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Anhui Liwei Chemical Co., Limited.

Wanwei PVA 14-92(L) (PVA 092-14)

    • Product Name: Wanwei PVA 14-92(L) (PVA 092-14)
    • 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 840636
    Product Name Wanwei PVA 14-92(L) (PVA 092-14)
    Viscosity 13-15 mPa·s (4% aqueous solution, 20°C)
    Degree Of Hydrolysis 92±1 mol%
    Saponification Value 10-15 mg KOH/g
    Ph 5-7
    Ash Content ≤0.3%
    Volatile Content ≤5%
    Average Degree Of Polymerization ~1400
    Appearance white or yellowish granular powder
    Solubility soluble in hot water (≥90°C)

    As an accredited Wanwei PVA 14-92(L) (PVA 092-14) factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Wanwei PVA 14-92(L) is packaged in 25 kg multi-wall paper bags with polyethylene liner, ensuring product protection.
    Container Loading (20′ FCL) 20′ FCL: Wanwei PVA 14-92(L) loaded in 20kg bags on pallets, secured with waterproof lining, protected from moisture and contamination.
    Shipping Wanwei PVA 14-92(L) is shipped as a dry, free-flowing powder in multi-layer kraft paper bags or fiber drums. Protect from moisture and humidity during transport. Non-hazardous, but minimize dust generation. Ensure clean, dry containers and avoid direct contact with water to prevent caking or dissolution.
    Storage Store in a cool, dry, well-ventilated area, away from heat, open flames, and direct sunlight. Keep the original container tightly sealed to prevent moisture absorption and contamination. Avoid dust accumulation and contact with strong oxidizing agents. Maintain moderate humidity and temperature to preserve product quality and ensure safe handling.
    Shelf Life Shelf life is approximately 2 years when stored unopened in a cool, dry place, away from moisture and sunlight.
    Application of Wanwei PVA 14-92(L) (PVA 092-14)

    A 35:65 w/w dry blend of polyvinyl alcohol grade 14-92(L) (hydrolysis 91–93 mol%, 4% aqueous viscosity 14–18 mPa·s, ash ≤0.5%) and oxidized corn starch is slurried in deionized water at 25°C ambient before injection into a continuous jet cooker operating at 130–135°C for 20–25 seconds residence time. The cooked size, maintained at 85–90°C in a circulation tank with low-shear mechanical agitation, is supplied to a double-squeeze sizing box on a high-speed sectional warping beam line. A wet pick-up of 9–11% on Ne 40/1 combed cotton warp yarn is targeted by regulating the squeezing roller pressure between 0.25–0.35 MPa. Because the partially hydrolyzed grade forms a film with a glass transition near 45°C and moderate cold-water swellability, the size paste penetrates the yarn hairiness core while leaving a pliable surface layer that resists shedding under the reciprocating reed of an air-jet loom operating at 800 rpm. Tensile strength retention after sizing, tested per ISO 13934-1, averages 12–15% improvement over unsized yarn, and hairiness index measured by a Zweigle G567 instrument drops by 38–42%. A critical processing bound exists: if the size liquor pH drifts below 5.5 due to starch acid degradation products, the protective colloid character of 14-92(L) is partially suppressed, causing localised gum drop accumulation on the first immersion roller. Desizing during the pre-treatment stage uses a 0.5% non-ionic surfactant bath at 70°C for 15 minutes and requires no enzymatic assist, a distinct advantage over fully hydrolysed grades that often demand elevated caustic scouring. Where the mill operates at relative humidity above 60%, pre-conditioned bulk bags stored at 15–25°C must be sealed immediately after weighing to avoid surface tacking of the granular material.

    What Limits the Pick-Up Rate When 14-92(L) Replaces Full-Hydrolysis PVA on the Size Press?

    On a metered-film size press running at 1200 m/min, a surface-sizing formulation of 14-92(L) combined with a low-viscosity amphoteric starch in a 25:75 solids ratio is typically prepared to 10–12% total solids content. The coil-wrapped transfer roll gap is set to deliver a film thickness of 14–18 μm to the paper web, which enters at 6–8% moisture. In this operating window, the partial hydrolysis of 14-92(L) confers a noticeable foam-suppression advantage over fully hydrolysed counterparts, reducing the airborne starch mist at the nip and eliminating the need for silicone-based defoamer that can otherwise contaminate the white-water circuit. Off-machine IGT surface strength, determined per ISO 3783, registers a 2.8–3.4 m/s pick velocity for offset printing grades with filler content up to 18%. The low ash attribute (conductivity of a 4% solution typically <250 μS/cm) minimizes abrasive wear on ceramic-coated metering rods. However, the pick-up efficiency becomes sensitive to the water retention index of the base sheet: when internal sizing with AKD exceeds 0.15% on fibre weight, the wicking-driven penetration of 14-92(L) into the fibre-fibre bond area decreases by approximately 15%, visible as a step-change in the oil absorptiveness of the sized sheet measured by the Cobb-Unger test. To offset this, the runnability window demands that the starch cooked with 14-92(L) is not allowed to cool below 60°C during holding, or retrogradation will create microgels that plate out on the backing rolls.

    A re-wettable adhesive lacquer for business form gluing is formulated by dissolving 14-92(L) into a co-solvent water/ethanol system at 65°C to a final concentration of 18%, then incorporating 5% (w/w on PVA) of a non-crystallising plasticiser such as trimethylolpropane ethoxylate and 0.3% potassium sorbate as preservative. The solution is applied via a direct gravure cylinder with 45 lines/cm engraving onto a clay-coated board surface at a depositing rate of 4.5–6.0 g/m² dry weight. Activated simply by a 20–30 μm water spray pulse, the film develops an open time of 3–8 seconds before the bond forms, a range that accommodates high-speed mail insertion. Adhesion performance falls under FDA 21 CFR 175.105 for indirect food contact and is validated through a 180° peel test at 300 mm/min crosshead speed, producing a value of 2.0–3.5 N/25 mm when bonded to uncoated kraft. A limiting factor emerges in packaging environments with sustained temperature above 30°C and relative humidity above 80%: the coating absorbs ambient moisture and the passive blocking begins at stacked board pressures exceeding 0.12 kg/cm². To circumvent premature delamination in the reel, the dried film should have a residual moisture content not exceeding 6% as measured by Karl Fischer titration, achieved by passing the web through a three-zone drying tunnel with the first zone not exceeding 95°C air temperature to prevent skin-over.

    How Does 14-92(L) Influence the Latex Copolymer Microstructure in High-Solids VA/VeoVa Dispersions?

    In semi-batch vinyl acetate–ester polymerisations catalyzed by persulfate redox initiation at 65–70°C, 14-92(L) serves as the primary protective colloid premixed with deionised water to a 10% stock solution and charged to the reactor at 4.5–5.5 parts per hundred of total monomer. Its intermediate degree of hydrolysis places the hydroxyl block length distribution in a regime where surface grafting proceeds to an equilibrium grafting ratio of roughly 12–18% without causing soluble polymer build-up that thickens the aqueous phase and hampers heat removal. A comparative series run in a 5-litre jacketed glass reactor with anchor stirring at 150 rpm and internal temperature control ±1°C illustrates the viscosity differentiation.

    Protective colloid type4% aqueous viscosity at 20°C (mPa·s)NVM of finished latex (%)Brookfield RVT viscosity, spindle #4 at 20 rpm (mPa·s)Coagulum on 100 mesh sieve (%)Freeze-thaw cycles passed per ISO 1147
    14-92(L) (hydrolysis 92 mol%)1655.23200<0.054
    PVA 15-79 (hydrolysis 79 mol%)1554.848000.122
    PVA 17-88 (hydrolysis 88 mol%)2354.574000.083
    PVA 14-98 (hydrolysis 98 mol%)1853.911000<0.021

    The data, obtained under identical initiator feed profiles and total solid target 55%, demonstrate that 14-92(L) produces a latex with the lowest finished viscosity among the partially hydrolysed comparators and provides the highest freeze-thaw stability without exceeding molecular weight build-up that would obstruct screen transfer during the manufacturing of waterborne contact adhesives. The low ash content is decisive here because residual sodium acetate from the manufacturing saponification, if present above 0.8%, would interfere with the partitioning of the emulsifier between the particle surface and the aqueous serum, shifting the particle size distribution to a D(0.5) below 800 nm and jeopardizing shear stability in pressure-fed wood gluing systems. The formulation must avoid combination with primary amine-based pH buffers above pH 8.5 during the delayed addition phase, as the acetate groups capable of transamidation accelerate precrosslinking at the monomer droplet interface.

    Water-Soluble Detergent Film — Melt Viscosity Instability Near 200°C

    A twin-screw compounding line with L/D 44 and co-rotating intermeshing screw profiles is used to blend 14-92(L) with 28% (by weight) glycerol as primary plasticiser, 3% sorbitol as secondary humectant, and 0.5% fine-particle silica as antiblocking agent. The dry-blended premix is gravity-fed into the first barrel zone at 80°C, progressing through a temperature ramp to 185°C at the dispersive mixing element and exiting through a slit die maintained at 195°C, at which point the melt flow index measured under 10 kg load ranges 1.2–1.8 g/10 min. The cast film, quenched on a polished chill roll at 8°C to prevent glycerol sweat-out, is oriented in the machine direction at a draw ratio of 1:3.2 and wound into master rolls of 35 μm thickness. Because residual PVA crystallinity arising from the 2–3% non-hydrolysed acetate spacer units is kinetically trapped during the rapid quench, the film exhibits a dissolution time of 28–34 seconds in 10°C water per the standardised single-chamber pod protocol, outpacing fully hydrolysed grades by roughly 40%. Tensile properties subjected to ASTM D882 at 250 mm/min gauge length and 23°C at 50% RH yield a longitudinal modulus of 3200–3800 MPa and an elongation at break of 180–210%. The plasticiser system must avoid any boric acid crosslinker often used for corrugator adhesives, because the resultant borate–diol network increases the hot-water insoluble residue above the 0.5% limit specified by major detergent unit-dose brand specifications. Processing right at the thermal degradation onset of the backbone (≈220°C) requires that extruder screw torque not surpass 75% of nominal drive load, else acetaldehyde generated through chain scission raises the head-space VOC content of the packaged film beyond 0.8 ppm.

    A dry-mix cementitious skim coat compound consisting of white Portland cement, graded calcium carbonate filler (D50=20 μm), and 0.8–1.2% 14-92(L) powder by total dry weight is packaged in moisture-barrier bags. Upon addition of 32–36% potable water at the job site and low-speed mixing with a helical paddle at 400 rpm, the PVA rewets and gradually dissolves, raising the plastic viscosity of the paste to 280–340 Pa·s measured on a Brookfield helical-path spindle at 5 rpm. The resultant open time at 23°C and 55% RH on a standard gypsum board substrate extends to 48–55 minutes, assessed by the loss of string tack under a 50 g stylus. Adhesive bond strength tested after 28 days curing per EN 12004 is 0.85–1.05 MPa on concrete tile backs, with failure mode shifting from interfacial to cohesive peeling when the addition rate crosses 1.0%. At incorporation levels above 1.5%, the air content carries over from the dry blending stage and a density deficit of 5–7% appears in the hardened mortar, so a defoaming agent must be introduced. The partially hydrolysed nature of 14-92(L) maintains suspension stability in the presence of calcium hydroxide without rapid gelation, a contrast to fully saponified grades that can form a stiffening gel network, but the formulator must avoid combining the product with calcium chloride-based accelerators in the initial powder phase, as the exothermic heat of hydration during mixing may evaporate intergranular water before the PVA grains fully hydrate.

    When a peelable temporary masking coating is required for anodised aluminium profiles during architectural transport, a 12% aqueous solution of 14-92(L) containing 2.0% diethylene glycol monobutyl ether as coalescent and 0.2% polysiloxane wetting agent is spray-applied through an air-assisted nozzle at a wet thickness of 140 μm. Flash-off occurs in a forced-air tunnel at 40°C for 3 minutes, forming a transparent film with Elmendorf tear strength of 800–1200 mN and adhesion to the substrate of 1–2 N/25 mm by ASTM D3330 tape test, a level that withstands floor-level site dust and incidental tool impact yet permits manual peel removal with a stretch release motion that elongates the film by 300% before fracture. The film remains removable without residue for up to 6 months when not exposed to sustained external UV-A radiation; if concrete wash-down water at pH >10 contacts the masked surface, the edge penetration causes premature debonding, requiring masking on folded edges to be secured with a secondary acrylic pressure-sensitive tape. The solution’s low ash footprint is critical in this scenario because any residual electrolyte promotes galvanic pin-hole attack on the freshly anodised pore layer during the temporary humidity exposure.

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    Certification & Compliance
    More Introduction
    In the portfolio of partially hydrolyzed polyvinyl alcohol resins, Wanwei PVA 14-92(L) (also designated PVA 092-14) occupies a narrow processing window defined by a hydrolysis degree of 92.0 ± 1.0 mol% and a 4% aqueous solution viscosity of 14.0 ± 1.5 mPa·s at 20 °C, measured in accordance with GB/T 12010.3-2010 and GB/T 12010.4-2010. The (L) suffix denotes a low-methanol specification, with residual methyl acetate and methanol typically below 0.8 wt% combined, reducing volatile organic compound release during downstream thermal processing. This grade is manufactured by Anhui Wanwei Group via continuous alcoholysis of polyvinyl acetate in a belt-saponification reactor, yielding a granular solid with a bulk density of 0.45–0.65 g/cm³ and a particle size distribution where ≥90% passes through a 20-mesh sieve. At this intermediate hydrolysis level, the macromolecule retains sufficient acetyl groups (~8 mol%) to disrupt crystalline domains, imparting cold-water solubility without requiring the elevated temperatures needed for fully hydrolyzed (>98 mol%) analogs. Consequently, the product finds utility in cold-water-soluble adhesive films, paper coating binders, textile warp sizes, and as a protective colloid for emulsion polymerization where surfactant demand must be minimized.

    Molecular Architecture Governs the Balance Between Solubility and Film Strength

    The average degree of polymerization for 14-92(L) is approximately 1400, corresponding to a viscosity-average molecular weight near 62 000 g/mol. The residual acetyl content (7.5–8.5 mol%) creates a blocky distribution of hydrophilic hydroxyl and hydrophobic acetate groups along the backbone, reducing crystallite size to ≤15 nm as measured by wide-angle X‑ray diffraction. This semicrystalline morphology allows dissolution in water at 20–25 °C within 15–25 minutes under gentle agitation, whereas an otherwise identical fully hydrolyzed grade (e.g., 17-99) demands sustained heating to 85 °C to achieve comparable clarity. Solution viscosity remains stable for ≥24 hours at pH 5–7, but a sharp drop occurs above pH 9 due to base-catalyzed deacetylation; the alkaline hydrolysis rate constant at 40 °C and pH 10.5 is approximately 0.12 h⁻¹. Film cast from a 10 wt% aqueous solution and dried at 80 °C exhibits a tensile strength of 38–45 MPa (=ISO 527-3 type 5 specimen, 50 mm/min) and an elongation at break of 250–350%, values that position it below fully hydrolyzed grades in strength but substantially higher in flexibility than 05-88 (hydrolysis 88 mol%, elongation >400%). The oxygen transmission rate of a 25 µm blown film (23 °C, 0% RH) is 3.5–5.0 cm³/(m²·day·atm), significantly higher than the <0.5 cm³/(m²·day·atm) barrier typical of 99% hydrolyzed PVOH, a direct consequence of the free-volume contribution from acetate side groups.

    What Distinguishes a Partially Hydrolyzed Grade from Fully Hydrolyzed and Low-Hydrolysis Alternatives?

    Under identical dissolution conditions (10% solids, 25 °C deionized water), 14-92(L) yields a clear solution with <1% insoluble residue, while a 17-99 fully hydrolyzed grade requires pre-swelling at 80 °C and still retains 2–5% insoluble gel particles visible on a 100 µm filter. This cold-solubility advantage is exploited in repulpable adhesive formulas where heated dissolution tanks are unavailable. Conversely, compared with an ultra-low-hydrolysis grade (05-88, hydrolysis 88 mol%, viscosity 5 mPa·s), 14-92(L) delivers a substantially higher wet tack: the loop tack on kraft paper (=ASTM D6195) reaches 4.2–5.8 N/25 mm versus 2.0–3.0 N/25 mm for 05-88 at 50% RH. The difference arises because the ~92 mol% hydrolysis level places the polymer close to the critical acetyl content where crystalline junction points can re-form during drying, providing cohesive strength without the brittleness of a fully hydrolyzed film.
    Comparative properties of four Wanwei PVOH grades in a standard adhesive formulation (12% aqueous solution, 2.5 phr glycerol)
    Property14-92(L)17-9920-9905-88
    Solution clarity (10%, 25 °C)ClearInsolubleInsolubleClear
    Solution preparation temperature20–25 °C85–95 °C85–95 °C20–25 °C
    Film tensile strength (=ISO 527-3)38–45 MPa55–68 MPa65–75 MPa20–28 MPa
    Elongation at break250–350%100–180%90–150%420–550%
    Loop tack, kraft paper (N/25 mm)4.2–5.8n/an/a2.0–3.0
    Cold-water resistance (re‑wetting time)8–15 s3–5 s
    Organic volatiles, residual (wt%)<0.8<0.5<0.5<1.2
    The practical implication for adhesive compounders is that 14-92(L) alone cannot meet the hot-water resistance demands of bottle-label adhesives requiring wash-off above 65 °C; those applications continue to rely on fully hydrolyzed grades crosslinked with glyoxal or zirconium salts. Published data indicates that blending 14-92(L) with 10–15% of a 99 mol% hydrolyzed grade increases the wet bond strength of paper-to-paper bonds under 40 °C water immersion by 35–50% while preserving room-temperature tack, but the optimum blend ratio is substrate-dependent and must be validated per TAPPI T812. In continuous emulsion polymerization of vinyl acetate, Wanwei PVA 14-92(L) serves as the primary protective colloid at addition levels of 4–8% based on monomer. The partially acetylated chain grafts with growing PVAc radicals to form a stable interfacial layer; the grafting efficiency, determined by solvent extraction and FT‑IR quantification of carbonyl absorption at 1735 cm⁻¹, typically reaches 35–45% under reactor conditions of 65–70 °C and a Rushton turbine impeller tip speed of 2.5–3.0 m/s. The resulting latex exhibits a particle size distribution with a D₅₀ of 0.8–1.5 µm and a coagulum level below 0.02% on a 40-mesh screen, significantly lower than the 0.1–0.3% coagulum observed when a fully hydrolyzed, non-grafting PVOH is used at the same concentration. Because residual acetyl groups reduce the Flory–Huggins interaction parameter with the acetate monomer, the colloid does not phase-separate during polymerization, even in the absence of added surfactant. One operational boundary must be respected: reactor pH must be maintained at 4.0–5.5; excursions above 6.0 initiate alkaline hydrolysis of the pendant acetyl groups, progressively converting the colloid toward a fully hydrolyzed analogue, which in turn destabilizes the latex and leads to a rapid increase in viscosity and grit formation.

    Blade Coating Rheology and Paper Surface Absorption

    In high-speed blade coaters operating at 800–1500 m/min, the pigment coating formulation containing 2.5–5.0 parts of 14-92(L) per hundred parts of kaolin or calcium carbonate exhibits a low-shear Brookfield viscosity of 800–1500 mPa·s (100 rpm, spindle #4) and a high-shear viscosity (10⁵ s⁻¹) of 45–70 mPa·s measured on a capillary viscometer per GB/T 12010.8. The partially hydrolyzed binder yields a water retention value of 85–110 g/m² under 2 atm pressure differential (TAPPI T701), which is 15–25% lower than that of fully hydrolyzed PVOH of comparable molecular weight. This reduced water holding capacity accelerates the setting rate on lightweight coated (LWC) papers but can provoke binder migration when the coat weight exceeds 12 g/m² per side; operators on pilot-scale Valmet Optiblade units have observed a mottling defect correlated with a drying rate exceeding 300 kg H₂O/m²·h, forcing a reduction in infrared dryer intensity from 80% to 55% of maximum power. Print gloss as tested by ISO 8254-1 (75° geometry) for a 7 g/m² coating improves by 4–6 points compared with a starch‑only binder, while the IGT pick resistance (ISO 3783) increases from 1.2 m/s to 2.5 m/s when 3 phr of 14-92(L) replaces an equal amount of oxidized starch—data validated across six production campaigns on a Vaahto coater at full width.

    When Warp Sizing Demands Rapid Desizing in Ambient Water

    Warp yarns sized with 14-92(L) on a Tsudakoma KS‑22 pre-wet sizing machine (size box temperature 40–45 °C, squeeze pressure 18 kN/m) attain a size add-on of 8–12% and yield a weaving efficiency of 94–97% for 40‑Ne cotton yarn on an air‑jet loom running at 750 rpm. The key differentiator from fully hydrolyzed 17-99 sizing is the desizing behavior: the 14-92(L) film re‑dissolves completely in a pad‑batch desizing bath at 30–35 °C within 10 minutes without enzymatic pretreatment, whereas 17-99 requires water at 80 °C plus a 0.5% wetting agent to achieve 90% removal in the same timeframe—conditions that can trigger thermal yellowing of optical brighteners on finished fabric. Residual size after a single wash is measured at 0.12–0.20% owf by the potassium dichromate oxidation method (GB/T 29865-2013), meeting the <0.3% threshold for subsequent reactive dyeing without dye-resist defects. This low‑temperature desizing capability is particularly valued in denim finishing lines where energy consumption per meter of fabric can be reduced by 1.2 MJ when switching from starch‑based or fully hydrolyzed PVOH sizes to 14-92(L). Storage in bulk silos requires conditioned air with a dew point below −10 °C to maintain the moisture content below 5.0 wt%; above this threshold the powder exhibits impaired flowability and can bridge in screw conveyors. Pre‑drying in a fluid‑bed dryer at 60 °C for 30 minutes is mandatory prior to melt processing, as residual moisture above 0.3% causes bubble formation and die‑lip build‑up during blown film extrusion through a 30:1 L/D single‑screw extruder with a melt temperature profile of 190–210 °C. Compatibility with common plasticizers such as glycerol and sorbitol is unremarkable, but mixing with amine‑terminated polyglycols or alkanolamines must be avoided because these nucleophilic species accelerate deacetylation at processing temperatures above 120 °C, leading to a shift in hydrolysis degree and unpredictable viscosity drift. The dust explosion risk, classified under St1 with KSt <200 bar·m/s and a minimum ignition energy of 10–30 mJ, necessitates explosion‑venting per NFPA 68 in pneumatic conveying lines.