Products

Products

Anhui Liwei Chemical Co., Limited.

Sinopec PVA 097-60

    • Product Name: Sinopec PVA 097-60
    • Factroy Site: Lingwu, Yinchuan, Ningxia, China
    • Price Inquiry: sales2@liwei-chem.com
    • Manufacturer: Anhui Liwei Chemical Co., Limited.
    • CONTACT NOW
    Specifications
    HS Code 510906
    Product Name Sinopec PVA 097-60
    Chemical Name Polyvinyl alcohol
    Cas Number 9002-89-5
    Appearance White or off-white granular powder
    Degree Of Hydrolysis 97.0 ± 0.5 mol%
    Viscosity 4 Aqueous Solution At 20 C 60.0 ± 3.0 mPa·s
    Ph 4 Aqueous Solution 5.0 - 7.0
    Volatile Content ≤ 5.0%
    Ash Content ≤ 0.5%
    Average Degree Of Polymerization 2400
    Average Molecular Weight ~105,000
    Water Solubility Soluble in hot water; swells in cold water
    Bulk Density 0.4 - 0.6 g/cm³
    Specific Gravity 1.19 - 1.31

    As an accredited Sinopec PVA 097-60 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Sinopec PVA 097-60 is supplied in 25 kg woven bags with polyethylene lining, ensuring safe handling and moisture protection.
    Container Loading (20′ FCL) Sinopec PVA 097-60 loaded in 20′ FCL, palletized bags, secured and ventilated, ensuring safe transport.
    Shipping Sinopec PVA 097-60 is shipped as a non-hazardous, water-soluble polyvinyl alcohol resin. It is packaged in sealed multi-layer paper bags with PE liners, typically 20 kg each, palletized and stretch-wrapped. Keep dry, ventilated, protected from moisture and heat during transit. Avoid direct sunlight and rough handling to preserve product quality.
    Storage Store Sinopec PVA 097-60 in a cool, dry, well-ventilated area, away from heat, open flames, and direct sunlight. Keep the original packaging tightly sealed to prevent moisture absorption, as the product is hygroscopic. Avoid dust accumulation and contact with strong oxidizing agents. Maintain stable temperatures and low humidity to preserve quality.
    Shelf Life Shelf life: 24 months when stored unopened in a cool, dry place away from moisture and direct sunlight.
    Application of Sinopec PVA 097-60
    In the suspension polymerization of vinyl chloride monomer (VCM), the primary dispersant system governs resin particle morphology, plasticizer absorption, and residual monomer desorption rates. Sinopec PVA 097-60, a partially hydrolysed grade with a nominal hydrolysis degree of 60 mol% and a 4% aqueous solution viscosity of 22 – 28 mPa·s at 20 °C, functions as a high-efficiency interfacial tension modifier. When combined with a secondary dispersant of higher hydrolysis degree (usually 72 – 80 mol%), the acetyl-rich PVA 097-60 preferentially adsorbs onto the monomer droplet surface during the initial shearing stage, reducing the interfacial tension to 4 – 6 mN/m and generating a high population of uniform droplets. Polymerization is conducted in a 70 m³ glass-lined stirred tank equipped with a three-blade retreat-curve impeller. A typical charging recipe for a suspension-grade S-PVC (K-value 66 – 68) uses a total dispersant mass of 0.08 – 0.12 wt% based on VCM weight, with the PVA 097-60 component adjusted to 30 – 50 % of the total dispersant blend, while the remainder is a high-hydrolysis PVA. The aqueous phase contains deionized water at a water-to-monomer ratio of 1.2 : 1, and a medium-efficiency initiator such as di(2-ethylhexyl) peroxydicarbonate (EHP) dosed at 0.03 – 0.05 phr. The cold-suspension technique maintains a jacket temperature cycling between 56 – 62 °C with a pressure profile peaking at 0.95 MPa. Particle size distribution measured by laser diffraction on the dried resin yields a median diameter of 120 – 150 µm with a span below 1.1. Finished PVC resin obtained must comply with bulk density specifications (0.48 – 0.56 g/cm³ per ASTM D1895-17 Method A) and plasticizer absorption per ASTM D1755 section 11. Any deviation in PVA 097-60 dosage versus agitator power number leads to undesirable fines generation or translucent agglomerates known as “glass beads,” a well-documented failure mode in fluidized-bed drying operations.

    What Limits Cold-Water Solubility and Surface Activity in Protective Colloid Applications?

    When a partially hydrolysed polyvinyl alcohol like Sinopec PVA 097-60 is deployed as the primary protective colloid in the emulsion polymerization of vinyl acetate monomer, the acetyl group distribution along the polymer backbone controls both grafting density and final latex rheology. The polymerization is typically run as a semi-batch process in a 10 m³ jacketed 316L stainless steel reactor with a dual-anchor and high-shear disperser combination. A pre-emulsion consisting of vinyl acetate (VAM) and a hydrophobic initiator such as dibenzoyl peroxide is fed over 3 – 4 hours into an aqueous phase containing 4 – 7 wt% PVA 097-60 based on total monomer mass. The carefully controlled hydrolysis degree of 60 mol% ensures that residual acetate groups participate in radical chain transfer to the polymer, generating PVA‑g‑PVAc copolymer in situ at the particle interface. This graft layer provides electrosteric stabilization, producing a latex with a Brookfield viscosity of 12 000 – 25 000 mPa·s and a mean particle diameter of 0.8 – 2.5 µm. In adhesive formulations meeting EN 204 D3 class for interior wood bonding, this homopolymer latex is further plasticized with dibutyl phthalate at 8 – 12 % of polymer solids. The resultant white glue demonstrates a wet tack exceeding 30 seconds and a shear strength on beech wood of more than 7 N/mm² when tested per EN 205. A processing limitation arises if the kettle temperature during the initial seed stage drops below 15 °C: the partially hydrolysed PVA solution can undergo thermoreversible gelation due to interchain hydrophobic association of acetyl segments. Therefore, the aqueous charge must be heated to 28 – 35 °C before initiator injection to avoid catastrophic phase separation. This grade also shows incompatibility with borate ions; even 0.1 wt% of borax in the final formulation will trigger instantaneous crosslinking, leading to a non-flowable paste—a property intentionally exploited in specialty adhesives but must be strictly avoided in standard D3 wood glues.Paper surface sizing at machine speeds exceeding 1 200 m/min on lightweight coated (LWC) base stock benefits from the balance of film strength and rapid re-solubility offered by a partial-hydrolysis PVA. Sinopec PVA 097-60 is solubilized in a continuous cooker at 15 – 18 % solids and then diluted into a recirculating size press solution. The working concentration at the metering size press (Voith SpeedSizer or similar) is maintained at 5 – 8 wt% PVA, often co-blended with thermally oxidized corn starch at a dry-weight ratio of 30 : 70 (PVA:starch) to optimize cost and IGT pick resistance. The surface tension of the size solution at the nip, measured by the Du Noüy ring method, falls to 38 – 42 mN/m, which ensures uniform wetting of the base sheet. The film split occurs in a flooded nip under a hydraulic pressure of 35 – 45 kN/m. Critical performance indicators for this application are the Cobb60 water absorption (target 20 – 25 g/m² per ISO 535) and the dry surface strength tested by IGT pick velocity (target >2.5 m/s using medium-viscosity oil per ISO 3783). Because the acetyl content of PVA 097-60 reduces excessive hydrogen bonding with cellulose, the sized sheet retains higher folding endurance and does not become brittle during offset printing. A processing caution concerns the microbiological stability of the starch‑PVA mixture in the recirculation loop: the tank must be blanketed with a biocide such as glutaraldehyde at 50 – 100 ppm active, as PVA 097-60 degrades slowly by enzymatic attack under prolonged storage above 40 °C. When the sized paper is intended for indirect food contact, migration limits and composition requirements under EU 1935/2004 and the German BfR Recommendation XXXVI for paper food contact material apply; the coating must exhibit a global migration below 10 mg/dm² in acetic acid simulant.
    Process Parameter Matrix for Sinopec PVA 097-60 Across Downstream Sectors
    Application SegmentEffective Working Concentration (wt%)Brookfield Viscosity of Working Solution (mPa·s)Critical Additives/Co-bindersProcessing EquipmentRegulatory Standard
    VCM Suspension Polymerization0.08–0.12 (on VCM mass)Water phase 8–12 at 25 °CHigh-hydrolysis PVA (e.g., 72–80 mol%)Glass-lined stirred tank, retreat-curve impellerResin: ASTM D1755
    PVAc Emulsion Protective Colloid4–7 (on monomer)40–80 (initial charge)Non-ionic surfactant (optional), plasticizer post-reactionStainless steel jacketed reactor with anchor & disperserAdhesive: EN 204/205
    Paper Surface Sizing (LWC)5–8 (aqueous size)120–250 at 60 °COxidized starch, insolubilizer, biocideMetering size press (e.g., Voith SpeedSizer)Paper: ISO 535, BfR XXXVI
    Ceramic Spray Drying Binder0.5–2.0 (on ceramic powder)Slip viscosity 300–600 at 20 °CPolyacrylate dispersant, antifoamPressure nozzle atomizer, counter-current towerCeramic: ISO 5754
    Water-Soluble Film Casting15–20 (casting solution)1 800–3 500 at 40 °CGlycerol (10–15 phr), release agentChill roll cast film line, T-die extrusion or solution castFilm: EN 13432, OECD 301B

    Remoistenable Adhesive Recipes Meeting FDA 21 CFR 175.105 and EN 13432

    Water-activated gummed tapes and envelope front seals rely on a dry film that becomes aggressively tacky within 2 – 4 seconds of wetting. A formulation based on Sinopec PVA 097-60 exploits its residual acetyl groups to reduce dry-film brittleness without excessive cold flow. A typical coating compound for high-speed ream wrapping consists of 100 parts PVA 097-60 (dry basis), 15 – 25 parts glycerol as humectant/plasticizer, 3 – 5 parts powdered dextrin to boost immediate tack, and a defoamer based on mineral oil emulsion at 0.2 parts. The solids content is adjusted to 28 – 32 % to achieve a No. 3 Zahn cup viscosity of 35 – 45 seconds for gravure coating. The adhesive is applied to 50 – 60 g/m² kraft liner by a direct gravure cylinder at a line speed of 150 – 200 m/min, with the dry coat weight controlled at 10 – 14 g/m² by varying the cylinder line screen. The coated paper passes through an IR drying tunnel with a web temperature of 95 – 105 °C and is immediately rehumidified with a steam curtain to prevent curling. Finished tapes tested per ASTM D1876-08 for 180° peel adhesion to recycled corrugated board exhibit a minimum average peel of 3.5 N/cm. In terms of compliance, for direct application on food packaging (dry food, non-fatty), the adhesive must conform to FDA 21 CFR 175.105, which limits the extractable fraction. Migration testing in 10 % ethanol and 3 % acetic acid simulants yields results below 50 ppb for residual monomers. While PVA 097-60 itself is biodegradable under OECD 301B conditions, the full formulated film must be tested as a composite. Users must verify that no amine-based crosslinkers were added, as they cause yellowing and loss of re-wettability during storage.When switching from fully hydrolysed grades to a 60 mol% hydrolysis PVA for polyester filament warp sizing, the adhesion mechanism shifts from hydrogen bonding to polar ester group interactions. Sinopec PVA 097-60 is cooked in a steam-injection atmospheric cooker to a 9 – 12 % solids concentration and then transferred into the size box of a sectional warping slasher. The size bath is kept at 85 – 90 °C and a synthetic acrylic size (e.g., with a glass transition temperature of ‑15 °C) is blended in at 20 – 30 % of the dry size mass to improve film elongation. For a 75 dtex/36f semi-dull polyester yarn bundle, the target size add-on after the high-pressure squeeze roll (nip load 35 kN) is 8 – 10 % owf. The yarn exiting the drying section with a surface temperature of 140 °C achieves a residual moisture below 0.5 %. Weaving is performed on an air-jet loom at 800 rpm; the shedding zone requires a size film with an abrasion resistance measured by the Zweigle G552 abrader to exceed 600 cycles per 50 mg of size loading. Desizing after weaving is accomplished by a continuous wash box at 80 °C with 0.5 g/L of a non-ionic wetting agent; complete removal is verified with iodine-boric acid spot test. A significant operational limitation: the partially hydrolysed PVA film softens and becomes tacky at high loom-humidity conditions (RH > 85 %). Therefore, the weaving shed must maintain a controlled climate at 25 ± 2 °C and 65 ± 5 % RH. The desizing effluent is treatable in standard aerobic wastewater plants, but the BOD5/COD ratio of PVA 097-60 is reported around 0.2 – 0.3, indicating recalcitrance to primary sedimentation and necessitating activated sludge acclimation per OECD 303A. Compliance with Oeko-Tex Standard 100 Annex 4 for textiles requires that the finished fabric contains less than 0.5 % residual size after final washing and bleaching.

    Ceramic Powder Processing: Spray-Dried Granulate Compaction Profiles

    The manufacturing of structural ceramics via dry pressing begins with a slurry containing a submicron alumina or zirconia powder dispersed in water. Sinopec PVA 097-60 is introduced as a temporary binder at a dosage of 0.8 – 1.5 wt% based on dry powder mass, along with 0.3 – 0.5 wt% of an ammonium polyacrylate dispersant. The slip with a solids loading of 60 – 65 wt% is mixed in a high-energy bead mill until the particle size distribution reaches a D90 of 1.2 µm. Spray drying is performed using a rotary or pressure nozzle atomizer with an inlet temperature of 220 – 250 °C and an outlet temperature of 90 – 105 °C. The resulting spherical granules exhibit a free-flowing morphology with an angle of repose below 30° and a bulk density of 1.10 – 1.25 g/cm³. For uniaxial pressing at 100 MPa in a hydraulic press, the green density reaches 55 – 58 % of theoretical density, and the diametral compressive strength (green strength) exceeds 2.5 MPa as measured by the three-point bending method on a 50 mm span rectangular bar per ISO 5754. The binder burnout cycle in a digitally controlled kiln ramps from room temperature to 600 °C at 0.5 °C/min under a flowing oxidizing atmosphere; PVA 097‑60 pyrolyzes without leaving detectable carbon residue because its chain structure lacks aromatic units. A deviant practice to avoid is the use of calcium-based sintering aids in the initial slurry, as free Ca2+ ions can complex with the hydroxyl groups of the partially hydrolysed PVA, sharply increasing the slip viscosity and causing premature moisture retention pockets in the granule that result in pressing lamination cracks. The debinding step must maintain a dew point below ‑10 °C to prevent capillary condensation in the pore network, which would induce blistering in the sintered body. Final sintered parts intended for ISO 13356 surgical implant ceramics demand that the binder system does not impart any trace heavy-metal contamination; Sinopec PVA 097‑60 must be supplied with a certificate of analysis showing ash content below 0.05 % and heavy metals (Pb, Cd, Hg) below 1 ppm each.

    How Acetyl Content Modulates Heat Seal Strength in Water-Soluble Unit-Dose Films

    Cast films extruded or solution-coated from Sinopec PVA 097‑60 can be tailored for laundry detergent pods and agrochemical water-soluble bags, though the 60 mol% hydrolysis grade introduces specific sealing and dissolution characteristics. The formulation masterbatch for a 30 µm blown or cast film typically contains 100 parts PVA 097‑60, 12 – 18 parts of sorbitol-based plasticizer, 2 – 4 parts of a stearate-based release agent, and process stabilizers such as hindered phenol antioxidants below 0.1 %. The melt is extruded through a cast film die with a melt temperature of 180 – 200 °C onto a chill roll maintained at 60 – 70 °C. The film’s tensile strength at break according to ASTM D882-18 is typically 25 – 35 MPa with an elongation at break of 250 – 350 %. Heat sealing is performed at a jaw temperature of 140 – 160 °C with a dwell time of 0.5 – 1.0 second; the partially hydrolysed grade requires a slightly lower seal initiation temperature than fully hydrolysed film, reducing the risk of burn-through but demanding tighter temperature tolerance (± 3 °C). Water dissolution time for a fully submerged 30 µm film in deionized water at 10 °C is between 60 – 90 seconds, a parameter that must be validated according to the dissolution test method referenced in ISO 16203 for household chemical packaging. A critical packaging incompatibility arises with liquid detergents containing high levels of free alkalinity (pH > 12): the residual acetyl groups of PVA 097‑60 can slowly saponify within the sealed pouch, generating acetic acid and leading to internal pressure buildup and long-term seal creep. Consequently, formulations using this specific grade are limited to pH values below 11.5 and must undergo accelerated aging at 40 °C/75 % RH for 8 weeks per ASTM F1249-20. For the European market, compliance with the EU Detergent Regulation (EC) No. 648/2004 Annex II on biodegradability requires that the film polymer meets the OECD 301B ready biodegradability criteria (> 60 % CO₂ evolution in 28 days). PVA 097‑60 is classified as inherently biodegradable under these conditions without the need for specific inoculum adaptation.As a temporary binder in the tape casting of electronic substrates, Sinopec PVA 097‑60 provides a clean burnout profile compatible with low-temperature co-fired ceramic (LTCC) processing with minimal ash residue. A slip is prepared from dielectric glass powder (e.g., Ca‑Al‑B‑Si‑O system) with 50 vol% powder loading in a mixture of methyl ethyl ketone and ethanol. The PVA 097‑60 binder is pre-dissolved in a water‑ethanol mixture at 10 % solids and added to the slip at a ratio corresponding to 6 – 8 parts binder per 100 parts powder. A plasticizer package including butyl benzyl phthalate (3 – 4 parts) is incorporated to give the cast green sheet enough flexibility for handling on a doctor blade coater with a gap height of 0.5 – 1.0 mm. The carrier film passes through a two-zone drying chamber where the first zone eliminates the bulk solvent at 40 °C and the second zone sets the polymer network at 70 °C. The dried tape shows a tensile strength of 3 – 5 MPa and 15 – 20 % elongation to break as per ASTM D638, with a cut-true tolerance suitable for via punching. During co-firing with silver conductors, the atmosphere is switched to nitrogen at a dew point of ‑40 °C to prevent oxidation. The residual carbon from PVA 097‑60 burnout must remain below 200 ppm in the fired ceramic, as specified in the quality acceptance protocols for RF modules. Any hygroscopic swelling of the binder during storage due to humidity > 60 % RH will cause tape elongation and misregistration of vias. Therefore, all rolls must be stored in sealed aluminum laminate bags with desiccant packs immediately after casting. The compliance framework for this application references IPC‑4101C for base materials and requires a declaration of halogen-free composition per IEC 61249‑2‑21, which Sinopec PVA 097‑60 satisfies by design.
    Free Quote

    Competitive Sinopec PVA 097-60 prices that fit your budget—flexible terms and customized quotes for every order.

    For samples, pricing, or more information, please contact us at +8615380400285 or mail to sales2@liwei-chem.com.

    We will respond to you as soon as possible.

    Tel: +8615380400285

    Email: sales2@liwei-chem.com

    Inquiry

    Get Free Quote of Anhui Liwei Chemical Co., Limited.

    Flexible payment, competitive price, premium service - Inquire now!

    Certification & Compliance
    More Introduction

    Sinopec PVA 097-60 is a partially hydrolyzed polyvinyl alcohol grade manufactured via continuous alcoholysis of polyvinyl acetate, yielding a granular or powdered resin with a hydrolysis degree controlled within 96.0–98.0 mol% and a 4% aqueous solution viscosity at 20°C in the range 58.0–62.0 mPa·s. The numerical designation 097-60 encodes the grade’s two principal specification anchors: the first segment indicates mean hydrolysis at approximately 97 mol%, while the second denotes viscosity bracket 60, distinguishing it from lower-viscosity grades sharing similar alcoholysis levels, such as PVA 097-27 (27.0–33.0 mPa·s) or higher-viscosity variants like PVA 099-92 (92.0–98.0 mPa·s at fully hydrolyzed ≥99.0 mol%). This mid-range molecular weight, reflected in a weight-average molecular weight typically spanning 120,000–150,000 g/mol, positions 097-60 as a multipurpose workhorse for aqueous binder systems where film flexibility, adhesion to cellulosic substrates, and manageable solution rheology must be balanced against cold-water solubility limits inherent to 97-series hydrolysis.

    Technical Specifications and Quality Conformance

    Batch release testing follows the GB/T 12010 series for polyvinyl alcohol resins. Volatile matter determined by GB/T 12010.3-2010 is held at ≤5.0% for as-supplied powder; material stored or transported under relative humidity exceeding 65% will require pre-drying with dehumidified air at ≤80°C to avoid lump formation during silo discharge and to restore flowability in gravimetric dosing units. Ash content per GB/T 12010.4-2010 is specified at ≤0.7% by mass, reflecting sodium acetate residuals from the alcoholysis catalyst neutralization step. This residual level is critical for applications where ionic contamination influences gelation behavior, notably in polyvinyl butyral (PVB) intermediate production and certain rheology-modified construction compounds. pH of a 4% aqueous solution, measured per GB/T 12010.8-2010, is maintained between 5.0 and 7.0. Purity, expressed as alcoholysis degree via GB/T 12010.5-2010, must fall within the 96.0–98.0 mol% envelope; excursions below 96.0 mol% shift solubility onset temperatures downward but reduce wet strength in cast films, while values above 98.0 mol% narrow the processing window for cold-water dissolution and elevate solution cloud points, complicating processing in jacketed vessels without pressurized heating.

    When comparing 097-60 against the partially hydrolyzed 088-50 (86.0–89.0 mol%, viscosity 49.0–55.0 mPa·s), the primary differentiator lies in the residual acetyl content. 088-50 retains 10–12 mol% acetate groups that disrupt interchain hydrogen bonding, resulting in cold-water solubility at ≤20°C but a lower glass transition temperature and reduced barrier properties to polar organic solvents. 097-60, with only 3–4 mol% residual acetate, demands dissolution heating to 60–85°C under continuous agitation—a processing penalty accepted for its superior film tensile strength (dry film typically 40–55 MPa per GB/T 1040.3-2006) and significantly lower equilibrium moisture regain under controlled humidity. Conversely, against fully hydrolyzed grades such as 100-27 (≥99.0 mol%, viscosity 27.0–33.0 mPa·s), 097-60 sacrifices maximum water resistance and thermal stability but delivers a broader hot-water solubility window and notably higher solution viscosity at equivalent solids loading, enabling reduced binder migration rates in paper coating color formulations.

    Why Does 97 mol% Hydrolysis Define the Performance Envelope?

    The 97 mol% alcoholysis target represents a deliberate engineering compromise between crystallinity-driven strength and residual acetate-enabled processing latitude. At 96–98 mol% hydroxyl content, polyvinyl alcohol chains pack into microcrystallites with an average crystallite size of 4–6 nm as measured by wide-angle X-ray scattering, sufficient to provide mechanical integrity to dried films yet small enough that interlamellar amorphous regions retain water permeability and swelling capacity. This semicrystalline architecture directly explains the grade’s effectiveness in textile warp sizing: the film coating on yarn surfaces must resist abrasion during weaving at room temperature but must be completely desized in hot water baths at 80–95°C without enzymic or oxidative assistants. Grades below 95 mol% hydrolysis often fail the abrasion resistance requirement on high-speed air-jet looms operating above 800 picks per minute; grades fully hydrolyzed above 99 mol% demand impractical desizing conditions that risk thermal damage to heat-sensitive synthetic blends. The narrow viscosity band of 58–62 mPa·s for 097-60 further ensures that size pickup on slasher machines running at 60–120 m/min remains within 8–14% add-on without excessive squeeze roll pressure adjustments, a direct consequence of the polymer’s Newtonian plateau extending to shear rates typical in size box circulation.

    In paper surface sizing, the interplay between hydrolysis degree and viscosity governs binder holdout and film continuity. On metered size presses operating at 800–1,500 m/min, a 4–6% solids solution of 097-60 applied at 0.5–1.5 g/m² dry pickup reduces Cobb 60 water absorptiveness values (measured per ISO 535:2014) by 40–60% relative to unsized base paper, while maintaining surface strength as quantified by IGT pick resistance exceeding 2.0 m/s on coated woodfree grades. This balance is less favorable with lower-hydrolysis grades, which plasticize under calender nip temperatures above 120°C, and with fully hydrolyzed grades, whose solutions at equivalent viscosity would require lower molecular weight polymers that lack the necessary film cohesion.

    Where extremely dry, free-flowing powder is required for dry-blend construction compounds—specifically cementitious tile adhesives conforming to EN 12004 or self-leveling underlayments tested per EN 13813097-60 is added at 0.3–1.0 wt% of binder to enhance open time and wetting characteristics on absorbent substrates. At these low addition levels, the polymer dissolves during mixing with water, increasing mix water viscosity only marginally (typically 5–15% rise in Brookfield viscosity at 20 rpm), yet it markedly retards skin formation by migrating to the mortar-air interface. Published data for this specific configuration regarding open time extension at +23°C/50% RH indicates an increase from 20 minutes to approximately 35–45 minutes as measured by wetting capability retention, though exact values depend on cement type and aggregate gradation.

    Precautions: Avoid combining 097-60 with high concentrations of borate ions or certain multivalent metal salts in alkaline media without pre-testing, as instantaneous gelation can occur through didiol complexation, resulting in intractable lumps that clog inline static mixers. In emulsion polymerization used as a protective colloid for vinyl acetate homopolymer and copolymer latices, 097-60 requires addition at 2–5% by weight of monomer in a pre-dissolved aqueous phase charged to the reactor before initiation. Its medium molecular weight provides sufficient grafting efficiency to stabilize particle nucleation while avoiding excessive latex viscosity that would impede heat transfer in jacketed stainless steel reactors equipped with anchor/paddle agitators. This grade competes with specialty partially hydrolyzed polyvinyl alcohol grades from other Asian suppliers, but Sinopec’s integrated coal-to-vinyl acetate monomer chain ensures batch-to-batch viscosity variation—as measured by the coefficient of variation over 12 consecutive batches—remains below 1.2%, a critical metric for continuous emulsion processes where drift in protective colloid rheology shifts particle size distribution.

    Key distinguishing parameters between Sinopec PVA 097-60 and adjacent grades in the Sinopec portfolio
    Parameter (Test Method)PVA 088-50PVA 097-60PVA 100-27
    Hydrolysis degree, mol% (GB/T 12010.5)86.0–89.096.0–98.0≥99.0
    Viscosity, 4% aq., mPa·s (GB/T 12010.3)49.0–55.058.0–62.027.0–33.0
    Cold-water solubility (10°C)Fully solubleInsoluble; requires ≥60°CInsoluble; requires ≥85°C
    Typical dry film tensile strength, MPa (GB/T 1040.3)30–4040–5555–70
    Equilibrium moisture at 65% RH, %8–106–85–7
    Primary application domainCold-water dissolvable films, detergentsTextile sizing, paper coating, constructionHigh-barrier films, PVB feedstock

    When Polyvinyl Alcohol Replaces Starch in Warp Sizing

    Cotton and cotton-polyester warp yarns sized with 097-60 on a single-size-box slasher demonstrate size add-on uniformity enhanced by the polymer’s film-forming ability. A typical sizing formula comprises 6–9% PVA solids, 0.3–0.5% lubricant (typically a coconut-based sulfonated oil), and optional antistatic agent, cooked at 90–95°C for 30–45 minutes. Viscosity stability of the cooked size, monitored over 8-hour run time in a jacketed size box maintained at 85°C, shows drift of less than ±5% from initial Brookfield viscosity, an attribute directly tied to the grade’s low residual catalyst ash and narrow molecular weight distribution. This stability minimizes recalibration of squeeze roll nip pressure and ensures weave room relative humidity adjustments (typically 70–78%) remain within a range that prevents size film brittleness from overdrying. In comparative mill trials, 097-60-sized cotton warps exhibited approximately 25–35% fewer loom stops per 100,000 picks compared to acid-modified starch-sized warps on identical rapier looms running 650 ppm, at a size cost penalty offset by reduced sizing agent consumption per meter of finished fabric.

    Rheological Considerations in High-Speed Coating Operations

    Coating color formulations for blade-coated paperboard employing 097-60 as sole or co-binder demand careful viscosity profiling. At 10% solids in water, a Brookfield RVF solution at 20 rpm, spindle 3, 25°C reads between 2,500–4,000 mPa·s, translating to acceptable high-shear viscosity under blade pressures for coat weights of 8–15 g/m². The polymer’s surface activity, originating from residual acetyl groups, contributes to pigment wetting without requiring additional low-molecular-weight surfactants that can cause foaming in the coating circulation loop. Published mill data indicate air entrainment in the return tank for a 097-60-only binder system is reduced by 40–50% relative to a carboxylated styrene-butadiene latex reference, though a combination of the two binders is typically employed to optimize stiffness and print gloss. Where 097-60 is substituted for a lower-viscosity grade such as 097-27, the higher molecular weight increases water retention values—measured with a Grade 4 Whatman filter paper under 0.5 bar pressure—by 15–20%, a critical advantage on lightweight coated papers where excessive dewatering into the base sheet causes blade scratches.

    In the production of polyvinyl alcohol-based adhesives for paper converting, 097-60 is dry-blended with fillers and cooked or dissolved in heated high-shear mixers. The resulting adhesive exhibits a setting speed faster than that of equivalent fully hydrolyzed grades due to earlier onset of gelation upon cooling, an effect amplified when boric acid is added as a crosslinking agent at 0.5–1.5% on PVA weight. Full gelation time at 25°C for a 15% solids solution with 1.0% boric acid is typically 60–90 seconds, compared to over 3 minutes for 100-27, a difference that determines line speed limitations on high-speed labelling machines.

    Regulatory conformance overview for Sinopec PVA 097-60
    Regulation / StandardScopeStatus
    EU REACH Regulation (EC) No 1907/2006Registration for substance as intermediate and formulated productCompliant (registered by OR)
    FDA 21 CFR §176.170Components of paper and paperboard in contact with aqueous and fatty foodsSubstance cleared subject to extractives limitations
    FDA 21 CFR §175.105Adhesives for indirect food contactCompliant
    RoHS Directive 2011/65/EURestriction of hazardous substances in electrical and electronic equipmentNot applicable to polymer matrix; no intentionally added restricted substances
    GB 9685-2016Hygienic standard for uses of additives in food contact materialsListed for paper and paperboard with specific migration limits