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Anhui Liwei Chemical Co., Limited.

JZ-II Medium-Viscosity VAE Emulsion

    • Product Name: JZ-II Medium-Viscosity 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 525461
    Appearance White milky liquid with uniform texture
    Solid Content 55.0 ± 1.0 %
    Viscosity 1500–3000 mPa·s (Brookfield, 25°C)
    Ph 4.0–6.0
    Glass Transition Temperature 0 °C
    Minimum Film Formation Temperature 5 °C
    Particle Size 1–2 μm
    Residual Vinyl Acetate Monomer ≤ 0.5 %
    Density 1.06 g/cm³
    Freeze Thaw Stability Stable under standard testing conditions

    As an accredited JZ-II Medium-Viscosity VAE Emulsion factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing JZ-II Medium-Viscosity VAE Emulsion is supplied in 200 kg drums, sealed to prevent spillage, contamination, and moisture loss.
    Container Loading (20′ FCL) 20′ FCL shipment of JZ-II Medium-Viscosity VAE Emulsion, palletized and secured, ensuring safe, efficient transport.
    Shipping JZ-II Medium-Viscosity VAE Emulsion ships in sealed drums or IBC totes, protected from freezing and extreme heat. Use dedicated tankers or clean, dry containers. Ensure proper labeling, ventilation, and secure loading. Avoid contact with acids or oxidizers. Transit temperature should remain between 5–35°C to maintain stability.
    Storage Store JZ-II Medium-Viscosity VAE Emulsion in tightly sealed, clean containers in a cool, dry, well-ventilated area. Keep away from direct sunlight, heat sources, and open flames. Avoid freezing; recommended storage temperature is 5–35°C. Protect from extreme temperatures and moisture contamination. Keep containers upright and inspect regularly. Material should be used within its shelf life, with proper handling to prevent spills.
    Shelf Life Shelf life is 6 months when stored sealed at 5–35°C, protected from freezing, heat, and direct sunlight.
    Application of JZ-II Medium-Viscosity VAE Emulsion

    Processing characteristics observed on industrial twin-screw compounding lines reveal that medium-viscosity vinyl acetate-ethylene copolymers with a solids content near 55 % and a Brookfield RVT viscosity in the range of 2 000–4 000 mPa·s (spindle #4, 20 rpm, 25 °C) occupy a narrow rheological window that simultaneously satisfies wet-out kinetics on cellulosic substrates and cohesive strength build-up during ambient evaporation. The rheology profile, absent pronounced shear-thinning artefacts below 100 s⁻¹, permits direct substitution into existing blade-coating infrastructure without modifying doctor-bar gap settings originally calibrated for homopolymer PVAc dispersions, yet the ethylene content—typically 10–25 wt% on dry polymer—introduces a permanent internal plasticization that suppresses minimum film-forming temperature below 0 °C, eliminating the reliance on fugitive coalescents that would otherwise breach evolving EU Decopaint Directive 2004/42/EC Phase III thresholds for indoor paints applied by roller.

    What dictates the adhesive bond durability classification under EN 204 for wood assembly?

    For interior jointing applications destined to carry a D3 durability classification under EN 204:2016, the emulsion must form a continuous film that withstands immersion in cold water without catastrophic bondline swelling, a requirement that directly correlates to the copolymer’s gel fraction after drying. In high-speed continuous lamination of parquet wear layers, the adhesive is applied via a multi-roll spreading unit at a rate of 120–180 g/m² wet weight, with the medium-viscosity grade demonstrating sufficient rheological hold-out to prevent strike-through on porous oak lamella under nip pressures exceeding 0.5 MPa. The addition level in a final ready-to-use formulation is typically 88–94 parts by weight (as-supplied emulsion), balanced with 4–7 parts plasticizer-free thickening agent and a polyphosphate-based wet-edge extender buffered to pH 4.0–5.5 to align with the natural acidic stabilization of the VAE colloid. Post-application, assemblies are pressed at 20–25 °C with a minimum of 0.7 N/mm² for 45–90 minutes in cold-press stacks, where the intrinsic low creep tendency of the crosslinked ethylene segments prevents spring-back during unloading—a failure mode frequently documented on mechanically assembled beech wood constructs when homopolymer adhesives with insufficient cohesive strength are substituted. Full cure across the bondline, verified by destructive shear testing per ASTM D905-08(2021), reaches a threshold exceeding 10 MPa on sapelli-mahogany substrates only after 7 days conditioning at 23 °C/50 % RH. The finished constructs correspond to EN 204 category D3 interior furniture and architectural joinery that encounters short-term accidental moisture exposure, including stair treads, laminated window boards, and kitchen worktop core laminations where urea-formaldehyde emissions must remain below the E1 limit defined in EN 16516.

    Paperboard lamination grease resistance and FDA 21 CFR migration limits

    In the construction of grease-resistant folding carton stock for dry pet food or microwavable popcorn packaging, the VAE dispersion functions as a monolithic barrier layer interposed between bleached kraft board and a printed surface ply, applied via a smooth-roll coater at a dry coat weight of 6–10 g/m². The medium-viscosity profile prevents misting at line speeds up to 400 m/min, a critical operational boundary recorded on a BOBST LEMANIC laminator where misting particles depositing on downstream infrared drying hoods triggered periodic shutdowns every < 8 hours when a low-viscosity grade with identical solids was trialled. The formulation add-on, expressed as dry adhesive mass per unit area, is controlled to within ±0.5 g/m² by an in-line beta-gauge feedback system; the dried film must exhibit a TAPPI T559 cm-02 kit value of at least 8 without pinholing, a property that degrades precipitously when the filler-to-binder ratio in the basecoating exceeds 0.15:1. Compliance with indirect food contact regulation rests on the absence of migrating substances above the thresholds in 21 CFR §176.170 (Components of Paper and Paperboard in Contact With Aqueous and Fatty Foods) and §176.180 (Components of Paper and Paperboard in Contact With Dry Food), with the ethylene-vinyl acetate copolymer requiring specific migration testing for vinyl acetate monomer (SML < 12 mg/kg) per Commission Regulation (EU) No 10/2011 Annex I. The downstream process integrates a wet lamination step immediately after adhesive transfer, followed by a three-zone hot-air tunnel operating at 90–110–70 °C with residence time 12–18 seconds, sufficient to evaporate residual water without blistering the polyethylene extrusion coating that may be added in a secondary offline step. Finished formats include aseptic beverage carton pre-laminates, frozen vegetable overwrap trays, and chocolate bar inserts where mineral oil barrier performance, measured by the Heptane Vapour Transmission Rate apparatus constructed according to DIN 53168, remains unaltered after 400 h of UV illumination in a QUV chamber cycling at 0.89 W/m² irradiance.

    Medium-viscosity VAE emulsions stabilized with a protective polyvinyl alcohol colloid are pumped into a holding tank feeding a puddle applicator positioned over a moving polypropylene spunbond web at a surface speed of 60–120 m/min during the production of wet-laid nonwoven wipes for healthcare surface disinfection. The bath concentration is maintained at 12–18 % dry binder on total liquor, with the add-on on dry fibre targeted at 22–28 % by mass, a range necessary to impart a cross-directional wet tensile strength exceeding 6.0 N/5 cm when measured under EDANA WSP 110.4.R4(09) after immersion in a 0.9 % saline solution at 37 °C for 24 hours, simulating prolonged skin contact. The bonding mechanism relies on thermal migration of the copolymer into cellulose fibre intersections during the through-air drying phase, which operates with an inlet air temperature of 135–150 °C for a dwell time of 4–7 seconds; deviation below 130 °C results in binder powdering when the ethanolamine-based quaternary ammonium disinfectant is applied during final converting, because incomplete film formation leaves accessible hydroxyl sites that undergo competitive hydrogen bonding disruption. This field-derived temperature floor was established after conductivity probes on a commercial Andritz line recorded a 14 % increase in lint particle shedding within 90 minutes of production when the dry-end circulation fan damper setting drifted ± 3 %. Compliance for disposable absorbent hygiene articles includes sensitivities to skin irritation and cytotoxicity prescribed in ISO 10993-5:2009 for medical device biocompatibility, as well as the absence of formaldehyde donors under the voluntary OEKO-TEX® Standard 100 Annex 4, product class II. The terminal article output encompasses spunlace-alternative economy-grade floor wipes, pre-saturated instrument cleaning cloths for dental operatories, and disposable patient bed underpad barrier layers where the binder also serves as a fluid-resistant coating applied via a gravure kiss-roll at a wet load of 40–55 g/m².

    When an interior wall paint formulation targets <5 g/L VOC without coalescent re-introduction

    The role of the VAE latex as the sole film-forming binder in a flat sheen wall paint that must comply with the SCAQMD Rule 1113 Architectural Coatings limit of 50 g/L VOC, and concurrently satisfy the more restrictive Blauer Engel RAL-UZ 102:2022 requirement of < 700 ppm volatile organic substances in the ready-to-use product, confronts the formulator with a direct trade-off between scrub resistance and low-temperature film coalescence. Medium-viscosity grades, employed at 14–18 parts by weight on total formula at a pigment volume concentration (PVC) between 40–55 %, are added to the let-down vessel after the pigment grind has been dispersed under a disk-type dissolver with a tip speed of 18–22 m/s, where the pre-neutralized anionic surfactant package interacting with the associative polyurethane thickener builds a controlled low-shear viscosity of 20–30 Krebs Units (KU) measured via a paddle viscometer conforming to ASTM D562-10(2020). The dried film, conditioned for 28 days at 23 °C/50 % RH, is required to survive > 1 000 wet scrub cycles according to ISO 11998:2006 using a non-abrasive scrub medium, and the inherent internal plasticization of the VAE chain eliminates the requirement for a slow-evaporating coalescent such as 2,2,4-trimethyl-1,3-pentanediol monoisobutyrate, which would otherwise delay full hardness development beyond day 14 and cause blocking at temperatures above 35 °C in stacked container storage. An incompatibility that must be rigorously avoided involves the post-blending of zinc oxide-based fungistatic additives at levels exceeding 0.5 % by mass into the finished paint if the zinc ion is not fully encapsulated in a silica shell; electrochemical monitoring with a silver chloride reference electrode has demonstrated a pH drift greater than 0.8 units over 72 hours in the wet state, leading to pre-gelation of the associative network and visible micro-agglomerates on drawn-down Leneta cards. The output product categories span indoor ceiling coatings with a dead-matte sheen angle of < 5 units at 85° glossmeter geometry, hygiene-sensitive washable coatings for medical consultation rooms where quaternary ammonium salt compatibility is tested by a modified ASTM E2197-17 method, and deep-tone accent base paints tinted with 14–16 g/L of oxide pigment dispersion to deliver a lightfastness index exceeding grade 7 on the ISO 105-B02:2014 blue wool scale.

    For polymer-modified cementitious slurry coatings applied with a medium-bristle brush to concrete basement retaining walls at a wet film thickness of 0.8–1.2 mm in a single coat, the liquid component—comprised of 85–95 wt% of the VAE medium-viscosity emulsion and the balance as a defoamer emulsion and an oligomeric silane coupling agent—is mixed with a Portland cement–silica fume dry blend at a liquid-to-powder ratio of 1:3.5 to 1:4.0 by mass. The polymer solids content in the cured matrix, determined via ignition loss according to ASTM D5403-93(2020), stabilizes at 12–16 % by total weight of the hardened mortar and is critical to bridging crack widths up to 0.3 mm at −10 °C as prescribed by EN 14891:2017 Clause 6.3.8 for flexible liquid-applied waterproofing products used beneath ceramic tiling. A repeatedly observed failure mode in continuous planetary mixer installations stems from the calcium-ion-triggered destabilization of the colloidal system when the dry blend is introduced too rapidly; a reduction in open time from 45 minutes to below 18 minutes, accompanied by a temperature spike exceeding 12 °C per minute within the mixing bowl, has been documented on a 200-litre Parabolic Dissolver when the powder fraction addition rate exceeded 20 kg/min—a processing conflict that forces the plant to adopt a stepwise incremental powder feed protocol with an inter-measurement rheological pause of 30 seconds per each 20 kg dosed. Tensile adhesion on primed C 30 concrete after 28 days of immersion in water according to EN 14891:2017 must remain above 0.8 MPa, a value achieved only when the copolymer’s internal plasticizer remains chemically intact; addition of amine-based accelerators, including triethanolamine, is contraindicated because the alkaline hydrolysis of the vinyl acetate ester linkage progresses at a rate accelerated by > 3× when the pore solution pH exceeds 13.2, as tracked by ATR-FTIR carbonyl band attenuation at 1 735 cm⁻¹ over a 90-day immersion period. The terminal products include flexible cementitious membrane systems for under-tile waterproofing in wetroom shower enclosures, external balcony and podium deck protection coatings qualified under ETAG 005 guidelines, and single-component repair mortars packaged in 20 kg pails where the liquid co-reactant is factory-preweighed and the VAE emulsion maintains dispersion stability through at least 3 freeze–thaw cycles per ISO 1147:1995.

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    Certification & Compliance
    More Introduction
    A water-borne dispersion of vinyl acetate-ethylene (VAE) copolymer, JZ-II Medium-Viscosity VAE Emulsion is manufactured with a poly(vinyl alcohol) protective colloid system and an anionic surfactant package. The product exhibits a solids content of 54–56 % (per ISO 3251, 2 h at 105 °C), a Brookfield viscosity of 2000–4000 mPa·s (ISO 1652, spindle 4, 20 rpm, 23 °C), and a pH of 4.0–5.5 (ISO 976). The minimum film-forming temperature (MFFT) without coalescing solvent is 0 ± 1 °C (ISO 2115), while the average particle size, determined by laser diffraction (ISO 13320), falls in the range 0.8–1.8 µm. Residual free monomer is controlled below 0.1 %, and the density at 20 °C is 1.06–1.08 g/cm³. These figures position JZ-II as an intermediate-grade dispersion intended for water-resistant assembly adhesives, paper and board lamination, cementitious admixtures, and textile binders.
    Table 1 — JZ-II Medium-Viscosity VAE Emulsion: Representative Property Profile
    PropertyValueTest Method
    Solids content54–56 %ISO 3251
    Viscosity (Brookfield RVT, sp. 4, 20 rpm)2000–4000 mPa·sISO 1652
    pH4.0–5.5ISO 976
    Minimum film-forming temperature (MFFT)0 ± 1 °CISO 2115
    Average particle size (D₅₀)0.8–1.8 µmISO 13320
    Density (20 °C)1.06–1.08 g/cm³ISO 2811-1
    Residual vinyl acetate monomer< 0.1 %GC headspace
    Freeze-thaw stabilityIrreversible coagulation below 0 °CVisual, cyclic exposure

    What Mechanisms Underpin the Adhesive Performance Advantage of JZ-II Over Homo-PVAc Emulsions?

    In D3 and D4 woodworking assembly applications tested to EN 204, the ethylene comonomer content (approximately 10–15 wt% on dry polymer) provides permanent internal plasticization. This eliminates the progressive embrittlement observed in poly(vinyl acetate) homopolymer films after combined humidity and temperature cycling as described in EN 12765. The medium-viscosity rheology permits controlled penetration into medium-density fiberboard (MDF) and birch plywood veneers while maintaining sufficient wet tack to hold substrates during closed assembly. Bond strength measured by tensile shear on beechwood conditioned to 12 % moisture content (EN 205) exceeds 10 N/mm² after 7 days at 23 °C and 50 % RH. When the emulsion is compounded with 5 parts polymeric methylene diphenyl diisocyanate (pMDI) crosslinker per 100 parts wet emulsion, hot-press cure at 80 °C and 0.7 MPa for 5 minutes yields a boiling-water-resistant D4 bond meeting the WATT 91 heat-resistance requirement of EN 14257. The PVOH colloid, however, reacts competitively with isocyanate groups; therefore, pMDI dosage must remain below 5 phr to avoid a viscosity increase exceeding 50 % within the 30-minute pot-life window. Mixing is performed with a low-shear anchor agitator at 100–300 rpm to avoid shear-induced destabilization of the emulsion. In high-speed paper-to-paper lamination operating at line speeds beyond 80 m/min, the pseudoplastic flow behavior—characterized by a power-law index of 0.35–0.40 across a shear-rate range of 10–1000 s⁻¹—allows clean transfer from engraved rollers (line screen 140–180 LPI) and rapid viscosity recovery to minimize strike-through into absorbent substrates. A dry coat weight of 3–5 g/m² delivers a T-peel strength of 1.5–2.0 N/15 mm on clay-coated board (ISO 11339, 100 mm/min jaw speed). By comparison, a low-viscosity grade (viscosity 500–1500 mPa·s) tends to generate aerosol mist at equivalent roller speeds and may penetrate excessively, while a high-viscosity product (above 8000 mPa·s) requires water addition that extends drying demand and dilutes protective colloid, risking localized coagulation on the roller surface.

    Compatibility Boundaries with Reactive Fillers and Crosslinkers

    JZ-II emulsion can be combined with ground calcium carbonate fillers up to 30 wt% on wet emulsion without phase separation if added under continuous low-shear stirring. When formulating two-component systems for structural wood joints, the selection of curing agent is critical. Acid-catalyzed urea-formaldehyde resins drive the mix pH below 3.5, at which point the PVOH-stabilized dispersion undergoes severe viscosity build and partial coagulation within 15 minutes; therefore, such combinations are industrially impractical. Aliphatic polyisocyanates based on hexamethylene diisocyanate (HDI) trimers, in contrast, maintain a near-neutral pH and extend pot-life to 60 minutes at 23 °C. Nevertheless, the hydrophilicity of the emulsion can slow the diffusion of hydrophobic isocyanates to the bond line; pre-mixing with propylene carbonate carrier (5 % on resin) improves dispersion quality without inducing destabilization. In cement-based tile adhesive formulations designed for classification C2 per EN 12004, incorporation of 3–6 wt% JZ-II on cement weight reduces the water-to-cement ratio while preserving flow-table consistency measured by DIN 18555-2. The ethylene segments raise transverse deformation from < 0.5 mm (unmodified) to values exceeding 2.5 mm, satisfying the S1 deformability class. However, the anionic stabilizer partially retards Portland cement hydration: initial set is delayed beyond 6 hours at 20 °C, and open time extends by an additional 30–45 minutes. When accelerated curing with forced hot air at 40 °C is applied to compensate, rapid surface moisture evaporation forms a polymer skin that impairs adhesion to porcelain stoneware; maintaining substrates at a saturated surface-dry condition eliminates this defect.

    Film Formation Latency Under High-Humidity Lay-Up Conditions

    The coalescing behavior of JZ-II shifts measurably when the relative humidity of the assembly environment exceeds 70 %. Evaporative cooling at the wet film surface depresses the apparent MFFT by 2–3 °C, which, combined with slow water release from the PVOH-rich layer, extends the tack-free time beyond 20 minutes at 10 °C. In edge-banding operations on pre-laminated particleboard, this latency can reduce initial grab sufficiently that components spring back before the nip pressure of a 0.5 MPa station closes completely. Pre-heating the substrate to 30–35 °C with infrared panels (specific emission 2.5–3.5 µm) and limiting the open time to 8–10 minutes restores instantaneous tack. Published data for this configuration in fully automated through-feed lines remains limited, but single-station laboratory simulations using a heated-plate press confirm that bond strength recovers to 95 % of the room-temperature reference. The comparative placement of JZ-II within the wider VAE portfolio is governed by viscosity, solids, and resulting application rate differences.
    Table 2 — Viscosity-Grade Differentiation in JZ-Series VAE Emulsions
    ParameterJZ-I (Low-viscosity)JZ-II (Medium-viscosity)JZ-III (High-viscosity)
    Brookfield viscosity (mPa·s)500–15002000–40008000–15000
    Solids content (%)52–5454–5655–57
    MFFT (°C)00+2
    Typical coat weight in lamination (g/m²)2–33–55–8
    Primary application focusSprayable or high-speed roll coat; low penetration toleranceMedium-speed lamination, assembly adhesives, tile mortar modificationTrowel-applied wood flooring, heavy-duty packaging, textured coatings
    Cold-set nonwoven binders for air-through bonded polyester webs require a formaldehyde-free crosslinker to keep residual formaldehyde below 16 mg/kg fabric, the Annex 4 limit under OEKO-TEX Standard 100. JZ-II is crosslinked with polyamidoamine-epichlorohydrin (PAE) resin at 2.5 % add-on and cured at 130 °C for 3 minutes, yielding a wet tensile strength retention of 65 % after 5 laundering cycles at 60 °C (AATCC 135). The resulting handle is judged as “soft” with dynamic drape coefficients below 0.55 on the Cusick drape meter; however, the PAE chemistry slightly elevates brittleness compared to a self-crosslinking VAE bearing N-methylolacrylamide groups. Thus, formulations exceeding 20 g/m² dry add-on show surface cracking on crease-fold tests if the curing temperature overshoots by more than 5 °C. No published life-cycle analysis data are available for this specific binder-substrate system. JZ-II must be stored in sealed, corrosion-resistant containers at 5–35 °C; accidental freezing causes irreversible coagulation. Even in closed packaging, a gradual pH rise to above 6.5 over 6 months signals microbial activity that demands biocide intervention (e.g., 100–200 ppm potassium sorbate). Blending with polyvinyl alcohol of higher hydrolysis degree (> 92 mol%) can further elevate the viscosity plateau and is not implemented on continuous mixing lines without in-line rheometer feedback to maintain a margin of ± 500 mPa·s from the target setpoint.