| 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 | 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. |
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.
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.
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 type | 4% 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%) | 16 | 55.2 | 3200 | <0.05 | 4 |
| PVA 15-79 (hydrolysis 79 mol%) | 15 | 54.8 | 4800 | 0.12 | 2 |
| PVA 17-88 (hydrolysis 88 mol%) | 23 | 54.5 | 7400 | 0.08 | 3 |
| PVA 14-98 (hydrolysis 98 mol%) | 18 | 53.9 | 11000 | <0.02 | 1 |
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.
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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| Property | 14-92(L) | 17-99 | 20-99 | 05-88 |
|---|---|---|---|---|
| Solution clarity (10%, 25 °C) | Clear | Insoluble | Insoluble | Clear |
| Solution preparation temperature | 20–25 °C | 85–95 °C | 85–95 °C | 20–25 °C |
| Film tensile strength (=ISO 527-3) | 38–45 MPa | 55–68 MPa | 65–75 MPa | 20–28 MPa |
| Elongation at break | 250–350% | 100–180% | 90–150% | 420–550% |
| Loop tack, kraft paper (N/25 mm) | 4.2–5.8 | n/a | n/a | 2.0–3.0 |
| Cold-water resistance (re‑wetting time) | 8–15 s | — | — | 3–5 s |
| Organic volatiles, residual (wt%) | <0.8 | <0.5 | <0.5 | <1.2 |