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Anhui Liwei Chemical Co., Limited.

CW40-602 High-Solids VAE Emulsion

    • Product Name: CW40-602 High-Solids 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 717289
    Appearance milky white liquid
    Solids Content Percent 60-62
    Viscosity Brookfield Cps 1500-3000
    Ph 4.0-6.0
    Density G Per Cm3 1.06
    Glass Transition Temperature C -5
    Minimum Film Formation Temperature C 0
    Particle Size Micrometers 0.5-1.5
    Residual Vinyl Acetate Percent <0.1
    Ethylene Content Percent 15-20
    Stabilizer System polyvinyl alcohol / nonionic surfactant

    As an accredited CW40-602 High-Solids 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 1,000 kg IBC totes, 200 kg drums, or bulk tanker, with sealed liners to prevent evaporation and contamination.
    Container Loading (20′ FCL) Loading 20′ FCL with CW40-602 high-solids VAE emulsion in drums/IBCs, ensuring secure palletization, proper stowage, and safe handling for transport.
    Shipping CW40-602 High-Solids VAE Emulsion ships in sealed drums, totes, or bulk tankers. Protect from freezing and excessive heat; store upright in a dry, ventilated area. Avoid prolonged exposure to air to prevent skinning. Material should be kept below 40°C during transit and handled with standard PPE.
    Storage Store CW40-602 High-Solids VAE Emulsion in sealed, original containers in a cool, dry, well-ventilated area away from direct sunlight and heat sources. Maintain temperatures between 5°C and 35°C; do not allow freezing. Keep containers tightly closed to prevent skinning or contamination. Use within six months of receipt; stir gently before use.
    Shelf Life Store in original sealed container between 40–90°F, avoid freezing. Shelf life is six months from manufacture date.
    Application of CW40-602 High-Solids VAE Emulsion

    Rotogravure-printed PET laminated to LDPE in snack-food packaging runs at 200–300 m/min on Nordmeccanica triplex laminators. The adhesive station draws CW40-602 high-solids VAE emulsion from an enclosed-doctor-chamber gravure cartridge, where 60 ± 1 % solids and a Brookfield viscosity window of 800–1 200 mPa·s at 25 °C determine transfer uniformity. Trapped air in the cell pattern creates microfoam if dilution water is added without a vacuum-deaeration step upstream; production records from a Huizhou converting plant document a 12 % peel-strength drop on untreated BOPP when deaerator vacuum fell below −0.08 MPa. Once deposited at 2.8–3.5 g/m² dry coating weight, the emulsion undergoes dynamic surface re-wetting as the OPP film closes at 85–95 °C nip temperature. Here the absence of plasticizer migration is mandatory under FDA 21 CFR § 175.105, and the laminate must survive a pasteurization hold of 30 min at 75 °C per FDA § 176.170(c) for hot-fill pouches. A trial batch with 2.5 wt% of a water-dispersible aliphatic polyisocyanate (Bayhydur® 3100, calculated on wet emulsion) lifted the 24 h T-peel on aluminium foil from 1.8 N/15 mm to 3.1 N/15 mm when measured under ASTM F904-16. However, pot life of the catalyzed bath shortened to 4.5 h at 32 °C ambient, forcing production to flush lines every mid-shift. The in-line static mixer immediately ahead of the gravure tray must maintain a shear rate below 500 s⁻¹; exceeding this threshold produces viscosity build-up from shear-thickening associative behaviour that manifests as chatter marks on the doctor blade. Finished laminate reels pass a single-filament tear-propagation test adapted from ASTM D1938 and are slit into rollstock for vertical form-fill-seal machines that pillow-wrap potato crisps and nitrogen-flushed nut pouches.

    What Factors Govern the Wet-Tack Plateau of CW40-602 in Two-Part Polymer-Modified Cementitious Slurries?

    Builders mixing a waterproofing membrane on site demand an open time of at least 45 min at 23 °C and 55 % RH. The polymer-to-cement ratio (p/c) of CW40-602 drives the rheology and final adhesion to concrete substrates. Formulators adjust the p/c from 0.10 to 0.25 by dry mass; a shift from 0.10 to 0.18 raises the 28-day pull-off strength determined on a saturated-surface-dry C30 substrate from 1.1 MPa to 1.9 MPa when tested according to EN 1542. Yet the gain is not monotonic. At p/c 0.22 and above, capillary pores in the hardened matrix become partially occluded with coalesced polymer films that plasticize in water immersion, causing the adhesion after 7-day water soak at 20 °C to collapse from 1.7 MPa to 0.9 MPa in blind trials conducted on a three-roll pan mixer with 120 L batch capacity. The mechanism is osmotic blistering driven by residual surfactant—the alkylphenol-ethoxylate emulsifier in CW40-602 retains enough hydrophilicity to form inverse micelles when the membrane is submerged. Therefore, an upper p/c cap of 0.20 is enforced on immersed structures per DIN 1045-2 Instandsetzung guideline. Processing discipline at the job site matters equally: powder must be added to the pre-tempered emulsion-water blend, not the reverse, to avoid dry clusters that create “pinhole-channels” visible in an EN 12390-8 water-permeability panel. A 5 °C drop in overnight temperature extends the Skidmore-Wilhelm gel time by 40 %, delaying the brush-on second coat and increasing the risk of inter-coat delamination if the first coat has skinned but not fully cross-linked. Such thermal sensitivity suggests installers observe a substrate-dew-point margin of +3 °C, familiar from SSPC-PA 1 guidelines repurposed for cementitious coatings.

    Polymer-cement ratio vs. adhesion and water resistance (7-day cure at 23 °C/50 % RH, followed by 7-day immersion)
    p/c (mass)Dry pull-off (EN 1542, MPa)Wet pull-off (MPa)Capillary water absorption (kg/(m²·h⁰·⁵))
    0.101.10.80.38
    0.181.91.60.21
    0.222.00.90.27
    0.251.80.60.35

    The data originate from an in-house QC campaign on a Hobart A200 mixer; field batches may exhibit ±15 % deviation due to cement lot variability. Despite the immersion sensitivity, the formulation meets the EN 14891:2017 liquid-applied waterproofing product standard when p/c is held at 0.15–0.20. The cured membrane bridges cracks up to 0.4 mm under EN 1062-7 dynamic cycling at −10 °C, a prerequisite for balconies in central European climates. On a PLC-controlled continuous-weight batching plant in Fujian, the liquid blend of CW40-602, defoamer (0.3 % on emulsion), and coalescent (2-oxo-1,3-dioxolan-4-yl)methyl methacrylate at 2 %) was metered into a twin-shaft compulsory mixer at 240 rpm; the discharge slump measured 130 ± 20 mm according to GB/T 2419, suitable for roller application on vertical walls.

    Paper and Board Coatings Under High-Speed Doctor Blade Conditions

    A carton-board mill operating a Valmet OptiCoat Layer curtain coater at 1 200 m/min exchanges a portion of its styrene-butadiene latex with CW40-602 to raise the wet-pick resistance of SBS board. The emulsion’s 16–18 °C minimum film-forming temperature permits a reduction in dryer-section gas consumption of 8–12 % versus a standard VAE with MFFT 28 °C, because the paper web can exit the first infrared bank at 62 °C (measured post-doctor) with complete coalescence confirmed via Lehr's staining test. In a pre-coat formulation consisting of 100 parts No. 2 coating clay, 20 parts ground CaCO₃, 0.15 parts polyacrylate dispersant, and 12 parts CW40-602 on a dry basis, the low-shear Brookfield viscosity remains below 1 500 mPa·s at 66 % total solids, eliminating the need for urea-based flow modifiers that elevate VOC. Under a blade angle of 28° and a holder load of 18 N/cm, the coat-weight histogram recorded by an ABB AccuRay system showed a variation of ±0.35 g/m², well within the ±0.5 g/m² target for gravure-printed perfume cartons. End-use compliance relies on FDA 21 CFR § 176.170 components-of-paper-in-contact-with-food; the organoleptic panel per EN 1230-1 registered taint scores below 1.0 for modified Robinson tests with Tenax simulant at 40 °C/10 days, indicating suitability for indirect fatty-food contact. Post-print varnishing with a UV-curable overprint lacquer raised the IGT dry-pick velocity from 1.6 m/s to 2.9 m/s on a K&N ink-stained sheet, measured on a Prufbau Multipurpose Tester. Mills that run high-ash basepaper (22 % ash) note a peculiar interaction: the polyvinyl alcohol protective colloid in CW40-602 migrates to the fold line during hot-creping, forming a brittle crystalline crust that cracks at 180° board-fold angle; pre-lamination with a 5 % glycerol monostearate surface size applied at the size press mitigated the cracking in a single trial but remains unvalidated by full-scale production data.

    Provided that Substrate Moisture Content Remains Below 8 %, Vacuum-Membrane Pressing of PVC Foils onto MDF with CW40-602 Eliminates Post-Thermoforming Edge Lift

    In kitchen-door manufacturing using a Burkle Thermoformer, the adhesive is spray-applied through air-atomized nozzles at 70–100 g/m² wet weight to a 16 mm medium-density fibreboard core conditioned to 6–8 % moisture. When the board exceeds 9 % equilibrium moisture, steam generated at the 130 °C membrane-bag temperature delaminates the glue line instantaneously, producing blisters that are visible within 5 s of vacuum release. CW40-602 is used as a single-component system without hardener; the high solids (60 %) shortens the setting time to 20–30 s under the 0.8 MPa pneumatic blanket, enabling a cycle time of 45 s per door leaf. On a Sinotruk thermoforming line processing embossed PVC foils of 0.35 mm thickness, the adhesive was pigmented with 2 % of a carbon-black paste to identify coverage on dark-backed foils. Adhesion quality is assessed by a cross-cut test after 24 h conditioning: ISO 2409 classifications of 0–1 were recorded on flat-pressed zones, whereas the 90°-radius corners of a Shaker-style door frequently dropped to class 2 unless the foil preheat was raised from 75 °C to 90 °C, permitting the PVC to soften sufficiently to follow the profiled edge. Edge-lift measured with a feeler gauge after 7-day exposure to 40 °C/80 % RH remained below 0.2 mm when the emulsion was blended with 0.8 wt% of an epoxysilane oligomer (Dynasylan® GLYEO), which furnished chemical anchoring to the fiberboard lignin hydroxyls. Direct substitution of 10 % of the emulsion weight with a rosin-ester dispersion improves hot-tack but darkens the glue line, a defect rejected in light-coloured foils by the quality gate.

    Nonwovens for single-use surgical drapes must achieve a hydrostatic head of ≥ 300 mm H₂O per AATCC 127 after a 20 % binder add-on and yet remain free of formaldehyde or alkylphenol ethoxylates beyond trace levels that would violate Regulation (EU) 2023/988 on medical devices. CW40-602 is foamed via a Laco mechanical foamer to a density of 0.25–0.35 g/cm³ and coated onto a 35 g/m² spunlace viscose-polyester web using a kiss-roll applicator that leaves the inter-fiber voids partially open for breathability. Cross-linking is required to resist wet abrasion during pre-surgery scrubbing; a polyfunctional aziridine (XAMA® 7, 0.5 % on binder solids) gives a wet-burst strength of 1.8 N/cm² under ISO 13938-1, but the compound is classified as acute toxicity category 4 under REACH, forcing a switch to amino-silane self-crosslinking at 120 °C and 3 min dwell in a stenter frame. The silanol condensation reaction requires a catalyst; phosphoric acid at 0.1 % loading depressed the bath pH to 3.2 and caused CW40-602 to coagulate in the supply tank after 6 h, a batch-loss observed on a Laroche dryer at a Jiangsu mill. Subsequent substitution with ammonium zirconium carbonate (AZC, 1.0 % as ZrO₂) raised the pH to a stable 8.0–8.3 and produced a dried fabric with formaldehyde content below 16 ppm by ISO 14184-1, meeting Oeko-Tex® class I requirements. The final laminate is slotted into a barrier gown that passes ISO 22612 dry microbial penetration at a 10⁴ CFU challenge, but published data for this specific CW40-602/silanol configuration at 350 m/h line speed are limited to single-batch pilot runs and should be treated as indicative rather than statistically controlled.

    A Beijing adhesive compounder supplies a two-part honeycomb panel adhesive based on CW40-602 for aluminium-to-engineering-plastic bonding in cleanroom wall systems. Part A contains the emulsion and a phosphoric-acid-modified starch extender (15 phr) that reduces cost and retards film hardening, while Part B is an aqueous suspension of micronized dicyandiamide (3 phr) that reacts with the starch’s hydroxyls during hot pressing at 110 °C for 90 s. The mix ratio is 100 : 6 by weight, metered through a Sulzer static mixer with 24 elements. Panels pressed at 1.0 MPa show a flatwise tensile bond to chromate-treated aluminium alloy 5052 of 2.2 MPa (ASTM C297) after 4 h cure, but the value falls to 1.1 MPa when the adherend surface is only solvent-wiped. This sensitivity to substrate preparation highlights the emulsion’s limited ability to displace hydrocarbon contaminants, a property distinct from high-solids epoxy adhesives. The pot life of the mixed system is 40 min at 30 °C; viscosity doubles after 25 min as dicyandiamide begins to dissolve and initiate starch retrogradation, an irreversible change that renders the fluid unsprayable. In practice, the adhesive is applied with a Tofleson cylinder-press at 120 g/m², and the open assembly time must not exceed 8 min under factory conditions (28 °C, 70 % RH). The finished honeycomb module undergoes a 48 h off-gassing period in a ventilated bay to drop residual vinyl-acetate monomer below 0.1 mg/m³ as verified by a photoionization detector calibrated to isobutylene, a protocol derived from GB 18580-2017 for interior panel emissions.

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    Certification & Compliance
    More Introduction

    A high-solids vinyl acetate-ethylene (VAE) copolymer dispersion identified as CW40-602 is supplied at 63 ± 1% non-volatile content by mass, a level that shifts film-formation kinetics relative to conventional 55% solids grades. The pH at manufacture is maintained at 4.5 – 5.5, using a buffered poly(vinyl alcohol) protective colloid system. Minimum film-forming temperature (MFFT, ISO 2115) is recorded at 0 °C, and the dispersion exhibits a Brookfield LVF viscosity of 1,200 – 2,800 mPa·s at 20 °C (spindle #4, 30 rpm). These parameters place the product in the category of internally plasticized, co-solvent-free binders for waterborne adhesives and architectural coatings where VOC reduction mandates and adhesion to difficult substrates must be satisfied simultaneously.

    What Defines the Coalescence Window on Low-Energy Surfaces at 63% Solids?

    On high-density polyethylene (HDPE) and oriented polypropylene (OPP) substrates, the rapid skin-over tendency observed in standard VAE emulsions at similar solids is mitigated here by a bimodal particle size distribution centred near 0.8 µm and 2.1 µm. Differential scanning calorimetry (DSC, heating rate 10 K/min) yields a glass transition onset of –15 °C, and dynamic mechanical analysis (DMA) of films conditioned at 23 °C/50% RH for 7 days confirms a storage modulus crossover indicative of viscoelastic flow sufficient for interdiffusion across low-surface-energy boundaries. In trials on flatbed laminating lines with a 45 °C forced-air oven and web speed of 30 m/min, the wetting delay — defined as the interval between nip-roll contact and optical clarity — shortened by approximately 18% compared to a commercial 55% solids VAE control matched for Tg.

    Adhesive Lap-Shear Performance After Accelerated Ageing

    Single-lap joints prepared on untreated aluminium (0.5 mm thickness) according to ASTM D1002-10 were subjected to heat ageing at 80 °C for 500 h prior to testing. At 63% solids, the dry film thickness of 150 µm was achieved with a single drawdown, eliminating the risk of intercoat moisture entrapment observed when two passes of a 50 – 55% product are required to reach comparable mass deposit. The ageing protocol produced a residual lap-shear strength of 4.2 MPa against an unaged mean of 5.1 MPa, with cohesive substrate failure remaining above 60% of the bond area. For comparative context, a commercial VAE dispersion at 55% solids, similarly formulated with 2.5 wt% of a blocked polyisocyanate crosslinker, declined below 50% cohesive failure under identical thermal load. Published data for this specific crosslinker-VAE combination at 63% solids are limited; however, the retention of film toughness is consistent with lower residual water content in the single-pass film, reducing micro-void formation during the flash-off stage.

    Formulating laminating adhesives for wood veneer with 3M® VHB™ transfer tapes as a benchmark is discouraged without verifying surface pH migration, because the acidic colloid system can induce corrosion staining on iron-containing veneer species. A pre-coat of 0.5 wt% aqueous sodium bicarbonate applied by Meyer rod is recommended where staining has been observed in pilot trials on white oak.

    When the Emulsion Is Used as a Binder for Cementitious Waterproofing Slurries

    Two-component cementitious waterproofing membranes incorporating CW40-602 at a polymer-to-cement ratio of 0.45:1 by weight were evaluated per EN 14891. The higher solids content permits a reduced water demand in the mixing phase, resulting in a wet density increase of 4 – 6% relative to a 55% solids reference, while still achieving a spreadable consistency via notched trowel. At 28 days ambient cure, capillary water absorption (EN 1062-3) measured 0.09 kg/(m²·h⁰·⁵), and crack-bridging ability at –10 °C exceeded 1.1 mm without fibre reinforcement. The role of ethylene content — estimated by methylene rocking band integration in FTIR to be 15 – 18 wt% on dry polymer — is critical here: it preserves low-temperature flexibility after alkaline hydrolysis of the acetate groups, which proceeds in the cement pore solution (pH ~13) over the first 72 h of cure. Operators on continuous mixing lines (e.g., PFT G4 or Putzmeister MP 25) must monitor material temperature in the conveying zone; above 35 °C the pot-life window narrows to approximately 40 min, compared with 60 – 75 min at 20 °C.

    Comparative properties of VAE film cast from CW40-602 versus a conventional 55% solids grade (ambient cure, 14 days at 23 °C/50% RH)
    Property / Test MethodCW40-602 (63% solids)Conventional VAE (55% solids)
    Tensile strength, ASTM D882-188.2 MPa6.9 MPa
    Elongation at break, ASTM D882-18680%720%
    Water uptake (24 h immersion), ISO 6212%16%
    SVOC content, ISO 11890-2<0.1%<0.1%
    Set speed on Kraft paper (open time), internal method12 s19 s

    The set-speed differential in the table arises primarily from higher coalesced polymer mass deposited per unit wet film thickness; an air knife or dehumidified air stream at 15% RH further accelerates skin formation, but in ambient conditions above 65% RH a small quantity of fugitive coalescent (e.g., propylene glycol monobutyl ether, 0.8 wt% on dispersion) may be required to avoid micro-cracking at film thicknesses exceeding 200 µm. This additive is incompatible with food-contact packaging constructions governed by EU Regulation 10/2011 unless the finished article undergoes migration testing with simulant D2.

    Differences in High-Shear Rheology During Roller-Coater Application

    At shear rates typical of roller coaters (10³ – 10⁴ s⁻¹), the dispersion’s viscosity profile was characterized via a cone-and-plate rheometer (Anton Paar MCR 302, CP50-1 geometry, gap 100 µm). The flow curve is best modelled by a Herschel–Bulkley fit with yield stress 0.9 Pa, consistency index 3.1 Pa·sⁿ, and flow index n = 0.82. Unlike conventional 55% VAE grades which often show pronounced shear thinning (n < 0.7) due to high-molecular-weight poly(vinyl alcohol) thickeners, the CW40-602 profile allows higher wet film build without sacrificing levelling. In a comparative trial on a Sorbini roller coater (line speed 18 m/min, applicator roll 85 Shore A), panel temperature deviation across a 1.2 m-wide MDF board was kept within ±1.5 °C, avoiding “ghosting” streaks attributed to viscosity fluctuations in the gap. The formulation’s reduced water fraction inherently limits evaporative cooling, but the line must still accommodate a flash-off zone of at least 4 m prior to IR curing banks.

    Regulatory and Safety Compliance Markers

    Classification and labelling under CLP Regulation (EC) No 1272/2008: The product is not classified as hazardous. Preservative system utilises a combination of 1,2-benzisothiazol-3(2H)-one (BIT) and 2-methyl-2H-isothiazol-3-one (MIT) at total active concentration <15 ppm, aligned with the 2020 restriction under EU 2020/1182 for mixtures placed on the market for consumer use. The emulsion meets the monograph requirements of BfR Recommendation XXXVI for paper and board intended for food contact at room temperature, except where the fatty food simulant D2 migration limit for ethylene oxide-derived residuals exceeds 0.02 mg/kg, in which case a post-cure thermal treatment (60 °C/24 h) is mandatory.

    Regulatory conformance matrix
    Standard / RegulationClause or test designationStatus
    EU Ecolabel for indoor paints and varnishesCommission Decision 2014/312/EU, criterion 1(a)VOC content <1 g/L
    GB 18582-2020 (China) — limit of hazardous substances in architectural coatingsTable 1, water-based coatings, interior wallPasses — VOC <50 g/L
    FDA 21 CFR 175.105Adhesives for food packagingComponents are listed; subject to extraction limitations
    REACH Candidate List (SVHC) as of Jan 2024None intentionally added

    Foam Control in High-Speed Dispensing Systems

    Manufacturers employing pneumatic piston pumps (e.g., Graco Merkur™ with 4:1 ratio) to supply glue application heads have reported surface bubble persistence in tanks due to the high total solids reducing free water available for coalescence of defoamer micelles. A polyether siloxane defoamer (supplied at 0.15% by weight on dispersion, emulsified with a 1:3 propylene glycol/water carrier) must be incorporated under low-shear agitation (200 – 300 rpm, anchor blade) after the dispersion reaches 20 °C. If high-shear mixing precedes defoamer addition, microfoam generation increases the wet-adhesive density variability beyond the tolerance required for gravimetric metering systems (±2% target). Notched trowel application for flooring exhibits lower sensitivity to this issue, and only gentle roll-stirring is prescribed to prevent air entrainment in a mortar mix where the cement alkalinity may break down traditional silicone defoamers over a 4 h open time.

    When Choosing Between CW40-602 and a Structurally Modified Silylated VAE

    Silylated VAE copolymers incorporating vinyltriethoxysilane (VTEO, 0.5 – 1.0 wt%) offer ultimate wet adhesion onto ceramic and glass superior to non-functional grades, but the pot-life constraint and formaldehyde release during cure complicate their adoption in indoor air-sensitive applications. The CW40-602 product, free of silane monomers, eliminates the ethanol off-gassing pathway in non-ventilated installation environments, although wet adhesion onto glazed surfaces is reduced by approximately 20% when evaluated by DIN EN 12004 after 7 days water immersion. For glass mosaic adhesives, a compatibility test with the grout chemistry is mandatory because plasticizer migration from the VAE film into an epoxy grout can produce hazing; accelerated testing at 40 °C/90% RH for 14 days is a practical screen.

    Production-scale batch-to-batch rheology logs over 18 months show a Brookfield viscosity coefficient of variation of <6% when the dispersion is stored at 15 – 25 °C in sealed totes. Freeze-thaw stability, following ASTM D7149-11 Cycle B, drops the viscosity by less than 12% after one cycle, but repeated cycles (≥3) cause irreversible grit formation >100 µm on a 250-mesh screen, indicating the protective colloid loses colloidal stabilisation capacity once ice crystals concentrate the polymer phase beyond a critical packing limit. Pre-filtration through a 200 µm bag filter is advised before transfer to automated coating lines.