| HS Code | 171807 |
| Polymer Type | High Density Polyethylene (HDPE) |
| Density | 0.957 g/cm³ |
| Melt Flow Rate 190 C 2 16 Kg | 0.35 g/10 min |
| Melting Point | 133 °C |
| Vicat Softening Temperature | 127 °C |
| Tensile Strength At Yield | 29 MPa |
| Elongation At Break | >600% |
| Flexural Modulus | 1250 MPa |
| Notched Izod Impact Strength 23 C | 250 J/m |
| Environmental Stress Crack Resistance 10 Igepal F50 | >1000 h |
| Shore D Hardness | 65 |
| Water Absorption | <0.01% |
| Thermal Conductivity | 0.45 W/mK |
| Volume Resistivity | >10^16 ohm-cm |
| Dielectric Constant 1 Mhz | 2.3 |
As an accredited QAPCO HDPE LOTRÈNE TR-571 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | QAPCO HDPE LOTRÈNE TR-571 is supplied in 25 kg polyethylene bags, 55 bags per pallet (1,375 kg/pallet). |
| Container Loading (20′ FCL) | QAPCO HDPE LOTRÈNE TR-571 is loaded in 20′ FCL containers as 25 kg bags, securely stowed for safe ocean transport. |
| Shipping | QAPCO HDPE LOTRÈNE TR-571 is a non-hazardous polyethylene resin, shipped as pellets in 25 kg PE bags, 1 MT jumbo bags, or bulk containers/trucks. Packaging is palletized and stretch-wrapped for transport. Store dry, ventilated, away from heat and direct sunlight; keep bags closed to prevent moisture. |
| Storage | Store QAPCO HDPE LOTRÈNE TR-571 in a cool, dry, well-ventilated warehouse, preferably in original sealed bags or containers. Protect from direct sunlight, rain, moisture, heat, and ignition sources. Keep away from strong oxidizers, oils, and contaminants. Stack pallets securely; use first-in, first-out rotation. Ensure good housekeeping and prevent static buildup. Avoid prolonged UV exposure. Do not store with food. |
| Shelf Life | Shelf life is 24 months from manufacture when stored unopened in original packaging in a cool, dry place away from direct sunlight. |
Lotrène TR-571 from QAPCO is a high molecular weight high density polyethylene whose downstream conversion is defined by a balance between high melt elasticity and controlled die swell. The grade is handled in extrusion blow moulding, heavy-gauge sheet extrusion, and high-strength blown film where sag resistance and environmental stress crack resistance dominate. Processing environments below treat the material as a rheological system, not as a universal HDPE drop-in. All numerical settings refer to production-scale equipment configurations reported in machine technical bulletins or to test methods listed in the text.
Extrusion blow moulding of UN-certified tight-head and open-top drums uses TR-571 as the main resin in formulations where the high load melt flow rate is controlled between 4.0 and 6.0 g/10 min under ISO 1133-1:2022 at 190 °C/21.6 kg. A single-station accumulator head machine with a 90 mm grooved-bush extruder and 24:1 L/D screw is set to a declining barrel profile of 190 °C, 210 °C, 220 °C, 215 °C, 205 °C; the adapter and die head remain at 210 °C. Melt temperature at the die entry is measured with an immersion probe and held within 215–225 °C; higher values reduce die head pressure but increase parison draw-down, while lower values raise pressure and cause sharkskin melt fracture at the die lip. For a 220 L L-ring tight-head drum, the parison die gap is set at 2.8–4.2 mm, target die swell is 35–50%, and the accumulator head is programmed with a 3 to 5% parison length overfeed at the bottom pinch zone to compensate for pre-blow sag. Blow pressure is set at 0.7–0.9 MPa, mold clamp force between 1,500 kN and 2,800 kN, and mold coolant inlet at 12–18 °C to avoid stress whitening at the pinch seam. The cycle time for a 220 L open-top drum runs from 160 s to 200 s; shorter cycles produce underfused pinch-off welds, while longer cycles generate inner-surface oxidation. Formulation is 100 parts TR-571, 2.25 parts of a 45% carbon black masterbatch in LDPE, 0.12 parts hindered phenolic antioxidant, 0.08 parts phosphite secondary stabiliser, and 0.25 parts HALS if the drum is exposed to outdoor weathering. Carbon black dispersion is inspected by ISO 18553:2002, with agglomerates greater than 0.5 mm² rejected because they initiate brittle failure in sidewall impact. Finished containers are qualified under UN 1H1 for tight-head and UN 1H2 for open-head designs; leakproofness is tested at 30 kPa internal air for tight-head types, hydraulic pressure is applied at 100 kPa for 30 min, stack load follows UN 6.1.5.3, and drop trials are performed after 24 h conditioning at -18 °C for Packing Group II. ESCR of pinch-off zones is checked under ASTM D1693-15 Condition B with 10% Igepal CO-630 at 50 °C; welds failing before 600 h indicate inadequate fusion temperature or excessive mold release. End products include 25 L jerrycans, 60 L open-head drums, 120 L cylindrical open-top containers, 220 L L-ring tight-head drums, and 1,000 L IBC inner bottles.
| Control parameter | Set range | Monitoring equipment |
|---|---|---|
| Melt temperature at die entry | 215–225 °C | Immersion thermocouple at head adapter |
| Accumulator die gap | 2.8–4.2 mm | Feeler gauge and linear transducer |
| Parison die swell | 35–50% | Cut-off mass vs parison length |
| Blow pressure | 0.7–0.9 MPa | Calibrated pressure transducer at blow pin |
| Mould coolant inlet | 12–18 °C | Chiller loop resistance temperature detector |
| Cycle time for 220 L open-top drum | 160–200 s | Machine PLC cycle timer |
In blown film extrusion of temporary enclosure liners, concrete curing sheets, and quarantine partitions, TR-571 is blended with 15–20 wt% of a C6-LLDPE to increase bubble symmetry and raise puncture resistance without sacrificing tensile yield. The melt is processed on a 250 mm spiral mandrel die with a 1.8 mm lip gap, 3.0:1 blow-up ratio, and frost line height at 10 to 12 die diameters. Extruder zones are profiled from 180 °C at the feed throat to 210 °C at the screen changer and 205 °C at the die; melt temperature is kept below 210 °C because higher levels reduce bubble tension and cause hunting at the nip rolls. Dual-lip air ring velocity is set between 5 and 7 m/s; insufficient lip air leads to gauge bands at the frost line, while excessive air chills the bubble at the die exit and produces visible shark-skin. The blend contains 85 wt% TR-571, 15 wt% C6-LLDPE MI 1.0 g/10 min, 0.8 wt% UV stabiliser masterbatch, and 0.2 wt% silica-filled slip/antiblock masterbatch. Film at 150 µm is produced at 180 kg/h; dart impact is tested under ISO 7765-1:2004 and Elmendorf tear under ASTM D1922-23 on machine and transverse direction samples. Compliance pathways vary with end use: concrete curing sheets require water retention measured by ASTM C156-23; temporary fumigation covers are evaluated for gas permeability under ASTM D3985-24; and structures intended for indirect food contact require organoleptic migration screening under EU 10/2011 with simulants assigned to the actual food type. This film is not considered a primary chemical packaging membrane unless a coextruded barrier layer is added, because the moisture vapour transmission rate of HDPE at 150 µm is higher than that of aluminium laminates. End products include 200 µm fumigation tarpaulins, 150 µm concrete cure covers, 250 µm temporary containment liners, and 100 µm dust partitions. Failure modes observed on production lines are bubble snaps in winds above 3 m/s and die lip drool from oxidative degradation; both are controlled by a low-pressure internal bubble stabiliser and chilled feed housing set at 35 °C.
Sheet extrusion and twin-sheet thermoforming of chemical containment bund liners and pallet dunnage use TR-571 as the structural layer where slow crystallisation permits lower internal stress in thick sections. A 120 mm single-screw extruder with 30:1 L/D, a melt pump, and a 1.2 m coat-hanger flat die is run at 220 °C, 228 °C, 230 °C, 225 °C from feed to die, with a screen pack of 80/120/80 mesh. The sheet is polished in a vertical three-roll stack with top roll at 85 °C, middle roll at 95 °C, and bottom roll at 80 °C; roll gaps are staged to deliver a 4.5 mm sheet at 180 kg/h. Closed-loop infrared edge heaters maintain sheet edges within ±2 °C of core temperature because cooler edges trim poorly and hotter edges feed thermoformer sag. Formulation uses 93.5 wt% TR-571, 4.0 wt% LLDPE, 2.0 wt% carbon black masterbatch, and 0.5 wt% stabiliser package. Twin-sheet forming on a rotary machine with 320 °C upper quartz heaters and 280 °C lower quartz heaters produces hollow pallet liners and sump forms with 6.5 mm wall thickness and welded perimeter flanges. The vacuum is staged 0.2 bar for pre-stretch, then 0.8 bar for full draw; core plug assist is maintained at 60 °C to prevent premature cooling. Chemical resistance is screened by ASTM D543-21 with 10% HCl and 30% NaOH for 30 days, and secondary containment duty is qualified under EPA 40 CFR 264.175 for 1,100 L tank bunds. Flammability of machine housing components made from the same sheet is classified by UL 94 HB. End products include 1.2 m × 1.2 m dunnage trays, 1.8 m × 0.9 m chemical pallet liners, 500 mm deep spill trays, and bund liner panels.
In open-head agrochemical and solid chemical packagings, the certification pressure is drop resistance after a -18 °C conditioning cycle. A 60 L open-head pail with a side handle is blown from TR-571 on a single-station shuttle machine with a 70 mm extruder and 600 kN clamp force; shot mass is 2.4 kg. Wall thickness distribution is specified as 2.2 mm at the sidewall and 2.8 mm at the corner radius, because drop cracks originate where the sidewall meets the base chime. The blow pin diameter is 48 mm, and the pin is equipped with a spreader die to force material into the handle pinch weld. Barrel temperatures are 195 °C, 215 °C, 225 °C, 220 °C, 210 °C; melt temperature is held at 225 °C. The mould is cooled with 10–15 °C water and cycle time is 85 s. Formulation adds 1.5 wt% carbon black masterbatch and 0.1 wt% calcium stearate; no odour-absorbing additive is used for seed treatment pails because any polar additive migrates to the surface and alters wettability. Drop testing follows UN 6.1.5.3 after 24 h of -18 °C storage; Packing Group II solid filling with a relative density of 1.2 is applied. Stack load is measured for 28 days at 40 °C with a load equivalent to 3 m stack height under the standard. Leakproofness is not required for open-head solid packages, but vacuum retention at -20 kPa is used as a production release test for pails with slip-lid closures. Outdoor storage of agrochemical solid containers is validated by ASTM D2565-23 Xenon-arc exposure for 500 h; colour retention and sidewall impact after exposure must remain within lot-specification limits. End products are 60 L seed treatment pails, 30 L veterinary mineral buckets, 45 L solid micronutrient tins, and 25 L UN solid packagings for copper oxychloride.
TR-571 is not qualified in the public domain as a PE100 pipe material under ISO 4437-2:2024. Hydrostatic design basis data, slow crack growth resistance, and rapid crack propagation performance are not reported in the QAPCO published technical file for this grade. Conversion of TR-571 into potable water pressure pipe or gas distribution pipe therefore cannot be validated without independent material reclassification. A pipe extrusion line may process the material because HDPE melt temperatures in the 200–220 °C range are accessible, but the finished pipe would lack the required 50-year design basis. Consequently, the realistic downstream scope for this grade excludes municipal pressure pipe, gas service pipe, and hot-water pressurised systems. Non-pressure conduit and corrugated drainage pipe are less demanding but still require stiffness and creep tests under EN 13476-2:2024; published data for these specific TR-571 configurations is limited. The operational boundary is meaningful because substituting a blow moulding grade into pipe extrusion typically causes excessive die swell and sag in large-diameter thick-wall sections, leading to wall thickness variation above ±10% of nominal. Processors considering non-pressure duct work should run a full lot qualification with melt flow stability checks per ISO 1133-1:2022, outer diameter control per ISO 3126:2005, and drop-weight impact per ISO 3127:2023.
Blow moulded float bodies and chemical dosing vessels made from TR-571 are processed on a 80 mm extruder with a 1.2 kg shot accumulator head for hollow technical parts. The die gap is varied during parison extrusion by a 20% wall-thickness program, from 3.5 mm at the bottom to 2.5 mm at the top, to produce uniform wall sections after forming. Melt temperature is maintained at 215 °C; cooling water inlet is 8–12 °C because thick float walls above 5 mm require low mould temperatures to shorten demould time. Formulation includes 0.5 wt% HALS at the top end of the recommended range and 2.0 wt% carbon black masterbatch for UV resistance. The components are not intended for permanent potable water contact; immersion testing is conducted under ASTM D543-21 in 10% NaCl and 5% sodium hypochlorite for 30 days. ESCR is measured with ASTM D1693-15 Condition A at 50 °C; articles with weld lines require 48 h notch aging before testing because residual orientation affects crack propagation. Water absorption is screened by ISO 62:2008, with maximum increase of 0.1% after 24 h at 23 °C. UV weathering is exposed under ASTM G154-23 cycle 1 for 1,000 h; retention of tensile elongation must remain above 70%. End products include 30 L marine floats, 150 mm chemical dosing floats, 80 L cleaning chemical dispenser bottles, and 45 L wastewater lift station floats. The material is incompatible with strong oxidisers at elevated temperature and with aromatic hydrocarbon solvents such as xylene; such service requires qualification of a different molecular design or barrier treatment.
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