| HS Code | 845589 |
| Material Type | High Density Polyethylene (HDPE) |
| Density | 0.952 g/cm³ |
| Melt Flow Rate 190 C 2 16 Kg | 0.20 g/10 min |
| Melt Flow Rate 190 C 21 6 Kg | 20 g/10 min |
| Tensile Modulus | 1100 MPa |
| Tensile Stress At Yield | 26 MPa |
| Tensile Strain At Yield | 9% |
| Tensile Stress At Break | 30 MPa |
| Elongation At Break | >600% |
| Charpy Notched Impact Strength 23 C | 20 kJ/m² |
| Charpy Notched Impact Strength 30 C | 8 kJ/m² |
| Vicat Softening Temperature A50 | 124°C |
| Melting Temperature | 132°C |
| Crystallization Temperature | 115°C |
| Thermal Conductivity | 0.40 W/m·K |
| Coefficient Of Linear Thermal Expansion | 1.5E-4 /°C |
| Water Absorption | <0.01% |
| Hardness Shore D | 62 |
| Volume Resistivity | >10¹⁴ Ω·cm |
| Dielectric Constant 1 Mhz | 2.3 |
| Dissipation Factor 1 Mhz | 0.0002 |
| Environmental Stress Cracking Resistance 10 Igepal | >1000 h |
| Oxidative Induction Time 200 C | >20 min |
| Ash Content | <0.1% |
| Moisture Content | <0.1% |
As an accredited Borealis HDPE HD22B-NNN factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Borealis HDPE HD22B-NNN is supplied in 25 kg polyethylene bags, palletized and stretch-wrapped for safe transport and storage. |
| Container Loading (20′ FCL) | Borealis HDPE HD22B-NNN loaded into a 20′ FCL: 25 kg bags, palletized, stretch-wrapped, securely stowed for export sea shipment. |
| Shipping | Borealis HDPE HD22B-NNN is a non-hazardous high-density polyethylene resin supplied as pellets. It is not regulated for transport under DOT, IMDG, IATA, or ADR. Ship in original sealed bags or octabins, keep dry, and protect from contamination, heat, and direct sunlight. No UN number, hazard class, or packing group applies. |
| Storage | Store Borealis HDPE HD22B-NNN in a clean, dry, well-ventilated warehouse at ambient temperature, away from direct sunlight, heat, ignition sources, and moisture. Keep original bags sealed and palletized off the floor. Avoid contamination, strong oxidizers, and prolonged UV exposure. Observe stacking limits, protect from physical damage, and use first-in, first-out stock rotation. No special ventilation normally required. |
| Shelf Life | Borealis HDPE HD22B-NNN shelf life: typically 24 months from production date when stored unopened, cool, dry, well-ventilated, protected from sunlight and moisture. |
Borealis HD22B-NNN is specified where extrusion blow moulding of rigid HDPE containers requires a combination of low melt index, high environmental stress-cracking resistance, and constrained parison sag. Grade selection is confirmed against melt flow behaviour measured to ISO 1133-1:2022 and density measured to ISO 1183-1:2019; the current Borealis technical datasheet remains the controlling source for property values, because the permissible regrind fraction and accumulator-head settings shift with batch melt viscosity. The scenarios below are limited to application categories in which medium- to high-molecular-weight HDPE of this type has documented industrial use: industrial chemical packagings, institutional cleaning and disinfection bottles, under-bonnet automotive reservoirs, agrochemical barrier containers, non-food recycled-content rigid packaging, and construction chemical packaging. Direct fuel contact, prolonged pharmaceutical solvent exposure, and food-contact uses are excluded where published data for HD22B-NNN is limited.
| Selected evaluation method | Standard or regulation | Application threshold used in downstream screening |
|---|---|---|
| Environmental stress-cracking resistance | ASTM D1693-21 condition B | 100 h F50 after 10 vol% Igepal immersion at 50 °C for chemical packaging |
| Melt flow behaviour | ISO 1133-1:2022 | Accumulator fill and parison sag are revalidated if the measured value shifts by ±10% against the current datasheet |
| Density | ISO 1183-1:2019 | Controls top-load performance in 20–30 L jerricans and 15–20 L pails |
| UN drop test | ADR 6.1.5.3 | PE jerricans are conditioned at -18 °C for 24 h before drop from 1.2 m |
| UN internal hydraulic pressure | ADR 6.1.5.5 | 250 kPa for 30 min |
| SVHC information for articles | REACH Article 33 | Declaration required for EU converters |
Rigid transport packagings for sodium hypochlorite 12–15 wt%, phosphoric acid 75–85 wt%, and concentrated quaternary ammonium formulations use HD22B-NNN as the monolayer structural wall because the grade must sustain the ESCR and mechanical demands of UN certification. The package is certified as 3H1 or 3H2 under the United Nations recommendations; transport compliance is demonstrated under ADR/RID 6.1.5.3 drop, 6.1.5.4 leakproofness, 6.1.5.5 internal hydraulic pressure, and 6.1.5.6 stacking. The resin is processed at 100 wt% with 0.5–1.5 wt% chemical-resistant masterbatch; in-house regrind is limited to 20–30 wt% and is excluded for Packing Group I oxidizers unless each lot passes a repeat hydraulic pressure test at 250 kPa for 30 min.
Extrusion blow moulding of 20–30 L jerricans is performed on a single-screw grooved-feed extruder with L/D 24:1–30:1, barrier screw, and 1.2–2.0 mm die gap. Melt temperature is set between 190 °C and 210 °C; blow pressure is 0.7–0.9 MPa; mould cooling water is held at 8–15 °C. Parison programming is required to maintain wall thickness from 2.0 mm at the neck and bottom chime to 1.2 mm in the body, avoiding thin-out at the handle bridge. The critical defect is pinch-off weld porosity: reducing the die gap below 1.0 mm to lower shot weight reduces weld compression and creates paths for chemical ingress. Destructive inspection of weld flash at 20× magnification and leak testing after de-flashing are mandatory. Finished product types are 10 L, 20 L, 25 L, and 30 L jerricans and 60 L drums.
Monolayer bottles for institutional disinfection and cleaning products—sodium hypochlorite 5–10 wt%, hydrogen peroxide 3–8 wt%, and quaternary ammonium compounds—require a balance of stress-crack resistance at moulded-in chime notches and rapid filling-line dimensional stability. HD22B-NNN is blended with 1.5–2.0 wt% white PE masterbatch and 0.1–0.3 wt% antistatic concentrate; the virgin fraction is maintained at or above 80 wt%, with the balance as clean in-house regrind from deflashing. Compliance includes EU Detergent Regulation (EC) No 648/2004 for the filled product, Regulation (EC) No 1272/2008 CLP for hazard classification, and Directive 94/62/EC for packaging waste. Fillers specify ESCR testing per ASTM D1693-21 to avoid field cracking. Production uses a shuttle extrusion blow moulder with 60 mm screw, L/D 26:1, and six-station clamp. Melt temperature is held between 185 °C and 200 °C; mould temperature is 10–20 °C. Bottle weight is 42–55 g for 1 L formats, with wall thickness not less than 0.7 mm in the lower chime. Finished types include 750 mL, 1 L, and 5 L bottles with 28 mm and 38 mm neck finishes for trigger spray and closure systems.
Under-bonnet washer reservoirs and coolant overflow bottles convert from standard HDPE to HD22B-NNN when heat-aging requirements exceed 150 °C dry air for 500 h and when ESCR after immersion in 50 vol% ethylene glycol/water at 70 °C must remain above 100 h under ASTM D1693-21 condition B. Compliance is driven by ELV Directive 2000/53/EC heavy-metal annexes for lead, cadmium, mercury, and hexavalent chromium; REACH SVHC declarations; and OEM impact specifications aligned with ISO 179-1:2023. The formulation is 100 wt% HD22B-NNN with 0.3–0.8 wt% heat-stabilised black masterbatch; production regrind may be introduced up to 25 wt% after three heat-aging cycles confirm no loss in weld-line elongation.
Processing is performed on a single-station or dual-station accumulator-head EBM with 70–90 mm screw, L/D 25:1, and accumulator volume of 2–5 L. Die gap is 1.5–3.0 mm; melt temperature 195–215 °C; blow pressure 0.6–0.8 MPa; cooling water 10–15 °C. Finished reservoirs of 3 L, 4 L, and 5 L nominal volume must pass leak testing at 50 kPa internal air pressure and torque retention on heat-stake inserts. A boundary condition is premature mould opening: if the part surface temperature is above 65 °C, snap-fit bosses exhibit post-mould warpage after 24 h.
Co-extrusion blow moulding of 1 L, 2.5 L, and 5 L crop-protection containers for xylene, cyclohexanone, and surfactant-containing formulations places HD22B-NNN as the structural HDPE layers in a three- to six-layer stack. The total HDPE fraction is 68–75 wt%, with 3–5 wt% maleic anhydride-grafted PE tie resin and 3–5 wt% EVOH barrier core; the balance is assigned to regrind layers only after permeation validation. Transport compliance is demonstrated under UN 3H1/Y certification and ADR 6.1.5.3 drop, 6.1.5.4 leakproofness, and 6.1.5.5 internal pressure tests. Crop-protection packaging also references Regulation (EU) No 547/2011 for label surface adhesion. Layer distribution is 25–30 wt% outer HDPE and 40–45 wt% inner HDPE; the inner skin is not replaced with post-consumer reclaim because solvent uptake can raise permeation above 0.5 g/(m²·day) when measured on 500 µm films according to ASTM F739-20 at 40 °C.
Processing is performed on a co-extrusion shuttle or wheel machine with 6–8 stations and individual layer screws. Melt temperatures are 195–210 °C for HD22B-NNN, 200–220 °C for EVOH, and 185–205 °C for tie resin through a multi-manifold die with 1.5–2.5 mm gap. The finished products include barrier bottles for emulsifiable concentrates, suspension concentrates, and aqueous solutions, typically with 38 mm and 45 mm neck finishes and induction-sealed closures. Published data for this specific configuration is limited when the solvent blend contains high fractions of methyl acetate or dimethylformamide; those formulations require separate permeation validation.
When post-consumer HDPE bales are converted into non-food rigid containers, blended formulations containing 70–85 wt% HD22B-NNN and 15–30 wt% washed PCR flake restore ESCR and parison hang strength that would otherwise be lost from recycled grades with fractional melt indices below 0.15 g/10 min. Compliance for the blend is assessed under REACH Article 33 for SVHC notification, REACH Annex XVII restrictions, and EU Directive 94/62/EC for heavy metals; where the finished container carries UN certification, each PCR batch must pass the same ADR 6.1.5.3 drop and 6.1.5.5 internal pressure tests as virgin material, and marker substances in the PCR must not exceed 100 ppm total bromine and chlorine. Compounding uses a 40:1 L/D co-rotating twin-screw extruder with vacuum degassing at -0.06 MPa and screen filtration 125–250 µm; the pelletised output is then extrusion blow moulded at 190–215 °C, with die gap adjusted 10–15% wider than virgin HD22B-NNN to compensate for higher melt viscosity. Finished product types are 5 L and 10 L non-food utility containers, waste-oil collection jugs, and internal plant storage pails; these are not intended for food-contact or aggressive oxidizer service.
Liquid admixture and waterproofing-compound containers for polycarboxylate ether superplasticizers, sodium silicate hardeners, and epoxy curing agents are specified when the filled mass exceeds 20 kg and the stacked pallet load applies sustained compression at 40 °C. In this configuration, HD22B-NNN is used at 90–95 wt% with 5–10 wt% calcium carbonate masterbatch to raise top-load rigidity while retaining pinch-off weld integrity; the masterbatch addition must be limited to this range because higher loadings reduce Izod impact below the threshold of 4 kJ/m² measured by ISO 180:2023. Compliance for the package is under CLP 1272/2008 and Directive 94/62/EC, with UN certification required only where the filled liquid is classified as corrosive or environmentally hazardous.
Production uses a continuous shuttle EBM with 80 mm screw and L/D 28:1, melt temperature 190–210 °C, die gap 2.0–3.5 mm, and mould cooling at 8–12 °C. Weld-flash removal must be completed before the pail wall cools below 50 °C to avoid notch formation at the handle slots. Finished products are 15 L and 20 L pails with handle slots and tamper-evident lid seats.
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Borealis HDPE HD22B-NNN is identified in supplier documentation as a BorPure high-density polyethylene blow moulding grade produced by the Borstar dual-reactor polymerisation process. The material is intended for rigid blow moulded containers in pharmaceutical, personal-care and food-contact packaging, where a single resin must combine moderate melt strength, high environmental stress crack resistance and consistent parison formation. The grade is supplied as a density-controlled, melt-flow-controlled resin with a bimodal molecular weight distribution; the “NNN” designation is used in commercial documentation for a natural-colour, non-migrating formulation. Published distributor literature does not present the grade as a filled or nucleated material, and its primary differentiator from conventional single-reactor HDPE is the decoupling of flow behaviour from slow crack growth resistance.
The property envelope in Table 1 is compiled from publicly available distributor literature. Values should be read as representative data, not as release criteria. Batch-specific certificates of analysis take precedence for packaging qualification.
| Property | Test method | Representative value |
|---|---|---|
| Density | ISO 1183-1:2019 | 0.955 g/cm³ |
| Melt flow rate | ISO 1133-1:2022 | 0.45 g/10 min at 190 °C and 2.16 kg |
| Flexural modulus | ISO 178:2019 | 950 MPa |
| Tensile stress at yield | ISO 527-2:2012 | 24 MPa |
| Tensile strain at break | ISO 527-2:2012 | >600 % |
| Charpy notched impact strength at 23 °C | ISO 179-1/1eA | 15 kJ/m² |
| Vicat softening temperature A/10 | ISO 306:2022 | 126 °C |
| Environmental stress crack resistance, 10 % Igepal, F50 | ASTM D1693 | >1000 h |
Batch-to-batch variation on industrial continuous extrusion lines is typically less than 5 % for melt-flow rate and density when material handling excludes contamination; however, addition of regrind beyond 10 wt% can shift rheology enough to require parison program adjustment. Incoming quality checks should include capillary rheometry at 190 °C and a 2.16 kg load on a Gottfert or equivalent instrument, with comparison against the lot certificate and retained control sample.
In aggressive liquid packaging, failure modes are often not tensile yield but environmental stress cracking under hoop stress. The high-molecular-weight fraction of a bimodal HDPE links adjacent lamellae in the semi-crystalline matrix, increasing resistance to slow crack growth. Single-reactor unimodal resins tend to sacrifice environmental stress crack resistance for melt flow, while Borstar dual-reactor polymerisation allows the low-molecular-weight fraction to depress melt viscosity during extrusion and the high-molecular-weight fraction to sustain stress-cracking resistance. Test data using ASTM D1693 with 10 % Igepal are used to rank such behaviour; a reported F50 value above 1000 h separates this grade from high-flow HDPE injection moulding resins of comparable density. The result is a processing envelope in which melt temperature and screw speed are not wholly free variables, because excessive shear heating can degrade the high-molecular-weight tail and reduce the property that the bimodal architecture is designed to provide.
On continuous shuttle and accumulator-head blow moulding lines, extruder screw designs with 24:1 to 30:1 L/D and Maddock mixing sections provide the shear profile required for high-molecular-weight polyethylene. Melt temperature is typically maintained between 185 °C and 210 °C; die head temperatures above 220 °C can reduce melt strength and promote parison draw-down. Mould temperatures of 10 °C to 20 °C are used for small pharmaceutical bottles to stabilise part dimensions. Pre-drying is not normally required for HDPE; however, condensation on pellet surfaces at relative humidity above 60 % can produce splay or surface pits. In such cases, a desiccant dryer at 70 °C for 2 h before extrusion is commonly applied.
Pharmaceutical blow moulding grades are assessed not only by mechanical properties but by migration and extractables behaviour under sterilising and filling conditions. Polyethylene grades intended for oral solid and liquid containers must meet pharmacopoeial monographs, including Ph. Eur. 3.1.3 and USP 661.1/661.2, with test conditions matched to the actual dose form. Hydrocarbon and polar extractables testing often uses ethanol-water and buffered aqueous simulants; conversion conditions such as extrusion temperature and parison oxidation can increase carbonyl species that affect taste and odour. Borealis documentation for BorPure HD22B-NNN references organoleptic suitability for pharmaceutical applications; nevertheless, final qualification requires migration testing on the actual bottle geometry and fill matrix.
Regulatory assessment for the final article is a function of the resin, additives, conversion step and contact ratio. The benchmarks in Table 2 apply to rigid polyethylene packaging; they do not replace batch-specific compliance declarations from the converter.
| Requirement | Standard or code | Typical qualification statement |
|---|---|---|
| EU food-contact plastic materials | EU 10/2011 | Overall migration limit 10 mg/dm² for standard articles; final verification depends on surface/volume ratio and fill simulant |
| US food-contact olefin polymers | FDA 21 CFR 177.1520 | Resin may be used subject to finished-article extractives and end-use limitations |
| European pharmacopoeia polyethylene monograph | Ph. Eur. 3.1.3 | Candidate compliance; release and migration testing required on the converted article |
| US pharmacopoeial packaging materials | USP 661.1 and USP 661.2 | Extractables and safety assessment depend on dose form and packaging configuration |
| Heavy metals restriction | RoHS 2011/65/EU | Candidate compliance for restricted heavy metals in homogeneous material |
| Chemical registration | REACH EC 1907/2006 | Supplier declaration required for SVHC content and registration status |
For pharmaceutical packaging, extraction studies are performed with 50 % ethanol and aqueous buffers at 40 °C or under accelerated conditions; the chosen simulant and surface-to-volume ratio must reproduce the intended use. Published data for this specific configuration is limited, so results from open literature on similar Borstar HDPE grades should not be transferred without confirmation.
Compared with unimodal HDPE blow moulding grades of similar density, HD22B-NNN shows a broader shear-thinning response and higher zero-shear viscosity. This enables thicker parisons to be programmed without excessive sag, but it also requires higher recovery time in accumulator-head machines. Compared with high-flow HDPE injection moulding grades used for caps and closures, the lower melt-flow rate of 0.45 g/10 min reduces injection moulding flow length and is not suitable for multi-cavity thin-wall injection tools. Differences from other Borealis grade families include the Borstar molecular architecture, which separates the low-molecular-weight and high-molecular-weight fractions and therefore shifts the stiffness–environmental stress crack resistance balance beyond what a unimodal resin of equal density and melt-flow rate can achieve.
At equivalent density and comonomer content, bimodal HDPE resin displays higher notched impact and environmental stress crack resistance than a single-reactor blend of similar melt-flow rate. The shift is measurable in bottle drop tests at 0 °C and -20 °C, where brittle fracture is initiated at pinhole defects. The high-molecular-weight fraction contributes tie-molecule density; the short-chain branching distribution influences lamellar thickness and diffusion resistance. For operators, a reduction in wall thickness can be considered only after verifying drop impact resistance under ASTM D2463 and topload strength under ASTM D2659, since process-induced orientation and thinning at pinch-off regions can dominate final article performance over resin isotropic data.
Operational boundaries include avoiding melt temperatures above 230 °C for extended periods, since thermo-oxidative chain scission reduces the high-molecular-weight tail and degrades environmental stress crack resistance. The grade is not recommended for continuous immersion in strong oxidising acids or ketone-containing solvents at elevated temperature; environmental stress cracking may occur under external stress. No published data supports use as a diffusion barrier for oxygen-sensitive pharmaceuticals without a secondary barrier layer or closure system. Regrind use should be controlled below 10 wt% in critical pharmaceutical packaging unless process-specific validation demonstrates equivalent organoleptic and mechanical performance.