KR200364479Y1 - Recycle system for waste asphalt concrete - Google Patents

Abstract

The present invention relates to a waste asphalt recycling operation system for storing waste asphalt crushed to a predetermined size and putting it in a dryer by a transfer means to dry, melt and recycle.

The waste asphalt recycling operation system of this paper crushes the waste asphalt collected at various construction sites to a certain standard, and puts the crushed products along the belt conveyor from the hopper to the storage unit stored in the hopper type aggregate storage bin for recycling. Belt Conveyor Input, Recycled Additive, Asphalt Modifier, Newze Asphalt by analyzing the characteristics of the dried and molten recycled asphalt with continuous 5-stage dryer system that inputs and puts the waste asphalt concrete crushed into the drying furnace equipped with the burner. Asphalt regeneration operation system characterized in that it is composed of an AP measuring unit for determining the mixing ratio with the concrete and administering the required amount, a mixing unit in which they are mixed, and a supply unit for supplying the recycled material mixed through the mixing unit to the vehicle. It is.

Description

Recycle system for waste asphalt concrete

This paper relates to a driving system of waste asphalt recycling apparatus, and more specifically, to a road opening. It is about the operation system of the facility that processes waste asphalt concrete (ascon) peeled off from the surface of pavement during renovation, various electricity and water piping work. The waste asphalt recycling system of this paper is used to process the waste asphalt recycling system in batches and store them in hot paths. By continuously providing the asphalt for the purpose, it is to provide a waste asphalt recycling apparatus operating system that can save resources as well as minimize the inconvenience of communication and can quickly recover the road.

In general, a road paved with a mixture of asphalt and aggregate heating and mixture is called an asphalt concrete pavement, which cuts the pavement that is commonly seen around.

When the asphalt concrete pavement is subjected to repeated heavy loads such as traffic, cracks or unevenness of the pavement may occur. In order to repair the asphalt concrete pavement deformed by cracks, freezing, irregularities, etc., the asphalt concrete pavement that needs to be repaired by manpower, machines, or equipment is crushed, removed, and new asphalt concrete is installed in its place. This will partially repair or repair the package.

In addition, even when various repairs such as gas pipes, water and sewage pipes, electricity, and telephone lines that are buried underground are required, the asphalt pavement is removed from the pavement surface of the corresponding area and then repaved.

However, waste asphalt concrete that has been crushed and removed in the meantime is considered to be unusable, and most of it is disposed of and discarded, resulting in waste of resources, and the removed asphalt is discarded in landfills such as the sea and rivers, resulting in the environment such as soil and water quality. Is greatly polluting.

In addition, in the prior art, after crushing the existing asphalt in the area to be removed and all the removal is completed, the newly manufactured asphalt concrete is paved in the entire area, which is not only caused by complaints, but also caused by traffic jams due to the delay of recovery work. There was a problem acting as a factor.

Waste asphalt recycling system of the present invention, the waste asphalt collected at various construction sites are crushed to a certain size and stored in a hopper type aggregate storage bin for regeneration, and the belt for inputting the pulverized product along the belt conveyor from the hopper into the drying furnace The conveyor conveying unit and the injected waste asphalt concrete crushed are put into a drying furnace equipped with a burner and dried and melted through a continuous 5-stage dryer system that is heated and dried. It is to provide an asphalt regeneration system comprising a supply unit for supplying regeneration materials to be mixed with the mixing unit is determined in the AP weighing tank for administering additives, asphalt modifiers, new asphalt concrete, etc. and mixed with them.

Currently, most of the technologies applied in the field as recycling technologies for waste asphalt concrete are hot mix method, and representative methods are waste asphalt concrete and new agent after directly recovering waste asphalt concrete by heating directly at the re-packaging site. Hot-In-Place Recycling method that mixes asphalt concrete and rejuvenator appropriately and repacks them on site, and recovers waste asphalt concrete to asphalt concrete recycling plant Hot-In-Plant Recyclimg and the like are known, which are heated and melted and then mixed with recycled additives and new asphalt concrete and recycled additives in a plant mixer to provide asphalt concrete for resurfacing.

The present invention is a waste asphalt concrete that can be selectively applied between hot-in-place recycling method and hot-in-plant recycling method according to the amount of generated concrete, site conditions and situation. It is to provide a playback system.

The present invention was devised to solve the above problems in the prior art, and when the amount of waste asphalt recovered during various renovation work is collected, it is collected and used in the separate place using the waste asphalt recycling apparatus of this paper. It is stored in a hot path and stored in a hot path, and then moved to a site where it is needed, or in a site where a lot of waste asphalt is generated, the waste asphalt regeneration device installed in the vehicle is moved directly and immediately regenerated at the site to provide continuous road repair asphalt. By doing so, it is intended to provide a waste asphalt recycling system that can save resources as well as minimize the inconvenience of vehicle communication and provide fast road recovery and fundamentally block environmental pollution caused by waste asphalt waste.

The waste asphalt recycling system of the present invention is intended to control the amount of transport of waste asphalt shredding for recycling, the amount of asphalt regeneration additives, asphalt modifiers, new concrete additions, etc. AP metering tank is provided to analyze the properties of reclaimed asphalt such as content and calculate the amount of regenerated additives, asphalt modifiers, etc., and the mixing ratio with new asphalt concrete is determined according to the properties of the regenerated product, and these are mixed and mixed. It is to provide a waste asphalt recycling system that controls the dosage.

In other words, in the present invention, a conveyor belt conveying apparatus is used to convey the required amount of crushed material into the drying furnace, and the conveying apparatus can change the rotational speed by using a rotational force such as a motor as a driving source. The debris is completely dry. It is melted and operated so that the internal temperature of the dryer is discharged before and after about 650 ℃. The sensor is converted into an electrical signal through a sensor installed at the beginning of the fifth stage discharge part of the dryer and is input to the controller. By controlling the driving speed of the transfer device for transferring the contents on the belt warp conveyor according to the change amount of the electric signal, the transfer device continuously operates at a high speed of more than 650 ° C. in the dryer internal temperature of the fifth stage discharge system of the continuous five-stage dryer system. Operation is performed and the feeder is operated at low speed between 650 ℃ and 600 ℃, resulting in a complete drying of the input inside the dryer above 650 ℃. It is intended to be melted to recover the concrete properties and discharged.

In addition, in order to recycle waste asphalt concrete, recycled asphalt must match the physical properties required by industrial standards. Therefore, regeneration additives such as asphalt can be used based on the measured and analyzed data when collecting the sample. The present invention relates to a waste asphalt concrete recycling system for discharging to meet the specifications required by construction, or mixing and mixing some new asphalt.

1 is a system diagram of the operation of the waste asphalt recycling apparatus of the present invention.

Figure 2 is a continuous five-stage drier dryer in this article.

3 is a feed amount operation of the present invention. Control state diagram.

*** Explanation of symbols for main parts of drawing ***

1: aggregate storage bin 2: belt conveyor input part

3: Drying, melting part with continuous 5-stage dryer system

4: The storage unit of the recycled asphalt. 5: AP metering unit

6 mixing unit 7 supply unit

8: Shinje asphalt supply unit 9: Asphalt modifier storage tank

10: regeneration additive storage tank 11: dryer inlet side

12: dry outlet side 13: burner

14 discharge box 15 demister filter

16 exhaust exhaust duct 17 dust collector

18: motor control damper 19: exhaust fan

20: chimney 21: motor

Waste asphalt recycling system of the present invention to achieve the above object, waste asphalt collected at various construction sites are crushed to a certain size and stored in a hopper type aggregate storage bin for regeneration, the crushed water along the belt conveyor from the hopper Belt conveyor input section for drying furnace, continuous 5 stage dryer system for inputting the waste asphalt concrete pulverized material (hereinafter abbreviated as `` pulverization '') into the drying furnace equipped with burner, heating and drying, . By analyzing the properties of the molten recycled asphalt, the AP weighing tank for administering the regeneration additives and asphalt modifiers, and the characteristics of the reclaimed asphalt are determined, and the mixing ratio with the new asphalt concrete is determined, and the mixing unit and the mixing unit are added and mixed. It is an object of the present invention to provide an asphalt recycling system comprising a supply unit for supplying mixed recycled materials to a vehicle.

In the present invention, the conveying amount through the conveyor belt is intended to adjust the input amount in connection with the result of measuring the internal temperature with a thermocouple temperature measuring sensor on the first entrance surface of the drying end.

That is, a conveyor belt conveying device is provided to allow the crushed material of the present invention to be conveyed into the drying furnace.

This feeder can change the rotational speed by using the rotational force of a motor or the like as a driving source.

And the drier is completely dry of shreds. Melted and the dryer internal temperature is discharged at about 650 ° C. The sensor temperature is converted into an electrical signal through a sensor installed in the discharge part of the fifth stage having the discharge part and input to the controller.

The control unit controls the driving speed of the transfer device for transferring the contents on the belt bend conveyor according to the change amount of the electrical signal input.

Hereinafter, the waste asphalt recycling system of the present invention will be described in detail with reference to the accompanying drawings.

1 is a piece of waste asphalt crushed to a predetermined size and dried by putting it into a dryer by a conveying means. A schematic diagram showing an operating system of a waste asphalt recycling apparatus for melting and regenerating, from a storage unit (1) and a hopper in which waste asphalt collected at various construction sites is crushed and stored in a hopper type aggregate storage bin for regeneration. Belt conveyor input unit (2) for feeding the pulverized product along the belt conveyor into the drying furnace, and drying and melting part having a continuous 5-stage dryer system for inputting the waste asphalt concrete crushed product into the drying furnace equipped with the burner and heating and drying it. 3), dry. After analyzing the characteristics of the storage part 4 of the molten reclaimed asphalt and the reclaimed asphalt, the mixing ratio with the regenerating additive, the asphalt modifier and the new asphalt concrete is determined, and the AP measuring part 5 for administering the required amount, and the mixing part where these are mixed ( 6) shows an asphalt regeneration operation system comprising a supply unit 7 for supplying regenerated materials mixed through a mixing unit to a vehicle vehicle.

In addition, a new zeal asphalt supply unit 8, a recycled asphalt modifier storage tank 9, a recycled additive storage tank 10, and the like are installed to analyze the characteristics of the recycled asphalt to determine the mixing ratio with the reclaimed additive, the asphalt modifier, and the new asphalt concrete. It is possible to administer the required amount and the asphalt storage unit 4 may be omitted so that the function may be performed in the AP measuring unit (5).

In addition, the exhaust gas discharged by acting on the dry heating of the recycled asphalt is passed through the exhaust fan 19 to the dust collector 17 for purification, and is discharged from the chimney 20 to the atmosphere.

The exhaust gas containing the mist powder which dried and heated regenerated aggregate in the drying and melting part 3 which has a continuous 5-stage dryer system is discharged | emitted through the exhaust duct 16 through the discharge box 14 of a hot hopper type | mold. The demister filter 15 is installed in the box 14 to remove the mist, and then passes through the exhaust duct 16 to be sucked into the dust collector 17 to remove dust. The exhaust fan 19, the chimney 20, etc. are installed to form a dust collecting function and a device, thereby forming a system that can more completely remove the mist or dust in the exhaust gas.

2 is a view showing a continuous five-stage dryer system dryer, which is a key equipment of the asphalt recycling system in the present article.

The rotary dryer 3 is formed in a cylindrical shape and is installed to be inclined rotatably on the base 24.

The rotary dryer 3 is installed to rotate by a motor 21 mounted on the base 24. For this purpose, a ring gear 31 is mounted on the outer circumference of the rotary dryer 3, and the ring gear described above. One side (lower side in the drawing) of the drive 31 is engaged with the drive gear 22 for receiving and driving the power of the motor 21, and the support ring 32 mounted on both sides of the outer circumference of the rotary dryer (3) They are supported by the support rollers 23 rotatably installed on the upper part of the base 24. Therefore, the rotary dryer 3 is rotated on the base 24 by the driving of the motor 21.

In addition, the rotary drier 3 has an inlet side 11 into which a crushed product (waste asphalt concrete pulverized product) is input is inclined in a state slightly higher than the outlet side 12, and the inclination angle is approximately 2 to 5 The angle of ° and inclined upwards, but the reason for limiting the rotary drier 3 itself to the inclination angle range of 2 ~ 5 ° is that the pulverized product is introduced into the inlet side (11) to the outlet side (12) It takes about 310 ~ 490 seconds to transfer the discharge to make the heating and drying of the pulverization is well done, the inlet side (11) when the inclination angle of the rotary dryer is less than 2 degrees close to the horizontal While the crushed powder is not transferred to the outlet side 12 or the feed rate is too slow, the transfer time may exceed 490 seconds, resulting in the overheating of the pulverized powder. When the inclination angle of the dryer 3 is 6 ° or more, the conveying speed of the pulverized product is so fast that the pulverized product may be discharged without being sufficiently heated and dried.

Therefore, the pulverized product introduced into the inlet side 11 of the rotary dryer 3 is sufficiently exposed to the flame heat of the burner, so that the pulverized product can smoothly move inside the rotary dryer and have the required adhesive strength in asphalt concrete. Most preferably, the rotary dryer 3 is inclined upwardly at an angle of about 2 to 5 degrees.

Each of the inlet port 11 and the outlet port 12 of the rotary dryer 3 is provided with an inlet port 25 and the outlet port 26 fixed to allow the rotating drum to rotate, the inlet port 25 A stack 27 is provided at the top of the exhaust gas, and a burner 28 is provided at the outlet 26.

When the pulverized material is introduced into the inlet 25, the pulverized product is automatically opened by the load of the pulverized material, and in the state in which the pulverized material is not injected, the closing operation is performed by its own weight so that the exhaust gas does not leak into the inlet, but only through the flue 27. An opening and closing plate 41 for guiding discharge is provided.

In the above, the flame spraying part of the burner 28 mounted to the discharge port 26 is inserted to a position adjacent to the discharge port side, and is installed to spray the flame toward the inlet side 11 at the central portion of the discharge port side 12.

The rotary dryer 3 of the present invention is formed to have a length of about 8 to 10 m when calculating a daily production amount capable of recycling waste asphalt concrete based on 400 to 500 tons, and according to the increase or decrease of the production amount, the rotary dryer (3). ) The overall length can be increased or decreased.

The interior of the rotary dryer 3 is divided into five consecutive drying zones in which the heating temperature gradually increases.

Referring to the characteristics of the continuous five-stage drying furnace, the rotary drum-type cylindrical dryer 3 is rotatably installed while the outlet side 12 is slightly inclined than the inlet side 11 into which the pulverized material is introduced. The crushed material introduced into the inlet side 11 is gradually transferred to the outlet side 12 while being not directly in contact with the flame sprayed from the burner 28 installed at the outlet side 12. In order to be heated and dried in a furnace, the inlet side 11 and the outlet side 12 are formed by dividing the continuous five-stage drying zone in which the heating temperature is gradually increased. ± 50 ℃ The second stage drying zone is 250 ± 50 ℃ The third stage drying zone is 350 ± 50 ℃ The fourth stage drying zone is 450 ± 50 ℃ and the fifth stage drying zone at the outlet side is 650 ± 50 ℃ With a rotating drum It is composed.

Dryer drum The burner is installed to heat the dryer. The burner of the dryer can use light oil or kerosene.The burner is automatically controlled to maintain the internal temperature of the dryer. To maintain the temperature to increase fuel efficiency.

Figure 3 shows the feed rate operations in this paper. A flowchart illustrating a control state is illustrated, and the controller will be described based on the flowchart.

Finally, the continuous five-stage dryer system dryer in this paper intends to discharge the desired properties by restoring the physical properties of the asphalt at the internal temperature of the dryer at 650 ° C. It checks whether each system is operating normally, and the conveying device is operated at low speed to achieve the drying and melting state.When the discharge temperature of the fifth stage discharge part of the drying furnace reaches 650 ℃ or more, the conveying device is operated at high speed and operated. When the internal temperature of the dryer of the fifth stage discharger is 650 ° C. to 600 ° C., the transfer device is operated at a low speed to adjust the discharge temperature by increasing the discharge temperature by receiving a small amount of the transfer amount. Stops, checks and corrects each system, and then transfers Intended to use the system.

In other words, the waste asphalt concrete regeneration system of this paper is to store a certain amount of crushed aggregate in the belt feeder type aggregate storage tank, and to install the belt feeder under the storage facility to transfer the desired amount of aggregate using the belt conveyor inside the dryer. The feed rate is adjusted to obtain emissions under certain conditions (above 650 ° C) in conjunction with the final discharge temperature of the dryer.

The dryer is a device for drying and melting aggregates, and a bucket having a certain angle is installed inside the rotating drum so that the aggregates can be evenly dried and bent at a specific angle to play drying efficiency and attached to a specific portion.

In addition, since the waste ascon is melted inside the dryer, it requires time and space for melting at the proper temperature when heat is applied. Therefore, the internal structure of the dryer is divided into five stages. The technical configuration is described in detail in the recycling method of waste asphalt concrete (see the technical contents filed by the same designer) which minimizes heat loss while operating at different stages of internal temperature while moving from the first stage to the fifth stage.

The control panel of the waste asphalt concrete regeneration system in this paper is a system that controls the entire waste asphalt regeneration facility. It automatically measures and analyzes the data inside the dryer and the given data such as storage tank, metering tank, and asphalt discharge and automatically reaches the target value. It provides the control system to produce and supply the finished product required by the product uniformity and the industrial product specification.

Waste asphalt reproduction driving system of this bill is dry. By analyzing the characteristics of the molten recycled asphalt, the mixing ratio with the reclaimed additive, asphalt modifier, and new asphalt concrete is determined, and the required amount is administered, mixed, and mixed, and the recycled material mixed through the mixing unit is supplied to the vehicle. As a system that controls the entire asphalt regeneration facility, it automatically measures and analyzes given data such as temperature inside the dryer, storage tank, weighing tank, and asphalt release, and releases it automatically when the target value is reached. It is possible to provide a driving system that controls the production and supply of finished products.

Claims (3)

Store waste asphalt crushed to a predetermined size and dry it by feeding it into the dryer by the transfer means. In the operating system of the waste asphalt recycling apparatus to melt and recycle, Waste asphalt collected at various construction sites is crushed to a certain size and stored in a hopper type aggregate storage bin for recycling, and belt conveyor input part for inputting crushed products along the belt conveyor from the hopper into the drying furnace, and used waste asphalt. Drying, melting and drying with a continuous five-stage dryer system for heating and drying concrete crushed products in a drying furnace equipped with a burner. Analyze the characteristics of the molten recycled asphalt, and determine the mixing ratio with the recycled additive, asphalt modifier, and new asphalt concrete, and the AP weighing portion to administer the required amount, the mixing portion mixed with them, the recycled material mixed through the mixing portion on the vehicle Asphalt regeneration operation system, characterized in that consisting of a supply unit for supplying. The method of claim 1, When the crushed material in the aggregate storage bin is transferred to the dryer through the conveyor belt, the amount of crushed water is transferred so that the internal temperature of the dryer is discharged at high speed over the final 650 ℃ and at low speed at 600-650 ℃. Asphalt regeneration operation system, characterized in that the input amount is adjusted. The method of claim 1, Dryer of continuous 5-stage drier system is 150 ± 50 ℃ for the first stage drying area on the inlet side, 250 ± 50 ℃ for the second stage drying area, 350 ± 50 ℃ for the third stage drying area, 450 ± 50 for the fourth stage drying area. And the fifth stage drying zone at the outlet side is operated to reach 650 ± 50 ° C. 3.