| HS Code | 347117 |
| Product Name | ExxonMobil Enable mLLDPE 27-05CH |
| Polymer Type | Metallocene Linear Low Density Polyethylene (mLLDPE) |
| Catalyst Type | Metallocene |
| Comonomer | Hexene |
| Density | 0.927 g/cm³ |
| Melt Index | 0.5 g/10 min (190°C/2.16 kg) |
| Peak Melting Temperature | 123 °C |
| Vicat Softening Temperature | 108 °C |
| Tensile Strength At Yield | 10.3 MPa |
| Tensile Strength At Break | 38.0 MPa |
| Elongation At Break | 600% |
| Flexural Modulus | 300 MPa |
| Dart Drop Impact | 220 g |
| Elmendorf Tear Strength Md | 180 g |
| Elmendorf Tear Strength Td | 390 g |
| Haze | 7% |
| Gloss 45 | 70 |
| Recommended Application | Blown film |
As an accredited ExxonMobil Enable mLLDPE 27-05CH factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | ExxonMobil Enable mLLDPE 27-05CH is supplied in 25 kg polyethylene bags, offering convenient storage and handling. |
| Container Loading (20′ FCL) | ExxonMobil Enable mLLDPE 27-05CH loaded in a 20′ FCL container, palletized bags secured, within weight limits, ready for export shipment. |
| Shipping | ExxonMobil Enable mLLDPE 27-05CH is shipped as non-hazardous polyethylene resin pellets in sealed moisture-barrier bags or octabins. Keep dry and protected from direct sunlight and excessive heat. No special dangerous-goods declaration is normally required; follow the SDS and transport documents. |
| Storage | Store ExxonMobil Enable mLLDPE 27-05CH in a cool, dry, well-ventilated area, away from direct sunlight, ignition sources, and excessive heat. Keep in original, sealed, labeled packaging on pallets; protect from moisture, contamination, and physical damage. Avoid prolonged outdoor storage, do not stack excessively, use first-in, first-out rotation, and follow the manufacturer’s SDS and local regulations. |
| Shelf Life | Shelf life is 24 months from date of manufacture when stored unopened in original packaging under dry, normal warehouse conditions. |
Industrial heavy-duty sack film made with ExxonMobil Enable mLLDPE 27-05CH is processed on three-layer blown-film lines using grooved-feed barrels, 30:1 to 33:1 L/D ratios, and die gaps of 1.8 mm to 2.5 mm. The nominal melt index of 0.5 g/10 min according to ASTM D1238-20 at 190 °C and 2.16 kg requires melt temperatures between 205 °C and 230 °C, and screen-changer backpressure is typically 10–15% higher than conventional Ziegler-Natta LLDPE of equivalent density. A standard core-heavy structure uses 80 wt% Enable 27-05CH, 10 wt% high-pressure LDPE, and 10 wt% slip/antiblock masterbatch. The LDPE fraction is included to stabilize bubble geometry during low-speed transitions because the 0.927 g/cm³ density measured by ASTM D1505-18 and 0.5 g/10 min melt index do not produce the melt strength of high-pressure LDPE. Films are evaluated under ASTM D1709-16a dart impact, ASTM D5748-19 Elmendorf tear, and ASTM D882-18 tensile. Published data for this exact formulation are limited, so converter trials should measure dart impact on 100 µm to 200 µm gauge before final sack release. For FIBC liner use, the load-bearing sack certification follows ISO 21898; the film is not the primary load-bearing element. Compliance for export packaging requires REACH SVHC verification and, where packaging is declared for electrical/electronic equipment, RoHS Directive 2011/65/EU.
Lamination sealant webs containing Enable 27-05CH are converted on cast coextrusion lines with die gaps of 0.4 mm to 0.8 mm and adaptor/die melt temperatures between 250 °C and 280 °C. The 0.927 g/cm³ density moves seal initiation temperature upward compared with lower-density metallocene sealants. When a specification requires heat-seal initiation below 95 °C, the sealant layer is typically diluted with 30–50 wt% lower-density ethylene-hexene plastomer. Seal strength is measured according to ASTM F88/F88M-15 using 25.4 mm width specimens and 200 mm/min crosshead speed, while hot-tack behaviour is evaluated with ASTM F1921-98. The sealant layer is commonly 8–15 µm in a 60–80 µm laminate, with the remainder composed of BOPP or PET and a solventless adhesive. Corona treatment to 38–40 mN/m under DIN ISO 8296 is required for stable lamination adhesion; treatment decay below 36 mN/m within 24 hr indicates excessive slip additive migration and a batch rejection risk. For food-contact laminates, the final article must comply with FDA 21 CFR 177.1520 and Commission Regulation (EU) No 10/2011 as amended, including overall migration below 10 mg/dm² under OM2. The regulatory checklist is summarised below.
| Regulatory reference | Clause or test condition | Limit or method |
|---|---|---|
| FDA 21 CFR 177.1520 | (c) Olefin polymers | Extractables limits per paragraph |
| EU Regulation (EU) No 10/2011 | Annex I, Table 1 | Authorized monomers/additives; SML verification |
| EU Regulation (EU) No 10/2011 | Article 17, Annex III, OM2 | 10 mg/dm² overall migration |
| REACH Regulation (EC) No 1907/2006 | Annex XVII | Restricted substances; SVHC declaration |
Converted articles include stand-up pouches, dry-food pouches, and retort-free ready-meal lidding where higher stiffness and abuse resistance offset the elevated seal initiation temperature.
Under high blow ratios of 2.8:1 to 3.2:1, silage wrap extrusion with Enable 27-05CH requires internal bubble cooling and a frost line height held between 600 mm and 900 mm. The 0.5 g/10 min melt index reduces extruder throughput at fixed screw speed compared with higher-MI resins and increases die melt pressure. A three-layer structure is used: core at 80 wt% Enable 27-05CH, with outer skins of UV-stabilized mLLDPE or LDPE. HALS-based UV masterbatch is added at 3–6 wt% of total film mass, and carbon black masterbatch at 2–3 wt%, depending on the outdoor storage life specified in EN 13207:2018. Polymer processing aid at 0.05–0.12 wt% is required to prevent die-lip build-up and melt fracture during 24-hour continuous runs. On production-scale lines, bubble instability appears after 6–8 hours when frost line height drifts below 600 mm; gauge variation then exceeds ±8% in random zones, making the film unsuitable for high-speed bale wrapper equipment. Finished film performance is tested under EN 13207:2018 for silage films and ASTM D5748-19 for tear. REACH SVHC confirmation is required for substances supplied in the UV and carbon black masterbatches.
For frozen food packaging structures with Enable 27-05CH in the core layer, dynamic puncture performance at −20 °C to −40 °C is evaluated under ASTM D3420-21 and Elmendorf tear under ASTM D5748-19. The core layer is typically 50–70 wt% of an 80–100 µm three-layer coextruded film, with sealant skins based on lower-density mLLDPE or ethylene-vinyl acetate copolymers. This grade is selected for the combination of 0.927 g/cm³ density and 0.5 g/10 min melt index, which raises stiffness and abuse resistance relative to lower-density sealant resins. The operational boundary is severe sub-zero ductility: when the core layer exceeds 70 wt% or the film core exceeds 40 µm in thickness, low-temperature puncture toughness can fall below specification because higher density raises the ductile-to-brittle transition temperature. Slip masterbatch is added at 1–2 wt% and silica-based antiblock at 2–4 wt%; plasticizers are not used. Food-contact compliance is governed by FDA 21 CFR 177.1520 and EU Regulation (EU) No 10/2011, with overall migration below 10 mg/dm² under OM2. Converter trials should verify heat seal strength at −20 °C using ASTM F88/F88M-15. Converted articles include frozen vegetable packs, seafood bulk bags, and ice cube bags.
In double-bubble collation shrink film lines, replacement of conventional Ziegler-Natta LLDPE with Enable 27-05CH narrows the orientation window because the metallocene molecular architecture produces higher shrink tension at a lower draw ratio. The first bubble is extruded at 115–125 °C, and the second bubble is oriented at 103–108 °C; bubble skin temperature deviation beyond ±2 °C generates visible gauge bands and frequent bubble collapse. Machine-direction orientation is typically held between 4.5:1 and 5.5:1, with transverse orientation between 3:1 and 4:1; the final balance is confirmed by ASTM D2838-18 shrink tension measurements. A representative formulation uses 70 wt% Enable 27-05CH, 25 wt% high-pressure LDPE of 0.919 g/cm³ density, and 5 wt% slip/antiblock masterbatch. The LDPE component stabilizes the second bubble and suppresses edge tear during transverse orientation; it is not added as inert filler. Die melt temperatures are held between 220 °C and 240 °C to avoid thermal degradation of the slip additive. Film thickness ranges from 45 µm to 70 µm for beverage multipack and can-pack collation. Compliance for secondary food packaging is limited to REACH and, where relevant, RoHS Directive 2011/65/EU; direct food contact is not intended for collation shrink film. End uses include shrink packs for PET water bottles, carbonated beverage cans, and multipack cartons.
Pallet hood film with post-consumer recycle in the core layer retains puncture resistance only when recycled LLDPE content is held below 20 wt% of total film mass. Cast-film lines with 3-layer A/B/C feedblocks are used; skin layers are based on virgin Enable 27-05CH to preserve dart impact and tear resistance, while the core contains the recycled fraction. Melt temperatures are maintained between 240 °C and 260 °C; higher temperatures cause gel formation from degraded recycled material and die-lip deposits that force shutdown for cleaning. The density of 0.927 g/cm³ and melt index of 0.5 g/10 min provide load retention on palletized goods; film thickness is typically 100–150 µm. Process capability is monitored with ASTM D1709-16a dart impact and ASTM D5748-19 Elmendorf tear after each recycle batch addition. Recycled LLDPE containing amine-based antistatic additives or unknown processing aids must be avoided because those additives can generate odour and compromise tear resistance. Compliance is governed by REACH Regulation (EC) No 1907/2006 and RoHS Directive 2011/65/EU as amended by Delegated Directive (EU) 2015/863 for industrial packaging declared with electrical/electronic goods. Converted articles include pallet hood covers, transport sacks, and construction-film overwrap.
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ExxonMobil Enable mLLDPE 27-05CH is a metallocene-catalyzed linear low density polyethylene resin intended for blown film extrusion. The grade carries a nominal density of 0.927 g/cm³ when determined under ASTM D792-20 or ISO 1183-1:2019 and a nominal melt index of 0.5 g/10 min at 190 °C and 2.16 kg when determined under ASTM D1238-20 or ISO 1133-1:2022. The first two numerals of the grade designation identify the nominal density; the final two numerals identify the nominal melt index. The regional suffix “CH” defines a product registration and additive configuration and does not alter the base polymer architecture. The pelletized resin is supplied without slip or antiblock additives in the base formulation. Polyethylene of this class is not hygroscopic, so pre-drying is not required for material kept in intact packaging; if pellets are transferred from cold storage into a production area above 60% relative humidity, condensation can form and hot-air pre-drying at 70 °C for 2 h should be performed before extrusion.
The base stabilizer package is intended for standard blown film melt temperatures up to 230 °C. Short excursions to 240 °C are acceptable only when residence time remains below 10 min; extended exposure above 240 °C can form oxidized gel particles at the die lip and reduce film appearance grades. Published data for this specific CH configuration is limited to nominal density and melt index; film property values vary with die gap, blow-up ratio, frost line height, and downstream converting equipment.
The primary difference from Ziegler-Natta LLDPE of equivalent 0.927 g/cm³ density and 0.5 g/10 min melt index is the narrower inter-chain composition distribution. Metallocene catalysis produces more uniform short-chain branching and reduces the high-molecular-weight highly crystalline fraction and the low-molecular-weight amorphous fraction simultaneously. This structural difference reduces hexane extractables under FDA 21 CFR 177.1520 conditions and improves organoleptic behavior in food-contact packaging. Compared with a Ziegler-Natta LLDPE, the film typically shows higher dart impact strength at 25 µm thickness under ASTM D1709 Method A and improved puncture resistance under ASTM D5748, while tensile yield strength remains within the same general range. Seal initiation temperature measured by ASTM F2029 can shift downward by approximately 5 °C to 10 °C; however, published data for this exact CH designation is limited, and package-level heat-seal validation remains mandatory.
Compared with high-pressure LDPE of the same melt index, the mLLDPE has higher tensile yield and puncture resistance but lower melt elasticity and lower shear thinning. This difference lowers bubble stability and raises die pressure on conventional blown film lines. The grade is therefore not a direct drop-in for high-pressure LDPE in high-stalk thin film; it is better positioned for gauges where toughness and stiffness are the controlling requirements. Compared with lower-density metallocene grades near 0.918 g/cm³, the 0.927 g/cm³ density raises stiffness and tensile modulus but sacrifices low-temperature dart impact. Compared with ethylene-vinyl acetate copolymer sealants, this grade has lower melt elasticity and lower low-temperature impact; it is not intended as a direct replacement for EVA in high-abuse frozen sealant layers.
Production-scale blown film processing on a grooved-feed extruder with an L/D of 25:1 to 30:1 and a barrier screw is recommended. A screen pack of 40/60/80 mesh is normally retained to protect the die. Typical starting conditions are melt temperature 190–230 °C, die gap 1.8–2.5 mm, blow-up ratio 2.0:1–3.0:1, and frost line height 4–8 die diameters. Because the narrow molecular weight distribution produces less shear thinning than high-pressure LDPE, die pressure may be 10–20% higher on the same screw profile. This effect becomes more pronounced at die gaps below 1.8 mm. A melt pump is advantageous because lower melt elasticity reduces drag-flow compensation and can cause throughput fluctuations at low screw speeds.
Bubble stability is the limiting processing variable at high blow-up ratios. Above 3.5:1, the low melt strain hardening of mLLDPE can cause flapping, gauge variation, and weld-line instability; increasing the die gap above 2.2 mm or blending 10–20 wt% high-pressure LDPE restores stability. Internal bubble cooling is recommended for outputs above 150 kg/h on a 250 mm die to maintain frost line height and thickness uniformity. Recovered edge trim and purge from the same grade can be reintroduced up to 20 wt% without meaningful density or melt index deviation, provided the reclaim is free of paper labels, adhesives, and printing inks. Higher regrind ratios can elevate gel counts and reduce dart impact repeatability.
At cold-chain and industrial packaging gauges of 50–125 µm, the resin is selected for high puncture and tear resistance, not for optical clarity. Dart impact measured under ASTM D1709 Method A on a 25 µm monolayer film depends on die gap, frost line height, and blow-up ratio; published data for this specific CH configuration is limited, and resin lot-to-lot values should not be substituted for package-level testing. The 0.927 g/cm³ density raises secant modulus compared with 0.918 g/cm³ metallocene grades but reduces low-temperature impact. For freezer applications at -25 °C, dart impact and puncture should be measured after films are conditioned according to ASTM D1709 and ASTM D5748. Tear balance follows ASTM D1922 or ISO 6383-2; machine-direction tear is typically the limiting quantity after high machine-direction orientation.
In agricultural silage wrap, the base resin must be compounded with a UV stabilizer system because the neat grade does not contain a UV package. Failure to add hindered amine light stabilizer and antioxidant at appropriate concentrations can lead to early embrittlement under accelerated weathering conditions. For food-contact evaluation, the base olefin polymer is covered by FDA 21 CFR 177.1520(c) when the final article meets the applicable extractives and use limitations. EU Regulation (EC) No 10/2011 Annex I requires overall migration below 10 mg/dm² and specific migration limits for any added masterbatch constituents. REACH Article 33 and Directive 2011/65/EU Annex II are not resin-specific certifications until the final article is characterized; however, no SVHC above 0.1 wt% or restricted heavy metals above the applicable limits are intentionally present in the base resin.
| Domain | Reference | Condition or limit |
|---|---|---|
| Olefin food-contact base resin | FDA 21 CFR 177.1520(c) | Use subject to Title 21 conditions; high-temperature and fatty-food applications require end-testing |
| European food-contact compliance | EU Regulation (EC) No 10/2011 Annex I | Overall migration limit 10 mg/dm²; specific migration limits apply to additives |
| REACH SVHC declaration | Regulation (EC) No 1907/2006 Article 33 | No SVHC above 0.1 wt% in homogeneous material based on supplier confirmation |
| RoHS restricted substances | Directive 2011/65/EU Annex II | Pb, Hg, Cr VI, PBB, PBDE below 0.1 wt%; Cd below 0.01 wt% unless exempted |
| Packaging heavy metals | US CONEG; EU Directive 94/62/EC | Sum of Pb, Cd, Hg, Cr VI below 100 ppm |
Use in heavy-duty shipping sacks at 80–125 µm thickness exploits the balance of stiffness and puncture resistance. In frozen food packaging, low-temperature impact is the governing property; in collation shrink film, melt strength limitations require blending with LDPE. No single set of blown film conditions produces all these properties simultaneously; the processor must select die gap, blow-up ratio, and frost line height for the failure mode that dominates the package.