Sundy PVA 098-05 (Sinopec PVA 098-05 /PVA 0599)

Among the polyvinyl alcohol (PVA) grades manufactured by Sinopec Sichuan Vinylon Works, the designation Sundy PVA 098-05—also catalogued as Sinopec PVA 0599—identifies a low-viscosity, fully hydrolyzed homopolymer. The numeric suffix encodes its position in the product matrix: a nominal degree of hydrolysis of 98.0–99.0 mol% and a 4 % aqueous solution viscosity at 20 °C in the range 5.0–7.0 mPa·s, corresponding to an approximate degree of polymerization of 500–600. This combination of high hydrolysis and low molecular weight distinguishes the grade from both high-polymerization fully hydrolyzed types (e.g., PVA 1799) and from partially hydrolyzed low-viscosity types (e.g., PVA 0588), creating a processing window where cold-water solubility, film tensile strength, and organic solvent resistance intersect. The grade is supplied as a white to off-white granular powder with a volatile matter content not exceeding 5.0 % and an ash (as Na₂O) specification of ≤0.5 % when tested according to GB/T 12010.2 or equivalent ISO 15023-2 methods.

Specification limits and the analytical basis for lot acceptance

Routine quality control relies on a minimal set of parameters that govern processability in aqueous formulation. The viscosity of a 4 wt% aqueous solution, measured with a Brookfield LV-type viscometer equipped with a UL adapter at 20.0 ± 0.1 °C, must fall between 5.0 mPa·s and 7.0 mPa·s. Hydrolysis degree, determined by saponification number titration referenced in GB/T 12010.5, is controlled to 98.0–99.0 mol%. Volatile matter, assessed by loss on drying at 105 °C to constant mass, is capped at 5.0 %; however, processors operating gravimetric feeding systems often impose an internal limit of ≤ 3.0 % to prevent bridging in hoppers at relative humidity exceeding 60 %. Ash content, determined by sulfated ash at 800 °C, is ≤0.5 %, with typical production values clustering around 0.3 %. pH of a 4 % aqueous solution at 25 °C ranges from 5.0 to 7.0. While not formally guaranteed on every certificate of analysis, the bulk density of the powder (untapped) averages approximately 0.45–0.55 g/cm³, a figure that directly influences bulk handling and conveying system design on continuous mixing lines.

Within the Sinopec product range, PVA 098-05 is the lowest-viscosity member of the fully hydrolyzed family. This places it adjacent to PVA 0599 in the alternative nomenclature; some regional distributors maintain both codes for the same grade. When procuring under the Sundy trademark, importers should confirm the certificate of analysis references the manufacturing standard Q/SH1115 002 (Sinopec Sichuan Vinylon Works enterprise standard), which mirrors the national framework GB/T 12010 series. REACH registration data for PVA substances (EC No. 618-339-3) covers this grade, and a typical RoHS compliance declaration is available on request; the product contains less than 0.1 % each of mercury, lead, hexavalent chromium, PBBs, and PBDEs by weight of homogeneous material.

Why does 098-05 dissolve in cold water despite 98 % hydrolysis?

The apparent paradox—that a fully hydrolyzed grade can hydrate without heating—resides in the low molecular weight coupled with the residual acetyl group distribution. At a degree of polymerization near 550, the crystalline domains formed by interchain hydrogen bonding lack the size and perfection seen in DP 1700+ polymers. The dissolution process in water at 15–25 °C proceeds by swelling at the amorphous surface layers, and the short chain length accelerates disentanglement and full dissolution within 30–60 minutes under moderate agitation in a high-shear disperser (e.g., a rotor-stator mixer operating at a tip speed of 10–15 m/s). By contrast, a PVA 1799 grade demands heating to 85–95 °C followed by cooling to maintain solubility. Processing plants that convert from 1799 to 098-05 in paper surface-sizing formulations eliminate the steam-jacketed cook tanks, reducing energy consumption and cycle time. Concentration limits must be respected: solutions above 12 wt% at 20 °C risk gelation within 24 h due to incipient crystallization, a threshold that drops to 8 wt% when 5 % ethanol or isopropanol is present as co-solvent. Published data for the exact gelation kinetics in high-shear circulation loops is limited; plant-scale reports indicate that pre-filtration through 50 μm bag filters removes microgels that occasionally form during extended recirculation past 8 h.

Textile warp sizing on high-speed shuttleless looms

In spun-yarn sizing for 100 % cotton and cotton/polyester blends, the low viscosity of 098-05 permits a size-box solids content of 8–10 % with stable pickup on multi-cylinder drying sections operating at 120–130 °C can surface temperature. On a Tsudakoma air-jet loom running at 800–900 rpm, sized yarns exhibit a weaving efficiency improvement of 2–4 percentage points over formulations based on PVA 1799 at equivalent add-on, attributable to reduced hairiness and lower warp break levels. Desizing with a conventional amylase/hot-water sequence (85 °C, 2 min) removes the size film completely, leaving residual ash below 0.1 % on cotton fabric, a requirement for subsequent reactive dyeing. Blending 098-05 with oxidized starch at ratios from 20:80 to 40:60 (PVA:starch on dry weight) is standard practice; the PVA fraction contributes the film flexibility needed to withstand the cyclic elongation imposed by reciprocating reed beats.

Paper surface strength and the influence of low-molecular-weight PVA

When applied via a metering size press to uncoated fine paper (basis weight 70–90 g/m²), a 6 % aqueous solution of 098-05 at 50–60 °C increases IGT surface strength (measured per ISO 3783) by 30–50 % over an unsized control. The critical advantage over starch-only surface sizing is the elimination of dusting during sheet-fed offset printing at speeds above 12,000 sheets/h. Because the grade lacks sufficient viscosity to cause film split misting on flooded-nip applicators, runnability on off-machine coaters is acceptable up to web speeds of 1,200 m/min. The pigment-binding capacity, however, is inferior to polyvinyl alcohol grades with DP above 1,000; a pigmented size press formulation containing 30 parts GCC per hundred parts binder will exhibit a wet pick resistance reduction of approximately 15 % relative to the same binder ratio using PVA 1799, as determined by the IGT pick test at 1.5 m/s. This limitation confines 098-05 to pre-coat or surface-strength-only applications unless co-binders (e.g., styrene-acrylic latex at 5–8 phr) are introduced.

Liquid packaging board producers have evaluated 098-05 as a curtain-coating primer to improve polyethylene extrusion-adhesion. A laminator running a L/D 30 single-screw extruder at 50 kg/h output reported that a primer layer consisting of 2 g/m² PVA 098-05 and 0.5 g/m² polyethylenimine raised the heat-seal bond strength (tested at 230 °C jaw temperature, 0.5 s dwell) from 2.5 N/15 mm to 3.8 N/15 mm, without the orange-peel surface defects observed with higher-viscosity PVA grades. Operational boundaries apply: the primer solution must be filtered to 10 μm and maintained at 35–40 °C to prevent viscosity drift, and the gap between curtain nozzle and web must remain at 40 ± 5 mm to avoid air entrainment.

When low-viscosity PVA replaces conventional grades in emulsion polymerization

Polyvinyl acetate and vinyl acetate-ethylene copolymer emulsions stabilized with Sundy PVA 098-05 exhibit a characteristic shift in particle size distribution and viscosity profile relative to those made with PVA 1788 or PVA 1799. In a batch reactor equipped with a 45° pitched-blade turbine at a tip speed of 3.5 m/s, the use of 5.0 phr (per hundred parts monomer) 098-05 as the sole protective colloid yields a latex with a median particle diameter of 1.2–1.8 μm, measured by laser diffraction. The resulting emulsion viscosity at 55 % solids is typically 2,000–4,000 mPa·s (Brookfield RVT, spindle #6, 20 rpm), substantially lower than the 8,000–12,000 mPa·s achieved with 1799 at the same solids, because the lower molecular weight reduces the hydrodynamic volume of the adsorbed PVA layer. This lower viscosity facilitates higher-solids polymerization (58–60 %) without exceeding the torque limit of a 75 kW anchor-agitator drive. However, the water resistance of films cast from such emulsions, as evaluated by 24-hour water absorption at 23 °C per ISO 62, rises from 8–10 % for a 1799-stabilized system to 14–18 % for the 098-05 system, necessitating the addition of a crosslinker (e.g., glyoxal at 0.1–0.3 wt% on latex) for applications requiring Type II wood adhesive performance per EN 204. Post-addition of a non-ionic surfactant (alkyl polyglycoside, 0.5 wt%) is routinely practiced to restore wetting on low-surface-energy substrates without depleting the protective colloid.

Incompatibility has been observed with amine-based pH adjusters: adding triethylamine or AMP-95 directly to a concentrated 098-05 solution above 50 °C causes localized gel particle formation due to rapid deacetylation under alkaline conditions. The recommended buffer is sodium acetate/acetic acid, and the pH adjustment sequence must ensure the PVA solution temperature remains below 40 °C when above pH 8.0.

Film casting and water-soluble packaging: property benchmarks

Cast films of 30–50 μm thickness, produced on a chill-roll line at 15 m/min with a die temperature of 80–85 °C, exhibit a tensile strength of 45–55 MPa (MD, ASTM D882) and elongation at break of 150–200 %. These values position the grade between PVA 0588 (high elongation, low strength) and PVA 1799 (high strength, elongation ≤ 100 %). In water-soluble pouch applications for agrochemicals, the disintegration time of a 40 μm film in water at 15 °C is 60–90 s, compared to > 180 s for 1799-derived film of identical thickness. Pre-drying of the resin to a moisture content below 0.5 % is mandatory for blown-film extrusion with a barrier screw of L/D 28; otherwise, steam bubbles generate pinholes that reduce oxygen barrier from <2 cm³/(m²·day·bar) (at 0 % RH, ASTM D3985) to unacceptable levels. The plasticizer package typically comprises glycerol at 10–15 phr and sorbitol at 3–5 phr, pre-blended in a hot mixing step at 70 °C before single-screw compounding.

In barrier film extrusion, the low melt viscosity of 098-05 enables processing at melt temperatures of 190–210 °C, approximately 20–30 °C lower than that required for 1799, a factor that reduces thermal degradation and yellowing when the residence time in the die exceeds 5 min. The trade-off manifests in a slightly higher equilibrium moisture regain—5.2 % at 65 % RH versus 4.8 % for 1799—owing to greater amorphous content; converters compensate by adjusting dryer zone temperatures upward by 5–10 °C during secondary processing.

Structural differences and how they govern substitution decisions

The three-digit core of the grade name—“098”—declares the essential differentiation: 98 mol% hydrolysis, compared with 88 mol% for the 0588 series or 99 mol% for the 1799 series. The trailing “05” indicates the viscosity bracket, approximately 5 mPa·s. In practice, this structure means the polymer chain contains roughly 1.5–2.0 mol% residual acetate groups, which are isolated along the backbone rather than forming blocky sequences. The low blockiness index, a consequence of the continuous saponification process used by Sinopec, enhances cold-water solubility while preserving interchain hydrogen bonding sufficient for high film strength. Substituting 098-05 for PVA 1799 reduces solution viscosity by a factor of 4–5 at equivalent concentration, making it possible to increase solids by 3–5 percentage points in adhesive formulations without exceeding the 5,000 mPa·s upper limit of roller coaters. Conversely, substituting it for PVA 0588 improves moisture resistance and tensile strength but sacrifices about 30–40 % of the elasticity and reduces adhesion to hydrophobic substrates such as PET film. The emulsifying power for vinyl acetate monomer is lower than that of 0588; the critical micelle-like concentration effect of PVA arises from the acetate block content, which is minimal in this grade. As a result, emulsion polymerization recipes must increase surfactant loading by 0.3–0.8 wt% on monomer to maintain nucleation rate, or operate with a seeded semi-batch profile where the initial charge contains 5–10 % of a high-hydrolysis, high-DP grade such as PVA 1799 as a particle-size control agent.

A recurring processing bottleneck in adhesive compounding arises when 098-05 is blended with fully hydrolyzed grades above 15 wt% of the high-DP component, leading to viscosity drift during storage due to progressive polymer aggregation. Rotational rheometry on a controlled-stress rheometer (cone-and-plate, 40 mm, 2° angle) has shown that a blend with 20 % PVA 1799 develops a yield stress of 1.2 Pa after 48 h quiescent aging at 25 °C, which necessitates in-line shear before application. For most users, maintaining the high-DP fraction below 10 % of total PVA eliminates the issue.

Global regulatory acceptability encompasses compliance with European Commission Regulation (EU) No 10/2011 on plastic materials intended for food contact, subject to the specific migration limit for vinyl alcohol of 60 mg/kg; the low residual sodium acetate and methanol levels typical of the grade ( <0.1 % and <1 ppm, respectively) support this status. The grade is also listed in the inventory of existing chemical substances in China (IECSC) and is registered under K-REACH for the Korean market.