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Anhui Liwei Chemical Co., Limited.

EVOH EW-3201

    • Product Name: EVOH EW-3201
    • 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 632466
    Ethylene Content 32 mol%
    Density 1.19 g/cm³
    Melt Flow Rate 1.0 g/10 min (190°C, 2.16 kg)
    Melting Point 183°C
    Glass Transition Temperature 64°C
    Tensile Strength 70 MPa
    Elongation At Break 200%
    Oxygen Transmission Rate 0.3 cm³/(m²·day·atm) (20°C, 65% RH, 20 μm film)
    Moisture Absorption 4.5% (20°C, 65% RH)
    Water Absorption 6.5% (20°C, 24 h immersion)
    Refractive Index 1.55
    Haze 2% (20 μm film)
    Solubility In Water insoluble

    As an accredited EVOH EW-3201 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing EVOH EW-3201 is supplied in 25 kg sealed polyethylene-lined paper bags, ensuring moisture protection and safe handling.
    Container Loading (20′ FCL) 20' FCL loaded with 25kg bags of EVOH EW-3201 on pallets, shrink-wrapped, secured, approximately 20 metric tons per container.
    Shipping EVOH EW-3201 is a thermoplastic copolymer resin supplied as pellets in sealed moisture-proof packaging, typically 25 kg bags on pallets. Ship non-hazardous, but protect from moisture, humidity, direct sunlight, and excessive heat. Store in a cool, dry area and handle with care to avoid bag damage.
    Storage Store EVOH EW-3201 in a cool, dry, well-ventilated area, away from direct sunlight and heat sources. Keep the container tightly sealed in its original packaging to prevent moisture absorption and contamination. Avoid exposure to high humidity; recommended storage temperature is below 25°C. Use within the manufacturer’s specified shelf life.
    Shelf Life Shelf life is typically 12 months when stored unopened, airtight, in a cool, dry environment.
    Application of EVOH EW-3201

    In seven-layer blown-film coextrusion lines producing vacuum pouches and modified-atmosphere lidding for processed meat, cheese, and ready-meal trays, EVOH EW-3201 is placed as the internal oxygen barrier core between two maleic anhydride-grafted polyolefin tie layers. The grade designation EW-3201, if interpreted under the common ethylene-content nomenclature as a 32 mol% ethylene vinyl alcohol copolymer, positions the barrier layer in the intermediate ethylene-content window; grade-specific oxygen transmission data for EW-3201 under ASTM D3985 at 23°C and 0% RH should be confirmed against the supplier certificate of analysis, because published data for this specific configuration is limited. The barrier layer is typically applied at 3–10 µm core thickness within a total film thickness of 45–120 µm, corresponding to 4–8 vol% of the structure, with 2–4 µm tie layers on each side and LDPE or LLDPE skins. For oxygen-sensitive processed meat, the packaging specification commonly requires oxygen transmission rate below 0.5 cm³/(m²·day·atm) at 23°C and 50% RH after film conversion; at 0% RH the same EW-3201 core typically reduces transmission by one to two orders of magnitude relative to unbarriered polyolefin films. Processing on a 7-layer blown-film line uses a spiral mandrel die with die gap 1.6–2.2 mm, blow-up ratio 2.5:1–3.2:1, and frost-line height set to stabilise the EVOH core without crystallinity loss. EVOH EW-3201 must be pre-dried in a desiccant hopper dryer at 80°C for at least 4 h to 0.3% maximum residual moisture, with drying air dew point at or below -40°C; barrel profile from feed to metering is typically 180°C, 195°C, 205°C, 210°C, 215°C, and residence time above 200°C is kept below 15 min to prevent gel particles. Adhesion between EVOH and tie layers is measured per ASTM F904 with minimum peel strength 2.5 N/15 mm after 24 h conditioning, and film tensile properties are verified according to ASTM D882 to ensure the EVOH core does not embrittle under vacuum-pack compression. The regulatory basis for food contact includes FDA 21 CFR 177.1360, Regulation (EU) No 10/2011 Annex I, and GB 4806.7-2023, with migration testing under EU 10/2011 conducted as part of the converter’s compliance documentation. Terminal finished products include vacuum pouches, MAP lidding films, and thermoformed meat trays where the EVOH core remains between moisture-protective polyolefin layers to limit oxygen transmission loss above 80% RH.

    What limits hydrocarbon permeation in multilayer fuel tanks under cyclic diurnal load?

    In six-layer blow-molded high-density polyethylene fuel tanks, EVOH EW-3201 is buried as a discrete hydrocarbon barrier layer between two maleic anhydride-grafted HDPE tie layers, with the layer stack commonly configured as HDPE skin/regrind/tie/EVOH/tie/HDPE. The EVOH layer is specified at 1.5–3.0 vol% of total wall thickness; for a tank shell wall of 6–8 mm, the EVOH layer thickness is approximately 0.10–0.40 mm, and the tie layers are each 2–4 vol%. This low addition ratio preserves the impact strength, weldability, and recyclability of the HDPE shell while reducing hydrocarbon permeation under the EPA 40 CFR Part 86 evaporative emission certification procedures and the CARB LEV III requirements; equivalent China 6 limits are enforced under GB 18352.6-2016, and permeation measurement is performed according to SAE J1737 or the sealed housing evaporative determination procedure in 40 CFR 86.1844; EW-3201-specific permeation data for this configuration should be obtained from supplier technical bulletins because published data for this specific configuration is limited. The production process uses an accumulator-head multilayer blow molder with a 6-layer coextrusion head and parison programming to control wall distribution at pinch-off and corners; the EVOH extruder is a 24:1–30:1 L/D barrier screw with compression ratio 3.0:1–3.5:1, and EVOH melt temperature is held between 195°C and 215°C. HDPE melt temperature is maintained at 220–240°C, and the coextrusion head adapter is held at 205–225°C to prevent degradation at the EVOH layer interface. Pre-drying conditions require 80°C for 4–6 h to residual moisture below 0.3%, with a desiccant dryer dew point below -40°C. Once blow molded, the tank shell is cooled in the mold for 15–25 min, and the EVOH layer is inspected by ultrasonic thickness mapping to confirm absence of thinning below 0.08 mm at pinch-off zones. Operational boundaries include the requirement that the EVOH layer not be exposed directly to external moisture or fuel contact—both sides must remain encapsulated by tie layers and HDPE to prevent barrier collapse under humid or solvent swelling conditions. Terminal finished products include automotive fuel tanks and filler pipes where the EVOH layer provides the hydrocarbon barrier required for evaporative emission compliance.

    Before a 1.2 mm five-layer PP/EVOH sheet enters a plug-assist thermoforming cavity, EVOH EW-3201 is coextruded as the central oxygen barrier layer between polypropylene skins and maleic anhydride-grafted PP tie layers. The EVOH addition ratio is held at 3–7 wt% of the sheet, corresponding to an absolute core thickness of 0.08–0.20 mm; thicker EVOH cores above 8 wt% are generally avoided because the sheet stiffness differential and the narrower forming window increase the incidence of plug-stretch thinning at container corners. The flat sheet process uses a 5-layer coextrusion line with a feedblock and flat die, chill-roll stack temperature maintained at 25–35°C, and EVOH melt temperature set between 200°C and 225°C. Pre-drying of EW-3201 is performed at 85°C for 4 h to residual moisture below 0.3%; barrel residence time above 200°C is limited to 15 min to avoid gel formation. The downstream thermoforming step heats the sheet surface to 145–160°C and forms it in a plug-assist machine with plug temperature controlled to avoid sticking; mold temperature is kept at 60–85°C, and draw ratios up to 3:1 are typical for shallow barrier containers. Oxygen transmission rate of the formed container is verified per ASTM D3985 or ASTM F1307, with the EVOH core providing the required barrier for oxygen-sensitive sauces and dairy products at 23°C and 50% RH. The regulatory basis for food contact includes FDA 21 CFR 177.1360, Regulation (EU) No 10/2011 Annex I, and GB 4806.7-2023; compliance testing includes overall migration and specific migration for any residual ethylene-vinyl alcohol oligomers. Terminal finished products are barrier cups, trays, and retort-stable containers for ambient sauces, dairy desserts, and ready-meal components.

    When oxygen diffusion in underfloor heating pipes exceeds 0.1 g/(m³·d) at 40°C

    In five-layer coextruded PE-RT barrier pipes for underfloor heating, EVOH EW-3201 is applied as an oxygen diffusion barrier between two tie layers and PE-RT inner and outer skins, with the pipe wall structure PE-RT/tie/EVOH/tie/PE-RT. The EVOH layer addition ratio is 4–6% of total wall thickness; for a pipe wall of 3.0–4.0 mm, the EVOH layer is 0.10–0.20 mm and is positioned closer to the outer surface to reduce inner-surface damage during fitting installation. The governing compliance condition is DIN 4726:2008, which requires oxygen permeability not exceeding 0.1 g/(m³·d) at 40°C for plastic piping in warm water heating systems, with oxygen diffusion measured under ISO 17455:2005. In the extrusion process, PE-RT skins are processed from a 33:1 L/D single-screw extruder at 220–250°C, while the EVOH layer is processed from a 24:1–30:1 L/D barrier screw at 195–215°C; the five-layer die is maintained at 210–230°C. EW-3201 must be pre-dried at 80°C for 4 h to residual moisture below 0.3% using desiccant air at -40°C dew point. Post-extrusion crosslinking of the PE-RT layers, if silane-crosslinked, occurs at 80–95°C in a water bath or steam chamber; the EVOH layer must not be subjected to external peroxide crosslinking because radical attack can degrade the vinyl alcohol segments and produce gel defects. Inline ultrasonic thickness scanning at 360° around the pipe circumference is used to verify EVOH layer continuity above 0.08 mm, because local thinning below this threshold creates oxygen ingress paths that invalidate the DIN 4726 requirement. The terminal products are oxygen barrier underfloor heating pipes and radiator connection pipes; published field data for EW-3201 in this specific five-layer PE-RT configuration is limited, so supplier monolayer data under ISO 14663-2 should be reviewed before extrusion trials.

    ScenarioRegulatory or standard referenceTest methodMeasured property
    Food packaging filmFDA 21 CFR 177.1360; EU 10/2011 Annex I; GB 4806.7-2023ASTM D3985; ASTM D882; ASTM F904Oxygen transmission; tensile; peel
    Automotive fuel tanksEPA 40 CFR Part 86; CARB LEV III; SAE J1737Sealed housing evaporative determination; ultrasonic thicknessHydrocarbon permeation; EVOH layer continuity
    Barrier sheet and thermoformed containersFDA 21 CFR 177.1360; EU 10/2011 Annex I; GB 4806.7-2023ASTM D3985; ASTM F1307Oxygen transmission
    Underfloor heating pipesDIN 4726:2008; ISO 17455:2005; ISO 14663-2Oxygen diffusion; ultrasonic thicknessOxygen permeability; EVOH layer continuity
    Pharmaceutical barrier bottlesUSP <661.1>/<661.2>; FDA 21 CFR 177.1360; EU 10/2011 Annex IASTM F1307; ICH Q3CPackage oxygen transfer; extractables
    Retort pouchesFDA 21 CFR 177.1390; ISO 11607-1:2019; EU 10/2011 Annex IASTM F1927; ASTM F88; ASTM F904Oxygen transmission; seal strength; peel
    Silage barrier filmsEN 13207:2018; EU 10/2011 Annex IASTM D3985Oxygen transmission

    A 500 mL extrusion blow-molded pharmaceutical bottle with a 5-layer HDPE/tie/EVOH/tie/HDPE wall structure uses EVOH EW-3201 at 2–5 wt% of total bottle mass, equivalent to an EVOH layer thickness of 0.05–0.15 mm in a wall of 0.6–1.0 mm. The EVOH barrier reduces oxygen ingress into oxygen-sensitive pediatric syrups, electrolyte solutions, and desiccant-free effervescent tablet packs, where the packaging oxygen transfer requirement is verified according to ASTM F1307 at 23°C and 40% RH, with acceptance often below 0.1 cm³/(package·day·atm) for the finished bottle. The pharmaceutical packaging regulatory package includes USP <661.1> for plastic components and USP <661.2> for the finished packaging system, supported by FDA 21 CFR 177.1360 and Regulation (EU) No 10/2011 Annex I; extractables profiling is performed under ICH Q3C solvent limits for packaging leachables where required. In production, the five-layer coextrusion blow-molding head is operated with HDPE melt temperature at 210–230°C, tie layer at 190–210°C, and EVOH EW-3201 at 195–215°C; parison programming is used to distribute the EVOH layer around the pinch-off and shoulder regions. Pre-drying is performed at 80°C for 4–6 h to residual moisture below 0.2% because pharmaceutical packaging lines often run lower moisture tolerance to avoid visible splay and gel streaks. Blow mold temperature is maintained at 8–15°C, and cycle time for a 500 mL bottle is typically 12–18 s, depending on wall thickness and line automation. A critical operational limitation is that steam autoclaving at 121°C temporarily saturates the EVOH layer and raises oxygen transmission until the bottle is dried at 23°C and 50% RH for at least 48 h; if immediate post-autoclave barrier is required, the structure should be replaced with aluminium foil laminate or glass. Terminal finished products include barrier bottles for oxygen-sensitive liquid pharmaceuticals and desiccant-free closures where EVOH EW-3201 allows omission of silica gel insert packages.

    Retort pouch interlayer adhesion and post-sterilization oxygen recovery

    In retort pouches and medical device sterile barrier packaging, EVOH EW-3201 is used as the oxygen barrier core in PET/EVOH/PP or BOPA/EVOH/CPP laminate structures, with the EVOH layer representing 5–12% of total film thickness and typically measuring 3–7 µm within a 50–80 µm laminate. The regulatory basis for food retort pouches includes FDA 21 CFR 177.1390 for laminated food contact structures and Regulation (EU) No 10/2011 Annex I; medical device sterile barrier packages follow ISO 11607-1:2019, with oxygen permeation tested per ASTM F1927 and seal strength per ASTM F88. The downstream production process uses either cast coextrusion with adhesive tie layers or dry-bond lamination with aliphatic polyurethane adhesives applied at 2–4 g/m² coat weight; the EVOH film or extruded layer is pre-dried at 80°C for 4 h to residual moisture below 0.3%. When the pouch is retorted at 121°C for 30 min under 0.18 MPa overpressure, the polypropylene inner layer must shield the EVOH core from full steam saturation; immediately after retort, oxygen transmission rises due to moisture uptake, then recovers toward dry values after 48 h at 23°C and 50% RH, measured per ASTM F1927. Interlayer adhesion is verified by ASTM F904 with peel strength above 2.5 N/15 mm after retort; failure at the EVOH-to-tie interface due to hydrolysis of unstabilized adhesive is a known production rejection mode. Terminal finished products include retortable MRE pouches, pet food pouches, and sterile barrier pouches for disposable medical devices, where the EVOH core provides oxygen exclusion without the thickness or cost of aluminium foil.

    At the bale edge of an oxygen-barrier silage film, the EVOH EW-3201 core layer is most vulnerable to oxygen ingress through folds, puncture damage, and weathered tie-layer interfaces, so the film is designed as a 5-layer blown structure with polyolefin skins, tie layers, and an EVOH core representing 3–6% of total film thickness or 5–12 µm within a 150–250 µm film. The governing standard is EN 13207:2018, which specifies requirements for thermoplastic silage films; food contact considerations for silage films used around feedstocks are assessed under Regulation (EU) No 10/2011, although silage films are not generally treated as food contact materials. The EVOH layer is processed on a blown-film line with blow-up ratio 2.5:1–3.0:1, frost-line height 500–900 mm, and EVOH melt temperature 190–210°C; pre-drying at 80°C for 4 h to moisture below 0.3% is mandatory to prevent hydrolysis gel at the die lip. The finished film is surface-treated to 38–42 dyn/cm for printing or sealing, and the EVOH layer is checked by a 360° online thickness gauge to prevent thin bands that would allow aerobic spoilage at the oxygen ingress sites. Published field data for EW-3201 in silage applications is limited, so the converter usually verifies oxygen transmission per ASTM D3985 at 23°C and 50% RH on film samples taken from the bale edge and from the unweathered body, rather than relying on supplier monolayer data alone. Terminal finished products include oxygen-barrier bale wrap, silage clamp sheets, and aerobically stable feed preservation films where the EVOH layer slows yeast and mold growth at the feed surface.

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    Certification & Compliance
    More Introduction

    EVOH EW-3201 is a random ethylene–vinyl alcohol copolymer supplied as pelletized barrier resin for coextruded film, sheet, and blow-moulded container structures. The grade designation is understood in supplier literature to denote a nominal 32 mol% ethylene moiety; reported melt mass-flow rate values fall near 1.1 g/10 min at 190 °C under a 2.16 kg load per ISO 1133-1, with a nominal density of 1.19 g/cm³ per ISO 1183-1. The barrier mechanism is not additive-based; it arises from high hydroxyl-group density, interchain hydrogen bonding, and low fractional free volume in the dry state. In polyolefin-based multilayer structures, EW-3201 is normally placed between two maleic anhydride-grafted tie layers because unmodified polyethylene or polypropylene exhibits inadequate wetting of the polar EVOH surface. The resin is therefore specified in five-layer and seven-layer assemblies, not as a discrete monomaterial film.

    Engineering property Nominal value Standard designation
    Ethylene content 32 mol% internal IR/NMR method
    Melt mass-flow rate 1.1 g/10 min at 190 °C, 2.16 kg ISO 1133-1
    Density 1.19 g/cm³ ISO 1183-1
    Melting point 181 °C DSC, second heat
    Oxygen transmission coefficient, dry 0.5 cm³·20 µm/m²·day·atm at 23 °C, 0% RH ASTM D3985

    What Process-Limiting Defects Appear on Multilayer Lines Above 240 °C?

    Thermal degradation in EW-3201 is governed less by barrel set point than by residence time above 230 °C. Production-scale reports describe gel flecks, yellow streaking, and acetic acid odour when a 32 mol% EVOH melt is retained in stagnant zones at metering temperatures above 240 °C for periods exceeding 10–12 minutes. Extruder configuration matters: a 75 mm barrier screw with 24:1 L/D and compression ratio between 2.5:1 and 3.0:1 is commonly used, but the feed section should remain below 70 °C to prevent pellet softening and bridging. At plant ambient relative humidity above 60%, open handling of EVOH pellets for more than 30 minutes can increase surface moisture; desiccant drying at 85 °C with a dew point below −40 °C for 4–6 hours is standard. Moisture levels above approximately 0.3 wt% in the hopper feed produce bubble defects, down-line viscosity loss, and gauge variation at the die lips.

    The coextrusion window is narrower than for polyolefins because EVOH degradation can generate acidic species that accelerate gel formation. A typical process makes use of a melt temperature between 215 °C and 235 °C, with die temperature held below 245 °C. Start-up and shutdown procedures should use a low-viscosity polyolefin purge rather than extended EVOH hold time. Direct blending of EW-3201 with amine-based antifog masterbatches or alkaline slip additives is avoided in the barrier layer because free amines have been implicated in yellowing and viscosity drift. Where a specifically EW-3201 technical datasheet is not available for a given layered configuration, the process limits above are drawn from published data for the 32 mol% EVOH family and should be confirmed by converter trials.

    Oxygen Barrier Retention Is a Function of Layered Structure, Not Resin Alone

    The oxygen transmission coefficient of EW-3201 is approximately 0.5 cm³·20 µm/m²·day·atm when measured at 23 °C and 0% relative humidity under ASTM D3985. This value is not a fixed material constant in a coextruded package; it changes when water sorbed from wet contents or humid storage plasticizes the EVOH lamella. Published curves for 32 mol% EVOH grades show a gradual increase in oxygen transmission up to approximately 60–65% RH, followed by a nonlinear rise above 65% RH as absorbed water disrupts interchain hydrogen bonding. Consequently, EW-3201 is specified in structures where polyolefin skins and tie layers maintain the internal RH at the EVOH interface below roughly 60% during the intended shelf-life.

    The barrier contribution is normally reported as oxygen transmission rate per unit area for the total multilayer film, not for the resin alone. A 10 µm EW-3201 core between two 10 µm anhydride-grafted tie layers in a polypropylene-rich sheet can produce oxygen transmission rates that differ by an order of magnitude depending on skin layer thickness, filler loading, and orientation. When the same barrier layer is buried between thicker polypropylene skins, equilibrium moisture at the EVOH core is reduced and the oxygen barrier remains closer to its dry-state value. When the structure is thinned or when the EVOH layer is placed too near the package interior, high humidity can raise the oxygen transmission coefficient to 3.0 cm³·20 µm/m²·day·atm or higher under test conditions, depending on tie-layer water transmission and conditioning time. The measurement itself should follow ASTM D3985 after conditioning at the intended RH plateau rather than at a single dry condition.

    EW-3201 differs from a general-purpose 29 mol% EVOH grade in dry oxygen barrier by approximately 15–25%, with the lower-ethylene grade recording a lower oxygen transmission coefficient under dry conditions but a more severe moisture-induced barrier loss at elevated humidity. Compared with a 44 mol% EVOH, EW-3201 retains a lower dry oxygen transmission coefficient but exhibits less moisture tolerance and lower flex-crack resistance in high-fat, high-moisture pouch applications. Compared with a 38 mol% EVOH grade, EW-3201 is generally preferred where dry barrier is the dominant requirement and prolonged retort exposure is not specified. Where published data for this specific configuration are limited, converter qualification should include oxygen transmission testing on the actual coextruded structure at 0%, 65%, and 90% RH.

    Moisture Uptake, Tie-Layer Acid Grafting, and Interlayer Peel Mechanics

    Adhesion between EW-3201 and polyolefin tie layers is not an automatic consequence of melt contact. Maleic anhydride-grafted polypropylene or polyethylene is required, and converter acceptance values are typically based on destructive T-peel tests according to ASTM F904. For nonretort flexible structures, a minimum peel strength of approximately 1.0 N/15 mm is often used; retortable structures may require values above 2.0 N/15 mm after processing. Unmodified polypropylene or polyethylene generally exhibits peel strength below 0.5 N/15 mm against EW-3201, which is insufficient for package integrity under thermoforming or drop-load conditions.

    Moisture uptake at the EVOH–tie interface is a failure mode that is distinct from barrier loss in the core. When package contents are aqueous or when retort steam drives water through the polyolefin skins, water molecules can concentrate at the tie-layer interface and reduce adhesion through plasticization of the anhydride-grafted region. This effect is more pronounced when the maleic anhydride graft level is low or when the tie layer is below 8–10 µm in the finished structure. Coextrusion operators have observed peel failure that initiates at the edge trim and propagates inward after retort, a pattern associated with interfacial moisture rather than bulk EVOH degradation. The corrective action is not always an EVOH grade change; increasing tie-layer thickness, selecting a tie resin with higher anhydride content, or moving the EW-3201 layer closer to the package exterior can restore adhesion.

    EW-3201 is also sensitive to condensation during pellet handling. The resin absorbs atmospheric moisture more rapidly than polyolefin and should not be left in open totes for extended periods in unair-conditioned plants. Pre-drying is required at relative humidity above 60%; fabricators running in tropical conditions typically install closed-loop desiccant drying to maintain pellet moisture below approximately 0.01 wt% before entering the extruder throat. Failure to do so produces surface streaks and local viscosity reduction that may be misdiagnosed as die lip deposition.

    When EW-3201 Replaces Polyamide-6 in Short-Shelf-Life Food Tray Coextrusions

    In dry-food and modified-atmosphere packaging, EW-3201 is sometimes introduced as a halogen-free replacement for polyamide-6 or as a barrier upgrade in polypropylene tray structures. The technical comparison is not based on resin price alone; it is a trade between oxygen barrier, moisture sensitivity, and thermoforming behaviour. Polyamide-6 exhibits a reported oxygen transmission coefficient that is roughly 5–10 times higher than a dry 32 mol% EVOH at equal thickness, but polyamide is less prone to catastrophic barrier loss when equilibrated at high moisture because its barrier loss is already substantial under dry conditions. EW-3201 therefore provides a much sharper dry barrier, but requires polyolefin skins with sufficient moisture resistance to keep the EVOH layer below its RH threshold.

    A common structure is PP/tie/EW-3201/tie/PP at a barrier-layer thickness of 8–15 µm. At those gauges, the oxygen transmission rate of the total tray is often controlled by tie-layer continuity and thermoforming-induced thinning rather than by the intrinsic resin coefficient. Corner thinning below 50% of the nominal barrier layer thickness has been documented on plug-assisted thermoforming lines running high-draw trays, and the resulting local oxygen ingress can exceed the predicted value from flat-sheet permeability data. EW-3201 is selected in these structures for its melt strength during sheet extrusion and for a lower dry-state oxygen transmission coefficient than polyamide-6. Operators should, however, validate thermoformed trays by measuring oxygen transmission perpendicular to the formed sidewall and corner regions rather than relying on flat-sheet data.

    Standard or regulation Scope Relevant condition
    FDA 21 CFR 177.1360 Ethylene-vinyl alcohol copolymers in food-contact articles subject to migration limits and end-use conditions
    EU Regulation (EC) No 10/2011 Plastics intended for food contact overall migration limit 10 mg/dm²
    REACH Registration and SVHC declaration no intentionally added SVHC in the base resin
    RoHS Directive 2011/65/EU Lead, mercury, cadmium, chromium(VI), PBB, PBDE compliance declared for homogeneous material

    Where retort or hot-fill conditions exceed 90 °C for extended periods, EW-3201 is not the first-choice EVOH grade. Higher-ethylene EVOH copolymers typically recover dry barrier more rapidly after steam exposure, although they sacrifice some dry-state oxygen barrier. In short-contact pasteurization up to approximately 90 °C, EW-3201 can perform when the total package design maintains the EVOH core below its critical moisture threshold. For shelf-stable products sterilized above 121 °C, a converter qualification programme should compare oxygen barrier after retort, post-retort adhesion, and flex-crack resistance before replacing an existing high-moisture-tolerant barrier layer.