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Anhui Liwei Chemical Co., Limited.

HS-460 High-Tg VAE Emulsion for Redispersible Polymer Powders

    • Product Name: HS-460 High-Tg VAE Emulsion for Redispersible Polymer Powders
    • 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 232318
    Glass Transition Temperature 23°C
    Solid Content 50 ± 2%
    Viscosity 800-1500 mPa·s
    Ph 5.0-7.0
    Mean Particle Size 1.0-3.0 μm
    Minimum Film Forming Temperature 15°C
    Protective Colloid Polyvinyl alcohol
    Stabilizer System Anionic/nonionic surfactants
    Residual Vinyl Acetate <0.1%
    Film Property Transparent, flexible, water-resistant

    As an accredited HS-460 High-Tg VAE Emulsion for Redispersible Polymer Powders factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Supplied in 200 kg plastic-lined drums or 1,000 kg IBC totes, ensuring product stability and safe handling.
    Container Loading (20′ FCL) 20′ FCL loaded with HS-460 VAE emulsion in drums/IBCs, secured and ventilated to prevent leakage, ensuring safe transit.
    Shipping Ship HS-460 High-Tg VAE Emulsion in sealed drums or IBCs, protected from freezing and direct sunlight. Maintain temperatures between 5–35°C. Use dedicated or lined equipment to prevent contamination. Label as non-hazardous per transport regulations, but avoid skin contact. Ensure upright handling and secure loading.
    Storage Store HS-460 High-Tg VAE Emulsion in sealed, clean containers in a cool, dry, well-ventilated area. Maintain temperatures between 5°C and 35°C; avoid freezing, excessive heat, and direct sunlight. Keep away from moisture and incompatible materials. Stir gently before use. Use within recommended shelf life to prevent coagulation or performance loss.
    Shelf Life Store in sealed containers at 5–35°C, away from freezing. Shelf life is 6 months from production date.
    Application of HS-460 High-Tg VAE Emulsion for Redispersible Polymer Powders

    A shift toward thin-bed installations and polymer-modified cementitious adhesives has placed a measurable demand on the glass transition temperature of spray-dried polymer powders. HS-460, a high-Tg vinyl acetate-ethylene (VAE) emulsion stabilized with a polyvinyl alcohol (PVA) protective colloid system, is engineered to yield redispersible polymer powders (RPP) with a minimum film formation temperature significantly above ambient conditions. This thermal barrier prevents cold flow and premature coalescence during powder storage at temperatures up to 40 °C and relative humidity values exceeding 70 %, a failure mode documented during bulk silo discharge audits in tropical climates. The emulsion’s high-Tg architecture—typically calibrated above 15 °C by modulated differential scanning calorimetry per ASTM E1356-08—is calibrated to survive the shear and thermal stresses of industrial-scale spray drying at inlet temperatures between 160 °C and 220 °C without generating intractable coagulum in the atomizer wheel deposits or cyclone fines.

    Within a 2 mm Notched Trowel Bed, What Prevents Particle Migration into the Porous Substrate?

    Ceramic tile adhesives classified as C2 S1 or C2 S2 per ISO 13007-1:2014 utilize HS-460-based RPP to achieve the required tensile adhesion strengths after water immersion and freeze-thaw cycling. The latex powder, re-emulsified upon contact with gauging water, forms a continuous polymer film interpenetrating the hydrated cement phases. A dosage window of 2.5 wt% to 4.0 wt% on total dry mix weight is standard for standard-setting formulations; exceeding 5.5 wt% in laboratory trials has produced a detectable plateau in tensile adhesion values while the open time—measured per EN 1346:2007—exhibited a non-linear extension, introducing a tackiness spike problematic for rapid tile bedding adjustments. On construction sites operating continuous ribbon mixers with a throughput of 80 kg/min, the high-Tg character of the redispersed polymer prevents surface skinning inside the mixing chamber at elevated ambient temperatures, a distinct advantage over lower-Tg counterparts that generate sticky residues on paddle blades and require mid-shift solvent cleaning.

    Once troweled onto aerated concrete or cement-sand screed with an open porosity exceeding 18 %, the latex-modulated mortar demonstrates controlled rheology; the polymer particles, with a post-dispersion diameter in the 1–10 µm range per laser diffraction analysis, coalesce preferentially at the capillary pore necks rather than migrating downward into the substrate. This mechanism preserves the adhesive’s film-forming polymer inventory at the bond line, a factor reflected in pull-off testing under EN 12004:2007+A1:2012 where failure modes shift from adhesive to cohesive within the substrate at polymer loadings above 3.0 wt%. The cured adhesive interfaces with porcelain stoneware tiles having water absorption below 0.5 wt%—a low-porosity substrate notorious for adhesion failure—while maintaining bond strengths above 1.0 N/mm² after 28-day standard cure and 7-day water immersion at 20 ± 2 °C.

    In external thermal insulation composite systems (ETICS) where base coats bridge expanded polystyrene (EPS) and mineral wool insulation boards, HS-460-based RPP is incorporated at 3.0 wt% to 4.5 wt% of the dry mortar. The resultant composite withstands the cyclic thermal stresses simulated by ETAG 004:2013 pull-through tests. A documented failure pattern on low-Tg powders manifests as polymer re-emulsification and subsequent wash-out during repeated rain exposure on west-facing elevations; the high-Tg VAE film within HS-460-derived powders exhibits water resistance sufficient to limit the 24-hour water uptake of the cured base coat to below 8 wt% when tested on a glass fiber mesh-embedded specimen. Production of these mortars on a horizontal ribbon blender with a fill level of 65 % and a mixing time limited to 180 seconds—critical for preventing frictional heat build-up that could trigger premature agglomeration of the latex powder—requires raw powder flowability metrics consistent with a Hausner ratio below 1.25 as measured by sieving and tapping on a 100 g sample. HS-460-derived powders, spray-dried with incorporated mineral anti-caking agents at 8–12 wt% on total powder mass, routinely meet this target.

    Viscosity Yield and Workability Retention in Self-Leveling Underlayments

    Calcium sulfoaluminate (CSA) cement-based and ternary binder self-leveling underlayments (SLUs) exhibit rapid setting kinetics that complicates polymer film integration. Incorporation of HS-460-derived RPP at 2.0 wt% to 3.5 wt% on total powder weight provides the necessary flow properties—typically a slump flow diameter of 240–260 mm per EN 12706:1999 when tested with a 30 mm diameter by 50 mm height flow ring—without retarding the ettringite formation that underpins early strength development. A critical formulation conflict arises when excessive retarders are deployed to extend open time; the high-Tg polymer film forms more slowly in the alkaline pore solution (pH > 12.5), and its coalescence kinetics are sensitive to the ratio of calcium sulfate to ye’elimite in the binder. At a binder-to-filler ratio of 30:70 (calcium carbonate filler), the redispersed HS-460 polymer at 3.0 wt% dosage has yielded a 28-day compressive strength of 28–32 MPa and flexural strength exceeding 7 MPa per EN 13892-2:2002.

    Processing bottlenecks observed on continuous mixing-pump systems operating at 15–20 L/min discharge rates involve air entrainment stability. Defoamer selection must compensate for the surface activity of the PVA colloid that survives spray drying; a combination of mineral oil-based and polyether siloxane defoamers, each at 0.15–0.25 wt% of total formulation, achieves an air content of 1.5–3.0 % in the fresh mortar as measured by the pressure method (ASTM C231/C231M-22). The high-Tg polymer avoids the stickiness-related viscosity climb that causes trowel drag and surface defects on poured floor areas exceeding 100 m² in single continuous placements. Finished floor flatness departures (measured with a 3 m straightedge) remain within 2 mm under these conditions. Post-cure, the polymer domains in the cementitious matrix resist plastic deformation under concentrated loads, contributing to the required surface hardness for receiving resilient floor coverings or moisture-cured urethane top coats within 6 hours of application.

    Patch repair mortars for vertical and overhead structural concrete restoration—meeting EN 1504-3:2005 Class R4 for structural repair—formulate with HS-460-based RPP to achieve the requisite combination of low shrinkage and high bond to prepared substrates. Here, the polymer powder loading is elevated to 4.0–6.0 wt% of the hydraulic binder (typically a blend of ordinary Portland cement, silica fume at 5–8 wt% cement replacement, and metakaolin at 3–5 wt%). The high-Tg nature of the re-emulsified polymer directly contributes to a restrained shrinkage below 400 µm/m when tested on a 40 x 40 x 160 mm prism subjected to 65 % RH at 20 °C per EN 12617-4:2002. Without this polymer architecture, repair materials applied at 40 mm thickness in a single overhead pass suffered cohesive cracking at the interface with the bond coat within 72 hours in documented site reports from marine infrastructure projects.

    Application on a vertical surface requires a plastic viscosity and yield stress tailored to prevent sag while retaining thixotropic responsiveness for easy gunning through a wet-mix shotcrete nozzle with a 25 mm orifice. The PVA-stabilized emulsion chemistry of HS-460 yields a re-dispersed polymer that contributes to a step-change in cohesion when the powder content crosses 3.5 wt%—the yield stress measured by a vane rheometer increases from approximately 200 Pa to 600 Pa within this dosage increment, a rheological signature well-suited for overhead patches. The same mechanism that prevents cold flow in the dry powder also mitigates polymer creep under sustained dead load in a vertical repair, a long-term deflection effect observable in low-Tg powder-modified mortars subjected to elevated service temperatures near 50 °C inside industrial flue or stack linings.

    Tensile Strength Retention of Glass Fiber Mesh-Reinforced Waterproofing Slurries After Alkali Immersion

    Flexible cementitious waterproofing membranes composed of a two-component slurry (polymer liquid plus cement powder) or a single-component powder system use HS-460-derived RPP to impart crack-bridging capability per EN 14891:2017. The high-Tg emulsion contributes to a glass transition onset in the dry film above 10 °C, ensuring that the membrane exhibits dimensional stability and resists dirt pick-up at service temperatures encountered on heated terraces and balconies. A typical formulation at 5.0 wt% powder dosage yields a crack-bridging performance of 0.75 mm at -5 °C when the membrane is applied at a dry film thickness of 2.0 mm over a pre-cracked concrete slab subjected to cyclical opening and closing on a motorized test rig.

    The chemical durability requirement for waterproofing membranes applied beneath ceramic tile on continuously submerged structures (swimming pools, retention tanks) translates into a demand for PVA-stabilized, high-molecular-weight polymer networks that resist alkali saponification. HS-460-based powders—when cured for 28 days and immersed in a pH 13 sodium hydroxide solution at 23 °C for 28 days—retain a tensile strength and elongation that are measurably less degraded than analogous VAE powders produced from lower-Tg, higher-ethylene emulsions. Published data for this specific configuration is limited to internal laboratory reports; however, the structural rationale rests on the higher vinyl acetate content and reduced ethylene incorporation, which limit alkaline hydrolysis of the acetate ester groups within the polymer backbone. The resulting membrane, when reinforced with an alkali-resistant glass fiber mesh at 160 g/m², withstands the dynamic and static pressure loads defined in the ETAG 022 guidelines for wet room coverings.

    Mineral-based grouts for wide joints (5–20 mm) in floor and wall tile installations demand a combination of high abrasion resistance—measured by the deep abrasion test per EN 12808-2:2008 with a wear volume typically below 350 mm³—and controlled stiffening to permit full joint filling without sagging. HS-460-based RPP at 1.5–2.5 wt% addition on grout powder weight replaces the traditional cellulose ether-dominated rheology control with a polymer-mediated cohesion that yields a firmer, less sticky paste. The high glass transition temperature of the dispersed polymer phase suppresses the instantaneous tack that can cause the float rubber to drag material out of the joint during the strike-off operation. When colored with iron oxide pigments at 0.5–2.0 wt%, the grout demonstrates enhanced resistance to efflorescence; the high-Tg latex reportedly reduces the capillary transport of dissolved calcium hydroxide to the exposed surface by creating a more tortuous pore network, though specific pore size distribution data via mercury intrusion porosimetry for HS-460 grout formulations are proprietary and not yet available in the open literature.

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    Certification & Compliance
    More Introduction

    Designated HS-460, the high-Tg vinyl acetate-ethylene (VAE) copolymer emulsion serves as a primary binder during the spray-drying production of redispersible polymer powders (RPPs). Its monomer ratio is engineered to deliver a glass transition temperature exceeding 15 °C after protective colloid integration and drying, a value notably above the −10 °C to 5 °C range typical of commodity VAE dispersions used in construction. The aqueous latex combines a solids content of 55 ± 1 wt% (per ISO 1628-1), a Brookfield RVT viscosity of 800–1,200 mPa·s (spindle 4, 20 rpm, 25 °C), and a pH of 4.5–5.5. Particle size distribution measured by dynamic light scattering places the d50 between 1.0 µm and 1.5 µm, with a minimum film formation temperature of approximately 18 °C in the neat emulsion. These parameters position HS-460 for powders requiring elevated mechanical strength, thermal resistance, and anti-blocking behavior that low-Tg analogues cannot provide.

    How Does the High Glass Transition Temperature Influence Powder Spray-Drying Efficiency?

    The shift from a soft copolymer backbone to one with a Tg above 15 °C introduces distinct processing demands at the industrial spray-drying tower. Laboratory and pilot-plant data from co-current rotary atomizer dryers (Niro type, chamber diameter 3.2 m, inlet air temperature 160–190 °C, outlet 70–85 °C) indicate that the drying rate curve exhibits a shorter constant-rate period relative to flexible-chain VAE grades. The latex feed must be pre-heated to 40–45 °C to lower extensional viscosity and prevent premature skin formation on atomizer wheel vanes. Without this adjustment, oversized agglomerates (> 250 µm) increase by 8–12% mass fraction, as confirmed by Alpine air-jet sieve analysis per ASTM D1921.

    A critical operational boundary emerges in the cyclone separation stage: powders derived from HS-460 exhibit a bulk density of 450–520 g/L (ISO 60) and a Hausner ratio of 1.35–1.45, reflecting moderate cohesiveness. When ambient relative humidity exceeds 60% at baghouse discharge, the powder’s surface adsorption capacity drives moisture uptake to 1.5 wt% within 20 minutes, as measured by Karl Fischer titration (ISO 15512). Conveying lines must therefore maintain dew points below −5 °C using desiccant dehumidifiers, or operators observe progressive flow problems in bulk tanker loading. Published data for this specific configuration is limited, but production-scale experience at facilities operating 3,000–5,000 metric tons per annum confirms that a two-stage cyclone with integrated refrigerated air-purge hoppers reduces lump rejection rates from 3.2% to below 0.7%.

    Film Formation and Redispersion Behavior in Cementitious Matrices

    When an RPP made from HS-460 is mortared into a thin-bed tile adhesive, redispersion proceeds via mechanical shear from a paddle mixer and alkaline hydrolysis of the poly(vinyl alcohol) protective colloid at pH > 12 in portland cement pore solution. The polymer particles released re-coalesce as water is consumed by cement hydration. Differential scanning calorimetry of films cast from redispersed HS-460 powder identifies a single glass transition onset at 19 °C (midpoint, ASTM E1356), demonstrating minimal plasticizer migration into the cement paste. This high Tg correlates with a Shore D hardness of 52–58 after 7-day wet curing at 23 °C, whereas a standard VAE powder with Tg −5 °C yields Shore A 78–85. The increased stiffness directly improves point-load resistance under heavy traffic, as verified by rolling-load tests according to method B of EN 12004:2017.

    The redispersion quality is assessed via sieve retention on a 150 µm screen after 30 s high-shear mixing in a Waring blender at 3,500 rpm. HS-460-based powders consistently produce residue below 0.5% when the spray-drying formula includes a polyvinyl alcohol blend with a hydrolysis degree of 88–90 mol% and Höppler viscosity of 4–6 mPa·s. Substitution of this colloid with a fully hydrolyzed grade (98–99 mol%) raises residue to 1.8–2.4%, a result of excessive colloid crystallinity impeding dissolution. Formulators must therefore balance powder storage stability against rapid redispersion; HS-460’s harder polymer core simultaneously reduces cold flow during bulk storage at temperatures up to 40 °C, enabling 6-month stacked pallet loads without significant caking, as measured by unconfined yield strength in a Schulze ring shear tester (ASTM D6773).

    When incorporating HS-460 powder into a C2TE-class tile adhesive per EN 12004, a dosage window of 3.0–4.5 wt% (based on total dry mortar mass) delivers tensile adhesion strengths exceeding 1.0 MPa after water immersion for 21 days and after heat ageing at 70 °C for 14 days. The high ethylene content of the copolymer backbone, approximately 10–14 wt% as determined by saponification and headspace GC, confers hydrolytic stability of the acetate ester groups, slowing saponification in the alkaline pore solution to a rate constant k of 7.2 × 10⁻⁴ h⁻¹ at 23 °C—about 40% lower than that observed for homopolymeric vinyl acetate dispersions of similar acetate block length. This resistance translates into retained flexibility of the polymer interpenetrating network after 10 years of natural weathering, evidenced by a decrease in elongation at break of only 15–20% measured on free films in accordance with ISO 527-3.

    When Cyclic Freeze-Thaw Conditions Reveal Powder Stability Limits

    Cold-climate logistics introduce thermomechanical stresses on bagged RPP inventory. HS-460 powder subjected to 10 cycles between −20 °C and +25 °C in a climatic chamber (ramp rate 1 °C/min, dwell 4 h at each extremum) exhibits a dry flow deterioration of 0.18–0.25 mL/s per test when measured by the Flodex™ method. The root cause is not ice crystal damage to the polymer particles themselves but rather condensation-induced migration of residual anti-caking agent (precipitated silica, 0.5–1.0 wt%) away from the particle surface into inter-agglomerate capillaries. Redispersion quality is unaffected for samples kept in factory-sealed PE-lined paper sacks with a moisture vapor transmission rate below 0.5 g/m²/day (ASTM F1249). Bulk shipments in unlined FIBCs, however, show a rise in sieve residue to 1.1–1.8% after a single winter-season transit through northern European distribution chains. This operational constraint necessitates specifying barrier packaging or admixing hydrophobic fumed silica at the expense of a 3–5% reduction in water resistance of the cured mortar, a trade-off documented in internal quality assurance records at two major dry-mix producers.

    Comparative Property Matrix Among VAE Grades for Redispersible Powders

    Property / Test Method HS-460 (High-Tg) Conventional VAE (Tg 0–5 °C) Flexible VAE (Tg −15 °C)
    Polymer glass transition (powder), °C, ASTM E135616–201–5−18 to −12
    Minimum film formation temperature (powder), °C, ASTM D23544–80–2−5 to −2
    Ash content at 800 °C, %, ISO 3451-110–1410–1411–15
    Bulk density, g/L, ISO 60450–520420–480380–440
    Tensile bond strength (standard climate), MPa, EN 13481.2–1.80.9–1.40.7–1.1
    Elongation at break (free film), %, ISO 527-3120–180250–400600–900
    Compressive strength contribution (mortar), % increase vs. unmodified, EN 13892-110–185–100–4
    Blocking resistance (powder), visual rating (1–5), internal method1.0–1.52.5–3.54.0–4.5
    Redispersion sieve residue (150 µm), %, internal method<0.50.3–0.80.2–0.6

    The matrix highlights HS-460’s strength, anti-blocking, and heat-resistance advantages at the cost of substantially lower elasticity compared to flexible VAE types. This performance envelope suits ceramic tile adhesives for large-format tiles, repair mortars, self-leveling underlayments, and external thermal insulation composite system base coats where dimensional stability under thermal loading is prioritized over crack-bridging capability.

    In comparison with acrylic-based or styrene-acrylic RPPs, the VAE polymer backbone of HS-460 inherently offers superior wetting of cement grains and higher adhesion to concrete substrates without the need for external coalescents. The ethylene segments introduce hydrophobicity sufficient to achieve a capillary water absorption coefficient of 0.08–0.12 kg/m²·h0.5 (EN 1015-18) when dosed at 4 wt% in a standardized mortar, outperforming poly(vinyl acetate)-only grades that typically exceed 0.2 kg/m²·h0.5. However, attempts to blend HS-460 powder with amine-based epoxy hardeners or strong Lewis acids in reactive cementitious composites must be avoided owing to premature crosslinking of residual acetate groups and destabilization of the protective colloid sheath. Manufacturers supplying two-component cement-polymer hybrid systems should conduct compatibility trials on a pilot mortar mixer to verify that open time remains within the project specification.

    Industrial Processing Windows and Manufacturing Tolerances

    Process Parameter Setpoint / Range Criticality Measurement Device
    Spray-dryer inlet temperature175 ± 10 °CHigh: affects particle morphologyMulti-point RTD array, ±1 °C
    Spray-dryer outlet temperature78–82 °CHigh: controls residual moistureDew-point sensor & dry-bulb thermocouple
    Atomizer wheel speed12,000–14,000 rpmMedium: shifts PSDLaser tachometer
    Feed latex temperature40–45 °CHigh: prevents skinningIn-line RTD, PID-controlled heat exchanger
    Post-dryer fluid-bed temperature30–35 °CMedium: anti-caking integrationIR pyrometer scanning bed surface
    Cooling screw residence time8–12 minMedium: limits thermal historyConveyor speed encoder
    Packaging humidity controlDew point −5 °CHigh: prevents lump formationChilled-mirror hygrometer

    Batch-to-batch variation in HS-460 emulsion typically remains within a narrow band: the solids content deviation is held to ±0.5 wt%, and the molecular weight distribution as determined by GPC-MALLS (polystyrene equivalent in THF) shows an Mw of 450,000–520,000 g/mol with a polydispersity index of 2.8–3.2. During the spray-drying campaign, operators monitor the real-time particle size distribution of the powder using an on-line laser diffraction probe (Malvern Insitec) mounted in the free-fall stream after the fluid bed. An upward drift in d90 above 180 µm typically signals a drop in atomizer wheel tip velocity or a cooling of the liquid feed, triggering an automated diversion valve to reject off-spec material. These rigorous controls enable HS-460 powder to consistently meet the EN 12004 requirement for open time adhesion greater than 0.5 MPa after a 30-minute placement delay, even in formulations incorporating high-range water reducers based on polycarboxylate ethers.

    Additives tolerated within the emulsion before spray drying include benzoate-based plasticizers at up to 2 wt% of polymer solids to lower MFFT if downstream winter-grouting applications demand it, as well as defoamers of the mineral oil/silica type (typical addition 0.1–0.3 wt%) to control air entrainment. However, addition of polypropylene glycol (PPG) with molecular weight above 1,000 g/mol results in phase separation during storage of the liquid latex and must be excluded. Polyvinyl alcohol stabilizers with a degree of hydrolysis outside the 88–92 mol% range similarly lead to coarse dispersions and eventual sedimentation within 48 h. These formulation constraints define the operational space for HS-460 variant customization, ensuring that the product remains a reliable backbone for dry-mix mortar manufacturers seeking high mechanical performance without sacrificing processability.

    For high-build trowelling mortars applied in thicknesses exceeding 10 mm, the high Tg of HS-460 reduces the risk of plastic settlement cracking because the polymer network stiffens early during dewatering. Ultrasonic pulse velocity measurements (PUNDIT, 54 kHz) conducted on 40 × 40 × 160 mm prisms show that the dynamic modulus of elasticity reaches 12 GPa after 28 days of wet curing, compared to 8–9 GPa for flexible VAE-modified mixes of identical polymer volume fraction (0.15–0.18). This elevated stiffness, however, necessitates careful joint design to accommodate thermal movement, as the coefficient of linear thermal expansion of the hardened composite increases from approximately 8 × 10⁻⁶ K⁻¹ (unmodified mortar) to 11 × 10⁻⁶ K⁻¹ at 4 wt% powder loading (TMA, ASTM E831). Engineering specifications for large-area unbonded screeds should therefore incorporate expansion joints at intervals no greater than 20 m when HS-460 is the sole binder modifier, unless crack-width calculations based on restrained shrinkage testing (ASTM C1581) indicate otherwise.