| HS Kodu | 337439 |
| Kimyasal Adı | polivinil alkol |
| Cas Numarası | 9002-89-5 |
| Kimyasal Formül | (C2H4O) n |
| Dış Görünüş | Beyaz granül toz |
| Hidroliz Derecesi | 99,9 mol% (tam hidroliz) |
| Viskozite | 60-70 mPa·s (% 4 sulu çözüm, 20 ° C) |
| Ph | 5-7 (% 4 sulu çözüm) |
| Uçucu İçerik | ≤%5,0 |
| Kül Içeriği | ≤%0,5 |
| Su çözünürlüğü | Sıcak suda çözünür; soğuk suda hafifçe çözünür; çoğu organik çözücüde çözünmez |
| Yoğunluk | 1.19-1.31 g /cm³ |
| Erime Noktası | 230 ° C (bozulma) |
Akredite bir Sinopec PVA 100-60'ı fabrikası olarak, katı kalite protokolleri uyguluyoruz - her seri tutarlı etkinlik ve güvenlik standartlarını sağlamak için katı testlerden geçiyor.
| Paketleme | Sinopec PVA 100-60, koruma için iç plastik astar ile 25 kg çoklu duvarlı kağıt torbalarda paketlenmiştir. |
| Konteyner Yükleme (20' FCL) | Sinopec PVA 100-60, konteyner başına yaklaşık 20 metrik ton, 20' FCL olarak yüklenen paletlerde 25kg torbalarda paketlenmiştir. |
| Nakliye | Sinopec PVA 100-60 (polivinil alkol) tehlikeli olmayan kargo olarak 25 kg çok katmanlı kağıt torbalarda, nem koruması için paletli ve sarılmıştır. Standart konteynerler transit sırasında nem maruz kalmasını önler. Kuru, temiz ve doğrudan ısıdan uzak tutun. Genel deniz veya kara taşımacılığı için özel tehlikeli mallar beyan gerekmez. |
| Depolama | Sinopec PVA 100-60'ı ısıdan, açık alevlerden ve doğrudan güneş ışığından uzak serin, kuru, iyi havalandırılmış bir alanda saklayın. Nem emilmesini ve kirlenmeyi önlemek için konteyneri sıkıca mühürleyin. Toz birikmesinden ve statik boşaltmadan kaçının. Oksidan maddelerden ve uyumsuz kimyasallardan ayrı saklayın. Orijinal ambalajı kullanın ve güvenli kullanım için yerel düzenlemeleri izleyin. |
| Raf ömrü | Raf ömrü, sızdırılmış, soğuk ve kuru saklandığında genellikle üretimden iki yıldır. |
Modern bir slasher boyutlama hattında 40/1 Ne pamuk iplikleri 650-750 ışın başına uçları ve 80 ile 120 m/dakika arasındaki çalışma hızları ile işleme 80 ile 120 m/dakika arasında, boyut kutusu tamamen hidroliz edilmiş PVOH'nin derilenmesini önlemek için 85-92 ° C sıcaklığını korumalıdır. Sinopec PVA 100-60, hidroliz derecesi ≥99 mol% ve 4% suyu çözüm viskozitesi 58.0-68.0 mPa · s 20 ° C önceden çözünür 500-1000 L düşük kesimli çapa agitatörü ve buharlı bir parçalanma halkası ile donatılmış bir 500-1000 L kaplı pişirme su ısıtıcısında çözünür. Kuru PVA granülleri ilk önce soğuk süreç suyunda 1: 8 oranında dağılır ve ardından en az 90 dakika boyunca 95±2 ° C agitasyon altında ısıtılır. Pişirilen 10-12% katı maddeler PVOH stok çözümü, daha sonra 25-45% PVOH içeren son boyut karışımı elde etmek için ayrı bir jelatinize edilmiş oksitlenmiş mısır nişastası bulamaşıyla karıştırılır, kuru katı maddelerde 0.3-0.8% (boyutlu katı maddelerde) yüksek eriyen bir parafin balmumu emülsiyonu ve 0.1-0.3% etoksil yağ asiti antistatik yağlayıcı ile tamamlanır. Boyut alımı, 12–18 kN/m basıncında çift sıkmalı bir silindir nip yoluyla kontrol edilir ve halka içilmiş pamuk için 8–14% kuru bir ekleme hedeflenir. Boyutlu warp kirişi, film kabarcıklamasını önlemek ve kalıntı nem içeriğini 6,5%'nin altında tutmak için son silindirlerde 95°C'ye indirmek için ilk üç kutunun 110°C'de tutulduğu çok silindirli kurutma bölümünde kurutulur. 100-60 ile ölçüleme, tipik olarak ASTM D2256-21 ile ölçüldüğü gibi, tek uçlu çekme mukavemetini 18-28% boyutu olmayan ipke göre yükseltirken, Zweigle G551 testeri tarafından aşınma direnci 35-60% iyileşir. Operasyonel sınır koşulları sıkıdır: boyut kutusu pH 5.5 ve 7.0 arasında kalmalıdır, çünkü 7.5 üzerindeki alkali geziler, sert su kullanılırsa borat veya kalsiyum iyon köprülemesi yoluyla ilerilecek jelasyona neden olur; Bor içeren sonraki tedaviler uyumsuz. Bitmiş kumaşta desizing, hidrojen peroksit kullanarak oksidatif pad-buhar işlemi ile 2
Bütçenize uygun rekabetçi Sinopec PVA 100-60'ı fiyatları - her sipariş için esnek şartlar ve özelleştirilmiş teklifler.
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Sinopec PVA 100-60 is a fully hydrolyzed polyvinyl alcohol resin manufactured by Sinopec Sichuan Vinylon Works. The grade designation encodes its primary molecular attributes: the prefix 100 indicates a hydrolysis degree exceeding 99.0 mol% (nominally 99.0–99.8%), and the suffix 60 corresponds to a Brookfield viscosity of 58–62 mPa·s measured on a 4 wt% aqueous solution at 20 °C per ISO 1652:2020. This viscosity plateau places 100-60 in the medium‑high molecular weight band of the Sinopec fully hydrolyzed portfolio, conferring elevated film toughness, high water‑wet tensile retention, and pronounced thickening efficiency relative to lower‑viscosity analogues such as 100‑27 (27±3 mPa·s) or 100‑37 (37±3 mPa·s).
Sinopec PVA 100-60 is supplied as a white to off‑white granular powder with a bulk density of 0.45–0.60 g/cm³. The volatile matter is held below 5.0 wt% (ASTM D‑4019), and the ash content (as Na₂O) does not exceed 0.5 wt%. The pH of a 4 % aqueous solution falls in the range 5.0–7.0, which minimizes corrosive interaction with metallic substrates during hot‑melt adhesive compounding. Acetate residue, a direct reflection of incomplete hydrolysis, is typically 0.1–0.4 wt% — an order of magnitude lower than the 1.5–2.0 wt% tolerated in 88 mol% partially hydrolyzed grades (Sinopec 200‑series). This residual acetyl content is the dominant structural variable governing cold‑water solubility, tensile modulus development in solution‑cast films, and compatibility with polyol plasticizers.
The polymer backbone is characterized by 1,3‑diol and 1,2‑diol configurations, with syndiotacticity indices influenced by the parent polyvinyl acetate polymerization temperature. For 100-60, the block‑character distribution of residual acetate groups is statistically random rather than blocky, as corroborated by 13C NMR sequencing of carbonyl signals. This randomness suppresses cold‑water swellability, elevates the glass transition temperature (~85 °C dry, ~40–45 °C at 50 % RH), and mandates dissolution temperatures above 90 °C in agitated vessels.
Dry PVA 100-60 grains exhibit negligible water uptake below 70 °C. Complete solubilization in a jacketed turbine‑agitated tank (typical tip speed 1.5–2.0 m/s) demands a 20‑min hold at 90–95 °C under moderate shear (Reynolds number> 10⁴ to prevent gel‑phase accumulation on baffles). When the powder is charged into cold water and subsequently heated, the slurry viscosity passes through a high‑torque gelation window between 60 °C and 80 °C, potentially exceeding 5000 mPa·s on the stirring drive if the concentration exceeds 8 wt%. Production‑scale experience with 100-60 in 15 m³ dispergators equipped with 45° pitched‑blade turbines reveals that uncontrolled temperature ramping during this gelation window has caused repeated shear‑pin failures on agitator shafts. Mitigation involves pre‑wetting the powder in a cold dispersion at <5 wt% solids or adopting a direct‑to‑hot‑water dosing strategy with active vacuum deaeration to remove entrained air, which otherwise nucleates micro‑gel fisheyes in downstream coating operations.
Once fully dissolved, the solution exhibits pseudoplastic behavior with a power‑law index of 0.85–0.95 at 6 wt%. Prolonged exposure to pH <3 at 70 °C triggers progressive acetyl cleavage and an eventual drift in viscosity, while storage at pH 8–10 in the presence of multivalent cations can induce salt‑out coagulation. Biocidal preservation with CMIT/MIT is compatible at 10–50 ppm active, though benzisothiazolinone (BIT) is preferred for systems intended for food‑contact indirect compliance under FDA 21 CFR 175.105.
Thin films obtained by solution casting of 100-60 (10 wt% aqueous, dried at 80 °C for 30 min, then conditioned at 23 °C /50 % RH) develop a tensile strength of 70–85 MPa and an elongation at break of 120–160 % when tested per ASTM D‑882 (50 mm/min crosshead speed). These values are roughly 20–30 % higher than those of 100‑37 films prepared under identical conditions, directly attributable to the higher number‑average degree of polymerization (Dp ≈ 1700–2000 vs. ~1200 for 100-37). The increased chain entanglement density also manifests in a drop of oxygen permeability from 0.99 cm³·mm/(m²·day·atm) (100‑37) to 0.60 cm³·mm/(m²·day·atm) (100‑60) at 0 % RH, as per ASTM D‑3985, making 100-60 the preferred barrier layer for bio‑degradable sachets where moisture‑triggered disintegration must be retarded by at least 48 hours under 85 % RH.
Paper surface sizing with 100-60 at pick‑up levels of 1.5–2.5 g/m² (dry basis) improves the IGT pick resistance (ISO 3783) by 30–40 % over starch‑only control. The critical parameter is the dynamic surface tension of the size press bath, maintained at 45–50 mN/m by adding 0.1–0.3 wt% of acetylene‑diol surfactant on PVA solids. If the viscosity of the 8 wt% solution at 50 °C exceeds 1800 mPa·s, the film‑split pattern transitions from smooth meniscus to ribbed instability, generating cross‑machine variation in Cobb values (ISO 535) of more than ±3 g/m². This condition is specific to 100-60 and its close analogue 100-80; lower‑molecular‑weight grades can be run at 10–12 wt% without ribbing. On‑machine data from a 1250 m/min Jagenberg size press indicate that 100-60 requires a minimum wet‑film split temperature of 45 °C to avoid transfer‑roll gumming, whereas 100-37 can operate as low as 38 °C.
In cotton and cotton‑polyester warp sizing, 100-60 provides a size add‑on of 12–14 % on 40 Ne ring‑spun yarns, yielding weaving efficiency improvements above 95 % on air‑jet looms running at 800 picks/min. The abrasion resistance of the sized yarn, measured as the number of cycles to break on a Zweigle G551 yarn‑on‑yarn abrasion tester, increases by 1.8–2.2× over carboxymethyl starch at identical add‑on. However, the fully hydrolyzed nature of 100-60 demands alkaline‑oxidative desizing: 2–3 g/L NaOH and 0.5–1.0 g/L H₂O₂ at 90 °C for 45 min. If desizing is attempted with hot water alone, residual size levels above 0.15 wt% on fabric weight persist, catalyzing uneven reactive dye uptake in subsequent continuous dyeing (shade variation> ΔE*ab 1.5). This constraint does not apply to partially hydrolyzed grades (Sinopec 200-80), which are cold‑water soluble but deliver lower film toughness.
In cementitious tile adhesives formulated to EN 12004 Class C2, the addition of 0.8–1.2 wt% 100-60 (by dry mix weight) imparts a wet‑adhesion tensile strength greater than 0.5 MPa after 28‑day water immersion. The polymer functions as a secondary rheological thickener, shifting the mortar from a shear‑thinning with yield behavior (Bingham model) to a Herschel‑Bulkley profile with a yield stress of 80–120 Pa. This elevation of yield stress is critical for extended open time: with 1.0 wt% 100-60, the open time (defined as the interval for which pull‑off strength remains >0.5 MPa after 30 min skinning) extends to 40 min at 23 °C/60 % RH. Below 1.0 wt%, the paste exhibits syneresis (bleeding) when placed on low‑porosity porcelain tiles with water absorption <1 %.
Compatibility with calcium aluminate cements (CAC) is sensitive to the PVA hydrolysis degree. 100-60, with its minimal acetate content, resists saponification in the highly alkaline cement pore solution (pH 13.5–14.0) for at least 6 months at 40 °C, as shown by FTIR monitoring of the carbonyl peak at 1735 cm⁻¹. In contrast, 200‑series PVA grades undergo partial saponification within 28 days under the same conditions, releasing acetic acid that lowers the calcium‑silicate‑hydrate (C‑S‑H) chain length and reduces compressive strength by 8–12 %.
| Property | Test Method | 100‑27 | 100‑37 | 100‑60 | 100‑80 |
|---|---|---|---|---|---|
| Degree of hydrolysis (mol%) | ISO 15023‑2 | 99.0–99.8 | 99.0–99.8 | 99.0–99.8 | 99.0–99.8 |
| Viscosity 4% aq., 20°C (mPa·s) | ISO 1652 | 24–30 | 34–40 | 58–62 | 76–84 |
| Dₚ (approx.) | SEC‑MALS | 600–800 | 1100–1300 | 1700–2000 | 2200–2500 |
| Tensile strength film (MPa) | ASTM D882 | 55–65 | 65–75 | 70–85 | 75–90 |
| Elongation at break film (%) | ASTM D882 | 140–180 | 130–160 | 120–160 | 110–140 |
| O₂ permeability (cm³·mm/(m²·day·atm)) | ASTM D3985, 0% RH | 1.30 | 0.99 | 0.60 | 0.45 |
| IGT pick resistance improvement* (%) | ISO 3783 | 15–20 | 25–30 | 30–40 | 35–45 |
The table above illustrates the systematic trade‑off between chain length (as reflected by viscosity) and key performance indicators. 100-60 occupies the central performance tier, balancing processability in high‑speed coating with enhanced barrier and adhesion. Moving to 100‑80 offers marginal film strength gains but raises the minimum dissolution temperature to 95–100 °C and introduces excessive thread‑webbing during adhesive transfer‑coating, reducing line speeds by 15–20 %.
Injection‑molded water‑soluble cores for hollow composite components exploit the melt‑processability of PVA 100-60. Plasticized with 15–20 phr glycerol and 3–5 phr urea, the compound can be processed on a single‑screw extruder (L/D 30:1, compression ratio 3.5:1) with barrel zones at 160 °C /180 °C /190 °C /195 °C (die). The melt viscosity at 190 °C and 100 s⁻¹ shear rate is approximately 1200 Pa·s, which requires a minimum injection pressure of 120 MPa and clamp tonnage of 3.5 kN/cm² projected area. A critical defect mode is thermal crosslinking via ether bonds; the addition of 0.2 phr hindered phenol antioxidant (Irganox 1010) delays the onset of gel particle formation by 12 min at 195 °C, as measured by pressure‑rise rheometry. Without stabilization, the residence time limit is 8 min, after which the melt flow index drops below 1.5 g/10 min (ASTM D1238, 190 °C/21.6 kg).
Sinopec PVA 100-60 is listed in the inventory of existing chemical substances of China (IECSC), the EU (EC No. 618‑340‑9), and the US TSCA Inventory. For adhesives intended for indirect food contact, it conforms to FDA 21 CFR 175.105 (Adhesives) and 176.170 (Components of paper and paperboard in contact with aqueous and fatty foods). Extractives in distilled water and heptane do not exceed 0.5 mg/dm² when tested per EN 1186‑3 at 40 °C/10 days. The grade is certified to EN 13432 for compostability: mineralization exceeds 90 % relative to microcrystalline cellulose within 180 days under controlled composting conditions at 58 °C. The heavy metal content (Pb, Cd, Hg, Cr⁶⁺) complies with the concentration limits of EU Directive 94/62/EC and CONEG model legislation, as summarized below.
| Regulation /Standard | Application Context | Limit /Criterion | Compliance Status |
|---|---|---|---|
| FDA 21 CFR 175.105 | Adhesives for food packaging | Good manufacturing practice | Conforms |
| FDA 21 CFR 176.170 | Paper & paperboard, aqueous/fatty food | Extractives limits | Conforms |
| EN 13432:2000 | Packaging recoverable via composting | Biodegradation ≥ 90 % in 180 days | Passes |
| EU 94/62/EC (Art. 11) | Packaging & packaging waste — heavy metals | Sum Cd, Pb, Hg, Cr⁶⁺ ≤ 100 ppm | Passes |
| CONEG | North American packaging heavy metals | Sum of 4 metals ≤ 100 ppm | Passes |
| REACH, Annex XVII | Restrictions on manufacture, placing on market | No restricted substance above threshold | Conforms |
| RoHS 2011/65/EU | Electrical/electronic equipment | Not applicable as non‑homogeneous material; however, Pb, Cd, etc. absent | Not required, but testable |
The preceding compliance data are derived from certificates of analysis issued by Sinopec and third‑party testing under ISO/IEC 17025 accreditation. The absence of organohalogen compounds is verified by combustion ion chromatography (EN 14582), with total fluorine, chlorine, and bromine each below the 50 ppm detection limit.
The practical upper bound for problem‑free processing of fully hydrolyzed PVA in aqueous solutions without vacuum deaeration is frequently encountered at the viscosity tier represented by 100‑60. When a 10 wt% solution of 100‑60 is held at 60 °C under ambient pressure, micro‑bubbles generated by agitator vortexing are trapped by a combination of high low‑shear viscosity (>2500 mPa·s at 0.1 s⁻¹) and elastic recoil, quantified by a first normal stress difference (N₁) exceeding 30 Pa. The resulting foam half‑life extends beyond 4 min, whereas 100‑37 solutions under identical conditions exhibit half‑lives below 1.5 min. The implication for continuous operation on a slot‑die coater is that the bubble‑free working volume fraction of the recirculating bead drops to 85–90 %, triggering streak defects in the dried film at line speeds above 50 m/min. This mechanistic explanation underlies why 100‑60 is specified with an absolute maximum continuous coating speed of 80 m/min without active degassing, a constraint that disappears with lower‑viscosity grades but reappears with 100‑80, which is typically limited to 40 m/min even with deaeration.