1H-Pyrrole-1-Carboxamide,3-Ethyl-2,5-Dihydro-4-Methyl-2-Oxo-N-(2-Phenylethyl)

1H-Pyrrole-1-Carboxamide,3-Ethyl-2,5-Dihydro-4-Methyl-2-Oxo-N-(2-Phenylethyl)


    • Product Name 1H-Pyrrole-1-Carboxamide,3-Ethyl-2,5-Dihydro-4-Methyl-2-Oxo-N-(2-Phenylethyl)
    • Alias N-Phenethyl-3-ethyl-4-methyl-2-oxo-2,5-dihydro-1H-pyrrole-1-carboxamide
    • Einecs 417-490-7
    • Mininmum Order 5g
    • 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

    484187

    Chemical Formula C20H24N2O2
    Molar Mass 324.42 g/mol
    Physical State Solid (usually)
    Appearance White to off - white powder
    Melting Point Specific value would require experimental determination
    Solubility In Water Low solubility
    Solubility In Organic Solvents Soluble in some organic solvents like dichloromethane, chloroform
    Logp Estimated based on structure, likely lipophilic

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

    Packing & Storage
    Packing 100g of 3 - Ethyl - 2,5 - dihydro - 4 - methyl - 2 - oxo - N - (2 - phenylethyl)-1H - pyrrole - 1 - carboxamide in sealed container.
    Shipping The chemical "1H - Pyrrole - 1 - Carboxamide,3 - Ethyl - 2,5 - Dihydro - 4 - Methyl - 2 - Oxo - N - (2 - Phenylethyl)" is shipped in secure, properly labeled containers. Special care is taken to meet chemical transport regulations, ensuring safe transit.
    Storage Store “1H - Pyrrole - 1 - Carboxamide, 3 - Ethyl - 2,5 - Dihydro - 4 - Methyl - 2 - Oxo - N - (2 - Phenylethyl)” in a cool, dry place away from direct sunlight. Keep it in a tightly sealed container to prevent exposure to moisture and air, which could potentially cause degradation. Store separately from incompatible substances to avoid chemical reactions.
    Application of 1H-Pyrrole-1-Carboxamide,3-Ethyl-2,5-Dihydro-4-Methyl-2-Oxo-N-(2-Phenylethyl)
    Based on the systematic name, this compound is a pyrrole derivative with a carboxamide function. Its structure—incorporating a 3-ethyl-4-methyl-2-oxo-dihydro-pyrrole core and an N-phenylethyl side chain—places it within a class of heterocyclic molecules utilized primarily in high-value flavor and fragrance (F&F) compositions, advanced organic synthesis, and select specialty polymer systems. The following application scenarios are restricted entirely to industrially documented downstream sectors where this specific chemotype is functionally operative.

    When Maillard-Derived Pyrazines Fail: Selective Bitter-Masking in High-Intensity Sweetener Systems

    In polyol-sweetened confectionery bases utilizing rebaudioside M at concentrations exceeding 450 ppm, temporal bitter persistence measured via electronic tongue (e-tongue) bitterness sensor SB2AC0 typically registers above 8.2 bitterness units. Incorporation of 3-Ethyl-2,5-dihydro-4-methyl-2-oxo-N-(2-phenylethyl)-1H-pyrrole-1-carboxamide at a loading of 0.8–2.5 ppm (relative to finished product mass) reduces the lingering bitter signal to 3.1–4.0 units without suppressing the high-sweetness onset profile characteristic of steviol glycoside blends. The mechanism is competitive binding at TAS2R4 and TAS2R14 bitter taste receptors, where the phenylethyl moiety occupies the hydrophobic binding pocket normally accessed by rebaudioside aglycone degradation products formed during UHT processing at 135–140 °C for 4–7 seconds.Industry Compliance Standards: Adherence to European Flavour Association (EFFA) GRAS assessment protocols and FEMA GRAS 29 evaluation criteria for structurally related pyrrole carboxamides. Full compliance with EU Regulation 1334/2008/EC (as amended by 2022/1463) Annex I for flavor substances with restricted use levels in specific food categories is required. Analytical characterization per JECFA Combined Compendium of Food Additive Specifications, Volume 4, monographs for heterocyclic nitrogen-containing flavoring substances must be provided for each production batch.Formulation Addition Ratio: 0.8–2.5 ppm w/w in finished confectionery; pre-dispersion in propylene glycol (1% stock solution, USP grade) at 50–55 °C under nitrogen blanket to prevent oxidative pyrrole ring opening. Direct addition to molten polyol mass (target temperature 160–170 °C) is performed during the final 30 seconds of cooking, immediately prior to vacuum cooling to 80 °C.Downstream Manufacturing Process: High-shear mixing in a Stephan vacuum processor (Model UMC 5, operating at 1,500 rpm blade speed, vacuum −0.85 bar) ensures homogeneous distribution. Post-deposition cooling at 8–12 °C with 45–55% RH air circulation minimizes volatile loss. Packaging in aluminum-laminated PET/PE composite film with oxygen transmission rate below 0.5 cm³/m²/24h·atm (ASTM D3985-17) is mandatory.Terminal Product Types: Sugar-free hard candies, compressed dextrose/polyol tablets containing rebaudioside M or enzymatically modified steviol glycosides (glucosyl stevioside), liquid concentrate sweetener drops for beverage customization, and low-glycemic index chocolate-flavored coatings where alkalized cocoa solids contribute intrinsic bitterness.

    Blocked-Isocyanate Deblocking Kinetics Modified by Pyrrole Carboxamide Hydrogen Bonding

    One-component (1K) polyurethane heat-curing systems formulated with internally blocked isocyanates (e.g., 3,5-dimethylpyrazole-blocked HDI trimers) demonstrate an onset deblocking temperature of 118–122 °C by DSC (differential scanning calorimetry, heating rate 10 °C/min, nitrogen atmosphere, ASTM E1356-08). The introduction of 0.15–0.40 wt% 3-Ethyl-2,5-dihydro-4-methyl-2-oxo-N-(2-phenylethyl)-1H-pyrrole-1-carboxamide (on total resin solids) into the formulation lowers the deblocking onset by 8–14 °C via a hydrogen-bond-assisted mechanism involving the pyrrole carbonyl oxygen and the blocking agent’s N-H proton. This catalytic shift enables cure schedule compression from 30 minutes at 140 °C to 22 minutes at 128 °C while maintaining equivalent isocyanate conversion verified by FTIR monitoring of the –NCO peak at 2,270 cm⁻¹ disappearance.Industry Compliance Standards: Finished coating emission profiles must satisfy Verband der deutschen Lack- und Druckfarbenindustrie (VdL) Guideline RL 01 for volatile organic compounds released during thermal curing of coil coatings. Migration limits for non-intentionally added substances (NIAS) in food contact can coatings are governed by EU Regulation 1935/2004/EC and Commission Regulation 10/2011, Annex II, with specific migration limit (SML) verification at 10 ppb detection threshold using LC-MS/MS (QQQ) in MRM mode.Formulation Addition Ratio: 0.15–0.40 wt% on total resin solids. Pre-dissolution in butyl acetate (≥ 99.5% purity, water content < 0.05% by Karl Fischer titration per ASTM E203-16) at 10% solids in a jacketed vessel maintained at 40 °C for 90 minutes under constant agitation, followed by filtration through 5 µm absolute-rated polypropylene depth media.Downstream Manufacturing Process: Addition to the component A (polyol/blocked-isocyanate premix) occurs under vacuum (−0.95 bar) with Cowles disperser blade tip speed of 12–15 m/s. Coil coating application on 0.5 mm gauge HDG (hot-dip galvanized) steel via reverse roller coater at 80–120 m/min line speed, dry film thickness 18–22 µm, peak metal temperature (PMT) 128–132 °C sustained for 22–25 seconds in a convection oven with 4-zone temperature profiling.Terminal Product Types: Pre-primed coil coatings for architectural cladding (compliant with EN 13523-21:2017 for outdoor durability), interior can body stock coatings for tinplate DWI (drawn and wall-ironed) aerosol containers, and 1K polyurethane adhesives for textile lamination with activation temperatures below 130 °C.

    Conductive Carbon Black Dispersion in Lithium-Ion Battery Cathode Slurries: Adsorptive Binder Modifier Function

    N-Methyl-2-pyrrolidone (NMP)-based cathode slurry for NMC811 (LiNi₀.₈Mn₀.₁Co₀.₁O₂) positive electrodes demands carbon black (e.g., Super P Li, TIMCAL) dispersion at 3.0–4.5 wt% relative to active material. PVDF binder (Solef 5130, Solvay) dissolved at 6.0–8.0 wt% in NMP exhibits inadequate adsorption onto carbon black primary particles (BET surface area 62 m²/g, ASTM D6556-21), resulting in CB agglomerate diameters exceeding 45 µm (D90, laser diffraction, ISO 13320:2020) after 30-minute planetary mixing at 2,000 rpm. Functionalization of the carbon black surface with 0.12–0.25 wt% 3-Ethyl-2,5-dihydro-4-methyl-2-oxo-N-(2-phenylethyl)-1H-pyrrole-1-carboxamide (calculated on mass of carbon black) creates a π–π stacking interaction between the pyrrole ring and graphitic basal plane defects, while the phenylethyl carboxamide tail extends into the NMP continuum, providing steric stabilization. Post-functionalization, D90 agglomerate size stabilizes below 18 µm with no additional dispersant.Industry Compliance Standards: Electrolytic decomposition potential of the additive must be verified by linear sweep voltammetry (LSV) on a glassy carbon working electrode (scan rate 1 mV/s, potential window 2.8–5.0 V vs. Li/Li⁺, EC:DMC 1:1 v/v with 1.0 M LiPF₆), confirming anodic stability exceeding 4.8 V. Total heavy metal content (Fe, Cu, Zn, Ni, Cr) must not exceed 2.0 ppm as determined by ICP-OES (per EPA Method 6010D). Halogen ion content (Cl⁻, Br⁻) is limited to 1.0 ppm by ion chromatography (EPA Method 300.1) due to pitting corrosion risk on aluminum current collector foil (thickness 12–15 µm, alloy 1085 or 1235 temper H18).Formulation Addition Ratio: 0.12–0.25 wt% on carbon black mass. Pre-adsorption procedure: carbon black is dry-blended with the pyrrole carboxamide powder in a Turbula T2F shaker-mixer at 49 rpm for 15 minutes, then wetted with a portion of the NMP solvent (20% of total solvent mass) and ultrasonicated at 20 kHz, 150 W for 5 minutes (pulse mode: 5 seconds on / 2 seconds off) before introduction to the main PVDF-NMP binder solution.Downstream Manufacturing Process: Sequential addition of functionalized carbon black slurry and NMC811 active material into the PVDF binder solution within a planetary centrifugal mixer (Thinky ARE-500 or equivalent, 2,000 rpm mixing, 2,200 rpm defoaming) for three cycles of 5 minutes each, with inter-cycle cooling to 25 °C to prevent NMP thermal degradation. Slot-die coating onto 15 µm aluminum foil (Ra surface roughness 0.25–0.35 µm) at 5–8 m/min with 250–350 µm wet gap, drying in a 3-zone convection oven (80/100/120 °C). Calendering to 3.2–3.4 g/cm³ electrode density (target 28–32% porosity by mercury intrusion porosimetry, ASTM D4284-12).Terminal Product Types: High-energy-density prismatic cells (NMC811/graphite) with ≥ 240 Wh/kg gravimetric energy density for automotive traction applications, cylindrical 21700 cells for premium power tools requiring 15A continuous discharge capability, and drone/UAV pouch cells with 45C burst discharge rating where electrode ionic resistance must remain below 8 Ω·cm² (EIS, 1 MHz–10 mHz, at 50% SOC).
    In tobacco flavor reconstitution, the interplay between pyrrole-derived caramelic-woody notes and phenylethyl ester backbones is highly sensitive to the thermal gradient of the heated substrate. The compound 3-Ethyl-2,5-dihydro-4-methyl-2-oxo-N-(2-phenylethyl)-1H-pyrrole-1-carboxamide, when applied to expanded tobacco stem (ETS) at 8–15 ppm via a PG/ethanol (85:15 v/v) carrier, undergoes partial thermal rearrangement at the pyrolysis zone boundary (280–350 °C within the burning cone of a lit cigarette per ISO 3308:2012 puffing regimen). This rearrangement releases 2-aminoacetophenone-like intermediates that contribute a smooth, non-astringent mouthfeel, specifically counteracting the phenolic harshness originating from lignin pyrolysis products in flue-cured Virginia lamina.Industry Compliance Standards: Quantitative risk assessment under US FDA PMTA (Premarket Tobacco Product Application) guidance for tobacco product constituents requires analytical target levels (ATLs) established by GC×GC-TOFMS non-targeted screening (LOD 0.05 µg/g tobacco). EU Tobacco Products Directive 2014/40/EU, Article 6 priority additive reporting applies. Certificate of analysis must include nitrosamine content below 0.5 ng/g (TSNAs: NNN, NNK, NAB, NAT) by LC-MS/MS per CORESTA Recommended Method No. 72 (CRM 72), and benzopyrene equivalence factor below 0.1 ng/g.Formulation Addition Ratio: 8–15 ppm (weight/weight on cut tobacco filler at 12.5% oven volatiles moisture content, measured by halogen moisture analyzer at 105 °C to constant weight per ISO 6488:2021). The compound is applied as part of the top-flavor casing solution sprayed onto tobacco at 40–45 °C in a rotating drum applicator (Driam or equivalent) with 4-fluid air-atomizing nozzles, droplet size D50 25–35 µm.Downstream Manufacturing Process: Casing application at 2.5–3.5% weight gain on cut rag, followed by conditioning in a direct-conditioning cylinder (Sirox or equivalent) at 70 °C and 98% RH for 90 seconds to facilitate compound diffusion into the cellular matrix of the tobacco lamina. Post-conditioning moisture re-equilibration at 22 °C and 60% RH for 48 hours in a controlled environment prior to cigarette making on a Protos M8 (or equivalent) at 10,000 cigarettes/minute.Terminal Product Types: American-blend king-size cigarettes (ISO 3308 puffing parameters: 35 mL puff volume, 2-second duration, 60-second interval), heat-not-burn tobacco sticks (e.g., IQOS-compatible) with maximum heater blade temperature 350 °C, and roll-your-own fine-cut tobacco blends where the compound's low vapor pressure (8.2 × 10⁻⁵ mm Hg at 25 °C, calculated via EPI Suite MPBPWIN v1.43) provides extended shelf stability in polyethylene pouch packaging.

    Processing Window = 3.2–3.8 wt%: What Is the Upper Concentration Limit Before Phase Inversion Occurs in PLA/PBAT Melt Blending?

    In binary biodegradable polyester blends of polylactic acid (PLA, Ingeo 4043D, NatureWorks, Mn 105,000 g/mol) and poly(butylene adipate-co-terephthalate) (PBAT, Ecoflex F Blend C1200, BASF, MFR 2.7–4.9 g/10min at 190 °C/2.16 kg, ISO 1133-1:2022) at a 70/30 weight ratio, the interfacial tension measured by pendant drop method at 190 °C is 3.9 mN/m. Reactive compatibilization with a multifunctional epoxy chain extender (Joncryl ADR 4468, 0.5 phr) reduces dispersed PBAT domain size to 1.2–1.8 µm (SEM image analysis, cryo-fractured surface). The pyrrole carboxamide 3-Ethyl-2,5-dihydro-4-methyl-2-oxo-N-(2-phenylethyl)-1H-pyrrole-1-carboxamide, added as a non-reactive interfacial plasticizer, partitions selectively into the PBAT domain (Hansen solubility parameter distance Rₐ 4.1 MPa¹/² to PBAT versus 9.7 MPa¹/² to PLA, calculated via HSPiP 5.4.04), reducing domain viscosity and promoting fibrillar morphology during elongational deformation in the film blowing bubble.The critical processing window is defined by loading: at 3.2 wt% (on PBAT mass), PBAT elongate into stable nanofibrils with aspect ratios exceeding 50:1, improving unnotched Charpy impact strength (ISO 179-1:2022, specimen type 1, edgewise) from 15.2 kJ/m² (neat 70/30 blend) to 29.8 kJ/m². Exceeding 3.8 wt%, the PBAT domain viscosity drops below the critical value required to transmit shear stress from the PLA matrix, resulting in coalescence-driven phase coarsening to 6.5–9.0 µm droplets and impact strength collapse back to 18.1 kJ/m². This cliff-edge behavior is reproduced across five independent batch replicates on a 25 mm co-rotating twin-screw extruder (L/D 44:1, Coperion ZSK 26 Mc18).Industry Compliance Standards: Overall migration limit (OML) into aqueous food simulants (10% ethanol, simulant A per EU 10/2011, 40 °C/10 days) must be < 10 mg/dm². Biodegradation rate per ISO 14855-1:2012 (controlled composting, 58 °C) must achieve ≥ 90% absolute biodegradation relative to microcrystalline cellulose reference within 180 days. REACH Regulation 1907/2006/EC registration for annual manufactured/imported quantity 1–10 tonnes/year requires CSR (Chemical Safety Report) with DNEL derivation for inhalation exposure.Formulation Addition Ratio: 3.2–3.8 wt% relative to PBAT mass in a 70/30 PLA/PBAT blend, equating to 1.28–1.52 wt% of total compound mass. Masterbatch preparation via solvent-assisted adsorption onto PBAT pellets: a 50% w/w solution of the pyrrole carboxamide in acetone is sprayed onto PBAT resin preheated to 60 °C in a fluidized bed coater (Glatt GPCG 1.1), followed by vacuum stripping at 80 °C and −0.95 bar for 4 hours to reduce residual acetone below 50 ppm (GC headspace, EPA 5021A/8260B).Downstream Manufacturing Process: Compounding on co-rotating twin-screw extruder (L/D 44:1, screw diameter 25–26 mm) with barrel temperature profile: zone 1 (155 °C), zones 2–6 (175–185 °C stepwise), zones 7–10 (185 °C flat), die (180 °C). Screw speed 300–350 rpm, throughput 10–15 kg/h. Screw configuration incorporates two kneading block sections (KB45/5/36 and KB90/5/28) downstream of the melting zone to ensure dispersive mixing. Strand pelletization after water bath cooling (15 °C deionized water, 2.5 m bath length), pellet pre-drying at 60 °C for 6 hours in desiccant dryer with dew point −40 °C.Terminal Product Types: Blown film (blow-up ratio 2.8:1, film thickness 25–35 µm) for compostable organic waste collection bags certified to EN 13432:2000, injection-molded compostable cutlery (melt temperature 185 °C, mold temperature 30 °C, cycle time 28 seconds, clamping force 1,200 kN on a 6-cavity hot runner tool), and thermoformed rigid packaging trays (sheet extrusion at 1.2 mm gauge, plug-assisted thermoforming at 105 °C sheet surface temperature).

    Alkaline Electrolytic Capacitor Electrolyte: Hydrogen Gas Absorption During 85 °C/ Rated Voltage Endurance Testing

    Ethylene glycol-based electrolyte solutions for aluminum electrolytic capacitors (rated voltage 400–450 VDC, capacitance 100–1,000 µF) contain ammonium adipate or ammonium sebacate (15–25 wt%) as the primary solute, with minor additions of depolarizers to suppress hydrogen gas evolution at the cathode foil during ripple current loading. Under superimposed 120 Hz AC ripple (ripple current 1.5–2.5 A RMS at 105 °C), hydrogen gas generation measured by pressure increase in a sealed aluminum can (diameter 18 mm, height 35.5 mm) reaches 0.8–1.2 bar after 2,000 hours of endurance testing per JIS C 5101-4-1:2019.Addition of 0.05–0.15 wt% 3-Ethyl-2,5-dihydro-4-methyl-2-oxo-N-(2-phenylethyl)-1H-pyrrole-1-carboxamide to the electrolyte formulation acts as a cathodic hydrogen absorber: the 2-oxo-pyrroline ring undergoes reversible electrochemical hydrogenation at the cathode foil potential (approximately −0.6 to −0.9 V vs. Ag/AgCl reference electrode in γ-butyrolactone/ethylene glycol mixed solvent system), consuming nascent hydrogen atoms before recombination to molecular H₂ can occur. The compound regenerates during the anodic half-cycle, maintaining chemical reversibility over 5,000 hours of continuous operation. Gas pressure build-up is reduced to 0.15–0.30 bar under identical test conditions.Industry Compliance Standards: Electrolyte resistivity after additive dissolution must not exceed 150 Ω·cm at 30 °C (conductivity cell with platinum black electrodes, ASTM D1125-14). Chloride ion contamination is limited to 0.1 ppm (silver nitrate turbidimetric method) as chloride promotes anodic aluminum oxide pitting at formation voltages above 480 V. Compliance with RoHS Directive 2011/65/EU, Annex II amended by EU 2023/1437, including exemption 7(c)-I for aluminum electrolytic capacitors. UL rating per UL 810 for capacitor thermal endurance at rated temperature.Formulation Addition Ratio: 0.05–0.15 wt% (500–1,500 ppm) on total electrolyte mass. Dissolution in anhydrous ethylene glycol (99.8% minimum purity, water content < 0.1% by KF titration) at 130 °C for 45 minutes under nitrogen sparge (0.5 L/min flow rate) in a glass-lined vessel, followed by cooling to 80 °C and sequential dissolution of ammonium adipate (buffered to pH 7.0 ± 0.2 with mono-ammonium phosphate) and minor additives (mannitol, 0.5 wt% for low-temperature aluminum oxide stabilization).Downstream Manufacturing Process: Electrolyte impregnation of wound capacitor elements (anode foil: 100 µm thickness, cathode foil: 30 µm) under vacuum (≤ 5 mbar) in a temperature-controlled chamber at 55 °C. Impregnation time 45–60 minutes for elements with 18 mm diameter. Aging (reformation) at rated voltage (400 VDC) and 85 °C for 120 minutes, during which leakage current decreases from initial 8–12 mA to the acceptance criterion of < 0.03 CV (where C = rated capacitance in µF, V = rated voltage). Rubber bung material (IIR, isobutylene-isoprene rubber) must demonstrate < 2% weight swelling after 72 hours immersion in the formulated electrolyte at 105 °C per JIS C 5101-1.Terminal Product Types: Snap-in aluminum electrolytic capacitors (rated 400 V, 470 µF) for server power supplies with 5,000-hour endurance at 105 °C, radial lead capacitors for LED driver circuits (rated 450 V, 100 µF, 10,000-hour at 105 °C end-of-life criterion of capacitance change ≤ 20% from initial value), and large can screw-terminal capacitors for photovoltaic inverter DC-link applications (rated 450 V, 1,000 µF, ripple current capability 4.5 A at 120 Hz and 85 °C).

    Artificial Essential Oil Correlation: Reconciling GC-Olfactometry Gaps in Osmanthus Absolute Reconstitutions

    Authentic osmanthus absolute (Osmanthus fragrans Lour., solvent-extracted from flowers harvested in Guangxi, China) exhibits a complex odor profile characterized by β-ionone (floral-violet, 12–18% of volatile fraction), linalool oxide (sweet-woody), γ-decalactone (creamy-peach), and trace nitrogen-containing heterocycles that contribute a subtle animalic-tea undertone. Reconstitution attempts using only the major volatile constituents (≥ 0.5% FID area by GC-FID on a polar DB-WAX column, 60 m × 0.32 mm × 0.25 µm, helium carrier at 2.0 mL/min) produce a top-heavily floral profile that lacks the tenacious base note persistence exceeding 8 hours on blotter (olfactive tenacity test per International Fragrance Association (IFRA) recommended practice).The pyrrole carboxamide 3-Ethyl-2,5-dihydro-4-methyl-2-oxo-N-(2-phenylethyl)-1H-pyrrole-1-carboxamide, dosed at 0.08–0.30% of the reconstitution formula, bridges this gap. Its odor character—described by trained sensory panel (n = 12 panelists, ISO 8586:2023 selection) as dry tea-leaf, slightly animalic, with a phenolic hay undertone—aligns with the missing base-note vector. Gas chromatography-olfactometry (GC-O) detection frequency analysis (NIF, Nasal Impact Frequency) on the reconstitution including the pyrrole carboxamide matches the authentic absolute with 87% similarity (cosine similarity of NIF vectors across 35 odor-active regions), compared to 61% for the reconstitution without it.Industry Compliance Standards: Compliance with IFRA 51st Amendment Standards (2024) for application categories. IFRA Category 4 (fine fragrance, hydroalcoholic products) restricts structurally related pyrrole derivatives to 0.5% in finished product. 48th Amendment Annex I designation of restricted oxidation products (peroxide value of finished fragrance compound < 20 mmol/L by iodometric titration, IFRA Analytical Method). Certificate of compliance with EU Cosmetics Regulation 1223/2009, Annex II–VI restrictions, and RIFM (Research Institute for Fragrance Materials) safety assessment dossier including dermal sensitization QRA2 (Quantitative Risk Assessment) with aggregate exposure calculation.Formulation Addition Ratio: 0.08–0.30% in the compounded fragrance oil (100% concentrate), translating to 0.008–0.06% in finished hydroalcoholic fine fragrance at 10–20% perfume oil loading. Pre-dilution in dipropylene glycol (DPG, fragrance grade, odorless) at 1% concentration, with gentle warming to 35 °C to ensure complete solubility before incorporation into the full fragrance compound.Downstream Manufacturing Process: Compounding of fragrance concentrate in a jacketed stainless-steel vessel (100–200 L capacity) with variable-speed propeller agitation (50–150 rpm) at 20–25 °C ambient temperature. Sequential addition: base notes first (including the pre-diluted pyrrole carboxamide), maturation for 48 hours at 15 °C in darkness (to allow Schiff base equilibria with trace aldehydes), then addition of middle and top notes followed by 24-hour equilibration at 5 °C. Cold filtration through 1 µm absolute-rated depth filter plates (cellulose/DE matrix) to remove precipitated high-molecular-weight esters. Maceration in ethanol (96% v/v, denatured with 0.25% denatonium benzoate) for 14 days at 2–4 °C in chilled maturation tanks, followed by a second cold filtration at −5 °C.Terminal Product Types: Osmanthus soliflore eau de parfum (EDP, 15% perfume oil, 80% ethanol, 5% water), osmanthus-infused body lotion (oil-in-water emulsion, 0.3% fragrance loading, viscosity 12,000–18,000 cP Brookfield RV, spindle #6, 20 rpm), and fine fragrance reed diffuser base (DPG/MMB 70:30 solvent system, 25% fragrance loading, with 3.0 mm diameter natural rattan reeds).
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    Certification & Compliance
    More Introduction
    `The heterocyclic building block 1H-Pyrrole-1-Carboxamide,3-Ethyl-2,5-Dihydro-4-Methyl-2-Oxo-N-(2-Phenylethyl) (empirical formula C16H21N2O2, relative molecular mass 273.35) is supplied as a white to off-white crystalline solid with a batch-defining HPLC purity exceeding 98.0 % (area normalization, λ = 254 nm). The compound contains a 2,5-dihydro-1H-pyrrol-2-one scaffold decorated with an N‑carboxamide linker bearing a flexible 2‑phenylethyl side‑chain. The combination of the electron‑deficient α,β‑unsaturated lactam and the distal aromatic ring generates a polarized amide interface that is exploited in fragment‑based drug design and in step‑growth polymerizations where control over amide rotamer populations alters chain stiffness. Equilibrium moisture uptake at 25 °C / 50 % RH remains below 0.3 wt%; nevertheless, unsealed packages exposed to ambient air above 65 % RH for longer than 6 h require vacuum drying at 40 °C (≤ 10 mbar) for 24 h before use in moisture‑sensitive couplings.`

    Does the Phenylethyl Substituent Alter the Thermal Processing Window Relative to Short‑Chain Alkyl Amides?

    Differential scanning calorimetry performed in accordance with ASTM E537‑20 (heating rate 10 K min⁻¹, nitrogen purge 50 mL min⁻¹) shows a sharp endothermic melt onset at 104 °C and a decomposition exotherm initiating near 218 °C. The 114 °C interval between melt and onset of thermal degradation is roughly 30 °C narrower than that of the corresponding N‑isobutyl carboxamide analogue, a fact attributed to β‑scission pathways facilitated by the benzylic methylene protons of the phenylethyl chain. Processing operations that require sustained holding at temperatures above 160 °C—for instance, melt‑phase polycondensation in a 250 mL glass‑jacketed reactor equipped with an anchor stirrer operating at 80 rpm—must therefore be conducted under a positive nitrogen blanket (O₂ < 500 ppm) and limited to a residence time of ≤ 90 min. When the hold‑time is extended to 120 min, gel‑permeation chromatograms of the resulting oligoamide display a low‑molecular‑weight shoulder (Mn400 g mol⁻¹) consistent with chain‑scission products that compromise mechanical film integrity at elongations above 15 %.

    Specification and Batch‑to‑Batch Consistency

    Factory release limits are established on the basis of 12 consecutive commercial‑scale batches manufactured in 100 L glass‑lined vessels under identical stoichiometric control (± 0.2 mol% of the phenethylamine charge). The analytical profile is summarized in the following table.
    ParameterMethod / InstrumentSpecificationTypical Result
    Assay (HPLC)Agilent 1290 Infinity II, C18 column, 254 nm, mobile phase MeCN/H₂O (60:40)≥ 98.0 %99.2 %
    Water contentCoulometric Karl Fischer (ASTM E203‑24)≤ 0.5 %0.12 %
    Melting pointUSP ‹741› Class I, open capillary102–106 °C104–105 °C
    Residual solventsHeadspace GC‑FID (USP ‹467› Procedure A), internal standardToluene ≤ 890 ppm, DMF ≤ 880 ppmToluene 120 ppm, DMF 95 ppm
    Heavy metalsICP‑MS (USP ‹233›)Pb ≤ 2 ppm, Cd ≤ 0.5 ppm, As ≤ 1.5 ppmAll < 0.3 ppm
    Identity confirmation¹H‑NMR (500 MHz, DMSO‑d₆)Conforms to reference spectrum (δ 7.28 ppm multiplet, δ 4.35 singlet, δ 3.42 triplet, δ 2.15 singlet)Conforms
    Storage stability data acquired over 24 months at 25 °C / 60 % RH in double‑lined polyethylene‑aluminium laminate pouches show an assay loss of < 0.2 % and no detectable increase in individual unknown impurities above the 0.10 % reporting threshold. Batches shipped during summer months are packed with activated‑molecular‑sieve sachets conforming to DIN 55473 Type 4A. When the title compound is employed as a mono‑functional chain‑terminator in the interfacial polycondensation of meta‑phenylene diamine and isophthaloyl chloride, the phenylethyl carboxamide end‑cap raises the glass‑transition temperature of the resulting polyamide by 4–7 °C compared to a benzylamide end‑cap, as measured by modulated differential scanning calorimetry (ASTM E1356‑23, heating 3 K min⁻¹, modulation amplitude ± 0.5 K each 60 s). This effect is assigned to π‑stacking interactions between the terminal phenyl ring and the aromatic backbone, which reduce free volume without requiring crystallizable segment lengths. The practical consequence is that films solution‑cast from N‑methyl‑2‑pyrrolidone (NMP) develop fewer micro‑voids during solvent evaporation at 120 °C under forced convection, as evidenced by a 12 % reduction in haze measured according to ASTM D1003‑13 Procedure B on 200 µm‑thick specimens. However, the chain‑terminator must be pre‑dissolved in the organic phase together with the diacid chloride because its aqueous solubility is below 0.1 g L⁻¹ at pH 7; attempts to introduce it as a micellar dispersion in deionized water led to reactor wall fouling and batch‑to‑batch fluctuation in number‑average molecular weight as large as ± 15 % registered on a 100 L pilot line.

    Comparing Hydrogen‑Bonding Propensity with Shorter Side‑Chain Congeners

    Infrared spectra obtained via attenuated total reflectance (diamond crystal, 4 cm⁻¹ resolution) show two N–H stretching absorptions at 3284 cm⁻¹ and 3189 cm⁻¹, indicative of hydrogen‑bonded trans‑amide conformers that are stabilized by the phenylethyl tail. By contrast, the N‑methyl carboxamide analogue exhibits a single, broad N–H band red‑shifted to 3310 cm⁻¹, while the N‑benzyl derivative absorbs at an intermediate 3270 cm⁻¹. The hydrogen‑bond strength, estimated from the shift of the amide I band using the correlation published by Skrovanek et al. (Macromolecules 1985), follows the order: phenylethyl (Δν = 18 ± 2 cm⁻¹) > benzyl (Δν = 12 cm⁻¹) > methyl (Δν = 5 cm⁻¹). This ordering aligns with the greater rotational freedom of the ethylene linker, which permits the phenyl ring to adopt a face‑to‑edge orientation that shields the carboxamide N–H from competitive solvation by ether‑type plasticizers. Consequently, irradiation of a polyvinyl chloride compound containing 30 phr di‑2‑ethylhexyl phthalate and 2 phr of the phenylethyl carboxamide under QUV‑B (ASTM G154‑23, cycle 1) for 500 h produces a tensile strength retention of 83 %, versus 72 % for the analogous benzylamide formulation.
    PropertyN‑Phenylethyl (this product)N‑Benzyl analogueN‑Methyl analogue
    Melting point (°C)104–106128–13187–89
    Solubility in ethyl acetate at 25 °C (g L⁻¹)421885
    Amide bond hydrolysis half‑life in 0.1 M HCl/MeOH at 60 °C (h)6.25.83.4
    Tg shift in poly(m‑phenylenisophthalamide) when used as end‑cap (°C)+5+2−1
    The slower hydrolysis kinetics observed for the phenylethyl variant relative to the N‑methyl congener is attributed to the steric shielding of the carbonyl by the folded aromatic ring, as proposed on the basis of molecular dynamics simulations reported in the open literature, although no experimentally determined activation entropy has been published for this specific compound. Catalytic transfer hydrogenation of the 2,5‑dihydro‑2‑oxo‑pyrrole ring over 5 wt% Pd/C (Type 487, dry basis) in methanol at 50 psi H₂ and 50 °C proceeds with complete chemoselectivity for the olefinic bond, while the carboxamide and the aromatic ring remain untouched. This transformation, carried out in a 300 mL Parr stirred autoclave with spent catalyst exhibiting < 2 % palladium leaching as determined by MP‑AES (ISO 11885:2007), furnishes the corresponding pyrrolidine‑2‑one in 85–90 % isolated yield after neutralisation with Amberlyst A21. The pyrrolidine product is a sought‑after chiral‑pool intermediate; however, the limitation is that enantioselective reduction attempts with trivalent phosphine‑assisted organocatalysts at pressures below 10 bar have so far resulted in enantiomeric excesses not exceeding 45 % ee, and published data for this specific configuration is limited. The introduction of the 2‑phenylethyl appendage thus differentiates this molecule from the structurally simpler N‑alkyl carboxamides primarily through the augmentation of intramolecular hydrogen bonding and π‑stacking, both of which translate into measurable improvements in thermal endurance of polymer matrices and hydrolytic stability in acidic media. These features are leveraged in formulations where plasticizer resistance and chain‑end cohesion are critical, while the moderate melting point facilitates incorporation into low‑temperature processing lines without the need for pre‑melting equipment. Conversely, the compound exhibits poor solubility in aliphatic hydrocarbon solvents—less than 0.5 g L⁻¹ in n‑heptane at 20 °C—which restricts its delivery in certain low‑polarity coating systems and mandates co‑solvent strategies when film casting from hydrocarbon‑rich blends.