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Anhui Liwei Chemical Co., Limited.

High Ethylene VAE Emulsion

    • Product Name: High Ethylene 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 702176
    Appearance Milky white liquid
    Solid Content 55±1%
    Viscosity 1000-3000 mPa·s
    Ph 5-7
    Density 1.05-1.10 g/cm³
    Glass Transition Temperature -10 to -5 °C
    Minimum Film Forming Temperature 0-5 °C
    Particle Size 0.2-1.0 μm
    Residual Vinyl Acetate Monomer ≤0.1%
    Ethylene Content 15-25%
    Film Elongation >600%
    Water Resistance Good

    As an accredited High Ethylene 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 drums or 1,000 kg IBC totes, with sealed liners to prevent moisture ingress and ensure stability.
    Container Loading (20′ FCL) 20′ FCL: High Ethylene VAE Emulsion loaded in drums or flexitank, secured, labeled, and containerized for safe transport.
    Shipping High Ethylene VAE Emulsion ships in sealed drums, IBC totes, or bulk tankers. Protect from freezing and excessive heat; store below 40°C. Use ventilated, dry containers with secure bracing. Avoid contact with acids or oxidizers. Ensure proper labeling and spill containment per local regulations.
    Storage Store High Ethylene VAE Emulsion in sealed, corrosion-resistant containers in a cool, dry, well-ventilated area away from direct sunlight and heat sources. Maintain temperatures between 5–35°C to prevent freezing or coagulation. Avoid contact with oxidizing agents and acids. Stir gently before use. Shelf life is typically six months under proper storage.
    Shelf Life Shelf life is typically 6–12 months when stored sealed, protected from frost, and kept at 5–40°C.
    Application of High Ethylene VAE Emulsion
    In furniture profile wrapping lines running plasticised PVC foil onto MDF/HDF cores, high ethylene VAE emulsion functions as the primary polymer binder in one-part waterborne laminating adhesives after blending with polyvinyl alcohol solution, defoamer, and rheology modifier. The ethylene comonomer content depresses glass transition below 0°C and reduces coalescent demand to near zero; this is important because retained coalescing solvent in the dry film softens the PVC surface and accelerates plasticiser migration from the decorative foil. Adhesive is applied to the reverse side of the foil by engraved roller or reverse-roll coater at a wet coat weight of 60–90 g/m². Multi-zone air impingement dryers remove water at 60–80°C, leaving a dry deposit in the range 15–25 g/m². Reactivation on the profile wrapping line uses short-wave IR emitters to bring the adhesive film to 55–65°C immediately before a series of profiled pressure rollers compacts the foil into primed grooves. Viscosity is controlled between 8,000 and 15,000 mPa·s per ISO 2555:2018; thickener addition above 2.0 wt% on formulation solids produces stringing and transfer roller pickup. Compliance for food-contact cabinet edge banding is evaluated under FDA 21 CFR 175.105 for indirect additives, and volatile organic compound limits in the European Union are governed by Directive 2004/42/EC. Residual vinyl acetate monomer is typically held below 0.1% as stated on supplier certificates, and formaldehyde-donor preservatives are excluded where REACH EC 1907/2006 restrictions apply. Quantitative peel-adhesion data for high ethylene VAE on plasticised PVC are frequently held as proprietary plant-reference values, and development trials compare substrate tear and cohesive failure modes rather than absolute peel numbers. Finished components include kitchen cabinet profiles, wardrobe doors, office desking, and door frame laminates.

    Why Is Formaldehyde-Free Binder Selection Critical in Carded Through-Air Nonwovens?

    During production of carded through-air nonwoven webs for hygiene topsheets and medical disposable fabrics, the binder is sprayed or foamed onto dry-laid fibre at an add-on level that commonly ranges from 15% to 25% by fabric weight. High ethylene VAE emulsions without N-methylolacrylamide crosslinking monomer are selected when producers must demonstrate low formaldehyde in finished goods under OEKO-TEX Standard 100 class I or II; the absence of formaldehyde-donor chemistry shifts crosslinking to carboxylated ethylene-VAE chains activated by ammonium zirconium carbonate or zinc ammonium carbonate at 0.3–1.0 phr. Through-air drying at 130–150°C for 6–15 s develops wet strength and water-fastness; residence time below 130°C leaves unreacted crosslinker at fibre crossover points and lowers tensile wet strength. Tensile properties are measured per ISO 9073-3:2023, thickness and absorbency by EDANA/INDA WSP 110.4, and binder distribution by iodine staining or bromophenol blue. The high ethylene content contributes dry flexibility and softness without external plasticiser, which is an advantage in line because an external plasticiser would migrate to the nonwoven surface and alter rewet characteristics. Production batch-to-batch variation is monitored by solids content, pH, and residual monomer; pH for carboxylated grades typically falls between 4.0 and 5.0, and raising pH above 6.5 during dilution with hard water can destabilise the colloid and generate screen plugging in foam applicators. The resulting converted webs are used as diaper leg cuffs, acquisition layers, spunlace replacement binders, and disposable medical gown fabrics.Precoat application on tufted carpet lines exposes high ethylene VAE emulsion to calcium carbonate slurries at filler-to-binder ratios between 3:1 and 5:1 by dry weight. The high ethylene segment of the copolymer improves compatibility with the hydrophobic polypropylene primary backing and reduces glass transition enough to maintain tuft-bind performance after floor installation at low ambient temperatures. In precoat compounding, a Cowles blade disperses calcium carbonate into the emulsion under high shear; air-froth foam density is adjusted to 0.6–1.0 g/cm³ before deposition through a knife-over-roll or slit-die applicator. The compound is dried in a multi-zone gas-fired oven at 120–160°C; residual moisture above 0.5% by mass causes blistering and delamination at the secondary-backing lamination stage. Tuft bind is tested per ASTM D1335-17; delamination strength of secondary backing is tested per ASTM D3936-17. For contract carpet in public spaces, radiant-panel performance is evaluated under ISO 9239-1:2010; high filler loadings can reduce flame spread but must be reconciled with binder demand because the polymer film is the continuous phase carrying the filler. Viscosity of the precoat compound is held between 4,000 and 8,000 mPa·s; over-thickened compound above 10,000 mPa·s produces edge strikethrough and uneven foam collapse on high-speed lines. Manufactured floor-covering formats include broadloom contract carpet, automotive floor covering, and carpet tile with bitumen or vinyl secondary backing.

    Spray-Dried High Ethylene VAE Powders in Exterior Tile Adhesive Formulations

    Converting high ethylene VAE emulsion to a free-flowing redispersible polymer powder requires spray drying at inlet air temperature 140–180°C and outlet temperature 60–80°C; the dispersion is co-sprayed with polyvinyl alcohol or other protective colloid at 5–15% on polymer solids, followed by post-addition of kaolin or precipitated silica anti-blocking agent below 1.0 wt%. The resulting powder has a bulk density of 400–600 g/L and redisperses to primary particle size under alkaline mixing; residual moisture above 1.5% causes caking and poor dry-blend flow. In exterior tile adhesive formulation, redispersible polymer powder dosage between 1.5% and 4.5% by total dry mix is used with Portland cement, quartz sand, cellulose ether, and superplasticizer. The high ethylene content improves deformation capacity and adhesion to porcelain and glass mosaic; adhesion after water immersion and freeze-thaw cycling is evaluated under EN 12004:2007+A1:2012 using EN 1348 tensile pull-off, where C2 classification requires ≥1.0 N/mm² for initial, water-immersed, heat-aged, and freeze-thaw conditions. Mixing on job sites uses a forced-action mixer with water addition controlled to produce pot life above 2 h; over-watering above 0.27 water/powder ratio typically reduces final polymer content per unit area and depresses wet-bond strength. Installed construction products include large-format porcelain tile adhesive, over-tile renovation mortar, and self-leveling underlayment for underfloor heating.
    ApplicationCompliance standardPerformance test methodCritical parameter
    Plasticised PVC profile laminationFDA 21 CFR 175.105ASTM D903-98(2017)Wet coat weight 60–90 g/m²
    Nonwoven hygiene binderOEKO-TEX Standard 100 class I/IIISO 9073-3:2023Binder add-on 15–25%
    Carpet precoatISO 9239-1:2010ASTM D1335-17Filler-to-binder ratio 3:1–5:1
    Tile adhesiveEN 12004:2007+A1:2012EN 1348C2 tensile adhesion ≥1.0 N/mm²
    Interior wall paintDirective 2004/42/ECASTM D2486-17VOC limit 30 g/L waterborne flat
    Alkaline paper coatingFDA 21 CFR 176.170, 176.180ISO 3783:2006Binder level 10–15 phr pigment

    Coalescent-Free Interior Wall Paint at High Pigment Volume Concentration

    Formulation work in high-PVC interior wall paint starts with a Cowles disperser running tip speed 18–25 m/s to disperse titanium dioxide and calcined clay into water, dispersant, and defoamer; pigment volume concentration in flat wall paint may reach 75–80%, where binder demand is economically critical and polymer distribution dominates scrub resistance. High ethylene VAE emulsion with minimum film formation temperature near 0°C eliminates the coalescent stage in low-odor formulations; the paint can be produced and stored at 5–35°C without film collapse at low temperature. Wet scrub resistance is tested under ASTM D2486-17, wet adhesion by ASTM D3359-17 tape test, and low-temperature film formation by ISO 2115:1996. The emulsion is typically added at 15–25% dry polymer on total formulation solids for flat finishes, with higher polymer content increasing gloss and blocking resistance. Freeze-thaw stability is controlled by pH 4.5–5.5 and small quantities of ethylene glycol or propylene glycol; below 0°C without antifreeze, ice crystals rupture the polymer dispersion and produce grit on application. In production-scale tinting, the emulsion shows tolerance for high-pH waterborne colorants up to 5 pH units above binder pH; colorant shock above 10% by volume can cause flocculation and loss of opacity. Finished architectural coatings include low-odor interior wall paint, ceiling emulsion, and high-opacity primer-sealer.

    When High Ethylene VAE Replaces Styrene-Acrylic Binder in Alkaline Paper Coating

    In alkaline paper and paperboard coating, the binder must withstand a wet coating colour pH of 8.0–9.5 where kaolin and calcium carbonate pigments are dispersed with polyacrylate salts. A high ethylene VAE emulsion at 10–15 parts per hundred pigment provides tensile strength and surface pick resistance for coated folding carton board and release liner base; its ethylene comonomer content reduces glass transition and permits calendering at lower temperatures without binder migration. Coating colour is applied by blade coater at 8–20 g/m² dry coat weight; short-dwell infrared and air flotation dryers evaporate water rapidly, requiring the binder to develop quick pick resistance. Surface strength is measured per ISO 3783:2006 using an IGT printability tester; wet binding capacity is checked with a Prüfbau printability tester after water application. For food-contact board, compliance is assessed under FDA 21 CFR 176.170 and FDA 21 CFR 176.180; European compliance may require BfR Recommendation XXXVI. The binder's low residual vinyl acetate monomer and absence of acrylonitrile differentiate it from carboxylated styrene-acrylic alternatives. Converted paper products include folding carton board, release liner base, and paper tube label stock.
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    Certification & Compliance
    More Introduction

    High Ethylene VAE Emulsion (HE-VAE) denotes an aqueous dispersion of a vinyl acetate-ethylene copolymer in which ethylene content on dry polymer is at least 18 wt%. The dispersion is stabilized by mixed anionic/nonionic emulsifiers and is supplied as a white to off-white liquid. Because model designations are manufacturer-specific, HE-VAE is used here as a class identifier rather than a proprietary grade code; procurement should reference the producer’s grade code and certificate of analysis. Representative specification ranges for commercial high-ethylene VAE grades are summarized below. The defining formulation advantage is internal plasticization through ethylene incorporation, which reduces the glass transition temperature and minimum film-forming temperature without external coalescent or plasticizer addition.

    PropertySpecification rangeMethod
    Nonvolatile content54–56%ISO 3251
    pH4.0–5.5ISO 976
    Brookfield RVT viscosity, spindle 3 at 20 rpm, 25 °C1,800–4,000 mPa·sISO 2555
    Density1.06–1.09 g/cm³ISO 2811
    Minimum film-forming temperature0 °CISO 2115
    Glass transition temperature midpoint-20 °C to -10 °CISO 11357-2
    Ethylene content on dry polymer18–25 wt%Producer-reported

    Commercial high-ethylene VAE products typically report ethylene content between 18 wt% and 25 wt% on dry polymer. The exact value is producer-reported and influences the balance between wet tack, tensile strength, and barrier properties. Where the application requires low plasticizer migration, grades at the upper end of the ethylene range are selected because they can form coherent films below 5 °C without dibutyl phthalate or benzoate plasticizers. Residual vinyl acetate monomer and free formaldehyde values should be obtained from the producer’s certificate of analysis and compared with REACH Annex XVII restrictions and food-contact status under 21 CFR 175.105 where applicable.

    What Distinguishes High-Ethylene VAE from Vinyl Acetate Homopolymers and Acrylic Dispersions?

    Vinyl acetate homopolymer emulsions exhibit a glass transition temperature near 30 °C and require external plasticizer or coalescent to produce flexible films at ambient temperature. High-ethylene VAE copolymerization inserts ethylene segments along the acetate backbone, reducing chain packing and shifting the glass transition temperature to between -20 °C and -10 °C as measured by ISO 11357-2. This structural change modifies tensile response. Under ISO 527-3, films from high-ethylene VAE typically display lower elastic modulus and higher elongation at break than analogous PVAc homopolymer films; specific values depend on molecular weight, branching, and crosslinker selection and should be taken from the supplier’s certificate of analysis rather than predicted from ethylene content alone.

    Compared with acrylic emulsions, high-ethylene VAE does not rely on alkyl acrylate or methacrylate comonomers for low-temperature film formation. Acrylic dispersions generally provide superior resistance to ultraviolet radiation and hydrolysis, whereas high-ethylene VAE offers adhesion to polar surfaces and, after corona treatment, to polyethylene and polypropylene films. The operational boundary is exterior durability: unmodified high-ethylene VAE should not be specified for long-term exterior wood or facade coatings unless light stabilizers and UV absorbers are incorporated and the formulation is evaluated under ISO 11341 or ASTM G154.

    Compared with ethylene-vinyl acetate redispersible powder, the wet high-ethylene VAE emulsion avoids the spray-drying step and the thermal history associated with powder production. Redispersible powder is preferred for dry-mix mortars and cementitious tile adhesives, whereas the wet emulsion is used in liquid adhesives, coatings, laminating, and binders. The difference is physical form and application method rather than polymer composition alone.

    Against solventborne polychloroprene, solventborne polyurethane, and EVA hot-melt systems, high-ethylene VAE is waterborne and can be compounded without solvent recovery or explosion-proof mixing. It does not require hot-melt application equipment. The trade-off is a water phase that introduces freeze-thaw sensitivity and slower set speed than solventborne adhesives. Open time, wet tack, and green strength should be measured using the applicable end-use procedure for the specific floor covering or packaging category; where standardized comparative methods are required, adhesive shear and peel methods such as ISO 4587 and ISO 11339 provide objective data.

    Film Formation Temperature, pH Stability, and Formulation Boundaries

    Minimum film-forming temperature for high-ethylene VAE is generally at or below 0 °C when tested per ISO 2115. Coalescent-free film formation proceeds at substrate temperatures above 5 °C. Below 0 °C, free water in the wet film can freeze before full particle deformation and interdiffusion, producing a discontinuous film with reduced adhesion and water resistance. Cold-weather application requires heated storage, heated application lines, or partial propylene glycol addition. Any glycol or coalescent addition must be counted against the VOC limit for the relevant product category under Directive 2004/42/EC or the applicable national regulation.

    The dispersion is anionically stabilized. pH drift below 4.0 accelerates hydrolysis of vinyl acetate and releases acetic acid, which further lowers pH and may generate coagulum. During compounding, pH is monitored per ISO 976 and buffered with dilute sodium bicarbonate solution to 4.5–5.0 before fillers are charged. Calcium carbonate raises pH and can destabilize the dispersion if added rapidly; production-scale mixing should use a low-shear planetary mixer with anchor sweep at 20–40 rpm rather than a high-speed Cowles blade. If a rotor-stator mill is required for pigment or filler dispersion, the emulsion should be added after the grind phase when batch temperature is below 35 °C to avoid shear-induced coagulum.

    Freeze-thaw stability is limited. Storage should be maintained at 5–30 °C. Frozen material may undergo irreversible coagulation, and repeated freeze-thaw cycles are not recommended. High-ethylene VAE should not be combined with cationic additives unless a compatibility trial confirms stable viscosity and particle size retention over 48 h. Excessive high-HLB nonionic surfactant additions can displace the anionic stabilizer layer; wetting agent additions should be minimized and pre-diluted before incorporation.

    Viscosity drift is monitored over 24 h and 72 h using ISO 2555 after compounding. If viscosity increases beyond the producer’s stated tolerance without pH change, coagulum or partial destabilization should be suspected and the batch screened through a 100 µm filter. Published data for individual production-scale batches varies with filler type and mixing history.

    In resilient flooring adhesive manufacture, high-ethylene VAE is combined with filler slurries, wetting agents, defoamers, and rheology modifiers. The high ethylene content allows plasticizer-free formulations, which removes external plasticizer migration as a failure mode in PVC floor coverings and maintains low-temperature flexibility of the bonded layer. Shear resistance on concrete and wood adherends is measured under ISO 4587; flexible floor covering peel resistance is measured under ISO 11339. Specific values depend on filler type, filler loading, substrate moisture condition, and surface preparation, and published data for individual formulations is limited.

    When High-Ethylene VAE Is Used in Laminating, Pressure-Sensitive, and Construction Adhesives

    For laminating adhesives applied by roll coater or reverse gravure at ambient temperature, the low MFFT supports coalescent-free wet-film laydown and reduces the risk of pinholing on absorbent paperboard. Corona-treated polyethylene and polypropylene film surfaces are used after verifying wetting tension per ISO 8296; adhesion values are influenced by surface energy and treatment age. High-ethylene VAE is likewise used in paper-to-film lamination where cold-temperature flexibility and plasticizer-free construction are required.

    Pressure-sensitive adhesive formulations based on high-ethylene VAE may require tackifier dispersion. Rosin ester or hydrocarbon tackifier dispersions must be checked for pH and anionic compatibility prior to addition because acidic or cationic tackifier systems can destabilize the polymer dispersion. Loop tack and peel adhesion can be measured by ASTM D6195 and ISO 29862, respectively; performance depends on tackifier concentration, drying conditions, and substrate.

    Construction adhesive applications include resilient flooring, wall covering, insulation, and general assembly. The product is selected where low-temperature flexibility, plasticizer-free formulation, and waterborne handling are required. The operational limit is water resistance: VAE films are not highly crosslinked and retain water sensitivity. For wet-area or high-humidity applications, crosslinkers such as glyoxal, aluminium chloride, or other approved reactive additives must be evaluated. Crosslinker addition changes pot life and pH; the batch should be checked for viscosity stability over 24 h and for gel fraction or solvent swell ratio if water resistance is claimed.

    In textile and nonwoven binder applications, high-ethylene VAE is applied by padding, spray bonding, or saturation. The lower glass transition temperature contributes to soft hand and low-temperature flex resistance, but dry and wet tensile strength should be measured per ISO 9073-3 and compared with the substrate specification. The emulsion is not a self-crosslinking binder unless a crosslinking monomer or external crosslinker is present; producers should be consulted for low-formaldehyde grades where textile certification is required.

    Product handling follows standard waterborne polymer practice: use stainless steel, HDPE, or lined carbon steel tanks; avoid copper and brass fittings that can generate metal ions and accelerate destabilization; protect from freezing; and maintain mild agitation in storage to prevent separation.