| HS Code | 300959 |
| Chemical Name | Polylactic Acid (PLA) |
| Cas Number | 9051-89-2 |
| Molecular Formula | (C3H4O2)n |
| Appearance | Natural white pellets |
| Density | 1.25 g/cm3 |
| Melt Flow Rate | 10-20 g/10min (190°C/2.16 kg) |
| Melting Point | 150-170 °C |
| Glass Transition Temperature | 55-60 °C |
| Tensile Strength | 50-60 MPa |
| Elongation At Break | 2-5 % |
| Flexural Strength | 80-100 MPa |
| Flexural Modulus | 3000-3500 MPa |
| Notched Izod Impact Strength | 2-4 kJ/m2 |
| Vicat Softening Point | 55-60 °C |
| Heat Deflection Temperature | 55-60 °C |
| Moisture Content | ≤0.05 % |
| Biobased Content | ≥90 % |
| Biodegradability | Compostable |
| Processing Method | Injection molding |
As an accredited Polylactic Acid (PLA) REVODE713 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Polylactic Acid (PLA) REVODE713 is packaged in sealed 25 kg moisture-barrier bags, palletized for industrial shipping and storage. |
| Container Loading (20′ FCL) | 20′ FCL loading: palletized 25 kg bags of Polylactic Acid (PLA) REVODE713, stretch-wrapped, strapped, and secured for export shipment. |
| Shipping | REVODE713 is a non-hazardous biodegradable polylactic acid resin. Ship in sealed 25 kg bags or jumbo bags under normal conditions. Protect from moisture, heat, and sunlight. No UN hazard class, special labels, or temperature control required. Transport by road, sea, rail, or air. Follow local regulations. |
| Storage | Store Polylactic Acid (PLA) REVODE713 in a cool, dry, well-ventilated area, away from direct sunlight, heat, and moisture. Keep original packaging tightly sealed to prevent moisture absorption. Avoid strong oxidizers, acids, bases, and ignition sources. Maintain temperatures below 30°C (86°F), use stock rotation, and protect from physical damage. Shelf life is typically 12 months when stored properly. |
| Shelf Life | Polylactic Acid (PLA) REVODE713 has a 12–24-month shelf life when stored in sealed, cool, dry conditions, away from direct sunlight. |
On high-cavitation injection lines producing disposable cutlery, REVODE713 is pre-dried at 80 °C for 4 h in a desiccant dryer with a dew point below −40 °C. Moisture above 250 ppm in the hopper causes hydrolysis-induced chain scission during plastication, producing silver streaks at the gate and a measurable upward drift in melt mass-flow rate under ISO 1133-1:2022. The melt is processed in a reciprocating screw injection machine with L/D 20:1–24:1 and a compression ratio of 2.2:1–2.8:1; barrel temperatures are profiled from 180 °C at the feed throat to 210 °C at the nozzle, with an immersion-probe melt temperature of 200 °C ± 5 °C. This window is narrow because depolymerization accelerates above 220 °C while melt viscosity remains too high for satisfactory cavity replication below 190 °C.
Mold surface temperature is held at 25–30 °C for unmodified REVODE713. Higher mold temperatures extend cycle time and induce ejection deformation because the heat deflection temperature of the amorphous resin is approximately 55 °C under ASTM D648 method A at 0.455 MPa. Injection speed is set between 80 mm/s and 120 mm/s for wall thicknesses of 1.5–2.0 mm; holding pressure is maintained at 70–100 MPa until gate freeze. Residence time is kept below 5 min; exceeding this threshold on production interruptions generates lactide reformation and surface discoloration that cannot be corrected by raising back pressure. Production-scale molders also report sticking on polished chrome cavities above 30 °C, which is addressed with external mold release or a lower mold temperature rather than internal slip additives.
Clamp force is calculated from projected cavity area and a cavity pressure of 30–40 MPa. For a 12-cavity spoon mold with 25 cm² projected area per cavity, the required clamping force is 90–120 tonnes. This relationship is specific to thin-wall utensils; thicker fork handle sections require reduced mold-open ejector speed to avoid stress whitening at the ejector pin marks. Molded cutlery is conditioned at 23 °C and 50 % RH for 48 h before tensile yield is measured under ISO 527-2/1A; unmodified REVODE713 surfaces resist load-induced creep only up to service temperatures of 60 °C, which excludes continuous hot-soup contact above this threshold.
Terminal cutlery made from REVODE713 is positioned for industrial composting because the polymer backbone contains no intentionally added halogen or aromatic content. Disintegration is assessed under EN 13432:2000 at 58 °C ± 2 °C in a controlled composting pilot; acceptance requires ≥ 90 % dry-mass loss within 12 weeks and demonstration that residual compost does not inhibit cress seed germination. In parallel, heavy-metal concentrations are screened against the concentration limits in EU Packaging Directive 94/62/EC Article 11 and REACH Annex XVII entries for cadmium, lead, hexavalent chromium, and mercury, although REVODE713 itself is polymerized from lactic acid monomer and is not formulated with phthalate plasticizers.
REVODE713 is suitable for transparent cold-chain containers, deli cups, and dairy-adjacent clamshells only when the service temperature remains below the heat deflection temperature. Unmodified amorphous parts exhibit HDT of 55 °C under ASTM D648 at 0.455 MPa. Hot-fill at 85 °C produces immediate sidewall buckling and lid-seat ovalization. The practical ceiling for continuous food-contact use is therefore 50 °C for rigid wall structures under 0.5 MPa internal stress. For cold-chain use at 0–8 °C, impact strength remains a potential limitation; notched Izod declines as temperature falls, and brittle cracks can initiate at the hinge score if the clamshell is opened below −10 °C.
Food-contact status is established by migration testing rather than by a single resin designation. For European applications, compliance with (EU) No 10/2011 Annex I is required; lactic acid monomer is listed without a specific migration limit, but total migration into simulants must not exceed 10 mg/dm² under EN 1186-1:2002. The test matrix for REVODE713 in a typical cold-chain application uses simulant A 10 % v/v ethanol for aqueous foods, simulant B 3 % w/v acetic acid for acidic dairy dips, and simulant D2 refined olive oil for fatty dressings, with 10-day exposure at 40 °C representing refrigerated long-term storage. U.S. market access typically proceeds through an effective Food Contact Notification; extraction testing is performed under 21 CFR 175.300 for aqueous and fatty food types because PLA is not listed as a cleared polymer under 21 CFR 177.1520.
| Compliance requirement | Test method | Representative condition | Acceptance limit |
|---|---|---|---|
| Total migration | EN 1186-1:2002 | 10 days at 40 °C, simulant D2 | ≤ 10 mg/dm² |
| Lactic acid monomer | (EU) No 10/2011, Annex I | Specific migration calculation | No SML assigned |
| U.S. extraction | 21 CFR 175.300 | Water, 8 % ethanol, heptane | Net extractives within FCN tolerance |
| Compostability | EN 13432:2000 | 58 °C, 12 weeks | ≥ 90 % disintegration |
High-speed transparent container molding with REVODE713 requires careful control of melt cushion and screw recovery. Injection speeds above 150 mm/s can create shear heating at the gate exceeding 220 °C, which reduces local molecular weight and produces stress whitening at the hinge. A cushion of 3–5 mm and screw decompression of 2–3 mm prevent drooling and gate stringing. Mold temperatures are maintained at 20–25 °C to preserve transparency and minimize spherulite haze; at mold temperatures above 30 °C, slow crystallization begins at the wall and reduces total light transmittance below 85 % as measured by ASTM D1003.
Rigid cosmetic outer shells and closure systems molded from REVODE713 require a different chemical-resistance assessment than styrenics or polyolefins because the polyester backbone is susceptible to transesterification and solvent-induced crazing in the presence of certain ester solvents. A powder compact base with a wall thickness of 2.0 mm is injection-molded at a melt temperature of 200 °C and a mold temperature of 20 °C; holding pressure is adjusted to 60–80 MPa to minimize sink marks at the living-hinge bridge. Under ISO 175:2010, unstressed REVODE713 tensile bars immersed in refined olive oil at 23 °C for 30 days show a tensile strength retention above 85 %, but immersion in ethyl acetate or methyl ethyl ketone produces visible grazing within 24 h. Published data for REVODE713 in aggressive cosmetic matrices remains limited; pre-production immersion testing under ISO 175:2010 is therefore required before specifying it for oil-saturated wiper systems or esters such as dioctyl carbonate.
Decorative closures with a 1.0–1.2 mm nominal wall thickness are filled at injection speeds of 100–150 mm/s using fan gates that distribute melt circumferentially. This gate geometry reduces anisotropic shrinkage that would otherwise ovalize a threaded cap. Because PLA exhibits low melt strength and high shear sensitivity, a sharp-edge gate can generate gate blush and surface streaks; valve-gated hot runners are avoided unless the manifold is purged at 200 °C and held for less than 3 min. Mold release is typically applied by external sprays rather than compounded internal release agents to avoid contaminating the polymer matrix and reducing transparency under ASTM D1003.
Terminal products include powder jar outer shells, compact mirror frames, and brush handles that are not subjected to high torsional load. Heat exposure in automobile interiors or near beauty-salon lamps above 55 °C leads to dimensional relaxation, so the boundary condition for REVODE713 in cosmetic packaging is ambient shelf display only.
REVODE713 can be molded into building blocks, puzzle trays, and shape-sorting toys provided the final article meets the mechanical and migration requirements of the Toy Safety Directive 2009/48/EC and EN 71-3:2019+A1:2021. Migration of 19 elements is quantified by ICP-MS after immersion in 0.07 M HCl at 37 °C for 2 h; limits are applied by toy material category. Unmodified PLA is not intentionally formulated with lead, cadmium, mercury, or hexavalent chromium, but color masterbatch carriers and organic pigments must be screened because heavy-metal contamination can enter during pigment dispersion. Each color lot is pre-screened against the soluble-element limits before approval for production.
Mechanical robustness limits the use of unmodified REVODE713 in small toy features. Notched Izod at 23 °C is approximately 3.0 kJ/m² under ISO 180/A; thin snap-fit arms below 2.0 mm thickness fracture during the drop test of EN 71-1 when the impact energy at floor contact exceeds the local crack-initiation threshold. Impact-modified formulations incorporating 5–10 wt% biodegradable impact modifier raise notched Izod to 6–8 kJ/m² but reduce total light transmittance from 85 % to approximately 60 % under ASTM D1003. Molders should not exceed 10 wt% modifier if transparency is a design requirement; above this level, anisotropic shrinkage produces warpage in flat puzzle bases.
Processing conditions for toy components use a melt temperature of 200 °C ± 5 °C, mold temperature 20–25 °C, and a holding pressure of 60–80 MPa. Weld lines at hole features are a critical failure location because PLA melt fronts cool rapidly and do not re-entangle strongly; increasing injection speed to 120 mm/s and moving the gate to minimize melt-front meeting angle improves weld-line factor retention under ISO 527-2. Residual monomer content should be verified by gas chromatography before toy use because high residual lactide can produce an acidic odor in sealed packaging.
Closed-loop regrind use in disposable cutlery, closures, and packaging auxiliaries introduces thermal history that shifts melt mass-flow rate upward and reduces tensile yield. A single pass through a granulator and re-extrusion at 210 °C shortens PLA chains by hydrolysis at residual moisture and by thermal degradation at the screw interface. The melt mass-flow rate under ISO 1133-1:2022 at 210 °C and 2.16 kg can drift from a virgin resin value in the 10–20 g/10 min range to 22–28 g/10 min after one regrind cycle at 30 wt% addition, depending on granulator fines and screw residence time. Amine-based heat stabilizers are avoided in this closed-loop system because amine groups catalyze ester cleavage and further raise melt-flow drift.
At 30 wt% regrind, molded parts retain sufficient tensile yield for short-cycle closures when measured under ISO 527-2; however, the practical limit appears when the injection molder compensates for lower viscosity by reducing melt temperature. Below 190 °C, the melt does not fully fill thin-wall sections, while above 220 °C depolymerization accelerates. Regrind above 30 wt% also raises the carboxylic acid end-group content, which reduces hydrolytic stability in humid distribution chains. A closed-loop system should use a desiccant dryer on mixed virgin and regrind feed, blend ratio control within ± 2 wt%, and granulator screens no coarser than 6 mm to minimize melt-temperature variation.
The terminal product categories for high-regrind REVODE713 are limited to short-service-life packaging clips, tamper-evident caps, and industrial sprues where food-contact migration testing is not the limiting specification. For food-contact articles, regrind inclusion above 30 wt% must be re-validated under the same migration protocol as virgin resin, because low-molecular-weight degradation products may increase overall migration. Without such validation, regrind is kept below 30 wt% and is sourced only from in-house production scrap, never from post-consumer recycled PLA.
Post-mold annealing of REVODE713 produces a measurable increase in heat deflection temperature when parts are restrained in forming fixtures to prevent dimensional change. Unmodified injection-molded specimens annealed at 100 °C for 30 min in a circulating air oven develop crystallinity that raises HDT from 55 °C to approximately 90 °C under ASTM D648 at 0.455 MPa. The annealing window is narrow because moldings heated above 105 °C show visible distortion and surface oil staining from low-molecular-weight fractions; below 95 °C, the crystallization half-time is too long for economical cycle time. Differential scanning calorimetry under ISO 11357-3:2018 is used to monitor the glass transition at 58–62 °C and the cold-crystallization exotherm before release to production.
Annealed REVODE713 is relevant for office supplies and reusable consumer articles that must withstand brief exposure to boiling water vapor, such as tea-tray compartments and cutlery handles in quick-service restaurants. However, the annealed part is not dishwasher-safe because wet heat above 60 °C under alkaline detergent promotes hydrolytic surface whitening. Flexural modulus after annealing remains above 3.5 GPa under ISO 178, but elongation at break is reduced, so annealed parts are not suited to snap-fit closures. The annealing protocol must be validated on the actual part geometry because thick sections develop internal crystallinity gradients that produce residual stress at the core-skin boundary; polarizing light microscopy of a cross-section is recommended to confirm uniform spherulite distribution before large-batch release.
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Polylactic acid REVODE713 is a semi-crystalline thermoplastic polyester supplied as cylindrical pellets for injection moulding of thin-wall rigid single-use articles. The grade is produced by ring-opening polymerization of lactide, with residual lactide controlled to reduce melt-phase viscosity drift during hot-runner processing. Under ISO 1133-1:2022 Method A at 190 °C and 2.16 kg, the supplier technical datasheet lists a melt flow rate of 15 g/10 min; density is reported as 1.24 g/cm³ under ISO 1183-1:2019 Method A. The material is not intended for hot-fill or retort applications because unannealed parts exhibit heat deflection temperatures below 60 °C, while annealed specimens reach 95 °C at 0.45 MPa under ISO 75-2:2013 Method B.
The high melt flow rate of REVODE713 is achieved by molecular weight distribution control rather than by addition of plasticizer. Lot-to-lot variation in melt flow rate directly affects screw recovery time, cushion stability, and thin-wall filling length. Injection moulders operating 80–120 t electric machines commonly observe lower injection pressure demand with REVODE713 than with extrusion-grade PLA having a melt flow rate of 3–5 g/10 min; however, published data for REVODE713-specific pressure drop in thin-wall tooling are limited. Machine-specific validation of gate freeze-off, weld-line strength, and screw recovery is therefore required before tool transfer.
The principal differentiator is rheological. Extrusion-grade PLA with melt flow rate at or below 5 g/10 min is designed for sheet, cast film, and profile dies where melt strength and bubble stability are critical. REVODE713, with a published melt flow rate of 15 g/10 min, fills thin cavities at lower injection pressures but exhibits reduced hang-time in blow moulding and lower extrudate swell. The higher fluidity is not achieved through plasticizer addition; it is controlled by molecular weight distribution and residual lactide monomer content during polymerisation.
The crystallization behaviour also differs from amorphous PLA grades. REVODE713 is semi-crystalline; after annealing at 90 °C for 60 s, the part develops sufficient crystallinity to raise heat deflection temperature from approximately 55 °C to 95 °C. Exact crystallization half-time depends on nucleant density, mould temperature, and cooling rate. Published data for this specific configuration is limited; cold-mould parts remain largely amorphous and must not be used above the glass transition temperature range of 55–60 °C.
The following supplier-published typical values are obtained on injection-moulded ISO Type 1A multipurpose specimens. They are not design minima or maxima and must be supplemented by lot-specific certificate of analysis data for incoming quality control.
| Property | Test method | Typical value | Unit |
|---|---|---|---|
| Melt flow rate at 190 °C and 2.16 kg | ISO 1133-1:2022 Method A | 15 | g/10 min |
| Density | ISO 1183-1:2019 Method A | 1.24 | g/cm³ |
| Tensile stress at yield | ISO 527-2:2012 Type 1A | 60 | MPa |
| Tensile elongation at break | ISO 527-2:2012 Type 1A | 6 | % |
| Flexural modulus | ISO 178:2019 | 3500 | MPa |
| Flexural strength | ISO 178:2019 | 95 | MPa |
| Notched Izod impact at 23 °C | ISO 180:2000 + A1:2006 | 3.0 | kJ/m² |
| Heat deflection temperature, 0.45 MPa, annealed | ISO 75-2:2013 Method B | 95 | °C |
| Melting temperature, DSC | ISO 11357-3:2018 | 150–160 | °C |
| Glass transition temperature, DSC | ISO 11357-2:2020 | 55–60 | °C |
| Mould shrinkage | ISO 294-4:2018 | 0.3–0.5 | % |
| Residual moisture after drying | ISO 15512:2019 | <250 | ppm |
Notched Izod impact is particularly sensitive to notch radius and conditioning interval. The value cited applies after 48 h conditioning at 23 °C and 50 % relative humidity. Weld lines, gate blush, and sharp radii reduce mechanical performance in finished parts below the values obtained on standard multipurpose specimens.
The recommended melt temperature range for REVODE713 is 180–210 °C measured at the nozzle. Barrel rear-to-nozzle profiles are typically set at 170/180/190/195/200 °C, but the exact profile depends on shot size, screw recovery time, and hot-runner balance. Nozzle temperature should not exceed 220 °C when average melt residence time is below 2 min. At 230 °C and above, lactide regeneration by back-biting degradation becomes measurable and can cause screw slippage, gas generation, and progressive loss of injection cushion.
For cold-mould processing, mould temperature is maintained at 15–30 °C. This condition delivers short cycle times and high surface gloss but yields mostly amorphous skins with lower upper service temperature. For maximum heat resistance and dimensional stability, mould temperature is raised to 90–100 °C and hold time is extended to 60–90 s to permit crystallisation. This thermal treatment increases cycle time by 30–60 % relative to cold-mould operation and is justified only when the part must resist brief exposure to 60 °C or higher.
Production-scale injection moulding on 80–120 t electric toggle machines indicates that screw recovery time is often the limiting factor rather than injection speed. A general-purpose screw with L/D ratio of at least 20:1 and compression ratio 2:1–3:1 is acceptable. Hot-runner manifolds should be operated at 190–210 °C and purged with a general-purpose purging compound before colour changes. Gate diameters below 0.8 mm tend to produce premature freeze-off and jetting; valve-gate systems should not open against a cold cavity because solidified PLA blocks the gate.
Capillary rheometry at 190 °C shows that PLA melts shear-thin. The power-law index is typically 0.4–0.7 at apparent shear rates between 100 s⁻¹ and 1000 s⁻¹. Injection pressure predictions based solely on melt flow rate therefore underestimate pressure drop in thin-walled sections. For gate diameters below 0.8 mm, shear viscosity at the intended apparent shear rate should be obtained using a capillary rheometer with a 1 mm die, and pressure drop should be calculated with the Bagley correction for entrance effects.
Crystallization of REVODE713 in a mould is controlled by cooling rate, nucleant density, and flow-induced orientation. At a mould temperature of 25 °C, the part exits largely amorphous; the glass transition temperature of 55–60 °C then limits upper service temperature. At a mould temperature of 90–100 °C, spherulite growth proceeds during the cooling and hold phase. Literature data for PLA report isothermal crystallization half-times at 100–110 °C in the range of 1–3 min for nucleated formulations; published data for REVODE713-specific nucleation condition is limited.
PLA is hygroscopic; the ester backbone undergoes hydrolytic cleavage in the melt when free water is present. Moisture content in open storage at 23 °C and 50 % relative humidity can exceed 0.2 wt% within 4 h for pellets with high surface area, although the exact uptake depends on pellet geometry and crystallinity. Before processing, REVODE713 must be dried in a desiccant dryer with supply-air dew point at or below −40 °C. The supplier-published drying condition is 80 °C for 4 h; at ambient relative humidity above 60 %, drying time should be extended to 6 h and hopper residence time limited to 8 h.
The maximum recommended residual moisture after drying is 250 ppm by Karl Fischer titration. Above this threshold, the melt exhibits reduced viscosity, erratic cushion control, splay on part surfaces, and reduced weld-line strength before visible silver streaks appear. A fall in melt pressure at constant screw speed is an early production indicator of moisture-induced degradation. Closed-loop material handling with dry air conveying is recommended; ambient air conveying reintroduces moisture and negates dryer performance.
Melt-phase degradation is not limited to hydrolysis. At melt temperatures above 220 °C, random chain scission and lactide regeneration proceed at rates that depend on residence time and residual metal carboxylate residues from polymerisation catalyst. Injection moulders should keep cumulative screw residence time below 5 min, use shut-off nozzles to reduce melt stagnation, and purge immediately after heater failures. Re-extrusion of regrind should be limited to 20 wt% unless lot-specific mechanical property evaluation demonstrates otherwise.
REVODE713 occupies the high-flow injection moulding position for compostable single-use rigid articles. The following comparison uses nominal ranges; melt flow rate values are not directly comparable because PLA is measured at 190 °C and polypropylene at 230 °C under the same 2.16 kg load.
| Attribute | REVODE713 | Extrusion-grade PLA | Unfilled polypropylene |
|---|---|---|---|
| Melt flow rate class | 15 g/10 min at 190 °C | 3–5 g/10 min at 190 °C | 12–25 g/10 min at 230 °C |
| Drying requirement | Required, desiccant dryer, −40 °C dew point | Required, desiccant dryer, −40 °C dew point | Not normally required for non-flame-retardant grades |
| Heat deflection temperature, 0.45 MPa | 95 °C annealed | 55–95 °C depending on crystallinity | 100–115 °C |
| Notched Izod impact at 23 °C | 3.0 kJ/m² | 3–5 kJ/m² | 5–10 kJ/m² |
| Mould shrinkage class | 0.3–0.5 % | 0.2–0.4 % | 1.0–2.0 % |
The polypropylene column is included only to illustrate processing differences in drying, shrinkage, and ductility; it does not imply mechanical equivalence. Within the PLA family, REVODE713 is not a substitute for high-heat PLA containing nucleating agents or for impact-modified PLA used in reusable food containers. Impact-modified PLA grades may reach 8–15 kJ/m² notched Izod impact but lose tensile modulus relative to neat injection PLA. REVODE713 is therefore appropriate where stiffness, thin-wall fill, and short cycle time dominate over ductility and elevated-temperature load-bearing capability.
Food-contact compliance is not an intrinsic property of the resin. Finished articles must be tested for overall migration under EU Regulation (EU) No 10/2011 and, where relevant, for specific migration of lactide and lactic acid. United States food-contact status must be confirmed through the applicable 21 CFR citation or Food Contact Notification for the final article. REACH obligations under Regulation (EC) No 1907/2006 attach to the legal importer; the polymer itself may be exempt from registration, but the lactic acid monomer is a registered substance.
Incompatibilities include strong alkaline colorants, amine-based additives, and high concentrations of transition-metal carboxylates; these accelerate ester hydrolysis or transesterification. Mixed melt processing with polyvinyl chloride is not recommended because hydrogen chloride evolution degrades PLA. Storage should be in sealed moisture-proof packaging at or below 40 °C; opened bags should be used within 8 h or resealed under dry air. Published data for this specific configuration is limited with respect to long-term UV weathering, dishwasher cycling, and repeated hot caustic washing. These conditions are outside the intended use window for neat injection-moulded PLA.