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NaturePlast NPW SEA 252 Nylon 11 Biocomposite

    • Product Name: NaturePlast NPW SEA 252 Nylon 11 Biocomposite
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 476619
    Density 1.08 g/cm³
    Melting Point 185 °C
    Glass Transition Temperature 45 °C
    Melt Flow Index 230 C 2 16 Kg 4 g/10 min
    Tensile Modulus 1500 MPa
    Tensile Strength At Break 35 MPa
    Elongation At Break 20 %
    Flexural Modulus 1300 MPa
    Charpy Impact Strength Notched 23 C 25 kJ/m²
    Shore D Hardness 65
    Water Absorption 24 H 23 C 2.5 %
    Bio Based Carbon Content 100 %

    As an accredited NaturePlast NPW SEA 252 Nylon 11 Biocomposite factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Supplied in 25 kg sealed paper bags with PE liner, moisture-protected and nitrogen-purged for safe handling and storage.
    Container Loading (20′ FCL) 20′ FCL container loaded with NaturePlast NPW SEA 252 Nylon 11 Biocomposite, securely packed for safe transport.
    Shipping NaturePlast NPW SEA 252 Nylon 11 Biocomposite ships as dry, sealed pellets in standard packaging to protect against moisture uptake. Store in a cool, dry area away from direct sunlight. Not classified as dangerous goods, so it transports via standard freight, avoiding excessive heat and humidity during transit.
    Storage Store in a cool, dry, well-ventilated area, ideally below 25°C, in its original sealed packaging. Protect from direct sunlight, moisture, and humidity, as the biocomposite is hygroscopic. Avoid exposure to extreme heat, sparks, or incompatible chemicals. Keep containers tightly closed to prevent contamination. Maintain good housekeeping and use within recommended shelf life for optimal performance.
    Shelf Life Store in sealed, dry, cool conditions. Shelf life is 2 years from date of manufacture when unopened.
    Application of NaturePlast NPW SEA 252 Nylon 11 Biocomposite

    In multilayer nylon 11 vapour management and pneumatic brake tubing, NPW SEA 252 is let down into virgin polyamide 11 at 25 wt% to 35 wt% for small-diameter vapour return and purge lines; for spiral-cut truck air brake jackets the grade is used at 15 wt% to 25 wt% in the outer core layer to retain the burst strength contribution of the virgin PA11 inner layer. Compliance is governed by ISO 7628-1:2010 for thermoplastic tubing in road vehicles and SAE J844 for non-metallic air brake tubing; formulations are additionally screened under REACH 1907/2006 and RoHS 2011/65/EU at compound level. Extrusion is performed on a single-screw tubing extruder with L/D 30:1, a barrier screw and three-zone vacuum calibration; pellets are pre-dried at 80°C for 4 h to below 0.08% moisture before melt processing. Melt zones are held at 210°C to 220°C, a narrow band because the seaweed-derived lignocellulosic filler fraction starts to brown at higher barrel settings, generating black specks and a measurable drop in elongation at break. Production-scale failure modes recorded on tubing lines include internal melt fracture at line speeds above 45 m/min when the outer layer viscosity falls below the inner layer viscosity, and pinhole formation in vacuum sizing when the compound moisture exceeds 0.12%. Terminal parts include compressed air brake lines for heavy goods vehicles, fuel vapour return tubes in gasoline direct injection evaporative systems, purge lines in hybrid fuel tanks, and protective jacketing for hydrogen fuel cell drain lines where low-temperature impact is required.

    Does NPW SEA 252 Retain Impact After Gamma Irradiation at 25 kGy?

    For reusable medical device housings, the relevant biological evaluation is ISO 10993-5:2009 for in vitro cytotoxicity and USP <88> Class VI for systemic injection, intracutaneous and implantation reactivity; if the component contacts only intact skin for transient periods, the minimum requirement is typically ISO 10993-1:2018 surface-contacting classification. NPW SEA 252 is introduced at 10 wt% to 20 wt% into a virgin polyamide 11 base for injection-moulded handles, instrument bodies and detachable clips; higher loadings above 20 wt% increase surface roughness and reduce post-sterilisation impact retention because moisture absorbed by the biofiller expands during autoclaving. Moulding uses an injection-moulding machine with a 25:1 general-purpose screw, melt temperature 200°C to 215°C, mould temperature 50°C to 70°C, and pre-drying to 0.06% moisture; hold pressure is maintained until gate freeze to avoid sink marks in thick clip bosses. Terminal products are dental scaler handles, examination light housings, surgical tray retaining clips and reusable instrument grips. Validation data for this specific NPW SEA 252 configuration under repeated autoclave cycles are not published; therefore batch release should include ISO 527-2:2012 tensile retention after 25 kGy gamma and 134°C steam cycles before production acceptance.

    Ophthalmic Frame Hinge Stress and Biofiller Dispersion Limits

    Injection moulding of NPW SEA 252 into eyewear front rims and temple arms typically uses a let-down of 8 wt% to 12 wt% in a polyamide 11/12 alloy to balance flexural recovery and hinge torque retention. The governing frame standard is ISO 12870:2016, with dimensional stability and nickel-free hinge assemblies also screened under REACH 1907/2006 and RoHS 2011/65/EU. The compound is pre-dried at 80°C for 4 h to 0.08% moisture and injected at 190°C to 210°C barrel temperature into polished steel moulds at 40°C to 60°C; biofiller agglomerates larger than 60 µm cause visible surface specks and must be removed by 100 µm melt filtration before the nozzle. Terminal parts are optical frames, sunglass fronts, children’s eyewear temple arms and snap-on optical lens covers. The main production defect observed on high-gloss moulds is gate blush when injection speed exceeds 45 mm/s, requiring reduced velocity profile rather than higher melt temperature because the natural filler imposes a 220°C ceiling before yellowing.

    Downstream sectorAddition ratio in PA11Melt ceilingPre-drying moisture limitPrimary standard set
    Automotive vapour and pneumatic tubing15–35 wt%220°C0.08%ISO 7628-1:2010; SAE J844
    Medical device housings10–20 wt%215°C0.06%ISO 10993-5:2009; USP <88>
    Ophthalmic frames8–12 wt%210°C0.08%ISO 12870:2016
    Industrial flexible conduit10–20 wt%220°C0.10%IEC 61386-23:2018; UL 94 HB
    Sports and recreation load parts20–30 wt%210°C0.06%ASTM D638-14; ISO 179-1:2020
    Electronic snap-fit clips15–25 wt%215°C0.10%IEC 62368-1:2018; RoHS 2011/65/EU

    When a corrugated loom extrusion line changes from fossil PA12 to NPW SEA 252, the material is generally added at 10 wt% to 20 wt% into PA11 carrier resin to maintain flexibility while increasing the bio-based content of the conduit wall without changing corrugator tooling. The relevant compliance set includes RoHS 2011/65/EU, UL 94 HB for flammability of the finished conduit, and IEC 61386-23:2018 for flexible conduit systems where installed in building or rail environments. Drying before extrusion is required at 80°C for 4 h to 0.10% moisture; single-screw corrugator lines with L/D 28:1 and vacuum calibration process the compound at 200°C to 220°C, with corrugator speed adjusted by 5% to 8% slower than virgin PA12 due to higher melt elasticity. Terminal products include railway cable protection conduits, robotic dress-pack covers, pneumatic control bundles, and split loom for off-highway equipment. The primary production bottleneck is corrugation collapse when the parison temperature exceeds 220°C; high-speed corrugation data for this specific grade remains limited, so line trials require stabilised parison weight verification every 30 min.

    When Barrel Residence Time Exceeds 6 Minutes at Lower Melt Temperatures

    Thermal degradation kinetics become the controlling factor when NPW SEA 252 is injection moulded into sports and recreation load-bearing components at addition ratios of 20 wt% to 30 wt% in PA11. The compliance baseline for mechanical validation is ASTM D638-14 for tensile properties and ISO 179-1:2020 for Charpy notched impact, with end-use requirements often referencing ISO 527-2:2012 and ISO 75-2:2013 HDT at 0.45 MPa. Pre-drying is set at 80°C for 5 h to 0.06% moisture; barrel profile is 195°C to 210°C with nozzle at 205°C, and back pressure limited to 20 bar to 30 bar to avoid excessive shear heating in the biofiller-rich melt. Total residence time must not exceed 6 min; above this threshold the natural filler undergoes progressive thermomechanical chain scission, producing caramel-like specks, reducing Charpy notched impact by more than 15%, and increasing melt volume-flow rate variability beyond the process capability window defined by ISO 1133-1:2022. Terminal products include trekking pole clamps, fishing reel side plates, archery riser inserts, and cycling saddle shells. Production-scale failures on 120 t clamp force machines are concentrated in short-shot conditions when the melt cushion falls below 3 mm, because the narrow temperature window leaves insufficient superheat for flow into thin ribs.

    Snap-Fit Retention Force in Dry-Moulded Electronic Device Clips

    Dry-moulded electronic snap-fit clips and internal brackets use NPW SEA 252 at 15 wt% to 25 wt% in PA11 to reduce water uptake while maintaining post-mould spring-back. The relevant compliance set is RoHS 2011/65/EU, IEC 62368-1:2018 for audio/video and information technology equipment, and ISO 294-1:2017 for injection moulding test specimen preparation. The material is dried to 0.06% moisture and moulded at 200°C to 215°C with injection speed below 55 mm/s and mould temperature 60°C to 80°C to prevent premature solidification at thin snap finger tips. Terminal parts are wearable electronic frames, battery bracket clips, laptop hinge covers, and sensor housings. Retention force stability depends on moisture content at moulding; above 0.10% moisture the moulded clip shows surface splay and snap-fit retention drops by 10% to 15% after 48 h conditioning at 23°C and 50% RH. Published data on long-term snap-fit creep in this natural-filled system is limited, so design validation should include ISO 527-2:2012 tensile creep measurements at 23°C and 50% RH.

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    Certification & Compliance
    More Introduction
    The material designated NaturePlast NPW SEA 252 Nylon 11 Biocomposite is a compounded polyamide 11 grade in which a renewable seaweed-derived filler phase is dispersed within a nylon 11 matrix obtained from castor oil-derived 11-aminoundecanoic acid. The product code separates the polymer family, filler origin, and grade level; NPW identifies the NaturePlast compounded biocomposite series, SEA the seaweed fraction, and 252 the specific formulation. Polyamide 11 itself contains a bio-based carbon fraction measurable by ASTM D6866-24 or ISO 16620-1:2018, with the unfilled matrix typically exceeding 90 % renewable carbon depending on stabilizer and processing-aid content. For NPW SEA 252, the seaweed filler is introduced to modify stiffness, density, and cool-down shrinkage relative to unfilled polyamide 11. Published property data for this specific configuration is limited; producer-issued lot datasheets remain the controlling source for melt flow, filler loading, moisture specification, and mechanical values. The grade is intended for injection moulding and selected extrusion applications where medium mechanical loads, chemical resistance, dimensional stability in humid environments, and bio-based raw-material content are specified. Generic polyamide 11 reference data cannot be substituted for a certificate of analysis, because filler particle size distribution and loading shift the rheological and mechanical response.

    What Regulatory and Compositional Boundaries Govern NPW SEA 252?

    Because the matrix is a long-chain polyamide synthesised from castor oil, the unfilled backbone generally meets high renewable-carbon thresholds, but the final biocomposite must be assessed under EU Regulation (EC) No 1907/2006 REACH for registered substances and under Directive 2011/65/EU RoHS for lead, mercury, cadmium, hexavalent chromium, PBB and PBDE. Compliance claims should be traceable to lot-specific X-ray fluorescence screening and supplier declarations. For food-contact applications, migration testing under Regulation (EU) No 10/2011 or FDA 21 CFR 177.1500 may be required; the seaweed fraction introduces additional extractables that must be quantified before any food-contact assertion is made. Total renewable carbon can be determined by ASTM D6866-24 and ISO 16620-2:2019. No universal statement of compostability should be attached to NPW SEA 252; polyamide 11 is hydrolytically stable under ambient conditions and is not certified as home compostable. If industrial compostability is claimed, it must be validated under ISO 14855-1:2012 or ASTM D5338-15 only for the exact environment and certificate scope. The REACH dossier and Safety Data Sheet should be consulted for any residual solvent, processing aid, or surface-treatment substance introduced during compounding. Before NPW SEA 252 is released to an injection-moulding barrel or single-screw extrusion line, the hygroscopicity of the polyamide 11 matrix and the seaweed filler must be addressed through closed-loop drying. Residual moisture above 0.1 % by weight, measured by ISO 15512:2019 or Karl Fischer titration, can hydrolyse the amide linkages during melt processing and reduce molecular weight. A desiccant dryer with dew point of −40 °C or lower, air temperature of 80 °C to 90 °C, and residence time of 4 h to 6 h is a conservative starting point; actual time depends on initial moisture and hopper design. Melt temperature for polyamide 11 compounds is typically maintained between 210 °C and 240 °C, with screw speed and back pressure selected to limit shear heating above 260 °C. For injection moulding, mould temperatures of 40 °C to 80 °C are used to control crystallinity and article surface quality; colder moulds can produce acceptable parts but may lower crystallinity and reduce dimensional stability at elevated service temperature. Base compounding for this filler class is normally carried out on a corotating twin-screw extruder with an L/D ratio of 40:1. If reprocessing is attempted on equipment with an L/D ratio below 24:1, dispersion of the seaweed filler may be incomplete and mechanical anisotropy may increase. A screw compression ratio of 2.2:1 to 2.8:1 and a metering length of 20 L/D to 22 L/D are common for unfilled polyamide 11; distributive mixing elements may be required for the filled SEA 252 grade. Shot size should remain within 25 % to 75 % of barrel capacity to limit residence time and thermal degradation. Because published processing data for NPW SEA 252 is limited, a shear-rate-dependent viscosity curve generated by capillary rheometry per ISO 11443:2021 is recommended before final barrel profiles, nozzle dimensions, and gate velocities are fixed.

    Mechanical and Thermal Substitution Benchmarks Under ISO Conditioning

    For engineering substitution, the relevant property set is governed by standardized specimen conditioning at 23 °C and 50 % relative humidity unless a dry-as-moulded condition is specified. Because no independent public database currently lists a complete ISO 527-2 and ISO 179-1 property card for NPW SEA 252, the matrix reference values below are presented only as unfilled polyamide 11 boundaries. Unfilled polyamide 11 is commonly reported with density in the range 1.03 g/cm³ to 1.05 g/cm³ under ISO 1183-1:2019, tensile yield stress 35 MPa to 45 MPa under ISO 527-2:2012, flexural modulus 900 MPa to 1200 MPa under ISO 178:2019, and notched Charpy impact at 23 °C of 5 kJ/m² to 15 kJ/m² under ISO 179-1:2023. NPW SEA 252 is expected to shift flexural modulus upward and notched Charpy impact downward relative to the unfilled matrix, depending on seaweed filler loading, particle aspect ratio, and interfacial adhesion. These shifts must be confirmed on production tools, because natural filler particle orientation and moisture uptake vary with gate location and wall thickness.
    ParameterStandardUse in NPW SEA 252 evaluation
    DensityISO 1183-1:2019Detects filler loading and affects weight-reduction comparisons
    Tensile modulus and strengthISO 527-1/-2:2012Replacement calculation for stiff structural clips and housings
    Flexural modulusISO 178:2019Assesses short-beam bending resistance under mounting loads
    Notched Charpy impactISO 179-1:2023Low-temperature and ambient ductility in snap-fit features
    Heat deflection temperatureISO 75-2:2013Upper service temperature for painted or coated parts
    Water absorptionISO 62:2008Dimensional stability and processing moisture control
    Bio-based carbonASTM D6866-24 / ISO 16620-2:2019Sustainability and feedstock verification
    Long-term creep, fatigue, and chemical-resistance comparisons require additional tests under ISO 899-1:2017, ASTM D7791-21, and ASTM D543-21 respectively. Data for NPW SEA 252 under these protocols is limited; qualification programmes should begin with screening at two representative stress levels rather than assuming linear extrapolation from unfilled PA11.

    When NPW SEA 252 Replaces Unfilled PA11 or Glass-Filled PA6

    Direct tool transfer from unfilled polyamide 11 to NPW SEA 252 should not be accepted without a shrink and flow review. Mould shrinkage for unfilled PA11 measured on plaque tools under ISO 294-4:2018 is generally in the range 0.8 % to 1.4 %, with the exact value controlled by wall thickness, mould temperature, and holding pressure. The seaweed filler in NPW SEA 252 can reduce overall shrinkage while increasing directional difference between flow and cross-flow orientations. Gates, rib thickness, and weld-line positions must therefore be adjusted using a production-scale trial with the actual tool steel temperature map, not a laboratory plaque. Compared with glass-filled polyamide 6, the unfilled polyamide 11 matrix of NPW SEA 252 has lower density and lower saturation water uptake. Unfilled PA11 is commonly reported to absorb 1.8 % to 1.9 % water at saturation under ISO 62:2008, while PA6 absorbs 9 % to 10 %. This reduces humid-service dimensional drift and tensile-property loss in NPW SEA 252 relative to standard PA6 compounds. Against talc-filled polypropylene, polyamide 11 provides higher heat deflection temperature under ISO 75-2:2013 and better resistance to aliphatic hydrocarbons when immersed according to ASTM D543-21; the biocomposite, however, is more hygroscopic and requires drying before processing. Against polyamide 12, NPW SEA 252 offers a bio-based polyamide backbone and similar long-chain amide chemistry, although the seaweed filler may reduce low-temperature impact. Published data for this specific configuration is limited; therefore, all substitution decisions should be made with a head-to-head capability study on the intended production press, using ISO 22514 or equivalent process-performance indices for critical dimensions. In consumer electronics housing and automotive interior trim applications, NPW SEA 252 is evaluated as a bio-based alternative to talc-filled polypropylene and glass-filled polyamide 6. Candidate parts include non-structural clips, cable-management channels, device housings, trim retainers, and moulded stiffeners where renewable raw-material content and polyamide chemical resistance are specified. Performance must be validated under end-use conditions: IEC 60068-2-30 for damp heat, ISO 4892-2:2013 for accelerated weathering if UV exposure is anticipated, and ISO 75-2:2013 or ASTM D648-18 for heat deflection. Outdoor service is limited by the PA11 matrix; long-term UV exposure can embrittle the surface unless carbon black, UV stabilizer, or coating is specified. Accelerated xenon-arc testing under ISO 4892-2:2013 with irradiance at 0.35 W/m² at 340 nm is a practical screening method, but correlation to outdoor weathering requires site-specific data. For interior parts, volatile organic compound and fogging requirements may apply under VDA 278 or ISO 12219-1:2021; the seaweed filler can alter the emission profile relative to unfilled PA11 and must be screened before production. Surface treatment for printing, painting, or bonding may require plasma activation or solvent wiping because natural fillers change surface polarity and may bloom low-molecular-weight species. Published data for this specific configuration is limited; therefore, trial parts should be produced on the intended production press with the actual hot-runner temperature profile and gate vestige, not extrapolated from generic PA11 processing curves.

    Assessing Batch-to-Batch Variation and Incoming Material Control

    Incoming material control for NPW SEA 252 should define moisture below 0.1 % by weight using ISO 15512:2019 or Karl Fischer titration, filler loading by ashing or thermogravimetric analysis linked to ISO 3451-1:2019, and melt viscosity by capillary rheometry per ISO 11443:2021. Because seaweed biomass can vary seasonally, the producer may report lot-specific bio-based carbon content by ASTM D6866-24 or ISO 16620-2:2019. Colour, odour, and outgassing should be measured before use in enclosed cabin interiors; VDA 277 or ISO 12219-1:2021 may be required by the OEM. The material should be stored sealed at 10 °C to 30 °C, and opened containers should be consumed within a defined period to avoid moisture regain. If regrind is used, addition should not exceed 20 % by weight without re-qualification unless supplier data supports higher ratios; natural filled grades are sensitive to repeated shear-history degradation and may show brownish discolouration at hot spots in the barrel. Injection moulders should monitor fill time, cushion, and peak cavity pressure as indirect indicators of viscosity shift. A sudden reduction in peak cavity pressure above 10 % from the validated baseline warrants a drying check and a melt-flow check before continued production.
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