| HS Code | 627254 |
| Density | 1.25 g/cm³ |
| Melt Flow Rate 190 C 2 16 Kg | 10 g/10 min |
| Tensile Strength At Yield | 55 MPa |
| Tensile Strength At Break | 50 MPa |
| Tensile Elongation At Break | 100% |
| Flexural Modulus | 2.2 GPa |
| Flexural Strength | 80 MPa |
| Notched Izod Impact Strength | 15 kJ/m² |
| Unnotched Izod Impact Strength | 50 kJ/m² |
| Heat Deflection Temperature At 0 45 Mpa | 125°C |
| Heat Deflection Temperature At 1 8 Mpa | 95°C |
| Vicat Softening Point | 125°C |
| Glass Transition Temperature | 60°C |
| Melting Temperature | 170°C |
| Rockwell Hardness | R100 |
| Water Absorption | 0.10% |
| Linear Mold Shrinkage | 0.3–0.6% |
| Antibacterial Test Standard | JIS Z 2801 |
| Antibacterial Activity Value | ≥2.0 |
As an accredited TERRAMAC TE-8005MT9 High Heat/Impact Antibacterial Polylactic Acid factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Packaged in 25 kg moisture-proof paper bags on pallets, stretch-wrapped, and labeled with product code, lot, and handling information. |
| Container Loading (20′ FCL) | 20′ FCL: TERRAMAC TE-8005MT9 High Heat/Impact Antibacterial Polylactic Acid, 25 kg bags, palletized, stretch-wrapped, strapped, loaded in clean, dry container. |
| Shipping | TERRAMAC TE-8005MT9 typically ships as a non-hazardous, non-regulated solid polymer. Pack in moisture-barrier bags, fiber drums, or octabins. Keep sealed to prevent moisture uptake and contamination. Store and transport at ambient temperature, away from water, direct sunlight, and incompatible chemicals. Follow local regulations; no DOT/IMDG/IATA hazardous classification required. |
| Storage | Store TERRAMAC TE-8005MT9 in a cool, dry, well-ventilated area away from direct sunlight, heat, moisture, and ignition sources. Keep containers tightly sealed in original packaging to prevent moisture absorption and contamination. Avoid dust generation and static buildup. Maintain low humidity and temperatures below 30°C. Use first-in, first-out rotation and follow the supplier’s safety data sheet. Store away from incompatible materials. |
| Shelf Life | Typically 12 months from manufacture when stored unopened in original packaging, cool, dry, and away from moisture and heat. |
In institutional catering and airline galley operations where polycarbonate trays are being substituted due to bisphenol A restriction concerns, the high-heat PLA grade enters the tooling as a pre-compounded pellet without downstream blending. Pre-drying in a desiccant dryer at 80 °C for 4 h is mandatory when ambient storage relative humidity has exceeded 60 %; residual moisture must be verified below 250 ppm using ISO 15512:2019 Karl Fischer titration before the first heat. Nozzle melt temperature is maintained at 210–230 °C, and the mold surface is held at 90–110 °C to force cold crystallization before ejection; parts ejected from a mold below 85 °C show incomplete crystal growth and fail hot-fill immersion at 85 °C after 30 min. Cold-runner regrind generated during process commissioning may be reintroduced at 20 wt% maximum, provided it is re-dried to the same moisture specification and has experienced no more than 3 heat histories above 200 °C. Food-contact compliance of the stackable tray or shallow bowl is established through Regulation (EU) No 10/2011 overall migration into simulant B for 2 h at 70 °C with a limit below 10 mg/dm²; repeated-use articles are additionally subjected to 3 consecutive simulant contacts because migration kinetics change as surface crystallinity increases. Antibacterial activity is assessed per ISO 22196:2011 against Staphylococcus aureus ATCC 6538P and Escherichia coli ATCC 8739 with a procurement threshold of 99 % reduction after 24 h; the exact antimicrobial chemistry must be obtained from the compounder before declaring food-contact suitability. The finished wall thickness is kept at 2.5–4.0 mm, and gate placement locates weld lines away from the base drop zone; 500 dishwasher cycles at 85 °C with alkaline detergent represent the validation target, although published data for this specific formulation in airline tray geometry is limited and should be confirmed on production tools.
Blender base shells, stand mixer head covers, and coffee machine internal chute components expose the molded material to local hot spots near motors, impact at snap-fit lugs, and chemical contact with coffee oils and detergents. The resin is processed on a 1200 kN hybrid injection molding machine with a general-purpose screw of L/D 20:1 and compression ratio 2.2:1; melt temperature is capped at 225 °C because residence times longer than 6 min at that temperature produce melt flow shifts above 15 % relative to virgin pellets measured by ISO 1133-1:2022 at 190 °C/2.16 kg. The mold is held at 100 °C minimum, and cooling times of 45–60 s for 2.0–3.0 mm walls are required to develop sufficient crystallinity for dimensional stability. When colour concentrate is unavoidable, the let-down ratio is restricted to 2.0 wt% of a PLA-carrier masterbatch with a melt flow rate below 15 g/10 min at 190 °C/2.16 kg per ISO 1133-1:2022; higher-viscosity carriers produce localized gloss differences and weld-line weakness. Regrind from sprues and runners is capped at 10 wt% because snap-fit geometries tolerate less molecular weight reduction than flat bases. For internal food-contact chutes, FDA 21 CFR 177.1520 does not automatically cover PLA because that section addresses olefin polymers; a food-contact suitability statement or FCN clearance is required from the supplier. Glow-wire verification according to IEC 60695-2-11:2014 may be required for unattended appliance housings with current-carrying parts; the typical 750 °C threshold is not automatically satisfied by PLA compounds without flame-retardant modification and must be tested on final part geometry. The terminal product is a blender base shell or coffee bean hopper chute where gate blush has been observed at injection speeds exceeding 100 mm/s; reducing peak injection speed to 60–80 mm/s and raising mold temperature to 105 °C eliminates the defect but extends cycle time by 8–10 s. Incoming inspection per ISO 180:2000 on 4.0 mm bars can use an internal threshold of 8 kJ/m² at 23 °C as a release gate, but this is an internal control value and not a supplier-published specification.
For diagnostic device enclosures, overbed table edge profiles, and wheelchair control-panel bezels in hospital wards, the specification is antimicrobial surface performance rather than biocompatibility; the grade should not be used for skin-contact devices or implants unless a full ISO 10993-1 evaluation has been supplied by the molder. These parts are exposed to quaternary ammonium disinfectants at 1000–2000 ppm active quaternary ammonium compound, 70 % isopropanol, and dilute hydrogen peroxide; cleaning compatibility is tested per ASTM D543-20 with final parts, and the antimicrobial surface must retain at least 2.0 log reduction after 100 wipe cycles. The injection molding process uses a melt temperature of 215 °C and a mold temperature of 95 °C, with holding pressure at 80 MPa for part walls between 2.0 mm and 3.5 mm. Regrind is excluded entirely for patient-facing surfaces; runner scrap is diverted to non-regulated housings or returned to the compounder, because quaternary ammonium and peroxide treatments can extract low-molecular-weight fractions from regrind more readily than from virgin pellets. Steam sterilization at 121 °C exceeds the practical continuous service temperature because saturated steam hydrolyzes the polyester backbone; hydrogen peroxide plasma below 60 °C is preferred but must be confirmed with the device manufacturer. The terminal product is a diagnostic cart control panel or bed rail impact guard where the notched Izod impact of incoming material is screened per ISO 180:2000 on 4.0 mm bars; an internal acceptance threshold of 8 kJ/m² at 23 °C is used before production release, but published data for this specific configuration is limited and the molder should verify the effect of textured surfaces and gate stress on final impact performance.
Unattended point-of-sale terminal enclosures and self-checkout kiosk housings require resistance to floor-level impact and fire safety validation for information technology equipment. The grade is injection molded into bezels and rear shells with wall thickness from 2.5 mm to 3.2 mm; melt temperature is held at 220–230 °C, mold temperature at 100–110 °C, and holding pressure at 70–90 MPa to maximize surface crystallinity and heat deflection temperature measured per ASTM D648-18 Method B at 0.455 MPa. Colour masterbatch let-down ratio for dark grey and charcoal housings is limited to 1.5–2.0 wt%, and 15 wt% regrind is allowable for internal non-cosmetic surfaces only after re-drying to below 250 ppm moisture. Final product requires assessment against IEC 62368-1:2018 for information technology equipment; if the part is classified as retaining current-carrying components, glow-wire testing per IEC 60695-2-11:2014 at 750 °C is often invoked, while PLA compounds without flame-retardant additives may not satisfy this requirement and must be verified before design lock. On a 1800 kN servo-driven machine, short-shot occurred at flow length-to-thickness ratios above 150:1; edge gates of at least 1.5 mm diameter are preferred over pin gates to reduce shear heating and gate blush at melt temperatures above 225 °C. The terminal product is a kiosk front bezel or rear access cover with snap-fit tabs, where the impact-modified PLA grade provides stiffness to resist deflection during screen cleaning and occasional cart impact.
| Application segment | Test method/standard | Condition | Acceptance or boundary |
|---|---|---|---|
| Institutional food-service tray | Regulation (EU) No 10/2011 overall migration | Simulant B, 2 h, 70 °C | Below 10 mg/dm² |
| Antibacterial surface | ISO 22196:2011 | 24 h, S. aureus ATCC 6538P, E. coli ATCC 8739 | At least 99 % reduction |
| Small appliance housing glow wire | IEC 60695-2-11:2014 | 750 °C if current-carrying | Verification required; PLA may not pass |
| Healthcare diagnostic enclosures | ASTM D543-20 chemical resistance | 70 % isopropanol, 0.5 % NaOCl, quaternary ammonium | No visual crazing; retain 2.0 log reduction after 100 cycles |
| Point-of-sale housings | IEC 62368-1:2018 | End-product safety | Confirmed on final enclosure |
In refillable cosmetic packaging, compact bases, jar outer shells, and closure overmolds impose a short-cycle injection molding environment combined with repeated handling and intermittent exposure to esters, oils, and alcohol-based makeup removers. The resin is dried to 200 ppm moisture and molded at 205–220 °C with polished mold surfaces held at 90–100 °C; mold release agents are excluded because they interfere with subsequent pad printing and reduce the measured antibacterial surface activity. Colour masterbatch is limited to 1.0–2.0 wt% of a PLA-compatible carrier for opaque high-gloss shades, while 10 wt% in-house regrind is permitted for non-contact outer shells only when covered by the supplier’s food-contact or cosmetic packaging compliance statement. The terminal compact base or refillable jar outer shell is paired with a PET or PP inner jar that contains the formulation; the PLA outer shell therefore is not a direct cosmetic contact layer but must still comply with REACH Annex XVII restrictions and EC No 1907/2006 SVHC content below 0.1 %. Snap-fit hinge lugs and closure threads are the primary impact-critical features; filling line temperatures of 60–70 °C and alcohol wiping at point-of-sale are used as validation conditions, and the antimicrobial surface is tested per ISO 22196:2011 after 24 h contact with the same challenge organisms. Published data for this exact cosmetic packaging configuration is limited, so the processor must confirm hinge cycling performance and fragrance resistance on production tools before committing to high-volume output.
Because portable diagnostic carrying cases and field-service equipment enclosures are subjected to frequent isopropanol disinfection and mechanical shock from transport, environmental stress cracking becomes a more critical failure mode than heat sag. The resin is injection molded into case halves with nominal wall thickness of 3.0 mm; the melt temperature is kept at 210–220 °C, the mold at 90–100 °C, and the cooling time is extended to 50–60 s to stabilize post-mold shrinkage. Regrind is capped at 12 wt% and only used in the non-visual inner shell; colour masterbatch, if required for case identification, is added at 1.5 wt% with a carrier melt flow rate matched to the base resin per ISO 1133-1:2022. Chemical resistance is evaluated according to ASTM D543-20 using 70 % isopropanol and 0.5 % sodium hypochlorite; visual crazing or a drop in notched Izod impact below the incoming threshold after 200 wipe cycles constitutes rejection. Antimicrobial performance under ISO 22196:2011 must be retained after 72 h repeated disinfection contact; the active agent’s resistance to alcohol extraction is a key limitation to verify with the compounder. On a 1500 kN two-platen injection molding machine, the long flow path across case halves produced weld lines at latch corners; increasing mold temperature to 100 °C and reducing fill speed to 50 mm/s moved the weld line away but extended cycle time by 6–8 s. The terminal product is a two-shell diagnostic carrying case with metal hinges, where the insert-molded hinge bosses require screw pull-out testing and the PLA surface must withstand latch cycling without impact whitening. Steam autoclaving at 121 °C is not permissible; hydrogen peroxide or alcohol-based disinfection below 60 °C is the expected cleaning route.
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The product designation TERRAMAC TE-8005MT9 identifies a Polylactic Acid (PLA) compound within the TERRAMAC series of bio-based aliphatic polyesters. The grade is specified as high-heat, impact-modified, and antibacterial. Because the suffix MT9 is manufacturer-specific, the exact identity and loading of the heat-stabilization, impact-modifier, and antibacterial additive packages should be confirmed against the supplier’s technical datasheet and batch certificate. The base polymer is a poly(L-lactic acid)-rich feedstock, in which the residual D-lactide level is typically held below 2 mol% to retain crystallization potential after molding. Published data for this specific configuration is limited; grade-specific values should not be inferred from other TERRAMAC grades.
In processing environments, the material requires moisture-controlled handling. A desiccant hopper dryer with a dew point of -40°C or lower and an inlet-air temperature of 80°C for 4 h is a standard starting point for moisture-sensitive PLA compounds. The target residual moisture before plastication is ≤250 ppm; moisture above this threshold accelerates hydrolytic chain scission during melt residence and mainly degrades impact-modified performance. An injection molding machine with a general-purpose screw of 20:1–25:1 L/D and a compression ratio of 2.5:1–3.0:1 is commonly used. Melt temperature should be maintained in the 190°C–230°C range, with residence time at the upper end limited to 5 min or less. Processing above 240°C is not recommended because lactide reformation and chain scission increase sharply.
Drying air flow rate should be at least 0.5 m³/h per 1 kg/h throughput, and the desiccant bed must be regenerated at 150°C–180°C to maintain the required dew point. In high-humidity environments above 60% RH, dried pellets should be conveyed by dry-air or vacuum loaders rather than exposed to ambient air for more than 30 min. If the pellets are left open in a humid molding shop, re-drying may be required before startup. These limits are operational boundaries; they are not indicative of a resin defect.
Antibacterial performance in plastics is often evaluated according to ISO 22196:2011 or JIS Z 2801:2010, using Staphylococcus aureus and Escherichia coli as test microorganisms. The method calculates an antibacterial activity value R; a reduction corresponding to R ≥ 2.0 after 24 h is a common acceptance threshold for non-food-contact surfaces. The TE-8005MT9 datasheet should be requested to confirm the exact R values and the antimicrobial agent chemistry. Inorganic silver-based systems are frequently used in PLA because of their thermal stability and low volatility; however, their dispersion is governed by the screw mixing-section geometry, back-pressure, and the particle-size distribution of the masterbatch. Incomplete distributive mixing creates local zones of low surface agent concentration, reducing antibacterial efficacy without necessarily changing bulk tensile properties.
Antimicrobial additives can also function as nucleating particles in PLA, increasing the non-isothermal crystallization onset and the cold-crystallization temperature. In a high-heat grade this effect is coupled with the base resin formulation; therefore preconditioning and process verification on injection molding machines with check-ring shutoff nozzles and closed-loop screw-position control are required before scale-up. Published data for this specific configuration is limited when the product is supplied as a ready-to-mold pellet instead of a let-down masterbatch.
On production-scale injection molding equipment, gate blush and plate-out are documented failure modes when melt temperature is excessive or screw back-pressure is too high for the additive package. A reverse-taper nozzle and a shut-off valve should be used to prevent drool. Hydraulic injection pressure set points between 80–140 MPa are common; the exact value depends on part geometry and wall thickness. If the material is further let down with colorant or processing aid on a co-rotating twin-screw extruder, the L/D ratio should be at least 32:1 and screw speed should be kept below 400 rpm to limit shear heating. The melt temperature at the die should not exceed 230°C.
| Property or requirement | Test method or standard designation | Data status for TE-8005MT9 |
|---|---|---|
| Antibacterial activity | ISO 22196:2011 / JIS Z 2801:2010 | Batch-specific R value to be confirmed |
| Heat deflection temperature | ISO 75-2:2013 Method B (0.45 MPa) | Annealing-history dependent |
| Notched Charpy impact strength | ISO 179-1:2010 1eA | Modifier-dependent; datasheet required |
| Melt mass-flow rate | ISO 1133-1:2022 (190°C, 2.16 kg) | Use supplier-specified MFR range |
| Residual moisture before molding | Karl Fischer coulometry | ≤250 ppm target |
Standard unmodified PLA typically exhibits an HDT-B value near 55°C under ISO 75-2 Method B and a notched Charpy impact strength of 2–4 kJ/m² using ISO 179-1 1eA specimens. These values are not sufficient for thin-wall electronic housings or food-service articles exposed to hot fill. High-heat PLA compounds shift the practical service window through a combination of low-D-lactide polymer, nucleating agents, and post-mold annealing at 90°C–120°C for 30 min–2 h depending on wall thickness. An annealed high-heat PLA part may reach an HDT-B above 90°C; some grades exceed 120°C. Impact modification typically raises notched impact into the 8–30 kJ/m² range depending on modifier chemistry and loading, while tensile modulus and tensile strength are reduced relative to unmodified PLA. The TE-8005MT9 trade designation indicates simultaneous optimization of these two conflicting requirements; exact values remain grade-specific.
Compared with standard extrusion PLA, the melt flow behaviour is also changed. Impact-modified PLA generally has a lower melt mass-flow rate than unmodified PLA at the same temperature and load, requiring higher injection pressure or wider gates. Hot-runner systems with internally heated nozzles and mold temperatures of 80°C–110°C are used to promote crystallinity. If the mold is kept below 60°C, the part may remain amorphous and the high-heat benefit will not develop. The crystallization half-time is temperature-dependent; at the mold surface, crystal growth and nucleation compete with rapid cooling, and the actual degree of crystallinity can be below 20% in the skin layer while exceeding 40% in the core of a thick section.
Thermal analysis according to ISO 11357-1 and ISO 11357-3 with a heating rate of 10°C/min under nitrogen can be used to verify the glass-transition temperature, cold-crystallization peak, and melting endotherm. The heat of fusion from the first heating cycle must be interpreted with care because processing history changes crystallinity. The maximum practical heat-deflection increase after annealing is achieved when the part reaches the formulation-specific crystallinity limit; additional annealing does not improve HDT and may cause oxidative yellowing of the antimicrobial package.
For mechanical property verification, specimens should be conditioned at 23°C and 50% RH for 48 h before testing. Tensile testing can be performed on ISO 527-2 Type 1A specimens at 5 mm/min or 50 mm/min depending on the property required. The notched Charpy impact test under ISO 179-1:2010 uses 1eA specimens and should include at least 10 specimens per batch to resolve ductile-brittle transitions near room temperature. Weld-line performance is highly dependent on gate location and melt temperature; weld-line strength can be significantly lower than the unnotched bulk value, particularly in impact-modified PLA.
When this material is evaluated for thin-wall food-service bowls that must withstand hot filling at 85°C–95°C, post-mold constrained annealing is often more effective than in-mold crystallization alone. A part removed without an annealing fixture can distort during subsequent crystallization because differential shrinkage develops between the skin and core. Fixtures must support the part in all critical dimensions and must not insulate the surface from oven air flow. Convection ovens with ±3°C chamber uniformity are preferred for annealing set points between 100°C and 110°C. Production records from single-cavity test molds with 2.0 mm wall thickness indicate that constrained annealing reduces post-mold warpage in semi-crystalline PLA, although published data for this specific configuration is limited.
For medical device and personal-care housing applications, antibacterial performance is often specified through ISO 22196; however, ISO 22196 is not a sterilization validation. If the application requires autoclaving at 121°C for 15 min, preliminary testing is required because impact-modified PLA may soften below the autoclave temperature unless crystallized. If electron beam or gamma irradiation is used, the effect on PLA molecular weight and on antimicrobial additive effectiveness should be tested according to ISO 11137-1. Published data for irradiation performance of this grade is limited. In food-contact use, compliance should be confirmed against EU Regulation No 10/2011 and the applicable FDA food-contact notification or clearance; it should not be assumed from the bio-based polymer identity alone.
In the field, standard PLA fails early in hot-water cycles at 65°C–75°C and in detergent solutions with pH above 9, whereas a high-heat crystallized PLA may delay failure through lower water diffusivity and higher HDT. The difference is not solely thermal; increasing the degree of crystallinity from an amorphous state to 30%–40% reduces water uptake and slows hydrolysis. Nevertheless, PLA remains susceptible to hydrolysis under prolonged wet heat and at pH above 10. Chemical resistance should be verified according to ISO 175 or an internal soak test with the actual detergent chemistry and fill temperature.
Impact modification introduces a second phase that can alter chemical resistance and migration behaviour. The exact modifier system for MT9 must be confirmed; aliphatic modifiers are generally preferred when industrial compostability is required, while aromatic-containing modifiers may improve toughness but can reduce biodegradation performance. If the product is certified to EN 13432 or ASTM D6400, that certification applies only to defined thicknesses and part geometries; it is not an unconditional material property. Comparative performance against petroleum-based ABS or PC/ABS shows lower heat resistance and lower notched impact energy, but the PLA compound may provide a lower fossil-carbon feedstock and, depending on the formulation, improved biodegradation of the base polymer under controlled composting conditions. The grade is not a drop-in substitute for all amorphous engineering thermoplastics because the crystallization cycle can add 15%–40% to the molding cycle.