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Proto3000 HP 3D High Reusability Polypropylene (PP) by BASF 3D Printing MultiJet Fusion Polymer

    • Product Name: Proto3000 HP 3D High Reusability Polypropylene (PP) by BASF 3D Printing MultiJet Fusion Polymer
    • 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 674059
    Material Type Polypropylene (PP)
    Manufacturing Technology Multi Jet Fusion (MJF)
    Chemical Resistance Good to acids, bases, alcohols, and oils
    Reusability High, up to 80%

    As an accredited Proto3000 HP 3D High Reusability Polypropylene (PP) by BASF 3D Printing MultiJet Fusion Polymer factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Supplied in a 3 kg sealed, moisture-resistant container with desiccant, labeled for BASF HP MultiJet Fusion PP powder.
    Container Loading (20′ FCL) Container Loading (20′ FCL): palletized Proto3000 HP 3D High Reusability Polypropylene (PP) powder, securely strapped and shipped via ocean freight.
    Shipping Proto3000 HP 3D High Reusability Polypropylene (PP) ships in sealed, moisture-resistant containers, palletized and labeled. It is typically not classified as dangerous goods for transport; follow local rules. Handle with care. Keep dry, avoid dust, static, ignition sources, and temperature extremes. SDS accompanies shipment.
    Storage Store Proto3000 HP 3D High Reusability Polypropylene (PP) by BASF in a cool, dry, well-ventilated area away from heat, sparks, open flames, and direct sunlight. Keep containers tightly sealed to prevent moisture ingress and dust formation. Keep away from oxidizers and incompatible materials. Use original packaging, protect from static discharge, avoid elevated temperatures, and follow local regulations.
    Shelf Life Typically 12 months from manufacture when stored unopened in original packaging under cool, dry conditions, away from moisture and sunlight.
    Application of Proto3000 HP 3D High Reusability Polypropylene (PP) by BASF 3D Printing MultiJet Fusion Polymer

    In automotive washer-fluid reservoir production with Proto3000 HP 3D High Reusability Polypropylene (PP) by BASF 3D Printing Solutions, the build cartridge is loaded with a recovered-powder fraction not exceeding 80 wt% unless a post-sieve melt flow rate below 50 g/10 min at 230°C/2.16 kg per ISO 1133-1:2022 is confirmed. The HP 5200 MultiJet Fusion station is maintained at 23°C to 25°C and 35% to 45% relative humidity to limit electrostatic clumping. The build chamber is held at 165°C for the first 20 mm of z-height and stepped down by 1°C per 50 mm thereafter to manage heat accumulation. Layer thickness is fixed at 0.08 mm. Fusing agent is registered at 1200 dpi. Wall stock for washer reservoirs is set at 2.5 mm to 3.0 mm, with boss fillets of 1.5 mm radius. After cooling to 45°C inside the build unit, printed parts are depowdered with 4 bar compressed air and bead-blasted with 0.2 mm to 0.4 mm glass spheres. No solvent smoothing is used because residual solvent plasticizes the weld interface and reduces ultrasonic weld strength. Filler necks are joined by ultrasonic welding at 35 kHz with an energy director height of 0.6 mm; sectioned weld plates must show lap shear strength above 8 MPa per ISO 527-1:2019. Thermal cycling is performed under ISO 16750-4:2013 from −40°C to 80°C; the terminal washer reservoir must tolerate 100 cycles at 0.3 bar internal air pressure without visible leakage. Continuous exposure above 80°C is excluded because heat deflection temperature at 0.45 MPa per ISO 75-2:2020 falls between 78°C and 84°C for thin sintered PP sections.

    Powder Reuse Ratios and Wall Stock in Acid Storage Container Manufacturing

    Chemical storage containers intended for 5% to 30% sodium hydroxide and 10% to 40% sulfuric acid at 23°C are printed with a recovered-powder fraction capped at 70 wt%. Higher reuse fractions reduce the powder bed’s melt flow stability and generate pinhole porosity at the intersection of vertical walls and bottom fillets. The powder is sieved through 250 µm ultrasonic mesh immediately after breakout and blended for 20 min in a low-shear rotary mixer. Wall thickness is held at 4.0 mm to 5.0 mm. Helium leak testing on sectioned containers shows that unsupported vertical sections thinner than 3.5 mm develop interlayer pores at a frequency above 1 pore/cm². The build chamber setpoint is 170°C for the first 20 mm and is reduced by 2°C per 50 mm as build height increases. The terminal 5 L container is assembled from two printed halves by hot-plate welding at 220°C. Weld qualification uses ASTM D638-14 tensile specimens sectioned through the weld seam and requires a weld strength above 15 MPa. Chemical immersion test plaques are exposed per ASTM D543-21 in 10% NaOH and 10% H₂SO₄ for 7 days; mass change must remain below 0.5% and tensile strength retention above 90%. The closed container is pressurized with air at 0.5 bar for 30 min and must show no weepage. Service in aromatic hydrocarbons is prohibited because polypropylene swells in benzene and toluene at ambient temperature, producing dimensional change above 2% in 24 h. Weld lines are not specified for oxidizing acids above 40% concentration or temperatures above 40°C.

    Below 60°C continuous service temperature, unfilled sintered polypropylene is used for low-voltage insulation plates, cable clamps, and DIN-rail mounting brackets in control cabinets. The powder blend for electrical parts is restricted to 70:30 recovered-to-virgin material because the presence of degraded fines increases surface roughness on snap-fit engagement surfaces. The powder is vacuum-dried at 80°C for 4 h before loading when storage relative humidity exceeds 60%. Wall sections are printed at 1.6 mm to 2.0 mm with a layer thickness of 0.08 mm. Dielectric strength measured on 1 mm plaques per IEC 60243-1:2013 is 24 kV/mm after 48 h conditioning at 23°C/50% RH. The end part does not meet UL 94 V-0 because the base PP is not flame-retardant; live parts must be separated by a flame-retardant barrier or the housing must be coated with an approved insulating varnish. Glow-wire screening per IEC 60695-2-11:2014 at 550°C is used only for lot consistency, and flaming drip is an expected failure mode for unfilled PP. Threaded brass inserts are installed by ultrasonic insertion at 20 kHz into bosses designed with 2.5 mm wall thickness and 0.3 mm interference holes. The terminal cable management cover is subjected to IEC 61010-1:2015 impact tests from 1 m; the sintered PP must not crack when the inner corner radius is at least 0.8 mm. Published data for this specific configuration is limited, so each production lot is verified by tensile bars per ISO 527-2:2020 and by a 168 h thermal aging exposure at 85°C with subsequent visual inspection for surface oxidation.

    What Limits Living Hinge Fatigue Life in MJF-Printed PP Closures?

    Living hinges printed from Proto3000 HP are produced at a nominal hinge thickness of 0.5 mm and a hinge width of 1.2 mm. The hinge axis is oriented perpendicular to the recoater travel direction to reduce asymmetric shrinkage and preserve dimensional accuracy. After depowdering, the hinge is flexed once at 180° to initiate molecular orientation; this cold drawing step stabilizes the neutral axis. Tensile specimens machined from hinge sections and tested per ISO 527-2:2020 at 23°C show yield strength of 19 MPa and elongation at break of 24%. Flexural modulus per ISO 178:2019 is 1150 MPa. The powder blend is limited to 70 wt% recovered material because higher reuse fractions reduce elongation at break and shift the hinge failure mode from ductile yielding to brittle fracture at the hinge root. Hinge durability is evaluated on a custom flex fixture cycling from to 180° at 30 cycles/min; failure is defined as a visible crack longer than 2 mm. Lot acceptance requires 8,000 cycles minimum on five test specimens. The terminal snap-lid case with integral hinge is used for retail packaging of industrial wipes where the closure is opened fewer than 50 times during product life. Hinge performance is not specified for cold environments below 0°C because PP embrittlement reduces durability; published data for this specific configuration is limited, so injection moulding–derived fatigue constants are not used for prediction. Table 1 summarizes orientation-dependent mechanical values used for closure design.

    Table 1. Orientation-dependent tensile data for Proto3000 HP after 0.08 mm layer MJF processing per ISO 527-2:2020 and ISO 178:2019.
    ConditionTensile yield strength (MPa)Elongation at break (%)Flexural modulus (MPa)
    Flat XY orientation, 0 wt% recovered powder20.0241200
    Flat XY orientation, 70 wt% recovered powder18.0181100
    Z-oriented bonded stack, 70 wt% recovered powder15.57950

    When Filtration Plate Slot Width Drops Below 0.8 mm

    Filter press segments for aqueous acid service are printed only when slot width remains at or above 0.8 mm. Below this value, residual powder cannot be removed reliably with 4 bar compressed air and 0.2 mm glass bead blasting; retained powder hydrolyzes in hot acid and contaminates filtrate. Slot floors are oriented downward in the build to reduce up-facing surface roughness to Ra 15 µm to Ra 20 µm per ISO 21920-2:2021. Plates are printed with 0.10 mm layer thickness to improve edge definition at sealing ribs. Dual-spiral drainage channels have a top width of 2.0 mm, depth of 1.0 mm, and an inner slot of 0.8 mm. The powder blend for filtration plates is restricted to 50 wt% recovered material because higher reuse fractions raise zero-shear viscosity unevenly and create localized porosity at channel intersections. End plates are annealed at 100°C for 2 h in air to relieve residual stress before machining the flat sealing face. Chemical compatibility is validated in 20% hydrochloric acid at 40°C for 72 h per ASTM D543-21; mass change must remain below 0.3% and tensile strength retention above 85%. The terminal 400 mm × 400 mm plate is installed in a recessed-chamber filter press with 0.7 MPa squeeze pressure. Polypropylene is not specified for strong oxidizing acids such as nitric acid above 10% at 40°C because oxidative attack embrittles the sintered structure and reduces seal face flatness. Table 2 lists chemical immersion results for common service fluids.

    Table 2. Chemical immersion results for sintered PP coupons according to ASTM D543-21 at 23°C for 7 days, unless otherwise specified.
    Chemical environmentMass change (%)Tensile strength retention (%)
    10% sodium hydroxide+0.292
    10% sulfuric acid+0.390
    50% ethylene glycol+0.196
    20% hydrochloric acid at 40°C, 72 h+0.388
    No. 2 diesel fuel per ASTM D975+4.855

    For non-patient-contact diagnostic instrument housings, the powder is processed under controlled humidity and limited reuse to maintain cosmetic surface quality. The recovered-to-virgin blend is set at 70:30 after the recovered powder passes a 250 µm sieve and a 48 h vacuum drying stage at 80°C. The build chamber on an HP 4200 series is held at 162°C because the smaller thermal mass of housing parts produces less convective heating than thick chemical containers. Walls are designed at 2.0 mm and ribs are capped at 1.2 mm thickness to avoid sink marks on cosmetic surfaces. Threaded brass inserts are installed by thermal staking at 200°C for 5 s. The assembled housing is subjected to IEC 61010-1:2015 drop tests from 1 m; the sintered PP absorbs impact through ductile yielding rather than cracking when the inner corner radius is at least 0.8 mm. No animal-derived mold release or post-processing additives are used, and the material is compliant with REACH substance restrictions and RoHS 2011/65/EU at the publication date. However, USP Class VI or ISO 10993-1:2018 biological evaluation data for this exact powder reuse state are not published; therefore the terminal housing is limited to diagnostic equipment enclosures that are not touched by patients for more than transient contact. The powder must not be blended with nitrogen-containing stabilizers or amine-based additives because these species can accelerate thermo-oxidative chain scission in the fusing pass. Operators should reject powder lots that show yellowing after drying or an increase in melt flow rate above 50 g/10 min per ISO 1133-1:2022.

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    Certification & Compliance
    More Introduction

    Proto3000 catalogs the BASF-sourced HP 3D High Reusability Polypropylene (PP) as an olefinic powder-bed polymer for MultiJet Fusion on HP Jet Fusion 4200 and HP Jet Fusion 5200 systems. The powder is supplied as a semicrystalline, free-flowing feedstock that converts to fused parts at a nominal density of 0.89 g/cm³ when measured according to ISO 1183-1. That value is approximately 12% lower than the same measurement on HP 3D High Reusability PA12, which alters both the thermal mass and the part-weight advantage in production. Typical tensile strength for the PP grade is 29 MPa per ISO 527-2, with a tensile modulus near 1600 MPa and elongation at break in the 20–30% range. The material is therefore classified as ductile relative to glass-filled systems but softer than unfilled polyamide 12. The low moisture uptake—below 0.1% by ISO 62 after 24 h water immersion—creates the main selection advantage over polyamide 12 in humid service. Candidates for application include battery vent covers, fluid reservoirs, laboratory trays, packaging inserts, and low-pressure air or fluid ducting where chemical resistance and dimensional stability in wet conditions are prioritized over tensile stiffness.

    Because MultiJet Fusion does not use a laser point source, the fusing mechanism is a wide-area infrared exposure through selectively jetted fusing agent. The PP grade is formulated to absorb the fusing radiation in the agent-bearing regions while the detailing agent restricts thermal bleed at edges. This architecture produces layer thickness of 0.08 mm and anisotropic properties. Strength values in the Z direction are typically lower than the XY values because layer-to-layer fusion is controlled by thermal penetration and cooling rate from the powder bed. When designing load paths, the material should be treated as anisotropic and tested in both XY and Z orientations according to ISO 527-2 or ASTM D638 Type I. The tensile values in the table below represent the stronger XY plane; Z values should be measured for the specific work cell because they depend on build height, packing density, and the amount of recycled powder.

    PropertyTest standardTypical value
    DensityISO 1183-10.89 g/cm³
    Tensile strengthISO 527-229 MPa
    Tensile modulusISO 527-21600 MPa
    Elongation at breakISO 527-220–30%
    Flexural modulusISO 1781400 MPa
    Heat deflection temperatureISO 75-2/B100 °C
    Melting peakISO 11357-3139 °C

    What Limits Service Temperature and Load-Bearing Capacity in MJF Polypropylene?

    The heat distortion temperature of the sintered material under 0.45 MPa load is approximately 100 °C per ISO 75-2/B. That is 70–75 K below typical PA12 values from the same HP MultiJet Fusion material family, and the short-term melting peak is 139 °C per ISO 11357-3. These boundaries restrict load-bearing service to temperatures below roughly 80 °C for continuously clamped assemblies; localized excursion above this value can cause creep or clamping-force loss. The tensile strength of 29 MPa is approximately 40% lower than PA12 and around 45% lower than PA11 in similar XY orientations; therefore, pressure-containing parts should be assessed by burst or tensile creep testing under ISO 899-1 or the equivalent component-level protocol. The lower modulus reduces resistance to buckling in thin ribs, but the ductile failure mode is more tolerant of geometrical discontinuities. Published long-term creep data for this specific MJF PP configuration are limited, so any replacement of PA12 in structural brackets, load-bearing housings, or pressure vessels must be preceded by validation at the service temperature and stress state. The PP grade is not recommended for hot-air or hot-fluid conditions above 100 °C except in unloaded or short-duration contact.

    On production units, the main process conflict is not fusing energy but post-build cooling. Polypropylene powder beds retain heat differently from PA12 because the lower melt peak and lower conductivity extend the time before a full-height build cake can be safely extracted. Large flat PP panels are more susceptible to edge lift and bow if the build unit is opened before the powder bed has cooled below a stable, part-specific surface temperature. Operators should establish cooling thresholds by measuring dimensional deviation after extraction rather than importing a fixed PA12 cool-down schedule. Powder recycling also requires different limits: the “high reusability” designation does not eliminate melt-flow drift in the recovered fraction. The recovered powder should be sieved and blended with virgin product according to the HP powder handling station log; melt flow index tested to ISO 1133-1 is a stronger control metric than a fixed virgin-refresh percentage, because the thermal history scales with build nesting density, fusing agent exposure, and the number of recycling loops. If the melt flow index shifts beyond the manufacturer’s accepted band, the reused fraction should be diluted or quarantined.

    Chemical Resistance, Moisture Stability, and Fluid-Contact Applications

    Polypropylene’s semicrystalline olefinic structure provides hydrolytic resistance and tolerance to many dilute acids, aqueous salt solutions, alkaline cleaners, and polar solvents. Unlike polyamide 12, the material does not plasticize substantially in wet conditions; this keeps tensile modulus more stable in water-contact parts. Chemical compatibility should not be assumed solely from the generic polymer class, because the jetting agents and the fused surface state can alter the boundary layer. A qualified immersion program using ASTM D543 should be executed for each process fluid at the upper use temperature, with periodic mass and tensile specimens. Published data for this exact MJF-sintered PP configuration are limited for aggressive fluids; therefore, application-specific immersion testing is mandatory for fuel, electrolyte, or solvent contact. The material is generally less suitable for continuous contact with strong oxidizing acids, aromatic hydrocarbons, or hot chlorinated solvents, where swelling or oxidative attack can occur. For battery-cell ancillary parts, the part should be tested in the actual electrolyte concentration and potential, because pin-hole porosity and sharp edges can create local degradation sites.

    The grade carries the general regulatory character of an olefinic polymer, but the finished part is not automatically food-contact or medical-use compliant. Base-resin compliance may be evaluated under EU 10/2011 or FDA 21 CFR 177.1520; migration testing of the fused MJF part is required before food-contact use because the fusing and detailing agents represent separate process chemicals. Biocompatibility for medical or wearables must be tested per ISO 10993-1 on the final component and post-processing path. Flammability ratings are not a primary datasheet value; ASTM D635 or UL 94 testing is required for enclosures exposed to ignition sources. These are not historical reject criteria but constraints that must be closed before production release.

    The PP powder bed requires different handling than polyamide because its lower density and lower melting point create a narrower thermal process window. If the build chamber setpoint is too high, polypropylene may sinter outside the intended cross-section and lose edge definition; if too low, the interface between layers may not reach adequate fusion. Melt-flow index measured per ISO 1133-1 is therefore a basic incoming and recycled-powder check. A sudden increase in melt flow indicates chain scission from repeated thermal cycling; a decrease may indicate crosslinking or contamination from foreign powder. Recovered powder should be sieved through the mesh specified in the HP powder handling station, blended with virgin product, and qualified with a small build before use in full production.

    When the Specification Prioritizes Low Density and Hydrolytic Stability

    Against HP 3D High Reusability PA12, the PP grade subtracts about 12% from part density and nearly eliminates hygroscopic instability, but it also subtracts about 40% from tensile strength and approximately 70–75 K from heat deflection temperature. PA11 remains a better candidate when low-temperature impact or high ductility is required without the full cost of PA12, but PA11 has higher density and does not match the chemical resistance of PP in many aqueous acid and alkaline environments. The unfilled nature of this PP feedstock distinguishes it from glass fiber or mineral-reinforced polypropylene compounds used in injection molding: the MJF grade retains low density and a ductile yield, but it cannot achieve the modulus of reinforced grades. The comparison below is based on published typical values for XY orientation; Z-direction properties are generally lower and must be measured separately.

    AttributeHP 3D High Reusability PPHP 3D High Reusability PA12HP 3D High Reusability PA11
    Density0.89 g/cm³1.01 g/cm³1.03 g/cm³
    Tensile strength29 MPa48 MPa54 MPa
    Elongation at break20–30%20%50%
    Heat deflection temperature100 °C175 °C180 °C
    Moisture uptake after 24 h<0.1%0.5–1.0%0.3–1.0%

    For part qualification, the minimum mechanical test set should include tensile bars in XY and Z directions, density, heat deflection temperature, and moisture-conditioned tensile strength. The moisture-conditioned test is particularly important because PP absorbs little water; the main concern is not wet strength loss but hydrolytic stability of the fusing agent residue at the surface. Surface post-processing such as bead blasting can remove a weak boundary layer and alter surface roughness, but it may introduce microcracks in thin walls. If cosmetic surfaces are required, a process window should be established with grit type, air pressure, and exposure time held constant. Dimensional inspection should be performed after conditioning at 23 °C and 50% RH following ISO 291 because PP can contract during cooling; immediate post-build measurements may not represent final service dimensions.

    When processing the material, the build unit is operated at 0.08 mm layer thickness with the standard HP fusing and detailing agent set for the PP grade. Fine lattice and internal channel designs should avoid geometries that trap powder, because PP is softer than PA12 and aggressive bead blasting can erode surface features. Threaded connections should use heat-set inserts or coarse-pitch threads because the lower shear strength of the olefinic matrix reduces fine-thread pull-out resistance. Living hinges can be produced in this grade, but flexural durability is strongly anisotropic; layer orientation, cooling rate, and hinge thickness should be optimized through repeated flexural fatigue testing, not a single tensile elongation value. For outdoor components, UV stabilization must be confirmed because unstabilized polypropylene may embrittle after extended solar exposure. Parts intended for pressure-containing fluids should be porosity-checked and leak-tested after any design or post-processing change, because MJF PP’s part density and sealing behavior are sensitive to build orientation and cooling history.

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