| HS Code | 414093 |
| Polymer Type | High Density Polyethylene (HDPE) |
| Density | 0.952 g/cm³ |
| Melt Flow Rate | 0.9 g/10 min (190°C/2.16 kg) |
| Melting Point | 130-135°C |
| Vicat Softening Point | 120-125°C |
| Tensile Yield Strength | ≥23 MPa |
| Elongation At Break | ≥500% |
| Flexural Modulus | ≥1000 MPa |
| Notched Izod Impact Strength | ≥50 kJ/m² |
| Hardness | 60-65 Shore D |
| Brittleness Temperature | ≤ -70°C |
| Environmental Stress Cracking Resistance | ≥1000 h |
| Water Absorption | <0.01% |
| Ash Content | ≤0.03% |
| Moisture Content | ≤0.1% |
| Crystallinity | 70-80% |
| Thermal Conductivity | 0.4-0.5 W/m·K |
| Dielectric Constant | 2.3-2.5 |
| Chemical Resistance | Good against acids, bases, and salts |
| Form | Pellets |
| Color | Natural |
| Molecular Weight Distribution | Broad |
| Bulk Density | 0.55-0.60 g/cm³ |
| Particle Size | 2-4 mm |
As an accredited Guangdong Zhongke HDPE HD52090 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Packaged in 25 kg PP woven bags, Guangdong Zhongke HDPE HD52090 is supplied palletized for industrial delivery. |
| Container Loading (20′ FCL) | 20′ FCL container loading: Guangdong Zhongke HDPE HD52090, 25 MT in 25 kg bags, palletized, shrink-wrapped, securely stowed for export. |
| Shipping | Guangdong Zhongke HDPE HD52090 is typically shipped as white pellets in 25 kg PP woven bags or 1000 kg jumbo bags, palletized and stretch-wrapped. Use clean, dry, covered containers; protect from moisture, sunlight, heat, and contamination. Store in a cool, dry, ventilated area. Suitable for standard sea and land export logistics. |
| Storage | Store in a cool, dry, well-ventilated warehouse away from direct sunlight, heat, moisture, and ignition sources. Keep original packaging sealed and palletized off the floor. Avoid prolonged UV exposure and contamination by dust, oils, or chemicals. Maintain ambient temperature, ideally below 40°C, with low humidity. Use first-in, first-out stock rotation and avoid excessive stacking. Follow local regulations and supplier SDS. |
| Shelf Life | Shelf life approximately 24 months when stored unopened in a cool, dry, ventilated area away from sunlight and heat. |
When HD52090 is processed on high-cavitation closure tooling, the melt mass-flow rate of 9.0 g/10 min determined under ISO 1133-1:2022 at 190 °C and 2.16 kg load, together with a nominal density of 0.952 g/cm³ determined under ISO 1183-1:2019, places the grade in the high-flow HDPE injection moulding window where screw recovery time, injection speed, and gate freeze-off time dominate the cycle. On a 250-tonne high-speed hydraulic press with a 24:1 L/D injection unit and a 50 mm diameter screw, a 32-cavity hot-runner closure tool with 0.8 mm valve-gate orifices typically reaches stable cavity packing only when the nozzle temperature is held at 220–235 °C, the hot-runner manifold is kept between 225–245 °C, and the barrel zones are profiled from 180–200 °C at the feed throat to 210–225 °C at the metering zone. Injection speed in the range of 80–120 mm/s generates cavity fill pressures of 70–110 MPa, after which holding pressure of 40–70 MPa must be maintained for 0.5–1.2 s to compensate for the shrinkage anisotropy of 1.6–2.2% in the flow direction and 1.8–2.4% in the transverse direction, as quantified on plaque specimens under ISO 294-4:2018. If the transfer position is delayed by more than 3 mm or the cushion falls below 2 mm, cavity pressure decay produces ovality in 30/25 mm tamper-evident closures and elevated release torque in the internal thread area.
The formulation for this closure application is compounded with 100 parts by mass of HD52090 resin, 1.0–2.0 wt% polyethylene-carrier colour masterbatch, 0.05–0.15 wt% erucamide slip concentrate where reduced slip force is required, and 0.08–0.20 wt% hindered phenolic antioxidant. Total additive loading should not exceed 3.0 wt% because higher let-down ratios shift the apparent melt flow rate and alter the hot-runner pressure balance. Regulatory compliance for beverage and food-contact closures is governed by FDA 21 CFR 177.1520 for olefin polymers, EU 10/2011 with an overall migration limit of 10 mg/dm², GB 4806.6-2016 for food-contact polyolefin resin, REACH (EC) 1907/2006, and RoHS 2011/65/EU. Terminal finished product types include 30/25 mm carbonated soft drink closures, 38 mm dairy closures, sports caps with tamper bands, and flip-top dispensing closures. Operational boundaries are defined by a bulk moisture content below 0.05%, melt temperature not exceeding 250 °C to avoid oxidative chain scission, and residence time at processing temperature limited to 5 min or less. Drying is not normally required for sealed pellet storage, but surface moisture after outdoor storage at relative humidity above 60% should be removed with desiccant drying at 80 °C for 2 h. The material should not be processed on equipment contaminated with polyoxymethylene or PVC because decomposition products can generate acid species that accelerate HDPE molecular weight reduction.
In thin-wall container production, the filling phase must overcome the fast crystallisation rate of HD52090 while preserving enough melt homogeneity to prevent jetting and flow-mark defects at nominal wall thicknesses of 0.6–1.0 mm. High-speed injection presses with 22:1 L/D injection units and stack-mould configurations are typically operated with barrel temperatures of 200–245 °C, mould temperatures of 10–20 °C, and injection speeds of 200–300 mm/s. Cavity filling under 60–100 MPa hydraulic pressure is followed by short holding pressure of 30–50 MPa for 0.3–0.8 s, producing cycle times of 5–9 s across 2+2-cavity stack tooling. The principal mechanical requirement for this application is top-load and sidewall stacking strength, which is verified on finished containers under ISO 12048:2000 compression and stacking tests; the injection moulded wall must retain dimensional stability after filling at 4 °C and after transport simulation at 35 °C. Mould shrinkage measured under ISO 294-4:2018 is normally between 1.5% and 2.0%, and post-mould warpage is controlled by uniform mould-temperature turbulence of ±2 °C or less.
The formulation for food-contact thin-wall packaging comprises 100 parts by mass HD52090, 1.0–2.0 wt% titanium dioxide white masterbatch for opacity, 0.05–0.15 wt% primary antioxidant, and 0.03–0.08 wt% acid neutraliser. Slip agents are excluded from the base formulation because migration into fatty food simulants can raise the specific migration burden under EU 10/2011 Article 11; where mould release is required, the concentration is held below 0.05 wt% and verified by extraction testing. Compliance standards include FDA 21 CFR 177.1520, EU 10/2011 overall migration limits, GB 4806.6-2016, and GB 9685-2016 for additives. Finished terminal product types include 500 mL, 750 mL, and 1 L dairy tubs, margarine tubs, food-service lids, and frozen dessert containers. If post-industrial regrind is used above 10%, migration behaviour and melt flow stability must be revalidated under the relevant food-contact conformity framework; post-consumer recycled content is not automatically covered by the same authorisation and requires separate regulatory approval. Melt temperature above 245 °C or screw speed above 150 rpm can generate localised shear heating sufficient to produce visible yellowing in unpigmented thin-wall sections.
| Application Segment | Regulation or Standard | Verification Point or Limit |
|---|---|---|
| Beverage closures | FDA 21 CFR 177.1520 | Olefin polymer specification and extractive limits for food-contact articles |
| Beverage closures | EU 10/2011 Annex I | Overall migration ≤ 10 mg/dm² in food simulants |
| Thin-wall food packaging | GB 4806.6-2016 | Polyolefin resin total migration and consumption limits |
| Thin-wall food packaging | GB 9685-2016 | Additive positive list and specific migration limits |
| Crates and pallets | ISO 8611-1:2011 | Rated load, fork-lift handling, and deflection criteria |
| Crates and pallets | RoHS 2011/65/EU | Pb, Hg, Cd, Cr(VI), PBB, and PBDE concentration limits |
| Industrial pail lids | UN Model Regulations Chapter 6.1 | Packing group drop-test and leakproofness qualification |
| Outdoor horticultural parts | REACH (EC) 1907/2006 Annex XVII | Restricted substance screening and SVHC communication duties |
Crate and pallet tooling imposes long flow lengths and multi-gate knit lines, making the molecular weight distribution of HD52090 the controlling factor for impact-critical ribs, corner blocks, and fork-entry openings. Injection moulding of 1200×1000 mm hygienic pallets is typically performed on clamp units rated at 8000–16000 kN, with melt temperatures between 220–250 °C, mould temperatures of 15–40 °C, and holding pressures of 50–80 MPa for 15–30 s. Sequential valve gating is used to displace weld lines away from load-bearing bosses, and gas counter pressure in the range of 0.2–0.5 MPa can be applied to reduce sink marks at the intersection of ribs and deck surfaces. The total cycle time for a 16 kg pallet on a 10000 kN press typically falls between 45–90 s, depending on wall section and mould-temperature stability. Impact-critical zones are evaluated under ISO 179-1:2010 Charpy notched impact and ASTM D256-23 Izod impact; flexural modulus is determined under ISO 178:2019 and tensile properties under ISO 527-2:2012.
The formulation for crates and pallets is based on 100 parts by mass HD52090, with 2.0–3.0 wt% carbon black or UV-stabilised colour masterbatch for outdoor service, 0.15–0.30 wt% primary antioxidant, 0.10–0.20 wt% secondary phosphite antioxidant, and 0.05–0.10 wt% nucleating agent to reduce post-mould warpage. For pallets intended for pharmaceutical or food logistics, the colour and additive package must comply with FDA 21 CFR 177.1520 where direct or incidental food contact is possible, and with EU 10/2011 for migration. Terminal finished product types include hygienic 1200×1000 mm pallets, stack/nest crates, bulk bins, and distribution totes. A recurrent production failure mode on this grade is weld-line impact rupture at the junction of multiple flow fronts when injection speed is reduced below 60 mm/s; in such conditions, the frozen skin ahead of the flow front prevents molecular interdiffusion and yields Charpy values below the design threshold. Flash generation at the parting line increases when melt temperature exceeds 250 °C or when clamp force drops below 0.8 kN/cm² of projected area. Regrind levels should be maintained below 20% for outdoor UV-critical applications because repeated thermal history lowers molecular weight and reduces stress-crack resistance.
When HD52090 replaces fractional-melt HDPE in industrial pail lids, the higher melt flow shortens injection time but increases the risk of flash formation at the tamper-evident tear band and at the outer retention bead. Processing is typically performed on 4- to 8-cavity cold-runner or hot-runner tools with melt temperatures of 200–240 °C, mould temperatures of 12–25 °C, injection pressures of 60–90 MPa, and holding pressures of 35–50 MPa for 4–8 s. Cooling time is set between 12–25 s to stabilise the lid-sealing geometry before ejection; ejection temperature above 60 °C can produce local deformation at the tear bridge and subsequent leakage in drop tests. Finished lids are qualified for stacking strength and leakproofness under UN Model Regulations Chapter 6.1 for dangerous goods packaging and under applicable international modal provisions such as ADR Chapter 6.1 and IMDG Code Chapter 6.1. Dimensional consistency is verified with attribute gauges across the 5 L, 10 L, and 20 L pail lid ranges, and torque tests are conducted on the closure-to-pail interface at 3–8 N·m to confirm consistent removal characteristics.
The formulation for pail lids is composed of 100 parts by mass HD52090, 1.5–2.0 wt% colour masterbatch, 0.10–0.25 wt% antioxidant, and 0.05–0.10 wt% mould release or lubricant additive. For food-grade pails, the formulation must comply with FDA 21 CFR 177.1520 and EU 10/2011; for dangerous goods packaging, the final lid must pass packing group drop heights and leakproofness conditioning under the relevant international regulations. Terminal finished product types include tamper-evident lids for 5 L to 25 L plastic pails, UN-certified closure systems for hazardous liquid or solid transport, and lid-locking rings for industrial chemical packaging. The most restrictive processing boundary occurs during low-temperature impact testing at -18 °C: if the mould temperature is below 10 °C or if regrind content exceeds 30%, the tear band can become brittle and fail before hinge elongation, producing a sharp separation rather than a controlled tearing response. Contact with high-concentration surfactant or oxidising chemical solutions at sustained temperatures above 40 °C should be validated separately because environmental stress cracking can initiate at the gate vestige under hoop stress.
Household storage systems and small appliance components moulded from HD52090 are produced on 120- to 400-tonne toggle-clamp presses, where the grade’s high flow reduces injection pressure in deep-draw drawer moulds but also narrows the processing window for gas-assisted hollow parts. In this application the material is typically compounded with 100 parts by mass HD52090, 1.0–2.5 wt% colour masterbatch, 0.05–0.15 wt% antioxidant, and 0.05–0.10 wt% slip agent for sliding drawer components. Melt temperature is maintained at 190–235 °C, mould temperature at 10–25 °C, and cycle time between 25–45 s depending on wall thickness. Compliance for this segment is governed by REACH (EC) 1907/2006, RoHS 2011/65/EU, and where the article is intended for repeated food contact, FDA 21 CFR 177.1520 or EU 10/2011; toy-like articles may additionally require EN 71-3 migration testing. Terminal finished product types include storage totes, drawer frames, appliance housings, waste bins, and modular shelving components. Continuous service temperature should not exceed 80 °C, and exposure to strong oxidising acids or aromatic hydrocarbons above 0.5 MPa stress should be avoided because the resulting environmental stress cracking can occur at moulded-in knit lines without visible yield deformation.
Because UV exposure dominates outdoor service life, nursery containers and drip-irrigation couplers represent the most UV-demanding injection-moulded segment for HD52090, where carbon black dispersion quality rather than melt index governs multi-season crack resistance. The formulation uses 100 parts by mass HD52090, 2.0–3.0 wt% carbon black masterbatch at 40% carbon black loading, 0.10–0.20 wt% hindered amine light stabiliser, and 0.08–0.15 wt% antioxidant. Injection moulding is carried out at melt temperatures of 200–235 °C, mould temperatures of 10–25 °C, and part weights from 50 g to 1.5 kg, producing cycle times of 18–45 s. Compliance is verified under ISO 179-1:2010 impact testing, ISO 178:2019 flexural testing, REACH (EC) 1907/2006, and RoHS 2011/65/EU; outdoor weathering claims should be supported by accelerated exposure under ISO 4892-2 rather than inferred from carbon black content alone. Terminal finished product types include nursery containers, hanging baskets, irrigation fittings, propagation trays, and landscape edging. Published data for this specific HD52090 configuration under multi-season agricultural UV and fertiliser contact is limited; therefore initial qualification should include tensile strength retention after 2000 h xenon-arc exposure and visual crack inspection after cyclic wet-dry exposure at 50 °C. Carbon black masterbatches containing heavy metal pigments must be rejected if the final article is required to meet packaging heavy metal limits under Directive 94/62/EC.
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Guangdong Zhongke HDPE HD52090 is an injection-moulding high-density polyethylene supplied by Guangdong Zhongke Refining & Petrochemical Co., Ltd. The grade occupies the high-flow HDPE segment for thin-wall rigid packaging and small containers. Its nominal melt mass-flow rate is 9.0 g/10 min at 190 °C under 2.16 kg load (ISO 1133-1:2022), and its as-moulded density is 0.952 g/cm³ (ISO 1183-1:2019). These two values define a narrow processing window between mould-filling fluidity and adequate stiffness. In comparison with extrusion blow-moulding HDPE grades with melt flow rates below 0.5 g/10 min and pipe grades below 0.1 g/10 min, HD52090 allows reduced hydraulic pressure and shorter cycle time in multi-cavity tools. The lower chain entanglement that enables this flowability also reduces slow crack growth resistance and notched impact; this trade-off is the central limitation of the grade.
| Property | Typical value | Test standard |
|---|---|---|
| Melt mass-flow rate (190 °C, 2.16 kg) | 9.0 g/10 min | ISO 1133-1:2022 |
| Density | 0.952 g/cm³ | ISO 1183-1:2019 |
| Tensile yield stress | 24 MPa | ISO 527-2:2012 |
| Flexural modulus | 900 MPa | ISO 178:2019 |
| Notched Izod impact at 23 °C | 4.0 kJ/m² | ISO 180:2019 |
| Heat deflection temperature at 0.45 MPa | 68 °C | ISO 75-2:2013 |
| Shore hardness | 62 Shore D | ISO 868:2003 |
The certificate of analysis for a specific lot should be checked against the producer’s specification because pellet additive level, colour masterbatch, and regrind fraction will shift tensile and impact values by approximately ±10%. For food-contact applications, the resin and finished article must meet FDA 21 CFR 177.1520 and Regulation (EU) No 10/2011; compliance is article-specific and requires migration testing of the finished part.
The primary difference is melt viscosity and its molecular origin. Blow-moulding HDPE grades are controlled at 0.20–0.35 g/10 min to provide parison melt strength, while PE100 pipe grades are often below 0.10 g/10 min for long-term hydrostatic strength. HD52090 at 9.0 g/10 min has lower zero-shear viscosity and shorter fill time, but the polymer chains are shorter and the tie-molecule concentration between lamellae is lower. This structural difference reduces environmental stress crack resistance and notched impact strength. Consequently, HD52090 is not specified for chemical drums, fuel tanks, or pressure pipes where slow crack growth governs service life. In injection-moulded closures and thin-wall containers, the lower viscosity permits cavity fill at reduced hydraulic pressure and allows wall sections of 0.4–1.2 mm without the flow-mark tendency associated with low-MFR HDPE.
| Material class | MFR (190 °C, 2.16 kg) | Density | Primary process | Process-limiting parameter |
|---|---|---|---|---|
| HD52090 injection grade | 9.0 g/10 min | 0.952 g/cm³ | Injection moulding | Gate freeze time |
| HDPE blow-moulding grade | 0.25 g/10 min | 0.955 g/cm³ | Extrusion blow moulding | Parison melt strength |
| PE100 pipe grade | 0.07 g/10 min | 0.958 g/cm³ | Pipe extrusion | Long-term hydrostatic strength |
The comparison shows that HD52090 is not a drop-in replacement for high-molecular-weight HDPE grades. Replacing a blow-moulding grade with HD52090 in a pail handle or a corrugated fitting reduces melt strength and stress-crack resistance. Conversely, unreinforced articles with wall sections below 1.2 mm benefit from shorter filling time and lower injection pressure. The density of 0.952 g/cm³ reflects a crystalline fraction in the region of 65–70%; higher crystallinity contributes stiffness but reduces sub-zero toughness.
Moisture uptake in HDPE is generally low, but unprotected storage at relative humidity above 60% can produce surface condensation. When free moisture exceeds 0.05 wt%, pre-drying at 80 °C for 2–3 h in a desiccant dryer is recommended to avoid splay on sidewalls. Barrel temperature settings should follow a rising profile from feed to nozzle: 180 °C, 190 °C, 200 °C, 210 °C, 220 °C. For a 40 mm screw with 22:1 L/D, screw speed of 80–150 min⁻¹ and back pressure of 0.5–1.5 MPa are typical. Nozzle melt temperature should be held at 200–240 °C. Residence time above 260 °C must be avoided because oxidative chain scission releases low-molecular-weight olefinic fragments and accelerates yellowing; hot-runner dead spots can exceed this limit even when the nozzle reading is lower.
Mould temperature is 20–40 °C. Higher mould temperatures improve surface gloss and weld-line strength but extend cooling time. With a 0.8 mm wall, cooling time is approximately 5–7 s at 30 °C mould temperature. Ejection surface temperature should remain below 80 °C to prevent ejector pin penetration. Mould shrinkage in thin-wall HD52090 is typically 1.8–2.2% in the flow direction and 1.5–2.0% transverse to flow; tooling dimensions must compensate for this anisotropy.
Capillary viscosity data for HD52090 across the full shear-rate window are not fully disclosed in public trade literature. For HDPE with MFR in the 8–10 g/10 min band, apparent viscosity at 190 °C and 100 s⁻¹ is generally 150–250 Pa·s. This value supports rapid flow through thin-wall sections, but shear-thinning becomes less effective at very high injection speeds. Above approximately 1,000 s⁻¹, the onset of sharkskin and jetting is possible at melt temperatures below 200 °C. Gate blush and flow hesitation are therefore controlled by adjusting injection velocity and gate diameter rather than by increasing melt temperature alone.
Gate freeze time is the limiting variable for pack effectiveness. With land length 0.8–1.0 mm and gate diameter 1.0–1.2 mm, the gate freezes within 0.3–0.8 s at mould temperatures of 20–40 °C. The velocity-to-pressure switch-over must occur before the gate reaches no-flow temperature. On a 1,200 kN hydraulic injection-moulding machine with a 40 mm screw, switch-over at 95–98% of shot weight is used for a 0.8 mm sidewall pail. Pack pressure of 40–60 MPa for 0.5–1.5 s is sufficient; after gate freeze, continued packing only consumes energy and does not reduce sink. In a multi-cavity tool, cavity-pressure sensors placed at the last cavity to fill are recommended. A cavity-pressure rise of 30–50 MPa at end of fill indicates that packing has been transmitted before gate freeze.
Masterbatch selection changes the solidification behaviour of HD52090. Organic pigments can nucleate crystallisation and shorten cycle time, while carbon black masterbatch at 2–3 wt% can reduce apparent MFR from 9.0 to 7.5–8.5 g/10 min and increase screw recovery time by 5–10% on a 40 mm screw. Regrind addition at 20–30 wt% changes bulk density and particle-size distribution; if the cushion position falls below 2–3 mm, shot-to-shot density variation appears as sink marks on flat bases. The cushion should be monitored with each shot and recorded in process logs. Drying of regrind may be required at 80 °C for 2 h when stored in unheated warehouses or exposed to condensation.
Thin-wall food container production with HD52090 is governed by the balance between cooling time and part ejection stiffness. For a 0.7 mm wall, a cooling time of 4–7 s at mould temperatures of 25–35 °C is required to bring the part surface below 80 °C. If the part is ejected above the Vicat softening point of 70–72 °C, ejector pin indentation and stack-rack distortion occur. Warpage arises from differential shrinkage across the cavity-core interface. A temperature asymmetry below 5 K between the two mould halves is more effective than increasing cooling time. For round containers, a central pin gate preserves axisymmetric flow and reduces radial shrinkage gradients; edge gates on rectangular parts promote corner bridging and sidewall curl.
On a 2+2 stack mould with 8 valve-gated hot-runner drops, fill imbalance is managed by setting valve opening delays individually. With HD52090, cavity-to-cavity mass variation should be held within ±0.05 g for a 12 g container; this prevents audible cracking during stack movement and ensures uniform brim flatness. A valve-gate pin retracting 3–5 mm with a clean shut-off is required because the low-viscosity melt can drool from open gates. For pail lids and caps that must withstand top-load of 200–300 N, finished-part buckling and creep tests should be performed because ISO tensile data alone do not predict assembly performance. Top-load testing can be conducted according to ASTM D2659-16 at a platen speed of 5 mm/min.
Published data for HD52090 in environmental stress crack resistance testing under ASTM D1693 or ISO 22088-3 are limited; the grade should not be selected for continuous exposure to polar solvents, strong detergents, or load-bearing service above 60 °C. Outdoor exposure requires a UV-stabilized formulation and verification under ISO 4892-2; the natural grade is not intended for long-term exterior use.