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Anhui Liwei Chemical Co., Limited.

EVOH EVAL F171B

    • Product Name: EVOH EVAL F171B
    • 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 162662
    Product EVOH EVAL F171B
    Resin Type Ethylene vinyl alcohol copolymer
    Ethylene Content 32 mol%
    Density 1.19 g/cm³
    Melt Flow Rate 1.7 g/10 min (190°C, 2.16 kg)
    Melting Point 183°C
    Glass Transition Temperature 72°C
    Crystallization Temperature 140°C
    Tensile Strength 75 MPa
    Elongation At Break 280%
    Oxygen Transmission Rate 20 µm Film 20 C 65 Rh 0.3 cc/m²·day·atm
    Water Absorption 4.5%
    Refractive Index 1.55

    As an accredited EVOH EVAL F171B factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing EVOH EVAL F171B is supplied in 25 kg net bags, with an inner polyethylene liner to protect against moisture and contamination.
    Container Loading (20′ FCL) EVOH EVAL F171B is loaded as 20′ FCL in sealed, moisture-proof packaging, ensuring safe, dry transport and product integrity.
    Shipping EVOH EVAL F171B is a thermoplastic ethylene-vinyl alcohol copolymer resin supplied as moisture-sensitive pellets. Ship in sealed, dry packaging, preferably vacuum-sealed aluminum-lined bags or drums. Protect from humidity, heat, and direct sunlight during transit. Store below 30°C. Non-hazardous for transport; avoid contamination and extreme conditions.
    Storage Store EVOH EVAL F171B in a cool, dry, well-ventilated area, away from direct sunlight, heat, and ignition sources. Keep containers tightly closed to prevent moisture absorption, as the resin is hygroscopic. Avoid exposure to humidity and extreme temperatures. Maintain stable conditions, ideally below 30°C, and use within the recommended shelf life to preserve quality.
    Shelf Life Store sealed in original packaging, cool and dry. Shelf life is typically two years from the manufacture date.
    Application of EVOH EVAL F171B

    Refrigerated protein and dairy packaging lines running modified-atmosphere or vacuum-skin formats typically specify a five-layer cast sheet sequence: polypropylene / maleated polyolefin tie / EVOH F171B / maleated polyolefin tie / polypropylene. The EVOH layer is maintained at 5–10% of the total sheet thickness, with finished sheet gauge between 350 µm and 700 µm; for a 500 µm sheet, the EVOH core measures 25–50 µm. The outer polyolefin layers protect the 32 mol% ethylene EVOH from water equilibrium; at 20 °C, 0% RH, the oxygen transmission rate of the sheet can be held to 0.4–0.6 cm³·25 µm/(m²·d·atm) when measured under ASTM D3985, but oxygen permeation rises by more than an order of magnitude when the local relative humidity exceeds 80%. Food-contact compliance is anchored to FDA 21 CFR 177.1360 and EU Regulation (EU) No 10/2011, Annex I; migration testing is conducted with a 10 mg/dm² overall migration limit using food simulants D1 and D2. Downstream, the sheet is produced on cast coextrusion lines with flat die widths of 800–1,200 mm, polished roll temperatures of 25–35 °C, and plug-assisted thermoforming at 135–150 °C with male or female cavity tools. The primary production failure mode is edge delamination at the tie/EVOH interface during thermoforming; peel adhesion is checked by ISO 11339 T-peel on the flat sheet before forming. Terminal finished products include rigid trays for sliced cured meats, smoked sausage, soft-ripened cheese, and modified-atmosphere packs sealed under 70% N₂ / 30% CO₂.

    What Limits Hydrocarbon Permeation in Multi-Layer Agricultural Chemical Bottles?

    Solvent-borne emulsifiable concentrate formulations containing xylene, cyclohexanone, and aromatic C9–C12 hydrocarbon fractions place two opposing demands on a multi-layer bottle, requiring a six-layer extrusion blow moulded container architecture: HDPE outer layer / regrind layer / maleated polyethylene tie / EVOH F171B / maleated polyethylene tie / HDPE inner layer. The EVOH barrier layer is held at 1.5–3.0% of the total wall thickness, equivalent to 40–80 µm in a 1.8–2.5 mm wall. HDPE inner and outer skins combined account for 65–75% of the wall, while regrind is controlled to 20–25% because higher regrind levels increase the melt flow of the HDPE streams and can shift the parison wall-thickness programming. The barrier layer stream is processed at 205–220 °C on accumulator-head blow moulding machines with 6-layer coextrusion die heads and screw L/D ratios of 24:1 to 30:1; water-cooled feed throats and compression-ratio screws in the barrier extruder reduce the risk of feed-bridging at the hopper from partially hydrated EVOH. Chemical compatibility and permeation resistance are tested under ASTM D2684 and against the UN Model Regulations Chapter 6.1 for liquid dangerous goods packaging; a common production specification for xylene-based emulsifiable concentrate is a maximum weight loss of 2% per year at 40 °C when the sealed bottle is stored upright. Finished products are 500 mL, 1 L, 5 L, and 20 L narrow-neck bottles with induction-sealed caps for emulsifiable concentrates, oil-based flowables, and highly active herbicide formulations.

    In passenger vehicle fuel system coextrusion blow molding, the plastic fuel tank is produced as a six-layer parison: HDPE outer / regrind / maleated polyethylene tie / EVOH F171B / maleated polyethylene tie / HDPE inner. The EVOH layer is held at 2–4% of total wall thickness, typically 80–150 µm within a 4–6 mm tank wall, because increasing the 32 mol% ethylene EVOH layer above 4% can lower low-temperature drop impact resistance and raises parison die swell mismatch. The tie layers are specified at 1–2% each, and the regrind layer is limited to 30–40% to retain parison melt strength; regrind particle size is controlled below 1.5 mm to avoid screen-pack pressure fluctuations. Continuous coextrusion blow moulding machinery with 3D die articulation and radial wall-thickness programming runs EVOH F171B at 205–225 °C melt temperature, with die head temperatures 10–15 °C below the HDPE stream to minimize gel formation; the barrier extruder uses a melt pump with 10–15 µm filtration. Hydrocarbon permeation is evaluated under UN ECE R34 Annex 5 at 40 °C using SHED or mini-SHED protocols, with tank-level hydrocarbon permeation reported in grams per square metre per 24 h for the specific certification cycle. North American evaporative emission compliance follows EPA 40 CFR Part 86 evaporative emission test procedures, and fuel soak resistance is screened under SAE J1681 with test fuels containing 10% ethanol. The process boundary is not the dry hydrocarbon barrier but the hydrated alcohol fuel condition: when fuel blends contain methanol or ethanol above E10, published data for this specific configuration is limited, and fuel soak tests under SAE J1681 are required before production release. Terminal products are 40–90 L saddle-shaped or flat fuel tanks for passenger vehicles.

    Barrier Laminates for Oxygen-Sensitive Cosmetic Formulations in Squeeze Tubes

    Cosmetic and personal-care formulations containing retinol, ascorbic acid, benzoyl peroxide, or volatile cyclomethicone require an oxygen and fragrance barrier laminate to meet a 24–36 month shelf-life claim. The tube sleeve is produced by coextrusion blown film or extrusion lamination with a structure of PE / tie / EVOH F171B / tie / PE, where the EVOH layer is 3–7% of the total laminate thickness; in a 250–300 µm printed sleeve, the EVOH layer is 8–20 µm. The polyolefin skins protect the 32 mol% ethylene EVOH from hydration during hot-fill and high-humidity storage, because the oxygen barrier of EVOH F171B reduces significantly above 70–75% RH inside the laminate. Primary packaging compliance in Europe is assessed under EU Regulation (EC) No 1223/2009 Article 17 for cosmetic products and under EU Regulation (EU) No 10/2011 for plastic food-contact migration limits; in the United States, the EVOH layer is evaluated under 21 CFR 177.1360. Downstream conversion takes place on 9-layer blown film dies with die gaps of 1.4–2.0 mm, blow-up ratios of 2.0–2.5, and frost-line heights of 500–900 mm; the EVOH melt stream is held at 215–230 °C while the PE skins are processed at 180–200 °C to prevent interfacial encapsulation defects. Peel adhesion between tie and EVOH is verified by ISO 11339 T-peel; adhesion below 15 N/15 mm after paste filling is associated with crimped-end delamination in production. Terminal finished products include 30–150 mL laminated squeeze tubes for anti-aging serums, peroxide-containing acne treatments, and vitamin C creams.

    Pharmaceutical blister packaging for oxygen-sensitive oral solid dose products is produced on three-layer or five-layer cast sheet lines using PP/EVOH/PP or PP/EVOH/PS structures. The EVOH F171B core is held to 4–8% of the total sheet thickness; for a 300 µm base sheet, the EVOH layer measures 12–24 µm. The forming process uses servo-driven plug-assisted thermoforming at 130–145 °C with forming air pressures of 3–5 bar; the EVOH layer remains above its glass transition temperature while the polypropylene skins retain enough modulus to avoid corner thinning below 60% of the initial sheet thickness. The base sheet is tested under USP <661.1> for plastic packaging systems and the polyolefin contact layers under Ph. Eur. 3.1.5; EVOH is also assessed for global migration under EU Regulation (EU) No 10/2011 and the packaging system is risk-assessed under ICH Q3D for elemental impurities. Oxygen barrier retention after thermoforming is measured by ASTM D3985 at 23 °C, 0% RH and at 23 °C, 75% RH; the difference between the two conditions is the critical specification because thin EVOH layers lose oxygen barrier when hydrated above 70% RH. Terminal finished products are push-through or peel-push blister cards sealed with aluminium foil lidding for cardiovascular agents, proton-pump inhibitors, and desiccant-free unit-dose formats.

    When Aromatic and Ketone Solvents Require Flexible Intermediate Bulk Container Liners

    Flexible intermediate bulk container and drum liner applications for solvent-based inks, coatings, and paint additives use a seven-layer blown film structure: PE skin / tie / EVOH F171B / tie / polyamide / tie / PE skin, or a five-layer PE/tie/EVOH/tie/PE construction when the package is not exposed to external moisture. The EVOH layer is specified at 5–8% of the total film thickness; in a 120 µm liner, the EVOH core is 6–10 µm. The EVOH layer operates in a partially hydrated state because most industrial solvent loads contain 0.2–2.0% water, so oxygen and solvent barrier cannot be predicted from dry-film data alone; liquid chemical permeation tests are conducted in accordance with ASTM D2684 or ASTM D814, while oxygen and water vapor transmission are measured by ASTM D3985 and ASTM F1249. Compliance for dangerous goods packaging follows the UN Model Regulations Chapter 6.1 and the IMDG Code packaging instructions; for non-hazardous industrial chemicals, the film is qualified by the same oxygen and water vapor transmission standards. Downstream conversion occurs on 7-layer blown film lines with 70 mm barrier-layer extruders, 1.2–1.8 mm die gaps, and 2.2–2.8 blow-up ratios; the barrier layer melt temperature is held at 205–225 °C. The terminal products are 200 L drum liners and 1,000 L flexible IBC liners for xylene, methyl ethyl ketone, butyl acetate, and isocyanate-containing formulations.

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    Certification & Compliance
    More Introduction

    EVOH EVAL F171B is an ethylene-vinyl alcohol copolymer supplied by Kuraray under the EVAL trade name. The grade carries a nominal ethylene content of 32 mol%; within the manufacturer’s series notation, F-series resins are the 32 mol% ethylene family, and the F171B designation identifies a specific melt-flow grade. Typical published data list a density of 1.19 g/cm³ per ISO 1183-1:2019 and a melt mass-flow rate of approximately 1.6 g/10 min at 190 °C under a 2.16 kg load per ISO 1133-1:2022. Differential scanning calorimetry per ASTM D3418 gives a melting endotherm near 183 °C. The oxygen barrier of the dry polymer is high: supplier typical data for a 20 µm film at 20 °C and 0 % RH are below 0.5 cm³·20 µm/(m²·day·atm) when measured per ASTM D3985. This barrier is not static because water plasticizes the hydroxyl-rich amorphous phase; at elevated relative humidity the oxygen transmission rate rises substantially. EVAL F171B is therefore used as an internal barrier layer in coextruded films, sheets, bottles, and thermoformed trays for oxygen-sensitive foods such as processed meat, cheese, sauces, and aseptic liquids. Compared with lower-ethylene EVOH grades, it occupies the standard-barrier position: slightly lower dry gas barrier than 27 mol% ethylene types but improved moisture tolerance and melt stability, and substantially higher barrier than 38 mol% or 44 mol% ethylene types.

    How Does the 32 mol% Ethylene Content Govern Crystallinity, Barrier, and Melt Stability?

    In ethylene-vinyl alcohol copolymers, the ethylene repeat unit interrupts the continuous hydrogen-bonding network of vinyl alcohol sequences. At 32 mol% ethylene, EVAL F171B retains sufficient vinyl alcohol content to provide high dry oxygen barrier, but the ethylene comonomer lowers crystallinity, melting point, and glass-transition temperature relative to 27 mol% grades. This has three practical consequences. First, the dry oxygen barrier remains high because crystalline domains and hydrogen-bonded amorphous regions restrict oxygen diffusion. Second, water uptake is lower than in lower-ethylene grades because fewer hydroxyl sites are available per unit mass; this reduces the relative humidity sensitivity of the core layer. Third, the lower melting endotherm near 183 °C and the reduced crystallinity widen the processing window in coextrusion, allowing lower die temperatures and less shear-induced gel formation. The melt is pseudoplastic; the ISO 1133-1 melt-flow value should not be used alone for die design. Capillary rheometry at 210 °C and 220 °C is required to characterize viscosity at coextrusion-relevant shear rates, especially for thin core layers below 10 µm.

    Because EVOH is hygroscopic, open hopper feeding at ambient relative humidity above 60 % can raise pellet moisture above the recommended processing limit. The resin should be pre-dried with desiccant air to a residual moisture content below 0.3 % by weight. Typical drying conditions on production-scale dryers are 80 °C to 90 °C for 4 h to 6 h, but the actual time depends on pellet bed depth, air dew point, and original moisture load. Melt stock temperature should be controlled between 210 °C and 230 °C in barrier film and sheet lines; excursions above 240 °C accelerate thermal degradation, which can cause gel specks, brown discoloration, and acetic-acid odor at the die. Long residence time above 230 °C is a common production-floor failure mode. The resin should not be left in a hot idle extruder; low-density polyethylene is the usual purge material, and the line should be flushed until visual contamination clears. Contact with PVC or PVDC melt streams is to be avoided because acid evolution can degrade EVOH and corrode downstream tooling.

    When EVAL F171B Replaces L171B or H171B in Flexible Barrier Packaging Structures

    A grade-to-grade substitution is not a simple drop-in change. Compared with L171B, a 27 mol% ethylene EVOH, EVAL F171B has moderately lower dry oxygen barrier, lower melting point, and better tolerance of incidental moisture exposure. On a cast film line that struggles with unmelted L-grade gels or moisture-related edge defects, moving to F171B can reduce rejects, but the structure thickness or layer ratio may need to be increased to meet the same oxygen transmission target. Compared with H171B, a 38 mol% ethylene EVOH, F171B provides higher gas barrier but lower thermoformability and pinch-off toughness. In deep-draw tray applications where corner thinning and stress whitening are the limiting defects, H171B may be preferred despite its lower barrier. The following gradient summarizes the position of EVAL F171B among common EVAL grades.

    PropertyL171BEVAL F171BH171BE105B
    Ethylene content27 mol%32 mol%38 mol%44 mol%
    Relative dry oxygen barrier at 20 °C, 0 % RHhighesthighreducedfurther reduced
    Moisture sensitivity at 80–90 % RHhighestmoderatelowerlowest
    Melt processabilitynarrower windowstandard baselinebroader windowbroad window

    Selection is driven by the oxygen transmission requirement under the actual package relative humidity, not by the dry-film datasheet value alone. A converter that must meet a package OTR of 0.2 cm³/(m²·day·atm) at 20 °C and 65 % RH may require a thicker F171B layer than an L171B layer, or a lower-ethylene grade if the line cannot deposit the additional thickness.

    At external relative humidity above 75 %, the oxygen transmission rate of EVAL F171B does not increase linearly. Absorbed water molecules interact with hydroxyl groups, increasing free volume and reducing the energy barrier to oxygen permeation. The measured OTR at 85 % RH can be an order of magnitude higher than the 0 % RH value, depending on thickness, temperature, and laminate construction. In practical packages, the EVOH core is therefore not exposed directly to the external environment. Polypropylene or high-density polyethylene outer layers retard moisture ingress, but they do not eliminate it; the design calculation must consider water activity at the EVOH core after the intended shelf life. Protective-layer thickness, tie-layer continuity, and water-vapor transmission rates of the outer layers are as important as the EVOH grade. Published data for EVAL F171B in all possible laminate configurations is limited; converter trials with conditioned barrier testing are required for shelf-life validation.

    Screw Design, Residence Time, and Purge Protocols for Barrier Coextrusion

    In production-scale barrier lines, EVAL F171B is usually processed on single-screw extruders with L/D 24:1 to 30:1 and a compression ratio of 2.5:1 to 3.5:1. Metallic clearances in the nonreturn valve and die should be maintained to avoid dead zones; stagnant melt degrades quickly above 220 °C. Temperature profiles are typically ramped from 180 °C at the feed section to 210–220 °C at the metering section, with the adapter and die held at 220–230 °C. Actual settings must be trimmed for screw speed, backpressure, and output rate, because shear heating can raise the melt temperature above the barrel setpoint. At the die, layer-to-layer viscosity matching with the tie resin and adjacent polyolefin is critical for interfacial stability; if EVAL F171B is far less viscous than the tie layer at the relevant shear rate, layer waviness and incipient encapsulation can occur. For shutdown, the extruder should be purged with low-density polyethylene and not left filled with EVOH under heat. Startup after idle periods should be preceded by visual inspection of the die exit for crosslinked gels.

    In rigid container coextrusion blow molding, EVAL F171B is used as the barrier layer in polypropylene and high-density polyethylene bottles for sauces, ketchup, and edible oils. The layer structure is usually a six-layer or seven-layer arrangement with regrind layers separating the barrier from the skins. The melt temperature of the EVOH is held at the lower end of its range to match the viscosity of the molten polyolefin; if the EVOH is overheated, it wets the die lip unevenly and can form drip strings at the parison cut. When the parison is pinched at the bottom, F171B contributes higher melt strength than a 44 mol% ethylene grade, reducing weld-line thinning, but it is less tolerant of deep pinch deformation than H171B. Blow molding trials that measure barrier retention at the sidewall, shoulder, and pinch-off areas are necessary because wall thickness distribution controls the local oxygen transmission rate.

    Under European and United States food-contact regimes, EVAL F171B is normally covered by supplier declarations for ethylene-vinyl alcohol copolymers. In the European Union, finished-article compliance is assessed under Regulation (EU) No 10/2011; the overall migration limit for plastics is 10 mg/dm² unless a stricter specific migration limit applies to a listed substance. In the United States, EVAL resins are generally considered food-contact substances under FDA 21 CFR 177.1360, subject to grade-specific limitations recorded in the manufacturer’s food-contact statement. The converter remains responsible for verifying that adhesion to tie resins, printing inks, and lamination adhesives does not raise migration above the applicable limits. For non-food industrial packaging, supplier documentation typically includes REACH and RoHS statements; heavy metals and substances restricted under Directive 2011/65/EU are not intentionally added, but this does not waive lot-level verification when the package is supplied to regulated electronic or automotive streams.

    AreaStandard or test methodCondition / criterion
    Melt mass-flow rateISO 1133-1:2022190 °C, 2.16 kg; approximately 1.6 g/10 min
    DensityISO 1183-1:2019Method A; 1.19 g/cm³
    Melting pointASTM D3418DSC; near 183 °C
    Oxygen transmission rateASTM D398520 °C, 0 % RH; supplier-reported
    European food contactEU 10/2011overall migration 10 mg/dm²
    United States food contactFDA 21 CFR 177.1360grade-specific food-contact statement

    In multi-layer flexible packaging, EVAL F171B is commonly deposited as a core layer of 5 µm to 15 µm depending on the package oxygen transmission target and the expected distribution relative humidity. On a five-layer cast film line, a typical configuration places the EVOH between two maleic anhydride-grafted polyolefin tie layers, with polyolefin skins providing heat-seal and moisture-barrier functions. The limiting process conflicts on such lines are usually in the die entrance, where unstable layer interfaces produce optical haze, and in edge trim recycling, where EVOH contamination of polyolefin trim can reduce film clarity and seal integrity. Edge trim containing EVAL F171B is more difficult to reuse directly in the skin layer; it is usually directed to an internal layer or kept as mixed-polymer scrap. In retort pouches and hot-filled containers, the post-retort oxygen barrier measured after water absorption is the controlling design value, not the dry-film datasheet oxygen transmission rate. Converters should condition finished packages at the intended worst-case temperature and relative humidity before setting the EVOH layer thickness.