Products

Ingeo™ Biopolymer 6202D Fiber-Grade Staple Fiber PLA

    • Product Name: Ingeo™ Biopolymer 6202D Fiber-Grade Staple Fiber PLA
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
    • CONTACT NOW
    Specifications
    HS Code 421366
    Density 1.24 g/cm³
    Melt Flow Rate 15 g/10 min (210°C, 2.16 kg)
    Relative Viscosity 3.0
    Melting Temperature 165-170°C
    Glass Transition Temperature 55-60°C
    Crystallization Temperature 100-120°C
    Tensile Strength 55 MPa
    Tensile Elongation 30%
    Tensile Modulus 3.5 GPa
    Moisture Content <0.025%
    Pellet Size 3 mm
    Bulk Density 0.8 g/cm³

    As an accredited Ingeo™ Biopolymer 6202D Fiber-Grade Staple Fiber PLA 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 (55 lb) multiwall bags, 40 bags per pallet, stretch-wrapped, totaling 1,000 kg per pallet.
    Container Loading (20′ FCL) 20′ FCL loading: Ingeo™ Biopolymer 6202D Fiber-Grade Staple Fiber PLA, palletized in dry container, moisture-protected, and securely stowed.
    Shipping Ingeo™ Biopolymer 6202D Fiber-Grade Staple Fiber PLA is shipped as a non-hazardous solid in moisture-protective bales, cartons, or bulk bags on pallets. No special dangerous-goods placards are required. Keep dry and away from excessive heat, moisture, and contamination during transport and storage at ambient temperatures.
    Storage Store Ingeo™ Biopolymer 6202D Fiber-Grade Staple Fiber PLA in a cool, dry, well-ventilated area, away from direct sunlight, heat, moisture, and ignition sources. Keep packaging sealed until use. Avoid prolonged storage at high temperatures or humidity to prevent hydrolytic degradation. Maintain clean, compatible conditions; do not store near strong acids, bases, or oxidizing agents.
    Shelf Life Two years from date of manufacture when stored in original packaging under cool, dry conditions, away from moisture and heat.
    Application of Ingeo™ Biopolymer 6202D Fiber-Grade Staple Fiber PLA

    What Calender Surface Temperature Preserves Fiber Identity in Mono-Component PLA Coverstock?

    Before 6202D staple reaches the card, residual moisture is reduced to below 250 ppm using a closed-loop desiccant dryer operated at 80 °C and a dew point of −40 °C for 4 h. The fiber is cut to 38 mm or 51 mm and carded on a nonwoven card with a random doffer to basis weights of 18–40 g/m². Calender bonding is conducted on a two-bowl thermofusion line with an engraved steel roll and a resilient cotton-filled backup roll; bond area is kept between 12 % and 18 %. Surface oil temperature is held in the range 150–165 °C at line speeds from 50 m/min to 120 m/min. At oil temperatures above 175 °C, fiber identity is lost and the web collapses into a film-like structure with CD tensile exceeding 12 N/50 mm but handle stiffness above 40 mN cm, measured on a Handle-O-Meter. At oil temperatures below 145 °C, bond points fracture during conversion and machine-direction tensile drops below 3 N/50 mm per ISO 9073-3:2023. The acceptable processing window is therefore narrower than for polypropylene, and calender gap pressure must be trimmed separately for each basis weight to prevent edge fusion. A 1.2 m wide line processing 20 g/m² coverstock typically requires a linear pressure of 40–60 N/mm. No binder resin is used; the thermoplastic bonding points are generated solely from the PLA staple structure, though 6202D is not a bicomponent fiber and requires higher calender temperature than PE/PP sheath-core staple.

    In absorbent hygiene articles, the thermally bonded web is positioned as topsheet or acquisition distribution layer. Strike-through time is measured by ISO 9073-13:2023; without surfactant modification, the hydrophobic PLA surface yields strike-through times above 10 s and rewet values above 0.5 g. A non-ionic wetting agent is therefore applied at 0.2–0.4 wt% by fiber mass during staple finishing, reducing strike-through time below 3 s on a 20 g/m² coverstock. Acquisition distribution layers made from 6202D are usually combined with cellulosic fluff pulp or superabsorbent polymer via adhesive or ultrasonic bonding. Because PLA melts at a lower temperature than polypropylene, ultrasonic bonding horns are run at 20 kHz with amplitude below 40 µm and line speed synchronized to avoid film formation. Finish selection is limited to non-ionic or anionic systems; amine-based antistatic agents are excluded because residual alkalinity accelerates hydrolytic chain scission during storage at relative humidity above 60 %. The lack of oxidative stabilizers means that storage in direct sunlight for more than 6 months before conversion may embrittle the web; packaging must be opaque and warehouse temperature kept below 40 °C.

    Limitations of mono-component PLA coverstock appear when converters attempt direct substitution into existing polypropylene calender lines without lowering roll temperatures. Polypropylene bonding lines often operate at oil temperatures of 155–165 °C but with lower contact time; PLA requires longer dwell but a lower upper limit. A steel-engraved roll with 16 % bond area and a peripheral speed of 80 m/min produces a dwell time of approximately 20–40 ms. At the upper boundary of 175 °C, melt spots create pinholes below 100 µm diameter detectable by light box inspection at 500 lux. At the lower boundary of 145 °C, bond points exhibit partial fusion and surface fuzz, leading to lint generation above 2 mg/m² in a 10-cycle Martindale abrasion test. Manufacturers running 6202D as a topsheet must therefore operate with a surface temperature differential no greater than 5 °C across the roll face; heated oil systems with individually controlled zones across 1.2 m width are required to prevent edge and centre property drift.

    For ring-spun yarn production on a modified cotton system, 6202D staple with a linear density of 1.3 dtex or 1.7 dtex and a cut length of 38 mm is blended with viscose or combed cotton at mass fractions up to 30 % PLA to limit drafting zone slippage and cylinder loading. The card sliver is processed through two draw frame passages with break drafts of 1.7 and main drafts of 6.0, followed by roving on a speed frame at a flyer speed of 900–1,100 rpm and ring spinning at spindle speeds of 10,000–12,000 rpm. The yarn linear density is commonly 25 tex or 37 tex for circular-knit apparel. Yarn tenacity is evaluated by ASTM D2256/D2256M-21; under standard atmosphere of 20 °C and 65 % RH, the yarn exhibits tenacity from 18 cN/tex to 22 cN/tex and elongation at break from 18 % to 25 %. The low moisture regain of approximately 0.4 % generates static charge during winding; a non-ionic antistatic finish is applied at 0.1–0.2 % add-on. Package hardness and unwinding tension are controlled on a precision winder with a taper angle of and traverse ratio of 2.6 to prevent sloughing.

    Knitted fabric from these yarns is scoured below 60 °C and heat-set on a stenter at 110–120 °C for 30–45 s. Disperse dyestuff exhaustion is performed at 110 °C with a hold time of 30–45 min; dyeing above 130 °C in aqueous medium causes measurable tenacity loss through hydrolytic chain scission, and the bath pH is buffered to 4.5–5.5. Garment ironing is restricted to the synthetic setting below 120 °C. The finished end-products include single-jersey knit tops, undergarments, and technical polo fabrics that do not require high-temperature laundry cycling above 60 °C. In blends with cotton, the PLA portion lowers fabric moisture regain and alters pilling behavior; pilling ratings are assessed by ISO 12945-2:2020, with blended fabrics typically one grade lower than pure cotton after 2,000 cycles due to the lower fiber abrasion resistance.

    Needlepunched Erosion Control Fabrics and the Soil Burial Tensile Boundary

    On erosion-prone slopes, 6202D staple is processed into needlepunched geotextile blankets with mass per unit area from 300 g/m² to 800 g/m². Carded cross-lapped webs are consolidated on a needle loom fitted with 15×18×36×3 barb needles at a board density of 4,000–6,000 needles/m and a needling density of 80–150 punches/cm². Needle depth is adjusted according to mass per unit area; for a 400 g/m² web, a penetration depth of 11–13 mm with a stripper plate gap of 2 mm produces acceptable surface integrity without needle breakage. Wide-width tensile strength is evaluated by ISO 10319:2015. A 400 g/m² 6202D needlepunched fabric typically shows machine-direction tensile strength above 8 kN/m and cross-direction strength above 6 kN/m, with elongation at break in both directions above 40 %. CBR puncture resistance by ISO 12236:2006 is normally above 1.5 kN for the same mass per unit area.

    The soil burial boundary is not controlled by a single material parameter; it shifts with soil pH, temperature, and microbial biomass. Quantitative published data for 6202D under standardized soil burial is limited; site-specific trials are required before specifying the fabric for permanent geotechnical functions. In temperate loam at 28 °C and 60 % water-holding capacity, aerobic biodegradation tests according to ASTM D5988-18 show mineralization lag phases of several weeks, but retained wide-width tensile data after partial degradation are not standardized by ISO 10319 because the standard assumes non-biodegradable filament or staple geotextiles. Therefore, 6202D should be specified for temporary erosion control where the fabric is covered by topsoil or vegetation within one growing season, not for permanent separation or reinforcement layers. Ultraviolet exposure also degrades PLA; uncovered stockpiles lose measurable tensile strength after 200–400 h of accelerated weathering under ISO 4892-2:2013, although this exposure time depends on radiant energy dose and moisture cycling.

    Geotextile property test matrix for needlepunched 6202D fabrics
    PropertyStandard designationTesting condition
    Mass per unit areaISO 9864:200523 °C, 50 % RH conditioning
    Wide-width tensileISO 10319:2015Gauge length 200 mm, strain rate 20 %/min
    CBR puncture resistanceISO 12236:2006Plunger speed 50 mm/min
    Dynamic perforationISO 13433:2006Cone drop from 500 mm
    Characteristic opening sizeISO 12956:2020Wet sieving with glass beads
    Aerobic biodegradation in soilASTM D5988-18Incubation at 28 °C

    Because crimp geometry rather than bonding controls thermal resistance, 6202D staple for high-loft fiberfill is cut to 32 mm or 51 mm, crimped to 10–14 crimps per 25 mm, and treated with a silicone-based finish at 0.15–0.35 % by fiber mass to reduce card clothing friction and improve refluff behavior. The opened fiber is garnetted into continuous batts of 100–300 g/m² and quilted between scoured cotton or polyester shells. Thermal resistance is measured by ISO 11092:2014, with typical clo values for a 200 g/m² batt in the range 0.8–1.2 clo depending on crimp retention and fiber-to-fiber contact area. Wash durability is assessed by five cycles of ISO 6330:2021; acceptable fiberfill retains at least 60 % of original loft, measured by thickness under a 0.5 kPa load.

    Because 6202D softens near 130–150 °C, drying or sterilization of filled textile products above 80 °C is prohibited unless the batt is removed. End-product flammability must be tested under 16 CFR Part 1610 for adult apparel or EN 14878:2007 for children's sleepwear; PLA generally has a lower ignition temperature and higher melt drip than FR-treated polyester, so some markets require a fire-blocking interliner. In cold-weather outerwear and bedding, the melt drip hazard should be evaluated with a full assembled garment or quilt test, not only a fabric-level vertical flame test, because molten polymer can transfer heat to the wearer even when the outer shell self-extinguishes.

    When 6202D Staple Replaces Polyester in Needlefelt Air Filtration Grades

    Once 6202D is substituted into needlefelt air filtration media, the continuous dry-heat ceiling shifts from polyester's 150 °C to a lower PLA operating threshold of 105 °C; excursions above 120 °C cause progressive shrinkage and loss of pleat geometry. The staple is blended with polyester or polypropylene at mass fractions of 30–50 % PLA to maintain mechanical integrity during pleating. Web formation uses a carded cross-lap followed by needlepunching at 200–400 punches/cm², then singeing and calender smoothing to control surface density. Filtration efficiency is classified according to ISO 16890-1:2016; ePM10 and ePM2.5 values depend on basis weight and fiber diameter, with a 550 g/m² needled felt commonly achieving ePM10 above 50 % at 0.2 m/s test velocity. Initial pressure drop for a 550 g/m² felt is typically 150–220 Pa at 0.2 m/s, measured on a filter test rig conforming to ISO 16890-4:2016.

    Operation of 6202D-containing needlefelts in moist gas streams is limited by hydrolytic chain scission. Continuous exposure at relative humidity above 60 % and gas temperatures above 50 °C reduces tensile retention; a decline in burst strength measured by ISO 3303-1:2020 may exceed 20 % within 3–6 months, depending on pH. The media should not be specified for acid mist or alkaline scrubber duties where condensate pH falls outside 4–9. In cleanable dust-collection bags, the upper shock pulse pressure should be limited to 0.4 MPa because PLA fibers are more notch-sensitive than PPS or aramid needlefelts. End products include pleated panel filters for HVAC and dust bag applications where lower-temperature operation aligns with specification requirements, but not high-temperature industrial baghouse service.

    Because 6202D spunlace webs must be dried below 80 °C, hydroentanglement lines running 6202D at web width 1.6 m impose lower drying temperatures than viscose-only webs. Staple fiber of 1.3–2.2 dtex and 38 mm cut length is carded and then subjected to multiple injector passes at water pressures of 60–200 bar to produce spunlace wipes from 40–80 g/m². The absence of binder permits biodegradability but requires a wetting agent to be exhausted onto the fabric at 0.3–0.5 wt%. Absorbency is measured by ISO 9073-4:2021; a 60 g/m² web exhibits water absorption capacity in the range 7–12 g/g. Drying on perforated drum dryers must keep air temperature below 80 °C to limit thermal shrinkage to 2 % in machine direction.

    Rewet and linting are controlled by adjusting injector pressure and belt mesh; excessive entanglement above 200 bar densifies the web and reduces bulk softness, while pressures below 60 bar leave the web too weak for packaging conversion. Converters should avoid wet wipes containing strong oxidizing agents because hypochlorite solutions above 0.5 % available chlorine cause surface pitting and tensile loss within 24 h under immersion at 23 °C. The end product is used for dry and wet wipes, not for disinfecting wipes that require oxidative chemistry. On a standard commercial spunlace line with a 1.6 m width and a line speed of 80–120 m/min, the production rate is limited by dryer capacity rather than entanglement speed, because the PLA web requires longer residence time at reduced air temperature to avoid thermal shrinkage.

    Free Quote

    Competitive Ingeo™ Biopolymer 6202D Fiber-Grade Staple Fiber PLA prices that fit your budget—flexible terms and customized quotes for every order.

    For samples, pricing, or more information, please contact us at +8618136850665 or mail to admin@ascent-chem.com.

    We will respond to you as soon as possible.

    Tel: +8618136850665

    Email: admin@ascent-chem.com

    Inquiry

    Get Free Quote of Ascent Petrochem Holdings Co., Limited

    Flexible payment, competitive price, premium service - Inquire now!

    Certification & Compliance
    More Introduction

    NatureWorks LLC supplies Ingeo™ Biopolymer 6202D as a fiber-grade polylactide (PLA) resin for staple fiber extrusion and spunbond nonwoven manufacture. The grade is specified with a nominal specific gravity of 1.24 (ASTM D792-20), a melt flow rate of 15–30 g/10 min at 210 °C/2.16 kg (ISO 1133-1:2022), and a crystalline melting peak in the range 155–170 °C when measured by differential scanning calorimetry (ISO 11357-3:2018). Glass transition is typically observed between 55 °C and 60 °C. The resin is supplied as cylindrical pellets and must be crystallized and dried before melt processing; residual moisture above 250 ppm hydrolyzes the ester backbone at melt temperatures above 200 °C, lowering intrinsic viscosity and causing filament breaks and die-face deposits during spinning. The optical purity of the polylactide is controlled to yield sufficient crystallization for drawn staple fiber while avoiding excessive crystallinity in the as-spun tow. No single property in this profile is adequate to predict staple fiber performance; fiber tenacity, crimp retention, and thermal shrinkage must be validated on the downstream line.

    Supplier-published typical properties for Ingeo 6202D
    PropertyValueTest method
    Specific gravity1.24ASTM D792-20
    Melt flow rate15–30 g/10 min at 210 °C/2.16 kgISO 1133-1:2022
    Melting peak155–170 °CISO 11357-3:2018
    Glass transition55–60 °CISO 11357-2:2020
    Tensile strength at break53 MPaASTM D638-14
    Tensile modulus3.6 GPaASTM D638-14
    Elongation at break6%ASTM D638-14
    Heat deflection temperature at 0.45 MPa55 °CISO 75-2:2013

    Values are typical for injection-molded test specimens and do not directly predict staple fiber tenacity or elongation.

    How Does Melt Viscosity Govern Spinnerette Pressure Drop and Draw Resonance?

    Melt flow rate alone does not define spinnerette pressure drop; shear viscosity under capillary conditions is the controlling parameter. With an MFR of 15–30 g/10 min, 6202D lies in the lower-viscosity range of PLA fiber grades, making it suitable for multi-hole spinnerettes with capillary diameters of 0.3–0.5 mm and hole L/D ratios of 2:1 to 4:1. Pressure drop across the spinnerette is a function of volumetric throughput, capillary geometry, and melt temperature; die temperature uniformity should be held within ±5 °C to avoid hole-to-hole denier variation above 10%. Draw resonance and ductile-to-brittle fracture are governed by elongational viscosity and cooling rate. PLA fiber extrusion of this grade generally uses melt temperatures of 210–240 °C; the spinnerette temperature is offset 5–10 °C above the melt line to prevent die-face freeze-off. At these temperatures, melt residence time is limited. Published data for 6202D at spinnerette shear rates above 1,000 s⁻¹ are limited; line trials are required to establish the pressure-velocity envelope.

    Extruder configuration for this grade typically uses a single-screw extruder with an L/D ratio of 24:1 to 30:1 and a compression ratio of 2.5:1 to 3:1. A screen pack of 40/60/120 mesh is installed before the melt pump to remove agglomerates. Melt pump volumetric control reduces pressure fluctuations to below ±1 bar; such control is critical because PLA has a sharper viscosity-temperature dependence than polyethylene terephthalate. Process temperatures are profiled from 180 °C at the feed throat to 210–240 °C at the metering section, and screw speed is matched to throughput to maintain melt temperature within ±5 °C. Feed throat flooding or inconsistent pellet shape produces output surging; pellets with high fines content can form clumps in the hopper and should be screened before use. Spinnerette holes are laser-drilled and inspected by borescope; deformation or wear of capillary edges changes draw-down and increases filament breaks. Periodic die-face wiping with silicone-free release agent prevents oligomer accumulation, while silicone-containing release agents should be avoided because they can transfer to fiber and interfere with downstream finish adhesion.

    After exit from the spinnerette, filaments enter a cross-flow quench cabinet. Quench air temperature is maintained at 15–25 °C with a velocity of 0.5–2.0 m/s depending on filament linear density and hole density. A lower quench temperature increases molecular orientation but also increases brittle fracture; a higher quench temperature produces lower orientation and higher residual shrinkage. Spin finish is applied before the first godet set. The as-spun tow is collected into cans at 700–1,200 m/min. The tow is then drawn in a separate process at lower speeds; draw temperatures of 80–110 °C permit segmental motion without excessive thermal crystallization. Inadequate quench air uniformity produces skin-core differences in birefringence, which later appear as crimp inconsistency and poor carding.

    Drawing is conducted in a two-stage hot-water or hot-oil bath; first-stage draw ratio is typically 2.5:1 to 4:1 and second-stage 1.1:1 to 1.5:1. The drawn tow passes into a stuffer-box crimper where crimp frequency is set at 8–14 crimps per inch. Heat-setting of PLA tow is often limited to 90–100 °C because higher temperatures can reduce crimp durability and cause interfilament fusion. The tow is then dried to below 0.5% residual water before cutting. Fiber tensile properties depend on draw ratio and crystallization; for PLA staple fiber, tenacity in the range 2.5–4.0 cN/dtex and elongation at break of 20–40% are common for high-draw staple, but published values for 6202D in specific cut lengths and finish packages are limited. Thermal shrinkage in hot air at 100 °C is typically 5–10% if annealing is insufficient.

    Before extrusion, the pellets are dried in a desiccant wheel dryer with a dew point of −40 °C or lower. Inlet air at 80 °C for 4 h reduces residual moisture below 250 ppm; moisture is determined by Karl Fischer titration (ISO 15512:2018). When ambient relative humidity exceeds 60%, hopper purge with dried air is required to prevent re-adsorption. Drying temperature is limited because PLA pellets can soften and agglomerate near the glass transition; the specified drying profile avoids pellet clumping. Residual moisture above 500 ppm has been associated with bubble formation and intrinsic viscosity losses exceeding 0.1 dL/g in industrial PLA extrusion, with corresponding filament weakness. Hydrolytic degradation follows pseudo-first-order kinetics with respect to ester concentration and dissolved water; doubling residual moisture from 250 ppm to 500 ppm shortens the time to measurable intrinsic viscosity loss. At melt temperatures above 230 °C, lactide regeneration and molecular weight redistribution occur simultaneously, producing volatile lactide that condenses on quench screens and die face. Total residence time from hopper to die exit should be kept below 15 min when melt temperature exceeds 230 °C; longer hold times increase color shift and filament breaks. Additives containing primary amines or strong nucleophiles should be avoided; they accelerate ester cleavage and reduce molecular weight during compounding.

    When 6202D Replaces 6100D or 6201D in an Existing Staple Fiber Line

    Published direct substitution data for 6202D against 6100D or 6201D in identical spinnerette configurations are limited. The principal differentiation is rheological: 6202D is specified for staple fiber and spunbond nonwoven throughput, whereas continuous-filament grades require higher intrinsic viscosity and melt strength for drawn yarn integrity. A line designed for 6100D continuous filament will typically require resetting melt temperature, quench air velocity, and draw ratio to avoid brittle fracture; no single parameter set can be transferred without line trials. 6202D is not recommended as a drop-in replacement for injection-molding grades such as 2003D or film grades such as 4043D because melt viscosity is outside the processing window for those processes.

    Stereochemical composition controls thermal crystallization. PLA with D-isomer content near 1.4% exhibits a crystallization half-time that permits orientation-induced crystallization during drawing but prevents excessive crystallinity in the as-spun tow. If the D-isomer content deviates, the draw temperature window shifts; higher D-isomer content reduces melting point and crystallinity, lower D-isomer content increases crystallization rate and can cause embrittlement in the quench cabinet. Grade-specific D-isomer content should be obtained from the certificate of analysis before modifying draw ratios.

    Staple fiber produced from 6202D is cut to 38 mm for cotton-system ring spinning, 51–76 mm for worsted and semi-worsted spinning, and 60–90 mm for needlepunch nonwovens. Fiber linear density is commonly controlled within 1.3–3.3 dtex; fineness is determined by ISO 1973:2021. Single-fiber tensile properties are measured by ISO 5079:2021. Crimp frequency is set on the tow crimper at 8–14 crimps per inch for carding, with a finish add-on of 0.2–0.8% by mass applied by kiss roll or dip. Nonionic antistats with low water content are preferred; ionic finishes may increase hydrolytic degradation during storage. Carded web formation at production speeds above 150 m/min requires antistatic finish and controlled fiber-to-metal friction; published data for PLA staple at higher speeds are limited.

    Thermal bonding of 100% PLA staple webs is constrained by the narrow interval between melting onset and thermal shrinkage; calender bonding temperatures are typically held at 150–160 °C with short dwell times. Blends with lower-melting bicomponent fibers are preferred for high-speed bonding because the melting point of 6202D is too close to the shrinkage onset to serve as a reliable binder. Needlepunched nonwoven fabrics from 6202D staple can be manufactured with needling densities of 100–300 punches/cm²; tensile and tear strength are determined by ISO 9073-2:1995 and ISO 9073-4:1997, respectively. Fabric stiffness increases with higher needling density and higher draw ratio, but published data for this specific grade in needlepunch constructions are limited.

    Because PLA has a heat deflection temperature near 55 °C under 0.45 MPa (ISO 75-2:2013), 6202D staple is not suitable for applications requiring repeated thermal sterilization above 121 °C or continuous exposure to humid air above 60 °C. Regulatory documentation for Ingeo PLA typically references FDA 21 CFR 177.1550, EU 10/2011, REACH, and RoHS Directive 2011/65/EU. Grade-specific compliance statements must be obtained from the supplier before use in food-contact or medical packaging.

    Top