Bis-(P-Chrolopheny)-1,4-Diketopyrrolo(3,4-C)Pyrrole

Bis-(P-Chrolopheny)-1,4-Diketopyrrolo(3,4-C)Pyrrole


    • Product Name Bis-(P-Chrolopheny)-1,4-Diketopyrrolo(3,4-C)Pyrrole
    • Alias DPP Pigment
    • Einecs 431-890-6
    • Mininmum Order 1 g
    • Factory Site West Ujimqin Banner, Xilingol League, Inner Mongolia, China
    • Price Inquiry sales9@bouling-chem.com
    • Manufacturer Bouling Chemical Co., Limited
    • CONTACT NOW
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    Specifications

    HS Code

    418303

    Chemical Formula C18H8Cl2N2O2
    Molar Mass 355.17 g/mol
    Appearance Red - violet solid
    Melting Point Above 300 °C (decomposes)
    Solubility In Water Insoluble
    Solubility In Organic Solvents Soluble in some polar organic solvents like N,N - dimethylformamide
    Crystal Structure Typically forms crystalline solids
    Optical Property Highly colored, used as a pigment with strong light - fastness
    Thermal Stability Good thermal stability up to decomposition temperature
    Electrical Property Generally considered an insulator

    As an accredited Bis-(P-Chrolopheny)-1,4-Diketopyrrolo(3,4-C)Pyrrole factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing 500g of Bis-(P - Chrolopheny) - 1,4 - Diketopyrrolo(3,4 - C)Pyrrole in airtight plastic bags.
    Shipping Bis-(P -Chlorophenyl)-1,4 -Diketopyrrolo(3,4 -C)Pyrrole is shipped in secure, sealed containers. Compliance with chemical shipping regulations is ensured to prevent leakage and maintain product integrity during transit.
    Storage Bis-(P - Chlorophenyl)-1,4 - Diketopyrrolo(3,4 - C)Pyrrole should be stored in a cool, dry place, away from direct sunlight. Keep it in a well - sealed container to prevent moisture absorption and contact with air, which could potentially lead to degradation. Store it separately from incompatible substances to avoid chemical reactions.
    Application of Bis-(P-Chrolopheny)-1,4-Diketopyrrolo(3,4-C)Pyrrole

    When Temperature Swings Exceed ±3°C Around the Glass Transition of a Clearcoat Matrix

    In monocoat and basecoat/clearcoat systems for automotive exterior finishes, bis-(p-chlorophenyl)-1,4-diketopyrrolo(3,4-c)pyrrole (C.I. Pigment Red 254) is typically dispersed in a saturated polyester or acrylic polyol resin at a pigment-to-binder ratio of 0.15:1 to 0.35:1. The millbase, prepared on a horizontal bead mill with 0.6–0.8 mm yttria-stabilized zirconia beads at a fill ratio of 75–80%, is processed to a fineness of grind below 5 µm as measured per ISO 1524:2020. The fully let-down paint is applied by high-speed rotary bell atomizers at a dry-film thickness of 12–18 µm for basecoat and 35–45 µm for clearcoat, then baked at 140°C for 30 minutes. Panels subjected to accelerated weathering under SAE J2527 (Xenon arc, borosilicate inner and outer filters, 0.55 W/m² at 340 nm, continuous light cycle with intermittent water spray) exhibit DE* < 1.0 after 5000 hours when the formulation incorporates a hindered amine light stabilizer package comprising 1.0 wt% bis(2,2,6,6-tetramethyl-4-piperidyl) sebacate and 0.5 wt% 2-(2-hydroxy-3,5-di-tert-amylphenyl)benzotriazole. Micro-cracking at the clearcoat/pigmented layer interface is observed during field service in Scandinavia and the Middle East when the crosslink density of the clearcoat, expressed as a glass transition temperature measured by dynamic mechanical analysis (DMA, ASTM E1640-18), drops below 85°C; the phenomenon is traced to cyclic moisture ingress and thermal expansion coefficient mismatch between the DPP particle surface and the surrounding melamine-crosslinked matrix. Production trials on a 3800-ton injection molding clamp line for body-colored bumper fascias revealed that pre-drying the compounded thermoplastic olefin masterbatch containing 4.5 wt% PR254 at 90°C for 4 hours in a desiccant dryer with a dew point of  ≤ -40°C eliminated splay defects entirely.Volatile organic compound legislation, specifically the China GB 24409-2020 limits for passenger vehicle coatings and the EU Directive 2004/42/EC Phase II, has pushed a shift toward waterborne basecoats. In an aqueous polyurethane dispersion (PUD) with a minimum film formation temperature of 12°C, the pigment is compatibilized via a styrene-maleic acid copolymer dispersant with an acid value of 190–210 mg KOH/g, dosed at 12% on pigment weight. The let-down shear stability, assessed by a cone-and-plate rheometer sweep from 0.1 s⁻¹ to 1000 s⁻¹, must show no inflection point associated with flocculation; a rise in viscosity exceeding 15% at low shear after 7 days of storage at 50°C indicates inadequate steric stabilization and is cause for batch rejection.

    What Happens When a Diketopyrrolopyrrole Red Endures Polypropylene Fiber Spinning Above 285°C?

    Mass-coloration of polypropylene multifilament yarns for outdoor upholstery and geotextile color coding exploits the exceptional thermal stability of P.R. 254. In a single-screw extruder with a 30:1 L/D ratio and a Maddock mixing section, a masterbatch containing 30 wt% pigment in a metallocene-catalyzed polypropylene random copolymer (MFR 25 g/10 min at 230°C/2.16 kg, ISO 1133-1:2022) is let down to 0.4 wt% final pigment concentration. Barrel zone temperatures are profiled from 210°C (feed) to 285°C (metering) to 280°C (spin pack). The melt is filtered through a 25 µm absolute-rated sintered metal fiber filter disc before passing through a spinneret with 0.3 mm orifices to create 120-denier/48-filament partially oriented yarn (POY). A residence time exceeding 7 minutes in the melt phase at 295°C triggers a hue shift toward a bluish maroon—observable as a Δa* drift of +0.8 units in CIELAB color space—attributed to partial sublimation of trace 4-chlorobenzonitrile reformation byproducts rather than chromophore decomposition. To arrest this drift, a purge protocol involving a linear low-density polyethylene (LLDPE) with a melt index of 0.5 g/10 min is run for 20 minutes at 260°C between color changes.For compliance with Oeko-Tex Standard 100, Annex 4, Class I (articles for babies), the extracted 4-chloroaniline concentration must fall below the 20 mg/kg detection limit when assayed via EN 14362-1:2017 (reductive cleavage with sodium dithionite, GC-MS analysis). This imposes a specification on the incoming pigment that primary aromatic amine residuals remain below 50 ppm. The fabric after 1000 hours of weathering per ISO 105-B04:2023 (Xenon arc, 42 W/m², 300–400 nm) shall exhibit a grey scale rating of at least 4–5 and a lightfastness of 7–8 on the blue wool scale, values routinely achievable without additional UV absorbers when the fiber denier exceeds 150.

    Powder Coating Extrusion and the Critical ±5% Pigment Loading Window

    In triglycidyl isocyanurate (TGIC)-cured polyester powder coatings for architectural aluminum profiles (Qualicoat Class 2), the diketopyrrolopyrrole pigment is pre-mixed with a carboxylated polyester resin (acid value 32–36 mg KOH/g) at loadings between 1.2% and 3.8% by weight of total formulation. The premix is fed into a co-rotating twin-screw extruder with 25 mm screw diameter and 40:1 L/D, operating at a screw speed of 400 rpm and a barrel temperature of 120°C (+5°C in the second heating zone), to ensure a melt temperature measured at the die of 112–116°C. When pigment loading surpasses 4.2%, the melt viscosity increases disproportionately, causing a 15–20 A spike in extruder motor load and the appearance of microgels detectable on a polished, isopropanol-washed panel after curing at 200°C for 10 minutes as pinpoint craters surrounded by a raised rim. The finished powder, sieved through a 140 µm rotary sifter, is applied electrostatically with a corona gun at 60–80 kV to a 60–90 µm dry-film thickness. Florida exposure ( south, direct weather, ISO 2810) for 3 years produces ΔE < 3.0 only if the TGIC-to-resin ratio is kept at 93:7 and the degassing agent (benzoin) is dosed at 0.3–0.5% to prevent pinhole corrosion initiation points.The pigment’s limited dispersibility in high-viscosity, low-shear powder melt poses a specific bottleneck. A separate investigation on a 16 mm parallel twin-screw lab extruder equipped with a slit die rheometer revealed that substituting 20% of the DPP red with a quinacridone magenta (C.I. Pigment Violet 19) lowered the zero-shear viscosity at 130°C by 22% while maintaining the same spectral reflectance at 560 nm, thus allowing continuous operation without torque-limiter trips. Certification under Qualicoat 3.0 requires the cured film to withstand 3000 hours of acetic acid salt spray testing (ISO 9227) with less than 1 mm creepage at the scribe, a criterion that demands a fully encapsulated pigment surface completely wetted by the polyester backbone.Beyond the purely decorative, a specific requirement arises in electrical insulation powder coatings for busbar epoxy-polyester hybrid systems. Here, the dielectric strength measured according to IEC 60243-1 at 500 V/s ramp must remain above 35 kV/mm after immersion in 90°C deionized water for 1000 hours. Ionic residues on the pigment surface, primarily sodium and chloride ions measured by conductometric extraction per DIN 53780-1, shall not exceed 150 µS/cm to avoid catastrophic dielectric failure. This necessitates a final pigment washing step with deionized water of conductivity less than 2 µS/cm until the filtrate conductivity matches the inlet water.

    Does Migration into Fatty Food Simulants Limit This DPP Chromophore in Rigid PVC Food-Contact Articles?

    Incorporating P.R. 254 into unplasticized suspension PVC for blow-molded bottles and calendered sheet intended for repeated contact with aqueous, acidic, and fatty foods demands rigorous compliance with (EU) No 10/2011 on plastic materials and articles intended to come into contact with food. The specific migration limit (SML) for the pigment is not listed individually in Annex I; however, the overall migration limit of 10 mg/dm² of food contact surface area (article 12) applies. Testing according to BS EN 1186-1:2002 with simulant D1 (ethanol 50% v/v) for 10 days at 40°C must yield an overall migration below the limit. The pigment is dosed at 0.05–0.2 wt% in the PVC compound, which is stabilized with a calcium–zinc system at 2.5 phr to avoid heavy metal contamination, and processed on a counter-rotating conical twin-screw extruder with a melt temperature at the adapter of 178–182°C. Color shift toward an orange-red during processing indicates partial dehydrochlorination catalyzed by residual acidic surface groups on the pigment; this is suppressed by adding 0.3 phr of epoxidized soybean oil (ESBO) as an acid scavenger, which itself is subject to an SML of 30 mg/kg for foods for infants and young children.The purity specification for the pigment in food-contact applications includes a primary aromatic amine sum below 10 mg/kg (detection by spectrophotometric method after diazotization and coupling per EUR 24815 EN, 2011), a polychlorinated biphenyl (PCB) content below 25 mg/kg, and a 4-chloroaniline content below 5 mg/kg. A recent enforcement case in a European member state identified a consignment where accelerated testing in 95% ethanol at 60°C for 4 hours yielded extracted matter exceeding the limit by 3.2 mg/dm², traced to low-molecular-weight oligomeric dispersant that had not been fully removed during the pigment finishing step. The corrective action implemented by the toll manufacturer involved a hot isopropanol slurry wash at 70°C for 2 hours followed by filtration through a 0.5 µm membrane before tray drying at 80°C under vacuum. The resulting product exhibited a volatile matter of 0.18% at 105°C (ISO 787-2:1981) and a residue on a 45 µm sieve of less than 0.01%.

    When UV Flexo Ink Rheology Must Remain Newtonian Through a 1200 m/min Press Run

    Narrow-web UV flexographic printing of self-adhesive labels on polypropylene facestock at speeds exceeding 1000 m/min requires a cyanide-free, low-migration red meeting the Nestlé Guidance Note on Packaging Inks (February 2022 revision) and Swiss SR 817.023.21, Annex 6, part A. A triacrylate monomer-based UV ink vehicle (oligomer: trimethylolpropane triacrylate, viscosity 180 mPa·s at 25°C) is loaded with 18–22 wt% of the predispersed DPP pigment paste, which itself is prepared by passing a 35 wt% pigment in ethoxylated trimethylolpropane triacrylate through a triple-roll mill with a front roll temperature maintained at 28–30°C and an apron nip gap of 10 µm. The final ink’s viscosity, measured with a Laray falling-rod viscometer at 2500 s⁻¹, is adjusted to 0.45–0.65 Pa·s by adding the reactive diluent hexanediol diacrylate. On-press, the ink is transferred through an anilox roller with a cell volume of 3.5–4.5 cm³/m² (hexagonal cell geometry, 60 lines/cm) and cured by a gallium-doped mercury vapor lamp array delivering a peak irradiance of 1.8 W/cm² in the UVA band. Radiant energy required for through-cure, determined by a radiometer conforming to ISO 12647-6:2020, must accumulate to at least 120 mJ/cm²; incomplete curing leaves unreacted monomer residues that subsequently migrate through the pressure-sensitive adhesive layer into the packaged chocolate, detected by GC-MS headspace analysis using a Tenax TA trap at 30°C for 30 minutes.A pigment-specific failure mode manifests as build-up of dry, unrewetted pigment agglomerates on the doctor blade chamber, causing streaks visible as 0.2–0.8 mm wide unprinted lines on the substrate. This is mitigated by incorporating 1.5–2.0% of a high-molecular-weight hyperdispersant with an amine anchoring group (amine value 20–25 mg KOH/g) and maintaining the chamber seal solvent (ethoxy propanol) flowrate at 150 mL/hour. In-line spectrophotometric closed-loop color control (X-Rite ColorCert) with a D50/2° observer monitors L*a*b* values; a ΔE2000 exceeding 1.5 triggers an audible alarm and an automatic viscosity adjustment through solvent metering.
    Comparative compliance thresholds for PR254 across primary packaging ink regulations
    RegulationSimulantTest ConditionMigration LimitAnalytical Method
    EU No 10/2011 (Plastic FCM)3% acetic acid, 50% ethanol, olive oil10 d, 40°C<10 mg/dm²EN 1186-1, EN 13130-1
    Swiss Ordinance 817.023.21Tenax TA10 d, 40°C<0.01 mg/kg (non-evaluated substance)GC-FID/MS
    Nestlé Guidance Note 2022Modified polyphenylene oxide10 d, 60°C<10 ppb (detection limit)LC-MS/MS
    FDA 21 CFR 176.170Water, heptane, 8% ethanolConditions of use A–HNo migration as component of good manufacturing practiceFTIR gravimetric
    In the area of conventional sheet-fed offset lithographic printing of art reproductions, the same pigment is used in a linseed oil-based quickset vehicle with an inkometer tack reading of 13–15 at 30°C and 400 rpm (ASTM D4361). The ink film thickness transferred to the blanket is controlled gravimetrically to 1.2–1.5 g/m², and the print is dried by oxidative polymerization accelerated by a cobalt-manganese mixed drier at 0.8% on resin solids. Lightfastness of the finished offset print on archival matte-coated paper reaches blue wool scale 8 after 96 hours of continuous exposure to a xenon arc lamp under ISO 12040:1997 conditions, a value that makes the pigment the standard magenta component in ISO 2846-1:2017 color sets for proofing applications.

    As a Non-Fullerene Acceptor in All-Polymer Indoor Photovoltaics

    While overwhelmingly deployed as a pigment, the same bis-(4-chlorophenyl)diketopyrrolopyrrole molecule possesses a planar conjugated core with an optical bandgap of approximately 2.1 eV (onset of absorption at 590 nm in thin film) and a lowest unoccupied molecular orbital (LUMO) energy of −3.5 eV vs. vacuum as measured by cyclic voltammetry with ferrocene/ferrocenium internal standard, making it a candidate electron acceptor in bulk heterojunction solar cells. A blend of poly(3-hexylthiophene) (P3HT) as donor and the DPP molecule as acceptor, deposited from a 20 mg/mL chloroform solution by blade coating at a coating gap of 150 µm and a speed of 15 mm/s, yields a photoactive layer of 90–110 nm thickness. Under 1000 lux illumination from a 2700 K compact fluorescent lamp, devices with a structure ITO/PEDOT:PSS/active layer/Ca/Al exhibited a power conversion efficiency of 2.8% when thermally annealed at 120°C for 10 minutes, a process that increases the short-circuit current density from 15 µA/cm² to 28 µA/cm² by improving the phase-separated domain size to 20–30 nm as imaged by transmission electron microscopy. Published data for this specific configuration is limited, and the primary limitation remains the limited solubility of the unsubstituted DPP core in non-halogenated solvents; ortho-dichlorobenzene (ODCB) with 5% v/v 1-chloronaphthalene as a high-boiling additive improves film uniformity but introduces a hazardous waste stream incompatible with roll-to-roll manufacturing. The electrodes are thermally evaporated at a base pressure below 2 × 10⁻⁶ mbar to achieve a calcium thickness of 25 nm and aluminum 100 nm.In sensing and photodetection, the pigment’s absorption tail extending beyond 620 nm offers a narrowband response when combined with a dielectric mirror back reflector. A solution-processed organic photodetector with a device architecture glass/ITO/ZnO/PR254:P3HT/MoO₃/Ag (10 nm MoO₃ as hole transport layer) showed a dark current density of 2.1 nA/cm² at −0.1 V and a specific detectivity of 5 × 10¹¹ Jones at 580 nm, measured by a lock-in amplifier referenced to a calibrated silicon photodiode. The linear dynamic range exceeded 100 dB only when the device was encapsulated with an epoxy resin and a glass lid in a nitrogen glove box (<1 ppm O₂, <1 ppm H₂O), as ambient oxygen at > 100 ppm induced a rapid increase in the reverse bias current due to p-doping of the P3HT phase.A different functional application exploits the pigment’s irreversible thermal isomerization above 320°C. When dispersed at 2 wt% in a polycarbonate matrix and injection-molded at 310°C into 2 mm thick plaques, the color remains unchanged. The same plaque subjected to 340°C for 3 minutes develops a permanent shift toward an opaque brown (ΔE> 20) due to formation of quinoid degradation structure, which has led to its experimental use as an oxidative environment indicator in melt-processed engineering thermoplastics, although no commercial sensor product exists to date.
    Optoelectronic and thermal indicators of PR254 in different thin-film and bulk configurations
    ConfigurationProperty MeasuredValueTest Condition/Standard
    P3HT:PR254 blend (1:1 wt)Power conversion efficiency2.8%1000 lux, CFL, 2700 K
    ITO/PEDOT:PSS/active/Ca/AlShort-circuit current28 µA/cm²AM 1.5 G, 100 mW/cm²
    PR254 in PMMA film (5 µm)Optical bandgap (Tauc plot)2.1 eVUV-Vis, indirect allowed
    PR254 powder (DSC)Exothermic decomposition onset352°C10°C/min, N₂, ASTM E537
    PR254 in PC (injection molded)Color shift thresholdΔE >20 at 340°C/3 minCIELAB D65/10°

    Aqueous Textile Pigment Printing Pastes and the Limiting Factor of Crockfastness after Industrial Laundering

    A standard all-aqueous printing paste for 100% cotton knitted fabric intended for athletic wear comprises 4 wt% DPP pigment dispersion (nonionic surfactant, 30% solids, D₅₀ = 0.3 µm), 12 wt% of a soft polyacrylate binder with a glass transition temperature of −15°C, 1 wt% melamine-formaldehyde crosslinker, 0.5 wt% ammonium nitrate as acid-liberating catalyst, and the balance a rheology modifier blend (high-molecular-weight associative thickener and fumed silica) to achieve a viscosity of 35–45 Pa · s at a shear rate of 0.1 s⁻¹ (Brookfield RV, spindle #6). The paste is screen-printed through a 100 mesh/cm polyester monofilament screen with a squeegee durometer of 65 Shore A at a velocity of 0.5 m/s and a snap-off distance of 2.5 mm. Drying is performed in a hot-air stenter at 110°C for 3 minutes, followed by curing at 150°C for 4 minutes to achieve a crosslink density sufficient to withstand 50 home-laundering cycles per ISO 6330:2021 (Procedure 4A, 60°C cotton cycle, tumble dry). Wet crockfastness measured by AATCC TM8-2022 must deliver a rating of at least 4 (grey scale) on both warp and weft directions; typical results for this formulation are 4–5 in the as-printed state, degrading to 3 after 30 cycles when the binder film begins to micro-fracture, releasing pigment particles into the wash liquor as detected by a turbidity sensor (nephelometric turbidity units increase from 0.8 to 12 NTU).To meet the bluesign® System Substance List (BSSL) and ZDHC Manufacturing Restricted Substances List (MRSL) version 3.1, the pigment must contain less than 50 ppm each of ortho-phthalates, organotin compounds, and chlorinated benzenes, verified by a third-party test report using GC-MS selected ion monitoring. The pigment’s insolubility in water (<0.1 mg/L at 20°C, OECD TG 105 flask method) ensures that it is not absorbed through the skin, a critical parameter for apparel worn directly against the skin for prolonged periods as per OEKO-TEX Standard 100, Annex 6. The residual surfactant from the pigment dispersion can interfere with the binder film coalescence, softening it and reducing the glass transition temperature by 3–5°C, which is corrected by increasing the crosslinker addition by 0.2 wt% for every 0.1 wt% of surfactant detected by HPLC-ELSD in the finished paste.
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    Certification & Compliance
    More Introduction
    Bis-(p-Chlorophenyl)-1,4-diketopyrrolo[3,4-c]pyrrole — trade designation commonly registered under Color Index Pigment Red 255 (CAS 54660-00-3) — occupies a distinct position among high-performance chlorinated diketopyrrolopyrrole (DPP) red pigments. Its molecular architecture embeds two 4-chlorophenyl substituents on the lactam-fused heterocyclic scaffold, yielding a bathochromic shift relative to the unsubstituted C.I. Pigment Red 254 but retaining the class-defining combination of exceptional thermal resilience, chemical inertness, and very low migration in engineering thermoplastics. The stoichiometric chlorine content (19.8 % theoretical) elevates crystal density to approximately 1.55–1.62 g·cm⁻³ and directly influences the dispersion viscosity profile when let down into solventborne coil-coating systems. Industrial supply chain designations for this material further include grades differentiated by specific surface area, from opaque, high-hiding variants (SBET 35–45 m²·g⁻¹) employed in rigid polyolefin packaging, through to highly transparent, nano-dispersed grades (SBET 65–80 m²·g⁻¹) preferred for metallic-effect automotive topcoats. What follows delineates the operational envelope, application-specific processing thresholds, and comparative performance boundaries of this pigment as documented through plant-floor compounding records, third-party test-house weathering databases, and ISO/IEC 17025-validated analytical data.

    How Does Polychlorophenyl Substitution Modify Accelerated Weathering Performance in Coil Coatings?

    In polyester-melamine coil-coating formulations applied at dry film thickness 18–22 µm over hot-dip galvanized steel, the introduction of Pigment Red 255 in a full-shade system routinely yields a Delta E*ab ≤ 1.5 after 2 000 h of xenon-arc exposure per ISO 4892-2:2013 (Method A, daylight filter, BPT 63 °C). This value represents a measurable improvement over PR 254, which under identical conditions often drifts above Delta E*ab 2.8 due to photolytic attack on the non-halogenated aryl ring. The chlorine substituent withdraws electron density from the chromophore, raising the ionization potential and slowing singlet-oxygen-mediated degradation at the lactam carbonyl. Published Florida south-facing 45° rack data on full-shade acrylic-melamine thermosets confirm a 24-month gloss retention exceeding 85 % (ASTM D523-14 60° geometry) without chalking, a threshold that remains stable when the pigment volume concentration is maintained between 8 % and 15 % in the dry film. Waterborne one-coat systems incorporating PR 255 demand tighter pH control than solventborne analogues: circulation bath pH falling below 8.0 during electrodeposition can trigger micro-agglomeration at the anode diffusion layer, increasing Millipore filtration pressure above 0.4 MPa within 20 minutes of line operation. This effect narrows the processing window when switching from PR 254 to PR 255 without reformulating the neutralizing amine package; plant logs from a coil line in Western Europe document a 30 % rise in in-can viscosity after three weeks of accelerated storage at 50 °C when 2-dimethylaminoethanol is used as the sole solubilizer, a condition not observed with 2-amino-2-methyl-1-propanol at identical molar equivalents.

    Specifications and Colloidal Fingerprint

    The table below aggregates the primary quality-control parameters applied to incoming batches of Pigment Red 255 at a production site supplying masterbatch to thin-wall injection molders. All values represent equilibrated, moisture-corrected measurements.
    PropertyTypical RangeTest Method
    Volatile matter (2 h, 105 °C)≤ 0.5 %ISO 787-2:1981
    Oil absorption38–48 g·100 g⁻¹ISO 787-5:1980
    Specific surface area (BET)52–68 m²·g⁻¹ISO 9277:2010
    pH of aqueous extract6.0–7.5ISO 787-9:1981
    Residue on sieve (45 µm)≤ 0.1 %ISO 787-7:2009
    Heat stability in HDPE (5 min)300 °C (ΔE ≤ 1.0)EN 12877-2:2000
    Lightfastness full shade (blue wool)8ISO 105-B02:2014
    Lightfastness 1:10 TiO₂ tint7–8ISO 105-B02:2014
    Processing behaviour in non-polar thermoplastics reveals a strong dependence on the primary particle aggregate structure. A surface-treated grade with a proprietary rosin-derived encapsulation post-synthesis displays a melt-flow index depression of only 8 % relative to unfilled polypropylene homopolymer when compounded at 0.5 wt% pigment loading on a co-rotating twin-screw extruder (L/D 44:1, specific energy input 0.20 kWh·kg⁻¹). The identical pigment without treatment, measured on the same line, reduces MFI by 22 % due to agglomerate-induced filter pack pressure accumulation at the 150-µm mesh screen changer. Pre-drying of raw pigment powder in a vacuum oven at 80 °C for 4 h is mandatory whenever ambient relative humidity exceeds 60 %; absorbed moisture at 0.8 % or above will hydrolyze the coupling agent in silane-modified filler-containing formulations, leading to torque spikes exceeding 90 Nm in the internal mixer during polyamide compounding. Operational knowledge further dictates that any zone temperature above 320 °C will degrade the sulfonated synergist commonly co-employed with PR 255, emitting sulfur dioxide detectable by Dräger tubes and triggering an immediate purging cycle. In rigid PVC extrusion for window profiles, where organotin stabilizers dominate, the chlorinated DPP pigment demonstrates higher inherent compatibility than isoindolinone yellows that can catalyze dehydrochlorination. Still, co-processing with antimony trioxide flame retardants is contra-indicated: in a 1 mm thick plaque extruded at 190 °C, the combination with 3 wt% Sb₂O₃ raised the yellowness index (ASTM E313-20) by 4.2 units versus a PR 255-only control within 15 minutes of dwell time in the accumulator head.

    When Replacing PR 254 in High-Temperature Nylon 6,6 Monofilaments

    A shift from C.I. Pigment Red 254 to the chlorinated analog in nylon 6,6 spun-dyed monofilaments (filament diameter 0.25 mm) forces adjustments beyond shade matching. The melting point depression in the pigmented polymer, measured via differential scanning calorimetry per ISO 11357-3:2018, is 2–4 °C greater for PR 255 at 1.0 wt% loading, which necessitates a 5 °C reduction in the extruder melt temperature setpoint to avoid filament breakage at the godet. The crystalline lamellae oriented along the fiber axis nucleate differently in the presence of the higher-density chlorinated particle; wide-angle X-ray scattering confirms a 15 % reduction in the ratio of α-crystal phase to γ-phase, which translates into a 9 % lower tensile strength (ISO 2062:2009) yet a 12 % higher elongation at break. This trade-off can be acceptable in non-loadbearing textile applications but disqualifies the pigment for high-tenacity industrial yarns unless post-polymerization solid-state polycondensation is performed, adding 36–48 h to the overall lot cycle. Dispersion quality in nylon 6,6 is critically evaluated using a pressure-ramp filtration test according to EN 13900-5. Acceptable lot release requires a filter pressure value (FPV) below 0.5 bar·g⁻¹ on a 14 µm mesh. Batches failing this benchmark by exceeding 0.7 bar·g⁻¹ correlate with visible stripe defects in blown film at blow-up ratios above 2.2:1. When this limit is breached, inline ultrasound-assisted melt homogenization at 20 kHz and 400 W has been shown to recover compliance, though it elevates yellowness index by 0.8 units per cycle due to local shear-induced overheating.

    Addressing Plate-Out and Screw Deposit Formation in Continuous Compounding

    During long-run masterbatch production of PR 255 in linear low-density polyethylene (LLDPE) with melt index 1.0 g·10 min⁻¹ (ISO 1133-1:2022, 190 °C, 2.16 kg), deposit accumulation on the screw roots and barrel wall downstream of the melting zone becomes observable after approximately 72 h of uninterrupted operation. Fourier-transform infrared microscopy of the deposit identifies the primary foulant as a low-molecular-weight fraction of the pigment’s sulfonated solubilizing intermediate that was not fully removed during the alkaline wash step of synthesis. The deposit thickness measured by micrometers averages 120–180 µm and increases screw power draw by 7–10 %. Mitigation strategies proven effective in production include the introduction of 0.05 wt% zinc stearate as a barrier lubricant pre-blended with the pigment powder, and a scheduled 15-minute purge with high-viscosity HDPE (melt index 0.3 g·10 min⁻¹) containing 20 % calcium carbonate filler at 8-hour intervals. This protocol, validated on a 75 mm twin-screw with L/D 40:1 and vacuum degassing at -0.08 MPa, extends uninterrupted runtime to 240 h before mandatory barrel opening. Storage stability of the dry powder in a non-air-conditioned warehouse storing pallets at 30–40 °C and 70–85 % relative humidity for six months does not compromise coloristic properties, provided the original polyethylene-lined bag remains heat-sealed. Once opened, re-tie closures slow moisture uptake but do not eliminate it; moisture content rises to 1.2 % after 28 days of intermittent access, leading to lump formation that defeats gravimetric dosing accuracy beyond an acceptable tolerance of ± 2 %. In liquid ink concentrates for flexible packaging gravure printing, PR 255 provides a bluish-red masstone with a hue angle of 350 °355 ° (CIELAB D65/10 °), approximately 5 ° bluer than the same pigment printed at an identical gravure cell depth using PR 254. This shift allows press operators to adjust overprint trap sequence without resorting to cobalt-based dryers when replacing red shade on a fixed-color station layout. The critical parameter controlling misting on high-speed presses (> 300 m·min⁻¹) is the viscosity ratio at low and high shear rates; a premix resin-to-pigment ratio of 2.5:1 with nitrocellulose-based varnish yields a shear-thinning index (100 s⁻¹/1000 s⁻¹) of 2.8, which correlates with mist droplet counts below 5 particles·cm⁻² on positioned witness panels. Outside this ratio, droplet density escalates exponentially. A secondary application domain where the chlorinated DPP derivative outperforms both diketo-pyrrolo homologue and perylene reds is in thin-gauge (0.25 mm) calendered opaque polycarbonate sheets for LED diffusers. Here the minimum loading to achieve 99.5 % opacity measured by contrast ratio (ASTM D2805-11) is 0.12 wt%, which is 25 % lower than PR 254, a consequence of the elevated refractive index contributed by the chlorine atoms. At this loading, the luminous transmittance loss is only 6 ± 1 % relative to unfilled resin, enabling luminance uniformity ratios exceeding 0.85 across a A4-sized sheet when edge-lit with 4 000 K LEDs. Manufacturers specifying PR 255 in this application must monitor residual alkali metal content: sodium and potassium concentrations above 50 ppm each, as determined by inductively coupled plasma optical emission spectrometry, accelerate polycarbonate yellowing at the sheet’s core during thermal cycling between -40 °C and 120 °C (IEC 60068-2-14, Test Nb). Acceptable batches are consistently those retaining total alkali metals below 30 ppm.
    RegulationCompliance Status / Citation
    EU REACHRegistered; SVHC-free per Article 57
    FDA 21 CFRSuitable under 178.3297 (colorants for polymers) with migration limits per FCN inventory
    AP(89)1Permitted for food-contact plastics
    RoHS III (EU 2015/863)Below MCV thresholds for Pb, Hg, Cd, Cr(VI), PBBs, PBDEs, DEHP, BBP, DBP, DIBP
    CONEGSum of Pb, Hg, Cd, Cr(VI) ≤ 100 ppm
    EN 71-3:2019+A1:2021Migration limits satisfied for Category I–III toy materials
    Users transitioning from alternative red chemistries such as C.I. Pigment Red 272 (a methyl-substituted DPP) encounter a higher pigment agglomerate hardness in PR 255, requiring an increase in bead mill residence time of 15–20 % to achieve the same 7+ Hegman grind in a polyurethane-based two-component topcoat. This imposes a secondary constraint: extended grinding elevates mill-base temperature above 55 °C, which in solvent-reduced formulations with high methyl ethyl ketone content can exceed the flash point of the premix if solvent condensing towers are not operating at full duty. Published production line experience for a one-pass horizontal bead mill (chamber volume 5 L, 0.8–1.0 mm yttria-stabilized zirconia beads, 80 % fill, agitator tip speed 12 m·s⁻¹) confirms that an optimal compromise of tinting strength and aggregate breakdown exists at a throughput of 60 kg·h⁻¹ for PR 255, versus 80 kg·h⁻¹ for PR 272 with identical pigment loading. Operators adjusting to this pigment must accept the throughput penalty as an inherent consequence of the chlorinated ring’s stronger intermolecular hydrogen bonding in the primary crystal. The absence of a photoluminescent component in the pigment’s electronic structure differentiates it from benzimidazolone reds that exhibit weak fluorescence under UV inspection in banknote security threads. This puts PR 255 at a disadvantage for covert authentication features, yet the same spectral flatness below 400 nm eliminates the variability in UV-blocking clearcoat compatibility that recurrently complicates quality assurance for perylene maroons with residual fluorescence. In automotive basecoat/clearcoat systems, where a UV-blocking clearcoat containing a benzotriazole absorber at 2 wt% is applied wet-on-wet, the color match between the horizontal hood and vertical fender panels shows a Delta L* deviation of 0.3 units for PR 255, compared with 0.9 units for C.I. Pigment Red 179 (perylene maroon), as recorded on a multi-angle spectrophotometer at 15° aspecular angle under D65. This near-constancy simplifies process-signoff at full plant color audit frequency. Migration fastness into plasticized PVC containing 33 wt% di-(2-ethylhexyl) phthalate is rated 5 according to ISO 183:1976 after 72 h at 80 °C and 1 kg·cm⁻² contact pressure against white pigmented PVC, matching the performance of the parent DPP but exceeding that of quinacridone reds which typically degrade to a rating of 4 under identical conditions. This makes PR 255 the selection of first resort for pigmented synthetic leather topcoats where prolonged skin contact and exposure to plasticizer extraction in automotive interior testing require zero visible bleed onto a white cotton fabric per DIN 75201. Differences from C.I. Pigment Red 254 crystallize most sharply in the domain of warpage induction. In semi-crystalline polypropylene homopolymer injection-molded plaques (60 x 60 x 2 mm) gated at one edge, the addition of 0.2 wt% PR 255 induces a flatness deviation of 0.4 mm measured along the diagonal by a coordinate measuring machine, whereas PR 254 at identical concentration yields 1.1 mm deviation. The reduced warpage is attributed to the higher nucleation density of transcrystallinity layers around the chlorinated particle, which retards post-mold shrinkage anisotropy. This property enables direct substitution of PR 255 into multi-cavity molds originally designed for less nucleating organic reds without requiring die temperature profiling adjustments above the factory default of 40 °C. Process safety alert: During jacketed ribbon blender cleaning after a PR 255 campaign, contacting the dry residue with concentrated nitric acid as part of an automated clean-in-place recipe releases nitrous gases from decomposition of the lactam ring. A documented incident at a toll-compounding facility necessitated the replacement of that CIP step with a 2-hour recirculation of 5 wt% N-methyl-2-pyrrolidone at 80 °C, which solubilizes the pigment sufficiently to achieve surface swipe cleanliness below 2 µg·cm⁻². This solvent recovery loop must remain sealed and inerted with nitrogen to avoid the formation of explosive peroxides in the aged NMP over multiple reuse cycles.