| HS Code | 333883 |
| Product Name | Hycail HM 1011 Clear General Purpose Extrusion/Thermoforming Polylactic Acid |
| Chemical Family | Polylactic Acid (PLA) |
| Grade | General Purpose Extrusion/Thermoforming |
| Appearance | Clear |
| Form | Pellets |
| Density | 1.24 g/cm³ |
| Melt Flow Rate | 10-14 g/10 min (190°C/2.16 kg) |
| Melting Point | 150-160 °C |
| Glass Transition Temperature | 55-60 °C |
| Tensile Strength | 50 MPa |
| Tensile Modulus | 3.5 GPa |
| Elongation At Break | 3% |
| Flexural Modulus | 3.5 GPa |
| Notched Izod Impact | 2 kJ/m² |
| Heat Deflection Temperature | 55 °C at 0.45 MPa |
| Vicat Softening Point | 60 °C |
| Biodegradability | Yes |
| Compostability | Yes |
As an accredited Hycail HM 1011 Clear General Purpose Extrusion/Thermoforming Polylactic Acid factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Hycail HM 1011 Clear General Purpose Extrusion/Thermoforming Polylactic Acid is supplied in 25 kg moisture-barrier lined cardboard boxes or bags. |
| Container Loading (20′ FCL) | Container Loading (20′ FCL): Hycail HM 1011 Clear General Purpose Extrusion/Thermoforming Polylactic Acid, palletized and secured for safe shipment. |
| Shipping | Hycail HM 1011 Clear General Purpose Extrusion/Thermoforming Polylactic Acid ships as non-hazardous solid resin pellets in sealed moisture-barrier bags, boxes, fiber drums, or bulk bags. It requires no dangerous goods classification. Store cool and dry, away from direct sunlight, heat, and moisture; standard handling applies. |
| Storage | Store Hycail HM 1011 Clear General Purpose Extrusion/Thermoforming Polylactic Acid in a cool, dry, well-ventilated area, away from direct sunlight, heat, ignition sources, and moisture. Keep original containers sealed, on pallets, off the floor. Protect from humidity to prevent hydrolysis; use desiccants if needed. Rotate stock first-in/first-out. Avoid temperatures above 30°C and prolonged humid storage. |
| Shelf Life | Shelf life: typically 12 months in unopened original packaging under cool, dry conditions, away from heat, moisture, and direct sunlight. |
Rigid food packaging sheet extrusion and thermoforming from Hycail HM 1011 begins with moisture management rather than thermal adjustment. The granulate is dried in a desiccant-bed dryer at 80 °C for 4 h to a residual moisture below 250 ppm measured by Karl Fischer titration per ISO 15512:2019. A single-screw extruder with L/D 30:1 and a chromium-plated barrier screw, equipped with vacuum venting near the metering zone, is profiled from 180 °C in zone 1 to 205 °C at the adapter, with the feed throat maintained at 30–40 °C. The melt is screened through a 200-mesh pack and delivered through a coat-hanger die with a lip gap set at 0.8–1.2 times the target sheet thickness, while melt pressure at the die inlet is held between 80 bar and 120 bar. The polished roll stack is held at 40–60 °C; lower roll temperatures preserve amorphous clarity but increase residual stress, while higher temperatures promote edge curl and blocking at the winder. Sheet in the 0.25–1.00 mm range is thermoformed on plug-assisted positive-pressure machines at a sheet surface temperature of 90–110 °C, mold temperature of 25–40 °C, and forming pressure of 3–6 bar. The processing window is narrow: melt temperatures above 220 °C accelerate random chain scission and lactide reformation, while surface temperatures below 90 °C increase stress whitening at corner draw ratios above 3:1. Regrind ratios of 10–20 wt% may be blended with virgin pellets, but repeated heat histories above 220 °C reduce melt stability and increase gel counts. When sheet-to-sheet blocking occurs on stack winders, a PLA-compatible slip/antiblock masterbatch at 0.5–2.0 wt% is dosed at the feed throat. Food-contact compliance is not automatic: converters must obtain a grade-specific Food Contact Statement and verify overall migration under Regulation (EU) No 10/2011 using EN 1186-1:2002 with 3 % (w/v) acetic acid and 10 % (v/v) ethanol for aqueous foods, and 20 % (v/v) ethanol or D2 simulant for fatty foods. For US use, the specific food contact notification must cover the intended condition of use; 21 CFR 174.5 alone is insufficient. End products include clamshell containers, bakery trays, fresh-cut produce punnets, and deli lids.
In transparent cold beverage cup and portion container production, vertical or horizontal form-cut-stack lines with a plug-assist thermoforming station govern the output. The critical process variable is sheet sag: at a surface temperature of 95–115 °C, PLA sheet loses melt strength non-linearly, so the time between the oven exit and forming station must be kept below 1.5 s on machines with a 600 mm forming width. Plug materials of syntactic foam or filled nylon are maintained at 70–80 °C to prevent chill marks; plug displacement is set to 70–85 % of cavity depth before final pressure application at 4–6 bar. Lip roll consistency is achieved by post-forming infrared edge heaters that raise the rim zone to 120–130 °C for 0.8–1.2 s before a cold curl tool folds the rim. Wall thickness in the sidewall is checked by a Hall-effect thickness gauge on every 50th cycle, with a coefficient of variation target below 5 %. For additive dosing, 0.2–0.5 wt% of an amorphous PLA-compatible nucleating agent may be metered into the throat when hot-fill simulation trials reveal excessive post-forming shrinkage after exposure to 60 °C water. Tensile yield and elongation are measured per ASTM D638-14, while Vicat softening temperature is determined per ASTM D1525-17; comparable extrusion PLA grades typically show Vicat softening values of 55–60 °C, and the lot certificate supersedes comparators. Food-contact migration testing uses simulant A (10 % ethanol) and simulant B (3 % acetic acid) under EN 1186-1:2002. End products include cups from 120 ml to 500 ml, portion containers, and cup lids.
Non-food blister packs and retail display trays made from clear PLA sheet require tooling modifications to avoid stress whitening at high draw ratios. The forming window is narrower than PVC or PETG; a sheet surface temperature of 100–110 °C is required for a cavity draw ratio of 3:1, and the plug-assisted pre-stretch must not exceed 60 % of the final cavity depth before high-pressure forming at 6–8 bar. Aluminum molds are water-cooled to 20–30 °C to freeze the amorphous orientation before cold crystallization can develop haze. Corner radii below 2 mm at a draw ratio above 2.5:1 produce visible stress whitening; radii of 4–6 mm or a stepped plug profile are used instead. For anti-static requirements in electronics trays, a non-amine antistatic masterbatch at 1.0–3.0 wt% can be compounded into the sheet, but amine-based antistats must be avoided because they accelerate hydrolytic degradation at processing temperatures. The finished blister is tested for haze per ASTM D1003-13 and for tensile impact of the formed wall per ISO 8256-1:2004. Compliance for non-food consumer goods includes REACH SVHC screening and RoHS Directive 2011/65/EU for electrical/electronic trays. End products include cosmetic clamshells, electronics cushion trays, and stationery display blisters.
| Parameter | Standard | Typical acceptance window |
|---|---|---|
| Residual moisture after drying | ISO 15512:2019 | <250 ppm |
| Melt mass-flow rate | ISO 1133-1:2022 | Report against lot certificate |
| Tensile strength at yield, elongation | ASTM D638-14 / ISO 527-2:2012 | Report against lot certificate |
| Vicat softening temperature | ASTM D1525-17 | Report against lot certificate |
| Haze of flat sheet | ASTM D1003-13 | Report against lot certificate |
| Overall migration, food contact | Regulation (EU) No 10/2011 / EN 1186-1:2002 | <10 mg/dm² |
| Industrial compostability of finished article | EN 13432:2000 / ASTM D6400-19 | Pass for article geometry |
On roll-fed form-fill-seal lines designed for amorphous PET sheet, conversion to Hycail HM 1011 cannot proceed by direct substitution because the sealing station must first be retuned. The extruded sheet, typically 0.20–0.40 mm thick, is fed through a preheating zone that brings the sealing area to 120–140 °C; PLA has a narrower seal initiation window than PETG, and jaw dwell times of 0.5–1.2 s at 3–5 bar are used. Seal strength is measured per ASTM F88/F88M-21 in peel mode; minimum acceptance values are set by the packer's distribution environment, commonly in the range 10–20 N/15 mm for dry goods. Because PLA sheet blocks on the unwind if the roll surface exceeds 35 °C, accumulators and dancer rolls must be shielded from oven radiation, and an anti-blocking masterbatch at 0.5–1.0 wt% is often used. The material is not suitable for high-moisture or oxygen-sensitive products unless a barrier coating is applied; uncoated sheet is assigned to dry, short-shelf-life goods. End products include single-serve confectionery packs, hardware part packs, and disposable sampling trays.
Because hydrolysis rather than thermal oxidation dominates failure in humid greenhouse environments, thermoformed propagation trays made from clear PLA sheet are limited to short-cycle germination and young plant handling. The hydrolysis risk dominates: PLA at 0.25–0.50 mm wall thickness loses impact strength when stored above 60 % relative humidity at 4 °C for more than 4–6 weeks, so the application is not recommended for long-term nursery containers. The trays are formed at a sheet surface temperature of 95–105 °C and mold temperature of 30–40 °C, with drain holes punched after forming when the web is still at 45–55 °C to reduce micro-cracking at hole edges. An impact modifier derived from a PLA-compatible aliphatic polyester can be compounded at 2–5 wt% to improve hole-punching toughness, but tensile modulus drops and the sheet becomes more difficult to trim cleanly. Industrial compostability of the finished tray is not inferred from resin certification alone; it requires article-level testing according to EN 13432:2000 or ASTM D6400-19, including disintegration at 58 °C and ecotoxicity assessment. End products include plug trays, cucumber and tomato seed trays, and humidity-dome bases.
Non-sterile dental and ophthalmic device trays can be thermoformed from clear PLA sheet only after the packaging engineer confirms that the medical device does not require long-term sterile barrier performance. The formed tray must meet ISO 11607-1:2019 for packaging system design, but PLA's moisture vapor transmission and oxygen permeability are higher than PET-G at equivalent thickness, so shelf-life modeling per ASTM F1980-21 for accelerated aging is required. The sheet is extruded at 0.40–0.70 mm and thermoformed at a surface temperature of 100–115 °C with mold temperatures of 25–35 °C to maintain transparency for visual inspection of the device. If the tray is sealed to a Tyvek lid, seal parameters are typically 115–135 °C at 0.8–1.6 s dwell and 3–5 bar; seal strength is tested per ASTM F88/F88M-21, but cohesive failure of the PLA flange may occur below 0.30 mm thickness. Sterilization limits are critical: gamma irradiation at 25 kGy causes measurable chain scission in PLA, and ethylene oxide can plasticize the tray; hydrogen peroxide gas plasma may be considered if the tray geometry is validated for condensate drainage. The use of 0.5–1.0 wt% of a PLA-compatible processing aid during extrusion is permitted only after its surface residue profile is reviewed under ISO 10993-5:2009 for cytotoxicity. Published data for Hycail HM 1011 in terminally sterilized medical packaging is limited, so the above values are validation starting points and must be confirmed on the actual forming and sealing line. End products include dental bur trays, contact lens insertion trays, and single-use ophthalmic surgical arranging trays.
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Hycail HM 1011 Clear General Purpose Extrusion/Thermoforming Polylactic Acid is an amorphous, high-clarity polylactide grade supplied as pellets for flat-die sheet extrusion and subsequent thin-gauge thermoforming. The designation HM 1011 identifies a general-purpose molecular weight distribution tuned for melt strength, sheet gauge stability, and optical clarity; it is not a nucleated high-heat compound and is not an impact-modified blend. As an aliphatic polyester derived from lactic acid, the material is subject to hydrolytic chain scission at melt temperature if residual moisture exceeds the supplier limit. The processing and property values compiled below are drawn from supplier technical literature and standard polymer engineering practice; lot-specific certificates of analysis control actual release limits for specific production campaigns.
Before extrusion, pellets must be dried in a desiccant dryer at 80 °C for 4 h to a residual moisture content below 250 ppm. Drying air with a dew point of -40 °C or lower and airflow of 3.7 m³/h per kg/h pellet throughput are required. If dried pellets remain in open hoppers for more than 1 h at ambient relative humidity above 60%, surface moisture re-adsorption is sufficient to produce molecular weight loss and edge curl on the sheet line. Overdrying above 100 °C causes pellet surface tack and bridging; therefore, hopper temperature setpoints above 100 °C are not recommended without continuous agitation. Moisture content should be verified by Karl Fischer titration or an equivalent calibrated moisture analyser, not by weight-loss methods alone, because PLA pellets can release volatiles that distort loss-on-drying readings.
On a single-screw extruder with 24:1 to 30:1 L/D and a barrier screw, melt temperature at the die is held at 190 °C to 210 °C. Die zone temperatures are normally 200 °C to 220 °C; polished roll stacks between 25 °C and 40 °C quench the amorphous sheet before spherulite growth occurs. The material’s melt volume-flow rate at 190 °C/2.16 kg under ISO 1133-1 falls in the range of 6 g/10 min to 10 g/10 min, providing moderate melt strength but a narrow sag window. A die gap of 1.5 to 2.5 times the target sheet thickness is used because PLA has lower melt strength than polystyrene or polyethylene terephthalate; excessive draw-down creates gauge variation and machine-direction orientation. Screen packs of 40/80/40 mesh are standard. Extruder head pressure above 250 bar indicates either insufficient melt temperature or screen blockage; sustained operation above 240 °C promotes lactide reformation, racemisation, and yellowing.
Production-scale flat-die lines have shown that melt pressure fluctuation above ±5 bar causes visible gauge bands in thin sheet. Barrel zones are profiled from approximately 170 °C at the feed throat to 200 °C at the metering zone, with the feed throat maintained below 45 °C to prevent pellet bridging. Screw speed is set to maintain a metering-zone fill factor above 80%; starved feeding above 85% fill may improve devolatilisation but reduces output stability unless controlled by a gravimetric feeder. Melt residence time above 220 °C should be minimised because thermal degradation follows a time-temperature superposition; long residence times at lower temperatures can produce the same lactide reformation as short residence times above 240 °C.
| Property | Value | Test method |
|---|---|---|
| Melt volume-flow rate, 190 °C/2.16 kg | 6–10 g/10 min | ISO 1133-1 |
| Density | 1.24 g/cm³ | ISO 1183-1 |
| Glass transition temperature | 55–60 °C | ISO 11357-2 |
| Tensile yield strength | 60 MPa | ISO 527-2/1A/50 |
| Tensile modulus | 3500 MPa | ISO 527-2/1A/1 |
| Elongation at break | 5% | ISO 527-2/1A/50 |
| Notched Charpy impact strength | 3 kJ/m² | ISO 179-1/1eA |
| Heat deflection temperature, 0.45 MPa | 55 °C | ISO 75-2/B |
| Vicat softening temperature, A50 | 58 °C | ISO 306/A50 |
| Light transmission, 1 mm plaque | 90–94% | ASTM D1003 |
| Haze, 1 mm plaque | 1–3% | ASTM D1003 |
Optical clarity in HM 1011 is process-dependent. Rapid quenching on the roll stack is required to suppress spherulite growth; roll temperatures above 40 °C or melt temperatures above 230 °C increase haze and shift transmitted colour toward yellow. Light transmission measured on 1 mm plaques under ASTM D1003 is reported in the range of 90% to 94%, with haze below 3%. The grade is not externally lubricated; therefore, surface migration during storage is minimal, and corona discharge treatment for printing or lamination should be applied at 38–44 dyn/cm for consistent surface energy. Crystalline content in the amorphous sheet should remain below 5%; crystallinity above this level produces stress whitening at thermoformed corners and dimensional instability after trimming.
Primary application formats include clear clamshell packaging, display trays, lids, cups, and thin-gauge blisters for ambient or cold-chain products. The unannealed heat deflection temperature remains below 60 °C; therefore, the material is not recommended for hot-fill containers or microwave reheating unless the part is crystallised after forming. Published data for high-speed plug-assisted forming of this specific grade is limited; the forming window is therefore defined by the measured glass transition and cold-crystallisation onset in supplier technical literature.
HM 1011 is differentiated from high-heat PLA by the absence of nucleating agents such as talc, phenylphosphonic acid zinc salt, or stereocomplex PDLA additives. High-heat grades crystallise during annealing at 100 °C to 120 °C and can achieve heat deflection temperatures above 100 °C at 0.45 MPa under ISO 75-2/B; unannealed HM 1011 remains below approximately 55 °C. Compared with impact-modified PLA, HM 1011 offers higher tensile modulus and optical clarity but lower ductility: notched Charpy impact strength measured under ISO 179-1/1eA is typically below 4 kJ/m², whereas impact-modified extrusion grades can exceed 20 kJ/m² but exhibit haze above 5% and tensile modulus below 2600 MPa.
| Property | HM 1011 | High-heat nucleated PLA | Impact-modified PLA | PETG | Test method |
|---|---|---|---|---|---|
| Density | 1.24 g/cm³ | 1.26 g/cm³ | 1.25 g/cm³ | 1.27 g/cm³ | ISO 1183-1 |
| Melt volume-flow rate, 190 °C/2.16 kg | 6–10 g/10 min | 5–8 g/10 min | 4–8 g/10 min | 8–15 g/10 min | ISO 1133-1 |
| Tensile modulus | 3500 MPa | 3600 MPa | 2600 MPa | 2100 MPa | ISO 527-2 |
| Elongation at break | 5% | 3% | 15–30% | 100–150% | ISO 527-2 |
| Notched Charpy impact strength | 3 kJ/m² | 3 kJ/m² | 20 kJ/m² | 15 kJ/m² | ISO 179-1/1eA |
| Heat deflection temperature, 0.45 MPa | 55 °C | 95 °C after annealing | 50 °C | 70 °C | ISO 75-2/B |
| Light transmission | 90–94% | 70–85% | 85–90% | 90–92% | ASTM D1003 |
Compared with injection moulding PLA grades, HM 1011 is deliberately less fluid: its melt volume-flow rate of 6–10 g/10 min at 190 °C/2.16 kg is lower than typical injection moulding PLA grades at 15–30 g/10 min. This lower fluidity is required because sheet extrusion depends on melt strength to support the web from die to roll stack; an injection moulding grade would sag excessively and produce gauge variation. Conversely, HM 1011 is not recommended for thin-wall injection moulding because filling pressure would be higher and weld-line strength lower than with grades designed for that process.
When thin-gauge packaging tools are run above 100 °C, the amorphous sheet enters the crystallisation regime. The HM 1011 preheat window is 90 °C to 110 °C, with aluminium tooling maintained at 30 °C to 50 °C for clear parts. Tool temperatures above 60 °C cause spherulite growth, haze increase, and dimensional instability because the part shrinks as it crystallises. Forming pressures of 3 bar to 5 bar and plug assist are typical on continuous thermoforming lines; plug temperature should not exceed 80 °C, because a hot plug induces premature crystallisation on the sheet surface. After trimming, residual stress in corners can be reduced by annealing at 80 °C for 30 min, but the anneal will reduce transparency and raise heat deflection temperature because crystallinity increases. Edge trim regrind can be reintroduced at 20 wt% to 30 wt%; repeated heat histories lower melt viscosity, so higher regrind levels increase gel formation and black specks. Sheet surface temperature uniformity should be maintained within ±2 °C across the forming area, verified by infrared pyrometry, to avoid non-uniform stretching and corner thinning.
For food-contact articles, compliance must be established for the specific converted part. PLA grades of this class are commonly evaluated under EU 10/2011 for overall migration in food simulants such as 10% ethanol, 3% acetic acid, and vegetable oil; the supplier of HM 1011 must provide the relevant migration data. Under United States regulations, PLA food-contact status is typically addressed through Food Contact Notifications rather than 21 CFR 177.1520, which covers polyolefins. Industrial compostability claims must reference EN 13432 or ASTM D6400; successful degradation depends on a managed composting environment at 58 °C ± 2 °C with sufficient moisture and oxygen. HM 1011 does not degrade in ambient landfill or marine conditions. RoHS and REACH declarations must be obtained from the supplier for the specific lot, because additive packages may vary by production site.
Storage of unopened bags should be maintained at 25 °C and 50% RH or lower. If bags are opened for more than 8 h, re-drying before extrusion is mandatory. Condensation during transfer from cold storage to a warm production area must be prevented; immediate pellet feeding from an unheated silo can produce surface moisture which hydrolyses the melt. HM 1011 should not be combined with strong bases, amines, or alkaline fillers because alkaline species catalyse ester hydrolysis and molecular weight loss. Prolonged contact with ketones, esters, and aromatic hydrocarbons can swell or stress-crack the formed article, and the material is not recommended for continuous service above 50 °C in the amorphous state.