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Как аккредитованная фабрика по производству биоразлагаемой полимолачной кислоты CiaoPlas™ PLA212LST(A) Natural Color Easy Process, мы соблюдаем строгие протоколы качества - каждая партия подвергается строгим испытаниям для обеспечения последовательных стандартов эффективности и безопасности.
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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.