| HS Code | 461458 |
| Chemical Name | Polyamide 11 (PA11) |
| Cas Number | 25035-29-6 |
| Color | Natural (translucent white) |
| Physical Form | Fine powder |
| Density | 1.03 g/cm³ |
| Bulk Density | 0.60 g/cm³ |
| Melting Point | 188 °C |
| Vicat Softening Temperature | 170 °C |
| Tensile Strength | 62 MPa |
| Elongation At Break | 320 % |
| Flexural Modulus | 1300 MPa |
| Shore Hardness | D 75 |
| Water Absorption 24h | 0.3 % |
| Dielectric Strength | 16 kV/mm |
| Particle Size D50 | 60 μm |
As an accredited Arkema Rilsan Fine Powders T NAT 2P PA11 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | 25 kg bag of Arkema Rilsan Fine Powders T NAT 2P PA11, natural polyamide 11 powder, in sealed plastic-lined paper sack. |
| Container Loading (20′ FCL) | 20′ FCL container loading of Arkema Rilsan Fine Powders T NAT 2P PA11: palletized bags, secured, dry, ventilated, no contamination. |
| Shipping | Ship Arkema Rilsan Fine Powders T NAT 2P PA11 in sealed, moisture-proof containers to prevent clumping. Keep dry, away from humidity and direct sunlight. Avoid exposure to excessive heat or sparks. No special hazardous classification under normal transport; protect packaging from damage during handling. |
| Storage | Store in a cool, dry, well-ventilated area away from direct sunlight, heat, and ignition sources. Keep containers tightly sealed to prevent moisture absorption and contamination. Maintain temperatures below 40°C. Avoid generating dust clouds; use grounded equipment. Follow local regulations for combustible powders. |
| Shelf Life | Shelf life is typically 2 years if kept in original unopened container, stored cool, dry, and away from sunlight. |
The use of Arkema Rilsan Fine Powders T NAT 2P PA11 in dishwasher rack coating begins with a dry powder formulation in which the PA11 resin constitutes 98.0–99.5 wt% of the total blend, with 0.3–1.0 wt% acrylate flow-control additive and 0.2–0.7 wt% hindered phenolic antioxidant; when a colored rack coating is required, an additional 0.5–2.0 wt% pigment concentrate is introduced only as a masterbatch to avoid dry-mix segregation. On a production-scale electrostatic spray line, the powder is charged by a corona gun operated at 60–80 kV, with a gun-to-part distance of 150–250 mm, and applied to a grit-blasted steel wire rack with a typical substrate roughness of SA 2½ per ISO 8501-1. The as-applied dry film thickness is controlled between 250 µm and 400 µm; thickness below 250 µm is associated with salt spray failure at weld points, while thickness above 400 µm is associated with drip formation during gelation and internal stress development after quenching. The coated rack then passes through a convection cure oven with air temperature set at 210–230 °C and a peak part metal temperature of 195–205 °C; residence time is determined by the cross-sectional mass of the rack wire and commonly falls between 8 min and 12 min. Compliance for food-contact use requires that the applied film meet FDA 21 CFR 175.300 resinous and polymeric coatings conditions for intended use; for EU export, Regulation (EU) No 10/2011 overall migration testing is conducted in 3% w/v acetic acid for 2 h at 70 °C, with acceptance below 10 mg/dm². Corrosion performance is verified by ISO 9227 NSS neutral salt spray exposure of 1,000 h with no red rust at scribed areas; adhesion is evaluated by ASTM D3359 cross-cut tape test on a parallel coupon, requiring classification 4B or better, and impact resistance is assessed per ASTM D2794 with a 1.8 J reverse impact on a 3 mm steel panel. Terminal products in this scenario include dishwasher basket assemblies, cutlery holders, and hot-water circulation rack modules for commercial dishwashing equipment; the operational boundary is that the PA11 film should not be continuously exposed to wash liquor above 75 °C at pH above 11, because alkaline hydrolysis of the amide bond accelerates with temperature. Production-scale failure data from conveyorized coating lines indicates that batch-to-batch variance in powder particle size distribution, specifically fines below 20 µm, increases transfer efficiency loss and causes back-spraying in corona guns when relative humidity exceeds 60%; therefore closed-loop powder feed with 40–45% relative humidity and sieve at 150 µm is maintained.
For fluidized-bed dip coating of ductile iron valve bodies, Rilsan T NAT 2P PA11 powder is charged into a fluidizing hopper with a porous polypropylene distributor plate; the addition ratio for this process is 100 wt% Rilsan T NAT 2P as the sole coating resin, with optional 0.1–0.5 wt% dry flow additive only where fluidization is irregular due to particle agglomeration. The process sequence begins with degreasing and shot blasting to SA 2½ surface preparation, followed by preheating in a forced-air oven at 280–310 °C until the valve body reaches a core temperature of 250–270 °C; the immersion step is normally 3–8 s, after which the part is withdrawn and post-fused in a second oven at 200–220 °C for 3–5 min. The upper immersion time limit is set by the thermal capacity of the casting and by the risk of film oxidation in the fluid bed; at immersion times beyond 10 s, the residual heat in heavy sections can raise the film surface above 240 °C, producing discoloration and a measurable loss of tensile elongation in the fused film when tested per ISO 527-3 on free films. For chemical service, the coating is specified at a dry film thickness of 350–500 µm; this thickness range is validated by ISO 2812-1 chemical immersion testing in 10% w/v sulfuric acid and 10% w/v sodium hydroxide solutions at 23 °C for 30 days, with acceptance criteria of loss of adhesion less than 1 mm from scribe and no blistering. Relevant compliance standards include ISO 15741 for coatings on buried or immersed steel structures and ISO 12944-6 corrosion class C5 where applicable; in potable or process water contact, NSF/ANSI 61 extraction testing is conducted, and in gas valve service EN 488 or ISO 15589-1 may be referenced depending on the operator specification. Terminal products include butterfly valve bodies, knife gate valve plates, pump impellers, and level transmitter housings. The operational boundary is that this coating is not recommended for continuous exposure to strong mineral acids above 60 °C, particularly 30% w/v HCl, where the amide linkage hydrolyzes at a rate that reduces film thickness by more than 50 µm/year; published data for this specific grade under such concentrated acid conditions is limited, and qualification by immersion testing is mandatory before installation.
| Application segment | Directive or standard | Test method designation | Typical acceptance criterion |
|---|---|---|---|
| Dishwasher racks | FDA 21 CFR 175.300 | Extraction cell per FDA guidance | Migration below specified extractive tolerance |
| Dishwasher racks EU | Regulation (EU) No 10/2011 | EN 1186-1 | < 10 mg/dm² |
| Valve bodies | ISO 15741 | ISO 9227 NSS | No red rust after 1,000 h |
| Automotive mechanisms | IATF 16949 | ISO 11997-1 Cycle B | No blistering after 500 h |
| Outdoor panels | EN 15706 | ISO 16474-2 Method A | ΔE* < 3.0 after 1,000 h |
| Potable water spools | NSF/ANSI 61 | NSF/ANSI 61 Section 4 extraction | No exceedance of normalized extraction limits |
| Offshore access structures | ISO 20340 | ISO 4624 pull-off | > 5 MPa adhesion after cyclic ageing |
On automotive seat mechanism coating lines, Rilsan Fine Powders T NAT 2P PA11 is processed as a high-thickness anti-creak and anti-corrosion layer over phosphate or zinc-iron treated spring steel substrates. The formulation starting point uses 99.0–99.5 wt% PA11 powder with 0.5–1.0 wt% of a silane-functional dry bonding agent to improve adhesion to the metallic conversion layer; no separate primer is used when the substrate has been shot-blasted or phosphate-treated to a surface roughness of Rz 40–70 µm per ISO 4287. The powder is applied by robotic electrostatic spray guns in multiple passes, each pass depositing 80–120 µm, to reach a final film thickness of 180–250 µm; the part is then cured in a multi-zone electrically heated convection oven with zone temperatures of 215 °C, 225 °C, and 205 °C, corresponding to a peak part temperature of 198–205 °C. Production validation is supported by PPAP documentation under IATF 16949, and occupational powder exposure is controlled within REACH Annex XVII dust limits. Adhesion to phosphate grain boundaries is evaluated with ASTM D4541 pull-off testing, with a minimum of 7 MPa adhesion strength required on 2 mm cold-rolled steel coupons; cyclic corrosion resistance is screened by ISO 11997-1 Cycle B using 500 h exposure. The terminal products are seat adjustment spring packs, recliner mechanism covers, and seatbelt anchor brackets. The process constraint on high-speed automotive lines is that post-cure quenching in water at 20 °C must be avoided, because rapid cooling of the PA11 film from above its crystallization temperature generates internal tensile stress at the coating-metal interface and reduces chip resistance under ASTM D3170 gravelometer testing; instead, forced-air cooling at 0.5–1.0 m/s is used to bring the part below 60 °C before handling.
When preheat oven air velocity drops below 3 m/s on perforated sheet metal, the heat transfer to the web between perforations becomes non-uniform, resulting in a local peak metal temperature differential of 15–25 °C across the sheet surface. This condition is observed in Rilsan T NAT 2P PA11 coating of perforated aluminum and steel panels used for outdoor furniture and architectural cladding; the addition ratio for this application is 97.5–99.0 wt% PA11 with 0.8–1.5 wt% UV stabilizer masterbatch based on hindered amine light stabilizers and 0.2–0.5 wt% carbon black concentrate where dark colors are required for weatherability. The sheet is first preheated in a convection tunnel to a surface temperature of 240–260 °C and then dipped into a fluidized bed of T NAT 2P powder for 2–5 s; the resulting film thickness is controlled between 200 µm and 300 µm by adjusting immersion time and substrate temperature. After post-fusion at 205–215 °C for 5 min, the coated panels are tested for weathering per ISO 16474-2 Method A or ASTM G154 Cycle 1, with color change ΔE* less than 3.0 after 1,000 h and gloss retention above 50% on smooth surfaces. Outdoor compliance is anchored to EN 15706 hardware durability and ISO 12944-5 coating systems for C4 coastal or C3 urban environments; when the end product is exported to the EU, REACH Annex XVII migration limits for PA11 monomer and additives are verified on the powder. Terminal products include park benches, perforated acoustic cladding panels, bus shelter louver panels, and public area litter-bin bodies. The processing boundary on perforated geometry is that open area fractions above 35% require reduced preheat temperature by 10–15 °C to prevent powder melt-through and sag along hole edges; conversely, open area below 10% may require extended post-fusion to compensate for lower edge heat retention.
Inside water distribution equipment manufacturing, Rilsan Fine Powders T NAT 2P PA11 is used as a barrier coating on carbon steel pipe spools and flanges that alternate between moist air, chlorinated potable water, and ambient storage conditions. The formulation is kept as a single-component system at 99.0–100 wt% PA11; no plasticizer is added, because low-molecular-weight plasticizers can migrate into potable water and exceed NSF/ANSI 61 normalized extraction limits. The spool interior is coated by electrostatic spray after grit blasting to SA 2½; the powder is cured in an indirect gas-fired oven with a part temperature of 200–210 °C for 8–10 min at a minimum dry film thickness of 250 µm on internal weld seams. Coating integrity is then checked by ASTM D5162 holiday testing at 1,500 V over the coated bore, with no more than 1 holiday per 10 m². Potable-water compliance is demonstrated by NSF/ANSI 61 Section 4 tank and pipe coatings extraction testing using pH 5 and pH 10 water exposure; where products are used in food-plant process water, FDA 21 CFR 175.300 remains the reference. Terminal products include flanged spool pieces, pump riser pipes, valve bonnets, and dip tubes for municipal and industrial water treatment skids. The operational boundary is that continuous chloramine exposure above 4 mg/L at temperatures above 50 °C induces oxidative degradation of the PA11 surface at a rate that is not fully covered by published data for this specific grade; therefore service trials are advised for chloraminated hot water loops.
Rilsan T NAT 2P PA11 is compounded as a 98.5–99.5 wt% single-component base powder with 0.3–0.7 wt% hindered phenol antioxidant and 0.1–0.3 wt% phosphate adhesion promoter for offshore access ladders and safety gratings; the additive package is selected to avoid zinc stearate, which can reduce adhesion to galvanized substrates after salt spray aging. The process begins with solvent degreasing of prefabricated steel ladders, followed by sweep blasting to SA 2 without damaging the hot-dip galvanizing layer; the powder is applied by fluidized bed dip coating after preheating to 230–250 °C, producing a nominal dry film thickness of 300–450 µm over weld fillets and open rungs. Post-fusion is carried out for 4–6 min at 200–215 °C, and cooling is controlled to 2–3 °C/min between 160 °C and 120 °C to avoid quench cracking at sharp rung intersections. The qualification program for offshore service references ISO 20340 cyclic ageing with 25 weeks exposure, including UV, salt spray, and condensation cycles, followed by adhesion testing per ISO 4624 with a minimum pull-off of 5 MPa and chalking rating per ISO 4628-6 not below 1. Terminal products include offshore access ladders, grating treads, handrails, and small structural attachments on helidecks. The operational limitation is that contact with aromatic hydrocarbon solvents above 40 °C, such as xylene or toluene, causes swelling and must be avoided; published data for this specific grade in continuous aviation fuel immersion is limited, and compatibility testing according to ISO 2812-1 is required before specifying the coating on fuel-handling structures.
Competitive Arkema Rilsan Fine Powders T NAT 2P PA11 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!
Arkema Rilsan Fine Powders T NAT 2P is a natural, unpigmented polyamide 11 powder formulated for dry coating deposition by electrostatic spray and fluidised-bed immersion. The polymer is synthesised from 11-aminoundecanoic acid of castor-oil origin; the unpigmented designation NAT indicates that the powder contains no chromatic pigment loading, which reduces variables associated with pigment dispersion and maintains consistent dielectric response during corona charging. The grade is specified for metal components that require a fused film with low coefficient of friction, typically 0.15–0.20 per ASTM D1894-14, resistance to stress cracking in dilute acids and alkalis, and sufficient impact toughness at low temperature. Typical application segments include dishwasher baskets, automotive tubing clips, valve springs, cable tray hardware, and industrial hanger brackets. The powder is charged by negative corona at 60–80 kV and projected onto a grounded substrate; in fluidised-bed lines, preheated parts are immersed into a cloud of powder fluidised by dried compressed air at a dew point no higher than −20 °C. The film fuses at 183–187 °C to a dense polyamide 11 coating. Because the material is a thermoplastic rather than a thermoset, overspray can be reclaimed when vibratory sieving eliminates foreign particulate above 250 µm. The grade is not interchangeable with extrusion or injection-moulding PA11 pellets. Pellets are specified by viscosity number according to ISO 307 and processed in single-screw or twin-screw extruders with L/D ratios above 24:1; the powder is specified by particle-size distribution and applied as a dry film. Attempts to feed T NAT 2P through the main throat of a single-screw extruder without a crammer lead to bridging and starve feeding because the bulk density is approximately 0.52–0.58 g/cm³.
In electrostatic deposition, the performance of Rilsan Fine Powders T NAT 2P is governed by the particle-size distribution. Laser diffraction measurements per ISO 13320-1:2020 typically place the median diameter D50 in the 100–120 µm range, with D90 below 200 µm. Fines below 10 µm must remain controlled because excessive fines increase moisture adsorption per unit mass and reduce flowability through Venturi injectors. Conversely, oversize particles above 250 µm can cause “orange peel” in films thinner than 150 µm. The electrostatic charge-to-mass ratio of a powder is inversely related to particle diameter, so a narrow distribution stabilises the electric field within the powder cloud. Production-scale electrostatic booths operating at flow rates of 3–6 kg/h per gun require fluidisation air at 1.5–2.5 bar; if the distribution broadens, powder output varies by more than 10% and transfer efficiency drops. The grade is therefore screened through vibratory sieves with mesh aperture 180–250 µm before reclaim. This control is absent in general-purpose extrusion-grade PA11 pellets, whose particle size is not relevant to film formation.
On high-volume dishwasher-basket lines, fluidised-bed coating with T NAT 2P follows a defined thermal sequence. The steel basket is phosphated and dried, then preheated in a convection oven to 300–320 °C. The preheat temperature exceeds the polyamide 11 melting peak by roughly 130 °C to provide sufficient thermal mass for fusion after immersion. The basket is dipped for 2–5 s; powder adheres to the hot metal surface, begins melting, and continues to flow into a continuous film after withdrawal. Gelation is completed in a post-heat tunnel at 200–220 °C for 3–5 min. Film thickness is normally controlled from 200–400 µm. On high-volume lines, the critical failure modes are entrapped air caused by outgassing from phosphate pores and edge coverage loss at sharp basket corners. When the coating thickness falls below 150 µm, pinholing after 500 h of neutral salt spray per ISO 9227:2022 is observed on zinc-phosphated steel. The fine powder is therefore not recommended for film thickness below 150 µm in detergent-containing environments. In pigmented grades, additional film thickness may be required for equivalent salt-spray protection because pigment particles alter melt rheology and can act as local stress concentrators during impact. For automotive tubing clips and valve springs, the same grade is applied electrostatically at film thickness 100–200 µm to prevent metal-to-metal wear; salt-spray resistance is validated per ISO 9227 and adhesion is checked by cross-cut per ISO 2409:2020. Trials on zinc-phosphated steel with 200 µm film show scribe creep under 2 mm after 1,000 h neutral salt spray per ISO 9227 when the coating is defect-free; edge coverage remains the limiting variable on stamped geometries.
After powder contact on a zinc-phosphated steel substrate, the melting peak of T NAT 2P, determined by differential scanning calorimetry under ISO 11357-3:2018, lies between 183 °C and 187 °C. Crystallisation on cooling begins near 150–160 °C, which defines the practical lower limit for levelling before solidification freezes the surface texture. The fusion window is narrow: if the metal surface cools below 178 °C before powder contact, wetting is incomplete and voids remain at the coating-substrate interface; if the surface exceeds 340 °C for more than 2 min, oxidative yellowing and chain scission increase the melt viscosity and reduce adhesion. The melt film is therefore maintained within ±5 °C of the target preheat. Fused film density is 1.03–1.05 g/cm³ per ISO 1183-1:2019, and Shore D hardness after fusion is typically 62–68 per ISO 868:2003. The coefficient of friction against polished steel, tested per ASTM D1894-14, is commonly 0.15–0.20. These values support use in sliding and impact applications where a nylon 11 coating reduces noise and prevents metal-to-metal wear. Parts must be handled above the crystallisation onset until the film has levelled; quench cooling below this range accelerates crystallinity and can reduce gloss. The limitation is temperature: continuous exposure above 120–130 °C in air causes progressive oxidative embrittlement, and published data for this specific configuration are limited.
For coaters selecting between polyamide 11 and polyamide 12 powders, the principal differences are thermal, chemical, and rheological. Polyamide 11 derived from castor oil has a higher melting peak than typical polyamide 12 powders; this raises the required preheat temperature but gives the fused coating greater retention of mechanical properties at elevated temperature. The density of PA11 is slightly higher than that of PA12, which affects powder transport and transfer efficiency. PA11 also shows higher water absorption at saturation, but its renewable carbon content is substantially higher because the monomer is obtained from castor oil rather than petrochemical laurolactam. The T NAT 2P grade is unpigmented; black or blue Rilsan T grades contain pigment masterbatches that lower volume resistivity and require rebalancing of electrostatic gun voltage. The following table summarises typical comparative values.
| Property | Rilsan Fine Powders T NAT 2P PA11 | Polyamide 12 fine powder, typical | Standard |
|---|---|---|---|
| Melting peak | 183–187 °C | 170–178 °C | ISO 11357-3 |
| Fused film density | 1.03–1.05 g/cm³ | 1.00–1.01 g/cm³ | ISO 1183-1 |
| Water absorption at saturation | 1.7–1.9 % | 1.4–1.5 % | ISO 62 |
| Shore D hardness after fusion | 62–68 | 60–65 | ISO 868 |
| Fluidised-bed preheat | 300–320 °C | 250–290 °C | equipment process data |
| Bio-based carbon content | castor-oil source, high | petrochemical source, low | ASTM D6866 |
In high-humidity coating halls, moisture uptake before processing becomes a hard processing boundary. Dry powder can be transported in closed hoppers, but exposure to relative humidity above 60 % for more than 8 h raises surface moisture content to levels that produce fluidisation spitting and uneven charging. Pre-drying is performed in desiccant or vacuum dryers at 80–90 °C for 4–6 h to reduce moisture below 0.1 %, measured by Karl Fischer titration per ISO 15512:2019. Moisture trapped in the powder during fusion creates steam pores; at film thickness below 200 µm, the pores can penetrate to the substrate and compromise salt-spray resistance. The powder should not be stored in open containers adjacent to curing ovens because cycled humidity condenses on cold powder surfaces and accelerates agglomeration. In high-humidity production buildings, closed-loop reclaim lines with silica-gel dehumidification keep the circulating air below 10 % relative humidity. When these conditions cannot be maintained, the grade may require longer drying than lot-averaged data suggest. Reclaim powder that has passed through the booth more than three times may accumulate fine particulate; screen classification every shift is used to keep D50 within lot specification. Published data for this specific configuration are limited for open-hopper operations in tropical climates, so coaters validate moisture content per shift.
For regulatory classification, the base resin in T NAT 2P is a polyamide 11 homopolymer. For food-contact use, coatings may be formulated and applied so that the final article meets FDA 21 CFR 177.1500 and Regulation (EU) No 10/2011 migration limits when the coating is not in direct contact with fatty foods above 120 °C. The natural grade contains no lead-cadmium pigments; compliance with RoHS Directive 2011/65/EU requires verification of raw-material trace metals below 0.1 % for lead, mercury, hexavalent chromium, and PBB/PBDE flame retardants. Under REACH Regulation (EC) No 1907/2006, the grade is supplied as a polymer article, and no monomer registration above the notification threshold is applicable if residual monomer remains below 0.1 %. The following table lists the principal compliance anchors.
| Regulatory area | Designation | Application condition |
|---|---|---|
| Food contact polymer | FDA 21 CFR 177.1500 | repeat-use coating, end-test requirement |
| European food contact | Regulation (EU) No 10/2011 | overall migration ≤ 10 mg/dm² |
| RoHS | Directive 2011/65/EU | heavy metal < 0.1 % |
| REACH | Regulation (EC) No 1907/2006 | polymer, no SVHC > 0.1 % |
| Bio-based carbon | ASTM D6866 | castor-oil-derived carbon measurement |