`VESTAMID CW1688 Bio30` in fuel vapor management begins with a material qualification that is dominated not by tensile strength but by zinc chloride (ZnCl₂) stress-cracking resistance under hood-level peak temperatures of **120°C**. In a co-extruded three-layer construction complying with **SAE J2045**, the outer shell at a wall thickness of **0.25–0.40 mm** must retain hoop stress integrity during thermal cycling from **-40°C** to **120°C** while simultaneously resisting the chloride salt slurry that accumulates on underbody routing brackets. The **8%** by weight glass fiber loading raises the conditioned tensile modulus to approximately **2.8–3.5 GPa** ( **ISO 527-1/-2** ), a **40–60%** increase over unfilled PA12, which directly allows downsizing the outer shell without exceeding the maximum permissible permeation flux of **15 mg/m²/day** for hydrocarbon vapor at **60°C**. Melt temperature should be maintained at **240°C–250°C** at the adapter zone when running multi-layer tubing dies with an EVOH barrier layer; excursions above **255°C** produce oxidative degradation of the barrier copolymer, while temperatures below **235°C** generate melt fracture at the die land due to the increased shear viscosity of the glass-filled compound. The bio-based organic fraction of **30%** ( **ISO 16620-1** ) does not alter the amide backbone chemistry, and therefore does not modify the established PA12 ZnCl₂ resistance that distinguishes this polymer from PA6 and PA66 in underhood automotive service.Injection-molded quick connectors for fuel vapor lines per **SAE J2044** demand a different set of processing controls. Gate placement must orient glass fibers circumferentially around the barb retention groove, because a weld line intersecting the groove at a **90°** angle reduces burst retention force by **15–25%** relative to a solid, weld-line-free molding. Mold temperature below **50°C** produces a frozen skin layer of **0.10–0.20 mm** that interrupts fiber continuity at the surface and creates a plane of weakness when connectors are subjected to assembly insertion and extraction forces. A preferred mold temperature of **60–80°C** promotes surface crystallinity sufficient to resist the abrasive action of steel connector barbs during the **10–15 N** insertion force typical of **8 mm** OD fittings. Pre-drying is mandatory: the compound must be dried at **80°C** for **4–6 hours** in a desiccant dryer producing a dew point no higher than **-35°C**, until residual moisture measured by Karl Fischer titration ( **ASTM D6869** ) falls below **0.10 wt%**. Processors operating at relative humidity above **60%** without a sealed hopper system will observe surface splay on molded connectors and internal voiding in extruded tubing shells, both attributable to steam generation from hydrolyzed polymer chain ends during plastication.
Does 8% Glass Loading Shift Burst Pressure Behavior in Pneumatic Control Lines?
The short-term burst pressure of **8 mm × 1 mm** pneumatic tubing extruded from this compound is approximately **20–30%** higher at **23°C** than unfilled PA12 of identical SDR, a direct consequence of the increased hoop stress capacity provided by the oriented glass fiber reinforcement. However, the magnitude of this benefit narrows significantly as operating temperature approaches the PA12 glass transition region of **45–55°C**; at **60°C** continuous operation, the matrix softens and load transfer to the fiber phase becomes less effective, reducing the burst advantage to **10–15%** over unfilled polymer. Cyclic impulse testing per **ISO 6803** at **0–10 bar** square-wave pressure, **1 Hz** frequency, for a minimum of **10⁶ cycles** should form the qualification basis for any pneumatic control circuit, because the dynamic fatigue behavior of the glass-filled compound diverges from static burst predictions when fiber-matrix debonding accumulates at the fiber ends. Published data for VESTAMID CW1688 Bio30 specifically under **ISO 6803** flexural fatigue conditions at **60°C** is limited; qualification programs should therefore include supplementary test coupons machined from extruded tube segments rather than relying solely on molded specimen data generated at room temperature.Extrusion of pneumatic control tubing from the compound requires a single-screw extruder with a minimum **L/D 24:1** configuration, a barrier screw geometry with a chrome-plated or bimetallic barrel, and a screen pack of **80/120/80 mesh** to remove unmelted polymer agglomerates that otherwise produce pinhole leak paths under **10 bar** service pressure. Barrel temperature zones should be set at **215°C** (feed), **225°C** (compression), **235°C** (metering), and **240°C** (die head), with a melt temperature target of **235–245°C**. Screw speed should be limited to **40–60 rpm** for **30 mm** screw diameters to control shear heating, which can push local melt temperatures above **260°C** and initiate chain scission at the glass fiber interface. Minimum bend radius specification for **8 mm** OD tubing from the compound at **23°C** is **3× OD**; this increases to **5× OD** at **-20°C**, reflecting the reduced cold flexibility inherent to glass reinforcement compared to unfilled VESTAMID L2140, though the PA12 backbone retains sufficient toughness for robotic arm festoon routing through continuously articulating cable carriers.
Processing Parameter Ranges for VESTAMID CW1688 Bio30 (8% GF PA12)| Parameter | Injection Molding | Single-Screw Extrusion |
|---|
| Barrel temperature, feed zone | 220–230°C | 210–220°C |
| Barrel temperature, compression zone | 230–240°C | 220–230°C |
| Barrel temperature, metering zone | 240–255°C | 230–240°C |
| Nozzle / adapter temperature | 250–260°C | 235–245°C |
| Mold temperature / calibrator temperature | 60–80°C | 30–50°C |
| Residual moisture before processing | < 0.10 wt% | < 0.10 wt% |
| Dew point of drying system | ≤ -35°C | ≤ -35°C |
| Maximum recommended screw speed | 80–120 rpm (30 mm) | 40–60 rpm (30 mm) |
Cable Sheathing for Subsea Hydraulic Umbilical Systems — Chemical Aging and Crush Resistance
Subsea umbilical cables employed in offshore production per **API 17E** and **ISO 13628-5** impose a combination of radial crush load, chemical exposure to methanol and glycol-based hydrate inhibitors, and sustained hydrolysis at water depths where conductor temperatures can exceed **70°C**. The **8%** glass loading in VESTAMID CW1688 Bio30 increases short-term radial crush strength by approximately **1.5–2.0×** relative to unfilled PA12 when measured by opposing-plate compression testing per **ASTM D2412** on **25.4 mm** OD tube with **2.0 mm** wall thickness. This crush resistance becomes critical during umbilical deployment and recovery operations, where multiple layers of sheathed conductors are wound under tension onto installation vessel reels, generating inter-layer contact pressures that plastically deform unreinforced polyamide sheathing and compromise the underlying electrical insulation. The glass fiber phase does not, however, improve longitudinal flexibility during minimum-bend-radius bending at **-40°C**, and the addition of fiber reinforcement should not be interpreted as a substitute for proper lay-length design of the helical conductor bundle.Chemical aging research on PA12 sheathing materials consistently demonstrates superior resistance to methanol and ethylene glycol compared to PA6 and PA66, attributable to the lower amide group density in the repeating unit — one amide linkage per **12** methylene units versus one per **6** in PA6 and PA66. Prolonged immersion in **99.9%** methanol at **50°C** for **1000 hours** typically produces a **30–50%** reduction in elongation at break in glass-filled PA12 compounds, while PA6-based sheath materials can lose **70–90%** of their original elongation under identical test conditions ( **ISO 175** immersion protocol with tensile testing per **ISO 527** ). The bio-based carbon fraction of **30%** in CW1688 Bio30 does not introduce additional hydrolytic degradation pathways, as the synthesized amide backbone is chemically identical to petrochemical-derived PA12. Published data for the specific behavior of CW1688 Bio30 in high-pressure methanol vapor at temperatures above **80°C** is limited, and qualification for subsea service should include supplementary testing in simulated hydrate inhibitor formulations at the design conductor temperature.Thermal oxidative aging in G12+/G13 ethylene glycol–water mixtures at continuous temperatures of **105–115°C** subjects injection-molded coolant manifold components to hydrolysis, mineral deposition, and dimensional instability from asymmetric thermal expansion. The PA12 backbone exhibits intrinsic hydrolysis resistance superior to PA6 and PA66 because the lower amide density reduces the number of water-accessible scission sites; this becomes measurable in coolant aging studies as retention of **70–85%** of initial tensile strength after **1000 hours** at **110°C** in **50:50** glycol-water ( **ISO 175** / **ISO 527** ), whereas PA66 compounds typically retain **50–65%** under identical conditions. The **8%** glass loading further improves dimensional stability by reducing the coefficient of linear thermal expansion from approximately **120–150 × 10⁻⁶ K⁻¹** in unfilled PA12 to **80–100 × 10⁻⁶ K⁻¹** parallel to flow direction and **120–150 × 10⁻⁶ K⁻¹** transverse to flow, producing a more isotropic expansion profile that minimizes warpage in asymmetric manifold geometries with wall thickness variations from **2.5 mm** to **6.0 mm**. Mold temperature selection directly governs the crystallinity level achieved: at **40°C** mold temperature, the crystalline fraction measured by differential scanning calorimetry at **10 K/min** heating rate ( **ISO 11357-3** ) typically reaches **35–40%**, while at **80°C** mold temperature the crystalline fraction increases to **45–50%**, enhancing chemical resistance and reducing creep under sustained clamping loads from mounting brackets.Coolant thermostat housings molded from the compound require particular attention to weld line integrity in multi-cavity tooling. Glass fibers oriented parallel to a weld interface produce a strength reduction of **15–25%** relative to woven or cross-fiber orientation, and this defect becomes nucleation sites for stress cracking when combined with hot glycol immersion. Sequential valve gating or melt flipping techniques should be incorporated wherever a weld line must intersect a pressure boundary surface. The bio-based monomer fraction does not modify the thermal degradation kinetics of the polymer in oxygen-rich coolant environments; oxidative induction time testing per **ISO 11357-6** on the compounded material indicates that stabilizer package selection, not feedstock origin, controls the onset of carbonyl index increase during long-term glycol immersion.
Reusable Diagnostic Housing Structures Survive 50 kGy Gamma Sterilization Without Embrittlement
Point-of-care diagnostic equipment housings and reusable laboratory automation chassis present a specific materials selection problem: the polymer must retain sufficient toughness after repeated gamma sterilization cycles while resisting dimensional drift in ambient laboratory humidity that fluctuates between **20%** and **80%** RH. PA12 absorbs approximately **0.6–0.7%** moisture at equilibrium in **23°C/50% RH** conditions ( **ISO 62** ), compared to **2.5–3.0%** for PA6 and **1.8–2.2%** for PA66. This reduced water affinity translates directly into retention of flexural modulus and dimensional stability in non-climate-controlled storage areas where diagnostic platforms may be staged for extended periods. The **8%** glass loading further reduces equilibrium moisture uptake by diluting the polymer phase and creates a stiffer load-bearing structure for cantilevered reagent drawer slides and automated pipetting arm mounts, where deflection under **20–50 N** static load must remain below **0.5 mm** over a **350 mm** span. Biocompatibility evaluation per **ISO 10993-1** must be completed on the finished component; the compound's bio-based carbon feedstock does not automatically confer medical-grade status, and no claim of **ISO 10993-5** (cytotoxicity) or **ISO 10993-10** (irritation) compliance should be made without lot-specific testing of molded housings at the finished device level.Gamma sterilization at a single **50 kGy** dose typically reduces elongation at break in glass-reinforced PA12 compounds by **10–20%** relative to unsterilized controls, reflecting chain scission events in the amorphous phase. Repeated **50 kGy** cycles produce cumulative damage that accelerates beyond linear extrapolation; design margin should limit cumulative absorbed dose to **100 kGy** unless post-sterilization mechanical testing confirms retention of the device's specified **5%** minimum elongation. Ethylene oxide sterilization at **55°C** with a **9–12 hour** exposure cycle imposes negligible mechanical property reduction on PA12 when residual moisture is maintained below **0.10 wt%** before gassing, as the low moisture absorption of the polymer minimizes retained ethylene oxide and ethylene chlorohydrin residuals that otherwise require aeration periods exceeding **72 hours** in higher-absorbing polyamides. Electron beam sterilization at **35–45 kGy** demonstrates similar property retention but requires careful consideration of the radiation-induced yellowing response in the stabilizer package, which shifts the color from natural to pale amber without affecting dimensional performance.
When Compressed Air Distribution Pipe Replaces Galvanized Steel in Manufacturing Plants
The long-term hydrostatic strength of PA12 pipe in compressed air distribution networks operating at **10–16 bar** must be evaluated against **ISO 1167** regression curves with extrapolation to the **50-year** design life mandated by plant engineering codes. Glass-fiber reinforcement at **8%** loading increases the short-term hoop stress at burst by approximately **25–35%** compared to unfilled PA12 of identical SDR, but the long-term creep rupture curve exhibits a steeper negative slope at operating temperatures above **60°C** because hydrolytic degradation at the glass-matrix interface reduces the effective load-bearing cross-section over time. Published **ISO 1167** regression data for CW1688 Bio30 specifically at **80°C** and beyond **10,000 hours** test duration is limited; extrapolation of design stress values for continuous compressed air service at elevated temperature should not proceed without supplementary creep testing conducted on pipe sections of the exact wall thickness and joining configuration used in the installation. For plants with sustained air temperatures below **50°C**, the compound provides a viable alternative to galvanized steel without the internal corrosion that generates particulate contamination in the air stream, which would otherwise require filtration to **ISO 8573-1** class 1 particle purity.Joint integrity in compressed air pipe networks relies on mechanical compression fittings rather than solvent cementing or fusion welding for this compound, and the glass fiber reinforcement increases the hoop stiffness that resists fitting blow-off at elevated temperature. Every joint must be qualified by pneumatic burst testing to **3.2×** rated working pressure per the fitting manufacturer's protocol, typically **51.2 bar** for a **16 bar** system. Ultraviolet resistance of PA12 sheathing and pipe exposed to daylight through building roof lights requires the addition of a carbon black UV-stabilized masterbatch during compounding; standard natural-grade material without adequate UV absorber will show surface chalking and embrittlement after **12–24 months** of direct sunlight exposure. The bio-based fraction does not modify UV degradation kinetics, and outdoor installation specification must therefore rely on stabilizer package verification via accelerated weathering per **ISO 4892-2** (xenon arc) with acceptance criteria of **≥70%** retention of tensile strength after **2000 hours** exposure.
Chemical Resistance and Compliance Checklist for VESTAMID CW1688 Bio30| Exposure Medium | Test Condition | Acceptance Metric | Reference Standard |
|---|
| Zinc chloride (road salt concentrate) | Immersion, 50 wt% ZnCl₂, 23°C, 500 h | No surface cracking at 10× magnification | SAE J2260 |
| Gasoline, ASTM Fuel C | Immersion, 23°C, 1000 h | ≥ 80% tensile strength retention | ISO 175 / ISO 527 |
| Diesel fuel, EN 590 | Immersion, 60°C, 1000 h | ≥ 70% tensile strength retention | ISO 175 / ISO 527 |
| Ethylene glycol 50:50 mixture | Immersion, 110°C, 1000 h | ≥ 70% tensile strength retention | ISO 175 / ISO 527 |
| Methanol, 99.9% | Immersion, 50°C, 1000 h | ≥ 50% elongation retention | ISO 175 / ISO 527 |
| Gamma irradiation (single dose) | 50 kGy, Cobalt-60 source | ≥ 80% elongation retention | ISO 11137 |
| Bio-based carbon content | Accelerator mass spectrometry | 30% biobased carbon | ISO 16620-1 / ASTM D6866 |
Inline skate frame rails, ski touring binding toe/heel components, and cycling cleat retention plates constitute a low-temperature impact application class where the glass-fiber loading in VESTAMID CW1688 Bio30 must balance stiffness gains against the embrittlement risk introduced by the reinforcement. At **8%** by weight loading, the Charpy notched impact strength at **-20°C** measured per **ISO 179-1/1eA** typically falls within **5–8 kJ/m²** for dry-as-molded specimens, which is sufficient for dynamic loading in boot-binding interfaces where peak impact forces during landings can reach **2–4 kN**. The PA12 glass transition temperature of approximately **45–55°C** ensures that the amorphous phase retains ductile molecular mobility at temperatures far below freezing, a property that distinguishes this polymer from PA6 and PA66 compounds that exhibit a pronounced ductile-to-brittle transition between **0°C** and **-10°C**. Published data for CW1688 Bio30 specifically under multi-axial impact at **-40°C** is limited; qualification test programs for ski-binding applications should include instrumented puncture testing per **ISO 6603-2** at the design minimum service temperature, with acceptance based on total energy absorption rather than peak force measurement.Void content in injection-molded sports equipment components must be maintained below **0.5%** by volume, as measured by density comparison per **ISO 1183** between the molded part and a fully consolidated compression-molded plaque of the same compound. Voids initiate preferentially at glass fiber ends and serve as crack nucleation sites under repeated low-temperature flexural loading in skate frame webs where clamping forces from axle bolts produce local compressive stresses above **40 MPa**. The **30%** bio-based carbon content does not compromise low-temperature toughness relative to petrochemical PA12, because the crystalline morphology — which governs the ductile-brittle transition — is controlled by processing conditions rather than monomer source. Mold temperature should be maintained at **60–80°C** with injection speeds that produce a fill time of **1.5–3.0 seconds** for wall sections of **3–6 mm**, avoiding the excessive shear that degrades fiber length below the critical aspect ratio of approximately **20:1** required for effective stress transfer in the frozen state.
Competitive Evonik VESTAMID CW1688 Bio30 Nylon 12, 8% Glass Fiber Reinforced 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
VESTAMID CW1688 Bio30 is a polyamide 12 injection-moulding and extrusion compound reinforced with 8% glass fibre by weight. The base polymer is nylon 12, designated PA12 under ISO 1043, and the Bio30 suffix identifies a renewable carbon content of 30% when assessed by ASTM D6866-21 or ISO 16620-2. The renewable carbon claim refers to the polymer fraction and does not imply biodegradability or compostability. Because the glass fibre loading is 8% by weight rather than volume, the filled density and melt viscosity differ from unfilled PA12 and from higher-fibre PA12 compounds. The material is specified for technical parts in which moisture uptake, chemical resistance, and dimensionally stable fibre reinforcement are required alongside a measurable bio-based carbon fraction.
The ISO 1043 designation for the compound is PA12-GF8, with GF indicating glass fibre and 8 denoting the nominal fibre weight percentage. Grade-specific datasheet values for VESTAMID CW1688 Bio30 are not reproduced here; comparative data from the same PA12 glass-fibre class are therefore used in the table below and should be validated against the current Evonik technical datasheet.
What Property Changes Are Introduced by an 8% Glass Fibre Weight Fraction?
Addition of short glass fibres at 8% by weight to a polyamide 12 matrix raises tensile modulus relative to unfilled PA12 by approximately 30–50%, depending on fibre length distribution, coupling agent chemistry, and fibre orientation after mould filling. Tensile test specimens are evaluated according to ISO 527-2; a 1 mm/min crosshead speed is used for modulus determination and 5 mm/min for strength and elongation after yield. The glass fibre reduces mould shrinkage and post-mould hygroscopic growth. Shrinkage anisotropy between flow direction and transverse direction becomes measurable at fibre loadings as low as 8%, and tooling must compensate for the lower shrinkage in the flow direction. Because polyamide 12 has lower equilibrium water absorption than PA6 or PA66 when measured to ISO 62, the reinforced compound retains a relatively small thickness growth in humid environments, but the fibre network further restrains resin swelling along the fibre axis. For structural components, finite-element material models should use a transversely isotropic stiffness matrix rather than an isotropic modulus, because fibre orientation produces a modulus in the flow direction that can be 1.5–2.0 times higher than the transverse direction in thin-wall sections.
Class-typical comparative values for unfilled PA12 and an 8% glass-fibre reinforced PA12 class; not lot-specific Evonik datasheet values
| Property | Test method | Unfilled PA12 | 8% glass-filled PA12 class |
| Density | ISO 1183-1 | 1.01–1.03 g/cm³ | 1.06–1.11 g/cm³ |
| Tensile modulus | ISO 527-2 | 1400–1600 MPa | 1800–2400 MPa |
| Tensile strength | ISO 527-2 | 45–50 MPa | 50–65 MPa |
| Tensile elongation at break | ISO 527-2 | >200% | 10–30% |
| Notched Charpy impact, 23 °C | ISO 179-1/1eA | 5–12 kJ/m² | 8–20 kJ/m² |
| Heat deflection temperature, 0.45 MPa | ISO 75-2/B | 130–150 °C | 150–170 °C |
The tabulated values are class-typical for an 8% glass-fibre reinforced PA12 and are not lot-specific for VESTAMID CW1688 Bio30. Where an application requires exact design allowables, the current Evonik technical datasheet and a statistically derived dataset from at least three production lots are required. Fibre content in incoming material should be checked by ash content according to ISO 3451-1, with a tolerance of ±1% around the nominal 8% by weight. Density and tensile modulus are useful incoming indicators because both shift immediately if the fibre fraction is off-target.
Notched impact response at 8% fibre content is not uniformly higher than unfilled PA12. In dry-as-moulded specimens, the fracture path is altered by fibre ends, and weld-line regions can show tensile strength reductions of 40–70% relative to uninterrupted flow. Sharp radii below 1.0 mm increase notch sensitivity in glass-filled polyamides; field failures in snap-fit arms and housing clips are typically initiated at knit lines or gate vestiges. For multi-gated parts, sequential valve-gate filling reduces the number of weld lines, but the fibre orientation around the gate remains highly anisotropic. Mould-filling simulation should include fibre orientation tensor data, because isotropic mechanical assumptions can overpredict transverse strength by 30% or more.
Drying, Screw Plastication, and Barrel-Residence Constraints
Polyamide 12 compounds are hygroscopic enough to require pre-drying before melt processing. For an 8% glass-fibre reinforced PA12, desiccant drying at 80 °C for 4–6 h reduces moisture to below 0.10% by weight; a maximum residual moisture limit of 0.15% is recommended because higher moisture promotes hydrolytic chain scission and surface silver streaks. Drying air dew point should be maintained below -30 °C. The barrel profile is commonly set between 230 °C and 260 °C, with the nozzle between 250 °C and 280 °C. If residence time exceeds 10 min above 280 °C, thermal degradation of polyamide 12 can generate colour shift and loss of impact. Mould temperatures of 40–80 °C are used; colder moulds reduce cycle time but limit crystallinity development and can produce underfilled glass-rich skin layers. Higher mould temperatures in the 70–80 °C range improve fibre wetting and dimensional stability.
On production-scale reciprocating screw injection moulding machines with 20:1 to 25:1 L/D three-zone screws, screw speed is typically 60–150 min⁻¹ and back pressure 5–15 bar. The fibre length distribution after plasticising will be shorter than the pellet fibre length; commercial compounding and injection moulding can reduce mean fibre length to 200–500 μm after plastication, which influences tensile modulus and impact. Screw wear is higher than unfilled PA12; bimetallic screws with wear-resistant tips and check rings are recommended for long production runs. The hold pressure required for PA12 glass-filled compounds is lower than for amorphous resins of similar viscosity, but packing time must be sufficient to seal the gate and to compensate for crystalline shrinkage. A pack-and-hold switch point set too early produces sink marks at bosses and ribs, while a late switch-over traps gas and can create burn marks at the last-filled region.
Melt rheology for short-glass polyamide 12 systems is shear-thinning. Capillary viscometry according to ISO 11443 at 250 °C and 1000 s⁻¹ typically places glass-filled PA12 apparent viscosity between 150 Pa·s and 300 Pa·s, but this range widens with moisture and fibre length. Moisture above 0.15% lowers apparent viscosity and can create an unstable melt curtain during extrusion. For injection moulding, low shear rates at the end of fill allow fibre orientation to relax; high injection velocities lead to higher orientation in the skin layer, raising flow-direction modulus but reducing transverse impact. If surface streaks appear, the first process response is to check dew point and polymer moisture before adjusting barrel temperature, because thermal masking of moisture streaks usually increases hydrolytic damage.
In fluid connectors, compressed-air lines, cable clips, and lightweight brackets, the specified material must balance low water absorption, fuel and oil resistance, and mechanical reinforcement. PA12 provides resistance to aliphatic hydrocarbons, oils, greases, and salt solutions, with property retention after exposure to fuels and glycols that is often better than PA6 and PA66 in under-bonnet environments. The 8% glass fibre content is sufficient to raise stiffness and reduce creep under load while retaining a lower density than 20–30% glass-filled PA12 compounds. The chemical compatibility of VESTAMID CW1688 Bio30 with production fluids should be verified by immersion testing under ISO 175 or ASTM D543 at the maximum service temperature and stress state. Published data for this exact grade in highly aggressive media is limited; generic PA12 compatibility tables do not account for fibre sizing, weld lines, or stress cracking agents such as zinc chloride at elevated temperature.
Water uptake of PA12 at saturation in 23 °C water is approximately 1.5% when tested to ISO 62; glass fibre reduces the resin volume and typically lowers total uptake below this value. This is lower than PA6 and PA66, which commonly reach 8–10% at saturation. Dimensional changes in humid service are therefore smaller. Because PA12 crystallises slowly at low mould temperatures, parts ejected below 40 °C may continue to shrink for hours after demoulding; for dimensioned components, post-mould conditioning at 23 °C and 50% RH according to ISO 291 provides a reproducible measurement basis. Parts destined for tolerances below 0.1 mm should be measured after conditioning, not at hot ejection, and the contraction allowance should include both mould shrinkage and subsequent moisture absorption.
When PA6, PA66, or Fully Bio-Based PA11 Are the Alternative
Material substitution comparisons are governed by the specification stack. PA6 and PA66 glass-filled grades deliver higher heat deflection temperature and tensile strength than a low-fibre PA12 compound; however, PA12 offers lower density, lower water uptake, and better retention of impact after moisture conditioning. PA66 GF with equivalent or higher loading can exceed the tensile modulus of PA12-GF8, but its density is typically 1.35–1.40 g/cm³ and its saturated water uptake is roughly five times higher than PA12. PA11 derived from castor oil can present renewable carbon content above 90%, which is higher than the 30% Bio30 designation, but PA11 is softer than a glass-filled PA12 compound unless reinforced. Within the VESTAMID portfolio, Bio30 grades differ from VESTAMID Terra PA610 and PA612 grades by polymer chain length, amide density, and the balance between renewable content and low water uptake. The specific choice depends on whether the specification prioritises renewable content, chemical resistance, or dimensional stability.
Compared with unfilled VESTAMID PA12, the CW1688 Bio30 material with 8% glass fibre has a higher melt viscosity at low shear rates and a slightly higher heat deflection temperature. The fibre network reduces post-shrinkage but increases sensitivity to knit-line strength. Compared with a 30% glass-fibre reinforced PA12, the 8% loading retains more elongation and a lower modulus, making it a less brittle candidate for snap-fits and components that require assembly deflection. The glass content is specified by weight; because glass density is approximately 2.54 g/cm³, the volume fraction is between 3% and 4% in a matrix of 1.01–1.03 g/cm³ density. This distinction is important when using micromechanical models to predict modulus.
The material should be specified with the ISO 1043 designation PA12-GF8 and, where renewable content is contractually relevant, the bio-based carbon content test report to ASTM D6866-21 or ISO 16620-2. Do not infer food-contact status from the Bio30 designation; grade-specific food-contact declarations, if required, must be obtained from Evonik documentation. REACH and RoHS compliance statements are product-specific and should be requested for the article or region of sale. For lot comparison, density, melt volume-flow rate, ash content, and tensile modulus are effective incoming quality checks; ash content by ISO 3451-1 verifies the glass fibre weight fraction, while ISO 1183-1 and ISO 527-2 provide mechanical consistency checks. Melt volume-flow rate may be tested to ISO 1133-1 at a condition appropriate for polyamide 12, with moisture removed and reported as mm³ per 10 min if a volume-flow instrument is used.