WO2012160555A1 - Process for recycling asphalt mixes - Google Patents

Process for recycling asphalt mixes Download PDF

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Publication number
WO2012160555A1
WO2012160555A1 PCT/IL2012/000206 IL2012000206W WO2012160555A1 WO 2012160555 A1 WO2012160555 A1 WO 2012160555A1 IL 2012000206 W IL2012000206 W IL 2012000206W WO 2012160555 A1 WO2012160555 A1 WO 2012160555A1
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WO
WIPO (PCT)
Prior art keywords
rehabilitant
polymer
porcelanite
activating agent
process according
Prior art date
Application number
PCT/IL2012/000206
Other languages
French (fr)
Inventor
Ronen Alexander Peled
Andrey Vorobiev
Gregory Svechinsky
Ilan Ishai
Original Assignee
Dsi - Dimona Silica Industries Ltd.
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 Dsi - Dimona Silica Industries Ltd. filed Critical Dsi - Dimona Silica Industries Ltd.
Publication of WO2012160555A1 publication Critical patent/WO2012160555A1/en

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Classifications

    • EFIXED CONSTRUCTIONS
    • E01CONSTRUCTION OF ROADS, RAILWAYS, OR BRIDGES
    • E01CCONSTRUCTION OF, OR SURFACES FOR, ROADS, SPORTS GROUNDS, OR THE LIKE; MACHINES OR AUXILIARY TOOLS FOR CONSTRUCTION OR REPAIR
    • E01C7/00Coherent pavings made in situ
    • E01C7/08Coherent pavings made in situ made of road-metal and binders
    • E01C7/18Coherent pavings made in situ made of road-metal and binders of road-metal and bituminous binders
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/34Silicon-containing compounds
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L53/00Compositions of block copolymers containing at least one sequence of a polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers
    • C08L53/02Compositions of block copolymers containing at least one sequence of a polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers of vinyl-aromatic monomers and conjugated dienes
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L95/00Compositions of bituminous materials, e.g. asphalt, tar, pitch
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09DCOATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D195/00Coating compositions based on bituminous materials, e.g. asphalt, tar, pitch
    • EFIXED CONSTRUCTIONS
    • E01CONSTRUCTION OF ROADS, RAILWAYS, OR BRIDGES
    • E01CCONSTRUCTION OF, OR SURFACES FOR, ROADS, SPORTS GROUNDS, OR THE LIKE; MACHINES OR AUXILIARY TOOLS FOR CONSTRUCTION OR REPAIR
    • E01C19/00Machines, tools or auxiliary devices for preparing or distributing paving materials, for working the placed materials, or for forming, consolidating, or finishing the paving
    • E01C19/02Machines, 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
    • E01C19/10Apparatus 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
    • E01C19/1004Reconditioning or reprocessing bituminous mixtures, e.g. salvaged paving, fresh patching mixtures grown unserviceable; Recycling salvaged bituminous mixtures; Apparatus for the in-plant recycling thereof
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2555/00Characteristics of bituminous mixtures
    • C08L2555/20Mixtures of bitumen and aggregate defined by their production temperatures, e.g. production of asphalt for road or pavement applications
    • C08L2555/22Asphalt produced above 140°C, e.g. hot melt asphalt
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2555/00Characteristics of bituminous mixtures
    • C08L2555/30Environmental or health characteristics, e.g. energy consumption, recycling or safety issues
    • C08L2555/34Recycled or waste materials, e.g. reclaimed bitumen, asphalt, roads or pathways, recycled roof coverings or shingles, recycled aggregate, recycled tires, crumb rubber, glass or cullet, fly or fuel ash, or slag
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2555/00Characteristics of bituminous mixtures
    • C08L2555/40Mixtures based upon bitumen or asphalt containing functional additives
    • C08L2555/80Macromolecular constituents
    • C08L2555/84Polymers comprising styrene, e.g., polystyrene, styrene-diene copolymers or styrene-butadiene-styrene copolymers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2555/00Characteristics of bituminous mixtures
    • C08L2555/40Mixtures based upon bitumen or asphalt containing functional additives
    • C08L2555/80Macromolecular constituents
    • C08L2555/86Polymers containing aliphatic hydrocarbons only, e.g. polyethylene, polypropylene or ethylene-propylene-diene copolymers

Definitions

  • the present invention relates to a process for recycling used asphalt mixes using a novel rehabilitant.
  • the present invention seeks to provide a process for recycling used asphalt mixes using a novel rehabilitating agent.
  • a process for rehabilitating a used asphalt mix including: combining porcelanite, an activating agent and a polymer to form a rehabilitant; and mixing the rehabilitant with the used asphalt mix at a temperature of at least about 140 °C.
  • the activating agent includes a quaternary ammonium compound.
  • the quaternary ammonium compound preferably includes at least two alkyl chains of 10 - 30 carbons, more preferably 15 - 18 carbons. Most preferably, the quaternary ammonium compound is di(hydrogenated tallow)dimethylammonium chloride.
  • the rehabilitant includes the activating agent in an amount of 3 - 20% of the porcelanite weight. More preferably, the rehabilitant includes the activating agent in an amount of 10 - 15% of the porcelanite weight.
  • the polymer is a thermoplastic polymer.
  • the thermoplastic polymer is preferably selected from polyethylene, polypropylene, EPDM rubber, styrene- butadiene-styrene copolymer and ethylene-vinyl acetate copolymer. Most preferably, the polymer is selected from styrene-butadiene-styrene copolymer and ethylene-vinyl acetate copolymer.
  • the ratio of the weight of the polymer to the combined weight of the porcelanite and the activating agent in the rehabilitant is from about 1:10 to about 10:1. More preferably, the ratio is from about 1:3 to about 1:1, and most preferably about 1:2.
  • the combining includes: blending the porcelanite with the activating agent to form an activated porcelanite, mixing the activated porcelanite with the polymer in an extruder at a temperature of about 100 °C to about 250 °C to form an extruded mixture; and granulating the extruded mixture. More preferably, the mixing the activated porcelanite with the polymer is at a temperature of about 100 °C to about 160 °C. The granulating preferably produces granules of about 3 - 5 mm.
  • the mixing the rehabilitant with the used asphalt mix is carried out on the surface where the used asphalt is laid.
  • the mixing the rehabilitant with the used asphalt mix is carried out in an asphalt plant. The mixing is preferably carried out at about 140 - 190 °C, more preferably about 150 °C.
  • composition for rehabilitating a used asphalt mix including: porcelanite, an activating agent and a polymer.
  • the activating agent includes a quaternary ammonium compound.
  • the quaternary ammonium compound preferably includes at least two alkyl chains of 10 - 30 carbons, more preferably 15 - 18 carbons. Most preferably, the quaternary ammonium compound is di(hydrogenated tallow)dimethylammonium chloride.
  • the rehabilitant includes the activating agent in an amount of 3 - 20% of the porcelanite weight. More preferably, the rehabilitant includes the activating agent in an amount of 10 - 15% of the porcelanite weight.
  • the polymer is a thermoplastic polymer.
  • the thermoplastic polymer is preferably selected from polyethylene, polypropylene, EPDM rubber, styrene- butadiene-styrene copolymer and ethylene-vinyl acetate copolymer. Most preferably, the polymer is selected from styrene-butadiene-styrene copolymer and ethylene-vinyl acetate copolymer.
  • the ratio of the weight of the polymer to the combined weight of the porcelanite and the activating agent in the rehabilitant is from about 1:10 to about 10:1. More preferably, the ratio is from about 1:3 to about 1:1, and most preferably about 1:2.
  • Fig. 1 is a simplified diagram of the structure of particles of an asphalt mix recycled according to the process of the present invention. DETAILED DESCRIPTION OF THE INVENTION
  • Hot recycling of used asphalt mixes is very widely used in the practice of pavement rehabilitation.
  • Asphalt, once laid on a road surface typically lasts for about 10-15 years, during which time it is exposed to oxygen, moisture and UV radiation from the sun. Due to oxidation and aging resulting from such exposure, the bitumen in the asphalt becomes brittle and loses its elastomeric properties that are required for asphalt pavements. It is desirable to recycle used asphalt rather than dispose of it in order to reduce costs and environmental impact.
  • the most common technique for renewing used asphalt is to add a maltenic petroleum fraction to the used asphalt.
  • Maltenic fractions are aromatic extracts from the heavy distillate fraction of crude oil and are characterized by the following properties: viscosity at 100°C 7-12 cSt, density at 15°C 0.96-0.99, pour point 15°C - 21°C.
  • the maltenic aromatic compounds in asphalt bitumen are destroyed by oxidation and aging. This causes the bitumen to become brittle and no longer suitable for road use.
  • the added maltenic fraction restores the lost elastomeric properties of bitumen.
  • Polymer-modified asphalt mixes usually have much better mechanical stability and elasticity and also age slower than unmodified asphalt mixes.
  • the polymer modifiers such as styrene-butadiene-styrene (SBS) and ethylene-vinyl acetate (EVA) block copolymers, are added to bitumen and form three-dimensional networks inside the W
  • bitumen phase continuous bitumen phase.
  • Typical concentrations of polymer in the bitumen are 3-6% by weight. Although the polymers modify the mechanical properties of bitumen and reduce the effects of bitumen aging, the bitumen is nonetheless still exposed to oxygen, moisture and UV radiation.
  • a composition for lowering the mixing temperature of stone matrix asphalt (SMA) and other asphalt mixes to about 165 °C is disclosed in WO 2010/116354, assigned to the assignee of the present invention and incorporated by reference herein in its entirety. It has now been found that this relatively inexpensive composition, can be used as part of an asphalt rehabilitating composition.
  • SMA stone matrix asphalt
  • rehabilitationant comprising porcelanite, an activating agent and a polymer
  • Porcelanite is a mineral found, inter alia, in deposits in the Dead Sea area of Israel and is described in detail in WO 2010/116354.
  • the activating agent is a quaternary ammonium compound.
  • the quaternary ammonium compound preferably has at least two long carbon chains.
  • the long carbon chains preferably comprise between 10 and 30 carbon atoms, more preferably from 15 to 18 carbon atoms.
  • An especially preferred compound is di(hydrogenated tallow)dimethylammonium chloride, available from Akzo-Nobel (Stockholm, Sweden) as Arquad 2HT-75 (hereinafter "2HT-75").
  • Activation of the porcelanite is preferably achieved by crushing the porcelanite to about 3 - 8 mm particle size granules, adding the activating agent, and blending the mixture until the desired particle size is achieved.
  • the porcelanite can be blended for about 5 minutes, followed by addition of the activating agent and further blending for an additional 1 - 5 minutes.
  • the weight of the activating agent in the rehabilitant is preferably between about 3 and 20% of the porcelanite weight. More preferably, the weight of the activating agent in the rehabilitant is between about 10 and 15% of the porcelanite weight.
  • the polymer is preferably a thermoplastic polymer.
  • the thermoplastic polymer include polyethylene, polypropylene, EPDM rubber, styrene- W
  • the ratio of polymer to activated porcelanite in the rehabilitant is preferably about 1:10 - 10:1, more preferably about 1:3 - 1:1, and most preferably about 1:2.
  • the rehabilitant is preferably formed by mixing the activated porcelanite with the polymer in an extruder at a temperature above the softening point of the polymer, typically about 100 - 250 °C and more preferably about 100 - 160 °C.
  • the extruded mixture is then granulated and cooled.
  • the granule size is preferably about 3 - 5 mm.
  • the rehabilitant is preferably mixed with used asphalt at a temperature of at least about 140 °C.
  • the mixing of the rehabilitant with the used asphalt can be performed in accordance with a method described in Basic Asphalt Recycling Manual, Asphalt Recycling and Reclaiming Association (Annapolis, MD, USA), 2001, hereby incorporated by reference herein in its entirety.
  • the rehabilitant is mixed with the used asphalt using hot in-place recycling (HIR) technology, wherein 100% recycling of the existed asphalt pavement is completed on site.
  • HIR hot in-place recycling
  • the existing asphalt pavement is heated to about 140 - 190 °C, preferably about 150 °C, and softened, permitting it to be scarified or hot rotary milled to a specified depth.
  • the scarified or loosened asphalt pavement is then mixed, placed and compacted with conventional equipment. New aggregate, new asphalt binder, recycling agents and/or new asphalt mix can be added on an as-required basis.
  • the recycling process is carried out in an asphalt plant.
  • the used asphalt is crushed to a size suitable for use as aggregates for asphalt mixes, typically less than 5 cm.
  • Rehabilitant is mixed with the crushed asphalt at a temperature of about 140 - 190 °C, preferably about 150 °C.
  • the rehabilitant is preferably added to the asphalt in an amount of about 1 - 10% of the asphalt weight, more preferably about 3 - 6% of the asphalt weight.
  • the mixing time is preferably about 50 - 80 sec, more preferably about 60 seconds.
  • the rehabilitated asphalt can be prepared in a batch or continuous process. After production, the hot rehabilitated asphalt can be loaded into trucks for delivery to a worksite, or stored in a hot storage facility.
  • the asphalt rehabilitated according to the present invention has superior properties relative to asphalt rehabilitated according to previously known methods and even relative to original asphalt mixes.
  • asphalt mixes are produced, a portion of bitumen is absorbed into the aggregate particle, while the balance remains on the surface of the particles. It is this surface bitumen which oxidizes and hardens during the lifetime of the asphalt on the road.
  • Fig. 1 demonstrates the distribution of layers in a particle 2 of asphalt after rehabilitation. Due to the high viscosities of both the bitumen in the used asphalt mix and the rehabilitant, the rehabilitant does not penetrate through the entire thickness of the surface bitumen layer.
  • the rehabilitant penetrates into an outer bitumen layer 12, which obtains visco- elastic properties similar to those of polymer-modified bitumen.
  • the concentration of the rehabilitant in outer bitumen layer 12 is relatively high. This effect improves the mechanical and anti-aging properties of the rehabilitated asphalt as compared to an original polymer-modified asphalt mix with a similar concentration of polymer.
  • a layer 14 of rehabilitant forms on the outside of the aggregate particles.
  • Layer 14 provides a rehabilitant-enriched zone with mechanical and chemical stability much better than those of even polymer-modified bitumen.
  • bitumen layer 12 is covered by layer 14, it has no direct contact with oxygen and humidity, which slows down the bitumen oxidation processes.
  • a further embodiment of the present invention is a composition for rehabilitating used asphalt mixes (hereinafter "rehabilitant") comprising porcelanite, an activating agent and a polymer.
  • rehabilitant a composition for rehabilitating used asphalt mixes
  • Preferable examples of the activating agent and polymer are described hereinabove with reference to the process for rehabilitating used asphalt mixes.
  • the weight of the activating agent in the rehabilitant is preferably between 3 and 20% of the porcelanite weight. More preferably, the weight of the activating agent in the rehabilitant is between 10 and 15% of the porcelanite weight.
  • the ratio of polymer to activated porcelanite in the rehabilitant is preferably about 1:10 - 10:1, more preferably about 1:3 - 1:1, most preferably about 1:2.
  • the present invention provides, in addition to the rehabilitation of used asphalt, the possibility to impart to the used asphalt new properties, specific for high-grade polymer-modified asphalts.
  • Mechanical and aging properties of the asphalt, rehabilitated by the process of the invention, are even better than those of standard polymer-modified asphalts.

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Health & Medical Sciences (AREA)
  • Civil Engineering (AREA)
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Abstract

A process for rehabilitating used asphalt is provided. The process involves mixing the used asphalt with a novel rehabilitating agent comprising the mineral porcelanite, an activating agent and a polymer. The process restores the elastic properties of asphalt and provides a rejuvenated asphalt with superior stability relative to asphalt rejuvenated with traditional rejuvenating agents.

Description

PROCESS FOR RECYCLING ASPHALT MIXES
CROSS-REFERENCE TO RELATED APPLICATIONS
Reference is made to U.S. Provisional Patent Application Serial No. 61/489,338, filed May 24, 2011 and entitled PROCESS FOR RECYCLING ASPHALT MIXES, the disclosure of which is hereby incorporated by reference and priority of which is hereby claimed pursuant to 37 CFR 1.78(a)(4) and (5)(i).
FIELD OF THE INVENTION
The present invention relates to a process for recycling used asphalt mixes using a novel rehabilitant.
BACKGROUND OF THE INVENTION
The following publications are believed to represent the current state of the art:
U.S. Patent Nos. 6,769,836, 7,503,202, 7,811,372, 7,838,575; and Basic Asphalt Recycling Manual, Asphalt Recycling and Reclaming Association (Annapolis, MD, USA), 2001.
SUMMARY OF THE INVENTION
The present invention seeks to provide a process for recycling used asphalt mixes using a novel rehabilitating agent.
Accordingly, there is provided in accordance with one embodiment of the present invention a process for rehabilitating a used asphalt mix including: combining porcelanite, an activating agent and a polymer to form a rehabilitant; and mixing the rehabilitant with the used asphalt mix at a temperature of at least about 140 °C.
Preferably, the activating agent includes a quaternary ammonium compound. The quaternary ammonium compound preferably includes at least two alkyl chains of 10 - 30 carbons, more preferably 15 - 18 carbons. Most preferably, the quaternary ammonium compound is di(hydrogenated tallow)dimethylammonium chloride.
In accordance with a preferred embodiment of the present invention, the rehabilitant includes the activating agent in an amount of 3 - 20% of the porcelanite weight. More preferably, the rehabilitant includes the activating agent in an amount of 10 - 15% of the porcelanite weight.
Preferably, the polymer is a thermoplastic polymer. The thermoplastic polymer is preferably selected from polyethylene, polypropylene, EPDM rubber, styrene- butadiene-styrene copolymer and ethylene-vinyl acetate copolymer. Most preferably, the polymer is selected from styrene-butadiene-styrene copolymer and ethylene-vinyl acetate copolymer.
In accordance with a preferred embodiment of the present invention, the ratio of the weight of the polymer to the combined weight of the porcelanite and the activating agent in the rehabilitant is from about 1:10 to about 10:1. More preferably, the ratio is from about 1:3 to about 1:1, and most preferably about 1:2.
Preferably, the combining includes: blending the porcelanite with the activating agent to form an activated porcelanite, mixing the activated porcelanite with the polymer in an extruder at a temperature of about 100 °C to about 250 °C to form an extruded mixture; and granulating the extruded mixture. More preferably, the mixing the activated porcelanite with the polymer is at a temperature of about 100 °C to about 160 °C. The granulating preferably produces granules of about 3 - 5 mm. In accordance with a preferred embodiment of the present invention, the mixing the rehabilitant with the used asphalt mix is carried out on the surface where the used asphalt is laid. In accordance with an alternative embodiment of the present invention, the mixing the rehabilitant with the used asphalt mix is carried out in an asphalt plant. The mixing is preferably carried out at about 140 - 190 °C, more preferably about 150 °C.
There is provided in accordance with an additional embodiment of the present invention a composition for rehabilitating a used asphalt mix including: porcelanite, an activating agent and a polymer.
Preferably, the activating agent includes a quaternary ammonium compound. The quaternary ammonium compound preferably includes at least two alkyl chains of 10 - 30 carbons, more preferably 15 - 18 carbons. Most preferably, the quaternary ammonium compound is di(hydrogenated tallow)dimethylammonium chloride.
In accordance with a preferred embodiment of the present invention, the rehabilitant includes the activating agent in an amount of 3 - 20% of the porcelanite weight. More preferably, the rehabilitant includes the activating agent in an amount of 10 - 15% of the porcelanite weight.
Preferably, the polymer is a thermoplastic polymer. The thermoplastic polymer is preferably selected from polyethylene, polypropylene, EPDM rubber, styrene- butadiene-styrene copolymer and ethylene-vinyl acetate copolymer. Most preferably, the polymer is selected from styrene-butadiene-styrene copolymer and ethylene-vinyl acetate copolymer.
In accordance with a preferred embodiment of the present invention, the ratio of the weight of the polymer to the combined weight of the porcelanite and the activating agent in the rehabilitant is from about 1:10 to about 10:1. More preferably, the ratio is from about 1:3 to about 1:1, and most preferably about 1:2.
BRIEF DESCRIPTION OF THE DRAWING
The present invention will be understood and appreciated more fully from the following detailed description, taken in conjunction with the drawing in which:
Fig. 1 is a simplified diagram of the structure of particles of an asphalt mix recycled according to the process of the present invention. DETAILED DESCRIPTION OF THE INVENTION
Hot recycling of used asphalt mixes is very widely used in the practice of pavement rehabilitation. Asphalt, once laid on a road surface, typically lasts for about 10-15 years, during which time it is exposed to oxygen, moisture and UV radiation from the sun. Due to oxidation and aging resulting from such exposure, the bitumen in the asphalt becomes brittle and loses its elastomeric properties that are required for asphalt pavements. It is desirable to recycle used asphalt rather than dispose of it in order to reduce costs and environmental impact.
The most common technique for renewing used asphalt is to add a maltenic petroleum fraction to the used asphalt. Maltenic fractions are aromatic extracts from the heavy distillate fraction of crude oil and are characterized by the following properties: viscosity at 100°C 7-12 cSt, density at 15°C 0.96-0.99, pour point 15°C - 21°C. The maltenic aromatic compounds in asphalt bitumen are destroyed by oxidation and aging. This causes the bitumen to become brittle and no longer suitable for road use. The added maltenic fraction restores the lost elastomeric properties of bitumen.
In a typical recycling process, the maltenic fraction or its dispersion in water and the heated oxidized asphalt are mixed and intensively agitated together. During this process, maltenic oils penetrate into the old bitumen structures and soften them. The short mixing time characteristic of asphalt production and the very high viscosity of old bitumen both retard this process.
One of the drawbacks of this method is that the maltenic oils do not penetrate the used asphalt uniformly. Bitumen structures located close to the surface of the asphalt particles are softened too much by a portion of the oils, while the residual oils remain on the surface and lubricate the particles. The resulting asphalt mix acquires the desired elasto-plastomeric properties but has low mechanical stability. Additionally, since the added fraction consists of fast-oxidizing aromatics, the recycled asphalt mix is as susceptible to oxidation and aging as was the original asphalt.
Polymer-modified asphalt mixes usually have much better mechanical stability and elasticity and also age slower than unmodified asphalt mixes. The polymer modifiers, such as styrene-butadiene-styrene (SBS) and ethylene-vinyl acetate (EVA) block copolymers, are added to bitumen and form three-dimensional networks inside the W
continuous bitumen phase. Typical concentrations of polymer in the bitumen are 3-6% by weight. Although the polymers modify the mechanical properties of bitumen and reduce the effects of bitumen aging, the bitumen is nonetheless still exposed to oxygen, moisture and UV radiation.
A composition for lowering the mixing temperature of stone matrix asphalt (SMA) and other asphalt mixes to about 165 °C is disclosed in WO 2010/116354, assigned to the assignee of the present invention and incorporated by reference herein in its entirety. It has now been found that this relatively inexpensive composition, can be used as part of an asphalt rehabilitating composition.
A first embodiment of the present invention is a process for rehabilitating used asphalt mixes comprising:
forming a composition (hereinafter "rehabilitant") comprising porcelanite, an activating agent and a polymer; and
mixing the rehabilitant with a used asphalt mix at high temperature.
Porcelanite is a mineral found, inter alia, in deposits in the Dead Sea area of Israel and is described in detail in WO 2010/116354. In one preferred embodiment, the activating agent is a quaternary ammonium compound.
The quaternary ammonium compound preferably has at least two long carbon chains. The long carbon chains preferably comprise between 10 and 30 carbon atoms, more preferably from 15 to 18 carbon atoms. An especially preferred compound is di(hydrogenated tallow)dimethylammonium chloride, available from Akzo-Nobel (Stockholm, Sweden) as Arquad 2HT-75 (hereinafter "2HT-75").
Activation of the porcelanite is preferably achieved by crushing the porcelanite to about 3 - 8 mm particle size granules, adding the activating agent, and blending the mixture until the desired particle size is achieved. Alternatively, the porcelanite can be blended for about 5 minutes, followed by addition of the activating agent and further blending for an additional 1 - 5 minutes.
The weight of the activating agent in the rehabilitant is preferably between about 3 and 20% of the porcelanite weight. More preferably, the weight of the activating agent in the rehabilitant is between about 10 and 15% of the porcelanite weight.
The polymer is preferably a thermoplastic polymer. Preferable examples of the thermoplastic polymer include polyethylene, polypropylene, EPDM rubber, styrene- W
butadiene-styrene copolymer and ethylene-vinyl acetate copolymer. The ratio of polymer to activated porcelanite in the rehabilitant is preferably about 1:10 - 10:1, more preferably about 1:3 - 1:1, and most preferably about 1:2.
The rehabilitant is preferably formed by mixing the activated porcelanite with the polymer in an extruder at a temperature above the softening point of the polymer, typically about 100 - 250 °C and more preferably about 100 - 160 °C. The extruded mixture is then granulated and cooled. The granule size is preferably about 3 - 5 mm.
The rehabilitant is preferably mixed with used asphalt at a temperature of at least about 140 °C. The mixing of the rehabilitant with the used asphalt can be performed in accordance with a method described in Basic Asphalt Recycling Manual, Asphalt Recycling and Reclaiming Association (Annapolis, MD, USA), 2001, hereby incorporated by reference herein in its entirety.
In accordance with one embodiment of the present invention, the rehabilitant is mixed with the used asphalt using hot in-place recycling (HIR) technology, wherein 100% recycling of the existed asphalt pavement is completed on site. In this method, the existing asphalt pavement is heated to about 140 - 190 °C, preferably about 150 °C, and softened, permitting it to be scarified or hot rotary milled to a specified depth. The scarified or loosened asphalt pavement is then mixed, placed and compacted with conventional equipment. New aggregate, new asphalt binder, recycling agents and/or new asphalt mix can be added on an as-required basis.
In an alternative embodiment, the recycling process is carried out in an asphalt plant. The used asphalt is crushed to a size suitable for use as aggregates for asphalt mixes, typically less than 5 cm. Rehabilitant is mixed with the crushed asphalt at a temperature of about 140 - 190 °C, preferably about 150 °C.
The rehabilitant is preferably added to the asphalt in an amount of about 1 - 10% of the asphalt weight, more preferably about 3 - 6% of the asphalt weight. The mixing time is preferably about 50 - 80 sec, more preferably about 60 seconds.
The rehabilitated asphalt can be prepared in a batch or continuous process. After production, the hot rehabilitated asphalt can be loaded into trucks for delivery to a worksite, or stored in a hot storage facility.
The asphalt rehabilitated according to the present invention has superior properties relative to asphalt rehabilitated according to previously known methods and even relative to original asphalt mixes. When asphalt mixes are produced, a portion of bitumen is absorbed into the aggregate particle, while the balance remains on the surface of the particles. It is this surface bitumen which oxidizes and hardens during the lifetime of the asphalt on the road.
Reference is now made to Fig. 1, which demonstrates the distribution of layers in a particle 2 of asphalt after rehabilitation. Due to the high viscosities of both the bitumen in the used asphalt mix and the rehabilitant, the rehabilitant does not penetrate through the entire thickness of the surface bitumen layer.
A layer 4 of old bitumen, absorbed by an outer layer of aggregates 6, stays unchanged. A layer 8 of oxidized bitumen located close to the stone surface 10 also stays unchanged due to its very high viscosity. Both of these layers provide high adhesion between the aggregate stones and the old oxidized bitumen.
The rehabilitant penetrates into an outer bitumen layer 12, which obtains visco- elastic properties similar to those of polymer-modified bitumen. As only a part of the bitumen is mixed with the rehabilitant, the concentration of the rehabilitant in outer bitumen layer 12 is relatively high. This effect improves the mechanical and anti-aging properties of the rehabilitated asphalt as compared to an original polymer-modified asphalt mix with a similar concentration of polymer.
Additionally, since it is difficult for the rehabilitant to penetrate into the oxidized bitumen, a layer 14 of rehabilitant forms on the outside of the aggregate particles. Layer 14 provides a rehabilitant-enriched zone with mechanical and chemical stability much better than those of even polymer-modified bitumen. Furthermore, since bitumen layer 12 is covered by layer 14, it has no direct contact with oxygen and humidity, which slows down the bitumen oxidation processes.
A further embodiment of the present invention is a composition for rehabilitating used asphalt mixes (hereinafter "rehabilitant") comprising porcelanite, an activating agent and a polymer. Preferable examples of the activating agent and polymer are described hereinabove with reference to the process for rehabilitating used asphalt mixes.
The weight of the activating agent in the rehabilitant is preferably between 3 and 20% of the porcelanite weight. More preferably, the weight of the activating agent in the rehabilitant is between 10 and 15% of the porcelanite weight. The ratio of polymer to activated porcelanite in the rehabilitant is preferably about 1:10 - 10:1, more preferably about 1:3 - 1:1, most preferably about 1:2.
The present invention provides, in addition to the rehabilitation of used asphalt, the possibility to impart to the used asphalt new properties, specific for high-grade polymer-modified asphalts. Mechanical and aging properties of the asphalt, rehabilitated by the process of the invention, are even better than those of standard polymer-modified asphalts.
It will be appreciated by persons skilled in the art that the present invention is not limited to what has been particularly shown and described hereinabove. Rather the scope of the present invention includes both combinations and subcombinations of various features described hereinabove as well as modifications thereof which would occur to a person of skill in the art upon reading the foregoing description and which are not in the prior art.

Claims

1. A process for rehabilitating a used asphalt mix comprising:
combining porcelanite, an activating agent and a polymer to form a rehabilitant; and
mixing said rehabilitant with said used asphalt mix at a temperature of at least about 140 °C.
2. The process according to claim 1, wherein said activating agent comprises a quaternary ammonium compound.
3. The process according to claim 2, wherein said quaternary ammonium compound comprises at least two alkyl chains of 10 - 30 carbons.
4. The process according to claim 3, wherein said at least two alkyl chains have 15— 18 carbons.
5. The process according to any one of claims 2 to 4, wherein said quaternary ammonium compound is di(hydrogenated tallow)dimethylammonium chloride.
6. The process according to any one of claims 1 to 5, wherein said rehabilitant comprises said activating agent in an amount of 3 - 20% of the porcelanite weight.
7. The process according to claim 6, wherein said rehabilitant comprises said activating agent in an amount of 10 - 15% of the porcelanite weight.
8. The process according to any one of claims 1 to 7, wherein said polymer is a thermoplastic polymer.
9. The process according to claim 8, wherein said thermoplastic polymer is selected from polyethylene, polypropylene, EPDM rubber, styrene-butadiene-styrene copolymer and ethylene-vinyl acetate copolymer.
10. The process according to claim 9, wherein said polymer is selected from styrene-butadiene-styrene copolymer and ethylene-vinyl acetate copolymer.
11. The process according to any one of claims 1 to 10, wherein the ratio of the weight of said polymer to the combined weight of said porcelanite and said activating agent in said rehabilitant is from about 1:10 to about 10:1.
12. The process according to claim 11, wherein the ratio of the weight of said polymer to the combined weight of said porcelanite and said activating agent in said rehabilitant is from about 1:3 to about 1:1.
13. The process according to claim 12, wherein the ratio of the weight of said polymer to the combined weight of said porcelanite and said activating agent in said rehabilitant is about 1:2.
14. The process according to any one of claims 1 to 13, wherein said combining comprises:
blending said porcelanite with said activating agent to form an activated porcelanite,
mixing said activated porcelanite with said polymer in an extruder at a temperature of about 100 °C to about 250 °C to form an extruded mixture; and
granulating said extruded mixture.
15. The process according to claim 14, wherein said mixing said activated porcelanite with said polymer is at a temperature of about 100 °C to about 160 °C.
16. The process according to claim 14 or 15, wherein said granulating produces granules of about 3 - 5 mm.
17. The process according to any one of claims 1 to 16, wherein said mixing said rehabilitant with said used asphalt mix is carried out on the surface where the used asphalt is laid.
18. The process according to any one of claims 1 to 16, wherein said mixing said rehabilitant with said used asphalt mix is carried out in an asphalt plant.
19. The process according to any one of claims 1 to 18, wherein said mixing said rehabilitant with said used asphalt mix is carried out at about 140 - 190 °C.
20. The process according to claim 19, wherein said mixing said rehabilitant with said used asphalt mix is carried out at about 150 °C.
21. A composition for rehabilitating a used asphalt mix comprising:
porcelanite;
an activating agent; and
a polymer.
22. The composition according to claim 21, wherein said activating agent comprises a quaternary ammonium compound.
23. The composition according to claim 22, wherein said quaternary ammonium compound comprises at least two alkyl chains of 10 - 30 carbons.
24. The composition according to claim 23, wherein said at least two alkyl chains have 15 - 18 carbons.
25. The composition according to any one of claims 22 to 24, wherein said quaternary ammonium compound is di(hydrogenated tallow)dimethylammonium chloride.
26. The composition according to any one of claims 21 to 25, wherein said rehabilitant comprises said activating agent in an amount of 3 - 20% of the porcelanite weight.
27. The composition according to claim 26, wherein said rehabilitant comprises said activating agent in an amount of 10 - 15% of the porcelanite weight.
28. The composition according to any one of claims 21 to 27, wherein said polymer is a thermoplastic polymer.
29. The composition according to claim 28, wherein said thermoplastic polymer is selected from polyethylene, polypropylene, EPDM rubber, styrene- butadiene-styrene copolymer and ethylene-vinyl acetate copolymer.
30. The composition according to claim 29, wherein said polymer is selected from styrene-butadiene-styrene copolymer and ethylene-vinyl acetate copolymer.
31. The composition according to any one of claims 21 to 30, wherein the ratio of the weight of said polymer to the combined weight of said porcelanite and said activating agent in said rehabilitant is from about 1:10 to about 10:1.
32. The composition according to claim 31, wherein the ratio of the weight of said polymer to the combined weight of said porcelanite and said activating agent in said rehabilitant is from about 1:3 to about 1:1.
33. The composition according to claim 32, wherein the ratio of the weight of said polymer to the combined weight of said porcelanite and said activating agent in said rehabilitant is about 1:2.
PCT/IL2012/000206 2011-05-24 2012-05-24 Process for recycling asphalt mixes WO2012160555A1 (en)

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