| Код ТН ВЭД | 782923 |
Как аккредитованный завод по 3D-печати полипропиленовых гранул Braskem GR105PP, мы соблюдаем строгие протоколы качества - каждая партия подвергается строгим испытаниям для обеспечения последовательных стандартов эффективности и безопасности.
| Упаковка | Braskem GR105PP 3D Printing Polypropylene Pellets supplied in 25 kg moisture-barrier bags, palletized and stretch-wrapped for shipping. |
| Погрузка контейнера (20-футовый контейнер) | 20′ FCL container loading of Braskem GR105PP 3D printing polypropylene pellets: palletized bags, shrink-wrapped, properly secured for safe ocean shipment. |
| Доставка | Braskem GR105PP 3D Printing Polypropylene Pellets ship as non-hazardous, non-regulated cargo in sealed 25 kg bags, octabins, or bulk containers. Keep dry and away from heat, sunlight, and ignition sources. Handle with dust controls; avoid inhalation and static discharge. No DOT/IMDG/IATA placards or special transport documentation required. |
| Хранение | Store Braskem GR105PP 3D Printing Polypropylene Pellets in original, sealed containers in a cool, dry, well-ventilated area. Protect from moisture, direct sunlight, heat, and ignition sources. Keep away from strong oxidizing agents. Maintain ambient temperature, avoid excessive stacking, and keep containers closed when not in use. Prevent pellet spills and dust; clean up promptly to avoid slip hazards. Follow local regulations and SDS. |
| Срок годности | Stable under normal storage conditions; typically 12 months in original packaging when kept cool, dry, and away from sunlight. |
Braskem GR105PP is a polypropylene pellet grade supplied for extrusion-based additive manufacturing. The material is evaluated under ISO 178:2019 for flexural modulus, ISO 527-2:2012 for tensile properties, and ISO 1133-1:2022 for melt flow rate. In industrial printing cells, pellet-fed screw deposition is used rather than filament conversion because the pellet form removes the additional thermal history of filament compounding. A drying step at 80 °C for 4 hours is applied when storage relative humidity exceeds 60%, as residual moisture can increase void formation at layer interfaces. The following application scenarios address automotive assembly, chemical processing, packaging development, laboratory equipment, living-hinge consumer goods, and outdoor service parts. Each scenario is limited to processes where polypropylene’s chemical resistance, fatigue tolerance, and low density provide a documented performance advantage over ABS and PLA.
Within automotive assembly plants, pellet-fed additive manufacturing cells running Braskem GR105PP are used for production-line jigs, robotic end-of-arm tooling, and paint-shop handling nests. The relevant quality system is IATF 16949:2016, with Clause 8.4.2.4 governing supplier quality management system development and ISO 9001:2015 Clause 8.4.1 controlling externally provided processes; in addition, REACH (EC) No 1907/2006 Article 33 obligations apply to SVHC communication. The standard feedstock ratio is 100 wt% GR105PP in the feed hopper, with no dilution by regrind because uncontrolled regrind molecular weight distribution can alter melt viscosity; when color or UV marking is specified, a carbon black masterbatch is metered at 2 wt% to 4 wt%, and final part mechanical properties must be re-validated under ISO 527-2:2012 because carbon black affects crystallinity. Processing on a large-format pellet extruder with a single screw of L/D 24:1 to 30:1 uses barrel temperatures of 200 °C to 230 °C, a screw speed of 15 rpm to 40 rpm, and nozzle diameters from 1.2 mm to 3.0 mm; layer heights between 0.8 mm and 2.0 mm are paired with print speeds of 30 mm/s to 80 mm/s to maintain interlayer adhesion. The build plate temperature is held at 80 °C to 100 °C, and a chamber temperature of 40 °C to 60 °C reduces warpage. Pellet bridging in hoppers can occur when ambient relative humidity falls below 20%; grounded metal feed throats and vibratory feeders mitigate this static-charge failure mode. Printed parts are used as robotic gripper jaws, CMM fixture plates, masking plugs, trim-assembly locators, and safety guarding spacers; these components replace machined HDPE or nylon because PP permits hot-plate welding of printed sections and has lower moisture uptake, with a density near 0.91 g/cm³ to 0.93 g/cm³. A limitation is that continuous service above 90 °C under load may exceed the practical heat distortion range of unfilled PP; design calculations should use ISO 75-2 HDT/B data for the grade.
Polypropylene is selected for corrosive fluid handling fixtures because of its resistance to many acids, alkalis, and aqueous salt solutions, as characterized by ISO 175:2010 and ASTM D543-20. The application includes prototype valve bodies, pump housing covers, filter plates, and immersion jigs used in electroplating and wastewater treatment lines. The material feed is 100 wt% virgin GR105PP; where prolonged outdoor storage is anticipated, a 10% active HALS masterbatch is added at 1.5 wt% to 2.0 wt%, yielding 0.15 wt% to 0.3 wt% active HALS in the melt, which is within typical PP stabilization practice. Pellet deposition is carried out at 205 °C to 225 °C with a nozzle diameter of 1.5 mm to 2.0 mm and a layer height of 0.6 mm to 1.0 mm. To reduce residual stress in thick sections, the parts are annealed at 110 °C to 120 °C for 2 hours; the limiting factor in annealing is that unrestrained walls above 8 mm can sag or distort, so support tooling or sand beds are required. Thermal exposure during annealing should be validated by dimensional checks because PP crystallinity development can produce anisotropic shrinkage across the build axis. The terminal components include acid bath dip racks, flange blanks for temporary piping, filter press wear strips, and pump impeller prototypes. Because welded seams and printed layer lines can act as permeation paths, the finished parts must be leak-tested under the service pressure specified for the line, and pressure-boundary use may require code assessment under PED 2014/68/EU or ASME B31.3. Published data for long-term chemical exposure in 3D-printed PP under continuous immersion at elevated temperature is limited; therefore, service validation under ASTM D543-20 test liquids at the target concentration and temperature is required before installation.
Because polypropylene offers repeated flexural endurance and low density, packaging development groups use Braskem GR105PP pellets to print prototype closures, thin-wall container sections, and living-hinge cap designs before injection molding tooling is cut. The regulatory frame for food-contact packaging includes FDA 21 CFR 177.1520 for olefin polymers and EU Regulation (EU) No 10/2011 Annex I, but printed prototypes are not automatically food-contact compliant; migration testing is mandatory under EU 10/2011 Article 19 if the printed part contacts food. The formulation is 100 wt% GR105PP for dimensional stability trials; when impact copolymer behavior is being simulated, 10 wt% to 20 wt% of an ethylene-propylene impact modifier is dry-blended with the pellets before feeding. The downstream process uses a pellet-fed extruder with a 0.8 mm nozzle and a 0.3 mm layer height at 210 °C to 225 °C, with print speeds between 25 mm/s and 45 mm/s. The build plate temperature is 80 °C to 90 °C, and a polypropylene build plate with a 0.1 mm to 0.2 mm PP adhesive sheet improves first-layer adhesion without solvent-based primers. Terminal outputs include snap-fit closure prototypes, bottle cap living hinges, tamper-evident band iterations, thin-wall tub lids, and blister tray mockups. The main processing limitation is that thin walls below 0.9 mm may exhibit void growth at layer interfaces; therefore, wall stock is kept at or above 1.0 mm for functional snap-fit trials. For all dimensional iterations, print orientation must be recorded because PP shrinkage is anisotropic and can shift the fitment of closure features between the X-Y plane and the Z axis.
Laboratory equipment manufacturers convert Braskem GR105PP pellets into diagnostic instrument housings, tube racks, and work-cell fixtures using pellet extrusion additive manufacturing. The relevant standards are ISO 13485:2016 for quality management in medical device manufacturing and ISO 10993-5:2009 for in vitro cytotoxicity testing, but no biocompatibility claim is assigned to the supplied pellet grade unless lot-specific and process-specific data are generated. The feed ratio is 100 wt% virgin GR105PP; the use of mold-release agents, slip additives, or regrind is excluded because these can introduce extractable species that would require additional ISO 10993-1:2018 toxicological risk assessment. The processing line uses a heated chamber at 50 °C to 60 °C, barrel temperatures of 210 °C to 230 °C, and a nozzle diameter of 0.8 mm to 1.2 mm, with layer height fixed at 0.4 mm. After printing, parts are annealed at 100 °C for 1 hour and wiped with 70% isopropyl alcohol. The terminal components include diagnostic analyzer chassis prototypes, laboratory tube racks, pipette calibration fixtures, and non-patient-contact equipment covers. Dimensional stability is limited by polypropylene’s shrinkage, typically in the range of 1.0% to 2.5% depending on build orientation; therefore, datums and mounting features are post-machined rather than used as-printed. For parts that may contact alkaline cleaning agents, compatibility is assessed under ISO 175:2010; repeated autoclave cycling above 121 °C is not recommended because part distortion can exceed dimensional tolerance limits.
When living-hinge endurance governs material choice, Braskem GR105PP is processed at a nominal extrusion temperature of 210 °C to 220 °C to produce protective cases, battery access covers, toolbox organizers, cable-management clips, and case latch levers. The relevant mechanical test method is ASTM D638-14 for tensile properties of plastics, with printed specimens cut parallel and perpendicular to the build direction; flexural modulus is evaluated under ISO 178:2019. For enclosure prototypes that may enter electrical equipment, flammability is assessed under UL 94; unfilled PP typically falls into the HB classification, but the printed part must be tested separately because layer voids and density variations affect burning behavior. The feedstock is 100 wt% GR105PP, and no talc or calcium carbonate filler is added because filler levels above 5 wt% reduce hinge endurance and increase notch sensitivity. The deposition process uses a pellet-fed screw extruder with a 0.6 mm nozzle, a 0.25 mm layer height, and print speeds of 25 mm/s to 40 mm/s. Hinge features are oriented with the hinge length parallel to the X-Y plane and the bend axis aligned to the layer direction; post-print flex cycling is performed to the customer’s cycle-count requirement because no ISO standard fully covers printed living-hinge endurance. The low surface energy of PP requires a polypropylene build plate with an adhesive PP sheet; otherwise first-layer lifting occurs at the ends of long parts. The service temperature should not exceed 80 °C under continuous load; above this, PP modulus decreases and hinge memory degrades.
Outdoor equipment manufacturers use Braskem GR105PP for pump covers, hatch spacers, fender tooling, and dock edge buffers where UV resistance and low moisture absorption are required. The applicable weathering standard is ISO 4892-2:2013, with a xenon-arc exposure method; UV-stabilized PP compounds are assessed for color change and retained tensile elongation under ISO 527-2:2012. The compounding ratio is 100 wt% GR105PP with 2 wt% of a 10% active HALS/UV stabilizer masterbatch, giving 0.2 wt% active stabilizer in the extrudate; for black parts, 2 wt% carbon black masterbatch is added and provides UV screening. Processing is performed on a large-format pellet extruder with a 2.0 mm nozzle, 1.0 mm layer height, and barrel temperatures of 210 °C to 230 °C, with a bed temperature of 80 °C to 100 °C and a chamber temperature of 45 °C to 60 °C. The terminal parts include pump access covers, marine battery trays, hinge shims, cable pass-through flanges, and dock edge buffers. Because PP has a low surface energy, structural adhesive bonding for field repairs should be preceded by flame, corona, or plasma treatment; mechanical fastening and hot-air welding are preferred joining methods.
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Braskem GR105PP 3D Printing Polypropylene Pellets are positioned within the manufacturer’s large-format additive manufacturing segment as an unfilled polypropylene homopolymer feedstock for pellet-fed extrusion systems. The designation GR105PP separates the grade from injection-moulding and blown-film polypropylene by its melt-flow index and crystallisation behaviour. The melt flow rate is 10.5 g/10 min at 230 °C under 2.16 kg load by ISO 1133-1. Density is 0.905 g/cm³ by ISO 1183-1. On single-screw pellet extruders with screw diameters from 25 mm to 45 mm and length-to-diameter ratios from 20:1 to 30:1, the material is deposited in the nozzle setpoint range of 220 °C to 240 °C. Build plate temperatures are held at 90 °C to 110 °C. The principal difference from conventional polypropylene extrusion grades is the control of melt viscosity and recrystallisation rate for layer-to-layer fusion in large bead widths and thick layer heights.
Grade-level physical property data for Braskem GR105PP are summarised below. These values are typical for the unfilled polypropylene homopolymer product category used in large-format pellet extrusion; lot-specific certificates of analysis may contain tighter limits.
| Property | Test method | Typical value or range |
|---|---|---|
| Melt flow rate, 230 °C/2.16 kg | ISO 1133-1 | 10.5 g/10 min |
| Density | ISO 1183-1 | 0.905 g/cm³ |
| Tensile stress at yield | ISO 527-2 | 30–35 MPa |
| Tensile elongation at yield | ISO 527-2 | 8–12 % |
| Flexural modulus | ISO 178 | 1300–1600 MPa |
| Charpy notched impact strength at 23 °C | ISO 179-1/1eA | 2–5 kJ/m² |
| Heat deflection temperature at 0.45 MPa | ISO 75-2 | 90–100 °C |
| Vicat softening temperature A50 | ISO 306 | 150–160 °C |
| Linear mould shrinkage | ISO 294-4 | 1.0–2.0 % |
| Coefficient of linear thermal expansion, 23–55 °C | ISO 11359-2 | 90–120 × 10⁻⁶ K⁻¹ |
Because polypropylene is a semi-crystalline polymer, the solid-to-melt transition spans a narrow interval between 130 °C and 165 °C, with the main melting endotherm near 160 °C in differential scanning calorimetry. This narrow transition produces a short thermal working window in large-format deposition. The melt flow rate of 10.5 g/10 min is lower than high-flow injection-moulding grades but higher than many sheet and thick-wall extrusion grades. This range balances bead spread against uncontrolled die swell and provides enough melt strength to bridge short gaps between deposited roads. At shear rates typical of deposition nozzles between 0.8 mm and 1.2 mm, the apparent melt viscosity for a polypropylene homopolymer of this melt flow rate lies approximately between 300 Pa·s and 500 Pa·s at 230 °C. On production-scale single-screw extruders with 20:1 to 30:1 L/D, compression ratios of 2.5:1 to 3.0:1 homogenise the melt while limiting excessive shear heating. Feed-throat temperature is maintained below 60 °C to prevent pellet softening and hopper bridging. If the feed throat approaches 70 °C, partially molten pellets can form a cohesive plug at the feed pocket and starve the screw.
Oxidative degradation is a process limit. At barrel temperatures above 250 °C and residence times longer than 10 min, random chain scission increases the melt flow rate and generates low-molecular-weight oxidation products. The upper barrel temperature should not exceed 240 °C unless the deposition head has a melt pump and residence-time control. On systems without a melt pump, prolonged idling at melt temperature has been reported to reduce bead-to-bead fusion by lowering apparent viscosity and producing a less coherent melt front.
Moisture uptake in unfilled polypropylene is low relative to polyamide, PETG, or ABS. However, surface moisture on pellets can generate steam during melting and create nozzle sputter, internal voids, and intermittent bead breakup. In production facilities with ambient relative humidity above 60 %, pre-drying at 80 °C for 4 h in a desiccant dryer is specified. Pellets stored in sealed hoppers with dry-air purge maintain residual moisture below 0.02 % by weight. Open hoppers in climates with dew points above 20 °C have been associated with first-layer adhesion loss when condensation transfers from pellet surfaces to the build plate. The material does not require the extended drying cycles common to nylon or PETG.
The starting processing window for large-format pellet extrusion is listed below. Setpoints require adjustment for nozzle diameter, extruder L/D, melt-pump presence, and build volume.
| Processing parameter | Setpoint or range |
|---|---|
| Pre-drying | 80 °C for 4 h, desiccant dryer |
| Feed throat temperature | < 60 °C |
| Barrel temperature profile | 190–230 °C |
| Nozzle setpoint | 220–240 °C |
| Build plate temperature | 90–110 °C |
| Heated build chamber | 80–100 °C |
| Nozzle diameter | 0.8–1.2 mm |
| Layer thickness | 0.3–0.5 mm |
Crystallisation studies on polypropylene homopolymer of this melt-flow class show a crystallisation exotherm peak between 110 °C and 125 °C at moderate cooling rates. Slow cooling through this interval produces larger spherulites and higher shrinkage, while rapid cooling reduces crystallite size and internal stress. In large-format extrusion, the previous layer is cooled below the crystallisation peak before the next bead is deposited, which limits interpenetration of polymer chains across the interface. A heated build chamber at 80–100 °C keeps the previous layer above the crystallisation onset long enough to improve interfacial strength. The result is a trade-off between build speed, chamber cost, and part morphology. When chamber temperature is too high, parts remain soft during printing and can distort under their own weight; when too low, layer adhesion becomes the limiting mechanical property.
Deposition speed and melt throughput also affect the bead cross-section. At nozzle diameters of 1.2 mm, layer heights of 0.5 mm, and print speeds above 60 mm/s, the melt front can exhibit sharkskin or uneven bead edges unless the barrel metering zone is maintained above 220 °C. On production lines, bead width is controlled by nozzle-to-bed gap rather than extrusion multiplier alone. When the gap exceeds the layer height by more than 0.2 mm, the bead is over-squeezed and can split into separate lobes. When the gap is too large, insufficient normal force leaves a rounded bead with poor contact area to the substrate.
Polypropylene has a low surface energy, typically 30–32 mN/m, which restricts wetting on untreated glass, PEI, and steel build plates. Adhesion is improved by using a polypropylene sheet, polypropylene-based tape, or a solvent-primed polyolefin interface. In production-scale prints, build plate temperatures below 90 °C cause first-layer edge curl, while plate temperatures above 110 °C soften the lower layers and increase dimensional drift in tall parts. Linear mould shrinkage by ISO 294-4 ranges from 1.0 % to 2.0 %. In additive deposition, shrinkage is anisotropic because contraction along the deposited bead differs from contraction across bead-to-bead interfaces. XY compensation factors of 1.5 % to 2.0 % and Z compensation of 1.0 % to 1.5 % are applied depending on toolpath geometry. Heated build chambers between 80 °C and 100 °C reduce differential cooling between part surfaces and interior regions. Without chamber heating, square polypropylene parts with edge lengths above 300 mm may exhibit corner lift exceeding 2 mm on open-frame systems.
Jigs, fixtures, assembly trays, and chemical-contact tooling are produced on pellet-fed systems where chemical resistance and impact toughness are more relevant than high modulus. Polypropylene homopolymer in this melt flow range resists dilute aqueous acids, bases, salts, and many polar organic solvents at ambient temperature. It is not recommended for continuous exposure to strong oxidising acids, chlorinated solvents, aromatic hydrocarbons, ketones, or hot xylene, which cause swelling or oxidative attack. At sustained service temperatures above 80 °C in air, oxidative degradation can reduce molecular weight and embrittle the part unless the grade contains a suitable stabiliser package. Published data for GR105PP-specific chemical compatibility at elevated process temperatures is limited; service testing under the actual chemical and thermal load is therefore required.
Post-processing of GR105PP parts by machining requires sharp low-rake cutting tools and moderate spindle speeds because polypropylene has a low heat deflection temperature and may smear or gum cutters. Flood coolant or compressed air is preferred over dry machining to limit local melting. Threaded inserts and heat-staked fasteners are preferred over adhesives because the low surface energy of polypropylene limits adhesive wetting. Flame or plasma treatment can increase surface polarity for bonding and painting.
The replacement decision is governed by the trade-off among stiffness, thermal distortion, chemical resistance, and density. PLA typically has higher tensile modulus, often 3000–3500 MPa by ISO 527-2, but heat deflection temperature at 0.45 MPa is usually 50–60 °C. ABS has tensile modulus near 2000–2500 MPa and heat deflection temperature near 90–100 °C, but it releases volatile styrenics during deposition and has higher density than polypropylene. PETG has higher tensile modulus than polypropylene but density near 1.27 g/cm³ and greater moisture uptake. GR105PP reduces mass because its density is 0.905 g/cm³ and provides a low surface energy polyolefin surface with better resistance to aqueous cleaning agents. However, layer-to-layer adhesion is lower than PETG or ABS because polypropylene crystallises at the interface between deposited layers. Heated build chamber operation at 80–100 °C and nozzle setpoints at the upper end of the melt window are required to obtain useful interlayer tensile strength. Published data for Z-direction tensile strength of GR105PP in large-format printed geometries is limited; printed polypropylene commonly exhibits anisotropic tensile properties with through-thickness values below the in-plane bulk yield stress.
Compared with glass-fibre-reinforced polypropylene pellet feedstocks, GR105PP is unfilled and therefore produces lower flexural modulus. Glass-filled polypropylene grades may exceed 3000 MPa in flexural modulus, but the reinforcement increases screw and nozzle wear in pellet-fed deposition and raises melt viscosity. GR105PP lowers equipment abrasion and avoids the abrasive filler settling and nozzle clogging observed with glass-filled feedstocks in small-diameter deposition heads. Regulatory status is application-dependent. Polypropylene homopolymer of this type can be evaluated for food-contact use under FDA 21 CFR 177.1520; direct food-contact certification for GR105PP must be confirmed from the supplier. Compliance with REACH and RoHS is expected for the base polymer, but additive package and colorant compliance must be verified for the specific lot. Reclaimed printed structures and support material can be re-extruded, though repeated thermal cycles increase melt flow rate through chain scission and may shift viscosity below the lower limit of the pellet extrusion window.