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Anhui Liwei Chemical Co., Limited.

CCP PVA BP-10H

    • Product Name: CCP PVA BP-10H
    • 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 123320
    Appearance white granular powder
    Degree Of Hydrolysis 99 mol%
    Viscosity 4 Percent Solution At 20c 10.0 ± 1.0 mPa·s
    Ph 4 Percent Solution 5.5 - 7.5
    Ash Content ≤ 0.5%
    Volatile Content ≤ 5.0%
    Bulk Density 0.45 - 0.55 g/cm³
    Particle Size 20 - 80 mesh
    Solubility soluble in hot water above 80°C
    Melting Point 220 - 240°C
    Average Molecular Weight about 44000

    As an accredited CCP PVA BP-10H factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing CCP PVA BP-10H is supplied in 25 kg net multi-wall paper bags with polyethylene lining for moisture protection.
    Container Loading (20′ FCL) One 20′ FCL container loaded with CCP PVA BP-10H, palletized and secured for safe transport.
    Shipping CCP PVA BP-10H is shipped as a free-flowing powder in sealed multi-layer bags or fiber drums to protect against moisture. Classified as non-hazardous for transport, it moves safely by sea, air, or land. Keep containers dry, avoid dust accumulation, and store in a cool, ventilated area.
    Storage Store CCP PVA BP-10H in a cool, dry, well-ventilated area away from direct sunlight, heat, and ignition sources. Keep the container tightly sealed to prevent moisture absorption and contamination. Avoid dust generation and store separately from oxidizing agents. Use appropriate ventilation and personal protective equipment when handling.
    Shelf Life Shelf life for CCP PVA BP-10H is typically 2 years from manufacture date when stored in a cool, dry place.
    Application of CCP PVA BP-10H
    In semicontinuous vinyl acetate-ethylene emulsion polymerisations conducted within baffled high-pressure reactors rated for 40 bar(g) and equipped with Pfaudler-style glass-lined cooling jackets, the grafting reaction between the acetate end groups of polyvinyl alcohol and growing poly(vinyl acetate-co-ethylene) radicals governs particle nucleation density and latex coagulum generation. BP-10H (partially hydrolysed grade, measured viscosity of 4 % aqueous solution at 20 °C within 5.0–6.5 mPa·s per ISO 12058-1:2018, residual acetate content 11.0–14.0 mol%) is pre-dissolved in deionised water at 90–95 °C for 60 minutes under slow agitation and then transferred to a holding vessel where the solution temperature is reduced to the polymerisation start temperature of 65 °C. In a production-scale 16 m³ reactor fitted with a two-flight impeller operating at 120–150 rpm, the protective colloid charge typically constitutes 4.0–6.0 wt% based on total vinyl acetate monomer mass. When the ethylene partial pressure is maintained between 18 bar and 26 bar and the delayed initiator feed of potassium persulfate (0.08–0.12 wt% on monomer) is synchronised with a dual-stream emulsifier post-addition of nonylphenol-free ethoxylated alcohol (cloud point > 85 °C), the resulting bimodal particle size distribution (D₅₀ 0.8–1.4 μm) reduces shear-thickening tendencies during spray drying for redispersible powder manufacture. A critical processing constraint is the dissolved oxygen content of the initial aqueous charge; concentrations exceeding 1.5 mg/L delay induction by 15–30 minutes and broaden the molecular weight distribution of the free polymer fraction, which later manifests as weak wet adhesion in formulated wood adhesives exceeding DIN EN 204 category D3 requirements. Compliance with indirect food contact applications for the resulting emulsion falls under FDA 21 CFR 175.300 and EU 10/2011 with overall migration limits below 10 mg/dm²; specific nitrosamine migration is monitored per EN 12868 when the latex is destined for bottle cap liner compounds. The terminal product forms range from single-component woodworking adhesives (white glue, D2/D3 class per ISO 19210) to weatherable exterior architectural coating binders enriched with vinyl versatate terpolymers. Residual formaldehyde in the emulsion, quantitated via ISO 14184-1:2011, must remain below 20 mg/kg when destined for mattress foam laminations that align with Oeko-Tex Standard 100 Class I. During post-polymerisation stripping, a wiped-film evaporator operated at 85 °C and −0.6 bar(g) reduces free monomer below 500 ppm without advancing the gel fraction; the devolatilised latex then passes through a 25 μm bag filter to remove microgrit formed by over-shear near the agitator hub. Formulation chemists must pre-buffer the aqueous phase with sodium acetate trihydrate (0.4–0.7 wt% on water) to prevent local pH drift below 4.5 because premature PVOH acetalisation can permanently insolubilise the colloid layer and collapse latex stability. Equipment fouling rates double when the nucleation step exceeds 72 °C due to accelerated graft-site termination, a phenomenon validated by comparative heat-transfer coefficient decay logs on a 10 m² shell-and-tube condenser over 300 consecutive batch records.

    What Differentiates Remoistenable Adhesive Performance from Conventional Wet Lamination?

    Remoistenable adhesive coatings utilise the thermoplastic swellability of partially hydrolysed PVOH rather than its outright dissolution, relying on controlled crystallite melting points introduced during the drying profile. A BP-10H stock solution at 15–25 % solids is blended with glycerol plasticiser at 8–12 parts per hundred dry resin and a defoamer based on polyether siloxane (0.05–0.10 wt%); the formaldehyde-donor insolubiliser glyoxal is deliberately omitted to preserve cold-water activation below 25 °C. This waterborne lacquer is applied to silicone-coated release liner via an enclosed doctor-blade gravure station with 150 lpi electromechanically engraved cylinders, running at 40–60 m/min through a three-zone arch oven where the final zone air temperature is capped at 105 °C to prevent irreversible lactone-induced insolubilisation that renders the film non-activatable. The dry coat weight is held at 4–8 g/m², monitored online by a near-infrared moisture sensor calibrated against ISO 287:2017 oven-dry mass. After transfer lamination to face stock paper, the adhesive surface exhibits a blocking resistance compliant with TAPPI T 477 om-19 at 40 °C and 90 % RH for 24 h. Regulatory thresholds for indirect food paper require extractives below 50 mg/kg simulating saliva under BfR Recommendation XIV testing, while the finished envelope or self-seal band remains within the lap-joint tensile strength retention limits of ISO 1924-3:2005 after 10 rewetting cycles. Terminal converted products include moisture-activated tape for corrugated case sealing, postage stamps conforming to UPU S28 curl-resistance criteria, and high-speed label applicator web rolls where the activation time is compressed below 0.3 seconds through micro-perforated facestock that accelerates water ingress.

    Surface Strength Metrics for Recycled Containerboard Treated via Film Press Application

    In paper mills running recycled fibre content above 80 %, the replenishment of surface strength through size-press additions becomes a closed-loop control variable directly tied to converting-line jams. BP-10H is combined with a thinned oxidised corn starch at a ratio of 3–8 dry parts PVOH per 100 dry parts starch, the exact proportion tuned by IGT pick velocity targets according to ISO 3783:2006. The size-press solution is prepared by cooking starch at 95 °C, then dosing PVOH pre-solution at 12 % solids into the service tank to achieve a combined working solids of 6–9 %; the circulating solution temperature is maintained at 55–65 °C because cooling below 50 °C induces retrogradation of the amylose fraction and viscosity drift exceeding ±15 mPa·s as measured on a Brookfield LV spindle #2 at 100 rpm. Application proceeds via a metering film press with roll hardness set to 0–2 P&J; the hydraulic loading on the rubber-covered metering roll controls film split and limits dry pick-up to 1.8–2.5 g/m² per side. The thin PVOH-enriched film plasticises the fibre surface, reducing dusting during flexo printing and increasing Scott bond internal strength by 12–18 % compared to pure starch control when tested per TAPPI T 569 om-14. Compatibility with wet-end rosin-alum systems demands that the size-press pH be buffered to 7.5–8.0 with sodium bicarbonate; unreacted aluminium ions carried with the wet web can crosslink PVOH into an insoluble gel that produces streaks on calender rolls. For food-contact grades, the finished board must comply with FDA 21 CFR 176.170 and 176.180, with chloroform-soluble extractives below 0.5 mg/in² of product surface. End-use formats include heavyweight produce shipping containers with water-resistant labels, pharmaceutical outer cartons that must pass USP <671> moisture vapour barrier classification, and gypsum board facing paper where sustained Cobb values below 40 g/m² per ISO 535:2014 after 2 min exposure are mandatory.

    When filament polyester warp yarns of 75 denier/36 filament are sized on a Zell single-size-box slasher at 80 m/min, the size formulation in the first box contains BP-10H at 4.5–6.0 % solids combined with a polyacrylic acid ester binder (1.2 % solids) and a hydrogenated vegetable oil-based lubricant (0.3 % solids on size weight). The inter-filament adhesion achieved under a squeezing pressure of 0.35 MPa yields a size add-on of 4.8–5.5 % owf, measured by the mass difference after desizing a conditioned warp sheet according to AATCC 94-2019. The blocky fracture artefact common to fully hydrolysed PVOH sizes—which generates bead-up deposits on drop wires and increases loom stop frequency—is suppressed by the intermediate residual acetyl content of BP-10H, permitting continuous air-jet weaving at 650 picks/min with weft insertion air pressure below 4.5 bar. Post-weaving desizing is carried out in a continuous open-width washer using enzymatic amylase for starch co-blends or a 0.8 % hydrogen peroxide pad-steam oxidative route at 90 °C, achieving residual ash below 0.02 % and PVA recovery rates exceeding 92 % via ultrafiltration membrane modules (molecular weight cut-off 20 kDa). The reclamation loop aligns with the effluent COD discharge limit of 80 mg/L stipulated in GB 4287-2012 Annex A. The finished fabric, after heat-setting at 190 °C, must pass extractable heavy metal and pentachlorophenol screens per OEKO-TEX Standard 100 Annex 4 for article class I. Representative end products include woven sports outer shells with a DWR finish, textured luggage fabrics exceeding 200 000 cycles in a Martindale abrasion test per ISO 12947-2:2016, and fusible interlinings where the PVOH size residue must not interfere with the adhesion peak temperature of low-density polyethylene dot coating applied at 120–130 °C.
    Regulatory Compliance and Standard Cross-Reference Matrix by Application Sector
    Application SectorKey Regulation/StandardCritical Compliance IndicatorBP-10H Performance Boundary
    Vinyl acetate-ethylene copolymer emulsion (indirect food packaging adhesives)FDA 21 CFR 175.300, EU 10/2011Overall migration < 10 mg/dm²; residual vinyl acetate monomer < 5 mg/kgRequires post-polymerisation stripping to < 500 ppm free monomer; high grafting efficiency reduces extractable PVOH fraction
    Remoistenable adhesive coatings on paper-based articlesBfR Recommendation XIV, FDA 21 CFR 175.105Cold-water extractives < 50 mg/kg; blocking resistance at 40 °C/90 % RHPlasticiser/PVOH ratio must be tuned to prevent excessive blocking while maintaining reactivation below 25 °C
    Surface sizing of recycled containerboard for food contactFDA 21 CFR 176.170, 176.180Chloroform-soluble extractives < 0.5 mg/in²; specific migration of aluminium < 1 mg/kgSize-press pH must remain above 7.5 to avoid insoluble PVOH-aluminium complex formation
    Textile warp sizing for Oeko-Tex Class I articlesOEKO-TEX Standard 100 Annex 4, GB 4287-2012Effluent COD < 80 mg/L; residual surfactant APEO < 100 mg/kgDesize effluent ultrafiltration recovery rate > 90 %; low ash content avoids downstream dyeing defects
    Water-based strippable protective masking filmsRoHS 2011/65/EU Annex II, VDA 278Brominated flame retardant < 1000 mg/kg; VOC fogging condensate < 2 mg per VDA 278 thermodesorptionAlkali solubility ensures clean removal without silicone contamination; drying must avoid temperatures that cause intra-film crosslinking

    When PVOH Protective Colloids Cross into Solvent-Borne Strippable Masking Coatings

    Partially hydrolysed PVOH can function as a temporary interface barrier in aqueous strippable masks when formulated with co-solvents that delay full dissolution, creating a continuous film with adequate tensile elongation for peel removal. A concentrated BP-10H solution at 20 % solids is let-down with ethanol (15–25 wt% of formulation) and a branched polyol ester plasticiser at 5 wt% on PVOH to depress the film-forming temperature to 30 °C, allowing deposition via reverse gravure coating on aluminium-plated automotive headlamp reflectors before physical vapour deposition metallisation. The wet film thickness is set to 50–75 μm and dried in a three-stage convection oven with a maximum web temperature of 85 °C, producing a transparent, flexible masking layer that resists the 180 °C flash heating cycle during sputtering. Peel force after processing, measured per ASTM D3330 Method A, remains between 1.5 N/25 mm and 3.5 N/25 mm; values below the lower limit indicate premature adhesion loss due to over-plasticisation, while values above 4.0 N/25 mm risk cohesive splitting and residue. The cured film must pass halogen-free certification per IEC 61249-2-21 with total chlorine and bromine below 900 ppm, and volatile condensable substances under VDA 278 thermodesorption at 90 °C must not exceed 2 mg to avoid fogging on optical-grade components. End-use configurations extend to temporary solder masking on circuit boards during selective conformal coating, and peelable protection for polished stainless-steel architectural panels during transport, where the masking film must withstand 14 days outdoor exposure without photo-embrittlement. The main process incompatibility arises when the coating bath is contaminated with divalent calcium ions from hard-water dilution; calcium-PVOH complexes raise solution viscosity unpredictably and create pinhole defects—deionised water with conductivity below 5 μS/cm is mandatory.

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    Certification & Compliance
    More Introduction
    The semi-crystalline thermoplastic polyvinyl alcohol resin designated CCP PVA BP-10H is a fully hydrolyzed homopolymer with a nominal degree of hydrolysis of 99.0–99.8 mol% and a 4 % aqueous solution viscosity (at 20 °C, Brookfield LV, spindle #1, 60 rpm) of 10–14 mPa·s. Manufactured via a controlled alcoholysis process that minimizes residual acetyl groups to fewer than 0.2 mol%, this grade exhibits a volatile matter content not exceeding 5.0 wt% (JIS K6726), ash residue of ≤ 0.5 wt%, and a pH in aqueous dispersion of 5.0–7.5. The high stereoregularity imparted by near-complete acetate removal translates into a melting endotherm peak at 228–242 °C (DSC, 10 K/min), a glass transition temperature of approximately 85 °C, and an oxygen transmission rate through a 25 µm cast film at 23 °C and 0 % RH falling below 0.5 cm³/(m²·24 h·atm) when sufficiently plasticized. Unlike partially hydrolyzed co-polymers that dissolve readily in cold water, BP-10H requires a dissolution temperature maintained above 85 °C under vigorous agitation; incomplete solvation below this threshold leads to gel-particle defects in downstream film or coating processes.

    What Distinguishes BP-10H from Lower Hydrolysis Grades Such as BP-05 or BP-17?

    The functional boundary between partially hydrolyzed polyvinyl alcohols (typically 87–89 mol% for grades like BP-05) and fully hydrolyzed types rests on cold-water dispersibility, crystallinity development, and interfacial adhesion to hydrophobic surfaces. BP-10H carries fewer than 0.2 mol% residual acetate groups; the consequent linear-chain packing yields a crystallinity index (Xc) of 50–55 % by density-gradient column, roughly 20 % higher than BP-05 at 88 mol% hydrolysis. This structural distinction governs practical behavior:

    Film Extrusion Processing Window and Thermal Stability Limits

    Work on cast-film lines with a L/D 30 single-screw extruder, barrier screw, and coat-hanger flat die indicates that a melt temperature range of 210–235 °C is processable without triggering noticeable chain scission when the residence time distribution is limited to 90–120 seconds. At temperatures exceeding 240 °C, acetic acid liberated by thermal elimination of residual acetate (even at < 0.2 mol%) autocatalyzes degradation, causing a rapid drop in intrinsic viscosity and an increase in yellowness index (YI D1925) beyond 1.5. Operators running BP-10H on blown-film towers must keep the die gap between 0.8–1.2 mm and employ a frost-line height control that avoids quenching rates faster than 80 °C/s, otherwise micro-voids originating from trapped moisture nucleate and reduce dart impact strength (ASTM D1709, Method A) below 150 g. Pre-drying to a moisture content of ≤ 0.3 wt% (loss-on-drying, 105 °C, 4 h) is mandatory when processing in ambient relative humidity above 60 %. The hygroscopic character of fully hydrolyzed PVA necessitates sealed resin hopper systems with dry-air purge. In co-extrusion with polyolefin tie layers, corona treatment at a surface energy of ≥ 42 mN/m (DIN 53364) on the BP-10H skin enables bonding without delamination during thermal cycling from -20 °C to 80 °C. A frequently encountered failure mode during down-gauging below 15 µm involves transverse-direction tear propagation initiated at gel-particle boundaries; this is mitigated by melt filtration through screens of 100–150 µm gauge and by verifying dissolution completeness via turbidity measurement (NTU ≤ 5 in a 10 % solution at 90 °C).
    Property Gradient: CCP PVA Partially vs. Fully Hydrolyzed Grades
    PropertyMethodBP-05 (87–89 mol%)BP-10H (99.0–99.8 mol%)BP-17 (97.5–98.5 mol%)
    4 % sol. viscosityBrookfield LV, 20 °C4.5–6.0 mPa·s10–14 mPa·s25–30 mPa·s
    Cold-water solubilityDissolution at 25 °CCompleteInsolublePartial, cloudy
    Tensile strengthASTM D882 (50 % RH)45–55 MPa75–90 MPa65–80 MPa
    Elongation at breakASTM D882200–300 %10–20 %30–60 %
    Oxygen permeability (25 µm, 0 % RH)ASTM D39850.8–1.2 cm³/(m²·d·atm)< 0.5 cm³/(m²·d·atm)0.6–0.8 cm³/(m²·d·atm)
    Adhesion to Polar Substrates and Water Wash-off Resistance In paper-coating formulations designed for high-holdout printability, BP-10H demonstrates a Cobb60 water absorption (ISO 535) value reduced by 35–40 % compared to coatings made with partially hydrolyzed PVA at identical coat weight. The hydroxyl-rich chain segments induce strong hydrogen bonding with cellulosic fibers; nonetheless, surface-bound BP-10H resists removal during offset printing dampening cycles only when the coating has been cured at a web temperature exceeding 180 °C for at least 3 seconds. If the drying section cannot achieve this, a crosslinker such as glyoxal at 0.05–0.2 % on dry weight is required. The same chemistry underpins its use in textile warp sizing where desizing on alkali-scouring ranges needs an oxidative step (hydrogen peroxide at 0.5 %, 80 °C) because single-stage hot water washing leaves residual film on cotton yarns, elevating stiffness by up to 15 %. In applications requiring water-soluble sacrificial layers—such as support structures in ceramic injection moulding—BP-10H is dissolved only after the green body is immersed in circulating water at 85 °C for 2–4 h. The dissolution rate can be accelerated to 0.8 mm/h by introducing 1–3 % methanol into the bath, though methanol quantities above 5 % risk stress-cracking the ceramic binder system. When Partial Replacement of Gelatin in Warp Sizing Yields Cycle Time Reductions In high-speed air-jet weaving where warp yarns are subjected to cyclic bending at 600–850 cycles/min, blends of BP-10H and modified starch at a 30:70 weight ratio reduce size pickup by 1.2–1.5 % absolute versus pure starch while boosting abrasion resistance (measured on a Zweigle abrasion tester) by 40 %. A mill trial on a Tsudakoma ZAX9100 loom processing Ne 40 combed cotton at 750 rpm recorded loom stop frequency dropping from 2.1 to 1.3 stops per hour when the size liquor temperature was maintained at 88–92 °C during application. The technical limitation is that size rebound moisture regain must be kept below 12 %; storage in a shed at > 70 % RH without polyethylene wrapping led to blocking and un-tieable knots on the beam, requiring re-sizing.
    Regulatory Compliance Synopsis for CCP PVA BP-10H
    Regulation / StandardApplicable ScopeStatus for BP-10H
    FDA 21 CFR §175.300Resinous and polymeric coatings for food contactPermitted, subject to extraction limits
    EU Regulation (EC) No 1935/2004Materials and articles intended to come into contact with foodCompatible when compounded with listed additives
    REACH (EC) 1907/2006Registration, evaluation, authorisation of chemicalsWeight-of-evidence polymer exemption; full registration not required
    RoHS 2011/65/EU (Recast)Restriction of hazardous substances in electrical equipmentInherently compliant; does not contain restricted phthalates, heavy metals, or BFRs
    JIS K6726:1994Testing methods for polyvinyl alcoholPrimary specification basis for moisture, ash, pH, viscosity
    Corona-treating BP-10H film beyond 42 mN/m wetting tension triggers surface crosslinking detectable as an insoluble gel fraction that complicates gravure printing ink adhesion. Laminators therefore calibrate treaters to a maximum 45 mN/m and verify dyne level within 30 minutes of treatment before the decay curve drops below 40 mN/m. When the film is overlaid with a polyethylene sealant layer immediately after offline treatment, residual active species catalyze interfacial esterification; a waiting interval of 24 h at 35 °C prior to lamination eliminates this anomaly. Plasticizer compatibility deserves explicit attention. Sorbitol and glycerol at loadings of 10–20 phr efficiently lower the glass transition to 15–35 °C without exudation, whereas propylene glycol-based plasticizers induce phase separation after storage under fluctuating humidity. Ethylene carbonate, though effective, must be excluded when the final article must meet EN 71-3 migration limits for toys. Published data for polycondensation plasticizers such as polyester adipates in BP-10H is limited; pilot-scale experiments indicate plasticizer bleed-out at loads above 8 phr when film thickness exceeds 50 µm. The difference between BP-10H and intermediate hydrolysis grades such as BP-17 (97.5–98.5 mol%) becomes critical in emulsion polymerisation stabilisation. Using BP-10H as a protective colloid in vinyl acetate emulsion polymerisation yields a particle size distribution skewed toward 0.8–1.5 µm and viscosity above 5000 mPa·s, while BP-17 under identical reactor conditions (semi-batch, 70 °C, potassium persulfate initiator) produces submicron particles and a final viscosity below 2000 mPa·s. This rheological contrast steers the selection of BP-10H toward high-viscosity wood adhesives meeting DIN EN 204 D3 requirements, where film-forming capacity and heat resistance are valued over pourability.