| HS Code | 193627 |
As an accredited INEOS HDPE ELTEX CAP508S2 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | INEOS HDPE ELTEX CAP508S2 pellets are typically supplied in 25 kg polyethylene bags or 1,000 kg bulk bags. |
| Container Loading (20′ FCL) | 20′ FCL loaded with palletized 25 kg bags of INEOS HDPE ELTEX CAP508S2, shrink-wrapped, total net weight approximately 20,000 kg. |
| Shipping | INEOS HDPE ELTEX CAP508S2 is shipped as non-hazardous HDPE pellets in 25 kg bags, octabins, or bulk trucks/containers. It is not regulated under ADR/IMDG/IATA. Keep dry, clean, and away from direct sunlight/ignition. Standard freight documentation and SDS apply; no special dangerous goods paperwork is required. |
| Storage | Store INEOS HDPE ELTEX CAP508S2 in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, ignition sources, and strong oxidizers. Keep original packaging sealed and pallets off the floor to prevent moisture and contamination. Avoid prolonged UV exposure and static buildup. Use first-in, first-out stock rotation. Do not store outdoors; protect from rain, dust, and physical damage. |
| Shelf Life | Shelf life: typically 24 months when stored unopened in original packaging, dry, below 40°C, and protected from direct sunlight. |
Carbonated soft drink closure production with INEOS HDPE ELTEX CAP508S2 is specified around a melt flow rate of 5.0 g/10 min under ISO 1133-1:2022 at 190 °C/2.16 kg and a density of 0.954 g/cm³ under ISO 1183-1. In a 48-cavity hot-runner injection mould with valve-gate sequencing and a reciprocating screw of L/D 24:1, the processing window is constrained to a barrel profile of 210–235 °C, a hot-runner manifold set point of 220–230 °C, and a mould coolant inlet temperature of 9–12 °C; deviation of melt temperature by more than ±5 °C from the set point shifts the neck diameter after demoulding and reduces top-load consistency at the capping head. Compliance for EU beverage contact is managed under (EU) No 10/2011 with overall migration testing per EN 1186-1 and specific migration limits for additives; for US submissions FDA 21 CFR 177.1520 applies. Formulation addition ratios on direct injection lines are restricted to 1.5–2.5 wt% colour masterbatch and 0.5–1.5 wt% slip/antiblock masterbatch; clean post-industrial regrind is tolerated at 10–15 wt%, but regrind fractions above 20 wt% shift neck diameter beyond ±0.15 mm in 23 °C dimensional checks. Downstream processing is single-stage injection moulding followed by automated vision inspection and in-line axial top-load verification using a load-cell-equipped closure test station at a crosshead speed of 50 mm/min. Converted parts are 28 mm and 30/25 mm tamper-evident carbonated soft drink closures with slitted bridges and retained neck bands.
Because cap dome deflection under capping head pressure replaces carbonation stress cracking as the limiting failure mode, still water closure moulding with CAP508S2 is operated at a reduced part mass target of 1.8–2.2 g per 29/25 mm closure, a mould temperature of 7–10 °C, and a high-flow hot-runner layout with 0.4 mm valve pins to avoid gate blush at injection linear speeds above 250 mm/s. Compliance is governed by (EU) No 10/2011, including aqueous simulant testing at 40 °C for 10 days, and FDA 21 CFR 177.1520; for drinking water contact in common export jurisdictions, BS 6920-1 or AS/NZS 4020 may be invoked depending on the finished pack certification route. Formulation is typically 100 wt% virgin CAP508S2 with a low-taste colour masterbatch at 1.0–2.0 wt%; slip agent addition above 1.5 wt% increases migration into the water simulant and reduces organoleptic panel scores below threshold. The process utilises high-speed injection machines with clamp force allocation of 0.45–0.55 tonnes per cavity on 96-cavity stack moulds, followed by post-mould cooling on plug conveyors that maintain roundness at 0.10 mm TIR. Finished articles are still water and flavoured water tamper-evident closures in 26 mm, 29 mm, and 30 mm neck finishes.
| Sector | Jurisdiction | Standard | Test method |
|---|---|---|---|
| Carbonated soft drink closures | EU / US | (EU) No 10/2011, FDA 21 CFR 177.1520 | EN 1186-1 overall migration |
| Still water closures | EU / UK / AU | (EU) No 10/2011, BS 6920-1, AS/NZS 4020 | Aqueous simulant migration |
| Pharmaceutical closures | US / EU | USP <661.1>, Ph. Eur. 3.1.3/3.1.4 | USP packaging component testing |
| Cosmetic closures | EU | Regulation (EC) No 1223/2009, REACH | Hinge flexural endurance |
| Household chemical closures | EU / UN | Regulation (EC) No 648/2004, UN TDG | ASTM D1693-21 ESCR |
| Edible oil closures | EU / CN / US | (EU) No 10/2011, GB 4806.7-2016, FDA 21 CFR 177.1520 | EN 1186-2 fatty simulant migration |
Where the closure contacts aqueous parenteral or ophthalmic products, pharmaceutical vial closures and metering dropper caps made from CAP508S2 are processed on electric injection moulding machines with barrier screws of L/D 20:1 to minimise residence time at melt temperatures of 200–220 °C. Compliance is anchored to Ph. Eur. 3.1.3/3.1.4 for polyethylene without and with additives, USP <661.1> for packaging components, and FDA 21 CFR 177.1520; ICH Q3D elemental impurity risk assessment is applied to catalyst residuals in the resin when the finished closure contacts aqueous drug formulations. Formulation addition in this sector is typically 0 wt% colourant for natural translucent closures or 2.0–3.0 wt% titanium dioxide masterbatch for opaque paediatric designs; pharmacopoeia-compliant processing aids are limited to total addition below 0.5 wt%. Mould surfaces are texturised to VDI 24 to reduce ejection drag without external release agents, and processing is performed in cleanroom conditions of ISO Class 7 or better. Terminal products include 18 mm and 20 mm metering dropper closures, tamper-evident syrup caps, and child-resistant push-and-turn closures tested to ISO 8317:2015.
In cosmetic flip-top and disc-top closures, hinge flexural endurance rather than short-term tensile strength determines the process window for CAP508S2; validation is performed by a 45° fold test at 23 °C, and hinge thickness is held between 0.8 mm and 1.2 mm to promote orientation along the folding axis. Injection is performed in 32-cavity cold-runner moulds with sequential valve gates, a melt temperature of 215–230 °C, and a mould temperature of 12–15 °C. Industry compliance for EU cosmetic packaging is under Regulation (EC) No 1223/2009 for the finished article and REACH for substance restrictions; where the closure is paired with a food-contact jar, (EU) No 10/2011 applies to the closure assembly. Additive loadings include 2.0–4.0 wt% colour masterbatch, 0.5–1.0 wt% slip additive for tactile properties, and up to 10 wt% clean regrind; regrind above 15 wt% shortens hinge flexural endurance to failure below 2,500 cycles in the 45° fold test at 23 °C. Process validation includes injection pressure monitoring at the hinge gate with a ±5 bar alarm window and automated vision inspection of hinge white-line formation. Converted caps are HDPE flip-top caps for shampoo, lotion, and body wash bottles in diameters from 24 mm to 33 mm.
Sodium hypochlorite and surfactant-containing detergent packages subject CAP508S2 closures to environmental stress cracking conditions that require validation by ASTM D1693-21 condition B on moulded plaques in 10 % Igepal CO-630 at 50 °C. The grade is processed on 48-cavity injection moulds fitted with pneumatic core-pull systems for tamper-evident band undercuts, with melt temperatures of 220–240 °C, mould temperatures of 15–20 °C, and accumulator-assisted injection giving a fill time below 0.35 s and a holding pressure profile of 40–60 MPa for 0.8 s. Regulatory compliance follows Regulation (EC) No 648/2004 for detergent products, Regulation (EC) No 1272/2008 for hazardous contents, and UN TDG performance requirements when the closure is part of a certified dangerous goods package; resin food-contact status under FDA 21 CFR 177.1520 is retained but does not automatically qualify the finished closure for hazardous liquid transport. Compounding adjustment is typically 1.0–2.0 wt% colour masterbatch, 0.5–1.0 wt% antistat/slip masterbatch, and 0–15 wt% post-industrial regrind; regrind above 20 wt% shortens the F50 transition time in the specified Igepal environment. Finished packaging components are detergent bottle caps, bleach spout caps, and agrochemical measuring closures with induction-seal liners.
Long-chain triglyceride sorption into the sealing liner and cap thread sets the removal torque ceiling for CAP508S2 edible oil closures. Published data for this specific closure configuration under long-term oil contact is limited beyond the manufacturer’s datasheet, so converter validation relies on the following in-mould thresholds. The injection moulding process uses a 24-cavity hot-runner mould with oil-cooled gate inserts at 70 °C to reduce shear heating in the gate land while the cavity wall is held at 10–12 °C and the nozzle melt temperature is 200–220 °C. Compliance for edible oil closures is under (EU) No 10/2011 with fatty food simulant D2 for oils, FDA 21 CFR 177.1520, and GB 4806.7-2016 for China-bound applications; overall migration is measured in 95 % ethanol or iso-octane per EN 1186-2. Formulation ratios are 1.0–2.0 wt% white masterbatch and up to 10 wt% internal regrind; slip additive addition above 0.8 wt% is avoided because it increases exudation into oil simulants and reduces closure removal torque below 150 N·mm after 28 days contact at 40 °C. Process stability is monitored by in-mould cavity pressure sensors requiring a repeatable peak cavity pressure of 25–35 MPa; a cycle-to-cycle shift beyond 5 MPa alters the seal bead flatness on the bore seal design. Terminal products include 28 mm and 31 mm flip-top caps for cooking oil pouches, mayonnaise jars, and condiment bottles.
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