| HS Code | 889607 |
| Density | 1.25 g/cm³ |
| Melt Flow Index 190 C 2 16 Kg | 7 g/10 min |
| Tensile Strength | 45 MPa |
| Tensile Modulus | 2600 MPa |
| Elongation At Break | 15 % |
| Flexural Modulus | 2800 MPa |
| Flexural Strength | 70 MPa |
| Charpy Notched Impact Strength 23 C | 10 kJ/m² |
| Charpy Unnotched Impact Strength 23 C | 40 kJ/m² |
| Heat Deflection Temperature 0 45 Mpa | 115 °C |
| Heat Deflection Temperature 1 82 Mpa | 75 °C |
| Vicat Softening Temperature | 120 °C |
| Bio Based Content | 70 % |
| Processing Temperature | 190-220 °C |
| Mold Temperature | 100-120 °C |
| Drying Temperature | 80 °C |
| Drying Time | 4 h |
As an accredited Natureplast PLHT 202 High Heat Impact Modified Polylactic Acid factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Natureplast PLHT 202 High Heat Impact Modified Polylactic Acid comes in 25 kg moisture-barrier bags, palletized and stretch-wrapped. |
| Container Loading (20′ FCL) | Natureplast PLHT 202 High Heat Impact Modified Polylactic Acid loaded in a 20′ FCL, palletized, moisture-protected, and secured for ocean transport. |
| Shipping | Natureplast PLHT 202 High Heat Impact Modified Polylactic Acid is shipped as non-hazardous solid resin pellets. It is not DOT/IMDG/IATA regulated. Pack in sealed moisture-barrier bags or drums. Store cool and dry, away from heat and ignition sources. Avoid dust. No UN number, hazard class, or packing group assigned. |
| Storage | Store Natureplast PLHT 202 in a cool, dry, well-ventilated area below 25°C, away from direct sunlight, heat, moisture, and ignition sources. Keep in tightly sealed original packaging to prevent moisture uptake and contamination. Rotate stock first-in, first-out; use within recommended shelf life. Protect from physical damage, open flames, and incompatible materials. Avoid humid conditions, as PLA can hydrolyze. |
| Shelf Life | Typically 12 months in unopened original packaging; store cool, dry, away from moisture, heat, and direct sunlight. |
The air-handling components hidden inside the instrument panel are subjected to forced air at 65–85 °C after a solar soak, and upper register surfaces can exceed 105 °C in parked-vehicle conditions. PLHT 202 is injection moulded into register vanes, demister grilles, blend-door carriers, and duct connectors where the part is not a load-bearing structural member. Before moulding, the pellet moisture is reduced to ≤ 250 ppm in a desiccant dryer with an air dew point of ≤ -40 °C, a hopper temperature of 80 °C, and a minimum residence time of 4 h. Moisture content above 400 ppm drives ester hydrolysis at melt temperature, causing silver streaking on visible surfaces and a measurable loss of notched impact strength after moulding.
| Control parameter | Range or target | Reference method / instrument |
|---|---|---|
| Desiccant air dew point | ≤ -40 °C | Dew point hygrometer at dryer outlet |
| Residual pellet moisture | ≤ 250 ppm | ISO 15512:2019 coulometric Karl Fischer |
| Hopper drying temperature | 80 °C | Hopper throat thermocouple |
| Minimum drying time | 4 h | Hopper volume / throughput calculation |
| Melt temperature band | 195–210 °C | Melt probe or IR pyrometer |
| Cavity mould temperature | 90–110 °C | Water-jacket thermocouple |
Melt temperature is limited to 195–210 °C. At 220 °C and above, molecular weight reduction and volatile formation produce splay, brown specks in hot-runner dwell zones, and a shift in lot-to-lot melt flow rate; at melt temperatures below 190 °C, screw recovery torque rises and the impact modifier phase may remain incompletely dispersed. The cavity wall is held at 90–110 °C, because an amorphous skin produced below 60 °C can deform above 55 °C under load. Injection speed is set to achieve a fill time of 1.5–2.5 s for thin-wall duct sections, but gates smaller than 1.5 mm diameter can generate shear rates above 50 000 s⁻¹ and trigger melt fracture. Holding pressure in the range of 60–80 MPa hydraulic is maintained until gate freeze, then released to prevent overpacking near the valve-gate tip. A valve-gated hot runner with polished channels and no dead spots is used. PVC residues above 0.1 wt% in the machine or hot runner generate hydrochloric acid during heating and accelerate polyester chain scission. Regrind from sprues and runners is metered into virgin pellets at not more than 20 wt% for visible register vanes; for hidden ducts, 30 wt% can be tolerated only when regrind moisture is ≤ 250 ppm and dust fraction is below 2 wt%.
Surface flammability for interior use is tested according to FMVSS 302 and ISO 3795. Volatile organic compound and fogging release are screened under VDA 278 when the finished component is installed in a vehicle cabin. The terminal parts are demister grilles, register vanes, blend-door levers, and HVAC duct connectors that must survive repeated air-temperature cycling without cracking at snap-fit attachment points.
In hospital and long-term care trayline operations, rethermalization domes and compartmented base trays are washed at rinse temperatures up to 82 °C, then reheated in microwave or conduction rethermalizers. PLHT 202 is injection moulded into meal trays and lids only when the food-contact surfaces are verified against EU Regulation 10/2011/EC and the destination market's national food-contact provisions. Migration testing is performed under EN 1186-1 to EN 1186-15; because migration depends on pigment selection, regrind history, and processing aids, the supplier's food-contact statement for PLHT 202 must be confirmed for each colour and regrind level. If coloration is required, a food-contact-approved pigment masterbatch is loaded at 0.5–1.5 wt%, and no external mould release is used unless listed in the formulation's food-contact approval.
The same moisture-control and melt-temperature limits apply: pre-drying at 80 °C for 4 h to ≤ 250 ppm moisture, melt temperature 195–205 °C, and cavity temperature 90–110 °C. Because municipal and hospital dish machines expose the trays to 82 °C rinse water, residual moulded-in stress is reduced by annealing parts for 30 min at 100 °C in a forced-air oven after ejection, or by maintaining the cavity at the upper end of the stated range. For parts with a wall thickness below 1.2 mm or living hinges, lower-rack dishwasher placement near the calrod is not recommended because local water temperatures can exceed 100 °C and cause deformation. Dishwasher resistance screening is performed under EN 12875-1, but published data for this specific grade in the selected part geometry is limited and must be verified with production parts.
The terminal products are compartment trays, dome lids, and trayline bases used for plated meal delivery. High-fat microwave browning or operation above 110 °C is outside the application boundary; only water-mediated rethermalization below 100 °C is appropriate.
Because low-voltage power conversion efficiencies between 85% and 92% reject 8–15% of input power as heat, desktop charging docks and wall adapters can reach internal air temperatures of 70–85 °C near the transformer. PLHT 202 is used for the outer shell, snap-fit chassis, and cable-management features when the end-product specification does not require UL 94 V-0 or a defined fire-enclosure barrier. Drying follows the 80 °C/4 h desiccant condition to ≤ 250 ppm, and melt temperature is held at 195–210 °C. Cavity temperature is set at 90–100 °C to produce a crystalline skin that resists post-mould distortion when the power supply reaches operating temperature. Wall thickness is maintained between 1.8 mm and 2.5 mm; ribs are designed not to exceed 0.6:1 rib-to-wall ratio to avoid sink on the visible face. Gates are placed on the non-appearance rear face; direct edge gates below 1.5 mm diameter are avoided to reduce shear heating.
Directive RoHS 2011/65/EU Annex II applies when the finished electrical product is within scope. Accessible surface temperature limits are evaluated under IEC 62368-1:2020; for surfaces contacted for short periods, the test boundary must be confirmed with the end-product manufacturer. The material should not be purged or processed after PVC-containing material without an intermediate non-PLA purge, because trace PVC above 0.1 wt% produces acidic degradation products. Regrind use in snap-fit enclosures is limited to 15 wt% because repeated heat histories reduce molecular weight and notch sensitivity at the assembly hooks. Terminal parts include wall adapter housings, desktop charging cradles, and power tool charger shells where cosmetic grain is not critical.
Returnable dunnage trays used in hot stamping and spot-welding cells are loaded with formed metal parts at part temperatures from 65 °C to 85 °C. PLHT 202 is extruded into heavy-gauge sheet and then thermoformed into nesting trays for in-plant logistics. Barrell temperatures are profiled from 165 °C at the feed zone to 195 °C at the die; melt temperature above 205 °C is avoided because sheet edge sag and molecular weight reduction become difficult to control. The most significant process conflict is the reuse of thermoforming edge trim and rejected trays. Ground sheet is predried and metered into virgin pellets at 20–30 wt%; when regrind exceeds 50 wt%, melt strength during thermoforming can drop enough to cause premature sag and thinning in the plug-assist area. Lot-to-lot variability is monitored by melt flow rate under ISO 1133-1 at 210 °C/2.16 kg; if the measured MFR rises beyond the supplier's stated upper bound for PLHT 202, regrind is reduced to 15 wt% and the regrind-drying moisture content is checked against 250 ppm by ISO 15512:2019.
During thermoforming, sheet surface temperature is brought to 115–130 °C, with the upper heater set higher than the lower heater at a ratio of 1.2:1 to control curl. Mould temperature is held at 90–100 °C to retain dimensional stability when the tray is loaded with hot parts. For sheet thickness from 2.0 mm to 4.0 mm, cycle time is typically 25–45 s. The terminal product is an in-plant returnable dunnage tray, not a primary food-contact package; no food-contact compliance documentation is required unless the dunnage enters a cleanroom or medical packaging line. The grade is not appropriate for continuous immersion in hot aqueous alkaline cleaning solutions above 60 °C, which can hydrolyze the polyester matrix.
For small appliance chassis components located within 40 mm of a positive temperature coefficient heater, the material is not in direct contact with the heating element but is exposed to an ambient cavity temperature of 75–85 °C. PLHT 202 may replace glass-filled polypropylene in fan brackets, wiring retainers, motor mounts, and airflow deflectors inside appliances where heat resistance and impact toughness are required but loads are modest. The pre-drying and melt-temperature parameters remain fixed at 80 °C for 4 h to ≤ 250 ppm and 195–210 °C. Cavity temperature is kept at 90–110 °C, and parts are held for 30 min at 100 °C after ejection only when the appliance maker finds lower-crystallinity skin layers cause dimensional movement during the first heating cycle.
Where IEC 60335-1 clause 30.1 applies to external accessible thermoplastics, the ball-pressure test is conducted at the temperature specified by the standard for the classified service condition. For external parts that can be held under load at 75 °C, PLHT 202 may fall within the range that requires standard ageing; where a 125 °C ball-pressure test is specified, certification testing on the production part is required, and published data for this specific configuration is limited. The material is not used as a direct heater housing or fan scroll around a bare resistance wire. For multi-cavity tools with shot weight below 5 g, hot-runner residence time above 200 °C is limited to avoid degradation; cold-runner sprue and runner designs with runner diameters of 4–6 mm are preferred. Regrind from runners is limited to 20 wt% because small brackets are sensitive to notch effects at the snap rivet or self-tapping screw points. The terminal parts are PTC heater standoffs, wiring loom clips, and fan air-deflector baffles used in small kitchen appliances.
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Natureplast PLHT 202 High Heat Impact Modified Polylactic Acid is a compounded polylactic acid grade in which the lactide-based polyester matrix is modified to increase heat deflection resistance and notched impact toughness relative to unmodified PLA. The model designation PLHT 202 identifies a high-heat grade; however, the manufacturer’s published datasheet for this specific configuration is limited in open technical channels, and exact melt volume-flow rate, tensile, and thermal values should therefore be read from the lot-specific certificate of analysis. The following sections anchor test methods and class-typical process limits for high-heat impact-modified PLA rather than repeating unverified lot-specific figures.
In comparison with unmodified PLA, the thermal and mechanical distinctions are structural rather than cosmetic. Standard PLA is limited by a low heat deflection temperature and brittle tensile behaviour, while nucleated high-heat PLA grades can shift heat resistance upward but often sacrifice ductility. Impact-modified PLA without high-heat chemistry can increase Charpy or Izod values significantly, but the dispersed elastomer phase may reduce crystallinity and suppress the heat deflection ceiling. PLHT 202 is positioned where both modification strategies are present, so the practical property balance depends on crystallite volume fraction, modifier domain size, and interfacial adhesion between the PLA matrix and the dispersed toughening phase. Published data for this specific configuration is limited, and direct substitution for polypropylene in hot-contact applications should be validated by part-level testing rather than by resin data alone.
High-heat PLA chemistry can follow two distinct routes. One route uses talc or another heterogeneous nucleant to reduce the free-energy barrier for spherulitic nucleation. Another route blends PLLA with a minor fraction of PDLA so that stereocomplex crystallites with a melting point around 220 °C to 230 °C act as a high-melting scaffold. The conventional PLA homocrystal melting point is generally between 170 °C and 180 °C; the stereocomplex route therefore extends the useful temperature range but raises cost and can complicate welding and thermoforming because the high-melting phase does not fully remelt at conventional PLA processing temperatures. In impact-modified grades, the dispersed modifier can interfere with this crystallization. If modifier particles are concentrated at the spherulite boundaries, they may restrict amorphous chain mobility and alter the brittle-to-ductile transition. A more efficient toughening morphology is a fine dispersion of modifier domains smaller than the notch-tip stress field; large domains can become stress concentrators at knit lines. The exact morphology in PLHT 202 is proprietary.
Heat deflection temperature measured under 0.45 MPa according to ISO 75-2:2013 Method B is the most commonly cited screening value for PLA compounds, but it does not directly indicate maximum continuous service temperature. Standard PLA typically exhibits an HDT in the range of 50 °C to 55 °C under 0.45 MPa when tested as injection moulded without annealing. High-heat PLA formulations use heterogeneous nucleating agents and, in some cases, stereocomplexation between PLLA and PDLA to raise the crystallization temperature and crystallite density. Differential scanning calorimetry according to ISO 11357-3:2018 shows that the isothermal crystallization half-time in nucleated PLA is shorter than in unmodified PLA; the Avrami exponent in bulk crystallization is commonly between 2 and 3, indicating mixed spherulitic growth. The HDT increase is not delivered through molecular modification alone; it requires a mould temperature or post-forming annealing step that allows cold crystallization to approach a minimum crystallite volume fraction. On production-scale injection machines, parts ejected from a mould held below 80 °C may remain predominantly amorphous even if the compound contains a nucleant package. A mould temperature between 90 °C and 110 °C is generally required to reach the practical HDT plateau for this class. This is a critical processing threshold: if the tool cannot maintain that surface temperature, the end part may test close to unmodified PLA despite the grade designation. Vicat softening temperature according to ISO 306:2022 Method B50 provides a secondary thermal comparison; high-heat PLA grades can shift Vicat A50 upward by 20 °C to 35 °C relative to standard PLA, but the exact PLHT 202 value must be confirmed from the manufacturer’s certificate.
The limiting factor is not only heat resistance but also cycle time and part ejection. Raising the mould temperature to 90 °C to 110 °C lengthens cooling time and can create sticking, plate-out, or gate drool if the tool surface is not polished or if the cooling circuit design does not provide uniform heat removal. For this class, the practical mould temperature control band is approximately ±5 °C around the chosen set point; excursions below that band reduce HDT, while excursions above can increase cycle time and sticking. High-heat PLA grades are often processed with a tempering tunnel or annealing rack at 100 °C to 120 °C for 30 min to 60 min as an alternative to a hot mould. This post-mould annealing route increases crystallinity but adds a secondary operation and can cause dimensional growth of less than 0.5% in semi-crystalline PLA parts depending on shape and constraint. Published data for PLHT 202 on annealing shrinkage is limited, and tool compensation must be validated with the actual lot. The use of an unheated conventional water-cooled mould below 80 °C will freeze the amorphous phase before spherulitic growth reaches a sufficient volume fraction; the resulting HDT gain may be 5 °C or less, which is below the practical requirement for hot-fill or solar-gain applications. The sensitivity of this transition makes mould temperature control more decisive than barrel temperature for this product class.
Desiccant drying is stricter than in polypropylene or ABS. PLA and its copolyesters undergo hydrolytic chain scission at melt processing temperatures; a wet pellet feed of 350 ppm water can generate gas splay, viscosity loss, and interfacial failure between the PLA matrix and impact-modifier domains. Desiccant drying at 80 °C for 4 h to a dew point of -40 °C is the usual boundary. Karl Fischer analysis according to ISO 15512:2019 should be used to confirm residual moisture below 250 ppm before the first heat. In compounding, a co-rotating twin-screw extruder with an L/D ratio of 40:1 and vacuum venting prevents hydrolytic chain scission during dispersion of the impact-modifier phase. The melt is then strand-pelletized and crystallized in a secondary step to prevent pellet blocking. Injection moulding with a general-purpose screw of L/D 20:1 to 24:1 and a shut-off nozzle is typical; the screw should not introduce excessive shear because the impact-modifier domains can coalesce under high shear heating, reducing toughness and creating surface streaks.
At the processing temperature, the melt is pseudoplastic. The melt volume-flow rate alone is insufficient to predict mould filling because impact modifiers change the extensional viscosity and die swell. A grade modified for high heat and high impact may show a lower melt-flow index than a standard PLA but can still fill thin walls when injection speed and holding pressure are optimized. Capillary rheometry data across shear rates from 100 s⁻¹ to 10,000 s⁻¹ should be requested for mould-filling simulation. Hot-runner systems for PLA require low-shear channel design and should avoid dead spots where stagnant melt can degrade. Valve-gate hot runners with electric or pneumatic actuation are preferred over hot-tip designs when gate vestige or stringing is observed. On production-scale equipment, gate stringing and plate-out in high-heat PLA have been traced to excessive residence time above 230 °C; barrel residence time should therefore be kept below 5 min wherever possible.
Failure modes observed on production-scale equipment with this class of material include gate blush when mould temperature is too low, post-eject warpage when annealing is uneven, and impact failure at knit lines where the modifier phase is segregated or where flow fronts meet at low temperature. Knit-line Charpy or Izod values can be significantly lower than bulk values; knit-line impact testing with ASTM D256 or ISO 179-1:2010 on double-gate specimens is therefore advisable for structural parts. The presence of a high-heat nucleant package can also increase the sensitivity of part weight to holding pressure, because the freezing point of the semi-crystalline melt is higher than standard PLA. Dimensional control in moulds with long flow paths may require profiled gate sizes and higher packing pressure than used for an unfilled amorphous PLA.
Unmodified PLA tested by ISO 527-2:2012 typically shows tensile modulus in the range of 3.0 GPa to 3.5 GPa and tensile strength near 60 MPa; notched Charpy impact energy under ISO 179-1:2010 is generally below 5 kJ/m². A separate high-heat modification can shift HDT upward while leaving those impact values unchanged or lower. An impact modification without nucleating chemistry can raise Charpy or Izod values substantially, sometimes by a factor of 2 to 3, but it may reduce the crystallinity available for thermal resistance and suppress HDT. The combination represented by PLHT 202 is intended to move both properties simultaneously; the exact tradeoff is lot-dependent and should be evaluated by tensile, notched impact, and HDT testing on the same moulded plaque. Testing should follow ISO 527-2:2012 for tensile properties, ISO 179-1:2010 for Charpy or ASTM D256 for Izod, and ISO 75-2:2013 for HDT. The differences from other products are therefore expressed in the shape of the property matrix, not in a single number.
| Requirement or property | Standard method or regulation | Condition or limitation |
|---|---|---|
| Melt volume-flow rate | ISO 1133-1:2022 | Condition must be selected from lot-specific datasheet; not repeated for PLHT 202 |
| Density | ISO 1183-1:2019 Method A | Immersion method; value is formulation-dependent |
| Tensile properties | ISO 527-2:2012 / ASTM D638-14 | Test speed and specimen type to be taken from datasheet |
| Notched Charpy impact | ISO 179-1:2010 | Notched specimen, method 1eA where applicable |
| Notched Izod impact | ASTM D256 | Notched specimen; results are not directly interchangeable with Charpy |
| Heat deflection temperature | ISO 75-2:2013 Method B | 0.45 MPa flexural stress; state mould temperature and conditioning |
| Vicat softening temperature | ISO 306:2022 Method B50 | 50 N load, 50 °C/h heating rate |
| Moisture content | ISO 15512:2019 | Karl Fischer; advise limit below 250 ppm before melt processing |
| Food-contact status | EU 10/2011; FDA 21 CFR 175.300 where applicable | Exact formulation clearance must be confirmed by the compound manufacturer |
| RoHS restricted substances | Directive 2011/65/EU as amended | Supplier declaration required |
| REACH SVHC | EC 1907/2006 | Article 33 duty applies at article level |
Production-scale usage scenarios for a high-heat impact-modified PLA such as PLHT 202 include injection-moulded reusable cups and trays that may see short contact with hot liquids above 80 °C, interior automotive trim exposed to solar gain, and consumer products where impact cracking after drop loading is the primary field failure, tested by ASTM D5276 where applicable. In each case, material selection should be tested under the end-use standard rather than inferred from virgin resin data. For automotive interior parts, odour, fogging, and scratch resistance require separate testing under OEM-specific protocols; published data for this specific configuration is limited. For food-contact applications, the final part must be validated under the relevant national migration protocol, and the compound’s compliance status must be confirmed with the manufacturer because impact modifiers and nucleants may not be covered by a generic PLA listing. The processing boundary is equally application-specific: a tool that cannot hold a mould surface above 80 °C will not reproduce the high-heat performance that the compound can deliver under a properly designed tempering cycle.