| HS Code | 829272 |
| Polymer Type | High-Density Polyethylene (HDPE) |
| Density | 0.94-0.96 g/cm³ |
| Melt Flow Rate 190 C 2 16 Kg | 0.2-8 g/10 min |
| Tensile Modulus | 800-1200 MPa |
| Tensile Strength At Yield | 20-30 MPa |
| Elongation At Break | >500% |
| Charpy Notched Impact Strength 23 C | 5-20 kJ/m² |
| Shore D Hardness | 55-65 |
| Vicat Softening Temperature | 110-125°C |
| Melting Temperature | 125-135°C |
| Water Absorption 24 H | <0.01% |
| Thermal Conductivity | 0.35-0.50 W/(m·K) |
| Coefficient Of Linear Thermal Expansion | 100-200 µm/(m·°C) |
| Flammability Ul 94 | HB |
| Processing Methods | Injection molding, extrusion, blow molding |
As an accredited Mocom (ALBIS) PE-HD ALTECH factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Typically, Mocom (ALBIS) PE-HD ALTECH is supplied in 25 kg moisture-resistant polyethylene bags, palletized and shrink-wrapped for transport. |
| Container Loading (20′ FCL) | Container Loading (20′ FCL): Mocom (ALBIS) PE-HD ALTECH, palletized 25 kg bags, dry container, ambient, secured cargo, standard industrial packaging. |
| Shipping | Mocom (ALBIS) PE-HD ALTECH is supplied as solid thermoplastic granules in moisture-barrier bags, octabins, or bulk bags on pallets. Ship in covered, dry transport at ambient temperature, avoiding direct sunlight, moisture, and contamination. Not classified as dangerous goods; comply with local regulations. Keep sealed until use. |
| Storage | Store Mocom (ALBIS) PE-HD ALTECH in a cool, dry, well-ventilated area, away from direct sunlight, heat, sparks, flames, and strong oxidizers. Keep in original, sealed containers or bags on pallets. Protect from moisture, dust, oils, and other contaminants. Avoid prolonged UV exposure and excessive stacking. Follow local regulations and supplier guidance. |
| Shelf Life | The shelf life is typically 12 months when stored dry, cool, and protected from direct sunlight in original, unopened packaging. |
Blow-molded inner liners for 1,000 L composite intermediate bulk containers are produced from ALTECH PE-HD in continuous extrusion blow molding cells equipped with a 60 mm grooved-barrel extruder, a 24:1 L/D ratio, and an accumulator head with parison programming. The compound is processed as supplied at 100 wt%; addition of a UV-stabilized HDPE carrier masterbatch at 1.5–2.5 wt% is specified only when the liner is qualified for outdoor storage under UN 31H2. Melt temperature is held at 190–210°C. Barrel zones exceeding 220°C generate gel particles from low-molecular-weight fractions, and these gels accumulate at the pinch-off weld to create a leak path during hydraulic pressure testing. A production-scale failure mode observed in liner manufacturing is axial thinning at the top corner radius caused by parison sag, corrected by setting the die gap to 2.8–3.4 mm and the preblow delay to 0.3–0.7 s. Because chemical compatibility is often the limiting design input, the unmodified liner is not specified for aromatic hydrocarbons, ketones, or chlorinated solvents above 40°C; these media require separate fluorination or coextrusion qualification. Compliance references ADR 6.5.2 for design type testing, FDA 21 CFR 177.1520(c) 1.1 or EU 10/2011 with an overall migration limit of 10 mg/dm² for food-contact liners, and EN ISO 16103 for dimensional assessment. End products include 1,000 L composite IBC liners, 200 L open-head drum liners, and 30 L carboy liners.
Injection molding of 1,200 mm × 1,000 mm logistics pallets and 600 mm × 400 mm returnable crates is performed with ALTECH PE-HD at 75–100 wt%, the balance being post-industrial regrind that must not exceed 25 wt% without revalidation of ISO 179-1/1eA Charpy notched impact at −30°C. Plasticating is carried out on a 140 mm screw with a 20:1 L/D ratio, and the injection unit is mounted on a press with a clamp force between 800 t and 1,200 t. Mold temperature is maintained at 10–25°C; the lower end accelerates skin solidification but increases frozen-in stress at rib intersections. Gate freeze-off time is set to 2.5–4 s. If the gate freezes before packing pressure decays, cavity pressure rises above 80 MPa and can initiate corner cracks during cold-chain vibration and impact. Compliance for logistics service is assessed under ISO 8611-1:2011 for pallet load capacity and ASTM D4169-22 for returnable crate transport simulation; stacking tests use a load class selected from ISO 8611-1, commonly 1,250 kg on a 1,200 mm × 1,000 mm pallet for 48 h at 23°C. End products are export pallets, pool pallets, and folding or rigid returnable crates.
Automotive windshield washer reservoirs and headlamp cleaning system bottles are extrusion blow molded or suction blow molded from ALTECH PE-HD with a wall thickness distribution between 1.1 mm and 2.3 mm. The compound is metered at 100 wt%, and black pigmentation is introduced as a 2.0 wt% carbon black masterbatch whose melt mass-flow rate at 190°C/2.16 kg is matched to the base resin within ±0.3 g/10 min to prevent streaking and knit-line weakness. Three-dimensional routing around vehicle package constraints is produced on suction blow molding cells with blow air pressure of 0.6–0.8 MPa and mold temperature of 8–15°C. Rapid mold cooling at the lower temperature boundary requires dehumidified air when ambient relative humidity exceeds 60%; otherwise surface condensation creates pitting at the pinch-off and along the parting line. The main production-line failure mode occurs when the parison thickness profile is offset by more than 0.2 mm from the programmed setpoint; the resulting pinch-off weld fails below the ISO 179-1/1eA Charpy notched impact value required for freezer-impact service. Published grade-specific comparative data for this exact washer bottle configuration is limited; first-article validation on the target suction blow molding line is mandatory before series release. Compliance is verified with ISO 179-1, ISO 527-2, and the vehicle manufacturer’s heat-aging and windshield washer fluid immersion protocol. End products are 3–7 L windshield washer reservoirs, headlamp washer bottles, and integrated filler neck assemblies.
Injection molding of dairy and still-beverage closures from ALTECH PE-HD is performed on high-speed machines with 48 or 96 cavities, a melt temperature of 200–215°C, and a mold temperature of 12–18°C. The compound is dosed at 96–98 wt%; the remaining 2–4 wt% is a lubricant/antioxidant masterbatch carried in a polyethylene with a density of 0.940–0.950 g/cm³ to avoid visible flow lines on the cap top. Hot-runner gate diameter is held at 0.8–1.2 mm for closure weights of 3–6 g; an undersized gate creates short shots at the skirt edge, while an oversized gate delays solidification and increases cycle time. Residence time in the barrel should remain below 8 min at 215°C to avoid oxidative chain scission that lowers torque retention. Torque retention after pasteurization at 85°C for 15 min is evaluated according to ASTM D2063-12; moisture vapor transmission rate is tested under ASTM F1249 at 38°C/90% RH. Compliance for food contact references FDA 21 CFR 177.1520 and EU 10/2011. End products are 28 mm and 38 mm closures for HDPE and PET bottles, tamper-evident caps, and snap-hinge squeeze bottle caps for still beverages and dairy.
| Scenario | Cited standard or regulation | Test or requirement | Relevant designation |
|---|---|---|---|
| Blow-molded IBC liner | ADR 6.5.2FDA 21 CFR 177.1520(c) 1.1EU 10/2011 | Drop, stacking, hydraulic pressure, leakproofness, migration limit | UN 31H2 |
| Pallet and crate | ISO 8611-1:2011ASTM D4169-22 | Load capacity, transport simulation | Logistics class selected by operator |
| Automotive washer reservoir | ISO 179-1ISO 527-2 | Charpy impact, tensile properties | OEM validation protocol |
| Closure | ASTM D2063-12ASTM F1249FDA 21 CFR 177.1520EU 10/2011 | Torque retention, WVTR, migration limit | Food-contact closure |
| Corrugated drainage pipe | ISO 9969:2016EN 13476-3 | Ring stiffness, structured-wall pipe characteristics | SN8 class |
| Fluorinated jerrican | ADR 6.1.3ASTM D1693 condition B | Design type testing, ESCR | UN 3H1 |
Twin-screw corrugated drainage pipe lines produce conduits with outside diameters from 100 mm to 1,000 mm using ALTECH PE-HD at 100 wt%, with a carbon black masterbatch added at 2.0–2.5 wt% through the main dosing hopper. The extruder is a counter-rotating twin-screw machine with a 40:1 L/D ratio, and melt temperature is limited to 195–210°C because the downstream vacuum forming blocks require a stable melt strength. Wall-thickness oscillation in the corrugation trough beyond ±0.4 mm reduces annular ring stiffness below the required SN8 class. The extrusion rate is synchronized with the corrugator speed using a laser wall-thickness scanner; if the scanner detects a trough-to-crest thickness deviation above 0.15 mm, the parison is rejected before socket cutting. Surface condensation on outdoor-stored granules must be removed when the ambient dew point exceeds the bulk resin temperature; a hopper air temperature of 70°C for 1 h is sufficient, while longer drying is not required for the base polymer. Compliance is verified under ISO 9969:2016 for ring stiffness and EN 13476-3 for structured-wall pipe characteristics. End products are cable ducts, land drainage pipes, stormwater retention module conduits, and corrugated culvert liners.
Coextrusion blow molding of 5–25 L jerricans for pesticides, solvents, and crop protection chemicals uses ALTECH PE-HD as the base layer at 85–100 wt% of the wall thickness; in-line regrind is introduced into the central layer at a maximum of 15 wt% only after environmental stress-cracking resistance has been confirmed according to ASTM D1693 condition B over 48 h. Inline fluorination is executed with a fluorine-in-nitrogen mixture at 0.5–2.0% fluorine during the blow molding cycle to reduce permeation of nonpolar solvents through the HDPE wall. The treatment depth is controlled by gas flow rate, blow pressure, and contact time; fluorine levels above 2.0% produce a brittle surface skin that cracks at the flash-line pinch-off during drop testing. The operational boundary is therefore not only the fluorine concentration but also the post-treatment cooling rate at the weld line; delayed cooling after demolding intensifies surface embrittlement. Compliance follows ADR 6.1.3 for design type testing of UN 3H1 jerricans. Published permeability data for this ALTECH PE-HD grade after inline fluorination is limited; barrier validation on the specific jerrican cavity geometry is therefore required. End products are 5 L and 20 L fluorinated HDPE jerricans, dosing containers, and returnable agricultural chemical packs.
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Mocom (ALBIS) PE-HD ALTECH is a compounded high-density polyethylene grade supplied as natural or pigmented granules. The designation PE-HD denotes a polymer backbone with a density of at least 0.941 g/cm³ as defined in DIN EN ISO 1043-1, and the ALTECH brand identifies a formulated compound rather than a virgin resin. For unreinforced injection-moulding grades of this class, density typically falls between 0.94 g/cm³ and 0.97 g/cm³ according to ISO 1183-1. Melt mass flow rate at 190 °C and 2.16 kg, measured according to ISO 1133-1:2022, is grade-dependent and commonly ranges from 0.2 g/10 min for high-molecular-weight extrusion types to 20 g/10 min for easy-flow injection types. Differential scanning calorimetry per ISO 11357-3 places the melting peak between 130 °C and 137 °C, with crystallinity determined by density and cooling rate. Because the matrix is non-polar and semi-crystalline, water absorption at 23 °C and 50% relative humidity is below 0.01 wt%. The compound is stabilised with a hindered phenolic and phosphite system, but the precise additive package, filler content, and melt flow rate require the grade-specific technical datasheet.
Rheologically, unfilled high-density polyethylene compounds are pseudoplastic. At melt temperatures between 190 °C and 230 °C, the shear viscosity of a grade with MFR 4 g/10 min to 12 g/10 min can vary from approximately 800 Pa·s to 300 Pa·s over shear rates of 100 s⁻¹ to 1000 s⁻¹, as measured by capillary rheometry in ISO 11443. The power-law index lies between 0.35 and 0.50. On single-screw extruders with 25:1–30:1 L/D and compression ratios of 2.5:1–3.5:1, a barrel profile of 180 °C at the feed throat to 210 °C at the die is used. For injection moulding, a screw with L/D of at least 20:1, a non-return valve with a free-flow end cap, and a nozzle temperature of 190 °C to 220 °C are standard. The mould temperature is maintained between 10 °C and 50 °C, with lower mould temperatures reducing cycle time but increasing flow orientation and shrinkage anisotropy.
Because the crystallisation temperature extends from 117 °C to 124 °C, cooling of sections thicker than 4 mm occurs with a pronounced skin-core temperature gradient. The melt pressure required to compensate volumetric shrinkage in unfilled PE-HD is typically 50 MPa to 80 MPa during hold, with a screw cushion of 2 mm to 5 mm. Premature hold release produces sink marks and microvoids. Mould shrinkage after 48 h per ISO 294-4 ranges from 1.5% to 3.5% for unfilled grades and falls to 0.6%–1.2% for mineral-filled formulations. Pre-drying is not required for dry granulate; however, granulate stored below the dew point can carry surface condensation, which is removed by drying at 80 °C for 2 h using a desiccant dryer with a dew point below −20 °C.
Compounding on twin-screw extruders with 36:1–48:1 L/D and specific energy input of 0.15 kWh/kg–0.25 kWh/kg is typical for colour and stabiliser dispersion. Melt flow variability is usually held within ±10% of the nominal value when tested under ISO 1133-1. In production-scale injection moulding, the main observed failure modes are gate blush from excessive injection speed, sink marks from inadequate packing, and warpage from non-uniform mould temperature; these are controlled by closed-loop melt temperature and cushion monitoring.
Low-temperature impact resistance in PE-HD compounds is not governed by the glass transition alone. The β-relaxation of polyethylene occurs below −100 °C, but the practical ductile-brittle transition is raised by notch severity, comonomer placement, molecular weight, cooling rate, and orientation. Notched Charpy impact strength per ISO 179-1/eA at 23 °C commonly falls between 4 kJ/m² and 20 kJ/m² for unreinforced high-density polyethylene compounds, depending on molecular weight and notch radius preparation. At −30 °C, the range narrows to approximately 2 kJ/m²–6 kJ/m². Thin sections with frozen-in orientation may show higher crack propagation resistance, but notched specimens eliminate that energy contribution and represent a lower-bound condition.
Environmental stress cracking resistance is the more common field failure boundary. Under ASTM D1693 condition B, using 10% Igepal CO-630 at 50 °C, high-density polyethylene resins in this class can show F50 failure times from below 10 h for low-molecular-weight easy-flow grades to above 1000 h for bimodal, low-MFR pipe grades. Injection-moulding grades with MFR above 8 g/10 min generally trade lower ESCR for fill speed. For applications with continuous surface-active chemical exposure, a reduced melt index and a known comonomer type are more important than room-temperature impact value.
Representative class-level data for unreinforced PE-HD ALTECH, unfilled PE-HD, a 20 wt% talc-filled polypropylene compound, and a dry 30 wt% glass-fibre-reinforced polyamide 6 are shown below. The PE-HD ALTECH values assume no mineral filler; grade-specific filler and impact-modifier packages will shift the envelope.
| Property | Test method | Unreinforced PE-HD ALTECH | Unfilled PE-HD | 20 wt% talc-filled PP | 30 wt% GF PA6 dry |
|---|---|---|---|---|---|
| Density | ISO 1183-1 | 0.94–0.97 g/cm³ | 0.95–0.97 g/cm³ | 1.03–1.07 g/cm³ | 1.35–1.42 g/cm³ |
| Tensile modulus | ISO 527-2 | 800–1500 MPa | 700–1400 MPa | 2500–3500 MPa | 9000–11000 MPa |
| Tensile yield stress | ISO 527-2 | 20–32 MPa | 20–30 MPa | 25–30 MPa | 110–140 MPa |
| Notched Charpy at 23 °C | ISO 179-1/eA | 4–20 kJ/m² | 4–15 kJ/m² | 2–6 kJ/m² | 8–15 kJ/m² |
| Heat deflection temperature B | ISO 75-2/B | 60–85 °C | 60–75 °C | 100–125 °C | 200–220 °C |
| Mould shrinkage | ISO 294-4 | 1.5–3.5% | 1.5–4.0% | 0.7–1.2% | 0.2–0.6% |
The main differences between PE-HD ALTECH and unfilled PE-HD are not necessarily visible in bulk tensile data; they appear in additive retention, molecular weight distribution control, and batch-to-batch melt flow range. Relative to a 20 wt% talc-filled polypropylene, the PE-HD matrix has lower density, lower heat deflection temperature under load, and higher linear shrinkage after moulding, but higher elongation at break and lower moisture sensitivity. Relative to 30 wt% glass-fibre-reinforced polyamide 6, the PE-HD compound has a much lower tensile modulus and lower HDT, but it does not require pre-drying for moisture uptake and it resists hydrolysis in polar aqueous environments.
When a mineral-filled PE-HD replaces an unfilled high-density polyethylene in extruded sheet and thermoforming, the process change involves more than a density increase. The filler raises low-shear melt viscosity and melt strength, reducing sag at the thermoforming temperature of 160 °C–200 °C. The thermal conductivity of an unfilled PE-HD is approximately 0.40 W/(m·K) to 0.45 W/(m·K); the addition of 20 wt% to 40 wt% mineral filler can increase this to 0.60 W/(m·K)–1.0 W/(m·K), reducing the sheet heating time for a given thickness. However, the same filler reduces drawability and increases the risk of local thinning at corners when the plug speed exceeds the material’s deformation rate. Published data for this specific PE-HD ALTECH configuration at filler loadings above 40 wt% is limited; processing trials on vacuum-assisted plug-assisted forming lines should therefore use starting sheet temperatures in the upper half of the crystalline melting range and an adjustable plug delay.
For parts with wall-thickness distribution requirements, a hot mould at 60 °C–90 °C and a well-controlled sheet temperature of 170 °C–190 °C are standard. Compared with unfilled PE-HD, mineral-filled grades produce reduced post-forming shrinkage and lower part-to-part dimensional variability, but cut edges can show filler-related wear on steel trim tools; hardened tool steel with Rockwell hardness of 58 HRC to 62 HRC is specified for blanking operations.
Chemical resistance of the PE-HD matrix is assessed by immersion testing under ASTM D543 at 23 °C and 60 °C. The material generally withstands dilute acids, alkalis, saline solutions, and many polar solvents with mass change below 1% after 7 days. It is not suitable for continuous contact with strong oxidising acids, aromatic hydrocarbons, or chlorinated solvents, where swelling and environmental stress cracking may occur. Outdoor weathering requires a UV-stabilised grade or a carbon black masterbatch added at 2 wt%–2.5 wt%. Melt blending with polyamide or polyester is not recommended because high interfacial tension produces gross phase separation and delamination in moulded articles.
| Regulation | Relevant code | Condition for supplied article |
|---|---|---|
| REACH SVHC | (EC) No 1907/2006 | Concentration below 0.1 wt% per article |
| RoHS | 2011/65/EU with (EU) 2015/863 | Lead, mercury, hexavalent chromium, PBB, PBDE below 0.1 wt%; cadmium below 0.01 wt% |
| US food contact | FDA 21 CFR 177.1520 | Grade-specific letter of compliance required |
| EU food contact | (EU) No 10/2011 | Overall migration ≤ 10 mg/dm²; specific migration limits apply |
| Flammability | UL 94 | Unfilled PE-HD typically HB at 1.6 mm and 3.2 mm; yellow card required |
Storage and drying boundaries are narrow. The granulate retains processability for 24 months when kept in sealed, UV-shielded packaging at 15 °C–35 °C and below 60% relative humidity. At higher humidity or after outdoor exposure, 80 °C drying for 2 h is applied only to remove surface condensation because the polymer itself is non-hygroscopic. The practical quality window for unfilled PE-HD injection moulding is set by screw recovery time, gate freeze time, and cushion stability rather than by thermal degradation. Holding at melt temperatures above 280 °C for more than 15 min can produce odour and a drop in impact strength, although the onset of thermo-oxidative degradation in properly stabilised compounds is normally above 300 °C under ISO 11357-6.