Method of recycling synthetic turf and infill product

Abstract
Disclosed herein is a method for recycling synthetic turf that includes agglomerating a plurality of synthetic turf fragments and extruding the agglomerated material. The method produces a recycled material suitable for use as infill in a synthetic turf. Accordingly, an infill for synthetic turf and a synthetic turf including that infill are also disclosed herein.
Description
FIELD OF THE INVENTION

This application is related to the field of synthetic turf, and more particularly to methods of recycling synthetic turf and infill materials produced thereby.


BACKGROUND

Synthetic turf has been used for years in athletic playing surfaces such as football, baseball, and soccer fields, and has more recently been used in other applications where an alternative to natural grass is desired. These applications include at least playgrounds, residential and commercial lawns and other landscaping, jogging paths, paintball fields, tennis courts, putting greens, and dog runs. Typically, synthetic turf includes a pile fabric having a backing and a plurality of upstanding ribbons, also called face fibers or filiform formations, resembling grass. Many synthetic turf products also include an infill material dispersed among the upstanding ribbons, which may consist of sand, tire rubber crumb, or other particulates, either singularly or in combination with each other. The infill material simulates the soil in natural turf, acts as a ballast, and/or contributes to the physical properties of the turf, such as resiliency, that make the turf suitable for a particular use.


Synthetic turf has a limited useful life, the length of which depends on the construction of the turf, the application for which it is used, and how the turf is maintained. As an example, a typical synthetic turf for use as an athletic field may have a useful life of from about 8 to 15 years. A large amount of synthetic turf is currently being used in hundreds of athletic fields and in other applications. To avoid sending that turf to landfills at the end of its useful life, there is a need for a method of recycling and reusing all or portions of the synthetic turf. There is also a need for a synthetic turf that is recyclable.


Recycling of a product typically refers to converting that product into a material or product for another use or extracting at least one of the individual components or materials of the product for use of that component or material in another product. The recycled product may be used in a similar product, such as when paper products are recycled to make other paper products, or may be used in a completely different product, such as when tires are recycled to make asphalt.


Methods for recycling carpet and for preparing carpet backing using recycled carpet scrap are known. Some such methods involve separating the carpet yarns, or tufts, from the backing, e.g. by cutting, and processing only the tufts to recover any nylon. In another recycling process the tufts can be spun into a new yarn for use in carpet or other textiles. One problem with these methods is that only the face fibers are recycled and the backing must be otherwise disposed of. Other methods of recycling carpets include grinding carpet scrap, including the backing, into a fine powder. The powder is then introduced into a carpet backing formulation which may be a precoat, laminate coating, skip coating, or foam coating. The formulation is then applied to a substrate, and cured by heating or drying. One problem with these processes for recycling carpet is that recycled material can make up only about 5% by weight of the carpet backing into which the recycled material is incorporated. This corresponds to approximately 2.5% by weight of a broadloom carpet.


Synthetic turf differs in composition from carpet, and those differences in composition make conventional carpet recycling processes unsuitable for recycling synthetic turf. The majority of carpet products use nylon face fibers, while the majority of current synthetic turf products use polyethylene. The primary coating of most broadloom carpet is a latex coating, while the primary coating in most synthetic turf is polyurethane. In the United States, only a small fraction of broadloom carpet includes a coating containing polyurethane, and only a small fraction of synthetic turfs have a coating containing latex.


Most of the synthetic turf manufactured in the past 6 years has had a polyurethane coating applied to the backing. There is a belief that polyurethane coated synthetic turf as a whole cannot be recycled. This is because the polyurethane coating, according to conventional wisdom, cannot be recycled. Polyurethane is thermoset (versus thermoplastic) and is therefore difficult and costly to recycle. Polyurethane is the reaction product of a polyol and an isocyanate. When these chemicals are mixed together and cured they form a solid polyurethane. The combination is applied to the backing of a tufted material for the purpose of locking the face fibers into the primary backing. An additional coating of a hot melt adhesive or a polyurethane foam can also be applied. This secondary coating is typically used to attach a secondary backing which can be polyester or polypropylene.


Many synthetic turf products include components that are not found in carpet and that are incompatible with, or at least undesirable in, conventional carpet recycling methods. For example, conventional carpet does not include infill. Typical infill materials for synthetic turf installations include sand, tire rubber crumb, and/or other particulates, either singularly or in combination with each other. Thus, recycling synthetic turf presents a unique problem not encountered in the recycling of carpet. Separating infill from the remainder of the turf may require use of special equipment, and there may be environmental concerns associated with disposing of the separated infill. Additional concerns in the recycling process are the effect of any residual infill particulates on the size reduction process and on the properties of the final product.


Conventional carpet recycling methods provide end products that are inconsistent with or that are not ideal uses of recycled synthetic turf. For example, nylon carpet recycling is focused primarily on separating and recovering the nylon, which is of greater value than other carpet components. In contrast, current synthetic turf typically contains little or no nylon. Additionally, conventional carpet recycling methods produce, as described above, a dry powder that can be incorporated in small amounts into carpet backings. Alternatively, for synthetic turf recycling, it is desirable to recover and reuse most or all of the synthetic turf, and to do so in a way that the recycled synthetic turf makes up a large percentage of the turf into which it is incorporated.


There remains a need for a method of recycling and reusing an existing synthetic turf, or at least a portion of an existing synthetic turf, to avoid sending the entire synthetic turf to a landfill when it is no longer useful. There is also a need for a synthetic turf that can be recycled and reused.


SUMMARY

Embodiments of this invention include methods for recycling and reusing synthetic turf. Final products of embodiments of the disclosed recycling methods are materials that can be used as synthetic turf infill.


Embodiments of this invention include methods of recycling synthetic turf including agglomerating synthetic turf fragments to form granules, placing the granules in an extruder, and extruding the granules to form an extrudate, for example a strand or ribbon. Embodiments of this invention eliminate the need to separate all of the infill from synthetic turf before the turf is recycled by providing a method of recycling synthetic turf that is effective even if the turf contains at least some infill material, such as sand and/or rubber.


Other embodiments of this invention provide infill for a synthetic turf. Infill of these embodiments includes pellets comprising (a) polyethylene, polypropylene, or nylon or a combination thereof; (b) polyester or polypropylene or a combination thereof; and (c) polyurethane, latex, hot melt, or a thermoplastic, or a combination thereof. The infill may further include a filler, or a modifier, or combination thereof. Embodiments of this invention eliminate the need to separate infill from synthetic turf before recycling by providing a synthetic turf product having an infill material that itself is made from recycled materials and is recyclable. This infill material may also be separated from the synthetic turf and reused as infill instead of being disposed in a landfill.


In yet other embodiments, this invention provides synthetic turf including any infill as described herein. In some embodiments, the synthetic turf includes the infill described herein and also includes additional infill materials such as sand, gravel, polymer beads, rubber, or any infill material known in the art.





BRIEF DESCRIPTION OF THE DRAWINGS


FIG. 1 is a flow chart of a process for recycling synthetic turf.



FIG. 2 illustrates infill pellets according to one embodiment of the present invention.



FIG. 3 is a cross-section of an infill pellet according to one embodiment of the present invention.





DETAILED DESCRIPTION

Embodiments of this invention provide methods of recycling and reusing an existing synthetic turf or a portion of an existing synthetic turf. Other embodiments of this invention provide infill for a synthetic turf wherein the infill is recyclable and can be incorporated into a synthetic turf such that the synthetic turf may be recycled and reused.


Typically, synthetic turf includes a pile fabric having a backing and a plurality of upstanding ribbons, also called face fibers or filiform formations, resembling grass. Typically, the upstanding ribbons are made of polyethylene, polypropylene or a blend thereof. The ribbons may also be made of nylon or any other material known in the art alone or in combination with polypropylene and/or polyethylene. These face fibers are tufted or sewn into a primary backing material which can be made of a number of different materials including, but not limited to, polypropylene and polyester. A primary coating material, or precoat, is applied to the fiber and primary backing to hold the face fibers in place. The primary coating of most synthetic turfs includes polyurethane and also typically includes a filler such as calcium carbonate or coal fly ash. Primary coatings may also include latex, hot melt adhesives, and/or thermoplastics in addition to or instead of polyurethane. Synthetic turfs may also have a secondary coating which may be similar to the primary coating described herein. Synthetic turfs may also have a secondary backing which can be made of a number of different materials including, but not limited to, polypropylene and polyester.


The face fibers typically make up from about 19 wt % to about 80 wt % of a synthetic turf. The primary backing typically makes up from about 1 wt % to about 25 wt % of a synthetic turf. The primary coating typically makes up from about 15 wt % to about 80 wt % of a synthetic turf.


Synthetic turf may also include an infill material dispersed among the upstanding ribbons, which acts as a ballast and/or contributes to the physical properties of the turf, such as resiliency, that make the turf suitable for a particular use. Synthetic turf infill may be made of any material suitable for providing desired physical properties for the synthetic turf, but most often includes materials such as sand, gravel, cork, polymer beads, and rubbers, including but not limited to crumb rubber, ethylene propylene diene monomer (EPDM) rubber, and neoprene rubber.


The face fibers may include polyethylene, polypropylene, nylon, or other materials singly or in combination. The face fibers may include from about 0 wt % to about 100 wt % polyethylene, from about 0 wt % to about 100 wt % polypropylene, and from about 0 wt % to about 100 wt % nylon. In some embodiments, the face fibers include blends of polypropylene (PP) and polyethylene (PE) in any of the following ratios of PP:PE—5:95; 10:90; 50:50; 90:10; 95:5 or any ratio that is within these ranges of ratios. In some embodiments, the face fibers include blends of PP and nylon in any of the following ratios of PP:nylon—5:95; 10:90; 50:50; 90:10; 95:5 or any ratio that is within these ranges of ratios. In some embodiments, the face fibers include blends of PE and nylon in any of the following ratios of PE:nylon—5:95; 10:90; 50:50; 90:10; 95:5 or any ratio that is within these ranges of ratios. In some embodiments, the face fibers include blends of PP, PE, and nylon in any of the following ratios of PP:PE:nylon—10:10:80; 10:80:10; 80:10:10; 33:33:33 or any ratio that is within these ranges of ratios.


The primary backing may include polyester, polypropylene, and other materials singly or in combination. The primary backing may include from about 0 wt % to about 100 wt % polyester or from about 0 wt % to about 100 wt % polypropylene. In some embodiments, the primary backing includes blends of PP and polyester in any of the following ratios of PP:polyester—5:95; 10:90; 50:50; 90:10; 95:5 or any ratio that is within these ranges of ratios


The primary coating may include polyurethane, latex, hot melt adhesive, and/or thermoplastics alone or in combination. Suitable hot melt adhesives include, but are not limited to, Reynolds 54-041, Reynolds 54-854, DHM 4124 (The Reynolds Company P.O. Greenville, S.C., DHM Adhesives, Inc. Calhoun, Ga.). Suitable thermoplastics include, but are not limited to polypropylene, polyethylene and polyester. The primary coating may also include a filler that may be coal fly ash, calcium carbonate, iron oxide, or barium sulfate, or any other filler known in the art. The primary coating may include from about 0 wt % to about 100 wt % polyurethane, from about 0 wt % to about 100 wt % latex, from about 0 wt % to about 100 wt % hot melt adhesive, and/or from about 0 wt % to about 100 wt % thermoplastic. The primary coating may include from about 0 wt % to about 80 wt % filler. In some embodiments, the primary coating includes polyurethane, latex, or thermoplastic and from about 20 wt % to about 80 wt % filler, or from about 40 wt % to about 60 wt % filler. In other embodiments, the primary coating includes hot melts and from about 0 wt % to about 50 wt % filler, or from about 1 wt % to about 25 wt % filler. Several embodiments of primary coating and secondary backing compositions are shown below in Table 1.














TABLE 1








Hot





Polyurethane
Latex
Melt
Polypropylene
Polyester


Sample
wt %
wt %
wt %
wt %
wt %




















1
10-70

10-40
5-40



2
30-97



3-70


3
10-70

10-40

5-40


4
30-97


3-70


5
10-70
10-40

5-40


6

30-97


3-70


7


30-97

3-70


8
10-70
10-40


5-40


9

30-97

3-70


10


30-97
3-70









The methods described herein may be used to recycle and reuse synthetic turf, including turf described above, or other synthetic surfaces having chemical make-up similar to synthetic turf.


Recycling synthetic turf begins with the removal of the material from the point of installation. Typically for a sports field, the synthetic turf is installed by unrolling a 15 foot wide by 150 foot long roll of turf. A field typically requires multiple rolls, which are laid out on the field side by side and seamed together to form the field. Infill is then installed. The infill may be one or more of sand, rubber, and/or any other suitable material as described previously. When a synthetic turf is removed, typically some of the infill is separated from the remainder of the infill. The infill may be removed prior to the removal of the turf or at the same time. For example, a machine may collect the infill and place it into a container or onto the field. The turf and infill may be removed at the same time by a machine or by hand. The turf is cut and the infill is dumped out. The turf is then downsized into sections (e.g. 1 by 1 foot for ease and efficiency of shipping) that can be accepted by the next process. The downsizing may be accomplished by hand or machine. The machine may be large or small and may use rotary blades or knifes or any of a variety of different methods known in the art. The downsized pieces, also referred to as turf fragments, are typically placed on pallets and shipped to a recycling facility.


One method of recycling synthetic turf is described below. A plurality of synthetic turf fragments are agglomerated. The granules of agglomerated turf fragments are placed into an extruder. The granules are extruded to form an extrudate, for example in the shape of a strand or ribbon.


In some embodiments, the downsized pieces of synthetic turf are placed into an agglomerator. Suitable agglomerators include Condux agglomerators, Netplasmak NPS agglomerators, or tub densifiers. The downsized pieces of turf should be of a size suitable for agglomeration. A suitable size will depend on the agglomeration equipment employed. For example, agglomerating equipment such as a Condux can accept sizes of up to 2 square feet. In some embodiments, the synthetic turf fragments are equal to or less than about 1 square foot. In some embodiments, the turf fragments are less than 6 square inches. In some embodiments, the turf fragments are less than 3 square inches.


The step of agglomerating the turf fragments involves using mechanical energy to densify the components of the turf fragments into smaller and denser granules. During agglomeration, some of the synthetic turf components are mechanically melted. In some embodiments, no heat is added during agglomeration; however, frictional forces cause the lower melting components to melt. Lower melting components include any components that melt as a result of the mechanical mixing during the agglomeration process, and in some embodiments include polyethylene and polypropylene. Agglomeration may also include further reduction in the size of the turf fragments, and particularly of the high melting components. For example, in some embodiments polyurethane does not melt, but is reduced to a powder. During agglomeration, higher softening components, such as polyurethane and rubber, may be encapsulated by the lower melting components. The rate of agglomeration depends on a variety of factors including at least the size of the turf fragments and the composition of the turf fragments. In some embodiments the rate of agglomeration is from about 50 to about 2000 lbs/hour, or from about 100 to about 500 lbs/hour, or from about 250 to about 350 lbs/hour. In one embodiment, the agglomeration process produces granules of agglomerated material. These granules have the same or very similar chemical composition as the starting synthetic turf fragments.


As an example of the agglomeration process, in one embodiment, downsized material (i.e. turf fragments) is fed into the Condux machine by hand or by belt into a shredder which cuts the turf fragments into smaller pieces. The shredder uses a rotary blade inside a steel box to cut the downsized material into smaller pieces. These smaller pieces are then transferred to a holding box where the material falls through a screen which allows through only pieces of a set size or smaller. The larger pieces are blown back to the shredder to be further downsized. As the material passes through the screen it is fed into a screw or auger which feeds the material between two steel plates that face each other, one twists and the other is stationary. The plates are shaped to have room in the center and are close together at the edge which generates friction and heat to soften the material. As the material softens it combines with any other material present. The combination of materials is pushed out of the plates as a strand or in small pieces which can be further downsized if needed. No heat is added during the process; however, the material can reach temperatures ranging from approximately 250° F. to 400° F. due to the mechanical energy. The agglomerated pieces are transferred to a screen for sizing. Those that pass through are boxed. The larger agglomerated pieces are sent to another shredder and then collected. The agglomerated material may be in the form of granules.


In some instances, it may be desirable to add fillers, modifiers, colorants, or other additives to the granules of agglomerated material prior to extrusion. In some embodiments, these additives may aid in extrusion of the agglomerated material and/or impart desired properties to the pellets of extruded product. Accordingly, in one embodiment of the present invention the disclosed method further includes the step of adding fillers, modifiers, or other additives. These additives may be added prior to or during the extrusion process. When the additives are added prior to extrusion, they are premixed with the granules of agglomerated material and added to the extruder. In other embodiments, the additives may be added during extrusion. One of skill in the art can determine for a given process, whether it is advantageous to add the additives prior to or during extrusion. One factor in this determination may be the type of extruder used. For example, twin screw extruders can efficiently mix the granules of agglomerated turf material and additives together during extrusion.


Fillers may include but are not limited to calcium carbonate, coal fly ash, iron oxide, or barium sulfate, or other fillers known in the art. Modifiers, colorants, or other additives that are suitable for use with the present invention include, but are not limited to, plasticizers, elastomers, compatibilizers, colorants, antimicrobials, and UV stabilizers. Examples of modifiers that can be used are: wax:, EPDM rubber; high and low density polyethylene; high and low density polypropylene; ExxonMobil Vistamaxx™ 6102, ExxonMobil Vistamaxx 3000 Propylene-based elastorner, ExxonMobil Exact 9361 ethylene-based plastomer resin, and ExxonMobil Exact 9371 ethylene-based plastomer resin (all available from Exxon Mobil Chemical, Houston, Tex.); Faraprene 381-35A (available from O'Neil Color and Compounding, Jasper, Tenn.); and any number of other modifiers. Suitable colorants include dyes and pigments; red, green, blue, black or any number of different colors can be added. However, in some embodiments, colorants may have very little effect due to the dark nature of the material.


In some embodiments, granules of agglomerated material make up from about 10 wt % to about 90 wt % of the material that is extruded. In some embodiments, the amount of filler added prior to or during extrusion is from about 10 wt % to about 90 wt % of the material that is extruded. In some embodiments, the amount of filler added prior to or during extrusion is from about 10 wt % to about 70 wt % or from about 10 wt % to about 50 wt % of the material that is extruded. In some embodiments, the amount of modifier added prior to or during extrusion is from about 10 wt % to about 90 wt % of the material that is extruded. In some embodiments, the amount of modifier added prior to or during extrusion is from about 10 wt % to about 70 wt % or from about 10 wt % to about 50 wt % of the material that is extruded. In some embodiments, the amount of colorant added prior to or during extrusion is from about 1 wt % to about 10 wt % of the material that is extruded.


The step of extruding the agglomerated turf material may be carried out with any equipment suitable for extrusion. A number of different extruders may be used for this process depending upon the type of mixing or heating that is desired. Examples of suitable extruders include single screw and twin screw extruders. The twin screw extruder may have co-rotating or counter rotating screws and the single screw extruder has one rotating screw. The screws can be designed to do a multitude of things but having the capacity to heat and mix the material is essential. Extruders typically have variable screw speeds and variable heating as well as variable feed rates. The appropriate speed and heat rate is determined by the type of output desired.


Extrusion is carried out at elevated temperatures. In some embodiments the temperature during extrusion is between about 200° F. and about 500° F., or between about 250° F. and about 450° F. In some embodiments the temperature during extrusion is between about 350° F. and about 400° F. In some embodiments the rate of extrusion is from about 3 to about 50,000 lbs/hour, or from about 100 to about 500 lbs/hour, or from about 300 to about 500 lbs/hour. Extrusion can be carried out using any size die that will provide a product of the desired size, but in some embodiments is carried out using a die that is between about 102 and about 305 mm in diameter.


In some embodiments, the extrudate is cut into pellets or granules. Suitable equipment for pelletizing includes, but is not limited to, pelletizers made by Gala Industries Inc. (Eagle Rock, Va.). In some embodiments, the extrudate is cut into pellets immediately after it emerges from the die and may be simultaneously cooled using water. In other embodiments, the extrudate is extruded into a water bath and is then cut into the desired size and shape. In some embodiments, the final product of the extrusion step is pellets of any desired shape including, but not limited to, spherical, cylindrical, or oval/football shaped. The pellets may also be of an irregular shape. This irregular shape might be advantageous, for example, to aid tight packing of the granules. The size and quantity of the pellets produced depends upon the speed of the extruder and the cutting system. In some embodiments, pellet sizes vary from 0.05 mm to 9 mm. In some embodiments, pellet sized vary from 1 mm to 6 mm or from 1 mm to 3 mm. In one embodiment the pellets are around 200 pellets per gram with a football shape.


As an example of the extrusion process, in one embodiment, agglomerated material (granules) is mixed with a calcium carbonate filler and a modifier, Exxon 6102. The mixture is 50 wt % agglomerated material, 10 wt % calcium carbonate, and 40 wt % Exxon 6102. The mixture is poured into the feed system of an extruder. The mixture is heated to 400° F. and mixed at 500 rpm's. The duration of mixing relates to the size of the extruder and the speed of operation. The mixture is then pushed out of the extruder by the screws through a plate on the end of the extruder. The plate has a multiplicity of small holes which may vary in size from about 0.5 mm to about 15 mm, through which the material is extruded. Strands of extruded material are produced. In one embodiment, the strands are then cooled in a water bath and cut by a strand cutter producing a pellet that has irregular edges. In another embodiment, the strands are fed into a water ring which cuts the strands and drops the pellet into water. This process can produce a football shaped pellet. In another embodiment, the strands are fed into a Gala cutting system that cuts the strand underwater, which produces a round pellet of about 0.05 mm to about 3 mm.


In one embodiment, the disclosed method further includes the step of separating at least 90% of non-recyclable components from the synthetic turf before the step of agglomerating the synthetic turf fragments. Many conventional synthetic turfs include large quantities of infill materials such as sand, gravel, and rubber. These materials, however, are not generally considered recyclable and are not favored for use in the recycling method described herein. Accordingly, in some instances, it may be desirable to remove at least some of the infill, or other components, of an existing synthetic turf before subjecting that synthetic turf to the recycling method described above. Separating the non-recyclable infill or other non-recyclable components may be accomplished before or after the synthetic turf is size reduced to turf fragments. In some embodiments, a portion of non-recyclable infill material is separated from the remaining synthetic turf. In some embodiments, at least 80% of the non-recyclable infill material is separated from the remaining synthetic turf. In some embodiments, at least 90% of the non-recyclable infill material is separated from the remaining synthetic turf. In some embodiments, at least 95% of the non-recyclable infill material is separated from the remaining synthetic turf. In some embodiments, at least 98% of the non-recyclable infill material is separated from the remaining synthetic turf.


One of skill in the art would recognize that the methods disclosed herein are not limited to use with synthetic turf, but are suitable for recycling other products made of similar materials.


Embodiments of this invention also provide infill for a synthetic turf. In some embodiments, the infill includes a material (for example particles or pellets) made from recycled synthetic turf. The terms particle and pellet are used interchangeably herein. In some embodiments, the infill is made by a process described herein.


In one embodiment the infill is a pellet or particle that is a mixture (a) polyethylene, polypropylene, or nylon or a combination thereof; (b) polyester or polypropylene or a combination thereof; and (c) polyurethane, latex, hot melt, a thermoplastic, polypropylene or polyethylene or a combination thereof. The pellets may include any component used in a synthetic turf, including but not limited to components used as the face fibers, the primary backing, the primary coating, and the infill as described previously herein. In some embodiments, sand, gravel, and rubber are present only as impurities and make up less than about 5 wt % of the infill pellets. In some embodiments, sand, gravel, and rubber make up less than 2 wt % of the infill pellets. In some embodiments, sand, gravel, and rubber are not present in the infill pellets.


In some embodiments the infill pellets of the present invention include: from about 19 wt % to about 80 wt % PE, PP, or nylon, or a combination thereof; from about 1 wt % to about 25 wt % PP or polyester, or a combination thereof; and from about 15 wt % to about 80 wt % polyurethane, latex, hot melt, or thermoplastic, or a combination thereof.


In some embodiments, infill pellets of the present invention include from about 10 wt % to about 90 wt % of recycled synthetic turf material. The percentage of recycled material in the final product may vary depending on the intended use for the pellets. For example, if more filler or modifier is required for a given use, the percentage of filler would be higher and the percentage of recycled material in the pellets would necessarily be lower. In some embodiments the infill functions as a ballast material. This infill may need more filler to increase the specific gravity of the pellets. In other embodiments, a material to be used as an infill for a playing surface may require less filler, but may also require additives for softness. The increased percentage of additives will influence the percentage of recycled material in the infill.


The pellets may be any desired shape. For example, in some embodiments the pellets can be substantially spherical, cylindrical, oval/football shaped, or may be an irregular shape. Different shapes may be advantageous for different uses. For example, irregularly shaped pellets may more efficiently than regularly shaped pellets. The extent of packing of the pellets can affect the physical properties of a synthetic turf that includes the pellets. The pellets may be any desired size but is typically from about 0.5 mm to about 9 mm. In some embodiments, the infill pellets are between about 1 mm and about 6 mm, or between about 1 mm and about 3 mm.


In some embodiments, the pellets are elastomeric. In some embodiments the durometer, or hardness, of the pellets may be between about 50 and about 100 using Shore OO. In some embodiments the density of the pellets is between about 40 to about 400 pellets/gram, or from about 2.5 to about 25 mg per pellet.


In some embodiments, the pellet is a mixture of components wherein the mixture has two or more phases. For example, the mixture may be a heterogeneous dispersion having a continuous phase and at least one disperse phase. The continuous phase includes lower melting components that have been melted and blended in a process such as agglomeration. The continuous phase may also be a mixture of these lower melting components and filler, such as calcium carbonate. The disperse phase includes higher melting components such as rubbers that are at least partially surrounded by the lower melting components of the continuous phase.


The physical properties of the pellets described herein can be adjusted by one skilled in the art at least by varying the size of the pellets, the shape of the pellets, and/or the composition of the pellets. For example, one of skill in the art would understand that the properties of the pellet may be adjusted by adjusting the amount of filler, additive, and/or modifiers. Thus, the pellets described herein can be made to have any desired physical property and are, thus, suitable for use in any synthetic turf.


Another embodiment of the invention is a synthetic turf that includes any of the pellets described above. This synthetic turf is suitable for a variety of uses, including but not limited to, athletic fields, landscaping, dog runs, putting greens, jogging paths, paintball fields, tennis courts, and playgrounds. Desired properties for a synthetic turf vary depending on the intended use of the turf. For example, depending on the intended use of the turf, one might prefer a softer surface (e.g. for playgrounds), a harder surface (e.g. for putting greens), or a surface that allows ideal ball bounce and/or ball roll (e.g. for athletic fields). Pellets described herein can be used to impart a variety of advantageous properties to synthetic turfs.


One important property of a synthetic turf is its capacity to absorb an impact, called the surface absorption, or G-Max. In some embodiments, synthetic turfs including the infill described herein have G-max values from about 75 to about 200. In some embodiments, the G-max values are from about 90 to 130.


A related property is the hardness of the synthetic turf. One measurement of the hardness of a synthetic turf is the force reduction value, also called the kraftabbau value. In some embodiments, synthetic turfs including the infill described herein have force reduction values from about 50 to about 75. In some embodiments, the force reduction values are from about 55 to about 70.


In some embodiments, a synthetic turf including infill pellets as described herein may also include another type of infill. This other type of infill may be any other infill used in synthetic turf including but not limited to sand, gravel, cork, polymer beads and rubbers. In some embodiments, multiple types of infill may be mixed together in a single layer in the synthetic turf. In other embodiments multiple types of infill may be disposed in a synthetic turf individually as discrete layers. Still other embodiments may include some combination of mixing and layering different types of infill.



FIG. 1 is a flow chart showing a process for recycling synthetic turf.



FIG. 2 is a brightfield reflected light image showing the surface of an infill pellet 10 according to one embodiment of the present invention. A disperse phase 12 appears as the dark inclusion on the surface of the infill pellet 10. The continuous phase 14 appears as lighter area of the surface of the infill pellet 10. In this embodiment, the disperse phase 12 includes butadiene rubber, and the continuous phase 14 includes polyethylene, polypropylene and calcium carbonate filler.



FIG. 3 is a brightfield reflected light image showing a cross-section of an infill pellet 20 according to one embodiment of the present invention. The pellet was cut at room temperature with a razor before the image was taken. As in FIG. 1, the disperse phase 22 appears as dark inclusions in the cross section of the infill pellet 20. The continuous phase 24 appears as the lighter areas of the infill pellet 20.


The following examples will serve to further illustrate the present invention without, at the same time, however, constituting any limitation thereof. On the contrary, it is to be clearly understood that resort may be had to various embodiments, modifications and equivalents thereof which, after reading the description herein, may suggest themselves to those skilled in the art without departing from the spirit of the invention.


EXAMPLE 1

Agglomerated material (granules), 50%; wax, 25%; calcium carbonate, 24%; and green dye, 1% were mixed together. The mixture was processed through a twin screw extruder at a temperature of between about 250° F. and about 450° F. at about 300 rpm for 10 to 20 seconds and strand cut. The pellet count was approximately 85 pellets per gram, or about 11.8 mg/pellet.


EXAMPLE 2

Agglomerated material (granules), 45%; Faraprene 381-35A, 45%; and calcium carbonate, 10% were processed through a twin screw extruder at a temperature of between about 250° F. and about 450° F. at about 300 rpm for 10 to 20 seconds and cut with a Gala underwater cutter. The pellet count was approximately 185 pellets per gram, or about 5.4 mg/pellet.


EXAMPLE 3

A mixture of agglomerated material (granules), 50% and Exxon 6102, 50% was processed through a twin screw extruder at a temperature of about 250° F. to about 450° F. at about 300 rpm for 10 to 20 seconds and cut with a strand cutter. The pellet count was approximately 85 pellets per gram, or about 11.8 mg/pellet.


EXAMPLE 4

The pellets from Example 1 were placed into a sample of synthetic turf. The turf sample was placed on a LisPort tester and tested. The material flattened quickly and the test was stopped before completion. No further data was generated from this sample.


EXAMPLE 5

The pellets from Example 2 were placed into a sample of synthetic turf. The turf sample was placed on a LisPort tester and tested for 80 hours. A G-max test was performed before, during, and after the LisPort testing to check the integrity of the turf sample and the pellets. The turf and the pellets both appeared to have little wear after the testing. G-max data for this test is shown in Table 2. Concrete and stone refer to the base that the turf is sitting on when tested.













TABLE 2









0 hours
24 hours
32 hours













Sample
Concrete
Stone
Concrete
Stone
Concrete
Stone





2
132
120
n/a
141
174
116


3
143
124
n/a
146
120
136














40 hours
+0 hours
80 hours













Sample
Concrete
Stone
Concrete
Stone
Concrete
Stone





2
237
149
129
121
156
164


3
180
162
147
125
137
152









EXAMPLE 6

The pellets from Example 2 were placed on the Roll Stool and tested. The Roll Stool is a test apparatus for wear testing the durability of floor coverings. The sample was tested to 10,000 cycles with good results. The tuft bind, a measure of the amount of force used to pull the turf yarn from the primary backing, was around 7.5 pounds as tested on a Twing Albert Tensile Tester according to ASTM standard D 1335-05.


EXAMPLE 7

The pellets from Example 3 were placed into a sample of synthetic turf. The turf sample was placed on a LisPort tester and tested for about 40 hours. The G-max at the start of the test was 125, and the G-max at the end of the test was 150. Both G-max values are considered good.


EXAMPLE 8

The pellets from Example 3 were placed on a the Roll Stool. The results were good after 10,000 cycles; however, some wear was observed on the pellets.


EXAMPLE 9

The pellets from Example 2 were extruded onto the back of a synthetic turf as a backing. The sample was placed on the roll stool and tested. The sample was tested to 10,000 cycles with good results. Little to no wear or deterioration of the sample was observed.


All patents, publications and abstracts cited above are incorporated herein by reference in their entirety. It should be understood that the foregoing relates only to preferred embodiments of the present invention and that numerous modifications or alterations may be made therein without departing from the spirit and the scope of the present invention as defined in the following claims.

Claims
  • 1. A method of recycling synthetic turf comprising: providing synthetic turf fragments comprising a backing and face fibers and including infill contained therein, wherein the turf fragments further comprise a thermoset polyurethane; removing from at least 80% to 98% of the infill from the synthetic turf fragments; agglomerating the synthetic turf fragments to form granules; placing the granules in an extruder; and, extruding the granules to form an extrudate.
  • 2. The method of claim 1 wherein at least 80% to from at least 95% of the infill is removed.
  • 3. The method of claim 1, further comprising adding a filler, a modifier, or a colorant, or a combination thereof to the granules before or during the step of extruding.
  • 4. The method of claim 3, wherein the granules, the filler and the modifier are combined together to form a combination such that granules are present in an amount of about 10 wt % to about 90 wt % of the combination, the filler is absent or present in an amount of about 0 wt % to about 50 wt % of the combination, and the modifier is present in an amount of about 10 wt % to about 90 wt % of the combination.
  • 5. The method of claim 3, wherein the filler is calcium carbonate, barium sulfate, coal fly ash, or iron oxide or a combination thereof.
  • 6. The method of claim 3, wherein the modifier is polypropylene, polyethylene, rubber, ExxonMobil Vistamaxx 3000 Propylene-based elastomer, Exxon PX 9361, ExxonMobil Exact 9371 ethylene-based plastomer resin, or Faraprene 381-35A, or a combination thereof.
  • 7. The method of claim 1, further comprising cutting the extrudate into pellets.
  • 8. The method of claim 1, wherein the step of agglomerating the synthetic turf fragments comprises mechanically melting the synthetic turf fragments and reducing the size of the synthetic turf fragments.
  • 9. The method of claim 1, wherein the step of extruding the granules comprises heating and mixing the granules.
  • 10. The method of claim 3, wherein the step of extruding the granules comprises heating and mixing the granules with the filler, the modifier, or the colorant or the combination thereof
  • 11. The method of claim 1, wherein the synthetic turf comprises: face fibers; the backing; and, a primary coating.
  • 12. The method of claim 11, wherein the face fibers comprise polyethylene, polypropylene or nylon or a combination thereof.
  • 13. The method of claim 11, wherein the backing comprises polyester or polypropylene or a combination thereof
  • 14. The method of claim 11, wherein the primary coating comprises polyurethane, latex, hot melt, or a thermoplastic or a combination thereof.
  • 15. The method of claim 12, wherein the polyethylene, polypropylene or nylon or the combination thereof comprise about 19 wt % to about 80 wt % of the synthetic turf fragments.
  • 16. The method of claim 13, wherein the polyester or polypropylene or the combination thereof comprise about 1 wt % to about 25 wt % of the synthetic turf fragments.
  • 17. The method of claim 14, wherein the polyurethane, latex, hot melt, or the thermoplastic, or the combination thereof comprise about 15 wt % to about 80 wt % of the synthetic turf fragments.
  • 18. The method of claim 1 wherein the granules placed in the extruder range in average size from about 1 millimeter to about 6 millimeters.
CROSS REFERENCE TO RELATED APPLICATIONS

This application claims priority to U.S. Provisional Application No. 61/122,592 filed Dec. 15, 2008, which is hereby incorporated by reference in its entirety.

US Referenced Citations (163)
Number Name Date Kind
3596576 Cicero et al. Aug 1971 A
3917498 O'Shima Nov 1975 A
4268551 Moore, Jr. May 1981 A
4337283 Haas, Jr. Jun 1982 A
4356220 Benedyk Oct 1982 A
4389434 Polman Jun 1983 A
4396653 Tomarin Aug 1983 A
4497853 Tomarin Feb 1985 A
4735825 Friedrich Apr 1988 A
4738407 Arrant Apr 1988 A
4882208 Breitscheidel et al. Nov 1989 A
5009586 Pallmann Apr 1991 A
5041320 Meredith et al. Aug 1991 A
5185380 Diessel et al. Feb 1993 A
5225130 Deiringer Jul 1993 A
5288349 Fink Feb 1994 A
5312573 Rosenbaum et al. May 1994 A
5424013 Lieberman Jun 1995 A
5565158 Sullivan et al. Oct 1996 A
5591802 David et al. Jan 1997 A
5848940 Yamada Dec 1998 A
5859071 Young et al. Jan 1999 A
5958527 Prevost Sep 1999 A
5976645 Daluise et al. Nov 1999 A
6029397 Motz et al. Feb 2000 A
6173528 Motz et al. Jan 2001 B1
6221445 Jones Apr 2001 B1
6237208 Meeth May 2001 B1
6299959 Squires et al. Oct 2001 B1
6491991 Seaton Dec 2002 B2
6527889 Paschal et al. Mar 2003 B1
6551689 Prevost Apr 2003 B1
6582819 McDaniel et al. Jun 2003 B2
6590042 Tang Jul 2003 B1
6616542 Reddick Sep 2003 B1
6672749 Nicholls et al. Jan 2004 B2
6689447 Prevost Feb 2004 B2
6723413 Walters Apr 2004 B2
6740387 Lemieux May 2004 B1
6746752 Prevost Jun 2004 B2
6753049 De Vries Jun 2004 B2
6767595 Prevost et al. Jul 2004 B2
6793164 Stroppiana Sep 2004 B2
6797216 Furgiuele et al. Sep 2004 B2
6800339 Motz et al. Oct 2004 B2
6805936 Seaton Oct 2004 B2
6814826 Bell Nov 2004 B1
6818274 Buck et al. Nov 2004 B1
6855650 Bohannon, Jr. Feb 2005 B1
6881793 Sheldon et al. Apr 2005 B2
6884509 Huff et al. Apr 2005 B2
6887535 Stroppiana May 2005 B2
6936201 Desai et al. Aug 2005 B2
6950599 Nicholls et al. Sep 2005 B2
6951670 Stroppiana Oct 2005 B2
6955841 Weghuis et al. Oct 2005 B2
6989179 Prevost et al. Jan 2006 B2
7001554 Bohannon Feb 2006 B2
7060334 Stroppiana Jun 2006 B2
7081283 Straughn Jul 2006 B2
7144609 Reddick Dec 2006 B2
7153553 Tetrault Dec 2006 B2
7155796 Cook Jan 2007 B2
7166340 Clark Jan 2007 B1
7171780 Hudson Feb 2007 B1
7245815 Nicholls et al. Jul 2007 B2
7250451 Tang Jul 2007 B2
7264854 Stroppiana Sep 2007 B2
7273642 Prevost Sep 2007 B2
7300689 Prevost Nov 2007 B2
7306838 Prevost Dec 2007 B2
7357966 Dipple et al. Apr 2008 B2
7386925 Germer Jun 2008 B2
7399514 De Clerck Jul 2008 B2
8110131 Dell'Orco et al. Feb 2012 B1
20010005958 Casimaty Jul 2001 A1
20010008322 Rosenbaum Jul 2001 A1
20010009710 Zegler et al. Jul 2001 A1
20010033902 Seaton Oct 2001 A1
20010046589 Stroppiana Nov 2001 A1
20010048177 Close et al. Dec 2001 A1
20020028307 Prevost Mar 2002 A1
20020029515 Prevost Mar 2002 A1
20020031653 Ricciardelli et al. Mar 2002 A1
20020039636 Fink et al. Apr 2002 A1
20020081399 Prevost et al. Jun 2002 A1
20020091011 Sosin Jul 2002 A1
20020096796 Estrada Jul 2002 A1
20020132067 Cartwright et al. Sep 2002 A1
20020159275 Nicholls et al. Oct 2002 A1
20030039773 Paschal et al. Feb 2003 A1
20030056432 Prevost Mar 2003 A1
20030106949 Stroppiana Jun 2003 A1
20030108688 De Vries Jun 2003 A1
20030118755 Motz et al. Jun 2003 A1
20030122283 Estrada Jul 2003 A1
20030157275 Weghuis et al. Aug 2003 A1
20040001951 Slootweg et al. Jan 2004 A1
20040013870 Sheldon et al. Jan 2004 A1
20040028841 Motz et al. Feb 2004 A1
20040033322 Stroppiana Feb 2004 A1
20040037975 Stroppiana Feb 2004 A1
20040214000 Huff et al. Oct 2004 A1
20040234719 Jones Nov 2004 A1
20050003193 Stroppiana Jan 2005 A1
20050008793 Prevost Jan 2005 A1
20050064112 Nicholls et al. Mar 2005 A1
20050096400 Villwock et al. May 2005 A1
20050130517 Bohannon, Jr. Jun 2005 A1
20050158482 Cook Jul 2005 A1
20060003893 Pursell et al. Jan 2006 A1
20060006564 Maldas et al. Jan 2006 A1
20060013989 Stull et al. Jan 2006 A1
20060045994 Dipple et al. Mar 2006 A1
20060093783 De Clerck May 2006 A1
20060100342 Jensen May 2006 A1
20060147670 Reddick Jul 2006 A1
20060148646 Pursell et al. Jul 2006 A1
20060172092 Tetrault Aug 2006 A1
20060204710 De Vries Sep 2006 A1
20060258811 Barcus et al. Nov 2006 A1
20070007682 Maldas et al. Jan 2007 A1
20070043128 Jenkines et al. Feb 2007 A1
20070049694 Koch et al. Mar 2007 A1
20070101566 Cook May 2007 A1
20070148398 Stroppiana Jun 2007 A1
20070154661 Stroppiana Jul 2007 A1
20070160800 Reddick Jul 2007 A1
20070166507 Atsma et al. Jul 2007 A1
20070275207 Higgins et al. Nov 2007 A1
20080020174 Stull et al. Jan 2008 A1
20080029917 Maldas et al. Feb 2008 A1
20080044598 Stroppiana Feb 2008 A1
20080044599 Stroppiana Feb 2008 A1
20080069642 Ayers et al. Mar 2008 A1
20080083103 Germer Apr 2008 A1
20080090955 Lambert et al. Apr 2008 A1
20080104914 Lemieux May 2008 A1
20080128933 Przybylinski et al. Jun 2008 A1
20080141516 Julicher et al. Jun 2008 A1
20080145574 Julicher et al. Jun 2008 A1
20080176009 Chereau et al. Jul 2008 A1
20080176010 Sawyer et al. Jul 2008 A1
20080182040 Chereau et al. Jul 2008 A1
20080187689 Dierkens et al. Aug 2008 A1
20080193226 Jones et al. Aug 2008 A1
20080206381 Price Aug 2008 A1
20080213515 Vey et al. Sep 2008 A1
20080219770 Prevost et al. Sep 2008 A1
20080248887 Shaneour Oct 2008 A1
20080260974 Morton-Finger Oct 2008 A1
20080260975 Morton-Finger Oct 2008 A1
20080268184 Cook Oct 2008 A1
20080274307 Chereau et al. Nov 2008 A1
20080280075 Reijen Nov 2008 A1
20080292819 Weghuis et al. Nov 2008 A1
20080299331 Gilardi Dec 2008 A1
20080317978 Smit et al. Dec 2008 A1
20090008824 Satori et al. Jan 2009 A1
20090011152 Stroppiana Jan 2009 A1
20090011845 Weber et al. Jan 2009 A1
20090286017 Horio et al. Nov 2009 A1
20100247814 Nisikawa et al. Sep 2010 A1
Foreign Referenced Citations (109)
Number Date Country
2514684 Feb 2007 CA
2521150 Feb 2007 CA
2597364 Feb 2008 CA
2639586 Oct 2008 CA
101135066 Mar 2008 CN
4130082 Mar 1992 DE
4120693 Dec 1992 DE
4136444 May 1993 DE
0136747 Dec 1986 EP
0259940 Jul 1992 EP
0848660 Jun 1998 EP
0906365 Apr 1999 EP
0737214 Mar 2001 EP
0996781 Oct 2002 EP
0899294 Apr 2003 EP
1319753 Jun 2003 EP
1378592 Jan 2004 EP
1389649 Feb 2004 EP
1394324 Mar 2004 EP
1353798 Dec 2004 EP
1591476 Nov 2005 EP
1486613 Apr 2007 EP
1803841 Jul 2007 EP
1889954 Feb 2008 EP
1584644 Mar 2008 EP
1416009 Jul 2008 EP
1950350 Jul 2008 EP
1967651 Sep 2008 EP
1972703 Sep 2008 EP
1983104 Oct 2008 EP
2119829 Nov 2009 EP
1889954 Mar 2010 EP
2155327 Sep 1985 GB
2196539 May 1988 GB
2372455 Aug 2002 GB
52070539 Jun 1977 JP
61098802 May 1986 JP
61102905 May 1986 JP
61130502 Jun 1986 JP
63063802 Mar 1988 JP
2167904 Jun 1990 JP
3072102 Mar 1991 JP
4120304 Apr 1992 JP
4120306 Apr 1992 JP
4197612 Jul 1992 JP
4309606 Nov 1992 JP
05200749 Aug 1993 JP
5302304 Nov 1993 JP
6193010 Jul 1994 JP
6240507 Aug 1994 JP
6240616 Aug 1994 JP
6280217 Oct 1994 JP
7137172 May 1995 JP
8000110 Jan 1996 JP
8003917 Jan 1996 JP
8120614 May 1996 JP
09003813 Jan 1997 JP
9041315 Feb 1997 JP
10018213 Jan 1998 JP
11209915 Aug 1999 JP
11293619 Oct 1999 JP
2000008314 Jan 2000 JP
2000017605 Jan 2000 JP
2000314103 Nov 2000 JP
2001254310 Sep 2001 JP
2002192120 Jul 2002 JP
2002242120 Aug 2002 JP
2004060393 Feb 2004 JP
2004092111 Mar 2004 JP
2005002783 Jan 2005 JP
2006233596 Sep 2006 JP
2007327314 Dec 2007 JP
2008180074 Aug 2008 JP
2008220744 Sep 2008 JP
2008222952 Sep 2008 JP
19970010719 Jan 1996 KR
20070097446 Oct 2007 KR
100799262 Jan 2008 KR
100834039 May 2008 KR
100834040 May 2008 KR
510405 May 1999 SE
445333 Jul 2001 TW
WO-9300396 Jan 1993 WO
WO-9418394 Aug 1994 WO
WO-9605374 Feb 1996 WO
WO-9949137 Sep 1999 WO
WO-0137657 May 2001 WO
WO-0209825 Feb 2002 WO
WO-0234860 May 2002 WO
WO-2004015009 Feb 2004 WO
WO-2004109017 Dec 2004 WO
WO-2005042135 May 2005 WO
WO-2005047602 May 2005 WO
WO-2005073297 Aug 2005 WO
WO-2006092337 Sep 2006 WO
WO-2006109110 Oct 2006 WO
WO-2006136436 Dec 2006 WO
WO-2007010324 Jan 2007 WO
WO-2007039191 Apr 2007 WO
WO-2008033342 Mar 2008 WO
WO-2008033343 Mar 2008 WO
WO-2008051073 May 2008 WO
WO-2008057881 May 2008 WO
WO-2008057886 May 2008 WO
WO-2008098905 Aug 2008 WO
WO-2008115085 Sep 2008 WO
WO-2008125895 Oct 2008 WO
WO2009078128 Jun 2009 WO
WO-2010075098 Jul 2010 WO
Non-Patent Literature Citations (2)
Entry
International Search Report and Written Opinion dated Mar. 26, 2010 in PCT/US2009/068090.
International Preliminary Report on Patentability dated Jun. 30, 2011 in PCT/US2009/068090.
Related Publications (1)
Number Date Country
20100151158 A1 Jun 2010 US
Provisional Applications (1)
Number Date Country
61122592 Dec 2008 US