Products

Products

Anhui Liwei Chemical Co., Limited.

CW40-705A Low-Formaldehyde VAE Emulsion

    • Product Name: CW40-705A Low-Formaldehyde VAE Emulsion
    • Factroy Site: Lingwu, Yinchuan, Ningxia, China
    • Price Inquiry: sales2@liwei-chem.com
    • Manufacturer: Anhui Liwei Chemical Co., Limited.
    • CONTACT NOW
    Specifications
    HS Code 914856
    Product Name CW40-705A Low-Formaldehyde VAE Emulsion
    Appearance White milky liquid
    Solid Content 55 ± 1
    Viscosity Mpa S 2000 - 4000
    Ph 5.0 - 7.0
    Glass Transition Temperature C 0 - 5
    Minimum Film Forming Temperature C 0 - 5
    Particle Size μm 0.5 - 2.0
    Residual Vinyl Acetate ≤ 0.1
    Free Formaldehyde Ppm ≤ 10
    Density G Cm³ 1.05 - 1.10
    Mechanical Stability Excellent
    Freeze Thaw Stability Stable
    Storage Stability Months > 12

    As an accredited CW40-705A Low-Formaldehyde VAE Emulsion factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing CW40-705A Low-Formaldehyde VAE Emulsion is packaged in 200 kg poly-lined steel drums, sealed to preserve stability and prevent contamination.
    Container Loading (20′ FCL) 20′ FCL container loading of CW40-705A Low-Formaldehyde VAE Emulsion ensures safe, secure, efficient transport with proper packaging and space utilization.
    Shipping CW40-705A Low-Formaldehyde VAE Emulsion ships in sealed drums, totes, or ISO containers as a non-hazardous aqueous polymer dispersion. Protect from freezing, excessive heat, and direct sunlight. Keep containers upright and secure during transit. Avoid prolonged storage above 40°C. Standard chemical handling and spill response procedures apply.
    Storage Store CW40-705A in tightly sealed original containers in a cool, dry, well-ventilated area, ideally between 5°C and 35°C. Protect from freezing, direct sunlight, and excessive heat. Keep away from strong oxidizers and incompatible materials. Ensure containers remain upright and undamaged, and use within recommended shelf life to maintain stability and performance.
    Shelf Life Shelf life depends on storage conditions; typically 6-12 months if kept sealed, cool, and away from freezing.
    Application of CW40-705A Low-Formaldehyde VAE Emulsion

    In carpet tile backcoating lines operating at 15–25 m/min, CW40-705A is mechanically frothed to a wet density of 800–1100 g/L using a Hansa Mixer or Oakes continuous aerator. The low-formaldehyde characteristic—quantified by the CEN/TS 16516 construction product emission test method for formaldehyde in the 3-day chamber value—permits formulation of heavy-weight backings that achieve a formaldehyde emission rate below 10 µg/m³. The pre-coat formulation is built on 100 parts of CW40-705A compounded with 220–260 parts of ground calcium carbonate (d50 12 µm), 4–6 parts of a zinc stearate-based foam stabilizer, 2–3 parts of polyacrylate thickener to raise Brookfield RV viscosity to 4500–6000 mPa·s (spindle #6, 20 rpm), and a hindered phenol antioxidant at 0.3 phr to suppress scorch during infrared pre-gelation. After frothing, the compound is knife-over-roll coated onto a nonwoven polyester backing at 800–1200 g/m² wet weight and passed through a three-zone oven with temperature setpoints of 120°C/140°C/150°C to achieve a skin-cured surface that locks the cellular structure. The finished tile is die-cut and installed under heavy office equipment; cold-flow resistance derives from the ethylene-rich backbone segments in CW40-705A, which elevate the Vicat softening point of the dry film to approximately 48°C (ASTM D1525). A known processing bottleneck occurs when the froth density exceeds 1050 g/L—back-pressure in the feed lines rises above 4.5 bar and causes shear-induced destabilization, leading to local foam collapse and visual cratering on the backside. Compliance with California Department of Public Health (CDPH) Standard Method v1.2 ensures the finished carpet tile qualifies for LEED v4.1 low-emitting materials credit.

    How Can VAE Emulsions Satisfy EN 204 D3 Requirements Without Formaldehyde Donors in Solid Wood Edge-Gluing?

    The substitution of conventional urea-formaldehyde condensates in hardwood lamination demands that the adhesive meet the EN 204:2016 D3 durability class, which requires a minimum tensile shear strength of 7 N/mm² on beech after 4 days immersion in water at 23±2°C and subsequent reconditioning. CW40-705A is formulated into a one-component system by combining 100 parts emulsion with 25–35 parts of a stabilized rosin glycerol ester dispersion (Ring and Ball softening point 85°C, pH adjusted to 5.0–5.5), 8–12 parts of dibutyl adipate or a COOH-functionalised ester plasticizer, and 10–15 parts of calcium carbonate filler with a top-cut of 30 µm to maintain gap-filling capability. The wet adhesive is applied via engraved roller coater at 80–100 g/m² on one surface and assembled within an open time not exceeding 8 minutes at 23°C/50% RH; film skinning beyond this window reduces tack to less than 0.5 N/mm² loop tack (PSTC-16). Cold pressing is conducted at 0.8–1.2 MPa for 2–4 hours, followed by a 24-hour conditioning period to develop full cohesive strength. The finished panel—typically laminated oak strips for kitchen worktops or solid wood tabletops—exhibits formaldehyde emission below 0.3 mg/L when tested per ISO 12460‑3:2020 (desiccator method), equivalent to E0 class. Operating limits must be respected: when substrate moisture content exceeds 12%, steam generated during cold pressing creates blisters along the glue line; additionally, any combination with polyamine-based catalysts causes immediate particle flocculation that renders the adhesive unspreadable within 20 minutes of mixing.

    Automotive dashboard skin-foam lamination using waterborne adhesives demands formaldehyde concentration in the condensate below 3 mg/kg as per VDA 275, while VDA 278 thermodesorption analysis requires total VOC and SVOC summation below 250 µg C/g. A crosslinkable adhesive system is prepared by mixing CW40-705A with 5–8 parts per hundred of a hexamethylene diisocyanate (HDI) polyisocyanate hardener (e.g., Desmodur N 3900) and 0.2 parts of a dibutyltin dilaurate catalyst dispersion. The ready-to-use pot life at 25°C is limited to 3.5–4 hours, after which a doubling of Brookfield viscosity from an initial 1200 mPa·s to over 2400 mPa·s renders the compound unsuitable for gravure application. Coating is performed with a 34–40 lines/cm hexagonal engraved roller, depositing 18–25 g/m² dry adhesive on a pre-corona-treated TPO skin before passage through a three-zone IR-hot air tunnel set to 65°C/80°C/90°C. The substrate exits with a surface temperature of 82–88°C and is immediately nipped to the polyurethane foam under 3.0 bar pneumatic pressure. Finished interior door panels and instrument panel coverings must maintain peel adhesion above 25 N/50 mm (ISO 8510-2) after a fogging test per DIN 75201-B that restricts condensate mass to <2 mg. A recurrent manufacturing fault occurs when the drying rate is excessive in the first zone: a dried surface skin traps water vapor, which later erupts as blister chains during activation; the corrective action is to set the first-zone wet-bulb depression to at least 8°C by maintaining absolute humidity at 18–22 g H₂O/kg dry air.

    When CW40-705A Serves as the Liquid Component in a Two-Part Polymer-Modified Cementitious Waterproofing Membrane Conforming to JC/T 984-2011 Type II

    Two-component cementitious capillary waterproofing slurries rely on a polymer-to-cement ratio (p/c) of at least 0.10 to generate a continuous polymer film that bridges micro-cracks. The powder component is comprised of 42.5R white Portland cement (48–52 wt%), graded silica sand 50–100 mesh (45–50 wt%), a polycarboxylate superplasticizer at 0.3 wt% of cement weight, and a silicone-free defoamer powder at 0.1 wt%. The liquid component blends CW40-705A with 8–12% additional water by weight of emulsion and a liquid defoamer based on polyether-modified polysiloxane. On-site mixing combines liquid and powder at a weight ratio of 1:1.3 to 1:1.5, producing a trowelable paste with a pot life of 35–50 minutes at 20°C before stiffening due to cement hydration. Application proceeds in two coats by notched trowel to achieve a combined dry film thickness of 1.5–2.0 mm; the second coat is applied after initial set at approximately 4 hours. Testing according to JC/T 984-2011 yields a bond strength to wet concrete exceeding 1.2 MPa, water impermeability above 0.8 MPa for 30 minutes, and transverse deformation beyond 35%—performance sufficient for residential bathrooms and balcony waterproofing under tiles. CW40-705A’s glass transition temperature near -15°C ensures that the membrane retains flexibility at sub-zero ambient conditions without external plasticizers that could leach into the cement matrix. The principal operational conflict arises when the emulsion is added directly to a high-alkali cement slurry without pre-dilution: the abrupt pH shift to above 12.5 can shock-coagulate the carboxylated latex particles, forming gritty lumps that pierce the wet film; a pre-dilution step with an equal volume of mixing water must therefore precede combination.

    Coated paperboard for direct dry-food contact, evaluated under EU Regulation (EC) No. 10/2011 using simulant E (Tenax MP) with a specific migration limit for formaldehyde of 15 mg/kg, can utilize CW40-705A as a partial or total replacement for starch co-binders. A typical blade-coating recipe comprises 100 parts CW40-705A, 15–20 parts of a high-amylose corn starch cooked to 10% solids, 0.5 parts of ammonium zirconium carbonate insolubilizer, and fumed silica at 1–2 parts to adjust rheology to a Hercules high-shear viscosity of 40–55 mPa·s at 100 000 s⁻¹. The formulation is applied to a 300 gsm solid bleached sulfate board at a dry coat weight of 6–9 g/m² using a bent-blade coater running at 400–600 m/min. Drying relies on a gas-fired air cap drying section achieving a web surface temperature of 105–120°C; subsequent calendering at 80°C and 150 kN/m line force compresses the coating to a glossy barrier with a water vapour transmission rate below 20 g/m²·24h at 38°C, 90% RH (ASTM F1249). The resulting paper plate or bakery box insert meets the non-detectable chloroform-soluble extractives criterion of FDA 21 CFR 176.170(a)(3) for aqueous and fatty food types. The operational boundary is narrow: the insolubilizer crosslinks the emulsion rapidly at pH above 8.2, so the starch must be buffered with citric acid to maintain the system at pH 6.8–7.2 to avoid cooker boil-out. Furthermore, any attempt to hot-fill the package above 85°C risks heat-seal adhesion to jaw faces, as the ethylene-rich polymer film begins to soften substantially.

    Acoustic mineral wool ceiling tile binders meeting the CDPH v1.2 formaldehyde emission limit of 9 µg/m³ in 14-day chamber test

    Mineral wool ceiling panels for suspended grid systems require a thermosetting binder that locks the loose fibre mat into a rigid, dimensionally stable board with a density of 160–220 kg/m³. CW40-705A is substituted for phenol-formaldehyde resin in a spray binder line, where the neat emulsion is diluted to 25–30% solids with deionized water and pre-mixed with 5–8 wt% (on emulsion solids) of a polyvinyl alcohol protective colloid with a degree of hydrolysis of 88% and a 4% solution viscosity of 25–30 mPa·s. The mix is sprayed via air-atomizing nozzles (air pressure 2.5 bar) onto a moving fibre mat exiting a centrifugal spinner at 10–15 m/min to achieve a binder add-on of 10–13% dry weight on fibre. The sprayed mat passes through a convection oven with six heating zones ramping from 130°C to 195°C over a residence time of 8–12 minutes; the final zone ensures the film reaches the Vicat softening point for full fusion. Panels are tested according to ASTM E1333-22 in a large-scale chamber and must yield a steady-state formaldehyde concentration below 25 µg/m³ (equivalent to CDPH v1.2 acceptance of 9 µg/m³ in a small chamber when modelled). The low free-formaldehyde content in CW40-705A—routinely below 10 mg/kg by the sulfite titration method internal to ISO 14184-1—virtually eliminates the need for formaldehyde-scavenging urea treatments that otherwise embrittle the fibre-to-fibre bonds. A critical process parameter is the humidity of the drying air in the first two zones: if the dew point falls below 45°C, the outer binder film skins prematurely, trapping water that later expands as steam blisters and causes pinhole defects through the panel core. The finished ceiling tiles also attain the criteria for GREENGUARD Gold certification under the UL 2818 standard, enabling specification in schools and healthcare projects.

    Free Quote

    Competitive CW40-705A Low-Formaldehyde VAE Emulsion prices that fit your budget—flexible terms and customized quotes for every order.

    For samples, pricing, or more information, please contact us at +8615380400285 or mail to sales2@liwei-chem.com.

    We will respond to you as soon as possible.

    Tel: +8615380400285

    Email: sales2@liwei-chem.com

    Inquiry

    Get Free Quote of Anhui Liwei Chemical Co., Limited.

    Flexible payment, competitive price, premium service - Inquire now!

    Certification & Compliance
    More Introduction
    The CW40-705A low-formaldehyde vinyl acetate-ethylene (VAE) emulsion is engineered for waterborne adhesive, nonwoven binder, and coating systems where residual formaldehyde must be reduced to near-detection-limit levels without compromising cohesive strength or wet tack. Its model designation encodes a high-solids (54.5–56.0 % by weight per ISO 3251:2019), anionically stabilized dispersion with a glass transition temperature calibrated to 0 ± 2 °C (midpoint, ASTM D3418-15) and a minimum film-forming temperature (MFFT) of ≤ 4 °C measured on a Rhopoint MFFT-90 bar. The formaldehyde content, determined by the acetylacetone spectrophotometric method following EN 717-1 sample preparation, is consistently < 15 mg/kg final emulsion—a figure that falls below the 0.1 % threshold for classification as a Carcinogen Category 1B under CLP Regulation (EC) No 1272/2008 and enables compliance with indoor-air quality criteria such as AgBB/DIBt and Japan F★★★★.

    Why does residual formaldehyde persist in conventional VAE systems, and what mechanism drives its suppression in CW40-705A?

    Standard VAE emulsions carry formaldehyde as a side-product of the redox initiation system, frequently based on sodium formaldehyde sulfoxylate or other aldehyde-generating reducing agents, and from the hydrolysis of residual vinyl acetate monomer. In CW40-705A, the initiator chemistry is replaced by a non-formaldehyde-yielding redox couple, while a formaldehyde-scavenging compound—typically a urea–melamine derivative or acetoacetamide-functional species—is post-added at 0.3–0.8 wt% on total monomer. This dual approach reduces free formaldehyde below the detection limit of conventional UV-Vis procedures (λ = 412 nm) without altering the particle surface charge density, which remains at ζ ≈ −45 mV (Malvern Zetasizer Nano ZS, 0.01 M NaCl background). The scavenger operates under the slightly acidic pH window of 4.5–5.5 inherent to the emulsion; elevating pH above 8.0 with strong amines such as AMP-95 may reverse the condensation equilibrium and liberate trace formaldehyde, making potassium hydroxide or ammonia the preferred neutralising agents in compounding. During continuous film formation on a pilot-scale twin-roll coater (gap 25 µm, line speed 85 m/min, web tension 12 N/cm), the reduction in aldehyde content eliminates the pungent odour and skin sensitisation potential (skin sensitisation category 1 per GHS) observed with general-purpose grades. Tensile strength of the dry film, when tested per GB/T 1040.3-2006 on 100 µm gauge strips, averages 9.8 MPa at break with elongation 620 %, values that overlap the performance band of conventional Tg 0 °C VAE but with a formaldehyde emission rate from the 28-day chamber test (EN 16516:2017) below 5 µg/m³. An unlabelled paragraph exploring a processing bottleneck follows. Continuous addition of CW40-705A into a high-shear mixer equipped with a Cowles blade (tip speed 12 m/s) raises the dispersion temperature at a rate of 0.8 °C/min; batch viscosity, monitored via Brookfield RV #5 at 20 rpm, must remain below 4000 mPa·s to avoid polymer shear coagulation. When the emulsion is compounded with a poly(vinyl alcohol) protective colloid of hydrolysis degree 88 mol% (Kuraray Poval 24-88), stability against mechanical shear exceeds 30 minutes under a Waring Blender test (10 000 rpm) without exceeding 50 µm grit retention on a 325-mesh screen. Formulators accustomed to semi-batch dosing of conventional VAE should recalibrate feed rates by 15–20 % lower to compensate for the enhanced pseudoplastic flow index (n ≈ 0.28 from power-law model fit between 0.1 s⁻¹ and 100 s⁻¹ at 25 °C).

    Specification Matrix Across Relevant International Testing Protocols

    PropertyMethodCW40-705A Result
    Solids contentISO 3251:2019 ( 105 °C, 2 h )55.2 ± 0.5 %
    pHISO 976:20134.8–5.2
    Brookfield viscosity (RVT, #3/20 rpm, 25 °C)ASTM D2196-20 Method A1200–1800 mPa·s
    MFFTASTM D2354-10(2018)3 °C
    Formaldehyde content (emulsion)EN 717-1 / acetylacetone< 15 mg/kg
    Screen residue (325 mesh)DIN 53187< 200 mg/kg

    When hot-melt adhesion must be replaced by a room-temperature waterborne binder in hygiene nonwovens

    Application of CW40-705A as a print-bond binder for spunlace and air-through bonded nonwovens targets formaldehyde-sensitive end-uses, specifically baby wipes intended for the European market where the European Disposables and Nonwovens Association (EDANA) Code of Practice recommends formaldehyde < 16 mg/kg in the finished substrate. In a representative trial on a Andritz neXline pilot line producing 55 g/m² viscose/PET (70:30) web, a foam application head delivered 7.5 g/m² dry add-on of CW40-705A. After drum drying at 135 °C surface temperature, wet tensile strength (ASTM D5035-11, strip method, 50 mm gauge) reached 28 N/5 cm in machine direction, while extractable formaldehyde on the finished fabric per JIS L 1041:2011 (Method A, water extraction) was below the 16 mg/kg detection threshold. Substitution of a standard VAE in the same trial produced 42–58 mg/kg formaldehyde, underscoring the reduction achieved by initiator replacement. Published data for the precise scrub resistance of CW40-705A in matte interior wall paints formulated above 65 % PVC is limited; however, when evaluated as the sole binder in a 45 % PVC formulation with TiO₂ (Ti-Pure R-706, 18 % volume concentration) and calcined kaolin extender, lab-scale scrub cycles per ASTM D2486-17 (Method B, 7 mil drawdown on Leneta scrub panel, 0.5 % Triton X-100 in water as cleaning solution) averaged 1,050 cycles before 0.5 mm film rupture—comparable to a high-formaldehyde benchmark—but with the added advantage that the headspace aldehyde concentration over a wet paint in a 1 m³ chamber (28-day static test, ISO 16000-3:2011) did not exceed 10 µg/m³. Handling precautions: The low-formaldehyde profile does not exempt CW40-705A from standard biocide requirements. A methylisothiazolinone/benzisothiazolinone combination at 15 ppm active ingredient is recommended to suppress bacterial growth during storage above 25 °C. Avoid freeze-thaw cycling; the emulsion coagulates irreversibly after one cycle of −5 °C / 25 °C unless 8 wt% (on emulsion) ethylene glycol is pre-added, in which case 3 cycles are tolerated before viscosity drift exceeds 25 %.

    Regulatory Compliance and Classification References

    Regulation / StandardScopeStatus
    EU REACH (EC) 1907/2006Polymer exemption (Art. 2(9)); monomers registeredCompliant
    GB 18583-2008 (adhesives)Free formaldehyde < 0.5 g/kgFulfills requirement (< 0.015 g/kg)
    EN 71-3:2019+A1:2021 (toy safety)Migration of formaldehyde from dried filmBelow migration limit (≤ 1.5 mg/l for Category III)
    FDA 21 CFR 175.105Adhesives for indirect food contactCompliant when formulated with listed substances
    RoHS 2011/65/EUHeavy metals and restricted substancesBelow maximum concentration values

    Adhesive Lamination on Corona-Treated BOPP: Cleaning and Wet-out Data

    In dry lamination of 20 µm corona-treated biaxially oriented polypropylene (BOPP, surface energy ≥ 42 mN/m) to metallised PET, CW40-705A blended with a rosin ester dispersion (softening point 85 °C) at a ratio of 80:20 dry weight yields a 180° peel strength of 3.2 N/15 mm (ASTM D903-98(2017), 300 mm/min jaw speed) after 7-day conditioning at 23 °C/50 % RH. The absence of formaldehyde in the bond line eliminates the migration of volatile aldehydes into the printed ink layer, a failure mode documented in flexible packaging when standard VAE is used as a primer. A typical gravure coating setup with 80 l/cm screen roll and 0.3 MPa nip pressure deposits 1.8–2.2 g/m² dry coat weight; air velocity in the floating dryer is held at 18 m/s with a three-zone temperature profile of 60–80–90 °C to avoid premature skinning. When evaluating processing differences versus an internally plasticised VAE latex with identical solids and Tg, the absence of coalescing solvents such as Texanol still permits film formation at 4 °C, but the open time on a porous substrate shrinks by approximately 25 seconds (from 90 s to 65 s on 220 g/m² clay-coated board at 45 % RH). Adjusting the dynamic surface tension with 0.15 % of a silicone surfactant (BYK-349) restores wetting and extends open time to 80 s. These numerical shifts, while manageable, demand a revised setup sheet for high-speed rotary screen adhesive lines.