| HS Code | 316049 |
| Productname | Chevron Phillips Marlex mLLDPE D173 |
| Polymertype | Metallocene Linear Low Density Polyethylene (mLLDPE) |
| Comonomer | Hexene |
| Catalysttype | Metallocene |
| Density | 0.917 g/cm³ |
| Meltindex | 0.9 g/10 min (190°C/2.16 kg) |
| Meltingpoint | 115 °C |
| Vicatsofteningpoint | 93 °C |
| Tensilestrengthatyield | 8.3 MPa |
| Tensilestrengthatbreak | 28 MPa |
| Elongationatbreak | 600% |
| Secantmodulus1percent | 172 MPa |
| Dartdropimpact | 250 g |
| Elmendorftearmd | 250 g |
| Elmendorfteartd | 400 g |
| Haze | 7% |
| Gloss | 65% |
| Coefficientoffriction | 0.2 |
As an accredited Chevron Phillips Marlex mLLDPE D173 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Chevron Phillips Marlex mLLDPE D173 is packaged in 25 kg moisture-proof PE bags, with 1,000 kg bulk bags available. |
| Container Loading (20′ FCL) | 20′ FCL container loaded with Chevron Phillips Marlex mLLDPE D173 polyethylene resin in bags, palletized and secured for ocean shipment. |
| Shipping | Chevron Phillips Marlex mLLDPE D173 is shipped as free-flowing polyethylene pellets in moisture-protected 25 kg bags or bulk containers. Store in a cool, dry, ventilated area away from direct sunlight, heat, and ignition sources; keep packaging sealed during transport and storage to prevent contamination and moisture ingress. |
| Storage | Store Chevron Phillips Marlex mLLDPE D173 in a cool, dry, well-ventilated area away from direct sunlight, heat, and ignition sources. Keep original containers or bags closed and palletized off the floor to prevent moisture, dirt, and contamination. Avoid prolonged UV exposure, maintain good housekeeping, follow the SDS and local regulations, and use first-in, first-out stock rotation. Store separately from incompatible materials. |
| Shelf Life | Under recommended storage conditions, Marlex mLLDPE D173 has a typical shelf life of about two years from manufacture. |
On blown-film lines producing heavy-duty shipping sacks with finished film thickness between 85 µm and 130 µm, Chevron Phillips Marlex mLLDPE D173 is introduced at 60–80 wt% alongside a high-pressure LDPE of melt index 0.25–0.5 g/10 min to stabilize the bubble against fluttering at high frost line heights. D173 is a metallocene-catalyzed hexene copolymer with nominal density 0.917 g/cm³ and melt index 0.9 g/10 min measured at 190 °C/2.16 kg per ASTM D1238 / ISO 1133-1:2022. Grooved-feed extruders with L/D 30:1 or higher and barrier screws optimized for linear polyethylenes are used; production settings include barrel temperatures from 185 °C in the feed section to 205 °C at the die, die gap 1.8–2.2 mm, blow-up ratio 2.2–2.8, and frost line height between 3 and 5 die diameters. The narrow molecular weight distribution of D173 reduces residence-time-dependent viscosity drift but increases back-pressure sensitivity relative to conventional Ziegler-Natta LLDPE; a melt pressure rise above 420 bar at the screen changer indicates gel accumulation and requires filter pack replacement. Heavy-duty sack formulations often include 2–4 wt% of a 20% silica-based antiblock masterbatch and 0.5–1.5 wt% erucamide slip masterbatch, but slip migration to seal surfaces can reduce seal strength after warehousing; for sacks that are stitched or heat-sealed, slip loading is kept at the lower end unless a controlled COF below 0.35 is required. The primary performance target is dart drop impact retention after downgauging; a 100 µm D173-rich film can maintain a dart drop impact above 800 g under ASTM D1709 Method A and Elmendorf tear above 12 N in the machine direction per ASTM D1922, but published data for D173-specific formulation is limited and should be verified on the target film line because variable frost line turbulence can shift results by 15–25%. The finished web is converted into sewn-open-mouth sacks, pinch-bottom sacks, and dunnage air bags for polymer resin, construction aggregate, and bulk agricultural commodities; dense paper laminates using D173 as a moisture barrier coating also enter this segment when total basis weight is reduced from 110 g/m² to 85 g/m². Regulatory status under FDA 21 CFR 177.1520(c) applies only to direct food contact; industrial sack uses are typically excluded from EU food-contact migration testing, but converters should still confirm REACH registration and RoHS recast 2011/65/EU for non-food marketing.
D173 is carried in the sealant layer during dry lamination of printed polyester or biaxially oriented polypropylene to a blown mLLDPE sealant web, with finished sealant layer thickness from 30 µm to 60 µm and total laminate thickness from 65 µm to 90 µm. The metallocene-catalyzed hexene copolymer provides a broader hot-tack plateau than conventional LLDPE, which reduces leaker formation at seal jaw temperatures between 95 °C and 130 °C. A coextruded blown film structure of 20/60/20 or 25/50/25 (D173 skins over a core of LDPE or metallocene VLDPE) is employed to keep seal initiation below 100 °C while maintaining stiffness in the laminate. Seal strength measured by ASTM F88 typically reaches a plateau above 12 N/25 mm for a 45 µm sealant web once the seal bar temperature exceeds 115 °C; however, published data for D173-specific hot tack and seal initiation is limited, and converter trials should verify against actual dwell time and jaw geometry. The sealant web is often corona-treated to 38–42 mN/m for adhesive lamination; surface wetting below 36 mN/m produces inconsistent adhesive coverage. For food contact, D173 falls under FDA 21 CFR 177.1520(c) as an olefin polymer, but the final laminate must be tested under 21 CFR 177.1390 or appropriate end-use conditions because migration of adhesives and printing inks is not covered by the resin compliance. Under EU Regulation (EU) No 10/2011, overall migration must not exceed 10 mg/dm² in the specified simulant; for fatty foods, simulant D1 or D2 may require a barrier layer if the D173 web contains processing aids above permitted levels. In vertical pouch lines, sealant web thickness variation greater than ±4 µm can cause jaw pressure to shift from 2.5 bar to 3.5 bar and create leakers; D173 lot-to-lot melt index variation is controlled tightly, but converter experience indicates that pre-drying is not normally required unless storage humidity exceeds 70% RH in open silos. Finished applications include stand-up pouches for dry mixes, frozen seafood pouches, and quart-size snack bags where the D173 sealant layer permits seal-through-moisture performance better than conventional LLDPE at high seal speeds.
For frozen food packaging of individually quick-frozen vegetables, meat cuts, and prepared seafood, the film must remain ductile at temperatures down to −30 °C after filling and freezing. D173 with density 0.917 g/cm³ is incorporated as the outer skin and seal layer in three-layer and five-layer blown coextrusions with EVOH or polyamide barrier cores. The low density limits the brittle transition shift caused by secondary crystallization during frozen storage; conventional Ziegler-Natta LLDPE at 0.918 g/cm³ may show a sharp dart impact drop when film is stored at −25 °C for 14 days, whereas D173-containing structures typically retain a substantial portion of room-temperature impact strength. A target specification for 70 µm frozen food web is dart drop impact above 700 g at −35 °C using ASTM D1709 Method A and puncture resistance above 90 N by ASTM D5748; these values are converter-defined targets rather than published D173 guarantees. Coextrusion line conditions include die gap 1.8–2.4 mm, blow-up ratio 2.0–2.6, and melt temperature at the die of 195–210 °C; in five-layer lines, D173 is isolated from EVOH by adhesive tie resin because direct contact causes unstable layer interfaces and reduced optical quality. The film is surface-printed or laminated to PET; if printed, corona treatment is maintained between 40 and 44 mN/m. The limiting operational boundary is moisture migration from the frozen product to the seal area; if seal bar contamination with ice crystals occurs, hot-tack strength measured by ASTM F1921 at 0.3 s dwell drops below the clean-surface baseline by about 20–40%. Finished packs range from 200 g retail frozen vegetable pouches to 2.5 kg institutional meat bag-in-box liners. Use of D173 at high layer percentages above 70% in a monolayer frozen food film is possible but usually requires addition of 10–20 wt% HDPE to reduce blocking, which can sacrifice low-temperature impact and is therefore limited to less demanding frozen non-meat applications.
| Application segment | Relevant standard or regulation | Practical boundary or target |
|---|---|---|
| Heavy-duty shipping sacks | ASTM D1709 Method A, ASTM D1922, ISO 527-3 | 100 µm film target dart > 800 g; MD tear > 12 N |
| Food sealant web | FDA 21 CFR 177.1520(c), Regulation (EU) No 10/2011, ASTM F88, ASTM F1921 | Overall migration ≤ 10 mg/dm²; seal plateau > 12 N/25 mm at 115 °C |
| Frozen food packaging | ASTM D1709 Method A, ASTM D5748, ASTM F1921 | 70 µm web target dart > 700 g at −35 °C; puncture > 90 N |
| Silage wrap | ASTM D5748, ISO 4892-3 | 25 µm film puncture > 4,500 mN; tensile retention ≥ 50% after 1,000 h UV |
| Stretch hood film | ASTM D5459, ISO 527-3 | Elastic recovery > 85% at 50% elongation; pre-stretch ≤ 80% |
| VFFS sealant layer | ASTM F1921 | Hot-tack 4–6 N/25 mm at 0.3 s dwell, 30 µm layer |
Agricultural bale wrap manufactured from D173-based blown film is usually converted at widths from 500 mm to 750 mm and thicknesses of 25–38 µm. The key mechanical demand is not tensile yield but puncture propagation resistance when film is stretched over haylage or maize silage bales with protruding stems. Formulations for this segment typically combine 65–80 wt% D173 with 15–25 wt% EVA or PIB-based cling masterbatch and 3–5 wt% white or UV-stabilized concentrate containing HALS at 6,000–10,000 ppm and a benzotriazole UV absorber at 2,000–4,000 ppm of the final film. The polyethylene matrix must be pre-stretched to 60–75% on turret wrappers; D173 provides the extensional viscosity needed to resist localized thinning but can develop high unwind force if the cling layer migrates. Wind-up tension is typically set to 8–12 N for 500 mm rolls to prevent blocking while preserving roll geometry. Puncture resistance is measured by ASTM D5748 with a 19 mm diameter probe; silage wrap specifications often require values above 4,500 mN at 25 µm thickness, but published D173-specific data is limited because such values depend on the concentration of tackifier and the amount of pre-stretch. Tear resistance and retention after UV aging are critical: after 1,000 h exposure to UVA-340 cycle conditions per ISO 4892-3, the film should retain at least 50% of initial tensile strength. The operational boundary is additive compatibility; amine-based HALS can be poisoned by agricultural chemicals using acidic preservatives on silage, and the converter should avoid direct contact of acidic silage inoculants with unstabilized edge trim. The finished product is applied in 4–6 layers over a round bale; insufficient overlap below 50% creates oxygen ingress and mould growth, while D173-based film with good puncture resistance reduces punctures during application on stem-rich haylage.
In pallet unitization, stretch hood film uses D173 in blown tubes from 40 µm to 80 µm, typically blended with 20–40 wt% LDPE and 5–8 wt% of a cling or slip control masterbatch dependent on the pallet surface. The film tube is drawn over a pallet load and released to recover; the critical property is elastic recovery after stretching to 50–70%, not absolute tensile strength. D173 with a density of 0.917 g/cm³ contributes a more uniform short-chain branching distribution than conventional hexene LLDPE, which reduces the coefficient of variation in MD/CD tensile ratio; converter evaluations show that tube width variation at the gusset can be held below ±5 mm on a 1.2 m collapsed frame. In blown film production, a die gap of 2.0–2.4 mm with BUR 2.0–2.5 and melt temperature 190–210 °C is used to balance MD and CD properties. The recovery force applied to the pallet is measured by ASTM D5459 and the elastic recovery at 50% elongation by ISO 527-3 can exceed 85% for D173-based hood film, but converters should regard this as a comparative target because published D173-specific values are limited. High unwind speed on an automatic stacker can cause blocking if the film surface temperature exceeds 35 °C in storage; antiblock loading is increased to 4–6 wt% of a 20–30% silica masterbatch when roll storage is not climate-controlled. Stretch hood films are not generally classified as food-contact unless the wrapped goods are primary food packages; when food contact is possible, the relevant Regulation (EU) No 10/2011 and FDA 21 CFR 177.1520(c) status of the D173 resin must be re-evaluated for the final compound because cling additives and antiblock masterbatch components may have separate migration limits. The finished pallet unitization film is applied with pre-stretch ratios between 50% and 80%; above 80%, the mLLDPE structure may undergo stress whitening and partial plastic deformation, leading to reduced holding force after transport vibration and temperature cycling.
Vertical form-fill-seal operations running at 40–80 packs per minute place narrow dwell time constraints on heat seal performance; the sealant layer in the back-seam and bottom seal must develop cohesive strength before the falling product exerts load. D173 is used in the inside layer of coextruded web for dry and frozen products at 20–35 µm layer thickness because its hot-tack peak occurs at relatively low temperature and remains broad enough to accommodate jaw temperature fluctuation of ±15 °C without leaker formation. Seal jaw settings in this segment are typically 115–140 °C, dwell time 0.2–0.5 s, and jaw pressure 2.5–4.0 bar; product temperature below 5 °C for frozen lines reduces heat transfer into the seal interface, and D173 is preferred over higher-density LLDPE because the lower melting plateau allows the interface to reach seal initiation earlier in the dwell cycle. Hot-tack force measured by ASTM F1921 at 0.3 s dwell commonly reaches 4–6 N/25 mm for a 30 µm sealant layer; published D173-specific data is limited, so converter trials with actual product contamination and film temperature are required. The outer layer of the structure is often a higher-modulus LLDPE or HDPE to provide stiffness and machinability; when D173 is used as the inside skin, the film surface coefficient of friction must be reduced with erucamide slip at 0.5–1.0 wt% of the skin layer, but too high slip loading can compromise seal strength by blooming to the seal interface. Processing the film over polished chill rolls at 35–45 °C after blowing reduces film blocking and static; the winding tension is set to 0.4–0.6 N/mm of film width. Applications include dry powder beverage mixes, confectionery, frozen chopped vegetables, and pet food pouches; the containment of dusty or granular products demands that the sealant layer resist contamination by fines, and D173-based films are generally run with start-up purge of 2–4 kg and a lower seal jaw temperature ramp of 10 °C/min until stable. No pre-drying is required under normal warehouse conditions, but film stored at elevated humidity above 70% RH should be conditioned in the packaging hall for 12–24 h before use to prevent condensation on the seal surface.
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Chevron Phillips Marlex mLLDPE D173 is a metallocene-catalyzed ethylene-hexene linear low density polyethylene resin supplied as free-flowing pellets. The manufacturer’s current technical data sheet identifies a nominal melt index of 1.0 g/10 min when tested according to ASTM D1238 at 190 °C with a 2.16 kg load, and a nominal density of 0.917 g/cm³ when tested according to ASTM D1505. The grade’s hexene comonomer and metallocene catalyst produce a narrow molecular weight distribution and a controlled short-chain branching distribution. These structural features differentiate D173 from conventional butene-based Ziegler-Natta LLDPE at equivalent density and melt index. The resin is specified for monolayer and coextruded blown film structures where lower seal initiation, higher dart impact resistance, and downgauging capability are required by converters in frozen food, heavy-duty sack, and collation shrink applications. The lot release properties on a certificate of analysis typically include melt index and density; film impact, tear, and seal values are not lot release specifications because they are strongly influenced by die gap, blow-up ratio, frost line height, and cooling configuration.
| Property | Nominal value | Test method |
|---|---|---|
| Melt index | 1.0 g/10 min | ASTM D1238 / ISO 1133-1:2022 |
| Density | 0.917 g/cm³ | ASTM D1505 / ISO 1183-1:2019 |
The hexene comonomer in D173 introduces short-chain branches longer than those found in butene-based LLDPE. During blown film quenching, this branch length distribution increases the probability of tie-chain formation between lamellae. Under ASTM D1709 dart impact testing of a 25 µm monolayer film, the improved interlamellar connectivity is typically expressed as higher energy dissipation before crack propagation; however, the exact dart drop value depends on blow-up ratio, frost line height, and die gap. The lower crystalline melting peak of D173 relative to a butene-based resin of comparable density can be confirmed by differential scanning calorimetry according to ASTM D3418. Hot-tack performance measured by ASTM F1921 is governed by the rate at which the seal interface solidifies after the sealing bar opens. Because D173 melts over a narrower temperature range and has a lower melting peak than a comparable C4-LLDPE, the hot-tack window shifts toward lower seal bar temperatures. On a jaw-type heat seal tester with a 0.5 s dwell and 0.275 MPa seal bar pressure, the seal initiation temperature for a 25 µm monolayer film is commonly reported below 110 °C. Published data for this specific configuration is limited, and converter-generated SIT curves on the target packaging machine are required to define the upper and lower sealing limits.
Downgauging trials focus on maintaining dart impact values measured under ASTM D1709 at reduced gauge. The exact gauge reduction permitted by D173 depends on the incumbent resin, die gap, blow-up ratio, and frost line height. Published data for this specific configuration is limited. Tear resistance measured under ASTM D1922 often limits downgauging before dart impact becomes the controlling variable. The film’s secant modulus under ASTM D882 is lower than that of HDPE or higher density LLDPE because the density is 0.917 g/cm³; therefore, D173 is placed in the sealant or toughness layer rather than in the core layer of coextruded structures.
Because D173 is produced with a metallocene catalyst, the resin has a narrower molecular weight distribution and lower shear viscosity than a conventional LDPE of equivalent melt index. In high-stalk operations, the reduced extensional viscosity can lower bubble stability when the blow-up ratio exceeds 3.0:1 or when the frost line height is below 200 mm. In low-stalk operations, die gap settings below 1.5 mm raise the shear stress at the die land and can initiate melt fracture at line-specific output rates. The onset of melt fracture is identified by surface roughness or spiral haze on the film; this is controlled by increasing die gap to 2.0 mm to 2.5 mm, reducing output, or raising the die temperature to 220 °C to 230 °C. The temperature ceiling of 230 °C is applied to limit oxidative degradation of the polymer and additive package; above this limit, gel counts measured on a standardized film surface area increase. The use of an internal bubble cooling system can extend output capability, but the manufacturer does not state a maximum output rate independent of line design. On production-scale lines with a 55 mm single-screw extruder and a 30:1 L/D screw, a barrel temperature profile from 180 °C at the feed throat to 220 °C at the adapter is representative for blown film conversion. Converter experience indicates that a common failure mode when switching from LDPE to D173 is bubble instability if the air ring is not adjusted; the lower extensional viscosity draws the bubble down more rapidly, and operators compensate by lowering melt temperature or increasing frost line height.
Blending D173 with 10 wt% to 30 wt% LDPE is used to improve bubble stability on lines designed for LDPE. The LDPE fraction increases extensional viscosity and reduces the risk of bubble sag. However, the addition of LDPE raises seal initiation temperature and reduces dart impact; the converter must balance these effects with measured ASTM F88 and ASTM D1709 values. At LDPE addition levels above 30 wt%, the mechanical and seal advantages of D173 are progressively reduced. Published data for this specific configuration is limited; blend optimization remains an empirical exercise on the production line. For additive functions, slip and antiblock masterbatches are introduced at letdown ratios of 2 wt% to 5 wt% for silica-based antiblock and 1 wt% to 2 wt% for erucamide slip. The migration kinetics of erucamide in the polymer matrix are temperature-dependent; a film stored at 23 °C typically requires aging periods of 48 h or longer before the coefficient of friction reaches a kinetic steady state under ASTM D1894. Overloading of low-molecular-weight amide waxes can produce rapid surface bloom that reduces seal strength under ASTM F88.
Replacement of a butene-based C4-LLDPE with D173 in an existing multilayer food film requires revalidation of seal strength, hot-tack force, and coefficient of friction. Seal strength measured by ASTM F88 is expected to increase at seal bar temperatures below 110 °C because the hexene comonomer lowers the temperature at which chain interdiffusion across the interface becomes measurable. Hot-tack force measured by ASTM F1921 must be mapped at the actual packaging line speed, because hot-tack is controlled by both seal bar cooling rate and resin crystallization kinetics. Coefficient of friction measured by ASTM D1894 may shift due to differences in slip agent migration kinetics; converters commonly observe that the required slip additive concentration differs from the C4-LLDPE baseline. The film’s blocking force under ASTM D3354 should be tested after 24 h and 48 h aging at 23 °C and 50% relative humidity to verify that the chosen antiblock loading is sufficient. Seal strength should be generated at 0.25 s, 0.5 s, and 1.0 s dwells to capture the full sealing curve. Published data for this specific configuration is limited; the transition must be qualified with internally generated SIT curves and visual inspection for gel or streak defects.
For frozen food and bag-in-box applications, D173 is formulated with slip and antiblock masterbatches before extrusion. The seal layer is coextruded with a core of HDPE or higher density LLDPE at total film gauges of 20 µm to 80 µm. Peel strength measured under ASTM F88 is used to set packaging line sealing conditions. Because D173 is a hexene-based mLLDPE, it is not suited to applications requiring high-temperature hot-fill or retort conditions above 121 °C; polypropylene or high-density polyethylene structures are required for those thermal loads. In heavy-duty sack production, D173 is typically processed as the seal layer in a three-layer coextrusion alongside a higher density LLDPE or HDPE core. The core supplies stiffness for stand-up handling of filled bags weighing 20 kg to 50 kg; the D173 seal layer contributes puncture resistance measured by ASTM D5748 and tear propagation resistance measured by ASTM D1922. Stable bubble formation is maintained at a blow-up ratio of 2.5:1 and a melt temperature of 210 °C to 220 °C on a conventional low-stalk line. Failure modes observed when the die temperature exceeds 230 °C include increased gel particle formation and surface roughness that lowers the down-gauging capability of the seal layer. The resin is not normally pre-dried at ambient storage below 60% relative humidity; if condensation exposure has occurred, a desiccant bed at 70 °C for 2 h is used before extrusion.
Chevron Phillips Marlex mLLDPE D173 is represented as complying with U.S. Food and Drug Administration regulation 21 CFR 177.1520 for olefin polymers. The applicable conditions of use for the resin as a food-contact article or component are set by the paragraph (c) tables in the regulation; the user must confirm that the final article meets end-use temperature and food-type restrictions. Under European conditions, the resin is evaluated against Regulation (EU) No 10/2011 for plastic materials and articles intended to come into contact with food. Compliance for specific migration limits is article dependent and must be verified on the final film. The resin is also subject to general chemical control requirements under REACH Regulation 1907/2006/EC and to restrictions on heavy metals and flame-retardant substances under Directive 2011/65/EU. The matrix below summarizes the often-referenced compliance pathways, not the full regulatory file.
| Regulation | Citation | Test/condition |
|---|---|---|
| U.S. food contact | 21 CFR 177.1520(c) | Olefin polymer, end-use condition of use per FDA tables |
| EU plastic food-contact | Regulation (EU) No 10/2011 | Overall migration and specific migration limits per final article |
| REACH | 1907/2006/EC | Substance registration and SVHC screening |
| RoHS | Directive 2011/65/EU | Restricted substances below specified maximum concentrations |
In lamination and heavy-duty bag converting, D173 is compared with higher melt index sealant resins and with lower melt index mLLDPE grades to manage the trade-off between output rate and bubble stability. A converter using a 45 mm single-screw extruder with a 24:1 L/D screw and a 2.0 mm die gap may select D173 over a 0.5 g/10 min mLLDPE because the higher melt flow reduces die pressure and permits thinner gauge without exceeding the extruder drive current. The differences from other products in the Marlex mLLDPE line are defined primarily by melt index and density; D173’s nominal 1.0 g/10 min melt index and 0.917 g/cm³ density position it for thin-gauge seal layers rather than high-stiffness core layers. When a film structure must meet a specific dart impact value under ASTM D1709 at 25 µm, the converter should run comparative sleeve trials against the incumbent resin because film properties are influenced as much by die gap, blow-up ratio, and frost line height as by resin type. Published data for this specific configuration is limited; the final grade selection is therefore based on measured film property values, not on nominal resin properties alone.