| HS Code | 320940 |
| Density | 0.960 g/cm³ |
| Melt Flow Rate 190 C 2 16 Kg | 0.35 g/10 min |
| Tensile Strength At Yield | 26.0 MPa |
| Tensile Strength At Break | 30.0 MPa |
| Elongation At Break | ≥500% |
| Flexural Modulus | 1.10 GPa |
| Izod Impact Notched | 0.800 J/cm |
| Hardness Shore D | 66 |
| Vicat Softening Point | 124 °C |
| Brittleness Temperature | <-70.0 °C |
| Heat Deflection Temperature | 71.0 °C at 1.82 MPa |
| Environmental Stress Crack Resistance | >1000 h |
| Coefficient Of Linear Thermal Expansion | 1.20E-4 /°C |
| Thermal Conductivity | 0.450 W/m·K |
| Water Absorption | <0.010% |
| Dielectric Constant | 2.30 |
| Dielectric Strength | 20.0 kV/mm |
| Volume Resistivity | >1.00E+16 ohm·cm |
As an accredited Chevron Phillips Chemical HDPE 4600 (IPS) / 4700 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Chevron Phillips Chemical HDPE 4600 (IPS)/4700 is packaged in 25 kg (55 lb) bags, with 40 bags per pallet. |
| Container Loading (20′ FCL) | 20′ FCL: approximately 18–20 MT of Chevron Phillips HDPE 4600 (IPS)/4700, supplied in 25 kg bags, palletized or floor-loaded. |
| Shipping | Chevron Phillips Chemical HDPE 4600 (IPS)/4700 is a non-hazardous polyethylene resin. It is typically shipped in 25 kg bags, octabins, or bulk hopper cars/trucks. Store in a cool, dry, clean area away from UV and ignition sources. No special transport placards are required; follow local regulations. |
| Storage | Store Chevron Phillips Chemical HDPE 4600 (IPS)/4700 in a cool, dry, well-ventilated warehouse away from direct sunlight, heat, ignition sources, and strong oxidizers. Keep containers closed and pallets off the floor. Protect from moisture, contamination, and dust accumulation. Use grounded equipment and appropriate PPE. Follow first-in, first-out rotation, good housekeeping, and local regulations. |
| Shelf Life | Shelf life is 2 years when stored in original, unopened packaging in a cool, dry, well-ventilated area, away from direct sunlight. |
Potable water mains from Chevron Phillips Chemical HDPE 4600 (IPS) and 4700 are extruded on single-screw machines with 30:1 to 36:1 L/D and helically grooved feed bushings. Barrel temperatures are set in a reverse profile from 190 °C at the feed throat to 215 °C in the metering zone. Adapter and die zones are held at 210 °C to 230 °C. A spiral mandrel die is used for diameters above 4 inches to minimize weld-line weakness. Melt temperature at the die entry is not permitted to exceed 230 °C. Oxidation at higher temperatures produces gel particles and surface pitting in the vacuum sizing tank. Vacuum calibration is held at 0.02 MPa to 0.05 MPa. Spray cooling water is kept below 25 °C. The finished wall contains 2.0 wt% to 2.5 wt% carbon black for outdoor UV resistance. Antioxidant and acid-neutralizer masterbatches are metered at the feed throat according to the pipe producer’s NSF-listed formulation. Butt fusion joining follows ASTM F2620. Heater surface temperature is 204 °C to 232 °C. Interfacial pressure during fusion is 75 psi to 90 psi. The joint is cooled under pressure until the surface reaches 80 °C. Premature clamp release creates cold-flow orientation loss at the bead. Terminal product forms include 2-inch through 65-inch IPS mains in DR 11, DR 17, DR 21, and DR 26.
| Service Temperature | PE4710 Pressure De-rating Factor | Source |
|---|---|---|
| 23 °C (73 °F) | 1.00 | PPI TR-4 |
| 27 °C (80 °F) | 0.95 | PPI TR-4 |
| 38 °C (100 °F) | 0.78 | PPI TR-4 |
| 49 °C (120 °F) | 0.63 | PPI TR-4 |
| 60 °C (140 °F) | 0.50 | PPI TR-4 |
The material specification shifts from AWWA C906 to ASTM D2513 and 49 CFR Part 192. PE4710-class compounds enter gas service only after slow crack growth and rapid crack propagation are validated. Qualification data include the notched pipe test of ISO 13479 and the S4 full-scale test of ISO 13477. A design life of 50 years under pressure fluctuation demands that the resin exhibit no crack initiation at the inside wall below the required hoop stress. Color coding for natural gas is achieved with a black inner wall and a yellow stripe coextruded on the outer wall. The base resin is unfilled. Carbon black loading remains 2.0 wt% to 2.5 wt% for ultraviolet stabilization. Processing on the pipe line uses the same 30:1 to 36:1 single-screw extruder but die and melt temperatures are held at the lower end of 200 °C to 220 °C to reduce thermal degradation during long runs. Butt fusion operators must qualify under 49 CFR 192.285. Squeeze-off of gas service lines is permitted only with tooling that produces a cold-flow closure without cutting the pipe. Elevated-temperature operation reduces the allowable operating pressure according to PPI TR-4. At 110 °F, the de-rating factor is 0.70. At 140 °F, the factor is 0.50. Terminal products include IPS DR 9.3, DR 11, and DR 13.5 gas mains from 1/2-inch through 8-inch.
Slurry service in mining demands erosion resistance in two-phase flows. HDPE 4600 (IPS) and 4700 pipes are used in tailings discharge, dredge discharge, and mill process water because the viscoelastic response of high-density polyethylene converts impact energy into local deformation rather than crack propagation. Published data for specific erosion rates in dilute and dense slurries is limited. Abrasion loss depends on velocity, particle angularity, pH, and bed depth. The wall thickness is selected to provide both pressure capacity and a sacrificial wear allowance. Heavy-wall DR 13.5, DR 17, and DR 21 are common. Extruders use grooved feed sections and 30:1 to 36:1 L/D. Pipe producers set wall-thickness control with four-point ultrasonic gauges after calibration. Field experience on production-scale systems shows that flow velocity above 8 m/s with angular quartz particles of 2 mm to 20 mm creates rapid scouring at bend outer walls. Velocity below 1 m/s allows solids to settle and produces localised wall loss at the pipe invert. Service temperature above 60 °C triggers the same 0.50 pressure de-rating factor. Compliance for tailings lines does not normally require NSF/ANSI 61. However, material traceability under ASTM D3350 and ISO 9001 process control are retained at the extrusion plant. Terminal products include 8-inch through 42-inch tailings lines, dredge floats, and pull-through discharge sections.
In produced water service, API Spec 15LE is the controlling specification for polyethylene line pipe in oil and gas production. HDPE 4700 is selected for produced water gathering because it resists wet CO2, hydrogen sulfide, and high-chloride brines at ambient temperatures. The material is not suitable for continuous transport of aromatic hydrocarbons, gas condensate, or crude blends where the aromatic fraction exceeds the resin supplier’s published chemical resistance limit. Free gas should be separated before the pipe. Two-phase slug flow creates localised flexural fatigue at fusion joints. The pipe is extruded in IPS diameters from 2-inch through 24-inch. DR 7.3 through DR 17 are used according to operating pressure. Carbon black at 2.0 wt% to 2.5 wt% provides ultraviolet protection for surface storage. No plasticizer or process oil is present in the compound. Thermal de-rating at 60 °C applies the 0.50 factor. Continuous exposure above 80 °C is not recommended for PE4710 pressure service because the long-term hydrostatic strength falls below the typical safety factor. Joining uses ASTM F2620 butt fusion. Mechanical couplings are acceptable only with internal stiffeners. Terminal products include produced water flowlines, injection lines, and temporary frac water transfer lines.
Chemical compatibility is not generic. HDPE 4600 (IPS) and 4700 are resistant to most mineral acids, alkalis, and neutral salt solutions at ambient temperature. Weight-change and tensile-retention data are generated by immersion coupons under ASTM D543. A waste stream containing toluene, methylene chloride, or trichloroethylene above 1% by volume is sufficient to soften the pipe wall and reduce pressure capacity. Strong oxidising acids such as concentrated nitric acid attack the polymer chain and are outside the service window. Dual-containment systems use an inner carrier of HDPE 4700 and an outer containment of HDPE 4600. The annular space is monitored with pressure transducers or visual sump detection. Extrusion of the carrier pipe follows the same spiral mandrel die and vacuum calibration process. Butt fusion and electrofusion joints are made according to ASTM F2620 and the fitting manufacturer’s electrofusion protocol. Regrind in chemical service is restricted to clean, unpigmented in-house scrap from the same resin grade because contaminants create stress risers at the fusion plane. Terminal products include acid waste branch lines, scrubber blowdown lines, and containment piping in electroplating facilities.
| Application | Primary Compliance Standard | Performance Parameter |
|---|---|---|
| Potable water mains | NSF/ANSI 61, AWWA C906 | Leachability and pressure rating |
| Natural gas distribution | ASTM D2513, 49 CFR 192 | Slow crack growth, rapid crack propagation |
| Oilfield produced water | API Spec 15LE | Brine and wet CO2 resistance |
| Industrial chemical drainage | ASTM D543 | Immersion tensile retention |
| Electrical conduit | UL 651A, NEMA TC 7 | Crush resistance and impact strength |
| Wastewater force mains | ASTM F714, ASTM D3350 | Long-term hydrostatic strength |
For buried duct banks, coilable HDPE conduit made from 4600-series material is governed by UL 651A for Schedule 40 and Schedule 80 HDPE conduit and NEMA TC 7 for smooth-wall coilable conduit. The pipe is not rated for internal pressure. Wall thickness is set by crush resistance and impact strength rather than hydrostatic design. Carbon black loading is maintained at 2.0 wt% to 2.5 wt% to protect outdoor storage. Vacuum calibration is used with an internal water ring to control inside-diameter sag. Line speeds for 1-inch through 6-inch conduit range from 2 m/min to 10 m/min depending on cooling capacity and wall thickness. A production-scale failure mode in this operation is intermittent inside-diameter ovality when the pulling tape tension varies at the reel. The terminal product is supplied in reels or 20-foot sticks with factory-installed pulling tape. Fitting compatibility is verified with NEMA TC 9 connectors. In areas where the conduit may be exposed to direct sunlight for more than 12 months, UV-stabilised black compound is specified rather than coloured material.
Wastewater force mains handle intermittent flow and hydrogen sulfide gas generation in the headspace. HDPE 4700 is resistant to sulfuric acid attack caused by biological oxidation of hydrogen sulfide above the water line. This is a known failure mode for concrete and ductile iron. The pipe is extruded in DR 13.5 through DR 32.5 with a smooth interior. Butt fusion joints eliminate leakage at the bell-and-spigot interface. Air-release valves are installed at high points to prevent vacuum collapse during pump shutdown. At 20 °C, the pipe is derated only by the standard temperature factor of 1.00. At 40 °C, the pressure rating is reduced by the 0.78 factor from PPI TR-4. Compliance is tied to ASTM F714 dimensions and ASTM D3350 material classification. Some wastewater reuse agencies require NSF/ANSI 61 testing when the force main may later carry reclaimed water. Terminal products include 4-inch through 36-inch force mains, lagoon transfer lines, and sludge transfer pipes.
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The Chevron Phillips Chemical HDPE 4600 (IPS) and HDPE 4700 grades are high-density polyethylene resins within the Marlex portfolio, supplied primarily for industrial piping, pressure pipe, sheet, and geomembrane extrusion. The 4600 designation is commonly associated with iron pipe size dimensioning in North American industrial and drainage piping, while the 4700 designation is specified where a lower melt-flow index and higher long-term hydrostatic strength are required. Both grades are ethylene-hexene copolymers with controlled short-chain branching and broad molecular weight distribution; the current ASTM D3350 cell classification should be verified against the latest PPI TR-4 listing. Manufacturer-published typical values place the 4600 nominal density at 0.946 g/cm³ and melt-flow index at 0.46 g/10 min (190 °C/2.16 kg); the 4700 grade shifts nominal density to 0.947 g/cm³ and melt-flow index to approximately 0.35 g/10 min.
The lower melt-flow index of 4700 corresponds to a higher weight-average molecular weight and greater apparent viscosity under constant shear. At 190 °C and 100 s⁻¹, 4700 exhibits elevated capillary viscosity relative to 4600, which increases head pressure and reduces output per screw revolution on a grooved-feed extruder. Both resins have broadened molecular weight distribution to balance shear thinning with processability, but 4700 shows a more pronounced strain-hardening response in extensional flow. This affects die swell, wall-thickness uniformity, and the onset of sharkskin during IPS pipe extrusion. For thin-wall pipe and small-diameter tubing, the melt fracture threshold shifts to lower output rates with 4700. Table 1 summarizes manufacturer-published typical values; current lot-specific datasheets govern final specifications.
| Property | Test method | HDPE 4600 (IPS) | HDPE 4700 |
|---|---|---|---|
| Melt-flow index (190 °C/2.16 kg) | ASTM D1238-20 / ISO 1133-1:2022 | 0.46 g/10 min | 0.35 g/10 min |
| Nominal density | ASTM D1505-18 / ISO 1183-1:2019 | 0.946 g/cm³ | 0.947 g/cm³ |
| Tensile yield strength | ASTM D638-14 / ISO 527-2:2012 | 23 MPa | 22 MPa |
| Elongation at break | ASTM D638-14 | >600 % | >600 % |
| Flexural modulus | ASTM D790-17 / ISO 178:2019 | 758 MPa | 800 MPa |
| Environmental stress crack resistance F50, 100 % Igepal | ASTM D1693-15 Condition A | >1,000 h | >1,000 h |
| Brittleness temperature | ASTM D746-20 | < -75 °C | < -75 °C |
On commercial single-screw extruders with 24:1 to 30:1 L/D ratio and grooved feed sections, 4600 is typically processed with barrel zone set points of 180–200 °C, adapter temperatures of 190–205 °C, and die temperatures of 195–210 °C. Melt temperature measured at the die entry is maintained between 190 °C and 210 °C to limit thermo-oxidative degradation. A barrier screw with a mixing section and a 20/40/60 mesh screen pack increases melt homogeneity and removes contamination. A gear pump after the screen changer reduces pressure pulsation and permits wall-thickness control within ±0.05 mm on pipe diameters up to 250 mm. The die land length-to-gap ratio is held at 15:1 to 25:1 to provide sufficient backpressure and reduce sharkskin. When 4700 replaces 4600, extruder amperage and die pressure increase by approximately 10–20 % at the same screw speed, and throughput may be reduced by 5–15 % unless melt temperatures are raised within the permissible upper limit. Unstable vacuum calibration, often caused by insufficient melt strength, appears as wall-thickness oscillation in pipe diameters above 160 mm; the higher melt strength of 4700 reduces this defect but requires higher vacuum pump capacity.
In pressure service, resin selection is governed by extrapolated hydrostatic strength evaluated according to ISO 9080:2022 and ASTM D2837-21. The 4700 grade is specified in PE4710-class pipe candidates because its higher molecular weight and controlled short-chain branching improve Stage II slow crack growth resistance under sustained internal pressure. The 4600 grade remains suitable for lower-pressure industrial and gravity drainage systems where long-term hoop stress is below the resin hydrostatic design basis. Slow crack growth is assessed by the Pennsylvania edge-notch tensile test, ASTM F1473, or the notched pipe test, ISO 13479; comparative data often show 4700 exceeding the PE4710 performance threshold at longer test times than 4600. Published data for this specific configuration is limited, and pipe-grade certification must be confirmed by the pipe manufacturer against final wall thickness and service temperature.
Butt fusion joining of 4600 and 4700 pipes is performed under ASTM F2620-22 with heater plate surface temperatures of 200–225 °C. Interfacial pressure during bead-up and fusion is set to 0.15 MPa ± 0.02 MPa for standard DIPS pipe. Electrofusion fittings for these resins are processed under ISO 21307:2017 using manufacturer-specific voltage and fusion time parameters. Because 4700 has higher melt viscosity, joint cooling time after electrofusion is extended by 10–20 % relative to 4600 to avoid brittle failure at the fitting interface. Injection molding of fittings from 4700 requires melt temperatures of 190–210 °C, mold temperatures of 10–40 °C, and injection velocities sufficient to prevent flow lines at the gate; published data for this specific configuration is limited.
In sheet and geomembrane extrusion, 4600 is processed on a single-screw extruder with a flexible lip die and a three-roll polishing stack. Roll temperatures are set at 80–100 °C for sheet thicknesses from 0.5 mm to 6 mm. Drawdown between die and roll stack is minimized to avoid orientation-induced anisotropy and to retain impact strength. For geomembrane, the resin is combined with 2.0–2.5 wt% carbon black and processed at die temperatures of 200–210 °C. The 4700 grade can be used for thicker geomembranes where high environmental stress crack resistance is required, but the higher melt viscosity may reduce line speed by 5–10 %.
Both grades are supplied with a hindered phenolic/phosphite antioxidant package; oxidative induction time at 200 °C by ASTM D3895-19 typically exceeds 20 min for unweathered pellets. For outdoor pipe and geomembrane applications, carbon black loadings of 2.0–2.5 wt% are required to meet ASTM D3350-21 weathering classification C or E. Natural grades without adequate carbon black or ultraviolet stabilizer have limited outdoor service life; prolonged ultraviolet exposure causes chain scission and can reduce elongation at break below the 50 % threshold within months. Hydrostatic testing at 20 °C and 60 °C under ISO 9080:2022 establishes the lower confidence limit of hydrostatic strength; selected pipe formulations based on 4700 commonly achieve a minimum required strength of 10 MPa at 20 °C for 50 years. The 4600 grade is more commonly assigned to non-pressure or low-pressure applications where long-term creep rupture is not the controlling design criterion.
Compared with the film extrusion grade Marlex HHM 5502, 4600 exhibits lower density and higher environmental stress crack resistance, which shifts application from thin film and blow molding to pipe and sheet. The injection molding grade Marlex HXM 50100 has a melt-flow index near 10 g/10 min, far above 4600 and 4700, making it suitable for thin-wall containers but unsuitable for pipe requiring creep rupture resistance. Within the same pipe family, 4600 provides lower head pressure and higher output than 4700, while 4700 provides lower melt-flow index and improved slow crack growth resistance. Selection between 4600 and 4700 depends on pipe pressure class, minimum required strength, and extrusion line capacity.
Rapid crack propagation in pressurized HDPE pipe is evaluated with the small-scale steady-state test, ISO 13477, or the full-scale test, ISO 13478. The 4700 grade is generally expected to show a lower critical pressure than 4600 at sub-zero temperatures because of its higher molecular weight and improved fracture toughness. In buried gas distribution pipe, the critical temperature for rapid crack propagation is often specified below -10 °C; pipe formulations containing 4700 may pass at wall thicknesses greater than those possible with 4600. However, rapid crack propagation resistance is also governed by pipe diameter, wall thickness, extrusion-induced orientation, and residual stress; resin-only comparisons are insufficient for final pipe qualification. Published data for this specific configuration is limited, and full-scale testing under ISO 13478 is required.
Compliance for potable water and industrial pipe applications is evaluated at the pipe or fitting level, not the pellet alone. Table 2 lists applicable standards that are commonly referenced in material certification packages.
| Standard/regulation | Scope | Applicability |
|---|---|---|
| NSF/ANSI 61 | Drinking water system components | Requires formulation-specific and pipe-level certification |
| FDA 21 CFR 177.1520 | Olefin polymers for food contact | Applicable when sheet or geomembrane contacts food |
| ASTM D3350-21 | Polyethylene pipe and fitting materials cell classification | Verify full cell class and PPI TR-4 listing |
| AWWA C901 / C906 | PE water service and distribution pipe | Pipe listing required, not resin-only |
| ISO 9080:2022 | Plastics piping and ducting systems — hydrostatic strength regression | Required for pressure rating |
| ASTM F2620-22 | Heat fusion joining of PE pipe | Governs butt fusion parameters |
At processing temperatures above 240 °C or hold-up times exceeding 10 min at melt temperatures above 210 °C, thermo-oxidative degradation reduces oxidative induction time and long-term hydrostatic strength. Surface condensation on cold regrind should be avoided because it produces splay and microvoids at die temperatures above 210 °C; pre-drying is not normally required for virgin pellets but may be necessary for regrind exposed to >60 % RH. These resins should not be combined with pro-degradant masterbatches or amine-based additives where long-term stabilization and potable-water certification are required.