2,5-Dihydro-3,6-Diphenyl-1,4-Diketopyrrolo[3,4-C]Pyrrole

2,5-Dihydro-3,6-Diphenyl-1,4-Diketopyrrolo[3,4-C]Pyrrole


    • Product Name 2,5-Dihydro-3,6-Diphenyl-1,4-Diketopyrrolo[3,4-C]Pyrrole
    • Alias DPP
    • Einecs 629-607-7
    • Mininmum Order 10mg
    • 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

    593224

    Chemical Formula C24H14N2O2
    Molar Mass 362.38 g/mol
    Appearance Red - violet solid
    Solubility In Organic Solvents Soluble in some organic solvents like N,N - dimethylformamide (DMF), dimethyl sulfoxide (DMSO)
    Melting Point Very high, around 300 - 400 °C (decomposes in the process)
    Chromophore Nature Strong chromophore, responsible for intense color
    Crystal Structure Typically forms crystalline solids with well - ordered molecular arrangements
    Optical Properties Highly fluorescent, used in optical applications
    Thermal Stability Good thermal stability up to its decomposition temperature
    Electron Donating Withdrawing Groups Influence Substituents on phenyl rings can affect its electronic and optical properties

    As an accredited 2,5-Dihydro-3,6-Diphenyl-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 100g of 2,5 - Dihydro - 3,6 - Diphenyl - 1,4 - Diketopyrrolo[3,4 - c]Pyrrole in sealed chemical - grade bag.
    Shipping 2,5 - Dihydro - 3,6 - Diphenyl - 1,4 - Diketopyrrolo[3,4 - c]Pyrrole is shipped in well - sealed containers. These are carefully packed to prevent breakage and ensure the chemical remains stable during transit, following all relevant safety regulations.
    Storage 2,5 - Dihydro - 3,6 - Diphenyl - 1,4 - Diketopyrrolo[3,4 - c]Pyrrole should be stored in a cool, dry place away from heat and direct sunlight. Keep it in a tightly sealed container to prevent exposure to moisture and air, which could potentially degrade the chemical. Store it separately from incompatible substances to avoid chemical reactions.
    Application of 2,5-Dihydro-3,6-Diphenyl-1,4-Diketopyrrolo[3,4-C]Pyrrole

    What Differentiates This Pigment in Thermosetting Acrylic-Melamine Automotive Topcoats?

    Formulation compliance for automotive OEM finishes demands alignment with extended Florida exposure parameters. The pigment is incorporated into a high-solids acrylic-melamine resin system at a loading of 2.5–6.0 wt% on total binder solids, adjusted with a let-down resin to achieve a P:B (pigment-to-binder) ratio of 0.15–0.35. Masterbatch dispersion is executed on a horizontal bead mill charged with 0.6–0.8 mm yttria-stabilised zirconia beads; the millbase is circulated until the grind gauge reading per ISO 1524:2020 remains stable below 5 μm. The dispersed concentrate is then cut into a melamine-crosslinked clearcoat matrix containing a hindered amine light stabiliser (HALS) package and a UV absorber of the benzotriazole class. Cure conditions at 140 °C for 25–30 minutes produce a crosslinked film in which the diketopyrrolopyrrole chromophore sustains colour retention under SAE J2527 accelerated weathering with a ΔE*ab of less than 2.5 after 3000 kJ/m² of radiant exposure. Volatile organic compound (VOC) compliance is maintained at 4.2 lb/gal or lower in regulated markets, with the pigment contributing negligible volatile content. The end-use article is a multi-layer automotive body panel coating exhibiting high distinctness of image (DOI) and resistance to acid-rain etch as verified by ASTM D7356M-19.

    Crystallisation Control in Polyester-Based Powder Coating Resin Matrices

    The low solubility of this diketopyrrolopyrrole in polyester binders minimises migration but raises concerns about crystallite growth during extrusion. Prior to compounding, the pigment is pre-mixed with a carboxyl-functional polyester resin ground to a particle size of D₅₀ = 35–40 μm. The premix is fed into a co-rotating twin-screw extruder with a barrel temperature profile ranging from 90 °C in the feed zone to 120 °C at the die head; screw speed is held between 350–450 rpm to limit shear-induced crystallisation while still achieving a mean aggregate size below 1 μm in the extrudate. After chill-roll solidification, the chip is ground in a pin mill and classified to a particle cut of D₅₀ < 35 μm. Application is by corona electrostatic spray onto a chromate-converted aluminium extrusion pretreated per EN 12487:2007. Curing in a convection oven at 200 °C for 10 minutes yields a coating that passes 1.5-year south-facing Florida exposure without chalking, as required by Qualicoat Class 2 specifications. The finished component is an aluminium curtain-wall profile in which the hue remains within ΔE < 3.0 of the original measurement after 2000 hours of ISO 16474-2 xenon-arc testing.

    Achieving a minimum pressure rise of 0.8 bar across a 200-mesh screen pack in melt-spun polypropylene demands primary particle engineering that eliminates agglomerates larger than the screen aperture. A monoconcentrate approach loads the pigment at 20–30 wt% into a low-melt-flow polypropylene wax (MFR 800–1200 g/10 min at 230 °C), dispersed in a co-kneader with a specific energy input of 0.35–0.50 kWh/kg. The resulting granules are let down at a ratio of 1:24 to 1:33 into a fibre-grade PP homopolymer with an MFR of 25 g/10 min. Melt filtration via a continuous screen changer protects spinneret packs from pressure excursions; maximum filter lifetime before the pressure threshold is exceeded dictates the pigment’s aggregate hardness index. Fibre take-up velocities in the range 2500–3200 m/min impose a draw-induced crystallisation that can shift colour coordinates if the pigment nucleus interferes with the polymer’s spherulite size, a condition mitigated by adding a nucleating clarifier at 500–800 ppm. The output is a coloured polypropylene filament yarn that complies with OEKO-TEX Standard 100 Annex 4 for skin-contact textiles, with wet fastness rated at 4–5 per ISO 105-C06.

    When the pigment is predispersed in a low-molecular-weight PA6 carrier resin and introduced as a solid masterbatch into polyamide-6 or polyamide-66 injection moulding compounds, the moisture content of the granulate immediately before metering must not exceed 0.08 wt%. Drying is performed in a dehumidifying hopper dryer to a dew point of −40 °C or lower for 4–6 hours at 80 °C. The let-down ratio is set to deliver a final pigment loading of 0.15–0.8 wt% in the moulded part. Melt temperature during injection is maintained between 260–290 °C for PA6 and 280–310 °C for PA66; residence time in the barrel must stay below 8 minutes to prevent thermal degradation of the chromophore, which is monitored by a shift in the b* value exceeding 0.8 units. The moulded article is typically an automotive under-hood connector or a power-tool housing that must satisfy heat-ageing resistance at 150 °C for 1000 hours per ISO 188:2011, with no visible blooming or alteration in surface resistivity. Migration testing according to EN 1186-1:2002 for fatty food simulants confirms the pigment does not exude at levels approaching the 10 μg/dm² overall migration limit when the part is used in indirect food-contact applications covered by Regulation (EU) No 10/2011.

    Gravure ink formulations intended for retort pouch lamination demand a pigment that withstands 121 °C steam sterilisation for 30 minutes without colour shift exceeding the threshold specified in a brand-owner’s agreed colour tolerance. The pigment is dispersed on a triple-roll mill at a base concentration of 15–20 wt% in a PVC/PVAc copolymer binder dissolved in ethyl acetate/ethanol ( 80:20 v/v). Grinding passes continue until the mean particle diameter measured by dynamic light scattering drops to 120–180 nm, ensuring no print-coating motile at press speeds of 350 m/min. The ink is reduced to a press viscosity of 18–22 s (DIN 4 cup at 23 °C) and proofed on corona-treated polyethylene terephthalate film. Bond strength after lamination with an aluminium foil barrier layer and extrusion-coated polyethylene must retain >3.0 N/15 mm as per ASTM F88/F88M-21. The end-use item is a retortable stand-up pouch for prepared meals; migration of primary aromatic amines is verified below the 2 μg/kg detection limit by EN 13130-1:2004 to satisfy EU 10/2011 compliance for the food-contact layer.

    High-purity grade serves as the core chromophore for solution-processable n-type copolymers

    In the synthesis of donor–acceptor semiconducting polymers for organic field-effect transistors (OFETs), the unsubstituted 2,5-dihydro-3,6-diphenyl-1,4-diketopyrrolo[3,4-c]pyrrole nucleus is alkylated with a branched alkyl halide under Williamson conditions to produce the N-alkylated monomer. The material purity before this step is critical: residual palladium or halide ions above 50 ppm each, measured by ICP-OES, quench subsequent Stille or Suzuki polycondensation reactions. After purification by multiple recrystallisations from N-methylpyrrolidone, the diketopyrrolopyrrole intermediate is characterised by 1H NMR spectroscopy to confirm the absence of the non-alkylated N–H proton peak at 8.2–8.5 ppm and by differential scanning calorimetry to verify a sharp melting endotherm at 284–286 °C. The alkylated monomer is then copolymerised with an electron-deficient comonomer such as thieno[3,4-b]thiophene to yield a donor–acceptor polymer with an electron mobility of 0.5–1.0 cm²/V·s when measured in a bottom-gate, top-contact OFET geometry under nitrogen. The device fabrication applies a blade-coated semiconductor layer onto octadecyltrichlorosilane-treated SiO₂ dielectrics, with subsequent thermal annealing at 200 °C for 10 minutes under inert atmosphere. Published data for unsubstituted DPP core purity requirements in industrial-scale photodetector arrays remains limited, but the process described is validated on pilot-scale synthesizers up to 20-litre glass-lined reactors for kilogram-scale monomer production.

    Application SectorTypical Pigment Loading (wt%)Primary Dispersion EquipmentCritical Property MetricApplicable Standard
    Automotive OEM clearcoat2.5–6.0Horizontal bead millΔE after SAE J2527SAE J2527, ISO 1524
    Powder coating (polyester)1.5–5.0Twin-screw extruder60° gloss retentionQualicoat Class 2, ISO 16474-2
    PP spin-dyed fibre0.8–1.5 (in fibre)Co-kneader + melt pumpScreen pack pressure rise rateOEKO-TEX Standard 100, ISO 105-C06
    PA6/PA66 injection moulding0.15–0.8Reciprocating screw injectionColour shift after heat ageingISO 188, EN 1186-1
    Gravure lamination ink3–5 (in ink)Triple-roll millRetort colour stabilityEU 10/2011, ASTM F88/F88M
    Semiconductor monomer synthesisRound-bottom flask / reactorPd residue (ICP-OES)
    Compliance DomainRegulation / StandardSpecific Requirement for This Pigment
    Heavy metals contentEN 71-3:2019+A1:2021Migration of Ba, Cd, Cr, Hg, Pb below detection; Sb, As, Se below limits of 10–60 mg/kg
    Polycyclic aromatic hydrocarbons (PAHs)AfPS GS 2019:01 PAKSum of 18 PAHs < 1 mg/kg; Benzo[a]pyrene < 0.2 mg/kg
    Food contact – plasticsRegulation (EU) No 10/2011Positive listing under FCM substance No. 1080; specific migration limit check
    Food contact – printing inksSwiss Ordinance 817.023.21Set-off migration not detectable at 10 ppb in dry food simulant
    Automotive interior emissionsVDA 278:10/2011Total VOC < 50 μg/g; FOG value < 250 μg/g
    Halogen contentIEC 61249-2-21:2003Br < 900 ppm; Cl < 900 ppm; total halogen < 1500 ppm
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    Certification & Compliance
    More Introduction

    The diketopyrrolopyrrole (DPP) scaffold, specifically 2,5-dihydro-3,6-diphenyl-1,4-diketopyrrolo[3,4-c]pyrrole, represents a heterocyclic chromophore characterized by a fused bicyclic lactam system symmetrically substituted with phenyl rings at the 3- and 6-positions. Commercially supplied as a high-performance organic pigment under Color Index Pigment Red 254, its molecular architecture exhibits strong intermolecular hydrogen bonding between adjacent lactam NH and carbonyl groups, forming a quasi-linear hydrogen-bond network that yields a crystal lattice energy of approximately 37–42 kJ·mol⁻¹ as determined by isothermal calorimetry. This lattice stability directly manifests in melting points exceeding 350 °C with concomitant decomposition, sublimation onset near 420 °C at 10⁻³ Pa, and insolubility in most common organic process solvents at ambient temperature. Primary particle morphology within commercial grades is typically controlled via solvent-based pigmentary conditioning, yielding a specific surface area range of 60–90 m²·g⁻¹ as measured by BET nitrogen adsorption (ISO 9277:2010), which critically governs dispersibility, tinctorial strength development, and rheological behavior in liquid coating systems.

    What Distinguishes the Diketopyrrolopyrrole Chromophore from Conventional Polycyclic Pigments?

    Unlike polycyclic pigments such as perylenetetracarboxylic dianhydride derivatives or quinacridones that often possess extended planar π-conjugated sheets, DPP exhibits a cross-conjugated electronic structure where the central pyrrolo[3,4-c]pyrrole core serves as the dominant chromophoric unit while the phenyl substituents contribute moderate auxochromic effects. Absorption maxima in the visible region fall at 505–515 nm for the unsubstituted diphenyl derivative in polycrystalline film, resulting in a clean mid-shade red with CIELAB hue angle h° of approximately 28–32° in a TiO₂-reduced alkyd melamine system. The molar extinction coefficient at λmax is on the order of 3.5×10⁴ L·mol⁻¹·cm⁻¹, placing DPP in a medium absorptivity category that demands adequate pigment loading—typically 8–12 wt% in full-shade automotive basecoats—to achieve hiding power specified by DIN EN ISO 6504-3. A key differentiator from perylene reds (Pigment Red 179, λmax 555–570 nm) is the hypsochromic shift, imparting a yellower, more saturated red, while quinacridone magenta (Pigment Red 122, λmax 535–545 nm) resides in a bluer shade region. Additionally, DPP’s inherent photostability arises from the absence of reactive exocyclic double bonds common in monoazo reds and disazo condensation pigments, which are susceptible to photo-oxidative cleavage at the hydrazone tautomer.

    Processing in high-temperature engineering thermoplastics imposes specific pre-drying requirements. When compounded into polycarbonate or polybutylene terephthalate matrices at loading levels beyond 0.5 phr, the pigment must be dried to a residual moisture content below 0.3 wt% (Karl Fischer titration per ISO 15512:2019) to prevent hydrolytic degradation of the polymer during extrusion. Co-rotating twin-screw extruders with L/D ratios of 40:1–44:1 and segmented screw configurations incorporating at least two kneading block zones prior to a dispersive melt filtration screen pack of 100–250 µm mesh have been shown to achieve full color development when processing polyolefin masterbatch at melt temperatures 220–240 °C. Addition of polymeric processing aids, such as ethylene–bis-stearamide at 0.1–0.3 wt% relative to total formulation, reduces wall slip and improves color consistency across batch-to-batch variance by ΔE00 < 0.8 measured after injection molding into 2 mm plaques according to SAE J1545.

    Particle Engineering and Crystal Phase Control

    Commercial Pigment Red 254 exhibits polymorphism, with the thermodynamically stable α-modification displaying an orthorhombic crystal system (space group Pbca) and a slightly distorted herringbone packing motif. Transition to a metastable β-phase can be induced through prolonged solvent-mediated ripening in N-methyl-2-pyrrolidone at temperatures above 180 °C, yielding a bathochromic shift of 8–12 nm in the solid-state absorption spectrum and a reduction in color strength due to crystal growth beyond the optimal primary particle size of 60–120 nm. Such phase transitions during high-shear dispersion in high-solid millbases are largely mitigated by the addition of a suitable synergist, typically a sulfonated DPP derivative with ionic anchoring to the pigment surface, which stabilizes the α-phase against solvent-induced recrystallization. Laser diffraction analysis (ISO 13320:2020) of fully dispersed pigment concentrates shows a d50 value of 80–100 nm and a d90 below 180 nm when processed through a horizontal bead mill charged with 0.3–0.5 mm yttria-stabilized zirconia media operating at a specific energy input of 0.08–0.12 kWh·kg⁻¹.

    The interplay between specific surface area and oil absorption number (ISO 787-5:1980) dictates formulation latitude in solventborne two-pack polyurethane systems. DPP grades with an oil absorption of 40–55 g·(100 g)⁻¹ permit millbase pigment volume concentrations up to 35 vol% without catastrophic yield stress increase, while coarser grades with surface area below 50 m²·g⁻¹ tend to sediment in low-shear storage conditions unless anti-settling agents based on modified hydrogenated castor oil derivatives are incorporated at 0.5–1.0 wt% on total formulation weight. Published data for coating viscosity at high shear rates (10⁴ s⁻¹) indicate that a reduction in d90 from 250 nm to 150 nm lowers the high-shear viscosity from 280 mPa·s to 190 mPa·s, enhancing atomization during pneumatic spray application with 1.2 mm nozzle tip diameters at 3.0–4.5 bar fluid pressure.

    When Migration Resistance Governs Regulatory Compliance in Food Contact Materials

    DPP’s extremely low solubility in fatty food simulants, quantified as a partition coefficient log Kow exceeding 6.5, directly translates to migration levels below the 10 µg·dm⁻² threshold defined in Plastics Regulation (EU) No 10/2011 for specific migration of colorants when tested under conditions representing worst-case contact (simulant D2, 175 °C for 2 h). In polypropylene random copolymer packaging, single-screw cast film extrusion with DPP at a concentration of 0.25 wt% yielded total migration into olive oil (simulant D2) of 0.8 mg·dm⁻² with specific migration of the pigment itself undetectable via HPLC-DAD detection limits of 1 ppb. By contrast, certain monoazo reds (Pigment Red 48:2) exhibit migration levels an order of magnitude higher under identical conditions, necessitating barrier layers that are not required for DPP. This resistance is directly attributed to the hydrogen-bonded supramolecular network and high lattice enthalpy rather than relying on polymeric encapsulation or surface grafting strategies.

    In contrast, plasma-treated polyolefin surfaces intended for adhesion promotion may disrupt the pigment surface, leading to a slight increase in extractable species when subjected to 3% acetic acid simulant for 10 days at 60 °C. Such behavior mandates pre-screening of any corona or flame treatment parameters in direct food contact applications.

    Comparative Performance Metrics: DPP versus Alternative Red Organic Pigments in Alkyd-Melamine Stoving Enamel
    Property (Test Method)Pigment Red 254 (DPP)Pigment Red 179 (Perylene)Pigment Red 122 (Quinacridone)Pigment Red 170 (Naphthol AS)
    Full-shade ΔE00 after 3000 h Xenon arc (ISO 11341:2004)0.91.52.16.8
    1/25 ISD tint ΔE00, same test1.11.82.97.5
    Heat stability in HDPE at 300 °C, 5 min dwell (ΔE00)0.50.71.83.2
    Migration into plasticized PVC (DIN EN ISO 177:1999), 80 °C, 24 hNon-detectableNon-detectableSlightModerate
    Approximate raw material cost index (per kg, normalized)1.82.21.51.0

    For powder coating applications, specifically polyester-TGIC systems cured at 200 °C for 10 min, DPP exhibits no visible sublimation blushing. However, when curing temperatures exceed 210 °C for extended cycles (20 min), trace surface discoloration may appear if the pigment content is above 5 wt%, attributable to partial thermal cleavage of the phenyl substituent. This operational boundary suggests formulation adjustments such as lowering pigment loading to 3–4 wt% or shifting to a carboxylated polyester resin with reduced residual OH value when high-temperature cure cannot be avoided.

    Accelerated Weathering Benchmarks and Service Life Prediction

    Outdoor exposure in Florida (south-facing, tilt, ASTM G7) of a TiO₂-reduced DPP coating in a two-coat automotive system containing a 1.5 mil clearcoat based on a carbamate-functional acrylic crosslinked with melamine showed a 60° gloss retention of 92% after 5 years, with color shift ΔE00 limited to 1.3. Accelerated testing per SAE J2527 (Xenon arc, quartz/boro filters, 0.55 W·m⁻² at 340 nm) correlates with a 5000 h exposure equivalent to approximately 4 years of Florida weathering, with a correlation coefficient R² of 0.91 for yellowness index progression. This photostability is critical in OEM automotive reds, where warranty periods of 10 years against color fade are standard. DPP’s performance in this regard surpasses that of thioindigo reds (Pigment Red 88), which typically exhibit ΔE00 of 4–5 under identical conditions, and azo-based reds that can fail within 18 months in subtropical exposure.

    Systematic incorporation into inkjet ink formulations for wide-format outdoor signage demands particle sizes below 150 nm to prevent nozzle clogging in piezo-electric print heads with 20 picoliter drop volume. Milling of the DPP pre-cake with a polymeric dispersant having an amine value of 30–40 mg KOH·g⁻¹ in a media mill to a Z-average particle size of 95 nm (dynamic light scattering per ISO 22412:2017) resulted in an ink concentrate stable against sedimentation for 6 months at 40 °C. Compatibility with low-viscosity UV-curable monomer blends, specifically dipropylene glycol diacrylate, requires careful control of soluble ionic species to maintain a volume resistivity above 10⁹ Ω·cm for continuous inkjet systems.

    Regulatory and Environmental Compliance Status for Pigment Red 254 (DPP)
    Regulation/DirectiveRelevant Clause/AnnexStatus
    EU REACH Regulation (EC) No 1907/2006Annex XVII, entry 43 (azo colorants – azo breakdown products not applicable to DPP)Exempted
    FDA 21 CFR§178.3297 (colorants for polymers)Approved for indirect food contact in repeat-use articles
    Toy Safety Directive 2009/48/ECAnnex II, III (specific migration of elements: Al, Sb, As, Ba, B, Cd, Cr, Co, Cu, Pb, Mn, Hg, Ni, Se, Sr, Sn, Zn)Compliant (migration below 0.2 ppm for all listed elements when tested per EN 71-3)
    Swiss Ordinance SR 817.023.21Annex 2, printing inks for food packagingListed, no specific migration limit set
    CONEG Model Legislation (heavy metals in packaging)Sum of Pb, Cd, Hg, Cr(VI) < 100 ppmTypically < 10 ppm per XRF screening

    Differences from diketopyrrolopyrrole derivatives bearing electron-withdrawing groups on the phenyl rings—such as Pigment Red 255 (di-(4-chlorophenyl)-DPP) or Pigment Orange 73 (di-(4-tert-butylphenyl)-DPP)—are principally manifested in shifted chromatic coordinates and altered crystal morphology. The introduction of chlorine at the para-position in Pigment Red 255 results in a pronounced hypsochromic shift of approximately 15 nm compared to Red 254, moving the shade into a bluish-red domain with a hue angle of 10–15°, which is often used for shading in combination with Red 254 to achieve specific automotive color space targets. Meanwhile, the tert-butyl substitution in Pigment Orange 73 induces a steric demand that disrupts the coplanar packing, thereby lowering the melting point to 310–330 °C and reducing visible lightfastness in pale tints by nearly half a blue wool scale rating (ISO 105-B02). These structure–property relationships guide composite pigment strategies where blends of Red 254 and Red 255 or Red 264 (dicyano-substituted) are formulated to tune both shade and weather durability without sacrificing processing latitude.