| HS Code | 194595 |
| Product Name | Sustainable 1001 Tough Injection Molding PLA Blend |
| Brand | Sustainable |
| Material Type | PLA Blend |
| Grade | 1001 |
| Processing Method | Injection Molding |
| Form | Pellets |
| Color | Natural / Off-white |
| Density | 1.24 g/cm³ |
| Melt Flow Rate | 10 g/10 min at 210°C/2.16 kg |
| Tensile Strength | 50 MPa |
| Tensile Modulus | 3300 MPa |
| Elongation At Break | 20% |
| Flexural Strength | 75 MPa |
| Flexural Modulus | 3300 MPa |
| Notched Izod Impact Strength | 50 J/m |
| Heat Deflection Temperature | 55°C at 0.455 MPa |
| Vicat Softening Temperature | 60°C |
| Biobased Content | 80% |
| Renewable Content | 80% |
| Compostability | Industrial Compostable |
| Moisture Content | < 0.5% |
| Drying Temperature | 80°C |
| Drying Time | 4 hours |
| Processing Temperature | 190-210°C |
| Mold Temperature | 20-40°C |
| Shrinkage | 0.3-0.5% |
| Storage Conditions | Cool, dry place |
| Shelf Life | 12 months |
As an accredited Sustainable 1001 Tough Injection Molding PLA Blend factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Sustainable 1001 Tough Injection Molding PLA Blend is supplied in 25 kg sealed, moisture-barrier foil-lined bags, palletized for industrial shipping. |
| Container Loading (20′ FCL) | 20′ FCL container loading for Sustainable 1001 Tough Injection Molding PLA Blend: 25 kg bags, palletized, shrink-wrapped, and securely loaded. |
| Shipping | Sustainable 1001 Tough Injection Molding PLA Blend ships as non-hazardous solid pellets in moisture-barrier bags, boxes, or lined supersacks on pallets. Keep dry, cool, and away from heat and UV. No special DOT/IMDG/IATA classification; standard freight applies. Protect packaging from puncture and contamination. |
| Storage | Store in a cool, dry, well-ventilated area in tightly sealed original containers. Keep away from heat, moisture, direct sunlight, ignition sources, and strong oxidizers. Maintain below 30°C and low humidity to prevent hydrolysis. Avoid dust generation and accumulation; use first-in, first-out rotation. Inspect containers regularly for leaks or damage. Do not store outdoors. Protect from UV light and contamination. |
| Shelf Life | Shelf life is 12 months from date of manufacture when stored in unopened containers in a cool, dry place. |
Competitive Sustainable 1001 Tough Injection Molding PLA Blend prices that fit your budget—flexible terms and customized quotes for every order.
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Sustainable 1001 Tough Injection Molding PLA Blend is an impact-modified polylactic acid compound supplied as cylindrical pellets. The formulation combines a semicrystalline PLA continuous phase with a dispersed toughening phase and a reactive chain-extension residue. The exact modifier chemistry and loading are not publicly disclosed, and independent verification of phase morphology is limited. Bio-based carbon content measured by ASTM D6866-20 is reported at a nominal 85%; the balance consists of non-PLA modifiers, some of which may be fossil-derived. The material is designed for injection molding of rigid components—electronic housings, snap-fit covers, clips, appliance brackets, and industrial guards—where unfilled PLA fractures at notches or weld lines, but where a fully petroleum-based material is not required.
Table 1 reports the manufacturer's typical dry-as-molded values. Mechanical test specimens are conditioned at 23 °C and 50% RH for 48 h before testing unless otherwise noted. The melt flow range is intentionally higher than that of extrusion-grade PLA to permit filling of thin walls, but it also reduces the processing window for thick sections.
| Property | Test method | Typical value |
| Melt mass-flow rate at 210 °C, 2.16 kg | ISO 1133-1:2022 | 15–25 g/10 min |
| Tensile stress at yield | ISO 527-2:2012, type 1A, 1 mm/min | 44 MPa |
| Tensile modulus | ISO 527-2:2012 | 2.3 GPa |
| Flexural modulus | ISO 178:2019 | 2.1 GPa |
| Notched Izod impact at 23 °C | ASTM D256-10 | 12 kJ/m² |
| Heat deflection temperature at 0.45 MPa | ISO 75-2:2013, Method B | 55 °C |
| Density | ISO 1183-1:2019 | 1.23 g/cm³ |
| Mold shrinkage, parallel | ISO 294-4:2018 | 0.4–0.6 % |
| Maximum residual moisture after drying | ISO 15512:2019 | 0.025 wt% |
Rheological response is pseudoplastic. At typical injection shear rates between 100 s-1 and 500 s-1, the compound flows sufficiently for thin walls, but small gates can still produce shear heating above 220 °C. A capillary rheometer is recommended for incoming lot verification when the melt mass-flow rate approaches the upper limit, because a shift of 5 g/10 min can indicate moisture ingress or chain scission from regrind contamination. At a shear rate of 100 s-1, dry material shows an apparent viscosity in the range of 300–600 Pa·s; at 1000 s-1, the value falls to approximately 80–150 Pa·s. These values are process-engineering estimates because capillary entrance-pressure corrections and wall slip are not fully published for this formulation.
Drying is mandatory before injection molding. A desiccant dryer with a closed-loop air flow and dew point no higher than -40 °C should hold pellets at 80 °C for 4 h. If the molding floor relative humidity is above 60%, the residence time should be extended to 6 h. Residual moisture above 0.025 wt% as measured by ISO 15512:2019 causes splay, nozzle drool, melt strength loss, and reduced notched impact. Open hopper time should be limited; the pellets reabsorb atmospheric moisture rapidly once the bag is opened. A documented production failure mode is intermittent splay caused by overnight hopper residence. In that case, a closed-loop desiccant dryer at -40 °C dew point and 80 °C drying temperature restored a stable melt stream.
At the press, melt temperature must remain below 220 °C. Residence time above 200 °C should not exceed 30 min. Stoppages longer than 15 min should activate barrel setback and reduce heater zones to 140 °C. These limits reflect the hydrolytic sensitivity of polylactic ester linkages; prolonged heat or moisture exposure shifts melt flow upward and produces a disproportionate loss in impact resistance.
Alkaline color concentrates, amine-based additive packages, and chlorinated paraffin external lubricants are incompatible with the blend unless compatibility is confirmed by capillary rheometry and ASTM D256-10 notched impact testing on molded plaques. These additives can accelerate ester cleavage, causing screw slippage, gate blush, poor weld-line strength, or a drop in melt strength.
Compared with unmodified injection PLA, Sustainable 1001 Tough trades tensile modulus and optical clarity for higher notched impact. Compared with medium-impact ABS, the blend offers a renewable carbon fraction and lower melt processing temperatures, but its heat resistance and ductility are lower. Table 2 summarizes the comparison based on typical published datasheets for general-purpose injection grades, not single-supplier specification limits.
| Property | Sustainable 1001 Tough | Unmodified injection PLA | Medium-impact ABS |
| Notched Izod impact at 23 °C, ASTM D256-10 | 12 kJ/m² | 3–5 kJ/m² | 20–30 kJ/m² |
| Tensile modulus, ISO 527-2:2012 | 2.3 GPa | 3.2 GPa | 2.1–2.5 GPa |
| Heat deflection temperature at 0.45 MPa, ISO 75-2:2013 Method B | 55 °C | 55–60 °C | 90–95 °C |
| Bio-based carbon fraction, ASTM D6866-20 | 85% | 99–100% | 0% |
| Typical melt temperature range | 185–210 °C | 180–210 °C | 220–250 °C |
The notched Izod improvement over unmodified PLA is significant for snap-fit applications, but the value remains below that of medium-impact ABS. The heat deflection temperature of 55 °C at 0.45 MPa means that load-bearing parts in hot enclosures or near motors may require a design review. Compared with ABS, the PLA blend is more sensitive to hydrolysis and requires stricter drying; however, it can be processed on lower-temperature molds and may reduce energy input in cooling circuits.
On a 1200 kN hydraulic injection molding machine with a 25 mm general-purpose screw and 20:1 L/D, typical barrel settings are 150–160 °C in the rear zone, 175–185 °C in the center zone, 190–200 °C in the front zone, and 190–205 °C at the nozzle. Screw speed is held below 100 rpm, with hydraulic back pressure of 5–10 bar. For 2 mm plaques, an injection linear ram speed of 50–100 mm/s and holding pressure of 40–60 MPa hydraulic are used. Transfer position is set by a short-shot study, and the screw cushion is maintained at 3–5 mm. Published data for wall sections above 4 mm are limited.
Screw design should favor low shear. A general-purpose screw with compression ratio 2.5:1 and a smear-free check ring is suitable. Barrier screws or high-compression screws above 3.0:1 may over-shear the impact modifier, raising melt temperature at the nozzle even when barrel settings are below 210 °C. Feed-zone temperature is critical: if the rear zone is below 140 °C, the granulate can compact and the screw may lose shot-weight stability. When screw skip was observed at 120 rpm, reducing screw speed to 80 rpm and increasing rear-zone temperature solved the instability.
Gate freeze time in a 2 mm wall section is generally reached within 2–4 s; holding time should be established by sequential part-weight increase, not by cycle-time convenience. If the gate freezes before packing is complete, the part exhibits sink marks and post-mold dimensional drift. Cooling time for a 2 mm wall is typically 15–25 s with a mold temperature of 30 °C. The part surface should be below 50 °C at ejection to avoid gate-area smearing.
Mold temperature controls freezing rate, shrinkage, and part release. A mold temperature of 20–30 °C shortens cycle time for thin-wall parts below 2.5 mm but can increase frozen-in orientation. For snap-fit and hinge features, a mold temperature of 35–40 °C improves weld-line strength and reduces notch sensitivity. At mold temperatures above 45 °C, ejection scuffing becomes more likely unless draft angles are at least 1.0 °. Because the as-molded grade has a heat deflection temperature of 55 °C at 0.45 MPa, service temperatures above 50 °C may require post-mold annealing or a redesign that reduces continuous load on the part.
Peak cavity pressure for a 2 mm plaque is generally 20–40 MPa. The switch-over from velocity to pressure control should occur at 95–98% of fill volume. If switch-over is too late, flash occurs at the parting line. If too early, short-shot and sink are likely. Maintaining a screw cushion of 3–5 mm reduces shot-weight variation and improves packing repeatability.
Post-mold annealing at 80 °C for 30 min increases the crystalline fraction and may raise the 0.45 MPa heat deflection temperature into the 65–75 °C range, but it also increases shrinkage by 0.2–0.3% and can cause warpage in parts with uneven wall sections. Annealing should be performed on fixtures to restrain part geometry; published data for this specific formulation are limited.
Gate design should avoid excessive shear. Gate diameters below 0.8 mm or land lengths below 1.0 mm can generate localized overheating, brown streaks, and reduced impact strength near the gate. Cold runners with full-round or trapezoidal cross-sections are preferred. Hot-runner systems are acceptable only if manifold thermocouples maintain the melt below 210 °C and there is no dead spot that can hold material for extended periods.
Part ejection is affected by shrinkage and mold texture. Mold-release sprays should be avoided because they interfere with post-mold printing or bonding. If release becomes difficult, adjust mold temperature and draft rather than add external lubricants. In-mold release coatings are possible only if their chemistry is verified to be non-alkaline and non-amine.
Mold shrinkage is anisotropic. Parallel shrinkage is 0.4–0.6%; perpendicular shrinkage can differ by 0.1–0.3 percentage points depending on gate location, orientation, and mold temperature. For dimensions above 50 mm, mold designers should use separate parallel and perpendicular shrinkage factors and validate them in a tool trial before locking tolerances. A 0.1 percentage point error in shrinkage prediction produces a 0.1 mm dimension error over 100 mm.
Part design should avoid sharp internal notches with radii below 0.5 mm at snap features. Notched Izod impact, measured at 23 °C, does not account for radius effects. For load-bearing snap arms, the gate location should fill along the snap arm length rather than across it. If a core pin divides flow, the resulting weld line can reduce local tensile strength to 50–70% of bulk; the weld line should be moved away from the snap arm. Published data for this specific compound are limited, but injection molders should evaluate knit-line strength using ISO 527-2:2012 tensile bars with a two-fan gate mold.
Regrind of sprues, runners, and short shots may be reintroduced at up to 15 wt% after drying. At 30 wt% regrind, notched Izod impact may fall below 8 kJ/m² and the melt flow may rise beyond the specified range. Published data for higher closed-loop content specific to this formulation are limited.
Storage of unopened bags should be in a cool, dry area below 30 °C. Opened material should be consumed within 24 h or sealed under desiccant. Material exposed to floor-level dust or high humidity should be re-dried and tested before use.
Incoming lot inspection should include melt mass-flow rate by ISO 1133-1:2022, residual moisture by ISO 15512:2019, and dry-as-molded notched Izod impact by ASTM D256-10. If the melt mass-flow rate exceeds 25 g/10 min, the lot should be dried and retested. A notched Izod value below 10 kJ/m² on dry specimens can indicate unwanted regrind contamination or oxidative chain degradation. These acceptance limits are based on the manufacturer's technical data sheet; external proficiency-test data for the specific grade are limited.