Produtos

Produtos

Anhui Liwei Chemical Co., Limited.

ROVACE 662

    Especificações
    Código SH 125102
    Nome Do Produto ROVACE 662
    Tipo Produto Emulsão de copolímero acrílico de vinil
    Família Química Copolímero acrílico-acetato de vinilo
    Estado Físico Líquido
    Aparência Líquido leitoso viscoso branco
    O Ph 5,0 - 6,0
    Conteúdo Sólidos 55 ± 1%
    Viscosidade 1000 - 2000 mPa · s
    Densidade 1,05 - 1,10 g /cm³
    Tamanho De Partícula 0,1 - 0,3 mícrons
    Temperatura De Transição Vítrea Aproximadamente 15 ° C
    Temperatura Mínima De Formação De Filme Aproximadamente 10 ° C
    Temperatura De Armazenamento 5 ° C a 40 ° C
    Aplicativo Revestimentos arquitetônicos, tintas, primers e adesivos
    Nome Do Produto ROVACE 662
    Fabricante Rohm e Haas Company /The Dow Chemical Company
    Tipo Produto Emulsão de copolímero acrílico de vinil
    Família Química Copolímero de acetato de polivinilo (PVAc)
    Estado Físico Líquido
    Aparência Emulsão leitosa branca
    Odor Odor acrílico suave
    Conteúdo Sólidos 55% em peso
    Viscosidade 1500 2500 cP a 25 ° C
    O Ph 6,0–8,0
    Gravidade Específica 1.04 avaliações 1.08
    Temperatura De Transição Vítrea Aproximadamente 5°C
    Temperatura Mínima De Formação De Filme Aproximadamente 0°C
    Solubilidade Em água Dispersível em água; forma uma película após a secagem
    Prazo De Validade 12 meses a partir da data de fabrico sob armazenamento recomendado
    Temperatura De Armazenamento 5 50 ° C; proteger do congelamento
    Aplicações Tintas, revestimentos, adesivos para embalagens, ligantes de papel e têxteis

    Como fábrica acreditada da ROVACE 662, aplicamos protocolos de qualidade rigorosos - cada lote é submetido a testes rigorosos para garantir padrões de eficácia e segurança consistentes.

    Embalagem e armazenamento
    Embalagem ROVACE 662 é embalado em tambores de 55 galões, contendo 200 kg líquidos, com número de lote e etiqueta de segurança.
    Carga de contêiner (20' FCL) O carregamento de contêiner FCL de 20 para ROVACE 662 garante embalagem segura, rotulagem adequada e conformidade para transporte de produtos químicos.
    Envio ROVACE 662 é normalmente enviado como uma emulsão de copolímero acrílico-acetato de vinila não perigosa, não regulamentada como mercadoria perigosa para transporte rodoviário, ferroviário, marítimo ou aéreo. Embale em tambores selados ou IBCs, proteja do congelamento e do calor excessivo e documente como não DG sob os regulamentos ADR, IMDG e IATA.
    Armazenamento Guarde o ROVACE 662 em seu recipiente original hermeticamente fechado em uma área fria, seca e bem ventilada, longe da luz solar direta, calor e fontes de ignição. Mantenha separado de substâncias incompatíveis, alimentos e rações para animais. Certifique-se de que a área de armazenamento esteja protegida e inacessível a pessoas e crianças não autorizadas. Siga sempre o rótulo do produto e a Ficha de Dados de Segurança (SDS) para requisitos específicos.
    Prazo de validade O prazo de validade é de 12 meses a partir da fabricação quando armazenado em recipientes originais fechados, protegidos do congelamento e da luz solar direta.
    Aplicação do ROVACE 662

    What Controls Final Peel Strength When PVC Decorative Film Is Heat-Laminated to MDF?

    In PVC membrane and flat-panel lamination, the adhesive is applied to the back of decorative vinyl film or to the MDF profile. ROVACE 662 is compounded as the principal binder at 70–85 wt% of the wet adhesive; the remaining formulation consists of defoamer at 0.1–0.3 wt%, rheological thickener at 0.2–0.5 wt%, and water. When heat-activation presses are used, the dried adhesive film is reactivated at 80–110°C under membrane vacuum or platen pressure ranging from 0.3 MPa to 0.8 MPa. Roll-coater gap settings are adjusted to a dry adhesive deposition of 20–40 g/m²; lower deposition produces telegraphing on smooth MDF surfaces, and higher deposition increases drying time beyond 20 minutes at 25°C. When membrane pressing three-dimensional profiles, adhesive bridging in sharp grooves occurs if dry film thickness exceeds 25 µm, and vacuum hold time below 60 s may leave edge lift. Terminal articles include vinyl-wrapped MDF doors, RTA furniture drawer fronts, desktops, interior wall panels, and profile-wrapped picture frames. Compliance for furniture panel surfaces is commonly assessed under ASTM D4541 for pull-off adhesion and ASTM D903 for peel resistance; REACH Regulation (EC) No 1907/2006 Annex XVII applies to migration of restricted substances from the bonded article. Operational limitations include plasticizer migration from low-cost PVC films into unmodified VAE adhesive layers at service temperatures above 60°C, which can cause time-dependent peel loss; published data for this specific configuration is limited and must be validated on the production film. Avoid introducing multivalent metal salts or cationic wetting agents into the compounded adhesive because charge neutralization destabilizes the emulsion.

    High-speed rotary labeling lines transfer ROVACE 662-based adhesives by engraved roller to paper label stock or directly to HDPE and PET bottle surfaces. The addition ratio in the compounded adhesive is typically 60–75 wt% of the wet formulation, with polyvinyl alcohol solution at 10–20 wt% for wet tack extension and defoamer at 0.05–0.2 wt%. The production process is rotary or inline label application at line speeds typical of modern rotary labelers, with compression rollers following the transfer point. The application system consists of a chromium oxide ceramic anilox roller, doctor blade, and rubber impression roller; roller pressures are typically set to 0.2–0.4 MPa to prevent adhesive sling. Foaming is controlled by defoamer addition and by maintaining adhesive pot temperature at 18–25°C; viscosity drift above 3000 mPa·s can cause uneven transfer. Terminal finished products include labeled HDPE detergent bottles, PET beverage containers, and paper-applied shrink sleeves. The governing compliance framework for non-food labels is REACH; where food-contact labeling is involved, FDA 21 CFR 175.105 or EU Regulation (EC) No 1935/2004 applies. Operational boundaries appear when relative humidity exceeds 70%; wet tack development slows on high-slip bottle surfaces, and transfer efficiency can fall below acceptable limits if roller engraving depth is less than 30 µm.

    Solvent-Free Carton Sealing at Line Speeds Above 40 m/min

    When flap closure is required within 30 seconds of adhesive transfer, carton sealing stations on folder-gluer lines run with circulating adhesive pots and wheel applicators. In this sector ROVACE 662 functions as the main binder at 65–80 wt% of the wet adhesive, supplemented with polyvinyl alcohol at 5–15 wt% for cohesive strength, defoamer at 0.05–0.2 wt%, and water. Production lines use stinger, wheel, or nozzle extrusion application with open times between 5 s and 30 s; compression sections apply contact pressure below 0.1 MPa for 0.5–2 s. Bond strength is normally tested under ASTM D1876 T-peel geometry after 24 h conditioned at 23°C and 50% RH. Finished articles include corrugated shipping cases, folding cartons, tray-formed packaging, and multiwall paper sacks. Compliance is established under FDA 21 CFR 175.105 for incidental food-contact adhesive use, with paper and paperboard components referenced under 21 CFR 176.170 and 21 CFR 176.180 where fatty or dry food contact is possible. The adhesive is not suitable for direct food contact and is not formulated for boil-in-bag or retort conditions; use above 60°C service temperature is outside the documented operating envelope.

    Softcover perfect binding and layflat book production require low-odor waterborne spine glues when reactive polyurethane hot melts are not specified. ROVACE 662 is introduced as the backbone polymer at 50–70 wt% of the wet adhesive, with polyvinyl alcohol solution at 15–30 wt%, filler dispersion at 5–15 wt%, and preservative at 0.1–0.3 wt%. The production process is inline perfect binding: the adhesive is applied to the routed spine, the cover is nipped, and the book enters a cooling and drying section before stacking. Spine adhesive viscosity is maintained between 2000 and 5000 mPa·s at application temperature; low viscosity causes strike-through into uncoated paper, and high viscosity prevents adhesive from penetrating the spine cuts. Drying is completed in a radio-frequency or air-knife section before in-line trimming. Terminal finished products include softcover trade books, catalogs, annual reports, and layflat notebooks. Relevant standards include ANSI/NISO Z39.48-1992 when paper permanence is specified and ASTM D903 for adhesive peel characterization; REACH registration for the formulated adhesive remains mandatory. The principal processing limitation is cold-condition flexibility: adhesive films containing insufficient ethylene content can crack at spine temperatures below 5°C, and low-temperature mechanical validation should be performed under ISO 6721-1 rather than extrapolating from room-temperature data.

    Replacing Solventborne Polychloroprene in Fabric-to-Foam Lamination

    Where open-cell polyurethane foam is bonded to woven or knitted textile face stock, waterborne VAE adhesives replace solventborne polychloroprene in markets where VOC content is restricted. ROVACE 662 is compounded as the primary binder at 60–80 wt% of the wet adhesive; rheological modifier at 0.2–0.5 wt%, defoamer at 0.05–0.2 wt%, and water constitute the balance. The production process is roll coating or air-assisted spray onto the foam sheet, passing through a forced-air tunnel at 80–110°C until the film is tacky, then immediate lamination with fabric under nip pressure of 0.3–0.6 MPa. Spray systems use air-atomizing guns with atomization air pressure between 0.4 and 0.7 MPa; roll systems use engraved rolls with cell volume 20–40 cm³/m². The open time after drying and before fabric lamination is controlled to 10–30 s to prevent loss of hot-tack. Terminal finished products include automotive seat covers, office chair upholstery, mattress ticking, and padded wall panels. Compliance for automotive interior components includes FMVSS 302 flammability testing on the finished laminate and REACH Regulation (EC) No 1907/2006 Annex XVII for restricted substances; furniture upholstery sold in Europe may require testing under EN 1021-1 and EN 1021-2 for cigarette and match ignition. Adhesion is evaluated under ASTM D751 for coated fabrics or ASTM D903 for flexible laminate peel. The operational boundary appears with polyester face fabrics containing fluorocarbon finishes; surface energy below 35 mN/m can require corona pre-treatment to achieve adequate bond strength. Foam substrates with ester-grade polyurethane are more prone to hydrolysis than ether-grade, so wet lamination before drying is not recommended. Do not combine with cationic antistatic agents that can coagulate the emulsion.

    When the Finished Article Must Comply with FDA 21 CFR 175.105 Incidental Food Contact

    Third-party audits of food-contact packaging adhesives require the converting plant to demonstrate that the adhesive formulation falls within the clearance described in FDA 21 CFR 175.105 for adhesives used in packaging, transporting, or holding food, provided that the adhesive is separated from food by a functional barrier. ROVACE 662 is incorporated at 55–75 wt% of the wet adhesive in cupstock and carton side-seam formulations; the remaining fraction consists of polyvinyl alcohol, defoamer, and water, with no plasticizer addition. The production process is roll coating of cupstock blanks followed by heat sealing of the side seam at 130–170°C; finished terminal products include paper cups, paperboard sleeves, and food cartons. Side-seam bond strength is tested on the finished cup according to ASTM D903 after hot-water filling at 80°C for 30 minutes; failure modes are documented as fiber tear, adhesive cohesive failure, or interfacial release. For cups used with hot liquids, the adhesive bond line must not fail below 90°C. EU Regulation (EC) No 1935/2004 and EU Regulation (EU) No 10/2011 apply to European converters, with migration testing under the EN 1186 series where the adhesive is not separated by an absolute barrier. The formulation should not be used in direct food contact, and migration test results for low-molecular-weight residuals must be established on the final converted article because the adhesive film itself is not a food-contact material.

    Application scenarioStandard or regulationDesignation /clauseAssessment endpoint
    PVC film lamination to MDFREACHRegulation (EC) No 1907/2006 Annex XVIIRestricted substances in final article
    Rotary bottle labelingFDA21 CFR 175.105Incidental food-contact suitability
    Carton sealingFDA21 CFR 176.170 /176.180Paper and paperboard food-contact components
    BookbindingANSI/NISOZ39.48-1992Paper permanence and adhesive compatibility
    Foam laminationFMVSS /ENFMVSS 302; EN 1021-1; EN 1021-2Flammability of upholstered furniture and automotive interiors
    Cupstock side-seamFDA /EU21 CFR 175.105; EN 1186 seriesMigration from final food-contact article
    Cotação Grátis

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    Certificação e Conformidade
    Mais Introdução

    ROVACE 662 is supplied as an aqueous polymer dispersion based on a polyvinyl acetate polymer backbone. The grade is used primarily in waterborne adhesive compounding and cellulosic converting operations where fast wet tack, controlled open time, and mechanical stability under shear are critical process variables. The manufacturer’s batch certificate of analysis controls non-volatile content, pH, low-shear viscosity, grit residue, and minimum film-formation temperature; these values are lot-specific and should not be replaced by generic class data during production qualification. The product can be formulated with selected waterborne tackifiers, plasticizers, and rheology modifiers, but the sequence of addition and the final pH require control to avoid destabilization. The product is classified as an industrial polymer dispersion. Regional exposure-limit, REACH, and food-contact compliance documentation should be requested for the intended downstream use. Residual volatiles, including vinyl acetate monomer, are normally quantified by headspace gas chromatography using an internal calibration procedure, and the release limit is stated in the supplier’s specification.

    How Does the Polyvinyl Acetate Backbone Influence Creep Resistance Relative to Ethylene-Modified Dispersions?

    The structural difference between ROVACE 662 and vinyl acetate-ethylene copolymer dispersions is the reduced incorporation of a low-glass-transition ethylene segment along the polymer chain. In processing terms that change shifts the glass transition region to a higher temperature, increases the yield stress of the dried film, and reduces low-temperature flexibility in the bonded joint. The practical result is improved static-load resistance in rigid assembly and reduced tack on low-energy polymer films at low temperature. Published quantitative data for this specific configuration are limited, so qualification should include differential scanning calorimetry under nitrogen at a heating rate of 10 K/min in accordance with ISO 11357-2. For plasticizer-free formulations, creep resistance can be evaluated by static shear at 60 °C with a 1 kg dead load. Failure modes should be classified as cohesive, adhesive, or substrate failure according to ASTM D5573. Compared with externally plasticized polyvinyl acetate homopolymers, formulations based on ROVACE 662 do not require dibutyl phthalate or benzyl butyl phthalate, thereby reducing long-term plasticizer migration and surface contamination.

    On a high-speed case erector equipped with a 0.4 mm nozzle and an air-over-pneumatic piston pump, adhesive bead consistency depends on the ratio between low-shear viscosity and high-shear viscosity. The material is discharged at a nominal pressure of 1.5 MPa to 4.0 MPa depending on line speed, nozzle wear, and fluid temperature. At line speeds above 250 m/min, insufficient viscosity recovery after the pump stroke produces intermittent bead thinning and starved flaps. Incoming lot checks therefore include a two-point rheological ratio measured at 1 s⁻¹ and 100 s⁻¹ on a concentric-cylinder rheometer following ISO 3219. A batch-to-batch variation exceeding 15% in the low-shear value can be a rejection criterion when the material is transferred through long feed lines because air release and shear history in diaphragm pumps alter dispersion stability. Filtration through a 150 µm bag filter before the applicator removes coagulum that otherwise accumulates behind the nozzle. On roll coaters, the fluid is applied at 20 µm to 40 µm wet film thickness; controlling solids against the certificate of analysis is essential for consistent dry adhesive coat weight.

    When Relative Humidity Exceeds 60%, Drying Rate Becomes a Process Boundary Rather Than a Formulation Defect

    Open-time testing is conducted at 23 °C and 50% relative humidity unless the application specification defines otherwise. At higher humidity, water removal from the adhesive film is retarded, and the onset of fiber-tearing adhesion can lag behind the production cycle. On corrugated board with a Cobb value above 35 g/m², the substrate absorbs water rapidly; when the board is too dry, the adhesive may skin before compression, causing loss of contact. The operational boundary is not only the glass transition temperature of the polymer but also the moisture sorption isotherm of the substrate and the wet-film thickness. A practical control is to reduce applied wet film thickness or increase compression dwell time rather than to alter polymer solids. If relative humidity exceeds 60%, unsealed paper substrates should be pre-conditioned or the line speed reduced. The product’s water-resistance limitations emerge after drying; hot-water immersion testing at 60 °C using EN 204 can distinguish water-redispersible films from crosslinked films.

    Qualification matrix for bonding paperboard and corrugated substrates
    PropertyTest methodEquipment/conditionsProcessing implication
    Non-volatile contentISO 3251Forced-air oven, 105 °C to constant massDetermines dry film thickness at a given wet coat weight
    Brookfield viscosityISO 3219Spindle No. 4, 20 rpm, 25 °CControls transfer pumps, roller transfer, and bead width
    pHISO 976pH meter with temperature compensationAffects colloidal stability and thickener response
    Sieve residueISO 4576150 µm sieveIndicates coagulum and nozzle-fouling tendency
    T-peel adhesionASTM D1876300 mm/min, 23 °C, 50% RHClassifies substrate fiber-tearing versus adhesive failure
    Lap shearASTM D10021.3 mm/min, conditioned specimensProvides comparative shear strength for rigid substrates

    Surface Energy, Contact Angle Hysteresis, and Adhesion to Laminated Polymer Films

    High-speed lamination of polyethylene terephthalate or biaxially oriented polypropylene to paper with waterborne dispersions is controlled by surface energy. The polymer film is typically corona treated to a dyne level of 38 mN/m to 42 mN/m; below this range, waterborne wetting is incomplete and the dried film retracts. ROVACE 662-based formulations are generally less capable of wetting untreated low-energy films than solventborne polyurethane or acrylic pressure-sensitive adhesives. When the application demands adhesion to untreated polypropylene, priming or adhesion promoters are required. The difference from acrylic dispersions is that polyvinyl acetate-based films tend to be more hydrophilic; after a single water immersion cycle, adhesion loss may be partly recoverable by drying, but hot-water resistance requires crosslinking. Contact-angle hysteresis measured with water before and after corona treatment should be recorded. If the film’s surface oxygen content falls below 8 at% by X-ray photoelectron spectroscopy, cohesive failure tends to shift to adhesive failure at the interface.

    Storage in unlined carbon-steel vessels is not recommended because low pH can generate iron ions that discolor the dried film and destabilize the dispersion. The material should be stored at 5 °C to 35 °C, protected from freezing. Freeze-thaw damage is detected as an increase in 45 µm sieve residue. Direct pH adjustment with strong alkali is not advised because localized pH excursions above 7.5 can saponify acetate groups and increase viscosity irreversibly. If pH adjustment is required, dilute ammonia or sodium bicarbonate solution should be added slowly under continuous agitation while monitoring pH. Avoid combination with amine-based additives unless prior stability screening is conducted, because some amines raise the continuous-phase pH and accelerate hydrolysis. Multivalent cations such as aluminum sulfate or calcium chloride can coagulate the dispersion; compatibility tests should be performed using a 100 g jar sample before production batching.

    Compared with polyvinyl acetate homopolymers plasticized externally with dibutyl phthalate or benzyl butyl phthalate, ROVACE 662 is designed to avoid long-term monomeric plasticizer migration. Compared with vinyl acetate-ethylene dispersions, the higher polyvinyl acetate character reduces low-temperature tack but improves heat resistance and static load resistance. Compared with solventborne polyurethane systems, the aqueous delivery reduces solvent emissions but imposes longer open times and lower cohesive strength unless crosslinkers are added. On a production-scale case sealer fitted with a 30:1 L/D piston pump and a 0.3 mm nozzle, bead width variation of ±0.5 mm was observed when low-shear viscosity differed by more than 20% between batches. That field data confirms the need for rheological incoming inspection and for closed-loop temperature control on the transfer vessel.

    Compliance checklist and required evidence for industrial adhesive use
    Compliance areaReferenceRequired evidenceApplication boundary
    Indirect food-contact adhesive21 CFR 175.105Supplier letter or formulation clearanceApplies to formulated adhesive, not necessarily neat dispersion
    EU chemical inventoryREACHExtended safety data sheetRegistration status must be confirmed for imported product
    Restriction of hazardous substances2011/65/EUSupplier declaration or test reportApplies to finished articles, not wet dispersion
    VOC contentASTM D3960, EPA Method 24Laboratory dataLow-VOC status depends on formulated additives
    Heavy metals in consumer articlesASTM F963Certified test laboratory reportRequired only for toy or child-contact end uses
    Dispersion mechanical stabilityISO 4576Sieve residue after specified shear historyPredicts nozzle and coater performance

    On a corrugated slitter-scorer line running E-flute board at 250 m/min, the adhesive’s green strength must be sufficient to maintain compression-bonded flaps without spring-back. The applied wet film is typically 25 µm to 35 µm thick, and compression dwell is limited to 0.5 s to 1.5 s. Under those conditions, the polymer’s rapid film formation and high wet tack are more important than final shear strength. Bonded samples pulled immediately after compression should show fiber-tearing failure on at least 80% of the bonded area. If fiber-tearing is not achieved, the adhesive may be drying too slowly, the substrate may be too saturated, or the wet film thickness may be too high. The correction is process-based first: reduce wet film thickness, increase substrate temperature, or raise compression dwell. Only after confirming that the processing window is centered should formulation adjustments be made.