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SABIC LLDPE RVL4068

    • Product Name: SABIC LLDPE RVL4068
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 639667
    Density 0.940 g/cm³
    Melt Flow Rate 190 C 2 16 Kg 4.0 g/10 min
    Tensile Stress At Yield 19 MPa
    Elongation At Break 800%
    Flexural Modulus 750 MPa
    Shore D Hardness 58
    Vicat Softening Temperature 125 °C
    Melting Temperature 129 °C
    Brittleness Temperature -70 °C
    Escr 100 Igepal >1000 h

    As an accredited SABIC LLDPE RVL4068 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing SABIC LLDPE RVL4068 is packaged as virgin pellets in 25 kg polyethylene bags, palletized and stretch-wrapped for safe delivery.
    Container Loading (20′ FCL) Container Loading (20′ FCL) for SABIC LLDPE RVL4068: 20-foot full container load, securely stowed, dry bulk packaging, protected from moisture and contamination.
    Shipping SABIC LLDPE RVL4068 is a linear low-density polyethylene resin supplied as free-flowing pellets. It is shipped in sealed multi-layer bags, bulk bags, or silo trucks. Not classified as hazardous, but should be stored dry, away from heat, ignition sources, and direct sunlight during transport.
    Storage Store SABIC LLDPE RVL4068 in a clean, dry, and well-ventilated area. Keep the material in its original unopened packaging or sealed silos to prevent moisture pickup and contamination. Avoid direct sunlight, high temperatures, and open flames or ignition sources. Ideal storage temperature is below 40°C; use within six months to maintain consistent processing and end-product quality.
    Shelf Life Store in a cool, dry area away from direct sunlight. Shelf life is 12 months from delivery if packaging remains unopened.
    Application of SABIC LLDPE RVL4068

    For potable water storage tanks rotomoulded from SABIC LLDPE RVL4068, service conditions under ANSI/NSF/CAN 61-2023 for drinking water contact are combined with olefin polymer compliance anchored to FDA 21 CFR 177.1520(c) 2.1 for US-manufactured vessels and EU Regulation (EC) No 10/2011 for articles placed on the European market. The resin’s melt-flow rate of 4.0 g/10 min at 190°C/2.16 kg (ISO 1133-1:2022) and density of 940 kg/m³ (ISO 1183-1:2019) require dry-flow powder screened to 35 mesh (500 µm) for uniform wall-thickness control on carousel-type rotational moulding machines with fabricated steel or cast aluminium moulds. The formulation is a 100 wt% virgin micropowder dry-blend with 0.8–1.2 wt% of a food-contact-approved hindered phenolic/phosphate antioxidant masterbatch; closed-loop regrind from the same certified article is held at or below 20 wt% only where national certification documents permit recycled rework in non-potable outer layers. Heating in forced-air ovens at 260–290°C and rotation ratios of 4:1 primary/2:1 secondary bring the Peak Internal Air Temperature (PIAT) to 200–210°C. Finished wall sections between 4 mm and 6 mm are cooled by forced air to 85°C followed by water mist to reduce warpage before demoulding; vertical water storage tanks of 200 L to 20,000 L, loft tanks, rainwater harvesting vessels, and transport tanks are the principal terminal product forms.

    The processing boundary is narrow: PIAT below 190°C leaves unmelted particle cores that reduce notched Charpy impact values under ISO 179-1:2020, while PIAT above 220°C accelerates stabilizer consumption and can shift colour and odour in drinking-water service. On carousel machines with multiple arms, the cooling phase is the longer cycle segment; potable-water tank moulders typically program 12–18 min of forced-air cooling before misting to limit internal stress at bosses and filling necks. Field failure data from production-scale tank lines show that most leaks originate at rotationally moulded-in threaded fittings rather than in the tank shell; insert melt temperature must exceed 210°C locally by extending soak time near fitting bosses. ASTM D1998-21 is used for upright polyethylene tank performance, and tank wall thickness is measured ultrasonically around the equatorial weld line where biaxial flow is slowest.

    What Changes When Diluted Fertilizer Is Held at 40°C for 90 Days?

    Agricultural sprayer and chemical storage vessels built from RVL4068 rely on the resin’s environmental stress-crack resistance, characterized by ASTM D1693-15 condition B at 1,000 h without failure, rather than short-term burst strength when exposed to dilute ammonium nitrate, urea, or glyphosate formulations at elevated ambient temperatures. The regulatory anchor for liquid dangerous goods transport in rotationally moulded IBCs is the UN 1H1 design type under UN Model Regulations Chapter 6.5, supplemented by ADR 6.5.2 for European road transport and US 40 CFR Part 165 for pesticide container integrity. A typical dry-blend for opaque agricultural tanks contains 100 wt% virgin RVL4068 powder with 2.0–3.0 wt% carbon black masterbatch for UV resistance where tanks are mounted on trailed sprayers, while translucent induction hopper formulations substitute 0.3–0.6 wt% hindered amine light stabilizer. Mould charging is performed on shuttle or carousel machines with steel moulds fitted with rotationally moulded-in threaded inserts for suction lines, drain fittings, and level-sensor bosses. The heating cycle is held at 280–300°C oven set temperature to reach a PIAT of 205–215°C, followed by slow air cooling to avoid differential shrinkage across long flat side walls. Wall thickness is specified at 5–8 mm for 600 L sprayer tanks and 8–10 mm for 1,000 L UN IBC outer shells. Finished terminal products include horizontal saddle tanks, front-mounted sprayer tanks, induction hoppers, and UN 1H1 intermediate bulk containers for liquid fertilizers and non-flammable agrochemicals.

    The critical field condition is not single-impact abuse but long-term stress cracking at the liquid line where concentrated fertilizer salts crystallize and create local capillary stress at the polymer surface. Vessels specified for 40°C continuous exposure must be tested with the actual diluted formulation, because the ESCR ranking of one polyolefin grade under Igepal does not automatically transfer to glycol ethers, surfactant-loaded agricultural formulations, or calcium chloride brines. The operational boundary is chemical compatibility: RVL4068 is not specified for concentrated mineral acids, strong oxidizers, or aromatic hydrocarbon solvents; compatibility testing under ISO 16101:2004 is required before filling with any agrochemical whose label lists no high-density polyethylene compatibility data. In rotomoulding, gate-closing force on the mould platen must be maintained above 15 kN on large IBC tools to prevent flash at the parting line during maximum internal air expansion; failing to hold this force produces thin equatorial sidewalls and reduces drop-test margin under UN 1H1 drop height of 1.2 m at -18°C.

    Polyethylene Secondary Containment Pallets and Dosing Tank Sumps

    In secondary containment applications, RVL4068 is selected when impact resistance at -20°C and continuous exposure to incidental caustic or acid drips must be maintained without the brittle failure risk of lower-molecular-weight rotomoulding grades. The applicable regulatory structure is US EPA 40 CFR 264.175 for hazardous waste containment, 40 CFR 112.7 for Spill Prevention, Control, and Countermeasure compliance, and ASTM D1998-21 for upright polyethylene tank performance; where containment pallets or sumps are used as part of a UN packaging assembly, UN 1H1/1H2 solid-plastics intermediate bulk container provisions are referenced. Formulation for carbon black stabilised outdoor containment articles typically uses 100 wt% RVL4068 dry-flow powder with 2.0–3.0 wt% UV8 carbon black masterbatch and, for static-sensitive liquid service, a conductive carbon black loading of 6–8 wt% is added at the expense of low-temperature impact strength; therefore non-conductive RVL4068 fabrications without conductive filler are grounded externally and are not specified for flammable solvents with flash points below 23°C. Processing on large-platen carousel machines with steel or cast aluminium moulds requires a PIAT of 210–215°C and a demould temperature below 80°C to prevent sink marks at rib intersections on containment pallet decks. Mould design includes draft angles of 3–5° and break-in flanges to reduce warpage across flat spans above 1.2 m. Terminal products include bunded pallets with 240 L sump capacity, containment basins, dosing tank sumps, and chemical troughs installed under pumps and day tanks.

    The principal field failure mode is not impact cracking but long-term creep at unsupported forklift pockets; structural support pads and steel reinforcement frames are therefore specified for pallets exceeding 1,000 kg static load. On production lines, warpage is measured along the diagonal after 24 h of free-standing cooling, and parts exceeding 1.5% dimensional change are rejected because stackability and sump volume are compromised. Rotational moulders running RVL4068 for large flat containment decks note that pellet-to-powder pulverizing must maintain a powder bulk density above 0.32 g/cm³; lower bulk density reduces charge weight and creates thin rims at the upper mould corners during rotation.

    Processed at 4°C cold-room temperatures, fish tubs and meat lugs for protein processing lines require repeated drop impact, cleaning with alkaline detergents at 80°C, and compliance with FDA 21 CFR 177.1520(c) 2.1 and EU Regulation (EC) No 10/2011 overall migration limits of 10 mg/dm². In this application RVL4068 is processed as a 100 wt% virgin powder with 0.3–0.8 wt% of a food-contact-approved stabilizer masterbatch; regrind generated from the same article may be reintroduced at up to 20 wt% only if batch documentation under EU 10/2011 confirms migration tests remain valid. Rotational moulding parameters differ from tank production because food containers have polished stainless steel mould surfaces and are cooled with forced air to a demould temperature of 70–80°C to minimize warpage in flat bases while preserving impact strength. The heating cycle is set to 270–290°C oven temperature, with PIAT held at 200–205°C to avoid internal scorch that could create odour-active degradation products. Terminal product forms include 40 L to 1,000 L insulated fish tubs, meat lugs, poultry crates, and ingredient handling bins used on conveyor lines and in cold rooms.

    If RVL4068 Is Used for Playground Panels and Slide Components

    Outdoor playground components rotomoulded from RVL4068 are specified when UV stabilization, colour retention, and impact toughness must align with EN 1176-1:2017 safety requirements for equipment and EN 71-3:2019+A1:2021 migration limits for elements accessible to children, even though the equipment is not formally classified as a toy under all member states. The dry-blend for coloured slide and panel parts contains 1.5–3.0 wt% inorganic pigment masterbatch and 2.0–3.0 wt% hindered amine light stabilizer/antioxidant masterbatch; heavy-metal-free pigments are mandatory because extraction tests must not exceed the EN 71-3 limits for lead, cadmium, barium, and chromium. Processing on carousel machines with polished stainless steel moulds uses a PIAT of 205–210°C, with cooling by forced air only to 75°C before demoulding to preserve surface gloss and reduce internal stress in double-walled slide decks. Wall thicknesses are controlled between 5 mm and 8 mm to meet head-impact and entrapment test requirements without excessive mass. Terminal product types include double-walled straight and spiral slides, tunnel elements, climbing panels, roof caps, and ground-level activity panels.

    The outdoor weathering envelope is defined by accelerated testing under ISO 4892-2:2013 cycle 1: specimens exposed for 1,500 h must retain at least 80% of initial tensile elongation at break under ISO 527-2:2012; lower-cost pigment systems that pass indoor colour tests often fail this outdoor requirement and are rejected by inspection houses. On large slide decks, ejection from the mould below 75°C can cause stress whitening at the column connection points, so cooling racks are programmed to avoid forced-air impingement directly on thick bosses.

    In buried wastewater service, septic and holding tanks exceed simple water storage requirements because internal hydrogen sulfide, external soil pressure, and long-term creep demands overlap with installation-induced point loads from gravel backfill. RVL4068 is used in this sector under EN 12566-1:2016 for prefabricated septic tanks, with local health approvals often referencing ISO 13272:2011 for buried plastics piping and chamber structures; the resin’s high molecular weight distribution supports slow crack growth resistance, although published long-term buried-tank data for this specific resin grade in aggressive sulfate-rich groundwater is limited. The formulation is a 100 wt% virgin powder with 2.0–3.0 wt% carbon black masterbatch for aboveground riser sections and 0.5–1.0 wt% processing antioxidant for thick sections; post-consumer recyclate is excluded because buried tank wall integrity cannot be verified by visual inspection. Rotational moulding equipment for single-piece septic tanks is typically a rock-and-roll or large carousel machine with mild steel moulds, a heating cycle of 300–320°C oven set temperature, and a PIAT of 210–215°C maintained for 18–25 min after peak to complete fusion in 10–12 mm walls. Cooling is the slowest phase: forced ambient air followed by controlled water mist is used to prevent differential shrinkage at ribbed sections, and demoulding occurs only below 70°C. Terminal product types include 1,000 L to 5,000 L septic tanks, pump chambers, grease traps, and soakaway tunnel sections.

    The main boundary condition is sustained internal temperature: continuous discharge above 60°C from dishwashers or laundry can lead to softening and creep in the top section, so inlet temperatures must be limited or tempered. On rock-and-roll machines, axial rotation speed must not exceed 6 rpm during cooling to avoid generating a non-uniform wall on the lower side of the tank; thickness deviation is checked with an ultrasonic gauge at 12 points around the circumference and rejected if the minimum wall falls below 90% of the specified value.

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    Certification & Compliance
    More Introduction

    Polyethylene resin SABIC LLDPE RVL4068 is a natural, free-flowing rotational-moulding powder classified as a linear low-density polyethylene. The grade is controlled to a nominal density of 0.938 g/cm³ when tested under ISO 1183-1 and to a melt mass-flow rate of 4.0 g/10 min at 190 °C under a 2.16 kg load when tested under ISO 1133-1. That combination places the material between film-grade LLDPE and medium-density HDPE in stiffness, while retaining enough flow for pressureless, low-shear cavity filling. The powder morphology eliminates pellet compounding or grinding before charging to multi-station carousel, shuttle, or rock-and-roll rotational-moulding equipment. Typical production uses include monolayer storage tanks, intermediate bulk containers, agricultural hoppers, and industrial housings requiring wall-thickness uniformity across parting lines, mould inserts, and deep undercuts. The natural grade is supplied without intentionally added slip agents or high lubricant loadings, allowing post-mould surface treatment and welding without the interference associated with migratory additives.

    What Limits the Processing Window for RVL4068 in Rotational Moulding Equipment?

    In rotational moulding, heat transfer occurs through a metal mould shell rather than through mechanical shear, so cycle control depends on oven air temperature, wall thickness, and air-flow distribution. Industrial practice on clamshell machines with a 4:1 rotational-speed ratio commonly uses oven setpoints between 260 °C and 300 °C. The target peak internal air temperature is generally 190 °C to 210 °C, measured with an in-mould thermocouple data logger. Below this range, powder coalescence is incomplete, pinholes form along the parting line, and the inside wall retains a granular surface. Above approximately 230 °C peak internal air temperature, oxidative degradation accelerates within the trapped air environment, producing yellowing, a drop in impact strength, and possible odour. The melt flow rate of 4.0 g/10 min is high enough to reduce melt-viscosity-limited bubble removal in thick sections, but remains below injection-moulding-grade flow to limit sagging on vertical walls.

    For moulded walls of 3 to 5 mm, heating time at 300 °C may fall between 12 and 18 min on a steel tool; for walls near 12 mm, heating time can exceed 35 min. Cooling rate must be controlled with forced air before water mist or spray, because rapid quench reduces warpage in flat tank panels but can also freeze in internal stress. Demoulding below 80 °C is typical to avoid dimensional distortion. Mould-release agents containing silicone or fluoropolymer additives should be restricted to thin films; excessive release-agent carryover at the polymer surface can reduce weld-line strength and compromise the peel adhesion of post-applied labels. The powder should be kept free of surface moisture before charging. Although LLDPE does not hydrolyze, powder stored at relative humidity above 80 % can carry surface water into the mould, producing steam porosity in the finished wall.

    The values shown in Table 1 are representative data drawn from the manufacturer’s public technical datasheet summaries for natural RVL4068. They are typical values, not lot-release specification limits. Certified lot values are supplied with the certificate of analysis.

    Typical physical and mechanical values reported for natural SABIC LLDPE RVL4068
    PropertyTypical valueTest method
    Density0.938 g/cm³ISO 1183-1
    Melt mass-flow rate, 190 °C / 2.16 kg4.0 g/10 minISO 1133-1
    Tensile yield stress17 MPaISO 527-2
    Elongation at break>700 %ISO 527-2
    Flexural modulus600 MPaISO 178
    Environmental stress-crack resistance>1,000 hASTM D1693
    Vicat softening temperature, A50118 °CISO 306

    Mechanical Response and Comparative Position Against HDPE and Butene-LLDPE

    Under tensile testing to ISO 527-2 at 23 °C, the grade shows a yield stress between 15 and 20 MPa and elongation at break above 700 %. Ductile response is retained at low temperature, but the exact ductile-to-brittle transition depends on cooling rate, wall thickness, and regrind content. Compared with HDPE rotational-moulding resins of density 0.945 to 0.955 g/cm³, RVL4068 exhibits lower flexural modulus, lower Vicat softening temperature, and lower creep resistance under continuous load. In exchange, it provides longer failure times under environmental stress-cracking conditions in the ASTM D1693 bent-strip test and better impact absorption in welded corner regions. Compared with butene-comonomer LLDPE rotational-moulding grades of similar melt flow rate, the density of RVL4068 is higher, which increases stiffness, chemical permeation resistance, and surface hardness while reducing some low-temperature impact tolerance.

    The product is distinguishable from film-grade LLDPE by its higher melt flow rate, powder morphology, and higher density. These differences reduce heating time in thick-walled rotomoulded parts and increase modulus after solidification. The material is not crosslinked and therefore does not require peroxide addition, cure monitoring, or gel content measurement. However, the absence of a crosslinked network lowers long-term creep resistance; prolonged tensile stress at elevated temperature will produce larger deformation than an HDPE or crosslinked PE alternative of comparable thickness.

    Because the polymer is an unmodified linear low-density polyethylene produced without intentionally added phthalate plasticizers, heavy-metal heat stabilizers, or halogenated flame retardants, the base resin may be evaluated against the food-contact provisions of EU Regulation (EU) No 10/2011 and U.S. FDA 21 CFR 177.1520 for olefin polymers. End-use compliance is not automatic. Overall migration limits in Regulation (EU) No 10/2011 depend on the food simulant, contact ratio, time, and temperature. Similarly, FDA 21 CFR 177.1520 applies to the polymer portion, not to colorants, masterbatch carriers, or post-mould additives. For industrial chemical packaging, the resin is a thermoplastic and can be reground and reprocessed; however, regrind addition above 20 % may reduce falling-weight impact strength and should be validated under ISO 6603-2. Service compatibility with aggressive fluids must be confirmed by immersion testing under ASTM D543, because polyethylene does not provide barrier performance equal to fluorinated or crosslinked systems in contact with strong oxidizing acids, aromatic hydrocarbons, or chlorinated solvents.

    When RVL4068 Replaces Crosslinkable Polyethylene in Rotomoulded Chemical-Storage Parts

    Crosslinked polyethylene rotomoulding grades require peroxide handling, precise temperature control to achieve gel content above 85 %, and cannot be fully melt-reprocessed. In contrast, RVL4068 is a non-crosslinking thermoplastic that can be reclaimed on the shop floor without peroxide addition or cure-time adjustment. Replacement of crosslinked PE with RVL4068 is generally considered for tanks that do not require continuous hydrostatic stress at temperatures above approximately 60 °C. The loss of network structure reduces creep resistance; this limitation must be evaluated by long-term hydrostatic testing under ISO 1167 or by accelerated elevated-temperature burst testing on weld-free rotomoulded prototypes.

    For crosslinked PE grades, typical ASTM D1693 environmental stress-crack resistance values may exceed 1,000 h. The LLDPE grade also shows high environmental stress-crack resistance, but the absence of crosslinking shifts failure modes from brittle slow crack growth to large-scale deformation when temperature and hoop stress increase. The chemical resistance profile remains that of a semi-crystalline polyethylene, with no sustained service expected in strong oxidizing acids, aromatic hydrocarbons, or chlorinated solvents. Published data for this specific configuration is limited when high-temperature oxidizing chemical service is combined with dynamic loading; immersion testing on rotomoulded prototypes is required before service.

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