| HS Code | 758385 |
| Density | 0.918-0.922 g/cm³ |
| Meltflowrate | 2.0 g/10min (190°C/2.16kg) |
| Tensilestrengthatyield | ≥8.0 MPa |
| Tensilestrengthatbreak | ≥20.0 MPa |
| Elongationatbreak | ≥500% |
| Dartimpactstrength | ≥80 g |
| Haze | ≤15% |
| Meltingpoint | 120-125°C |
| Vicatsofteningpoint | ≥90°C |
| Brittlenesstemperature | ≤-70°C |
| Bulkdensity | 0.50-0.60 g/cm³ |
| Ashcontent | ≤0.05% |
| Moisturecontent | ≤0.05% |
| Granuleshape | Cylindrical pellets |
| Color | White or natural |
| Odor | Odorless |
As an accredited CHN Energy Ningxia Coal LLDPE 7042 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | CHN Energy Ningxia Coal LLDPE 7042 is supplied in 25 kg PP woven bags, 40 bags per pallet (1000 kg). |
| Container Loading (20′ FCL) | 20′ FCL container loading of CHN Energy Ningxia Coal LLDPE 7042 in 25 kg bags, palletized and securely wrapped for export. |
| Shipping | CHN Energy Ningxia Coal LLDPE 7042 is a non-hazardous polyethylene resin. It is usually shipped in 25 kg PP woven bags or 500–1000 kg jumbo bags, palletized and stretch-wrapped. Transport by truck, rail, or sea container. Store cool, dry, ventilated, away from sunlight, moisture, and heat. |
| Storage | Store CHN Energy Ningxia Coal LLDPE 7042 in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, and ignition sources. Keep original bags sealed, palletized, off the floor, and protected from crushing. Avoid moisture, UV exposure, oils, acids, alkalis, and strong oxidizers. Maintain clean handling, appropriate PPE, and first-in, first-out rotation. Do not stack excessively. Inspect regularly. |
| Shelf Life | Shelf life is typically 24 months under proper storage: dry, cool, ventilated, away from direct sunlight and heat. |
On three-layer coextrusion blown-film lines configured with a 65 mm grooved-feed extruder and a 350 mm spiral mandrel die, CHN Energy Ningxia Coal LLDPE 7042 is processed in the inner and core layers for industrial liners and heavy-duty sacks at layer distributions of 20/60/20 or 30/40/30, depending on seal-integrity requirements. The resin, with a nominal melt index of 1.8–2.2 g/10 min per ASTM D1238 and density of 0.918–0.922 g/cm³ per ASTM D1505, is dry-blended with 15–30 wt% high-pressure LDPE having a 0.25–0.35 g/10 min melt index to increase bubble stability and reduce neck-in. Barrel temperatures from feed zone to metering zone follow a rising profile of 170 °C, 185 °C, 195 °C, and 200 °C; melt pressure at the adapter is held between 30 MPa and 38 MPa at 80–100 rpm screw speed. Pressure oscillation exceeding ±1.0 MPa generally indicates feed bridging in the grooved intake zone when ambient dew point rises above 18 °C and resin is conveyed directly from outdoor silos. Die gap is set at 1.4–2.0 mm, blow-up ratio is maintained within 2.8:1–3.5:1, and frost line height is positioned 5–8 die diameters above the lips. Film produced at 120–200 µm exhibits machine-direction tensile strength at break per ASTM D882 of 25–35 MPa and transverse-direction tensile strength of 20–28 MPa, with elongation at break of 500–750% at a crosshead speed of 500 mm/min. Dart drop impact per ASTM D1709 Method A for a 150 µm three-layer structure is typically not less than 150 g at 23 °C. Seal strength on side-gusset sacks is evaluated per ASTM F88 at 80–110 N/25 mm when the inner layer is formulated from 100% 7042 and jaw temperature is held at 135–150 °C. Surface condensation from resin stored in unheated warehouses with relative humidity above 80% should be removed with a desiccant hopper at 65 °C for 2 h before extrusion; otherwise gel speck formation increases in the outer film surfaces. Non-food industrial liners are normally assessed against REACH and the RoHS Recast 2011/65/EU; food-contact sack liners fall under FDA 21 CFR 177.1520 and EU 10/2011 when the final migration test per EN 1186 yields an overall migration value below 10 mg/dm². The continuous service temperature should not exceed 65 °C, and the material is not suitable for hot-fill packaging above 85 °C.
Cast stretch film operations select 7042 for the core layer in A/B/A coextrusion at 70–85 wt% of the structure, with cling skins containing metallocene LLDPE, EVA, or polyisobutylene-modified compounds. The cast process uses a 100–150 mm barrier screw extruder, a flat die gap of 0.5–1.0 mm, and chill rollers maintained at 15–30 °C. Line speeds of 300–600 m/min are achievable because the 2.0 g/10 min melt index of 7042 reduces head pressure and extruder motor load relative to fractional-melt LLDPE. Drawdown to 10–20 µm thickness requires controlled neck-in; neck-in is reduced by blending 10–20 wt% high-pressure LDPE or by positioning the air-knife assembly to create an air gap of 5–15 mm. Puncture resistance is determined per ASTM D5748; a 20 µm film containing 80 wt% 7042 and 20 wt% metallocene LLDPE typically shows puncture energy values of 0.8–1.2 J depending on additive loading and cooling-roll temperature. Cling performance is measured per ASTM D5458, with a peel force on the cling skin of 0.5–0.9 N/cm; the cling layer is not produced from 7042 alone but requires 0.5–1.5 wt% polyisobutylene masterbatch or an EVA skin layer. Pre-stretch on pallet-wrapping equipment is limited to 200–300%; above this range, or at ambient temperatures below 10 °C, the butene comonomer architecture of 7042 increases elastic recovery and reduces holding-force retention when assessed by ISO 527-3 hysteresis cycling. Processing conflicts arise when the corona treater is run above 42 mN/m, because excessive surface oxidation increases blocking after roll storage at 35 °C for 48 h. Published data for the specific CHN Energy Ningxia Coal 7042 formulation in high-cling multilayer cast films is limited; incoming lot verification by ASTM D1238, ASTM D1505, and film tear testing per ASTM D1922 is required when the resin source or additive package is changed.
| Function | Active chemistry | Typical let-down ratio | Measurement standard |
|---|---|---|---|
| Slip | Erucamide 5 wt% in LLDPE carrier | 2–4% | ASTM D1894 kinetic COF <0.25 |
| Antiblock | Synthetic silica 10 wt% in LDPE carrier | 1–2% | ASTM D1003 haze <8% |
| Process aid | Fluoropolymer PPA 3 wt% in LLDPE carrier | 0.5–1% | Melt-pressure reduction 5–12% |
| UV stabilization | HALS 10 wt% in LLDPE carrier | 3–6% | ISO 4892-2 retention >75% elongation |
Where photooxidative service life beyond 24 months is required, 7042 is used in three-layer greenhouse film with a layer ratio of 25/50/25 and a total thickness of 150–200 µm. The outer layer is compounded with 0.3–0.6 wt% hindered amine light stabilizer masterbatch, 0.1–0.3 wt% benzotriazole UV absorber, and 2–3 wt% titanium dioxide white or carbon black masterbatch for light diffusion. The middle layer contains 10–15 wt% EVA with 14–18% vinyl acetate to improve infrared retention and night-time heat conservation. Processing on a 50 mm three-layer blown-film line with a 200 mm die uses a blow-up ratio of 2.0:1–3.0:1 and a melt temperature of 180–200 °C, the lower range being selected to limit EVA degradation and acid formation in the middle layer. Light transmission and haze are assessed per ASTM D1003; total visible light transmission in unpigmented UV-stabilized film at 160 µm is normally above 88%. Anti-fog performance is assessed by the condensation test method in EN 13206, with glycerol ester anti-drip masterbatch let-down of 0.5–1.0 wt%. Pesticide compatibility is a critical processing boundary: sulfur-containing fumigants and halogenated vapours attack benzotriazole stabilizers and can produce embrittlement within 12–18 months, invalidating standard UV warranty conditions. After 3,000 h accelerated weathering per ISO 4892-3, the film should retain at least 75% of original elongation at break when tested per ISO 527-3. The stabilizer system of 7042 must be verified by lot because public technical bulletins do not disclose the exact antioxidant package used by the supplier.
The sealant layer of BOPP/LLDPE laminates uses 7042 at 20–40 µm coating weight on extrusion lamination lines equipped with a 90 mm screw, L/D 30:1, melt temperature of 280–300 °C, and an air gap of 150–200 mm to obtain adhesion to primed BOPP or oriented PET. The low heat-seal initiation temperature, commonly 100–115 °C as measured by hot-tack testing per ASTM F1921, permits sealing through product contamination at packaging speeds above 60 cycles/min on horizontal form-fill-seal equipment. Seal strength is evaluated per ASTM F88 at 15–25 N/25 mm for 25 µm sealant film sealed at 135 °C jaw temperature and 0.35 MPa jaw pressure. Food-contact compliance for the final laminate is assessed under FDA 21 CFR 177.1520 and EU 10/2011/EC, with overall migration per EN 1186 below 10 mg/dm² and specific migration limits for erucamide and synthetic silica additives per EU 10/2011 Annex II. For the Chinese domestic market, GB 4806.7-2016 applies, with a total migration limit of 10 mg/dm² under prescribed simulant conditions. Slip performance is controlled by adding 2–4 wt% erucamide masterbatch at 5% active content and 1–2 wt% synthetic silica antiblock masterbatch at 10% active content, resulting in a kinetic coefficient of friction below 0.25 per ASTM D1894 after 24 h aging. Amine-based process aids or slip concentrates should be avoided because they can react with erucamide and shift the slip bloom rate, producing inconsistent seal initiation. The maximum continuous sealing temperature should remain below 160 °C; above this threshold, seal strength declines as the oriented film substrate begins to shrink and disrupt the seal interface.
Thin-gauge agricultural mulch film at 8–25 µm exposes the drawdown capacity of 7042 to the melt-fracture boundary of the extruder and die. On a 45 mm smooth-bore single-screw extruder with a 150 mm die, a die gap below 1.0 mm and a melt temperature below 185 °C tend to induce shark-skin on the bubble surface; the standard corrective action is to raise melt temperature to 195–210 °C and open the die gap to 1.2 mm. The critical shear-rate boundary for visible surface melt fracture is equipment-specific and must be determined by on-line bubble-surface inspection at each die because published data for this CHN Energy Ningxia Coal grade in sub-15 µm monolayer structures is limited. The film is formulated with 1.5–3.0 wt% carbon black masterbatch for weed exclusion and 0.1–0.3 wt% UV stabilizer masterbatch. Elmendorf tear resistance is measured per ASTM D1922; machine-direction tear strength is maintained above 400 g at 25 µm gauge by limiting high-pressure LDPE content to 10–20 wt%, because excess LDPE raises modulus and causes brittle splitting at planting slits. Dart drop impact per ASTM D1709 Method A for 25 µm mulch film is typically not less than 80 g, but the value depends heavily on carbon black dispersion quality. Extended ultraviolet exposure requires the film to retain at least 50% of original elongation after 1,200 h under ISO 4892-2 conditions when a full-service-life mulch formulation is specified. The processing window narrows when the ambient extrusion hall temperature falls below 15 °C; frost-line instability and edge weave increase unless the air-ring chilling air is preconditioned to 20–25 °C.
Thermally stressed at freezer temperatures from -40 °C to -18 °C, 7042-based blown film at 40–100 µm is used for frozen vegetable bags and ice packaging. The butene-comonomer structure preserves puncture resistance at -30 °C when measured per ASTM D5748, provided the film is manufactured with a blow-up ratio of 2.5:1–3.0:1 and a die gap of 1.5 mm to limit excessive orientation. Additive loading is restricted to 2–3 wt% silica antiblock masterbatch and 1–2 wt% slip masterbatch; direct food-contact compliance per FDA 21 CFR 177.1520 and EU 10/2011 is required. Seal initiation at 105–120 °C supports vertical form-fill-seal lines running at 80–120 bags/min. The lower room-temperature stiffness of 7042 relative to HDPE limits unsupported bag width to about 400 mm when filling heads apply side loads; wider bags require gusseted construction or a HDPE-rich blend to prevent creasing and seal misalignment.
For self-adhesive surface protection film, 7042 is coextruded as the backing layer at 30–60 µm; inline corona treatment to 38–42 mN/m is applied before the adhesive coating station, with wetting tension readout per DIN 53364 or ASTM D2578. The stabilizer package of 7042 must be verified to avoid migration into pressure-sensitive adhesives; published data for this specific CHN Energy Ningxia Coal grade in high-corona thin films is limited, so a 72 h adhesion retention test per ASTM D3330 is mandatory for each incoming lot. Corona levels above 42 mN/m promote oxidative species that can increase unwind force and adhesive transfer after accelerated aging at 40 °C and 90% relative humidity.
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Produced on a gas-phase fluidised-bed train at the Ningxia coal-to-olefin complex, CHN Energy Ningxia Coal LLDPE 7042 is a butene-1 copolymerised linear low-density polyethylene supplied as natural-colour pellets. Release values on the manufacturer’s certificate of analysis are controlled to a melt mass-flow rate of 1.7–2.3 g/10 min at 190 °C under 2.16 kg load when tested according to ISO 1133-1, and to a base density of 0.918–0.922 g/cm³ according to ISO 1183-1. Film tensile yield strength is specified at not less than 8.0 MPa in both machine and transverse directions under ISO 527-3, with elongation at break exceeding 500% at a 25 mm/min crosshead speed. The resin is polymerised with a butene comonomer, which yields generally lower dart impact and puncture resistance than metallocene-catalysed hexene or octene grades of similar density, but higher elongation and dart impact than LDPE film grades at equivalent thickness. The broader molecular weight distribution of the Ziegler-Natta product also provides lower extrusion pressure than many metallocene resins on single-screw blown-film lines.
Commercial applications for this grade are concentrated in general-purpose blown film with thickness 20–80 µm, including garment bags, lamination film, light agricultural film and consumer packaging. The melt index and density combination is selected when converters require adequate bubble stability on medium-output lines without the higher melt strength of LDPE or the narrower shear tolerance of mLLDPE.
The selection is governed by the conversion window rather than by a single mechanical property. In blown film, LDPE provides higher melt strength and lower draw resonance, but at equivalent film thickness its tensile yield and puncture resistance are lower than those of LLDPE 7042 when tested to ISO 527-3 and ISO 7765-1. Metallocene-catalysed hexene or octene LLDPE grades with similar density typically show higher dart impact and puncture resistance and a lower hexane extractable fraction; however, their narrower molecular weight distribution creates higher extrusion pressure and more pronounced shear sensitivity on older single-screw lines. Chilled air ring and low-pressure die designs that handle mLLDPE effectively may not be necessary for LLDPE 7042, but the grade may require a wider die gap of 1.8–2.2 mm to control melt fracture at output rates above 0.6 kg/h per centimetre of die circumference.
| Parameter | Standard designation | Typical release range | Evaluation basis |
| Melt mass-flow rate | ISO 1133-1 | 1.7–2.3 g/10 min | 190 °C, 2.16 kg load |
| Density | ISO 1183-1 | 0.918–0.922 g/cm³ | 23 °C, compression-moulded plaque |
| Tensile yield stress | ISO 527-3 | ≥ 8.0 MPa | MD and TD, 25 mm/min |
| Elongation at break | ISO 527-3 | ≥ 500% | MD and TD, 25 mm/min |
| Dart impact resistance | ISO 7765-1 | Material-specific; set per film thickness | Method A, conditioned film |
| Food-contact migration | Commission Regulation (EU) No 10/2011 | Converter-specific | Finished article testing |
| RoHS additive compliance | Directive 2011/65/EU | Compound-level declaration | Conformity assessment by converter |
Because certificate-of-analysis values for dart impact and haze are influenced by film gauge, die geometry and additive package, they are not fixed as release criteria. The tabulated values are used as conformance indicators; converters should obtain the producer’s current product datasheet for the exact specification version.
On blown-film lines operating with automatic gauge control, a melt index shift of 0.2 g/10 min within the release range can produce detectable gauge-profile movement if the die gap is held constant. The producer’s 1.7–2.3 g/10 min certificate-of-analysis band is therefore paired with production-blend hopper control at the conversion plant; in silo-to-silo batch changes, converters often run a transition regime of 10–15 min before re-establishing the blow-up ratio target. This is not a defect in the resin but a normal consequence of polyethylene rheology, and it is more visible in thin films below 25 µm.
When 20–50 µm films are conditioned for 40 h at 23 °C ± 2 °C and 50% ± 10% relative humidity per ISO 291, tensile properties are direction-dependent due to blow-up ratio and frost line selection. A typical 2.5:1 blown film may show machine-direction elongation at break above 500% and transverse-direction elongation above 650%, but actual values depend on die gap, frost line height and internal bubble cooling settings. Dart drop impact to ISO 7765-1 method A is commonly used as release criterion and reflects the short-chain branching of a butene-based LLDPE; converters using this grade should expect a lower dart impact than a comparable density octene-based metallocene grade but a higher value than a 0.926 g/cm³ MDPE film at equal thickness. Elmendorf tear strength to ISO 6383-2 often shows a marked machine-direction/transverse-direction imbalance; increasing blow-up ratio to 2.8:1 shifts orientation toward machine direction and reduces the difference. Published data for this specific configuration is limited, and inline measurements on the production line should be used to set the final blow-up ratio.
In a 55 mm single-screw blown-film line fitted with an L/D 30:1 barrier screw and a 100 mm spiral mandrel die, the resin is typically processed with barrel set points progressing from 160 °C in the feed zone to 195 °C at the metering zone and die temperatures of 195–205 °C. Melt temperature measured at the adapter should be maintained between 190 °C and 215 °C. A die gap of 1.8–2.5 mm is preferred because LLDPE 7042 exhibits lower melt strength than LDPE; narrower gaps increase wall shear stress and promote sharkskin on the film surface at high outputs. Blow-up ratios in the range of 2.0:1 to 3.0:1 are common, while frost line height should be set between 4 and 7 die diameters to balance bubble quench and MD/TD orientation. On lines without internal bubble cooling, output is often limited by bubble instability at high frost line heights rather than by motor load. At melt temperatures below 185 °C, the resin may exhibit unmelted particle defects and increased die-lip build-up; raising the adapter temperature by 5 °C normally restores bubble stability when a grooved feed section is not in use.
Processors evaluating the grade on a new line should record adapter pressure, die inlet pressure and bubble diameter variance during the first 30 min of operation. A rising die inlet pressure at constant screw speed, combined with a drop in frost line height, is typically an indication of melt-temperature drift or feed bridging rather than a change in the resin itself. The melt pressure under normal conditions on a 55 mm line may lie between 18 MPa and 28 MPa, depending on die gap and output; sudden pressure excursions above 10% of the baseline warrant a hopper level and screen-pack inspection.
Dry blending with a fractional-melt LDPE of 0.2–0.8 g/10 min is used on production lines where the available die gap cannot be increased. Adding 15 wt% LDPE broadens the molecular weight distribution and increases melt strength, allowing the same die to operate at a lower apparent shear stress and reducing surface melt fracture on film produced above 0.7 kg/h per centimetre of die circumference. The blend retains sufficient dart impact for many liner applications, but a tensile yield reduction is commonly observed when the LDPE fraction reaches 30 wt%; the magnitude is line-dependent and published data for this specific configuration is limited. In blown film, the frost line height usually must be lowered by 15–20% to avoid excessive cooling of the mixed melt; chill-roll cast film lines can use higher LDPE levels but are not the primary conversion route for this grade.
Commercial film structures using this resin include light agricultural tunnel film of 30–60 µm, garment bags of 25–40 µm, lamination film of 20–30 µm and general-purpose liners up to 80 µm. The resin is not designed for high-temperature wet-food retort or high-barrier coextrusion structures where a density of 0.926 g/cm³ or higher and a barrier tie layer are required. In multilayer structures, LLDPE 7042 is typically used in the core or outer layer rather than the sealing layer when the sealant layer requires a very low seal initiation temperature.
Compared with a 0.945 g/cm³ high-density film grade, LLDPE 7042 provides higher elongation and dart impact at equal thickness but lower water-vapour barrier. For applications requiring a water-vapour transmission rate below 5 g/(m²·day) at 38 °C and 90% RH per ISO 15106-1, an additional barrier layer or higher-density grade is required. The lower density also reduces handling stiffness, so film towers with automatic roll transfer may require a higher gusset or thicker film to maintain roll-forming performance.
Because the base 7042 resin does not contain a high slip or antiblock package, film blocking may occur in high-wound rolls if the film is stored above 30 °C or at consistently high relative humidity. Converters requiring a coefficient of friction below 0.25 typically add a slip/antiblock masterbatch rather than relying on the base resin. The grade should be processed below 260 °C to limit thermal-oxidative chain scission and gel formation; prolonged hold-up time at high temperatures should be avoided. Contact with strong oxidising agents or process temperatures above 300 °C can cause rapid degradation. Food-contact use of the finished film requires converter-specific migration testing under Commission Regulation (EU) No 10/2011 as amended, because the certifier evaluates the finished article rather than the polymer alone. For electrical and electronic applications, additive-package verification against Directive 2011/65/EU is required at the compound level.
In bulk handling systems, pellets stored in unheated silos may develop surface condensation when transferred to a warm blending area. A hopper purge with dry air at 40 °C for at least 30 min mitigates moisture-related bubble defects. Pellet fines separation at the hopper cone can alter feed stability; installing a fines-screening step before the extruder feed throat is recommended where wide particle-size distribution is observed in railcar shipments.