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Braskem FL105PP 3D Printing Polypropylene Filament

    • Название продукта: Braskem FL105PP 3D Printing Polypropylene Filament
    • Сайт Factroy: Округ Юду, Ганьчжоу, Цзянси, Китай
    • Запрос цены: admin@ascent-chem.com
    • Производитель: Ascent Petrochem Holdings Co., Limited
    • Свяжитесь сейчас
    Спецификации
    Код ТН ВЭД 593519

    Как аккредитованный завод Braskem FL105PP 3D Printing Polypropylene Filament, мы соблюдаем строгие протоколы качества - каждая партия подвергается строгим испытаниям для обеспечения последовательных стандартов эффективности и безопасности.

    Упаковка и хранение
    Упаковка Braskem FL105PP 3D printing polypropylene filament, 1.75 mm, supplied on 1 kg spools, sealed in moisture-barrier bags, packed in cartons.
    Погрузка контейнера (20-футовый контейнер) 20′ FCL loading description for chemical Braskem FL105PP 3D printing polypropylene filament: palletized, secured, dry ambient transport, no mixed cargo.
    Доставка Braskem FL105PP 3D Printing Polypropylene Filament ships as a non-hazardous solid in sealed spools with desiccant, packed in moisture-barrier bags and cartons. Transport at ambient temperature; protect from moisture, direct sunlight, and excessive heat. Not regulated under DOT/IMDG/IATA.
    Хранение Store Braskem FL105PP polypropylene filament in a cool, dry, well-ventilated area, away from direct sunlight, heat, sparks, and strong oxidizers. Keep sealed in original packaging with desiccant to minimize moisture absorption. Maintain ambient temperature, ideally 15–30°C, and low humidity. Avoid dusty environments and prolonged UV exposure. Rotate stock first-in, first-out. Inspect packaging before use.
    Срок годности Typically 24 months when stored sealed in original packaging, dry, at room temperature, and protected from UV light.
    Применение полипропиленовой нити для 3D-печати Braskem FL105PP

    Chemical-process and fluid-handling prototypes produced from FL105PP filament are typically configured as valve bodies, impeller housings, tray liners, and short-run storage canisters. The unfilled semicrystalline polypropylene matrix exhibits low equilibrium moisture uptake—commonly reported below 0.05% after 24 h immersion under ISO 62:2008—which limits hygroscopic swelling in wet-service environments. Fluid compatibility assessments are conducted in accordance with ISO 175:2010 and ASTM D543-21; the material is generally resistant to aqueous salt solutions, dilute mineral acids below 10% by weight at 23 °C, many detergent solutions, and short-chain alcohols such as 70% isopropanol. Resistance is load-dependent: a part under external stress in 10% sodium hydroxide or 30% sulfuric acid can develop environmental stress cracking at interlayer interfaces even when the polymer itself is chemically compatible. Aromatic solvents, chlorinated solvents, and strong oxidizing acids are not recommended for continuous contact. Process parameters for fluid-contact components favor full interlayer fusion, with nozzle setpoints in the range 220–240 °C, a heated bed at 90–100 °C, and a passively or actively heated build chamber from 45 °C to 60 °C. On open-frame equipment, a PP-specific adhesion promoter or corona-treated PP build sheet is required to prevent edge lift; edge lift is commonly observed on parts with footprints exceeding 250 mm × 150 mm when the ambient temperature falls below 20 °C. For fluid-contact duties, 100% infill and a minimum wall thickness of 2.0 mm are specified to reduce microvoid networks that increase permeation and bacterial fouling. If the spool has been stored at relative humidity above 60%, a 80 °C forced-air drying step for 2–4 h is applied before extrusion to remove surface condensation and suppress steam-generated porosity. Post-print annealing at 100–110 °C for 1–2 h in a forced-air oven can increase crystalline order and relieve internal stress; however, the upper temperature bound may cause slight oxidation and surface discoloration that reduces adhesive bonding of subsequent coatings. Dimensional tolerance after annealing is anisotropic: through-thickness shrinkage is larger than in-plane shrinkage, and printed holes or flanges should be reamed or machined after thermal treatment. The operational boundary for this polymer in wet chemical service is defined by continuous temperature, load, and concentration; sustained exposure above 40 °C to strong oxidizers or above 60 °C to ethylene glycol-water mixtures should require separate long-term immersion testing, not extrapolation from short-term swelling data.

    What Limits Flexural Fatigue in Thin-Section Living-Hinge Prints?

    Flexural fatigue in thin-section living-hinge prototypes printed from FL105PP is controlled by raster orientation, the number of layer interfaces across the hinge web, and stress concentration at the hinge root. In injection-molded polypropylene, a living hinge with a thickness of 0.25 mm to 0.50 mm can withstand repeated flexing because the polymer chains are oriented across the hinge during molding; in fused-filament fabrication, the layer lines introduce through-thickness mechanical anisotropy that becomes the primary fatigue-limiting variable. When the hinge axis is aligned parallel to the raster direction, tensile stress during flexing is carried along continuous extrusions; when the axis is perpendicular, cyclic tensile stress acts across interlayer boundaries and crack initiation occurs at the weakest interface. The preferred build strategy for closure prototypes is to print the hinge web with a 0.4 mm nozzle, 0.20 mm layer height, and 100% rectilinear infill oriented at 0° relative to the hinge axis. A web thickness of 0.35–0.40 mm is often specified to produce two full layers across the hinge; a single-layer web below 0.20 mm is rarely capable of surviving flexural fatigue beyond prototype validation. Stress-whitening at the hinge root after repeated flexing is an accepted visual indicator of craze formation and impending failure; in printed parts, whitening appears first along raster boundaries. Flexural properties are evaluated under ASTM D790-17 or ISO 178:2019, and notch sensitivity is measured by ASTM D256-23e1; published fatigue data for FL105PP in this specific configuration is limited, so cyclic validation under ASTM D7774-17 is required for closure designs that must survive 10,000 or more flexural cycles. Post-print annealing at 100 °C for 30–60 min after removing the part from the build plate can reduce residual stress but may also relax hinge geometry if the web is unsupported. Operational use should avoid direct sunlight and elevated temperature above 50 °C, because oxidative degradation reduces molecular weight and accelerates surface cracking at the hinge root. For terminal-use closures, injection molding remains the robust production process; the printed FL105PP hinge is a functional prototype that validates geometry, tactile feedback, and short-term fatigue, not a direct substitute for long-life molded polypropylene.

    In automotive climate-control and fluid-management prototyping, FL105PP is deposited into short-run air ducts, windshield-washer reservoirs, coolant overflow tank prototypes, and instrument-panel air distribution components. The use case is driven by polypropylene’s low density and its resistance to ethylene glycol-water mixtures, washer fluids, and road-splash chemicals at moderate temperatures. Fluid resistance is evaluated under ISO 175:2010 for immersion and ASTM D543-21 for reagent exposure; long-term exposure to hot ethylene glycol-water at 100 °C should be avoided because oxidation embrittlement and additive extraction can accelerate. The continuous-use temperature for unfilled polypropylene prototypes under low mechanical load is typically limited to 80 °C based on heat deflection temperature measured under ISO 75-2:2013 method B; peaking above 100 °C can produce dimensional distortion at clamped flanges and sealing faces. For ducting, wall thicknesses of 1.5–2.0 mm with 40–60% infill are used to balance mass and stiffness, while reservoir prototypes require 100% infill and a 2.5 mm minimum shell to reduce vapor permeation and hydraulic leak paths. A heated build chamber at 45–60 °C, a bed at 90–100 °C, and a 0.25 mm layer height are typical for these larger parts; increasing layer height to 0.30 mm shortens print time but lowers interlayer bond strength and increases the probability of leak paths at seams. The z-seam should be positioned away from sealing surfaces and clamp planes, because the seam creates a local thickness irregularity and potential leak channel. Flange faces printed in the X-Y plane require post-machining or gasket compression in the range 20–30% for a reliable seal; silicone or EPDM gaskets are preferred. Production-scale fused-filament cells report edge lift on duct sections longer than 250 mm unless polypropylene adhesion promoters are applied to the build surface; an enclosed build volume is more reproducible than an open-bed platform for this geometry. Printed reservoir prototypes are subjected to glycol immersion at 60 °C for 7 days and pressure-decay testing at 20–30 kPa before use on vehicle test benches; published data for FL105PP in this specific configuration is limited, so each new geometry requires its own leak and distortion validation.

    When a Pack Closure Must Pass Burst and Drop Tests

    Pack closure prototypes printed from FL105PP are used for short-run bottle caps, child-resistant closures, tamper-evident bands, and threaded neck finishes where functional testing precedes tooling investment. The dominant failure mode in printed closures is not thread stripping but z-direction interlayer separation during hydrostatic burst testing; because fused-filament parts exhibit lower strength perpendicular to the build plane, closure designers should orient the closure base parallel to the build plate and align the thread helix so that thread flanks are not built as unsupported overhangs greater than 45°. Thread root geometry should include a radius of at least 0.5 mm to reduce stress concentration at the junction of the neck and skirt; a sharp root below 0.3 mm is a known crack-initiation site in printed polypropylene. A wall thickness of 1.2–1.5 mm for the closure skirt and 0.8–1.0 mm for the tamper-evident band is specified with 100% infill to limit helical leak paths. The extrusion profile uses a 0.4 mm nozzle and 0.20 mm layer height, with cooling fan speed reduced to avoid abrupt crystallization and layer-to-layer delamination; a build chamber held at 45–55 °C improves interlayer bonding. Burst testing is performed according to ASTM D1599-18 or a pressure-decay method at 30–50 kPa for low-viscosity liquids; drop testing follows ASTM D2463-15 or an ISTA 1A sequence from 0.80 m. In drop testing, printed closures often fail at the interlayer boundary around the thread start rather than the hinge or skirt; this failure can be mitigated by adding a 0.20 mm sacrificial chamfer and by orienting the thread start away from the build-plane seam. Food-contact status for polypropylene homopolymer is recognized under FDA 21 CFR 177.1520 and Regulation (EU) No 10/2011, but printed articles are not automatically compliant because microvoids, surface roughness, colorants, and post-processing agents may affect migration behavior. A printed closure intended for direct food contact must undergo migration testing under EU 10/2011 Annex V with simulants appropriate to the food type; sealing the outer surface does not remove the need for compliance testing. For closures that contain post-consumer recycled material or additives, supplier documentation must confirm the formulation meets 21 CFR 177.1520(b) and applicable REACH restrictions.

    Laboratory Jigs and Solvent-Immersion Fixtures

    When laboratory jigs, instrument housings, fluidic manifolds, and immersion fixtures are printed from FL105PP, the material selection is based on its broad room-temperature resistance to aqueous reagents, saline buffers, and short-chain alcohols. Immersion testing under ISO 175:2010 and ASTM D543-21 typically shows low mass change in 70% isopropanol, 3% hydrogen peroxide, and physiological saline at 23 °C; stress-cracking resistance, however, is lower when parts are clamped or press-fit into stainless-steel frames, so continuous external stress should be below 20% of the printed yield stress in these environments. Strong oxidizers, aromatic hydrocarbons, and chlorinated solvents are incompatible with polypropylene and should not be used in immersion service. For aqueous acid and base fixtures, the concentration limit is typically 10% at 23 °C under unstressed immersion; higher temperatures or continuously applied loads shift the acceptable boundary and require ASTM D543 multi-temperature screening. Repeated autoclave exposure at 121 °C is not recommended for FFF polypropylene jigs because internal microvoids expand and produce delamination blisters; dry-heat exposure is limited to 80 °C for unstressed fixtures and 60 °C for fixtures with press-fit inserts. UV sterilisation chambers can embrittle unfilled polypropylene; if germicidal UV exposure is anticipated, a UV-stabilised grade or post-print coating is necessary. On a standard direct-drive FFF platform with an all-metal hot end, FL105PP is processed at 220–240 °C and 25–40 mm/s for perimeter features; slower speed improves layer bonding in thick fixtures, while higher speed produces visual under-extrusion at tight radii. The compliance evaluation for laboratory use includes RoHS 2011/65/EU and REACH documentation; because filament batches may contain nucleating agents or pigments, the supplier certificate should be obtained for each lot. For fixtures that contact cell-culture media or biological fluids, printed polypropylene is not automatically classified as biocompatible; cytotoxicity testing per ISO 10993-5:2009 is required before any such use.

    The following exposure classes apply to unstressed FL105PP printed specimens with 100% infill and 2.0 mm wall thickness:

    Fluid classTest methodImmersion conditionStress state boundary
    Dilute mineral acid, ≤10%ISO 175:201023 °C, 7 daysUnstressed or <20% of yield stress
    Ethylene glycol-water 50%ISO 175:201060 °C, 7 daysUnstressed; not for continuous load
    Isopropanol 70%ASTM D543-2123 °C, 21 daysLight intermittent load
    Sodium hydroxide 10%ASTM D543-2123 °C, 7 daysUnstressed only
    Toluene, xylene, chlorinated solventsASTM D543-2123 °C, 24 hNot recommended

    For non-load-bearing wearable trial devices, orthotic shell prototypes, and veterinary limb-form fixtures, FL105PP is printed with 3.0–4.0 mm wall thickness and 20–40% triangular infill to reduce mass while retaining flexural stiffness for fitting trials. The low density of unfilled polypropylene, generally cited near 0.905 g/cm³ in supplier datasheets, is a design variable in wearable prototypes, but the creep behavior of unfilled polypropylene limits the duration of sustained mechanical load. At 23 °C, a printed shell under continuous bending or compression exhibits time-dependent strain; therefore, these components are used for short-duration shape evaluation and not as final load-bearing orthoses. Surfaces intended for skin contact must be sanded and sealed because as-printed layer ridges concentrate localized pressure; a 0.20 mm layer height and 3 perimeter shells reduce surface roughness at the build surface. Cleaning is performed with 70% isopropanol or neutral detergent; autoclave processing is not used because internal voids may delaminate and create contamination reservoirs. For any application involving prolonged skin contact, cytotoxicity evaluation under ISO 10993-5:2009 and irritation testing are required; FL105PP is not supplied with an implantable or long-term skin-contacting medical-grade certification unless the supplier explicitly documents the relevant lot-specific biological endpoints.

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    Сертификация и соответствие требованиям
    Более подробное введение

    Braskem FL105PP is a polypropylene-based monofilament supplied for fused filament fabrication and direct-drive feed systems. The product is offered in nominal diameters of 1.75 mm and 2.85 mm; supplier quality documentation typically specifies a maximum average diameter deviation of ±0.05 mm and ovality below 0.03 mm when measured by two-axis laser micrometer at 23 °C. Spools are typically wound with controlled tension in the range 1–2 N for 1.75 mm filament to prevent cross-wind entrapment. The resin is an unfilled polyolefin, and its density is reported in the range 0.90–0.91 g/cm³ by ISO 1183-1:2019 method A. Water uptake after 24 h immersion at 23 °C is below 0.05 % according to ISO 62:2008, which is a primary difference from hygroscopic polyamide filaments. Published grade-specific mechanical data for FL105PP are limited; the values cited for unfilled polypropylene should be verified against the supplier certificate of analysis before load-bearing use.

    The melt-flow characterization associated with the grade is a nominal 10.5 g/10 min at 230 °C under 2.16 kg load, measured by ISO 1133-1:2022 procedure A. This places FL105PP in the low-MFR extrusion region where melt strength is sufficient for stable filament drawing but melt viscosity remains high enough to require elevated nozzle temperatures. A differential scanning calorimetry melting peak appears near 160–170 °C using ISO 11357-3:2018; recrystallization during cooling typically onsets between 115 °C and 130 °C. The difference between the melting peak and recrystallization onset defines the available bed-temperature band; if the build surface cools below the recrystallization onset before layer deposition, differential shrinkage at the first layer exceeds the adhesion limit of most untreated build plates.

    What is the practical extrusion window for FL105PP on direct-drive fused filament systems?

    The lower nozzle boundary is governed by interlayer diffusion. At nozzle temperatures below 210 °C, the melt is insufficiently mobile to wet the previous layer, and weld-line strength falls rapidly. The upper nozzle boundary is set by thermo-oxidative stability; polypropylene chain scission accelerates during prolonged residence above 240 °C even with a stabilizer package. A reverse-temperature barrel profile from 220 °C in the feed zone to 230 °C at the nozzle is used to maintain melt compressibility without excessive viscous heating. On production-scale single-screw extruders with 24:1 to 30:1 L/D barrels, pressure fluctuations from unstable melt compression appear as filament diameter ripple; closed-loop laser micrometer control is therefore needed for diameters below 2.85 mm. The build plate should be held at 80–100 °C, and a heated enclosure at 30–50 °C prevents the part surface temperature from lagging the air temperature by more than 10–20 °C during the first 5–10 deposited layers.

    Recommended fused filament fabrication settings for Braskem FL105PP.
    ParameterValue
    Nozzle diameter0.4 mm to 0.6 mm
    Extruder temperature210–240 °C
    Bed temperature80–100 °C
    Enclosure air temperature30–50 °C
    Initial layer print speed15–25 mm/s
    Infill print speed40–60 mm/s
    Layer height0.15–0.25 mm
    Part cooling fan0–20 %
    Feedstock drying60–80 °C for 4–6 h

    Practical failure analysis on unheated desktop systems shows corner lift exceeding 2 mm over a 100 mm span when the bed is below 70 °C and the cooling fan is active above 20 %. In heated enclosures, this deformation is reduced but not eliminated because the part core remains above the recrystallization onset while the outer surface undergoes constrained shrinkage. Extruder feed problems occur when spool winding tension exceeds 2 N; the resulting ovality at the drive wheel reduces bite depth and causes periodic under-extrusion along the infill path. Batch-to-batch melt-flow variation of ±1 g/10 min can shift the onset of stable extrusion by 5–10 °C; the nozzle temperature should be adjusted against a single-batch melt flow rate certificate rather than a fixed generic profile.

    Moisture uptake in polypropylene is sufficiently low that dry-room storage is not mandatory; however, surface moisture from humid environments can create steam pinholes and audible popping at the nozzle. A desiccant dryer operating at 60–80 °C for 4–6 h with an air-supply dew point of −40 °C is recommended before long runs. Filament exposed to 60 % RH at 23 °C rarely shows bulk moisture absorption above 0.05 %, but condensation on the spool surface can cause localized feed-zone slip in direct-drive extruders. Ovality above 0.03 mm produces periodic bite-depth changes in hardened steel drive wheels, visible as under-extrusion bands. For long runs, a hopper purge with the same PP resin is recommended after filament changes from PLA or PA6 to avoid interfacial gel formation in the hot end. Residual PLA can carbonize at PP nozzle temperatures above 220 °C, producing nozzle blockage. A purge sequence consisting of a commercial purging compound followed by 200–300 g of FL105PP is used on production extruders with direct-drive heads.

    Adhesion, shrinkage, and warpage thresholds for unfilled polypropylene

    The linear coefficient of thermal expansion for unfilled polypropylene is 100–150 × 10⁻⁶ K⁻¹ by ISO 11359-2:1999, approximately three times that of unfilled polylactic acid. Semicrystalline shrinkage occurs after solidification and is non-uniform across the layer plane because the center of a bead cools slower than the edges. This produces curl at corners when the bed temperature drops below the recrystallization onset of 115–130 °C. A bed temperature of 80–100 °C does not eliminate shrinkage but reduces the temperature difference between the first deposited layer and the build surface. Interlayer adhesion in printed PP is lower than in amorphous materials because rapid crystallization at the free surface limits polymer chain interdiffusion across the interface. Published data for FL105PP specifically are limited; in unfilled PP printed parts, Z-direction tensile strength is commonly observed to reach only 40–60 % of the XY-direction value when tested by ISO 527-2:2012 on machined specimens. Adhesion to unmodified glass, PEI, and steel is low; a PP sheet or PP-compatible film applied to the build plate provides a semicrystalline bonding surface that avoids acidic or solvent-based adhesion promoters. Bed adhesion troubleshooting on smooth polyimide tape fails because the oxygen-containing surface energy of polyimide is insufficient to wet polypropylene. A mechanically roughened PP sheet with surface roughness Ra 1–3 µm creates a low-energy surface that molten PP can wet without oxidative treatment.

    Material replacement with FL105PP is usually evaluated on density, moisture resistance, and chemical compatibility rather than stiffness. Table 1 compares typical unfilled polypropylene values representative of FL105PP with PLA and dry PA6. The density difference has direct part-mass implications: at equal printed volume, a PP part at 0.90 g/cm³ is approximately 27 % lighter than a PLA part at 1.24 g/cm³.

    Comparative property matrix for unfilled polypropylene filament representative of Braskem FL105PP, PLA, and dry PA6.
    Property and test methodBraskem FL105PP/unfilled PPPLAPA6 dry
    Density, ISO 1183-1:2019 method A0.90–0.91 g/cm³1.24–1.26 g/cm³1.12–1.14 g/cm³
    Saturation water absorption, ISO 62:2008, 23 °C<0.05 %0.3–0.5 %8–10 %
    Tensile modulus, ISO 527-2:2012 type 1A1.2–1.6 GPa3.0–3.5 GPa2.5–3.0 GPa
    Tensile yield strength, ISO 527-2:201230–35 MPa50–60 MPa70–80 MPa
    Elongation at yield, ISO 527-2:20128–12 %2–4 %3–5 %
    Notched Charpy impact, ISO 179-1:20103–5 kJ/m²2–4 kJ/m²5–8 kJ/m²

    The comparative table shows why FL105PP is not a direct stiffness replacement for PLA. Its tensile modulus is roughly half that of PLA; however, the lower density and higher elongation at yield reduce peak stress in snap-fit features. The PP chain has a low glass transition temperature near 0 °C, so printed parts retain impact resistance in cold environments where PLA is brittle. The PA6 comparison is affected by moisture; dry PA6 has higher tensile strength, but after conditioning at 50 % RH at 23 °C, the tensile modulus of PA6 can fall below 1.5–2.0 GPa, eroding its stiffness advantage. For continuous load applications, creep testing under ISO 899-1:2003 is required because polypropylene exhibits time-dependent deformation at stresses well below the short-term yield value.

    When chemical exposure and low density justify replacing PLA or polyamide

    Polypropylene homopolymer is selected for environments where hydrolysis, dilute aqueous acids, and alkaline cleaning agents limit PLA or polyamide service life. Chemical resistance can be evaluated by ASTM D543-21 immersion. Unfilled PP exposed to 10 % sodium hydroxide at 23 °C for 7 d typically shows mass change below 0.5 %, while PA6 absorbs water and plasticizes. In dilute hydrochloric acid, PP retains useful tensile strength if the test temperature does not exceed 40 °C; oxidizers such as fuming nitric acid, chlorosulfonic acid, and hot concentrated hydrogen peroxide degrade the tertiary carbon positions in the polymer backbone. Chlorinated solvents including dichloromethane and chloroform swell and dissolve polypropylene at elevated temperatures, and continuous exposure to aliphatic hydrocarbons above 60 °C is not recommended without permeation testing. For hydrocarbon barrier applications, oxygen and fuel vapor transmission should be measured by ASTM D3985-17 and ISO 15105-2:2023; unfilled PP is a poor gas barrier compared with polyethylene terephthalate or polyamide, and published data for FL105PP printed parts are limited. Environmental stress cracking in polyolefins is accelerated by polar surfactants at elevated temperature; printed parts with residual stress from differential cooling should be annealed at 100–110 °C for 1–2 h before prolonged exposure to detergent solutions. Annealing reduces frozen-in orientation but can produce additional dimensional change; the change should be measured on a printed coupon before modifying CAD scale.

    Regulatory compliance for the filament product is separate from the base resin. Braskem virgin polypropylene grades may satisfy FDA 21 CFR 177.1520 as olefin polymers when the finished article meets end-use limitations and migration thresholds; the filament product does not carry an automatic food-contact approval statement. Under EU directives, virgin polyolefin resins are generally registered under REACH and are not expected to contain restricted substances above the RoHS Directive 2011/65/EU thresholds when unmodified. The material is typically rated UL 94 HB at 1.5 mm thickness, but flammability is thickness-dependent and the rating applies to compression-molded or printed test plaques, not to every geometry. Saturated steam sterilization at 121 °C can deform unsupported printed parts because the heat deflection temperature of unfilled PP under 0.45 MPa is near 90–100 °C by ISO 75-2:2013 method B. Fixturing and low residual stress are required for autoclave cycles; published data for FL105PP after repeated steam sterilization are limited. Post-processing with isopropanol or ethanol does not dissolve polypropylene, but ultrasonic cleaning at 60–80 °C can induce stress relaxation in thin walls. If food-contact use is intended, migration testing should follow EU Regulation 10/2011 or applicable FDA regulatory limits for the specific food simulant and time-temperature condition. The filament is not formulated as a medical-grade resin unless a specific grade designation and supporting biocompatibility data are provided by Braskem.

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