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Anhui Liwei Chemical Co., Limited.

Wanwei PVA 17-88(L) (PVA 088-20)

    • Product Name: Wanwei PVA 17-88(L) (PVA 088-20)
    • Factroy Site: Lingwu, Yinchuan, Ningxia, China
    • Price Inquiry: sales2@liwei-chem.com
    • Manufacturer: Anhui Liwei Chemical Co., Limited.
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    Specifications
    HS Code 825639
    Appearance White granular powder
    Degree Of Hydrolysis 88±1 mol%
    Viscosity 4 Solution At 20c 20.0-28.0 mPa·s
    Ph 4 Solution 5-7
    Ash Content ≤0.5%
    Volatile Content ≤5.0%
    Average Degree Of Polymerization 1700±100
    Particle Size 20-80 mesh
    Solubility Soluble in hot water, insoluble in organic solvents
    Density 0.45-0.60 g/cm³ (bulk density)

    As an accredited Wanwei PVA 17-88(L) (PVA 088-20) factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing 20 kg net per multi-wall paper bag with inner PE liner, palletized and shrink-wrapped for safe transport and storage.
    Container Loading (20′ FCL) One 20′ FCL container loaded with Wanwei PVA 17-88(L) (PVA 088-20), securely packed and stowed for safe transport.
    Shipping Wanwei PVA 17-88(L) (PVA 088-20) is shipped as a free-flowing, moisture-sensitive powder in sealed 20 kg multi-layer kraft/PE bags, packed on pallets and shrink-wrapped. It is non-hazardous under transport regulations. Avoid exposure to rain or high humidity; keep bags dry, clean, and away from sharp objects during loading and transit.
    Storage Store Wanwei PVA 17-88(L) in a cool, dry, well-ventilated area away from heat, open flames, and strong oxidizers. Keep the container tightly sealed to prevent moisture absorption and contamination. Protect from direct sunlight and physical damage. Avoid generating dust; use appropriate handling equipment. Maintain stable temperatures and follow local regulations for safe storage.
    Shelf Life Store in a cool, dry place, away from moisture. Shelf life is typically two years from the production date when unopened.
    Application of Wanwei PVA 17-88(L) (PVA 088-20)
    Within the film-transfer surface sizing operation on a modern fourdrinier or gap former, Wanwei PVA 17-88(L) (PVA 088-20) functions as the primary film-forming binder at addition rates of 2.0–4.5 wt% on a dry starch basis when co-blended with oxidatively thinned corn starch. The partially hydrolyzed grade, with a degree of hydrolysis of 86.5–89.0 mol% and a 4% aqueous solution viscosity of 20.0–24.0 mPa·s at 20°C, contributes specific Cobb values of 22–28 g/m² after 60 seconds at a size press pickup of 1.8–3.2 g/m² per side, tested per ISO 535:2023. Compliance anchors to FDA 21 CFR 176.170 for components of paper and paperboard in contact with aqueous and fatty foods, and BfR Recommendation XXXVI for paper in contact with foodstuffs. The mill-scale preparation involves cooking the PVA 17-88(L) granular feed in a jet cooker at 95–98°C for 25–30 minutes to achieve full solubilization prior to blending with gelatinized starch at a starch-to-PVA solids ratio typically between 8:1 and 12:1. Critical to downstream converting operations is the IGT dry pick resistance, which shifts from 1.2 m/s with neat starch to 2.8–3.5 m/s with the PVA-modified formulation per ISO 3783:2015, measured on clay-coated linerboard. A documented operational boundary arises when rod metering size presses run surface speeds exceeding 1,200 m/min: the low-viscosity profile of the 088-20 grade can reduce film splitting efficiency, necessitating a minimum wet-film caliper of 12 µm at the nip to prevent skip-coating defects. Terminal converted products include virgin-fiber linerboard, white-top testliner, and coated folding boxboard for pharmaceutical secondary packaging.

    What governs the desizing efficiency of PVA 088-20 on high-speed air-jet looms?

    In spun cotton and polyester-cotton blend warp sizing, the adopted addition level of PVA 17-88(L) ranges from 6.0–10.0 wt% of the sizing liquor total solids, with the balance composed of oxidized maize starch, acrylic co-binder, and a lubricant wax dispersion at 0.3–0.5% of total formula mass. The primary regulatory framework is ZDHC MRSL Version 3.1, specifically prohibiting intentionally added nonylphenol ethoxylates in the spin finish or after-wax, and OEKO-TEX Standard 100 Annex 4 for residues on finished woven fabric intended for direct skin contact. The size liquor is prepared in a high-shear pressure cooker at 105°C for 20 minutes and maintained at 82–85°C in the size box of a multi-cylinder slasher running at 60–100 m/min. The key process parameter is the squeeze roll pressure setting of 12–18 kN/m across the nip, which directly controls size add-on to 8–14% on warp yarns of Ne 20–40. Trough viscosity stability under continuous cooking conditions defines the operational fitness of the 088-20 grade: viscosity decay of less than 8% over a 6-hour size-box dwell is a measured parameter using a Brookfield LV viscometer, spindle #2 at 60 rpm, cross-checked against ASTM D445-21. Desizing on the downstream continuous open-width wash range requires a hot-water solubility window above 70°C, and the 17-88(L) specification of ≤0.5% insoluble gel particle content per ISO 16247:2004 enables a residual size content of less than 0.15% o.w.f. after four wash boxes operating in counterflow at 90–95°C. Process failure at the weaving stage manifests when air-jet looms running at 800–1,200 picks/min record drop-wire stop rates exceeding 4.5 stops per 100,000 picks, traced to inadequate size film cohesion under high-frequency cyclic flexural stress. Converted end-products include dyed and printed shirting fabrics, pocketing, and bleached white bed linen sheeting.Where PVA 088-20 serves as the protective colloid in the emulsion polymerization of vinyl acetate homopolymers and vinyl acetate-ethylene (VAE) copolymers, the charged quantity falls between 3.0–6.0 wt% based on the total monomer feed in batch processes, and 4.0–8.0 wt% in semi-continuous delayed addition profiles designed to control particle nucleation rate. The applicable regulatory template includes the EPA 40 CFR Part 63 National Emission Standards for Hazardous Air Pollutants for Polymer and Resin Production (Subpart U) for residual monomer stripping, and REACH Annex XVII entries for vinyl acetate monomer classification. The semi-continuous polymerization is conducted in a glass-lined, jacketed reactor of 10–25 m³ capacity, equipped with a pitched-blade turbine impeller operating at a tip speed of 2.8–3.5 m/s. PVA 17-88(L) is pre-dissolved in demineralized water at 12.0–14.0% solids and charged to the initial reactor fill. Initiation proceeds with a redox couple — typically tertiary-butyl hydroperoxide and sodium formaldehyde sulfoxylate — injected at equimolar rates to sustain a polymerization temperature of 68–72°C within a ±1.5°C control band. The molecular architecture of the resulting polyvinyl alcohol-g-poly(vinyl acetate) graft copolymer, formed via chain transfer to the PVA backbone, determines the latex shear stability profile measured under ISO 13320:2020 particle size distribution analysis against a target number-average diameter of 800–1,400 nm. A formulation advisory is recorded: PVA 088-20 exhibits reduced grafting efficiency when the vinyl acetate ethylene content exceeds 18 wt% and the total reactor pressure surpasses 45 bar, evidenced by an increase in coagulum to above 0.08% on a 40-mesh screen. Terminal adhesive grades include D3-class woodworking dispersion adhesives per EN 204:2016 and peelable wall covering pre-pastes packaged in 5–25 kg HDPE pails.

    Core-winding adhesive rheology and the open-time versus green-bond conflict

    In high-speed spiral paper tube winding for cores of 50–150 mm internal diameter, the PVA 088-20-based adhesive compound is formulated to 12.0–18.0% total solids in cold water at 20–25°C, with the PVA portion comprising 40–55% of the dry mixture alongside pregelatinized starch and light calcium carbonate filler. The operative compliance standard is the German BGVV XXXVI recommendation for paper and board for food contact, supplemented by EU No 10/2011 migration testing on the innermost liner ply. Processing occurs on a continuous spiral tube winder at a belt speed of 20–40 m/min, where a doctor bar applies the aqueous adhesive to the ply web at a coat weight of 30–50 g/m² wet. The shear-dependent viscosity of the mix — profiled on a rheometer across a shear rate range of 0.1 to 1,000 s⁻¹ — must maintain a low-shear (0.5 s⁻¹) apparent viscosity above 18,000 mPa·s for slump resistance while allowing high-shear (800 s⁻¹) viscosity below 2,500 mPa·s for smooth blade transfer. A documented processing conflict emerges when ambient humidity during summer months in subtropical converting plants exceeds 85% RH: the open time of the PVA-modified adhesive shortens to less than 8 seconds, versus 14–18 seconds at 55% RH, causing premature skinning on the transfer roll. The remediation involves inline water addition controlled by a process viscometer and a PID-tuned metering pump maintaining viscosity at 3,200 ± 150 mPa·s Brookfield RVT, spindle #4 at 20 rpm per ISO 2555:2018. Terminal wound cores serve textile yarn carriers, pressure-sensitive tape rolls, and stretch film spools.
    Comparative performance profile of PVA 088-20 versus PVA 17-99 in selected application parameters
    ParameterTest MethodPVA 17-88(L)PVA 17-99
    Aqueous solubility at 20°CInternal dissolution time test, 4% solids≤45 min≤90 min (requires heating to 85°C)
    4% solution viscosity at 20°CISO 3105:2019 (Ubbelohde)20.0–24.0 mPa·s25.0–31.0 mPa·s
    Degree of hydrolysisInternal alkoxyl titration86.5–89.0 mol%98.0–99.0 mol%
    Surface tension, 1% solutionISO 304:2020 (Wilhelmy plate)48–52 mN/m55–58 mN/m
    Film tensile strength, 30 µm cast filmASTM D882-1838–42 MPa58–65 MPa
    In interior wall putty and skim-coat compounds based on white Portland cement and hydrated lime binders, PVA 088-20 is dry-blended at 0.8–2.2 wt% of the total powder formulation. The governing performance standard is JG/T 298-2010 (China) for interior putty, specifying a bond strength after water immersion of not less than 0.4 MPa and an initial drying time of less than 2 hours. The water-retention mechanism of the partially hydrolyzed PVA grade operates synergistically with cellulose ethers: when dosed at 1.5 wt% PVA 088-20 and 0.35 wt% hydroxypropyl methylcellulose (viscosity 40,000 mPa·s at 2%), the capillary water loss to a porous concrete substrate at 23°C/50% RH is reduced to 18–22% of total mix water after 30 minutes compared to 35% for the HPMC-only control, measured via filter-paper water-retention apparatus per ASTM C91/C91M-23 modified procedure. The dry-mix is factory-blended in a horizontal ribbon mixer of 2–5 metric ton batch capacity for 8–12 minutes, then packed in 20 kg three-ply valve bags with a polyethylene moisture barrier liner to prevent hygroscopic clumping during warehouse storage in monsoon-affected distribution regions. A critical field limitation is documented: in trowel-applied applications on gypsum plaster substrates with substrate moisture content above 10%, the PVA film at the interface can undergo partial re-emulsification, lowering the adhesion pull-off strength to below 0.25 MPa per ISO 4624:2023. Terminal end-products include single-coat white skim coat, tape-jointing compound for drywall, and lightweight base coat for expanded polystyrene external thermal insulation composite systems (ETICS).

    When chlorine residuals destabilize PVA-protected PVC suspension polymerization

    In the suspension polymerization of vinyl chloride monomer to produce S-PVC resins of K-value 57–70, PVA 088-20 is deployed as the primary suspending agent at 0.06–0.12 wt% based on VCM charge, typically in combination with a secondary dispersant such as a low-hydrolysis (55%) PVA grade or a hydroxypropyl methylcellulose of 50 cP viscosity. The regulatory perimeter is defined by EPA 40 CFR 63 Subpart J for polyvinyl chloride and copolymers production covering residual VCM stripping to below 1 ppm in the dried resin, and the ECHA Restriction Report for VCM under REACH Annex XVII entry 47. The polymerization is carried out in a 100–150 m³ stainless-steel autoclave with reflux condenser, charged with demineralized water at a water-to-monomer ratio of 1.05:1 to 1.20:1. The PVA 088-20 is pre-dissolved to a 5.0% stock solution at 90°C and dosed via a mass flow meter into the aqueous phase prior to VCM injection. Agitation is maintained by a three-tier Pfaudler-type impeller at 70–90 rpm, correlated to a tip speed of 4.5–5.8 m/s. A known process perturbation occurs when municipal water supplies carry a residual free chlorine concentration exceeding 0.5 mg/L into the batch: the oxidative chain scission of the PVA backbone at the 1,2-diol units increases the polydispersity index of the suspending agent, causing a drop in the interfacial tension control efficacy and a measurable coarsening of the PVC particle size distribution from a targeted median diameter of 130–150 µm toward a bimodal profile with a shoulder at 200–250 µm. The in-process remedy is activated carbon filtration of raw water to ≤0.1 mg/L residual chlorine, verified by DPD colorimetric testing. The finished PVC resin finds application in rigid pipe extrusion per EN 1452 and flexible medical tubing per ISO 10993 biocompatibility series.Through the aqueous coating of remoistenable gummed paper tape, PVA 088-20 is formulated at 15–22% solids content with the addition of a hygroscopic plasticizer — typically glycerol at 8–12% of PVA dry weight — and a minor fraction of dextrin (5–10% of total solids). The relevant compliance boundary is FDA 21 CFR 175.105 for adhesives used in articles for packaging, transporting, or holding food, with migration testing conducted under conditions of use simulating the moist paper surface. The coating line configuration comprises a reverse gravure coater applying the warm (45–50°C) solution to a bleached kraft liner of 60–80 g/m² basis weight at a line speed of 80–150 m/min. Dry coat weight is held at 12–18 g/m², and the forced-air drying tunnel operates at 120–140°C air temperature with a residence time of 18–25 seconds to achieve a final moisture content of 4–6% in the adhesive layer. The primary functional metric is the blocking resistance at 40°C/90% RH storage for 48 hours: the unwinding force measured on a tensile tester per FINAT FTM 3 must remain below 600 cN/25 mm width to prevent converting line stoppage. A documented incompatibility exists: combination of the PVA 088-20 formulation with amine-functional silane adhesion promoters intended for difficult substrates leads to elevated pH above 9.2, which accelerates the ester-hydrolysis of residual acetate groups and increases the gel content upon re-wetting, degrading the open tack development curve. Terminal converted formats include 48 mm-wide gummed paper tape for carton sealing, kraft paper sealing tape for courier envelopes, and pre-gummed hinge strips for stamp albums.With a dry-mix addition rate of 0.5–1.2 wt% based on the stucco plaster mass in gypsum wallboard production, PVA 088-20 dissolves into the aqueous gauging water at the pin mixer, contributing to the interfacial adhesion between the hemihydrate-derived gypsum core and the multi-ply, recycled-fiber face and back papers. The applicable product standard is ASTM C1396/C1396M-17 for gypsum board, with the specific bond performance measured as the paper-to-core bond strength per ASTM C473-20, requiring a minimum wet bond of 15 N and dry bond of 25 N on a 75 mm wide specimen. The PVA 17-88(L) powder is pneumatically conveyed from a bulk bag discharge station and dosed via a loss-in-weight feeder into the mixer at a rate synchronized with the board line speed, which typically ranges from 60–120 m/min on a 1.2–1.25 m wide forming belt. The exothermic set reaction of calcium sulfate hemihydrate rehydration reaches a peak temperature of 55–60°C in the core at the cutting knife station approximately 3–4 minutes downstream of the mixer. The PVA film, migrating partially with the water front toward the paper-gypsum interface, strengthens the mechanical interlock zone identified in SEM cross-sections at 500x magnification as a dense, non-porous layer of 40–80 µm thickness. A process failure mode is recognized when the board is overdried at kiln temperatures exceeding 315°C for >45 minutes: the PVA film at the interface thermally degrades via chain scission and coloration to a Gardner index above 3, creating a visible yellow line on the facing paper and reducing the wet bond strength below the 15 N pass threshold. Terminal products include standard 12.7 mm wallboard, 15.9 mm Type X fire-rated board per ASTM E119 fire endurance test, and moisture-resistant green board for bathroom ceiling applications.
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    Certification & Compliance
    More Introduction

    Polyvinyl alcohol grade Wanwei PVA 17-88(L), also commercially interchangeable with the designation PVA 088-20, is a partially hydrolyzed homopolymer manufactured via controlled alcoholysis of polyvinyl acetate. The numerical suffix defines its primary structural parameters: a nominal degree of polymerization of 1700 and a residual acetyl content corresponding to a hydrolysis degree of 86.0–89.0 mol%. The parenthetic “L” denotes a low-ash variant with a residue on ignition not exceeding 0.3% under ISO 1598:1990 test conditions, compared to the standard 0.5% threshold for the non-L analogue. Aqueous viscosity, measured at 4% solids and 20 °C in accordance with ISO 3105:1994 using an Ubbelohde capillary viscometer, falls within 20.0–26.0 mPa·s. Volatile matter is controlled to ≤5.0% and the pH of a 4% solution ranges from 5.0 to 7.0. These attributes position the grade between fully hydrolyzed barrier films and low-viscosity dispersion aids, with the intermediate hydroxyl density enabling a thermal dissolution window 15–20 °C lower than that of a 98–99 mol% hydrolyzed counterpart.

    Why Does an 88 mol% Hydrolysis Level Create a Processable Borax Response Window?

    Partial hydrolysis introduces a blocky residual acetate distribution along the polymer backbone, imparting mild hydrophobicity that retards complete hydration while still permitting complexation with borate ions. In aqueous remoistenable and dextrin-blended adhesive systems, titrating borax (sodium tetraborate decahydrate) at 0.2–1.0 wt% of PVA solids elevates Brookfield viscosity by 30–60% within a pH window of 8.0–9.5, a reversible di-diol crosslink that a fully hydrolyzed grade (≥98 mol%) cannot form due to steric constraints from contiguous hydroxyl sequences. On a Sakurai-type open-time tester operated at 23 °C and 50% RH, a 10% solids formulation based on Wanwei PVA 17-88(L) extends open time to 45–60 s versus 20–30 s for a comparable-viscosity fully hydrolyzed grade, while set speed measured on 200 g/m² kraft linerboard recovers 85% of ultimate fiber tear within 120 s. Processing on a continuous high-shear stator-rotor dissolver (IKA Ultra-Turrax UTL 2000, tip speed 23 m/s) requires pre-swelling the granulate at 18–22 °C for 30 min to avoid fisheye formation; the jacketed vessel is then ramped to 85–90 °C over 20 min with helical-ribbon agitation at 40 rpm. Plant-floor batch logs from corrugated board laminators show that substituting PVA 17-88(L) for a standard 17-88 reduces insoluble gel counts on a 100 µm filter screen by 35–50%, attributed to the lower ash and narrower cation residue spectrum.

    Emulsion Polymerization Protective Colloid and Grafting Efficiency

    Polyvinyl acetate homopolymer and vinyl acetate-ethylene (VAE) copolymer latices stabilized with Wanwei PVA 17-88(L) exhibit a characteristic particle size distribution and rheological profile distinct from those produced with hydroxyethyl cellulose or fully hydrolyzed PVA. When fed as a 10% aqueous solution into a continuous stirred-tank reactor (CSTR) series—first stage 75 °C, 0.6 MPa ethylene partial pressure, potassium persulfate initiation—the 1700 degree of polymerization generates a Huggins constant (k′) of 0.35–0.40 in the aqueous phase, indicative of a mid-range solvent quality that permits interfacial grafting without premature phase separation. Grafting ratio, determined by solvent extraction (Soxhlet, acetone 48 h) and subsequent iodine complexation per DIN 53726, falls between 25% and 35% under these conditions, whereas a 2400-DP, 88 mol% grade elevates grafting to 40–50% at the expense of a 2–3-fold increase in high-shear viscosity. The resulting latices, measured on a Malvern Zetasizer Nano ZS with sample dilution to 0.01% solids, yield a z-average particle diameter of 900–1300 nm with a polydispersity index below 0.15. On a pilot coater running a comma-bar process at 15 m/min, the low coarse-grain count (<50 ppm on a 200 mesh screen) reduces surface defects classed as “fish-eyes” by 0.8–1.2/m² relative to a cellulose ether-stabilized latex of equivalent solids. Published data for adhesive anchorage on corona-treated LDPE (Dyne level 42 mN/m) is limited; however, manufacturers report peel adhesion retention above 80% after 7 d water immersion at 40 °C when the base emulsion combines PVA 17-88(L) with 0.5 wt% of a polyfunctional aziridine crosslinker.

    Warp sizing on air-jet looms operating at insertion rates exceeding 850 ppm imposes a lubricating yet tough film on ring-spun cotton and polyester-cotton blends. Wanwei PVA 17-88(L) delivers a size add-on of 8–12% on a single-end slasher from West Point Foundry configured with 12 drying cylinders graded from 110 °C to 130 °C. The film’s elongation at break, measured at 23 °C and 65% RH per ASTM D882-18, reaches 180–210%, while tensile strength hovers at 45–55 MPa. These values ensure encapsulation that resists shedding under the high-frequency beat-up motion, holding warp breaks below 0.7 per 100,000 picks in a 40 s Ne, 120 ends/inch construction. During enzymatic desizing, a 0.5% α-amylase bath at 65 °C and pH 6.5 degrades the starch component within 8 min, while the PVA film undergoes oxidative cleavage via persulfate or is reclaimed through ultrafiltration with rejection efficiencies exceeding 95% on polysulfone spiral-wound membranes with 5 kDa molecular weight cut-off. This reclamability represents the primary operational divergence from PVA 17-99, whose higher crystallinity reduces cold-water solubility and mandates peroxide boosters for equivalent size removal.

    When Low Ash Content Drops Below 0.3% in Optical-Grade Extrusion and Coating

    Optical clarity in water-soluble film packaging and high-end inkjet receptive layers is governed by the concentration of inorganic residues that scatter incident light at the Mie regime. For Wanwei PVA 17-88(L), a sodium oxide equivalent below 0.25%—confirmed on a Thermo Scientific iCAP 7400 ICP-OES after microwave-assisted digestion in HNO₃/H₂O₂—lowers the yellowness index (YI E313) of a 50 µm cast film to 1.8–2.5, compared to 3.5–5.0 for the standard-ash 17-88. During co-rotating twin-screw extrusion (Berstorff ZE 25, L/D = 40:1) with a glycerol-trimethylolpropane plasticizer package dosed at 15 phr, the melt temperature can be maintained at 195–205 °C without generating conjugated polyene sequences that would yellow the web. Pressure transducers at the strand die register stable backpressure (40–60 bar) with a residence time distribution centered at 90 s. In a multi-layer curtain coater for polyethylene-coated board, a 6% solution of PVA 17-88(L) filtered through 10 µm absolute-rated melt-blown polypropylene cartridges yields a wet-layer thickness of 80 µm and a dry coat weight of 4.8 g/m². Binder migration, quantified via FTIR-ATR peak ratio mapping (C=O at 1730 cm⁻¹ against C–O at 1090 cm⁻¹), remains within ±2% across a 10 cm sampling grid, meeting the uniformity specification for dye-fixation layers in silica-pigmented inkjet media.

    Viscosity Specification Cross-Reference and Processing Limitations

    ParameterWanwei PVA 17-88(L)Wanwei PVA 17-88Wanwei PVA 17-99Kuraray PVA 088-20
    Hydrolysis (mol%)86.0–89.086.0–90.098.0–99.086.0–89.0
    Viscosity¹ (mPa·s)20.0–26.020.0–26.025.0–31.020.0–26.0
    Ash content (%)≤0.3≤0.5≤0.5≤0.3
    Volatile matter (%)≤5.0≤5.0≤5.0≤5.0
    pH (4% aq.)5.0–7.05.0–7.05.0–7.05.0–7.0
    Gelation onset² (°C)~18~18~35~18

    ¹ Brookfield LV, 4% solids, 20 °C, ISO 3105:1994. ² Onset of storage modulus intersection G′/G″ at 1 Hz, 10% aqueous solution.

    Regulatory Compliance and Material Safety Boundaries

    StandardRelevant Scope / ClauseStatus for 17-88(L)
    FDA 21 CFR175.300 – Resinous and polymeric coatings; 176.170 – Components of paper and paperboard in contact with aqueous and fatty foods; 176.180 – Components of paper and paperboard in contact with dry foodCompliant at specified extractives limits
    EU 10/2011Plastic materials and articles intended to come into contact with food; Overall migration limit 10 mg/dm² (Annex I)Meets OML for aqueous simulants under 40 °C/10 d testing
    REACH (EC) No. 1907/2006Substance registered; no SVHC inclusion as of the last ECHA updateFull registration
    CONEG / TPCHHeavy metals: sum of Pb, Hg, Cd, Cr(VI) <100 ppmIndependently verified below threshold

    Operational boundaries must be observed: aqueous solutions stored below 15 °C without antimicrobial preservative exhibit mold growth within 48–72 h; the presence of multivalent cations (Fe³⁺, Al³⁺) above 20 ppm induces ionic crosslinking and irreversible gelling. Amine-based additives, including alkanolamines used as pH adjusters in certain adhesive formulations, accelerate discoloration during hot storage and are to be avoided where color stability is a specification parameter.