| HS Code | 340705 |
As an accredited FREP (Fujian Refining & Petrochemical) HDPE HDI54200 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | FREP HDPE HDI54200 is supplied in 25 kg polyethylene-lined woven bags, palletized, or 1,000 kg jumbo bags for bulk shipment. |
| Container Loading (20′ FCL) | 20′ FCL loading for FREP HDPE HDI54200: 25 kg bags, approx. 25 MT per container, secured for sea transport. |
| Shipping | FREP HDPE HDI54200 is typically shipped in 25 kg PP woven bags or 500–1000 kg jumbo bags, palletized and stretch-wrapped. It is transported by truck, rail, or sea container in a dry, ventilated environment, away from moisture, heat, and direct sunlight. Non-hazardous; standard cargo handling applies. |
| Storage | Store FREP HDPE HDI54200 in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, moisture, and strong oxidizers. Keep original bags sealed, palletized, and undamaged; avoid contamination and prolonged UV exposure. Maintain moderate stacking heights to prevent deformation. Use first-in, first-out rotation. Protect from rain. Observe fire precautions and keep away from ignition sources. |
| Shelf Life | The shelf life is 24 months when stored in original packaging under cool, dry, ventilated conditions, away from direct sunlight. |
When FREP (Fujian Refining & Petrochemical) HDPE HDI54200 is run on a 5000 kN hydraulic clamp injection moulding machine with an 80 mm diameter, 22:1 L/D general-purpose screw, open-top pails of 20 L and 25 L nominal capacity are typically filled using a hot-tip gate located in the bucket base rather than a side gate, because the base gate shortens flow length to the rim and reduces incomplete fill at the handle attachments. Melt temperature measured at the nozzle is held between 210 °C and 240 °C, mould temperature is maintained at 12 °C to 28 °C, back pressure is set at 8 bar to 14 bar, and holding pressure is applied at 55 MPa to 75 MPa for 8 s to 15 s, depending on wall thickness and hot-runner pressure drop. The pail wall thickness is specified at 2.0 mm to 3.5 mm for UN-certified dangerous goods packaging; bottom chime and top rim sections are dimensioned at 3.8 mm to 5.0 mm to pass stacking and drop requirements under ADR 6.1.5 and 49 CFR Part 178. Colour masterbatch is introduced by gravimetric side-feeder at 1.5 wt% to 2.5 wt% for carbon black or mineral pigment systems, and 2.0 wt% of a polyethylene-based antioxidant/UV stabilizer masterbatch is recommended when the pail is stored outdoors in tropical break-bulk export routes. Chemical compatibility testing is run according to ASTM D543-21 for immersion of moulded plaques in the specific fill chemical for 21 days at 40 °C; environmental stress-crack resistance is evaluated using ASTM D1693-21 Condition B in 10% Igepal CO-630 at 50 °C, and the lot is released only when the failure time exceeds 200 h for aggressive oxygenated solvents. Density and melt mass-flow rate are verified on every lot by ISO 1183-1:2019 Method A and ISO 1133-1:2022 Procedure A at 190 °C/2.16 kg, respectively; if the melt flow ratio is below the certificate value, injection velocity is increased by 10 mm/s and the transfer position is shifted 2 mm earlier to maintain fill pressure inside the cavity. The terminal article is a straight-walled stackable pail with a tamper-evident tear skirt and an injection-moulded handle of the same grade, used for water-based latex, solvent-borne adhesive concentrates, and liquid detergent packs.
| Property | Standard | Test condition | Lot release criterion |
|---|---|---|---|
| Melt mass-flow rate | ISO 1133-1:2022 | 190 °C/2.16 kg | ±10% of CoA |
| Density | ISO 1183-1:2019 | Method A, 23 °C | ±0.002 g/cm³ of CoA |
| Environmental stress-crack resistance | ASTM D1693-21 | Condition B, 10% Igepal CO-630, 50 °C | no failure before 200 h |
| Chemical immersion | ASTM D543-21 | 40 °C, 21 days, end-use fill | ≤5% mass change |
| Drop test | ADR 6.1.5.3 | 1.2 m, -18 °C | no rupture |
Injection of vented crates for cold-chain primary packaging is carried out on toggle machines of 3500 kN to 8000 kN with accumulator-assisted filling, using two or four hot-tip gates positioned to avoid weld lines along the base corners. The grade is processed at a melt temperature of 225 °C to 250 °C, with a cooling time of 18 s to 35 s for wall sections of 3.0 mm to 4.5 mm; mould cavity pressure at gate freeze is held between 45 MPa and 60 MPa to reduce anisotropic shrinkage after ejection. Collation shrink after 24 h at 23 °C and 50% RH is controlled below 1.2% in the flow direction and 0.9% in the transverse direction using ISO 294-4:2018; when measured shrinkage exceeds this limit, holding time is extended by 3 s and mould temperature is raised to 25 °C from the baseline 15 °C. The rib-to-wall thickness ratio for the crate base is kept at 0.45:1 to 0.60:1 to prevent sink marks and maintain compression stack rating; gate diameter is set at 1.2 mm to 2.0 mm for a nominal flow length of 380 mm to 520 mm. For outdoor logistics crates exposed to UV and sub-zero handling, a hindered-amine light stabilizer masterbatch is dosed at 0.6 wt% to 1.2 wt%, and impact resistance after conditioning at -18 °C for 24 h is verified by ISO 179-1:2010 Charpy notched impact with a minimum of 6 kJ/m²; published data for FREP HDI54200 at this temperature is limited, so incoming-lot verification on a notched injection-moulded specimen is used as the release check rather than relying on producer data. Terminal crates are used for wet fish transport, bakery tray stacking, and pharmaceutical distribution where washdown with sodium hypochlorite at 200 ppm available chlorine at 60 °C must not cause cracking after 100 cycles in a commercial crate washer.
For injection-moulded 38 mm and 45 mm high-density polyethylene closures with tamper-evident bands, the HDI54200 pellet is normally processed at a melt temperature of 215 °C to 235 °C on a 48-cavity hot-runner mould with valve gates of 0.8 mm to 1.2 mm diameter. The cycle time is controlled primarily by closure bridge and tamper band ejection, not by screw recovery, when running on a screw diameter of 45 mm and an L/D of 21:1; fill time is set at 0.12 s to 0.22 s, and hold pressure is limited to 45 MPa to 60 MPa to prevent gate blush and liner-seat distortion. Slitting of tamper-evident bands is conducted inline using rotary slitting knives after ejection at a part surface temperature of 35 °C to 45 °C; when the surface temperature is below 30 °C, slit quality deteriorates and the reject rate for cracked bridges exceeds 2.5%. Dimensional control of the liner seat is measured to a diameter tolerance of ±0.10 mm using a structured-light scanner; lot-to-lot variation in melt mass-flow rate influences seat flatness, so the injection velocity profile is adjusted in 5 mm/s increments based on the certificate of analysis, but only after a hot-runner needle-valve timing check. Organoleptic compliance for dairy and mineral water closures is evaluated under EU 10/2011 with migration testing in 3% acetic acid, 10% ethanol, and 50% ethanol at 40 °C for 10 days, and in the United States under FDA 21 CFR 177.1520; the closure is not released for fatty-food contact above 40 °C unless an oxygen-barrier liner is inserted and the overall migration limit of 10 mg/dm² is confirmed. Terminal products include aseptic UHT milk closures, sports drink caps, and non-carbonated beverage closures for hot-fill applications up to 85 °C when closure cooling water is maintained at 8 °C to 12 °C to preserve tamper-band shape.
With wall stock specified at 0.45 mm to 0.65 mm for round dairy tubs of 200 ml to 500 ml, plastication becomes the limiting constraint when the mould cycle time drops below 3.8 s on a 32-cavity stack mould. The HDI54200 feedstock is processed at a melt temperature of 220 °C to 240 °C and a screw speed of 120 min⁻¹ to 180 min⁻¹, with screw-back pressure set at 10 bar to 14 bar to homogenise the melt without excessive shear heating. On a 60 mm diameter, 22:1 L/D general-purpose screw, recovery time at maximum speed is 1.6 s to 2.2 s for a shot mass of 320 g; if cooling time is below 2.4 s, the screw cannot fully retract before clamp opening, and short feed at the next shot triggers cavity pressure alarms. The mould is run with an injection profiling strategy that reaches 140 mm/s at peak fill and then decays to 35 mm/s during the last 1.5 mm of stroke to prevent flash along the tub rim. Demoulding relies on a stripper plate and pulsed air ejection at 5 bar; part surface temperature at ejection is 55 °C to 65 °C, measured by a fixed infrared pyrometer. Slip/antiblock additive dosing at 800 ppm to 1500 ppm reduces nested-tub separation force in downstream filling lines, but is controlled because excessive slip agent can lower the coefficient of friction below 0.15 and cause stack instability on filling conveyors. Food-contact compliance is maintained under EU 10/2011 and EC 2023/2006 good manufacturing practice, with an overall migration limit of 10 mg/dm² in dairy simulant 50% ethanol at 40 °C for 10 days; the moulding hall is maintained at positive pressure and regrind ratio is capped at 15 wt% of post-industrial scrap from the same production campaign. Terminal dairy tubs are used for stirred yoghurt, cream, and high-fat desserts, but not for retort sterilisation because the HDPE base has insufficient upper service temperature for retort above 100 °C.
High-gloss rectangular storage bins of 2.5 mm to 4.0 mm nominal wall are moulded on a 9000 kN toggle press with a bead-blasted cavity surface of VDI 24 or A2 class, using a fan gate of 3.0 mm width and 1.5 mm depth at the bottom rib junction to reduce visible blush. Melt temperature is set at 230 °C to 250 °C, mould temperature at 30 °C to 45 °C, and injection speed at 60 mm/s to 90 mm/s; the melt is transferred to hold at 95% of filled cavity volume, and hold pressure is held at 50 MPa for 12 s to 20 s to replicate the textured surface and prevent sink marks at side-wall rib junctions. Gate blush area is quantified by image analysis of the surface roughness delta against surrounding cavity steel; the acceptance limit is Ra ≤ 0.5 µm above background according to ISO 4287:1997, and gate land temperature is lowered by 5 °C if blush reoccurrence is detected in statistical process control. Colour masterbatch loading for an opaque mineral-tinted bin is 2.0 wt%, while a pearlescent effect increases loading to 3.5 wt%, requiring an increase in screw-back pressure to 15 bar to improve pigment dispersion. Flexural modulus of the moulded part is measured by ISO 178:2019 on a 80 mm × 10 mm × 4 mm specimen cut from the bin base, with an incoming-lot acceptance value of ≥1000 MPa; if the measured value falls below this limit, the mould is inspected for cooling channel blockage, and hold pressure is increased by 5 MPa before lot release. Closures for these bins are typically injection moulded in the same grade on a separate 1600 kN machine, with the living hinge thickness set at 0.35 mm and hinge flex life tested to 10,000 cycles using a proprietary pneumatic flex fixture at 30 cycles/min without visible cracks. Terminal bins are used in household storage, retail display, and refrigerated storage at temperatures not below -20 °C; the product is not specified for continuous use with hot water above 80 °C because thin side walls may distort under residual moulded-in stress.
Threaded dosing chambers and cap adapters for agricultural sprayers are gated through a ring gate of 0.5 mm thickness at the base of the minor thread diameter to prevent weld lines across the pressure-bearing thread root; the part is moulded at a melt temperature of 220 °C to 240 °C, with a mould temperature of 15 °C to 25 °C and a clamp force of 1800 kN to 4500 kN, depending on cluster size. Thread flank tolerance is held at ±0.08 mm on the pitch diameter, and the mating thread is checked with a non-contact measuring projector after 24 h post-moulding to allow for post-shrinkage of 0.6% to 1.0% across the thread diameter. Incoming-lot environmental stress-crack resistance is tested according to ASTM D1693-21 Condition C in 10% linear alkylbenzene sulfonate at 50 °C; minimum time to 50% failure is set at 96 h for the agricultural grade. The HDI54200 product is not inherently UV-stabilised, so carbon black or hindered-amine stabilizer masterbatch is added at 1.5 wt% to 2.5 wt% for external sprayer caps; without this additive, exposure to 0.50 W/m² UV-A in a Xenon-arc apparatus per ISO 4892-2:2013 for 500 h produces a loss in tensile elongation of more than 30%, and the cap leaks at the thread root after 1.2 bar internal hydraulic pressure. The moulded part is filled with the end-use chemical formulation at 25 °C and 40 °C for 30 days and then submitted to a drop test from 1.5 m per ASTM D5276-19 at -10 °C; cracking in the thread region constitutes a lot rejection. Terminal products are used in knapsack sprayer closures, induction-sealed container caps, and metering chambers for dilute glyphosate or paraquat formulations where continuous service temperature does not exceed 50 °C.
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