US20100272898A1

US20100272898A1 - Method for preparing a selectively permeable protective structure

Info

Publication number: US20100272898A1
Application number: US12/762,919
Authority: US
Inventors: John Chu Chen; Donna Lynn Visioli
Original assignee: EI Du Pont de Nemours and Co
Current assignee: EIDP Inc
Priority date: 2009-04-23
Filing date: 2010-04-19
Publication date: 2010-10-28
Also published as: EP2421709A1; US9321250B2; US20100273380A1; WO2010124054A1; WO2010124051A1; JP2012524833A; CN102414021A

Abstract

A method for preparing a selectively permeable protective structure. The selectively permeable structure comprises a membrane having a moisture vapor permeation value of at least 200 g-mil/m²/24 h and barrier to liquid water, and a supporting substrate.

Description

This application claims priority to U.S. provisional application 61/172,036, filed Apr. 23, 2009 now pending and U.S. provisional application 61/237,789, filed Aug. 28, 2009 now pending; the entire disclosures of which are incorporated herein by reference.
This invention relates to a method for preparing a selective permeable structure.

BACKGROUND

Personal protection from exposure to harmful chemical and biological agents is often of concern to firefighters, medical practitioners and similarly situated personnel. Such protection often includes the use of apparel that provides a barrier to such agents. Butyl rubber is often used in standard protective clothing. However, garments made from butyl rubber are bulky and nearly impermeable to air and moisture (I. Lee, Yang and Wilusz;
Polymer Engineering & Science, 1996, 36, 1217) resulting in unbearable levels of heat inside the garments during use. Other protective apparel includes textiles coated with polymeric materials to provide a chemical and/or biological barrier.
Equipment is often wrapped or packaged with film or fabric tarpaulins, hoods or other covers to prevent surface damage during transportation and storage. These covers may be prepared from high barrier (highly moisture impermeable) films and fabrics (see, e.g., http://www.heritagepackaging.com/productservices/barrierpackaging/bpbasics/bp basics.htm).
Many relatively small items are shipped on pallets, that is, platforms that are easily moved by forklifts or small cranes. Pallets provide convenience in loading and unloading goods from shipping containers, and in moving smaller amounts of goods over shorter distances, such as within warehouses, or to deliver a retail quantity. The small items may be unpackaged or packaged, for example in bags or boxes, when they are placed on the pallets.
A loaded pallet preferably has integrity and stability, so that the goods are not damaged or lost during shipping. To provide the necessary integrity and stability, the pallet and its load have been typically wrapped together in film, for example overlapping layers of polyethylene stretch wrap that may be applied by machine or by hand. See, e.g., US RE38429. Other generally practiced methods of providing integrity and stability to loaded pallets include wrapping the pallet and its load in heat shrinkable film, encasing the loaded pallet in a sheath or “hood” which may be heat shrinkable or stretchable, and containing the goods in a single carton or box. These methods are sometimes referred to, individually or collectively, as “pallet unitizing”.
Using barrier films for wrapping small objects or articles in sealed bags is generally suitable since the object may be dried before being sealed in the bags and/or drying agents may be included inside the sealed bags. This approach is less suitable for large objects such as vehicles, boats, motors, machinery, industrial goods, pallets or containers holding smaller articles, and other bulky equipment because the covers are typically not hermetically sealed around the object and thorough drying of the object may not be feasible. This may be especially problematic during storage or when shipping by ship or railroad, because the large objects may be exposed to adverse weather conditions for long periods of time. Atmospheric moisture and/or rain may enter the space under the cover and be trapped and condense. With high barrier covers, there is no way for water to permeate back outside the cover, resulting in a buildup of moisture inside the cover, leading to the possibility of corrosion.
Large amounts of money are lost each year because of corrosion of, for example, iron, steel, and other metals. There are many factors affecting corrosion rate including moisture, oxygen, and salt presence. A common corrosion occurs due to electrochemical reactions at high humidity conditions. For example, when iron is exposed to moist air, it reacts with oxygen to form rust (iron oxide). The result of corrosion may be the formation of metal oxide that flakes off easily, causing extensive pitting thereby causing structural weakness and disintegration of the metal. Corrosion can also affect other properties of metal parts such as reducing conductivity or increasing surface roughness so that moving parts become unable to move freely.
In addition to corrosion of metals, mold growth may occur in the condensed moisture on the surface of the equipment.
Using a film or cover with a high water vapor transmission rate can prevent condensation of water inside the cover by allowing equilibration of the trapped moisture back into the surrounding atmosphere. Using such a film prevents or reduces rust formation and corrosion and reduces the opportunity for mold growth.
Various permeable materials having a wide range of mechanical and transport properties are known. Depending upon the particular application in which the permeable material is to be employed, however, certain combinations of properties are required. For example, in a protective apparel application, it is desirable that the material may transport water vapor and block the transport of harmful chemicals and/or biological agents, and be lightweight and flexible over a broad temperature range. A need exists for a material that can be a flexible, solid material with membrane characteristics that facilitate the transport of water vapor, for example, from a wearer of membrane-containing apparel to the atmosphere; allow moisture to permeate the garments to the extent necessary to afford comfort to the wearer, thus reducing heat stress; and block entry of certain chemical compounds and biological agents.
Many previous permeable membranes are microporous (i.e., permeable due to the presence of microscopic pores through which vapor can pass). Microporous membranes, which may be laminated on or between nonwoven textiles, have increased permeability, but may not provide adequate barriers to liquids because of their nonselective permeability. Liquids under pressure may be able to penetrate the pores. Most microporous films are biaxially oriented, so only a small amount of shrinkage is possible, and they cannot be shrunk without losing their porosity. They may also have low tear strength and their surfaces may be easily fouled, thereby losing permeability.
Various references describe semipermeable materials produced from a variety of polymers that may be useful for protective covers. See e.g., U.S. Pat. No. 6,579,948. Recently protective fabrics comprising a selectively permeable membrane comprising organic acid-modified ionomer compositions have been disclosed (U.S. Pat. No. 7,514,380). Although compositions disclosed therein provide excellent selective permeability, adhesion to certain textiles may be insufficient to provide a robust protective structure.
Because no single material has emerged which satisfies all of the technical requirements and that presents a cost-effective alternative, it is desirable to provide a selectively permeable membrane or structure or layer that displays a combination of mechanical properties, low temperature flexibility, selective transport, ease of processability, and cost-effectiveness, so as to render it suitable for use as a protective cover for objects that limits corrosion and/or mold growth.

SUMMARY OF THE INVENTION

This invention provides a method for preparing a selectively permeable multilayer structure or article comprising or consisting essentially of:
1) preparing a first composition comprising, consisting essentially of, or consisting of
(i) one or more ethylene acid copolymers; and
(ii) one or more organic acids; wherein at least 50% of the combined acidic groups in the acid copolymer and the organic acid are nominally neutralized to salts with metal ions and at least 50% of the metal ions are alkali metal ions;
(2) melt blending the first composition with a terpolymer of ethylene, acrylic acid or methacrylic acid, and an alkyl acrylate or alkyl methacrylate;
and optionally with one or more ethylene-containing polymers selected from the group consisting of polyethylene (PE) homopolymers, copolymers of ethylene and an α-olefin, copolymers of ethylene and a diolefin, and ethylene copolymers obtained from copolymerization of ethylene with at least one polar monomer selected from the group consisting of vinyl acetate, acrylic ester, methacrylic ester and carbon monoxide, wherein the ethylene-containing polymer does not comprise a carboxylic acid comonomer, to provide a second composition in a molten condition;
3) contacting a substrate with the molten second composition to adhere, embed, or impregnate the melted composition to the substrate or adhere, embed, or impregnate the substrate to the molten second composition to provide a coated substrate;
4) cooling the coated substrate to allow the molten second composition to cool and solidify.
In the method, the one or more ethylene acid copolymers may comprise an E/W ethylene acid copolymer or ionomer of the acid copolymer wherein E represents copolymerized units of ethylene, W is present in about 2 to about 35 weight % of the copolymer and represents copolymerized units of at least one C₃to C₈α,β-ethylenically unsaturated carboxylic acid; and the one or more monocarboxylic acids have from 4 to 36 carbon atoms, or salts thereof.
An embodiment is one in which the second composition comprises, consists essentially of, or consists of
(a) 30 to 99 weight %, based on the combination of (a), (b) and (c), of a blended combination of
(1) 70 to 90 weight %, based on the combination of (1) and (2), of one or more E/W ethylene acid copolymers or ionomers of the acid copolymers wherein E represents copolymerized units of ethylene, X is present in about 2 to about 35 weight % of the copolymer and represents copolymerized units of at least one C₃to C₈α,β-ethylenically unsaturated carboxylic acid;
(2) 10 to 30 weight %, based on the combination of (1) and (2), of one or more organic acids having from 4 to 36 carbon atoms, or salts thereof; wherein at least 50% of the combined acidic groups in the E/W copolymer and the organic acid are nominally neutralized to salts with metal ions; wherein at least 50% of the metal ions are alkali metal ions;
(b) 1 to 30 weight %, based on the combination of (a), (b) and (c), of E/X/Y ethylene acid terpolymers wherein E represents copolymerized units of ethylene, X is present in about 2 to about 35 weight % of the copolymer and represents copolymerized units of acrylic acid or methacrylic acid, and Y is present in about 1 to about 35 weight % of the copolymer and represents copolymerized units of alkyl acrylate or alkyl methacrylate; and
(c) 0 to 60 weight %, based on the combination of (a), (b) and (c), of one or more second ethylene-containing polymer selected from the group consisting of polyethylene homopolymers, copolymers of ethylene and an α-olefin, copolymers of ethylene and a diolefin, and ethylene copolymers obtained from copolymerization of ethylene with at least one polar monomer selected from the group consisting of vinyl acetate, acrylic ester, methacrylic ester and carbon monoxide, wherein the second ethylene-containing polymer does not comprise a carboxylic acid comonomer; wherein (a), (b) and (c) total 100 weight %.
Of note is the method wherein the second composition comprising (a), (b) and optionally (c) has greater adhesion to the substrate than a corresponding composition comprising (a) that does not comprise (b), the other components being identical.
The method can be used to prepare a selectively permeable structure that can be used as a protective article. Notably, the second composition has a moisture vapor permeation value (MVPV) of at least 200 g-mil/m²/24 h and high water-entry pressure; and the selectively permeable structure has a moisture vapor transmission rate (MVTR) of at least 30 g/m²/24 h. The MVPV and MVTR are measured at 37.8° C. and 100% relative humidity according to ASTM F-1249.

DETAILED DESCRIPTION OF THE INVENTION

The entire disclosures of all references are incorporated herein by reference and tradenames or trade marks are shown in upper case. The word(s) following the verb “is” can be a definition of the subject.
“(Meth)acrylic acid” includes methacrylic acid and/or acrylic acid and “(meth)acrylate” includes methacrylate and/or acrylate.
“Selectively permeable” means permeation is allowed only to certain molecules in a specific state such as vapor or gas and not to other molecules or in a different state such as liquid or solid. Such molecules can be dissolved or dispersed in the matrix of certain materials such as a film or sheet of the composition disclosed herein and thereafter be diffused or migrated through the material.
The selectively permeable composition may have MVPV of at least 200, at least 800, at least 900, at least 1200, at least 2000, at least 4,000 g-mil/m²/24 h, or even higher. MVPV is an indicator of the inherent permeability of the composition, by measuring moisture permeation of a membrane comprising the composition, which may be a film or sheet that is normalized to 1 mil thickness.
Selectively permeable protective articles may have MVTR of at least 30, at least 50, at least 100, at least 500, or at least 1000 g/m²/24 h, or even higher. MVTR measures total moisture vapor transmitted through an article across its smallest dimension during a unit time, disregarding the structure thickness. For a membrane of a given composition and MVPV, MVTR decreases as the thickness increases.
A selectively permeable article provides a combination of mechanical properties, low temperature flexibility, selective transport, ease of processability, and cost-effectiveness.
Extrusion coating a selectively permeable composition comprising an organic acid modified-ionomer composition, as disclosed in U.S. Pat. No. 7,514,380, onto substrates such as paper or fabrics has experienced poor adhesion of the composition to the substrate. Previously, inclusion of 20 to 30 weight % of ethylene alkyl (meth)acrylate copolymers have been used to improve adhesion of other selectively permeable compositions (e.g., copolyester amide copolymers [PEBAX®]) to substrates. While improving adhesion, the ethylene alkyl (meth)acrylate copolymers may have a negative effect on the moisture breathability of the coating.
Surprisingly, an ethylene acrylic acid alkyl (meth)acrylate terpolymer (e.g., ethylene (meth)acrylic acid n-butyl acrylate terpolymer) can be effective in promoting the adhesion of organic acid-modified ionomer to fabrics under relatively mild processing conditions. At 10 weight % level (versus a typical modification level of 30 weight % for ethylene alkyl acrylate dipolymers) such a terpolymer demonstrated enhanced fabric adhesion, while adequately retaining the moisture permeability of the original organic acid modified ionomer.
The composition can be formed into a monolithic or continuous membrane that functions as a selectively permeable barrier. Monolithic continuous membranes, in contrast to microporous membranes, have high water-entry pressure and are waterproof and liquidproof. High water-entry pressure refers to >150 cm (or >250 cm or >500 cm) H₂O hydrostatic head, as described in DIN EN20811:92.
Therefore, monolithic membranes provide barriers to liquids such as water, while still allowing permeability to water vapor under appropriate conditions. A monolithic barrier is also effective at preventing exposure to liquids such as water, solvents, oils, corrosive fluids and the like, or particulates or solids, including dust, irritants, mold spores, allergens, pollen, animal dander, hair and the like.
The selectively permeable membrane may be selective to liquid penetrants depending on the size and polarity of the penetrants, i.e., has selectivity so as to be capable of allowing water to diffuse through at a higher rate than virtually all organic liquids having a molecular weight higher than that of methanol.
The acid copolymers used in the method are preferably “direct” or “random” acid copolymers. Direct or random copolymers are polymers polymerized by adding all monomers simultaneously, as distinct from a graft copolymer, where another monomer is grafted onto an existing polymer, often by a subsequent free radical reaction.
In the first step of the method, an organic acid-modified ionomer is prepared from an ethylene acid copolymer that comprises one or more E/W copolymers where E represents copolymerized units of ethylene, W represents copolymerized units of at least one C₃-C₈α,β-ethylenically unsaturated carboxylic acid, and W can be from about 3 to 35, 4 to 25, or 5 to 20, weight % of the E/W copolymer and ethylene can make up the rest.
Examples of W include acrylic acid or methacrylic acid. Specific acid copolymers include ethylene/acrylic acid dipolymers and ethylene/methacrylic acid dipolymers. An ethylene/methacrylic acid dipolymer of note comprises 19 weight % of copolymerized units of methacrylic acid.
Ethylene acid copolymers may be produced by any methods known to one skilled in the art such as use of “co-solvent technology” disclosed in U.S. Pat. No. 5,028,674.
Ionomers are obtained by neutralization of an acid copolymer. Neutralizing agents including metal cations such as sodium or potassium ions are used to neutralize at least some portion of the acidic groups in the acid copolymer. Unmodified ionomers are prepared from the acid copolymers such as those disclosed in U.S. Pat. No. 3,264,272. “Unmodified” refers to ionomers that are not blended with any material that has an effect on the properties of the unblended ionomer. The acid copolymers may be used to prepare unmodified, melt processable ionomers by treatment with a metal compound. The unmodified ionomers may be nominally neutralized to any level such as about 15 to about 90% or about 40 to about 75% of the acid moieties.
The organic acids may be monobasic, having fewer than 36 carbon atoms, or salts thereof. The acids are optionally substituted with from one to three substituents independently selected from the group consisting of C₁-C₈alkyl, OH, and OR¹in which each R¹is independently C₁-C₈alkyl, C₁-C₆alkoxyalkyl or COR²; and each R²is C₁-C₈alkyl.
Examples of organic acids include C₄to C₃₆(such as C₃₄, C_4-26, C_6-22, or C_12-22) acids. At high neutralization such as greater than 80%, up to 100%, nominal neutralization (i.e., sufficient metal compound is added such that all acid moieties in the copolymer and organic acid are nominally neutralized), volatility is not an issue and organic acids with lower carbon content may be used, though it is preferred that the organic acid (or salt) be non-volatile (not volatilize at temperatures of melt blending of the agent with the acid copolymer) and non-migratory (not bloom to the surface of the polymer under normal storage conditions (ambient temperatures)). Examples of organic acids include, but are not limited to, caproic acid, caprylic acid, capric acid, lauric acid, stearic acid, isostearic acid, arachidic acid, behenic acid, erucic acid, oleic acid, and linoleic acid. Organic (fatty) acids include palmitic acid, stearic acid, oleic acid, erucic acid, behenic acid, isostearic acid, 12-hydroxystearic acid, or combinations of two or more thereof. Saturated organic acids, such as stearic acid, arachidic acid, and behenic acid, may be preferred.
Organic acids may be commercially available as a mixture of named organic acid(s) and a number of structurally different organic acids of varying lesser amounts. When a composition comprises a named acid, other unnamed acids may be present at levels conventionally known to be present in commercial supplies of the named acid. For example, a commercially available mixture of acids includes 90 weight % of a mixture of arachidic acid (C₂₀acid) and behenic acid (C₂₂acid) with 6 weight % of C₁₈acids and 4 weight % of other acids.
Salts of any of these organic acids may include the alkali metal salts, such that the metal ions present in the final composition comprise at least 50% of alkali metal ions, including lithium, sodium, potassium salts and/or cesium salts, preferably sodium salts or potassium salts.
The amount of basic metal compound capable of neutralizing acidic groups may be provided by adding the stoichiometric amount of the basic compound calculated to neutralize a target amount of acid moieties in the acid copolymer and organic acid(s) in the blend (herein referred to as “% nominal neutralization” or “nominally neutralized”). Thus, sufficient basic compound is made available in the blend so that, in aggregate, the indicated level of nominal neutralization could be achieved. Greater than 50%, 60%, 70%, 80% or 90% (or even 100%) of the total acidic groups in the E/X/Y copolymers and organic acids may be nominally neutralized with metal ions; and the metal ions comprise at least 50 mole % alkali metal ions, preferably sodium or potassium. Small amounts of salts of alkaline earth metal and/or transition metal ions may be present in addition to the alkali metals.
Metal compounds may include compounds of alkali metals, such as lithium, sodium, potassium, or cesium or combinations of such cations. Examples include sodium, potassium, cesium or any combination of sodium, potassium, and/or cesium, optionally including small amounts of other cations such as other alkali metal ions, transition metal ions or alkaline earth ions. Metal compounds of note include formates, acetates, nitrates, carbonates, hydrogencarbonates, oxides, hydroxides or alkoxides of the ions of alkali metals, especially sodium and potassium, and formates, acetates, nitrates, oxides, hydroxides or alkoxides of the ions of alkaline earth metals and transition metals. Of note are sodium hydroxide, potassium hydroxide, sodium acetate, potassium acetate, sodium carbonate and potassium carbonate.
The ethylene acid copolymers or unmodified ionomers may be mixed with organic acids or salts thereof and/or metal compounds, by any means known to one skilled in the art, to prepare a blended modified ionomer composition comprising (1) and (2) as described above. It is substantially melt-processable and may be produced by combining one or more ethylene acid copolymers, one or more monobasic carboxylic acids or salts thereof, basic compound(s) to form a mixture; and heating the mixture under a condition sufficient to produce the composition. Heating may be carried out under a temperature in the range of from about 80 to about 350, about 100 to about 320, or 120 to 300° C. under a pressure that accommodates the temperature for a period from about 30 seconds to about 2 or 3 hours. For example, the composition may be produced by melt-blending an acid copolymer and/or ionomer thereof with one or more organic acids or salts thereof; concurrently or subsequently combining a sufficient amount of a basic metal compound capable of neutralization of the acid moieties to nominal neutralization levels greater than 50, 60, 70, 80, 90%, to near 100%, or to 100%. A salt-and-pepper blend of components may be heated or the components may be melt-blended in an extruder. For example, a twin-screw extruder may be used to mix and treat the acid copolymer and the organic acid (or salt) with the metal compound at the same time. It is desirable that the blending is conducted so that the components are intimately mixed, allowing the basic metal compound to neutralize the acidic moieties.
Treatment of acid copolymers and organic acids with metal compounds in this manner (concurrently or subsequently), such as without the use of an inert diluent, may produce a composition without loss of processability or properties such as toughness and elongation to a level higher than that which would result in loss of melt processability and properties for the ionomer alone.
In a second step, the organic acid-modified ionomer is melt blended with an E/X/Y ethylene acid terpolymer and optionally a second ethylene-containing polymer as defined above.
The ethylene acid terpolymers are preferably direct or random acid copolymers. The ethylene acid terpolymer component comprises one or more E/X/Y terpolymers where E represents copolymerized units of ethylene, X represents copolymerized units of at least one C₃-C₈α,β-ethylenically unsaturated carboxylic acid, Y represents copolymerized units of a softening comonomer (softening means that the polymer is made less crystalline).
Examples of X include acrylic acid or methacrylic acid and X can be from about 3 to 35, 4 to 25, or 5 to 20, weight % of the E/X/Y copolymer and ethylene can make up the rest. Examples of Y include alkyl acrylate, alkyl methacrylate, or combinations thereof wherein the alkyl groups have from 1 to 8, or 1 to 4, carbon atoms. Notable are E/X/Y copolymers wherein Y is present in at least 1 weight %, or about 2 to about 35 weight % of the E/X/Y copolymer. Ethylene can make up the rest of the E/X/Y terpolymer.
Specific terpolymers include ethylene/acrylic acid/n-butyl acrylate, ethylene/methacrylic acid/n-butyl methacrylate, ethylene/acrylic acid/iso-butyl acrylate, ethylene/methacrylic acid/iso-butyl methacrylate, ethylene/acrylic acid/methyl acrylate, ethylene/methacrylic acid/methyl methacrylate, ethylene/acrylic acid/ethyl acrylate and ethylene/methacrylic acid/ethyl methacrylate terpolymers, or combinations of two or more thereof.
Preferably, the modified ionomer combination of (1) and (2) is prepared and subsequently blended with the E/X/Y terpolymer. Blending the E/X/Y terpolymer with the E/W dipolymer prior to, or simultaneously with, conversion of the E/W dipolymer to the organic acid-modified ionomer may result in a composition in which improved adhesion to substrates is not observed.
Optionally, an additional ethylene-containing polymer may be blended with the organic acid-modified ionomer and E/X/Y terpolymer. Blending with such polymers may provide better processability, improved toughness, strength, flexibility, and/or compatibility of the blend when adhering to a substrate as described below. The compositions may comprise 0 to 60 weight %, preferably 0 to 30 weight % of the additional ethylene-containing polymer, such as 0.1 to 60 weight % or 0.1 to 30 weight %.
The ethylene-containing polymers may include polyethylene (PE) homopolymers and copolymers. PE homopolymers and copolymers may be prepared by a variety of methods, for example, the well-known Ziegler-Natta catalyst polymerization (e.g., U.S. Pat. No. 4,076,698 and U.S. Pat. No. 3,645,992), metallocene catalyzed polymerization, VERSIPOL catalyzed polymerization and by free radical polymerization. The polymerization may be conducted as solution phase processes, gas phase processes, and the like. Examples of PE polymers may include high density PE (HDPE), linear low density PE (LLDPE), low density PE (LDPE), very low or ultralow density PEs (VLDPE or ULDPE), lower density PE made with metallocene having high flexibility and low crystallinity (mPE). Metallocene technology is described in, for example, U.S. Pat. Nos. 5,272,236, 5,278,272, 5,507,475, 5,264,405, and 5,240,894.
The density of PE may range from about 0.865 g/cc to about 0.970 g/cc. Linear PE may incorporate α-olefin comonomers such as butene, hexene or octene to decrease density to within the density range so described. For example, a copolymer may comprise a major portion (by weight) of ethylene that is copolymerized with another α-olefin having 3-20 carbon atoms and up to about 20% by weight of the copolymer. Other α-olefins are propylene, 1-butene, 1-hexene, 4-methyl-1-pentene, 1-octene, 1-decene, 1-tetradecene, 1-octadecene, or in combinations of two or more. Of note are metallocene polyethylenes comprising ethylene/octene copolymers.
The PE copolymer may also be an ethylene propylene elastomer containing a small amount of unsaturated compounds having a double bond. The term “PE” when used herein is used generically to refer to any or all of the polymers comprising ethylene described above.
Ethylene copolymers having small amounts of a diolefin component such as butadiene, norbornadiene, hexadiene and isoprene are also generally suitable. Terpolymers such as ethylene/propylene/diene monomer (EPDM) are also suitable.
The ethylene-containing polymer may include ethylene copolymers obtained from copolymerization of ethylene with at least one polar monomer such as ethylene/vinyl acetate copolymer (EVA), ethylene/acrylic ester copolymers, ethylene/methacrylic ester copolymers, ethylene/vinyl acetate/CO copolymers, ethylene/acrylic ester/CO copolymers, and/or mixtures of any of these.
EVA includes copolymers derived from the copolymerization of ethylene and vinyl acetate or the copolymerization of ethylene, vinyl acetate, and an additional comonomer. The vinyl acetate comonomer may have 2 to 45 or 6 to 30 weight % derived from vinyl acetate. An EVA may have a melt flow rate, measured in accordance with ASTM D-1238, of from 0.1 to 60 g/10 or 0.3 to 30 g/10 minutes. A mixture of two or more different EVAs may be used.
Ethylene/alkyl (meth)acrylate copolymer includes copolymers of ethylene and one or more C_1-8alkyl (meth)acrylates. Examples of alkyl (meth)acrylates include methyl acrylate, ethyl acrylate and butyl acrylate. Examples of the copolymers include ethylene/methyl acrylate copolymer ethylene/ethyl acrylate copolymer, ethylene/butyl acrylate copolymer, or combinations of two or more thereof. Alkyl (meth)acrylate may be incorporated into an ethylene/alkyl (meth)acrylate copolymer at 2 to 45, 5 to 45, 10 to 35, or 10 to 28 weight %.
Ethylene/alkyl (meth)acrylate copolymers may be prepared by processes well known to one skilled in the art using either autoclave or tubular reactors.
See, e.g., U.S. Pat. Nos. 2,897,183, 3,404,134, 5,028,674, 6,500,888, and 6,518,365. Because the methods for making an ethylene/alkyl (meth)acrylate copolymer are well known, the description of which is omitted herein for the interest of brevity. Tubular reactor produced ethylene/alkyl (meth)acrylate copolymers are commercially available from E. I. du Pont de Nemours and Company, Wilmington, Del. (DuPont) such as ELVALOY® AC. The ethylene/alkyl (meth)acrylate copolymers may vary significantly in molecular weight and the selection of the melt index (MI) grade of polymer may be made by balancing the properties of the ethylene/alkyl (meth)acrylate copolymer with those of the neutralized organic acid and ethylene acid copolymer to provide the desired mix of permeability and structural properties needed for a specific variable permeability construction. A mixture of two or more different ethylene/alkyl (meth)acrylate copolymers may be used. Of note is the method wherein the second composition has at least one ethylene/alkyl (meth)acrylate copolymer present in from 5 to 30 weight %.
Preferably, the modified ionomer combination of (1) and (2) is prepared and subsequently blended with the E/X/Y terpolymer and the optional ethylene-containing polymer. However, in some embodiments the ethylene-containing polymer may be melt blended with the components of the organic acid-modified ionomer during its preparation or prior to blending with the E/X/Y terpolymer. That is, blending with the ethylene-containing polymer and neutralization of the E/W dipolymer and organic acid and may be conducted simultaneously in a single process operation.
In other embodiments the modified ionomer combination of (1) and (2) may be prepared, melt blended with the ethylene-containing polymer and then melt blended with the ethylene acid terpolymer. For example, a salt-and-pepper blend of the organic acid-modified ionomer and the ethylene-containing polymer may be heated above their melting temperatures and mixed or the components may be melt-blended in an extruder. The resulting composition may be collected, for example as pellets, and subsequently blended with the E/X/Y terpolymer.
In other embodiments the organic acid-modified ionomer may be prepared and melt blended with the ethylene-containing polymer and the ethylene acid terpolymer at the same time, that is, in a single process operation. A salt-and-pepper blend of the organic acid-modified ionomer, the ethylene-containing polymer and the ethylene acid terpolymer may be heated above their melting temperatures and mixed or the components may be melt-blended in an extruder, either after pre-blending a pellet blend or by feeding the components to the extruder in metered amounts.
When blending polymeric resins the higher flow or lower viscosity resin tends to flow more readily relative to other lower flow resins. This melt rheology effect tends to facilitate the higher flow resin to disperse and distribute more effectively in the blend during the melt blending process and enable more effective distribution at the interface with higher melt shear field. Depending on the blending and extrusion conditions, the ethylene-containing polymer and the E/X/Y terpolymer components may be concentrated near the surface of the extrudate, providing improved adhesion to the substrate.
The composition may additionally comprise from 0.01 to 15, 0.01 to 10, or 0.01 to 5, weight %, based on the total composition weight, of additives including plasticizers, stabilizers including viscosity stabilizers and hydrolytic stabilizers, primary and secondary antioxidants, ultraviolet ray absorbers, anti-static agents, dyes, pigments or other coloring agents, inorganic fillers, fire-retardants, lubricants, reinforcing agents such as glass fiber and flakes, synthetic (for example, aramid) fiber or pulp, foaming or blowing agents, processing aids, slip additives, antiblock agents such as silica or talc, release agents, tackifying resins, or combinations of two or more thereof. These additives are described in the Kirk Othmer Encyclopedia of Chemical Technology.
The additives may be incorporated into the composition by any known process such as by dry blending, extruding a mixture of the various constituents, the conventional masterbatch technique, or the like.
The composition can further comprise a fire retardant such as a chemical additive including, but not limited to, phosphorous compounds, antimony oxides, and halogen compounds, particularly bromine compounds, and others well known in the art. A loading of such additives can be between 20 to 30, or about 25% (of the final air-dried composition or air-dried film weight).
The composition may also comprise fillers, fibers, or pulps in added quantities that may be up to 30 to 40 weight % of the total composition. These materials may provide reinforcement or otherwise modify the mechanical properties of the composition, without negatively impacting the selective permeability of the composition. Fillers include, for example, inorganic materials such as carbon black, TiO₂, calcium carbonate (CaCO₃). Fibers, including chopped fibers, include glass fibers, aramid fibers, carbon fibers and the like. Pulps include, for example aramid micropulps (micropulp has a volume average length from about 0.01 to about 100 micro-meters).
The melt blending steps described above provide a selectively permeable composition that is subsequently applied to a substrate.
In the method, the composition is applied to a substrate in molten condition by, for example but not limitation, extrusion coating to a substrate or lamination of two substrate layers by means of an inner layer of the composition applied in molten form to adhere the substrates together. Generally, the substrate and a layer of the third composition may be arranged in overlaying or overlapping fashion to provide a protective structure. When used with a substrate, the selectively permeable composition may have a thickness from about 10 to about 250 μm.
Extrusion coating the selectively permeable composition onto a substrate can be done as follows: dried granulates or pellets of the blend components fed into a single or double screw extruder, either as a salt-and-pepper blend or from separate feeders and melt blended in the extruder. The components may be melt blended prior to the extrusion coating operation. The molten polymer composition is passed through a slot die to form a molten polymer curtain. The molten curtain drops onto the moving substrate to be immediately pressed onto that substrate and cooled by a quench drum or between a chill roll and a nip roll.
Extrusion lamination is similar, except the molten curtain of selectively permeable composition is dropped between two layers of substrate and then cooled. The result is a structure wherein a layer of selectively permeable composition is positioned between two layers of substrate. In extrusion lamination, the two substrate layers may be the same or different for sandwich structures described below.
In some embodiments the polymer composition can be coated directly on a substrate utilizing fabric impregnation and coating techniques. For example, the selectively permeable composition is a coating applied directly on the substrate (via extrusion coating, spraying, painting or other appropriate application methods). Such coating can be applied using spreading methods known in the art such as with a rubber doctor blade or with a slit extrusion machine.
The composition can be applied to one side or both sides of a textile substrate. In the case where the substrate is coated or laminated on one side, the composition may be applied to the side that is directly exposed to the environment to provide a liquid-impermeable outer surface. Alternatively, in applications where mechanical wear or abrasion is likely, the composition may be applied to the side of the textile substrate opposite the side exposed to the mechanical wear to afford protection of the polymeric composition.
In other embodiments the composition can be impregnated in a substrate or the substrate can be impregnated in the polymer.
The selectively permeable composition may be formed at least partially in the substrate by impregnating the substrate with the composition by applying the molten composition to the substrate and then cooling the composition while it is in contact with the pores of the substrate.
The composition can be dispersed throughout the substrate such as a loosely woven fabric where the composition fills gaps in the substrate and does not just adhere on the surface of a substrate. The substrate can be impregnated inside the selectively permeable membrane through lamination or coextrusion process to have the permeable compositions on both sides of the substrate.
The composition can also be accommodated between two layers of textiles in a sandwich-like manner. Several layer assemblies can also be assembled one above the other. For example, the configuration can comprise the selectively permeable membrane layer, a substrate layer, another selectively permeable membrane layer, another substrate layer, and so on, depending upon desired applications of the protective structure. Other configurations can comprise variations of the aforementioned sandwich configuration, including a plurality of selectively permeable membrane layers, a plurality of substrate layers, and so forth, including mixtures thereof.
The substrate may be any material providing support, shape, esthetic effect, protection, surface texture, bulk volume, weight, or combinations of two or more thereof to enhance the functionality and handability of the structure.
A substrate can be a vehicle to aid in incorporating the selectively permeable composition or provide mechanical support for the membrane so that permeability is not hindered. Preferably a substrate has water vapor diffusion that is greater than the water vapor diffusion of the selectively permeable membrane so that the water vapor diffusion characteristics of the structure are essentially provided by the selectively permeable composition. That is, the substrate does not substantially affect the passage of water vapor through the layered structure, and for example, may have a measured MVTR of at least 1.8, 4, 5, or even 10, Kg/m²/24 hours.
Any support or substrate meeting these desired characteristics may be used with the selectively permeable composition. Examples include a textile or porous sheet material. Sheets made from synthetic fiber spun fabrics, such as nonwoven textiles, may be used as a textile substrate. Cloth that is woven, knitted or the like is also suitable as a textile substrate. A fabric may comprise flame retardant(s), filler(s), or additive(s) disclosed above.
For example, a fabric may comprise a 50% nylon-50% cotton blend woven fabric (also known as NYCO) such as those by Bradford Dyeing Association, Inc., in Bradford, R.I. A fabric of note is a polyester woven fabric from Millikin and Company (Spartanburg, S.C.).
A textile may also include nonwoven textiles prepared from polypropylene, polyethene, polyesters such as polyethylene terephthalate or mixtures thereof, and other spun bonded polymer fabrics.
While the substrate has been described generally as a textile, the substrate can be any other material that is capable of accommodating thereon one or a plurality of layers or accommodating therein a dispersion of the selectively permeable composition.
Cellulosic materials such as paper webs (for example Kraft or rice paper), materials made from synthetic fiber spun fabrics, microporous films, or even perforated films having large percentages of open areas such as perforated PE films, may be used as materials for the substrate(s), for example. These materials may be reinforced with fibers. Microporous films of note may be prepared from polypropylene, polyethylene or combinations thereof. They may be monolayer or multilayer films (for example, three-layer films comprising an inner layer of polypropylene between two outer layers of polyethylene). Microporous films are available from Celgard, LLC, Charlotte, N.C. under the CELGARD tradename.
Suitable polymers for the a microporous film are (1) linear ultrahigh molecular weight polyethylene having an intrinsic viscosity of at least 18, preferably 18 to 39, deciliters/gram, (2) linear ultrahigh molecular weight polypropylene having an intrinsic viscosity of at least 6 deciliters/gram, and (3) mixtures of (1) and (2).
The microporous film may include a finely divided, particulate, substantially water-insoluble, inorganic filler, for example a siliceous filler, which is distributed throughout the matrix and which is present in amount 50 to 90%, particularly 50 to 85%, by weight of the film. The filler may be silica, precipitated silica, or silica having an average ultimate particle size of less than 0.1 μm and may occupy 35 to 80% of the total volume of microporous film. Because they have a relatively narrow range of pore sizes, films may be made by extruding a polymeric composition which contains an inorganic filler and a processing oil, e.g. a paraffinic oil, naphthenic oil or aromatic oil, uniformly distributed therein; followed by extraction of the processing oil, e.g. with trichloroethylene. Some films are disclosed, for example, in U.S. Pat. Nos. 4,937,115 and 3,351,495 and films are sold by PPG Industries under the tradename TESLIN.
Specific examples of porous or perforated films include a porous PE film having a porosity of about 55% and a pore size of about 0.25 microns, available under the tradename CELGARD K878 from Hoechst Celanese Corp; a porous PE film available under the tradename MSX 1137P from 3M Co.; and a filled porous PE film available under the designation Van Leer 10× from Van Leer Corp. TESLIN SP7 is a filled porous PE films containing about 60% silica, having a thickness of about 0.18 mm (0.007 inch), a tear strength measured as described above of about 90 g, a porosity of about 65%, an average pore size of about 0.1 micron and a largest pore size of 4 to 10 microns. TESLIN X457 is similar to TESLIN SP7 but is more porous. TESLIN SP10 is similar to TESLIN SP7 but has a thickness of about 0.25 mm (0.010 inch). All three TESLIN films are available from PPG Industries. A perforated high density polyethylene film, 0.11 mm (4.5 mil) thick, with an open area of about 36%, is available under the tradename DELNET from Applied Extrusion Technologies.
A substrate can be a porous sheet material comprising a fluoropolymer. A substrate can be sheet material made with expanded polytetrafluoroethylene that is available from many companies, including W. L. Gore & Associates of Wilmington, Del. Other porous substrates include porous or microporous polyurethane films, filter materials from companies such as Millipore, nano- or micro-fiber structures, natural or synthetic fibers, other related supports that add dimensional stability, or combinations of two or more thereof.
The method provides structures comprising the selectively permeable composition and a substrate.
The composition can be used in protective garments and structures, such as drapes, shelters, tents, and other coverings for personnel or objects, where it functions as a biological and/or chemical barrier. The protective structures can also be in the form of, for example, tarpaulins, covers, and the like. The polymer composition can be present as a layer of material added to the protective garments or structure, or as one component of a fabric incorporated into the protective garment or structure.
Coated fabrics, used previously as tarpaulins or other covers, may have at least one wear resistant outer layer that generally needs high flexibility, high resistance to marring from wear, abrasion, scuffing, and scratching, high mechanical strength and toughness. Coating compositions preferably exhibit good adhesion to fabrics and other substrates such as plastic films and cellulosic materials such as paper or paperboard. They also desirably exhibit good melt processability, good colorability, good printability, and high transparency and/or gloss. Previous coating compositions for these applications include plasticized or flexible polyvinyl chloride. The composition described herein provides a superior coating composition to previous coating materials because it is selectively permeable.
The protective structure may further comprise other layers such as adhesive layers, thermal insulation layers, cushioning layers, absorptive layers, reactive layers, and the like.
Insulation layers and cushioning layers may comprise an organic thermoplastic fiber-based material comprising, e.g., polyester, polyethylene or polypropylene. For example, the thermal insulating or cushioning layer is a fiberfill batt comprising polyester. A fiberfill batt sold as THERMOLITE ACTIVE ORIGINAL by DuPont is suitable. Alternatively, the thermal insulating layer may comprise melt-blown fibers, such as melt-blown polyolefins, sold as THINSULATE, by 3M. They may also include other materials such as fiberglass batts.
The mechanical properties and ease of processing of the selectively permeable composition, and its ability to transport water vapor and block liquids, optionally combined with a support substrate render protective structures thereof applicable for covering or enclosing articles during transport and storage. The structure so made is also referred to as selectively permeable membrane or structure. The mechanical properties and ease of processing of the selectively permeable structure, and its ability to transport water and block organic molecules, combined with a support substrate render protective structures thereof applicable for various applications, such as, for example, chemical and/or biological protective clothing for health care or military applications. Examples include chemical and/or biological protective apparel comprising any of the aforementioned various embodiments of the selectively permeable protective structure. A biological barrier is any structure that provides resistance to harmful or undesirable biological agents such as bacteria, microbes, viruses and the like that, for example, may be present in blood, sera, and other bodily fluids or may be present as aerosols.
The protective structure can be used in protective garments such as for health care applications including gowns and other apparel for operating room, patient visitor, medical, dental, and similar applications. The apparel can be selected, for example, from the group consisting of gowns, aprons, shirts, trousers, overcoats, gloves, shoes, boots, overboots, socks, hoods, hats, caps, masks, and eye goggles. Other health care equipment can be selected, for example, from the group consisting of screens, drapes, and breathable dressings.
Protective garments may also be used in military, food preparation, transportation, industrial and manufacturing procedures other applications that require protection from biological and/or chemical agents, heat, irritants and the like. The unique properties of the selectively permeable structure are useful for applications including protective clothing for “first responders” in chemical threat situations, or for hazardous materials handling. In addition to apparel listed above for health care applications, protective apparel may also include helmets and gas masks.
The selectively permeable protective structure may also be suitable for fabrics used in responding to biological and/or chemical spills. It may be used for fabrics for tents, awnings and other shelters. These uses may be protective, since they block transmission of the agent from one place to another.
Other uses for the selectively permeable structure include covering objects during transportation and storage to provide protection from liquid water while allowing water vapor to permeate out of the enclosed space, preventing a buildup of moisture inside the enclosed space, thereby reducing the possibility of corrosion, mold growth and other deleterious effects resulting from excess moisture. Articles for this use include (1) films or sheets of material comprising the selectively permeable structure that may be wrapped around or draped over the object(s) being packaged such as tarpaulins, pallet wrapping films and the like; (2) bags, pouches, hoods or sheathes comprised completely of the selectively permeable structure described herein or which comprise other materials such as other polymeric materials, woven or nonwoven textiles and the like and have windows, patches or areas thereon which comprise the selectively permeable structure, including heat shrinkable hoods and pallet stretch hoods; (3) rigid or semi-rigid or flexible structures such as tubs, boxes, bins and the like, comprised completely of the selectively permeable structure or comprised in part of other materials having one or more windows of the variably permeable multilayer structure thereon; (4) lidding material comprised completely of the selectively permeable structure or comprised in part of other materials having one or more windows of the selectively permeable structure thereon. The lidding material may be used in combination with rigid or semi-rigid or flexible structures such as tubs, boxes, bins and the like to prepare a package comprising the selectively permeable structure; (5) patches of the selectively permeable structure over designed openings of packages to provide the desired permeability; and (6) packages in which the selectively permeable structure is covered by a removable protective cover that allows a user to expose the selectively permeable structure to the environment at an appropriate time.
The following Examples are presented to demonstrate and illustrate, but are not meant to unduly limit the scope of, the invention.

Examples

MI, the mass rate of flow of a polymer through a specified capillary under controlled conditions of temperature and pressure, was determined according to ASTM 1238 at 190° C. using a 2160 g weight, in g/10 minutes.
For samples with high water permeability (>100 g/m²-24 h), the water vapor transmission tests were conducted on a Mocon PERMATRAN-W 101K, following ASTM D6701-01, at 37.8° C. at 100% relative humidity. For the other samples, the transmission tests were conducted on a Mocon PERMATRAN-W 700, following ASTM F1249-01. Moisture vapor permeation values (MVPV) on film samples are reported in g-mil/m²-24 h while MVTR are reported in g/m²-24 h. The compositions had MVPV of at least 800 (or at least 1200) g-mil/m²/24 h.
Another method for determining material “breathability,” or evaporative resistance, uses a Guarded Sweating Hotplate Test according to ASTM F1868, ISO 11092.

Moisture Vapor Transmission Rate (MVTR) of Multilayer Structure

This is measured by a method derived from the Inverted Cup method of MVTR measurement [ASTM E 96 Procedure BW, Standard Test Methods for Water Vapor Transmission of Fabrics (ASTM 1999)]. A vessel with an opening on top is charged with water and the opening is covered first with a moisture vapor permeable (liquid impermeable) layer of expanded-PTFE film (“ePTFE”), and then with the sample for which the MVTR is to be measured, and finally by woven fabric overlayer [NYCO 50:50 nylon/cotton blend, 6.7 oz/yd²(0.23 kg/m²) treated with durable water repellant finish]. The three layers are sealed in place, inverted for 30 minutes to condition the layers, weighed to the nearest 0.001 g, and then contacted with a dry stream of nitrogen while inverted. After 19 h at 23° C., the sample is reweighed and the MVTR calculated (kg/m²·24 h) by means of the following equation:
MVTR=1/[(1/MVTR_obs)−(1/MVTR_mb)]
where MVTR_obsis the observed MVTR of the experiment and MVTR_mbis the MVTR of the ePTFE moisture barrier (measured separately). The values are the average of results from three replicate samples.
In order to illustrate the moisture permeance associated with a film layer involving a selectively permeable composition as described herein, extrusion cast films were prepared from the materials listed below. The selectively permeable composition was also extrusion coated onto substrates to illustrate its adhesion to the substrates.
Thermoplastic compositions are polymeric materials that can flow when heated under pressure. Melt index (MI) is the mass rate of flow of a polymer through a specified capillary under controlled conditions of temperature and pressure. Melt indices reported herein are determined according to ASTM 1238 at 190° C. using a 2160 g weight, with values of MI reported in grams/10 minutes.

Materials Used

EAC-1: an ethylene/methacrylic acid dipolymer with 19 weight % of methacrylic acid, having MI of 395 g/10 min.
EAC-2: a terpolymer comprising ethylene, n-butyl acrylate (28 weight %) and acrylic acid (6.2 weight %), having MI of 200 g/10 min.
EAC-3: a terpolymer of ethylene, n-butyl acrylate (23.5 weight %) and methacrylic acid (9 weight %), having an MI of 200 g/10 min.
EAC-5: a terpolymer of ethylene, n-butyl acrylate (15.5 weight %) and acrylic acid (8.5 weight %), having an MI of 60 g/10 min.
EAC-6: a terpolymer of ethylene, n-butyl acrylate (15.5 weight %) and acrylic acid (10.5 weight %), having an MI of 60 g/10 min.
ABA: A mixture containing 90 weight % of a mixture of arachidic acid and behenic acid with 6 weight % C₁₈acids and 4 weight % other acids commercially available under the tradename HYSTRENE® 9022 from Chemtura.
EMA-1: An ethylene/methyl acrylate copolymer with 24 weight % methyl acrylate with MI of 20 g/10 min.
EBA-1: An ethylene/butyl acrylate copolymer with 35 weight % butyl acrylate, having melt index of 40 g/10 min.
EBA-2: An ethylene/butyl acrylate copolymer with 27 weight % butyl acrylate, having melt index of 4 g/10 min.
Mod-1: a blend of EAC-2 and 5 weight % ABA wherein 93% of the combined carboxylic acid groups in the terpolymer and the ABA were neutralized to potassium salts.
EMA-2: An ethylene/methyl acrylate copolymer with 20 weight % methyl acrylate with MI of 8 g/10 min.
Ionomer I-1: a terpolymer comprising ethylene, n-butyl acrylate (23.5 weight %) and methacrylic acid (9 weight percent), neutralized to 52% with sodium using sodium hydroxide, with MI of 1.
Employing a Werner & Pfleiderer twin-screw extruder, a mixture of EAC-1 and ABA was neutralized to 93-95% with a masterbatch of potassium hydroxide in EMA-1 to a neutralization level of 93-95% to provide Composition A. The weight ratios of the polymeric materials are summarized in Table 1. A portion of Composition A was further neutralized with neat potassium hydroxide to provide Composition B.

	TABLE 1

	Parts by weight	% Nominal

	EAC-1	ABA	EMA-1	Neutralization

Composition A	73.2	18.4	8.4	93-95
Composition B	73.2	18.4	8.4	106

Composition A was extrusion coated at 0.8 mil thickness onto polypropylene nonwoven textile (PP NW) and 50-pound Kraft paper substrate sheets using an Egan extrusion coating machine equipped with a matte-surface chill roll, an Edlon®/Teflon®-covered pressure roll, corona treater and a Cloeren EBR 40-inch die. The substrates were corona treated at 3 KW/ft². The machine settings included a 6 inches air gap and 80 psi nip roll pressure. Adhesion was tested by T-peel test according to ASTM2234-95. The adhesion peel strength between the coating and the substrate are summarized in Table 2. In the Tables, the abbreviations indicate as follows: “p”=peels, “d”=delaminates, “ft”=fiber tear, “fp”=fiber peel and “t”=tears. These runs show low adhesion of Composition A to the nonwoven textile under the conditions indicated.

TABLE 2

	Extrusion			Adhesion
	Temp		Chill roll	peel
Substrate	(° C.)	Feet/min	Temp (° C.)	strength	Comments

PP NW	375	235	69	7 g/in	p
Kraft	375	235	69	115 g/in	p
PP NW	375	400	71	10 g/in	p
Kraft	375	400	71	203 g/in	fp
PP NW	400	235	73	8 g/in	p
Kraft	400	235	73	230 g/in	fp
PP NW	400	400	76	9 g/in	p
Kraft	400	400	76	316 g/in	fp, ft

Composition A was blended with 30 weight % of EMA-2 and then extrusion coated at 375° F. and 0.8 mil thickness onto polypropylene nonwoven textile (PP NW) and 24-pound Kraft paper substrate sheets, using similar conditions as those above. These runs show low adhesion of Composition A modified with an ethylene/methyl acrylate copolymer to the nonwoven textile under the conditions indicated.

TABLE 3

	Extrusion		Adhesion Peel
Substrate	Temp (° C.)	Feet/min	strength (g/in)	Comments

PP NW	370	235	10	p
Kraft	370	235	178	fp, p
PP NW	370	400	7	p
Kraft	370	400	137	fp, p

Similarly, Composition A was melt blended with the polyethylenes listed and EAC-2 to provide compositions containing 35 weight % of Composition A, 10 weight % of EAC-2 and 55 weight % of polyethylene; 30 weight % of Composition A, 15 weight % of EAC-2 and 55 weight % of polyethylene; 30 weight % of Composition A, 15 weight % of EAC-2 and 50 weight % of polyethylene; 40 weight % of Composition A, 10 weight % of EAC-2 and 50 weight % of polyethylene; or 45 weight % of Composition A, 10 weight % of EAC-2 and 45 weight % of polyethylene.
In order to assess adhesion of compositions wherein Composition A or B were modified with various polymers, the following tests were performed. Using a Werner & Pfleiderer twin-screw extruder, the Compositions A and B were melt blended with additional materials to provide the compositions summarized in Table 4. The compositions in Table 4 were processed into 2-mil-thick cast films.
For the film samples, water vapor permeation tests were conducted on a Mocon Permatran-W® 101K, following ASTM D6701-01, at 37.8° C. Water vapor permeation values (WVPV) on film samples are reported in g-mil/m²-24 h while moisture vapor transmission rates (MVTR) are reported g/m²-24 h.

	TABLE 4

	Weight %	WVTR

Example	Composition A	Composition B	EBA-1	EAC-2	Mod-1	I-1	mil-g/M₂-day

C1	100	0	0	0	0	0	12721
2	90	0	10	0	0	0	10193
3	80	0	20	0	0	0	2910
4	70	0	30	0	0	0	1376
5	90	0	5	5	0	0	7934
6	80	0	10	10	0	0	6666
7	70	0	15	15	0	0	2657
8	90	0	0	10	0	0	6663
9	80	0	0	20	0	0	4019
10	70	0	0	30	0	0	1558
C11	0	100	0	0	0	0	13102
12	0	90	0	10	0	0	8793
13	0	80	0	20	0	0	4445
14	0	70	0	30	0	0	2102
15	0	90	0	0	10	0	8602
16	0	80	0	0	20	0	5947
17	0	70	0	0	30	0	4685
18	0	90	0	0	0	10	8464
19	0	80	0	0	0	20	6507
20	0	70	0	0	0	30	4446

The physical properties of some of the films are summarized in Table 5. To assess adhesion of the compositions to a polypropylene nonwoven textile substrate, the films were heat sealed between two layers of substrate at 325° F. at 40 psi for 1.0 sec to provide a 3-layer structure of PP nonwoven/film/PP nonwoven.

TABLE 5

Tensile modulus,	Elmendorf Tear,	Tensile strength,	Elongation at break,
psi	g/mil	psi	%

Example

MD

TD

ave

MD

TD

ave

MD

TD

ave

MD

TD

ave

C1	25400	18300	21850	9.07	20.6	14.84	1600	1100	1350	290	149	220
2	21200	17600	19400	10	24.5	17.25	1730	1140	1435	451	321	386
3	19700	18000	18850	12.62	22.13	17.38	1550	880	1215	483	247	365
4	15700	Film tear	NA	1.77	4.38	3.08	1300	Film tear	NA	435	NA	NA
5	20800	20100	20450	16.57	26.34	21.46	1570	1330	1450	388	386	387
6	16400	15100	15750	22.39	53.4	37.90	1760	1220	1490	539	414	476
7	13700	11100	12400	40.51	77	58.76	1600	1050	1325	534	386	460
8	19600	18900	19250	20.5	21.42	20.96	1790	1370	1580	487	376	432
9	16800	14900	15850	54.05	73.89	63.97	1820	1630	1725	542	518	530
10	13200	14400	13800	95.65	154.83	125.24	1790	1452	1621	560	507	534

The adhesion was tested by the T-peel test and reported in Table 6.

TABLE 6

T-peel Strength

lbf/in

gm/in

		Standard		Standard
Example	Average	deviation	Average	deviation

C1	1.267	0.691	652	314
2	1.544	0.708	799	321
3	0.823	0.432	427	196
4	1.229	0.423	633	192
5	1.436	0.758	708	344
6	1.812	0.662	928	301
7	1.528	0.579	787	263
8	2.048	0.573	1023	260
9	1.534	0.37	756	168
10	1.433	0.394	725	179
C11	1.12	0.235	508	107
12	1.835	0.27	832	122
13	1.789	0.057	811	26
14	1.283	0.071	582	32
15	0.769	0.173	349	78
16	0.996	0.456	452	207
17	1.29	0.553	585	251
18	1.085	0.284	492	129
19	0.889	0.317	403	144
20	1.003	0.31	455	141

Compositions modified with EAC-2, an ethylene/acrylic acid/n-butyl acrylate terpolymer, showed better adhesion to PP nonwoven in these tests compared to unmodified compositions or compositions modified with ethylene/alkyl acrylate dipolymers. Compositions in which the ethylene/acrylic acid/n-butyl acrylate terpolymer was in the form of an ionomer prior to blending did not exhibit improved adhesion (Examples 15-20).
Compositions were prepared as summarized in Table 7 and were extrusion coated onto polypropylene nonwoven textile (PP NW), polyethylene/polyethylene terephthalate nonwoven textile (PE/PET NW) and 50-pound Kraft paper sheets at around 200 feet/minute, using an similar conditions as those described above.

TABLE 7

Example	Composition A	EBA-2	EMA-1	EAC-2

21	70	30	0	0
22	70	0	30	0
23	90	0	0	10

The extrusion-coating runs are summarized in Table 8.

TABLE 8

				Extrusion	Corona
		Thickness		Temperature	Treatment	Chill roll
Example	Composition	(mil)	Substrate	(° C.)	(Kw/ft²)	(° C.)

24	Example 21	0.8	PP NW	400	3	74
25	Example 21	0.8	Kraft	400	3	74
26	Example 21	1.0	PP NW	420	6	80
27	Example 21	1.0	Kraft	420	6	80
28	Example 21	1.0	PE/PET NW	420	6	86
29	Example 21	1.0	Kraft	420	6	86
30	Example 22	1.0	PP NW	420	6	95
31	Example 22	1.0	Kraft	420	6	95
32	Example 23	1.0	PP NW	420	6	77
33	Example 23	1.0	Kraft	420	6	77
34	Example 23	1.0	PE/PET NW	415	4	101
35	Example 23	1.0	PE/PET NW	415	4	101
36	Example 23	1.0	PP NW	450	4	111
37	Example 23	1.0	Kraft	450	4	111

For the runs in which the substrate was a polypropylene nonwoven, WVTR was measured on the coating after peeling it from the substrate. For the runs in which the substrate was Kraft paper or PE/PET nonwoven, WVTR was measured on the entire 2-layer structure.

TABLE 9

	Adhesion peel
Example	strength (g/inch)	Comments	WVTR¹

24	0.1	p	1938
25	62	p	1063
26	0.3	p	2479
27	13	p	856
28	0.5	p	NA
29	124	p, fp	627
30	29	p, t	1889
31	79	p, fp	1175
32	0.7	p	3760
33	208	fp	1140
34	473	(p, d, fp, t)²	3774
35	633	(p, fp)³
36	17	p	3301
37	78	p, d	1652

¹In g/[m²-day].
²Inside of roll.
³Outside of roll.

Composition A modified with 10 wt % EAC-2, an ethylene acrylic acid n-butyl acrylate terpolymer, showed good adhesion to Kraft paper and excellent adhesion to PE/PET NW. These results are superior to those obtained when Composition A was modified with 30 weight % EBA-1, an ethylene/n-butyl acrylate dipolymer. The composition containing EAC-2 also had higher WVTR, showing it retained more moisture permeability from Composition A.

Claims

1. A method for preparing a selectively permeable multilayer structure or article comprising:

(1) preparing a first composition comprising

(i) one or more ethylene acid copolymers; and

(ii) one or more organic acids; wherein at least 50% of the combined acidic groups in the acid copolymer and the organic acid are nominally neutralized to salts with metal ions and at least 50% of the metal ions are alkali metal ions;

(2) melt blending the first composition with a terpolymer of ethylene, acrylic acid or methacrylic acid, and an alkyl acrylate or alkyl methacrylate;

and optionally with one or more ethylene-containing polymers selected from the group consisting of polyethylene (PE) homopolymers, copolymers of ethylene and an α-olefin, copolymers of ethylene and a diolefin, and ethylene copolymers obtained from copolymerization of ethylene with at least one polar monomer selected from the group consisting of vinyl acetate, acrylic ester, methacrylic ester and carbon monoxide, wherein the ethylene-containing polymer wherein the ethylene-containing polymer does not comprise a carboxylic acid comonomer, to provide a second composition in a molten condition;

(3) contacting a substrate with the molten second composition to adhere, embed, or impregnate the melted composition to the substrate or adhere, embed, or impregnate the substrate to the molten second composition to provide a coated substrate;

(4) cooling the coated substrate to allow the molten second composition to cool and solidify.

2. The method of claim 1 wherein the substrate comprises textile or porous sheet material.

3. The method of claim 2 wherein the substrate is one or more porous films, flash spun non-woven fabrics, woven fabrics of synthetic fibers, natural fibers or combinations thereof, scrims, or filter materials.

4. The method of claim 3 wherein the substrate is a woven fabric of synthetic fibers, natural fibers or combinations thereof.

5. The method of claim 1 wherein at least 50% of the metal ions are sodium ions.

6. The method of claim 1 wherein at least 50% of the metal ions are potassium ions.

7. The method of claim 1 wherein the ethylene-containing polymer is selected from the group consisting of ethylene copolymers obtained from copolymerization of ethylene with at least one polar monomer selected from the group consisting of vinyl acetate, acrylic ester, methacrylic ester and carbon monoxide.

8. The method of claim 7 wherein the ethylene-containing polymer is an ethylene/alkyl acrylate or ethylene/alkyl methacrylate copolymer.

9. The method of claim 1 wherein the second composition comprises

(a) 30 to 99 weight %, based on the combination of (a), (b) and (c), of a blended combination of

(1) 70 to 90 weight %, based on the combination of (1) and (2), of one or more E/W ethylene acid copolymers or ionomers of the acid copolymers wherein E represents copolymerized units of ethylene, X is present in about 2 to about 35 weight % of the copolymer and represents copolymerized units of at least one C₃to C₈α,β-ethylenically unsaturated carboxylic acid;

(2) 10 to 30 weight %, based on the combination of (1) and (2), of one or more organic acids having from 4 to 36 carbon atoms, or salts thereof; wherein at least 50% of the combined acidic groups in the E/W copolymer and the organic acid are nominally neutralized to salts with metal ions; wherein at least 50% of the metal ions are alkali metal ions;

(b) 1 to 30 weight %, based on the combination of (a), (b) and (c), of E/X/Y ethylene acid terpolymers wherein E represents copolymerized units of ethylene, X is present in about 2 to about 35 weight % of the copolymer and represents copolymerized units of acrylic acid or methacrylic acid, and Y is present in about 1 to about 35 weight % of the copolymer and represents copolymerized units of alkyl acrylate or alkyl methacrylate; and

(c) 0 to 60 weight %, based on the combination of (a), (b) and (c), of one or more second ethylene-containing polymer selected from the group consisting of polyethylene homopolymers, copolymers of ethylene and an α-olefin, copolymers of ethylene and a diolefin, and ethylene copolymers obtained from copolymerization of ethylene with at least one polar monomer selected from the group consisting of vinyl acetate, acrylic ester, methacrylic ester and carbon monoxide, wherein the second ethylene-containing polymer does not comprise a carboxylic acid comonomer; wherein (a), (b) and (c) total 100 weight %.

10. The method of claim 9 wherein the ethylene-containing polymer is selected from the group consisting of ethylene copolymers obtained from copolymerization of ethylene with at least one polar monomer selected from the group consisting of vinyl acetate, acrylic ester, methacrylic ester and carbon monoxide.

11. The method of claim 10 wherein the ethylene-containing polymer is an ethylene/alkyl acrylate or ethylene/alkyl methacrylate copolymer.

12. The method of claim 7 wherein the second composition comprising (a), (b) and optionally (c) has greater adhesion to the substrate than a corresponding composition comprising (a) that does not comprise (b), the other components being identical.

13. The method of claim 1 wherein the second composition has a moisture vapor permeation value of at least 200 g-mil/m²/24 h measured at 37.8° C. and 100% relative humidity according to ASTM F-1249 and high water-entry pressure.

14. The method of claim 1 wherein the selectively permeable structure has a moisture vapor transmission rate of at least 50 g/m²/24 h measured at 37.8° C. and 100% relative humidity according to ASTM F-1249.