| HS Code | 961579 |
| Product Name | TRANSMARE BIO-35MI-10NF30-0.101 |
| Manufacturer | Transmare |
| Material Type | Polylactic Acid (PLA) compound |
| Polymer Base | Polylactic Acid (PLA) |
| Filler | Bamboo Fiber |
| Filler Content | 30% |
| Grade | High Impact Injection Molding |
| Processing Method | Injection Molding |
| Appearance | Natural/Beige Pellets |
| Form | Solid Pellets |
| Bio Based | Yes |
| Biodegradable | Yes |
| Compostable | Yes (industrial composting) |
| Density | 1.30 g/cm³ (typical) |
| Melt Flow Rate | 35 g/10 min (190°C/2.16 kg, typical) |
| Tensile Strength | 35 MPa (typical) |
| Tensile Modulus | 4500 MPa (typical) |
| Elongation At Break | 4% (typical) |
| Flexural Modulus | 5000 MPa (typical) |
| Flexural Strength | 60 MPa (typical) |
| Notched Charpy Impact Strength | 6 kJ/m² (typical) |
| Notched Izod Impact Strength | 7 kJ/m² (typical) |
| Heat Deflection Temperature | 60°C at 0.45 MPa (typical) |
| Vicat Softening Temperature | 70°C (typical) |
| Drying Temperature | 80°C |
| Drying Time | 3-4 hours |
| Melt Temperature | 180-200°C |
| Mold Temperature | 20-50°C |
| Moisture Content | <0.025% |
As an accredited TRANSMARE BIO-35MI-10NF30-0.101 30% Bamboo Fiber High Impact Injection Polylactic Acid factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | For TRANSMARE BIO-35MI-10NF30-0.101: 25 kg moisture-proof kraft paper bags with inner PE liner, palletized and stretch-wrapped for transport. |
| Container Loading (20′ FCL) | TRANSMARE BIO-35MI-10NF30-0.101 30% bamboo fiber high-impact injection polylactic acid securely loaded into a 20′ FCL container for safe ocean transport. |
| Shipping | TRANSMARE BIO-35MI-10NF30-0.101 ships as non-hazardous, solid PLA compound pellets containing 30% bamboo fiber. Pack in moisture-barrier bags or fiber drums. Keep dry, cool, sealed, and away from heat, sunlight, and contamination. Not regulated for transport; standard freight applies. Handle carefully to prevent package damage. Use appropriate PPE when handling. |
| Storage | Store TRANSMARE BIO-35MI-10NF30-0.101 in a cool, dry, well-ventilated warehouse. Keep original packaging tightly sealed, off the ground, away from direct sunlight, heat, ignition sources, moisture, and incompatible materials. Maintain low humidity, ideally 15–25°C; use desiccant if required. Prevent dust and contamination. Avoid prolonged humid-air exposure to reduce hydrolysis risk. Rotate stock using FIFO and follow the supplier’s SDS. |
| Shelf Life | Shelf life is typically 12 months when sealed in original packaging, stored cool, dry, and away from moisture and sunlight. |
Competitive TRANSMARE BIO-35MI-10NF30-0.101 30% Bamboo Fiber High Impact Injection Polylactic Acid prices that fit your budget—flexible terms and customized quotes for every order.
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TRANSMARE BIO-35MI-10NF30-0.101 is a high-flow injection-molding grade of polylactic acid compounded with 30 wt% bamboo fiber and a high-impact modification package. The code fragment -35MI is interpreted as a melt flow index class of 35 g/10 min when determined at 210 °C under 2.16 kg load according to ISO 1133-1:2022, while -NF30 denotes the nominal natural fiber loading and -0.101 is a formulation revision identifier. The material is intended for injection-molded rigid articles requiring a balance of bio-based content, stiffness, and improved notched impact behavior relative to unmodified PLA. Published data specific to this commercial formulation is limited; numerical ranges cited below derive from peer-reviewed studies of PLA/bamboo fiber composites at similar fiber contents and from standard test methods, not from lot-specific certificates of analysis.
Rheologically, the 35 g/10 min MFR class places this compound within a fast-fill regime for thin-wall tooling. The presence of lignocellulosic fiber reduces melt elasticity and can induce wall slip at high shear rates. Nozzle pressure losses are typically higher than neat PLA at equivalent MFR because the fiber network increases extensional viscosity. Capillary rheometry on bamboo/PLA systems reported in the literature indicates shear-thinning behavior with a power-law index n in the range of 0.3–0.5 at 190–210 °C. Injection tooling therefore requires adequately sized gates, preferably ≥1.0 mm for wall sections ≤2.5 mm, and polished runner surfaces to reduce flow marks.
Compounding of this product class is typically executed on a co-rotating twin-screw extruder with a length-to-diameter ratio of 40:1–48:1 and a side feeder for bamboo fiber to limit fiber attrition. Barrel temperatures are commonly profiled as 170 °C, 180 °C, 190 °C, 200 °C, 200 °C, 195 °C, and 190 °C across zones. Melt temperature monitored via infrared probe should not exceed 210 °C. Vacuum venting at -0.08 MPa is applied to remove moisture and volatile extractives. Raw bamboo fiber is pre-dried at 90 °C for 3 h to reach <1 % moisture before compounding because fiber moisture variation is a known source of batch-to-batch inconsistency in melt pressure and mechanical properties.
Injection molding of TRANSMARE BIO-35MI-10NF30-0.101 is constrained by the thermal sensitivity of both PLA and bamboo lignocellulose. The recommended melt temperature range is 190–210 °C. Barrel profiles should begin at 160–170 °C in the feed zone and rise to 200–210 °C at the metering zone. Nozzle temperature is typically set at 200–205 °C. Mold temperature should be held between 30 °C and 60 °C; lower mold temperatures reduce cycle time but may increase molded-in stress, while higher mold temperatures improve surface appearance and fiber wetting at the cost of longer cooling time.
A medium-shear general-purpose screw with L/D 20:1–24:1 and compression ratio 2.5:1–3.0:1 is adequate. A non-return valve with zero-clearance ring should be used to prevent fiber packing in the valve. Injection speed is set in the medium-to-high range to maintain a continuous melt front; excessively low speed can cause premature freezing in thin sections, while excessively high speed may generate shear heating beyond 215 °C. Holding pressure is commonly 60–80 MPa, with holding time adjusted to gate seal. Back pressure should be kept at 0.5–1.0 MPa to homogenize melt without extending residence time. Screw speed is typically 50–100 rpm for screw diameters of 25–35 mm. Mold shrinkage for this class of material is anisotropic, with published values of 0.5–0.9 % in the flow direction and 0.8–1.3 % transverse to flow under ISO 294-4 conditions. Tooling should account for this anisotropy in dimensional tolerance planning.
Pre-drying of pellets is mandatory. A desiccant dryer is set at 80 °C for 4 h, using a dew point of -40 °C or lower. Target residual moisture before injection is <250 ppm, as measured by ISO 15512:2019. Moisture above this level hydrolyzes PLA ester linkages during processing, causing viscosity loss, splay, and a measurable reduction in tensile strength. If ambient relative humidity exceeds 60 %, pellets should be transferred directly from dryer to hopper through a sealed line or consumed within 2 h of drying.
Residence time at melt temperatures above 200 °C should not exceed 5 min. Longer residence times produce discoloration and an acrid odor from thermal degradation of bamboo hemicellulose. Thermogravimetric analysis under nitrogen shows initial mass loss for bamboo lignocellulose beginning near 230 °C, but visible browning and strength loss can occur earlier in oxygen-containing melt atmospheres. Hot runner systems should be operated at ≤210 °C, and any heated sprue bush should be configured for minimum dead volume. If a shutdown exceeds 15 min, the barrel should be purged with virgin PLA at 190 °C before restart.
Production-scale experience on servo-electric toggle presses with clamping force in the 1000–1600 kN range indicates that gate blush and gas burns are the most frequent defects when this class of material is run outside the stated window. Ventilation depth in the mold should be 0.01–0.02 mm for the cavity periphery. Excessive vent depth may generate flash because the high-flow matrix fills thin gaps readily.
In substitution trials where this grade replaces talc-filled polypropylene or ABS in rigid consumer packaging, the processing comparison is not direct. Bamboo-filled PLA exhibits higher melt pressure sensitivity to fiber orientation than talc-filled systems. Unlike talc, bamboo fiber has a measurable aspect ratio and can partially orient during filling, producing tensile and shrinkage anisotropy. Compared with unfilled PLA, the fiber network reduces die swell and improves dimensional stability but narrows the melt processing window. Compared with glass-filled PLA, the bamboo fiber grade produces lower abrasion on screw and barrel surfaces and reduces melt density, but it does not achieve equivalent tensile modulus. These differences are evaluated through ISO 527-2, ISO 178, and ISO 180 before tool design release.
The primary substitution logic is weight reduction and bio-based content. Bamboo fiber density is approximately 1.30–1.50 g/cm³, whereas continuous glass fiber is near 2.54 g/cm³. At 30 wt% loading, a bamboo-filled PLA compound can yield a molded part density in the range of 1.28–1.36 g/cm³, compared with 1.45–1.55 g/cm³ for a 30 wt% glass-filled PLA compound. The bamboo-filled grade also reduces tool wear and eliminates glass-fiber skin irritation hazards during handling. However, tensile modulus of bamboo-filled PLA is lower: published ranges for 30 wt% bamboo/PLA composites are 4.0–5.5 GPa, while glass-filled PLA at equivalent loading commonly exceeds 8.0 GPa. Notched Izod impact values depend strongly on the impact modifier and coupling agent; for similar systems, values of 4.0–8.0 kJ/m² are reported when a high-impact modifier is present.
In semi-structural housings, the grade is not a drop-in replacement for glass-filled ABS where heat deflection temperature under load exceeds 80 °C. For PLA/bamboo composites, HDT at 0.45 MPa is typically 55–65 °C per ISO 75-2:2013, whereas ABS grades commonly reach 90–100 °C. The product therefore suits non-thermal load-bearing housings, snap-fit enclosures, interior trim, and disposable rigid items rather than under-hood or hot-water-contact components.
Table 1 summarizes published property ranges for comparable PLA/bamboo fiber systems. Values are not lot-specific guarantees for TRANSMARE BIO-35MI-10NF30-0.101 but provide a screening basis for material selection. The largest source of variation is fiber surface treatment: alkaline, silane, or maleic anhydride-grafted PLA coupling treatments shift tensile strength and notched impact by 10–30 % depending on dosage.
| Property | Test method | Neat PLA | PLA + 30 wt% bamboo fiber | PLA + 30 wt% glass fiber |
|---|---|---|---|---|
| Density | ISO 1183-1:2019 | 1.24 g/cm³ | 1.28–1.36 g/cm³ | 1.45–1.55 g/cm³ |
| Tensile strength | ISO 527-2:2012 | 50–70 MPa | 48–63 MPa | 80–110 MPa |
| Tensile modulus | ISO 527-2:2012 | 3.0–3.5 GPa | 4.0–5.5 GPa | 8.0–10.0 GPa |
| Elongation at break | ISO 527-2:2012 | 2.0–6.0 % | 1.5–3.2 % | 1.0–2.0 % |
| Notched Izod impact | ISO 180:2019 | 2.0–3.0 kJ/m² | 4.0–8.0 kJ/m² | 5.0–8.0 kJ/m² |
| HDT at 0.45 MPa | ISO 75-2:2013 | 50–55 °C | 55–65 °C | 60–70 °C |
| Mold shrinkage, flow direction | ISO 294-4 | 0.4–0.7 % | 0.5–0.9 % | 0.2–0.4 % |
For application-specific comparison, tensile testing should follow ISO 527-2:2012 specimen type 1A, and flexural testing should follow ISO 178:2019 at 2 mm/min. Notched Izod impact is reported with edgewise notch orientation and specimen type 1A. The available published data for this specific configuration is limited; when a manufacturer-specific data sheet is available, it supersedes these literature ranges.
Biobased and biodegradable claims cannot be assumed from bamboo fiber content alone. The impact modifier and processing aids must also be evaluated. Table 2 presents the applicable test matrix for regulatory screening. Certification for industrial composting under EN 13432:2000 requires 90 % disintegration in 12 weeks and 90 % biodegradation in 180 days for the complete formulation. If the impact modifier is non-biodegradable, the compound will fail organic recovery thresholds even though PLA and bamboo are compostable.
| Area | Standard or regulation | Typical condition or requirement | Relevance to bamboo-filled PLA |
|---|---|---|---|
| Biobased carbon content | ASTM D6866-22 | Carbon isotope ratio by accelerator mass spectrometry | Confirms biogenic fraction if supplier certifies |
| Industrial compostability | EN 13432:2000 | 90 % disintegration in 12 weeks; 90 % biodegradation in 180 days | Requires evaluation of impact modifier and stabilizers |
| Food contact migration | EU 10/2011 or FDA 21 CFR 175.300 | Specific migration limits by simulant and time/temperature | Lot-specific testing required before food-contact use |
| Automotive interior emissions | VDA 277 | Total VOC emission by headspace GC | Natural fiber extractives may increase volatile content |
| Flammability | UL 94 | HB or V rating at stated thickness | Bamboo fiber can increase burn rate; flame retardant needed for V-class |
| Hazardous substances | EU 2011/65/EU RoHS and 1907/2006 REACH | Restricted substance limits and SVHC declaration | Required for electronic accessory applications |
For automotive interior clips and housings, emission testing under VDA 277 may reveal higher total volatile organic compound values than mineral-filled PLA because bamboo lignin and extractives can release low-molecular-weight aldehydes at elevated tooling temperatures. Specimen conditioning should follow the relevant standard atmosphere, typically 23 °C and 50 % relative humidity for 88 h, before mechanical testing.
Continuous service temperature for this material class is not equivalent to short-term HDT. Sustained exposure above 55 °C can initiate progressive deformation, especially under load. Steam sterilization at 121 °C is not acceptable because PLA undergoes hydrolysis and rapid mechanical degradation. Dishwasher cleaning cycles above 65 °C should be excluded unless the part has been specifically validated. Alkaline cleaning agents with pH above 9 hydrolyze PLA ester bonds and cause surface erosion. Strong oxidizing acids and concentrated acetic acid are also incompatible. If chemical resistance is required, testing should follow ISO 175:2010 with the intended contact fluid and service temperature.
The compound should not be combined with amine-based additives, certain azo colorants, or high-pH masterbatches during downstream compounding because these can accelerate PLA degradation. Storage should be in vapor-barrier bags at 15–30 °C and relative humidity below 60 %. Under uncontrolled humidity, natural fiber can absorb moisture and generate processing defects even after nominal drying. In injection molding plants with mixed recycled feedstock, delivery systems and granulators must be segregated because PLA contamination in PET recycling streams causes haze and thermal degradation; bamboo fiber also complicates separation in mechanical recycling. The material is therefore not a default drop-in for commingled municipal recycling flows, but it is suitable for controlled biopolymer waste streams where industrial composting or dedicated PLA chemical recycling infrastructure exists.