| HS Code | 932531 |
| Density | 1.20 g/cm³ |
| Melt Flow Rate | 10 g/10 min (190°C/2.16 kg) |
| Tensile Strength | 60 MPa |
| Tensile Elongation At Break | 4% |
| Flexural Modulus | 3000 MPa |
| Flexural Strength | 90 MPa |
| Notched Izod Impact Strength | 3 kJ/m² |
| Heat Deflection Temperature | 55°C (0.45 MPa) |
| Vicat Softening Temperature | 60°C |
| Melting Temperature | 170°C |
| Glass Transition Temperature | 60°C |
| Mold Shrinkage | 0.5% |
| Antibacterial Activity | ≥2.0 (JIS Z 2801) |
| Biodegradability | Yes |
As an accredited TERRAMAC TE-7003 Low Density Antibacterial Injection Molding Polylactic Acid factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | TERRAMAC TE-7003 is supplied in 25 kg moisture-barrier paper bags, palletized and stretch-wrapped for secure transport and storage. |
| Container Loading (20′ FCL) | Container Loading (20′ FCL): TERRAMAC TE-7003 Low Density Antibacterial Injection Molding Polylactic Acid, palletized, secured, moisture-protected, and efficiently stowed. |
| Shipping | For shipping, TERRAMAC TE-7003 Low Density Antibacterial Injection Molding Polylactic Acid is a non-hazardous polymer and is not regulated for transport. It is packaged in sealed moisture-barrier bags, typically 25 kg, palletized and shrink-wrapped. Keep dry and cool; avoid moisture, heat, and direct sunlight. Follow standard industrial handling. |
| Storage | Store TERRAMAC TE-7003 in a cool, dry, well-ventilated area away from direct sunlight, heat, and ignition sources. Keep containers tightly sealed in original packaging to prevent moisture absorption and contamination. Maintain low humidity and recommended storage temperature, typically below 30°C. Avoid prolonged exposure to humid air. Stack safely to prevent package damage. Use FIFO inventory practices. |
| Shelf Life | Typically 12 months from manufacture when stored unopened in a cool, dry place, away from heat and moisture. |
TERRAMAC TE-7003 is a pre-compounded low-density antibacterial injection molding polylactic acid. The application boundaries described below are confined to ambient-temperature injection molded articles where density reduction, surface antibacterial activity, and stiffness are required in the same component. Continuous service above 50°C, hot-fill above 60°C, and steam sterilization are outside the operational window because low-crystallinity PLA softens under load below 60°C when measured by ISO 75-2/B and undergoes accelerated hydrolysis in wet heat. Before molding, the resin is dried in a desiccant-wheel dryer at 80°C for 4–6 h to residual moisture below 250 ppm by ISO 15512:2019 Method A. Plant air above 60% RH requires closed conveying and hopper drying, because moisture hydrolyzes the ester backbone and produces viscosity loss above 10%, silver streaking, and reduced antibacterial surface activity. Purging is conducted with low-MFR PLA purge compound or acrylic-based purge; polycarbonate, PVC, and acetal purge compounds create transesterification or acidic degradation products at PLA melt temperatures and are not used.
Injection molding of TE-7003 for in-vitro diagnostic housings and specimen collection outer shells places the material in short-term contact with ex vivo biological fluids. Compliance at the component level is assessed under ISO 10993-5:2009 for cytotoxicity, ISO 10993-10:2021 for sensitization, and production documentation is maintained under ISO 13485:2016. The antibacterial surface is qualified by ISO 22196:2011 antibacterial activity testing with acceptance at R ≥ 2.0 against Staphylococcus aureus ATCC 6538P and Escherichia coli ATCC 8739 after 24 h contact. The formulation addition ratio for this segment is 100 wt% TE-7003 as-supplied. Regrind generated from sprues and runners is limited to 15 wt% maximum, provided the regrind has not exceeded two heat histories and is dried identically to virgin material. No secondary silver-based, zinc-based, or organotin biocide masterbatch is added to this formula, because free biocide addition above 0.2 wt% changes melt viscosity, increases plate-out on mold vents, and interferes with ultrasonic welding of diagnostic cartridge shells.
Downstream tooling for this segment uses hot runner valve-gated systems with polished S136 or equivalent stainless steel cavity steel and SPI A2 surface finish, with total wall thickness of 0.8–1.2 mm. Clamp force for an eight-cavity family mold is selected at 4–5 kN/cm² of projected area. The barrel profile is set rear 175–185°C, center 185–195°C, front 195–205°C, and nozzle 200–210°C. Mold temperature is maintained at 25–35°C with thermolators and counterflow baffles, because lower wall temperature causes premature solidification at the flow front and higher temperature increases cooling time and reduces dimensional capability below ±0.05 mm for snap-fit features. Fill velocity is set at 100–150 mm/s for thin-wall filling, with switchover at 95–98% fill by screw position. Hold pressure is maintained at 60–80 MPa for 2–3 s; back pressure of 0.5–1.0 MPa is sufficient to keep the pre-compounded antibacterial dispersion uniform without excessive shear heating. Typical terminal articles include 24-hour urine collection cup outer shells, transport vial carriers, benchtop analyzer cassette housings, and pipette tip rack bodies. Ultrasonic weld joints and snap-fit engagement in these parts require post-mold annealing at 60°C for 30 min when dimensional creep under storage above 40°C is a concern.
Thin-wall cosmetics jars and airless dispenser outer shells at wall stock of 0.7–1.0 mm are sensitive to gate freeze-off and sink mark formation when the low-density PLA compound is molded in multi-cavity tools. Cosmetic packaging under EU Regulation 1223/2009 and ISO 22716:2007 requires traceability of the compounded resin and control of organoleptic properties. REACH Regulation 1907/2006 documentation and heavy metals screening remain mandatory for EU market access, while EU 10/2011 migration limits are not automatically triggered because the pack is not intended for direct food contact. The pigmented formulation addition ratio uses 1.0–2.5 wt% of a PLA carrier color concentrate. TiO₂-based white masterbatch above 3.0 wt% is not recommended because opacity gain is offset by measurable loss in Charpy notched impact and an increase in shrinkage anisotropy from 0.3% to 0.6%. If post-mold metallization or UV-cured lacquering is specified, the molded surface is corona treated to 38–42 mN/m within 24 h before coating. Corona energy exceeding 2.0 kW/m²/min can etch the surface and reduce ISO 22196:2011 antibacterial activity by removing the top polymer layer.
Processing uses a two-platen toggle injection molding machine with a 22:1 L/D screw and compression ratio of 2.0–2.5:1. Screw diameter is selected so that shot size is 30–70% of maximum barrel capacity. Smaller shots increase residence time and larger shots produce inconsistent plastication. Melt temperature at the nozzle is held at 195–205°C, while the mold is cooled to 20–30°C. Cooling time for a 0.8 mm wall jar is typically 6–10 s. Ejection is inhibited by undercuts and polished texture depth above 0.025 mm, so draft angles below 0.5° are not used. Finished product classes in this segment include cosmetic cream jars, compact foundation housings, lip balm shells, and airless dispenser outer bodies. Physical property validation uses ISO 527-2 for tensile modulus, ISO 178 for flexural modulus, and ISO 179-1/1eU for unnotched Charpy impact. Gloss retention after 500 h of artificial weathering under ISO 4892-2 Method A is compared against the approved masterbatch.
Oral care handles require a different failure management strategy than HIPS because PLA exhibits lower notched impact strength and higher stiffness. For toothbrush handles, TE-7003 is processed at 100 wt% with a color concentrate at 1–2 wt%. If transparent handles are required, no colorant is added and the screw is purged with a low-MFR PLA purge compound before the run. The formula addition ratio for a slide-core toothbrush handle includes a maximum 10 wt% of in-house regrind. Higher regrind percentages raise the risk of contamination by cellulose fibers from the packaging area, which create black specks and inconsistent antibacterial surface distribution. Compliance for oral care plastics is primarily EN 71-3:2019+A1:2021 for trace element migration when the article is child-directed or child-appealing, ISO 22196:2011 for antibacterial surface performance, and REACH Annex XVII entries for phthalates and CMR substances. The processed handle is not a medical device unless the manufacturer adds a drug-delivery or therapeutic claim; in that case ISO 10993-1 evaluation is required.
Molding of a toothbrush handle in TE-7003 requires a low-compression screw of 2.0:1 compression ratio and a cold runner with full-round cross section of 5–8 mm diameter. The nozzle temperature is set at 200–210°C, the front zone at 195–205°C, and the rear zone at 175–185°C. Mold temperature is kept between 25°C and 35°C. If mold temperature exceeds 40°C, ejection-induced deformation in long and slender handles becomes measurable as bowing greater than 0.5 mm over a 180 mm length. Hold pressure is applied at 50–70 MPa for 2–4 s, with gate diameter at 1.0–1.5 mm. A shut-off nozzle is used to prevent drool, because PLA has lower melt elasticity than HIPS and nozzle drool leads to shot weight variation above 0.3%. Terminal products include manual toothbrush handles, replaceable-head toothbrush bodies, floss pick frames, and tongue cleaner handles. For floss pick frames that undergo repeated flexure, the geometry is thickened at the hinge by 0.2–0.4 mm relative to HIPS to maintain fatigue life. Published data for this specific configuration is limited, and mold-flow simulation with dynamic mechanical analysis is recommended.
| Downstream segment | Mandatory/typical standard | Test method or clause | Parameter or limit assessed |
|---|---|---|---|
| In-vitro diagnostic housings | ISO 10993-5:2009; ISO 10993-10:2021; ISO 13485:2016 | ISO 22196:2011 antibacterial activity | R ≥ 2.0 at 24 h; cytotoxicity viability ≥ 70% |
| Cosmetic jars and closures | EU 1223/2009; ISO 22716:2007; REACH 1907/2006 | ISO 4892-2 Method A | Gloss retention after 500 h artificial weathering |
| Oral care handles | EN 71-3:2019+A1:2021; ISO 22196:2011 | ISO 527-2; ISO 179-1/1eU | Bowing ≤ 0.5 mm over 180 mm length |
| Single-use cutlery and trays | EN 13432:2000; ASTM D6400-21; EU 10/2011 | ISO 178; EN 13432 Annex A disintegration | Overall migration ≤ 10 mg/dm²; disintegration ≥ 90% after 12 weeks |
| Writing instruments | EN 71-3:2019+A1:2021; REACH Annex XVII | ISO 178 flexural; EN 71-3 migration limits | Element migration below Category III limits |
| Personal care hygienic cases | RoHS 2011/65/EU; ISO 22196:2011 | ISO 4892-2 Method A; IEC 62321 XRF screening | Pb ≤ 1,000 ppm; Cd ≤ 100 ppm; R ≥ 2.0 |
The use of TE-7003 in single-use cutlery and cold food service is determined by the certification chain under EN 13432:2000 and ASTM D6400-21 rather than by resin price alone. For food contact in the EU, the finished article is assessed under Regulation EU 10/2011 with an overall migration limit of 10 mg/dm² in the appropriate food simulants. In the US, the compound or finished article must be covered by an applicable food contact notification or meet FDA 21 CFR 174–178 component requirements at the formulator level. The antibacterial additive in TE-7003 requires confirmation for food contact compliance in each jurisdiction. If the intended use is direct food contact, the supplier documentation for the antibacterial system must be reviewed against EU 10/2011 positive list entries and FDA clearances. The formulation addition ratio for cutlery production uses 100 wt% TE-7003 with up to 5 wt% post-industrial regrind and 2–3 wt% of an EN 13432-certified colorant masterbatch. Talc or calcium carbonate is not used above 0.5 wt% as a nucleating agent, because mineral fillers can compromise disintegration performance and create a rougher surface that accumulates food residue.
High-output cutlery molding demands multi-cavity cold runner tools with 16–32 cavities, heated sprue bushings, and tunnel gates of 0.8–1.2 mm. Clamp force for a 16-cavity fork mold is selected at 150–250 t depending on projected area and runner layout. Mold-flow simulation confirms pressure drop below 100 MPa. Barrel temperatures are rear 175–185°C, middle 185–195°C, front 195–205°C, and nozzle 200–210°C. The mold is cooled to 15–25°C to achieve rapid solidification and cycle times of 20–35 s. Ejection temperature is kept below 55°C to prevent fork tine distortion. Post-mold, the cutlery is not exposed to temperatures above 50°C during warehousing because PLA heat deflection temperature under ISO 75-2/B is below 60°C for unstressed parts. Terminal articles include forks, spoons, knives with serrated edges, cold food trays, and clamshell inserts. Mechanical performance is verified using ISO 178 flexural test on the finished cutlery. The bending force at break is specified by the purchaser, commonly 10–15 N for fork tines depending on tine length.
| Parameter | Thin-wall 0.6–1.0 mm | Thick-wall 1.5–2.0 mm |
|---|---|---|
| Desiccant drying | 80°C for 4–6 h, dew point ≤ -40°C, residual moisture ≤ 250 ppm | 80°C for 4–6 h, dew point ≤ -40°C, residual moisture ≤ 250 ppm |
| Rear zone | 175–185°C | 170–180°C |
| Center/middle zone | 185–195°C | 180–190°C |
| Front zone | 195–205°C | 190–200°C |
| Nozzle | 200–210°C | 195–205°C |
| Mold temperature | 25–35°C | 20–30°C |
| Fill velocity | 100–150 mm/s | 60–100 mm/s |
| Hold pressure | 60–80 MPa for 2–3 s | 50–70 MPa for 3–5 s |
| Back pressure | 0.5–1.0 MPa | 0.3–0.7 MPa |
| Screw surface speed | 60–120 rpm | 50–100 rpm |
| Cooling time | 6–10 s at 0.8 mm wall | 12–20 s at 1.8 mm wall |
| Residence time limit | ≤ 8 min at 210°C | ≤ 8 min at 210°C |
Pen barrels and mechanical pencil bodies molded from low-density PLA develop different gate-vestige geometry than ABS because the melt solidifies rapidly and the gate freezes before full packing is achieved. In writing instruments, the resin formulation is adjusted with 1–2 wt% color concentrate and 3–5 wt% of impact-modifier masterbatch when repeated clip insertion requires higher notch resistance. If the clip is overmolded from TPU directly onto the barrel, the barrel surface is corona treated at 36–40 mN/m and overmolding is performed within 4 h. The TPU selected is in Shore A hardness range 70–85 to prevent delamination caused by differential shrinkage. Compliance for writing instruments sold to the European market is anchored to EN 71-3:2019+A1:2021 for migration of aluminum, antimony, arsenic, barium, boron, cadmium, chromium, cobalt, copper, lead, manganese, mercury, nickel, selenium, strontium, tin, organic tin, and zinc. If the product is marketed to children under 14 years, EN 71-1 mechanical and physical requirements also apply. REACH Annex XVII and SVHC documentation are mandatory for the plastic and colorant masterbatch.
Injection molding uses a 20:1 L/D general-purpose screw with a shut-off nozzle and cold runner system. Barrel temperatures are set rear 170–180°C, center 180–190°C, front 190–200°C, and nozzle 195–205°C. Mold temperature is held at 20–30°C, and cooling time for a 10 mm diameter pen barrel with 1.2 mm wall is 8–12 s. Pen barrel concentricity is controlled by core pin cooling. Core deflection above 0.02 mm creates visible wall thickness variation and cap fit defects. The material is injected at moderate velocity 60–100 mm/s to avoid jetting in the long core. If jetting is observed, a tab gate or fan gate replaces the pinpoint gate. Terminal products include disposable pen barrels, mechanical pencil bodies, marker housings, and desktop organizer clips. For snap-fit cap retention, radial undercut is reduced from ABS design values by 20–30% because the lower elongation at break of PLA increases hoop-stress cracking risk at the cap mouth.
Personal care storage cases, toothbrush travel covers, and beauty tool handles are exposed to daily disinfection wipes and intermittent UV sanitizer cycles, which gradually roughen the PLA surface and alter antibacterial activity. The material is evaluated under ISO 22196:2011 before and after 2,000 wipe cycles with 70% ethanol and after 500 h of simulated UV exposure according to ISO 4892-2 Method A. A surface roughness change of more than 0.2 µm Ra after disinfection indicates hydrolytic etching and may require design changes, such as reducing texture depth to 0.015 mm or moving to satin surface finish SPI C1. The molding formula for this segment uses 100 wt% TE-7003 with 0.5–1.0 wt% lubricant masterbatch to stabilize ejector pin release. Additional slip agents are not increased above 1.0 wt% because they migrate to the surface and can reduce ISO 22196:2011 antibacterial activity.
These cases are molded with hot runner multi-cavity tools and polished cavities to minimize surface roughness. Melt temperature is kept at 195–205°C, mold temperature at 25–35°C, injection speed at 50–100 mm/s, and hold pressure at 60–80 MPa for 2–4 s. Shrinkage compensation for flat lids and bases requires gate placement at the geometric center. Off-center gating increases warpage beyond 0.5 mm over a 150 mm length. The terminal articles include toothbrush travel covers, reusable cosmetic brush guards, sanitizer bottle sleeves, and beard trimmer guard housings. Because these products may be sold with electronic personal care devices, compliance documentation includes RoHS Directive 2011/65/EU screening for lead, cadmium, mercury, and hexavalent chromium. In homogeneous materials, RoHS limits are 1,000 ppm for lead and 100 ppm for cadmium. XRF screening according to IEC 62321 should provide detection capability of 100 ppm for lead and 10 ppm for cadmium to maintain adequate signal-to-noise for compliance decisions.
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TERRAMAC TE-7003 Low Density Antibacterial Injection Molding Polylactic Acid is specified as a compounded polylactic acid (PLA) grade for high-cavitation injection molding, combining reduced part mass with an antibacterial surface function. The base polymer is a semicrystalline polyester derived from fermentative lactic acid; the low-density and antibacterial modifications are introduced during melt compounding and are intended to remain dispersed through the melt phase. The grade is positioned for rigid consumer, personal-care, packaging, and hygiene-related components that require measurable microbial reduction on the as-molded surface. Because the manufacturer’s public datasheet does not always publish full compositional and lot-specific mechanical values, molders should obtain a current certificate of analysis and qualify the material on the target tool before production release.
Material architecture in TERRAMAC TE-7003 is best understood as a two-level modification of a PLA matrix. The resin is an injection-molding-grade polylactic acid with melt rheology adjusted for thin-wall fill; the low-density designation indicates that the compounded specific gravity is lower than that of a comparable mineral-filled or high-crystallinity PLA grade, although the exact density-reduction strategy is not disclosed in all public regional datasheets. If the reduction is achieved through microcellular void formation, the packing phase behavior differs from that of solid PLA; if it is achieved through a low-density filler, the screw-recovery and venting characteristics will be closer to conventional filled systems. The antibacterial modification is typically an inorganic additive dispersed in the melt. Because silver-based antibacterial agents can be redox-sensitive at elevated temperature, local melt temperature and residence time become the primary limits on process robustness. The base polymer remains subject to hydrolytic degradation, so moisture control is not a secondary consideration.
Thermal degradation in PLA proceeds through random chain scission, lactide regeneration, and hydrolysis. At melt temperatures above 210 °C, molecular weight reduction can proceed at a rate that depends on residual moisture and residence time. Degradation products include lactide and oligomeric acids, which can accelerate further hydrolysis. In antibacterial grades, acid generation can also destabilize silver carriers and shift surface coloration. Processing windows should therefore be bounded by melt residence time and temperature, not only by fill pressure. Capillary rheometry at 190–210 °C for injection-molding PLAs typically yields a shear-thinning power-law index of 0.6–0.8; the consistency index depends on molecular weight, moisture, and the low-density modification. In a hot-runner high-cavitation tool, pressure drop across the manifold should be calculated with a shear viscosity measured at the actual gate shear rate. Because TERRAMAC TE-7003 incorporates a low-density modification, the melt compressibility can be higher than that of unmodified PLA; holding pressure should be profiled using gate-freeze time rather than a fixed timer.
Before melt processing, predrying in a desiccant dryer is specified for PLA-class materials to reduce moisture content below 250 ppm as measured by ISO 15512:2019. A drying schedule of 80 °C for 4 h with a dryer dew point of -40 °C or lower is class-typical. Hopper residence time at drying temperature should not exceed 6 h to avoid lactide formation and bridging. On production-scale injection molding lines with clamping forces from 800 kN to 3,000 kN, the principal processing bottleneck for low-density PLA grades is frequently not clamp force but screw recovery and gas venting, particularly when the density reduction creates a more compressible melt. Parting-line vents of 0.02–0.03 mm depth or vacuum-vented tools are often required to prevent burn marks and gas entrapment. Melt temperature should be profiled from rear to nozzle within the range 180–210 °C unless the certificate of analysis states otherwise; prolonged operation above 210 °C can accelerate molecular weight loss and reduce antibacterial activity.
Antibacterial agents in PLA compounds can lose efficacy through thermal decomposition, additive agglomeration, or surface migration during melt processing. Class-typical molding trials on reciprocating-screw machines indicate that melt temperatures above 210 °C and cumulative residence time beyond 10–15 min can shift ISO 22196:2011 activity from greater than 2 log10 reduction toward marginal performance; these values are not a substitute for TERRAMAC TE-7003 lot-specific data. Screw geometry with a three-zone general-purpose design, length-to-diameter ratio between 20:1 and 24:1, and compression ratio between 2.5:1 and 3.5:1 is commonly used. Back pressures of 2–8 MPa and moderate screw rotation are preferred to limit shear heating. Small gates can generate high local shear rates; mold-fill simulation should keep gate shear rates below 50,000 s⁻¹ as a starting limit for silver-based antibacterial systems, though published data for this specific configuration is limited.
Process capability studies on a 16-cavity hot-runner tool for similar low-density PLA grades have shown that shot-to-shot part mass can vary by 0.2–0.5% when screw recovery speed is too high, while melt volume-flow rate remains within specification. A recurring failure mode is gate blush caused by gas breakout from the melt at the gate; venting and lower melt temperature reduce the defect. Another observed failure mode is variability in antibacterial performance between cavities, often caused by non-uniform residence time in hot-runner manifolds. Cavity-specific validation is therefore required. The molder should establish a screw-recovery profile that avoids over-shearing the low-density melt and maintain a cushion between 3–6 mm.
The following class-typical reference data for unfilled injection-molding PLA are provided as a comparative baseline; they are not a certificate of analysis for TERRAMAC TE-7003 and should be superseded by lot-specific measurements.
| Parameter | Test method | Typical PLA class value | Relevance to TE-7003 |
|---|---|---|---|
| Melt volume-flow rate at 210 °C/2.16 kg | ISO 1133-1:2022 | 8–20 cm³/10 min | Controls thin-wall fill pressure; low-density modification may shift MVR relative to standard PLA. |
| Density | ISO 1183-1:2019 | 1.24–1.26 g/cm³ for unmodified PLA | TE-7003 is designated low-density; exact value must be confirmed from the certificate of analysis. |
| Tensile strength at yield | ASTM D638-14 | 50–65 MPa | Antibacterial and low-density modifications may place the value in the lower portion of this range. |
| Tensile modulus | ASTM D638-14 | 3.0–3.8 GPa | Lower part mass may be accompanied by reduced stiffness; rib design should compensate. |
| Flexural modulus | ASTM D790-17 | 3.0–3.6 GPa | Influences ejection force and warpage control. |
| Notched Izod impact | ASTM D256-23 | 2–4 kJ/m² | PLA remains notch-sensitive; sharp corners should be radiused. |
| Heat deflection temperature at 0.45 MPa | ASTM D648-18 | 50–60 °C amorphous; annealed can exceed 90 °C | Low-density structure may slow heat transfer; mold temperature and annealing determine final HDT. |
| Antibacterial activity | ISO 22196:2011 | ≥2 log10 reduction for qualifying claims | Must be revalidated on the final molded part, not on resin pellets alone. |
| Moisture content at molding | ISO 15512:2019 | ≤250 ppm | Higher moisture produces hydrolysis, viscosity loss, and surface defects. |
| Mold shrinkage | ASTM D955-21 | 0.3–0.6% amorphous, 0.8–1.2% crystalline | Shrinkage anisotropy can increase with low-density modifications; tool allowance should be confirmed. |
Compared with general-purpose PLA injection molding grades, TERRAMAC TE-7003 adds two concurrent property modifications: reduced part mass and antibacterial surface activity. The trade-off is a narrower processing window because both modifications alter melt rheology and thermal stability. In comparison with mineral-filled PLA, the low-density designation avoids the density increase associated with talc or calcium carbonate loadings of 10–20 wt%, which can raise compounded density to 1.35–1.45 g/cm³. Compared with antimicrobial ABS or polypropylene compounds, TE-7003 retains the bio-based carbon content and hydrolytic degradation profile of PLA; however, it also inherits PLA’s lower heat deflection temperature and requires crystallinity management or annealing for service above 55 °C under load. Bio-based carbon content can be quantified by ASTM D6866, while industrial composting certification, where applicable, is evaluated under EN 13432 or ASTM D6400; the antibacterial modification may affect compostability and must be confirmed with the grade-specific documentation.
When low-density modification is produced by microcellular void formation, the packing phase is shortened and sink marks are mitigated, but the insulating void structure reduces effective thermal diffusivity. Mold temperature then controls the freeze-off rate and the development of the amorphous skin. For thin-wall parts below 1.5 mm, mold temperatures of 20–40 °C are typical for fast cycle and dimensional stability; for sections above 3 mm or where heat resistance is specified, mold temperatures of 90–110 °C promote crystallization and raise heat deflection temperature. Part ejection and cycle time must accommodate the slower annealing step. In production tools, conformal cooling channels are beneficial when crystallinity is required in thick sections because non-uniform mold temperature can produce differential shrinkage and warpage.
Crystallization of PLA is relatively slow compared with polypropylene. Isothermal crystallization half-times for PLA can range from 2 min to 20 min depending on stereochemistry and nucleating agents. In low-density grades, the presence of voids or low-density fillers may further reduce thermal conductivity, slowing cooling and modifying crystallization. Cycle-time increases of 30–60 s can occur in thick sections when mold temperature is raised to induce crystallinity. Published data for TE-7003-specific crystallization half-times is limited; the molder should map crystallization behavior using differential scanning calorimetry on the actual compounded resin.
Before committing to production, the molder should obtain a current certificate of analysis for TERRAMAC TE-7003 and confirm three parameters: moisture content after drying, melt volume-flow rate at 210 °C/2.16 kg, and antibacterial log reduction after molding. The antibacterial claim is not established by the resin certificate alone; it must be revalidated on the final molded part geometry, because gate shear, mold temperature, and post-molding aging can affect additive distribution. Published data for this specific configuration is limited in public sources; therefore, a design of experiments across melt temperature, injection speed, and hold pressure is warranted. Molded parts intended for food-contact or medical applications require separate regulatory review under the applicable FDA 21 CFR, EU 10/2011, or ISO 10993-5 pathway, and antibacterial efficacy claims are subject to regional biocide registration requirements.