| HS Code | 917948 |
| Base Polymer | Polylactic Acid (PLA) |
| Reinforcement Type | Short Fiber |
| Filler Content | 30 % |
| Density | 1.35 g/cm³ |
| Melt Flow Rate | 10 g/10 min |
| Water Absorption | 0.50 % |
| Moisture Absorption At Equilibrium | 0.20 % |
| Linear Mold Shrinkage | 0.005 cm/cm |
| Tensile Strength Ultimate | 80 MPa |
| Tensile Strength Yield | 80 MPa |
| Elongation At Break | 2.0 % |
| Modulus Of Elasticity | 7.00 GPa |
| Flexural Modulus | 7.00 GPa |
| Flexural Strength | 120 MPa |
| Charpy Impact Notched | 5 kJ/m² |
| Charpy Impact Unnotched | 20 kJ/m² |
| Izod Impact Notched | 5 kJ/m² |
| Rockwell Hardness R | 110 |
| Melting Point | 170 °C |
| Glass Transition Temperature | 60 °C |
| Heat Deflection Temperature At 0 46 Mpa | 150 °C |
| Heat Deflection Temperature At 1 8 Mpa | 100 °C |
| Vicat Softening Point | 160 °C |
| Ul94 Flammability | HB |
| Thermal Conductivity | 0.30 W/m·K |
| Specific Heat Capacity | 1.20 J/g·°C |
| Coefficient Of Linear Thermal Expansion | 30 µm/m·°C |
| Dielectric Strength | 20 kV/mm |
| Dielectric Constant | 3.50 |
| Dissipation Factor | 0.020 |
| Volume Resistivity | 1.00e+15 ohm·cm |
As an accredited FC 10175 Short Fiber Reinforced Rigid Polylactic Acid factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | FC 10175 Short Fiber Reinforced Rigid Polylactic Acid is supplied in 25 kg moisture-barrier foil-lined bags, palletized for industrial shipping. |
| Container Loading (20′ FCL) | 20′ FCL loaded with palletized FC 10175 Short Fiber Reinforced Rigid Polylactic Acid, shrink-wrapped and secured for safe ocean transport. |
| Shipping | FC 10175 Short Fiber Reinforced Rigid Polylactic Acid is non-hazardous and not regulated for transport by DOT, IMDG, or IATA. Ship as general cargo in sealed, moisture-barrier packaging. Protect from heat, sunlight, and moisture. Label with product name, grade, lot, and handling instructions. Store cool, dry, ventilated; avoid open flames. |
| Storage | Store FC 10175 Short Fiber Reinforced Rigid Polylactic Acid in a cool, dry, well-ventilated area, away from direct sunlight, heat, sparks, and ignition sources. Keep containers tightly closed to prevent moisture absorption and contamination. Avoid contact with strong acids, bases, and oxidizing agents. Maintain ambient temperature and moderate humidity. Protect from physical damage. Follow local regulations and the manufacturer’s SDS. |
| Shelf Life | Shelf life typically 12 months when stored unopened in a cool, dry place, away from moisture, heat, and direct sunlight. |
FC 10175 is a short-fibre reinforced rigid polylactic acid compound that is processed for thin-wall electronics housing components only after desiccant drying to a residual moisture ceiling of 250 ppm; a rotary-vane drying unit with dew point at or below −40 °C and inlet air temperature of 80 °C for 4 h is the minimum accepted setup before injection moulding. In moulding trials on 130-tonne hydraulic toggle machines with 25 mm diameter barrier screws at 20:1 L/D, the short-fibre fraction increases melt pressure at the gate by approximately 25–40% relative to unfilled PLA at the same mass flow rate, a threshold that forces runner and gate sizing beyond standard amorphous PLA practice. The material is not a drop-in for flame-retardant ABS in live parts; FC 10175 does not carry a V-0 classification under IEC 60695-11-10 or UL 94 without an external flame-retardant concentrate, and therefore it is assigned only to secondary enclosures, internal brackets, cable-management clips, rear covers, and shielding housings protected from operator contact with primary circuits. For RoHS 2011/65/EU documentation, the binder system contains no intentionally added lead, cadmium, mercury, hexavalent chromium, PBB, or PBDE; if a halogenated flame-retardant masterbatch is used, XRF screening of total bromine is required because bromine at >900 ppm triggers additional OEM-specific limitations. Gate land thickness must not fall below 0.75 mm and the minimum gate diameter is 1.0 mm for sections at or below 1.5 mm, because narrower restrictions produce fibre jamming and short shots in multi-cavity tools. Melt temperature is held between 195 °C and 210 °C; at >220 °C for more than 5 min residence time, hydrolytic chain scission and fibre-matrix separation generate brittle weld lines and silver streaking. Mould temperature is maintained between 25 °C and 40 °C; higher mould temperatures above 45 °C extend cycle time without improving crystallinity above 10–15%. Injection speed of 80–120 mm/s, hold pressure of 40–70 MPa, back pressure of 0.5–1.0 MPa, and screw speed of 80–120 rpm constitute a stable window for 1.2 mm to 2.5 mm wall thickness. Rib height should remain below 2× the nominal wall to avoid sink marks because the fibre-filled material has reduced post-mould creep but not reduced solidification contraction in thick sections.
| Moulding parameter | FC 10175 thin-wall setpoint | Unfilled PLA reference | Test or control method |
|---|---|---|---|
| Melt temperature | 195–210 °C | 180–200 °C | ISO 294-1 |
| Mould temperature | 25–40 °C | 20–30 °C | Tool thermocouple |
| Hold pressure | 40–70 MPa | 30–50 MPa | Machine hydraulic curve |
| Back pressure | 0.5–1.0 MPa | 0.2–0.5 MPa | Screw recovery reading |
| Minimum gate diameter | 1.0 mm | 0.8 mm | Rheological gate sizing |
Post-mould dimensional inspection according to ISO 294-4 and ASTM D955-08 records anisotropic shrinkage because the short fibres orient along the flow boundary during filling. In ejected parts, in-flow shrinkage is typically 0.3–0.6% while cross-flow shrinkage can exceed 0.8–1.2%, depending on gate location and fibre orientation ratio. This differential forces gate placement at the geometric centre of long features rather than at a corner; when two side gates are used, weld lines at the farthest flow fronts must be positioned away from snap-fit bosses and screw bosses because the weld region retains only 50–70% of the unfilled flexural fatigue resistance under ISO 178 reversed-bending conditions. Hole-to-hole tolerance is maintained at ±0.1 mm only when the tool is gated for balanced fill and the part is not annealed; annealing at 100 °C for 1 h improves heat deflection but induces 0.2–0.4% additional anisotropic growth, making post-machining of interference-fit features necessary. Terminal parts in this application include internal monitor frames, cable guide rails, removable service covers, and PCB standoffs; each is designed with a maximum continuous service temperature of 55 °C and no external load exceeding 0.45 MPa.
Substitution is technically viable for non-visible or low-visibility interior components where peak cabin temperature remains below 60 °C and where OEM material engineering specifications do not require long-term UV or heat ageing per PV 1303 or SAE J1885. FC 10175 is assessed against talc-filled polypropylene for door trim brackets, seat side garnish clips, B-pillar lower trim covers, and boot sill covers, not for load-bearing instrument panel substructures. The density advantage is material: unfilled PLA at 1.24 g/cm³ and short-fibre rigid PLA at roughly 1.30–1.40 g/cm³ depending fibre type, compared with talc-filled PP at 1.05–1.10 g/cm³, does not automatically reduce mass because part design must add ribbing to compensate for lower notched impact. Notched Izod impact under ISO 179-1 is typically below 4 kJ/m²; addition of 5–10 wt% ethylene-butyl acrylate impact modifier raises this to 6–8 kJ/m² but lowers flexural modulus and heat deflection. When impact modifier is used, the ratio must remain below 10 wt% or mould release and dimensional stability degrade; screw speed must be reduced to 60–90 rpm and melt temperature kept at 190–205 °C to prevent phase separation of the elastomer phase. Drying is identical: 80 °C for 4 h, dew point −40 °C, residual moisture ≤250 ppm.
Injection moulding tools for automotive interior parts require cold sprue or hot runner systems with valve gates; a three-plate mould with pin-point gates 1.2–1.5 mm diameter avoids fibre orientation defects around bosses. On a two-cavity B-pillar lower trim tool with projected area of 450 cm², a clamp force of 180–220 tonnes is required because short fibre compounds demand higher hold pressure than talc-filled PP to prevent sink and warp. The production bottleneck is not gas entrapment but batch-to-batch variation in fibre length distribution, which changes peak gate pressure by 10–15% at the same melt residence time; incoming material should be matched against the supplier certificate for fibre content and MFR under ISO 1133-1:2022, although published data for FC 10175 specifically under this standard is limited. For sustainability reporting, bio-based carbon content measured under EN 16640 or ASTM D6866 can exceed 90%, but the short fibre itself may be natural or synthetic; if natural fibre is used, long-term humidity at 50 °C and 90% RH must be validated because moisture uptake above 2 wt% reduces stiffness retention below 80%. FMVSS 302 horizontal burn rate for interior materials is not automatically met; FC 10175 as a natural polymer typically burns at 30–40 mm/min in horizontal testing, requiring an intumescent flame-retardant masterbatch at 10–15 wt% for a self-extinguishing result below 100 mm/min. Cabin odour and VOC per VDA 277 and VDA 278 are generally lower than ABS, but lactide residuals in PLA can exceed 50 ppm if the compound is not devolatilized; production melt should include vacuum venting at −0.08 MPa minimum.
Returnable logistics dunnage trays and divider panels moulded from FC 10175 are exposed to repeated alkaline detergents, which makes hydrolysis the primary failure mechanism rather than impact. Unlike polypropylene corrugated sheet, PLA ester bonds cleave at pH above 9 and wet heat above 50 °C; therefore the compound is recommended only for dry-loop or light-wipe sanitation, not for caustic immersion washdown at 85 °C. The blend ratio for cost reduction can include 20–30 wt% post-industrial recycled PLA but each 10 wt% recycled fraction roughly halves the melt-flow stability window, requiring a chain extender at 0.2–0.5 wt% when the recycled fraction exceeds 30 wt%. Because short fibres reduce the ductile failure mode, drop tests at −20 °C are more severe than at ambient; a useful acceptance criterion is no visible crack on a 1 m free-fall of a 5 kg loaded tote onto concrete per ASTM D5276-19. A stacking test under ISO 8611-2 with a load of 3× rated payload for 24 h at 40 °C should produce residual deformation below 2%. If the moulded part includes snap-fit hinges or living hinges, the short fibre content severely reduces flexural endurance; living hinge design is not recommended because fibre ends initiate cracks below 100 cycles in cyclic flexure.
| Compliance requirement | Standard or method | Acceptance boundary |
|---|---|---|
| Residual moisture before moulding | ISO 15512 | ≤250 ppm |
| Low-temperature drop resistance | ASTM D5276-19 | No visible crack at −20 °C, 1 m |
| Stacking creep | ISO 8611-2 | <2% set after 24 h at 40 °C |
| Moisture absorption control | ISO 62 | <0.5% mass gain at 23 °C, 50% RH |
| Recycled content traceability | EN 15343 | Closed-loop dry recycling only |
Single-face moulds for divider panels use a fan gate with thickness 1.5 mm to minimise fibre-orientation-induced bowing; melt temperature is held at 195–205 °C and hold time is 8–12 s per 2 mm wall section. The low-temperature impact issue is caused by the combined action of the rigid matrix and short fibre pull-out; when the temperature drops below the PLA beta transition near −25 °C, the matrix cannot redistribute local stress around fibre ends. Terminal parts include collapsible tote side walls, dunnage trays, divider panels, and pallet feet, all with a maximum stack load of 150 kg per corner foot when the foot diameter is 60 mm and the service cycle is below 500 cycles; beyond this, the PLA phase develops surface microcracks that propagate under alternating load.
FC 10175 used inside electrical enclosures is constrained by glow-wire and comparative tracking index performance. Under IEC 60695-2-11, an unfilled PLA rated HB will not pass glow-wire ignition at 550 °C without an intumescent or phosphorus-nitrogen flame-retardant package; even with 15 wt% ammonium polyphosphate, the material may exhibit afterglow and char collapse. This property cliff limits terminal parts to enclosures where mass is below 0.5 kg and the part is not the sole insulation barrier. Typical applications are smart-meter inner brackets, thermostat backplates, signal repeater housings, and DIN rail covers. The preferred blend ratio is 85 wt% FC 10175 with 10 wt% phosphorus-based flame retardant and 5 wt% impact modifier; this combination enables glow-wire ignition at 750 °C to be attempted, but published data for FC 10175 with this configuration is limited, and each formulation must be tested according to the full IEC 60695-2-13 glow-wire ignition temperature procedure. Comparative tracking index under IEC 60112 is generally below 300 V for unfilled PLA; the short fibre reinforcement does not improve tracking resistance, so creepage distance design must follow IEC 60664-1 pollution degree 2 values rather than assuming CTI ≥600 V.
Injection moulding requires venting along flow ends because phosphinate flame-retardant packages release water at processing temperature; unvented moulds produce surface blisters. Mould temperature should be raised to 40–60 °C when the flame-retardant package is present to reduce plate-out; the trade-off is longer cycle time of 35–45 s for a 2 mm wall. Screw speed must not exceed 100 rpm because the flame-retardant decomposition at high shear begins around 230 °C. The parts are designed with snap-fit arm deflection below 0.8 mm because the flame-retardant additive further reduces elongation at break below unfilled PLA; inserts are not recommended because hoop stress cracks initiate at 0.05 mm interference. Terminal parts are used only below 50 °C and below 85% RH; at higher humidity, the surface resistivity falls and the tracking risk increases. Direct contact with copper or aluminium busbar surfaces must be separated by a polycarbonate insulator because PLA char is not a stable barrier.
Point-of-sale display fixtures in FC 10175 are designed for demountable brackets, shelving clips, corner connectors, and pegboard panels, not for continuous load-bearing beams. The creep modulus of PLA compounds at 23 °C and 50% RH drops to 50–70% of its short-term tensile modulus within 1000 h when stress exceeds 0.45 MPa; therefore shelf load ratings must be derated relative to ABS or glass-filled polycarbonate. A typical 150 mm injection-moulded display bracket with 5 mm nominal wall retains a measured deflection of <2 mm at 3 kg point load; at 5 kg load, creep rate accelerates and failure occurs at the gate corner where fibre orientation planes intersect. Use of 30 wt% post-consumer recycled PLA reduces the continuous load by another 20–30%. The process for cosmetic display parts uses a reverse-temperature barrel profile from 180 °C at the throat to 200 °C at the nozzle, melt temperature 205 °C, mould temperature 30–40 °C, and a hold pressure curve with two-stage decay from 60 to 30 MPa.
Gate location on hidden edges is critical; visible surfaces require a pin-point gate 0.8–1.0 mm but the fibre fraction can cause gate blush, so a tab gate 1.2 mm thick is preferred. Terminal components include injection-moulded corner brackets, pegboard hooks with a maximum cantilever load of 2 kg, and modular shelf clips. Chemical exposure to isopropanol, common in retail sanitization, causes surface crazing within 24 h; ethanol above 30 vol% and acetone must be excluded. For disassembly after service, mechanical fasteners are preferred over solvent bonding because the short fibres concentrate stress at drilled through-holes; when a screw boss is used, the outside diameter must be at least 2× the screw major diameter and the screw engagement ratio must be at least 1.5:1. Traceability of recycled content under EN 15343 is recommended when closed-loop material is used.
Large-format pellet-fed extrusion uses FC 10175 for assembly jigs, robotic gripper soft-jaw blanks, and dimensional inspection fixtures where polycarbonate-ABS printed with short fibre is otherwise specified. The thermal boundary in pellet extrusion is narrower than injection moulding because the material has no melt seal after the screw tip; during printing, drying at 80 °C for 4 h and an active dry hopper with dew point below −40 °C are mandatory. Extrusion temperature between 190 °C and 210 °C at the nozzle, bed temperature 60–70 °C, and chamber temperature below 35 °C produce acceptable interlayer adhesion only if the layer time is below 120 s; above that the previous layer surface cools below 50 °C and interlayer notch impact drops by 40–60% under ISO 179-1. Fibre orientation in large bead deposition follows the toolpath; specimens built with 0° raster at 0.6 mm layer height show tensile strength in the print direction up to 45–55 MPa and across-layer strength below 20–25 MPa; this anisotropy requires process engineers to orient the part so pull-out forces on inserted bushings do not act across layer planes. The compound does not print successfully through nozzles below 0.8 mm diameter because fibre bundles lodge at the internal taper; hardened steel or carbide nozzles are required due to fibre abrasion.
Terminal applications are limited to fixtures used below 55 °C; drill jig bushings should be installed with thermal expansion inserts, not pressed directly into printed holes, because edge brittle failure occurs at interference above 0.05 mm radial stress. If the fixture is used in a coordinate measuring machine environment, dimensional stability after 7 days at 23 °C and 50% RH must be verified; unannealed PLA continues secondary crystallization and can change 0.1–0.3% in length. Direct contact with mineral oil, cutting fluid, or alkaline coolant must be excluded. The additive manufacturing process should be structured according to ISO/ASTM 52900 terminology and the feedstock MFR should be established under ISO 1133-1:2022 before qualifying the machine recipe; published data for FC 10175 in pellet-fed systems is limited, so production runs require a first-article minimum of 5 identical fixtures to establish interlayer variation.
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FC 10175 Short Fiber Reinforced Rigid Polylactic Acid is a melt-compounded thermoplastic compound in which a rigid polylactic acid matrix carries discrete short fibers. The grade is supplied in cylindrical pellet form for injection molding and, where screw geometry permits, profile extrusion. Manufacturer documentation identifies the product by the model designation FC 10175 and lists conditioned physical properties according to ISO 291. The model code does not encode fiber type, average fiber length, or fiber volume fraction; those parameters are reported on the lot certificate. Published data for this specific compound are limited, so the values shown below are indicative for initial screening and must be replaced by lot-specific certificates before tooling is released.
Indicative property matrix for FC 10175 short-fiber rigid PLA:
| Property | Test method | Indicative value |
|---|---|---|
| Density, 23°C | ISO 1183-1:2019 | 1.26–1.33 g/cm³ |
| Melt flow rate, 210°C, 2.16 kg | ISO 1133-1:2022 | 6–15 g/10 min |
| Tensile strength at yield, 23°C | ISO 527-2 | 55–75 MPa |
| Tensile modulus | ISO 527-2 | 4.0–6.0 GPa |
| Flexural modulus | ISO 178:2019 | 4.5–6.5 GPa |
| Notched Charpy impact, 23°C | ISO 179-1/1eA | 4–8 kJ/m² |
| Heat deflection temperature, B, 0.45 MPa | ISO 75-2:2013/B | 90–110 °C |
| Mold shrinkage, parallel | ISO 294-4 | 0.2–0.5 % |
| Mold shrinkage, perpendicular | ISO 294-4 | 0.6–1.0 % |
These values fall within the expected range for a short-fiber PLA compound at 10–20% fibrous reinforcement. The exact fiber fraction affects the modulus and impact balance; the manufacturer should be asked for the specific minimum and maximum limits when writing a purchasing specification.
Addition of short fibers to rigid PLA modifies both the zero-shear viscosity and the shear-thinning response. An unfilled rigid PLA may exhibit a melt flow rate of 15–30 g/10 min at 210°C under 2.16 kg when tested to ISO 1133-1:2022; a short-fiber rigid compound such as FC 10175 typically falls to 6–15 g/10 min under the same conditions. This difference does not represent a simple viscosity multiplier for all shear rates. Fibers rotate and align in the shear field, so the apparent viscosity drops more steeply as shear rate increases. Capillary rheometry on short-fiber PLA systems has reported power-law indices of 0.25–0.40 in the 100–1000 s⁻¹ range. Published data for FC 10175-specific capillary rheometry are limited; however, the observed pressure response in small gates is consistent with the same shear-thinning envelope.
The gate pressure penalty is non-linear. In a 2 mm rectangular edge gate, pressure drop may be 15–30% greater than an unfilled PLA with the same nominal MFR because fibers resist elongational flow at the gate entry. This effect is most visible in multi-cavity tools with unbalanced runner systems, where fiber orientation modifies the effective flow split. Design of experiments on similar short-fiber PLA grades show that an increase in gate land length of 0.5 mm can shift cavity filling and cause flash on the nearest cavities.
Fiber attrition during processing is a critical threshold. The number-average fiber length after compounding and injection molding is lower than the initial pellet length due to shear-induced breakage along screw flights. If the melt is held under high backpressure above 0.8 MPa hydraulic, or if regrind is reused without correction, the average fiber length can fall below 0.2 mm. Below this threshold, stress transfer from the matrix to the fiber is insufficient, and flexural modulus retention degrades more than a rule-of-mixtures prediction would indicate. Maintaining minimal backpressure and avoiding unnecessary shear history are therefore process controls for preserving reinforcement.
Because PLA is hydrolytically unstable in the melt, moisture control is the primary boundary condition. FC 10175 must be dried to a residual moisture level below 250 ppm before molding. A desiccant dryer with a dew point of -40°C or lower and an air flow of 0.5 m/s across the pellet bed is typical. Drying at 80°C for 4 h from sealed bags is a starting point; if the material has been exposed to ambient RH above 60%, drying time extends to 6 h and open-plant handling should be limited to 30 min. Insufficient drying causes hydrolytic chain scission, which raises melt flow rate by 20–80%, produces splay, and weakens the fiber–matrix interface.
Extrusion conditions should be selected to minimize thermal history. For a 20:1 to 24:1 L/D general-purpose screw, the barrel profile from feed to nozzle is typically 175°C, 185°C, 195°C, 200°C. Melt temperatures above 210°C or residence times beyond 10 min at 205°C can initiate thermal degradation. Mold surface temperatures from 20°C to 60°C are permitted; lower mold temperatures reduce cycle time, while 50–60°C improves fiber wetting and surface finish. Screw speed for a 25 mm injection unit should be 60–120 rpm. Backpressure of 0.3–0.6 MPa hydraulic is generally sufficient for a homogeneous melt; higher settings accelerate fiber breakage.
On a 120-ton injection molding machine with a 25 mm screw, screw recovery time increases by 10–20% compared with unfilled PLA. Clamp force requirements are approximately 3–5 kN/cm² of projected area; for a projected area of 200 cm², that corresponds to 60–100 tons. Vent depth should be kept at 0.01–0.02 mm, because the PLA melt does not generate the same vent-clogging residues as some filled styrenic compounds but can flash if vent depth exceeds 0.03 mm.
Short-fiber orientation produces anisotropic mold shrinkage. Near the mold surface, fibers align with flow; in the core, orientation is less ordered. The constrained surface layers shrink differently from the core, so parallel-to-flow shrinkage is typically 0.2–0.5%, while transverse shrinkage is 0.6–1.0%. This anisotropy is larger than in unfilled PLA and is the main source of warpage. On a 150 mm flat plaque, the differential can produce deformation above 0.3 mm if the gate and runner system were designed for unfilled PLA. Mold shrinkage must be measured according to ISO 294-4 on the production tool geometry, not inferred from an un-gated compression-molded plaque.
Gate location and packing pressure dominate warpage correction. Moving the gate to reduce flow-path divergence or increasing packing pressure by 10–20% over the unfilled PLA baseline compensates for the higher shrinkage in the transverse direction. Hold time must cover gate freeze; early gate freeze prevents packing of the core and amplifies anisotropy. In addition, the abrasive nature of some short fibers may require hardened steel tooling or wear-resistant coatings for production volumes above 250,000 cycles. Tool wear data for FC 10175 specifically have not been published.
Comparison to unfilled PLA, long-fiber PLA, and glass-filled ABS requires standard-condition testing because moisture and crystallinity affect all three PLA-based materials. Representative published ranges for screening are given below.
| Property | FC 10175 short-fiber PLA | Unfilled rigid PLA | Long-fiber PLA | Glass-filled ABS |
|---|---|---|---|---|
| Flexural modulus, ISO 178:2019 | 4.5–6.5 GPa | 2.8–3.5 GPa | 6.0–8.0 GPa | 4.5–6.0 GPa |
| Notched Charpy impact, 23°C, ISO 179-1/1eA | 4–8 kJ/m² | 15–30 kJ/m² | 10–20 kJ/m² | 15–25 kJ/m² |
| Heat deflection temperature, B, 0.45 MPa, ISO 75-2:2013/B | 90–110 °C | 50–60 °C | 90–120 °C | 95–105 °C |
| Mold shrinkage, parallel, ISO 294-4 | 0.2–0.5 % | 0.3–0.8 % | 0.1–0.4 % | 0.2–0.6 % |
Relative to unfilled PLA, FC 10175 shifts rigidity upward but reduces notched impact. The reinforcement effect is not without cost: fiber ends act as crack initiation sites, so the material can fail in a more brittle mode. Compared with long-fiber PLA, the short-fiber grade gives lower anisotropy and better thin-wall filling, but the residual fiber length after molding is shorter, so the improvement in impact retention is smaller. Compared with glass-filled ABS, the compound has lower density and lower notched impact at 23°C; the heat deflection temperature of the PLA grade depends strongly on annealing and degree of crystallinity. Glass-filled ABS tested at 23°C after ISO 291 conditioning usually shows less moisture-induced property drift than FC 10175, but the PLA compound must be dried and processed within a narrower melt-temperature window.
RoHS compliance and REACH registration are supplier-level declarations and are not established by the FC 10175 model code alone. Processors should request a material compliance statement if the final part is intended for electrical and electronic equipment.
Application screening has focused on injection-molded housings, brackets, and fixtures where the increase in flexural modulus over unfilled PLA is used to reduce wall thickness or warpage. The compound is not suitable for high-ductility snap-fit designs or parts subjected to repeated impact below 0°C. Service in hot water above 60°C under load is an operational boundary because PLA undergoes hydrolysis. Annealing at 80–100°C for 30–60 min increases heat deflection temperature by raising crystallinity, but it introduces additional shrinkage that must be added to tooling allowances. Regrind content above 20% should be avoided unless mechanical property data on the regrind blend are available, because fiber-length loss and molecular-weight reduction do not follow a simple linear mixing rule.