| HS Code | 278053 |
| Chemical Composition | Polylactic Acid (PLA) |
| Density | 1.24 g/cm³ |
| Melt Flow Rate | 8 g/10 min (210°C/2.16 kg) |
| Glass Transition Temperature | 55°C |
| Melting Temperature | 175°C |
| Tensile Strength | 60 MPa |
| Tensile Modulus | 3500 MPa |
| Elongation At Break | 3.5% |
| Flexural Strength | 100 MPa |
| Flexural Modulus | 3600 MPa |
| Notched Izod Impact Strength | 2.5 kJ/m² |
| Heat Deflection Temperature | 55°C (0.45 MPa) |
| Vicat Softening Temperature | 60°C |
| Biobased Carbon Content | 100% |
| Compostability | Certified compostable (EN 13432, ASTM D6400) |
As an accredited Luminy Polylactic Acid (PLA) LX175 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Luminy Polylactic Acid (PLA) LX175 typically comes in 25 kg moisture-proof bags or 1,000 kg bulk bags on pallets. |
| Container Loading (20′ FCL) | 20′ FCL loading of Luminy PLA LX175: 25 kg bags, palletized, shrink-wrapped, evenly stacked/secured in dry container, max payload. |
| Shipping | Luminy Polylactic Acid (PLA) LX175 is shipped as non-hazardous solid polymer pellets in moisture-barrier bags, lined cartons, or bulk containers. Store and transport dry, cool, ventilated, away from direct sunlight, heat, and moisture. It is not classified as dangerous goods; follow standard regulations and supplier SDS. |
| Storage | Store Luminy Polylactic Acid (PLA) LX175 in a cool, dry, well-ventilated area away from heat, moisture, direct sunlight, ignition sources, and incompatible materials such as oxidizers. Keep containers tightly sealed to prevent moisture uptake. Recommended: 10–30 °C, low humidity (<50% RH), good air circulation. Follow manufacturer guidance, rotate stock first-in, first-out, and inspect containers regularly. Do not store near food or beverages. |
| Shelf Life | Luminy PLA LX175 typically has a 12-month shelf life when stored dry, sealed in original packaging, and kept below 30°C. |
Luminy PLA LX175 is processed on all-electric injection moulding machines of 120–350 tonnes clamp force, with barrel temperature zones set between 170 °C (rear) and 210 °C (nozzle), for thin-wall food-contact serviceware including cold-beverage cups with wall thickness from 0.55 mm to 0.90 mm. Pre-conditioning of granules in desiccant dryers operating at 60–80 °C for 4–6 h with a dew point at or below −40 °C is non-negotiable: residual moisture in excess of 250 ppm induces hydrolytic chain scission during plastication, evidenced by splay marks radiating from the gate, a reduction in injection pressure demand of 10–20% at constant fill speed within a barrel residence time of 5–8 min, and a measurable fall in notched Izod impact strength below the 2.5 kJ/m² baseline specified under ISO 180/1A. The melt flow rate of LX175, reported in the 3–6 g/10 min band at 210 °C under 2.16 kg load (ISO 1133-1:2022), positions the grade for thin-wall flow while retaining melt strength sufficient for cutlery fill across 16–32 cavity tooling; platen parallelism of ≤ 0.05 mm per 100 mm platen width is advised because the processing window is bounded by thermal degradation onset at approximately 230 °C and incomplete plastication below 175 °C. The nucleating system in the LX series accelerates isothermal crystallisation once cavity wall temperature exceeds 90 °C, permitting post-mould annealing at 100–110 °C for 20–30 min to elevate heat deflection temperature (0.45 MPa, ISO 75-2/B) from an as-moulded value of approximately 55 °C to above 90 °C; this step is required for hot-beverage lid applications but imposes linear shrinkage of 1.2–1.8% that must be compensated in cavity dimensioning. Formulation practice for LX175 in serviceware consists of 96–98 wt% virgin resin blended with 2–4 wt% of a PLA-carrier masterbatch; the inclusion of non-PLA polymeric additives above 5 wt% invalidates the organic recovery claim under EN 13432:2000 and triggers re-qualification at an accredited certification body. Food-contact compliance for EU markets is established through Commission Regulation (EU) No 10/2011 as amended by Regulation (EU) 2020/1245, with overall migration limits of 10 mg/dm² under OM2 conditions; US market clearance is carried via the resin manufacturer's Food Contact Notification, and buyers are directed to reference the specific FCN number supplied on the letter of conformity. Terminal articles produced from LX175 in this category include cold-drink cups, disposable cutlery sets, delicatessen containers with hinged lids, and hot-beverage lids that undergo the annealing cycle described above.
Within the cosmetic packaging sector, the injection moulding of LX175 into airless pump actuators, foundation compact bases, lipstick tube sleeves, and 30–50 ml cream jars routinely generates post-industrial regrind from runner systems and start-up purge that represents between 8% and 15% of total shot weight. Biobased carbon content is measured according to ASTM D6866-22 (Method B, AMS) and remains unaffected by mechanical recycling because the radiocarbon signature is molecular rather than process-history-dependent; however, two processing risks accompany regrind inclusion above 10 wt%: cumulative thermal history reduces melt viscosity by up to 20% through progressive chain scission, and the nucleating agent's crystallisation kinetics are altered, producing parts with higher haze when measured per ASTM D1003-21. Cosmetic packaging contact with aggressive formulation constituents — ethanol, benzyl alcohol, and certain ester-based fragrance carriers — can induce environmental stress cracking (ESC) in PLA articles subjected to hoop stress from metal inserts or snap-fit closures; chemical resistance screening per ISO 175:2010 is therefore recommended prior to production release, and published data for LX175 specifically in ethanol-rich cosmetic matrices is limited, so validation must be conducted on the finished component geometry rather than extrapolated from tensile bars. The formulation approach for decorative cosmetic packaging pairs 95–100 wt% LX175 with 0–5 wt% of colour masterbatch; where high-gloss black or deep red components are specified, 2–3 wt% of a PLA-compatible pigment masterbatch achieves sufficient opacity without exceeding the 5 wt% additive ceiling that preserves industrial compostability claims under EN 13432:2000. Downstream manufacturing involves injection moulding on 60–180 tonne hydraulic or all-electric presses with polished cavity surfaces achieving SPI A-2 gloss finish; surface energy of moulded LX175 ranges from 38 to 42 mN/m (DIN 55660-2), necessitating inline corona treatment at 1–1.5 kW per 300 mm electrode width or plasma pre-treatment to raise surface energy above 48 mN/m before pad printing or hot-foil stamping of brand elements. Terminal articles in this sector are regulated under Regulation (EC) No 1223/2009 for cosmetic products, where packaging must not react with the formulation, and under REACH (Regulation (EC) No 1907/2006) with the polymer exemption stated at Article 2(9); a declaration of conformity citing batch-specific migration data under aqueous simulant per EU 10/2011 is typically issued by the moulder to the brand owner.
Moulded in ISO 14644-1 Class 8 or Class 7 cleanrooms, single-use medical device components fabricated from LX175 — luer lock caps, pipette tip racks, diagnostic cartridge housings, and surgical instrument handles — are produced under validated processes documented within an ISO 13485:2016 quality management system, where each lot is accompanied by a device master record and batch release testing. Sterilisation compatibility constitutes the principal processing conflict in this sector: ethylene oxide (EtO) processing at 37–55 °C with gas exposure times of 2–6 h and subsequent aeration is the preferred modality for PLA because molecular weight retention after a standard EtO cycle typically remains above 90% of the as-moulded value; gamma irradiation above 25 kGy produces yellowing quantified by a yellowness index increase exceeding 5 units (ASTM E313-20) and embrittlement characterised by a 30–50% reduction in elongation at break after a 30 kGy dose, while steam sterilisation at 121 °C is categorically incompatible with LX175 because the glass transition temperature of 55–60 °C is exceeded and deformation under load occurs. The formulation practice for medical LX175 components is 100 wt% virgin resin with zero regrind inclusion because ISO 13485 process validation protocols generally prohibit post-industrial recycled material without full re-qualification of biocompatibility per ISO 10993-1:2018, which requires cytotoxicity testing (ISO 10993-5:2009) and, for patient-contacting devices, sensitisation and irritation endpoints (ISO 10993-10:2010). Downstream production equipment for this sector requires all-electric machines of 35–100 tonnes with closed-loop injection control capable of shot-to-shot weight repeatability of ±0.1%; mould temperatures are held at 25–40 °C to retain transparency, and cycle times for 96-cavity pipette tip racks run from 12 to 18 s depending on wall section. Terminal product types in this application cluster include single-use surgical instrument handles, pipette tip inserts, microcentrifuge tube racks, and diagnostic device housings that fall under Class I device rules of Regulation (EU) 2017/745; the corresponding technical documentation must address polymer stability, sterilisation compatibility, and extractables screening under ISO 10993-18:2020 where patient contact duration exceeds transient classification.
| Application scenario | Primary regulatory reference | Test method designation | Threshold / limit |
|---|---|---|---|
| Food-contact serviceware | Regulation (EU) No 10/2011, amended by (EU) 2020/1245 | EN 1186-1:2002 overall migration | < 10 mg/dm² |
| Food-contact serviceware | EN 13432:2000 | ISO 14855-1:2012 controlled composting | ≥ 90% biodegradation in 180 days |
| Cosmetic packaging | Regulation (EC) No 1223/2009 | ISO 175:2010 chemical resistance | No visible attack after 7 days |
| Medical device components | ISO 10993-1:2018 / ISO 13485:2016 | ISO 10993-5:2009 cytotoxicity | Cytotoxicity grade ≤ 2 |
| Beverage closures | EU food law tamper-evidence provisions | ASTM D3198-97(2021) | Removal torque 1.5–2.5 N·m |
| Electronics enclosures | UL 94 / RoHS Directive 2011/65/EU | UL 94 flammability test | HB at 1.5 mm and 3.0 mm |
| Agricultural fasteners | No mandatory EU harmonised standard | ISO 17556:2019 soil biodegradation | CO₂ evolution per protocol |
At 23 °C and 50% relative humidity, injection-moulded LX175 caps of 28 mm and 38 mm finish diameters, produced on 96-cavity high-speed moulds with cycle times of 8–12 s, exhibit initial removal torque values between 1.5 and 2.5 N·m when tightened to 1.2–1.8 N·m application torque, measured per ASTM D3198-97 (Reapproved 2021). The nucleated crystallisation behaviour of the LX series confers the dimensional precision required for continuous-thread closure geometry — roundness deviation below 0.15 mm on the thread crest — but the elongation at break of approximately 4% (ISO 527-2/1A) imposes a crack propagation risk at stress concentrations in tamper-evident bridge segments, a failure mode observed on production lines when ejection forces exceed 6–8 kN per cavity and insufficient draft angles on the tamper band create tensile stress during part removal. Hot-fill processes are excluded from this application family: the as-moulded heat deflection temperature of approximately 55 °C at 0.45 MPa (ISO 75-2/B) cannot accommodate filling temperatures above 60 °C without thread deformation, and carbonated beverage closures are similarly excluded due to creep-induced loss of seal force over shelf life. Formulation for closure applications typically modifies LX175 with 1–3 wt% of an erucamide or oleamide slip agent delivered via a PLA-carrier masterbatch, reducing the coefficient of friction to below 0.3 (ASTM D1894) for cap-on-bottle torquing and preventing closure jamming in bulk feeding systems; anti-static additive inclusion at 0.5–1 wt% is advised where vision inspection systems rely on non-contact orientation and particulate attraction interferes with sensor readings. Process settings for this sector demand melt temperatures of 200–215 °C to fill long flow path thread geometries and back pressure of 10–15 bar to homogenise slip agent dispersion without exceeding 8 min residence time at temperature, beyond which ester bond thermal degradation accelerates and mould deposit formation on cavity vents increases. Terminal products include 28 mm and 38 mm flat-top closures for still water and juice bottles, 30/25 mm linered caps for dairy-based beverages in chilled distribution, and tamper-evident bands that satisfy the visual evidence requirements of EU food law without separate insert moulding.
Electronic enclosure applications for LX175 — router housings, laptop keyboard keycaps, and identity card reader frames — face a dual constraint: UL 94 HB flammability classification at 1.5 mm and 3.0 mm thicknesses is attainable without halogenated additives, but the unannealed heat deflection temperature of approximately 55 °C (0.45 MPa, ISO 75-2/B) precludes deployment in zones where continuous service temperature exceeds 45 °C unless a post-mould crystallisation anneal at 95–105 °C for 30–60 min is applied, which raises HDT to above 80 °C but reduces dimensional accuracy by 1.2–1.8% and converts the material from transparent to opaque. Formulation practice for LX175 in electronics diverges from the food-contact and medical sectors: 85–90 wt% virgin LX175 is frequently blended with 10–15 wt% of a bio-based impact modifier such as poly(butylene succinate) (PBS) or poly(butylene adipate-co-terephthalate) (PBAT) to raise notched Izod impact strength from the homopolymer baseline of approximately 2.5 kJ/m² to 6–10 kJ/m² (ISO 180/1A), a modification that sacrifices tensile modulus from approximately 3,500 MPa toward 2,000–2,400 MPa and forfeits transparency; this blend strategy addresses drop-test failures observed on production lines when unmodified LX175 parts passed UL 94 testing but cracked under 0.5 m drop impact during final assembly. Downstream production equipment for keyboard keycaps requires precision injection moulds of 16–32 cavities with hot-runner systems capable of maintaining gate temperature within ±2 °C, because flow-line-induced haze in LX175 nucleated melts appears when cavity fill velocity falls below 200 mm/s; cycle times of 15–25 s are typical for wall sections of 1.2–2.0 mm. The regulatory framework for LX175 electronic parts includes the RoHS Directive 2011/65/EU (no restricted substances present in the unfilled resin), REACH Regulation (EC) No 1907/2006 with the polymer exemption at Article 2(9), IEC 62368-1:2018 for AV/ICT equipment safety applicable to the finished device, and ISO 11469:2016 for polymer part marking; where ecolabels demand renewable content, ASTM D6866-22 radiocarbon testing is specified to verify biobased carbon fraction of 70–85% in the blended formulation. Terminal products are limited to low-thermal-load enclosures, keyboard keycaps, card reader housings, and router top covers with ambient service temperatures not exceeding 40 °C in the unannealed state.
| Parameter | Food-contact serviceware | Cosmetic packaging | Medical components | Beverage closures | Electronics | Agricultural |
|---|---|---|---|---|---|---|
| Melt temperature | 175–210 °C | 180–205 °C | 180–205 °C | 200–215 °C | 180–205 °C | 180–205 °C |
| Mould temperature (amorphous) | 25–40 °C | 25–40 °C | 25–40 °C | 25–35 °C | 25–40 °C | 25–40 °C |
| Mould temperature (crystallised) | 90–110 °C | Not specified | Not specified | Not specified | 95–105 °C | Not specified |
| Cycle time range | 8–20 s | 15–30 s | 12–18 s | 8–12 s | 15–25 s | 10–20 s |
| Clamp force range | 120–350 t | 60–180 t | 35–100 t | 150–350 t | 80–200 t | 50–200 t |
In vineyard and nursery operations where single-season polymer components are specified, LX175 is injection-moulded into vine shoot positioning clips, plant labeling tags, and seed tray cell inserts using formulations of 98–100 wt% virgin resin, with 1–2 wt% carbon black masterbatch added only where UV screening is required to delay photodegradation-induced embrittlement during a single growing season. The degradation pathway for LX175 buried in agricultural soil is governed by ISO 17556:2019 (aerobic biodegradation in soil), which measures CO₂ evolution under controlled conditions of 20–25 °C and 40–60% water-holding capacity; published degradation data for LX175 specifically under field soil conditions is limited, and the rate observed in accelerated laboratory testing at 28 °C is not linearly extrapolatable to field service because soil microbial consortia, nitrogen availability, and moisture cycling dominate the hydrolysis window. A measurable service-life conflict arises from the mechanical property penalty of soil contact: tensile modulus retention after 6 months of soil exposure can fall below 60% of baseline as surface pitting initiates, yet the same part may remain dimensionally functional for 18–24 months in dry soil before load-bearing failure under tensile load of 2–4 N is observed. Downstream production for agricultural LX175 items utilises standard hydraulic injection machines of 50–200 tonnes with general-purpose screws; no special metallurgy is required because PLA processing temperatures of 180–205 °C do not generate corrosive gases, and tooling can be constructed from P20 or 718 steel without surface treatment. Terminal product types in this cluster include vineyard shoot positioning clips designed for single-season replacement, nursery pot label tags, seedling tray inserts for transplant automation, and greenhouse ventilation louver clips; the latter application exposes LX175 to sustained UV-A and UV-B radiation at greenhouse film-filtered levels that can reduce notched Izod impact strength by 30–50% within 4–6 months, as measured per ISO 180/1A on exposed specimens.
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Luminy Polylactic Acid (PLA) LX175 is a high-heat PLA homopolymer grade supplied by TotalEnergies Corbion for injection moulding, thermoforming, and rigid packaging conversion. The LX175 designation corresponds to a melting endotherm near 175 °C when measured by differential scanning calorimetry under ISO 11357-3:2018 at a heating rate of 10 °C/min. The thermal response is obtained by reducing D-lactic acid stereochemical defects in the L-lactide chain rather than by adding mineral filler or impact modifier. The grade is supplied as cylindrical pellets, with a density typically reported at 1.24 g/cm³ under ISO 1183-1:2019, and is used in rigid food-service ware, hot-fill packaging, and technical parts that require dimensional stability after crystallisation.
Before melt processing, LX175 must be dried in a desiccant dryer to a residual moisture content below 250 ppm. Drying at 80 °C for 4–6 h with a return-air dew point of −40 °C or lower is typical. At melt temperatures above 180 °C, residual moisture hydrolyses PLA and reduces molecular weight, causing lower melt strength, higher screw amperage variation, and increased sensitivity to mould plate-out. These effects are observed on production-scale equipment with L/D 32 twin-screw compounding lines and 25 mm single-screw injection moulding barrels. The drying step is not a conservative recommendation; it is a boundary condition for maintaining process stability.
Because high-heat PLA crystallises slowly relative to its rapid vitrification, mould temperature is the principal process variable separating LX175 from standard amorphous PLA. In a cold mould at 20–30 °C, the part freezes into a largely amorphous state, and the heat-deflection temperature remains below 60 °C under ISO 75-2:2013 method B. When the mould is held between 90 °C and 110 °C, nucleation and crystal growth proceed sufficiently before ejection to produce a semicrystalline skin and core. The heat-deflection ceiling then moves into the range of 100–150 °C, depending on part thickness, mould residence time, and post-mould annealing. This processing dichotomy is often more significant than the resin choice itself.
PLA crystallinity is governed by the stereochemical regularity of the L-lactide sequences. A lower D-isomer concentration reduces the number of chain segments excluded from the crystal lattice, permitting higher lamellar thickness and a higher equilibrium melting point. In LX175, this is observed as a shift of the main melting endotherm to approximately 175 °C and faster isothermal crystallisation at temperatures between 100 °C and 120 °C. The result is not an increase in the amorphous glass transition, which remains near 55–60 °C, but an increase in the maximum service temperature that can be reached after crystallisation. Processors comparing LX175 to standard L105 or L130 should therefore interpret heat-deflection data only in relation to mould-temperature history and not as an intrinsic, processing-independent property.
This distinction is critical when reviewing certificates of analysis. The stereochemical purity of PLA is controlled during lactide purification and polymerisation; lot-to-lot variation in residual lactide, molecular weight, and D-isomer content affects melt viscosity and crystallisation rate. A lot with a higher D-isomer concentration retains the same grade name but may crystallise more slowly and exhibit a slight depression in melting point. Published data for this specific configuration is limited; production validation should include differential scanning calorimetry under ISO 11357-3:2018 and a moulded plaque heat-deflection test rather than relying solely on resin datasheet values.
On production-scale injection-moulding lines, the following process envelope is used for LX175 when semicrystalline parts are required: barrel set points of 180–210 °C, a metering-zone temperature not exceeding 210 °C, a screw back pressure of 5–15 bar, and a mould temperature of 90–110 °C. Residence time above 180 °C should remain below 8 min; longer residence accelerates thermal degradation, increases lactide reformation, and causes yellowing. Thin-wall parts below 2 mm may require higher injection speeds, but excessive shear can reduce molecular weight and produce visible flow hesitation marks. These conditions are not universal; they should be adjusted with short-shot studies and cavity-pressure measurement because gate geometry and runner size alter the local cooling rate.
In extrusion and thermoforming, LX175 is processed as cast sheet, and the cooling history after extrusion controls whether the sheet remains thermoformable or embrittles due to premature spherulite growth. Sheet is typically extruded through a coat-hanger die and cooled on a three-roll stack with roll temperatures of 50–70 °C. The sheet should be quenched sufficiently to retain a low crystalline fraction before forming; otherwise, incomplete forming, localised whitening, and loss of deep-draw definition occur. During heating, the sheet reaches a forming temperature between 100 °C and 120 °C, where the polymer softens but does not yet flow. Thermoforming pressure and plug speed must compensate for the lower melt strength of linear PLA relative to branched PLA; deep undercuts and sharp corners are the first regions to exhibit thinning.
Moisture control remains necessary in thermoforming. Sheet exposed to relative humidity above 60% for prolonged periods can absorb sufficient water to create splay, bubbles, and a loss of draw uniformity. In practice, freshly extruded sheet should be formed within a controlled timeframe or protected in moisture-barrier packaging. Pre-drying of sheet at 60–70 °C for 4–8 h may be required if visible splay or surface roughness appears; however, excessive drying temperature above 80 °C can deform the sheet before forming.
Hot-fill packaging and reusable food-service articles are the main application classes where LX175 replaces standard PLA. In hot-fill lines operating at 85–95 °C, amorphous standard PLA parts may soften and lose dimensional stability; LX175 can withstand these temperatures only if the part has been crystallised. This is generally achieved with a hot mould or post-mould annealing at 80–100 °C for 15–30 min. Annealed LX175 exhibits a measurable increase in heat deflection temperature, but also a reduction in notched impact strength because crystallised PLA is more brittle than its amorphous counterpart. Impact performance should be evaluated with ISO 179-1:2010 Charpy specimens from the production tool, not from compression-moulded plaques.
The difference between LX175 and other Luminy PLA grades can be summarised by thermal profile and crystallisation potential. Standard L105 and L130 grades are formulated for lower melt temperatures and general-purpose conversion; they do not provide the same upper heat-deflection ceiling after annealing. LX175 is not an impact-modified PLA, a stereocomplex PLA, or a mineral-filled compound. Its tensile modulus in the unfilled state remains close to 3500 MPa when tested under ISO 527-1:2019, which is comparable to other PLA homopolymers, but its ability to retain stiffness above the glass transition after crystallisation is the defining separation. Users requiring toughness at room temperature should evaluate toughened PLA compounds rather than relying on LX175 alone.
Substituting LX175 into a cold-mould tool without adjusting mould temperature will not produce the intended high-heat performance and may only raise material cost. The grade requires higher mould temperatures and more aggressive pre-drying than standard L105 or L130, and those process requirements must be accepted as part of the material change. In cold-mould applications where dimensional stability above 60 °C is not required, a standard PLA grade may be more practical.
Rheological characterisation of LX175 should be performed with a capillary rheometer or a rotational rheometer equipped with parallel plates, using steady-shear data across 100–1000 s⁻¹ at 190 °C and 210 °C. The melt is shear-thinning, but linear PLA has a lower zero-shear viscosity than branched PLA grades and may exhibit a sharper onset of melt fracture in high-speed extrusion. When transferring data from standard PLA, errors in viscosity can lead to over-packing or sink marks. Production trials with a 32 mm diameter screw and 20:1 L/D ratio have shown that the actual melt temperature can exceed set point by 5–12 °C if screw speed and back pressure are not optimised. Therefore, melt-temperature measurement with a needle probe is recommended during setup.
Post-mould annealing of LX175 is not always required if the mould is hot enough, but for parts with varying wall thickness, annealing can equalise crystallinity. Annealing at 80–100 °C for 15–30 min increases crystalline content; however, shrinkage of 0.3–0.8% in the machine direction may occur and must be compensated in tool geometry. If the part is not fixtured during annealing, warpage arises from differential crystallisation and residual stress relaxation. Published data for this specific configuration is limited, so dimensional validation on the production tool is required.
Processors often observe plate-out on the mould surface when processing LX175 at high temperatures or with long residence time. The deposit consists largely of low-molecular-weight PLA and lactide, and is managed by lowering barrel temperatures, reducing hot-runner dead spots, and cleaning vents. Drying against a dew-point meter is more reliable than fixed time; a rise in vent vacuum or a decline in melt strength despite unchanged settings usually indicates moisture breakthrough. Moisture analysers with a detection limit below 100 ppm are required to verify drying because standard halogen moisture balances may not distinguish surface moisture from internal moisture at the required level.
Regulatory positioning for LX175 should be verified against the specific conversion process and food-contact condition. PLA homopolymer may comply with FDA 21 CFR 175.300 and EU 10/2011 for certain food-contact applications, but migration testing is required for the finished article because processing aids, masterbatch, and printing inks can alter overall compliance. Industrial compostability is commonly cited under EN 13432 or ASTM D6400; certification applies to the finished packaging item, not to the resin alone. The grade is not home-compostable in a predictable timeframe and should not be described as marine-biodegradable. Users should confirm SVHC concentration below 0.1 wt% under REACH and verify RoHS applicability for electrical and electronic equipment if conductive additives or colourants are introduced downstream.
| Purpose | Standard or regulation | Notes |
|---|---|---|
| Melt mass-flow rate | ISO 1133-1:2022 | Processing control for injection moulding and extrusion |
| Density | ISO 1183-1:2019 | Material conversion and part mass |
| Tensile properties | ISO 527-1:2019 | Short-term mechanical design |
| Heat deflection temperature | ISO 75-1:2013, ISO 75-2:2013 | Maximum use temperature under flexural load |
| Vicat softening temperature | ISO 306:2022 | Softening behaviour |
| Compostability | EN 13432, ASTM D6400 | Industrial composting if certified by an independent body |
| Food contact | FDA 21 CFR 175.300, EU 10/2011 | Specific migration limits require end-product validation |
Post-industrial recycling of LX175 is feasible if it is kept separate from PET and polyolefins. Reprocessing increases yellowing and reduces molecular weight; therefore, reclaimed LX175 is generally used at 10–20 wt% in non-critical packaging layers. The specific proportion depends on the number of heat histories and the final part requirements. LX175 should not be mixed with PET or polyolefins because melt-phase separation and hydrolytic degradation during reprocessing reduce properties.
Compared with polyhydroxyalkanoates and polybutylene succinate, LX175 offers higher stiffness and melting point but lower elongation and moisture barrier. Compared with PET, it has a lower processing temperature and lower density, but also lower impact strength and a narrower hot-fill window. The absence of mineral filler means that translucency and food-contact compliance are governed by the PLA matrix; however, unfilled LX175 also has lower stiffness than talc-filled PLA and lower impact strength than impact-modified PLA.