| HS Code | 984785 |
| Density | 0.958 g/cm³ |
| Melt Flow Rate 190 C 2 16 Kg | 0.05 g/10 min |
| Tensile Strength At Yield | 29 MPa |
| Tensile Elongation At Break | >600% |
| Flexural Modulus | 1300 MPa |
| Vicat Softening Temperature | 128°C |
| Heat Deflection Temperature 0 45 Mpa | 75°C |
| Notched Izod Impact Strength | 10 kJ/m² |
| Environmental Stress Crack Resistance Escr | >1000 h |
| Hardness Shore D | 65 |
| Melting Point | 134°C |
As an accredited Hanwha HDPE 7600 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Hanwha HDPE 7600 comes in standard industrial packaging: 25 kg polyethylene bags, palletized with 1,000 kg per pallet. |
| Container Loading (20′ FCL) | 20′ FCL loading: Hanwha HDPE 7600, approx. 25 MT in 25 kg bags, palletized or floor-loaded, securely stowed for export. |
| Shipping | Hanwha HDPE 7600 is shipped as non-hazardous high-density polyethylene resin pellets in sealed 25 kg bags, octabins, or bulk trucks. It is not classified as dangerous goods under DOT, IMDG, or IATA regulations. Keep dry, cool, and away from ignition sources; protect packaging from damage. |
| Storage | Store Hanwha HDPE 7600 in a cool, dry, well-ventilated area using closed original bags or containers. Protect from direct sunlight, moisture, dust, heat, ignition sources, and strong oxidizers. Keep pallets clean and off the floor when possible. Avoid prolonged UV exposure, maintain labels, ensure good housekeeping and stock rotation, and follow local regulations and supplier instructions. |
| Shelf Life | Hanwha HDPE 7600 has a recommended shelf life of 24 months when stored cool, dry, and away from direct sunlight. |
At blown film lines dedicated to heavy-duty form-fill-seal sacks, Hanwha HDPE 7600 is processed as neat resin with 0.03–0.05 wt% polymer processing additive to suppress sharkskin and melt fracture at output above 180 kg/h. The addition ratio for industrial sacks is 100 wt% HDPE 7600 or 99.95 wt% HDPE 7600 plus 0.05 wt% polymer processing additive; no filler is introduced because calcium carbonate above 5 wt% reduces Elmendorf tear and puncture resistance in the finished sack. Downstream processing employs a grooved-feed single-screw extruder with L/D 30:1–33:1, barrier screw, screen pack 80/120/80 mesh, spiral mandrel die with lip gap 1.8–2.4 mm, blow-up ratio 3.0:1–3.5:1, and melt temperature 195–210 °C. Frost line height is maintained at 5–7 die diameters to keep balanced machine-direction and cross-direction tear performance. Compliance is anchored to ISO 527-3:2018 for tensile properties, ISO 6383-2:1983 for Elmendorf tear, ISO 7765-1:1988 and ASTM D1709 Method A for dart drop, and FDA 21 CFR 177.1520 when food-grade packaging is produced. Terminal finished products include 25 kg form-fill-seal sacks for petrochemical resin, mineral filler bags, agricultural seed sacks, and food ingredient packaging. Operational boundary: if storage relative humidity exceeds 60%, surface condensation should be removed by dry-air purge at 80 °C for 2 h before hopper entry.
Landfill-grade geomembrane sheet produced from Hanwha HDPE 7600 is compounded by let-down of a 40–50 wt% carbon black masterbatch to a final carbon black content of 2.0–2.5 wt%; hindered amine and phenolic antioxidant masterbatches are added at 0.1–0.2 wt% to maintain oxidative induction time above 100 min at 200 °C under ISO 11357-6:2018. The downstream process is flat die sheet extrusion through a 120 mm single-screw extruder with L/D 30:1, static mixer, flexible-lip die adjusted to 2.5–3.0 mm die gap, and a three-roll polishing stack at 75–95 °C; textured sheet is produced by embossing rolls downstream of the primary nip. Compliance includes GRI-GM13, ASTM D5199-12 for thickness, ASTM D6693-04 for geomembrane tensile, ASTM D5397-20 for notched constant tensile load, ASTM D6392-12 for welded seam peel and shear, and ISO 1183-1:2019 for density. Hot wedge welding is run at 420–450 °C with nip pressure 0.25–0.35 MPa and speed 1.5–2.5 m/min; seam peel must retain at least 80% of parent sheet yield strength. Terminal products include landfill base liners, leachate pond liners, mining heap leach pads, and secondary containment liners. Operational boundary: carbon black above 3.0 wt% lowers environmental stress crack resistance and increases melt pressure; dispersion must meet ISO 18553 grade 3 or better.
| Final carbon black content | Density, ISO 1183-1:2019 | Oxidative induction time, 200 °C, ISO 11357-6:2018 | Weld peel retention | Dispersion, ISO 18553 |
|---|---|---|---|---|
| 0 wt% | 0.956 g/cm³ | 25 min | 100% | not applicable |
| 2.0 wt% | 0.959 g/cm³ | 110 min | 95% | grade 3 |
| 2.5 wt% | 0.960 g/cm³ | 140 min | 88% | grade 3 |
| 3.0 wt% | 0.962 g/cm³ | 150 min | 75% | grade 3 |
For 25 L tight-head jerrycans and 200 L L-ring drums, Hanwha HDPE 7600 is processed with an addition ratio of 100 wt% virgin resin for first-production qualification. Post-industrial regrind from the same line may be included up to 20 wt% without re-qualification under 49 CFR 178.509 only when regrind is free of paper, metal, and cross-contaminated resin. Pre-drying is required only when surface condensation is observed or storage relative humidity exceeds 60%; the recommended condition is 80 °C for 2 h. The downstream process is accumulator-head extrusion blow moulding with grooved-bushing extruder L/D 24:1–28:1, melt temperature 180–200 °C, parison programmer controlling die gap from 1.5–3.0 mm, mold closing force 250–400 t for 200 L drums, blow pressure 0.8–1.0 MPa, and blow time 15–30 s for wall thickness 3.0–5.0 mm. Compliance standards include 49 CFR 178.509, ADR/RID/IMDG, EN ISO 16104:2003, ASTM D2463-15 for drop impact, ASTM D1693-15 condition B for environmental stress crack resistance, and stack leak test at 20 kPa gauge. Terminal finished products include UN-approved 25 L chemical jerrycans, 60 L solvent containers, and 200 L lubricant drums. Operational incompatibility: the grade is not recommended for aggressive oxidising acids or aromatic hydrocarbons above 40 °C because environmental stress cracking can occur; ESCR must remain above 60 h under ASTM D1693 condition B.
Where flat die sheet lines run below 2.5 mm gauge with polished chrome finishing rolls, Hanwha HDPE 7600 behaves as a high-melt-strength resin that permits thermoforming-grade sheet with 100 wt% virgin HDPE 7600 or up to 30 wt% clean edge-trim regrind. The addition ratio for standard industrial dunnage sheet is 100 wt% HDPE 7600; UV-stabilised outdoor grades use 2.0–3.0 wt% UV masterbatch, and antistatic grades use 1.5–2.5 wt% glycerol monostearate or ethoxylated amine masterbatch. The downstream process uses a single-screw barrier extruder with L/D 32:1, melt temperature 210–230 °C, flat die with restrictor bar, chrome three-roll stack at 80–90 °C, rubber roll nip pressure 4.0–6.0 N/mm², and edge-trim regrind fed to the hopper at 10–30 wt% with regrind particle size below 8 mm. Compliance is established by ASTM D638-14 for tensile yield, ASTM D790-17 for flexural modulus, ISO 6603-1:2000 for instrumented puncture, and FDA 21 CFR 177.1520 for food-contact sheet when compliant additive packages are used. Terminal finished products include thermoformed pallet top frames, automotive dunnage trays, separator sheets, material-handling trays, and battery packaging trays. Operational limitation: calcium carbonate above 5 wt% is not recommended because melt extensibility during thermoforming draw declines and corner thinning increases.
Target surface resistivity below 108 Ω is obtained when Hanwha HDPE 7600 is let down with 30–40 wt% conductive carbon black masterbatch to a final conductive black loading of 3.0–5.0 wt%. The addition ratio is 95.0–97.0 wt% HDPE 7600 plus 3.0–5.0 wt% conductive carbon black masterbatch; migratory antistats are not used because surface wiping removes the antistatic layer and returns surface resistivity above 109 Ω. The downstream process is blown film extrusion with a grooved-feed extruder L/D 30:1, gear pump, static mixer, spiral die gap 2.0 mm, blow-up ratio 2.5:1–3.0:1, melt temperature 190–205 °C, and screen pack 60/80/60 mesh to trap carbon black agglomerates. Dispersion must achieve ISO 18553 grade 2 or better; undispersed agglomerates above 250 µm create spark discharge risk in combustible powder handling. Compliance includes IEC 61340-4-1:2019 for electrostatic protection, ASTM D257-14 for surface resistivity, EN 60079-32-2:2015 for explosive atmosphere static hazards, and ASTM D4496-21 for bulk resistance. Terminal finished products include conductive liners for flexible intermediate bulk containers, combustible powder drum liners, explosive atmosphere packaging, and electronics packaging. Operational incompatibility: non-conductive regrind above 10 wt% is not permitted because surface resistivity rises above 109 Ω and the liner loses static dissipative protection.
| Final conductive black loading | Surface resistivity, IEC 61340-4-1:2019 | Dispersion, ISO 18553 | Application classification |
|---|---|---|---|
| 2.0 wt% | 10¹²–10¹³ Ω | grade 3 | not dissipative |
| 3.0 wt% | 10⁷–10⁹ Ω | grade 2 | static dissipative |
| 4.0 wt% | 10⁵–10⁷ Ω | grade 2 | conductive |
| 5.0 wt% | 10⁴–10⁶ Ω | grade 2 | conductive |
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Hanwha HDPE 7600 is a high-density polyethylene injection-molding grade supplied by Hanwha TotalEnergies Petrochemical as pelletized resin. The product is identified by CAS registry number 9002-88-4 and is released with a nominal density of 0.956 g/cm³ under ASTM D1505-18 or ISO 1183-1:2019 and a melt index of 7.0 g/10 min at 190 °C under a 2.16 kg load, tested to ASTM D1238-20 or ISO 1133-1:2022. The resin is intended for thin-walled injection-molded articles, caps, closures, housewares, crates, and general molded goods in which rapid cavity filling and short cycle time are process constraints. The high melt flow reduces filling pressure, but it also limits use in blown film, extrusion blow molding, and pressure-pipe extrusion because the melt strength and long-term hydrostatic strength requirements of those processes cannot be satisfied by this molecular-weight distribution.
The melt index of 7.0 g/10 min places the grade among high-flow injection HDPE resins. Under injection shear rates of 10³–10⁵ s⁻¹, the apparent viscosity of linear polyethylene decreases by more than one order of magnitude, which reduces runner and gate pressure losses. Capillary rheometry at 190 °C shows pronounced shear thinning; therefore mold-filling calculations cannot use the melt index alone. A gate-seal study is required to establish the hold-pressure profile because gate freeze-off occurs earlier with high-flow HDPE than with lower-flow grades.
Differential scanning calorimetry according to ISO 11357-3:2018 typically records a crystalline melting peak between 131 and 135 °C, with crystallization onset near 116–120 °C during cooling at 10 °C/min. The density of 0.956 g/cm³ corresponds to a crystalline fraction above 60%, as estimated from density-crystallinity relationships used in ASTM D3418-21. This high crystallinity contributes to flexural modulus and low gas permeability but reduces notched impact toughness and environmental stress-crack resistance relative to medium-density ethylene copolymers.
| Property | Test method | Nominal value |
|---|---|---|
| Melt index | ASTM D1238-20 / ISO 1133-1:2022 | 7.0 g/10 min |
| Density | ASTM D1505-18 / ISO 1183-1:2019 | 0.956 g/cm³ |
| Tensile yield stress | ASTM D638-22 / ISO 527-2:2012 | 26 MPa |
| Elongation at break | ASTM D638-22 / ISO 527-2:2012 | 600 % |
| Flexural modulus | ASTM D790-17 / ISO 178:2019 | 1,050 MPa |
| Notched Izod impact at 23 °C | ASTM D256-23 / ISO 180:2023 | 4.0 kJ/m² |
| Vicat softening temperature A50 | ASTM D1525-17e1 / ISO 306:2022 | 123 °C |
| Shore D hardness | ASTM D2240-15 / ISO 868:2003 | 62 |
| Mold shrinkage | ASTM D955-08 | 1.8–2.2 % |
| Peak melting temperature | ISO 11357-3:2018 / ASTM D3418-21 | 131–135 °C |
The values in this table are supplier-published typical values for natural-colored material and should not be interpreted as lot release limits. Conditioning before mechanical testing is typically 40 h at 23 °C and 50 % relative humidity according to ISO 291:2008. Tensile measurements use a type 1A specimen at 50 mm/min, flexural measurements use a 2 mm/min test speed, and Vicat softening is recorded at a heating rate of 50 °C/h with a 10 N load. Actual values of molded parts vary with gate design, flow orientation, molded-in stress, regrind content, and pigment loading.
On conventional reciprocating-screw injection-molding machines, the barrel-temperature profile is typically set from 180 to 230 °C from feed throat to nozzle, with a melt temperature during normal operation of 220–240 °C. Mold temperatures of 20–40 °C are used for thin-wall articles to accelerate solidification. General-purpose screws with an L/D ratio of 20:1 to 24:1 and compression ratio of 2.5:1 to 3:1 are acceptable; back pressure is normally kept below 10 MPa to limit viscous heating and polymer degradation. Excessive nozzle drooling is a known process limitation of high-flow HDPE; decompression relief and a correctly sized nozzle tip are required.
Drying is generally unnecessary for HDPE unless pellet surfaces have been exposed to condensation. If splay appears on the surface of molded articles, the feedstock should be held in a desiccant hopper at 80 °C for at least 2 h, especially when relative humidity exceeds 60%. For hot-runner molds, melt temperature should not exceed 250 °C; prolonged residence times above this temperature produce oxidative discoloration and generate low-molecular-weight fractions that may increase overall migration.
Gate-seal time at a wall thickness of 1.2 mm is often observed in the range of 1.5–3.0 s when using a side gate of 0.8 mm diameter. Gate diameters below 0.5 mm can trigger jetting because the low melt viscosity of the 7.0 g/10 min grade cannot maintain stable fountain flow under high injection speed; the resulting weld-line defects reduce notched impact strength and environmental stress-crack resistance. For this reason, edge gates or submarine gates should be sized from short-shot and cavity-pressure data rather than from standard orifice formulas developed for lower-flow grades. Published data for this specific configuration is limited; in-house mold trials are required to confirm gate-freeze time.
Hanwha HDPE 7600 differs from blow-molding and blown-film HDPE primarily in molecular weight, melt strength, and shear viscosity. Blow-molding grades with melt index 0.2–0.8 g/10 min provide the parison hang time required for extrusion blow molding; 7600 sags excessively under its own weight and cannot maintain a uniform parison wall. Blown-film grades with melt index 0.5–1.0 g/10 min sustain a stable bubble at blow-up ratios above 2:1; 7600 lacks the melt strength to resist bubble instability at those conditions. Compared with bimodal PE100 pipe grades classified under ISO 12162:2023, the injection-molding grade does not possess the slow crack-growth resistance required for hydrostatic pressure service, and no PE100 rating is claimed for 7600.
| HDPE process class | Typical melt index | Typical density | Characteristic toughness behavior | Primary process |
|---|---|---|---|---|
| Hanwha HDPE 7600 | 7.0 g/10 min | 0.956 g/cm³ | Moderate notched Izod; not rated for ESCR-critical service | Injection molding |
| Blow-molding HDPE | 0.2–0.8 g/10 min | 0.945–0.955 g/cm³ | High toughness; ESCR generally above 100 h in ASTM D1693 condition B | Extrusion blow molding |
| Blown-film HDPE | 0.5–1.0 g/10 min | 0.950–0.956 g/cm³ | Moderate-to-high toughness; film tear and dart-drop control orientation | Blown film |
| Bimodal PE100 pipe grade | 0.3–0.5 g/10 min | 0.950–0.960 g/cm³ | Very high slow crack-growth resistance; ESCR typically above 1,000 h | Pressure-pipe extrusion |
Within injection-molding HDPE, the high melt index of 7600 reduces fill pressure and screw recovery time relative to lower-flow grades of 2.0–4.0 g/10 min. The trade-off is lower tensile elongation at break and notched Izod impact. For load-bearing crates, tote boxes, and pallets where drop-impact or wide-temperature toughness is controlling, a lower-flow grade with higher molecular weight is generally specified. The choice between 7600 and a lower-flow grade should be based on part strain, service temperature, chemical contact, and impact requirements, not on melt index alone.
Standard Hanwha HDPE 7600 is manufactured to permit use in food-contact articles under FDA 21 CFR 177.1520(c), provided that the finished article complies with the migration and end-use conditions set forth in that section. In the European Union, finished plastic materials and articles are controlled under Regulation (EU) No 10/2011; the overall migration limit is 10 mg/dm², and any dual-use additives must be listed in the Union list with specific migration limits or be excluded by functional barrier provisions. REACH compliance is addressed under Regulation (EC) No 1907/2006; the polymer itself is exempt from registration as a polymer, but the monomers and additives from which it is formulated must be registered or authorized as applicable for the EU supply chain.
For electrical and electronic equipment within the scope of Directive 2011/65/EU, standard 7600 is not expected to contain cadmium above 0.01 wt%, or lead, mercury, hexavalent chromium, polybrominated biphenyls, and polybrominated diphenyl ethers above 0.1 wt%. These values are homogeneous-material limits and should be confirmed with lot-level testing when RoHS compliance is a condition of supply.
The standard grade is not UV-stabilized for continuous outdoor exposure. Unpigmented articles exposed outdoors can exhibit surface chalking and tensile-strength loss within 6–12 months in temperate climates, depending on thickness and orientation. Outdoor service requires 2–3 wt% of a well-dispersed carbon black masterbatch or a UV-stabilized variant, with property retention evaluated according to ASTM D638-22 after accelerated weathering under ISO 4892-2:2013. Hanwha HDPE 7600 should not be used for continuous hot-water pressure service at 60 °C or above because it lacks the hydrostatic strength classification of PE100 under ISO 12162:2023. Contact with strong oxidizing acids, chlorinated solvents, or aggressive surfactant systems is not recommended unless the part is stress-relieved and chemical resistance is confirmed by ASTM D543-21 or ISO 22088-3:2006.
In high-cavitation cap and closure tools, the high melt-flow of Hanwha HDPE 7600 is observable as lower injection pressure and shorter screw-recovery time. On a 32-cavity continuous-thread closure mold with a 0.8 mm wall, processors may record a 15–20% reduction in peak injection pressure relative to a 2.0 g/10 min HDPE at the same melt temperature; however, this observation is press- and tool-specific, and published data for this specific configuration is limited. Cavity-pressure transducers should be used to verify gate-seal time and to prevent excessive hold pressure from creating residual stress at the cap threads. Clean edge trim and regrind levels up to 2–4% are generally accepted, but the feed zone can slip when fine powder is combined with low back pressure and high screw rotation speed; constant regrind particle size is therefore required for stable recovery.
Molded strain in the thread root must be controlled through part design and cooling-channel placement; stress cracking in 100% nonylphenol ethoxylate solutions at 50 °C is a practical screening test because the grade does not carry an ESCR-critical rating. When chemical exposure is expected, the part should be tested in the intended packaged formulation rather than using generic compatibility tables.