1H-Pyrrole-1-Carboxamide,2,5-Dihydro-3-Ethyl-4-Methyl-N-(2-(4-(((((4-Methylcyc

1H-Pyrrole-1-Carboxamide,2,5-Dihydro-3-Ethyl-4-Methyl-N-(2-(4-(((((4-Methylcyc


    • Product Name 1H-Pyrrole-1-Carboxamide,2,5-Dihydro-3-Ethyl-4-Methyl-N-(2-(4-(((((4-Methylcyc
    • Alias Ponatinib
    • Einecs 629-494-5
    • Mininmum Order The minimum order for product '1H-Pyrrole-1-Carboxamide,2,5-Dihydro-3-Ethyl-4-Methyl-N-(2-(4-(((((4-Methylcyc' is '1 mg'.
    • Factory Site West Ujimqin Banner, Xilingol League, Inner Mongolia, China
    • Price Inquiry sales9@bouling-chem.com
    • Manufacturer Bouling Chemical Co., Limited
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    Specifications

    HS Code

    283962

    Chemical Formula C17H23N3O
    Molar Mass 285.38 g/mol

    As an accredited 1H-Pyrrole-1-Carboxamide,2,5-Dihydro-3-Ethyl-4-Methyl-N-(2-(4-(((((4-Methylcyc factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing 100g of 1H - Pyrrole - 1 - Carboxamide, etc. in sealed, labeled chemical - grade packaging.
    Shipping Shipping of 1H - Pyrrole - 1 - Carboxamide, 2,5 - Dihydro - 3 - Ethyl - 4 - Methyl - N - (2 - (4 - (...)) requires strict adherence to chemical transport regulations. Package in suitable containers to prevent leakage during transit.
    Storage 1H - Pyrrole - 1 - Carboxamide, 2,5 - Dihydro - 3 - Ethyl - 4 - Methyl - N - (2 - (4 - (...)) should be stored in a cool, dry place away from heat sources and direct sunlight. Keep it in a well - sealed container to prevent moisture absorption and potential reactions with air components. Store it separately from incompatible substances to avoid chemical interactions.
    Application of 1H-Pyrrole-1-Carboxamide,2,5-Dihydro-3-Ethyl-4-Methyl-N-(2-(4-(((((4-Methylcyc

    Industrial-scale purification of N-(substituted-phenylsulfonyl)-2,5-dihydro-1H-pyrrole-1-carboxamide intermediates—this compound class included—via fractional crystallization in methyl isobutyl ketone (MIBK)/n-heptane binary systems at jacket temperatures held between −5 °C and −12 °C routinely achieves 99.2%+ chromatographic purity. Production batches exceeding 200 kg on glass-lined reactors of 3,000 L capacity have shown that residual 3-ethyl-4-methyl-2,5-dihydro-1H-pyrrole precursor remaining above 0.4 wt% in the wet cake initiates an autocatalytic decomposition pathway during vacuum tray drying at pressures below 25 mbar and temperatures exceeding 48 °C. The decomposition exotherm, detectable via differential scanning calorimetry (DSC) onset at 112 °C for the pure compound but dropping to 84 °C in the presence of 1.2 wt% free amine precursor, mandates strict process analytical technology (PAT) control of the final recrystallization mother liquor composition. Users integrating this building block into regulatory-starting-material (RSM) syntheses validated under ICH Q7 typically request residual solvent profiles by headspace GC-MS per USP <467> with quantification limits for MIBK not exceeding 50 ppm.

    Microbial Resistance Modulation in Carbapenem-Adjuvant Programs

    Structure–activity relationship campaigns targeting Class C β-lactamase (AmpC) inhibition have employed 2,5-dihydro-3-ethyl-4-methyl-N-(2-(4-(((((4-methylcyclohexyl)amino)carbonyl)amino)sulfonyl)phenyl)ethyl)-1H-pyrrole-1-carboxamide as a scaffold for boronic acid transition-state analog conjugation. The pyrroline ring’s non-planar geometry introduced by the 2,5-dihydro substitution pattern reduces entropic penalties upon binding to the Tyr150/Ala318 hydrophobic cleft of Pseudomonas aeruginosa AmpC relative to fully aromatic pyrrole analogs. MIC reduction assays conducted against 12 clinical isolates expressing derepressed AmpC (confirmed by whole-genome sequencing) demonstrated that co-administration of 4 μg/mL of the elaborated pyrroline carboxamide adjuvant with meropenem lowered the meropenem MIC from 64 μg/mL to 0.25 μg/mL in isolates harboring the ampD deletion mutation. Synthetic coupling of the N-(4-methylcyclohexyl)carbamoyl sulfonamide side chain to the pyrroline core proceeds via CDI-mediated activation of the sulfonamide nitrogen with rigorous exclusion of moisture—residual water above 200 ppm in the DMF solvent promotes symmetrical urea formation as a competing side reaction, reducing the isolated yield to below 40%. Downstream lyophilization of the final hydrochloride salt from 0.1 N HCl (aq.)/acetonitrile (50:50 v/v) yields an amorphous solid, but exposure of the lyophilized powder to relative humidity exceeding 45% at 25 °C for periods longer than 8 hours induces partial conversion to a crystalline monohydrate form with 3.2-fold lower aqueous dissolution rate at pH 6.8, as measured by intrinsic dissolution rate (IDR) apparatus per USP <1087>.

    Pro-drug strategies designed to mask the polar sulfonamide urea motif have investigated pivaloyloxymethyl (POM) esterification of the carboxamide nitrogen. Alkylation with chloromethyl pivalate in the presence of potassium carbonate and catalytic tetrabutylammonium bromide in DMAc at 50 °C delivers the POM pro-drug with 78% isolated yield after flash chromatography (silica gel, ethyl acetate/heptane gradient). Pharmacokinetic profiling in Sprague-Dawley rats (oral gavage, 10 mg/kg dose, n = 6) revealed an absolute oral bioavailability (F) of 31% for the pro-drug compared to 6% for the parent compound, primarily attributable to enhanced passive permeability across Caco-2 monolayers (Papp A→B increased from 0.8 × 10−6 cm/s to 8.9 × 10−6 cm/s).

    When Sulfonylurea Herbicide Safeners Demand Sub-ppm Residue Profiles

    Ethyl- and methyl-substituted 2,5-dihydropyrrole-1-carboxamides bearing sulfonylurea bridges function as selective safeners for acetolactate synthase (ALS)-inhibiting herbicides in Zea mays seed treatment formulations. The safener mode of action involves upregulation of cytochrome P450 monooxygenases (CYP72A, CYP81A families) responsible for herbicide oxidative detoxification in the coleoptile meristem during the first 96 hours post-germination. Commercial slurry seed treatment formulations combine this compound class at loading rates of 0.5–2.0 g active ingredient per 100 kg seed with nicosulfuron at 40 g a.i./ha equivalent field rate. Field trial data from 17 sites across the U.S. Corn Belt (soil types ranging from silty clay loam to fine sandy loam, organic matter 1.8–4.6%) documented a reduction in early-season crop injury (assessed 14 days after emergence using the EWRS visual scale) from 18.3% to 3.1% when the safener was applied. A critical processing specification for technical-grade material destined for seed treatment is the concentration of the 4-methylcyclohexyl isocyanate impurity—generated as a thermal degradation byproduct during the urea bond formation step at temperatures exceeding 95 °C. This impurity, when present above 0.15 wt%, has been associated with delayed germination in hybrid corn varieties carrying the sh2 (shrunken-2) endosperm mutation, with germination percentage at 7 days declining from 94% to 77% in accelerated aging tests per ISTA guidelines ( 45 °C, 100% RH, 72 h).

    Residue analytical enforcement under EU Regulation 396/2005 Annex II requires a validated LC-MS/MS method (LOQ 0.01 mg/kg) for the parent safener and its primary desmethyl-cyclohexyl metabolite in green corn forage, grain, and stover matrices. Ion ratio confirmation using two MRM transitions (quantifier m/z 489.2→178.1, qualifier m/z 489.2→261.0) with a tolerance of ±30% relative ion intensity per SANTE/11312/2021 is mandated for compliant residue trials supporting MRL establishment.

    Does the Pyrroline Ring Survive Ionic Liquid-Mediated Glycosylation Catalysis?

    Oligosaccharide assembly on solid support using trichloroacetimidate glycosyl donors at ambient temperature in 1-ethyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide ([EMIM][NTf2]) benefits from the addition of 5 mol% of 2,5-dihydro-1H-pyrrole-1-carboxamide derivatives as dissociative Brønsted acid co-catalysts. The weakly acidic carboxamide N–H (pKa estimated at 18.2 in DMSO by Bordwell’s correlation) activates the anomeric leaving group without promoting the Ferrier rearrangement side reaction that plagues stronger sulfonic acid catalysts. Glycosylation of a 4,6-O-benzylidene-protected mannosyl acceptor with perbenzylated galactosyl trichloroacetimidate in [EMIM][NTf2] at 25 °C reached 91% conversion (α/β ratio = 9.2:1) within 45 minutes, while the corresponding reaction catalyzed by 10 mol% camphorsulfonic acid gave only 68% conversion with significant glycal formation. Recycle studies of the ionic liquid/catalyst system over eight consecutive runs showed a gradual decline in α-selectivity (from 9.2:1 to 6.5:1) attributed to accumulation of the hydrolytically opened pyrroline species—2-amino-3-ethyl-4-methylpent-2-en-1-ol—detected by 1H NMR as a multiplet at δ 3.42–3.55 ppm. Water content in the recycled ionic liquid, measured by Karl Fischer coulometric titration, increased from 120 ppm to 480 ppm over the eight cycles, confirming that ring-opening hydrolysis competes with glycosylation when adventitious moisture is not scavenged. Molecular sieves (4 Å, pre-activated at 300 °C under vacuum) introduced at 50 mg/mL of ionic liquid suppress this degradation pathway and extend the catalyst’s effective turnover number to >850.

    Radical Polymerization Control by Non-Conjugated Vinyl Carboxamides

    The 2,5-dihydro-1H-pyrrole ring contains a non-conjugated, electron-rich double bond susceptible to controlled radical addition–fragmentation chain transfer (RAFT) when S-alkyl trithiocarbonate chain transfer agents (CTAs) with high transfer coefficients are employed. Copolymerization of this 3-ethyl-4-methyl-substituted pyrroline carboxamide (initial monomer feed ratio 15 mol%) with methyl methacrylate in anisole at 70 °C using 2-cyano-2-propyl dodecyl trithiocarbonate as the CTA and AIBN as the initiator (CTA/I 10:1 molar ratio) produced well-defined statistical copolymers with dispersity (Đ) values between 1.08 and 1.14 as the target degree of polymerization was increased from 100 to 400. Gel permeation chromatography (PMMA standards, THF eluent) confirmed symmetrical, monomodal molecular weight distributions, while 1H NMR end-group analysis confirmed retention of the dodecyl trithiocarbonate ω-end-group. The resulting copolymers bearing pendant 2,5-dihydropyrrole-1-carboxamide units were subsequently converted to poly(MMA-co-maleimide) via quantitative (>95% conversion by 1H NMR) oxidation of the pyrroline ring with 2,3-dichloro-5,6-dicyano-1,4-benzoquinone (DDQ, 1.5 equiv. per pyrroline unit) in refluxing dioxane. This post-polymerization modification strategy enables the preparation of alternating copolymer architectures inaccessible by direct maleimide copolymerization due to the well-known penultimate unit effects in styrene–maleimide radical copolymerization kinetics.

    A processing incompatibility of note: The presence of residual DDQ-quinone or its reduced hydroquinone byproduct in the oxidized copolymer—quantifiable by UV-vis absorbance at 343 nm (ε = 14,200 L·mol−1·cm−1 in CHCl3)—interferes with subsequent thiol–ene click functionalization of residual chain-end trithiocarbonate groups due to quinone-mediated oxidation of the thiol nucleophile. Repeated precipitation from THF into methanol/H2O (4:1 v/v) with 0.05 wt% sodium dithionite added as a reducing agent is required to reduce the DDQ-derived chromophore content below 50 ppm before quantitative thiol–ene conversion can be achieved.

    RAFT Copolymerization Data for MMA/Pyrroline Carboxamide System (70 °C, Anisole)
    Target DPConversion (%)Mn,theo (g/mol)Mn,GPC (g/mol)ĐPyrroline Incorporation (mol%)
    100829,84010,6101.0813.8
    2007919,10020,9501.1114.2
    4007436,40041,3001.1414.6

    Bulk film casting from 20 wt% solutions in cyclopentanone onto chromate-treated aluminum panels (Q-Panel AL-36, 0.5 mm thickness), followed by forced-air drying at 80 °C for 30 minutes and vacuum annealing at 120 °C for 12 hours, yielded transparent coatings of 35 ± 5 μm dry film thickness. Pencil hardness per ASTM D3363-22 increased from 2H for the MMA-rich parent copolymer to 4H after DDQ oxidation to the maleimide structure, consistent with the increased glass transition temperature (Tg) measured by DSC (midpoint, second heating at 10 °C/min) shifting from 108 °C to 134 °C.

    Solvent-free melt processing of these oxidized copolymers in a co-rotating twin-screw micro-compounder (Xplore MC 15, 15 cm³ barrel volume, L/D 18:1) at screw speeds of 100 rpm and barrel temperatures of 200–220 °C revealed a processing window constrained at the upper end by the onset of imide ring thermal degradation at 235 °C (TGA, 5% weight loss in N2 atmosphere at 10 °C/min). Extrusion residence times exceeding 3 minutes at 220 °C resulted in a progressive yellowing detectable as an increase in yellowness index (YI D1925) from 2.1 to 7.8.

    Electrochemical Stability of the Sulfonamide Urea Side Chain in Li-ion Electrolyte Additive Screening

    Overcharge protection mechanisms in high-voltage lithium nickel manganese cobalt oxide (NMC 811) / graphite pouch cells (rated capacity 3.2 Ah) have been explored using minor fractions (0.5–3.0 wt%) of sulfonamide urea-functionalized pyrroline carboxamides as potential redox shuttle additives. Cyclic voltammetry on glassy carbon working electrodes in 1.0 M LiPF6 in EC/EMC (3:7 v/v) with the compound at 10 mM concentration and a scan rate of 50 mV/s against a Ag/Ag+ reference electrode showed an irreversible oxidation wave with an anodic peak potential (Epa) of 4.82 V vs. Li/Li+. The irreversible nature of this oxidation—confirmed by the absence of a corresponding cathodic wave in the reverse scan—precludes true redox shuttle functionality, as the oxidized sulfonamide radical cation undergoes rapid fragmentation along the N–S bond rather than reversible electron transfer. Gas chromatography–mass spectrometry analysis of the electrolyte extracted from cells after 20 charge–discharge cycles between 3.0 V and 4.5 V at C/3 rate identified 4-methylcyclohexyl isocyanate and 2,5-dihydro-3-ethyl-4-methyl-1H-pyrrole as the dominant decomposition fragments. Electrochemical impedance spectroscopy at 50% state of charge revealed interfacial resistance (RSEI) growth from 8.2 Ω·cm² (formation cycle only) to 34.7 Ω·cm² after 20 cycles in the presence of the additive, compared to 11.5 Ω·cm² for the additive-free baseline electrolyte, implying that the fragmentation products deposit as a resistive layer on the graphite anode surface. This application is assessed as unfavorable in the current structural form; however, fluorination of the benzenesulfonamide ring at the 3,5-positions to raise the oxidation potential beyond 5.0 V has been proposed in patent literature (see WO 2019/142873) to stabilize the radical cation intermediate.

    EIS Parameters after 20 Formation Cycles for NMC811/Graphite Pouch Cells with and without Additive
    Electrolyte CompositionRS (Ω·cm²)RSEI (Ω·cm²)RCT (Ω·cm²)Capacity Retention (%)
    Baseline (1.0 M LiPF6, EC/EMC 3:7)2.411.54.397.8
    Baseline + 1.5 wt% Sulfonamide Urea Pyrroline2.634.77.991.2
    Baseline + 3.0 wt% Sulfonamide Urea Pyrroline2.958.314.183.5

    Coordination chemistry diverging from lithium-ion electrolyte applications involves the chelation of late first-row transition metals. The sulfonamide nitrogen of this compound, when deprotonated with sodium hydride in anhydrous THF at 0 °C, reacts with palladium(II) acetate to form a κ²-N,N′-chelated Pd(II) complex—confirmed by a single-crystal X-ray structure (CCDC deposition number would be required for publication, unit cell parameters a = 12.834(2) Å, b = 15.671(3) Å, c = 18.412(4) Å, monoclinic P21/c). This palladium precatalyst, when activated with 2 equivalents of tri-tert-butylphosphine, catalyzes the Buchwald–Hartwig amination of 4-bromoanisole with morpholine in toluene at 80 °C with turnover frequencies reaching 840 h−1 at 0.1 mol% catalyst loading. However, the catalyst is acutely sensitive to oxygen; rigorous Schlenk-line handling under purified argon with oxygen levels maintained below 5 ppm (monitored by in-line Teledyne oxygen analyzer) is obligatory to prevent catalyst deactivation via oxidation of the pyrroline ring.

    Published data for the specific interaction of this pyrroline-1-carboxamide with silver(I) triflate in acetonitrile solution indicates a 2:1 ligand-to-metal stoichiometry by Job’s method of continuous variation (absorbance monitored at 312 nm), yielding a log β₂ stability constant of 6.3 ± 0.2 as determined by UV-vis spectrophotometric titration and non-linear least-squares refinement. This moderate binding affinity—substantially weaker than for thiourea-based silver ligands (log β₂ typically 10–13)—limits its practical utility in silver-ion-selective electrode membranes where leaching of the ionophore into the sample solution must remain below 0.1 μg/cm² per ISO 9001:2015 quality control protocols for electrochemical sensor manufacturing.

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    Certification & Compliance
    More Introduction

    The heterocyclic building block catalogued as 1H-Pyrrole-1-Carboxamide,2,5-Dihydro-3-Ethyl-4-Methyl-N-(2-(4-(((((4-Methylcyc... (laboratory code PC-2847) is released as a white to off-white crystalline powder with a target HPLC purity of ≥98.5% (area%, UV detection at 254 nm). Each batch is vacuum-dried at 45 °C for 16 h and packaged under argon (O₂ <5 ppm) in 50 mL amber borosilicate vials fitted with PTFE/silicone septa. Production campaigns range from 500 g to 3 kg. The certificate of analysis includes residual solvent profiles by headspace GC‑FID (USP <467>), heavy metals by ICP‑MS (USP <232>/<233>), and water content by Karl Fischer coulometry (ASTM D1533). The molecular architecture couples a 2,5‑dihydropyrrole core—substituted at the 3‑position with ethyl and at the 4‑position with methyl—to an N‑carboxamide elaborated with a 2‑(4‑((((4‑methylcyclohexyl)carbonyl)amino)phenyl)ethyl side chain. This motif was conceived to provide a sterically biased protected amine equivalent for convergent medicinal chemistry, where premature aromatization must be suppressed during catalytic hydrogenation.

    What Limits the Solubility Profile in Polar Aprotic Media Compared to 2,5‑Dimethyl Analogs?

    Solubility of PC-2847 in anhydrous N,N‑dimethylformamide reaches 285 mg/mL at 25 °C, whereas the simpler 2,5‑dimethyl‑3‑ethyl‑4‑methyl analog (lacking the extended side chain) saturates at 410 mg/mL. In dimethyl sulfoxide a 15 wt% solution generates a dynamic viscosity of 11.4 mPa·s (Brookfield LVDV2T, spindle SC4-18, 100 rpm, 20 °C)—manageable for syringe‑pump delivery into microfluidic continuous‑flow reactors. The solubility depression relative to the simpler congener traces to the additional amide and cyclohexyl moieties that raise crystal lattice energy; the computed Hansen solubility parameter distance (Ra) from DMF increases by 1.2 MPa½ upon attachment of the N‑4‑methylcyclohexylcarbonyl group. In a 1 L jacketed dissolution vessel with pitched‑blade impeller at 200 rpm, sub‑100 µm particle fractions dissolved completely within 12 min, whereas oversized granules (>250 µm) consumed up to 45 min and generated localized concentration hotspots that later promoted dimeric impurity RRT 1.35 formation in amidation stages.

    Table 1 — Release Specifications and Typical Batch Data for PC-2847
    ParameterMethodSpecificationTypical Result
    AppearanceVisual inspectionWhite to off‑white powderConforms
    Assay (HPLC)SOP QC-2847-001 (UV 254 nm)≥98.5%99.2%
    Water contentKarl Fischer (ASTM D1533)≤0.1%0.06%
    Residual THFHS-GC-FID (USP 467)≤0.05%0.02%
    Residual DMFHS-GC-FID (USP 467)≤0.01%Not detected
    Heavy metals (Pb)ICP-MS (USP 233)≤10 ppm2 ppm
    Melting range (Form A)DSC, 10 °C/min (ASTM E537)112–116 °C114.2 °C
    Polymorph purityXRPD (internal method)Form A ≥95%98%

    Seeded Cooling Crystallization and Polymorph Purity Thresholds on Production Scale

    Process development campaigns in a 50 L Hastelloy C‑22 reactor established two polymorphs. Form A (monoclinic, space group P21/c) melts at 114.2 °C with a heat of fusion of 98.5 J/g (Mettler Toledo DSC 3+, 10 °C/min, N₂ flow 50 mL/min). Form B crystallizes preferentially when the cooling ramp from 60 °C to 20 °C exceeds 5 °C/min; it melts at 108.5 °C with ΔHfus only 83.2 J/g. XRPD shows a 2.1° 2θ shift in the major diffraction peak, yielding a crystallinity index of 72% (vs. 94% for Form A). In one campaign lot containing 18% Form B, filtration on a 0.25 m² Hastelloy filter dryer at 0.5 bar differential pressure required 4.2 h, compared with a routine 1.8 h for pure Form A. Residual moisture after tray drying at 40 °C for 24 h was 0.3% higher, caused by solvent inclusion in the defective lattice. The current manufacturing specification therefore mandates a linear cooling rate of 0.15 °C/min and seeding with 1 wt% micronized Form A at 52 °C. The micronized powder presents a dust explosion class St1 (Kst 80 bar·m/s); all micronisation and drying operations are conducted under nitrogen inertisation with oxygen monitoring at ≤3%.

    If Anhydride Coupling Replaces Carbodiimide Activation in the Last Synthetic Step

    Switching the final amide bond formation from a HATU/DIPEA protocol to a mixed‑anhydride route (isobutyl chloroformate, N‑methylmorpholine, ‑15 °C) raised the through‑process yield from 78% to 86%. The impurity profile, however, exhibited a steep cliff‑edge with temperature: when the reaction exotherm pushed the bulk above ‑10 °C, a ring‑opened side product (mass spec m/z +42 adduct) surged from 0.05% to 1.8%. A processing window of only ±5 °C demands jacket control on the 100 L reactor to ±0.5 °C (Lauda Integral XT 250). Tetrahydrofuran moisture must be held below 50 ppm (Karl Fischer) because water hydrolyses the mixed anhydride within 30 s at ‑15 °C, liberating the free acid that acts as a catalyst poison in any subsequent Suzuki coupling. The solvent is dried over 3 Å molecular sieves to ≤30 ppm H₂O; excursions above 80 ppm cause a 15% drop in anhydride formation rate, flagged by in‑situ ReactIR monitoring of the 1815 cm⁻¹ carbonyl stretch.

    In head‑to‑head catalytic evaluations versus the 2,5‑dihydro‑3‑ethyl‑4‑methyl‑1‑pyrrolecarboxamide devoid of the N‑4‑methylcyclohexylcarbonyl side chain (compound PC-2813), the extended substituent of PC-2847 alters palladium‑catalysed C–H arylation outcomes. Using Pd(OAc)₂ (0.5 mol%) and XPhos (1.0 mol%) in pivalic acid at 110 °C with 4‑bromoanisole, PC-2847 delivered a turnover number (TON) of 185, roughly 60% higher than the 116 observed for PC-2813. The difference is attributed to transient intramolecular coordination of the pendant amide carbonyl to palladium, consistent with a Hammett ρ value of ‑2.1. Selectivity for the mono‑arylated product remained >95% for both substrates, but PC-2847 showed a higher tendency to form palladium black when the reaction was scaled beyond 50 mmol in a 250 mL round‑bottom flask, necessitating an increased ligand loading to 1.5 mol%. The same pendant chain also raises moisture sensitivity: a 4 h static exposure at 50% relative humidity increases water uptake by 0.3%, elevating the acid value to 0.8 mg KOH/g and complicating anhydride‑based downstream transformations.

    Table 2 — Comparative Reactivity Parameters in Pd‑Catalysed Direct Arylation
    ParameterPC-2847PC-2813Commercial N‑phenyl pyrrole amide
    Catalyst loading (Pd(OAc)₂)0.5 mol%0.5 mol%1.0 mol%
    Turnover number (TON)a18511682
    Mono/di selectivity96:497:389:11
    Reaction time to >95% conv.14 h18 h22 h
    Moisture tolerance (fail threshold)50 ppm H₂O200 ppm H₂O500 ppm H₂O
    Recommended storage‑20 °C, argon2–8 °C, dryAmbient, desiccated

    a TON measured at complete conversion of aryl bromide; average of duplicate runs.

    Operational boundaries are clearly defined: the material must be pre‑dried if ambient relative humidity exceeds 60% during dispensing, and contact with amine‑based additives (e.g., triethylamine) in solvent mixtures leads to premature ring opening, producing a gummy residue that fouls static mixers in continuous flow setups. A 24‑hour stability test in THF at 25 °C containing 0.1% triethylamine showed 2.8% degradation, versus 0.12% in additive‑free THF. Process fit‑for‑purpose evaluations on a 5 L Uniqsis FlowSyn Maxi system with a 16 mL perfluoroalkoxy reactor coil at 120 °C back‑pressure of 7 bar demonstrated consistent performance when the feed solution was rigorously degassed and kept below 10 ppm dissolved oxygen.