COMPOSITE HOUSE WRAP FORMED OF LOW DENSITY POLYETHYLENE FOAM WITH EVACUATED CLOSED CELLS AND HAVING TORTUOUS PATHS OF THERMAL CONDUCTIVITY

Abstract

A house wrap for a building comprises a reinforcing drainage plane layer configured to face the outside of the building; a breathable, non-perforated barrier film bonded to the drainage plane layer; and at least one insulating layer including a perforated expanded low density polyethylene foam layer, wherein in the expanded low density polyethylene layer at least 80% of the blowing agents are dissipated from closed cells within the expanded low density polyethylene layer, forming evacuated closed cells whereby a partial vacuum is formed within the closed cells of the low density polyethylene layer.

Claims

1. A house wrap for a building consisting essentially of: A drainage plane layer for the house wrap and configured to face the outside of the building; A breathable, barrier film layer bonded to the drainage plane; and At least one low density polyethylene foam layer having evacuated closed cells forming a tortuous thermal conductive path along the cell walls through the foam layer, and wherein the total thickness of the house wrap is less than 175 mils and wherein the house wrap has an insulating R-Value of at least 2 and wherein at least 80% of the primary blowing agent is dissipated from the cells within the expanded low density polyethylene, forming evacuated closed-cell low density polyethylene sheets.

2. The house wrap for a building according to claim 1, wherein the at least one low density polyethylene foam layer is coupled to a non-woven layer which is then coupled to the barrier film layer.

3. The house wrap for a building according to claim 2 wherein the house wrap has an insulating R-Value of at least 6.

4. The house wrap for a building according to claim 3 wherein the barrier film layer is one of polyethylene (PE) or polytetrafluoroethylene (PTFE), and wherein the total thickness of the house wrap is less than 175 mils.

5. The house wrap for a building according to claim 1 wherein the barrier film is bonded to the drainage plane layer through thermal bonding, and wherein the total thickness of the house wrap is less than 175 mils.

6. A house wrap for a building comprises: A reinforcing layer providing a drainage plane for the house wrap and configured to face the outside of the building; A barrier layer including a breathable barrier film bonded to the first layer; and A third non-woven coupling layer; and at least one insulating layer, including a perforated low density polyethylene foam layer, having evacuated closed cells forming a tortuous thermal conductive path along the cell walls through the foam layer, and wherein the total thickness of the house wrap is less than 175 mils and wherein the house wrap has an insulating R-Value of at least 6 and wherein at least 90% of the primary blowing agent is dissipated from cells within the expanded low density polyethylene, forming evacuated closed-cell low density polyethylene sheets.

7. The house wrap for a building according to claim 6 wherein the barrier film is a non-perforated polyethylene (PE) film.

8. The house wrap for a building according to claim 6 wherein the barrier film is a non-perforated polytetrafluoroethylene (PTFE) film.

9. The house wrap for a building according to claim 6 wherein the barrier film is bonded to the first layer through thermal bonding.

10. The house wrap for a building according to claim 6 wherein the total thickness of the house wrap is less than 175 mils.

11. The house wrap for a building according to claim 6 wherein the barrier film is a non-perforated polytetrafluoroethylene (PTFE) film, and wherein the total thickness of the house wrap is less than 175 mils.

12. The house wrap for a building according to claim 11 wherein the barrier film is bonded to the first layer through thermal bonding.

13. The house wrap for a building according to claim 6 wherein the barrier film is a non-perforated film of polyethylene (PE), and wherein the total thickness of the house wrap is less than 175 mils.

14. A process of forming a housing wrap comprising the steps of: providing a mixture, including low density polyethylene pellets and an effective amount of glycerides as a degassing agent; adding a primary blowing agent to the mixture in an amount about 20-40% of the low density polyethylene by weight, wherein the primary blowing agent is comprising one of liquid propane, liquid butane, and combinations thereof, and gasifying the blowing agent to expand the low density polyethylene; forming the expanded low density polyethylene into sheets, curing the expanded low density polyethylene at a temperature between 20° C. to 30° C. until 80% of the primary blowing agent is dissipated from the cells within the expanded low density polyethylene, forming evacuated closed-cell low density polyethylene sheets; coupling at least one expanded low density polyethylene, forming evacuated closed-cell low density polyethylene sheet to a barrier layer, including a breathable barrier film; and bonding the barrier layer to a drainage plane for the house wrap which is configured to face the outside of the building.

15. The process of forming a house wrap according to claim 14 wherein at least 95% of the primary blowing agent is dissipated from the cells within the expanded low density polyethylene before closed-cell low density polyethylene sheets are subsequently processed.

16. The process of forming a house wrap according to claim 14 wherein at least 99% of the primary blowing agent is dissipated from the cells within the expanded low density polyethylene before closed-cell low density polyethylene sheets are subsequently processed.

17. The process of forming a house wrap according to claim 14 wherein the effective amount of glyceride is about 0.3-5% of the low density polyethylene by weight.

18. The process of forming a house wrap according to claim 14 wherein the effective amount of glyceride is about 1-4% of the low density polyethylene by weight.

19. The process of forming a house wrap according to claim 14 wherein the curing step is at least 14 days before closed-cell low density polyethylene sheets are subsequently processed.

20. The process of forming a house wrap according to claim 14 wherein the curing step is at least 30 days before closed-cell low density polyethylene sheets are subsequently processed.

Description

BRIEF DESCRIPTION OF THE FIGURES

[0038] FIG. 1 is a schematic plan view of a system for implementing the process of the present invention; and

[0039] FIG. 2 is a schematic top view of the system of FIG. 1 taken in the direction of the arrow II shown in FIG. 1.

[0040] FIG. 3 is a composite house wrap formed of low density polyethylene foam with evacuated closed cells and having tortuous paths of thermal conductivity in accordance with one embodiment of the present invention;

[0041] FIG. 4 is a schematic cross section of the house wrap with high insulating properties in accordance FIG. 3;

[0042] FIG. 5 is a schematic cross section of a modified version of house wrap with high insulating properties in accordance FIG. 3; and

[0043] FIG. 6 is a schematic cross section of a modified version of house wrap with high insulating properties in accordance FIG. 3.

DESCRIPTION OF THE PREFERRED EMBODIMENTS

[0044] In summary, one object of the present invention relates to a process of forming expanded, closed-cell low density polyethylene foam comprising the effective steps of: providing a mixture, including low density polyethylene pellets. and an effective amount of glycerides as a degassing agent; adding a primary blowing agent comprising one of liquid propane, liquid butane, and combinations thereof, to the mixture and gasifying the blowing agent to expand the low density polyethylene; forming the expanded low density polyethylene into sheets, curing the expanded low density polyethylene until 80% of the primary blowing agent is dissipated from the cells within the expanded low density polyethylene, forming closed-cell low density polyethylene sheets.

[0045] Low density polyethylene (LDPE) is a thermoplastic, with the formula (C.sub.2H.sub.4).sub.n, which is defined by a density range of 0.910-0.940 g/cm.sup.3. It is un-reactive at room temperatures, except by reaction with strong oxidizing agents. It is known as being quite flexible, and tough. LDPE has more branching (on about 2% of the carbon atoms) than high density polyethylene (HDPE).

[0046] The LDPE molecules are less tightly packed and less crystalline than HDPE because of the side branches, and thus its density is lower. It is typically found as a powder or pellet forms and has a CAS #9002-88-4. U.S. suppliers of polyethylene include of AccuStandard Inc; Aceto Corporation; AK Scientific, Inc.; Cambridge Isotope Laboratories, Inc.; CarboMer, Inc.; Dow Chemical Company; EMCO Industrial Plastics, Inc.; HBCChem, Inc.; Pressure Chemical Co.; Scientific Polymer Products, Inc.; Lanxess; ExxonMobil; Lyondell Basell; Chevron-Phillips; INEOS; Covestro; Solvay; and Waterstone Technology, LLC.

[0047] Glycerides, more correctly known as acylglycerols, are esters formed from glycerol and fatty acids. Glycerol has three hydroxyl functional groups, which can be esterified with one, two, or three fatty acids to form monoglycerides, diglycerides, and triglycerides, respectively.

[0048] A monoglyceride is a glyceride in which each glycerol molecule has formed an ester bond with exactly one fatty acid molecule. The more formally correct terms in modern convention are acylglycerol and monoacylglycerol. Any monoacylglycerol is either a 1-monoacylglycerol or a 2-monoacylglycerol, depending on the position of the ester bond on the glycerol moiety. 1-monoacylglycerides possess a chiral centre at carbon 2.

[0049] A diglyceride, or diacylglycerol (DAG), is a glyceride consisting of two fatty acid chains covalently bonded to a glycerol molecule through ester linkages. One example is 1-palmitoyl-2-oleoyl glycerol, which contains side-chains derived from palmitic acid and oleic acid. Diacylglycerols can also have many other combinations of fatty acids attached at either the C-1 and C-2 positions or the C-1 and C-3 positions. 1,2 di-substituted glycerols are always chiral, 1,3 di-substituted glycerols are chiral if the substituents are different from each other. Acceptable diglycerides and monoglycerides suitable for the present invention include those under CAS #91052-47-0, 10303-53-4 and 41670-62-6.

[0050] A triglyceride (TG, triacylglycerol, TAG, or triacylglyceride) is an ester derived from glycerol and three fatty acids (tri-+glyceride). There are many different types of triglycerides, with the main division being between saturated and unsaturated types. Saturated fats are “saturated” with hydrogen—all available sites where hydrogen atoms could be bonded to carbon atoms are occupied. There exists no carbon-carbon double bonds. Saturated fats have a higher melting point and are more likely to be solid at room temperature. Unsaturated fats have double bonds between some of the carbon atoms, reducing the number of sites where hydrogen atoms are bonded to carbon atoms. Unsaturated fats have a lower melting point and are more likely to be liquid at room temperature. Acceptable triglycerides suitable for the present invention include those under CAS #65381-09-1 and 97794-26-8.

[0051] Propane is a three-carbon alkane with the molecular formula C.sub.3H.sub.8, a gas at standard temperature and pressure, but compressible to a transportable liquid. A by-product of natural gas processing and petroleum refining, it is one of a group of liquefied petroleum gases (LP gases). The others include butane, propylene, butadiene, butylene, isobutylene and mixtures thereof. Propane has a CAS #74-98-6.

[0052] Butane is an organic compound with the formula C.sub.4H.sub.10 that is an alkane with four carbon atoms. Butane is a gas at room temperature and atmospheric pressure. The term may refer to either of two structural isomers, n-butane or isobutane (or “methylpropane”), or to a mixture of these isomers. In the IUPAC nomenclature, however, “butane” refers only to the n-butane isomer (which is the isomer with the unbranched structure). Butanes are highly flammable, colorless, easily liquefied gases. Butane has a CAS #106-97-8.

[0053] In the present invention FIG. 1 is a schematic plan view of a system for implementing the process of the present invention; and FIG. 2 is a schematic top view of the system of FIG. 1 taken in the direction of the arrow II shown in FIG. 1.

[0054] In accordance with the present invention, and as schematically shown in the drawings, a low density polyethylene prepared by conventional process is mixed, for example in a hopper 1, with an effective amount of a glyceride, preferably a monoglyceride, forming a degassing agent, to form a dry mixture (as discussed below, in alternative embodiments the dry mix includes a preliminary auxiliary blowing agent, a surface activation agent, a separation agent, a fire retarding agent, a crosslinking agent to improve strength of the foam, a coloring agent and an anti-discoloration agent). The amounts of the ingredients are generally expressed relative to the amount of the low density polyethylene. The present invention provides an effective amount of glyceride to be about 0.3-5% of the low density polyethylene by weight, and more preferably about 1-4% of the low density polyethylene by weight, and more preferably about 2.5% of the low density polyethylene by weight.

[0055] The degassing agent, such as glycerides, may be referenced as a hydrocarbon scavenger additive and the low density polyethylene may be mixed, for example in a hopper 1, with an effective amount of hydrocarbon scavenger additive which can include other materials other than glyceride. Hydrocarbon scavenger additives include glycerides, activated carbon, sodium bicarbonate, graphite, silica gels, zeolites, diatomaceous earth, and polymer absorbents called “petrogels”: polyolefin-based hydrophobic absorbents that demonstrate selective absorption of hydrocarbon (oil) molecules in water, and mixtures of the above, with glycerides and glyceride-containing mixtures being preferred. Mixed into the low density polyethylene are hydrocarbon scavenger additives that react with the expanded low density polyethylene in a manner that causes short chain molecules of Hydrocarbon Scavengers to have an affinity for hydrocarbon structures of the primary blowing agent, and draw these variants to oxygen-rich environments, namely to the exterior of the composite structure. As the cells deplete, the process slows accordingly and consumes more time to evacuate the remaining hydrocarbon-based molecules than when the process was initiated. The present invention provides an effective amount of hydrocarbon scavenger additives to be about 0.3-5% of the low density polyethylene by weight, and more preferably about 1-4% of the low density polyethylene by weight, and more preferably about 2.5% of the low density polyethylene by weight.

[0056] The dry mixture is conveyed in an extruder barrel 3, where it is likely processed in a series of stages at different temperatures. A conventional thermocouple control box can be used to maintain a particular required temperature in each of the processing stages in the extruder barrel 3.

[0057] A conventional coil or screw conveys the mixture through the extruder barrel 3. A twin-screw conveyor is preferred as it yields a homogeneous mixture without damage to the mixture or batch. In the extruder barrel 3, the dry mixture is heated at a temperature of about 170° C. to form a melted and softened polyethylene mass. In the extruder barrel 3, the primary blowing agent is introduced at 7 into the polyethylene mass to subject the mass to cell expansion. This primary blowing agent is introduced at a suitable pressure.

[0058] The preferred primary blowing agent is propane, however butane or a mixture of propane and butane may be used. When using liquid propane as the primary blowing agent, an effective amount of propane is about 15-50% of the low density polyethylene by weight, and more preferably about 20-40% of the low density polyethylene by weight, and more preferably about 24-28% of the low density polyethylene by weight. It is possible that other liquid petroleum gases and mixtures thereof may be utilized but propane, butane and mixtures thereof have been proven to be effective. Another advantage to using liquid propane (or butane) is its cost-effectiveness and availability.

[0059] After the introduction of the primary blowing agent and expansion of the polyethylene mass, the mass is subjected, within the extruder barrel, to a temperature of about 100° C., wherein it begins to cool. Temperatures of about 100° C. prepares the mass for proper and efficient cutting. This completes the heating and blowing process.

[0060] The expanded mass continues its travel through a second portion 8 of the extruder barrel which typically does not have any coil or screw therein. In this second portion 8 of the extruder barrel, a desired quantity of the expanded mass is cut, for example, by a conventional cutting blade 9. The expanded mass is still in a softened state. The desired quantity depends, of course, on the size of the final sheet or tube desired. The cut, expanded mass is next subjected to a temperature of about 105° C. in the extruder barrel and extruded through a die and mandrel 20 into a free expansion zone 10 and cooling zone 11 at atmospheric pressure and room temperature. The temperature of the mass should be raised slightly after cutting because a temperature of about 100° C. is too cool for proper extruding. After extrusion, the foamed polyethylene mass expands naturally in the atmosphere, but not explosively, and cools at room temperature for a short period, e.g., a few seconds. The cooling mass of polyethylene is then formed into a sheet 12 by conventional rollers 13, the thickness being determined by the desired end use of the product.

[0061] The sheet 12 can then be wound on rolls 25, after which it is maintained at room temperature (typically 20° C. to 30° C., preferably about 25° C.) for a curing period of 1-30 days, but preferably closer to 30 days. The cells of the expanded mass are degassed as the entrapped blowing agent works its way out of the cells. Typically 80% of the primary blowing gas is degassed from the cells and not in the sheet within a few days, namely at least two days, and at least 95% of the primary blowing gas is degassed from the cells and not in the sheet by 15 days, and more than 99% (actually more than 99.9%) of the primary blowing gas is degassed from the cells and not in the sheet by 30 days. The closed-cell low density polyethylene sheet of the present invention is available for subsequent processing into other products such as a house wrap or fabric sheet when 80% of the primary blowing agent is degassed from the sheet 12. The sheet 12 must be sufficiently degassed, namely at least 80%, preferably at least 95%, and more preferably at least 99% of the primary blowing agent before the sheet 12 is subsequently processed.

[0062] Testing of the sheet formed according to the present invention, using propane as the primary blowing agent with a curing time of 15 days yielded no trace amounts of butane in the samples tested. The testing was performed by Vapor Analysis by Material Characterization Services LLC at the Oneida Research Services facility in Englewood, Colo. in August 2016. The test was performed three times and utilized two control samples. The gas concentrations were measured in parts per million, wherein measurements of Argon and CO2 being registered in separate control samples at levels as low as 7 parts per million, evidenced the accuracy of the testing, and 0 parts per million of the blowing agent were found in the samples of the invention sheet 12 tested. With the accuracy of the testing performed, this yields a degassing of greater than 99.9993% of the primary blowing agent.

[0063] During the mixing step, additives can be added in appropriate amounts to impart additional characteristics to the final product, such as a flame-retardant such as tin aluminum, zinc, magnesium or a bromine-based flame retardant. A further additive can include about 0.1% to about 0.2% by weight of the polyethylene a cross linking agents such as azobisformamide (ABFA) or dicumyl peroxide, which can be added in powder form to increase the resistance of the final product to tearing, as well as generally increasing the mechanical properties, as well as about 0.1% of an ultra-violet absorber to prevent discoloration and deterioration. Optionally, a separating agent may be included in the initial mixing step. A suitable separating agent to be initially mixed with the low density polyethylene is ZnC (Zinc Carbide). The separating agent, added preferably in powder form, aids in preventing the LDPE from sticking to the coil 5 or walls of the extruder barrel 3. The amount of separating agent added is substantially about 0.3% by weight of the polyethylene. The additives to the dry mix may be in the form of a known Masterbatch (MB) component, which generally is a solid or liquid additive for plastic used for coloring plastics (color masterbatch) or imparting other properties to plastics (additive masterbatch). Masterbatch is a concentrated mixture of pigments and/or additives incorporated during a heat process into a carrier resin, which is then cooled and cut into a granular shape. Color Masterbatch, generally 1-5% by weight of the polyethylene, allows the processor to color the raw polymer economically during the plastics manufacturing process.

[0064] Additionally, the dry mix can include an auxiliary preliminary blowing agent. Suitable auxiliary preliminary blowing agents to be initially mixed with the low density polyethylene, preferably in powder form, include Azodicarbonamide. N,N′-dinitrosopentamethylene-tetramine, (commercially-available as Unicel NDX, gasifying temperature of about 195° C.), and 4,4′ Oxybis (commercially-available as Celogen OT, gasifying temperature of about 150° C. Azodicarbonamide, or azo(bis) formamide, is a chemical compound with the molecular formula C.sub.2H.sub.4O.sub.2N.sub.4, with a CAS #123-77-3, and a gasifying temperature of about 195° C. N,N′-dinitrosopentamethylene-tetramine has a CAS #101-25-7, and also has a gasifying temperature of about 195° C. 4,4′ Oxybis is a chemical compound with the molecular formula C.sub.4H.sub.10O.sub.3 with a Cas #111-46-6, and a gasifying temperature of about 150° C. The amount of auxiliary preliminary blowing agent added is about 0.5-2%, and preferably about 1% by weight of the polyethylene. Azodicarbonamide is the preferred initial auxiliary blowing agent.

[0065] With the use of an initial auxiliary blowing agent, a surface activation agent may also be initially mixed with the low density polyethylene, preferably in powder form, and suitable surface activation agents include zinc oxide, cadmium oxide and calcium carbonate. The surface activation agent is added in an amount ranging from about 0.1 to about 0.2% by weight of the polyethylene. The surface activation agent performs several important functions. First, it activates the blowing process while preventing too rapid an expansion of the LDPE cells during initial blowing. Secondly, it keeps the temperature in the extruder barrel 3 down during the initial blowing process. For example, where azodicabonamide is used as the auxiliary blowing agent, the surface activation agent assists in maintaining a temperature of around 150° C. in the relevant stage of the extruder barrel 3. In the absence of this agent, the gasified blowing agent would raise the temperature to around 196° C.

[0066] The use of the auxiliary blowing agent allows the mass to be heated and mixed to form a homogeneous mixture then heated to gasify the preliminary auxiliary blowing agent in a first blowing step, then the partially expanded mass is generally cooled prior to being reheated to the appropriate temperature for the blowing with the primary blowing agent discussed above.

[0067] With the use of the auxiliary blowing agent, the total residence time in the extruder barrel 3 generally ranges from about 30 minutes to about 1 hour to complete the process. The auxiliary blowing agent, if used, can be considered as part of the primary blowing agent for degassing purposes, whereby the sheet 12 must be sufficiently degassed, namely at least 80%, preferably at least 95% and more preferably at least 99% of the blowing agents are removed (including both the primary and the auxiliary blowing agents if an auxiliary blowing agent is used) before it is subsequently processed.

[0068] House Wrap

[0069] The closed cell expanded low density polyethylene sheet 12 formed by the present invention can be formed into a variety of products, and it is particularly well suited for products utilizing high thermal resistance (without exposure to extreme high temperatures that would melt the foam) and flexibility. One of these include a composite house wrap 100 as outlined herein and shown in FIGS. 3-6, the primary embodiment shown in FIGS. 3-4.

[0070] Without being limited to theory, it is believed that the process of forming the low density expanded polyethylene foam 12 of the invention creates a firmer cell that keeps the cell structure from collapsing, and allows the blowing agent to fill the cells and then evacuate, through hydrocarbon-philic chemistry, without collapsing the cell structures and, therefore, yields an effectively evacuated cell or vacuum (or technically a partial vacuum). A vacuum is the best form of insulation, and the manufacturing process results in an extremely thin material which is highly insulating as the numerous cell walls create a tortuous path for thermal conductivity. By creating micro cells that are semi-rigid and have or form contain a vacuum, the house wrap 100 becomes advantageous for the building industry. With stacking these “evacuated cells” on top of each other (multiple layers 12 and/or thicker layers 12) and creating a barrier to trap restrict heat or air conditioned airflow. A 1.5 mm extruded composite house wrap 100 produces an R-6 product.

[0071] In summary, one aspect of the present invention relates to a composite house wrap 100 provided with integral sections or layers 50, 40, 30 and 12 as described below. The house wrap 100, according to the present invention shown in FIGS. 3-4, will provide barrier protection plus provide moisture vapor transmission and an insulation R-value of approximately R-6 or higher.

[0072] The terms about. Of approximately or similar terms should be read as meaning within ten percent within this application. This house wrap 100 is specifically designed to add enhanced insulating characteristics as opposed to conventional house wraps, while maintaining a cost effective and easy-to-handle house wrap.

[0073] As with most extruded material and prior art LDPE, the LDPE layer(s) 12 of the house wrap 100 utilizes a gas injection process to create a structure of randomized gas-filled spheres throughout the material of the sheet 12. However, unlike any other extruded material or other LDPE structures, the injection gas used to create the gas-filled spheres within the layer 12 is completely expunged from the material during the curing process, thereby creating a unique extruded material. The material has been tested and determined to be comprised of a countless number of evacuated cells without even a trace amount of the injection or blowing gas used in the creation of the material. There is a class of insulation materials known as mass insulation. The measured insulation magnitude of mass insulation materials is referred to as an R-value. The R-value is dependent upon the thermal conductivity [W/(m-° K)] of the material and the pathlength that the heat traverses. (thermal energy). It is for this reason that the thickness of mass insulation is commonly treated or accepted as a linear function with respect to the material's R-value. The reason for this treatment or acceptance is due to the fact that very frequently heat traverses through mass insulation as a linear function of its thickness. Hence, R-value is a linear function of a material's thickness. The material structure description of the sheet 12 of the invention reveals that a more accurate classification for this insulation material is “absence of mass” insulation, which is due to the fact that its structure consists of a countless number of evacuated cells that are devoid of mass, namely elemental and molecular gases. The material is essentially comprised of randomized structures of the evacuated cells. Due to the cells' evacuated state, their thermal conductivity across the cell approaches the value of a vacuum, which is zero. The result is that each evacuated cell acts as a thermo-physical barrier to the conduction of heat through the material. This interrupts the natural directional flow of heat, and introduces a three-dimensional non-linear tortuous path in which the heat traverses through the material through the cell walls. It is important to realize that the tortuous path shown in the figures only illustrate a two-dimensional tortuous path when, in fact, it is actually a significantly more complex three-dimensional tortuous path. It is key to understand that the R-value for “absence of mass” insulation material is greatly enhanced by the length of the tortuous path traversed by the heat (thermal energy).

[0074] The house wrap 100 has a total thickness of generally less than 80 mils for the embodiment of FIGS. 3-4 and effectively always less than 175 mils for the embodiments of FIGS. 5-6. The house wrap 100 can be attached to a building in any conventional fashion, such as nail guns, or the like. The house wrap 100 has the flexibility and durability that is comparable to, and actually better than many, existing commercial house wraps. The house wrap 100 of the present invention can also be used as a roof paper or roof underlay.

[0075] The first, or front or drainage plane layer 40 is a reinforcing grid or mesh that functions as a drainage plane and will face the outside cladding. The mesh layer 40 can be formed effectively from polyethylene, however substantially any material providing the structural equivalent and suitable for the desired work environment could be used. The thickness of the mesh layer 40 and barrier layer 30 is, typically less than 10 mils, generally 8-9 mils. The mesh layer 40 can be formed effectively of into a wide variety of grid patterns, even a structural non-grid pattern of structural as suggested again below.

[0076] The front layer 40 serves a drainage function by providing a space for water drainage. Secondly, the front layer 40 as well as the barrier layer 30 serves as a reinforcing member for the house wrap 100 to provide structural integrity to the entire assembly.

[0077] The front layer 40 could take other forms, such as spaced ribs or an elongated diamond pattern. Essentially the spaced ribs alternative design would be the mesh layer 40 without the cross bracing. The spaced ribs could be vertical or angled at essentially any angle to form more definitive drainage channels. A “vertical” orientation of such ribs would also allow the house wrap 100 to be easily rolled up in one direction (i.e. rolled about an axis parallel to the ribs). The ribs need not be straight members, but each rib could be a zig-zag, herringbone-shaped or diamond-shaped construction. The interconnected mesh layer 40 of the preferred embodiment is believed to add structural integrity while still allowing for an efficient drainage plane for the house wrap 100.

[0078] The second or middle or barrier film layer 30 is a breathable, non-perforated barrier film 30 which is bonded to the first layer 40 and together have a thickness of no greater than about 10 mils, generally 8-9 mils as noted. The second or middle layer 30 may be formed of a polyethylene (PE) or a Polyurethane (PUR) material, but a myriad of other breathable film layer materials could be used assuming the cost concerns could be addressed, such as PVC film or polytetrafluoroethylene (PTFE) film. The PE or PUR materials are the most cost effective. In one embodiment, the film 30 is bonded to the layer 40 through thermal bonding. Other bonding techniques may be used, such as adhesives. The film layer 30 should have acceptable breathability for the field of house wraps.

[0079] Collectively, the film layer 30 and layer 40 may be tested or evaluated together for forming the house wrap 100. Collectively, the film layer 30 and layer 40 should exhibit an ASTM E-2273 (2016) test result of greater than 95%. ASTM E-2273 represents the standard test method for determining drainage efficiency of exterior insulation and finish system clad wall assemblies. Collectively, the film layer 30 and layer 40 should exhibit an air porosity (Gurley-Hill Air Porosity—TAPPI T-460 (2016)) of at least two thousand sec. Collectively, the film layer 30 and layer 40 should exhibit a water resistance of at least three hundred cm (AATCC-127 (2016).

[0080] The rear or foam layer 12 is a perforated expanded low density polyethylene foam 12 that is formed as noted above, and that is bonded to the middle layer 30, such as through nonwoven layer 50. The nonwoven layer 50 is the third layer.

[0081] The fourth or rear LDPE foam layer 12 is perforated, wherein a series of equally spaced perforations may extend through the layer 12. The perforations can be conical which may provide certain advantages to the house wrap 10 of the present invention. However, cylindrical shaped perforations would also be acceptable. The perforations can be formed on layer 12 through a perforation roller which has a series of perforation pins thereon. For the conical shaped perforations as shown, the pins would have a shape similar to the final desired shape of the perforations (with three holes per square inch being a preferred perforation density). The layer 12 can be perforated before it is assembled, which is the accepted perforation method, or the perforations can be made after the house wrap is assembled, which is less desirable.

[0082] The foam layer 12 should be about 1-1.1 millimeters (39-43 mils) in thickness, generally less than 45 mils, and always less than 75 mils for a conventional house wrap 100 of FIGS. 3-4. This design will provide insulation R-values of R-6 or greater.

[0083] The non-woven layer 50 of two to six mils thickness provides an improved bonding layer or adhesion-promoting layer for the barrier film layer 30 and the foam layer 12, and yields improved stability and performance to the house wrap 100. Nonwoven layer 50 is formed from staple fibers, such as polyester fibers, bonded together by chemical, mechanical, thermal or solvent treatment. The non-woven layer 50 may be described as denoting a fabric which is neither woven nor knitted.

[0084] The FIGS. 3-4 show a house wrap 100 embodiment with a single layer of foam layer 12, however as noted above, multiple layers could be used as shown in the embodiment of FIG. 5. Hypothetically, a thick house wrap 100 up to ½ inch thick having multiple layers 12 exhibits an R-30 value. ASTM C-518 doesn't allow for multiple layers (>2 layers). An extended or thicker foam layer 12 of up to 2.5 millimeters (98 mils) can be formed using the process of the present invention and this is shown in FIG. 6 and represents an alternative method of achieving R-values up to R-15.

[0085] The foam 12 of the invention has other uses as well. Another particularly useful product is utilizing the LDPE foam in the construction of a composite fabric material as disclosed in U.S. Pat. No. 8,429,764, which is incorporated herein by reference.

[0086] Whereas particular embodiments of the invention have been described above for purposes of illustration, it will be evident to those skilled in the art that numerous variations of the details of the present invention may be made without departing from the spirit and scope of the present invention.