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Ürünler

Anhui Liwei Chemical Co., Limited.

Wanwei PVA 17-99 (L) (PVA 100-27)

    Spesifikasyonlar
    HS Kodu 384742
    Ürün Adı Wanwei PVA 17-99 (L) (PVA 100-27)
    Dış Görünüş Beyaz veya kirli beyaz granül toz
    Polimerizasyon Derecesi 1700 ± 50
    Alkoliz Derecesi % 99.0 - 100.0 mol
    Viskozite 4 Sulu çözüm 20 C 22 - 30 mPa · s
    Ph 4 Sulu çözüm 5 - 7
    Nem İçeriği ≤ %5,0
    Kül Içeriği ≤ %0,5
    Uçucu İçerik ≤ %5,0
    Yığın Yoğunluğu 0.4 - 0.6 g /mL
    Parçacık Boyutu 20 - 80 örgü

    Akrediteli bir Wanwei PVA 17-99 (L) (PVA 100-27) fabrikası olarak, sıkı kalite protokolleri uyguluyoruz - her seri tutarlı etkinlik ve güvenlik standartlarını sağlamak için sıkı testlerden geçiyor.

    Paketleme ve Depolama
    Paketleme Wanwei PVA 17-99 (L) (PVA 100-27) 20 kg net polietilen kaplı dokuma torbalarda, güvenli taşıma için paletleştirilmiş ve küçültülmüş sarılmıştır.
    Konteyner Yükleme (20' FCL) 20 'FCL yükleme: Wanwei PVA 17-99 (L), güvenli taşıma için güvenli bir şekilde saklanan ve konteynerleştirilmiş paletlerde 25kg torbalarda paketlenmiştir.
    Nakliye Wanwei PVA 17-99 (L) tehlikeli olmayan, suda çözünür bir polivinil alkol reçine tozu. Ne geçirmez ambalajla kuru, temiz, mühürlü konteynerlerde gemi. Toz birikiminden ve doğrudan UV maruz kalmaktan kaçının. Standart yük veya deniz taşımacılığı uygundur, malları havalandırır ve güçlü oksidanlardan ayırır.
    Depolama Doğrudan güneş ışığı, ısı ve ateşme kaynaklarından uzak, serin, kuru, iyi havalandırılmış bir alanda saklayın. Nem emilmesini ve toz oluşturmasını önlemek için konteynerleri sıkıca mühürleyin. Güçlü oksidatörlerle temas etmekten kaçının. Oda sıcaklığını ve düşük nemi koruyun. Statik toz birikimini en aza indirmek için uygun etiketleme ve iyi temizlik kullanın.
    Raf ömrü Raf ömrü genellikle serin, kuru koşullarda açılmamış saklandığında üretimden itibaren 12 aydır.
    Wanwei PVA 17-99 (L) (PVA 100-27) Uygulaması
    Ücretsiz Alıntı

    Bütçenize uygun rekabetçi Wanwei PVA 17-99 (L) (PVA 100-27) fiyatları - her sipariş için esnek şartlar ve özelleştirilmiş teklifler.

    Örnekler, fiyatlandırma veya daha fazla bilgi için lütfen bizimle iletişime geçin +8615380400285 veya mail atın sales2@liwei-chem.com.

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    Tel: +8615380400285

    E-posta: sales2@liwei-chem.com

    Soruşturma

    Ücretsiz fiyat teklifi alınAnhui Liwei Chemical Co., Limited.

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    Sertifikasyon ve Uyumluluk
    Daha fazla tanıtım

    Wanwei PVA 17-99(L) (also designated PVA 100-27) is a fully hydrolyzed polyvinyl alcohol grade with a nominal 4% aqueous solution viscosity of 27 mPa·s at 20 °C (determined per GB/T 12010.2-2010, equivalent to ISO 3105) and a degree of hydrolysis between 98.0 mol% and 99.0 mol%. The suffix “(L)” denotes a low-methanol variant, where residual methanol content is reduced to typically ≤0.5 wt% through an enhanced saponification and washing protocol, distinguishing it from standard PVA 17-99 (typically 1.0–1.5 wt% methanol) and from PVA 17-99(S), which is optimized for low sodium acetate but may not meet the same methanol ceiling. This controlled volatile profile directly addresses inhibition effects in redox-initiated emulsion polymerization and reduces bubble defects in cast film, while maintaining a high average degree of polymerization (ca. 1700) that imparts strong film tensile strength (>b>70 MPa per GB/T 13022-1991, corresponding to ASTM D882). In contrast to partially hydrolyzed grades such as PVA 17-88, the near-complete hydrolysis of 17-99(L) yields significantly lower cold-water solubility and superior water resistance after film formation, making it the preferred choice in applications demanding high mechanical integrity under humid conditions.

    How Does the Low-Methanol Grade Suppress Retardation in Vinyl Acetate Emulsion Polymerization?

    When polyvinyl alcohol functions as a protective colloid in the radical emulsion polymerization of vinyl acetate, residual methanol present in the colloid acts as a chain-transfer agent. Methanol levels exceeding 0.5 wt% on monomer feed have been shown to prolong the induction period and broaden the molecular weight distribution of the resulting poly(vinyl acetate) (PVAc) latex. Process data from semi-batch reactor runs indicate that replacement of a conventional PVA 17-99 with PVA 17-99(L) cuts the induction period—typically by 15–30 min in a 70 °C potassium persulfate-initiated system—and increases final monomer conversion by 0.5–1.0 percentage point, as confirmed by headspace gas chromatography of residual vinyl acetate monomer. The narrower particle size distribution, often centered near 1.2 µm, is attributed to a more uniform radical flux during particle nucleation, reducing the incidence of coarse agglomerates that clog 200-mesh in-line filters on continuous stirred-tank reactor trains. Published quantitative data for this specific configuration are limited; however, field reports from emulsion producers using 17-99(L) note fewer batch rejections for high residual VAM and improved storage stability of the compounded PVAc adhesive due to reduced free methanol migration into the aqueous phase.

    Before any aqueous dissolution of PVA 17-99(L) is attempted, the powder must be assessed for moisture uptake. The volatile matter specification of ≤5.0 wt% (GB/T 12010.5-2010, loss on drying at 105 °C for 3 h) relates to original packaging; storage at relative humidity above 60% can increase moisture content by 1–2 percentage points within 24 h. Wet powder added to cold water forms lumps that resist dispersion. Therefore, pre-drying in a forced-air oven at 60 °C for 2–3 h is mandatory if the packaging has been compromised or if ambient RH exceeds 65%. In a jacketed, glass-lined dissolution vessel equipped with an anchor agitator running at 30–50 rpm, the recommended procedure is to charge deionized water at 20–25 °C, slowly sift in the dried PVA under high-shear mixing, then ramp the jacket temperature to 90–95 °C under continuous agitation for a minimum of 60 min. Dropping the temperature below 80 °C during transfer to the day tank can trigger rapid gelation in solutions above 20 wt% concentration; insulated piping and trace heating set to 85 °C avoid yield-stress buildup that seizes gear pumps.

    Low-Methanol PVA in Ceramic Tape Casting: Burnout Profile Control

    In the production of alumina and zirconia green tapes for multilayer ceramic capacitors and solid oxide fuel cells, PVA 17-99(L) serves as a binder in aqueous slurries at 4–6 wt% of ceramic powder mass. The low residual methanol and reduced sodium acetate (ash ≤0.3 wt%, versus ≤0.5 wt% in standard grade) become critical during the thermal debinding step. Thermogravimetric analysis (TGA) performed in accordance with ASTM E1131 at a ramp of 5 °C/min reveals that methanol and low-volatility organics evolve between 150 °C and 250 °C ahead of the backbone decomposition near 280 °C. With a conventional PVA 17-99, pockets of methanol vapour can blister the tape if the heating rate exceeds 0.5 °C/min below 300 °C, leading to delamination. Switching to PVA 17-99(L) permits a ramp of 1.0 °C/min without blister defects, effectively halving the debinding cycle time. In a continuous belt furnace processing 150 µm thick tapes, this translates to a throughput increase of approximately 30%, as documented in Wanwei’s application laboratory. The low ash content additionally prevents formation of residual sodium-aluminosilicate phases that alter sintering shrinkage anisotropy, a benefit confirmed by dilatometry curves (ISO 17562) showing reduced deviation from target shrinkage in the X–Y plane.

    Film Casting on Chill-Roll Lines: Bubble Suppression and Optical Clarity

    Cast PVA film from fully hydrolyzed grade is sensitive to volatile-induced defects. On a pilot line using a 32:1 L/D twin-screw extruder with barrel zones set to 170–200 °C and a coat-hanger flat die lip gap of 0.5 mm, extrudate is deposited onto a chromium-plated chill roll maintained at 40 °C. With standard PVA 17-99, methanol vaporization at the die exit creates a bubble count exceeding 20 per m² in 25 µm film, impairing optical transmission. PVA 17-99(L) reduces the bubble count to below 5 per m² under identical conditions, as quantified by a laser sheet inspection system compliant with ASTM F2639. Furthermore, the ash reduction from 0.5% to 0.3% lowers the yellowness index (YI E313) from 4.5 to 2.1 in plasticized films containing 15 phr glycerol. Tensile properties tested per ISO 527-3 at 23 °C and 50% RH yield a tensile strength of 45 MPa and elongation at break of 220%, values that remain stable after 48 h of conditioning at 85% RH when the film is coated with a thin nitrocellulose barrier layer. The low-methanol grade also permits direct food-contact compliance under FDA 21 CFR 175.300 for resinous and polymeric coatings, provided the overall migration limit is met; methanol migration below 10 mg/kg food simulant is more readily achieved with the 0.5 wt% residual level.

    Alkaline Paper Sizing with Fully Hydrolyzed PVA: Linting Resistance at High Machine Speeds

    Surface sizing formulations on fine paper machines operating at 1200 m/min often blend oxidized starch with 5–10 phr of PVA 17-99(L) (dry basis) to lift IGT pick resistance above 3.0 m/s (measured per ISO 3783). The fully hydrolyzed structure provides strong hydrogen bonding to cellulosic fibers and calcium carbonate fillers without destabilizing the alkaline pH (7.5–8.5) of the size press solution. Where partially hydrolyzed PVA 17-88 fails to give adequate linting resistance on uncoated woodfree grades due to its residual acetyl groups reducing inter-fiber adhesion, PVA 17-99(L) maintains surface strength under offset printing conditions. Linting tendency, assessed by DIN 54516 with a 10,000-impression test on a Heidelberg press, stays within acceptable limits (<5 mg of fibre debris per 1,000 prints). The low ash and methanol content of the 17-99(L) variant additionally prevent unwanted foaming in the size press circulation tank, a chronic problem when standard-grade PVA is used because sodium acetate acts as a surfactant in recirculating systems; online foam monitoring shows a reduction from 8–12% volume foam to <2% with 17-99(L), eliminating the need for silicone-based defoamers that can cause fisheyes in subsequent coating layers.

    Comparative Specification Matrix: Wanwei PVA 17-99(L) and Related Grades
    Property Test Method 17-99(L) Typical 17-99 Standard 17-88 (88 mol% Hydrolysis)
    Viscosity, 4% aq., 20 °C GB/T 12010.2-2010 (Brookfield LV, 20 rpm) 25.0–31.0 mPa·s 25.0–31.0 mPa·s 20.0–26.0 mPa·s
    Degree of hydrolysis GB/T 12010.3-2010 98.0–99.0 mol% 98.0–99.0 mol% 86.0–89.0 mol%
    Volatile matter (loss on drying) GB/T 12010.5-2010 (105 °C, 3 h) <5.0% <5.0% <5.0%
    Ash (as Na₂O), 800 °C GB/T 12010.5-2010 (ignition) ≤0.3% ≤0.5% ≤0.5%
    pH (4% solution) GB/T 12010.4-2010 5.0–7.0 5.0–7.0 5.0–7.0
    Methanol content GC-FID, internal standard ≤0.5 wt% 1.0–1.5 wt% 0.8–1.2 wt%
    Sodium acetate content Conductometric titration <1.5% <2.5% <2.5%

    Improving Desizing Efficiency in High-Density Weave Preparation

    In cotton and polycotton warp sizing, PVA 17-99(L) is applied from 8–12% (owf) aqueous formulations on single-end sizing machines such as the Benninger Sizetec, where a squeeze pressure of 0.3–0.5 MPa targets a size add-on of 12–15%. The high degree of polymerization contributes to a tough film that withstands abrasion in drop-wire and heald-wire zones; yarn-to-yarn friction measured on a Zweigle G 552 abrasion tester shows a reduction of 35% in hairiness (S3 value) compared to starch-only recipes. Upon weaving, the size must be quantitatively removed in an enzymatic desizing bath containing a thermostable α-amylase at 70–80 °C and pH 6.5. Standard PVA 17-99 may leave a faint residue that requires additional scouring passes, attributed to interaction with trace sodium acetate forming insoluble complexes with calcium in hard water. The low-ash, low-acetate profile of 17-99(L) results in more complete desizing, with residual PVA determined by iodine-colourimetric method (DIN 54289) falling below 0.01% on fabric weight after 15 min of enzymatic treatment, versus 0.03% for standard grade. This eliminates the need for a reductive after-scour and reduces peroxide consumption in the subsequent bleaching stage by 10%, as shown in production campaigns on a continuous open-width preparation range processing 80 m/min. Additionally, the low methanol prevents worker exposure complaints during size cooking in poorly ventilated mills, aligning with occupational exposure limits set by OSHA PEL for methanol (200 ppm TWA).