|
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 | 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. |
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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).
PVDF-based coil coating topcoats and the decade-long gloss retention imperative under Florida natural weatheringArchitectural 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).
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°CExtruded 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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| Property | C.I. Pigment Red 255 | C.I. Pigment Red 254 | C.I. Pigment Red 264 |
|---|---|---|---|
| CAS | 84632-65-5 | 84632-65-5 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/100g | 35–45 g/100g | 45–55 g/100g |
| Heat stability in PVC (DIN EN 12877-1, 180 °C, 30 min) | ΔE*₀₀ 0.8 | ΔE*₀₀ 0.6 | ΔE*₀₀ 1.1 |
| Lightfastness (ISO 105-B02, blue wool scale) | 7–8 | 7–8 | 7–8 |
| Weather fastness (Florida 2-year, alkyd-melamine) | ΔE*₀₀ 1.5 (β-rich) / 3.5 (α-rich) | ΔE*₀₀ 1.0 | ΔE*₀₀ 1.3 |
| Specific gravity | 1.52 | 1.60 | 1.58 |
| Regulation / Standard | Status / Details |
|---|---|
| EU REACH (EC) No 1907/2006 | Registered, annual volume >10 t. SVHC: not listed. |
| FDA 21 CFR § 178.3297 | Clear 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/EU | Pb, Cd, Hg, Cr⁶⁺, PBBs, PBDEs not intentionally added; all below 100 ppm (Cd < 10 ppm). |
| German BfR Recommendation IX | Compliant, with restriction to 0.25% in pigmented PVC for toys. |
| Japan JHOSPA | Listed in Positive List. Migration limit: 30 μg/mL in simulant. |