| HS Code | 352037 |
| Polymer Type | High Density Polyethylene (HDPE) |
| Density | 0.954 g/cm³ |
| Melt Flow Rate 190 C 2 16 Kg | 0.45 g/10 min |
| Tensile Strength At Yield | 26 MPa |
| Tensile Strength At Break | 30 MPa |
| Tensile Elongation At Break | >600% |
| Flexural Modulus | 1100 MPa |
| Vicat Softening Temperature | 127 °C |
| Melting Temperature | 130 °C |
| Deflection Temperature At 0 45 Mpa | 75 °C |
| Brittleness Temperature | -70 °C |
| Environmental Stress Crack Resistance | >1000 h |
| Shore D Hardness | 64 |
| Thermal Conductivity | 0.35 W/m·K |
| Electrical Resistivity | >1E15 ohm·cm |
| Dielectric Constant | 2.3 |
| Dissipation Factor | 0.0003 |
As an accredited Braskem HDPE RPR7A5 WE factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Braskem HDPE RPR7A5 WE typically comes in 25 kg polyethylene bags, 55 bags per pallet, totaling 1,375 kg per pallet. |
| Container Loading (20′ FCL) | Loading of 20′ FCL with Braskem HDPE RPR7A5 WE polyethylene resin, packed in 25kg bags, palletized, shrink-wrapped, and securely stowed. |
| Shipping | Braskem HDPE RPR7A5 WE is shipped as a non-hazardous thermoplastic resin, typically in 25 kg polyethylene bags, palletized and stretch-wrapped. Transport in clean, dry trucks or containers. Protect from moisture, direct sunlight, and contamination. Store in a cool, dry warehouse. Standard freight rules apply; no hazardous-materials documentation required. |
| Storage | Store Braskem HDPE RPR7A5 WE in a cool, dry, well-ventilated area using sealed original packaging. Keep containers closed when not in use. Keep away from direct sunlight, heat, ignition sources, moisture, and strong oxidizers. Prevent dust, contamination, and static buildup. Maintain moderate temperatures, avoid stacking damage, rotate stock, and prevent pellet loss to drains. Follow supplier SDS and local regulations. |
| Shelf Life | Braskem HDPE RPR7A5 WE typically has a 24-month shelf life when stored unopened in cool, dry conditions, away from sunlight and moisture. |
Production-scale rotational molding of Braskem HDPE RPR7A5 WE for stationary crop-protection and fertilizer tanks begins with a pulverized powder classified through a 35-mesh (500 µm) screen; powder dry-flow and bulk density are controlled because bridging in mold corners consistently produces thin walls at the tank shoulder and around threaded outlet bosses. The dry-blend formulation treats the resin as 100 phr. Clean in-house regrind generated only from identical RPR7A5 WE parts is metered at up to 20 phr; addition above 25 phr is excluded from chemical-contact service because environmental stress cracking resistance declines disproportionately when regrind is exposed to surfactants, emulsifiable concentrates, and aqueous pesticide formulations. A low-melt-index PE carrier color concentrate is added at 2.0–3.0 phr to provide UV opacity in white, green, or black. Because the WE designation indicates a weather-stabilized polymer package, no supplemental hindered amine light stabilizer concentrate is used in standard agricultural outdoor storage. Carousel-type rotational molding machines with offset arm rotation ratios of approximately 4:1 are used; mold heating in forced-air ovens at 270–300 °C continues until the peak internal air temperature reaches 195–205 °C. At PIAT above 210 °C, the inner surface begins to degrade before full wall consolidation, while below 190 °C incomplete particle coalescence leaves pinholes at corner radii. Cooling is staged from forced air at 0.5–1.5 °C/min to water mist below 90 °C to reduce residual stress in flat roof sections. Powder stored in open silos above 60% relative humidity is pre-dried at 60 °C for 2 h before blending to reduce pinhole defects. Finished parts range from 1,000 L vertical cone-bottom tanks to 15,000 L horizontal stationary tanks, secondary containment basins, and saddle-mounted transport skids. For stationary storage, tank wall design is documented under ASTM D1998-21; secondary containment compatibility is reviewed under EPA 40 CFR 264.193. When potable water or food-grade liquid contact is required, the grade can be specified against FDA 21 CFR 177.1520 and EU 10/2011 for overall migration, provided no regrind from non-food-contact service is introduced.
| Standard / method | Scope |
|---|---|
| ASTM D1998-21 | Polyethylene upright storage tank design and production requirements |
| EPA 40 CFR 264.193 | Secondary containment system compatibility for hazardous substance storage |
| ASTM D1693 Condition B | Environmental stress cracking resistance of polyethylene in surfactant-bearing fluids |
| FDA 21 CFR 177.1520 | Olefin polymer compliance for food-contact liquid storage where applicable |
For floating marine structures molded from HDPE RPR7A5 WE, the primary design conflict is between thick mooring bosses required for mechanical strength and thin shell walls required for weight control. The shell is rotationally molded as a one-piece hollow body that receives a secondary closed-cell polyurethane foam fill for reserve buoyancy. Density verification follows ISO 1183-1:2019 for the molded shell and ASTM D2842 for water absorption of the rigid cellular core; for recreational vessel flotation materials, 33 CFR 183.114 addresses buoyancy and water absorption documentation. The dry-blend ratio uses 100 phr of HDPE RPR7A5 WE with a UV-opaque color concentrate at 1.5–2.5 wt%; regrind is limited to 10 wt% because low-temperature impact performance at -20 °C is the controlling design property and regrind reduces notched Izod impact values. Foam fill is not a dry-blend component; it is injected as a two-component polyurethane system with a free-rise density of 32–48 kg/m³ after the shell has cooled below 40 °C. The shell is molded on shuttle-type rotational molding machines using machined cast aluminum molds. The biaxial rotation ratio is adjusted to approximately 3.5:1 to maintain wall thickness in the mooring-eye boss; the mold is heated at an oven set point of 290–310 °C and held until PIAT reaches 195–205 °C. After air cooling to 80 °C, water mist is applied at a rate not exceeding 4 °C/min to prevent differential shrinkage between the thick boss and the thin shell body. Terminal parts include unlit channel marker buoys, mooring buoys, pontoon floats, and dock flotation blocks rated for continuous immersion. Published data for this specific formulation at the precise transition wall thickness is limited; therefore, lot-specific notched impact testing under ASTM D256 is required before releasing parts for cold-climate marine service. Field inspection records indicate that wall thickness below 5 mm at the mooring-eye boss correlates with brittle fracture at attachment points, so design drawings set a 6 mm minimum boss wall to preserve ductile yielding.
One-piece food-contact bulk containers produced from RPR7A5 WE eliminate the hygienic weakness of welded or bolted seams; the entire container body, fork pockets, and lid-sealing rim are formed in a single rotational molding operation. The dry-blend uses 100 phr of food-approved HDPE RPR7A5 WE, 1.5–2.5 phr of FDA-compliant color concentrate, and up to 30 phr of in-house regrind generated solely from the same food-grade grade. Regrind level is not raised above 30 phr because mechanical impact resistance measured by ASTM D256 declines and cold-drop failures occur at fork-entry corners. Molds are fabricated from stainless steel or polished aluminum, and release agents are selected from non-silicone food-grade chemistries. The oven cycle is terminated at an internal air temperature of 195–205 °C; lower PIAT values leave microvoids at deep draw ribs, while higher values oxidize the inner contact surface. Forced-air cooling to 70 °C precedes demolding; rapid water-quench cooling is avoided because it increases warp in flat sidewalls. Regulatory compliance is documented under FDA 21 CFR 177.1520, EU 10/2011 with overall migration testing, and 3-A Sanitary Standards for removable product contact surfaces where applicable. End products include 200 L to 1,000 L bulk bins, pallet boxes, meat and dairy transport containers, and hopper-bottom process bins.
In diesel transfer tank production, the controlling failure mode is environmental stress cracking at molded-in threaded bosses, baffle transitions, and insert bosses under continuous hydrocarbon contact and vehicle vibration. The formulation uses 100 phr of virgin RPR7A5 WE with carbon black or diesel-resistant color concentrate at 1.0–2.0 phr; regrind is restricted to 10 phr or eliminated entirely in fuel-contact walls because regrind lowers ESCR and swell resistance. No plasticizer or impact modifier is added, as these would increase fuel permeation and impair weld-line strength at molded-in inserts. Double-wall tank shells are molded with internal baffles by sequential charging or by removable core pins. The machine is run at a lower oven temperature of 275–295 °C and a PIAT of 195–205 °C to minimize inner-surface oxidation; after demolding, tanks are pressure-decay tested at 35 kPa and post-cured at 20–25 °C for 24 h before fitting brass or stainless steel inserts. Product documentation aligns with ASTM D1998-21 for upright tank wall design, EPA 40 CFR 112 for spill prevention and secondary containment, and ASTM D1693 Condition B for ESCR of the resin. For conductive or static-dissipative service, surface resistivity is measured by ASTM D257, though the base resin remains electrically insulating. Terminal configurations range from 200 L to 1,000 L rectangular transfer tanks, auxiliary diesel tanks, and portable refueling skids. The grade is not recommended for gasoline or high-aromatic solvent contact because swelling and permeation exceed diesel service limits.
When play structures must meet impact attenuation requirements, the rotomolding tool design starts with uniform shell wall distribution and rounded transition radii to prevent stress concentration during fall impacts. Play components fabricated from RPR7A5 WE use the resin's low-temperature ductility to absorb impact without sharp-edged fracture. The dry-blend ratio is 100 phr HDPE RPR7A5 WE, 2.0–4.0 phr of high-opacity weather-stable color concentrate, and up to 15 phr of clean in-plant regrind. Regrind above 15 phr is not used in impact-critical shells because the drop-weight impact value decreases and visual inspection failures occur at gate regions. Structural and safety documentation references ASTM F1487-21, EN 1176-1:2017, and EN 1176-3 for slides; colorants and additives are screened under RoHS 2011/65/EU and REACH for heavy metals and phthalates. Rotational molding tools for slides and tunnel sections are fabricated from cast aluminum with textured cavity surfaces. The oven set point is held at 285–305 °C; the cycle is terminated at 195–205 °C PIAT. Cooling is performed in still air or forced air to 75 °C, followed by gentle water mist on thick rib intersections to control warping without imposing residual stress. Finished goods include rotomolded slides, crawl tunnels, play panels, roofs, and interactive water-play basins.
On work-zone delineation lines, ballast-filled polyethylene shells are rotationally molded with double-wall construction and internal baffles to accept water or sand ballast; the material must resist repeated low-speed impacts, UV exposure, and temperature fluctuations without stress cracking at the ballast fill port. The compounding ratio is 100 phr of RPR7A5 WE, 2.0–3.0 phr of high-opacity color concentrate in orange or white, and 10–20 phr of regrind only from unpigmented or same-color barrier scrap. Higher regrind fractions are excluded because the low-speed impact recovery window narrows and the shell risks cracking in sub-zero conditions. The shells are molded on independent-arm carousel machines with large cast aluminum molds. Oven temperature is set at 280–300 °C and PIAT is maintained at 190–200 °C because wall sections from 4 mm to 8 mm must consolidate without inner-surface oxidation. Air cooling is followed by water mist below 80 °C; parts are demolded only after the mold surface reaches 55 °C to prevent post-mold deformation at the stacking lugs. For work-zone devices, documentation is aligned with MASH 2016 or NCHRP 350 where impact testing is required, and material identification is certified under ISO 11469 to aid end-of-life recycling. Terminal products include water-filled longitudinal channelizers, sign bases, barricade shells, and round delineator drums.
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Braskem HDPE RPR7A5 WE is a high-density polyethylene grade supplied in pellet form. The WE suffix denotes a widened specification window relative to the corresponding prime resin; consequently, the material is not defined by a single datasheet value but by the lot-specific certificate of analysis. The polymer is directed toward general-purpose rigid packaging, non-food crates, pallets, dunnage, and thick-wall drainage products. Melt flow, density, and mechanical properties should be confirmed by the molder or extruder against the supplied raw-material test data before production tooling is released.
In rigid crates and pallets with wall thickness between 2 mm and 6 mm, the grade is processed either by conventional injection molding or low-pressure structural foam. With wider melt-mass-flow variation from lot to lot, closed-loop cushion and shot-size control become necessary. The density span of 0.952 g/cm³ to 0.960 g/cm³ can move semicrystalline shrinkage in the range of 1.5 % to 2.5 % after 48 h; multi-cavity tools with unbalanced runners may show cavity-to-cavity mass variation if the lot is not pre-screened.
On a 70 mm grooved feed single-screw extruder with an L/D ratio of 30:1, changing from a prime blow-molding HDPE with 0.3 g/10 min MFR to a WE grade with a high-lot MFR of 1.0 g/10 min can lower melt pressure at the die by approximately 10 % to 20 %. A metering pump is therefore advised when wall thickness tolerances of ±0.2 mm are required. Substitution also changes die swell: a broader molecular weight distribution generally produces higher die swell, so a pin and die combination matched to the former grade may produce oversized parisons or excessive flash in blow molding. The WE configuration is thus suitable for applications where trimming to 3 % flash is already normal scrap. Where flash cannot be reground, the specification may not be suitable.
Melt mass-flow rate is determined according to ISO 1133-1:2022 at 190 °C under 2.16 kg load. A companion high-load value at 21.6 kg is used to compute the melt flow ratio; wider MFR ratios indicate a broader molecular weight distribution. Capillary rheometry at 210 °C shows the usual shear-thinning response: apparent viscosity is generally in the range of 800 Pa·s to 1200 Pa·s at 100 s-1, decreasing to 200 Pa·s to 350 Pa·s at 1000 s-1. These values are class-typical and must be verified for the specific lot because the WE designation expands the allowable viscosity envelope.
| Property | Test method | Unit | Indicative family window |
|---|---|---|---|
| Melt mass-flow rate (190 °C, 2.16 kg) | ISO 1133-1:2022 / ASTM D1238 | g/10 min | 0.4–1.0 |
| Density | ISO 1183-1:2019 / ASTM D1505 | g/cm³ | 0.952–0.960 |
| Tensile yield stress (23 °C) | ISO 527-2 type 1A | MPa | 24–29 |
| Tensile strain at break | ISO 527-2 type 1A | % | 300–700 |
| Flexural modulus | ISO 178 | GPa | 1.0–1.3 |
| Notched Izod impact | ISO 180/A | kJ/m² | 6–12 |
| ESCR (100 % Igepal, Condition B) | ASTM D1693 | h | >50 |
| Shore D hardness | ISO 868 | — | 65–70 |
Published data for the WE-specific lot are limited; the ranges in Table 1 represent a class envelope for low-melt-index HDPE extrusion grades and should not be treated as guaranteed values. For load-bearing articles, tensile and flexural values should be generated after conditioning at 23 °C and 50 % relative humidity for 40 h according to ISO 291.
In injection molding on a 1500 kN clamp force machine with a 40 mm three-zone screw, barrel settings are generally 210 °C in the rear zone, 220 °C to 230 °C in the center, and 230 °C to 240 °C in the nozzle. Mold temperature is maintained at 10 °C to 30 °C. Injection pressure of 60 MPa to 100 MPa is typical for 2 mm to 3 mm wall thickness; pack pressure is held at 40 MPa to 60 MPa for 4 s to 8 s. Low melt-index HDPE is susceptible to gate blush when shear rate exceeds approximately 40,000 s-1; consequently, gate openings should be at least 60 % of part wall thickness and injection velocity should be profiled.
Repeated recycling of sprues and runners beyond 20 % regrind by weight may shift melt flow upward through chain scission. The shift is not always linear with regrind percentage and should be tracked by melt flow verification at the start and end of each production run. If regrind is added through a side feeder on a twin-screw compounding line, the feeder calibration should be adjusted when bulk density changes by more than 5 %.
On a single-screw extruder with an L/D ratio of 30:1 and a 60 mm diameter screw, acceptable barrel settings for this grade family are 180 °C to 200 °C in the feed section, 200 °C to 215 °C in the compression section, and 210 °C to 230 °C in the metering section. Adapter and die head temperature should be maintained at 215 °C to 235 °C. A screen pack of 40/60/80 mesh and a breaker plate are typically used. Prolonged residence time above 240 °C for more than 10 min risks oxidative degradation, gel formation, and color shift from white to yellow.
Predrying is not normally required below 60 % relative humidity. If surface moisture is observed on pellets after outdoor storage or condensation conditions, a 2 h drying step at 80 °C in a desiccant dryer is recommended before processing. For thick-wall extruded profiles above 10 mm, a dry air hopper set to 70 °C can reduce surface splay and internal voids caused by volatiles from moisture or process additives.
For material-selection decisions, the RPR7A5 WE grade is compared with three alternative HDPE platforms in Table 2. The data are class-wide approximations and do not replace lot-specific values.
| Polymer class | Typical MFR (190 °C, 2.16 kg) | Density range | ESCR class | Typical processing route |
|---|---|---|---|---|
| Braskem HDPE RPR7A5 WE | 0.4–1.0 g/10 min | 0.952–0.960 g/cm³ | >50 h | Injection molding, blow molding, extrusion |
| Injection-molding HDPE | 4–20 g/10 min | 0.955–0.965 g/cm³ | 5–30 h | High-speed injection molding |
| Extrusion blow-molding HDPE | 0.2–0.5 g/10 min | 0.948–0.958 g/cm³ | 100–1000 h | Extrusion blow molding |
| Blown-film HDPE | 0.8–1.2 g/10 min | 0.958–0.964 g/cm³ | 30–100 h | Blown film |
These differences affect dimensional stability, impact behavior, and environmental stress crack resistance. The WE grade occupies a low-melt-index region more suitable for thick wall sections than for thin-wall high-speed injection; mold filling of sections below 1.0 mm may require higher melt temperature or a fluidity-enhancing masterbatch, but the latter may reduce stiffness and long-term creep resistance.
Environmental stress cracking resistance is measured on compression- or injection-molded specimens according to ASTM D1693. The test uses 10 % or 100 % Igepal CO-630 at 50 °C; Condition B under constant strain is the standard for high-density packaging. In a wide-specification grade, the molecular weight distribution may vary more than in a prime resin because reactor transitions or co-product blending can alter the high-molecular-weight tail. That variation changes ESCR, die swell, and melt strength. Users quantifying long-term cracking in dishwashing or chemical exposure should not rely on a single lot; a minimum of three non-consecutive lots should be tested.
Differences from injection grades are marked: injection HDPE with MFR above 4 g/10 min typically has shorter stress-cracking resistance and lower tensile strain at break. Conversely, a low-melt-index blow-molding HDPE with MFR of 0.2 g/10 min to 0.5 g/10 min generally provides higher ESCR but lower output on high-speed injection lines. The RPR7A5 WE grade therefore sits in an intermediate position: processable by injection and extrusion but with a broader property envelope than either prime injection or prime blow-molding grade.
Compliance for Braskem HDPE RPR7A5 WE is documented through lot-level certificates and supplier declarations. For food-contact packaging, the end-use article must meet FDA 21 CFR 177.1520 and, for the European Union, EC 1935/2004 and EU 10/2011 migration limits, with verification performed on the final packaging because process additives and unintended contaminants may migrate. Under REACH, the polymer and its additives are subject to registration; under RoHS Directive 2011/65/EU, lead, mercury, cadmium, hexavalent chromium, PBB, and PBDE must remain below the specified thresholds for electrical and electronic equipment. The WE suffix does not automatically imply post-consumer recyclate content; if recycled material is incorporated, the relevant ISO 14021 recycled-content claims must be supported by the supplier. Reprocessing operations should limit total regrind to 20 % by weight to limit MFR shift and impact loss.