VAE Emulsion CW FH-Ⅲ
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Product Name:
VAE Emulsion CW FH-Ⅲ
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Factroy Site:
Lingwu, Yinchuan, Ningxia, China
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Price Inquiry:
sales2@liwei-chem.com
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Manufacturer:
Anhui Liwei Chemical Co., Limited.
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CONTACT NOW
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VAE Emulsion CW FH-Ⅲ is typically used in formulations when pH, temperature, and shear conditions and minimum film-forming temperature, storage stability, and compatibility restrictions must be controlled within specific ranges.
Specifications
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HS Code
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279354
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| 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 Segment | Core Regulatory / Performance Standard | Key Test Designation |
|---|
| Interior wall paint | GB/T 9756-2018 Grade I | Scrub resistance cycling per GB/T 9266 |
| Wood adhesives D4 | EN 204:2016 / JIS K 6806 | Boiling water tensile shear (4 h) |
| Carpet pre-coat | IMO FTP Code Part 5 / ISO 4919 | Tuft withdrawal force; flammability |
| ETICS base coat | EOTA ETAG 004 / EN 13501-1 | Adhesion to EPS; water absorption |
| Hygiene nonwoven | FDA 21 CFR 176.170 / OEKO-TEX 100 Class I | Indirect food contact extraction |
| Paperboard lamination | FDA 21 CFR 176.170(c) / EU 10/2011 | Vinyl acetate monomer SML 0.02 mg/kg |
| Textile roller blind | BS 5867-2:2008 Type B | Limited 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
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Certification & Compliance
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VAE Emulsion CW FH-Ⅲ is manufactured under an ISO 9001 quality system and complies with relevant regulatory requirements.
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COA, SDS/MSDS, and related certificates are available upon request.
For certificate requests or inquiries, contact: sales2@liwei-chem.com.
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:
| Property | Test Method | CW FH-Ⅲ | REF-VAE |
| Open time (min) | EN 1346 | 38 | 22 |
| Tensile adhesion strength, 28 d dry (N/mm²) | EN 1348 | 1.8 | 1.5 |
| Adhesion after water immersion (N/mm²) | EN 1348 | 1.3 | 0.8 |
| Adhesion after heat ageing (N/mm²) | EN 1348 | 1.4 | 0.9 |
| Pot life (h), 23 °C | EN 12004 Annex A | 4.2 | 2.6 |
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.
| Property | Standard | CW FH-Ⅲ | CW FH-Ⅱ |
| Tensile strength (MPa) | ISO 527-3 / 500 mm/min | 5.8 | 4.9 |
| Elongation at break (%) | ISO 527-3 | 820 | 750 |
| Water absorption, 24 h (%) | ASTM D570 | 6.2 | 11.5 |
| Water-whitening recovery (Δ Haze, %) after 24 h drying | Internal DTM-108 | 3.5 | 18.2 |
| Blocking resistance, 50 °C/80 % RH (N/25 mm) | ASTM D907 | 1.1 | 2.8 |
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.