange heated asphalt mixture, the heat exchange heated asphalt mixture 100
The mixing ratio of the recycled material to the city part is lO ~ 45jJ
Lt part, and the heating temperature of the heated new aggregate is 20
The present invention relates to a method for producing a heat exchange heated asphalt mixture using bituminous waste material, characterized in that the temperature is in the range of 0 to 250C. According to this generation Ij, which is made up of the above S configuration, during mixing, what percentage of the waste material of ρ is mixed in at room temperature to 1, and is heated indirectly by the heat dissipation of the backing material, so the drum dryer mixing method is not suitable. There is no need for installation, and by simply installing coloring, which is automatically fed into a mixer at room temperature, into a conventional asphalt plant, it is possible to produce composite material that recycles waste materials. Since the mixing ratio is 10 to 45ii 1 part, it is unnecessary to use a softener for correction of Kendaido, and since the mixing rate of discontinued publications is low, it is also effective against fluctuations in the quality of supplied waste materials. It has many excellent effects, such as greatly reducing the effects of lotus. Embodiments of the present invention will be explained below based on the drawings. The first picture is a schematic diagram of the plant.

アスファルトプラント1は要部に耕規骨制のドライヤ2
と合材のミキサ3とを配設し、前記ミキ′I73上部に
は計1(:t’!4a、4b、4cを配し℃ある。該計
量槽は石粉用4a、骨材用4b・アスファルト用4Cと
に分け、石粉用計V槽4aには石粉を石粉エレベータ5
を介して収容する石粉ビン6を配設し、iiJ記創拐月
計量槽4bには廃刊を廃札ホンパフを介して収容イる廃
材ヒン8とドライヤ2で加熱された骨相を保温して収容
するホットビン9を配設している。
The asphalt plant 1 has a dryer 2 with a tillage structure in the main part.
A total of 1 (:t'! 4a, 4b, 4c) are arranged on the top of the mixer I73, and the measuring tank is 4a for stone powder, 4b for aggregate, Separated into 4C for asphalt and V tank 4a for stone powder, stone powder is transported to stone powder elevator 5.
A stone dust bin 6 is installed to store the discontinued publications through a waste book puff 8 and a dryer 2 heats and stores the bone tissue heated in the dryer 2. A hot bin 9 is provided for this purpose.

前記ホットビン9上稀にはスクリーン10を配し、該ス
クリーン10と前記ドライヤ2の吐出口部との間に14
.拐を搬送するホットエレベータ11を配設しである。
A screen 10 is sometimes arranged above the hot bin 9, and between the screen 10 and the discharge port of the dryer 2, a screen 14 is provided.
.. A hot elevator 11 is provided to transport the cargo.

前記ドライヤ2には、その煙筒12との間に乾式サイク
ロッ13%湿式ザイクロン14.排風機15を順次配設
し、前記乾式サイクロン13は熱風管13aを前記ホッ
トエレベータ11に接続して加熱できるよう構成してい
る。
The dryer 2 has 13% dry Zyclone and 14% wet Zyclone between it and the smoke tube 12. Exhaust fans 15 are arranged one after another, and the dry cyclone 13 is configured to be able to heat a hot air pipe 13a connected to the hot elevator 11.

また前記廃材ホッパ7は図示しないベルトフィーダで所
定量の廃材を吐出し、図示しないべルトコンベヤで廃拐
ビン8に搬送ストックさせる。別に図示しないプラント
本体の操作室から指令が出されると、Q@ビン80図示
しないスクリューコンベアが作動してプラント本体の計
量槽4bにホットビン9の加熱骨材と共に累加計量され
、ミキサ3に投入されるよう構成され。
Further, the waste material hopper 7 discharges a predetermined amount of waste material using a belt feeder (not shown), and transports and stocks the waste material into a scrapping bin 8 using a belt conveyor (not shown). When a command is issued from the operation room of the plant main body (not shown), a screw conveyor (not shown) of the Q@bin 80 is activated, and the aggregates are cumulatively weighed into the measuring tank 4b of the plant main body together with the heated aggregate in the hot bin 9, and then fed into the mixer 3. It is configured so that

ドライミキシング後、アスファルト計量槽4cからアス
ファルトが添加され、ウェットミキシングされて再生合
材が&Iiされる。前記ドライヤ2は支柱17上に膜製
され、基端構成体2aと上端構成体2bとの間に回転体
2Cを図示しない駆動機構を介して軸心な中心に回転自
在に装設している。図面中符号2dはバーナ、2eは火
炎、2fは排出0.2gは投入口である。
After dry mixing, asphalt is added from the asphalt measuring tank 4c, wet mixing is performed, and the recycled mixture is mixed. The dryer 2 is mounted on a support 17, and a rotating body 2C is rotatably installed at the axial center between the base end structure 2a and the upper end structure 2b via a drive mechanism (not shown). . In the drawing, 2d is a burner, 2e is a flame, 2f is an exhaust port, and 0.2g is an input port.

前記回転体2Cは円筒体であり、基端部の方から火炎部
2h、内壁部21、投入口部2jに区分し、火炎部2h
には第3図にボすように、断回路り字形の補助羽根18
を円筒内壁局面に摘心Pに対して放射状に配列装設しで
ある。前記内壁部21には第4図に下すように掻揚羽根
19を円筒内壁局面に摘心Pに対して放射状に配列装設
している。該掻揚羽根19は第6図に示すように、断回
路り形基体部19aに検版19b、19bを配列して断
匍略コ字形に形成している。図中符−Q19Cは柵板の
固定相である。
The rotating body 2C is a cylindrical body, and is divided into a flame part 2h, an inner wall part 21, and an inlet part 2j from the base end.
As shown in Fig. 3, there is an auxiliary blade 18 in the shape of a broken circuit.
are arranged radially on the inner wall surface of the cylinder with respect to the center P. In the inner wall portion 21, as shown in FIG. 4, scraping blades 19 are arranged on the cylindrical inner wall surface in a radial arrangement with respect to the center P. As shown in FIG. 6, the raking blade 19 is formed into a substantially U-shape by arranging test plates 19b, 19b on a broken-circuit base portion 19a. The symbol -Q19C in the figure is the stationary phase of the fence plate.

前記投入口部2jには第5図及び第7図に示すように、
板状の逆流防止羽根20を円筒内壁局面に摘心Pに対し
て放射状に、かつ摘心Pを通る軸線に対して傾斜状に配
列装設しである。
As shown in FIGS. 5 and 7, the input port 2j has
Plate-shaped backflow prevention blades 20 are arranged on the inner wall surface of the cylinder radially with respect to the pinch center P and inclined with respect to the axis passing through the pinch center P.

しかして火炎2eは筒内雰囲気を200〜250Cに&
Mできるよう調整してあり、投入口2gから新規骨材1
6を投入して回転体2Cを回転吏せる。この工程におい
て、逆流防止羽根20は骨相か上端構成体2b方向へ逆
流することを防止すると共にドライヤー中心部に骨相を
移送する。掻揚羽根19は回転体20内壁底部に落下す
る骨相を上方へ周壁に清って掻き揚げると共に上部に主
るに従って柵板19bの間から骨材16を・落下させ、
これは第8図にボ1ように回転体2C筒円に平均的に降
種のように落下させ、骨材に平均的に熱吸収を促進させ
る。このことは、再生素材の混入率が10重量%から4
5員量%まで増加するに従い、新規骨材量は減少するの
で、sr規背骨材量多ければ多いように降車状に落下し
、また倉規骨材が少なけれは少ないように降電状に落下
しつるように柵板19bを設置しである。
However, flame 2e has a cylinder atmosphere of 200~250C &
It has been adjusted to allow for new aggregate 1 from the input port 2g.
6 and rotate the rotating body 2C. In this step, the backflow prevention blade 20 prevents the bone phase from flowing back toward the upper end structure 2b and transports the bone phase to the center of the dryer. The scraping blades 19 scrape up the bone material that has fallen on the bottom of the inner wall of the rotating body 20 upwards onto the peripheral wall, and drop the aggregate 16 from between the fence plates 19b to the upper part.
As shown in Fig. 8, the particles are allowed to fall evenly like seeds falling onto the cylinder of the rotating body 2C, thereby promoting heat absorption into the aggregates on an average basis. This means that the content of recycled materials ranges from 10% by weight to 4% by weight.
As the amount of new aggregate increases to 5%, the amount of new aggregate decreases, so if there is a large amount of sr backbone material, it will fall in a descending manner, and if there is less sr. A fence board 19b is installed so that it hangs securely.

次に火炎部2hにおいては補助羽根18によって骨材1
6を周壁に沿ってすくい上げ回転体2Cの筒頂部分では
骨材16を落下させずに筒側部においてのみ骨材16を
落下させることによって、火炎2eの進行を骨材によっ
て阻害しないように構成しており、粗骨伺と細骨材とが
円筒側部に混在し、この間に骨材相互に熱交換が行なわ
れ、所望の温度に容易に達することが可能となる。上記
構成によって、骨材16はドライヤ2において200〜
250 Uo)i([4,囲に任意に加熱されて排出口
2fから排出され、ホットエレベータ11によってスク
リーン10を介してホットビン9に一時的に蓄積される
。ホットエレベータ11はドライヤ2の排熱を乾式サイ
クロン13を介して送られて保温されて(・るから、ド
ライヤ2で加熱された骨材がホットエレベータ11で冷
めることはないし、またホットビン9も光分保温されて
いる。
Next, in the flame part 2h, the aggregate 1 is
By scooping up the flame 2e along the peripheral wall and not dropping the aggregate 16 at the top of the cylinder of the rotating body 2C, but dropping the aggregate 16 only at the side of the cylinder, the progress of the flame 2e is not obstructed by the aggregate. The coarse bone and fine aggregate are mixed on the cylindrical side, and during this time heat exchange occurs between the aggregates, making it possible to easily reach the desired temperature. With the above configuration, the aggregate 16 is in the dryer 2 with a
250 Uo) i ([4, The heat is heated arbitrarily and is discharged from the discharge port 2f, and is temporarily stored in the hot bin 9 via the screen 10 by the hot elevator 11. Since the aggregates are sent through the dry cyclone 13 and kept warm, the aggregates heated by the dryer 2 do not cool down in the hot elevator 11, and the hot bin 9 is also kept warm.

前記廃材ビン8にはアスファルト舗装板をあらかじめ切
削機で切削した廃材、或いはクラッシャーによるクラツ
シング1ullが収奪されている。しかして、6計を槽
4a 、4b、4cからアスファルト、骨材、廃材1石
粉等が各々計量されてミキサ3に投入されて混合される
。アスファル)tは廃材の抽出アスファルトt4rに混
入率を乗じた値を差し引い1こ値だけの新しいアスファ
ルトヲ添加する。アスファルト、骨材、5初等の混合物
100重量部に対してアスファルト廃材の賛は10〜4
5貞甘部の範囲内で適宜混合する。これら混合比率は島
相の質、新規骨相の粒度、使用目的、気温の変動巻を勘
案して決定する〇 ミキサ3による混合の過程で、アスファルト廃材及びア
スファルト、石粉等は200〜250Cに加熱されてい
る新規骨相によって熱交換され混和し%混合物の目標温
度160cに近ずく。
The waste material bin 8 collects 1 μl of waste material obtained by previously cutting asphalt paving boards with a cutting machine or crushed by a crusher. Asphalt, aggregate, waste stone powder, etc. are weighed from the six tanks 4a, 4b, and 4c, respectively, and charged into the mixer 3 to be mixed. Asphalt) t is the value obtained by multiplying the extracted asphalt t4r of the waste material by the mixing rate, and 1 value of new asphalt is added. Asphalt, aggregate, 100 parts by weight of the primary mixture of 5 to 100 parts by weight of asphalt waste material
5. Mix appropriately within the range of 50%. These mixing ratios are determined by taking into consideration the quality of the island phase, the particle size of the new bone phase, the purpose of use, and fluctuations in temperature. During the mixing process by mixer 3, asphalt waste, asphalt, stone powder, etc. are heated to 200 to 250C. Heat is exchanged and mixed by the new bone phase, and the target temperature of the mixture approaches 160c.

!j[規骨材の加熱温度の設電は、外気温、運搬F9i
[時間等によって銅条される。気温19〜20Uの場合
、%+r規骨拐骨材熱温度は光材の混入率10%のとき
200C,20%のとき220t、’、30%のとき2
35m;、45%のとき250Cとして混合物の目標温
度をx60Uに近ずく目安となる。
! j [Electrical setting for heating temperature of aggregate is based on outside temperature, transportation F9i
[Copper strips vary depending on time. When the air temperature is 19 to 20 U, the thermal temperature of bone aggregate based on %+r is 200 C when the mixing rate of light material is 10%, 220 T when it is 20%, 2 when it is 30%.
When the temperature is 35m and 45%, 250C is used as a guideline to bring the target temperature of the mixture closer to x60U.

このようにして製造された再生合材は一般従来の合材と
同様にして用いる。これらを′用いて舗装した路面の力
学的性状についてマーシャル試験、ホイールトラッキン
グ試験(試験温度6oc、接地圧6.4 h−9/ a
d )、及び繰り返し曲げ試験(供試体寸法3X3X4
0crn%スパン30画の2点載荷方式1周波数511
. )の結果を410図、第11図、第12図に享1−
0これによると、廃材20〜45%混入の再生混合物の
動的安定度は、新規混合物に比べて1.5倍程度太き(
、又、施工1年後の動的安定度も大きくなっており、耐
流動性に優れ、供用後の二−デングに対しても非常に安
定しているといえる。
The recycled composite material thus produced is used in the same manner as general conventional composite materials. Marshall test and wheel tracking test (test temperature 6oc, ground pressure 6.4 h-9/a) were conducted to check the mechanical properties of the road surface paved using these
d), and repeated bending test (specimen size 3X3X4
0 crn% span 30 strokes 2 point loading method 1 frequency 511
.. ) are shown in Figure 410, Figure 11, and Figure 12.
According to this, the dynamic stability of recycled mixtures containing 20 to 45% waste materials is about 1.5 times greater than that of new mixtures (
In addition, the dynamic stability after one year of construction has increased, and it can be said that it has excellent flow resistance and is extremely stable against second dengue after being in service.

再生混合物の低温時における繰り返し破壊回数は、島相
混入率が高い程、破壊回数か増加するという結果となり
、又、施工1年後の結果ではこの相関は再生混合物の方
が新規混合物より破w1回数が太き(、低温時の耐久性
に優れているといえる。
The number of repeated failures of the recycled mixture at low temperatures increases as the island phase mixing rate increases, and the results one year after construction show that this correlation shows that the recycled mixture has a higher failure w1 than the new mixture. The number of cycles is large (it can be said that it has excellent durability at low temperatures.

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

図面は本発明に係り、第1図はアスファルトプラント概
略図、第2因はドライヤ横断端面図。 第3図は第2図におけるA −A [「面図、第4図は
第2図におけるB−B断面図、第5図は第2図における
C−C吋面図、第6図は掻揚羽根斜視図、第7図は逆流
防止羽根斜視図、第8図は回転体の回転時を示す第2図
でのLl−Li l、四回、第9図は回転体の回転時を
示す第2図での八−入断面図、第1O図はマーシャル安
定度試験結果表、第11図は切取供試体による変形率表
。 第12図は破壊曲げ試験結果表。 l・・・アスファルトプラント 2・・・ドライヤ 2a・・・基端構成体2b・・・上
端構成体 2c・・・回転体2d・・・バーナ 2e・
・・火炎 2f・・・排出口 2g・・・投入口 2 h 11.火炎部 21…内壁部 2j・・・投入口部 3・・・ミキサ 4a・・・石粉用計縫4N 4b・・・骨材用計Pit
槽4 c−゛°アスファルト用計を槽 5・・・石粉エレベータ 6・・・石粉ビン7・・・廃
材ホッパ 8・・・廃材ビン9・・・ホットビン 1o
・・・スクリーン11・・・ホットエレベータ 12・・・煙筒 13・・・乾式ザイクロン14・・・
湿式ザイクロン 15・・・排風機16・・・骨材 1
7・・・支柱 18・・・補助羽根 19・・・掻揚羽根19a・・・
基体部 19b・・・横板19c・・・固定材 2o・
・・逆流防止羽根、if’Jiン1
The drawings relate to the present invention; FIG. 1 is a schematic diagram of an asphalt plant, and the second diagram is a cross-sectional end view of a dryer. Figure 3 is a side view of A-A in Figure 2, Figure 4 is a sectional view taken along line B-B in Figure 2, Figure 5 is a cross-sectional view taken along line C-C in Figure 2, and Figure 6 is a cross-sectional view taken along line C-C in Figure 2. Figure 7 is a perspective view of the lifting vane, Figure 7 is a perspective view of the backflow prevention vane, Figure 8 shows the rotation of the rotating body, and Figure 9 shows the rotation of the rotating body. Fig. 2 is the 8-section cross-sectional view, Fig. 1O is the Marshall stability test result table, Fig. 11 is the deformation rate table for cut specimens, Fig. 12 is the destructive bending test result table. l... Asphalt plant 2... Dryer 2a... Base end structure 2b... Upper end structure 2c... Rotating body 2d... Burner 2e.
...Flame 2f...Outlet 2g...Inlet 2h 11. Flame part 21... Inner wall part 2j... Input port part 3... Mixer 4a... Meter stitch for stone powder 4N 4b... Meter Pit for aggregate
Tank 4 c-゛° asphalt meter Tank 5... Stone powder elevator 6... Stone powder bin 7... Waste material hopper 8... Waste material bin 9... Hot bin 1o
... Screen 11 ... Hot elevator 12 ... Smoke tube 13 ... Dry Zyclone 14 ...
Wet Zyclone 15...Exhaust fan 16...Aggregate 1
7... Support column 18... Auxiliary blade 19... Raking blade 19a...
Base part 19b...Horizontal plate 19c...Fixing material 2o.
・・Backflow prevention blade, if'Jin 1

Claims (1)

【特許請求の範囲】 (11f!A青質舗装廃材を破砕して再生素材となし、
加熱した新規骨材と再生素材なミキサ内で混合して熱交
換を行い1次にフィラー、加熱したfIF規アスファル
トの順にミキサに投入し、混練してなる熱交換式加熱ア
スファルト混合物を製造するさい、該熱交換式加熱アス
ファルト混合物100重葉部に対し、前記再生素材の混
合率が10〜451普部であり、前記加熱した新規骨材
の加熱温度は200へ250cの範囲であることを特徴
とする瀝青質舗装廃材を利用した熱交換式加熱アスファ
ルト混合物の製造方法。 (2111骨材を加熱するアスファルトプラントに於け
るドライヤは、骨材投入口から骨材が回転摺動落下可能
の傾斜により、バーナ口に至る円筒体であり、バーナの
火炎部における円筒内壁には、骨材が火炎の進行を阻害
することなく円筒内の全周に沼って移動可能の形状の補
助羽根を装設し、バーナの火炎部以遠の円筒内壁には骨
材が円筒横断面に均一に分布oJ能な掻揚羽根を装設し
、骨材投入口附近の円筒内壁には骨材の逆流防止羽根を
装設することを特徴とする瀝青質舗装FjF材を利用し
た熱交換式加熱アスファルト混合物の製造装置。
[Claims] (11f!A) Crushing blue pavement waste material to make recycled material,
When manufacturing a heat exchange type heated asphalt mixture, the heated new aggregate and recycled material are mixed in a mixer for heat exchange, and the first filler and the heated fIF standard asphalt are charged into the mixer in that order and kneaded. , the mixing ratio of the recycled material is 10 to 451 parts per 100 parts of the heat exchange type heated asphalt mixture, and the heating temperature of the heated new aggregate is in the range of 200 to 250 c. A method for producing a heat exchange heated asphalt mixture using bituminous pavement waste. (2111 A dryer in an asphalt plant that heats aggregate is a cylindrical body that extends from the aggregate input port to the burner port with an inclination that allows the aggregate to rotate and slide down. , auxiliary blades are installed in a shape that allows the aggregate to swamp and move around the entire circumference of the cylinder without inhibiting the progress of the flame, and the aggregate is placed in the cross section of the cylinder on the inner wall of the cylinder beyond the flame part of the burner. A heat exchange type using bituminous pavement FJF material, which is equipped with scraping blades capable of uniformly distributing oJ and equipped with blades to prevent backflow of aggregate on the inner wall of the cylinder near the aggregate input port. Equipment for producing heated asphalt mixture.
JP22969683A 1983-12-05 1983-12-05 Method and apparatus for producing asphalt mixture heated by heat exchange utilizing waste bituminous paving material Granted JPS60120757A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22969683A JPS60120757A (en) 1983-12-05 1983-12-05 Method and apparatus for producing asphalt mixture heated by heat exchange utilizing waste bituminous paving material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22969683A JPS60120757A (en) 1983-12-05 1983-12-05 Method and apparatus for producing asphalt mixture heated by heat exchange utilizing waste bituminous paving material

Publications (2)

Publication Number Publication Date
JPS60120757A true JPS60120757A (en) 1985-06-28
JPH0380922B2 JPH0380922B2 (en) 1991-12-26

Family

ID=16896269

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22969683A Granted JPS60120757A (en) 1983-12-05 1983-12-05 Method and apparatus for producing asphalt mixture heated by heat exchange utilizing waste bituminous paving material

Country Status (1)

Country Link
JP (1) JPS60120757A (en)

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4000000A (en) * 1972-09-05 1976-12-28 Mendenhall Robert Lamar Process for recycling asphalt-aggregate compositions
JPS5210318A (en) * 1975-07-15 1977-01-26 Michio Jinno Method of manufacturing highhclass asphalt
JPS5466922A (en) * 1977-11-07 1979-05-29 Taisei Douro Kk Method of making room temperature working asphlt mixture utilizing wasted asphalt mixture

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4000000A (en) * 1972-09-05 1976-12-28 Mendenhall Robert Lamar Process for recycling asphalt-aggregate compositions
JPS5210318A (en) * 1975-07-15 1977-01-26 Michio Jinno Method of manufacturing highhclass asphalt
JPS5466922A (en) * 1977-11-07 1979-05-29 Taisei Douro Kk Method of making room temperature working asphlt mixture utilizing wasted asphalt mixture

Also Published As

Publication number Publication date
JPH0380922B2 (en) 1991-12-26

Similar Documents

Publication Publication Date Title
AU2008241518B2 (en) Method and apparatus for making asphalt concrete using foamed asphalt cement
US4802139A (en) Apparatus for producing a heated reproduction asphalt mixture
US20110247525A1 (en) Method and plant for preparing hot-mix asphalt
JP7189649B2 (en) Method for producing asphalt mixture
CN105951560A (en) Waste asphalt heating stirring machine, waste asphalt regenerating system and waste asphalt regenerating method
JP2011117270A (en) Manufacturing method of asphalt mixture
CN105672098A (en) Recycled asphalt concrete processing complete equipment with premixing device
CA1118157A (en) Method and apparatus for recycling asphalt- aggregate compositions
JPH0259882B2 (en)
WO2010054453A1 (en) A method and a plant for preparing hot-mix asphalt
US6196710B1 (en) Dust distributor for asphalt mixing machine
US4921730A (en) Method of producing a recycled asphalt mixture
JPS60120757A (en) Method and apparatus for producing asphalt mixture heated by heat exchange utilizing waste bituminous paving material
JPH0118204B2 (en)
US3369798A (en) Apparatus for and method of blending dry materials
JP2002212430A (en) Method for preparing recycled hot asphalt mixture containing waste glass grains
JP7049744B2 (en) Asphalt plant and its asphalt mixture manufacturing method
JP4002588B1 (en) Manufacturing method of asphalt composite
JPS6338257Y2 (en)
CN206070302U (en) Regeneration asphalt mixing station and its mix pot
CN205874908U (en) Bank of tubes formula heat transfer mixer, heating mixing system and regeneration system in pitch
KR930009343B1 (en) Process for producing and device of cement a mixture sand
JP3955751B2 (en) Method for producing asphalt mixture
JPH05171615A (en) Mixing of wastes
JPS598807A (en) Machine for melting and regenerating concrete asphalt waste material