Productos

Productos

Anhui Liwei Chemical Co., Limited.

Emulsión Dairen DA-102 VAE

    • Nombre del producto: Emulsión Dairen DA-102 VAE
    • Sitio de fábrica: Lingwu, Yinchuan, Ningxia, China
    • Consulta de precio: sales2@liwei-chem.com
    • Fabricante: Anhui Liwei Chemical Co., Limited.
    • Contactar Ahora
    Especificaciones
    Código HS 304886
    Nombre Del Producto Emulsión Dairen DA-102 VAE
    Apariencia Líquido lechoso blanco
    Contenido Sólido 55 ± 1
    Viscosidad Cps 500 - 1500
    Valor De Ph 4,5 - 6,0
    Tamaño De Partícula μm 0,5 - 2,0
    Temperatura De Transición Vítrea C -5
    Densidad G Cm³ 1,05 - 1,10
    Tensión Superficial Dyn Cm 30 - 40
    Estabilidad De Congelación Descongelación Estable hasta 5 ciclos
    Estabilidad De Almacenamiento 6 meses a 5-35°C

    Como fábrica acreditada de Emulsión Dairen DA-102 VAE, hacemos cumplir estrictos protocolos de calidad: cada lote se somete a rigurosas pruebas para garantizar estándares consistentes de eficacia y seguridad.

    Embalaje y almacenamiento
    Embalaje Dairen DA-102 VAE Emulsion se suministra en tambores sellados de 200 kg, etiquetados con detalles del producto e instrucciones de manejo de seguridad.
    Carga De Contenedores (20 'FCL) 20 'FCL: Emulsión VAE en tambores paletizados /IBC, asegurada, carga de contenedores optimizada, estiba segura, peso equilibrado para el tránsito.
    Envío La emulsión Dairen DA-102 VAE se envía en tambores sellados o bolsas IBC. Proteger de la congelación y el calor extremo; almacenamiento ideal entre 5 y 35 ° C. Utilice contenedores secos y ventilados, manténgase en posición vertical y evite la exposición prolongada a la luz solar. No clasificado como mercancía peligrosa, pero siga los procedimientos estándar de manejo de productos químicos y contención de derrames.
    Almacenamiento Guarde la Emulsión Dairen DA-102 VAE en recipientes originales herméticamente cerrados en un área fresca, seca y bien ventilada. Evite la luz solar directa, las fuentes de calor y la congelación; mantenga temperaturas entre 5 ° C y 35 ° C. Mantener alejado de oxidantes fuertes y materiales incompatibles. Úselo dentro de la vida útil recomendada y revuelva suavemente antes de usar si se produce una separación.
    Duración La vida útil es de 6 meses a partir de la fecha de fabricación cuando se almacena correctamente; evite la congelación y mantenga entre 5 y 40 ° C.
    Aplicación de Emulsión Dairen DA-102 VAE

    The substitution of solvent-borne polyurethane dispersions in hardwood assembly applications becomes technically viable when a polyvinyl acetate-ethylene copolymer such as Dairen DA-102 is formulated to satisfy the EN 204 D3 durability classification, which mandates a minimum wet shear strength of 2.0 N/mm² after immersion in cold water for 4 days according to the test sequence specified in EN 205:2016. In beech-to-beech lap joints cured at 0.8 MPa clamping pressure under ambient conditions, wood failure percentages exceeding 85% are consistently recorded at an adhesive dry solids pickup of 150–180 g/m² applied by toothed roller coater. The addition ratio of DA-102 in the final compounded adhesive typically varies between 88 wt% and 94 wt%, with the remainder comprising a combination of polyvinyl alcohol protective colloid not exceeding 3.0 wt%, an aluminum chloride catalyst at 0.3–0.6 wt% to accelerate chain entanglement during cold pressing, and a defoamer based on mineral oil at 0.2 wt%. Production processes in finger-jointed solid wood panels intended for interior door stiles follow a sequence of twin-belt press feeding at linear speeds of 15–25 m/min, where the open assembly time must remain within 8–12 minutes at 23°C and 50% RH to prevent skin-over that compromises penetration into vessel elements of ring-porous species such as oak. The finished goods include laminated kitchen benchtop substrates, cross-laminated solid wood edge-glued panels for shelving, and structural finger-jointed studs used in timber-frame construction certified under EN 14080:2013. One observed processing boundary is the rapid viscosity increase above 40°C storage temperature, which triggers partial grafting of acetate groups onto the hydroxyl functionality of cellulosic thickeners, rendering the pot life shorter than the 90-minute window demanded by automated spreaders.

    What governs the wet tack performance of VAE emulsions in high-speed paper lamination?

    High-speed alcohol-resistant laminating adhesives for security envelope window film attachment operate at line speeds exceeding 200 m/min and impose a wet tack threshold of at least 8 N/25mm within 0.4 seconds of combining, a requirement met by DA-102 when formulated at 54–56% solids with 2.5 phr of a rosin ester dispersion having a softening point of 85°C. The adhesive is delivered via a slot-die coating station with a gravure roll engraved at 60 lines/cm and a cell depth calibrated to transfer 3.2–3.8 g/m² dry coat weight onto 60 g/m² bleached kraft paper. Regulatory compliance for indirect food contact in dry food packaging is documented under FDA 21 CFR 175.105 and the applicable migration limit for vinyl acetate monomer is controlled below 2 ppb in 10% ethanol simulant according to EU Regulation 10/2011 annex I. The downstream process involves unwinding the paper roll through a 4-roll tension-controlled accumulator, applying the adhesive only on the flap area, and subsequently marrying it with a polypropylene window patch under a nip roll exerting a linear load of 15 N/cm. End products range from bank statement envelopes to tamper-evident courier pouches, where the bond must survive 48-hour conditioning at 40°C and 90% RH without delamination. A limitation encountered on water-based flexo presses is foam generation when return flow exceeds 30 L/min in a closed-chamber doctor blade system; therefore, a silicone-free defoamer metered at 0.15% on wet weight is required.

    Manual roller coating of low-VOC interior paints demands rheology that prevents spatter while ensuring film coalescence above 5°C. When Dairen DA-102 is incorporated at 22–28 dry weight percent of the total formulation as the sole binder, the resulting paint meets the EU Directive 2004/42/CE phase II limit of 30 g/L VOC for matte wall finishes. The compliance path is validated through ISO 11890-2:2020 headspace gas chromatography, confirming residual vinyl acetate monomer below 100 ppm. Pigment volume concentration is maintained between 45% and 55% using rutile titanium dioxide at 17° and a coarse calcium carbonate extender with a median particle size of 5 µm, dispersed on a high-speed dissolver equipped with a 450 mm diameter Cowles blade rotating at 18 m/s tip speed. The factory-scale tinting process integrates a volumetric dispenser dosing 4 mL/L of phthalocyanine blue colorant into the let-down phase, and the finished paint passes 5,000 cycles of wet scrub resistance under ISO 11998:2006 with a film thickness loss of less than 15 µm. End-use products include odor-free nursery wall coatings applied by airless spray at 180 bar and contract-grade emulsion for hotel corridors where the dried film must resist staining from quaternary ammonium disinfectants. A known formulation constraint is the incompatibility with strong amine-based pH adjusters like 2-amino-2-methyl-1-propanol above 0.5 wt%, which causes yellowing and a rubbery coagulum at the air-liquid interface in storage containers.

    Crack-bridging polymer-modified cementitious waterproofing slurries

    Two-component flexible cementitious waterproofing membranes produced under EN 14891:2017 for liquid-applied water impermeable products beneath ceramic tiling achieve the required crack-bridging ability of at least 0.75 mm at −5°C when the liquid component contains 65–75% by mass of DA-102 blended with 25–35% water and 0.5% of a hydrophobic silane oligomer. This liquid admixture is combined with a powder blend of ordinary Portland cement conforming to EN 197-1 CEM I 42.5 N, silica sand graded 0.1–0.5 mm, and microsilica at 5% of cement weight in a mixing ratio of 0.40–0.45 liquid-to-powder by mass. The mixing step employs a forced-action paddle mixer rotating at 400 rpm for 120 seconds, producing a slurry with a Brookfield viscosity of 15,000–22,000 mPa·s suitable for trowel application onto a primed concrete substrate at a wet film thickness of 1.5 mm. After a 28-day cure at 23°C and 60% RH, the membrane exhibits tensile adhesion strength to concrete exceeding 0.8 N/mm² (EN 1542:1999) and elongation at break above 100% (ISO 527-3:2018 specimen type 5 at 200 mm/min). The table below shows the variation in compressive and flexural properties across the working range of polymer-cement ratios. Finished applications include waterproofing of swimming pool basins subjected to hydrostatic pressure of 2.5 bar and balcony substrates exposed to thermal cycling from −20°C to +60°C. An operational boundary for site mixing is the narrow pot life window of 35–40 minutes at 30°C, beyond which a skin formation inhibits proper bonding to the second coat; retempering with additional water violates the manufacturer’s warranty and reduces long-term chloride ion resistance.

    Polymer:Cement Ratio (mass) Compressive Strength (EN 13892-2, MPa) Flexural Strength (ISO 178:2019, MPa) Crack Bridging at −5°C (EN 1062-7, mm)
    0.35 28.5 6.2 0.45
    0.40 21.3 7.8 0.72
    0.45 14.7 8.9 1.10
    0.50 10.4 9.1 1.35

    Paperboard lamination for aseptic beverage cartons subjects the adhesive line to hydrogen peroxide sterilization at 70–75°C for 12–18 seconds followed by exposure to a 35% hydrogen peroxide bath at 80°C before the application of a polyethylene extrusion coating. In this scenario DA-102 is employed at its native solids content of 55% without further compounding, deposited by a three-roll offset gravure applicator onto the back side of a liquid packaging board consisting of a bleached kraft liner, a chemi-thermomechanical pulp middle layer, and a low-density polyethylene barrier layer. The target dry coat weight is held to 1.8–2.2 g/m² to minimize burn-through during the subsequent extrusion of LDPE at 320°C melt temperature. The adhesive must comply with FDA 21 CFR 176.170 for components of paper and paperboard in contact with aqueous and fatty foods, as well as the German BfR Recommendation XXXVI for paper and board intended for food contact. Process monitoring relies on an in-line scanning infrared sensor calibrated to the carbonyl stretch at 1735 cm⁻¹, which triggers an alarm if coefficient of variation in coat weight exceeds 3.5% over a 10-second rolling window. Finished cartons holding ultra-high-temperature processed milk achieve a 6-month shelf life at ambient storage, and the adhesive layer survives the 25-minute retort cycle at 121°C required for neutral-pH dairy alternatives. Published data for this specific configuration is limited regarding long-term oxidative embrittlement under direct UV exposure, necessitating validation through ASTM G154 accelerated weathering for warehouse storage conditions exceeding 6 months prior to filling.

    When thermoplastic backcoating must simultaneously anchor loop pile yarns and resist bitumen bleed-through

    Carpet tile secondary backing adhesives formulated with VAEs having a glass transition temperature around 0°C are applied via puddle-coating onto the reverse side of a tufted polyamide 6,6 primary backing at a spread rate of 800–1,100 g/m² wet weight. A compound containing 85 parts DA-102, 15 parts calcium carbonate filler with a median particle diameter of 3 µm, and 1.5 parts of a melamine-formaldehyde crosslinker (hexamethoxymethylmelamine) cures at 140°C for 8 minutes in a five-zone tenter frame with air impingement nozzles delivering a velocity of 25 m/s. The final assembly must pass the ISO 24343-1:2012 peel test for textile floor coverings with a minimum force of 35 N/50mm, while also exhibiting less than 10% bitumen staining after contact with a hot-melt bitumen compound at 180°C in a simulation of the bitumen-backed carpet tile reheating that occurs during installation. Regulatory conformance under the European Construction Products Regulation 305/2011 requires declaration of formaldehyde emissions tested according to EN 717-2 at a chamber loading of 1.0 m²/m³, with values typically below 0.02 mg/m³. End products include open-plan office floor tiles of 50 cm × 50 cm dimensions and co-extruded stair treads with integrated edge reinforcement, all subjected to castor chair rolling tests per EN 985:2001. A critical processing failure mode manifests when the web tension in the stenter drops below 50 N, inducing crepeing of the coating surface that leads to audible squeak during simulated foot traffic at 1 Hz frequency.

    Thermal lamination of PET film to wetlaid polyester scrim achieves a kill step for microbial spores only above 135°C glueline temperature

    In the manufacture of sterile single-use surgical drapes, an autoclavable adhesive joint is required between a 25 µm polyethylene terephthalate film and a spunlaced polyester-cellulose nonwoven fabric weighing 45 g/m². A coated layer of DA-102 modified with 3.0% on dry weight of an epoxysilane adhesion promoter and thickened with a high-molecular-weight polyurethane associative thickener (HEUR) to a viscosity of 35,000 mPa·s at 10 s⁻¹ is applied using a knife-over-roll coater set to a gap of 150 µm, delivering 12 g/m² dry add-on. The lamination occurs in a double-belt press where the bonding zone temperature is ramped from 120°C to 140°C over a 45-second dwell, after which the composite is subjected to ethylene oxide sterilization at 55°C for 3 hours followed by a 14-day aeration to reduce residual EO below 4 ppm per ISO 10993-7:2008. The bioburden validation requirement follows ISO 11135:2014 and mandates no loss of bond strength exceeding 15% after a double sterilization cycle. This application falls under EU Medical Device Regulation 2017/745 for class I sterile devices, and the adhesive component must be traceable through the UDI database with a lot-specific certificate of analysis recording the glass transition midpoint by DSC (ISO 11357-2:2020) at −2±1°C. Finished goods are packaged in cleanroom class ISO 7 environments and released after bioburden and endotoxin testing according to USP <85>. An observed incompatibility arises with certain radiation-based sterilization methods where electron beam doses above 25 kGy cause chain scission in the ethylene sequences, reducing elongation at break by more than 30%, which restricts the composite to ethylene oxide or moist-heat sterilization only.

    Cotización gratuita

    Competitive Emulsión Dairen DA-102 VAE precios que se ajustan a su presupuesto - términos flexibles y citas personalizadas para cada pedido.

    Para muestras, precios o más información, contáctenos en +8615380400285 O envíelo por correo a sales2@liwei-chem.com.

    Le responderemos lo antes posible.

    Teléfono: +8615380400285

    Correo electrónico: sales2@liwei-chem.com

    Consulta

    Obtenga una cotización gratuita deAnhui Liwei Chemical Co., Limited.

    Condiciones de pago flexibles, precio competitivo, servicio de primera calidad: ¡consúltenos ahora!

    Certificación y cumplimiento
    Más Introducción

    Dairen DA-102 is a carboxylated, colloid-stabilized vinyl acetate-ethylene (VAE) copolymer emulsion designed for low-odor, solvent-free adhesive and binder formulations. The product is supplied at 55 ± 1% non-volatile content, with a pH of 4.5–5.5 (ISO 976) and a Brookfield RVT viscosity of 500–1500 mPa·s at 25 °C, spindle 3, 20 rpm (ISO 2555). The minimum film-forming temperature (MFFT) registers at 0 °C (ISO 2115), reflecting an ethylene comonomer weight fraction higher than that of Dairen DA-101 and conventional poly(vinyl acetate) homopolymers. This shift in copolymer composition depresses the glass transition temperature (Tg, mid-point DSC) to approximately 0 °C versus 10 °C for DA-101 and 30–35 °C for a standard PVAc homopolymer, permanently plasticising the polymer backbone without external plasticisers. Consequently, DA-102 films deliver dry tensile elongation values exceeding 500% (ASTM D638, 50 mm/min) while retaining cohesive strength sufficient for fibre-tearing bonds on cellulosic substrates. The emulsion’s carboxyl functionality provides reactive sites for crosslinking with polyvalent metal ions or glyoxal resins, enabling controlled adjustment of water resistance and heat resistance in finished articles.

    What Distinguishes DA-102 from Lower-Ethylene VAE Grades and Standard PVAc?

    The primary differentiator originates in the ethylene–vinyl acetate monomer ratio during emulsion polymerisation. Higher ethylene incorporation disrupts poly(vinyl acetate) crystallinity, permanently lowering the polymer’s Tg and imparting flexibility without migratory plasticisers. Table 1 contrasts DA-102 with two adjacent product classes. The data highlight that DA-102 occupies a midpoint: markedly softer than DA-101-type dispersions but substantially stronger in cohesive shear than ultra-low-Tg, rich-ethylene VAE grades typically reserved for pressure-sensitive applications. For hot-cleanup conditions, the reduced water-whitening tendency relative to pure PVAc becomes decisive, while the modulus remains high enough to avoid cold-flow problems in stack-rolled laminates.

    PropertyDA-102DA-101 (lower C2H4)PVAc Homopolymer
    Solids content (%)55 ± 155 ± 150–55
    Brookfield viscosity (mPa·s)500–15001000–25003000–8000
    MFFT (°C, ISO 2115)01018–20
    Film elongation at break (%, ASTM D638)> 500300–45010–30
    Water uptake, 24 h immersion (wt%, DIN EN ISO 62)15–2512–1840–60
    Cationic compatibilityControlled via carboxyl densityLimitedNone

    Adhesive Film Performance: Initial Tack, Shear Holding Power and Creep Behaviour

    DA-102 formulated with 2.5–5.0 wt% glyoxal-based crosslinker (on dry polymer) and applied to 50 µm PET film at 30 g/m² dry coat weight yields a loop tack value of 8–12 N/25 mm (FINAT FTM 9) and a static shear holding time exceeding 72 hours on stainless steel at 1 kg load and 23 °C, 50% RH. The failure mode transitions from cohesive to adhesive at crosslinker additions above 4.0 wt%. In high-speed carton-sealing lines, the emulsion’s initial wet tack on clay-coated board measured by a PT-1000 probe tack tester stabilises within 0.3–0.8 N/mm², enabling acceleration to 150 m/min belt speed without substrate slip. Because the polymer backbone is intrinsically tacky, total plasticiser demand drops by 30–50% relative to DA-101, reducing VOC emissions in formulated products. Thermal creep resistance on aluminium (tested per ASTM D3654 at 60 °C) remains below 0.5 mm/h displacement when a 0.5 mm bond line is post-cured at 22 °C for seven days. Specification writers should note that ambient humidity above 70% RH during film formation can retard water evaporation and lengthen the open time; pre-drying bonded substrates at 40 °C for 60 seconds eliminates this variability on automated lines.

    When Coagulation Control Defines Nonwoven Production Speed

    Wet-laid nonwoven processing presents a narrow operational window for DA-102 because the carboxyl surface stabilisation responds sharply to electrolyte concentration and pH. The emulsion is anionically stabilised in the pH range 3.8–6.0; outside this interval, zeta potential drops below |15 mV| and coagulation becomes spontaneous. In a typical furnish containing 10% DA-102 as binder on fibre weight, the addition of a calcium chloride coagulant solution must be ramped at a controlled rate of 0.5–1.2 kg CaCl₂·2H₂O per 100 kg of commercial emulsion. The post-addition pH, measured 60 seconds after mixing, must fall within 4.0–4.5. A deviation of ±0.3 pH units leads to two unacceptable outcomes: at lower pH, the emulsion undergoes micro-flocculation that increases the residual moisture in the wet web by 15–20%, elevating dryer load; at higher pH, the coagulation time doubles, causing binder migration to the sheet surface and dry-strength loss of 25–40% (strip tensile, TAPPI T 494). Production-scale tanks equipped with inline pH probes (e.g., Mettler Toledo InPro 3250) and mass flow-based dosing skids maintain the critical window when throughput exceeds 500 kg/h wet web. Finishing dryers must then achieve a web exit temperature of 105–115 °C for at least 45 seconds to fully coalesce the deposited polymer and activate carboxyl–metal ion crosslinking.

    Where nonwoven saturation replaces wet-end addition, the narrow sensitivity recedes but is replaced by foam-control demands. DA-102 exhibits a foam drainage half-life of 6–9 seconds (DIN 53902) in the absence of defoamer, which generates visible pinholes in impregnated substrates when line speed exceeds 80 m/min. A polyether-siloxane defoamer dosed at 0.15–0.30% on wet emulsion mass suppresses foam height below 50 mm in a Ross-Miles column test without impairing rewet properties. The binder distribution can be verified by potassium iodide staining (TAPPI UM 559): a coefficient of variation above 12% across the cross-direction profile signals inadequate defoaming or uneven spray nozzle overlap.

    Managing Rheological Stability Under High-Shear Pumping

    When DA-102 is transferred via progressive cavity or diaphragm pumps over recirculation loops exceeding 50 metres, shear-induced coagulation must be mitigated. The emulsion’s shear stability, measured by a Maron mechanical stability tester at 80 °C and 1000 s⁻¹, shows a coagulation threshold at 60–90 minutes of continuous shear. Translating to plant conditions, this dictates that recirculation pump speed not exceed 1200 rpm on a 50 mm rotor-stator and that static mixer elements have an equivalent L/D ratio of < 15. Thickening with alkali-swellable acrylics (ASE) lowers the critical shear rate; therefore, viscosity adjustment is preferentially performed with non-associative polyurethane thickeners in the post-shear zone. A permanent viscosity loss of > 15% after 24 hours of batch recirculation indicates incipient destabilisation and requires immediate dilution water addition or a drop in pump speed.

    Regulatory Compliance Matrix and Exposure Limits

    RegulationRelevant Clause or MethodStatus /Limit
    FDA 21 CFR175.105 (Adhesives for food packaging), 176.170 (Components of paper and paperboard in contact with aqueous and fatty foods)Compliant for use under specified extraction conditions
    EU Regulation (EC) No 1935/2004Overall migration limit < 10 mg/dm² (simulant B, 40 °C, 10 days)Pass
    REACH (EC) No 1907/2006Substances of Very High Concern list; monomer residuesNo SVHC > 0.1% w/w; vinyl acetate monomer residual < 1000 ppm
    RoHS (2011/65/EU)Cadmium, lead, mercury, hexavalent chromium, PBBs, PBDEsNot detected (detection limit 2 ppm)
    GB 9685-2016 (China)Permitted additives in food contact adhesivesDA-102 polymer listed under CAS 24937-78-8

    Occupational exposure monitoring during spray application of DA-102-containing adhesives should follow the gravimetric inhalable dust fraction method per MDHS 14/4; time-weighted average concentrations should remain below 3 mg/m³. Amine-based additives, including commercial triethylamine scrubbers, trigger premature flocculation and are incompatible. Alkali-metal silicate extenders cause irreversible gelation at addition levels above 2 wt% and must be avoided in formulated blends.