| HS Code | 961358 |
| Manufacturer | Dow |
| Product Name | ELITE mLLDPE 5400G |
| Polymer Type | Metallocene linear low-density polyethylene (mLLDPE) |
| Comonomer | 1-Octene |
| Catalyst Type | Metallocene |
| Density | 0.917 g/cm³ |
| Melt Index | 1.0 g/10 min (190 °C/2.16 kg) |
| Melt Flow Ratio | 30 (I21/I2) |
| Peak Melting Temperature | 122 °C |
| Vicat Softening Point | 104 °C |
| Brittleness Temperature | < -70 °C |
| Tensile Strength At Yield | 9.0 MPa |
| Tensile Strength At Break | 25 MPa |
| Ultimate Elongation | 600% |
| Flexural Modulus | 170 MPa |
| Dart Drop Impact | 300 g (1.0 mil film) |
| Elmendorf Tear Strength Md | 250 g |
| Elmendorf Tear Strength Td | 350 g |
| Haze | 10% |
| Gloss | 60 |
As an accredited Dow ELITE mLLDPE 5400G factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Dow ELITE mLLDPE 5400G is supplied in 25 kg moisture-barrier bags, with optional 1,000 kg bulk bags for industrial use. |
| Container Loading (20′ FCL) | 20′ FCL container loading of Dow ELITE mLLDPE 5400G: palletized 25 kg bags, shrink-wrapped and securely stowed for ocean shipment. |
| Shipping | Dow ELITE mLLDPE 5400G ships as non-hazardous polyethylene resin pellets, normally in sealed 25 kg bags, octabins, or bulk. Transport in dry containers/trucks at ambient temperature; keep dry, clean, and protected from UV and contamination. No special UN hazard class applies. |
| Storage | Dow ELITE mLLDPE 5400G should be stored in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat sources, moisture, and strong odors. Keep pellets in original sealed packaging on pallets, off the floor, protected from contamination and physical damage. Use first-in, first-out rotation, avoid prolonged UV exposure or excessive temperatures, and maintain good housekeeping with containers kept closed. |
| Shelf Life | Typically 24 months from manufacture when stored unopened in a cool, dry, UV-protected area; avoid prolonged sunlight/heat. |
Dow ELITE 5400G, an enhanced polyethylene produced via solution-phase metallocene catalysis, is commonly specified at a nominal density of 0.918 g/cm³ (ASTM D1505) and a nominal melt index of 1.0 g/10 min under a 2.16 kg load at 190 °C (ASTM D1238). In heavy-duty form-fill-seal sack conversion the resin is usually blended with 10–20 wt% low-density polyethylene on a three-layer blown-film line equipped with a 300 mm spiral mandrel die, a 30:1 L/D grooved-feed extruder, and internal bubble cooling. Melt temperatures are held between 205 °C and 225 °C, die gap is set at 1.8–2.2 mm, blow-up ratio is controlled between 2.2:1 and 2.8:1, and frost-line position is maintained 600–900 mm above the die. At these parameters, 80–120 µm sacks exhibit converter acceptance values commonly above 400 g dart impact per ASTM D1709 method A and Elmendorf tear values above 250 g MD / 300 g TD per ASTM D1922. The narrow metallocene molecular-weight distribution reduces shear-thinning response and lowers melt strength relative to conventional Ziegler-Natta LLDPE; running 100% 5400G without LDPE at high output can produce bubble oscillation and web wander unless internal bubble cooling pressure is maintained within ±1.5 mbar and the stabiliser cage is locked at 1.5–2.5 die diameters above the die. In form-fill-seal operations, hot-bar temperatures of 145–165 °C, dwell times of 0.4–0.8 s, and jaw pressures of 2–4 bar produce seal strengths above 8 N/25 mm on 80 µm film when tested per ASTM F88. Processing above 240 °C introduces oxidation gels, while melt temperatures below 195 °C produce unmolten resin particles appearing as fish-eye defects at the die lip. The resulting sacks are used for 25–50 kg granular chemicals, polymer pellets, fertiliser, and construction powders. For hazardous-materials transport packaging, converted sacks must pass drop and stacking tests under UN 6.1.5; food-contact sacks require olefin polymer compliance under 21 CFR 177.1520(c) and Commission Regulation (EU) No 10/2011, with overall migration below 10 mg/dm².
Agricultural greenhouse film produced at 150–200 µm gauge is typically coextruded in a three-layer configuration in which 5400G occupies the core layer. The outer layer, often 25–30 wt% of the total structure, carries the UV-stabiliser package; the core layer, 40–50 wt%, contributes puncture and tear resistance; the inner layer, 25–30 wt%, carries anti-fog and infrared-absorber additives. Coextrusion is run on a three-layer blown-film line with a die gap of 2.0–2.5 mm and a blow-up ratio between 2.2:1 and 3.0:1. Core-layer melt temperature is maintained at 210–225 °C, while UV-loaded skin layers are kept below 230 °C to limit HALS degradation. HALS loading at 0.3–0.8 wt% and benzotriazole UV absorber at 0.15–0.3 wt% in the skin layers are typical; the core layer generally omits additive masterbatch to preserve tear resistance. Film acceptance criteria after weathering per ISO 4892-2 cycle 1 or ASTM G154 require tensile break strength retention above 80% after 8000 h of xenon-arc exposure, and haze below 35% per ASTM D1003 for newly extruded film. Converter field reports identify poor dispersion of anti-fog packages as the dominant cause of droplet coalescence on the inner surface after 6–9 months of service. Because 5400G is a metallocene-catalysed resin with a narrow comonomer distribution, additive masterbatch carriers with high-viscosity LDPE are preferred to avoid localised melt-index dilution and bubble holes. The finished greenhouse film is used for multi-season tunnel covers, low tunnels, and soil solarisation in Mediterranean and continental climates, where tear propagation resistance per ASTM D1922 and puncture resistance per ASTM D5748 are the primary mechanical criteria.
| Layer | Polymer basis | Weight share | Additive package | Test method |
|---|---|---|---|---|
| Outer | LDPE/EVA | 25–30% | HALS 0.3–0.8 wt%; benzotriazole 0.15–0.3 wt% | ISO 4892-2 |
| Core | Dow ELITE 5400G | 40–50% | Processing stabiliser only 0.05 wt% | ASTM D1922 |
| Inner | LDPE/EVA | 25–30% | Anti-fog 0.5–1.2 wt%; IR absorber 0.5–1.0 wt% | ASTM D1003 |
Frozen food packages using 5400G as the sealant web are typically converted as laminated structures with BOPET or BOPA print webs and a 40–70 µm polyethylene sealant sheet. The critical qualification test is Gelbo flex testing conducted at -30 °C per ASTM F392; specifications for 50 µm sealant webs often require fewer than 5 pinholes per 300 cycles. Heat-seal strength is measured according to ASTM F88 on a flat-jaw laboratory sealer at 130 °C, 0.5 s dwell time, and 2 bar jaw pressure; a 50 µm laminate sealant layer commonly falls between 8 and 12 N/25 mm. Hot tack, measured per ASTM F1921, benefits from the uniform comonomer incorporation of mLLDPE and permits high-speed vertical form-fill-seal start-up below 100 °C seal bar temperature. In practice, sealant webs are blended with 20–30 wt% LDPE to reduce screw amperage and improve seal-through-contamination for frozen vegetable and IQF seafood packaging. The blown-film process for the sealant layer operates at a die gap of 1.8–2.2 mm, a blow-up ratio of 2.2:1–2.8:1, melt temperature of 210–225 °C, and frost-line height of 500–800 mm. Film defects to monitor include lane lines caused by poor mixing of high-viscosity LDPE masterbatches and micro-pinholes at the collapse frame caused by excessive web tension. For direct food contact, the sealant layer must comply with 21 CFR 177.1520(c) for olefin polymers and EU Regulation No 10/2011, with overall migration below 10 mg/dm². A limitation of this grade in frozen-food laminating is its relatively low melt index of 1.0 g/10 min; extrusion coating lines may require higher melt-index resins when converting at line speeds above 150 m/min. Published data for this specific grade on -30 °C Gelbo flex pinhole counts is limited, so converter qualification against incumbent LLDPE/LDPE blends is required before commercial change-over.
Stretch hood film formulated with 5400G is generally produced as a three-layer blown structure with an 80–120 µm total thickness and layflat widths from 1.3 m to 2.2 m. The outer layer is an LDPE-rich skin with antiblocking masterbatch, the core layer contains 60–80 wt% 5400G, and the inner layer is an LDPE/mLLDPE blend designed to prevent pallet-side blocking. Processing uses a three-layer die with a 2.0–2.5 mm die gap, blow-up ratio from 2.5:1 to 3.5:1, melt temperature from 210 °C to 230 °C, and a take-off speed adjusted to maintain controlled bubble tension at the collapsing cage. Mechanical acceptance tests include tensile strength and elongation per ISO 527-3, dart impact per ASTM D1709, puncture resistance per ASTM D5748, and tear strength per ASTM D1922. For pallet loads of cement bags and agricultural produce stored for 24–72 h, stretch hood suppliers commonly require tensile stress retention above 70% at 60% pre-stretch, measured after 24 h at 23 °C by ISO 527-3 loading in the machine direction. Failure on the stretch hood machine usually appears as corner breakage when the film is opened by grippers or as excessive sag when the core layer lacks elastic recovery. Because 5400G has lower melt strength than high-pressure LDPE, bubble stability at blow-up ratios above 3.0:1 is limited; adding 15–20 wt% LDPE is necessary for stable operation on lines without internal bubble cooling. The resulting hoods are applied to palletised loads at pre-stretch ratios of 60–80%, where the resin's puncture resistance reduces tear propagation from sharp corners of stacked timber, bagged cement, or PET bottle bundles.
Monolayer industrial liners and drum liners using 5400G are typically run on high-blow-up-ratio blown-film lines at 40–75 µm gauge. Melt temperature is held at 200–225 °C, die gap at 1.5–2.0 mm, blow-up ratio at 2.5:1–4.0:1, and output is limited to 150–200 kg/h on a 250 mm die because the resin's narrow molecular weight distribution reduces bubble stability at high blow-up ratio without LDPE addition. The target performance is puncture energy above 3 J per ASTM D5748 and Elmendorf tear above 250 g MD / 300 g TD at 50 µm per ASTM D1922, although published data for this specific grade in monolayer drum liners is limited. In chemical drum liner applications, the film is subjected to 55±2 °C water and chemical immersion tests per ASTM D543 for 7 days; converters often require a maximum tensile strength loss of 10% after exposure to dilute acids and alkalis. The main field failure mode is puncture-induced tear propagation when wetted powder or sharp-edged scrap is compacted in 120 L waste containers; using 10–15 wt% LDPE improves downgauging tolerance but reduces dart impact. For non-food chemical packaging, compliance with EU Regulation No 1907/2006 (REACH) and, where relevant, Directive 2011/65/EU (RoHS) is verified by raw-material declarations rather than film testing.
Collation shrink film converting at 45–60 µm thickness typically blends 5400G with LDPE and a LLDPE copolymers to balance transverse shrinkage and seal strength in multi-pack bundled bottles and cartons. The melt temperature on cast-film lines is maintained between 215 °C and 230 °C, chill-roll temperature is held at 15–25 °C, and die gap is set at 0.8–1.2 mm to limit draw resonance. Free shrink is measured in oil at 130 °C per ASTM D2732; collation converters commonly target transverse shrinkage of 30–55% after 10 s immersion and machine-direction shrinkage below 10%. Seal initiation temperature is screened by heat-seal testing per ASTM F88, with conversion lines operating at 115–135 °C seal-bar setpoint and 0.3–0.6 s dwell. The primary process limitation is melt-strength-driven neck-in on cast lines; blending 15–25 wt% LDPE reduces neck-in and improves gauge uniformity across 800–1000 mm web widths. The converted film is used for collation of PET bottle bundles, canned goods, and paperboard cartons, where shrink force and optical clarity per ASTM D1003 are balanced against load-retention requirements during distribution.
Competitive Dow ELITE mLLDPE 5400G prices that fit your budget—flexible terms and customized quotes for every order.
For samples, pricing, or more information, please contact us at +8618005193850 or mail to sales8@ascent-chem.com.
We will respond to you as soon as possible.
Tel: +8618005193850
Email: sales8@ascent-chem.com
Flexible payment, competitive price, premium service - Inquire now!
Dow ELITE 5400G is introduced as an enhanced polyethylene resin for blown film structures in which puncture resistance, optical clarity, and heat-seal initiation are primary specification variables. The nominal melt flow rate is 1.0 g/10 min measured at 190 °C under a 2.16 kg load in accordance with ISO 1133-1:2022 and ASTM D1238. The nominal density is 0.916 g/cm³ determined by ASTM D792. These values place the material in the linear low density polyethylene class at the low-crystallinity end and separate it from higher-density 0.923–0.927 g/cm³ butene LLDPE grades. Typical end uses include heavy-duty shipping sacks, frozen food packaging, high-speed form-fill-seal structures, and industrial liners where cold-temperature impact strength, tear propagation resistance, and controlled optical quality are required. The product is produced on a single-site catalyst platform, and the resulting molecular architecture differs from high-pressure LDPE and conventional Ziegler-Natta LLDPE in extrusion pressure response, bubble stability, film optics, and seal behavior.
The structural source of the performance difference is the distribution of short-chain branches across molecular weight fractions. In a conventional Ziegler-Natta LLDPE, comonomer insertion is favored in lower-molecular-weight chains; the higher-molecular-weight fraction remains more linear and crystallizes into thicker lamellae. This produces a broad melting endotherm, higher internal haze, and elevated gel counts. In 5400G, the constrained geometry catalyst system distributes the alpha-olefin more uniformly across molecular weights. The result at 0.916 g/cm³ is a more uniform lamella thickness distribution, which reduces refractive index contrast responsible for internal haze and improves low-temperature dart impact without requiring a density reduction below standard LLDPE film grades. The resin does not carry the same long-chain branching density as high-pressure LDPE; therefore it exhibits lower melt strength, less pronounced strain hardening, and a less shear-thinning processing curve. This difference is measurable in bubble stability and in blown film die pressure. The absence of long-chain branching also changes heat-seal morphology: seal strength develops through interdiffusion and crystallization, and the narrower composition distribution generally lowers seal initiation temperature relative to a butene LLDPE of equivalent density. Published grade-specific gel permeation chromatography and differential scanning calorimetry curves are limited; comparative conclusions should be confirmed with a production lot and a control resin run on the same line.
The melt rheology of 5400G differs from a branched LDPE of equivalent 1.0 g/10 min melt index in two process-critical ways. The low-shear viscosity is higher, and the degree of shear thinning is lower. This shifts the extruder pressure–output relationship and may require a screw with a longer metering section and a moderate compression ratio. Machine builder technical bulletins for 0.916 g/cm³ single-site mLLDPE blown film commonly specify a barrier screw with an L/D ratio of 24:1–30:1, a compression ratio between 2.8:1 and 3.2:1, and a spiral mandrel die gap between 1.5 mm and 2.5 mm. The melt temperature window is generally 200–240 °C. The bubble is typically run at a blow-up ratio of 2.0:1–2.8:1 with the frost line positioned 1.0–2.0 die diameters above the air ring to avoid unstable deformation. Failure modes reported on production lines include sharkskin melt fracture at high screw speeds, bubble sag when the frost line is too low, and wrinkling in the collapsing frame if the bubble is over-cooled. Pre-drying is not required when the resin is stored in sealed packaging below 60% relative humidity; surface moisture can be removed by an 80 °C desiccant hopper residence of 2 h. Processors should verify motor-load margin before running at high output because the pressure drop through the die can be higher than LDPE at the same screw speed.
Substitution into a three-layer LDPE skin formulation does not preserve bubble geometry and sealing behavior. The lower melt strength of 5400G can make the bubble more sensitive to air ring turbulence and may require a lower blow-up ratio or a higher frost line than a branched LDPE. In a 70/30 LDPE/5400G blend, viscosity mismatch between the two resins can produce local flow instabilities unless the screw contains a distributive mixing section such as a Maddock or pin mixer of 4–6 L/D. The seal initiation temperature generally shifts downward relative to a butene LLDPE of equal density, but the final heat-seal curve is affected by film gauge, chill-roll temperature, seal bar pressure, dwell time, and the presence of slip or antiblock additives. Heat seal strength is measured according to ASTM F88/F88M; hot tack is measured according to ASTM F1921. In heavy-duty shipping sacks, the use of 5400G as a core or skin layer can improve dart impact and slow-rate puncture at reduced gauge, but the downgauge target must be validated against filled-package drop tests and seal integrity under load. Published comparative data for this exact multilayer structure are limited; converters should run a design-of-experiments across die gap, blow-up ratio, and blend ratio before final specification.
On cast film lines, the chill-roll quench rate produces smaller crystalline structures and different optical and seal properties than blown film. The resin is used in high-speed packaging where low seal initiation and stable hot tack are required; the coefficient of friction and blocking force must be controlled with additive packages that do not compromise clarity. For cast film, the extruder barrel profile typically limits the feed zone to approximately 180 °C and the die to 240 °C to minimize thermal degradation, but the optimum profile must be established on the specific line because residence-time distribution varies with screw design and throughput.
Mechanical and optical comparisons must be made at constant gauge, blow-up ratio, and cooling rate. Tensile properties are measured according to ASTM D882, Elmendorf tear according to ASTM D1922, dart impact according to ASTM D1709 Method A, puncture resistance according to ASTM D5748, haze according to ASTM D1003, and specular gloss according to ASTM D2457. At 0.916 g/cm³, 5400G exhibits lower crystallinity than a 0.923 g/cm³ butene LLDPE and therefore generally provides higher dart impact and puncture energy at equivalent gauge. The uniform comonomer distribution reduces the large crystalline domains that contribute to internal haze; however, surface haze from die lines and additives must be separated from internal haze by measuring films without process aids or by optical microscopy. In frozen food packaging, the low-temperature impact resistance is the dominant specification; typical test temperatures of -18 °C are applied to films before dart impact and bag drop evaluation. In form-fill-seal packaging, the same optical and impact properties must be combined with controlled coefficient of friction, which is measured according to ISO 8295 or ASTM D1894. Published film property data for 5400G across all gauge and processing combinations are limited; each converter should generate an internal property matrix from production lots.
Food contact status for 5400G is generally supported by the olefin polymer provisions of FDA 21 CFR 177.1520(c). In the European Union, the final article must comply with Regulation (EU) No 10/2011 and its migration limits for monomers, additives, and overall migration. A resin compliance letter does not automatically clear a converted film because lamination adhesives, printing inks, process aids, and regrind streams can introduce substances not covered by the resin certification. Migration testing under the EN 1186 series and specific migration methods is conducted on the finished article under the intended food contact time and temperature. For high-temperature microwave or retort conditions, additional testing is required because the food simulant and exposure conditions may exceed the resin supplier’s default compliance request.
| Regulatory or Test Domain | Standard or Clause | Condition or Application |
|---|---|---|
| US food contact | FDA 21 CFR 177.1520(c) | Olefin polymer compliance; final article clearance required |
| EU food contact | Regulation (EU) No 10/2011 | Positive list and overall migration; finished article testing required |
| Melt characterization | ISO 1133-1:2022, ASTM D1238 | 1.0 g/10 min at 190 °C/2.16 kg |
| Density | ASTM D792 | 0.916 g/cm³ nominal |
| Film mechanical testing | ASTM D882, ASTM D1922, ASTM D1709 | Gauge-controlled comparison required across production lots |
Storage below 30 °C and below 60% relative humidity is typical warehouse practice for preserving additive performance and minimizing surface moisture absorption before extrusion. Extended residence above 80 °C in a drying hopper may consume antioxidants and shift the oxidative induction time, and additive interactions should be evaluated when the resin is combined with processing aids, slip, antiblock, or color concentrates because seal strength, optical quality, and film color can be affected by incompatible additive chemistry.