| HS Code | 544635 |
| Product Name | CW FS-II VAE Emulsion for Flexible Substrates |
| Chemical Base | Vinyl Acetate-Ethylene Copolymer |
| Appearance | Milky white liquid |
| Solid Content | 55 ± 1% |
| Viscosity | 3000-6000 mPa·s |
| Ph | 4.5-6.5 |
| Particle Size | 0.2-1.0 μm |
| Glass Transition Temperature | 0°C |
| Minimum Film Forming Temperature | 5°C |
| Density | 1.05 g/cm³ |
As an accredited CW FS-II VAE Emulsion for Flexible Substrates factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | CW FS-II VAE Emulsion is supplied in 200 kg drums or 1000 kg IBC totes, sealed for safe transport. |
| Container Loading (20′ FCL) | CW FS-II VAE Emulsion for Flexible Substrates is loaded in a 20′ FCL, using flexitanks or drums for safe, efficient transport. |
| Shipping | CW FS-II VAE Emulsion ships in sealed drums or IBC totes, protected from freezing and extreme heat. Use dedicated or properly cleaned equipment; avoid contact with incompatible materials. Standard non-hazardous chemical transport applies, but confirm local regulations. Secure loads upright, label clearly, and provide SDS to carrier. |
| Storage | Store CW FS-II VAE Emulsion in its original, tightly sealed container in a cool, dry, well-ventilated area away from direct sunlight and heat sources. Avoid freezing; maintain temperatures between 5°C and 35°C. Keep away from incompatible materials. Use within recommended shelf life and stir gently before use if needed. |
| Shelf Life | Store in a cool, dry place away from frost. Unopened shelf life is typically 12 months from manufacture date. |
In high-speed diaper converting lines operating at 400–600 ppm (pieces per minute), leg cuff nonwovens are adhesively bonded to PE backsheet using slot-die coating or controlled-spray systems. CW FS-II VAE emulsion, due to its mechanical stability under shear rates exceeding 10,000 s⁻¹, maintains a low foam profile when recirculated through a Nordson FP-200 or similar hot melt-alternative slot applicator retrofitted for waterborne adhesives. The neat emulsion is adjusted to a viscosity of 800–1200 mPa·s (Brookfield LV, #3@20 rpm) by dilution with deionized water up to 5% and its pH buffered to 4.5–5.0 with ammonium hydroxide to preserve colloidal stability. Target add-on is 2.8–3.5 g/m² dry, which correlates to a wet film thickness of 18–22 µm when applied at the recommended solids of 50±2%. Skin-contact safety is validated per OEKO-TEX Standard 100 Annex 4 (Product Class I for baby articles) and ISO 10993-5 cytotoxicity screening for any residual monomers. Process bottleneck: in through-air drum dryers at 130–140°C, insufficient dwell time—less than 2.5 s—leads to incomplete film formation, evidenced by a drop in crease resistance peel strength below 0.8 N/25 mm (measured per WSP 401.1). The resulting bonded composite becomes the leg cuff elastic attachment zone of open-style baby diapers, a component that undergoes cyclic elongation during wear without cohesive failure.
A common failure in blackout curtain backcoatings is the “paper feel” caused by high-modulus acrylic binders that suppress fabric drape. CW FS-II VAE, with a measured Tg of approximately -10 °C (DSC, mid-point), imparts a perceptibly softer handle that approaches the flexibility of plasticized PVC without the monomer migration risk. The coating compound is prepared by dispersing 100 parts (wet) of the emulsion with 120–150 parts of ground calcium carbonate (D50 5 µm), 3–5 parts of polyacrylate thickener, and 1 part of defoamer, resulting in a paste viscosity of 20–30 Pa·s (Brookfield RV, #6@2.5 rpm). This formulation places the dry binder content at approximately 55–65 wt% of the coating. Fire safety compliance for contract upholstery and curtains mandates passing the BS 5867-2:2008 Type B performance specification in combination with a halogen-free phosphorous-nitrogen synergist added at 8–12 phr. During knife-over-roll coating on polyester warp-knit scrim at line speeds of 15–25 m/min, the wet thickness is held at 120–150 µm; forced-air drying at 110–130°C for 3–5 min removes water and initiates vinyl-acetate crosslinking if a blocked acid catalyst is present. The finished roll is calendered to embed the coating into the fabric interstices. End products include hotel drapery liners, room dividers, and projection screen surfaces, where the coated textile must survive repeated folding without cracking.On the secondary-backing application deck, carpet mills push calcium carbonate loading to reduce cost, yet at a filler-to-binder dry weight ratio beyond 4:1, CW FS-II VAE precoat compounds exhibit a sharp drop in tuft bind strength measured per ISO 4919. The emulsion is compounded with 350–450 parts of untreated whiting (mean particle size 10 µm) per 100 parts of emulsion at 53% solids, resulting in a dry binder fraction of only 12–16 wt% within the filled coating. The precoat is mechanically foamed to a cup weight of 200–300 g/L using an Oakes or Hansa foam generator with air pressure regulated to 0.3–0.5 bar, and applied via a parabolic foam roller onto the back of tufted nylon 6,6 loop-pile greige goods at a wet add-on of 600–800 g/m². Because CW FS-II’s carboxylation level increases its interaction with calcium ions from the filler, the colloidal stability remains adequate; otherwise, premature coagulation generates pinholing in the foam coat. Compliance with the Carpet and Rug Institute CRI Green Label Plus program is documented by demonstrating total volatile organic compound (TVOC) emissions below 0.5 mg/m³ after 14 days in chamber testing per ASTM D5116 and California Section 01350. After drying in a three-zone oven with zone temperatures of 120 °C, 140 °C, and 110 °C, the precoat is laminated with a polypropylene Action Bac® or synthetic latex unitary backing. Finished carpet tiles and broadloom produced from this process must sustain heavy rolling traffic without edge fraying or fiber loss, and are specified in commercial office environments under the LEED v4.1 Low-Emitting Materials credit.
Attempts to formulate permanent pressure-sensitive adhesives directly from VAE emulsions often result in a steep trade-off between loop tack and cohesive strength. When CW FS-II is compounded with a hydrogenated rosin ester dispersion (softening point 85 °C, acid value 12 mg KOH/g), a tackifier loading above 30 parts per hundred parts of emulsion solids shifts the failure mode to cohesive split; accelerated aging at 40 °C for 1 week reduces the 180° peel adhesion to stainless steel (measured per ASTM D3330 Test Method A) by more than 50%. The optimized formulation maintains tackifier at 25–30 phr on dry weight, with CW FS-II providing 65–70% of the binder solids. The roll-to-roll transfer coating process begins with a 25 µm wet film deposited on a silicone-coated release liner (PET film; release force 5–10 cN/25 mm) by comma blade, then dried in zones of 80 °C, 105 °C, and 95 °C to a final dry adhesive thickness of 28–32 µm. The adhesive film is laminated to a spunlace nonwoven carrier (basis weight 40 g/m²) at a nip pressure of 2 bar. Biocompatibility of the dried adhesive is verified under ISO 10993-5 (MEM elution, L929 cells) and USP Class VI (121 °C extraction), supporting claims for skin contact up to 30 days. The finished product is slit into 2.5 cm-wide rolls and used as surgical drape fixation strips and wound dressing border tapes, where the film must maintain skin adhesion without leaving residue upon removal.The following table collates the performance thresholds and corresponding international standards referenced across the described application environments.| Downstream Application | Critical Performance Parameter | Test Standard & Minimum Threshold |
|---|---|---|
| Flexible Packaging Lamination | T-peel bond strength (BOPP/paper) | ASTM D1876 – min. 2.0 N/15 mm |
| Hygiene Nonwoven Leg Cuff | Crease resistance at 30 % extension | WSP 401.1 – peel force ≥ 0.8 N/25 mm |
| Blackout Curtain Backcoating | Fire behaviour (Type B) | BS 5867-2:2008 – char length ≤ 150 mm |
| Carpet Precoat | Tuft bind | ISO 4919 – ≥ 4.5 kg for heavy-contract |
| Medical Tape PSA | Peel adhesion to stainless steel | ASTM D3330 Method A – 3.0–5.0 N/25 mm; ISO 10993-5 cytotoxicity ≤ Grade 2 |
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CW FS-II is a high-ethylene-content vinyl acetate–ethylene (VAE) copolymer emulsion, colloidally stabilised and supplied at a nominal solids level of 55 ± 1% (ISO 3251). The polymer backbone, with an ethylene incorporation of approximately 15–20 wt% (internal FTIR calibration), permanently depresses the glass transition temperature to −15 °C (DSC, midpoint, ISO 11357‑2) and reduces the minimum film formation temperature to below 0 °C (ISO 2115, white point method). These physical characteristics permit film coalescence at ambient temperature without the addition of volatile coalescing agents or external plasticisers. The emulsion is preserved with a formaldehyde-free biocide package and exhibits a pH of 4.5–5.5; Brookfield RVT viscosity (spindle 3, 20 rpm, 25 °C) is maintained within 1 500 – 3 000 mPa·s. The copolymer’s inherent film flexibility, low odour, and adhesion to a broad range of polar and non-polar surfaces position CW FS-II as a primary binder for flexible substrates that demand plasticiser-free compliance and robust mechanical integrity under dynamic flexural stresses.
In vinyl acetate–ethylene copolymers, the ethylene moieties act as an internal plasticiser, increasing free volume and chain mobility. This structural effect is directly responsible for the shift in balance between cohesive strength and surface wetting. At the 15–20 wt% ethylene level incorporated in CW FS-II, dynamic mechanical analysis (DMA, 1 Hz, tensile mode) shows a tan δ maximum at −10 °C, indicating that the material dissipates energy efficiently at ambient and sub‑ambient temperatures while retaining sufficient cohesive modulus for fibre-to‑fibre or film‑to‑film bonds. For comparison, a lower-ethylene VAE grade (CW FS‑I, ethylene content approx. 8–12 wt%) yields a Tg near +5 °C and an MFFT of +8 °C; the resulting films are stiffer and require thermal activation during lamination, typically above 90 °C.
On surface‑modified polyethylene terephthalate (PET) film, CW FS‑II delivers a 180° peel adhesion of 2.8 N/25 mm (ASTM D903, coat weight 25 g/m² dry, dried 3 min at 80 °C) and a loop tack value of 3.2 N/25 mm (PSTC‑16, identical coating conditions). The failure mode is cohesive within the adhesive layer, confirming an optimised adhesion–cohesion equilibrium. When the ethylene content is increased beyond 25 wt% (experimental benchmarks), tack values rise above 5 N/25 mm but the shear holding power (PSTC‑107, 1 kg load) drops below 1 h, indicating excessive cold flow that causes blocking in roll‑fed converting lines. Conversely, grades with less than 10 wt% ethylene require substantial coalescing solvents to achieve film integrity at 23 °C, elevating volatile organic compound (VOC) release during drying. Thus the ethylene‑segment window employed in CW FS‑II is the calibrated point where ambient‑temperature film formation, cohesive safety, and low‑VOC operation intersect.
| Property | Test Method | CW FS‑I | CW FS‑II |
|---|---|---|---|
| Solids content | ISO 3251 (2 h, 105 °C) | 55 ± 1% | 55 ± 1% |
| pH | ISO 976 | 4.5–5.5 | 4.5–5.5 |
| Brookfield viscosity | ISO 2555 (spindle 3, 20 rpm, 25 °C) | 2 000–4 000 mPa·s | 1 500–3 000 mPa·s |
| MFFT | ISO 2115 | +8 °C | <0 °C |
| Tg (DSC midpoint) | ISO 11357‑2 | +5 °C | −15 °C |
| Ethylene content (approx.) | FTIR (internal) | 8–12 wt% | 15–20 wt% |
| Peel adhesion on PET (ASTM D903) | coat wt. 25 g/m², dried 3 min/80 °C | 1.8 N/25 mm | 2.8 N/25 mm |
| Loop tack on LDPE (PSTC‑16) | same coating conditions | 1.1 N/25 mm | 3.2 N/25 mm |
On high‑speed nonwoven binder lines operating at web speeds of 100–300 m/min, mechanical shear stability is the primary process discriminant. CW FS‑II, when subjected to the Maron mechanical stability test (ISO 4576, 1 000 rpm for 20 min), generates less than 0.5% sieve residue on a 45 µm mesh, confirming its suitability for rotor‑stator pumps and recirculating saturator baths. Viscosity drift over an 8‑hour production shift remains below ±10% of initial values, provided the bath temperature is kept between 18 °C and 32 °C. Electrolyte tolerance, critical for spunlace lines where water hardness can fluctuate, has been quantified by the calcium‑ion stability test (DIN 53780): addition of 10 mL of 1% CaCl₂ solution to 50 g of emulsion induces no visual coagulum after 15 min of mixing. The static surface tension of the neat emulsion is 38–42 mN/m (Du Noüy ring, ISO 304), which ensures adequate spontaneous wetting onto rayon and cellulosic substrates; for highly hydrophobic fibres such as polypropylene, a non‑ionic wetting surfactant at 0.2–0.5% on wet emulsion weight is recommended, and foam generation is then controlled with a silicone‑free defoamer dosed at 0.05–0.1% to avoid surface‑energy defects in the finished nonwoven.
Conventional plasticised poly(vinyl acetate) adhesives rely on dibutyl phthalate or triacetin to impart film flexibility, thereby posing long‑term migration risks under food‑contact conditions. Substituting CW FS‑II eliminates the plasticiser entirely. On a laminating line combining 40 g/m² kraft paper and a 20 µm corona‑treated polyethylene film, CW FS‑II achieves a bond strength of 4.5 N/25 mm (ISO 11339, T‑peel at 300 mm/min) after 24 h conditioning at 23 °C/50% RH. Under identical coating and drying conditions, a commercial plasticised PVAc (plasticiser content 12%) yields 3.8 N/25 mm. The oven temperature profile can be reduced from the typical 120 °C peak (required for plasticiser‑containing formulations to drive off water and minimise residual plasticiser volatiles) to a maximum of 80 °C, which lowers energy consumption by approximately 20% and reduces the risk of thermal shrinkage of the PE web.
Since CW FS‑II forms a permanently flexible film without migratory additives, the laminate complies with the extractive requirements of FDA 21 CFR §175.105 (indirect food additives) and the specific migration limits of EU Regulation 10/2011 (overall migration <10 mg/dm²). Blocking tendency, a frequent failure mode in roll‑fed packaging, is evaluated by the force required to separate two adhesive‑coated surfaces stored under load. Per ASTM D3916 (contact pressure 0.7 N/cm², 24 h at 35 °C), CW FS‑II exhibits a blocking force of <0.5 N/cm², whereas plasticised PVAc formulations typically measure above 1.2 N/cm². This low blocking characteristic is attributed to the non‑polar ethylene segments that preferentially orient at the film‑air interface during drying, reducing the surface tack without compromising interfacial adhesion.
Application via engraved roll coaters with cell volumes of 12–20 cm³/m² demands a viscosity profile that is stable under the high‑shear conditions at the doctor‑blade nip. Rheometric data (cone‑plate, ISO 3219, 0.1–1 000 s⁻¹) show that CW FS‑II exhibits shear‑thinning behaviour with a power‑law index n of 0.6–0.7. This pseudoplasticity permits a controlled pickup without dripping; at an applied nip pressure of 2–4 bar and a speed differential between applicator and transfer rolls of ±5%, a uniform dry add‑on of 2–4 g/m² is maintained on polyester films. However, if the emulsion is subjected to shear rates exceeding 10 000 s⁻¹—as can occur in poorly sized centrifugal pumps—partial desorption of the protective colloid can trigger micro‑coagulum that manifests as streaks on the coated substrate. Progressive cavity pumps are therefore specified for transfer duties. Additionally, the emulsion should be protected from repeated freeze–thaw cycles; storage below +5 °C can lead to irreversible gelation, and the ideal storage range is +10 °C to +35 °C with a shelf life of 6 months in sealed containers.
VAE copolymers display a broad thermoplastic window that can be exploited for heat‑sealable overprint varnishes and cold‑seal symmetry adhesives. CW FS‑II, coated at 2.5 g/m² dry on corona‑treated biaxially oriented polypropylene (OPP), initiates a measurable seal at 65 °C (JIS Z1707, 1.0 s dwell, 2 bar pressure). The seal strength reaches 3.1 N/25 mm at a jaw temperature of 80 °C and plateaus before declining beyond 140 °C due to thermal softening of the film substrate. Hot tack—the ability to hold a seal while still hot—measured by an Instron‑based method (jaw opening 0.2 s after seal closure, 200 mm/min pull), yields 0.8 N/25 mm at 60 °C seal temperature. This is adequate for vertical form‑fill‑seal packaging where the product drop imposes immediate stress on the still‑warm longitudinal seal. In comparative tests, conventional acrylic‑based pressure‑sensitive adhesives deliver higher ambient tack but show negligible hot tack at 60 °C, requiring additional heat‑seal lacquers.
Process engineers should note that prolonged exposure of the dry film to temperatures above 180 °C initiates deacetylation, evidenced by discolouration and a brittle residue. The practical sealing range is therefore confined to 65–160 °C, and dwell times should not exceed 2 s at the upper limit. On metallised OPP, where the aluminium vacuum‑deposition layer can act as a heat sink, the seal initiation temperature shifts upward by approximately 5 °C, and best results are achieved by pre‑heating the metallised web to 35–40 °C before the seal station. No primer is required, provided the metal surface energy is maintained above 42 mN/m through in‑line corona treatment.
| Standard/Regulation | Requirement/Test | CW FS‑II Status |
|---|---|---|
| FDA 21 CFR §175.105 | Adhesives for indirect food contact; extractives limits | Compliant |
| EU 10/2011 and amendments | Overall migration <10 mg/dm² | Confirmed by independent laboratory (EN 1186‑1) |
| REACH (EC 1907/2006) | SVHC content <0.1% w/w | No substances of very high concern above threshold |
| German BfR Recommendation XIV | Plasticised polymer dispersions for food contact | Applicable; plasticiser‑free nature simplifies declaration |
| ISEGA migration certificate | Specific migration of monomers (vinyl acetate <12 mg/kg) | Pass |
| ISO 14001 / OHSAS 18001 framework | VOC content, emissions during application | VOC <0.1% (ISO 11890‑2), no formaldehyde donor |
| AICS/NZIoC/DSL inventory status | All components listed | Fully inventoried |
In aqueous contact applications, colloidal stability must be maintained in the presence of dissolved multivalent salts. A zinc‑ion tolerance test (addition of 5 mL of 10% ZnSO₄ solution to 50 g emulsion) produces no destabilisation at 25 °C over 24 h, confirming robustness for coatings on zinc‑primed metal foils. However, direct blending with polyamine or polyimine crosslinkers leads to rapid viscosity build and eventual gelling within pot‑life; pH adjustment with ammonia or volatile buffering agents is not recommended, as the elevated pH (>7.5) accelerates ester hydrolysis and shortens wet‑state shelf life. For applications demanding enhanced water resistance, a blocked isocyanate or carbodiimide crosslinker can be post‑added at 0.5–1.0 wt% on polymer solids and must be mixed under low shear immediately before use, with a working pot‑life of 4–6 h at 23 °C.