Extrusion coating of elongated substrates

Information

  • Patent Grant
  • 9919503
  • Patent Number
    9,919,503
  • Date Filed
    Tuesday, September 16, 2014
    9 years ago
  • Date Issued
    Tuesday, March 20, 2018
    6 years ago
Abstract
The present disclosure relates to extrusion coating systems, extrusion coated substrates, and processes for making the same. In some aspects, extrusion coating systems as described herein may include an at least partially insulated outlet wall, which may facilitate production of coated substrates exhibiting a very desirable surface texture and appearance. Coated substrates of the present invention may be utilized in a variety of end applications, including, but not limited to, interior and exterior construction materials for homes, buildings, and furniture.
Description
FIELD OF THE INVENTION

This invention relates to processes and systems for coating substrates.


BACKGROUND

Various methods for applying coatings to a substrate are known in the art. One method of coating a substrate includes extrusion coating a substrate with a thermoplastic coating material. Such extrusion coated articles can be useful in a wide variety of applications, including, for example, as interior and exterior construction materials for homes, buildings, and furniture. According to this coating method, a substrate comprising wood, plastic, metal, or other desirable material, is passed through an extruder and a coating material is applied to at least a portion of the surface of the substrate. Once coated, the article is allowed to cool and the final coated substrate preferably exhibits enhanced aesthetic (e.g., gloss and surface smoothness) characteristics.


As the coated substrate exits the coating die and enters the cooling zone, water and other volatile material within the substrate may vaporize, thereby causing undesirable bubbles or blisters in the coating along the surface of the finished product. While at least partially submerging the coated substrate in a quench liquid has been found to help minimize this type of bubbling, quench cooling has also been observed to create a certain surface roughness that degrades the visual acceptability of the final product. Even substrates that show little or no blistering without a quench bath tend to exhibit undesirable surface texture when exposed to a quench liquid cooling bath.


Thus, a need exists for an extrusion coating process and system capable of producing coated substrates that exhibit an acceptable surface texture and appearance. It is also desirable that such a process and system could be economically implemented to existing extrusion coating systems, while minimizing process time and maximizing production rate.


SUMMARY

One embodiment of the present invention concerns a process for coating a substrate. The process comprises the steps of (a) introducing an elongated substrate and a coating material into a die; (b) contacting said substrate with said coating material in said die to thereby provide a coated substrate; (c) removing said coated substrate from said die via a die outlet defined by a die outlet wall of said die; (d) passing said coated substrate removed from said die outlet through a shaped passageway formed in an insulating member affixed to said die outlet wall and having a thermal conductivity less than the thermal conductivity of said die outlet wall; and (e) cooling said coated substrate withdrawn from said insulating member via contact with a quench fluid to thereby provide a cooled coated substrate.


Another embodiment of the present invention concerns a system for applying coating material to a substrate. The system comprises a die for contacting the elongated substrate with the coating material to thereby produce a coated substrate. The die comprises an inlet wall, an outlet wall, and a coating chamber disposed at least partially therebetween. The inlet wall defines a die inlet for receiving said elongated substrate into said die and the outlet wall defines a die outlet for discharging said coated substrate from said die. The system further comprises an insulating member affixed to said outlet wall. The insulating member has a thermal conductivity less than the thermal conductivity of said outlet wall and defines a shaped passageway configured to at least partially surround said die outlet thereby allowing said coated substrate exiting said die outlet to pass through said insulating member. The system also comprises a quench zone located adjacent said insulating member for cooling said coated substrate discharged from said shaped passageway of said insulating member.


Yet another embodiment of the present invention concerns a process for coating an elongated substrate. The process comprises the steps of (a) pushing an elongated substrate into an inlet of an extrusion coating die; (b) passing said elongated substrate through said die along a substantially horizontal die axis; (c) introducing a coating material into said die; (d) during at least a portion of said passing, contacting said substrate with said coating material introduced into said die to thereby provide a coated substrate; (e) removing said coated substrate from said die via a die outlet defined within an outlet wall of the die; and (f) cooling said coated substrate removed from said die outlet via contact with a quench liquid to thereby provide a cooled, coated substrate, wherein said cooled coated substrate has an average Rmax surface roughness of not more than 30.


Still another embodiment of the present invention concerns a coated article comprising an elongated substrate; and a thermoplastic resin coating extrusion coated onto said substrate. The coated article is a water-quenched article that has not been subjected to a post-quench treatment step and has an average Rmax surface roughness of not more than 30.





BRIEF DESCRIPTION OF THE DRAWINGS

Various embodiments of the present invention are described in detail below with reference to the attached drawing figures, wherein:



FIG. 1 is a process flow diagram of a coating system configured according to one embodiment of the present invention;



FIG. 2 is a perspective view of a die assembly capable of extrusion coating an elongated substrate according to one embodiment of the present invention;



FIG. 3 is an exploded perspective view of the die assembly depicted in FIG. 2, particularly illustrating the insulating member affixed to the outlet wall of the die;



FIG. 4a is a partial rotated exploded view of the die outlet wall and insulating member of the die assembly illustrated in FIGS. 2 and 3;



FIG. 4b is a perspective view of an insulating member affixed to the die outlet wall, particularly illustrating the minimum distance between the insulating member and the die outlet;



FIG. 5a is an extrusion coated article according to one embodiment of the present invention;



FIG. 5b is an extrusion coated article according to another embodiment of the present invention;



FIG. 5c is an extrusion coated article according to yet another embodiment of the present invention;



FIG. 5d is an extrusion coated article according to still another embodiment of the present invention;



FIG. 6a is a scanning electron microscope (SEM) image taken along a portion of the surface of the substrate coated in Example 34 at a magnification of 250 times (250×);



FIG. 6b is an SEM image taken along a portion of the surface of the substrate coated in Example 35 at a magnification of 250×;



FIG. 6c is an SEM image taken along a portion of the surface of the substrate coated in Example 37 at a magnification of 250×;



FIG. 6d is an SEM image taken along a portion of the surface of the substrate coated in Example 39 at a magnification of 250×;



FIG. 6e is an SEM image taken along a portion of the surface of the substrate coated in Example 41 at a magnification of 250×;



FIG. 6f is an SEM image taken along a portion of the surface of the substrate coated in Example 36 at a magnification of 250×;



FIG. 6g is an SEM image taken along a portion of the surface of the substrate coated in Example 38 at a magnification of 250×;



FIG. 6h is an SEM image taken along a portion of the surface of the substrate coated in Example 40 at a magnification of 250×;



FIG. 6i is an SEM image taken along a portion of the surface of the substrate coated in Example 42 at a magnification of 250×;



FIG. 7a is an SEM image taken along a portion of the surface of the substrate coated in Example 43 at a magnification of 250×;



FIG. 7b is an SEM image taken along a portion of the surface of the substrate coated in Example 44 at a magnification of 250×; and



FIG. 7c an SEM image taken along a portion of the surface of the substrate coated in Example 45 at a magnification of 250×.





DETAILED DESCRIPTION

Processes and systems configured according to embodiments of the present invention may be useful for applying a coating material to at least a portion of a substrate. In some embodiments, processes and systems described herein may be useful for extrusion coating a polymeric material onto an elongated substrate to thereby provide an extrusion-coated substrate having an acceptable visual appearance. In particular, the coated substrate may exhibit a substantially bubble-free and non-textured surface, a combination which has heretofore been difficult to achieve using conventional coating methods. Coated substrates produced according to various embodiments of the present invention can be utilized for a variety of applications. In one embodiment, coated substrates or articles may be selected from the group consisting of interior and exterior construction materials, including, but not limited to, door jambs, window jambs, other door or window parts, flat panel shelving, pultrusion articles, exterior molding, exterior trim, and interior or exterior siding. Additional details regarding embodiments of the present invention will now be discussed in detail, with reference to the drawing figures.


Referring initially to FIG. 1, a schematic flow diagram of a coating system 12 configured according to one embodiment of the present invention is provided. Coating system 12 includes a pretreatment zone 14, a drying zone 16, an optional staging area 18, a die 20, a quench zone 22, and an optional post treatment zone 24. As shown in FIG. 1, a substrate can be sequentially passed through pretreatment zone 14, drying zone 16, and optional staging area 18 before being introduced into die 20. Die 20 is configured to facilitate contact between at least a portion of the surface of the substrate and a coating material introduced into die 20 from a coating source 30. The resulting coated article is cooled in quench zone 22 before being optionally treated in a post treatment zone 24. If not further processed in post-treatment in zone 24, the cooled, coated substrate may simply be removed from coating system 12, as indicated by line 26.


Coating system 12 can be configured to process any substrate capable of being extrusion coated. In some embodiments, the substrates employed in coating system 12 may be rigid or substantially rigid substrates, and, in the same or other embodiments, may not be a wire, a tube, or a co-extruded substrate. The substrates coated in coating system 12 may also be elongated substrates having any suitable dimensions. According to one embodiment, the substrate may have a length, or largest dimension, of at least about 5 feet, at least about 6 feet, at least about 8 feet, at least about 10 feet, at least about 12 feet and/or not more than about 25 feet, not more than about 20 feet, or not more than about 15 feet. In the same or another embodiment, the substrate can have a length in the range of from about 5 feet to about 25 feet, about 8 feet to about 20 feet, or about 10 feet to about 15 feet. The substrate can also have a width, or second largest dimension, of at least about 1 inch, at least about 2 inches, or at least about 4 inches and/or not more than about 10 inches, not more than about 8 inches, or not more than about 6 inches, or in the range of from about 1 to about 10 inches, about 2 to about 8 inches, or about 4 to about 6 inches. The thickness, or shortest dimension, of the substrate being coated in coating system 12 can be at least about 0.10 inches, at least about 0.25 inches, at least about 0.5 inches and/or not more than about 4 inches, not more than about 2 inches, or not more than about 1 inch, or in the range of from about 0.10 to about 4 inches, about 0.25 to about 2 inches, or about 0.5 to about 1 inch.


Coated substrates produced using coating system 12 may have a wide variety of shapes and/or sizes and may be made of a variety of materials. In one embodiment, the substrates coated in coating system 12 can comprise a material selected from the group consisting of natural wood, wood composites, plastics including cellularized PVC and other foams, metal, fiberglass, ceramics, cement, and combinations thereof. In the same or other embodiments, the substrate material comprises medium-density fiber board (MDF), particle board, oriented strand board (OSB), and combinations thereof. In one embodiment, the substrate can have an average initial moisture content, measured just prior to its introduction into die 20 of coating system 12 of at least about 2 weight percent, at least about 5 weight percent, at least about 8 weight percent and/or not more than about 15 weight percent, not more than about 12 weight percent, or not more than about 10 weight percent, or in the range of from about 2 weight percent to about 15 weight percent, from about 5 weight percent to about 12 weight percent, or about 8 weight percent to about 10 weight percent, based on the total weight of the substrate. In other embodiments, the initial moisture content of the substrate can be less than about 5 percent, less than about 3 percent, or less than about 2 percent, based on the total weight of the substrate.


Any coating material exhibiting sufficient processability and adhesion to the selected substrate may be employed by coating system 12. In one embodiment, the coating material may comprise one or more polymers or resins, such as thermoplastic polymers or resins capable of being applied to the substrate in a molten or melted form under the operating conditions of die 20. In one embodiment, the glass transition temperature of the polymers utilized in the coating material can be at least about 50° C., at least about 60° C., at least about 65° C., at least about 70° C., at least about 75° C. and/or not more than about 170° C., not more than about 160° C., not more than about 150° C., not more than about 140° C. Examples of polymers or polymer resins suitable for use in coating materials employed with embodiments of the coating system described herein include, but are not limited to, polyesters and copolyesters, such as polyethylene terephthalate or glycol modified polyethylene terephthalate; acid modified polyethylene terephthalate; polycarbonates; acrylics such as poly(methylmethacrylate); poly(acrylonitrile-styrene-acrylate); poly(acrylonitrile-butadiene-styrene); poly(styrene-acrylonitrile); cellulose esters; polyolefins such as polypropylenes and polyethylene; nylons; and polyvinylchloride (PVC).


The coating material can also comprise one or more additives selected from the group consisting of color pigment, UV stabilizers, compatibilizers, rubbers, gloss modifiers (e.g., calcium carbonate), opacity modifiers (e.g., titanium dioxide), impact modifiers (e.g., styrene-butadiene-styrene polymers, acrylonitrile-butadiene-styrene polymers, or methacrylate-butadiene-styrene polymers), and other types of stabilizers typically employed to ensure a durable and appealing finish to the coating applied to the substrate. Several suitable coating compositions are described in detail in co-pending U.S. Patent Application Publication No. 2010/0015456, the entire disclosure of which is incorporated herein by reference to the extent not inconsistent with the present disclosure.


Referring back to FIG. 1, the substrate can initially be introduced into a pretreatment zone 14, which can comprise one or more stages configured to prepare the substrate for coating. For example, pretreatment zone 14 can include one or more milling stages for forming an initial blank stock substrate into a substrate having a desired shape by milling and/or cutting the substrate to a desired profile and/or length. Exemplary substrates are illustrated in FIGS. 5a-5d, which will be discussed in detail shortly, although other suitable shapes are contemplated.


Turning back to FIG. 1, pretreatment zone 14 may also comprise at least one cleaning stage for removing particles of dirt, dust, or other debris from the surface of the substrate before coating. The cleaning stage may comprise a high pressure steam cleaning, a high pressure air cleaning, a solvent cleaning, a water bath cleaning, and/or any other cleaning process appropriate for the particular type of substrate employed in coating system 12. In some embodiments, pretreatment zone 14 may include a stain bath for staining at least a portion of the substrate prior to coating.


Following pretreatment, the substrate can then be introduced into drying zone 16. Drying zone 16 can be configured to heat at least a portion of the surface of the substrate to thereby facilitate removal of at least some of the volatile materials within the substrate. Drying zone 16 can also be operable to remove surface moisture from the substrate, thereby facilitating a more precise control of the substrate size by minimizing the effects of moisture swelling. In one embodiment, the substrate can be dried in the drying zone 16 for at least about 5 seconds, at least about 10 seconds, at least about 20 seconds and/or not more than about 15 minutes, not more than about 10 minutes, not more than about 5 minutes, or in the range of from about 5 seconds to about 15 minutes, about 10 seconds to about 10 minutes, or about 20 seconds to about 5 minutes. Drying zone 16 can be maintained at a temperature of at least about 10° C., at least about 20° C., at least about 30° C., at least about 35° C. and/or not more than 80° C., not more than about 70° C., not more than about 60° C., not more than about 50° C., or in the range of from about 10° C. to about 80° C., about 20° C. to about 70° C., or about 30° C. to about 60° C.


Once removed from drying zone 16, the substrate can pass through optional staging area 18 before being introduced into die 20 via a feed system 28. Feed system 28 can comprise any suitable device or apparatus for pushing the substrate into and at least partially through die 20. In some embodiments, feed system 28 can also be operable to properly align the substrate with an inlet of die 20 (not shown in FIG. 1). Specific configurations of die 20 will be discussed in detail shortly. In some embodiments, feed system 28 can comprise a plurality of rollers, positioned above and below the substrate (not shown), which are configured to engage and push the substrate into die 20. Feed system 28 can be configured to supply individual substrate members into die 20 in a substantially continuous manner, such that, for example, the individual substrate members are fed to the die 20 in a butt-to-butt manner, where contact is maintained between the back end of a first substrate member and the front end of a second substrate member fed behind the first substrate member. In this way, die 20 may be operated in a continuous or semi-continuous manner.


As the substrate is introduced into die 20, at least a portion of the surface of the substrate can be contacted with a coating material introduced into die 20 from coating source 30. Coating source 30 can be any suitable system or apparatus for providing a coating, and, in one embodiment, may be an extruder. The temperature in the die 20 during the coating process can be any temperature sufficient to maintain the incoming coating material in a liquid or substantially liquid state. In some embodiments, the temperature in die 20 during coating can be at least about 50° C., at least about 100° C., at least about 200° C. and/or not more than about 500° C., not more than about 400° C., not more than about 300° C., or in the range of from about 50° C. to about 500° C., about 200° C. to about 400° C., or about 200° C. to about 300° C. The pressure in die 20 during the coating step can be at least about 25 pounds per square inch (psi), at least about 50 psi, at least about 75 psi and/or not more than about 5,000 psi, not more than about 3,500 psi, not more than about 2,000 psi, not more than about 1,500 psi, not more than 1,000 psi, or in the range of from about 25 to about 5,000 psi, from about 50 to about 3,500 psi, or from about 100 to about 2,000 psi.


Turning now to FIGS. 2 and 3, one embodiment of a die 120 suitable for use in coating system 12 as described above is provided. Die 120 can be any suitable type of die capable of contacting at least a portion of a substrate 100 with a coating material to thereby provide a coated substrate 102. In one embodiment, die 120 can be a cross-head die configured and operated as described, for example, in U.S. Pat. Nos. 6,660,086 and 7,347,795, or co-pending U.S. Pat. App. Publication No. 2011/0223342, the entireties of which are incorporated herein by reference to the extent not inconsistent with the present disclosure. In one embodiment, die 120 can be configured to apply a coating material to at least a portion of the surface of substrate 100 in a uniform and controlled manner and can be operated continuously and at an average line speed of at least about 25 feet per minute (ft/min), at least about 50 ft/min, at least about 75 ft/min, at least about 100 ft/min, or at least about 125 ft/min.


As shown in FIGS. 2 and 3, die 120 comprises a die block 112 and a die plate 114 coupled to or proximate the front wall of die block 112. As used herein, the directional terms “front” and “forward,” when referring to a die, designate the side or direction at which a substrate would normally exit the die after being coated. Conversely, the directional terms “rear” and “back,” as used herein, refer to the side of the die in which the substrate is intended to enter. Thus, as shown in FIG. 2, a substrate 100 would normally pass through die 120 from back to front along a die axis 115, as generally indicated by arrows 180 and 182. According to one embodiment depicted in FIG. 2, die axis 115 may be a substantially horizontal die axis such that it is oriented within about 5° of the horizontal.


As particularly illustrated in FIG. 3, die 120 comprises an inlet wall 122 defined by die body 112, an outlet wall 124 defined by die plate 114, and a coating chamber 126 disposed at least partially therebetween. Inlet wall 122 defines a die inlet 132 configured to receive a substrate (not shown in FIG. 3) into die 120 and outlet wall 124 defines a die outlet 134 configured to discharge the coated substrate from die 120. In one embodiment, die inlet 132 and die outlet 134 each define respective inner and outer profiles that may correspond, or substantially correspond, to the shape of the lateral cross-sectional profile of the substrate, as will be discussed in detail shortly.


According to one embodiment, die 120 can further comprise a first insulating member 150 affixed to at least a portion of outlet wall 124 of die 120. In some embodiments, as depicted in FIG. 2, die 120 can include an optional second insulating member 152 disposed between die block 112 and die plate 114. Insulating member 150 (and insulating member 152 when present), can be constructed of any suitable insulating material having a thermal conductivity lower than the thermal conductivity of outlet wall 124 of die 120. In one embodiment, insulating member 150 and, if present, insulating member 152 can be formed of a material having a thermal conductivity of at least about 0.01 Watts per-meter Kelvin (W/mK), at least about 0.05 W/mK, at least about 0.1 W/mK and/or not more than about 2 W/mK, not more than about 1 W/mK, not more than about 0.5 W/mK, or in the range of from about 0.01 to about 2 W/mK, from about 0.05 to about 1 W/mK, or about 0.1 to 0.5 W/mK, measured according to ASTM C-177. Examples of suitable insulating materials can include, but are not limited to, mica and calcium silicate. In one embodiment, insulating members 150, 152 can have a thickness, X, as shown in FIG. 3 of at least about ⅛ inch, at least about ¼ inch, at least about ½ inch and/or not more than about 3 inches, not more than about 2 inches, not more than about 1 inch, not more than about ¾ inches, or in the range of from about ⅛ inch to about 3 inches, from about ¼ inch to about 2 inches, or about ½ inch to about 1 inch.


In an alternative embodiment, die 120 may comprise a device or system capable of creating a fluid insulator in place of, or in addition to, insulating member 150. According to this embodiment, a region or “curtain” of air, nitrogen, or other pressurized fluid may be configured proximate die outlet 134 and may perform a similar function as insulating member 150. Similarly to insulating member 150, the temperature of outlet wall 124 may be maintained within a similar temperature range as described in detail below.


Turning now to FIG. 4a, an exploded rotated view of die plate 114 and insulating member 150 of die 120 is provided. As shown in FIG. 4a, insulating member 150 comprises a substrate inlet 154, a substrate outlet 156, and a shaped passageway 158 defined therebetween. In addition, one or more metal support plates (not shown) may be positioned on either side of insulating member 150 for further stabilization and support. Insulating member 150 can be affixed to outlet wall 124 of die 120 such that shaped passageway 158 at least partially surrounds die outlet 134, as shown in FIG. 4b, and reduces the surface area of outlet wall 124 exposed to the downstream quench zone (not shown). As a result, the temperature of outlet wall 124 proximate die outlet 134 may be maintained closer to the temperature of the coating melt within die 120, and, in some embodiments, may be no more than about 60° C., no more than about 50° C., no more than about 40° C., not more than about 35° C., or not more than about 20° C. less than the temperature of the coating material contacted with the substrate in die 120. In other embodiments, the temperature of die outlet wall 124 may be less than 5° C., less than 2° C., or less than 1° C. lower than the temperature of the coating material contacting the substrate within die 120.


According to one embodiment illustrated in FIG. 4b, a small gap 180 may be formed between the inner edge of substrate inlet 154 (shown as edge 162) and the outer edge of die outlet 134 (shown as edge 164) when insulating member 150 is affixed to outlet wall 124 of die 120 as shown in FIG. 4b. In one embodiment, the smallest gap 180 formed (also known as the minimum distance) between the edge 162 of substrate inlet 154 and the edge 164 of die outlet 134 can be at least 1 mil, at least 2 mils, at least 5 mils and/or not more than about 100 mils, not more than about 85 mils, not more than about 75 mils, not more than about 65 mils, not more than about 50 mils, not more than about 45 mils, not more than about 35 mils, not more than about 25 mils, not more than about 20 mils, or not more than about 10 mils, or from about 1 mil to about 30 mils, about 1 mil to about 25 mils, or about 1 mil to about 20 mils. In one embodiment, the sizes of the cross-sections of shaped passageway 158 and die outlet 134 may be substantially the same, such that the cross-sectional areas of shaped passageway 158 and die outlet 134 can be within no more than about 25 percent, no more than about 20 percent, no more than about 15 percent, no more than about 10 percent, no more than about 5 percent, or no more than about 1 percent of one another.


Shaped passageway 158 may be configured to have any suitable cross-sectional shape. Preferably, shaped passageway 158 can have a constant cross-sectional shape and/or size, such that the size and/or shape of shaped passageway 158 remains substantially constant throughout its entire length. In general, the cross-sectional shapes of die outlet 134 and substrate inlet 154 of shaped passageway 158 may be different from one another, while, in some embodiments, the cross-sectional shapes may be substantially the same. For example, in one embodiment, the cross-sectional shapes of die outlet 134 and shaped passageway 158 may be substantially geometrically similar, while, in other embodiments, shaped passageway 158 and die outlet 134 may have congruent cross-sectional shapes. As used herein, the term “geometrically similar” refers to two or more objects having substantially the same shape, while the term “congruent” refers to two objects having the same shape and size. Further, at least one of shaped passageway 158 and die outlet 134 may have a cross-sectional shape geometrically similar to the lateral cross-sectional shape of the coated substrate passing therethrough. Specific examples of lateral cross-sectional shapes of the coated substrate will be discussed in detail shortly.


Turning back to FIG. 2, as coated substrate 102 exits outlet 134 of die 120 and passes through insulating member 150, at least a portion of the coating on the substrate can maintain contact with at least a portion of the wall of shaped passageway 158. In one embodiment, the residence time of coated substrate 102 in shaped passageway 158 can be at least about 0.1 seconds, at least about 0.25 seconds, at least about 0.5 second and/or not more than about 2 seconds, not more than about 1.5 seconds, not more than about 1 second, or in the range of from about 0.1 seconds to about 2 seconds, about 0.25 seconds to about 1 second, or about 0.5 seconds to about 1 second, measured from the time a single point on coated substrate 102 exits die outlet 134 until the time the same point exits shaped passageway 158.


Referring again to FIG. 1, the coated substrate exiting die 20 enters quench zone 22, wherein it can be at least partially cooled via contact with a quench fluid to thereby provide a cooled, coated substrate. In one embodiment, the temperature of the quench fluid in quench zone 22 can be at least about 2° C., at least about 4° C., at least about 8° C., at least about 10° C., at least about 15° C. and/or not more than about 65° C., not more than about 55° C., not more than about 45° C., not more than about 35° C., or in the range of from about 4° C. to about 55° C., from about 10° C. to about 45° C., or about 15° C. to about 35° C. Examples of suitable quench fluids can include, but are not limited to, water, air, or nitrogen, or any other liquid or gas suitable for use with the specific type of substrate and coating material being used. In some embodiments, the pressure of quench zone 22 can be less than 250 kPa, less than 175 kPa, less than about 100 kPa, less than about 75 kPa, less than about 50 kPa, or less than about 25 kPa.


Quench zone 22 can include any suitable means for contacting the coated substrate with a quench fluid. In one embodiment, quench zone 22 may include a quench bath for at least partially submerging the coated substrate into a quench liquid. In another embodiment, quench zone 22 can include a pressure box configured to maintain a pressurized environment for the coating material to cool on the substrate. When quench zone 22 utilizes a pressure box (not shown), the pressure box can be configured to cool the coated substrate under a pressure of at least about 20 psi, at least about 25 psi, at least about 30 psi and/or not more than about 100 psi, not more than about 80 psi, not more than about 60 psi, or in the range of from about 20 to about 100 psi, from about 25 psi to about 80 psi, or from about 30 psi to about 60 psi. In other embodiments, quench zone 22 may utilize any other suitable cooling system or method, including, for example, cooled rollers (not shown). In some embodiments, coated substrate 102 may simply be allowed to cool at ambient temperature and/or pressure.


Once the cooled, coated substrate is removed from quench zone 22, it can then be passed through an optional post treatment zone 24, if desired. Examples of suitable post-treatment processes can include, but are not limited to, abrasion via one or more types of media treatment, gloss enhancements, in-line primer treatments, painting, staining, and combinations thereof. In another embodiment shown in FIG. 1, the cooled, coated substrate may be removed from coating system 12 with no post-quench treatment, as indicated by line 26.


According to one embodiment, the cooled, coated articles produced by systems and processes according to embodiments of the present invention may exhibit a highly desirable surface texture and visual appearance. For example, in one embodiment, the cooled, coated substrate withdrawn from coating system 12 may be substantially bubble-free. As used herein, the term “substantially bubble free” refers to a coated substrate exhibiting less than 10 bubbles per 100 square feet as measured by visual detection. In one embodiment, coated substrates according to embodiments of the present invention can exhibit less than about 10 bubbles per 100 square feet, less than about 5 bubbles per 100 square feet, less than about 2 bubbles per 100 square feet, or less than 1 bubble per 100 square feet.


In the same or other embodiments, the water-quenched, extrusion coated substrate exiting quench zone 22 may have a relatively smooth, untextured surface. For example, in one embodiment, at least a portion of the surface of the coated substrate can have an average Rmax surface roughness of no more than about 40, no more than about 30, no more than about 25, no more than about 20, no more than about 15, no more than about 12, or no more than about 10. As used herein, the term “average Rmax surface roughness” refers to the maximum roughness depth measured from the highest point to the lowest point along the measurement length, averaged over all measurements taken. The values for surface roughness parameters, including Rmax, provided herein were measured using a Mitutoyo Surftest SJ-201P roughness tester with a 5-micron stylus, as described in detail in Examples 34-42 below. In addition to Rmax, several other roughness parameters were measured via profilometry for several coated substrates and values and descriptions for each of these additional parameters are provided below in Examples 34-42. In some embodiments, coated substrates having a surface texture as described above may be obtained even in the absence of post-quench treatment, such as sanding, buffing, or the like. Unlike conventionally-prepared water-quenched articles, extrusion coated articles of the present invention exhibit unexpected surface smoothness while retaining an acceptable visual appearance, including a reduced occurrence of bubbles and surface blisters.


Referring now to FIGS. 5a-d, several coated substrates 200a-d configured according to various embodiments of the present invention are illustrated. As shown in each of FIGS. 5a-d, each coated substrate 200a-d comprises an elongated substrate 210a-d and at least one coating layer 220a-d extrusion coated thereon. Although shown as including a single coating layer in FIGS. 5a-d, it is contemplated that coated articles according to some embodiments of the present invention may include two or more coating layers. The average thickness of coating layer (or layers, if applicable) 220a-d may be at least about 2 mils, at least about 4 mils, at least about 6 mils and/or not more than about 40 mils, not more than about 35 mils, not more than about 25 mils, or not more than about 15 mils, as determined based on the amount of coating material consumed during steady state coating of the substrate. For example, average coating thickness can be calculated by dividing the total volume of coating material consumed by the total surface area of substrate coated with that volume of material.


The coating layer 220a-d can be affixed to substrates 210a-d such that the coating material can be sufficiently adhered directly to at least a portion of the substrate. Unlike conventional “peel-and-stick” or other similar coatings, coated substrates according to embodiments of the present invention do not include a layer of glue or other adhesive disposed between the surface of the substrate and the coating material. In one embodiment, the coating can have an average adhesion peel force of at least 0.10 pounds (lb), at least about 0.25 lbs, at least about 0.35 lbs, or at least 0.40 lbs and/or not more than about 2 lbs, not more than about 1.5 lbs, not more than about 1 lb, not more than about 0.75 lbs, not more than about 0.65 lbs, or not more than 0.50 lbs, measured with a 90° T-Peel test described in ASTM Method D3330, Method F or in the range of from about 0.10 to about 2 lbs, about 0.35 to about 1.5 lbs, or about 0.40 to about 1 lb.


In some embodiments, the coating may be applied to only a portion of the surface of the substrate, as illustrated in FIGS. 5b and 5d, such that at least about 50 percent, at least about 65 percent, at least about 75 percent, at least about 85 percent, or at least about 95 percent of the total surface area of substrate 200 is covered with a coating material. In some embodiments as shown in FIGS. 5b and 5d, one or more sides of an n sided substrate (wherein n is an integer between 3 and 10, inclusive) may be left partially (FIG. 5b) or totally (FIG. 5d) uncoated, such that n−1 sides are completely coated by the material. In other embodiments, the entirety of substrate 210a,c may be coated such that all sides of the substrate are completely encapsulated by the coating material, as particularly illustrated in FIGS. 5a and 5c.


In addition, as particularly illustrated by the exemplary coated substrates 200a-d in FIGS. 5a-d, coated substrates of the present invention can also have any desired lateral cross-sectional shape. In one embodiment, the substrate may have a symmetric lateral cross-section, while, in other embodiments, the substrate can have a non-symmetric lateral cross-section. As used herein, the term “symmetric” refers to any shape which exhibits symmetry along all lines drawn through the center point of the shape. Similarly, the term “non-symmetric” refers to a shape which exhibits asymmetry along at least one line drawn through its center point. In one embodiment, the substrate may have a symmetric circular (as shown in FIG. 5a), while, in other embodiments, the substrate may have a non-symmetric square (FIG. 5b) or rectangular lateral cross-section (as shown in FIG. 5c). In another embodiment, the substrate may have an irregularly-shaped non-symmetric lateral cross-section that includes at least one curvilinear side having both concave and convex sections, as depicted in the embodiment shown in FIG. 5d.


The various aspects of the present invention can be further illustrated and described by the following Examples. It should be understood, however, that these Examples are included merely for purposes of illustration and are not intended to limit the scope of the invention, unless otherwise specifically indicated.


EXAMPLES
Example 1

Two samples of natural finger-jointed pine were prepared for coating in a lab scale extrusion coating system. The first sample had a rectangular lateral cross-section measuring approximately ⅝ inch (1.6 cm) by ⅞ inch (2.2 cm) and the second sample had a complex cross-sectional shape similar to the one depicted in FIG. 5d, which is used with many commercially-available types of crown molding. This sample, referred to as the E1 cross-section sample, had lateral cross-sectional dimensions measuring approximately 3.25 inches (8.3 cm) by ⅝ inch (1.6 cm).


Each of the samples described above were preheated in an oven to a temperature of about 100° F. (38° C.) and the heated substrates were placed in a staging area before being individually passed through a die assembly connected to a 2½-inch extruder. A thermoplastic coating material that included glycol-modified poly(ethylene terephthalate), a calcium carbonate gloss modifier, a titanium dioxide opacity modifier, a UV stabilizer, and an impact modifier was extruded into the die assembly and applied to each substrate at a melt temperature of 500° F. (260° C.). The pressure in the die assembly was maintained between 300 and 500 psi (2070 and 3450 kPa) during coating and the target coating thickness was between 0.006 and 0.0012 inches (0.015 and 0.030 cm). The substrates passed through the die assembly at a line speed of 25 board feet per minute (7.6 meters per minute).


In this Example, no insulating member was employed on the die outlet wall and no water bath was employed. The coated samples exited the die assembly and were allowed to cool in under ambient temperature and pressure. Upon visual inspection of the cooled, coated substrates, it was noted that the samples had an unacceptably high concentration of surface bubbles and blisters.


Example 2

Two wood samples having a rectangular and an E1 cross-section were prepared and coated as described above in Example 1, except the coated samples exiting the die assembly were immediately passed into a water bath to cool. The temperature of the water bath was maintained between 60° F. and 75° F. (16° C. and 24° C.). The outlet wall of the die assembly was not insulated and was directly contacted by the water bath. The temperature of the die outlet wall was approximately 100° F. to 150° F. less than the melt temperature. Upon visual inspection, it was noted that the cooled, coated substrates were substantially bubble-free, but exhibited an unacceptable surface texture.


Example 3

Two wood samples having a rectangular and an E1 cross-section were prepared and coated as described above in Example 1. The coated samples exiting the die assembly were immediately passed into a water bath to cool, as described above in Example 2. In addition, a ⅛-inch (0.32 cm) thick mica insulating member with a rectangular opening was affixed to the outlet wall of the die and the coated substrate passed through the insulating member as it exited the die assembly. The rectangular opening was larger than the die opening, so that a portion of the outlet wall of the die was still exposed to quench water. Coated samples exiting the die outlet passed through the insulating member and were cooled in a water bath as described in Example 2. Upon visual inspection, it was noted that the cooled, coated substrates were substantially bubble-free, but exhibited an unacceptable surface texture.


Example 4

A wood sample having a rectangular cross-section was prepared and coated as described above in Example 1. The coated sample exiting the die assembly was passed through an insulating member affixed to the outlet wall of the die as described in Example 3, except the opening of the insulating member was cut to have the same size and shape as the coated substrate. Upon visual inspection, it was noted that the cooled, coated substrate was not only substantially bubble-free, but also exhibited a smooth, non-textured surface.


Example 5

A wood sample having an E1 cross-section was prepared and coated as described above in Example 1. The coated sample exiting the die assembly was passed through an insulating member affixed to the outlet wall of the die having the same size and shape as the coated substrate, similar to the procedure described in Example 4. Upon visual inspection, it was noted that the cooled, coated E1 substrate was not only substantially bubble-free, but also exhibited a smooth, non-textured surface.


Examples 6-18

Several samples of finger-jointed pine having an E1 cross-section were prepared and coated as described in Example 1. Similar to Example 5, each coated sample was passed through a ⅛-inch thick mica insulator affixed to the die outlet wall and cut to have an opening the same size and shape as the coated substrate. The melt temperature of the coating was maintained at 475° F. (246° C.), but the water bath temperature, the substrate preheat temperature, and the die outlet wall temperature were varied. Each of the cooled, coated substrates removed from the quench water bath was visually evaluated and the surface appearance was noted. The operating conditions and visual appearance results for each of Examples 6-18 are summarized in Table 1, below.









TABLE 1







Operating Conditions and Results for Samples Coated in


Examples 6-18












Water Bath
Preheat
Die outlet wall




Temperature
Temperature
Temperature
Surface


Example
(° F.)
(° F.)
(° F.)
Appearance














6
80
110
475
No texture or






bubbles


7
40
70
400
No texture or






bubbles


8
120
150
400
No texture or






bubbles


9
80
110
475
No texture or






bubbles


10
120
70
550
No texture or






bubbles


11
40
150
550
No texture or






bubbles


12
80
110
475
No texture or






bubbles


13
120
70
400
No texture or






bubbles


14
40
150
400
No texture or






bubbles


15
80
110
475
No texture or






bubbles


16
120
150
550
No texture or






bubbles


17
40
70
550
No texture or






bubbles


18
80
110
475
No texture or






bubbles









Examples 19-21

Several samples of finger-joint pine having an E1 cross-section were prepared and coated as described in Example 1. Each substrate was coated in a die assembly with a melt temperature of 475° F. (246° C.) and a die outlet wall temperature of 500° F. (260° C.), but the thickness of the mica insulating insulator affixed to the outer wall of the die was varied. The opening in the insulating member was cut to match the size and shape of the E1 profile. The water bath temperature was maintained between 65° F. and 80° F. (18° C. and 27° C.). Each of the cooled, coated substrates removed from the quench water bath were visually evaluated and the surface appearance was noted. The insulator thickness and visual appearance results for each of Examples 19-21 are summarized in Table 2, below.









TABLE 2







Operating Conditions and Results for Samples Coated in


Examples 19-21









Example
Insulator Thickness (in)
Surface Appearance





19
475
No texture or bubbles


20
400
No texture or bubbles


21
400
No texture or bubbles









Examples 22-30

Several samples of medium-density fiber board (MDF) and finger-joint pine (FJP) each having an E1 cross-sectional shape were prepared and coated as described in Example 1, above. The melt temperature of the coating was 500° F. and the samples were passed through the die at a board speed of 15 feet per minute. The sample coated in Example 22 was allowed to cool under ambient conditions, while the samples coated in Examples 24-30 were cooled in a water quench bath maintained at a temperature of about 70° F. No insulating member was used in Examples 22-24. For Examples 25-30, a ⅛-inch thick mica insulator having an inlet of E1 shape, but varying size were used in order to vary the clearance between the inner edge of the insulator inlet and the outer edge of the die outlet. The surface appearance and texture of the cooled, coated substrates for each run were observed. The minimum insulator clearance and the visual appearance results for the samples tested in each of Examples 22-30 are summarized in Table 3, below.









TABLE 3







Operating Conditions and Results for Samples Coated in


Examples 22-30














Insulator





Quench
Clearance,
Surface


Example
Substrate
Medium
mils
Appearance





22
MDF
Air
No insulator
Smooth and glossy


23
MDF
Water, 70° F.
No insulator
Very rough/textured


24
FJP
Water, 70° F.
No insulator
Very rough/textured


25
MDF
Water, 70° F.
200
Very rough/textured


26
FJP
Water, 70° F.
200
Very rough/textured


27
MDF
Water, 70° F.
100
Moderately






rough/textured


28
FJP
Water, 70° F.
100
Moderately






rough/textured


29
MDF
Water, 70° F.
10
Smooth, matte


30
FJP
Water, 70° F.
10
Smooth, matte









Examples 31-33

Several samples of medium density fiberboard having an E1 cross-section were prepared and coated as described in Example 1. Each substrate was coated in a die assembly with a melt temperature of 500° F. and was passed through a mica insulator having a thickness of ⅛ inch and a clearance of 100 mils, measured from the outer edge of the die outlet to the inner edge of the insulator inlet. The speed at which the substrate passed through the die was varied. The coated substrates were cooled in a water bath having a temperature of 70° F. Each of the cooled, coated substrates removed from the quench water bath were visually evaluated and the surface appearance was noted. The line speed and visual appearance results for each of Examples 31-33 are summarized in Table 4, below.









TABLE 4







Operating Conditions and Results for Samples Coated in


Examples 31-33










Line Speed



Example
(feet/min)
Surface Appearance












31
15
Rough/textured


32
50
Moderately rough


33
100
Slightly rough









Examples 34-42

Several 8-foot long samples of medium-density fiber board (MDF) and finger-joint Radiata pine (FJP) each having an E1 cross-sectional shape were prepared and coated as described in Example 1, above. The samples were passed through the die at a board speed of 15 feet per minute. The sample coated in Example 34 was allowed to cool under ambient conditions, while the samples coated in Examples 35-42 were cooled in a water quench bath maintained at a temperature of about 60° F. No insulating member was used in Examples 34-36. For Examples 37-42, various ¼-inch thick mica insulators, each having an E1-shaped inlet of but a different opening size, were used in order to vary the clearance between the inner edge of the insulator inlet and the outer edge of the die outlet. The surface appearance and texture of the cooled, coated substrates were observed for each run. The minimum insulator clearance and the visual appearance results for the samples tested in each of Examples 34-42 are summarized in Table 5a, below.









TABLE 5a







Visual Inspection Results for Samples Coated in


Examples 34-42













Quench






Medium,
Insulator
Surface


Example
Substrate
Temperature
Clearance, mils
Appearance





34
MDF
Air, ambient
No insulator
Smooth, no






texture


35
MDF
Water, 60° F.
No insulator
Heavily textured


36
FJP
Water, 60° F.
No insulator
Heavily textured


37
MDF
Water, 60° F.
200 mil
Heavily textured


38
FJP
Water, 60° F.
200 mil
Heavily textured


39
MDF
Water, 60° F.
100 mil
Lightly textured


40
FJP
Water, 60° F.
100 mil
Lightly textured


41
MDF
Water, 60° F.
 20 mil
Smooth, no






texture


42
FJP
Water, 60° F.
 20 mil
Smooth, no






texture









After cooling, the samples were cut into 3-foot segments and surface roughness measurements were taken at two randomly-selected locations on the back (flat) side of the sample. The surface roughness of each sample was measured using a Mitutoyo SJ-210 having a 2 micron stylus with a 60 degree radius. The measurements were taken in accordance with the procedure described in the roughness tester manual over a sample length of 1 inch. The results of the surface roughness measurements for each of the samples in Examples 34-42 are summarized in Table 5b, below.


In addition to Rmax, which as discussed above, is the maximum roughness depth measured from the highest point to the lowest point along the measurement length, the following surface roughness parameters were also measured for each sample in Examples 34-42: Ra, Rq, Rz, Rv, Rp, and Rpm. Ra is the arithmetic average surface roughness, calculated over the entire measured array, while Rq is the root-mean-square average between the height deviations and the mean line or surface calculated over the entire measured array. Rz is an average of the ten greatest peak-to-valley separations in the sample, while Rmax is the maximum roughness depth measured from the highest peak to the lowest value along a measurement length. Rv is the maximum profile valley depth or the height difference between the mean (average) height line and the lowest point over the entire measurement length, while Rp is the maximum profile peak height or the height difference between the mean height line and the highest point over the entire measurement length. Rpm is the average maximum profile peak height, measured as the average of successive Rp values over the measurement length. Values for each of these roughness parameters, taken for each coated substrate in Examples 34-42 are provided in Table 5b, below.


Additionally, several scanning electron microscope (SEM) images were taken of each of the coated substrates in Examples 34-42 at an SEM HV of 5.0 kV (Examples 34 and 35) or 3.0 kV (Examples 36-42) and a magnification of 250×. The resulting images for coated MDF substrates are presented as FIGS. 6a-6e (Examples 34, 35, 37, 39, and 41), while the coated FJP substrates are provided as FIGS. 6f-6i (Examples 36, 38, 40, and 42)









TABLE 5b







Surface Roughness by Profilometry for Examples 34-42















Example
Measurement
Rmax
Rpm
Ra
Rq
Rz
Rp
Rv


















34
#1
9.723
4.605
1.378
1.718
7.917
6.031
5.146



#2
9.277
4.168
1.269
1.613
7.415
4.908
5.793



Average
9.50
4.39
1.32
1.67
7.67
5.47
5.47


35
#1
108.77
50.192
16.522
20.693
90.266
67.791
57.965



#2
100.76
47.123
14.328
18.816
78.695
60.456
40.305



Average
104.77
48.66
15.43
19.75
84.48
64.12
49.14


36
#1
99.729
44.638
13.298
16.968
77.073
56.278
43.501



#2
96.309
35.371
11.924
15.582
62.132
52.951
43.357



Average
98.02
40.00
12.61
16.28
69.60
54.61
43.43


37
#1
53.11
22.24
7.914
9.936
44.103
26.983
28.822



#2
64.643
29.671
8.379
10.692
50.643
36.243
29.068



Average
58.88
25.96
8.15
10.31
47.37
31.61
28.95


38
#1
55.861
16.167
6.02
8.08
30.776
33.064
22.797



#2
53.53
21.787
8.372
10.638
45.464
26.678
33.494



Average
54.70
18.98
7.20
9.36
38.12
29.87
28.15


39
#1
35.99
18.045
6.351
7.849
33.911
21.917
20.74



#2
45.161
18.771
6.163
7.901
39.761
22.143
28.486



Average
40.58
18.41
6.26
7.88
36.84
22.03
24.61


40
#1
35.307
13.883
6.229
7.549
31.805
15.914
19.393



#2
62.23
17.512
6.737
8.671
37.489
21.601
40.628



Average
48.77
15.70
6.48
8.11
34.65
18.76
30.01


41
#1
13.313
5.266
1.826
2.35
9.744
6.835
6.694



#2
13.76
6.426
2.102
2.583
11.475
7.7
6.674



Average
13.54
5.85
1.96
2.47
10.61
7.27
6.68


42
#1
12.926
5.289
1.154
1.484
8.735
9.395
5.317



#2
9.013
4.688
1.186
1.495
8.266
5.403
4.542



Average
10.97
4.99
1.17
1.49
8.50
7.40
4.93









Examples 43-45

Several samples of medium density fiberboard having an E1 cross-section were prepared and coated as described in Example 1. Upon exiting the die outlet, each substrate was passed through a mica insulator having a thickness of ¼ inch and a clearance of 100 mils, measured from the outer edge of the die outlet to the inner edge of the insulator inlet. The speed at which the substrate passed through the die and insulator was varied. The coated substrates were cooled in a water bath having a temperature of 60° F. Each of the cooled, coated substrates removed from the quench water bath were visually evaluated and the surface appearance was noted. Additionally, the surface roughness of each of the cooled substrates was measured using a Mitutoyo SJ-210 having a 2 micron stylus with a 60 degree radius, as described in Examples 34-42 above. The line speed and visual appearance results for each of Examples 43-45 are summarized in Table 6a, below, while the surface roughness measurements are provided in Table 6b. Additionally, several scanning electron microscope (SEM) images were taken of each of the coated substrates in Examples 43-45 at an SEM HV of 3.0 kV and a magnification of 250×. The resulting images are provided in FIGS. 7a-7c.









TABLE 6a







Operating Conditions and Visual Results for Samples Coated


in Examples 43-45










Line Speed



Example
(feet/min)
Surface Appearance












43
15
Lightly textured


44
50
Less textured


45
100
Smooth, no texture
















TABLE 6b







Surface Roughness by Profilometry for Examples 43-45















Example
Measurement
Rmax
Rpm
Ra
Rq
Rz
Rp
Rv


















43
#1
30.544
15.799
4.833
6.043
28.146
16.387
14.973



#2
31.667
13.52
4.509
5.72
28.174
14.31
17.681



Average
31.11
14.66
4.67
5.88
28.16
15.35
16.33


44
#1
17.064
6.804
2.155
2.734
13.897
8.241
8.823



#2
15.669
6.672
2.305
2.881
13.916
8.154
8.837



Average
16.37
6.74
2.23
2.81
13.91
8.2
8.83


45
#1
18.796
7.72
2.437
3.06
15.642
8.383
11.169



#2
22.156
8.54
2.586
3.307
17.916
12.019
10.689



Average
20.48
8.13
2.51
3.18
16.78
10.2
10.93









The preferred forms of the invention described above are to be used as illustration only, and should not be used in a limiting sense to interpret the scope of the present invention. Obvious modifications to the exemplary embodiments, set forth above, could be readily made by those skilled in the art without departing from the spirit of the present invention.


The inventors hereby state their intent to rely on the Doctrine of Equivalents to determine and assess the reasonably fair scope of the present invention as pertains to any apparatus not materially departing from but outside the literal scope of the invention as set forth in the following claims.

Claims
  • 1. A system for extrusion coating a thermoplastic resin coating material onto an elongated substrate, said system comprising: a die for contacting an elongated substrate with a molten thermoplastic resin coating material to produce a coated substrate,wherein said die comprises an inlet wall, an outlet wall, and a coating chamber disposed at least partially therebetween,wherein said inlet wall comprises a die inlet for receiving said elongated substrate into said die and said outlet wall comprises a die outlet for discharging said coated substrate from said die;an extruder for introducing the thermoplastic resin coating material into the die;an insulating member affixed to said outlet wall,wherein said insulating member has a thermal conductivity less than the thermal conductivity of said outlet wall and comprises a shaped passageway configured to at least partially surround said die outlet to allow said coated substrate exiting said die outlet to pass through said insulating member; anda quench zone located adjacent said insulating member for cooling said coated substrate discharged from said shaped passageway of said insulating member,a second insulating member disposed between said coating chamber and said outlet wall, wherein said second insulating member has a thermal conductivity less than the thermal conductivity of said outlet wall,a feed system located upstream of said die for introducing said substrate into said die inlet, wherein said fee system includes a pushing device operable to push said elongated substrate into said die inlet;wherein said coated substrate has a length of at least 5 feet;wherein said elongated substrate comprises natural wood, wood composites, medium-density fiber board, particle board, oriented strand board, plastic, cellularized PVC, foam, metal, fiberglass, ceramics, cement and combinations thereof; and wherein said resin coating material comprises one or more of polyesters, copolyesters, polycarbonates, acrylics, cellulose esters, polyolefins, nylons, and polyvinylchloride.
  • 2. The system of claim 1, wherein the minimum distance between the edge of said shaped passageway proximate said die outlet and the edge of said die outlet is less than 100 mils.
  • 3. The system of claim 1, wherein the minimum cross-sectional areas of said shaped passageway and said die outlet are within no more than about 25 percent of one another.
  • 4. The system of claim 1, wherein the cross-sectional shape of said shaped passageway and the cross-sectional shape of said die outlet are geometrically similar.
  • 5. The system of claim 1, wherein said shaped passageway has a constant cross-sectional area.
  • 6. The system of claim 1, wherein the cross-sectional shape of said shaped passageway and the cross-sectional shape of said die outlet are congruent.
  • 7. The system of claim 1, wherein at least one of the cross-sectional shapes of said die outlet and said shaped passageway are non-symmetrical.
  • 8. The system of claim 1, wherein each of said die outlet and said shaped passageway have an irregular cross-sectional shape including at least on curvilinear side having both convex and concave sections.
  • 9. The system of claim 1, wherein said thermal conductivity of said insulating member is at least 0.01 and/or not more than 5 W/mK at 25° C.
  • 10. The system of claim 1, which is a continuous system configured to operate at a line speed of least 25 board feet per minute.
  • 11. The system of claim 1, wherein said cooled coated substrate has an average Rmax surface roughness of not more than 30.
  • 12. The system of claim 11, wherein said cooled coated substrate has an average Rmax surface roughness of not more than 40.
  • 13. The system of claim 11, wherein the surface of said cooled coated substrate has less than 10 bubbles per 100 feet.
  • 14. The system of claim 11, wherein said resin coating is extrusion coated onto said surface such that all of the sides of said elongated substrate are completely encapsulated by said resin coating.
  • 15. The system of claim 11, wherein said resin coating layer has an average thickness of at least 2 mils and not more than 40 mils.
  • 16. The system of claim 11, wherein said substrate has two or more coating layers.
  • 17. The system of claim 16, wherein each resin coating layer has an average thickness of at least 2 mils.
  • 18. The system of claim 11, wherein said resin coating is adhered directly to at least a portion of the substrate and has an adhesion peel force of at least 0.10 pounds.
  • 19. The system of claim 11, wherein said substrate has a non-symmetrical lateral cross-sectional shape.
  • 20. The system of claim 11, wherein said substrate has a symmetrical lateral cross-sectional shape.
CROSS REFERENCE TO RELATED APPLICATIONS

This application is a divisional of Ser. No. 13/706,408, filed Dec. 6, 2012, which is incorporated by reference herein.

US Referenced Citations (221)
Number Name Date Kind
2216519 Quarnstrom Oct 1940 A
2926729 Zanini Mar 1960 A
2991273 Hechelhammer et al. Jul 1961 A
2999835 Goldberg Sep 1961 A
2999846 Schnell et al. Sep 1961 A
3028365 Schnell et al. Apr 1962 A
3084662 Badger et al. Apr 1963 A
3148172 Fox Sep 1964 A
3153008 Fox Oct 1964 A
3169121 Goldberg Feb 1965 A
3207814 Goldberg Sep 1965 A
3271367 Schnell et al. Sep 1966 A
3368740 Rohde Feb 1968 A
3402682 Peden Sep 1968 A
3410938 Schippers Nov 1968 A
3544669 Schock Dec 1970 A
3599286 Karet Aug 1971 A
3694538 Okamoto et al. Sep 1972 A
3720027 Christensen Mar 1973 A
3741843 Louis Jun 1973 A
3772405 Hamb Nov 1973 A
3793128 Chancellor, Jr. et al. Feb 1974 A
3852933 Guzzo Dec 1974 A
3853462 Smith Dec 1974 A
3941904 Hoh et al. Mar 1976 A
3961118 Michaelis et al. Jun 1976 A
3980005 Buonaiuto Sep 1976 A
4000219 Smejkal Dec 1976 A
4123436 Holub et al. Oct 1978 A
4124574 Preston et al. Nov 1978 A
4143187 Pilgrim et al. Mar 1979 A
4156069 Prevorsek et al. May 1979 A
4181764 Totten Jan 1980 A
4190686 Muis Feb 1980 A
4194038 Hipp et al. Apr 1980 A
4209475 Herrington Jun 1980 A
4222911 Christenson Sep 1980 A
4301053 Wolfrey Nov 1981 A
4397986 Hornbaker Aug 1983 A
4420920 Hewitt Dec 1983 A
4430484 Quinn Feb 1984 A
4433088 Haaf et al. Feb 1984 A
4452933 McCready Jun 1984 A
4465820 Miller et al. Aug 1984 A
4514449 Budich Apr 1985 A
4558096 Boon et al. Dec 1985 A
4567142 Lloyd Jan 1986 A
4576846 Noel Mar 1986 A
4589456 Traben May 1986 A
4613653 Kitchens et al. Sep 1986 A
4740556 Abolins et al. Apr 1988 A
4757110 Sato Jul 1988 A
4760114 Haaf et al. Jul 1988 A
4774794 Grieb Oct 1988 A
4775597 Birkmeyer et al. Oct 1988 A
4790851 Suire et al. Dec 1988 A
4872907 Areaux Oct 1989 A
4935306 Ohtsuka et al. Jun 1990 A
4963435 Hara et al. Oct 1990 A
4981898 Bassett Jan 1991 A
4982014 Freitag et al. Jan 1991 A
4984406 Friesen Jan 1991 A
4987702 Anschutz Jan 1991 A
5010162 Serini et al. Apr 1991 A
5084511 Abe et al. Jan 1992 A
5095069 Ambrose et al. Mar 1992 A
5162058 Uenaka et al. Nov 1992 A
5166237 Abe et al. Nov 1992 A
5197319 Beekel Mar 1993 A
5286547 Tyerman Feb 1994 A
5288559 Oka et al. Feb 1994 A
5312863 Van Rheenen et al. May 1994 A
5321056 Carson et al. Jun 1994 A
5344700 McGath et al. Sep 1994 A
5382401 Pickett et al. Jan 1995 A
5415943 Gorger et al. May 1995 A
5417904 Razi et al. May 1995 A
5484632 Mercer, Jr. et al. Jan 1996 A
5625999 Buzza et al. May 1997 A
5654347 Khemani et al. Aug 1997 A
5665798 Speaks et al. Sep 1997 A
5672391 Santarossa Sep 1997 A
5674928 Chisholm et al. Oct 1997 A
5696176 Khemani et al. Dec 1997 A
5725944 Jones et al. Mar 1998 A
5824373 Biller et al. Oct 1998 A
5858522 Turk Jan 1999 A
5897708 Hsu Apr 1999 A
5898043 Uemae et al. Apr 1999 A
5907006 Rennie et al. May 1999 A
5914083 Yada et al. Jun 1999 A
5925698 Steckel Jul 1999 A
5962573 Berta Oct 1999 A
5965075 Pauley et al. Oct 1999 A
5972471 Jasenof et al. Oct 1999 A
5976676 Miki et al. Nov 1999 A
5985397 Witt et al. Nov 1999 A
5997456 Butters et al. Dec 1999 A
6020414 Nelsen et al. Feb 2000 A
6074727 Miller et al. Jun 2000 A
6083601 Prince et al. Jul 2000 A
6093773 Evans et al. Jul 2000 A
6114021 Pankratz Sep 2000 A
6153264 Schmid et al. Nov 2000 A
6168866 Clark Jan 2001 B1
6203915 Prissok et al. Mar 2001 B1
6206965 Rao et al. Mar 2001 B1
6298626 Rudden Oct 2001 B2
6306507 Brunelle et al. Oct 2001 B1
6336265 Niedermair Jan 2002 B1
6352657 Veldhuis et al. Mar 2002 B1
6352784 Katagiri Mar 2002 B1
6353050 Bastiaens et al. Mar 2002 B1
6391461 Ryntz et al. May 2002 B1
6394784 Gellert et al. May 2002 B1
6448328 Kappler et al. Sep 2002 B1
6455161 Regnier et al. Sep 2002 B1
6461792 Kawamura et al. Oct 2002 B1
6500895 Bastiaens et al. Dec 2002 B1
6540624 Isogawa Apr 2003 B1
6551662 Schmid et al. Apr 2003 B1
6576309 Dalgewicz, III et al. Jun 2003 B2
6579611 Iwashita et al. Jun 2003 B1
6583189 King Jun 2003 B1
6584743 Paxton et al. Jul 2003 B2
6592668 Rao et al. Jul 2003 B2
6596784 King Jul 2003 B1
6601357 Tunis Aug 2003 B2
6616998 Greer et al. Sep 2003 B2
6660086 Prince et al. Dec 2003 B1
6667367 Berta Dec 2003 B1
6673293 Mistopoulos Jan 2004 B1
6680104 Boris et al. Jan 2004 B2
6716522 Matsumoto et al. Apr 2004 B2
6780359 Burch Aug 2004 B1
6841239 Hasegawa Jan 2005 B2
6852765 Decker et al. Feb 2005 B2
6933043 Son et al. Aug 2005 B1
6991632 Ritland Jan 2006 B2
6994752 Estrada et al. Feb 2006 B2
7022257 Ohkido et al. Apr 2006 B1
7022768 Lacroix et al. Apr 2006 B1
7034072 Milic Apr 2006 B2
7081488 Bardman et al. Jul 2006 B2
7097879 Bolton et al. Aug 2006 B2
7160977 Hale et al. Jan 2007 B2
7175905 Curtis et al. Feb 2007 B2
7226985 Hale et al. Jun 2007 B2
7318958 Wang Jan 2008 B2
7335399 Bolton et al. Feb 2008 B2
7368511 Hale et al. May 2008 B2
7374795 Prince et al. May 2008 B2
7435483 Lee et al. Oct 2008 B2
7644553 Knauseder Jan 2010 B2
7687768 Hashizume et al. Mar 2010 B2
7694468 Prince et al. Apr 2010 B2
7695498 Ritland Apr 2010 B2
7766915 Jackson Aug 2010 B2
7868090 Juikar Jan 2011 B2
7883597 Blahut Feb 2011 B2
7901435 Slivka et al. Mar 2011 B2
8065848 Carlson et al. Nov 2011 B2
8071198 Michalczyk et al. Dec 2011 B2
8071695 Strand et al. Dec 2011 B2
8113143 Prince et al. Feb 2012 B2
8197733 Sudano Jun 2012 B2
8394784 Stroumpoulis et al. Mar 2013 B2
8734909 Iyer et al. May 2014 B2
20010013211 Rudden Aug 2001 A1
20010055671 Pickett et al. Dec 2001 A1
20020034629 Jones Mar 2002 A1
20020090471 Burger et al. Jul 2002 A1
20020121064 Erwin Sep 2002 A1
20020136911 Yamamoto et al. Sep 2002 A1
20020139047 Haddad Oct 2002 A1
20020192451 Kobayashi et al. Dec 2002 A1
20030093078 Ritland May 2003 A1
20030108735 Hoppe et al. Jun 2003 A1
20030211347 Rabinovitch et al. Nov 2003 A1
20040003903 Wenrick et al. Jan 2004 A1
20040023052 Ambroise Feb 2004 A1
20040048055 Branca Mar 2004 A1
20040109946 Prince et al. Jun 2004 A1
20040131871 Lee et al. Jul 2004 A1
20040236063 Suzuki et al. Nov 2004 A1
20050037176 Domine Feb 2005 A1
20050050814 Prince et al. Mar 2005 A1
20050102963 Nien et al. May 2005 A1
20050106406 Curtis et al. May 2005 A1
20050137332 Hale et al. Jun 2005 A1
20050137356 Hale et al. Jun 2005 A1
20050288401 Pearson et al. Dec 2005 A1
20060022376 Prince et al. Feb 2006 A1
20060111519 Strand et al. May 2006 A1
20060255496 Wells Nov 2006 A1
20060258801 Martin et al. Nov 2006 A1
20060267238 Wang Nov 2006 A1
20060270806 Hale Nov 2006 A1
20070000568 Bohme et al. Jan 2007 A1
20070059463 Melkonian Mar 2007 A1
20070104930 Grohman May 2007 A1
20070235705 Burger et al. Oct 2007 A1
20070292569 Bohme et al. Dec 2007 A1
20080118741 Michalczyk et al. May 2008 A1
20080145564 Allam et al. Jun 2008 A1
20080145637 Frank Jun 2008 A1
20080153984 Renken et al. Jun 2008 A1
20090011164 Masuda et al. Jan 2009 A1
20090035581 Sudano Feb 2009 A1
20090036581 Joshi et al. Feb 2009 A1
20090064627 Struthers et al. Mar 2009 A1
20100003410 King et al. Jan 2010 A1
20100015456 Lizotte et al. Jan 2010 A1
20100021677 West et al. Jan 2010 A1
20100036007 Journee Feb 2010 A1
20100211180 Helmuth et al. Aug 2010 A1
20110223342 Iyer et al. Sep 2011 A1
20110245876 Brumfield Oct 2011 A1
20130005892 Lizotte et al. Jan 2013 A1
20130011563 Lizotte et al. Jan 2013 A1
20130060345 Tepie Mar 2013 A1
Foreign Referenced Citations (44)
Number Date Country
2133696 May 1995 CA
201626102 Nov 2010 CN
9316759 Feb 1994 DE
44 24 767 Nov 1995 DE
198 57 045 Jun 2000 DE
20 2011 003953 May 2011 DE
10 2012 001910 Aug 2013 DE
0 132 218 Jan 1985 EP
0 210 297 Feb 1987 EP
0210297 Feb 1987 EP
0 488 711 Jun 1992 EP
0 510 463 Oct 1992 EP
653469 May 1995 EP
2 861 738 May 2005 FR
1 397 270 Jun 1975 GB
2 024 658 Jan 1980 GB
S52 103465 Aug 1977 JP
58-118231 Jul 1983 JP
S59 155024 Sep 1984 JP
60-085921 May 1985 JP
1-225647 Sep 1989 JP
3-26752 Feb 1991 JP
8-34866 Feb 1996 JP
1996 034866 Feb 1996 JP
08300590 Nov 1996 JP
09-302078 Nov 1997 JP
9324135 Dec 1997 JP
11-90827 Apr 1999 JP
1999245590 Sep 1999 JP
2002-337291 Nov 2002 JP
2003-056168 Feb 2003 JP
2004-211039 Jul 2004 JP
2005-154731 Jun 2005 JP
2005-264136 Sep 2005 JP
2006-281544 Oct 2006 JP
20110073672 Jun 2011 KR
WO 9618685 Jun 1996 WO
WO 9746627 Dec 1997 WO
WO 9827159 Jun 1998 WO
WO 0127200 Apr 2001 WO
WO 0158663 Aug 2001 WO
WO 2006093916 Sep 2006 WO
WO 2006102705 Oct 2006 WO
WO 2008040498 Apr 2008 WO
Non-Patent Literature Citations (87)
Entry
English Translation EP0210297A1, Feb. 1987.
December, Timothy S., et al.; “The Effects of TPO Composition on Adhesion and Proposed Chemical Mechanism”; Paint and Coatings Industry; Mar. 2008; www.pcimag.com; pp. 76-82.
Berta, Dominic A.; “Formulating Plastics for Paint Adhesion”; Chapter 3 from Coatings of Polymers and Plastics, 2003, edited by Ryntz, Rose, A. and Yaneff, Phillip V.; pp. 85-119.
ASTM D 2457 Mar. 2008.
ASTM D 3359-02 Oct. 2002.
ASTM D3330 Oct. 2004.
ASTM D 523 Jun. 2008.
ASTM E 1164 Jun. 2009.
ASTM E 308 Jan. 2009.
“Blendex BMAT Data Sheet Styrene Acrylonitrile”, http://www.ides.com/info/datasheet/E73798/BLENDEX-BMAT, Sep. 13, 2012.
“Paraloid™ KM-377 Acrylic Impact Modifier”, Technical Data Sheet, The Dow Chemical Company.
“Blendex BMAT Modifier Resin”; Chemtura; www.chemtura.com; Effective Jun. 4, 2008; (2007).
“Butyl acrylate-methyl methacrylate polymers”; Chemical Book; www.chemicalbook.com; (2008).
“Paraloid KM-377 Impact Modifier”; Material Safety Data Sheet, DOW; Revision Date: Feb. 7, 2004.
Turner, S. R., et al.; “Polyesters Based on 1,4-Cyclohexanedimethanol”; Modern Polyesters: Chemistry and Technology of Polyesters and Copolyesters; (2003); pp. 280-282.
“Chlorocarbons and Chlorohydrocarbons—C2 to Combustion Technology”; Encyclopedia of Chemical Technology; 4th Edition, vol. 6, (1993), pp. 620-623.
Notification of Transmittal of the International Search Report and the Written Opinion of the International Searching Authority dated Jan. 22, 2010 for International Application No. PCT/US2009/004107.
Copending U.S. Appl. No. 12/721,080, filed Mar. 10, 2010, Subramanian Iyer et al.
Copending U.S. Appl. No. 12/503,675, filed Jul. 15, 2009, Jeremy Richard Lizotte et al.
Strasser, CFD Investigation of Gear Pump Mixing Using Deforming/Agglomerating Mesh, J. Fluids Eng.—Apr. 2007—vol. 129, Issue 4, 476 (9 pages).
Notification of Transmittal of the International Search Report and the Written Opinion of the International Searching Authority dated Apr. 28, 2011 for International Application No. PCT/US2011/026942.
USPTO Office Action dated Apr. 2, 2012 for copending U.S. Appl. No. 12/503,675.
USPTO Office Action dated May 7, 2012 for copending U.S. Appl. No. 12/721,080.
Copending U.S. Appl. No. 13/616,672, filed Sep. 14, 2012, Jeremy Richard Lizotte et al.
Copending U.S. Appl. No. 13/616,681, filed Sep. 14, 2012, Jeremy Richard Lizotte et al.
USPTO Office Action dated Dec. 6, 2012 for copending U.S. Appl. No. 12/503,675.
Copending U.S. Appl. No. 13/706,408, filed Dec. 6, 2012, Tony Wayne Helton.
USPTO Office Action dated Jan. 11, 2013 for copending U.S. Appl. No. 12/721,080.
USPTO Office Action dated Feb. 26, 2013 for copending U.S. Appl. No. 13/616,672.
USPTO Office Action dated Feb. 27, 2013 for copending U.S. Appl. No. 13/616,681.
Copending U.S. Appl. No. 13/861,412, filed Apr. 12, 2013, Gordon L. King.
UPSTO Offfice Action dated Jul. 16, 2013 in copending U.S. Appl. No. 13/706,408.
Notification of Transmittal of the International Search Report and the Written Opinion of the International Searching Authority dated Jul. 18, 2013 for International Application No. PCT/US2013/037957.
USPTO Office Action dated Aug. 23, 2013 in copending U.S. Appl. No. 12/721,080.
USPTO Office Action dated Sep. 13, 2013 in copending U.S. Appl. No. 13/616,681.
Fred W. Billmeyer, Jr., Textbook of Polymer Science, 3rd Edition, John Wiley & Sons, Inc., New York, p. 153 (1984).
Carraher, Introduction to Polymer Chemistry 3rd Edition, CRC Press, Taylor & France Group, Boca Raton FL p. 240 (2013).
USPTO Office Action dated Jan. 6, 2014 in copending U.S. Appl. No. 12/503,675.
Notification of Transmittal of the International Search Report and the Written Opinion of the International Searching Authority, or the Declaration—International Application No. PCT/US2013/072546 dated Mar. 11, 2014.
Notice of Allowance received in Co-pending U.S. Appl. No. 12/721,080 dated Apr. 10, 2014.
Notice of Allowance received in C0-pending U.S. Appl. No. 13/706,408 dated May 12, 2014.
USPTO Office Action dated Jun. 2, 2014 in copending U.S. Appl. No. 13/616,672.
USPTO Office Action dated Aug. 29, 2014 in copending U.S. Appl. No. 12/503,675.
ASTM D882; “Standard Test Method for Tensile Properties of Thin Plastic Sheeting”; Published Sep. 2012.
ASTM D1037; “Evaluating Properties of Wood-Based Fiber and Particle Panel Materials”; Published Jun. 2012.
ASTM D4541; “Standard Test Method for Pull-Off Strength of Coatings Using Portable Adhesion Testers”; Published Apr. 2009.
Chemical Abstract Services No. 25852-37-3.
Notification of Transmittal of the International Search Report and the Written Opinion of the International Searching Authority, or the Declaration—International Application No. PCT/US2014/059839 dated Jan. 22, 2015.
Notification of Transmittal of the International Search Report and the Written Opinion of the International Searching Authority, or the Declaration—International Application No. PCT/US2014/059824 dated Mar. 30, 2015.
USPTO Office Action dated May 11, 2015 in copending U.S. Appl. No. 12/503,675.
USPTO Office Action dated Dec. 19, 2014 in copending U.S. Appl. No. 13/616,672.
Office Action dated Aug. 14, 2015 received in U.S. Appl. No. 13/616,672.
USPTO Office Action dated Apr. 27, 2015 in copending U.S. Appl. No. 13/616,681.
USPTO Office Action dated Sep. 25, 2012 for copending U.S. Appl. No. 12/721,080.
USPTO Notice of Allowance dated Jun. 20, 2014 in copending U.S. Appl. No. 13/706,408.
Copending U.S. Appl. No. 14/496,549, filed Sep. 25, 2014, Jennifer Lynne Peavey; now U. S. Publication No. 2015/0110996.
Copending U.S. Appl. No. 14/496,508, filed Sep. 25,2014, Jennifer Lynne Peavey; now U. S. Publication No. 2015/0110986.
Copending U.S. Appl. No. 14/496,529, filed Sep. 25, 2014, Jennifer Lynne Peavey; now U. S. Publication No. 2015-0110988.
Copending U.S. Appl. No. 14/496,483, filed Sep. 25, 2014, Jennifer Lynne Peavey; now U. S. Publication No. 2015/0110995.
Copending U.S. Appl. No. 14/496,567, filed Sep. 25, 2014, Chad Alan Frazier; now U. S. Publication No. 2015/0107175.
USPTO Office Action dated Mar. 25, 2015 in copending U.S. Appl. No. 14/496,567.
Copending U.S. Appl. No. 14/571,568, filed Dec. 16, 2014, Kevin Michael Cable.
Notice of Allowance and Fee(s) Due dated May 18, 2016 received in U.S. Appl. No. 13/616,672.
Office Communication notification dated Jul. 12, 2016 received in co-pending U.S. Appl. No. 14/496,508.
Office Communication notification dated Sep. 7, 2016 received in co-pending U.S. Appl. No. 14/496,529.
Office Communication notification dated Apr. 27, 2016 received in co-pending U.S. Appl. No. 14/496,483.
Office Communication notification dated Aug. 18, 2016 received in co-pending U.S. Appl. No. 14/496,567.
Office Communication notification dated Apr. 11, 2016 received in co-pending U.S. Appl. No. 12/503,675.
Office Communication notification dated Apr. 7, 2016 received in co-pending U.S. Appl. No. 14/496,529.
Office Communication notification dated Sep. 14, 2015 received in co-pending U.S. Appl. No. 13/616,681.
Notification of Transmittal of the International Search Report and the Written Opinion of the International Searching Authority, or the Declaration—International Application No. PCT/US2015/065681 dated Mar. 8, 2016.
Office Communication notification dated Oct. 27, 2015 received in co-pending U.S. Appl. No. 12/503,675.
Office Communication notification dated Nov. 18, 2015 received in co-pending U.S. Appl. No. 14/496,567.
Office Communication notification dated Mar. 2, 2016 received in co-pending U.S. Appl. No. 14/496,567.
Office Communication notification dated Sep. 23, 2016 received in co-pending U.S. Appl. No. 12/503,675.
Notice of Allowance and Fee(s) Due dated Sep. 28, 2016 received in U.S. Appl. No. 13/616,672.
Office Communication notification dated Oct. 14, 2016 received in co-pending U.S. Appl. No. 13/616,681.
Office Communication notification dated Sep. 28, 2016 received in co-pending U.S. Appl. No. 14/496,549.
Office Communication notification dated Jun. 15, 2017 received in co-pending U.S. Appl. No. 12/503,675.
Notice of Allowance and Fee(s) Due dated Jan. 30, 2017 received in U.S. Appl. No. 13/616,672.
Office Communication notification dated Feb. 21, 2017 received in co-pending U.S. Appl. No. 13/616,681.
Office Communication notification dated Dec. 12, 2016 received in co-pending U.S. Appl. No. 14/496,508.
Office Communication notification dated Mar. 9, 2017 received in co-pending U.S. Appl. No. 14/496,529.
Notice of Allowance and Fee(s) Due dated Jun. 28, 2017 received in co-pending U.S. Appl. No. 14/496,529.
Office Communication notification dated Oct. 26, 2016 received in co-pending U.S. Appl. No. 14/496,483.
Office Communication notification dated Feb. 22, 2017 received in co-pending U.S. Appl. No. 14/496,483.
Office Communication notification dated Mar. 9, 2017 received in co-pending U.S. Appl. No. 14/496,567.
Related Publications (1)
Number Date Country
20150004349 A1 Jan 2015 US
Divisions (1)
Number Date Country
Parent 13706408 Dec 2012 US
Child 14487355 US