| HS Code | 945624 |
| Density | 0.965 g/cm³ |
| Melt Flow Rate | 3.0 g/10 min (190°C/2.16 kg) |
| Tensile Strength At Yield | 28 MPa |
| Tensile Strength At Break | 25 MPa |
| Elongation At Yield | 9% |
| Elongation At Break | 600% |
| Flexural Modulus | 1400 MPa |
| Notched Izod Impact | 40 J/m |
| Vicat Softening Point | 128°C |
| Heat Deflection Temperature | 75°C at 0.45 MPa |
| Hardness | Shore D 65 |
| Environmental Stress Crack Resistance | 10 h (100% Igepal) |
| Molding Shrinkage | 2.0-3.0% |
| Melt Temperature | 200-230°C |
| Mold Temperature | 20-60°C |
| Moisture Absorption | <0.01% |
| Uv Stabilization | Yes |
As an accredited Braskem HDPE HDI0653U1 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Braskem HDPE HDI0653U1 packed in 25 kg bags, 55 bags per pallet, shrink-wrapped for industrial shipping. |
| Container Loading (20′ FCL) | Braskem HDPE HDI0653U1, packaged in 25kg bags, palletized and loaded into a 20-foot FCL for safe, efficient ocean shipment. |
| Shipping | Braskem HDPE HDI0653U1 is shipped as non-hazardous polyethylene resin pellets, usually in 25 kg bags, bulk bags, or octabins on pallets. Transport by truck, rail, or container under dry, clean conditions. Keep packaging closed; avoid moisture, sunlight, and contamination. No special DOT, IMDG, or IATA hazard classification is required. |
| Storage | Store Braskem HDPE HDI0653U1 in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, flames, and strong oxidizers. Keep original bags or containers tightly closed to prevent moisture, dust, and contamination. Use pallets, avoid crushing or high stacks, and follow first-in, first-out inventory. Protect from UV exposure and extreme temperatures. Maintain good housekeeping and segregate from incompatible materials. |
| Shelf Life | Shelf life is approximately 24 months when stored in original packaging, cool, dry, ventilated area, away from direct sunlight and heat. |
Sidewall deflection in HDI0653U1 thin-wall containers is governed by differential shrinkage between the gate region and the rim, not by bulk melt flow alone; published moulding trials on equivalent high-flow HDPE grades show that mould temperature imbalance of ±2 °C across the cavity can produce measurable ovality in containers with wall stock below 0.8 mm. The base resin is processed neat at 100 wt% or blended with 0.5–2 wt% of a nucleating and processing-aid masterbatch; for applications where recycled content is permitted under food-contact migration rules, 10–30 wt% of mechanically recycled HDPE may be introduced only if the recyclate has a positive EFSA opinion or is sourced from a closed-loop process validated under EU Regulation 10/2011 and FDA 21 CFR 177.1520. Compliance for dairy cups, deli containers and margarine tubs includes EU Regulation 10/2011, FDA 21 CFR 177.1520, and sensory tests under EN 1230-1:2009 where odour or taint is critical; U.S. converters also verify total chromium, cadmium, lead and mercury under CONEG model legislation and file food-contact substance notifications for antimicrobial or oxygen-scavenging masterbatches if used. The injection process uses fast-fill, pressure-limited profiles in machines with clamp force from 2,000 kN to 8,000 kN, screw L/D ratios of 20:1–24:1, and cold runners or hot runners with small gate diameters of 0.8–1.5 mm; melt temperature is maintained at 210–240 °C, mould temperature at 15–35 °C, and holding pressure at 30–50 MPa to limit sink marks around rim snap features. The production bottleneck is cooling time; for a 0.6 mm wall, demoulding without deformation requires surface temperature below 70 °C, and cycle times are commonly 6–12 s in multi-cavity stack moulds. Demoulded article types include injection-moulded dairy cups, single-serve ice cream containers, delicatessen trays, hinged-lid food storage boxes, and thin-wall lids for non-hot-fill applications below 70 °C continuous fill.
The standards applicable to HDI0653U1 downstream sectors are consolidated below; converters must verify the final formulation because masterbatch carriers and regrind streams alter overall migration and organoleptic profiles.
| Downstream sector | Primary standard | Secondary standard | Numerical limit or test condition |
|---|---|---|---|
| Food/beverage closures | FDA 21 CFR 177.1520 | EU Regulation 10/2011 | Overall migration 10 mg/dm²; organoleptic test EN 1230-1 |
| Thin-wall food containers | EU Regulation 10/2011 | FDA 21 CFR 177.1520 | Overall migration 10 mg/dm²; sensory test EN 1230-1 |
| Housewares and utility articles | REACH Annex XVII | RoHS Directive 2011/65/EU where relevant | Heavy metal sum 100 ppm under EU 94/62/EC |
| Crates, pallets and logistics trays | ISO 8611-1 | ISO 178 | Heavy metal sum 100 ppm under EU 94/62/EC |
| Industrial pails | ADR 6.1.5 where UN packaging applies | EU Regulation 10/2011 where food contact applies | Overall migration 10 mg/dm²; drop test per ADR 6.1.5 |
| Child-resistant chemical closures | ISO 8317:2015 | REACH Annex XVII | Heavy metal sum 100 ppm under EU 94/62/EC |
When housewares converters run high-cavitation tools, the resin must enter the mould with sufficient fluidity to replicate textured surfaces and retain post-mould ductility for snap-fit assembly. HDI0653U1 is injection-moulded in open-nozzle reciprocating-screw machines with melt temperatures between 190 °C and 220 °C, mould temperatures from 20 °C to 40 °C, and back pressure not exceeding 1.5 MPa; higher back pressure combined with screw speeds above 200 rpm can generate shear heating and local melt temperatures above 240 °C, producing colour streaking and molecular chain scission. Compliance for household articles that are not used for food contact is bounded by REACH Annex XVII, RoHS Directive 2011/65/EU for electrical accessories, and EU Directive 94/62/EC for heavy metals in packaging components; when the article may come into occasional food contact, the converter must verify the full formulation under EU Regulation 10/2011 or FDA 21 CFR 177.1520, including colour masterbatches and UV stabiliser packages. In formulation, the resin is supplied at 96–100 wt% with 0–4 wt% pigment masterbatch; for storage containers exposed to detergents or oils, environmental stress crack resistance is improved by blending 10–20 wt% butene- or octene-based LLDPE with a melt flow rate of 0.5–1.5 g/10 min, although this blend reduces flexural modulus by roughly 10–20% and lengthens cooling time. Downstream processing is performed on standard reciprocating-screw injection presses with clamp force from 1,200 kN to 10,000 kN; deep-draw storage boxes require textured mould surfaces and draft angles no less than 0.5°. The critical process limit is warpage in flat bases and sidewalls after ejection; holding pressure and gate freeze time must be adjusted to compensate for differential shrink in parts with wall thickness transitions from 1.5 mm to 5 mm. Finished article types include storage boxes, utility baskets, hangers, flower pots, waste bins, trays and non-food household containers.
HDI0653U1 is used in rigid logistics applications where thick walls and high projected areas demand controlled flow-front velocity and sustained holding pressure. The melt is prepared at 210–250 °C and injected into chilled moulds at 15–35 °C; the flow rate reduces injection pressure drop in flow paths exceeding 1,000 mm, but wall sections below 3 mm can freeze prematurely and compromise corner strength. Compliance for industrial crates and pallets references ISO 8611-1 for pallet performance, ISO 178 for flexural modulus measurement, ASTM D638-14 for tensile yield stress, and EU Directive 94/62/EC with heavy metal limits of 100 ppm total lead, cadmium, mercury and hexavalent chromium. Formulation for indoor logistics parts uses 85–100 wt% HDI0653U1 with 0–15 wt% clean post-industrial regrind from edge trim or rejected parts; outdoor or cold-room applications add 1–3 wt% UV stabiliser masterbatch and 0.1–0.5 wt% antioxidant masterbatch to prevent chain scission under prolonged UV exposure and repeated washing. This grade is not intended for heavy-duty pallets requiring maximum environmental stress crack resistance; light-to-medium crates and trays are within scope when validated under ISO 8611-1 load deflection and corner-impact protocols. Downstream processing is performed on hydraulic or hybrid injection presses with clamp force from 8,000 kN to 25,000 kN; the screw is often a barrier-type design with L/D of 22:1–25:1 and a compression ratio of 2.2:1–3.0:1. The production bottleneck is cooling time for thick bosses and rib intersections; segregated cooling circuits are maintained at 10–20 °C in high-shrinkage zones, while holding pressure at 40–70 MPa is maintained until gate freeze. Premature gate sealing causes sink marks at rib bases and reduces stacking-lug dimensional accuracy. Finished product types include stackable beverage crates, logistic trays, pallet corner blocks, agricultural harvesting crates and collapsible distribution boxes.
Refrigerated core cooling becomes advantageous in pail production when wall thickness exceeds 2.5 mm and the handle boss is solidified last. HDI0653U1 is processed neat at 100 wt% or with 1–4 wt% colour and UV masterbatch; clean in-house regrind from rejected pails may be introduced up to 20 wt% only when the pail is not subject to UN dangerous goods certification, because batch-to-batch regrind variability can alter drop-test performance under ADR 6.1.5. Compliance for industrial pails includes ADR 6.1.5 or IMDG requirements for non-dangerous solid outer packaging where applicable, EU Directive 94/62/EC for heavy metals, and FDA 21 CFR 177.1520 when the pail is intended for food ingredient storage; food-grade pails also require organoleptic validation under EN 1230-1:2009 and overall migration testing under EU Regulation 10/2011. In processing, the melt temperature is held at 210–230 °C; the mould core is supplied with water/glycol at 5–15 °C through baffle or bubbler circuits, while the cavity is kept at 20–35 °C to avoid surface freeze and gloss mismatch. The resulting asymmetrical cooling produces a skin-core morphology that increases impact toughness but can generate internal residual stress if holding pressure is released before gate freeze; the recommended holding pressure range is 40–60 MPa for gate diameters of 2–4 mm. The key process limit is handle boss sink: the boss wall section can be 2.5–4 times the nominal wall, requiring sequential valve gates or two-stage packing pressure to avoid visible sink marks. Published multi-factor interaction data for this specific configuration is limited; converters must verify final dimensions and drop-test behaviour on production tooling. Moulded article types include 1 L to 5 L open-head pails for paints, adhesives, construction chemicals, food ingredients and lubricant additives.
Non-food chemical and agrochemical closures impose a different additive tolerance than food-contact caps because the closure must retain child-resistant torque over repeated open-close cycles while resisting attack from esters, surfactants and hydrocarbon-based formulations. HDI0653U1 is compounded with 1–2 wt% of a high-purity erucamide slip masterbatch and 0.5–1.5 wt% of a UV/antioxidant additive package; the base resin remains 96–98.5 wt%, with no post-consumer recyclate because the risk of contaminant-induced stress cracking is high. Compliance is driven by REACH Annex XVII for phthalates and heavy metals, EU Directive 94/62/EC with 100 ppm heavy metal limits, and for closures used on certain chemical products, ISO 8317:2015 child-resistant packaging testing and chemical compatibility protocols under ISO 16750-type exposure sequences; food-contact status is not applicable, but the closure must not contaminate the packaged product through additive migration. The injection process is run on multi-cavity unscrewing or collapsible-core moulds because child-resistant designs have internal thread undercuts; melt temperature is held at 200–230 °C, mould temperature at 20–35 °C, and injection speed is set lower than for thin-wall food containers to prevent jetting through small gates of 0.8–1.2 mm. Torque retention is the primary process-related failure mode: excessive slip additive above 2 wt% migrates to the surface within 24–72 h and reduces thread engagement friction below the child-resistant torque requirement. Finished closure types include child-resistant closures for household cleaning chemicals, agrochemical bottle caps, automotive fluid bottle caps and dispensing closures for industrial cleaners.
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Braskem HDPE HDI0653U1 is a high-density polyethylene injection-moulding grade with a nominal melt flow rate of 6.0 g/10 min at 190 °C/2.16 kg and a nominal density of 0.953 g/cm³. The product is supplied in pellet form and is formulated for narrow molecular-weight distribution, intended to balance injection pressure requirements against solid-state stiffness in thin-wall and general-purpose rigid packaging. The material is classified as a general-purpose HDPE injection resin, not as a blow-moulding or film grade.
Table 1 lists the typical lot-average values that are used for incoming resin acceptance when certification is based on ISO methods. The values are not guaranteed specification limits; lot-specific certificates of analysis from Braskem remain the controlling documents.
| Property | Test method | Typical lot-average range |
|---|---|---|
| Melt flow rate | ISO 1133-1:2022 | 5.8–6.2 g/10 min |
| Density | ISO 1183-1:2019 | 0.951–0.955 g/cm³ |
| Tensile yield stress | ISO 527-2:2012 | 24–26 MPa |
| Tensile yield strain | ISO 527-2:2012 | 7–9 % |
| Flexural modulus | ISO 178:2019 | 1,000–1,100 MPa |
| Notched Izod impact, 23 °C | ISO 180/A:2019 | 2.5–3.0 kJ/m² |
| Vicat softening temperature, A50 | ISO 306:2022 | 122–126 °C |
The melt flow rate is the most sensitive incoming parameter because blending with off-spec low-MFR material shifts injection pressure and can produce short shots in high-cavitation tooling. Density at 0.953 g/cm³ controls stackability, top-load rigidity, and wall-thickness distribution in containers. Flexural modulus and Izod impact are evaluated together when the part is exposed to drop loading at low temperature, because an increase in stiffness alone does not predict impact survival.
Shot-to-shot variation on a 120-ton hydraulic injection-moulding machine with a 24:1 L/D general-purpose screw is most commonly observed at the cushion boundary. With HDI0653U1, a screw-back position of 3 mm to 6 mm and a decompression distance of 2 mm to 4 mm are typical. Back pressure in the range 0.5 MPa to 1.5 MPa is sufficient for melt homogeneity; above 2.0 MPa, shear heating can raise melt temperature by 8 °C to 12 °C and shift viscosity below the design value. Injection velocity should be profiled so that the flow-front velocity through gates larger than 1.2 mm does not exceed 250 mm/s; higher velocities cause jetting in thin-wall containers and surface splay from gas entrapment. Hold pressure is typically 60 % to 80 % of peak injection pressure, with hold time set to gate freeze. If gate freeze time is not confirmed by a short-shot weight plateau, parts can exhibit sink marks and elevated shrinkage.
Pre-drying is not required for HDPE under normal conditions; however, condensation on cold pellets stored below 10 °C and moved into a 25 °C moulding hall can introduce surface moisture. If surface moisture is visible or if splay occurs at melt temperatures below 200 °C, a hopper dryer at 60 °C for 2 h removes condensate without introducing oxidative yellowing. At storage relative humidity above 60 %, this hopper-dryer conditioning reduces surface-splay risk.
At melt temperatures above 250 °C or residence times beyond 5 min, the antioxidant package is consumed faster than the polymer chain-scission rate. The practical maximum barrel setting for HDI0653U1 is 230 °C at the nozzle, with rear zone 170 °C to 190 °C and front zone 200 °C to 220 °C. When mould temperatures are kept below 15 °C, solidification is rapid but crystallinity remains lower at the surface; this reduces notched Izod impact in thin sections and increases susceptibility to weld-line fracture. Mould temperatures above 40 °C extend cooling time but improve gate-region shrinkage uniformity.
Cycle time in a 2 mm wall part often lies between 8 s and 14 s, depending on part geometry and cooling-circuit configuration. Pressure drop through long hot-runner systems should be measured; with an 8 mm runner diameter and 40 mm/s screw speed, the pressure at the nozzle is typically 70 MPa to 90 MPa. If the measured nozzle pressure exceeds 100 MPa, the runner diameter or gate count should be reviewed rather than increasing melt temperature, because the latter accelerates molecular weight loss.
Environmental stress-cracking resistance of HDI0653U1 is lower than that of higher-molecular-weight blow-moulding grades. The lower chain entanglement density required for 6.0 g/10 min flow reduces ESCR; parts exposed to surfactants, ethanol-water mixtures, or lipophilic soils may crack at stress concentrations. If ESCR is acceptance-critical, the part should be tested according to ASTM D1693-15 under the intended chemical solution at 50 °C, not inferred from density alone. Published data for HDI0653U1 in ethanol-water mixtures is limited; validation on the finished article is required.
Warpage in thin-wall lids is governed by anisotropy. With an edge-gated rectangular lid of 1.5 mm thickness, orientation along the flow direction can generate shrinkage of 1.6 % to 2.1 % in the flow axis and 0.9 % to 1.3 % transverse. The resulting differential strain produces corner lift unless tool cooling is balanced within ±5 °C. Post-mould fixturing for 30 s to 60 s is used on high-speed closures to stabilise flatness, but it does not correct a fundamentally unbalanced gate or cooling configuration.
The most immediate contrast is with blow-moulding HDPE grades in the 0.3–1.0 g/10 min MFR range. Those grades provide higher ESCR and melt strength but require higher injection pressure and longer cycle times when used without tooling modifications. HDI0653U1 at 6.0 g/10 min reduces melt viscosity and allows thin-wall fill below 1 mm at moderate clamp force; however, the lower molecular weight reduces drop-impact resistance at 0 °C.
Compared with a higher-flow HDPE injection-moulding grade at approximately 20 g/10 min, HDI0653U1 gives lower injection speed and higher notched Izod impact, but it may not fill extremely long flow-length-to-thickness ratios above 250:1 without a second gate. The density difference also matters. At 0.953 g/cm³, the grade has slightly lower flexural modulus than a 0.961 g/cm³ HDPE injection grade, so top-load applications requiring higher stiffness per unit mass may require ribbing or a higher-density grade. The grade is therefore specified for parts where balanced flow and impact resistance are primary, while higher-density high-MFR grades are selected for absolute stiffness and faster cycles.
Braskem HDPE HDI0653U1 is not formulated with heavy metals, brominated flame retardants, or intentionally added perfluorinated substances. Regulatory screening should nevertheless be performed on the finished article, because polymerisation catalysts, processing aids, or colour masterbatches can affect the final compliance status.
| Compliance area | Reference / method | Condition or limitation |
|---|---|---|
| US food contact | FDA 21 CFR 177.1520(c) | Olefin polymer; finished-article migration testing required |
| EU food contact | (EU) No 10/2011 | Migration kinetics in polymer matrices depend on wall thickness, crystallinity, and processing temperature |
| Packaging heavy metals | 94/62/EC | Sum of Pb, Cd, Hg, and Cr(VI) ≤ 100 mg/kg |
| RoHS | 2011/65/EU | No brominated flame retardants intentionally added |
| REACH | 1907/2006 | Polymer substance; SVHC declaration per lot from supplier |
The grade should not be specified for continuous contact with strong oxidising agents, aromatic hydrocarbons, or chlorinated solvents at elevated temperature. If outdoor weathering is required, long-term performance should be confirmed against ISO 4892-2 or ISO 4892-3 data on the specific part thickness; if the application exceeds the stabiliser package, additional UV masterbatch may be required. Avoid combination with transition-metal stearates at high loadings because these additives can destabilise the polymer during long residence times.