| HS Code | 971624 |
| Material Name | Polylactic Acid Fiber |
| Chemical Composition | Polylactic acid (PLA), a polyester of lactic acid |
| Renewable Source | Corn starch, sugarcane, or sugar beet |
| Biodegradability | Biodegradable under industrial composting conditions |
| Density | 1.24-1.27 g/cm3 |
| Melting Point | 130-180 degrees Celsius |
| Glass Transition Temperature | 55-60 degrees Celsius |
| Tensile Strength | 2.5-4.5 cN/dtex |
| Elongation At Break | 20-40% |
| Moisture Regain | 0.4-0.6% |
| Uv Resistance | Good |
| Flammability | Low flammability and low smoke generation |
| Dyeability | Dyeable with disperse dyes |
| Production Method | Melt spinning |
| Acid Resistance | Moderate |
| Alkali Resistance | Low |
| Elastic Recovery | Moderate |
| Softness | Soft hand feel |
| Thermal Stability | Limited above 100 degrees Celsius in moist conditions |
As an accredited Polylactic Acid Fiber factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Polylactic Acid Fiber is supplied in 25 kg moisture-resistant woven bags with polyethylene liners, labeled for industrial use. |
| Container Loading (20′ FCL) | Polylactic Acid Fiber loaded into a 20′ FCL container, palletized and secured for safe ocean transport. |
| Shipping | Polylactic Acid Fiber is generally non-hazardous and not classified as dangerous goods for transport. Ship in dry, sealed, moisture-barrier packaging, away from heat, sunlight, and ignition sources. Label with product name, lot, net weight, and handling instructions. No special UN hazard class required. |
| Storage | Store polylactic acid fiber in a cool, dry, well-ventilated area away from direct sunlight, heat, moisture, and ignition sources. Keep in original sealed packaging on pallets, off the floor, to prevent moisture uptake and hydrolysis. Separate from strong acids, bases, and oxidizing agents. Avoid prolonged high temperatures and heavy stacking; rotate stock using first-in, first-out principles, maintaining stable humidity. |
| Shelf Life | Polylactic acid fiber shelf life is usually 12–24 months when stored cool, dry, and protected from moisture, heat, and sunlight. |
Drying of semicrystalline PLA fibre grade containing 1.4 mol% D-lactide and a melt flow rate of 30 g/10 min at 210°C/2.16 kg per ISO 1133-1:2022 precedes meltblown conversion on a 30:1 L/D single-screw extruder with barrel temperature zones set at 180°C, 210°C, 230°C, and 235°C, followed by a 200-mesh screen changer. Residual moisture above 250 ppm hydrolyses the aliphatic ester linkages, lowering intrinsic viscosity below 0.45 dL/g and producing melt droplets rather than continuous filaments at the die. The meltblown die body is held at 235°C ± 2°C, spinneret orifices of 0.25 mm diameter are spaced at 30 holes/cm, and compressed air at 0.45 MPa and 250°C attenuates the extrudate to median fibre diameters of 2–5 μm at a die-to-collector distance of 180 mm. For a 20 g/m² PLA meltblown layer laminated between two spunbond PLA carrier layers for Type IIR medical face masks under EN 14683:2019, differential pressure measured according to EN 14683:2019 Annex C typically falls between 40 Pa/cm² and 60 Pa/cm². Submicron particle capture is not an inherent property of uncharged PLA meltblown media; without corona charging or hydrocharging, 0.3 μm particle filtration efficiency remains below 50% at a continuous airflow of 85 L/min. Inline electrostatic charging of the dry web raises initial efficiency above 80%, but charge decay accelerates above 50% RH, and sustained exposure at 40°C and 85% RH leads to surface hydrolysis, web embrittlement, and measurable tensile loss within 72 h. This filter configuration is therefore specified for low-moisture, single-shift disposable mask production rather than long-duration respirator cartridges.
A spunbond line configured for polypropylene cannot transfer directly to PLA without adjustment of quench air temperature and draw-jet pressure. PLA spunbond resin with nominal melt flow rate of 70–85 g/10 min at 210°C/2.16 kg per ISO 1133-1:2022 is extruded at 230–240°C through a spinneret with 0.35 mm orifices and 6,000 holes/m, then quenched with air at 18°C and 1.2 m/s before slot-jet attenuation at 3,500–5,000 m/min. Filament breaks increase above 5,500 m/min because PLA elongational viscosity is lower than isotactic polypropylene at equivalent melt temperature, and the window between melt fracture and capillary break is narrower than 15°C. Hydrophilic finishing is mandatory for hygiene applications: a sorbitan monooleate ethoxylate or phosphate ester spin finish at 0.3–0.6 wt% on fibre mass reduces liquid strike-through time to <3 s per ISO 9073-8:1995 and improves downstream carding and thermal bonding. The resulting spunbond nonwoven of 40 g/m² is tested for tensile strength using ASTM D5034-21, for tear propagation using ISO 9073-4, and for synthetic blood penetration using ISO 16604:2004 Class 2 at 1.75 kPa. Terminal product specifications for surgical gown reinforcement and isolation gown sleeves require a minimum machine-direction tensile strength of 45 N/50 mm and a hydrostatic head above 300 mm H₂O per ISO 811. Drying prior to extrusion is critical at 80°C for 4 h to below 250 ppm moisture; uncontrolled resin exposed to 60% RH in an open hopper can reach 2,000 ppm within 30 min, causing hydrolysative molecular weight loss and a drop in web tensile strength of more than 20% on a single production shift.
| Downstream segment | Standard designation | Measured property | Production control window |
|---|---|---|---|
| Meltblown mask filter layer | EN 14683:2019 Type IIR | Bacterial filtration efficiency, differential pressure, splash resistance | 20 g/m² PLA layer; ΔP 40–60 Pa/cm²; BFE ≥ 98% |
| Spunbond surgical gown fabric | ISO 16604:2004 Class 2 | Synthetic blood penetration | Pass at 1.75 kPa; basis weight 40 g/m² |
| Ring-spun PLA staple yarn | ISO 105-C06:2010 A1S | Wash fastness of disperse dyeing | Grade ≥ 4 at 60°C |
| Needlepunched crop protection mat | ISO 17556:2019 | Aerobic soil biodegradation | Visible integrity loss 12–24 months at 20°C, pH 5.5–7.5 |
| Bicomponent acquisition layer | ISO 9073-13:2006 | Repeated liquid strike-through time | Third insult <2.5 s at 18 g/m² |
| Automotive door panel substrate | VDA 277:2017 | VOC emission | ≤ 50 μg C/g after aeration |
| Bioresorbable suture | ISO 10993-5:2009 | Cytotoxicity, L929 cell line | Grade 0 or 1 |
In staple fibre conversion, the processing window is defined by fibre-to-metal friction and heat generation in high-speed carding. A 1.7 dtex, 38 mm PLA staple fibre with crimp frequency of 12–16 crimps/25 mm and a tenacity of 32 cN/tex is processed on a flat-top card with cylinder speed 360 rpm, flat speed 120 mm/min, and licker-in speed 800 rpm. Drafting on a single-zone drawframe uses break draft of 1.7, total draft of 8.0, and top roller shore hardness 63 Shore A to limit fibre lapping. Roving twist is set at 60 turns/m; ring spinning of 30/1 Ne yarn uses a twist factor αe of 3.4–3.8 and spindle speed 10,000–12,000 rpm. Yarn evenness measured by ISO 16549:2021 on a capacitance tester typically shows Uster CVm of 11–13% for optimised PLA/cotton blends at 50/50 by mass. Dyeing is performed with disperse dyes at 110°C and pH controlled between 5.0 and 6.0 for 30 min; alkaline scouring above pH 8.0 at 100°C for more than 20 min causes surface pitting and tenacity loss exceeding 15%. Wash fastness is rated according to ISO 105-C06:2010 test A1S, with typical values for dark disperse dyeings of grade 4 or better on PLA-rich substrates. Terminal goods include workwear, athletic apparel, and sock yarns where mild industrial laundering below 60°C is specified.
On needlepunch lines producing biodegradable crop protection mats, PLA staple fibre is blended with jute or hemp at 30/70 by mass to balance initial tensile strength and soil degradation rate. The carded cross-lapped web is pre-needled at 120 punches/cm² and final-needled at 220 punches/cm² on boards fitted with 15,000 needles/m of 0.5 mm gauge. Basis weight ranges from 300 g/m² to 800 g/m², and tensile strength is measured according to ASTM D4595-17 wide-width strip method. A 500 g/m² PLA/hemp mat typically exhibits machine-direction tensile strength of 8–12 kN/m and elongation at break of 25–35%. In neutral to acidic soil at 25°C and 55% RH, aerobic biodegradation under ISO 17556:2019 proceeds through hydrolysis of the PLA component followed by microbial assimilation; visible loss of mechanical integrity occurs between 12 months and 24 months at 20°C soil temperature. Alkaline soils above pH 7.5 accelerate surface erosion and reduce service life below one growing season. The terminal product is used as a weed-suppressing mulch mat in perennial planting rows and as a temporary erosion-control blanket on slopes up to 2:1; installation must avoid dry summer air above 60°C surface temperature because PLA fibre shrinkage initiates at 65°C under zero load.
When PLA bicomponent sheath-core fibre is calendered into a hygiene acquisition layer, the sheath polymer is a low-D-lactide copolymer with a melting point of 130°C and the core is a higher-melting PLA homopolymer at 160°C, coextruded at a 50/50 sheath/core ratio and a fibre fineness of 2.2 dtex. Carded webs at 18 g/m² are bonded on a two-roll calender at 135°C ± 3°C, nip pressure 60 N/mm, and dwell time 0.02 s, producing bond points that retain core orientation and prevent web embrittlement. Liquid strike-through time is measured by ISO 9073-13:2006 in repeated insult mode; the third insult strike-through time remains below 2.5 s when a migration-resistant surfactant finish is applied at 0.4 wt%. Cross-direction tensile strength at 18 g/m² is typically 4–6 N/25 mm per ISO 9073-3, and elongation at break is 25–35%. The moisture regain of PLA is 0.5%, which causes static build-up during carding above 40% RH unless antistatic finish is applied; surface resistivity before finishing is above 10¹² Ω and after finishing below 10⁹ Ω per ASTM D257-14. Terminal product is an acquisition distribution layer for baby diapers and adult incontinence pads, where PLA replaces polyethylene/polypropylene bicomponent fibre at up to 100% of the nonwoven but requires storage below 50°C to prevent thermal shrinkage of the low-melting sheath.
Compression moulding of carded, needled PLA/hemp mats uses PLA staple fibre as a melt-binder phase at 30 wt% with hemp fibre at 70 wt%. The needled mat is preheated in a contact oven at 190°C for 120 s, then transferred to a hydraulic press and compressed at 4 MPa for 60 s in a mould held at 25°C. Cooling below the PLA glass transition of 55–60°C occurs before demoulding to prevent springback. Flexural modulus measured according to ISO 14125 on a 2.5 mm thick trimmed plaque is typically 3.5–4.5 GPa, and tensile strength by ISO 527-4 is 25–35 MPa. Volatile organic compound emission is measured according to VDA 277:2017 by headspace gas chromatography; total VOC values above 50 μg C/g require post-moulding aeration at 60°C for 4 h before interior release. The terminal component is a door panel insert or rear parcel shelf substrate, but continuous service temperature must remain below 50°C to avoid creep and dimensional distortion. Moisture content of the hemp phase must be dried to 2 wt% or lower before moulding; higher moisture causes steam pockets, delamination at the PLA/hemp interface, and flexural modulus loss greater than 20%.
Melt-spun PLA monofilament for resorbable sutures is produced from medical-grade resin with residual monomer below 0.25 wt% and tin catalyst below 10 ppm. The dried resin is extruded at 190–210°C through a 0.5 mm capillary die, quenched in a water bath at 25°C, drawn in two stages to a total draw ratio of 4:1 at 80°C, and annealed under nitrogen at 100°C for 12 h. Straight tensile strength per ISO 527-1 on conditioned monofilament is typically 410 MPa with Young’s modulus of 3.2 GPa; knot pull strength is determined using USP <881> and is typically 55–65% of straight tensile strength due to brittle notch sensitivity. Hydrolysis is bulk-phase; tensile strength loss becomes measurable before mass loss. For a semicrystalline 0.35 mm monofilament in phosphate-buffered saline at pH 7.4 and 37°C, published in vitro data show that tensile strength retention falls below 50% after 12–20 weeks depending on initial crystallinity, while mass loss occurs later as oligomers diffuse from the fibre core. Sterilization by gamma irradiation above 25 kGy causes radical-induced chain scission and reduces tensile strength by 30–40%; ethylene oxide sterilization according to ISO 11135:2014 is preferred, with maximum residual ethylene oxide below 4 mg/m² and residual ethylene chlorohydrin below 9 mg/m² per ISO 10993-7:2008. Cytotoxicity is assessed with ISO 10993-5:2009 using L929 cells and must yield a grade of 0 or 1; skin sensitisation is evaluated according to ISO 10993-10:2021. Terminal formats include USP 3-0 and USP 4-0 monofilament sutures and knitted surgical meshes; clinical handling is limited by fibre stiffness and shape memory that resists flattening during knot tying.
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Polylactic acid fiber is a melt-spun aliphatic polyester in which the stereochemical composition of the polymer backbone controls crystallization kinetics, thermal resistance, and hydrolytic stability. Fiber-grade PLA is supplied as cylindrical or spherical pellets with a density of 1.24 g/cm³ ± 0.01 g/cm³, a melt mass-flow rate of 6 g/10 min to 30 g/10 min at 210°C under 2.16 kg load when tested in accordance with ISO 1133-1:2022, and a residual lactide content below 0.3 wt%. Representative product models include Ingeo 6202D from NatureWorks for staple fiber and spunbond processes and Luminy LX175 from TotalEnergies Corbion for monofilament and multifilament yarns; product model numbers in these portfolios encode D-lactide content, additive package, and melt rheology. The polymer is typically specified with a number-average molecular weight between 80,000 g/mol and 120,000 g/mol and a polydispersity index below 1.8 by gel permeation chromatography against polystyrene standards. In the melt phase, the material behaves as a shear-thinning fluid with a melt density near 1.08 g/cm³ at 230°C and an apparent viscosity of 50 Pa·s to 200 Pa·s at 100 s⁻¹, depending on molecular weight and D-lactide content. These values function as extrusion-control inputs rather than commercial descriptors: a shift in melt mass-flow rate from 15 g/10 min to 25 g/10 min reduces spinline tension and may require spinneret hole diameter or draw ratio changes.
Fiber-grade PLA differs from packaging-grade PLA primarily in D-lactide content, melt viscosity stability, and additive formulation. Packaging-grade PLA often contains D-lactide levels of 4 mol% to 12 mol% to suppress crystallinity and improve thermoformability; fiber-grade PLA used for high-tenacity filament typically contains D-lactide below 1.5 mol% to preserve crystallization under draw, while binder fiber grades may contain 4 mol% to 8 mol% D-lactide to lower melting point to 130°C–150°C for thermal bonding. In melt processing, the critical difference appears as spinline crystallization: low-D PLA crystallizes rapidly under strain at take-up velocities above 1,000 m/min, whereas high-D PLA remains amorphous over a longer draw window. A production-scale single-screw extruder with L/D 30:1 and a barrier screw is typically operated at 220°C to 240°C melt temperature for low-D grades; at 250°C, thermal degradation causes a 5% to 10% loss in intrinsic viscosity within 10 min residence time. Melt filtration through 20 μm to 40 μm sintered metal or screen packs is required to remove gel particles; spinneret pack pressure is maintained between 80 bar and 150 bar to ensure uniform filament denier across a 0.3 mm hole diameter spinneret. Batch-to-batch variation in residual lactide from 0.1 wt% to 0.3 wt% can alter melt viscosity by ±10%, requiring closed-loop extruder speed compensation.
Predrying is performed in a desiccant-bed dryer delivering a dew point of -40°C or lower. The resin is dried at 80°C for 4 h to 6 h to reduce moisture content below 250 ppm; for spunbond lines operating above 200 kg/h, residual moisture below 100 ppm is recommended because hydrolytic chain scission accelerates rapidly above 230°C. A moisture content of 400 ppm at a melt temperature of 230°C can reduce intrinsic viscosity by 0.05 dL/g to 0.10 dL/g within 8 min of barrel residence time. The dried pellets are conveyed with dry air to the extruder throat; exposure to ambient air at RH 60% or higher for more than 15 min can raise surface moisture above the target. Twin-screw compounding extruders with L/D 36:1 are used when masterbatch pigments or nucleating agents are added; distributive mixing is preferred over dispersive mixing to limit shear heating.
Commercial PLA fiber grades are specified by linear density, tenacity, elongation at break, crimp, and shrinkage. The values in Table 1 are representative ranges for a 1.7 dtex staple fiber after mechanical crimping and heat setting at 100°C for 10 min. These values are measured according to ISO 2062:2009 for tensile properties, ISO 1973:1995 for linear density, and ISO 11357-3:2018 for melting temperature. Specification compliance does not guarantee spinline stability; melt rheology, spin finish type, and quench air uniformity on the specific spinning line often control filament break rate more than the certificate of analysis.
| Property | Typical range | Test method |
|---|---|---|
| Linear density | 1.6–1.8 dtex | ISO 1973:1995 |
| Tenacity | 2.8–4.0 cN/dtex | ISO 2062:2009 |
| Elongation at break | 20–35% | ISO 2062:2009 |
| Crimp number | 8–14 crimps per 25 mm | ASTM D3937-21 |
| Moisture regain at 65% RH | 0.4–0.6% | ASTM D2654-89a |
| Melting temperature | 130–180°C | ISO 11357-3:2018 |
| Glass transition temperature | 55–60°C | ISO 11357-2:2020 |
Tenacity in staple fiber form is lower than high-tenacity filament because staple drawing is often limited to 2.5:1 to 3.5:1 to preserve crimp; filament grades can achieve 4.5 cN/dtex to 6.0 cN/dtex at draw ratios of 3.5:1 to 4.5:1, as measured by ISO 2062:2009. Residual spin finish content is controlled below 0.3 wt% because migration kinetics in polymer matrices affect downstream carding and needling.
The thermal behavior of PLA fiber is dominated by the glass transition at 55°C to 60°C, cold crystallization at 80°C to 100°C, and melting at 130°C to 180°C, depending on D-lactide content and thermal history. In differential scanning calorimetry at 10°C/min, low-D PLA shows a single melting endotherm with a peak at 165°C to 180°C; high-D binder grades show a broad endotherm at 130°C to 150°C. Isothermal crystallization half-time at 105°C for low-D PLA is typically 2 min to 5 min, while high-D grades may require 10 min to 20 min; this difference determines thermal bonding window and dimensional stability. During heat setting, the fiber is constrained at 100°C to 120°C for 5 min to 15 min to develop crystallinity and reduce hot-air shrinkage at 60°C to below 5%. A critical processing threshold is 120°C in aqueous dyeing: disperse dyeing at 110°C for 30 min to 45 min yields acceptable color yield without exceeding 10% strength loss, but raising the dyebath to 130°C can reduce tenacity by 15% to 25% due to hydrolytic chain scission. Ironing and consumer drying above 140°C are outside the recommended use window for standard PLA fiber.
Under industrial composting conditions specified in EN 13432:2000 and ASTM D6400-21, PLA fiber is designed to undergo hydrolysis followed by microbial mineralization to more than 90% carbon dioxide within 180 days at 58°C ± 2°C and relative humidity above 50%. Biodegradation in soil or marine water is not a claimed behavior for standard PLA fiber grades; published data for ambient soil degradation of PLA textiles is limited and highly variable. For durable textile applications, PLA fiber is not a direct replacement for PET when the end-use requires hydrolytic stability in hot-wet environments such as autoclaving, industrial laundry at 85°C, or prolonged contact with alkaline detergent above pH 10.
Substitution of PLA fiber for PET on nonwoven and textile lines requires changes to drying, extrusion temperature, quenching, drawing, and downstream bonding. PLA has a melt density of 1.08 g/cm³ at 230°C and a solid density of 1.24 g/cm³, compared with PET at 1.38 g/cm³; this reduces fiber weight per unit length by approximately 10% at equal denier. Melt temperature set points are 220°C to 240°C for PLA versus 280°C to 295°C for PET, which reduces energy input but narrows the operating window because PLA degradation accelerates above 240°C. Quench air temperature for PLA is typically 20°C to 25°C with humidity above 60% RH to prevent static; PET lines often use 20°C to 30°C air with lower humidity. Draw ratios for PLA filament are limited to 3.5:1 to 4.5:1, below PET’s typical 4.0:1 to 6.0:1, because PLA’s lower melt strength causes spinline breaks at higher ratios. In thermal bonding, PLA binder fiber bonds at 130°C to 150°C, whereas PET binder fiber requires 170°C to 200°C; this allows PLA nonwovens to be bonded on calenders set 30°C to 40°C lower. In dyeing, PLA can be dyed with disperse dyes at 110°C, but PET requires 130°C with high-pressure equipment; PLA’s low glass transition means dyed PLA textiles can show dimensional change above 60°C unless heat set.
| Property | PLA fiber | PET fiber | PA6 fiber |
|---|---|---|---|
| Solid density | 1.24 g/cm³ | 1.38 g/cm³ | 1.13–1.14 g/cm³ |
| Melting point | 130–180°C | 245–260°C | 215–225°C |
| Glass transition | 55–60°C | 70–80°C | 40–50°C |
| Tenacity | 2.8–6.0 cN/dtex | 4.0–8.0 cN/dtex | 4.0–7.0 cN/dtex |
| Elongation at break | 20–40% | 15–35% | 25–45% |
| Moisture regain at 65% RH | 0.4–0.6% | 0.2–0.4% | 4.0–4.5% |
| Thermal degradation onset in air | 250°C | 300°C | 350°C |
Operational boundaries for PLA fiber extrusion include a maximum melt temperature of 240°C, a preferred spin pack pressure below 150 bar, and a maximum ambient residence time of 15 min at RH 60% or higher after drying. The resin should not be blended with amine-based additives, strong bases, or certain metal carboxylates that accelerate chain scission; compatibility with common spin finishes is generally acceptable, but high-pH finishes above pH 10 can reduce fiber strength during storage. In compounding, peroxide additives intended for viscosity modification should be avoided unless specifically formulated for PLA because uncontrolled free-radical reactions can reduce molecular weight from 100,000 g/mol to below 60,000 g/mol within minutes. For medical or hygiene applications, the final article must be validated against ISO 10993-5 for cytotoxicity when skin contact is intended, and compostability claims must be substantiated according to EN 13432:2000 or ASTM D6400-21 for the finished article, not the resin alone.