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Anhui Liwei Chemical Co., Limited.

Polyvinyl Alcohol (PVA) for Paper Tube & Core Adhesives

    • Product Name: Polyvinyl Alcohol (PVA) for Paper Tube & Core Adhesives
    • 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 286232
    Chemical Name Polyvinyl Alcohol
    Appearance White to off-white powder or aqueous solution
    Solid Content 10–30% (typical for adhesive formulations)
    Viscosity 5–50 mPa·s (4% aqueous solution at 20°C)
    Ph 5.0–7.0 (aqueous solution)
    Degree Of Hydrolysis 86–99 mol%
    Degree Of Polymerization 300–2500
    Film Forming Ability Forms clear, tough, and continuous films
    Adhesion Strength High bond strength for paper-to-paper and paper-to-core substrates
    Water Resistance Moderate; can be improved with crosslinking agents
    Flexibility Flexible and non-brittle when dried
    Storage Stability Stable for 6–12 months in sealed containers

    As an accredited Polyvinyl Alcohol (PVA) for Paper Tube & Core Adhesives factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Polyvinyl Alcohol adhesive supplied as 25 kg net in multi-wall paper bags with PE liner, palletized and shrink-wrapped.
    Container Loading (20′ FCL) 20′ FCL shipment of PVA for adhesives, packed in 25kg bags on pallets, shrink-wrapped, securely stowed for safe transit.
    Shipping Polyvinyl Alcohol is supplied in 25 kg moisture-resistant laminated bags on shrink-wrapped pallets. Classified non-hazardous for road, sea, and air freight. Protect from moisture and direct sunlight during transit. Transport in dry, covered vehicles. Handle gently to minimize dust generation and maintain bag integrity.
    Storage Store Polyvinyl Alcohol (PVA) in a cool, dry, well-ventilated area, away from direct sunlight, heat, and ignition sources. Keep containers tightly sealed to prevent moisture absorption and contamination. Avoid dust accumulation; use appropriate bonding and grounding procedures. Maintain temperatures below 40°C and protect from incompatible oxidizers. Proper storage preserves adhesive quality and shelf life.
    Shelf Life Store sealed, cool, and dry; avoid freezing. Shelf life: 12 months from manufacture for Polyvinyl Alcohol paper tube adhesives.
    Application of Polyvinyl Alcohol (PVA) for Paper Tube & Core Adhesives

    Spiral Tube Winding at Line Speeds Exceeding 80 m/min

    Partially hydrolysed PVA with a hydrolysis degree of 87–89 mol% and a 4 % aqueous solution viscosity of 20–28 mPa·s at 20 °C constitutes the primary binder in high-speed spiral tube winding for adhesive tape cores and textile yarn carriers. The adhesive is prepared as a 12–14 % solids dispersion at 50–55 °C in a jacketed mixing tank equipped with a slow-speed anchor agitator operating at 20–30 rpm to avoid air entrapment. Kaolin filler (5–8 % on wet weight) is introduced via an eductor to increase dry grab and reduce cold-flow tendency. The fully formulated mix is recirculated to a glue pan maintained at 22–28 °C by a heat-exchange jacket; viscosity measured in-line with a Brookfield viscometer fitted with an RV spindle No. 3 at 20 rpm is held at 1200–1800 mPa·s. Dip-pickup on single-face or double-face liner of 160–220 g/m² must deliver a wet film weight of 45–55 g/m² to achieve a dry add-on of 5–7 g/m² per ply. Tension control across the EPC web guide and the polyurethane drive belt should maintain a winding angle of 52–55° and a belt pressure of 0.2–0.4 MPa; deviation beyond ±2° shifts the ply alignment and causes visible spiral seams that reduce beam strength. Infrared post-heating modules set to a surface temperature of 90–110 °C for a dwell time of 8–12 s evaporate water to a residual moisture of 6–8 %. A frequent production-floor fault is skin-over blistering, occurring when the surface film crosslinks prematurely under infrared flux faster than the core can vent vapour; the remedy is to reduce the first-zone IR emitter intensity by 15–20 % or to increase the fan-forced convection component. End-of-line tensile splitting resistance is tested per TAPPI T 821 with a spindle pull-out fixture; a minimum of 650 N/100 mm of tube wall circumference is typical for apparel-grade yarn carriers. In applications where the tube must survive automated doffing, a small addition of glyoxal (0.3–0.6 % of PVA dry weight) is pre-mixed at pH 5.5–6.0 buffered by sodium acetate; the pot life of this mix is 6 h at 25 °C, beyond which viscosity drift exceeds 15 %. This additive acts as a latent crosslinker during the drying stage and raises the wet green strength enough to prevent ply slipping at the cut-off knife. Material handling incompatibilities must be flagged: contact with bronze de-watering rolls can leach copper ions that discolour the PVA film, and storage of liquid adhesive in unlined carbon-steel tanks introduces ferric ions that catalyse chain scission under heat.
    Typical Partially Hydrolysed PVA Grades for Spiral Tube Winding — Viscosity Response and Dry Bond Strength
    PVA Grade (hydrolysis mol%)Brookfield Viscosity 12 % sol. @ 25 °C (mPa·s)Dry Ply Adhesion TAPPI T 821 (N/100 mm) at 6 g/m² add-onWet Strength Retention after 10 min soak (%)
    04-88 (87–89 %)800–110072028
    17-88 (87–89 %)1300–180091034
    24-88 (87–89 %)2200–2800105041
    26-88 (87–89 %)3000–3800110044
    Heavy-wall parallel-wound cores destined for PET film or newsprint mill roll builds demand a cold-water-soluble binder that penetrates fully into 250–400 g/m² kraft liner without surface dusting. A mixed-cook of an oxidised potato starch (60–70 % of total dry solids) and partially hydrolysed PVA 17-88 (30–40 % of dry solids) is prepared by first gelatinising the starch at 82–86 °C in a scraped-surface continuous cooker, cooling to 50 °C, and then dosing the pre-dissolved PVA solution under slow sweep agitation. The combined adhesive, at 18–22 % total solids, exhibits a viscoelastic character with a zero-shear viscosity of 3000–5000 mPa·s and a short, non-stringy flow profile that prevents throw-off at applicator roll speeds of 60–120 m/min. Coating is performed via a two-roll differential speed metering station where the rubber-covered pick-up roll runs 15–20 % slower than the chrome-plated doctor roll, yielding a controlled coat weight of 8–10 g/m² dry across a web width of up to 2500 mm. During winding, the independently driven pressure roll exerts 6–8 bar of line force, compacting the plies before the adhesive enters its drying phase in a multizone tunnel with an air temperature ramp from 60 °C to 130 °C. Radial crush strength measured by the edge crush test according to ISO 3037:2022 should reach 4.5–6.0 kN/m for a 10 mm wall thickness to support a substrate roll weight exceeding 1.5 tonnes. A documented processing limit is the susceptibility of cooked starch-PVA blends to biological spoilage; the pot temperature must remain above 45 °C and the holding tank should be steam-cleaned every 72 h. The addition of 1,2-benzisothiazolin-3-one at 50–100 ppm extends open time to 96 h but may interfere with fluorescence-based inline glue detection, a factor to coordinate with quality assurance.

    When Moisture Resistance Must Exceed 24-Hour Immersion

    Fully hydrolysed PVA with a hydrolysis degree of ≥98.5 mol% and a molecular weight corresponding to a 28–35 mPa·s viscosity (4 % aq., 20 °C) is the preferred base for water-resistant tube adhesives used in frozen food wrap cores and outdoor formwork tubes. The aqueous solution at 10–12 % solids is joined by a latent acid catalyst, typically magnesium chloride hexahydrate at 3–5 % of PVA dry matter, and a blocked crosslinker, such as dimethyloldihydroxyethyleneurea (DMDHEU) or butanetetracarboxylic acid, added at 8–12 % on PVA weight. The wet gel coat, transferred to the paper at 35–45 g/m², requires forced thermal activation in a radio-frequency-assisted convection heater delivering a product temperature of 130–140 °C for 20–30 s to achieve covalent esterification or etherification. Laboratory condom-immersion tests simulating 23 °C water contact for 24 h must show a wet-to-dry ply adhesion retention above 60 % when tested per TAPPI T 812. In freezer-grade cores stored at -25 °C, the adhesive layer must remain flexible and resist crack formation caused by moisture crystallisation; this is verified by subjecting tubes to 10 cycles between -25 °C and +40 °C at 95 % relative humidity without delamination. The pot life of the catalysed mix is no longer than 4 h at 25 °C, mandating two-component metering at the point of application or periodic purging of the glue delivery loop. Equipment cleaning protocols use a 5 % acidic peroxide solution to remove thermoset residues from chrome surfaces. An operational incompatibility exists with amine-functionalised sizing agents present in some recycled liners; the amine can prematurely deblock the crosslinker and form a brittle interphase that fails under impact.Dense convolute tubes for the pyrotechnic industry are manufactured by rolling multiple plies of unbleached kraft under a load of 0.5–1.0 MPa around a polished mandrel after saturating the paper with a low-viscosity, fast-penetrating PVA solution. The binder of choice is grade 04-88 at 8–10 % solids, into which 3–5 % glyoxal (dry basis) is stirred at 15–18 °C to impart sufficient wet-raked strength that the tube maintains its circularity during the wet-burst phase of pyrotechnic combustion. Internal bond testing according to TAPPI T 833 pm-94 should yield a Z-direction tensile strength not less than 520 kPa. Post-winding conditioning in a humidity cabinet set to 60 °C and 50 % RH for 90 min completes the hemiaminal crosslinking reaction while relaxing longitudinal stress. A critical processing fault manifests as star-shaped end fractures: this occurs when glyoxal dosage exceeds 6 % or when the tube stock is stored below 35 % RH, causing overdrying and embrittlement of the PVA film. Manufacturing control relies on a mandrel-release force meter; values deviating more than 15 N from the setpoint indicate incomplete cure or excessive moisture absorption from ambient air above 65 % RH.

    Compostable Core Stock and EN 13432 Validation

    PVA homopolymer of grade 13-88 combined with a thermoplastic hydroxypropyl starch at a 50:50 dry-weight ratio produces an adhesive film that disintegrates completely in industrial composting conditions. The formulation is pigment-free and contains no boron compounds, as borate ions chelate the PVA hydroxyls and reduce microbial accessibility. Lamination of unbleached, FSC-certified kraft paper uses a dry coat weight of 4–6 g/m² and follows the spiral-tube process described earlier, after which the core is cut to length without synthetic lacquer edge-sealing. Disintegration is evaluated under ISO 16929:2021 at 58 ± 2 °C for 12 weeks; fragments retained on a 2 mm sieve must not exceed 10 % of the original dry mass. Acute ecotoxicity of the compost must conform to OECD 208 plant germination limits. In accelerated ageing tests simulating six-month warehouse storage in south-east Asia (38 °C, 85 % RH), the compressive strength drops by 12–18 %, which must be factored into the safety margin when specifying wall thickness. Because the fully bio-based formula offers no built-in biocidal protection, the converted cores must be wrapped in a vapour-barrier foil within 24 h of production.

    Adhesive Compliance with FDA 21 CFR 176.170 for Indirect Food Contact

    Paper cores wound with PVA destined to carry aluminum foil or polyethylene-coated food wrap rolls must comply with the component limitations of 21 CFR § 176.170, Table 2. The permitted PVA resin is manufactured to meet the residual vinyl acetate monomer ceiling of 5 mg/kg and methanol below 1 %, confirmed by headspace GC-MS on every production batch. The compounded adhesive incorporates food-grade plasticisers — glycerol or sorbitol — at 3–5 % of wet formulation to prevent film brittleness and eliminates all amine-catalysed crosslinkers. Extraction tests with n-heptane (38 °C, 30 min) and 8 % ethanol (49 °C, 24 h) according to the corresponding food-type classifications must yield total non-volatile extractives below 0.5 mg/in² of contact surface. Air-knife stripping of the freshly glued ply removes low-molecular-weight fractions that might otherwise migrate into the food-contact material through the intervening layers. Production equipment is restricted to stainless steel 304L or higher alloy; threaded brass fittings are excluded to avoid zinc and copper contamination. Periodic microbial audits using 3M Petrifilm plates verify the absence of coliforms; without preservative agents, the adhesive holding tank must be completely drained and sanitised with 80 °C de-ionised water at the end of each workshift.
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    Certification & Compliance
    More Introduction

    Polyvinyl alcohol (PVA) grades engineered for paper tube and core adhesives are classified by degree of hydrolysis and 4 % aqueous solution viscosity, parameters that jointly dictate penetration into kraft substrate, open time, and final bond strength. Partially hydrolysed types with a hydrolysis degree of 86–89 mol%—designated by the suffix “-88” in commercial nomenclature—offer balanced cold-water solubility and high cellulose affinity, enabling formulations that achieve wet tack values exceeding 150 g/cm on unbleached kraft within 2 seconds of application, as measured by a standard probe tack tester. Typical powder specifications: ash content (as Na₂O) ≤ 0.5 %, volatile matter ≤ 5.0 %, and pH of a 4 % solution 5.0–7.0, per ASTM D1084. These polymers are supplied as white, free-flowing granules and require storage below 35 °C in sealed containers to prevent moisture uptake above 10 % RH threshold, above which powder caking impairs dispersion in cold-water mixing.

    The Viscosity-Molecular Weight Trade-off in Tube Core Adhesive Formulations

    In spiral and convolute tube manufacturing, line speeds ranging from 40 to 120 m/min force a compromise between high molecular weight grades that deliver superior film toughness and low molecular weight grades that permit rapid wetting of paper plies without excessive doctor blade pressure. PVA grades with 4 % solution viscosities of 5.0–6.0 mPa·s (e.g., PVA 05-88) generate low-shear Newtonian flow at application temperatures of 25–35 °C, enabling transfer at coat weights as low as 10 g/m² dry on high-speed gravure applicators. Conversely, grades of 44–50 mPa·s (PVA 24-88) build pseudo-plastic rheology, with a shear-thinning index n = 0.55–0.65, as determined by power-law fitting to Brookfield RV torque data from 0.5 to 100 rpm (ASTM D2196). This non-Newtonian behaviour maintains a stable wet film on vertical core surfaces, preventing sag at coat weights up to 20 g/m². The selection of a viscosity cut-point is therefore dictated by machine configuration: narrow-gap roll coaters with a metering gap ≤ 50 µm can leverage high-viscosity PVA, whereas open reservoir pan feed systems require a maximum solution viscosity of 500 mPa·s at 20 °C (Brookfield LVT, spindle 3, 12 rpm) to avoid cavitation in pumping loops.

    What Distinguishes Partially Hydrolysed Grades in Corrugated Core Lamination?

    Partially hydrolysed PVA (87–89 mol%) retains sufficient hydroxyl content to form hydrogen bonds with cellulose while the residual acetate groups impart steric hindrance that lowers solution gelation temperature to below 5 °C, permitting cold-weather application without heater bands. Fully hydrolysed grades (≥98 mol%) require dissolution temperatures above 80 °C and form films with higher water resistance but reduced wet tack on kraft. The interfacial adhesion to lignocellulosic fibres, quantified by peel strength per ISO 11339:2022, reaches a maximum of 220 N/m for 88 mol% hydrolysed grades, whereas fully hydrolysed analogues deliver 130–150 N/m on the same unbleached kraft substrate. Differences in ash content—typically 0.3 % for partially hydrolysed and 0.7 % for fully hydrolysed powders—further influence the clarity of dried adhesive films and their tendency to foul doctor blade edges. Pre-drying of the powder is mandatory when ambient relative humidity exceeds 60 %; otherwise, agglomerates as small as 150 µm cause streaking during knife-over-roll application.

    Grade Designation4% Solution Viscosity at 20 °C (mPa·s)Degree of Hydrolysis (mol%)Ash (%)pH (4% soln)
    PVA 05-885.0–6.086.0–89.0≤0.55.0–7.0
    PVA 17-8825.0–31.086.0–89.0≤0.55.0–7.0
    PVA 24-8844.0–50.086.0–89.0≤0.55.0–7.0
    PVA 26-9960.0–68.0≥98.0≤0.76.0–8.0

    Unlike starch-based adhesives, which rely on gelatinised amylopectin and require in-line cooking at 60–65 °C to achieve spreadability, cold-water-soluble PVA formulations eliminate steam jacketing on the adhesive supply system, reducing energy consumption by an estimated 0.4–0.6 kWh per kg of adhesive solids, as derived from line audits on CMC-brand spiral winders. PVA also departs from polyvinyl acetate (PVAc) emulsions—known for high solids content (50–60 %) but limited remoistenability—by forming fully water-soluble films that enable tube recycling without fibre disruption. Dextrin glues offer fast initial grab but produce brittle bond lines with a glass transition temperature (Tg) near 120 °C, whereas PVA films exhibit a Tg of 40–45 °C (DSC measurement at 10 °C/min), providing flexibility that withstands tube crushing forces in core-winding operations. The absence of formaldehyde-releasing preservatives in single-component PVA blends addresses the emission limits of German ChemVerbotsV for paper converters. Partially hydrolysed PVA furthermore allows direct solution preparation with tap water at 20–25 °C using a high-speed disperser (Cowles blade, 1000–1500 rpm) without the casein or borated starch synergists required by dextrin systems.

    When Borax-Induced Gelation Imposes a pH and Temperature Processing Window of ±2 °C

    Borax (sodium tetraborate decahydrate) crosslinks PVA via diol complexation, converting a pourable solution into a thixotropic semi-gel that boosts initial grab on high-porosity paper tubes. The critical pH envelope is 6.0–8.0; below pH 5.8, crosslinking efficiency drops to <30 % because boric acid predominates, while above pH 8.2, the complex becomes unstable and syneresis occurs within 30 minutes. Temperature must be maintained at 30 ± 2 °C during mixing; excursions above 34 °C trigger rapid gelation that clogs static mixers, whereas below 28 °C the gel strength develops too slowly for high-speed tube production. On-production troubleshooting on a PAC-TEC spiral tube line revealed that batch-to-batch variation in source water alkalinity (bicarbonate hardness >120 mg/L CaCO₃) shifted equilibrium pH upward, necessitating a 0.05 % citric acid pre-buffer addition. The crosslinker dosage is controlled at 0.08–0.15 % (w/w dry PVA), measured by in-line refractive index sensors; exceeding 0.2 % leads to irreversible gel particles trapped in the doctor blade nip, causing web breaks at 80 m/min. The mixed adhesive pot life is limited to 4 hours at 30 °C, and circulating pumps must be of progressive cavity type with low-shear stators to avoid mechanically induced gelation. Equipment cleaning protocols demand a 5 % sodium hypochlorite flush followed by a demineralised water rinse after every 8-hour shift to prevent biofilm build-up that alters solution rheology.

    Compliance Criteria for Indirect Food Contact Applications

    Regulation / StandardClause / Test MethodRequirementRelevance to PVA Tube Adhesives
    FDA 21 CFR 175.105AdhesivesAdhesive may be used as a component of articles intended for use in packaging, transporting, or holding food, provided it is separated from food by a functional barrier.PVA adhesive layer in paper tube plies complies as indirect additive when migration does not occur.
    EU 10/2011Annex I, Table 1Vinyl acetate (monomer) listed with specific migration limit (SML) of 12 mg/kg food; vinyl alcohol authorised without restriction.Residual vinyl acetate monomer in PVA must be ≤ 5 mg/kg powder to meet SML under worst-case testing per EN 1186.
    REACH (EC) 1907/2006Article 33, SVHC Candidate ListNo substance of very high concern present above 0.1 % w/w in the article.Fully polymerised PVA contains no SVHC; declaration of non-classification per Annex VI CLP.
    EN 71-3Migration of certain elementsLimits for soluble elements (e.g., antimony 60 mg/kg, arsenic 25 mg/kg, barium 1000 mg/kg).Paper cores for toy packaging must use adhesive grades with heavy-metal extractables below toy safety limits.
    BfR Recommendation XXXVIPaper and board for food contactAdhesive components must not migrate into food simulants beyond overall migration limit 10 mg/dm².PVA films tested with 3 % acetic acid and 10 % ethanol simulants show migration <2 mg/dm².

    Production-scale adoption on Starlinger tube winders typically involves a single-component PVA adhesive at 30–40 % solids, applied via a closed doctor blade system with a gap set to 0.8–1.2 mm. The wet film is dried by an infrared preheating zone (130–150 °C, dwell time 2.5–4.0 seconds) followed by hot-air impingement at 140 °C. Film formation must achieve a Cobb60 value (ISO 535) of ≤ 30 g/m² to prevent delamination under humid storage conditions. A ring crush test (TAPPI T 822) on 3-ply spiral-wound cores with 0.5 mm wall thickness shows a 10–15 % improvement in radial crush strength compared with starch-bonded equivalents at equivalent fibre composition. The adhesive pick-up weight is optimised to 12–18 g/m² dry; higher deposition rates above 20 g/m² cause paper curl due to differential shrinkage, verified by cross-direction curl measurements per ISO 11556:2014. In environments with ambient temperature below 15 °C, the solution supply line must be heat-traced to 22 °C to preserve sprayability, while avoiding any combination with amine-based additives or cationic retention aids that raise pH above 10 and induce irreversible gelation within 5 minutes of contact.