| HS Code | 912162 |
| Density | 0.912 g/cm³ |
| Melt Index | 3.5 g/10 min |
| Peak Melting Temperature | 116 °C |
| Vicat Softening Temperature | 86 °C |
| Crystallization Temperature | 100 °C |
| Tensile Strength At Yield | 7.5 MPa |
| Tensile Strength At Break | 24 MPa |
| Elongation At Break | 600% |
| Flexural Modulus | 120 MPa |
| Hardness Shore D | 44 |
| Film Haze | 6% |
| Film Gloss | 70% |
| Dart Drop Impact | 200 g |
| Elmendorf Tear Md | 300 g |
| Elmendorf Tear Td | 400 g |
| Puncture Resistance | 8 J/mm |
| Coefficient Of Friction | 0.2 |
| Seal Initiation Temperature | 90 °C |
As an accredited ExxonMobil Exceed VLDPE 3512CB factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Supplied in 25 kg polyethylene bags on pallets; each pallet contains 1,000 kg (40 bags) of ExxonMobil Exceed VLDPE 3512CB. |
| Container Loading (20′ FCL) | One 20-foot FCL container loaded with ExxonMobil Exceed VLDPE 3512CB polyethylene resin in 25 kg bags, securely stowed for shipment. |
| Shipping | ExxonMobil Exceed VLDPE 3512CB is shipped as a non-hazardous polymer resin, typically in 25-kg moisture-resistant bags, octabins, or bulk trucks/containers. Transport by truck, rail, or sea under dry, ventilated conditions; protect from moisture, sunlight, heat, and contamination. No special UN classification or placarding is required. |
| Storage | Store ExxonMobil Exceed VLDPE 3512CB in a cool, dry, well-ventilated warehouse in original, closed packaging. Protect from direct sunlight, heat, moisture, dust, and contamination. Keep away from ignition sources and strong oxidizing agents, and avoid prolonged UV exposure. Palletize off the floor, use first-in, first-out rotation, maintain good housekeeping, and follow local regulations and supplier guidance. |
| Shelf Life | Shelf life: 5 years from manufacture when stored in original, unopened packaging in a dry, clean environment below 50°C. |
Metallocene-catalysed very low density polyethylene copolymer with nominal density 0.912 g/cm³ (ASTM D792) and melt flow rate 3.5 g/10 min (ASTM D1238, 190 °C/2.16 kg) functions as the sealant web in three-layer and five-layer cast coextrusion structures for vertical form-fill-seal and horizontal form-fill-seal packaging lines. The resin is processed on cast coextrusion equipment with extruder L/D ratios of 28:1 to 32:1, barrier screws, gear pumps, and die zones maintained at 260–290 °C. The sealant layer is positioned as the inside web at 20–30% of total film thickness, typically 20–50 µm within a total gauge of 70–130 µm. A production formulation for the sealant layer is 98–100 wt% Exceed VLDPE 3512CB, with 0–2 wt% antiblock masterbatch and 0–2 wt% slip masterbatch. Combined masterbatch loading above 3 wt% raises haze, and in high-speed packaging such visually degraded film is rejected by automatic optical inspection systems; the masterbatch carrier is a low-density polyethylene with melt index 1.0–2.0 g/10 min to avoid gel-induced pinholes.
Seal initiation, seal plateau, and hot-tack behaviour are measured on laboratory heat-sealing equipment calibrated to 0.1 °C jaw temperature. ASTM F1921 hot-tack is evaluated with a 0.2 s delay and 0.3 MPa jaw pressure; ASTM F88/F88M seal strength is tested on 25 mm strips at 300 mm/min jaw separation. In high-speed VFFS lines running above 70 cycles/min, the seal bar dwell time can drop below 150 ms, and the sealant layer must produce sufficient seal force over the 95–115 °C jaw range before the filled pack drops into the conveyor. The VLDPE sealant layer provides a wider hot-tack plateau than conventional LLDPE; production trials on a three-layer cast line with polyamide barrier core measured seal strength of 10–14 N/25 mm at 120–130 °C jaw temperature and 0.5 s dwell, while hot-tack at 105 °C remained above 4 N/25 mm. These values are process-validation data from specific line configurations and should not be treated as product release limits because they shift with film thickness, substrate thermal conductivity, product fill viscosity, and jaw contamination.
For food-contact use, the sealant layer complies with U.S. FDA 21 CFR 177.1520 covering olefin polymers and European Union Regulation (EU) No 10/2011 on plastic materials and articles intended to come into contact with food, including overall migration limit 10 mg/dm² and specific migration limits under Regulation (EU) 2020/1245. Downstream terminal products include snack food bags, cereal and instant noodle sachets, cookie slug wraps, frozen vegetable pillow packs, and pre-made open-mouth bags for high-speed filling of dry powders.
On multi-layer blown film lines producing frozen seafood, poultry, and IQF vegetable bags, the sealant layer is formulated with 70–85 wt% Exceed VLDPE 3512CB and 15–30 wt% low-density polyethylene with a melt index of 0.2–0.8 g/10 min to increase bubble stability during high blow-up ratio processing while preserving dart impact at cold-chain storage temperatures. The blown film process operates with a die gap of 1.8–2.5 mm, a blow-up ratio of 2.2–2.8, and a frost line height of 600–900 mm; die temperature is held at 220–250 °C. The LDPE addition raises melt strength, but at loadings above 30 wt% the low-temperature dart impact retention declines and the seal initiation temperature increases by 5–8 °C, narrowing the hot-tack window on high-speed vertical baggers. Melt pressure at the screen pack is not to exceed 35 MPa; higher pressure indicates gel build-up or screen blinding and requires changing the 60/80/100/60 mesh assembly before surface roughness on the sealant layer creates channel leaks in frozen liquid packs.
Low-temperature abuse resistance is evaluated by ASTM D1709 Fenwal dart drop on films conditioned to −40 °C according to ASTM D618; values for a 70/30 VLDPE/LDPE sealant film at 50 µm gauge are typically 1.5–2.0 times those of a comparable 50 µm conventional LDPE film, but direct numerical comparisons require identical die gaps and frost line heights. Tear resistance is measured by ISO 6383-2 trouser tear and ASTM D1922 Elmendorf tear; puncture energy is tested per ASTM D5748. Regulatory compliance for frozen food applications includes FDA 21 CFR 177.1520 for olefin polymers and EU Regulation (EU) No 10/2011; frozen meat and poultry contact may also require USDA FSIS acceptance depending on the establishment’s HACCP plan. Terminal product forms include IQF vegetable pillow packs, frozen seafood shrink bags used in low-temperature distribution, poultry portion bags, and chub films for ground meat.
Liquid detergent refill pouches, edible oil pour-spout pouches, and wet wipe bolsters place the sealant layer under flexural fatigue, hydrostatic pressure, chemical contact, and repeated drop loading. In these structures the sealant film is produced as a 30–60 µm cast layer of 90–100 wt% Exceed VLDPE 3512CB with 0–10 wt% low-density polyethylene to adjust film stiffness and lamination bond; the LDPE content above 10 wt% reduces flex-crack resistance and increases seal initiation temperature. The film is corona treated to 38–42 mN/m and adhesive-laminated to reverse-printed 12 µm polyethylene terephthalate or 15 µm biaxially oriented polyamide. The cast film process uses a 90–120 mm extruder, L/D 30:1, barrier screw, 60/80/100/60 screen pack, feed block coextrusion when multilayer sealant films are produced, and a chill roll maintained at 18–24 °C. Die temperature is held at 260–290 °C. Output fluctuations above 5% alter gauge in the sealant layer and create low-gauge channels in side-gusset corners where burst failure initiates.
Seal strength is tested according to ASTM F88/F88M on 25 mm strips; hermetic leakage is determined by ASTM F2095 for whole package leak, while burst testing follows ASTM F1140 with internal pressurisation rates of 5–10 kPa/s and failure thresholds typically set at 250–500 kPa depending on pouch volume. Solventless adhesive lamination uses two-component polyurethane at coating weight 2.0–2.5 g/m², with lamination nip temperature 50–60 °C and maturing for 48 h at 40 °C. Flex-crack resistance is assessed by Gelbo flex testing per ASTM F392; leak failures in side-gusset corners after 10,000 cycles are classified as pinholes or seal creep. In spouted pouch corners, the sealant must survive double seals at the base gusset and the fitment flange; line inspection includes 0.2 mm resolution X-ray or vision systems, and the sealant layer must not exceed 0.1% gel count at 500 µm equivalent size to prevent false rejects. Regulatory compliance is anchored to EU Regulation (EU) No 10/2011, U.S. FDA 21 CFR 177.1520, and China GB 4806.7 for food contact plastic materials; non-food detergent refill pouches are assessed under REACH Regulation (EC) No 1907/2006 and CLP Regulation (EC) No 1272/2008 where applicable. Terminal product types include stand-up spouted pouches for baby food, liquid detergent refill pouches, beverage concentrate pouches, and wet wipe refill packs.
In extrusion lamination of paperboard and aluminium foil pouches for dry beverage powders, single-serve condiments, and pharmaceutical sachets, 20–35 wt% Exceed VLDPE 3512CB is blended into 65–80 wt% low-density polyethylene extrusion coating resin to reduce neck-in and improve seal initiation after the coated substrate is rewound and converted. The coating blend is processed on a 90–120 mm extruder with L/D 33:1, a T-slot die with internal deckles, and a melt temperature of 300–330 °C. Coating weight is controlled to 15–30 g/m² through line speed and die bolt adjustment; line speed is typically 150–250 m/min. The air gap between die exit and nip is set at 150–250 mm, and the chill roll temperature is held at 10–20 °C to limit crystallinity at the seal interface. The addition of VLDPE at 20–35 wt% to a 0.918 g/cm³ LDPE reduces neck-in but increases melt extensional viscosity; above 35 wt% the coating may draw unevenly at high line speeds and create transverse gauge bands on the laminated reel.
Adhesion of the polyethylene coating to foil or paperboard is measured by ASTM D1876 T-peel with minimum peel strength of 1.5–2.5 N/cm depending on substrate treatment; heat seal strength after conversion is measured by ASTM F88/F88M, and seal integrity by dye penetration ASTM F3039. Food-contact laminates must comply with FDA 21 CFR 177.1520 and EU Regulation (EU) No 10/2011; pharmaceutical sachets may require European Pharmacopoeia monograph 3.1.3 on polyolefins or USP <661.1> plastic packaging materials depending on the dossier. Terminal products include dry beverage powder sachets, sugar and salt portion packs, condiment sachets, and aluminium foil lids for single-serve food containers.
Under warehouse pre-stretch conditions with film gauges of 8–12 µm, the cast stretch line formulation includes 15–30 wt% Exceed VLDPE 3512CB, 70–85 wt% linear low-density polyethylene, and 1–2 wt% cling additive masterbatch based on polyisobutylene or sorbitan ester chemistry. The presence of VLDPE improves elongation at break and puncture propagation resistance without the high tackifier loadings that create roll blocking in warehouse storage. The film is produced on a cast stretch line with a 120–150 mm extruder, L/D 30:1, barrier screw, and die temperature 250–280 °C. Chill roll temperature is set at 15–25 °C; edge trim is recycled into the core layer of multilayer structures at up to 20 wt%. In three-layer A/B/A stretch films the outer layers carry the cling and slip additives while the core contains VLDPE to maintain stretch recovery; addition above 30 wt% VLDPE in machine wrap can soften the film excessively and reduce on-pallet load retention because the stress relaxation at 200% elongation increases.
Mechanical testing follows ASTM D882 for tensile properties at 500 mm/min crosshead speed, ASTM D5748 for puncture resistance, and ASTM D5458 for cling. A reference 10 µm machine wrap film with 20 wt% VLDPE typically exhibits transverse tensile elongation above 500% and puncture resistance above 0.8 J; these values shift with resin lot, tackifier type, and film gauge. The film is compliant with non-food packaging provisions of REACH Regulation (EC) No 1907/2006; shipments into North America may require heavy metal declarations under CONEG model toxics legislation. Terminal product forms include machine stretch wrap rolls, pre-stretched hand wrap, and stretch hood films for beverage and appliance pallets.
For heavy-duty liners for free-flowing mineral powders, plastic pellets, and agricultural seed sacks, three-layer blown film lines use a core containing recycled in-house trim and skin layers containing 75–90 wt% Exceed VLDPE 3512CB and 10–25 wt% linear low-density polyethylene. The blend is selected to stabilise dart impact and tear propagation at total film gauges of 100–250 µm. Processing on a heavy-duty blown film extruder with L/D 30:1 uses a die gap of 2.0–2.8 mm, a blow-up ratio of 1.8–2.4, and a die temperature of 210–240 °C. The high melt strength contributed by the low-density component prevents bubble instability when running start-up scrap above 15%; screw speed and back pressure are adjusted to hold melt pressure below 35 MPa to prevent melt fracture on the inside seal layer.
Terminal performance is tested by ASTM D1709 dart drop on 100 µm film at −20 °C, ASTM D1922 Elmendorf tear in machine and transverse directions, ISO 6383-2 trouser tear, and ISO 21898 for FIBC cycled lifting. Seal strength is measured by ASTM F88/F88M; for mineral powder sacks, a 25 mm seal strength minimum of 8–12 N/25 mm is used for release. Non-food chemical compliance is verified against REACH Regulation (EC) No 1907/2006 and RoHS Directive 2011/65/EU where export to electronics manufacturers requires heavy metal declarations. Food-grade agricultural seed sacks additionally fall under FDA 21 CFR 177.1520 and EU Regulation (EU) No 10/2011. Terminal product types include FIBC liners, bulk chemical drum liners, mineral export sacks, and agricultural seed bags used in cold-climate warehousing.
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