Produtos

Produtos

Anhui Liwei Chemical Co., Limited.

Emulsão VAE CW 40-602

    • Nome do produto: Emulsão VAE CW 40-602
    • Site da Factroy: Lingwu, Yinchuan, Ningxia, China
    • Consulta de preço: sales2@liwei-chem.com
    • Fabricante: Anhui Liwei Chemical Co., Limited.
    • Contacte Agora
    Especificações
    Código SH 379488
    Tipo De Produto Emulsão de Copolímero de Acetato de Vinil-Etileno (VAE)
    Aparência Líquido branco a esbranquiçado
    Conteúdo Sólido 55% ± 1%
    Viscosidade 25 C 2500 4000 cP
    O Ph 4.0 avaliações 5.0
    Temperatura De Transição Vítrea Tg Aproximadamente -10 ° C
    Temperatura Mínima De Formação De Filme Mfft Aproximadamente 0°C
    Densidade 25 C 1,05 g/cm³
    Tamanho De Partícula 1.0 profundidade 2.0 µm
    Sistema Emulsionante Não iónico, estabilizado com PVA

    Como fábrica acreditada Emulsão VAE CW 40-602, aplicamos protocolos de qualidade rigorosos - cada lote é submetido a testes rigorosos para garantir padrões de eficácia e segurança consistentes.

    Embalagem e armazenamento
    Embalagem VAE Emulsion CW 40-602 é fornecido em tambores de 200 kg ou bolsas IBC de 1000 kg, com fechos selados e invioláveis para manuseio seguro.
    Carga de contêiner (20' FCL) 20 “FCL: Emulsão VAE CW 40-602 carregada em flexitank dentro do contêiner para transporte a granel seguro e eficiente.
    Envio VAE Emulsion CW 40-602 é enviado como uma dispersão aquosa não perigosa, normalmente em tambores ou bolsas IBC. Mantenha os recipientes selados, na vertical e protegidos contra congelamento ou calor excessivo. Evite derramamentos e descargas ambientais. Certifique-se de rotulagem adequada, ventilação e carregamento seguro para evitar vazamentos durante o trânsito.
    Armazenamento Armazene VAE Emulsion CW 40-602 em recipientes originais selados em uma área fria, seca e bem ventilada. Mantenha as temperaturas entre 5 ° C e 35 ° C; proteger do congelamento, luz solar direta e fontes de calor. Evite o contato com materiais incompatíveis. Mantenha os recipientes bem fechados e use dentro do prazo de validade declarado pelo fabricante. Mexa suavemente antes de usar.
    Prazo de validade Conservar em recipiente original selado a 5 30 ° C, protegido contra geadas. O prazo de validade é de 6 meses a partir da data de produção.
    Aplicação da Emulsão VAE CW 40-602
    Quando um copolímero aquoso de acetato de vinilo-etileno é selecionado para pinturas de paredes interiores de baixo odor que devem cumprir o rótulo francês A + VOC e a GB 18582-2020 da China, a ausência de amônia e o baixo teor de monômero residual na VAE Emulsion CW 40-602 torna-se uma variável de processamento crítica. Os dissolventes em escala de produção com um impulsor de disco dental de **1.200 rpm** lidam rotineiramente com uma formulação úmida que compreende **15-25% em peso** da emulsão junto com uma concentração de volume de pigmento de **55-70%**. A fase de descida é particularmente sensível: a construção de viscosidade superior a **2.500 mPa·s** a **23°C** entra ar que persiste através de testes de resistência à sag (ISO 16862:2022). Os operadores compensam introduzindo monoisobutirato coalescente de 2,2,4-trimetil-1,3-pentanediol a **3-5%** de sólidos ligantes, mas somente após o pH ter sido tamponado para **8,0-8,5** com hidróxido de sódio. Um desvio abaixo do pH **7,4** inicia a desestabilização parcial dos domínios ricos em acetato de vinilo, aumentando a retenção de grãos em peneiras **40 µm** acima de um limiar aceitável de **20 mg/kg**. O produto final é uma pintura de parede mate a semi-brilhante (ângulo ISO 2813 **60°** brilho especular abaixo **15** em bases profundas) onde a resistência à esfregagem molhada classificada de acordo com ISO 11998:2023 excede rotineiramente **5.000 ciclos** a **100 µm** espessura do filme seco. As instalações de fabricação no Delta do Rio Yangtze registram uma variância de depuração de lote para lote de menos de **8%** quando a velocidade de agitação pós-adição é limitada a **600 rpm** e a temperatura da camisa do recipiente baixada é mantida abaixo de **35°C**.
    Cotação Grátis

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    Para amostras, preços ou mais informações, entre em contato conosco em +8615380400285 Ou envie para sales2@liwei-chem.com.

    Responderemos a você o mais rápido possível.

    Telefone: +8615380400285

    E-mail: sales2@liwei-chem.com

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    Certificação e Conformidade
    Mais Introdução

    VAE Emulsion CW 40-602

    A self-crosslinking vinyl acetate-ethylene copolymer dispersion designed for medium-modulus adhesive formulations, nonwoven binder applications, and cementitious membrane modification where balanced water resistance and dry-pick strength are process-critical.

    How Does the Ethylene Content in CW 40-602 Influence Adhesive Cohesion Over the Service Temperature Range?

    The incorporation of approximately 18–22 wt% ethylene in the copolymer backbone depresses the glass transition temperature of the base polymer to –5 °C ± 3 °C (midpoint, DSC per ISO 11357-2:2020, second heat cycle). In formulated pressure-sensitive adhesive (PSA) lines on a 100 m/min coating and drying line fitted with a floating-knife system, the permanent tack measured by loop tack (ASTM D6195-22) remains above 4.5 N/25 mm at 0 °C on untreated biaxially oriented polypropylene film, a threshold rarely achieved by conventional polyvinyl alcohol-stabilized VAE grades. This internal plasticization eliminates the need for external coalescent addition, which directly lowers VOC output below 0.05 g/L (EPA Method 24) in ready-to-use compounds. The molecular architecture also retards the hydrolysis rate of the acetate moieties under alkaline conditions; immersion in a saturated Ca(OH)₂ solution (pH 12.4 ± 0.2) for 28 days at 40 °C yields less than 2.3 % weight loss, compared to 3.8–5.1 % for a comparable PVA-stabilized homopolymer dispersion, substantially preserving cohesive integrity in fresh concrete bonding overlays.

    Meanwhile, the soft domain contribution from the ethylene segments introduces a shear-sensitivity plateau above 60 °C when the dispersion is thickened with hydrophobically modified alkali-swellable emulsions (HASE). On a 25 mm coaxial cylinder fixture (ISO 3219:1993), the high-shear viscosity at 10 000 s⁻¹ drops to 18–22 mPa·s, enabling clean gravure cylinder transfer in print lamination without misting. This behaviour is in contrast to all-acrylic dispersions of comparable solids, which typically retain 30 % higher high-shear viscosity, demanding dilution or higher dryer temperatures.

    Technical Specifications

    PropertyValueMethod
    Solids content55.0 ± 1.0 %ISO 3251:2019, 2 h at 105 °C
    pH4.5–5.5ISO 976:2013
    Brookfield viscosity (LVF, spindle 3, 30 rpm, 25 °C)2800–4200 mPa·sISO 2555:2018
    Minimum film-forming temperature (MFFT)0 °CISO 2115:2000
    Surface tension38–42 mN/mDu Noüy ring, DIN 53914
    Average particle size (D₅₀)0.8–1.2 µmLaser diffraction, ISO 13320:2020
    Freeze-thaw stabilityPasses 5 cycles (–10 °C/RT)ASTM D7149-05 (modified)

    When Formulating Water-Resistant D3/D4 Wood Adhesives Without External Crosslinker, the Processing Window Narrows

    CW 40-602 incorporates N-methylol acrylamide (NMA) functionality that initiates self-crosslinking under acidic catalysis at 70–80 °C in a hot press. The degree of cure, tracked via the toluene-insoluble gel fraction (ASTM D2765-16), reaches 78–84 % after 3 minutes at 90 °C and 1.0 MPa clamping pressure using beech adherends. This generates a wet shear strength in the 3.5–4.2 N/mm² range per EN 204/D4 durability classification, without the addition of polymeric isocyanate or emulsifiable MDI. The latent crosslinking is triggered only above the MFFT and upon acidification to pH 2.8–3.2; adding 0.3 wt% of a latent acid catalyst such as ammonium chloride or a blocked sulfonic acid reduces the onset temperature by approximately 8 °C. This is critical on a radio-frequency edge-gluing press where the glue line reaches 72 °C within 45 seconds. However, pot-life stability in pre-catalyzed adhesive mixes is limited to 4–6 hours at 25 °C, beyond which particle sedimentation and micro-flocculation increase the residue on a 50 µm screen to over 15 mL/L, potentially blocking slot-die coating heads and causing daily clean-out cycles.

    A Comparison with Standard Emulsion Polymer Chemistries in Cementitious Membrane Formulation

    In two-component flexible cementitious waterproofing slurries mixed at a polymer-to-cement ratio (p/c) of 0.45 by weight, CW 40-602 provides a measurable elongation advantage at the expense of early compressive strength. The following data set, generated on a lab-scale Hobart mixer (EN 196-1:2016 mortar mixer, 140 rpm), contrasts CW 40-602 with a conventional carboxylated styrene-butadiene (S/B) latex and a plasticizer-free PVAc homopolymer.

    Parameter (28 days cure, 23 °C/50 % R.H.)CW 40-602S/B Latex (50 % solids)PVAc Homopolymer (55 % solids)Test Method
    Compressive strength (MPa)22.528.130.4EN 12190
    Flexural strength (MPa)7.97.25.3EN 196-1
    Crack bridging at –5 °C (mm)1.80.60.2EN 1062-7 (modified)
    Capillary water absorption coefficient (kg/m²·h⁰·⁵)0.120.180.28EN 1062-3
    Adhesion to moist concrete (N/mm²)2.41.91.5EN 1542

    The lower compressive strength is a direct consequence of the low-Tg ethylene component and is acceptable in traffic-bearing layers only when thickness is limited to 2 mm and the p/c ratio does not fall below 0.40. The substantially wider crack bridging at sub-zero temperature confirms the material’s utility over unheated underground parking decks where seasonal movement exceeds 0.5 mm. During continuous mixing on a PFT G4 plastering machine, the polymer must not coagulate under the shear gradients at the stator-rotor interface; CW 40-602 maintains a stable particle size distribution after 20 minutes of recirculation, whereas S/B latex shows a 40 % increase in D₉₀, indicating nascent gel formation that can clog the 10 mm material hose.

    Compatibility Boundaries and Additive Selection

    Formulations based on CW 40-602 tolerate up to 8 wt% of plasticizer (dibutyl phthalate or triacetin) before phase inversion occurs in the continuous drying film, visualized optically as a change from translucent to opaque at a dry-film thickness of 500 µm. The dispersion is stabilized with a nonionic/anionic surfactant system, so strongly cationic wetting agents, particularly quaternary ammonium salts above 0.1 wt% on binder solids, induce rapid shock coagulation; viscosity jumps from 3800 mPa·s to over 50 000 mPa·s within 30 seconds. This is a common formulation pitfall when introducing biocides or anti-static additives. Furthermore, blends with fully hydrolyzed PVA solutions (degree of hydrolysis> 98.5 mol%) exhibit a miscibility gap that manifests as a heterogeneous dried film with reduced tensile strength (~30 % reduction at 50:50 blend ratio) due to thermodynamic incompatibility between the VAE copolymer and the highly crystalline PVA domains. For tackifying wood adhesives, rosin ester dispersions with an acid number 10–15 mg KOH/g are preferred to avoid pH drift and hydrolytic destabilization of the NMA crosslinking moieties during three-month ambient storage.

    Beyond its use in construction and woodworking, the emulsion finds a niche in sizing cellulosic nonwovens where a combination of hydrophobic hand-feel and dry tensile resilience is required. On a Fleissner hydroentanglement line operating at 120 m/min, a 2.5 wt% wet-pickup of CW 40-602 applied via a kiss-roll impregnation saturator raises the machine-direction dry tensile index of a 55 g/m² carded viscose web from 3.2 N·m/g to 5.8 N·m/g (ISO 1924-2:2008), without the embrittlement observed after 170 °C cure cycles with conventional self-crosslinking acrylics. The reduced thermal demand—drying at 110 °C is sufficient to reach full cure—saves approximately 15 % of the energy load compared to acrylic binder systems requiring 135–145 °C for methylol crosslinking. Nevertheless, the emulsion’s sensitivity to shear at low pH remains a limiting factor in recirculating ink-jet print binders, where pressure drops across the 20 µm nozzles exceed 5 bar and transient acidic conditions from photopolymer initiators can cause tip build-up after 8 hours of continuous operation. Published data for this specific configuration is limited, but field reports indicate that adding 0.2 % of a steric stabilizer with a polyvinylpyrrolidone backbone extends run time to approximately 24 hours before necessitating a clean-out cycle.