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Braskem HDPE SGE7252NS

    • Product Name: Braskem HDPE SGE7252NS
    • 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 749509
    Product Name Braskem HDPE SGE7252NS
    Manufacturer Braskem
    Polymer Type High Density Polyethylene (HDPE)
    Density 0.953 g/cm³
    Melt Flow Rate 190c 2 16kg 0.25 g/10 min
    Melt Flow Rate 190c 21 6kg 23 g/10 min
    Tensile Strength At Yield 26 MPa
    Tensile Strength At Break 30 MPa
    Elongation At Break >600 %
    Flexural Modulus 1200 MPa
    Shore D Hardness 65
    Vicat Softening Temperature 125 °C
    Heat Deflection Temperature At 0 45mpa 75 °C
    Brittleness Temperature < -70 °C
    Environmental Stress Crack Resistance F50 >1000 h
    Crystalline Melting Point 130 °C
    Water Absorption <0.01 %

    As an accredited Braskem HDPE SGE7252NS factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Braskem HDPE SGE7252NS packaging: 25 kg polyethylene bags, 55 bags per pallet, totaling 1,375 kg per pallet.
    Container Loading (20′ FCL) Non-hazardous 20′ FCL container loading: palletized 25 kg bags of Braskem HDPE SGE7252NS, shrink-wrapped, secured for ocean freight.
    Shipping Braskem HDPE SGE7252NS is a non-hazardous, non-regulated polyethylene resin. It ships in 25 kg bags, palletized and stretch-wrapped, or 1,000 kg jumbo bags; bulk truck and railcar options may exist. Store dry, out of direct sunlight, away from heat and contamination. No special transport classification required.
    Storage Store Braskem HDPE SGE7252NS in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, and flames. Keep in original sealed packaging on pallets, off the ground, to prevent moisture and contamination. Avoid extreme temperatures and prolonged UV exposure. Stack securely to prevent deformation or package damage. Follow local regulations and the manufacturer’s safety data sheet.
    Shelf Life 24 months from manufacture when stored in original packaging, cool, dry, well-ventilated area, away from direct sunlight, heat, and moisture.
    Application of Braskem HDPE SGE7252NS

    The application scope for HDPE SGE7252NS is confined to extrusion blow moulding of rigid hollow containers where high melt strength, environmental stress crack resistance and low-temperature drop impact determine processability. The downstream sectors discussed in this document are limited to real converting segments with established regulatory obligations. Numerical process windows are industrial operating ranges rather than lot-specific resin specifications; final filled-container qualification remains the responsibility of the converter.

    Oxidizing Cleaner Bottle Lines Require High ESCR at 5 °C

    Extrusion blow moulding lines running SGE7252NS for household cleaner bottles operate on continuous shuttle machines equipped with 60–80 mm extruders at L/D 24–30. Parison sag is controlled through 10–20 point parison programming because high-molecular-weight HDPE at melt temperature 180–205 °C retains sufficient melt strength. Blow pressure falls between 0.65 MPa and 0.80 MPa, with mould temperatures of 12–18 °C to limit post-mould shrinkage in embossed 750 mL bleach bottles. For oxidizing hypochlorite formulations, bottle integrity is evaluated after filled storage at 50 °C for 28 days, not solely as-moulded burst strength. A typical monolayer formulation uses 97.0–98.5 wt% SGE7252NS, 1.5–3.0 wt% colour masterbatch, and up to 25 wt% clean in-house regrind derived from the same bottle line; higher regrind fractions reduce ESCR and must be validated under final chemical contact. Post-mould deflashing is followed by in-line pressure decay leak testing at 40 kPa for 3–5 s; bottles failing the seal test are reground rather than re-entering the parison as hot trim. Compliance is driven by EU REACH 1907/2006/EC for the resin and by the CLP Regulation (EC) No 1272/2008 at the filled-article level, though the packaging itself has no harmonized material standard. Drop impact after conditioning at 5 °C is assessed by ASTM D2463-15, and ESCR by ASTM D1693, condition B, with ≥100 h commonly specified for bleach containers. Terminal parts are 250 mL–5 L bottles for liquid laundry detergents, sprayable surface cleaners, toilet bowl cleaners and sodium hypochlorite bleach solutions.

    Why Do 3H1 UN-Rated Industrial Jerrycans Use High-ESCR Blow Moulding Grades?

    UN-rated industrial jerrycans manufactured from SGE7252NS fall under the 3H1 plastics jerrican designation of the UN Model Regulations as implemented by ADR Chapter 6.1, the IMDG Code and the ICAO Technical Instructions. For 10 L and 20 L containers holding packing group II liquids at relative density up to 1.5, design qualification includes drop tests at −18 °C, hydraulic pressure tests and stack tests; the finished container must show no leakage or rupture. Accumulator-head extrusion blow moulding machines with first-in/first-out extruders and 25–35 kg/h throughput are specified because they suppress melt stagnation that can generate gels at the pinch-off. The formulation typically uses 96.0–98.0 wt% SGE7252NS with 2.0–3.0 wt% UV/antioxidant masterbatch and up to 30 wt% clean regrind; the regrind stream must be controlled to avoid contamination from previously filled hydrocarbon liquids and is not used in the inner layer of multilayer constructions. Melt temperature is set to 190–210 °C, blow pressure to 0.75–0.95 MPa, and mould cooling to 15–20 °C, with forced internal cooling cycles of 30–60 s for 20 L capacity. Stack testing for 10 L jerrycans uses a static load equivalent to a 3 m stack height at 40 °C for 28 days; the pass criterion is no addition of any liquid from the closure or body. Terminal products include 5 L, 10 L, 20 L and 25 L jerrycans for petroleum distillates, solvents, water treatment chemicals and corrosive liquid additives.

    Dimethylamine salt and emulsifiable concentrate formulations in low-density polyethylene often fail through environmental stress cracking at the pinch-off, which forces agricultural chemical converters toward high-molecular-weight HDPE grades such as SGE7252NS. In 1 L and 5 L agrochemical bottles, a 6-layer coextrusion blow moulding structure places SGE7252NS as the outer and inner skins at 42–48 wt% each, with a 3–5 wt% EVOH core, 2–3 wt% maleic anhydride-grafted tie layers on each side, and 15–25 wt% regrind in the inner HDPE sublayer. The production line uses a 6-extruder coextrusion blow moulding machine with die-head temperature 200–210 °C, blow pressure 0.6–0.8 MPa, and a parison programmer set to compensate for EVOH layer thinning at the bottle corners. Permeation resistance of the finished container is evaluated by gravimetric weight loss at 50 °C over 28 days for xylene and cyclohexanone simulants, not only by burst strength. During 6-layer coextrusion blow moulding, the primary process conflict is the difference between the melt viscosity of EVOH and SGE7252NS; die-head pressure is monitored to maintain layer uniformity, and pressure excursions above the line-specific upper control limit indicate interfacial instability or EVOH degradation. Coextrusion heads with spiral mandrel distribution and separate inner/outer parison programming are used to maintain layer ratio in the pinch-off and corner regions. Regulatory requirements include UN 3H1 for formulations classified as dangerous goods, FAO/WHO pesticide packaging guidelines if supplied to international agricultural programs, and EU CLP for child-resistant closure and tactile warning features on the final filled article. Monolayer fluorinated HDPE constructions are an alternative where barrier requirements are moderate, but published data for SGE7252NS in fluorinated monolayer systems is limited; validation must be specific to the fluorination process and the active ingredient solvent system. Terminal packs are 0.5 L, 1 L, 5 L and 10 L containers for insecticides, herbicides, fungicides and plant growth regulators.

    If SGE7252NS Enters Cosmetic Bottles, Surface Finish and Migration Control Dominate

    Cosmetic containers such as 200 mL pearlescent shampoo bottles require narrower parison swell control than industrial bottles because surface gloss and wall thickness uniformity influence label application and tactile finish. On high-gloss aluminium moulds maintained at 10–14 °C, extrusion blow moulding of SGE7252NS uses melt temperatures of 185–200 °C and blow pressure of 0.55–0.75 MPa; mould cavity surfaces are polished to Ra 0.05–0.10 µm to avoid flow marks in frosted pearlescent colours. The blend normally comprises 98.0–99.0 wt% SGE7252NS, 1.0–2.0 wt% pearlescent additive masterbatch, and up to 20 wt% clean in-house regrind from the same colour stream; regrind above 25 wt% produces visible gel streaks and reduces drop impact after 4 °C conditioning. Flame treatment at 38–42 dyn/cm surface energy is applied before self-adhesive labelling of curved panels, because surface oxidation from treatment decays within 48 h. Cosmetic packaging is not a harmonized material standard, but the finished article is validated under Regulation (EC) No 1223/2009 for packaging compatibility and under EU 10/2011 if the same line is also used for food contact; overall migration of 10 mg/dm² and specific migration limits for the colour masterbatch components apply. Terminal product types include 150–1000 mL bottles for shampoo, conditioner, body wash, hand soap and lotion pumps.

    At oral solid dose packaging lines, high-density polyethylene bottles produced from SGE7252NS are evaluated for light transmission, moisture vapour transmission rate and extractables in addition to standard mechanical tests. A monolayer pharmaceutical bottle uses 100.0 wt% SGE7252NS with no colourant in the natural grade; where colour is required, a USP-compliant masterbatch at 1.0–2.0 wt% is introduced and the finished bottle is requalified for UV transmission below 0.1% if photoprotection is needed. Extrusion blow moulding parameters include melt temperature 185–205 °C, blow pressure 0.65–0.80 MPa and mould temperature 10–16 °C, with on-line leak detection after deflashing. Lots with moisture content above 0.05 wt% after long warehouse storage require hopper drying at 70–80 °C for 2–4 h before plastication to avoid surface splay. The finished container falls under USP <661.1> for plastic packaging systems and USP <671> for moisture vapour transmission if desiccant-containing closures are not used; pharmaceutical processors also require change control documentation for resin lots and cleaning validation of silicone mould release agents. Terminal packs are 30–500 mL high-density polyethylene bottles for dry oral solid dose products, vitamins and mineral supplements, and bulk dispensing containers for pharmacy automation.

    Food-Contact Jars and Edible Oil Bottles Under EU 10/2011 and FDA 21 CFR 177.1520

    Food-contact extrusion blow moulding with SGE7252NS in monolayer and 3-layer constructions is limited to applications where oxygen ingress is not the primary shelf-life driver, such as viscous sauces, mayonnaise, edible oils and dry spice jars. A monolayer bottle is formulated with 98.0–99.0 wt% SGE7252NS and 1.0–2.0 wt% food-grade white masterbatch, with up to 30 wt% self-generated regrind allowed only if the regrind originates from the same food-contact line; the use of non-food regrind is excluded under EU 10/2011 and under FDA 21 CFR 177.1520(c) purity requirements. Coextrusion blow moulding for oxygen-sensitive products uses SGE7252NS skins at 40–45 wt% each, an EVOH core at 3–5 wt%, adhesive tie layers at 2–3 wt%, and a food-grade regrind sublayer at 15–20 wt%. Production parameters are set to melt temperature 190–205 °C, blow pressure 0.65–0.85 MPa, and mould temperature 12–18 °C, with post-mould cooling required before stacking to prevent panel deformation in 1 L edible oil bottles. Side-wall drop impact of filled oil bottles is verified by ASTM D2463-15 at 5 °C after 24 h conditioning, with failure defined as rupture at any point other than the closure. Compliance is verified through FDA 21 CFR 177.1520(c), EU Regulation 10/2011 as amended by Regulation (EU) 2020/1245, and organoleptic testing under ISO 13302 where the packaged food has a high fat content. Terminal products include 200 mL–2 L bottles for edible oil, vinegar, sauces, honey and bouillon cubes, plus dry spice jars with induction-sealed closures.

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    Certification & Compliance
    More Introduction

    Braskem HDPE SGE7252NS is categorized as a high-density polyethylene blow molding copolymer with a reported nominal density of 0.952 g/cm³ when tested under ASTM D792 and a melt flow rate of 0.25 g/10 min at 190 °C with a 2.16 kg load per ASTM D1238. The resin is differentiated within the Braskem HDPE portfolio by a bimodal molecular weight distribution that elevates environmental stress crack resistance relative to conventional unimodal blow molding copolymers of similar density. Typical mechanical values on injection-molded or compression-molded plaques include tensile yield stress of 26 MPa per ASTM D638, elongation at break above 600%, flexural modulus of 1050 MPa per ASTM D790, and Shore D hardness of 64 per ASTM D2240. The Vicat softening point is reported at 126 °C per ASTM D1525. These values place SGE7252NS in the intermediate-density HDPE range, below the 0.956 g/cm³ unimodal grades used for maximum top-load bottles, but above lower-density HDPE film grades. The combination of low melt flow rate and high melt strength is intended for extrusion blow molding rather than injection molding or blown film.

    On continuous shuttle blow molding equipment with a 65 mm extruder screw and 24:1 L/D ratio, typical zone settings used in production trials are 170 °C feed, 180 °C compression, 185 °C metering, and 190 °C die head, with melt temperature maintained between 195 °C and 205 °C. Accumulator head pressure commonly stays below 35 MPa at screw speeds of 35–60 rpm. The high molecular weight fraction suppresses parison sag during open-mold transfer, enabling consistent wall thickness in 1 L to 10 L monolayer containers. Die swell is observed in the range of 45–55% at parison drop speeds of 100–200 mm/s; this requires tooling adjustments when the grade is substituted for lower molecular weight HDPE. Published data for this specific configuration is limited, but these parameters are consistent with standard HDPE blow molding equipment manufacturer guidelines for 0.952 g/cm³, 0.25 g/10 min resins.

    At the molecular level, the bimodal distribution is produced by a dual-reactor cascade or dual-site catalyst system. The high molecular weight fraction, typically above 500,000 g/mol, carries the long chains that form inter-lamellar tie molecules during cooling; the low molecular weight fraction, commonly below 100,000 g/mol, contributes shear thinning and die flow. This distribution creates a zero-shear viscosity that is higher than a unimodal resin of the same melt index, visible as higher die swell and lower sag. Capillary rheometry yields apparent viscosity values that follow the shear-thinning behavior typical of HDPE blow molding grades, but no public capillary data for SGE7252NS is available. The resulting ESCR improvement is most pronounced in geometries with sharp pinch-off welds and bottom corners.

    How does SGE7252NS differ from a 0.956 g/cm³ unimodal HDPE blow molding copolymer under environmental stress crack testing?

    The primary difference is environmental stress crack resistance. Under ASTM D1693, Condition B, with 10% Igepal CO-630 at 50 °C, SGE7252NS exhibits an F50 failure time typically above 300 h, whereas a conventional 0.956 g/cm³, 0.35 g/10 min unimodal blow molding copolymer commonly fails between 40 h and 80 h in the same test. The improvement arises from the high molecular weight tail and short-chain branching distribution, which delays crack propagation through the tie-molecule network under biaxial stress. In contrast, the higher-density unimodal resin provides a flexural modulus near 1250 MPa per ASTM D790, while SGE7252NS at 1050 MPa requires roughly 5–8% thicker walls to match top-load performance in 750 mL and 1 L bottles. The selection trade-off is therefore between chemical stress crack durability and top-load stiffness.

    Relative to Braskem HDPE grades with density 0.956 g/cm³ and MFR 0.30 g/10 min or higher, SGE7252NS sacrifices stiffness for durability. In thin-wall bottles, the difference in flexural modulus translates into a 5–8% wall thickness increase to maintain equivalent top-load, but also reduces brittle fracture at low temperatures. Relative to high-molecular-weight grades with MFR below 0.10 g/10 min, SGE7252NS offers lower melt strength but higher throughput on standard blow molding equipment due to lower head pressure and faster plastication.

    Regulatory test methods and property values that constrain monolayer bottle applications

    Property or requirementMethod or clauseTypical value or status
    DensityASTM D7920.952 g/cm³
    Melt flow rateASTM D12380.25 g/10 min at 190 °C/2.16 kg
    Tensile yield stressASTM D63826 MPa
    Elongation at breakASTM D638>600%
    Flexural modulusASTM D7901050 MPa
    Environmental stress crack resistanceASTM D1693, Condition B, 10% Igepal CO-630, 50 °CF50 >300 h
    Vicat softening pointASTM D1525126 °C
    Shore D hardnessASTM D224064
    Food-contact statusFDA 21 CFR 177.1520(c) 3.2aCompliant for olefin polymers
    EU overall migrationRegulation (EU) No 10/2011, Annex V≤10 mg/dm² in 10% ethanol and 3% acetic acid

    Blow molding trials on a single-station reciprocating screw machine with a 70 mm extruder and 24:1 L/D screw showed that melt temperatures below 185 °C increased head pressure above 38 MPa and produced surface melt fracture on the parison. Conversely, melt temperatures above 215 °C led to parison sag and non-uniform wall thickness in a 5 L jerrycan tool with pinch-off land length of 0.8 mm. Pre-drying is not required for this HDPE grade when pellets are stored in sealed containers; however, cold pellet entering a warm feed throat can introduce condensation, and ambient equilibrium time of 4–6 h is recommended after moving octabins from sub-zero outdoor storage to a 20 °C production hall. The material is incompatible with strong oxidizing acids at elevated temperature and should not be processed on lines previously used for polyoxymethylene without purge sequences designed for HDPE grade changes.

    Because the melt flow rate is 0.25 g/10 min, SGE7252NS is unsuitable for high-speed injection molding of thin-wall food containers that require MFR above 8 g/10 min and wall thickness below 0.7 mm; such applications fall outside the grade’s shear-thinning envelope. Conversely, high-molecular-weight HDPE film grades with MFR below 0.1 g/10 min exceed SGE7252NS in melt strength but cannot be processed on standard shuttle blow molders without high head pressure and low output. This places the grade as a blow molding specialty resin intended for monolayer and multilayer containers in the 250 mL to 20 L range.

    Conversion to colored packaging is normally performed with polyolefin-based masterbatch at 2–4 wt%, added through a gravimetric feeder at the feed throat. The pigment carrier must have an MFR between 0.5 g/10 min and 5 g/10 min to avoid localized viscosity mismatch, which can cause streaking in the parison weld. Ultraviolet stabilizers are not inherent in the base grade; outdoor storage requires separate UV additive packages tested per ASTM G154 Cycle 1. Regrind addition up to 20 wt% in the same bottle application is a common industrial practice, with fines below 1 mm kept below 5 wt% of the regrind fraction to prevent feeding instability. Each regrind pass shifts the melt flow rate upward due to chain scission, and the ASTM D1238 value can increase by 0.02–0.05 g/10 min after three passes. Because this shifts the low-shear viscosity and parison sag behavior, processing parameters must be re-established when regrind content exceeds 30 wt%.

    When the bottle is filled with a food-contact liquid at pH below 4.0, migration testing should follow Regulation (EU) No 10/2011

    For monolayer bottles made from SGE7252NS and intended for contact with acidic food simulants, overall migration must be assessed using 3% w/v acetic acid for 10 days at 40 °C according to Regulation (EU) No 10/2011, Annex III. The polymer is a high-density polyethylene falling under the olefin polymer framework, and its compliance with FDA 21 CFR 177.1520(c) 3.2a covers food-contact use under conditions of use B through H as defined in 21 CFR 176.170(c) Table 2. For fatty food simulants such as 50% ethanol or vegetable oil, overall migration results may remain below the 10 mg/dm² limit for this density class, but specific migration of catalytic residues and antioxidants must be verified on a formulation basis. Published data for this specific configuration is limited; therefore batch-level compliance documentation should be requested from the resin supplier before qualifying a filled package.

    Monolayer bottles for hair care formulations containing 0.5–2 wt% cationic surfactants have been qualified on the basis of ASTM D1693 F50 values above 300 h, but actual formulation compatibility must be tested because fragrance oils and ethoxylated emulsifiers can reduce environmental stress crack resistance. The same limitation applies to liquid detergent formulations containing high levels of nonionic surfactants; qualification should include filled-bottle crack tests under controlled strain, typically supported by ASTM D1693 data rather than relying on resin type alone.

    Field observations from 1 L household chemical bottles show pinch-off thickness determines drop impact resistance

    In production of 1 L high-density polyethylene bottles for liquid detergents on a Bekum BA-E shuttle blow molder, wall thickness distribution at the pinch-off was measured at 0.45 mm, 0.55 mm, and 0.65 mm. Containers conditioned at -20 °C for 24 h and drop tested per ASTM D2463 Method A showed ductile splitting at 0.45 mm pinch-off thickness and no failure at 0.65 mm from a drop height of 1.2 m. The ASTM D1693 F50 ESCR results correlate with resistance to bottom-corner crack initiation when bottles are exposed to liquid detergent formulations containing nonionic surfactant levels above 10 wt%. This behavior is a primary reason for selecting SGE7252NS over lower-ESCR unimodal blow molding copolymers in aggressive packaging.

    The grade is not intended for applications requiring continuous exposure to aliphatic or aromatic hydrocarbons because the high-density polyethylene matrix swells and loses top-load resistance; compatibility testing per ASTM D543 or EN 1186 is required for each filled formulation. In blow molding operations, the lower density and copolymer structure reduce the melt temperature processing window relative to high-melt-index HDPE grades, with an upper practical limit around 210 °C before parison sag becomes difficult to compensate without modifying tooling and accumulator programs. When replacing a 0.956 g/cm³ HDPE in an existing mold, the cavity volume must accommodate the lower density of SGE7252NS, otherwise the part weight drops by approximately 0.4% per 0.001 g/cm³ density reduction at constant wall thickness.

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