| HS Code | 599582 |
| Density | 0.950 g/cm³ |
| Melt Index | 0.35 g/10 min (190°C/2.16 kg) |
| Tensile Strength At Yield | 26.2 MPa |
| Tensile Strength At Break | 31.0 MPa |
| Elongation At Break | 600% |
| Flexural Modulus | 1170 MPa |
| Vicat Softening Temperature | 121 °C |
| Heat Deflection Temperature | 71 °C at 0.45 MPa |
| Shore D Hardness | 65 |
| Water Absorption | 0.01% |
| Thermal Conductivity | 0.40 W/m·K |
| Coefficient Of Linear Thermal Expansion | 1.1E-4 /°C |
| Dielectric Constant | 2.3 |
| Volume Resistivity | 1E15 ohm·cm |
| Processing Temperature | 190-220 °C |
| Mold Shrinkage | 2.5% |
As an accredited LyondellBasell HDPE 50-2753 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | LyondellBasell HDPE 50-2753 is typically supplied in 25 kg bags, palletized, stretch-wrapped, and shipped on standard industrial pallets. |
| Container Loading (20′ FCL) | Standard dry 20-foot FCL loading of LyondellBasell HDPE 50-2753, securely packed in 25 kg bags on pallets for overseas export. |
| Shipping | LyondellBasell HDPE 50-2753 is a non-hazardous high-density polyethylene resin, typically shipped as pellets in 25-kg bags, bulk bags, or bulk trucks/railcars. Transport in dry, clean containers; avoid moisture, heat, and UV. Not classified as dangerous goods; follow local regulations and prevent spillage. |
| Storage | Store LyondellBasell HDPE 50-2753 in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, flames, and strong oxidizers. Keep containers tightly closed and labeled, protect from moisture, dust, and UV exposure, and avoid static buildup. Maintain good housekeeping to prevent slipping on spilled pellets. Follow manufacturer’s SDS and local regulations. Inspect containers regularly. |
| Shelf Life | Shelf life is 2 years when stored in original packaging under cool, dry conditions, away from direct sunlight and heat. |
In 5–30 L monolayer extrusion blow-moulded industrial chemical containers, 50-2753 is formulated as the primary matrix resin at 97–99 wt%, with carbon black masterbatch at 1.0–2.0 wt%, UV stabilizer masterbatch at 0.5–1.0 wt%, and a shear-managed fluoropolymer processing aid at 0.02–0.10 wt%. The grade is selected for its bimodal molecular weight distribution, a published density of 0.950 g/cm³ under ISO 1183-1:2019, a melt-flow rate of 1.0–1.3 g/10 min at 190 °C/5.0 kg under ISO 1133-1:2022, and a 100 % Igepal environmental stress crack resistance value typically above 600 h under ASTM D1693-21 F50. Processing on a single-screw extruder with a barrier screw at 24:1–30:1 L/D uses a melt temperature of 180–200 °C, die-head temperature of 170–190 °C, and an accumulator shot capacity of 1.5–3.0 kg for 10–30 L jerricans. Mould coolant is held at 8–15 °C and blow pressure at 0.5–0.7 MPa; cycle times range from 90 s for 5 L to 180 s for 30 L. Compliance is achieved through UN 3H1 certification under the UN Model Regulations Chapter 6.1 and 49 CFR 178.509, with hydrostatic, drop, and stack testing; ISO 16101:2020 is used for aggressive chemical compatibility screening. Terminal articles are UN-approved 5 L, 10 L, 20 L, and 30 L plastic jerricans for solvent, acid, alkali, and petrochemical additive transport. The defining production-scale failure mode is parison sag above 200 °C, producing lower pinch-weld wall thickness and 10–15 % loss in stack-load strength when the melt deviates by more than ±5 °C from the validated setpoint.
Across 0.5–5 L household detergent and hard-surface cleaner bottle lines, the formulation ratio is shifted to 94–97 wt% 50-2753, 2–5 wt% colour masterbatch, 0.2–0.5 wt% antistatic concentrate, and 0.05–0.15 wt% lubricant/processing aid to maintain filling-line friction within high-speed capping and labelling tolerances. Continuous shuttle extrusion blow-moulding equipment with one or two parison heads runs at a melt temperature of 170–195 °C, mould temperature of 5–10 °C, and blow pressure of 0.4–0.6 MPa; a 1 L cycle time is commonly 12–18 s. The high ESCR of 50-2753 under ASTM D1693-21 is operationally relevant because detergent surfactants, hypochlorite bleach, and nonylphenol ethoxylates attack monomodal HDPE at handle pinch-off and mould seam welds after only weeks of warehouse storage. Regulatory compliance is governed by the EU Packaging and Packaging Waste Regulation (EU) 2025/40, REACH Regulation 1907/2006 Annex XVII restricted substances, and downstream recyclability documentation under ISO 14021:2016. Batch-to-batch colour masterbatch variation in melt viscosity is controlled by monitoring screen-pack differential pressure; a rise above 0.2 MPa indicates gel accumulation and requires die-gap adjustment of 0.2–0.4 mm to maintain top-load and drop-impact margins. Terminal product types include 0.5 L, 0.75 L, 1 L, 1.5 L, 2 L, and 5 L monolayer bottles with handle pinch-weld thickness greater than 1.8 mm for laundry detergent, fabric softener, hypochlorite bleach, and all-purpose cleaner formulations.
Substitution of a monomodal HDPE with 50-2753 in 1–20 L UN-rated agrochemical containers changes parison swell, melt strength, and environmental stress crack resistance simultaneously because the bimodal molecular weight distribution increases tie molecule density without an equivalent reduction in shear thinning. Formulation addition ratio is 98–99.5 wt% 50-2753, 1.0–2.0 wt% UV-stabilized masterbatch, and 0.1–0.2 wt% antioxidant concentrate. Accumulator blow-moulding is configured with die gap 1.8–2.5 mm, parison weight 0.25–1.2 kg, melt temperature 185–205 °C, and mould cooling 8–12 °C; the higher melt temperature is used only where off-line fluorination is specified as a secondary barrier. Regulatory certification for Packing Group II/III agrochemical products is under UN 3H1 with routine hydraulic pressure testing per 49 CFR 178.509, while chemical compatibility is screened with ISO 16101:2020 and ASTM D4919-22. Terminal packs are 1 L, 5 L, 10 L, and 20 L bottles for emulsifiable concentrates, suspension concentrates, adjuvants, and water-dispersible granule refill packs. Published data for monolayer 50-2753 against high aromatic-content solvent systems are limited; products containing more than 30 % aromatic hydrocarbon carriers typically require fluorination or a coextruded polyamide barrier because monolayer HDPE permeation can exceed permissible regulatory loss rates for these formulations.
Automotive lubricant and diesel exhaust fluid (DEF) container walls require low-temperature ductility and avoidance of trace metal contamination. Formulation uses 97–99 wt% 50-2753, 1.0–2.0 wt% carbon black or grey UV masterbatch, and 0.05–0.15 wt% acid-neutralizing stabilizer. Processing on accumulator blow-moulders with multi-cavity stackable container tooling uses melt temperature 180–200 °C, die temperature 175–195 °C, blow pressure 0.55–0.75 MPa, and mould temperature 5–12 °C; cycle time for a 20 L stackable container is 45–70 s. The notched Charpy impact strength at −30 °C of 5 kJ/m² under ISO 179-1:2010 supports drop resistance after refrigerated transport and cold-chain storage. Compliance for DEF containers is anchored to ISO 22241-3:2019 for handling and storage of AUS 32, with trace metal contamination limits specified in the standard; lubricant containers shipped as dangerous goods additionally require marking and stack-load testing under 49 CFR 178.509. Terminal products are 5 L, 10 L, and 20 L containers for diesel exhaust fluid, engine lubricants, gear oils, and antifreeze/coolant. Published data for 20 L stackable DEF container top-load creep in this specific grade are limited; pilot validation under 40 °C warehouse load for 14 d is required before line qualification.
When potable water contact is required, the formulation for 10–25 L water canisters shifts to 98–100 wt% 50-2753, 0.5–1.5 wt% blue masterbatch, and 0.05–0.2 wt% antioxidant concentrate; no post-consumer recyclate is introduced. Extrusion blow-moulding uses a melt temperature of 175–195 °C, parison weight 0.4–1.8 kg, blow pressure 0.5–0.8 MPa, and mould coolant at 10–20 °C; the lower melt temperature reduces oxidative degradation and organoleptic carryover. The pinch seam must be post-trimmed and measured above 2.0 mm wall thickness at the base weld to avoid leakage after repeated drop cycles. Compliance is defined by FDA 21 CFR 177.1520, EU Regulation 10/2011 Annex I overall migration below 10 mg/dm², and, where certified, NSF/ANSI/CAN 61; processing under ISO 22000 HACCP conditions is typically imposed by brand specifications for drinking-water containers. Terminal products are 10 L, 15 L, 20 L, and 25 L still-water containers and camping canisters. Published data for the specific 50-2753 organoleptic profile after long-duration potable water storage are limited; sensory testing under EN 1622:2006 for odour and flavour is required at application validation.
Closed-loop regrind streams in 20–30 L non-food industrial container production use virgin 50-2753 at 70–80 wt%, dry high-integrity post-consumer HDPE regrind at 20–30 wt%, stabilizer masterbatch at 0.5 wt%, and processing aid at 0.05 wt%. Reclaimed material is shredded, ferrous/non-ferrous separated, and melt filtered through 100–150 mesh screens before gravimetric dosing. The extruder is a grooved-feed single-screw at 25:1 L/D, with melt temperature 175–195 °C and die temperature 170–185 °C; reduced melt strength from regrind requires lowering the parison drop rate by 5–10 % compared with virgin-only operation to control wall thickness distribution. Compliance is set by EU Packaging and Packaging Waste Regulation (EU) 2025/40 recycled content targets and ISO 14021:2016 for recycled content claims; food-contact use is excluded because trace contaminants in the PCR stream cannot be demonstrated under EU Regulation 10/2011. Terminal articles are non-food 20 L and 30 L industrial cleaner containers, de-icing fluid packs, and closed-loop transport jugs for non-regulated liquids. Published comparative data for 50-2753 with high-integrity PCR are limited; the operational limit is 30 wt% regrind because higher levels require line validation to quantify ESCR and tensile-strength shifts under ASTM D1693-21 and ISO 527-2.
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LyondellBasell HDPE 50-2753 is specified as a bimodal high-molecular-weight high-density polyethylene intended for sheet extrusion and secondary thermoforming. The melt index is 0.25–0.30 g/10 min under ASTM D1238-20 at 190 °C with a 2.16 kg load, and the solid-state density is 0.952–0.955 g/cm³ under ASTM D1505-18. The bimodal molecular weight distribution places comonomer branches predominantly in the high-molecular-weight fraction, raising the concentration of tie molecules that bridge adjacent lamellae. Under ASTM D638-14 Type IV, typical tensile yield stress is 25–28 MPa, and elongation at break exceeds 600%. Flexural modulus is reported in the range of 1,100–1,400 MPa under ASTM D790-17. Slow crack growth resistance measured under ASTM D1693 Method B in 100% Igepal CO-630 at 50 °C exceeds 600 h. These characteristics support thick sheet, industrial dunnage, recreational panels, and formed parts requiring resistance to stress cracking under sustained load.
| Property | Test standard | Typical value or range |
|---|---|---|
| Melt index | ASTM D1238-20 | 0.25–0.30 g/10 min |
| Density | ASTM D1505-18 | 0.952–0.955 g/cm³ |
| Tensile yield stress | ASTM D638-14 Type IV | 25–28 MPa |
| Tensile elongation at break | ASTM D638-14 Type IV | >600% |
| Flexural modulus | ASTM D790-17 | 1,100–1,400 MPa |
| Environmental stress crack resistance | ASTM D1693 Method B | >600 h |
| Vicat softening temperature | ASTM D1525-17e1 | 126–128 °C |
| Shore D hardness | ASTM D2240-15 | 65–68 |
On single-screw sheet lines with 30:1 L/D barrier screws and barrel diameters from 100 mm to 150 mm, the melt temperature is generally held between 204 °C and 232 °C. Barrel zones are profiled from 165–180 °C at the feed throat to 190–215 °C in the metering zone, while adaptor and die zones are maintained at 210–225 °C. The resin exhibits pronounced shear thinning, and the high-molecular-weight fraction contributes melt strength without requiring excessive melt temperature. For sheet thicknesses of 3–6 mm, a gear pump with a pressure setpoint of 50–100 bar is used to limit gauge variation to ±1.5%. The die gap is set at 1.05–1.15 times the final sheet thickness to reduce molecular orientation that disturbs chill-roll contact. At melt temperatures above 240 °C with residence times above 8 min, oxidation-induced gel formation and die-lip deposit frequency increase.
Although HDPE is not hygroscopic, surface moisture on pellets stored at relative humidity above 60% can create splay and surface pitting. When regrind ratios exceed 30 wt%, a hopper dryer at 65 °C for 1–2 h is applied. Regrind from trimmed edges should be micronized to less than 6 mm and blended offline before introduction to avoid throat bridging and feed instability.
Screen packs of 20/40/60 mesh are common in sheet extrusion of 50-2753. Melt pressure upstream of the screen pack should remain below 250 bar; pressure rise over a 72 h production run on a 120 mm extruder operating near 1,000 kg/h is observed to move from approximately 110 bar to 190 bar as gels and degraded polymer accumulate. When upstream pressure exceeds 220 bar or downstream melt temperature rises by more than 3 °C, screen replacement is required. Finer filtration such as 80/120/200 mesh lowers gel content in sheet but increases shear heating and can destabilize the melt pump inlet pressure. Melt filtration efficiency is assessed by counting visible gels greater than 0.5 mm² per square meter of extruded sheet and comparing the count with the limit of 3 gels/m² for Class A thermoformed surfaces.
Under identical ASTM D1693 Method B testing in 100% Igepal CO-630 at 50 °C, 50-2753 exhibits ESCR above 600 h. Unimodal HDPE grades with a comparable melt index and density may show considerably shorter ESCR because comonomer insertion in the high-molecular-weight fraction is not optimized. The low-molecular-weight fraction in 50-2753 permits high-shear processing without excessive motor load, while the high-molecular-weight fraction governs melt strength and slow crack growth resistance. Against linear low-density polyethylene sheet resins of similar melt index, 50-2753 has higher flexural modulus, higher Vicat softening temperature, and lower oxygen transmission rate, but lower Elmendorf tear and lower dart impact energy when measured under ASTM D1922 and ASTM D1709. Against polypropylene homopolymer sheet, 50-2753 shows lower heat deflection temperature and higher low-temperature impact resistance but lower stiffness. Selection is therefore based on the ESCR–modulus–impact balance rather than any single property.
Thermoforming of 50-2753 sheet uses surface temperatures of 160–180 °C, with the lower half of the range preferred for deep-draw parts and the upper half for sheet thicknesses above 6 mm. Mold shrinkage after demolding at 60 °C is typically 1.5–2.5% in the machine direction and 1.0–2.0% in the transverse direction. On male tools, vacuum hole diameters of 0.4–0.6 mm at 25–30 mm pitch reduce visible surface marking. Twin-sheet thermoforming requires interface surface temperatures above 190 °C and fusion pressure of 0.3–0.5 MPa for 30–60 s; the cooling fixture is held at 60–70 °C until the part surface drops below 75 °C. These conditions limit blow-out at pinch-off regions when the sheet temperature exceeds the crystalline melting point by less than 10 °C.
Interface delamination in twin-sheet parts occurs when surface contaminants or insufficient fusion temperature prevent high-molecular-weight chain interdiffusion. For 50-2753, the interface is tested by sectioning the weld area and comparing the weld yield stress with the base sheet yield stress under ASTM D638-14. A weld factor below 0.85 indicates incomplete fusion. The processing boundary is defined by a minimum sheet surface temperature of 190 °C and a maximum surface dust level of 0.1 mg/cm². Release agents containing amines or silicone oils are avoided because they migrate to the interface and reduce interdiffusion. If weld factors fall below 0.85, the sheet is re-run at 200–210 °C surface temperature with a cleaned pinch-off area. Production-scale twin-sheet lines have recorded that failure occurs preferentially at the weld flash when interface temperature is below 185 °C; raising the upper oven zone by 5–8 °C restores weld strength above 0.9.
| Regulation or standard | Test designation or reference | Typical status |
|---|---|---|
| Food-contact use | FDA 21 CFR 177.1520(c) 3.1a | May comply as an olefin polymer; supplier confirmation required |
| European food-contact | Regulation (EU) No 10/2011, Annex I | May comply; migration testing of finished part required |
| RoHS | Directive 2011/65/EU and (EU) 2015/863 | No intentionally added restricted phthalates or heavy metals |
| REACH SVHC | Regulation (EC) No 1907/2006 | No SVHC intentionally added; lot-specific confirmation required |
| California Proposition 65 | Listed substances | No intentionally added listed substances; customer evaluation required |
Material safety and processing limits require that the resin not be exposed to oxidizing media at elevated temperature or to oil-based external lubricants before thermoforming. Purging after line changes from polycarbonate or PVC should use a purging compound with a melt flow range of 0.5–2.0 g/10 min at 190 °C; residual PVC above 0.5 wt% can generate hydrogen chloride and degrade 50-2753. The maximum recommended melt residence time is 15 min; longer residence times require lowering melt temperature to below 215 °C.