| HS Code | 518252 |
| Chemicalname | Ultra-high molecular weight polyethylene |
| Form | Powder |
| Color | White |
| Odor | Odorless |
| Averageparticlesize | 20 µm |
| Bulkdensity | 0.40 g/cm³ |
| Specificgravity | 0.93-0.94 |
| Meltingpoint | 130-136 °C |
| Molecularweight | 2,000,000 g/mol |
| Moisturecontent | <0.1% |
| Thermaldecompositiontemperature | >300 °C |
| Crystallinity | 45-55% |
| Waterabsorption | <0.01% |
| Chemicalresistance | Excellent to acids, alkalis, and solvents |
| Coefficientoffriction | Low |
| Abrasionresistance | High |
As an accredited Mitsui Chemicals MIPELON UHMWPE PM-200 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Mitsui Chemicals MIPELON UHMWPE PM-200 is packed as a fine white powder in 15 kg moisture-resistant paper bags. |
| Container Loading (20′ FCL) | Standard 20′ FCL dry container loaded with Mitsui Chemicals MIPELON UHMWPE PM-200, securely palletized in bags and stowed for export. |
| Shipping | Mitsui Chemicals MIPELON PM-200 is a fine UHMWPE powder typically shipped in sealed, moisture-resistant bags or drums under dry ambient conditions. Protect from moisture, ignition sources, and static; minimize dust generation. Generally non-hazardous for transport, but verify the SDS and local regulations before shipment. |
| Storage | Store MIPELON UHMWPE PM-200 in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, and open flames. Keep containers tightly closed to prevent moisture ingress and dust formation. Avoid prolonged UV exposure and store separately from strong oxidizers. Use appropriate dust-control practices, ensure good housekeeping, and follow local regulations and the SDS. |
| Shelf Life | Typically indefinite if stored dry, sealed, away from heat and sunlight; no fixed expiry, but confirm supplier’s retest policy. |
Within anti-scratch two-component polyurethane topcoats for injection-moulded ABS and PC/ABS automotive interior components, Mitsui Chemicals MIPELON PM-200 is introduced as a discrete solid-lubricant phase rather than as a migrating wax. The grade is an ultra-high-molecular-weight polyethylene powder with a reported average particle size of 20 μm and a typical density of 0.94 g/cm³. The production-scale dispersion sequence normally consists of a pre-wetting stage in which PM-200 is charged into a butyl acetate/xylene blend at 25–30 wt% non-volatile content and dispersed with a high-speed disc disperser operating at 18–25 m/s peripheral speed. High shear is held for 15–20 min to break loose agglomerates, followed by low-shear let-down at 5–8 m/s so that the spherical particle geometry is preserved. The dosage range is controlled at 1.0–3.5 wt% based on total resin solids; above 3.5 wt%, the cured film shows a measurable reduction in 20° gloss under ASTM D523-14 and an increased tendency for micro-sedimentation when final viscosity falls below 60 KU at 23°C. Abrasion resistance is screened with ASTM D4060-19 using CS-10 wheels at 500 g load for 1000 cycles; comparative panel testing typically records a 35–60% reduction in mass loss, although published data for this specific configuration is limited and must be verified on the target substrate. Surface slip is measured by ASTM D1894-14, where the kinetic coefficient of friction on cured clearcoat can drop to 0.08–0.15 without shifting pencil hardness below the F–H range evaluated by ISO 15184:2020. Adhesion after humidity ageing is checked by ASTM D3359-23 cross-cut, with no loss greater than 1 rating unit on PC/ABS after 240 h at 50°C and 90% RH. Terminal product types include automotive HVAC louvers, door panel inserts, centre console trim, and black high-gloss sports equipment housings. PM-200 is non-polar and does not participate in isocyanate crosslinking, so the isocyanate/hydroxyl ratio is not altered; however, the powder should be pre-dried at 60°C for 4 h if stored above 60% relative humidity, and the dispersion should not be aged beyond 48 h at 25°C because solvent evaporation raises viscosity and promotes irreversible agglomerate settling.
Polyamide 66 and polyoxymethylene compounds that use PM-200 as an internal wear modifier are produced on co-rotating twin-screw extruders with an L/D ratio of 40:1 and segmented screw geometry. The UHMWPE powder is dry-blended with pre-dried polymer pellets and 0.2–0.5 wt% antioxidant masterbatch before introduction into zone 1; the processing temperature profile for PA66 is established at 230–260°C, whereas POM requires a narrower window of 170–200°C because thermal depolymerisation becomes significant above 200°C. At addition levels between 5.0 wt% and 15.0 wt% in PA66, PM-200 remains immiscible and does not homogenise into the matrix; the dispersed domains act as solid-lubricant inclusions rather than as a melt-blended thermoplastic component. Extruder torque increases by 5–15% at the upper end of this range, so barrel venting is maintained at -0.08 MPa to remove moisture and low-molecular-weight volatiles. Injection moulding of the compounded pellets is conducted on multi-cavity tools with clamp force typically in the 80–120 t range, using a drying hopper set at 80°C for 4 h before moulding. Mechanical verification includes ISO 527-2:2012 tensile strength, ISO 178:2019 flexural modulus, and ASTM D3702-94(2019) wear factor on a thrust washer machine. In unfilled PA66, tensile strength may decrease by 10–20% at 15 wt% loading, while notched Charpy impact under ISO 179-1:2010 can show a similar directional shift; the compensating benefit is a reduction in dynamic friction and wear rate by approximately 30–50%, though published data for this specific configuration is limited and actual values depend on glass-fibre content, mould temperature, and counterface roughness. Terminal parts include window regulator pulleys, seat track slide blocks, office printer gears, and conveyor chain guides that must operate without external grease or oil. This last requirement is particularly relevant in automotive sensors and paper-path components where silicone migration from mould-release agents must be avoided. The main processing boundary is moisture: PA66 must be pre-dried to below 0.1% moisture before compounding to prevent hydrolysis at the 230–260°C barrel temperatures. For POM, the compounder must avoid residence times beyond 8–12 min at melt temperature, because the combined effect of high shear and PM-200’s low thermal conductivity can create local hot spots and depolymerisation if the screw speed is raised above 400 rpm.
On continuous extrusion lines for EPDM dense seals and glass run channels, a stable coefficient of friction reduction is obtained by adding MIPELON PM-200 in the internal mixer before carbon black and oil are fully incorporated, not in a late let-down stage. The dosage range used in production is 5–10 phr on the elastomer; below 5 phr, the reduction in abrasion loss under ISO 4649:2017 is usually less than 15%, while above 10 phr, tensile strength and elongation at break may decline and thin lip sections become difficult to extrude cleanly. Mixing is carried out in a tangential internal mixer with a fill factor of 0.75–0.85 and a batch temperature not exceeding 110°C before the sulphur donor cure system is added in the second pass. PM-200 is an inert semi-crystalline powder with a melting point near 135°C; it does not participate in sulphur vulcanisation or peroxide crosslinking, so it remains as dispersed domains in the cured EPDM matrix. Extrusion of the final strip profile uses a cold-feed vented extruder with a head temperature profile of 50–90°C; die swell at 5–7 phr PM-200 is only mildly changed, but the final cross-section must be verified with a 10× optical comparator because the particles can slightly reduce the sharpness of fine lip edges. Friction testing by ASTM D1894-14 shows kinetic coefficient values of 0.10–0.20 against glass and painted steel. Compression set remains within OEM limits when measured by ASTM D395-18 Method B for 22 h at 70°C; hardness measured by ASTM D2240-15 typically falls in the 55–65 Shore A range. Terminal products are door seals, trunk weatherstrips, window channels, and HVAC flap seals. The primary operational boundary is dispersion temperature: if the batch exceeds 120°C before sufficient shear has been applied, the powder particles can deform and lose the spherical geometry that contributes to slip. No silane coupling is required, and PM-200 does not interact with amine-based accelerators; however, the two-stage mixing sequence should keep the powder separate from high-temperature accelerator masterbatch until the second pass to avoid localised cure-rate variation.
PM-200 is incorporated into epoxy-polyester and polyester-HAA powder coatings at 0.5–3.0 wt% of the total powder mass to raise mar resistance on appliance cabinets and office furniture without using amide waxes that can plate out on the extruder screw. The premix is prepared in a high-intensity mixer running at 1500–2000 rpm for 3–5 min; the powder is then melt-mixed in a twin-screw extruder with zone temperatures held at 90–110°C, which is below the 135°C onset of UHMWPE flow and allows the particles to remain as discrete inclusions within the binder. After cooling and air-jet milling to a target D50 of 35–45 μm, the powder is applied by corona or tribo electrostatic spray. The gel cure cycle is 180°C for 12–15 min or 200°C for 10 min, depending on the carboxyl-terminated polyester ratio and the accelerator package. At addition levels above 3.0 wt%, the cured surface develops an orange-peel texture and a measurable reduction in pencil hardness under ISO 15184:2020; impact resistance measured by ASTM D2794-93(2019) may also decline because continuous UHMWPE domains act as stress concentrators under rapid deformation. Acceptance testing uses ASTM D4060-19 for abrasion resistance, ASTM D523-14 for 60° gloss, and ASTM D3359-23 for adhesion to zinc-phosphated steel. Terminal articles are appliance side panels, metal shelving frames, and office furniture components that require scuff resistance during handling and shipping. Because powder coatings are cured above 180°C, PM-200 particles can partially soften and flatten at the film surface; therefore, formulations for glossy black finishes should target the lower end of the dosage range, while textured low-gloss systems can operate near the 3.0 wt% boundary. Moisture exposure of the premix is controlled to 0.5% maximum before extrusion; pre-drying at 60°C for 2 h is applied if the powder has been stored at relative humidity above 60%. Regulatory screening for appliance applications is typically performed against EU RoHS Directive 2011/65/EU Annex II as amended by (EU) 2015/863, and the final paint film must be approved against the appliance manufacturer’s food-contact or cosmetic-contact specification where applicable.
In lithium 12-hydroxy stearate thickened greases produced in 1,000–3,000 kg contactor kettles, PM-200 is added to the cooled base-oil-thickener dispersion at 2–8 wt% after saponification and before final homogenisation. The production process requires a high-shear recirculation step with a toothed stator-rotor mill operating at 3,000–5,000 rpm; the mixture temperature is maintained below 80°C to prevent swelling of the UHMWPE particles in the base oil. If the addition is made earlier, at saponification temperatures above 90°C, the low-density powder tends to float and become entrained in the vapour phase, causing batch-to-batch variation in the final NLGI grade. The role of PM-200 is not to replace the lithium thickener network but to reduce sliding friction in boundary lubrication conditions; four-ball wear screening is performed in accordance with ASTM D2266-01(2015) at 400 N load, 75°C, and 60 min duration, although published data for this specific configuration is limited, so formulators should map the change in cone penetration and oil separation after the addition. Penetration is recorded as 265–295 0.1 mm after 60 strokes using ASTM D217-21a, and weld load is screened by DIN 51350-2. Terminal product types are low-speed sliding bearings, open gear lubricants, automotive door check mechanisms, and seat slide rails. The primary operational boundary is high-speed rolling-element bearing service above 3000 rpm, where shear heating can raise the grease temperature beyond 100°C and cause low-density UHMWPE particles to separate, reducing load-carrying capacity and increasing oil bleed. The product is not a substitute for extreme-pressure additives such as sulphurised olefins or phosphorus-based anti-wear agents, and the formulation must be validated against the bearing manufacturer’s salt-spray and fretting corrosion tests before release.
Bonded anti-friction coatings for threaded fasteners and industrial slide rails utilise PM-200 at 5–15 wt% of the dry film mass in a phenoxy or epoxy resin carrier to prevent stick-slip and reduce torque-tension scatter on zinc-plated fasteners. The downstream process consists of dissolving the resin in methyl ethyl ketone, dispersing the UHMWPE powder with a high-speed dissolver at 10–15 m/s, and spray-applying the coating through a 0.8–1.2 mm nozzle at 2.5–4.0 bar air pressure. Coated parts are cured at 180–200°C for 15–20 min; at these temperatures PM-200 softens but does not flow, so the cured film retains a particle-textured surface rather than developing a continuous gloss film. Fastener torque-tension testing is conducted in accordance with ISO 16047:2005, and the kinematic coefficient of friction of the coated surface is measured by ASTM D1894-14. Terminal articles include automotive engine fasteners, seat frame bolts, industrial slide rails, and locking hinges. The coating must not be applied as a full-film bearing surface without a resin binder because PM-200 is not a film former; at loadings above 15 wt%, adhesion under ASTM D3359-23 declines and the dried film becomes excessively friable under shear. The system is incompatible with strong alkaline cleaning baths above 80°C because the phenoxy resin binder can soften, and the coating should not be specified for surfaces that require continuous immersion in strong solvents such as methylene chloride or N-methyl-2-pyrrolidone. Batch uniformity is monitored by evaluating solids content at 125°C for 1 h and by measuring the viscosity of the ready-to-spray dispersion at 25°C, which is typically controlled within the 40–90 s Ford #4 cup range to maintain consistent dry film build with minimal particle settling.
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