Cnooc Shell Cspc Huizhou Hdpe 5021d

CNOOC & Shell (CSPC Huizhou) HDPE 5021D

    • Product Name: CNOOC & Shell (CSPC Huizhou) HDPE 5021D
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    VTB
    Specifications
    HS Code 455133
    Density 0.952 g/cm³
    Melt Flow Rate 190 C 2 16 Kg 0.35 g/10 min
    Tensile Strength At Yield 26 MPa
    Tensile Strength At Break 30 MPa
    Elongation At Break >600%
    Flexural Modulus 1200 MPa
    Vicat Softening Temperature 124°C
    Melting Temperature 131°C
    Crystallization Temperature 112°C
    Environmental Stress Crack Resistance >1000 h
    Izod Notched Impact Strength 20 kJ/m²
    Hardness Shore D 65

    As an accredited CNOOC & Shell (CSPC Huizhou) HDPE 5021D factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing CNOOC & Shell (CSPC Huizhou) HDPE 5021D comes in 25 kg polyethylene-lined woven bags, 40 bags per 1,000 kg pallet.
    Container Loading (20′ FCL) 20′ FCL loading of CNOOC & Shell (CSPC Huizhou) HDPE 5021D: palletized 25kg bags, shrink-wrapped, stowed and lashed for export.
    Shipping CNOOC & Shell (CSPC Huizhou) HDPE 5021D is shipped as a non-hazardous polymer in 25 kg polyethylene bags, palletized and stretch-wrapped. It is typically loaded into 20-foot FCL containers for sea freight from Huizhou, China. Store dry, away from direct sunlight; no special dangerous-goods handling required.
    Storage Store in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, flames, and strong oxidizers. Keep bags/containers tightly closed to prevent moisture and contamination. Protect from physical damage; stack pallets securely and avoid excessive height. Use original packaging; rotate stock first-in, first-out. Avoid contact with incompatible substances and keep away from foodstuffs.
    Shelf Life Shelf life is typically 24 months when stored unopened in a cool, dry, ventilated area, away from direct sunlight and moisture.
    Application of CNOOC & Shell (CSPC Huizhou) HDPE 5021D

    In shuttle-type accumulator-head blow moulding of 10–30 L UN-certified jerrycans, the HDPE 5021D grade from CNOOC & Shell (CSPC) Huizhou is run at a melt temperature of 180–210 °C through a 70–90 mm screw with 24:1 L/D, delivering a parison to a diverging tool with a blow-up ratio of 2.5:1 to 3.0:1. The processing window is constrained by the grade’s nominal melt flow rate of 0.85 g/10 min under ISO 1133-1:2022 at 190 °C/2.16 kg and its nominal density of 0.956 g/cm³; wall-thickness control depends on a 20–60 point parison programmer because the pinch-off zone and top-load radius can degrade to below 1.2 mm when tooling wear exceeds 0.15 mm. The compound is dry-blended with 98.5–99.0 wt% virgin HDPE 5021D, 1.0–1.5 wt% carbon black or heavy-metal-free pigment masterbatch, 0.05–0.15 wt% hindered amine light stabilizer, and 0.02–0.05 wt% fluoropolymer-free process aid; addition of carbon black above 1.8 wt% alters zero-shear viscosity sufficiently to require a 5–8 °C melt-temperature increase. The compliance path for this downstream sector is anchored to UN Model Regulations 6.1.5.2, ADR 6.1.5, 49 CFR 178.509, and ASTM D4919, with design-qualification tests including a 250 kPa hydrostatic hold for 30 min and a 1.2 m drop at −18 °C. Terminal products are 5 L, 10 L, 20 L, 25 L, and 30 L jerrycans for Class 3 flammable liquids, designated as UN 3H1/Y1.5/250 packagings after certification.

    What governs barrier-layer distribution in 0.5–2 L agrochemical bottles?

    When a six-layer co-extrusion head runs HDPE 5021D as both skin layers at 185–200 °C, the EVOH core remains below its thermal degradation limit only if the barrier extruder is held at 200–205 °C and the die gap is kept within 0.6–1.2 mm; widening the gap beyond 1.4 mm produces observable layer inversion at the weld line and raises oxygen transfer rate above the 0.02 cm³/m²·day design ceiling. The total wall composition is typically 58–72 wt% virgin HDPE 5021D, 2–4 wt% EVOH barrier resin, 1.5–2.5 wt% maleic anhydride-grafted tie resin, and 15–30 wt% post-consumer HDPE regrind confined to the central regrind layer and encapsulated to prevent direct product contact. At tie-resin addition below 1.5 wt%, interlayer adhesion fails under 1.0 m drop impact, while above 2.5 wt% the outer skins lose through-thickness stiffness and the bottle top-load resistance at 23 °C drops below 220 N. The downstream production process is continuous co-extrusion blow moulding with an 80 mm main extruder at 25:1 L/D, a 90 mm spiral mandrel die head, parison swell controlled to 20–35%, and blow pressure held at 0.7–0.9 MPa. Regulatory instruments for this sector include UN Model Regulations 6.1.4 for packaging of hazardous chemicals, EPA FIFRA 40 CFR 156 for pesticide label-packaging compatibility, EU BPR for treated articles, and ISO 16101 for transport packaging compatibility. Terminal products are 0.5 L, 1 L, and 2 L multi-layer bottles for organophosphate and pyrethroid formulations, with nitrogen permeability controlled by the EVOH layer and closure systems limited to high-density polypropylene caps with fluoropolymer-lined seals.

    Application zoneRegulatory instrumentTest method / designationAcceptance threshold
    UN-certified jerrycanUN Model Regulations 6.1.5.2Hydrostatic pressure 250 kPa / 30 min; drop 1.2 m at −18 °CNo leak, no rupture
    Agrochemical barrier bottleEPA FIFRA 40 CFR 156Permeation and drop impact 1.0 mNo package incompatibility
    Recycled-content non-food bottleEU Packaging Directive 94/62/ECHeavy metal sum ≤100 mg/kgPb, Cd, Hg, Cr(VI) compliance
    Automotive washer reservoirISO 16750-4Vibration profile 10–1000 HzNo weld-line crack
    Extruded non-food sheetREACH Annex XVIISVHC communicationNo restricted substance
    Detergent bottleEU CLP + UN GHSLabel content compatibilityNo stress-cracking leakage

    Post-consumer recyclate addition to HDPE 5021D is not a simple viscosity adjustment: a 15–40 wt% PCR fraction narrows the parison die-swell range and forces the accumulator-head line to reduce shot size by 4–8% at constant die gap because the recycled fraction contains trace amounts of calcium carbonate, mixed HDPE grades, and oxidized gel seeds. The practical formulation for non-food containers is 60–85 wt% virgin 5021D, 15–40 wt% washed post-consumer HDPE flake with residual moisture below 0.08 wt%, 0.05–0.12 wt% phenolic antioxidant, and 0.02–0.05 wt% calcium stearate acid neutralizer. The melt is processed at 180–195 °C rather than the higher virgin-only range, because gel counts above 200 μm increase by a factor of 2–3 at temperatures above 205 °C; a 45 μm continuous screen changer or 325-mesh screen pack is used when PCR exceeds 25 wt%. The relevant compliance framework includes REACH SVHC communication requirements, EU Packaging Directive 94/62/EC heavy-metal limits, and ISO 14021 for recycled-content claims. Operational boundaries are explicit: at PCR loadings above 30 wt%, published recycling studies report environmental stress-crack resistance can fall by 30–50% against virgin benchmarks, though published data for this specific 5021D configuration is limited and line qualification must verify lot-to-lot gel content. Terminal products are 500 mL–5 L non-food detergent bottles, industrial dosing jugs, and household chemical containers.

    Automotive washer reservoir pinch-off seam failure under vibration loading

    Pinch-off seam failure in blow moulded windscreen washer reservoirs is commonly misread as a wall-thickness deficiency; in production-scale tools, the failure more often originates at ethylene-rich low-molecular-weight tails squeezed into the weld seam when the accumulator head drools beyond 0.15 mm during transfer. For this application, HDPE 5021D is compounded with 96.5–98.0 wt% virgin resin, 1.5–2.0 wt% carbon black/UV masterbatch, and 0.03–0.08 wt% primary antioxidant; no external processing oil is used because oil migration onto reservoir surfaces changes weld strength and increases stress-crack susceptibility. The process is extrusion blow moulding with a 75–90 mm screw at 24:1 L/D, melt temperature 190–210 °C, blow pressure 0.65–0.85 MPa, and mould surface temperature held at 15–25 °C. The critical quality parameter is not average sidewall thickness but pinch-off tail length, which should remain below 0.7 mm; when tooling is worn beyond 0.2 mm, tail length increases and the seam fails under ISO 16750-4 swept-sine vibration from 10–1000 Hz. The component qualification also references ASTM D256 Izod impact at −30 °C and ISO 178 flexural modulus, with expected modulus near 1,100 MPa for the base resin. Terminal products are 2.0 L, 3.5 L, and 5.5 L windscreen washer reservoirs with pump-flange insert geometry, and 1.0–3.0 L technical fluid reservoirs for off-highway vehicles, where OEM material approval permits a nominal density of 0.956 g/cm³.

    When sheet extrusion through a three-roll stack runs with HDPE 5021D and 30% in-plant regrind

    If sheet extrusion through a three-roll stack is run with HDPE 5021D and 20–30 wt% clean in-plant regrind, the limiting variable is drawdown rather than thermal uniformity, because the blow-moulding-grade melt exhibits lower melt strength than a dedicated sheet grade and the sheet web begins to sag at a gauge above 3.0 mm unless melt temperature is reduced to 180–190 °C. The formulation is 70–80 wt% virgin 5021D, 20–30 wt% edge-trim regrind, and 0.02–0.05 wt% phosphite-antioxidant masterbatch; no regrind is used above 30 wt% because sheet impact strength declines disproportionately at the trim hot-blend point. The production line uses a 105 mm single-screw extruder at 30:1 L/D, a melt pump, a 900–1,600 mm sheet die, and a three-roll calender running at 12–18 m/min with roll temperatures of 85–95 °C. Compliance for non-food sheet uses REACH Annex XVII and EU Packaging Directive 94/62/EC heavy-metal limits; food-contact sheet is not assigned to this grade configuration without independent compliance testing under EU 10/2011. Terminal products are 1.5–4.0 mm thermoformed dunnage trays, nestable pallet covers, and machinery transit covers, with in-plant regrind recovered from skeleton trim at 12–18% of net sheet output.

    Continuous wheel-type blow moulding of 500 mL–5 L detergent bottles uses a 60–75 mm screw at 24:1 L/D, melt temperature 180–195 °C, die gap 0.4–1.0 mm, blow pressure 0.6–0.8 MPa, and a blow-up ratio of 2.0:1 to 2.5:1. The addition package for this sector is 1.0–1.5 wt% white masterbatch, 0.03–0.07 wt% erucamide slip additive, and 0.02–0.04 wt% silica antiblock; the erucamide content must not exceed 0.08 wt% because surface migration above that threshold lowers cap torque retention and creates a measurable loss in closure seal tension after 72 h of storage at 40 °C. The governing regulatory frame is UN GHS label content compatibility and EU CLP for packaging of hazardous liquid detergents; package qualification follows drop tests from 1.0 m and leak tests after 24 h of simulated transport vibration. Terminal products are trigger-spray detergent bottles, concentrated laundry liquid bottles, and non-sterile household wetting-agent containers in the 0.5–5 L range.

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    Certification & Compliance
    More Introduction

    CNOOC & Shell (CSPC Huizhou) HDPE 5021D is a high-density polyethylene resin specified for extrusion blow molding of small-to-medium rigid containers. The producer technical literature lists nominal values rather than guaranteed sale specifications. The grade is typically supplied as pellets and is converted on shuttle blow molders, reciprocating screw machines, and accumulator-head equipment where parison stability is the controlling requirement.

    PropertyNominal valueTest method
    Melt mass-flow rate0.85 g/10 minISO 1133-1:2022
    Density at 23 °C0.950 g/cm³ISO 1183-1:2019
    Tensile yield stress24 MPaISO 527-2:2012
    Elongation at break>600%ISO 527-2:2012
    Flexural modulus950 MPaISO 178:2019
    Vicat softening temperature A50124 °CISO 306:2022

    These values place 5021D in a mid-flow blow molding segment. The melt mass-flow rate of 0.85 g/10 min under ISO 1133-1:2022 is approximately one order of magnitude below CSPC 5306J, a nominal 6.0 g/10 min injection grade. That difference excludes thin-wall injection molding as a primary conversion route. The density of 0.950 g/cm³ is lower than that of many high-rigidity HDPE grades, which shifts the balance toward environmental stress crack resistance and parison consolidation rather than maximum top-load modulus. Common applications include household chemical bottles, personal care containers, and small industrial liquid packaging with wall thicknesses from 0.6 mm to 2.0 mm. In large containers above 5 L, melt strength may become limiting; published data for this specific configuration is limited.

    What Processing Window Governs Extrusion Blow Molding of 5021D?

    On shuttle blow molders equipped with reciprocating screw extruders having L/D ratios between 24:1 and 30:1, a starting barrel temperature profile from feed throat to die is 180 °C, 190 °C, 200 °C, and 210 °C, with die temperature held at 200 °C. Mold temperature is maintained between 10 °C and 30 °C to control cooling rate and reduce post-mold shrinkage. Blow air pressure is typically set at 0.5–0.8 MPa, depending on parison wall thickness, mold venting, and container geometry. Production-scale experience on 25:1 L/D barrier screws indicates that die-exit melt temperature should not exceed 215 °C; at 225 °C and higher, parison sag increases and side-wall thickness distribution deteriorates. Published data for this specific configuration is limited, but the standard corrective action is to reduce barrel temperatures, lower screw speed, or both.

    Because HDPE is not hygroscopic, pre-drying is generally unnecessary. If resin is stored in an unheated warehouse with relative humidity above 60% or is transferred from a cold silo into a warm production hall, surface condensation can generate splay and bubble defects in the parison. Drying at 80 °C for 2–4 h in a desiccant dryer is applied under those conditions. Regrind from flash and rejected containers can be blended with virgin resin, provided it is dry and free of polar contamination. Typical regrind levels on blow molding lines are between 20 wt% and 30 wt%; higher fractions may reduce melt strength and increase gel counts after multiple heat histories.

    Batch-to-batch variance should be controlled by reviewing the producer’s certificate of analysis for melt mass-flow rate and density. Because parison sag is sensitive to low-shear melt viscosity, a shift in MFR within the allowed specification may require adjustment of die gap, extrusion speed, or parison programming.

    Pinch-off weld failure is a recurring defect in small bottles when mold temperature falls below 10 °C or when blow pressure is insufficient to force material into the pinch-off land. The parison swell characteristics of 5021D require careful die gap and blow delay settings. A blow delay of 0.2–0.5 s after mold close is often used to improve base weld thickness. For a 500 mL bottle on a double-station shuttle machine, cycle times of 12–18 s are typical, but these depend on wall thickness, mold cooling layout, and ambient temperature. Published data for this specific configuration is limited.

    When 5021D Replaces Higher-Density Blow Molding Grades in Rigid Packaging

    The main distinction among CSPC HDPE grades is the combination of melt flow, density, molecular architecture, and additive package. In direct comparison, 5021D differs from 5000S primarily in density and conversion route. 5000S is used in film, tape, and monofilament extrusion where orientation and tensile strength dominate; its nominal density of 0.954 g/cm³ provides higher modulus but generally lower stress crack resistance than 5021D under the same ASTM D1693 test. Compared with 5200B, a large-part blow molding grade with nominal MFR of 0.35 g/10 min, 5021D produces lower head pressure and higher throughput on small shuttle machines, but it is less suitable for containers above approximately 20 L where parison length and sag resistance become limiting.

    GradeNominal MFR (g/10 min, ISO 1133-1:2022)Nominal density (g/cm³, ISO 1183-1:2019)Primary conversion routeDistinguishing processing constraint
    5021D0.850.950Extrusion blow moldingParison sag control above 215 °C
    5000S0.900.954Film, tape, monofilament extrusionHigher density reduces low-temperature impact resistance
    5200B0.350.956Large-part blow moldingHigh melt strength but lower throughput
    5306J6.00.957Injection moldingHigh flow unsuitable for stable parison formation

    5021D is not interchangeable with injection molding grades such as 5306J. The low MFR of 5021D would require high injection pressure and may produce short shots in thin-wall molds designed for 6.0 g/10 min material. Conversely, 5306J lacks the melt strength needed to hold a stable parison on a blow molder. Selection of 5021D for rigid packaging should therefore be based on container volume, wall thickness distribution, and the required environmental stress crack resistance under the intended contact liquid.

    Chemical compatibility testing is mandatory for aggressive or oxidizing formulations. The resin is not recommended for continuous contact with strong oxidizing acids, aromatic solvents, or halogenated hydrocarbons. Polar liquids containing high levels of nonylphenol ethoxylates can accelerate environmental stress cracking in HDPE; compatibility should be evaluated under ASTM D1693-B at 50 °C using the production container geometry. The upper continuous service temperature for unstressed HDPE is commonly cited at 65 °C, but this value is formulation-dependent and must be validated for the finished part under load and chemical contact.

    Regulatory Status and Food-Contact Compliance Pathways

    Polyethylene resins may be evaluated for food-contact suitability under FDA 21 CFR 177.1520 in the United States and under EU Regulation (EC) No 1935/2004 with specific migration testing under Commission Regulation (EU) No 10/2011. The producer’s compliance declaration for 5021D should be consulted to confirm whether the specific lot and additive package are cleared for direct food contact. Finished articles intended for food contact should be tested for overall migration under ISO 1186-1:2019 or specific migration in the selected food simulant. For industrial packaging, compliance with REACH depends on monomer and additive registration status. RoHS 2011/65/EU heavy metal restrictions are generally applicable to electrical and electronic equipment rather than packaging, but packaging components may have separate obligations under 94/62/EC and local packaging regulations.

    Pellets should be stored below 50 °C and protected from UV radiation. Prolonged exposure to sunlight can oxidize the polymer surface and shift color. The certificate of analysis should include melt mass-flow rate under ISO 1133-1:2022, density under ISO 1183-1:2019, and ash content where applicable.

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