| HS Code | 506672 |
| Grade | HD5420GA |
| Manufacturer | PetroChina Dushanzi Petrochemical |
| Polymertype | High-density polyethylene (HDPE) |
| Density | 0.954 g/cm³ |
| Meltflowrate | 0.20 g/10min (190°C/2.16kg) |
| Tensileyieldstrength | ≥25 MPa |
| Elongationatbreak | ≥500% |
| Flexuralmodulus | ≥1000 MPa |
| Notchedimpactstrength | ≥10 kJ/m² |
| Vicatsofteningtemperature | ≥120°C |
| Brittlenesstemperature | ≤-70°C |
| Environmentalstresscrackresistance | ≥1000 h |
| Oxidationinductiontime | ≥20 min |
| Meltingpoint | 130°C |
| Hardness | 60 Shore D |
As an accredited PetroChina Dushanzi HDPE HD5420GA factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | PetroChina Dushanzi HDPE HD5420GA is supplied in 25 kg woven bags, with 40 bags (1,000 kg) per pallet. |
| Container Loading (20′ FCL) | PetroChina Dushanzi HDPE HD5420GA loaded in 20′ FCL container: 25kg PP/PE bags, palletized, shrink-wrapped, securely stowed for export shipment. |
| Shipping | Shipped as non-hazardous polymer pellets in 25 kg bags or 1,000 kg jumbo bags, palletized and stretch-wrapped. Typically transported by truck, rail, or sea freight under normal conditions. Use clean, dry containers; avoid moisture, direct sunlight, heat, and ignition sources. Store in cool, ventilated warehouse. Not classified as dangerous goods. |
| Storage | Store PetroChina Dushanzi HDPE HD5420GA in a cool, dry, well-ventilated warehouse. Keep original bags closed, palletized, and off the floor. Protect from direct sunlight, heat, moisture, and contaminants. Keep away from ignition sources and strong oxidizers. Avoid prolonged UV exposure. Use first-in, first-out rotation and follow the SDS. Handle carefully to prevent package damage. Maintain good housekeeping. Do not smoke. |
| Shelf Life | Shelf life: typically 24 months in original unopened packaging, stored cool, dry, ventilated, away from direct sunlight. |
Dushanzi HD5420GA is a high-density polyethylene blow moulding grade supplied with a nominal density of 0.954 g/cm³ under ISO 1183-1:2019 and a melt flow rate of 0.25 g/10 min under ISO 1133-1:2022 at 190°C/2.16 kg. Supplier technical literature reports a flexural modulus near 1,100 MPa under ISO 178:2019 and tensile elongation at break above 600% under ISO 527-2:2012. The grade belongs to the high molecular weight extrusion blow moulding segment, in which parison melt strength, pinch-off weld morphology, and environmental stress cracking resistance govern the commercial conversion window. The following downstream segments are specific to industrial packaging, automotive tanks, water treatment cabinets, and barrier container structures, not to film or pipe conversion.
For a 200 L open-head drum produced on a high-speed shuttle blow moulder equipped with a 120 mm grooved-barrel extruder and a 15 kg accumulator head, the limiting conversion defect is not melt pressure but gravitational thinning of the parison before mould closure. HD5420GA is processed at a melt temperature of 190°C to 220°C; the upper limit is set by a measurable loss of parison hang time above 225°C, which produces wall-thickness deviation in the top chime and bottom corner regions. The accumulator head is operated with a die gap of 2.5 mm to 4.0 mm, and parison programming varies the gap by 20% to 35% across the drop length to keep the finished sidewall between 1.8 mm and 2.5 mm. The spiral mandrel uses 6 to 8 ports because fewer ports create visible knit lines that become impact initiation sites after drop testing. Blow air is delivered at 0.6 MPa to 0.8 MPa, and mould temperature is held at 12°C to 28°C to limit cooling time below 90 s for a 200 L body. Die swell factors of 1.25:1 to 1.35:1 are compensated by tooling diameter to maintain parison weight. The pinch-off weld is the critical mechanical zone; after deflashing, a flash thickness of 0.3 mm to 0.6 mm is the accepted range because thicker flash retains stress concentrations that reduce drop-impact performance under ISO 2248:2018. For lubricant and solvent packaging, the formulation is limited to neat HD5420GA, with a UV stabilizer masterbatch at 2.0 wt% to 2.5 wt% only when drums are stored outdoors, and carbon black masterbatch at 1.5 wt% to 2.0 wt% where UV exposure exceeds six months. Zinc stearate at 0.05 wt% is allowable as an acid scavenger; levels above 0.1 wt% are associated with lower environmental stress crack resistance in field trials. Pre-drying is unnecessary when pellet moisture is below 0.05 wt%; at silo relative humidity above 80%, surface condensation can cause splay defects and must be removed by dry-air purging at 60°C for 1 h. Compliance for dangerous goods packaging is established under the UN Manual of Tests and Criteria, ISO 2234:2018 stack-load testing, and ISO 2248:2018 drop testing. Food-contact use requires end-use migration testing under FDA 21 CFR 177.1520(c) and, where applicable, EU Regulation (EU) No 10/2011. End products include 200 L lubricant drums, 120 L open-head powder containers, and 220 L IBC inner bottles for water-based emulsions.
The following homologation test matrix applies to a 200 L tight-head or open-head drum converted from HD5420GA; conditions are adjusted to the declared packaging group.
| Test | Reference | Typical condition | Acceptance criterion |
|---|---|---|---|
| Drop impact of filled drum | ISO 2248:2018 | 1.2 m, 23°C, Packing Group II | No leak and no rupture |
| Stack load | ISO 2234:2018 | 40°C, 28 days | No rupture or leaning beyond specified deflection |
| Leakproofness | UN Manual, Part III 6.1.5.3 | 20 kPa, 5 min | No leak |
| Hydraulic pressure | UN Manual, Part III 6.1.5.5 | 100 kPa, 30 min | No leak |
| ESCR F50 | ASTM D1693-21 | 100% Igepal CO-630, 50°C | F50 > 500 h |
On a 15-tonne extrusion blow moulder producing 20 L crop-protection jerricans for aromatic solvent concentrates, HD5420GA is selected for handle pinch-off strength and surface fluorination response rather than for neat monolayer permeation resistance. The base wall is formulated with 2.0 wt% to 2.5 wt% light-stable UV absorber/hindered amine masterbatch, and 5 wt% to 10 wt% in-plant regrind is incorporated only after screening below 1.0 mm to avoid gel defects in the handle pinch. Melt temperature is held at 190°C to 205°C, and the parison drop time is 3.5 s to 4.5 s before clamp closure. Parison programming increases wall thickness at the handle zone by 30% to prevent pinch-off thinning. Online fluorination uses 0.1% to 0.2% fluorine in nitrogen introduced into the blow gas for 1.0 min to 2.0 min, producing a 10 nm to 20 nm fluorinated boundary that is widely reported to reduce xylene permeation by one to two orders of magnitude relative to untreated HDPE while leaving the bulk tensile yield strength at 26 MPa to 29 MPa under ISO 527-2:2012. The fluorination gas oxygen content is maintained below 0.1% to prevent exothermic surface degradation. The jerrican is homologated as UN 3H1 for Packing Group II liquids, requiring leakproofness at 20 kPa and hydraulic pressure at 100 kPa for 30 min. Pesticide containers in the United States must also satisfy 40 CFR Part 165 container design and residue removal requirements. The finished articles are 20 L crop-protection jerricans and 10 L solvent-based adhesive containers.
Monolayer diesel tanks in the 60 L to 120 L range for off-highway equipment and generator sets are extrusion-blow-moulded from HD5420GA because the ESCR failure time under ASTM D1693-21 at 50°C in 100% Igepal CO-630 is specified above 600 h. The mould must be designed with a pinch-off insert angle of 45° to 60° and a land length of 0.5 mm to 1.0 mm; a sharper insert produces a V-notch that fails under multi-axial impact at -40°C according to ISO 6603-2:2023, while a thicker land leaves amorphous material that can develop slow crack growth after 500 h of diesel exposure. Melt temperature is controlled at 200°C to 215°C, and the mould temperature is maintained at 8°C to 15°C for rapid solidification. Post-mould cooling fixtures hold the tank at 25°C to 35°C for 30 min to prevent warpage of the filler neck and mounting bosses. Wall thickness distribution scanning after moulding rejects tanks with more than 10% wall thinning in the bottom corners. The formulation uses 2.0 wt% to 2.5 wt% carbon black masterbatch for outdoor UV stability, and no stearamide slip additive is used because low-molecular-weight amide layers at the pinch-off interface reduce weld strength. For diesel tanks installed on non-road mobile machinery, permeation control is evaluated under 40 CFR 1060.103, and material-level fuel resistance is confirmed by volume swell testing according to ASTM D543. End products include 60 L to 120 L diesel tanks and 80 L urea/SCR tanks.
Closed-loop regrind from 200 L drums and 20 L jerricans is blended with virgin HD5420GA at 15 wt% to 30 wt% only on twin-screw compounding lines with an L/D ratio of 44:1 and a melt filter of 100 µm to 150 µm. The recycled fraction shifts the melt flow rate upward by approximately 0.05 g/10 min per 10 wt% addition and narrows the upper melt-temperature tolerance by 5°C to 8°C, so accumulator-head conversion is restricted to 190°C to 205°C to avoid flash thinning at the pinch-off. Twin-screw compounding uses a temperature profile of 180°C/200°C/210°C/215°C/215°C/210°C across the six zones. Melt filter pressure differential is monitored; a rise above 0.8 MPa triggers screen change. The blend is acceptable for non-food industrial packaging when tensile yield strength remains above 24 MPa under ISO 527-2:2012 and notched Charpy impact at 23°C remains above 20 kJ/m² under ISO 179-1:2023. Recycled content in food-contact packaging is not automatically permitted under FDA 21 CFR 177.1520; a separate suitability determination under 21 CFR 170.39 is required, including source-control documentation and migration testing with food simulants. Published comparative data for this specific HD5420GA/PCR configuration above 30 wt% addition is limited, so full end-use validation is required before commercial release. End products include 25 L to 60 L industrial tote shells, 120 L open-top waste containers, and 50 L water heater expansion vessels.
For a 100 L brine cabinet used in residential water softening, the wall must combine creep resistance under continuous 0.5 MPa internal hydrostatic pressure at 60°C with compliance to NSF/ANSI 44. HD5420GA is blown into a two-part cabinet mould with a wall thickness of 2.0 mm to 2.5 mm and a pinch-off flash thickness below 0.5 mm. The accumulator head is run at 185°C to 195°C to prevent surface flow lines that appear above 200°C when the melt front passes the cabinet ribs. The parison is programmed to increase thickness by 25% at the bottom corner to avoid thin-out at the sump area. The mould has core sections below 10°C at deep draw areas to prevent blow-outs. After trimming, the HDPE cabinet is assembled with injection-moulded polypropylene lids and elastomer seals. The formulation contains 1.5 wt% titanium dioxide masterbatch for opacity and no impact modifier, because the base grade provides Izod impact above 25 kJ/m² at 23°C under ISO 180:2019. For potable-water contact, extraction testing follows EU Regulation (EU) No 10/2011 with an overall migration limit of 10 mg/dm² and FDA 21 CFR 177.1520(c) subject to end-use hot-fill testing. The grade is not recommended for continuous hot-water pressure service above 60°C because the creep modulus declines rapidly beyond that threshold. End products include 100 L water softener brine cabinets, 40 L reverse osmosis accumulator tanks, and 60 L filter housing liners.
Sheet coextrusion and 3D blow moulding lines use HD5420GA in the regrind carrier layer of three-layer barrier containers for aggressive solvents and oxygen-sensitive liquids. The A-layer is an ethylene-vinyl alcohol copolymer with 6 mol% to 8 mol% ethylene content to retain barrier at 80% relative humidity; the B-layer is a maleic anhydride-modified polyethylene tie resin at 2 wt% to 3 wt%; and the C-layer is a 30 wt% to 50 wt% blend of HD5420GA regrind and virgin HD5420GA. The HDPE layer is processed at 200°C to 210°C with a melt pressure of 18 MPa to 22 MPa at the die, and the layer distribution is held at 10% barrier, 5% tie, and 85% HDPE regrind by volumetric pumps. The finished containers target oxygen transmission below 0.5 cm³/(m²·day·atm) at 23°C and 50% relative humidity under ASTM D3985-17. A minimum HDPE layer thickness of 0.8 mm is required at the handle pinch to avoid delamination after a 1.2 m drop test under ISO 2248:2018. Adhesive layer thickness is held at 5% of total wall; below 3%, delamination appears after 50 thermal cycles from -20°C to 60°C. End products include 5 L agrochemical barrier bottles, 10 L solvent-based ink containers, and 20 L oxygen-sensitive adhesive containers.
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PetroChina Dushanzi HDPE HD5420GA is a bimodal high-density polyethylene resin produced at the Dushanzi Petrochemical complex in Xinjiang. The grade is positioned for pressure pipe extrusion and is classified as a PE100 material under ISO 12162 based on long-term hydrostatic strength evaluation according to ISO 9080. Typical lot-release data include density by ISO 1183-1, melt mass-flow rate at 190 °C and 5 kg by ISO 1133-1, tensile yield stress by ISO 527-2, and oxidation induction time by ISO 11357-6. The nominal density is 0.954 g/cm³ and the nominal melt mass-flow rate is 0.20 g/10 min at 5 kg. These values place the grade in the low-flow, high-molar-mass segment of the HDPE slate: it is not intended for high-flow injection moulding, and it is not a low-melt-strength blow moulding grade. The molecular weight distribution is bimodal; a low-molar-mass fraction contributes shear thinning during extrusion, while a high-molar-mass fraction provides slow crack growth resistance and long-term pressure integrity. Certificates of analysis govern lot-specific properties and should be checked against the purchaser’s incoming specification before silo discharge.
Incoming inspection for pipe resin typically prioritizes density, melt flow rate, tensile yield stress, and oxidation induction time. Density is measured on compression-moulded plaques conditioned at 23 °C; the reference method is ISO 1183-1:2019. Melt mass-flow rate is determined at 190 °C under a 5 kg piston load using a melt indexer with a standardized die of 2.095 mm diameter. Tensile yield stress is reported on Type 1B or Type 5A specimens according to ISO 527-2:2012. The table below reproduces representative values from the producer’s technical data sheet; they are not batch guarantees, and sales specifications may contain minimum or maximum limits.
| Property | Standard | Value |
|---|---|---|
| Density | ISO 1183-1:2019 | 0.954 g/cm³ |
| Melt mass-flow rate, 190 °C, 5 kg | ISO 1133-1:2022 | 0.20 g/10 min |
| Tensile yield stress | ISO 527-2:2012 | 23 MPa |
| Elongation at break | ISO 527-2:2012 | >600 % |
| Flexural modulus | ISO 178:2019 | 950 MPa |
| Notched Charpy impact, -30 °C | ISO 179-1:2023 | 13 kJ/m² |
| Environmental stress-cracking resistance, F50, 100 % Igepal, 50 °C | ASTM D1693-15 | >1000 h |
| Oxidation induction time, 200 °C | ISO 11357-6:2018 | >30 min |
The 0.20 g/10 min melt mass-flow rate at 5 kg is a low-shear flow index. It cannot be used to estimate extrusion output directly because the bimodal molecular weight distribution produces pronounced shear thinning; high-molar-mass chains align under shear and lower apparent viscosity at pipe extrusion rates. Capillary rheometry at 190 °C and 210 °C on a laboratory piston rheometer shows a declining viscosity curve with shear rate, but published data for this specific configuration is limited. Pipe extrusion line output is controlled by grooved-barrel intake, screen pack resistance, die land dimensions, and melt temperature rather than by melt index alone.
HD5420GA is processed on grooved-barrel single-screw extruders with L/D ratios between 30:1 and 40:1. The grooved feed section increases solids conveying and discharge stability; screw designs with barrier flights and mixing elements are used to homogenize melt temperature. The recommended melt temperature window is 200–230 °C, with die temperatures generally 205–225 °C. At melt temperatures below 190 °C, the high-molar-mass fraction can raise melt pressure and increase the risk of melt fracture at high output. Above 240 °C, residence-time degradation becomes relevant: thermo-oxidative chain scission reduces molecular weight, lowers oxidation induction time measured by ISO 11357-6, and can generate surface roughness or gel particles. Pre-drying is not normally required when pellets are stored in dry silos below 60 % RH; wet pellets from outdoor storage or condensation on cold pellets can produce surface pitting and should be dried at 80 °C for 2–4 h before extrusion if moisture is visible. Carbon black masterbatch for black pipe is typically added at 2.0–2.5 wt% using a gravimetric side feeder; dispersion is evaluated by ISO 18553 or equivalent. Vacuum calibration and spray cooling are used to control wall dimensions and residual stress. Pipe producers must qualify welding procedures to ISO 21307 and hydrostatic pressure resistance to ISO 1167.
Production-scale trials on 75 mm and 120 mm grooved-barrel single-screw lines have shown that screw speeds above 110 rpm may produce melt temperature spikes if the barrier gap is too small; head pressure is machine-dependent and not a material property. If the line is started after an idle period, the first 10–15 min of extrudate should be discarded until melt temperature and melt pressure stabilize. Melt filtration through 60/100/60 mesh screen packs is standard for pipe lines; gels or unmelted high-molar-mass domains trapped on the screen raise pressure drop. Published data for specific pressure values is limited.
The controlling long-term failure mode in pressurized HDPE pipe is slow crack growth, initiated by surface scratches, rock impingement, or fusion weld imperfections. HD5420GA’s high-molar-mass fraction increases the time for craze fibrils to disentangle; the grade reports an environmental stress-cracking resistance F50 greater than 1000 h under ASTM D1693-15 with 100 % Igepal at 50 °C. For pipe-specific qualification, notched pipe test ISO 13479 and full-notch creep test ISO 16770 are applied; published data for HD5420GA in the full-notch creep configuration is limited, and the value should be obtained from the pipe producer’s qualification file. In potable water systems with chlorine dioxide or free chlorine residuals, standard PE100 resins can show accelerated oxidation and reduced slow crack growth resistance; the pipe manufacturer must verify the specific disinfectant concentration, temperature, and pressure regime. The grade is not a substitute for a chlorinated-water-specific polyethylene unless validated. Regrind from pipe production may be reintroduced if it is dry, clean, and limited to the producer’s specified addition level; uncontrolled addition of lower-molar-mass HDPE or degraded regrind reduces weld-line slow crack growth resistance and hydrostatic strength.
HD5420GA differs from injection moulding HDPE grades primarily in melt flow and solidification response. Thin-wall packaging and closures typically require melt mass-flow rates from 15 g/10 min to 30 g/10 min at 2.16 kg; HD5420GA has 0.20 g/10 min at 5 kg, a far lower flow index. Injection moulding this grade into thin-wall cavities would require high melt temperature, high injection speed, and high clamp force; spiral flow length at 220 °C is low, and gates can freeze before packing is complete. Blow moulding HDPE in the same density range is formulated for high melt strength and parison sag resistance; it is not necessarily formulated to pass ISO 9080 long-term hydrostatic strength classification. Unimodal HDPE pipe resins may have different shear viscosity and ESCR balance, but they do not necessarily achieve the same separation of processing and slow crack growth functions. HD5420GA’s bimodal architecture separates these functions across the molecular weight distribution, giving a PE100 classification at the nominal density of 0.954 g/cm³ without raising density to the maximum of the HDPE range. This is a meaningful distinction in design: density controls stiffness and water absorption, but excessive density can reduce slow crack growth resistance; the grade is therefore selected for pressure pipe rather than for applications requiring only high modulus.
Lot certification for HD5420GA should include density, melt flow rate, tensile yield stress, notched Charpy impact, and oxidation induction time. In-process testing should monitor melt pressure stability and melt temperature at the die; a drifting melt pressure curve may indicate screen pack plugging from gels or carbon black agglomerates. Melt filtration pressure rise at 250 °C through a 150 µm screen can be used for gel detection, but published data for this specific configuration is limited. Silos should be purged with dry air if the resin is stored for extended periods in humid climates. The resin should not be exposed to open flame or high-temperature oil; normal olefin handling precautions apply. No specific food-contact prohibition is associated with the base olefin polymer under FDA 21 CFR 177.1520, but the final pipe or fabricated article must be tested by the converter for end-use compliance.