| HS Code | 893958 |
As an accredited PetroChina Daqing HDPE QL585P factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | PetroChina Daqing HDPE QL585P is packaged in 25 kg woven bags, palletized, and 1000 kg jumbo bags for transport. |
| Container Loading (20′ FCL) | PetroChina Daqing HDPE QL585P in 25 kg bags; 20′ FCL loads about 25 MT loose, shrink-wrapped and securely stowed. |
| Shipping | PetroChina Daqing HDPE QL585P is shipped as a non-hazardous high-density polyethylene in 25 kg PP woven bags, palletized and stretch-wrapped. Transport in clean, dry containers or trucks, protecting from moisture, sunlight, heat, and contamination. Store in a cool, ventilated warehouse. No special hazard classification required. |
| Storage | Store PetroChina Daqing HDPE QL585P in a cool, dry, well-ventilated warehouse. Keep in original sealed bags on pallets, off the floor, away from direct sunlight, rain, moisture, heat, ignition sources, and strong oxidizers. Avoid contamination, sharp objects, and excessive stacking. Use first-in, first-out rotation. Maintain ambient temperature and low humidity for optimal resin stability. |
| Shelf Life | Under proper storage, shelf life is 24 months from production date; keep cool, dry, ventilated, and away from sunlight. |
Thin-wall food container conversion exposes PetroChina Daqing HDPE QL585P to a process conflict between melt flow length and organoleptic stability. When cavity wall thickness drops below 0.50 mm and flow path exceeds 100 mm, the melt front temperature decays rapidly in a cold runner mold; injection velocity below 180 mm/s generates flow lines and short shots, while velocity above 320 mm/s can increase shear heating at the gate to the point where low-molecular-weight oxidation products exceed the sensing threshold for packaged dairy products. Compliance in this sector is anchored to EU Regulation 10/2011 Annex I with an overall migration limit of 10 mg/dm², FDA 21 CFR 177.1520 for polyolefins under aqueous, acidic and fatty food simulants, GB 4806.7-2016 for domestic China distribution, and REACH Regulation (EC) No 1907/2006 Annex XVII for restricted pigments. Formulation addition ratios for dairy tub conversion are typically 100 wt% QL585P plus 2.0–4.0 wt% white titanium dioxide/polyethylene carrier masterbatch, 0.05–0.10 wt% of a non-ester slip/antiblock package, and 0.03–0.08 wt% of a food-contact-grade acid scavenger; the masterbatch carrier must be matched to the melt index of QL585P to prevent segregation in the screw root. Production equipment is normally a 250–400 t toggle-clamp machine with an accumulator-assisted hydraulic unit or electric screw drive running melt temperature 200–225°C, mold temperature 20–35°C, injection pressure 90–120 MPa, hold pressure 55–75 MPa, and back pressure 4–8 MPa. Valve-gated hot runners with 0.8–1.2 mm gate diameters are preferred over open sprue bushing feeds to limit gate freeze-off variability. Core and cavity steel is S136 ESR or 1.2738 HH with vent depths 0.015–0.02 mm at end of flow; vents deeper than 0.03 mm produce flash in thin-wall sections. Terminal products include 200–500 mL dairy tubs, 500–1000 mL delicatessen containers, and 750–1200 mL rectangular takeaway trays with wall thickness 0.38–0.65 mm.
The frozen layer kinetics of thin-wall QL585P define the pack-pressure window. At wall thickness 0.45 mm, gate freeze occurs within 0.6–1.0 s after screw transfer; hold pressure applied later than this cannot compensate for volumetric shrinkage in the base. Mold temperature fluctuation above ±3°C across the cavity shifts part weight by 0.30–0.50%, which produces visible sink marks at boss features and side-wall ripple. The process alarm band is therefore narrower than general HDPE injection: melt temperature variation should be kept within ±5°C, and injection velocity variation within ±10 mm/s. Hot runner temperature control via dual-zone PID with thermocouple placement 5 mm from the gate land is the preferred configuration; open manifold systems without zone trim can create flow imbalance above 4%, causing flash on one cavity and short shot on the opposite cavity. Screw geometry is also relevant: a 20:1 L/D three-zone screw with a check ring and a compression ratio of 2.5–3.0:1 provides sufficient plasticating without excessive residence time. Because producer-published capillary rheometry data for QL585P at high shear rates is limited, processors should generate curves at 190°C and 230°C across shear rates 100–1000 s⁻¹ before tool hardening; lot-to-lot melt index variation can shift short-shot thresholds by 6–8°C.
Closure development for QL585P is limited to non-carbonated water and dry food closures where the formulation addition ratio is 0.8–2.5 wt% low-migration masterbatch plus 0.03–0.08 wt% food-contact lubricant, the relevant compliance anchors are FDA 21 CFR 177.1520 and EU 10/2011 with organoleptic verification under EN 1622, and the downstream process uses 48–96-cavity injection tools at 200–235°C melt temperature producing 28 mm PCO 1881, 38 mm dairy and 55 mm dry food jar closures, whereas carbonated soft drink caps are excluded without ASTM D1693 ESCR validation because thread root stress cracking is the failure limit.
The shift from virgin pellet to a compounded melt containing 30 wt% of in-house pail regrind alters the melt elasticity and pack stage behavior of QL585P. Regrind particles with a lower bulk density than pellets enter the feed throat unevenly, causing screw torque fluctuation and melt pressure ripple in the metering zone; the resulting weight variation in a 1.1 kg pail can exceed ±0.8% unless the regrind is blended offline before hopper loading. The formulation addition ratio for industrial pails is therefore 70 wt% QL585P virgin, 30 wt% clean post-industrial regrind, plus 1.5–3.0 wt% carbon black or UV masterbatch and 0.05–0.15 wt% of a processing stabilizer, with the exact carbon black loading adjusted to maintain weld line strength after outdoor weathering. Compliance is anchored to UN dangerous goods packaging standards for open-head plastics drums and pails: the 1H2 open-head plastics drum category under ADR/RID/IMDG Code, with design type testing including drop height at 1.2 m after conditioning at −18°C for liquid-filled pails, leakproofness, hydraulic pressure at 100 kPa for 30 min, and stacking at 40°C for 28 days.
The injection stage in pail production is not the primary cycle time driver; the pack and cooling stages dominate because the thick flange and sidewall must be solidified without gate stringing. A two-stage pack profile of 70 MPa for 5 s followed by 50 MPa for 8 s limits sink at the handle boss while preventing overpacking at the gate. Injection melt temperature upper limit is 230°C; above this, the post-industrial regrind fraction can oxidize and the odor profile shifts. Mold temperature is kept at 20–35°C with cooling water at 15–20°C using baffle inserts in the flange ring; a cooling time below 25 s can cause wall buckling during ejection, while above 40 s energy per unit exceeds the line target. Post-mould air cooling on a 12-station rotary table removes residual heat from the base insert; without this station, stack deformation after 48 h can exceed 2.5 mm under a 400 kg top load. Terminal products include 5 L, 10 L, 20 L, and 25 L open-head pails for water-based paints, adhesives, lubricant greases, and dry food powders; closed-head 1H1 formats may require a different weld-line strategy because the handle insert disrupts the flow front around the bung boss. Regrind above 30 wt% is not recommended without melt flow ratio testing per ISO 1133-1:2022 and impact testing per ISO 179-1:2010.
Logistics crate conversion with QL585P is dominated by low-temperature impact retention and shrinkage anisotropy across the long axis of a 600 mm × 400 mm ventilated crate. The material is normally formulated with 1.5–3.5 wt% of a polyethylene-carrier carbon black masterbatch and 0.2–0.8 wt% of a hindered amine light stabilizer masterbatch when the crate is used in outdoor agricultural collection; where indoor closed-loop distribution is the only duty, pigment loading can be reduced to 0.5–1.5 wt% to minimize viscosity shift. For impact-critical cold storage, 4.0–8.0 wt% of an EPDM or metallocene plastomer modifier may be added, but only after verifying that the modifier does not reduce the in-mold flow length of QL585P below 70% of the virgin value at 210°C. Standards for logistics crates are less food-contact driven and more mechanical: tensile yield per ISO 527-2:2012, notched Charpy impact per ISO 179-1:2010 at −20°C, and top-load/deformation under ISO 12048:1994 for complete, filled transport packages; for pallet boxes, ISO 8611-1:2011 applies if the crate base is pallet-footed. RoHS 2011/65/EU applies only when the crate is integrated into an electrical appliance or white-goods transport system; REACH Annex XVII restricts heavy metal colorants. Pre-drying is not required when internal moisture is below 0.02 wt%; if outdoor bulk storage exceeds 60% relative humidity, surface moisture must be removed by a dry-air hopper at 60–70°C for 1–2 h. Processing on a 500–800 t clamp force machine with a 1.5–3.0 kg shot weight uses melt temperature 210–240°C, mold temperature 20–30°C, injection pressure 90–130 MPa, and a two-stage packing profile with 80 MPa for 6 s and 55 MPa for 10 s. Because the long sidewall of a crate is 550–600 mm, gate placement is normally a single submarine or banana gate at the base center or two side gates with a sequential valve to reduce weld line formation; the mold is cooled by a central water manifold with coolant temperature 12–18°C to shorten cycle time to 28–38 s. Terminal products include ventilated fruit and vegetable crates, nestable general-purpose logistics boxes, 1200 × 1000 mm pallet bases with interlocking legs, and collapsible warehouse boxes with hinge inserts. Outdoor-grade crates for unrefrigerated transport require an additional UV weathering test per ISO 4892-2:2013 for a minimum of 1000 h when specified; indoor crates are not subjected to this certification.
HDPE QL585P enters the domestic article market only where the converter controls three simultaneous variables: pigment migration, sink-mark depth at wall section changes, and post-mould part flatness. The formulation addition ratio is typically 1.0–3.0 wt% of a high-opacity white or pastel masterbatch, 0.05–0.15 wt% of a nucleating agent to suppress shrinkage anisotropy, and 0.03–0.10 wt% of a food-grade acid scavenger; for toy-grade applications the masterbatch must be selected from pigments with low heavy-metal migration, not merely low total metal content. Compliance is governed by EN 71-3:2019+A1:2021 for the migration of 19 elements from toy materials, with limits in mg/kg for Category I, II, and III materials; ISO 8124-1:2018 mechanical small-part hazard limits for toys intended for children under 36 months; FDA 21 CFR 177.1520 for food-contact storage items; and GB 4806.7-2016 for domestic food-contact use. Articles intended for prolonged skin contact must also meet REACH Annex XVII entry 43 restrictions on polycyclic aromatic hydrocarbons. Processing on a 200–400 t injection machine with a 40–70 mm screw uses melt temperature 195–220°C, mold temperature 18–30°C, injection speed 80–150 mm/s, and pack pressure 50–70 MPa for 5–10 s. Gate placement is the dominant warpage lever: for a 350 mm × 250 mm drawer organizer, a single edge gate produces a flatness deviation above 2.0 mm, while a four-point or film gate layout around a central flow leader reduces deviation to below 0.8 mm. Cooling time for 2.0–3.0 mm walls is 12–20 s; ejection temperature above 75°C leads to post-mould bowing under the weight of stacked parts. Terminal products include stackable kitchen organisers, cutlery trays, refrigerator bins, toy storage boxes, and non-food household containers. Toys intended for water play are not assigned to QL585P if the mould contains internal stress concentration at weld lines because repeated thermal cycling in 55°C water can accelerate environmental stress crack development.
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