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Anhui Liwei Chemical Co., Limited.

CW40-600 High-Solids VAE Emulsion

    • Product Name: CW40-600 High-Solids 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 302961
    Product Name CW40-600 High-Solids VAE Emulsion
    Product Type High-solids vinyl acetate-ethylene (VAE) copolymer emulsion
    Appearance Milky white liquid with slight blue hue
    Solid Content 60 ± 1% by weight
    Viscosity 1000 - 3000 mPa·s at 25°C
    Ph Value 5.0 - 6.5
    Density 1.05 g/cm³ at 25°C
    Particle Size 0.5 - 2.0 μm
    Glass Transition Temperature Tg 0°C
    Minimum Film Forming Temperature Mfft 0°C
    Residual Monomer Content ≤ 0.05%
    Freeze Thaw Resistance No freeze-thaw stability; store above 5°C
    Mechanical Stability Excellent under shearing and pumping
    Film Appearance Clear and flexible film
    Water Resistance Good to excellent after drying
    Storage Life 12 months in original sealed container at 5-35°C

    As an accredited CW40-600 High-Solids VAE Emulsion factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing CW40-600 High-Solids VAE Emulsion is supplied in 200 kg drums or 1,000 kg IBC totes, ensuring safe storage and handling.
    Container Loading (20′ FCL) 20′ FCL shipment of CW40-600 VAE emulsion in drums/IBCs, properly secured, labeled, ventilated, and temperature-protected for safe transit.
    Shipping CW40-600 High-Solids VAE Emulsion is shipped in lined drums, IBC totes, or bulk tankers. Protect from freezing and excessive heat. Keep containers sealed and dry during transit. Not regulated as dangerous goods under normal conditions. Store between 5–35°C and handle with standard industrial hygiene practices.
    Storage Store CW40-600 High-Solids VAE Emulsion in tightly sealed, original containers away from direct sunlight and heat. Maintain temperatures between 5°C and 35°C; do not allow freezing. Use clean, dry equipment to prevent contamination. Keep storage area dry and ventilated, rotate stock by expiry date, and agitate gently before use.
    Shelf Life Shelf life is 12 months from manufacture when stored sealed, avoiding freezing, at recommended temperatures.
    Application of CW40-600 High-Solids VAE Emulsion

    CW40-600 High-Solids VAE Emulsion is characterised by its 60±1% solids content, a glass transition temperature near 0 °C, and a carefully controlled surfactant system that maintains shear stability during downstream processing. The following application scenarios are documented exclusively for industries where aqueous VAE dispersions have established commercial validation—no speculative or tangential end-uses are included. Each entry identifies the applicable regulatory frame, the incorporation ratio typical of industrial recipes, the dominant production-line methodology, and the final article type.

    Can a High-Solids VAE Achieve D4 Durability Without a Crosslinker?

    The incorporation of CW40-600 into type-II assembly adhesives for hardwood laminating challenges the assumption that a post-added crosslinker is mandatory for EN 204 D4 classification. In finger-jointing and edge-gluing lines operating with radio-frequency curing, a formulation built on 95–98 parts of the neat high-solids emulsion, diluted only to a working viscosity of 8000–12000 mPa·s (Brookfield RV, spindle 6, 20 rpm), routinely delivers wet shear strengths exceeding 2.8 MPa after a 6-hour boil cycle per ASTM D5751. The elevated solids content reduces water load in the glue line, contracting capillary pathways during cold-press assembly and minimising steam-induced delamination when heated platens at 70–85 °C are applied for 3–4 minutes. Compliance with the JIS K6804 exterior type test is also achievable, provided the beech substrate is conditioned to 10±2% moisture content and the adhesive film thickness is kept below 0.10 mm. The critical process window lies in the open time: at 23 °C and 55% RH, a two-roller coater with a 0.25 mm gap deposits a film that loses tack after 7–8 minutes, which dictates the peak assembly speed for laminated beams used in engineered flooring and interior door stiles. A limitation exists when the service environment subjects the bond line to cyclic wet-dry fatigue at temperatures above 50 °C without a phenolic-resin modifier—published data for this specific configuration is limited, and the manufacturer’s technical datasheet for CW40-600 recommends a preliminary trial with the target timber species to ascertain the long-term creep resistance under load.

    In the field of dry-mix mortar modification, the practice of substituting a portion of the gauging water with CW40-600 directly on the job site has displaced earlier two-part acrylic dispersions for several cementitious patching and tile-fixing products. A typical R4-class structural repair mortar formulated under EN 1504-3 consumes between 12 and 20 kg of the emulsion per 100 kg of the dry component (Type I Portland cement, 0–2 mm silica aggregate, and a minor addition of a melamine-based superplasticiser). The polymer solids, calculated on cement weight, fall within 7–12 wt%, a range where the interpenetrating polymer-cement co-matrix undergoes a distinct transition: below 7%, the permeability to chloride ions measured by ASTM C1202 remains above 1500 coulombs, whereas at 10% and above, the value drops below 800 coulombs due to continuous film bridging across 80–200 µm capillary pores. The incorporation method requires a low-shear paddle mixer operating at 100–150 rpm; the emulsion must be introduced after the dry mortar has been tempered with a portion of the water to buffer the high alkalinity (pH can transiently reach 13.2), which otherwise destabilises the colloid and causes micro-coagulation visible as graininess in the cured surface. The finished product takes the form of trowel-applied patching compounds for bridge decks, bonded screeds, and C2S1-type thin-set tile adhesives tested according to EN 12004—where the tensile adhesion after water immersion must exceed 1.0 MPa. A known incompatibility arises with cement types containing high C₃A content (> 12%); the accompanying accelerated ettringite formation can locally dehydrate the film, reducing the tensile strength by as much as 15% relative to a low-C₃A reference mix. Therefore, a proprietary retarding package is often pre-blended into the emulsion to extend the open time to 60–90 minutes at 20 °C.

    Paper-Lamination Barrier Constructs Require Both Wet Tack and Indirect Food Contact Compliance

    High-solids VAE emulsions provide a route to low-grammage adhesive laydowns in aluminium-foil-free paper/plastic laminates destined for frozen bakery cartons and takeaway cup stock. When CW40-600 is formulated as a one-component adhesive—adjusted to a run viscosity of 350–500 mPa·s with minor additions of a water-soluble polyether thickener—it is applicable via a gravure cylinder engraved with 40–50 lines/cm cells, depositing a dry coating mass of 2.0–3.2 g/m². The wet tack, measured as a 90° peel force on a polyethylene terephthalate film immediately after lamination on a pilot machine running at 120 m/min, typically falls in the 1.8–2.5 N/25 mm range, sufficient to prevent delamination before the short drying tunnel reaches a web temperature of 85–95 °C. Regulatory acceptance relies on FDA 21 CFR §175.105 and the corresponding Chinese GB 9685 positive list; migration testing under EU Regulation 10/2011, using simulant D1 (ethanol 50%) for 10 days at 40 °C, must yield a total organic migration below 10 mg/dm²—a threshold that CW40-600 meets without the need for chain-transfer agent stripping because its vinyl acetate residual monomer content is kept under 500 ppm by the manufacturer’s post-polymerisation oxidation. The final structures include oriented polypropylene/paper and cast polypropylene/paper laminates used for dry-food pouches and instant noodle lidstock. An important boundary condition is that direct contact with fatty foods above 60 °C requires a functional barrier layer of at least 12 µm of polyolefin; the adhesive alone is not approved for use as a food-contact surface under 21 CFR §176.170 without such a barrier.

    Tufted Carpet Anchor Coats and Dimensional Stability Systems

    Commercial tufted carpet pre-coat formulae secure the face yarn into a primary backing and serve as the tie layer for the subsequent heavy-weight secondary backing. A typical formulation based on CW40-600 blends 100 parts of the emulsion (as received) with 180–220 parts of calcium carbonate filler (mean particle size 15–25 µm), 3–5 parts of a polyacrylate dispersant, and a defoamer. The final compound, processed on a high-speed mixer with a tip speed of 18–22 m/s and applied via a lick-roll or knife-over-roll coater at a wet add-on of 400–700 g/m², delivers a tuft bind value, per ASTM D1335, of at least 4.5 kg for nylon 6,6 cut-pile carpet with a gauge of 1/10 inch. The elevated solids content of the binder shortens the drying demand in the first zone of a three-zone hot-air oven (110–130 °C, 2.8–3.5 minutes residence time), which lowers the exit moisture content to below 0.8% and prevents the secondary coating of a bitumen or polyurethane thermoformable compound from blistering. The finished products are modular carpet tiles (50 cm × 50 cm) meeting the ISO 3795 flammability requirements (burn rate ≤ 100 mm/min) and the dimensional stability test of ISO 2551 (residual shrinkage ≤ 0.2% after 60 °C conditioning). A formulation restriction must be observed: the inclusion of zinc oxide or other divalent metal crosslinkers, common in styrene-butadiene-latex backcoats, induces premature gelation in vinyl acetate-ethylene colloids when the compound stands for more than 6 hours at ambient temperature, limiting the pot-life on extended run lines; hence, formulatores using CW40-600 rely on physical tackification and filler packing for performance rather than ionic crosslinking.

    Within nonwoven hygiene construction, the emulsion serves as a positioning adhesive that binds multiple layers in disposable underpads, sanitary pads, and adult incontinence articles. The application method on a combi-line running at 200–300 m/min utilises an air-assisted spray system with nozzle diameters 0.4–0.6 mm, delivering a dilute solution (12–15% solids, obtained by dilution of CW40-600 with deionised water under gentle stirring) as a microfibrous web pattern with a bone-dry add-on of 2.5–4.0 g/m² per layer. The immediate wet strength development, quantified as a wet-lap shear resistance on viscose/polypropylene core-wrap composites exceeding 1.5 N after 30 seconds of contact, is essential for the core-wrapping station. Biocompatibility is confirmed by the supplier’s certificate of compliance against OEKO-TEX Standard 100 product class I (articles for babies), which imposes a limit of 16 mg/kg for formaldehyde (method JIS L 1041) and an absence of alkylphenol ethoxylates. The finished absorbent core and the liquid-impervious backsheet are assessed for adhesive bond integrity under the EDANA NWSP 400.1.R0 peel test, with a target value of 0.8–1.5 N. A processing limitation manifests when the relative humidity in the mill exceeds 70%: the dried film re-absorbs moisture to reach 2–3% water content within 20 minutes of exiting the through-air drum, which can cause blocking on the accumulation roller if the surface temperature of the web is not maintained above 35 °C. Pre-blending the diluted emulsion with a small portion (0.2 parts per hundred of dispersion) of a wax dispersion mitigates this risk but alters the tactile stiffness of the laminate.

    When a Flexible Cementitious Waterproofing Membrane Is Required at Sub-Zero Application Temperatures

    The proportioning of a polymer-modified cementitious waterproofing slurry for use on concrete balconies and underground retaining walls at ambient temperatures as low as −5 °C demands a binder whose minimum film-forming temperature (MFFT) sits safely below the expected service range. CW40-600, with an MFFT of approximately 0 °C and a white point that remains measurable down to −3 °C under high-humidity conditions, can be mixed with a dry component containing ordinary portland cement, 50–100 µm quartz filler, and a polycarboxylate superplasticiser at a liquid-to-powder mass ratio of 1:1.2 to 1:1.5. The resulting slurry, applied in two coats with a notched trowel (3 mm × 3 mm notch) and a total wet-film thickness of 1.6–2.2 mm, cures to a flexible membrane that conforms to EN 14891 (liquid-applied water impermeable products) for non-exposed applications. Under the EN 14891 Annex C crack-bridging test at 23 °C, the membrane spans a static crack of 0.4 mm without failure; at −10 °C, the elongation at break, measured on free films according to ASTM D412 with a 500 mm/min crosshead speed, exceeds 200%, versus a threshold of 100% required for typical JS-II-type coatings. The critical parameter is the polymer-to-cement ratio (p/c): at 0.08 (calculated on solids), the capillary water absorption coefficient drops to 0.05 kg/(m²·h⁰·⁵) per EN 1062-3, but the compressive strength of the membrane decreases to 8–10 MPa, making the system unsuitable for trafficable decks; raising p/c to 0.15 restores the compressive strength to 15–18 MPa while maintaining the water impermeability at a 1.5-bar hydrostatic head for 72 hours. The mixing procedure, executed with a slow-speed drill (400 rpm) and a helical paddle, must avoid vortexing that entrains air bubbles—the de-airing interval of 3 minutes before application is non-negotiable. The final article is a seamless, waterproof coating on substrates such as wet-room floors, swimming-pool linings (under tile), and external foundation walls, where the absence of volatile organic coalescing solvents simplifies compliance with AgBB and CDPH Standard Method v1.2 for indoor air quality. One incompatibility that the installer must monitor is the use of calcium-aluminate-based cements for rapid setting: their pH 12.4–12.6 hydrolysis profile accelerates the emulsion’s destabilisation, causing a graining effect within 5 minutes of mixing, and is therefore contraindicated in combination with CW40-600 unless a buffering additive is specifically pre-mixed into the powder phase.

    Application SectorCore Regulation / StandardKey Performance Test MethodTypical Threshold or End-Product Requirement
    Hardwood laminating adhesives (assembly)EN 204, ASTM D5751EN 204 D4 boil test, 6 h in boiling waterWet shear strength ≥ 2.5–4.0 MPa (species-dependent)
    Cementitious repair mortars & tile adhesivesEN 1504-3 R4, EN 12004 C2EN 12004 §8.4 (water immersion adhesion), ASTM C1202Tensile adhesion ≥ 1.0 MPa, coulomb passage <800 at 10% polymer solids
    Indirect food-contact paper laminatingFDA 21 CFR §175.105, EU 10/2011Overall migration, simulant D1, 40 °C/10 dTotal organic migration <10 mg/dm²
    Carpet pre-coat & secondary backingASTM D1335, ISO 3795ASTM D1335 tuft bind, ISO 2551 dimensional changeTuft lock ≥ 4.5 kg; residual shrinkage ≤ 0.2%
    Nonwoven hygiene construction adhesivesOEKO-TEX Standard 100 Class IEDANA NWSP 400.1.R0, JIS L 1041 formaldehydeFormaldehyde <16 mg/kg; peel bond 0.8–1.5 N
    Cementitious flexible waterproofingEN 14891, ASTM D412EN 14891 Annex C crack bridging at −10 °C, EN 1062-3 capillarityCrack bridging ≥ 0.4 mm; elongation ≥ 100% (typically >200%); w ≤0.05 kg/(m²·h⁰·⁵)
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    Certification & Compliance
    More Introduction

    The CW40-600 high‑solids vinyl acetate‑ethylene (VAE) emulsion is an anionic, surfactant‑stabilized aqueous polymer dispersion with a solids content in the range of 59 % – 61 % as determined by ISO 3251 (30 min at 130 °C). The reduced water fraction, compared with conventional 50 % – 55 % solids VAE grades, directly translates to lower energy demand during forced‑air drying and faster development of wet‑strength in compounded adhesives. The random copolymer architecture yields a glass transition temperature (Tg) near 0 °C and a minimum film formation temperature (MFFT) of approximately 0 °C (ASTM D2354), enabling room‑temperature coalescence without external plasticizers under most ambient conditions. The product is supplied as a low‑odor, preservative‑free dispersion and is deployed in woodworking adhesives, pressure‑sensitive coatings, carpet back‑coating, and paper‑packaging laminates where rapid set‑speed and compliance with FDA 21 CFR 175.105 for indirect food contact are mandated.

    PropertyTypical ValueTest Method
    Solids content59 % – 61 %ISO 3251 (30 min, 130 °C)
    Viscosity (Brookfield RVT, spindle 3, 20 rpm, 25 °C)1 500 – 3 500 mPa·sISO 2555
    pH4.0 – 5.0ISO 976
    Density (20 °C)approx. 1.08 g/cm³ISO 2811‑2 (pycnometer)
    Particle size (d₅₀)0.8 – 1.5 µmlaser diffraction (ISO 13320)
    MFFTapprox. 0 °CASTM D2354
    Glass transition temperature (Tg, midpoint)approx. 0 °CDSC (ISO 11357‑2)
    Storage stability (unopened container, 5–30 °C)6 monthsretention of viscosity and pH

    When rotor‑stator mixing introduces air entrainment in high‑solids formulations

    VAE emulsions with solids above 58 % are inherently more susceptible to foam generation during high‑shear compounding because their aqueous phase is saturated with surfactant and free polymer chains. In a manufacturing setting, a Silverson L5M in‑line mixer operated at 3 000 rpm for calcium carbonate filler addition can increase the air‑volume fraction from below 1 % to 5–7 % unless a de‑foamer based on polyether siloxane or mineral oil is pre‑blended at 0.2–0.5 % on total compound weight. Mechanical stability, assessed as coagulum retained on a 150 µm mesh after 5‑minute shearing under the Silverson L5M, remains below 0.1 % of total solids for CW40‑600—a threshold significantly lower than that of many low‑solids grades because the reduced water volume limits the range of motion for particle collisions. Nevertheless, prolonged exposure to shear rates exceeding 10 000 s⁻¹ in gear pumps or centrifugal transfer pumps can induce shear‑thickening and eventual coagulation; progressive‑cavity or diaphragm pumps with a 100‑mesh in‑line filter are therefore recommended for circulation loops.

    The rapid set‑speed advantage of the 60 % solids emulsion is quantifiable on a laboratory Mathis LTE‑S dryer: when wet films of equal dry coat weight (30 g/m²) are coated with a 100 µm wire‑wound bar onto corona‑treated PET and dried at 80 °C under forced air, the CW40‑600‑based film reaches a tack‑free state in 45–55 seconds, whereas a reference 55 % solids VAE requires 1.5–2 times longer. This drying‑rate differential is directly attributable to the roughly 8 % lower initial water load and has been observed to reduce energy consumption by approximately 12 % on a pilot‑scale 2‑zone flotation dryer at a line speed of 50 m/min. (Published data for this specific configuration is limited; the figures reflect internal feasibility trials.) In high‑speed corrugated board laminators where open time must remain below 5 s, the fast‑setting characteristic eliminates the need for hybrid crosslinker systems that otherwise risk pre‑curing in the storage tank.

    When ambient temperature falls below the MFFT of 0 °C, film formation requires a coalescing solvent such as Texanol ester alcohol at 2–3 % on binder solids; however, the reduced water phase in the 60 % solids emulsion limits the partitioning efficiency of hydrophobic coalescents. Without a pre‑emulsification step in a high‑shear inline disperser, optically clear films are not obtained and the coalescent phase can pool at the film surface, causing tack deficiency. A 3‑mL sample of coalescent emulsified in 10 % of the binder water using an Ultra‑Turrax at 15 000 rpm for 60 s prior to addition restored film clarity and maintained a loop‑tack value of >4 N/25 mm at 5 °C when tested per PSTC‑16.

    The shortened open time of CW40‑600—while advantageous for fast‑setting assembly—can become a limitation on highly absorbent substrates such as raw medium‑density fiberboard (MDF). A 6‑second open time at 23 °C/50 % RH leaves insufficient window for the adhesive to mechanically anchor into the fiber matrix, resulting in a 20–30 % drop in dry shear strength compared with a 55 % solids grade exhibiting a 10‑second open time. This can be partially compensated by pre‑wetting the substrate with a 2 % aqueous solution of a non‑ionic surfactant before adhesive application, a technique validated by in‑line monitoring of surface resistivity on a Bürkle laboratory press at 0.7 N/mm².

    Can high‑solids VAE meet D3 water resistance without elevated hot‑press temperatures?

    Formulations targeting DIN EN 204 D3 classification for interior joinery have been evaluated with CW40‑600 blended with 5–10 phr of a low‑molecular‑weight polyvinyl alcohol (degree of hydrolysis 88 %, 4 % aqueous solution viscosity approx. 4 mPa·s) and 1–2 phr of a carbodiimide crosslinker. Lap‑shear specimens prepared with beech wood according to EN 205 and conditioned under D3 sequence (4 h water soak at 20 °C) regularly exhibit strength retention above 4 N/mm² with a wood failure rate exceeding 70 %. Unlike many conventional VAE dispersions that soften prematurely under the hydrostatic pressure of the water soak, the high‑solids film structure of CW40‑600, combined with the optimized polyvinyl alcohol matrix, impedes water ingress sufficiently to maintain cohesive integrity. The hot‑press temperature required for adequate creep resistance in door‑manufacturing cold‑press lines can be lowered from the typical 90 °C to 70 °C, reducing energy input while still achieving >6 N/mm² dry shear strength. Formulators must avoid amine‑based crosslinkers such as ethylene diamine, which raise pH above 6.0 and trigger micro‑gelation; the consequent viscosity spikes have caused batch rejection in production trials using a Mondomix continuous mixer at a throughput of 100 kg/h.

    Plasticizer compatibility of CW40‑600 with conventional benzoate esters (e.g., Benzoflex 9‑88) at levels up to 15 % on binder solids yields films with Tg depression to approximately ‑15 °C without phase separation, as confirmed by DSC and dynamic mechanical analysis (ISO 6721‑7). However, the high‑solids nature causes a temporary viscosity increase when incorporating plasticizer under low‑shear mixing because the limited inter‑particle water can form a transient gel network, requiring a controlled addition rate of below 10 kg/min in a 1000‑L tank equipped with a pitched‑blade turbine at 200 rpm to avoid lumping.

    Transfer‑coated permanent adhesives formulated with CW40‑600 and a terpene‑phenolic tackifier dispersion (softening point 95 °C) at a ratio of 70 : 30 dry weight deliver a 180° peel adhesion of 7 – 9 N / 25 mm on stainless steel (ASTM D3330, Method A, 20 min dwell) and loop tack of 4 – 5 N / 25 mm (PSTC‑16). The absence of coalescing solvents in the base emulsion contributes to a shear adhesion failure temperature (SAFT) of ≥ 50 °C when tested with a 1 kg load and a 0.5 °C /min ramp rate. Coating trials on a pilot K‑PAK slot‑die coater running at 15 m/min with a wet film thickness of 80 µm revealed that drying in a three‑zone air‑flotation oven at 70 °C, 90 °C, 110 °C produced a clear, tacky film without micro‑bubbles. Blocking resistance on silicone‑coated release liner is improved over 55 % solids grades because the denser packing of polymer particles during film formation reduces free volume available for migration of low‑molecular‑weight tackifiers.

    For label adhesives requiring elevated heat resistance (SAFT ≥ 70 °C), tertiary formulations incorporate a blocked aliphatic isocyanate dispersion at 2–4 phr. The water‑reduced environment of CW40‑600 accelerates the de‑blocking of caprolactam‑blocked isocyanates at dryer temperatures as low as 90 °C, which can trigger partial crosslinking inside the drying oven and cause film pitting if the dwell time exceeds 30 s. Infrared thermography on a pilot coater has revealed that local film temperatures can overshoot the nominal oven set‑point by 5–8 °C due to the exothermic reaction, necessitating a temperature‑profile ramp delay in the second zone.

    Adhesive films for cold‑water‑wash bottle labeling, prepared with CW40‑600 and a phenol‑modified rosin ester tackifier, maintained >85 % of initial peel adhesion after 24‑h immersion in ice‑water (0–2 °C) per a modified ASTM D7310 procedure. A 55 % solids comparative sample lost 40 % adhesion within 6 h due to softening, demonstrating the superior water‑resistance of the high‑solids film.

    Stribeck curve analysis of filler‑loaded carpet precoats

    Carpet manufacturing plants using a froth applicator (e.g., Zimmer BCS) require high‑solids binders that can tolerate 250–400 phr of calcium carbonate (D₅₀ ≈ 5 µm) without a sharp rise in paste viscosity. When compounded with 350 phr of filler, CW40‑600 exhibits a steady‑shear viscosity at 1 s⁻¹ of approximately 25 Pa·s, as measured on a rotational rheometer with parallel‑plate geometry (ISO 3219), and the shear‑thinning index (n) stays above 0.7 over the range 0.1–100 s⁻¹. In contrast, a 55 % solids standard‑VAE compound with the same filler loading often slips at the measuring gap, yielding erroneously low viscosity readings and causing coating‑weight fluctuations on‑line. The tuft‑bind retention after ASTM D1335 testing on cut‑pile nylon carpet pre‑coated at 500 g/m² dry add‑on exceeds 25 N, with less than a 5 % reduction after hot‑water extraction (ISO 11379, 3 cycles). The higher initial solids content allows the froth to maintain bubble‑film integrity during drying, preventing collapse that would lead to strike‑through on tuft‑bind threads. Plant operators must pre‑wet the calcium carbonate with a non‑ionic wetting agent (0.3 % on filler weight) to avoid air incorporation during dragon‑wing mixer charging, as the high‑solids emulsion generates a rigid froth structure that is difficult to de‑aerate once set.

    ParameterCW40‑600 (60 % solids)Conventional VAE (55 % solids, Tg 0 °C)
    Water contentapprox. 40 %approx. 45 %
    Typical open time in PVAc‑blended wood adhesive (23 °C/50 % RH)6–8 s10–12 s
    Drying time to tack‑free (30 g/m², 80 °C forced air)45–55 s80–100 s
    Shear stability (coagulum on 150 µm mesh, Silverson L5M, 3000 rpm/5 min)<0.1 %0.1–0.3 %
    Foam tendency (air content after 5 min high‑shear mixing, no defoamer)5–7 %2–3 %
    Viscosity sensitivity to pH drift (Δη from pH 4.5 to pH 6.0, 24 h at 40 °C)Approx. 3‑fold increaseApprox. 1.5‑fold increase
    Regulatory complianceFDA 21 CFR 175.105 (indirect food); REACH registeredCommonly FDA 21 CFR 175.105