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Lotte Chemical HDPE HIVOREX 5000S

    • Product Name: Lotte Chemical HDPE HIVOREX 5000S
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 565887
    Density 0.954 g/cm³
    Melt Flow Rate 0.8 g/10 min at 190°C/2.16 kg
    Tensile Strength At Yield 25 MPa
    Elongation At Break >500%
    Flexural Modulus 1000 MPa
    Notched Izod Impact Strength 50 J/m
    Vicat Softening Point 125 °C
    Heat Deflection Temperature 75 °C at 0.46 MPa
    Shore D Hardness 65
    Environmental Stress Crack Resistance >1000 h
    Water Absorption <0.01%
    Dielectric Constant 2.3
    Volume Resistivity >10^16 Ω·cm
    Coefficient Of Thermal Expansion 1.2 x 10^-4 /°C

    As an accredited Lotte Chemical HDPE HIVOREX 5000S factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Lotte Chemical HDPE HIVOREX 5000S comes in 25 kg polyethylene-lined woven bags, palletized at 1,000 kg per pallet for transport.
    Container Loading (20′ FCL) 20′ FCL loaded with Lotte Chemical HDPE HIVOREX 5000S in 25 kg bags, palletized, shrink-wrapped, and secured for ocean transport.
    Shipping Lotte Chemical HDPE HIVOREX 5000S is shipped as non-hazardous high-density polyethylene resin pellets, usually in 25 kg bags or 1000 kg jumbo bags. Transport by truck, rail, or ocean container. Store cool and dry; protect from moisture, sunlight, and contamination. No special UN hazard classification required.
    Storage Store Lotte Chemical HDPE HIVOREX 5000S in a cool, dry, well-ventilated area at ambient temperature, away from direct sunlight, heat, sparks, and open flames. Keep in original sealed bags or containers on pallets to prevent moisture, dust, and contamination. Avoid strong oxidizers. Maintain stable stacking to prevent deformation, and follow local regulations and SDS recommendations. Protect from prolonged UV exposure.
    Shelf Life Lotte Chemical HDPE HIVOREX 5000S has a shelf life of 12 months when stored in a cool, dry, well-ventilated area.
    Application of Lotte Chemical HDPE HIVOREX 5000S
    In woven flexible intermediate bulk containers and laminated sack manufacturing, a significant proportion of HIVOREX 5000S enters flat tape extrusion lines. The resin is specified with a melt flow index of 0.60 g/10 min measured under ISO 1133-1:2022 and a density of 0.955 g/cm³ under ISO 1183. This viscosity window supports stable draw resonance-free operation across slot die gaps from 0.8 mm to 1.2 mm. Single-screw extruders with 30:1 L/D and barrier screws are typically set to a barrel profile of 170 °C in the feed section, 200–220 °C in the compression zone, and 215–230 °C at the adapter and flat die head. Water bath quench temperatures are maintained between 25 °C and 35 °C, and the air gap between die exit and water surface is kept below 30 mm to prevent differential quenching. Pre-drying at 80 °C for 2 h is unnecessary below 60 % relative humidity, but outdoor storage in coastal or monsoon conditions with RH above 60 % can introduce surface moisture sufficient to cause pinholes and tape dimensional variance. After quenching, the tape enters a first set of heated godets at 90–105 °C and is drawn at a total draw ratio of 5.5:1 to 7.5:1, followed by annealing at 5–8 % relaxation to control shrinkage. Tape tenacity and elongation at break are evaluated under ISO 2062; finished woven fabric tensile strength is commonly assessed under ISO 13934-1. For food contact woven sacks, resin compliance is referenced to FDA 21 CFR 177.1520 and EU Regulation 10/2011, but converters must validate overall migration and specific migration limits on the finished article because additive masterbatches, coatings, and recycled edge trim inclusion can alter the compliance envelope despite the base polymer meeting olefin polymer specifications.

    What Draw Ratio Window Keeps 5000S Monofilament Tenacity Above 0.40 N/den in Netting Lines?

    Monofilament extrusion for aquaculture cage netting, safety nets, and predator exclusion systems uses 5000S in the 0.60 g/10 min MFR range to maintain filament diameters from 0.15 mm to 0.60 mm. The conversion route typically begins with a single-screw extruder with 30:1 L/D fitted with a metering pump and screen pack combination of 60/100/120 mesh, feeding a multi-hole die plate. Die temperatures are held at 220–240 °C, and the extrudate is quenched in water at 28–40 °C before entering a two-stage hot air or hot water orientation unit. The first draw stage is commonly set at 4:1 to 5:1 at 95–100 °C, and the second stage at 1.5:1 to 1.8:1 at 105–115 °C, yielding total draw ratios between 7:1 and 9:1. At total draw ratios above 9:1, filament breaks increase on multi-position winders and knot efficiency under ISO 1806 declines even as straight tenacity under ISO 2062 may exceed 0.40 N/den. The operational boundary for this configuration is therefore not the maximum attainable tenacity but the narrow window in which drawn filaments survive twisting and netting without fibrillation at the draw point. In field applications, UV stabilisation is mandatory; carbon black masterbatch at 2.0–2.5 wt % final carbon black or hindered amine light stabilizer systems are incorporated prior to extrusion, with weathering retention verified by accelerated exposure under ISO 4892-2:2013 at 2000 h UV-irradiation cycles. Water absorption is below 0.01 % under ISO 62, which supports dimensional stability in marine service, but the stabilizer package must be selected to resist extraction in continuous immersion if the netting is used in brackish water.Where geotextile separation layers and erosion-control blankets require fibrillated tape, 5000S is cast at tape thicknesses between 35 µm and 65 µm and widths up to 50 mm depending on final denier. The oriented tape is passed over rotating pin or needle rollers that cut a defined zigzag pattern after the longitudinal draw stage. Draw ratios are lower than monofilament operation, commonly 5:1 to 6.5:1, because excessive orientation reduces the diagonal web strength of the fibrillated structure. Production lines often run a water quench at 30–40 °C and an orientation oven at 100–110 °C, with annealed shrinkage controlled to 3 % or less by a relaxation godet set 5–7 % below the final draw speed. The material is then used in woven and nonwoven geotextile structures where wide-width tensile strength is determined under ISO 13934-1, static puncture resistance under ISO 12236, and tear resistance under ASTM D4533-04. Because geotextile service involves direct soil burial, environmental stress cracking resistance is a decisive property; 5000S of this density range is selected for high molecular weight retention rather than melt flowability, and the specification may include ESC testing under ASTM D1693-15 Condition B or ISO 22088-3. Carbon black at 2.0–2.5 wt % final loading is more than a UV screen in this application; it also reduces oxidative degradation at the tape surface in soil contact when the compounded system is processed below 240 °C to avoid gel formation. Published data for site-specific tensile retention after multi-year soil burial of 5000S fibrillated geotextiles is limited, so field validation remains necessary for design service life beyond 25 years.
    Comparative processing window for HIVOREX 5000S across three extrusion configurations
    ParameterFlat tape for woven sacksMonofilament for nettingFibrillated tape for geotextile
    Melt temperature at die215–230 °C220–240 °C210–230 °C
    Quench bath temperature25–35 °C28–40 °C30–40 °C
    Orientation zone temperature90–105 °C105–115 °C100–110 °C
    Total draw ratio5.5:1–7.5:17:1–9:15:1–6.5:1
    Typical final denier600–1,200 den300–1,200 den800–2,000 den

    Extruded Anti-Hail and Anti-Insect Netting Profiles Under Quench Stability and UV Package Constraints

    Anti-hail and anti-insect netting in apple orchards, vineyards, and berry tunnels is regularly warp-knitted from 5000S monofilament or tape yarn that has been extruded through spinneret plates with hole diameters from 0.30 mm to 0.80 mm. The substrate for Raschel knitting machines demands a filament with uniform denier and low twist liveliness. Melt temperature at the spinneret is limited to 220–235 °C; higher temperatures reduce viscosity enough to cause spray nozzles and melt swell variation across multi-orifice dies. Quench water at 25–32 °C with constant circulation is critical because stagnant warm water creates asymmetric cooling and ovality that propagate as knit-in defects. The subsequent draw is performed in heated air at 95–110 °C with a draw ratio of 6:1 to 8:1. Draw point localization is a recurring failure mode on lines without temperature control across the full godet width; the corrective range is a godet surface temperature variation not exceeding ±2.5 °C. For agricultural netting, UV durability is specified through accelerated weathering under ISO 4892-2:2013 and sometimes ISO 4892-3:2016 for fluorescent UV exposure, depending on market. The base polymer is usually compounded with a 40 wt % carbon black masterbatch in an LDPE carrier at a dosing rate of 5–6 wt %, yielding 2.0–2.5 wt % black in the final filament. Incompatibility is observed when low-crystallinity masterbatch carriers are replaced with high-viscosity film carriers at the same letdown ratio; undispersed agglomerates cause draw breaks and weak spots that cannot be detected by inline diameter gauges alone. Mesh breaking force after knitting is assessed under ISO 1806, while individual filament elongation is verified under ISO 2062 with a gauge length of 250 mm.

    When 5000S Is Shifted to Synthetic Rope Yarn and Marine Hauler Strands

    Although not a dedicated rope resin, 5000S enters rope manufacturing when converters require a floating HDPE fibre with higher melt strength than injection-moulding grades and a balance between abrasion resistance and elongation under cyclic load. The strand is usually a drawn monofilament or fibrillated tape of 1,000–2,200 denier that is twisted on a ring twister at 120–220 turns per metre before being laid into 3-strand or 8-strand construction. A key processing constraint is that pre-twist filament tension must be controlled within ±10 % of the set value on the creel; tension variation produces uneven lay length and shifts the load-elongation curve of the finished rope under ISO 2307. The resin's low water absorption of 0.01 % under ISO 62 minimises wet strength loss compared with polyamide, but creep in continuous tension is higher than for polyester and must be accepted in mooring systems where elongation under sustained load is acceptable. If the rope is intended for food-contact marine aquaculture support lines, compliance extends only to structural use; direct food contact is not covered unless the converter demonstrates migration limits under EU Regulation 10/2011 for the finished twisted article. UV stability for ropes in continuous sunlight is achieved with carbon black or ultraviolet stabiliser masterbatch, with purchaser specifications sometimes requiring retained break force after 2000 h exposure under ISO 4892-2:2013 of not less than 80 % of the unexposed value. In practice, extruder purging is required when switching from 5000S to lower-viscosity HDPE because residual high-viscosity material held in the die lips can cause melt fracture on the next specialty grade and reduce twist uniformity.Among smaller-volume but technically demanding downstream applications, artificial turf thatch and decay-resistant landscaping yarn is produced from 5000S through flat or round monofilament extrusion followed by fibrillation or debossing to create a texturised surface that holds infill and mimics natural grass structure. The melt is passed through spinnerets at 220–235 °C, quenched at 25–35 °C, and drawn to a denier range of 800–1,600 den with total draw ratios between 5:1 and 7:1. Because turf yarn is exposed to continuous UV light, ozone, and abrasive foot traffic, the stabilisation and processing package must avoid extrusion temperatures above 240 °C, at which point chain scission can increase melt index above the acceptable upper limit and reduce slit resistance. Abrasion resistance is commonly evaluated by the simulated wear test described in FIFA Quality Programme for Football Turf – Test Method 04 or by the Lisport abrasion method under EN 15306, depending on the intended outdoor sports market. The high molecular weight of 5000S delays fibre fracture under repeated stud impact, but the same property limits throughput on small extruders with 25:1 L/D because melt pressure rises beyond safe barrel limits when output exceeds the plastication capacity. Published data for this specific configuration is limited for 5000S compared with dedicated turf grades; converters should run pilot extrusion trials to correlate melt pressure, die swell, and denier reproducibility before full-scale commitment.

    ESCR and UV-Weathering Thresholds in Outdoor Agricultural Screen Fabrics

    Outdoor insect screens, shade cloth, and windbreak fabrics produced from 5000S tape are typically manufactured on water-quench slit-film lines and then woven into open-mesh structures. The resin's melt flow index of 0.60 g/10 min under ISO 1133-1:2022 supports extended draw ratio stability across tape widths from 2 mm to 8 mm, but the final fabric mechanical properties are more sensitive to weave density and tape thickness than to base resin tensile values alone. Tensile and elongation tests on the woven fabric follow ISO 13934-1, while mesh width stability is checked after 24 h immersion in water at 23 °C to identify any shrinkage from internal orientation stresses. The most important long-term property is environmental stress cracking resistance because the tape is under continuous stress in tensioned screen applications. Verification uses ASTM D1693-15 Condition B or ISO 22088-3, with F50 values dependent on the specific UV stabiliser formulation and processing history rather than on the base resin alone. Black screen fabric generally contains 2.0–2.5 wt % dispersed carbon black, while white or coloured screens require hindered amine light stabilisers and UV absorbers to reach equivalent weathering performance; white pigmented 5000S fabric is generally not specified for multi-year continuous exposure at elevations above 1000 m without additional stabilisation. The outdoor screen market also imposes a low-shrinkage requirement; annealing at 100–110 °C with 4–6 % relaxation is common, and final heat shrinkage in hot air at 120 °C under ISO 11501 is often limited to 1.5 % or less for precision knitted shade structures.
    Relevant test standards and endpoints for downstream qualification of HIVOREX 5000S
    Application areaStandard designationMeasured endpoint
    Woven sack tape tensileISO 2062Tenacity and elongation at break
    Woven fabric tensileISO 13934-1Wide-width strip tensile
    Geotextile punctureISO 12236Static puncture resistance
    Netting mesh breaking forceISO 1806Mesh break force
    Rope physical propertiesISO 2307Breaking load and elongation
    Environmental stress crackingASTM D1693-15 / ISO 22088-3F50 hours
    Accelerated UV weatheringISO 4892-2:2013Retained break force after exposure
    Food contact base resinFDA 21 CFR 177.1520Olefin polymer compliance
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    Certification & Compliance
    More Introduction

    Lotte Chemical supplies the high-density polyethylene grade HIVOREX 5000S as a linear ethylene-based extrusion resin for blown film, cast film, and thin-sheet conversion. The material is identified by a nominal melt flow rate of 0.8 g/10 min under ISO 1133-1:2022 at 190 °C and 2.16 kg, and a nominal density of 0.954 g/cm³ under ISO 1183-1:2019. In commercial practice, the grade is used for grocery sacks, industrial liners, produce bags, heavy-duty packaging, and agricultural covers where gauge reduction and load-bearing capacity are specified. The linear molecular architecture with minimal short-chain branching produces a higher flexural modulus and a higher tensile yield stress than low-density polyethylene at equivalent thickness under ISO 527-2 test speed conditions.

    The resin differs from higher-flow HIVOREX injection grades by its lower melt flow rate and correspondingly higher melt strength during film bubble formation. This property set raises backpressure and torque relative to a 5.5 g/10 min injection moulding grade, but it improves tensile elongation and environmental stress crack resistance in the film state as measured by ISO 527-2 and ASTM D1693. For converters, the trade-off is a narrower high-shear processing envelope and longer heating requirements in the feed section.

    What Distinguishes HIVOREX 5000S from Low-Melt-Flow Film Grades During Bubble Formation?

    The 0.8 g/10 min melt flow rate does not define viscosity; rather, it predicts shear-dependent flow under a standardized low shear condition. In film extrusion at shear rates of 100–1000 s-1, the material operates in the pseudoplastic region, so localized shear reduces viscosity and stabilizes melt conveying. Bubble stability is generally acceptable at blow-up ratios of 3:1 to 5:1, provided the die land length is matched to the high viscosity. The molecular weight distribution is sufficiently broad to limit melt fracture at moderate output, but sufficiently narrow to restrict gel accumulation during long campaigns. Processors using smooth-bore extruders without grooved feed sections often need to elevate feed-zone temperatures by 5–10 °C to maintain stable melt feeding.

    The baseline property set below is compiled from standard datasheet values; it is not a specification limit and should be compared with the lot-specific certificate of analysis.

    Property Test method Unit Typical value
    Melt flow rate at 190 °C, 2.16 kg ISO 1133-1:2022 g/10 min 0.8
    Density ISO 1183-1:2019 g/cm³ 0.954
    Tensile stress at yield ISO 527-2:2012 MPa 27
    Tensile strain at break ISO 527-2:2012 % >500
    Flexural modulus ISO 178:2019 MPa 1000
    Shore D hardness ISO 868:2003 Shore D 62
    Vicat softening temperature, A120 ISO 306:2022 °C 124
    Environmental stress crack resistance, F50, 10 vol% Igepal, 50 °C ASTM D1693-15 h >100

    The tensile yield value of 27 MPa under ISO 527-2 reflects the high crystallinity associated with the 0.954 g/cm³ density. Lot-to-lot variation in melt flow rate of ±0.1 g/10 min can alter film machine direction orientation; converters should verify the certificate of analysis before setting die gaps below 0.8 mm.

    Melt Temperature, Pressure, and Die Gap Boundaries Define the Processing Window

    On a 90 mm grooved-barrier single-screw extruder with a 30:1 L/D barrier screw, barrel set points are commonly staged from 170 °C at the feed section to 190 °C at the metering section, with adapter and die metal temperatures maintained between 200 °C and 215 °C. Immersion probe melt temperatures above 220 °C can accelerate thermal-oxidative degradation, increasing gel counts in cast film and reducing retained tensile strength. Screw-tip melt pressures typically fall between 20 MPa and 30 MPa at screw speeds of 60–80 min-1, depending on die diameter, land length, and filtration pack condition. Die gaps below 0.8 mm may increase shear heating and destabilize output, whereas gaps above 1.5 mm can reduce drawdown and compromise gauge uniformity. For monolayer blown film, frost-line height is generally held at 6–10 times the die diameter, and internal bubble pressure is trimmed to maintain a 3:1–5:1 blow-up ratio. Capillary rheometry per ISO 11443 at 190–210 °C is preferred for die land design because shear viscosity at 100 s-1 is high relative to film grades with MFR above 1 g/10 min. These are industrial operating boundaries; published data for this specific resin configuration on other extruder platforms is limited.

    Injection moulding and thin-wall conversion are outside the primary application envelope for HIVOREX 5000S. Flow distance is limited by the higher melt viscosity, and wall thicknesses below 0.8 mm can freeze off before complete mould filling unless melt temperatures approach 230 °C. Such high melt temperatures are not recommended because oxidative gel formation may shift mechanical performance. A high-flow grade such as HIVOREX 2200J with a nominal MFR of 5.5 g/10 min and density of 0.965 g/cm³ is more appropriate when short cycle times dominate.

    Film tensile properties should be verified on finished film specimens under ISO 527-3:2018 because orientation and frost-line geometry shift the balance of machine-direction and transverse-direction elongation. Compression-moulded plaque data alone do not predict film tear resistance or dart impact; those responses require ASTM D1922 and ASTM D1709 on the actual film structure.

    When Regrind and Masterbatch Are Reintroduced into Monolayer Film

    Edge trim and start-up film regrind may be reintroduced into monolayer film at controlled ratios. At regrind levels up to 20 wt%, melt pressure and bubble stability generally remain within normal limits if the regrind is free of moisture and label contamination. Above 30 wt%, shifts in melt flow rate and dart impact can become measurable; converters should recondition or reduce regrind load when gauge variation exceeds ±8%. Slip and antiblock masterbatches based on erucamide and silica are typically dosed at 1–3 wt%; higher doses can lower tensile strength and raise haze. Under storage at relative humidity above 60%, surface moisture on pellets may create microvoids and bubble instability; predrying at 60–70 °C for 2–4 h before cast-film processing limits this defect. The resin should not be combined with certain metal stearates at elevated temperatures if colour and oxidative stability are critical; published data for this specific additive interaction is limited.

    Food-Contact Compliance and Regulatory Limits

    Under FDA 21 CFR 177.1520, high-density polyethylene may be used as a base polymer for food-contact articles, subject to end-use temperature and food-type restrictions. In the European Union, compliance is evaluated under Regulation (EU) No 10/2011; the overall migration limit is 10 mg/dm² for plastic food-contact materials unless a specific simulant lowers the permitted value. REACH obligations for registration and safety data sheet communication apply at the supplier level. Lead, cadmium, mercury, and hexavalent chromium concentrations are controlled to satisfy RoHS 2011/65/EU thresholds in electrical and electronic equipment applications. The resin is not inherently flame retardant, and it is not intended for direct contact with strong oxidizing acids or aromatic solvents at elevated temperature.

    In coextruded structures with ethylene-vinyl alcohol or polyamide barrier layers, HIVOREX 5000S is placed as the skin or core layer; maleic anhydride grafted tie resins are required for interlayer adhesion. The melt temperature is generally maintained near 215 °C to avoid excessive viscosity mismatch with the barrier layer, which can create interfacial instability. In cast film coextrusion with polypropylene skins, the HDPE layer is typically melted at 200–220 °C, and output split ratios are limited by the solidification difference between the two materials. These are process-specific limits; no single ISO method governs all interfacial stability boundaries.

    How Do Adjacent HIVOREX Grades Compare in Flow, Density, and End-Use Profile?

    The table below positions HIVOREX 5000S against representative Lotte HDPE grades with different melt flow rates and densities. Values are nominal datasheet typologies and should be verified against current technical data sheets.

    Grade MFR, ISO 1133-1 Density, ISO 1183-1 Typical conversion route Difference from HIVOREX 5000S
    HIVOREX 5000S 0.8 g/10 min 0.954 g/cm³ Blown film, cast film, sheet Reference
    HIVOREX 2200J 5.5 g/10 min 0.965 g/cm³ Thin-wall injection moulding Lower viscosity, shorter cycle, lower ESCR, higher density
    HIVOREX 7000F 0.04 g/10 min 0.951 g/cm³ High-strength film, geomembrane liners Higher molecular weight, higher melt pressure, higher tensile elongation, lower MFR
    HIVOREX 5200B 0.35 g/10 min 0.955 g/cm³ Large-part blow moulding Lower MFR, higher ESCR, higher melt strength, longer cycle

    Compared with HIVOREX 2200J, the lower MFR of 5000S creates a higher melt strength that improves bubble stability but reduces flow length in injection tools. Compared with HIVOREX 7000F, 5000S processes at lower screw-tip pressure and is more tolerant of older extrusion equipment, but it does not develop the same ultimate tensile elongation under ISO 527-2 and dart impact under ASTM D1709 in very high molecular weight film. Compared with HIVOREX 5200B, 5000S has higher flow and shorter moulding cycles but lower ESCR under ASTM D1693 in aggressive wetting-agent environments.

    Agricultural film producers running a 70 mm barrier screw with a 2.0 m die at 190–210 °C often specify HIVOREX 5000S for weed barrier and silage covers where tensile yield strength and puncture resistance are more important than optical clarity. At a 4:1 blow-up ratio and 0.9 mm die gap, gauge variation is generally maintained within ±7% when melt pressure remains above 18 MPa. Preheating the die lip to 205 °C before start-up reduces initial melt fracture on the inner bubble surface. Because the resin has no long-chain branching, it is not a direct replacement for low-density polyethylene in shrink film; shrink memory and transverse direction elongation are lower.

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