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NatureWorks Ingeo™ 3D700 3D Printing Biopolymer

    • Название продукта: NatureWorks Ingeo™ 3D700 3D Printing Biopolymer
    • Сайт Factroy: Округ Юду, Ганьчжоу, Цзянси, Китай
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    Код ТН ВЭД 791726

    Как аккредитованный завод по биополимерной 3D-печати NatureWorks Ingeo™ 3D700, мы соблюдаем строгие протоколы качества - каждая партия подвергается строгим испытаниям для обеспечения последовательных стандартов эффективности и безопасности.

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    Применение биополимера для 3D-печати NatureWorks Ingeo™ 3D700

    In high-tolerance monofilament extrusion for fused filament fabrication, the critical process variable is moisture-induced hydrolysis in the feed throat and barrel, because Ingeo 3D700 pellets that have equilibrated above 250 ppm moisture undergo molecular weight reduction before the melt reaches the die, producing diameter fluctuation, reduced tensile strength below the 60 MPa yield strength listed in ISO 527-2:2012, and surface roughness in the wound filament. Drying in a desiccant dryer at 80°C for 4 h with a dew point of -40°C or lower is required, and dried resin is conveyed under dry air to a single-screw extruder having an L/D ratio of 24:1 to 30:1, a three-zone screw, and a melt pump fitted with a 60/80/100 mesh screen pack. The barrel profile is set from 180°C at the feed section to 210°C in the metering section, with a die temperature of 205°C; melt temperature at the die is measured with an insertion thermocouple and should remain within 195°C to 210°C to avoid shear-thinning instability that appears as die swell variation. The molten filament exits through a 1.75 mm or 2.85 mm die, passes through a water bath maintained at 45°C to 55°C, and is pulled by a calibrated take-up unit with an in-line laser diameter gauge that controls the haul-off to hold tolerance at ±0.05 mm. The formulation addition ratio in this scenario is 100% Ingeo 3D700; if spool edge trim and start-up scrap are reused, regrind content is limited to 10 wt% because reprocessing increases melt flow rate above the virgin 6 g/10 min at 210°C/2.16 kg per ISO 1133-1:2022 and shifts final diameter ovality. The downstream production process consists of pellet drying, single-screw plastication, melt filtration, water quenching, diameter gauging, and spooling. Terminal finished product types are FFF/FDM filament spools for desktop and industrial printers. Incoming lots are conditioned at 23°C and 50% RH for 40 h per ISO 291:2008 prior to tensile verification. No ISO diameter tolerance exists for FFF filament; the governing specification is the internal manufacturer standard. Production-scale failure data indicates that when pellet moisture exceeds 250 ppm, die drool accumulates at the die lip within 20 min to 30 min of continuous running, and the resulting filament exhibits a repeating diameter wave that cannot be corrected by haul-off speed alone.

    What Limits Pigment Loading in a 6 g/10 min Melt During Masterbatch Dilution?

    Compounded color filament for FFF requires that masterbatch additives do not shift melt viscosity beyond the range acceptable for downstream filament extrusion. Ingeo 3D700 has a melt flow rate of 6 g/10 min at 210°C/2.16 kg per ISO 1133-1:2022; a PLA-carrier masterbatch is typically added at 2 wt% to 4 wt%, and inorganic pigment loadings above 1 wt% of the final compound are restricted because agglomerates larger than 30 µm cause nozzle plugging in 0.4 mm and 0.6 mm printer nozzles. Compounding is performed in a co-rotating twin-screw extruder with L/D 40:1 and side feed for pigments, followed by a screen pack of 60/80/100 mesh and an underwater pelletizer. The barrel temperature in the twin-screw is held at 190°C to 205°C; residence time is kept below 2 min because PLA undergoes progressive thermal degradation above 220°C, and the measured melt flow rate can drift upward by 0.5 g/10 min to 1.0 g/10 min after a single pass as determined by ISO 1133-1:2022. The downstream production process includes pre-compounding of the masterbatch at a 25:1 to 50:1 let-down ratio, gravimetric feeding with loss-in-weight feeders at ±0.5% accuracy, and re-extrusion into filament on a single-screw line. Industry compliance for pigments used in children's products and general consumer goods is assessed under REACH 1907/2006, RoHS 2011/65/EU, and EN 71-3:2019 migration limits for specific elements; colorants are selected only from those with documented migration below the relevant limits when the filament is intended for toy or school use. Finished products include colored PLA filament, matte PLA filament, and low-gloss PLA for visual prototyping; the terminal parts are not load-bearing and are used for appearance models, packaging mockups, and design verification.

    Field data from twin-screw compounding lines shows that insufficient pigment dispersion in PLA carrier produces visible color streaks that cannot be removed by increasing screw speed, because the local temperature rise above 220°C accelerates depolymerization at pigment-resin interfaces. A melt pump after the screen pack is used to stabilize compound discharge, and the filter holder is inspected at 8 h intervals for gel-particle accumulation.

    Application segmentStandard or referenceParameter evaluated
    FFF monofilament extrusionISO 1133-1:2022Melt flow rate 6 g/10 min at 210°C/2.16 kg
    FFF monofilament extrusionISO 527-2:2012Tensile yield strength 60 MPa
    FFF monofilament extrusionISO 1183-1:2019Density 1.24 g/cm³
    Thermal distortionISO 75-2/BHDT 55°C at 0.45 MPa
    Investment casting patternsASTM D5630-22Ash content below 0.1%
    Toy and school articlesEN 71-3:2019Specific element migration limits
    Electronics assembly aidsRoHS 2011/65/EURestricted substance compliance
    Patient-specific modelsISO 13485:2016 / ISO 14971:2019Quality management and risk management

    Burnout Pattern Expansion, Ash Content, and Shell Cracking in Ceramic Investment Casting

    In investment casting, a PLA pattern printed from Ingeo 3D700 replaces the wax or PMMA pattern in the lost-wax sequence. The material is used at 100 wt%, without plasticizer dilution, because low-volatility plasticizers can remain as ash. If enhanced wicking or lower viscosity is needed, foundries introduce a printed internal lattice instead of adding a filler; published data for PLA-specific wax-addition ratios is limited, and uncontrolled blending with wax changes the coefficient of thermal expansion and the glass transition from the listed 55°C to 60°C range. The printed pattern is coated with a ceramic prime slurry, stuccoed with zircon or fused silica, and dried at 25°C to 30°C and 30% to 50% RH before sealing. During thermal dewax and burnout, the PLA pattern expands above its glass transition, and shell cracking may occur if the furnace ramp exceeds 2°C/min through the 50°C to 100°C interval; the recommended burn-out plateau is 600°C to 650°C for 2 h in an air atmosphere to achieve ash content below 0.1% as measured by ASTM D5630-22. A ceramic shell foundry may use an autoclave dewax stage at 0.6 MPa with a 150°C saturated steam cycle, but this is less common for PLA because water absorption above 0.5% in the pattern induces surface blistering during autoclave; dry flash-fire burnout is preferred. The downstream production process continues with metal pour under vacuum or gravity for aluminum alloys, stainless steel, and titanium aluminide; the PLA pattern has no halogenated residue, avoiding chloride-induced hot cracking in titanium castings. Terminal finished products are investment-cast metal components for aerospace brackets, turbine blade prototypes, and art foundry castings. Process engineers should qualify their shell system with a test pattern containing the same infill percentage and wall thickness as production, because the pattern collapse pressure is a function of printed density, not just material identity. This is a deep-dive process conflict because the material's low 55°C HDT per ISO 75-2/B is not the limiting factor; the limiting factor is the green strength of the ceramic shell during moisture release and the expansion mismatch between PLA and the first prime coat.

    Medical modeling laboratories that print anatomical replicas for pre-operative planning use Ingeo 3D700 at 100% infill or 1.6 mm shells with 10% to 20% triangular infill, depending on whether the model will be cut with oscillating saws. The formulation addition ratio is 0 wt% additives for standard bone-colored prints; if radiopacity is required, barium sulfate is not added to 3D700 because it raises melt viscosity and accelerates nozzle abrasion, and published data for radiopaque PLA-compound certifications is limited. Printing is performed at a nozzle set point of 200°C to 215°C, with a glass build plate held at 55°C and a part-cooling fan operating at 40% to 60% after the first layer. The downstream process follows DICOM segmentation, STL mesh repair to 0.1 mm maximum deviation, and FFF deposition with layer heights of 0.1 mm to 0.2 mm. Quality management for the production of patient-specific models is controlled under ISO 13485:2016, with risk management per ISO 14971:2019; because the models are non-implantable and non-sterile, ISO 10993-5:2009 and ISO 10993-10:2021 are not applied. Terminal products are anatomical teaching specimens and surgical planning models for cranio-maxillofacial, orthopedic, and cardiothoracic procedures. The main limitation is dimensional creep if models are stored above 50°C or exposed to alcohol-based cold sterilants, which craze PLA surfaces.

    When Assembly Jigs Operate Below the 55°C HDT Threshold

    In electronics and light mechanical assembly, additive fixtures printed from Ingeo 3D700 replace machined acetal and aluminum nests in dry, ambient environments. The material is printed at 100 wt% virgin resin, with 4 perimeter walls and 40% rectilinear infill to resist screw torque and clamp preload. The production process uses FFF machines with nozzle temperature 205°C, bed temperature 55°C, and layer height 0.2 mm; printed jigs are then tapped with brass heat-set inserts or fitted with nylon dowels. The applicable quality standard is dimensional inspection under ISO 8015:2011 with general tolerances class ISO 2768-1:1989 for non-critical features; material restriction under RoHS 2011/65/EU applies when fixtures enter electronics manufacturing lines. The terminal products are pick-and-place trays, solder paste stencil frames, wire-routing combs, and go/no-go gauges. The operational boundary is continuous service below 50°C; the heat deflection temperature of Ingeo 3D700 is 55°C at 0.45 MPa per ISO 75-2/B, and localized contact with soldering irons or hot air rework stations above 55°C causes permanent indentation. This is a shallow application zone because the material's function is dimensional, not structural; no secondary crystallization or annealing step is recommended due to the risk of warpage greater than 0.3 mm/100 mm.

    Architectural massing models and thin-section facade studies printed from Ingeo 3D700 are produced at 100 wt% resin with a layer height of 0.12 mm and no added filler. The downstream process begins with a building information model export at 1:200 to 1:500 scale, splitting large facades into interlocking panels with 0.2 mm clearance, followed by FFF printing at 200°C and assembly with acrylic solvent cement. Compliance for display models in public buildings may require flame retardancy certification according to EN 13501-1:2018; unreinforced PLA generally achieves Euroclass E and is not suitable for escape-route installations without additional fire treatment. The terminal product is a temporary design model, competition model, or client review model. Because thin sections below 1.2 mm curl during cooling, the print bed is maintained at 55°C and the build chamber is enclosed to avoid air drafts; this is the only process-specific control required. Published data for architectural model durability beyond 24 months is limited, as PLA dimensionally relaxes under cyclic humidity above 60% RH.

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    Более подробное введение

    NatureWorks Ingeo™ 3D700 3D Printing Biopolymer is a polylactic acid (PLA)-based thermoplastic resin supplied in pellet form for conversion into monofilament feedstock used in material extrusion additive manufacturing. The grade is formulated to provide a controlled melt-viscosity profile for filament drawing, high stiffness in the printed part, and dimensional stability during cooling. In the manufacturer’s published representative data, density is 1.24 g/cm³ when determined in accordance with ISO 1183-1, melt flow rate is 6.0 g/10 min at 210 °C and 2.16 kg when determined in accordance with ISO 1133-1, and tensile yield strength is approximately 60 MPa with tensile modulus of 3.6 GPa when tested to ISO 527-2. The notched Izod impact is approximately 16 J/m under ISO 180/1A, and heat deflection temperature under 0.45 MPa is approximately 55 °C under ISO 75-2/B. These lot-average values should be replaced by the lot certificate for release-critical decisions.

    PropertyTest methodRepresentative value
    DensityISO 1183-11.24 g/cm³
    Melt flow rateISO 1133-16.0 g/10 min at 210 °C/2.16 kg
    Tensile yield strengthISO 527-260 MPa
    Tensile modulusISO 527-23.6 GPa
    Notched Izod impactISO 180/1A16 J/m
    Heat deflection temperatureISO 75-2/B55 °C at 0.45 MPa

    Primary conversion route is single-screw extrusion into 1.75 mm or 2.85 mm filament for fused filament fabrication of jigs, fixtures, inspection gauges, sacrificial tooling, and short-run manufacturing aids. The resin is not supplied as ready-to-use filament. For applications requiring cyclic snap-fit deflection or repeated drop impacts, the higher-impact Ingeo grades should be evaluated against the notched Izod boundary of 16 J/m.

    The Melt Processing Window Requires Closed-Loop Diameter Control

    The melt processing window in filament conversion is narrow enough that closed-loop diameter control is used on production lines. Barrel setpoints are commonly profiled from 170 °C at the feed throat to 200–210 °C in the metering zone; die temperature is held at 190–205 °C. A 25 mm single-screw extruder with L/D 28:1 and a barrier screw is a typical converting configuration; the melt temperature at the die is maintained below 230 °C to limit lactide reformation and molecular weight loss. Melt pressure at the screen pack is controlled below 200 bar; higher backpressure increases residence time and shear heating, which reduces intrinsic viscosity. Filament diameter is measured with a dual-axis laser gauge and maintained at ±0.03 mm for 1.75 mm filament and ±0.05 mm for 2.85 mm filament by closed-loop puller speed adjustment. Quench air temperature is set between 20 °C and 30 °C; uneven cross-flow creates ovality above 0.03 mm, which transfers downward as feed-path variation in the printer extruder. The low melt flow rate of 6.0 g/10 min increases melt strength relative to high-flow PLA, but it also requires higher extruder torque and may reduce maximum volumetric throughput in very high-speed printers.

    For pellet-fed large-format additive manufacturing systems with heated bed and enclosed build chamber, nozzle setpoints between 200 °C and 230 °C are used, with bed temperature maintained at 50–60 °C. The lower bed temperature relative to amorphous styrenic filament grades reduces energy input and permits unheated or lightly heated chambers below 45 °C. Layer adhesion is evaluated by z-direction tensile specimens in accordance with ISO 527-2; published data for z-axis strength of 3D700 in pellet-fed large-format printing is limited, and end users typically establish internal acceptance limits on printed tensile coupons. Warpage in unfilled PLA is controlled by keeping the first-layer bed adhesion zone below the cold-crystallization onset and by maintaining uniform chamber air temperature.

    What Happens When the Grade Is Annealed Above Its Glass Transition?

    The glass transition onset of PLA is near 55–60 °C; as-printed heat deflection temperature under 0.45 MPa is approximately 55 °C (ISO 75-2/B). When components must tolerate service at 80–100 °C, annealing is performed in a forced-air oven with chamber uniformity of ±2 °C. A typical cycle is 80–100 °C for 30–60 min. The thermal treatment drives cold crystallization, raising crystalline content from below 3 % in rapidly quenched filament to approximately 30–40 %; this shifts the heat deflection threshold upward, but published data for annealed 3D700 HDT values is limited and must be validated on the production part geometry. Annealing simultaneously produces anisotropic shrinkage of 0.2–0.5 % in the build plane and introduces distortion in unsupported walls thinner than 2 mm. Aluminum or filled-epoxy fixtures are used to constrain critical dimensions; post-anneal metrology is conducted at 23 °C and 50 % RH according to ISO 291 class conditions. The melting onset remains near 150–160 °C; annealed parts must not approach this range.

    Grade Selection Depends on Notched Izod Boundary and Stiffness Targets

    Grade selection between 3D700, 3D850, and 3D870 depends on the notched Izod boundary and stiffness target. The 3D700 grade is positioned as the high-stiffness, lower-impact formulation; its representative notched Izod impact is 16 J/m (ISO 180/1A). The 3D850 and 3D870 grades are formulated for higher impact resistance and are specified for snap-fits, clips, and parts subjected to repeated drop loads. In fixtures where deflection under load must be minimized, 3D700 is selected when impact requirements do not exceed 16 J/m. Compared with amorphous styrenic filament grades, 3D700 does not require a chamber at 100–110 °C; bed adhesion is achieved at 50–60 °C, and styrene monomer is absent from the resin chemistry. Relative to glycol-modified PET filament, 3D700 has lower density and lower drying temperature, but PETG typically provides higher impact strength and elongation at break; selection for functional tooling therefore requires a defined load case.

    If Residual Moisture Exceeds 250 ppm Before Melt Processing

    PLA is hydrolytically sensitive in the melt; moisture above 250 ppm causes molecular weight reduction, viscosity loss, bubble formation, and filament diameter variation. Resin exposed to ambient RH above 60 % must be pre-dried in a desiccant dryer with dew point of -40 °C or lower. Drying at 80 °C for 4–6 h is standard for pellets; over-drying at 100 °C for extended periods can initiate pellet sintering in the hopper. A closed-loop hopper loader with dry-air purge is preferred over tray drying in humid production environments. Moisture analyzer verification by ASTM D7191 or an equivalent Karl Fischer method is used before startup; batches above 250 ppm are returned to the dryer. Extruder venting must remain closed to avoid moisture re-entry; if the line uses a vented barrel, the vent port must be plugged or maintained under dry-air sweep. Production failure modes associated with under-dried material include intermittent bubble formation at the die lip, filament breakage during winding, and printer nozzle popping during subsequent melt processing.

    Unopened original packaging stored at 25 °C and below 50 % RH has a shelf life of approximately 24 months from the manufacturing date. Opened packaging should be resealed and dried before use. The resin should not be combined with amine-bearing colorants or additives, because amines accelerate polyester degradation. Pigment masterbatches based on PLA or a compatible biodegradable carrier are recommended; incompatible carriers may reduce interlayer adhesion, observed as delamination in ISO 527-2 z-direction specimens. Processing aids that alter melt rheology should be validated through melt flow rate measurement to ISO 1133-1 before production.

    Regulatory Documentation and Test Standard Mapping

    Regulatory documentation differs between lot-specific and application-specific declarations. REACH registration and RoHS 2011/65/EU declarations should be requested from the supplier for the specific lot; general Ingeo resin certifications do not automatically confer food-contact clearance under FDA 21 CFR or EU 10/2011 unless the grade and end application are listed in a specific compliance letter. The test standard mapping in the first table represents physical and mechanical property determinations; thermal properties such as melt onset and glass transition should be reported from differential scanning calorimetry in accordance with ISO 11357-1 and ISO 11357-3 when comparative thermal analysis is required.

    RequirementStandard or directiveVerification boundary
    Restriction of hazardous substancesRoHS 2011/65/EUSupplier declaration for specific lot
    REACH SVHC screeningRegulation (EC) No 1907/2006Current SDS and SVHC list
    Tensile propertiesISO 527-2Injection-molded or printed coupons
    Melt flow rateISO 1133-1Pellets, 210 °C/2.16 kg
    Heat deflectionISO 75-2/B0.45 MPa
    Notched IzodISO 180/1AConditioned specimens
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