| HS Code | 575352 |
| Density | 1.01 g/cm³ |
| Melting Point | 178 °C |
| Glass Transition Temperature | 37 °C |
| Tensile Modulus | 1500 MPa |
| Yield Stress | 42 MPa |
| Yield Strain | 5% |
| Elongation At Break | >200% |
| Flexural Modulus | 1200 MPa |
| Charpy Notched Impact Strength 23c | no break |
| Shore Hardness D | 55 |
| Water Absorption 24h 23c | 0.2% |
| Melt Volume Rate 230c 2 16kg | 5 cm³/10min |
As an accredited Evonik VESTAMID® Care ME62 Medical Grade Nylon 12 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Evonik VESTAMID Care ME62 is packaged as 25 kg sealed polyethylene bags, double-lined and boxed, ensuring clean, moisture-protected delivery. |
| Container Loading (20′ FCL) | 20′ FCL container loading of Evonik VESTAMID® Care ME62 nylon 12: palletized, secured, full container load ensuring safe transport. |
| Shipping | Evonik VESTAMID® Care ME62 ships in sealed, moisture-proof containers to preserve purity. Store in a cool, dry area away from direct sunlight and extreme heat. Handle with clean, dry equipment to prevent contamination. Transport upright, protected from physical damage, and maintain ambient conditions. Ensure compliance with medical material handling regulations. |
| Storage | Store Evonik VESTAMID® Care ME62 in its original, unopened container in a cool, dry, well-ventilated area away from direct sunlight, heat sources, and moisture. Keep tightly sealed when not in use to prevent humidity absorption and contamination. Avoid exposure to dust, chemicals, or extreme temperatures. Under recommended conditions, shelf life is typically 2 years from delivery. |
| Shelf Life | Shelf life is typically 2 years from manufacture date when stored cool, dry, and in original sealed packaging. |
When VESTAMID® Care ME62 is co-extruded as the outer jacket of a braid-reinforced intravascular catheter shaft, the primary process conflict on L/D 24:1 single-screw extrusion lines is the maintenance of lumen concentricity while a barium sulfate-filled inner layer and an unfilled outer layer converge in a spiral mandrel die. The inner layer for radiopacity is formulated at 15–25 wt% barium sulfate; the outer layer is run without filler. Published data for ME62-specific melt stability at barium sulfate additions above 30 wt% are limited, but production-scale runs on L/D 24:1 extruders with 2.8:1 compression-ratio screws have documented die-lip deposit accumulation after 6–8 h when filler predispersion is not completed before the final melt zone. Concentricity tolerance below ±0.05 mm on a three-axis laser gauge is retained only when the die melt temperature is held within 225 °C ± 5 °C; any upward drift increases outer-layer melt viscosity relative to the inner layer and induces radial migration of the filled layer, a defect that escapes undetected in line-speed trials below 20 m/min but appears during subsequent braid compression. The downstream process includes pre-drying at 80 °C for 8–12 h to a residual moisture content below 0.10 wt%, co-extrusion through a spiral mandrel die with 0.8–1.5 mm annular gaps, vacuum sizing at 20–40 kPa, puller forces below 12 N for sub-1.0 mm lumens, and braid-reinforcement over jacketing with a second PA12 layer or an outer PEBA layer. Device-level compliance is determined under ISO 10555-1:2013 and ISO 11070:2014; material-level biological evaluation follows ISO 10993-1:2018, ISO 10993-5:2009, ISO 10993-10:2010, and ISO 10993-11:2017, with resin test documentation aligned to USP <88> Class VI. Terminal finished devices produced from this frame are diagnostic angiographic catheters, guide catheters, microcatheters, introducer sheaths, and outer shafts for balloon catheter assemblies.
The burst rating of unreinforced ureteral access sheath and intermittent catheter tubing is governed less by dry tensile strength than by residual hoop orientation after vacuum sizing. In this application, VESTAMID® Care ME62 is processed without filler; external plasticizer addition is not required because a high-flexibility medical PA12 base is selected. The formulation addition ratio includes a polyamide-compatible color masterbatch at 1–3 wt% and a processing aid at 0.1–0.3 phr; filler is omitted from the cylindrical shaft to prevent surface striations that become nucleation points for encrustation in contact with synthetic urine. Extrusion is performed on a single-screw extruder with L/D 25:1 and a barrier screw at a die melt temperature of 220–240 °C. The extrudate enters a water-cooled vacuum tank with first-stage vacuum 25–35 kPa; draw ratios above 1.1:1 between puller and extruder screw output have been observed to reduce hoop strength and produce anisotropic shrinkage after aging in synthetic urine according to ISO 20696:2018. Batch-to-batch variance in raw resin moisture above 0.10 wt% is a documented source of pinholes and lumen surface roughness, requiring closed-loop dry-air drying at -40 °C dew point before processing. Compliance is evaluated under ISO 20696:2018 for intermittent urinary catheters, ISO 8669-2:2016 for urine collection bags, and the material-level ISO 10993-1:2018, ISO 10993-5:2009, and ISO 10993-10:2010 suite. Terminal finished product configurations are unisex intermittent catheters, flanged drainage catheters, ureteral access sheaths without inner obturators, and suprapubic catheter extension sections.
A central production constraint in non-invasive ventilation circuits is the corrugator vacuum profile required to prevent rib spring-back while retaining a continuous inner lumen for passing respiratory gases. In this unlabelled but distinct application, VESTAMID® Care ME62 is formulated with a white masterbatch at 2–4 wt% for light shielding and an anti-block silicate at 0.1–0.5 wt% to reduce blocking during coil packaging; no plasticizer and no radiopaque filler are added because the circuit must remain transparent under ISO 5367:2014 visual inspection. The downstream process is continuous corrugation: a L/D 28:1 single-screw extruder delivers melt at 210–230 °C to a vacuum corrugator with mold halves heated to 60–80 °C; vacuum in the corrugator chambers is held at 30–50 kPa, and internal mandrel air pressure is controlled between 0.5 kPa and 1.5 kPa. Dwell time in the corrugator must be sufficient to set the outer ribs below the glass transition of PA12 before cutting; premature release generates non-concentric end cuts and leaks at the 22 mm tapered connectors. Industry compliance routes for this segment include ISO 5367:2014 for breathing tubes, ISO 80601-2-12:2020 for ventilator performance, and ISO 18562-1:2017 for volatile organic compound release from gas pathway components; biological evaluation follows ISO 10993-1:2018 and ISO 10993-10:2010. Terminal finished products are ventilator circuit tubing, CPAP conduits, oxygen supply extensions with tapered fittings, humidifier feed tubes, and coaxial anesthesia breathing sets.
Injection molding of VESTAMID® Care ME62 into surgical handpiece components creates a narrow processing window because the material’s melt viscosity is lower than unmodified PA12 and the molded part must retain dimensional stability after repeated exposure to hospital-grade detergents. The formulation addition ratio for this segment is unfilled neat resin with a mold-release masterbatch at 0.2–0.5 wt% and a color masterbatch at 1–3 wt%; glass-fiber reinforcement is deliberately not used because the resulting modulus increase exceeds the overmolded living hinge requirements. Downstream production involves a three-zone screw injection molding machine with L/D 20:1, barrel temperatures 220–250 °C, mold temperatures 40–60 °C, injection pressures 70–120 MPa, hold pressures 50–70% of injection pressure, and back pressure 5–10 MPa. When overmolding onto stainless steel inserts, insert preheating to 100–120 °C is necessary to prevent premature skin solidification and delamination along the metal-polymer interface; untreated stainless steel with residual machining oil produces visible knit lines at gate locations and reduces pull-out strength by over 30% in internal break-loose tests. Compliance requirements are defined by ISO 13485:2016, IEC 60601-1:2005 for active medical devices, USP <88> Class VI, and biological evaluation under ISO 10993-5:2009 and ISO 10993-10:2010. Terminal finished product types include endoscopic handle body shells, arthroscopic shaver housings, ultrasonic surgical handpiece clamshells, and bipolar forceps insulation sleeves.
Gamma exposure at 25 kGy changes the post-molding dimensional stability of PA12 components by annealing then gradually embrittling the semicrystalline phase; therefore drug delivery device housings using VESTAMID® Care ME62 are processed with conservative antioxidant and lubricant loadings to avoid runaway oxidation during routine sterilization validation. The formulation addition ratio for this segment is neat resin with a high-purity lubricant at 0.2–0.5 wt% and a color masterbatch at 0.5–1.5 wt%; talc and calcium carbonate are excluded because their extractable ion burden may interfere with drug-stability testing. The downstream production sequence is multi-cavity hot-runner injection molding with melt temperature 220–250 °C, mold temperature 50 °C, fill time 0.8–2.5 s, and packing decay from 60 MPa to 20 MPa over 3–5 s. After molding, housing halves are ultrasonically welded at 20 kHz with amplitude 20–30 µm; weld strength below 85% of the nominal wall tensile strength is rejected during production lot auditing. Regulatory compliance is anchored to ISO 11608-1:2022 for pen injection systems, ISO 10993-4:2017 for hemocompatibility where accidental blood contact occurs, ISO 10993-5:2009, ISO 10993-10:2010, and USP <88> Class VI; ISO 13485:2016 governs supplier and OEM quality system interfaces. Terminal finished products are insulin pen chassis components, dry powder inhaler actuator bases, intranasal spray pump collars, and housings for needle-free injection devices. Published data for VESTAMID® Care ME62 exposure above 40 kGy are limited; repeated sterilization cycles at 25 kGy should be validated per device-specific risk assessment rather than assumed from unfilled PA12 literature.
The following compliance matrix consolidates the standard designations by downstream segment for supplier documentation and device-level technical file construction.
| Downstream segment | Device-level standards | Material-level standards |
|---|---|---|
| Intravascular catheter shafts | ISO 10555-1:2013; ISO 11070:2014 | ISO 10993-5:2009; ISO 10993-10:2010; ISO 10993-11:2017; USP <88> Class VI |
| Ureteral access sheath and intermittent catheter tubing | ISO 20696:2018; ISO 8669-2:2016 | ISO 10993-1:2018; ISO 10993-5:2009; ISO 10993-10:2010 |
| Non-invasive ventilation and oxygen circuit tubing | ISO 5367:2014; ISO 80601-2-12:2020; ISO 18562-1:2017 | ISO 10993-1:2018; ISO 10993-10:2010 |
| Surgical instrument handles and insulation | ISO 13485:2016; IEC 60601-1:2005 | ISO 10993-5:2009; ISO 10993-10:2010; USP <88> Class VI |
| Drug delivery device housings | ISO 11608-1:2022; ISO 13485:2016 | ISO 10993-4:2017; ISO 10993-5:2009; ISO 10993-10:2010; USP <88> Class VI |
| In vitro diagnostic fluidic manifolds | ISO 13485:2016; RoHS Directive 2011/65/EU | ISO 10993-18:2020; ISO 10993-5:2009 |
Microfluidic manifold tooling for in vitro diagnostic instruments presents a different set of boundary conditions because the PA12 part is exposed to reagent residuals, alkaline cleaning agents, and repeated thermal cycling between 4 °C and 60 °C. In this application, VESTAMID® Care ME62 is used as a neat resin with carbon black masterbatch at 0.5–2 wt% for opaque light-sensitive reagent areas and a process lubricant at 0.1–0.2 wt%; no mineral filler is introduced because ion-leachable calcium carbonate would drift the electrochemical noise floor of on-board sensors. The downstream process is injection molding with valve-gated hot runners; melt temperature is held at 220–240 °C, mold temperature at 50–70 °C, injection velocity 50–100 mm/s, and hot-runner manifold temperature not exceeding 260 °C to prevent gate-vestige plateout observed on prototype tools after 50,000 cycles. Compliance is evaluated through ISO 13485:2016, ISO 10993-1:2018, ISO 10993-5:2009, ISO 10993-10:2010, and ISO 10993-18:2020 for chemical characterization of leachables; restriction of hazardous substances is documented under RoHS Directive 2011/65/EU and REACH Article 33. Terminal finished products are IVD manifold cassettes, reagent reservoir closures, on-board fluid routing blocks, and analyzer fluidic connector bodies. Long-term compatibility with high-ionic-strength buffers and sodium hypochlorite at 1,000 ppm available chlorine requires device-specific validation because published data for this precise configuration are limited.
Competitive Evonik VESTAMID® Care ME62 Medical Grade Nylon 12 prices that fit your budget—flexible terms and customized quotes for every order.
For samples, pricing, or more information, please contact us at +8615365186327 or mail to admin@ascent-chem.com.
We will respond to you as soon as possible.
Tel: +8615365186327
Email: admin@ascent-chem.com
Flexible payment, competitive price, premium service - Inquire now!
Evonik VESTAMID® Care ME62 is a medical-grade nylon 12-based thermoplastic elastomer supplied as pellets for extrusion and injection moulding of catheter shafts, multi-lumen tubing, luer fittings, and respiratory components. The grade has a nominal Shore D hardness of 62 measured according to ISO 868 and a density of 1.01 g/cm³ measured according to ISO 1183-1. The material must be dried to a residual moisture content no greater than 0.10% by ISO 15512 before melt processing. At 23 °C and 50% RH, the equilibrium moisture uptake is approximately 1.2% by ISO 62; this value is lower than that of PA6 or PA66 and contributes to dimensional stability in humid clinical environments. The polymer architecture consists of polyamide 12 hard segments and polyether soft segments, which provides flexibility without ortho-phthalate plasticizers.
The resin is used when unplasticized polyamide 12 is too stiff for thin-wall bending applications. The flexible grade retains a nylon 12 backbone, so its moisture absorption and chemical resistance profile differ from plasticized PVC. Unlike PVC, ME62 does not contain ortho-phthalate or citrate plasticizers; therefore, loss of flexibility through plasticizer migration into lipid-rich fluids is not the dominant failure mode. However, the polyether segment is susceptible to thermal oxidative degradation above 260 °C, so the processing window is narrower than that of unplasticized polyamide 12 or PVC. This limitation is an operational boundary, not a comparative defect.
Chemical characterisation for medical devices typically follows ISO 10993-18. The supplier documentation may include a qualitative list of monomers, oligomers, processing aids, and residual solvents, but published extractables data for finished-device configurations is limited. Because the backbone is based on nylon 12, residual monomer chemistry is dominated by laurolactam rather than ε-caprolactam; the medical-grade specification controls residual monomer concentration. Analytical screening should include response factors for oligomeric amides and polyether-derived degradation products. The absence of plasticizers reduces the number of extractable species relative to plasticized PVC, but the detector must be validated for low-molecular-weight polyamide oligomers.
General-purpose polyamide 12 grades are typically rigid, with tensile modulus in the range of 1,200 MPa to 1,500 MPa by ISO 527-1/-2, whereas ME62 is reported at approximately 210 MPa in dry-as-moulded specimens. Elongation at break is reported at >300% by ISO 527-2, compared with 50% to 200% for many unplasticized PA12 extrusion grades. The Shore D hardness of 62 places ME62 between rigid PA12 tubing and very soft polyether block amide grades. Relative to plasticized PVC, the absence of low-molecular-weight plasticizers changes the extractables profile; the relevant extractables are low-molecular-weight polyamide oligomers and processing aids. The nylon 12 backbone also provides lower water absorption than PA6 or PA66, which reduces swell-induced lumen reduction in humid storage.
Table 1 lists supplier-reported typical values used for initial material selection. Design calculations for body-contact devices should use conditioned rather than dry-as-moulded values because equilibrated moisture reduces modulus. Published data for dynamic multiaxial fatigue at body temperature is limited; device-specific testing is required.
| Property | Measurement Condition | Value | Test Method |
|---|---|---|---|
| Shore hardness | 15 s, 23 °C | 62 D | ISO 868 |
| Density | 23 °C | 1.01 g/cm³ | ISO 1183-1 |
| Tensile modulus | dry as moulded, 23 °C | 210 MPa | ISO 527-1/-2 |
| Elongation at break | dry as moulded, 23 °C | >300% | ISO 527-2 |
| Melting temperature | second heating, 10 K/min | 172 °C | ISO 11357-3 |
| Equilibrium moisture uptake | 23 °C, 50% RH | 1.2% | ISO 62 |
For process development, the following production-scale windows are used for tube extrusion and injection moulding. Drying must be performed in a desiccant dryer, not a hot-air hopper dryer, because the moisture specification is ≤0.10%. At dew points above -30 °C, drying time must be extended or the material will hydrolyse during melting. Table 2 summarizes the recommended processing envelope.
| Parameter | Extrusion | Injection Moulding |
|---|---|---|
| Drying temperature | 80 °C | |
| Drying time | 4 h to 6 h | |
| Dew point | ≤ -30 °C | |
| Melt temperature | 210 °C to 250 °C | 230 °C to 270 °C |
| Mould temperature | — | 20 °C to 60 °C |
| Screw L/D ratio | 24:1 to 30:1 | General-purpose screw |
On a 30 mm single-screw extruder with a 30:1 L/D barrier screw, melt-temperature overshoot above 260 °C is observed as surface roughness and a reduction in melt strength. Screw speed is typically limited to 40 rpm to 80 rpm for tubes with outer diameter below 2.0 mm. If torque fluctuates by more than 15% of setpoint, the cause is usually feed bridging or incomplete drying; sustained operation under such conditions produces gel particles in the tube wall. Multi-cavity connector tools with projected area above 200 cm² require mold-filling simulation because the material solidifies quickly in thin gate regions. Published data for all specific tool geometries is limited; processing windows should be validated on the actual production line.
Melt rheology is non-Newtonian and shear-thinning, typical of polyamide 12-based block copolymers. Capillary rheometry to ISO 11443 at 230 °C is recommended for injection pressure mapping. In multi-cavity tools, tapered runners below 1.5 mm diameter can produce premature freeze-off before gate sealing is complete. Short-shot studies are therefore required before production release. Because the polyether segment contributes to melt elasticity, high-shear mixing sections are generally avoided; they generate viscous dissipation and increase the risk of local overheating.
In multi-layer catheter coextrusion, the interfacial melt temperature between ME62 and a tie layer must remain below 260 °C to limit polyether segment scission. An overshoot of 10 °C above the setpoint in the metering zone can reduce melt strength and produce wall-thickness variation in tubes with wall thickness below 0.25 mm. The defect appears as periodic lumen eccentricity and can be detected by ultrasonic wall measurement systems. The corrective action is to reduce screw speed, increase barrel cooling in the compression zone, or use a reverse temperature profile on 25 mm to 35 mm extruders. Residence time in the die adapter should not exceed 10 min; stagnant melt zones contribute to gel formation and black speck contamination.
For thin-wall tubing, vacuum calibration with vacuum pressure of 0.4 bar to 0.8 bar and cooling water temperature of 10 °C to 30 °C is used. Higher vacuum pressure can cause stick-slip marks; lower vacuum can produce lumen collapse. These parameters are equipment-specific and depend on die land length and cooling tank length. The PA12 backbone permits high melt elasticity, but the polyether phase limits the maximum draw-down ratio.
ME62 is not supplied sterile. Ethylene oxide sterilization at 55 °C and 60% RH is generally compatible, but aeration must be validated to meet residual limits under ISO 10993-7. Gamma irradiation at typical doses of 25 kGy to 50 kGy may reduce elongation at break in the polyether phase; post-irradiation tensile testing to ISO 527-2 on finished tubing is required because dose rate and oxygen exposure affect degradation kinetics. Steam sterilization at 134 °C is not recommended for repeated cycles because the nylon 12 hard segments hydrolyse. If steam is unavoidable, a single cycle at 121 °C must be validated for dimensional and mechanical stability.
Extractables screening should follow ISO 10993-12 using polar and nonpolar solvents. Because the grade is plasticizer-free, the extractables profile is not dominated by plasticizer migration; it is shifted toward low-molecular-weight polyamide oligomers and processing aids. The manufacturer supplies change-control documentation and biological evaluation summaries; however, final biocompatibility is the responsibility of the device manufacturer according to ISO 10993-1:2018. For blood-contacting applications, haemocompatibility testing according to ISO 10993-4 is required unless the supplier can provide device-specific data. Not suitable for long-term implantable applications exceeding 30 days without complete biological safety evaluation.
In urological drainage and respiratory tubing applications, ME62 is processed at wall thicknesses between 0.20 mm and 0.30 mm. The material resists kinking when bent to small radii; however, published data for kink radius as a function of Shore D hardness is limited. Device-specific kink testing should be conducted under the applicable standard for the finished device. Multi-layer catheter shafts may combine ME62 with polyamide 12 or polyethylene tie layers; interfacial adhesion must be tested on production-run samples because layer viscosity ratio and melt temperature influence peel performance. Incompatible fluid contact with concentrated mineral acids, strong oxidising agents, or polar solvents should be avoided because the polyamide segments are attacked by these media.