|
HS Code |
106761 |
| Chemical Formula | C16H8Cl2N2O2 |
| Molecular Weight | 329.15 |
| Appearance | Solid (usually) |
| Color | Typically has a certain color depending on purity (like pale yellow - brownish) |
| Melting Point | Specific value depending on purity, usually in a certain range |
| Boiling Point | Decomposes before boiling in normal conditions |
| Solubility | Poorly soluble in water, soluble in some organic solvents like DMF, DMSO |
| Density | A specific density value related to its solid state |
| Stability | Stable under normal conditions but can react with strong oxidizing or reducing agents |
| Pka | Has relevant pKa values for acidic or basic functional groups if applicable |
As an accredited 3,6-Bis(4-Chlorophenyl)-2,5-Dihydropyrrolo[3,4-C]Pyrrole-1,4-Dione factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Packaged in 100 - gram containers: 3,6 - Bis(4 - Chlorophenyl)-2,5 - Dihydropyrrolo[3,4 - c]Pyrrole - 1,4 - Dione. |
| Shipping | Ship 3,6 - Bis(4 - Chlorophenyl)-2,5 - Dihydropyrrolo[3,4 - c]Pyrrole - 1,4 - Dione in sealed, corrosion - resistant containers. Ensure proper labeling for chemicals. Ship via approved carriers following hazardous material shipping regulations. |
| Storage | Store "3,6 - Bis(4 - Chlorophenyl)-2,5 - Dihydropyrrolo[3,4 - c]Pyrrole - 1,4 - Dione" in a cool, dry place away from direct sunlight. Keep it in a tightly - sealed container to prevent moisture absorption and potential reaction with air components. Avoid storing near incompatible substances to ensure its chemical stability over time. |
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Achieving optimal dispersion of 3,6-bis(4-chlorophenyl)-2,5-dihydropyrrolo[3,4-c]pyrrole-1,4-dione (C.I. Pigment Red 255) in polyester/triglycidyl isocyanurate (TGIC) powder coatings begins with the control of specific energy input on a co-rotating twin-screw extruder configured at an L/D ratio of 24:1 to 28:1. The extruder barrel temperature profile, typically set between 90 °C and 110 °C, must remain below the onset of premature TGIC crosslinking while still achieving a melt viscosity low enough to de-agglomerate the pigment’s primary crystallites to a Hegman fineness below 12 µm. The compound is subsequently dry-blended with an acrylic or polyester clear binder and milled to a particle size distribution where 90% of the volume is ≤ 50 µm, using an air classifier mill, which influences both electrostatic application uniformity and film smoothness. In hydroxyalkylamide (HAA) curing variants, the pigment’s chlorophenyl substituents introduce a subtle catalytic surface activity that can accelerate yellowing if the stoving schedule exceeds 200 °C for more than 15 minutes; therefore, film builds are restricted below 80 µm when bonding temperatures approach 205 °C. Published automotive-specification Florida exposure data for PR255 monocoats, measured according to ISO 11341:2022 using a xenon-arc lamp with a 340 nm cut-on filter, indicate a total colour change ΔE*ab of less than 3.0 after 5000 kJ/m² when the pigment loading is maintained between 0.8 wt% and 1.2 wt% relative to total binder solids. This outdoor durability makes it suitable for architectural aluminium profiles certified under Qualicoat Class 2 and AAMA 2604 specifications, where single-pigment shading systems rely on its clean yellowish-red hue to avoid metamerism under daylight D65 and fluorescent TL84 illuminants. Operational boundaries are pronounced: relative humidity exceeding 60% during powder electrostatic application leads to moisture adsorption on the pigment surface, increasing film resistivity and producing a mottled finish; pre-conditioning of the reclaimed powder at 40 °C for 4 hours is mandatory in production environments without climate control. Further, combination with zinc-rich anticorrosive primers must be avoided because cathodic disbondment at scribe lines can accelerate darkening via quinoid-to-aromatic redox transitions at the pigment–metal interface, a phenomenon documented in ISO 12944-6 cyclic ageing protocols. What Limits the Use of 3,6-Bis(4-Chlorophenyl)-2,5-Dihydropyrrolo[3,4-C]Pyrrole-1,4-Dione in Solventborne Single-Layer Topcoats?The primary constraint is not photodegradation but rather the pigment’s tendency to recrystallise in weak solvents during flash-off when the basecoat is formulated above the critical pigment volume concentration (CPVC) without an effective steric stabiliser. In OEM production lines applying a polyurethane or polyacrylate-melamine clear-over-base system, a dispersed pigment concentrate is passed through a horizontal bead mill charged with yttria-stabilised zirconia beads of 0.3–0.5 mm diameter at a peripheral disc speed of 10–12 m/s. The millbase vehicle, often a blend of aldehyde resin and a high-molecular-weight polyurethane dispersant with an amine value below 5 mg KOH/g, ensures rheological compatibility with the let-down polyester. The final basecoat carries between 0.3 wt% and 0.8 wt% of PR255 on total solids, and its viscosity, adjusted to 18–25 seconds in a DIN 4 flow cup at 23 °C, dictates transfer efficiency on high-speed rotary bell atomisers turning at 40,000–60,000 rpm. A Hegman grind gauge reading finer than 5 µm (ISO 1524:2023) is verified before let-down because any residual aggregates serve as nuclei for colour drift during the three-month shelf-life stabilisation period required by tier-1 automotive suppliers. In single-layer industrial topcoats, the absence of a clearcoat exposes the pigment directly to acid rain hydrolysis and abrasion; data generated using SAE J2527 (xenon arc with daylight-B/B optical filter, 0.55 W/m² at 340 nm) indicate that the addition of a hindered amine light stabiliser at 1.0% on binder can suppress gloss loss from 30% to below 15% after 2000 hours, but only if the pigment’s surface is pre-treated with a silane coupling agent to minimise free-chloride photorelease, which otherwise degrades the HALS. Visual match under illuminant D65 for a tri-coat red is achieved with a metamerism index MID65 < 1.0, yet the chlorophenyl groups shift the reflectance curve toward longer wavelengths compared to C.I. Pigment Red 254, rendering the pigment unsuitable for formulations that must simultaneously meet both high chroma and hiding power below 15 µm dry film thickness. Fibre-grade Polypropylene Colouration and Shrinkage Anisotropy PhenomenaWhen PR255 is processed as a masterbatch in polypropylene homopolymer on a twin-screw extruder with barrel zones profiled from 190 °C at the feed throat to 230 °C at the die, the pigment acts as an efficient heterogeneous nucleating agent, raising the crystallisation onset temperature from approximately 115 °C to 125–128 °C as measured by differential scanning calorimetry at a cooling rate of 10 K/min (ISO 11357-3:2018). This accelerated nucleation, particularly pronounced at let-down pigment concentrations as low as 0.1 wt%, generates a transcrystalline morphology that induces differential shrinkage: injection-moulded tensile bars exhibit a mould-direction contraction of 1.8–2.2% versus 1.2–1.4% in the transverse direction per ISO 294-4:2018, causing bowing in flat-article moulds with a length-to-thickness ratio exceeding 50:1. Fibre spinning is similarly affected; melt-blown grade PP (MFI 800 g/10 min at 230 °C/2.16 kg, ISO 1133-1:2022) with 0.15 wt% PR255 added via a compounded pellet exhibits an increase in birefringence retardation at the take-up godet, which compromises nonwoven fabric uniformity unless the pigment surface is passivated with a 0.5–1.0 µm layer of a low-molecular-weight polyethylene wax during the flush-paste stage. Production-scale evidence shows that stable fibre spinning at a spin-draw ratio of 3.5 and a line speed of 2500 m/min is achievable only when the masterbatch’s pigment content is limited to 30% by weight; higher loadings produce filter pack pressure build-up beyond 120 bar after 4 hours of continuous operation. In thin-wall food packaging applications regulated under Commission Regulation (EU) No 10/2011, overall migration into 10% ethanol at 40 °C for 10 days (EN 1186-1:2002) falls below the 10 mg/dm² intervention limit for well-dispersed PR255, but such compliance is negated if processing residence time exceeds 5 minutes, as shear-induced decomposition generates trace chlorinated aromatics detectable by headspace GC-MS above the 0.1 µg/L threshold. In high-speed coil coating lines, pigment dispersion stability during rapid solvent evaporation determines colour consistency.The application of a polyester-melamine topcoat containing PR255 onto a moving flat metal substrate at a line velocity of 120–160 m/min demands pigment aggregates below 1 µm to prevent shade drift as the peak metal temperature reaches 232–249 °C within 30 seconds. A pigment paste pre-dispersed in a combination of phthalate-free plasticiser and isophorone at a weight ratio of 1:0.6 on pigment is let down into a high-solids polyester resin with a hydroxyl value of 40–60 mg KOH/g, and the resultant coating, applied at a wet film thickness of 65–75 µm, is tested for overbake stability using a 300 °C oven hold for double the nominal cure time per ASTM D2454-18. Instrumental colour readings at 10° observer for specular-included measurements reveal that PR255 maintains an ΔE* below 1.2 versus the standard bake, outperforming many perylene maroons that shift yellow under the same conditions, but the margin narrows to ΔE 2.5 when the substrate is hot-dip galvanised steel with a zinc phosphate pretreatment that releases residual alkali. EN 13523-10:2017 xenon-arc exposure of a clear-over-pigmented rig, with a radiant exposure of 4000 MJ/m² behind 3 mm glass, confirms a chalking rating of 0 (ISO 4628-6:2016) and a gloss retention above 85% at a 60° geometry. Migration issues in polyvinylidene fluoride (PVdF) topcoats containing 70% PVdF resin and 30% acrylic modifier are managed by limiting free chloride content in the pigment to below 100 ppm (Ion Chromatography, ISO 10304-1:2023), a specification critical for avoiding catalytic dehydrohalogenation of the fluoropolymer during panel-forming operations. Production lines utilising a Gravure kiss-coat head with engraving of 50 lines/cm demonstrate consistent dry film colour when the pigment-specific circulation pump returns the paint to the holding tank at a shear rate below 10,000 s⁻¹, preventing transient thixotropic structure breakdown that would otherwise deposit macro-aggregates at the reversal doctor blade. Solvent-based ink formulations for exterior signage and decorative laminates incorporate 3,6-bis(4-chlorophenyl)-2,5-dihydropyrrolo[3,4-c]pyrrole-1,4-dione at loadings of 5–15 wt% in the dispersion base, milled on a triple-roll mill with water-cooled chrome-plated steel rolls set to a hydraulic pressure of 12–15 MPa and a frontal nip gap of 15–25 µm to achieve a transparency index suitable for process printing. The pigment’s high resistance to migration, assessed by EN 645:1993 contact tests with modified polyphenylene oxide (Tenax) at 60 °C for 10 days, allows its use in indirect food contact printing on packaging outer layers, although the chlorophenyl substituents depress solubility in acrylate-based UV-curable monomers; drop-on-demand piezoelectric printheads operating at 20 kHz experience nozzle deviation rates above 0.1% when pigment particle size exceeds 0.5 µm Dv90 as measured by dynamic light scattering (ISO 22412:2017). Re-solubility in a nitrocellulose/ethanol/isopropyl acetate solvent blend at a solvent-to-resin ratio of 3.5:1 remains acceptable for gravure line speeds over 200 m/min, provided that residual hypophosphorous acid from the pigment synthesis is neutralised to a pH of 5.5–6.5, as acid-catalysed esterification with the binder’s free hydroxyl groups otherwise raises the apparent viscosity beyond the target 18–25 mPa·s at 23 °C and 2500 s⁻¹. When Flame-Retardant Additives Interact with DPP Chromophores in ABS Injection MouldingInjection moulding of acrylonitrile-butadiene-styrene (ABS) coloured with PR255 for electronic equipment housings compliant with IEC 62368-1 fire enclosure requirements introduces a colour stability risk arising from the brominated epoxy or phosphate ester flame retardants packaged at loadings of 12–18 wt%. On a moulding line with a clamping force of 1600 kN, barrel nozzle temperatures set to 240–260 °C, and a holding pressure of 800–1000 bar, the melt residence time must be kept below 3 minutes to limit the generation of hydrogen halide species that cause a hypsochromic shift, shifting the red shade towards a dull maroon measurable as a Δa* value of −2.5 or more versus the virgin compound (CIELAB D65/10°, specular excluded). Pre-drying the pigment and the base resin to a moisture content below 0.03% using a desiccant dryer with a dew point of −40 °C for 4 hours at 80 °C is critical: entrapped water vapour hydrolyses polybrominated diphenyl ether alternatives, forming acidic byproducts that attack the particle surface. A single-screw reciprocating machine fitted with a three-zone general-purpose screw of an L/D ratio of 20:1 and a compression ratio of 2.5:1 yields consistent colour at a back pressure of 5–10 bar when PR255 is dosed as a 1% masterbatch in a styrenic carrier; direct addition of dry pigment powder at the hopper causes ejection of fines from the vent port and results in ultimate ΔE variation of ±1.5 across a 48-cavity hot-runner system. In automotive interior applications requiring compliance with DIN 75200 fogging standard (reflectometric method, 100 °C for 6 hours), the use of a sterically hindered phenolic antioxidant in synergy with the flame retardant does not induce blooming of the chlorinated DPP chromophore, as confirmed by Fourier-transform infrared spectroscopy of hexane washings.
Calender-grade flexible polyvinyl chloride films pigmented with 0.05 wt% PR255 for garden furniture exhibit no warp in shade upon accelerated QUV-B 313 testing per ISO 4892-3:2016, provided epoxidised soybean oil stabiliser levels remain below 5 phr to avoid solubilisation of the pigment surface. |
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3,6-Bis(4-Chlorophenyl)-2,5-Dihydropyrrolo[3,4-C]Pyrrole-1,4-Dione, listed on the Colour Index as C.I. Pigment Red 254 and identified by CAS 84632-65-5, represents one of the most commercially significant diketopyrrolopyrrole (DPP) chromophores in high-performance organic pigment portfolios. Commercial grades — including products such as Irgazin DPP Red BO and other DPP Red BTR-type modifications — deliver a clean, highly saturated yellowish red mass tone with strong absorption in the visible spectrum centred near 550 nm. In automotive OEM basecoat/clearcoat systems, powder coatings, and rigid PVC extrusion, the pigment is selected for its excellent migration fastness, high chroma, and capacity to retain colour integrity under long-term outdoor exposure. Its balance of opacity and tinting strength, combined with a well‑characterised behaviour across common binder chemistries, distinguishes it from earlier perylene‑ or quinacridone‑based reds, while requiring careful matching of dispersion equipment and processing parameters to exploit the full colouristic potential without generating filter blockages or hue drift in melt‑processed polymers.
The 2,5‑dihydropyrrolo[3,4‑c]pyrrole‑1,4‑dione core is an electron‑deficient, rigid bicyclic system; the frontier orbital energies and consequently the absorption band position are directly modulated by the nature of the aryl residues at the 3‑ and 6‑positions. With 4‑chlorophenyl substituents, the compound exhibits a hypsochromic shift relative to unsubstituted phenyl analogues, while the electron‑withdrawing character of the chlorine atom raises the oxidation potential and contributes to photochemical stability. The resulting hue angle in full shade, when measured by a spectrophotometer over a white background in an alkydmelamine stoving enamel, typically falls between 30° and 36°, with chroma C* values exceeding 70 at a pigment volume concentration of 10%. This differentiates the product sharply from 3,6‑bis(4‑cyanophenyl)‑DPP (C.I. Pigment Red 255), where the stronger electron‑withdrawing nitrile group shifts the absorption hypsochromically further, producing a bluer, more magenta‑biased red with chroma approximately 10‑15% lower under identical test conditions per DIN EN ISO 18314‑3. Conversely, C.I. Pigment Orange 73, bearing 4‑methylphenyl groups, exhibits a bathochromic shift and delivers an orange masstone with markedly reduced fastness to light and weathering. The precise positioning of the chlorine substituent also influences the agglomerate strength distribution owing to altered surface energy, a parameter that directly affects dispersibility in bead milling and twin‑screw compounding operations.
Commercial grades of Pigment Red 254 are supplied as finely divided powders with a specific surface area (BET nitrogen adsorption, ISO 4652) typically in the range 45–65 m²/g and oil absorption (ASTM D281) of 50–70 g/100g. The median particle size by transmission electron microscopy or dynamic light scattering is centred around 0.07–0.12 µm, with the exact value tuned by post‑synthesis conditioning to optimise between transparency for metallic effect coatings and hiding power for solid‑shade coil coatings. Residue on a 45 µm sieve per ISO 787‑18 must remain below 0.1% to avoid visible speckling in thin‑film applications. The tinting strength, determined by the relative colour yield method of ISO 787‑24 using a masterbatch diluted to 1:100 with titanium dioxide in a long‑oil alkyd system, is routinely specified to fall within ±5% of the standard batch. Achieving this reproducibility at production scale requires bead mills with a specific energy input exceeding 0.08 kWh/kg pigment and three‑roll mills set to a nip gap below 5 µm. In high‑speed dispersers, a Hegman grind gauge reading (ASTM D1210) of 7+ on a North Standard scale is the minimal acceptance criterion for automotive topcoat intermediates, with the final let‑down stage demanding no residual agglomerates larger than 10 µm as determined by optical microscopy on a draw‑down sample.
| Property | Specification / Typical Range | Test Method |
|---|---|---|
| Molecular formula | C₁₈H₁₀Cl₂N₂O₂ | — |
| Molar mass | 357.2 g/mol | Calculated |
| Melting / decomposition | Decomposes above 340°C | DSC, ISO 11357‑1 |
| Density (25°C) | 1.54 g/cm³ | ISO 787‑2 |
| Oil absorption | 55–65 g/100g | ASTM D281 |
| Specific surface area (BET) | 50–60 m²/g | ISO 4652 |
| pH of aqueous extract (10% slurry) | 6.5–7.5 | ISO 787‑9 |
| Residue on 45 µm sieve | ≤0.05% | ISO 787‑18 |
| Heavy metals (Pb, Cd, Hg, CrVI) | <100 ppm total | EN 71‑3 (migration), REACH Annex XVII |
The compound is supplied under various article models differentiated by primary crystal size and surface treatment. A fine‑particle grade optimised for high‑transparency waterborne basecoats exhibits a BET surface area of 65–70 m²/g and a Hegman dispersibility of 8 after 60 min bead milling in an aqueous acrylic‑polyurethane grinding medium with a pigment loading of 25 wt%. A coarse‑particle version targeting heavy‑duty industrial enamels with maximum hiding power is controlled by milling to a narrower crystallite size distribution with d₅₀ near 0.15 µm and oil absorption held below 55 g/100g to minimise solvent demand. Such physical specification differences yield a covering power variation of up to 30% when assessed by the contrast‑ratio method of ISO 6504‑3 at 20 µm dry film thickness. In terms of regulatory compliance, all common commercial versions meet the purity criteria of EU Directive 94/62/EC for heavy metals and are compliant with FDA 21 CFR §178.3297 for colorants in polymers intended for repeated‑use food contact articles, although migration limits in specific food simulants must be verified for each compound formulation.
In the application window for automotive solid‑shade basecoats, the pigment is typically predispersed into a cellulose acetate butyrate (CAB)‑acrylic grinding base at a pigment‑to‑binder ratio of 1:2.5 using a horizontal bead mill charged with 0.8–1.0 mm yttria‑stabilised zirconia beads. The mill base is then tinted into a clearcoat binder system containing aminoplast crosslinkers and acid catalyst. Cure schedules of 20 min at 140°C produce no significant color drift, and the final coating exhibits a 20° gloss of 90+ and distinctness‑of‑image (DOI) retention without surface haze. Differences from high‑performance inorganic alternatives such as encapsulated cadmium red become evident in the temperature‑controlled curing of waterborne basecoat‑clearcoat systems on mixed‑substrate car bodies: whereas cadmium sulfoselenide pigments can exhibit a colour burn‑back of ΔE*ᵃᵇ > 2.0 after overbake at 160°C/30 min, Pigment Red 254 maintains a change of less than 0.5 CIELAB units, measured by instrument geometry d/8° and specular included per ASTM D2244.
Production-scale manufacture of single‑pigment masterbatches in polyethylene or polypropylene is routinely carried out on co‑rotating twin‑screw extruders with an L/D ratio of 40:1 to 48:1 and specific torque density above 11 Nm/cm³. Pigment Red 254 is introduced via side‑stuffing at 40% loading; melt temperatures are tightly controlled in the range 200–230°C for LDPE and 220–250°C for PP. Under these conditions, filter pressure value (FPV) monitoring according to DIN EN 13900‑6 through a screen pack of 400 mesh provides a direct readout of dispersion quality: a well‑dispersed lot sustains a pressure rise of less than 0.3 bar/(g·cm⁻²), whereas a poorly dispersed batch leads to rapid screen blinding and pressure excursions exceeding 1.0 bar/(g·cm⁻²) within 30 min, requiring a line stop. The pigment’s intrinsic thermal stability in polyolefins permits short‑term exposure of 5 min at 300°C without mass‑tone degradation, and injection‑moulded colour plaques measured against a standard exhibit ΔE*ᵃᵇ < 1.0 when processed with a melt residence time up to 8 min at 280°C. By contrast, DPP‑based Pigment Red 255, while offering a bluer red shade, exhibits perceptible colour drift at 280°C in the same HDPE grade, with ΔE* > 1.5 appearing after 5 min. This difference makes Pigment Red 254 the preferred choice for blow‑moulded coloured transport packaging where cycle‑to‑cycle thermal history varies.
An important processing boundary arises in engineering thermoplastics containing reactive end‑groups. Published evidence from laboratory‑scale compounding trials confirms that exposure to polyamide 6,6 at melt temperatures above 260°C for durations exceeding 4 min leads to a gradual loss of chroma and a shift in hue angle of +2–4°, attributed to nucleophilic attack by terminal amine groups on the DPP carbonyl moieties. Consequently, Pigment Red 254 is not recommended for unreinforced polyamide injection‑moulded parts where visual colour consistency must be maintained after regrind re‑processing. In such matrices, quinacridone magenta (C.I. Pigment Red 122) or a suitably stabilised perylene maroon (C.I. Pigment Red 179) provides substantially better melt‑phase chemical resilience, albeit at a higher raw material cost per kilogram and with a trade‑off in yellow‑biased red purity.
Full‑shade and reduction drawdowns subjected to xenon‑arc radiation under cycle A of ISO 4892‑2 (daylight filter, irradiance 0.55 W/m² at 340 nm, chamber temperature 65°C, relative humidity 50%) reveal exceptionally high photostability. After 3000 h exposure, acrylic‑melamine crosslinked enamels formulated with Pigment Red 254 at a 20:80 TiO₂ reduction ratio yield ΔE*₀₀ values < 1.0 and show no evidence of chalking or gloss loss beyond 10% of the initial 60° gloss. In polyester‑based powder coatings cured with triglycidyl isocyanurate (TGIC) at 200°C/10 min, 12‑month Florida outdoor exposure (5° south, black box) produces a colour shift of less than 1.2 ΔE*ᵃᵇ, with the pigmented film maintaining flexibility and intercoat adhesion. This performance places the pigment on par with perylene reds and significantly above conventional naphthol AS reds such as Pigment Red 170, which under identical Florida conditions typically record ΔE* > 4.0 and notable gloss deterioration after 18 months. Compared to the quinacridone line, Pigment Red 254 matches the Blue Wool scale ratings of 8 (full shade) and 7–8 (1:10 reduction) but achieves substantially higher chroma in the yellow‑red region, an advantage exploited in premium automotive styling hues requiring high flop index alongside long‑term colour fidelity.
A documented limitation is the pigment’s susceptibility to alkaline environments. Immersion tests based on ASTM D1308 (20°C, 24 h, 5% sodium hydroxide solution) consistently produce visual lightening and a loss of chroma exceeding 3 CIELAB units, accompanied by a measurable decrease in film micro‑hardness if the binder does not form a sufficient barrier. Therefore, Pigment Red 254 is excluded from direct‑to‑concrete or alkaline plaster coatings unless a chemically resistant primer layer isolates the pigment from the substrate. In coil coating applications where a chromate‑free pretreatment bath raises the pH at the metal‑coating interface, extended humidity testing per ISO 6270‑2 has revealed isolated instances of adhesion loss attributable to pigment‑binder interface degradation; those cases are routinely mitigated by introducing a thin (5–8 µm) epoxy blocking layer between pretreatment and colour coat.
| Pigment | C.I. Number | Hue Angle h° (approx., full shade) | Chroma C* (approx., full shade) | Lightfastness (Blue Wool, masstone/reduction) | Heat Stability in HDPE (°C/5 min) | Migration Fastness in PVC (ISO 18314) |
|---|---|---|---|---|---|---|
| DPP Red 254 | Pigment Red 254 | 34° | 72 | 8 / 7‑8 | 300 | 5 |
| DPP Red 255 | Pigment Red 255 | 28° | 63 | 8 / 7‑8 | 280 | 5 |
| Quinacridone magenta | Pigment Red 122 | 3° | 48 | 8 / 8 | 300 | 5 |
| Perylene maroon | Pigment Red 179 | 12° | 54 | 8 / 8 | 320 | 5 |
The shift toward more environmentally stringent automotive coating lines, which increasingly employ waterborne basecoat formulations with low volatile organic content, has placed additional demands on pigment dispersibility and stability. In highly alkaline waterborne systems stabilised with dimethyl amino ethanol at pH 8.5–9.0, early commercial lots of Pigment Red 254 showed a rheology instability during storage, with viscosity rises exceeding 30% after 28 days at 40°C. Later grades treated with a polymeric dispersant shell incorporating a sterically stabilising polyether segment resolved the issue, maintaining a mill base viscosity of 800–1200 mPa·s at 100 s⁻¹ across the entire shelf‑life period. Thus, the choice of grade model in conjunction with the dispersant chemistry is a determining factor for robust industrial application, and direct substitution of a standard solventborne grade into a high‑pH waterborne system without prior qualification invariably results in colour flocculation or gloss reduction in the cured film.
When benchmarked against perylene maroon in automotive interior trim specifications requiring low‑glare, soft‑feel surfaces, Pigment Red 254 provides superior brightness and yellow‑red chromatic definition at equal pigment loading, but its higher oil absorption increases the required matting agent dose by approximately 15% to meet a 2‑gloss‑unit surface at 60°. This translates into a slight productivity penalty in two‑component polyurethane soft‑feel paints applied with robotic spray equipment; published data for this specific configuration is limited, and plant‑specific trials with a bell speed of 25,000 rpm and a fluid delivery rate of 200 cc/min have yielded mixed gloss‑uniformity results, particularly on vertical sections. In such high‑demand decorative applications, the technical community continues to evaluate surface‑modified variants of the pigment to lower oil absorption without sacrificing weather fastness or dispersion kinetics.