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Anhui Liwei Chemical Co., Limited.

Wanwei PVA 13-88(L) (PVA 088-13)

    • Product Name: Wanwei PVA 13-88(L) (PVA 088-13)
    • 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 254393
    Product Name Wanwei PVA 13-88(L)
    Pva Type PVA 088-13
    Appearance White granular solid
    Degree Of Hydrolysis 88.0 ± 1.0 mol%
    Viscosity 4 Aqueous Solution 20 C 13.0 ± 1.0 mPa·s
    Ph 4 Aqueous Solution 5.0 - 7.0
    Ash Content ≤ 0.5%
    Volatile Content ≤ 5.0%
    Water Solubility Soluble in water
    Average Degree Of Polymerization ~1300
    Melting Point 220 - 230°C

    As an accredited Wanwei PVA 13-88(L) (PVA 088-13) factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Supplied as 25 kg multi-walled paper bags with polyethylene liner, ensuring moisture protection and safe handling.
    Container Loading (20′ FCL) 20′ FCL container loading of Wanwei PVA 13-88(L) in sealed bags, palletized, secured, and protected from moisture for safe transport.
    Shipping Wanwei PVA 13-88(L) ships as a non-hazardous, water-soluble powder or granule. Pack in sealed multi-layer bags or FIBCs, protected from moisture and humidity. Store dry, away from heat sources. No special transport restrictions apply, but keep containers intact to prevent caking or spillage during handling.
    Storage Store Wanwei PVA 13-88(L) in a cool, dry, well-ventilated area, away from direct sunlight, heat sources, and oxidizers. Keep containers tightly sealed to prevent moisture absorption and dust formation. Maintain stable room temperature, avoid stacking heavy loads, and follow local regulations for polymer storage.
    Shelf Life Shelf life: 2 years under dry, cool, sealed conditions; avoid moisture and direct sunlight for stability.
    Application of Wanwei PVA 13-88(L) (PVA 088-13)

    POLYVINYL ACETATE AND VINYL ACETATE-ETHYLENE EMULSION POLYMERIZATION

    In the semi-continuous stirred-tank reactor typical of industrial vinyl acetate-ethylene (VAE) and polyvinyl acetate (PVAc) latex production, the partial hydrolysis profile of PVA 088-13—a medium-viscosity grade with a saponification degree tightly controlled between 87 and 89 mol%—determines the balance between electrosteric stabilization and grafting efficiency onto the forming polymer particle. The polymerization is conducted at 55–85 °C under ethylene partial pressures of 1.5–4.0 MPa, with a jacket-cooled 10–25 m³ stainless steel autoclave fitted with a dual-impeller agitator running at tip speeds below 3.5 m/s to limit shear-induced coagulation. PVA 088-13 is employed at 2–8 wt% on total monomer, pre-dissolved in deionized water at 20–25 °C using a high-turbulence eductor to avoid undissolved microgel particles that would otherwise nucleate grit; heating the aqueous PVA solution above 80 °C during preparation of the initial charge frequently leads to the formation of insoluble agglomerates that pass through the 150 µm guard filters and appear as speck contamination in the finished adhesive. In VAE systems where residual vinyl acetate monomer is stripped to below 500 ppm via a countercurrent steam stripping column, the protective colloid contributes to a latex with a minimum film-forming temperature (MFFT) adjustable between 0 °C and 15 °C, a viscosity profile in the range of 500–4,000 mPa·s (Brookfield RV, spindle #4, 20 rpm), and a surface tension of 46–52 mN/m. These emulsions are compliant with FDA 21 CFR 175.105 for indirect food-contact adhesives and with GB/T 27573-2011 for VAE copolymer dispersions used in woodworking and lamination; specific migration testing according to EU Regulation 10/2011 may be required when the latex is applied in food-packaging laminates. Finished products include single-component wood assembly adhesives, high-solids laminating adhesives for flexible packaging, nonwoven binder dispersions for wipe substrates, and joint compound modifiers; in each, the 088-13-stabilized latex delivers a cohesive strength-to-elongation ratio that resists bond creep at service temperatures up to 60 °C, a property directly correlated with the degree of PVA grafting measured by acetone extraction of the dried film.

    How Does Spray-Drying Atomization Energy Influence Redispersibility of 088-13 Stabilized Powders?

    The conversion of PVA 088-13-stabilized VAE latex into a free-flowing, redispersible polymer powder for dry-mix mortar formulations introduces a critical processing window within the spray-drying tower that directly governs the rehydration behavior of the powder when mixed with cementitious binders at the construction site. The parent latex, typically containing 50–55 wt% solids and a PVA 088-13 protective colloid loading of 6–12% based on polymer solids, is diluted to 40% solids and pumped at 2.0–3.5 MPa through a rotary atomizer wheel (peripheral speed 140–180 m/s) or a high-pressure single-fluid nozzle into a co-current drying chamber where the inlet air temperature is maintained at 160–185 °C and the outlet temperature at 75–90 °C. Excessive inlet temperature—excursions beyond 195 °C—dehydrates the polyvinyl alcohol shell to the extent that carbonyl and ether crosslinks form irreversibly, rendering the powder partially insoluble and causing a loss of redispersibility detectable as an increase in the screen residue on a 150 µm sieve from the specification limit of <1.0% to >4.5%. Addition of 8–15 wt% of a mineral antiblocking agent (typically kaolin or precipitated calcium carbonate with a mean particle diameter 1–3 µm) is metered into the cyclone separation stream to prevent cold-blocking during storage at ambient temperatures above 28 °C. The resulting powder must comply with JC/T 2189-2013 and EN 12004:2017, the latter specifying tensile adhesion strength on concrete after water immersion and heat ageing: with a polymer-to-cement ratio of 0.05, the material is expected to achieve adhesion values exceeding 0.5 MPa under standard conditioning and not less than 0.3 MPa after 21 days water storage in a ceramic tile adhesive formulation based on ordinary Portland cement CEM I 42.5. The powder is incorporated into self-levelling underlayments, external thermal insulation composite systems (ETICS) base coats, and flexible tile adhesives classified as C2S1 or C2S2. A well-documented limitation: in cement-rich repair mortars with a polymer/cement ratio below 0.03, the redispersed PVA 088-13 film exhibits insufficient coalescence at low curing temperatures (<8 °C), leading to a discontinuous polymer phase and a marked decline in flexural strength after 28 days wet storage when compared with fully hydrolyzed protective colloids.

    Typical tensile adhesion strength of 088-13 redispersible powder in a C2 tile adhesive (substrate: concrete slab, loading rate 250 N/min)
    Polymer/cement ratio (wt)Adhesion after 28 d standard cure (MPa)Adhesion after water immersion (MPa)Adhesion after heat ageing (MPa)
    0.030.7 ± 0.10.4 ± 0.10.5 ± 0.1
    0.051.1 ± 0.20.7 ± 0.10.8 ± 0.1
    0.081.4 ± 0.21.0 ± 0.21.2 ± 0.2

    WARP SIZING ON HIGH-SPEED SHUTTLELESS WEAVING MACHINES

    On a modern single-end sizing machine running 40s–80s Ne cotton or polyester/cotton blended yarns at creep speeds of 300–600 m/min, the size formulation in the cooking kettle is brought to 95–98°C and held for 45–60 min under mechanical agitation to ensure complete dissolution of PVA 088-13 granules before blending with oxidized starch (typically 1:1 to 1:3 PVA-to-starch dry weight ratio) and acrylic copolymer size in a total solids concentration of 10–14%. The PVA 088-13 fraction within the solids commonly ranges from 25% to 50%, with the higher boundary required for fine-count yarns and high loom speeds above 800 picks/min where the shed geometry imposes severe cyclical abrasion forces. The size bath temperature in the double-dip sizing trough is maintained at 88–92°C because the partial-acetyl-group content of 088-13 depresses the cloud point sufficiently that a temperature drop to below 80°C initiates surface skinning and a viscosity drift that produces uneven add-on. After squeeze-roll expression at a nip pressure of 1.8–3.0 kN/cm, the sized yarn is dried over a multi-cylinder dryer array with a progressive temperature profile from 105°C (first cans) to 130°C (final cans), and the residual moisture is brought to 7–8% to preserve elongation-at-break. The sized warp is woven on air-jet or rapier looms into greige fabrics destined for denim bottomweights, poplin shirting, and home-textile bed linens. Through the scouring and desizing process, the water solubility of 088-13 in cold water (20°C) allows enzymatic or oxidative desizing to reduce residual PVA on fabric to below 0.1% owf, meeting the discharge requirements of Oeko-Tex Standard 100 Annex 4 for baby-wear articles. The principal process vulnerability: when ambient relative humidity in the weaving shed consistently exceeds 75%, the sized yarn absorbs moisture, the film swells, and the PVA phase undergoes plasticization that raises the coefficient of friction at the metal-to-yarn contact points, resulting in a spike in end-breakage rate that is most pronounced on air-jet looms with high insertion frequency.

    When Seal Integrity Depends on Vicat Softening Point: Water-Soluble Film from PVA 088-13

    The fabrication of water-soluble unit-dose packaging for laundry detergents and automatic dishwashing products demands a film with a dissolution profile that is neither so fast that the sachet disintegrates in high-humidity warehouse storage nor so slow that residue remains at the end of a cold-water wash cycle; PVA 088-13, formulated with 18–25 parts of glycerin or sorbitol per hundred parts of resin, yields a film with a Vicat softening temperature of approximately 42–48°C and a disintegration time at 10°C of 45–70 seconds when tested according to the protocol for soluble packaging in EU Regulation (EC) No 648/2004 on detergents, Annex VII. The film is produced predominantly via solution casting onto a polished stainless steel belt running at 3–6 m/min, employing a 20–30 wt% aqueous PVA solution that has been deaerated under vacuum (−0.08 MPa) and applied through a precision slot die with a wet-film thickness setpoint of 400–800 µm; melt extrusion, while feasible with sufficient plasticizer, is generally avoided because the narrow melt-processing window for 088-13 (onset of thermal decomposition at approximately 180°C versus a melting point of 160–170°C) demands a tightly controlled twin-screw extrusion profile with L/D > 40 and barrel zones held within a ±2°C band. After drying in a multi-zone tunnel oven with air temperatures ramping from 70°C to 110°C, the continuous film is conditioned to 9–12% moisture and slit into rolls. Finished articles include laundry detergent pods, automatic dishwasher tablets enclosed in PVA film, agrochemical water-soluble pouches, and embroidery backing films; for the detergent sector, the film must pass the OECD 301B ready-biodegradability test and comply with EU 10/2011 migration limits if contact with food-contact surfaces is plausible in the consumer home. An explicit operational boundary: PVA 088-13 film is incompatible with liquid formulations containing free amines or ammonia at concentrations above 0.5%, which catalyze ester-group hydrolysis and cause progressive embrittlement of the seal area visible as micro-crazing under 20× magnification within 72 hours of filling at 40°C accelerated storage.

    What Determines Cobb60 Values in Size Press Applications Using 088-13 Blends?

    The incorporation of PVA 088-13 into surface size formulations for bleached board and fine paper grades targets surface strength and resistance to water penetration, expressed as the Cobb60 value measured per ISO 535:2014. At the film-transfer size press of a Voith SpeedSizer or an OptiSizer running at a web speed of 900–1,400 m/min, the starch-based size solution is enriched with PVA 088-13 at a dry addition rate of 0.5–2.0 g/m² per side, corresponding to a PVA concentration of 3–8 wt% in the size-press bath (total solids 12–18%, temperature 55–65°C). The partial hydrolysis of 088-13 creates a continuous film that bridges surface fibers and reduces the tendency for fiber picking during offset printing; the resulting sheet shows an IGT dry pick resistance increase of 1.5–2.5 m/s over neat oxidized starch alone, while the Cobb60 value typically falls from 100 g/m² (starch only) to 35–55 g/m² for a paperboard grade intended for frozen-food packaging, depending on the wet-end balance of alkenyl succinic anhydride internal sizing. Compliance for direct food contact grades is governed by FDA 21 CFR 176.170 and 176.180 for fatty and aqueous food types, with extractives testing per EN 645 and EN 1541. End products include folding carton board, coated duplex board for detergent boxes, and archival-grade text paper. A processing constraint encountered in mills with closed water circuits: the return of broke containing PVA 088-13 to the wet-end stock preparation system raises the anionic trash level and interferes with retention aid chemistry; at broke usage rates exceeding 15% of total fibre furnish, the system may require supplementary fixing agents and an adjustment of the zeta potential to maintain first-pass ash retention above 60%.

    Surface size formulation effect on linerboard Cobb60 and IGT pick resistance (PVA 088-13:oxidized starch dry blend)
    PVA fraction in size blend (wt%)Size pickup total (g/m²/side)Cobb60 (g/m²)IGT dry pick (m/s)
    0 (starch reference)1.5982.1
    201.5623.2
    401.5463.9
    601.5334.3

    Film Formation and Removal Dynamics in Leave-on Cosmetic Masks: pH, Film Modulus, and User Safety

    The utility of PVA 088-13 as a film-former in peel-off cosmetic masks arises from its ability to generate a continuous, flexible film at room temperature upon dehydration, with a film modulus that can be tuned between 80 and 200 MPa by adjusting the plasticizer blend. A typical cold-process formulation dispenses PVA 088-13 at 12–18 wt% into deionized water preswollen at 25°C, then raises the temperature to 85°C under low-shear paddle mixing until a clear, bubble-free mucilage is obtained; after cooling below 40°C, 5–10 wt% of humectants (glycerin, butylene glycol), 1–3 wt% of polyvinylpyrrolidone as a co-film-former, and 0.3–0.8 wt% of a phenoxyethanol-caprylyl glycol preservative system are incorporated. The finished mask composition, filled into multi-laminate tubes or sachets, must pass a challenge test conducted according to ISO 11930:2019 and comply fully with the safety assessment requirements of EU Cosmetics Regulation (EC) No 1223/2009, Annex I, including a margin of safety calculation for dermal absorption of any residual vinyl acetate monomer kept below the 1 ppm trace level achievable by the resin manufacturing process. The product is applied at a wet thickness of 0.5–1.0 mm and dries within 20–30 minutes to a film that is stripped off manually; the removal force, measured on a texture analyzer equipped with a 90° peel fixture, should fall between 0.8 and 1.5 N/cm to balance user comfort with effective cohesion. A documented boundary condition for dermo-cosmetic safety: the water-vapor transmission rate (WVTR) of a neat PVA 088-13 film cast from aqueous solution at 10 mil dry thickness is approximately 120–180 g/(m²·24 h) measured at 38°C/90% RH per ASTM E96, a value sufficiently low that prolonged occlusion of skin areas prone to folliculitis can create a microenvironment favorable to malassezia overgrowth; many formulators therefore limit the concentration of 088-13 to below 15% in products intended for facial leave-on application and incorporate a polyol at a minimum 1:0.4 PVA-to-plasticizer ratio to reduce film rigidity without compromising the clean peel character.

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    Certification & Compliance
    More Introduction

    A technical designation of PVA 13-88(L), also coded as PVA 088-13, identifies a partially hydrolyzed polyvinyl alcohol resin manufactured by Anhui Wanwei Updated High-Tech Material Co., Ltd. The numeric suffix 13-88 encodes two fundamental molecular parameters critical to process behavior: a degree of polymerization of approximately 1300 and an alcoholysis degree of 88 ± 1 mol%. The appended (L) variant indicates a low-methanol, low-ash refinement path achieved through a post-saponification washing regime, reducing residual sodium acetate content below 1.0% by mass as determined by ISO 15023-2:2019 titration methodology. Viscosity of a 4% aqueous solution at 20°C ranges from 20.0 to 26.0 mPa·s measured on a Brookfield LV viscometer, spindle No. 1 at 30 rpm, placing this grade squarely in the medium-viscosity partial-hydrolysis segment suitable for temporary sizing films that require cold-water solubility without sacrificing film strength.

    When comparing this grade against fully hydrolyzed homologues such as Wanwei PVA 17-99 or PVA 05-100, the 88 mol% residual acetate content disrupts intra- and inter-chain hydrogen bonding sufficiently to depress aqueous solution gelling temperature below 35°C and enables complete dissolution in water at 15–25°C without thermal jacketing. The trade-off manifests as a lower tensile strength of the conditioned film—specimens conditioned at 23°C and 50% RH per ASTM D882-18 yield an ultimate tensile stress of 44–52 MPa, versus 60–70 MPa for the fully hydrolyzed PVA 17-99. Elongation at break, however, rises to 180–240%, offering a compliance advantage in flexible substrate sizing where brittle fracture during weaving loom take-up is a documented failure mode.

    What Distinguishes the (L) Post-Treatment from Standard 13-88

    The standard PVA 13-88 grade typically carries a sodium acetate residue of 1.2–2.0%, a consequence of methyl acetate by-product neutralization with sodium hydroxide during alcoholysis. In hot-water-based warp sizing formulations, this alkali content can elevate pH of the size bath to 7.5–8.5, promoting oxidative yellowing of cotton warps under continuous drying cylinder contact at 120–140°C. The (L) variant, processed through a cascade countercurrent washing and membrane-assisted methanol recovery system, achieves sodium acetate below 0.7% and pH of a 4% solution within 5.5–7.0. This shift eliminates the requirement for acetic acid buffer addition previously necessary to stabilize color-sensitive viscose staple fibers during sizing, a process bottleneck well-documented on Karl Mayer sectional warping lines operating at speeds exceeding 800 m/min.

    Ash content determined by ignition at 800°C per ISO 3451-1:2019 is held to 0.1% maximum for the 13-88(L), whereas the standard grade routinely reaches 0.3%. For paper surface sizing applications where PVA is co-mixed with oxidized starch and optical brightening agents, elevated ash contributes to insoluble residue deposition on film-press metering rolls, shortening roll regrind intervals from 12 months to as little as 7 months on Voith SpeedSizer units run at 1200–1500 m/min.

    When Processing Temperatures Exceed 80°C in Aqueous Preparation

    Dissolution protocol for PVA 13-88(L) demands active attention to temperature ramp rates. Although its partial hydrolysis permits cold-water swellability, practical tank mixing in textile mills employs a water pre-charge at 25–35°C under propeller agitation at 400–600 rpm, followed by indirect steam injection to raise temperature to 85–90°C over 30–40 minutes. Holding temperature at 90°C for 60 minutes under continuous agitation eliminates micro-gel “fish eyes” that originate from incomplete particle hydration. Thermal exposure beyond 95°C for intervals exceeding 2 hours initiates a gradual deacetylation side reaction, shifting the hydrolysis degree upward and irreversibly increasing the gelling tendency upon cooling to size box application temperatures of 70–75°C. This thermal history effect is measurable as a viscosity drift of +2 to +4 mPa·s in re-cooled solution and correlates with an increased incidence of size skin formation on prewetting rollers of Benninger Sizecoat units.

    A deep-dive processing conflict emerges when 13-88(L) is incorporated into blends with acrylate-based sizing copolymers for zero-twist polyester filament yarns. Acrylate latexes frequently require neutralization with ammonia to pH 8.0–9.0. The combination of residual polyvinyl acetate segments in 13-88(L) and elevated pH above 8.5 at 80°C leads to a saponification-driven viscosity plateau within 45 minutes of blending, as monitored on a Brookfield DV3T with small sample adapter. Operators on single-end sizing equipment for carbon fiber precursor yarn witness a sudden loss of fluidity: measured consistency rises from an initial 30 mPa·s to beyond 120 mPa·s, triggering low-pressure alarms on diaphragm pumps preset to 0.4 MPa. Mitigation demands either pre-buffering the PVA solution to pH 6.0–6.5 with dilute phosphoric acid or selecting an acrylate grade stabilized with non-ionic emulsifier systems free of amino functionality.

    Volatile matter content at delivery, measured by drying at 105°C to constant mass per ISO 15512:2019, is specified below 5.0%. In geographic regions with ambient relative humidity persistently above 65%, the powder absorbs atmospheric moisture during pneumatic conveying to day silos on Suzuka-type sizing equipment, raising surface moisture to 7–8%. This increment causes bridging in gravimetric loss-in-weight feeders and a drift of −1.5% in as-fed solids basis per batch. Pre-conditioning of ambient air to a dew point of −5°C in the conveying loop is recommended for continuous operations targeting ±0.5% size add-on.

    Adhesion performance to cotton cellulose fibers, as derived from standard single-yarn pull-out tests modeled on ASTM D2256-21 principles, shows lateral shear adhesion values of 8.2–9.5 cN/tex after conditioning at 65% RH. When compared to PVA 17-88, which possesses a higher DP of 1700 and identical hydrolysis, the 13-88(L) exhibits 12–15% lower adhesion but 20% faster desizing removal. Desizing efficiency, quantified by residual PVA on fabric via iodine complexation spectrophotometry at 690 nm after an amylase oxidative desize stage, reaches 99.2% removal within 90 seconds of hot water spray at 95°C. Split grades with DP around 1000 (e.g., PVA 10-88) remove even faster but generate lower loom efficiency due to a loss of film flexibility under high-velocity shuttleless weaving impact cycles, as recorded on Tsudakoma ZAX9100 air-jet looms with weft insertion rates of 2200 m/min.

    A Comparative Specification Matrix

    ParameterWanwei PVA 13-88(L)Wanwei PVA 13-88 (Standard)Wanwei PVA 17-88Test Method
    Alcoholysis degree88 ± 1 mol%88 ± 1 mol%88 ± 1 mol%ISO 15023-2:2019
    Viscosity (4%, 20°C)20.0–26.0 mPa·s20.0–26.0 mPa·s28.0–34.0 mPa·sBrookfield LV, Sp1, 30rpm
    Degree of polymerization~1300~1300~1700Calculated from viscosity
    Sodium acetate content≤0.7%≤2.0%≤1.5%ISO 15023-2:2019
    Ash (800°C)≤0.1%≤0.3%≤0.3%ISO 3451-1:2019
    Volatile matter (105°C)≤5.0%≤5.0%≤5.0%ISO 15512:2019
    pH (4% solution)5.5–7.06.0–8.56.0–8.0ISO 1148:1980
    Film tensile strength (50% RH)44–52 MPa42–50 MPa48–56 MPaASTM D882-18
    Elongation at break180–240%180–240%210–270%ASTM D882-18

    In emulsion polymerization, 13-88(L) functions as a protective colloid for vinyl acetate homopolymer and ethylene-vinyl acetate copolymer dispersions. The low residual acetate and sodium content minimize interference with persulfate initiator decomposition kinetics, maintaining a polymerization onset temperature of 68–72°C without the induction period extension observed with standard PVA grades carrying 1.5% sodium acetate. A bench-scale reactor trial of 1.5 L working volume with VAc monomer at 50% solids loading, initiated with 0.3% ammonium persulfate on monomer mass, recorded an exothermic peak at 21 minutes for 13-88(L) versus 27 minutes for standard 13-88. Particle size distribution measured by laser diffraction shifted only marginally: mean particle size 0.82 μm with a span of 0.91, acceptable for wood adhesive applications meeting EN 204 D3 classification.

    Yet a limitation exists: when this PVA grade is deployed in PVAc emulsion systems destined for crosslinking via metal salt complexation (e.g., aluminum chloride or zirconium ammonium carbonate additions at 0.1–0.3% on total mass), the low pH buffer capacity results in a rapid pH drop below 4.0 upon salt addition. This drop triggers localized coagulation visible as micro-grit on 200-mesh screen retention, increasing filtered residue from 0.02% to 0.15%. The use of 13-88(L) in such formulations requires a buffer pre-treatment with sodium bicarbonate at 0.05–0.1% to stabilize pH above 5.5.

    For paper surface sizing on lightweight coated grades (LWC), 13-88(L) is metered at a dose of 0.3–0.8 parts per hundred dry fiber, combined with a styrene-acrylate surface sizing agent. Pigment binder migration, evaluated via cross-section SEM with backscattered electron imaging on a Hitachi SU3500 system, reveals that the low molecular weight fraction (extracted via 24-hour Soxhlet with water) of 13-88(L) penetrates to a depth of 18–25 μm, sufficiently deep to anchor coating layers without causing print mottle. A comparison with PVA 05-88 (DP ~500) shows that the lower DP grade penetrates excessively beyond 35 μm, reducing IGT pick strength by 15% in off-line testing per ISO 3783:2015.

    Compliance and Food Contact Status

    Migratory constraints demand precise documentation. PVA 13-88(L) meets the compositional requirements of FDA 21 CFR § 176.170 for components of paper and paperboard in contact with aqueous and fatty foods, as well as § 175.105 for adhesives. Heavy metal content, determined by ICP-OES after microwave-assisted acid digestion, registers below detection limits for lead (<2 mg/kg), cadmium (<0.5 mg/kg), mercury (<0.1 mg/kg), and hexavalent chromium (<1 mg/kg). Monomer residual vinyl acetate is below 5 mg/kg by headspace GC-MS per EN 13628-1:2002. These values align with EU Regulation EC 1935/2004 and the Plastics Implementation Measure EU 10/2011, specific migration limit for vinyl acetate being 12 mg/kg food simulant.

    Industrial hygiene monitoring during powder handling of 13-88(L) has documented dust levels of 1.2–2.8 mg/m³ for total inhalable dust during manual bag dumping into a hopper with local exhaust ventilation of 0.5 m/s capture velocity. This falls within the 3 mg/m³ 8-hour TWA for particles not otherwise classified under OSHA 29 CFR 1910.1000. Nevertheless, operators are advised that prolonged exposure to airborne PVA dust can cause minor mucous membrane irritation; respirator selection guidance recommends an N95 filtering facepiece (assigned protection factor 10) for repeat bag-breaking operations exceeding 30 minutes per shift.

    Fiber warp sizing remains the largest volume application. A mill trial conducted on a Karl Mayer SMR-800 sizing machine processing Ne 40/1 cotton warp yarn, 7200 ends, with size pick-up targeted at 12.5%, recorded a weaving efficiency of 94.3% on a Picanol Omniplus-800 air-jet loom at 650 rip insertions per minute. Sizing formulation comprised 85 kg 13-88(L), 10 kg maize cationic starch (DS 0.03–0.05), 3.5 kg acrylic sizing agent (solids 25%), and 1.5 kg textile wax emulsion per 800 L water. Desizing was completed in a single wash box at 90°C with 1.5 g/L amylase, 0.5 g/L non-ionic wetting agent, achieving a Tegewa violet scale rating of 7–8 (complete removal). This is contrasted with earlier runs on standard 13-88 that required a two-box desize train to reach the same rating, attributable to calcium soap deposits from sodium acetate residues binding the PVA film to the cellulose.

    Storage stability in sealed, moisture-proof bags at 25°C and below 60% RH exceeds 24 months without measurable change in viscosity or dissolution rate. If bags are opened and re-sealed in high-humidity environments, plasticization by sorbed moisture can promote cold-flow and caking within 3 weeks, requiring a powder flowability assessment via Schulze ring shear tester. Critical consolidation stress at 5 kPa pre-shear for fresh powder measures 2.1 kPa unconfined yield strength; after 3 weeks at 75% RH, this rises to 4.8 kPa, indicating cohesive arching potential in silos with outlet diameters below 0.6 m.