Products

Revode 110 Thermoforming Sheet Extrusion Polylactic Acid Resin

    • Product Name: Revode 110 Thermoforming Sheet Extrusion Polylactic Acid Resin
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
    • CONTACT NOW
    Specifications
    HS Code 143026
    Productname Revode 110 Thermoforming Sheet Extrusion Polylactic Acid Resin
    Chemicalname Polylactic Acid (PLA)
    Grade Revode 110
    Form Pellets
    Color Natural
    Density 1.24-1.25 g/cm³
    Meltflowrate 2-6 g/10 min (190°C/2.16 kg)
    Meltingpoint 155-170°C
    Glasstransitiontemperature 55-60°C
    Tensilestrength 50-60 MPa
    Elongationatbreak 3-5%
    Flexuralstrength ≥70 MPa
    Flexuralmodulus 3000-3500 MPa
    Vicatsofteningtemperature ≥55°C
    Heatdeflectiontemperature ≥50°C
    Moisturecontent ≤0.5%
    Ashcontent ≤0.1%
    Stereochemicalpurity ≥95% L-lactide
    Renewablecontent ≥90%
    Biodegradability Industrial compostable
    Processingmethod Thermoforming sheet extrusion
    Dryingtemperature 80°C
    Dryingtime 4 hours
    Extrusiontemperature 180-230°C

    As an accredited Revode 110 Thermoforming Sheet Extrusion Polylactic Acid Resin factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Revode 110 Polylactic Acid Resin is typically packaged in 25 kg net multiwall paper bags, palletized and shrink-wrapped for transport.
    Container Loading (20′ FCL) 20′ FCL container loaded with 25kg bags of Revode 110 PLA resin, palletized and secured for thermoforming sheet extrusion.
    Shipping Revode 110 PLA resin is shipped in sealed moisture-barrier bags inside fiber drums or cartons, palletized and stretch-wrapped. Store in a cool, dry, ventilated area away from heat and sunlight. Handle as non-hazardous, but avoid dust generation and static. Follow MSDS and local transport regulations.
    Storage Store Revode 110 Thermoforming Sheet Extrusion Polylactic Acid Resin in a cool, dry, well-ventilated area, away from heat, ignition, and sunlight. Keep original packaging sealed to prevent moisture uptake, which can degrade PLA. Recommended: below 30°C, low humidity, FIFO rotation, and adherence to shelf-life guidance. Protect from physical damage and avoid prolonged high temperatures or damp conditions.
    Shelf Life Shelf life is 12 months when stored unopened in original packaging under cool, dry conditions, away from moisture and sunlight.
    Application of Revode 110 Thermoforming Sheet Extrusion Polylactic Acid Resin

    Ambient produce, bakery, and deli clamshells represent the highest-volume downstream cut for Revode 110 sheet extrusion. The resin must be pre-dried in a desiccant dryer with a dew point of -40 °C or lower and a drying temperature of 80 °C for a minimum of 4 h; residual moisture before extrusion should be below 250 ppm, and values above 400 ppm produce measurable intrinsic-viscosity loss from ester hydrolysis at melt temperatures exceeding 180 °C. This hydrolysis-driven viscosity drop appears on the thermoforming line as edge-tear during plug-assisted forming, sheet sag after the downstack, and inconsistent wall thickness in corners. If lot MFR under ISO 1133-1 at 190 °C/2.16 kg drifts below 2 g/10 min, screw torque rises and sheet edge-thickness variation increases; above 4 g/10 min, sag after the roll stack becomes difficult to correct by adjusting roll gap alone. A single-screw extruder with 30:1 to 36:1 L/D, a barrier screw with compression ratio between 2.5:1 and 3.5:1, and a melt pump ahead of the die provides the melt stability required for sheet widths above 800 mm. The melt temperature should be held at 200 °C to 210 °C, and the flat die should be set at 190 °C to 205 °C; residence time above 10 min at these temperatures accelerates yellowing and reduces molecular weight. On a vertical three-roll stack, the middle roll temperature is maintained between 25 °C and 45 °C, and polished rolls are used to minimize surface haze on stock between 0.35 mm and 0.80 mm. Thermoforming uses a sheet surface temperature of 90 °C to 110 °C, plug temperature of 85 °C to 95 °C, and mold temperature of 35 °C to 50 °C; draw ratios should remain below 2.0:1 for uninterrupted PLA sheet. Finished articles include vented produce clamshells, bakery containers, deli trays, and low-temperature cup lids. Food-contact compliance under EU Regulation (EU) No 10/2011 requires overall migration below 10 mg/dm², and U.S. applications rely on the supplier’s Food Contact Notification clearance; industrial composting claims are verified against EN 13432 or ASTM D6400. The material is not suitable for hot-fill, retort, or microwave service above 60 °C.

    What Limits Cold-Chain Dairy Cup and Portion-Pack Forming?

    At 2 °C to 6 °C, unmodified PLA sheet enters a brittle regime for dairy cups and snap-fit portion lids, and flange cracks propagate during filling-line capping if the thermoformed lip radius is below 1.5 mm. Notched Izod impact measured under ISO 180 at 23 °C for sheet-extrusion PLA grades typically falls between 2 kJ/m² and 4 kJ/m²; this value drops further at refrigeration temperatures, so cold-chain converters often add an impact-modifier masterbatch at 3 wt% to 8 wt%. Loadings above 10 wt% generate visible haze and can invalidate industrial compostability certification under EN 13432 when the modifier backbone is not biodegradable within 180 days. For dairy lids, a three-layer A/B/A coextrusion structure places 20 wt% to 30 wt% clean post-industrial regrind in the core; the skin layers remain 8% to 12% of total sheet thickness to preserve surface gloss and food-contact compliance. The sheet surface temperature before plug-assisted pressure forming is held at 95 °C to 105 °C, mold temperature at 40 °C to 55 °C, and forming pressure at 0.4 MPa to 0.6 MPa. Finished products are cold-fill yogurt cups, dessert cups, and lid stock for dairy tubs; they are not suitable for hot-fill above 60 °C or for steam sterilization. Regulatory documentation for dairy applications relies on EU 10/2011 aqueous food simulant testing and the supplier’s FDA Food Contact Notification; converters verify organoleptic neutrality under the finished-food packer’s sensory protocol because low-molecular-weight residuals can migrate into dairy emulsions.

    The compliance matrix across the downstream segments is as follows:

    SegmentStandardCritical limit
    Fresh produce and dairy food-contact articlesEU Regulation (EU) No 10/2011Overall migration below 10 mg/dm²
    U.S. food-contact applicationsFDA Food Contact NotificationUse conditions and resin composition per supplier FCN
    Industrial compostabilityEN 13432 / ASTM D6400≥90% biodegradation in 180 days, ≥90% disintegration in 12 weeks
    EU REACHRegulation (EC) No 1907/2006SVHC content below 0.1 wt%
    EU packaging heavy metalsDirective 94/62/ECSum of lead, cadmium, mercury, hexavalent chromium below 100 ppm

    Unlike food-contact packaging, horticultural propagation trays produced from Revode 110 are selected for stiffness, soil-contact durability, and industrial compostability rather than low migration. Trays are pressure formed from sheet between 0.5 mm and 1.5 mm. To raise flexural modulus for multi-cell propagation trays, mineral fillers such as talc or calcium carbonate are added at 5 wt% to 15 wt%; the trade-off is a measurable drop in notched impact and increased opacity. The sheet is extruded in the same melt temperature window as clear packaging but uses a textured roll surface to hide filler-induced surface defects. Thermoforming tooling for propagation trays uses deeper draw pockets, and the draw ratio must not exceed 2.5:1 when filler is present because filler particles initiate microvoids in corners. Processing trials show that sheet moisture above 300 ppm causes pinholes near the cell bottom during forming. Finished articles include plug trays, nursery pots, and transport trays for vegetable seedlings. Compliance is governed by REACH for substances of very high concern and, if compostability is claimed, by EN 13432; food-contact clearance under EU 10/2011 is not required for these non-food articles. The material is not intended for long-term outdoor weathering because hydrolytic degradation and UV embrittlement reduce service life beyond one crop cycle unless stabilizer packages are used, and such stabilizers may compromise compostability.

    Consumer Goods Blister and Display Tray Forming Conditions

    Non-food blisters for cosmetics, toys, and hardware use Revode 110 sheet from 0.25 mm to 0.60 mm. The forming process relies on thermal conduction from polished aluminum tooling rather than plug assistance for shallow blister cavities; mold temperature is held between 30 °C and 45 °C, and sheet surface temperature between 90 °C and 105 °C. Sealing to printed paperboard differs from PVC or PET because PLA is polar and requires a seal-lacquer system rated for polylactic acid; heat-seal dwell and temperature are set by the board coating, with typical start-up values of 0.5 s to 1.2 s and 140 °C to 160 °C. To prevent nested blisters from blocking, a slip agent such as erucamide at 0.2 wt% to 0.5 wt% and a synthetic silica antiblock at 0.1 wt% to 0.3 wt% are compounded into the sheet or added as masterbatch. Excessive slip above 0.8 wt% can reduce heat-seal bond strength and cause visible haze. Finished products include cosmetic display trays, toy blisters, flashlight clamshells, and hardware accessory inserts. REACH compliance requires SVHC content below 0.1 wt%; EU Packaging Directive 94/62/EC limits the sum of lead, cadmium, mercury, and hexavalent chromium to 100 ppm by weight. Published data for this specific configuration is limited for long-term stress crack resistance under high humidity; therefore, secondary packaging should avoid sustained compression above PLA’s glass transition region of approximately 55 °C to 60 °C.

    When Hinged Retail Containers Are Produced Without Post-Form Annealing

    For hinged clear retail containers produced from Revode 110, creasing and folding replace a true living hinge because unmodified PLA exhibits brittle fracture after repeated flexing below 25 °C. If a living hinge is required, the formulation must include a flexible bio-based or biodegradable copolyester at 5 wt% to 15 wt%; this reduces clarity and may require migration and compostability revalidation. The sheet is extruded at 0.4 mm to 0.8 mm and formed on shuttle or steel-rule-die equipment with sheet surface temperatures of 80 °C to 95 °C to avoid tearing at fold lines. Post-form annealing is deliberately avoided for transparent retail containers because holding formed clear PLA at 65 °C to 80 °C encourages spherulitic haze and dimensional warpage. Finished articles include clear gift boxes, display cubes, jewelry trays, and point-of-sale trays. Compliance is non-food; REACH and general packaging regulations apply, and if the container is marketed as compostable, the entire assembly—including adhesives and paperboard—must meet EN 13432. The operational boundary is strict: these containers cannot be stacked in hot warehouses above 50 °C because wall deflections exceed visual tolerance.

    Because cup lids are trimmed at high speed after pressure forming, sheet gauge control across the web must be held within ±0.02 mm to prevent plug-assist binding and rim-curl cracking. Food-service cold cup lids from Revode 110 are produced from 0.25 mm to 0.50 mm sheet, while cold drink cups use 0.50 mm to 0.70 mm sheet. The thermoforming line runs at 25 to 40 cycles/min; the sheet surface temperature is set at 100 °C to 115 °C and the rim-curl station requires a core sheet temperature above 95 °C. When sheet moisture exceeds 300 ppm or when the center of the web is below 90 °C, edge cracking appears as micro-tears in the curled rim. Finished products are cold drink cups, strawless lids, and sampler portion cups. Food-contact compliance follows EU (EU) No 10/2011 with overall migration below 10 mg/dm² and the supplier’s FDA Food Contact Notification. The product is limited to cold service; filling with liquids above 50 °C deforms the cup rim and eliminates lid seal.

    Free Quote

    Competitive Revode 110 Thermoforming Sheet Extrusion Polylactic Acid Resin prices that fit your budget—flexible terms and customized quotes for every order.

    For samples, pricing, or more information, please contact us at +8618136850665 or mail to admin@ascent-chem.com.

    We will respond to you as soon as possible.

    Tel: +8618136850665

    Email: admin@ascent-chem.com

    Inquiry

    Get Free Quote of Ascent Petrochem Holdings Co., Limited

    Flexible payment, competitive price, premium service - Inquire now!

    Certification & Compliance
    More Introduction
    Revode 110 Thermoforming Sheet Extrusion Polylactic Acid Resin is a biobased aliphatic polyester grade specified for cast-sheet extrusion and subsequent plug-assisted pressure forming of thin-wall rigid articles. The resin is supplied as pellets and belongs to the manufacturer’s sheet-extrusion series; the model designation distinguishes it from injection-moulding and fibre-grade PLA through controlled melt mass-flow rate and elevated melt strength. Polylactic acid is derived from lactic acid, and the rheological behaviour, crystallisation rate, and forming response of Revode 110 are influenced by D-lactide content, residual moisture, and thermal exposure. Specification values such as melt mass-flow rate under ISO 1133-1:2022 at 190 °C and 2.16 kg, density under ISO 1183-1:2019, and water content under ISO 15512:2019 must be read from the supplier’s batch certificate because secondary literature does not provide reliable lot-specific data for this grade. Published data for unfilled PLA sheet-extrusion grades generally place density at 1.24 g/cm³ to 1.26 g/cm³, tensile yield strength at 45 MPa to 65 MPa under ISO 527-2, elongation at break at 2% to 6%, and Vicat softening temperature at 55 °C to 60 °C under ISO 306 method A50. The melt mass-flow rate for sheet grades is typically below 10 g/10 min; exact Revode 110 lot values are controlled by the certificate of analysis. The grade should not be assumed to match generic PLA data sheets for injection-moulding resin.

    When Moisture Control Determines Melt Stability in PLA Sheet Lines

    Hydrolysis is the dominant degradation mechanism during extrusion of PLA. If pellet moisture exceeds 250 mg/kg at the feed throat, simultaneous heat and water in the barrel cleaves ester linkages and produces lower molecular weight fragments. The resulting increase in melt flow rate and loss of melt strength appears on the line as sheet sag, edge neck-in, microvoids in formed parts, and inconsistent gauge control. Pre-drying in a desiccant-wheel dryer with a dew point of -40 °C or lower is required before processing Revode 110. A set-point of 80 °C for 4 h to 6 h is typical for hopper drying, but residence time must be validated with moisture analysis. Closed-loop conveying is recommended when ambient relative humidity exceeds 60%. Hopper inlet temperature should not exceed 100 °C because pellet clumping and oxidative discolouration can occur before melting. Single-screw extruders with a barrier screw and 30:1 L/D ratio are commonly used for Revode 110 sheet lines. Barrel temperatures from 170 °C to 200 °C and die temperatures from 190 °C to 200 °C maintain melt homogeneity without excessive shear heating. Co-rotating twin-screw lines should maintain the melt temperature below 210 °C at the die probe. A melt-temperature excursion of 5 °C above the upper limit narrows the thermal stability window and accelerates lactide generation. Thermal exposure at 230 °C for more than 10 min produces yellowing, a rapid increase in melt flow rate, and reduced melt strength; during line stops the screw must be purged or the die isolated to avoid extended residence. Vacuum venting with a pressure of approximately -0.08 MPa can remove small amounts of volatile degradation products but cannot compensate for inadequately dried pellets. Moisture above 0.05% by mass at the feed throat is a processing failure condition on most sheet lines. Regrind must be dried under the same conditions as virgin resin and is typically limited to 25 wt% to 30 wt% of the feed stream for food-contact sheet because hydrolysed regrind lowers intrinsic viscosity and reduces dart impact of formed parts. From the polishing stack, the amorphous sheet is transferred to a thermoformer either inline or offline. Infrared ceramic or quartz heaters raise the sheet surface temperature to 90 °C to 110 °C; for a 0.35 mm monolayer sheet, the practical forming band is approximately 5 °C wide when high-speed matched-metal trim is used. Below 85 °C the sheet fractures at the plug-assist contact point. Above 115 °C the material develops thermal crystallinity, producing haze, out-of-register trim, and dimensional instability. Plug temperature is maintained between 80 °C and 100 °C, while mould temperature is typically held at 30 °C to 60 °C. Plug materials such as syntactic foam or PEEK reduce localised heat loss and improve wall-thickness uniformity. Unfilled Revode 110 sheet is typically thermoformed into berry punnets, salad bowls, bakery punnets, deli trays, transparent lids, and consumer-goods blisters. The material is not specified for hot-fill, retort, or microwaveable food containers unless the formed part is annealed to increase crystallinity. For industrial trays and electronics packaging, dimensional repeatability and lower thermal processing input are the primary criteria. Steel-rule die cutting is conducted at room temperature; if edge cracking occurs, preheating the trim die to 30 °C to 50 °C reduces fracture. Avoid contact with alkaline cleaning solutions above pH 9 because PLA undergoes surface hydrolysis and stress cracking.

    Does Revode 110 Occupy a Separate Thermoforming Niche from Injection PLA, PET, and Filled PLA?

    Injection-moulding PLA grades are formulated for high flow and thin-wall filling, with melt mass-flow rate values commonly above 15 g/10 min under ISO 1133-1:2022. Such grades do not maintain a stable sheet web between the die and polishing stack. Revode 110 is controlled toward a lower MFR and higher melt strength, which permits sag resistance during heating and clamping. Because of that lower flow, Revode 110 may not fill thin-wall injection moulds and should not be substituted into injection-moulding specifications without rheological verification. Polyethylene terephthalate sheet is dried at higher temperatures and processed at melt temperatures from 270 °C to 300 °C. PET provides higher heat resistance, better oxygen barrier, and broader thermoforming behaviour. The density of PET is approximately 1.38 g/cm³, while unfilled PLA sheet falls between 1.24 g/cm³ and 1.26 g/cm³. Revode 110 is not a drop-in PET replacement for hot-fill packaging, retort applications, or high-barrier modified-atmosphere trays. Oxygen transmission of PLA-based sheet must be verified under ASTM D3985 when barrier-critical shelf life is claimed. PET lines must be purged thoroughly before switching to PLA because residual PET at 270 °C will degrade PLA rapidly. Mineral-filled PLA grades contain talc, calcium carbonate, or cellulosic fibre to raise flexural modulus and reduce formulation cost. Those grades produce opaque sheet and may exhibit reduced thermoformed gloss, lower tear resistance, and narrower melt extensibility. Revode 110 is specified where transparency and renewable-carbon content are required. The choice between unfilled and filled PLA should be made using tensile data under ISO 527-2, flexural data under ISO 178, and Charpy impact data under ISO 179-1; published data for this specific comparison is limited and should be confirmed on the target line. Annealing can alter the thermal performance of Revode 110 formed parts. Amorphous PLA exhibits Vicat softening near 55 °C to 60 °C under ISO 306 method A50. Formed parts may be annealed in jigs at 100 °C to 120 °C for 30 min to 60 min to increase crystallinity and raise Vicat softening above 120 °C, but this step reduces clarity and adds anisotropic linear shrinkage of approximately 2% to 3%. Mould dimensions must compensate for that shrinkage. The D-lactide content of Revode 110 controls crystallisation rate; lower D-isomer content accelerates crystallisation but narrowens the annealing window. Users should verify D-lactide content against the certificate of analysis before setting annealing cycles.

    Regulatory Evaluation of Thermoformed Revode 110 Articles

    European food-contact compliance for finished Revode 110 articles is evaluated under Regulation (EU) No 10/2011. The overall migration limit for plastic food-contact materials is 10 mg/dm² of food-contact surface; specific migration limits apply to additives, monomers, and oligomers. Compliance is a finished-article property and requires migration testing on representative articles, not resin pellet certification alone. For United States applications, polylactic acid food-contact status is not covered by a generic 21 CFR 177 listing; the supplier must confirm whether Revode 110 is covered by an effective FDA food-contact notification for the intended food types and use conditions. Industrial and electrical applications may require REACH Article 33 declarations for substances of very high concern above 0.1% w/w and RoHS 2011/65/EU screening under IEC 62321. Revode 110 is not flame-retardant, UV-stabilised, or impact-modified unless specifically ordered with those additives. Additive packages can alter regulatory compliance and must be disclosed by the supplier. Compostability claims for Revode 110 packaging cannot be inferred from the resin alone. Certification to EN 13432 or ASTM D6400 is a finished-article assessment that includes disintegration, biodegradation, heavy-metal limits, and ecotoxicity testing. Use of non-certified colorants, adhesives, labels, or coating layers can invalidate industrial compostability declarations even if the base resin is certified.
    Standard or regulationTest method or clauseRelevance to Revode 110
    ISO 1133-1:2022Method A, 190 °C, 2.16 kgMelt mass-flow rate for incoming resin and regrind control
    ISO 1183-1:2019Immersion methodDensity for yield and fill-weight calculation
    ISO 15512:2019Karl Fischer titrationPellet moisture before drying and after drying
    ISO 306A50 methodVicat softening point of amorphous or annealed sheet
    ISO 527-2Type 1B specimenTensile acceptance of sheet and formed parts
    ISO 179-1Charpy edgewiseImpact resistance of formed parts
    Regulation (EU) No 10/2011Overall migration, 10 mg/dm²Food-contact compliance required for packaging
    ASTM D3985Coulometric sensorOxygen transmission for barrier-critical packaging
    EN 13432 / ASTM D6400Disintegration, biodegradation, ecotoxicityFinished-article compostability certification
    Top