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Mitsubishi FGF Recycled PP Glassfiber (30% 3D Printing Polymer

    • Product Name: Mitsubishi FGF Recycled PP Glassfiber (30% 3D Printing 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 622874
    Productname Mitsubishi FGF Recycled PP Glassfiber (30% 3D Printing Polymer
    Manufacturer Mitsubishi Chemical Corporation
    Materialtype Recycled polypropylene with 30% glass fiber
    Basepolymer Recycled polypropylene (PP)
    Reinforcement Glass fiber
    Glassfibercontent 30%
    Recycledcontent Yes
    Processingtechnology Fused Granular Fabrication (FGF)
    Feedstockform Pellets
    Typicaldensity 1.10-1.15 g/cm3
    Typicaltensilestrength 60-80 MPa
    Typicaltensilemodulus 4500-6000 MPa
    Typicalflexuralmodulus 4000-5500 MPa
    Typicalheatdeflectiontemperature 120-150 °C
    Typicalmeltingpoint 160-170 °C
    Typicalprinttemperature 230-270 °C
    Typicalbedtemperature 80-100 °C
    Typicaldryingcondition 80 °C for 4 hours
    Typicalcolor Black
    Chemicalresistance Good against most acids, bases, and solvents
    Moistureabsorption Low

    As an accredited Mitsubishi FGF Recycled PP Glassfiber (30% 3D Printing Polymer factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Packaged in 25 kg sealed moisture-proof bags, stacked on pallets, for Mitsubishi FGF Recycled PP Glassfiber 30% 3D printing polymer.
    Container Loading (20′ FCL) Container Loading (20′ FCL): Mitsubishi FGF Recycled PP Glassfiber (30% 3D Printing Polymer) loaded into a 20′ FCL container for secure export.
    Shipping Mitsubishi FGF Recycled PP Glassfiber (30%) 3D Printing Polymer ships as non-hazardous solid pellets/filament in sealed moisture-barrier bags, drums, or pails. Keep dry, at ambient temperature, away from heat, UV, and contamination. Standard road, sea, or air freight applies; no special hazardous transport classification. Follow local regulations and supplier SDS.
    Storage Store in a cool, dry, well-ventilated place. Keep containers closed when not in use to protect against moisture, dust, and contamination. Protect from direct sunlight, heat, flames, and oxidizers. Avoid prolonged UV exposure and high humidity. Maintain stable ambient temperature. Use first-in, first-out. Keep away from acids, solvents, and strong oxidizing agents. Do not crush or stack excessively.
    Shelf Life Shelf life is typically 12–24 months when stored sealed in a cool, dry place, away from heat, moisture, and direct sunlight.
    Application of Mitsubishi FGF Recycled PP Glassfiber (30% 3D Printing Polymer

    For vacuum-forming mold bodies produced from the supplied Mitsubishi FGF recycled PP glass-fibre granulate at 30 wt% glass loading, the fibre fraction reduces linear mould shrinkage after cooling but increases melt viscosity at the extrusion nozzle. The material is processed through a single-screw extruder with an L/D ratio of at least 24:1; barrel set points are profiled from 195 °C at the feed throat to 230 °C at the die. Layer times below 45 seconds produce interlayer weld strengths above 80% of the in-plane tensile strength when tested according to ISO 527-1:2019. Moisture above 0.02 wt% in the recycled polypropylene feedstock produces splay and void nucleation on machined mold faces; pre-drying at 80 °C for 4 hours in a desiccant dryer with -40 °C dew point is required when ambient relative humidity exceeds 60%. A bed temperature of 95–105 °C and a sealed chamber at 60–70 °C reduce warpage in tools exceeding 1,200 mm in length. Post-print annealing at 100 °C for 2 hours per 25 mm of wall thickness stabilises machined dimensions before tooling release. Compliance for European industrial customers is assessed under REACH Annex XVII of Regulation (EC) No 1907/2006 and RoHS Directive 2011/65/EU Annex II for homogeneous materials; self-declared recycled content follows ISO 14021:2016 and chain-of-custody verification uses ISO 22095:2020 where required by the moulding plant. Finished parts in this segment include vacuum-former plug assists, deep-draw trim fixtures, and replaceable mold face inserts for short-series packaging trays and appliance covers.

    The processing window for interlayer adhesion is narrow. If the die temperature falls below 225 °C, the glass fibres are not fully wetted by the recycled PP melt and delamination appears along the weld line. If the die temperature exceeds 240 °C, the recycled fraction can release volatile organic compounds from accumulated polymer degradation and oxidised fibre sizing; the resulting splay deposits require manual scraping of the nozzle face during continuous builds. A vented screw with a length of 24D and a compression ratio of 2.5:1 is specified for pellet-fed extrusion to remove residual moisture and trapped air from the recycled feedstock. Operators monitor melt pressure at the nozzle; values above 80 bar indicate glass accumulation in the die orifice and trigger a purge cycle with unfilled recycled PP.

    What Limits Recycled-Feedstock Viscosity Stability in Automotive Locating Gauges?

    Automotive assembly gauges and body-in-white locating fixtures require dimensional repeatability after thousands of handling cycles. Batch-to-batch variation in the recycled feedstock produces changes in bead width of ±0.3 mm at equal screw speed, requiring calibration after every silo refill. The target melt flow rate window is 8–15 g/10 min at 230 °C/2.16 kg, tested according to ISO 1133-1:2022. Batches falling below 6 g/10 min produce inconsistent layer fusion at nozzle diameters above 6 mm; batches above 20 g/10 min indicate chain scission and lower flexural modulus. Incoming granulate is checked for viscosity ratio and ash content before line release. The 30 wt% glass fibre fraction is verified by thermogravimetric analysis at 600 °C in nitrogen, tolerance ±2 wt%, or by ISO 3451-1:2019.

    Printing parameters for locating gauges use 8 mm hardened steel nozzle, 5 mm layer height, and extrusion multiplier calibrated to 97–100% of theoretical bead volume. Under-filling below 95% creates intra-bead porosity that reduces edge definition on net-shape fixture surfaces; over-filling above 102% generates ploughing at toolpaths and increases lateral wall pressure. On a production line with a 1,200 mm × 800 mm build envelope, first-layer peel was traced to bed plate emissivity differences across the aluminium tooling plate; a 0.5 mm polypropylene sheet mask restored uniform adhesion. End products include CMM fixture bases, lift-assist gauge nests, and weld-cell gap-check plates. Continuous service temperature is limited to 90 °C because the recycled PP matrix loses creep resistance above this boundary; short-term spikes to 110 °C are permissible only without mechanical load. No amine-based mould release or epoxy-based coatings are applied to locating surfaces without barrier primers, because polar constituents migrate into the polypropylene matrix and destabilise machined bore tolerances. Restricted substance compliance follows RoHS Directive 2011/65/EU Annex II and plant-specific IMDS entry rules for assembly aids.

    When gripper fingers are printed from 30% glass-fibre recycled polypropylene, high-cycle robotic end-of-arm tooling requires machining at contact faces to remove the as-printed surface texture. Glass fibres orient predominantly in the deposition plane, producing in-plane tensile strength in the range 55–70 MPa when tested per ISO 527-4:2021; the Z-direction interlaminar strength is typically 50–60% lower. Gripper fingers with cantilevered load paths therefore require toolpath segmentation that aligns continuous beads along the principal bending axis. The use of 2.5 wt% maleic anhydride-grafted polypropylene coupling agent is limited to situations where the recyclate feedstock already contains residual coupling agent from previous compounding; additional dosing without analytical verification may create excess acid sites and nozzle corrosion. Creep modulus at 23 °C and 1,000 hours falls by 35–45% relative to short-term values according to ISO 899-1:2017, so sustained clamping loads should not exceed 15 MPa surface pressure. Terminal parts include vacuum gripper brackets, tapered nest jaws, and contoured end effector plates; these components are validated under ISO 10218-2:2011 for robot cell integration rather than as structural machine elements. For cleanroom-adjacent assembly areas, particle shedding from cut glass fibres must be controlled by sealing machined edges with a waterborne polyurethane barrier. If the EOAT operates inside an electrostatic discharge protected area, surface resistivity must be measured separately because the glass-filled PP is not inherently static-dissipative.

    Compliance verification matrix for the application segments
    ObligationStandard or referenceApplicable segment
    Restricted substance restrictionREACH Annex XVII of Regulation (EC) No 1907/2006All segments
    RoHS hazardous substance verificationDirective 2011/65/EU Annex IIThermoforming moulds, automotive gauges, robotic EOAT
    Recycled content self-declarationISO 14021:2016All segments where recycled content is claimed
    Chain of custody for recycled materialISO 22095:2020Automotive OEM, marine OEM, construction projects
    Tensile property of anisotropic printed compositeISO 527-4:2021Robotic EOAT, concrete formliners
    Glass-fibre content verificationISO 3451-1:2019Incoming inspection for all FGF batches
    Melt flow rate of regranulateISO 1133-1:2022Incoming inspection for all FGF batches
    Heat deflection temperatureISO 75-2:2013Foundry patterns, thermoforming moulds

    When Foundry Patterns Demand Low Thermal Mass Without Sacrificing Abrasion Resistance

    Foundry matchplates and core boxes printed as low-volume replacements for cast aluminium or machined urethane require abrasion resistance against silica sand and dimensional stability under repeated stripping. The 30 wt% glass-fibre reinforcement raises heat deflection temperature to approximately 130–145 °C at 0.45 MPa when measured according to ISO 75-2:2013, but continuous exposure to core-box vent temperatures above 95 °C causes warpage in webs thinner than 10 mm. The granulate is processed with 4 mm layer height and 6 mm nozzle diameter; printed shells are filled with low-density polyurethane foam to increase bending stiffness without increasing thermal mass. FGF toolpaths use 40% overlap between adjacent beads; lower overlap values leave inter-bead channels that fill with release agent and swell the matrix. Release agents based on medium-chain paraffinic oil are preferred over aromatic solvent carriers; aromatic carriers craze the polypropylene surface after 20–30 cycles and require resurfacing of the matchplate face.

    Machining of foundry pattern faces requires sharp carbide tooling because glass fibres at 30 wt% cause frictional heating at the cut edge; coolant or compressed air is used to prevent local melting. Toolpath offsets of 0.15 mm are maintained from the as-printed surface before finishing. Terminal products include loose patterns for small-batch iron and aluminium casting, split core boxes, and sand-blast mask templates. Dimensional verification is performed on a coordinate measuring machine after 48 hours of room-temperature conditioning; total shrinkage from print to final machined pattern is held within 0.35–0.50% in the X-Y plane and 0.70–0.90% in the Z direction. Published data for this specific recycled FGF grade in foundry service is limited; the dimensional ranges above are based on short-fibre PP-GF30 composite behaviour under thermal cycling.

    In marine plug construction, a recycled polypropylene glass-fibre granulate reduces the need for wooden substructures but introduces a moisture absorption limit of 0.05 wt% after 24 hours water immersion per ISO 62:2008. The material is not suitable for autoclave cure cycles above 110 °C because the matrix creeps under vacuum bag pressure and the glass-fibre sizing degrades. For wet layup and vacuum infusion plug surfaces, the printed blank is sealed with an epoxy tooling paste and polished to a Class A surface; direct exposure of as-printed glass-filled polypropylene to styrene-based resins must be tested for styrene migration into the matrix. Tooling compounds with 30 wt% glass fibre are machined with carbide-tipped cutters at 18,000–22,000 rpm and 0.2 mm depth of cut to avoid fibre pull-out and delamination at bead boundaries. The resulting plugs support small-batch hull fairings, deck hatch surrounds, and composite trim fixtures; service life is governed by cyclic humidity and UV rather than mechanical fatigue. UV stabilisation is required for outdoor storage; published data for unprotected recycled PP of similar filled grade indicates surface embrittlement after 500 hours of accelerated weathering per ISO 4892-2:2013, while a 2 wt% hindered amine light stabiliser masterbatch extends the onset of surface hairline crazing beyond 1,200 hours. No halogenated flame retardant is used because marine OEMs require low smoke and low toxicity compliance for enclosed compartments.

    Glass-Fibre Attrition and Concrete Formwork Liner Durability

    Concrete casting formliners and reusable architectural formwork are printed from this regranulate at a 30 wt% glass-fibre loading that balances flexural modulus against melt processability. Screw-induced fibre attrition during FGF extrusion on production-scale single-screw extrusion heads reduces mean glass fibre length from the compound pellet value of 0.8–1.2 mm to 0.3–0.5 mm in the deposited bead. This reduction lowers flexural modulus by 15–20% compared with injection-moulded plaques from the same feedstock, as measured by ISO 178:2019. Formliner panels are therefore printed with 6 mm wall thickness and 45% bead overlap to retain section stiffness after machining of relief features. The alkaline concrete environment at pH 12.5–13.0 does not hydrolyse the embedded glass fibre below 40 °C, but formwork submerged in wet concrete for more than 72 hours must be sealed with a two-part polyurethane coating because recycled PP contains low levels of polar contaminants that increase water wicking at inter-bead interfaces. Release agents used on these liners include vegetable-oil-based emulsion systems; mineral-oil-based formulations cause swelling of the PP matrix after repeated contact.

    Terminal products include reusable formliners for precast concrete panels, column capital moulds, and edge-form negative templates. Load-bearing formwork is outside the scope of this material; printed liners are intended only to transfer hydrostatic concrete pressure to external steel or plywood supports. Compliance with the European Construction Products Regulation Regulation (EU) No 305/2011 requires verification of release agent compatibility and weathering resistance for the intended service conditions. No load-bearing structural use is permitted without independent mechanical testing of the assembled formwork system under the relevant Eurocode partial safety factors.

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    Certification & Compliance
    More Introduction

    The Mitsubishi FGF Recycled PP Glassfiber 30% 3D Printing Polymer is a pellet-fed fused granulate fabrication feedstock built on a recycled polypropylene matrix carrying a nominal 30% short glass fiber reinforcement by weight. The product designation identifies it as a granular material for screw-extrusion additive manufacturing rather than filament; it is intended for gantry or robotic large-format systems equipped with positive pellet feed, heated build plates, and enclosed or semi-enclosed build volumes. In contrast to unreinforced recycled PP, the glass fiber phase raises tensile modulus from roughly 1.5 GPa to a representative class range of 5.5–6.5 GPa when tested according to ISO 527-2, while lowering elongation at break into the short-fiber-reinforced range. Against virgin PP GF30, the recycled grade carries a wider melt-flow control band and more stringent incoming-stream quality screening because post-consumer and post-industrial source streams introduce viscosity drift, color variation, and occasional ethylene-containing copolymer fractions. Lot-release documentation for this grade is typically organized around melt flow rate, filler content, density, and tensile modulus. The melt flow rate is generally controlled in the range of 8–15 g/10 min at 230°C under 2.16 kg according to ISO 1133-1:2022, while ash content after fiber burn-off is held at 30 ± 2 wt% according to ISO 3451-1:2019. These indices matter more than a single nominal value because recyclate feedstock variability is the dominant source of batch-to-batch shift in processing behavior.

    What Processing Boundaries Govern Large-Format Extrusion of This Grade?

    Pellet drying is the first critical control point. Polypropylene itself absorbs less than 0.05% moisture at 23°C and 50% relative humidity according to ISO 62, but the glass-fiber sizing can carry surface moisture into the melt. Pre-drying at 80°C for 4 h in a desiccant dryer with a dew point of −40°C is required when ambient relative humidity exceeds 60%. Closed-loop drying is preferred; dry-mix desiccant masterbatches do not reliably remove sizing moisture from a pellet bed. Barrel temperature profiles should stage from 180°C at the feed throat to 200°C in the compression zone, 220°C in the metering section, and 230°C at the die. The melt temperature must not exceed 250°C for more than 60 s, because oxidative chain scission and glass-sizing decomposition degrade melt strength, shift melt flow rate, and cause fiber-matrix debonding. On production-scale extrusion heads, a metering-zone process window of ±5°C is observed: below 215°C, melt viscosity increases, screw torque rises, and glass fiber length attrition accelerates, while above 235°C, the melt film loses stability and bead slump increases. Single-stage screws with 20:1–24:1 L/D, 3:1 compression, and hard-faced surfaces are typical; screws designed for pellet-fed FGF should avoid excessive shear in the metering section to preserve fiber length. Nozzle diameters from 2 mm to 6 mm are used depending on bead width. Layer height is generally 1.5–3.0 mm, bead width 3–8 mm, and extrusion multiplier 1.00–1.15. The build plate is held at 90–100°C and the chamber at 60–80°C where possible to reduce semicrystalline shrinkage stress. Since PP GF30 exhibits anisotropic mold shrinkage of 0.4–0.7% parallel and 0.8–1.2% transverse according to ISO 294-4, a polypropylene raft or glass-fiber-reinforced PP tape is normally required for adhesion. Interlayer diffusion in PP proceeds through chain reptation across the weld interface; cooling below 60°C before sufficient entanglement freezes the interface and produces Z-direction weakness.

    Parameter Set point or range Production note
    Pre-drying temperature 80°C 4 h, desiccant dryer, dew point −40°C
    Feed zone 180–190°C Prevent premature melting and bridging
    Metering zone 220–235°C ±5°C process window
    Die/melt temperature 230–245°C Hard limit 250°C
    Nozzle diameter 2–6 mm Select for bead width 3–8 mm
    Layer height 1.5–3.0 mm Single bead, no ironing
    Build plate 90–100°C PP raft or PP tape required
    Chamber 60–80°C Reduce warpage in long beads
    Extrusion multiplier 1.00–1.15 Compensate fiber-filler expansion

    Post-industrial and post-consumer polypropylene streams are compounded with E-glass chopped strand of nominal 4.5 mm length and an aminosilane surface size. The compound contains maleic anhydride-grafted PP as a coupling agent at 1–3 wt%, a hindered phenol/phosphite antioxidant package at 0.3–0.5 wt%, and an acid scavenger. The silane coupling reaction at the fiber interface creates a rigid interphase that raises tensile modulus but reduces elongation at break to 2–4%. Recyclate sources may include ethylene-propylene copolymer fractions from packaging waste, which lower the crystalline melting point to 160–165°C and reduce warpage at the expense of heat deflection temperature. Compliance documentation should include REACH SVHC confirmation, RoHS Directive 2011/65/EU Annex II substance screening, and California Proposition 65 statements where post-consumer content enters consumer goods. Food-contact status is not automatic; specific grade approval under FDA 21 CFR 177.1520 or EU Regulation 10/2011 must be obtained from the supplier before use in food-contact or potable-water components. The material is supplied as cylindrical pellets typically 2–4 mm in length and 2–3 mm in diameter to maintain gravimetric feed uniformity in hoppers and flexible feed tubes.

    The Mechanical and Thermal Property Envelope Demands Anisotropic Testing

    The values below are representative of a 30 wt% short-glass polypropylene compound conditioned at 23°C and 50% relative humidity for 48 h. The exact certificate of analysis for the Mitsubishi recycled grade may differ from these class values; FGF-printed specimens should always be tested in XY and Z orientations because layer interfaces are strength-limiting. Injection-molded data do not transfer directly to large-format printed parts.

    Property Test method Typical value Unit
    Density ISO 1183-1:2019 1.12–1.15 g/cm³
    Melt flow rate ISO 1133-1:2022 8–15 g/10 min
    Tensile modulus ISO 527-2/1A/50 5.5–6.5 GPa
    Tensile strength at break ISO 527-2/1A/50 60–75 MPa
    Elongation at break ISO 527-2/1A/50 2–4 %
    Flexural modulus ISO 178:2019 4.8–5.5 GPa
    Flexural strength ISO 178:2019 95–115 MPa
    Charpy notched impact ISO 179-1/1eA 5–9 kJ/m²
    HDT at 0.45 MPa ISO 75-2/B 140–150 °C
    HDT at 1.80 MPa ISO 75-2/A 125–135 °C
    Mold shrinkage, parallel ISO 294-4 0.4–0.7 %
    Mold shrinkage, transverse ISO 294-4 0.8–1.2 %

    FGF parts are anisotropic. Tensile strength in the Z direction commonly reaches 50–70% of XY strength because interlayer weld lines contain residual air and disrupt fiber orientation across the interface. The heat deflection temperature applies to short-term thermal exposure; under continuous load above 80°C, creep modulus decreases and tooling can deform. Autoclave tooling above 100°C is outside the operational boundary of this PP-based material. Published fatigue data for this exact recycled FGF configuration remains limited; cyclic load-bearing components should be validated on printed dogbones according to ISO 527-2 in the intended print orientation before production release.

    When Recycled PP GF30 Replaces ABS or PA6 in FGF Tooling

    Against a virgin PP GF30 compound, the recycled grade lowers feedstock carbon intensity but introduces broader melt-flow and color variability. The mechanical envelope is generally within 85–100% of virgin PP GF30 because the glass fiber fraction dominates stiffness; tensile strength is more sensitive to recyclate quality and may fall 5–15% depending on the post-consumer fraction. Against unreinforced recycled PP, the 30% fiber content raises tensile modulus from 1.3–1.8 GPa to 5.5–6.5 GPa and raises HDT at 0.45 MPa from 85–100°C to 140–150°C, while elongation at break falls from above 50% to 2–4%. Against ABS GF30, this PP grade has a lower density of 1.12–1.15 g/cm³ compared with approximately 1.20 g/cm³ and offers better resistance to dilute acids and alkalis, but it has lower surface hardness and lower tensile strength. ABS GF30 typically reports tensile strength in the range of 75–95 MPa. Against PA6 GF30, the recycled PP grade absorbs markedly less moisture—below 0.1% at saturation versus 2.5–3.0% for PA6 according to ISO 62—but PA6 GF30 provides higher tensile strength in the range of 170–190 MPa, higher heat deflection, and greater resistance to aromatic hydrocarbons. Against other PP-based FGF feedstocks, this grade differs primarily in fiber loading: a 20% glass fiber grade has lower stiffness and warpage, while a 40% glass fiber grade increases screw and nozzle abrasion and raises Z-direction brittleness. The recycled content also distinguishes this product from mineral-filled PP grades, which have lower density and lower anisotropy but do not achieve the same tensile modulus at equivalent loading.

    Thermoforming tools, assembly jigs, robotic end effectors, and sacrificial mandrels represent the primary application envelope. The coefficient of linear thermal expansion in the flow direction is typically 3.0–4.0 × 10⁻⁵ K⁻¹ according to ISO 11359-2, roughly half that of unreinforced PP, permitting moderate-temperature layup tools up to 80°C. Dimensional stability under load is not sufficient for injection mold inserts or autoclave cycles exceeding 100°C. In chemical service, the PP matrix resists mineral acids, alkalis, and aqueous salt solutions at 23°C according to ISO 22088-2 stress-crack screening, but strongly oxidizing acids, aromatic hydrocarbons, and chlorinated solvents cause attack or environmental stress cracking. Outdoor service requires UV stabilization; without a hindered amine light stabilizer package or carbon black, PP GF30 surfaces chalk and embrittle within 12–24 months. Post-processing by machining releases glass fiber dust, requiring local exhaust ventilation and respiratory protection. The material is not considered food-contact-capable unless the supplier provides a specific approved grade and the FGF process is validated to prevent surface voids that retain contamination.

    Receiving inspection should include melt flow rate, ash content, density, and a printed XY tensile specimen. Fiber length attrition through the screw is a known production-scale effect: a nominal chopped strand of 4.5 mm can reduce to a mean post-extrusion length of 0.3–0.6 mm, which reduces tensile strength by 5–10% relative to a well-molded specimen. Screw speed and backpressure therefore control final fiber length distribution. Differential scanning calorimetry according to ISO 11357-3 should show a crystallization peak between 115°C and 125°C. If the peak shifts below 110°C, the batch may contain higher ethylene or impurity fractions and should be quarantined or processed with a lower chamber temperature. Because the product is pellet-fed, bulk density, pellet geometry, and feed-throat bridging must be evaluated on the specific extruder hopper; pellets of 2–4 mm length and 2–3 mm diameter are typical for uniform gravimetric feeding. No extension of the processing window should be attempted without rheological verification on the target extrusion head.

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