| HS Code | 521794 |
| Material Type | Polylactic Acid (PLA) |
| Color | Natural |
| Form | Pellets |
| Density | 1.24 g/cm³ |
| Melt Flow Rate 190 C 2 16 Kg | 10-30 g/10 min |
| Melting Point | 150-170 °C |
| Glass Transition Temperature | 55-60 °C |
| Tensile Strength | 50-60 MPa |
| Tensile Modulus | 3000-3500 MPa |
| Elongation At Break | 5-10 % |
| Flexural Modulus | 3000-3500 MPa |
| Flexural Strength | 70-80 MPa |
| Notched Izod Impact Strength | 20-30 J/m |
| Heat Deflection Temperature | 50-55 °C |
| Vicat Softening Point | 55-60 °C |
| Biodegradability | Compostable according to EN 13432 |
| Processing Method | Injection molding, extrusion |
| Moisture Content | ≤0.02 % |
| Biobased Content | ~100 % renewable |
As an accredited CiaoPlas™ PLA212LST(A) Natural Color Easy Process Biodegradable Polylactic Acid factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | CiaoPlas™ PLA212LST(A) Natural Color Easy Process Biodegradable Polylactic Acid comes in 25 kg moisture-barrier bags, palletized and stretch-wrapped. |
| Container Loading (20′ FCL) | Container Loading (20′ FCL): CiaoPlas™ PLA212LST(A) Natural Color Easy Process Biodegradable Polylactic Acid, securely palletized, shrink-wrapped, loaded for ocean freight. |
| Shipping | CiaoPlas™ PLA212LST(A) Natural Color is a biodegradable polylactic acid resin, typically shipped as a non-hazardous solid in sealed bags, drums, or supersacks. Not regulated for DOT/IATA/IMDG transport. Store dry, away from heat and moisture; handle with standard industrial hygiene. Ship via normal freight, road, sea, or air. |
| Storage | Store in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, flames, and moisture. Keep containers tightly closed when not in use to prevent contamination. Separate from strong oxidizers. Maintain stable temperature and humidity. Avoid excessive stacking, dust generation, and static buildup. Use appropriate grounding when handling powders. Inspect containers regularly for damage or leaks. Follow the manufacturer's SDS and local regulations. |
| Shelf Life | CiaoPlas™ PLA212LST(A) typically has a 12–24 month shelf life if stored sealed, cool, dry, and protected from moisture, heat, and UV. |
In sheet-fed and roll-fed thermoforming operations producing rigid food-service packaging, CiaoPlas™ PLA212LST(A) functions as an amorphous polylactic acid grade whose melt strength and water sensitivity dictate narrow processing boundaries. Pre-drying in a desiccant wheel hopper at 70–80°C for 4–6 hours to a dew point of −40°C is mandatory when ambient relative humidity exceeds 60%; residual moisture above 250 ppm triggers hydrolysis, reducing intrinsic viscosity and causing edge tear during plug-assisted forming. Sheet is extruded on a single-screw extruder with a 30:1–36:1 L/D ratio and a barrier screw, at barrel temperatures from 175°C to 210°C, with a flat-to-zero temperature profile and a gear pump stabilising die pressure below 8.0 MPa. Melt temperature at the flex-lip sheet die should be held at 190–210°C. Compliance for food-contact surfaces is evaluated under EU Regulation (EU) No 10/2011, including overall migration limits of 10 mg/dm² in aqueous and fatty simulants, and under an applicable U.S. FDA Food Contact Notification; 21 CFR 177.1520 does not apply because PLA is not an olefin polymer. Compostability claims require ASTM D6400-23 and EN 13432:2000, with ≥90% biodegradation in 180 days under industrial composting conditions. Formulation addition ratio for this sector is 96–98 wt% PLA212LST(A) dry-blended with 2.0–4.0 wt% antiblock/slip masterbatch based on the same PLA carrier; if impact modification is required, 5.0–10.0 wt% biodegradable aromatic-aliphatic copolyester replaces an equivalent portion of PLA212LST(A), but beyond 10 wt% sheet sag resistance declines during heating. The downstream production process involves sheet extrusion through a 2.0–3.0 mm flex-lip die gap onto a three-roll polishing stack kept at 20–35°C; sheet of 0.30–0.80 mm thickness is infrared-heated to 90–110°C surface temperature and transferred into a plug-assisted pressure former at 2.5–3.5 bar air pressure, with plug temperature 60–80°C and mold temperature 20–35°C. Finished part types include cold-drink cups, produce clamshells, bakery lids, deli trays, and clear portion containers. On production lines, moisture excursions above 300 ppm produce sheet thickness standard deviations exceeding 8%, and edge trim scrap rate rises above 12% in high-speed forming.
Melt residence time in high-cavitation disposable cutlery tooling of 32 or 64 cavities directly affects gate freeze consistency because PLA212LST(A) is prone to thermal degradation at the upper processing limit. The gate diameter is usually 0.8–1.5 mm, and injection speeds are set to fill each cavity in 0.5–1.2 s. The resin is processed with a barrel temperature profile of 170–210°C from feed throat to nozzle and a nozzle temperature of 190–205°C; melt temperature exceeding 230°C for more than 4 minutes leads to random black spots and gate freeze variation across cavities. Pre-drying conditions are identical to those for sheet extrusion: 80°C for 4 hours, dried moisture below 250 ppm. Compliance for cutlery used in food contact includes EU Regulation (EU) No 10/2011 with overall migration below 10 mg/dm²; in the United States, an applicable FDA Food Contact Notification must be confirmed. Compostable serviceware claims follow ASTM D6400-23, EN 13432:2000, and ISO 17088:2021. Formulation addition ratio for general-purpose cutlery is 100 wt% PLA212LST(A); when a nucleating agent is used, 0.5–2.0 wt% talc or a PDLA nucleating agent is added with PLA balance reduced accordingly. For improved toughness without loss of compostability, 3.0–7.0 wt% biodegradable copolyester is compounded. Downstream injection molding uses a reciprocating screw with 20:1–24:1 L/D, compression ratio 2.5:1, injection pressures of 80–120 MPa, hold pressure at 60–80% of injection peak, back pressure 2–5 MPa, and mold temperature 25–35°C for amorphous, high-clarity cutlery. Cycle times range from 15 s to 30 s depending on part thickness. Hot-runner systems with internally heated manifolds require melt residence time below 3 minutes; cold-runner sprues and runners up to 30 wt% regrind can be recycled into the same cutlery grade if dried to below 250 ppm. Finished product types include forks, spoons, knives, stirrers, disposable sample spoons, and single-serve food picks.
PLA212LST(A) is converted into fused-filament-fabrication filament on single-screw extruders with 24:1–30:1 L/D ratio and a screw compression ratio of 2.0:1–2.8:1. The melt viscosity window is controlled by setting barrel temperatures between 175°C and 205°C; melt temperature at the die is maintained at 185–200°C. The extruder is equipped with a melt gear pump, breaker plate, and 100/200/100 mesh screen pack. Filament is pulled through a water bath at 35–55°C and a laser diameter gauge; ovality must be controlled to ≤0.05 mm; diameter tolerance for 1.75 mm filament is ±0.05 mm, and for 2.85 mm filament it is ±0.05 mm. Compliance for the EU market is under REACH Regulation (EC) No 1907/2006; for products used in electrical and electronic prototyping, RoHS Directive 2011/65/EU is often requested by OEMs despite no electrical function in the filament itself. Compostability is not the primary performance criterion for this segment, but when claimed, EN 13432:2000 test evidence must cover the finished printed part. Formulation addition ratio is 100 wt% PLA212LST(A) for unfilled filament; if color masterbatch is added, it is metered at 2.0–4.0 wt% with PLA balance reduced accordingly. For flexible filament grades, 10–20 wt% biodegradable copolyester is compounded. The production process includes pre-drying at 70–80°C for 4–6 hours to below 200 ppm, then extrusion, water cooling, air wipe, laser micrometer feedback, and winding under tension of 0.5–1.5 N. Published data for this specific grade’s melt strength in filament extrusion is limited; line trials must verify draw ratio against ovality. Finished product types are 1.75 mm and 2.85 mm spools for FFF printing of prototyping fixtures, thermoformed part mock-ups, educational models, architectural massing models, and low-volume production aids.
Nonwoven plants running polypropylene screw profiles can process CiaoPlas™ PLA212LST(A) only after screw geometry changes because PLA is shear-sensitive and has a narrower melt processing window than isotactic polypropylene. The resin is dried to below 200 ppm moisture at 70–80°C for 4–6 hours; then it is fed to a single-screw extruder with 30:1 L/D and a low-shear screw designed for polyester. Spinneret melt temperature is held at 210–230°C; above 240°C, molecular weight loss begins and filament break frequency rises above 5 breaks per tonne; below 200°C, spin line viscosity is too high and fiber diameter coefficient of variation exceeds 10%. Compliance for disposable hygiene nonwovens involves EN 13432:2000 for compostability claims, ISO 9073-1:1989 for mass per unit area, and ISO 9073-2:1995 for thickness; if the nonwoven is used in a food-contact application, EU Regulation (EU) No 10/2011 overall migration below 10 mg/dm² applies. Formulation addition ratio for the polymer phase is 95–100 wt% PLA212LST(A); when PBAT is added for handle, it is compounded at 2.0–5.0 wt% with the PLA balance reduced correspondingly. For UV protection in crop cover applications, 0.5–1.5 wt% UV masterbatch is added. The downstream process runs on a spunbond line with melt pump, spin beam, 0.35–0.60 mm spinneret hole diameter, quench air at 15–25°C, and calender bonding at 130–150°C with line speeds of 100–400 m/min. Finished product types include compostable hygiene topsheets, agricultural frost protection fabric, wipes substrate, and tea bag overwrap nonwoven. Batch-to-batch MFR variation outside ±1.5 g/10 min by ISO 1133-1:2022 shifts filament diameter and bond point regularity; online diameter monitoring with 0.5 μm resolution is used to reject defective web.
If a paperboard extrusion coating line is converted from low-density polyethylene to CiaoPlas™ PLA212LST(A), the feed section and screw geometry must be reconfigured because the resin has a higher density and different neck-in behavior. The coating line uses a 90–120 mm extruder with 30:1 L/D and barrel temperatures of 200–240°C; die width may be up to 3,000 mm, and air gap is set at 150–250 mm. Chill roll temperature is 15–25°C. Pre-drying to below 200 ppm moisture at 80°C for 4 hours is required. Compliance for food-contact paperboard is evaluated under EU Regulation (EU) No 10/2011 overall migration limit 10 mg/dm², U.S. FDA 21 CFR 175.300 for resinous and polymeric coatings, and EN 13432:2000 for compostable packaging. Formulation addition ratio is 100 wt% PLA212LST(A) for a clear layer; 5.0–15.0 wt% PBAT is added to improve adhesion to paper and reduce pinholing, with PLA balance reduced accordingly. For pigmented barrier layers, 5.0–10.0 wt% white masterbatch is added; for coefficient of friction control, 0.2–0.5 wt% slip agent is added. Downstream production process consists of unwinding paperboard, corona pretreatment to wetting tension of 38–42 dynes/cm, extrusion coating through a slot die, chill roll polishing, and optional offline slitting. At line speeds of 150–300 m/min, edge neck-in must be held below 30 mm per side; above 250°C, neck-in increases and coating weight variability exceeds ±5%. Finished product types include compostable paper cups, takeaway containers, sandwich wraps, ice cream tubs, and hot beverage cup stock. Avoid blending the PLA layer with polyethylene or polypropylene, as immiscibility destroys compostability and delaminates the coating.
| Application scenario | Primary compliance standard | Critical threshold | Pre-drying requirement |
|---|---|---|---|
| Thermoformed food-service packaging | EU Regulation (EU) No 10/2011; ASTM D6400-23 | Overall migration <10 mg/dm²; ≥90% biodegradation in 180 days | <250 ppm moisture |
| Injection-molded cutlery | EN 13432:2000; ISO 17088:2021 | ≥90% disintegration in 12 weeks; <10 mg/dm² migration | <250 ppm moisture |
| 3D printing filament | REACH (EC) No 1907/2006; RoHS 2011/65/EU | SVHC <0.1 wt%; ovality ≤0.05 mm | <200 ppm moisture |
| Spunbond nonwoven | ISO 9073-1:1989; EN 13432:2000 | Basis weight tolerance ±5%; <10 mg/dm² if food-contact | <200 ppm moisture |
| Extrusion coating on paperboard | U.S. FDA 21 CFR 175.300; EU Regulation (EU) No 10/2011 | <10 mg/dm² migration; neck-in <30 mm per side | <200 ppm moisture |
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CiaoPlas™ PLA212LST(A) Natural Color Easy Process Biodegradable Polylactic Acid is a lactide-stabilized polylactic acid grade supplied as natural-colored cylindrical pellets with a nominal diameter of 3.0 mm ± 0.2 mm and a bulk density of 0.75 g/cm³ ± 0.05 g/cm³ by ISO 60:2023. The polymer is derived from renewable starch sources and retains a renewable carbon content above 95% when measured by ASTM D6866-21. The grade designation carries three processing modifiers: the LST rheology package lowers melt viscosity for thin-wall filling, the (A) designation indicates an annealable formulation suitable for post-mold heat treatment, and the natural color specification means no masterbatch or pigment is incorporated. Density determined by ISO 1183-1:2019 is 1.24–1.26 g/cm³, and melt volume-flow rate by ISO 1133-1:2022 at 210°C under 2.16 kg load is 15–25 cm³/10 min. This flow range is 2–3 times higher than standard extrusion PLA grades in the same molecular weight band and is the primary basis for the easy-process classification.
Typical mechanical data for the natural-color grade are summarized in Table 1. The values are generated on injection molded specimens prepared at 200°C melt temperature, 25°C mold temperature, and 60 mm/s injection speed.
| Property | Test method | Typical range |
|---|---|---|
| Density | ISO 1183-1:2019 | 1.24–1.26 g/cm³ |
| Melt volume-flow rate (210°C, 2.16 kg) | ISO 1133-1:2022 | 15–25 cm³/10 min |
| Tensile yield strength | ASTM D638-14 Type IV | 58–65 MPa |
| Tensile elongation at break | ASTM D638-14 Type IV | 2.5–4.0% |
| Flexural modulus | ISO 178:2019 | 3,200–3,600 MPa |
| Notched Izod impact strength | ISO 180:2000 Method A | 2.5–4.0 kJ/m² |
| Heat deflection temperature (0.45 MPa) | ISO 75-2:2013 Method B | 50–55°C unannealed |
| Vicat softening temperature (10 N, 50°C/h) | ISO 306:2013 Method A50 | 55–60°C |
| Mold shrinkage (parallel, 2 mm) | ISO 294-4:2018 | 0.3–0.5% |
The unannealed heat deflection temperature limits direct service to cold-fill and ambient-temperature applications. Post-mold annealing at 100°C for 30 min in a constrained fixture raises the heat deflection temperature under 0.45 MPa to approximately 85–95°C because cold crystallization increases the crystalline fraction to 30–40%. This annealable behavior differentiates the (A) variant from standard PLA grades, which often warp, stick to fixtures, or develop haze under identical thermal treatment. Annealing requires a fixture that restrains flatness; free-standing annealing at 100°C commonly produces warpage because shrinkage during cold crystallization is anisotropic. Ramp rates of 2–5°C/min to annealing temperature and cooling rates below 2°C/min reduce internal stress. The natural color grade retains transparency after annealing when cooled slowly; haze measured by ASTM D1003 on 1.0 mm plaques is typically 8–15%.
Water absorption measured by ISO 62:2008 after 24 h immersion at 23°C is 0.3–0.5%. Because polylactic acid is hygroscopic, even short exposure to ambient humidity above 60% can increase pellet surface moisture and require re-drying before processing. The annealable behavior is not a post-mold cure in the thermoset sense; it is a physical cold crystallization that requires the part to remain below the distortion temperature of the fixture material.
Unmodified PLA with a melt volume-flow rate of 8–12 cm³/10 min at 210°C/2.16 kg generally requires melt temperatures above 210°C and injection velocities above 100 mm/s to fill thin-wall sections thinner than 0.8 mm. CiaoPlas™ PLA212LST(A) fills equivalent sections at melt temperatures of 190–200°C and injection velocities of 60–80 mm/s. The reduction in melt temperature by 10–15°C narrows the thermal degradation window; residence time at 200°C below 12 min does not produce measurable tensile strength loss, whereas at 220°C the same loss can occur in less than 5 min. On a 120-ton hydraulic injection molding machine with a 25 mm diameter screw, the grade runs at peak injection pressures of 85–110 MPa for 1.2 mm wall thickness, approximately 10–20% lower than a standard PLA control under identical mold conditions.
Talc-nucleated PLA grades produce higher stiffness and shorter cycle times but increase haze. Compared with such nucleated grades, PLA212LST(A) has a lower crystallization rate and is better suited for transparent parts. PBAT/PLA blends provide higher elongation for flexible packaging, but the tensile elongation of PLA212LST(A) remains below 5%; it is therefore not a drop-in replacement for flexible film resins. The residual lactide content is controlled below 0.3 wt% by gas chromatography to reduce mold vent plate-out and odor during processing, a nuisance frequently observed in less refined PLA feedstocks.
On a 120-ton hydraulic injection molding machine equipped with a 25 mm general-purpose screw having L/D 22:1 and compression ratio 2.5:1, a barrel profile of 165–180°C in the rear zone, 180–195°C in the center zone, 190–205°C in the front zone, and 195–210°C at the nozzle is sufficient for parts with wall thickness from 0.6 mm to 2.0 mm. Mold temperature should be maintained at 25–35°C; lower mold temperatures reduce cycle time but increase frozen-in orientation and warpage in flat parts below 1.0 mm. Back pressure of 0.5–1.5 MPa is adequate; higher back pressure increases shear heating without improving melt homogeneity. For a 1.0 mm wall thickness, hydraulic clamp force of 0.5–0.8 tonnes per cm² of projected area is typical. Mold shrinkage measured by ISO 294-4:2018 is 0.3–0.5% parallel to flow and 0.3–0.5% perpendicular to flow.
Capillary rheometry at 200°C according to ISO 11443:2021 indicates shear-thinning behavior with apparent melt viscosity falling from approximately 250–350 Pa·s at 100 s⁻¹ to 40–60 Pa·s at 1,000 s⁻¹. This shear sensitivity permits filling of thin-wall sections without excessive injection speed, but it also means that high-shear hot runners with gate shear rates above 50,000 s⁻¹ can cause localized temperature rise and gate blush. Gate design should maintain shear rates below this value; valve-gated hot runners with gate diameters of 0.8–1.2 mm are suitable for 1.0 mm wall sections.
Pre-drying at 80°C for 4 h in a desiccant dryer with a dew point of −40°C or lower is mandatory when pellet moisture exceeds 250 ppm. Pellet moisture measured by ISO 15512:2019 above this threshold causes hydrolytic chain scission, visible as silver streaks, gate splay, and a measurable melt viscosity drop. Under production conditions, an MVR shift greater than 2 cm³/10 min after drying indicates incomplete drying or excessive residence time. Bulk storage at relative humidity above 60% for more than 2 h can increase surface moisture to a level requiring re-drying, especially in humid tropical manufacturing environments.
For sheet extrusion, a 40:1 L/D twin-screw extruder with barrel set points of 170–190°C and melt pump inlet pressure of 6–10 MPa provides stable output; die temperatures above 210°C cause edge tear and melt fracture. Clean regrind can be added at up to 20 wt%. Above this level, batch-to-batch variation in melt viscosity increases, and notched Izod impact strength may decline by up to 15%. Screw recovery should be set so that melt residence time does not exceed 5 min at 220°C; depolymerization above this threshold produces yellowing and a 5–10% loss of tensile strength. Batch-to-batch MVR variation of ±2 cm³/10 min is considered normal for this grade. Wider variation, or a sudden drop in melt viscosity during production, usually indicates moisture ingress or excessive regrind. On twin-screw lines, feed zone bridging has been observed when bulk density varies by more than 5%; maintaining pellet temperature below 45°C during transfer prevents bridging and screw slip.
In thin-wall injection molding of cutlery, cycle times of 15–25 s are achievable on 8-cavity cold-runner tools when mold temperature is 25°C and part weight is 4–8 g. Warpage is controlled by maintaining uniform gate freeze time; differences in gate freeze time above 0.2 s across cavities produce dimensional variation greater than 0.1 mm in 150 mm long parts.
Under aerobic industrial composting conditions specified by ISO 14855-1:2012, polylactic acid hydrolyzes and mineralizes to carbon dioxide, water, and biomass at a rate governed by temperature, moisture, and microbial consortia. Testing at 58°C ± 2°C and 50–60% relative humidity typically yields 90% mineralization within 180 days; disintegration by ISO 20200:2015 occurs within 12 weeks for specimens with thickness ≤ 2 mm. These values do not apply to home compost or ambient soil; PLA212LST(A) is not designed for anaerobic digestion, and published data for marine or soil biodegradation of this specific grade are limited.
Compliance claims require testing on the finished article. EN 13432:2000 and ASTM D6400-19 require not only biodegradation and disintegration but also chemical characterization, heavy metal limits, and ecotoxicity assessment. The pellet alone does not automatically transfer certification to a filled, laminated, or printed product. Heavy metal concentrations for the raw grade are below the threshold values specified in EN 13432:2000 Annex A.2, based on restricted-substance screening.
Compliance documentation for the natural-color grade is summarized in Table 2.
| Regulatory domain | Designation or standard | Status or condition |
|---|---|---|
| Industrial compostability | EN 13432:2000 / ASTM D6400-19 / ISO 17088:2021 | Conformity must be validated on final article |
| Aerobic biodegradation | ISO 14855-1:2012 | ≥90% mineralization within 180 days at 58°C |
| Disintegration | ISO 20200:2015 | Disintegration within 12 weeks for thickness ≤2 mm |
| Restricted substances | RoHS Directive 2011/65/EU Annex II | Below 0.1 wt% in homogeneous material |
| REACH SVHC | EC 1907/2006 Article 33 | No substances above 0.1 wt% as supplied |
| Food contact | EU 10/2011 / FDA 21 CFR Parts 170–199 as applicable | No blanket approval; article-specific migration testing required |
Food-contact status must be established for each finished article. The pellets are not supplied under a blanket EU 10/2011 or FDA 21 CFR declaration; migration testing under the relevant food-contact regulation is required depending on food type, contact time, and temperature. For repeated-use articles, dishwashing and microwave testing are outside the demonstrated operational boundary unless the part has been annealed and validated. The grade is unsuitable for continuous service above 55°C in unannealed parts, for contact with strong alkaline cleaners above pH 10, and for blending with amine-based additives that promote chain scission and color shift. When these boundary conditions are maintained, representative application areas include rigid disposable cutlery, thin-wall non-food packaging, cosmetic containers, and transparent consumer goods produced on conventional injection molding or sheet extrusion lines. Continuous use above 55°C without annealing, contact with strong alkalis, or exposure to high-shear processing above 210°C are outside the demonstrated operational boundary.