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Anhui Liwei Chemical Co., Limited.

BJ-705 VAE Emulsion

    • Product Name: BJ-705 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 907069
    Product Type Vinyl Acetate-Ethylene (VAE) Emulsion
    Appearance Milky white liquid
    Solid Content 58-60%
    Viscosity 2500-4500 mPa·s (Brookfield spindle 4, 60 rpm, 25°C)
    Ph 5.0-7.0
    Particle Size 0.5-1.5 μm
    Glass Transition Temperature -7°C
    Minimum Film Forming Temperature 0°C
    Film Appearance Transparent and flexible
    Residual Vinyl Acetate <0.5%
    Density 1.15 g/cm³ at 25°C
    Storage Stability 6 months at 5-40°C, protect from freezing

    As an accredited BJ-705 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 inner packaging to prevent contamination.
    Container Loading (20′ FCL) 20′ FCL container loading of BJ-705 VAE Emulsion: palletized drums secured, moisture-proof, ventilated, labeled, and blocked to prevent shifting.
    Shipping BJ-705 VAE Emulsion ships in sealed drums, IBC totes, or bulk tankers, depending on quantity. Protect from freezing, excessive heat, and direct sunlight. Keep containers upright and well-ventilated during transport. Ensure proper labeling and handling per SDS to prevent spillage and contamination.
    Storage Store BJ-705 VAE Emulsion in its original, tightly sealed container in a cool, dry, well-ventilated area. Maintain temperatures between 5–35°C; avoid freezing. Protect from direct sunlight, heat, and ignition sources. Prevent contamination and skinning by resealing after use. Use within the manufacturer’s shelf life.
    Shelf Life Shelf life is 12 months when stored sealed in original container, protected from frost and direct sunlight.
    Application of BJ-705 VAE Emulsion

    Coalescence Rate and Open Time in Cold-Press Wood Lamination

    BJ-705, a vinyl acetate-ethylene copolymer emulsion delivered at 54–56% solids content, exhibits viscoelastic coalescence behavior suited to waterborne assembly adhesives for solid wood edge-gluing, finger-jointing, and face lamination where cold-press schedules predominate. The formulation route typically blends 85–92% of the emulsion as supplied, mixed with 3–7% of a plasticizer such as triacetin or dibutyl adipate to modulate minimum film formation temperature, 1–2% of a mineral-oil-based defoamer, 0.2–0.5% of a polyurethane associative thickener targeting a Brookfield viscosity of 8,000–15,000 mPa·s (spindle 4, 20 rpm), and 0.1–0.3% of a methylisothiazolinone/benzisothiazolinone preservative system to meet in-can stability requirements under ISO 11930. Compliance is demonstrated against EN 204 classification for non-structural thermoplastic wood adhesives, with an ASTM D 5751-type wet shear test after 4-hour water soak yielding bond strengths exceeding 5.0 MPa on beech substrates, while the stricter EN 12765 creep resistance criteria for service class D3 demand a minimum 1.0 mm pass under 150 N static load at 50 °C. Production-scale application relies on a multi-head curtain coater or a slot-die extrusion system calibrated to deposit 120–180 g/m² wet film weight, followed by an open assembly window of 8–15 minutes at 20 °C and 55% RH; premature skinning is prevented by maintaining application-room humidity below 60% and avoiding forced air velocities above 0.5 m/s across the glue line. The cold-press cycle employs a platen pressure of 0.5–1.0 MPa for 20–45 minutes, and bond strength development as a function of press time has been modelled using a modified Voigt rheological framework—final adhesion correlates with the completion of polymer interdiffusion and with the evaporation of 70–80% of the water fraction into the wood pore structure. Finished articles include laminated hardwood panels for tabletops, laminated veneer lumber beams, and finger-jointed window scantlings destined for interior millwork.

    In low-odor interior wall paints formulated below a pigment volume concentration of 70%, the binder demand is satisfied by the addition of BJ-705 at 13–17% of wet paint weight, a range that balances wet-scrub resistance against raw material cost in retail-grade acrylic/VAE hybrid compositions. The emulsion is post-added to the let-down stage of a high-speed disperser after the TiO₂ slurry has been ground to a Hegman gauge reading of 5–6, and the blend is stabilized with 0.3–0.5% of a sodium polyacrylate dispersant plus 0.2% of an amino alcohol pH buffer to maintain the system at pH 8.0–8.8. Regulatory compliance is governed by the EU Ecolabel for indoor paints (Decision 2014/312/EU) limiting volatile organic compound content below 10 g/L, by the Chinese GB 18582-2020 standard for indoor decorating materials, and by the French VOC labelling class A+ protocol. The formulated paint is applied by airless spray using a 0.017–0.021 inch tip orifice or by microfiber roller at a wet film thickness of 100–150 µm, drying to a 50–75 µm dry film under ambient conditions; scrub resistance per ASTM D2486 Method B typically surpasses 1,200 cycles before film failure when the VAE fraction constitutes at least 60% of the total binder solids. The finished goods are decorative flat and eggshell wall paints packaged in 1–15 L containers for consumer and professional markets.

    How Does BJ-705 Concentration Affect Peel Adhesion in Foil-to-Paper Lamination?

    Converters laminating aluminum foil to coated paper for aseptic beverage cartons and flexible food packaging evaluate adhesive performance via peel strength measured according to ASTM F88 with a 25 mm wide strip pulled at 300 mm/min. BJ-705, when compounded with 0.5–1.5% of a blocked isocyanate crosslinker to enhance heat resistance, is gravure- or smooth-roll coated onto the paper substrate at a dry coat weight of 2.5–4.5 g/m², representing a consumption rate of 4.5–8.0 kg of emulsion per tonne of laminated web. The lamination process sequences through an infrared pre-heat zone evaporating water to a residual moisture content below 2%, followed by a heated nip at 70–85 °C and 1.2–2.0 bar line pressure, where the foil web is introduced and bonded. Adhesion values exceed 250 N/m immediately off-line and, following 72-hour conditioning at 23 °C and 50% RH, routinely surpass 350 N/m with paper fiber tear observed in over 80% of specimens. Compliance with food-contact requirements is substantiated under FDA 21 CFR 175.105 for indirect adhesives and under European Regulation 1935/2004/EC with migration testing conducted per EN 1186-1; additionally, the grade is manufactured without alkylphenol ethoxylates, facilitating REACH Annex XVII compliance. A production-scale validation on a Nordmeccanica Super Simplex laminator running at 180 m/min revealed that transfer-weight variability must be maintained within ±0.2 g/m² to avoid tunneling defects on the foil side, with a wash-up protocol requiring 30-minute solvent-free water flushing to prevent dried emulsion build-up on engraved gravure cells. Finished products include laminated paperboard juice boxes, coffee bag inner liners, and pharmaceutical strip-packaging foil laminates.

    T-peel adhesion of BJ-705 foil-to-paper laminate at varying dry coat weight, tested per ASTM F88 after 24 h conditioning
    Coating dry weight (g/m²)Peel strength (N/25 mm)Failure mode
    2.84.2–5.1Adhesive/foil interfacial failure
    3.56.5–7.8>80% paper fiber tear
    4.38.0–9.2Full fiber tear, limited foil rupture

    Post-added at 0.15–0.25 polymer solids/cement weight ratio, BJ-705 functions as a concrete improver in two-component polymer-modified cementitious waterproofing slurries destined for interior wet areas, balconies, and below-grade tanking. The formulation combines 42.5R ordinary Portland cement, graded silica sand (0.1–0.4 mm), and a cellulose ether rheology modifier dosed at 0.03–0.06% by cement weight, with the emulsion replacing part of the gauging water to maintain a water-to-cement ratio of 0.35–0.42. The slurry is mixed in a forced-action paddle mixer at 100–150 rpm for 3–5 minutes and applied by notched trowel or stiff brush in two coats reaching a cured thickness of 1.5–2.0 mm. Cure commences with 48-hour moist covering at 20 °C and progresses to full hydration over 28 days. Mechanical performance is assessed under JC/T 984-2011: at a polymer solids/cement ratio of 0.20, the flexural bond strength to concrete after 7-day water immersion typically exceeds 1.8 MPa, while water impermeability reaches a positive-side pressure of 0.6 MPa for 30 minutes without leakage. A critical processing threshold exists: increasing the polymer fraction above 0.28 depresses 28-day compressive strength by more than 35% relative to the unmodified mortar, and the initial setting time extends beyond 12 hours, rendering troweling impractical. Conversely, reducing the ratio below 0.12 causes the flexural strength to drop below 1.0 MPa and permits crack bridging capacity to disappear under a 0.5 mm crack opening at 0 °C. Thus, plant-scale batching systems employ gravimetric dosing of the liquid component with an accuracy of ±0.5 kg per 200 kg cement charge, and job-site mixing instructions prohibit the addition of extra water beyond the pre-calibrated volume. The cured membrane constitutes a contiguous, flexible waterproofing layer that is subsequently over-tiled with cementitious tile adhesives.

    Effect of polymer solids/cement ratio (p/c) on polymer-modified cement mortar containing BJ-705 VAE emulsion
    p/c ratioCompressive strength (28 d, MPa)Flexural bond strength (7 d water, MPa)Water impermeability (positive side, MPa)Initial setting time (min)
    0.1038.20.90.2235
    0.1832.51.60.4298
    0.2428.72.20.7385
    0.3020.32.10.6560

    When the Emulsion Integrates into Air-Through Bonded Nonwoven Binder Systems

    In the manufacture of air-through bonded nonwoven webs for facial wipes, industrial wipers, and hygiene top-sheets, BJ-705 is applied at 8–18% dry add-on relative to fiber weight via a foam-impregnation unit operating with a blow ratio of 4:1–6:1 to minimize wet pick-up and reduce drying energy. The binder tank is charged with the neat emulsion, diluted with deionized water to a solids content of 12–20%, and adjusted to pH 4.8–5.2 using a 0.5% solution of citric acid to maintain compatibility with the foam generator’s rotor-stator mixer. A formaldehyde-free crosslinking agent, such as an adipic dihydrazide-based compound, is pre-dispersed at 0.4–0.8% on emulsion solids to raise the wet strength sufficiently to pass the EDANA NWSP 020.1 wet tensile test at ≥20 N/50 mm. Compliance with human safety standards is demonstrated via OEKO-TEX Standard 100 certification under product class I for articles with direct skin contact, with test criteria for formaldehyde below 16 mg/kg and for heavy metals per Annex 4 of the standard. The foam is deposited through a parabolic distributor onto a carded web moving at 60–120 m/min, after which the web enters a through-air drum oven set to 135–150 °C with a residence time of 2.5–4.5 seconds sufficient to lower moisture content to 3–5%. Finished roll goods exhibit dry tensile strengths of 50–70 N/50 mm in the machine direction and a Handle-O-Meter stiffness below 30 g, suitable for conversion into folded wet wipes and spunlace-replacement materials.

    Compression Set and Tuft Lock Are Dictated by the Interaction Between VAE and Calcium Carbonate Fillers in Carpet Pre-coat Compounds

    The pre-coat layer of tufted broadloom carpet, which locks the polypropylene or nylon pile yarns into the primary backing prior to application of a secondary latex or polyurethane foam backing, is formulated with BJ-705 at 22–28% dry weight of the wet compound, corresponding to 40–50% of the liquid emulsion on a total batch weight basis. The compound is loaded with 350–450 phr of ground calcium carbonate (d₅₀ ≈ 4–6 µm), dispersed under high shear in a Cowles blade dissolver to achieve a Hegman grind of 4 NS or better, and then decanted to a mechanical froth mixer where air is incorporated to a target wet density of 0.55–0.75 g/cm³ monitored via an online density flowmeter. The froth is applied by a ribbed roll coater to the reverse side of the greige good at a wet pick-up of 400–650 g/m², calibrated to match the pile height and stitch density, and the carpet passes through a three-zone forced-convection oven with zone temperatures of 110 °C, 140 °C, and 160 °C at a line speed of 8–12 m/min. The curing mechanism relies on evaporation of water and subsequent film formation of the VAE, enhanced by the inclusion of 0.3–0.6% of a polymeric adhesion promoter to improve wet tuft lock; tuft bind strength tested per ASTM D1335 typically exceeds 35 N for loop-pile constructions. Carpet manufacturers targeting the EU market rely on the GUT e.V./CRI Green Label Plus criteria for indoor air emissions, and BJ-705-based compounds deliver total volatile organic compound levels below 0.25 mg/m³ after 24 hours in a 1 m³ chamber per ISO 16000-6. End-use products include contract office carpet tiles, hospitality broadloom, and automotive interior mats where durability under dynamic loading must satisfy ASTM D5252 hexapod tumbler testing for at least 10,000 cycles without significant edge fraying or pile loss.

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    Certification & Compliance
    More Introduction
    BJ-705 VAE Emulsion is a carboxylated vinyl acetate‑ethylene copolymer dispersion stabilized with a poly(vinyl alcohol) protective colloid system. The product is supplied at 55 ± 1 % non‑volatile content (ISO 3251, 105 °C / 2 h), with a pH of 4.0–5.5 (ISO 976) and a Brookfield RVT viscosity of 1500–3000 mPa·s (spindle 3, 20 rpm, 23 °C, ISO 2555). The dispersed phase exhibits a mean particle size of 0.8–1.2 µm (laser diffraction, ISO 13320), and the minimum film‑formation temperature (MFFT) lies below 0 °C (ISO 2115), reflecting a glass transition temperature (Tg, DSC midpoint, ISO 11357‑2) of approximately −5 °C. The ethylene comonomer content, on a dry polymer basis, is 18–22 wt%, imparting permanent flexibility without external plasticizers and a surface energy low enough to wet low‑polarity substrates such as corona‑treated LDPE and polypropylene nonwovens. The residual vinyl acetate monomer is controlled to < 500 ppm (GC headspace, EPA 8260D), and the emulsion is free of alkylphenol ethoxylates (APEO).

    How does the ethylene comonomer ratio alter film mechanics and cohesive strength?

    Raising the ethylene fraction from the range typical of a homopolymer‑modified VAE (8–12 %) to the 18–22 % incorporated in BJ-705 shifts the film from a semi‑rigid thermoplastic to an elastomeric network. Tensile properties measured on films cast and conditioned according to ISO 527‑3 (type 5 specimens, 200 mm/min) show an elongation at break of 600–750 % accompanied by a tensile strength of 4.5–6.5 MPa. By contrast, a conventional vinyl acetate homopolymer emulsion of similar solids content often fractures below 50 % elongation unless externally plasticized. The trade‑off appears in the shear‑resistance domain: the higher ethylene content reduces the storage modulus (G′) above the glass transition, and lap‑shear specimens prepared with BJ-705 on beech (Fagus sylvatica) under EN 204 D2 conditions yield failure adhesion values of 3.2–4.0 N/mm² when formulated as‑is, compared with >5.5 N/mm² obtainable from a homopolymer with a Tg of 30 °C. The internal plasticization mechanism eliminates plasticizer migration, a critical factor in long‑term adhesive bond stability on porous substrates.
    Physical and rheological profile – BJ-705 VAE Emulsion
    PropertyMethodTypical Value
    Solids contentISO 3251 (105 °C, 2 h)55 ± 1 %
    pHISO 9764.0–5.5
    Viscosity (Brookfield RVT, 20 rpm)ISO 25551500–3000 mPa·s
    MFFTISO 2115< 0 °C
    Glass transition temperature (Tg)ISO 11357‑2 (DSC, midpoint)−5 °C
    Average particle sizeISO 133200.8–1.2 µm
    Residual VAc monomerGC‑HS, EPA 8260D< 500 ppm
    APEO contentDIN EN ISO 18254‑1none detected
    In laminated paper‑board packaging, the absence of external plasticizers allows direct contact with fatty and dry foodstuffs without plasticizer extraction (migration testing per EU 10/2011, overall migration < 10 mg/dm²). Converters running air‑knife or rod‑coat lines at line speeds exceeding 150 m/min observe good mechanical stability under recirculation: after 30 min in a high‑shear gear pump loop (Waukesha Cherry‑Burrell, 600 s⁻¹), viscosity loss is typically below 8 %, and micro‑foam generation remains below 2 % of the total volume when defoamer is omitted. The low‑shear viscosity profile makes BJ-705 suitable for roller‑coat applications where a coat weight of 40–60 g/m² (wet) is targeted, because the emulsion does not “crawl” or dewet from clay‑coated board surfaces at application speeds. When formulated with 1.0–1.5 % (on wet weight) of a glyoxal‑based crosslinker, wet rub resistance (ISO 105‑X12, water) improves by a factor of 3 over the uncrosslinked control, while preserving a film elongation above 400 %.

    Where BJ-705 Diverges from PVAc Homopolymer Emulsions – a Comparative Snapshot

    Product differentiation becomes most apparent under conditions of fluctuating ambient humidity. PVAc homopolymer films plasticized with 10–15 % dibutyl phthalate (DBP) lose dimensional stability at relative humidity (RH) above 80 % because water ingress accelerates plasticizer hydrolysis and surface‑blooming. BJ-705 films, containing no external plasticizer, do not exhibit exudation. In high‑frequency wood bonding, assembly‑line trials on a Hess OMS multi‑spindle glue spreader with spruce (Picea abies) lamellas demonstrated that BJ-705, when catalyzed with 3 % aluminum chloride solution (30 % conc.), met the EN 204 D3 durability classification (4 h cold water soak, recovery > 60 % of dry strength), whereas a DBP‑plasticized homopolymer failed due to plasticizer leaching, yielding residual strengths below 2 N/mm². BJ-705 also circumvents the volatile organic compound (VOC) burden associated with coalescing‑solvent‑laden acrylic dispersions, maintaining a VOC content of < 1 g/L (ISO 11890‑2) without the need for Texanol or butyl glycol.

    Open‑time extension without sacrificing heat creep resistance

    On fully automatic edge banding machines (e.g., Homag KAL 310) where hot‑melt polyurethane reactive adhesives dominate, BJ-705 is employed in specialty cold‑press manual operations for curved profiles. The key formulation challenge is balancing open time against heat resistance. Neat BJ-705 exhibits a wet tack time of approximately 4–7 minutes on high‑pressure laminate (HPL) with moisture content < 8 %. Addition of 0.3–0.8 % (w/w dry polymer) carboxymethyl cellulose (low‑viscosity type, DS < 0.9) extends the open phase to 10–12 minutes, allowing repositioning. However, the inclusion of water‑soluble thickeners depresses heat‑resistance temperature (EN 14257, step test) from 65–70 °C to 52–58 °C. To recover performance, a blocked isocyanate dispersed in BJ-705 at 2.5 % on resin solids is preferred; post‑cure (3 days at 40 °C) elevates the heat resistance beyond 80 °C while the thickener‑extended open time is preserved. The emulsion demonstrates high compatibility with a range of water‑dispersible isocyanates and aziridine crosslinkers, but pot‑life constraints demand attention. When mixed with a hydrophilically modified HDI‑trimer (NCO content 19–21 %), the formulation gels within 45–55 minutes at 23 °C, requiring static mixer application and frequent purging on discontinuous layouts. Anhydrous aluminum chloride catalysis avoids the pot‑life cliff but necessitates a forced‑drying station; without thermal activation (> 45 °C for 2 min), crosslinking efficiency drops below 40 %. Textile lamination of nonwoven webs (carded polyester, 30 gsm) using spray‑foam application benefits from the pseudoplastic flow character. Viscosity measured at a shear rate of 1000 s⁻¹ (controlled‑stress rheometer, ISO 3219) remains below 200 mPa·s, enabling fine atomization through nozzle systems operating at 2–3 bar air pressure. Peel strengths on PET nonwoven‑to‑PET film (T‑peel, ASTM D1876, 300 mm/min) reach 2.3–3.1 N/25 mm after 24 h ambient cure, without the “zippy” peel typical of stiff acrylic binders that crack the fiber loops. Published data on low‑denier (< 1 dpf) bicomponent fiber interlaminar bonding confirms that high‑ethylene VAEs like BJ-705 prevent fiber‑tear migration failures seen with vinyl acetate‑VeoVa copolymers, because the adhesive film’s elongation better matches the substrate’s deformation.

    Operational Boundaries and Material Incompatibilities

    Two explicit processing restrictions govern the use of BJ-705 in non‑woven and construction adhesives. First, direct blending with polyamine‑based curing agents (e.g., diethylenetriamine adducts) rapidly causes pH shock and micro‑coagulation because the isoelectric point of the PVOH stabilizer is near pH 3.5, and an alkaline environment above pH 8.5 de‑stabilizes the colloid. Pre‑buffering with citric acid to a pH of 5.8–6.2 is necessary before amine addition. Second, cement‑based tile adhesive formulations should be avoided entirely: the alkaline hydrolysis of the vinyl acetate backbone releases acetate ions that retard alite hydration and can depress 28‑day compressive strength (EN 196‑1) by more than 30 %. Published saponification half‑lives at pH 12.5 and 23 °C indicate significant degradation within 6–8 hours, making BJ-705 unsuitable for hydraulic‑binder modification. The product is fit for cement‑free mastics and waterproofing pastes where it acts as the sole binder, providing crack‑bridging ability (DIN EN 1062‑7, class A4) at dry film thicknesses from 0.5–1.5 mm. When stored in unopened containers at 5–30 °C, the emulsion shows less than 0.5 % sediment after 6 months (ISO 15715), and scraping of bottom‑settle is unnecessary if gentle recirculation is applied for 10 minutes prior to transfer to day tanks.
    BJ-705 versus a lower‑ethylene VAE grade (BJ-704) in a model bookbinding adhesive
    Performance criterionMethodBJ-705 (18–22 % ethylene)BJ-704 (9–11 % ethylene)
    Film elongation at breakISO 527‑3680 %350 %
    Adhesion to biaxially oriented PP (corona 42 dynes/cm)FINAT FTM 1 (180° peel)2.8 N/25 mm0.8 N/25 mm
    Low‑temperature flexibility (mandrel bend, −20 °C)DIN EN 13523‑7no crackinghairline cracks
    Page‑pull strength (coated art paper, 80 gsm, PUR‑bound)Internal method (ISO 1924‑2 adapted)5.2 N/cm4.2 N/cm
    Dry shear on oak (EN 204 D2)EN 2054.1 N/mm²5.8 N/mm²
    Where the process demands high cohesive strength and shear resistance on wood, the lower‑ethylene grade may be preferred; however, BJ-705 is selected when substrate wetting, elongation, and low‑modulus flexibility dominate. Published adhesion tests using flame‑treated polypropylene (contact angle with water < 55°) confirm that BJ-705 provides a critical surface tension overlap without primer, while the lower‑ethylene analog requires an additional chlorinated polyolefin prime coat to reach comparable peel levels. In carpet secondary backing lamination, BJ-705, compounded with 20 wt% calcium carbonate filler (d50 = 8 µm), delivers tuft‑bind strength averaging 6.4 N (ISO 4919), approaching the performance of styrene‑butadiene latexes but without the 4‑phenylcyclohexene odor and with lower total VOC. The emulsion withstands the mechanical work input of a twin‑screw compounder (Werner & Pfleiderer ZSK‑25, L/D 40) at 80 °C barrel temperature without pre‑coagulating, provided the free water content remains > 40 % throughout the processing zone. When higher filler loadings are attempted (> 30 phr), dynamic surface tension constraints cause foaming that requires vacuum de‑aeration of the makedown tank; published recommendations suggest adding 0.15 % by weight of a non‑silicone acetylenic diol‑based defoamer to maintain entrained air below 2 vol%.