| 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 | 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. |
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.
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.| Application Sector | Key Regulation/Standard | Critical Compliance Indicator | BP-10H Performance Boundary |
|---|---|---|---|
| Vinyl acetate-ethylene copolymer emulsion (indirect food packaging adhesives) | FDA 21 CFR 175.300, EU 10/2011 | Overall migration < 10 mg/dm²; residual vinyl acetate monomer < 5 mg/kg | Requires post-polymerisation stripping to < 500 ppm free monomer; high grafting efficiency reduces extractable PVOH fraction |
| Remoistenable adhesive coatings on paper-based articles | BfR Recommendation XIV, FDA 21 CFR 175.105 | Cold-water extractives < 50 mg/kg; blocking resistance at 40 °C/90 % RH | Plasticiser/PVOH ratio must be tuned to prevent excessive blocking while maintaining reactivation below 25 °C |
| Surface sizing of recycled containerboard for food contact | FDA 21 CFR 176.170, 176.180 | Chloroform-soluble extractives < 0.5 mg/in²; specific migration of aluminium < 1 mg/kg | Size-press pH must remain above 7.5 to avoid insoluble PVOH-aluminium complex formation |
| Textile warp sizing for Oeko-Tex Class I articles | OEKO-TEX Standard 100 Annex 4, GB 4287-2012 | Effluent COD < 80 mg/L; residual surfactant APEO < 100 mg/kg | Desize effluent ultrafiltration recovery rate > 90 %; low ash content avoids downstream dyeing defects |
| Water-based strippable protective masking films | RoHS 2011/65/EU Annex II, VDA 278 | Brominated flame retardant < 1000 mg/kg; VOC fogging condensate < 2 mg per VDA 278 thermodesorption | Alkali solubility ensures clean removal without silicone contamination; drying must avoid temperatures that cause intra-film crosslinking |
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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| Property | Method | BP-05 (87–89 mol%) | BP-10H (99.0–99.8 mol%) | BP-17 (97.5–98.5 mol%) |
|---|---|---|---|---|
| 4 % sol. viscosity | Brookfield LV, 20 °C | 4.5–6.0 mPa·s | 10–14 mPa·s | 25–30 mPa·s |
| Cold-water solubility | Dissolution at 25 °C | Complete | Insoluble | Partial, cloudy |
| Tensile strength | ASTM D882 (50 % RH) | 45–55 MPa | 75–90 MPa | 65–80 MPa |
| Elongation at break | ASTM D882 | 200–300 % | 10–20 % | 30–60 % |
| Oxygen permeability (25 µm, 0 % RH) | ASTM D3985 | 0.8–1.2 cm³/(m²·d·atm) | < 0.5 cm³/(m²·d·atm) | 0.6–0.8 cm³/(m²·d·atm) |
| Regulation / Standard | Applicable Scope | Status for BP-10H |
|---|---|---|
| FDA 21 CFR §175.300 | Resinous and polymeric coatings for food contact | Permitted, subject to extraction limits |
| EU Regulation (EC) No 1935/2004 | Materials and articles intended to come into contact with food | Compatible when compounded with listed additives |
| REACH (EC) 1907/2006 | Registration, evaluation, authorisation of chemicals | Weight-of-evidence polymer exemption; full registration not required |
| RoHS 2011/65/EU (Recast) | Restriction of hazardous substances in electrical equipment | Inherently compliant; does not contain restricted phthalates, heavy metals, or BFRs |
| JIS K6726:1994 | Testing methods for polyvinyl alcohol | Primary specification basis for moisture, ash, pH, viscosity |