| Код ТН ВЭД | 200301 |
Как аккредитованная фабрика Ingeo ™ Biopolymer 3001D High Flow Injection Molding PLA, мы соблюдаем строгие протоколы качества - каждая партия подвергается строгим испытаниям для обеспечения последовательных стандартов эффективности и безопасности.
| Упаковка | |
| Доставка | |
| Хранение |
In high-cavitation thin-wall cutlery production, the governing constraint is not pellet feed stability but the interaction between barrel residence time, gate freeze-off, and moisture-induced molecular weight loss. Ingeo 3001D exhibits a melt mass-flow rate of 15 g/10 min at 210 °C under 2.16 kg when measured according to ISO 1133-1:2022, allowing flow lengths above 150 mm in wall sections of 0.8 mm to 1.2 mm in multi-cavity cutlery tools. The applicable compliance boundary for food-contact cutlery is EU Regulation 10/2011, with overall migration testing per EN 1186-1:2002 and specific migration of lactic acid per EN 13130-1:2004; compostability claims require EN 13432, including biodegradation per ISO 14855-1:2012 and disintegration per ISO 16929. The U.S. market requires the manufacturer’s Food Contact Notification for polylactic acid; no 21 CFR section is applied without verification of the FCN. In formulation terms, 100 parts Ingeo 3001D is processed with regrind content not exceeding 20 wt%; external plasticizers are absent, and demoulding difficulty is addressed with an erucamide slip masterbatch at 0.5 wt% to 1.0 wt%, with 1.5 wt% as the maximum threshold before seal strength and printability are compromised. Drying in a dehumidifying dryer at 80 °C for 4 h with a dew point below -40 °C is mandatory, giving residual moisture below 250 ppm to prevent hydrolysis in the melt. The production process uses a reciprocating screw with L/D ratio 22:1 to 24:1 and compression ratio 2.5:1; barrel zones are set from 180 °C at the feed throat to 205 °C at the nozzle, while the hot runner manifold is held between 205 °C and 215 °C. If manifold residence time exceeds 5 min above 220 °C, lactide evolution produces plate-out on valve pins and causes gate-vestige splitting. Injection velocity is set at 80 mm/s to 120 mm/s to fill cavities in 0.15 s to 0.35 s; hold pressure of 60 MPa to 80 MPa is applied for 3 s to 5 s, followed by cooling of 8 s to 12 s at mould temperatures between 25 °C and 40 °C. Terminal parts in this scenario are single-use forks, spoons, knives, and sporks for airline, institutional, and quick-service food operations.
Production-scale reciprocating screw data show that screw speeds above 120 min⁻¹ generate shear heating sufficient to raise melt temperature by 5 °C to 8 °C, moving the melt into the degradation-sensitive range above 220 °C; screw speed is therefore limited to 80 min⁻¹ to 100 min⁻¹, with back pressure at 0.5 MPa to 1.0 MPa. In tools with valve-gate hot runners, valve pin sticking occurs when resin moisture exceeds 250 ppm or when the manifold temperature is allowed to fluctuate more than ±3 °C during start-up. The ejection phase requires polished cores with draft angles of 1° to 2°; forced ejection at lower draft results in stress whitening at the cutlery rim and measurable bending failure under ASTM D790-17 at loads below 2 N at the handle midpoint.
Threaded cosmetic closures moulded from Ingeo 3001D encounter a specific conflict between rigid thread geometry and low elongation at break: the resin’s tensile elongation of 3.5% per ASTM D638-14 leaves little margin for forced ejection from unscrewing cores if thread depth exceeds 0.8 mm without adequate draft and radiused transitions. Compliance for cosmetic primary packaging is governed by EU Regulation (EC) No 1223/2009, with material-level packaging heavy-metal limits under Directive 94/62/EC, Annex II, and REACH obligations under Regulation (EC) No 1907/2006; filling and manufacturing hygiene follow ISO 22716:2007. The formulation boundary uses 100 parts Ingeo 3001D with a PLA-carrier color or pearlescent masterbatch at 2 wt% to 4 wt%, and where surface scratch resistance is required, a mineral-based additive at 0.5 wt% to 1.0 wt%; no external plasticizer is included because it can reduce thread torque retention and promote stress cracking in contact with ester-based cosmetic oils. Chemical resistance screening is performed according to ISO 175:2010 with representative formulation simulants. The downstream process uses hydraulically driven unscrewing cores in 8- to 16-cavity tools; melt temperature is held at 195 °C to 210 °C, mould temperature at 30 °C to 45 °C, injection speed at 60 mm/s to 100 mm/s, and hold pressure between 50 MPa and 70 MPa for wall thicknesses of 1.5 mm to 2.5 mm. Submarine gates with diameter 0.8 mm to 1.2 mm are used to keep gate vestige below 0.1 mm, because visible vestige on a closure outer wall is a reject criterion in post-mould metallization and soft-touch coating. Terminal products in this scenario include lipstick tubes, compact cases, jar caps, airless pump collars, and mascara wand handles.
Stress-cracking failures in the outer thread base are observed when closures are stored in contact with isopropyl myristate or similar ester-based oils at temperatures above 40 °C; the failure mode appears as circumferential cracking on the thread root after 48 h to 120 h in aggressive formulations. This limits unmodified Ingeo 3001D to formulations with confirmed compatibility, and no claim of universal chemical resistance is supported without lot-specific ISO 175:2010 data.
Child-care article moulding with Ingeo 3001D shifts the risk concentration from melt flow to elemental migration compliance, because coloured toys and play articles must satisfy EN 71-3:2019+A1:2021 migration limits for soluble elements and ASTM F963-23 for U.S. market access. The formulation boundary is 100 parts Ingeo 3001D with 2 wt% to 5 wt% of a cadmium-free, lead-free colour masterbatch; plasticizers are omitted because exudation can increase soluble fractions during simulated saliva extraction. The downstream injection moulding process uses melt temperature 190 °C to 210 °C, mould temperature 25 °C to 40 °C, and wall thickness 2.0 mm to 3.0 mm; where living hinges or snap-fits occur, tool design requires radiused transitions not less than 0.5 mm and gate vestige below 0.1 mm to avoid stress concentration. Relevant compliance also includes Directive 2009/48/EC, REACH Regulation (EC) No 1907/2006 Annex XVII restrictions on phthalates and cadmium, and CPSIA lead content limits. Terminal product types are figurines, construction blocks, play tools, and toy vehicle bodies.
Fatigue failure in tamper-evident band hinges is the central process conflict for high-flow PLA closures, because the base resin’s notched Izod impact is 16 J/m per ASTM D256-23 and the hinge section thickness is commonly reduced to 0.4 mm to 0.8 mm to permit flexure. Compliance for beverage and food closures is EU Regulation 10/2011, with overall migration per EN 1186-1:2002, and compostability claims require EN 13432; the U.S. market requires the manufacturer’s Food Contact Notification. In formulation, 100 parts Ingeo 3001D may be blended with a biodegradable elastomer at 2 wt% to 5 wt% to improve hinge flex life; loadings above 5 wt% reduce thread hoop strength and torque retention by more than 15% under closure ramp tests, but published data for this specific formulation gradient is limited. An erucamide slip masterbatch is added at 0.5 wt% to 1.0 wt% to reduce cap ejection friction. The downstream process uses closure tools with unscrewing or collapsible cores; melt temperature is set at 190 °C to 210 °C, mould temperature at 20 °C to 35 °C, and injection speed is configured to fill the hinge section in 0.1 s to 0.3 s. Cycle time ranges from 20 s to 30 s. Liner retention relies on undercut geometry rather than adhesion, because the surface energy of PLA is commonly reported at 38 mN/m to 44 mN/m; alcohol-based sterilization or flavour concentrates may induce stress cracking, requiring compatibility screening. Terminal products include beverage caps, flip-top closures, sports cap bases, and lotion pump caps.
Hinge flexural endurance should be evaluated using ASTM D790-17 cyclic loading because unmodified Ingeo 3001D has limited flex life; elastomer addition at 2 wt% to 5 wt% is a starting range, and production-scale cap assembly verification is required since pick-and-place orientation force differs from laboratory fixtures. Published data for this specific configuration is limited.
The thermal deflection threshold of Ingeo 3001D limits its use in appliance trim to components that remain below 55 °C under a load of 0.46 MPa when measured by ASTM D648-18; for a control knob positioned near a coffee boiler or oven vent, this threshold is exceeded unless post-mould annealing is applied. Compliance is governed by RoHS Directive 2011/65/EU, with Pb, Cd, Hg, and Cr(VI) measurement according to IEC 62321-5:2013 and IEC 62321-4:2013, plus REACH Regulation (EC) No 1907/2006. The formulation is 100 parts Ingeo 3001D with 1 wt% to 3 wt% colour masterbatch; glass-fibre reinforcement is not used because it increases screw wear and reduces surface gloss for fascia parts. If a UL 94 flame rating is required, a non-halogenated flame-retardant masterbatch at 5 wt% to 10 wt% may be incorporated only after verification of notched Izod and melt flow shifts. The downstream process uses melt temperature 190 °C to 210 °C, mould temperature 25 °C to 40 °C, and cooling time 15 s to 25 s for wall sections of 1.5 mm to 3.0 mm. Post-mould annealing at 80 °C for 1 h raises the heat deflection temperature to approximately 85 °C at 0.46 MPa but introduces volumetric shrinkage of 0.3% to 0.5%, which must be compensated in tool dimensions. Terminal product types include control knobs, fascia trims, internal clips, and non-heat-exposed housings.
For transparent cold-use food service trays, the amorphous clarity of Ingeo 3001D is retained only when the cooling rate from melt to below the glass transition temperature of approximately 55 °C to 60 °C is rapid enough to suppress spherulite growth and haze. Compliance is established under EU Regulation 10/2011 and Regulation (EC) No 1935/2004, with overall migration testing per EN 1186-1:2002; U.S. food-contact status depends on the manufacturer’s Food Contact Notification. The formulation boundary is 100 parts Ingeo 3001D with no nucleating agent, because nucleating additives increase crystallinity and reduce transparency; if anti-block performance is needed for stackability, an antiblock masterbatch is added at 0.2 wt% to 0.5 wt%. Regrind is limited to 10 wt% when optical clarity is a release criterion, and moisture must remain below 250 ppm after drying at 80 °C for 4 h. The production process uses valve-gate hot runner or cold runner systems, melt temperature 185 °C to 205 °C, mould temperature 15 °C to 25 °C, injection speed 100 mm/s to 150 mm/s, and cooling time 6 s to 10 s for wall thicknesses of 0.6 mm to 1.5 mm. Terminal products are clear deli containers, bakery clamshell inserts, cold cup lids, and fruit trays.
Конкурентные цены Ingeo ™ Biopolymer 3001D High Flow Injection Molding PLA, которые соответствуют вашему бюджету - гибкие условия и индивидуальные котировки для каждого заказа.
Для получения образцов, цен или более подробной информации свяжитесь с нами по адресу +8618136850665 или отправить по почте admin@ascent-chem.com.
Мы ответим вам как можно скорее.
Телефон: +8618136850665
Электронная почта: admin@ascent-chem.com
Гибкие условия оплаты, конкурентоспособные цены, первоклассное обслуживание — обращайтесь прямо сейчас!
The Ingeo™ Biopolymer 3001D High Flow Injection Molding PLA is a poly(lactic acid) (PLA) resin formulated for injection molding of thin-wall articles, multi-cavity tooling, and components with extended flow-path requirements. The grade is supplied in pellet form and is characterized by a nominal specific gravity of 1.24 g/cm³ when tested according to ASTM D792. Published manufacturer data indicate a melt mass-flow rate of 15 g/10 min at 210 °C under 2.16 kg load using ASTM D1238, placing the material in the high-flow segment of the Ingeo portfolio. These values are representative batch-release data and are not specification limits; lot-specific certificates of analysis should be consulted for production decisions. The typical property set is summarized in Table 1.
| Property | Typical Value | Test Standard |
|---|---|---|
| Specific gravity | 1.24 g/cm³ | ASTM D792 |
| Melt mass-flow rate | 15 g/10 min at 210 °C/2.16 kg | ASTM D1238 |
| Tensile yield strength | 60 MPa | ASTM D638 |
| Tensile elongation at break | 3.5% | ASTM D638 |
| Flexural strength | 83 MPa | ASTM D790 |
| Flexural modulus | 3820 MPa | ASTM D790 |
| Notched Izod impact | 16 J/m | ASTM D256 |
| Heat deflection temperature at 0.45 MPa | 55 °C | ASTM D648 |
The numerical designation 3001D is a supplier product code for a high-flow injection molding grade within the broader Ingeo PLA product family. The supplier’s public documentation does not assign a formal compositional meaning to the suffix, but the grade is differentiated from general-purpose injection molding, extrusion, and high-heat PLA materials by its balance of melt fluidity and molecular weight retention. Published data for this specific configuration are limited with respect to direct side-by-side comparisons; however, the elevated melt flow rate relative to general-purpose injection grades permits reduced filling pressure, thinner nominal wall sections, and shorter cooling time. The corresponding trade-off is a reduction in melt strength, which restricts the use of 3001D in profile extrusion, blow molding, and foaming processes where extensional viscosity and strain hardening are required. Products in the Ingeo line described as high-heat or nucleated grades typically exhibit higher heat deflection temperatures and increased crystallinity development, while impact-modified grades use elastomeric or particulate additives to raise notched Izod values. The 3001D grade is not formulated as an inherent high-heat or high-impact system.
Pre-drying is required before melt processing. Ingeo PLA is hygroscopic, and ambient moisture uptake shifts melt flow rate upward through hydrolysis while producing splay, silver streaking, and reduced tensile strength in molded parts. Moisture content should be verified by Karl Fischer titration according to ISO 15512 or ASTM D6869; the target is below 0.025% (250 ppm). Typical drying conditions use 80–100 °C for 4–6 h in a desiccant-bed dryer with a dew point of -40 °C or lower. Production environments with relative humidity above 60% should employ hopper drying and avoid open pellet transfer. On production-scale injection molding machines ranging from 60 tonnes to 250 tonnes clamp force with 20:1 to 24:1 L/D general-purpose screws, barrel temperature profiles are commonly set from 180 °C at the rear zone to 220 °C at the nozzle, with a measured melt temperature of 190–230 °C. Mold temperature may be controlled between 25 °C and 60 °C; lower mold temperatures shorten cycle time but increase internal stress, while higher mold temperatures improve surface replication at the cost of longer cooling. Screws with a compression ratio of 2.2:1 to 3.0:1 and low-shear check rings are used in practice; high-compression, high-shear screws can generate excessive frictional heat and accelerate polymer degradation. Residence time at melt temperature should not exceed the supplier-recommended limit, because extended hold times produce lactide reformation, viscosity drift, and black specks. Purge procedures at the end of production commonly use polypropylene or general-purpose polystyrene, because PLA degrades when left at elevated temperature in the barrel. Published data for screw-specific optimization of 3001D is limited; process validation on the actual molding cell is required.
The high melt flow rate of 3001D influences mold filling through a reduction in injection pressure and an increase in flow length relative to wall thickness. Melt viscosity is temperature- and shear-rate dependent, but the supplier’s public documentation does not provide a full shear-rate viscosity curve. When such data are required, parallel-plate rheometry may be performed according to ISO 6721-10 or capillary rheometry according to ISO 11443. In practical injection molding, the high-flow characteristic permits wall sections down to 0.4–0.8 mm for short flow distances, although gate size, venting, and mold temperature dominate the lower wall limit. Published data for wall-section minima in multi-cavity tooling for this specific grade are limited. Injection pressures on production-scale machines are typically lower than those required for general-purpose PLA; actual values depend on flow-path length, gate geometry, and cavity thickness. Rapid filling speed is usually combined with a short hold-pressure profile to reduce gate freeze-off and molded-in stress. The material stiffens rapidly during cooling; therefore screw cushion and switch-over point should be controlled within narrow tolerances to prevent sink marks and dimensional variation. Jetting, gate-stringing, and weld-line visibility are potential failure modes in thin-wall tooling with poor gate placement or undersized runners.
End-use applications for Ingeo 3001D are concentrated in injection molded articles where high clarity, dimensional replication, and short cycle times are primary requirements. Typical examples include thin-wall drinking cups, cosmetic packaging, rigid consumer packaging inserts, single-use cutlery, and non-load-bearing housings for consumer electronics. These applications exploit the material’s tensile yield strength of 60 MPa and flexural modulus of 3820 MPa determined under ASTM D638 and ASTM D790, respectively. The notched Izod impact value of 16 J/m under ASTM D256 indicates a comparatively brittle response relative to polyolefins; impact-critical closures, snap-fit arm designs, and load-bearing living hinges require careful section design or selection of a higher-impact Ingeo grade. Continuous service temperature is limited by the heat deflection temperature of 55 °C at 0.45 MPa when tested under ASTM D648. Molded parts should not be exposed to temperatures above the glass transition range for sustained periods, because dimensional relaxation and warpage can occur. The resin is not recommended for hot-fill containers, dishwasher-durable items, or other applications with repeated thermal excursions above 50–55 °C unless post-mold annealing or nucleating packages are applied.
When a high-flow PLA grade is selected over a general-purpose injection grade, the primary benefits are the ability to fill thinner, longer, or multi-cavity geometries at lower melt temperature and reduced injection pressure. The 3001D grade is differentiated from standard injection molding PLAs by its higher nominal melt flow rate. This flow characteristic can support shorter cycle times and lower clamp force requirements; however, these gains are accompanied by lower notched impact resistance, higher notch sensitivity, and lower heat deflection temperature than some impact-modified or nucleated grades in the same product family. The material’s reduced melt strength makes it unsuitable for extrusion foam, blow molding, and profile extrusion operations. In mold-filling simulations, apparent melt viscosity should be measured on the actual lot because the supplier’s published data are not sufficient for high-accuracy CAE analysis. Shrinkage is typically lower than semi-crystalline commodity resins but is anisotropic; mold shrinkage values are not publicly specified for all geometries. Different Ingeo grades with lower melt flow may be selected when thick-wall parts require less jetting, better packing control, or reduced gate-stringing. Direct substitution of 3001D in a mold developed for a general-purpose PLA may require re-validation of shot size, cushion, hold pressure, and cooling time.
Compliance statements for Ingeo 3001D should be confirmed with the supplier for the specific packaging or medical application. Unfilled PLA grades of this type are commonly evaluated under food contact regulations such as EU 10/2011 and US FDA 21 CFR 175.300, but migration limits depend on additive composition, final part thickness, and food type. The material is not inherently implantable-grade; biomedical device developers must conduct ISO 10993 biological evaluation on the finished device. The resin is moisture-sensitive, and storage in sealed bags is required after opening. Published data for long-term outdoor UV stability and hydrolytic aging of this specific configuration are limited; UV-exposed outdoor applications require stabilizer additives that are not part of the standard formulation.