| HS Code | 424098 |
| Product | Polylactic Acid REVODE213TR |
| Chemical Formula | (C3H4O2)n |
| Cas Number | 9051-89-2 |
| Material Type | Biodegradable polylactic acid resin |
| Appearance | Transparent to light yellow pellets |
| Density | 1.25 g/cm3 |
| Melt Flow Rate | 10-20 g/10 min at 190°C/2.16 kg |
| Melting Point | 155-165°C |
| Glass Transition Temperature | 55-60°C |
| Heat Deflection Temperature | 55°C at 0.45 MPa |
| Vicat Softening Temperature | 60°C |
| Tensile Strength | 50-60 MPa |
| Tensile Modulus | 3000-3500 MPa |
| Elongation At Break | 3-5% |
| Flexural Strength | 70-80 MPa |
| Flexural Modulus | 3000-3500 MPa |
| Notched Izod Impact Strength | 2-3 kJ/m2 |
| Water Absorption | <0.5% |
| Biobased Content | >90% |
| Biodegradability | Compostable |
| Processing Method | Injection molding |
| Thermal Decomposition Temperature | >250°C |
As an accredited Polylactic Acid REVODE213TR factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Polylactic Acid REVODE213TR is supplied in 25 kg net-weight moisture-resistant bags, palletized and securely wrapped for shipment. |
| Container Loading (20′ FCL) | 20′ FCL loaded with non-hazardous Polylactic Acid REVODE213TR in 25 kg bags, securely stowed and lashed for ocean transport. |
| Shipping | Polylactic Acid REVODE213TR is shipped as a non-hazardous, solid thermoplastic resin, typically in moisture-resistant 25 kg bags or bulk bags. It requires no special transport classification. Keep dry, cool, ventilated, away from direct sunlight and ignition sources. Avoid moisture exposure to prevent hydrolysis. |
| Storage | Store Polylactic Acid REVODE213TR in a cool, dry, well-ventilated warehouse. Keep original packaging sealed and palletized, away from direct sunlight, heat, moisture, and oxidizing agents. Recommended conditions: 10–30 °C, relative humidity below 50%. Prevent prolonged exposure to humid air to avoid hydrolysis. Rotate stock and use within specified shelf life. Keep away from acids, alkalis, and strong solvents. |
| Shelf Life | Polylactic Acid REVODE213TR: typical shelf life is 12 months when stored unopened in a cool, dry area, away from moisture/heat. |
In cold-fill transparent food packaging, REVODE213TR is processed on standard three-zone general-purpose screws with compression ratios between 2.5:1 and 3.0:1 and check-ring non-return valves. Drying in a desiccant-bed dryer at 80 °C for 4–6 h to a residual moisture content below 250 ppm is mandatory; hopper dew point must remain below -40 °C because PLA hydrolyzes at melt temperatures above 185 °C when moisture exceeds 0.025 wt%. Melt temperature is held at 195–205 °C at the nozzle, and mould temperature is set between 20 °C and 35 °C to limit haze. Food-contact compliance is established under Regulation (EU) No 10/2011 Annex I for the lactic acid monomer (FCM substance number 134) and under the supplier’s FDA Food Contact Notification where applicable; converters must verify overall migration below 10 mg/dm² under EN 1186-1:2002 and, where required, specific migration of lactic acid using appropriate migration test methods. A typical formulation for transparent lids and clamshells adds 0.5–1.5 wt% of a PLA-compatible slip/antiblock masterbatch and 0.2–0.5 wt% of a sorbitol-free nucleating agent to reduce cycle time, at the cost of a 2–5 % increase in haze measured by ASTM D1003-21. The process involves high-speed injection with fill times of 0.2–0.5 s for wall sections of 0.6–1.2 mm, followed by hold pressures of 50–70 MPa to minimise sink marks. Terminal products include cold-fill deli cups, salad bowls, produce punnets, clear lids for dairy drinks, and hinged clamshells for bakery items; all are limited to service temperatures below 55 °C unless post-mould annealing at 90–110 °C for 20–30 min has been qualified.
The living hinge is the first failure zone in PLA packaging because the polymer’s elongation at break, measured on dry type I specimens under ASTM D638-14, is typically below 5 %. In closures and flip-top caps, REVODE213TR is modified with an aliphatic polyester impact modifier at 5–10 wt%, plus 0.2–0.5 wt% of an epoxy-functional chain extender to rebuild melt strength after regrind addition. The modifier increases notched impact strength from 2–3 kJ/m² to 8–15 kJ/m² when tested under ISO 179-1:2023, but it reduces light transmission from approximately 90 % to 70–80 % at 550 nm. Moulding requires a cold runner system or thermally gated hot runner with small gate diameter of 0.6–1.0 mm; the hinge zone is gated so that flow crosses the hinge transversely to prevent molecular orientation along the flex line. Screw speed is limited to 60–120 rpm, and back pressure is kept at 0.5–1.5 MPa to avoid viscous heating and yellowing. Compliance for cosmetics and personal-care closures follows REACH, EU 10/2011 if food contact is involved, and ISO 9001:2015 traceability; heavy-metal migration for cosmetics packaging is tested under EN 71-3 when formats reach toy-like dimensions. Terminal products include flip-top caps for shampoos, clear closure shells for colour cosmetic jars, translucent pill organizers, and dispensing caps for lotion bottles; published data for hinge cycle life of REVODE213TR specifically below −20 °C is limited.
Regrind use is constrained by the molecular-weight loss that occurs during each heat history. Melt-flow-rate measurements under ISO 1133-1:2022 at 210 °C/2.16 kg show an increase of 2–5 g/10 min after three passes when drying is incomplete, which corresponds to a 10–20 % reduction in weight-average molecular weight. For transparent lids, first-pass regrind from cold-runner scrap is incorporated at 10–20 wt%, while hot-runner edge trim and start-up purge are limited to 5 wt%. Above 20 wt%, notch sensitivity under ASTM D256-10 becomes the controlling variable, not haze. The processing window narrows: melt temperature must be reduced from 200 °C to 190 °C, and residence time must be held below 3 min to avoid lactide reformation and off-odour in the finished lid. Sorting and drying of regrind at 60 °C for 2 h before blending is required, because any moisture in the recycled fraction causes uneven melt viscosity and flow lines. For food-contact lids, the use of post-industrial scrap is covered under the converter’s good manufacturing practice system and the overall migration limit of 10 mg/dm² under Regulation (EU) No 10/2011; if recycled content from post-consumer sources is introduced, compliance with Regulation (EU) 2022/1616 on recycled plastic food-contact materials must be evaluated. Terminal products include high-clarity lids for cold-beverage cups, sauce portion cups, and dairy single-serve containers; haze remains below 5 % at 1 mm thickness only when regrind is kept below 15 wt% and dried to below 100 ppm moisture.
Table 1. Regrind addition limits and failure thresholds for high-clarity lid production.
| Regrind blend ratio | Measured property | Failure threshold | Test method |
|---|---|---|---|
| 10 wt% | Haze at 1 mm | 3–4 % | ASTM D1003-21 |
| 15 wt% | Haze at 1 mm | 4–5 % | ASTM D1003-21 |
| 20 wt% | Notched Izod impact | 2.0–2.5 kJ/m² | ASTM D256-10 |
| >20 wt% | Melt-flow-rate drift | +5 g/10 min vs virgin | ISO 1133-1:2022 |
PLA has a sharper shear-thinning response than PET and a lower processing plateau. At the nozzle, shear rates in thin-wall moulding exceed 10,000 s⁻¹, where REVODE213TR’s apparent viscosity can drop by 60–70 % relative to its zero-shear value. Capillary rheometry data at 200 °C show a transition from Newtonian to power-law behaviour between 100 s⁻¹ and 1,000 s⁻¹; above 5,000 s⁻¹, melt fracture and gate blush appear when melt temperature is below 190 °C. Injection machines used for deep-draw clear housewares typically have screw diameter of 22–32 mm, a shot weight utilisation of 50–80 % of barrel capacity, and clamp force between 800 kN and 3,500 kN. The process uses a first-stage injection speed of 80–150 mm/s, a second-stage hold pressure of 40–65 MPa for 2–4 s, and cooling time of 8–20 s depending on wall thickness. A critical boundary occurs at wall thickness below 1.0 mm: the cooling rate exceeds PLA’s crystallisation half-time, so the part remains amorphous and exhibits high haze if mould temperature is above 40 °C. At wall thickness above 3.0 mm, sink marks and vacuum voids require gas counterpressure of 0.5–1.0 MPa or sequential valve-gate opening. Transparent housewares are compounded with 0.2–0.8 wt% of a nucleating masterbatch only when the design can tolerate a transmission drop of 5–10 %; for maximum clarity, no nucleating agent is used and mould temperature is kept at 15–25 °C. Compliance follows RoHS 2011/65/EU, REACH Article 33 SVHC screening, and mechanical testing under ISO 527-1:2019 for tensile and ISO 178:2019 for flexural properties. Terminal products include clear desk organisers, drawer storage trays, magazine files, and display stands for small retail items; these products are not intended for dishwasher service above 55 °C or prolonged UV exposure unless stabilised.
Across short-run cosmetic packaging campaigns, REVODE213TR is processed in eight-cavity hot-runner tools with pneumatically actuated valve gates to minimise gate vestige on transparent outer surfaces. The formulation is adjusted after measurement of yellowness index under ASTM D1925-70 and haze under ASTM D1003-21: a 0.1–0.3 wt% loading of a PLA-compatible UV absorber and 0.3–0.8 wt% of a scratch-resistant masterbatch are used for jars that will undergo automated filling lines. Pearlescent or tinted batches replace the masterbatch with 1–3 wt% of pigment masterbatch; the proportion is verified because loadings above 3 wt% cause brittleness and gate-stringing. The downstream process requires low-speed injection at 30–60 mm/s for thick-wall jars of 2–5 mm wall thickness, followed by extended hold pressure of 60–80 MPa for 5–10 s to prevent internal shrinkage. Mould temperature is cycled from 15–25 °C for optical clarity to 90–100 °C for stress-relief annealing of threads and snap-fit undercuts, but the two-stage thermal cycle extends total cycle time by 10–20 s. Regulatory compliance includes Regulation (EC) No 1223/2009 for cosmetic packaging safety, REACH Annex XVII restrictions, and ISO 22715:2006 for cosmetic packaging classification; if the jar contains food-like products, EU 10/2011 migration testing is added. Terminal products include transparent cream jars, compact powder bases, lip balm tubes, serum bottle over-caps, and fragrance collar inserts. Published data for long-term fragrance compatibility with unmodified PLA is limited; barrier-coated liners are recommended for aggressive solvents and ethanol-containing formulations.
For filament extrusion, REVODE213TR is dried to 100–250 ppm moisture using a desiccant hopper at 70–80 °C, then processed on a single-screw extruder with a screw diameter of 25–45 mm, an L/D ratio of 28:1 to 36:1, and a melt pump for constant throughput. The formulation normally remains unfilled; where colour is required, 0.5–1.5 wt% of colour masterbatch is added at the throat, and 0.1–0.2 wt% of a heat stabilizer is used to preserve molecular weight during multiple heat histories. Melt temperature at the die is held at 180–195 °C, water-bath temperature at 40–55 °C, and filament diameter is controlled to 1.75 ± 0.05 mm or 2.85 ± 0.05 mm using dual-axis laser gauges. Ovality above 0.03 mm or diameter drift exceeding 0.05 mm leads to extruder skipping, which is the main field failure. Compliance for toys and educational filament includes EN 71-3 migration of elements, REACH, and RoHS 2011/65/EU; for food-contact printed articles, the finished printed object must be assessed under EU 10/2011 if intended for repeated contact. Terminal products are PLA filament spools for fused deposition modelling machines, used in transparent prototypes, anatomical models, jigs, and classroom printing; the amorphous printed parts have heat deflection below 55 °C under ISO 75-2:2013 method B unless annealed at 80–100 °C for 30–60 min.
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Polylactic Acid REVODE213TR is a poly(L-lactic acid)-based injection-molding resin supplied in transparent pellet form and intended for thin-wall packaging, cosmetic components, and short-term medical consumables where optical clarity and stiffness are controlled by cooling rate. The grade is differentiated from general-purpose polylactide by a narrower melt viscosity band and by an additive package that suppresses spherulitic haze during rapid solidification, not by a fundamental change in polymer backbone. When conditioned to 0.25% moisture or below, the resin melts into a pseudoplastic stream with a melt flow index of 10–20 g/10 min at 190 °C under 2.16 kg load in accordance with ISO 1133-1:2022. Density measured under ISO 1183-1:2019 is typically 1.24 g/cm³. These figures are representative datasheet ranges for transparent PLA injection grades of this viscosity class; batch-specific certificates should be consulted for lot-level variation.
General-purpose PLA injection grades typically contain minimal nucleation and rely on rapid mold cooling to preserve amorphous transparency, but they exhibit inconsistent haze on thick sections because slow core cooling permits spherulite growth. REVODE213TR uses a nucleated formulation that raises the onset crystallization temperature from approximately 105–110 °C to 120–125 °C under non-isothermal DSC at 10 °C/min heating, allowing faster solidification without excessive crystal size. This shifts the practical mold-temperature limit for transparent molding from 40 °C in unmodified PLA to 60 °C; above this threshold, haze increases because spherulite diameter approaches visible-light wavelengths. The trade-off is reduced melt elasticity and slightly lower notched impact strength compared with opaque high-heat PLA grades compounded with talc or stereocomplex nucleating agents.
| Property | Test Standard | REVODE213TR Typical | General-Purpose Transparent PLA | Nucleated Opaque PLA High-Heat |
|---|---|---|---|---|
| Melt flow index | ISO 1133-1:2022 | 10–20 g/10 min | 5–15 g/10 min | 8–15 g/10 min |
| Density | ISO 1183-1:2019 | 1.24 g/cm³ | 1.24 g/cm³ | 1.25 g/cm³ |
| Tensile strength | ISO 527-2:2012 | 60–65 MPa | 58–62 MPa | 55–60 MPa |
| Elongation at break | ISO 527-2:2012 | 3–5% | 4–6% | 2–4% |
| Notched Izod impact | ISO 180:2023 | 2.0–3.0 kJ/m² | 2.5–3.5 kJ/m² | 3.0–4.0 kJ/m² |
| Heat deflection temperature at 0.45 MPa | ISO 75-2:2013 | 55–60 °C | 50–55 °C | 90–100 °C |
| Light transmittance on 2 mm plaque | ASTM D1003-21 | 92–94% | 90–93% | 70–80% |
| Haze on 2 mm plaque | ASTM D1003-21 | <2% | <3% | 15–30% |
Moisture control is the primary variable determining property retention in REVODE213TR because polylactide undergoes hydrolytic chain scission at processing temperatures. A moisture content above 250 ppm causes measurable loss of intrinsic viscosity within 10 min at 200 °C; the result is an increase in melt flow index by 2–5 g/10 min, silver streaking on the part surface, and a reduction in notched Izod impact of 20–30%. Desiccant drying at 80 °C for 4 h with a drying-air dew point below -40 °C is the minimum acceptable condition. At ambient relative humidity above 60%, dried pellets should be conveyed with dry air and held in the machine hopper for no longer than 30 min; otherwise, a hopper-top desiccant dryer or nitrogen purge is required.
Barrel temperature profiles should be set from 180 °C at the feed throat to 210 °C at the metering zone, with nozzle temperature limited to 195–205 °C. Melt temperature measured by an insertion pyrometer should not exceed 215 °C because thermal degradation accelerates above this point and generates lactide monomer that acts as a plasticizer, reducing melt viscosity and final stiffness. Screws with a compression ratio of 2.5:1 to 3:1 and a length-to-diameter ratio of 20:1 to 24:1 provide adequate plastication without excessive shear heating. Back pressure should be set at 0.5–1.0 MPa to homogenize the melt; higher back pressure above 1.5 MPa increases residence time and temperature, promoting molecular weight loss.
In thin-wall parts below 1.0 mm nominal wall thickness, high injection speeds of 100–150 mm/s are necessary to prevent premature freeze-off. Holding pressure is typically 50–70% of the peak injection pressure for 2–4 s, after which gate freeze is complete. Because PLA has a narrow solidification range, the transparent processing window at mold temperatures above 60 °C is only ±5 °C; a mold temperature excursion to 70 °C or above produces measurable haze in thick sections. This is the critical threshold risk for REVODE213TR compared with more forgiving amorphous resins such as ABS or polycarbonate.
Downstream validation on a 120-ton hydraulic injection molding machine with a 24:1 general-purpose screw has shown that gate blush and splay are controlled by reducing decompression distance to 2–3 mm and by using a shut-off nozzle when cycle times exceed 15 s. In hot-runner molds, external heating zones should be set to 190–200 °C for the manifold and 200–210 °C for the nozzle; higher settings produce yellowing and acrid odor due to lactide evolution. Published data for hot-runner configurations with heated sprue bushings and valve-gate sequencers is limited; mold trials are required to establish maximum residence time before viscosity shift exceeds 5%.
In thin-wall containers with nominal wall thickness of 0.8 mm, the low melt viscosity of REVODE213TR permits filling of flow-length-to-wall-thickness ratios up to 150:1 when injection pressure reaches 80–100 MPa and the mold is held at 25 °C. The amorphous material exhibits a mold shrinkage of 0.3–0.5% in the flow direction and 0.3–0.5% in the transverse direction after 48 h at 23 °C and 50% RH. For applications requiring dimensional stability above 50 °C, the mold can be cycled at 80–100 °C to induce crystallinity, but this converts the product into a translucent state and increases cycle time by 20–40%. The grade is therefore specified for cold-fill packaging, cosmetic caps, transparent medical device housings, and disposable laboratory components, not for hot-fill or retort-class containers.
Compared with PET, REVODE213TR has lower density and lower drying temperature but lower tensile modulus and lower heat distortion; compared with amorphous polylactide copolymers containing D-lactide, REVODE213TR has higher tensile strength at the expense of lower elongation at break. The product is distinguishable from REVODE standard heat-resistant grades by maintaining high light transmittance after molding but lacking the 90–100 °C heat deflection temperature plateau. Vicat softening temperature under ISO 306:2022, method B50, is typically 55–60 °C, limiting continuous service temperature to 45 °C in amorphous moldings. Renewable carbon content tested under ASTM D6866-22 is typically 95–100%, differentiating the grade from fossil-derived transparent polymers such as PMMA, PET, and polycarbonate.
Thermal degradation of PLA proceeds through intramolecular transesterification and unzipping to lactide, with activation energy reported in the range of 110–130 kJ/mol. At 200 °C, the rate constant for molecular weight reduction is low enough for short residence times, but above 220 °C the melt becomes increasingly acidic because lactic acid and oligomeric carboxyl end groups catalyze further chain scission. This autocatalytic behavior means that a melt temperature excursion of only 10 °C can reduce number-average molecular weight by 15% within 8 min. For REVODE213TR, the recommended melt residence time at 210 °C is 5–8 min; at 230 °C, it falls to 2–3 min. These limits are derived from gel permeation chromatography measurements of unfilled PLA and should be verified for specific machine configurations.
Additives containing primary or secondary amines, such as some antistatic masterbatches, accelerate aminolysis and should be avoided unless compatibility is confirmed by capillary rheometry. Purge materials should be low-viscosity polyolefins or PLA-based purge compounds; residues of polyamide or acetal should be eliminated before startup because they create incompatible interfaces and splay. Short-term medical device housings may be sterilized by gamma irradiation up to 25 kGy; however, irradiation causes chain scission and yellowing. Ethylene oxide sterilization at 55 °C is generally compatible, but steam autoclave at 121 °C is outside the grade’s operating envelope unless the part is fully crystallized and annealed. Published data for this specific formulation under repeated sterilization is limited.
Food-contact and medical suitability are application-specific. The resin is generally supplied with REACH and RoHS declarations, but food-contact status under EU Regulation 10/2011 or FDA must be verified through the manufacturer’s current Food Contact Statement and migration test results under the intended temperature and time profile. For composting claims, EN 13432 biodegradation testing requires specific wall thickness and sample preparation; thin-wall molded parts of REVODE213TR can be assessed under ISO 14855-1:2012 for ultimate aerobic biodegradation. No conclusion is made here regarding biodegradability in marine environments because published data for this specific formulation is limited.
In cosmetic packaging with snap-fit closures, cycle times of 12–18 s are achieved when mold temperature is maintained at 20–25 °C and ejection is performed after part surface temperature drops below 45 °C. Ejector pins should have a draft angle of 1.5–2° because PLA has limited elastic recovery and high surface hardness. Parts removed above 50 °C exhibit post-mold warpage. The product is not recommended for parts with undercuts exceeding 0.5 mm in amorphous form unless a two-stage ejection system is used.