| HS Code | 764958 |
| Product Name | Polylactic Acid (PLA) REVODE101 |
| Chemical Name | Polylactic acid |
| Cas Number | 26100-51-6 |
| Appearance | White to light-yellow pellets |
| Density | 1.24-1.25 g/cm3 |
| Melt Flow Rate | 10-30 g/10 min (190°C, 2.16 kg) |
| Melting Point | 150-170°C |
| Glass Transition Temperature | 55-60°C |
| Tensile Strength | 50-60 MPa |
| Elongation At Break | 3-10% |
| Flexural Modulus | 3000-3500 MPa |
| Impact Strength | 2-5 kJ/m2 |
| Heat Deflection Temperature | 50-55°C |
| Biodegradability | Compostable and biodegradable |
As an accredited Polylactic Acid (PLA) REVODE101 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Polylactic Acid (PLA) REVODE101 supplied in 25 kg sealed, moisture-resistant foil-lined bags, stacked on pallets for industrial transport. |
| Container Loading (20′ FCL) | Container loading for Polylactic Acid (PLA) REVODE101 in 20′ FCL: palletized 25 kg bags, shrink-wrapped, securely braced for ocean shipment. |
| Shipping | Polylactic Acid (PLA) REVODE101 is shipped as non-hazardous thermoplastic pellets in sealed moisture-barrier bags, lined cartons, sacks, or bulk bags. It is not DOT/IMDG/IATA regulated and has no UN number or hazard class. Keep dry, cool, and away from heat, sunlight, moisture, and contamination. |
| Storage | Store Polylactic Acid (PLA) REVODE101 in a cool, dry, well-ventilated area away from direct sunlight, heat, moisture, and ignition sources. Keep containers tightly closed and sealed to prevent hydrolysis and contamination. Maintain temperatures below 30°C and low humidity. Avoid contact with strong oxidizers. Use original packaging and follow local regulations. Shelf life may be reduced by prolonged exposure to heat or moisture. |
| Shelf Life | Polylactic Acid (PLA) REVODE101: store sealed, cool, and dry; typical shelf life is approximately 24 months. |
In thin-wall single-use food serviceware with wall sections below 1.0 mm, REVODE101 is processed on reciprocating-screw injection moulding machines fitted with desiccant-bed dryers and closed-hopper feed. The resin is dried at 80 °C for 4 h to a residual moisture level below 250 ppm, preferably below 100 ppm, because melt-phase hydrolysis at barrel temperatures above 190 °C reduces molecular weight within minutes and produces silver streaks, gate blush, and brittle rim sections. Barrel profiles are set with feed zone 180–195 °C, compression zone 195–210 °C, metering zone 200–215 °C, and nozzle 200–215 °C. Total holdup time is held below 5 min; at melt temperatures above 230 °C the homopolymer undergoes rapid thermal chain scission with a measurable drop in melt viscosity and a colour shift toward yellow. The injection stage uses high screw-forward velocity in the 100–150 mm/s range and peak pressure between 70–110 MPa, followed by pack-and-hold at 50–70% of peak pressure. Mould temperature is maintained at 20–30 °C with turbulent-flow water circuits, because PLA quenched against a cold mould retains higher transparency and releases earlier; raising mould temperature toward 35–40 °C reduces residual stress but increases cycle time and may induce haze. Gate design for lids and cups requires a full-round or wide-edge gate with a land thickness of 60–70% of wall stock; multi-cavity tools benefit from valve-gated hot runners with full-round channels and a heated drop tip orifice of 1.0–1.5 mm. Mechanical testing on moulded plaques under ASTM D638 typically reports tensile yield near 60 MPa and elongation at break below 10%, indicating notch sensitivity and the need to avoid sharp transitions at the rim or hinge. Heat deflection temperature under ASTM D648 at 0.45 MPa is below 60 °C, so hot-fill service, microwave reheating, and retort conditions are outside the operational boundary. Food-contact compliance is not automatic for the resin: a finished article must demonstrate overall migration below 10 mg/dm² under Regulation (EU) No 10/2011 and, for US market access, must be covered by a valid Food Contact Notification or an FDA clearance held by the resin supplier and referenced for the specific manufacturing conditions. If REVODE101 is blended with colour masterbatch, the carrier resin must be PLA-compatible; polyolefin-carrier masterbatches produce haze and weld-line separation in thin sections. Amine-based slip agents should not be used as processing aids because they accelerate hydrolytic degradation during melt processing.
Comparative regulatory conformance pathways for single-use serviceware:
| Jurisdiction | Reference standard or regulation | Critical pass criterion |
|---|---|---|
| European Union | Regulation (EU) No 10/2011 | Overall migration below 10 mg/dm² |
| United States | Food Contact Notification or 21 CFR clearance | Finished-article migration testing under intended food simulants |
| China | GB 4806.7-2016 | Total migration below 10 mg/dm² |
| Compostability | EN 13432, ASTM D6400 | Disintegration ≥90% after 12 weeks; biodegradation ≥90% after 180 days |
The extrusion line configuration for REVODE101 transparent sheet runs on a single-screw extruder with an L/D ratio of 30:1 to 36:1, a barrier screw, and a gear pump ahead of a flexible-lip flat die. The same low-moisture specification applies: residual moisture above 250 ppm reduces melt strength and generates edge voids and longitudinal die lines. Melt temperature at the die is kept between 190 °C and 210 °C; higher temperatures produce sag between the die and the vertical calender, causing transverse gauge variation greater than ±5% and web wander. The roll-stack temperature controls gloss, crystallinity, and trimming behaviour. A top roll set at 30–45 °C, a middle roll at 25–35 °C, and a bottom roll at 20–30 °C is typical for amorphous sheet; roll temperatures above 55 °C initiate contact crystallisation, which appears as local haze bands and reduces thermoform drawability. Conversely, roll temperatures below 20 °C freeze in orientation and cause edge splitting during inline trimming. The extruded sheet is usually 0.25–0.70 mm thick and is stored in sealed polyethylene film because PLA sheet picks up moisture within hours at relative humidity above 60%. Thermoforming uses plug-assisted processing with sheet surface temperature of 90–120 °C and aluminium mould temperature of 20–30 °C. The low melt strength of unmodified PLA limits draw ratios; for a tray with depth-to-width ratio above 0.4, plug geometry must be optimised to redistribute material into corners, otherwise thinning below 50% of initial gauge occurs near the base radius. Impact resistance is measured on formed trays by falling-dart puncture under ASTM D3763 or ISO 6603; published data for this specific configuration is limited, but package validation typically sets a minimum puncture energy for the target produce pack rather than relying on a resin-level value. Moisture vapour transmission is higher than PET and can be quantified by ASTM F1249 at 38 °C/90% RH, but the usefulness of REVODE101 in produce trays is restricted to short-shelf-life chilled applications where condensation is accepted and barrier is not the controlling variable.
Because REVODE101 combines high transparency with a melt-flow range suited to multi-cavity tooling, short-life writing instruments and translucent stationery shells are moulded without the impact strength required for long-service power tools or luggage. The material injection conditions follow the same drying and barrel-temperature envelope as thin-wall food serviceware. ABS or polycarbonate replacement in pen barrels is limited to low-load assemblies because notched impact strength under ASTM D256 is below typical amorphous thermoplastics used for drop-prone personal electronics. Mating features should incorporate generous radii and avoid thread roots sharper than 0.3 mm; sonic welding of translucent shells is generally replaced by snap-fit or UV-cured adhesive bonding because PLA has a narrow weld thermal window.
Substitution of general-purpose polystyrene in cosmetic jars, compacts, and loose-powder trays is driven by the need for optically clear walls and a renewable feedstock, but the conversion boundary is set by chemical compatibility rather than melt processing. Clarity and surface gloss of REVODE101 are close to GPPS, while the elastic modulus under ASTM D638 is adequate for rigid closures. However, PLA stress-cracks in contact with ester-based fragrance oils, ketones, and some ethanol-water systems above 40 °C; chemical resistance testing is performed under ASTM D543-21 or ISO 2812-1 with the actual formulation at 40 °C for 72 h, followed by tensile retention and visual crazing assessment. Fragrance migration kinetics in polymer matrices are sorption-controlled, and polar migrants diffuse more readily into PLA than into polyolefins; a barrier varnish or an EVOH liner may be required for aggressive fragrances. Decoration processes use low-solvent pad printing, UV-cured screen ink, or hot-stamping foil. Corona or plasma surface treatment is used to raise surface energy for adhesion; solvent-borne inks based on methyl ethyl ketone or ethyl acetate should be avoided because they induce crazing at gate areas. Moulded-in colour in REVODE101 requires PLA-compatible masterbatch and reduces transparency if the pigment loading exceeds 0.5 wt% in transparent packages. Drop testing of thick-wall jars on concrete from 1.0 m is generally acceptable, but thin-wall compacts with wall sections below 1.2 mm may crack at the hinge or sidewall when impact-modified resin is not used. Regulatory compliance for cosmetic packaging does not require food-contact clearance but must satisfy REACH Regulation (EC) No 1907/2006, Annex XVII restrictions, and Regulation (EC) No 1223/2009 for cosmetics placed on the EU market; the packaging must not release substances that alter the cosmetic formulation or exceed the limits set in the product safety file.
Diameter stability in PLA filament starts in the drying system, not the die. REVODE101 can be converted into monofilament for material extrusion only after drying at 80 °C for 4 h to 250 ppm or lower, and the extruder should be a single-screw unit with an L/D of at least 28:1, a mixing section, and a gear pump connected to a round die with a land length of 2.0–2.5 mm. Melt temperature at the die is held between 190 °C and 205 °C; higher temperatures reduce melt strength and cause sag in the air gap, while lower temperatures increase die swell and make diameter control unstable. The extrudate is quenched in a water bath at 30–40 °C, and the air gap between die and water surface is kept between 5–10 mm. A dual-axis laser gauge measures diameter at 1 kHz, controlling draw-down through a capstan. For 1.75 ±0.05 mm filament, ovality should be held below 0.05 mm because high-oval stock causes extruder gear slip and under-extrusion in desktop printers. Take-up tension is maintained below 2 N to avoid cold-drawing orientation that raises shrinkage at the print bed. The resulting filament is more brittle than compounded PLA filament grades and must be stored in sealed bags with silica gel; moisture absorption above 300 ppm produces steam pops and reduces interlayer adhesion. Impact modification of 5–15 wt% may be used in compounding to reduce brittleness, but this moves the melt behaviour away from the neat REVODE101 injection-moulding envelope. Tensile properties of printed test bars under ASTM D638 Type IV are typically below injection-moulded values, often in the 70–85% range for strength, because of layer interfaces; this relationship should be validated on the target machine rather than assumed from pellet data. Print-bed adhesion is acceptable at 50–60 °C on PEI or build plates with PLA-rated adhesive; print chamber temperatures above 50 °C may soften unsupported geometries and reduce overhang quality. Published data for this specific configuration is limited because REVODE101 is optimised for injection moulding, so filament producers must evaluate melt strength and impact toughness after any additive package such as impact modifier or nucleating agent.
In laboratory consumables and pre-surgical anatomical models, REVODE101 is injection moulded for non-implantable parts that require dimensional stability during short-term use and the ability to be cut, drilled, or marked without melting. Examples include tray liners, specimen containers, teaching models, and bone-model shells made from CT-derived tooling. The resin can be processed on conventional injection machines without the high mould temperatures required for semi-crystalline polyolefins, which allows tooling from less thermally aggressive aluminium alloys. Sterilisation is a process boundary: steam autoclave cycles at 121 °C or 134 °C exceed the heat deflection temperature and produce gross deformation; low-temperature hydrogen peroxide gas plasma or ethylene oxide is generally compatible, but validation under ISO 11135 or ISO 14937 is required for the finished device. Gamma irradiation at 25 kGy may cause chain scission and yellowing, so dose mapping and property retention testing under ISO 527-2 should be performed if radiation sterilisation is considered. For anatomical models that are not intended for implantation, the main regulatory expectation is cleanliness, dimensional accuracy, and manufacturability; if parts contact intact skin, a cytotoxicity assay under ISO 10993-5 is often requested but is not an inherent property of the resin. Dimensional changes after conditioning at 23 °C/50% RH are low, but immersion in water or humid environments leads to gradual hydrolysis and surface whitening; models used repeatedly in wet labs should be stored in dry trays and not soaked in disinfectants above 40 °C.
The degradation rate of unmodified PLA clips in soil is not linear, because hydrolysis is accelerated by temperature, moisture, and microbial abundance in the root zone. Short-life horticultural clips, vine fasteners, and plant tags moulded from REVODE101 have initial tensile strength near 60 MPa under ASTM D638, but this value drops sharply once the part surface becomes coated with soil biofilm and the local pH shifts. Industrial compostability can be referenced under EN 13432 or ASTM D6400, which require disintegration ≥90% after 12 weeks and biodegradation ≥90% within 180 days in a managed composting facility. Soil burial under ASTM D5988 or ISO 17556 is much slower and is not the same as compostability; an unmodified PLA clip buried in soil at 20 °C may retain significant strength after one season, while in a hot, moist compost pile it can disintegrate in months. Moulded horticultural parts exposed to UV require a stabilised compound; unstabilised REVODE101 develops surface crazing and a drop in elongation at break after continuous outdoor exposure, and weathering protocols under ASTM G154 or ISO 4892-2 should be used to establish a replacement interval. Wall thickness near the hinge of a vine clip is typically 1.5–2.5 mm, and the living hinge should be flexed at installation temperature above 15 °C because PLA hinge fracture is common at cold-field temperatures. The injection moulding window follows the same drying requirements as food serviceware, but mould temperature can be raised to 30–40 °C to reduce hinge stress and improve crystallinity at the gate. If the clip is coloured with masterbatch, the carrier resin must be PLA-compatible; polyolefin carriers reduce hinge performance and create delamination in the stress-whitened bend zone. After the first growing season, used clips should be routed to an industrial composting facility rather than left in the field, because soil degradation under ambient conditions is too slow to justify an unmanaged disposal claim.
Comparative degradation requirements for short-life horticultural items:
| Condition | Standard | Typical pass criterion |
|---|---|---|
| Aerobic industrial compost | EN 13432, ASTM D6400 | Disintegration ≥90% by mass after 12 weeks; biodegradation ≥90% by 180 days |
| Respiration in compost | ISO 14855-1 | Carbon conversion relative to cellulose control |
| Soil burial | ASTM D5988, ISO 17556 | No universal pass/fail; report mass loss and tensile retention |
| UV weathering | ASTM G154, ISO 4892-2 | Buyer-defined tensile or elongation retention after exposure |
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Polylactic Acid (PLA) REVODE101 is an unfilled, transparent, general-purpose polyester resin supplied as cylindrical pellets and intended primarily for injection moulding, rigid packaging, and thin-wall articles. The polymer is a linear aliphatic polyester obtained from lactide monomers; the backbone ester linkages are susceptible to hydrolytic chain scission during melt processing when moisture is not controlled. The grade is not formulated with impact modifiers, nucleating agents, or melt-strengthening additives, and it therefore occupies a narrower processing window than toughened PLA compounds, nucleated PLA grades, or fossil-based polyolefins. Representative screening data are generated under ISO 1183-1, ISO 1133-1, ISO 527-2, and related methods; lot-specific certificates supersede general literature values. Applications requiring continuous-use temperature above 60 °C under load are outside the typical thermal capability. REVODE101 is not a drop-in replacement for polystyrene or polypropylene without recalibrating drying, melt temperature, and tooling because melt rheology, shrinkage behaviour, and moisture sensitivity differ.
Moisture control is the primary determinant of melt stability. Pellets as supplied may contain up to 0.25 % moisture; melt processing requires reduction to 0.025 % (250 ppm) or lower. A desiccant dryer with a dew point not above -40 °C and an inlet air temperature of 80 °C for 4 h to 6 h is used on production lines. Vacuum drying at 70 °C to 80 °C for 6 h to 8 h is an alternative when the vacuum system maintains adequate water vapour removal. At ambient relative humidity above 60 %, open hoppers allow rapid moisture regain, and closed-loop drying with insulated hoses becomes necessary. Twin-screw compounding and injection moulding field data show that wet pellets raise the melt flow index measured under ISO 1133-1 at 190 °C with 2.16 kg load, reduce tensile yield stress measured under ISO 527-2, and produce surface splay. Melt temperatures are typically held at 190 °C to 210 °C. Continuous melt residence above 220 °C for more than 10 min accelerates random chain scission, lactide regeneration, and yellowing. Screw designs with 24:1 to 40:1 L/D and compression ratios of 2.2:1 to 3.0:1 are used; high-shear mixing can generate viscous heating that raises melt temperature above the set point.
| Property | Method | Representative range | Test condition |
|---|---|---|---|
| Density | ISO 1183-1 | 1.24–1.26 g/cm³ | 23 °C |
| Melt flow index | ISO 1133-1 | 8–18 g/10 min | 190 °C, 2.16 kg |
| Moisture content | ISO 15512 | ≤ 0.25 % as supplied; ≤ 0.025 % after drying | Karl Fischer |
| Tensile yield stress | ISO 527-2 | 55–65 MPa | Type 1A, 50 mm/min |
| Tensile modulus | ISO 527-2 | 3.0–3.6 GPa | 1 mm/min |
| Flexural modulus | ISO 178 | 3.2–3.6 GPa | 2 mm/min |
| Notched Izod impact | ISO 180/A | 2.5–4.0 kJ/m² | 23 °C, notch A |
| Heat deflection temperature | ISO 75-2/B | 50–60 °C | 0.45 MPa |
| Vicat softening temperature | ISO 306/B50 | 55–65 °C | 50 N, 50 K/h |
| Glass transition temperature | ISO 11357-2 | 55–60 °C | DSC, second heating |
| Melting temperature | ISO 11357-3 | 150–170 °C | DSC, second heating |
| Haze | ASTM D1003 | 2–5 % | 2 mm injection-moulded plaque |
Published data for this specific REVODE101 configuration is limited in open-access literature; the ranges above are representative screening values for unfilled PLA and should not be used as lot-release limits. Against impact-modified PLA compounds, REVODE101 exhibits lower notched Izod impact, lower elongation at break, and lower haze. Against nucleated or heat-resistant PLA grades, the heat deflection temperature under ISO 75-2/B is lower, commonly below 60 °C, whereas nucleated grades may exceed 90 °C under the same load. The material is not equivalent to melt-strengthened PLA grades used for foamed sheet or blown film; bubble instability and draw resonance occur when unmodified REVODE101 is processed on conventional blown-film lines. Compared with amorphous PET and polystyrene, the processing temperature is lower, but drying and residence-time restrictions are more severe.
In thin-wall injection moulding with hydraulic clamp forces between 150 tonnes and 300 tonnes, the nozzle melt temperature is maintained at 200 °C to 205 °C, and mould surfaces are held at 25 °C to 35 °C. Linear mould shrinkage measured after 24 h under ISO 294-4 is typically 0.4 % to 0.6 %; gate positions are set to compensate for differential shrinkage between flow and transverse directions. Production-scale trials on 36:1 L/D reciprocating-screw machines indicate that back pressure should be limited to 5 bar to 10 bar; higher back pressure raises melt temperature without improving homogenization. Shot sizes should not exceed 60 % to 70 % of barrel capacity to avoid residence-time excursions. Hold-pressure profiles are set to compensate for the relatively high melt viscosity; inadequate packing produces sink marks in sections thicker than 3 mm. When mould temperature exceeds 40 °C, ejection becomes difficult because the part remains above the glass transition, and cycle time increases. Polished stainless steel tooling and direct gates support demoulding; release sprays are not required when the mould is correctly cooled.
Elevated barrel temperatures produce non-linear changes in processability. At a barrel front set point of 215 °C or higher, the apparent shear viscosity of unmodified PLA can fall by 10 % to 20 % relative to the 200 °C baseline, as measured by capillary rheometry under ISO 11443 at 100 s⁻¹. The reduction is not a processing advantage; it accompanies molecular weight loss and broadens the molecular weight distribution. Published data for this specific REVODE101 configuration is limited, but field observations on reciprocating-screw machines show that melt flow index can drift upward from 8–18 g/10 min by more than 50 % after 30 min at 220 °C, leading to flash, warpage, and reduced impact resistance. The critical processing window is therefore ±5 °C around the recommended barrel profile. Zones should be profiled from 185 °C at the throat to no more than 210 °C at the nozzle. At 215 °C nozzle set point, flash becomes difficult to control in vents and ejector clearances; at 185 °C nozzle set point, short shots and gate freeze-off occur in sections thinner than 1.5 mm. Avoid melt blending with unneutralized amine-based additives, high-alkali fillers, or metal carboxylates; alkaline species accelerate ester backbone cleavage and prematurely reduce melt stability. If colour concentrates are used, the carrier resin should be a compatible PLA or neutral polyester to avoid phase segregation.
For flat-sheet extrusion for thermoforming, melt temperature at the die is set between 195 °C and 205 °C, with chill-roll temperatures from 15 °C to 30 °C. Sheet gauge control above 1.0 mm becomes difficult because unmodified PLA exhibits low melt strength, producing draw resonance and edge waver. Lines with melt pumps and doctor-blade controls generate more stable output than gravity-fed single-screw extruders. Thermoforming requires sheet surface temperatures of 70 °C to 90 °C; plug-assisted forming reduces corner thinning in deep-draw cavities. Moisture regain during sheet storage must be controlled, because wet sheet generates bubbles and surface splay during heating. Extrusion-grade and blow-moulding PLA grades differ from REVODE101 mainly in melt flow index and melt strength; film grades are typically formulated with chain extenders or branching agents, while REVODE101 does not contain these modifications.
Under REACH, the polymer itself is generally exempt from registration, but the registration status of constituent lactide monomers and any additives must be confirmed from the supplier safety data sheet. RoHS 2011/65/EU restrictions apply to electrical and electronic equipment; PLA resin does not inherently contain the restricted heavy metals, but converter-specific pigments and additives can alter the final article status. For food-contact packaging, REVODE101 must be assessed under EU 10/2011 or the applicable national migration framework for the finished article, not for the resin alone. Migration limits are article-specific and depend on temperature, time, and food simulant. Biobased carbon content is determined by ASTM D6866-22; published data for this specific REVODE101 configuration is limited, but PLA derived from plant starch typically exhibits renewable carbon fractions above 95 %. Certificates of composition, lot-specific melt flow index, and drying conditions should be retained in the batch record for traceability under ISO 22000 or equivalent food-safety management systems.
Regrind compatibility is a further processing boundary. Clean, dried regrind from unfilled REVODE101 can be recombined with virgin pellets at 20 % to 30 % by weight for non-appearance parts; higher regrind fractions reduce tensile elongation and increase melt flow index because hydrolytic chain scission accumulates through each heat history. The material should not be mixed with petroleum-based polyolefin scrap unless a dedicated compatibilizer system is used, because phase separation and delamination occur. Storage in sealed, moisture-barrier packaging below 30 °C is required; pallets stored in unheated warehouses above 60 % relative humidity require pre-drying before production scheduling.