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Anhui Liwei Chemical Co., Limited.

Airflex 426 High-Solids Carboxylated VAE Emulsion

    • Product Name: Airflex 426 High-Solids Carboxylated 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 965238
    Polymer Type Carboxylated Vinyl Acetate-Ethylene (VAE) Copolymer
    Appearance White liquid
    Total Solids Content 65.5 wt%
    Brookfield Viscosity 25 C 2500 cP (mPa·s)
    Ph 5.0
    Density 1.09 g/cm³
    Glass Transition Temperature 0°C
    Minimum Film Forming Temperature 0°C
    Particle Size 1.5 µm
    Film Appearance Clear, flexible, tacky film
    Mechanical Stability Excellent

    As an accredited Airflex 426 High-Solids Carboxylated VAE Emulsion factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Airflex 426 High-Solids Carboxylated VAE Emulsion is packaged in 200 kg drums or 1,000 kg IBC totes.
    Container Loading (20′ FCL) 20′ FCL container loading of Airflex 426 VAE emulsion via flexitank or drums, ensuring secure stowage, stability, and safe transport.
    Shipping Airflex 426 High-Solids Carboxylated VAE Emulsion ships in drums, totes, or bulk tankers. Protect from freezing and excessive heat; ideal storage 40–90°F. Material is non-hazardous per DOT, though avoid skin contact. Keep containers sealed and use within shelf life to prevent skinning or settling.
    Storage Store Airflex 426 in original, sealed containers away from direct sunlight and extreme heat. Maintain storage temperature between 40°F and 100°F (5°C–38°C) to prevent freezing or coagulation. Keep containers upright and dry. Thoroughly stir or recirculate before use. With proper storage, shelf life is typically six months from manufacture date.
    Shelf Life Shelf life of Airflex 426 is six months from shipment when stored at 15–27°C in sealed, undamaged containers.
    Application of Airflex 426 High-Solids Carboxylated VAE Emulsion

    In water-based laminating adhesives for paperboard food packaging, the shift away from solvent-borne systems compels formulators to address two conflicting demands: aggressive wet tack development on high-speed cup-forming lines and sustained bond integrity after exposure to hot fill temperatures or microwave reheating. Airflex 426, a carboxylated vinyl acetate–ethylene (VAE) emulsion with a solids content of 63–65%, is typically introduced as the sole polymeric binder in the compounded adhesive, comprising 85–95 wt% of the wet formulation. The remaining fraction is allocated to a benzoate ester plasticizer (2–5 phr on emulsion weight), a polymeric defoamer (0.2–0.5 phr), and an alkali-swellable associative thickener adjusted to deliver a Brookfield RVT viscosity of 2200–3800 mPa·s at 20 rpm. This recipe architecture leverages the carboxyl functionality: upon neutralization to pH 6.8–7.5 with ammonium hydroxide, the emulsion undergoes controlled thickening and acquires a pronounced shear-thinning rheology that minimizes misting during roller application yet rebuilds structure instantly within the adhesive nip. Compliance with indirect food contact regulations is documented under FDA 21 CFR 175.105, the European Union’s Framework Regulation EC 1935/2004 with migration testing per EU No 10/2011 Annex III simulants, and China’s GB 9685-2016 positive list for adhesives in food-contact materials. On the production floor, the adhesive is transferred via a three-roll film coater or a slot-die system onto clay-coated recycled board at a wet deposition weight of 18–28 g/m². Forced-air impingement ovens operating between 110°C and 135°C reduce moisture content to below 0.8% within a residence time of 8–14 seconds before the coated web enters a heated nip calendar where it is bonded to the second substrate under a line pressure of 40–80 N/cm at a web speed of 120–180 m/min. The finished constructions—single-wall paper cups, clamshell takeaway boxes, frozen food folding cartons, and microwaveable sleeve trays—must routinely survive 90°C water-fill testing for 30 minutes without delamination and pass the TAPPI T 494 dry peel test at a minimum of 2.8 N/cm. A persistent bottleneck encountered on low-grammage boards arises when residual moisture in the adhesive layer, if exceeding 1.2% at the nip entry, generates steam blistering under the release pressure; this is mitigated by integrating an inline near-infrared moisture sensor that interlinks with oven damper controls to clamp the exit moisture within a ±0.15% tolerance window.

    What defines a packaging adhesive’s fitness for high-speed cup-forming lines?

    Converters processing polyethylene-laminated paperboard for dairy and beverage cups confront a specific failure mode: fiber tear at the side-seam after flame ionization treatment alters the surface energy of the PE layer unevenly. When a carboxylated high-solids VAE replaces traditional EVA hot melts in this cold-seal application, the adhesive must deliver sufficient green grab within 0.3–0.6 seconds of compression at 0.2–0.4 MPa to prevent the circular blank from springing open on the forming mandrel. Airflex 426 is compounded in these cold-seal formulations at 88–93% of the wet mix, alongside a solvent-free rosin ester dispersion added at 6–10 dry-weight percent to promote specific adhesion to polyolefin surfaces. The applicable food-contact framework extends to the European Regulation EU 10/2011 with the amendment 2020/1245 for plastic multi-layer structures, and the compliance dossier must contain time–temperature superposition migration data from 40°C/10 days and 70°C/2 hours simulating long-term shelf storage and hot filling. Production application proceeds through a gravure-coated pattern station that deposits parallel stripes of adhesive at a coating weight of 3–5 g/m² dry; the stripes are dried for 2–4 seconds at 80–90°C before the board is folded and pressed. End-of-line quality assurance relies on the ASTM F904 bond strength test performed after 24 hours of conditioning at 23°C/50% RH, with a target value exceeding 4.5 N/25 mm. The ultimate consumer articles—aseptic juice bricks, single-serve milk cartons, and yogurt multipack sleeves—expose the adhesive to cyclic refrigeration at 4°C and thermal shock when condensing steam from ambient-temperature opening prompts the adhesive’s carboxylate crosslinking sites to maintain cohesion; a documented operational limitation is the emulsion’s sensitivity to zinc stearate slip agents that bloom from the PE surface and can depress peel values by 18–25% when concentrations exceed 800 ppm.

    When a spunlace nonwoven is destined for a dispersible wet wipe, the binder’s gel-phase crosslinking under acidic pH becomes the decisive factor—not merely its dry tensile strength. The high carboxylic acid content of Airflex 426, expressed as an acid number in the range of 4–7 mg KOH/g dry polymer, renders the emulsion responsive to divalent cations and low-pH trigger mechanisms. In a standard pre-moistened wipe line, the binder is applied to a viscose/polyester (70/30) carded web of 40–55 g/m² basis weight through a saturation-foam process that controls the wet pick-up to 140–170%. The formulated bath contains Airflex 426 at a concentration equivalent to 12–18% add-on by fiber weight, supplemented by a silicone-based softening agent at 0.3–0.8% on bath weight and, where wet strength specification demands, a glyoxal-based crosslinker at 0.1–0.3 phr on emulsion solids. Regulatory conformity for baby care and feminine hygiene categories is anchored to the EDANA/INDA GD3 flushability framework, ISO 10993-5:2009 for in vitro cytotoxicity and ISO 10993-10:2021 for skin sensitization and irritation, and, for wipes claimed as flushable, the slosh-box disintegration requirement of ≥80% passage through a 12.5 mm sieve after 3 hours under INDA FG 504.2. The saturated web passes through a steam-through-air dryer at 150–170°C with a residence time of 18–30 seconds, where moisture is driven to below 6% and the carboxyl groups partially esterify with cellulose hydroxyls at the fiber–binder interface. Finished roll goods are converted into canister wipes, sachet-packed cosmetic pads, and individually folded adult cleansing cloths; a recurring production issue encountered on high-speed log slitting equipment is the generation of tacky edges if the dryer profile overshoots 175°C by more than 4°C, which catalyzes excessive film formation that resists rewetting and elevates the dynamic coefficient of friction above 0.85, causing jams in the infeed of the infeed conveyor.

    Binder Add-on (% on fiber)MD Dry Tensile (N/50 mm) ISO 9073-3CD Wet Tensile (N/50 mm) after ISO 9073-3 soakMass Loss in GD3 Slosh Box (%) at 180 minSoftness Handle Panel Rank (1–5, 1=softest)
    1022.6 ± 1.97.3 ± 0.886.4 ± 2.21.3
    1434.1 ± 2.412.9 ± 1.182.1 ± 3.12.1
    1847.5 ± 3.018.2 ± 1.676.5 ± 2.82.9
    2258.3 ± 3.724.0 ± 2.068.8 ± 3.53.7

    In polymer-modified cementitious waterproofing slurries applied to concrete substrate for balcony and bathroom envelopes, the liquid component is often mistaken as a simple acrylic dispersion, yet the ethylene backbone of a VAE provides a critical low-temperature crack-bridging capability that acrylics cannot match without external plasticizer migration. The two-component formulation combines a liquid admixture—comprising Airflex 426 at 78–88 wt%, potable water at 10–18 wt%, a liquid defoamer (0.3–0.6%), and a biocide—with a dry-mix powder that contains ordinary Portland cement 42.5R to 52.5N, graded silica sand (80–120 mesh), and a cellulose ether water-retention agent. The liquid-to-powder mass ratio is held between 1:1.2 and 1:1.5, producing a lump-free slurry with a viscosity of 6000–12000 mPa·s (Brookfield Helipath, T-bar spindle). Conformity to JC/T 23445-2009 Type II requirements demands a crack-bridging capacity of ≥0.75 mm at −10°C and tensile strength ≥1.8 MPa after water immersion; supplementary testing under ASTM D6083-21 and EN 14891:2022 for liquid-applied water impermeable products often accompanies export shipments. The slurry is applied with a notched trowel or an airless spray unit in two consecutive coats to a cumulative dry film thickness of 1.8–2.5 mm, with the second coat applied after the first has set to touch but before full cure (2–4 hours at 23°C/60% RH). Curing proceeds for 7 days under damp hessian or an acrylic-based curing membrane; insufficient moist curing depresses the carboxylate–cement hydrate complexation and delaminates the coat from the concrete under thermal cycling per GB/T 16777-2008 cycle B. The resulting seamless monolithic membrane serves as the waterproofing under tiled surfaces in shower cubicles, swimming pool surrounds, and plaza terraces, where it is permanently exposed to alkaline seepage water with a pH exceeding 12.5—an environment that rapidly hydrolyzes uncarboxylated VAE grades but leaves the crosslinked matrix of Airflex 426 intact for a verified service life exceeding 15 years in field inspections of installations in subtropical coastal climates.

    High-Solids Carboxylated VAE in Furniture Membrane Pressing

    Thermoforming PVC and PETG foils onto contoured medium-density fiberboard (MDF) panels in vacuum membrane presses demands an adhesive that tolerates a temperature–pressure cycle ranging from 120–140°C and 0.5–0.9 MPa while simultaneously wetting micron-scale surface irregularities without causing grain raise. Airflex 426 is formulated for this application as a single-component sprayable dispersion with a solids content adjusted to 55–60% through the addition of deionized water and a coalescing agent, typically a dibenzoate ester blend at 1.5–2.5 wt% of the wet compound. The carboxylation chemistry provides a dedicated interaction with the calcium stearate and calcium carbonate fillers embedded in the PVC film’s plastisol skin, a mechanism absent in standard VAE types. Industry compliance for the adhesive’s emission profile is mapped to the OEKO-TEX Standard 100 product class II for direct skin contact furniture components, while the emission chamber measurement follows EN 16516:2017 with a targeted equilibrium concentration of volatile organic compounds below 0.08 mg/m³ after 28 days. On the shop floor, the adhesive is applied by a reciprocating pistol spray system delivering a wet film of 55–75 g/m² uniformly across the sanded MDF substrate conditioned at 8–10% moisture content. The sprayed faces are flash-dried for 15–25 minutes at 35–45°C in a multi-tier rack dryer until the adhesive reaches a tacky, translucent state with a residual moisture content of 2.5–4.0%. The panel is then positioned in a single-membrane press where an upper silicone rubber membrane exerts even pressure while a heated platen at 125°C activates the polymer’s flow into the foil; the cycle time spans 45–90 seconds with an intensive force dwell of 20–30 seconds. Finished components—gloss-finish kitchen drawer fronts, vinyl-wrapped door stiles and rails, and sound-barrier enclosure panels for luxury white goods—are subjected to an ISO 2409:2020 cross-cut adhesion test on the curved profile (mandrel diameter 25 mm), where a rating of 0 or 1 is required for batch release. An operational limit manifests when pressing high-gloss white foils thinner than 0.3 mm: the adhesive’s residual surfactants, if not fully evaporated during flash-off, can migrate into the PVC layer and generate micro-yellowing under QUV-B 313 nm irradiation for 500 hours as per ASTM G154, a defect prevented by extending the flash drying by an additional 8–12 minutes whenever ambient humidity exceeds 70% RH.

    If a tipping paper adhesive fails on a PROTOS 90S at 7000 cpm, the root cause is seldom viscosity drift—it is rapid set-time collapse under the combined influence of porous plug wrap and condensate micro-droplets from the garniture cooling. High-speed cigarette assembly divides the adhesive’s duty into a lap-seam bond on the filter wrap and an anchor-coat bond between the tipping paper and the tobacco rod. Airflex 426, with its built-in carboxylic acid sites that can be partially neutralized with sodium hydroxide to pH 5.8–6.4, exhibits a controlled degree of water re-wettability that suits rotary-screw application at line speeds exceeding 5000 units per minute. The formulated adhesive is diluted to a running solids of 45–50% and may contain polyvinyl alcohol (PVOH, 88% hydrolysis grade) at 0.5–1.5% of the wet batch to tune open time and initial tack; the final viscosity is held in a narrow corridor of 2800–3600 mPa·s at 25°C (Brookfield LV, spindle #4, 60 rpm) because a deviation above 4000 mPa·s produces stringing and a deviation below 2200 mPa·s causes starvation on the transfer rollers. Regulatory acceptance relies on FDA 21 CFR 175.105 for incidental food-contact adhesives and the Council of Europe Resolution AP(2008)2 on paper and board articles intended to come into contact with foodstuffs, supplemented by migration modeling using the EN 13130-1 framework where the adhesive represents less than 1% of the total article weight. During manufacture, the adhesive is delivered to a closed-circuit pan-fed application system on the filter assembler, where a chrome-plated steel applicator roller running with a gap of 0.08–0.15 mm transfers a precise 12–18 µm wet film to the cork-patterned tipping paper. The bond is set within 0.15–0.30 seconds under the folding belts and chilled to 5–10°C immediately afterwards to arrest the plastic flow of the emulsion. The continuous production runs yield billions of filter cigarettes annually, and the adhesive’s principal quality gate is the open-time coupon test conducted on a bench imitating the maker’s dwell: a bond formed after 1.5 seconds of open time must achieve 90% fiber tear when peeled by hand at 23°C/55% RH. A known boundary condition for Airflex 426 in this segment is its incompatibility with amine-based buffering systems used in some reconstituted tobacco sheets; exposure to fugitive amines volatilized during the rod-forming step can catalyze premature crosslinking of the carboxylic groups, elevating the glass transition temperature of the bond line from a design value of approximately −5°C to above 10°C, which subsequently increases the risk of seal pop-off during the lip-pressure release test.

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    Certification & Compliance
    More Introduction

    Airflex 426 is a high-solids carboxylated vinyl acetate-ethylene (VAE) copolymer emulsion supplied at 65% non-volatile content by weight (ASTM D1489-21) with a pH of 4.5–5.5 and a Brookfield RV viscosity of 2,000–4,000 mPa·s at 25 °C (spindle 3, 20 rpm, ASTM D2196-18). The dispersed polymer carries a carboxylic acid functionality sufficient to produce an acid number of 15–25 mg KOH/g, enabling ambient-temperature ionic crosslinking with multivalent metal ions or reactive resins. The medium-coarse particle size, centered at 0.8 µm (laser diffraction, Malvern Mastersizer), balances rheology control with film coalescence on porous substrates. A differential scanning calorimetry midpoint glass transition temperature (Tg) of 0 °C (ASTM D3418-21) imparts room-temperature tack, while the minimum film-forming temperature (MFFT) is commensurate at 0 °C (ASTM D2354-10(2019)). The dried film exhibits a density of 1.08 g/cm³ and a surface energy of 44 mN/m (Owens-Wendt two-liquid method), which is sufficient for wetting corona-treated polyethylene without primer.

    Table 1. Airflex 426 Typical Physical Properties
    PropertyValueTest Standard
    Solids content65%ASTM D1489-21
    pH4.5–5.5
    Brookfield RV viscosity (25 °C)2,000–4,000 mPa·sASTM D2196-18
    Average particle size (D50)0.8 µmLaser diffraction
    Acid number (dry polymer)15–25 mg KOH/gTitration
    Tg (DSC midpoint)0 °CASTM D3418-21
    MFFT0 °CASTM D2354-10(2019)
    Density (liquid)1.08 g/cm³ASTM D1475-20
    Surface energy (dried film)44 mN/mOwens-Wendt

    Zinc ammonium carbonate crosslinking drives D3/WATT 91 durability in beech assembly adhesives

    For structural wood bonding requiring a D3 classification under DIN EN 204:2016, Airflex 426 is crosslinked with zinc ammonium carbonate (ZAC) solution at 3.0 wt% (dry zinc oxide on wet emulsion). The addition is made under 500 rpm paddle agitation for 10 min to avoid localized gel particles. Pot life at 23 °C, defined as the time for viscosity to double from an initial mixed value of 3,200 mPa·s, extends to 6–8 h; at 35 °C this collapses to 2.5 h, imposing a firm processing window on continuous extrusion coaters lacking chilled hoppers. Bonded beech specimens conditioned at 20 °C/65% RH for 7 days routinely develop mean tensile shear strengths of 2.5 N/mm² and survive 4 h cold-water soak with residual strengths above 1.8 N/mm², thereby exceeding the normative 1.0 N/mm² D3 threshold. After the WATT 91 boil test (1 h boiling water, 2 h cold water), values remain above 1.2 N/mm², a result unattainable with non-carboxylated VAE emulsions. Zinc ions coordinate carboxylate groups to form a pseudo-crosslinked network; dynamic mechanical analysis (DMA) of a film post-cured for 72 h at 23 °C shows a storage modulus E′ at 150 °C of 8.2 MPa versus 1.8 MPa for the uncrosslinked control, yielding a calculated crosslink density near 1.2 × 10⁻³ mol/cm³ from rubber elasticity. The formulation pH must remain below 5.5 to prevent precipitation of zinc hydroxide; ammonia evolved during drying can raise pH locally, and forced ventilation of the bond line during assembly is recommended to avoid a chalky surface that degrades adhesion.

    What differentiates high-solids carboxylated VAE from standard VAE in roll-coat paper lamination?

    On a production-scale roll coater with a metering rod applying a wet film of 40 g/m² to 250 g/m² kraft linerboard, the higher solids of Airflex 426 reduce the water load by 18% compared to a conventional 55% solids VAE. This translates into a measurable open-time advantage: at 25 °C and 50% RH, the adhesive surface becomes tack-free in 8 s—assessed by finger transfer—whereas a 55% solids VAE required 25 s under identical conditions. The consequence on a laminator running at 60 m/min is a reduction in blocking tendency at the wind-up reel; edge-weld defects, which occurred at 12 per 10,000 m run with the standard grade, dropped to fewer than 1 per 10,000 m. Instantaneous green bond strength, measured with a spring-loaded wheel pull-off device (in-house method approximating ASTM D1876), reached 0.5 N/15 mm within 2.0 s of nip closure, nearly double the 0.3 N/15 mm of the lower-solids comparator. This early strength development, coupled with a final T-peel value of 6.8 N/15 mm after 24 h conditioning, permits the converter to accelerate line speed without sacrificing die-cut precision. The carboxylic acid functionality further contributes to re‑pulpability: handsheets prepared according to TAPPI T 205 sp-18 from laminated board showed 95% fiber recovery after alkaline repulping at 50 °C, as the ionic linkages disassociate above pH 8.5.

    Adhesive film formation on low-energy surfaces and the role of carboxyl groups in interfacial adhesion

    Airflex 426 coalesces without co-solvent above its MFFT, forming a continuous film that adheres to corona-treated polyethylene terephthalate (PET) with a dyne level of 52 mN/m (ASTM D2578-23). Lap shear adhesion to 50 µm biaxially oriented polypropylene (BOPP, treated to 40 mN/m) was measured at 2.1 N/cm after 48 h conditioning at 23 °C/50% RH (ASTM D3163-01). The carboxyl groups promote specific hydrogen-bonding interactions with oxidized polymer surfaces, raising the work of adhesion compared to non-functional VAE grades. In production, the emulsion is often blended with 1–2 wt% of an aliphatic polyurethane dispersion (PUD) to increase ultimate peel strength; without the PUD additive, lap shear after 7-day aging at 40 °C maintains 85% of the initial value, indicating resistance to thermal deactivation of the interface. A limiting factor is the sensitivity of the carboxylated polymer to residual alkaline cleaners on film surfaces: NaOH concentrations above 0.01 wt% on the substrate cause in‑situ ionomer conversion at the interface, reducing peel strength by 30%. A distilled-water rinse prior to lamination is required when alkaline pre-treatment is used.

    In high-frequency wood gluing operations, where the adhesive must tolerate rapid dielectric heating, the ionic character of Airflex 426 reduces the incidence of arcing. The carboxylic acid groups, partially neutralized to sodium salt during emulsion manufacture (yielding a pH of 4.5–5.5), confer a specific conductivity of approximately 1.5 mS/cm, which dissipates charge accumulation in the glue line. On a 27.12 MHz Holz-Her Acoustic high-frequency press bonding 40 mm thick beech blocks with a 3-second cycle, arcing events recorded per 1,000 cycles dropped from 12 with a non-carboxylated VAE of identical solids to 1. This operational benefit comes with a corrosion caveat: neutralization levels above 10 mole% of total carboxyl content promote pitting on 304 stainless steel applicator rolls; 316L stainless or Hastelloy C-22 is specified for continuous-contact parts in such high-moisture environments. Additionally, the carboxylated latex is incompatible with borax (sodium tetraborate decahydrate), which causes instantaneous gelation through polyionic complexation. Any dextrin-based tackifier blends must be reformulated with benzoate ester plasticizers, added at 3–5 wt% on emulsion, to avoid press-clogging during rotary screen application.

    Table 2. Comparative Performance: Airflex 426 versus Standard VAE and Carboxylated SBR
    PropertyAirflex 426 (65% solids)Standard VAE (55% solids)Carboxylated SBR (50% solids)
    Film tensile strength (MPa, ASTM D882-18)6.55.04.0
    Elongation at break (%)650800900
    Water absorption — 24 h immersion (wt%, ASTM D570-98)8.5 (ZnO crosslinked)2512 (sulfur‑cured at 150 °C)
    Wood tensile shear — D3 (DIN EN 204)Pass (>2.0 N/mm²)Fail (<1.0 N/mm²)Pass (with crosslinker)
    Paper-to-paper T-peel (N/15 mm, ASTM D1876)6.84.23.5
    Re-pulpability (TAPPI T 205)Good (ionic, pH-reversible)FairPoor (sulfur crosslinks)
    Pot life at 23 °C (crosslinked)6–8 hNot applicable4 h (with accelerator)

    Because the carboxylated VAE network is formed ionically, heat resistance differs fundamentally from vulcanized SBR: service temperatures above 120 °C cause progressive decarboxylation and network collapse. The emulsion is therefore unsuited to engine-housing hot‑melt replacements. Furthermore, the anionic charge demands careful selection of wetting agents—cationic or strongly acidic surfactants cause macro‑gelation within minutes. Storage stability of the unopened container at 5–35 °C exceeds 12 months, but repeated freeze‑thaw cycles must be avoided: the latex coagulates irreversibly below 0 °C. For full performance, the minimum application temperature must exceed the MFFT by at least 5 °C, and materials should be pre‑conditioned when relative humidity exceeds 60%.