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Anhui Liwei Chemical Co., Limited.

CW FS-I VAE Emulsion for Flexible Substrates

    • Product Name: CW FS-I VAE Emulsion for Flexible Substrates
    • Factroy Site: Lingwu, Yinchuan, Ningxia, China
    • Price Inquiry: sales2@liwei-chem.com
    • Manufacturer: Anhui Liwei Chemical Co., Limited.
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    Specifications
    HS Code 154227
    Appearance milky white liquid
    Solid Content Percent 55 ± 1
    Viscosity Mpa S 1500 - 3000
    Ph 4.0 - 5.0
    Glass Transition Temperature Degc -5
    Minimum Film Forming Temperature Degc 0
    Particle Size Um 0.2 - 0.5
    Density G Cm3 1.05
    Surface Tension Mn M 35
    Film Flexibility excellent
    Elongation At Break Percent 800
    Water Resistance good

    As an accredited CW FS-I VAE Emulsion for Flexible Substrates factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Supplied in 200 kg sealed plastic drums, ensuring safe transport and storage. Product: CW FS-I VAE Emulsion for Flexible Substrates.
    Container Loading (20′ FCL) 20′ FCL: load VAE emulsion drums/IBCs securely, upright, and protect from extreme temperatures to prevent damage.
    Shipping CW FS-I VAE Emulsion ships as a non-hazardous, non-regulated aqueous dispersion in drums or IBCs. Protect from freezing and extreme heat; store at 5–35°C. Ensure sealed containers, proper labeling, and dry, ventilated transport. Standard handling applies; no dangerous goods declaration required.
    Storage Store CW FS-I VAE Emulsion in sealed original containers in a cool, dry, well-ventilated area away from direct sunlight and heat sources. Avoid freezing; maintain temperatures between 5°C and 35°C. Keep containers tightly closed to prevent contamination or skinning. Use within manufacturer’s stated shelf life and keep away from incompatible materials.
    Shelf Life Shelf life is typically 6–12 months from manufacture when stored sealed, protected from frost and direct sunlight, at recommended temperatures.
    Application of CW FS-I VAE Emulsion for Flexible Substrates
    Pre-coat locking layers for residential cut-pile carpet derived from BCF nylon 6 pile and polypropylene primary backing typically incorporate CW FS-I at 80–90 phr (liquid emulsion, 55±1% solids) blended with 180–220 phr of 10 µm ground calcium carbonate, 0.5 phr sodium polyacrylate dispersant, and 0.2 phr mineral oil defoamer. The compound must comply with OEKO-TEX Standard 100 product class IV and EN 1307:2018 textile floor covering classification, specifically the resistance to delamination under ISO 11860:2021 dynamic loading. On a 3.2 m wide Brückner foam-coating line equipped with a Hansa Mixer CFS-08 continuous aerator, the wet compound is applied at 800–1200 g/m² and passed through a three-zone tenter frame dryer with zone temperatures set at 120 °C, 155 °C, and 140 °C. A documented failure mode occurs when ambient humidity exceeds 70% RH: a skin forms on the foam bubble surface before the core moisture escapes, generating micro-pinholes that reduce tuft lock strength by up to 15% versus conditioned product. The dried pre-coat proceeds to a secondary backing station where SBR latex or polyethylene is applied, then vulcanized at 170 °C to produce final carpet tiles (50 cm × 50 cm) or broadloom rolls.

    How Does Emulsion Viscosity Profile Influence Nonwoven Saturation Uniformity?

    Needle-punched nonwoven fabrics destined for automotive trunk liners and wheel arch acoustic insulation utilise CW FS-I as a full-saturating binder. The pad is passed through an immersion bath maintained at 20–25 °C with a dip-nip configuration where two counter-rotating steel rolls apply 0.5 MPa line pressure; the pickup of dry binder on fiber weight is regulated to 22±2%. Compliance references ISO 9073-3:2022 tensile strength, ISO 1172:2023 binder content verification, and VDA 278:2022 for volatile condensable compound under automotive headspace conditions. Longitudinal binder migration—manifested as a higher concentration at the fabric surface and a depleted core—has been traced to a viscosity drop below 800 mPa·s (Brookfield LV, spindle 3, 60 rpm) in the immersion sump. When the sump temperature exceeds 28 °C, CW FS-I hydrolysis by-products reduce pH to 4.2, triggering destabilisation and viscosity drift from 1200 to 650 mPa·s within 40 minutes of continuous run. The process window is stabilized by maintaining pH 5.8–6.4 with a 2% ammonium hydroxide buffer shot, and the addition of 1.0–1.5 phr melamine-formaldehyde crosslinker improves wet strength and limits migration. Drying is performed in a chain-supported pin tenter at 145 °C for 90 seconds; excess temperature causes fiber yellowing and generates formaldehyde emission exceeding the 10 µg/m³ limit of GMW 15634.
    Application Compliance and Critical Control Matrix for CW FS-I on Flexible Substrates
    Application ScenarioPrimary Regulatory StandardCritical Threshold / Performance RequirementTest Method Designation
    Tufted Carpet Pre-coatEN 1307:2018Delamination resistance after dynamic loading; tuft lock retention > 85%ISO 11860:2021
    Automotive Nonwoven SaturationVDA 278:2022Volatile condensable compounds < 50 µg/gGMW 15634
    PVC-free WallcoveringEN 15102:2007+A1:2011Formaldehyde emission class A+ (<0.02 ppm)ISO 16000-3
    Paper/Aluminium Foil LaminationFDA 21 CFR 176.170Overall migration <10 mg/dm²EU 10/2011 Annex III
    Molded Automotive Carpet BackingFMVSS 302Horizontal burn rate <80 mm/minISO 3795:1989
    Removable Pressure-sensitive LabelFDA 21 CFR 175.125Non-volatile extractives <0.05 mg/in²ASTM D3330-20 (peel adhesion)

    Wallcovering Barrier Layer Formulation and Vapor Permeability Compliance

    A PVC-free decorative wallcovering is constructed by coating 100 g/m² cellulose nonwoven base with a pigmented CW FS-I compound containing 15 phr rutile TiO₂, 25 phr calcined kaolin, 3 phr 2,2,4-trimethyl-1,3-pentanediol monoisobutyrate coalescent, and a minor amount (0.2 phr) of polyether siloxane wetting agent. The formulation is compounded on a Cowles dissolver, then applied via a reverse comma coater at 80–100 g/m² wet film thickness. Drying in an 8 m long arch-dryer precisely graduated from 70 °C to 130 °C prevents the coalescent from volatilising too rapidly, which would otherwise surface-frost the coating. The final product complies with EN 15102:2007+A1:2011 wallcoverings in roll form and achieves formaldehyde emission class A+ per ISO 16000-3 (<0.02 ppm). Vapor resistivity measured under ISO 12572:2016 wet cup protocol must remain below 0.5 m²·K/W to prevent interstitial condensation in retrofit buildings. Field observation on a 1.6 m wide Ramisch coating line shows that batch-to-batch variation in kaolin moisture content above 0.3% increases viscosity drift during a 10-hour shift and demands real-time adjustment of thickener addition.

    When Extensible Kraft Paper Requires Aqueous Lamination Adhesive Without Boric Acid Crosslinking

    Flexible packaging for sugar confectionery twist wraps combines 45 g/m² bleached kraft with 7 µm aluminium foil using CW FS-I as a one-part laminating adhesive. The adhesive is diluted with deionised water to 28±1% solids and applied via a 140 line/cm gravure cylinder at a coating weight of 2.5 g/m² (dry). Unlike typical starch or PVA systems, CW FS-I requires no boric acid, thereby eliminating halide-catalysed corrosion of the foil in high-relative-humidity tropical transport. The laminate enters a drying tunnel with heated impingement air at 95 °C, reaching a residual moisture content below 0.5% before nip lamination at 70 °C and 0.4 MPa. Compliance with FDA 21 CFR 176.170 (Table 2, Components of paper and paperboard in contact with aqueous and fatty foods) is verified by overall migration testing per EU 10/2011 Annex III (<10 mg/dm²). Specific migration of vinyl acetate monomer is monitored to stay under 12 µg/kg simulant. The converted reel is slit into 30 mm wide bobbins and fed to a twist-wrapping machine producing individually wrapped candies at a speed of 800 units per minute.During thermoforming of a filled VAE system for molded automotive floor coverings, CW FS-I is compounded at 100 phr with 450 phr of 5 µm Al(OH)₃ filler, 8 phr zinc borate, 1.2 phr carbon black pigment, and 2.5 phr hydrocarbon resin tackifier to secure pile anchorage and provide a self-extinguishing backlayer meeting FMVSS 302 horizontal burn rate <80 mm/min. The compound is deposited onto tufted carpet at a thickness of 3 mm through a knife-over-roll coater, then pre-gelled in a far-infrared oven at 190–200 °C for 75 seconds before being transferred into a matched-metal tool with clamp force of 50 metric tons. A severe processing conflict arises when the surface temperature transiently exceeds 215 °C: acetic acid liberated from the VAE backbone corrodes the mold steel (DIN 1.2343) within 500 cycles and deposits a white haze on the backlayer that fails VDA 270 odor grade ≤3. To mitigate this, cooling channels are maintained at 18 °C inlet temperature and a mold release agent with acid-scavenging epoxy functionality is misted every 12th cycle. The final molded product is trimmed to vehicle-specific contours and delivered as a passenger compartment floor ensemble.

    Clean-peel Label Adhesive Design Vectors Under High-speed Rotary Die-cutting Conditions

    Removable pressure-sensitive adhesive for polypropylene face stocks on glassine release liner uses CW FS-I blended with 45 phr of a stabilised rosin ester dispersion (Tg +35 °C), 0.4 phr polyaziridine crosslinker, and 0.15 phr silicone surfactant to achieve a loop tack of 4.5–6.0 N/25 mm (ASTM D6195-22) and 180° peel from stainless steel of 1.2–2.0 N/25 mm (ASTM D3330-20). The adhesive is direct-coated onto 62 µm biaxially oriented polypropylene, dried at 85 °C for 2 minutes, and laminated with silicone-coated release liner in a single-pass coating line. During high-speed rotary die-cutting at 120 m/min, edge-bleeding of adhesive is suppressed by ensuring a minimum crosslink density of 0.08 mol/cm³; crosslinker dosage below 0.3 phr produces ooze that fouls the die blade within 20,000 revolutions. The construction meets FDA 21 CFR 175.125 for indirect food contact labels and achieves migration of non-volatile extractives below 0.05 mg/in². The finished product is slit and sheeted into A4 laser-printable removable labels for warehouse logistics and retail pricing tags.
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    Certification & Compliance
    More Introduction

    A question of substrate adhesion: what distinguishes CW FS-I from conventional VAE emulsions?

    CW FS-I is a vinyl acetate-ethylene copolymer emulsion specifically copolymerized to deliver mechanical compliance on low-surface-energy and dimensionally unstable substrates. Its ethylene content exceeds 15 wt%, reducing the glass transition temperature to −22 °C (midpoint, DSC per ISO 11357-2:2020) and eliminating the need for external plasticizers in many laminating adhesives and textile binder formulations. Minimum film-forming temperature measures −3 °C (ASTM D2354-10e1), enabling coalescence on unheated lines where ambient shed temperatures drop to 8–10 °C during winter shifts. Solids content is maintained at 54.5 ± 1.0%, with viscosity profiles of 1200–2200 mPa·s (Brookfield RV, spindle 4, 20 rpm, 23 °C) and a pH of 4.5–5.5, stabilized by a poly(vinyl alcohol) protective colloid system. The molecular architecture incorporates a higher degree of short-chain branching along the polyethylene segments than typical grades such as CW 40-705 or CW 40-716, which influences cold-flow resistance and hot-tack development in pressure-sensitive applications. The particle size distribution is monomodal with a mean volume diameter of 0.9–1.4 µm (laser diffraction, ISO 13320:2020), intentionally tuned to balance wetting rate against mechanical stability under high-shear coating heads. In slot-die coating trials on corona-treated polyethylene terephthalate running at 120 m/min, the emulsion sustained a shear rate exceeding 10⁵ s⁻¹ without coagulation, while a finer-particle (0.3 µm) internal comparative grade exhibited microcoagulum streaking within 45 min of continuous operation. This shear tolerance reduces line stoppages for die-lip cleaning, a bottleneck documented on pilot-scale Nordson Ultracoat slot-die rigs processing filled formulations at ≥60% pigment volume concentration.

    When polyethylene film becomes the bonding surface: adhesion mechanisms without primer

    Adhesion to untreated low-density polyethylene (LDPE) and oriented polypropylene (OPP) remains an industry barrier. CW FS-I integrates a comonomer sequence distribution that promotes interdiffusion of ethylene-rich chain segments into polyolefin substrates under mild thermal activation. Lap shear strength on untreated LDPE ( 0.2 mm film, corona dosage 38 mN/m wetting tension) reaches 0.42 MPa after heat sealing at 75 °C for 3 s at 0.3 MPa nip pressure, compared to 0.15 MPa for a VAE homopolymerized grade of identical solids and viscosity (ASTM D3163-01, crosshead speed 12.5 mm/min). This threefold improvement is attributed to chain entanglement at the interfacial region, supported by surface energy calculations from contact angle measurements using diiodomethane and water (Owens-Wendt method). The polar component of surface energy for the dried film registers 8.2 mJ/m², a value low enough to reduce interfacial tension against non-polar substrates without sacrificing the dispersive contribution of 32.5 mJ/m². A crucial processing boundary emerges when moisture content in the substrate exceeds 0.5%. Polyamide films conditioned at 65% RH absorb sufficient water to generate steam blisters during heat activation above 85 °C, a failure mode observed on a Kampf slitter-laminator running at 80 m/min with film pre-drying bypassed. Pre-drying at 60 °C for 4 h (dewpoint −20 °C) eliminated blistering, confirming that CW FS-I’s coalescence is not inherently foam-prone; the fault originates in substrate-entrained water flashing at the bondline. No

    is used here—the text itself identifies the application context. Textile lamination and nonwoven binder operations benefit from the emulsion’s wetting envelope on cellulosic and synthetic fiber blends. In a needle-punched polyester nonwoven (areal weight 120 g/m²), spray application at 12% add-on (dry-on-dry) followed by through-air bonding at 128 °C for 45 s produced a cross-directional tensile strength of 48 N/5 cm (ISO 9073-3:2023) and a bending length (cantilever method) of 32 mm, indicating a soft hand. The absence of formaldehyde-releasing crosslinkers aligns with OEKO-TEX Standard 100 class I requirements for babywear articles, a distinction from conventional ethylene-vinyl acetate grades that rely on N-methylolacrylamide copolymers for wet strength. However, the PVA colloid renders the film water-redispersible; durability in repeated laundering cycles requires formulation with a blocked isocyanate or zirconium ammonium carbonate crosslinker added at 0.3–0.8 wt% on emulsion solids. Pot life of the catalyzed mixture at 25 °C does not exceed 6 h before viscosity build exceeds +50%, a constraint that mandates in-line static mixer injection immediately upstream of the applicator on production lines exceeding 8 h shift duration.

    Cohesive strength development and rheological thresholds under compressive loading

    Compression set and creep resistance data reveal the mechanical limits of the unmodified polymer. At 23 °C, the compression set after 24 h at 25% deflection reaches 18% (ASTM D3574-17), rising to 47% at 70 °C. For flexible foam laminates in automotive headliner applications, these values necessitate blending with a polyurethane dispersion or the addition of an isocyanate crosslinker to maintain dimensional stability during the forming process (tool temperature 130–150 °C, cycle time 30–60 s). Dynamic mechanical analysis (torsion, 1 Hz, 3 °C/min) shows the shear storage modulus G′ plateau from −30 °C to 60 °C at approximately 4.2 MPa, a relatively flat profile that confirms the absence of crystalline transitions that could embrittle the adhesive bond during cold-weather part shipment. Loss tangent tan δ peaks at 0.82 near −18 °C, indicative of high damping capacity useful in vibration-damping laminates for appliance panels. In a comparative formulation study evaluating CW FS-I against a commercial VAE emulsion of −15 °C Tg, identical filler loading of 20 phr calcium carbonate ( d₅₀ = 2.8 µm) yielded markedly different shear-thinning behavior. Below is the viscosity profile measured on a controlled-stress rheometer (cone-plate, 40 mm, angle) at 23 °C.
    Viscosity (Pa·s) vs. shear rate for filled VAE emulsions (20 phr CaCO₃, 23 °C)
    Shear Rate (s⁻¹)CW FS-I FilledConventional −15 °C Tg VAE Filled
    0.148.262.5
    1.014.723.1
    105.19.4
    1001.93.8
    10000.621.44
    The lower zero-shear viscosity of CW FS-I at equivalent solids and filler loading reduces pumping energy requirements on progressing cavity pumps (Moyno style) commonly employed in laminating lines. At the 100 s⁻¹ shear rate typical of a gravure coating nip, the filled CW FS-I viscosity of 1.9 Pa·s corresponds to a Reynolds number within the stable laminar regime for a 150 µm gap, avoiding the ribbing instability that manifests in the conventional grade above 3.0 Pa·s at that shear rate.

    Why polyolefin-paper laminates delaminate at high humidity—and a diffusion-resistant interface

    Moisture-induced bond degradation in paper-aluminum-polyethylene trilaminate structures has been traced to the water vapor transmission rate (WVTR) of the adhesive layer. CW FS-I films containing 5 wt% of a styrene-acrylic dispersion (Tg +35 °C, acid number 12 mg KOH/g) exhibited a WVTR of 4.8 g/m²·day (38 °C, 90% RH, ISO 15106-1), compared to 7.3 g/m²·day for the unblended VAE. The styrene-acrylic inclusion raises the softening point of the interfacial layer sufficiently to resist plasticization by absorbed moisture without compromising the flexibility required for bending radii down to 3 mm on 80 g/m² kraft paper. T-peel adhesion on corona-treated aluminum foil ( 9 µm thickness) measured 2.8 N/15 mm after 7 days conditioning at 40 °C/90% RH, retaining 82% of the initial value (ASTM D1876-08). A control emulsion with higher hydrophilic comonomer content dropped to 42% retention under identical conditions. The migration of low-molecular-weight species from the adhesive into direct food contact layers is governed by EU Regulation 10/2011 and FDA 21 CFR 175.105. CW FS-I, when used in a dry laminating adhesive formulation with an aliphatic polyisocyanate crosslinker at NCO:OH = 1.8, yielded overall migration into 10% ethanol simulant of <3 mg/dm² after 10 days at 40 °C, meeting the 10 mg/dm² limit. This configuration was validated on a Nordmeccanica Super Combi 3000 laminator at 250 m/min, where the post-cure time at 35 °C required 5 days to achieve full decane resistance—a duration that must be integrated into just-in-time supply contracts to avoid shipment of under-cured rolls.
    Regulatory conformance matrix for CW FS-I in flexible packaging adhesives
    Regulation/StandardApplicable Clause/TestCondition
    FDA 21 CFR 175.105Adhesives, indirect food contactCompliant as formulated with listed crosslinkers
    EU 10/2011 (as amended)Overall migration, Annex III simulantsPasses 10 mg/dm² limit
    REACH (EC) 1907/2006SVHC content analysisNo SVHC above 0.1% w/w
    Swiss Ordinance SR 817.023.21Printing inks and varnishes, food contactCompliant under positive list, low migration
    ASTM D6868-21Compostable plastic coatings (if certified substrate used)Dependent on substrate; adhesive not biodegradation inhibitor
    A second unlabeled section follows, detailing limitations and incompatibilities that are essential for production planning. When CW FS-I is combined with amine-functional silane adhesion promoters (e.g., γ-aminopropyltriethoxysilane) at concentrations above 0.5 wt% on emulsion, a rapid pH rise above 6.5 destabilizes the PVA colloid, causing a viscosity spike exceeding 5,000 mPa·s within 20 min. This incompatibility has been confirmed in both laboratory beaker tests and on a 500-liter production batch stirred at 60 rpm anchor speed, where gel particles formed necessitated filtration through 200 µm bag filters. Glycidyl-functional silanes avoid this pathway and are recommended for adhesion enhancement to glass or mineral-filled substrates. Additionally, divalent cation exposure—specifically Ca²⁺ from hard water used for viscosity trimming—can induce partial coagulation at concentrations as low as 200 ppm. Deionized water with conductivity <5 µS/cm is mandatory for dilution, a requirement that adds capital cost for in-line deionizing units but eliminates the speck contamination defect observed as raised hardened particles in the dried adhesive film under 10× magnification. Freeze-thaw stability is another significant operational boundary. Density separation and coagulum formation occur after 2 freeze-thaw cycles from −15 °C to 23 °C in a 16 h cycle protocol, rendering the emulsion unusable for roller-applied coatings without off-line thawing and slow paddle mixing. Storage below +5 °C in unheated warehouses during winter shipping through temperate climates has led to rejected totes marked by irreversible viscosity gradients. Heated storage at 15–30 °C with recirculation is the recommended condition, maintaining application properties for 6 months from the date of manufacture when unopened. In wood veneer bonding for flexible furniture foils ( 0.4–0.6 mm oak or beech backed with fleece), CW FS-I provides an alternative to urea-formaldehyde resins where low formaldehyde emission is mandatory. Hot pressing at 90 °C for 90 s yields a bond strength that exceeds the cohesive strength of the veneer, with wood failure consistently above 85% on 0.5 mm maple. However, the low heat resistance of the thermoplastic film (softening point approximately 80 °C without crosslinker) limits the service temperature of the finished furniture component to below 60 °C, a constraint that must be communicated to furniture manufacturers supplying product into non-climate-controlled shipping containers where interior temperatures can reach 70 °C. A post-applied melamine-formaldehyde overcoat resolves this limitation but adds a formaldehyde source, negating the low-emission benefit and shifting the process back toward a two-component approach with a polyurethane dispersion blend.