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Ningxia Baofeng Energy HDPE HD55110

    • Product Name: Ningxia Baofeng Energy HDPE HD55110
    • 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 777093
    Polymer Type High Density Polyethylene (HDPE)
    Density 0.955 g/cm³
    Melt Flow Rate Mfr 190 C 2 16 Kg 11.0 g/10 min
    Tensile Yield Strength ≥25 MPa
    Elongation At Break ≥500%
    Flexural Modulus ≥1000 MPa
    Vicat Softening Temperature ≥120°C
    Shore D Hardness ≥60
    Notched Izod Impact Strength ≥40 J/m
    Environmental Stress Cracking Resistance Escr ≥1000 h
    Water Absorption <0.01%
    Dielectric Constant 1 Mhz 2.3
    Volume Resistivity ≥10^16 Ω·cm
    Oxidation Induction Time 200 C ≥20 min
    Ash Content ≤0.03%
    Moisture Content ≤0.1%

    As an accredited Ningxia Baofeng Energy HDPE HD55110 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Ningxia Baofeng Energy HDPE HD55110 is supplied in 25 kg polyethylene woven bags, typically 25 metric tons per 20-foot container.
    Container Loading (20′ FCL) 20′ FCL loading for Ningxia Baofeng Energy HDPE HD55110: 25 kg bags, palletized, about 18–22 MT net, secure seaworthy packing.
    Shipping Ningxia Baofeng Energy HDPE HD55110 is a non-hazardous high-density polyethylene resin, typically supplied in 25 kg bags on pallets. Ship in dry, clean containers via sea or road, avoiding moisture, direct sunlight, and heat. No dangerous goods classification; standard cargo handling applies. Keep packaging sealed during transit.
    Storage Store Ningxia Baofeng Energy HDPE HD55110 in a cool, dry, well-ventilated warehouse away from direct sunlight, heat, and ignition sources. Keep original bags or containers sealed and palletized to prevent moisture, dust, and contamination. Avoid contact with strong oxidizers. Observe stack-height limits, use first-in-first-out rotation, protect packaging from damage, ensure spill containment, and follow local regulations.
    Shelf Life Ningxia Baofeng Energy HDPE HD55110 shelf life: typically 12 months in unopened original packaging, stored cool, dry, away from sunlight.
    Application of Ningxia Baofeng Energy HDPE HD55110

    Across thin-wall dairy and food-service container lines, HD55110 is processed as a high-flow narrow molecular weight distribution HDPE whose melt classification under ISO 1133-1:2022 at 190°C/2.16 kg places it in the fast-fill segment for valve-gated hot-runner tools running 4 to 16 cavities. The regulatory basis for direct food contact is FDA 21 CFR 177.1520 for olefin polymers, EU Regulation 10/2011 Annex I overall migration provisions, and (EC) No 2023/2006 GMP requirements; converters exporting to multiple jurisdictions normally issue a Declaration of Compliance tied to lot-specific certificates rather than grade designation alone. The production formulation for white pigmented dairy and margarine containers is based on 2.0–4.0 wt% titanium dioxide masterbatch, 0.05–0.15 wt% nucleating agent, and a combined phenolic/phosphite antioxidant package at 0.06–0.12 wt%; higher nucleant loadings in trial runs have produced secondary crystallization effects visible as crease-whitening at thin wall hinges near lid undercuts. High-speed injection molding machines with clamp force ratings between 250 and 500 t are used, with screw L/D ratios of 20:1 to 24:1, accumulator-driven injection speeds of 200–350 mm/s, melt temperature of 205–235°C, mold temperature of 8–20°C, and holding pressure between 40 and 70 MPa. Production line cycle time runs from 4.5 to 8.0 s; surface splay appears when ambient RH exceeds 60% for extended silo residence or when regrind above 20 wt% introduces moisture-laden fines, so desiccant drying is reserved for masterbatch at 80°C for 2 h under documented humidity excursions. Terminal articles include 250 mL to 1000 mL dairy pots, margarine tubs, sauce cups, and related lidless thin-wall packaging, where stacking stiffness after chilled distribution and mouth-opening dimensional stability are the primary converter acceptance criteria.

    Why do high-cavity closure tools accept fast melt transit but not inconsistent cushion control?

    Closure manufacturing from HD55110 on 32 to 96 cavity stack molds is less constrained by melt viscosity than by short-shot repeatability and post-molding slip additive migration. Food-contact closures cite FDA 21 CFR 177.1520 and EU Regulation 10/2011; child-resistant caps intended for cleaning and chemical products require ISO 8317:2015 torque and opening-force certification, while pharmaceutical contact components are evaluated under USP <661.1> plastic material characterization and Ph. Eur. 3.1.3 polyolefin requirements. The additive package is specified differently from thin-wall food packaging: erucamide slip additive at 500–1500 ppm, synthetic silica antiblock at 800–2000 ppm, and color masterbatch at 1.0–3.0 wt%. Slip loadings above 3000 ppm create mold-vent plate-out on consecutive-run 96-cavity trials and are rejected; slip reduction below 500 ppm yields cap removal torque drift that fails closure-level shelf-life checks after 72 h of ambient aging. Injection-compression molding is run with clamp force ratings from 350 to 650 t, melt temperature of 205–230°C, mold temperature of 10–25°C, and cycle time of 5.5–9.5 s; back pressure is limited to 5–12 MPa because screw recovery occurs during ejection and excessive back pressure extends recovery beyond the mold-open window. On production lines, cushion variation beyond ±1.5 mm across a 96-cavity stack mold is correlated with cap out-of-roundness exceeding 0.15 mm and with induction-seal liner wrinkles at downstream capping stations. Terminal closure types include tamper-evident screw caps for dairy milk, still water, and non-carbonated beverages, as well as household chemical closures fitted with induction seal liners; carbonated soft drink closures are generally supplied from PP grades, and published comparative ESCR data for this specific configuration is limited.

    Unlike thin-wall food-service lines, industrial pail production from HD55110 is governed by dangerous-goods packaging codes and drop-test severity rather than migration testing alone. Open-top pails intended for hazardous substances are marked 1H2 and tight-head containers 1H1 under UN Model Regulations Chapter 6.1, with conformity across ADR, RID, and IMDG transport modes; food-grade pails additionally cite FDA 21 CFR 177.1520 and EU Regulation 10/2011 when contents are food ingredients. The formulation for exterior-storage and chemical pails uses hindered amine light stabilizer at 0.20–0.50 wt%, a phenolic/phosphite antioxidant blend at 0.10–0.20 wt%, and color masterbatch at 1.5–3.5 wt%; clean internal regrind is added at 10–25 wt% provided the lot MFR under ISO 1133-1:2022 remains within the supplier certificate range and adhesive label contamination is absent. Injection machines for 5–25 L pails are specified with clamp forces of 800–1600 t, accumulator-assisted injection speeds of 180–300 mm/s, and shot capacity at least 30% above nominal pail shot mass. Melt temperature is maintained at 215–245°C, mold temperature at 15–35°C, holding pressure at 50–80 MPa, and total cycle time at 28–45 s. Hydraulic core pulls for handle bosses require sequenced open/close movement; cushion below 3 mm has repeatedly produced sink marks at the handle bridge and drop-test leakage on production runs. UN drop-test height is assigned by packing group: 1.8 m for PG I, 1.2 m for PG II, and 0.8 m for PG III. Terminal articles include open-top 5–25 L pails for coatings, adhesives, water-based chemical formulations, construction compounds, and food ingredients; compression and stacking evaluation is performed under ISO 12048.

    Structural-foam pallet molding under ISO 8611 service loads

    For structural-foam pallet production, HD55110 is compounded with a chemical blowing agent to correct thick-section sink and to raise panel stiffness at reduced part density. Reusable plastic pallets are qualified under ISO 8611-1:2011 test methods and ISO 8611-2:2011 performance criteria for racking, flexural, and impact sequences; pallets in direct contact with food or pharmaceutical materials additionally cite FDA 21 CFR 177.1520, and wood-packaging quarantine rules such as ISPM 15 do not apply to solid plastic decks. The formulation uses azodicarbonamide-based blowing agent masterbatch at 0.5–1.5 wt%, HALS UV-stabilizer masterbatch at 0.2–0.5 wt%, and process regrind at 15–30 wt%; regrind content is capped because repeated heat history shifts the melt viscosity and degrades top-skin foam uniformity. Low-pressure structural foam injection machines are specified with clamp forces from 1500 to 2500 t, shot sizes above 30 kg, and melt temperature of 200–230°C; mold temperature is held at 10–25°C and cycle time runs from 80 to 150 s because solidification of the 20–35 mm deck section is the controlling variable rather than injection fill. Blowing agent loadings above 1.5 wt% produce density variation across the deck and have been associated with top-skin delamination at injection gate swirl zones; published data for this specific configuration is limited. Terminal products include 1200 × 1000 mm and 1100 × 1100 mm distribution pallets, rackable hygienic pallets for food and pharmaceutical logistics, and heavy-duty export pallets carrying ISO 8611 racking loads.

    When storage containers cross the EN 71-3 boundary without toy intent

    Under the EN 71-3 boundary, stackable storage containers and household totes molded from HD55110 require a regulatory decision before colorant and filler packages are frozen. General consumer articles are assessed under REACH Regulation (EC) No 1907/2006 Annex XVII restricted-substance conditions and, only if toy classification applies, EN 71-3:2019 migration limits for heavy metals; food storage containers cite FDA 21 CFR 177.1520 and EU Regulation 10/2011. The production formulation uses 2.0–4.0 wt% color masterbatch, 0.05–0.10 wt% antioxidant, and optionally 3.0–10.0 wt% calcium carbonate masterbatch to reduce warpage in large flat bases; filler loadings above 10 wt% are avoided for export markets with freezer storage because cold-temperature impact toughness under ISO 179-1 deteriorates. Injection molding is performed on conventional cold-runner machines with clamp forces from 300 to 800 t, melt temperature of 200–230°C, mold temperature of 15–35°C, and cycle times of 25–50 s depending on side-wall thickness. Deep-draw geometry and low draft angles used for stack-nesting require multiple air poppets and extended ejection dwell; mouth-opening dimensional tolerance of ±0.5 mm is the primary lid-to-base fit criterion and the most common converter rejection cause. Terminal products include stack-and-nest storage bins, under-bed boxes, laundry baskets, and modular shelving components.

    Pharmaceutical closure adapter molding from HD55110 departs from industrial packaging because extractables profiles and cleanroom discipline override cost-driven process shortcuts. Materials for pharmaceutical contact are characterized under USP <661.1> plastic material tests and Ph. Eur. 3.1.3 polyolefin monographs, with additional assessment under FDA 21 CFR 177.1520 when the component is used in a food-medical interface; no zinc stearate mold release or erucamide slip additive is permitted in the base formulation unless explicitly justified in the extractables dossier. The formulation is constrained to 0.0–1.5 wt% color masterbatch and a phenolic/phosphite antioxidant package at 0.04–0.08 wt%; batch-to-batch additive variation is controlled by supplier certificate of analysis and is traceable to the resin lot. Injection molding occurs in an ISO Class 8 cleanroom under ISO 14644-1:2015, using all-electric injection molding machines with clamp forces from 120 to 250 t, melt temperatures of 200–225°C, mold temperatures of 15–30°C, and cycle times of 12–20 s; all-electric drives are preferred because hydraulic oil mist conflicts with cleanroom particle counts. Terminal articles include closure adapters, dosing cup components, dust caps, and lid inserts for oral liquid and ophthalmic packaging; dimensional capability and cleanliness are specified together, with bioburden sampling replacing visual inspection as the release control.

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    Certification & Compliance
    More Introduction

    HD55110, a high-density polyethylene from Ningxia Baofeng Energy, is positioned for extrusion blow molding, medium-gauge sheet, and limited thick-section injection work. The product designation belongs to the producer’s HDPE slate that also includes 5000S, 5502, 8008, and 7000F. Nominal melt mass-flow rate is 1.10 g/10 min at 190 °C/2.16 kg and nominal density is 0.955 g/cm³. These figures come from the producer’s published nominal data; the batch certificate remains the controlling document for die design and thermal profiling. Publicly available data for this specific configuration is limited, so pilot trials are necessary when substituting HD55110 into an existing tool. The resin sits between lower-flow blow-molding grades and higher-flow injection grades, which defines its processing latitude and property trade-offs.

    Product Designation and the 1.10 g/10 min Melt Flow Envelope

    The 1.10 g/10 min melt mass-flow rate determined under ISO 1133-1:2022 characterizes a medium-viscosity HDPE. In extruder pressure-flow terms, this lowers head pressure relative to a 0.35 g/10 min 5502-type resin at constant screw speed, but it also reduces parison hang strength; the optimum die gap and pre-blow timing must be established on the specific production line. Density of 0.955 g/cm³ contributes stiffness and chemical resistance but reduces low-temperature impact relative to HDPE copolymers below 0.945 g/cm³. The molecular weight distribution and short-chain branching, visible through flow rate ratio and comonomer content, are not disclosed in all public literature; their effects appear during processing as shifts in shear thinning and die swell.

    Which Specification Values Govern Lot Acceptance for HD55110?

    Table 1 lists the property set normally reported for HD55110. The values are nominal and are not guaranteed minima or maxima. Specimens for mechanical testing are conditioned at 23 ± 2 °C and 50 ± 10% relative humidity per ISO 291 before evaluation. Where a property is critical, test specimens should be taken from the same lot used in production and compared against the batch certificate.

    Property Standard and specimen Nominal value
    Melt mass-flow rate, 190 °C/2.16 kg ISO 1133-1:2022 1.10 g/10 min
    Density ISO 1183-1 0.955 g/cm³
    Tensile yield stress ISO 527-2, type 1A, 50 mm/min 26 MPa
    Tensile elongation at break ISO 527-2, type 1A 600 %
    Flexural modulus ISO 178 1,100 MPa
    Charpy notched impact strength, 23 °C ISO 179-1/1eA 6.0 kJ/m²
    Vicat softening temperature, A50 ISO 306 126 °C
    Shore D hardness ISO 868 63
    Environmental stress crack resistance, F50, 10% Igepal CO-630 ASTM D1693-B 50 h

    Extrusion processing of HD55110 is performed on single-screw extruders with a length-to-diameter ratio of at least 25:1 and a barrier screw with compression ratio between 2.5:1 and 3.0:1. A typical barrel profile from feed throat to metering section is 180 °C, 200 °C, 210 °C, 215 °C; adapter and die head are held at 200–210 °C. Melt temperature should not exceed 225 °C for extended residence; above 240 °C oxidation leads to chain scission and gel formation. Virgin pellets stored below 60% relative humidity do not require drying, but condensation on cold pellets must be removed with a desiccant-air hopper dryer at 80 °C for 2 h when surface moisture exceeds 0.05 wt%. Extruder head pressure and motor load should be charted hourly; a gradual pressure rise indicates melt filtration blockage or gel accumulation.

    Thermal stability of HD55110 is monitored by oxidative induction time at 210 °C using ISO 11357-6 or ASTM D3895. Olefin materials in this density class typically show OIT values above 20 min when sufficient hindered phenolic stabilization is present; shorter values indicate antioxidant depletion or contaminated regrind. Differential scanning calorimetry per ISO 11357-3 records a peak melting temperature near 130–135 °C and a crystallization temperature near 115–118 °C; downstream annealing temperatures should remain at least 10 °C below the crystallization onset to minimize post-mold shrinkage.

    When Blow Molding Operations Shift from 5000S or 5502 to HD55110

    Extrusion blow molding with HD55110 runs with lower head pressure than 5502 because of higher melt flow. Barrel set points can be reduced by 5–10 °C to maintain melt temperature and die swell. For 1–10 L containers, a divergent die gap of 1.5–2.5 mm is used; pre-blow delay is shortened relative to 5502 because parison drawdown occurs more rapidly under its own mass. Blow pressure is held at 0.6–0.8 MPa and mold surface temperature at 15–25 °C. Container qualification uses drop impact per ASTM D2463, top load per ASTM D2659, and environmental stress crack resistance per ASTM D2561. In replacement trials, load at yield, wall-thickness distribution, and pinch-off weld strength are compared directly with the incumbent material. Large jerry cans above 20 L may show increased parison sag depending on die temperature; 5502 remains preferable when a long hang time is unavoidable.

    Parison programming must be tuned to wall-thickness distribution. A typical die gap of 1.5–2.5 mm is maintained at the top and bottom, with an additional 0.5–1.0 mm of die opening at the pinch-off region for containers with square cross-sections. The accumulator head should be pressure-controlled within 0.1 MPa to avoid repeatability errors. In continuous extrusion shuttle machines, melt temperature variation between shots should not exceed ±3 °C; larger variation creates bottle weight drift and top-load scatter.

    Grade Nominal MFR Nominal density Main processing window Operational limitation
    HD55110 1.10 g/10 min 0.955 g/cm³ Extrusion blow molding, sheet, thick-section injection Parison sag above 20 L unless tool adjusted
    5000S 0.90 g/10 min 0.954 g/cm³ Blow molding Lower melt flow than HD55110
    5502 0.35 g/10 min 0.955 g/cm³ Large blow-molded containers Higher head pressure, longer cycle
    8008 8.0 g/10 min 0.956 g/cm³ Injection molding Lower ESCR than HD55110
    7000F 0.04 g/10 min 0.955 g/cm³ High-strength film Not suitable for blow molding

    Sheet extrusion from HD55110 is carried out on a single-screw line with polished three-roll stack temperature of 75–90 °C. Sheet thickness from 1–4 mm is typical. Vacuum forming is performed at a sheet surface temperature of 150–165 °C; forming at temperatures above 170 °C causes local gloss change and may promote post-shrinkage. Draw ratios should not exceed 3:1 because localized thinning consumes the elongation reserve. The higher melt flow relative to 5000S can raise sheet output at equal screw speed, but it also reduces sag resistance in vertical edge sections during heating.

    Exclusion Boundaries for Pressure Pipe and Thin-Wall Injection

    HD55110 is not positioned for PE100 pressure pipe service under ISO 4427. Hydrostatic design stresses of 8 MPa at 20 °C are not supported by the available long-term data for this melt flow class. Pipe designers should select certified PE100 or PE100-RC resins with the appropriate MRS classification under ISO 9080 and ISO 12162. In injection molding, HD55110 can fill thick-walled parts with wall thickness above 2.5 mm; it is not suitable for multi-cavity thin-wall closure molds where flow-length-to-wall-thickness ratios exceed 150:1, because freeze-off occurs before complete packing. High-flow HDPE grades such as 8008 are required for those tools.

    Regulatory documentation should be checked by the converter for each lot. Under REACH, the polymer itself is exempt from registration; monomers and additives are covered by the supplier safety data sheet. Food-contact status is not automatically established across all markets; compliance with FDA 21 CFR 177.1520 or EU 10/2011 must be confirmed on the final article, including migration testing. Storage is recommended below 40 °C, protected from ultraviolet exposure. Avoid dry blending with amine-based antistatic concentrates without pre-validation because surface bloom can reduce heat-seal strength in downstream packaging. Mechanical recycling of regrind is possible up to 20 wt%, provided the regrind is clean and dried; higher levels can increase gel counts in film and sheet.

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