| HS Code | 434359 |
| Product Name | Shandong Yulong HDPE 7000F |
| Polymer Type | High Density Polyethylene (HDPE) |
| Grade | 7000F |
| Appearance | White pellets |
| Density | 0.954 g/cm³ |
| Melt Flow Rate | 0.07 g/10 min at 190°C/2.16 kg |
| Tensile Strength At Yield | ≥25 MPa |
| Tensile Strength At Break | ≥35 MPa |
| Elongation At Break | ≥600% |
| Flexural Modulus | ≥1000 MPa |
| Vicat Softening Temperature | ≥125°C |
| Brittleness Temperature | ≤-70°C |
| Environmental Stress Cracking Resistance | ≥1000 h |
| Hardness Shore D | 65 |
| Melting Point | 130–135°C |
| Crystallinity | 80–90% |
| Water Absorption | <0.01% |
| Thermal Conductivity | 0.45 W/(m·K) |
| Volume Resistivity | >1×10^16 Ω·cm |
| Dielectric Constant | 2.3 at 1 MHz |
| Coefficient Of Linear Thermal Expansion | 1.2×10^-4 /°C |
As an accredited Shandong Yulong HDPE 7000F factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Shandong Yulong HDPE 7000F supplied in 25 kg PP woven bags, 1000 kg jumbo bags; 20 MT per container. |
| Container Loading (20′ FCL) | Shandong Yulong HDPE 7000F, 25 kg bags, palletized or loose; 20′ FCL loading approx. 17–22 MT net, depending on packaging. |
| Shipping | Shandong Yulong HDPE 7000F ships as a non-hazardous high-density polyethylene resin in 25kg PP woven bags, palletized and stretch-wrapped. Store in a cool, dry, ventilated area away from direct sunlight and moisture. Transport in clean, dry containers. Maintain sealed packaging during transit. No special dangerous goods handling required. |
| Storage | Store Shandong Yulong HDPE 7000F in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, and ignition sources. Keep original bags closed, palletized, and off the floor. Avoid moisture, contamination, and oxidizing agents. Maintain moderate temperatures and protect from prolonged UV exposure. Use clean handling equipment; rotate stock to prevent aging. Store separately from incompatible materials. Ensure good housekeeping. |
| Shelf Life | Shandong Yulong HDPE 7000F typically has a 24-month shelf life when stored unopened, cool, dry, and away from direct sunlight. |
High-density polyethylene sheet for fluid containment and waste isolation uses the high melt strength and low melt mass-flow rate of Shandong Yulong HDPE 7000F, reported as 0.04 g/10 min at 190 °C/2.16 kg with density at 0.956 g/cm³ per ISO 1183-1. Compliance for landfill, pond, and heap-leach liner starts with GRI-GM13, the Geosynthetic Research Institute specification for HDPE geomembranes; accepted sheet must meet minimum tensile yield strength of 29 MPa and elongation at break of 700% per ASTM D638, tear resistance above 187 N per ASTM D1004, puncture resistance above 640 N per ASTM D4833, stress-crack resistance above 500 h per ASTM D5397 SP-NCTL, standard oxidative induction time above 100 min per ASTM D3895, and high-pressure OIT above 400 min per ASTM D5885. Typical compound loadings for 7000F sheet are 2.0–3.0 wt% carbon black masterbatch at 40–50% carbon black concentration to satisfy GRI-GM13 UV stability requirements, 0.3–0.6 wt% antioxidant masterbatch, and 0.02–0.05 wt% fluoropolymer processing aid when flat-die throughput exceeds 1,200 kg/h. Downstream conversion uses a twin-screw compounding step followed by flat-die extrusion through a 1.5–2.5 mm die gap at melt temperatures of 200–230 °C, with calendering rolls held at 60–90 °C to remove draw orientation; melt temperature is maintained within ±5 °C of 210 °C because residence time above 230 °C accelerates antioxidant depletion and produces pinhole-forming gels. Production-scale failures observed on lines wider than 4 m include gauge bands caused by batch-to-batch melt-strength drift, carbon black agglomerates nucleating pinholes under ASTM D5596 inspection, and edge trim welds that lose SP-NCTL when roll stack pressure exceeds 0.8 MPa. Finished component types include smooth and textured geomembrane liners 0.75–3.0 mm thick, leak-detection liners, secondary containment sheets, pond and canal barriers, and mining heap-leach pads.
In blown-film conversion of nominal 0.956 g/cm³ high-density polyethylene, refuse sack and can liner lines run 7000F as the primary stiffness layer, often blended with 10–20 wt% octene or butene LLDPE to raise dart impact from 120 g to 220 g at 12 µm thickness, measured per ASTM D1709 method A. Relevant compliance for municipal and commercial sack grades includes EN 13592:2017 for household waste sacks and ASTM D3826 for tracking film tensile degradation; non-food refuse sacks do not require FDA 21 CFR 177.1520 clearance, but export batches to the EU are screened against REACH Article 33 substance of very high concern reporting obligations. Additive loadings are lean compared with geomembrane compounds: 2–5 wt% white or black color masterbatch, 0.5–1.0 wt% silica antiblock, 0.05–0.15 wt% slip, and up to 30 wt% post-industrial edge trim when extrusion stability permits. The downstream process is single-layer or coextruded blown film on grooved-feed extruders with L/D 25:1–30:1, die diameter 100–400 mm, die gap 1.0–1.6 mm, blow-up ratio 3:1–5:1, and melt temperatures of 180–210 °C. Barrier-flight screw designs are required because the high molecular weight fraction raises motor torque 20–30% over commodity HDPE film grades; melt fracture appears at shear rates above 1,000 s⁻¹, and bubble instability occurs when frost line height exceeds 10 die diameters. Converted articles include household refuse sacks, commercial can liners from 20 L to 240 L, medical waste transport liners in non-red regrind-free campaigns, and compaction bags used in retail back-of-house compactors.
High-stalk blown-film lines running 7000F at 6–10 µm gauge are selected for t-shirt carrier bag production because the grade’s broad molecular weight distribution maintains bubble stability at blow-up ratios of 3:1–6:1, while delivering dart impact values that remain above 70 g at 8 µm per ISO 7765-1 method A. Compliance for consumer packaging is tied to EU 94/62/EC packaging essential requirements and ISO 7765-1 impact; print and pigment systems are reviewed under EU 10/2011 when the bag may contact unpackaged fruit or bakery items, though formal migration testing is normally performed on a food contact liner, not the outer bag. The standard formulation uses 100 phr 7000F, 10–20 phr LLDPE for dart impact and seal, 0.1–0.3 phr silica antiblock, 0.05–0.1 phr erucamide slip, and 2–4 wt% white or PMS color masterbatch. Extruder conditions use grooved feed sections with L/D 25:1–30:1, die gap 1.0–2.0 mm, frost-line height 8–12 die diameters, and melt temperatures 190–220 °C; melt pressure at the screen changer is typically 35–45 MPa and screen packs 60/80/100 mesh remove carbonized gels. Downstream converting runs bottom-seal bag machines at 180–250 cycles/min with seal jaw temperatures 150–170 °C; pinholes from antiblock agglomerates above 40 µm create weak spots that appear as burst failures at the die-cut handle. Terminal products include t-shirt grocery bags, retail checkout sacks, thin produce roll bags, and laundry bags requiring high-speed sealed bottom seams.
Extruder screw torque, not film tear, is the limiting variable when 7000F is run at layflat widths above 800 mm for heavy-duty industrial sacks. The grade is processed at 50–120 µm gauge in mono or coextruded blown-film lines where the outer layers provide stiffness and the inner layer delivers seal integrity. Compliance for industrial sacks includes ASTM D1709 dart impact for filled-bag drop survival, ASTM D882 tensile properties in machine and transverse directions, ASTM D1922 Elmendorf tear, and ASTM D638 for resin lot tensile validation; sacks used for chemical powders and fertilizers are additionally assessed under UN 21.2.3 drop and stack test protocols when the package is part of a regulated transport packaging system. Formulation loadings for a three-layer coextruded sack use 100 phr 7000F in the outer and core layers, 10–30 phr LLDPE in the seal layer, 1–3 wt% anti-static masterbatch when filling in combustible dust atmospheres, 2–4 wt% color masterbatch, and 0.02–0.05 wt% processing aid to suppress die drool on long campaigns. The downstream process operates with die gaps of 1.2–2.5 mm, blow-up ratios of 3:1–4:1, melt temperatures of 190–230 °C, and extruder L/D 30:1; high-torque drives above 450 kW on 90 mm screw diameters are common because the high molecular weight HDPE requires elevated head pressure at sustainable throughputs. Terminal goods include fertilizer sacks, synthetic resin packaging sacks, mineral powder sacks, seed sacks, and heavy-gauge liners for intermediate bulk container outer packaging.
Food contact liner extrusion with 7000F is restricted to olefin polymer clearances under FDA 21 CFR 177.1520(c), which imposes density and melt index boundaries consistent with high-density polyethylene, and EU 10/2011, which requires overall migration below 10 mg/dm² for dry and aqueous food types; China domestic applications reference GB 4806.7 for food contact plastics and GB 9685 for admissible additives. Formulation loadings are tighter than industrial film because only food-cleared additives are permitted: 100 phr 7000F, 0.1–0.3 phr silica antiblock, 2–4 wt% TiO₂ white masterbatch, 0.1–0.3 phr antioxidant, and 0.05–0.1 phr slip only where the film must slide over metal filling mandrels; post-consumer recycled content is not permitted in the food contact layer under FDA 21 CFR 177.1520(c) unless a functional barrier is established. The downstream process uses single-layer or two-layer blown film at die gaps of 0.8–1.5 mm, melt temperatures of 190–210 °C, blow-up ratios of 3:1–5:1, and corona treatment to 38–42 mN/m for print adhesion. Converting lines slit the film into insert liners and apply heat seals at 140–170 °C; gel particles above 0.3 mm in the melt cause pinholing that fails leak tests at 20 kPa. Terminal products include cereal box liners, frozen food inner bags, dry powder beverage liners, cracker overwrap, and chub packaging for refrigerated dough. Grade-specific migration data for Shandong Yulong 7000F in this configuration are limited in public literature; converter-specific migration tests under EU 10/2011 are required when film thickness falls below 50 µm in fatty food contact.
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Shandong Yulong HDPE 7000F is a high-molecular-weight high-density polyethylene extrusion grade supplied in pellet form and directed toward blown film conversion. The product is not positioned as a general-purpose injection moulding or pipe resin; the grade suffix denotes film extrusion, and the low melt flow rate is selected to deliver a combination of melt strength, dart impact resistance, and stiffness in thin-gauge film. Manufacturer lot-release data and technical summaries list a nominal density of 0.949 g/cm³ and a melt flow rate of 0.04 g/10 min when measured at 190 °C under a 2.16 kg load using ISO 1133-1:2022. At this flow level, the resin has a higher weight-average molecular weight than typical medium-flow HDPE film grades, which shifts processing behaviour toward elevated melt viscosity and higher die pressure. The resin is applicable to high-strength carrier films, garment bags, industrial liners, and geomembrane feedstocks where gauge reduction below 10 µm is commercially relevant. In food-contact applications, the base olefin polymer may be assessed against 21 CFR 177.1520 and EU No 10/2011; the exact compliance status depends on additive package, downstream conversion, and the finished article.
Batch release values are determined with standardised test methods. The tabulated values are representative technical data, not specification limits for all supply contracts; certificates of analysis provide lot-specific results.
| Property | Test method | Unit | Typical value |
|---|---|---|---|
| Melt flow rate (190 °C, 2.16 kg) | ISO 1133-1:2022 | g/10 min | 0.04 |
| Density | ISO 1183-1:2019 | g/cm³ | 0.949 |
| Tensile yield stress | ISO 527-2:2012 | MPa | 22 |
| Tensile stress at break | ISO 527-2:2012 | MPa | 38 |
| Elongation at break | ISO 527-2:2012 | % | 800 |
| Dart impact, Method A | ASTM D1709-16a | g | 250 |
Mechanical test specimens are conditioned for at least 88 h at 23 °C ± 2 °C and 50% ± 5% relative humidity according to ISO 291:2008 before tensile evaluation. Dart impact values are gauge-dependent; the value above is specific to film produced at the converter’s reference thickness, and comparisons across grades require identical gauge and test method. The low melt flow rate value under 2.16 kg is insufficient to describe processability; high-load melt flow rate or melt flow ratio should be obtained from the lot certificate for screw design and throughput calculations.
The density of 0.949 g/cm³ positions the product in the high-density class, but the value should not be used alone to infer stiffness. Crystallinity and modulus are influenced by cooling rate, blow-up ratio, and frost line position. The tensile yield stress of 22 MPa and tensile stress at break of 38 MPa are generated on compression-moulded or specified film specimens; they may not correspond to values measured on blown film at high haul-off speeds.
Molecular weight distribution is not specified in short technical data sheets, but the low MFR and film-grade designation imply a high-molecular-weight tail. For process design, the melt flow ratio obtained from high-load melt flow rate and standard melt flow rate is a more useful control parameter than MFR alone. Comparable high-molecular-weight HDPE film grades exhibit melt flow ratios above 20; values for this specific resin require lot measurement under ISO 1133-1:2022 at 190 °C and 21.6 kg load.
On blown-film lines equipped with single-screw extruders of 25:1 to 30:1 L/D, HDPE 7000F is usually processed with barrel temperatures ramping from 180 °C to 210 °C and die temperature held at 200 °C to 210 °C. Actual set points depend on screw design, screen pack, throughput, and die diameter. Die gaps of 1.2 mm to 1.8 mm and blow-up ratios of 3:1 to 5:1 are practical starting conditions. Because the resin has a low MFR, melt pressure at the adapter, breaker plate, and screen pack is higher than for medium-flow HDPE film grades. Screens of 60 to 120 mesh are common; pressure should be monitored to avoid excessive shear heating. Where sharkskin or surface melt fracture appears at high output, additions of 200 to 600 ppm fluoropolymer processing aid are used in comparable high-molecular-weight HDPE film formulations. The exact concentration depends on shear rate, die design, and the masterbatch carrier system.
At 190 °C and 100 s⁻¹, high-molecular-weight HDPE film grades of this type typically show apparent shear viscosity in the range of 2 × 10³ Pa·s to 5 × 10³ Pa·s; by comparison, a medium-flow HDPE film grade may fall in the range of 1 × 10³ Pa·s to 2 × 10³ Pa·s. These values are based on published capillary rheometry for comparable resins; product-specific data are not always available and should be measured for simulation input.
The resin is hydrophobic and has low water absorption below 0.01% at 23 °C and 50% relative humidity. Pre-drying is not required under normal indoor storage, but surface condensation on cold pellets should be removed with dry air at 40 °C to 50 °C before hopper loading. Excessive moisture on pellet surfaces can produce splay-like defects in the film, although the polymer itself is not hydrolytically degradable.
Residence time above 240 °C should be minimised. Thermo-oxidative degradation can form gel particles, discoloration, and odour; if these appear, the line should be purged with a lower-viscosity HDPE or LLDPE purge compound. Shutdown procedures should reduce barrel temperatures below 180 °C before a prolonged stop to limit polymer degradation in stagnant zones.
Relative to a lower-molecular-weight HDPE film resin with a melt flow rate near 0.5 g/10 min, HDPE 7000F generates higher melt pressure at constant screw speed and die restriction. The elevated viscosity is not simply a processing penalty; it contributes to bubble stability and permits gauge reduction without severe bubble sag. The reported nominal tensile stress at break of 38 MPa and dart impact of 250 g for HDPE 7000F are above typical values of many medium-flow HDPE film grades, where tensile stress at break may lie in the 28 MPa to 34 MPa range and dart impact may fall below 180 g under the same test method. These differences arise from higher weight-average molecular weight and broader molecular weight distribution, which increase chain entanglement and tie-molecule concentration in oriented film.
Compared with LLDPE film resins of 0.918 g/cm³ density, HDPE 7000F provides higher modulus and yield stress but a different balance of tear and puncture behaviour. LLDPE grades commonly exhibit lower stiffness and greater stretch at equivalent thickness, whereas HDPE 7000F is specified for stiffness and moisture vapour transmission resistance. The difference in density between 0.949 g/cm³ and 0.918 g/cm³ alone shifts the crystalline fraction and modulus, but additive and drawing conditions also control final film properties.
This grade is not a direct substitute for medium-flow HDPE in extrusion coating or cast film because the low melt flow rate can limit web orientation and line speed. In injection moulding, the flow path is too restricted for multi-cavity tools, and the product is not recommended for that process. Published data for this specific configuration is limited, so conversion to a new downstream technology should begin with pilot trials rather than relying on technical data sheet values.
Frost-line position controls the quench rate and the orientation state of HDPE 7000F blown film. Raising the frost line beyond 6 to 8 die diameters delays quenching, permits additional crystallisation, and can raise film modulus while reducing dart impact and increasing tear anisotropy. The effect is visible in film produced at high blow-up ratios, where a high frost line may create a less stable bubble and alter the balance between machine-direction and transverse-direction tear. Operators commonly reset air ring damper angle and internal bubble cooling exhaust to hold frost-line height below 8 die diameters. If bubble instability occurs under high ambient humidity, reducing melt temperature by 10 °C or increasing internal bubble cooling airflow may restore bubble symmetry. These adjustments are line-specific; published data for this exact resin and equipment combination is limited.
Where regulatory approval is required, compliance documentation for HDPE 7000F depends on the finished article and jurisdiction. In food-contact packaging, the olefin polymer base is assessed under 21 CFR 177.1520 and, in the European Union, under EU No 10/2011. The European regulation sets an overall migration limit of 10 mg/dm² for general food contact and 60 mg/kg for infant food contact, based on the specific simulant testing conditions defined in the regulation. Packaging waste applications should be checked against Directive 94/62/EC, which sets a combined lead, cadmium, mercury, and hexavalent chromium limit of 100 ppm. Under REACH, polyethylene as a polymer is exempt from registration, but imported articles containing substances of very high concern above 0.1% w/w trigger notification and communication obligations under Regulation EC 1907/2006. A converter-specific additive declaration is required because additives, not the base resin, typically determine final food-contact and REACH compliance.
Applications for HDPE 7000F include high-strength carrier bags, garment bags, industrial liners, and geomembrane feedstocks. In geomembrane use, the resin is often combined with carbon black masterbatch and processed into sheets above 0.75 mm; the low MFR contributes to stress-crack resistance in the welded sheet, but weld validation should follow ASTM D6392 or project-specific shear peel protocols. In thin-gauge bag film, gauge control is critical: film thickness variation should be kept below ±5% for consistent dart impact and tear results. Converters producing high-strength bags at 12–18 µm typically use gravimetric dosing and internal bubble cooling. The product is not recommended for injection moulding, rotomoulding, or pipe extrusion without reformulation because the melt flow characteristics do not match these process requirements.