| HS Code | 295781 |
| Density | 0.953 g/cm³ |
| Melt Index | 10 g/10 min at 190°C/2.16 kg |
| Tensile Strength At Yield | 31 MPa |
| Tensile Strength At Break | 30 MPa |
| Elongation At Break | >100% |
| Flexural Modulus | 1,300 MPa |
| Vicat Softening Temperature | 127°C |
| Heat Deflection Temperature | 90°C at 0.45 MPa |
| Shore D Hardness | 66 |
| Notched Izod Impact Strength | 80 J/m |
| Environmental Stress Crack Resistance | >1000 h |
| Water Absorption | <0.01% |
| Coefficient Of Linear Thermal Expansion | 1.5×10⁻⁴ /°C |
| Thermal Conductivity | 0.35 W/m·K |
| Specific Heat Capacity | 1.9 kJ/kg·K |
As an accredited Dow HDPE IP-10 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Dow HDPE IP-10 comes in 25 kg moisture-resistant bags, palletized and shrink-wrapped for secure industrial transport and storage. |
| Container Loading (20′ FCL) | 20′ FCL container loaded with Dow HDPE IP-10 high-density polyethylene resin in 25 kg bags, palletized, shrink-wrapped, and securely stowed. |
| Shipping | Dow HDPE IP-10 is a non-hazardous high-density polyethylene resin, typically shipped as pellets in 25-kg bags, bulk bags, or bulk truck/rail containers. It is not transport-regulated. Store dry and clean, away from heat, moisture, and contaminants, using standard industrial handling practices. |
| Storage | Store Dow HDPE IP-10 in a cool, dry, well-ventilated warehouse away from direct sunlight, heat, flames, and strong oxidizers. Keep original bags or containers closed, palletized, and off the floor to avoid moisture and contamination. Maintain ambient temperatures, limit prolonged UV exposure, and use good housekeeping to minimize dust. Follow local regulations and the manufacturer’s SDS. |
| Shelf Life | Dow HDPE IP-10 shelf life is typically indefinite when stored sealed in a cool, dry, well-ventilated area, away from direct sunlight and contaminants. |
Dow HDPE IP-10 is a narrow-molecular-weight-distribution injection molding grade with a nominal melt flow rate of 9.0 g/10 min at 190 °C/2.16 kg per ISO 1133-1:2022 and a nominal density of 0.953 g/cm³ per ISO 1183-1:2019. In high-output thin-wall food container molding, the material is processed on accumulator-assisted hydraulic injection machines with clamp force from 250 t to 350 t. The plasticating unit uses a general-purpose polyolefin screw with an L/D ratio of 20:1 to 25:1 and a compression ratio from 2.5:1 to 3.5:1. Melt temperature is maintained at 200 °C to 220 °C, mold temperature at 15 °C to 30 °C, and hot runner manifold temperature at 215 °C to 225 °C. High-speed filling with injection velocity from 250 mm/s to 350 mm/s is used to exploit shear thinning at apparent shear rates above 1,000 s-1; flow length to wall thickness ratios up to 250:1 are attainable in sidewalls of 0.8 mm to 1.2 mm when sequential valve gates respond within 20 ms. Hold pressure is set from 450 bar to 650 bar, and back pressure is kept at 5 bar to 10 bar to avoid shear over-heating. For direct food contact, only virgin pellet feed is normally used; post-industrial regrind from the same converting line may be introduced up to 10 wt% without a new compliance assessment, provided the regrind is dry and free of cross-polymer contamination. Because HDPE IP-10 is not hygroscopic, pre-drying is not required unless bulk handling exposes pellets to condensation; if surface moisture is visible, a dehumidifying dryer at 70 °C to 80 °C for 1 h to 2 h is applied. Resin moisture content is verified below 0.01% by weight before processing. Shot-to-shot fill time variation is held within ±0.02 s to keep part weight stability below ±0.3%. Color masterbatch let-down is 2 wt% to 3 wt%, using only pigment systems listed in EU 10/2011 positive lists. Terminal products include dairy cups with 0.8 mm sidewall thickness, margarine tubs, delicatessen containers, and stackable food service trays with top-load values above 350 N after 24 h at 4 °C.
| Regulation/standard | Designator | Condition or limit |
|---|---|---|
| US FDA indirect food additive | 21 CFR 177.1520(c) 3.1a | Olefin polymer clearance for food contact; article must be used within end-use temperature and food-type limitations of the clearance |
| EU food contact plastics | EU 10/2011 | Overall migration limit 10 mg/dm² for general food contact; 60 mg/kg for infant food contact |
| REACH SVHC declaration | Article 33 | Article-level declaration required above 0.1 wt% SVHC |
| CONEG toxics in packaging | ICP heavy metal screen | Sum of Pb, Cd, Hg, Cr(VI) below 100 mg/kg per packaging component |
For non-carbonated water and dairy closures, the decisive property is not only spiral flow length but also part ejection stiffness after solidification. Dow HDPE IP-10 is used in valve-gated hot runner molds with 48 to 96 cavities; hot runner tip temperature is controlled within ±5 °C of the melt set point to avoid premature gate freeze-off or stringing. Closure skirt wall thickness is 0.8 mm to 1.2 mm, tamper-evident band bridge width 0.3 mm to 0.5 mm, and thread root radius not less than 0.2 mm. Injection fill time is 0.15 s to 0.35 s, with transfer to hold phase at 95% of filled volume using injection pressure 700 bar to 900 bar. Hold pressure is set at 450 bar to 550 bar with 0.5 s hold time; final cushion is kept at 3 mm to 5 mm. Mold temperature is 12 °C to 20 °C to accelerate solidification, and total cycle time for a 2.0 g water closure is 6 s to 9 s. Formulation uses a polyolefin-based color masterbatch at 2 wt% to 4 wt%; when low removal torque is required, an erucamide-containing slip masterbatch is added at 0.5 wt% to 1.0 wt%, and cap removal torque is characterized on a torque tester at 5 rpm according to the closure manufacturer’s internal specification. Compliance for food closures is evaluated under FDA 21 CFR 177.1520(c) 3.1a and EU 10/2011; if the closure includes a liner, the liner material is separately assessed. Products include 30/25 mm mineral water closures, 38 mm dairy screw caps, and 28 mm edible oil closures. Published data for carbonated beverage closure retentivity specifically for IP-10 is limited; such applications require creep-rupture validation at 45 °C and internal pressure values above typical still-water hydrostatic loads.
Industrial material handling components molded from Dow HDPE IP-10 use wall thicknesses from 3 mm to 6 mm and rib-to-wall ratios of 0.6:1 to 0.8:1 to maintain flatness across base panels up to 1,200 mm in length. Molding is performed on two-platen hydraulic machines with clamp force from 800 t to 1,500 t and accumulator-assisted injection units capable of shot weights up to 5 kg; fill time is kept below 2.0 s to reduce gate freeze-off at the sprue or valve gate. Melt temperature is 200 °C to 230 °C, mold temperature 15 °C to 35 °C, and injection pressure 800 bar to 1,000 bar. Post-industrial regrind from the same production line is added at 20 wt% to 30 wt%; above 30 wt%, notched Izod impact under ISO 180/1A can decline by more than 10% and base-panel warpage after demolding increases unless cooling fixtures are used. Outdoor service applications require a hindered amine light stabilizer masterbatch at 2 wt% to 4 wt%; accelerated weathering per ISO 4892-2 is used to specify UV resistance, not a resin-intrinsic property. Compliance for distribution pallets is tested under ISO 8611 for racking load capacity, static bending, and fork-lift handling; the resin itself is assessed for REACH SVHC content at article level above 0.1 wt%, and RoHS 2011/65/EU applies only if embedded electronic tracking modules are present. Products include collapsible fruit crates, distribution totes, hygienic fish crates with open lattice sidewalls, and export pallets with molded-in drainage channels.
For freezer-grade housewares, Dow HDPE IP-10 is formulated with 2 wt% to 3 wt% color masterbatch and, where cycle-time reduction below 15 s is required, a nucleating agent masterbatch at 0.1 wt% to 0.2 wt%. The part design uses minimum base radii of 3 mm and wall thickness transition no steeper than 2:1 to prevent stress concentration at drop-impact points. Low-temperature notched Izod impact values on production specimens at -20 °C under ISO 180/1A are typically 4 kJ/m² to 6 kJ/m², depending on gate location and cooling rate; published data for this specific configuration is limited. Melt temperature is 190 °C to 210 °C, mold temperature 15 °C to 25 °C, injection speed 200 mm/s to 300 mm/s, and hold pressure is profiled from 500 bar to 300 bar over 4 s to compensate for shrinkage. Stacking top-load resistance is checked by compression testing at 23 °C with a crosshead speed of 10 mm/min; products must withstand 450 N per container column without sidewall buckling. Compliance includes REACH and repeated food storage under EU 10/2011 where the article is intended for food contact, but not all pigments and nucleators carry an EU food contact listing; direct food contact requires positive-list verification for each additive. Terminal products include freezer storage boxes, refrigerator drawers, and modular consumer storage cubes with snap-fit lids.
Industrial pail production from Dow HDPE IP-10 uses a base formulation of 100 wt% virgin resin for food or chemical contact, but non-food pails may incorporate post-industrial regrind from the same plant up to 30 wt% without altering the melt temperature window. Above 30 wt%, the regrind fraction is increased to 40 wt% only when the pail wall thickness is raised above 2.0 mm and the screw recovery time is extended by 15% to ensure melt density uniformity. At 40 wt% regrind, the melt flow rate measured at 190 °C/2.16 kg per ISO 1133-1 can shift upward by 0.5 g/10 min to 1.0 g/10 min, which reduces hold-pressure transfer consistency in hot runner systems and requires a wider final cushion of 5 mm to 8 mm. Process settings for 10 L to 30 L open-head pails include melt temperature 200 °C to 225 °C, mold temperature 15 °C to 30 °C, injection speed 150 mm/s to 250 mm/s, and cooling time 15 s to 25 s scaled by the square of wall thickness. Handle lugs are insert-molded with a surrounding boss diameter-to-thickness ratio of 2:1 to minimize gate blush; the gate land length is kept below 0.5 mm where the lug meets the pail wall. Cross-polymer contamination with PVC or PET must remain below 50 mg/kg because incompatible melt phases cause delamination at the gate and boss areas. For dangerous goods pails, certification testing follows UN 1H2 for the specific filling commodity, including hydrostatic pressure, drop impact at -18 °C, and stack compression for 28 days at 40 °C. For non-hazardous products, industry acceptance testing includes top-load and drop testing under ISTA 3A procedural guides. Terminal products include paint pails, lubricant containers, and non-hazardous chemical buckets with gasketed closures. Post-consumer regrind is not used in food-contact or UN-certified dangerous goods packaging due to unknown contaminant profiles.
General-purpose dosing scoops and measuring spoons molded as single-use food-contact accessories are produced by direct injection molding within the standard melt and mold temperature ranges; no additional additive modification is required beyond a food-contact color masterbatch at 2 wt% and compliance with FDA 21 CFR 177.1520(c) 3.1a.
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Dow HDPE IP-10 is a high-density polyethylene copolymer injection-molding resin. The grade is characterized by a nominal melt flow rate of 10 g/10 min measured at 190 °C/2.16 kg according to ASTM D1238, and a nominal density of 0.957 g/cm³ according to ASTM D1505. Typical applications include thin-wall industrial pails, caps, housewares, and crate components in which high flow, moderate stiffness, and adequate impact resistance are required. The following property set is derived from typical published values for the grade; single-point values are not specification limits.
| Property | Test method | Unit | Typical value |
|---|---|---|---|
| Melt flow rate | ASTM D1238 | g/10 min | 10 |
| Density | ASTM D1505 | g/cm³ | 0.957 |
| Tensile strength at yield | ASTM D638 | MPa | 28 |
| Elongation at break | ASTM D638 | % | 700 |
| Flexural modulus | ASTM D790 | MPa | 1,200 |
| Notched Izod impact | ASTM D256 | J/m | 45 |
| Vicat softening point | ASTM D1525 | °C | 126 |
The density and melt-flow combination places Dow HDPE IP-10 at the higher-flow end of HDPE injection grades without moving to the lower stiffness of low-density ethylene copolymers. In injection molding, this permits filling of long, thin-wall flow paths with lower pressure loss than lower-melt-flow grades in the same density class. However, high-flow HDPE resin data sheets generally do not provide adequate fatigue, weld-line, or environmental stress crack resistance performance for engineering design; those values are tool- and application-specific.
For converters in food-contact and industrial packaging, the relevant regulatory status is evaluated under FDA 21 CFR §177.1520 for olefin polymers when the grade is used in an unmodified form and under EU Regulation 10/2011 if the finished article is to be sold in the European Union. A compliance statement for a particular part must account for colorants, processing aids, line lubricants, and reuse of regrind, because the base resin clearance does not automatically extend to the finished article. Where specific migration data for a packaging configuration are unavailable, laboratory testing using food simulants is required.
At the same injection velocity and melt temperature, a resin with a 10 g/10 min melt flow rate develops lower apparent viscosity than a 4 g/10 min HDPE of equivalent density. In multi-cavity pails and thin-wall containers, the pressure needed to fill the tool is therefore lower at a fixed fill time. Published comparative data for IP-10 against a specific lower-flow grade in identical tooling are limited, but the effect can be estimated from nozzle pressure traces on production machines: a reduction in peak injection pressure is commonly observed when switching from lower-MFR to higher-MFR grades of the same base density. The benefit is largest in tools with high gate velocity or with wall thickness below 1.2 mm, where pressure loss is dominated by shear. The limitation is also clear: lower MFR resins promote chain entanglement and generally provide higher notched Izod impact and better environmental stress crack resistance. In sour cream, detergent, or oil-based filling environments, the higher-MFR grade may require stress-cracking checks under actual load and temperature.
Compared with injection grades at 20 g/10 min or 30 g/10 min, IP-10 retains a higher zero-shear viscosity and higher density. In high-output cup and cap tools, a higher-flow grade may fill smaller gates at lower pressures; IP-10 compensates with better stiffness and greater resistance to post-mold deformation at elevated service temperature. Selection between IP-10 and a 20 g/10 min grade should be based on minimum wall thickness, gate size, part mass, and top-load specification rather than on melt flow alone.
Starting melt temperatures for IP-10 are usually set between 220 °C and 260 °C. Below 220 °C, flow marks and incomplete filling are documented in thin-wall sections; above 260 °C, viscosity falls to the range where nozzle drool, stringing, and thermal oxidation become process control problems. Barrel zone profiles of 190/200/210/220 °C with nozzle at 225 °C are reasonable starting settings for a general-purpose screw with 20:1–24:1 L/D ratio. Mold temperatures are typically 15–50 °C; lower mold temperatures reduce cycle time but lower weld-line toughness and gloss, while higher mold temperatures improve melt front merging but increase cooling time.
Back pressure below 0.3 MPa leads to inconsistent melt density and shot-weight fluctuation on reciprocating-screw machines; a back pressure of 0.5–1.0 MPa is often sufficient to homogenize the melt without excessive screw recovery torque. Screw surface speed in the range 0.2–0.5 m/s is used for general-purpose PE screws. Higher speeds generate frictional heat and can push the melt above the intended discharge temperature even when barrel zones are unchanged.
Because HDPE IP-10 is not hygroscopic, hopper drying is not required for normal dry-flow operations. Condensation from cold silo storage or rapid transfer into a warm plant at relative humidity above 60 % can introduce surface moisture. In that case, a hot-air hopper dryer at 60–80 °C for 1–2 h removes surface moisture without creating the long residence times that promote oxidation. Regrind levels up to 20 wt% are commonly used in pail and crate production; the effect on melt flow should be monitored by ASTM D1238, because repeated extrusion cycles can shift molecular weight distribution and change the processability of the recycled fraction.
Pre-colour tumble blending with a 2 wt% masterbatch is generally adequate; high-shear compounding is not required for pellet-to-pellet letdown.
The practical filling limit of IP-10 is governed by geometry, gate location, and injection velocity rather than by MFR alone. For thin-wall pails with wall thickness of 0.8–1.2 mm and flow length-to-thickness ratios above 200:1, filling is routinely performed with melt temperatures above 230 °C and injection velocities of 150–250 mm/s on hydraulic or electric toggle presses with clamp force determined by projected area and cavity pressure. Cavity-pressure-based process control is preferred over injection-pressure-only control because the switchover to pack pressure determines sink marks, warpage, and dimensional consistency in pail rims and sealing surfaces.
Mold shrinkage for this density class is typically 1.5–2.0 % in the flow direction and 1.2–1.8 % perpendicular to flow. The exact value depends on wall thickness, gate size, hold pressure, and mold cooling. Tool designers should use a shot-specific shrinkage study; data-sheet values are inappropriate for sealing surfaces or snap-fit dimensions.
For industrial pails and food canisters, environmental stress cracking is a potential failure mode when the filled product contains surfactants, vegetable oils, mineral oils, or oxygenated solvents. Under-stress contact with such liquids can initiate crack propagation at gate vestiges, welds, or sharp corners. ASTM D1693 ESCR testing is used as a screening method, but full-container testing under the intended fill material and service temperature remains the only reliable qualification method. Published data on IP-10 after exposure to specific detergent formulations is limited; converters must request a raw-material supplier study or conduct their own.
Compared with high-molecular-weight blow-molding HDPE resins below 1 g/10 min, IP-10 is unsuitable for continuous blow molding of large containers because low melt strength does not support parison sag. For injection molding, the low melt strength is not a limitation except in gas-assisted or foamed processes where cell coalescence and melt front stability are influenced by extensional viscosity.
The service temperature window of HDPE IP-10 is bounded by the Vicat softening point and the ductile-to-brittle transition. For hot-fill applications, continuous exposure above 60 °C under load can cause creep and dimension loss; in sub-zero conditions, impact resistance depends on part design, not only on Izod. No published brittle-to-ductile transition curve for this specific formulation is available in the open literature; part validation under transport conditions is therefore required.