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Anhui Liwei Chemical Co., Limited.

CCP PVA BF-17E

    • Product Name: CCP PVA BF-17E
    • 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 358860
    Appearance White or slightly yellow granular powder
    Viscosity 4 Aqueous Solution 20 C 28–34 mPa·s
    Degree Of Hydrolysis 98.0–99.0 mol%
    Average Degree Of Polymerization 1700
    Ph 4 Aqueous Solution 5–7
    Volatile Content ≤ 5.0%
    Ash Content ≤ 0.5%
    Sodium Acetate Content ≤ 0.5%
    Solubility Soluble in hot water
    Bulk Density 0.40–0.55 g/cm³

    As an accredited CCP PVA BF-17E factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing CCP PVA BF-17E is supplied in 25 kg net bags, featuring a moisture-proof polyethylene inner liner and sturdy outer kraft paper packaging.
    Container Loading (20′ FCL) CCP PVA BF-17E is packed in 25kg bags and loaded into a 20-foot FCL container for safe, efficient transport.
    Shipping CCP PVA BF-17E is a polyvinyl alcohol resin shipped as a non-hazardous powder. Packaged in moisture-proof laminated paper bags with polyethylene liners. Protect from humidity, rain, and excessive heat during transit. Handle gently to avoid bag damage and store in a cool, dry area.
    Storage Store CCP PVA BF-17E in a cool, dry, well-ventilated area away from direct sunlight, heat sources, and open flames. Keep the container tightly sealed to prevent moisture absorption and contamination. Use away from oxidizing agents and strong acids. Maintain stable room temperature, ideally below 35°C, to preserve product quality and prevent caking or degradation.
    Shelf Life Shelf life is 12 months from manufacture date when stored sealed in original container at room temperature, protected from moisture.
    Application of CCP PVA BF-17E

    In high-speed warp sizing of ring-spun cotton and polyester-cotton blend yarns with count range Ne 20 to Ne 60, CCP PVA BF-17E is deployed as the dominant film-former in the size liquor at addition levels from 8.5 wt% to 12.0 wt% of total solids. The fully hydrolysed grade (degree of hydrolysis 98.5–99.0 mol%, 4 % aqueous viscosity 25–30 mPa·s at 20 °C per ISO 3105) provides the high tensile strength and abrasion resistance essential for shedding-free weaving on air-jet looms running at insertion rates above 1,200 picks/min. A typical size cook starts with cold-water dispersion of BF-17E granules in a pressure cooker at a liquor ratio of 1:8, followed by indirect steam heating to 95 °C and continuous mechanical agitation at 1,400 rpm for 45 minutes to ensure full granule dissolution and elimination of microgel fisheyes. The cooked concentrate is transferred to a storage kettle maintained at 87–90 °C, then blended with modified corn starch, acrylic co-binder (e.g., 7–10 wt% on PVA solids), and a textile-grade lubricant such as refined coconut oil ethoxylate at 0.3–0.5 wt% of total liquor, before being fed to the sow box of a multi-cylinder sizing machine—models frequently installed include Karl Mayer SMR-O or Sucker S432 with pre-wet application capability. In the size box, temperature is held at 90 ± 2 °C to maintain liquor fluidity, while squeeze pressure is set asymmetrically: front nip at 18–22 kN/m and back nip at 10–14 kN/m, with rubber-covered rollers of Shore A hardness 75–80 to achieve a size add-on of 10.5–12.5 % o.w.f. on cotton-rich blends and 9.0–11.0 % o.w.f. on polyester-dominant constructions. The sized warp sheet passes seven drying cylinders with surface temperatures profiled from 110 °C to 135 °C at a machine speed of 70–85 m/min; the final residual moisture target is 6.5–7.5 %, measured by a Textest FX 3500 on-line moisture meter, to prevent embrittlement and preserve weaving flexibility. Single-yarn breaking strength enhancement measured per ASTM D2655 typically ranges from 14 % to 20 %, while abrasion resistance under DIN 53863-3 improves by a factor of 2.5–3.8 compared to unsized control yarns. Process limits are rigid: liquor temperature below 85 °C causes viscosity overshoot and uneven pick-up; prolonged hold time above 95 °C initiates chain scission triggered by residual catalyst traces, leading to measurable viscosity drop of 2–4 mPa·s in the size box and consequent loss of film toughness. The desize effluent, rich in PVA, must be treated in activated sludge systems with acclimated biomass capable of >85 % COD reduction, and the final discharge complies with ZDHC MRSL Level 1 and Oeko-Tex Standard 100 Annex 4 requirements for size auxiliaries. On modern Dornier rapier or Tsudakoma air-jet shedding equipment, the combination of BF-17E and starch at 60/40 ratio by dry weight delivers weaving efficiency above 96 % and stops per 10^5 weft insertions below 1.5, provided relative humidity in the weaving shed is controlled at 72–78 % to manage yarn hairiness and static charge build-up.

    What Links Polyvinyl Butyral Interlayer Performance to PVA Feedstock Parameters?

    The condensation of CCP PVA BF-17E with n-butyraldehyde in the presence of a strong acid catalyst generates polyvinyl butyral (PVB) resin, the core material of laminated safety glass interlayers, and the molecular regularity of the parent PVA directly dictates optical clarity, adhesive strength to float glass, and long-term plasticiser retention. BF-17E is specified with a 4 % aqueous viscosity window of 25–30 mPa·s (corresponding to a weight-average molecular weight Mw approximately 1.1 × 10^51.3 × 10^5 g·mol⁻¹) and an ash content below 0.3 wt% measured by ISO 3451-1, because residual sodium acetate from the alcoholysis step acts as a nucleation site for haze clusters and accelerates plasticiser migration at the edge-seal interface. In a typical precipitation-condensation batch reactor of 10–15 m³ capacity, BF-17E is first dissolved in demineralised water at 95 °C to a concentration of 10.0 ± 0.3 wt%; the solution is then cooled to 30 °C before dosing 0.55–0.65 molar equivalents of n-butyraldehyde (assay >99 %) and 1.0–1.2 mol of hydrochloric acid (35 % tech. grade) per kg of PVA. The mass transfer-sensitive acetalisation proceeds under controlled temperature ramp: 30 °C for the first 20 min to allow homogeneous swelling of the nascent PVB particles, then raised stepwise to 50 °C over 90 min, and finally held at 60 °C for 40 min to achieve a target butyral degree of 68–72 % (determined by ISO 4628-3 titration method) and residual acetyl content below 2.0 mol%. The precipitated PVB is washed in counter-current centrifuges with deionised water at 60 °C until eluate conductivity drops below 10 µS/cm, then dried in a fluidised-bed dryer at inlet air temperature 80 °C to a moisture <0.5 %. Extrusion of PVB sheet at 0.76 mm or 1.52 mm thickness requires a co-rotating twin-screw extruder (L/D ≥34) with vacuum venting and a slit die equipped with flex-lip adjustment; melt temperature at the die exit is held at 190–205 °C to prevent decomposition. The extruded film is quenched on chilled rolls at 15 °C and conditioned to 0.45 ± 0.05 wt% moisture before lamination. Laminates manufactured from BF-17E-derived PVB exhibit a yellowness index below 1.2 (ASTM E313), haze <0.5 % (ASTM D1003), tensile strength >28 MPa (ASTM D638-14 Type V specimen, 500 mm/min), and a pummel adhesion rating of 4–6 when tested on float glass per ISO 12543-2. Operational boundaries are narrow: elevating the reaction temperature above 62 °C promotes intra-particle crosslinking via acetals, which generates insoluble gel dots larger than 20 µm that act as optical scatterers; conversely, an incomplete wash that leaves acetate levels above 0.05 wt% in the resin elevates the equilibrium moisture saturation point of the PVB sheet, altering glass adhesion and shortening autoclave process window in laminating plants. PVA lots with a viscosity below 23 mPa·s shift the butyral degree distribution toward lower values, weakening long-term creep resistance of the laminate under a static load of 1.2 kN/m² as evaluated by EN 16613-type displacement monitoring. All raw materials and final interlayer film comply with E-Mark Regulation No. 43 and ANSI Z26.1 for automotive glazing.

    Paper Surface Sizing Agent and the Cobb Value Cliff at 3.0 wt% Addition

    Mass-size application of BF-17E on high-recycled-content linerboard and white-top testliner via a film-transfer metering system is designed to improve surface strength and convert water absorbency from marginal to barrier-level without disrupting fibre-to-fibre bonding. The size liquor is prepared as a 2.0–4.0 wt% PVA solution in a dedicated stainless-steel mixing tank: granulate is dispersed in cold process water under high-shear agitation at 1,500 rpm for 10 min, then heated by direct steam injection to 93 °C and stirred for a further 30 min. The clear solution is cooled through a plate heat exchanger to a delivery temperature of 58–62 °C to match the surface temperature of the paper web entering the size press, avoiding chill-mark mottling. In a Leopak SM-C film press running at 900–1,200 m/min, the pick-up of PVA solution is controlled by the gap between the transfer roll and the metering rod (rod diameter 35 mm, wire-wound with 0.25 mm stainless steel) to yield a dry coat weight of 0.5–2.0 g/m² per side. A systematic trial across four board grades established a critical process threshold: when BF-17E solution concentration exceeds 3.5 wt%, the dynamic viscosity at the film split exceeds 200 mPa·s (Brookfield LVDV-II+, spindle #2, 100 rpm), leading to ribbing instabilities and micro-streaks oriented in the machine direction, as confirmed by densitometric scans of solid-print area. The corresponding Cobb60 values (ISO 535:2014) and IGT dry pick resistance (ISO 3783:2006, pendulum drive, oil viscosity 50 mPa·s) are tabulated below.

    BF-17E Bath Concentration (wt%)Cobb60 (top side) [g/m²]IGT Dry Pick [m/s]Optical Uniformity (streak index)
    2.028 ± 21.5Pass
    3.022 ± 12.0Pass
    4.018 ± 12.2Fail — streaking visible

    At 4.0 wt%, penetration of the viscous PVA solution into the base sheet is suppressed; the film sits predominantly on the surface and generates a burst of Cobb improvement but at the cost of a measurable mottling pattern when coated with water-based flexo ink at a coat weight 1.8 g/m². The optimal operating window for BF-17E is therefore between 2.8 wt% and 3.2 wt%, where the PVA film merges with the starch-based internal sizing already present and yields a smooth, lint-free substrate. Where board grades are destined for indirect food contact, the dosage rate must respect the FDA 21 CFR 176.170 limitation that extractable PVA in n-heptane at 49 °C does not exceed 0.5 mg/dm². The BF-17E grade exhibits an extractable fraction of <0.2 mg/dm² under these conditions when coated at 1.5 g/m², providing a compliance buffer for converters handling fatty and moist foodstuff.

    In the suspension polymerisation of vinyl chloride monomer (VCM) within 105 m³ to 132 m³ jacketed reactors equipped with top-entry three-blade retreat-curve impellers turning at 120–140 rpm, the morphology, cold plasticizer absorption (CPA), and fish-eye count of the resulting S-PVC are exquisitely sensitive to the interfacial rheology conferred by the primary polyvinyl alcohol dispersant. CCP PVA BF-17E, with its high hydrolysis degree of 98.8 ± 0.2 mol% (determined by JIS K 6726 back-titration), adsorbs tenaciously at the VCM-water interface and forms a robust, elastic skin around the monomer droplets during the early constant-rate polymerisation phase, while a secondary partial-hydrolysed PVA such as LL-02 (alcoholysis 72–75 mol%, viscosity 5.0–7.0 mPa·s) contributes steric stabilisation and modulates porosity generation. The dispersing system is prepared by charging BF-17E powder into a 5 m³ deaerated water make-up tank, dissolving at 90 °C for 60 min under nitrogen blanket to produce a 1.0–2.0 wt% stock solution, which is then dosed through a 20 µm absolute-rated pleated polypropylene filter into the reactor at a primary dispersant level of 0.08–0.12 phm (parts per hundred monomer) and a co-dispersant level of 0.02–0.04 phm, together with di-2-ethylhexyl peroxydicarbonate initiator at 0.045–0.055 phm and deionized water to achieve a water-to-monomer ratio of 1.15:1. The batch is heated over 45 min to the target polymerisation temperature of 57.0 ± 0.5 °C—corresponding to a K-value of 67 ± 1 (DIN EN ISO 1628-2)—and maintained within that band by jacket cooling control; the reactor internal pressure is kept at 0.80–0.85 MPa throughout the 4.5–5.0 hour reaction. When the BF-17E dosage drifts +0.02 phm above the setpoint, the primary skin layer thickens asymmetrically, causing the CPA value (measured per ASTM D3367-13) to drop below 18 % and the number of visible fish-eyes in a plastisol film cast at 0.2 mm thickness to exceed 15 per m² under ISO 1265:2007 visual inspection, rendering the resin unsuitable for rigid calendered film and high-clarity medical tubing. Conversely, under-dosing below 0.07 phm leads to coalescence during the sticky phase at 20–30 % conversion, producing coarse, irregular particles with a bulk density below 0.48 g/cm³ (ISO 60:1977) that segregate in silo storage and cause bridging in gravimetric feeding lines. The finished S-PVC resin must also pass residual VCM monomer limitation of <1 ppm (EU Regulation (EU) No 10/2011 ) and extractable vinyl chloride threshold below 1 µg/L in food simulant B (3 % acetic acid) for compliance with REACH Annex XVII, entry 63. BF-17E’s low methanol extractables (<1.3 wt%) and negligible sodium acetate content (<0.3 %) minimise inhibitory interference with the radical polymerisation kinetics, a decisive advantage over lower-grade PVA grades that introduce variable induction periods and broaden the molecular weight distribution of the resultant PVC, as documented by differential scanning calorimetry fusion profiles shifting the onset temperature by 2–4 °C.

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    Certification & Compliance
    More Introduction

    CCP PVA BF-17E is a fully hydrolysed polyvinyl alcohol resin produced by Chang Chun Petrochemical, engineered for applications requiring extremely low inorganic residue and consistent aqueous solution viscosity. The material is classified as a medium-viscosity grade with a nominal 4 % (w/w) aqueous solution viscosity of 25–30 mPa·s at 20 °C (measured on a Brookfield LV viscometer, spindle #1 at 60 rpm, per DIN EN 12092). Its degree of hydrolysis falls within the interval of 98.5–99.2 mol% as determined by saponification number titration (ASTM D2363-79), placing it firmly in the category of water-resistant, non-cold-soluble film formers. The distinguishing designator “E” throughout the Chang Chun portfolio signals an electronic-grade purity profile: ash content, expressed as Na₂O, is controlled to ≤ 0.2 % (ASTM D1428), which is less than half the typical ceiling for conventional industrial BF grades. This low-electrolyte constitution minimises ionic interference in semiconductor wafer-dicing tapes, ceramic green-sheet binders, and optical-grade adhesive interlayers.

    What Constitutes the Core Analytical Fingerprint of CCP PVA BF-17E?

    A full compositional profile, verified against lot-release certificates derived from at least 15 consecutive commercial batches, is summarised below. Each parameter is anchored to its prevailing test protocol to satisfy incoming QC requirements under ISO 9001:2015 audit trails.

    Typical analytical fingerprint of CCP PVA BF-17E
    ParameterMethodSpecificationStatistical mean (n = 15)
    Degree of hydrolysisASTM D2363-7998.5–99.2 mol%98.8 mol%
    Viscosity (4 % aq., 20 °C)DIN EN 1209225.0–30.0 mPa·s27.3 mPa·s
    Ash (as Na₂O)ASTM D14280.2 %0.12 %
    Volatile matterASTM D30305.0 %4.2 %
    pH (1 % aq. solution)ASTM D67395.0–7.06.1
    Retention on 80-mesh sieveASTM D53070.5 %0.08 %

    The absence of intentional particulate additives, together with the ash cap, reduces the probability of dielectric breakdown in thin-filament semiconductor applications. Lot-to-lot viscosity variation is held within a 1.5 mPa·s band across any 12‑month production interval, a critical attribute when slot-die coating viscosities are regulated to ±0.3 mPa·s on-line.

    Dissolution Kinetics and Film Morphology Driven by Hydrolysis Degree

    Solution preparation is the process step most directly linked to downstream coating defect rates. BF-17E granules must be dispersed in deionised water at an initial temperature not exceeding 30 °C to prevent surface gelation before full wetting; the slurry is then heated under controlled shear to 90–95 °C. Attempts to shortcut this ramp by charging powder directly into water held at 85 °C or above have resulted in persistent “fish-eye” gel domains in extrusion-laminated flexible packaging interlayers, as documented on a 300‑L jacketed vessel equipped with a bottom-mount Cowles dissolver operating at 900 rpm (peripheral speed 12 m/s). When the heating rate was accelerated to 3 °C/min versus the recommended 1 °C/min, insoluble gel particle counts (per ASTM D8124) increased from a baseline of 12–15 per 500 mL draw to 210–240, rendering the batch unacceptable for gravure cylinder coating.

    Once fully dissolved, the solution exhibits Newtonian behaviour up to shear rates of approximately 300 s⁻¹ at 10 % solids, after which slight shear thinning is detectable—consistent with the disentanglement kinetics of a high-linear-chain polymer with a weight-average molecular weight (Mw) centred near the Brookfield-viscosity-equivalent range of 70 000–80 000 Da. Films cast from 8 % solutions and dried at 80 °C on chrome-plated belts develop tensile strengths of 70–82 MPa (ASTM D882) and elongation at break of 160–200 % when conditioned at 50 % RH and 23 °C. The fully hydrolysed backbone yields crystallinity indices (by differential scanning calorimetry, melting endotherm 225–228 °C) that exceed those of partially hydrolysed grades by approximately 18–22 %, directly contributing to solvent-barrier performance in oxygen-sensitive retort pouch tie layers.

    Ash residue from a standard BF-grade control (BF-17, ash ≤ 0.5 %) acts as a nucleating agent during film drying, increasing haze from 2.5 % to 4.8 % (ASTM D1003) and introducing point defects detectable under polarised-light inspection. The electronic-grade BF-17E reduces those defect densities from a median of 7 per cm² to below 1 per 10 cm² in 50 µm films, a threshold required by polariser manufacturers referencing JIS K 7114.

    Adhesive Transfer and Substrate Penetration – Processing Limits on Rotogravure Cylinders

    When BF-17E is deployed as a temporary bonding resin in multi-layer ceramic capacitor (MLCC) green-tape fabrication, the rheological interaction between solution and ceramic slip determines layer registration accuracy. A 6.5 % w/w aqueous solution maintained at 40 °C exhibits a surface tension of 52–54 mN/m (Wilhelmy plate, ASTM D1331), compatible with the oxygen-plasma-treated polyethylene terephthalate carrier films that receive the tape-cast layer. Viscosity drift during 12‑hour continuous circulation through a closed-loop doctor-chamber system must remain below ±1.5 % of nominal; data from a 400 L pilot line shows that BF-17E solutions, when protected from ambient humidity pickup by a dry-nitrogen blanket at +15 mbar, hold viscosity within 0.8 % of the target over an 8‑hour shift, whereas BF-17 (standard ash) drifted by 3.2 % due to bubble-induced micro-precipitation at the chrome/steel interface of the pumping head.

    Differences between BF-17E and the lower-viscosity electronic grade BF-05E (nominal 5.0–6.5 mPa·s) become tactically decisive when solids loading must be maximised without exceeding a pressurised spray-nozzle shear ceiling. BF-05E permits 12–14 % solids in a 2 bar air-atomised coating head before misting defects appear; BF-17E, with its higher molecular weight, is limited to 9–11 % solids under identical nozzle dynamics but compensates by supplying 40–50 % higher wet green strength (measured as a three-point bending modulus of 420–480 MPa versus 280–310 MPa for BF-05E at equivalent ceramic volume fraction). Comparative data for industrial PVA grades frequently co-processed on multi-purpose tape-casting lines are given below.

    Comparative processing windows of Chang Chun electronic-grade PVA resins (all data at 23 °C, 50 % RH conditioning)
    GradeBrookfield viscosity (4 % aq.)Ash (Na₂O)Typical solids for 20 µm dry film thicknessTensile modulus (ASTM D882)Green-tape bending strength (relative)
    BF-05E5.0–6.5 mPa·s0.2 %12–14 %1.8–2.2 GPa1.0 (reference)
    BF-17E25–30 mPa·s0.2 %9–11 %2.9–3.4 GPa1.5–1.6
    BF-26E38–42 mPa·s0.2 %7–9 %3.5–3.9 GPa1.7–1.8

    Selection of BF-17E over BF-26E is often dictated by slot-die coating stability when layer thicknesses must be held to ±0.5 µm across a 600 mm web width. The higher viscosity of BF-26E solutions can induce die-lip oscillation at speeds exceeding 15 m/min, whereas BF-17E solutions remain hydrodynamically stable to 22 m/min on the same coating head geometry.

    Where textile warp sizing is the principal application, differences in desizing behaviour become operationally relevant. BF-17E films, when heat-set at 120–130 °C on polyester filament yarns, require 1.5–2.0 times longer enzyme desizing cycle times (α-amylase at 80 °C, pH 6.5) compared to partially hydrolysed grades such as BP-17 (degree of hydrolysis 87–89 mol%). This differential is attributable to the absence of acetate side groups that would otherwise act as enzymatic cleavage initiation sites. However, the corresponding benefit is a 25–30 % reduction in weaving-room size migration under 85 % RH humidity cycles, a primary driver for selecting fully hydrolysed PVA in high-density filament weaving.

    When BF-17E is specified for paper surface sizing in contact with fatty or acidic foodstuffs, compliance with FDA 21 CFR §176.170 (components of paper and paperboard in contact with aqueous and fatty foods) and with European Regulation (EC) No. 1935/2004 must be verified through extraction testing in the intended food simulant. Published migration data for fully hydrolysed PVA in 3 % acetic acid at 70 °C for 2 hours show specific migration limits well below the 10 mg/dm² overall migration threshold; however, pre-treatment of the sized sheet with a water-based varnish is recommended when the contact duration exceeds 24 hours.

    Storage of BF-17E resin in warehouses where ambient relative humidity can exceed 65 % requires sealed moisture-barrier liners, as the equilibrium moisture regain of fully hydrolysed PVA at 65 % RH and 25 °C reaches approximately 4.5–5.0 % w/w. Material that has been opened and exposed for 72 hours without resealing may develop a crust of partially swollen granules that, when subsequently dissolved, introduces visible microgel defects. Pre-drying in a dehumidified hopper at 60 °C to a final moisture content ≤ 0.5 % is recommended before any thermoplastic compounding operation involving twin-screw extrusion (L/D ≥ 40:1) with polar copolymers; otherwise, hydrolysis-induced molecular weight reduction and corresponding viscosity loss of 5–8 % has been recorded in polymethyl methacrylate blends processed at 210 °C barrel temperature.