| HS Code | 525680 |
| Product Name | Polylactic Acid REVODE213T |
| Chemical Name | Polylactic Acid (PLA) |
| Brand | REVODE |
| Grade | 213T |
| Manufacturer | Zhejiang Hisun Biomaterials Co., Ltd. |
| Appearance | White to off-white pellets |
| Cas Number | 26100-51-6 |
| Density | 1.24-1.25 g/cm³ |
| Melt Flow Rate | 10-20 g/10 min at 190°C/2.16 kg |
| Melting Point | 155-175 °C |
| Glass Transition Temperature | 55-60 °C |
| Tensile Strength | 50-70 MPa |
| Elongation At Break | 2-10% |
| Flexural Modulus | 3000-4000 MPa |
| Heat Deflection Temperature | Up to 120 °C |
| Vicat Softening Temperature | Up to 130 °C |
| Biodegradability | Industrial compostable |
| Processing Method | Injection molding |
As an accredited Polylactic Acid REVODE213T factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Polylactic Acid REVODE213T is packaged in 25 kg moisture-resistant paper sacks, palletized, and shrink-wrapped for industrial shipping. |
| Container Loading (20′ FCL) | 20′ FCL standard dry container loading for Polylactic Acid REVODE213T: palletized, shrink-wrapped, labeled, and secured for safe ocean shipment. |
| Shipping | Polylactic Acid REVODE213T is a non-hazardous thermoplastic resin. Ship in sealed 25 kg bags or 1000 kg jumbo bags, palletized and stretch-wrapped. Store dry, below 50°C, avoiding moisture, direct sunlight, and ignition sources. No UN number, hazard class, or special transport labels required. |
| Storage | Store Polylactic Acid REVODE213T in a cool, dry, well-ventilated area away from direct sunlight, heat, and ignition sources. Keep original containers tightly sealed to prevent moisture uptake and contamination. Recommended conditions: 5–25°C and relative humidity below 50%. Separate from strong oxidizers. Avoid dust generation and static discharge. For extended storage, follow supplier drying recommendations before processing. |
| Shelf Life | Store cool, dry, and well-ventilated away from sunlight; shelf life is typically 12 months in unopened original packaging. |
Injection molding of spoons, forks, and knives from REVODE213T on a 1200 kN hydraulic press with a 2+2 cold-runner stack mold requires the virgin pellet fraction to be maintained at 95–100 wt%, while post-industrial regrind is limited to 15 wt% because repeated heat histories shift melt volume-flow rate above the grade-specific upper control limit under ISO 1133-1:2022 at 210 °C with a 2.16 kg load. Pre-drying at 80 °C for 4–6 h in a desiccant dryer with a dew point below -40 °C is required before the upstream hopper; at ambient relative humidity above 60%, hopper residence beyond 15 min reintroduces sufficient moisture to produce splay, silver streaking, and molecular weight hydrolysis at the melt-cast end-gate region. The production process uses a general-purpose screw with a compression ratio of 2.5:1 to 3.0:1, a barrel temperature profile from 170 °C at the feed throat to 200 °C at the nozzle, and mold temperatures between 25 °C and 40 °C to preserve transparency. For fork tines and knife serrations, the narrow flow channels require injection speeds above 80 mm/s to prevent premature freeze-off, while knife spine thickness above 3 mm demands a packing pressure hold of 6–10 s to minimize sink marks at the buttress transition. Food-contact compliance is evaluated under EU Regulation (EU) No 10/2011 with an overall migration limit of 10 mg/dm² and under the grade-specific U.S. FDA 21 CFR Part 177 clearance statement; 21 CFR 177.1520 does not automatically cover polylactic acid and must not be cited without supplier certification for REVODE213T. Industrial compostability is verified according to EN 13432:2000, which requires disintegration of 90% of material mass to fragments below 2 mm within 12 weeks and full biodegradation of 90% within 6 months under controlled composting. Finished product types include reusable-looking but industrially compostable spoons, forks, knives, and combined utensil kits for airline, catering, and institutional food-service operators.
Where dry-goods display packaging for tea leaves, snack mixes, small hardware, or cosmetic accessory sets requires a transparent PLA shell with a hinged lid and a compostability certificate, REVODE213T is processed in multi-cavity valve-gated cold-runner molds with polished A1 surface finishes to maintain gloss without secondary flame treatment. The formulation addition ratio for this application class is typically 98.5–100 wt% virgin REVODE213T, 0–1.0 wt% color masterbatch, and 0.5–1.5 wt% of an anti-block/slip masterbatch based on erucamide or a biodegradable aliphatic wax to reduce in-mold friction and improve demolding of thin hinge sections. The downstream production route uses injection molding rather than sheet extrusion because the integrated hinge requires local molecular orientation and a thickness reduction to 0.25–0.40 mm; the hinge zone is gated independently from the base to create a flow front that orients polymer chains across the hinge line. Mold temperature is held at 20–30 °C to avoid hinge whitening, and cooling time is typically 8–12 s for a total wall thickness of 1.2–1.6 mm. Compliance for this dry-food packaging is assessed under the same food-contact migration protocols of EU Regulation (EU) No 10/2011, and compostability claims are validated under EN 13432:2000 or ASTM D6400-23 depending on the destination market. Terminal finished product types include hinged transparent boxes, clamshell trays for dry snacks, and clear display containers with snap-fit closures for non-refrigerated retail shelves.
| Standard / Regulation | Scope | Numerical threshold or test condition |
|---|---|---|
| EU Regulation (EU) No 10/2011 | Plastic food-contact materials | Overall migration 10 mg/dm²; simulant selection per Annex III |
| U.S. FDA 21 CFR Part 177 | Indirect food additives | Grade-specific FCN or TOR clearance for REVODE213T; no blanket olefin clause |
| EN 13432:2000 | Industrial compostability of packaging | Disintegration 90% to <2 mm in 12 weeks; biodegradation 90% in 6 months |
| ASTM D6400-23 | Compostable plastics in municipal/industrial facilities | Disintegration 90%; ultimate biodegradation 90% of organic carbon |
| ISO 14855-1:2012 | Aerobic biodegradation under controlled composting | CO₂ evolution relative to cellulose reference; test duration 45–180 days |
| REACH (EC) No 1907/2006 | Registration, evaluation, authorization of chemicals | SVHC content below 0.1 wt%; Annex XVII restrictions apply |
For cold-chain beverage lids and portion cups with wall thickness below 0.6 mm, high-speed all-electric injection units with clamp forces from 1500 kN to 2500 kN are employed because hydraulic response alone cannot maintain the required 200–400 mm/s injection speed without excessive pressure drop at the gate. The addition ratio for this thin-wall configuration is 98–99 wt% REVODE213T with 1–2 wt% of a high-purity slip masterbatch; nucleating agents at 0.2–0.5 wt% may be added to shorten cooling time, but they introduce haze in the lid dome and are generally avoided for transparent cold-drink lids. The production process uses a heated sprue bushing or valve-gated hot runner with a drop-to-drop balance of ±0.5% fill weight across 8–16 cavities to prevent differential shrinkage and warpage that would break the lid undercut seal. Mold temperature is maintained at 10–20 °C through turbulent-flow water circuits with Reynolds numbers above 5000; lower mold temperatures reduce crystallization and maintain ductile puncture resistance under ISO 6603-2:2016. The operational boundary is cold-chain use above 4 °C for lids subject to impact loading; below -10 °C, the amorphous PLA matrix exhibits brittle fracture at perforation lines and stacking lugs unless impact-modified, but impact-modified grades sacrifice transparency. Compliance for this food-contact application is established under EU Regulation (EU) No 10/2011 and the grade-specific U.S. FDA 21 CFR Part 177 clearance, while the terminal format is typically a clear lid with a peripheral snap ring for paper or PLA cold-drink cups, a condensation-resistant dessert cup, or a portion cup for cold sauces and dressings.
During pilot production of a 50 ml cosmetic jar with a 5 mm base wall on a 1200 kN hybrid machine, the main process conflict is sink-mark formation at the thick bottom-to-sidewall transition, which cannot be resolved by increasing injection speed alone. The formulation addition ratio for thick-walled cosmetic primary packaging is 96–99 wt% REVODE213T, 1–4 wt% pearlescent or solid color masterbatch, and 0.2–0.5 wt% of a biodegradable mold-release additive; the color masterbatch often contains mica or titanium dioxide, which slightly increases thermal conductivity and alters the packing-pressure freeze-off point under ISO 11357-5 differential scanning calorimetry. The production process uses a cold runner with a sprue diameter of 4–6 mm and a retractable sprue puller because the thick sprue remains molten longer than the cavity and can cause gate drool. Holding pressure is staged from 60 bar to 80 bar for 8–12 s, and cooling time is extended to 20–35 s until the core temperature drops below the heat deflection temperature under ISO 75-2:2013. The compliance framework for cosmetic packaging is not food-contact but is governed by REACH (EC) No 1907/2006 for substance restrictions and Regulation (EC) No 1223/2009 for cosmetic product safety when the jar is used as primary packaging for creams, balms, or powders. Terminal finished product types include thick-walled cream jars, sifter inserts, and threaded closures with a gasket seat for anhydrous cosmetic formulations; contact with high-water-content emulsions above 60% relative humidity should be evaluated for PLA hydrolysis over shelf life.
Compounding on a co-rotating twin-screw extruder with a 44:1 L/D ratio and side-feeding permits dispersion of 5–15 wt% of an aliphatic polyester or reactive impact modifier into REVODE213T for reusable household articles that require higher notched impact strength than unmodified PLA can provide. The addition ratio is 84.5–94.5 wt% REVODE213T, 5–15 wt% impact modifier, 0.5–2.0 wt% compatibilizer or chain extender, and 0–1.0 wt% color masterbatch; the chain extender is required when the modifier contains residual moisture or carboxyl groups that accelerate PLA chain cleavage during residence time above 120 s. The production process uses a barrel profile from 160 °C to 200 °C with a vacuum vent at -0.08 MPa to -0.09 MPa to strip volatiles, followed by strand pelletizing and a second desiccant drying step at 75 °C for 4 h before injection molding. The major process conflict is viscosity mismatch between the PLA matrix and the modifier: when modifier melt flow rate differs by more than 10 g/10 min under ISO 1133-1:2022 from the matrix, the dispersed phase forms large droplets above 2 µm that reduce impact efficiency and create gate blush on visible surfaces. Screw elements with multiple kneading blocks and reverse elements upstream of the side feeder are used to generate shear heating above 10 kW specific mechanical energy, but the melt temperature must not exceed 210 °C because PLA degrades rapidly at higher temperatures. Notched Charpy impact strength under ISO 179-1:2010 typically increases from the unmodified range of 2–3 kJ/m² to 5–8 kJ/m² with 10–15 wt% modifier loading, but the exact shift for REVODE213T must be verified because published data for this specific configuration is limited. The compliance framework is REACH (EC) No 1907/2006 for the European market, with attention to Annex XVII restrictions for articles intended for prolonged skin contact; no food-contact claim is made for impact-modified household articles unless the modifier and compatibilizer are confirmed as food-contact listed. Terminal finished product types include toothbrush handles, hair combs, storage baskets, garment hangers, and cable-management clips where residual impact loading occurs at room temperature.
| Configuration | Melt temperature (°C) | Mold temperature (°C) | Moisture limit (ppm) | Regrind limit (wt%) |
|---|---|---|---|---|
| Disposable cutlery | 190–210 | 25–40 | <250 | ≤15 |
| Thin-wall cold lids | 195–215 | 10–20 | <200 | ≤10 |
| Impact-modified household articles | 160–200 | 30–60 | <250 | ≤20 |
Mechanical recycling of sprue, runner, and short-shot scrap at 20–35 wt% regrind has been evaluated on a 90-ton all-electric machine for non-food display clips, shelf-edge strips, and point-of-sale mounting hooks made from REVODE213T. The addition ratio for this scrap-containing configuration is 65–80 wt% virgin REVODE213T, 20–35 wt% dry regrind ground to a particle size below 6 mm, and 0–1.0 wt% color masterbatch; the regrind fraction is metered through a gravimetric blender with a batch tolerance of ±0.2 wt% because irregular flake density creates volumetric feeder drift. The production process uses a single-stage screw with a mixing tip and a back pressure of 10–15 bar to homogenize the viscosity difference between virgin and reprocessed material; injection speed is reduced by 15–25% relative to the all-virgin setting to prevent jetting at the tab gate. Compliance for non-food display applications is evaluated under REACH (EC) No 1907/2006 for restricted substances and under EN 13432:2000 only when the final article is intended for industrial composting; if the article enters municipal mixed waste, compostability claims are not made. Terminal finished product types include shelf-edge data strips, display hooks, packaging clips, and temporary point-of-sale supports where transparency and rigidity are required but food-contact certification is not part of the application specification.
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Polylactic Acid REVODE213T is an injection-molding grade of poly(L-lactic acid) supplied in pellet form for thin-wall packaging, rigid disposable articles, and non-implantable medical housings. The resin is a semicrystalline aliphatic polyester produced by catalytic ring-opening polymerization of lactide; its melt viscosity at 210 °C and 2.16 kg is controlled to fill thin sections without excessive injection pressure. Table 1 presents the principal physical and mechanical properties reported in the manufacturer’s technical bulletin and expressed according to ISO and ASTM methods. The values are typical ranges; lot-specific certificates of analysis may vary with molecular weight distribution, residual lactide content, and additive package.
| Property | Test method | Nominal range or typical value |
|---|---|---|
| Melting temperature by DSC | ISO 11357-3 | 150–160 °C |
| Glass transition temperature | ISO 11357-2 | 55–60 °C |
| Melt flow index at 210 °C, 2.16 kg | ISO 1133-1:2022 | 10–20 g/10 min |
| Density | ISO 1183-1:2019 | 1.24–1.26 g/cm³ |
| Tensile strength at yield | ASTM D638-14 | 60–65 MPa |
| Elongation at break | ASTM D638-14 | 2–5 % |
| Tensile modulus | ASTM D638-14 | 3000–3600 MPa |
| Flexural modulus | ISO 178:2019 | 2800–3300 MPa |
| Notched Izod impact at 23 °C | ISO 180:2019 | 2.0–4.0 kJ/m² |
| Heat deflection temperature at 0.45 MPa | ISO 75-2:2013 method B | 50–55 °C |
| Moisture content as packed | ISO 15512 | < 0.025 wt% (250 ppm) |
The melt-flow range distinguishes REVODE213T from high-molecular-weight film and fiber grades, which generally display lower flowability and require higher melt pressure in thin sections. For downstream injection molders, the practical consequence is that REVODE213T can be processed on standard reciprocating-screw machines without specialized plastication units, provided the thermal and moisture limits are not exceeded.
Compared with extrusion film PLA grades, which typically exhibit a melt flow index below 5 g/10 min at 210 °C under 2.16 kg, REVODE213T has a lower melt viscosity and a wider mold-filling window. On a 120-tonne hydraulic injection molding machine with a 22:1 L/D screw, the lower viscosity reduces peak injection pressure relative to a general-purpose extrusion PLA grade during thin-wall filling; published data for this exact comparison is limited, so machine-specific pressure-loss studies under ISO 11443 are recommended. High-heat PLA compounds containing nucleating agents or stereo-complex fractions can achieve heat deflection temperatures above 100 °C after isothermal crystallization, whereas REVODE213T in an as-molded, fast-cooled state remains near 50–55 °C under 0.45 MPa. The trade-off is processing stability: REVODE213T does not require the same narrow mold-temperature control as fast-crystallizing high-heat PLA grades, but it also cannot be specified for hot-fill or high-temperature service without annealing.
Against polypropylene homopolymer, REVODE213T has higher density, 1.24–1.26 g/cm³ versus approximately 0.90 g/cm³, and higher flexural modulus, 2800–3300 MPa versus approximately 1300–1700 MPa, but lower notched Izod impact and greater susceptibility to hydrolytic degradation in aqueous service above 50 °C. This stiffness permits down-gauging in rigid packaging, but impact-limited designs require radiused corners and mold-filling analysis to avoid brittle failure at knit lines. Differences from other PLA grades are also reflected in residual lactide content and optical haze. Published data specific to REVODE213T is limited for optical performance; haze should be measured under ISO 14782 and total luminous transmittance under ASTM D1003 before specification in optically critical articles.
Before any melt processing, REVODE213T must be dried in a desiccant dryer with a dew point of -40 °C or lower to a moisture content below 250 ppm (0.025 wt%). Typical drying conditions are 80 °C for 4 h; hopper residence time should not exceed 6 h at that temperature, because prolonged exposure to heated air can increase lactide generation and yellowing. At ambient relative humidity above 60 %, pellets transferred from an open container re-adsorb moisture within 30–60 min; closed-loop conveying with dry-air purge is therefore required for continuous production. In injection molding, melt temperature is normally set between 180 °C and 210 °C, with the nozzle zone maintained at the lower end to reduce drool. Exceeding 230 °C causes rapid random chain scission, generating lactide, acetaldehyde, and carbonaceous degradation products.
Mold temperature is a critical boundary condition. For REVODE213T, a mold surface temperature of 25–40 °C is typical. At mold temperatures below 20 °C, the melt freezes before complete crystallization, producing low weld-line strength and anisotropic shrinkage. Above 45 °C, cycle time lengthens without a proportional increase in crystallinity unless an annealing step follows. Holding pressure is typically 50–70 % of injection pressure; packing time must be sufficient to gate seal because PLA has relatively high volumetric shrinkage during solidification. Injection velocity profiles should deliver a short filling phase, usually 0.5–1.5 s for thin-wall parts, to avoid premature skin freeze. Parts ejected at 45–55 °C may continue to shrink after molding and should be dimensionally stabilized on a cooling fixture.
Rheologically, PLA melt is shear-thinning. At 190 °C, apparent viscosity values for general-purpose injection PLA typically range from 200 to 350 Pa·s at 100 s⁻¹ and from 60 to 120 Pa·s at 1000 s⁻¹. Published capillary rheometry data for REVODE213T itself is limited; injection molders should generate lot-specific viscosity curves under ISO 11443. Because the activation energy for PLA flow is approximately 70–90 kJ/mol, a 10 °C increase near 200 °C can lower melt viscosity by more than 30 %, making nozzle temperature control a sensitive process variable.
Under conditions of extended residence time or high moisture, PLA undergoes hydrolytic and thermal degradation simultaneously. Melt viscosity decreases disproportionately to temperature; a drop of more than 10 % in melt pressure at constant screw speed during a production run is often an early indicator of molecular weight reduction rather than temperature drift alone. On a 100-tonne all-electric injection molding machine, a residence time above 360 s at 210 °C has been associated in failure analyses with visible silver streaks, a reduction in notched Izod impact to below 2 kJ/m², and elevated acetaldehyde concentration in the molded part. This is especially relevant for food-contact packaging because acetaldehyde can affect sensory performance. If the screw buffer position is set too high or shot size is less than 25 % of barrel capacity, prolonged residence occurs and degradation products accumulate in the compression zone. Cleansing with a purging compound or lowering the barrel to a hold temperature below 160 °C at shutdown reduces discoloration.
Moisture levels above 250 ppm produce hydrolytic scission even within the normal melt-temperature window. At 210 °C, an increase in moisture content from 100 ppm to 500 ppm can reduce melt viscosity by 20–40 %; for REVODE213T specifically, lot-specific capillary rheometry under ISO 11443 is required to establish the exact slope. The operational boundary is therefore defined by dryer performance rather than by set-point alone. Desiccant rotor dryers with a dew point of -50 °C are preferred in high-humidity plants. A moisture analyzer using ISO 15512 should be placed at the feed throat to confirm pellet dryness before startup.
Dry storage in sealed foil-lined bags at 10–30 °C is recommended. Once a bag is opened, remaining pellets should be re-sealed with desiccant or consumed within 8 h in a plant with relative humidity below 50 %. At relative humidity above 60 %, open exposure should not exceed 30 min. Regrind use should be limited to 20 wt% to retain impact strength and dimensional stability; multiple heat histories accelerate hydrolysis and raise acetaldehyde. A closed-loop regrind system with a granulator screen size of 6–8 mm and dry-air conveying minimizes fines and moisture ingress on high-volume packaging lines.
Food-contact and regulatory compliance for REVODE213T depends on the final article and the downstream additives used. The base resin may be assessed under EU Regulation (EU) No 10/2011 for plastic food-contact materials; specific migration limits for lactic acid and overall migration under the intended food-contact conditions should be verified on the finished article. In the United States, PLA may be covered through applicable Food Contact Notifications; published data for REVODE213T-specific FCN citations is limited and must be confirmed with the supplier. Regulatory conformity under REACH, RoHS Directive 2011/65/EU as amended by Delegated Directive (EU) 2015/863, and industrial composting standards is summarized in Table 2.
| Regulatory or standards domain | Relevant designation | Typical status for REVODE213T base resin |
|---|---|---|
| EU food contact | Regulation (EU) No 10/2011 | Requires finished-article migration testing; overall migration limit of 10 mg/dm² applies under intended conditions. |
| U.S. food contact | FDA 21 CFR and applicable FCN | Supplier confirmation required for specific Food Contact Notification listing. |
| REACH | Regulation (EC) No 1907/2006 | No SVHC intentionally introduced; downstream importer registration and communication obligations apply. |
| RoHS | Directive 2011/65/EU as amended by (EU) 2015/863 | Applies to electrical and electronic equipment only; restricted substance limits are 0.1 wt% for lead, mercury, hexavalent chromium, PBB, and PBDE; cadmium limit is 0.01 wt%. |
| Industrial composting | EN 13432 / ASTM D6400 | Full article certification required; resin alone cannot be certified. |
Application envelopes are defined by mechanical and thermal limits. REVODE213T is used in disposable cutlery, thin-wall containers, cosmetic jars, caps and closures, and non-implantable diagnostic housings. Structural parts exposed to continuous load above 50 °C or to aqueous environments above 45 °C require stress-rupture testing under ISO 22088 or tensile testing under ISO 527-2 and are generally outside the unfilled PLA design window unless the part is annealed and high molecular weight is retained. Alcohol-based sanitizers, esters, ketones, and high-pH cleaning agents can induce environmental stress cracking; compatibility should be tested under ISO 22088-3. The resin is not suitable for steam sterilization at 121 °C or for repeated hot-water washing above 60 °C; it softens near the glass transition and loses dimensional stability.