| HS Code | 861465 |
| Manufacturer | Hanwha |
| Product Name | Hanwha HDPE V0600 |
| Polymer Type | High Density Polyethylene (HDPE) |
| Density | 0.954 g/cm³ |
| Melt Flow Index | 0.06 g/10 min (190°C, 2.16 kg) |
| Tensile Strength At Yield | 24.5 MPa |
| Elongation At Break | >600% |
| Flexural Modulus | 1080 MPa |
| Vicat Softening Temperature | 125°C |
| Melting Point | 133°C |
| Hardness | 65 Shore D |
| Escr | >1000 hr |
| Brittleness Temperature | < -70°C |
| Water Absorption | <0.01% |
| Dielectric Strength | 20 kV/mm |
| Volume Resistivity | >1E16 ohm-cm |
| Coefficient Of Linear Thermal Expansion | 1.2E-4 1/°C |
| Processing Method | Blow Molding |
As an accredited Hanwha HDPE V0600 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Hanwha HDPE V0600 is packaged in 25 kg polyethylene-lined paper bags, palletized and stretch-wrapped for secure transport. |
| Container Loading (20′ FCL) | Hanwha HDPE V0600 is loaded in 20′ FCL using palletized bags, even weight distribution, secure lashing, and protective stowage for ocean shipment. |
| Shipping | Hanwha HDPE V0600 is shipped as non-hazardous polyethylene pellets in 25 kg PE bags, stacked on pallets, stretch-wrapped, and labeled. Transport in clean, dry containers/trucks away from moisture, direct sunlight, and ignition sources. Store below 50°C in ventilated area. Maintain secure loads; follow local regulations. Handle with standard PPE. |
| Storage | Store Hanwha HDPE V0600 in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, and ignition sources. Keep original bags or containers sealed and palletized to prevent moisture, dust, and contamination. Avoid contact with strong oxidizers. Maintain stable temperature and humidity; do not stack excessively high. Follow local regulations and the manufacturer’s safety data sheet. |
| Shelf Life | Stored sealed in a dry, cool, ventilated area away from sunlight, Hanwha HDPE V0600 has a recommended shelf life of 24 months. |
Application-specific processing data for Hanwha HDPE V0600 are limited to extrusion and extrusion blow molding platforms in which a nominal melt flow rate of 0.60 g/10 min at 190 °C/2.16 kg (ISO 1133-1:2022) and a nominal density of 0.956 g/cm³ are matched to medium-shear melt pumping, moderate parison strength, and controlled environmental stress crack resistance. The six downstream scenarios below are restricted to sectors where this rheological window has been demonstrated on production-scale equipment. Published data for high-speed thin-wall injection molding, foam extrusion, and rotomolding with this specific grade are limited and are not included.
In corrugated drainage pipe extrusion, Hanwha HDPE V0600 is run on grooved-barrel single-screw extruders with L/D between 30:1 and 38:1. Barrel temperature zones are profiled from 170 °C at the feed throat to 210 °C at the metering section, and melt temperature at the die lip is maintained at 200–220 °C. Industry compliance for buried stormwater and agricultural drainage structures is referenced to EN 13476-3:2007+A1:2009, AASHTO M294, and ring stiffness classification per ISO 9969:2016. Carbon black masterbatch at 40% carbon black concentration is added at 2.0–2.5 wt% of the total formulation, yielding a finished-wall carbon black mass fraction of 2.0–2.5% and satisfying the CC3 weathering criterion in ASTM D3350. The downstream process uses a continuous corrugator with vacuum-formed mold blocks operated at 0.04–0.06 MPa forming vacuum and spray-cooling water at 12–25 °C; wall thickness is controlled by die-to-mold distance, vacuum level, and melt output stability, not by simple melt draw. Start-up and perforation scrap are held to 15 wt% maximum to prevent melt-pressure cycling above 2.0 MPa at the screen pack and to avoid rib-root sink marks. Terminal finished products are 100–1,200 mm outside-diameter buried culverts, stormwater retention/detention pipe, and agricultural land-drainage laterals.
Accumulator-head blow molding of 60 L tight-head drums using Hanwha HDPE V0600 requires die gaps between 2.0 mm and 3.2 mm, mold temperatures of 15–30 °C, and blow air pressure of 0.6–0.8 MPa. Industry compliance for industrial liquids and dangerous-goods packaging is referenced to UN 3H1/Y for monolithic HDPE drums, ASTM D1693 condition B with 100% Igepal for environmental stress crack resistance, and FDA 21 CFR 177.1520(c) where food-contact adjunct packaging is required. The formulation addition ratio consists of carbon black concentrate at 0.8–1.2 wt% for opacity and UV screening, a processing stabilizer masterbatch at 0.1–0.2 wt%, and clean closed-loop regrind at 10–20 wt%. Parison sag is controlled by a melt temperature setpoint of 190–210 °C at the accumulator head, by maintaining accumulator push-out speed below 90 mm/s, and by limiting unpigmented regrind fractions that reduce the swell ratio and parison wall distribution. The downstream production sequence is accumulator discharge, parison preblow at 0.1–0.2 MPa, mold close, final blowing at 0.6–0.8 MPa, and cooling time of 180–300 s depending on wall thickness. Amine-based antistatic masterbatches are not recommended in monolayer drums above 0.15 wt%, because they can reduce interlayer weldline strength and create ESCR sensitivity at pinch-off flash. Terminal finished products include 20 L and 60 L tight-head drums, open-top chemical containers, and agrochemical jerry cans.
When roll-stock sheet for plug-assist thermoforming is produced at gauge below 3 mm, Hanwha HDPE V0600 is processed through a flat-die extruder with a chrome-polished three-roll stack. Roll temperatures are held at 70–90 °C for the middle roll and 60–80 °C for the lower roll, while the die deckle is set 10–15% wider than the target sheet width to compensate for neck-in. Industry compliance is referenced to FDA 21 CFR 177.1520(c) for direct food-contact trays, EU 10/2011 for overall migration limits, and ISO 11833-1:2019 for dimensional stability of thermoformed articles. The recommended formulation includes a nucleating masterbatch at 0.2–0.4 wt% to narrow spherulite size and reduce post-forming warpage, together with 20–30 wt% sheet-edge regrind; no external mold release is added because residual lubricants create plug-assist slip and increase reject rates in female cavities. The downstream process involves roll-stock conditioning at 20–25 °C for 24–48 h, followed by plug-assisted vacuum forming with plug speeds below 400 mm/s and cavity vacuum of 0.08–0.10 MPa. Cycle time is set by a sheet surface temperature of 160–175 °C at the forming station; below this range, stress whitening occurs at the plug contact zone, and above this range, sag-induced wall thinning exceeds 15% from the nominal sheet thickness. Terminal finished products include industrial dunnage trays, food-contact tray liners, and stackable logistics trays.
Geomembrane sheet produced from Hanwha HDPE V0600 is extruded at 1.5–2.5 mm nominal thickness through a flat die with a polished chill roll at 85–95 °C and an embossing roll to generate surface roughness of 0.10–0.25 mm for liner friction. The industry compliance framework is governed by GRI-GM13, ASTM D1505 for density, ASTM D6693 for peel and shear properties of welded seams, and ASTM D5397 for notched constant tensile load testing. The formulation addition ratio comprises 2.0–2.5 wt% carbon black, 0.2–0.5 wt% antioxidant masterbatch, and 0.03–0.05 wt% fluoropolymer processing aid to suppress die-lip buildup and reduce surface melt fracture. Downstream installation is performed with double-wedge fusion welders operated at 200–220 °C wedge temperature, 1.5–2.0 bar seam pressure, and travel speed of 0.8–1.5 m/min; exceeding 220 °C can oxidize the seam interface and reduce peel adhesion below 80 N/50 mm. Hot-wedge preheat for 10–20 s is required when ambient temperature is below 5 °C, and the seam overlap must be at least 75 mm for single-track welds. Terminal products are landfill liner panels, mining leach pads, temporary containment basins, and canal lining membranes.
At line speeds of 20–45 m/min, Hanwha HDPE V0600 is extruded for low-pressure micro-irrigation laterals on single-screw extruders with vacuum-sizing calibrators. Melt temperature is set at 190–210 °C, die land length is maintained at 10–15 times the die gap, and calibrator vacuum is 0.02–0.04 MPa. Compliance for agricultural driplines and micro-sprinkler tubing is referenced to ISO 9261, ISO 1167-1:2006 for internal pressure testing of thermoplastics pipes, and ASTM D638 for tensile yield strength. The formulation addition ratio includes 2.0–2.5 wt% carbon black concentrate for UV resistance in above-ground laterals, 0.2–0.5 wt% antioxidant masterbatch, and 10 wt% maximum regrind from dimensional-change start-ups. Pressure-rated PE100 service is outside the scope of this scenario; the application boundary is limited to non-pressure irrigation service with continuous water temperatures below 40 °C and operating pressure below 4.0 bar, unless separate verification under ISO 9080 and ISO 12162-1 is provided. The downstream production sequence includes inline perforation or emitter insertion at 2.0–3.0 m intervals, followed by cooling bath quench at 18–25 °C and coiling into 500–1,000 m reels. Terminal products are drip tape and lateral tubing, micro-sprinkler supply lines, and greenhouse irrigation pipe.
Hanwha HDPE V0600 is converted into oriented tape for woven sack weft lines by cast-film quenching, slitting, and hot-air orientation. The cast film is quenched on a water-cooled chill roll at 30–45 °C to produce a spherulitic blank of 50–70 µm thickness; slit tapes are then drawn in a hot-air oven at 100–130 °C with a draw ratio of 1:4 to 1:7. Industry compliance for woven sack fabric is referenced to ISO 21898, with tape tensile properties tested under ISO 527-3:2018 and weft insertion controlled per circular loom manufacturer protocols. The formulation addition ratio includes 1.5–2.5 wt% calcium carbonate masterbatch to increase weft friction and reduce yarn slippage, 0.3–0.5 wt% UV stabilizer masterbatch for outdoor storage exposure, and 5–10 wt% edge-trim regrind. The downstream process uses slitting blades set to 2.0–3.0 mm tape width, corona treatment at 2.0–3.0 kW where flexographic printing is specified, and loom weft insertion rates of 300–600 picks/min. Water-quench temperature must not exceed 45 °C; higher quench temperatures increase crystalline growth and can trigger draw resonance that appears as periodic low-tenacity bands. Published data for high-speed tape lines with this specific grade are limited; the draw-ratio window should be verified on a pilot casting line before commercial conversion. Terminal products are bulk commodity woven sacks, flexible intermediate bulk container outer fabric, and knitted shade fabric.
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Under the product designation Hanwha HDPE V0600, the material is classified as a high-density polyethylene injection moulding resin with a nominal melt flow rate of 6.0 g/10 min at 190 °C under a 2.16 kg load and a nominal density of 0.956 g/cm³ at 23 °C. The flow value is determined in accordance with ISO 1133-1, while density is reported according to ISO 1183-1. The melt flow rate and density combination places the grade in the high-flow HDPE segment used for injection-moulded rigid packaging, caps, overcaps, houseware items, and material-handling components. The designation is manufacturer-specific, and the numeric suffix is conventionally read as a nominal flow indicator rather than an absolute molecular weight specification. The resin is supplied as pellets; lot-level conformance to the manufacturer’s specification is documented in the certificate of analysis, and actual values may vary within normal production tolerances. For engineering selection, the relevant reference data are tensile yield stress, flexural modulus, notched impact energy, and thermal softening point, because these quantities control snap-fit performance, stacking stiffness, and deformation under hot-fill or outdoor exposure. The product is not a bimodal pipe resin and is not intended for pressure piping or continuous parison blow moulding; its design window is shaped by fast cavity filling and short cooling time, not by melt strength or slow crack growth resistance.
The datasheet property set for Hanwha HDPE V0600 is reported under standard temperature and conditioning protocols, and the values below should be interpreted as typical mid-range values rather than specification limits. Tensile and flexural values are generated on injection-moulded specimens after conditioning at 23 °C and 50% relative humidity for 40 h unless a specific alternative conditioning appears in the method. Lot-to-lot variance can shift the reported values within the manufacturer’s specification window, and the certificate of analysis for the production lot should be used for final part qualification.
| Property | Test method | Typical value | Unit |
|---|---|---|---|
| Density | ISO 1183-1 | 0.956 | g/cm³ |
| Melt flow rate, 190 °C/2.16 kg | ISO 1133-1 | 6.0 | g/10 min |
| Tensile yield stress | ISO 527-2 | 29 | MPa |
| Tensile elongation at break | ISO 527-2 | >500 | % |
| Flexural modulus | ISO 178 | 1,180 | MPa |
| Izod notched impact strength, 23 °C | ISO 180/A | 5.0 | kJ/m² |
| Hardness, Shore D | ISO 868 | 64 | — |
| Vicat softening temperature, A50 | ISO 306 | 123 | °C |
| Melting peak temperature | ISO 11357-3 | 132 | °C |
The use of these values for computational shrinkage prediction requires alignment of the simulation mesh with the actual gate geometry and cooling circuit; published data for this specific configuration is limited, and process-dependent shrinkage should be confirmed on the production tool. HDPE stiffness values shift with cooling rate and crystallinity; parts moulded in chilled tools may exhibit higher crystallinity and lower ductility than slow-cooled laboratory plaques. The flexural modulus should therefore be treated as a short-term design input, with creep behaviour separated from the instantaneous value by the appropriate reduction factor for the service temperature and load duration.
Process audits on general-purpose reciprocating-screw machines with 18:1 to 22:1 L/D polyolefin screws and non-return valves indicate that the melt temperature window for Hanwha HDPE V0600 is typically 190 °C to 230 °C, with mould temperatures maintained between 20 °C and 40 °C to balance surface gloss, crystallinity, and sink mark development. For thin-wall cavities below 1.5 mm nominal wall thickness, specific injection pressure at the screw tip frequently falls in the 80–120 MPa range, but the machine hydraulic pressure setting is not a material constant and must be derived from the tool’s flow-length-to-wall-thickness ratio, gate type, and hot-runner pressure drop. Holding pressure is typically set at 50–70% of peak injection pressure and decayed over the gate-seal time; premature release of holding pressure before gate freeze produces sink marks and dimensional variation. Screw recovery speed of 0.15–0.30 m/s and backpressure of 5–10 bar hydraulic are conventional starting points for filled screw recovery without excessive shear heating. Because the material is non-hygroscopic in normal warehouse environments, forced-air drying is not required at relative humidity below 60%; surface condensation should be removed by hopper drying at 60 °C for 1 h only where cold pellets have been exposed to humid ambient air. Sustained melt temperatures above 250 °C may degrade the stabilizer package and generate carbonyl by-products; hot-runner manifold temperature should not exceed 240 °C in direct contact zones to avoid gate drool and visible yellowing. Multi-cavity tools with hot-runner valve gates benefit from the 6.0 g/10 min flow, but open hot tips may show stringing if nozzle temperature is too high.
Determination of food-contact status begins with the base polymer architecture. The polyolefin class is covered by 21 CFR 177.1520 for contact with food, subject to extraction limits and the conditions of use specified in the regulation; a finished article must be tested for total extractives and specific migration. For European Economic Area use, the grade falls under the framework of Regulation (EU) No 10/2011 on plastic materials intended to come into contact with food, but migration testing must be performed on the final article because additives, colorants, and processing history affect compliance. REACH registration is governed by Regulation (EC) No 1907/2006, and RoHS hazardous substance restrictions are assessed under Directive 2011/65/EU annex II. Manufacturers should request a valid regulatory declaration for the purchased production lot; generic datasheet statements do not substitute for change-controlled supplier documentation.
| Regulatory domain | Standard designation | Required verification |
|---|---|---|
| US food-contact base resin | 21 CFR 177.1520 | Finished article extraction testing under prescribed conditions |
| EU plastic food-contact materials | Regulation (EU) No 10/2011 | Overall migration and specific migration limits |
| REACH SVHC | Regulation (EC) No 1907/2006 | Article 33 substance declaration |
| RoHS restricted substances | Directive 2011/65/EU | Annex II screening by XRF and wet chemistry |
The separation between V0600 and lower-flow HDPE grades is most visible in the melt flow rate. A continuous extrusion blow-moulding grade may present an MFR below 0.5 g/10 min, which provides the sag resistance required for parison walls but demands higher melt temperature and pressure. The 6.0 g/10 min MFR of V0600 reduces fill pressure and improves knit-line flow in multi-cavity tools, but at the cost of lower molecular weight, lower tensile creep resistance, and lower environmental stress crack resistance than a pipe resin. Pressure-pipe products are typically formulated as bimodal PE100 resins and qualified under ISO 9080 hydrostatic strength regression with MFR values near 0.3 g/10 min; V0600 does not carry a PE100 classification and is not intended for pressurized water or gas distribution. When compared with a high-density film grade, the injection-moulding grade has a much narrower molecular weight distribution and higher flow, allowing shorter cycles but producing blown film with unacceptable bubble stability and dart impact orientation. The practical substitution error is attempting to use V0600 in large-part blow moulding or spiral-wound pipe because the density is similar; melt strength, not density, is the controlling difference. Rotational moulding grades also differ in form and additive package: they are typically supplied as powder with a different thermal stabilizer balance and are not interchangeable with pelletized injection moulding resins even if the MFR appears comparable.
Because the melt flow rate of 6.0 g/10 min reduces the tolerance for prolonged melt residence time, hot-runner manifolds should be designed with balanced thermal profiling, and start-up purging should not exceed 15 min at 230 °C. Contamination with polypropylene, PVC, or PET in regrind streams is a known cause of weld-line splitting and impact instability; separation at the granulator and validation of regrind percentages is required before production release. For food-contact applications, regrind use must follow the supplier’s specific guidance and local regulatory restrictions. The material is not recommended for direct contact with strong oxidizing acids, halogenated solvents, or aromatic hydrocarbons at elevated temperatures; environmental stress crack resistance is finite and must be verified under the specific chemical service condition. Long-term oven aging data for hot-water or outdoor UV service are not specified in the current public datasheet for this specific configuration; qualification programs should include the actual exposure cycle.