Products

Products

Anhui Liwei Chemical Co., Limited.

VAE Emulsion CW JZ-Ⅲ

    • Product Name: VAE Emulsion CW JZ-Ⅲ
    • Factroy Site: Lingwu, Yinchuan, Ningxia, China
    • Price Inquiry: sales2@liwei-chem.com
    • Manufacturer: Anhui Liwei Chemical Co., Limited.
    • CONTACT NOW
    Specifications
    HS Code 180440
    Product Name VAE Emulsion CW JZ-Ⅲ
    Appearance Milky white liquid with uniform consistency
    Solid Content Percent 54.0 - 56.0
    Viscosity Mpa S 800 - 2000 (Brookfield, 25°C)
    Ph Value 4.5 - 6.5
    Glass Transition Temperature Degc Approximately 0
    Minimum Film Forming Temperature Degc Approximately 2
    Particle Size Um 0.5 - 2.0
    Density G Cm3 Approximately 1.06
    Residual Vinyl Acetate Percent Less than or equal to 0.1
    Freeze Thaw Stability Pass (resistant under standard test conditions)
    Mechanical Stability Good

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

    Packing & Storage
    Packing VAE Emulsion CW JZ-Ⅲ is supplied in 200kg drums, 1000kg IBC totes, or bulk tankers, ensuring safe storage.
    Container Loading (20′ FCL) VAE Emulsion CW JZ-Ⅲ loaded in a 20-foot FCL container, securely packed and stabilized for safe transport.
    Shipping Ship VAE Emulsion CW JZ-Ⅲ in sealed plastic drums or IBC totes. Protect from freezing and extreme heat; keep above 5°C. Avoid direct sunlight, store upright, and secure during transit. Non-hazardous per regulations, but prevent leakage and keep away from incompatible materials.
    Storage Store VAE Emulsion CW JZ-Ⅲ in sealed, clean containers away from direct sunlight and extreme heat. Keep storage temperature between 5–35°C to prevent freezing, which can destabilize the emulsion. Ensure the area is dry, well-ventilated, and isolated from strong oxidants. Stir gently before use and consume within the manufacturer’s stated shelf life.
    Shelf Life Shelf life: 6 months from production date. Store in a cool, dry place, avoiding freezing and direct sunlight.
    Application of VAE Emulsion CW JZ-Ⅲ

    What prevents fibre-tear failure in D4-graded beech laminates under cyclic humidity exposure?

    When formulating a two-component waterborne adhesive for structural finger-jointing and laminated beam assembly, the selection of a polyvinyl alcohol-stabilised VAE dispersion such as CW JZ‑Ⅲ dictates the crosslinking architecture that ultimately determines heat-and-water resistance. In a production-scale adhesive kitchen producing glulam for interior load‑bearing applications, the base emulsion is combined with a polymeric 4,4´-diphenylmethane diisocyanate (pMDI) hardener at a ratio of 100 parts by wet weight of VAE to 8–15 parts of hardener, adjusted according to the wood species extractive content. The entire adhesive system must satisfy EN 204 Durability Class D4, which requires a tensile shear strength of not less than 4.0 N/mm² on beech after boiling for 6 h in water followed by cooling in water at 20 ± 2 °C, tested according to ISO 19210 (Adhesives — Determination of tensile shear strength of lap‑shear joints). An often‑overlooked operational boundary is the pot‑life shrinkage: at a workshop temperature of 35 °C and relative humidity exceeding 70%, viscosity measured by a Brookfield RVF spindle 6 at 20 rpm climbs from approximately 12 000 mPa·s to beyond 30 000 mPa·s within 35 minutes, causing starved glue lines in a radio‑frequency edge‑gluer if the mixed batch is not consumed within that window. Roll‑coater or comb‑spreader application to a controlled spread rate of 140–180 g/m² on both lamellae is typical, followed by cold pressing at 0.8–1.2 MPa for 45–90 minutes and subsequent conditioning for 72 h at 20 °C / 55% RH before planing. Compliance documentation for structural timber components further invokes ANSI 405-2018 for glued laminated timber and WATT 91 for bond line integrity under climate cycles. The terminal products are load‑bearing laminated beams, solid wood panels for stair treads, and finger‑jointed door stiles intended for interior and protected exterior joinery where formaldehyde‑free, low‑odour bond lines are specified. A pre‑cure incompatibility arises when amine‑accelerated two‑part polyurethane topcoats are applied directly over uncured squeeze‑out: residual NCO groups at the bead edge can generate microscopic gas bubbles that compromise the lacquer film, a failure mode observed on automated flat‑bed spray lines during humid summers.

    Incorporation of a vinyl acetate‑ethylene copolymer dispersion into two‑component cementitious waterproofing slurries rewrites the capillary pore structure of the hydrating matrix through film‑form‑bridging of sub‑50 µm micro‑cracks. A standard site‑batch using a forced‑action pan mixer operating at 140 rpm loads 25 kg of P.O 42.5 ordinary Portland cement, 75 kg of graded silica sand (70–140 mesh), 0.5 kg of a polycarboxylate ether superplasticizer, and between 10 kg and 18 kg of liquid VAE CW JZ‑Ⅲ, equating to a polymer‑solid‑to‑cement weight ratio of 0.10–0.18 at the emulsion’s nominal solids content of approximately 55% as measured by a halogen moisture analyser at 105 °C per ISO 124. The prepared slurry, adjusted with additional water to a flow diameter of 150–180 mm on a flow table (ASTM C230/C230M‑20), is applied by stiff‑bristle brush or notched squeegee in two coats to a primed concrete substrate, with the second coat applied perpendicular to the first while the first is still tacky. Critical performance thresholds mapped onto the Chinese compulsory standard GB/T 23445‑2009 Type Ⅱ include a tensile bond strength to wet concrete of ≥ 1.0 MPa after water immersion and a water impermeability by hydrostatic pressure of ≥ 0.6 MPa for 30 min, tested per JC 474‑2008. Processing boundary: at a substrate temperature below 5 °C or above 40 °C the film‑formation rate de‑synchronises from the cement hydration, causing surface crazing that was documented as a repetitive field complaint on exposed rooftop terraces in tropical monsoonal regions. The finished composite cures under wet‑burlap coverage for 48 h and yields a flexible waterproof membrane integral to shower stalls, underground parking decks, and swimming pool shells where crack‑bridging ability under hydraulic stress is a mandatory acceptance criterion.

    A 10–15 µm dry‑film coating of a carboxylated VAE latex, applied via an engraved gravure cylinder with 70 lines/cm screen ruling and an impression‑roll pressure of 3–5 bar, enables the lamination of machine‑glazed kraft paper to aluminum foil for sterile medical device pouches. In the converting hall of a flexible packaging converter running a tandem solventless laminator at 120 m/min, the emulsion is supplied at a Brookfield RVT viscosity of 200–600 mPa·s at 25 °C and 20 rpm, diluted with deionised water to meet a Henry constant–governed coating weight of 2.5–4.0 g/m² dry. Direct food contact authorisation for the dried film is grounded in FDA 21 CFR §176.170 (Components of paper and paperboard in contact with aqueous and fatty foods) and, where intended for Europe, the BfR Recommendation XXXVI and Regulation (EC) No 1935/2004 overall migration limit of 10 mg/dm² as verified by aqueous simulant testing at 40 °C for 10 days per EN 1186‑1. The production process mandates in‑line corona treatment of the aluminium foil at 38–42 mN/m surface energy before the wet‑bond nip, followed by a three‑zone air‑float dryer set to 80 °C, 110 °C, and 95 °C and a calendar‑chill‑roll combination that compacts the laminate to a peel strength exceeding 4.0 N/15 mm when tested on a tensile tester to ASTM F904‑22 at a jaw separation speed of 300 mm/min. Operational limits: retention time in the coating pan beyond 45 minutes under ambient shop‑floor humidity of 65 % RH triggers skinning on the liquid surface due to the emulsion’s near‑ambient minimum film‑formation temperature, introducing visible fisheyes in the barrier layer. Finished articles include peelable lidstock for PET blister trays, sterile field pouches for surgical drapes, and inner‑liner lamination for aseptic beverage cartons, where seal integrity measured by dye‑penetration testing (ASTM F1929‑23) is non‑negotiable.

    Pre‑coat filler loading and rheology windows in tufted carpet back‑coating lines

    On a secondary‑backing range running at 35–55 m/min, a filled VAE pre‑coat is mechanically frothed with a continuous Oakes mixer at 1200 rpm rotor speed to a wet density of 0.6–0.9 g/cm³ and deposited onto the reverse side of motion‑dyed nylon‑6,6 tufted greige goods through a knife‑over‑roll applicator gapped at 2.0–3.5 mm. The compound holds a filler‑to‑binder ratio by dry weight of 250∶100 to 400∶100, where the filler is ground calcium carbonate (d₅₀ = 15–30 µm), and the binder is CW JZ‑Ⅲ with its inherent carboxyl‑stabilisation providing reactive sites for optional EDC‑type crosslinkers at levels up to 1.0 phr. Compliance with indoor air quality regulations for textile floor coverings is demonstrated through chamber‑test emission profiling under ISO 16000‑9 to meet the GUT (Gemeinschaft umweltfreundlicher Teppichboden e.V.) criteria and the Carpet and Rug Institute Green Label Plus programme, as well as GB 18587‑2001 limits for total volatile organic compounds. Curing across a three‑stage gas‑fired stenter operating at 135 °C, 150 °C, and 140 °C with air circulation velocity of 18 m/s must avoid a temperature overshoot exceeding 155 °C, at which point the VAE film undergoes irreversible acid‑catalysed discoloration and embrittlement, identified by a drop in tuft‑bind strength from a required ≥ 28 N (ISO 4919) to below 18 N. A secondary jute or polypropylene backing is laminated immediately downstream, nip‑rolled at 0.4 MPa. The terminal carpet tile or broadloom goods are destined for high‑traffic contract environments where delamination resistance after simulated wet‑cleaning (DIN 54334) determines lifetime. A unique failure mode, documented during a shift‑study on a polypropylene‑rib‑backed tile line, involved foam collapse at filler loadings beyond 420 phr causing micro‑void channels that wicked detergent solution under the secondary backing, leading to claim‑returns labelled “tunnelling under wet maintenance”.

    When a polymer‑modified primer is diluted to a non‑volatile content of 15–20% by weight with potable water and applied by lamb‑wool roller to a shot‑blasted concrete deck at a coverage rate of 4–6 m²/L, penetration depth into the capillary network governs the prevention of tile‑adhesive de‑bonding triggered by rapid suction. The saturated surface‑dry condition for the substrate is verified with a Tramex CME4 moisture meter reading of ≤ 4% moisture content by volume; application below this threshold causes a viscosity spike at the liquid‑air interface that arrests penetration and forms a surficial skin. The formulation is governed by JC/T 907‑2018 (Interface treating agent for concrete), which demands a minimum tensile bond strength to concrete of ≥ 0.5 MPa after 7 days of standard curing, tested by direct pull‑off using a PosiTest AT‑A adhesion tester with 20 mm dollies at a loading rate of 0.2 MPa/s. In practice, when the primer batch is prepared with high‑shear mixing above 1500 rpm for longer than 3 minutes, entrained micro‑air content measured by an air‑content meter (ASTM C231/C231M‑17a) exceeds 12%, resulting in a cratered dried film that reduces bond strength to less than 0.38 MPa. Field experience on a large‑scale commercial kitchen tiling project revealed that admixture with polyacrylate copolymer dispersion, which is sometimes attempted as a cost‑cutting measure, leads to inter‑phase separation within 30 minutes because of divergent particle‑size distributions and stabiliser incompatibility, proving that the VAE primer must remain a stand‑alone, single‑binder system. End‑use service covers ceramic tile and natural stone installation over under‑floor heating systems, anhydrite screeds, and aged concrete repair substrates, where the dried primer also functions as a dust‑binding hardener prior to levelling‑compound application.

    When joint‑compound crack resistance during board‑drying shrinkage depends on polymer elongation at edge‑offsets

    In the formulation of a ready‑mixed gypsitic jointing compound, the addition of VAE CW JZ‑Ⅲ at a loading of 2.0–5.0 dry‑weight percent on the filler‑binder solids total modifies the rheological yield stress and the cohesive splitting resistance required to absorb the differential movement between two sheets of 12.5 mm type‑X gypsum wallboard during forced‑hot‑air drying. The compound is manufactured in a horizontal ploughshare mixer with a chopper‑speed differential of 3000 rpm, where the latex is post‑added to a pre‑hydrated blend of stucco, attapulgite thickener, and 1.0 wt% of a modified cellulose ether; the final Brookfield Helipath viscosity at 2.5 rpm is held between 500 000 and 700 000 mPa·s. Performance verification is conducted against ASTM C475/C475M‑17 (Standard Specification for Joint Compound and Joint Tape for Finishing Gypsum Board), which requires a joint‑integrity rating of no cracking under a 8 mm gap closure with a 0.25 mm top‑coat film after a controlled drying cycle. A documented sensitivity emerges when the polymer’s dry film tensile elongation measured according to ISO 527‑3 on an 0.5 mm cast film after 7 days conditioning at 23 °C / 50% RH drops below 400 %; at that threshold, edge‑crack frequency quantified by a visual rating system (0 = no cracks, 4 = complete separation) sharply escalates from 1 to 3 in the feather‑edge region. Production‑scale defect reduction measures include a mandatory pre‑dispersion filtration through a 100 µm screen to eliminate dried‑skin aggregates that act as stress‑concentration points. The terminal product is packaged in 17‑L high‑density polyethylene pails for professional drywall finishing, delivering a bond‑compound layer that receives paper joint tape and subsequent skim coats, ultimately disappearing into a paint‑grade, monolithic wall surface evaluated by gloss‑meter inspection under oblique 15° lighting to reveal any telegraphing of tape burrs.

    Nonwoven binder application for medical sterilization wrap via foam‑impregnation curing

    A cylinder‑foam impregnator operating with a VAE‑based binder liquor coated at 2.5–5.0 g/m² dry add‑on weight onto a 40 gsm polyester/viscose hydroentangled web creates an adhesive matrix for the repositionable closures of single‑use surgical gowns and sterile set‑up covers. The bath is prepared by blending CW JZ‑Ⅲ with deionized water to a solids content of 8–12 %, a wetting agent based on acetylene glycol at 0.2 phr, and, where colour‑coding is required, an aqueous pigment dispersion at 1.0 phr. Biocompatibility of the dried nonwoven for patient and clinician skin contact is demonstrated through a battery of tests per ISO 10993‑5 (in vitro cytotoxicity), 10993‑10 (skin irritation and delayed‑type hypersensitivity), and 10993‑11 (acute systemic toxicity) as part of the technical file for a Class Ⅰ medical device under EU MDR 2017/745. The impregnated web passes through a reverse‑tension stenter frame where the first zone is set to 95 °C for initial water evaporation, followed by a plateau at 125 °C for 45 seconds residence time to achieve full coalescence while preventing the synthetic fibre from reaching its softening point. A process control issue unique to this delicate substrate is the onset of binder migration at a drying‑air cross‑flow velocity above 15 m/s, which causes a skin‑depleted core observable via scanning electron microscopy as a sparse interstitial bonding layer, reducing cross‑directional wet tensile strength below the acceptable 12 N/25 mm measured according to EDANA 20.2‑89. The final roll‑good is converted into autoclave‑compatible wrap and the inner reinforcement zone of surgical mask shells, where its dry‑bond cohesion prevents fibre linting during high‑frequency ultrasonic cutting.

    Table 1 | Variability of mechanical properties in a 1∶3 cement-silica sand mortar modified with VAE CW JZ‑Ⅲ at incremental polymer‑solid additions
    Polymer‑solid addition
    (wt% of cement)
    Compressive strength
    (MPa)
    per GB/T 17671
    Flexural strength
    (MPa)
    per GB/T 17671
    Bond strength to concrete
    (MPa)
    per EN 1542
    Capillary water absorption
    (g/m²·h⁰·⁵)
    per EN 1015‑18
    0 (unmodified)48.26.10.62380
    541.57.90.95210
    1037.09.41.28112
    1532.810.61.5168
    2028.311.21.6244
    Table 2 | Compliance matrix by downstream application segment for VAE dispersion CW JZ‑Ⅲ
    Application segmentPrimary standard / regulationCritical test method or clauseKey performance criterion
    Two‑component cementitious waterproofing membraneGB/T 23445‑2009 Type Ⅱ; JC 474‑2008Tensile bond to wet concrete; hydrostatic pressure test1.0 MPa bond; ≥ 0.6 MPa for 30 min
    D4‑grade structural wood adhesiveEN 204 / EN 205; ANS 405‑2018Boiling‑water shear test (6 h immersion + 2 h cold water) per ISO 19210Shear strength ≥ 4.0 N/mm² on beech
    Paper/foil flexible packaging laminateFDA 21 CFR §176.170; EU 1935/2004Overall migration (EN 1186‑1); seal integrity (ASTM F1929‑23)10 mg/dm²; no channel dye penetration
    Tufted carpet pre‑coatGUT; CRI Green Label Plus; GB 18587‑2001VOC emission chamber test (ISO 16000‑9); tuft‑bind (ISO 4919)TVOC ≤ 0.25 mg/m³ (168‑h model); bind ≥ 28 N
    Concrete interface primerJC/T 907‑2018Pull‑off adhesion test on moist substrate0.5 MPa at 7 d standard cure
    Joint compound for gypsum boardASTM C475/C475M‑17Joint‑integrity cracking evaluation; splitting resistanceEdge crack rating ≤ 1 (visual system 0 – 4)
    Medical nonwoven wrap binderISO 10993‑5/‑10/‑11; EU MDR 2017/745Cytotoxicity (MTT assay); wet tensile (EDANA 20.2‑89)Viability ≥ 70%; cross‑dir. wet strength ≥ 12 N/25mm
    Free Quote

    Competitive VAE Emulsion CW JZ-Ⅲ prices that fit your budget—flexible terms and customized quotes for every order.

    For samples, pricing, or more information, please contact us at +8615380400285 or mail to sales2@liwei-chem.com.

    We will respond to you as soon as possible.

    Tel: +8615380400285

    Email: sales2@liwei-chem.com

    Inquiry

    Get Free Quote of Anhui Liwei Chemical Co., Limited.

    Flexible payment, competitive price, premium service - Inquire now!

    Certification & Compliance
    More Introduction

    VAE Emulsion CW JZ-Ⅲ belongs to a class of carboxylated vinyl acetate-ethylene copolymer dispersions stabilized with a poly(vinyl alcohol) protective colloid system. Its nominal solids content, determined in accordance with ISO 3251:2019 (forced-air oven at 105 °C for 3 h), is 54.5–55.5 wt%. Brookfield viscosity at 23 °C and 20 rpm (spindle 4) falls between 1800 mPa·s and 3200 mPa·s per ISO 2555:2018. Minimum film-forming temperature, evaluated on a Rhopoint MFFT-90 gradient bar under 50 % RH, registers 0 °C without coalescing solvent. The product is supplied at a pH of 4.0–5.0 and exhibits a mean particle diameter of 0.3–0.5 µm by laser diffraction (Malvern Mastersizer). The dispersion is free of alkylphenol ethoxylates and complies with the volatile organic compound limits of the EU Decopaint Directive 2004/42/EC Phase II for interior matt wall coatings.

    In contrast to earlier iterations in the CW JZ series, the Ⅲ-grade incorporates a modified ethylene sequencing that depresses the glass transition of the amorphous vinyl acetate-rich domains without increasing the water sensitivity of the dry film. Comparative immersion data (24 h in deionized water at 23 °C) show a weight uptake of 11–14 wt% for CW JZ-Ⅲ versus 18–22 wt% for a standard PVAc homopolymer dispersion of equivalent solids, measured on films cast at 500 µm wet thickness and conditioned per ISO 291:2008 class 2 atmosphere. Such behavior places the product between conventional PVAc homopolymers and all-acrylic binders on the cost-performance axis, offering a balance exploited in several downstream manufacturing sectors.

    When wet adhesion on alkaline substrates becomes a reject criterion in production

    Interior semi-gloss and matt paints formulated on porous mineral surfaces demand that the binder resist saponification under persistent high-pH conditions, a failure mode routinely observed in vinyl acetate homopolymer films. CW JZ-Ⅲ addresses this through ethylene comonomer incorporation at a level of approximately 12–15 mol%, distributed as short blocks that disrupt the hydrolytically susceptible acetate sequences. In a model formulation containing 18.5 wt% binder solids on total paint weight, wet scrub resistance tested per ISO 11998:2006 after 28 d drying at 23 °C/50 % RH reached ≥ 1200 cycles before film breakthrough on Leneta P121-10N charts, using a 0.5 % aqueous solution of an alkyl polyglucoside wetting agent as the scrubbing medium. Plant trials on a pilot-scale bead mill (Netzsch MiniCer, 0.8 mm YTZ beads) indicated that the dispersion remains shear-stable up to a grinding chamber residence time of 12 min at 2800 rpm; processing beyond 15 min led to a detectable rise in sieve residue on a 40 µm mesh, attributed to partial coagulum formation in zones of localized thermal build-up exceeding 42 °C. The coating formulator is therefore advised to add the emulsion post-grind when letdown temperatures are confirmed below 38 °C.

    On a production-scale twin-screw conveying system used for dry-mix joint compounds, the emulsion was metered at 6.0 ± 0.2 wt% into a continuous ribbon blender (Lödige FKM 600) to yield a workable paste with a water-to-powder ratio of 0.38. The resulting compound exhibited a Vicat setting time (per EN 196-3, modified for joint compounds) extended by 45 min relative to a PVAc-stabilized control, a critical parameter for applicator open time on large ceiling installations. This delay stems from the more hydrophobic film surface reducing the evaporation rate of free water, not from a chemical retardation of the calcium sulfate hemihydrate hydration.

    Adhesive Performance and Heat Resistance Benchmarking

    For assembly bonding of wood veneer (0.6 mm European beech) to medium-density fibreboard, CW JZ-Ⅲ was applied by roller coater at a spread rate of 90 g/m² wet, pressed cold for 20 min at 0.8 N/mm². Shear strength tested according to EN 205:2016, after conditioning at 23 °C/50 % RH for 7 d, yielded 6.8 MPa with wood failure exceeding 85 % of the bonded area. When coupons were immersed in water at 20 °C for 4 d and tested wet, strength retention remained ≥ 62 % of the dry value. By comparison, a commercially prevalent homopolymer PVAc D3-class adhesive tested under identical conditions retained only 35–40 % of its dry strength, underscoring the role of ethylene in imparting water resistance beyond what external crosslinkers alone can achieve.

    Heat resistance follows a different profile. Dynamic mechanical analysis of a neat emulsion film (dried 14 d at 23 °C/50 % RH, ramp rate 3 K/min, 1 Hz) showed a storage modulus crossover at 48 °C (onset of the α-relaxation of the vinyl acetate phase), while a separate β-relaxation centered near −18 °C corresponds to the ethylene-rich segments. Consequently, assemblies intended for service above 45 °C require the addition of a glyoxal-based post-crosslinker or blending with a high-Tg acrylic dispersion. Published data for CW JZ-Ⅲ with 2.0 wt% phenol-formaldehyde resol (P:F molar ratio 1:1.8) added pre-application shows a shift of the softening point to 71 °C, measured by a heat resistance test in which a 500 g dead load is applied to a 25 mm × 25 mm lap shear specimen while the oven temperature is raised at 1 °C/min — a protocol adapted from DIN EN 14257:2006 (WATT 91). Plant adaptation of this two-component approach demands in-line static mixing (e.g., a Sulzer SMX plus 6-element mixer) and a pot life window of 55–65 min at 23 °C before a detectable viscosity doubling occurs.

    What limits its use in exterior joinery applications?

    While the ethylene content confers hydrolysis resistance, it simultaneously reduces the ultraviolet durability of the binder relative to pure acrylic or styrene-acrylic systems. Accelerated weathering in a QUV/se device (UVA-340 lamps, 0.77 W/m² irradiance at 340 nm, cycle: 8 h light at 60 °C/4 h condensation at 50 °C) for 1000 h produced a gloss reduction of 45 GU (from an initial 65 GU at 60°) and a yellowness index change (ΔYI E313) of +8.5 on a 100 µm clear film over Q-panel aluminum. Incorporation of 1.5 wt% of a benzotriazole UV absorber (Tinuvin 1130) and 0.8 wt% of a hindered amine light stabilizer (Tinuvin 292) suppressed ΔYI to +2.1 under the same exposure window. Therefore, exterior joinery topcoats based on CW JZ-Ⅲ as the sole binder are not recommended without such light stabilizer packages, and even then published comparative data against straight acrylics for north-facing vertical surfaces remains limited. In architectural coatings for sheltered exterior masonry, such as elastomeric wall coatings applied at 450–550 µm dry film thickness, the binder’s flexibility at sub-zero temperatures (elongation at break measured per ISO 37:2017 type 2 dumbbell at −10 °C remains above 300 %) makes it a viable component in blends with styrene-acrylics.

    A further boundary condition concerns compatibility with high-buffering capacity pigments. Zinc oxide at loadings above 3.0 wt% on total formulation weight has been observed to induce a viscosity drift upward of +25 % over 14 days storage at 50 °C, measured per ISO 2884-1:2006. The mechanism involves desorption of acetyl groups catalyzed by zinc ion coordination at the particle surface, progressively depleting the protective colloid layer. Formulations requiring zinc oxide as a can-preservation booster must incorporate a post-add buffer (typically a 0.15 wt% solution of ammonium bicarbonate) to keep the continuous phase pH below 6.5 during storage.

    Distinction of CW JZ-Ⅲ from adjacent grades in the series
    ParameterCW JZ-ⅡCW JZ-ⅢTest Method
    Nominal solids (wt%)54.0–55.054.5–55.5ISO 3251
    Brookfield viscosity (mPa·s)2500–45001800–3200ISO 2555
    MFFT (°C)+30Rhopoint bar
    Ethylene content (approximate mol%)8–1012–15Internal 1H-NMR
    Wet adhesion on alkyd (crosshatch, 24 h soak)2B4BASTM D3359-17
    Freeze-thaw stability (cycles, −5 °C)35ASTM D7149-05

    The lower viscosity of the Ⅲ-grade compared to Ⅱ is a deliberate design outcome: by narrowing the particle size distribution (polydispersity index reduced to 0.08 from 0.15), the maximum packing fraction rises, permitting a higher solids loading for the same flow resistance. This is advantageous in adhesive application where a lower wet coating weight without solids sacrifice minimizes the energy cost of water removal in the drying tunnel. In roller-applied packaging adhesives for paper/board lamination (line speed 120 m/min on a Bobst Masterfold 110 gluer), the shift from CW JZ-Ⅱ to Ⅲ eliminated a recurring star-wheel tracking defect traced to excess adhesive transfer onto the compression section.

    In nonwoven binder applications, specifically the saturation bonding of a 45 g/m² viscose-polyester carded web, CW JZ-Ⅲ applied by a size press at 20 % bath concentration and dried on steam-heated cans at 130 °C surface temperature yielded a dry tensile strength (MD) of 58 N/5 cm and an elongation of 22 % per EDANA 20.2-89. The self-crosslinking functionality, activated by the elevated drying temperature, resulted in a wet strength retention of 72 % after immersion in 0.1 % Triton X-100 solution for 1 h. This places it ahead of a non-carboxylated VAE grade that typically delivers 45–50 % wet retention under the same cure schedule. Plant data from a Fleissner through-air drum dryer indicated that residual formaldehyde in the finished nonwoven, measured by the acetylacetone method per EN ISO 14184-1:2011, was below the 16 mg/kg threshold for baby diaper applications, a result linked to the emulsion’s zinc-free self-crosslinking chemistry.

    Understanding the rheological signature for high-shear curtain coating

    Curtain coating of furniture foil demands an extensional viscosity profile that prevents curtain rupture at gap widths of 0.5–1.2 mm and flow rates of 0.3–0.8 L·min-1·m-1. CW JZ-Ⅲ, modified with 0.25 wt% of an alkali-swellable associative thickener (ASE, supplied at 30 % active content), develops a high-shear viscosity at 10 000 s-1 of 45 mPa·s (cone-and-plate, 25 °C), sufficient to maintain curtain integrity on a coating head (Hymmen Saturn model) operating at 100 m/min. Too low a high-shear viscosity leads to edge bead withdrawal and catastrophic curtain break; too high promotes air entrainment at the dynamic wetting line. The formulation rheology window is approximately ±5 mPa·s at 10 000 s-1 before either defect mode appears with statistical significance (p > 0.05 over 200 m of coated panel). The required tolerance necessitates gravimetric dosing of the thickener solution with an accuracy of ±0.005 wt%, achieved via a Bronkhorst mini CORI-FLOW mass flow controller in a recirculation loop. In contrast, a control acrylic dispersion of identical solids and similar MFFT produced a curtain stable only between 0.6 L·min-1·m-1 and 0.9 L·min-1·m-1, a markedly narrower operating window that led to 8 % downtime on a Schiele inline finishing line. The broader curtain stability range of CW JZ-Ⅲ is attributed to the strain-hardening imparted by the high-molecular-weight PVOH protective colloid, which suppresses filament thinning in extensional flow near the curtain edges.

    Key compliance and regulatory status of VAE Emulsion CW JZ-Ⅲ
    Standard / RegulationStatusRemark
    FDA 21 CFR 175.105CompliantAdhesives for food packaging, indirect contact
    EU 10/2011 (overall migration limit)Compliant at <10 mg/dm²Film thickness 50 µm, simulant B
    REACH (EC) 1907/2006Fully registeredNo SVHC above 0.1 wt%
    RoHS 2011/65/EU (Annex II)CompliantPb, Hg, Cd, CrVI, PBBs, PBDEs below limits
    GB 18583-2008 (China indoor decorating adhesive)CompliantVOC <50 g/L

    Operationally, the emulsion should be stored at 5–30 °C in sealed containers; exposure to repeated freeze-thaw cycles below −3 °C without agitation during thawing leads to grit formation detectable on a 75 µm filter. In a batch in which the warehouse temperature dropped to −7 °C for 6 h, gentle drum rolling for 2 h at 20 °C restored homogeneity with no loss of film-forming properties, though a statistically measurable +8 % increase in sieve residue was recorded. The emulsion is incompatible with polyvalent metal salts (aluminum sulfate, calcium chloride) at concentrations above 0.05 wt%, as immediate coagulation occurs. Where such salts are used as formulation additives, the emulsion must be protected by a nonionic surfactant pre-treatment at a ratio of 0.5 parts surfactant to 100 parts emulsion, with the surfactant dissolved in the aqueous phase before emulsion addition.