Patent Application
20190084284
This invention relates to a method for bonding fabric and a polyolefin elastomer using an aqueous adhesive.
The use of polyolefin resin dispersions in bonding polyolefin elastomers to fabric has been described. For example, JP2002-012812 discloses an aqueous polyolefin dispersion for application of a skin coating on fabrics. However, the prior art does not disclose the one-component adhesive formulation disclosed in the present application.
The problem addressed by the present invention is to provide good bonding of fabrics to elastomeric materials.
The present invention provides a method for bonding a fabric to a polyolefin elastomer; said method comprising applying to the fabric: (a) from 10 to 90 wt % of an aqueous dispersion of a thermoplastic polymer; and (b) from 10 to 90 wt % of an aqueous dispersion of a rosin, wherein percentages are based on total dry weight of thermoplastic polymer and rosin.
Percentages are weight percentages (wt %) and temperatures are in ° C., unless specified otherwise. References to room temperature (RT) or ambient temperature indicate a temperature from 20-25° C.; unless otherwise specified, preparations and testing were performed at ambient temperature. Weight percentages of monomer residues are based on the total weight of monomer residues in the polymer. Weight percentages of polymers and rosins are specified on a dry weight basis.
Preferably, the fabric is a synthetic fabric, i.e., one comprising at least 40 wt % of a synthetic polymer, preferably at least 50 wt %, preferably at least 60 wt %, preferably at least 70 wt %, preferably at least 80 wt %, preferably at least 90 wt %. Preferred synthetic fabrics include those comprising polyimide fibers (e.g., NYLON) or polyester fibers (preferably polyethylene terephthalate (PET)). Preferably, the fabric has a weight from 100 to 500, preferably from 150 to 400, preferably from 200 to 350, grams per square meter (g/m2).
The polyolefin elastomer is a polymer or copolymer comprising at least one non-polar (i.e., containing only carbon and hydrogen) olefin-based polymer. Each at least one non-polar olefin-based polymer comprises at least 50 wt % polymerized units of olefinic monomers and no polar component (i.e., units of monomers containing elements other than carbon and hydrogen). Preferably, the non-polar olefin-based polymer comprises a propylene/alpha-olefin copolymer, preferably a propylene/ethylene copolymer, and at least one of (i) a styrenic block copolymer, (ii) a homogeneously branched ethylene/alpha-olefin copolymer, (iii) an olefin block copolymer, and (iv) a random polypropylene copolymer. Preferably, the middle foam layer comprises a propylene/alpha-olefin copolymer and at least two, three or all four of components (i)-(iv). The at least one non-polar olefin-based polymer can comprise a single propylene/alpha-olefin copolymer or a blend of two or more propylene/alpha-olefin copolymers. Likewise, each of the (i) a styrenic block copolymer, (ii) a homogeneously branched ethylene/alpha-olefin copolymer, (iii) an olefin block copolymer, and (iv) a random polypropylene copolymer can be present neat or as a blend of two or more copolymers. The at least one non-polar olefin-based polymer can also comprise one or more optional additives such as processing aids, extenders, blocking agents, pigments and/or dyes, antioxidants, UV-stabilizers and/or absorbers, flame retardants, fillers (such as talc, calcium carbonate), and the like.
Preferably, the at least one non-polar olefin-based polymer comprises at least 30, preferably at least 40, preferably at least 50, weight percent (wt %) propylene/alpha-olefin copolymer. The maximum amount of propylene/alpha-olefin copolymer in the at least one polar olefin-based polymer preferably does not exceed 90, preferably does not exceed 80, preferably does not exceed 70, wt %. The middle foam layer can be compositionally the same as the top skin layer with the exception of the gas and by-products attributable to the foaming process.
The total amount of (i) styrenic block copolymer, (ii) homogeneously branched, linear ethylene/alpha-olefin copolymer, (iii) olefin block copolymer, and (iv) random polypropylene copolymer in the at least one polar olefin-based polymer preferably is at least 10, preferably at least 20, preferably at least 30, wt %. The maximum total amount of (i) styrenic block copolymer, (ii) homogeneously branched ethylene/alpha-olefin copolymer, (iii) olefin block copolymer, and (iv) random polypropylene copolymer in the middle foam layer preferably does not exceed 70, preferably does not exceed 60, preferably does not exceed 50, wt %.
The propylene/alpha-olefin copolymer preferably is characterized as having substantially isotactic propylene sequences. “Substantially isotactic propylene sequences” means that the sequences have an isotactic triad (mm) measured by 13C NMR of greater than 0.85; preferably greater than 0.90; preferably greater than 0.92; preferably greater than 0.93. Isotactic triads are well-known in the art and are described in, for example, U.S. Pat. No. 5,504,172 and International Publication No. WO 00/01745, which refers to the isotactic sequence in terms of a triad unit in the copolymer molecular chain determined by 13C NMR spectra.
The propylene/alpha-olefin copolymer preferably has a melt flow rate (MFR) in the range of from 0.1 to 25 g/10 minutes, measured in accordance with ASTM D-1238 (at 230° C./2.16 Kg). All individual values and sub-ranges from 0.1 to 25 g/10 minutes are included and disclosed by this range; for example, the MFR can be from a lower limit of 0.1 g/10 minutes, 0.2 g/10 minutes, or 0.5 g/10 minutes to an upper limit of 25 g/10 minutes, 15 g/10 minutes, 10 g/10 minutes, 8 g/10 minutes, or 5 g/10 minutes. For example, the propylene/alpha-olefin copolymer may have a MFR in the range of 0.1 to 10 g/10 minutes; or the propylene/alpha-olefin copolymer may have a MFR in the range of 0.2 to 10 g/10 minutes. In a preferred embodiment, the propylene/alpha-olefin is a propylene/ethylene copolymer.
Preferably, the propylene/alpha-olefin copolymer has a density from 0.85 to 0.89 g/cc. All individual values and sub-ranges from 0.85 to 0.89 g/cc are included and disclosed herein; for example, the density can be from a lower limit of 0.85, 0.86, 0.87 or 0.88 g/cc to an upper limit of 0.855, 0.865, 0.875, 0.885 or 0.89 g/cc. For example, the density can be from 0.85 to 0.89 g/cc, or in the alternative, from 0.85 to 0.87 g/cc, or in the alternative, from 0.87 to 0.89 g/cc, or in the alternative, from 0.86 to 0.888 g/cc. Preferably, the propylene/alpha-olefin is a propylene/ethylene copolymer.
The propylene/alpha-olefin copolymer comprises units derived from propylene and one or more alpha-olefin comonomers. Exemplary comonomers utilized to manufacture the propylene/alpha-olefin copolymer are C2 to C10 alpha-olefins; for example, C2, C4, C6 and C8 alpha-olefins. The propylene/alpha-olefin copolymer comprises from 1 to 30 wt % of one or more units derived from one or more alpha-olefin comonomers.
The propylene/alpha-olefin copolymer has a molecular weight distribution (MWD), defined as weight average molecular weight divided by number average molecular weight (Mw/Mn) of 3.5 or less; or 3.0 or less; or from 1.8 to 3.0. In a further embodiment, the propylene/alpha-olefin is a propylene/ethylene copolymer. Such propylene/alpha-olefin copolymers are further described in the U.S. Pat. Nos. 6,960,635 and 6,525,157. Such propylene/alpha-olefin copolymers are commercially available from The Dow Chemical Company, under the trade name VERSIFY, or from ExxonMobil Chemical Company, under the trade name VISTAMAXX.
Preferably, the thermoplastic polymer in component (a) above is a homopolymer or copolymer of C2-C8 (preferably C2-C4) aliphatic alpha-olefins such as ethylene, propylene, 1-butene, etc., or their combination; a functionalized (maleic anhydride and/or carboxylic acid) homopolymer or copolymer of alpha-olefins; a copolymer of C2-C8 (preferably C2-C4) aliphatic alpha-olefins with styrene; a polyurethane; an epoxy, or their combination. As used herein, the term anhydride and/or carboxylic acid functionalized, olefin-based polymer refers to an olefin-based polymer into, or onto, which maleic anhydride and/or carboxylic acid functional groups are grafted. Grafting reactions, are described for example in U.S. Pat. Nos. 8,450,430 and 7,763,692. Alternatively, the functional group may be present in a copolymer (i.e., carboxylic acid functional group) which is copolymerized with the olefin monomers to form the olefin based polymer. Especially preferred thermoplastic polymers include, e.g., styrene-ethylene-butene-styrene (SEBS) block copolymer (preferably with a styrene content no greater than 35 wt %) and maleic anhydride-modified ethylene-vinyl acetate (EVA) copolymer. Preferably, the Mw of the thermoplastic polymer is from 20,000 to 100,000; preferably at least 25,000, preferably at least 30,000; preferably no more than 85,000, preferably no more than 70,000.
Preferably, the thermoplastic polymer is a styrene ethylene butene styrene (SEBS) block copolymer with a styrene content of equal to or less than 35 wt %, and preferably a Young's modulus of equal to or less than 10 MPa. All individual values and sub-ranges from equal to or less than 10 MPa are included and disclosed herein; for example, the Young's modulus of the thermoplastic elastomer can be equal to or less than 10 MPa, or in the alternative, equal to or less than 9 MPa, or in the alternative, equal to or less than 8 MPa, or in the alternative, equal to or less than 6 MPa, or in the alternative, equal to or less than 4 MPa. In a preferred embodiment, the Young's modulus of the thermoplastic polymer is no less than 0.5 MPa. All individual values and sub-ranges of a styrene content equal to or less than 35% by weight are included and disclosed herein. For example, the styrene content can be from an upper limit of 35 wt %, or in the alternative, 30 wt %, or in the alternative, 25 wt %. Preferably, polystyrene-saturated polybutadiene-polystyrene and polystyrene-saturated polyisoprene-polystyrene block copolymers comprise polystyrene end-blocks having a number average molecular weight from 5,000 to 35,000 and saturated polybutadiene or saturated polyisoprene mid-blocks having a number average molecular weight from 20,000 to 170,000. The saturated polybutadiene blocks preferably have from 35-55% 1,2-configuration and the saturated polyisoprene blocks preferably have greater than 85% 1,4-configuration. The total number average molecular weight of the styrenic block copolymer is preferably from 30,000 to 250,000 if the copolymer has a linear structure. Such block copolymers preferably have an average polystyrene content from 10% by weight to 30%, preferably from 10% by weight to 20% by weight.
Preferably the aqueous dispersion of the thermoplastic polymer contains a dispersant. In one preferred embodiment, the dispersant is a C18-C32 aliphatic carboxylic acid, preferably a C18-C28 aliphatic carboxylic acid, preferably a C20-C26 aliphatic carboxylic acid. In one preferred embodiment of the invention, the dispersant is an olefin-acrylic acid copolymer, preferably one having from 10 wt % to 30 wt % acrylic acid, preferably from 15 wt % to 25 wt %. In a preferred embodiment of the invention, other materials such as partially hydrolyzed polyvinyl alcohol, styrene maleic anhydride copolymers, maleic anhydride modified polyethylene, polypropylene, or polyolefin copolymers, maleic anhydride modified styrene-diene block copolymers, or their mixtures may also be used as dispersants. Optionally the conventional cationic, ionic, or non-ionic surfactants can be used in combination with above polymeric dispersing agents. Preferably, the aqueous dispersion of the thermoplastic polymer comprises from 30 to 70 wt % of the thermoplastic polymer (based on total weight of the aqueous dispersion), preferably from 40 to 60 wt %, preferably from 45 to 55 wt %. When the dispersant is a C18-C32 aliphatic carboxylic acid, preferably it is present in an amount from 2 to 10 wt % based on the weight of the thermoplastic polymer, preferably from 2 to 8 wt %, preferably from 3 to 7 wt %. When the dispersant is an olefin-acrylic acid copolymer, preferably it is present in an amount from 15 to 35 wt % based on the weight of the thermoplastic polymer, preferably from 20 to 30 wt %, preferably from 22 to 28 wt %. Preferably, the aqueous dispersion is substantially free of organic solvent, i.e., it contains less than 3 wt % organic solvent based on total dispersion weight, preferably less than 2 wt %, preferably less than 1 wt %, preferably less than 0.5 wt %, preferably less than 0.2 wt %, preferably less than 0.1 wt %. Preferably, solvents which may be present within the stated limits in the aqueous dispersion (from preparation of the thermoplastic polymer) or in the composition are hydrocarbyl solvents, preferably aromatic solvents, preferably toluene.
Preferably, the combined aqueous dispersions of thermoplastic copolymer and rosin comprise at least 20 wt % of the thermoplastic polymer, preferably at least 30 wt %, preferably at least 35 wt %, preferably at least 40 wt %; preferably no more than 80 wt %, preferably no more than 70 wt %, preferably no more than 65 wt %, preferably no more than 60 wt %, percentages based on total weight of dry thermoplastic polymer and rosin. Preferably, the aqueous dispersions of thermoplastic copolymer and rosin comprise at least 20 wt % of the rosin, preferably at least 30 wt %, preferably at least 35 wt %, preferably at least 40 wt %; preferably no more than 80 wt %, preferably no more than 70 wt %, preferably no more than 65 wt %, preferably no more than 60 wt %, percentages based on total weight of dry thermoplastic polymer and rosin.
Preferably, the aqueous rosin dispersion comprises a rosin ester resin, a non-hydrogenated aliphatic C5 resin, a hydrogenated aliphatic C5 resin, an aromatic modified C5 resin, a terpene resin, a hydrogenated C9 resin, or combinations thereof, where “C5” and “C9” refer to the number of carbon atoms in the starting materials used. Preferably, the rosin has a softening point from 25 to 180° C., preferably from 65 to 160° C., preferably from 90 to 140 ° C. Preferably, the rosin has density from 0.92 g/cc to 1.06 g/cc and has a melt viscosity less than 1000 pascal second (Pa·s) at 175° C. Preferably, the rosin has a weight-average molecular weight (Mw) from 300 to 2,000. Preferably, the rosin is substantially free of organic solvent, as defined above for the thermoplastic polymer.
Preferably, the aqueous dispersions of thermoplastic copolymer and rosin (collectively, “the adhesive”) are mixed together at room temperature, preferably using conventional mixing equipment. The adhesive is coated on a fabric substrate at room temperature. The coating thickness of the adhesive on the fabric preferably is from 2 to 30 microns, preferably from 4 to 15 microns, preferably from 5 to 10 microns. Preferably, the coated fabric is dried to remove water, preferably in an oven at a temperature below 150° C., preferably below 140° C., preferably below 130° C., preferably below 120° C.; preferably at least 100° C., preferably at least 110° C. The coated dried fabric is laminated with the polyolefin elastomer, preferably at a temperature from 80 to 180° C., preferably from 100 to 160° C., preferably from 115 to 155° C. Preferably, the compression force during the lamination is from 2 to 50 kN, preferably from 4 to 25 kN, preferably from 8 to 20 kN.
Coating Procedure
Lamination Procedure
Fabric: The fabric used in this study is a typical commercially available black PET fabric.
POE sheet: The POE sheet is made from Dow product XUS57551 (0.87 g/cc, 3.35 MFR) which is a blend of INFUSE™ and VERSIFY™.
Water borne dispersion 1-1: The base resin of the dispersion is FUSABOND C250, a Maleic Anhydride (MAH) modified Ethylene-Vinyl Acetate (EVA) copolymer, and the surfactant package of the dispersion is DMEA neutralized Ethylene-Acrylic Acid (EAA) copolymer. The average particle size of dispersion 1-1 is around 550 nm, solid content is 50.0 wt. %, and the viscosity around 380 cps.
Water borne dispersion 1-2: The base resin of the dispersion is KRATON G1643, a Styrene Ethylene Butene Styrene (SEBS) block copolymer with a styrene content of 16.6-20.6%, and the surfactant package of the dispersion is DMEA neutralized Ethylene-Acrylic Acid (EAA) copolymer. The average particle size of dispersion 1-2 is around 960 nm, solid content is 50.0 wt.%, and the viscosity around 295 cps.
Water borne dispersion 2: Water borne rosin dispersion is used as tackifier dispersion, and the surfactant package of the dispersion is DMEA neutralized Ethylene -Acrylic Acid (EAA) copolymer. The average particle size of dispersion 2 is around 550 nm, solid content is 50.0 wt.%, and the viscosity around 580 cps.
Note: All of the waterborne dispersions mentioned above are produced using Dow's mechanical dispersion technology.
1) Adhesive Formulating
2) Coating & Lamination
3) Peel strength testing (ASTM D751-06, ASTM D2724-03)
The rosin dispersion was an aqueous rosin ester gum sold under the trade name ROSIN GLYCEROL ESTER 202.
Water borne FUSABOND C250/Rosin dispersion (solid mass ratio, 50/50) blend; with the solid content of 45.0 wt %.
Water borne KRATON G1643/Rosin dispersion (solid mass ratio, 50/50) blend; with the solid content of 45.0 wt %.
Water borne FUSABOND C250 dispersion with the solid content of 45.0 wt.%.
Water borne KRATON G1643 dispersion with the solid content of 45.0 wt.%.
Water borne rosin dispersion with the solid content of 45.0 wt.%.
Table 1 shows the bonding strength of the laminated samples prepared by using different adhesives. The bonding strength of a blank sample (POE sheet was directly laminated with fabric without any adhesive in between.) is also presented.
It is observed from Table 1 that the Examples show a peel strength more than 2.0 Kgf/3 cm, which can meet the peel strength requirements, but the Comparative Examples did not meet the performance requirements.
It is believed that the blends of SEBS or EVA-g-MAH dispersion and rosin dispersion have good penetration to the fabric structure during the coating process and act as hot melt adhesives after drying process. Rosin could be the effective tackifier to the base resin, and the unexpected synergistic effect enhances the adhesion.
The inventive examples (blends of SEBS or EVA-g-MAH dispersion and rosin dispersion) offer a good balance of performance and cost, including the environmental benefit.
| Number | Date | Country | |
|---|---|---|---|
| Parent | 15326164 | Jan 2017 | US |
| Child | 16193402 | US |
