Background of the Inven ion

The present inven ion relates to asphalt plants and especially to batch type asphalt plants to which an asphal recycling system is added for utilizing old asphaltic pavement materials, and the like, to produce high quality new paving materials.

In the past, asphalt plants have generally bee of two types, one being of the type where the aggregate is dried and mixed with the liquid bitumen in the dryer and the other being a batch type where the liquid bitumen is mixed with the aggregate later in the mixer crimping mill. Batch type plants typically have hopper feeds for feeding different size cold aggregate materials by means of a cold feed conveyor into the dryer. The dryer typically involves a large elon ated drum having a burner irected into one end, with the aggregate being fed therethrough from the other end, and providing rota¬ tion of the drum with flights for mixing the aggregate material with the hot gases and causing it to be dried. As the material passes through the drum, the hot air and gases from the burner pass out the other end of the dryer into a ducting system which is directed towards a wet wash, mechanical ollector, or fabric filter dust collector for cleaning the air and gases prior to their discharge from a stack. Meanwhile, the dried aggregate aterials are fed up a slat type hot elevator to a batching tower, where the material is passed through screens for separating it into sizes and asphalt liquid from an asphalt storage tank is fed into the weigh box or mixer at the bottom of the tower, along wit hi ineral fillers and mixed with the aggregate prior to 'loading into a truck.

Entire plants are typically controlled by a

control room having the plant controls. This type of plant has been commonly used around the world, but has the disadvantage of not being able to process old, used asphaltic pavement materials. The present invention is .specifically directed to add to an existing batch type asphalt plant a used asphalt recycle plant utilizing the waste heated air and gases from the existing batch type plant, as well as the existing filter system, and being controlled to provide additional heated gases as needed along with controls for cutting in the recycling plant as needed .

It is accordingly, an aim of the present inven ion to recycle existing asphalt materials utilizing waste heat and other components of an existing batch type asphalt type plant.

Summary of the Invention

The present invention provides for an asphalt recycling system and a process of recycling asphalt materials, such as old used pavement materials, at an existing batch type asphalt plant thereby requiring less heat to recycle the material and smaller amounts of liquid asphalt and filler minerals while utilizing existing components such as the existing plant filtering system.

The existing asphalt plant has an aggregate dryer having gas discharge ducts connected to a filtering system. A recycling dryer has input ducts connected to the output duct of the existing plant dryer and has outlet duct from the recycling dryer connected back into the duct to the filtering system. Dampers- allow the recycling dryer to be cut in or out, as desired, while a recycle booster burner is operatively connected to the recycled dryer for pro-

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v id ing additional heat to the recycle dryer control to maintain the temperature at a predetermined desired level. A recycle feeder bin is positioned to feed the old asphaltic materials to the recycle dryer and a hammermill, or the like, may be used to break up the used asphaltic materials to a predetermined aggregate size. A recycled storage bin or silo is connected to r ceive and store the heated recycled asphialt from the recycle dryer and may be connected to the existing batching tower of the asphalt plant for blending with other aggregates and materials. Temperature sensors can sense the temperature in the output of the recycling dryerfor controlling the recycling booster burner to maintain the output temperature by controlling the recycled booster burner. Processes for recycling asphaltic materials included breaking up the old asphaltic materials and feeding the old asphaltic materials to recycle dryer. Any gases are directed from an aggregate plant asphalt dryer into the recycle dryer and the asphaltic materials are heated in the recycle dryer. The adding of heated air to the recycle dryer by the recycle burner allows the heat in the recycle dryer to be controlled to a predetermined level while utilizing waste heat from the asphalt plant. The exhaust gases from the recycle dryer are then fed to e asphal plant's filtering system by way of the existing input duct to the filtering system. Heated used asphaltic materials are fed to an asphalt storage bin and may be fed to an existing batching tower .

Brief Des _* ,cription —o—f the —D—r—awings

Other objects, features and advantages of the present invention will be apparent from the written

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description and the drawings, in which:

Figure 1 is a perspective v ew of a portion of batch type asphalt plant having a recycling asphalt plant phantom view attached thereto;

Figure 2 is a block diagram of an asphalt recycling plant in accordance with the present invention;

Figure 3 is another block diagram of a modified recycling asphalt plant in accordance with the present invention.

Description of the Preferred Embodiments

Referring to Figure 1 , a batch type asphalt plant 10 is shown having a asphalt recycling plant 11 attached thereto. The batch type asphalt plant 10 includes a batching tower 12 having a mineral filler Mr. 13 adjacent thereto and a plant control room 14 or controlling the operation o the batching tower 1 . An aggregate dryer 15 is con ected by a slat type conveyor 16 for conveying heated aggregate materials into the batching tower 12. A liquid asphalt storage tank 17 is connected by way of pipes 18 to the batching tower 12. The asphalt storage tank 17 has a heater 20, while the aggregate dryer has an aggregate heating burner 21 on one end thereof. A plurality of storage hoppers 22 may be loaded with different size aggregate materials and are fed by a cold feed conveyor 23 into the dryer 15 and are fed from one end of the dryer 4 to the other end of the dryer 25, while the heated air from the burner 21 passes heated air and gases through the dryer 1*5 and out the outlet duct 26. The heated aggregate materials are then fed through the conveyor 16 to the ^" batching tower 12 while the heated air and gases containing a large amount of particulate

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materials a r fed o a bag house or a fabric filter dust collector 27 where an air blower 28 directs the cleaned gases through a stack 30. In operation, trucks can be directed to beneath the batching tower 12 in the space 31 , mixed with different size aggregates which are screened in the tower 12 mixed with the asphaltic material from the asphalt storage tank 17 and mineral filler material from the mineral filler bin 13 to form the hot asphalt material for use in paving, and the like.

In the present invention, a duct 32 is connected to the duct 26 while a damper is placed in the duct 26 for controlling the flow of the heated gases through the duct portion 33 or through the duct 32, as desired. The heated gases are fed to an asphalt recycling dryer 34 when additional heated air is added to produce the desired amount of heat. The exhaust gases are fed through the duct 35 back to the duct 33, where a damper is placed to control the direction of the flow of gases into the filter system 27. Used asphaltic pavement materials, or the like, may be dumped into a hammermill 36 to reduce their si e to a predetermined aggregate where they are stored in a recycled feed bin 37 and fed into the recycle dryer 34 through a conveyor 38.

The recycling plant may more clearly be seen in connection with Figure 2, in which an existing dryer 15 has a burner 21 connected to one end thereof and is connected through a conveyor 16 to a batch tower 12. The heated gases are passed through a duct 26 to the bag house 27 and through a blower 28 and out the stack 30. The duct 32 has been added to the duct 6 _. and a damper 40 and 41 have been placed in the ducts for controlling the heated gases either irectlv to the bag house 27, or as shown in

connection with Figure 2, into the duct 32 and into the recycling dryer 34. The recyling dryer 34 receives material in the recycling material input 42 and has a booster burner 43 connected to the input duct portion 44 feeding to the recycle drum 34. This portion 44 has refractory material 45 lining the input so that the portion 44 can withstand the added heat from the booster burner 43. The booster burner 3 can be a conventional existing aggregate dryer burner. A temperature sensor 46 is placed on the heated air output from the recycled drum 34 while a temperature sensor 47 is placed on the output for the recycled material from the recycle dryer 34. These temperature sensors ar e connected by way of lines 50 and 51 to the burner 3 so that the temperature of the recycled material can be maintained at a predetermined level by operating the booster burner 43 as needed to increase the temperature of the heated gases being fed to the recycle dryer 3*1 from the existing plant dryer 15.

A hot recycling slat type conveyor 52 is con ected from the ecycling dryer 34 to a hot recycling storage silo 53, which may be connected to an auger or feed type conveyor 5 to the batch tower 12, or it can be mixed with aggregates from the batch type asphalt plant along with liquid asphalt for re¬ use as paving material, or the like. The heated gases are fed from the recycling dryer 3 through the outlet duct 35 and into the filter system 27 where the gases are filtered. A damper 55 is located in the duct portion 33 so that gases from the existing batch type asphalt plant can be fed through the section -33 directly to the bag house 27 or can alternatively be fed through the connecting duct pipes 32 to the dryer 34 and back through the ducting

35 into the existing duct or directly into the filter system 27.

Figure 3 shows the entrance of used asphaltic paving material entering the system at the input 56 into a hammermill 36, where it can be broken up into a predetermined size prior to being fed into a cold feeder or recycle feed bin 37 , where it is fed throu h a cold recycle feed conveyor 38 into the recycle dryer 34. The heated and broken up asphalt material is then fed through a hot recycling slat conveyor 52 into the hot recycling storage silo 53 and through the feeder slat conveyor 54 to the mixing or batch tower 12. The original batch type asphalt plant dryer 15 has a burner 21 for directing heated air through the dryer 15 while the standard aggregate aterials are fed into the input 23 and out the conveyor 16 to the batch tower 12. The booster burner 43 is placed onto an elbow of the ducting 32 for adjusting the temperature of the gases being fed to the recycling dryer 3 from the batch type asphalt plant dryer 15. The air and heated gases from the dryer 34 are fed through the duct 35 into the dust collector or bag house 27.

It should be clear at this point that an asphalt recycling system has been provided for recycling used asphalt pavement materials and this is done in a process of breaking up the materials in a hammermill 36, feeding the broken up materials through a recycle feed bin 37 and conveyor 38 to a recycle dryer 34. The next step is heating the recycled materials to a p edetermined temperature using the waste heat from an existing batch type asphalt plant dryer 15 and addin heat to the material through a booster burner and controlling the booster burner to maintain the temperature in t e

recycling dryer. The process also includes the step of feeding the heated air from the recycle dryer to the filtering system and feeding the recycle asphalt material to a storage bin and to an existing batching tower .

It should be clear that both a process and a system for reprocessing used asphalt pavement material has been provided which utilizes the waste heat from a batch type asphalt plant as well as existing ducting and filtering system, along with the existing batching tower and controls while reducing the amount of liquid asphalt and mineral filler needed to make up an asphalt batch. This increases the efficie cy of the batch type asphalt plant, u ilizes the otherwise wasted broken up asphalt materials. The present invention, however, is not to be construed as limited to the forms shown, which are to be considered illustrati e rather than restrictive .

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