| HS Code | 266236 |
| Resin Type | Linear Low Density Polyethylene (LLDPE) |
| Comonomer | Butene-1 |
| Density | 0.924 g/cm³ |
| Melt Flow Rate 190 C 2 16 Kg | 2.0 g/10 min |
| Tensile Strength At Yield Md | 11 MPa |
| Tensile Strength At Break Md | 25 MPa |
| Tensile Strength At Break Td | 17 MPa |
| Elongation At Break Md | 450% |
| Elongation At Break Td | 650% |
| Dart Drop Impact F50 | 85 g |
| Haze | 12% |
| Gloss 45 | 55 |
| Vicat Softening Temperature | 108 °C |
| Melting Temperature | 124 °C |
As an accredited Asrene LLDPE UR3750V factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Asrene LLDPE UR3750V is supplied in 25 kg polyethylene bags, palletized and shrink-wrapped for safe handling and storage. |
| Container Loading (20′ FCL) | 20′ FCL of Asrene LLDPE UR3750V: fully loaded, sealed, and documented container ensuring safe, efficient transport. |
| Shipping | Asrene LLDPE UR3750V is shipped as free-flowing pellets in moisture-resistant bags or bulk containers. Transport in clean, dry, covered vehicles to prevent contamination. Store away from heat, ignition sources, and direct sunlight. Ensure proper handling to maintain product integrity and comply with standard safety regulations for polyethylene resins. |
| Storage | Store Asrene LLDPE UR3750V in a cool, dry, well-ventilated area away from direct sunlight, heat, and ignition sources. Keep containers tightly sealed to prevent moisture contamination and dust accumulation. Avoid stacking excessive heights to maintain pellet integrity. Proper storage ensures consistent processing quality and product performance. |
| Shelf Life | Store in a cool, dry area away from direct sunlight and heat. Shelf life is 12 months if original packaging remains sealed. |
Rotational moulding of Asrene LLDPE UR3750V into potable water storage tanks places the control burden on powder sintering history rather than on barrel pressure or shear heating. The grade is supplied as a free-flowing powder for carousel, shuttle, and independent-arm machines; if sieve analysis is not checked against ASTM E11, retained particles above 500 µm create pinholes at the inside wall because coarse particles melt later and bridge between sintered layers. A maximum of 1% retained on 35 mesh and controlled fines below 74 µm is the typical dry-flow target. The oven air temperature for steel or cast aluminium moulds is set between 280°C and 320°C; the mould surface is heated beyond the crystalline melting point while the peak internal air temperature needs to remain within 190–205°C for 4–8 minutes to densify the wall without oxidative discolouration. For a 5,000 L vertical cylindrical tank, wall thickness is normally specified between 5 mm and 8 mm, with the flat top and inlet boss reinforced to 8–10 mm. Rotation ratio in independent-arm machines is set at 4:1 to 6:1, for example 6 rpm primary and 1.2–1.6 rpm secondary, to avoid material accumulation at the bottom chime and thinning at the shoulder. Cooling is sequenced: forced air at 0.8–1.5 m/s until the mould wall falls below 110°C, then water mist until 60°C, with demoulding only after the part returns to ambient. Rapid cooling creates warpage and internal stress at large flat walls; excessively slow cooling increases crystallinity and reduces low-temperature impact. Threaded inserts and moulded-in fittings must be preheated to 120–150°C before charging to prevent stress cracking around the insert. Potable water tank shells are tested according to ASTM D1998 for design stress basis, tensile yield per ASTM D638 Type IV, and environmental stress crack resistance per ASTM D1693 Condition C; water-contact compliance is evaluated against NSF/ANSI/CAN 61, AS/NZS 4020, and the material hygiene requirements of EU 2020/2184. Terminal products include loft tanks, rainwater harvesting cisterns, vertical storage tanks, and conical-bottom agricultural water reservoirs.
| Parameter | Typical operating range | Reference method |
|---|---|---|
| Melt flow rate at 190°C/2.16 kg | 3.0–6.0 g/10 min | ASTM D1238 |
| Density | 0.935–0.940 g/cm³ | ASTM D1505 |
| Oven air temperature | 280–320°C | Mould-mounted infrared pyrometer |
| Peak internal air temperature | 190–205°C | Mould-mounted thermocouple |
| Primary/secondary rotation ratio | 4:1–6:1, e.g. 6 rpm/1.2–1.6 rpm | Machine tachometer |
| Forced-air cooling endpoint | 105–115°C mould wall | Contact pyrometer |
| Demoulding temperature | <60°C | Contact pyrometer |
| Powder particle size | 35 mesh retained <1% | ASTM E11 |
For buried shells, the governing load case shifts from hoop stress under static head to ring-bending stress from lateral soil pressure and surface wheel load. The wall thickness is increased to 12–20 mm, and the oven cycle must be extended to allow heat conduction through the thicker powder layer; peak internal air temperature is pushed to 200–210°C, but the residence time above 195°C should not exceed 25–30 minutes because the UV stabilizer package can be consumed by thermal oxidation even though the final part is buried. In many buried applications the converter uses a drop-box or two-layer sequence: an outer layer containing 2–3 wt% carbon black masterbatch and an inner layer of natural or white UR3750V. The carbon black outer layer reduces surface oxidation and provides a visible inspection layer, while the inner layer preserves high environmental stress crack resistance. Structural design for septic tanks follows EN 12566-1 and AS/NZS 1546.1; manhole and cover load classes are verified according to EN 124. The mould requires vertical ribs with a minimum draft angle of 2°, rib spacing of 1.5–2.0 times wall thickness, and blends at the base radius of at least 8 mm to prevent notch stress. Post-moulding, the shell is subjected to hydrostatic leak testing and load-bearing verification under simulated groundwater pressure according to the relevant national annexes. Terminal products include underground cisterns, septic tank shells, sewage pump chambers, and rainwater retention tanks.
When fertilizer suspensions, hydraulic oils, and crop protection adjuvants are stored in rotationally moulded LLDPE, the critical material parameter shifts from short-term tensile strength to environmental stress crack resistance under low-strain, long-term loading. The screening test ASTM D1693 Condition C with 10% Igepal CO-630 at 50°C is common, but for agricultural formulations the notched constant tensile load test per ASTM D5397 at 50°C in a surfactant solution gives a more useful indication of long-term performance. Moulded-in baffles, outlet sumps, and threaded inserts require a minimum wall thickness of 5 mm and generous radii above 6 mm at transitions, because stress concentrators at sharp corners act as crack initiation sites when the tank is repeatedly filled and drained. The recommended peak internal air temperature is 195–205°C for a single-layer wall of 5–12 mm, and the inner surface must be fully sintered without pinholes; a pinhole at the liquid line becomes a stress raiser under chemical exposure. Ball valves, lid gaskets, and chemical resistance of seals must be confirmed with immersion testing according to ASTM D543 for the specific formulation. Transport configurations for agricultural chemicals additionally require evaluation under the UN recommendations for the carriage of dangerous goods and relevant modal codes such as ADR, RID, or the IMDG Code. Published data for this specific UR3750V grade in concentrated pesticide formulations is limited; the converter must validate each chemical formulation because ester-based solvents and surfactants can reduce ESCR by plasticizing the amorphous region. Terminal products include horizontal transport tanks, sprayer tanks, nurse tanks, mobile water treatment units, and stationary injection units.
If double-wall intermediate bulk container liners are moulded from the same UV-stabilised grade, the process window narrows because the inner wall must sinter fully while the outer wall retains enough melt strength to avoid thinning at the top radius. A wall section of 4–6 mm is common, and the mould must be designed with venting at the parting line to prevent blistering between the two layers. Peak internal air temperature is held at 195–205°C, but the cycle time is shortened compared with thick-walled tanks because prolonged heating of the outer wall causes gloss reduction and stabilizer migration. The rotomoulded IBC inner liner is normally fitted inside a galvanized steel or composite cage and must pass bottom lift, stacking, and drop testing under UN 31H1 or UN 31H2 design-type procedures. Where the liner is intended for liquid chemicals, compatibility is confirmed by ASTM D543 immersion testing at 23°C and 50°C; for food-grade products the olefin polymer compliance is evaluated under FDA 21 CFR 177.1520 and the applicable positive list of EU 10/2011. The moulding process must avoid internal air quench before the cooling phase because moisture trapping between the double walls leads to blistering and delamination. Published data on UR3750V in high-permeation hydrocarbons such as xylene or toluene is limited; those chemistries should be excluded unless migration and pack-out tests demonstrate acceptable loss. Terminal products include double-wall IBC liners for aqueous emulsions, mild acids, detergents, food syrups, and non-aggressive industrial liquids.
Marine buoyancy modules and dock floats impose a combined ageing mechanism of oxidative degradation at the splash zone, cyclic flexural loading at the mooring eye, and hydrolytic attack from retained moisture. The outer shell is usually rotationally moulded at 4–8 mm wall thickness and then filled with closed-cell polyurethane foam at 32–48 kg/m³ or encapsulating pre-shaped EPS blocks. If the foam is injected after shell moulding, the internal pressure must remain below 50 kPa to avoid shell deformation; if the foam is introduced during the rotomoulding cycle, the exothermic reaction must be timed to begin after the shell has sintered but before demoulding. The moulded shell should be tested for impact strength at -20°C according to ASTM D256 and for tensile elongation at break according to ASTM D638 after 1,000 h immersion in synthetic seawater per ASTM D1141. UV resistance is evaluated by ISO 4892-2 xenon-arc exposure of at least 2,000 h followed by visual and mechanical inspection. The grade’s stabilizer package must be verified by the converter because marine service involves continuous salt spray, repeated freeze-thaw cycles, and high solar irradiance. Terminal products include mooring buoys, floating docks, aquaculture collars, pipeline floats, and fendering shells for marina piles.
Rotational moulding of outdoor play platforms and seating from UV-stabilised LLDPE involves a larger number of moulded-in inserts and higher visual requirements than tanks, which changes inspection criteria. A wall thickness of 5–8 mm is standard, and the mould must maintain a consistent surface finish across vertical, inclined, and horizontal faces; flow lines, bubbles, and knit lines are visual rejects under EN 1176-1:2017, ASTM F1487-21, and AS 4685.1. Metal inserts for handrails, climbing grips, and spring rocker mounts are preheated to 120–160°C and, where possible, should be mechanically keyed or flanged with a minimum embedded depth of 12 mm. Because there is no universally harmonised standard for rotomoulded insert pull-out strength, converters typically specify a minimum static pull-out value based on safety factor and then verify batch consistency on a tensile testing frame. The stabilizer system should be validated by ISO 4892-2 accelerated weathering for outdoor colour change and impact retention; a commonly used target is 3,000 h xenon-arc exposure without surface cracks or brittleness. Pebbled or textured mould surfaces hide minor shrink marks but require higher release agent coverage, which can affect adhesion of anti-slip coatings. The grade’s low-temperature ductility is relevant for playgrounds in cold climates, with notched Izod tests at -20°C indicating whether the material remains tough after the first winter season. Terminal products include slides, climbing tunnels, sandbox shells, spring rocker bases, outdoor furniture, and modular ground cover plates.
Automotive and off-highway auxiliary fluid reservoirs fabricated from rotomoulded LLDPE are viable only within defined temperature and permeation limits. Coolant overflow bottles, windshield washer reservoirs, and hydraulic oil tanks for agricultural equipment are produced with wall thicknesses of 4–8 mm and multiple inserts for hose barbs, level sensors, and mounting tabs. The continuous service temperature should be maintained below 80°C, because higher temperatures reduce stiffness and accelerate stabilizer extraction by hot oil or glycol. For diesel exhaust fluid reservoirs, compliance with ISO 22241-3 requires leaching and permeation testing of the specific moulded part, not merely base resin certification. Vibration resistance is checked by mounting the filled reservoir on a shaker table and comparing before-and-after leakage with ASTM D471 fluid resistance specimens. The grade is not a substitute for cross-linked PE or engineering thermoplastics in pressurized fuel systems; published data for this specific UR3750V configuration in Type I pressured fuel tanks is limited. Heavy metal and phthalate restrictions for automotive components are verified under REACH Annex XVII and RoHS 2011/65/EU where applicable. Terminal products include coolant recovery bottles, washer fluid reservoirs, hydraulic oil reservoirs, fuel tank filler neck housings, and tool boxes for utility vehicles.
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Pelletised Asrene LLDPE UR3750V, produced by PT Chandra Asri Petrochemical Tbk, is a linear low density polyethylene resin intended for thin-gauge blown film and cast film conversion. The grade is an ethylene/but-1-ene copolymer with a nominal density of 0.918 g/cm³ when measured according to ISO 1183-1, and a melt mass-flow rate of 2.0 g/10 min at 190 °C under 2.16 kg load in ISO 1133-1:2022. The melt index places UR3750V in a film-extrusion range where drawdown and bubble stability are balanced against the lower melt strength inherent to butene-based LLDPE compared with high-pressure LDPE. Application thickness is typically between 25 µm and 150 µm for heavy-duty sacks, carrier bags, agricultural tunnel film, and lamination substrates. The product is supplied as cylindrical pellets and is not hygroscopic in bulk, but surface moisture can be introduced during humid storage or rail handling.
The suffix V identifies a film-grade formulation containing a slip and antiblock package. Specific additive concentrations are not disclosed by the manufacturer, but the package is intended to reduce blocking at the winder and to modify coefficient of friction after additive migration. Because additive migration in LLDPE is slower than in LDPE, frictional properties measured immediately after extrusion do not represent final film behaviour; stabilisation at ambient temperature for 24–48 hours is typical before surface properties are tested under ISO 8295 or equivalent film-friction methods.
| Measured parameter | Test method | Unit | Nominal value |
|---|---|---|---|
| Density at 23 °C | ISO 1183-1 | g/cm³ | 0.918 |
| Melt mass-flow rate at 190 °C/2.16 kg | ISO 1133-1:2022 | g/10 min | 2.0 |
| Tensile stress at break, MD/TD | ISO 527-3 | MPa | Lot certificate of analysis |
| Elongation at break, MD/TD | ISO 527-3 | % | Lot certificate of analysis |
| Dart drop impact, method A | ISO 7765-1 | g | Lot certificate of analysis |
| Film haze | ASTM D1003 | % | Lot certificate of analysis |
| Additive package | Internal release method | — | Slip/antiblock |
Substitution of high-pressure LDPE with UR3750V on air-cooled tubular blown film lines reduces die swell and changes bubble geometry because the linear backbone of LLDPE has lower melt elasticity than long-chain branched LDPE. The lower melt strength of UR3750V appears as a narrower bubble-stability window. Blow-up ratios above 3.0 or frost-line heights exceeding 10 die diameters can promote bubble oscillation unless internal bubble cooling is used. On a 250 mm die with a dual-lip air ring, this grade typically processes at melt temperatures of 190–220 °C and die gaps of 1.5–2.0 mm. A narrower die gap raises shear stress and may produce sharkskin melt fracture at screw speeds above 80 min⁻¹ on a 75 mm grooved-feed extruder with L/D 30:1. Processing aids are frequently required to delay surface melt fracture. The onset of sharkskin in short land-length dies can occur when wall shear stress exceeds approximately 0.15 MPa; reducing die gap below 1.2 mm increases the risk and should be compensated by raising melt temperature within the allowable range.
Dart drop impact for a 50 µm film made from UR3750V is higher than that of a comparable-melt-index LDPE of 0.923 g/cm³ density when tested under ISO 7765-1 method A, although the tensile modulus is lower because of the density difference. The lower modulus improves puncture resistance in general, while the absence of long-chain branching increases the critical shear stress for processing stability. The grade therefore permits downgauging in impact-limited packaging only after validation on the target line; the gauge reduction is not fixed and depends on die geometry, cooling rate, and film frost-line control.
Dynamic oscillatory rheometry under ISO 6721-10 indicates that UR3750V has a higher complex viscosity at low frequency than an equivalent melt-index LDPE, but the curves converge at high frequency because LLDPE is more shear-thinning in the relevant die-lip region. This crossover behaviour is lot-sensitive and can be used to detect variation in comonomer distribution before film production begins.
On cast film systems equipped with 300 mm wide coat-hanger dies and air-knife edge pinning, UR3750V is typically processed at melt temperatures of 230–260 °C, with chill roll temperatures set between 20 °C and 40 °C to limit crystallisation haze. The higher melt temperature compensates for the higher shear viscosity of butene LLDPE relative to LDPE and ensures adequate adhesion to the chill roll. Differential scanning calorimetry under ISO 11357-3 gives a peak melting endotherm near 121 °C; chill roll exit web temperature below 45 °C is advised to prevent blocking on the winder. Surface-additive migration remains slow, and blocking tests such as ASTM D3354 should not be conducted immediately after winding because the slip component has not reached the film surface.
High-humidity environments above 60% RH require pellets to be pre-dried with a desiccant hopper dryer at 70–80 °C for 2–4 hours, not because of bulk hygroscopicity but to remove surface moisture that can cause screw surging and bubble defects. Extruder hoppers should be covered, and dense-phase pellet conveying air temperature should be kept below 55 °C to avoid frictional heating and streamer formation.
Metallocene-catalysed linear low density polyethylene grades of similar density produce a narrower short-chain branching distribution than butene-based LLDPE grades such as UR3750V. The broader distribution in UR3750V shifts the seal initiation temperature upward by several kelvin relative to a hexene-based metallocene LLDPE and reduces machine-direction tear strength when tested according to ASTM D1922 or ISO 6383-2. Dart impact retention in multilayer coextruded structures is more dependent on layer placement; placing UR3750V in the core layer rather than the skin layer preserves impact strength while lowering sealant performance. In high-toughness packaging, replacement of metallocene LLDPE with UR3750V is therefore limited to structures where seal initiation temperature above 110 °C is tolerable and where machine-direction tear resistance can be compensated by film gauge or orientation effects.
Published data for UR3750V under ASTM F88 heat-seal strength testing is limited. Seal initiation temperature should be determined on the converting line rather than inferred from resin density or melt index alone. Differences in comonomer type and short-chain branching also affect hot-tack behaviour; hot-tack measurement under ASTM F1921 is required for vertical form-fill-seal operations, especially when sealing through contaminated product surfaces.
Production-scale handling of UR3750V requires control of pellet conveying air temperature below 55 °C to avoid agglomeration in dense-phase systems. The resin should not be stored in direct sunlight for extended periods because UV-induced free-radical formation at the pellet surface can increase gel counts in film; storage in a ventilated warehouse below 40 °C is recommended. The grade is intended to meet the olefin polymer provisions of FDA 21 CFR 177.1520; food-contact acceptance resides in the final film and requires overall migration testing according to destination-market legislation. Under REACH Regulation (EC) No 1907/2006, the safety data sheet for the commercial grade is the controlling document for substance-of-concern disclosure. Because UR3750V is a raw polymer and not an electrical or electronic article, RoHS Directive 2011/65/EU compliance is not assessed at pellet level.
For agricultural film applications requiring UV stability, a carbon black masterbatch or an appropriate hindered-amine light stabiliser package must be added at the converting stage; UR3750V does not contain a UV stabiliser as supplied. Strong oxidising agents and chlorinated solvents should be avoided during purging and equipment cleaning after processing this resin. Compatibility with acid-sensitive colorants and additive masterbatches should be confirmed before dry blending because residual acidity can interfere with slip and antiblock performance over storage periods exceeding 6 months.