Terramac Te 2000 Standard Transparent Injection Molding Polylactic Acid

TERRAMAC TE-2000 Standard Transparent Injection Molding Polylactic Acid

    • Product Name: TERRAMAC TE-2000 Standard Transparent Injection Molding Polylactic Acid
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
    • CONTACT NOW
    VTB
    Specifications
    HS Code 560340
    Materialtype Polylactic Acid (PLA)
    Appearance Transparent
    Density 1.25 g/cm³
    Meltflowrate 15 g/10 min at 190°C and 2.16 kg
    Tensilestrength 60 MPa
    Tensileelongationatbreak 5%
    Flexuralstrength 95 MPa
    Flexuralmodulus 3.5 GPa
    Notchedizodimpactstrength 2.0 kJ/m²
    Heatdeflectiontemperature 55°C at 0.45 MPa
    Vicatsofteningtemperature 60°C
    Glasstransitiontemperature 60°C
    Meltingtemperature 170°C
    Moldingshrinkage 0.3-0.7%
    Waterabsorption 0.1%
    Lighttransmittance 90%
    Haze 2%
    Processingmethod Injection Molding

    As an accredited TERRAMAC TE-2000 Standard Transparent 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-2000 Standard Transparent Injection Molding Polylactic Acid comes in 25 kg moisture-barrier bags, palletized and stretch-wrapped for industrial shipping.
    Container Loading (20′ FCL) Container loading (20′ FCL): TERRAMAC TE-2000 Standard Transparent Injection Molding Polylactic Acid in 25 kg bags, palletized, shrink-wrapped, securely stowed.
    Shipping TERRAMAC TE-2000 Standard Transparent Injection Molding Polylactic Acid is shipped as non-hazardous thermoplastic pellets in sealed moisture-barrier bags or octabins, palletized and shrink-wrapped. It is not classified as dangerous goods for transport. Keep dry, avoid heat and moisture, and handle with standard cargo precautions. Store in a cool, dry area.
    Storage Store TERRAMAC TE-2000 in a cool, dry, well-ventilated area away from direct sunlight, heat, and moisture. Keep containers tightly closed in original packaging to prevent hydrolysis. Recommended storage: below 30°C and under 50% relative humidity. Segregate from strong acids, bases, and oxidizers. Protect from physical damage and static buildup. Reseal opened packages promptly and use first-in, first-out stock rotation.
    Shelf Life Shelf life is 12 months when stored sealed in original packaging, cool, dry, away from moisture and direct sunlight.
    Application of TERRAMAC TE-2000 Standard Transparent Injection Molding Polylactic Acid

    Cold-fill beverage service articles molded from TERRAMAC TE-2000 are produced on conventional hydraulic or all-electric reciprocating-screw injection molding machines with screw diameters between 25 mm and 35 mm and L/D ratios from 20:1 to 24:1; cavity steel is polished to at least SPI A-2 or A-1 to preserve the transparent surface finish required for shelf display. The resin must be pre-dried in a desiccant dryer with a dew point of -40°C or lower at 70–80°C for 4–6 h to reduce residual moisture below 250 ppm; batches exposed to ambient relative humidity above 60% for more than 30 min must be re-dried because hydrolytic chain scission during plastication generates silver streaks, gate splay and a loss of notched impact strength when tested by ISO 179-1. Regulatory documentation for this application follows EU Regulation 10/2011, Annex I Table 1 for authorized monomers and additives, and Annex V for overall migration testing, with an overall migration limit of 10 mg/dm² for food-contact articles; U.S. route is documented through a Food Contact Notification under 21 CFR 170.100 or an applicable exemption, because 21 CFR 175.300 is not automatically applicable to injection molded articles unless a coating function exists. Formulation addition ratio starts from 98.0–99.0 wt% virgin TE-2000, 1.0–2.0 wt% PLA-compatible transparent masterbatch and 0–0.5 wt% external lubricant; raising lubricant above 0.5 wt% increases weld-line haze and reduces drop impact performance when tested by ISO 6603-1. Barrel zone settings of 180°C, 195°C, 205°C and 210°C from feed to nozzle, mold temperature 20–35°C, injection speed 40–120 mm/s and hold pressure 500–800 bar are typical starting parameters; cooling time for a 1.0–1.5 mm wall section is 8–18 s. Terminal product types include 250–500 mL transparent tumblers, airline juice cups, promotional stadium glasses and cold-beverage tasting cups. If compostability labeling is required, the finished article must meet EN 13432, which specifies disintegration, biodegradation and ecotoxicity criteria independently of food-contact migration testing. The operational boundary is hot-fill and dishwasher use: continuous service above 50°C is not recommended because typical heat deflection temperature under load by ISO 75 remains below 55°C and therefore below common hot-fill and dishwasher peak temperatures.

    What Restricts the Maximum Filling Pressure in Thin-Wall Transparent Overcaps and Dispensing Closures?

    In thin-wall overcaps with nominal wall thickness between 0.6 mm and 1.0 mm, the limiting variable during filling is not melt degradation but flash formation at the parting line and core deflection under cavity pressure. Melt-flow rate is measured per ISO 1133-1:2022 at 210°C under 2.16 kg load for each incoming lot because shifts above ±10% relative to the qualified value alter the filling-pressure window and require revalidation of the injection velocity profile. On production tools with cavity pressure sensors such as Kistler 6182A mounted behind ejector pins, peak cavity pressure is maintained between 350 bar and 500 bar; exceeding 500 bar produces visible flash at the cap edge and damages the sealing ribs, while pressures below 350 bar increase sink marks around the closure threads. For multi-cavity closure tools, projected-area clamp force should be not less than 0.6–0.8 tonnes per square centimetre of projected area, and mold alignment must be verified at operating temperature to avoid asymmetric flash distribution when the tool reaches 25–35°C. Compliance for the finished accessory in the European Union is anchored to Packaging and Packaging Waste Directive 94/62/EC, Article 11, with the sum of lead, cadmium, mercury and hexavalent chromium not exceeding 100 mg/kg, and to REACH Regulation 1907/2006 Annex XVII restrictions; if the overcap contacts a cosmetic formulation, compatibility is assessed under the responsibility of the cosmetic product safety report. Formulation addition ratio is 99.0–99.5 wt% TERRAMAC TE-2000 with 0.5–1.0 wt% high-transparency slip additive; no fillers, nucleating agents or impact modifiers are used because they create surface haze and increase the likelihood of gate blush in thin sections. The downstream process sets melt temperature at 190–210°C, mold temperature at 20–35°C, injection speed in the range of 80–160 mm/s, and hold time of 3–8 s for a 0.8 mm nominal wall; cooling time is 6–12 s. Terminal product types include fragrance pump overcaps, lotion pump collars, deodorant stick caps and transparent cosmetic tottle closures. The operational boundary is child-resistant certification: adding child-resistant mechanisms often requires external spring elements that cannot be overmolded with PLA without introducing stress cracking; such designs must be validated by torque-retention testing rather than assumed from material substitution.

    Transparent Cosmetic Rigid Packaging Jar Bodies, Lip Balm Tubes and Snap-Fit Compacts

    The principal processing conflict in transparent cosmetic rigid packaging is sink-mark formation opposite thick jar bases while maintaining low birefringence around snap-fit undercuts. Multi-cavity molds with 8–16 cavities are gated through hot runner valve gates to avoid cold sprue vestiges; cavity inserts are polished to SPI A-1 finish, and draft angles are held at 0.5–1.0° to reduce ejection drag without creating visible side-wall striations. Compliance assessment follows Regulation (EC) No 1223/2009 for cosmetic product safety, Packaging and Packaging Waste Directive 94/62/EC Article 11 heavy-metal limits of 100 mg/kg total, and ISO 22715:2006 for cosmetic packaging; if the container is used for lipophilic cream formulations, short-term and long-term compatibility testing per ISO 175 should be completed because ester-based cosmetic bases can induce environmental stress cracking in PLA at a stress level below the tensile yield point. Formulation addition ratio is 99.0–99.8 wt% TERRAMAC TE-2000 with 0.2–1.0 wt% cosmetic-grade colorant and 0.1–0.3 wt% external mold release agent; the release agent is kept below 0.3 wt% because higher levels migrate to the part surface during annealing and lower the gloss reading measured at 60° per ISO 2813. Production process parameters begin at melt temperature 195–210°C, mold temperature 25–35°C, hold pressure 400–700 bar and cooling time 12–25 s for a 1.5 mm nominal wall; thicker cosmetic jar bases may require injection-compression molding to reduce packing pressure and lower molded-in stress. Terminal product types include 15–50 mL cream jar bodies, transparent lip balm tubes with snap-fit bases, pressed powder compact covers and sample jar systems with internal platforms. The operational boundary is dimensional stability after washing: repeated dishwashing in water above 60°C is not recommended because PLA parts can distort and lose snap-fit retention; cold or warm water washing below 40°C is the defined replacement-use condition.

    Transparent Consumer Electronics Accessory Housings Shift the Tooling Focus from Optical Polish to Dimensional Stability

    When transparent protective housings are required for consumer electronics accessories, tool commissioning shifts from flatness and gloss alone to post-mold shrinkage uniformity after thermal cycling from 23°C to 55°C. The resin is processed at melt temperature 185–205°C, mold temperature 20–30°C, screw back pressure 5–10 bar and screw rotation 60–100 min⁻¹; gate placement at the thickest boss area rather than at the visible exterior reduces jetting and weld-line haze in the lens window. Compliance is evaluated against RoHS Directive 2011/65/EU Annex II restricted substances, REACH Regulation 1907/2006 Candidate List of Substances of Very High Concern, and UL 94 HB flammability for enclosures when end-product safety standard IEC 62368-1:2018 requires a flame rating. Formulation addition ratio uses 97.0–100 wt% TERRAMAC TE-2000; if drop resistance must exceed 0.5 J at 23°C by ISO 6603-1, an impact modifier is added at 3–8 wt%, but the resultant loss of visual clarity must be measured by haze per ISO 14782. Antistatic masterbatch at 0.5–1.5 wt% may be used for ESD-controlled assembly environments, though surface resistivity should be verified by IEC 61340-2-3 before claiming ESD-safe packaging. Terminal product types include earbud charging case lids, desktop webcam transparent shells, smart speaker light rings and transparent display stand components. The operational boundary is continuous heat exposure: PLA housings should not be used in environments exceeding 55°C adjacent to charging coils or power-conversion circuits unless thermal imaging of the finished device verifies lower local temperature; published data for TE-2000 in this specific electronic accessory configuration is limited, so pre-production thermal cycling per IEC 60068-2-14 is required.

    When Medical Device Enclosure Applications Require Biocontamination Control Without Steam Sterilization

    Cleanroom injection molding of TERRAMAC TE-2000 for medical device enclosures is limited to non-implantable, short-duration patient-contact or contactless diagnostic equipment categories because the resin cannot withstand steam autoclaving at 121°C without deformation. The production environment should meet ISO 14644-1:2015 Class 8 as a minimum for non-skin-contacting covers, with Class 7 or better when the part is used within a patient breathing zone or near fluid pathways. Biological safety is addressed by testing the final enclosure under ISO 10993-5:2009 for cytotoxicity and ISO 10993-10:2013 for irritation and sensitization, while the molding site operates under ISO 13485:2016 for medical device quality management. Formulation addition ratio is 99.5–100 wt% virgin TERRAMAC TE-2000 and 0–0.5 wt% medical-compatible colorant; mold release agents are omitted because leachable substances can invalidate the ISO 10993 assessment, and reprocessed material is excluded from medical lots unless validated through ISO 10993-5 and ISO 10993-10 after incorporating the specified regrind percentage. The downstream process uses a dedicated cleanroom injection molding cell with dry-air conveying from the dryer to the hopper, melt temperature 185–205°C, mold temperature 20–30°C and minimum plastication residence time of less than 5 min at melt temperature to reduce lactide regeneration and hydrolytic molecular-weight loss. Terminal product types include transparent diagnostic instrument covers, laboratory analyzer viewports, pipette carousel dust covers and non-patient-contact medical device display lenses. Sterilization validation must consider that ethylene oxide is generally compatible but requires aeration to meet residue limits under ISO 10993-7; gamma irradiation at 25 kGy may reduce molecular weight and must be followed by post-irradiation tensile testing per ASTM D638-14 to verify that mechanical properties remain above the device specification. Published data for TERRAMAC TE-2000 in this specific cleanroom medical configuration is limited; pilot validations are required before locking the sterilization method and annual production line release.

    For transparent toy components and educational models, child-contact migration limits determine the usable masterbatch loading before mechanical performance is considered. The relevant European compliance is EN 71-3:2019+A1:2021 for migration of certain elements, with limits applied to the finished accessible material; U.S. requirements include ASTM F963-23 and 16 CFR 1303 for lead in surface coatings, while phthalate restrictions in 16 CFR 1307 apply if plasticized additives are introduced. Formulation addition ratio is 99.0–99.5 wt% TERRAMAC TE-2000 with 0.5–1.0 wt% EN 71-3-compliant masterbatch and 0.2 wt% maximum slip additive; no post-consumer recycled material is used because trace heavy-metal content cannot be demonstrated consistently in toy-grade transparent parts. The production process sets melt temperature at 190–205°C, mold temperature at 20–30°C, injection speed at 30–70 mm/s for lens-like parts to reduce jetting, and hold pressure at 300–600 bar. For thick transparent toy lenses, a cold runner with a full-round gate is preferred over a hot runner to avoid gate vestige that can create sharp edges; after demolding, the gate area is trimmed and edge-radius checked to 0.25 mm minimum to satisfy mechanical safety provisions under EN 71-1. Terminal product types include kaleidoscope lenses, transparent toy window inserts, building block panels and hobby model canopy glazing. The operational boundary is small-part classification: toys and educational models intended for children under 3 years are not released without small-part cylinder testing because transparent PLA fragments can create a choking hazard if a snap-fit feature fails during drop testing.

    Free Quote

    Competitive TERRAMAC TE-2000 Standard Transparent Injection Molding Polylactic Acid prices that fit your budget—flexible terms and customized quotes for every order.

    For samples, pricing, or more information, please contact us at +8618005193850 or mail to sales8@ascent-chem.com.

    We will respond to you as soon as possible.

    Tel: +8618005193850

    Email: sales8@ascent-chem.com

    Inquiry

    Get Free Quote of Ascent Petrochem Holdings Co., Limited

    Flexible payment, competitive price, premium service - Inquire now!

    Certification & Compliance
    More Introduction

    TERRAMAC TE-2000 Standard Transparent Injection Molding Polylactic Acid is a semi-crystalline poly(L-lactic acid) supplied by Unitika Ltd. for general-purpose transparent injection-molded components. The grade is delivered as cylindrical pellets and is classified as a standard-flow injection molding PLA. Typical datasheet values include a density of 1.24–1.26 g/cm³ under ISO 1183-1:2019, a melt flow rate of 8–12 g/10 min at 190 °C under a 2.16 kg load according to ISO 1133-1:2022, and tensile yield strength in the range of 58–62 MPa with a tensile modulus of 3.3–3.7 GPa under ISO 527-2:2012. The formulation is not compounded with mineral fillers, impact modifiers, or nucleating agents, which permits retention of optical clarity in walls up to approximately 3 mm. However, the aliphatic polyester backbone limits continuous load-bearing service above approximately 50 °C unless the part is annealed or converted to a semicrystalline state. The resin is hygroscopic at processing temperatures; hydrolytic chain scission proceeds rapidly if pellet moisture content exceeds 250 ppm. Predrying is therefore required at 80 °C for 4–6 h in a desiccant dryer with a dew point of −40 °C or lower before melt processing.

    On production-scale injection molding lines, TE-2000 is typically processed on a reciprocating-screw machine with shot capacity positioned between 40% and 70% of barrel volume to minimize hot residence time. Barrel profiles are set from 170–180 °C at the feed throat to 190–200 °C at the nozzle, with the actual melt temperature measured by an immersion probe maintained below 220 °C. Thermal excursions above 230 °C accelerate lactide reformation and acetaldehyde formation, producing yellowing, splay, and reduced molecular weight. Melt temperature below 180 °C increases injection pressure demand and creates unmelted-pellet defects in thin ribs. A standard general-purpose screw with an L/D ratio of 20:1 to 26:1 and compression ratio of 2.0:1 to 3.0:1 is suitable; a low-shear screw is preferred to limit adiabatic heating. Screw speed is maintained at 50–150 rpm and back pressure at 0.5–1.0 MPa.

    Melt Rheology, Drying, and Barrel Temperature Profiles in Injection Molding

    Processing of TE-2000 is configured around controlled melt temperature and low residual moisture rather than elevated mold temperature. Barrel temperature settings from feed throat to nozzle are commonly profiled at 170 °C, 185 °C, 195 °C, 200 °C, and 190 °C. Injection pressure generally falls between 60 MPa and 120 MPa, with hold pressure set at 40–80% of injection pressure. Screw rotation below 50 rpm can extend cycle time and reduce melt homogeneity, while rotation above 200 rpm can generate excessive shear heating and promote polymer degradation. Mold surface temperature is ordinarily set at 20–40 °C to produce an amorphous, transparent part. Mold temperatures above 55 °C accelerate spherulitic crystallization, generating haze, warpage, and nonuniform shrinkage. For a 2 mm wall section, cooling time is commonly 10–20 s depending on mold geometry, coolant temperature, and part ejection temperature. The recommended ejection surface temperature is below 50 °C to prevent deformation during part removal.

    Representative injection-molded physical properties for TERRAMAC TE-2000 are compiled below. The values are typical and are not specification limits; published data for this specific configuration is limited, and lot-specific certificates of analysis remain controlling for production validation. Test specimens are conditioned at 23 °C and 50% RH according to ISO 291:2008 unless otherwise noted.

    Property Test Method Typical Value
    Density ISO 1183-1:2019 1.24–1.26 g/cm³
    Melt flow rate ISO 1133-1:2022, 190 °C, 2.16 kg 8–12 g/10 min
    Tensile yield strength ISO 527-2:2012 58–62 MPa
    Tensile modulus ISO 527-2:2012 3.3–3.7 GPa
    Flexural strength ISO 178:2019 85–95 MPa
    Flexural modulus ISO 178:2019 3.4–3.8 GPa
    Charpy notched impact strength ISO 179-1:2010/1eA 2.5–4.0 kJ/m²
    Heat deflection temperature ISO 75-2:2013, method B, 0.45 MPa 54–58 °C
    Light transmittance, 3 mm ISO 13468-1:2019 88–91%
    Molding shrinkage, flow direction ISO 294-4:2018 0.3–0.5%

    The notch sensitivity of TE-2000 is consistent with unmodified PLA and is lower than impact-modified PLA grades, which typically exceed 10 kJ/m² but sacrifice tensile modulus and optical transparency. The heat deflection temperature under 0.45 MPa load is 54–58 °C, reflecting an amorphous PLA matrix. Nucleated or annealed PLA grades can reach 90–120 °C but generally show reduced light transmittance and require mold temperatures above 90 °C. These differences position TE-2000 as a standard transparent injection molding grade rather than a high-heat or impact-modified material.

    How Does TE-2000 Differ from General-Purpose PLA and Heat-Resistant Copolymer Grades?

    TE-2000 differs from general-purpose PLA grades intended for sheet extrusion or fiber spinning primarily in melt viscosity and additive package. Extrusion-grade PLA typically exhibits melt flow rates below 5 g/10 min at 190 °C and 2.16 kg, whereas TE-2000 operates in the 8–12 g/10 min range, allowing faster filling of multi-cavity injection molds with wall thickness from 1.0 mm to 3.0 mm. Thin-wall parts below 0.8 mm may require a higher-flow PLA grade with melt flow rate above 20 g/10 min to prevent short shots and excessive injection pressure. Compared with impact-modified PLA, TE-2000 maintains higher light transmittance and higher tensile modulus but exhibits Charpy notched impact of only 2.5–4.0 kJ/m². Impact-modified PLA, by contrast, commonly exceeds 8–15 kJ/m² at the expense of tensile modulus, which may fall below 2.5 GPa.

    Compared with nucleated heat-resistant PLA grades, TE-2000 does not contain talc or other nucleating agents, so it will not reach the 90–120 °C HDT values typical of annealed or nucleated PLA under 0.45 MPa load. The standard transparent grade also differs from high-heat copolyesters and polycarbonate in processing temperature, density, and environmental resistance. Polycarbonate typically processes above 280 °C and offers notched Izod impact exceeding 20 kJ/m², but TE-2000 processes at 190–220 °C and has a density near 1.25 g/cm³. The lower processing temperature reduces energy input but also reduces part tolerance to hot-fill, steam sterilization, and continuous service above 55 °C.

    In transparent disposable packaging, cosmetic housings, protective covers, and non-load-bearing internal components, TE-2000 can be processed on standard injection molding machines without the hot runner temperatures and hardened barrel materials required for polycarbonate. The material is not intended for structural parts requiring sustained impact, hot-water contact, or repeated autoclave exposure. If a transparent part must survive boiling water or 121 °C steam sterilization, the design should move to a heat-resistant PLA grade or an alternative transparent polymer.

    Gate dimensions for TE-2000 are commonly sized at 60–80% of the nominal wall thickness for edge gates. Tunnel or sub-gates thinner than 0.8 mm can induce high shear and material degradation. Cold runner diameters from 3 mm to 6 mm are used; hot runner manifolds should maintain melt temperature below 210 °C and eliminate dead spots. Vent depths of 0.015–0.025 mm on parting lines prevent gas burning and short shots in trapped-flow areas. Draft angles of 1–2° for textured surfaces and 0.5° for polished surfaces are used to avoid ejection drag. Molded parts are measured for dimensional stability after conditioning at 23 °C and 50% RH under ISO 291:2008. Production molders should anticipate shrinkage of 0.3–0.5%, with lower shrinkage in the flow direction and higher shrinkage transverse to flow. Uneven hold pressure above 100 MPa can reduce sink marks but may also increase molded-in stress, leading to warpage after exposure to warm environments.

    When High Ambient Humidity and Alkaline Service Conditions Limit TE-2000 Use

    Moisture control is the dominant boundary condition for TE-2000. At ambient relative humidity above 60%, pellets absorb moisture rapidly; open bag storage beyond 8 h can raise pellet water content above 500 ppm, producing splay, bubbles, and reduced weld-line strength during injection molding. A desiccant dryer with a dew point of −40 °C or lower should be used for predrying at 80 °C for 4–6 h. If ambient humidity exceeds 60%, the drying time should be extended or a closed hopper dryer should be maintained at 60 °C to protect dried pellets. Moisture content can be verified by Karl Fischer titration under ISO 15512:2019; processing should not begin when pellet moisture exceeds 250 ppm.

    The aliphatic polyester backbone is susceptible to alkaline hydrolysis. End-use environments with aqueous pH above 8, strong detergents, or repeated contact with alkaline cleaning solutions can cause surface etching, stress cracking, and loss of impact strength. Long-term exposure to hot water above 55 °C accelerates molecular weight reduction. The material is also sensitive to certain ketone, ester, and chlorinated solvents, which can induce swelling or environmental stress cracking. Compatibility with cosmetic formulations, food simulants, and cleaning agents should be tested under the actual service temperature and contact time. Sterilization by steam autoclave at 121 °C is not generally applicable to transparent amorphous TE-2000 parts because the HDT is below autoclave temperature.

    Regulatory compliance must be confirmed for the specific application and production site. PLA is not listed among restricted substances under RoHS 2011/65/EU, but additive and colorant packages require verification. For food-contact use, confirmation against Regulation (EU) No 10/2011 or a valid US FDA food-contact notification should be obtained from the supplier. Bio-based carbon content may be determined by ASTM D6866-22 when renewable-origin claims are required. No blanket food-contact, medical, or biodegradation certification should be assumed without lot-specific documentation.

    In injection molding plants, the most frequently observed production failures with TE-2000 are moisture-induced splay, gate blush from excessive injection speed, and warpage from nonuniform mold temperature. These are controlled by maintaining pellet moisture below 250 ppm, reducing injection velocity in gate areas, and balancing coolant circuits to maintain mold surface temperature within 20–40 °C. If production requires annealing for dimensional stability, the parts should be restrained during annealing at 80–100 °C for 20–60 min; however, this process converts the transparent amorphous structure to a semicrystalline state and raises haze. The trade-off between transparency and heat resistance must be determined for each part geometry and end-use requirement.

    Top