WO2021003541A1 - Process of agglomeration by coacervation of vulcanized rubber powder and resulting product - Google Patents
Process of agglomeration by coacervation of vulcanized rubber powder and resulting product Download PDFInfo
- Publication number
- WO2021003541A1 WO2021003541A1 PCT/BR2019/050269 BR2019050269W WO2021003541A1 WO 2021003541 A1 WO2021003541 A1 WO 2021003541A1 BR 2019050269 W BR2019050269 W BR 2019050269W WO 2021003541 A1 WO2021003541 A1 WO 2021003541A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- rubber powder
- camelback
- coacervation
- agglomeration
- product
- Prior art date
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B28—WORKING CEMENT, CLAY, OR STONE
- B28B—SHAPING CLAY OR OTHER CERAMIC COMPOSITIONS; SHAPING SLAG; SHAPING MIXTURES CONTAINING CEMENTITIOUS MATERIAL, e.g. PLASTER
- B28B17/00—Details of, or accessories for, apparatus for shaping the material; Auxiliary measures taken in connection with such shaping
- B28B17/04—Exhausting or laying dust
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B11/00—Making preforms
- B29B11/06—Making preforms by moulding the material
- B29B11/12—Compression moulding
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B17/00—Recovery of plastics or other constituents of waste material containing plastics
- B29B17/02—Separating plastics from other materials
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/30—Mixing; Kneading continuous, with mechanical mixing or kneading devices
- B29B7/34—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices
- B29B7/38—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary
- B29B7/40—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with single shaft
- B29B7/42—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with single shaft with screw or helix
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B60—VEHICLES IN GENERAL
- B60C—VEHICLE TYRES; TYRE INFLATION; TYRE CHANGING; CONNECTING VALVES TO INFLATABLE ELASTIC BODIES IN GENERAL; DEVICES OR ARRANGEMENTS RELATED TO TYRES
- B60C1/00—Tyres characterised by the chemical composition or the physical arrangement or mixture of the composition
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08C—TREATMENT OR CHEMICAL MODIFICATION OF RUBBERS
- C08C4/00—Treatment of rubber before vulcanisation, not provided for in groups C08C1/00 - C08C3/02
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J3/00—Processes of treating or compounding macromolecular substances
- C08J3/12—Powdering or granulating
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L17/00—Compositions of reclaimed rubber
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L53/00—Compositions 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
- C08L53/02—Compositions 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
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/52—Mechanical processing of waste for the recovery of materials, e.g. crushing, shredding, separation or disassembly
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/62—Plastics recycling; Rubber recycling
Definitions
- the present invention describes an agglomeration process by coacervation of vulcanized rubber powder and resulting product. More specifically, it comprises a process for recycling scraps or vulcanized rubber scraps resulting from the process of manufacturing tread or recycling old tires, and this process does not regenerate, but seeks to preserve the good properties of camelback to the maximum by using of the rubber powder in a suitable granulometry and through the use of an agglomerating product added by coacervant polymer.
- This agglomeration process aims to obtain a product that preserves the properties of the agglomerated material as much as possible, avoiding the use of high temperatures (> 70 ° C), depolymerizing processes or that physically-chemically alter the good quality of the agglomerated material, in order to facilitate handling in the usual processes without the need for process aids to avoid blocking or excessive adhesion to the walls of the equipment used in the production process.
- the recycling process developed standardizes the granulometry of comminuted rubber (mechanical or cryogenic micronization) preserving the original properties without chemical or thermal treatment, without generating effluents, fumes or residues.
- the treadmill production plants end up generating various residues (scraps, refuse, burrs and others) resulting from the manufacturing process, which are discarded or directed to recycling, generating an environmental liability that is difficult to solve due to material characteristics and the high cost for correct recycling.
- the current recycling process and reuse of these materials is usually carried out by separating vulcanized rubber from other components (such as metals and fabrics), so that the materials (tires, scraps and scraps) are cut into chips and classified by a sieve system.
- the chips are ground and then subjected to autoclave digestion with chemicals, such as: dixylil disulfide and mineral oils, to devulcanize them.
- the product obtained can then be refined in mills until obtaining the regenerated, rubber with compromised properties and an unpleasant odor, producing fetid, effluent fumes highly contaminated with a difficult and costly treatment process and residues resulting from this process.
- the document IT201 1AN0150 describes a method of producing a compound for making bitumen modified for asphalts is disclosed, comprising the following steps: grinding of vulcanized rubber to obtain vulcanized granulated rubber with a particle size of less than 0.4 mm mixture of said fragmented vulcanized rubber, SBS and lubricant in the extruder, where the percentage by weight of lubricant is comprised between 1% and 50% in comparison with the weight of the mixture and the vulcanized fragmented rubber in percentage by weight of 70-100% in comparison with the weight of SBS in order to obtain an extruded compound containing the said vulcanized fragmented rubber, SBS and lubricant.
- the present inventor developed an agglomeration process that uses an asphalt with SBS (binder) and tire rubber powder with a particle size equal to or greater than 24 mesh, obtained cryogenically or mechanically.
- the rubber powder is treated with the binder cold and without any other product in the ratio of 1 to 3, that is, 1 portion of binder to 3 of rubber powder, so that the resulting product obtained is used as an additive for manufacturing new tires and / or to generate new products.
- the process is purely mechanical, does not use other products or heating, and does not produce effluents, fumes or waste.
- the object of the present invention is a process of agglomeration by coacervation of vulcanized rubber powder due to the process of manufacturing tread and recycling old tires, this process does not regenerate, but seeks to preserve as much as possible the good properties of the camelback through the use of rubber powder in an appropriate size and through the use of a agglomerating product added with coacervant polymer.
- This agglomeration process aims to obtain a product that preserves the properties of the agglomerated material as much as possible, avoiding the use of high temperatures (> 70 ° C), depolymerization processes or that physically-chemically alter the good quality of the agglomerated material, in order to facilitate handling in the usual processes without the need for process aids to avoid blocking or excessive adhesion to the walls of the equipment used in the production process.
- the recycling process developed standardizes the granulometry of comminuted rubber (mechanical or cryogenic micronization) preserving the original properties without chemical or thermal treatment, without generating effluents, fumes or residues. Resulting in a final product that preserves the quality of scraps and scraps to the maximum, being able to be added to new compounds as a highly compatible additive due to the preservation of the characteristics and properties of the camelback.
- a characteristic of the present invention is a process of agglomeration by coacervation of vulcanized rubber powder and resulting product that provides the use of asphalt added with SBS and tire rubber powder with a granulometry equal to and greater than 24 mesh, obtained cryogenically or mechanically.
- a characteristic of the present invention is a process of agglomeration by coacervation of vulcanized rubber powder and the resulting product that provides a process is to obtain a recycle that can be added in high dosage without appreciably changing the characteristic properties of the camelback.
- a characteristic of the present invention is a process of agglomeration by coacervation of vulcanized rubber powder and the resulting product that provides elastoplastic polymer at rest, showing significant shrinkage or shrinkage that eliminates the air trapped in the core of the agglomerate with which the powder becomes integral. of the cluster.
- a characteristic of the present invention is a process of agglomeration by coacervation of vulcanized rubber powder and the resulting product that provides a mixture of SBR rubber powder with SBS is 100% compatible.
- a characteristic of the present invention is a process of agglomeration by coacervation of vulcanized rubber powder and resulting product that provides a camelback rubber powder with a particle size of less than 24 mesh which maintains the primary characteristics of the tailings derived from the banding process tire tread or recycling old tires.
- a characteristic of the present invention is a process of agglomeration by coacervation of vulcanized rubber powder and the resulting product that provides a final yield, then it is 1.5 kg of binder for 3 kg of camelback rubber powder.
- the agglomeration process by coacervation of vulcanized rubber powder and the resulting product describes an agglomeration process that uses asphalt with SBS and tire rubber powder with a grain size equal to and greater than 24 mesh, obtained cryogenically or mechanically, which can either be produced in the same plant or purchased from third parties.
- Camelback means the vulcanized synthetic rubber compound of SBR (synthetic copolymer of styrene-butadiene emulsion) reinforced with carbon black in sufficient quantity to reach the standard hardness of 63 + - 1 Shore A, measured according to with the ASTM D 2240 standard, using shore A measured durometer.
- the density of the standard camelback compound is 1.15 g / cm 3 and the tensile strength is 15 + - MPa.
- Step 1 mixing in cold compatibilizer
- the binder used in camelback rubber powder is oxidized asphalt (free from volatiles) and added with SBS polymer (75% styrene - butadiene (25%).
- the binder is produced by petrochemical industries at the end of the oil residue, which receives an oxidative treatment to eliminate or chemically modify light fractions.
- the material is added with a percentage of elastoplastic polymer to improve the physical-chemical properties of the binder. Resulting in a dark, thermoplastic product with high tensile strength, not friable, nor brittle under impact.
- the compatibilizing mixture is made cold in usual equipment, such as: closed mixer (bambury) or open mixer (cylinder or refiner), where the SBR rubber powder (camelback) is mixed with asphalt added with SBS, in proportion from 1 to 3 of binder in relation to the rubber powder.
- closed mixer bambury
- open mixer cylinder or refiner
- SBR rubber powder camelback
- asphalt added with SBS asphalt added with SBS
- the elastoplastic polymer at rest shows significant shrinkage or shrinkage that eliminates the air trapped in the core of the agglomerate, with which the powder becomes part of the agglomerate.
- SBR rubber powder The particles of vulcanized rubber (SBR rubber powder) are surrounded by the SBS molecules and the product retracts involving the SBR particles (rubber powder) with an asphalt film containing SBS highly compatible with SBR.
- Step 2 Finish cold plate to form
- the agglomeration process is completed with the addition of an additional 50% of agglomerate (oxidized asphalt added with SBS polymer). This provides for the formation of a blanket by compression between the cylinders of the open mixer in such a way that the material agglomerates and loosens from the walls of the mixing equipment.
- the final yield is then a ratio of 1.5 binder to 3 rubber powder ie 1.5 binder to 3 SBR rubber powder.
- This material can be cured by adding curing agents or it can be used as an additive in new compositions. Dosing is at the discretion of the formulator who can dose according to the specification of the product to be manufactured.
- the binder used is a special asphalt that is oxidized to eliminate undesirable components and added with a minimum percentage of polymer compatible with the powder used.
- the rubber powder - SBR is made with an elastomer that contains 25% styrene and 75% butadiene.
- the polymer added to the asphalt to agglomerate the SBR powder is SBS which contains 25% butadiene and 75% styrene. So the mixture of SBR rubber powder with SBS is 100% compatible.
- the process does not use high temperature or regenerating substances to prevent the formation of 'mercaptan' responsible for toxic and smelly fumes.
- the agglomeration process uses an agglomerating product added by coacervant polymer. Additive with thermoplastic polymer with high dimensional recovery power to make the product agglomerate and coacervant so that the vulcanized rubber reduced to powder is mechanically fixed and compacted by coacervation which is evident through the formation of laminates.
- the agglomeration process has the following steps:
- the material goes to micronization, which can be done mechanically by grinding, grinding or by cryometry, for particles with a particle size smaller than 24 mesh (mesh ⁇ 24 #);
- cryometric micronization is performed at low temperature ( ⁇ 70 ° C) and does not compromise the good quality of the camelback, considering what the ASTM D 2000 standard establishes for the camelback, temperature in the heat resistance test carried out according to ASTM D 573 - 70h at 70 ° C;
- the resulting rubber powder is mixed with the cold binder in usual equipment, such as: closed mixer (bambury) or open mixer (cylinder or refiner);
- the SBR rubber powder (camelback) is mixed with oxidized asphalt and reinforced with approximately 15% of SBS elastoplastic (styrene - butadiene - styrene) forming the binder that allows to obtain a product of assured quality, as long as the standard dosage is maintained : 3 kg of camelback rubber powder for 1 kg of binder;
- the material is left to stand for some time until it has cooled down so that the coacervation reactions can occur;
- the vulcanized rubber particles SBR rubber powder
- the agglomeration process is completed with the addition of an additional 50% agglomerant (oxidized asphalt added with reinforcing SBS polymer);
- the agglomerated material can be vulcanized simply by adding the curing agents and doing the heat treatment to obtain the cure.
- the agglomerate can be used as an additive at the discretion of the formulator who can dose according to the specification of the product to be manufactured either as rubber in new compositions of camelback or other uses such as: floors, carpets, casters and the like.
- the agglomeration process does not use temperatures above 70 ° C, does not add process aids, regenerating agents or any other product that could compromise the good quality of the material to be agglomerated.
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Ceramic Engineering (AREA)
- General Chemical & Material Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
Abstract
Description
Claims
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PCT/BR2019/050269 WO2021003541A1 (en) | 2019-07-11 | 2019-07-11 | Process of agglomeration by coacervation of vulcanized rubber powder and resulting product |
BR112022000504A BR112022000504A2 (en) | 2019-07-11 | 2019-07-11 | Agglomeration process by coacervation of vulcanized rubber powder and resulting product |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PCT/BR2019/050269 WO2021003541A1 (en) | 2019-07-11 | 2019-07-11 | Process of agglomeration by coacervation of vulcanized rubber powder and resulting product |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2021003541A1 true WO2021003541A1 (en) | 2021-01-14 |
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ID=74113514
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/BR2019/050269 WO2021003541A1 (en) | 2019-07-11 | 2019-07-11 | Process of agglomeration by coacervation of vulcanized rubber powder and resulting product |
Country Status (2)
Country | Link |
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BR (1) | BR112022000504A2 (en) |
WO (1) | WO2021003541A1 (en) |
Citations (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB445591A (en) * | 1934-12-22 | 1936-04-15 | Martinus Joaennes Stam | Improvements in the manufacture of rubber products |
US2239659A (en) * | 1936-12-10 | 1941-04-22 | Firestone Tire & Rubber Co | Art of treating rubber |
US3290268A (en) * | 1964-11-16 | 1966-12-06 | Phillips Petroleum Co | Rubber masterbatching |
US4511679A (en) * | 1982-12-21 | 1985-04-16 | Toyo Soda Manufacturing Co., Ltd. | Process for preparing a rubber-asphalt composition |
US4599370A (en) * | 1984-12-06 | 1986-07-08 | Plastic Specialties And Technologies, Inc. | Powdered elastomer dry blends and process for injection molding |
BR0314190A (en) * | 2002-09-10 | 2005-07-26 | Schill & Seilacher | Microcapsules for rubber production and method for producing these |
JP2007126518A (en) * | 2005-11-01 | 2007-05-24 | Bridgestone Corp | Reclaimed rubber-containing rubber composition and pneumatic tire |
CN101955671A (en) * | 2010-09-17 | 2011-01-26 | 天津海泰环保科技发展有限公司 | Continuous feeding system for dispersion and accurate measurement of powder for production of rubber powder modified asphalt |
CN102070789A (en) * | 2009-11-25 | 2011-05-25 | 中国石油天然气股份有限公司 | Preparation method of powdered rubber |
CN107474464A (en) * | 2016-06-07 | 2017-12-15 | 中国石油化工股份有限公司 | A kind of polymerized conjugated diene/SBS compounded rubber particles and preparation method thereof and application of the compounded rubber particle in modified pitch |
CN107696334A (en) * | 2017-11-07 | 2018-02-16 | 成都新柯力化工科技有限公司 | A kind of ecological, environmental protective reclaims method of the rubber system for ultra-fine rubber powder |
CN108102281A (en) * | 2018-01-09 | 2018-06-01 | 中昊黑元化工研究设计院有限公司 | A kind of asphalt modifier and preparation method thereof |
-
2019
- 2019-07-11 BR BR112022000504A patent/BR112022000504A2/en not_active Application Discontinuation
- 2019-07-11 WO PCT/BR2019/050269 patent/WO2021003541A1/en active Application Filing
Patent Citations (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB445591A (en) * | 1934-12-22 | 1936-04-15 | Martinus Joaennes Stam | Improvements in the manufacture of rubber products |
US2239659A (en) * | 1936-12-10 | 1941-04-22 | Firestone Tire & Rubber Co | Art of treating rubber |
US3290268A (en) * | 1964-11-16 | 1966-12-06 | Phillips Petroleum Co | Rubber masterbatching |
US4511679A (en) * | 1982-12-21 | 1985-04-16 | Toyo Soda Manufacturing Co., Ltd. | Process for preparing a rubber-asphalt composition |
US4599370A (en) * | 1984-12-06 | 1986-07-08 | Plastic Specialties And Technologies, Inc. | Powdered elastomer dry blends and process for injection molding |
BR0314190A (en) * | 2002-09-10 | 2005-07-26 | Schill & Seilacher | Microcapsules for rubber production and method for producing these |
JP2007126518A (en) * | 2005-11-01 | 2007-05-24 | Bridgestone Corp | Reclaimed rubber-containing rubber composition and pneumatic tire |
CN102070789A (en) * | 2009-11-25 | 2011-05-25 | 中国石油天然气股份有限公司 | Preparation method of powdered rubber |
CN101955671A (en) * | 2010-09-17 | 2011-01-26 | 天津海泰环保科技发展有限公司 | Continuous feeding system for dispersion and accurate measurement of powder for production of rubber powder modified asphalt |
CN107474464A (en) * | 2016-06-07 | 2017-12-15 | 中国石油化工股份有限公司 | A kind of polymerized conjugated diene/SBS compounded rubber particles and preparation method thereof and application of the compounded rubber particle in modified pitch |
CN107696334A (en) * | 2017-11-07 | 2018-02-16 | 成都新柯力化工科技有限公司 | A kind of ecological, environmental protective reclaims method of the rubber system for ultra-fine rubber powder |
CN108102281A (en) * | 2018-01-09 | 2018-06-01 | 中昊黑元化工研究设计院有限公司 | A kind of asphalt modifier and preparation method thereof |
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BR112022000504A2 (en) | 2022-03-15 |
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