| HS Code | 350678 |
| Product Name | PetroChina Dushanzi HDPE T60-800 |
| Manufacturer | PetroChina Dushanzi Petrochemical Company |
| Polymer Type | High Density Polyethylene (HDPE) |
| Grade | T60-800 |
| Application | Injection Molding |
| Melt Flow Rate Mfr 190 C 2 16 Kg | 8.0 g/10 min |
| Density | 0.960 g/cm³ |
| Tensile Strength At Yield | 28 MPa |
| Elongation At Break | 500% |
| Flexural Modulus | 1200 MPa |
| Izod Notched Impact Strength | 50 J/m |
| Vicat Softening Temperature | 125 °C |
| Heat Deflection Temperature | 75 °C |
| Hardness | Shore D 66 |
| Melting Point | 135 °C |
| Molding Shrinkage | 1.5-3.0% |
| Color | Natural |
| Form | Pellet |
As an accredited PetroChina Dushanzi HDPE T60-800 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | PetroChina Dushanzi HDPE T60-800 typically comes in 25 kg bags or 1,000 kg jumbo bags; 20 MT per container. |
| Container Loading (20′ FCL) | Container Loading (20′ FCL): PetroChina Dushanzi HDPE T60-800, 25kg bags, palletized, shrink-wrapped, securely loaded in 20-foot FCL for sea export. |
| Shipping | PetroChina Dushanzi HDPE T60-800 ships as a non-hazardous polymer, typically in 25 kg PP woven bags or 1,000 kg jumbo bags; bulk options may exist. Transport as general cargo. Keep dry, ventilated, and protected from moisture, heat, direct sunlight, and contamination. No special dangerous-goods handling required. |
| Storage | Store PetroChina Dushanzi HDPE T60-800 in a cool, dry, well-ventilated warehouse at ambient temperature, away from direct sunlight, heat, flames, and oxidizing agents. Keep original bags sealed on pallets, off the floor, preventing moisture, dust, and contamination. Use first-in, first-out stock rotation. Avoid prolonged UV exposure and excessive stacking. Maintain clean handling to preserve resin quality. Do not store outdoors. |
| Shelf Life | Typically indefinite if kept in cool, dry, ventilated storage, away from direct sunlight, moisture, and heat in original sealed packaging. |
PetroChina Dushanzi HDPE T60-800 is specified as a PE100-class bimodal high-density polyethylene with a nominal density of 0.960 g/cm³ under ISO 1183-1:2019 and an MFR at 190°C/5 kg near 0.8 g/10 min under ISO 1133-1:2022. In potable water transmission pipe extrusion, the grade is processed on a grooved-feed single-screw extruder with an L/D ratio between 30:1 and 38:1 and a barrier mixing section, with barrel zones stepping from 170°C to 205°C and the die head held at 190°C to 205°C to avoid both pellet slip and local oxidative degradation. The pipe compound for black mains is let down with a carbon black masterbatch to a final carbon black content of 2.0 wt% to 2.5 wt%, which is required for UV stabilization under ISO 4427-2:2020 and must not exceed 2.5 wt% because higher loadings reduce slow crack growth resistance measured under ISO 13479:2022. The melt is forced through a spiral-mandrel die into vacuum calibration sleeves at 15°C to 25°C water temperature; wall-thickness distribution is controlled to the tolerances of ISO 4427-2:2020 for SDR 11 and SDR 17 pressure ratings. The resulting pipe, typically from 20 mm to 630 mm outside diameter, is joined by butt fusion according to ISO 21307:2017 with heater plate surface temperatures of 200°C to 230°C and shall not be backfilled until complete cooling of the fusion bead. The finished water main is hydrostatically tested at 1.5 times the nominal operating pressure for a duration specified in the project specification; long-term strength is validated by ISO 1167-1:2006 and ISO 9080:2012 with a 50-year required strength of 10.0 MPa at 20°C.
| Application | Standard / test method | Reference criterion |
|---|---|---|
| Potable water pipe | ISO 4427-2:2020; ISO 1167-1:2006; ISO 9080:2012 | PE100 MRS 10.0 MPa at 20°C, 50-year service life |
| Gas distribution pipe | ISO 4437-2; ISO 13477:2008; ISO 13479:2022 | RCP critical pressure criterion at 0°C; SCG no brittle failure in notched pipe test |
| Geomembrane | GRI GM13; ASTM D5885-18; ASTM D5397 | HP-OIT minimum 400 min at 200°C; NCLT failure time specified per project |
| Buried cable duct | IEC 61386-24:2019 | Impact resistance and ring stiffness for buried installation |
| Blow moulded drum | UN 1H1; ADR/RID | Drop test at -18°C and hydraulic pressure test per packing group |
Rapid crack propagation in gas distribution pipe is evaluated by the ISO 13477:2008 S4 test, in which a pipe specimen of seven outside diameters is conditioned at 0°C and impacted axially under internal pressure; a PE100-grade material is acceptable when the measured critical pressure exceeds the maximum operating pressure by the margin stated in ISO 4437-2. For T60-800, the bimodal molecular architecture provides a high-molecular-weight fraction that arrests crack extension, but the arrest capacity is reduced if the melt is held above 210°C for extended residence time because oxidative chain scission attacks the longest chains first. Gas pipe is extruded in SDR 11 or SDR 17 through a spiral or basket die at 185°C to 205°C, with black or yellow outer layers containing 2.0 wt% to 2.5 wt% carbon black for black grades and cadmium-free organic pigments for yellow grades that must show no adverse effect in notched pipe slow crack growth testing under ISO 13479:2022. Field joining is by butt fusion in accordance with ISO 21307:2017, with the heating tool maintained at 200°C to 230°C and fusion pressure controlled to produce a double bead without internal restriction; electrofusion couplers require scraping of the oxide skin immediately before assembly as specified in ISO 12176-1:2012. The completed network operates at conveyance pressures up to 0.8 MPa for 20 mm to 630 mm mains, and the installed pipe is pressure-tested under ISO 4437-2 after backfilling to avoid thermally induced joint stress.
Flat-die and calendered geomembrane produced from T60-800 uses a let-down of 2.5 wt% to 3.0 wt% carbon black masterbatch to achieve a carbon black dispersion rating of A1 or A2 under ISO 18553:2002 and a final sheet density within the range 0.940 g/cm³ to 0.960 g/cm³. The resin is extruded at 195°C to 215°C through a slot die onto polished cooling rolls, yielding sheet thicknesses of 1.0 mm, 1.5 mm, 2.0 mm, or 2.5 mm with a thickness tolerance of ±10% under GRI GM13. Hot-wedge field welding is carried out at 360°C to 430°C; because the high-molecular-weight fraction increases melt viscosity and reduces flow into the weld root, the wedge speed, gap, and pressure are set to produce continuous squeeze-out along both edges of the seam. Destructive and non-destructive seam tests are performed on site: peel and shear tests follow ASTM D6392, while air-channel tests are used to detect unbonded sections. The geomembrane is specified for landfill basal and cap liners, evaporation ponds, and heap leach pads where chemical exposure is prolonged; long-term stress crack resistance is measured by ASTM D5397 notched constant tensile load testing, and quality control includes standard OIT by ASTM D3895 and high-pressure OIT by ASTM D5885-18 to confirm antioxidant retention through extrusion and welding.
The substitution of PVC by PE100-grade HDPE in buried cable ducting eliminates solvent-welded joints and allows trenchless installation by ploughing or horizontal directional drilling. T60-800 is extruded at 180°C to 200°C into solid-wall ducts of 32 mm to 160 mm outside diameter, with wall thicknesses selected for the installed depth and traffic loads under IEC 61386-24:2019. Because the duct is not pressurized, the design is governed by ring stiffness and low-temperature impact resistance; the high-density fraction raises flexural modulus for ring stiffness, and the high-molecular-weight fraction maintains impact strength at -5°C. The pipe enters vacuum calibration with water below 25°C to reduce residual stress and shall not be coiled at temperatures below 0°C. Internal lubricant is generally omitted for fibre optic microducts; if cable blowing demands a coefficient of friction below 0.15, a low-torque additive is let down at 0.1 wt% and the duct is then flushed to remove additives before cable installation. Joints use integral bell-and-spigot or push-fit couplers, and no solvent cement is permitted because it causes stress cracking in HDPE.
In extrusion blow moulding of 220-L tight-head drums, T60-800 is processed at a melt temperature of 185°C to 205°C to maintain parison sag resistance, but the screw speed and back pressure are reduced if the melt temperature falls below 180°C because surface melt fracture appears as sharkskin on the parison. The accumulator-head equipment uses a 50 mm to 120 mm barrel diameter with a shot size matched to the drum and a blow air pressure of 0.6 MPa to 0.8 MPa inside a mould cooled to 10°C to 20°C. The resin is let down with 1.5 wt% to 2.0 wt% colour masterbatch and a standard antioxidant package; no plasticizer or filler is required. The finished drum is evaluated as a UN 1H1 rigid plastics packaging for dangerous goods, which includes a drop test at -18°C from a height according to packing group and a hydraulic pressure test specified in ADR/RID; these tests require the combination of impact strength and environmental stress crack resistance available from the PE100-type high-molecular-weight HDPE. The pinch-off weld and the top chime area are inspected for thickness reduction below 2.5 mm because that region is the first to fail under transport vibration.
Because mining slurry pipelines operate under sustained abrasion from coarse tailings and low-frequency cyclic pressure surges, thick-wall T60-800 pipe is produced with an additional wear allowance of 2.0 mm to 4.0 mm beyond the pressure rating for diameters up to 315 mm. The extrusion line is configured with a grooved-feed single-screw extruder at 190°C to 205°C and a spiral-mandrel die that minimizes weld-line formation in the pipe wall; the internal surface roughness is controlled to an Ra below 3.2 µm to reduce particle impingement. Slurry pipelines are joined by butt fusion or electrofusion at above-ground installations with longitudinal restraints to accommodate thermal expansion; the operating flow velocity is held between 1.5 m/s and 3.5 m/s so that solids do not deposit and erosion of the invert is limited. The pressure rating is calculated under ISO 4427-2:2020 while the abrasion allowance is derived from a site-specific wear model such as the Miller or modified Miller correlation, and the pipe is inspected for thinning at bends where particle impingement is greatest. The grade is not recommended for slurry temperatures above 45°C because the long-term hydrostatic strength declines sharply above that threshold and the wear rate accelerates against the softened pipe wall.
Chlorine resistance in T60-800 irrigation mainlines is evaluated by accelerated immersion in sodium hypochlorite at 2.0 mg/L to 5.0 mg/L free chlorine and elevated temperature, followed by notched pipe slow crack growth testing under ISO 13479:2022. The service temperature is limited to 45°C or below for pressure pipe because higher temperatures accelerate antioxidant depletion and creep rupture. The pipe is extruded at 185°C to 200°C in SDR 17 or SDR 11 from 20 mm to 250 mm outside diameter, with a smooth internal surface to limit biofilm adhesion and a black UV-stabilized outer layer for above-ground use; if white or blue outer pigmentation is required, the pigment system must be checked for heat build-up because surface temperature above 60°C can reduce the design life. Drip and sprinkler mainlines are joined by barbed fittings at smaller diameters and butt fusion at larger diameters; the installed system is pressure-tested at 1.5 times the nominal operating pressure for 1 h. Blending with post-consumer recyclate is not permitted in chlorinated water service because non-uniform antioxidant depletion creates local brittle zones that are not detected by short-term burst testing.
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PetroChina Dushanzi HDPE T60-800 is a high-density polyethylene resin supplied by PetroChina Dushanzi Petrochemical Company for injection molding of rigid, thin-wall articles. The product is identified by a nominal density of 0.960 g/cm³ when measured according to ISO 1183-1:2019 and a melt flow rate of 8.0 g/10 min at 190 °C under 2.16 kg load according to ISO 1133-1:2022. This combination places T60-800 in the high-flow, high-density segment of the HDPE product map, distinct from low-MFR pipe extrusion grades and high-melt-strength blow-molding grades. The resin is supplied in pellet form with a density that imparts surface hardness, flexural stiffness, and chemical resistance while retaining polyethylene toughness. During injection molding, the 8.0 g/10 min melt flow rate reduces pressure loss in thin-wall cavities and permits shorter cycle times, but the product is not formulated for hydrostatic pressure pipe service, large-part blow molding, or blown film extrusion. Lot-specific certificates of analysis should be used for production release because melt flow and density are controlled within defined release windows rather than fixed singular values.
| Property | Test method | Typical value | Unit |
|---|---|---|---|
| Density | ISO 1183-1:2019 | 0.960 | g/cm³ |
| Melt flow rate, 190 °C/2.16 kg | ISO 1133-1:2022 | 8.0 | g/10 min |
| Tensile stress at yield | ISO 527-2:2012 | 28 | MPa |
| Tensile elongation at yield | ISO 527-2:2012 | 9 | % |
| Flexural modulus | ISO 178:2019 | 1300 | MPa |
| Charpy notched impact strength, 23 °C | ISO 179-1/1eA | 4.5 | kJ/m² |
| Heat deflection temperature, 0.45 MPa | ISO 75-2:2013 Method B | 75 | °C |
| Vicat softening temperature, A50 | ISO 306:2013 | 127 | °C |
The operational distinction originates in melt viscosity and molecular weight distribution. PetroChina Dushanzi HDPE T60-800 at 8.0 g/10 min under 2.16 kg load displays a substantially lower melt viscosity than PE100 pipe grades, which are commonly specified with MFR under 5 kg below 0.4 g/10 min and with bimodal molecular weight distributions to generate slow crack growth resistance. On a 120 t hydraulic injection molding machine, the lower viscosity typically reduces injection pressure by 20–30 % relative to a 2.0 g/10 min HDPE when filling the same 1.0 mm wall-thickness cap mold at a melt temperature of 220 °C. This pressure reduction allows multi-cavity tooling with smaller runner diameters and lower clamp force reserves. The trade-off is reduced melt strength: T60-800 cannot sustain large parison or sheet sag during blow molding or thermoforming. In blow molding of similar high-flow HDPE grades, parison sag becomes process-limiting at die gaps above approximately 3.0 mm; published data for this specific configuration is limited. The grade is therefore not interchangeable with 5000S-type blow-molding resins or with pipe resins in applications requiring long-term hydrostatic strength, high melt elasticity, or ASTM D2837 stress-rupture performance.
| Attribute | T60-800 | Low-flow pipe HDPE | Blow-molding HDPE |
|---|---|---|---|
| Melt flow rate | 8.0 g/10 min, 190 °C/2.16 kg | <0.1 g/10 min, 190 °C/2.16 kg; 0.2–0.4 g/10 min, 190 °C/5 kg | <0.1–0.2 g/10 min, 190 °C/2.16 kg |
| Density | 0.960 g/cm³ | 0.950–0.960 g/cm³ | 0.950–0.957 g/cm³ |
| Melt strength | Low | High | High |
| Primary processing method | Injection molding | Pipe and profile extrusion | Extrusion blow molding |
| Relative environmental stress crack resistance | Lower | High | Medium-high |
| Cycle-time orientation | Short cooling and fill time | Not cycle-time-limited in extrusion | Longer due to parison solidification |
The product also differs from linear low-density polyethylene film grades and polypropylene impact copolymers. Relative to hexene-LLDPE near 0.918 g/cm³, T60-800 has higher flexural modulus and surface hardness but lower dart drop impact, puncture resistance, and tear resistance. Relative to a polypropylene impact copolymer of comparable melt flow rate, T60-800 has lower heat deflection temperature and lower tensile modulus, but better low-temperature impact performance in the region of -20 °C. These differences position the resin where high-density polyethylene surface hardness, short cycle time, and injection moldability are more important than film toughness or high-heat dimensional stability.
Injection molding of T60-800 is compatible with standard screw L/D ratios of 20:1 to 24:1 and compression ratios of 2.0:1 to 2.5:1. A non-return valve with low leakage is required for weight-repeatable shot control. Melt temperature measured at the nozzle should be controlled between 190 °C and 230 °C; nozzle temperatures above 240 °C increase the risk of chain scission, yellowing, and oxidation product formation. Mold temperature should be maintained between 20 °C and 60 °C, with lower values favoring faster solidification but higher in-mold stress. Back pressure should be limited to 0.5–1.5 MPa; excessive back pressure or screw speed above 150 rpm can generate shear heating, which depresses melt viscosity and makes shot weight unstable. The resin does not require pre-drying when stored at ambient relative humidity below 60 %, but surface moisture should be removed at 80 °C for 2 h if condensation has occurred. The material should not be mixed with polypropylene-rich regrind above 5 wt% without a compatibilizer because dispersed polypropylene domains reduce Charpy impact and can cause delamination. Residence time above 230 °C should not exceed 10 min to avoid viscosity drift and visible surface streaking. These boundary conditions are derived from processing of high-flow 0.960 g/cm³ HDPE on production-scale machines; published data for T60-800 under every screw geometry is limited.
Processors should verify incoming lots with melt flow rate according to ISO 1133-1:2022 at 190 °C and 2.16 kg, density according to ISO 1183-1:2019 using a density gradient column at 23 °C, and pellet contamination using 40-mesh screens or film analysis. Type 1A tensile specimens should be injection molded according to ISO 294-1:2017 and tested according to ISO 527-2:2012 at 50 mm/min. Flexural modulus should be determined according to ISO 178:2019 at 2 mm/min. Charpy notched impact should be conducted according to ISO 179-1/1eA with a 0.25 mm notch radius at 23 °C. Heat deflection temperature should be measured according to ISO 75-2:2013 Method B at 0.45 MPa. These methods provide comparable values across HDPE suppliers and prevent false equivalence when melt flow is reported under different loadings. If the product is intended for food contact, converters must confirm compliance with FDA 21 CFR 177.1520 and GB 4806.7-2016 for each production lot, including total migration testing under EU Regulation (EU) No 10/2011 where relevant. No food-contact certification is implied by this technical description without supplier and converter documentation specific to the production lot.
T60-800 is specified for thin-wall containers, caps, closures, household articles, cosmetic packaging, and general-purpose injection-molded products with wall thickness in the 0.5–1.5 mm range. The 8.0 g/10 min melt flow rate permits filling of long flow paths at moderate injection pressure and fast injection velocities, typically 80–140 mm/s for wall sections of 1.0 mm. Packing pressure should generally be 60–80 % of peak injection pressure to compensate for high post-fill shrinkage, and pack time should be set to gate freeze-off time determined by short-shot sequence or pressure decay. The density of 0.960 g/cm³ gives higher modulus and surface hardness than lower-density HDPE grades, but the high-density matrix has lower environmental stress crack resistance than hexene-copolymer pipe or medium-density blow-molding grades. T60-800 should not be used for detergent bottles, fuel containers, or aggressive surfactant packaging unless ESCR testing according to ASTM D1693 or equivalent demonstrates adequate lot-specific performance. The material is not suitable for pressure pipe service under ISO 4427 design stress classification because it lacks the long-term creep rupture data and stabilizer package required for PE100 or PE80 certification. Cold runner diameters should not be less than 0.8 mm for wall thickness of 1.0 mm; smaller runners increase shear heating and may cause flow marks. Mold venting of 0.02–0.03 mm depth is required to prevent burn marks at short fill times. These boundaries define the product niche in short-cycle rigid injection molding rather than long-term load-bearing or high-parison applications.