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Anhui Liwei Chemical Co., Limited.

Kuraray VPB053-PVA Structural Fiber for Paper Making

    • Product Name: Kuraray VPB053-PVA Structural Fiber for Paper Making
    • 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 675226
    Material Polyvinyl alcohol (PVA)
    Fiber Length 3–5 mm cut length for papermaking
    Specific Gravity 1.26
    Tensile Strength 1200 MPa
    Youngs Modulus 30 GPa
    Elongation At Break 8%
    Melting Point 230 °C
    Moisture Regain ~1% at 20 °C and 65% RH
    Fibrillation Behavior Fibrillates under mechanical beating to form branched microfibers
    Alkali Resistance Excellent; stable in concentrated alkali solutions

    As an accredited Kuraray VPB053-PVA Structural Fiber for Paper Making factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Kuraray VPB053-PVA Structural Fiber for Paper Making is supplied in 20 kg sealed, moisture-proof polyethylene-lined woven bags.
    Container Loading (20′ FCL) 20′ FCL loaded with palletized cartons of Kuraray VPB053-PVA structural fiber, securely stowed and protected for paper-making use.
    Shipping Kuraray VPB053-PVA Structural Fiber ships in dry, sealed packaging to prevent moisture absorption. Standard ground or freight transport is suitable; avoid excessive compression and exposure to rain. Store in a cool, dry warehouse and handle with clean gloves. No special hazmat classification is typically required for this non-hazardous fiber.
    Storage Store Kuraray VPB053-PVA structural fiber in a cool, dry, well-ventilated area away from direct sunlight, heat sources, and open flames. Keep the original packaging tightly sealed to prevent moisture absorption and contamination. Avoid exposure to excessive humidity and static electricity. Maintain good housekeeping to minimize dust accumulation. Use proper storage temperatures and follow manufacturer recommendations for shelf life.
    Shelf Life Kuraray VPB053-PVA structural fiber has a typical shelf life of two years when stored dry in original packaging.
    Application of Kuraray VPB053-PVA Structural Fiber for Paper Making

    Automotive engine intake and fuel filtration media produced with Kuraray VPB053-PVA structural fiber are designed to reconcile two opposing sheet requirements: high enough wet-web tensile to survive inclined-wire dewatering at commercial speed, and low enough air resistance after resin stiffening to keep engine parasitic load within the original equipment calibration band. The fibre is introduced at 8–18 wt% of total oven-dry furnish, with the remainder composed of a softwood kraft base refined to 20–35°SR, a dissolving or mercerized pulp portion for chemical uniformity, and a polyester or bicomponent staple fraction where fully synthetic filter grades are specified. Stock preparation is sequenced so VPB053 is added after the main refining step to avoid excessive axial cutting; the furnish is diluted to 0.08–0.18% headbox consistency and treated with a high-molecular-weight polyacrylamide retention aid at 0.01–0.03% dry pulp equivalent. Formation occurs on an inclined wire or Rotoformer with low-vacuum wet boxes in the first 30–50% of the forming length. The wet sheet enters a multicylinder dryer where surface temperatures reach 130–160°C; under breaker-stack nip pressure and residual moisture, PVA fibre surfaces plasticize and consolidate at crossings with cellulose, producing a bond that is not melt-derived because PVA degrades before reaching a stable melt state. Post-impregnation uses a low-phenol phenolic or acrylic binder at 15–25% dry resin pickup to develop crush resistance and pleat lock. The operational boundary with highest batch-to-batch variance is dry-end static accumulation when relative humidity falls below 35%, causing PVA fibre clumping in the trim return and visible basis-weight bands across the reel. Compliance is anchored to ISO 19438 for fuel filter particle retention and pressure drop, ISO 5011 for engine air cleaner capacity, ISO 4548-12 for lubricating-oil filter burst and cyclic fatigue, plus sheet-level methods ISO 1924-2, ISO 5636-3, ISO 535, and ISO 2144 for tensile, permeance, Cobb, and ash. Terminal finished product types include pleated fuel cartridges for gasoline direct-injection and common-rail diesel systems, coalescing filter elements for fuel-water separation, and high-collapse oil filter elements where end-cap bonding must survive 1.0 MPa burst pressure.

    StandardMetricTypical mill verification boundary
    ISO 19438Fuel filter contaminant capacity and differential pressureElement-level test at rated flow and 4–7 µm retention
    ISO 5011Engine air cleaner gravimetric capacity and efficiencyFull element test at rated air flow
    ISO 4548-12Oil filter static burst and cyclic fatigueBurst threshold not less than 1.0 MPa
    ISO 1924-2Tensile index and elongationMachine and cross direction after resin cure
    ISO 5636-3Bendtsen air permeancePre-pleat sheet permeability window
    ISO 535Cobb water absorptivenessVerification of resin holdout
    ISO 2144Ash contentResidual ash after ignition at 900 °C

    What Mechanism Governs Fibril Consolidation When VPB053 Is Co-Refined with Fibrillated Lyocell in Separator Base Stock?

    Battery separator base stock wet-laid with VPB053 and fibrillated lyocell depends on a dual-network mechanism: the cellulose fibrillation provides hydrogen-bonded surface area that controls pore size, while VPB053 contributes wet dimensional stability and preserves open structure during high-temperature calendering. Formulation addition is set at 12–25 wt% on total fiber, with lyocell refined to 30–60°SR and, in high-safety traction cell grades, a silane-sized microglass or ceramic whisker fraction at 5–15 wt%. Refining of VPB053 must be conducted at low specific edge load below 0.5 J/m; higher energy inputs truncate the fiber and increase fines, which collapses the pore network under subsequent calendering. The furnish approaches the former at 0.05–0.12% consistency, dewatering through a high-vacuum flatbox system before a dryer profile capped at 130°C. Hot calendering is the critical control point: linear pressures from 50–120 kN/m compact PVA-cellulose crossing zones while leaving the interstitial lyocell network open enough to meet Gurley air resistance targets of 300–1500 s/100 mL at 20–40 µm sheet thickness. When VPB053 addition exceeds 25 wt%, online capacitance profile scanners consistently identify hard spots with local Gurley values above 5000 s/100 mL; these defects generate coating-bar vibration above 600 m/min on ceramic slurry lines and are generally traced to PVA-rich flocs formed in the fan pump loop. Compliance references include IEC 62660-3 for secondary lithium-ion cell abuse tolerance, ISO 5636-3 for permeance, ISO 1924-2 for tensile index, ISO 534 for thickness, ISO 2144 for ash after 900 °C, and ISO 6588-1 for aqueous extract pH. Terminal finished product types include lithium-ion separator base for automotive traction cells, capacitor separator paper, and nickel-metal hydride battery separator substrates where residual ash must remain below 1.0 wt% after ignition.

    StandardParameterSeparator base stock acceptance boundary
    IEC 62660-3Secondary lithium-ion cell mechanical and thermal abuseCell-level validation for traction applications
    ISO 5636-3Bendtsen air permeancePre-calendered sheet permeability range
    ISO 1924-2Tensile index and elongationMachine direction after wet press
    ISO 534Thickness and apparent density20–40 µm after hot calendering
    ISO 2144Ash contentBelow 1.0 wt% after 900 °C
    ISO 6588-1Aqueous extract pHCompatibility with lithium salt electrolyte

    Food-contact heat-sealable base paper for single-serve tea and coffee bags uses VPB053 at 5–15 wt% of total fibre to raise wet-openability and seal integrity without increasing basis weight. The furnish includes abaca and bleached hardwood kraft with VPB053 added post-refining to preserve fibre length; stock consistency is controlled at 1.8–3.5% before dilution. On an inclined wire machine running at 80–120 m/min, the sheet is formed with a target moisture after the press section of 55–65% and dried to 4–8% final moisture. Because PVA does not hornify on drying, the sheet retains a higher wet-flexibility index than a comparable all-cellulose sheet, a property that reduces bag rupture during automated over-wrapping. A corona discharge unit treats the top side before a heat-sealable dispersion or extrusion coating is applied at 2–4 g/m². On the converter, vertical form-fill-seal machines operate with seal-jaw temperatures of 150–200°C and dwell times of 0.1–0.3 s; the PVA network limits seal strike-through by maintaining surface density under heat. Compliance is based on FDA 21 CFR 176.170 for paper and paperboard in direct contact with aqueous and fatty foods, EU Regulation 1935/2004, BfR Recommendation XXXVI, and mechanical verification through ISO 1924-2 and ISO 535. Terminal finished products include single-chamber tea bags, pyramid coffee filter pouches, and herbal infusion sachets where seal-peel force is maintained at 0.8–1.5 N/15 mm after immersion in boiling water.

    When Maximum Pleat Rigidity Is Required in Gas Turbine Intake Filter Media

    Gas turbine inlet and high-efficiency HVAC filter media incorporating VPB053 are configured for static-pleat designs in which bending stiffness and low pressure drop are simultaneous requirements. VPB053 addition is set at 15–30 wt% of total fiber, with the balance comprising glass fiber, roughened polyester staple, and flame-retardant viscose or cellulosic pulp. Low-shear mixing at 1.0–2.0% consistency is used with a nonionic defoamer at 0.02–0.05% on fiber weight to prevent rope formation and white-water foam. The sheet forms on an inclined wire with vacuum-assisted dewatering at 20–60 kPa differential; wet-web solids entering the dryer are typically 35–45%. The primary process boundary occurs in the after-dryer section: sheet temperatures above 180°C induce visible yellowing and reduce tensile energy absorption in the PVA network, so the dryer profile is capped at 160°C with final moisture below 2.5%. Pleating is performed on rotary pleaters with back tension of 60–120 N/m; insufficient tension results in irregular pleat heights and reduces filter pack integrity under compressor surge conditions. Compliance references include ISO 16890-1 for particulate matter efficiency classification, EN 779 for legacy filter class reporting, ISO 5636-3 for permeance, ISO 1924-2 for tensile stiffness, and ISO 535 for water absorption. Terminal finished products include static pleated panels for gas turbine inlet houses, compact pleated HVAC filters, and industrial dust collector cartridge media in basis weights from 80–140 g/m².

    Mechanical Reinforcement in Abrasive Backing and Disc Base Paper

    Coated abrasive backing and fibre disc base papers require cross-direction tear resistance, controlled elongation at break, and uniform saturant absorption for resin anchor coats. VPB053 is introduced at 10–20 wt% on total oven-dry fiber; the furnish includes bleached softwood kraft, cotton linter pulp, and a wet-strength polyamide-epichlorohydrin resin. Separate low-intensity refining of VPB053 preserves fibre length, and blending occurs in the machine chest immediately before the fan pump. The paper machine is configured with a conventional Fourdrinier and a wet-press loading of 60–100 kN/m; after size-press application of starch, the sheet receives a phenolic or latex saturant at 10–25 g/m² dry pickup and is cured at 120–150°C. The VPB053 network increases dynamic tear resistance under the high-tension saturator frames used in abrasive base production, reducing web breaks at speeds above 150 m/min. Compliance is verified with ISO 1924-2 for tensile properties, ISO 2758 for bursting strength, ISO 2493-1 for bending stiffness, ISO 5636-3 for air permeance, and ISO 5630-1 for accelerated ageing. Terminal finished products include paper-backed abrasive discs for automotive repair, orbital sanding discs, and fibre disc bases used with coated abrasive grain of 80–400 mesh.

    Release liner base paper and high-speed silicone coating substrates formulated with VPB053 at 3–10 wt% on total fiber target reduced surface picking and stable silicone holdout after machine calendering. The furnish is bleached hardwood/softwood kraft refined to 25–40°SR; VPB053 is added after refining and dispersed at 0.15–0.25% headbox consistency. After on-machine film-press surface treatment with oxidized starch, the sheet is supercalendered or soft-calendered to apparent density between 1.0–1.4 g/cm³. The structural fibre network reduces dusting and surface fibre release during high-speed silicone coating, a failure mode that otherwise increases splice breaks and causes silicone skips on release liners. Compliance references are ISO 1924-2 for tensile properties, ISO 5636-3 for permeance, ISO 535 for water absorbency, ISO 8791-2 for Bendtsen roughness, and FDA 21 CFR 176.170 where the liner is used in indirect food-contact label stock. Terminal finished product types include release liners for self-adhesive labels, double-sided tape liners, and casting papers for polyurethane leather where surface roughness targets remain below 1.0 µm Bendtsen.

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    Certification & Compliance
    More Introduction

    Kuraray VPB053-PVA structural fiber is a polyvinyl alcohol short-cut fiber supplied for wet-end addition in papermaking furnishes. The manufacturer’s grade designation decodes as a nominal linear density of 0.5 dtex and a cut length of 3 mm; the product belongs to the KURALON VP papermaking series and is positioned between VPB033 (0.3 dtex) and VPB103 (1.0 dtex) in surface area and bonding-point count. PVA density is routinely reported in the 1.26–1.30 g/cm³ range under ISO 1183-1:2019, which is lower than cellulose and sufficiently close to water to allow uniform dispersion without the buoyancy separation observed with polypropylene or polyester fibers. Thermogravimetric analysis under ISO 11358-1:2022 places the onset of thermal decomposition near 225–230°C in nitrogen; therefore, dryer surface temperatures above 200°C are outside the recommended operating envelope because of discoloration and embrittlement risk.

    Mechanical property ranges for PVA papermaking fibers are typically 6.0–8.5 cN/dtex dry tenacity and 12–18% elongation at break when tested according to ISO 5079:2020 for single fibers. Wet tenacity is generally 2–3 cN/dtex lower than dry tenacity. The fiber is not intended as a melt adhesive; its bonding mechanism is hot water plasticization rather than melting. Lot-to-lot variance in cut length is controlled within ±0.5 mm, and the fiber is shipped in compressed bales with a moisture content of 4–5% under ISO 287:2017. Published data for VPB053-PVA specifically is limited, but the general PVA fiber property band is verified by the manufacturer’s technical data sheets.

    How does a 0.5 dtex/3 mm fiber geometry alter sheet formation and drainage?

    At 0.5 dtex and 3 mm, the approximate fiber count is 6.7×10⁶ fibers per gram. This is calculated by converting linear density to mass per unit length and dividing the cut-length mass. Lower-denier VPB033 yields approximately 1.1×10⁷ fibers per gram, while higher-denier VPB103 yields approximately 3.3×10⁶ fibers per gram. The higher count of VPB053-PVA provides more discrete bonding points than the coarser grade without creating the extreme wet-end surface area of the fine grade. In a laboratory sheet prepared to ISO 5269-2:2004, the effect on drainage should be quantified with ISO 5267-1:1999; because the PVA surface is smooth and non-fibrillating, the freeness shift is expected to be less than that produced by an equal mass of refined softwood fines. Formation uniformity is influenced by fiber length: the 3 mm cut is below the length threshold at which hydraulic entanglement becomes severe, but longer than a microfiber. The result is a sheet structure in which VPB053-PVA fibers bridge adjacent cellulosic flocs, improving tensile energy absorption without creating the continuous plastic film that a fully soluble PVA binder would produce.

    The fiber cross-section is round or slightly oval; this shape reduces fiber-to-fiber mechanical entanglement compared with fibrillated cellulosic fibers. The smooth surface creates a large contact area at the fiber-cellulose interface when the fiber plasticizes, but before drying it can reduce wet-web friction. On a fourdrinier wet end, this can lead to slightly lower wet-web tensile at the open draw; mills should evaluate open-draw runnability when replacing cellulosic refining with PVA structural fiber. Furnish pH should be maintained between 6.0 and 8.0. At pH below 4.0, acid-catalyzed hydrolysis of PVA is negligible in normal process residence times but can reduce fiber strength after prolonged storage; at pH above 10.0, the fiber may swell excessively in high-temperature pulper chests.

    In wet-end addition, VPB053-PVA is introduced as a dry fiber or as a pre-slurried suspension at 0.05–0.50% consistency. Low-shear rectangular stock tanks are unsuitable because the hydrated fiber can settle into a stagnant bottom layer and partially gel if the furnish temperature exceeds 55°C; a side-entry high-shear disperser with tip speed above 10 m/s or a slotted-screen deflaker should precede machine chest injection. The typical addition range in manufacturer technical literature is 0.5–3.0% on bone-dry papermaking fiber, with higher loadings possible up to 5% before formation and retention losses become limiting. Because PVA is nonionic, it does not respond to cationic polyacrylamide retention agents as strongly as anionic cellulose fines; streaming potential at the headbox should be maintained near -5 to -10 mV according to ISO 13099-1:2012. The required retention aid dose may increase by 0.05–0.10 kg/ton when VPB053-PVA is added at 2%, but overcharging can cause deposition on forming fabric. Pilot-scale experience indicates that adding VPB053-PVA and high-charge cationic starch at the same low-shear injection point can produce gelatinous agglomerates because of hydrogen-bonded complex formation; the two additives should be separated, with VPB053-PVA at the machine chest and cationic starch at the fan pump suction.

    Headbox temperature should remain below 55°C to preserve the fiber’s discrete geometry before forming; if headbox temperature exceeds 60°C, the fiber can soften prematurely and adhere to headbox internals. On high-speed machines above 800 m/min, retention of discrete PVA fibers is also influenced by the forming fabric design. A 0.7 mm mesh fabric with low open area may not retain smoother PVA fibers as efficiently as it retains cellulosic fines, so the retention system must be rebalanced using streaming potential rather than trial-and-error dosage adjustments.

    When hot water solubility becomes the controlling parameter

    The functional performance of VPB053-PVA depends on the wet web reaching the fiber’s hot water softening range. Manufacturer technical literature identifies hot water dispersibility in the 60–70°C range; below 55°C the fiber remains inert, and above 75°C it can dissolve too quickly and lose its structural bridging identity. The practical dryer window is therefore ±5°C around the target softening point. In a Yankee dryer configuration with the pressed sheet entering at 40–45% moisture and a surface temperature of 105–115°C, the fiber is held within the bonding window while the sheet dries. Slow cylinder dryers in high-basis-weight grades above 120 g/m² may not deliver sufficient heat to the sheet core to trigger bonding, particularly in the center plies. When the fiber is used as a binder, dryer section temperature control is not a cosmetic adjustment; cross-machine moisture streaks can create local tensile differences exceeding 10% because some lanes do not reach the dissolution threshold. This is a critical process limit rather than a general papermaking parameter.

    After the sheet enters the dryer, the PVA fiber swells, migrates partially into adjacent fiber lumens, and forms hydrogen bonds between cellulosic surfaces. The partial dissolution is not complete; if the fiber dissolves completely, thin spots can develop in low-basis-weight sheets. This is why VPB053-PVA is classified as a structural fiber, not a fully soluble binder. The reel moisture content should be controlled at 4–6%; overdrying below 3% moisture can cause the PVA to become brittle and reduce fold endurance.

    Differentiation from cellulosic, polyester, and other PVA papermaking fibers

    VPB053-PVA differs from cellulosic refining agents because it does not fibrillate under mechanical refining. It is added after refining to avoid shortening; refiners should be bypassed because the fiber is already cut to 3 mm and further mechanical action reduces its bridging efficiency. Unlike polyester or polyethylene fibers, PVA has a density near 1.28 g/cm³ and a hydroxyl-rich surface, eliminating the need for surfactant pre-dispersion and reducing foam formation. Compared with KURALON VPB033 and VPB103, VPB053-PVA has an intermediate fiber count and surface area. The 0.3 dtex grade provides more bonding points per unit mass but can increase wet-end fines and reduce freeness; the 1.0 dtex grade increases bulk and air permeance but has fewer bonds. VPB053-PVA is therefore selected when a balance between dry tensile, bulk, and drainage is required. Unlike fully hydrolyzed PVA structural fibers used in cement or concrete reinforcement, VPB053-PVA is a short-cut hot water-sensitive grade intended for papermaking and cannot be used as a substitute for polyvinyl alcohol fibers designed for alkali resistance.

    Table 1 — Comparative property ranges for KURALON VP papermaking PVA grades
    PropertyTest methodVPB033VPB053-PVAVPB103
    Nominal linear densityISO 1973:20210.3 dtex0.5 dtex1.0 dtex
    Nominal cut lengthManufacturer optical method3 mm3 mm3 mm
    DensityISO 1183-1:20191.26–1.30 g/cm³
    Dry tenacityISO 5079:20206.0–8.5 cN/dtex
    Elongation at breakISO 5079:202012–18%
    Hot water dispersibility onsetManufacturer dispersion test60–70°C60–70°C60–70°C

    Values are typical ranges from manufacturer technical documentation; independent verification on production furnish is required because fiber performance shifts with refining, retention chemistry, and dryer profile.

    For filter base paper, VPB053-PVA is used at the low end of the addition range, typically 0.5–1.5%, because excess PVA can reduce pore size and alter air permeance. Air permeance measured by ISO 5636-3:2013 and burst strength by ISO 2758:2014 should be monitored together; the fiber’s contribution is expressed as a shift in the burst-strength-to-air-permeance ratio rather than as a tensile increase alone. In tea bag paper, the hot water bonding response is critical because the sheet must retain wet strength during steeping while avoiding off-taste; the papermaker should verify sensory acceptance on the finished article because PVA process residues and low-molecular-weight fractions can exhibit organoleptic effects at trace levels. Published data for VPB053-PVA in tea bag paper is limited, so laboratory-scale bag forming and steeping trials are mandatory before production approval.

    Molded pulp operations can use VPB053-PVA at 0.5–2.0% on bone-dry fiber to improve dry crush resistance after hot pressing. Because the forming tool operates at 150–180°C, the fiber reaches its softening range only if the tool remains closed for the required dwell; cycle times shorter than 20 s may not develop full bonding. Crush resistance should be verified with ISO 12192:2011, and the post-pressing moisture content should be kept between 4 and 6% to avoid embrittlement.

    Regulatory status for VPB053-PVA is determined on the finished paper or board because the fiber itself is only one furnish component. PVA is permitted as a component of paper and paperboard under FDA 21 CFR 176.170 for contact with aqueous and fatty foods, subject to extraction limits applicable to the final sheet. EU market placement requires compliance with Regulation (EC) No 1935/2004 overall migration limits and, for German buyers, BfR Recommendation XXXVI for paper and board. The fiber as supplied contains no halogenated flame retardants and no per- or polyfluoroalkyl substances by formulation, but the converter must verify that coatings, retention aids, and sizing agents do not introduce restricted substances. Total extractable content can be measured with ISO 10106:2021.

    Table 2 — Compliance verification matrix
    Standard or regulationScope
    ISO 5269-2:2004Preparation of laboratory sheets for physical testing
    ISO 1924-2:2008Tensile properties of paper and board at constant rate of elongation
    ISO 5267-1:1999Schopper-Riegler freeness
    ISO 535:2023Cobb water absorption
    ISO 5636-3:2013Bendtsen air permeance
    FDA 21 CFR 176.170Components of paper and paperboard in contact with aqueous and fatty foods
    BfR Recommendation XXXVIPaper and board for food contact
    Regulation (EC) No 1935/2004Framework regulation for food contact materials
    ISO 10106:2021Total extractable content

    The operational limit for this product is the combined moisture and temperature boundary: storage at relative humidity above 70% can increase fiber moisture enough to cause bale-to-bale clumping, while exposure to temperatures above 200°C during drying degrades the PVA backbone. The product is not compatible with strong oxidizing agents or with high-charge cationic polymers added at the same low-shear point; these boundaries are not product defects but constraints of the PVA chemistry.