| Код ТН ВЭД | 478664 |
Как аккредитованный Mitsubishi ROLASERIT PP01 PP01 3D Printing Powder завод, мы соблюдаем строгие протоколы качества - каждая партия подвергается строгим испытаниям для обеспечения последовательных стандартов эффективности и безопасности.
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In automotive low-pressure fluid-carrying components, PP01 powder is processed where the requirement is not high-temperature stability but rather density reduction, resistance to washer fluid, coolant splash, and continuous vibration. The semi-crystalline polypropylene matrix provides a part density near 0.90 g/cm³ after laser sintering, which reduces unsprung mass in bracket structures and allows larger wall sections without exceeding mass targets. Because PP01 is not a polyamide or polyketone powder, the powder bed temperature is maintained in the lower 100–120 °C band during building, and the high recrystallization enthalpy of polypropylene imposes a controlled cooldown rate of 0.5–1.0 °C/min in the build cake to limit anisotropic shrinkage and edge lift on flat sealing flanges. Production trials on polymer powder bed fusion systems with a 30 W CO₂ laser operating at 10.6 µm wavelength indicate that thin ribs and bosses below 1.2 mm require contour scan duplication because PP01 has lower laser absorption than PA12 powders and can exhibit shallow interlayer fusion when energy density is transferred too rapidly through the melt pool. Industry compliance verification for this downstream segment references REACH Regulation (EC) No 1907/2006, RoHS Directive 2011/65/EU, and ASTM D543-21 for chemical resistance after immersion in automotive service fluids; flammability behavior is separately assessed under ISO 3795:1989 because unfilled polypropylene burns horizontally and must be validated when interior cabin placement is intended. The powder blend ratio on a production line starts at 45–55 wt% virgin PP01 with the balance composed of same-source reclaimed powder sieved to 150 µm; when the part design includes internal channels or snap-fit tabs, the reclaimed content is reduced to 40 wt% maximum to preserve elongation at break. Pre-drying at 80 °C for 4 h in a desiccant dryer is implemented when powder exposure exceeds 60% RH for more than 24 h, even though polypropylene water uptake is typically below 0.03% by mass after 24 h immersion at 23 °C, because surface moisture interferes with electrostatic powder spreading. Downstream production includes powder blending, sieving, build preparation with voxel compensation for shrinkage, laser sintering, in-cake cooling, breakout, residual powder removal from internal gallery sections using compressed air and ultrasonic cleaning, and final dimensional inspection with optical measurement systems. Terminal finished product types include windshield washer fluid reservoirs, pump mounting brackets, duct end connections, and low-pressure ventilation housings; pressurization is generally limited to below 0.5 bar because the sintered wall porosity and interlayer fusion boundaries differ from injection-moulded PP pipe.
The fatigue behavior of a laser-sintered PP01 living hinge is governed not by the bulk tensile yield behavior of the powder alone, but by the orientation of the hinge axis relative to the build plane and by the number of contour scans fused across the hinge root. When the hinge axis is aligned parallel to the blade plane, repeated flexing applies tensile stress perpendicular to interlayer fusion lines, which can initiate microcracks at residual particle boundaries long before bulk yield is reached; the preferred build orientation therefore places the hinge axis at 45–90° to the primary scan direction to interrupt continuous interlayer crack growth. Compliance for mechanical validation uses ISO 178:2019 for flexural modulus, ASTM D638-14 for tensile yield stress and elongation at break, and ASTM D7774-22 for flexural fatigue life under displacement-controlled cycling. Fatigue tests on thin sintered sections show that hinge thickness below 0.8 mm produces an unacceptable scatter in cycle count because partially fused powder particles at the neutral axis act as stress concentration sites that do not exist in injection-compounded polypropylene with oriented molecular chains. The powder blend ratio for hinge-bearing components is set at 100 wt% virgin PP01 for first-article production and at ≤30 wt% recycled PP01 after validation, because the contaminant-rich recycled fraction increases microvoid density at hinge roots and reduces the number of cycles to first visible whitening. Downstream processing uses a layer thickness of 0.10 mm, at least 2 contour passes per layer at the hinge root, and a reduced fill scan spacing on the hinge shoulders to promote local polymer coalescence; after unpacking, the hinge root is not blasted with angular ceramic media, which would notch the surface, but is cleaned with glass bead peening at 0.2–0.4 MPa followed by a controlled flex cycle of 20–50 cycles to relax residual stress. Terminal finished product types include snap-fit enclosure lids, folding crate segments, cable carrier chain links, and reusable packaging clip closures where continued flexing at low strain is required; these components are not intended for continuous load-bearing hinges in industrial machinery without mechanical fasteners because the fatigue margin of sintered PP01 under high cycle counts has not been demonstrated at the same level as injection-moulded oriented PP hinge grades.
Semicrystalline PP01 components used in industrial fluid manifolds exhibit resistance to aqueous acids, dilute alkalis, saline brines, and some polar solvents under continuous immersion at 23 °C, but the same parts can develop environmental stress cracking in contact with ketones, chlorinated solvents, strong oxidizing acids, and aromatic hydrocarbons at elevated temperature. The technical distinction between PP01 and glass-filled PP injection grades is that sintered PP01 contains interparticle fusion boundaries that can act as preferential permeation paths when wall sections are below 2.5 mm; therefore manifolds are designed with minimum wall stock of 3.0 mm where sustained hydrostatic pressure is applied. Industry compliance for this segment is anchored to ASTM D543-21 for chemical resistance after immersion, ISO 175:2010 for long-term fluid exposure, ASTM D1598-23 for time-to-failure under constant internal pressure, and ISO 9080:2012 where the component is intended to be fitted into a thermoplastic pipe network; final pressure testing is driven by the specific system design code, but a common production gate is a 1.5× maximum working pressure hold for 30 min with no visible weeping at fusion lines. The powder blend ratio for chemical-contact manifolds is maintained at 40–50 wt% virgin PP01 with the remaining fraction from one-cycle reclaimed powder, and the reclaimed powder is rejected after 2 processing cycles because the increased melt flow rate and particle size distribution shift produce porosity that compromises hydrostatic integrity. Downstream production of a fluid manifold from PP01 involves building the part with internal bores no smaller than 3 mm unless secondary drilling is performed, because residual unsintered powder is difficult to evacuate from narrow internal galleries; after the build is cooled, powder is removed by combination of vacuum, compressed deionized air, and ultrasonic bath treatment. The manifold is then hydrostatically tested, dried in a forced-air oven at 60 °C for 2 h, and inspected by optical borescope for internal fusion defects. Terminal finished product types include reagent distribution manifolds, low-pressure drain traps, electroplating bath flow guides, and chemical dosing adaptors for environments that are chemically compatible with polypropylene and do not exceed continuous service temperatures approaching 80 °C; manifold applications with strong oxidizers, chlorinated solvents, or sustained pressure above 1.0 bar are outside the demonstrated operational boundary for sintered PP01 without additional sealing and reinforcement.
| Validation target | Standard designation | Specific test condition |
|---|---|---|
| Chemical resistance | ASTM D543-21 | Immersion in 10% aqueous reagent at 23 °C for 48 h; retained tensile elongation recorded |
| Flexural modulus | ISO 178:2019 | Conditioned at 23 °C and 50% RH prior to three-point bending |
| Tensile yield stress | ASTM D638-14 | Type IV specimen, testing speed 50 mm/min |
| Hydrostatic pressure | ASTM D1598-23 | Sustained pressure at 1.5× maximum working pressure for 30 min |
Patient-specific external orthotic shells and prosthetic socket check sockets are produced from PP01 where the design objective is a lightweight, moisture-tolerant, and chemical-resistant device that can be iteratively modified without investing in injection tooling. The powder bed fusion route allows a clinician-captured limb scan to be converted into a shell with variable wall thickness, but the fused part remains a sintered polyolefin with porosity at interparticle boundaries, and therefore PP01 is not used as an implantable or long-term mucosal contact material without additional validation. PP01 as supplied is not a USP Class VI certified resin; final devices require finished-device biocompatibility testing under ISO 10993-1:2018 for evaluation planning, ISO 10993-5:2009 for cytotoxicity, and ISO 10993-10:2021 for skin sensitization. Manufacturing quality is governed by ISO 13485:2016 for medical device quality management, and the device may fall under EU MDR 2017/745 as a Class I external orthosis or custom-made device depending on the intended clinical use. The powder blend ratio for all patient-contact builds is set at 100 wt% virgin PP01; recycled powder is not introduced into the same build because the biocompatibility validation would be invalidated by uncontrolled contamination from previously processed industrial lots. Downstream production for an orthotic shell from PP01 begins with laser sintering at 0.10 mm layer thickness, followed by slow in-cake cooling to minimize distortion across the large thin cross-sections typical of brace geometries. After breakout, residual powder is removed by medical-grade compressed air and isopropyl alcohol cleaning, followed by vacuum drying at 45 °C for 2 h to reduce surface residues; no solvent-based smoothing or coating is applied unless the coating itself has completed a separate biocompatibility assessment. Terminal finished product types include ankle-foot orthosis outer shells, orthotic insole base plates, prosthetic socket check sockets used during fitting, and custom interface frames for external rehabilitation devices; these products are limited to external use and are not validated for continuous skin exposure under moisture without a separate liner system.
When PP01 powder is reintroduced into subsequent builds after being exposed to elevated powder bed temperatures near the melting onset for prolonged periods, oxidative chain scission and fines generation alter both the melt flow index and the particle size distribution of the reclaimed fraction. This is not a linear degradation process; operators on production laser sintering platforms observe batch-to-batch variance where the first recycle cycle often retains acceptable coalescence, but the second and third cycles can produce a sudden drop in tensile elongation and an increase in warpage because the lower-molecular-weight fraction reduces melt strength during cooling. The acceptance gate for reclaimed PP01 is therefore defined by ISO 1133-1:2022 for melt flow rate under 230 °C and 2.16 kg load, ISO 13320:2020 for laser diffraction particle size measurement, and ISO 3451-1:2019 for ash content as an indicator of contamination. A stable production blend begins at 50 wt% fresh PP01 and 50 wt% once-reclaimed PP01 after sieving through 150 µm mesh; when the once-reclaimed powder shows an MFR drift greater than 15% relative to the virgin lot reference, the reclaimed content is reduced to 30 wt%, and when the twice-reclaimed powder remains outside that limit, the lot is discarded from sintering use. Published data for PP01-specific long-term recyclate aging is limited, and the above limits represent production gate criteria rather than supplier-issued absolute values. Downstream production of recycled PP01 parts requires in-line sieving after every build, moisture control at <0.05% by mass, and pre-drying at 80 °C for 4 h when the powder has been stored in unsealed containers near process heat. The laser sintering parameters are held constant from the virgin baseline for the first recycle cycle, but the recycled blend is inspected more frequently at the build periphery where warpage and curl appear first; if curl exceeds 0.3 mm over a 100 mm span, the recycle fraction is reduced or the powder is returned to the supplier for reconditioning. Terminal finished product types made from recycled PP01 blends are restricted to non-critical jigs, bin dividers, shop-floor trays, gauge housings, and packaging fixtures where a slight reduction in elongation does not create a safety or compliance risk; recycled PP01 is not routed into medical, fluid-pressure, or fatigue-sensitive components.
| Powder state | Test method | Acceptance limit |
|---|---|---|
| Virgin reference lot | ISO 1133-1:2022 | MFR deviation ≤10% from supplier certificate |
| Once-reclaimed PP01 | ISO 13320:2020 | Volume-median D50 ≤90 µm and D90 ≤180 µm |
| Twice-reclaimed PP01 | ISO 1133-1:2022 | MFR drift ≤15% relative to virgin reference; discard if exceeded |
In low-mass aerial vehicle applications, PP01 is selected for brackets and sensor mounts where density reduction is coupled with sufficient elongation to avoid crack propagation at threaded insert bosses under propeller-induced vibration. The failure mode that dominates this downstream segment is not monotonic overloading but high-cycle vibration fatigue at small strain amplitudes, so the part design includes increased fillet radii, thicker boss walls, and metal insert retention features that distribute stress over a larger sintered area. Compliance for mechanical acceptance references ISO 527-2:2012 for tensile properties of moulded and extruded plastic specimens, ASTM D256-23 for notched Izod impact, and UL 94 for flammability classification; the unfilled polypropylene powder is typically expected to fall into the HB classification, and a formal flame rating must be generated for each final geometry because wall thickness and residual powder influence the result. The powder blend ratio for drone brackets is held at 60 wt% virgin PP01 and 40 wt% once-reclaimed PP01 when the bracket is non-load-bearing, but load-path components such as motor mounts use 100 wt% virgin PP01 because the dynamic load environment cannot tolerate recycle-related microvoids. Downstream production includes laser sintering at 0.12 mm layer thickness with extra contour passes around threaded insert pockets, followed by slow cooling, bead blasting with spherical glass media, and ultrasonic insertion of brass inserts at 20 kHz after the hole has been reamed to the insert manufacturer’s recommended interference diameter. The final bracket is inspected for insert pull-out force using a tensile tester with a crosshead speed of 5 mm/min, and parts are rejected if the insert rotates before the minimum pull-out threshold established from the design specification. Terminal finished product types include antenna brackets, sensor array mounts, wire routing guides, and camera gimbal isolation frames where the PP01 part acts as a vibration-damped adapter between a stiffer carbon-fiber airframe member and the electronic assembly; motor mounts with direct propeller load transfer are not produced from unreinforced PP01 unless the design has been validated specifically for the expected axial and radial forces.
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Mitsubishi ROLASERIT PP01 PP01 3D Printing Powder is a polypropylene-based powder feedstock supplied for powder bed fusion additive manufacturing, typically charged to selective laser sintering systems with open parameter control. The PP01 grade is supplied as a controlled particle population intended to provide uniform recoating at layer thicknesses between 0.10 mm and 0.15 mm. The powder is used as a lower-density alternative to polyamide 12 feedstocks in jigs, fixtures, ducting, and fluid-contact housings where polypropylene's non-polar backbone provides resistance to aqueous acids, alkalis, and polar solvents. Unlike extrusion-grade polypropylene pellets or mechanically ground polypropylene powder, ROLASERIT PP01 is supplied with controlled particle size distribution and morphology for laser sintering; these characteristics influence powder flow, recoating flatness, and the density of the sintered part. The product identity should be confirmed against the supplier certificate of analysis because particle size, melt behaviour, and apparent density vary by production batch.
Apparent density of the powder is typically reported in the range of 0.42 g/cm³ to 0.48 g/cm³ under ISO 60:1977, and the median particle size D50 is approximately 55 µm by laser diffraction under ISO 13320:2020. Melt peak temperature of the powder is near 140 °C when measured by differential scanning calorimetry according to ISO 11357-3:2018. These values are supplier-typical and must be verified against the batch-specific certificate of analysis before process parameters are locked. The powder should be stored in sealed conductive containers below 60 % relative humidity and away from direct ultraviolet exposure. Although equilibrium moisture uptake of polypropylene is low, surface-static clustering is a documented handling bottleneck on polyolefin powders; ionizing bars, grounded hoppers, and conductive vacuum lines reduce electrostatic clustering during transfer. When containers are opened outside sealed hoppers at relative humidity above 60 %, the powder should be dried in a desiccant or vacuum dryer at 80 °C for 4 h to 6 h before loading to reduce flow irregularities and recover consistent apparent density after transport.
Powder aging in polypropylene laser sintering is governed by thermo-oxidative chain scission during repeated high-temperature exposure. Recycling should include sieving at 125 µm followed by apparent density and melt flow rate checks to detect accumulated fines or degraded fractions. A refresh ratio of 30 % to 50 % virgin powder is commonly required to maintain tensile elongation within 15 % of virgin values; this should be validated on the installed machine because chamber temperature uniformity and laser energy density change degradation kinetics.
On open-architecture SLS systems fitted with 30 W CO₂ lasers, initial screening for ROLASERIT PP01 is conducted at laser powers of 15 W to 20 W, scan speeds of 6 m/s to 8 m/s, hatch spacings of 0.10 mm to 0.12 mm, and layer thicknesses of 0.10 mm to 0.15 mm. These combinations produce areal energy densities near 0.020 J/mm² to 0.033 J/mm² and volumetric energy densities of approximately 0.15 J/mm³ to 0.25 J/mm³. The build chamber setpoint is maintained between 95 °C and 110 °C, with the feed bed held 5 °C to 10 °C below the build bed to limit agglomeration. Narrow thermal control is required because the difference between the powder-bed preheating temperature and the melt peak of PP01 is smaller than that of PA12; deviations above the upper setpoint produce part growth and powder caking, while deviations below produce curl and layer delamination. Machine-specific laser spot diameter, beam quality, and chamber thermal uniformity change the effective melt-pool size, so these parameters require validation on the installed system.Mechanical testing should be performed on specimens built in both XY and Z orientations because powder bed fusion parts are anisotropic. The values in the table reflect XY-oriented specimens printed with optimized energy density and subsequently conditioned at 23 °C and 50 % relative humidity for 48 h before testing. Z-direction tensile strength and elongation are typically 30 % to 50 % lower than XY-direction values for polypropylene laser sintering due to interlayer diffusion limitations; the exact reduction depends on layer thickness, scan strategy, and powder refresh ratio. The supplier's public datasheet does not provide full fatigue, creep, or UV aging datasets for this specific configuration, so cyclic and sustained-load applications require in-house testing under ASTM D2990 or ISO 527-1 creep protocols.
| Property | Test method | Unit | Typical value | Condition |
|---|---|---|---|---|
| Apparent density | ISO 60:1977 | g/cm³ | 0.45 | As-poured powder |
| Median particle size D50 | ISO 13320:2020 | µm | 55 | Laser diffraction |
| Melt peak temperature | ISO 11357-3:2018 | °C | 140 | Second heating |
| Sintered part density | ISO 1183-1:2019 | g/cm³ | 0.90 | 23 °C |
| Tensile strength, XY | ISO 527-1/-2:2012 | MPa | 24 | 50 mm/min |
| Tensile modulus, XY | ISO 527-1/-2:2012 | MPa | 1300 | 1 mm/min |
| Elongation at break, XY | ISO 527-1/-2:2012 | % | 28 | 50 mm/min |
| Flexural modulus | ISO 178:2019 | MPa | 1000 | 2 mm/min |
| Charpy notched impact | ISO 179-1/1eA:2010 | kJ/m² | 4.5 | 23 °C |
Because polypropylene has a non-polar backbone, sintered PP01 parts exhibit low equilibrium moisture uptake and do not undergo hydrolysis when exposed to aqueous acids and alkalis at ambient temperature. This behaviour makes PP01 a candidate for jigs, fixtures, and fluid-contact housings in wet processing lines, provided the temperature remains below the heat deflection temperature of the material. Continuous exposure to strong oxidising acids, aromatic hydrocarbons, or chlorinated solvents should be avoided; polypropylene swells in aliphatic and aromatic hydrocarbon environments, and the degree of swell depends on the specific solvent and stress state. For outdoor use, UV stabilisation is not supplied by the sintering process itself; parts should be painted or protected from direct sunlight unless the end user has validated UV weathering according to ISO 4892-2 or ASTM G154.
Chemical resistance should be verified on sintered test coupons, not assumed from injection-moulded polypropylene data, because porosity and interlayer boundaries influence permeation and stress cracking. Immersion testing under ASTM D543-20 or ISO 175:2010 is appropriate for screening. The low moisture absorption also reduces dimensional change in humid environments relative to PA12, but the lower thermal stability of polypropylene limits continuous service at elevated temperatures compared with polyamide powders.
ROLASERIT PP01 differs from polyamide 12 feedstocks primarily in density, thermal profile, mechanical stiffness, and chemical resistance. The lower density of PP01 reduces part mass at equivalent volume, while the lower melt peak permits lower build chamber setpoints and lower heat input. These differences require adjustment of powder bed temperature, laser energy density, and powder refresh ratio on existing equipment. PA12 offers higher tensile strength and stiffness, while PP01 offers lower moisture absorption and better resistance to polar chemicals. Substitution is therefore not a direct material swap; process development must be repeated on the target machine.
| Property | Test method | ROLASERIT PP01 | PA12 PBF feedstock | Practical consequence |
|---|---|---|---|---|
| Density | ISO 1183-1:2019 | 0.90 g/cm³ | 1.01 g/cm³ | Lower part mass with PP01 |
| Water absorption, 24 h | ISO 62:2008 | <0.05 % | 0.5 %–1.0 % | PP01 more dimensionally stable in humid conditions |
| Melt peak | ISO 11357-3:2018 | 140 °C | 176 °C–180 °C | PP01 requires lower build chamber temperature |
| Tensile strength, XY | ISO 527-1/-2:2012 | 24 MPa | 45 MPa–50 MPa | PA12 higher load-bearing capacity |
| Tensile modulus | ISO 527-1/-2:2012 | 1300 MPa | 1500 MPa–1800 MPa | PA12 slightly stiffer |
| Elongation at break, XY | ISO 527-1/-2:2012 | 28 % | 15 %–30 % | PP01 comparable in XY ductility |
| Resistance to polar solvents | ASTM D543-20 | High | Moderate | PP01 better for acid and base contact |