| HS Code | 466717 |
| Density | 1.01 g/cm³ |
| Melting Point | 178 °C |
| Tensile Strength | 50 MPa |
| Elongation At Break | 200% |
| Flexural Modulus | 1100 MPa |
| Hardness | Shore D 65 |
| Water Absorption 24h | 0.35% |
| Abrasion Resistance | Excellent |
| Chemical Resistance | Resistant to most solvents, oils, and greases |
| Uv Resistance | Good (stabilized for outdoor use) |
| Coefficient Of Friction | 0.35 |
| Dielectric Strength | 30 kV/mm |
As an accredited EMS-Griltech Grilamid DM 10 Nylon 12 Monofilament factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Packaged on moisture-protected reels or spools, typically in 1–5 kg quantities, ensuring clean, tangle-free nylon 12 monofilament delivery. |
| Container Loading (20′ FCL) | 20′ FCL: palletized Grilamid DM 10 nylon monofilament, securely braced, kept dry, ventilated, and protected from heat and moisture. |
| Shipping | Grilamid DM 10 Nylon 12 Monofilament ships in sealed, moisture-proof packaging to prevent absorption and degradation. Store away from direct heat and sunlight. Handle with care to avoid kinking or abrasion. Non-hazardous under standard transport regulations, but protect from heavy loads during transit to maintain filament integrity. |
| Storage | Store Grilamid DM 10 Nylon 12 Monofilament in its original, unopened packaging in a cool, dry, well-ventilated area. Keep away from direct sunlight, heat sources, and high humidity to prevent moisture absorption. Avoid exposure to solvents, dust, or contaminants. Properly sealed, it typically maintains quality for up to two years from delivery. |
| Shelf Life | Store sealed in a cool, dry place away from UV and moisture. Shelf life is typically 5 years from shipment. |
Melt-pressure stability in the metering pump, rather than barrel zone temperatures alone, controls ovality when Grilamid DM 10 is drawn to 0.18 mm diameter for angling leader and tippet material. Nylon 12 monofilament is selected over PA6 in this end use because saturation water absorption is approximately 1.5 wt% under ISO 62, compared with 8.0–10.0 wt% for PA6. The lower equilibrium moisture reduces wet knot-strength loss and diameter swell after immersion. Formulations on production lines typically combine 96.0–98.0 wt% DM 10, 2.0–4.0 wt% UV-stabilizer masterbatch based on a hindered amine light stabilizer, and 0.2–0.5 wt% processing lubricant. The lubricant level is kept below 0.5 wt% because higher addition reduces interfilament friction on the final spool and can cause coil slippage in spin-cast reels.
Pre-drying is mandatory even though PA12 absorbs less moisture than PA6. The resin is dried at 80 °C for 4–6 h with a desiccant dryer to below 0.10 wt% residual moisture; hopper residence time beyond 6 h at ambient RH above 60% re-wets the granulate and produces microbubble defects. Extrusion uses a single-screw extruder with L/D 25:1 to 30:1, a barrier screw, a melt pump, and a screen pack of 20 μm absolute rating. Melt temperature at the die is maintained between 235 °C and 245 °C; pressures upstream of the gear pump are held within ±0.3 MPa of setpoint. The melt is quenched in water at 35–45 °C, after which a two-stage orientation line applies a total draw ratio of 4.0:1 to 5.0:1. Final relaxation of 5–8% occurs in a hot-air oven at 130–150 °C. Closed-loop laser gauges hold diameter tolerance to ±0.005 mm; ovality above 0.010 mm indicates die lip contamination or draw resonance and triggers an automatic cut-transfer to waste. Terminal output is spooled monofilament from 0.10 mm to 0.50 mm for fresh- and saltwater leader systems. Tensile testing follows ASTM D2256/D2256M-21; 24-hour wet-condition measurements are used for product acceptance because dry values overstate field knot retention.
Abrasive monofilament made from DM 10 is used in industrial deburring brushes, surface conditioning discs, and gear polishing tools. The formulation is a two-phase system: 65.0–85.0 wt% DM 10, 15.0–35.0 wt% silicon carbide in F320 to F400 particle sizes, 0.5–1.0 wt% organosilane coupling agent, and 0.3–0.5 wt% hindered phenol antioxidant. Lower SiC loadings below 15 wt% produce filaments with insufficient cutting action, while loadings above 35 wt% shift the melt from a continuous polymer matrix to a particle-dominated suspension. Published continuous-run data for DM 10 above 35 wt% SiC remains limited because filler agglomeration changes melt filtration and orienting stability.
Compounding is performed on a co-rotating twin-screw extruder with L/D 40:1 and a side stuffer for SiC addition after the primary melting zone. Barrel temperatures from the feed throat to the die are profiled from 210 °C to 245 °C, with the side-stuffing zone kept 10 °C lower to prevent polymer degradation at the filler interface. The melt is filtered through a progressive pack of 40 μm, 60 μm, and 40 μm screens; pressure drop across the pack is recorded, and a rise of more than 1.5 MPa indicates screen blinding by fines or agglomerates. The die is a hardened tool-steel plate with land lengths shortened by 20–30% relative to unfilled monofilament to limit pressure loss. Extrusion melt temperature is maintained at 240–250 °C. Quench water at 40–60 °C is used, and the orientation draw is limited to 3.5:1 to 4.2:1 because the filled matrix cannot sustain the 4.5:1 draw typical of unfilled PA12 without filament breaks.
| SiC loading (wt%) | Melt temperature adjustment | Maximum stable draw ratio | Observed production-line failure mode |
|---|---|---|---|
| 15 | +5 °C above unfilled setpoint | 4.2:1 | die-lip abrasion after 8–12 h |
| 25 | +8 °C | 4.0:1 | gear-pump pressure fluctuation ±1.5 MPa |
| 35 | +10 °C | 3.5:1 | filament snap at orienting stand; line stops |
Terminal products are straight or crimped abrasive filaments from 0.40 mm to 1.20 mm, cut to length for cup brushes, deburring wheels, and cylinder brushes. Compliance covers Directive 2011/65/EU for heavy-metal content in the SiC filler and REACH Article 33 for SVHC candidates. Suppliers of SiC are required to provide X-ray fluorescence screening data because recycled abrasive grit intermittently carries cadmium or lead above the 100 mg/kg threshold. Dimensional acceptance uses DIN 53805-1 or equivalent single-filament thickness measurement; Shore hardness of the compounded matrix is not a substitute for cutting-performance testing on the final brush.
Spiral link fabrics for paper machine dryer sections and dewatering belts are produced from monofilament that must be crimped into helices without stress cracking. DM 10 is processed as a 100 wt% virgin monofilament or with 0.8–1.2 wt% hydrolysis-stabilizer masterbatch in wet-section belt variants. The absence of particulate fillers is a requirement; particles larger than 10 μm become surface protrusions and create wear points during spiral-loop friction. Pre-drying to 0.08 wt% moisture is applied at 80 °C for 5 h. Extrusion uses a melt temperature of 230–240 °C, a 20 μm screen pack, and a water quench at 30–50 °C. The oriented filament is drawn to 3.8:1–4.6:1 before crimping.
The critical process step is thermal annealing after orientation and before spiral forming. If annealing is run below 140 °C, residual shrinkage remains above 3% and the finished spiral fabric tightens unevenly on the machine frame. If annealing exceeds 170 °C, the filament surface becomes too soft for consistent loop retention and adjacent helices can slip under tension. Production-scale lines therefore use a two-zone oven at 140–160 °C followed by a controlled cooling zone at 60–80 °C. Shrinkage is measured on free filaments according to ISO 11501; accepted values for paper machine clothing are typically below 2.5% after 15 min at 150 °C. Terminal monofilament diameters range from 0.20 mm to 0.80 mm. The finished spiral fabric is used in dryer screens and in dewatering belts where the lower water absorption measured under ISO 62 reduces hydrolytic chain scission relative to PA6 in wet acid conditions. REACH and mill-level ISO 9001 traceability apply; no direct food-contact migration standard is claimed for this grade unless separately tested.
When woven into food-grade spiral mesh belts for continuous ovens, proofers, freezers, and wash stations, Grilamid DM 10 monofilament is selected for low water absorption and reduced dimensional swell in high-humidity cycles. The extrusion formulation is 100 wt% virgin DM 10; no post-industrial regrind is used because food-contact migration testing under 21 CFR 177.1500 is completed only on virgin resin. A heat-stabilizer masterbatch may be added at 0.5–1.5 wt% only if the masterbatch carrier and additives are listed in the relevant food-contact inventory. Pre-drying to 0.10 wt% moisture at 80 °C for 4–6 h prevents surface pits in the monofilament that would trap food soil and increase cleanout time.
Monofilament is extruded at 230–245 °C, quenched in water at 35–50 °C, oriented at 4.0:1 to 4.8:1, and annealed at 145–165 °C to stabilize free shrinkage below 2% per ISO 11501. Terminal diameters for spiral fabric rods are 0.40 mm to 1.50 mm. Continuous service temperature in dry heat should not exceed 100 °C; operation above 110 °C under load reduces bending fatigue life and may cause rod deformation. Compliance requires migration testing under 21 CFR 177.1500 for nylon 12, with overall migration evaluated under Regulation (EU) No 10/2011 at <10 mg/dm² and specific migration of laurolactam where the target article is specified. A compliance checklist is provided below.
| Jurisdiction | Standard or regulation | Test endpoint | Typical acceptance criterion |
|---|---|---|---|
| United States | 21 CFR 177.1500 | nylon 12 resin for repeated food contact | formulation compliance |
| European Union | Regulation (EU) No 10/2011 | overall migration | <10 mg/dm² |
| European Union | Regulation (EU) No 10/2011 | specific migration of laurolactam | substance-specific limit |
| Global | REACH Annex XVII | restricted substances | absence of listed SVHCs |
Monofilament filter fabrics for liquid-solid separation, sludge dewatering, and chemical bath filtration are produced from DM 10 when the process fluid contains weak acids, oils, or water at pH levels that swell PA6. The base extrusion is 100 wt% DM 10; antistatic variants incorporate 10–20 wt% conductive carbon black masterbatch to reduce surface resistivity without reducing mesh flexibility. No mineral filler is used in filtration grades because surface roughness of the monofilament affects filter cake release and backwashing efficiency. The monofilament is extruded at 230–245 °C, oriented to 4.2:1–4.8:1, and heat-set at 140–160 °C to lock mesh geometry before weaving on rapier looms. Fabric tension must be uniform within ±0.5 N/cm across the reed width; nonuniform warp tension produces diagonal wrinkles that reduce belt tracking stability.
Chemical compatibility for each process fluid is not inferred from nylon 12 generic data and must be tested under ISO 175 or ISO 22088-2 for environmental stress cracking. Under ISO 175 immersion in dilute acetic acid, PA12 typically shows lower mass increase than PA6, but published data for DM 10 in oxidizing acids at elevated temperature is limited. Terminal products are woven filter belts, drum covers, and screen elements in mesh counts from 12 threads/cm to 80 threads/cm using monofilament from 0.10 mm to 0.60 mm. Compliance includes REACH Article 33 and end-user site chemical exposure limits; food-contact status is not automatically conferred unless the specific mesh is tested under Regulation (EU) No 10/2011.
High-mesh-count screen printing fabrics for textile and printed electronics applications use monofilament that must combine high tensile modulus with low diameter variation. DM 10 is extruded as 100 wt% unfilled monofilament; pigment masterbatch is limited to 1.0–2.0 wt% because higher pigment loadings create hard agglomerates that break through the melt filter and cause surface defects. Pre-drying at 80 °C for 4–6 h to 0.10 wt% moisture is standard. Extrusion uses a 20 μm screen pack, melt temperature 235–245 °C, and a quench bath at 30–45 °C. The filament is drawn at 4.5:1 to 5.0:1 and heat-set at 145–165 °C; the higher draw ratio within the stable range is used for 0.10–0.15 mm filaments to increase modulus and reduce mesh deflection during squeegee passes.
Diameter tolerance for screen printing monofilament is ±0.003 mm for filaments below 0.15 mm and ±0.005 mm above 0.15 mm. Ovality above 0.008 mm produces local mesh openings that vary ink deposit thickness by more than 5%. Terminal products are plain-weave screen printing meshes with mesh counts from 43 threads/cm to 165 threads/cm. The material is tested for tensile properties according to ASTM D2256/D2256M-21 and for diameter by optical micrometer according to DIN 53805-1. Directive 2011/65/EU screening applies when the fabric is used in printed electronic applications where the finished assembly is placed on the EU market.
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EMS-Griltech Grilamid DM 10 Nylon 12 monofilament is a melt-spun single-strand extrusion produced from a polyamide 12 base resin. The DM 10 designation identifies a specific melt-viscosity and stabilization package within the EMS-Griltech Grilamid monofilament portfolio. Published documentation for this exact configuration is limited; batch certificates therefore take precedence over generic literature values. Representative property ranges for oriented Grilamid PA12 monofilament include a density of 1.01–1.03 g/cm³ under ISO 1183-1, a melting peak between 175 °C and 180 °C measured by ISO 11357-3, and an equilibrium moisture uptake of 0.7–0.9 % at 23 °C and 50 % RH according to ISO 62. The product is drawn and heat-set to produce circular cross-sections with controlled diameter, ovality, linear density, and residual shrinkage. It is supplied as a continuous monofilament, not as a twisted multifilament yarn or cast film.
The amide-block architecture of PA12 places amide groups at wider spacing than in PA6 or PA66. The result is a lower density and a markedly lower equilibrium moisture absorption. In wet-end paper machine clothing, a PA6 monofilament can reach saturation moisture above 2.5 %, while PA12 remains below 1.0 %. This difference reduces the swelling-driven change in mesh opening and limits the plasticization loss of modulus. PA6 and PA66 can exhibit higher dry tensile strength, but their mechanical values shift more strongly after saturation. In contrast, PA12 maintains a flatter stiffness response across humidity cycles. This is a specification driver where dimensional tolerance must remain stable between wet and dry process conditions. The lower density also produces a lighter fabric for a given yarn diameter, which influences machine clothing energy demand. PA12 has a lower melting point than PA66, which reduces the required heat-setting temperature but also lowers the upper service temperature in dry-heat applications.
| Property | PA12 monofilament | PA6 monofilament | PA66 monofilament | Test method |
|---|---|---|---|---|
| Density | 1.01–1.03 g/cm³ | 1.12–1.14 g/cm³ | 1.13–1.15 g/cm³ | ISO 1183-1 |
| Moisture absorption at 23 °C and 50 % RH | 0.7–0.9 % | 2.5–3.0 % | 2.0–2.5 % | ISO 62 |
| Tensile strength of oriented monofilament | 350–500 MPa | 400–550 MPa | 450–600 MPa | ISO 2062 |
| Elongation at break | 20–35 % | 20–40 % | 15–30 % | ISO 2062 |
| Continuous service temperature in dry air | 80–100 °C | 90–110 °C | 100–120 °C | Manufacturer data |
Production experience on multi-roll stretching lines indicates that PA12 monofilament is less aggressive in terms of die deposit formation than PA66 at equivalent melt temperature, but it requires a narrower quench-temperature band to avoid irregular crystallinity. Extrusion melt temperature is generally maintained between 220 °C and 250 °C; the quench water bath is set at 20–40 °C. A two-stage draw sequence is used. The first stage is performed below 80 °C, while the second stage is performed between 120 °C and 150 °C. Total draw ratio typically ranges from 3:1 to 5:1. Higher draw raises tensile strength and reduces elongation at break. In-line diameter sensors are required because viscosity shifts from recycled or regranulated edge trim can change die swell by more than 0.02 mm at constant pump speed. Pre-drying is required when resin moisture exceeds 0.10 %. A desiccant dryer set at 80 °C for 4–6 h is typical for PA12 monofilament extrusion. Moisture is usually verified by Karl Fischer titration under ISO 15512 before melt processing. Poor drying produces surface splay and lowers melt strength, but PA12 absorbs moisture more slowly than PA6 and therefore tolerates a wider ambient exposure window before processing.
Liquid filtration fabrics converted from PA12 monofilament are specified for processes that alternate hot water, alkaline cleaning agents, and steam sterilization. The lower amide-group concentration slows the rate of hydrolytic chain scission. In accelerated water-aging tests at 80 °C for 1000 h, oriented PA12 monofilaments may retain more than 80 % of initial tensile strength, although values for the DM 10 grade depend on stabilizer content and draw ratio. PA6 and PA66 specimens under identical conditions can show earlier embrittlement. However, PA12 is not inert. Concentrated sulfuric acid, formic acid, phenols, and strong oxidizing baths cause degradation. A compatibility trial is required before use in process streams containing chlorine dioxide, sodium hypochlorite at elevated temperature, or ketone-containing solvents. When autoclave exposure at 121 °C is repeated, dimensional change must be distinguished from strength retention; the fabric can shrink if the monofilament has not been heat-set above the autoclave temperature. The base resin may be listed under FDA 21 CFR 177.1500 for nylon resins in repeated-use food-contact articles, but the finished monofilament and fabricated fabric must be evaluated under the applicable food-contact or filtration standard. Compliance is specific to the formulation and the end-use conditions.
Paper machine clothing forming fabrics use PA12 monofilament in high-density weaves with repeat patterns that demand precise bending recovery. The failure mode observed on industrial fabric lines is not usually tensile overload but surface fibrillation at knuckles after millions of flex cycles. PA12 grades with controlled orientation have lower surface friction and less debris shedding under wet conditions than PA6 of the same diameter. The advantage is maintained at low temperature, but in dry sections above 100 °C the thermal limit of PA12 must be respected. Fabricators often specify residual free shrinkage below 1.5 % after 30 min at 150 °C, but for DM 10 the certificate values govern.
The orientation process for PA12 monofilament passes through a mesophase that crystallizes further during drawing and heat setting. The first-stage draw introduces shear-induced orientation and is typically performed at a roll temperature of 40–60 °C. The second-stage draw and relaxation occur at 110–140 °C and control frozen stress. A total draw ratio of 4:1 to 5:1 produces tensile strength in the upper part of the range but can reduce elongation at break to 20–25 %. Heat-setting at 120–150 °C reduces residual free shrinkage. Differential scanning calorimetry of drawn monofilament often shows a post-setting crystallinity increase of 5–10 % relative to the as-quenched strand. Insufficient heat-setting yields a monofilament that shrinks during downstream coating or lamination; excessive heat-setting embrittles the surface and reduces loop abrasion resistance. At draw ratios above 5.2:1, surface fibrillation in abrasion testing may increase. Below 2.8:1, tensile strength may be insufficient for high-tension industrial fabric requirements.
Dry-running spiral link belts and industrial conveyor fabrics represent a different loading state. The PA12 monofilament is subjected to repeated compression at the hinge, bending over small radii, and abrasive contact with product surfaces. Compared with high-tenacity PET monofilament, PA12 has lower initial modulus and greater elongation at break, which shifts failure from brittle cracking to ductile yielding at low strain. The trade-off is a lower continuous service temperature and higher creep. For load-bearing dryer belts operating above 80 °C, PET or PPS monofilament may be more appropriate unless PA12 is evaluated under the specific creep-load duration. Published creep-rupture data for DM 10 monofilament under industrial belt tension is limited; the design should include a safety factor determined from prototype trials.
Accelerated ageing programs for PA12 monofilament measure retained tensile strength, elongation, and free shrinkage after immersion in deionized water at 80 °C for 500 h and 1000 h. Tests on oriented PA12 monofilament generally show tensile strength retention above 80 % after 1000 h, while elongation retention may drop by 10–15 %. These values are not specifications; they vary with antioxidant package, diameter, and draw ratio. The same data cannot be transferred directly from resin plaques tested under ISO 527-2. A monofilament-specific sample geometry is required because orientation and surface area differ from injection-molded specimens. Outdoor exposure without carbon black or UV stabilizer leads to surface cracking and strength loss. Black formulations with well-dispersed carbon black improve resistance under ISO 4892-2 xenon-arc testing, but the DM 10 grade may not be UV-stabilized unless specified. Continuous dry-air service above 80 °C also requires oxidative stabilization; oxidation induction time measured under ISO 11357-6 at 200 °C is a quality-control indicator but does not predict long-term performance.
No single property benchmark determines the suitability of Grilamid DM 10 Nylon 12 monofilament. Selection is made against specific mesh-opening stability, flexural fatigue, hydrolytic ageing, and processing tolerance requirements. Where the application demands maximum dry tensile modulus or continuous service above 100 °C, the material should be compared directly with PA66, PET, PPS, or PEEK monofilaments using the same monofilament diameter and test method. Published data for the DM 10 designation remains limited for several high-temperature and aggressive-chemical configurations; qualification trials on the finished fabric or belt therefore remain the controlling technical decision.