Products

Lubrizol ESTANE M88A-565 OR UV PW TPU for 3D Printing

    • Product Name: Lubrizol ESTANE M88A-565 OR UV PW TPU for 3D Printing
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 471468
    Materialtype Thermoplastic Polyurethane (TPU)
    Form Powder
    Color White
    Shoreahardness 88 A
    Density 1.18 g/cm³
    Bulkdensity 0.55 g/cm³
    Particlesized50 60 µm
    Tensilestrength 30 MPa
    Elongationatbreak 450%
    Tearstrength 80 kN/m
    Vicatsofteningtemperature 80 °C
    Uvstabilization Yes
    Processingtechnology Powder Bed Fusion / 3D Printing
    Abrasionresistance 30 mm³

    As an accredited Lubrizol ESTANE M88A-565 OR UV PW TPU for 3D Printing factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Packaging: 25 kg moisture-barrier foil bags, palletized, clearly labeled, protecting Lubrizol ESTANE M88A-565 OR UV PW TPU for 3D printing.
    Container Loading (20′ FCL) Container Loading (20′ FCL): Lubrizol ESTANE M88A-565 OR UV PW TPU for 3D Printing, palletized, shrink-wrapped, strapped, and evenly distributed for ocean transport.
    Shipping Lubrizol ESTANE M88A-565 OR UV PW TPU for 3D Printing ships as a non-hazardous thermoplastic polyurethane powder/resin. Pack in sealed, moisture-barrier bags or drums. Store and transport at ambient temperature, avoiding moisture, heat, and direct sunlight. Not regulated for transport unless SDS states otherwise; use standard freight.
    Storage Store Lubrizol ESTANE M88A-565 OR UV PW TPU in original packaging in a cool, dry, well-ventilated area, away from direct sunlight, heat, sparks, and open flames. Keep containers tightly sealed to prevent moisture absorption and contamination. Protect from UV exposure. Maintain 15–30°C, avoid strong oxidizers, and keep away from incompatible materials. Dry before 3D printing if moisture-exposed.
    Shelf Life Shelf life: typically 24 months when stored in original, unopened packaging in a cool, dry place, away from sunlight and moisture.
    Application of Lubrizol ESTANE M88A-565 OR UV PW TPU for 3D Printing
    In powder-bed fusion work cells producing outdoor athletic footwear midsole lattices, the UV-stabilized powder is charged without a secondary antioxidant masterbatch because the grade is supplied as a ready-to-process formulation. The formulation addition ratio therefore refers not to compounding but to the working mixture of virgin powder and sieved overflow recovered from the build. Production sites typically maintain a fresh-to-recovered ratio of 80:20 for visible midsole surfaces and 60:40 for interior lattice struts where slight surface texture variation is acceptable. When recovered powder exceeds 40 wt%, downskin surfaces develop orange-peel morphology and z-axis tensile elongation in thin-walled struts may fall below 150% after the recovered fraction carries thermal history from previous builds. Compliance for the finished footwear component is evaluated under ISO 20344:2021 for whole-shoe assessment and ISO 17707:2005 for flexing endurance; specimens are conditioned at 23±2 °C and 50±5 % RH for at least 48 h before testing. The downstream process builds midsoles on laser-based powder bed fusion or inkjet fusing systems with layer thickness controlled at 0.08–0.12 mm; the build chamber is held at a temperature derived from differential scanning calorimetry, generally 25–35 °C below the melting onset of the Shore 88A grade, adjusting for ambient humidity and part cross-section. After cool-down under nitrogen, the parts are de-powdered, bead-blasted with 60–120 µm glass microspheres, and inspected for residual porosity and partially fused surface particles. Terminal product types include UV-exposed midsole lattice cores, rebound pods, and heel counter plugs for trail shoes where brand-level flex targets commonly exceed 30,000 flex cycles before visible crack initiation.

    When Sintered Orthotic Shells Are Subjected to ISO 10993-5 Cytotoxicity Limits

    Custom ankle-foot orthosis shells and prosthetic test sockets produced from the powder require traceable virgin material because recoverable overflow powder can carry extractable residues from previous non-medical builds and from progressive thermal degradation. The working ratio is therefore set at 100:0 virgin powder for skin-contacting Class I devices, or 90:10 virgin-to-recovered powder only when the recovered fraction is segregated by material lot, sieved at 150 µm, and documented under ISO 13485:2016 batch traceability. Addition of processing aids such as fumed silica flow agents is not recommended above 0.05 wt% because leachable silicon oxide particles may shift cytotoxicity assay results. Compliance follows ISO 10993-1:2018 biological evaluation planning, with extraction performed according to ISO 10993-12:2021, cytotoxicity assessed by ISO 10993-5:2009, and skin sensitization by ISO 10993-10:2013. The downstream production process uses nitrogen-inerted powder bed fusion with oxygen concentration maintained below 3%; powder is dried in a vacuum oven at 70–80 °C until moisture measured by ISO 15512:2016 falls below 0.05% by mass. Build orientation is chosen to align the ankle joint axis with the y-direction of the build, and layer thickness remains at 0.10 mm to reduce stair-step edges on the orthotic shell. Post-processing avoids solvent smoothing because volatile solvents can be retained in the cellular surface and change extraction profiles; surfaces are cleaned with filtered compressed air and, where necessary, wiped with 70% isopropanol followed by vacuum drying at 40 °C for 4 h. Terminal product types include paediatric lower-limb orthoses, spinal brace liner pads, and prosthetic check sockets. Steam autoclaving above 121 °C is outside the operational boundary; repeated wet-heat sterilization may accelerate hydrolysis and reduce tensile elongation to failure.Sintered TPU gaskets for outdoor power distribution enclosures impose a narrow processing window because the part must seal against water ingress at IP65 while retaining compression set after long-term altitude and UV exposure. The formulation addition ratio in continuous powder-bed service production is held between 70:30 and 60:40 virgin-to-recovered powder by mass; recovered powder is sieved below 150 µm, and mixed in a low-shear tumbler to preserve particle size distribution. No plasticizer or internal mold release is added at the machine; the UV-stabilized powder is used as supplied, and the addition of external flow aids above 0.1 wt% is avoided because fine-particle segregation creates powder bed density gradients that manifest as sealing face porosity. Compliance for the finished gasket assembly references IEC 60529:1989 for ingress protection, UL 94 HB for flammability classification of non-structural sealing components, RoHS 2011/65/EU for restricted substance documentation, and ISO 37:2017 for tensile stress-strain property retention after aging. The downstream process is inkjet-based powder bed fusion, with the build chamber held at an oxygen concentration below 3% and a surface preheat controlled to within ±2 °C of the lot-specific melting onset offset. Gasket wall sections below 1.0 mm require a fusing energy density increase of 3–5% over the thick-wall setpoint to maintain interlayer coalescence; above 2.5 mm, the energy density is reduced to avoid overfusing and z-axis expansion of 0.4–0.6%. After unpacking, gaskets are annealed at 80 °C for 4 h in a forced-air oven to relieve residual stress, then compressed at 25% deflection for 24 h to verify recovery to at least 90% of original thickness before release. Terminal product types include outdoor enclosure compression seals, cable entry grommets, ventilation plug bodies, and dust boot collars.
    Downstream scenarioCompliance referenceTest method or clauseProcess variable controlled
    Outdoor athletic footwear midsole latticeISO 20344:2021, ISO 17707:2005whole-shoe flexing, bond strengthpowder refresh ratio, layer thickness
    Orthotic shell and prosthetic check socketISO 10993-1:2018, ISO 10993-5:2009, ISO 10993-10:2013extraction, cytotoxicity, skin sensitizationvirgin powder segregation, oxygen level
    Outdoor enclosure gasketIEC 60529:1989, UL 94 HB, RoHS 2011/65/EUIP sealing, flammability, restricted substancespost-sintering porosity, wall thickness
    Automotive cabin prototypeFMVSS 302, VDA 278:2011, REACHburn rate, VOC/FOG, SVHC documentationdrying, fusing energy, post-process bake-out
    Sports protective lattice linerASTM F1446-20, EN 1621-2:2014headgear impact attenuation, limb protector impactlattice cell size, strut diameter
    Industrial dust cover and bellowsISO 9001:2015, RoHS 2011/65/EUprocess capability, substance declarationsfresh powder ratio, sieve cut

    Does Long-Wave UV Exposure Alter Retention of Shore A 88 in Automotive Cabin Prototypes?

    Automotive cabin prototype parts such as flexible HVAC bellows, harness grommets, and trim-dummy components are produced from the UV-stabilized powder to evaluate long-wave filtered sunlight and cabin heat without painted skins. The formulation addition ratio is differentiated by part visibility: visible prototypes intended for design review are built from 100% virgin powder to minimize yellowing and surface texture drift, while non-visible functional prototypes use a 70:30 virgin-to-recovered ratio after recovered powder has passed a 150 µm sieve. The stabilizer package reduces oxidative gloss loss under xenon-arc exposure; automotive validation laboratories typically expose parts to 500–750 h cycles under ISO 4892-2:2013 with irradiance and black-standard temperature defined by the OEM test specification. Flammability documentation follows FMVSS 302 for horizontal burn rate of interior materials; volatile organic compound and fogging emissions are assessed by VDA 278:2011, with post-sintering bake-out at 80 °C for 8 h used to reduce retained fusing-agent residues below the OEM reportable threshold. The downstream production process uses powder bed fusion with 0.10 mm layer thickness, then slow cooling in a nitrogen purged chamber to prevent orange-brown discoloration at the surface; any dyeing or flame-retardant surface coating must be qualified for flammability and fogging after application. Terminal product types include HVAC bellows for electric vehicle climate systems, cable bellows and grommets, seat adjustment dust covers, and design review seat trim plugs. Long-wave UV retention is not infinite: after extended xenon arc or Florida exposure, the part may retain Shore A hardness but show measurable surface yellowing when stabilizer depletion occurs at high accumulated radiant energy; lot-to-lot validation under ISO 4582:2017 is required before production release.

    Helmet liner lattice cores and ASTM F1446 conditioning requirements

    Protective sports padding made from the sintered TPU lattice uses the elastomer’s strain-rate response rather than rigid foam energy absorption, which demands strict control of strut diameter and cell topology. The powder is loaded as 100% virgin material for energy-critical helmet liner cores; for non-impact training protectors, a 80:20 virgin-to-recovered blend is permitted only when the recovered powder is from the same material lot and has been sieved below 125 µm. The addition of rigid fillers is avoided because filler particles act as stress risers in thin struts and may reduce tensile elongation at break below 250% in preliminary tests. Compliance for headgear test protocols follows ASTM F1446-20 for conditioning and impact attenuation evaluation, while limb protectors are assessed under EN 1621-2:2014; specimens are conditioned at 23±2 °C and 50±5 % RH for a minimum 48 h before testing. The downstream production process uses laser-based powder bed fusion with a layer thickness of 0.10 mm and a build chamber temperature tuned to maintain a self-supporting lattice without closed-cell ballooning. Lattice design parameters for helmet liners typically specify strut diameters between 2.0 mm and 4.0 mm and cell sizes adjusted to the impact energy level of the target standard; after the build, parts are dry-blasted to remove adherent powder from internal channels, then inspected by micro-computed tomography for closed-cell occlusion. Terminal product types include bicycle helmet liner cores, rib protectors, and knee/elbow impact pads for off-road sports. The operational boundary is defined by attenuation stability after repeated impact: if a strut fractures in a non-designed local buckling mode, the part is rejected because the failure mode cannot be recovered by annealing.

    If Powder Refresh Ratios Drop Below 60:40 in Continuous MJF Production

    Continuous additive manufacturing service production of UV-exposed flexible dust covers, bellows, and vibration isolators is more sensitive to powder refresh ratio than the visible appearance alone suggests. The working mixture is maintained between 80:20 and 60:40 virgin-to-recovered powder by mass; recovered powder is sieved at 150 µm, conditioned to 40–50% RH before blending, and mixed in a low-shear tumble blender for 20 min per production lot. When the recovered fraction exceeds 40 wt%, process operators observe an increase in zero-curl defects and a measurable decline in consolidated surfaces; z-axis dimensional error rises from ±0.2 mm to ±0.5 mm, and thin-section tensile elongation measured by ISO 37:2017 may fall below 150% on wall sections below 1.2 mm. Compliance in this scenario is controlled by ISO 9001:2015 process capability records and RoHS 2011/65/EU documentation; if the parts enter machinery under the EU Machinery Directive, the technical file must include a declaration of the TPU shore hardness and working temperature range. The downstream production process is inkjet-based powder bed fusion; powder bed temperature, fusing energy, and detailing agent density are adjusted for each build because the recycled fraction contains partially oxidized surfaces that alter melt coalescence. At the start of each shift, a validation coupon is built with a 0.10 mm layer thickness and sintered under the same energy profile as production parts; the coupon is tested for Shore A hardness and dimensional accuracy before release of the build queue. Terminal product types include flexible exhaust bellows, equipment dust covers, vibration isolation pads, and custom end-effector sleeves for automated lines. If the fresh powder ratio is not restored above 60:40 after a high-recover production period, the operational boundary is exceeded and the powder bed is discharged or downgraded to non-critical internal tooling.
    Process risk thresholds for continuous powder-bed fusion of UV-stabilized Shore 88A TPU
    ParameterAcceptable rangeFailure thresholdObserved failure mode
    Fresh-to-recovered powder ratio80:20 to 60:40below 60:40zero-curl defects, z-axis drift
    Residual moisture by ISO 15512:2016<0.05%above 0.08%surface craters, interlayer porosity
    Build chamber oxygen<3%above 5%yellowing, tensile retention loss
    Layer thickness0.08–0.12 mmabove 0.12 mmpoor interlayer coalescence
    Build chamber offset below melt onset25–35 °Coffset above 35 °Cpart growth, downskin distortion
    Post-fusion annealing80 °C for 4 habove 100 °C for 8 hcompression set loss, surface discoloration
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    Certification & Compliance
    More Introduction

    The Lubrizol ESTANE M88A-565 OR UV PW TPU is a thermoplastic polyurethane powder supplied for additive manufacturing operations that require a nominal hardness of 88A combined with ultraviolet stabilization. The product designation carries three technical markers: the 88A hardness class, a UV-stabilized additive package, and powder feedstock format suitable for direct powder-bed fusion or subsequent melt compounding into filament. Hardness is confirmed by durometer testing in accordance with ASTM D2240-15. Because the material is supplied as a powder, initial moisture content and particle size distribution are more decisive for process stability than they are for pelletized polyurethane feedstock; a desiccant drying step before melt processing is therefore treated as a mandatory unit operation rather than an optional conditioning step.

    Where grade-specific tensile strength, elongation at break, tear strength, or melt-flow values are required for design calculations, the current manufacturer’s technical data sheet should be used. The values in this document for the general 88A Shore hardness TPU class are drawn from public industrial literature and are not represented as lot-specific certificate data. Published data for this specific configuration is limited; qualification work should include testing on the target additive manufacturing machine with the intended powder reuse ratio.

    What Distinguishes the M88A-565 OR UV Powder from Unstabilised 88A TPU Feedstocks?

    The primary differentiation is the ultraviolet stabilization package. In unstabilized thermoplastic polyurethane exposed to outdoor ultraviolet radiation, urethane segments and polyol backbones undergo photo-oxidative chain scission. The resulting degradation appears as surface chalking, color shift, and loss of tensile elongation before bulk tensile failure. A UV-stabilized formulation such as the OR UV powder is designed to extend the exposure interval before 50% retention of original elongation is reached under accelerated weathering. Comparative evaluation is commonly performed in a fluorescent UV condensation apparatus using ASTM G154-16 Cycle A with UVA-340 lamps and 8 h ultraviolet exposure at 60 °C alternating with 4 h condensation at 50 °C. Published data for this specific configuration is limited; however, UV-stabilized TPU grades generally maintain higher elongation retention and lower ΔE values than unstabilized controls after 500 h to 1000 h of exposure.

    Powder handling differs from pelletized TPU because the high surface area of fine particles accelerates moisture uptake. The powder is typically dried in a desiccant dryer at 80 °C to 90 °C for 3 h to 4 h, with supply air dew point held below −40 °C. Residual moisture above 0.03 wt% as measured by Karl Fischer titration in accordance with ISO 15512:2019 is associated with intermittent filament porosity, diameter fluctuation, and surface defects when the powder is melt-compounded into filament. For direct powder-bed fusion, moisture above 0.08 wt% can contribute to part surface roughness and increased fuming at the melt pool. Sieving with vibratory screens in the 200 mm to 300 mm diameter range is used to remove large agglomerates and maintain flowability before the powder is charged to the build hopper.

    Powder-Bed Fusion of a Shore 88A Urethane Powder

    Processing in powder-bed fusion requires managing the competition between complete interparticle coalescence and thermal degradation. The melting range for 88A Shore hardness TPU powder is commonly observed between 160 °C and 200 °C by differential scanning calorimetry under ISO 11357-3:2018. Build chamber temperatures are normally held below the onset of melt to reduce curling, while the incident energy source supplies the additional enthalpy for full melt. Layer thicknesses in the 100 µm to 150 µm range are common for flexible TPU powders because thicker layers may leave residual porosity and thinner layers increase build time without proportional property gain. Oxygen exposure at the melt surface can lead to yellowing and loss of molecular weight; a nitrogen or reduced-oxygen atmosphere is therefore preferred where the equipment configuration allows it.

    Compared with polyamide-12 powders, this TPU powder requires lower energy input and produces parts with lower tensile modulus and higher elongation. Typical 88A Shore hardness TPU class values for ultimate tensile strength fall between 25 MPa and 35 MPa when tested under ASTM D638-14; elongation at break commonly spans 300% to 600%. These values are orientation-dependent in additive manufacturing because layer-plane interfaces act as stress concentrators. Tensile specimens printed in the z-direction may retain 60% to 80% of xy-plane tensile strength, and the exact retention ratio depends on energy density, powder bed temperature, and powder recycle ratio. The grade-specific datasheet should be consulted for design allowable values.

    When Interlayer Fusion in Fused Filament Fabrication Is Governed by Melt Viscosity

    When the powder is melt-compounded into filament, the processing objective shifts from powder coalescence to controlled melt viscosity at the nozzle inlet and rapid solidification after layer deposition. Production-scale compounding of TPU powders into filament is normally performed on co-rotating twin-screw extruders with 40:1 to 52:1 L/D ratio, using barrel zones from 180 °C to 220 °C. A melt pump at the die stabilizes filament diameter to ±0.05 mm or better as measured by a laser micrometer, which is necessary for consistent feeding in fused filament fabrication. During printing, melt zone temperatures for 88A Shore hardness TPU generally fall between 210 °C and 240 °C, with heated bed settings between 40 °C and 70 °C. Interlayer adhesion is sensitive to print speed, nozzle geometry, and part cooling fan speed; excessive cooling reduces weld line strength, while insufficient cooling allows thin walls to deform under their own weight.

    Against other 3D printing feedstocks, the ESTANE M88A-565 OR UV PW material occupies the flexible segment of the property envelope. Polylactic acid and poly(ethylene terephthalate) glycol have higher tensile moduli, lower elongation at break, and lower abrasion resistance than this TPU class. A 95A or 65D TPU, by contrast, provides higher modulus and lower elastic recovery because the higher hard-segment content restricts chain mobility; the 88A class is generally selected when gasket-like sealing, vibration absorption, or flexural fatigue resistance is required. The powder form with UV stabilization distinguishes the product from unstabilized pelletized TPU used in conventional injection molding, because the additive package and particle size distribution are designed for additive manufacturing rather than for high-shear injection molding.

    The following property matrix represents the general 88A Shore hardness TPU class and is provided for preliminary material screening only. Lot-specific values should be obtained from the manufacturer.

    PropertyTest methodTypical class rangeNotes
    HardnessASTM D2240-1587A–89A15 s delay reading
    Ultimate tensile strengthASTM D638-1425–35 MPaType IV specimen
    Elongation at breakASTM D638-14300–600%Test speed 500 mm/min
    Tear strengthASTM D624-00(2020)80–120 kN/mDie C
    Specific gravityISO 1183-1:20191.10–1.15Method A
    Vicat softening temperatureISO 306:201365–95 °CA50 method

    Regulatory and durability assessment must be anchored to the following test methods. Compliance status should be confirmed with the supplier for the specific production site and target market.

    AssessmentStandard or regulationRelevance
    Ultraviolet weatheringASTM G154-16Monitors ΔE and elongation retention under UVA-340 lamps
    Xenon arc exposureISO 4892-2:2013Records CIELAB color shift and surface chalking
    Moisture determinationISO 15512:2019Karl Fischer titration; target below 0.03 wt% before extrusion
    Melt mass-flow rateISO 1133-1:2022Used for lot release after drying
    Thermal stabilityISO 11358-1:2014Thermogravimetric onset; detects additive-related residue
    Chemical inventoryREACH Regulation (EC) No 1907/2006European chemical registration obligations
    Hazardous substancesRoHS Directive 2011/65/EURestricted substance screening

    For direct powder-bed fusion applications, build orientations should be selected so that tensile loads do not align with the z-axis unless the design includes a safety factor derived from through-thickness tensile data. The powder is hygroscopic and should be stored below 50% relative humidity in sealed containers after drying. Because UV stabilization retards photo-oxidation but does not prevent hydrolytic chain scission, immersion in hot water or prolonged exposure to high humidity above 60% remains an operational boundary.

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