Sinopec PVA 098-10, also designated as PVA 1098 in certain regional nomenclature, is a medium-viscosity, fully hydrolyzed polyvinyl alcohol homopolymer manufactured via continuous alcoholysis of polyvinyl acetate. Its molecular architecture—a backbone of 1,3-glycol units with a hydrolysis degree controlled to a narrow window of 98.0–99.0 mol%—places it at the boundary between conventional fully hydrolyzed grades and the partially hydrolyzed series, yielding a distinct balance of cold-water resistance and hot-water solubility. The grade is produced under the Sinopec Sichuan Vinylon Works quality system, with lot-to-lot variation in 4 % aqueous solution viscosity at 20 °C held to 10.0–14.0 mPa·s when tested per GB/T 12010.2-2010 (Ubbelohde viscometer method). Residual sodium acetate, expressed as ash, is limited to ≤ 0.5 % (GB/T 12010.3), and volatile matter at 105 °C to ≤ 5.0 %, making the product directly usable in dry-blend formulations without the post-drying step often required for higher-ash competitors.
The product’s mean degree of polymerization falls between 1000 and 1100, corresponding to a weight-average molecular weight of approximately 44,000–48,000 g·mol⁻¹. This positions 098-10 below the high-toughness film grades (DP > 1700) but above the low-viscosity emulsion polymerization protectives (DP 500–600), yielding a rheological profile that favors spray-dried powder processing, high-speed paper coating, and textile warp sizing where excessive stringiness must be avoided. The following sections examine performance boundaries, processing windows, and formulation conflicts observed on production-scale equipment, with comparative data drawn against the partially hydrolyzed grades Sinopec PVA 088-20 (088-20) and PVA 0588 (0588), as well as the low-DP fully hydrolyzed grade 1788.
Aqueous Dissolution Kinetics and Film-Forming Thresholds
Complete dissolution of 098-10 requires a slurry make-down temperature above 85 °C under moderate-shear agitation; solution hold tanks operated below 80 °C with this grade exhibit progressive gelation within 4–6 hours due to intermolecular hydrogen bonding between syndiotactic sequences. This gelation threshold is steeper than that observed for the 88 mol% hydrolyzed series, which remain flowable down to 60 °C at equivalent concentration. In continuous film-casting lines where dope temperature is maintained at 90–92 °C in a jacketed trough, the Newtonian plateau extends to a shear rate of approximately 200 s⁻¹; beyond this, slight pseudoplasticity develops. The critical overlap concentration (c*) for 098-10 in deionized water at 20 °C is approximately 2.8 % w/w, meaning that in typical 6–8 % sizing formulations, the chains are fully entangled, and the zero-shear viscosity follows a power-law exponent of 3.4 with concentration, consistent with the de Gennes scaling prediction for neutral polymers in a good solvent. Operators of horizontal size presses should note that bath viscosity drift of more than ±0.5 mPa·s from the nominal 12 mPa·s setpoint can alter pick-up by 0.5–0.8 g/m², a shift that directly impacts IGT dry pick resistance per ISO 3783:2020.
Dense, stand-alone paragraph without a header reads: When substituted for PVA 088-20 in a standard adhesive compound for spiral paper tube winding, the higher hydrolysis degree of 098-10 reduces open time by approximately 15–25 seconds on a 120 g/m² Kraft liner at 23 °C and 50 % RH, as measured by a finger-tack probe test adapted from TAPPI T 484. This reduced tack window is offset by a 30–40 % gain in wet shear strength after 24-hour water immersion at 23 °C, attributed to the lower equilibrium moisture regain of the fully hydrolyzed film and its resistance to plasticization by imbibed water. In production trials on a 1,200 mm wide spiral winder running at 80 m/min, the substitution eliminated the secondary over-lacquer step previously needed to prevent delamination under high-humidity shipping conditions, reducing total adhesive cost per linear meter by 11 % despite the slightly higher raw material price of 098-10 versus 088-20. Pre-drying of the powder at 60 °C for 2 hours is recommended when storage relative humidity exceeds 60 %, as moisture content above 5.5 % leads to caking in the hopper of gravimetric feeders and irregular dissolution rates in continuous jet cookers.What Distinguishes 098-10 from the Partially Hydrolyzed Series in Protective Colloid Applications?
In vinyl acetate emulsion polymerization, the selection of a protective colloid governs not only latex stability but also grafting efficiency, particle size distribution, and final film water sensitivity. Sinopec 098-10, with a residual acetyl content of 1–2 mol% (remainder hydroxyl), yields a more hydrophobic graft copolymer with polyvinyl acetate than does a 88 mol% hydrolyzed grade. When used at a 4 % charge on monomer weight in a semi-batch reaction initiated by potassium persulfate at 70 °C, the final latex exhibits a bimodal particle size distribution with a primary mode at 800–1,200 nm and a secondary fine mode around 200 nm, as measured by laser diffraction per ISO 13320:2020. The presence of the fully hydrolyzed protective shell depresses water absorption of the dried film to 8–10 % after 24-hour soak versus 15–20 % for an equivalent latex stabilized with a 88 mol% PVA of similar DP. However, the higher grafting reactivity also raises the minimum film-forming temperature (MFFT) of the neat latex by 3–5 °C, which must be compensated with a coalescent when application temperatures fall below 10 °C. Published data for this specific grade in vinyl acetate-ethylene copolymer systems is limited; existing plant records indicate that the copolymerization of ethylene under 30 bar partial pressure reduces the grafting differential between 098-10 and 088-20, rendering the fully hydrolyzed advantage less pronounced in high-ethylene-content lattices.
| Property | Test Method | 098-10 (1098) | 088-20 | 0588 | 1788 |
|---|---|---|---|---|---|
| Hydrolysis degree | GB/T 12010.5 | 98.0–99.0 mol% | 87.0–89.0 mol% | 86.0–89.0 mol% | 97.0–99.0 mol% |
| Viscosity (4 % aq, 20 °C) | GB/T 12010.2 | 10.0–14.0 mPa·s | 20.0–26.0 mPa·s | 4.5–6.0 mPa·s | 20.0–26.0 mPa·s |
| Degree of polymerization | GB/T 12010.6 | 1000–1100 | 1700–1800 | 500–600 | 1700–1800 |
| Ash (as Na₂O) | GB/T 12010.3 | ≤ 0.5 % | ≤ 0.5 % | ≤ 0.5 % | ≤ 0.5 % |
| Volatile matter | GB/T 12010.4 | ≤ 5.0 % | ≤ 5.0 % | ≤ 5.0 % | ≤ 5.0 % |
| pH (4 % solution) | GB/T 12010.1 | 5–7 | 5–7 | 5–7 | 5–7 |
When 098-10 Replaces 0588 in Redispersible Polymer Powder Production
The spray-drying of vinyl acetate-ethylene copolymer dispersions into redispersible polymer powders for cementitious dry mortars places a dual demand on the protective colloid: it must stabilize the primary dispersion and also serve as the anti-caking matrix powder. Here, 0588 (DP 500–600, viscosity 4.5–6.0 mPa·s) is conventionally chosen because its low solution viscosity permits a high solids feed of 45–50 % to the spray dryer without exceeding the nozzle back-pressure limit of 40 bar on a rotary atomizer running at 12,000–15,000 rpm. Substituting 0588 with 098-10 reduces the maximum atomizable solids to approximately 38–42 % at equivalent pumping temperatures, increasing specific drying energy by an estimated 12–15 %. The trade-off observed on a Niro-type co-current tower with inlet temperature 160 °C and outlet 65 °C is a markedly lower blocking tendency of the finished powder after storage at 35 °C and 75 % RH for 72 hours; the cold-water re-dispersibility, as measured by the Ross-Miles foam test variant adapted for mortar admixture characterization, degrades by less than 5 % compared to a 15–20 % loss observed with the low-DP fully hydrolyzed grade 0588. This improvement is attributed to the higher glass-transition temperature and lower hygroscopicity of the 098-10 shell, which resists inter-particle sintering under warehouse conditions in tropical climates. Plant operators blending 098-10 into a ternary colloid system (e.g., with a low-viscosity partially hydrolyzed grade and a superplasticizer compatibility agent) should be aware that the mixed powder’s dissolution profile becomes biphasic: the fine fraction of 098-10-rich particles requires an additional 90–120 seconds of wet mixing at 800 rpm in a forced-action mixer to reach full dispersion, beyond the point where visual lump-free consistency is observed.
Textile Sizing and the Creel-Speed Barrier
On a modern high-pressure single-end sizing range processing 40/2 Ne polyester/cotton blend yarns at a creel speed of 600 m/min, the size box temperature must maintain the 098-10 solution above 88 °C to prevent skinning on the immersion rollers. At a size concentration of 8 % solids and a squeeze pressure of 4 kN/m, the pick-up on the yarn sheet stabilizes at 12.5–13.5 % (dry on dry). Loom-shop monitoring under 25 °C and 65 % RH conditions documented a warp break rate of 0.8–1.2 stops per million picks for 098-10 sized warps, statistically indistinguishable from the reference 088-20 formulation, but with a lower shed drop-out of powdered size due to improved film cohesion at the crossover points. A notable limitation: the fully hydrolyzed film requires a desizing bath pH above 10.5 (adjusted with sodium hydroxide) and a bath temperature of 80 °C to achieve complete removal within a 45-second dwell time in a continuous enzymatic-oxidative desizing range; partially hydrolyzed grades strip cleanly under identical conditions at pH as low as 9.5. Mills transitioning from 088-20 to 098-10 for tensile strength advantages must therefore validate desizing efficacy using a TEGEWA scale rating of 4 or better (scale 1–5) before committing to bulk production.
Film Weldability and the Avoidance of Amine-Based Crosslinkers
Thermal welding of 098-10 films to lignocellulosic substrates via a heated bar at 180 °C and 0.3 MPa pressure for 2 seconds achieves bond strengths exceeding the internal cohesion of the substrate; this property has led to its use in biodegradable packaging laminates where the PVA layer acts as both barrier and adhesive. However, any formulation containing primary amine-functional additives—such as certain wet-strength agents based on polyamidoamine-epichlorohydrin (PAE) resins—must be strictly avoided. The residual acetate groups in 098-10, though minimal, are sufficient to undergo imine formation with amines at drying temperatures above 120 °C, leading to a rapid, uncontrolled viscosity build in the solution and embrittlement of the final film. This incompatibility is not observed with the purely hydroxyl-bearing grades that have been completely saponified (hydrolysis > 99.5 mol%), making 098-10 a poor substitute for super-fully-hydrolyzed PVA in chemistries that include amine-cure systems. When crosslinking is required, glyoxal at a ratio of 5–10 % on PVA weight, catalyzed by a magnesium chloride hexahydrate latent acid, delivers a pot life of 6–8 hours at 25 °C and 50 % RH, with full insolubilization achieved after 3 minutes at 150 °C.
Application of 098-10 as a temporary binder in high-alumina castables exposes a rheological conflict not apparent in standard cellulose-ether-modified systems. The polymer’s burnout profile in air, as measured by thermogravimetric analysis at 10 °C/min ramp, shows complete decomposition by 550 °C with no carbon residue above 600 °C, which is compatible with most sintering schedules. However, at addition levels exceeding 0.5 wt% on the castable dry weight, the counter-ion effect of residual sodium acetate elevates the slurry’s electrical conductivity, accelerating the dissolution of MgO fines and shortening the working time by 15–20 % in a system designed for a 60-minute open time at 20 °C. Plant trials conducted on a 1,200 kg batch mixed in a planetary intensive mixer quantified the workability loss via a flow cone test per ASTM C230/C230M-21, with the spread drop from 220 mm to 175 mm occurring 12 minutes earlier when 098-10 was present at 0.8 % compared to a non-ionic cellulosic binder control. This places a practical upper dosage limit on 098-10 in deflocculated refractory castables, beyond which on-site water addition to restore flowability compromises the fired modulus of rupture.
| Parameter | Threshold | Consequence of Deviation |
|---|---|---|
| Solution make-down temperature | ≥ 85 °C | Microgel nucleation, viscosity drift in size press or coating bath |
| Spray dryer feed solids (standalone) | ≤ 42 % at 40 bar atomization | Nozzle blockage, excessive agglomerates in powder |
| Storage relative humidity (powder) | ≤ 60 % without pre-drying | Caking in feed hopper, erratic gravimetric dosing |
| Contact with amine-containing additives | Temperature > 120 °C | Imine crosslinking, irreversible viscosity spike, film embrittlement |
| Desizing bath pH for complete removal | ≥ 10.5 at 80 °C | Residual size on fabric, dyeing non-uniformity |
| Castable addition level with MgO binder | ≤ 0.5 wt% | Slump loss acceleration, fired strength reduction due to excess water |
The saponification profile of 098-10 imparts a surface activity that differs from both the far more hydrophilic 99+ mol% grades and the surfactant-like 88 mol% series. This intermediate surface energy, quantified by a contact angle of 42–45° on a polished chromium plate for a 5 % solution dried at 80 °C, makes the polymer effective as a transfer metallization primer for vacuum-deposited aluminum on cellulose acetate film. In this niche application, the PVA interlayer must adhere to the substrate and receive a uniform aluminum nucleation layer without outgassing during the 10⁻⁴ mbar deposition step. Trials on a batch metallizer with a deposition rate of 3 nm/s confirmed that an 098-10 primer layer of 0.8–1.2 µm dry thickness eliminated the pinholing observed with a low-DP grade, while maintaining an optical density of 2.8 on the aluminum layer, sufficient for barrier packaging requiring an oxygen transmission rate below 0.5 cm³/m²·day·atm.
