| HS Code | 747753 |
| Density | 0.935 g/cm³ |
| Melt Flow Rate 190 C 2 16 Kg | 5.0 g/10 min |
| Melting Temperature | 126 °C |
| Vicat Softening Temperature | 108 °C |
| Tensile Stress At Yield | 15.5 MPa |
| Elongation At Break | 800% |
| Flexural Modulus | 700 MPa |
| Environmental Stress Crack Resistance 10 Igepal F50 | >1000 h |
| Izod Impact Strength 23 C | No break |
| Izod Impact Strength 40 C | 25 kJ/m² |
| Shore D Hardness | 55 |
| Brittleness Temperature | -80 °C |
As an accredited SABIC LLDPE R50035EE factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | SABIC LLDPE R50035EE is supplied as pellets in 25 kg bags, with 40 bags per shrink-wrapped pallet (1,000 kg total). |
| Container Loading (20′ FCL) | 20′ FCL: SABIC LLDPE R50035EE loaded as full container load, secured properly, protected from moisture and heat for safe transport. |
| Shipping | SABIC LLDPE R50035EE is shipped as non-hazardous linear low-density polyethylene resin in pellet form. It is typically packaged in 25 kg bags, octabins, or bulk hopper trucks. Protect from moisture and direct sunlight, and store in a clean, dry area to prevent contamination. |
| Storage | Store SABIC LLDPE R50035EE in a clean, dry, well-ventilated area away from direct sunlight, heat sources, and ignition. Keep the original sealed packaging intact to prevent moisture and contamination. Recommended storage temperature is below 50°C. Avoid prolonged outdoor exposure and stacking excessively high to preserve material flow and performance. |
| Shelf Life | Shelf life is indefinite when stored properly in original packaging, in a cool, dry area, protected from direct sunlight and moisture. |
Vertical polyethylene chemical storage tanks are rotationally molded from SABIC LLDPE R50035EE when process economics require a balance between typical datasheet density 0.935 g/cm³ and melt mass-flow rate 5.0 g/10 min at 190°C/2.16 kg. The melt index is determined under ISO 1133-1:2022 or ASTM D1238-23. Powder is pulverized to 35 mesh and charged into a fabricated steel or cast aluminum mold with a biaxial rotation ratio of 4:1 to 4.5:1. Oven air temperature is maintained at 280°C to 320°C. Peak internal air temperature (PIAT) is brought to 200°C to 215°C and held for 20 min to 35 min depending on wall thickness. Thin corners below 5 mm can overheat before thick sidewalls consolidate. Mold venting and thermocouple placement therefore follow the thickest section. Cooling from 120°C to 70°C is controlled at 2°C/min to 4°C/min with forced air and water mist. Demolding above 70°C produces warped flat sidewalls. Chemical storage tanks for diluted mineral acids and caustic solutions are designed under ASTM D1998-21. Hazardous-liquid tanks require UN 31A/Y certification. ESCR behavior is evaluated using ASTM D1693-22 condition B in 10% Igepal CO-630 at 50°C. Published long-term resistance data for concentrated nitric acid or aromatic hydrocarbons are limited. ASTM D543-21 immersion coupons are required before service.
| Requirement | Standard / test method | Condition |
|---|---|---|
| Density | ASTM D1505-18 | 23°C |
| Melt mass-flow rate | ISO 1133-1:2022 | 190°C, 2.16 kg |
| ESCR | ASTM D1693-22 condition B | 10% Igepal CO-630, 50°C |
| Upright tank design | ASTM D1998-21 | Hydrostatic/vacuum |
| Hazardous-liquid drop | 49 CFR 178.603 | -18°C |
| Hazardous-liquid hydrostatic | 49 CFR 178.605 | Design pressure |
Agricultural trailed sprayer tanks use R50035EE because the 5.0 g/10 min low-shear flow fills narrow baffle ribs and molded-in sump details without increasing peak internal air temperature above 220°C. A typical dry-blend formulation is 96.5–98.0 wt% R50035EE powder, 2.0–3.0 wt% LLDPE-carrier UV masterbatch, and 0.5–1.0 wt% pigment masterbatch. The dry blend is tumble-mixed in a high-speed mixer at 800–1000 rpm for 4 min to prevent masterbatch segregation. Oven temperature is set at 270–300°C. Peak internal air temperature is controlled to 195–210°C. If PIAT remains below 195°C, bridging occurs at the baffle edges. If PIAT exceeds 220°C, surface oxidation and foaming increase. The addition of a non-LLDPE carrier masterbatch at 3 wt% can dilute environmental stress crack resistance. Processors compare F50 values per ASTM D1693-22 condition A before approving a masterbatch. Published data for this specific grade/masterbatch combination are limited. A five-specimen comparison against virgin R50035EE is required for each lot. For glyphosate and paraquat formulations diluted to field strength, LLDPE is generally resistant at 23°C. Concentrated xylene or cyclohexanone carriers cause swelling. ASTM D543-21 immersion in the actual formulation is required.
In marine buoy production, the outer shell is rotomolded from R50035EE at wall thickness 5–12 mm. The mold is charged with 98.0–99.0 wt% R50035EE powder and 1.0–2.0 wt% UV/HALS masterbatch. Carbon black is avoided where white or yellow outer skins are specified. Oven temperature is set to 280–300°C. Peak internal air temperature is controlled to 200–210°C for 20–25 min. After cooling below 50°C, the shell is filled with a two-component closed-cell polyurethane foam of nominal density 32 kg/m³. The foaming exotherm can exceed 120°C inside the shell. The LLDPE shell is not demolded until wall temperature is below 60°C. Low-temperature impact is assessed by ARM impact or ASTM D5628-18. Salt spray per ISO 9227 for 500 h is used for metal insert compatibility. Pinholes at the foam filling port are the main field failure, caused by vent bore diameters below 12 mm. A vent insert with a 12–16 mm bore is specified.
For traffic-rated underground utility chambers, the mold is charged with R50035EE blended with 2.0–2.5 wt% carbon black masterbatch for pre-installation outdoor storage. Molded wall thickness is 6–12 mm. Removable core blocks form conduit entry stubs. Excessive cooling rate across the 120°C to 70°C window freezes residual stresses at corner radii below 12 mm. Sulfate-rich groundwater attacks poorly fused powder particles at the inner wall. ESCR testing per ASTM D1693-22 condition B is therefore specified on samples taken from the tank bottom corner. For traffic-rated chambers under AASHTO H-20 loads, vertical deflection is measured with a hydraulic actuator at 5 mm/min until 5% deformation. Published data for R50035EE in this specific structural configuration are limited. Full-scale proof tests are required. The powder should be pre-dried at 80°C for 4 h when exposed to relative humidity above 60%. Moisture during molding creates pinholes and lowers burst strength.
Rework of flash and rejected parts is dry-blended into virgin R50035EE at 10–20 wt% for non-critical tanks. Above 20 wt%, the molded part’s low-temperature impact and ESCR are no longer guaranteed by the virgin grade datasheet. Melt mass-flow rate of a 30 wt% regrind blend should be measured per ISO 1133-1:2022. An increase above 5.5 g/10 min indicates shear- or thermo-oxidative chain scission from multiple heat histories. The regrind is ground to 35 mesh, passed through a 0.5 mm screen, and blended in a paddle mixer for 10 min at 60 rpm. For UN 31A/Y dangerous goods tanks, any regrind level above 20 wt% requires full design qualification retesting under 49 CFR 178.603 drop at -18°C and 178.605 hydrostatic pressure. The reason is not homopolymer contamination but reduction in high-molecular-weight fraction. The comonomer-rich chain segments are more susceptible to chain scission at rotomolding heat history. The inner wall of parts containing regrind exhibits a higher carbonyl index measured by FTIR at 1715 cm⁻¹. If the carbonyl index doubles relative to virgin, ESCR F50 falls below the acceptance threshold.
When stainless steel is not justified, dry-bulk material-handling bins and hoppers are rotomolded from R50035EE. The 0.935 g/cm³ density provides higher panel stiffness than lower-density LLDPE rotomolding grades used for marine buoys. Wall sections of 4–8 mm resist product swelling from hygroscopic powders. Corners are designed with 25–50 mm internal radii to avoid powder hang-up. The mold is rotated at 4:1. Oven temperature is held at 290–310°C. Peak internal air temperature is 205–215°C. For food-contact use, the molded bin must comply with FDA 21 CFR 177.1520 and EU 10/2011 overall migration of 10 mg/dm². Resin compliance alone is insufficient. Stiffness and creep are assessed by ASTM D2990-17 compressive creep under 23°C and 50% RH. Published creep modulus data for R50035EE are limited. Panel deflection is validated on a prototype with granular fill of bulk density 800 kg/m³.
In large flat-bottom silo liners, the warpage mechanism is governed by crystallization shrinkage across the cooling window. The 0.935 g/cm³ density grade crystallizes at a higher temperature than 0.920 g/cm³ LLDPE. The part must be held in the mold under forced air until the wall reaches 70°C before release. Cooling rate between 120°C and 70°C is set at 2–3°C/min. A water mist is applied only after the mold surface drops below 90°C. Mold release is not sprayed on the powder-contact surface. The mold is treated with a semi-permanent release at 250°C cure. In flat sections with span-to-thickness ratio above 100:1, steel stiffener channels are clamped to the mold backside to reduce out-of-plane distortion. Thermocouple verification of the peak internal air temperature at 205–215°C is the main control point. Low PIAT below 195°C leaves unconsolidated powder in the peripheral flange.
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SABIC LLDPE R50035EE is a linear low-density polyethylene rotational moulding grade supplied by SABIC as a free-flowing powder with a typical density of 0.935 g/cm³ and a melt flow rate of 5.0 g/10 min at 190 °C/2.16 kg (ISO 1133-1:2022). The resin is intended for monolayer rotomoulded parts in which low-temperature ductility, environmental stress crack resistance, and moderate flexural stiffness are required. Typical converted articles include storage tanks, intermediate bulk container liners, agricultural chemical tanks, marine buoyancy components, and thick-walled industrial or playground housings. The designation sits within the SABIC R50035E product family; the EE suffix identifies the European-market grade variant with a defined stabilization package and release documentation. The product is normally supplied as natural or pre-coloured powder, and the converter adds colour concentrate in a polyethylene carrier before charging.
| Property | Test method | Typical value |
|---|---|---|
| Density | ISO 1183-1:2019 | 0.935 g/cm³ |
| Melt flow rate | ISO 1133-1:2022 | 5.0 g/10 min |
| Tensile stress at yield | ISO 527-2:2012 | 17 MPa |
| Tensile elongation at break | ISO 527-2:2012 | >300 % |
| Flexural modulus | ISO 178:2019 | 550 MPa |
| Environmental stress crack resistance, 100 % Igepal, F50 | ASTM D1693-15 | >1000 h |
Values are typical for natural material and are not specification limits. Published values for the EE variant may differ by colour and lot; the current supplier certificate of analysis controls the incoming specification. The resin is an ethylene/α-olefin copolymer with a linear backbone and short-chain branches. This architecture reduces crystallinity relative to high-density polyethylene and produces a more diffuse lamellar structure. In rotomoulded parts, the practical consequence is that the grade retains a larger fraction of tie molecules between crystalline regions, which is the known structural origin of improved stress crack resistance under ASTM D1693-15 and improved notched Charpy response at low temperatures relative to higher-density rotational moulding powders. Because comonomer type and branch distribution are proprietary, published data for this specific configuration are limited; however, the density and melt-flow-rate combination is documented in the supplier’s technical datasheet and is consistent with a medium-stiffness, high-ESCR LLDPE class.
In a rotational moulding tool, the part cools from the outside inward after the peak internal air temperature has been reached. A density of 0.935 g/cm³ places LLDPE R50035EE below the stiffness range of HDPE but above low-density polyethylene. For a flat tank wall of 6 mm nominal thickness, the lower crystallinity reduces shrinkage-induced warpage and allows the solidifying layer to densify without large internal void formation. At the same time, the flexural modulus of 550 MPa (ISO 178:2019) supplies enough sidewall rigidity for self-supporting vertical tanks of moderate capacity. Rotomoulders selecting this grade for a 2 000 L cylindrical water tank should nevertheless verify hopper or baffle support design because creep modulus under continuous hydrostatic load is lower than that of a 0.945 g/cm³ HDPE rotomoulding grade.
Production-scale experience on independent-arm carousel machines with 2.0–3.5 m swing diameters shows that the powder charges best when stored above 15 °C and below 60 % relative humidity. Mold release spray should be applied as a thin, uniform layer, because excess release agent can increase surface defects. The grade is normally processed at an oven air temperature of 260–320 °C, with a peak internal air temperature of 190–210 °C. The lower half of that range is preferred for thin-wall parts below 5 mm, while the upper half may be required for thick bosses, inserts, or ribs. The exact setpoint is tool- and machine-specific; a thermocouple inside the cavity is required to establish the oven residence time.
Rotational moulding densification involves powder sintering, coalescence, and bubble removal. For LLDPE R50035EE, the 5.0 g/10 min melt flow rate accelerates particle coalescence relative to 3.0 g/10 min grades, but it also lowers melt strength. When the peak internal air temperature is kept between 190 °C and 205 °C, the viscosity is low enough for bubbles to dissolve but high enough to limit localised thinning. If the mould is heated above 210 °C internal air temperature, oxidation can begin at the inner surface and create a degraded skin that reduces environmental stress crack resistance. If the peak internal air temperature is below 180 °C, pinholes and partial sintering can persist in thick corners. Cooling should proceed in stages: forced air to 80 °C internal temperature, followed by water mist or spray to 45 °C, and final air cooling to demolding. Quenching too rapidly from 100 °C can increase warpage and shrink marks, particularly on large flat panels.
Powder charging consistency depends on dry flow rate and particle size distribution. Rotational moulding powders are typically pulverized to a median particle size of 250–350 μm. Although the exact published particle size distribution for LLDPE R50035EE is limited, converter check-in tests should include ASTM D1895-17 apparent density and a standard funnel flow test. In deep pockets or narrow ribs, poor powder flow can cause localised bridging before the mould enters the oven. On shuttle machines with 2.5 m swing diameter, this failure mode appears as non-uniform wall thickness, bubbles at the inner radius, or incomplete fill at bosses. Pre-drying is not normally required for rotational moulding powder stored in sealed silos at relative humidity below 60 %. If storage exceeds 6 months or humidity exceeds 60 %, drying at 70–80 °C for 2–4 h in a desiccant dryer reduces surface moisture. Moisture above 0.05 wt% can create pinholes or surface roughness.
For parts with long flow paths or complex internal geometries, the 5.0 g/10 min melt flow rate of LLDPE R50035EE balances ease of flow against impact performance. In comparison with a 0.935 g/cm³ LLDPE rotomoulding grade having a lower melt flow rate of 2.0–3.0 g/10 min, this grade tends to produce fewer pinholes in ribs and inserts at the same peak internal air temperature. In comparison with a 7.0–10.0 g/10 min high-flow LLDPE, LLDPE R50035EE generally retains higher low-temperature impact and environmental stress crack resistance. The trade-off is a narrower processing window: the higher flow reduces the time available for bubble diffusion during cooling, so the cooling rate must not be so rapid that gas bubbles are trapped before solidification. In practice, multi-station shuttle machines often set the forced-air cooling fan to medium rather than maximum when running 8–12 mm walls, and the demolding time is extended by 15–20 % versus a 3.0 g/10 min grade.
Because LLDPE R50035EE is a rotomoulding powder rather than a film pellet, it is not suitable for blown film extrusion. The powder contains no slip or antiblock additives required for film handling; processing it in film would produce gels and poor bubble stability. The material is also not optimised for injection moulding. Although the melt flow rate permits injection, the low density and moderate modulus do not provide the stiffness expected from an injection moulding HDPE or polypropylene. Use in injection moulding should be limited to prototype or low-stress parts and should be preceded by a purge and mould-flow evaluation.
Compared with a typical HDPE rotomoulding powder of 0.944–0.952 g/cm³ and similar melt flow rate, LLDPE R50035EE shows lower flexural modulus, lower hardness, and higher low-temperature impact resistance. The HDPE grade is selected when higher creep resistance or hydrocarbon barrier is required; LLDPE R50035EE is selected when stress cracking resistance and ductility are dominant. Compared with a crosslinkable HDPE rotomoulding grade, LLDPE R50035EE does not require a curing stage and remains reprocessable as a thermoplastic, but it lacks the creep resistance and high-temperature stiffness associated with a crosslinked network. The linear polyethylene backbone also gives LLDPE R50035EE a more defined melting point than a branched low-density polyethylene, which assists in setting a repeatable peak internal air temperature.
| Material class | Density range | Melt flow rate range | Relative stiffness | Relative ESCR | Relative low-temperature impact |
|---|---|---|---|---|---|
| LLDPE R50035EE | 0.935 g/cm³ | 5.0 g/10 min | Moderate | High | High |
| HDPE rotomoulding grade | 0.944–0.952 g/cm³ | 3.0–6.0 g/10 min | Higher | Moderate | Lower |
| Crosslinkable HDPE grade | 0.940–0.950 g/cm³ | 6.0–9.0 g/10 min pre-cure | Higher after cure | Moderate | Moderate |
Ranges shown are typical class descriptions from rotomoulding grade technical literature and are not exact SABIC specifications. For direct material substitution, the current SABIC datasheet and part qualification data must be used.
The grade can be considered for food-contact applications only if the specific variant and colour package are listed in the supplier’s food-contact statement and the finished article is tested under the applicable national migration standard, such as EU Regulation 10/2011 or FDA 21 CFR 177.1520. No blanket food-contact claim applies to every lot or colour. The resin is manufactured under a quality management system certified to ISO 9001:2015; specific REACH and RoHS statements are provided in the supplier’s product stewardship bulletin. In chemical storage applications, the end use must be evaluated for the intended chemical at the service temperature because stress crack resistance is fluid-specific and temperature-dependent. Published data for this specific configuration are limited for aggressive oxidizing agents; immersion testing under ASTM D543-21 is required before specifying the material for agricultural or industrial chemical tanks.
LLDPE R50035EE should not be used above 60 °C continuous service under constant internal pressure without derating. Above this temperature, creep modulus and hydrostatic design stress decline, and the part may deform. The grade is not recommended for direct contact with strong oxidizing acids, free aromatic solvents, or high-octane oxygenated fuel blends at elevated temperature. When external UV resistance is required, a sufficient UV-stabilized variant or an approved UV masterbatch must be selected; the base natural powder does not provide long-term weathering by itself. If the material is stored outdoors or exposed to sunlight for more than 12 months, surface oxidation may affect odour, taste, or impact.