| HS Code | 146441 |
| Density | 0.930 g/cm3 |
| Molecular Weight | 3.0 x 10^6 g/mol |
| Melting Point | 135 °C |
| Vicat Softening Temperature | 80 °C |
| Crystallinity | 45-50% |
| Tensile Modulus | 700 MPa |
| Tensile Strength At Yield | 17 MPa |
| Tensile Strength At Break | 22 MPa |
| Elongation At Break | >300% |
| Charpy Notched Impact Strength | No break |
| Shore D Hardness | 60 |
| Water Absorption | <0.01% |
| Coefficient Of Friction | 0.10-0.20 |
| Abrasion Resistance | High |
As an accredited Braskem UTEC UHMWPE 3041 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Braskem UTEC UHMWPE 3041 is supplied in 25 kg moisture-resistant paper bags, 40 bags per pallet, totaling 1,000 kg. |
| Container Loading (20′ FCL) | 20′ FCL container loading of Braskem UTEC UHMWPE 3041 in 25 kg bags, securely stowed for ocean transport. |
| Shipping | Braskem UTEC UHMWPE 3041 ships as a non-hazardous solid ultra-high-molecular-weight polyethylene resin in moisture-barrier bags or boxes on pallets. It is not regulated for transport (no UN number or hazard class). Keep dry, avoid prolonged heat/UV, and prevent contamination during handling and storage. |
| Storage | Store Braskem UTEC UHMWPE 3041 resin in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, and open flames. Keep containers tightly closed and protect from moisture, dust, and contamination. Avoid contact with strong oxidizing agents. Maintain good housekeeping, use first-in/first-out stock rotation, inspect containers regularly, and follow local regulations and the safety data sheet. |
| Shelf Life | Store unopened in original packaging in a cool, dry place away from sunlight and heat; shelf life is generally indefinite under proper storage conditions. |
In dry-running bottling and packaging lines, UTEC 3041 chain guides, star wheel wear strips, and auger flights are machined from compression-molded sheet rather than injection molded, because the resin exhibits no measurable melt mass-flow rate under 2.16 kg at 190 °C per ISO 1133-1:2022 and cannot be processed by conventional screw injection. Published technical literature places the grade in the 3.0–3.4 million g/mol molecular weight class, which requires consolidation under applied heat and pressure instead of melt-phase pumping. Sheet destined for food-contact chain guides is compression molded at a plateau temperature of 190–200 °C with sustained hydraulic pressure from 5 MPa to 10 MPa until the core reaches the crystalline melting zone identified by differential scanning calorimetry at 133–136 °C per ISO 11357-3. Demolding before uniform core consolidation produces density gradients and subsurface porosity that later appear as delamination in thin machined sections. Components are produced with carbide-tipped tools at surface speeds from 200 m/min to 400 m/min, low rake angles, and positive chip evacuation, because the polymer’s low thermal conductivity causes local melting at uncontrolled feed rates. For food-equipment compliance, the stock meets FDA 21 CFR 177.1520(c) for repeat-use polyolefin articles and EU Regulation (EU) No 10/2011 with an overall migration limit of 10 mg/dm². Lot certification should include extractables testing under NSF/ANSI 51 where incidental contact with potable water occurs. Moisture absorption remains below 0.01 % per ASTM D570, so cleaning with 2–3 % sodium hydroxide solution or 0.5–1.0 % peracetic acid at 60 °C does not induce hydrolytic breakdown. Continuous operating temperature is limited to 70 °C because flexural modulus falls sharply as the alpha relaxation is approached, and dry-running coefficient of friction against polished steel is reported in the range 0.10–0.15, but field data for specific chain speeds above 120 m/min should be validated with a pilot trial.
| Standard/Regulation | Method/Clause | Parameter |
|---|---|---|
| FDA 21 CFR | 177.1520(c) 2.1 | Repeat-use polyolefin articles for food contact |
| EU Regulation (EU) No 10/2011 | Annex I overall migration | 10 mg/dm² |
| NSF/ANSI 51 | Materials for food equipment | Incidental potable water contact |
| ISO 1133-1:2022 | Melt mass-flow rate | Not measurable at 2.16 kg / 190 °C |
| ASTM D4020 | UHMWPE molding and extrusion specification | Baseline for compression molding |
Mineral processing slurry pumps, hydrocyclone feed spools, and flotation cell wear plates are cut from UTEC 3041 because the material combines low wet-sliding friction with resistance to three-body abrasion from quartz and magnetite fines. In ASTM G65-16 dry-sand/rubber-wheel testing, unfilled UHMWPE typically records volume loss below 2.0 mm³/kg, while carbon steel exceeds 100 mm³/kg under the same procedure. Wet slurry wear is highly dependent on particle shape, solids loading, and impeller tip speed, so the dry-sand result is used only as a comparative ranking rather than a direct service-life predictor. The processing path for pump liners begins with compression molding of blanks from 50 mm to 200 mm thick, followed by stress-relief annealing at 120 °C for 1 h per 25 mm of thickness and final CNC machining to an interference fit of 0.1–0.3 % of the casing bore diameter. This shrink-fit installation prevents liner rotation under reverse-flow conditions but can induce compressive creep at temperatures above 60 °C, leading to axial extrusion behind the gland. Batch-to-batch variance in powder bulk density from 0.38 g/cm³ to 0.48 g/cm³ alters mold fill height by up to 10 % when volumetric filling is used; processors compensate by weighing each charge instead. Published field failure modes include localized gouging when sharp crushed rock exceeds 50 mm top size, cavitation pitting at suction-side liner joints, and flange-face stress cracking when bolt torques exceed the manufacturer’s recommended limit. The primary limitation is thermal softening: at slurry temperatures above 65 °C, cut resistance decreases and dimensional movement accelerates. The grade is therefore not recommended for continuous service in agitated leach tanks where exothermic oxidation reactions may exceed this boundary. Chemical exposure in flotation circuits including dilute sulfuric acid at pH 2–4, sodium metabisulfite, and polyacrylamide flocculant does not attack the polymer, but REACH Regulation (EC) No 1907/2006 compliance applies to the synthetic polymer matrix and to any residual process aids.
In paper forming sections, UTEC 3041 is machined into dewatering foils, suction box covers, and deflector blades that operate against polyester forming fabric at wire speeds from 900 m/min to 1,500 m/min. The polymer’s dry-sliding friction against moving fabric is lower than that of high-density polyethylene and alumina-filled materials, which reduces drive power consumption. Published comparative data for specific machine speeds and fabric tension is limited and should be obtained from pilot tribometer testing under ASTM D3702-94 thrust-washer conditions or a full-scale forming-section trial. The critical geometric parameter is wear flat width on the foil leading edge: once the flat exceeds 0.5 mm, vacuum-assisted dewatering efficiency drops and fabric wear accelerates. Machining from compression-molded block requires stress relief after rough cutting at 120 °C for 1 h per 25 mm of thickness, followed by finish passes that maintain straightness within 0.05 mm per 1,000 mm. Internal stress in as-sintered block causes bowing during machining; therefore all six faces are skim-cut before final dimensions are established. Wet-end chemistry imposes an operational boundary: continuous exposure to strong acid or alkaline felt cleaning chemicals above pH 1 or 13 is not recommended at elevated machine temperature, and sustained stock temperature above 70 °C reduces creep resistance. The resin resists papermaking additives including kaolin, calcium carbonate, and rosin size, but aromatic process solvents used in some specialty furnish cleaning programs can cause measurable swelling. A 30-day immersion coupon per ASTM D543 is the standard pre-installation qualification method for such solvents.
Municipal wastewater clarifiers and thickeners use UTEC 3041 wear shoes, scraper blade edges, and chain guides submerged in primary sludge at 5–35 °C. The polymer is selected because water absorption is below 0.01 % per ASTM D570, so dimensional change in continuous immersion is negligible compared with nylon or acetal. Machined flights are produced from 20 mm to 50 mm compression-molded sheet, then drilled with oversize fastener holes to accommodate linear thermal expansion of approximately 1.5–2.5 × 10⁻⁴ m/m°C. Attachment is typically made with 316 stainless steel countersunk bolts through slotted holes, because the polymer moves differentially relative to steel support frames during seasonal temperature swings. Chemical exposure includes residual sodium hypochlorite at 1–5 mg/L, ferric chloride, alum, and polymer flocculants. UHMWPE is inert to these species, but continuous contact with mixed oxidants above 10 mg/L free chlorine can embrittle the surface over multiyear service. Notched Izod impact testing per ASTM D256 typically reports no break at -40 °C, which reduces brittle fracture when rigid flights encounter settled grit. The main processing limitation is low thermal conductivity during sheet production: if cooling rate is too rapid, residual stress leads to warping after machining. Shops control this by slow cooling under pressure at 10–15 °C/h from 160 °C to 80 °C before removing the part from the press. Published data for this specific municipal clarifier configuration is limited; life extension over cast iron and polyamide is commonly observed but site-specific validation under ASTM G65-16 abrasive wear and ASTM D638-14 tensile retention after exposure is required.
In dry bulk storage, UTEC 3041 liner panels are installed inside silo discharge cones, hopper transitions, and transfer chutes carrying fly ash, limestone powder, cement, or grain. The replacement of Hardox plate with UHMWPE is driven by the lower wall friction coefficient of 0.10–0.20 against conditioned bulk solids, which promotes mass flow and reduces ratholing. The actual flow-function boundary depends on Jenike shear cell data for the stored powder per ASTM D6128. Installation involves 10 mm to 30 mm thick compression-molded sheets cut to panel sizes and fastened with countersunk bolts or welded studs through slotted holes. Differential expansion between the steel cone and the polymer liner must be calculated using the polymer’s linear expansion coefficient of 1.5–2.5 × 10⁻⁴ m/m°C. A 3 m steel cone warmed by 20 °C can impose approximately 9–15 mm of relative movement, which slotted holes absorb only if oriented correctly along the cone circumference. Field failure occurs when panels are rigidly bolted without expansion allowance, causing buckling at the midline and tearing around fastener heads. Thermoforming of flat liner panels into conical radius sections requires heating to 140–160 °C with heated molds; the process must not exceed 220 °C because chain scission and oxidative discoloration begin. The polymer resists abrasion from fine powders, with ASTM G65-16 volume loss below 2.0 mm³/kg, but streams containing sharp coarse particles larger than 50 mm may cut the surface. Such conditions require a composite design with ceramic inserts or segmented steel-backed panels. REACH Regulation (EC) No 1907/2006 applies to EU installations, and the resin meets FDA 21 CFR 177.1520(c) for incidental food contact in grain handling.
Off-highway truck body liners, excavator bucket wear pads, and crane boom wear strips are produced by compression molding UTEC 3041 powder into slabs from 25 mm to 150 mm thick. The powder is loaded into a mold cavity and heated under hydraulic pressure from 5 MPa to 10 MPa until the full cross-section reaches 180–200 °C. Maintaining plateau temperature for 10 min per 10 mm of thickness ensures chain diffusion across powder particle boundaries. Premature demolding before the core temperature exceeds 180 °C creates internal voids that are not visible on the surface but appear as white stress concentrations during CNC machining or as localized collapse under high-frequency impact. Molded density is checked against 0.925–0.945 g/cm³ per ISO 1183-1. A density below 0.900 g/cm³ in thick slabs indicates incomplete consolidation. Tensile yield for fully consolidated UTEC 3041 is reported in the range 20–24 MPa per ASTM D638-14, with elongation at break exceeding 300 %; these values drop sharply if oxidation has occurred. Production-scale platen presses used for such parts require platen parallelism within 0.05 mm/m and multi-zone heating control, because thickness variance across a 1,500 mm mold translates directly into density variation and warpage after cooling. The cooling segment is a bottleneck: forced cooling at rates above 15 °C/h introduces residual stress that causes slab bowing. Presses are therefore held under pressure and cooled from 160 °C to 80 °C over several hours. Slabs are then machined with carbide tooling, but the polymer’s elongation and toughness make chip control difficult; compressed-air chip evacuation and low-feed roughing passes are used to prevent chip wrapping. This grade is not suitable for injection molding or single-screw extrusion, because its melt viscosity exceeds the measurable range and would cause severe screw blockage.
Chemical transfer pumps, valve seats, and throttle bushings are fabricated from UTEC 3041 where dilute acids, alkalis, and salt solutions create corrosive conditions that attack stainless steel and bronze. The polymer withstands continuous immersion in 10 % sulfuric acid at 60 °C, 20 % sodium hydroxide at 60 °C, and 3 % sodium hypochlorite solution at ambient temperature, with weight change below 1 % over 30 days in qualification testing per ASTM D543. Strong oxidizing media are an operational boundary: concentrated nitric acid above 10 %, bromine, fluorine, and mixed acids containing sulfonic acid groups degrade UHMWPE through chain scission and should not contact the grade. Aromatic hydrocarbons, chlorinated solvents, and some esters cause swelling above 5 % and are likewise outside the chemical compatibility envelope. Pump internals are machined from compression-molded tube or rod with dimensional tolerances of ±0.05 mm on bearing bores; the material’s low elastic modulus requires heavier interference fits than bronze but must be limited to 1–2 % of diameter to avoid creep-induced seizure. The pressure-velocity limit for dry-running service is typically below 0.07 MPa·m/s; above this value, frictional heat generation exceeds the polymer’s low thermal conductivity and causes localized melting. Where abrasive particles are present, throttle bushings machined from UTEC 3041 show lower wear than PTFE or acetal, but the material is not recommended for high-pressure gas service because rapid decompression can generate internal voids. REACH Regulation (EC) No 1907/2006 and RoHS Directive 2011/65/EU compliance apply when such pump components are integrated into electrical or electronic equipment.
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