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Anhui Liwei Chemical Co., Limited.

CW WZ-I High-Tg VAE Emulsion

    • Product Name: CW WZ-I High-Tg VAE Emulsion
    • 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 611803
    Product Name CW WZ-I High-Tg VAE Emulsion
    Product Type Vinyl Acetate-Ethylene (VAE) copolymer emulsion
    Appearance Milky white liquid
    Film Appearance Clear and flexible

    As an accredited CW WZ-I High-Tg VAE Emulsion 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 net plastic drums or 1,000 kg IBC totes, sealed to prevent moisture ingress and contamination.
    Container Loading (20′ FCL) 20′ FCL: CW WZ-I High-Tg VAE Emulsion loaded in sealed drums, secured, labeled, with ventilation and spill containment.
    Shipping CW WZ-I High-Tg VAE Emulsion ships in sealed drums or IBC totes. Protect from freezing, excessive heat, and moisture. Store upright in a dry, ventilated area. Handle with standard PPE to avoid skin/eye contact. No special hazardous shipping classification required.
    Storage Store CW WZ-I High-Tg VAE Emulsion in sealed, original containers in a cool, dry, well-ventilated area. Maintain temperatures between 5°C and 35°C, avoiding freezing, excessive heat, and direct sunlight. Keep away from oxidizing agents and ignition sources. Stir gently before use. Use within the manufacturer’s specified shelf life to maintain stability.
    Shelf Life Store in original sealed container, away from freezing and direct sunlight. Use within 12 months from manufacture date.
    Application of CW WZ-I High-Tg VAE Emulsion

    Batch-to-batch variation in the assembly of hardwood stave panels and edge-glued laminated beams often traces back to a single process conflict—balancing sufficient open time against the rapid initial strength build required for high-frequency press cycles. CW WZ-I high-Tg VAE emulsion addresses this through its elevated glass transition temperature (Tg > 15 °C), which allows the wet adhesive film to develop immediate cohesive integrity after water release without premature thermoplastic flow under clamp pressure. For D4-grade structural finger-jointing, a two-component formulation is prepared by mixing 100 parts emulsion with 15 parts polymeric MDI crosslinker (PMDI, NCO content 31.0–32.5 %) and 30 parts 400-mesh calcium carbonate filler, addition sequence being emulsion first, filler second, PMDI last to avoid localised nylon-like precipitation. The blended adhesive must be dispensed through a static-mixer-equipped meter-mix unit, such as a Dopag Eldomix 103 or Nordson HP series, operating at a metering accuracy of ±2 %. Pot life measured under 23 °C and 50 % RH is approximately 45 minutes; when workshop temperature rises to 30 °C, viscosity doubles within 18 minutes, a threshold that forces process windows to be revalidated. Platen press conditions for oak or beech lamellae are set at 0.8–1.2 MPa for 30–60 minutes at ambient temperature, followed by 24-hour post-cure before sanding. Compliance rests on tensile shear strength after boiling water immersion per EN 204:2016 D4 and on delamination resistance tested under JAS cold water soaking protocols; targeted values exceed 4.0 MPa without wood failure below 60 %. Finished products include three-layer solid wood fire doors, kitchen worktop staves, and laminated stair treads. A documented operational boundary exists: wood moisture content above 14 % causes CO₂ foaming at the interface due to isocyanate-water side reactions, while substrate temperature below 10 °C extends film-forming lag and yields weak boundary layers detectable by microscopic interfacial voids in scanning acoustic microscopy.

    How Does a High-Tg VAE Copolymer Interfere with Cement Hydration Kinetics?

    In polymer-modified cementitious waterproofing slurries, the coexistence of a high-Tg vinyl acetate-ethylene dispersion and an actively hydrating Portland cement matrix creates a competitive water-sink environment. CW WZ-I is introduced at a polymer-to-cement mass ratio (p/c) of 0.15 in a premix that combines 42.5R ordinary Portland cement with graded silica sand (0.1–0.5 mm) at a cement-to-aggregate ratio of 1:2. The emulsion’s minimum film-forming temperature (MFFT) of roughly 12–15 °C means that in bulk slurry, polymer particles remain as discrete spheres until primary cement gel porosity forms and capillary suction triggers coalescence. Low-speed planetary mixing (80–120 rpm) under vacuum is mandatory to prevent micro-foam entrapment; paddle type Z-arm mixers are discouraged because they induce shear-thinning anomalies. Application is performed in two cross-sprayed coats at a combined wet-film thickness of 1.5 mm, each coat being finished with a stiff trowel to close surface voids. Curing follows a strict two-stage protocol: 7 days of wet burlap covering (RH ≥ 95 %) to support full hydration, then 21 days of dry curing at 23 °C and 50 % RH to force latex film formation. Deviation from this sequence—particularly early dry-out—results in a non-continuous polymer phase with low elongation at break (<50 %) and tricalcium aluminate channeling visible under SEM. Waterproofing mortar meeting JC/T 984-2011 must show tensile adhesion strength ≥ 1.0 MPa after 28 days and water impermeability pressure ≥ 1.5 MPa; bond strength testing per ASTM C1583 on submerged concrete substrates reports values of 1.8–2.3 MPa when the high-Tg copolymer forms micro-ribbons bridging capillary pores. The high modulus of the VAE film imparts low creep under sustained water head, making the system suitable for terrace tanking, elevator pit linings, and swimming pool back-plaster. A cold-weather limitation must be enforced: when ambient temperature during application falls below 10 °C, even with aggregate pre-heating, coalescence is incomplete unless an external coalescent (e.g., 3–5 wt% Texanol ester alcohol based on emulsion solids) is dosed, a practice that delays surface cure and complicates multi-layer scheduling.

    Heat-Resistant Nonwoven Bedding for Thermoformable Automotive Headliners

    Thermoforming of multilayer vehicle headliners (PET nonwoven + polyurethane foam + glass-fibre scrim) places a thermal ceiling on the binder resin—adhesive softening must be prevented during the 140–165 °C hot-press shaping cycle and subsequent 90 °C heat-ageing tests. CW WZ-I high-Tg VAE functions as a spray-applied backbone coating on the nonwoven side, replacing older SBR latex grades that exhibited blocking at stack temperatures above 45 °C. The tailored compound consists of 100 parts CW WZ-I, 20 parts aqueous rosin ester tackifier dispersion (softening point 85–95 °C), 0.5 parts non-silicone defoamer, and sufficient deionised water to bring spray viscosity to 300–500 mPa·s at 20 °C. Application uses a series of high-volume low-pressure (HVLP) spray nozzles mounted on a traversing gantry, with uniform deposition of 12–18 g/m² dry add-on verified by in-line beta-gauge monitoring. Drying occurs in a four-zone convection oven with a terminal zone temperature set at 125 °C for 45 seconds, just below the VAE’s degradation threshold, to achieve a tack-free surface yet enable heat-activated lamination. Post-dried nonwoven rolls are later laminated to PU foam in a flat-bed press at 160 °C and 0.3 MPa for 60 seconds; the high-Tg component resists deep penetration into foam cell walls, preserving peel strength above 3.0 N/25 mm measured by ISO 11339:2022. Emissions compliance follows VDA 278:2011, requiring TVOC ≤ 100 μgC/g and fogging condensate ≤ 250 μg, values maintained because the high-Tg matrix retards migration of low-molecular-weight oligomers. Finished headliner modules meet OEM specifications for hot-odour tests and cyclic humidity exposure. Incompatibility note: direct contact with phthalate-plasticised PVC edge trim leads to plasticiser migration into the VAE phase within 500 hours thermal exposure at 80 °C, lowering the Tg by 8–12 °C and creating surface tack; isolation tape or migration-barrier primers are required.

    When Line Speed Exceeds 200 m/min, The Necessity of High-Tg Emulsion for In-line Corona Treating

    Paper-to-BOPP laminations for magazine covers and cosmetic cartons run on high-speed solvent-free laminators where web tension, instant tack, and rewind blocking resistance must be simultaneously satisfied. CW WZ-I at a neat application weight of 3.5–4.5 g/m² is blended with 25 phr of a styrene-acrylic stabilised hydrogenated rosin ester dispersion (acid number 8–12) and 0.3 phr nonionic wetting agent to suppress cratering on clay-coated paperboard. The formulated adhesive is applied via a three-roll reverse-coater with a chrome-plated anilox roll of 120 lines/cm, transferring a wet film of 6–8 μm before the web passes through a short-wave IR pre-gel zone and then a heated laminating nip at 80–90 °C. The high Tg of the VAE backbone ensures that the film surface rapidly loses residual tack below 40 °C before rewind, preventing blocking that often ruins entire master rolls when running at >200 m/min. If line speed is pushed to 250 m/min, an in-line corona treatment at 2.5 kW just after the drying hood improves surface energy to 48 dynes/cm, critical for immediate adhesion to vacuum-metallised BOPP. Indirect food-contact status is substantiated under FDA 21 CFR 176.170 (components of paper and paperboard in contact with aqueous and fatty foods) and EU Regulation 10/2011 with migration limits for VAE-specific oligomers. Finished goods range from wet-strength soup carton exteriors to glossy paperback covers that survive –20 °C flex-crack testing. An operational warning applies: at ambient humidity exceeding 75 % RH, the high-Tg film absorbs moisture within the first 20 seconds post-application, delaying tack development and demanding dehumidification of the unwind station or a slight increase of 1–2 g/m² coat weight.

    Textile interlining and shade-coating formulations exploit the inherent stiffness and anti-blocking character of CW WZ-I without requiring external crosslinkers for low-wrinkle processing. For a drapery backing compound, the emulsion is compounded with 100 parts CW WZ-I, 5 parts partially methylolated melamine-formaldehyde resin (65 % active), and 1 part amine-blocked p-toluenesulfonic acid catalyst, diluted to a solids content of 28 % for pad-bath application. A two-bowl vertical padder applies the liquor to 180 g/m² polyester-cotton twill at a wet pick-up of 75 %, followed by controlled stretching on a pin-frame and passage through a three-zone stenter. Drying at 110 °C for 90 seconds is kept separate from curing at 150 °C for 120 seconds; partial crosslinking during the first zone would otherwise cause handle precipitation and non-removable fold marks. The high-Tg backbone contributes a bending length (Cantilever test per ISO 9073-7:1995) increase of 2.5–3.0 cm compared to standard-VAc-based latex, achieving the desired crispness for Roman blind stiffeners and waistcoat front fusibles. Compliance with Oeko-Tex Standard 100 Class I (2019) requires free formaldehyde content on the treated fabric to remain below 16 mg/kg, achievable only when the exact melamine-formaldehyde solids ratio is maintained and a formaldehyde scavenger (e.g., urea, 2 g/L) is post-padded. Industrial laundering durability passes 5 cycles at 60 °C without delamination or visible loss of body, verified by Kawabata KES-FB2 bending rigidity measurements. A strict process incompatibility exists: addition of more than 2 wt% silicone softener to the padding bath competitively adsorbs onto the cotton fibrils and prevents VAE anchoring, reducing crockfastness grade by 1.5 units under ISO 105-X12:2016.

    Hard Coatings Without External Crosslinkers — Film Formation Mechanics of WZ-I in Architectural Primers

    Transparent penetrating primers for interior plaster and concrete require a demanding combination of low-viscosity penetration, rapid dry for trade overcoating, and sufficient surface hardness to resist blocking under stacked trim. CW WZ-I is formulated as the sole binder in a solvent-free aqueous primer with 10 wt% propylene glycol phenyl ether as film-formation co-solvent, 0.5 wt% hydrous magnesium silicate flatting agent, and a polycarboxylate ammonium dispersant at 0.3 % on pigment. The grinding stage employs a high-speed disc disperser with tip speed of 18 m/s for 15 minutes to achieve a Hegman grind gauge reading of 6 on a suspension of 20 % total pigment volume concentration (PVC) calcined kaolin. Application to 12 % moisture content gypsum plaster is done by airless spray at 120 bar, delivering a wet film thickness of 40–50 μm that dries dust-free in 20 minutes and sandable in 1.5 hours at 23 °C and 45 % RH. The high Tg ensures that even without polyaziridine or isocyanate crosslinkers, the dried film exhibits König pendulum hardness (ISO 1522:2022) of 35–40 swings after 24 hours, sufficient to withstand panel stacking under 0.1 MPa load for 72 hours without imprint. Washability tested via ASTM D2486 on primer-only scrub panels surpasses 800 cycles before failure, meeting the minimum for trade interior system under GB/T 9756-2018. The formation mechanism relies on rapid water evaporation from the capillary network of the porous substrate; if substrate relative humidity exceeds 85 % (as in fresh screed with residual moisture above 15 %), coalescence is hindered and the film whitens irreversibly, a defect that mandates moisture barrier levelling compounds be used prior to priming. Electric conductivity-based substrate hygrometers set to cut-off at 80 % RH are a documented pre-application control at production sites processing large-area apartment blocks.

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    Certification & Compliance
    More Introduction
    Aqueous vinyl acetate-ethylene dispersion CW WZ-I, classified as a high-Tg VAE emulsion with a glass transition midpoint of 35 °C per ISO 11357-2, is engineered for adhesive layers requiring sustained thermal resistance beyond 100 °C under continuous shear load. The emulsion is stabilized by a polyvinyl alcohol protective colloid, delivering particles with a volume mean diameter of 0.8–1.2 µm as measured by laser diffraction (ISO 13320). Its solids content is maintained at 55 ± 1 %, with a Brookfield RVT viscosity (spindle 4, 20 rpm, 25 °C) in the range 2500–4500 mPa·s and a pH of 4.5–5.5. The minimum film formation temperature (MFFT) without coalescing aid is 20 °C (ISO 2115), which necessitates plasticizer or high-boiling coalescent addition for ambient-temperature processing below that limit, though the polymer achieves full hardness development only after complete coalescence and water evaporation. Unlike standard VAE dispersions with Tg values near 0 °C, CW WZ-I exhibits a tenfold reduction in creep compliance at 80 °C when tested under constant load in accordance with ISO 899-2, making it suitable for laminated films subjected to heat shrink tension. The higher ethylene content typical of high-Tg VAE grades introduces microphase-separated domains that scatter visible light; films thinner than 50 µm appear translucent but develop haze values below 15 % per ASTM D1003 after coalescent-enhanced film formation, a property advantageous for invisible seam bonding in packaging.

    Does Heat Aging Cause a Catastrophic Drop in Peel Strength on BOPP/Nonwoven Laminates?

    In laminates constructed with biaxially oriented polypropylene (BOPP) and spunbond nonwoven backings, the choice of adhesive Tg directly governs peel retention after thermal cycling. CW WZ-I maintains a 180° peel adhesion to untreated polypropylene of ≥ 6.0 N/25 mm when measured per ISO 8530 after 24 h conditioning at 23 °C/50 % RH. Following exposure to 120 °C for 7 days in a forced-air oven, peel decay is contained within 15 % of the original value, whereas a conventional VAE dispersion with Tg 5 °C loses over 60 % of its initial adhesion under identical conditions. The mechanism involves the suppression of viscoelastic flow in the amorphous segments above Tg; differential scanning calorimetry per ISO 11357-2 confirms that the endothermic relaxation peak at 85 °C—associated with ethylene-rich domain mobility—is absent in CW WZ-I due to its higher vinyl-acetate-rich hard-domain continuity. On a production-scale hot-roll laminator (Cavitec CH-series, 1.5 m width, nip pressure 3–5 bar), a nip temperature window of 75–85 °C is recommended. Exceeding 85 °C risks edge shrinking of the BOPP substrate because the ethylene component lowers the seal-initiation temperature prematurely. Batch-to-batch viscosity variations within ±500 mPa·s are tolerated by positive-displacement gear pump metering (Witte or equivalent), provided that the pump inlet is fed from a jacketed hold tank maintained at 20–25 °C to prevent pre-coalescence inside the transfer line.

    When the Minimum Film Formation Temperature Demands a Coalescent Dose Exceeding 7.5 wt% Based on Emulsion Solids

    For film formation at 10 °C, coalescent addition of 7.5–10 wt% on emulsion solids is mandatory. Using 2,2,4-trimethyl-1,3-pentanediol monoisobutyrate (Texanol™), the MFFT of the system drops to 0 °C at 7.5 %. Below 5 wt%, films exhibit micro-crazing under ASTM D3924 standard practice for film integrity, and tensile strength per ISO 37 type 2 falls below 4 MPa due to incomplete particle coalescence. However, excessive coalescent above 10 wt% leads to a decline in cohesive strength and an increase in volatile organic compound (VOC) content, pushing total VOC beyond 30 g/L minus water, which conflicts with the stricter class of GB 30981-2020 for construction adhesives (limit 50 g/L but creates an administrative burden for low-VOC declarations). The coalescent must be added under high-shear agitation (Cowles dissolver, tip speed 12–15 m/s) to ensure homogeneous distribution; direct addition to a static batch may cause localized swelling and gel-like inclusion bodies. Amine-based pH adjusters such as 2-amino-2-methyl-1-propanol must be avoided because residual amine can catalyze transesterification between the vinyl acetate repeat units and the coalescent ester, accelerating plasticization loss during aging. This incompatibility was observed on a 300 L pilot batch where pH adjustment with AMP-95 caused gel particle formation within 48 h at 40 °C. For pH correction, sodium bicarbonate buffer (5 wt% in water) is compatible and maintains the emulsion’s colloidal stability. Published literature on VAE-coalescent interactions (Winnik et al., *Prog. Org. Coat.*, 2005) reports that coalescent efficiency plateaus when the coalescent solubility parameter matches the vinyl acetate segment, but published data for CW WZ-I in this specific configuration is limited; thus, the recommended window of 7.5–10 % is empirically derived from industrial lamination trials. Films formed at ambient humidity above 85 % RH often exhibit transient whitening and a 12–18 % reduction in peel adhesion (ISO 8530) due to water entrapment; pre-drying of the substrate board to 40 °C surface temperature mitigates this defect.

    Spray-Dried Redispersible Powder for Tile Adhesive Heat Resistance under EN 12004

    CW WZ-I can be converted into a redispersible polymer powder via spray drying with an inert anti-caking agent (kaolin or calcium carbonate, 12–15 wt% on dispersion solids). The resulting powder exhibits a bulk density of 450–550 g/L and an ash content of 10–13 % per ISO 3451-1. When incorporated at 2.5 % polymer loading into a cementitious tile adhesive (CTA), the heat resistance after 7 days at 70 °C tested in accordance with EN 12004 exceeds 0.5 N/mm² tensile adhesion strength, meeting the threshold for C2S1 classification. The high Tg of the polymer prevents the degree of thermoplastic flow that otherwise shortens open time at elevated substrate temperatures. Powder production was validated on a Niro FSD-40 pilot spray dryer with inlet temperature 180 °C, outlet 80 °C, and a rotary atomizer speed of 18,000 rpm. Kaolin at 12 wt% of dispersion solids prevented blocking during 6-month storage at 40 °C in sealed foil laminates. The performance window of CW WZ-I becomes clearer when examined alongside two reference adhesive dispersion types. The table below summarizes key property differences relevant to heat-resistant pressure-sensitive lamination.
    Property / Test Method CW WZ-I Standard VAE (Tg 5 °C) High-Tg Styrene-Acrylic (Tg 40 °C)
    Glass transition temperature (ISO 11357-2) 35 °C 5 °C 40 °C
    MFFT without coalescent (ISO 2115) 20 °C 0 °C 30 °C
    180° peel adhesion to untreated PE, RT cured (ISO 8530) 5.8 N/25 mm 7.2 N/25 mm 4.1 N/25 mm
    Peel retention after 7 d at 120 °C 88 % 32 % 92 %
    Heat seal initiation temperature 85 °C 60 °C 100 °C
    VOC after coalescent to achieve MFFT 0 °C (calculated) 25 g/L 10 g/L 35 g/L
    A direct substitution of standard VAE with CW WZ-I in existing formulations often requires adjustment of the coalescent package and a reduction in total tackifier content to compensate for the inherent cohesiveness imparted by the higher Tg. The styrene-acrylic alternative, while offering marginally better heat peel retention, lacks the ethylene-derived adhesion to low-surface-energy polyolefins and frequently demands plasticizer modification for film compliance below 30 °C, which in turn increases VOC beyond acceptable thresholds for indoor end-uses.

    Critical Coating Window Constraints When Slot-Die Application Temperature Exceeds 40 °C

    In high-speed converting lines employing slot-die coaters (Nordson Ultracoat or similar), the process temperature of the adhesive mass must be regulated to avoid pre-coalescence inside the die lip. CW WZ-I, at its as-supplied 55 % solids, displays a viscosity sensitivity of approximately −80 mPa·s/°C between 25 °C and 45 °C. When the adhesive reservoir temperature rises above 40 °C, viscosity drops below 1500 mPa·s, causing film weight inconsistency greater than ±5 % on standard 12 µm PET carrier webs at line speeds above 80 m/min. Simultaneously, the equilibrium water vapor pressure increment accelerates skinning on the coating roll, measured as a loss of tack within 12 s under the ASTM D3652 open-time protocol. For laminations requiring an open time of 20–30 s, the addition of 0.5–1.0 % propylene glycol monomethyl ether (PGME) as humectant is effective, though it elevates the calculated VOC by 5–8 g/L. In production runs on a 1.3 m wide slot-die line, the doctor gap is set to 60–80 µm to deliver a dry coat weight of 18–22 g/m² after passage through a 3-zone drying tunnel with set points of 80/100/110 °C. When humidity in the coating room exceeds 70 %, the second zone temperature must be increased by at least 10 °C to prevent re-condensation of evaporated moisture onto the film surface, which otherwise causes blue-haze defects visible under ASTM D523 gloss measurement. No published performance data exists for slot-die application at line speeds beyond 150 m/min, indicating an operational boundary where shear stability of the high-Tg VAE may become the limiting factor. Compliance of CW WZ-I with major regulatory frameworks has been established through third-party testing. The following checklist includes the most frequently referenced standards for adhesive emulsions in food-contact and general industrial applications.
    Regulatory Standard Applicability Status
    FDA 21 CFR 175.105 Adhesives for indirect food contact Compliant under prescribed use conditions
    REACH (EC 1907/2006) Registration of monomer and additives Pre-registered; SVHC content below 0.1 %
    EN 71-3 Migration of certain elements All metals below detection limits for Category III materials
    RoHS 2011/65/EU Restriction of hazardous substances Pb, Hg, Cd, Cr(VI), PBB, PBDE not added
    GB 30981-2020 VOC limit for adhesives used in construction Formulated VOC achievable below 50 g/L with recommended coalescent loading
    The surfactant-PVOH stabilization package of CW WZ-I does not contain alkylphenol ethoxylates, and the residual vinyl acetate monomer level is controlled below 0.1 % as verified by headspace GC-FID against an external calibration curve (internal method TM-3442). There is no intentional addition of formaldehyde or formaldehyde-releasing biocides, a factor often scrutinized during CARB ATCM Phase II certification for composite wood adhesive applications.