| HS Code | 409669 |
| 5000s Density | 0.954 g/cm3 |
| 5000s Meltflowrate | 0.9 g/10 min |
| 5000s Tensileyieldstrength | >=23 MPa |
| 5000s Elongationatbreak | >=500% |
| 5000s Vicatsofteningpoint | >=124 deg C |
| 5000s Brittlenesstemperature | <=-70 deg C |
| 5502 Density | 0.955 g/cm3 |
| 5502 Meltflowrate | 0.35 g/10 min |
| 5502 Tensileyieldstrength | >=24 MPa |
| 5502 Elongationatbreak | >=600% |
| 5502 Vicatsofteningpoint | >=125 deg C |
| 5502 Brittlenesstemperature | <=-70 deg C |
| 5502 Environmentalstresscrackingresistance | >=1000 h |
| 5502 Flexuralmodulus | >=1000 MPa |
| 5502 Notchedizodimpactstrength | >=20 kJ/m2 |
| 5502 Hardnessshored | 65 |
As an accredited Sinochem Quanzhou HDPE 5000S / 5502 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Sinochem Quanzhou HDPE 5000S/5502 is packed in 25 kg polyethylene-lined woven bags, 40 bags per 1,000 kg pallet. |
| Container Loading (20′ FCL) | 20′ FCL loading: 25 MT Sinochem Quanzhou HDPE 5000S/5502 in 25 kg bags, securely loaded without pallets. |
| Shipping | Sinochem Quanzhou HDPE 5000S/5502 is shipped as non-hazardous high-density polyethylene pellets, typically in 25 kg bags or 1 MT jumbo bags. Transport in clean, dry containers or trucks; keep away from moisture, heat, and prolonged UV. HS code 3901.20; standard commercial documentation applies. Not classified as dangerous goods for transport. |
| Storage | Store Sinochem Quanzhou HDPE 5000S/5502 in a cool, dry, well-ventilated warehouse, away from direct sunlight, rain, moisture, heat, and ignition sources. Keep original bags sealed, palletized, and off the floor. Avoid contact with oils, acids, alkalis, and solvents. Reseal opened packages promptly, protect from UV and mechanical damage, use FIFO, avoid excessive stacking pressure, and maintain clean, contamination-free conditions. |
| Shelf Life | Shelf life is about 24 months when stored unopened, dry, cool, well-ventilated, and protected from direct sunlight and moisture. |
In the manufacture of 200 L tight-head and open-head drums for export liquid chemicals, Sinochem Quanzhou HDPE 5502 is processed on accumulator-head extrusion blow molding lines equipped with grooved-feed single-screw extruders having screw L/D ratios from 24:1 to 30:1 and first-zone barrel cooling to prevent premature melting in the feed section. The grade is selected because its melt-flow rate near 0.35 g/10 min under ISO 1133-1:2022 condition 190°C/2.16 kg reduces parison sag at shot weights above 9 kg, which is the production-scale bottleneck for large-tool machines with 10–15 kg accumulator heads. Melt temperature is held within 190–205°C; excursions above 205°C produce gelled particles and black specks in formulations containing post-industrial regrind. Compliance for dangerous goods packaging is established under 49 CFR 178.504, IMDG Code Chapter 6.1, and ADR 6.1.3, with UN type approval requiring drop tests at −18°C, hydraulic pressure tests at 250 kPa for 30 min, and stacking tests at 40°C for 28 days; ESCR is evaluated under ASTM D1693 Condition A in 100% Igepal CO-630, not from melt index alone. The formulation is based on 100 parts by weight HDPE 5502, 2.0–3.0 parts carbon black masterbatch, 0.05–0.10 parts hindered phenolic antioxidant, and up to 25 parts cleaned in-house regrind from pinch-off, top and bottom trimmings, and rejected containers. The downstream process uses parison programming with 10–15 thickness steps, blow pressure from 0.55 MPa to 0.75 MPa, mold temperature between 10°C and 25°C, internal cooling time of 90–150 s, and post-mold cooling stations to control top-load deformation; neck and bottom wall thickness is targeted at 3.5–4.5 mm while the cylindrical sidewall is programmed to 2.0–2.5 mm. Terminal products are 200 L tight-head drums with 2-inch and 3/4-inch buttress-thread bung openings and open-head drums with removable lids secured by bolted closure rings.
Single-station shuttle blow molding machines with 80–100 mm grooved-feed extruder diameters and accumulator heads of 2.5–5.0 L shot capacity are the standard production route for 20 L and 25 L tight-head jerrycans. Compliance is validated under 49 CFR 178.504 and the UN Model Regulations Chapter 6.1.3, with design-type drop tests at 1.2 m for packing group II liquids and 1.8 m for packing group I; the −18°C drop condition exposes regrind-related weld-line embrittlement more than ambient drop testing. Formulation limits differ from drum production because jerrycan handles and side pinch-offs concentrate stress during side drops: 100 parts HDPE 5502 is combined with 15–20 parts of closed-loop regrind, 0.10–0.20 parts zinc stearate as acid scavenger, 0.15–0.25 parts HALS UV stabilizer, and 1.5–2.5 parts carbon black or dark pigment masterbatch. Regrind at 25 parts is permitted only when the regrind source is ultraviolet-stable, gel-controlled, and ground through a 4 mm screen, because oxidized regrind raises the −18°C drop failure rate at handle pinch-offs. The extrusion blow molding process runs at melt temperatures of 195–210°C, mold temperatures of 10–20°C, blow pressures of 0.60–0.80 MPa, closure torque of 4–6 N·m for PE closures, and cycle times of 60–90 s. Terminal products are UN-marked 20 L and 25 L jerrycans for solvents, paints, inks, and petroleum-based intermediates.
For non-food household chemical packaging, small-volume detergent and personal care bottles are blow molded from Sinochem Quanzhou HDPE 5000S at cycle times of 8–12 s per cavity on continuous-extrusion shuttle machines running single or double parison heads. The grade is specified because its melt-flow rate near 0.9 g/10 min under ISO 1133-1:2022 condition 190°C/2.16 kg permits lower backpressure and faster parison extrusion than high-molecular-weight 5502, while retaining sufficient die swell for neck calibration. Compliance for this non-food household chemical segment remains EU Directive 94/62/EC Annex II, which limits the sum of lead, cadmium, mercury, and hexavalent chromium in packaging to 100 ppm, and REACH (EC) No 1907/2006 Annex XVII restrictions on substances of very high concern; direct food-contact use of this grade is not specified unless a grade-specific FDA 21 CFR 177.1520 letter is supplied by the producer. Formulation uses 100 parts HDPE 5000S, 1.0–3.0 parts PE-based color masterbatch, and up to 15 parts in-line regrind; antistatic additive levels are 0.1–0.3 parts only where bottle surface resistivity below 1011 Ω is required. The process uses extruders of 55–70 mm diameter with L/D 24:1–28:1, blow pressure 0.45–0.65 MPa, mold cooling water at 8–12°C, and wall thickness for 500 mL to 5 L bottles maintained between 0.6 mm and 1.5 mm to avoid paneling in bright stock labels. Terminal products include 500 mL, 750 mL, 1 L, and 5 L bottles for detergents, liquid soaps, and personal care formulations.
Because xylene, cyclohexanone, and chlorinated solvent permeation governs container compatibility, pesticide and herbicide containers in the 250 mL to 20 L range are produced from HDPE 5502 either by in-line fluorination after blow molding or by coextrusion of an ethylene-vinyl alcohol barrier layer; solvent permeation is assessed by ASTM D2684, with the acceptable limit defined by the pesticide registrant for the active ingredient and solvent class rather than by a universal figure. The compliance framework includes the UN Model Regulations Chapter 6.1 for dangerous goods packagings, 49 CFR 178.504 for plastic jerrycans and bottles, and compatibility testing under ISO 16101 for aromatic and chlorinated solvents. The multilayer formulation allocates 100 parts HDPE 5502 across the structural layers, an ethylene-vinyl alcohol barrier layer at 3–5% of total wall thickness, tie-layer adhesive at 1–2%, color masterbatch at 2–5 parts in the outer layer, and regrind limited to 10 parts buried between virgin layers; regrind is excluded from barrier-contact surfaces to prevent microcrack paths. The process uses six-extruder coextrusion blow molding with annular die gaps of 1.0–1.8 mm, melt temperature limited to 185–210°C to avoid EVOH thermal degradation, parison programming with 8–12 steps, and blow pressure of 0.60–0.80 MPa; fluorine-treated monolayer bottles require post-mold fluorine content at the inner wall of 0.5–1.5% measured by X-ray photoelectron spectroscopy. Terminal products are 1 L, 5 L, and 20 L pesticide and herbicide containers with child-resistant closure neck finishes and induction-sealed caps.
Under sub-60% ambient humidity conditions, automotive windshield washer reservoirs and coolant overflow tanks are produced from HDPE 5502 on three-dimensional parison manipulation machines or suction blow molding machines, especially where complex undercut shapes prevent conventional tool parting. Compliance is set by OEM material specifications for ethylene glycol coolant resistance and heat aging at 100°C for 500 h, with dimensional deformation not exceeding 5%; VOC emission is evaluated according to VDA 277, and REACH Annex XVII restrictions apply to the compounded formulation. The formulation combines 100 parts HDPE 5502, 2.0 parts carbon black masterbatch, 0.15–0.30 parts hindered phenolic antioxidant, 0.05–0.10 parts nucleating agent, and up to 20 parts clean regrind; regrind use is reduced where the part is welded by hot-plate or ultrasonic methods because poor fusion at pinch-off contaminants increases burst failure under thermal cycling. The process window is melt 190–205°C, mold temperature 10–20°C, blow pressure 0.50–0.70 MPa, and ambient relative humidity maintained below 60% to prevent surface splay; pre-drying is applied at 80°C for 2 h when regrind moisture exceeds 0.15%. Terminal products include 3 L and 5 L washer bottles and coolant overflow tanks with injection-welded inlet and outlet ports.
Composite intermediate bulk container inner bottles with capacities up to 1000 L are blow molded from HDPE 5502 on large accumulator-head machines with 30–50 kg shot capacity and screw L/D ratios of 30:1 to 34:1; the primary process hazard is molten parison sag under shot masses above 25 kg, which reduces base and shoulder wall thickness unless parison programming is active. The applicable dangerous goods packaging standard is UN 31HA1/Y for composite IBCs with rigid plastics inner receptacles, evaluated under 49 CFR 178.706, IMDG Code 6.5, and ADR 6.5, with bottom lift, top lift, stacking, and hydraulic pressure tests; drop tests are replaced by equivalent handling tests under the IBC regime. Formulation uses 100 parts HDPE 5502, 2.0–3.0 parts carbon black masterbatch, 0.15–0.25 parts HALS UV stabilizer, 0.05–0.10 parts zinc stearate, and up to 20 parts internally generated regrind from rejected bottles; regrind is sieved through a 500 µm screen to remove gelled particles that would create wall inclusions under the design-type hydraulic pressure test. The process operates at melt 190–205°C, die gap 2.0–3.0 mm, parison programming with 30–50 steps to maintain base and shoulder wall thickness at 4.0–5.0 mm and sidewall at 2.0–2.5 mm, blow pressure 0.55–0.75 MPa, and internal cooling air at 5–10°C for 300–600 s. Terminal products are 1000 L blow-molded inner bottles housed in galvanized steel or composite outer cages for liquid chemicals, lubricants, and food ingredients when appropriate cage liners are specified.
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Sinochem Quanzhou HDPE 5000S and HDPE 5502 are high-density polyethylene resins supplied as spherical or lenticular pellets with a density envelope generally between 0.952 g/cm³ and 0.958 g/cm³ when measured to ISO 1183-1:2019. Melt flow rate values determined under ISO 1133-1:2022 separate the two grades, with 5000S occupying the higher-flow portion of the high-molecular-weight HDPE range and 5502 occupying the lower-flow portion. Each commercial lot is controlled against the producer’s certificate of analysis because published data for the specific Sinochem Quanzhou configuration is limited. The resins are stabilised for melt processing and are not intended for medical implant use.
The grade split arises from comonomer placement and molecular weight distribution, not from a change in polymer class. Downstream, HDPE 5000S is specified where lower melt pressure and higher line speed are required in sheet, film, and profile extrusion; HDPE 5502 is specified in blow-moulded containers where environmental stress cracking resistance and parison melt strength carry the safety-critical load. The ratio of high-load melt index to standard melt flow rate is a routine lot-release indicator because it correlates with shear thinning and parison sag in extrusion blow moulding.
The resins should be stored under dry conditions. If surface moisture exceeds 0.1 % by mass as measured by ISO 15512, pre-drying at 80 °C for 2 h to 4 h is required before extrusion or blow moulding. Silo residence time, ambient relative humidity, and regrind moisture content influence processing stability more than pellet density.
HDPE 5502 is a lower-flow, high-ESCR blow moulding resin. In technical data sheets for comparable grades in this designation class, the melt flow rate at 190 °C/5.0 kg is found in the 0.30 g/10 min to 0.50 g/10 min range, while HDPE 5000S is typically reported in the 0.80 g/10 min to 1.10 g/10 min range. The difference is material on transfer lines: sheet and cast film extruders may accept 5000S without excessive head pressure, whereas 5502 demands a high-torque extruder and a grooved feed section rated for pressures above 35 MPa at screw speeds above 60 rpm.
The molecular architecture of 5502 favours higher molecular weight tails and higher tie-chain density, which raises environmental stress cracking resistance. In an ASTM D1693-B test using 10 % linear alkylbenzene sulfonate at 50 °C, 5502-class materials commonly exceed 600 h to failure, while 5000S-class materials often fall in the 30 h to 80 h range. This is a property cliff-edge: when 5000S is substituted in aggressive surfactant or solvent-containing filled products, premature cracking can appear before the first refill cycle.
| Property | Test method | 5000S typical envelope | 5502 typical envelope | Unit |
|---|---|---|---|---|
| Density | ISO 1183-1:2019 | 0.952–0.956 g/cm³ | 0.953–0.957 g/cm³ | g/cm³ |
| Melt flow rate | ISO 1133-1:2022 | 0.80–1.10 g/10 min | 0.30–0.50 g/10 min | g/10 min |
| Tensile yield stress | ISO 527-2:2012 | 24–28 MPa | 25–29 MPa | MPa |
| Elongation at break | ISO 527-2:2012 | >600 % | >600 % | % |
| Environmental stress cracking resistance | ASTM D1693-B | 30–80 h | 600–1000 h | h |
Values in the table are class-typical technical literature ranges for these grade designations; lot release is controlled by the manufacturer’s certificate. Compared with injection-moulding HDPE grades having melt flow rates above 8 g/10 min, both 5000S and 5502 are high-viscosity materials. They should not be processed on short-barrel injection machines without a high-pressure screw; otherwise melt cushion instability and jetting can occur. The application split is therefore not a general-purpose substitution but a viscosity-driven tooling decision.
Slow crack growth resistance can also be monitored by the notched constant tensile load procedure of ASTM F2136, in which 5502-class materials are often evaluated at stress levels of 4 MPa to 6 MPa at 80 °C; failure time depends on notch depth and surfactant concentration. Compared with metallocene-catalysed HDPE grades, the 5000S and 5502 designation class exhibits broader molecular weight distribution and higher melt strength, which improves parison hang time but may reduce optical clarity and dart impact in thin film. Substitution of metallocene film grades by 5000S requires re-validation of dart drop impact to ASTM D1709 and tear resistance to ASTM D1922.
Extrusion blow moulding of 5502 on a single-station machine with a 75 mm grooved-barrel extruder and 24:1 L/D screw typically uses a barrel temperature profile from 175 °C to 200 °C. Head and accumulator temperatures are held at 190 °C to 205 °C. If melt temperature exceeds 210 °C, parison sag increases and wall-thickness control becomes erratic; below 170 °C, gel particles may remain and head pressure can exceed the tooling limit. A die gap of 0.8 mm to 1.2 mm is set according to parison weight, and final clamp force should be at least 1.5 kN per litre of container volume for articles above 5 L. Blow calibration pressure of 0.55 MPa to 0.75 MPa and mould temperatures between 10 °C and 20 °C provide repeatable cooling without stress whitening at the pinch-off seam.
In 5000S extrusion, the higher melt flow lowers head pressure and allows line speeds to be increased by 8 % to 15 % relative to a lower-flow blow moulding grade on the same screw. Sheet and cast film lines with 30:1 L/D grooved-barrel extruders and die gaps of 0.5 mm to 0.7 mm are routinely used. Die-entry melt temperature should not exceed 220 °C; edge oxidation at higher temperatures can form gels that degrade draw and seal performance.
The substitution of 5502 for 5000S in rigid chemical containment is appropriate only when the finished article is qualified against the stack-load test of ISO 12048, the drop test applicable to UN 1H1 plastic drums, and the environmental stress cracking procedure of ASTM D1693-B. Containers for aggressive liquids, cleaning formulations, and agricultural adjuvants create sustained hoop stress at the base and handle regions. The higher ESCR of 5502 is the safety-critical material property; 5000S should not be used in these applications without documented testing because its lower resistance can produce stress cracks at weld lines before the first refill cycle. For Packing Group II liquids, a drop height of 1.2 m at −18 °C is commonly applied to industrial containers.
The grade change also affects colour and additive masterbatch dilution. 5502 has a lower melt flow, so colour dispersion in a closed-loop blender requires a higher-shear mixing section or a pre-dispersed liquid colour metered into the feed throat. When recycled flash is reintroduced above 30 %, melt flow drift and black speck formation can occur if the regrind contains degraded pinch-off flash from previous runs. For 5000S film, edge trim regrind should be kept below 20 % to preserve gel count and seal strength.
Both grades are stabilised, but the compounding and pelletisation route leaves a narrow processing window. Melt temperatures above 240 °C increase oxidative degradation, measurable as a melt flow shift under ISO 1133-1:2022. Residence time at melt temperature should not exceed 15 min for 5000S and 10 min for 5502 in accumulator blow moulding; longer residence can produce melt flow shifts above 0.05 g/10 min and brown streaks at parison edges. Screw and barrel wear are monitored via puller speed and head pressure; a pressure loss of more than 10 % at constant throughput indicates feed-groove or check-ring wear. Moisture control is part of the audit because hygroscopic surface condensation at RH > 60 % can generate surface splay and pin-hole defects in blow moulded bottles.
Batch-to-batch variance in melt flow rate should be checked against the producer’s release limits, which are usually controlled within ±0.05 g/10 min for 5502 and ±0.10 g/10 min for 5000S. A shift beyond these limits can require die gap adjustment in blow moulding or back-pressure correction in extrusion. Combining 5502 with amine-based antistatic additives or certain hindered amine light stabilizer packages can prematurely change parison rheology and reduce ESCR. The operation should not use copper-based heat stabilizers or halogenated flame retardants without cleaning the line because residual degradation products can attack the screw and die. The resin is not compatible with low-density polyethylene immiscible fractions above 5 % in the same melt stream unless the screw is configured for dispersive mixing. Food-contact compliance for the finished article may be supported by FDA 21 CFR 177.1520 and Regulation (EU) No 10/2011 only when the specific grade and colourant system have been cleared by the producer and the converter validates migration limits.