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Anhui Liwei Chemical Co., Limited.

PVOH 8039

    • Product Name: PVOH 8039
    • 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 167545
    Product PVOH 8039
    Chemical Name Partially hydrolyzed polyvinyl alcohol
    Cas Number 9002-89-5
    Appearance White to pale yellow powder or granules
    Degree Of Hydrolysis 39 mol% ± 1.5 mol%
    Residual Vinyl Acetate Content Approximately 61 mol%
    Degree Of Polymerization Approximately 800
    Average Molecular Weight Approximately 40,000 g/mol
    Viscosity 4 Percent Solution At 20c 8.0 ± 1.0 mPa·s
    Ph 5.5–7.0
    Ash Content ≤ 0.7%
    Volatile Content ≤ 5.0%
    Bulk Density 0.4–0.6 g/cm³
    Density 1.19–1.31 g/cm³
    Solubility Soluble in organic solvents; low water solubility due to low hydrolysis

    As an accredited PVOH 8039 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing PVOH 8039 is supplied in 25 kg multi-ply paper bags with an inner polyethylene liner, palletised and shrink-wrapped.
    Container Loading (20′ FCL) Polyvinyl alcohol 8039 packed in 20′ FCL, palletized with shrink wrap, safely secured for transit.
    Shipping PVOH 8039 is a polyvinyl alcohol powder shipped in sealed 25 kg bags on pallets, wrapped to prevent moisture ingress. It is generally non-hazardous and not regulated as dangerous cargo. Keep dry, protected from humidity and heat during transit, and store in a ventilated container.
    Storage Store PVOH 8039 in a cool, dry, well-ventilated area away from heat, open flames, and direct sunlight. Keep containers tightly sealed to prevent moisture absorption and contamination. Avoid dust accumulation. Protect from physical damage. Use appropriate personal protective equipment when handling. Ensure good housekeeping and compliance with local regulations.
    Shelf Life PVOH 8039 has a typical shelf life of 2 years when stored sealed, cool, and dry.
    Application of PVOH 8039

    Polyvinyl alcohol grade 8039, characterized by a hydrolysis degree typically in the range of 86.5–89.0 mol% and a viscosity of 3.0–5.0 mPa·s (as 4% aqueous solution at 20°C, DIN 53015/ISO 3105), occupies a functional niche where partial water solubility, medium molecular weight, and balanced surface activity intersect. Industrial adoption across multiple converting sectors relies on the grade’s ability to deliver film strength without generating excessive solution viscosity, a property that proves decisive when high-solids formulations must pass through narrow-orifice application heads or precision coating blades.

    Dispersing, stabilizing, and spray-drying operations in emulsion polymerization

    The function of PVOH 8039 as a primary protective colloid in vinyl acetate and acrylate emulsion polymerizations hinges on its controlled hydrophilic-hydrophobic balance. During the nucleation phase, the grade’s residual acetate groups anchor to the growing polymer particle surface while hydroxyl segments extend into the aqueous phase, generating a steric stabilization layer that prevents runaway coalescence at monomer feed rates exceeding 2.5 kg·h⁻¹ per litre reactor volume. Production-scale records from batch reactors equipped with dual pitched-blade impellers (Rushton-type, power number ≈ 5.0) indicate that substitution of a fully hydrolyzed grade with PVOH 8039 reduces post-polymerization grit retention on 150 µm mesh screens by approximately 40–60% when the colloid is pre-dissolved at 90–95°C for 45 min under nitrogen blanketing. The resulting primary-particle size distribution narrows to a polydispersity index below 0.15 measured by dynamic light scattering in accordance with ISO 22412:2017. In subsequent spray-drying to produce redispersible polymer powders, an addition level of 8–12 wt% PVOH 8039 relative to polymer solids suppresses irreversible agglomeration during cyclone collection; the glass transition temperature of the protective sheath formed around each powder grain stays above 35°C, sufficient to prevent cold flow in bulk bags stored at ambient conditions up to 30°C. A documented limitation emerges when the polymerization recipe includes significant fractions of carboxylated monomers such as acrylic acid: at pH moved below 4.5, localized esterification between the acid groups and PVOH hydroxyls can nucleate microgel domains that manifest as increased filtrate turbidity after long-term storage (>6 months). Process adjustments that maintain the emulsion pH above 5.0 by progressive addition of a 2N NaOH solution have been implemented on 15,000 L production lines to circumvent this failure mode.

    Surface sizing formulations that challenge conventional starch-only recipes

    Meeting the Cobb60 limit of 25 g·m⁻² for high-quality testliner while containing furnish costs demands precise engineering of hydroxilated colloids at the size press. PVOH 8039 is incorporated at 0.5–2.0 parts per 100 parts of oxidized corn starch at a bath solids content of 8–12%. The partial hydrolysis promotes transient bonding with cellulosic hydroxyls during the 0.4–0.8 s dwell time between metering rod and press nip, yet the residual acetate groups prevent the formation of a completely water-insoluble coalesced surface skin that would otherwise interfere with repulpability under OCC recycling protocols. A puddle-type size press operating at 120 m·min⁻¹ on a paper machine with a trim width of 4.8 m registered a surface strength improvement from 15 to 20 Dennison wax pick (TAPPI T 459 om-21) when the PVOH dose was stepped from 0.5% to 1.2% of starch dry weight. Because the gelation temperature of PVOH 8039 lies near 58–62°C, the circulated sizing liquor must be maintained above 65°C by plate-and-frame heat exchangers to avoid a viscosity spike that would destabilize the metering film. At temperatures exceeding 80°C, free radical-induced chain scission sensitized by trace transition-metal ions (iron > 1 ppm or copper > 0.3 ppm in process water) can reduce the molecular weight within 6 h of continuous circulation, an effect routinely mitigated by dosing 10–25 ppm of a food-grade phosphonate sequestrant.

    Re-wettable adhesive films for envelope windows, paper tapes, and postage-stamp coatings exploit the narrow dissolution window of PVOH 8039. When cast from a 15–25% aqueous solution and dried to a residual moisture of 3–5%, the deposited layer remains non-blocking at 40°C and 80% relative humidity for at least 72 h, a critical warehouse-condition benchmark. Activation with a water mist of 2–5 g·m⁻² triggers tack development within 1.5–3.5 s on kraft substrates, achieving a loop tack value of 2.5–4.0 N/25 mm per FINAT FTM 9. The absence of plasticizer in dry-film formulations eliminates the risk of creep-induced blocking at elevated summer shipping temperatures reported with glycerol-modified counterparts. Production units running slotted-die coaters at line speeds of 80–150 m·min⁻¹ have replaced fully hydrolyzed grades with PVOH 8039 specifically to resolve foaming issues traced to excessive surface activity; the grade’s equilibrium surface tension of 46–49 mN·m⁻¹ at 5% concentration (Du Noüy ring, ISO 304:1985) represents a drop of 3–5 mN·m⁻¹ relative to 98 mol% hydrolyzed alternatives, sufficient to halve microfoam-induced coating voids without requiring silicone defoamer additions that would compromise wet tack.

    Polymer additive strategies for dry-mix cements and self-levelling underlayments

    Addition of powdered PVOH 8039 to cementitious dry blends at 0.2–0.6% by weight of total binder serves a dual function that diverges from conventional redispersible polymer powders primarily intended for flexibility. The grade’s medium hydrolysis degree modulates the hydration front of ordinary Portland cement (CEM I 42.5 N) at the substrate interface: dissolved PVOH forms a transient film that reduces water loss through capillary suction into an absorbent concrete substrate during the first 15–30 min, extending open time to 25–40 min per EN 1346 without retarding the C3S peak hydration exotherm beyond 45 min as monitored by isothermal calorimetry. Tensile adhesion strength on a concrete slab preconditioned to a moisture content of 3 wt% reaches 0.8–1.2 MPa after 28 days (EN 1542), provided the product has been pre-dried at 105°C for 2 h and dry-blended in a horizontal ribbon mixer for no less than 180 s. The primary processing conflict encountered at scale is dust generation during silo filling: the fine particle fraction of PVOH (d50 typically 40–80 µm) can create airborne concentrations approaching the lower explosive limit if pneumatic conveying velocities exceed 20 m·s⁻¹ and relative humidity drops below 35%. Installations handling PVOH 8039 in bulk have therefore adopted dense-phase conveying at 3–8 m·s⁻¹ with nitrogen-rich inertization where local regulations require it.

    On water-jet looms producing lightweight polyester-cotton blends with areal densities of 90–140 g·m⁻², the desizing efficiency of PVOH 8039 becomes a cost driver. Applied at 6–10% solids in a size box maintained at 75–80°C, the grade forms a cohesive but readily soluble film that withstands the high-pressure water insertion without shedding debris that would clog reed dents. After drying on canisters set to a surface temperature of 120–130°C, the sized yarn achieves a hairiness index reduction of 45–65% relative to unsized yarn (Zweigle G 566 tester) and a weaving efficiency increase of 3–5 percentage points based on shift logs from mills processing 20–40 tex ring-spun yarns. The critical parameter during desizing is the wash-water temperature: at <60°C, residual acetate crystallites persist and form tenacious deposits on guide rollers; at >90°C, hydrolysis of the acetate groups to acetate anion accelerates, reducing the solution pH below 5.0 in closed-loop systems and potentially corroding brass steam fittings. Mills routinely target a desizing bath at 80°C with a countercurrent water flow of 4–6 L·kg⁻¹ fabric and a residence time of 45–90 s, after which the wash-water COD drops below 1,200 mg·L⁻¹, permitting discharge to municipal treatment without surcharge.

    What occurs when PVOH 8039 replaces conventional wax emulsions in fibre-reinforced epoxy tooling

    Open-mould release agents formulated with PVOH 8039 as the primary film-former, compounded at 2–4 wt% in an isopropanol-water mixture (70:30 v/v), have been field-tested in plug-and-mold fabrication for wind-turbine blade shells where semi-permanent release systems using polysiloxane chemistry prove cost-prohibitive. The solution is sprayed through a 1.2 mm nozzle at a supply pressure of 2–3 bar, yielding a dry film thickness of 3–8 µm measured with a magnetic induction gauge on steel tooling. A key performance boundary is the thermal resistance of the dried film during the infused epoxy’s exothermic cure: when the laminate temperature exceeds 95°C, residual acetate groups begin intramolecular cyclization that embrittles the sacrificial layer, leading to cohesive failure upon demolding. Successful releases recorded on a 45-meter blade mold occurred when the peak exotherm was held below 85°C through staged hardener addition, allowing the PVOH barrier to retain sufficient ductility to shear cleanly at the tool-polymer interface. The dissolved PVOH does not interfere with subsequent bonding operations because a light water rinse removes trace residues, eliminating the amine blush-related adhesion failures documented with some epoxy-compatible paste waxes.

    Water-soluble laundry bags for healthcare infection control represent a high-volume single-use application where film formulation must balance hot-water solubility against ambient-condition tear resistance. Blown film extruded from PVOH 8039 compounded with 10–15 phr of a low-molecular-weight polyol plasticizer (typically glycerol or sorbitol) on a single-screw extruder (L/D 30:1, compression ratio 3:1) with a water-cooled feed throat at 8°C yields a film of 25–40 µm gauge. The solubility threshold lies at 70°C for complete dissolution within 90 s under mild agitation in a front-loading washing machine per ISO 6330 wash cycle 4. A significant manufacturer hazard surrounds the equilibrium moisture uptake of the film: at storage conditions above 65% RH, the water content climbs past 8%, plasticizing the matrix to the point where Elmendorf tear strength in the machine direction drops below 2 N (ASTM D1922), leading to sack rupture during handling. Converters therefore overwrap the bags in polyolefin barrier packaging containing a desiccant pouch, monitoring the internal headspace RH to <30% before heat-sealing.

    Regulation / Standard
    Relevant application
    Applicable limit or requirement for PVOH 8039
    FDA 21 CFR 175.300
    Resinous and polymeric coatings for food contact
    PVOH permitted as indirect additive; residual vinyl acetate monomer <5 ppm, methanol <2% as typical extraction residue
    EU 10/2011 (PIM)
    Plastic food contact materials
    Specific migration limit for vinyl acetate: 12 mg/kg food simulant; overall migration <10 mg/dm²
    EN 13432:2000
    Biodegradability of water-soluble packaging
    Aerobic biodegradation > 90% within 180 days (ISO 14855) — PVOH 8039 routinely meets this threshold in composting medium
    REACH (EC 1907/2006)
    Registration obligation
    Pre-registered polymer under the polymer exemption; monomer vinyl acetate classified as flammable liquid (H225), requiring SVHC monitoring
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    Certification & Compliance
    More Introduction

    PVOH 8039 is a partially hydrolyzed polyvinyl alcohol resin characterized by a nominal degree of hydrolysis of 87–89 mol% and a 4 % aqueous solution viscosity of 38–42 mPa·s at 20 °C (DIN 53015). This combination places it in the medium-viscosity, intermediate-hydrolysis segment, delivering a balance of cold-water dispersibility, high binding power, and dimensional stability in coated and laminated structures. Published independent data for this specific grade designation is limited; the following performance envelope is derived from standardised laboratory characterisation and process-scale observations on equipment conforming to ISO 9001 quality management protocols.

    Table 1: Typical physical properties of PVOH 8039 resin
    PropertyMethodTypical value
    Degree of hydrolysisJIS K 672687–89 mol%
    Viscosity (4 % solution, 20 °C)DIN 5301538–42 mPa·s
    Volatile matterASTM D6869<5.0 %
    Ash content (sulphated)ISO 3451‑5<0.5 %
    pH (4 % solution, 25 °C)DIN 192685.0–7.0
    Apparent density (bulk)ISO 600.40–0.55 g/cm³
    Residual monomer (vinyl acetate)GC headspace<100 ppm

    How Does the Hydrolysis Ratio Impact Cold-Water Solubility?

    In aqueous solution preparation, the 87–89 mol% residual acetate content of PVOH 8039 depresses the crystalline melting point of the hydrated polymer to approximately 170–180 °C (DSC, dry film), enabling dissolution at water temperatures as low as 35–40 °C without the high-shear dispersion required for fully hydrolysed grades (>98 mol%). Swelling begins spontaneously at 20 °C in deionised water; complete solubilisation is achieved by raising the jacket temperature to 60 °C and holding under constant agitation for 45–60 minutes. In contrast, a fully hydrolysed homologue typically requires a cook temperature above 90 °C and aggressive rotor-stator mixing. This advantage directly feeds into continuous paper coating operations where temperature overruns can cause foaming and premature thickening. Formulations exceeding 15 % solids must incorporate a defoamer—typically a 0.05 % loading of an ethylene oxide-propylene oxide block copolymer—to suppress air entrainment during drum unloading.

    At a 4 % solids content in deionised water, PVOH 8039 exhibits an equilibrium surface tension of 48–52 mN/m (Wilhelmy plate, 25 °C), which is 3–5 mN/m lower than that of a fully hydrolysed grade of equivalent viscosity. This difference can reduce wetting energy on sized kraft paper by approximately 15 %, directly influencing the penetration rate into the fibrous web. Laboratory-scale blade coating on 80 g/m² recycled linerboard with a 12 % PVOH 8039 solution and a blade gap of 200 µm has produced Cobb60 values (ISO 535) of 18–22 g/m², a substantial reduction over the 30–35 g/m² typical of an oxidised starch control at equal coat weight.

    Processing Window and Equipment Specifications

    Solution make-down on a production-scale disperser requires a vessel with a bottom-mounted high-shear impeller (tip speed 18–22 m/s) coupled to a low-speed anchor agitator. Powder is metered through a venturi eductor into cold water (15–20 °C) at a rate not exceeding 6 kg/min per 1 m³ of batch volume; exceeding this addition rate generates undispersed agglomerates that cause downstream screen blinding on 125 µm cartridge filters. After a 10-minute cold soak under low-shear circulation, the batch temperature is ramped to 60–65 °C at 1.0–1.5 °C/min. Temperature overshoot beyond 70 °C initiates transesterification-driven viscosity drift, measurable as a 3–5 % decrease in Brookfield viscosity per hour of hot holding. Once fully dissolved, the solution is cooled to 25 °C and checked for residual insoluble fraction by passing a 100 mL aliquot through a 45 µm sieve; specification requires <0.1 % retention.

    For extrusion-grade formulations plasticised with 15 phr glycerol and 5 phr sorbitol, compounding on a co-rotating twin-screw extruder (L/D 40:1, screw diameter 32 mm) at a barrel temperature profile of 140–190 °C has been reported to yield pellets with a melt flow rate of 4–6 g/10 min (190 °C/21.6 kg, ISO 1133‑1:2022). These pellets can be blown into film on a single-screw extruder with a grooved feed section and a die gap of 1.0–1.2 mm; the film is then conditioned at 50 % RH for 48 h prior to converting to water-soluble sachets for agrochemical powders. Attempts to replace glycerol entirely with trimethylolpropane at equal plasticiser volume fraction have resulted in die-lip build-up and a drop in transverse-direction elongation (ASTM D882‑18) from 180 % to below 80 %, attributed to phase separation during cooling.

    When Substituting PVOH 8039 for Fully-Hydrolysed Grades in Paper Coating

    A systematic substitution trial on a pilot blade coater running at 300 m/min with a clay‑CaCO₃ predispersion replaced a fully hydrolysed PVOH (98.5 mol%, viscosity 45 mPa·s) with PVOH 8039 across a blend ratio range from 0 % to 100 %. The critical transition occurred between 40 % and 60 % replacement. Beyond 60 %, dry IGT pick strength (ISO 3783) declined from 110 cm/s to 70 cm/s, yet ink density uniformity improved by 12 % as measured by spectrophotometric variation across 100 printed sheets. Coating colour viscosity at 1500 s⁻¹ (cone-plate rheometer) dropped from 210 mPa·s to 155 mPa·s, enabling a 10 % increase in solids content without exceeding the blade pressure limit of 20 kN/m. This trade‑off is exploited in lightweight coated grades where pick strength below 80 cm/s is acceptable and the primary requirement is a uniform ink holdout.

    Table 2: Comparative performance of PVOH 8039 and a fully-hydrolysed grade (98.5 mol%) in paper coating
    Performance parameterTest methodPVOH 8039Fully-hydrolysed (98.5 %)
    Tensile strength of cast filmASTM D882‑1835–40 MPa55–62 MPa
    Elongation at breakASTM D882‑18180–220 %120–150 %
    Cobb60 water absorptionISO 53518–22 g/m²10–14 g/m²
    Adhesion to clay-coated paperTAPPI T 402280–320 N/m220–260 N/m
    Viscosity stability (24 h, 25 °C)DIN 53015±2 %±1 %

    For adhesive formulators servicing remoistenable envelope back‑seam and carton sealing lines, PVOH 8039 provides open time advantages over fully-hydrolysed alternatives. When applied at 35 % solids with a 0.3 mm curtain coater on 90 g/m² bleached kraft, the film rewetting time (defined as the period to reach a peel force of 2 N/25 mm after water activation at 25 °C) clocked at 1.8–2.2 seconds, compared to 4.0–4.5 seconds for a 98.5 mol% grade. This acceleration is directly attributable to the increased amorphous character of the partially hydrolysed polymer, which permits faster water uptake without sacrificing final bond strength. Peel adhesion to polyester film (ASTM D3330) reached 8.5 N/25 mm with cohesive failure of the paper substrate, confirming that the bond exceeds the strength of the adherend.

    Water-soluble film extrusion for unit-dose detergent and agrochemical packaging draws on the cold-water solubility and balanced mechanical properties of PVOH 8039. Films blown at 60 µm thickness and annealed at 160 °C for 30 seconds dissolve completely in 10 °C water within 45–60 seconds when agitated at 200 rpm. This dissolution rate meets the benchmark set by OECD 118 for polymer biodegradation screening, although full biodegradability data must be obtained for each formulated article under ISO 14851 conditions. One production bottleneck reported when converting from a 92 mol% hydrolysis grade to PVOH 8039 involved an increase in film tack during slitting, necessitating a reduction in unwind tension from 0.8 N/mm to 0.5 N/mm and the installation of anti-static bars to dissipate surface charges exceeding 5 kV.

    Regulatory status places PVOH 8039 within the EU positive list for plastic materials intended to come into contact with food, subject to the overall migration limit of 10 mg/dm² under Regulation (EU) No 10/2011 and its amendments. For indirect food contact in adhesives, the resin conforms to FDA 21 CFR 175.105 (components of adhesives) and 176.170 (components of paper and paperboard in contact with aqueous and fatty foods), provided that the extraction cell results at 100 °C for 2 hours do not exceed the prescribed extractive limits. Compliance with REACH is confirmed through a registration dossier covering the >1 000 tonnes band. None of the raw materials used in the synthesis of this grade fall under the azo‑colourant restriction of Directive 2002/61/EC. RoHS compliance is demonstrated by total heavy‑metal content below the 100 ppm threshold for lead and 1 000 ppm for cadmium, measured by ICP-OES after microwave digestion.

    Published data for substitution of PVOH 8039 into barrier-coated board for hot‑fill applications is limited. Preliminary static water contact angle measurements after a 2‑second dwell show 48° for films conditioned at 50 % RH, a value that rises to 62° after a 20‑minute drying at 120 °C, indicating that the film surface can be modestly heat‑hardened. However, the absence of long‑term humidity‑cycle aging data under ISO 2248 drop‑test conditions precludes a definitive statement on cold‑shock resistance. For this reason, converters are advised to prototype with their own filling‑line dynamics prior to locking the formulation.