| HS Code | 145258 |
| Product Name | TERRAMAC TE-1030 High Impact Injection Molding Polylactic Acid |
| Material Type | Polylactic Acid (PLA) |
| Grade | High Impact Injection Molding |
| Density | 1.25 g/cm3 |
| Melt Flow Rate | 10 g/10 min at 190°C and 2.16 kg |
| Tensile Strength | 55 MPa |
| Tensile Elongation At Break | 100% |
| Flexural Modulus | 2.4 GPa |
| Flexural Strength | 80 MPa |
| Notched Izod Impact Strength | 15 kJ/m2 |
| Heat Deflection Temperature | 55°C at 0.45 MPa |
| Vicat Softening Point | 60°C |
| Melting Point | 170°C |
| Glass Transition Temperature | 60°C |
| Mold Shrinkage | 0.3% to 0.8% |
| Biobased Content | 100% |
As an accredited TERRAMAC TE-1030 High Impact 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-1030 is packaged in 25 kg moisture-barrier paper bags, 40 bags per pallet, shrink-wrapped for transport. |
| Container Loading (20′ FCL) | 20′ FCL, dry general-purpose container; palletized 25 kg bags or bulk bags, moisture-protected, secured stow for TERRAMAC TE-1030 PLA resin. |
| Shipping | TERRAMAC TE-1030 High Impact Injection Molding Polylactic Acid ships as non-hazardous solid resin pellets, typically 25 kg in sealed moisture-barrier bags or octabins, palletized. Store dry at ambient temperature, away from heat, moisture, and direct sunlight. Standard freight; no dangerous goods classification required. |
| Storage | Store TERRAMAC TE-1030 in a cool, dry, well-ventilated area away from direct sunlight, heat sources, and moisture. Keep containers tightly sealed to prevent hydrolysis and degradation. Avoid prolonged storage near strong oxidizers, acids, or bases. Minimize dust and static. Maintain ambient temperature and humidity per SDS; rotate stock FIFO. Follow manufacturer’s SDS and local regulations. |
| Shelf Life | Shelf life is 12 months from manufacture when stored unopened in a cool, dry place, away from moisture and sunlight. |
Reusable food-contact cutlery and dinnerware are converted from TERRAMAC TE-1030 by injection molding only after pellet moisture is reduced below <250 ppm through desiccant drying at 80 °C for 4 h; failure to do so on production lines produces splay at the gate, erratic melt flow, and embrittlement near the sprue detectable by ISO 1133-1:2022 melt flow ratio shift. Compliance for food-contact articles is governed by FDA 21 CFR 177.1520 for PLA homopolymer, EU 10/2011 with an overall migration limit of 10 mg/dm², China GB 4806.7-2016 for food-contact plastic articles, and REACH Annex XVII restrictions where applicable. The formulation addition ratio is controlled by food-contact lot traceability: virgin TERRAMAC TE-1030 pellets may be blended with 0–15 wt% post-industrial regrind from the same production line, while post-consumer regrind is excluded unless explicitly authorized under the relevant food-contact regulation; color masterbatch is added at 1–3 wt%, and food-grade slip/antiblock masterbatch is introduced at 0.2–1.0 wt%. Downstream processing is performed on reciprocating-screw injection molding machines with L/D 20:1–24:1, compression ratio 2.2:1–3.0:1, reverse-temperature profile from 180 °C at the feed throat to 205–210 °C at the nozzle, and mold temperature held at 20–40 °C; injection pressure is normally 80–120 MPa, and clamp force is calculated at 4–5 tons/in² of projected area because thin-walled cutlery ribs require rapid filling while excessive shear raises local melt temperature above the 210 °C ceiling at which random chain scission accelerates. Terminal article types produced in this segment include forks, knives, spoons, plates, bowls, and shallow trays for institutional food service.
A specific process conflict arises when regrind content exceeds 15 wt% because retained heat history can lower notched Izod impact values under ISO 180:2019 below thresholds required for repeated dishwashing rack abuse. Shot size is maintained at 50–70% of barrel capacity to keep melt residence time under 8 min; if automation extends cycle time, the rear barrel zone is reduced to 170–180 °C to limit degradation. Cold-runner tooling is preferred over hot-runner for food-contact serviceware because hot-runner dead spots can retain degraded PLA that later releases into the melt stream and increases notched Izod variability. Published data for TERRAMAC TE-1030 specifically across repeated regrind cycles is limited; processors therefore qualify each regrind lot by melt flow rate under ISO 1133-1:2022 and notched impact under ISO 180:2019 before batch release.
| Process variable | Recommended boundary condition | Reference method or equipment |
|---|---|---|
| Pellet moisture after drying | <250 ppm | ISO 15512:2019; desiccant dryer to -40 °C dew point |
| Drying temperature and time | 80 °C, 4 h | Desiccant-bed hopper dryer |
| Melt temperature | 180–210 °C | IR pyrometer; melt pressure transducer |
| Mold temperature | 20–40 °C | Pressurized water thermolator |
| Shot size | 50–70% of barrel capacity | Reciprocating screw; L/D 20:1–24:1, compression 2.2:1–3.0:1 |
| Melt residence time | ≤8 min at full melt; preferred ≤5 min | Shot-to-barrel capacity ratio and cycle time audit |
Thick-walled cosmetic jars and caps impose a longer heat-removal path than cutlery, which shifts the process conflict from shear heating to gate freeze time and pack pressure decay. Regulatory references for cosmetic packaging include EU 1223/2009, which obligates the responsible person to ensure packaging does not compromise product safety through migration, 94/62/EC for packaging heavy metal limits of 100 mg/kg sum of lead, cadmium, mercury and hexavalent chromium, and REACH Annex XVII for restricted substances. If the jar is promoted for food-adjacent balm use, FDA 21 CFR 177.1520 may also apply. The formulation addition ratio for cosmetic packaging normally uses 1.0–2.5 wt% color masterbatch and 0.1–0.3 wt% mold release; pearlescent effect masterbatch may replace standard color at 1–2 wt%, but any filler or visual-effect additive must be re-qualified because talc or metal-flake nucleants can increase crystallization rate and freeze the gate before the packing phase is complete. The downstream production process uses a melt temperature of 185–205 °C, mold temperature 25–35 °C, hold pressure 60–80 MPa, and cooling time of 20–45 s depending on wall thickness from 2 mm to 6 mm; thick-wall tools require valve-gate hot runners with individual nozzle temperature control and in-cavity pressure sensors to detect gate freeze by watching pressure decay. Terminal finished product types include cosmetic cream jars of 30–200 mL, closure caps, airless dispenser overcap shells, and compact cases.
Gate freeze time is not a single material value but a function of tool steel temperature, gate diameter, and melt compressibility. For PLA grades in a 2 mm gate on a 5 mm wall, in-cavity pressure transducer studies typically report gate freeze between 2 s and 6 s at 30 °C mold temperature, but published data for TERRAMAC TE-1030 in this specific configuration is limited; therefore process development must map gate freeze empirically on the target tool. A critical operational boundary is chemical resistance: PLA formulations are not universally compatible with ethanol-rich or fragrance-loaded cosmetic formulas; any formulation containing more than 20 wt% ethanol or containing terpenes such as limonene should be evaluated for environmental stress cracking under ASTM D543-21 before commercial approval.
Toy components molded from TERRAMAC TE-1030 are subject to stricter traceability and heavy-metal restrictions than general household goods because colorants, nucleants, and regrind must not introduce elements above the migration limits in EN 71-3:2019+A1:2021 or the soluble heavy metal limits in ASTM F963-23. Mechanical integrity is evaluated under EN 71-1 drop, torque, and tension tests, while REACH Annex XVII and US CPSIA phthalate and heavy-metal restrictions apply. The formulation addition ratio typically permits 1–4 wt% certified toy-grade color concentrates, while regrind is restricted to ≤10 wt% post-industrial material of known formulation; post-consumer regrind is excluded because its elemental composition cannot be demonstrated compliant. Processing on injection molding machines uses melt temperatures of 190–210 °C, mold temperatures of 20–35 °C, and injection speeds sufficient to fill ribs and thin walls but not so high that shear-induced molecular weight reduction creates weak weld lines near gate points. Terminal finished article types in this segment include building blocks, puzzle pieces, toy cooking accessories, and figurine components.
Color masterbatch dispersion is a more critical control variable in toys than in single-color cutlery because inorganic pigment agglomerates can act as stress-concentration sites during EN 71-1 drop tests. The processor should require masterbatch suppliers to provide sieve residue data under ISO 787-7 and perform test moldings at the stated addition ratio before production batch approval. A defined limitation is impact performance relative to ABS or impact-modified polypropylene: although TERRAMAC TE-1030 is a high-impact PLA grade, toy designs requiring repeated free-fall from heights above 1 m onto concrete should be validated with production-run samples because notched impact retention after molding is influenced by moisture, melt residence time, and color masterbatch dispersion uniformity.
| Downstream segment | Primary compliance references | Key test or limit |
|---|---|---|
| Food-contact cutlery and dinnerware | FDA 21 CFR 177.1520; EU 10/2011; China GB 4806.7-2016 | Overall migration 10 mg/dm²; batch traceability of regrind |
| Cosmetic jars and caps | EU 1223/2009; 94/62/EC; REACH Annex XVII | Packaging heavy metals sum 100 mg/kg; compatibility ASTM D543-21 |
| Toy components | EN 71-3:2019+A1:2021; ASTM F963-23; CPSIA | Element-specific migration limits in mg/kg |
| Horticultural fasteners and tags | EN 13432; ISO 14855-2; EN 17033 | Biodegradation ≥90% within 6 months under controlled composting |
| Consumer electronics accessories | RoHS 2011/65/EU Annex II; IEC 62321-3-1:2013; UL 94 HB | Lead 0.1%; cadmium 0.01% |
| Retail fixtures and garment hangers | REACH; EU 94/62/EC; NFPA 701 where relevant | SVHC screening; store-specific flame certificate |
Horticultural clips and plant identification tags produced from TERRAMAC TE-1030 are used where industrial compostability is a stated end-of-life route, but the degradation pathway must be specified with technical precision to avoid overstating soil removal. The relevant compliance standards are EN 13432 for packaging recoverable by composting, ISO 14855-2 for ultimate aerobic biodegradation under controlled composting conditions, EN 17033 only where ambient soil biodegradation is a specific claim, REACH Annex XVII, and national fertilizer or agricultural input regulations for colored articles left in field soil. The formulation addition ratio for durable outdoor horticultural articles is 1–3 wt% carbon black masterbatch for UV-shielding and 0.3–1.0 wt% UV stabilizer if the clip must survive multiple seasons; however, UV stabilizer addition above 1.0 wt% may slow compost disintegration, so the downstream buyer must decide whether UV durability or compostability has priority. The downstream production process uses thin-wall injection molding with melt temperature 190–210 °C, mold temperature 15–35 °C, and fast injection to fill long tag flow paths without freeze; clip tools are typically cold-runner multi-cavity designs because hot-runner residence time degrades PLA and reduces compostability test reproducibility. Terminal finished product types include plant clips, grafting clips, tree ties, plant identification tags, and seedling tray corner reinforcements.
The critical kinetic limitation is that PLA hydrolysis in ambient soil at 20–30 °C is extremely slow compared with the 58 °C composting environment specified in ISO 14855-2. A statement such as “degradable in soil” is not substantiated without EN 17033 data and may be technically misleading for this material. Processors should retain molding rejects and conduct EN 13432 disintegration trials on each product geometry because part thickness and crystallinity after rapid cooling can delay disintegration under industrial compost conditions.
Low-power consumer electronics accessory enclosures and keyboard top covers are molded from TERRAMAC TE-1030 where service temperatures remain below 55 °C and where flammability requirements do not exceed UL 94 HB. Compliance for this segment is dominated by RoHS 2011/65/EU Annex II for restricted substances, IEC 62321-3-1:2013 for screening of lead, mercury, cadmium, and hexavalent chromium, REACH Annex XVII, and UL 94 HB rather than UL 94 V-0 because unmodified PLA grades typically cannot meet V-0 without halogen-free flame retardants that alter mechanical properties and may invalidate environmental claims. The formulation addition ratio in this segment uses 1–3 wt% color masterbatch and 0.2–0.8 wt% anti-scratch additive; if a soft-touch effect is required, overmolding is avoided unless the soft elastomer layer is thermally compatible, because PLA melt adhesion to TPE overmolding systems varies substantially across suppliers. Downstream production is run on electric injection molding machines with melt temperature 190–210 °C, mold temperature 20–30 °C, and packing pressure controlled to avoid warpage across long flat covers; weld lines formed around holes and bosses are the limiting mechanical features and should be moved away from high-bending-load zones by gate repositioning rather than by excessive fill speed. Terminal finished article types include phone cases, e-reader back shells, mouse top covers, and keyboard keycaps for low-temperature consumer devices. The operational boundary is explicit: this material is not suitable for power adapter housings, laptop structural frames, or any component that experiences sustained contact above 55 °C or requires UL 94 V-0 fire protection.
Garment hanger and point-of-sale display components are produced from TERRAMAC TE-1030 in multi-cavity cold-runner tools where cycle time, ejection force, and drop resistance after ejection determine process viability. Compliance requirements in this segment are commercial rather than food-contact: REACH registration and SVHC screening, EU 94/62/EC where the article is packaging or packaging-like at end of life, RoHS 2011/65/EU if the hanger contains electrical components such as integrated lighting or digital display elements, and local store fixture flammability standards such as NFPA 701 for textile-adjacent displays in North America. The formulation addition ratio is 0.1–0.5 wt% processing aid to control ejection force, plus 1–3 wt% color masterbatch; if higher bending stiffness is required for thin hanger profiles, 5–10 wt% mineral filler can be compounded, but the resulting notched Izod value under ISO 180:2019 must be re-qualified because filler addition reduces impact retention and makes thin sections more susceptible to breakage during mold ejection. Processing uses melt temperature 190–210 °C, mold temperature 20–35 °C, and clamp force calculated at 3–5 tons/in² projected area; high-volume production tools are typically 8- to 32-cavity cold-runner systems with mold temperature uniformity critical for consistent shrinkage and hanger hook dimensional accuracy. Terminal finished article types include garment hangers, shelf brackets, display hooks, and signage frames for retail environments. This segment does not require compostability certification, so regrind ratios up to 20 wt% may be used if mechanical property retention is monitored by MFR under ISO 1133-1:2022 and notched Izod under ISO 180:2019.
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TERRAMAC TE-1030 is a high-impact injection molding grade of polylactic acid supplied by Unitika Ltd. within the TERRAMAC biobased polymer series. The formulation is intended for injection-molded rigid parts where unmodified PLA exhibits insufficient notched impact resistance under service loading. Because the material belongs to the impact-modified PLA class, the expected property envelope includes reduced tensile modulus and increased notched impact energy relative to standard injection-molding PLA; the exact magnitude of that shift is modifier-dependent and must be taken from the current technical data sheet for TE-1030. Published data for this specific configuration is limited in open technical literature, and production mold-filling studies should therefore precede tooling commitments.
The matrix is based on lactic acid repeat units, with an elastomeric or compatibilized dispersion producing the high-impact behavior. Melt flow rate is commonly measured under ISO 1133-1:2022 at 210 °C and 2.16 kg; injection-molding PLA grades typically occupy a melt flow rate band of 5–25 g/10 min. A single-point MFR value does not capture shear thinning. Capillary rheometry under ISO 11443:2021 or ASTM D3835-16 is used to establish the viscosity curve at shear rates typical of thin-wall filling. During mold filling, shear heating in the runner and gate can reduce melt viscosity by several percentage points; excessive shear generated by undersized gates may induce chain scission and surface splay.
A desiccant-wheel dryer with a dew point of ≤ -40 °C is required before processing. The pellets are not transported directly from humidity-uncontrolled storage into the feed throat. Drying at 75–85 °C for 4–6 h reduces residual moisture below 250 ppm, measured by ISO 15512:2019 Karl Fischer titration. At storage relative humidity above 60%, sealed hopper transfer and closed conveying are imposed. Drying above 90 °C risks pellet sintering and bridging in the hopper. Moisture in the melt causes hydrolytic chain scission, viscosity loss, splay, and a measurable reduction in notched impact energy.
| Parameter | Operating band | Equipment or method |
|---|---|---|
| Drying temperature | 75–85 °C | Desiccant-wheel dryer |
| Drying time | 4–6 h | Closed-conveying hopper |
| Dew point | ≤ -40 °C | Air dryer monitor |
| Residual moisture | < 250 ppm | ISO 15512:2019 |
| Melt temperature | 190–210 °C | Injection cylinder, rear to nozzle |
| Mold temperature | 25–40 °C | Water thermolator |
| Back pressure | 0.3–0.7 MPa | Hydraulic injection unit |
| Screw compression ratio | 2.0:1–2.5:1 | General-purpose screw, L/D 20:1–24:1 |
When cylinder temperatures exceed 220 °C, thermal degradation of PLA proceeds by random chain scission and lactide regeneration. The degradation rate accelerates with temperature and residence time. On a 36 mm screw machine with L/D 20:1, melt residence time at 200 °C should be held below 5 min; longer cycles with large shot-to-barrel ratios produce yellowing, viscosity reduction, and loss of impact strength. The practical melt set point is therefore placed near 200 °C, with an upper working limit of 210 °C; the processing window in the upper melt-temperature region is approximately ±5 °C. Hot runner manifolds should be temperature-mapped to avoid local residence-time broadening in dead spots. If the melt is held above 220 °C during a stoppage, purging at reduced temperature is required before restart.
Mold temperature exerts a first-order effect on surface gloss, shrinkage anisotropy, and post-mold dimensional stability. A water thermolator set to 25–40 °C is common for impact-modified PLA; lower mold temperatures freeze the skin quickly and reduce cycle time, while higher mold temperatures improve knit-line strength and reduce internal stress. Mold shrinkage measured under ASTM D955 typically falls near 0.3–0.5% in flow and 0.4–0.6% transverse, but shrinkage is geometry-dependent and is not a resin constant. Gate location, wall thickness variation, and molded-in stress dominate warpage. A mold-temperature uniformity of ±2 °C across the cavity is recommended for flat parts with length above 200 mm.
Screw geometry for TERRAMAC TE-1030 should avoid high-shear compression. A general-purpose screw with L/D 20:1–24:1 and compression ratio 2.0:1–2.5:1 is used; compression ratios above 2.5:1 can generate shear heating sufficient to push melt temperature toward the degradation boundary. Back pressure is held at 0.3–0.7 MPa to maintain melt density without excessive work input. Injection pressure commonly falls in the 70–100 MPa range on direct-pressure hydraulic machines, although the value is cavity dependent. Clamp force is calculated from projected area and cavity pressure, not from the resin alone; a typical multiair-cavity tool with 2–3 mm wall sections may require 60–120 tons depending on runner balance, gate type, and fill pressure. A screw cushion of 3–5 mm is maintained to avoid melt decompression and gas bubble entrapment.
Comparative mechanical testing under ISO 527-2:2012 and ISO 180/1A defines the product difference relative to unmodified PLA. Unmodified injection-molding PLA typically exhibits tensile modulus near 3.0–3.5 GPa and notched Charpy impact energy of 3–5 kJ/m². Impact-modified PLA of the TERRAMAC TE-1030 class typically shifts tensile modulus downward to 2.0–2.5 GPa and raises notched Charpy impact energy to 10–30 kJ/m², with tensile elongation increasing from approximately 3–5% to 10–40%. These are class-level ranges for impact-modified PLA, not certified values for TE-1030. The improvement ratio is not uniform below 0 °C; low-temperature impact remains lower than that of many petroleum-based amorphous thermoplastics. Flexural modulus measured under ISO 178 decreases in the same direction. The practical consequence is that TERRAMAC TE-1030 is suited to stiff but less brittle components where standard PLA fails by crack initiation at notches or bosses.
When an elastomeric impact modifier is dispersed into PLA, the cost is reduced heat resistance. Heat deflection temperature measured under ASTM D648 or ISO 75-2 commonly remains below 60 °C for non-annealed impact-modified PLA. Annealing in a constraining fixture at 100 °C for 20–30 min raises crystallinity and increases heat deflection by 20–30 °C, but the part undergoes dimensional change and must be validated in the finished geometry. Vicat softening temperature under ISO 306 is also thickness-dependent and should not be used interchangeably with heat deflection data. For service above 60 °C, molded part performance should be verified under load because creep modulus decreases with temperature.
When annealing is selected for TERRAMAC TE-1030 parts, the part must be held in a dimensionally stable fixture to control shrinkage. Cold-crystallization exotherms during heating are measured by differential scanning calorimetry under ISO 11357-1 and ISO 11357-3. The annealing temperature is placed between the glass transition and the cold-crystallization peak, typically near 100 °C. The resulting crystallinity raises heat deflection and chemical resistance but also increases brittleness at low strain rates. Dimensional change of 0.2–0.5% can occur during annealing, which is why post-mold inspection templates are used instead of relying on cavity dimensions.
Exposure of molded high-impact PLA parts to hot water above 60 °C causes hydrolytic degradation of the ester backbone. Alkaline cleaning agents and strong amine-based solutions accelerate surface attack. Solvent resistance testing under ISO 175 should be performed when incidental contact with oils, greases, or cleaning fluids is expected. Aliphatic hydrocarbons and mineral oils generally show limited effect at ambient temperature, while ketones, chlorinated solvents, and hot aqueous acid or alkali conditions degrade the surface. Outdoor exposure is not automatically acceptable; ultraviolet weathering under ISO 4892-2 is required for applications receiving direct sunlight. Continuous service above 60 °C is not recommended unless the part is annealed and the load is validated for creep.
Regulatory status for impact-modified PLA is formulation-specific. Conformance to REACH under EC 1907/2006 and RoHS 2011/65/EU must be confirmed from the supplier’s current certification. Biobased carbon content can be verified by ASTM D6866-22 or EN 16640, but the net biobased fraction of TE-1030 depends on whether the impact modifier is petroleum-derived. Industrial compostability under EN 13432 is not automatically granted to injection-molded parts; thick-walled parts above 2 mm may fail the disintegration criterion even when the resin formulation is certified. Food-contact clearance under EU No 10/2011 or FDA 21 CFR 177.1520 is grade-specific and is not assumed for impact-modified PLA unless the supplier has submitted the exact product for compliance review.
Where TERRAMAC TE-1030 diverges most from petroleum-based high-impact resins is in processing temperature and moisture handling. ABS and HIPS process at melt temperatures above 220 °C; impact-modified PLA processes near 200 °C and therefore reduces thermal energy input. The same advantage becomes a boundary under elevated service temperature, where PET, ABS, and polycarbonate retain modulus above 80–120 °C. Against other biobased tough compounds, TE-1030 occupies a stiffness-toughness position closer to PLA than to ductile low-modulus materials such as PBAT- or PBS-based compounds. Flexural modulus under ISO 178 remains approximately one order of magnitude above typical PBAT systems, while notched impact energy remains below that of highly ductile PBAT/PBS blends. The selection criterion is therefore whether the part requires creep resistance and stiffness with moderate impact enhancement, or deep ductility at the expense of rigidity.