Products

Products

Anhui Liwei Chemical Co., Limited.

VAE Emulsion CW FH-Ⅲ

    • Product Name: VAE Emulsion CW FH-Ⅲ
    • Factroy Site: Lingwu, Yinchuan, Ningxia, China
    • Price Inquiry: sales2@liwei-chem.com
    • Manufacturer: Anhui Liwei Chemical Co., Limited.
    • CONTACT NOW
    Specifications
    HS Code 279354
    Product Name VAE Emulsion CW FH-Ⅲ
    Appearance white milky liquid
    Solid Content 55±1%
    Viscosity 1000-1500 mPa·s at 25°C
    Ph 5.0-6.0
    Residual Vinyl Acetate ≤0.5%
    Particle Size 0.5-2.0 μm
    Glass Transition Temperature -5°C
    Minimum Film Forming Temperature 0°C
    Film Tensile Strength ≥8 MPa
    Elongation At Break ≥500%

    As an accredited VAE Emulsion CW FH-Ⅲ factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing VAE Emulsion CW FH-Ⅲ is supplied in sealed 200 kg plastic drums, ensuring safe transport and storage.
    Container Loading (20′ FCL) VAE Emulsion CW FH-III is safely loaded into 20′ FCL containers, ensuring stable transport with proper sealing and temperature control.
    Shipping VAE Emulsion CW FH-Ⅲ ships as a non-hazardous aqueous dispersion in drums, IBC totes, or bulk tankers. Ensure containers are sealed, upright, and protected from freezing or extreme heat. Use sheltered, ventilated transport; handle with standard PPE and avoid leaks during loading and unloading.
    Storage Store VAE Emulsion CW FH-Ⅲ in sealed, original containers in a cool, dry, well-ventilated area away from direct sunlight and heat. Maintain temperatures between 5–35°C to prevent freezing or coagulation. Keep away from strong oxidizers and incompatible materials. Stir gently before use and follow shelf-life guidelines for optimal performance.
    Shelf Life Shelf life: 6 months from manufacture, stored sealed at 5–35°C, protected from freezing and direct sunlight.
    Application of VAE Emulsion CW FH-Ⅲ
    In the formulation of flat and eggshell interior architectural coatings targeting GB/T 9756-2018 Grade I scrub resistance (≥ 5 000 cycles on a 7–8% PVC formulation), CW FH-Ⅲ is incorporated at 15–22 wt% of the total wet paint. The typical manufacturing sequence involves a high-speed disperser (circumferential speed 18–22 m/s) for the pigment grind phase, using a separate let-down vessel where the emulsion is added under low-shear agitation (50–80 rpm anchor stirrer) to avoid shear-induced coagulation. Compliance with GB 18582-2020 low-VOC requirements is achieved without coalescing solvents, given the minimum film-forming temperature of 0 °C; the final dried film conforms to GB/T 9756-2018 for adhesion, contrast ratio, and accelerated weathering. This grade’s moderate carboxylation permits post-addition of associative thickeners to adjust ICI viscosity to 0.12–0.18 Pa·s for roller application. Terminal products are water-based interior wall paints sold under China Environmental Labeling plan Type II, often packaged in 5 L to 18 L pails for the professional applicator market.

    What governs the balance between open time and water resistance in D4 wood bonding?

    When D4 durability classification (EN 204:2016, pass after 4 h boiling water, tensile shear strength ≥ 4 N/mm²) is specified for edge-glued panels and finger joints in solid hardwood, CW FH-Ⅲ is formulated into a two-component system with an aliphatic polyisocyanate crosslinker at 10–15% on wet adhesive weight, yielding an NCO:OH ratio of 1.5–1.8. The working pot life on the shop floor, measured by a Brookfield DV3T #6 spindle at 20 °C, drops from 90 min to 35 min as the crosslinker dose increases—a critical boundary because roller-coater application at 100 g/m² single-side spread requires a minimum of 45 min stable viscosity of 15–25 Pa·s. Adjusting the emulsion’s pH buffer from the as-supplied 4.5–5.5 up to 6.8–7.2 using a sodium carbonate/bicarbonate buffer solution extends pot life by 15–20% without compromising boil resistance, as verified by specimens bonded with 3-layer beech assemblies cured at 20 °C/65% RH for 7 days followed by the EN 204 boiling cycle. The adhesive meets applicable parts of ANSI/HPVA Type I and JIS K 6806 D4, and the finished products are exported as finger-jointed plantation teak bench components for the European DIY retail channel.

    Carpet pre-coat filler loading capacity and coagulation kinetics under foamed coating conditions

    A 1.2 m wide blade-over-roll coater is employed to apply a CaCO₃-filled VAE pre-coat onto tufted polypropylene primary backing at line speeds of 30–45 m/min, depositing a compound loaded with 450–550 phr calcium carbonate (d₅₀ = 5 µm). CW FH-Ⅲ’s carboxylation level, determined by 0.5–1.0 meq/g acid monomer incorporation, provides Ca²⁺ stability that prevents shock-induced grit formation when the filler slurry is injected into the emulsion stream via a static mixer operating under a pressure drop of 0.3–0.5 bar. A thermal shock test on the compounded compound (cycling between 5 °C and 40 °C over 8 h) is requisite to confirm the absence of localised coagulation; formulations falling outside a total solids of 78–82% exhibited visible gel specks at the doctor blade interface, leading to transverse coating streaks detectable under 10× magnification. The dried pre-coat must contain a minimum 15% binder content on filler solids to achieve fibre anchorage values exceeding 12 N (ISO 4919 tuft-withdrawal force). A secondary compounding step incorporates 120 phr alumina trihydrate to meet the IMO FTP Code Part 5 flammability for cruise ship commercial carpet tiles; the coated textile then proceeds to a latex lamination stage with a 1.2 mm thick secondary backing before being cut into 50×50 cm modular carpet tiles for the contract hospitality market.

    When Portland cement challenges latex stability in thin-bed base coats

    Blending CW FH-Ⅲ into a CEM I 42.5R White Portland cement dry mix at 18–25% dose on total powder weight, alongside 25–30% cement and 50–60% silica sand (0.1–0.6 mm), introduces the critical parameter of pH shock. Within the first 10 min of mixing, pH rises from nominally neutral to >12.5; if the protective colloid system and carboxylation degree are not precisely matched, microfloc formation leads to a steep reduction in spread rate from 13 kg/m²/h to below 8 kg/m²/h using a 10 mm notched trowel. Production-scale processing employs a continuous single-shaft paddle mixer (NETZSCH or M-tec type) where the emulsion is pre-diluted with water to 30% solids before being injected into the dry-mix stream to dampen the exothermic hydration peak; the compound is discharged within 4 min and applied within a pot life of 90 min. After curing at 23 °C/50% RH for 28 days, specimens must satisfy EOTA ETAG 004 adhesion to EPS of ≥ 0.08 MPa (failure in EPS) and the water absorption coefficient w ≤ 0.5 kg/(m²·h⁰·⁵). The base coat is subsequently reinforced with 160 g/m² alkali-resistant glass fibre mesh and finished with a 2–3 mm synthetic render to form a fire-rated B-s1,d0 external wall assembly for multi-storey residential buildings in climate zone Csa.For air-through bonded nonwoven substrates destined for hygiene acquisition layers (diaper top sheets), CW FH-Ⅲ is applied at 8–12% binder add-on via a foam finishing or saturation bonding line; the dried web meets FDA 21 CFR 176.170 compositional limits for indirect food contact and OEKO-TEX Standard 100 Class I requirements, and the final product is slit onto 150 mm width rolls for converter integration.In solvent-free dry lamination of 300 g/m² solid bleached sulphate board to 15 µm LDPE film for frozen food cartons, CW FH-Ⅲ is blended with a polyvinyl alcohol solution at a ratio of 85:15 (dry/dry) to form an adhesive layer deposited at 3–4 g/m² dry coat weight via a multi-roll gravure coater running at 200–250 m/min. The emulsion complies with FDA 21 CFR 176.170(c) and European Regulation 1935/2004/EC on materials intended for contact with food; migration testing per EU 10/2011 specific migration limits for vinyl acetate monomer (0.02 mg/kg) is routinely passed. An inline corona treatment of the LDPE side to 42–48 dyne/cm is standardly employed before the lamination nip to ensure bond strengths exceeding 2.5 N/15 mm (ASTM D1876). The finished laminate is printed, die-cut, and glued into gable-top cartons for liquid dairy and juice products.

    Achieving BS 5867 Type B curl resistance through structured composite knife coating

    CW FH-Ⅲ is compounded into an aqueous paste containing 8–10 phr melamine-formaldehyde resin and 5 phr intumescent ammonium polyphosphate, then coated onto 180 g/m² polyester-cotton base fabric using a floating knife coater with a gap setting of 0.3 mm and a line speed of 15–30 m/min. The dry add-on is controlled to 25–35% to achieve a dry film thickness of 50–70 µm. To prevent concave curling in horizontal roller blind slats operated at 95% RH, the back side receives a second, unfilled emulsion topcoat at 5 g/m² dry weight applied via a kiss roll coater after the first coat reaches dust-free condition. The composite structure passes BS 5867-2:2008 for limited flame spread (Test 1, Method C) when tested at the 900 mm specimen length; the cured coating emits formaldehyde levels below 0.1 mg/m³ as per the French A+ regulation. Post-curing in a hot air stenter at 150 °C for 3 min drives the etherification crosslinking reaction to completion; residual free formaldehyde is scavenged by post-addition of urea at 2% into the compound, confirmed by acetylacetone method titration. The coated fabric is slit to 1.5 m width and fabricated into cord-operated roller blinds with spring-assist mechanisms for the European domestic market.
    Application SegmentCore Regulatory / Performance StandardKey Test Designation
    Interior wall paintGB/T 9756-2018 Grade IScrub resistance cycling per GB/T 9266
    Wood adhesives D4EN 204:2016 / JIS K 6806Boiling water tensile shear (4 h)
    Carpet pre-coatIMO FTP Code Part 5 / ISO 4919Tuft withdrawal force; flammability
    ETICS base coatEOTA ETAG 004 / EN 13501-1Adhesion to EPS; water absorption
    Hygiene nonwovenFDA 21 CFR 176.170 / OEKO-TEX 100 Class IIndirect food contact extraction
    Paperboard laminationFDA 21 CFR 176.170(c) / EU 10/2011Vinyl acetate monomer SML 0.02 mg/kg
    Textile roller blindBS 5867-2:2008 Type BLimited flame spread Test 1, Method C
    Free Quote

    Competitive VAE Emulsion CW FH-Ⅲ 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
    VAE Emulsion CW FH-Ⅲ is a vinyl acetate‑ethylene copolymer dispersion stabilised by a nonionic/anionic surfactant system and carboxyl‑functionalised for targeted metal‑ion reactivity. The grade is manufactured without added formaldehyde, residual vinyl acetate monomer is held below 500 ppm, and total VOC content is < 0.5 g/L per ISO 11890-2. Typical specification ranges at delivery: solids content 54–56 % (ISO 3251), pH 4.0–5.5 (ISO 976), Brookfield RV viscosity (spindle 4, 20 rpm, 25 °C) 800–2000 mPa·s, minimum film formation temperature (MFFT) < 1 °C (ISO 2115), glass transition temperature (Tg, mid‑point by DSC) -12 °C, and average particle size 0.9–1.1 µm (laser diffraction). The product conforms to FDA 21 CFR 175.105 for indirect food contact adhesives, REACH Regulation (EC) No 1907/2006, and RoHS Directive 2011/65/EU; formaldehyde content is non‑detectable (10 ppm) by VdL-RL 01. Designed as a high‑ethylene, low‑MFFT binder, CW FH‑Ⅲ provides cohesive peel strengths and wet adhesion superior to the earlier CW FH‑II grade, particularly in systems where post‑application humidity exposure or water‑whitening resistance is critical. The ethylene sequencing yields a soft‑block character that imparts film flexibility without external plasticiser, while the carboxyl‑density increase of approximately 1.2 mol‑% over CW FH‑II enables controlled ionic crosslinking with polyvalent cations such as Al³⁺ and Zn²⁺. In high‑speed nonwoven lamination lines running at 200–300 m/min, immediate green tack determines bond integrity before full coalescence. CW FH‑Ⅲ, with an MFFT below 0 °C and a fast‑setting profile, permits fibre bonding at low add‑on weights (2–4 g/m² dry binder) without external plasticiser. Spray application through reciprocating hydraulic nozzles operating at 40–60 bar yields a uniform film on cellulose/polyester blends. The emulsion’s carboxyl functionality provides ionic crosslinking with multivalent metal salts—typically aluminium chloride at 0.5–1.0 % on binder solids—increasing wet tensile strength retention to more than 70 % after 24 h water immersion per EDANA 120.2-20. Under identical conditions, CW FH‑II exhibits wet strength retention below 55 % owing to its lower carboxyl content. For pre‑bonded webs, oven drying at 130–150 °C for 8–15 s is standard; CW FH‑Ⅲ tolerates line stops of up to 3 min without irreversible skinning in nozzles when the circulation pH is buffered to 4.5–4.8 with citric acid. Brookfield viscosity stability during 24‑h recirculation at 25 °C is maintained within ±10 % of initial value, and defoamer compatibility with polyether siloxane types permits downstream coating weights within ±3 % of target.

    Influence of Calcium Ion Tolerance on Long-Pot-Life Mortar Admixtures

    Extended pot life in cementitious tiling systems is contingent on the emulsion’s resistance to Ca²⁺‑induced coagulation. CW FH‑Ⅲ exhibits a critical coagulation concentration (CCC) for CaCl₂ of 0.45 mol/L, measured by turbidimetric titration, surpassing that of many standard VAE copolymers. In a two‑component polymer‑modified tile adhesive formulated to EN 12004 C2 classification, replacement of a conventional VAE with CW FH‑Ⅲ extends the open time at 20 °C, 60 % RH to 38 min while maintaining tensile adhesion strength after water immersion (EN 1348) above 1.2 N/mm². Pot life, assessed as the period during which notched trowel application remains homogeneous, exceeds 4 h; standard VAE‑based mortars often show viscosity doubling within 2.5 h due to calcium‑bridged micro‑gel formation. Wet mortar density (1.65 g/cm³) is retained, and air‑void spacing factor measured by EN 480-11 remains < 0.20 mm. The following table summarises comparative performance against a widely used reference VAE grade (REF‑VAE) in a 30 % polymer‑to‑cement ratio formulation:
    PropertyTest MethodCW FH-ⅢREF-VAE
    Open time (min)EN 13463822
    Tensile adhesion strength, 28 d dry (N/mm²)EN 13481.81.5
    Adhesion after water immersion (N/mm²)EN 13481.30.8
    Adhesion after heat ageing (N/mm²)EN 13481.40.9
    Pot life (h), 23 °CEN 12004 Annex A4.22.6
    Cement‑mortar workability data were obtained with a planetary mixer (Collomatic, 140 rpm) and a Portland cement CEM I 42.5 R at a water/cement ratio of 0.35. CW FH‑Ⅲ requires no additional retarder; free calcium concentration in the wet mortar remains below 8 mmol/L after 3 h, whereas REF‑VAE formulations exceed 14 mmol/L, triggering premature polyelectrolyte bridging.

    When CW FH-Ⅲ Replaces Standard VAE in Low-Energy-Cure Carpet Backing

    In conventional carpet backing, VAE dispersions with higher minimum film formation temperature (MFFT) necessitate elevated dryer temperatures—often 150–165 °C—to achieve full coalescence and adequate tuft‑lock. Because CW FH‑Ⅲ has an MFFT below 1 °C and a Tg of -12 °C, the pre‑coat and secondary‑backing layers develop continuous films at oven set‑points as low as 120 °C. On a full‑scale coating line with a 3.2‑m‑wide pin‑clip stenter and infrared pre‑heating modules, reduction of the tunnel air temperature from 155 °C to 125 °C cut specific energy consumption by 18 % (from 2.1 kWh/m² carpet to 1.72 kWh/m²). Tuft‑lock retention, measured by ISO 4919 after 10,000‑cycle Hexapod walk, remained above 12 N, while delamination strength (ASTM D3936) was 8.2 N/50 mm versus 7.6 N/50 mm for a standard VAE cured at 155 °C. The internal plasticisation from the ethylene‑rich sequences avoids the volatile plasticiser emissions associated with low‑Tg all‑acrylic or externally plasticised VAc‑VeoVa backings. Film‑property comparisons are given in the table below.
    PropertyStandardCW FH-ⅢCW FH-Ⅱ
    Tensile strength (MPa)ISO 527-3 / 500 mm/min5.84.9
    Elongation at break (%)ISO 527-3820750
    Water absorption, 24 h (%)ASTM D5706.211.5
    Water-whitening recovery (Δ Haze, %) after 24 h dryingInternal DTM-1083.518.2
    Blocking resistance, 50 °C/80 % RH (N/25 mm)ASTM D9071.12.8
    The water‑whitening recovery test applies 100 µm wet films on glass, immersion at 23 °C for 24 h, and haze measurement after 24 h ambient re‑conditioning. The rapid clarity recovery of CW FH‑Ⅲ correlates with lower inter‑particle surfactant desorption, enabling its use in transparent top‑coat formulations without optical compromise.

    How do residual surfactant migrants affect overpaintability in wallboard primer applications?

    Intercoat adhesion failures in gypsum wallboard primer‑surfacer systems are frequently attributed to exudation of emulsifier and wetting‑agent residues to the primer‑air interface. CW FH‑Ⅲ employs a surfactant package that yields surface‑exuded organic carbon, quantified by DI‑water extraction and TOC analysis, of 0.18 mg/m² after 28‑day conditioning at 23 °C/50 % RH. Standard VAE dispersions with identical solids and film‑drying regimes typically register 0.7–0.9 mg/m². Cross‑cut adhesion (ASTM D3359, method B) of a conventional waterborne acrylic topcoat applied over a 50‑µm dry CW FH‑Ⅲ primer film gave a rating of 4B with < 5 % removal; the same topcoat over a standard VAE primer peeled to 2B after 72‑h humidity exposure at 40 °C. The difference is attributed to the high ethylene content that favours surfactant anchorage within the polymer matrix during coalescence, reducing migration to the film surface. Formulators should note that at pH levels above 6.5 the electrostatic repulsion of the carboxylate groups can cause a slight increase in surface surfactant accumulation; maintaining a drop‑pH of 4.5–5.0 during primer let‑down is recommended. Airless spray application with a tip size 0.017–0.021 in and fluid pressure of 120–150 bar yields a wet‑film thickness of 80–100 µm without sagging on vertical gypsum faces when the primer is thickened with a compatible polyurethane associative thickener to a Stormer viscosity of 90–100 KU. Pre‑drying of the substrate to < 0.5 % free moisture (by calcium carbide method) prevents blistering at line speeds above 25 m/min.