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Revode 210 Injection Molding Polylactic Acid Resin

    • Product Name: Revode 210 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 566795
    Appearance White to light yellow cylindrical pellets
    Polymertype Polylactic Acid (PLA)
    Processingmethod Injection Molding
    Density 1.24-1.25 g/cm³
    Meltflowrate 10-20 g/10 min at 190°C/2.16 kg
    Meltingpoint 165-175°C
    Glasstransitiontemperature 55-60°C
    Tensilestrength 60-65 MPa
    Elongationatbreak 3-6%
    Flexuralstrength 80-90 MPa
    Flexuralmodulus 3000-3500 MPa
    Notchedizodimpactstrength 3-4 kJ/m²
    Heatdeflectiontemperature 55-60°C
    Vicatsofteningpoint 60-65°C
    Moisturecontent ≤0.025%
    Biobasedcontent 100%
    Biodegradability Compostable according to EN 13432 and ASTM D6400
    Dryingtemperature 80-100°C
    Dryingtime 2-4 hours
    Injectiontemperature 190-220°C
    Moldtemperature 20-50°C

    As an accredited Revode 210 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 210 Injection Molding Polylactic Acid Resin is packed in 25 kg moisture-barrier bags on pallets.
    Container Loading (20′ FCL) 20′ FCL container: palletized 25 kg bags of Revode 210 Injection Molding Polylactic Acid Resin, shrink-wrapped, approximately 20 MT net.
    Shipping Revode 210 Injection Molding Polylactic Acid Resin ships as non-hazardous solid pellets in sealed 25 kg bags or 1000 kg jumbo bags, palletized and stretch-wrapped. Transport in clean, dry containers at ambient temperature. Avoid moisture, heat, direct sunlight. Keep packages closed until use. Follow SDS and local regulations.
    Storage Store Revode 210 Injection Molding Polylactic Acid Resin in a cool, dry, well-ventilated area, away from direct sunlight, heat, ignition sources, and incompatible materials. Keep containers tightly sealed to prevent moisture absorption. Maintain stable temperature and low humidity, avoid static buildup, and protect from water, acids, bases, and oxidizers. Follow the manufacturer’s SDS and shelf-life recommendations; use first-in, first-out inventory.
    Shelf Life Shelf life is approximately 24 months when stored unopened in original packaging, in a cool, dry place away from moisture and sunlight.
    Application of Revode 210 Injection Molding Polylactic Acid Resin

    At production scale, injection moulding of single-use cutlery from high-flow PLA begins with drying at 80 °C for 4 h to reach a residual moisture level below 250 ppm; in plants where ambient relative humidity exceeds 60 % RH, desiccant-bed hopper dryers with a dew point of -40 °C are required because PLA hydrolyzes rapidly above 260 °C in the presence of moisture. Multi-cavity tools for forks, spoons, and knives are generally run on reciprocating-screw machines with clamp forces between 80 t and 150 t and shot capacities sized to keep melt residence time below 10 min at 190–205 °C melt temperature. The mould surface temperature is maintained at 25–35 °C with chilled-water circuits; higher settings reduce fill pressure but extend cycle time and increase downstream crystallinity variation. Screw speed ranges from 80 rpm to 150 rpm with back pressure at 0.5–1.5 MPa, and injection speed is set to 80–150 mm/s to prevent jetting at the spoon bowl-to-handle transition. Knife blanks, which have a thicker spine and a thin edge, require profiled cooling time and gate freeze verification before holding pressure release; otherwise sink marks form at the intersection of the blade and the tang.

    Mechanical acceptance for cutlery uses ASTM D638 tensile yield strength of 55–65 MPa and elongation at break below 5 %; the low elongation mandates a minimum edge radius of 0.5 mm on knife serration profiles to prevent brittle fracture during cutting trials. Food-contact end products must be verified against EU Regulation 10/2011 overall migration limit of 10 mg/dm² or 60 mg/kg, and for industrial compostability the finished part must meet EN 13432 disintegration and biodegradation thresholds. Typical terminal parts include airline meal service flatware, institutional catering spoons and forks, and hospital cafeteria cutlery where the service temperature is below 55 °C and contact time with hot liquids is below 15 min.

    Where Does High-Flow PLA Fit in Cold-Fill Dairy and Ready-Meal Packaging?

    Cold-fill packaging tools running Revode 210 require a different thermal strategy than cutlery tools because wall thickness falls to 0.5–1.2 mm and flow length-to-thickness ratios can exceed 200:1 in rectangular tubs. Hot runner systems with valve gates are used to control gate freeze; sequential valve gating is preferred for lids and rectangular bases to move weld lines away from the sidewall-base transition, where frozen-in stress causes cracking under drop loads. Melt temperature is held at 195–215 °C, and the mould is run with 10–15 °C chilled water to achieve cycle times of 8–14 s for 0.8 mm wall sections. Holding pressure is profiled in two stages: a short high-pressure stage at 60–80 MPa to pack the gate, followed by a lower stage at 30–40 MPa to reduce gate stress and prevent warpage across the sealing flange. Mould release relies on draft angles of 1.5–2.0° on the cavity side because PLA exhibits a friction coefficient higher than polyolefins on non-polished tool steel.

    Compliance for this segment is governed by EU Regulation 10/2011 for cold or ambient food contact; fatty dairy products require migration testing with food simulant type D2 under 40 °C for 10 days if the package is intended for whole-milk yogurt. Hot-fill, microwave, and dual-ovenable applications are outside the operational boundary of unreinforced PLA because heat deflection temperature under 0.45 MPa remains below 60 °C unless post-mould annealing is applied. Terminal components include delicatessen portion pots, cold soup containers, yogurt cups with snap-on lids, and living-hinge sauce lids where the hinge is limited to a small number of flex cycles by design. The use of reclaimed PLA in food contact is not permitted unless the recyclate has been authorized under a specific food-contact approval, so production scrap is directed to industrial composting streams or non-food applications.

    AssessmentStandard or regulatory referenceCritical criterion
    EU food contactEU Regulation 10/2011Overall migration 10 mg/dm² or 60 mg/kg
    US food contactFood Contact NotificationGrade-specific FCN verification for Revode 210
    Industrial compostabilityEN 13432Biodegradation ≥90 % in 180 days; disintegration ≥90 % in 12 weeks
    US compostabilityASTM D6400Equivalent heavy metals and ecotoxicity criteria
    Aerobic biodegradation measurementISO 14855-1Controlled composting at 58 °C

    For cosmetic packaging, the dominant moulding issue is not fill speed but post-mould dimensional stability in thread engagement and snap-fit closures. Multi-start threads on PLA caps require a radial clearance of 0.2–0.4 mm because unreinforced PLA exhibits anisotropic mould shrinkage of 0.3–0.5 % in the flow direction and 0.2–0.4 % transverse to flow; designs without clearance fail in assembly due to thread galling or collar splitting. Low-odour pigments must be used at 1.5–2.5 wt% because PLA has a lower odour threshold than polyolefins and volatile residuals from colour masterbatches become apparent in sealed packs. The process window for glossy surfaces uses a melt temperature of 190–205 °C, a mould surface temperature of 25–35 °C, and fast injection to replicate polished cavity finish; longer residence times above 210 °C cause yellowing that is visible on white and pastel bases.

    Post-mould annealing at 80–100 °C for 30–60 min is applied when closures require a heat distortion temperature above 80 °C for retort lipstick bases or hot-fill cosmetic jars; crystallization during annealing raises the degree of crystallinity to approximately 35–40 % but reduces impact resistance, so annealed parts are not used for snap-fit components that undergo repeated flexing. Chemical compatibility is limited: prolonged contact with formulations having pH above 9 or containing ethyl acetate and strong polar ester solvents can induce environmental stress cracking, and closure developers must run compatibility testing per internal protocols referenced to ASTM D543 for chemical resistance. Terminal components include airless pump collars, compact mirror frames, jar closures with lot-coded inner liners, and lipstick bases for formulations that do not include aggressive plasticizing esters.

    Medical Device Housings and Single-Use Diagnostic Components

    Medical device contract moulders typically select all-electric machines with oil-free clamping areas for PLA components used as non-patient-contacting housings and diagnostic cartridge supports. The processing boundary is narrower than in packaging because mould temperature must be controlled to ±2 °C across multi-cavity tools to maintain consistent part mass and dimensional tolerance; closed-loop hot runner controllers and cavity pressure sensors are used for parts with masses below 2 g. Drying at 80 °C for 4 h is mandatory, with inline moisture analysis on the feed throat to reject lots above 250 ppm. Melt temperature is set at 190–205 °C, and hold pressure is adjusted so that gate freeze occurs before holding pressure decay; early gate release creates micro-voids that propagate during drop impact. Ejection requires uniform force distribution because PLA parts at 0.8–1.5 mm wall can fracture if the ejector pin retraction stroke is not synchronized with the robot end-of-arm tooling.

    Sterilization compatibility is the critical qualification issue. Ethylene oxide cycles at 55 °C and relative humidity of 30–80 % are generally less damaging, but gamma irradiation at a nominal dose of 25 kGy causes chain scission in the amorphous phase and can reduce tensile elongation by more than half depending on stabilizer package; published data for Revode 210 under gamma sterilization is limited, so moulders must validate mechanical performance on finished parts per ISO 10993-5 cytotoxicity and ISO 10993-10 irritation and sensitization if the component is part of a medical device system. Steam autoclave sterilization at 121 °C is outside the operational boundary because the heat deflection temperature of unreinforced PLA is below the autoclave temperature. Terminal applications are limited to benchtop analyzer bezels, diagnostic reader frames, sample tray cartridges, and laboratory consumable supports where the part does not contact body tissue or fluids for extended periods.

    When Heat Deflection Limits Permit Replacement of ABS in Internal Electronic Brackets

    When service temperatures remain below 50 °C, PLA can replace ABS in internal electronic brackets if the design eliminates sharp internal corners and living hinges. The tensile modulus of unreinforced PLA is approximately 3000–3500 MPa per ASTM D638, which is higher than general-purpose ABS and allows thinner walls in low-load brackets; however, notched Izod impact strength is typically 2.0–3.5 kJ/m², so ribs and bosses must use a radius-to-wall-thickness ratio of at least 0.25:1 to prevent crack initiation at the base. Screw bosses for self-tapping screws with thread-forming geometry crack under radial stress unless the boss outer diameter is at least 2.5 times the screw nominal diameter; moulded-in brass inserts are preferred for assembly points that are disassembled more than twice. Mould shrinkage in the range of 0.3–0.5 % requires that locating features be designed with reference to the gate location, because flow-direction shrinkage differences can shift hole centers by more than 0.15 mm across a 100 mm span.

    Flame retardance is the main regulatory constraint: neat PLA without flame-retardant additives generally does not meet UL 94 V-2 above 1.5 mm thickness, so internal brackets are limited to low-voltage or non-enclosure areas where the end-product standard does not require a V-2 or V-0 rating. Processing on vertical clamp machines with barrel capacities of 50–150 t uses melt temperatures of 185–200 °C to minimize thermal degradation and mould temperatures of 20–30 °C; heated sprue bushings are used when cold runner volume exceeds 20 % of shot weight to prevent premature freeze at the sprue puller. Terminal components include optical sensor mounts, cable clips inside display enclosures, power supply insulation brackets, and internal frame components for instruments that do not generate surface temperatures above 50 °C.

    Greenhouse production environments expose PLA clips to 60–80 % RH and 35–45 °C for weeks, which shifts the failure mode from impact fracture to creep deformation. For vine clips and plant tags, the design requirement is creep resistance at warm temperatures, not rapid soil biodegradation; the glass transition temperature of the amorphous phase is close to 55–60 °C, so 40 °C service remains below the onset of large-scale chain mobility, but continuous load above 0.5 MPa can cause measurable deflection after 24 h at that temperature. The moulding process uses multi-cavity cold runner tools with melt temperatures of 190–205 °C and mould temperatures of 25–35 °C; colour masterbatches for outdoor exposure require UV stabilizer loadings of 1–2 wt% because unstabilized PLA yellows and embrittles after 6 months of direct sunlight. Clips that must survive installation flexing use a lower crystallinity profile by reducing mould temperature and avoiding post-mould annealing, trading some stiffness for higher elongation at break.

    Compostability claims for horticultural articles must distinguish industrial composting from soil degradation. PLA parts certified to EN 13432 will hydrolyze in an industrial composting facility at 58 °C, but the same parts in agricultural soil at 25 °C can remain substantially intact for 24 months or longer, so they are not soil biodegradable in the sense of home compostable or soil additive materials. End products include greenhouse vine clips, substrate pot tags, nursery identification tags, and seeding tray inserts where the parts are recovered and composted at the end of the growing cycle rather than left in the soil. The use of regrind from cold runners is feasible at 20–30 % addition by weight for horticultural parts if the regrind is dried and colour consistency is not critical; higher regrind fractions increase brittleness and reduce clip installation success.

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    Certification & Compliance
    More Introduction

    Processors evaluating Revode 210 Injection Molding Polylactic Acid Resin are presented with an unmodified poly(L-lactic acid) grade supplied in pellet form for reciprocating-screw injection molding of short-cycle, thin-section articles. The resin’s technical identity is controlled by three parameters: melt mass-flow rate, residual moisture after drying, and the degree of crystallinity developed during cooling from the melt. Unlike a polyolefin, the polymer does not require high barrel temperatures to develop fluidity; instead, thermal history, moisture content, and shear heating determine whether the process remains stable or proceeds toward hydrolytic degradation. If the material is handled within the specified envelope, the molder obtains a transparent part with tensile modulus in the range 3.0–3.6 GPa under ISO 527-2:2012 and a surface finish suitable for ambient-temperature consumer packaging and industrial components. The values in this document describe the unmodified injection-molding PLA class to which the grade belongs; the supplier’s certificate of analysis remains the controlling specification for any production lot.

    What Drying, Barrel Temperature, and Residence-Time Boundaries Protect Molecular Weight?

    Pre-drying in a desiccant or closed-loop hot-air dryer is mandatory. Residual pellet moisture above 250 ppm leads to ester hydrolysis at melt temperatures above 180°C. A workable production condition is 80°C for 4 h with a dryer dew point of -40°C or lower; the dried pellets should not be exposed to ambient air longer than 30 min when relative humidity exceeds 60%. Barrel settings are generally profiled from 170°C at the hopper throat to 200–210°C at the nozzle, while measured melt temperature is held between 190°C and 220°C. At 230°C and above, lactide reformation, yellowing, and loss of notched impact strength become detectable within 5 min of static residence. Cumulative hot residence time should not exceed 8 min at 200°C. If a press fault interrupts cycling, barrel heater outputs should be reduced to 160–170°C until restarting. General-purpose screws with 20:1 to 24:1 L/D and compression ratio 2.5:1 to 3.0:1 are acceptable. Compression ratios above 3.5:1 can produce excessive shear heating and should be avoided.

    Shot size should fill between 30% and 70% of the barrel capacity; smaller shots prolong residence time, while larger shots increase pressure loss and screw recovery time. The screw should use a reverse-taper or shut-off nozzle; PLA has low melt strength and can drool from open nozzles. Back pressure of 5–20 bar and decompression of 3–5 mm are typical. Because the resin’s viscosity is moisture-sensitive, process windows narrower than ±5°C are not unusual when dimensional tolerance is tight.

    At the gate, the polymer responds to shear with a measurable reduction in apparent viscosity, but the effect is weaker than in high-MFR polypropylene. Injection speeds of 50–120 mm/s for wall thickness 1.0–2.0 mm are commonly used to prevent gate freeze-off. Speed above 150 mm/s can initiate gate blush and localized shear heating, particularly in unhardened tool steel. Hold pressure is typically 500–900 bar at the cavity, but the set point must be derived from cavity pressure transducer data rather than machine hydraulic pressure because runner losses vary. The cushion should be kept at 2–5 mm to minimize stagnant melt volume. For multi-cavity tools, cavity-to-cavity fill time differences exceeding 0.02 s are often associated with amorphous orientation gradients and later dimensional movement.

    Mechanical Property Development and Dimensional Stability After Ejection

    Tensile modulus for this unmodified PLA class under ISO 527-2:2012 is generally 3.0–3.6 GPa, with tensile stress at break between 45 MPa and 70 MPa depending on draw speed and conditioning. Notched Izod impact strength per ISO 180:2019 remains low, commonly 2.0–4.0 kJ/m², because the amorphous matrix is notch-sensitive. Unnotched Charpy impact per ISO 179-1:2010 may exceed 15 kJ/m², but snap-fit corners and sharp changes in section should be designed using the notched value. Heat deflection temperature at 0.45 MPa per ISO 75-2:2013 is typically 50–60°C for as-molded amorphous specimens; at 1.8 MPa, values below 55°C are typical. The tool temperature is normally 25–60°C, so the part leaves the mold in an amorphous state and continues cold crystallization and physical aging during the following 24–48 h. Mold shrinkage per ISO 294-4:2018 is commonly 0.3–0.7%, with additional shrinkage of 0.1–0.3% after annealing. Dimensional acceptance should be based on parts conditioned for at least 48 h at 23°C and 50% relative humidity.

    During cooling from the melt, differential scanning calorimetry per ISO 11357-3 generally shows a glass transition near 55–60°C, a cold-crystallization exotherm between 90°C and 120°C, and a melting endotherm between 150°C and 170°C. These transitions explain the post-mold dimensional movement: amorphous chains densify below the glass transition, and cold crystallization can proceed above the glass transition during annealing or in-service exposure above 60°C.

    The following table positions the unmodified injection-molding class relative to two common PLA modifications; values are class-level ranges gathered from published PLA processing literature and should not replace the supplier certificate.

    Representative comparison of unmodified injection-molding PLA class with nucleated high-HDT PLA and impact-modified PLA grades
    Property Revode 210 class (unmodified PLA) Nucleated high-HDT PLA Impact-modified PLA Test method
    Melt mass-flow rate 10–30 g/10 min at 210°C/2.16 kg 5–15 g/10 min 8–20 g/10 min ISO 1133-1:2022
    Tensile modulus 3.0–3.6 GPa 3.2–3.8 GPa 2.5–3.0 GPa ISO 527-2:2012
    Notched Izod impact 2.0–4.0 kJ/m² 2.0–3.5 kJ/m² 6.0–15.0 kJ/m² ISO 180:2019
    HDT at 0.45 MPa 50–60°C 100–120°C after annealing 45–55°C ISO 75-2:2013

    Because unmodified poly(L-lactic acid) crystallizes slowly at mold temperatures below 80°C, Revode 210 is positioned differently from nucleated high-HDT PLA grades. Nucleated grades require mold temperatures of 90–120°C and post-mold annealing at 100–110°C for 20–30 min to raise HDT above 100°C, at the cost of longer cycle time, higher tooling energy load, and greater warpage risk. Impact-modified PLA grades attain notched Izod impact above 10 kJ/m² by blending with biodegradable elastomers or aliphatic polyesters, but tensile modulus often falls to 2.5 GPa or lower and transparency is typically reduced. The unmodified injection-molding grade therefore occupies a narrow compromise: higher flow and clarity than impact-modified grades, and lower HDT but simpler processing than nucleated grades.

    When a Cold-Runner Mold Demands Low Pressure Drop and Balanced Cavity Filling

    Cold-runner tools with long sprue and runner lengths amplify the effects of melt compressibility and rapid solidification. Runner diameters below 4 mm generate steep pressure loss and excessive shear heating; for flow path ratios above 150:1, a valve-gated hot-runner system with independent tip temperature control is preferred. Nozzle temperature should be maintained at 200–210°C and the nozzle tip should not be allowed to freeze because solidified PLA can remain as a cold slug. PLA has lower thermal diffusivity than semi-crystalline polypropylene, so cooling time is commonly 10–20% longer at the same wall thickness. Mold temperature uniformity should be held to ±5°C across the cavity. A temperature difference of 5°C between cavity halves can produce measurable warp, and on flat parts with 100 mm flow length, warpage values above 0.3 mm are not unusual when the tool is poorly balanced. Multi-cavity tools require cavity pressure verification rather than artificial runner balancing alone; fill time differences above 0.02 s can correlate with amorphous orientation gradients and delayed dimensional movement.

    On production lines, silver streaks or splay are most often caused by wet pellets or a dew point above -30°C in the hopper dryer; raising mold temperature or injection speed does not correct hydrolysis. Brown streaks and yellowing are associated with dead spots in the manifold or extended barrel residence time. Gate blush occurs when the injection speed exceeds the melt’s critical shear rate at the gate; the correction is a larger gate diameter or lower velocity, not higher melt temperature. Sprue sticking is common when the nozzle tip temperature drops below 190°C or when the nozzle tip radius does not match the sprue bushing radius. These failure modes have been documented on conventional hydraulic presses with clamp forces from 80 tonnes to 250 tonnes when processing unmodified PLA; they are not machine-specific but are amplified by poor thermocouple placement and worn check rings.

    Storage Conditions That Prevent Hydrolytic Pre-Degradation

    Unopened resin should be stored in sealed aluminum-foil multiwall bags at 15–35°C and protected from direct sunlight. Opened bags should be used within 8 h in ambient relative humidity above 60%, or resealed under dry nitrogen. If pellets have been exposed to moisture, they must be re-dried at 80°C for at least 4 h; repeated hot-air drying cycles above 100°C may generate lactide dust and increase feed bridging in the hopper. The resin is not recommended for prolonged exposure to hot aqueous acid or alkaline media above 50°C, and its room-temperature abrasion resistance is below that of semi-crystalline fossil-based engineering resins. No food-contact, medical, or compostability claim is made without the supplier’s lot-specific certification; compliance statements under REACH Article 33 of Regulation (EC) No 1907/2006 or RoHS Directive 2011/65/EU Annex II should be verified against the Safety Data Sheet and certificate of analysis.

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