Topics

Ldpe Fb3003 Fe3000 And Fe8000 Decoding Producer Code Grades

LDPE FB3003, FE3000 and FE8000: Decoding Producer Code Grades

Low-density polyethylene is produced by high-pressure free-radical polymerization in autoclave or tubular reactors operating at 1000–3000 bar and 150–310°C. The polymer architecture contains both short-chain branches, primarily butyl and ethyl branches, and long-chain branches generated by intermolecular chain transfer. Long-chain branch density in commercial LDPE is typically 0.5–5 branches per 1000 carbon atoms, and this population controls melt strength, extensional viscosity and bubble stability in blown film. The producer grade codes FB3003, FE3000 and FE8000 are not universal chemical designations. Within the Lotrene product line, the F prefix identifies film-extrusion resins, while the second character separates additive/density subfamilies and the trailing four digits encode a melt-flow class. Published supplier data sheets list FB3003 and FE3000 at a nominal melt mass-flow rate of 0.30 g/10 min at 190°C/2.16 kg, and FE8000 at 0.80 g/10 min. Density values are 0.920 g/cm³ for FB3003 and 0.922 g/cm³ for FE3000 and FE8000 under ISO 1183-1. These differences are small in absolute terms but produce measurable shifts in modulus, tear balance and heat-seal initiation.

What Do the F, B and E Characters Actually Signify in the Lotrene Range?

The alphabetic portion of the code should not be read as an industry-standard comonomer or catalyst marker. LDPE is a homopolymer; the B and E characters in FB3003 and FE3000/FE8000 function as proprietary subfamily identifiers for density and film-additive packages. FB3003 is documented as a 0.920 g/cm³ film grade with a general-purpose additive formulation, while FE3000 and FE8000 are documented at 0.922 g/cm³ with heavier-duty film extrusion stabilization. The trailing digits align only partially with melt-flow behaviour: FB3003 and FE3000 share 0.30 g/10 min nominal MFR, yet their densities differ, confirming that the suffix does not carry density information. Because producer codes are not regulated, grade substitution cannot be performed by code logic alone. The ISO 1133-1:2022 melt mass-flow rate and ISO 1183-1:2019 density values on the lot certificate are the controlling physical data.

Comparative Data for LDPE Film Grades
PropertyTest MethodFB3003FE3000FE8000
Melt mass-flow rateISO 1133-1:2022, 190°C/2.16 kg0.30 g/10 min0.30 g/10 min0.80 g/10 min
DensityISO 1183-1:20190.920 g/cm³0.922 g/cm³0.922 g/cm³
Vicat softening temperature A50ISO 30694°C95°C94°C
Tensile stress at break MD/TDISO 527-325/18 MPa24/18 MPa21/17 MPa
Elongation at break MD/TDISO 527-3350/550%300/600%400/500%
Dart drop impact F50ASTM D1709A130 g140 g100 g
HazeASTM D10036%8%7%

Melt Rheology and Bubble-Stability Thresholds in Fractional-Melt Blown Film

At 190°C and a representative shear rate of 100 s⁻¹, LDPE grades with 0.30 g/10 min MFR typically exhibit apparent viscosities in the range 1200–1800 Pa·s, whereas a 0.80 g/10 min resin drops to approximately 800–1100 Pa·s. The power-law exponent for LDPE generally lies between 0.35 and 0.45, indicating strong shear thinning, but the relevant film-extrusion deformation is elongational. Long-chain branching produces strain hardening, and the fractional-melt grades FB3003 and FE3000 sustain stable stalk formation at frost-line heights of 7–10 die diameters. A die gap of 1.0–1.5 mm is required to prevent melt fracture when output rate exceeds 3.5 kg/cm·h. FE8000 allows higher screw speed but exhibits lower bubble tension at blow-up ratios above 2.5; operators typically reduce blow-up ratio to 2.0–2.2 and raise die temperature to 180–195°C to maintain gauge uniformity. A die-lip temperature deviation of 0.5°C can produce transverse gauge error of ±3% on a 350 mm die.

On a 90 mm grooved-barrier extruder with an L/D ratio of 30:1 and a 350 mm blown-film die, substituting FE3000 with FE8000 typically lowers specific energy consumption by 0.08–0.12 kWh/kg and permits 10–18% higher screw speed before head pressure reaches 350 bar. The melt filtration pack should remain at 150–250 mesh for fractional-melt LDPE; finer packs above 250 mesh cause melt-temperature overshoot above 215°C, where oxidation-induced gel formation accelerates. Hopper heating at 40–60°C is needed only when storage relative humidity exceeds 60% because LDPE moisture absorption is below 0.01% by mass. These operational boundaries are production-floor constraints, not grade datasheet optional notes.

When Downgauging Below 40 µm Exposes Tear-Balance Drift

Film downgauging below 40 µm on FE3000-based lines shifts failure away from tensile yield toward Elmendorf tear propagation. At 30 µm, FE3000 tear strength measured under ISO 6383-2 may fall to 3.5–4.0 N/mm in machine direction and 5.0–6.0 N/mm in transverse direction. FB3003 at 0.920 g/cm³ retains lower modulus and similar dart impact because thinner crystalline lamellae maintain toughness, but its lower stiffness can increase film deformation during winding. Reducing film thickness below 25 µm with FE8000 requires internal bubble cooling; without internal bubble cooling, stalk resonance produces gauge bands of ±8%. The extrusion temperature profile should progress from 150°C at the feed zone through 160/170/180°C to the die, with melt temperature controlled at 185–195°C. Melt temperatures above 200°C in FE8000 reduce elongational hardening at low draw and raise haze by 0.5–1.0% through oxidative gel dispersion.

Because density controls melting onset, the 0.920 g/cm³ FB3003 exhibits a lower seal-initiation temperature than the 0.922 g/cm³ FE grades. Differential scanning calorimetry under ISO 11357-3 generally shows peak melting at 108–112°C for these films, with FB3003 beginning melting at 101–104°C. Impulse sealing on a 300 mm wide bar at 115°C for 1.0 s can achieve bond strengths above 8 N/15 mm for FB3003, while FE3000 may require 118–122°C for equivalent hot-tack. Corona treatment to 38–42 mN/m is required before solvent-based lamination or printing; untreated LDPE film surface energy is 30–32 mN/m under ISO 8296.

Antioxidant Stabilization and Shelf-Life Boundary Conditions

LDPE film grades are stabilized with hindered phenolic primary antioxidants at approximately 300–800 ppm and organophosphite processing stabilizers at 500–1200 ppm. The exact additive loading is lot-specific and appears in the supplier certificate. FE3000 and FE8000 can be processed on high-speed cast film lines only when residual phosphite concentration survives extended residence time; repeated extrusion passes consume stabilizer and reduce oxidative induction time. Under ISO 11357-6 at 200°C, an oxidative induction time below 20 minutes indicates critical antioxidant depletion for long-term outdoor exposure. Natural LDPE without carbon black or hindered amine light stabilizer embrittles after 6–12 months of ultraviolet exposure; inclusion of 2.0–3.0 wt% carbon black masterbatch or a suitable UV stabilizer system is required for outdoor durability.

Regulatory and Test Designation Checklist
Regulation or StandardClause or MethodCondition or Limit
EU Regulation 10/2011Annex III overall migration≤10 mg/dm² for food-contact film
FDA 21 CFR 177.1520Olefin polymer specificationsExtractable fraction depends on food type and temperature
ISO 1133-1:2022Method A, 190°C/2.16 kgMelt mass-flow rate
ISO 1183-1:2019Method DDensity of solid film
ISO 6383-2Elmendorf tearMD/TD tear propagation
ISO 8296Wetting tension measurementCorona-treated film 38–42 mN/m

Product substitution using only the four-character producer code is technically insufficient. The melt-flow class embedded in FB3003, FE3000 and FE8000 requires verification against ISO 1133-1:2022 because the same code can conceal additive-package differences, lot-to-lot viscoelastic drift and storage-derived stabilizer loss. Density must be verified under ISO 1183-1:2019, and downstream film properties must be assessed at the intended gauge, blow-up ratio and frost-line height. For food-contact applications, the specific migration limits of EU Regulation 10/2011 and the olefin polymer requirements of FDA 21 CFR 177.1520 govern the final compliance position.

Top