Products

Braskem HDPE GP100OR

    • Product Name: Braskem HDPE GP100OR
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
    • CONTACT NOW
    Specifications
    HS Code 410531
    Density 0.960 g/cm³
    Melt Flow Rate 190 C 2 16 Kg 10 g/10 min
    Tensile Strength At Yield 31 MPa
    Tensile Strength At Break 22 MPa
    Elongation At Break 600%
    Flexural Modulus 1400 MPa
    Notched Izod Impact At 23 C 50 J/m
    Notched Izod Impact At 20 C 30 J/m
    Shore D Hardness 65
    Vicat Softening Temperature 128°C
    Heat Deflection Temperature At 0 45 Mpa 80°C
    Melting Temperature 134°C
    Mold Shrinkage 1.5-2.0%
    Melt Temperature 200-230°C
    Mold Temperature 20-50°C

    As an accredited Braskem HDPE GP100OR factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Braskem HDPE GP100OR is supplied in 25 kg polyethylene bags, palletized for secure industrial storage and transport.
    Container Loading (20′ FCL) 20′ FCL Container Loading: Braskem HDPE GP100OR resin, 25 kg bags, palletized, shrink-wrapped, uniformly distributed, secured for ocean freight.
    Shipping Braskem HDPE GP100OR is a non-hazardous high-density polyethylene resin shipped as pellets. Typical packaging includes 25 kg bags, 1,000 kg jumbo bags, or bulk trucks/railcars. It is not DOT, IMDG, or IATA regulated. Store dry and cool, away from sunlight, heat, moisture, and contamination. Keep containers closed. Handle with care.
    Storage Store Braskem HDPE GP100OR in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, flames, and strong oxidizers. Keep original bags sealed and palletized, off the floor and away from moisture, dust, oils, and other contaminants. Avoid prolonged UV exposure. Maintain moderate temperatures and practice first-in, first-out inventory rotation. Follow local regulations and supplier guidance. Do not stack excessively.
    Shelf Life Braskem HDPE GP100OR: no defined shelf life if stored cool, dry, sealed, and out of direct sunlight; typical 24 months.
    Application of Braskem HDPE GP100OR

    Braskem HDPE GP100OR is an extrusion blow moulding grade with a melt flow rate in the 0.3 g/10 min region when measured at 190°C/2.16 kg under ISO 1133-1:2022. Its nominal density under ASTM D792-20 is 0.954 g/cm³, with tensile yield at 23°C of 26 MPa under ASTM D638-14 and flexural modulus near 1100 MPa under ISO 178:2019. These values place the material in the high-molecular-weight HDPE class used for large rigid packaging and automotive fluid reservoirs. Barrel temperature settings across an 80 mm single-screw extruder with 25:1 L/D begin at 170°C in zone 1 and rise to 195°C at the accumulator head, while mould temperature is held between 10°C and 25°C. Pre-drying is not required below 60% relative humidity; equilibrium moisture uptake remains below 0.01 wt%. The molecular weight distribution creates sufficient melt strength for unsupported parison lengths above 300 mm, reducing drawdown-induced thin-out in deep-draw tools.

    Which Parison Wall Distribution Deviations Trigger UN Packing Group II Drop and Stack Test Failures?

    For 20 L tight-head jerry cans marked UN 3H1/Y1.5/100 and intended for Packing Group II liquids, wall thickness distribution is the controlling variable in container certification. On a single-station shuttle machine with a 90 mm extruder and 26:1 L/D, the parison programmer sets a die gap of 2.2 mm for the bottom pinch-off region, widens to 3.8 mm at the chime shoulder, and narrows to 1.8 mm before the top weld line. If the chime area falls below 1.4 mm after mould shrinkage, drop energy concentrates at the mould parting line and the container cannot reliably survive the bottom drop impact test at 1.2 m onto a rigid concrete surface after 24 h conditioning at -18°C under 49 CFR 178.603. The hydraulic pressure test per 49 CFR 178.605 applies 100 kPa internal pressure for 30 min; GP100OR jerry can designs pass this sequence when the pinch-off weld line retains notched Izod impact values above 5 kJ/m² at 23°C under ISO 179-1:2023, and when the flash is trimmed without creating a sharp root radius. Stack compression under UN Manual of Tests and Criteria Part III Section 31.6.1.6 imposes a load equivalent to a stack height of 3.0 m for 28 days at 40°C. Sidewall thickness above 1.5 mm in the label panel typically limits week-four top-load deflection to below 8% of column height when the mould is held near 15°C and cooling time is set at 22 s. GP100OR exhibits F50 environmental stress crack resistance above 150 h under ASTM D1693-15, condition B, 10% Igepal CO-630, 50°C, but the full-package test matrix remains the governing qualification path because weld lines and pinch-off geometry introduce stress concentrations not present in notched laboratory specimens.

    Certification testStandard or methodCritical GP100OR-related parameterPass criterion
    Bottom drop impact49 CFR 178.603Chime wall thickness after shrinkageNo leakage at 1.2 m, -18°C, 24 h
    Hydraulic pressure49 CFR 178.605Weld-line integrity at handle pinch-offHold 100 kPa for 30 min
    Leakproofness49 CFR 178.604Neck finish roundness and bore sealNo leak at 20 kPa for 5 min
    Stack compressionUN Manual Part III 31.6.1.6Creep modulus at 40°CNo leak or structural failure at 3.0 m stack height for 28 days

    In agricultural chemical packaging, the survival of a 1 L to 10 L bottle against emulsifiable concentrate formulations is directly tied to the high-molecular-weight tail of GP100OR. Aromatic hydrocarbon co-solvents and nonylphenol ethoxylate surfactants accelerate environmental stress crack growth in low-density regions; the 0.954 g/cm³ density and broad molecular weight distribution produce F50 environmental stress crack resistance values above 150 h under ASTM D1693-15, condition B, 10% Igepal CO-630, 50°C. Blow moulding is carried out on two-cavity shuttle machines with shot weights of 250 g to 900 g. Parison programming must maintain a sidewall thickness above 0.8 mm at the label panel; below this threshold, gravitational creep during hot filling at 45°C can cause the panel to bow outward by more than 2 mm and compromise cap torque retention after 72 h at 35°C. For products containing methyl methacrylate or cyclohexanone, post-mould surface fluorination is required to reduce permeation loss below 0.5 wt% per year; the GP100OR base resin alone does not provide a solvent barrier. Batch-to-batch MFR variation of ±0.03 g/10 min is observed on production lines and may require parison programmer setpoint changes of 0.2 mm to 0.4 mm on the die gap to maintain the same wall thickness distribution.

    Hot Plate Weld Melt Penetration and Burst Pressure in Coolant Expansion Bottles

    Automotive coolant expansion bottles blow moulded from GP100OR are joined to injection-moulded HDPE spigots and mounting brackets by hot plate welding. The weld zone features a melt penetration depth of 0.5 mm to 1.0 mm, generated at a hot plate surface temperature of 215°C to 235°C and a clamp force of 0.2 N/mm² to 0.4 N/mm². If melt penetration is below 0.3 mm, cold weld lines reduce burst pressure to approximately 80 kPa; acceptable assemblies for pressurised passenger car surge tanks should withstand 150–250 kPa internal air pressure at 25°C for 30 s without leakage. Published burst-pressure data for GP100OR-specific hot plate welded assemblies is limited; the values cited here are representative of high-molecular-weight HDPE with comparable melt strength. GP100OR’s upper continuous service temperature in a 50% ethylene glycol mixture at 130°C is limited by oxidative induction time; OEM programmes commonly specify OIT above 20 min at 200°C under ISO 11357-6:2018. Mating surface flatness must be held within 0.1 mm total indicated runout to prevent channel leaks at the hot plate interface. The HDPE grade is not suitable for under-hood reservoirs with continuous exposure above 130°C or with high concentrations of hot oil mist; those conditions require polyamide or polypropylene blends.

    Stack compression at 40°C introduces a different failure mode in 1000 L intermediate bulk container inner bottles blow moulded from GP100OR on a 120 mm single-screw extruder with 30:1 L/D and a 12 kg accumulator shot. Top-load creep under a 3.0 m stack height imposes a static load of approximately 8 kPa on the base container; the critical design parameter is the hoop-wall thickness in the cylindrical sidewall transition near the bottom chime. A wall thickness above 1.8 mm limits circumferential strain to below 2.5% after 28 days at 40°C, while sections below 1.3 mm exhibit localised buckling and ultimately pinch-off cracking. The parison programmer must shift 0.5 mm additional die gap at the lower 20% of the parison to compensate for low-blow-ratio expansion. Hydraulic leak testing at 20 kPa internal air pressure for 5 min is followed by drop impact at 0.8 m onto a steel plate at -5°C for industrial liquids; GP100OR containers pass this sequence only when the sprue and flash line are heat-treated or polished. The base resin is not recommended for strong oxidising acids such as 98% sulfuric acid or 30% hydrogen peroxide, which induce chain scission at the inner wall.

    When UV Stabilizer Migration Alters the Surface Oxidation Induction Time in Above-Ground Storage Tanks

    For outdoor water storage and irrigation tanks blow moulded from GP100OR in shot sizes from 5 kg to 25 kg, the base resin without an adequate UV stabiliser package develops surface microcracks after 12–18 months of continuous exposure in high-UV climates. The controlling property is surface oxidation induction time, not bulk oxidation induction time; measurement of OIT at 200°C under ISO 11357-6:2018 on the outer 100 µm shows a decline from 20 min to 4 min when a 0.5 wt% hindered amine light stabiliser package is omitted. Processes add a UV masterbatch at 1.0 wt% to 2.5 wt% during extrusion blow moulding, with the exact dosage dependent on annual solar irradiance and wall thickness. The 0.954 g/cm³ density grade retains tensile yield above 20 MPa after 2,000 h of accelerated weathering under ASTM G154-23 cycle 1 when stabilised; unstabilised sections transition to brittle crack strains below 50%. Surface extraction of stabiliser in standing water is a recognised limitation; tanks used for potable water may require migration testing to Regulation (EU) 10/2011 or NSF/ANSI 61 depending on jurisdiction. Avoid post-welding reheating above 180°C, because residual antioxidant may volatilize and reduce long-term UV shelf life. Published data for GP100OR-specific OIT after extended weathering is limited; the ranges above reflect stabilisation practice for high-molecular-weight HDPE in outdoor tank service.

    On portable diesel fuel cans in the 5 L to 20 L range, GP100OR is processed without pre-drying at a melt temperature of 190°C. The critical performance attribute is permeation resistance to aromatic hydrocarbons in diesel; untreated HDPE GP100OR allows weight loss up to 1.0 wt% per year at 23°C, which generally satisfies class II portable fuel container emission limits only when wall thickness is maintained above 1.5 mm. Conductivity for electrostatic discharge is not an inherent property; anti-static or conductive carbon black masterbatch must be added at 4–7 wt% to achieve surface resistivity below 10⁹ Ω per ASTM D257-14 if the container is intended for use near explosive atmospheres. Welding of spouts and vent caps onto GP100OR fuel can bodies requires the same hot plate weld penetration range of 0.5–1.0 mm; lower melt depth produces leak paths at the spout root. Avoid storage of diesel fuel above 35°C in these containers because the diffusion coefficient rises sharply and weight loss can exceed the certified emission threshold within 30 days.

    Free Quote

    Competitive Braskem HDPE GP100OR prices that fit your budget—flexible terms and customized quotes for every order.

    For samples, pricing, or more information, please contact us at +8618136850665 or mail to admin@ascent-chem.com.

    We will respond to you as soon as possible.

    Tel: +8618136850665

    Email: admin@ascent-chem.com

    Inquiry

    Get Free Quote of Ascent Petrochem Holdings Co., Limited

    Flexible payment, competitive price, premium service - Inquire now!

    Certification & Compliance
    More Introduction

    Braskem HDPE GP100OR is a high-density polyethylene extrusion blow-molding compound carrying an orange pigmentation package. The OR suffix in the product nomenclature identifies the colored formulation; pigment loading is not disclosed in the standard technical data sheet. The base resin is characterized by a nominal melt flow rate of 0.30 g/10 min at 190 °C/2.16 kg when tested to ASTM D1238-20 and a density of 0.960 g/cm³ when tested to ASTM D792-20. This melt flow range places the material in the high-molecular-weight HDPE class used for extrusion blow molding rather than injection molding, where melt flow rates of 5–20 g/10 min are more common.

    What Melt Flow Rate and Density Values Define the GP100OR Processing Window?

    The processing identity of Braskem HDPE GP100OR depends on the combination of low melt flow rate and high density. The representative values below are derived from manufacturer-published data and should not be interpreted as specification limits. Lot-to-lot variation should be controlled through certificate-of-analysis review, especially for parison length control on shuttle machines.

    Representative GP100OR physical and mechanical properties
    PropertyTest methodRepresentative value
    Melt flow rate at 190 °C/2.16 kgASTM D1238-200.30 g/10 min
    DensityASTM D792-200.960 g/cm³
    Tensile strength at yieldASTM D638-1428 MPa
    Elongation at breakASTM D638-14>600 %
    Flexural modulusASTM D790-171,350 MPa
    Notched Izod impact at 23 °CASTM D256-106.5 kJ/m²
    Environmental stress crack resistance, F50, 10% Igepal, 50 °CASTM D1693-15>600 h
    Vicat softening temperatureASTM D1525-17128 °C
    Shore D hardnessASTM D2240-1568

    In continuous-extrusion shuttle blow molding, the practical melt temperature window is 200–220 °C. On a 60 mm single-screw extruder with a 24:1 L/D ratio, barrel temperatures are typically set from 180 °C at the feed throat to 215 °C at the adapter. Die-head zones are maintained at 205–215 °C. Exceeding 230 °C increases the rate of parison sag and can degrade the orange pigment, producing color drift and odor. Published data for the exact output rate of this pigmented compound on a given extruder is limited; output depends on screw speed, head pressure, and tooling geometry.

    Pellets are not hygroscopic in the bulk-diffusion sense, but surface condensation on pellets stored at relative humidity above 60% can cause splay at the die lip. A hopper dryer at 70–80 °C for 1–2 h is applied when surface moisture is observed on production batches. On accumulator-head machines with an 80 mm extruder and 24:1 L/D, stable parison formation is observed at melt temperatures of 210–220 °C. Above 225 °C, parison length variation increases measurably, and operators typically compensate by adjusting die gap or parison programming.

    When High ESCR and Drop-Impact Retention Are Required for Industrial Packaging

    GP100OR is directed toward extrusion blow-molded containers in which the orange color is integrated into the part rather than added as a masterbatch at the press. Typical application contexts include automotive fluid reservoirs, agricultural chemical packaging, and industrial drums. The orange pigmentation allows visual identification of service fluids or contents, which is critical when color coding is part of the logistics specification. The high environmental stress crack resistance of the base resin, with F50 greater than 600 h under ASTM D1693-15, supports container walls exposed to non-neutral liquids and external mechanical load.

    For blow-molded containers above 10 L, parison programming with 10–20-point wall-thickness control is required to compensate for parison swell and sag. Blow pressure is typically 0.6–0.8 MPa, and clamp force is calculated from the mold parting-line projected area. Drop-impact performance should be verified on production samples using ASTM D2463-15 for blow-molded containers, because the colored formulation may affect weld-line integrity and pinch-off toughness relative to unpigmented base resin. Published data for this specific orange configuration is limited; converter trials are used to establish minimum wall thickness at the pinch-off zone.

    The pigment package can also act as a stress riser in thin-wall sections if dispersion is incomplete. A barrier screw with a Maddock mixing section and screen pack of 20/40/60 mesh is commonly used to improve pigment dispersion and retain melt homogeneity. On high-output lines, inadequate mixing appears as surface streaks and variable drop-impact results rather than gross visual specks. Weld-line failures in container bases frequently originate at the pinch-off zone when mold temperature falls below 10 °C or when parison length exceeds the programmed profile beyond ±2% of the targeted value.

    Regulatory Status, Food-Contact Limitations, and Heavy-Metal Verification

    The base polyolefin component of GP100OR may be covered by 21 CFR 177.1520 for olefin polymers. However, the pre-colored orange formulation does not automatically inherit food-contact status. The specific pigment package must be assessed separately under the intended use conditions, including migration limits in 21 CFR 178.3297 or relevant European Union measures. The compliance checklist below identifies the regulatory items that converters must verify against supplier documentation.

    Regulatory verification matrix for Braskem HDPE GP100OR
    Regulatory itemStandard or referenceVerification scope
    U.S. food-contact base resin21 CFR 177.1520Covers olefin polymer; pigmented compound requires separate migration assessment
    EU plastic food-contactRegulation (EC) 1935/2004Overall migration limit of 10 mg/dm² must be demonstrated on finished article
    REACH registrationRegulation (EC) 1907/2006Substance registration obligations apply above 1 t/a; verify no SVHC above 0.1% w/w in formulation
    RoHS restricted substancesDirective 2011/65/EUCadmium, lead, mercury, hexavalent chromium, PBB, and PBDE levels must be confirmed for colored compound
    Color migration in packaging21 CFR 178.3297Pigment migration limits apply when orange color contacts food or pharmaceutical contents

    The orange pigment package may contain heavy-metal-based colorants if not sourced to pigment-exclusion specifications. Cadmium-based orange pigments are not permitted under RoHS-constrained applications. Suppliers of GP100OR should provide a heavy-metal certificate for each lot when the finished component enters electrical or electronic equipment. For automotive fluid reservoirs, OEM material specifications often add separate limits for odor, fogging, and extractable polar species; these are not covered by a generic HDPE datasheet and require part-level testing.

    GP100OR differs from GP100 natural in pigment dispersion, not base molecular architecture

    The orange variant shares the base melt flow and density envelope of the unpigmented GP100 blow-molding platform. The primary differences are rheological and morphological rather than architectural. The pigment phase can shift the melt flow rate by a small amount, typically within the normal lot-to-lot variation of the base resin; certificate-of-analysis values should supersede generic datasheet values. The pigmented compound also shows lower light transmission and may have altered notched impact sensitivity because the particulate colorant can initiate microvoid formation under high triaxial stress.

    The material is not intended for blown film. Film-grade HDPE often combines a higher melt flow rate and lower density to improve dart impact and tear resistance, whereas GP100OR uses a low melt flow rate and high density to increase stiffness, chemical resistance, and parison melt strength. Injection-molding HDPE grades with melt flow rates above 5 g/10 min flow more easily but cannot sustain parison formation without excessive sag. For this reason, substitution of GP100OR with injection-grade HDPE in blow molding produces wall-thickness variation, poor pinch-off strength, and low top-load performance.

    Continuous exposure to strong oxidizing acids, chlorinated hydrocarbons, or aromatic hydrocarbons under elevated hoop stress should be avoided, because these agents accelerate environmental stress cracking even though short-term chemical resistance appears adequate. The orange pigmentation does not function as a UV stabilizer. Outdoor service requires an additional carbon black or hindered amine light stabilizer package unless the finished part is installed in a shielded location. Processing temperatures above 230 °C should be avoided to limit pigment degradation, odor generation, and loss of ESCR. These conditions define the operational boundary for GP100OR in extrusion blow molding.

    Top