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Evonik VESTAMID® LX9012 Bio30 Nylon 12

    • Product Name: Evonik VESTAMID® LX9012 Bio30 Nylon 12
    • 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 982972
    Product Evonik VESTAMID LX9012 Bio30
    Material Type Nylon 12 (Polyamide 12), bio-based
    Elongation At Break Percent >200

    As an accredited Evonik VESTAMID® LX9012 Bio30 Nylon 12 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 polyethylene-lined bags, ensuring moisture protection and safe handling of Evonik VESTAMID® LX9012 Bio30 Nylon 12.
    Container Loading (20′ FCL) 20′ FCL: palletized bags of Evonik VESTAMID® LX9012 Bio30 Nylon 12, securely loaded, ventilated, dry, protected from moisture and damage.
    Shipping Ship Evonik VESTAMID® LX9012 Bio30 Nylon 12 in sealed, moisture-proof packaging to preserve its bio-based polyamide properties. Store cool, dry, and ventilated; protect from heat and humidity. It is not classified as dangerous goods, but avoid dust inhalation and wear standard PPE during handling.
    Storage Store Evonik VESTAMID® LX9012 Bio30 Nylon 12 in its original, unopened packaging in a cool, dry, well-ventilated area. Keep sealed to prevent moisture absorption, which can affect processing. Avoid direct sunlight, heat sources, and humidity. Ideal temperature is below 30°C. Use within shelf life, rotating stock as needed.
    Shelf Life Store unopened in a cool, dry place; shelf life is typically two years from date of manufacture.
    Application of Evonik VESTAMID® LX9012 Bio30 Nylon 12

    In heavy-duty commercial vehicle air brake circuits, PA12 tube stock is specified over PA6 and PA66 because the equilibrium moisture regain of PA12 remains below 0.75% at 50% RH, limiting the burst-strength decay that water-plasticized short-chain nylons show after several thousand hours of load cycling. VESTAMID® LX9012 Bio30 in this segment is normally charged as a 100 wt% virgin resin feed; if a manufacturer proposes closed-loop regrind from tube start-up scrap, the addition ratio should not exceed 20 wt% without repeating the ISO 7628:2019 hydrostatic burst and SAE J844 environmental ageing sequence, because regrind-induced molecular weight reduction alters hoop-stress retention. The applicable compliance set comprises SAE J844 for nonmetallic air brake tubing, ISO 7628:2019 for air brake tube dimensional and performance properties, and DIN 74324-1 for European vehicle approval documentation. Downstream production is performed on a single-screw extruder with L/D not less than 24:1, preferably with a barrier-flight screw and a grooved feed section that controls melt-temperature rise below 250 °C; the resin must be predried to below 0.10% moisture at 80 °C for 4–8 h because hydrolytic degradation at the die lip manifests as microvoids and erratic inner-diameter chatter. The tube is vacuum-calibrated at the die exit and cooled through a water bath with descending temperature zones from 60 °C to 15 °C, followed by in-line laser diameter gauging and spark inspection for pinhole detection. Terminal finished products are truck, bus, and trailer air brake tubes, typically in 6 mm to 16 mm outside-diameter sizes, supplied in self-coiling or straight lengths with lot-level traceability under IATF 16949 documentation.

    What Is the Practical Lower Addition Limit for Radiopaque Loading in Catheter-Grade PA12?

    Medical-grade PA12 catheter shaft extrusion uses VESTAMID® LX9012 Bio30 as a 100% free-flowing compound feed only when the finished device does not require imaging contrast; where fluoroscopic tracking is specified, a barium sulfate-containing PA12 compound is processed at 100 wt%, but if the unfilled Bio30 grade is used as a dilution resin with a radiopacifier masterbatch, the let-down ratio is bounded by ISO 10993-1 biological evaluation, with published formulation practice limiting radiopacifier addition to the minimum needed to maintain visibility under 70 kVp fluoroscopy rather than a fixed universal percentage. The compliance framework for this segment is USP Class VI for systemic toxicity endpoints, ISO 10993-5 for cytotoxicity, ISO 10993-10 for irritation and sensitization, and ISO 10993-23:2021 for irritation under the updated test hierarchy, supported by material change management under ISO 13485. The downstream process is a cleanroom catheter shaft extrusion line, typically a 20:1 to 24:1 L/D single-screw extruder with a hardened barrel and a polished die tip, run at a melt temperature between 210 °C and 240 °C, with closed-loop vacuum sizing and water-free cooling for dimensionally critical lumens. Predrying at 70 °C for 6–12 h to below 0.10% moisture is mandatory; moisture-derived splay and lumen pitting are rejectable in catheter shafts with wall thicknesses below 0.25 mm. Terminal finished devices are minimally invasive catheter shafts, urological thermoplastic tubing, and non-implant device components, with published data for this specific Bio30 configuration in intravascular applications limited, requiring end-use validation by the device manufacturer.

    When Pneumatic Control Tube Dies Are Run at High Line Speeds

    In factory automation and rail pneumatic control installations, PA12 tube is processed at high haul-off velocities where melt fracture and dimensional tolerance loss become the binding constraints. The compounding addition ratio for VESTAMID® LX9012 Bio30 in this downstream segment is normally 100 wt% as supplied; if UV-stabilised black or colour-coded tube is required, a PA12 carrier masterbatch is added at a let-down ratio not exceeding 4 wt%, because higher organic pigment loading can reduce ISO 14743:2004 push-in fitting retention force through surface hardness changes. The relevant compliance standards are ISO 14743:2004 for push-in connector fittings and thermoplastic tube end geometry, ISO 8573-1:2010 for compressed air quality classes, and REACH 1907/2006 for European chemical registration. The downstream production line is a high-speed single-screw extruder with L/D 30:1, screw cooling in the feed zone, and a low-pressure die designed to maintain melt temperature between 220 °C and 240 °C at high screw output; moisture is held below 0.08% by desiccant dryers at 75 °C for 6 h, because high line speed amplifies moisture-generated surface roughness. Dimensional control is maintained by a twin-chamber vacuum calibrator with closed-loop air flow, and the finished tube is tested for minimum bend radius at −20 °C and +60 °C thermal cycling. Terminal products are push-in pneumatic control lines, machine tool air supply tubing, and rail door actuator lines with outside diameters from 4 mm to 12 mm, often supplied in self-coiling formats without internal spring support.

    Below-glass-transition impact behaviour in injection-molded structural shells often rules out short-chain polyamides, and PA12 compounds are specified when the part must survive multiple drops onto ice or rock without brittle cracking. VESTAMID® LX9012 Bio30 in this segment is dosed at 100% compound from pre-dried silos; if a manufacturer blends in in-house regrind from sprues and rejected shells, the addition ratio is typically capped at 30 wt% only after notched impact testing per ISO 179-1:2023 and tensile testing per ISO 527-2 confirm that the blend retains the required low-temperature Charpy values, because PA12 regrind can shift the crystalline morphology when reheated. The compliance base is REACH 1907/2006 for consumer goods, RoHS 2011/65/EU for restricted substances, and DIN ISO 5355 for ski touring boot shell to binding interface compatibility if the component is marketed as alpine equipment. The downstream production step is injection molding on a reciprocating screw machine with clamp force selected to keep melt residence time below the manufacturer’s degradation threshold; melt temperature is held between 240 °C and 270 °C, mold temperature is maintained at 40–80 °C to favour surface gloss and reduce sink marks, and gates are positioned away from high-tensile areas because PA12 weld-line strength is sensitive to flow-front temperature. Mold filling simulation should be combined with short-shot studies on the actual tool, not generic data, because unfilled PA12 exhibits a pronounced viscosity plateau under shear thinning. Terminal parts are alpine ski touring boot cuffs, mechanical orthotic brace shells, and cold-climate protective equipment housings, where published data for this specific Bio30 configuration in sport goods is limited and must be verified through end-use drop and flex-fatigue tests.

    Loose Tube Buffer Extrusion Beneath IEC 60794-1-2 Kink and Crush Loads

    In outdoor optical fibre cable manufacturing, PA12 serves as a loose tube buffer because its low post-molding shrinkage and controlled adhesion to water-blocking gels prevent micro-bend loss in stranded cable cores. The addition ratio for VESTAMID® LX9012 Bio30 in this segment is 100 wt% virgin compound; if a colour concentrate is needed for fibre identification, a PA12-based masterbatch is let down at 2–4 wt%, while the use of non-PA12 carrier resins is excluded because immiscible inclusions act as crack initiation points in the IEC 60794-1-2 crush test. Compliance is anchored to IEC 60794-1-2 for mechanical test procedures including crush, impact, and kink cycling, Telcordia GR-20 for outdoor plant optical cable performance when the cable is destined for North American operator networks, and ISO 1133-1:2022 for melt-mass flow rate verification prior to extrusion. Processing is performed on a precision single-screw extruder with L/D 30:1, a low-temperature screw profile, and a gear pump to stabilise melt delivery to the loose tube die, with melt temperature maintained between 230 °C and 250 °C. The resin is predried at 80 °C for 6 h to below 0.10% moisture; excessive moisture creates hydrolytic effects that elevate attenuation in finished cable after temperature cycling. The extrudate is quenched in a hot-water trough to set the crystalline structure, then vacuum-calibrated for wall thickness uniformity around the fibre bundle. Terminal products are optical fibre loose tube buffer tubes and certain tight-buffered cable jackets in outdoor infrastructure, with final cable tests performed under IEC 60794-1-1 and customer-specific bend-radius protocols.

    Application segmentPrimary compliance standardsCritical test conditionEnd-use boundary
    Air brake tubingSAE J844, ISO 7628:2019, DIN 74324-1Hydrostatic burst after environmental ageingTube wall below 1.0 mm requires ±5 °C die control
    Catheter shaft extrusionUSP Class VI, ISO 10993-5, ISO 10993-10, ISO 10993-23:2021Cytotoxicity and irritation endpointsWall thickness below 0.25 mm is splay-sensitive
    Pneumatic control lineISO 14743:2004, ISO 8573-1:2010, REACH 1907/2006Push-in fitting retention after thermal cyclingColor masterbatch above 4 wt% risks fitting-tube slip
    Injection-molded shellREACH 1907/2006, RoHS 2011/65/EU, DIN ISO 5355Charpy impact at −20 °CRegrind above 30 wt% requires full notched impact revalidation
    Optical loose tubeIEC 60794-1-2, Telcordia GR-20, ISO 1133-1:2022Crush and kink cyclingNon-PA12 masterbatch carrier excluded
    Application segmentAddition ratioDrying thresholdMelt temperaturePrimary process constraint
    Air brake tubing100 wt% virgin; regrind ≤20 wt%Below 0.10% moisture; 80 °C for 4–8 h230–250 °CDie excursion beyond 250 °C causes gel-particle occlusion
    Catheter shaft extrusion100 wt% unfilled or minimum radiopaque loadingBelow 0.10%; 70 °C for 6–12 h210–240 °CMoisture-derived lumen pitting below 0.25 mm wall
    Pneumatic control line100 wt% as supplied; masterbatch ≤4 wt%Below 0.08%; 75 °C for 6 h220–240 °CHigh line speed amplifies melt fracture at die lip
    Injection-molded shell100% compound; regrind ≤30 wt%Below 0.10%; 80 °C for 4–6 h240–270 °CWeld-line strength drops if flow-front temperature falls
    Optical loose tube100 wt% virgin; PA12 masterbatch 2–4 wt%Below 0.10%; 80 °C for 6 h230–250 °CHydrolytic degradation increases temperature-cycled attenuation
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    Certification & Compliance
    More Introduction

    Evonik VESTAMID® LX9012 Bio30 Nylon 12 is a bio-attributed polyamide 12 powder supplied for powder bed fusion additive manufacturing. The Bio30 suffix indicates 30 % bio-attributed or renewable feedstock content assigned through a mass balance accounting path, while the LX9012 base polymer remains an unfilled PA12 laser sintering grade. The product is therefore classified as a bio-based or bio-circular variant of conventional VESTAMID® LX9012, not as a separate polyamide 11 or polyamide 6 grade. Thermal analysis under ISO 11357-3 on powder samples typically shows a melting peak in the 173–178 °C range, and tensile testing on laser-sintered XY specimens per ISO 527-2 returns tensile modulus values from 1450 MPa to 1650 MPa when conditioned at 23 °C and 50 % RH. The same standard yields tensile strength values in the 42–48 MPa range and elongation at break from 15 % to 25 % for unfilled PA12 powder bed fusion parts. Because published mechanical data for this specific Bio30 configuration is limited, these values should be treated as screening ranges rather than guaranteed minimums. Lot-specific certificates of analysis and printed witness coupons are required for production qualification.

    In the manufacturer’s powder bed fusion portfolio, the VESTAMID® LX series includes unfilled and filled laser sintering grades; the 9012 designation references an unfilled PA12 chemistry, and the Bio30 suffix differentiates the feedstock accounting from the petroleum-based grade. The product is supplied as a free-flowing powder with a particle size distribution typical of PA12 laser sintering powders, with D50 values in the 50–60 µm range by laser diffraction per ISO 13320 and a bulk density by ISO 60 in the 0.42–0.47 g/cm³ envelope. No pellet form is supplied; the material is not intended for direct injection molding or single-screw extrusion unless converted by a compounder. This distinction matters in production planning because the quality of laser sintering depends on particle shape, packing density, and recoater behavior, not only on melt viscosity. The Bio30 material should be sieved to 150 µm and blended with virgin powder according to the refresh ratio that is qualified for the specific machine platform.

    What process boundaries emerge when Bio30 enters an existing PA12 powder bed fusion queue?

    In a powder bed fusion system using a 100 W CO₂ laser and 0.12 mm layer thickness, the dominant process conflict is between layer consolidation and dimensional control. If the build chamber surface temperature is maintained below 168 °C, curl deformation increases because the recrystallization shrinkage of PA12 exerts stress at the part edges, and the tensile strength measured under ISO 527-2 can fall below 40 MPa. If the build chamber is raised above 176 °C, partially fused powder attaches to downfacing surfaces, edge definition degrades, and the resulting dimensional error can exceed 0.3 mm on small features. The usable recoat-plane window for unfilled PA12 is therefore not wider than 5–7 °C, and the Bio30 feedstock attribution does not remove this thermal boundary. Published data for this specific configuration is limited; any substitution into an existing qualified PA12 build should begin with a nine-part offset study and a full-build density cube layout to verify that the thermal conditions remain inside the target window.

    Laser energy density should be monitored because the bio-attributed powder may exhibit minor differences in particle shape or packing density. On a typical CO₂ laser powder bed system, an energy density in the 0.03–0.06 J/mm² range is used for unfilled PA12, calculated from laser power divided by scan speed and hatch spacing. Lower energy density produces incomplete melt coalescence and lowers part density by 2–5 %. Higher energy density creates surface growth and yellowing due to thermal degradation of the amide groups. The Bio30 grade should be qualified using a hatch spacing of 0.15–0.25 mm and scan speed from 8–12 m/s, depending on laser power, but these settings must be tuned to the actual beam profile and galvo calibration of the machine. No universal parameter set can be assumed from the petroleum-based LX9012 grade.

    Thermal, moisture, and packing-density boundaries in VESTAMID® LX9012 Bio30

    The unfilled PA12 specification window for powder bed fusion includes a part density of 0.92–0.95 g/cm³ by ISO 1183-2, bulk powder density of 0.42–0.47 g/cm³ by ISO 60, and a particle size D50 between 50 µm and 60 µm. Moisture content before processing should be below 0.1 % by ISO 15512 Karl Fischer titration. If the powder exceeds that value, it should be dried at 80 °C for 12 h under dry air or vacuum. Neglecting this boundary leads to steam bubbles, surface haze on vertical walls, and reduced notched Charpy impact values by ISO 179-1/1eA. The bio-attributed feedstock does not change the amide group density or the equilibrium moisture uptake of the PA12 repeat unit; the saturation moisture content at 23 °C and 50 % RH remains below 0.7 % by mass for the polymer backbone. These properties are not unique to the Bio30 suffix and should be verified by lot-specific certificates.

    Powder recycling is the most important variable for mechanical property retention. Fresher powder yields higher elongation, while heavily recycled powder loses ductility because thermal cycling broadens the molecular weight distribution. In production, a refresh ratio of 40–50 % virgin powder can maintain acceptable elongation for many non-critical parts, but the exact ratio must be validated with tensile bars per ISO 527-2. Published data for the Bio30 specific performance at different refresh ratios is limited. If the used powder is re-dried, sieved, and blended with 50 % virgin material, the tensile strength may be recoverable to within 5 % of all-virgin values, but the elongation at break can still decrease by more than 20 % due to chain degradation. A blend ratio above 50 % used powder is not advisable for load-bearing parts unless the build is approved by mechanical testing.

    Screening propertyTest methodRange for unfilled PA12 powder bed fusion
    Melting peakISO 11357-3173–178 °C
    Tensile modulus, XYISO 527-21450–1650 MPa
    Tensile strength, XYISO 527-242–48 MPa
    Elongation at break, XYISO 527-215–25 %
    Notched Charpy impactISO 179-1/1eA4–6 kJ/m²
    Part densityISO 1183-20.92–0.95 g/cm³
    Bulk powder densityISO 600.42–0.47 g/cm³
    Moisture content before buildISO 15512≤ 0.1 %

    When compared with glass-filled PA12 laser sintering powders, VESTAMID® LX9012 Bio30 is unfilled and therefore has a lower tensile modulus; glass-filled PA12 grades can reach 2500–3500 MPa under ISO 527-2 but generate higher recoater blade wear and require more frequent hopper cleaning. When compared with polyamide 11 powders derived from castor oil, the PA12 Bio30 grade usually has a lower moisture uptake because the PA12 backbone has a lower amide group density than PA11, but the actual equilibrium moisture content must be measured under ISO 62. When compared with PEEK or polypropylene powder bed materials, PA12 Bio30 has a lower continuous use temperature but is processable at standard CO₂ laser powder bed fusion build chamber temperatures of 170–175 °C. The primary difference from conventional VESTAMID® LX9012 is the bio-attributed carbon accounting; the melting peak and laser absorption behavior are not expected to shift beyond normal lot-to-lot variation, but published comparative data for this specific Bio30 configuration is limited. Users should not assume identical tensile isotropy without printing a tensile bar layout in XY, XZ, and ZY orientations.

    The mechanical response of laser-sintered unfilled PA12 is orientation-dependent. Under ISO 527-2, tensile bars printed in the Z direction can show tensile strength 10–15 % lower than XY specimens, and elongation at break can be 30–50 % lower because interlayer adhesion limits deformation. This anisotropy is a function of layer thickness, laser energy density, and build chamber temperature, not the bio-attributed feedstock. A production qualification plan should include tensile bars in XY, XZ, and ZY orientations and should reject parameters if the Z-direction tensile strength falls below 40 MPa in unfilled PA12. Dimensional precision is equally sensitive to the powder bed temperature profile. A temperature gradient across the build platform of more than 3 °C can create warpage at the edges of the build envelope, especially for parts longer than 150 mm. The recoater speed should be reduced to 80–120 mm/s when the used powder fraction exceeds 30 %, and the powder bed should be heated to the setpoint at least 60 min before laser scanning begins. These machine-level checks are more influential than the Bio30 feedstock characteristic, but because published data for this specific configuration is limited, the first production run should not be combined with a new customer application.

    Porosity in laser-sintered PA12 parts is minimized when the applied energy density is sufficient to fully melt the particle cores but not so high as to degrade the polymer. Under ISO 1183-2, part density values in the 0.92–0.95 g/cm³ range are considered typical for unfilled PA12 laser sintering. A density below 0.90 g/cm³ usually indicates incomplete coalescence and is associated with reduced tensile elongation; a density above 0.97 g/cm³ is uncommon for unfilled PA12 unless the part has been infiltrated or compression-molded. Dye penetrant inspection can reveal open porosity, but gas pycnometry is preferred because it gives a closed-cell fraction that is traceable to the density method. The Bio30 suffix does not remove the need for porosity testing in critical fluid-handling parts.

    When regulatory documentation and bio-feedstock traceability are mandatory for production parts

    The bio-attributed feedstock claim is subject to the manufacturer’s mass balance certificate and should be audited against ISO 14040 and ISO 14044 life-cycle assessment boundaries if carbon footprint comparisons are used in procurement. The Bio30 suffix does not by itself establish food-contact status; any application under FDA 21 CFR 177.1500 or EU Regulation 10/2011 must be supported by specific migration testing and a written compliance letter from the supplier. RoHS screening under IEC 62321 for restricted substances is usually below threshold in unfilled PA12, but conformity is not valid without a batch-specific test report. REACH Article 33 obligations apply to the current candidate list at the time of use, not to the Bio30 designation alone. If the part is intended for aerospace or transport interiors, the fire behavior must be tested under FAR 25.853 or ISO 4589-2, because unfilled PA12 is not inherently flame-retardant and may not meet UL 94 V-0 criteria. These boundaries are not altered by the bio-attributed content.

    In production, VESTAMID® LX9012 Bio30 should be handled with stainless steel scoops and containers to avoid cross-contamination with carbon-filled or glass-filled powders. The recoater blade should be inspected after every job for fused bead formation, particularly when the used powder fraction exceeds 30 %. If fused beads larger than 150 µm are present, the powder should be sieved before blending. A nitrogen or dry-air blanket over the feed hopper reduces moisture uptake when ambient relative humidity exceeds 60 % RH; without this, the powder may gain moisture during long builds. The use of anti-static additives is not required if the powder is properly dried and the recoater speed is kept within 80–120 mm/s; however, the addition of any flow aid changes the powder bed packing and must be re-qualified using the same density cube and tensile bar layout.

    To avoid porosity and edge growth, the recoat temperature profile must be qualified first

    Production qualification of VESTAMID® LX9012 Bio30 should begin with a reduced-size build platform containing a 3 × 3 array of density cubes, tensile bars, and wall-thickness coupons. The build chamber surface temperature should be logged at intervals no greater than 15 min during warm-up and scanning. If the temperature at the center and corner of the powder bed differs by more than 3 °C, the build should be stopped and the heater calibration corrected before parameters are accepted. After the build, the coupons should be conditioned at 23 °C and 50 % RH for 24 h before destructive testing. Dimensional compensation factors should be re-established by measuring the as-built dimensions of the density cubes; petroleum-based PA12 values of 1.1–1.4 % in XY may not transfer exactly if the Bio30 powder batch has a different particle shape or bulk density. Tensile testing should be performed consistently; ASTM D638-14 and ISO 527-2 values are not directly comparable due to specimen shape and strain-rate differences. The qualification plan should also include a used-powder build with 40 % recycled material to expose any early ductility loss. If the part is later post-processed by vapor smoothing or dyeing, mechanical testing should be repeated because solvent ingress can reduce notched Charpy impact under ISO 179-1/1eA.

    A documented build log is the only acceptable evidence for production release. The log should include lot number, drying time and temperature, powder moisture content, ambient humidity, recoater speed, build chamber setpoint, laser power, scan speed, hatch spacing, and the measured part density. Without these records, a bio-attributed feedstock claim alone does not establish process capability for a particular part number. Published data for this specific Bio30 configuration is limited, so the production site must generate its own machine-specific capability data before relying on the material for load-bearing serial production.

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