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TERRAMAC TE-1070 Flexible High Flow Injection Molding Polylactic Acid

    • Product Name: TERRAMAC TE-1070 Flexible High Flow Injection Molding Polylactic Acid
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 897147
    Materialtype Polylactic Acid (PLA)
    Processingmethod Injection Molding
    Flexibility Flexible
    Flowability High Flow
    Biobasedcontent 100%
    Density 1.25 g/cm3
    Meltflowrate 20 g/10 min (190°C, 2.16 kg)
    Tensilestrength 30 MPa
    Tensileelongation 200%
    Flexuralmodulus 1000 MPa
    Notchedizodimpact 10 kJ/m2
    Heatdeflectiontemperature 55°C (0.45 MPa)
    Vicatsofteningpoint 60°C
    Meltingpoint 170°C
    Glasstransitiontemperature 60°C
    Moldshrinkage 0.3-0.5%
    Moistureabsorption 0.1%
    Melttemperature 180-210°C
    Moldtemperature 20-40°C
    Dryingtemperature 80°C
    Dryingtime 4 h

    As an accredited TERRAMAC TE-1070 Flexible High Flow Injection Molding Polylactic Acid factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing TERRAMAC TE-1070 supplied in 25 kg moisture-barrier paper bags, palletized, for flexible high-flow injection molding polylactic acid.
    Container Loading (20′ FCL) 20′ FCL: TERRAMAC TE-1070 flexible high-flow injection molding polylactic acid in palletized, moisture-protected bags, securely stowed for dry ocean transport.
    Shipping TERRAMAC TE-1070 is a non-hazardous polylactic acid resin. It is not regulated for transport by DOT, IMDG, IATA, or ADR. Standard shipping uses sealed moisture-barrier 25 kg bags, palletized and shrink-wrapped. Store cool and dry, avoiding heat, moisture, and direct sunlight. Handle with normal industrial hygiene.
    Storage Store indoors in a cool, dry, well-ventilated area, away from direct sunlight, heat, and ignition sources. Keep in sealed original packaging to prevent moisture uptake, which can degrade PLA. Maintain low humidity and moderate temperature. Avoid strong acids, bases, and solvents. Protect from physical damage. Use FIFO rotation; dry resin before processing if moisture-exposed.
    Shelf Life Shelf life is 12 months from manufacture when stored unopened in a cool, dry place, protected from moisture and heat.
    Application of TERRAMAC TE-1070 Flexible High Flow Injection Molding Polylactic Acid

    Thin-wall cutlery and portion-cup injection molding using TERRAMAC TE-1070 is configured around a melt-temperature envelope of 190–210 °C, a mold temperature of 15–30 °C, and a residual moisture target below 250 ppm as measured by Karl Fischer titration prior to plastication. The high-flow flexible grade permits filling of cavity L/t ratios exceeding 150:1 at wall thickness below 1.2 mm, but the processor must use screw geometry with a compression ratio of 2.5:1 to 3:1 and a non-return valve clearance of less than 0.05 mm to avoid shot-weight drift. In production-scale runs on a 1200 kN hydraulic injection molding machine, the primary failure modes are splay caused by moisture above 300 ppm, gate blush from excessive injection velocity above 250 mm/s, and warpage when mold cooling is unbalanced by more than 5 °C between core and cavity. The formulation is run at 100 wt% TERRAMAC TE-1070; where tinting or opaque coloring is required, a PLA-carrier masterbatch is metered at 1–3 wt%, with loadings above 3 wt% necessitating a revalidation of melt mass-flow rate per ISO 1133-1:2022 because pigment concentrates can reduce spiral-flow length by up to 8% in fast-cycling thin-wall tools. Compliance for food-contact articles is assessed under EU Regulation (EU) No 10/2011 with an overall migration limit of 10 mg/dm² and specific migration limits for any authorized additives, while biodegradability claims for single-use tableware are tested via EN 13432 or ASTM D6400 using ISO 14855-1 aerobic composting; industrial compostability requires ≥90% disintegration after 12 weeks and ≥90% biodegradation within 180 days. Downstream injection molding for this segment uses hot-runner edge gating with valve-gate sequencing, injection pressures of 70–110 MPa, hold pressures of 40–70 MPa, and cycle times between 18 s and 35 s depending on part weight. Terminal articles include multi-packs of spoons, forks, knives, portion cups, cold-use lids, and airline meal trays requiring material recovery through controlled composting streams rather than conventional landfill.

    Compliance matrix for thin-wall foodservice articles molded from TERRAMAC TE-1070
    FrameworkTest method or designated annexCritical value or condition
    EU Regulation (EU) No 10/2011EN 1186-1 overall migration≤10 mg/dm²
    EN 13432ISO 14855-1 aerobic compost≥90% biodegradation in 180 days
    ASTM D6400ASTM D5338 compost≥90% CO₂ conversion
    ISO 1133-1:2022Melt mass-flow rate 210 °C, 2.16 kgVerify against supplier certificate for each batch

    In cosmetic closures and cream jar injection molding, the repeat flexural opening of snap-fit lids places the material under intermittent stress at the hinge, so the processor selects TERRAMAC TE-1070 for its combination of hinge flex resistance and a melt flow rate high enough to fill multi-cavity tools without excessive orientation. The formulation used in high-gloss cosmetic packaging is typically 100 wt% neat TERRAMAC TE-1070; if custom shades are required, a PLA-compatible color masterbatch is added at 0.5–2 wt%, and the melt is homogenized with a dynamic mixer or static mixer in the nozzle to prevent visible streaking. The downstream process employs polished P20 or S136 mold cavities with surface finishes at or finer than SPI A-2, heated sprue bushings, and valve-gated hot runners; melt temperature is held at 195–215 °C and mold temperature at 25–40 °C to preserve surface gloss while limiting sink marks on thick bosses. Injection speed is lowered in the first 30% of filling to prevent jetting, then increased to 120–200 mm/s for the remaining path, with hold pressure adjusted until gate freeze occurs at 2–4 s after transfer. Compliance for cosmetic articles is directed by Regulation (EC) No 1223/2009 for materials intended to contact cosmetic formulations, REACH Regulation (EC) No 1907/2006 Annex XVII restrictions, and ISO 22715:2006 for packaging requirements where visual and functional integrity are specified; heavy-metal migration from pigmented lots is verified by ISO 11885 or equivalent acid-extraction methods. Terminal finished product types include snap-fit cream jars, outer caps, inner caps, airless pump collars, and overcap sets for skin-care and color-cosmetic lines where mono-material PLA recovery routes are preferred over multi-resin assemblies.

    Where Does Cavity Pressure Drop Shift Weld-Line Integrity in Thin-Wall Wearable Electronics Enclosures?

    For non-electrical wearable accessories and thin-wall enclosures, TERRAMAC TE-1070 is processed at a melt temperature of 200–220 °C with mold temperatures of 20–35 °C. The main process conflict arises when two melt fronts converge behind a core pin or speaker hole; the weld-line strength of flexible PLA is sensitive to holding pressure and local pressure drop. On an electric injection molding machine with a 1400 kN clamp and a screw diameter of 28 mm, cavity pressure sensors placed at the last 15% of flow length record peak pressures of 35–55 MPa; if cavity pressure at the weld line falls below 30 MPa, tensile strength measured on ISO 527-2:2012 Type 1A specimens machined from the weld zone can decline by more than 25% relative to the bulk. The formulation ratio is maintained at 90–100 wt% TERRAMAC TE-1070, with 0–10 wt% clean post-industrial regrind or a PLA-compatible impact modifier; the use of non-PLA impact modifiers above 5 wt% is avoided because crystallization-rate suppression can lead to post-ejection shrinkage beyond 1.5%, although published data for this specific configuration is limited and molders should verify on their own tooling. Downstream production uses sequential valve-gated hot runners with gate diameters of 0.8–1.5 mm, gas counterpressure where gloss differences are problematic, and post-molding conditioning at 23 °C/50% RH for 48 h before dimensional inspection. Compliance is anchored to Directive 2011/65/EU (RoHS) Annex II restricted substances and REACH candidate-list screening; where the enclosure carries a user-contact surface, skin irritation assessment follows ISO 10993-23 or a validated in vitro alternative as specified by the downstream device quality system. Terminal articles include phone case shells, earbud charging-case covers, smartwatch band links, and rigid frames for passive wearable straps where the article is not subjected to sustained electrical safety requirements but must meet dimensional stability and drop-impact expectations.

    Horticultural Clip Retention Force Is Governed by Crystallization Rate During Short Cooling Windows

    For plant clips, plant tags, and nursery propagation components, the short cycle-time demands of horticultural injection molding impose a narrow crystallization window because the cold mold freezes the surface before the core can develop spherulitic structure. The formulation is processed at 100 wt% TERRAMAC TE-1070; when color is required for crop-line identification, 1–2 wt% of a PLA-compatible masterbatch is dosed, and loadings above 2 wt% are suspected to reduce clip opening force by changing the cooling-rate-dependent crystallinity, although published data for this specific configuration is limited. The downstream process should pre-dry the resin at 80 °C for 4–6 h to <250 ppm moisture, use a mold temperature of 10–20 °C, an injection speed of 150–250 mm/s, and a holding pressure of 45–65 MPa; cycle times for 0.8–1.5 g clips are typically 12–20 s on a 900 kN toggle-clamp machine. The primary failure mode in field use is premature fracture at the hinge after repeated opening; this is controlled by verifying the hinge section thickness at 0.25–0.45 mm and by avoiding sharp corners at the gate remnant. Compliance for horticultural articles marketed in the EU is evaluated under REACH Annex XVII and, for compostable claims, EN 13432 or ASTM D6400; if the article is intended to degrade in soil, additional ecotoxicity testing under OECD 208 is used by some certification bodies, but such soil-degradation claims are not automatically covered by industrial compostability certifications. Terminal finished product types include vine clips, grafting clips, plant labels, pot tags, seed tray markers, and temporary propagation trays used inside greenhouses where high humidity and moderate temperature accelerate any uncontrolled hydrolysis if the articles are stored beyond one growing season.

    For multi-cavity writing instrument barrels and snap-cap stationery components, the high spiral-flow length of TERRAMAC TE-1070 enables filling of tools with flow-path-to-thickness ratios above 180:1 at wall thickness of 1.0–1.8 mm, but the barrel diameter tolerances must be held within ±0.05 mm to maintain cap fit. The compounding ratio is maintained at 100 wt% TERRAMAC TE-1070; in tinted versions, 2–4 wt% PLA-based masterbatch is added, and the blend is dried to <250 ppm moisture before molding to prevent die build-up and surface streaking. The production process uses valve-gated hot-runner systems with 16–32 cavities, mold temperatures of 20–30 °C, melt temperatures of 190–210 °C, and holding pressures of 50–75 MPa; post-molding operations include pad printing or laser marking, and ultrasonic welding for end caps where energy directors are molded at 60° included angle. Compliance for stationery articles placed on the EU market is assessed against REACH Annex XVII, and if the article is intended for children under 14 years, the finished component must meet EN 71-3 migration limits for nineteen elements; writing instruments used by children may also fall under EN 71-1 mechanical safety requirements. Terminal articles include refillable pen bodies, snap caps, marker bodies, eraser retainer tubes, and correction-tape housings, where the flexible PLA grade provides cap retention without an elastomeric insert and allows single-material assembly for simplified recovery.

    When Disposable Personal-Care Tool Bodies Require Controlled Hydrolytic Stability During Storage

    For single-use personal-care tool bodies such as facial brush bases, cosmetic applicator frames, and disposable spatula handles, TERRAMAC TE-1070 can be injection molded only when moisture is controlled below 250 ppm and the residence time in the barrel is kept below 6 min, because the flexible PLA backbone undergoes hydrolytic chain scission at melt temperatures above 210 °C when moisture exceeds 300 ppm. The formulation ratio is set at 100 wt% TERRAMAC TE-1070, and no external lubricant or release agent is added; if mold release is necessary because of textured surfaces, a non-amine, non-soap release is used at <0.1 wt% of the shot weight or avoided entirely through draft angles of 1–2°. The downstream process uses a 1100 kN servo-electric injection molding machine with a low-compression screw of 22 mm diameter, barrel temperatures profiled from 180 °C at the feed throat to 205 °C at the nozzle, mold temperatures of 15–25 °C, and injection speeds of 80–160 mm/s; because the part may be exposed to skin-care oils during use, post-molding dimensional checks are performed after 48 h at 23 °C/50% RH and again after 24 h immersion in a reference emollient to screen for excessive swelling. Compliance for cosmetic-contact tools is governed by Regulation (EC) No 1223/2009 for finished product safety, REACH Annex XVII restrictions, and ISO 22716:2007 for manufacturing hygiene controls in the filling environment; where the tool body is painted or decorated, the printed layer is screened under EN ISO 2409 cross-cut adhesion and ISO 2812-1 chemical resistance. Terminal finished product types include single-use facial brush handles, cosmetic applicator bases, disposable spatula handles for cream scoops, and promotional beauty-tool bodies intended for short-term use before disposal through industrial composting where local collection permits.

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    Certification & Compliance
    More Introduction

    TERRAMAC TE-1070 is a flexible high-flow injection molding grade of polylactic acid (PLA) supplied in pellet form for conventional reciprocating-screw injection molding machines. The material is specified for thin-wall and multi-cavity applications in which standard PLA grades show short shot formation or excessive part stiffness after demolding. The product’s technical identity is established by melt volume flow rate under ISO 1133-1:2022 at 210 °C with a 2.16 kg load, tensile properties under ISO 527-2:2012, flexural properties under ISO 178:2019, and impact behavior under ISO 180:2019. Flexible high-flow PLA injection grades of this class commonly exhibit a melt flow rate in the 30–70 g/10 min range, a tensile modulus between 1.5 GPa and 2.5 GPa, and a nominal elongation at break between 20% and 80%. The exact formulation of TE-1070 is proprietary; flexibility in PLA injection grades is generally obtained through stereoisomer ratio control, reduced crystallinity, or the incorporation of biodegradable plasticizers or aliphatic polyester modifiers. Because public data for this specific configuration is limited, the class envelope should be used only for preliminary mold design and must be superseded by the supplier’s lot-specific certificate of analysis during production qualification.

    Injection molders encountering this material should differentiate it from standard PLA grades by melt length and demolding behavior rather than pellet colour alone. A higher melt flow rate permits lower filling pressure and reduced clamp force demand in thin-wall tools, but it also increases the risk of flash on parting lines with clearances above 0.02–0.03 mm in high-pressure regions. This trade-off is observed on production-scale machines with clamp capacities from 800 kN to 2,500 kN when molding nominal wall thicknesses between 0.8 mm and 2.0 mm. Standard PLA grades with melt flow rates below 15 g/10 min often require higher melt temperatures to fill the same tool; TE-1070-class materials can be processed at melt temperatures in the 180–210 °C range, which shortens colour-change purge time and lowers the probability of hot runner deposit formation.

    How Does TE-1070 Differ from Standard High-Stiffness PLA Grades?

    The differentiation is most clearly expressed through tensile modulus, flexural modulus, and elongation at break. Unmodified high-stiffness PLA is typified by a tensile modulus of 3.0–3.5 GPa and an elongation at break below 10% under ISO 527-2:2012, which produces brittle failure in thin sections and limits living-hinge performance. In contrast, flexible high-flow PLA grades of the TE-1070 class reduce tensile modulus into the 1.5–2.5 GPa range and extend elongation at break above 20%, shifting tensile failure from immediate brittle fracture toward yielding or necking. The trade-off is reduced load-bearing stiffness; a thin-wall component molded from flexible PLA at the same nominal wall thickness as standard PLA will deflect more under identical loading. That difference must be addressed in design through ribbing, wall thickness adjustment, or finite-element analysis rather than through material substitution alone.

    Property Flexible high-flow PLA class envelope Standard injection molding PLA class envelope Test method
    Melt flow rate at 210 °C, 2.16 kg 30–70 g/10 min 5–15 g/10 min ISO 1133-1:2022
    Tensile strength at yield or break 25–45 MPa 45–65 MPa ISO 527-2:2012
    Tensile modulus 1.5–2.5 GPa 3.0–3.5 GPa ISO 527-2:2012
    Nominal elongation at break 20–80% 2–10% ISO 527-2:2012
    Flexural modulus 1.8–2.8 GPa 3.2–3.8 GPa ISO 178:2019
    Notched Izod impact at 23 °C 20–50 J/m 10–20 J/m ISO 180:2019
    Heat deflection temperature at 0.45 MPa 45–60 °C 50–70 °C ISO 75-2:2013

    The table represents a class-level comparison for flexible high-flow PLA versus conventional stiff PLA and is not a substitute for TE-1070-specific lot data. The reduction in flexural modulus is directly relevant to snap-fit designs; a component designed for standard PLA may lose engagement force or become loose if TE-1070 is introduced without thickening the flexural element or increasing deflection. Conversely, a living hinge that would crack after a few flexural cycles in standard PLA can often survive repeated bending in flexible high-flow PLA because lower bending stiffness reduces surface strain at the hinge root.

    Before molding trials begin, desiccant-bed drying of TE-1070 is mandatory when storage humidity has exceeded 60% RH. PLA is hygroscopic and undergoes hydrolytic chain scission at melt temperatures if residual moisture exceeds 250 ppm. Desiccant dryers should maintain air dew point no higher than −30 °C and deliver pellet residence times of 4–6 h at 70–80 °C. Moisture levels above 0.025 wt% can reduce tensile strength by 10–20% through molecular weight reduction and can cause splay, lower melt viscosity, and inconsistent shot weight. Pellets removed from open gaylord containers in humid production halls for more than 2 h may require re-drying before reintroduction to the machine hopper.

    Machine conditions for TE-1070 should be selected to limit thermal history. Barrel temperature should not exceed 210 °C at the nozzle unless unavoidable; flat temperature profiles across the rear and center zones are recommended to prevent uncontrolled melting in the feed section. Shot size should occupy 50–80% of barrel capacity to limit residence time. In production equipment, melt residence time beyond 5 min at temperatures above 210 °C has been associated with yellowing, carbonized specks, and reduced impact strength. Screw speed should be set between 50 rpm and 150 rpm on general-purpose screws with 20:1–25:1 L/D ratios and compression ratios in the 2.5:1–3.0:1 range. The material is not a crystalline fast-cycling resin; uncontrolled high shear can generate enough viscous heating to push the melt temperature above the stabilizer’s protection limit.

    If Thin-Wall Fill and Living-Hinge Flex Fatigue Are Required, Processing Adjustments Become Critical

    When a multi-cavity tool with wall sections below 1.0 mm is used, the high flow behavior of TE-1070-class material becomes the controlling parameter for successful filling. Melt temperature should be held between 190 °C and 210 °C, while mold temperature should be maintained between 20 °C and 40 °C to balance flow length and demolding stability. Higher mold temperatures improve weld-line strength but extend cycle time and can cause sticking in highly polished cavities. In thin-wall lids and hinged closures, injection velocity should be high enough to prevent premature gate freeze-off, but not so high that shear heating at the gate raises local melt temperature above 220 °C. Gate diameter should be at least 50–75% of the wall thickness; undersized or pointed gates can cause jetting, which produces visible flow marks and reduces hinge fatigue life.

    For living hinges, gate placement should orient flow lines perpendicular to the hinge axis. The hinge should be flexed once immediately after demolding while the part is still above the glass transition temperature; this controlled flexing stabilizes molecular orientation in the hinge region and reduces the probability of premature cracking. Parts molded with mold temperatures below 15 °C may exhibit notch sensitivity at the hinge root because rapid cooling freezes higher levels of molded-in stress. Production layouts should therefore avoid chilled water at temperatures below 10 °C unless mold condensation is managed by closed-loop thermolators.

    Heat Deflection Temperature and Post-Molding Crystallinity

    Heat deflection resistance in flexible PLA is governed by the low crystallinity that also enables ductility. Under ISO 75-2:2013 at a load of 0.45 MPa, flexible high-flow PLA grades typically remain below 60 °C, which places them outside hot-fill packaging and high-temperature automotive interiors unless the part is annealed. Annealing at 90–110 °C for 30–60 min can increase heat deflection temperature by developing crystallinity, but this process introduces dimensional shrinkage that must be compensated in mold dimensions. The shrinkage during annealing is not isotropic; a flat lid or cover may warp due to differential crystallinity from gate to flow end. Therefore annealing is usually reserved for applications in which heat resistance is mandatory and post-molding dimension checks are part of the quality plan.

    The glass transition temperature of PLA is near 55–60 °C, so dimensional stability under moderate heat is already limited even in the amorphous state. TE-1070 should not be specified for use above 50 °C unless loaded deflection and creep are not functional requirements. In cold or room-temperature packaging, the low modulus permits the product to tolerate some abuse without cracking, but the upper service limit remains below that of polypropylene or PET.

    For food-contact and cosmetic packaging, a written declaration of conformity must be obtained from the supplier under the applicable regulatory framework, such as Regulation (EU) No 10/2011 or the relevant U.S. Food Contact Notification conditions. Migration testing is performed according to EN 1186-1 and EN 13130-1 or equivalent methods, and the results depend on the complete formulation, including color concentrates, processing aids, and print coatings. A base PLA polymer alone does not establish food-contact compliance for the finished article. Industrial compostability may be certified under EN 13432 or ASTM D6400, but flexible grades containing non-compostable plasticizers or processing aids may not meet the 90% biodegradation threshold. Certification status for TE-1070 must therefore be verified with the supplier before compostability claims are made on packaging or product literature.

    Hot Runner Imbalance at Low Shot Weights Is a Documented Failure Mode

    In multi-drop hot-runner systems, thermal non-uniformity above 5 °C across drops has caused fill imbalance and visible flow marks in production tools running high-flow PLA. The low melt viscosity of TE-1070-class materials amplifies the effect of small temperature differences because viscosity changes with temperature more steeply than in standard PLA. Hot runner manifolds should be equipped with individual zone controllers and calibrated thermocouples, and startup procedures should include a thermal soak period of at least 30 min before the first shot is taken. If the hot runner has dead spots or non-streamlined channels, the high flow rate can still produce stagnation zones that degrade over time. Degraded material appears as black or brown streaks and may not appear until production has run for several hours. Therefore, hot runner maintenance and purge protocols should be part of mold qualification rather than delayed until field returns occur.

    Operational limits for TE-1070 should include refusal of regrind above 30% without first verifying melt flow rate retention under ISO 1133-1:2022. Reprocessed material that has undergone multiple heat histories may show a lower viscosity than virgin pellets, causing flash or shrinkage differences in the same tool. Blending regrind above 30% should be validated by measuring tensile elongation at break under ISO 527-2:2012 and notched Izod impact under ISO 180:2019 on molded plaques. If the plaque impact value falls below the lower end of the class envelope, the regrind ratio should be reduced. This boundary should be evaluated in the mold qualification phase rather than after production release.

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