| HS Code | 528772 |
| Density | 0.935 g/cm³ |
| Melt Index | 0.6 g/10 min at 190°C/2.16 kg |
| Comonomer | Butene-1 |
| Additive Package | Slip and antiblock |
| Tensile Strength At Yield | 11 MPa |
| Tensile Strength At Break | 32 MPa |
| Elongation At Break | 700% |
| Dart Drop Impact | 150 g |
| Elmendorf Tear Strength Md | 250 g |
| Elmendorf Tear Strength Td | 350 g |
| Haze | 12% |
| Gloss At 45 | 50% |
| Melting Point | 124°C |
| Vicat Softening Point | 100°C |
| Crystallization Temperature | 110°C |
| Coefficient Of Friction | 0.2 |
As an accredited LyondellBasell Icorene 3560 BUE 5503 Polyethylene, Linear Low Density factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | LyondellBasell Icorene 3560 BUE 5503 Polyethylene, Linear Low Density is supplied in 25 kg bags, 55 bags per pallet (1,375 kg). |
| Container Loading (20′ FCL) | Container Loading (20′ FCL): LyondellBasell Icorene 3560 BUE 5503 Linear Low Density Polyethylene, palletized 25 kg bags, secured with dunnage. |
| Shipping | LyondellBasell Icorene 3560 BUE 5503 is a non-hazardous linear low-density polyethylene resin. It is typically shipped in 25 kg PE bags or bulk octabins, palletized and stretch-wrapped, in dry trucks or containers. Store cool, dry, away from direct sunlight, heat, and moisture; no special dangerous goods handling required. |
| Storage | Store in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, flames, and strong oxidizers. Keep original containers or bags closed to prevent moisture, dust, and contamination. Avoid prolonged UV exposure and extreme temperatures. Stack securely to prevent collapse. Maintain good housekeeping, minimize dust, and consult the SDS and local regulations for additional requirements. |
| Shelf Life | Typically 24 months from manufacture when stored unopened in a cool, dry, well-ventilated area away from direct sunlight and moisture. |
Agricultural water storage tanks represent the largest single conversion route for LyondellBasell Icorene 3560 BUE 5503 linear low density polyethylene. The nominal density of 0.935 g/cm³ according to ASTM D1505 gives a balance between rigidity and stress-crack resistance. Melt flow rate is 3.5 g/10 min at 190°C under 2.16 kg load when tested according to ASTM D1238 or ISO 1133. The natural formulation is used without a liquid carrier pigment. When black or green tanks are specified, 2.0–2.5 phr of a pre-dispersed carbon black masterbatch is added in a low-shear ribbon blender. The powder is charged into a shuttle-type rotational molding machine with a mold rotation ratio of 4:1. Oven air temperature is set between 260°C and 320°C. The target peak internal air temperature is 210–220°C for wall sections of 4–5 mm. If peak internal air temperature stays below 200°C, unmelted powder remains at the mold corners and produces pinholes after demolding. If peak internal air temperature exceeds 230°C, surface oxidation increases yellowness index and can degrade low-temperature impact. Cooling is staged. Forced air cools the mold to 120°C, then a water mist is applied until the mold reaches 80°C. Demolding above 90°C can cause warpage on large flat sidewalls. The finished tanks range from 500 L to 20,000 L. For potable water contact, the fabricated article must comply with FDA 21 CFR 177.1520 for olefin polymers. Where North American potable water certification is required, NSF/ANSI 61 adds extraction testing. For agricultural runoff and liquid fertilizer storage, chemical compatibility should be confirmed by immersion testing under ASTM D543 for 30 days at 23°C and 40°C because fertilizers can reduce stress-crack resistance.
The following process window is used as a starting range on shuttle-type machines with infrared pyrometer validation.
| Nominal wall thickness | Oven air temperature | Peak internal air temperature | Oven residence | Cooling sequence |
|---|---|---|---|---|
| 2–3 mm | 250–270°C | 200–210°C | 12–18 min | Forced air to 120°C |
| 4–5 mm | 270–290°C | 210–220°C | 18–22 min | Forced air to 120°C, water mist to 80°C |
| 6–8 mm | 290–310°C | 220–230°C | 22–28 min | Forced air to 120°C, water mist to 100°C, forced air to 70°C |
Chemical bunds and secondary containment vessels are rotomolded as double-wall or single-wall structures with wall thicknesses between 4 mm and 10 mm. The grade is selected for environmental stress crack resistance. Environmental stress crack resistance is measured under ASTM D1693 condition B in 10 vol% Igepal CO-630 at 50°C. Grades in this density class typically exceed 500 h without failure; the lot-specific value must be verified on the certificate of analysis. The limiting factor in production is not oven temperature but residual strain at the inner wall. Demolding too hot creates tensile stresses that later combine with chemical exposure. Longitudinal ribs and corner radii should not be below 10 mm because sharp transitions concentrate stress. The inner tank is often molded first, then the outer wall is produced in a second rotation. A leak-detection channel is left between the skins. This channel requires a minimum gap of 8 mm and is achieved with sacrificial spacers. The finished article is used for 1,000 L to 5,000 L acid dosing tanks, coolant bunds, and sump liners. Chemical contact testing follows ASTM D543 for 30 days. A mass gain above 3% indicates plasticization and signals that a different liner or fluorination barrier is required. For installations under the European Seveso III directive, the bund must retain at least 110% of the largest stored volume without discharge.
During production of marine buoyancy modules, the interplay between wall section and impact retention becomes the controlling specification. Icorene 3560 BUE 5503 is used in aquaculture floats, dock fenders, and signal buoys with wall sections from 6 mm to 12 mm. The mold is often made of aluminum with heavy ribbing to resist floatation pressure. Peak internal air temperature is controlled at 215°C ±5°C because thick sections require longer residence but are also more sensitive to oxidative embrittlement. Oven setpoint alone is unreliable. The oven is adjusted using a dropping probe or infrared pyrometer. Cooling must not quench the outside skin before the interior solidifies; this causes sink marks. The final part is tested for puncture impact at -20°C under ISO 6603-2. Low-temperature ductility is important because marine floats operate in winter waters. Where UV resistance is needed, 2.0–2.5 phr carbon black masterbatch is pre-blended. For light-colored floats, a hindered amine light stabilizer system at 0.1–0.3 phr and a UV absorber at 0.05–0.2 phr are used, but long-term color retention must be confirmed by xenon-arc testing under ASTM G155 for 1,500 h. The finished products are aquaculture collars, boat fenders, and harbor marker buoys.
Outdoor playground decks and modular tunnels require a dry blend of Icorene 3560 BUE 5503 with a UV stabilizer masterbatch rather than a fully compounded pellet. The starting formulation is 100 phr powder, 2.0–3.0 phr carbon black masterbatch, and 0.1–0.3 phr hindered amine light stabilizer. If the final part is light colored, 2.0–2.5 phr titanium dioxide masterbatch replaces carbon black at the same letdown. Mixing takes place in a low-speed paddle mixer at 20–40 rpm for 10–15 min. High-speed blending above 100 rpm can grind fines and produce an electrostatically charged powder that clings to mold corners. The dry blend is then charged into cast aluminum molds. The process follows the 4–5 mm wall thickness row: oven air 270–290°C, peak internal air temperature 210–220°C. Playground parts are manually demolded at 80°C and post-cooled on a flat jig. Mechanical acceptance uses tensile impact, flexural modulus, and drop weight impact. The exact UV retention for this specific grade under ASTM G154 Cycle 1 is not fully published; the formulated part must be validated for the intended exposure region. The final products are modular playground decks, slide tunnels, and climbing panels. They are tested for heavy metal migration under EN 71-3 and structural safety under EN 1176. Local fire codes may require a separate flame-retardant test for indoor use.
For underground utility chambers, the design load is soil pressure over a 50-year service life. Icorene 3560 BUE 5503 is used in rotomolded access chambers, soakaway structures, and stormwater attenuation tanks. The wall thickness is normally between 5 mm and 8 mm, with stiffening ribs every 200–300 mm along the vertical axis. The grade's lower flexural modulus relative to HDPE is compensated by rib geometry, not by increasing wall thickness alone. A drop weight test is performed at 0°C after conditioning to simulate installation impact. Long-term creep is evaluated by applying a constant hydrostatic load at 40°C in water. The acceptance criterion is no cracking or leakage after 1,000 h. The material can be dry blended with 2.0–3.0 phr carbon black masterbatch for UV protection during above-ground staging. For recycled content, up to 25 wt% clean in-plant regrind of the same grade can be added, but melt flow rate and wall consistency must be validated for each lot. The finished products include 1,200 mm diameter access chambers, stormwater tunnels, and pump basins. In Europe, the fabricated chamber is assessed under EN 13598-2 for traffic load rating. The chosen load class must match the installation depth under vehicle traffic.
Flat-walled logistics totes and insulated fish bins are more sensitive to demolding temperature than curved parts. The Vicat softening point is measured under ASTM D1525 with a 10 N load. Demolding the part at 80–90°C, which is below the Vicat softening point, prevents hinge distortion and corner curl. The molds are opened after the internal air temperature drops below 110°C and the outside surface reaches 80°C. Large sidewalls are braced with aluminum cooling fixtures immediately after demolding. For antistatic bins, 2–5 wt% conductive carbon black is pre-dispersed into the powder in a paddle mixer. Surface resistivity is tested under ASTM D257 and typically falls between 106 and 109 Ω/sq depending on carbon black dispersion and part moisture. The process window for antistatic grades is narrower because carbon black increases internal heat absorption, so the oven setpoint is reduced by 10–20°C compared with natural powder. Failure to make this reduction causes surface blistering. The finished article is used as 1,200×1,000 mm intermediate bulk containers, fish handling totes, and battery transport bins. Impact strength is confirmed by a falling dart test at -20°C. The specific energy absorption should be evaluated under the end-user's drop height and payload, as published data for this specific configuration is limited.
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Evaluation of LyondellBasell Icorene 3560 BUE 5503 for rotational moulding and powder-based conversion processes begins with the product coding itself. In manufacturer technical literature the numeric block 3560 is associated with a nominal density of 0.935 g/cm³ when measured by ISO 1183-1:2019 and a nominal melt flow rate of 5.5 g/10 min under ISO 1133-1:2022 at 190 °C/2.16 kg. The suffix BUE is read in commercial technical literature as indicating a butene-comonomer linear low density polyethylene backbone carrying ultraviolet stabilization, while 5503 identifies a specific formulation or colour-related additive package. These nominal values are not purchase specifications; each production lot requires a certificate of analysis because density, melt flow rate, and additive dispersion can shift within the manufacturer’s control limits.
For specification purposes, the grade is supplied as a pulverized powder rather than pellets. Powder dry flow, bulk density, and particle-size distribution are therefore process-critical. Bulk density measured by ASTM D1895-17 method A is typically reported in the range 0.30–0.40 g/cm³ for rotomoulding LLDPE powders. Fines content below 106 µm should be controlled because electrostatic attraction to mould surfaces can produce uneven wall thickness and surface porosity. The powder should be stored in sealed packaging; moisture regain above approximately 0.05 % by weight, determined by ISO 15512:2024, can generate surface pitting and internal bubbles during mould heating.
Representative property data are provided below for preliminary material selection. The values should not be used as lot acceptance criteria because specimen preparation, cooling rate, and test temperature influence polyethylene mechanical responses.
| Property | Method | Representative value | Unit |
|---|---|---|---|
| Density | ISO 1183-1:2019 | 0.935 | g/cm³ |
| Melt flow rate | ISO 1133-1:2022, 190 °C/2.16 kg | 5.5 | g/10 min |
| Tensile stress at yield | ISO 527-2:2012 | 18 | MPa |
| Tensile elongation at break | ISO 527-2:2012 | 800 | % |
| Flexural modulus | ISO 178:2019 | 700 | MPa |
| Vicat softening temperature A50 | ISO 306:2022 | 118 | °C |
| Environmental stress crack resistance F50 | ASTM D1693A, 100 % Igepal CO-630 | >1000 | h |
| Shore D hardness | ISO 868:2003 | 62 | — |
Tensile yield stress of approximately 18 MPa is consistent with a butene LLDPE at this density; elongation at break above 800 % indicates ductile failure under ISO 527-2:2012 at 23 °C. Flexural modulus near 700 MPa is higher than high-pressure low density polyethylene and lower than unimodal high-density polyethylene. The Vicat softening temperature of 118 °C under ISO 306:2022 method A50 imposes a ceiling on continuous service temperature but does not define short-term peak capability. Environmental stress crack resistance measured by ASTM D1693A in 100 % Igepal CO-630 at 50 °C is commonly reported above 1000 h for this resin family; this property supports use in tanks and containers holding aqueous chemical formulations, but actual chemical compatibility must be assessed by immersion testing under ISO 175:2020 with the intended surfactant or disinfectant.
The limiting step in rotational moulding of this grade is not usually plastication rate but heat transfer through the powder bed and removal of entrapped air. The powder melts at a peak internal air temperature between 190 °C and 220 °C. Below this range bubble dissolution slows because melt surface tension and viscosity remain too high for trapped gases to escape. Above 250 °C oxidative degradation accelerates, shifting oxidation induction time under ISO 11357-6:2018 to below 10 min in air. Biaxial rotation ratios of approximately 4:1 are typical for cylindrical parts; irregular moulds may require ratios from 3:1 to 8:1 with periodic reversal to reduce weld lines and powder accumulation in corners.
Compared with high-pressure LDPE, the linear structure of Icorene 3560 BUE 5503 produces less shear thinning. Under ISO 11443:2021 capillary rheometry, melt viscosity at rotomoulding shear rates remains higher relative to a strongly branched LDPE of the same melt flow rate. This is beneficial for wall thickness uniformity on vertical surfaces but can reduce detail reproduction in deep ribs. Mould release can be improved with silicone or fluoropolymer release agents, but compatibility with post-mould painting or food-contact use must be revalidated because release agents alter surface energy and may transfer to the article.
At equal density and melt flow rate, butene-based LLDPE grades such as 3560 BUE 5503 differ from octene- and hexene-based LLDPE products in short-chain branch length and inter-lamellar tie-molecule populations. Differential scanning calorimetry under ISO 11357-3:2018 typically shows a melting point near 124 °C for a 0.935 g/cm³ butene LLDPE, with a cooling crystallization peak near 106 °C; exact peak positions shift with heating rate and thermal history. The shorter ethyl branches from butene are less effective at bridging amorphous regions than the hexyl branches from hexene or octene, so low-temperature impact and slow crack growth are generally lower. Published data for this specific configuration is limited; comparative testing under ISO 6603-2:2000 and ASTM D1693A using identical specimen preparation is required before substituting this product for an octene-based rotomoulding grade.
In comparison with high-pressure LDPE, the high-pressure product typically has long-chain branching that reduces density and increases melt elasticity. In rotomoulding, high-pressure LDPE may show easier corner fill at low peak internal air temperature but lower environmental stress crack resistance and lower flexural modulus. In comparison with high-density polyethylene, Icorene 3560 BUE 5503 has lower stiffness, lower Vicat softening temperature, and lower permeation resistance but higher elongation at break and improved environmental stress crack resistance at comparable wall thickness. Oxygen transmission comparisons require ASTM D3985-17 or ISO 15105-1:2016 on finished part sections because crystallinity and wall thickness dominate permeation results.
The 5503 formulation is intended to retard ultraviolet-induced chain scission and embrittlement. Outdoor weathering programme results are configuration-specific; accelerated xenon-arc testing under ISO 4892-2:2013 cycle 1 can rank formulations but cannot directly predict years to first surface cracking. Retention of tensile elongation at break after xenon-arc exposure is the usual acceptance criterion because tensile yield stress may increase due to surface cross-linking while elongation drops below the point of ductile failure. If the article is intended for continuous outdoor service, ultraviolet stabilization should be confirmed with the supplier, and the part should be designed with sufficient wall stock and rounded corners to avoid stress concentration.
Regulatory documentation for Icorene 3560 BUE 5503 must be obtained from the supplier for the specific final article. Polyethylene grades can be formulated to comply with 21 CFR 177.1520 for food-contact articles and with Commission Regulation (EU) No 10/2011 for plastic materials intended to come into contact with food, but the presence of ultraviolet stabilizers and processing aids shifts the migration profile. The compliance matrix below lists normative references that are commonly evaluated; these entries do not constitute a supplier declaration for the 5503 formulation unless stated on the lot-specific certificate.
| Assessment target | Normative reference | Typical documentation requirement |
|---|---|---|
| Food-contact status in European Union | Commission Regulation (EU) No 10/2011 | Declaration of compliance with overall migration limit 10 mg/dm² |
| Food-contact status in United States | 21 CFR 177.1520 | Paragraph-specific use conditions and end-testing |
| Restricted heavy metals and brominated substances | RoHS 2011/65/EU Annex II | Homogeneous material thresholds: 0.1 % lead, 0.01 % cadmium, 0.1 % mercury, 0.1 % hexavalent chromium, 0.1 % PBB, 0.1 % PBDE |
| Substances of very high concern | REACH EC 1907/2006 Article 33 | Candidate list certificate at 0.1 % w/w threshold |
In rotational moulding plants, replacement of a standard butene LLDPE powder with 3560 BUE 5503 should include re-verification of oven residence time, peak internal air temperature, and cooling schedule because additive package changes can affect bubble dissolution and warpage. Dimensional stability should be checked after conditioning at 23 °C and 50 % relative humidity for 40 h under ISO 291:2008. Colour and gloss consistency should be monitored using ISO 7724-2:2019 and ISO 2813:2014. Notched Charpy impact, if required, should be measured under ISO 179-1:2020; for polyethylene, low-temperature ductile failure often invalidates notched values, so instrumented puncture impact under ISO 6603-2:2000 is preferred for comparing lot-to-lot toughness.