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L100-M Injection Molding High Crystallinity Polylactic Acid

    • Product Name: L100-M Injection Molding High Crystallinity Polylactic Acid
    • 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 847035
    Material Type Polylactic acid (PLA)
    Grade Type Injection molding, high crystallinity
    Density 1.24-1.25 g/cm³
    Melt Flow Rate 10-20 g/10 min at 190 °C and 2.16 kg
    Glass Transition Temperature 55-60 °C
    Melting Temperature 165-180 °C
    Crystallinity High, typically >40%
    Tensile Strength 60-70 MPa
    Tensile Modulus 3.0-3.6 GPa
    Elongation At Break 2-5%
    Flexural Modulus 3.0-3.8 GPa
    Flexural Strength 90-110 MPa
    Notched Izod Impact Strength 15-30 J/m
    Heat Deflection Temperature 120-140 °C at 0.455 MPa
    Vicat Softening Temperature 140-160 °C
    Rockwell Hardness 75-85 HRR
    Processing Melt Temperature 190-230 °C
    Mold Temperature 100-120 °C
    Drying Temperature 80 °C
    Drying Time 4 hours
    Biobased Content 100%
    Industrial Compostability Yes

    As an accredited L100-M Injection Molding High Crystallinity Polylactic Acid factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing L100-M Injection Molding High Crystallinity Polylactic Acid is packaged in 25 kg moisture-barrier, foil-lined bags on pallets for industrial shipping.
    Container Loading (20′ FCL) Container Loading (20′ FCL): L100-M high-crystallinity PLA injection molding grade, palletized bags, shrink-wrapped, strapped, and securely loaded for export.
    Shipping L100-M Injection Molding High Crystallinity Polylactic Acid is a non-hazardous polymer resin. Ship in sealed moisture-barrier bags, drums, or supersacks via standard freight. Protect from moisture, heat, sunlight, and contamination. Not regulated by DOT, IMDG, or IATA. Keep packages closed, labeled, and dry.
    Storage Store L100-M Injection Molding High Crystallinity Polylactic Acid in a cool, dry, well-ventilated area. Keep containers tightly closed, palletized, and away from moisture, heat, direct sunlight, and ignition sources. Maintain low humidity and temperatures below 30°C. Use original packaging, reseal opened bags promptly, protect from physical damage, follow FIFO, observe supplier shelf-life recommendations, and avoid incompatible chemicals or strong odors.
    Shelf Life Shelf life is 24 months when stored in a cool, dry, well-ventilated area in original, unopened packaging, protected from moisture and heat.
    Application of L100-M Injection Molding High Crystallinity Polylactic Acid

    Commercial injection moulding of reusable PLA drinkware and hot-fill trays with L100-M does not permit the broad barrel-temperature flexibility of amorphous PLA. The material exhibits a crystallization rate plateau between 100°C and 110°C; below 95°C, spherulite growth is too slow to lock geometry before ejection, and above 115°C, cycle time increases while the gate region is exposed to thermal degradation that releases lactide and acetaldehyde. Drying is run in a desiccant dryer with supply dew point at -40°C, bed temperature of 80°C, dwell not less than 4 h, and hopper outlet moisture controlled below 250 ppm by Karl Fischer titration. Barrel settings from feed to nozzle of 180°C, 190°C, 200°C, 205°C, 200°C are used with a 22:1 L/D screw and compression ratio 2.5:1. Melt temperature at the nozzle is held between 210°C and 215°C using an immersion thermocouple; melt flow rate after drying is typically 10–20 g/10 min at 210°C/2.16 kg, tested per ISO 1133-1. Fill speed is trimmed to 25–40 cm³/s for 2.0 mm wall sections. Lower speeds cause gate freeze before packing; higher speeds produce shear heating above 240°C and surface splaying at the gate. Mold halves are conditioned with a pressurized water thermolator at 100°C for the A-side and 110°C for the moving side. The hot runner is externally heated and uses valve gates; cold runner pressure drop lowers cavity melt temperature by 8–12°C and destabilizes the process. A 1200 kN hydraulic injection moulding machine is required for a 4-cavity drinkware tool with 32 g shot weight.

    Fully crystallized L100-M parts measure 1.28–1.30 g/cm³ density per ISO 1183-1. Crystallinity is checked on first heating DSC as the melting endotherm minus cold crystallization enthalpy, divided by 93 J/g for fully crystalline PLA. Hot-fill parts are rejected if the cold-crystallization peak remains above 2 J/g. Heat deflection temperature under ASTM D648 Method B at 0.455 MPa is 95–105°C for 4 mm specimens; local thickness reductions around bosses lower the effective HDT below 90°C and must be evaluated by thermal imaging after filling with 85°C water. Food-contact compliance is verified under EU No 10/2011 with an overall migration limit of 10 mg/dm² in simulant A for aqueous hot-fill. The exact L100-M formulation must also carry the applicable US FDA Food Contact Notification; plant regrind above 10% triggers additional migration testing because the second heat history shifts low-molecular-weight species to the surface.

    Does High-Crystallinity PLA Survive the Brew Chamber Without Post-Mould Annealing?

    Single-serve beverage capsules molded from high-crystallinity PLA are subjected to a pressure pulse at 90–95°C when the brew chamber closes. The dominant failure is not instantaneous burst but creep deformation of the sealing rim. Capsules produced with amorphous PLA rims distort under the 44 mm sealing ring load, allowing bypass flow. L100-M molded with a cavity wall temperature of 100°C reaches rim flatness deviation below 0.10 mm after a 90°C water spike of 30 s. The capsule wall thickness is 0.35–0.50 mm; high-velocity injection above 50 cm³/s is required to fill before solidification, but shear rates over 80,000 s⁻¹ at the 0.5 mm valve gate reduce molecular weight and create silver streaking. Back pressure is held at 5–10 bar. Nozzle pressure at switchover to holding phase is set at 60–70 MPa; holding time is kept short, 0.3–0.5 s, because the gate freezes almost immediately in the thin wall. Clamp force on an 8-cavity capsule tool is 1000–1500 kN.

    The central process conflict is that a mold temperature high enough for rim crystallization of 95–100°C extends cooling time to 25–40 s, while high-output capsule lines require cycle times below 12 s. Hybrid tooling uses conformal cooling in the body to hold 60°C while the rim and flange area remain at 95–100°C. This differential cooling creates a gradient structure; the rim may exceed 30% crystallinity while the thin body remains below 15%. The low-crystallinity body retains enough ductility for rapid ejection; microtensile strips cut from the body exhibit elongation at break above 2.5% per ISO 527-3, whereas the crystallized rim falls below 1.5%. Cooling channels are cut to 0.8 mm from the cavity surface to improve heat transfer; mold trials log in-cavity pressure transducers to detect imbalanced filling across the 8 cavities. Published data for L100-M in this exact configuration is limited, and process parameters must be confirmed on the specific high-speed tool.

    L100-M alone does not provide oxygen barrier for roasted coffee. The oxygen transmission rate is several times higher than PET or PP/EVOH structures; a separate internal liner or outer scavenging layer is required for shelf life above 2 months. Burst resistance is validated on a burst tester ramping to 2 MPa at 95°C. Parts with gate blush or mold-fill weld lines consistently fail below 1.2 MPa; gate design is therefore optimised by short-shot analysis before production. Dimensional stability after brewing is measured by a 90°C water immersion test for 60 s, not by dry HDT alone.

    Dimensional Stability, Stress-Whitening Thresholds, and Fragrance Contact Limits

    Airless dispenser components molded from L100-M are selected for the temporary high modulus required to hold a snap-fit under spring return load. Flexural modulus measured per ISO 178 on 4 mm specimens is 3.8–4.2 GPa after full crystallization. Draft angles below 0.5° are not recommended because high crystallinity raises ejection friction and produces white marks on vertical ribs; ejection force is logged on each cycle with strain-gauge ejector pins, and forces above 8 kN signal a draft or surface texturing issue. Gate stress-whitening occurs when nozzle melt temperature drops below 195°C or when injection velocity exceeds 45 cm³/s through a 0.8 mm pin gate. The tool is run at 100°C mold temperature, and parts are ejected after the cavity pressure decays below 0.5 MPa to avoid gate breakout.

    Fragrance contact is a rejection risk. Lipophilic ester-based fragrance systems are absorbed into PLA and plasticize the surface, causing a tacky feel and a reduction in surface hardness from 80 Shore D to 70–72 Shore D after 72 h immersion at 23°C. Chemical resistance screening follows ISO 175 with the actual formulation; visual change is ranked against a laboratory grey scale, and a drop of more than 2 grades disqualifies the material. Dimensional stability under humid conditions is influenced by water absorption. PLA absorbs 0.3–0.5% water at equilibrium per ASTM D570; snap-fit diameters can expand by 0.1–0.2 mm when moved from 23°C/50% RH to 40°C/75% RH for 72 h. Tools are cut to compensate for post-mould shrinkage of 0.8% in flow direction and 1.0% across flow after 48 h at 23°C.

    Parts ejected from a mold at 100°C retain about 0.2% internal stress. Annealing at 80°C for 20 min removes 60–70% of that stress but produces a further shrinkage step of 0.2–0.4%. Cosmetic components with tight cap-to-bottle fit are therefore gauged after annealing, not immediately after ejection. Tamper-evident closures made from L100-M limit regrind to not more than 20%; the second heat history accelerates crystallization and narrows the injection window because the melt begins to crystallize prematurely in the hot runner.

    In greenhouse clips and vine fasteners, the selection criterion shifts from thermal resistance to hydrolysis resistance. L100-M molded at 100°C and used in soil-contact or high-humidity environments retains approximately 80% of initial flexural strength after 6 months at 25°C and 80% RH, tested per ISO 178. Continuous saturated conditions above 50°C degrade PLA by hydrolytic chain scission, and clips lose functional stiffness within weeks; the application is therefore limited to temperate horticulture, not steam-sterilized substrates. Unstabilized PLA develops surface chalking and measurable tensile strength loss after 500 h in a QUV weathering chamber; multi-season outdoor use requires a UV stabilization package pre-validated with the exact L100-M formulation. The application is a shallow zone: no special prototyping is required beyond standard tensile and flexural coupons because the failure mode is gradual and non-safety-critical.

    The matrix below consolidates the critical input variables, test methods, and rejection thresholds discussed in the preceding application scenarios.

    Downstream segmentCritical input variableTypical acceptable windowGoverning testSpecific limitation
    Hot-fill containersResidual moisture after dryingbelow 250 ppmKarl Fischer titrationHDT B at 0.455 MPa is 95–105°C; no cold-crystallization peak above 2 J/g
    Coffee capsulesRim mold temperature95–100°C rim, 60°C bodyISO 527-3Burst not below 1.2 MPa at 95°C; oxygen barrier not provided by L100-M
    Cosmetic packagingNozzle melt temperature and gate velocity200–215°C; not exceeding 45 cm³/sISO 178, ISO 175Fragrance sorption reduces surface hardness by 8–10 Shore D; no regrind above 20%
    Agricultural clipsService relative humidity25°C and 80% RHISO 178Retains at least 80% strength at 6 months; not for saturated service above 50°C
    Electronics framesWall thickness and service temperature1.5 mm; service below HDTUL 94, IEC 62368-1HB documentation only; no V-2, V-1, or V-0 without pre-validated FR package
    Medical housingsSterilization temperatureEtO chamber 37–55°CISO 11135, ISO 10993-5Residual EtO below 4 mg/device; not for autoclave at 121°C

    When Low-Voltage Frames Require UL 94 HB Without Flame Retardants

    Internal brackets and low-voltage housing frames use high-crystallinity PLA only when the service temperature remains below the HDT and the component is not a fire enclosure. A 1.5 mm thick specimen molded at 105°C can achieve a comparative tracking index above 400 V per IEC 60112, but the material is not specified for creepage-critical circuits. Weld lines at the intersection of side ribs lower tensile strength by 25–40% relative to unreinforced material, as measured by ASTM D638 Type I specimens cut across the weld. Gate placement is moved to the thickest wall to avoid a weld line at a retaining hook. The part is evaluated under IEC 62368-1 for low-voltage equipment; material documentation must list UL 94 HB at minimum for non-fire enclosure use.

    Because PLA is not inherently flame retardant, use in enclosures requiring V-2, V-1, or V-0 is outside the application envelope unless a specific FR additive package is pre-validated with the exact L100-M formulation. The flow length is limited to 120–150 mm for 1.0 mm wall thickness at 200°C melt temperature; longer flow paths require multiple gates and create additional weld lines. A two-plate tool with a hot runner is used for internal frames to reduce cold sprue regrind, since secondary heat history from regrind accelerates crystallization and causes short shots in thin ribs. Clamp force for a 4-cavity electronic frame tool with 14 g total shot weight is 900–1200 kN.

    EtO Sterilization Replaces Autoclave Exposure in Diagnostic Housings

    Non-implantable diagnostic housings molded from L100-M are processed only for low-temperature sterilization cycles because the HDT at 0.455 MPa does not support steam autoclave at 121°C without gross distortion. Ethylene oxide sterilization under ISO 11135:2014 with a chamber temperature of 37–55°C and relative humidity of 60–80% does not exceed the onset of cold crystallization, but it requires aeration to reduce residual EtO to below 4 mg/device per ISO 10993-7. Cytotoxicity is evaluated per ISO 10993-5 on extracted media; PLA grades containing tin-based catalysts require tighter lot acceptance criteria for tin residues. Gamma irradiation at 25–40 kGy causes chain scission and recombination in PLA; tensile strength after 25 kGy can decline by 10–20%, and the part may yellow. Electron-beam irradiation at the same dose generates less heat exposure and can be used only when the total heat rise remains below 55°C.

    In-use mechanical testing uses ASTM D638 at 23°C and after conditioning at 40°C/75% RH for 72 h. The benefit of high-crystallinity morphology is a lower initial extractables profile; amorphous regions are more accessible to extraction solvents, so molders must verify that mold release is not carried into final parts. Extractable metals from processing equipment and mold steel are measured by ICP-MS after 24 h in 50% ethanol/water at 37°C. Devices with integrated snap fits are subjected to a 10-cycle assembly-disassembly test under a minimum force gauge; failure at the gate or weld line before cycle 10 is cause for tooling adjustment. The grade is not recommended for implantable use; published data for L100-M in long-term tissue contact is limited, and the processing package should be qualified by the end user under the relevant medical device quality system.

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    Certification & Compliance
    More Introduction

    L100-M Injection Molding High Crystallinity Polylactic Acid is a poly(L-lactide)-rich biopolyester supplied as pellets for short-cycle injection molding of dimensionally stable rigid parts. The grade is characterized by a narrow D-lactide isomer window of 1.0–1.5 mol%, which preserves chain regularity and accelerates crystallization when the mold surface is held above the cold-crystallization onset. Representative data from the product specification sheet indicate a density of 1.25 g/cm³ per ISO 1183-1:2019 and a melt flow index of 15–30 g/10 min at 210 °C under a 2.16 kg load per ISO 1133-1:2022. Total residual lactide is specified below 0.3 wt%, and bulk moisture in sealed original packaging is maintained below 400 ppm. These properties place L100-M in the medium-flow segment for thin-wall parts down to 1.0 mm nominal wall when balanced gates and end-of-fill vents are used. The grade is intended for caps, cosmetic packaging, disposable medical device housings, and heat-resistant reusable serving ware where post-molding crystallinity is used to lift the upper service temperature.

    Representative physical properties of L100-M after injection molding with mold temperature 95–110 °C
    PropertyTest methodRepresentative value
    Melt flow indexISO 1133-1:2022 at 210 °C, 2.16 kg15–30 g/10 min
    DensityISO 1183-1:20191.25 g/cm³
    Tensile strength at yieldISO 527-2:201265 MPa
    Tensile modulusISO 527-2:20123.5 GPa
    Flexural strengthISO 178:201995 MPa
    Flexural modulusISO 178:20194.0 GPa
    Notched Izod impact strengthISO 180/A:2019 at 23 °C3.5 kJ/m²
    Heat deflection temperature BISO 75-2:2013 Method B, 0.45 MPa95–110 °C
    Heat deflection temperature AISO 75-2:2013 Method A, 1.8 MPa60–75 °C
    Vicat softening temperatureISO 306/B50:2014150 °C
    Degree of crystallinity by DSCISO 11357-3:201845–55%
    Mold shrinkageISO 294-4:20180.3–0.8% depending on flow direction

    How should L100-M be handled and processed in reciprocating screw injection molding?

    Pre-drying in a desiccant dryer is mandatory whenever ambient relative humidity exceeds 60% or packaging has been open for more than 30 min. The resin should be dried at 80 °C for 4–6 h with a dew point of -40 °C or lower to a target moisture level of 250 ppm or less. Moisture in the melt above 250 ppm hydrolyzes the ester linkages, producing a measurable decrease in melt viscosity, silver streaking, and loss of notched impact strength. A closed hopper with dry air purge and short feed lines is recommended because PLA reacquires surface moisture rapidly in high-humidity environments. Opened bags should be re-sealed with desiccant and processed within 8 h when the plant relative humidity exceeds 60%.

    Recommended starting processing range for L100-M on reciprocating screw injection molding machines
    ParameterSet point or range
    Drying temperature and time80 °C, 4–6 h
    Maximum residual moisture250 ppm
    Melt temperature200–220 °C
    Barrel rear / center / front165–195 °C / 195–210 °C / 200–215 °C
    Nozzle temperature205–215 °C
    Mold temperature95–110 °C
    Injection pressure80–120 MPa
    Hold pressure50–80 MPa
    Back pressure0.5–1.5 MPa
    Screw speed80–150 rpm
    Maximum melt residence time8 min at 200 °C; 3–4 min at 220 °C

    On a production-scale toggle clamp machine of 80–120 t with a 22–25 mm general-purpose screw of L/D 20–24, the barrel profile should be kept at 165–195 °C in the rear zone, 195–210 °C in the center, and 200–215 °C at the front, with nozzle temperature controlled at 205–215 °C. A screw with a compression ratio of 2.0–2.5:1 and a ring-type non-return valve is preferred; high-shear barrier screws can generate localized melt temperatures above 240 °C, causing lactide regeneration and plate-out on the mold. Mold temperature controllers should use pressurized water with a minimum gauge pressure of 0.4 MPa to avoid boiling at 110 °C. The hot runner manifold, if used, should maintain zone-to-zone temperature uniformity within ±2 °C and contain no dead spots. Vent depth should be 0.012–0.025 mm and gate diameter 0.8–1.2 mm for thin-wall parts. Back pressure above 2.0 MPa should be avoided because excessive shear heating can reduce molecular weight and cause yellowing. Injection velocity should be profiled from 40–80 mm/s for moderate wall sections, with the transition to hold by screw position rather than time to avoid overpacking the gate. Hold pressure should be 50–80 MPa for 2–4 s until gate freeze is confirmed; premature hold release increases sink marks, while excessive hold pressure enlarges perpendicular shrinkage near the gate. For multi-cavity tools, cavity-to-cavity filling imbalance above 5% by part weight can produce measurable crystallinity differences because the cooling time is coupled to local packing pressure.

    Cooling time is dictated less by the freeze-off of the gate than by the time required to build crystallinity at the mold wall. At mold temperatures below 95 °C, parts can demold with a smooth surface but retain low bulk crystallinity, causing post-mold shrinkage and upward heat-distortion drift during storage. At mold temperatures of 100–110 °C, spherulitic crystallization proceeds quickly enough that the demolded part reaches 45–55% crystallinity before ejection; differential scanning calorimetry per ISO 11357-3:2018 shows a cold-crystallization exotherm peak near 105 °C and a melt endotherm between 165 °C and 175 °C for the as-molded grade. The isothermal crystallization half-time at 105 °C is in the range of 30–60 s for a fast-crystallizing PLA backbone, although the actual value depends on melt residence history, shear, and part wall thickness. A mold temperature of 110 °C is therefore favored for heat-deflection temperature targets above 95 °C, but cycle time increases by 10–20 s compared with 60 °C mold operation because the solidification rate decreases with higher surface temperature. Warpage is generally reduced by higher mold temperature, but thick-to-thin transitions can retain anisotropic shrinkage of 0.3% parallel to flow and 0.8% perpendicular to flow if packing pressure is released before the gate freezes.

    Process capability studies on a 120 t toggle-clamp machine with a valve-gated hot runner showed that cavity pressure at gate freeze should be at least 35 MPa to prevent ejection-induced warpage. When cavity pressure falls below 25 MPa, the part surface can exhibit sink over ribs and lower local crystallinity, producing later dimensional change after exposure to 65 °C. These effects are amplified in mineral-filled or impact-modified PLA compounds, but L100-M does not require those additives for stiffness after crystallization.

    High-rigidity service comparisons against amorphous PLA and mineral-nucleated grades

    Compared with amorphous injection molding PLA, L100-M after crystallization shows a heat-deflection temperature increase of 35–45 °C under 0.45 MPa and a flexural modulus increase in the range of 10–15% under ISO 178:2019. This improvement is a consequence of the crystalline phase acting as physical crosslinks rather than of plasticizer removal. The trade-off is a reduction in optical clarity; molded parts change from transparent in amorphous PLA to translucent or opaque as crystallinity exceeds 20%. Impact resistance remains low, with notched Izod values of 3.5 kJ/m² per ISO 180/A:2019, which is below polycarbonate and impact-modified ABS benchmarks and restricts L100-M to non-impact-critical rigid housings.

    Unlike mineral-nucleated PLA compounds, L100-M may be formulated without talc or other inorganic nucleating agents, reducing the risk of abrasion in gates and screws and lowering the ash content of the finished part. However, published data for this specific formulation’s nucleation package is limited; converter trials should confirm whether an external nucleant is present and whether it affects food-contact declarations. Compared with a general-purpose PLA containing 2–4 mol% D-isomer, L100-M shows a shorter isothermal crystallization half-time at 105 °C and can reach higher final crystallinity within a fixed 60 s holding time. This difference allows the use of hot runners and lower pack pressures without dropping below the crystallinity threshold needed for service above 60 °C.

    Use in hot water or dishwasher cycles is not recommended unless the full part geometry has been annealed and tested to EN 12875-1 or equivalent. Because PLA is biodegradable only under industrial composting conditions, disposal claims must follow EN 13432 or ASTM D6400 only where the finished part has been certified; the high-crystallinity grade does not imply home-compostability.

    When hot-fill and microwave reheating govern part design

    Hot-fill and microwave reheat applications require crystallinity levels above 40%, because amorphous regions soften near 55–60 °C. In injection-molded L100-M parts produced with mold temperatures of 100–110 °C, heat-deflection temperature values under 0.45 MPa of 95–110 °C permit short hot-fill exposure up to 85 °C for non-pressure closures, but continuous service at 85 °C is not implied without post-mold annealing. For microwave reheating, PLA has a low dielectric loss factor compared with amorphous polyamide, so heating is governed primarily by food temperature rather than direct energy absorption; the grade should be tested for specific food simulants under EU 10/2011 or applicable FDA conditions because migration and warpage can occur at oil temperatures above 120 °C. The part should not be used as a pressure vessel or as a lid in superheated steam because PLA undergoes hydrolytic degradation and distortion.

    L100-M must be stored in sealed, moisture-barrier packaging at or below 30 °C and below 60% relative humidity. The resin is not compatible with high-humidity long-term storage without re-drying; moisture regain above 400 ppm can occur within hours at 70% relative humidity. The grade should not be combined with amine-based flame retardants or strong acid masterbatches due to chain scission and color shift, and compounding with polyolefin regrind is not recommended without compatibilization because phase separation lowers weld-line strength. Regrind levels up to 20 wt% can be tolerated for non-appearance parts if the regrind is dried to 250 ppm and limited to two heat histories. For finished articles, food-contact suitability is not automatically granted by bio-based content; the molder must verify migration limits under the intended food type, contact time, and temperature using EU 10/2011 or applicable FDA food-contact provisions. REACH and RoHS screening may be requested for specific export markets, but declarations are lot-specific and must be obtained from the supplier.

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