WO1985005439A1 - Asphalt recycle plant - Google Patents

Asphalt recycle plant Download PDF

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Publication number
WO1985005439A1
WO1985005439A1 PCT/US1984/000726 US8400726W WO8505439A1 WO 1985005439 A1 WO1985005439 A1 WO 1985005439A1 US 8400726 W US8400726 W US 8400726W WO 8505439 A1 WO8505439 A1 WO 8505439A1
Authority
WO
WIPO (PCT)
Prior art keywords
dryer
recycle
asphalt
recycling
plant
Prior art date
Application number
PCT/US1984/000726
Other languages
French (fr)
Inventor
David F. Brashears
Emanuel J. Elliott
Theodore G. Butler
Original Assignee
Mechtron International Corp.
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 Mechtron International Corp. filed Critical Mechtron International Corp.
Priority to JP50212584A priority Critical patent/JPS61502136A/en
Publication of WO1985005439A1 publication Critical patent/WO1985005439A1/en

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Classifications

    • E—FIXED CONSTRUCTIONS
    • E01—CONSTRUCTION OF ROADS, RAILWAYS, OR BRIDGES
    • E01C—CONSTRUCTION OF, OR SURFACES FOR, ROADS, SPORTS GROUNDS, OR THE LIKE; MACHINES OR AUXILIARY TOOLS FOR CONSTRUCTION OR REPAIR
    • E01C19/00—Machines, tools or auxiliary devices for preparing or distributing paving materials, for working the placed materials, or for forming, consolidating, or finishing the paving
    • E01C19/02—Machines, tools or auxiliary devices for preparing or distributing paving materials, for working the placed materials, or for forming, consolidating, or finishing the paving for preparing the materials
    • E01C19/10—Apparatus or plants for premixing or precoating aggregate or fillers with non-hydraulic binders, e.g. with bitumen, with resins, i.e. producing mixtures or coating aggregates otherwise than by penetrating or surface dressing; Apparatus for premixing non-hydraulic mixtures prior to placing or for reconditioning salvaged non-hydraulic compositions
    • E01C19/1059—Controlling the operations; Devices solely for supplying or proportioning the ingredients
    • E01C19/1063—Controlling the operations
    • E—FIXED CONSTRUCTIONS
    • E01—CONSTRUCTION OF ROADS, RAILWAYS, OR BRIDGES
    • E01C—CONSTRUCTION OF, OR SURFACES FOR, ROADS, SPORTS GROUNDS, OR THE LIKE; MACHINES OR AUXILIARY TOOLS FOR CONSTRUCTION OR REPAIR
    • E01C19/00—Machines, tools or auxiliary devices for preparing or distributing paving materials, for working the placed materials, or for forming, consolidating, or finishing the paving
    • E01C19/02—Machines, tools or auxiliary devices for preparing or distributing paving materials, for working the placed materials, or for forming, consolidating, or finishing the paving for preparing the materials
    • E01C19/10—Apparatus or plants for premixing or precoating aggregate or fillers with non-hydraulic binders, e.g. with bitumen, with resins, i.e. producing mixtures or coating aggregates otherwise than by penetrating or surface dressing; Apparatus for premixing non-hydraulic mixtures prior to placing or for reconditioning salvaged non-hydraulic compositions
    • E01C19/1013—Plant characterised by the mode of operation or the construction of the mixing apparatus; Mixing apparatus
    • E01C19/1027—Mixing in a rotary receptacle
    • E01C19/1036—Mixing in a rotary receptacle for in-plant recycling or for reprocessing, e.g. adapted to receive and reprocess an addition of salvaged material, adapted to reheat and remix cooled-down batches
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27—FURNACES; KILNS; OVENS; RETORTS
    • F27B—FURNACES, KILNS, OVENS, OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B19/00—Combinations of furnaces of kinds not covered by a single preceding main group
    • F27B19/04—Combinations of furnaces of kinds not covered by a single preceding main group arranged for associated working
    • E—FIXED CONSTRUCTIONS
    • E01—CONSTRUCTION OF ROADS, RAILWAYS, OR BRIDGES
    • E01C—CONSTRUCTION OF, OR SURFACES FOR, ROADS, SPORTS GROUNDS, OR THE LIKE; MACHINES OR AUXILIARY TOOLS FOR CONSTRUCTION OR REPAIR
    • E01C19/00—Machines, tools or auxiliary devices for preparing or distributing paving materials, for working the placed materials, or for forming, consolidating, or finishing the paving
    • E01C19/02—Machines, tools or auxiliary devices for preparing or distributing paving materials, for working the placed materials, or for forming, consolidating, or finishing the paving for preparing the materials
    • E01C19/10—Apparatus or plants for premixing or precoating aggregate or fillers with non-hydraulic binders, e.g. with bitumen, with resins, i.e. producing mixtures or coating aggregates otherwise than by penetrating or surface dressing; Apparatus for premixing non-hydraulic mixtures prior to placing or for reconditioning salvaged non-hydraulic compositions
    • E01C2019/1081—Details not otherwise provided for
    • E01C2019/1095—Mixing containers having a parallel flow drum, i.e. the flow of material is parallel to the gas flow

Definitions

  • the present invention relates to asphalt plants and especially to batch type asphalt plants to which an asphalt recycling system is added for utilizing old asphaltic pavement materials, and the like, to produce high quality new paving materials.
  • asphalt plants have generally been 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 elongated drum having a burner directed into one end, with the aggregate being fed therethrough from the other end, and providing rotation of the drum with flights for mixing the aggregate material with the hot gases and causing it to be dried.
  • 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.
  • the dried aggregate materials 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 with mineral 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.
  • 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 viding 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 receive and store the heated recycled asphalt 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 dryer for 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 the asphalt 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.
  • Figure 1 is a perspective view of a portion of batch type asphalt plant having a recycling asphalt plant phantom view attached thereto;
  • FIG. 2 is a block diagram of an asphalt recycling plant in accordance with the present invention.
  • FIG. 3 is another block diagram of a modified recycling asphalt plant in accordance with the present invention.
  • a batch type asphalt plant 10 having an asphalt recycling plant 11 attached thereto.
  • the batch type asphalt plant 10 includes a batching tower 12 having a mineral filler bin 13 adjacent thereto and a plant control room 14 for controlling the operation of the batching tower 12.
  • An aggregate dryer 15 is connected 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 24 to the other end of the dryer 25, while the heated air from the burner 21 passes heated air and gases through the dryer 15 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 materials a r e fed to a bag house or a fabric filter dust collector 27 where an air blower 28 directs the cleaned gases through a stack 30.
  • 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.
  • 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 size 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 26 and a damper 40 and 41 have been placed in the ducts for controlling the heated gases either directly 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 43 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 43 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 34 from the existing plant dryer 15.
  • a hot recycling slat type conveyor 52 is connected from the recycling dryer 34 to a hot recycling storage silo 53, which may be connected to an auger or feed type conveyor 54 to the batch tower 12, or it can be mixed with aggregates from the batch type asphalt plant along with liquid asphalt for reuse as paving material, or the like.
  • the heated gases are fed from the recycling dryer 34 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 through 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 materials 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 34 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.
  • an asphalt recycling system 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 predetermined temperature using the waste heat from an existing batch type asphalt plant dryer 15 and adding heat to the material through a booster burner and controlling the booster burner to maintain the temperature in the 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.

Abstract

An asphalt recycling system (11) and process are incorporated into an existing batch type asphalt plant (10). The existing asphalt plant (10) has an aggregate dryer (15) and air discharge ducts (26) connected to a filtering system (27). A recycling dryer (34) has input ducts (32) connected to the existing aggregate dryer discharge ducts (26) and output ducts (35) connected from the recycling dryer back to the existing ducts (33) to the filtering system (27). A recycle feeder bin (37) for feeding reclaimed asphalt pavement to the recycle dryer (34) is connected to the recycle dryer. A recycle booster burner (43) is operatively connected to the recycle dryer (34) through the input duct (32) to the dryer for providing additional heat to the recycle dryer (34) so that the waste heat from the existing aggregate dryer (15) and the booster burner (43) provide a predetermined heat to the recycle dryer (34) for heating the asphalt material. A recycling storage bin or silo (53) is connected to receive the heated recycled asphalt from the recycle dryer (34). A hammermill (36) or other means may be provided for breaking up the old asphaltic materials, such as old paving materials prior to entry of the material into the recycle dryer (34). Dampers are provided for directing heated gases from the existing batch type asphalt plant to the recycling system, as needed, and temperature controls (47, 51, 46, 50) are utilized to control the recycle booster burner (43) to provide the right combination of exisiting waste and added heat for the recycle dryer (34). The stored recycled asphalt materials may be fed to an exisiting plant batching tower (12) for batching and loading into vehicles.

Description

ASPHALT RECYCLE PLANT
Background of the Invention
The present invention relates to asphalt plants and especially to batch type asphalt plants to which an asphalt 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 been 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 elongated drum having a burner directed into one end, with the aggregate being fed therethrough from the other end, and providing rotation 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 materials 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 with mineral 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 invention 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 viding 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 receive and store the heated recycled asphalt 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 dryer for 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 the asphalt 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 Desc ription of the Drawings
Other objects, features and advantages of the present invention will be apparent from the written description and the drawings, in which:
Figure 1 is a perspective view 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 an asphalt recycling plant 11 attached thereto. The batch type asphalt plant 10 includes a batching tower 12 having a mineral filler bin 13 adjacent thereto and a plant control room 14 for controlling the operation of the batching tower 12. An aggregate dryer 15 is connected 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 24 to the other end of the dryer 25, while the heated air from the burner 21 passes heated air and gases through the dryer 15 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 materials a r e fed to 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 size 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 26 and a damper 40 and 41 have been placed in the ducts for controlling the heated gases either directly 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 43 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 43 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 34 from the existing plant dryer 15.
A hot recycling slat type conveyor 52 is connected from the recycling dryer 34 to a hot recycling storage silo 53, which may be connected to an auger or feed type conveyor 54 to the batch tower 12, or it can be mixed with aggregates from the batch type asphalt plant along with liquid asphalt for reuse as paving material, or the like. The heated gases are fed from the recycling dryer 34 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 through 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 materials 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 34 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 predetermined temperature using the waste heat from an existing batch type asphalt plant dryer 15 and adding heat to the material through a booster burner and controlling the booster burner to maintain the temperature in the 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 efficiency of the batch type asphalt plant, utilizes 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 illustrative rather than restrictive.

Claims

ClaimsI Claim:
1. An asphalt recycling system characterized by: an existing asphalt plant (10) having an aggregate dryer (15) and gas discharge; a recycle dryer (34) for reheating used asphalt and having an input duct (32) connected to the discharge duct (26) of said existing asphalt plant, said recycling dryer (34) also having an outlet duct (35) whereby heated unfiltered air is passed through said recycling dryer (34) from said asphalt plant dryer (15); recycle feeder means (42) connected to said recycle dryer (34) for feeding old asphaltic materials to said recycle dryer (34); and auxiliary recycle booster heat means (43) operatively connected to said recycle dryer (34) for providing additional heat to said recycle dryer (34).
2. An asphalt recycling system in accordance with Claim 1, in which said auxiliary recycle heat booster means (43) is a recycle booster burner.
3. An asphalt recycling system in accordance with Claim 2, in which said existing asphalt plant (10) includes a filtering system (27) having ducts (33) connected thereto from said plant gas discharge.
4. An asphalt recycling system in accordance with Claim 3, in which said recycle dryer input duct (32) and said existing asphalt plant discharge duct (26) have dampers (40, 41) placed therein controlling the passage of heated and filtered gases from said existing asphalt plant dryer to said recycle dryer (34) and through the existing plant discharge duct (26) to said asphalt plant filtering system (27), whereby heated unfiltered gases may be directed to said filter system through said recycle dryer (34) or may bypass said recycle dryer to said filter system (27).
5. An asphalt recycling system in accordance with Claim 4, in which said existing asphalt plant (10) discharge duct (26) has a portion forming a bypass (35) between an input duct (32) to said recycle dryer (34) and an output duct (35) from said recycle dryer (34) and has a damper (55) located in said bypass duct (53) adjacent the recycle dryer input duct (35) and adjacent the recycle dryer discharge duct connection to said existing duct.
6. An asphalt recycling system in accordance with Claim 2, in which a temperature sensor (46) is connected to the output of said recycle dryer (34), output duct (35) for measuring of the heat of the discharge duct, said sensor being operatively connected to said recycle booster burner (43).
7. An asphalt recycling system in accordance with Claim 6, in which said recycle dryer (34) has a recycle asphalt discharge (52) and has a temperature sensor (47) placed therein for measuring the temperature of the discharged recycled asphalt material, said sensor being operatively connected to said recycle burner (43).
8. An asphalt recycling system in accordance with Claim 7, in which said recycle dryer input duct (44) has a portion having refractory lining (45) therein.
9. An asphalt recycling system in accordance with Claim 8, in which said recycling dryer asphalt material discharge (52) includes a conveyor connecting said recycle dryer (34) to said recycle storage means (53).
10. An asphalt recycling system in accordance with Claim 9, including a recycle storage means (53) having a conveyor (54) connecting said recycle storage means to an existing asphalt plant batch tower (12).
11. An asphalt recycling system in accordance with Claim 1, including a hammermill (36) connected to said recycle feeder means (42) for reducing the size of recycled asphalt materials.
12. A process of recycling asphalt materials characterized by the steps of: breaking up old asphaltic materials; feeding said broken up asphaltic materials to a recycle dryer (34); directing heated gases from an asphalt plant (10), asphalt dryer (15) into said recycling dryer (34); adding additional heated air to said recycling dryer from an auxiliary heat source (43); heating said old asphaltic materials in said recycling dryer (34); discharging gases from said recycle dryer (34) to an exhaust system; and feeding recycled asphalt materials from said dryer.
13. A process in accordance with Claim 12, including the step of sensing the temperature of said heated gases discharged from said recycle dryer (34) for controlling the addition of heated air to said recycle dryer.
14. A process in accordance with Claim 13, including the step of sensing the temperature of recycled asphalt materials discharged from said recycling dryer (34) for controlling the heated air added to said recycling dryer (34).
15. A process in accordance with Claim 14, including the step of controlling the flow of heated gases from said asphalt plant (10) to said recycling dryer (34) with dampers (40, 41).
16. A process in accordance with Claim 15, including the step of feeding recycled asphalt materials from said asphalt storage bin (53) to a batching tower (12) of said asphalt plant (10).
PCT/US1984/000726 1983-03-07 1984-05-10 Asphalt recycle plant WO1985005439A1 (en)

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JP50212584A JPS61502136A (en) 1984-05-10 1984-05-10 Asphalt recirculation equipment

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EP0181858A4 (en) 1986-10-02
EP0181858A1 (en) 1986-05-28

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