| HS Code | 715981 |
| Density | 1.25 g/cm³ |
| Melt Flow Rate | 3.0 g/10 min (190°C/2.16 kg) |
| Tensile Strength At Yield | 45 MPa |
| Tensile Elongation At Break | 200% |
| Flexural Modulus | 2300 MPa |
| Notched Izod Impact Strength | 150 J/m |
| Heat Deflection Temperature | 55°C at 0.46 MPa |
| Vicat Softening Point | 60°C |
| Melting Point | 170°C |
| Glass Transition Temperature | 60°C |
| Biobased Content | 100% |
As an accredited TERRAMAC TP-4030 High Impact Extrusion/Blow Molding Polylactic Acid factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | TERRAMAC TP-4030 is supplied in 25 kg moisture-resistant paper bags on pallets; bulk quantities available in 500 kg sacks. |
| Container Loading (20′ FCL) | 20′ FCL loading: Terramac TP-4030 high-impact extrusion/blow molding PLA in 25 kg bags, palletized, stretch-wrapped, and secured for sea transport. |
| Shipping | TERRAMAC TP-4030 is a non-hazardous, non-regulated polylactic acid resin in solid pellet form. Ship in sealed moisture-barrier bags, boxes, or bulk bags on pallets. Protect from moisture, heat, sunlight, and contamination. Keep dry; no special DOT/IATA/IMDG hazard class required. Maintain clean, closed packaging and avoid static discharge during pneumatic transfer. |
| Storage | Store TERRAMAC TP-4030 in a cool, dry, well-ventilated area away from direct sunlight, heat, flames, and oxidizing materials. Keep original packaging tightly closed to prevent moisture ingress and contamination. Avoid prolonged storage above recommended temperatures, as polylactic acid may degrade or cake. Use first-in, first-out inventory practices. Ground handling equipment to prevent static discharge. Store in accordance with SDS and local regulations. |
| Shelf Life | Shelf life is typically 12 months when stored unopened in a cool, dry place away from direct sunlight and moisture. |
On cosmetics filling lines, the hollow packaging wall is subjected to drop tests of filled containers from 0.8–1.2 m without crack propagation at the neck or pinch-off. TERRAMAC TP-4030 is processed in this sector as a monolayer or multilayer parison material, typically at 96–98 wt% TP-4030 with 2–4 wt% polyester-compatible colour masterbatch; where lower surface friction is required, 0.3–0.8 wt% of a non-amine slip masterbatch replaces an equivalent portion of colour masterbatch because primary and secondary amine additives accelerate aminolytic chain scission of PLA ester linkages. Drying before extrusion uses a desiccant dryer with dew point ≤ −40 °C, hopper temperature 80 °C, residence 4–6 h, and a return-air moisture target < 250 ppm. The extruder is a single-screw barrier design with 25:1–30:1 L/D and compression ratio 2.5:1–3.0:1; the barrel profile is ramped from 165 °C at the throat to 195–205 °C at the metering section, while the die head is held at 190–200 °C. Blow moulding tools are maintained at 18–25 °C, and blow air pressure is set between 0.6–0.8 MPa to limit parison ballooning and improve contact replication. Drop-impact verification follows ASTM D2463-15, and melt-flow shift is measured according to ISO 1133-1:2022. EU packaging compliance is anchored to Directive 94/62/EC heavy-metal limits with total lead, cadmium, mercury, and chromium(VI) not exceeding 100 mg/kg; REACH Annex XVII restrictions apply to phthalate plasticisers and SVHC content above 0.1 wt%. Terminal products include 50–500 mL cosmetic cream jars, lotion bottles, and pump bottles. Production records show wall-thickness variation at the pinch-off can exceed 0.4 mm if parison programming is not tuned for the higher melt strength of impact-modified PLA; operators should purge with polyethylene before shutdown to avoid residue carbonisation.
On cold-fill dairy and deli packaging lines, TERRAMAC TP-4030 extruded sheet is configured for amorphous PLA rather than crystallised PET, so the thermoforming window is narrower: sheet surface temperature is maintained at 90–110 °C, below the onset of rapid cold crystallisation, while tool temperature is kept at 20–30 °C to prevent premature haze and embrittlement. Formulation for this sector is regrind-driven; converters run 80–90 wt% virgin TP-4030 and 10–20 wt% plant regrind from skeleton scrap, provided the flake is dried to the same moisture specification and is not reprocessed more than three cycles, because each extrusion pass shifts melt flow rate upward and reduces sheet melt strength. Sheet extrusion uses a single-screw extruder with 30:1 L/D, a barrier screw, and a flat die at 195–210 °C; the polishing stack is set between 25 °C and 40 °C. Food-contact compliance under EU 10/2011 requires overall migration below 10 mg/dm² using the test conditions in Annex III, and U.S. converters must verify that the specific TERRAMAC grade is covered by an applicable FDA food-contact notification or 21 CFR 174.5 GMP compliance. Terminal products are 250–500 mL cold-fill dairy cups, deli trays, and clamshells; hot-fill above 60 °C is outside the operational boundary because heat deflection temperature is below typical hot-fill thresholds. Edge tear during trimming is an observed failure when sheet temperature drops below 85 °C, and moisture above 250 ppm produces silver streaks and hydrolysis-induced viscosity loss.
Dry-powder supplement jars are blow-moulded with TERRAMAC TP-4030 as a monolayer structure when the filling powder has water activity below 0.4 aw and the package includes a desiccant sachet; the formulation ratio is 97–99 wt% TP-4030 with 1–3 wt% white masterbatch, and no amine-based oxygen scavenger is used because it can reduce molecular weight at melt processing. Multilayer coextrusion with EVOH is technically possible but requires tie-layer qualification; published data for this specific TP-4030/EVOH configuration is limited, so drop-in monolayer conversion should not be extrapolated. The blow moulding sequence uses a grooved-feed extruder with 25:1–28:1 L/D, melt temperature 190–200 °C, die head 185–195 °C, mold temperature 15–22 °C, and parison programming to maintain sidewall thickness above 0.6 mm in pinch-off zones. Because PLA is hygroscopic, dried resin must be conveyed in closed hoppers with dew point ≤ −40 °C; if ambient relative humidity exceeds 60%, neck and thread regions can develop surface splay and reduced top-load strength. Relevant compliance includes EU 10/2011 for food contact and U.S. FDA 21 CFR 174.5 for good manufacturing practice; for products marketed with organic or clean-label claims, the converter must also document that migration of lactic acid and processing aids remains within applicable limits. Terminal product types are 100–500 g protein powder jars, supplement canisters, and scoop-included nutraceutical containers. Top-load tests according to ASTM D2659-16 are used to verify closure integrity after drop testing, and field failures are often traced to over-drying the masterbatch, which causes pigment agglomeration and notch-like weak points.
For blow-moulded toy and hobby components fabricated from TERRAMAC TP-4030, impact performance must be reconciled with the chemical migration limits of Toy Safety Directive 2009/48/EC and EN 71-3:2019+A1:2021; formulations normally contain 94–98 wt% TP-4030 and 2–6 wt% heavy-metal-free colour masterbatch, with cadmium, lead, and chromium pigments excluded because their migration limits are enforced at levels below 10 mg/kg in the final toy. The extrusion blow moulding equipment is a single-screw machine with 20:1–25:1 L/D for smaller parisons, melt temperature 185–200 °C, die gap set to 0.8–1.5 mm for wall-thickness control, mold temperature 15–20 °C, and blow pressure 0.4–0.7 MPa. For hollow components such as balls, building blocks, and hobby spheres, mechanical safety under EN 71-1:2014+A1:2018 requires no small parts detachment after drop and torque tests; the high-impact modification of TP-4030 reduces brittle cracking at low temperatures but does not eliminate the need for radiused pinch-off trimming. Process limitations include reduced melt strength relative to HDPE, so parison sag must be controlled by high-speed extrusion and proper die temperature, not by lowering melt temperature below 180 °C, which raises viscosity and shear heating. Products in this segment are 60–250 mm diameter hollow toy shells, puzzle balls, and sensory hobby items. If the parts are later used in electronic learning devices, RoHS Directive 2011/65/EU applies with restricted substances 0.1 wt% for lead and 0.01 wt% for cadmium.
Rigid extruded tubes and display sleeves for cosmetic sampling and promotional packaging are produced from TERRAMAC TP-4030 at 95–98 wt% with 2–5 wt% colour or mineral filler masterbatch; the sector does not use plasticiser additions because they depress modulus and increase scratch-whitening under vacuum calibration. The profile extrusion line uses a single-screw extruder with 24:1–28:1 L/D, melt temperature 190–205 °C, a tube die with land length 10–15 times the die gap, and a vacuum calibration tank with water temperature 35–45 °C to balance gloss and dimensional stability. Puller speed is set to produce a draw ratio below 1.1:1; higher draw ratios orient the amorphous PLA and create stress whitening at cut edges. Packaging compliance for cosmetic and promotional contact uses REACH Annex XVII, and when the tubes are used for edible lip balm or solid fragrance, the converter must test under EU 10/2011 with overall migration < 10 mg/dm². Terminal products include 10–50 mm diameter transparent rigid tubes, point-of-sale sleeves, and refillable sampling cylinders. Drying is identical to other PLA extrusion operations: 80 °C for 4 h, dew point ≤ −40 °C, moisture < 250 ppm. An observed failure mode is inner-wall rippling when calibration vacuum exceeds −0.02 MPa; this creates periodic drag marks and notch sites.
When TERRAMAC TP-4030 is converted into large-format fused granular fabrication filament, diameter stability is the primary process target: ±0.05 mm for 1.75 mm filament and ±0.10 mm for 2.85 mm filament. The resin is extruded neat at 100 wt%; when stabiliser masterbatch is used, the ratio is 99.0–99.5 wt% TP-4030 and 0.5–1.0 wt% hydrolysis stabiliser masterbatch because spooled filament may be stored in uncontrolled humidity. The extrusion line comprises a single-screw extruder with 24:1 L/D, melt pump, laser diameter gauge, and air cooling at 20–30 °C; melt temperature is held at 190–200 °C because higher temperatures accelerate monomer regeneration and reduce melt viscosity. The resulting filament is used in large-format printers with nozzle diameters 0.8–1.2 mm; printed parts are non-food decorative housings and tooling fixtures. Compliance includes REACH and, where the printed parts enter electrical enclosures, RoHS 2011/65/EU restricted-substance ceilings of 0.1 wt% lead and 0.01 wt% cadmium. Published data for this specific TP-4030 filament configuration is limited to internal converter trials; therefore, spooling tension and drying history must be recorded per batch, and moisture-related diameter drift beyond ±0.10 mm should be treated as a process limit rather than a resin defect.
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TERRAMAC TP-4030 High Impact Extrusion/Blow Molding Polylactic Acid is a polylactic acid compound supplied in pellet form for extrusion blow moulding of hollow parts and for heavy-gauge sheet extrusion. The grade belongs to the TERRAMAC 4000 series, in which the suffix distinguishes a low-melt-flow, impact-modified formulation from unmodified PLA grades intended for injection moulding or fibre spinning. Polylactic acid in this category is derived from renewable carbohydrate feedstocks and requires controlled drying before melt processing. The material is not a direct drop-in replacement for polyolefins in every hollow component; its use is restricted to applications where a combination of renewable content, specific stiffness, surface hardness, and dimensional stability is required and where lower continuous-service temperature can be accepted. The following sections define the technical boundary conditions, processing requirements, and comparative position of the grade without promotional claims.
In extrusion blow moulding, the molten tube must resist sag under its own weight while the mould closes and inflation pressure is applied. Unmodified PLA grades with melt flow rates above 10 g/10 min at 210 °C and 2.16 kg load generally exhibit insufficient melt strength and excessive parison draw-down on longer tools. TP-4030 is positioned in the low-melt-flow portion of the PLA range; published melt flow-rate values for this product family are typically below 5 g/10 min when measured according to ISO 1133-1 at 210 °C with a 2.16 kg load. The lot-specific certificate of analysis provides the controlling value because small shifts in molecular weight or impact-modifier content can alter flow behaviour.
Reduced flow is accompanied by higher molecular weight retention and rheological modification that increases extensional viscosity during parison stretching. The practical effect is a wider processing window on shuttle blow moulders and accumulator-head machines, but the window remains narrower than that of high-density polyethylene. Parison sag tests on a laboratory blow moulder are recommended because melt flow-rate measurements do not fully capture strain-hardening behaviour relevant to parison lengths between 40 cm and 70 cm. On production equipment, wall-thickness programming is necessary to compensate for upper-parison thinning and lower-parison accumulation.
Drying prior to processing is mandatory for TP-4030. In a desiccant hopper dryer with a dew point of ≤ -40 °C and adequate airflow per the dryer manufacturer’s recommendation, pellets are dried at 80 °C for 4 h to 6 h to reduce residual moisture below 250 ppm. Higher moisture levels hydrolyse PLA during plastication, causing a measurable loss of molecular weight, lower melt viscosity, parison splitting, splay, and surface defects. Batch-to-batch moisture content should be verified by Karl Fischer titration or a calibrated moisture analyser before start-up. Overdrying at temperatures above 90 °C can induce pellet agglomeration and thermal degradation in the feed throat.
Extrusion blow moulding of TP-4030 is typically performed on single-screw extruders with a screw length-to-diameter ratio of 24:1 to 30:1 and a compression ratio of 2.5:1 to 3.0:1. Barrel set points from feed to metering are maintained between 160 °C and 190 °C; head and die temperatures are held between 190 °C and 200 °C. The melt temperature measured by an immersion probe at the die exit should be controlled between 190 °C and 205 °C. Because PLA is shear-sensitive, screw speed is set to maintain a die-head pressure that avoids excessive shear heating. Long residence time above 230 °C causes rapid thermal degradation and should be avoided by purging during any line stoppage longer than 5 min.
Accumulator-head machines with programmable parison control are preferred over reciprocating-screw units because they allow wall-thickness profiling of the lower-melt-strength parison. Mould cooling water temperature is controlled between 15 °C and 25 °C; blow pressure is typically 0.4 MPa to 0.6 MPa. Linear mould shrinkage of impact-modified PLA is in the range 0.3 % to 0.5 % for uncontrolled cooling. Parts should remain on the blow pin until the wall temperature drops below the heat deflection threshold; early ejection produces gate-area distortion and progressive dimensional instability.
Published data for this specific configuration is limited because extrusion blow moulding of PLA remains a developing industrial process. Processing trials should therefore be run with the actual tooling, parison length, and wall-thickness programme, using the manufacturer’s certificate of analysis as the baseline. The operational boundary is narrow: melt temperature variation of ±5 °C around the established set point can shift parison sag and part weight enough to move the process outside the specification limit.
Replacing high-density polyethylene or polypropylene with TP-4030 changes the processing economics and tooling behaviour. PLA has a density of approximately 1.24 g/cm³ according to ISO 1183-1, whereas HDPE is typically near 0.95 g/cm³; parts therefore gain mass at equivalent wall thickness. Drying is mandatory for PLA but not for HDPE or PP, and melt temperature cannot be raised to reduce viscosity because thermal degradation accelerates above 205 °C. Parison sag is higher than HDPE at the same melt temperature, and die swell is generally lower; die gap and blow ratio settings must be adjusted on the basis of measured part-weight distribution rather than transferred directly from polyolefin settings.
Relative to unmodified PLA grades, TP-4030 has a lower tensile modulus and higher elongation at break when tested under ISO 527-2. The impact modification reduces stiffness and tensile yield stress, but increases notched impact resistance as measured by ISO 179-1/1eA. This trade-off is characteristic of impact-modified PLA: the dispersed elastomeric or biodegradable modifier phase absorbs energy during impact but reduces load-bearing resistance. The heat deflection temperature under 0.45 MPa load, evaluated by ISO 75-2/B, remains below that of semi-crystalline polyolefins and below the PLA melting region; the amorphous matrix has a glass transition temperature near 55 °C to 60 °C. Continuous service above this range requires annealing or validation on the final part.
| Control dimension | Test method | Process relevance |
|---|---|---|
| Melt mass-flow rate | ISO 1133-1, 2.16 kg, 210 °C | Parison drawdown and extrusion back-pressure control |
| Density | ISO 1183-1 | Part mass and wall-thickness calculation |
| Tensile yield stress and elongation at break | ISO 527-2 | Mechanical design and drop-test correlation |
| Notched Charpy impact strength | ISO 179-1/1eA | Impact toughness of the finished hollow part |
| Heat deflection temperature | ISO 75-2/B, 0.45 MPa | Maximum service temperature limit |
| Residual moisture | Karl Fischer titration, ISO 15512 | Hydrolysis prevention before extrusion |
| Industrial compostability | EN 13432 or ASTM D6400, article-specific | End-of-life claim for the final packaging article |
Applications for TP-4030 include small to medium hollow containers, cosmetic packaging, blow-moulded rigid sleeves, protective packaging, and industrial housings where improved impact toughness relative to standard PLA is needed. The grade is not appropriate for hot-fill containers, carbonated beverage bottles, or continuous service above the heat deflection limit without additional crystallisation. Food-contact suitability must be evaluated on the finished article under the applicable regional migration and use conditions; no blanket compliance statement is assumed from the raw resin specification alone.
Regrind from blow moulded flash and tails can be re-extruded after drying, but repeated heat histories degrade molecular weight and reduce melt strength. On production lines, addition of clean regrind is typically limited to 20 % by weight; higher levels require rheological testing of the extrudate and impact testing of the final part. TP-4030 should not be blended with unmodified PLA injection grades without pilot validation because the melt-strength balance and impact performance change rapidly outside the supplier-specified let-down range.