Classifications

• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L21/00—Compositions of unspecified rubbers
• • 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
• • 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
  • C08J11/00—Recovery or working-up of waste materials
  • C08J11/04—Recovery or working-up of waste materials of polymers
  • C08J11/06—Recovery or working-up of waste materials of polymers without chemical reactions
• • 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
  • C08J3/005—Processes for mixing polymers
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L1/00—Compositions of cellulose, modified cellulose or cellulose derivatives
  • C08L1/08—Cellulose derivatives
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L19/00—Compositions of rubbers not provided for in groups C08L7/00 - C08L17/00
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L19/00—Compositions of rubbers not provided for in groups C08L7/00 - C08L17/00
  • C08L19/003—Precrosslinked rubber; Scrap rubber; Used vulcanised rubber
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L27/00—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers
  • C08L27/02—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers not modified by chemical after-treatment
  • C08L27/04—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers not modified by chemical after-treatment containing chlorine atoms
  • C08L27/06—Homopolymers or copolymers of vinyl chloride
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L67/00—Compositions of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Compositions of derivatives of such polymers
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L77/00—Compositions of polyamides obtained by reactions forming a carboxylic amide link in the main chain; Compositions of derivatives of such polymers
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L95/00—Compositions of bituminous materials, e.g. asphalt, tar, pitch
• • 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
  • C08J2300/00—Characterised by the use of unspecified polymers
  • C08J2300/30—Polymeric waste or recycled polymer
• • 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
  • C08J2319/00—Characterised by the use of rubbers not provided for in groups C08J2307/00 - C08J2317/00
• • 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
  • C08J2321/00—Characterised by the use of unspecified rubbers
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
  • C08K7/00—Use of ingredients characterised by shape
  • C08K7/02—Fibres or whiskers
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
  • C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L27/00—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers
  • C08L27/02—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers not modified by chemical after-treatment
  • C08L27/04—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers not modified by chemical after-treatment containing chlorine atoms
• • 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

• This invention relates to methods of processing waste comprising vulcanized rubber and/or tire waste and to products obtained from processing of same.
• a typical scrapped automobile tire weighs 9.1 kg. Roughly 5.4-5.9 kg (13 lb) consists of recoverable rubber, composed of 35 percent natural rubber and 65 percent synthetic rubber.
• a typical truck tire weighs 18.2 kg and also contains from 60 to 70 percent recoverable rubber.
• Truck tires typically contain 65 percent natural rubber and 35 percent synthetic rubber.
• the majority of modern tires are steel-belted radials, containing 10-15% metals and 10% cords (e.g. polyester, nylon or rayon).
• the tire rubber waste is divided into categories defined by their size and method of production, i.e. slit tires, shredded tires or chipped tires, ground rubber and crumb rubber.
• Rubber recycling process begins with shredding. After most of the steel and reinforcing cords are removed, a secondary grinding takes place, and the resulting rubber powder is ready for product remanufacture. The manufacturing applications that can utilize this inert material are restricted to those which do not require its devulcanization. In the rubber recycling process, devulcanization begins with cleavage of the sulfur-sulfur bonds which cross-linked the vulcanized rubber molecules, thereby facilitating the formation of new cross-linkages. Two main rubber recycling processes have been developed: the modified oil process and the water-oil process.
• tire reinforcing fiber (or tire cords) has very few uses in recycling and poses another significant problem in tire recycling industries.
• a rare example for a method for recycling tire cords is provided by U.S. Pat. No. 3,468,974 which teaches a molding composition containing 64-91% tire cord (polyamide) and 3-36% vulcanized rubber which is produced from extrusion pelletizing tire cord material.
• production of products made of rubber originated from tires requires a step of devulcanization of the rubber.
• WO 2009/019684 there is disclosed a method for manufacturing a polymeric plastic product from used mineral oils, waste of hydrolysis of vegetable oils and/or animal fats as well as scrap automobile and/or other tires and/or other rubber waste.
• U.S. Pat. Application No. 2005/0279965 describes a method for producing a composite material comprising mixing crumb rubber from recycled tires, plastic and asphalt in a high shear mixer.
• U.S. Pat. Nos. 6,558,773 and 6,703,440 disclose a compression molding product made by blending and heating together rubber and a binder (e.g. ultra low density polyethylene) and extruding the blend followed by compression molding into a desired product.
• a binder e.g. ultra low density polyethylene
• U.S. Pat. No. 6,169,128 teaches a method for processing discarded plastic and rubber with a binder to obtain a processable material and useful products therefrom.
• WO 2004/074594 teaches a panel for roofing or siding applications preferably made of a blend of rubber tire and drums.
• the subject matter discloses a composite material comprising a first component and a second component, the first component comprising an organic element and a thermoplastic element and the second component comprising at least one element selected from the group consisting of vulcanized rubber and tire cords.
• the subject matter further discloses a process comprising:
• the subject matter further discloses a process comprising:
• thermoplastic waste subjecting at least organic waste and thermoplastic waste to at least one processing step selected from the group consisting of drying, particulating, mixing and heating under shear forces, to obtain a first component;
• the first and/or second components before it is processed and the obtained composite material due to a loss of matter such as moisture or other volatiles, the formation of some volatile compounds during processing, decomposition of materials and other factors that should be taken into account when comparing the content of a component in the composite material and that in an intake material.
• the present invention is aimed, inter alia, at providing, on the one hand, a solution for vulcanized rubber and tire waste material including tire cords and on the other hand, for unsorted waste, such as domestic waste.
• the solution is provided by processing a combination of the above to obtain a compacted composite material.
• the present disclosure thus provides a composite material made from the aforesaid waste material, a method of processing the waste material into a useful composite material, and articles of manufacture from the waste-derived composite material.
• organic waste is used herein to denote, without being limited thereto, any carbon including waste that was or is living, such as garden waste (leaves, grass clippings, branches, hay, flowers, sawdust, woodchips and bark), food waste (fruit, vegetables, grains, meat, egg shells, bones, oil, fat, or dairy products) as well as others (paper, feces, dust, hair, wood ash). Since the composite material comprises organic material it inherently comprises fingerprints that are unique to materials of biological origin e.g. DNA, proteins, chlorophyll, potassium, nitrogen and phosphorous etc., which are absent from materials of synthetic origin. The organic waste typically includes organic fibers.
• organic element is used herein to denote any carbon-based material originating from organic waste.
• the organic element may be a combination of various organic elements originally forming organic waste and it may be organic waste that following processing according to the invention underwent some modification (chemical and/or physical) into a different form of chemical material (i.e. that was not originally present in the organic waste).
• organic fiber is used herein to denote fibers of organic or man-made origin.
• the organic fiber includes any one of cellulose, hemicellulose and/or lignin and combinations of same, the latter also known by the term “lignocellulosic biomass”.
• thermoplastic waste or “thermoplastic” is used herein to denote solid or essentially solid material that turn upon heating above a melting temperature into a hot flowable material (soft, malleable, moldable, remoldable and, extrudable, weldable material) and reversibly solidify into an elastic state when cooled back below its melting temperature. Upon further cooling below the glass temperature, the thermoplastic adopts a solid state, typically amorphous.
• Thermoplastics include, without being limited thereto, polyolefins, polystyrene, polyvinylchloride, polyethylene terephthalate, polyacrylonitrile, polybutadiene, polystyrene, polycarbonate, nylon, polyurethane, co-polymers thereof and other material having a thermoplastic property as defined above.
• thermoplastic element is used herein to denote a plastic material that exhibits thermoplastic properties.
• substantially unsorted waste or “SUW” is used herein to denote waste material, including, solid, semi-solid and/or fluid material, which may include plant material, result from human and animal activities, may originate from municipal waste, industrial waste (e.g.
• the waste may be decomposable combustible waste, such as paper, wood, fabric or non-combustible waste, such as metal, glass, sand and ceramics.
• the waste may also originate from landfills including old landfills.
• the waste is either unsorted, e.g. obtained as is, i.e. in the form it is received at a waste management facility or at a waste dump or from a landfill; or the waste is partially sorted, i.e. from which one or more elements are selectively removed before processing, albeit, the majority of the waste is retained as is.
• Such selectively removed elements may have an economical value as recyclable materials or articles, and may include, without being limited thereto, metal parts, e.g. batteries, aluminum and iron, glass, ceramics, paper, cardboard and plastic containers such as bottles, storage bowls, commercial plastic ready to cook containers etc.
• metal parts e.g. batteries, aluminum and iron, glass, ceramics, paper, cardboard and plastic containers such as bottles, storage bowls, commercial plastic ready to cook containers etc.
• majority of waste retained it is meant that at least about 80% by weight of the original waste material (i.e. of the unsorted, as is, waste) and at times above 90% and even 95% by weight of the original waste material is retained.
• the elements that are removed from the waste does not exceed about 20%, about 10% or even about 5% of the weight of the original waste.
• MSW military solid waste
• the MSW may be composed wood, wood derived products such as paper, cardboard, tissues and the like, food scraps and plastics.
• the Environmental Protection Agency reported in the United States that MSW was composed of the following ingredients, as percent by weight: paper (32.7%), glass (5.3%), metals (8.2%), plastics (12.1%), rubber, leather and textiles (7.6%), wood (5.6%), yard trimmings (12.8%), food scraps (12.5%), other (3.2%).
• the waste in some embodiments SUW, may be used in accordance with the invention as a wet material (namely, including water and/or moisture) or is used as dry material (i.e., comprising less than 0.1% w/w moisture).
• Drying is used to denote the treatment of waste or any of the elements of the composite material so as to remove therefrom liquids.
• the removal is of at least some amount of volatile liquids (i.e. liquids having a vapor pressure of at least 15 mmHg at 20 C, e.g. water and ethanol). Drying results in a dried waste or element, namely, waste comprising not more than 10% moisture, not more than 5% moisture, and at times even not more than 1% moisture.
• some level e.g. above 1%) of liquid (e.g. water) in the waste is maintained after drying.
• the amount of liquid removed from the waste can be controlled to fit the intended use of the eventually obtained composite material. Further, drying encompass any means of drying, e.g.
• drying includes removal of at least 50% of the moisture, at times 60%, 70%, 80%, 90%, 95% and even, at times, up to 99% of the moisture initially contained in the waste or the element (this may be determined by weighting the waste or the element before and after drying). It is noted that 99-100% percent of the moisture does not have to be removed from the waste and in some applications it is even preferred that some water remains in the waste for the subsequent procedure for preparing the composite material or for the processing of the waste with the rubber and/or tire cords.
• the waste obtained after drying and used for preparing composite material as disclosed herein has water and optionally other volatile liquids such as ethanol, at content in the range of about 1% and about 11%.
• vulcanized rubber is used herein to denote cross-linked rubber polymers.
• the rubber polymers are typically hydrocarbon elastomers, such as polyisoprene (either natural rubber e.g. gum rubber or synthetic rubber) and styrene-butadiene rubber (SBR).
• SBR styrene-butadiene rubber
• the cross-linking typically includes reaction of the rubber polymer with sulfur, peroxides or any other cross linking agent known to those versed in the art, during which individual polymer chains are covalently interlinked to each other to yield a three dimensional matrix.
• the vulcanization of the rubber polymers gradually transforms the elastomers into thermosets.
• the degree of vulcanization may vary from one rubber to the other, depending on the application of the vulcanized rubber. It is to be understood that any vulcanized rubber at any degree of vulcanization may be used. It should also be noted that the vulcanized rubber may comprise a portion of non-vulcanized or devulcanized rubber, especially when the source of vulcanized rubber is rubber residues and discarded vulcanized rubber from rubber manufacturing plants. Typically, non-vulcanized or de-vulcanized rubber would not exceed more than 10% or even 5% or even as low as 1% of the total weight of the vulcanized rubber mass.
• the vulcanized rubber may also comprise rubber additives such as fillers and fibers including residues or contaminants to which the rubber was exposed to during vulcanization reaction, during its use, or processing (e.g. retreading, recycling treatment or size reduction into crumb rubber).
• rubber additives such as fillers and fibers including residues or contaminants to which the rubber was exposed to during vulcanization reaction, during its use, or processing (e.g. retreading, recycling treatment or size reduction into crumb rubber).
• the vulcanized rubber may be less than 100% pure and may comprise small amounts of other residues in an amount of between 0.1 and 20% w/w of the total weight of the vulcanized rubber, at times the vulcanized rubber comprises between 0.5 and 10% w/w residues, or between 1 and 5% w/w residues.
• residues include tire cords, steel, silica, anti-tackifying agents, oil, sand, iron, ash, and calcium carbonate.
• the “vulcanized rubber” is vulcanized rubber from disposed vulcanized rubber products such as, without being limited thereto, used tires, bumpers, shoe soles, latex and rubber gloves, conveyor belts and may also arrive from industrial rubber residues and discarded vulcanized rubber from rubber manufacturing plants. The latter may comprise some partially or non-vulcanized rubber as a minor component. In some other embodiments, the vulcanized rubber originates from virgin material, either natural or synthetic.
• the discarded vulcanized rubber products (e.g. the tire waste) are grinded into any kind of particulated form of rubber known in the art such as scrap, shreds slits chips, ground rubber and crumb rubber.
• vulcanized rubber may be any component of tire waste, including, without being limited thereto, whole tire (the tread and the casing), or different forms of processing (sizing and shaping) of tire including tire slit, tire chips, ground rubber, crumb rubber, tire shreds, tire powder, tire cords etc.
• tire shreds or tire chips In most cases the production of tire shreds or tire chips involves primary and secondary shredding by tire shredders. The discarded tires also undergo a size reduction process to typically obtain tire shreds, tire chips, ground rubber or crumb rubber. Similarly, when other sources of vulcanized rubber are used, these are also reduced by size to obtain processable particles.
• Tires are predominantly of vulcanized rubber, tire cords and steel. Other constituents may include carbon, minerals (e.g. zinc and sulfur). According to the Technical Guidelines on Identification and Management of Used Tires, UNEP, Basal convention, 1999 on average tires comprise 45-47% rubber, 21-22% carbon, 16-25% steel, about 5% tire cords, 1-2% zinc, about 1% sulfur and 5-8% additives. Therefore, all of these components may be present in tires waste as used herein.
• “Tire shreds” is used to denote tire particulates that are irregularly shaped and vary in size, with size varying from 300 to 460 mm long by 100 to 230 mm as wide, down to as small as 100 to 150 mm in length.
• the size and shape may be controlled by the process of their preparation, the manufacturer instructions/equipment and condition.
• internal steel belt fragments along the edges of the tire shreds are exposed.
• the steel belt fragments are typically removed from the tire shreds prior to processing according to the invention.
• the steel belt fragments are removed by a magnetic separator, gravimetric separation techniques, Eddy Current Separator System and any other commonly used separation techniques.
• Teire chips are used herein to denote processed tire shreds that typically have a size from 76 mm down to 13 mm.
• “Ground rubber” is used herein to denote rubber sized from 19 mm down to 0.15 mm (No.
• ground rubber 100 sieve depending, inter alia, on the type of size reduction equipment and the intended application.
• the production of ground rubber may be achieved by granulators, hammer mills, or fine grinding machines. Granulators typically produce particles that are regularly shaped and cubical with a comparatively low-surface area. At times, fiberglass belts or cords are separated from the fine rubber powder, usually by an air separator. Ground rubber may be subjected to a dual cycle of magnetic separation, then screened and recovered in various size fractions. “Crumb rubber” is used herein to denote rubber sized from 4.75 mm (No. 4 sieve) down to less than 0.075 mm (No. 200 sieve).
• any common method that is used to convert scrap tires to crumb rubber may be applied such as the crackermill process, the granulator process and the micro-mill process.
• the crackermill process wherein scrap tires is passed between rotating corrugated steel drums, generates irregularly shaped torn particles rendering a large surface area. These crumbs range in size from approximately 4.75 mm to 0.5 mm (No. 4 to No. 40 sieve) and are commonly referred to as ground crumb rubber.
• the granulator process is used to obtain granulated crumb rubber particles, by shearing apart the rubber with revolving steel plates that pass at close tolerance. Fine ground crumb rubber in the size range from 0.5 mm (No. 40 sieve) to as small as 0.075 mm (No.
• Tire cords which is used interchangeably with the term “tire fibers” denotes a high strength (high modulus) fibrous filamentary material having a relatively low degree of shrinkage and exhibits a low degree of hysteresis. Tire cords are used as reinforcement filaments which provide tires better resistance to compression fatigue for rubber products.
• the tire cords while referring to tires, may be derived also from rubber conveyor belts, agricultural and plumbing rubber hosing etc.
• Tire cords may include, without being limited thereto, polyester (e.g.
• polyethylene terephthalate, PET polyamide
• polyamide polyamide
• aromatic polyamide e.g. aramid and p-aramid
• rayon cotton
• carbon fibers or any other material used in tire/belting industry.
• Other sources for the tire cords are virgin materials i.e. materials such as fibers made of rayon, nylon and polyesters, that were not derived from a used product, and fibers that are equivalent to tire cords from the textile industry or textiles such as old cloths or synthetic carpets.
• the present disclosure provides a composite material comprising a first component and a second component, the first component comprising an organic element and a thermoplastic element and the second component comprising at least one element selected from the group consisting of vulcanized rubber and tire cords.
• the first component comprises at least an organic element and a thermoplastic element.
• the organic element is in a range from at least about 10% (w/w) of the total composite material, at times, about 15% w/w, about 20% w/w, about 25% w/w, about 30% w/w, about 35% w/w, about 40% w/w and even at least about 48% w/w out of the total weight of the composite material to an upper % w/w of up to about 49% w/w, typically less than about 45% w/w, about 40% w/w, about 35% w/w or even less than about 30% w/w of organic matter.
• the first component also comprises a thermoplastic element.
• the amount of the thermoplastic element is in a range from at least 1% w/w, 2% w/w, 5% w/w or even 10% w/w of the total composite material to an upper % w/w of up to about 49% w/w, typically less than about 45% w/w, about 40% w/w, about 35% w/w or even less than about 30% w/w of thermoplastic element of the total composite material.
• the amount of the first component is between about 10% w/w to about 50% w/w of the composite material.
• the first component may also include plastic.
• the amount of plastic in the first component may be from null to about 40% w/w, or to about 35% w/w or even to about 30% w/w. In some embodiments, the amount of plastic in the composite material is at least 1% w/w, 3% w/w, 5% w/w, 10% w/w or even 15% w/w but not more than 30% w/w or 25% w/w or even not more than 20% w/w.
• plastic material that may form part of the first component and thus of the composite material include synthetic polyolefins (e.g.
• HDPE high density polyethylene
• LDPE low density polyethylene
• LLPE linear low density polyethylene
• PP polypropylene
• PS polystyrene
• HIPS high impact polystyrene
• PVC rigid and plasticized polyvinylchloride
• ABS acrylonitrile butadiene styrene
• PU polyurethane
• PA polyamides
• EVOH ethylene vinyl alcohol copolymers
• the first component also comprises an inorganic element such as metal, sand and clay.
• the amount of the inorganic element may range from at least about 1% w/w, about 2% w/w, about 5% w/w, about 10% w/w or at least about 15% w/w of inorganic matter; but less than about 50% w/w, about 40% w/w, about 30% w/w or even less than about 20% w/w in the composite material.
• the first component is derived from substantially unsorted waste (SUW).
• the unsorted waste is municipal solid waste (MSW).
• MSW municipal solid waste
• the different elements of the first component i.e. the organic element, the thermoplastic element etc. may originate from the same source, e.g. the same bulk of SUW/MSW, it may at times, be provided from different sources.
• the organic element may be provided from garden cuttings and/or organic domestic waste
• the thermoplastic element may be from collected plastic bottles and containers.
• the second component comprises at least one element selected from vulcanized rubber and tire cords.
• the amount of the second component out of the combined first component and second component is in the range from at least about 50% w/w, about 55% w/w, about 60% w/w, about 65% w/w, about 70% w/w, about 75% w/w, about 80% w/w or at least about 85% w/w of the total weight of the composite material to an upper limit of less than about 90% w/w, about 85% w/w, about 80% w/w, about 75% w/w, about 70% w/w about 65% w/w or less then about 60% w/w of the total weight of the combined first component and second component.
• the amount by weight of vulcanized rubber out of the total combined first component and second component is in the range from at least about 20%, about 25%, about 30%, about 35%, about 40%, about 45%, about 50% or at least about 55% of the total weight to an upper limit of less than about 90% (when no tire cords are present), about 85% (when tire cords may also be present), about 80%, about 75%, about 70% about 65 or less then about 60% of the total weight.
• the amount of tire cords by weight out of the total combined first and second components is in the range from at least about null, about 1%, about 2%, about 5%, about 10%, about 15%, about 20% or at least about 25% to an upper limit of less than about 30%, about 25%, about 20%, about 15%, about 10% about 5% or less then about 3%.
• tire cords are also considered to be plastic material (e.g. polyamide and polyester), it is to be understood that polymers in the form of cords being suitable for use as tire cords are calculated as being tire cords only and not as part of the thermoplastic element in the first component. Similarly, plastic material that is not in the form of cords that are suitable for use as tire cords are calculated here as part of the thermoplastic element in the first component.
• plastic material e.g. polyamide and polyester
• the total weight of the combined first component and of the second component is the total weight of the composite material.
• the second component at least comprises vulcanized rubber.
• tire cords may assist in increasing the mechanical strength of the resulting composite material.
• the length of the tire cords used also has an effect on the strength of the resulting composite material: the longer the fiber, the stronger the resulting material.
• the increased mechanical strength enables the use of the composite material various applications where resilient materials are usually utilized.
• the composition may be fine-tuned by adding certain other elements either during the preparation thereof or after it is formed.
• Some non-limiting examples for other elements that may be beneficial to incorporate into the composite material are color pigments and active carbon.
• the first component is processed waste comprising at least organic waste and thermoplastic waste.
• processed waste refers to waste that was subjected to at least one manipulation of drying, mixing while heating under shear forces, extruding, and optionally also particulating and sieving. At times the processing of the waste to obtain the first component may comprise all of aforementioned actions.
• the processed waste is obtained, in some embodiments as particulate material in the size range of between about 0.01 mm and about 2.5 mm in diameter, but may be at times smaller than about 1.5 mm, even more typically particles having a size of between about 0.7 mm and about 1.5 mm or smaller than about 0.7 mm in diameter are used.
• the first component is particulate processed waste having a size range of between 0.01 mm and 0.7 mm in diameter.
• the waste is substantially unsorted waste (SUW) which may provide a processed waste as described in co-pending PCT/IL2010/000027.
• This processed waste is prepared by processing substantially unsorted waste using the following minimal steps of particulating substantially unsorted waste that comprises organic matter and optionally plastics and heating while mixing the particulate waste material to a temperature of at least about 100 C under shear forces to thereby obtain the processed waste.
• the unsorted waste may be dried prior to processing.
• the processed waste used, at times, as a first component may be characterized by its surface energy.
• the processed waste obtained from SUW has a surface energy that is above about 35 dyne/cm, preferably above about 40 dyne/cm and even more preferably above 45 dyne/cm.
• the surface energy of polyethylene is about 35 dyne/cm and of polypropylene is about 31 dyne/cm, and of Polytetrafluoroethylene (PTFE/Teflon) 18-20 dyne/cm.
• the processed SUW has thus a high surface energy, and in fact the processed SUW has a surface energy that is higher than polyolefins.
• This relatively high surface energy permits strong interaction at its surface with other polar substances, such as paint, adhesives, wood, various stones and others, e.g. upon processing with the second component to form the composite material of the invention.
• the composite material is comprised of 10-50% w/w of a first component, 20-90% w/w vulcanized rubber, and 0-30% w/w tire fibers, wherein the combined amount of vulcanized rubber and tire fibers is between 50 to 90% w/w.
• the composite material also comprises up to 12%, typically up to 10% w/w volatile liquids (i.e. liquids having a vapor pressure of at least 15 mmHg at 20 C, e.g. water and ethanol).
• the vulcanized rubber comprises tire crumb.
• the composite material may further comprise fillers and other additives that are customary in article manufacturing such as absorbents, plasticizers, binders, carbon black, UV blockers, metals, weight additives, sand, silica and pigments.
• additives that are customary in article manufacturing such as absorbents, plasticizers, binders, carbon black, UV blockers, metals, weight additives, sand, silica and pigments.
• the combined amount of these additives typically does not exceed more than 10%, or not more than 5% and even not more than 2% wt of the total weight of the composite material.
• the composite material comprises as much as 90%, 85%, 80%, 75%, 70%, 65%, 60%, 55%, or 50% crumb rubber, 50%, 45%, 40%, 35%, 30%, 25%, 20%, 15%, or 10% of the first component; 40%, 35%, 30%, 25%, 20%, 15%, or 10% cords and up to 10, 9, 8, 7, 6, 5, 4, 3, 2, 1% volatile liquids (e.g. water) by weight.
• volatile liquids e.g. water
• the minimal amounts of crumb rubber and of the first component are 50% and 10% by weight, respectively.
• the composite material comprises organic element, thermoplastic element and the second component consists of vulcanized rubber. According to yet another embodiment the composite material comprises organic element, thermoplastic element and the second component consists of tire fibers.
• the composite material exhibits some thermoplastic behavior that may be characterized by the following parameters (properties):
• the composite material was also found to be injectable, e.g. when heated, may be subjected to injection molding.
• the composite material is found to hold tire-derived pollutants, such as aromatic hydrocarbons, (PAHs) and certain metals such as iron, arsenic, cadmium, chromium, manganese, intact in the composite material and thus minimize or eliminate environmental hazards associates with disposal of tire waste.
• PAHs aromatic hydrocarbons
• the holding of polluting substances may be determined by leaching testes, such as described by procedures such as EPA SLO-846 method 1310 and as compared to leaching of the second component according to the invention without being combined with the first component as described herein.
• compositions that can define the composite material include:
• the present disclosure also provides a process comprising:
• the first component is processed unsorted waste.
• the processed unsorted waste may be obtained by mixing and heating dried and particulated SUW, under shear forces and finally extruded as explained in detail in co-pending PCT/IL2010/000027, which is hereby incorporated by reference.
• the processing of the SUW comprises at least one of particulating, drying, blending, sieving and mixing while heating, extruding the melt that is obtained after mixing while heating under shear forces, granulating and sieving.
• the processing of the SUW to obtain the first component may comprise all of aforementioned actions.
• the processed SUW is obtained, in some embodiments as particulate material.
• a finding of the present process is that while heating for the purpose of recycling of vulcanized rubber requires high temperatures and high pressure, the composite material of the invention can be prepared at much lower temperatures and pressure than other recycling processes of vulcanized rubber. Thus the process of the invention may be regarded a more energy efficient process as compared to those used to recycle vulcanized rubber.
• the first component and the second component are mixed before mixing while heating under shear forces.
• the amount of the first component and of the second component may vary.
• the first component is in an amount between about 10% out of the total weight of the combined amount of the first component and second component (w/w) to about 50% w/w and the second component is in an amount of between about 50% w/w to about 90% w/w of the combined amount of the first component and the second component.
• the first component comprises organic waste.
• the amount of the organic waste may be in a range from a lower % by weight of at least about 10% w/w of the total mixture, at times, about 15%, about 20%, about 25%, about 30%, about 35%, about 40% and even at least about 48% by weight out of the total weight of the combined first and second components to an upper % of up to about 49%, typically less than about 45%, about 40%, about 35% or even less than about 30% of organic matter by weight out of the total weight of the combined components.
• the first component also comprises thermoplastic waste.
• the amount of the thermoplastic waste is in a range from a lower at least 1%, 2%, 5% or even 10% by weight out of the total weight of the combined first and second components to an upper % of up to about 49%, typically less than about 45%, about 40%, about 35% or even less than about 30% of thermoplastic waste by weight out of the total weight.
• the second component comprises at least one element selected from the group consisting of vulcanized rubber and tire cords.
• the amount of the second component out of the total weight of the combined first and second components may range from at least about 50%, about 55%, about 60%, about 65%, about 70%, about 75%, about 80% or at least about 85% by weight of the total weight of the combined first and second components to an upper limit of less than about 90%, about 85%, about 80%, about 75%, about 70% about 65 or less then about 60% by weight of the total weight of the combined components.
• the amount by weight of vulcanized rubber out of the total weight of the combined first and second component may range from at least about 20%, about 25%, about 30%, about 35%, about 40%, about 45%, about 50% or at least about 55% to an upper limit of less than about 90% (e.g. when no tire cords are present at all), about 85%, about 80%, about 75%, about 70% about 65 or less then about 60% of the total weight of the combined components.
• the tire rubber is selected from the group consisting of tire slit, chipped tires, ground rubber and crumb rubber and the tire cords are selected from the group consisting of at least one of polyester, polyamide, polyvinyl alcohol and rayon.
• the heating under shear forces is at a temperature in the range of between about 10° C. to about 20° C. In some embodiments, the temperature is at any range of between a lower end of 115 C, 120 C, or 125 C to an upper end of 160 C and 180 C.
• the mixing while heating may be preceded with a pre-mixing (without heating) of the first component and the second component.
• particulating may take place prior to mixing. For example, when the first component is processed unsorted waste, the latter may be particulated and sieved before it is mixed with the at least one of vulcanized rubber and tire fibers.
• the first component particulate has a size range of between about 0.01 mm and about 2.5 mm in diameter, in some embodiments between 0.01 mm and about 0.7 mm, in some embodiments between about 0.7 mm and about 1.5 mm and in some embodiments between about 1.5 and about 2.5
• Particulating may be met by grinding, shredding, slitting, dicing, crushing, crumbing, chopping by conventional size reduction processes, including, without being limited thereto, shredders, grinders, choppers, granulators, which, when necessary, may be equipped with blades, hammers or plates that are made of robust materials such as stainless steel or titanium. Further, prior to mixing while heating, drying may take place.
• the drying may be of the first and/or second components as received, on particulated matter. Drying may be achieved by any means, e.g. by placing the waste outdoors and allowing it to dry, under a stream of dry air, in an oven chamber or by squeezing the liquid out.
• the first component is SUW which is subjected to drying and particulating prior to mixing with the second component.
• Such elements may include, recyclable material or articles, such as batteries, aluminum and iron, glass, ceramics, paper, cardboard etc.
• the separation of such elements from the particulate matter may be executed by the use of suitable sieves, magnetic separators, eddy current separators, floatation systems, gravimetric separation techniques, etc.
• loose steel cords may be separated from the shredded tires by means of passing the shredded tires upon a conveyor under a magnet or a series of magnets. Some amount of loose steel cords may still remain in the second component. It is estimated that vulcanized rubber may still about 0.1, 0.2, 0.5, 1, 2, 3, 4 or even up to 5% by wt of the total weight of the rubber forming the second component.
• the process disclosed herein does not require the removal of tire shreds and/or tire cords typically removed from tire recycling processes. In other words, the process disclosed herein allows recycling of these elements as well. Without being bound by theory, it is believed that the presence of the tire shreds and tire cords affects the mechanical properties of the resulting composite material.
• the mixing may also involve the addition of at least one plastic material.
• the mixing of the plastic material may be prior to, or during the mixing while heating under shear forces.
• the plastic may be added at a pre-mixing stage, as described above, or it may be added while heating and mixing.
• the plastic may be selected from the group consisting of polyethylene, polyvinylchloride, polystyrene, polyurethane, thermoplastic elastomers polypropylene and mixtures thereof.
• the amount of plastic added may be such to obtain in the melt an amount of thermoplastic material in a range of between 1% and 49%.
• additives used as fillers may include, without being limited thereto, sand, minerals, recycled tire material, glass, wood chips, thermosetting materials, other thermoplastic polymers, gravel, metal, glass fibers and particles, etc. These fillers may originate from recycled products; however, virgin materials may also be employed.
• Other additives may be added to improve the appearance, properties, texture or scent of the composite material such as pigments, odor masking agents (e.g. activated carbon), oxidants (e.g. potassium permanganate) or antioxidants.
• curing agents may be added such as sulphur, peroxides prior to or during the heating while mixing.
• first and second component as well as any other additives may be introduced into the process simultaneously or sequentially, before, during and after the process.
• the addition of the various elements may be in portions.
• the compounder may receive first a portion of the first component, e.g. SUW, followed by the introduction of the second component, e.g. vulcanized rubber.
• the compounder may include various inlets for introducing the various elements at different locations, thus, for example, allowing the introduction of one component after other components have already been subjected to some level of heating while mixing under shear forces.
• the mixing while heating under shear forces may be performed in a compounder selected from the group consisting of extruder, internal mixer (Banbury), co-kneader, and continuous mixer.
• a compounder selected from the group consisting of extruder, internal mixer (Banbury), co-kneader, and continuous mixer.
• the mixing while heating using shear forces typically results in a homogenous melt/blend.
• the extruder comprises a heated barrel containing rotating therein a single or multiple screws.
• the screws may be co-rotated, counter-rotated planetary rotated (such as in a planetary roller extruder). Screws may be intermeshing, or non-intermeshing.
• the extrusion apparatus may be a single extruder or combinations of extruders (such as in tandem extrusion) which may be any one of the extruders known in the plastics industry, including, without being limited thereto, single screw extruder, tapered twin extruder, tapered twin single extruder, twin screw extruder, multi-screw extruder.
• extruder in the context of the invention is a single screw extruder.
• the extruder is equipped with a venting zone.
• the extruder comprises a nozzle that is chilled during extrusion.
• the extruder may be segmented and configured so as to apply differential temperature and/or pressure as desired. Sufficient shearing, mixing and residence time are generally required so as to allow the combined components to reach the required/desired temperature, which is determined by obtaining a composite material exhibiting the thermoplastic behavior.
• the desired material temperature can be reached by two ways: either by heat absorbed from the compounder or other device, or by friction caused by the shearing forces, or a combination of the two ways.
• the compounder is set to a temperature of between about 100° C. and 200° C., and at times to a temperature of between about 120° C. and 190° C., or even between about 140° C. and about 180° C.
• the temperature of the material is usually higher than the machine set temperatures, due to heating caused by shearing forces.
• the resulting composite material may be regarded as sterile, namely, that pathogens contained in the components prior to the process, such as in the unsorted waste are destroyed.
• the hot melt resulting from the mixing while heating is then cooled to ambient temperatures (e.g. room temperatures which are typically around 25° C.) to obtain the composite material.
• ambient temperatures e.g. room temperatures which are typically around 25° C.
• the composite material may be re-processed under the same or different conditions used for its formation.
• the composite material is subjected to one or more cycles of heating under shear forces at the same conditions used for its production.
• a process comprising providing a composite material as disclosed herein and subjecting the composite material to at least heating at a machine temperature of between 100° C. to 180° C. and at least one additional process step selected from the group consisting of extruding, molding, compression molding, whereby an article of manufacture is obtained, having a desired shape.
• the composite material may be reheated to a temperature in a range of between above about 100° C. above 130° C. and even above 140° C. an up to about 160° C., 180° C. or 200° C., at which it turns into soft, flowable matter.
• Additives and fillers as detailed above are also optionally added to the composite material.
• Table 1 lists possible products (articles of manufacture) that can be prepared by processing the composite material disclosed herein, alongside parameters that are characterize the specified product.
• the composite material are used as an additive to manufacturing processes, to be added, for example, to a thermoplastic hot melt comprising virgin or recycled plastic.
• the composite material of the invention is also used in variety of industrial processes, to form a variety of semi-finished or finished products.
• Non-limiting examples include building material, panels, boards, pallets, pots, component of plant growth substrate, and many others.
• the composite material is the sole component or is in a mixture with other materials.
• the process comprises preparing an article comprising two or more materials adhered to one another to form laminates and the like, where at least one layer comprises the composite material.
• Such multi-layer structures may be obtained by lamination, co-calendering, co-compression, co-extrusion, co-injected or tandem extrusion of two or more materials (one being the composite material of the invention) so as to form the multi-layer product.
• the composite material is added in some embodiments as filler, for example, to be mixed with bitumen (asphalt), to yield a modified bitumen material, like polymer modified bitumen.
• the modified bitumen material may be used as a substitute for bitumen in the construction of roads, pavements, platforms, waterproofing membranes, polymeric asphalt and so forth.
• the bitumen-like material is prepared by mixing the composite material with bitumen in a mixer.
• the composite material is mixed at any amount with the bitumen, from even 1% up to 95% of the mixed composite material/bitumen.
• the bitumen like material is formed from about 90% composite material and in fact, the bitumen is used as an additive to the composite material. It has been found that the resulting bitumen like material is injectable and can be processed using an extruder.
• the first is a self-designed extruder (screw diameter: 70 mm, screw length: 2650 mm, clearance of screw to barrel: 0.1 mm, die and adapter length 190 mm, die opening diameter: 10 mm) and the second is an Erema RM 120 TE (screw diameter: 120 mm, screw length: 4000 mm, clearance of screw to barrel: 0.1-0.2 mm, die and adapter length 370 mm, die opening diameter: 50 mm), both having a venting zone.
• An extrudate from SUW was prepared following the extrudate II process described in PCT/IL2010/000027
• Substantially unsorted waste (SUW) collected from private households was shredded in a shredder (type ZSS 850 ex Zerma, China) equipped with steel blades and then ground in a granulator (granulator type GSH 500/600 ex Zerma, China) into particles of a size of between several microns to several centimeters.
• the ground particulates were then sieved to collect particulates in the range of 100-200 mm in diameter.
• the 100-200 mm particulates flow passes through a magnet that removes at least some of the original magnetic metallic content of the SUW.
• the remaining particulate flow is ground (granulator type GSH 500/600 ex Zerma, China) and sieved again to obtain particulates having an approximate size of 20 mm.
• the ground particulates were then air dried for a few days, dried under a stream of dry air, until at least some, but not all liquid was removed to obtain dried particulates.
• the dried particulates were fed into single screw extruder (Erema) that was set at a temperature of 180 C and a rotation rate of about 50 rpm.
• the particulated material was processed in the extruder with a residence time of between about 3 minutes to about 5 minutes.
• the extrudate was cooled to room temperature (herein “extrudate II”).
• the extrudate was subsequently ground by a granulator (Zerma) and sieved to obtain particulates having an approximate size smaller than 0.7 mm in diameter. Larger particulates were reground and sieved again and so forth until substantially all of the SUW was particulated into particles smaller than 0.7 mm in diameter.
• Zerma granulator
• Crumb rubber made from discarded tire was obtained from a tire recycling plant (Tyrec), in a size range of between 0.3 and 5 mm divided to three size categories: under-0.5 mm, 0.5-2 mm, 2-4 mm.
• the tire shreds were obtained by cutting discarded tires in a cutter shredder (type BDR 2000 ex MTB, France). After shredding, tire cords were separated from the tire shreds. When necessary, the tires or the tire shreds were first dried before further processing with an air blower, reaching a moisture content of no more than 10% wt. The tire shreds were then passed on a conveyer under a magnet to separate loose steel cords.
• the melt was transferred after cooling to a Demag, Ergotech Viva 80-400 injection machine (temperature: 150 C, injection pressure: 40-90 bar, injection speed: 30-50 mm/s) or a 250 tones press to obtain injection molding or compression molding articles, respectively.
• a Demag, Ergotech Viva 80-400 injection machine temperature: 150 C, injection pressure: 40-90 bar, injection speed: 30-50 mm/s
• a 250 tones press to obtain injection molding or compression molding articles, respectively.
• the mixing of SUW extrudate with the crumb rubber allowed the injection molding and extrusion of vulcanized rubber as if it were a thermoplastic material.
• Tire cords were obtained from a tire recycling plant (Tyree).
• the tire cords comprise nylon (polyamide 6 and polyamide 6,6), rayon and polyester.
• SUW, crumb rubber and tire cords 4:5:1 were mixed in a self mixer at 23 rpm to obtain a substantially homogeneous mixture.
• the mixture was introduced into the home made single screw extruder described above which was set at a machine temperature of 180° C. and a screw rotation rate of 50 rpm having a temperature gradient from 110° C. to 180° C. for a residence time of about 3 minutes. The fumes from the venting zone were removed with a vent.
• the melt was transferred after cooling to a Demag, Ergotech Viva 80-400 injection machine (temperature: 150 C, injection pressure: 40-90 bar, injection speed: 30-50 mm/s) or a 250 tones press to obtain injection molding or compression molding articles, respectively.
• a Demag, Ergotech Viva 80-400 injection machine temperature: 150 C, injection pressure: 40-90 bar, injection speed: 30-50 mm/s
• a 250 tones press to obtain injection molding or compression molding articles, respectively.
• the mixing of SUW extrudate with the crumb rubber allowed the injection molding and extrusion of vulcanized rubber as if it were a thermoplastic material.
• Example 3 Crumb rubber and SUW were obtained as detailed in Example 3. Tire cords equivalents were obtained from discarded carpets. The discarded carpets comprise nylon (polyamide 6 and polyamide 6,6) and polyester fibers.
• SUW, crumb rubber and tire cords 4:5:1 were mixed in a self mixer at 23 rpm to obtain a substantially homogeneous mixture.
• the mixture was introduced into the home made single screw extruder described above which was set at a machine temperature of 180° C. and a screw rotation rate of 50 rpm having a temperature gradient from 110° C. to 180° C. for a residence time of about 3 minutes. The fumes from the venting zone were removed with a vent.
• the melt was transferred after cooling to a Demag, Ergotech Viva 80-400 injection machine (temperature: 150 C, injection pressure: 40-90 bar, injection speed: 30-50 mm/s) or a 250 tones press to obtain injection molding or compression molding articles, respectively.
• a Demag, Ergotech Viva 80-400 injection machine temperature: 150 C, injection pressure: 40-90 bar, injection speed: 30-50 mm/s
• a 250 tones press to obtain injection molding or compression molding articles, respectively.
• the mixing of SUW extrudate with the crumb rubber allowed the injection molding and extrusion of vulcanized rubber as if it were a thermoplastic material.
• compositions comprising an odor absorbent (active carbon) and/or a coupling agent (CA, Bondyram® 7100 purchased from Polyram, Israel) were prepared according to the procedure described in Examples 3 and 4.
• the additives were added to the mixture of the processed SUW and the second component (tire powder and/or tire cords). The results are summarized in tables 4 and 5.
• compositions of the invention comprising 3% active carbon and 2% coupling agent (the mechanical properties of the closest composition without additives is presented in parentheses for sake of comparison).
• SUW/crumb/ Charpy Max. Tensile Modulus of Elongation at Flexural Flexural cords/PP Impact Strength Elasticity Break Strength Modulus (w/w) (KJ/m2) (MPa) (MPa) (%) (MPa) (MPa) 35:50:10:0 10.23 1.9 343.8 3.0 3.7 359.2 (9.4) (1.8) (370.4) (2.1) (4.6) (409.0) 25:50:0:20 7.37 4.1 708.8 2.7 8.4 650.3 (7.92) (4.5) (741.4) (2.4) (9.4) (653.6)
• the products exhibit improved resistance to degradation relative to the corresponding rubber products.
• There are several methods to determine resistance to degradation which may be caused by various factors such as thermal oxidation, UV radiation, salt water, acid rain, and so on.
• the tests are performed according to a standard analysis protocol for deterioration of rubber.
• dynamic determination of ozone degradation may follow the JIS K6259 protocol, surface cracking, and surface ozone cracking in a chamber, surface ozone cracking outdoors or in chamber, dynamic ozone cracking in a chamber may follow the ASTM standards D518, D1149, D1171 and D 3395, respectively.
• These standards address material testing and exposure to ozone, either in a chamber (indoor) or outdoors, as well as with static and dynamic test conditions.
• Other tests include progressive stress accelerated life test (PS-ALT),
• the mechanical properties of the compression molding articles can be determined as well, following the appropriate standard and using standard testing machines.
• a composition of SUW/rubber/tire cords 40:50:10% wt is mixed in a mixer with 10% wt bitumen at a mixing rate of 23 rpm and at a temperature of 25° C. until the mixture seemed to be homogeneous.
• the obtained bitumen is a softer product in comparison to a product made without the bitumen.
• the mechanical properties of the product e.g. Charpy impact, max. tensile strength, modulus of elasticity, elongation at break, flexural strength, and flexural modulus) are tested according to standard analysis protocols.

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