| HS Code | 246503 |
| Material Type | High Density Polyethylene (HDPE) |
| Density | 0.935 g/cm³ |
| Melt Index 190 C 2 16 Kg | 0.35 g/10 min |
| Tensile Strength At Yield | 24 MPa |
| Tensile Strength At Break | 30 MPa |
| Elongation At Break | 600% |
| Flexural Modulus | 1100 MPa |
| Vicat Softening Temperature | 126°C |
| Melting Temperature | 132°C |
| Environmental Stress Crack Resistance Escr F50 100 Igepal | 1000 h |
| Hardness Shore D | 65 |
| Brittleness Temperature | < -70°C |
| Thermal Conductivity | 0.43 W/m·K |
| Mold Shrinkage | 2.0-3.0% |
As an accredited NOVA Chemicals HDPE HB-W355-A factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | NOVA Chemicals HDPE HB-W355-A is supplied in 25 kg polyethylene-lined bags for secure handling and storage. |
| Container Loading (20′ FCL) | NOVA Chemicals HDPE HB-W355-A loaded in a 20-foot FCL, palletized bags, dry, clean, securely stowed, with compliant shipping documentation. |
| Shipping | NOVA Chemicals HDPE HB-W355-A ships as solid polyethylene resin pellets in 25 kg bags, bulk bags, or bulk truck/rail hopper cars. It is not DOT/IMDG/IATA regulated, nonhazardous. Store in a cool, dry, clean area away from ignition sources, moisture, and contaminants to preserve product quality. |
| Storage | Store NOVA Chemicals HDPE HB-W355-A in a cool, dry, well-ventilated area, preferably indoors in original sealed bags or containers. Protect from direct sunlight, moisture, heat, and ignition sources. Keep away from strong oxidizers and contaminants. Palletize and stack according to supplier limits to prevent bag damage. Maintain clean handling areas to control pellet spills. |
| Shelf Life | Shelf life is 24 months when stored in original, unopened packaging in a cool, dry, ventilated area away from direct sunlight. |
Containers for household and institutional cleaning formulations are converted from NOVA Chemicals HDPE HB-W355-A on long-stroke accumulator blow molding machines with extruder diameters from 65 mm to 120 mm and 24:1 to 30:1 L/D ratios. The grade’s nominal density of 0.955 g/cm³ (ASTM D1505) and melt index of 0.35 g/10 min (ASTM D1238, 190°C/2.16 kg) place the processing window between 180°C and 205°C on the melt thermocouple. Parison programming is set as a ten-point profile to compensate for sag in neck-to-shoulder transitions; die gap settings from 4.0 mm to 8.5 mm produce final sidewall thickness from 0.7 mm to 1.2 mm depending on bottle capacity from 500 mL to 5 L. Blow air pressure is maintained between 0.6 MPa and 0.9 MPa; mold temperatures are controlled from 15°C to 25°C with closed-loop chiller circuits to avoid differential shrinkage at handle pinch weld zones.
Compliance under Regulation (EC) No 648/2004 on detergents and REACH Annex XVII restricts specific substances, but the HDPE substrate is qualified by contact condition testing per ASTM D543 with representative cleaning agents: sodium hypochlorite at 5% active chlorine, quaternary ammonium chloride at 10%, ethanolamine at 15%, and linear alkylbenzene sulfonate at 20%. Stress crack resistance is assessed per ASTM D2561, with a typical qualification target of no field-equivalent failure after 30 days of constant strain exposure at 50°C. Terminal articles include trigger spray bottles, 750 mL dish soap bottles, 1 L bleach bottles, and 5 L concentrated cleaner jerrycans with 28/410 and 38/400 neck finishes.
In automotive aftermarket fluid packaging, the same HDPE grade is used for motor oil, antifreeze/coolant, and windshield washer fluid containers where combined requirements of ESCR and low-temperature drop impact govern material selection. The converter typically operates shuttle blow molding machines with 90 mm to 110 mm extruders and accumulator heads; melt temperatures are held at 185°C to 200°C, while mold temperatures remain between 10°C and 20°C to shorten cycle time without inducing excessive frozen-in stress in pinch-off seams. Motor oil fill temperatures up to 60°C require the bottle to maintain dimensional stability; formulations with high detergent additives are known stress crack agents, so ESCR evaluation follows ASTM D1693 Method B with 100% Igepal CO-630 at 50°C. For antifreeze, qualification includes immersion in 50% ethylene glycol/water at 50°C for 14 days per ASTM D543, with weight gain and tensile retention recorded against an unexposed control. Drop impact at -18°C is assessed per ASTM D2463; 5 L filled bottles are typically expected to survive 1.8 m impact without leaking. Terminal articles include 1-quart oil bottles with 38 mm closures, 5-quart containers with handle pinch, 4 L coolant bottles, and 1 L washer fluid bottles.
| Application class | Melt temperature (°C) | Mold temperature (°C) | Blow air pressure (MPa) | Typical minimum sidewall (mm) |
|---|---|---|---|---|
| Household chemical | 180–205 | 15–25 | 0.6–0.9 | 0.7 |
| Automotive fluid | 185–200 | 10–20 | 0.7–1.0 | 0.8 |
| Agricultural pesticide | 185–200 | 12–20 | 0.7–1.0 | 0.9 |
| Personal care | 180–190 | 20–30 | 0.5–0.7 | 0.6 |
| Industrial sanitizer | 180–195 | 12–20 | 0.7–1.0 | 1.6 |
Agricultural crop protection formulations impose a different set of constraints because the bottle must survive distribution as a UN-certified dangerous goods package. For a 5 L or 10 L HDPE jerrican, UN Model Regulations Chapter 6.1 classification such as UN 3H1/Y for liquids with specific gravity up to 1.8 is obtained only after the specific packaging design passes leakproofness at 30 kPa, hydraulic pressure at 250 kPa for 30 min, and drop tests corresponding to packing group II, including -18°C drops onto a steel impact plate. Wall thickness distribution is biased by parison programming so that bottom chine and handle pinch zones reach 1.8 mm to 2.4 mm; sidewall sections can be as low as 0.9 mm if top-load retention above 500 N at 40°C is not required. For emulsifiable concentrate formulations containing xylene, C9 aromatic solvent, or cyclohexanone, in-line fluorination at fluorine gas concentrations of 0.1% to 1.0% in nitrogen is used to reduce permeation and paneling. Excessive surface oxidation can reduce impact resistance, so qualification by ASTM D2463 at -18°C is mandatory after fluorination. Carbon black masterbatch added at 2.0 wt% to 2.5 wt% maintains ultraviolet stabilization; dispersion below 10 µm agglomerate size is verified by film scanning. Terminal products include 1 L hand sprayer bottles, 5 L F-style jugs with 63 mm closures, and 10 L multi-trip refillable containers.
For high-gloss personal care and topical pharmaceutical intermediate containers, HB-W355-A is processed at lower melt temperatures and with polished mold surfaces to reduce surface defects. The formulation often contains 2 wt% to 4 wt% of a white masterbatch based on titanium dioxide to achieve opacity; the masterbatch carrier must be a HDPE-compatible LLDPE or LDPE with melt index between 1 g/10 min and 5 g/10 min to prevent optical gel formation. Cosmetic product contact assessment follows Regulation (EC) No 1223/2009 and REACH Annex XVII; for pharmaceutical intermediate packaging, extractables testing according to USP 661.1 and Ph. Eur. 3.2.2 is required to establish organic extractable levels below specified thresholds. Extrusion blow molding on shuttle machines with 70 mm to 90 mm extruders is preferred for 200 mL to 1 L bottles; mold temperature is held at 20°C to 30°C to improve gloss, and blow pressure is 0.5 MPa to 0.7 MPa. Pinch weld flash may be recycled only if it has been dried to less than 0.05% moisture; wet regrind from post-consumer sources is not accepted. Terminal products include 250 mL shampoo bottles, 500 mL body wash bottles, and 750 mL lotion bottles with snap hinge closures.
| Segment | Regulatory framework | Material qualification method | Typical acceptance criterion |
|---|---|---|---|
| Household chemical | Regulation (EC) No 648/2004; REACH Annex XVII | ASTM D543, ASTM D2561 | No stress crack failure at 30 days/50°C |
| Automotive fluid | No dangerous goods classification for lube oil; OEM release standards | ASTM D1693, ASTM D2463 | ESCR retained after coolant contact; no leakage at -18°C drop |
| Agricultural pesticide | UN Model Regulations Chapter 6.1; ADR/RID | UN drop test, hydrostatic pressure | Packaging group II at 1.8 specific gravity |
| Personal care/pharmaceutical intermediate | Regulation (EC) No 1223/2009; USP 661.1; Ph. Eur. 3.2.2 | Extractables profiling | Below USP monograph thresholds |
| Industrial sanitizer | REACH; CLP for hypochlorite mixtures | ASTM D543, ASTM D2463 | Tensile retention above 80% after 7 days/23°C |
| Recycled-content coextrusion | EU Packaging and Packaging Waste Directive 94/62/EC; REACH Article 31 | Layer thickness by IR; drop impact | 85%–95% of virgin drop impact retention |
Sodium hypochlorite attack on unstabilized polyethylene proceeds through free radical oxidation, chain scission, and eventual stress crack propagation, particularly at pinch-off seams and handle roots. The compatibility boundary for HB-W355-A in industrial water treatment is therefore defined by free chlorine concentration, temperature, and exposure duration rather than short-term tensile retention alone. Immersion testing per ASTM D543 at 23°C for 7 days in 5.25% NaOCl typically shows tensile yield retention above 80%; at 12.5% active chlorine and 40°C, the same property can fall below 70% and drop impact per ASTM D2463 at -18°C becomes the controlling failure mode. To extend service life, the container wall is thickened in the lower body and base corners to at least 1.6 mm; parison programming at the bottom pinch is biased to 2.0 mm. Continuous shuttle blow molding lines with 80 mm to 100 mm extruders operate at melt temperatures 180°C to 195°C; higher temperatures increase die swell and improve knit line strength but reduce output stability due to lower melt strength. Hydrogen peroxide above 30% and nitric acid above 20% are not recommended for unlined HB-W355-A containers; fluorinated or polyamide barrier layers are required if mixed oxidizers or low pH acids coexist. Terminal articles include 10 L translucent water treatment carboys, 20 L sodium hypochlorite jerricans, and 5 L peracetic acid sanitizer containers.
Three-layer coextrusion blow molding is used to incorporate post-consumer recycled HDPE without sacrificing the ESCR and drop impact of the virgin surface layers. In a typical A-B-A structure for a 750 mL household cleaner bottle, layer distribution is controlled at 20/60/20 by volumetric screw feed and verified by infrared layer thickness measurement; some converters move to 15/70/15 when the PCR rheology is stable within ±15% of virgin HB-W355-A melt index. The PCR core is processed at 175°C to 185°C, while virgin skins run at 190°C to 205°C to reduce degradation of post-consumer stabilizer packages. EU Packaging and Packaging Waste Directive 94/62/EC and REACH Article 31 require communication of recycled content; the PCR layer must meet REACH SVHC exclusion thresholds if the finished article is placed on the EU market. Drop impact retention after 30 wt% PCR in the core is observed to remain within 85% to 95% of virgin bottle values when the PCR melt flow index is held between 0.2 g/10 min and 0.7 g/10 min, based on converter qualification trials; published data for narrower layer-ratio configurations is limited. Terminal products include household cleaning bottles with 35 wt% PCR, laundry care bottles with 50 wt% PCR in the core, and automotive lubricant bottles with A-B-A shell and carbon black core.
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NOVA Chemicals HDPE HB-W355-A is a pelletised high-density polyethylene extrusion blow moulding resin. The grade is supplied for large-part blow moulding where low melt index, high melt strength, and environmental stress cracking resistance govern tool design and part service. Nominal published values include a density of 0.955 g/cm³ and a melt index of 0.35 g/10 min at 190°C/2.16 kg when tested according to ASTM D1238 or ISO 1133-1:2022. The molecular architecture is controlled to provide high melt elasticity, which separates the grade from general-purpose HDPE resins used in continuous extrusion blow moulding of thin-walled containers.
Because a single-point melt index value does not capture the shear-thinning response required for parison control, the grade is best characterised by the following set of nominal values from published NOVA Chemicals documentation. The values are lot-average data, not contractual specification limits. The test methods listed are the applicable standards for this resin class.
| Property | Nominal value | Test method |
|---|---|---|
| Density | 0.955 g/cm³ | ASTM D1505 / ISO 1183-1:2019 |
| Melt index | 0.35 g/10 min | ASTM D1238 / ISO 1133-1:2022 at 190°C/2.16 kg |
| Flexural modulus | 1,300 MPa | ASTM D790 / ISO 178:2019 |
| Tensile strength at yield | 28 MPa | ASTM D638 / ISO 527-2:2012 |
| Elongation at break | >600% | ASTM D638 |
| Environmental stress cracking resistance | >1,000 h F50 | ASTM D1693 Condition B, 100% Igepal CO-630 |
| Vicat softening temperature | 126°C | ASTM D1525 / ISO 306 |
| Brittleness temperature | <-75°C | ASTM D746 |
| Hardness | 64 Shore D | ASTM D2240 |
The density of 0.955 g/cm³ places the grade in the high-density range, providing greater top-load strength and lower permeation than medium-density resins. The melt index of 0.35 g/10 min is intentionally low; this raises melt viscosity and reduces flow under standard conditions, but the broad molecular weight distribution compensates by generating strong shear thinning during extrusion. The tensile yield strength of 28 MPa and flexural modulus of 1,300 MPa define the short-term stiffness envelope, while the elongation at break above 600% indicates ductile failure behaviour rather than brittle fracture. The environmental stress cracking resistance under ASTM D1693 Condition B exceeds 1,000 h in 100% Igepal CO-630, which is material to containers holding surfactant-based liquids or agricultural chemicals. The Vicat softening point of 126°C and brittleness temperature below -75°C describe the thermal limits for short-term deflection and low-temperature impact.
Between a conventional unimodal 0.35 g/10 min HDPE and HB-W355-A, the main difference is the breadth of the molecular weight distribution. In a standard unimodal resin, the high-molecular-weight fraction is smaller, so the zero-shear viscosity and shear-thinning response are lower. HB-W355-A exhibits stronger shear thinning under extrusion conditions; the apparent viscosity at low shear is high enough to resist parison sag, while at die-lip shear rates the viscosity is low enough to permit screw recovery and mould filling. This distinction cannot be inferred from melt index alone because ASTM D1238 measures only a single low-shear condition. The practical consequence is that HB-W355-A transfers onto large accumulator-head tools with less parison draw-down and more uniform wall thickness. The trade-off is that die swell is greater, and die gap adjustments must be recalculated for the same nominal wall thickness.
Compared with a higher-melt-index blow moulding resin such as 0.7 g/10 min, HB-W355-A is not suited to small, thin-walled bottles because the higher viscosity limits cooling-limited output and can reduce parison surface definition at low melt temperature. Conversely, compared with a lower-density blow moulding copolymer, the 0.955 g/cm³ density of HB-W355-A improves stiffness and barrier behaviour but reduces ESCR relative to a lower-density ethylene copolymer of similar melt index. The grade is therefore selected when the part requires high melt strength, thick walls, and a balance of stiffness and crack resistance rather than maximum ESCR or minimum cycle time.
On a shuttle blow moulder with 80 mm accumulator head and 24:1 L/D screw, HB-W355-A is processed with barrel zones set from 180°C to 210°C, die temperature 200°C to 220°C, and mould temperature 10°C to 30°C. The head tooling typically uses diverging die geometry to compensate for high die swell. Screw cooling may be required if melt temperature exceeds 220°C due to shear heating. HDPE is not hygroscopic; drying is unnecessary unless surface moisture from condensation is present, in which case a 60°C hopper dryer for 2 h removes surface water. Blow air pressure between 0.6 MPa and 0.8 MPa is typical for thick-section parts. For walls above 6 mm, extended blow time is required to allow crystallisation and to reduce post-mould shrinkage.
In large-part blow moulding, parison length and melt viscosity impose conflicting demands. At a shot mass exceeding 5 kg, the parison must support its own weight during transfer from the die to the mould. The low melt index of 0.35 g/10 min reduces sag, but it also reduces flow into the accumulator head. An 80 mm extruder with 24:1 L/D and barrier screw provides acceptable recovery for shot sizes up to approximately 10 L. Above that, larger extruder diameter or reduced cycle time may be required. Die swell is typically higher than a unimodal HDPE; for a 5 mm nominal wall part, the die gap may be reduced by 15–30% depending on head pressure and melt temperature. Operators should map parison length and diameter across a range of die gap and melt temperature settings before production because the relationship is nonlinear.
Production-scale failure modes observed on accumulator-head lines include fold-over pinch-off defects when the melt temperature exceeds 220°C, incomplete flash removal when the melt is too cold, and uneven wall thickness from parison sag if the mould transfer time is extended. If the melt temperature is held above 220°C for more than 10 min residence time, chain scission can reduce molecular weight and cause a measurable loss in ESCR. Process monitoring should therefore include melt temperature at the die, screw speed, shot size, and parison hang length rather than barrel set-points alone.
For aggressive liquid packaging, environmental stress cracking resistance is a critical performance boundary. The grade maintains F50 above 1,000 h under ASTM D1693 Condition B in 100% Igepal CO-630; however, this is an accelerated laboratory test and does not guarantee compatibility with all formulations. Surfactant-based agricultural chemicals, aliphatic hydrocarbons, and oxygenated solvents may plasticise or swell the resin. Pre-qualification should include storage at 60°C with the packaged liquid and measured top-load retention after exposure. Strong oxidising agents such as concentrated hydrogen peroxide should be avoided or specifically tested. Ultraviolet exposure embrittles HDPE unless adequate carbon black or UV stabiliser is compounded into the part; unpigmented natural resin should not be used outdoors for extended service without stabilisation.
Regulatory documentation for HB-W355-A is application-specific; the base polymer class may fall under several jurisdictions. HDPE in this density class is often assessed under FDA 21 CFR 177.1520 for food-contact applications, but a grade-specific determination is required. Under EU No 10/2011, migration testing is conducted on the finished article, not the resin alone. The resin is not formulated with heavy-metal pigments; RoHS compliance for cadmium, lead, mercury, chromium VI, PBB and PBDE should be confirmed against the lot-specific certificate. REACH obligations for substances of very high concern are not triggered by the base polymer, but imported formulations may require registration documentation.
| Regulatory or standard dimension | Reference | Required verification |
|---|---|---|
| Food-contact base polymer | FDA 21 CFR 177.1520 | Confirm grade-specific paragraph and conditions of use |
| EU food-contact article testing | EU No 10/2011 | Overall migration and specific migration tests on finished article |
| Heavy-metal restrictions | RoHS 2011/65/EU | Supplier certificate for Pb, Cd, Hg, Cr(VI), PBB, PBDE |
| European chemical regulation | REACH 1907/2006 | Confirm registration dossier and SVHC content below 0.1% |
| Material specification | ASTM D4976-12a | Grade designation and property compliance against buyer specification |
Industrial drums, agricultural chemical tanks, and intermediate bulk container liners are among the thick-walled blow moulding applications for which HB-W355-A has been evaluated. For drum applications, drop testing is conducted under ASTM D2463-15 or equivalent UN/DOT transport requirements, and top-load compression resistance is measured under ASTM D2659-16. The high ESCR of the grade is directly relevant to these applications, particularly where the filling liquid contains wetting agents or minor solvents. In automotive fuel tank components, permeation resistance at the finished-part level depends on wall thickness, fluorination, or barrier technologies; published data for this specific configuration is limited, and motor fuel service requires end-use permeability testing rather than resin-level data alone.