| HS Code | 646695 |
| Gradename | Lotte Chemical Titan HDPE HF0961 |
| Polymertype | High Density Polyethylene (HDPE) |
| Density | 0.961 g/cm³ |
| Meltflowrate | 0.08 g/10 min |
| Tensilestrengthatyield | 28 MPa |
| Tensilestrengthatbreak | 42 MPa |
| Elongationatbreak | 700% |
| Flexuralmodulus | 1200 MPa |
| Vicatsofteningtemperature | 125 °C |
| Meltingpoint | 134 °C |
| Crystallizationtemperature | 115 °C |
| Escr | >1000 h |
| Brittlenesstemperature | < -70 °C |
| Hardness | 62 Shore D |
| Waterabsorption | < 0.01% |
As an accredited Lotte Chemical Titan HDPE HF0961 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Lotte Chemical Titan HDPE HF0961 is packaged in 25 kg polyethylene-lined woven bags, with 40 bags per 1,000 kg pallet. |
| Container Loading (20′ FCL) | 20′ FCL container loading of Lotte Chemical Titan HDPE HF0961: 25 kg bags, palletized, shrink-wrapped, evenly loaded, and secured for ocean transit. |
| Shipping | Lotte Chemical Titan HDPE HF0961 is a non-hazardous high-density polyethylene shipped in 25 kg bags or bulk, palletized and stretch-wrapped. Store in a dry, clean, ventilated area away from sunlight, moisture, heat, and contaminants. Transport by truck, rail, or sea under standard cargo conditions. Ensure packaging remains sealed. |
| Storage | Store in original unopened packaging in a cool, dry, well-ventilated warehouse away from direct sunlight, moisture, heat, ignition sources, and strong oxidizers. Stack pallets safely; avoid puncturing bags. Keep containers closed to prevent contamination. Keep off damp floors and away from acids, alkalis, and incompatible materials. Use dust controls and grounding where needed. Follow manufacturer SDS and local regulations. Maintain good housekeeping. |
| Shelf Life | Shelf life is 24 months from manufacture when stored in original packaging in a cool, dry, well-ventilated area away from sunlight. |
In thin-wall injection molding of dairy spread containers, delicatessen tubs, and single-serve condiment cups, the melt flow rate of HDPE HF0961—reported as 9 g/10 min under ASTM D1238 conditions of 190 °C and 2.16 kg—determines the maximum flow length attainable before gate freeze-off arrests cavity filling. Melt temperature at the nozzle is maintained between 210 °C and 245 °C, while mold surface temperature is held at 8 °C to 18 °C to compress the cooling-dominated portion of cycle time below 4 s in 0.4 mm to 0.8 mm wall stock. Injection velocity profiles of 200 mm/s to 400 mm/s are specified to outrun the solidification front, and hydraulic injection pressure commonly reaches 140 MPa to 180 MPa in valve-gated hot runner systems feeding 32 to 128 cavity stack molds. Holding pressure between 60% and 80% of peak injection pressure is applied for 0.8 s to 2.0 s to suppress sink marks adjacent to rim stiffeners; excessive packing beyond this window induces warping across the container base due to asymmetric shrinkage along flow and transverse directions. Food-contact compliance for this application segment is established under FDA 21 CFR 177.1520, which defines olefin polymer identity, n-hexane and xylene extractable fraction limits, and conditions of use for high-density polyethylene in contact with aqueous, acidic, and fatty foods. European Union market access requires conformity with Regulation (EU) No 10/2011, including the overall migration limit of 10 mg/dm² of food contact surface area specified in Article 12. Terminal products manufactured from HF0961 in this segment include in-mold-labeled margarine tubs, stackable deli containers for delicatessen and foodservice channels, and single-serve condiment portion cups with lid-seating annular grooves.
Injection-molded caps and closures for non-carbonated beverage bottles, pharmaceutical vials, and household chemical packages impose dimensional requirements that differ fundamentally from thin-wall container applications. The removal torque after 24 h ambient conditioning is governed by the annular rib compression seal geometry, the thread engagement depth, and the viscoelastic recovery capacity of the polymer following mold stripping. HDPE HF0961 permits filling of multi-thread start geometries with thread depths of 0.6 mm to 1.1 mm while maintaining dimensional consistency for bottle neck finishes specified by the International Society of Beverage Technologists, including ISBT PCO 1881 for 28 mm non-carbonated water closures. Application torque values for 28 mm closures typically fall within 1.7 N·m to 2.3 N·m, with removal torque after 72 h expected to remain above 0.8 N·m to prevent leakage under simulated distribution stacking loads. Environmental stress crack resistance is assessed under ASTM D1693 using Igepal CO-630 surfactant at 50 °C; closure formulations containing plasticizer-free colorant concentrates exhibit longer F50 values than equivalent compounds with incompatible organic pigments, owing to reduced stress concentration at pigment agglomerates. Processing for this segment employs melt temperatures of 190 °C to 230 °C, mold temperatures of 12 °C to 25 °C, and unscrewing or collapsible-core tooling to demold internal thread forms without damage. Cycle times range from 5 s to 10 s per closure depending on cavity count; leaf-slit collapsible cores permit ejection without rotational motion but require additional actuation sequencing in the mold base. Terminal products include push-pull sports caps for bottled water, screw caps for shampoo and conditioner bottles, and child-resistant closure systems tested in accordance with ISO 8317.
Storage totes, basinware, stackable drawer organizers, and wardrobe accessories produced from HDPE HF0961 exploit the melt flow rate of 9 g/10 min to fill thin hinge sections of 0.4 mm to 0.8 mm and snap-fit latch geometries that would short-shot in lower-flow HDPE grades. Mold temperature is held between 15 °C and 30 °C with melt temperature at 200 °C to 235 °C; wall stock in the main panel sections spans 1.2 mm to 2.8 mm, permitting total cycle times of 18 s to 35 s in 500 t to 1,200 t clamp force machines. Freezer-safe storage articles require dart impact testing at -18 °C in accordance with ASTM D1709 to confirm ductile failure mode at the lowest intended service temperature; HDPE HF0961 retains sufficient impact strength at this condition when wall thickness is maintained at or above 1.4 mm and flow fronts are balanced to prevent cold weld lines at handle attachment points. Food-contact housewares fall under FDA 21 CFR 177.1520 and Regulation (EU) No 10/2011; non-food storage items must comply with REACH Annex XVII restrictions on phthalate plasticizers and heavy metals. Warpage management for large flat lid panels employs differential cooling circuit layouts—core-side temperature offset by 3 °C to 6 °C relative to cavity side—to counteract asymmetric shrinkage and ensure consistent nesting clearances for vertical stackability. Terminal products include modular wardrobe drawers, under-bed storage totes, rectangular basins with rolled rims, and stackable desktop organizers with injection-molded polycarbonate transparent inserts.
Open-head and tight-head pails of 5 L to 25 L capacity intended for dangerous goods transport require packaging approval under the UN Recommendations on the Transport of Dangerous Goods, Chapter 6.1, which imposes destructive testing conditions that directly govern the injection molding parameter window for HDPE HF0961. Drop testing at -18 °C targets the most vulnerable zones: gate weld lines at the pail base center, handle lug attachment bosses, and the junction between sidewall and bottom corner radius. The drop height for Packing Group II liquids of specific gravity 1.2 is 1.8 m; for Packing Group III solids with specific gravity below 1.0, the drop height reduces to 0.8 m. Stacking load capacity is verified at 40 °C for a continuous duration of 28 days, with the applied load equivalent to the total mass of identical packages in a 3 m stack. Wall section thickness in certified pails ranges from 1.8 mm to 2.6 mm, with additional material concentrated at the ear lugs and bottom chime to distribute impact energy over a larger plastic volume; finite element mold flow analysis is used to position the gate at the base center such that weld lines migrate to low-stress regions away from the handle axis. Environmental stress crack resistance of the formulated compound is assessed under ASTM D1693 with Igepal CO-630 at 50 °C; pails intended for agrochemical concentrates, lubricating greases, and surfactant-based cleaning products require F50 values exceeding 100 h, and blend adjustment with higher molecular weight HDPE may be necessary when aggressive contents are specified. Processing parameters include melt temperature of 190 °C to 225 °C, mold temperature of 15 °C to 30 °C, injection pressure of 80 MPa to 120 MPa, and total cycle time of 25 s to 45 s in 800 t to 1,600 t clamp force machines operating single- or two-cavity pail molds. Terminal products include UN-certified paint pails, food-grade edible oil containers with tamper-evident lid systems, and chemical packaging pails with molded-in bung threads for sealed closure plugs.
Clinical laboratory specimen cups, reagent reservoirs, and diagnostic assay consumables injection molded from HDPE HF0961 occupy a regulatory territory distinct from food-contact housings and industrial packaging. Medical device packaging falls under ISO 10993-1 biological evaluation of medical devices, requiring cytotoxicity testing of the finished article in accordance with ISO 10993-5; polymer resin compliance with USP Class VI biological reactivity testing—covering systemic injection, intracutaneous, and implantation protocols—is commonly cited as supporting evidence for regulatory submissions. The material itself is listed under FDA 21 CFR 177.1520 for food-contact use, which does not independently qualify the article for medical packaging; device manufacturers must verify that processing aids, mold release agents, and colorant carriers introduced during compounding and molding do not leach above extractable limits specified in USP <661.1> for plastic packaging systems. Gamma sterilization at 25 kGy to 40 kGy is the dominant terminal sterilization modality for HDPE diagnostic containers; the polymer exhibits acceptable retention of tensile properties and impact strength following this dose range when antioxidant packages are formulated for radiation tolerance. Electron beam sterilization at 20 kGy to 35 kGy offers an alternative for thin-wall articles where dose penetration is uniform. Ethylene oxide sterilization is generally avoidable for HDPE because the polymer can absorb residual gas; if mandated by product configuration, aeration cycles must extend to 48 h to 72 h at 40 °C to reduce EO residuals below limits specified in ISO 10993-7. Cleanroom molding under ISO 14644-1 Class 8 or Class 7 conditions is typical for medical articles; mold temperature of 10 °C to 20 °C, melt temperature of 195 °C to 230 °C, and cycle time of 8 s to 15 s are applicable. Terminal products include graduated specimen collection containers, urinalysis cups with lid closures, and reagent storage bottles with volumetric markings.
Returnable transit packaging—beverage crates, agricultural produce crates, bakery trays, and fish boxes—requires HDPE compounds that retain stiffness under repeated impact and compressive loading across multiple distribution cycles. HDPE HF0961 is processed in this segment at melt temperatures of 200 °C to 240 °C, mold temperatures of 12 °C to 25 °C, and wall thicknesses of 3.0 mm to 5.5 mm; cycle times extend to 20 s to 40 s due to cooling-dominated thermal behavior in thick rib and boss sections. Machine clamp force requirements commonly reach 1,000 t to 1,800 t for single-cavity beer crate molds with projected areas exceeding 90,000 mm². Low-temperature impact testing under ASTM D256 at -18 °C is applied to crate corner sections and bottom rib intersections; the notched Izod approach is supplemented by full-crate drop testing from 1.2 m onto concrete at 0 °C to replicate distribution yard handling conditions. Outdoor storage of empty crates necessitates UV stabilization; natural HDPE exposed continuously to sunlight undergoes chain scission at the surface that reduces tensile elongation at break by more than 50% after 12 months under ASTM D2565 accelerated weathering conditions in xenon-arc apparatus. Carbon black at 1.5 wt% to 2.5 wt% or hindered amine light stabilizer systems at 0.1 wt% to 0.3 wt% are formulated to extend service life to 5 to 10 years; the selection between black and light-stabilized colors depends on end-user sorting logistics and brand visibility requirements. Mold flow analysis identifies weld line positions at the crate base grid intersection; gate placement at the center of the base panel directs weld lines into low-stress zones between rib junctions. Terminal products include beer and soft drink bottle crates with integrally molded stacking bosses, ventilated produce crates for orchard and field collection, and interlocking bread trays with anti-slip top edges.
Consistent comparative processing data for HDPE HF0961 across the principal injection molding application segments is consolidated below for reference in tooling and process engineering.
| Application Segment | Melt Temperature (°C) | Mold Temperature (°C) | Typical Cycle Time (s) | Wall Thickness (mm) | Clamp Force Range (t) |
|---|---|---|---|---|---|
| Thin-Wall Food Containers | 210–245 | 8–18 | 4–8 | 0.4–0.8 | 350–900 |
| Caps and Closures | 190–230 | 12–25 | 5–10 | 0.6–1.1 (thread) | 250–600 |
| Housewares and Storage | 200–235 | 15–30 | 18–35 | 1.2–2.8 | 500–1,200 |
| UN-Certified Industrial Pails | 190–225 | 15–30 | 25–45 | 1.8–2.6 | 800–1,600 |
| Medical / Diagnostic Containers | 195–230 | 10–20 | 8–15 | 0.8–1.6 | 200–500 |
| Returnable Logistics Crates | 200–240 | 12–25 | 20–40 | 3.0–5.5 | 1,000–1,800 |
Injection molded toy components—building blocks, snap-fit vehicle wheels, sorting boxes, and outdoor play accessories—utilize HDPE HF0961 for living hinge and torsional snap-fit connections that demand repeated flexural cycles without brittle fracture. Melt temperature of 195 °C to 225 °C, mold temperature of 15 °C to 25 °C, and wall thickness of 1.5 mm to 3.5 mm are typical in this segment; cycle times range from 15 s to 25 s in multi-cavity tools of 16 to 48 cavities. European toy safety compliance requires conformity with EN 71-3, which specifies migration limits for nineteen elements including lead at 2.0 mg/kg in dried material and cadmium at 1.3 mg/kg; these limits apply to the complete toy component as molded, not only to the base resin. United States market access under the Consumer Product Safety Improvement Act imposes total lead content restrictions of 100 mg/kg in accessible substrate materials. Small parts regulations under 16 CFR 1501 apply to detachable components intended for children under 36 months; the small parts cylinder test determines whether a component requires choking hazard labeling or design modification. Colorant systems for HDPE toy applications must be selected from pigments that do not exceed migration thresholds under simulated saliva and perspiration extraction conditions specified in EN 71-3; organic pigments containing soluble heavy metal contaminants are eliminated from formulations at the supplier qualification stage. Terminal products include interlocking building elements, ride-on toy wheels with snap hubs, and bathroom play sets with suction-cup attachments.
Competitive Lotte Chemical Titan HDPE HF0961 prices that fit your budget—flexible terms and customized quotes for every order.
For samples, pricing, or more information, please contact us at +8618136850665 or mail to admin@ascent-chem.com.
We will respond to you as soon as possible.
Tel: +8618136850665
Email: admin@ascent-chem.com
Flexible payment, competitive price, premium service - Inquire now!
Lotte Chemical Titan HDPE HF0961 is a high-density polyethylene resin supplied in pellet form for blown-film extrusion. The grade is defined by a nominal density of 0.961 g/cm³ tested under ASTM D1505 or ISO 1183-1, and a melt-flow rate of 0.9 g/10 min at 190°C/2.16 kg according to ASTM D1238 or ISO 1133-1. These two parameters place HF0961 in the medium-high-density segment used for thin-gauge HDPE film. The density level provides stiffness and downgauging potential, while the 0.9 g/10 min melt-flow rate gives a balance between extruder processability and bubble stability. Primary application fields include T-shirt grocery bags, refuse sacks, and industrial liners.
| Property | Test method | Published value |
|---|---|---|
| Nominal density | ASTM D1505 / ISO 1183-1 | 0.961 g/cm³ |
| Melt-flow rate | ASTM D1238 / ISO 1133-1 | 0.9 g/10 min |
Published grade-specific mechanical test values for HF0961 are limited in public trade literature. Converters therefore qualify downstream performance through lot-to-lot capability runs on the target blown-film line rather than relying solely on single-point datasheet values. This limitation is common for polyolefin grades where principal lot-release data are density and melt-flow rate.
Although comonomer type is not disclosed in public datasheets, the 0.961 g/cm³ density indicates limited short-chain branching. The higher crystallinity relative to 0.954–0.958 g/cm³ film grades increases modulus but reduces low-temperature impact. The 0.9 g/10 min melt-flow rate does not by itself define molecular weight distribution; gel permeation chromatography or rheotens melt-strength testing is required to compare bubble stability. Published data for this specific configuration is limited, so substitution decisions should be validated on the target line.
On high-stalk HDPE film lines, the processing window is set by three interacting variables: melt temperature, frost line height, and blow-up ratio. For a 0.961 g/cm³ film resin, melt temperatures between 190°C and 220°C are typical. Below 190°C, the high crystalline melting point increases the risk of unmelt gels and spider-line melt fracture at the die lip. Above 230°C, residence-time degradation can generate oxidised gels that appear as fisheyes in 20–25 µm film. Single-screw extruders with grooved feed sections, barrier-flighted screws, and 25:1 to 30:1 L/D ratios are commonly used. Melt pressure before the screen changer typically falls between 200 bar and 350 bar, depending on throughput, die gap, and screen-pack condition. If screen-charger pressure rises more than 50–70 bar above the clean-screen baseline, shear heating shifts the effective melt temperature upward and narrows bubble stability.
Frost line height is maintained at 6 to 10 die diameters for a stalk-bubble configuration. A lower frost line increases quench and reduces haze but can lock in excessive machine-direction orientation and raise splitting risk. A higher frost line lowers orientation but may allow bubble wander and gauge bands. Blow-up ratio is generally held between 3:1 and 5:1. Above 5:1, the high-density crystalline network tends to produce low Elmendorf tear in the transverse direction and reduces conversion efficiency on bag lines. Die gaps from 0.8 mm to 1.5 mm are common for this density class; narrower gaps increase shear stress and may promote melt fracture, while wider gaps reduce orientation and require higher frost line control.
Pre-drying is not generally required because HDPE has low equilibrium moisture uptake. If storage occurs at relative humidity above 60% or if pellets are exposed to condensation, surface moisture can create splay, pinholes, or bubble defects. In such cases a hopper dryer at 60–70°C for 2–4 h is sufficient, provided the drying air is dew-point-controlled below −20°C and free of oil.
Conversion experience on narrow-web bag lines shows that die temperature uniformity influences gauge spread more strongly than screw speed for HF0961. The high density increases solidification rate, so a non-uniform die temperature profile tends to freeze thickness defects into the web before the collapsing frame can correct them. Automated air rings with segmented dies are used on high-output lines to hold gauge variation within ±5% on 25 µm film. Internal bubble cooling air flow must be balanced with the main air ring; an imbalance greater than 10% of total air volume can induce oscillating frost line height and unstable bubble diameter. On lines without automatic bubble cage adjustment, a fixed bubble cage set at 1.2–1.5 times the die diameter at the frost line prevents oscillation.
Film properties are not single-point values. Tensile yield strength in HDPE film of this density class is typically evaluated under ASTM D882 or ISO 527-3, dart impact under ASTM D1709 method A, and Elmendorf tear under ASTM D1922. As density rises from 0.949 g/cm³ to 0.961 g/cm³, tensile yield increases but dart impact and tear generally decrease. For HF0961, the selection priority is not maximum impact or maximum tear, but a balance between film stiffness and manufacturability on thin-gauge bag lines. Target film thickness for T-shirt bags is typically 20–25 µm, while refuse sacks may run 30–50 µm. Below 15 µm, the high-density stiffness aids downgauging, but tear resistance becomes limiting; converters may blend with LLDPE at 10–20% to improve dart impact and machine-direction tear.
At the converting stage, bag machines handle HF0961 film with higher blocking resistance than low-density film because the high density lowers surface tack. However, high-density film also has a higher coefficient of friction against metal surfaces unless slip additives are incorporated. Corona treatment is not normally needed for bag fabrication; when printing is required, surface tension should be verified with dyne solutions to be at least 38 mN/m. HDPE film often shows surface decay more slowly than LLDPE but still requires inline treatment for water-based inks.
Reground edge trim from HF0961 film can be re-introduced up to 20 wt% in typical bag production without major loss of bubble stability. Higher regrind levels increase gel count and reduce dart impact because of molecular weight degradation during reprocessing. These limiting regrind levels are line-specific and should be verified by ASTM D1709 and ASTM D1922 on finished film.
Because the melt-flow rate of 0.9 g/10 min is higher than fractional-melt HDPE grades of 0.2–0.3 g/10 min, direct substitution without process changes can produce low melt strength, bubble flutter, and loss of gauge control. Melt temperature is typically reduced by 10–20°C when moving from a fractional-melt resin to HF0961. The higher MFR also lowers extruder motor load at constant output, often by 10–15% on grooved-feed extruders with 25:1 L/D or greater, because the higher melt index corresponds to lower viscosity at typical shear rates above 100 s⁻¹. The advantage is faster screw recovery, lower head pressure, and the ability to run a tighter screen pack for gel control. The trade-off is reduced bubble stability in large-diameter dies above 300 mm; for heavy-duty films thicker than 50 µm, a fractional-melt high-molecular-weight HDPE is generally preferred.
Within the Lotte Chemical Titan HDPE film slate, lower-density grades are specified when puncture and dart impact dominate, while fractional-melt grades are specified for heavy-duty liners and large-part film. HF0961 occupies the high-output thin-gauge segment. Its 0.9 g/10 min MFR is significantly higher than fractional-melt film grades, allowing faster line speeds and thinner film on extruders of 100 mm screw diameter or smaller. Converters upgrading from a 0.2 g/10 min grade should expect lower head pressure and shorter residence time but must tighten frost-line control.
Compared with a lower-density blown-film HDPE of 0.949 g/cm³ and similar melt-flow rate, HF0961 films show higher tensile modulus and lower dart impact under ASTM D1709. Seal initiation temperature is higher by approximately 5–10°C because the crystalline fraction is higher. Heat-seal settings on bag machines may therefore require an increase in seal-bar temperature or dwell time to maintain hermetic seals. The higher density also reduces water-vapour and gas permeability, but the improvement in water-vapour transmission rate is smaller than the difference between HDPE and polypropylene. These differences should be evaluated with ASTM F1249 water-vapour transmission-rate testing when barrier claims are required.
Converters using HF0961 in food-contact applications must verify grade-specific certification against FDA 21 CFR 177.1520 for olefin polymers. Compliance under 21 CFR 177.1520(c) depends on end-use extractives testing and condition-of-use limits, not solely on resin composition. For EU markets, compliance must be assessed under EU 10/2011 migration requirements, with specific migration limits for any additives used in masterbatch or processing aids. REACH registration obligations apply at the supplier level, and downstream users must confirm the grade is covered in Section 1 of the safety data sheet. RoHS screening is relevant only when the final film is incorporated into electrical or electronic equipment; Directive 2011/65/EU restricted substances are not typical for polyethylene film, but batch-specific certificates should be requested if the film is part of a RoHS-controlled assembly.
Storage conditions influence conversion. Prolonged exposure to direct sunlight can pre-degrade the pellet surface and create gel speck contamination in film. The resin should be kept in sealed containers at ambient temperature below 40°C. Avoid combining with pro-oxidant masterbatches or amine-based additive packages without a compatibility trial, because amine chemistry can interact with phenolic processing stabilisers and shift tone or odour. Purge between HF0961 and LLDPE or plasticised materials is required to avoid film appearance defects and contamination of recycled scrap streams.