| HS Code | 717138 |
| Oxygen Barrier | Excellent low oxygen transmission rate, preserving product integrity and extending shelf life. |
| Aroma Retention | Strong resistance to permeation by fragrances and essential oils, preventing scent loss. |
| Chemical Resistance | Highly resistant to oils, solvents, and aggressive cosmetic ingredients. |
| Clarity | Provides transparent or translucent layers suitable for premium cosmetic packaging aesthetics. |
| Flexibility | Maintains sufficient flexibility for squeeze tubes and collapsible hoses when co-extruded with other layers. |
| Processability | Compatible with co-extrusion and thermoforming processes used in tube manufacturing. |
| Layer Adhesion | Bonds effectively with tie layers to produce stable multi-layer structures. |
| Low Migrants | Exhibits minimal leachable components, ensuring product purity and compliance safety. |
| Moisture Resistance | Provides moderate water vapor barrier, reducing humidity-related degradation. |
| Thermal Stability | Withstands typical processing temperatures during extrusion and molding. |
| Recyclability | Usable in engineered multilayer designs that support material recovery streams. |
| Tensile Strength | Offers adequate mechanical rigidity to resist puncturing and deformation in thin layers. |
As an accredited EVOH for Cosmetic Plastic Tubes & Hoses factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | EVOH resin supplied in 25 kg sealed moisture-proof bags, packed on pallets, for cosmetic tube and hose extrusion. |
| Container Loading (20′ FCL) | 20′ FCL shipment of EVOH resin for cosmetic tubes/hoses, packed in sealed bags, secured on pallets, protected from moisture and contamination. |
| Shipping | EVOH for cosmetic tubes & hoses is shipped in moisture-barrier sealed bags or drums, palletized and stretch-wrapped to prevent contamination. Standard transit is 7-15 days via sea or air freight. Handle with care, keep dry, and store below 30°C away from direct sunlight. |
| Storage | Store EVOH resin in a clean, dry, cool, well-ventilated area, away from direct sunlight, heat, and ignition sources. Keep containers tightly sealed to prevent moisture absorption and contamination. Avoid contact with strong oxidizers. Maintain stable room temperature and use a first-in, first-out system to ensure freshness and consistent processing performance. |
| Shelf Life | Shelf life: 24 months from production date when stored in a cool, dry place, protected from moisture and direct sunlight. |
EVOH barrier layers in cosmetic tubes and hoses are specified when oxygen-sensitive actives, fragrance partitioning, or flavour retention demand an oxygen ingress barrier beyond that of polyolefin-only structures. The following application scenarios are limited to documented downstream manufacturing configurations and do not include pharmaceutical parenteral or medical device uses where separate ISO 10993 or pharmacopoeia requirements apply.
In a five-layer PE/tie/EVOH/tie/PE tube body for a 0.5 wt% retinol facial cream, the EVOH layer is specified at 12–15 µm within a 300–350 µm wall, equivalent to 3.8–4.6 wt% of the tube body compound. Oxygen ingress through the sidewall is controlled by a 32 mol% ethylene EVOH; oxygen transmission of the tube body is assessed according to ASTM D3985-17 at 23 °C and 0 % RH, with typical values between 0.02 cm³/(m²·day·atm) and 0.08 cm³/(m²·day·atm). Migration of retinol into the inner LDPE layer is a separate failure mode and is not directly addressed by oxygen transmission testing; package compatibility studies under ISO 22716:2007 and Annex I of EU Regulation (EC) No 1223/2009 record batch-specific inner-layer extractables data before filling.
On production-scale five-extruder lines, the outer PE extruder is a 45 mm 24:1 L/D single-screw, the EVOH extruder is a 35 mm 28:1 L/D barrier screw, and the inner PE extruder is a 45 mm 24:1 L/D single-screw. The EVOH melt temperature is held at 200–230 °C; above 235 °C amber gel particles appear after 8–10 min residence time in the adapter and die, generating visible specks in the tube wall and forcing a purge with LDPE at 210 °C. Tie layers are maleic anhydride-grafted polyethylene at 8–15 µm each, applied through two separate extruders or through a feedblock with tie-layer split. The spiral mandrel die operates at 20–30 bar melt pressure. The extruded sleeve is cut, the shoulder is injection molded from cosmetic-contact LDPE, and tubes are filled under vacuum. Terminal formats are 30 mL and 50 mL tubes for retinol creams, ascorbic acid serums, and tocopherol/ubiquinone anti-aging emulsions.
The limiting operational boundary is moisture sensitivity of EVOH. At 65 % RH, oxygen transmission of the barrier layer increases to 0.5–1.2 cm³·mm/(m²·day·atm) when conditioned and tested per ASTM D3985-17 at 65 % RH. The outer LDPE and tie layers reduce relative humidity at the EVOH surface to 45–55 % RH when ambient humidity is 65 % RH; at ambient 90 % RH, the EVOH surface approaches 70–75 % RH and oxygen barrier deteriorates by a factor of 10–20. Tubes intended for bathroom storage therefore require an outer HDPE cap or moisture shielding layer, and pre-drying of EVOH resin to < 0.05 % moisture with a desiccant dryer at 80–90 °C is mandatory before extrusion.
| EVOH grade ethylene content (mol%) | Layer thickness (µm) | OTR at 23 °C, 0 % RH (cm³/(m²·day·atm)) | OTR at 23 °C, 65 % RH (cm³/(m²·day·atm)) |
|---|---|---|---|
| 27–29 | 12 | 0.03–0.05 | 0.4–0.8 |
| 32 | 12 | 0.05–0.16 | 0.5–1.2 |
| 38–44 | 12 | 0.30–0.80 | 1.5–3.5 |
Alkaline pH 9.5–10.5 hair colour developer in a 250 mL hose requires an inner LDPE or LLDPE layer of 80–120 µm to prevent direct contact between the developer and the EVOH barrier. Fragrance partitioning into the polyolefin inner layer is controlled by the lipophilic character of the fragrance compounds; EVOH does not reverse this partitioning, but it reduces oxygen-driven oxidation of fragrance aldehydes and terpenes during shelf life. The EVOH layer is inserted as the third of seven layers at 10–20 µm, representing 4.2–5.8 % of the total hose wall and 3.5–5.0 wt% of the multilayer compound. Oxygen transmission of the hose wall is tested according to ASTM D3985-17 at 23 °C, 0 % RH; hoses with 10 µm EVOH show 0.05–0.15 cm³/(m²·day·atm), while 20 µm EVOH hoses show 0.02–0.06 cm³/(m²·day·atm).
The seven-layer hose is coextruded on a line with a 50 mm 30:1 L/D outer HDPE extruder, a 30 mm 30:1 L/D EVOH extruder with barrier-flight screw, and tie-layer extruders for maleic anhydride-grafted PE at 8–12 µm. Melt pressure before the feedblock is 180–220 bar; the EVOH residence time is held below 20 min because EVOH forms crosslinked gel particles that cannot be removed without die cleaning after extended heat history. Shutdown purges use LDPE at 210 °C. The hose is corrugated in-line, cut to length, and assembled with injection-moulded taper and dispensing brush tips. Regulatory documentation references REACH Regulation (EC) No 1907/2006 Annex XVII restrictions for phthalates and heavy metals in plastic packaging, while the cosmetic product safety report follows Annex I of EU Regulation (EC) No 1223/2009.
Intermittent squeeze cycling in hair colour developer hoses produces flexural fatigue at the shoulder-to-hose junction. The EVOH layer is not the primary crack initiation site when tie-layer adhesion is above 2.5 N/15 mm as measured by ASTM F904-16; below that adhesion value, delamination at the tie/EVOH interface creates pinholes after 5,000–10,000 cycles. Final assembled formats are 100 mL and 250 mL developer tubes with nozzle caps and brush tips, filled under nitrogen to reduce oxidative damage to fragrance aldehydes.
A three-layer PE/tie/EVOH dispensing hose for a 100 mL continuous-spray sunscreen is specified with outer diameter 5.0 mm and wall thickness 1.0 mm. The EVOH core is 25–35 µm, corresponding to 5.0–6.5 wt% of the hose compound; this concentration is higher than in squeeze tubes because the small internal volume and high surface-area-to-volume ratio increase oxygen ingress per unit product. The UV filter package includes avobenzone and octocrylene, which degrade through triplet-state and singlet-oxygen pathways; the package cannot prevent photochemical degradation if the hose is transparent, but opaque white PE outer layers block visible and UV light while the EVOH core reduces oxygen ingress. Oxygen barrier is tested at 23 °C, 0 % RH according to ASTM D3985-17; whole-hose values for a 30 µm EVOH layer are 0.01–0.04 cm³/(m²·day·atm).
The hose is extruded on a 25 mm 28:1 L/D EVOH single-screw with a mixing section and a 35 mm 24:1 L/D PE extruder. EVOH melt temperature is maintained at 205–225 °C; outer PE melt temperature above 250 °C can overheat the EVOH in the die and produce interfacial roughness. Vacuum sizing with chilled water at 10–15 °C sets the outer diameter before haul-off. The hose is cut and welded to pump components; final formats are 100 mL and 150 mL continuous-spray bottles filled under nitrogen. Packaging documentation references REACH Regulation (EC) No 1907/2006 and ISO 22716:2007; UV filter stability testing may follow ISO 24443:2012 for simulated SPF after storage, but that method measures product performance and not packaging barrier.
A 75 mL toothpaste tube body is coextruded as a five-layer PE/tie/EVOH/tie/PE sleeve with total wall thickness 250–300 µm. The EVOH barrier layer is 8–12 µm, representing 3.0–4.2 % of the tube wall and 2.8–3.8 wt% of the body compound. This is lower than that used for retinol creams because toothpaste flavour compounds—menthol, eucalyptol, anethole—have higher permissible oxygen ingress limits than retinoids. Flavour retention is not defined by a single ISO method; filled-tube studies use gas chromatographic headspace analysis after 6 months at 40 °C, while oxygen ingress is measured by ASTM D3985-17 at 23 °C, 0 % RH. Compliance references ISO 11609:2017 for dentifrice requirements and ISO 22716:2007 for packaging material acceptance records.
The line configuration uses a 35 mm 24:1 L/D EVOH extruder at 195–220 °C and a 50 mm 28:1 L/D PE extruder. The shoulder is injection molded separately from LDPE without EVOH, creating a barrier discontinuity that is the dominant oxygen ingress path in the finished tube; whole-tube ASTM D3985-17 testing on filled tubes shows shoulder oxygen ingress 3–5 times higher per unit area than through the sidewall. To offset this, the shoulder wall is thickened to 1.0–1.4 mm and sealed with an aluminium-free EVOH-containing laminate membrane over the orifice. Terminal configurations are 75 mL and 100 mL opaque toothpaste tubes for anti-cavity and whitening pastes.
For a recyclable polyethylene tube, EVOH content is capped below 5 wt% of the whole tube, including shoulder and cap, because EU Directive 94/62/EC packaging waste assessments and RecyClass PE film guidelines treat higher EVOH concentrations as incompatible with polyethylene recycling streams. The cap translates to an EVOH layer of 12–18 µm in a 300 µm tube body with a 1.0–1.2 mm HDPE shoulder. At 4.8 wt% loading, EVOH must be present as discrete lamellae; large EVOH domains create gel-like defects in recycled HDPE film at 0.1–0.3 mm thickness. Oxygen barrier of the tube body is measured according to ASTM D3985-17 at 23 °C, 0 % RH; with 15 µm EVOH, values are 0.03–0.08 cm³/(m²·day·atm). This structure is not specified for oxygen-sensitive retinoids in high-humidity bathroom storage because the thinner moisture shielding layers weaken EVOH barrier retention.
Production uses five-layer coextrusion with a 45 mm 24:1 L/D PE screw and a 30 mm 28:1 L/D EVOH screw. The recyclability claim is conditional on local sorting and washing infrastructure; published data for three-dimensional tube recyclability under RecyClass testing is limited because RecyClass protocols primarily evaluate flat films. Completed tube configurations are 50 mL and 150 mL body lotion tubes sold in markets where packaging recyclability is a retail listing criterion.
| Application | Standard/Regulation | Test Method | Control Value |
|---|---|---|---|
| Retinol facial cream tube | EU Regulation (EC) No 1223/2009 Annex I; ISO 22716:2007 | ASTM D3985-17 | OTR ≤0.08 cm³/(m²·day·atm) at 23 °C, 0 % RH |
| Hair colour developer hose | REACH (EC) No 1907/2006 Annex XVII; EU Regulation (EC) No 1223/2009 | ASTM D3985-17; ASTM F904-16 | OTR ≤0.15 cm³/(m²·day·atm) at 10 µm; bond ≥2.5 N/15 mm |
| Sunscreen spray hose | ISO 22716:2007; REACH (EC) No 1907/2006 | ASTM D3985-17 | OTR ≤0.04 cm³/(m²·day·atm) at 30 µm |
| Toothpaste tube | ISO 11609:2017; ISO 22716:2007 | ASTM D3985-17 | Sidewall OTR ≤0.08 cm³/(m²·day·atm); shoulder OTR 3–5× sidewall |
| Recyclable PE tube | EU Directive 94/62/EC; RecyClass PE film guidelines | ASTM D3985-17 | EVOH <5 wt% of whole tube |
| Airless pump hose | ISO 22715:2006; ISO 22716:2007 | ASTM D3985-17; ISO 178:2019 | OTR ≤0.10 cm³/(m²·day·atm); flexural modulus 180–240 MPa at 7 wt% |
The airless pump hose for a water-free 10 wt% ascorbic acid serum is specified with inner diameter 3.0 mm and wall thickness 0.6–0.8 mm. The five-layer PE/tie/EVOH/tie/PE hose uses an EVOH layer of 20–30 µm, corresponding to 5.5–7.0 wt% of the hose compound because the small internal volume and high surface-area-to-volume ratio require a thicker barrier layer than standard squeeze tubes. Oxygen barrier is measured at 23 °C, 50 % RH according to ASTM D3985-17; the hose wall achieves 0.04–0.10 cm³/(m²·day·atm). The higher EVOH loading increases flexural modulus from 120–160 MPa at 3 wt% EVOH to 180–240 MPa at 7 wt%, measured by ISO 178:2019. Cyclic bending beyond 50,000 cycles at the pump connector can initiate EVOH layer fatigue cracks; published data for this specific configuration is limited and must be validated with the final pump geometry.
The hose is extruded on a 20 mm 30:1 L/D single-screw barrier EVOH extruder with melt pump and a 30 mm 24:1 L/D LLDPE extruder. The die is a spiral mandrel with annular gap 0.3 mm; melt temperature for EVOH is 200–225 °C, melt pressure 150–200 bar. Because of the small inner diameter, vacuum calibration is replaced by pressure sizing at 0.4–0.8 bar. The finished hose is cut to 60–100 mm and assembled with a metal-free spring and piston. Final assembled formats are 30 mL and 50 mL airless pump bottles for anhydrous vitamin C serums. Packaging documentation references ISO 22715:2006 and ISO 22716:2007.
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Ethylene-vinyl alcohol copolymer for cosmetic plastic tubes and hoses is supplied as a semicrystalline random copolymer in pellet form, with ethylene comonomer disrupting the hydrogen-bonded vinyl alcohol network. Commercial tube-sidewall grades include Kuraray EVAL F101B and L171B, Soarnol A4412, Soarnol D2908, and equivalent coextrusion products. Ethylene content spans 27 mol% to 44 mol%; melt mass-flow rate at 190 °C/2.16 kg typically ranges from 1.7 g/10 min to 3.2 g/10 min for tube coextrusion, with high-flow variants up to 8–12 g/10 min for thin-wall hose structures. Density is documented between 1.12 g/cm³ and 1.19 g/cm³ under ASTM D792-20. Differential scanning calorimetry per ISO 11357-3 places the melting peak near 191 °C for 27 mol% ethylene and near 158 °C for 44 mol% ethylene. Oxygen transmission for a 25 µm film of 32 mol% EVOH is commonly reported between 0.4 cc/m²·day·atm and 1.5 cc/m²·day·atm at 23 °C/65% RH using a Mocon OX-TRAN 2/21 coulometric sensor per ASTM D3985-17. The resin is therefore used as the central barrier core of five-layer or seven-layer tube sleeves, typically PE/tie/EVOH/tie/PE or PP/tie/EVOH/tie/PP.
Oxygen barrier in EVOH arises from hydrogen bonding among vinyl alcohol segments; absorbed water disrupts this network. When relative humidity increases from 0% to 90%, oxygen permeability of 32 mol% EVOH increases by 8–15 times. This is the main operational limitation in cosmetic squeeze tubes and hoses because the neck and shoulder are repeatedly exposed to humid air, tap water, and condensed moisture from the formula. At an internal core humidity above 75%, the OTR of a 25 µm EVOH layer can shift from below 1 cc/m²·day·atm to 10–30 cc/m²·day·atm depending on ethylene content, orientation, and thermal history. Outer and inner polyolefin skins reduce moisture transfer but do not block it completely. A 350 µm LDPE-skinned sidewall typically transmits water vapour at 2–5 g/m²·day at 40 °C/90% RH, producing gradual humidification of the EVOH core. Moisture uptake of 32 mol% EVOH at 23 °C/85% RH is commonly reported between 5 wt% and 9 wt%. This absorbed water lowers the dry-state glass transition temperature from near 55–62 °C to below 20 °C, increasing chain mobility and allowing greater oxygen, nitrogen, and fragrance molecule diffusion in the neck flex zone. Published data for long-term cosmetic-specific ageing of EVOH tubes at high humidity is limited; most stability programmes therefore use accelerated storage at 40 °C/75% RH for 3–6 months to assess barrier retention.
Tie-resin choice in five-layer tube coextrusion is driven by peel adhesion and rheological matching. Maleic anhydride grafted polyolefins with melt indices between 1 g/10 min and 4 g/10 min at 190 °C/2.16 kg are typically used to bond EVOH to LDPE, LLDPE, HDPE, or PP skins. Adhesion is evaluated after tube-sidewall sealing by ASTM F88/F88M-21; acceptable structures usually require a peel force above 2.5 N/15 mm. On five-layer spiral mandrel dies the EVOH layer is fully encapsulated to avoid surface contact with humid air. For a 350–400 µm sidewall, the EVOH core is commonly 35–50 µm, representing 10–15% of total wall thickness. The functional outer and inner skins each occupy 30–35% of the wall, while tie layers occupy 8–10%. This ratio is not cosmetic decoration alone; it controls water ingress, EVOH humidification rate, and crimp-seal integrity. In high-output coextrusion blow-moulding, layer-ratio drift can occur when the viscosity difference among EVOH, tie resin, and adjacent polyolefin exceeds ±200 Pa·s at 100 s⁻¹ and 210 °C. Comparative production runs on 60–75 mm blown-film and blow-moulding lines with L/D 28:1 have shown that narrowing this viscosity window reduces neck-thinning and annular haze to below 5% gauge variation.
Cosmetic formula interactions with EVOH are dominated by polarity and molecular size. Ethanol, propylene glycol, and short-chain glycolic solvents plasticise the vinyl alcohol phase and can reduce barrier performance by a factor of 2–4 in high-alcohol serums; nonpolar esters and hydrocarbons show lower sorption into EVOH. Published solubility and diffusion data for complete cosmetic formulations are limited, so transfer testing is often performed according to EU 10/2011 with simulants if the tube is intended for dual food-oral-care use. Limonene, linalool, and other terpene fragrance components have high vapour pressures and low molecular weights; their transmission through a coextruded sidewall is governed by skin-layer sorption, EVOH layer thickness, and concentration gradient. When fragrance barrier is critical, a 44 mol% EVOH core may require a thickness increase of 30–50% relative to 32 mol% EVOH to compensate for lower dry-state barrier, but the higher-ethylene grade offers better flex-crack resistance in thin-walled hose profiles.
The substitution of PVdC or aluminum foil with EVOH is a balance of transparency, flexural endurance, and moisture-limited barrier. PVdC maintains lower oxygen permeability at high relative humidity and has low water transmission, but it is chlorinated and releases hydrogen chloride under thermal degradation, complicating melt processing and recycling. Aluminum foil supplies near-zero oxygen and fragrance transmission but forms pinhole defects after repeated crease-flexing, blocks transparency, and prevents metal detection. EVOH provides a halogen-free transparent barrier and is selected in high-flex tube sidewalls where repeated squeezing and cap rotations create intermittent fold lines at the shoulder and crimp. High-ethylene EVOH grades near 44 mol% are specified when stress-cracking resistance is more important than maximum oxygen barrier; these grades exhibit oxygen permeability higher by a factor of 2–5 than 27–32 mol% EVOH under dry conditions. Table 1 summarises comparative oxygen transmission values for monolayer 25 µm films at 23 °C/65% RH; complete tube structures must be tested separately because layer ratio, orientation, and core moisture condition alter the values.
| Material | OTR for 25 µm film (cc/m²·day·atm) | Moisture sensitivity | Sidewall conversion constraint |
|---|---|---|---|
| EVOH 32 mol% | 0.4–1.5 | High; OTR increases >10× at 90% RH | Requires tie layers and hydrophobic skins |
| PVdC | 2–10 | Low; OTR change <2× across RH range | Chlorinated; corrosive processing |
| PA6 | 25–60 | Moderate; plasticises at high RH | Higher flex-crack resistance but lower oxygen barrier |
| PET | 50–100 | Moderate | Moderate fragrance barrier; not sufficient for oxygen-sensitive creams |
| Aluminum foil 9 µm | <0.001 | None | Flex-crack pinholes; opaque |
Processing of EVOH in cosmetic tube sidewalls is constrained by a narrow thermal window. Manufacturer processing guides for 32 mol% EVOH recommend barrel temperatures of 180–225 °C, an adapter set point of 230 °C ±5 °C, and die temperatures of 225–235 °C. At melt temperatures above 240 °C, EVOH forms amber gel particles from vinyl alcohol condensation and degradation; at temperatures below 185 °C, melt fracture and sharkskin can appear at the die lip. Pre-drying in desiccant hoppers at 80 °C for 4–6 h to a moisture content below 0.3 wt% is mandatory. In plants with relative humidity above 60%, hopper heaters and closed feed lines are used to prevent pellet re-moisture. Exposure of molten EVOH at the die exit for 15–30 s to humid air can raise surface moisture sufficiently to produce micro-foaming and visible annular haze. Typical extrusion rates for 35–50 mm diameter tube sleeves range from 20 kg/h to 40 kg/h per extruder on a 60 mm multi-layer blow-moulding line. Tube sidewall sealing is conducted at 170–200 °C with dwell times of 0.8–1.5 s; excessive dwell causes EVOH layer shrinkage at the crimp, while insufficient dwell produces delamination under cap torque.
Steady-state oxygen flux through the tube sidewall is approximated by Fickian transport across the EVOH core. For a multilayer tube, oxygen permeability of the complete wall is dominated by the EVOH layer when skins are polyolefinic. A sidewall with 40 µm EVOH and an EVOH permeability coefficient of 0.05 cc·mm/m²·day·atm at 23 °C/65% RH gives a core-layer OTR of approximately 1.25 cc/m²·day·atm before skin resistance. At an oxygen partial-pressure differential of 0.21 atm, the oxygen flux through the core is near 0.26 cc/m²·day. This calculation supports the use of EVOH in oxygen-sensitive creams, vitamin C serums, retinol preparations, and natural oil formulations. For a 0.02 m² tube surface, a sidewall OTR of 0.1 cc/m²·day·atm corresponds to a flux of 0.021 cc/m²·day at 0.21 atm differential. Actual shelf life depends on product volume, headspace oxygen, and antioxidant capacity. Published data for specific cosmetic formulations is limited; package development commonly uses headspace oxygen analysis over 3–6 months at 25 °C/60% RH and 40 °C/75% RH to validate the barrier design.
The performance envelope of EVOH in cosmetic hoses is bounded by the interaction between barrier layer humidity and product solvent load. In water-in-oil emulsions and anhydrous oils, the EVOH core remains dry through package shelf life and retains low oxygen permeability; in alcohol-based toners and high-glycol formulations, the inner polyolefin layer allows slow ethanol migration, which plasticises the EVOH and raises oxygen and fragrance permeability. For this reason, package engineers may specify 44 mol% EVOH for alcohol-containing products despite its lower dry-state barrier, because higher ethylene content reduces solvent uptake and provides more stable flex-crack performance at low temperatures. The same high-ethylene EVOH is often used in hose profiles where the annular cross-section is repeatedly compressed by pump-actuator overcap retention.
Specifications for EVOH barrier cores in cosmetic tubes are verified by standardised test methods. Cosmetic packaging is assessed under EU Regulation (EC) No 1223/2009; when the tube is also intended for food or oral-care products, migration testing follows EU 10/2011 using simulants assigned to the tube formulation. Table 2 summarises the principal incoming-resin and finished-sidewall methods. Grade-specific technical bulletins control lot-release limits for ethylene content, melt viscosity, and residual volatiles.
| Property | Standard/test method | Typical acceptance window |
|---|---|---|
| Melt mass-flow rate | ISO 1133-1:2022 | 1.7–3.2 g/10 min at 190 °C/2.16 kg |
| Density | ASTM D792-20 | 1.12–1.19 g/cm³ |
| Oxygen transmission rate | ASTM D3985-17 | 0.4–1.5 cc/m²·day·atm for 25 µm film at 23 °C/65% RH |
| Water vapour transmission rate | ASTM F1249-20 | 20–60 g/m²·day at 38 °C/90% RH for 25 µm film |
| Ethylene content | ISO 14663:2016 | 27–44 mol% |
| Peel adhesion | ASTM F88/F88M-21 | >2.5 N/15 mm after seal |
| Visual gel count | Optical inspection | No gel >100 µm in barrier layer |
Published data for cosmetic-specific long-term compatibility of EVOH with high-ethanol serums and terpene-rich fragrance systems is limited. Package qualification therefore depends on storage testing under controlled RH and temperature, because the EVOH oxygen barrier is conditional on core dryness. When aqueous formulations or humid-use environments drive core relative humidity above 75%, the oxygen barrier declines by approximately one order of magnitude, and the finished tube may no longer meet the required oxygen ingress limit for oxidation-sensitive actives. In those conditions, barrier performance differs from PVdC and aluminum-based laminates, which maintain lower moisture-coupled oxygen transmission but carry processing, flex-crack, or transparency constraints.