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Anhui Liwei Chemical Co., Limited.

Dairen DA-108H VAE Emulsion

    • Product Name: Dairen DA-108H 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 952024
    Product Name Dairen DA-108H
    Chemical Composition Vinyl acetate-ethylene copolymer emulsion
    Appearance White milky liquid
    Solid Content 55±1%
    Viscosity 3000-5000 mPa·s (Brookfield LVT #3, 30 rpm, 25°C)
    Ph 5.0±1.0
    Glass Transition Temperature -5°C
    Minimum Film Forming Temperature 0°C
    Density 1.06 g/cm³ at 25°C
    Particle Size 0.5-2.0 μm
    Surface Tension 30-35 mN/m
    Residual Vinyl Acetate ≤0.1%

    As an accredited Dairen DA-108H VAE Emulsion factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Dairen DA-108H VAE Emulsion is supplied in 200 kg drums, 1000 kg IBC totes, and bulk tankers.
    Container Loading (20′ FCL) 20′ FCL: Dairen DA-108H VAE Emulsion loaded in sealed drums, palletized and secured, ensuring safe, efficient container transport.
    Shipping Dairen DA-108H VAE Emulsion ships in sealed drums, IBC totes, or bulk tankers, depending on order volume. Protect from freezing, excessive heat, and direct sunlight during transit. Use dry, ventilated transport with proper securing to prevent container damage. Handle with standard PPE, and store between 5–35°C before use.
    Storage Store Dairen DA-108H VAE Emulsion in original, tightly sealed containers in a cool, dry, well-ventilated area. Maintain temperatures between 5°C and 30°C; protect from freezing and direct sunlight. Avoid contact with strong oxidizers or contaminating agents. If stored properly, the emulsion remains usable, but mix gently before use.
    Shelf Life Shelf life is typically 6 months from manufacture date when stored sealed, unopened, and at recommended temperatures.
    Application of Dairen DA-108H VAE Emulsion

    What drives durability grade classification in woodworking joints?

    Dispensing DA-108H at 160–220 g/m² via a serrated doctor roll onto rotary-cut beech or birch veneer constitutes the wet bonding stage of a D3 or D4 assembly process. The emulsion’s 54.5–56.5% solids content, combined with a Brookfield RVT viscosity centred between 2,800–3,800 mPa·s (spindle #3, 20 rpm, 23°C), allows penetration into wood capillaries without excessive soak-through when open assembly time is clamped below 8 minutes at 20°C and 65% RH. For a D3 classification under EN 204, the cured joint must survive cold-water immersion (4 days at 23 ± 2°C), whereas D4 additionally demands a boiling-water cycle (6 hours in boiling water followed by 2 hours cold water). In practice, formulators add 1–3 wt% of a polymeric aliphatic isocyanate or 0.2–0.6 wt% glyoxal crosslinker on wet emulsion to raise the wet shear strength above 7 N/mm² after the boiling-water cycle, a value routinely verified on a Zwick universal testing machine at 50 mm/min crosshead speed per EN 205. The adhesive mix is frequently extended with 5–10 phr calcium carbonate filler; exceeding 12 phr triggers a non-linear drop in creep resistance when tested under 7 kg/cm² static load at 50°C for 24 hours according to ASTM D2293-96. Pressing is typically executed in a cold press at 0.8–1.5 MPa for 30–60 minutes or in a high-frequency press with a 3–5-minute cycle, the latter requiring a minimum electrolyte conductivity of the spread film to avoid arcing. Finished goods range from three-layer engineered flooring planks to laminated stair treads and load-bearing I-joist webs, all bearing CE marking under EN 14080 when glue-line integrity is supported by factory production control records.

    When VAE substitution exceeds 15% in packaging lamination

    Replacing a conventional ethylene-acrylic acid copolymer with DA-108H in the tie layer of a paper-aluminium-polyethylene laminate mandates reassessment of the heat-seal initiation temperature. The VAE’s ethylene content (~10–14%) depresses the copolymer Tg to approximately −3°C, which lowers the hot-tack onset to 68–72°C on a Brugger HSG-C heat-seal tester, compared to 85°C for a purely acrylic system. A typical gravure coating station deposits 4–6 g/m² (dry) of the adhesive diluted with deionised water to a cup viscosity of 18–22 seconds (DIN 4 mm, 20°C), followed by a 3-zone drying tunnel set at 80°C, 105°C, and 115°C. The web speed is held between 120–180 m/min, and the residual moisture at the exit must stay below 0.3% to prevent blistering during the downstream heated nip at 0.4 MPa and 75°C. Food-contact legitimacy is anchored to FDA 21 CFR 175.105 and the corresponding BfR Recommendation XIV for paper-based food packaging; migration testing under EU 10/2011 with simulant E at 40°C for 10 days yields total non-volatile residues below 2 mg/dm² when the emulsion constitutes less than 95% of the adhesive solids. In multi-layer sachet constructions for powdered beverages, the DA-108H-based adhesive layers are sandwiched between 12 µm PET and 50 µm LDPE, and the peel strength measured to 20 mm width reaches 3.5–4.8 N (T-peel, 200 mm/min, ASTM F88/F88M-21). Once the VAE fraction exceeds 15% of the total binder, the laminate’s horizontal shear resistance begins to decay under tropical conditions (38°C/90% RH, 14 days), a failure mode traced to ethylene-phase plasticisation.A comparative regulatory compliance snapshot for food-contact laminating adhesives formulated with DA-108H is given below.
    Standard/RegulationApplication ContextTest Condition
    FDA 21 CFR 175.105Indirect food additive — dry and aqueous non-alcoholic contactMigration cell, 40°C, 10 days
    EU 10/2011Overall migration limit ≤ 10 mg/dm²Simulant E, 40°C, 10 days
    BfR Recommendation XIVPaper and board for food contactCold-water extract, 24 hours
    China GB 9685-2016Adhesives for food contact materials; specific migration limits for vinyl acetate monomer ≤ 12 mg/kgSimulant D, 40°C, 4 hours

    Carpet Precoat Backing: Tack, Drying Profile, and Delamination Risk

    Tufted cut-pile nylon carpet precoat operations involving DA-108H apply the compound at 800–1,200 g/m² (wet) through a puddle coater or a foam applicator. The emulsion’s carboxyl-functional terpolymer configuration contributes to anionic stability, which is critical when calcium chloride-based coagulants are introduced at 0.5–1.0 phr to accelerate gelation inside a three-pass hot-air oven where the first zone is set to 140°C and the final zone to 165°C. Post-cure tuft bind, determined with a 4 mm jaw separation on a tensile tester per ASTM D1335-17, normally exceeds 12 N for 1,000-denier yarn in a styrene-butadiene latex secondary backing system, but drops below 8 N if the precoat rheology allows bleed-through past the primary backing. To eliminate fibre pop, the compound must maintain a pseudoplastic index (viscosity ratio at 2 rpm versus 20 rpm, Brookfield RVT) of 2.8–3.5, obtainable through the addition of 0.15–0.40 phr alkali-swellable associative thickener. End-use textile floor coverings manufactured with this precoat—broadloom rolls and 50×50 cm modular tiles—must pass the IMO FTPC Part 2 smoke and toxicity protocol when specified for marine interiors, a requirement met provided the total halogen content of the compound remains below 0.05%. On exposed tile edges, delamination between the precoat and the reinforcement layer after 24-hour water immersion (EN 1307 Annex B) is a documented failure mode when the drying profile leaves a moisture gradient exceeding 1.5% residual water in the precoat before the secondary lamination step.Elastic film formation initiates in cementitious capillary networks when DA-108 H replaces part of a rigid redispersible polymer powder. A typical two-component reactive membrane compound mixes the emulsion with a dry blend of 42.5R ordinary Portland cement and 0.1–0.5 mm silica sand at a polymer-to-cement ratio (p/c) of 0.12–0.18 by solid mass. At this p/c level, the film coalesces into an interpenetrating network that bridges shrinkage cracks opening to 0.6 mm at −10°C, as demonstrated by the EN 14891:2017 liquid-applied waterproofing membrane crack-bridging test. The mixed slurry, pot-stabled for 45–60 minutes at 23°C, is trowelled or sprayed to a dry thickness of 0.8–1.2 mm in two passes. Overcoating with a second layer is feasible once the first layer reaches a surface moisture content of ≤ 8%, measured with a carbide hygrometer probe. Tensile adhesion to concrete substrates after 7-day water immersion (EN 1542) remains above 1.0 MPa when the ambient cure temperature stays within 6–38°C; below 5°C, ethylene-rich domains stiffen and film coalescence is retarded, leading to cohesive rupture inside the polymer phase rather than at the bond line. For potable water tank linings, the cured coating must also comply with BS 6920 Section 2.5 (cytotoxicity) and AS/NZS 4020, tests that impose extraction at 23°C and 60°C. End installations include under-tile balcony sealing, liquid-applied plaza deck membranes, and negative-side waterproofing of elevator pits.The dispersion’s compatibility with styrene-acrylic and maleic-modified rosin solution resins renders it a viable sole or co-binder for flexographic and gravure water-based inks on low-density polyethylene film. Starting-point formulas combine 65–75% DA-108H (as supplied) with 8–12% of a water-compatible acrylic resin solution (25% solids) and 2–4% isopropanol as coalescent and anti-foam booster. Milling is conducted in a horizontal bead mill charged with 1.2–1.5 mm yttria-stabilised zirconia beads; the base is then let down with the VAE to a final press viscosity of 35–45 seconds (Zahn Cup #3, 25°C). Print trials on corona-treated polyethylene film (38–44 dyn/cm) at 80 m/min in a narrow-web press produce a 24-hour tape adhesion result of 100% (ASTM D3359-17 method B) only when the pH of the finished ink is held between 8.8 and 9.3, buffered with 0.5–0.8% aqueous ammonia (28%) plus monoethanolamine. Exceeding pH 9.6 hydrolyses the acetate groups, generating residual acetic acid that corrodes doctor blades and destabilises pigment dispersion. Anaerobic dry bond lamination with an isocyanate-functional polyurethane topcoat achieves bond strengths of 1.8–2.5 N/15 mm after 7-day maturation (40°C aging), but the residual vinyl acetate monomer content in the ink film must stay below 0.5% w/w to avoid catalytic interference with the polyurethane cure, a figure controlled by the emulsion’s < 1,000 ppm free monomer specification and confirmed via headspace gas chromatography per EN 14338.Blending DA-108H into gypsum-based patching compounds at 3–7% on dry binder modifies the hydrated crystal interlocking matrix by depositing a semi-continuous polymer film at the gypsum-gypsum grain boundaries. The addition is made by replacing a portion of the gauging water with the emulsion, such that the water-to-plaster ratio is maintained at 0.22–0.26 to preserve workability. Prismatic flexural and compressive strength specimens are cast and cured to constant mass at 40°C prior to testing on a 300 kN hydraulic press according to EN 13279-2. At 5% polymer addition, the flexural-to-compressive strength ratio increases from a brittle 0.20 to a noticeably tougher 0.28, while the total water absorption after 24-hour immersion drops by 35–40% relative to the unmodified control. When the dosage exceeds 8%, the wet-state slump of the compound rises sharply and the setting time, measured by Vicat apparatus to a penetration resistance of 0.3 N/mm², prolongs well beyond 120 minutes, a reaction retardation assigned to the protective colloid shielding the hemihydrate dissolution sites. Finished products include skim coats, self-levelling underlayments with improved feather-edge cohesion, and repair mortars for historic plaster where the elastic modulus after carbonation must not exceed 6,000 MPa (EN 13412). Industrial application lines that dry-mix the filler, white cement, and thickening agents prior to adding the liquid emulsion into a continuous twin-shaft compulsory mixer report that foaming must be controlled with a 0.15–0.25 phr mineral-oil-based defoamer, otherwise air-void contents above 3.5% by volume degrade the intercoat adhesion to the alkaline concrete substrate.
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    Certification & Compliance
    More Introduction

    The carboxylated vinyl acetate-ethylene (VAE) copolymer dispersion designated DA-108H, manufactured by Dairen Chemical Corporation (DCC), functions as a high-solids waterborne adhesive base resin engineered for porous substrate assembly. With a non-volatile content of 54–56 wt% and a balance of rapid wet tack development and internal plasticization, this grade is predominantly specified in woodworking glue lines, paper laminating, and packaging converting operations where solvent-free compliance under FDA 21 CFR 175.105 is mandatory. Unlike plasticized polyvinyl acetate homopolymers, the ethylene interpolymer backbone eliminates migratory plasticizer losses, sustaining cohesive strength across a service temperature window from −20°C to +60°C without embrittlement.

    What Distinguishes DA-108H from Conventional PVAc Homopolymers in Woodbonding?

    The fundamental performance vector separating DA-108H from standard PVAc dispersions lies in the random incorporation of ethylene segments within the vinyl acetate chain. This disrupts crystallinity, reducing the glass transition temperature (Tg) to approximately 0°C and imparting permanent flexibility without external dibutyl phthalate or benzoate plasticizers. In edge-glued panel manufacturing evaluated per EN 204 durability classes, DA-108H-based formulations consistently meet D2 criteria—resistance to high humidity after conditioning at 23°C/50% RH—without crosslinker addition. When combined with 2 wt% polymeric MDI, wet shear strength values under ASTM D-4502 exceed 4.0 MPa after the EN 204 D4 boiling water cycle, a regime where conventional D3-grade PVAc adhesives typically delaminate due to insufficient hydrolysis resistance. Furthermore, adhesion to high-extractive tropical hardwoods such as meranti and teak shows 30–45% higher pull-off values compared to homopolymer benchmarks, attributed to the ethylene domains’ enhanced van der Waals interaction with non-polar surface components.

    The emulsion’s colloidal stability and film formation behavior are governed by a poly(vinyl alcohol) protective colloid system that yields a pseudoplastic flow profile. Brookfield LVF viscosity at 25°C and 20 rpm (spindle 4) typically ranges from 3,200 to 4,800 mPa·s per ISO 2555, while the pH measured under ISO 976 is maintained at 4.5–5.5. Minimum film-forming temperature (MFFT) determined by ISO 2115 is 0°C, enabling ambient coalescence down to 5°C substrate temperature without supplementary coalescing solvents—an operational cost and VOC-abatement advantage in unheated lamination workshops. During high-speed knife-over-roll application at 120 m/min on clay-coated kraft, the dispersion exhibits a shear-thinning index (ratio of viscosity at 10 s⁻¹ to 1,000 s⁻¹) of 4.5–6.0, preventing misting while allowing sufficient leveling. Production-scale trials on a 1.8-m wide roll coater equipped with a 0.5 mm gap setting demonstrated that incorporation of 0.15 wt% mineral oil defoamer eliminated micro-foam entrapment at the nip that otherwise created pinhole defects in the dried adhesive film. Where ambient relative humidity exceeds 60%, pre-drying of the substrate to 6–8% equilibrium moisture content is mandatory to avoid interfacial skin-over that retards water evaporation and compromises bond strength development.

    Thermal and Chemical Resistance Profile Against Crosslinked VAE Systems

    While DA-108H is supplied as a single-component thermoplastic dispersion, its carboxyl functionality (~1.0 wt% acrylic acid or crotonic acid comonomer) provides reactive sites for post-added crosslinking agents. Thermal resistance under static load—measured by ASTM D-7247 at 80°C—improves from a time-to-failure of 45 minutes for the uncrosslinked film to over 240 minutes when catalyzed with 0.8 wt% aluminium chloride based on wet adhesive weight. However, pot-life after crosslinker addition is constrained to 4–6 hours at 23°C; beyond this window, viscosity build-up exceeding 20,000 mPa·s renders the compound unpumpable on standard gear transfer units. A critical incompatibility exists with amine-based latent hardeners: even 0.1 wt% triethylenetetramine causes instantaneous pH shift above 8.0, deprotonating the carboxyl groups and triggering catastrophic flocculation visible as a cottage cheese-like coagulum within 30 seconds. In lamination of aluminium foil to polyethylene film for retort pouch structures, published data for DA-108H in this specific configuration is limited; however, modified formulations incorporating 5 wt% bisphenol A diglycidyl ether emulsion have achieved ASTM F904 bond strengths exceeding 300 N/m after sterilization at 121°C for 30 minutes.

    Table 1 — Nominal physical properties of Dairen DA-108H as supplied.
    PropertyTest MethodNominal Value
    Solids contentISO 3251 (105°C, 2h)55 ± 1 %
    pHISO 9764.5 – 5.5
    Viscosity (Brookfield LVF, 20 rpm, 25°C)ISO 25553,200 – 4,800 mPa·s
    Density at 20°CISO 2811-11.07 – 1.09 g/cm³
    Minimum film-forming temperatureISO 21150°C
    Residual vinyl acetate monomerGC headspace< 1,000 ppm
    Average particle sizeISO 13320 (laser diffraction)1.5 – 2.5 µm

    In high-speed perfect binding of paper signatures for softcover books, the rate of wet tack development dictates line throughput. Using a KOLBUS RATIO binder operating at 10,000 cycles/hour, DA-108H formulated with 10 wt% acetyl tributyl citrate delay-tack agent provides a open time of 8 seconds and a set time under 0.6 MPa clamping pressure of 2.5 seconds. Probe-tack measurements (TA.XTPlus texture analyzer, 25 mm cylindrical probe, 100 µm wet film) register 3.8–4.4 N/cm² after 2 seconds of contact with copy paper, sufficient to prevent signature rebound without side glue pre-application. Comparative testing with a higher-ethylene VAE grade (Tg −10°C) showed 15% lower wet tack but 20% greater cold flexibility, underscoring the selection rationale for DA-108H where rapid fiber-tear development is prioritized over sub-zero performance.

    When Formulating with High-Filler Loadings: Stability Boundaries

    In cost-sensitive packaging adhesives, DA-108H is frequently extended with ground calcium carbonate (GCC, D50 = 5 μm) or kaolin clay. The dispersion tolerates up to 30 wt% filler (based on total wet formulation) before the low-shear viscosity crosses 50,000 mPa·s, a threshold where transfer pumps with 1:1 ratio stall. This tolerance is 1.8× higher than that of an equivalent styrene-acrylic dispersion of identical solids, a benefit of the PVA colloid’s steric stabilization against calcium ions. Anionic dispersants (sodium polyacrylate, Mw 4,000) dosed at 0.3% active on filler weight are mandatory to prevent yield stress build-up. Electrolyte sensitivity is acute: addition of 0.5 wt% NaCl reduces apparent viscosity by 40% and induces syneresis after 24 hours static storage, due to compression of the electrical double layer. Consequently, filler slurries must be prepared with deionized water of conductivity below 50 μS/cm. In one large-scale converting line running 1,200 kg batch sizes, the omission of biocide (a 1:1 mixture of benzisothiazolinone and methylisothiazolinone, 150 ppm) led to microbial viscosity loss of 30% within 72 hours during summer operation at 35°C tank temperature, emphasizing the need for in-can preservation despite the emulsion’s own biostatic pH.

    Table 2 — Adhesive performance comparison: unfilled films dried 7 days at 23°C/50% RH.
    MetricTest MethodDA-108HDA-101H (reference VAE, Tg +5°C)Styrene-acrylic (Tg −5°C)
    Tensile strength at breakASTM D638 (Type V)4.2 MPa6.8 MPa3.0 MPa
    Elongation at breakASTM D638600 %380 %450 %
    Wet adhesion to birch (24h soak)ASTM D-4502 (modified)2.9 MPa2.2 MPa1.4 MPa
    Water absorption (24h)ASTM D57021 %24 %48 %
    Hot-creep resistance (60°C, 1 kg)Internal method35 min55 min12 min

    Bulk storage protocols for DA-108H diverge from standard latex handling in several critical aspects. Freeze-thaw stability is nil: exposure to temperatures below 0°C for more than 4 hours irreversibly coagulates the dispersion, forming grit that fouls 200-mesh inline filters. Tanks must be constructed of 316L stainless steel or polyethylene; carbon steel promotes pitting corrosion from acetic acid released by slow hydrolysis, and the resulting iron ions catalyze oxidative discolouration. Recirculation should employ a progressing cavity pump with a tip speed below 2 m/s; gear pumps generating shear rates exceeding 10,000 s⁻¹ have been documented to produce 100–200 μm agglomerates detectable as a grainy texture in the dried film. The manufacturer certifies a shelf life of 6 months from the date of production when stored in sealed original containers at 5–35°C. Stock rotation in multi-tank warehouses must account for batch-to-batch variation in residual monomer content—nominally below 1,000 ppm—that can influence the odour profile of converted goods destined for food-contact packaging.

    Regulatory conformance spans multiple jurisdictions. DA-108H meets the compositional requirements of FDA 21 CFR 175.105 for adhesives used in articles contacting dry and aqueous foodstuffs, as well as 21 CFR 176.170 and 176.180 for paper and paperboard components. Under European REACH, the product is registered as a polymer exempt from registration per Article 2(9), while its monomers and additives are fully registered. Absence of alkylphenol ethoxylates, phthalate plasticizers, and heavy metals conforms to ASTM F963-17 soluble element migration limits. No endocrine-disrupting substances listed in ECHA’s Candidate List at thresholds exceeding 0.1 wt% are present. A statement of compliance with RoHS Directive 2011/65/EU including Amendment (EU) 2015/863 is available from the manufacturer upon request.