| HS Code | 718143 |
| Product Name | ISO-TECH ISO-MID PA 12 |
| Manufacturer | ISO-TECH |
| Product Type | Hot-melt adhesive glue stick |
| Base Resin | Polyamide (PA) |
| Color | Amber |
| Application Temperature C | 200-230 |
| Service Temperature Range C | -40 to +120 |
| Viscosity At 200 C Mpa S | 4000-6000 |
As an accredited ISO-TECH ISO-MID PA 12 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | 1 kg spool of ISO-TECH ISO-MID PA 12, vacuum-sealed in moisture-barrier packaging with desiccant, labeled with product details. |
| Container Loading (20′ FCL) | 20' FCL: palletized ISO-MID PA 12, securely braced and blocked, protected from moisture, with proper load distribution. |
| Shipping | Ship ISO-TECH ISO-MID PA 12 as polyamide 12 (nylon 12) powder. It is not regulated as dangerous goods under ADR, IMDG, or IATA in normal packaging. Use sealed, moisture-proof containers; avoid dust accumulation and ignition sources. Label as non-hazardous polymer powder and keep away from incompatible materials. |
| Storage | Store ISO-TECH ISO-MID PA 12 in its original, tightly sealed container in a cool, dry, well-ventilated area away from heat, sparks, open flames, and direct sunlight. Protect from moisture and maintain storage temperatures between 15–25°C. Keep containers closed when not in use. Under these conditions, typical shelf life is 12 months. |
| Shelf Life | The shelf life of ISO-TECH ISO-MID PA 12 is typically 2 years from manufacture when stored sealed in a cool, dry place. |
| Scenario | Primary compliance standard | Addition ratio | Critical process parameter | Terminal product type |
|---|---|---|---|---|
| Selective laser sintering | ASTM F3091/F3091M-14 | 40–50 wt% virgin refresh; 0.2–0.5 wt% fumed silica | Bed temperature 168–176°C; layer 0.10–0.12 mm | Manifolds, housings, fixtures |
| Automotive multilayer fuel lines | SAE J2260 | 75–85 wt% PA 12 base in outer/inner layer | Melt temperature 230–250°C; vacuum 0.2–0.4 bar | Fuel feed and vapor lines, urea supply lines |
| Cable sheathing | IEC 60811-100:2012 | 80–90 wt% PA 12 base | Melt temperature 220–240°C; line speed 20–80 m/min | Sensor cable jackets, robot dress-pack jackets |
| Medical catheter tubing | ISO 10993-1:2018 | 70–90 wt% PA 12 base; 10–30 wt% BaSO₄ | Melt temperature 210–230°C; wall 0.10–0.30 mm | Catheter shafts, microcatheter liners |
| Laser direct structuring / MID | IPC/JEDEC J-STD-020E | 80–95 wt% PA 12 base; 4–8 wt% LDS additive | Mold temperature 80–110°C; laser 1064 nm | Sensor housings, antenna substrates |
| Unbonded flexible pipe | API Spec 17J:2014 | 100 wt% PA 12 base; 0.5–1.5 wt% antioxidant | Melt temperature 240–260°C; sheath die vacuum 0.2–0.6 bar | Pressure sheaths, subsea flowline sheaths |
Selective laser sintering powder-bed fusion with ISO-TECH ISO-MID PA 12 operates as a semi-crystalline build process in which the feedstock powder is dried at 80°C for 12–24 h to reduce residual moisture below 0.10 wt% before loading into a 70–100 W CO₂ laser system operating at 10.6 µm. Compliance is anchored to ASTM F3091/F3091M-14 for polyamide 12 powder specification, while mechanical evaluation after build uses ASTM D638-14 Type IV specimens and ISO 527-2:2012 at a test speed of 50 mm/min. The formulation addition ratio is not a conventional melt-compounded additive system; virgin ISO-TECH ISO-MID PA 12 powder is refreshed at 40–50 wt% virgin material blended with 50–60 wt% reused powder, with 0.2–0.5 wt% fumed silica flow additive and 0.2–0.5 wt% hindered phenolic antioxidant blended in low-shear tumbling units prior to sieving. The downstream production process involves a heated build chamber maintained at 168–176°C, which holds the powder bed within approximately 12 K below the melt peak, and layer thickness is controlled at 0.10–0.12 mm with hatch spacing of 0.08–0.15 mm. Terminal finished product types include functional manifolds, HVAC ducting, low-volume production housings, automotive interior brackets, and lightweight assembly fixtures.
Production-scale failure modes observed on SLS systems with 150 mm × 150 mm build plates include uneven thermal gradients when bed heater elements deviate more than ±2°C across the build area, producing warped lower layers and anisotropic shrinkage of 0.8–1.5% in the z-axis. Recycle ratios above 60 wt% used powder cause an increase in zero-shear viscosity and produce orange-peel surfaces. If recycled powder is not resieved below 100 µm, un-melted particle defects appear on as-built surfaces. Addition of external flow agents above 0.5 wt% increases powder flowability but reduces tensile strength measured per ASTM D638-14 by more than 8% relative to unmodified virgin powder.
On automotive multilayer fuel vapor line coextrusion lines, ISO-TECH ISO-MID PA 12 functions as the outer polyamide layer because its equilibrium moisture absorption of approximately 0.7 wt% at 23°C and 50% RH preserves dimensional stability in ethanol-blended fuel environments. Compliance is assessed under SAE J2260 permeation limits for nonmetallic fuel tubing and DIN 73378:2013 for polyamide tubing dimensions; fuel resistance is verified by immersion in ASTM Reference Fuel C at 60°C for 168 h with tensile retention above 70%. In a coextruded four-layer construction of PA12/tie/EVOH/tie/PA12, the ISO-TECH ISO-MID PA 12 compound used in the inner and outer layers is formulated with 75–85 wt% PA 12 base resin, 10–18 wt% medium-molecular-weight plasticizer, 2–4 wt% carbon black masterbatch, and 0.5–1.5 wt% copper-complex heat stabilizer. Downstream production processing uses a 45 mm single-screw extruder with L/D 30:1, a barrier screw, melt temperature of 230–250°C, and a coextrusion die with spiral mandrel distribution. Vacuum sizing at 0.2–0.4 bar below atmosphere and haul-off speed of 20–60 m/min are adjusted to maintain wall thickness of 0.8–1.5 mm. Finished components include diesel fuel feed and return lines, vapor recovery lines, and selective catalytic reduction urea supply lines for light- and heavy-duty vehicles. If melt temperature exceeds 260°C for more than 10 min, heat stabilizer depletion causes gel formation and black specks in the outer layer, requiring line shutdown and screw removal.
In halogen-free cable sheathing, ISO-TECH ISO-MID PA 12 is selected where the bundled wire must withstand combined abrasion, low-temperature impact, and oil mist. Industry compliance is demonstrated through IEC 60811-100:2012 for sheath mechanical tests, ISO 6722-1:2011 for automotive single-core cables, and RoHS 2011/65/EU as amended by (EU) 2015/863 for restricted substances. The formulation loading for a flame-retardant sheath uses 80–90 wt% ISO-TECH ISO-MID PA 12, 8–15 wt% halogen-free nitrogen-phosphorus flame retardant masterbatch, 1–2 wt% UV stabilizer, and 0.5–1.0 wt% processing lubricant. The downstream production process applies the sheath on a 65 mm single-screw extruder with L/D 25:1 operating at 220–240°C melt temperature and 20–80 m/min line speed, followed by immersion into a three-zone water trough with a temperature gradient of 50°C/30°C/15°C. Terminal product types include sensor cable jackets, automotive ABS sensor cable sheathing, industrial robot dress-pack jackets, and fiber optic distribution cable outer jackets. Shrinkage above 3% in the jacket after 15 min at 150°C per IEC 60811-502:2012 is caused by line-induced molecular orientation frozen into the sheath during cooling; reducing melt temperature and raising the first trough temperature to 50°C lowers longitudinal shrinkage below 2%.
Catheter shaft extrusion with ISO-TECH ISO-MID PA 12 demands a closed-loop drying and microextrusion line because residual moisture above 0.08 wt% produces microbubbles in tubing with wall thickness below 0.15 mm. Compliance is evaluated under ISO 10993-1:2018 biological evaluation, ISO 10993-5:2009 cytotoxicity, USP <88> Class VI, and 21 CFR 177.1500 for nylon resins in food-contact applications where applicable. The compounding formulation for a radiopaque catheter shaft is 70–90 wt% ISO-TECH ISO-MID PA 12, 10–30 wt% barium sulfate with a median particle size of 1–2 µm, and 0.2–0.5 wt% high-temperature amide wax dispersant. Downstream production uses a 19 mm microextruder with L/D 24:1, a PEEK screw, and melt temperature of 210–230°C; the melt is drawn through a crosshead die and vacuum-calibrated with 0.1–0.3 bar vacuum to control ovality below 0.03 mm. Finished device types include balloon catheter outer shafts, diagnostic catheter bodies, microcatheter liners, and endoscopic instrument sheath tubing. Published data for this specific configuration is limited for long-term drug compatibility, so chemical resistance must be verified on the final sterilized device rather than inferred from raw resin alone.
With LDS activation at 1064 nm, the filler dispersion threshold narrows to ±0.5 wt% in ISO-TECH ISO-MID PA 12 because the spinel-based LDS additive must be uniformly distributed in the surface region without forming agglomerates larger than 20 µm. There is no single ISO-level LDS standard; compliance is handled through the laser equipment supplier's process control documentation, ISO 9001:2015 for manufacturing quality, and IPC/JEDEC J-STD-020E moisture sensitivity level classification where assemblies are reflow-soldered. The compounding addition ratio is 80–95 wt% ISO-TECH ISO-MID PA 12 base resin, 4–8 wt% copper-chromium spinel LDS additive, and 0–15 wt% glass fiber when higher flexural modulus is required. Downstream injection molding uses a 70 t clamp force machine with melt temperature of 250–270°C, mold temperature of 80–110°C, and back pressure of 5–10 bar; after molding, the surface is laser-activated at 1064 nm, then copper, nickel, and gold layers are deposited by additive electroless plating. Terminal parts include automotive steering-angle sensor housings, three-dimensional antenna structures, medical instrument handles with conductive traces, and consumer electronic MID substrates. If the LDS additive loading exceeds 8 wt%, tensile elongation falls below 5% and screw torque during compounding rises by approximately 20%.
The pressure sheath extrusion window for ISO-TECH ISO-MID PA 12 in unbonded flexible pipe is defined by melt strength requirements over annular gaps from 5 mm to 15 mm over the pipe carcass without sagging. Compliance is governed by API Spec 17J:2014 and ISO 13628-2:2012 for unbonded flexible pipes, with tensile properties measured per ISO 527-2:2012 at 23°C and 60°C. The formulation addition is substantially neat: 100 wt% ISO-TECH ISO-MID PA 12 with 0.5–1.5 wt% antioxidant package and 0–6 wt% plasticizer where subsea installation temperature falls below −30°C. Downstream production runs on a 120 mm single-screw extruder equipped with a grooved feed section, L/D 30:1, melt temperature of 240–260°C, and a vacuum-calibrated sheath die with differential pressure control of 0.2–0.6 bar; extrusion is continuous around the interlocked carcass at 0.5–2.0 m/min. Terminal finished product types include pressure sheaths for flexible risers, outer sheaths for subsea flowlines, and internal wear layers in high-pressure gas lift lines. Operational boundaries include avoiding continuous service above 90°C in the presence of methanol or strong inorganic acids because solvent-induced crystallization and hydrolysis reduce elongation at break below 50% after 1,000 h.
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ISO-TECH ISO-MID PA 12 is a semi-crystalline polyamide 12 compound supplied as pelletized feedstock for injection molding and profile extrusion. The material is designated PA12 under ISO 1043-1:2011 and is controlled by the manufacturer’s certificate of analysis for density, melt volume-flow rate, residual moisture, and tensile properties. Published product-specific data for the ISO-MID formulation remains limited; the numerical ranges referenced below are representative unfilled PA12 injection and extrusion grade values measured under ISO 527-1/-2, ISO 1183-1, ISO 62, ISO 1133-1, and ISO 11357-3. Incoming inspection of ISO-TECH ISO-MID PA 12 typically applies a density window of 1.01–1.04 g/cm³, a melt volume-flow rate at 235 °C and 5 kg of 8–20 cm³/10 min, and a dried pellet moisture content below 0.10% by mass. The polymer occupies a processing niche between short-chain PA6/PA66 and long-chain PA11: lower amide group density produces saturated water absorption near 1.5% by mass, reducing hygroscopic dimensional movement and stabilizing electrical surface resistance in humid production environments.
The distinction is rooted in the C12 aliphatic repeat unit. A longer methylene sequence lowers the concentration of hydrogen-bonding amide groups, reducing equilibrium moisture uptake relative to PA6 and PA66. Under ISO 62 saturation at 23 °C in water, unfilled PA12 typically reaches 1.5% by mass, whereas PA6 reaches 9.5–10.0% and PA66 reaches 8.0–9.0%. At 23 °C and 50% relative humidity, PA12 attains approximately 0.7–0.8% moisture, while PA6 and PA66 reach approximately 2.5–3.0%. This differential changes part dimensions, tensile modulus, and impact behavior. The lower dry tensile modulus of PA12, commonly 1400–1600 MPa, relative to PA6 at 2500–3500 MPa and PA66 at 2700–3300 MPa, is a design trade-off: rigidity is sacrificed for lower hygroscopic expansion, lower density, and higher elongation at break. At –40 °C, PA12 retains more impact ductility than dry PA66 in many unfilled systems; notched Charpy impact values for conditioned PA12 are commonly reported between 6 kJ/m² and 12 kJ/m², while dry PA66 values may be 3–5 kJ/m². The melting temperature of PA12 is 175–180 °C, which limits continuous service above 80–100 °C unless the grade is glass-fiber reinforced.
| Property | Method | PA12 | PA6 | PA66 |
|---|---|---|---|---|
| Density | ISO 1183-1 | 1.01–1.04 g/cm³ | 1.12–1.15 g/cm³ | 1.13–1.16 g/cm³ |
| Saturated water absorption at 23 °C in water | ISO 62 | 1.5% | 9.5–10.0% | 8.0–9.0% |
| Tensile modulus, dry as molded | ISO 527-1/-2 | 1400–1600 MPa | 2500–3500 MPa | 2700–3300 MPa |
| Melting temperature | ISO 11357-3 | 175–180 °C | 220–225 °C | 255–265 °C |
| Typical melt-processing range | Manufacturer data | 230–260 °C | 240–270 °C | 270–300 °C |
Compared with PA11, PA12 displays a melting point approximately 10–15 °C lower and a slightly narrower processing window. Compared with PA610 and PA1012, PA12 typically exhibits lower water absorption but also lower modulus; the selection is governed by dimensional tolerance, chemical exposure, and low-temperature impact requirements.
Before melt processing, ISO-TECH ISO-MID PA 12 must be dried in a desiccant dryer with a dew point at or below –30 °C. Drying at 80 °C for 4–8 h normally reduces residual moisture from sealed-bag levels to below 0.10% by mass. A hot-air tray dryer is not sufficient when ambient relative humidity exceeds 60%, because PA12 equilibrium moisture at 50% RH is 0.7–0.8% and diffusion from the pellet core is slow below 80 °C. Residual moisture above 0.15% at melt temperatures above 230 °C leads to hydrolytic chain scission, observed as a drop in melt viscosity, silver streaks, and reduced tensile elongation.
On a conventional reciprocating-screw injection molding machine with a three-zone general-purpose screw of 20:1 to 25:1 L/D and compression ratio 2.0:1 to 2.5:1, barrel temperatures from feed to nozzle are typically 210–230 °C, 235–250 °C, 240–255 °C, and 230–250 °C. Mold temperature is set at 30–80 °C. Lower mold temperatures reduce cycle time but produce lower crystallinity and higher post-mold shrinkage. Higher mold temperatures near 80 °C improve dimensional stability and reduce internal stress in snap-fit geometries. Hold pressure is typically 50–80% of the first-stage injection pressure; hydraulic injection pressure commonly falls between 60 MPa and 100 MPa depending on flow length and wall thickness. Back pressure is maintained at 0.3–0.7 MPa hydraulic to ensure melt homogeneity without excessive frictional heat. Melt residence time at 250 °C should not exceed 10–15 min; beyond this window oxidative degradation can increase yellowness index and lower notched impact strength. If interruption occurs, the barrel is purged with a low-viscosity polyolefin or a dedicated purging compound, not with PVC or acetal, because acid buildup can accelerate degradation of polyamide.
Profile extrusion uses a single-screw extruder with 24:1 to 30:1 L/D, a 3:1 compression ratio, and barrel zones from 190–210 °C at the feed throat to 230–250 °C at the die. Melt temperature measured by an immersion thermocouple should remain between 230 °C and 250 °C. A melt pump between screw tip and die reduces surging and controls wall thickness in pneumatic tubing. Vacuum venting at –0.8 bar gauge is recommended if regrind content exceeds 20%, because recycled flake can carry surface moisture. Regrind levels above 30% can raise melt viscosity fluctuations and increase tube ovality. Die land length and drawdown ratio must be adjusted for PA12’s higher die swell relative to PA6; published values for die swell in unfilled PA12 depend on shear rate, but die diameter is commonly sized 5–10% smaller than final outer diameter when a vacuum calibration tank is used.
Capillary rheometry on unfilled PA12 at 235 °C shows shear-thinning behavior with apparent viscosity falling from approximately 800–1200 Pa·s at 100 s⁻¹ to 150–250 Pa·s at 1000 s⁻¹. These are representative ranges; lot-specific curves should be generated on a capillary rheometer with a 1 mm diameter die and 20:1 length-to-diameter ratio. The flow-length-to-wall-thickness ratio for unfilled PA12 is typically limited to 200:1 at 1 mm wall and 260 °C. Thin-wall connectors below 0.75 mm wall thickness may require fast injection velocities above 150 mm/s screw speed and melt temperatures near 250–260 °C, but this narrows the residence-time window. Shear rates above 10,000 s⁻¹ in gate lands produce melt fracture and surface haze; gate diameters below 0.5 mm should be avoided unless a hot-runner system with independent nozzle heating is used.
Across automotive fluid-handling and industrial automation applications, ISO-TECH ISO-MID PA 12 is processed into pneumatic tubing, fuel-vapor lines, cable sheathing, and quick-connect housings. In coiled pneumatic tube production, lower moisture uptake helps maintain outer diameter and roundness after conditioning cycles at 23 °C and 50% RH for 168 h. Resistance to zinc chloride stress cracking is not absolute; stressed snap-fit connectors exposed to zinc chloride road de-icer have exhibited stress crack initiation at outer fiber strain above 1.0–1.5% in PA12 grades. Snap-fit retention features therefore keep maximum fiber strain below 1.0% or use radiused corners with at least 0.5 mm radius to reduce notch sensitivity. In cable harness conduit, PA12 offers lower specific density than PA66. At a wall thickness of 0.5 mm, the mass per meter of PA12 convoluted tube is about 15–20% lower than PA66 tube of equal outer diameter, assuming a density difference of about 0.10 g/cm³.
For selective laser sintering or film applications, ISO-MID PA12 powder or sheet variants, if supplied, require separate specifications; this description addresses only pelletized injection and extrusion grades. Published data for this specific configuration is limited, so part qualification must include verification of tensile properties, heat deflection temperature under ISO 75-1/-2, and impact behavior on specimens cut from production parts.
Hygroscopic expansion is a primary failure mode in assemblies that contain both PA12 and metal inserts. The coefficient of linear thermal expansion of unfilled PA12 is typically 100–150 × 10⁻⁶ K⁻¹ in the flow direction and 120–160 × 10⁻⁶ K⁻¹ transverse to flow; moisture-induced linear expansion from dry to 50% RH is approximately 0.15–0.25%. The corresponding value for PA66 can be 0.5–0.8% under the same moisture swing, creating greater risk of insert cracking or dimensional interference. For a gear or clip with a 20 mm critical dimension, PA12 would be expected to change roughly 0.03–0.05 mm due to moisture absorption from dry to 50% RH; the same geometry in PA66 could move 0.10–0.16 mm unless annealed and conditioned.
Part acceptance tests should include conditioning to equilibrium at 23 °C and 50% RH for 168 h and dimensional measurement with a calibrated coordinate measuring machine. Post-mold annealing of unfilled PA12 at 120–150 °C for 2 h per 5 mm wall thickness reduces locked-in orientation and stabilizes crystallinity, but temperatures above 160 °C may cause surface oxidation and discoloration. Shrinkage prediction must account for flow direction: mold shrinkage values for unfilled PA12 are typically 0.7–1.5% in the machine direction and 1.0–1.8% transverse, depending on wall thickness, mold temperature, and gate size. Using a mold temperature at the low end of the range, 30–40 °C, can produce post-mold growth of 0.2–0.5% when the part is subsequently heated or humidified. This is a frequent batch-to-batch variability source in injection facilities that do not control mold temperature tightly.
For regulatory documentation, ISO-TECH ISO-MID PA 12 is typically evaluated under REACH Article 33 obligations and RoHS Directive 2011/65/EU Annex II restrictions. A supplier certificate of conformity should confirm the absence of cadmium, lead, mercury, hexavalent chromium, PBB, and PBDE above the permitted maximum concentration of 0.1% by mass in homogeneous materials. Food-contact status is not implied for all grades; where applicable, the supplier must state compliance with FDA 21 CFR 177.1500 or EU 10/2011 with specific migration limits for laurolactam and caprolactam. Unfilled PA12 is not inherently flame retardant; the material typically meets UL 94 HB at thicknesses of 1.5 mm or greater, but a passing UL 94 V-2 or V-0 classification requires a listed flame-retardant variant. For electrical applications, the comparative tracking index of unfilled PA12 is often 600 V under IEC 60112, but this value drops in the presence of carbon black or high regrind content.
| Standard or regulation | Parameter | Typical basis |
|---|---|---|
| ISO 1874-1 | Designation and specification | PA12 injection/extrusion grade |
| ISO 1043-1:2011 | Polymer identification | PA12 |
| ISO 527-1/-2 | Tensile modulus, yield stress, elongation | 1400–1600 MPa, 45–50 MPa, >200% |
| ISO 1183-1 | Density | 1.01–1.04 g/cm³ |
| ISO 62 | Water absorption | Saturated 1.5%; 50% RH 0.7–0.8% |
| ISO 1133-1 | Melt volume-flow rate | 8–20 cm³/10 min at 235 °C/5 kg |
| IEC 60112 | Comparative tracking index | 600 V for unfilled natural grade |
| RoHS 2011/65/EU | Restricted substances | ≤0.1% in homogeneous material |
These standards positions are verification starting points, not a substitute for lot-specific certificates. The purchaser must request the manufacturer’s ISO 11469 marking recommendations and any UL Yellow Card if the part enters electrical enclosures.