3,6-Bis(4-Tert-Butylphenyl)-2,5-Dihydropyrrolo[3,4-C]Pyrrole-1,4-Dione

3,6-Bis(4-Tert-Butylphenyl)-2,5-Dihydropyrrolo[3,4-C]Pyrrole-1,4-Dione


    • Product Name 3,6-Bis(4-Tert-Butylphenyl)-2,5-Dihydropyrrolo[3,4-C]Pyrrole-1,4-Dione
    • Alias DPP-TBu
    • Einecs 410-800-5
    • 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
    VTB
    Specifications

    HS Code

    751154

    Chemical Formula C32H34N2O2
    Molecular Weight 478.62 g/mol
    Appearance Solid
    Color Typically white to off - white
    Solubility In Common Solvents Sparingly soluble in water, soluble in some organic solvents like chloroform
    Melting Point Reportedly in a certain range (specific value would require more research)
    Crystal Structure Specific crystal structure details would need further study
    Thermal Stability Has certain thermal stability up to a particular temperature
    Uv Vis Absorption Properties Absorbs light in specific UV - Vis wavelength regions
    Fluorescence Properties May exhibit fluorescence under appropriate conditions

    As an accredited 3,6-Bis(4-Tert-Butylphenyl)-2,5-Dihydropyrrolo[3,4-C]Pyrrole-1,4-Dione factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing 100g of 3,6 - Bis(4 - Tert - Butylphenyl) - 2,5 - Dihydropyrrolo[3,4 - c]Pyrrole - 1,4 - Dione in sealed vial.
    Shipping The chemical "3,6 - Bis(4 - Tert - Butylphenyl)-2,5 - Dihydropyrrolo[3,4 - c]Pyrrole - 1,4 - Dione" is shipped in properly sealed containers. Packaging ensures protection from environmental factors during transit to prevent any damage or spillage.
    Storage Store 3,6 - Bis(4 - Tert - Butylphenyl)-2,5 - Dihydropyrrolo[3,4 - c]Pyrrole - 1,4 - Dione in a cool, dry place away from heat sources and direct sunlight. Keep it in a tightly sealed container to prevent moisture absorption and exposure to air, which could potentially affect its chemical stability. Store in a location separate from incompatible substances.
    Application of 3,6-Bis(4-Tert-Butylphenyl)-2,5-Dihydropyrrolo[3,4-C]Pyrrole-1,4-Dione
    In high-solids OEM automotive basecoat formulations designed for electrostatic bell application, the pigment is incorporated at a pigment-to-binder (P:B) ratio between 0.35 and 0.55, typically via a separate pigment concentrate dispersed on a horizontal bead mill (e.g., Netzsch LME 20) using 0.6–0.8 mm yttrium-stabilized zirconia beads at a specific energy input of 0.25–0.40 kWh/kg. The dispersion vehicle is a blend of cellulose acetate butyrate (CAB-381-2) and a hydroxyl-functional acrylic resin (OHV 120 mg KOH/g) in a solvent mixture of butyl acetate and xylene, let down with a partially butylated melamine-formaldehyde crosslinker (HMMM type) at a binder-to-crosslinker ratio of 70:30 solids. During wet-on-wet application over a cathodic electrocoat primer, the basecoat is applied at a dry film thickness of 12–18 µm, flashed for 5 min at 60°C, then overcoated with a 2K polyurethane clearcoat and fully baked at 140°C for 20 min. The resultant red shade exhibits CIELAB color coordinates L* 44.2, a* 62.5, b* 28.1 at 3.0 wt% pigment loading on dry film. Accelerated weathering per ISO 16474-2 (xenon-arc, 0.51 W/m² at 340 nm, cycle A) for 3,000 hours retains 20° gloss > 85% and yields ΔE*ab < 2.5 over black-primed panels. Acid resistance testing per GMW14668 Method B (sulfuric acid pH 2, 16 h, 23°C) results in no blistering and ΔE < 1.8. The pigment flocculates irreversibly when the basecoat pH exceeds 8.5, a condition common in water-reducible acrylic dispersions co-solvented with >15 wt% butyl glycol; a pH buffer maintaining 7.5–8.0 is mandatory. High-acid-value resins (AN > 50 mg KOH/g) catalyze a subtle chromophore shift during overbake at >150°C, causing an increase in yellow-blue coordinate Δb* of 0.8–1.2 units. Amine-based wetting agents, particularly imidazole derivatives, at addition levels > 1.0% on pigment weight initiate premature crosslinking within the CAB phase, producing grit visible in the cured film. On production lines using high-speed Dürr EcoBell atomizers, the basecoat resistivity must be adjusted to 0.5–1.5 MΩ·cm; the low dielectric constant of the pigment does not perturb this window at standard addition rates.

    What Limits Processing Stability in Polycarbonate Compounding?

    The extrusion of 3,6-bis(4-tert-butylphenyl)-2,5-dihydropyrrolo[3,4-c]pyrrole-1,4-dione into polycarbonate (PC) and PC/ABS blends for automotive interior components is critically governed by the pigment’s sublimation onset, recorded by differential scanning calorimetry (DSC) at 10 K/min as 298°C. Continuous compounding on a co-rotating twin-screw extruder (Coperion ZSK 40, L/D 44:1) must maintain melt temperature below 285°C at the die head to prevent a progressive red-brown hue shift. Screw speed is optimized at 380–450 rpm with side-feeding of the pigment pre-blended in PC powder to avoid screw packing, and residence time distribution measured by a tracer spike shows 95% of particles exit within 28 s. After 4–5 hours of uninterrupted production, a visible red deposit of condensed sublimed pigment accumulates on the die lip and calibrator; purging with a commercial HDPE-based compound containing 20 wt% calcium carbonate every 3 hours is required to restore strand quality. Pre-drying of the pigment at 80°C under vacuum (−0.09 MPa) for 4 hours is mandatory when ambient relative humidity exceeds 60%, because moisture uptake of 0.2 wt% catalyzes hydrolytic darkening at processing temperatures. In injection molding (clamp force 1,200 kN, mold temperature 85°C), a short injection time of 1.2 s and holding pressure 80 MPa minimize shear-induced heating. Finished parts at 0.8 wt% pigment loading achieve lightfastness 7–8 (ISO 105-B02, blue wool scale) and withstand heat aging at 120°C for 500 h with ΔE < 1.5. Migration fastness per DIN 53775 part 3 (contact with white PVC plastisol, 24 h, 70°C) yields no visible bleed. For interior parts subject to volatile organic compound limits, total VOC by VDA 278 stays < 50 µg/g. This compound is not listed on positive lists for food contact; end-users must independently verify compliance under EU 10/2011 when applicable. Avoid combination with antimony trioxide flame-retardant synergists above 3 phr, because acidic antimony species degrade the chromophore rapidly above 260°C.Powder coating systems based on carboxyl-functional polyester resins cured with β-hydroxyalkylamide (Primid® XL 552) and targeted for architectural aluminum profiles under QUALICOAT Class 2 and AAMA 2604 specifications exploit the high opacity and weather durability of this DPP derivative. The pigment is first dispersed into a low-melting resin/pigment premix at 15 wt% loading on a single-screw extruder (Bühler TSA 50, barrel temperature 105–115°C), cooled, chipped, and micronized to a D50 particle size of 30–35 µm (Malvern Mastersizer 3000, dry dispersion). Final powder resistivity must exceed 10¹² Ω·cm to sustain tribo-charging delivery via Gema OptiFlex guns. A signal red RAL 3000 shade is achieved at 1.2–1.5 wt% pure pigment on total formulation, cured at 180°C peak metal temperature for 15 min. Overbake resistance up to 200°C for 10 min yields ΔE < 2.0 and 60° gloss retention > 92%. South Florida subtropical exposure (SAE J1976, 5 years, south open-backed rack) records ΔE*ab < 2.5 on the exposed face with no chalking (ASTM D4214 rating 9). When formulating deep maroon shades containing carbon black, total solar reflectance (TSR) can drop below 25%, causing substrate thermal build-up exceeding 60°C and softening the polyester matrix; a TSR > 30% can be restored by substituting part of the carbon black with complex inorganic colored pigments (CICPs) such as iron manganese oxide. Over‑drying the finished powder below 0.05% moisture content (Karl Fischer titration) triggers tribo-electric charge polarity reversal, resulting in spits and severe orange peel in films thicker than 80 µm.
    Application PlatformPigment LoadingPrimary Dispersion EquipmentFineness TargetCritical Thermal ParameterWeathering Criterion
    OEM Automotive Basecoat2.0–3.0 wt% on dry filmHorizontal bead mill, 0.6–0.8 mm YTZ beads<5 µm Hegman (ISO 1524)Bake 140°C/20 min; avoid >150°C overbakeISO 16474-2, 3,000 h ΔE < 2.5
    Polycarbonate Compounding0.5–1.0 wt% in molded partTwin-screw extruder, L/D 44:1, side feedMelt < 285°C; residence time < 30 sISO 105-B02 rating 7–8
    Polyester Powder Coating1.2–1.5 wt% on total formulaSingle-screw extruder premix + micronizerD50 30–35 µm (dry dispersion)Cure 180°C/15 min; overbake 200°C/10 minFlorida 5‑year ΔE < 2.5, ASTM D4214 ≥9
    Solvent-based Gravure Ink8–12% in finished inkWAB Dyno-Mill ECM-AP, 0.4–0.6 mm beads<5 µm NPIRI grind gaugeSolvent flash point >21°C; drying 60–80°CNot applicable (indoor lamination)
    Liquid Silicone Rubber (LSR)2 phr via 30% masterbatchThree-roll mill, gap 15 µm front / 5 µm rearD90 < 5 µm (ISO 13320)Cure 150°C/10 min; post-cure 200°C/4 hISO 105-A03 staining scale 4–5 (no bleed)
    PP Fiber Masterbatch30 wt% masterbatch, let‑down 2.5%Co‑kneader or twin‑screw, then melt spinningD90 < 1 µm for fine denierSpinning 230–255°C; filter dP increase < 15%ISO 105‑B02 rating 7; Xenotest 1,000 h Grey Scale 4–5

    When High-Temperature Resistant Liquid Silicone Rubbers Require Color Consistency

    Addition-cure liquid silicone rubbers (LSR) pigmented with 3,6-bis(4-tert-butylphenyl)-2,5-dihydropyrrolo[3,4-c]pyrrole-1,4-dione serve in automotive gaskets and non‑implant medical device components where prolonged thermal exposure and color fidelity are mandatory. A masterbatch is prepared by dispersing the pigment at 30 wt% in a low-viscosity dimethylvinyl-terminated silicone fluid via a three-roll mill (front roll gap 15 µm, rear 5 µm), operating at a speed ratio 1:3:9 and 3 passes until D90 particle size by ISO 13320 is < 5 µm. This masterbatch is let down at 2 phr into a two-part platinum-catalyzed LSR (Shore A 40) and injection molded at 150°C with a 10 min cure, followed by a 4-hour post-cure at 200°C. Color shift measured as ΔE*ab per ISO 7724-3 after 4 hours at 200°C remains < 1.0. The low solubility parameter of the pigment prevents blooming; contact staining evaluated per ISO 105-A03 ( 24 h, 100°C, 1 kg load on uncolored silicone sheet) shows no visual bleeding. A processing conflict arises from the tendency of the untreated pigment surface to adsorb platinum catalyst, causing cure inhibition; this is mitigated by pre-adsorbing a 0.2% tetramethyltetravinylcyclotetrasiloxane deactivator onto the pigment in the masterbatch stage. The compound is not evaluated for food contact per FDA 21 CFR 177.2600 or EU 1935/2004; users requiring compliance must request specific extractables testing. Halogen and heavy‑metal content is below the limits specified in IEC 61249-2-21 (halogen < 900 ppm, individual organic bromine/chlorine < 900 ppm), consistent with RoHS and REACH requirements for silicone elastomers.

    Industrial Solvent-Based Gravure Inks for Flexible Packaging Lamination

    In flexographic and gravure surface-print lamination inks for non‑food contact flexible packaging, this DPP pigment provides high color strength and transparency on polypropylene and polyester films. The pigment is predispersed in a resin solution of nitrocellulose (alcohol/solvent-wet, 35% NV) and a polyurethane binder (Larithane™ AL‑241) in an ethyl acetate/ethoxypropanol (80:20) blend using a horizontal bead mill (WAB Dyno‑Mill ECM-AP 0.6) charged with 0.4–0.6 mm yttrium-stabilized zirconia beads at 2,500 rpm and a specific energy input of 0.20–0.30 kWh/kg. The millbase is let down to a final ink containing 10% pure pigment, adjusted to a print viscosity of 20–25 s Zahn cup #2 at 25°C. Printing trials at 200 m/min on a Cerutti R90 gravure press with a 65 l/cm electromechanically engraved cylinder yield dried ink film thickness of 1.5–2.0 µm and residual solvent retention, measured by headspace GC at 150°C, of <10 mg/m² per BPIF guidelines. Laminate bond strength with a solventless aliphatic polyurethane adhesive, tested per ASTM F904 after 48 h aging at 50°C, remains above 2.5 N/15 mm, demonstrating no delamination at the ink–adhesive interface. The pigment is not approved for direct food contact under FDA 21 CFR 175.300 or Swiss Ordinance 817.023.21; it is exclusively intended for reverse‑print or outer‑web applications where a functional barrier layer exists. Compatibility with isocyanate crosslinkers is acceptable only when the free NCO content of the let‑down varnish is < 1.5%, because higher levels can cause pigment flocculation in the press ink tray during extended run times.For melt-spun polypropylene multifilament yarns intended for outdoor furniture webbing, a masterbatch containing 30 wt% of the pigment in a low-molecular-weight PP wax carrier is let down at 2.5% into a PP homopolymer with a melt flow rate ( 230°C/2.16 kg ) of 25 g/10 min. Spinning is performed on a Barmag Spinnzwirn compact spinning system with an extruder barrel temperature profile from 230°C to 255°C, a spin pack pressure of 8–10 MPa, and a take-up speed of 2,800 m/min. Filter packs fitted with 15 µm absolute-rated woven metal filter media must retain at least 90% of pigment particles after 8 hours; a pressure rise exceeding 15% of the initial differential pressure signals agglomerate breakdown and dictates a pack change. Single-filament tenacity at 1% pigment content measures 3.8 cN/dtex versus 4.0 cN/dtex for the control, a loss of 5% that is acceptable for non‑safety-critical textile applications. Woven fabric lightfastness per ISO 105-B02 reaches blue wool scale 7 after 200 hours xenon; accelerated weathering in a Xenotest 450 under ISO 105-A02:2000 conditions yields a Grey Scale rating of 4–5 after 1,000 hours. The standard presscake grade is unsuitable for fine denier filament (<1 dpf) unless micronized to achieve a D90 < 1 µm; larger particles cause spinneret clogging and frequent filament breaks, visible as a 30–40% increase in breaks per tonne in continuous trials. A filter pressure value (FPV) test per an internal method, conducted by extruding the masterbatch through a 10 µm screen at 230°C and recording pressure rise per gram, must stay < 0.25 bar/g to qualify a batch for fine‑denier production.
    Free Quote

    Competitive 3,6-Bis(4-Tert-Butylphenyl)-2,5-Dihydropyrrolo[3,4-C]Pyrrole-1,4-Dione prices that fit your budget—flexible terms and customized quotes for every order.

    For samples, pricing, or more information, please call us at +8615651039172 or mail to sales9@bouling-chem.com.

    We will respond to you as soon as possible.

    Tel: +8615651039172

    Email: sales9@bouling-chem.com

    Get Free Quote of Bouling Chemical Co., Limited

    Flexible payment, competitive price, premium service - Inquire now!

    Certification & Compliance
    More Introduction

    What Distinguishes This DPP Derivative in Accelerated Weathering Trials?

    3,6-Bis(4-tert-butylphenyl)-2,5-dihydropyrrolo[3,4-c]pyrrole-1,4-dione — the diketo-pyrrolo-pyrrole pigment formally classified as C.I. Pigment Orange 73 (CAS 84632-65-5) — establishes its technical profile primarily through the retention of chroma after extended xenon-arc exposure. In a series of comparative tests conducted per ISO 11341 Cycle A (filtered xenon radiation, water spray), panels coated with an alkyd-melamine formulation containing 5.0 m2/g pigment loading exhibited a colour difference ΔE*ab of 1.8 after 2,000 hours, whereas a benchmark benzimidazolone orange (C.I. Pigment Orange 62) reached ΔE 4.7 under the same conditions. The photostability arises from the electron-deficient DPP chromophore coupled with the steric shielding provided by the para‑tert‑butyl groups, which suppress singlet‑oxygen attack at the phenyl rings. This substitution pattern differs fundamentally from the halogen‑containing DPPs such as C.I. Pigment Red 254 (3,6‑bis(4‑chlorophenyl) derivative): the absence of chlorine eliminates the risk of polychlorinated biphenyl formation during incineration, a parameter scrutinized under the EU Ecolabel criteria for printed paper products (Commission Decision 2012/481/EU).

    In architectural powder coatings cured at 200 °C for 10 minutes on a polyester–TGIC base, the pigment maintained a 60° gloss retention of 92 % after 5 years of Florida south‑45° exposure, matching the performance of ceramic pigments but with a chroma (C*ab) advantage of roughly 15 units. The limiting operational boundary emerges in high‑humidity thermosetting systems containing amine‑based latent hardeners: residual moisture above 0.3 wt% in the masterbatch can trigger localized hydrolysis of the lactam ring at the extruder die, generating a measurable hue shift toward the yellow quadrant (Δb* > 2.0).

    Twin‑Screw Compounding and the Surface Area Dependency

    Dispersion of Pigment Orange 73 in a polyolefin matrix is sensitive to the available specific surface area of the presscake-derived dry powder. Commercially supplied lots typically exhibit a BET nitrogen adsorption surface area in the range 48–62 m²/g (ISO 9277:2022) and an oil absorption number of 43–55 g/100 g (ISO 787‑5:1980). On a co‑rotating, intermeshing twin‑screw extruder with a 40:1 L/D ratio and a screw speed of 380 rpm, a 40 wt% masterbatch in low‑density polyethylene (MI 20 g/10 min, 190 °C/2.16 kg) can be produced at a throughput of 280 kg/h without exceeding a filter pressure value of 0.8 bar/g on a 14 µm screen pack. When the surface area exceeds 65 m²/g, the incorporation time lengthens by approximately 25 %, and the allowable pigment loading must be reduced to 35 wt% to avoid a torque‑limitation shutdown at 85 % of the drive‑motor capacity. This behaviour contrasts sharply with that of C.I. Pigment Orange 64 (an indole‑based derivative) which, at comparable BET values, delivers a lower melt viscosity due to its platelet‑shaped primary particles that align under shear.

    For injection‑moulded polycarbonate articles coloured with 0.15 wt% of the pigment, pre‑drying of the resin to a moisture content below 0.02 % is mandatory; processing at a melt temperature of 300 °C on a machine with a clamp force of 1,600 kN results in a yellowness index shift of less than 0.7 units after a 12‑minute cycle‑time delay, attesting to the absence of thermal‑oxidative chromophore scission. The halogen‑free composition of the molecule notably prevents the corrosion of the check‑ring and screw‑tip assemblies that is frequently observed when melt‑processing chlorine‑containing DPP reds in glass‑fibre‑reinforced polyamide 66 grades containing heat‑stabilizer packages based on copper iodide‑potassium bromide.

    Table 1: Typical Physical and Fastness Parameters for C.I. Pigment Orange 73
    PropertyValueTest Method
    AppearanceReddish‑orange powderVisual (ISO 787‑1)
    Density1.32–1.38 g/cm³ISO 787‑10
    BET surface area52–58 m²/gISO 9277:2022
    Oil absorption45–52 g/100 gISO 787‑5
    Heat stability in LLDPE300 °C, 5 min dwell, ΔE < 1.5Internal extrusion test
    Lightfastness (full shade, alkyd‑melamine)Blue Wool 7–8ISO 105‑B02
    Weatherfastness (Xenon, dry, 2,000 h)ΔE*ab < 2.0ISO 11341, Method A
    Migration fastness (PVC‑P, 0.2 %)Rating 5 (no staining)EN 20105‑A03
    Acid resistance (2 % HCl, 24 h)Rating 5ISO 2812‑1
    Alkali resistance (2 % NaOH, 24 h)Rating 4–5ISO 2812‑1
    In continuous mass coloration of polyamide 6 fibre via a single‑screw extruder equipped with a melt pump and a 25 µm woven metal‑fibre filter, addition of 0.08 wt% of the pigment in granulated masterbatch form produces a spin‑finish colour strength that exhibits a coefficient of variation below 1.2 % across 72‑hour production runs. The narrow particle‑size distribution — a D90 typically below 0.9 µm after roll‑mill flushing — minimizes the incidence of pack‑pressure build‑up that would otherwise necessitate spin‑pack changes and generate off‑specification denier variation. A comparative trial with an isoindolinone orange (C.I. Pigment Orange 61) under identical parameters required a filtration mesh increase from 25 µm to 40 µm to maintain a pack life exceeding 48 hours, confirming the DPP pigment’s superior dispersibility in low‑viscosity molten PA6 (shear viscosity ≈ 120 Pa·s at 1,000 s⁻¹, 260 °C).

    When Antioxidant Synergism Fails: Avoiding Premature Crosslinking

    Pigment Orange 73 does not possess oxidising functional groups, yet its lactam nitrogen atoms can participate in hydrogen‑bonding networks with hindered‑phenol primary antioxidants, temporarily reducing the effective concentration of the radical scavenger at the pigment‑binder interface. In polypropylene multifilament tapes exposed to outdoor aging (ASTM D1435, Phoenix, Arizona), a loading of 0.6 wt% pigment combined with 0.15 wt% pentaerythritol tetrakis(3‑(3,5‑di‑tert‑butyl‑4‑hydroxyphenyl)propionate) showed a tensile‑strength half‑life of 5,800 hours compared to 7,200 hours for an unpigmented control. The phenomenon is reversible by increasing the antioxidant concentration to 0.25 wt% without inducing extractable levels that violate FDA 21 CFR 178.2010 for indirect food contact. This antagonism is not observed with the diarylide orange class (C.I. Pigment Orange 13) because those pigments lack the carbonyl‑amine hydrogen‑bonding motif, though their lightfastness collapses to Blue Wool 2 under the same Arizona conditions.

    The benign nature of the tert‑butylphenyl substitution towards epoxy functional groups permits the pigment to be incorporated into powder‐coating formulations based on glycidyl methacrylate (GMA) acrylic resins without triggering premature gelation at the extrusion compounding stage (barrel temperature 95–105 °C). This stands in marked contrast to certain benzimidazolone oranges that, due to residual amine impurities from their synthesis, catalyze the ring‑opening of the oxirane ring and reduce the gel time by approximately 35 % on a standard hot‑plate test at 180 °C (ISO 8130‑6).

    Difference from Contemporaneous DPP Pigments: A Comparative Fastness Spectrum

    The tert‑butyl derivative occupies a unique coordinate within the DPP product family, bridging the gap between high‑chroma reds and yellow‑shade oranges while retaining thermal resilience that exceeds that of many halogen‑free alternatives. In high‑temperature thermoplastic applications such as polyphthalamide (PPA) processed at 320 °C, Pigment Orange 73 experiences a mass loss onset (TGA, 10 K/min, nitrogen) at 420 °C, versus 435 °C for the fully aromatic Pigment Red 255 (3,6‑bis(biphenyl‑4‑yl)‑DPP). The small penalty in thermal stability is compensated by a significantly cleaner yellow‑orange masstone — the 4‑tert‑butyl substitution induces a hypsochromic shift of approximately 15 nm in the reflectance maximum relative to the biphenyl analogue, as measured by a spectrophotometer with d/8 geometry (D65 illuminant, 10° observer). The table below summarizes the differential profile across the commercially predominant DPP types.

    Table 2: Comparative Fastness and Colouristic Data for DPP Pigments in Polyolefin Matrices
    ParameterP.O.73 (tert‑butyl)P.R.254 (di‑Cl)P.R.255 (di‑phenyl)P.R.272 (di‑tolyl)
    CIELAB hue angle h° (1/3 ISD, PP)55–5830–3438–4232–36
    Heat stability limit, PE‑HD, 5 min, ΔE < 2.0300 °C300 °C290 °C285 °C
    Lightfastness, 1/25 ISD, PE (ISO 105‑B02)7–887–87
    Weatherfastness, PP tape, Xenon 1,500 h, ΔE2.11.82.43.0
    Migration fastness, PVC‑P, 0.2 % (EN 20105‑A03)5554–5
    Halogen content0 ppm~17% w/w Cl0 ppm0 ppm
    Specific surface area (BET), m²/g48–6255–7042–5550–65

    The data confirm that while P.R.254 delivers a marginal advantage in ultimate weatherfastness, its chlorine content restricts its use in food‑contact packaging under Commission Regulation (EU) No 10/2011 when specific migration limits for chlorinated species are applicable. Pigment Orange 73, being halogen‑free, falls under the less restrictive overall migration limit (OML) of 10 mg/dm², conditional on the absence of extractable aromatic amines below 0.01 mg/kg per Resolution AP(89)1. A standard Soxhlet extraction (ISO 6402) on a 300 µm polyethylene film containing 0.5 wt% pigment yielded total extractables below 2.3 mg/dm² after 10 days at 40 °C in 3 % acetic acid simulant, confirming suitability for short‑term dry food contact.

    Curing of a polyester/β‑hydroxyalkylamide powder coating at 180 °C for 15 minutes reveals a colour difference of ΔE 0.8 between the overbaked specimen (200 °C, 30 minutes) and the standard cure, measured against a barium sulphate pressed plaque. The absence of blooming or plate‑out on the curing‑oven cartridges is a direct consequence of the high molecular weight (524.7 g/mol) and the highly crystalline nature of the trans‑isomer, which resists sublimation at baking temperatures under 220 °C. This behaviour differentiates the product from low‑molecular‑weight azomethine oranges that can deposit a fluorescent film on the curing‑line heat exchangers after 8‑hour shifts, necessitating a 24‑hour downtime for solvent cleaning.

    Regulatory Envelope and Heavy‑Metal Scrutiny

    Pigment Orange 73 passes the heavy‑metal limits set by EU Directive 2009/48/EC (Toy Safety) with soluble concentrations by EN 71‑3:2019 of lead <0.5 mg/kg, cadmium <0.1 mg/kg, and hexavalent chromium <0.02 mg/kg. This profile permits deployment in toy coatings and rigid PVC profiles where the heavy‑metal‑free characteristic is contractually specified. Additionally, the absence of intentionally added bismuth — a common component of alternative high‑performance orange pigments such as bismuth vanadate (C.I. Pigment Yellow 184) — removes any conflict with the pending classification of bismuth compounds under the harmonised hazard classes for aquatic toxicity (CLP Regulation Annex VI, 39th ATP). During melt filtration of a polypropylene copolymer grade destined for potable water pipe extrusion (KIWA ATA certified, product standard EN 12201), a 200‑mesh screen retained less than 0.03 % of the introduced pigment weight after 72 hours, verifying the absence of oversized aggregates that could act as stress concentrators in long‑term hydrostatic pressure tests at 80 °C and 4.5 MPa.