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Revode 201 Injection Molding Polylactic Acid Resin

    • Product Name: Revode 201 Injection Molding Polylactic Acid Resin
    • 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 459303
    Product Name Revode 201 Injection Molding Polylactic Acid Resin
    Chemical Name Polylactic Acid (PLA)
    Cas Number 26100-51-6
    Grade Injection Molding
    Appearance Natural/White Pellets
    Density 1.24 g/cm³
    Melt Flow Rate 10-20 g/10 min at 190°C/2.16 kg
    Melting Point 165-175°C
    Glass Transition Temperature 55-60°C
    Tensile Strength 50-60 MPa
    Elongation At Break 2-5%
    Flexural Modulus 3000-3500 MPa
    Notched Izod Impact Strength 2-3 kJ/m²
    Heat Deflection Temperature 55-60°C
    Vicat Softening Point 60-65°C
    Moisture Content <0.025%
    Molding Shrinkage 0.3-0.8%
    Processing Temperature 180-220°C
    Mold Temperature 20-40°C
    Drying Conditions 80°C for 2-4 hours
    Biodegradability Biodegradable/Compostable

    As an accredited Revode 201 Injection Molding Polylactic Acid Resin factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Revode 201 Injection Molding Polylactic Acid Resin is supplied in 25 kg moisture-barrier foil-lined bags, palletized and shrink-wrapped.
    Container Loading (20′ FCL) Revode 201 Injection Molding Polylactic Acid Resin loaded in 25 kg bags into a 20′ FCL container for secure transport.
    Shipping Revode 201 Injection Molding Polylactic Acid Resin is shipped as non-hazardous solid pellets in moisture-barrier lined bags, boxes, or drums. Keep containers sealed, dry, and cool, away from direct sunlight and heat. Follow the SDS and local transport regulations. Not DOT/IMDG/IATA regulated unless contaminated or otherwise specified.
    Storage Store Revode 201 Injection Molding Polylactic Acid Resin in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, moisture, and ignition sources. Keep containers tightly sealed in original packaging to prevent moisture absorption. Separate from oxidizers, acids, and bases. Avoid prolonged storage in humid conditions; pre-dry before molding according to supplier recommendations. Store between 5–30°C if possible.
    Shelf Life Shelf life is 24 months when stored in original packaging, in a cool, dry, ventilated area away from direct sunlight.
    Application of Revode 201 Injection Molding Polylactic Acid Resin

    On a typical 16-cavity cold-runner cutlery mold with a 1600 kN clamp force, the limiting defect is not short-shot but gate blush at the part surface adjacent to the sprue bushing. The resin is formulated at 98–100 wt% Revode 201, with a PLA-carrier color masterbatch at 0–2 wt% and, only when ejection marks are observed on the core side, an internal release masterbatch at 0.2–0.5 wt%. Desiccant drying at 80 °C for 4 h to a residual moisture level below 250 ppm, quantified by ISO 15512:2019 Method B, is mandatory because moisture above 250 ppm produces hydrolysis-induced splay and a measurable loss in melt strength within 20–30 min of residence time. Lot-to-lot melt flow index measured per ISO 1133-1:2022 should be logged in incoming QC because a shift of 2 g/10 min is sufficient to alter injection velocity demand on a 16-cavity tool. The barrel profile is set from 175 °C at the feed throat to 195 °C at the nozzle, with a melt temperature ceiling of 205 °C; excursions above 210 °C or cumulative residence time beyond 8 min initiate molecular weight loss that shifts the notched Izod impact below the breakage threshold for fork tines. Mold temperature is held at 20–35 °C, back pressure at 0.5–1.0 MPa, and injection speed at 80–150 mm/s to avoid shear heating at gate lands below 1.5 mm diameter. The production-scale defect pattern on these lines is a weld line at the tine crotch, which is managed by the use of a general-purpose screw with L/D 20:1 and compression ratio 2.4:1 rather than a high-shear barrier screw. Compliance for European food-contact distribution rests on EU Regulation (EC) No 1935/2004 and Commission Regulation (EU) No 10/2011, with overall migration testing against food simulants under the assigned conditions; where industrial compostability is claimed, the finished article must meet the disintegration and biodegradation requirements of EN 13432:2000/AC:2005 or ASTM D6400-23. For United States distribution, a grade-specific food-contact notification must be confirmed because 21 CFR 177.1520 does not automatically cover polylactic acid homopolymers. Terminal finished products in this segment are single-use spoons, forks, knives, and sporks; the operational boundary is that these parts are not hot-fill, microwave, or dishwasher serviceable and should be stored below 45 °C to avoid distortion.

    What Governs Thin-Wall Draw Ratio Stability in PLA Food-Contact Containers?

    Thin-wall container molding shifts the limiting variable from melt viscosity to solidification rate at the flow front, and Revode 201 responds to this shift primarily through mold temperature and injection speed. In this segment the compound is set at 97–99 wt% Revode 201, 0.2–0.5 wt% nucleating agent masterbatch, 0.5–1.5 wt% slip/antiblock masterbatch, and 0.5–2 wt% white or custom color concentrate. The nucleating agent is kept below 0.5 wt% because higher addition creates a cliff-edge increase in thin-wall brittleness and lowers elongation at break under ISO 527-2:2012. Drying follows the same 80 °C / 4 h desiccant cycle to below 250 ppm moisture. The downstream injection molding process uses valve-gated hot-runner tooling with wall sections between 0.6 mm and 1.2 mm, hot-runner manifold temperature from 195 °C to 205 °C, melt temperature from 185 °C to 200 °C, mold temperature from 35 °C to 50 °C, injection velocity from 150 mm/s to 300 mm/s, and cycle time between 8 s and 18 s depending on gate freeze time. At wall thickness below 0.8 mm, flow-front freeze-off causes short shots unless injection velocity is maintained above 200 mm/s; at mold temperatures below 35 °C, frost lines and flow marks appear on the sidewall. The compliance path for dairy containers, cold food cups, clamshells, and trays is Commission Regulation (EU) No 10/2011, with overall migration below 10 mg/dm², plus Directive 94/62/EC heavy-metal limits where the article is classified as packaging; compostable marketing claims require EN 13432:2000/AC:2005. Terminal finished product types are thin-wall cups, lids, clamshell containers, and cold food trays. The operational boundary is that hot-fill above 50 °C, microwave exposure, or prolonged contact with fatty foods above 40 °C can induce distortion and stress cracking unless the part is annealed after molding.

    Thick-Wall Cosmetic Jar Molding and Surface Replication Limits

    When a 50 mL polypropylene jar tool is converted to Revode 201, holding pressure and cooling time require rebalancing because the resin solidifies more sharply than semi-crystalline polypropylene and shows sink marks at thick wall intersections. The formulation addition ratio for cosmetic jars, caps, and compacts is 96–99 wt% Revode 201, 1–4 wt% pearlescent color masterbatch, 0.2–0.6 wt% nucleating agent masterbatch to reduce sink, and 0.2–0.5 wt% internal mold release only when ejector pin marks are visible on the base. Barrel temperatures are kept at 180–195 °C to limit yellowing; mold temperature is set at 30–55 °C to improve surface replication of engraved logos and to reduce visible weld lines. Holding pressure is maintained at 60–80% of injection pressure for 6–12 s, with cooling time between 15 s and 25 s for wall thicknesses of 2–4 mm. A sub-gate diameter below 1.2 mm is avoided because it raises shear heating and produces gate blush on the jar sidewall. The regulatory basis for cosmetic packaging is REACH 1907/2006 Annex XVII and Directive 94/62/EC, with the heavy-metal sum for lead, cadmium, mercury, and hexavalent chromium kept below 100 mg/kg. Compatibility with cosmetic formulations is assessed by ISO 175:2010 immersion at 23 °C for 7 days; aromatic solvents and high-alcohol formulas above 20% ethanol are considered outside the safe operating window because they promote environmental stress cracking in PLA. Terminal finished product types include thick-wall jars, closure caps, and compact cases. The operational boundary is that filling temperatures must remain below 45 °C, and the pack cannot be positioned as a hot-fill or dishwasher-resistant package.

    For rigid writing instrument barrels where drop performance after ink refill insert is specified by ISO 11540:2014, the resin is compounded at 92–97 wt% Revode 201 with 3–8 wt% biodegradable impact modifier; plasticizer addition above 5 wt% is excluded because it lowers the heat deflection temperature under ISO 75-2:2013 Method A below 45 °C and causes clip retention failure. The downstream process uses multi-cavity cold-runner tooling with melt temperature 175–190 °C, mold temperature 20–30 °C, injection speed 60–120 mm/s, and cooling time 10–18 s for barrel wall thicknesses of 1.0–2.0 mm. A lower mold temperature maintains the dimensional tolerance required for refill insertion, but it also raises residual stress; if stress cracking appears at the threaded end, annealing at 60 °C for 30 min reduces the failure rate. Regulatory compliance for general stationery falls under REACH 1907/2006; products marketed to children under 14 years must meet the migration limits for 19 elements in EN 71-3:2019 + A1:2021. Terminal finished product types are retractable pen barrels, ruler bodies, and desk organizer trays. The operational boundary is that ink reservoirs and cleaning solvents containing ketones or esters can soften the resin at the barrel interior; published data for this specific formulation under long-term ink contact is limited, so compatibility testing before mold commissioning is required.

    When Soil Contact and UV Surface Degradation Define Pot Service Life

    Because PLA is not ambient-soil biodegradable, nursery pot producers must separate industrial-compostability claims from in-use degradation expectations. The formulation addition ratio for injection-molded nursery pots, propagation trays, and plant labels is 96–100 wt% Revode 201, 1–3 wt% carbon black or earth-tone masterbatch, and 0.5–1.5 wt% UV stabilizer masterbatch only when outdoor exposure beyond 6 months is specified and the stabilizer is approved under the relevant compostability scheme; for thin-wall propagation trays, an impact modifier at 0–3 wt% is used to reduce cracking during demolding. The production process operates with wall thickness from 1.5 mm to 3.0 mm, melt temperature 180–200 °C, mold temperature 35–60 °C, injection speed 50–100 mm/s to avoid jetting, and cycle time 25–40 s. Increasing mold temperature to 60 °C raises crystallinity and lowers warpage on flat tray bases, but it also increases core sticking if the tool lacks sufficient draft; draft angles below 1.5° produce ejection marks and white stress zones. Compliance for industrial compostability claims is anchored to EN 13432:2000/AC:2005, with biodegradation testing per ISO 14855-1:2012 and disintegration testing per ISO 16929:2013; heavy-metal thresholds are stated in EN 13432. Terminal finished product types are nursery pots, propagation trays, and plant identification labels. The operational boundary is that these articles are not home compostable, are not ambient soil biodegradable, and will develop surface chalking after prolonged UV exposure unless a stabilizer masterbatch is included.

    Flat Rigid Houseware Molding Is Not a Drop-In Substitution for HDPE

    Drawer trays and hangers molded from Revode 201 exhibit warpage when gates freeze before packing is complete, which is the primary tool conversion issue in flat rigid housewares. The resin is formulated at 95–100 wt% Revode 201, with color masterbatch at 1–3 wt% and, for hangers requiring snap-fit flex, an impact modifier at 0–5 wt%; plasticizer is not used because flat parts with visible surfaces reject at even minor HDT loss. The downstream injection molding process uses cold-runner tooling with fan gates or edge gates, melt temperature 180–200 °C, mold temperature 25–45 °C, holding pressure 70–85% of injection pressure, pack time 8–15 s, and cooling time 15–30 s for part thicknesses of 2.0–4.0 mm. The cooling time is set by gate freeze, not by part ejection temperature; premature gate freeze creates sink and warpage on flat bases, while excessive holding pressure over 85% generates flash at the parting line. Compliance for these non-food houseware products is REACH 1907/2006 and, where sold to consumers in the European Union, Regulation (EU) 2023/988 General Product Safety Regulation; articles intended for children must additionally meet EN 71-3:2019 + A1:2021. Terminal finished product types are drawer dividers, storage trays, hangers, and point-of-sale display stands. The operational boundary is a continuous service temperature below 50 °C, no dishwasher exposure, and no load-bearing application above 5 kg unless the rib design is verified by testing because creep deformation is more pronounced than with HDPE.

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    Certification & Compliance
    More Introduction

    Revode 201 Injection Molding Polylactic Acid Resin is an unfilled, high-flow polylactic acid grade supplied in pellet form for short-cycle injection molding of thin-wall food-service packaging, disposable cutlery, cosmetic containers, and non-load-bearing consumer housings. The manufacturer’s controlled-lot specification for Revode 201 identifies a nominal melt volume-flow rate of 18 cm³/10 min at 210 °C and 2.16 kg when tested to ISO 1133-1:2022, a density of 1.25 g/cm³ by ISO 1183-1:2019, a pellet bulk density of 0.75–0.85 g/cm³ by ISO 60, and residual pellet moisture below 0.025 wt% by ISO 15512. Reported mechanical values from ISO 527-2 are tensile yield strength 58–63 MPa, tensile elongation at break 4–7%, flexural modulus 3.2–3.6 GPa by ISO 178, and notched Izod impact strength at 23 °C of 2.5–3.5 kJ/m² by ISO 180/1A. Heat deflection temperature is 52–58 °C under 0.45 MPa load by ISO 75-2/B. Mold shrinkage is 0.3–0.5% in the flow direction and 0.2–0.4% transverse when measured on 2.0 mm plaques by ISO 294-4. The product is not intended for blow molding, cast film, or extrusion sheet processes because its low melt strength produces parison sag, web instability, and inadequate draw-down.

    What Drying and Melt-Temperature Boundaries Prevent Hydrolytic Degradation?

    The critical processing boundary is moisture. Polylactic acid undergoes hydrolytic chain scission in the melt when residual moisture exceeds 0.05 wt%. At 0.05–0.10 wt% moisture, melt viscosity drops, nozzle drool and flash increase, and tensile strength of molded parts falls by 10–15% relative to dry resin. At higher moisture levels, splay and silver streaks appear at the gate and the part becomes brittle. Pre-drying is therefore mandatory when opened-bag moisture exceeds 0.025 wt%. A desiccant dryer with a dew point ≤ −40 °C and an air temperature of 80 °C for 3–4 h lowers moisture to 0.010–0.025 wt%. If the resin has been stored in unopened moisture-barrier bags at 20–25 °C and RH < 60%, drying can be omitted for the initial use; however, opened bags exposed to ambient air must be dried within 30 min or re-sealed. At 23 °C and 50% RH, dried PLA regains approximately 0.005–0.010 wt% moisture in 30 min, so hopper loading should be continuous and the hopper inlet should be blanketed with dried air where feasible.

    Barrel zone settings for a 25–40 mm general-purpose screw with 20:1–24:1 L/D and compression ratio 2.0:1–2.5:1 are 170–180 °C in the feed zone, 180–190 °C in the compression zone, 190–200 °C in the metering zone, and 195–205 °C at the nozzle. The actual melt temperature, measured with a needle pyrometer at the nozzle, is held between 185 °C and 205 °C. Operation above 210 °C accelerates lactide reformation, yellowing, and molecular weight loss; operation below 175 °C increases screw torque and produces unmelted granules. Screw speed is 80–150 min⁻¹ depending on screw diameter. Back pressure is 0.3–0.7 MPa, sufficient to homogenize the melt without excessive shear heating. Total residence time in the barrel is kept below 5 min; after 8–10 min, degradation products are detectable as acetaldehyde and a yellow-brown color shift.

    ParameterRecommended rangeUnitEquipment or measurement method
    Pre-drying temperature80°CDesiccant dryer
    Pre-drying time3–4hDesiccant dryer
    Residual moisture target≤0.025wt%ISO 15512
    Dew point≤−40°CDew-point meter
    Barrel zones feed/compression/metering/nozzle170–180 / 180–190 / 190–200 / 195–205°CNeedle pyrometer
    Melt temperature185–205°CNeedle pyrometer
    Mold surface temperature20–35°CThermocouple
    Back pressure0.3–0.7MPaHydraulic pressure
    Screw rotation speed80–150min⁻¹Tachometer
    Injection pressure60–120MPaHydraulic pressure
    Hold pressure50–70% of injection pressureHydraulic pressure
    Fill time0.3–0.8sInjection velocity profiling
    Cooling time15–40sWall thickness 1.5–3.0 mm
    Residence time≤5minTimer
    Clamp force3–5tons/in² projected areaClamp-force calculation

    On an all-electric injection molding machine with a 40 mm screw and 20:1 L/D, screw recovery time for Revode 201 is typically 10–15 s at 120 min⁻¹. This is longer than an equivalent melt-flow amorphous PET or polystyrene because PLA has higher heat capacity and lower bulk density in the feed section. The observed shot-to-shot variation in melt volume-flow rate on production lots is approximately ±10%, requiring adjustment of injection velocity, transfer position, and hold pressure after each lot change. Thin-wall parts with 0.4–0.8 mm wall sections are filled with profiled injection velocity and a fill time of 0.3–0.8 s; a fill time above 1.0 s can produce flow marks and short shots. Peak injection pressure is typically 60–120 MPa, but for 0.5 mm wall sections, screw-tip pressure can reach 130 MPa. Holding pressure is 50–70% of the peak injection pressure and is maintained for 2–4 s until gate freeze-off for a 1.0 mm side gate. Cooling time for 1.5–3.0 mm wall thickness is 15–40 s. Clamp force requirement is 3–5 tons/in² of projected area, but thin-wall molding may require 5–7 tons/in² if the mold is not stiff enough to prevent flashing.

    Gate dimensions for unfilled PLA are side gate depth 0.6–0.8 mm, land length 0.8–1.0 mm, pinpoint gate diameter 0.8–1.2 mm, and submarine gate diameter 0.8–1.2 mm. Sharply tapered gates create excessive shear heating and degrade the resin; oversized gates prolong freeze-off and increase sink marks. Vent depths are 0.015–0.025 mm; deeper vents cause flash. Mold surfaces for clear parts require a polish of Ra 0.05–0.10 µm; textured surfaces increase ejection force. Draft angles are 0.3–1.0° on textured surfaces and 0.5–1.0° on ejector pins. PLA parts are brittle at ejection; sharp corners, undercuts, and insufficient draft cause stress whitening and cracking. Hot-runner systems should be externally heated, fully balanced, and free of dead spots. Internally heated torpedo systems can create local temperatures above 220 °C and produce black specks. Copper-alloy hot-runner components are not recommended because PLA melt acidity attacks copper-based alloys in extended runs. Independent published data for Revode 201 in specific hot-runner configurations is limited; therefore, mold trials are required before high-cavitation production.

    When Revode 201 Replaces General-Purpose Amorphous PLA or Impact-Modified ABS

    The principal difference between Revode 201 and a general-purpose PLA extrusion or thermoforming grade is the melt-flow range. General-purpose extrusion PLA often has an MVR of 3–8 cm³/10 min at 210 °C/2.16 kg; Revode 201 has a nominal MVR of 15–25 cm³/10 min by ISO 1133-1:2022. The higher flow permits filling of 0.4–0.8 mm wall sections without raising melt temperature to a range that causes flash and molecular degradation. The trade-off is lower melt strength. Extrusion and blow-molding PLA grades have higher intrinsic viscosity and melt strength for parison stability, film bubble stability, and draw-down; Revode 201 is not suitable for these processes.

    PropertyTest methodRevode 201General-purpose extrusion PLAImpact-modified PLA
    Melt volume-flow rate at 210 °C/2.16 kgISO 1133-1:202215–25 cm³/10 min3–8 cm³/10 min10–20 cm³/10 min
    Tensile yield strengthISO 527-258–63 MPa50–60 MPa35–45 MPa
    Tensile elongation at breakISO 527-24–7%3–6%10–30%
    Flexural modulusISO 1783.2–3.6 GPa3.0–3.5 GPa2.0–2.8 GPa
    Notched Izod impact at 23 °CISO 180/1A2.5–3.5 kJ/m²2.0–3.5 kJ/m²8–25 kJ/m²
    Heat deflection temperature at 0.45 MPaISO 75-2/B52–58 °C50–60 °C45–55 °C
    DensityISO 1183-1:20191.24–1.26 g/cm³1.24–1.26 g/cm³1.20–1.28 g/cm³

    Compared with impact-modified PLA, Revode 201 has higher stiffness and tensile strength, but lower impact resistance and elongation. Notched Izod impact strength for Revode 201 is 2.5–3.5 kJ/m² by ISO 180/1A, while an impact-modified PLA may be 8–25 kJ/m². Revode 201 is therefore not appropriate for living hinges, snap-fits requiring repeated flexure, or service below 0 °C under impact. Impact-modified PLA also has a lower flexural modulus, typically 2.0–2.8 GPa versus 3.2–3.6 GPa for Revode 201.

    When Revode 201 replaces impact-modified ABS in a disposable service item, the converter must accept a lower continuous-use temperature. ABS typically has an HDT of 90–100 °C at 0.45 MPa by ISO 75-2/B, whereas amorphous Revode 201 has an HDT of 52–58 °C. Revode 201 parts can warp or deform under load above 50 °C. If hot-fill or hot-service performance is required, the tool should be operated at 100–110 °C and the cycle time extended to 60–120 s to develop crystallinity, or the demolded part should be annealed at 100 °C for 30 min. Post-mold annealing raises crystalline content to 30–40% as measured by differential scanning calorimetry and increases HDT to 85–100 °C at 0.45 MPa, but it also increases shrinkage and warpage and can reduce impact strength further.

    Food-contact compliance for Revode 201 is supplier-controlled. Converters must verify that finished articles meet the applicable migration limits under EU Regulation 10/2011 for plastic food-contact materials, including any specific migration limits for lactic acid, lactide, and oligomers. Under U.S. law, the supplier should provide documentation that the polymer is manufactured from monomers authorized for food-contact use under 21 CFR 174.5 or a specific food-contact notification. RoHS screening by IEC 62321 and REACH SVHC verification under Regulation (EC) No 1907/2006 are lot-specific and require a certificate of compliance. Revode 201 is not intended for medical implants, long-term in-vivo use, or load-bearing safety components because its hydrolytic degradation profile is not controlled for such applications. The resin should not be blended with PVC residues or exposed to chlorine-containing purge compounds because thermal decomposition products accelerate hydrolysis. Storage in sealed moisture-barrier bags at 20–25 °C and RH < 60% is recommended; shelf life under these conditions is 12 months from the production date on the certificate of analysis.

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