| HS Code | 350866 |
| Density | 0.920 g/cm3 |
| Melt Index | 1.0 g/10 min |
| Comonomer | Butene |
| Polymer Type | Linear Low Density Polyethylene (LLDPE) |
| Tensile Strength At Yield | 10.3 MPa |
| Tensile Strength At Break | 26.2 MPa |
| Elongation At Break | 1000% |
| Flexural Modulus | 207 MPa |
| Dart Drop Impact | 120 g |
| Elmendorf Tear Strength Md | 250 g/mil |
| Elmendorf Tear Strength Td | 400 g/mil |
| Haze | 12% |
| Gloss | 60% |
| Melting Point | 122 °C |
| Vicat Softening Point | 100 °C |
| Brittleness Temperature | -70 °C |
As an accredited Chevron Phillips 6120 LLDPE Cast/Blown Film Resin, Butene Copolymer factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
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High-speed cast pallet stretch film operations running Chevron Phillips 6120 butene-copolymer LLDPE in the core layer operate with a nominal resin density of 0.918 g/cm³ under ASTM D1505 and a nominal melt index of 1.0 g/10 min under ASTM D1238 at 190°C/2.16 kg. The formulation addition ratio for 6120 is held between 60 wt% and 80 wt% in the core layer, with metallocene octene LLDPE at 10–30 wt% and low-density polyethylene at 5–15 wt% in adjacent layers to manage dart impact and edge-trim uniformity. A tackifier-bearing polyisobutylene cling masterbatch is added at 1.0–2.5 wt% in the cling layer, while a silica anti-block masterbatch at 0.5–1.5 wt% is used on the opposite outer layer. Above 3.0 wt% anti-block, cling force measured under ASTM D5458 drops below 0.40 N, which is the lower bound observed on automated pallet wrapping lines operating at 2.5–3.0 m/s film feed rate. The compliance framework for industrial stretch film is not food-contact-specific; it falls under EU Packaging and Packaging Waste Directive 94/62/EC Article 11 with a combined lead, cadmium, mercury, and hexavalent chromium limit of 100 mg/kg. Physical property verification uses ASTM D5748 for trapezoidal tear propagation and puncture resistance, ASTM D882 for machine-direction and transverse-direction tensile yield, ASTM D1922 for Elmendorf tear, and ASTM D1894 for kinetic coefficient of friction.
On production lines, the resin is processed through a single-screw extruder with L/D 30:1, a barrier screw with Maddock mixing tip, and screen pack of 60/80/100 mesh. The cast die gap is set at 0.5–0.8 mm, melt temperature at 235–250°C, and the air gap between die lip and chill roll at 20–40 mm. The chill roll temperature is maintained at 15–25°C. When chill roll temperature falls below 12°C at line speeds above 400 m/min, condensation on the chill roll can create pinholes at frost bands, and the edge trim tends to fracture under oscillation from the air knife. Melt temperatures above 255°C increase gel count and produce die-lip deposit from degraded polyisobutylene cling additive. The terminal product types include machine stretch film slit to 500 mm at 20–23 µm, hand-held stretch film slit to 450 mm at 12–17 µm, and heavy-duty pallet wrap slit to 750 mm at 25–35 µm.
| Cast film gauge | Chill roll temperature | Line speed | Slit width and film type |
|---|---|---|---|
| 12–17 µm | 15–20°C | 350–500 m/min | 450 mm hand stretch film |
| 18–23 µm | 18–25°C | 300–450 m/min | 500 mm machine stretch film |
| 25–35 µm | 20–25°C | 250–350 m/min | 750 mm heavy-duty pallet wrap |
Seal initiation in blown food-contact webs based on 6120 is governed less by nominal melting point than by the distribution of short-chain branches introduced by the butene comonomer. The food-contact layer is typically compounded at 70–85 wt% 6120 with 10–20 wt% LDPE and 5–15 wt% linear medium-density polyethylene for stiffness. Slip and anti-block masterbatches are added at 1.0–2.0 wt%, and fluoropolymer-free polymer processing aid is used at 200–800 ppm. Elevated processing aid above 1,000 ppm can interfere with heat seal strength in the finished laminate; seal strength is measured under ASTM F88/F88M-21 at 0.5-second dwell and 2.8 bar jaw pressure. The butene-copolymer structure widens the seal initiation range, and the measured seal initiation temperature is typically between 85°C and 95°C on crimp sealers with 0.5-second dwell. At heat-seal jaw temperatures above 130°C, high-crystallinity fractions in the butene LLDPE cause zoned seal deformation and inconsistent seal width.
Extrusion is carried out on three-layer blown film lines with die gap 1.8–2.5 mm, blow-up ratio 2.2–2.8, melt temperature 190–210°C, and output 2–4 kg/h/mm die circumference. Frost line height is set between 6 and 9 die diameters to balance bubble stability and tear resistance. Air ring and internal bubble cooling are operated with moderately low cooling rates to prevent the butene-copolymer film from excessive crystalline orientation that raises haze above 12% measured by ASTM D1003. The downstream production process includes corona treatment to 38–42 mN/m before lamination or printing. Terminal product types include frozen vegetable bag film at 60–80 µm, fresh-cut produce lidding substrate at 20–40 µm, and vertical form-fill-seal webs for dry food powder sachets at 40–60 µm.
| Standard or regulation | Clause or test method | Measured boundary |
|---|---|---|
| FDA 21 CFR 177.1520(c) | Olefin polymers for direct food contact | Conditions of use B through H; extractables limited by paragraph (d) |
| Regulation (EU) No 10/2011 | Annex I, Annex III, Annex IV | Overall migration limit 10 mg/dm²; simulant selection per Annex III food categories |
| EC 1935/2004 | Articles 3, 11, 15 | No transfer of constituents in quantities endangering human health |
| Commission Regulation (EC) No 2023/2006 | Annex | Good manufacturing practice for food-contact material production |
| REACH EC 1907/2006 | Annex XVII | Restricted heavy metal and PAH limits for packaging components |
In heavy-duty form-fill-seal packaging of granular fertilizers, chemical intermediates, and polymer pellets, 6120 is compounded at 60–75 wt% with high-density polyethylene at 15–25 wt% and metallocene LLDPE at 10–20 wt%. The HDPE fraction increases secant modulus, but above 25 wt% the Elmendorf tear measured by ASTM D1922 drops below 5 N at 140 µm thickness, creating a formulation ceiling that is not present at 180 µm. Carbon black UV masterbatch is added at 1–2 wt%, and an antioxidant/acid-scavenger masterbatch at 0.1–0.3 wt% if the sack is destined for products containing residual metal ions. The compliance framework for non-food heavy-duty sacks relies on ISO 527-3:2018 for tensile strain at break, ASTM D3786/D3786M-20 for burst strength, ASTM D1922 for propagation tear, and ASTM F392/F392M-23 for flex-crack resistance in multilayered constructions. When an end user requires transport packaging for dangerous goods, the full sack-and-filling construction must be qualified separately under the relevant UN transport packaging performance test; film resin data alone is not sufficient for that classification.
Extrusion is performed on a three-layer blown film line with die diameter 400–600 mm, die gap 2.0–2.8 mm, blow-up ratio 2.0–2.5, and melt temperatures 180–205°C. Internal bubble cooling is required above 160 µm thickness. Output drops from 3.0 kg/h/mm die circumference to 1.8–2.2 kg/h/mm when the bubble is undercooled because the butene LLDPE crystalline network builds too slowly, causing web bagging at the collapsing frame. Frost line height is set at 7–10 die diameters. Corona treatment is applied after the collapsing frame at 38–42 mN/m for printability. Terminal articles include 120–180 µm polymer pellet sacks, 150–220 µm mineral filler bags, and 140–200 µm pet food sacks with gusseted side seams.
Agricultural silage wrap produced from 6120 at film thickness below 25 µm requires a blend of 60–80 wt% 6120 with 10–20 wt% metallocene LLDPE and 5–15 wt% EVA or polar copolymer. The butene comonomer distribution in 6120 yields a broader melting range that can absorb stress during bale wrapping at −10°C, but dart impact measured by ASTM D1709 drops sharply when the film is oriented at blow-up ratios above 3.5. UV stabilization is introduced through a HALS-based masterbatch at 5–10 wt%; white pigment masterbatch is added at 8–12 wt% for light reflection and thermal load reduction. Compliance for agricultural silage films is governed by EN 13207:2018 for mechanical specifications, ISO 527-3:2018 for tensile elongation, ASTM D1922 for tear resistance, and ASTM D1709 for puncture impact. Under REACH EC 1907/2006 Annex XVII, the formulation must avoid cadmium-, lead-, and chromium-based pigments above restricted thresholds.
Process conditions on a three-layer blown film line include die gap 1.8–2.5 mm, blow-up ratio 2.5–3.5, melt temperature 185–205°C, and internal bubble cooling to stabilize the high blow-up ratio. At thicknesses from 25 µm to 50 µm, the film is wound as wide-web bale wrap. Thicker products include pit covers at 150–200 µm and greenhouse films at 150–200 µm. A process incompatibility occurs when recycled silage film contains soil residue: quartz particles of 10–30 µm create tear propagation sites in films below 20 µm, so filtration through a 100–150 mesh screen pack is required when post-industrial regrind exceeds 10 wt%. Terminal product types include bale wrap at 25–30 µm, silage pit cover at 150–200 µm, greenhouse cover film at 150–200 µm, and agricultural mulch film at 15–25 µm.
In breathable cast backsheet lines for absorbent hygiene articles, 6120 is evaluated only as the polymer fraction in a calcium carbonate-filled microporous web and is not run neat. The formulation addition ratio begins with 45–55 wt% surface-treated calcium carbonate masterbatch, with 6120 occupying 30–45 wt% of the total compound, metallocene octene LLDPE at 10–15 wt%, and LDPE at 5–10 wt%. The calcium carbonate is specified at 1.2–2.0 µm median particle size with stearic acid surface coating. Moisture content of the filled compound is maintained below 200 ppm before extrusion; above this limit, hydrolytic degradation produces pinholes and reduces machine-direction orientation uniformity. Titanium dioxide is added at 1–3 wt% for opacity and ultraviolet scattering. Compliance for non-medical absorbent hygiene backsheet falls under General Product Safety Directive 2001/95/EC, REACH EC 1907/2006 Annex XVII, and ISO 10993-5:2009 when the finished article is a component of a medical device. The downstream production process is cast extrusion followed by embossing and machine-direction orientation at a stretch ratio of 2.5:1–3.5:1; die gap is set at 0.6–0.8 mm, melt temperature at 220–245°C, and line speed at 150–300 m/min. If the production environment exceeds 60% RH, the calcium carbonate masterbatch is pre-dried at 80°C for 4–6 h. Terminal product types include diaper backsheet at 12–20 µm, adult incontinence backsheet at 20–35 µm, and feminine hygiene strip film at 12–18 µm. Published data specific to 6120 in high-filler breathable cast configurations is limited; pre-production trials across the orientation gap and embosser pressure are required before commercial output.
For protective masking films applied to stainless steel sheet, anodized aluminum, and pre-painted coil, 6120 is formulated at 70–90 wt% with LDPE at 10–30 wt% and an adhesion-modifying polyolefin masterbatch at 1–3 wt%. The low-molecular-weight fraction of 6120 affects both corona holding time and the peel force after application to flat metal. Slip and anti-block are limited to 0.5–1.5 wt% because higher slip loadings cause surface energy decay from 42 mN/m to below 36 mN/m within 30 days, compromising adhesion under shear. The compliance framework for electronics-protecting films includes RoHS 2011/65/EU Annex II restricted substance limits and REACH EC 1907/2006 Annex XVII; metal-facing protective films used in prolonged outdoor storage are additionally tested under ISO 4892-3:2016 UV exposure protocols. Processing is conducted on a cast film line at melt temperature 220–250°C, die gap 0.5–0.8 mm, chill roll temperature 15–25°C, and line speed 200–400 m/min. Corona treatment is applied at 38–42 mN/m. Terminal product types include 30–50 µm stainless steel sheet protection, 50–70 µm pre-painted coil masking, and 30–40 µm acrylic sheet protective film.
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