| HS Code | 120834 |
| Polymer Type | High Density Polyethylene |
| Density | 0.954 g/cm³ |
| Melt Flow Rate | 0.35 g/10 min (190°C/2.16 kg) |
| Tensile Strength At Yield | 25 MPa |
| Tensile Strength At Break | 30 MPa |
| Elongation At Break | >600% |
| Flexural Modulus | 1100 MPa |
| Vicat Softening Point | 125°C |
| Melting Point | 130°C |
| Environmental Stress Crack Resistance | >1000 h (F50, 10% Igepal) |
| Hardness | 60 Shore D |
| Notched Izod Impact Strength | 300 J/m |
As an accredited Lotte Chemical Titan HDPE HM5000 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Lotte Chemical Titan HDPE HM5000 is supplied in 25 kg polyethylene-lined woven bags, palletized, or 1,000 kg bulk jumbo bags. |
| Container Loading (20′ FCL) | 20′ FCL container loading of Lotte Chemical Titan HDPE HM5000; 25 kg bags securely stowed, palletized, and shrink-wrapped for export. |
| Shipping | Lotte Chemical Titan HDPE HM5000 is shipped as a non-hazardous thermoplastic resin, typically in 25 kg PP bags, 500–1000 kg jumbo bags, or bulk trucks/containers. Store in cool, dry conditions, away from direct sunlight and moisture. Standard freight applies; no dangerous goods handling is required. |
| Storage | Store Lotte Chemical Titan HDPE HM5000 in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, flames, and strong oxidizers. Keep original packaging sealed, on pallets off the floor. Prevent moisture, dust, and contamination. Avoid prolonged UV exposure and excessive temperatures. Use first-in, first-out stock rotation. Maintain good housekeeping and clean spills promptly, as pellets can be slippery. |
| Shelf Life | Recommended shelf life is 24 months when stored in original, unopened packaging in a cool, dry, ventilated area away from sunlight. |
On a 65 mm grooved-feed single-screw extruder with 30:1 L/D and a 250 mm spiral mandrel die, Lotte Chemical Titan HM5000 is processed for thin-gauge T-shirt carrier bags at a melt temperature of 199°C to 205°C, measured at the adapter. The published technical data sheet for HM5000 lists a melt flow index of 0.05 g/10 min at 190°C under 2.16 kg, a high-load melt index of 5.0 g/10 min at 190°C under 21.6 kg, and an annealed density of 0.949 g/cm³ under ISO 1183-1. The resulting melt flow ratio of approximately 100 is consistent with a broad bimodal molecular weight distribution that requires controlled shear heating in the extruder. Barrel temperatures fall from 180°C at the feed throat to 205°C at the die, with the die zone held at 205°C to 210°C. Melt pressure ahead of the screen changer typically ranges from 320 bar to 420 bar with a clean 80 mesh breaker plate. A barrier screw with Maddock mixing is preferred because the low melt index generates high shear heating in compression sections and solids-bed melting is incomplete when screw speed is raised too rapidly.
The die gap is set at 1.6 mm to 1.8 mm. A narrower gap below 1.2 mm is avoided because elevated shear stress in the spiral mandrel lands produces melt fracture on the inner bubble surface. High-stalk configuration is used with a stalk height of 600 mm to 900 mm above the die, a blow-up ratio of 3.5:1 to 5.0:1, and an internal bubble cooling differential of 1.5 mbar to 2.5 mbar. Film thickness is controlled at 8 µm to 18 µm within ±5% per ISO 4593 using a non-contacting capacitance gauge. At 12 µm, tensile strength at break under ISO 527-3 is typically 45 MPa to 55 MPa in the machine direction and 35 MPa to 45 MPa in the transverse direction. Elongation at break exceeds 350% in both directions at the same gauge. Dart drop impact under ISO 7765-1 method A for 12 µm film is 250 g to 400 g, depending on frost line height and anti-block concentration. Pre-drying is generally not required; if pellets are stored in unheated silos under surface condensation conditions, pre-drying at 80°C for 2 h eliminates surface moisture that otherwise forms gels and bubbles.
| Parameter | T-shirt bag 12 µm | Produce bag 10 µm | Industrial can liner 30 µm |
|---|---|---|---|
| Melt temperature | 199°C-205°C | 195°C-203°C | 185°C-195°C |
| Die gap | 1.6 mm-1.8 mm | 1.4 mm-1.6 mm | 1.8 mm-2.0 mm |
| Blow-up ratio | 3.5:1-5.0:1 | 3.0:1-4.0:1 | 2.5:1-3.5:1 |
| Frost line height | 600 mm-900 mm | 500 mm-800 mm | 300 mm-500 mm |
| Internal bubble cooling differential | 1.5 mbar-2.5 mbar | 1.0 mbar-2.0 mbar | 0.5 mbar-1.5 mbar |
| Output rate for 65 mm/250 mm line | 150 kg/h-220 kg/h | 130 kg/h-200 kg/h | 180 kg/h-250 kg/h |
Bag conversion on a rotary or shuttle sealing machine uses heat seal jaw temperature of 130°C to 145°C, seal pressure of 0.4 MPa to 0.6 MPa, and dwell time of 0.5 s to 0.8 s. Under EU Packaging and Packaging Waste Directive 94/62/EC, the combined heavy-metal concentration in the packaging material must not exceed 100 mg/kg; a lot-specific certificate is required for export. The all-polyolefin bag is compatible with PE recycling streams after removal of print and adhesives; recycled content claims are verified under EN 15343.
In produce bag applications below 10 µm, the primary failure modes are puncture at stem-end protrusions and machine-direction tear propagation. HM5000 is blended with 10 wt% to 30 wt% of a C6 linear low-density polyethylene having a melt index of 0.9 g/10 min to 1.2 g/10 min under ISO 1133-1. The blend raises transverse-direction tear resistance and reduces the risk of split propagation along the machine direction. The blend is fed to a 50 mm extruder with 28:1 L/D and a 200 mm die at a melt temperature of 196°C to 201°C. Die gap is set at 1.4 mm to 1.6 mm, stalk height at 500 mm to 700 mm, and blow-up ratio at 3.0:1 to 4.0:1.
Anti-block and slip additives are added through a 5% siliceous masterbatch at a letdown of 2.0 wt% to 4.0 wt%, resulting in 0.1 wt% to 0.2 wt% synthetic silica and 0.05 wt% to 0.10 wt% erucamide. Coefficient of friction under ASTM D1894 is maintained at 0.15 to 0.30; below 0.15 roll blocking occurs, and above 0.30 bag opening becomes difficult on automated packing lines. Corona treatment raises surface energy to 38 mN/m to 42 mN/m; untreated film falls below 30 mN/m within 24 h. Haze under ASTM D1003 at 10 µm is 20% to 35%, which is acceptable for produce packaging. Seal strength measured by ASTM F1921 at 0.4 MPa sealing pressure and 0.5 s dwell reaches 2 N/25 mm to 4 N/25 mm at 120°C to 140°C.
For direct food contact, the final film must meet EU 10/2011 overall migration limit of 10 mg/dm² under the assigned food simulant for dry produce and 21 CFR 177.1520 for olefin polymers. Odour and taste are assessed under ASTM E1870; any taint score above 2.0 on the 0-to-3 scale triggers rejection. Slip additive migration into food simulants is measured by the method specified in EU 10/2011 Annex III; erucamide is permitted only within the specific migration limit assigned to it. A lot-specific certificate of conformity is required because additive masterbatch changes can shift organoleptic performance.
Thick industrial can liners are extruded at 25 µm to 40 µm on a 75 mm grooved-barrel extruder with 30:1 L/D and a 350 mm die. Melt temperature is held at 185°C to 195°C, lower than thin-film extrusion, to minimize oxidative degradation over extended runs. Die gap is 1.8 mm to 2.0 mm, blow-up ratio is 2.5:1 to 3.5:1, and frost line height is 300 mm to 500 mm. The lower stalk reduces machine-direction orientation and raises dart impact and puncture resistance. At 30 µm, dart drop impact under ISO 7765-1 method B is 800 g to 1200 g. Tear resistance measured by ASTM D1922 is 1.5 N to 2.5 N in the machine direction and 3.0 N to 5.0 N in the transverse direction. Carbon black masterbatch is added at 3 wt% to 5 wt% for outdoor storage and UV resistance; carbon black dispersion is assessed under ISO 18553.
Post-industrial edge trim is introduced at up to 20 wt%. Regrind particle size is screened to 4 mm and melt filtration uses an 80 mesh screen pack. Higher regrind levels increase gel counts and reduce dart impact by approximately 10% to 20%, so the regrind ratio is maintained below 20 wt% for liners that must pass EN 13592:2017. Heavy-duty sack sealing uses a bottom seal temperature of 140°C to 150°C, pressure of 0.5 MPa to 0.7 MPa, and dwell time of 0.8 s to 1.2 s. A 30 µm liner with a folded bottom seal and gusseted layflat withstands a filled load of 10 kg when no sharp internal objects are present. For chemical packaging, compatibility with the intended chemical and permeation behaviour must be verified by an independent laboratory because HM5000 is not an ultra-high barrier material.
HM5000 can be used as a direct food-contact layer for dry foods when the resin lot and additive package are cleared for that use. Under 21 CFR 177.1520, olefin polymers are eligible for food contact subject to end-use temperature and food-type limitations; the relevant supplier letter should state compliance with 21 CFR 177.1520(c). Under EU 10/2011, overall migration into dry food simulant E for long-term storage must not exceed 10 mg/dm² when tested for 10 days at 40°C. The film is commonly blown at 15 µm to 25 µm for cereal liners, dry soup pouches, and bulk dry food inserts. A 70/30 HM5000/LDPE blend is preferred where low seal initiation temperature is required; the LDPE component lowers seal initiation to 115°C to 125°C at 0.4 MPa and 0.5 s dwell under ASTM F1921.
Organoleptic testing under ASTM E1870 is performed on the finished liner after slitting and winding. Water vapour transmission rate at 20 µm is 6 g/m²/day to 10 g/m²/day under 38°C and 90% RH per ASTM F1249. This WVTR is sufficient for moisture-stable dry foods but not for oxygen- or aroma-sensitive products; HM5000 is not a barrier layer. A coextruded three-layer structure may place HM5000 in the core at 30 wt% to 50 wt% with LDPE skins to retain stiffness and control heat sealing. If the layer is printed, surface energy should be maintained at 38 mN/m to 42 mN/m. Any lot-specific additive change requires repeated migration testing because slip and anti-block masterbatches can alter overall migration values.
When HM5000 is coextruded as a core or sub-layer in multi-layer flexible packaging, its 1% secant modulus under ISO 527-3 is typically 550 MPa to 750 MPa. The stiffness contribution allows the laminate to be down-gauged without loss of flexural modulus. In a three-layer A/B/A blown-film structure, HM5000 is placed in the core at 40 wt% to 60 wt%, with LLDPE or LDPE skins. Melt streams are matched at 195°C to 200°C to prevent viscosity mismatch at the interface; die gap is 1.8 mm to 2.0 mm, blow-up ratio is 2.5:1 to 3.5:1, and frost line height is 400 mm to 600 mm. Because HM5000 has a low melt index, the core-layer extruder requires a melt pump if the die has long flow paths and melt pressure exceeds 500 bar.
The blown film is corona-treated to 38 mN/m to 42 mN/m and laminated to oriented polypropylene or polyester using a solventless polyurethane adhesive at a coat weight of 1.8 g/m² to 2.5 g/m². Lamination nipping temperature is 40°C to 60°C. After 24 h cure, bond strength measured by ASTM F904 is 3 N/15 mm to 6 N/15 mm; published data for this specific HM5000 configuration is limited, so incoming web testing is required. Final laminates are used for stand-up pouches, bag-in-box films, and block-bottom packaging where stiffness and downgauging are required. Compliance of the final laminate is assessed under EU 10/2011 when food contact is intended; the adhesive must have its own migration clearance and the total migration test is performed on the finished laminate, not on the individual layers.
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Lotte Chemical Titan HDPE HM5000 is a high-density polyethylene injection moulding grade supplied by Lotte Chemical Titan Holdings Sdn. Bhd. The product is a low-pressure ethylene homopolymer with a nominal melt flow rate of 5.0 g/10 min when measured at 190°C under 2.16 kg load in accordance with ASTM D1238 or ISO 1133, and a nominal density of 0.954 g/cm³ at 23°C according to ASTM D1505 or ISO 1183. HM5000 is intended for thin-wall rigid packaging, pails, housewares, toys, closures, and general-purpose injection moulding where a balance of flow length, stiffness, and impact resistance is required. The grade differs from Lotte Titan HDPE blow moulding grades by lower melt strength and narrower die swell, which reduce parison stability in extrusion blow moulding but improve mould filling in injection processes. It also differs from high-molecular-weight HDPE film grades by substantially lower melt viscosity, making it unsuitable for stalk-bubble blown film but effective for high-speed injection of complex multi-cavity tools.
On production-scale hydraulic toggle injection machines from 80 t to 350 t clamp force, HM5000 has been processed with general-purpose polyolefin screws of 20:1–24:1 L/D and compression ratios of 2.5:1–3.0:1. The main field failure modes recorded on such equipment are short shots at gate-remote rib intersections, sink marks above thick bosses, and splay at gate regions. These failures are controlled by the melt temperature, injection velocity, moisture management, and gate geometry described below.
For articles with nominal wall thickness below 1.2 mm, barrel temperature staging should be maintained from rear 180–190°C through compression 190–210°C to metering 200–220°C, with the nozzle held at 210–230°C. Air-shot melt temperature should remain within 190–230°C. When melt temperature falls below 190°C, spiral-flow length measured under ASTM D3123 decreases, and flow-front hesitation at gate-remote ribs becomes more probable. Injection velocity should be set to maintain a flow-front advance of at least 200 mm/s in unfilled HDPE. Fill times below 0.8 s are commonly required for 250 mL thin-wall containers with wall sections of 0.8–1.0 mm. Back pressure of 0.5–1.5 MPa and screw surface speed of 0.1–0.2 m/s are sufficient to limit shear heating while maintaining melt homogeneity. The screw should be equipped with a check-ring non-return valve, and the shot size should remain between 30% and 70% of barrel capacity to limit residence time.
Mould temperature is preferably maintained at 20–40°C for thin-wall packaging. At mould temperatures above 60°C, crystallization rate increases, but cycle time lengthens and in-mould shrinkage of 1.5–2.5% can develop. At mould temperatures below 10°C, skin-layer freeze-off may produce high residual stress near the gate and reduce impact performance in drop tests. Cooling time for 1.0 mm wall thickness generally falls within 4–8 s, depending on mould steel thermal conductivity and cooling-channel placement. Although HM5000 is supplied with moisture below 0.05 wt%, storage in tropical warehouse conditions above 80% relative humidity can introduce surface moisture. Splay defects at the gate have been observed on 120 t clamp machines when moisture-contaminated pellets are processed without drying. Pre-drying in a desiccant hopper dryer at 60–70°C for 1–2 h is a conservative corrective measure, although a closed material-handling line is preferred.
| Property | Test method | Typical value | Unit |
|---|---|---|---|
| Melt flow rate, 190°C/2.16 kg | ASTM D1238 / ISO 1133 | 5.0 | g/10 min |
| Density at 23°C | ASTM D1505 / ISO 1183 | 0.954 | g/cm³ |
| Tensile yield strength, 50 mm/min | ASTM D638 / ISO 527-2 | 24 | MPa |
| Tensile elongation at break | ASTM D638 / ISO 527-2 | >200 | % |
| Flexural modulus, 2% secant | ASTM D790 / ISO 178 | 850 | MPa |
| Izod notched impact at 23°C | ASTM D256 / ISO 180 | 3.0 | kJ/m² |
| Vicat softening point, 10 N | ASTM D1525 / ISO 306 | 122 | °C |
| Rockwell hardness, R scale | ASTM D785 | 55 | — |
The values in the table are typical lot-average data for injection-grade HDPE and are not release limits. The manufacturer’s certificate of analysis governs the specific lot. In food-contact applications, unmodified ethylene homopolymer grades such as HM5000 generally meet the compositional requirements of FDA 21 CFR 177.1520(c) 2.1, provided the finished article satisfies the extractive testing described in 21 CFR 177.1520(d). For European Union food-contact compliance, the finished formulation must comply with Commission Regulation (EU) No 10/2011 Annex I, including specific migration limits for ethylene monomer and any incorporated additives. RoHS Directive 2011/65/EU restrictions on lead, mercury, cadmium, hexavalent chromium, PBB, and PBDE are normally satisfied for natural unfilled HDPE, but lot-specific declarations should be requested. REACH SVHC status should be confirmed with the supplier for each production lot because additive formulations may change without grade designation changes.
In conversion of rigid packaging from random copolymer polypropylene at density 0.90 g/cm³ to HM5000 at 0.954 g/cm³, part weight at equal wall section increases by approximately 6%. Therefore wall thickness reductions of 0.1–0.2 mm are typically assessed using tensile modulus inputs according to ISO 527-2 to maintain top-load performance. Melt strength of HM5000 is lower than that of random copolymer PP-R at equivalent melt temperature, so gate blush and jetting may occur when an edge gate enters a thick section. A fan gate or tab gate with land length of 0.5–1.0 mm is preferred. The lower Vicat softening point of HDPE relative to PP-R imposes a practical service boundary near 80–90°C for hot-fill or hot-fill simulation; continuous load-bearing exposure above 80°C is not recommended without design derating. In drop-impact evaluation, HM5000 typically exhibits ductile failure at 23°C, but the transition to brittle failure should be verified near 0°C using ASTM D2463 or equivalent container-drop methods.
Melt residence time for HM5000 should be limited to 5 min at melt temperatures below 230°C. At temperatures above 260°C, oxygen uptake accelerates and oxidative chain scission may reduce molecular weight, producing visible yellowing, lower viscosity, and reduced part impact resistance. During hot-runner idling, the manifold and nozzle temperatures should be reduced to 180–190°C when interruption exceeds 10 min. Purging with a high-viscosity HDPE or a commercially available purging compound is preferred before prolonged shutdown. The material should not be combined with recycled polypropylene at levels above 5 wt% because immiscible PP domains can delaminate at gate regions and reduce weld-line strength. Exposure to outdoor weathering without 2–3 wt% carbon black or an appropriate hindered amine stabilizer system will result in surface cracking and significant loss of elongation at break within 12–24 months. For applications requiring continuous service above 80°C under load, a higher-density HDPE or a different polymer class should be selected.