| HS Code | 254239 |
| Density | 1.25 g/cm3 |
| Melt Flow Rate | 10-20 g/10 min (190°C/2.16 kg) |
| Melting Point | 170-180 °C |
| Glass Transition Temperature | 55-60 °C |
| Crystallization Temperature | 100-120 °C |
| Tensile Strength | 50-60 MPa |
| Elongation At Break | 3-5% |
| Flexural Strength | 80-100 MPa |
| Flexural Modulus | 3500-4000 MPa |
| Notched Izod Impact Strength | 2.5-3 kJ/m2 |
| Heat Deflection Temperature | 120 °C |
| Vicat Softening Point | 140 °C |
| Biobased Content | 100% |
| Biodegradability | Compostable |
| Form | Pellets |
| Color | White to off-white |
| Processing Method | Injection molding |
As an accredited Polylactic Acid REVODE713 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Polylactic Acid REVODE713 is supplied in sealed 25 kg moisture-barrier bags, palletized and stretch-wrapped for industrial storage and transport. |
| Container Loading (20′ FCL) | Container Loading (20′ FCL): Polylactic Acid REVODE713 bagged or palletized chemical cargo, evenly distributed, securely braced for ocean freight. |
| Shipping | Polylactic Acid REVODE713 is a non-hazardous, biodegradable thermoplastic resin. Ship in dry, sealed bags, drums, or containers at ambient temperature. Protect from moisture, heat, direct sunlight, punctures, and contamination. Keep packages closed and palletized securely during transit. No UN hazard class or special transport label is required; follow local regulations. |
| Storage | Store Polylactic Acid REVODE713 in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, and ignition sources. Keep original containers tightly closed to prevent moisture absorption. Recommended conditions: below 30°C and low humidity. Separate from strong acids, bases, and oxidizing agents. Avoid prolonged storage in hot, humid environments. Follow manufacturer instructions and local regulations. Use first-in, first-out stock rotation. |
| Shelf Life | Store in a cool, dry, ventilated area in original sealed packaging; typical shelf life is 12 months from manufacture. |
In thin-wall cutlery injection moulding, REVODE713 is treated as a high-melt-flow PLA resin whose process stability depends more on residual moisture than on barrel temperature. The pellets are predried in a desiccant hopper at a dew point not above −40 °C, at 80 °C for 4 h to 6 h, until the residue measured by ISO 15512:2019 is below 0.025% (250 ppm). Barrel temperature is profiled from 165 °C at the throat to 195 °C at the metering zone, with the nozzle kept below 205 °C to limit lactide outgassing and screw drool. Mould cooling temperature is held between 15 °C and 35 °C for amorphous, transparent cutlery; elevated mould temperatures above 90 °C are used only where crystallized spoons require dimensional stability at higher ambient temperatures. Injection speed is set to fill the cavity in 0.8 s to 1.5 s, hold pressure is maintained at 50 MPa to 70 MPa for gate seal, and back pressure of 5 MPa to 8 MPa with screw speed of 70 min⁻¹ to 120 min⁻¹ prevents melt-temperature overshoot. Gate thickness is not less than 0.6 mm and land length is not above 1.2 mm, because PLA freezes rapidly and thin gates cause short shots, jetting, and weld-line splitting. Under ISO 527-2, the oriented mouldings typically show tensile modulus between 3300 MPa and 3600 MPa and elongation at break below 4%; under ISO 179-1/1eA, notched Charpy values in unlaminated cutlery are usually 2.5 kJ/m² to 4 kJ/m². End products are disposable forks, spoons, stirrers, and sampling spatulas that meet EN 13432:2000 or ASTM D6400-19 when the entire packaging article is certified, not only the resin pellet. Continuous service temperature is governed by ISO 75-2/B at 0.45 MPa, which remains near 55 °C in amorphous parts; the cutlery is therefore not positioned for hot soup, microwave reheating, or extended contact with boiling water. Published data for this specific grade in thin-wall cutlery configuration is limited; the parameter ranges cited are derived from ISO methods and general PLA injection-moulding practice.
The restriction is determined by the low amorphous heat deflection point, not by melt strength alone. Sheet extrusion of REVODE713 is run at melt temperatures between 180 °C and 205 °C, with a polished roll stack at 40 °C to 50 °C; sheet thickness is controlled from 0.3 mm to 0.8 mm and residual moisture is kept below 0.02%. Thermoforming uses a plug-assisted process with an areal draw ratio of 2:1 to 3:1, sheet surface temperature of 85 °C to 110 °C before the mould closes, and aluminium or steel tooling held at 95 °C to 110 °C to induce 25% to 35% crystallinity in the finished wall. The additional crystallization raises the Vicat softening point measured under ISO 306/B50 from approximately 55 °C in amorphous sheet to a practical ceiling near 95 °C, but the thermoformed cup still fails hot-fill above 50 °C because wall stock thins at corner radii during plug inversion. Process operators compensate with plug speed 250 mm/s to 400 mm/s and plug temperature near 100 °C; however, the crystallization window narrows between 95 °C and 120 °C per ISO 11357-3, making cycle time the control variable rather than oven setpoint. End formats include 150 ml to 500 ml dessert cups and dairy portion packs. Compliance follows Commission Regulation (EU) No 10/2011, including Annex II overall migration limit not exceeding 10 mg/dm² for food-contact verification, and EN 13432:2000 where compostability is claimed; the cups are intended for chilled or ambient dry use, not for retort, microwave, or hot-fill above 50 °C.
Before REVODE713 pellets are converted into fused filament fabrication feedstock, the material is predried at 60 °C for 4 h to 6 h to a maximum moisture content of 250 ppm. The extrusion line uses a single-screw extruder with 28:1 L/D and a three-zone screw with shallow metering depth, operated at a melt temperature of 185 °C to 205 °C and a melt pump pressure of 8 MPa to 12 MPa before the die. Filament is quenched in a water bath maintained at 45 °C to 55 °C; bath temperature below 40 °C creates an amorphous skin with internal voids, while bath temperature above 60 °C increases crystallization and makes the filament too brittle for spooling. A dual-axis laser gauge controls diameter to 1.75 mm ± 0.05 mm, with ovality not exceeding 0.02 mm; feedback adjusts puller speed between 20 m/min and 50 m/min. The printed parts are built at a nozzle setpoint of 200 °C to 220 °C and a bed temperature of 20 °C to 50 °C; print speed is kept between 40 mm/s and 80 mm/s to avoid under-extrusion from melt viscosity shifts. ISO 527-2 values for printed PLA tensile bars typically fall between 45 MPa and 55 MPa in the XY direction, which is lower than injection-moulded reference values because interlayer fusion limits load transfer. End uses are prototype jigs, assembly aids, and dry-goods display fixtures; parts are not suitable for continuous exposure above 50 °C or to water spray above 40 °C.
Paperboard coating with REVODE713 requires a wider die gap and a shorter air gap than LDPE because PLA's extensional viscosity is lower and film neck-in is severe at melt temperatures above 230 °C. The resin is predried to below 0.015% moisture and fed to a 90 mm screw with 30:1 L/D; melt temperature at the die is controlled between 200 °C and 225 °C. The flat die gap is set at 0.4 mm to 0.7 mm, and the air gap from die lips to nip is held at 180 mm to 250 mm to minimize neck-in before the melt curtain contacts the paperboard. Corona treatment at 2 kW to 4 kW is applied to the board surface immediately before the nip; coating weight is maintained at 15 g/m² to 30 g/m² and controlled by line speed of 80 m/min to 200 m/min with a cooled polishing roll at 25 °C to 40 °C. Adhesion is tested by ISO 2409 cross-cut tape pull; values below grade 1 are typical on corona-treated kraft, while untreated board shows delamination. End structures include cold-drink paper cups, sandwich boxes, and dry-catering trays. Regulatory compliance for food-contact paperboard is assessed under Commission Regulation (EU) No 10/2011 and, where applicable, FDA 21 CFR 176.170 for paper and paperboard components; PLA itself requires verification against the supplier's FCN because 21 CFR 177.1520 does not apply to PLA. The coating is not a high-barrier layer; oxygen transmission under ISO 15105-2 and water-vapour transmission under ISO 15106-3 are higher than PE and PET, so this track is for short-life food service, not long shelf-life packaging.
GPPS substitution is viable only when the tool is modified to accept PLA's lower thermal conductivity and wider viscosity dependence on shear. The mould shrinkage under ISO 294-4 is typically 0.3% to 0.8% parallel to flow and 0.2% to 0.5% transverse, compared with GPPS at 0.3% to 0.6%; tools dimensioned for GPPS may still pass dimensional checks if the shrinkage correction is adjusted, but side-wall rib thickness below 0.4 mm creates short shots. Melt temperature is kept between 175 °C and 195 °C, mould temperature at 15 °C to 30 °C, injection velocity to fill in 0.5 s to 1.0 s, and hold pressure from 45 MPa to 65 MPa. A 180-tonne clamp press running a single-cavity electronic accessory blister with projected area of 350 cm² requires a clamping force reserve because PLA's viscosity curve under ISO 11443 falls sharply above 210 °C; any overshoot causes flash and screw drool. The end product is a clear, brittle blister for dry goods, electronics installation parts, or stationery. Drop impact is limited: notched Charpy under ISO 179-1/1eA remains near 2 kJ/m² to 4 kJ/m², so the blister must not be used for heavy tools or sharp metal components without radiused corners. Compliance includes REACH polymer exemption confirmation, RoHS heavy-metal screening, and EN 13432:2000 if the blister is claimed compostable.
For refrigerated dessert packaging lines, cold-chain moulded tubs produced from REVODE713 are engineered for close dimensional control in lid rims rather than impact toughness, because PLA exhibits brittle fracture below 10 °C unless impact-modified. The melt is processed at 180 °C to 200 °C with mould temperature at 15 °C to 35 °C; thin side walls of 0.6 mm to 1.0 mm require fast injection with valve-gated hot runners and gate diameter not below 0.8 mm. Under ISO 527-2, tensile modulus is 3200 MPa to 3600 MPa and stress at break is 55 MPa to 65 MPa; under ISO 178, flexural modulus is approximately 3000 MPa to 3500 MPa. The lid rim seats are held to a circularity tolerance of 0.2 mm using an eight-cavity cold-runner tool, because post-mould moisture uptake above 0.3% causes dimensional swelling. Secondary operations include ultrasonic welding of tamper-evident bands on lids, which requires horn amplitude of 30 µm to 50 µm and weld pressure of 0.2 MPa to 0.4 MPa; PLA welds best with short 0.1 s to 0.3 s pulses to avoid melt squeeze-out. The finished tubs are used for chilled dairy, frozen desserts at −20 °C only when impact modifiers are added, and cold packed dry goods. Compliance is under Commission Regulation (EU) No 10/2011; compostability claims require EN 13432:2000. These tubs are not for microwave or oven use.
| Downstream track | Primary food-contact or compostability standard | Critical moisture or conditioning limit | Mechanical or dimensional test method |
|---|---|---|---|
| Thin-wall cutlery | EN 13432:2000; EU 10/2011 | 0.025% residual moisture | ISO 527-2; ISO 179-1/1eA |
| Thermoformed portion cups | EU 10/2011; EN 13432:2000 | 0.02% sheet moisture | ISO 306/B50; ISO 11357-3 |
| FFF filament | ISO 527-2 for printed bars | 250 ppm before extrusion | ISO 527-2 |
| Extrusion coating | FDA 21 CFR 176.170; EU 10/2011 | 0.015% residual moisture | ISO 2409; ISO 15106-3 |
| Dry-goods blister | EN 13432:2000; REACH; RoHS | 0.025% before moulding | ISO 294-4; ISO 179-1/1eA |
| Cold-chain tubs | EU 10/2011 | 0.3% post-mould moisture uptake | ISO 527-2; ISO 178 |
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Polylactic Acid REVODE713 is a poly(L-lactide)-based injection moulding resin supplied within the REVODE 700 series. Because the grade-specific technical datasheet is lot-controlled, the values stated here are the representative specification envelope for REVODE713-class PLA and must be checked against the manufacturer’s certificate of analysis. The resin is distinguished from generic extrusion PLA by a controlled melt mass-flow rate and an additive/nucleator package intended for thin-wall cavity filling. The solid density is generally 1.24–1.26 g/cm³ under ISO 1183-1, and pellet bulk density is approximately 0.70–0.85 g/cm³. The polymer is not a polyolefin; it is a melt-processable polyester that hydrolyzes under heat and moisture, so all handling, drying, and processing limits are ordered around that single failure mode.
The primary specification inputs are melt volume-flow rate under ISO 1133-1, moisture content by ISO 15512 or coulometric Karl Fischer titration, tensile properties by ISO 527-2, flexural properties by ISO 178, notched Charpy impact by ISO 179-1/1eA, and heat deflection temperature by ISO 75-2 method B. For an injection-moulding grade of this class, the melt mass-flow rate is typically specified between 5 g/10 min and 15 g/10 min at 210 °C under 2.16 kg. Tensile yield stress is commonly 58–65 MPa and tensile modulus 3200–3500 MPa; notched Charpy impact is low at 2.0–3.5 kJ/m². These are not lot-release values and do not replace first-article trials.
Moisture is the most important inbound quality variable. PLA pellets at ambient relative humidity above 60% can absorb more than 3000 ppm moisture within 24 h. The correct drying condition for REVODE713-class material is 80 °C in a desiccant dryer with dew point ≤ -40 °C for 4–6 h, resulting in moisture ≤ 250 ppm. Drying above 90 °C can agglomerate pellets and should be avoided.
The melt rheology is shear-thinning and fast-freezing. On injection moulding machines with screw diameters of 30–35 mm, the barrel profile is set from feed to nozzle at 160–170 °C, 180–200 °C, 200–210 °C, and 200–210 °C. Back pressure is limited to 5–15 bar because additional shear work lowers molar mass. Injection speed is held at 40–120 mm/s for wall thicknesses below 2.0 mm. A shot-size-to-barrel-capacity ratio of 1.5:1–2.5:1 is specified to keep material residence time below 15 min; longer residence times produce lactide, yellowing, and a drifting cushion position.
On production-scale equipment, lot-to-lot melt mass-flow rate shifts of ±1 g/10 min within the specification envelope are observable. Such variation changes fill time and packing response; process adjustments should therefore be made against the recorded MFR and moisture certificate rather than against the local machine. If fill imbalance occurs, runner balancing and gate land length changes are usually more effective than raising barrel temperature because PLA thermal degradation is not recoverable.
For multi-cavity tools, clamp force requirements are generally 0.5–0.8 t/cm² of projected area. Because PLA has a sharp solidification window, hot-runner systems should use externally heated manifolds with temperature stability of ±1 °C; cold sprue bushings are preferred for short runs because they avoid additional residence time. Gate diameter for polyolefin molds is often reduced; for PLA, gates should be slightly larger, typically 0.8–1.2 mm for a wall of 1.0 mm, to avoid excessive shear heating.
| Parameter | Set point | Equipment or measurement reference |
|---|---|---|
| Desiccant dryer temperature | 80 °C | dew point ≤ -40 °C |
| Drying residence | 4–6 h | moisture ≤ 250 ppm by Karl Fischer |
| Barrel melt profile | 180–210 °C | nozzle thermocouple, reduced at high screw speed |
| Mold surface temperature | 15–40 °C amorphous; 90–110 °C crystallized | pressurized water or oil thermoregulator |
| Back pressure | 5–15 bar | hydraulic injection unit |
| Injection speed | 40–120 mm/s | screw diameter 30–35 mm |
| Maximum residence time | <15 min | barrel capacity 1.5–2.5 shot volumes |
The most important commercial difference is processing orientation. Extrusion-grade PLA is usually polymerized or compounded for high melt strength, low die swell, and slower crystallisation; REVODE713-class injection PLA is formulated for lower viscosity under shear and faster nucleation in a cold mold. Compared with ABS, this PLA has higher tensile modulus and is not fossil-based, but it has significantly lower impact strength and heat deflection temperature.
| Property | Test method | REVODE713-class injection PLA | Unmodified extrusion PLA | General-purpose ABS |
|---|---|---|---|---|
| Melt mass-flow rate | ISO 1133-1 | 5–15 g/10 min at 210 °C, 2.16 kg | 2–10 g/10 min at 210 °C, 2.16 kg | 5–25 g/10 min at 220 °C, 10 kg |
| Density | ISO 1183-1 | 1.24–1.26 g/cm³ | 1.24–1.26 g/cm³ | 1.03–1.07 g/cm³ |
| Tensile yield stress | ISO 527-2 | 58–65 MPa | 55–65 MPa | 35–45 MPa |
| Tensile modulus | ISO 527-2 | 3200–3500 MPa | 3000–3500 MPa | 2000–2600 MPa |
| Notched Charpy impact | ISO 179-1/1eA | 2.0–3.5 kJ/m² | 2.0–4.0 kJ/m² | 10–25 kJ/m² |
| Heat deflection temperature, method B | ISO 75-2 | 50–55 °C | 50–55 °C | 85–100 °C |
Thin-wall food-service and packaging applications are the usual conversion routes. REVODE713 can be injected into cutlery, caps, cosmetic closures, and single-serve containers where wall thickness is below 1.2 mm. The high stiffness assists demolding; the low elongation at break requires adequate draft angles and rounded corners. Food-contact status is not inherent to the resin, and each finished article must be tested under EU Regulation (EU) No 10/2011 for migration and, where applicable, under national food-contact provisions. Industrial compostability claims require item-specific certification under EN 13432 or ASTM D6400; pigments, print, and additives must be within the certified formulation.
Unmodified REVODE713-class PLA is not suited to hot-fill, dishwasher, or enclosed electronic housing applications unless crystallinity is deliberately developed in the tool or through post-mold annealing. In such cases, the tooling and cycle time must be re-evaluated because crystallization changes shrinkage, heat deflection, and ejection behaviour.
Regrind is used in injection moulding, but PLA differs from polypropylene or ABS. Each pellet-drying and melt-residence step cleaves ester bonds; the melt mass-flow rate increases, impact decreases, and gas streaks become more frequent. Conservative processes hold post-industrial regrind below 20–30 wt% in the feed. Regrind should be dried separately at 80 °C for 4–6 h and screened to ≤5 mm particles to avoid bridging. A relative MFR increase above 15% after 10 h of continuous operation indicates molar mass loss, and the response should be a barrel temperature reduction of 5–10 °C rather than a back pressure increase.
Masterbatch carriers must be PLA-compatible and dried to the same 250 ppm moisture limit. Amine-based slip additives and alkaline processing aids can attack the polyester backbone; they should not be used unless pre-validated by melt stability trials. If mold release is required, use only release chemistry selected for PLA and confirm by measuring molecular weight retention rather than visual appearance. Purging after shutdown is normally performed with polyolefin; residual PVC or acetal in the barrel must be avoided because they degrade into acidic species that accelerate PLA hydrolysis.
The glass transition temperature of PLA is 55–60 °C under ISO 11357-2, and the heat deflection temperature under ISO 75-2 method B is 50–55 °C for amorphous specimens. This is the binding service limit for unmodified REVODE713-class parts. Hot-fill, dishwasher, and enclosed electronics applications are excluded unless the article is crystallized. Crystallized PLA can reach 80–110 °C under the same test method, but only when the mold temperature is kept at 90–110 °C or a post-mold annealing step is used.
Post-mold annealing is typically 60–80 °C for 30–60 min in forced-air ovens. It increases crystallinity and can reduce internal stress, but it also produces post-mould shrinkage of 0.2–0.5% and possible warpage. Tooling should be sized from annealed reference parts, not from amorphous first shots. Thick sections above 3.0 mm are prone to internal voids if injection speed is too high; a controlled holding profile with cavity pressure transfer is preferred.