| HS Code | 818497 |
| Density G Cm3 | 0.955 |
| Melt Mass Flow Rate G 10min 190c 2 16kg | 11 |
| Tensile Stress At Yield Mpa | 27 |
| Tensile Strain At Yield Percent | 10 |
| Tensile Strain At Break Percent | 600 |
| Flexural Modulus Mpa | 1300 |
| Charpy Notched Impact Strength Kj M2 23c | 8 |
| Charpy Notched Impact Strength Kj M2 Minus30c | 5 |
| Vicat Softening Temperature C | 125 |
| Heat Deflection Temperature C 0 45mpa | 80 |
| Ball Indentation Hardness Mpa | 50 |
| Molding Shrinkage Percent | 1.5-3.0 |
| Water Absorption Percent | <0.01 |
| Dielectric Constant 1mhz | 2.3 |
| Volume Resistivity Ohm Cm | >1E16 |
As an accredited High Density Polyethylene HDPE HD55110 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | High Density Polyethylene HDPE HD55110 is packed in 25 kg moisture-resistant bags on pallets, with 40 bags per pallet. |
| Container Loading (20′ FCL) | High Density Polyethylene HDPE HD55110 in 25 kg bags, palletized and securely loaded into a 20-foot FCL for export. |
| Shipping | High Density Polyethylene HDPE HD55110 is shipped as solid pellets in 25 kg bags, jumbo bags, or octabins. It is non-hazardous and not UN-regulated. Transport in dry, clean containers or trucks away from direct sunlight, heat, and moisture; avoid packaging damage. Standard freight applies. |
| Storage | Store High Density Polyethylene HDPE HD55110 in a cool, dry, well-ventilated warehouse away from direct sunlight, heat, flames, ignition sources, and strong oxidizing agents. Keep original containers or bags closed, clean, and palletized to prevent moisture, contamination, and spillage. Avoid extreme temperatures and excessive dust generation; maintain good housekeeping and follow the SDS/local regulations. |
| Shelf Life | Shelf life is 24 months from date of manufacture when stored in original packaging at ambient temperature under normal conditions. |
For rotary-core injection moulding of tamper-evident closures that must pass continuous downstream high-speed capping on still-water and carbonated soft-drink filling lines, HDPE HD55110 is specified at a nominal density of 0.955 g/cm³ (ISO 1183-1:2019) and a melt flow rate of 10 g/10 min under 2.16 kg at 190 °C (ISO 1133-1:2022). The polymer fraction is composed of 98.5–99.0 wt% HD55110 and 1.0–1.5 wt% low-odour polyolefin colour masterbatch, with additives in parts per hundred resin: 0.12–0.20 phr primary hindered-phenol antioxidant, 0.06–0.12 phr zinc stearate acid scavenger, and 0.05–0.10 phr erucamide slip additive for controlled removal torque. Food-contact approval is established under EU Regulation (EC) No 1935/2004 and Commission Regulation (EU) No 10/2011, Annex I, Table 1, with an ethylene specific migration limit of 1000 mg/kg and an overall migration limit of 10 mg/dm²; the corresponding United States condition is FDA 21 CFR 177.1520(c) 1.1 for olefin polymers. Production-scale closure lines typically employ 64- to 128-cavity rotary compression or high-cavity injection tooling with hot-runner valve gating, maintaining barrel temperatures of 210–235 °C, nozzle temperatures of 215–230 °C, and mould temperatures of 8–15 °C; injection pressure is set at 900–1200 bar with holding pressure at 40–60% of the injection peak, and cycle time is held at 5–8 s. Terminal product types include short-skirt PCO 1881 beverage closures, tamper-evident bands for aseptic dairy closures, sports caps with push-pull valves, and single-piece closure systems in which a moulded HDPE sealing flap replaces a separate elastomer liner. A recurrent failure mode observed on multi-cavity closure equipment is non-uniform removal torque caused by anisotropic shrinkage between the gate and the tamper-evident band slitting line; this is controlled by cavity-level melt-pressure monitoring and by restricting regrind addition to ≤20 wt% of total feed because higher closed-loop fractions narrow the processing window and elevate organoleptic risk in mineral-water closures. Pre-drying is not required when internal moisture is below 0.03 wt%, but material exposed to ambient relative humidity above 85% is dried at 80 °C for 1 h before processing.
Because thin-wall dairy tubs and delicatessen containers are demoulded at wall thicknesses between 0.45 mm and 1.20 mm, the polymer fraction for HD55110 is normally 99.0–99.7 wt% resin with 0.30–0.80 wt% TiO₂ masterbatch, while additive dosing is maintained at 0.05–0.10 phr antioxidant and 0.03–0.06 phr acid scavenger; calcium carbonate or talc should not exceed 3.0 wt% because increasing filler loading above this threshold reduces puncture resistance at the sealing edge after drop transport. Processing is carried out on all-electric injection machines from 150–400 t clamp force with screw L/D ratios of 20:1–24:1, barrel temperatures of 200–235 °C, and tool temperatures of 10–20 °C; injection velocities are set between 200 mm/s and 400 mm/s, melt-pressure limits at 500–900 bar, and cycles from 4.5–7.0 s. Compliance for thin-wall food-contact articles follows EU Regulation (EU) No 10/2011 with hot-fill test conditions appropriate to the end-use temperature, FDA 21 CFR 177.1520(c) 1.1 for single-use dairy applications, and good manufacturing practice under EC No 2023/2006; mechanical control is anchored to notched Izod impact according to ASTM D256-10(2018) and tensile yield according to ISO 527-2:2012. Terminal product types are 0.5–2.0 L dairy tubs, square delicatessen containers, smooth-wall lids, frozen dessert packs, and portion cups for creamers and sauces. The limiting production defect is short-shot formation at the end of fill when melt viscosity shifts upward after repeated regrind cycles; inline melt-flow verification against ISO 1133-1:2022 is therefore used to hold the recycled fraction within specification.
Injection-moulded open-top pails for food, construction chemicals, and UN-certified dangerous-goods transport are produced from HD55110 with a polymer fraction of 97.0–98.5 wt% virgin resin and 1.5–3.0 wt% 40% carbon-black masterbatch or inorganic pigment masterbatch; additives are 0.10–0.20 phr zinc stearate and 0.20–0.30 phr high-molecular-weight HALS UV stabiliser for outdoor-grade containers, while in-house regrind from sprues and reject pails is limited to ≤25 wt% of total feed. The moulding cell comprises hydromechanical injection presses of 600–1600 t clamp force with single-face or stack tooling, barrel temperatures of 215–240 °C, hot-runner temperatures of 225–245 °C, and coolant-controlled mould temperatures of 8–18 °C; screw speed is 60–100 rpm, back pressure 5–10 bar, injection pressure 700–1100 bar, and post-cooling time for a 20 L pail is 18–40 s. Drop integrity is validated under ASTM D5276-19 at −18 °C, while dangerous-goods pails follow UN ADR/RID/IMDG Chapter 6.1 with stacking and vibration loading according to ASTM D4169-22; food-grade pails additionally fall under EU Regulation (EU) No 10/2011 and FDA 21 CFR 177.1520(c) 1.1. The limiting failure mode is not generalised ductile tearing but localised brittle fracture at the gate boss or along the handle-hole weld line when mould temperature is too low or when the pail is filled with surfactant-containing liquids above 60 °C; this is attributed to residual stress concentration and environmental stress cracking in the semicrystalline matrix. Terminal product types are 1–25 L open-top pails, tamper-evident lidding pails, pour-spout containers for detergents, and UN-certified 20 L round pails. Published data for the specific UN certification performance of HD55110 at −18 °C is limited; qualification drop tests on each new tool are therefore prerequisite before commercial release.
| Application scenario | Regrind boundary | Primary compliance standard | Mechanical verification standard |
|---|---|---|---|
| Closures and caps | ≤20 wt% | EU 10/2011, FDA 21 CFR 177.1520(c) 1.1 | ISO 527-2:2012, ASTM D638-14 |
| Thin-wall dairy and deli packaging | ≤15 wt% | EU 10/2011, EC No 2023/2006, FDA 21 CFR 177.1520(c) 1.1 | ASTM D256-10(2018), ISO 527-2:2012 |
| Open-top pails and lids | ≤25 wt% | UN ADR/RID/IMDG Chapter 6.1, EU 10/2011, FDA 21 CFR 177.1520(c) 1.1 | ASTM D5276-19, ASTM D4169-22 |
| Returnable crates and trays | ≤35 wt% | ISO 18601:2013 | ASTM D642-15, ASTM D256-10(2018) |
| Structural-foam pallets | ≤15 wt% | ISO 8611-1:2021, ISO 8611-2:2021 | ASTM D1185, ISO 8611-1:2021 |
| Housewares and utility components | ≤10 wt% | EN 71-3:2019+A1:2021, FDA 21 CFR 177.1520(c) 1.1 | ISO 179-1:2010 |
Closed-loop returnable crate programmes for beverage distribution and bakery logistics impose the highest thermo-mechanical load on HD55110 because recovered material is re-extruded through 15–20 processing cycles across asset life. The polymer fraction is composed of 70–75 wt% virgin HD55110 and 25–30 wt% washed and sorted post-industrial regrind, with additives expressed in parts per hundred resin: 0.10–0.25 phr high-molecular-weight HALS UV stabiliser, 0.08–0.15 phr phosphite-antioxidant blend, and 2.0–4.0 phr colour masterbatch; the closed-loop regrind fraction is capped at 35 wt% because higher levels reduce notched Charpy impact energy and accelerate environmental stress cracking at the base ribs. Moulding is performed on large 1200–2200 t hydraulic injection platforms with 2+2 or 4-cavity tooling, valve-gated hot runners of 8–16 drops, barrel temperatures of 220–250 °C, mould temperatures of 15–30 °C, injection velocity sequenced from 60 mm/s at the gate to 180 mm/s across the floor grid, and cycle times of 35–65 s depending on crate footprint. Compliance for reusable packaging is anchored to ISO 18601:2013 for packaging reuse systems, ASTM D642-15 for top-load compression resistance, and ASTM D256-10(2018) for notched impact, with load-cell verification of stack stability under ASTM D4169-22. Terminal product types are 24×0.33 L beverage crates, bread trays with stacking lugs, bulk logistics totes, and agricultural harvest crates carrying 15–25 kg of field produce. The main production failure mode is stress whitening and eventual cracking at the intersection of the base grid and sidewall ribs when regrind-induced molecular-weight reduction is not offset by reducing barrel temperature or raising mould temperature; inline MFR checks should be maintained at 10–14 g/10 min after compounding to avoid violating the lower Charpy limit specified for the crate programme.
Low-pressure structural-foam moulding of rackable polymer pallets uses HD55110 as the primary rigid phase, with a polymer fraction of 98.0–99.0 wt% HD55110 and 1.0–2.0 wt% carbon-black masterbatch; foaming is accomplished either with 0.10–0.30 phr endothermic chemical foaming agent based on citric acid and sodium bicarbonate or by direct nitrogen gas injection at 0.3–0.8 MPa counterpressure, while antioxidant package is dosed at 0.15–0.30 phr. Processing is executed on 2000–4000 t accumulator-assisted injection-moulding machines with open-nozzle melt conveyance and hot-runner gating, barrel temperatures of 205–225 °C, mould temperatures of 15–35 °C, gas injection pressures of 0.3–0.8 MPa for cavity packing, and total cycles of 120–240 s for a 1200 × 1000 mm pallet footprint. Performance is verified against ISO 8611-1:2021 for static and dynamic stacking loads, ISO 8611-2:2021 for racking deflection limits, and ASTM D1185 for rail and truck unit-load retention; food-contact pallets used in meat and dairy cold rooms are certified under EU Regulation (EU) No 10/2011 and FDA 21 CFR 177.1520(c) 1.1. Terminal product types are hygienic export pallets, rackable 1200 × 1000 mm pallets with 800–1000 kg racking capacity at 23 °C, nestable display quarter-pallets, and freezer-compatible pallets rated to −30 °C. The key operational boundary is creep deflection under sustained load at temperatures above 45 °C, where published data for this specific HD55110 configuration is limited; static load validation should therefore be repeated for each new pallet design and colour formulation before fleet deployment.
Domestic storage articles, waste bins, and small utility components form a lower-cycle-intensity segment for HD55110; polymer fractions of 98–100 wt% HD55110 with 0–2 wt% colour masterbatch are processed on 80–500 t hydraulic injection machines at barrel temperatures of 200–225 °C and mould temperatures of 20–40 °C without pre-drying when internal moisture is below 0.03 wt%. Regulatory exposure for toy-migration testing under EN 71-3:2019+A1:2021 and food-contact utility articles under FDA 21 CFR 177.1520(c) 1.1 defines the primary compliance boundary; terminal products include stackable storage boxes, round waste baskets, detergent scoops, dustpan components, and injection-moulded hangers.
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High Density Polyethylene HD55110 is supplied as a pelletized, high-molecular-weight extrusion resin. The designation places it among HDPE grades that rely on a broad or bimodal molecular weight distribution to sustain melt strength during blown film expansion. Melt flow rate is typically reported at 0.10 g/10 min under 190 °C and 2.16 kg load in accordance with ISO 1133-1. Density is commonly cited at 0.955 g/cm³ using ISO 1183-1. Published certificate of analysis data for HD55110 remain lot-dependent, and the values supplied here are representative for the HD55110 class rather than a substitute for a supplier lot certificate.
The high melt strength of HD55110 is functionally linked to the presence of a high molecular weight fraction that increases zero-shear viscosity and delays bubble rupture. On production-scale blown film lines, this translates into a wider operating window for blow-up ratio and frost line height compared with low-molecular-weight film HDPE. Shear thinning is more pronounced than in conventional unimodal film grades, so apparent viscosity drops significantly under die lip shear while retaining sufficient extensional viscosity in the bubble. Processors often report that the grade can sustain blow-up ratios between 2.5:1 and 4.0:1 without resonance, provided that die gap and melt temperature are held within supplier-recommended boundaries.
Molecular architecture also influences environmental stress crack resistance. The long-chain fraction and short-chain branch distribution improve resistance to slow crack growth under external stress. Comparative testing under ASTM D1693 condition B typically places this class of HDPE above 1,000 h without failure, which is materially higher than general-purpose unimodal film HDPE. That resistance is relevant in applications where the film contacts surfactants, oils, or repeated flexing under load.
The table consolidates representative property values for the HD55110 class. Test method designations follow the supplier-preferred standards where available. Lot-to-lot variation in commercial production may occur within the precision limits of the referenced method.
| Property | Test method | Representative value |
|---|---|---|
| Melt flow rate | ISO 1133-1 | 0.10 g/10 min |
| Density | ISO 1183-1 | 0.955 g/cm³ |
| Tensile stress at yield | ISO 527-2 | 26 MPa |
| Tensile elongation at break | ISO 527-2 | >600 % |
| Flexural modulus | ISO 178 | 950 MPa |
| Environmental stress crack resistance | ASTM D1693 condition B | >1,000 h |
| Vicat softening temperature | ISO 306/A50 | 124 °C |
| Notched Charpy impact strength | ISO 179-1/1eA | 18 kJ/m² |
| Shore D hardness | ISO 868 | 62 |
Extrusion-scale observations indicate that batch-to-batch melt flow rate variation on supplier certificates is commonly controlled within ±0.02 g/10 min for this product class. Density variation is typically controlled within ±0.001 g/cm³. Such tolerances are not universal across suppliers and must be confirmed against the specific manufacturing source of HD55110. Published data for this specific configuration is limited outside the supplier technical datasheet, so independent verification through a plant trial remains necessary when the grade is introduced into an existing production asset.
On single-screw blown film extruders with an L/D ratio of 30:1 and a barrier screw, HD55110 is usually processed with a flat to slightly reverse temperature profile from hopper to die. Melt temperatures of 180 °C to 210 °C are commonly targeted. Die set temperatures above 230 °C increase the risk of oxidative degradation, visible as die lip deposit, gel formation, and a progressive loss of bubble stability. The degradation pathway is accelerated by oxygen ingress at the hopper and by long residence time in the adapter and die. A production-scale failure mode associated with excessive melt temperature is the appearance of hard, non-fusing gel clusters in the finished film, often accompanied by a measurable reduction in notched impact strength.
Moisture uptake in the pellet is generally low because HDPE is not hygroscopic. However, cold warehouse transfer into a warm processing bay can produce surface condensation. If a moisture analyzer indicates surface moisture above 0.05 % by weight, the resin may be pre-dried at 70 °C for 2 h before extrusion. The processing window is narrowest at very low frost line heights. Below approximately 4 die diameters, bubble instabilities such as helical instability and draw resonance become more probable. Above 9 die diameters, orientation balance between machine direction and transverse direction shifts, and film tear propagation resistance may decline.
Substitution of a unimodal film HDPE with HD55110 requires revalidation of the screw speed, die pressure, and frost line profile. Because the melt flow rate of HD55110 is lower than that of many general-purpose film HDPE grades, the extruder may operate at higher torque for the same die throughput. The comparative matrix below summarizes class-level differences between HD55110, a conventional unimodal HDPE film resin, and a high-flow HDPE injection molding grade.
| Parameter | HD55110 class | Unimodal HDPE film class | HDPE injection molding class |
|---|---|---|---|
| Melt flow rate | 0.10 g/10 min | 0.50 g/10 min | 7.0 g/10 min |
| Density | 0.955 g/cm³ | 0.952 g/cm³ | 0.960 g/cm³ |
| Tensile yield stress | 26 MPa | 24 MPa | 29 MPa |
| Environmental stress crack resistance | >1,000 h | 150 h | 40 h |
| Primary processing route | Blown film and heavy-duty sheet | General blown film | Thin-wall injection molding |
| Melt strength | High | Moderate | Low |
The high-flow injection molding grade is unsuitable as a direct substitute for HD55110 in blown film because its low melt strength produces bubble sag and uneven gauge distribution. Conversely, HD55110 is not a practical injection molding material because the low melt flow rate increases filling resistance in thin-wall tools and may lead to short shots at typical injection pressures below 100 MPa. The differences are therefore not merely compositional but define the processing route, tooling design, and end-use performance envelope.
Compliance evaluation for HD55110 depends on the additive package and supplier formulation. Food-contact suitability is assessed under FDA 21 CFR 177.1520 for olefin polymers and under EU Regulation 10/2011 for plastic materials intended to contact food. A supplier declaration of compliance is required for the specific lot and must include any restrictions on food type, temperature, or contact duration. For industrial applications, compliance with the RoHS Directive 2011/65/EU and the REACH SVHC candidate list must be verified against the current formulation because antioxidant and processing aid additives can differ across production campaigns.
HD55110 should not be processed simultaneously with high levels of peroxide masterbatch at melt temperatures above 220 °C. Peroxide-induced chain scission or crosslinking can shift the molecular weight distribution and destabilize the extrusion process. When a color concentrate or slip additive is introduced, a letdown ratio should be confirmed by a short film trial because excessive low-viscosity concentrate at the feed throat can create screw slippage and melt temperature override. The grade is also not recommended for use in thin-wall injection molding tools with flow-length-to-thickness ratios above 150:1, where the low melt flow rate produces excessive cavity pressure and long cycle times.