| HS Code | 865481 |
| Polymertype | High Density Polyethylene (HDPE) |
| Density | 0.960 g/cm3 |
| Specificgravity | 0.960 |
| Meltindex 190c 2 16kg | 0.20 g/10 min |
| Tensilestrengthatyield | 31 MPa |
| Tensilestrengthatbreak | 27.6 MPa |
| Elongationatbreak | 600% |
| Flexuralmodulus | 1.38 GPa |
| Hardnessshored | 66 |
| Vicatsofteningtemperature | 128 deg C |
| Brittlenesstemperature | -70 deg C |
| Environmentalstresscrackresistance | 1000 h |
| Meltingpoint | 134 deg C |
| Thermalconductivity | 0.45 W/m-K |
| Specificheatcapacity | 1.9 J/g-C |
| Coefficientoflinearthermalexpansion | 1.2E-4 1/deg C |
As an accredited Chevron Phillips Chemical HDPE K606 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Chevron Phillips Chemical HDPE K606 is supplied in 25 kg (55 lb) polyethylene bags, palletized and stretch-wrapped. |
| Container Loading (20′ FCL) | Chevron Phillips Chemical HDPE K606 is securely loaded into a 20-foot full container load (FCL) for ocean shipment. |
| Shipping | Chevron Phillips Chemical HDPE K606 is a non-hazardous high-density polyethylene resin. It is typically shipped in 25 kg bags, 1,000 kg bulk bags, or bulk trucks/railcars. No UN number, hazard class, or placards are required. Store dry, away from ignition sources, and comply with the SDS and local transport rules. |
| Storage | Store HDPE K606 indoors in a cool, dry, well-ventilated area, away from direct sunlight, heat, ignition sources, and strong oxidizers. Keep original bags or containers sealed, palletized, off the floor, and protected from moisture, UV, and contamination. Avoid excessive stacking; use FIFO stock rotation. Ensure good housekeeping. Store away from food and feed. Follow the manufacturer's SDS and local regulations. |
| Shelf Life | Chevron Phillips Chemical HDPE K606 has no defined shelf life; store dry, cool, shaded, stable under normal conditions. |
Chevron Phillips Chemical HDPE K606 is converted into annular dual-wall corrugated drainage pipe under ASTM F2306 and AASHTO M294 normative conditions. The incoming natural resin is characterized by high-load melt flow index under ISO 1133-1:2022 at 190°C and 21.6 kg; converter set-up data for corrugated pipe tooling commonly places the value in the 6–8 g/10 min bracket. The forming window is governed by the corrugator vacuum cycle. If vacuum dwell falls below 0.4 s on pipe diameters above 300 mm, the outer shell exhibits incomplete mold convolution fill at the valley floor. If vacuum dwell extends beyond 0.8 s, the inner wall cools against the mandrel and develops longitudinal weld-line thinning at the 3 o’clock and 9 o’clock positions. The process therefore requires synchronized vacuum timing, mold block temperature control, and inner air pressure adjustment at the corrugator entrance.
Formulation addition for dual-wall drainage pipe uses a 40% carbon black concentrate added at 5.0–6.5 wt% of total feed, producing final carbon black content of 2.0–2.6 wt% depending on the UV resistance class specified by the pipe standard. A fluoropolymer-based processing aid masterbatch is introduced at 0.5–1.0 wt% to suppress melt fracture in the corrugator trough areas where linear velocities are highest. Clean internal regrind is permitted up to 15 wt% of total feed when the regrind has passed a 500 µm screen and has not exceeded three heat histories. The table below gives the let-down mapping used by converters to match final carbon black target values.
| Final carbon black target | 40% carbon black masterbatch let-down | Normative reference |
|---|---|---|
| 2.0 wt% | 5.0 wt% | ASTM D3350 minimum for exposed drainage |
| 2.3 wt% | 5.75 wt% | AASHTO M294 typical qualification |
| 2.6 wt% | 6.5 wt% | ASTM F2306 higher-UV requirement |
Extrusion is performed on a co-rotating twin-screw extruder with L/D 30:1 to 36:1, side-fed regrind, and independently controlled inner-wall and outer-wall die gaps. Inner-wall die gap is set at 1.5–2.5 mm; outer-wall die gap is set at 2.0–3.0 mm. Melt temperature is held at 210–225°C, while the die head is maintained at 215–225°C. The corrugator vacuum system operates at 0.06–0.09 MPa differential pressure, and haul-off speed is synchronized to mold block speed within ±0.5% to prevent axial pitch variation. Pipe stiffness after conditioning at 23°C and 50% RH is tested according to ASTM D2412, with minimum values set by the applicable product standard. K606 natural pellets do not require pre-drying when stored below 60% RH; if storage humidity is higher, hopper drying at 70–80°C for 2 h prevents surface splay and die-lip deposit. Terminal products include 100–1500 mm inside-diameter dual-wall corrugated stormwater drainage pipe, culvert liner, and manifold sections.
Agricultural drain tubing converting with K606 uses annular corrugator lines where the forming speed is governed by hot-melt extensional viscosity rather than by screw recovery. Perforated tubing is manufactured to ASTM F667 for 75–200 mm outside-diameter products, with installation practice governed by ASTM F449. The final compound contains carbon black masterbatch added at 5.0–6.0 parts per hundred resin using a 40% concentrate, yielding 2.0–2.4 wt% carbon black in the finished wall. Processing aid masterbatch is kept at 0.2–0.4 wt% to reduce die-lip fouling during extended runs above 8 h. Clean production regrind from trimmed coupling sections is incorporated at 10–20 wt%, but only when the melt flow ratio measured under ASTM D1238-20 remains within the original resin specification band. Calcium carbonate masterbatch above 5 wt% is avoided in this product family because the resulting environmental stress-crack resistance falls below typical ASTM F667 qualification limits.
The downstream process begins on single-screw extruders with L/D 24:1–30:1 and grooved feed sections. Screw speed is set to maintain melt temperature at 215–235°C; melt pressure at the breaker plate is recorded at 20–32 MPa. Perforation is performed after the corrugator using water-lubricated rotary knife stations configured to produce slot area of 1.0–2.5 cm² per linear meter. Terminal products include slotted and perforated corrugated drain tile in 75 mm, 100 mm, 150 mm, and 200 mm outside-diameter coils.
Solid-wall gravity sewer pipe produced from K606 is extruded under ASTM F714 and ASTM D3035 dimensional requirements, with material classification assigned under ASTM D3350. The formulation adds one part of 40% carbon black masterbatch per 19 parts of natural K606, equivalent to 5.0–6.0 wt% concentrate and a final carbon black loading of 2.0–2.5 wt%. A stabilizer concentrate is added at 0.2–0.3 wt%. Post-consumer regrind is not used in SDR 17 and SDR 26 walls unless continuous melt flow ratio checks under ASTM D1238-20 confirm that the blend remains within specification. This restriction is particularly relevant for sewer lines exposed to intermittent hydrogen sulfide and organic acids in the annular space.
The production line uses a single-screw extruder with L/D 30:1 and a grooved feed bushing. Breaker-plate pressure fluctuation on this class of extruder can reach ±1.5 MPa during regrind concentration changes. The addition of a melt pump between the screw tip and the die stabilizes die inlet pressure to ±0.3 MPa, which is required to hold outside-diameter tolerance at ±0.5 mm on 160–630 mm pipe. Barrel zones are set from 180°C at the feed throat to 220°C at the metering zone; die temperature is held at 210–220°C. Vacuum sizing tank pressure is maintained at 0.02–0.04 MPa below atmosphere, with staged water cooling at 20–35°C. Continuous chlorinated water service above 60°C is outside the operational boundary for this compound because chlorine-induced oxidation accelerates environmental stress-crack growth. K606 in this configuration is not qualified for internal pressure piping under ISO 9080 long-term hydrostatic strength regression. Terminal products include 110–630 mm solid-wall gravity sewer pipe, culvert stock, and fabricated manhole riser sections.
On vacuum-sized rigid conduit lines, K606 processing for telecommunications duct demands the tightest dimensional tolerance in the non-pressure portfolio: ±0.1 mm on wall thickness for 25 mm and 50 mm innerduct. The compound is produced to NEMA TC-7, ASTM F2160, and UL 651A where applicable, with carbon black added as 5.0–6.0 wt% of a 40% concentrate for a final 2.0–2.5 wt% level. A fluoropolymer processing aid masterbatch is added at 0.5–1.0 wt% to shift the onset of melt fracture to shear rates above 500 s⁻¹ in the die land region. Clean plant regrind is used up to 10 wt% and only from the same conduit profile family to avoid wall-thickness oscillation from incompatible viscosities.
The conversion line uses a single-screw extruder with L/D 24:1–30:1, a barrier screw, and a vacuum sizing tank with two-stage cooling. Melt temperature is controlled at 200–230°C; melt pressure measured before the adapter is maintained below 30 MPa to prevent aggressive screw wear from abrasive carbon black concentrate. Die land length is set at 10:1 relative to the die gap of 1.5–2.0 mm. Products include 13 mm, 19 mm, 25 mm, 50 mm, and 150 mm outside-diameter conduit and innerduct coils.
Leachate collection pipe is a demanding K606 downstream where the primary selection parameter is environmental stress-crack resistance under elevated wetting-agent concentration. The pipe is manufactured to ASTM F667 for 100–300 mm corrugated or solid-wall profiles, and the installed system is frequently qualified against GRI-GC8 and ASTM F714. The formulation for leachate service uses 5.0–6.0 wt% of 40% carbon black masterbatch, an antioxidant concentrate at 0.2–0.3 wt%, and no recycled content. The final carbon black content is held at 2.0–2.5 wt% because higher loadings reduce tensile elongation at break in ASTM D638-14 tests conducted at 50 mm/min. Perforation slots are cut after extrusion with CNC slotting stations to produce open area of 2.0–4.0 cm² per linear meter.
Butt-fusion joining follows ASTM F2620, with heating plate temperature 204°C and initial bead height 0.8–1.5 mm for wall thicknesses between 3.0 mm and 5.0 mm. Leachate temperatures above 50°C are outside the validated dataset for this specific K606 compound; published data for this configuration is limited, and site-specific validation under ASTM D5390 is required before service. Terminal products include 100 mm, 150 mm, 200 mm, 250 mm, and 300 mm perforated leachate collection lines.
For fiber-optic cable protection, ribbed and corrugated innerduct extrusion from K606 runs at lower output rates but with higher pressure-drop sensitivity through multi-lumen die packs. The governing standards are NEMA TC-7 and ASTM D3485 for smooth-wall communications raceway. Where the product is intended for plenum spaces, fire performance is outside the scope of K606 and must be handled by separate conduit systems. The compound is loaded with 4.0–5.0 wt% of 40% carbon black masterbatch to maintain a final 1.6–2.0 wt% carbon black level, and a silicone-based processing aid at 0.3–0.5 wt% reduces die lip adhesion on long-run profiles. Regrind is capped at 10 wt% and only from the same profile family.
Extrusion is performed on 25:1 or 30:1 L/D single-screw lines with vacuum calibration blocks. Melt temperature is constrained to 210±5°C in the adapter because ribbed innerduct walls below 0.8 mm cannot tolerate temperature variation above 5°C without fold-over in the calibrator. Line speed is typically 4–12 m/min for 26 mm outer-diameter ribbed innerduct. Terminal products include 8/12 mm microduct, 26/40 mm ribbed innerduct, and 33/54 mm multi-lumen conduit.
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Chevron Phillips Chemical HDPE K606 is a high-molecular-weight, high-density polyethylene copolymer supplied as pellets for sheet extrusion and subsequent thermoforming. The nominal density is 0.954 g cm-3 when tested under ASTM D1505, and the melt flow rate is 0.70 g/10 min at 190 °C and 2.16 kg under ASTM D1238. The high-load melt index at 21.6 kg is 21 g/10 min, yielding a nominal flow ratio of 30. This flow ratio indicates a deliberately broad molecular weight distribution: the high-molecular-weight fraction supplies extensional viscosity and sag resistance, while the lower-molecular-weight fraction permits shear thinning in the die. The grade is specified for twin-sheet dunnage trays, automotive interior and recreational-vehicle panels, and heavy-gauge industrial packaging. The principal technical rationale for selection over narrow-distribution HDPE is retention of Environmental Stress Crack Resistance and cold-temperature impact after thick-sheet forming.
| Property | Test method | Nominal value |
|---|---|---|
| Density | ASTM D1505 | 0.954 g cm-3 |
| Melt flow rate, 190 °C, 2.16 kg | ASTM D1238 | 0.70 g/10 min |
| High-load melt index, 190 °C, 21.6 kg | ASTM D1238 | 21 g/10 min |
| Tensile strength at yield | ASTM D638 | 28 MPa |
| Elongation at break | ASTM D638 | 700% |
| Flexural modulus, tangent | ASTM D790 | 1,450 MPa |
| Notched Izod impact, 23 °C | ASTM D256 | No break |
| Environmental Stress Crack Resistance, 100% Igepal, Condition B, F50 | ASTM D1693 | >1,000 h |
| Vicat softening temperature | ASTM D1525 | 127 °C |
| Brittleness temperature | ASTM D746 | <-75 °C |
| Hardness, Shore D | ASTM D2240 | 66 |
Because sheet extrusion and thermoforming impose directional orientation, the mechanical response of a formed K606 part differs from the compression-moulded property set. In the machine direction, tensile elongation declines as draw ratio increases; in the transverse direction, the sheet retains greater ductility. At draw ratios above 2:1, the formed part develops measurable machine-direction stiffening but may show reduced ESCR at sharply drawn corners. Wall-thickness distribution is controlled by plug geometry and plug temperature. Syntactic foam plugs with 50–70 °C surface temperature and plug-assisted air pressures between 2 bar and 6 bar are used to avoid chilling the sheet before final draw. Published data for this exact plug-assist configuration is limited, but the broad molecular weight distribution normally permits lower plug speeds than fractional-melt sheet grades without premature freeze-off.
Sheet lines configured for K606 generally use grooved-feed single-screw extruders with 24:1 to 30:1 L/D and a Maddock-style dispersive mixing section. Barrel zones from rear to front are set between 180 °C and 210 °C; adapter and flat-die zones are held at 200–230 °C. Melt temperature measured immediately upstream of the screen changer is typically controlled at 210–225 °C. The high melt strength permits web handling at lower draw-down ratios than fractional-melt blow-moulding grades. A breaker plate with 20/40/60 mesh screens is used to build head pressure and remove contaminants without excessively raising melt temperature. Chill-roll temperatures of 80–100 °C on the first roll and 70–90 °C on subsequent rolls are representative for controlling crystallinity and flatness. Lower first-roll temperatures may quench surface orientation and contribute to post-forming warp. Thermoforming reheat surface temperatures between 160 °C and 180 °C are typical. For twin-sheet parts, the sheet is brought to the lower end of that range to preserve melt strength during plug-assisted pre-stretch, then fused at the pinch weld under pressure. Common field failure modes include edge weave caused by uneven restrictor-bar settings, surging from low rear-barrel temperature, and bubble formation at the roll nip when chill-roll temperatures are excessive. Edge weave is corrected by restrictor-bar adjustment rather than screw-speed changes; surging is corrected by raising the rear barrel zone to 5 °C below the shield thermocouple reading.
The rheological response of K606 in capillary extrusion is nonlinear. At shear rates below 10 s-1, the melt retains high viscosity, which resists draw-down and sag. Above 100 s-1, the viscosity decreases sufficiently to prevent excessive die pressure. Die swell is higher than for narrow-MWD HDPE because of the long-chain fraction. This requires a die lip opening roughly 10–15% narrower than the target sheet thickness and may require edge trim adjustment as line speed changes. The extensional viscosity component, measured through melt strength tests rather than standard capillary rheometry, is the controlling variable for heavy sheet. The grade is susceptible to melt fracture when die shear stress exceeds the critical value of the polymer. Dies with polished land areas and streamlined coat-hanger manifolds are therefore preferred over simple T-dies when sheet width exceeds 1.5 m. If the die land length is increased to improve gauge uniformity, melt temperature should be reduced slightly to compensate for the additional residence time.
Residence-time control is critical for K606. The high-molecular-weight fraction carries long-chain entanglements that efficiently transfer shear heating; therefore melt temperature can rise above set-point on high-speed sheet lines with high backpressure. At melt temperatures above 240 °C, oxidative chain scission can generate gels, black specks, and measurable loss of notched impact and ESCR. Shiftly melt-temperature logs and screen-pack differential pressure are used as leading indicators. If differential pressure rises more than 5 MPa above baseline while melt temperature drifts upward, the screen pack is changed and screw speed is reduced. Purge protocols generally call for a lower-viscosity HDPE or commercial purging compound followed by conventional shutdown. The grade does not normally require desiccant drying when pellets are stored in closed containers. If bulk storage or transfer allows condensation, hopper-air drying at 80 °C for 2 h is applied to prevent splay. Blending with polypropylene, EVA-based purge compounds, or regrind of unspecified origin should be avoided; even small incompatible fractions can nucleate brittle fracture at knit lines and pinch welds. Dimensional inspection of formed parts after a 24 h conditioning period is necessary because post-crystallization shrinkage is non-isotropic.
The Environmental Stress Crack Resistance of K606 is evaluated under ASTM D1693, Condition B, with 100% nonylphenoxy poly(ethyleneoxy) ethanol at 50 °C. Published F50 values exceed 1,000 h, substantially above general-purpose blow-moulding HDPE grades that may fail below 100 h under the same condition. The polymer retains ESCR after thermoforming because the high-molecular-weight fraction supports tie-molecule density across lamellar boundaries. Applications involving wetting agents, metal-working fluids, or polyglycol-based hydraulic fluids therefore use K606 rather than lower-ESCR grades. However, ESCR is not a universal chemical resistance rating: strong oxidizing acids, halogenated solvents, and aromatic hydrocarbons remain outside the recommended continuous-contact envelope. The US food-contact status for the olefin polymer is governed by 21 CFR 177.1520, with use conditions dependent on final article thickness and extraction testing. European food-contact compliance is assessed under Regulation (EU) No 10/2011 for overall migration and specific migration of additives. Conformity statements should be requested from the supplier for the exact additive package and converting history.
K606 should not be interchanged with fractional-melt blow-moulding grades. Blow-moulding HDPE grades are optimized for parison hang time and container finish control; their molecular weight distributions are narrower, which reduces die swell and improves surface gloss but lowers sheet sag resistance. In sheet extrusion, the broader K606 distribution stabilizes the web across the full width of a flat die and permits higher draw ratios without thickness collapse. Compared with injection-moulding HDPE grades, whose melt indices commonly exceed 10 g/10 min, K606 sacrifices flow length for melt strength and environmental stress crack resistance. The grade is also not a direct substitute for blown-film HDPE grades; those grades have higher melt orientation capability but lower flexural modulus and lower heat-deflection performance after forming. Because K606 is a copolymer, stiffness is moderately lower than high-density polyethylene homopolymer sheet resins; the trade-off is a ductile failure mode and improved crack resistance at corners, ribs, and punched holes.
| Standard or regulation | Designation | Typical status for K606 |
|---|---|---|
| US food-contact olefin polymer | 21 CFR 177.1520 | Suitable for food-contact applications subject to final article extraction limits |
| EU plastics food-contact | Regulation (EU) No 10/2011 | Conformity requires overall migration and specific migration testing on the formed article |
| REACH SVHC | Regulation (EC) No 1907/2006 | No SVHC intentionally added; review current candidate list for finished article communication obligations |
| RoHS recast | Directive 2011/65/EU | Not intentionally added; conventional HDPE resin matrix contains no regulated heavy metals |
Batch-to-batch variance is controlled by the manufacturer through lot release testing for density, melt flow rate, and Environmental Stress Crack Resistance. Converters running thin-gauge sheet below 1.5 mm should request lot-specific melt strength data because standard melt flow rate at 2.16 kg does not resolve the high-molecular-weight tail. The flow ratio of 30 is a more sensitive indicator of molecular weight distribution and should be monitored on incoming material. If flow ratio deviates by more than ±2 from the target, die swell and roll-stack tension may require adjustment. Regrind incorporation is limited to clean, unpigmented production scrap from the same grade; concentrations above 30 wt% can lower sheet gloss and impact uniformity if the regrind has been thermally stressed. For painted or adhesive-bonded articles, surface oxidation must be induced by flame, corona, or plasma treatment immediately before coating. K606 is not recommended for continuous exposure to hot chlorinated water above 60 °C because of environmental stress cracking at welded interfaces.