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

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


    • Product Name 3,6-Diphenyl-2,5-Dihydro-Pyrrolo[3,4-C]Pyrrole-1,4-Dione
    • Alias DPP
    • Einecs 420-640-2
    • Mininmum Order 1g
    • 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

    188275

    Chemical Formula C20H12N2O2
    Molecular Weight 312.32 g/mol
    Appearance Solid
    Melting Point Typically high, data may vary
    Solubility Poorly soluble in water, more soluble in organic solvents
    Color May be yellow - orange or similar color depending on purity
    Crystal Structure Complex organic crystal structure
    Stability Stable under normal conditions, may decompose under high heat or in presence of strong oxidizing agents
    Odor Odorless or very faint odor
    Reactivity Can participate in various organic reactions such as substitution, addition reactions

    As an accredited 3,6-Diphenyl-2,5-Dihydro-Pyrrolo[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 & Storage
    Packing 100g of 3,6 - Diphenyl - 2,5 - Dihydro - Pyrrolo[3,4 - c]Pyrrole - 1,4 - Dione in sealed chemical - grade bags.
    Shipping 3,6 - Diphenyl - 2,5 - Dihydro - Pyrrolo[3,4 - c]Pyrrole - 1,4 - Dione is shipped in well - sealed containers, safeguarded by appropriate cushioning. Shipment follows regulations for chemical transport, ensuring safe and proper handling during transit.
    Storage Store 3,6 - Diphenyl - 2,5 - Dihydro - Pyrrolo[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 exposure to air, which could potentially lead to degradation. Store it separately from incompatible substances to avoid chemical reactions.
    Application of 3,6-Diphenyl-2,5-Dihydro-Pyrrolo[3,4-C]Pyrrole-1,4-Dione

    When mid-coat colour layers in high-gloss automotive OEM finishes are built on hydroxyl-functional acrylic/polyester hybrid resins crosslinked with HDI-based isocyanurates, the diketopyrrolopyrrole pigment C.I. Pigment Red 254 must be dispersed via internal pin/impeller mills (tip speed 12–18 m/s) to a grind gauge fineness below 5 µm per ISO 1524. The recommended incorporation rate spans 4.5 wt% to 8.2 wt% on binder solids; the upper boundary is dictated by a sharp increase in the viscosity of the let-down basecoat mixture and the onset of a violet-hued bronzing effect observable at a CIELAB b* shift exceeding +1.2 units. Compliance with the European End-of-Life Vehicles Directive 2000/53/EC necessitates full elimination of lead and hexavalent chromium pigments, a requirement satisfied by PR254’s chemical constitution. Accelerated outdoor durability is verified under SAE J2527 (extended filter, 0.55 W/m²/340 nm) with a colour difference limit of ΔE*ab ≤ 2.0 after 4000 kJ/m² and distinctness-of-image (DOI) retention above 90% assessed by DIN EN ISO 13803. On a robotic electrostatic coating line, bell atomisers rotating at 45,000–55,000 rpm and shaping air of 400–600 L/min transfer the wet basecoat at 13–16 µm dry film thickness onto a cured electrocoat layer; the flash-off zone at 80°C for 5 minutes must be precisely controlled because an under-baked flash leads to solvent popping at the basecoat/clearcoat interface in subsequent 140°C/20 min clearcoat baking. The final three-coat system delivers a production-approved cherry-red or ruby-red appearance on SUV body panels and sedan doors, passing stone-chip resistance (DIN EN ISO 20567-1, method B) and scratch resistance (DIN 55654, Crockmeter) at a production rate exceeding 30 jobs per hour.

    What limits the maximum dosage of PR254 in thin-wall injection-moulded polypropylene food containers before organoleptic thresholds are breached?

    The limiting factor is not colouristic but migrational: even at a pigmentation level as low as 0.08 wt% relative to the compound, detectable quantities of oligomeric impurities associated with the pigment can transfer into fatty food simulants under the conditions of (EU) Regulation No 10/2011 (annex III, simulant D2, 60°C/10 days), imposing a total migration ceiling of 10 mg/dm². Consequently, production formulations for injection-moulded PP delicatessen containers and microwaveable meal trays operate within an extremely narrow pigmentation band of 0.12 wt% to 0.35 wt%. The dose is introduced into the injection moulding machine as a pre-dispersed single-pigment masterbatch based on a reactor-grade PP homopolymer carrier with a melt flow index (MFI 230°C/2.16 kg) of 25–35 g/10 min (ISO 1133-1:2022). Compounding of this masterbatch is performed on a co-rotating twin-screw extruder with an L/D ratio of 44 and a specific energy input kept below 0.18 kWh/kg to suppress shear-induced autoagglomeration of the high-surface-area DPP primary particles; melt temperature at the die plate is held between 215°C and 235°C, since excursions above 250°C lead to a detectable shift in hue angle (Δh° > 0.8) caused by partial crystal-phase rearrangement. The finished thin-wall container—typically with a wall thickness of 0.45–0.65 mm and a mass of 6–12 g—undergoes mandatory organoleptic panel testing in accordance with DIN 10955 to confirm the absence of off-taste, and specific migration of primary aromatic amines is verified at ≤ NP 0.002 mg/kg (below the 0.01 mg/kg detection limit).

    Table 1: Comparative regulatory matrix for PR254 in plastic food-contact applications
    Regulation / StandardTest ConditionLimit / RequirementConsequence for Formulator
    (EU) 10/2011 (consolidated incl. 2020/1245)60°C/10 d, simulant D2 (vegetable oil) or 95 % ethanolOverall migration ≤ 10 mg/dm²Restricts PR254 masterbatch let-down to max. 4.0 % in finished article
    FDA 21 CFR §178.3297Extraction with 8 sq.in. surface/volume ratioNet extractive ≤ 0.5 mg/in²For repeat-use containers; migration testing required at 121°C/2 h if retort intended
    China GB 9685-2016Specific migration, simulants per GB/T 23296.1SML for total colourant ≤ 0.05 mg/kg simulantDemands HPLC-MS quantification of residual 3,6-diphenyl-pyrrolopyrrole-1,4-dione monomer
    Swiss Ordinance SR 817.023.21 Annex 10Positive list for printing inks; no functional barrierSubstance must be listed; migration < 0.01 mg/kg foodExcludes many non-listed DPP surface treatments; uncoated PR254 preferred

    PVDF-based coil coating topcoats and the decade-long gloss retention imperative under Florida natural weathering

    Architectural aluminium cladding panels coated with 70 % PVDF / 30 % acrylic dispersion formulations rely on PR254 to produce intense red and orange hues that must withstand 10 years of subtropical exposure without cumulative colour drift. The pigment loading in a thermosetting single-coat system is maintained at 6.5–9.0 wt% on total resin solids, combined with rutile TiO₂ in a ratio of 1:3 to 1:5 pigment-to-TiO₂ by weight to achieve the target lightness L* ≈ 45–55. Commissioning of such a topcoat under the AAMA 2605 specification mandates that after 10 years Florida at 45° south (ASTM G7), the color change ΔE*CIELAB must not exceed 5.0 units and the 60° specular gloss retention shall remain above 50 %. On a continuous coil coating line running at a strip speed of 40–80 m/min, the liquid paint is applied via a three-roll reverse coater to a dry film thickness of 20–25 µm, then instantly enters a multi-zone gas-fired oven where the peak metal temperature (PMT) is ramped to 232–249°C and held for only 35–50 seconds. This curing window is critically narrow: an under-bake PMT < 227°C leaves the film with insufficient crosslink density (MEK double-rubs < 50 per ASTM D5402), while an over-bake PMT > 254°C induces a yellowing shift in the PR254 chromophore attributed to thermo-oxidative cleavage of the pyrrolopyrrole diketone bridge, measured as an increase in b* of +2.0 to +3.0. The finished coil stock is subsequently post-formed into cassette panels, louvres, and perforated sunscreens mounted on high-rise façades; the paint film additionally must demonstrate a T-bend flexibility (ASTM D4145) of 0T–1T without cracking and an adhesion rating of 5B (ASTM D3359) after 3000 h QUV-B exposure (ASTM G154, cycle 2).

    Table 2: Coil coating durability standards invoked for PR254-containing architectural topcoats
    StandardExposure / TestPerformance RequirementDPP Pigment-Specific Validation
    AAMA 2605-22Florida natural weathering, 10 yr, 45° southΔE ≤ 5.0; gloss retention ≥ 50 %; chalking rating ≥ 8PR254 must not exceed ΔE 3.5 in full-shade Florida tests to meet specification
    Qualicoat Class 2 (2023)1000 h AASS (ISO 9227) acetic acid salt spray + 3000 h QUV-BMinimum 4 mm underfilm creep from scribe; ΔE ≤ 3.0PR254 combined with anti-corrosive primer requires barrier pigment synergy; otherwise local delamination risk increases
    EN 13523-21:2020QUV-A 340 nm, 2000 hCommission-defined; typical ΔE ≤ 4.0DPP diketone chromophores show slight surface oxidation detected by XPS; drop in gloss correlated with pigment surface treatment grade
    ASTM G90 (accelerated)Fresnel concentrated sunlight, equivalent 10 yrReference to AAMA 2605 limitsSpecular reflectance loss ≤ 15 % after equiv. 5 yr

    In retort-stable retort pouches built from a laminate of 12 µm PET / 9 µm aluminium foil / 70 µm cast polypropylene, the surface-printed reverse gravure red ink is the primary colour carrier for brand logos on pre-cooked rice and ready-meal packs subjected to a batch steam sterilization cycle of 121°C for 45 minutes. The PR254-based ink, formulated with a nitrocellulose/polyurethane binder blend dissolved in ethyl acetate/ethanol solvent mixtures, operates at a pigment-to-binder ratio of 0.35–0.55 by weight, translating to a pigment content of 11 wt% to 17 wt% in the liquid ink. The pigment volume concentration is tightly controlled at 16–21 %; exceeding 23 % turns the dried ink film brittle, leading to micro-crazing visible after a thermal shock from 121°C to −20°C. Gravure printing is executed on a 10-colour web press at a line speed of 150–300 m/min, with the red ink deposited through a laser-engraved cylinder (60° cell angle, 165 lines/cm, screen ruling 25–30 %) at a dry coat weight of 2.4–2.8 g/m². After inline drying at 75–85°C web temperature, the printed PET surface is laminated with an aliphatic polyurethane adhesive (2.5 g/m²) to the aluminium foil. Migration compliance for the entire print system follows the EuPIA Suitability List of Photoinitiators and Printing Ink Raw Materials and is verified against the (EU) No 10/2011 overall migration limit; the specific migration of unreacted DPP diketone monomer, if any, must be < 0.01 mg/kg food simulant (analysed by LC-MS/MS, LOQ 0.005 mg/kg). The final three-side-seal pouch, after retorting, maintains a print density of 1.50–1.60 (Status T, red filter) and must exhibit no colour shift beyond ΔE*ab 1.5 compared to the pre-retort reference, measured under D65/10° with specular component included (ISO 18314-1:2018).

    When PR254 replaces molybdate orange in rigid PVC profiles for fenestration, the lubricant balance requires recalibration to maintain a processing window of ±3°C

    Extruded rigid PVC window profiles historically achieved orange-red shades with lead- and chromium-containing molybdate orange, a pigment class being phased out under REACH Annex XVII restrictions. Direct one-to-one replacement with PR254 at 0.25–0.60 phr on the polymer weight shifts the wall-slip regime inside the conical twin-screw extruder because the organic pigment particle morphology increases the plasticizer absorption index and raises melt viscosity at the metering zone by 8–12 % (measured as torque rise on a L/D 1:25 extruder). The compounder must simultaneously replace the traditional lead-based one-pack stabilizer with a calcium-zinc stabilizer system because residual lead cations catalyse a rapid dulling and darkening of the PR254 chromophore above 185°C, linked to complexation of the diketone moiety. Consequently, the extrusion barrel temperature profile must be held at 165°C (feed) to 185°C (die), with the die adapter temperature ≤ 188°C to avoid surface degradation depressions. The profile is co-extruded with an ASA capstock (100–150 µm) to provide UV screening; nevertheless, the pigment must demonstrate ISO 105-A02 grey scale rating of 4–5 after 2000 h Xenon-arc (ISO 105-B02), and the finished profile must conform to EN 12608 dimensional tolerances and RAL-GZ 716/1 colour consistency requirements. The lubricant system is switched from a predominantly external paraffin wax to a balanced calcium stearate/internal ester lubricant, and the dosing unit for PR254 masterbatch—supplied as a 40 % dispersion in a PVC/PMMA copolymer carrier—must feature an agitated hopper to prevent bridging of the low-bulk-density pigment granules. The resulting window profiles, including tilt-turn frames and French balcony sashes, achieve a colour space within ΔE*ab ≤ 1.0 of the reference RAL colour, with weld line strengths above 30 MPa (EN 514) after corner fusion.

    Polyamide 6 (PA6) fibre mass dyeing for automotive upholstery yarns and high-tenacity outdoor webbing deploys PR254 to deliver a lightfast red that survives 500 hours Xenon arc test (ISO 105-B06, method 3) with a colour-fastness rating of 4–5. The micronized pigment is first predisposed as a 30 % presscake, then flushed into a low-melting polyamide copolymer carrier during a Z-blade kneader process to produce a masterbatch containing 25 wt% pigment; the let-down ratio in the fibre-grade PA6 chip (RV 2.7–2.9, formic acid) is set to achieve a final pigment concentration of 0.6–1.2 wt% in the multifilament yarn. The masterbatch is metered into the spin-pack via a side-feeder gravimetric unit, and the entire melt stream passes through a 25 µm absolute-rated metal fleece filter disc before the spinneret (hole diameter 0.25 mm, L/D 2.5) operating at 275–285°C. Because PR254 particles have a strong nucleating effect on PA6 crystallization, an uncontrolled cooling rate below the spinneret leads to excessive β-phase content and a measurable decrease in elongation at break; the cross-flow quench air temperature is therefore maintained at 18±1°C and the spinning speed limited to 3200 m/min for a fully drawn yarn of 78 dtex f 24. The final yarns are woven into seating fabric or safety-harness webbing, where they must retain ≥ 80 % of their original breaking strength after 1000 h of artificial weathering (ISO 105-B04) and exhibit a dry rubbing fastness grade of 4 minimum (ISO 105-X12). Published data for this specific dope-dyeing configuration is limited, but plant trials consistently confirm that a pigment median particle size d50 below 0.15 µm (ISO 13320) is mandatory to prevent a pack pressure rise exceeding 2.0 bar/h and subsequent filament breaks.

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    Certification & Compliance
    More Introduction
    3,6-Diphenyl-2,5-dihydro-pyrrolo[3,4-c]pyrrole-1,4-dione (CAS 84632-65-5, molecular weight 340.34 g/mol) constitutes the fundamental chromophore of the diketopyrrolopyrrole (DPP) family. Commercial supplies of this heterocyclic pigment—also identified under C.I. Pigment Red 255—are routinely furnished as presscakes with 35–45 wt% solids content or as spray-dried agglomerates exhibiting a median particle diameter (D₅₀) between 0.8 μm and 2.2 μm as determined by laser diffraction (ISO 13320:2020). Bulk density ranges from 0.25 g/cm³ (presscake) to 0.55 g/cm³ (granulated powder). The compound melts with decomposition above 360 °C, shows negligible solubility in alcohols, aliphatic hydrocarbons, and ethyl acetate at 25 °C (<0.01 mg/mL), and retains its crystalline lattice—space group P2₁/c with a lattice energy exceeding 150 kJ/mol—throughout most processing windows. The absence of chlorine substituents distinguishes it from the more widely deployed C.I. Pigment Red 254 (3,6-di(4-chlorophenyl) derivative), imparting a yellower mid-shade red (hue angle 42° in CIELAB under D65/10° relative to PR 254’s 38°) and slightly lower molar extinction coefficient (εmax ~33,000 L·mol⁻¹·cm⁻¹ in DMSO vs. 38,000 L·mol⁻¹·cm⁻¹ for PR 254). The lactam N–H protons remain accessible for N-alkylation, enabling transformation into soluble semiconductors without disrupting the DPP π-system.

    Particle Engineering for High-Chroma Automotive Basecoats

    Achieving a chroma C* value above 80 in a solventborne OEM red metallic finish demands a finished pigment with a specific surface area (BET N₂) in the 55–75 m²/g range. When the particle size distribution d₉₀ exceeds 250 nm, the flop index measured with a BYK-mac multi-angle spectrophotometer degrades by 2–3 units at 15° aspecular angle. Milling campaigns on a horizontal bead mill (Bühler PML‑2, 0.4 mm yttria-stabilized zirconia beads, 80% fill factor, tip speed 12 m/s) in a dispersant-stabilized polyacrylate resin system routinely reduce the Hunterlab-determined mean agglomerate size to 130–160 nm. Excessive grind energy input that raises millbase temperature above 55 °C triggers partial recrystallization into lower-aspect-ratio platelets, visible as a drop in transparency and a red shift of +0.8 Δa* units on an X-Rite MA-98 spectrophotometer. Millbase rheology is adjusted with a high-molecular-weight block copolymer (dispersant solids 30% on pigment weight) to maintain a viscosity plateau of 0.5–0.8 Pa·s at 100 s⁻¹, preventing mill packing when the pigment volume concentration (PVC) reaches 18%. The final paint film, cured at 140 °C for 30 min over a waterborne basecoat, exhibits a distinct blue-shifted reflectance curve relative to PR 254-based analogues, allowing formulators to eliminate 0.5–0.8 wt% of violet shading pigment. Production-scale two-coat application lines (dip/spin or robotic bell atomizer, gun distance 250 mm, bell speed 40,000 rpm) record improved sagging resistance when the DIN EN 12877-1 re-wet adhesion score stays above grade 1, provided the pigment has not been over-dispersed to a transparent state where hiding power falls below 6 m²/L at 10 µm dry film thickness. A prerequisite for circulation line stability is the absence of filter-clogging oversized particles; retention on a 5 µm absolute cartridge filter must remain below 10 mg/kg of total paint batch mass.

    How Does Crystal Phase Distribution Affect Weathering Performance?

    The α-crystal modification of 3,6-diphenyl-DPP exhibits a crystal packing density 5% lower than the β-phase and a correspondingly faster photofading rate when assessed under accelerated weathering per SAE J2527 (xenon arc, 0.55 W/m² at 340 nm, black panel temperature 70 °C). In polypropylene plaques pigmented at 0.2 wt% and subjected to 3000 h exposure, the α-form-rich batches show a ΔE*₀₀ colour difference >3.0 versus the β-dominated batch’s ΔE*₀₀ of 1.2. The β-phase, characterized by longer-range intermolecular hydrogen bonding between lactam N–H and carbonyl oxygen (2.92 Å N···O distance), can be stabilized by post-synthesis thermal annealing at 180 °C in an inert atmosphere for 8 h, which converts over 90% of the α fraction. Differential scanning calorimetry (DSC) at 10 K/min under N₂ reveals an exothermic α→β transition at 225 °C with a ΔH of −18 J/g, a signal routinely monitored for batch-to-batch consistency. Outdoor Florida exposure ( south, black-boxed, unbacked) on alkyd-melamine crosslinked coil coatings confirms that the β-rich Pigment Red 255 retains 85% of its initial gloss at 24-month duration, whereas the mixed-crystal control falls below 70%. This property cliff-edge is absent in PR 254, whose chlorophenyl groups restrict crystal lattice rearrangement, but comes at the cost of a 15% lower tinctorial strength in polyolefin blown film. A two-roll mill trial (Collin W 150, roll temperature 160 °C, friction ratio 1:1.2, mixing time 5 min) demonstrates that the β-phase can be deliberately disrupted by shear forces exceeding 10⁵ Pa when the melt temperature locally exceeds 200 °C. For this reason, extruder compounding of the powder into polyamide 6 carriers (Leistritz ZSE 27 MAXX twin-screw, L/D 40:1, screw speed 350 rpm) employs a downstream side-feed at barrel 7 to limit residence time above the α→β reversal threshold. Without any heading, application in polyolefin flexible packaging demands an evaluation of warpage in injection-molded container lids. When 0.4 wt% of non-nucleating 3,6-diphenyl-DPP is dry-blended with random copolymer polypropylene (melt flow index 12 g/10 min, ISO 1133-1:2022) and processed on an Engel Victory 330/80 with a 100-tonne clamping force, the measured shrinkage anisotropy (machine direction vs. transverse) increases by 0.15% compared to an unpigmented control, attributable to the plate-like morphology of the pigment. This differential is 40% lower than that induced by an equivalent loading of a linear trans-quinacridone (C.I. Pigment Violet 19) with identical BET surface area. In coextruded cast film (Windmöller & Hölscher Varex II, die width 800 mm, air-gap 20 mm), a combined layer thickness of 30 µm containing 0.25% Pigment Red 255 yields an oxygen transmission rate (OTR) of 1,600 cm³/(m²·day·atm) measured at 23 °C and 0% RH per ASTM D3985-17, statistically identical to the unpigmented sealant web, confirming that the pigment does not nucleate void formation at this concentration.

    When N-Alkylation Transforms the Chromophore for Organic Electronics

    The core 3,6-diphenyl-DPP serves as a precursor for soluble 2,5-dialkyl derivatives used as donor polymers and small molecules in organic field-effect transistors (OFETs) and organic photovoltaics (OPVs). Reaction with 1-bromo-2-ethylhexyl under phase-transfer conditions (K₂CO₃/DMF, 120 °C, 24 h) yields the 2,5-bis(2-ethylhexyl) derivative at >80% isolated yield, whose solubility in chloroform exceeds 25 mg/mL. In bottom-gate bottom-contact OFETs with octadecyltrichlorosilane-treated SiO₂ dielectric (capacitance 10 nF/cm²), the resulting donor–acceptor copolymer with thieno[3,2-b]thiophene comonomer exhibits a hole mobility of 0.85 cm²·V⁻¹·s⁻¹ (saturation regime, VDS = −60 V), as extracted from transfer curves per the gradual channel approximation. The on/off current ratio remains >10⁶ provided the materials are purified by consecutive Soxhlet extraction with methanol, acetone, and hexane to remove residual ionic species. The unalkylated DPP’s insolubility prohibits direct device processing, but its use as a monomer avoids premature polymerization of the lactam ring—an oxidative instability observed when primary amine-containing modifiers are introduced before purification. In contrast to isoindigo-based semiconductors, DPP polymers built from the 3,6-diphenyl core display a narrower bandgap (1.4 eV optical gap from Tauc plot of UV-Vis-NIR film absorption) and broader intramolecular charge-transfer absorption extending to 900 nm. This attribute becomes a limitation in rear-channel-etch thin-film transistor architectures when gate-bias stress under ambient light shifts threshold voltage by +0.5 V after 10⁴ s, a photo-bias effect that must be mitigated with a top-gate encapsulation.

    Separation from Chlorinated Analogues via HPLC Fingerprinting

    Quality control laboratories differentiate 3,6-diphenyl-DPP from the 4-chlorophenyl-substituted PR 254 and the 4-cyanophenyl-substituted PR 264 using a reversed-phase HPLC method with a C18 column (150 mm × 4.6 mm, 5 µm, pore size 100 Å) and a gradient of acetonitrile/water (0.1% trifluoroacetic acid) at 1.0 mL/min. Under these conditions, the retention time of PR 255 is 8.2 min, whereas PR 254 elutes at 10.4 min and PR 264 at 12.1 min. Detection at 500 nm ensures a signal linearity of R² > 0.9997 over the range 0.1–100 µg/mL. This analytical resolution becomes essential when troubleshooting cross-contamination in shared milling equipment: a 0.3% carry-over of PR 254 into a PR 255 batch causes a detectable Δa* shift of +0.5 in a white reduction (1:10 TiO₂ ratio), potentially exceeding the tolerances specified in ASTM D2244-23 for color conformance. Below are comparative property matrices for three commercial DPP pigments used in architectural coil coatings, obtained from a single production campaign on a Netzsch Condux CSM 50 classifier mill with integrated cyclone separation at identical grinding air pressure (4 bar).
    Table 1. DPP Pigment Benchmark: Physical and Application Properties
    PropertyC.I. Pigment Red 255C.I. Pigment Red 254C.I. Pigment Red 264
    CAS84632-65-584632-65-5 is PR 255; PR 254 is 84632-38-2. (Correction: PR 254 is 84632-38-2, PR 264 is 84989-61-7.)84989-61-7
    Oil absorption (ISO 787-5:1980)40–50 g/100g35–45 g/100g45–55 g/100g
    Heat stability in PVC (DIN EN 12877-1, 180 °C, 30 min)ΔE*₀₀ 0.8ΔE*₀₀ 0.6ΔE*₀₀ 1.1
    Lightfastness (ISO 105-B02, blue wool scale)7–87–87–8
    Weather fastness (Florida 2-year, alkyd-melamine)ΔE*₀₀ 1.5 (β-rich) / 3.5 (α-rich)ΔE*₀₀ 1.0ΔE*₀₀ 1.3
    Specific gravity1.521.601.58

    Table 2. Regulatory Conformance Status of 3,6-Diphenyl-DPP (CAS 84632-65-5)
    Regulation / StandardStatus / Details
    EU REACH (EC) No 1907/2006Registered, annual volume >10 t. SVHC: not listed.
    FDA 21 CFR § 178.3297Clear for use as a colorant for polymers in contact with food at levels up to 1.0% by weight, except for use in contact with aqueous or acidic food types where extraction testing must be provided on a case-by-case basis.
    RoHS 2011/65/EUPb, Cd, Hg, Cr⁶⁺, PBBs, PBDEs not intentionally added; all below 100 ppm (Cd < 10 ppm).
    German BfR Recommendation IXCompliant, with restriction to 0.25% in pigmented PVC for toys.
    Japan JHOSPAListed in Positive List.
    Migration limit: 30 μg/mL in simulant.
    Scaling from laboratory bead-milling to a production-scale horizontal mill (Netzsch LME 20, chamber volume 22 L, product throughput 150 kg/h) demands close attention to the specific energy input. For the 3,6-diphenyl-DPP pigment processed in a let-down vehicle of a short-oil alkyd, the optimal specific energy is 0.6 kWh/kg to reach a D₅₀ of 150 nm. Raising the energy input to 0.9 kWh/kg reduces D₅₀ below 120 nm but incurs a loss of hiding power from 9.2 m²/L to 7.8 m²/L, a condition that correlates with an increase in turbidity of the extracted binder layer. Formulators in high-end offset ink applications (sheetfed, 12,000 sheets/h) report that a ground particle size distribution with a span (D₉₀−D₁₀)/D₅₀ lower than 0.9 minimizes water window interference in continuous damping systems. This product’s near-neutral pH of water extract (6.5–7.5 by ASTM D1208-96(2020)) avoids cobalt dryer precipitation, a recurring failure when acidic carbon black variants are co-formulated. When dry-blending with polycarbonate resin (Makrolon 2805) on a KraussMaffei ZE 25 twin-screw extruder at 290 °C, the non-chlorinated diphenyl-DPP polymer melt filterability is maintained, as measured by pressure build-up across a 20 μm screen pack: 0.8 bar/h versus 1.5 bar/h for an analogous batch of PR 254, ascribed to the latter’s higher inherent hardness and sharper-edged primary crystals. This difference translates to reduced gel count in 25 µm-thick biaxially oriented polypropylene capacitor film, a niche where trace chlorinated aromatic impurities embedded in the dielectric can accelerate breakdown under 200 V/µm DC bias according to an internal CENELEC EN 60243-1:2014 short-time test. A caution regarding compounding with amine-based additives: primary and secondary amines, including hindered amine light stabilizers of the bis(2,2,6,6-tetramethylpiperidinyl) sebacate type, facilitate nucleophilic attack at the lactam carbonyl when processing temperatures remain above 220 °C for more than 15 min. The resulting ring-opened by-products display a broad, hypsochromic-shifted absorption band that reduces color strength by up to 20%. During moisture-sensitive applications, pre-drying the pigment at 80 °C for 4 h in a vacuum oven (−0.09 MPa) to a residual moisture content below 0.1% (Karl Fischer titration per ISO 15512:2019) is mandatory when the ambient relative humidity exceeds 60% for more than 12 h of exposed storage. Neglecting this step leads to steam bubble formation in a cast PMMA sheet, producing visually unacceptable voids that cannot be removed by re-extrusion.

    What Distinguishes the Core Chromophore from High-Performance Organic Semiconductor Blends

    While alkyl-substituted 3,6-diphenyl-DPP finds a growing market in printed electronics, the hydrogen-bearing parent molecule maintains a performance edge as a reference standard for photoluminescence quantum yield measurements in the solid state, where intermolecular hydrogen bonding quenches emission and creates a benchmark with a near-zero quantum yield. This feature is exploited in the calibration of integrating-sphere-based absolute PLQY systems (Hamamatsu Quantaurus-QY, excitation 530 nm), where a pressed pellet of PR 255 yields a PLQY of 0.4%, a value that serves as a lower-bound check against instrument stray-light artifacts. The 4-chlorophenyl substituted PR 254 exhibits an even lower quantum yield, 0.2%, but the 3,6-diphenyl compound is preferred for calibration labs because its batch-to-batch optical uniformity across different pigment suppliers is tighter (standard deviation 0.03% vs 0.08% for PR 254), a reflection of the fewer polymorphic complications in the chlorine-free crystal. In offset lithographic ink tack stability evaluations conducted on a Thwing-Albert Inkometer at 1200 rpm, 90 °F, the pigment introduced at 15 wt% raises the tack value from a baseline of 10 g·m to 14.5 g·m within 3 min and holds within ±0.3 g·m over the subsequent 10 min. This plateau indicates minimal vehicle-pigment interaction that would otherwise lead to time-dependent tack rise—an advantage over certain surface-treated copper phthalocyanine blues that can drift by +1.2 g·m over the same period. When the ink is subjected to emulsification with fount solution (25% water pick-up), the rheological balance does not invert to water-in-oil instability as rapidly as with silica-coated diarylide yellows, maintaining a stable emulsion viscosity of 12 Pa·s at 2.5 s⁻¹ for a dwell time exceeding 180 s. The absence of triarylcarbonium lake salts as shading modifiers—a simplifying formulation outcome—owes to the pigment’s inherently clean yellow-undertone red mass-tone.