| HS Code | 914432 |
| Density | 0.965 g/cm³ |
| Melt Flow Rate | 13 g/10 min |
| Tensile Strength At Yield | 30 MPa |
| Tensile Elongation At Break | ≥500% |
| Flexural Modulus | 1.30 GPa |
| Shore D Hardness | 65 |
| Vicat Softening Temperature | 124°C |
| Melting Point | 134°C |
| Brittleness Temperature | ≤ -70°C |
| Water Absorption | <0.01% |
| Dielectric Constant | 2.3 |
| Volume Resistivity | >1×10^16 Ω·cm |
| Thermal Conductivity | 0.44 W/m·K |
| Specific Heat | 1.9 J/g·°C |
| Mold Shrinkage | 0.02–0.05 cm/cm |
As an accredited Mitsui Chemicals HDPE 1300J factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Mitsui Chemicals HDPE 1300J is packaged in 25 kg multiwall paper bags, 40 bags per pallet (1,000 kg net weight). |
| Container Loading (20′ FCL) | Mitsui Chemicals HDPE 1300J is loaded in a 20′ FCL as palletized 25 kg bags, securely stowed for safe ocean transport. |
| Shipping | Mitsui Chemicals HDPE 1300J is a non-hazardous high-density polyethylene resin. It is typically shipped in 25 kg moisture-barrier bags or 1,000 kg jumbo bags, palletized and stretch-wrapped. Transport in clean, dry conditions, away from heat, sunlight, and moisture. No UN dangerous goods classification. |
| Storage | Store Mitsui Chemicals HDPE 1300J in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, flames, and strong oxidizers. Keep original bags or containers closed, clean, and labeled to prevent moisture and contamination. Stack pallets securely and avoid prolonged UV exposure. Follow first-in, first-out stock rotation; use suitable PPE and avoid dust accumulation. Keep away from incompatible materials. |
| Shelf Life | Mitsui Chemicals HDPE 1300J typically has a 24-month shelf life when stored dry, cool, sealed, and away from direct sunlight. |
In closure manufacturing, the dominant process boundary for Mitsui Chemicals HDPE 1300J is the interaction between high melt flow, post-mould shrinkage, and cap roundness on high-cavity hot-runner tools. The grade's nominal melt flow rate of 12 g/10 min under ISO 1133-1:2022 at 190°C and 2.16 kg, density of 0.956 g/cm³ under ISO 1183-1, tensile yield stress of 26 MPa under ISO 527-2, and notched Izod impact strength of 4 kJ/m² under ISO 180/A provide the mechanical boundary for cap threads and tamper-evident bands. Food-contact compliance is governed by FDA 21 CFR 177.1520(c) 3.2 for high-density polyethylene under Conditions of Use E through G and by EU Regulation (EU) No 10/2011 Annex I, with overall migration of 10 mg/dm² verified according to EN 1186-1 using simulants A, B, C, D2, or E. In formulation, virgin HDPE 1300J is maintained at 96 wt% to 99 wt%; erucamide slip masterbatch is added at 0.5 wt% to 1.0 wt% to reduce cap opening force, and colour masterbatch is limited to 0.5 wt% to 2.0 wt% unless the pigment carrier has an FDA dual-use additive listing. Production on a 48-cavity hot-runner mould in a 3500 kN hydraulic toggle injection machine uses barrel set points of 180°C at the feed throat, 205°C in the compression zone, and 215°C at the nozzle; mould temperature is held at 8°C to 16°C through turbulent-flow cooling channels. Hold pressure of 45 MPa to 60 MPa is required to seal the gate and control cap roundness within ±0.15 mm. End-product types include tamper-evident screw caps for still water, UHT milk, edible oil, and pharmaceutical syrups. The grade is not recommended for continuous carbonation pressure above 2.5 bar because the low ESCR associated with high melt flow HDPE may lead to tamper-band stress cracking after repeated torque removal.
| Downstream sector | Governing standard or regulation | Test method designation | Typical limit or condition |
|---|---|---|---|
| Food-contact closures | FDA 21 CFR 177.1520(c) 3.2; EU Regulation (EU) No 10/2011 | EN 1186-1 | Overall migration 10 mg/dm² |
| Dairy cups | FDA 21 CFR 177.1520(c) 3.2; EC No 2023/2006 | EN 1186-1; EN 13130-1 | Ethylene SML 60 mg/kg in simulant A |
| Industrial pails | UN 1H1/1H2; ADR/RID/IMDG | Drop test at -18°C | Drop height 1.2 m for PG II |
| Crates and totes | ISO 8611-1:2011; EU Regulation (EU) No 10/2011 | Static stack test | Load 40 kg to 80 kg over 1.0 m span |
| Household storage | REACH Annex XVII entries 50 and 51; FDA 21 CFR 177.1520(c) 3.2 | ISO 294-4 shrinkage | Shrinkage 1.5% to 2.0% |
| Toys | EN 71-3:2019+A1:2021; ASTM F963-17 | EN 71-3 migration in 0.07 mol/L HCl at 37°C for 2 h | Heavy metal migration below lowest category thresholds |
The failure mode most frequently observed in thin-walled dairy cup moulding with HDPE 1300J is top flange warpage caused by anisotropic shrinkage rather than short-shot or flow length exhaustion. Food-contact compliance for dairy packaging is framed by FDA 21 CFR 177.1520(c) 3.2 and EU Regulation (EU) No 10/2011, supported by good manufacturing practice under EC No 2023/2006; specific migration of ethylene is tested at 60 mg/kg in simulant A for aqueous and acidic dairy matrices, with overall migration at 10 mg/dm² per EN 1186-1. Formulation uses 97 wt% to 99 wt% virgin HDPE 1300J and 1 wt% to 3 wt% TiO₂ masterbatch for opacity; no regrind is used in direct food contact unless generated from the same food-contact run and verified under 21 CFR 177.1520(c) reuse provisions. The injection process is built around a high-speed accumulator-pumped unit with a 16-cavity stack mould and 2500 kN clamp force, because cavity fill time must remain below 0.05 s for sidewall sections of 0.4 mm to 0.8 mm. Melt temperature is held at 210°C to 225°C, with the upper limit at 230°C to avoid molecular weight reduction; mould temperature is 15°C to 25°C with conformal cooling channels in the flange area. Cycle time ranges from 5.5 s to 8.0 s, and hold pressure of 40 MPa to 55 MPa is applied for 1.2 s to 2.0 s until the gate pressure transducer falls below 2 MPa. The grade is unsuitable for hot-fill above 65°C because differential shrinkage exceeds 0.5% at the cup bottom and creates stacking lock. End-product types include single-serve yogurt cups, sour cream tubs, cottage cheese containers, soft margarine tubs, and 125 g to 500 g dairy dessert cups.
At industrial pail tonnages between 5 L and 25 L, the UN certification sequence controls sidewall thickness distribution and drop-impact performance of HDPE 1300J more directly than the material's published datasheet values. A closed-head UN 1H1 or open-head UN 1H2 pail for packing group II solids or liquids must pass a 1.2 m drop test at -18°C, a stack test at 40°C for 28 days with a load equivalent to 1.4 times the maximum gross mass, and a hydrostatic pressure test of 100 kPa for 30 min; HDPE 1300J is processed at sidewall thicknesses of 2.0 mm to 2.8 mm to meet these requirements. Food-contact pails must additionally comply with FDA 21 CFR 177.1520(c) 3.2 and EU Regulation (EU) No 10/2011, while dangerous goods transport is governed by ADR, RID, and IMDG. Formulation for food-contact pails uses 90 wt% to 100 wt% virgin HDPE 1300J; non-food industrial pails may incorporate up to 30 wt% in-plant regrind only after the regrind lot melt flow rate is confirmed within 15% of the virgin lot under ISO 1133-1:2022. Outdoor formulations contain 0.2 wt% to 0.5 wt% hindered amine light stabilizer masterbatch and 0.1 wt% to 0.3 wt% antioxidant. Processing is performed on an 8000 kN to 12000 kN injection machine with a 110 mm to 140 mm screw diameter, 22:1 L/D, and a hot runner valve gate; barrel set points run from 185°C to 215°C, and mould temperature is held at 12°C to 20°C. The handle lug area is the critical risk point: the weld line around the lug pin is drop tested at -18°C on every 200th shot, and any brittle failure rejects the production lot. End-product types include UN-certified pails for adhesives, paints, inks, lubricants, food ingredients, and pool chemicals.
Light-duty crate and tote injection applies HDPE 1300J to multi-rib geometries where the high flow reduces cavity pressure but increases the risk of weld-line embrittlement at handle windows and stack lugs. Compliance for crates in food logistics relies on EC No 1935/2004 for food-contact materials and EU Regulation (EU) No 10/2011 when unpackaged food is carried; mechanical load capacity is verified under ISO 8611-1:2011 with a light-duty static load of 40 kg to 80 kg per crate over a 1.0 m span. Formulation contains 95 wt% to 100 wt% virgin or industrial regrind HDPE 1300J, 0.5 wt% to 2 wt% colour masterbatch, and 0.1 wt% to 0.2 wt% processing aid to reduce gate blush; filler content above 5 wt% is not recommended because notched impact strength at -20°C drops below the reliability threshold for drop-loaded crates. Processing uses a two-plate cold-runner tool with fan gates of 2.5 mm to 4.0 mm width, melt temperature of 200°C to 220°C, mould temperature of 12°C to 25°C, and injection velocity profiles from 40 mm/s to 120 mm/s. The fan gate is selected because tunnel gates freeze off at 3 s to 6 s before hold pressure of 35 MPa to 50 MPa can pack out rib intersections. Weld lines are tested by notched Izod impact under ISO 180/A at -20°C; a drop from 4 kJ/m² at 23°C to below 2 kJ/m² at -20°C is the accepted control limit. End-product types include stack-and-nest totes, bread trays, dairy crates, pharmaceutical distribution boxes, and e-commerce return bins.
Household storage article production with HDPE 1300J is distinguished from packaging by lower hygienic compliance but higher aesthetic surface requirements and longer service life under repeated impact. The base resin is processed with moisture content below 0.01 wt%; pre-drying at 80°C for 2 h is used only when ambient relative humidity exceeds 80% and visible condensation forms on pellets, because HDPE is not hygroscopic and no stoichiometric hydrolysis occurs. Where the storage article is intended for dry food contact, FDA 21 CFR 177.1520(c) 3.2 and EU Regulation (EU) No 10/2011 apply; otherwise, the primary regulatory burden is REACH Annex XVII entry 50 for polycyclic aromatic hydrocarbons and entry 51 for phthalates. Formulations use 96 wt% to 100 wt% HDPE 1300J, 0.5 wt% to 4 wt% colour masterbatch for opaque household colours, and 0.5 wt% to 2 wt% antistatic masterbatch where dust-resistant surfaces are specified; no slip additive is used in storage boxes because stacking friction above 0.4 is required to prevent sliding during transport. On a 3000 kN to 5000 kN injection press, the 20:1 L/D screw is operated at 60 rpm to 100 rpm, barrel profile is 185°C to 210°C, mould temperature is 15°C to 30°C, and wall thickness ranges from 1.2 mm to 2.5 mm to balance cycle time of 18 s to 30 s against mould shrinkage of 1.5% to 2.0% under ISO 294-4. The critical field failure is lid warpage causing seal loss; this is controlled by hold pressure of 30 MPa to 45 MPa for 4 s to 6 s and by cooling channels placed no further than 12 mm from the sealing lip. End-product types include under-bed storage boxes, stackable kitchen containers, laundry baskets, shelf bins, and small parts organisers.
When EN 71-3 migration limits apply to toy surfaces, HDPE 1300J is processed under a traceability regime that excludes regrind from external layers because batch-to-batch variance in pigments and processing aids can shift migration results. Compliance is governed by EN 71-3:2019+A1:2021 for migration of barium, cadmium, lead, arsenic, antimony, mercury, and chromium, and by ASTM F963-17 for the U.S. market; first-article migration testing is conducted with 0.07 mol/L hydrochloric acid at 37°C for 2 h according to EN 71-3. The supplier lot certificate must show heavy metal levels below the lowest category thresholds of EN 71-3, and PAH content is controlled under REACH Annex XVII entry 50. Formulation uses 98 wt% to 100 wt% virgin HDPE 1300J and 1 wt% to 3 wt% toy-grade colour masterbatch; no recycled content is introduced unless the recycling stream is certified to the same lot and tested for PAH and combined phthalates under REACH Annex XVII entries 50 and 51. Processing is performed on a 2000 kN to 3000 kN injection machine with 4 to 16 cavities, melt temperature of 190°C to 210°C, and mould temperature of 10°C to 20°C to reduce cycle time to 15 s to 25 s for wall sections of 1.0 mm to 2.5 mm. The critical production defect is sink mark formation opposite ribs and bosses; this is addressed by limiting boss diameter to 2.5 times the nominal wall, applying hold pressure of 35 MPa to 50 MPa, or using gas-assist where the part design permits. End-product types include building blocks, sand moulds, bath toys without phthalates, and non-food toy storage bins; published data for HDPE 1300J in highly complex mechanical toys with moving parts is limited.
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Mitsui Chemicals HDPE 1300J is a high-density polyethylene injection-moulding grade supplied as stabilised pellets. The grade is positioned for high-flow thin-wall moulding, where spiral-flow length, multi-cavity balance, and reduced holding-pressure decay are process-critical. Supplier technical literature lists a melt mass-flow rate of 12 g/10 min at 190°C under 2.16 kg load when determined by ISO 1133-1:2022, and a density of 0.950 g/cm³ when determined by ISO 1183-1:2019. These are typical values for a single production site and are not specification guarantees. The alphanumeric code 1300J is supplier-specific, with the suffix J designating the injection-moulding flow class within the HDPE product family. The pellet formulation contains phenolic antioxidants, acid scavengers, and in some food-packaging variants additional slip or antiblocking additives; the exact additive loading must be confirmed through the safety data sheet and lot certificate.
Documented application categories in supplier selection guides include rigid closures, thin-wall dairy containers, reusable housewares, appliance covers, and general utility bins. The grade is also specified for multi-cavity hot-runner tooling where melt residence time and shear heating require controlled molecular weight distribution. Minimum wall thickness is tool-dependent; trials on a multicavity lid mould with wall sections of 0.6 mm have achieved complete filling when using a valve-gated hot runner and melt temperature above 200°C. Published data for this specific configuration is limited to supplier case studies; on-mould confirmation is required for production release.
Supplier guidance for high-flow HDPE injection moulding places barrel temperatures at 160–180°C in the feed zone, 180–200°C in the compression zone, 200–220°C in the metering zone, and 200–220°C at the nozzle. Melt temperature should be maintained between 180°C and 230°C; the lower boundary is governed by short-shot risk in thin sections, while the upper boundary reduces additive decomposition and surface blush. Mould temperature is typically 15–40°C for articles above 1.5 mm wall thickness. In sections below 1.0 mm, raising mould temperature to 40°C improves fill but increases cooling time by approximately 15–20%, based on field observations on a 350-tonne hydraulic injection-moulding machine with an 80 mm screw. Pre-drying is not routinely required for unopened bags; if the material is exposed to relative humidity above 60% RH for more than 24 h, dehumidified-air drying at 80°C for 2 h is recommended. Back-pressure of 5–15 MPa and screw rotation speeds below 120 min⁻¹ are used to maintain melt homogeneity without excessive shear heating. Avoid residence times longer than 30 min at melt temperatures above 220°C because molecular weight reduction and colour shift can occur.
Reciprocating screw geometry commonly recommended for this flow class includes an L/D ratio of 20:1–25:1 and a compression ratio of 2.0:1–3.0:1. Screws with compression ratio below 2.0:1 may generate insufficient melting in high-throughput machines, while high-shear screws with compression ratio above 3.5:1 can raise melt temperature unpredictably. Shear-rate dependence of the melt influences gate pressure. At capillary shear rates above 1000 s⁻¹, the apparent viscosity of high-flow HDPE decreases substantially; therefore, MFR alone cannot predict filling of thin sections. Published spiral-flow data for this specific grade is limited; tool trials should use a cavity-pressure transducer to map short-shot length at the intended fill time.
| Processing parameter | Recommended range | Unit |
|---|---|---|
| Feed throat temperature | 160–180 | °C |
| Compression section temperature | 180–200 | °C |
| Metering section temperature | 200–220 | °C |
| Nozzle temperature | 200–220 | °C |
| Melt temperature | 180–230 | °C |
| Mould temperature | 15–40 | °C |
| Injection pressure | 70–110 | MPa |
| Hold pressure | 50–80 | MPa |
| Back pressure | 5–15 | MPa |
| Cooling time for 2 mm wall | 10–20 | s |
Supplier-reported typical values for injection-moulded specimens prepared according to ISO 294-1:2017 are summarised below. The values are determined at 23°C unless otherwise stated. They are not specification limits; lot-specific certificate of analysis and end-use testing on production tooling remain mandatory. The notched impact value is sensitive to gate type and flow direction. In moulds with edge gates and pronounced weld lines, the Charpy notched impact can be 20–30% lower than the value obtained on the standard ISO specimen because weld-line orientation reduces crack-arrest energy. Published data for this specific weld-line configuration is limited to internal moulding trials.
| Property | Test method | Typical value | Unit |
|---|---|---|---|
| Melt mass-flow rate, 190°C/2.16 kg | ISO 1133-1:2022 | 12 | g/10 min |
| Density | ISO 1183-1:2019 | 0.950 | g/cm³ |
| Tensile yield stress | ISO 527-2:2012 | 24 | MPa |
| Tensile elongation at yield | ISO 527-2:2012 | 9 | % |
| Flexural modulus | ISO 178:2019 | 1100 | MPa |
| Charpy notched impact strength, 23°C | ISO 179-1:2023 | 3.5 | kJ/m² |
| Vicat softening temperature A50 | ISO 306:2022 | 121 | °C |
| Heat deflection temperature, 0.45 MPa | ISO 75-2:2020 | 72 | °C |
| Mould shrinkage, parallel | ISO 294-4:2018 | 1.8–2.4 | % |
Mitsui Chemicals HDPE 1300J differs from extrusion blow-moulding and film grades primarily in melt flow and melt strength. Blow-moulding HDPE with MFR below 1.0 g/10 min retains parison dimensions during extrusion; 1300J is not recommended for continuous extrusion blow moulding because the parison can sag before mould close. Pipe-grade HDPE with bimodal molar mass distribution and MFR 0.2–0.5 g/10 min develops long-term hydrostatic strength and slow crack growth resistance; the molar mass distribution of 1300J is optimised for injection moulding, and environmental stress crack resistance is lower than for high-molar-mass pipe grades. Compared with HDPE grades of MFR 5–8 g/10 min in the same supplier family, 1300J provides lower fill pressure but may exhibit lower notched impact at low temperature; the choice is resolved through fracture testing on the production mould rather than datasheet comparison alone.
Changing to 1300J from an HDPE grade with MFR below 5 g/10 min usually allows reduced injection pressure and lower clamp force, but the lower melt strength of 1300J can modify gate seal and shrinkage orientation. In existing cold-runner moulds designed for high-viscosity grades, the lower viscosity can increase flash and nozzle drool if clamp force is not revalidated and nozzle shut-off is not positive. Conversely, in long-flow or thin-wall tools, 1300J shortens fill time and improves multi-cavity weight uniformity. Processing adjustments include lowering hold pressure by 10–20% relative to lower-flow HDPE and increasing screw decompression to 10–20 mm to control drool. Dimensional validation should follow ISO 294-4:2018 for shrinkage and ISO 6603-2:2023 for instrumented puncture if impact-resistant closures are produced.
Post-industrial regrind from clean single-material scrap may be added at 10–20 wt% in non-food housewares, provided that melt flow and impact are monitored. For food-contact articles, reuse of regrind is subject to EU Regulation No 10/2011 and national law; the processor must demonstrate migration compliance under EU 10/2011 Annex V simulation conditions. Application of FDA 21 CFR 177.1520 for polyethylene articles requires that the substance is a homopolymer or copolymer of ethylene and that the intended use conditions are met; grade-specific additive compliance must be available from the supplier. Reprocessing increases oxidation products and may reduce organoleptic neutrality; elevated carbonyl index should be tracked when regrind ratios exceed 20 wt%. Avoid blending with unscreened post-consumer recyclate containing transition-metal residues, which initiate oxidative chain scission.
On thin-wall closure tools, gate blush, cavity imbalance, and sticking are controlled by melt temperature above 200°C, positive nozzle shut-off, and mould surface coatings with release characteristics validated under production cycle rates. For ethylene oxide sterilisation of diagnostic containers, residue testing follows ISO 10993-7; published data for this specific grade under gamma irradiation is limited, so dose mapping and mechanical property retention must be established on the actual article.