|
HS Code |
233773 |
| Chemical Formula | C28H31N |
| Molecular Weight | 379.55 g/mol |
| Appearance | Solid |
| Melting Point | 162 - 166 °C |
| Solubility | Soluble in organic solvents like dichloromethane, chloroform |
| Purity | Typically high purity for research grade |
| Odor | Odorless (usually) |
| Stability | Stable under normal conditions, protect from light and moisture |
As an accredited 2,4-Bis(4-(Tert-Butyl)Phenyl)-1H-Pyrrole factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | 100g of 2,4 - Bis(4 - (Tert - Butyl)phenyl)-1H - Pyrrole in a sealed chemical - grade container. |
| Shipping | 2,4 - Bis(4 - (Tert - Butyl)phenyl)-1H - Pyrrole is shipped in properly sealed containers, following strict chemical transport regulations. Packing ensures protection from environmental factors during transit to prevent any leakage or degradation. |
| Storage | Store 2,4 - Bis(4 - (Tert - Butyl)phenyl)-1H - Pyrrole in a cool, dry place, away from direct sunlight and heat sources. 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. |
In the production of cast and blown polyolefin packaging films running at line speeds exceeding 250 m/min, maintaining optical clarity and seal integrity depends critically on suppressing radical-driven chain scission during the extrusion and air-gap phase. 2,4-Bis(4-(tert-butyl)phenyl)-1H-pyrrole is incorporated into LLDPE or homo-PP formulations at concentrations ranging from 0.08 to 0.20 wt%, typically co-stabilised with a hydrolytically stable phosphite processing stabiliser (e.g., tris(2,4-di-tert-butylphenyl) phosphite) at a 1:2 to 1:3 ratio. The phosphite handles melt-phase hydroperoxide decomposition during extrusion barrel temperatures of 220–260°C, while the pyrrole derivative intercepts carbon-centred radicals formed when the melt emerges from the die gap and contacts atmospheric oxygen. The synergistic ratio is optimised via oven ageing at 90°C and differential scanning calorimetry: isothermal OIT at 190°C per ASTM D3895 and dynamic OIT per ISO 11357-6:2022. On a Reifenhäuser cast-film line equipped with a gravimetric feeding system, the additive is pre-blended via a high-intensity mixer to a 5% compound masterbatch using carrier resin with MFR 8 g/10 min, then let down at the extruder throat. Field experience shows that masterbatch inhomogeneity—detected as additive speck counts above 2 per m²—can lead to gel particle formation downstream, requiring screen pack changes after 8–10 h of operation. The final film exhibits residual pyrrole content after processing, detected by LC-MS extraction, which is critical for food contact compliance. Under (EU) No 10/2011, the compound currently does not appear on the Union List of authorised substances; hence its use in films intended for food contact requires a declaration of compliance supported by migration testing (overall migration <10 mg/dm² and specific migration of the substance below the default 0.01 mg/kg limit, unless toxicological data justify a higher SML). For non-food industrial shrink films and heavy-duty sacks the regulatory constraint is relaxed, and the stabilising efficiency becomes the primary metric. End articles include laminated snack packaging, pet food liners, and collation shrink films where maintenance of burst strength after 12-month ambient storage is specified.What Limits the Service Life of Glass-Fibre-Reinforced PP Components in Under-Bonnet Environments?Long-term thermal resistance in glass-fibre-reinforced polypropylene (PP-GF) used for engine covers and intake manifolds demands a stabiliser package that withstands peak temperatures of 140–150°C. The pyrrole compound is incorporated at 0.3–0.8 wt% in combination with a thioester synergist such as distearyl thiodipropionate (DSTDP) at a 1:1.5 ratio, added during compounding on a co-rotating twin-screw extruder with an L/D of 44:1 and a melt temperature of 230–245°C. The stabiliser blend is first coated onto the PP powder via a high-speed blender to ensure homogeneous distribution before the 30 wt% short-glass-fibre addition. Injection moulding is performed with a clamp force of 800–1200 tonnes, mould temperature 60–80°C. Accelerated heat ageing is conducted per ISO 188 at 150°C in a forced-air oven; tensile strength retention of at least 70% after 2000 h is the typical specification for under-bonnet applications. Simultaneous fogging test according to DIN 75201 (gravimetric method, 100°C for 16 h) must yield condensate mass below 2 mg, while VDA 277 total volatiles are kept under 50 µg C/g. An operational boundary encountered on production floors is that contact with copper-containing heat stabilisers or residual catalyst traces from propylene polymerisation can deactivate the pyrrole radical trap and cause a sharp loss in OIT—such combinations are strictly avoided and require purging of the alloy system before changeover. The finished moulded parts are tested for tensile strength per ISO 527-2 and charpy impact per ISO 179-1.
When Non-Halogenated, Low-Molecular-Weight Hole Transport Materials Are Processed via Slot-Die CoatingSolution-processed organic electronics and perovskite photovoltaics demand hole-transport layers (HTL) that form pin-hole-free amorphous films without parasitic absorption. The tetra-substituted pyrrole, dissolved in anhydrous toluene or o-xylene at a concentration of 10–20 mg/mL, is deposited on patterned ITO substrates via a slot-die coater with a coating gap of 150–200 µm and substrate temperature 60°C. The wet film is annealed at 120°C for 20 min inside a nitrogen glovebox, yielding a dry thickness of 30–50 nm with a root-mean-square roughness below 0.8 nm measured by AFM in tapping mode. The ionization potential of the solid film, determined by photoelectron yield spectroscopy in air, falls near 5.45 eV, a close energetic alignment to the valence band of MAPbI₃ absorbers. This permits efficient hole extraction without doping, while the tert-butylphenyl substituents suppress crystallisation and maintain morphological stability under an operating temperature of 85°C. Published data for this specific molecular configuration in operational OLED stacks is limited, but preliminary screening on laboratory-scale devices (ITO/PEDOT:PSS/HTL/emissive layer/LiF/Al) shows a turn-on voltage below 3.5 V at 10 mA/cm². Manufacturing integration requires careful control of the coating atmosphere to keep dew point below −40°C, as moisture levels above 5 ppm cause de-wetting defects. The final HTL film is compatible with subsequent thermal evaporation of electron-transport materials, and the absence of heavy metals facilitates compliance with the RoHS Directive 2011/65/EU and its amendments.Polyester-based thermoplastic polyurethanes (TPU) exposed to atmospheric nitrogen oxides (NOₓ) undergo a well-characterised yellowing mechanism involving nitration of the polyester soft segment and formation of coloured quinoid structures. Addition of 0.5–1.2 phr of 2,4-bis(4-(tert-butyl)phenyl)-1H-pyrrole in combination with a benzotriazole UV absorber (0.3–0.5 phr) retards the discolouration in injection-moulded TPU shoe soles and sports equipment grips. The pyrrole compound is introduced during the prepolymer stage, dissolved in the polyol component to avoid particle agglomeration, and processed in a twin-screw reactor-extruder with an effective L/D of 48:1. The melt temperature is maintained between 160°C and 190°C to prevent thermal degradation of the additive. The stabilised TPU is subjected to ISO 105-B02 (blue wool scale) and a custom NOₓ gas exposure test at 40°C, 85% RH for 48 h; the ΔYI (yellowness index) is typically reduced by 35–50% relative to the unstabilised control. This performance is critical for white and pastel-coloured consumer goods where even slight yellowing is unacceptable. Regulatory verification for skin-contact applications requires compliance with REACH Annex XVII (restricted substances) and, when exported to California, adherence to Proposition 65 thresholds. The amine-free nature of the pyrrole derivative avoids the formation of N-nitrosamines, a known risk with secondary amine-based light stabilisers, making it suitable for articles that undergo repeated skin contact. The production process also mandates that relative humidity in the compounding hall stay below 60%, as absorbed moisture can hydrolyse the ester linkages in TPU during moulding, causing additive migration and a loss of surface stabilisation. Finished articles include watch straps, phone cases, and automotive interior soft-touch panels.Lithium-Ion Cathode Electrolyte Interphase Films from Heterocyclic PrecursorsIn high-voltage NMC811/graphite cells, oxidative decomposition of standard carbonate electrolytes at the cathode surface reduces calendar and cycle life. Addition of 1–2 wt% of the pyrrole derivative to a baseline electrolyte (1 M LiPF₆ in EC/EMC 3:7 v/v) results in preferential anodic oxidation during the first charge sweep. Linear sweep voltammetry on Pt electrode shows an onset current increase at 4.3 V vs. Li/Li⁺, about 0.15 V lower than the pure electrolyte, indicating formation of a cathode-electrolyte interphase (CEI). Half-cell cycling of NMC811 at 4.4 V upper cutoff shows an initial coulombic efficiency drop of approximately 2–3% in the formation cycle (attributable to CEI building charge), but the capacity retention after 200 cycles at 1C rate improves by 8–12% relative to the additive-free control. Post-mortem XPS analysis on the harvested cathode surfaces reveals a thicker organic–inorganic hybrid film incorporating pyrrole-derived species. Industrial application awaits validation in 18650-format cells under UN 38.3 transportation testing; the additive must remain anhydrous (water content <20 ppm) and is injected via a syringe port in a dry room at dew point below −50°C. Regulatory framework under the proposed EU Battery Regulation (2023/1542) requires declaration of hazardous constituents, and the compound, containing no fluorine or heavy metals, simplifies end-of-life recycling considerations.When the Melt Residence Time Window Shrinks in Fine-Denier PP Fibre SpinningHigh-speed melt spinning of polypropylene continuous filaments for nonwoven fabrics operates at spinneret temperatures of 230–240°C and demands a stabiliser that survives a short residence time without generating volatile decomposition products that condense on the die face. 2,4-Bis(4-(tert-butyl)phenyl)-1H-pyrrole is incorporated at 0.12–0.25 wt% together with 0.05–0.08 wt% of calcium stearate as acid scavenger, dry-blended and fed into a single-screw extruder with a L/D of 30:1. The screw design uses a 3:1 compression ratio and an intensive mixing section to ensure additive dispersion in a melt stream with a typical residence time of 6–10 min. Property loss at the spinneret is tracked by measuring the melt flow rate shift: an increase exceeding 15% relative to the unfilled base resin indicates unacceptable chain breakdown. Fibre tenacity tested per ISO 5079 at a denier of 1.8–2.2 dpf should remain above 3.0 cN/dtex. In spunbond applications, the web is thermally bonded at 140–150°C, and the stabiliser must not cause yellowing under the calender heat. Regulatory compliance for hygiene and medical nonwoven (drapes, gowns) demands conformity with ISO 10993-5 (cytotoxicity) and OEKO-TEX Standard 100 Class I, while for food-contact nonwoven (tea bags, coffee pads) the stabiliser must meet (EU) No 10/2011 overall migration limits, a pathway that requires the supplier to provide detailed substantiation of non-volatile residue. The production environment must be kept free of amine emissions from other lines, as airborne amine contaminants can cause surface-bound chromophores that emerge only after gamma sterilisation. When these conditions are observed, fibre-grade stabilised PP yields roll goods with uniform filament diameter and a defect count below 0.5 per m², suitable for high-speed converting into hygiene topsheets and medical barrier textiles. |
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| Parameter | Method/Standard | Value |
|---|---|---|
| Molecular formula | High-resolution mass spectrometry (ESI-TOF) | C₂₄H₂₉N |
| Molecular weight | Calculated from isotopic pattern | 331.47 g mol⁻¹ |
| Appearance | Visual inspection | White to off-white crystalline powder |
| Purity (HPLC) | In-house method based on ISO 13885-1:2020, C18 column, acetonitrile/water gradient | ≥99.0 % |
| Melting range | Differential scanning calorimetry (DSC) per ASTM E794-23, heating rate 10 K min⁻¹ | 180–185 °C |
| Residual palladium | ICP-MS per ASTM E2823-17 | <5 ppm |
| Loss on drying | Vacuum oven 60 °C, 4 h | ≤0.2 % |
| Property | PYR-2441 (2,4-bis(4-tert-butylphenyl)pyrrole) | 2,5-Diphenylpyrrole | N-Phenylpyrrole |
|---|---|---|---|
| Melting point (°C, DSC onset) | 180–185 | 224–226 | 62–64 |
| Tg (°C) | 92 ± 2 | 69 ± 3 | −5 ± 2 |
| Td₅ (5% mass loss, N₂, °C) | 356 ± 4 | 332 ± 5 | 241 ± 6 |
| HOMO (eV, UPS) | −5.38 ± 0.05 | −5.51 ± 0.08 | −5.08 ± 0.04 |
| Solubility in toluene at 25 °C (g L⁻¹) | 120 | 7 | >200 |
| Sublimation temperature at 10⁻⁶ mbar (°C) | 145–155 | 155–165 | Non-congruent sublimation observed |