| HS Code | 204260 |
| Melt Flow Rate 190 C 2 16 Kg | 11 g/10 min |
| Density | 0.954 g/cm³ |
| Tensile Strength At Yield | 29 MPa |
| Tensile Elongation At Break | 1000% |
| Flexural Modulus | 1200 MPa |
| Vicat Softening Point | 127°C |
| Heat Deflection Temperature 0 45 Mpa | 75°C |
| Hardness Shore D | 65 |
| Melting Point | 133°C |
| Environmental Stress Cracking Resistance Escr | 10 h |
As an accredited TPI Polene HDPE HJ1100 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | TPI Polene HDPE HJ1100 supplied in 25 kg polyethylene-lined woven bags, stacked on pallets; each pallet contains 40 bags. |
| Container Loading (20′ FCL) | TPI Polene HDPE HJ1100 loaded in 20′ FCL: 25 kg bags, palletized, stretch-wrapped, evenly stacked, secured for ocean shipment. |
| Shipping | TPI Polene HDPE HJ1100 ships as non-hazardous polyethylene pellets, usually in 25 kg bags or 1 MT jumbo bags, palletized and stretch-wrapped inside 20'/40' containers. Store in a cool, dry, ventilated area away from direct sunlight, heat, and moisture. No special transport classification. |
| Storage | Store TPI Polene HDPE HJ1100 in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, ignition sources, and moisture. Keep in original sealed packaging on pallets, off the floor. Avoid contamination from oils, chemicals, or dust. Do not exceed safe stacking heights; handle carefully to prevent bag damage. Maintain moderate temperatures and avoid prolonged UV exposure. |
| Shelf Life | Typically 24 months when stored in original packaging under cool, dry, ventilated conditions, away from direct sunlight and moisture. |
At 11.0 g/10 min melt flow rate determined under ISO 1133-1:2022 and 0.957 g/cm³ density under ISO 1183-1:2019, HDPE HJ1100 is processed as the continuous virgin polyolefin phase for thin-wall injection-molded dairy tubs, delicatessen containers, and snap-on lids. The dry-blend is prepared from 97.0–98.5 wt% virgin HJ1100, 1.0–2.0 wt% white or custom color masterbatch, and 0.5–1.0 wt% slip/antiblock concentrate based on erucamide or oleamide; organic slip addition above 2.0 wt% is avoided because notched impact retention declines below 90% of neat resin values when measured under ISO 179-1/1eA at 23°C. Food-contact compliance is evaluated under FDA 21 CFR 177.1520 for olefin polymers, EU Regulation No 10/2011 overall migration limit of 10 mg/dm² or 60 mg/kg food simulant, and GMP Regulation (EC) No 2023/2006 process hygiene; final article suitability depends on surface-to-volume ratio and food simulant selection for each cavity geometry. Injection processing on high-cavitation hot-runner systems uses melt temperatures of 200–230°C, mold water 10–30°C, injection velocity 120–250 mm/s, holding pressure 500–900 bar, and projected-area clamp demand of 3.5–5.5 kN/cm²; screw L/D is specified at 20:1–25:1 to limit shear heating and melt-temperature overshoot. Terminal finished products include 250–1,000 mL tubs for dairy desserts, margarine, ice cream, deli salads, ready-to-eat portions, and corresponding snap-on lids with tamper-evident rims.
Stackable dairy crates, bread trays, and retail tote boxes impose a flatness requirement that is most sensitive to differential shrinkage across rib-to-wall junctions. In returnable dairy crate conversion, HJ1100 is blended as 60–80 wt% virgin resin with 20–40 wt% closed-loop regrind, 1.0–2.0 wt% black masterbatch, and 0.3–0.5 wt% hindered amine light stabilizer when outdoor storage is part of the distribution cycle; regrind above 40 wt% has been observed on production-scale equipment to reduce flexural modulus by 5–8% and to shorten repeated drop-loading life at -10°C. Mechanical validation uses ISO 178:2019 three-point flexure, ASTM D638-22 tensile yield, ASTM D1693-15 environmental stress-crack resistance, and ISO 8611-1:2011 load-bearing procedures for distribution units; direct food contact in dairy crates is assessed under FDA 21 CFR 177.1520. Low-pressure structural-foam or compact injection molding is performed at melt temperature 210–235°C, mold cooling 15–35°C, holding pressure 600–1,000 bar, and total cycle 35–60 s; flatness control on multi-gate tools requires delayed valve-gate opening and post-mold cooling fixtures because rib-to-wall thickness ratios from 0.6:1.0 to 0.8:1.0 create a concave bow at the gate-freeze boundary. Terminal parts include 20–24 bottle dairy crates, 600×400 mm bread trays, 1,200×1,000 mm distribution totes, and returnable beverage crate shells for 0.33 L and 0.50 L units.
| Formulation | Flexural modulus ISO 178:2019 | ESCR ASTM D1693-15 | Notched Izod ISO 180/A |
|---|---|---|---|
| 100 wt% virgin HJ1100 | 1,100 MPa | >20 h reported for general HDPE injection grades | 4.5 kJ/m² |
| 80/20 virgin/regrind | 1,050–1,080 MPa | 16–19 h retention envelope | 4.3 kJ/m² |
| 60/40 virgin/regrind | 995–1,030 MPa | 12–15 h retention envelope | 4.0 kJ/m² |
Published data for HJ1100 at the exact regrind fractions above is limited; the table consolidates retention envelopes from commercial high-flow HDPE crate molding practice and should be verified on production tooling with the specific regrind source.
Because closure threads and tamper-evident bridges are filled under high-cavitation hot-runner pressure, gate freeze time imposes a lower bound on injection velocity in HJ1100 closure conversion. Food-contact and potable-water closure systems use FDA 21 CFR 177.1520, EU Regulation No 10/2011, NSF/ANSI/CAN 61, and ISO 8317:2015 child-resistant package test methods when specified by brand protocols. The let-down is typically 97.5–99.0 wt% neat HJ1100, 0.5–1.5 wt% white masterbatch, 500–1,200 ppm erucamide slip, and 0.1–0.3 wt% acid-neutralized antioxidant carrier; no ethylene-vinyl alcohol oxygen-barrier masterbatch is used in single-wall closure stock intended for non-carbonated products. Melt temperature is held at 210–240°C, mold temperature 10–25°C, injection velocity 150–300 mm/s, holding pressure 500–900 bar, and cycle time 6–10 s on 32–96 cavity hot-runner tools. Gate diameter is maintained at 0.6–1.0 mm to control gate freeze without excessive shear heating; post-mold cooling on rotary platen plates reduces cap-skirt ovality to ≤0.30 mm at a 28 mm finish. Finished products include tamper-evident screw caps, flip-top dispensing caps, dairy bottle closures, detergent bottle closures, and 28–63 mm neck finishes for still water and household chemical packaging.
For 5–25 L open-head pails, the decisive qualification test is cold-drop impact at -20°C, run on production containers rather than on tensile bars, because gate area and rim thickness control real-world failure initiation. Formulations for food-grade pails are based on 96–98 wt% virgin HJ1100, 2–4 wt% white masterbatch, and 0.2–0.5 wt% processing stabilizer; for non-food industrial pails, the masterbatch may be replaced by 1–2 wt% black masterbatch and 0.3–0.5 wt% UV stabilization without food-contact additive restrictions. Dangerous-goods pails are certified as removable-head plastics packagings under UN 1H2 for packing groups II and III, with drop height and stack-load validation per UN Model Regulations, while food-grade pails require compliance with FDA 21 CFR 177.1520 and EU Regulation No 10/2011. Injection is run at melt temperature 200–230°C, mold temperature 15–35°C, injection pressure 700–1,000 bar, holding time 10–18 s, and total cycle 25–40 s for pails with wall thickness 1.8–2.8 mm; hot-runner valve gating is used to balance flow to the rim, and in-mold labeling is synchronized with the injection cycle to prevent label displacement at the gate zone. Terminal articles include 5 L, 10 L, 15 L, 20 L, and 25 L open-head pails with tamper-evident lids for waterborne coatings, adhesives, edible oils, construction chemicals, and food concentrates.
Thick-section houseware tooling often runs with gas-counterpressure assist when wall thickness exceeds 2.5 mm, because sink marks and top-load deformation are the primary reject modes. HJ1100 is let down with 1.0–2.5 wt% masterbatch and 0.3–0.8 wt% pigment when opaque molded-in color is specified; flame-retardant systems are not recommended unless full mechanical property revalidation is performed under IEC 60695-2-11. Toy-adjacent children's articles require compliance with EN 71-3:2019+A1:2021 migration limits, ASTM F963-23 mechanical and chemical requirements, and REACH Annex XVII phthalate restrictions. Melt temperature is held at 190–220°C, mold temperature 15–40°C, screw L/D 20:1–24:1, and cooling time is extended proportionally to section thickness. Finished parts include stackable storage boxes, laundry baskets, pedal-bin bodies, drawer organizers, and waste containers.
For returnable pallets molded with post-industrial HDPE regrind, the melt pool must remain homogeneous at regrind fractions up to 50 wt%; otherwise low-temperature foot impact fails at the weld-line boundary formed at the center stringer. Formulation for structural-foam pallets uses 50–70 wt% virgin HJ1100, 30–50 wt% closed-loop post-industrial HDPE agglomerate, 0.5–1.5 wt% endothermic chemical foaming agent, and 0.3–0.5 wt% process stabilizer; regrind melt-flow variability greater than ±2.0 g/10 min from the virgin stream reduces skin density and should be rejected at intake. Performance validation follows ISO 8611-1:2011 for flat pallets, with bending stiffness, racking resistance, and corner drop; fire performance may be assessed under NFPA 13 commodity classification when required by warehouse insurers. Low-pressure injection foaming is performed at melt temperature 200–225°C, mold cooling 20–40°C, injection speed 60–120 mm/s, gas counterpressure 5–15 bar, and screw L/D 24:1–30:1; resulting skin density is 0.92–0.95 g/cm³ with core void cell size 0.1–0.5 mm. Terminal articles include returnable export pallets, half pallets, retail display pallets, and freezer-compatible distribution pallets.
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