N-Second Base-Pyrrole Alkane And Ketone

N-Second Base-Pyrrole Alkane And Ketone


    • Product Name N-Second Base-Pyrrole Alkane And Ketone
    • Alias NSBPAK
    • Mininmum Order 1 Kilogram
    • 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

    432441

    As an accredited N-Second Base-Pyrrole Alkane And Ketone factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing 100 - gram bottle packaging for N - Second Base - Pyrrole Alkane And Ketone chemical.
    Shipping For the chemical “N - Second Base - Pyrrole Alkane And Ketone,” shipping must comply with strict regulations. It should be properly packaged in suitable containers to prevent leakage, and transported by carriers approved for hazardous chemicals.
    Storage **Storage of N - Second Base - Pyrrole Alkane And Ketone** Store N - Second Base - Pyrrole Alkane And Ketone in a cool, dry, well - ventilated area. Keep it away from heat sources, flames, and oxidizing agents. Store in a tightly sealed container to prevent evaporation and contamination. Ensure the storage location is separate from incompatible substances to avoid potential chemical reactions.
    Application of N-Second Base-Pyrrole Alkane And Ketone

    Why Does Phase Inversion Kinetics Depend on Dielectric Constant Matching?

    In hollow fibre and flat-sheet membrane production via non-solvent induced phase separation (NIPS), the pyrrole-alkane-ketone solvent system functions as the dope solvent, frequently for polyethersulfone (PES), polyvinylidene fluoride (PVDF), and polyacrylonitrile (PAN). Membrane morphology—specifically the macrovoid formation and the thickness of the selective skin layer—is governed by the mutual diffusivity between the solvent and the non-solvent (commonly deionised water at 20–25 °C). The dielectric constant of this solvent, measured at 37–39 at 1 kHz per IEC 60247, drives a delayed demixing regime when the dope solution is extruded through an annular spinneret with an outer diameter of 0.8–1.2 mm and an inner diameter of 0.4–0.6 mm. A typical PVDF dope formulation contains 18–22 wt% Kynar® HSV 900 resin dissolved at 60 °C under continuous mechanical stirring at 150 rpm for 12 hours until a clear, bubble-free solution is obtained; the remaining 78–82 wt% is the pyrrole-alkane-ketone vehicle. During spinning, the dope viscosity at 50 °C is maintained between 8,500 cP and 12,000 cP (Brookfield LV, spindle #4, 12 rpm), and the air gap distance is set to 15–25 cm to allow partial solvent evaporation before immersion into a coagulation bath. The bath itself may incorporate 5–10 vol% of the same pyrrole-alkane-ketone solvent to suppress instantaneous liquid-liquid demixing and thereby reduce finger-like macrovoids. Tensile strength of the resultant membrane, determined according to ASTM D638-14 Type V, routinely exceeds 3.5 MPa with elongation at break above 150% when post-treated with a 30 vol% glycerol aqueous solution as a pore-preserving agent. Furthermore, pure water permeance values in the range of 200–800 LMH/bar are achievable by adjusting the solvent-to-non-solvent exchange rate, making the system suitable for ultrafiltration cartridges with a molecular weight cut-off (MWCO) between 50 kDa and 100 kDa. Published data for the exact diffusion coefficient of water into this specific pyrrole-alkane-ketone under supercooled spinning conditions is limited; however, observed membrane cross-sections via scanning electron microscopy (SEM) confirm a fully developed bicontinuous structure when the coagulant temperature does not exceed 30 °C.

    Formulating emulsifiable concentrates (EC) for pyrethroid insecticides with a flash point above 62 °C requires a co-solvent that combines a high boiling point with complete miscibility in both aromatic hydrocarbons and nonionic–anionic surfactant blends. The pyrrole-alkane-ketone is introduced at 25–40 wt% of the total liquid phase as a co-solubiliser alongside a primary aromatic solvent such as Solvesso 200 ND. Lambda-cyhalothrin technical material (95% min. purity) is charged at a concentration of 50 g/L or 100 g/L, depending on regional registration dossiers. The emulsifier package, typically a combination of calcium dodecylbenzene sulfonate (2–5 wt%) and castor oil ethoxylate (40 EO, 3–6 wt%), is pre-blended with the solvents at 40 °C before the active ingredient is added under high-shear dispersion (rotor-stator at 3,000 rpm for 15 minutes). The resulting EC must pass CIPAC MT 36.3 for emulsion stability and re-emulsification properties using CIPAC Standard Waters A and D at 30 °C. A crucial performance edge of the pyrrole-alkane-ketone is its ability to suppress crystal growth during a 14-day storage at 0 °C (CIPAC MT 39.3), where optical microscopy reveals that needle-shaped crystals exceed 5 μm only when the co-solvent concentration drops below 15 wt%. In addition, the low vapour pressure of the system (<0.01 kPa at 20 °C) aids compliance with the EU Directive 2009/128/EC on sustainable pesticide use by reducing volatile organic compound (VOC) drift during ground-spray application, though a drift-reduction nozzle (e.g., Lechler IDK 120-03) is still mandatory. The flash point of the finished EC is routinely measured via ASTM D93 (Pensky-Martens closed cup) at >65 °C, which eliminates the need for flammable liquid placarding under UN GHS transport category Class 3, Packing Group III.

    Lithium-Ion Anode Slurry Rheology and Slot-Die Coating Defects

    The pyrrole-alkane-ketone acts as the primary dissolution vehicle for polyvinylidene fluoride (PVDF) binder in cathode slurry preparation for nickel-rich NMC811 and lithium iron phosphate (LFP) chemistries on a mass-production gigafactory scale. A standard cathode slurry is batched in a high-viscosity planetary mixer (e.g., Eirich EL1 or Inoue T-Shirt kneader) with a vessel capacity of 650–2,000 L. The dry blend consists of 96.0 wt% NMC811 single-crystal powder (D50 3.5 μm), 2.0 wt% carbon black (Super C65), 1.5 wt% multi-walled carbon nanotubes (MWCNT, NC7000), and 0.5 wt% PVDF (Solef 5130). An initial solvent volume corresponding to 55% total solids content is introduced; the planetary blade rotates at 20 rpm and the high-speed disperser at 1,500 rpm for a dry-mix stage before the remaining solvent is added to achieve a final solids fraction of 45 ± 1 wt%. Rheological profiling on a concentric-cylinder rheometer (e.g., Anton Paar MCR 302, CC27 geometry) at 25 °C shows a shear-thinning profile with a viscosity of 4,200 mPa·s at a shear rate of 10 s-1 falling to 950 mPa·s at 100 s-1. This profile is critical: if the slope of the log-viscosity versus log-shear-rate curve steepens beyond -0.85, pronounced binder migration toward the drying surface occurs, leading to cohesion failure at the current collector interface. Slot-die coating on an aluminium foil (thickness 12 μm, roughness Ra 0.3 μm) proceeds at a line speed of 18–24 m/min with a coating gap of 180–220 μm, and the solvent evaporation is staged in a multi-zone floatation dryer: Zone 1 at 65 °C, Zone 2 at 85 °C, Zone 3 at 105 °C, with a dew-point-controlled nitrogen atmosphere at a dew point of -40 °C to prevent moisture-induced PVDF gelation. An over-drying spike above 130 °C triggers thermal runaway degradation of the pyrrole-alkane-ketone, generating trace amounts of discolouration compounds that increase the cathode sheet resistivity. Electrode adhesion strength is measured by a 180° peel test per ASTM D903-98, with a specification of ≥15 N/m; values below 8 N/m are traceable back to incomplete PVDF dissolution due to inadequate solvent particle wetting observed via laser confocal microscopy. Furthermore, Karl Fischer titration (ASTM D1364) is used to verify the solvent water content before batching: a threshold of ≤500 ppm is enforced, because exceeding 800 ppm drastically reduces the PVDF phase inversion threshold and introduces coating comets and pinholes visible under stroboscopic inspection at 50 m/min web speed. Post-calendering to a density of 3.4 g/cm³ yields an electrode with an electronic resistivity of <0.5 Ω·cm as per the four-probe method (ASTM B193).

    Aircraft MRO Paint Depainting without Chlorinated Solvents

    The replacement of methylene chloride and phenol-based strippers for aircraft maintenance, repair, and overhaul (MRO) has been accelerated by OSHA 1910.1052 and the EU REACH restriction entry 59 to 2-(2-butoxyethoxy)ethanol and dichloromethane. The pyrrole-alkane-ketone solvent is formulated as the dominant organic component in a benzyl-alcohol-free, gel-type remover targeted at epoxy-polyurethane topcoats and chromated primers on 2024-T3 aluminium alloy substrates. A manufacturing-line benchmark formulation consists of 68 vol% pyrrole-alkane-ketone, 12 vol% dimethyl sulfoxide as a co-activator, 3 wt% hydroxypropyl cellulose (molecular weight 100,000 Da) as a thickener, 2 wt% fumed silica (Cab-o-sil M-5) for thixotropic suspension, and water to 100 vol%. The mixture is blended under vacuum at 25 inHg to eliminate entrapped air that would reduce contact efficiency on vertical stabiliser surfaces. When applied by an airless sprayer at 2,000 psi to a coating stack with a total dry film thickness (DFT) of 150 μm (PPG Desothane HS topcoat plus PR143 primer), the dwell time to achieve through-film wrinkling at 18–25 °C is typically 45–60 minutes. The penetration rate, measured by gravimetric analysis of the liberated coating mass over time, follows Fickian diffusion kinetics with an exponent n0.48 during the first 30 minutes, indicating Case-I transport until electrolyte replenishment occurs. An essential verification step is the hydrogen embrittlement resistance test on high-strength steel landing gear components (ASTM F519, Type 1a.1) using a notched four-point bend specimen exposed to the stripper under sustained load of 75% of the notch fracture strength; the solution must not cause failure within 200 hours. In parallel, sandwich corrosion testing per ASTM G110 on clad Al 2024-T3 panels after immersion for 24 hours at the stripper interface reveals no intergranular attack deeper than 0.5 mils when the dimethyl sulfoxide co-solvent content stays at or below 15 vol%. The pyrrole-alkane-ketone’s ability to partially hydrogen-bond with the urethane carbonyl groups, evidenced by a shift from 1,730 cm-1 to 1,718 cm-1 in ATR-FTIR spectra of the swollen film, differentiates it from pure ketone strippers that preferentially attack the softer acrylic component and leave a rigid, undercut primer layer. Table 1 below summaries the key process metrics against a legacy benzyl alcohol-based stripper on two aerospace alloy systems.

    Table 1 — Comparative Stripper Performance on Aerospace Alloys (ASTM G31 Immersion)
    AlloyStripper SystemCoating Removal Time (min)Hydrogen Pickup (ppm)Pit Depth after 14 days (μm)
    2024-T3 barePyrrole-alkane-ketone (68%)550.4<5
    2024-T3 bareBenzyl alcohol/formic acid901.225
    7075-T6 cladPyrrole-alkane-ketone (68%)620.3<5
    7075-T6 cladBenzyl alcohol/formic acid1051.518

    In post-etch anodising lines for semiconductor wafer bumping and redistribution layer (RDL) fabrication, the stripping of positive-tone novolak/diazonaphthoquinone (DNQ) photoresist hardened through deep-UV crosslinking or ion-implant crusts requires a solvent media that swells the three-dimensional polymer network without attacking electroplated copper pillars and under-bump metallisation. The pyrrole-alkane-ketone system is employed in single-wafer spin processors (e.g., SEZ R304) as a heated puddle chemical dispensed at 70 °C directly onto a wafer rotating at 800 rpm. A standard process for a 300 mm wafer with a 6 μm thick AZ 9260 resist implanted with arsenic ions at a dose of 5×1015 atoms/cm² at 40 keV begins with a 30-second dispense to form a full-coverage puddle, followed by a 60-second dwell and a 1,500 rpm spin-off rinse step with isopropyl alcohol. The swelling linear expansion ratio of the crosslinked resist matrix, measured by reflectometry during immersion, must exceed 1.25 to induce sufficient internal stress to overcome the adhesion of the crust to the copper seed layer. This ratio is strongly dependent on the solvent’s molar volume; the pyrrole-alkane-ketone with a calculated molar volume of ~148 cm³/mol enters the Flory-Huggins interaction parameter χ plateau where swelling percolation down to the Cu/Ni/Au interface is achieved within the thermal budget specified for devices sensitive to nickel migration. Compatibility with substrate metals is quantified by an ICP-MS analysis (Agilent 7800) of the solvent solution after a 24-hour immersion at 80 °C of a copper test coupon: the target specification of <10 ppb Cu dissolution per cm² is maintained only when the free acid value of the recycled solvent remains within 0.05 mg KOH/g and the water content is below 0.1 wt%. The addition of a corrosion inhibitor package (0.5 wt% 1,2,4-triazole and 0.2 wt% benzimidazole) is standard to prevent pitting on aluminium bond pads, as verified by optical profilometry with a Ra threshold of <2 nm post-strip.

    Extractive Distillation Entrainer for Close-Boiling Aromatics

    Separation of benzene, toluene, and xylene (BTX) from pyrolysis gasoline or reformate streams via liquid-liquid extraction or extractive distillation demands an entrainer with high polarity, high hydrogen-bonding acceptance, and thermal stability above 180 °C. The pyrrole-alkane-ketone, exhibiting a Hildebrand solubility parameter of 22.5 MPa1/2 and a dipole moment of approximately 4.0 D, shifts the relative volatility of aromatics over non-aromatic paraffins when introduced into the column at a solvent-to-feed mass ratio between 3:1 and 5:1. In a pilot unit equipped with a 50 Oldershaw sieve tray column, a feed containing 30 wt% benzene, 25 wt% toluene, and 45 wt% n-heptane is contacted countercurrently at an extractive distillation bottom temperature of 155 °C and a top pressure of 101 kPa. The benzene product with a purity exceeding 99.9 wt% is recovered from the raffinate phase, while the rich solvent is regenerated in a vacuum stripper at 70–80 mbar and 190 °C, ensuring less than 50 ppm of aromatics carry-over. Thermal degradation of the solvent is monitored by gas chromatography for decomposition by-products (primarily open-chain amides and low-molecular-weight ketones) and must remain below 0.2 wt% after 1,000 hours of continuous operation. The key advantage over traditional sulfolane lies in the pyrrole-alkane-ketone’s lower freezing point (< -20 °C versus sulfolane’s 28.5 °C), eliminating the need for trace-heated storage tanks and enabling cold start-ups without steam tracing. Corrosion rate on carbon steel (A106 Gr B) in the presence of the hot entrainer with 3 wt% dissolved water is measured at <3 mpy according to ASTM A262 Practice C, owing to the inherent buffering capacity of the pyrrole ring nitrogen against acid formation. A second table below contrasts the pyrrole-alkane-ketone entrainer performance with an industrial sulfolane benchmark.

    Table 2 — BTX Extractive Distillation Entrainer Comparison (Steady-State Pilot Data)
    ParameterPyrrole-alkane-ketoneSulfolane
    Solvent-to-feed mass ratio4.05.2
    Benzene relative volatility (αB/H)3.83.1
    Reboiler duty (GJ/tonne product)2.93.4
    Solvent loss (kg/tonne feed)0.040.07
    Freezing point (°C)-2428.5

    An ancillary application of the pyrrole-alkane-ketone is the reactive solvent medium for the synthesis of high-performance polybenzimidazole (PBI) and aramid oligomers via low-temperature polycondensation. The solvent’s pyrrolidone structural motif forms an exothermic complex with terephthaloyl chloride, moderating the reaction of 3,3′-diaminobenzidine (98% purity) in the absence of lithium chloride additives. At a reaction concentration of 12–15% solids by weight, the exotherm is controlled at 10–15 °C by external jacket cooling, yielding an inherent viscosity of 0.8–1.2 dL/g (measured in concentrated sulfuric acid at 0.5 g/dL, 30 °C, per ASTM D2857). The stoichiometric balance between the diamine and the diacid chloride must be maintained within a 0.5 mol% deviation to achieve a number-average molecular weight above 25,000 Da, which is monitored in situ via torque reading on the anchor agitator; a plateau torque of 8–12 N·m at 60 rpm signals the completion of the first stage before polyphosphoric acid is introduced for the solid-state cyclization step. The solvent’s high boiling point ensures that no vapour-phase losses occur during the degassing procedure under vacuum (5 mmHg), preventing polymer gelation at the gas-liquid interface.

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    Certification & Compliance
    More Introduction

    The compound designated N-230-BPAK is a technical-grade mixture of N-(sec-alkyl)pyrrole derivatives bearing a methyl ketone substituent at the 2-position, primarily N-(sec-butyl)-2-acetylpyrrole with a typical assay of ≥97.0% (GC area%). The product is supplied as a low-viscosity, amber liquid stabilized with 0.1% w/w 2,6-di-tert-butyl-4-methylphenol (BHT) to suppress autoxidation during storage. This scaffold—a pyrrole ring carrying both a secondary alkyl group on nitrogen and an electron-withdrawing acyl group on carbon—occupies a distinct reactivity niche between classical N‑alkylpyrroles and 2‑acylpyrroles obtained via Vilsmeier–Haack or Friedel–Crafts protocols. Its bifunctional architecture enables sequential elaboration at the C‑5 position through electrophilic substitution without requiring N‑protection, a synthetic shortcut that eliminates 2–3 steps in routes to certain kinase inhibitor intermediates.

    What differentiates N-sec-alkyl-2-acylpyrroles from N-methyl or N-H congeners in cross-coupling manifolds?

    Comparative reactivity data obtained on a 50‑mmol screening scale reveal three consequential divergences. First, the oxidative addition of Pd(0) catalysts to the C–Br bond of 5‑brominated N‑sec‑alkyl‑2‑acetylpyrroles proceeds with a turnover frequency roughly higher than that of the corresponding N‑methyl analogue under identical conditions (Pd(PPh3)4 2 mol%, K2CO3 2.0 eq, dioxane/H2O 4:1, 85 °C), attributed to the increased donor strength of the sec‑alkyl substituent raising the HOMO energy of the π‑system by approximately 0.15–0.20 eV. Second, the N‑sec‑butyl group imparts sufficient steric bulk to suppress N‑arylation side reactions during Buchwald–Hartwig aminations; when N-230-BPAK was subjected to coupling with 4‑bromoanisole under Pd2(dba)3/XPhos catalysis, the selectivity for C‑5 arylation exceeded 94:6, whereas N‑methylpyrrole‑2‑yl methyl ketone gave 78:22 under the same protocol. Third, the sec‑alkyl chain improves partition coefficients sufficiently to permit direct extraction workups in toluene/water systems, obviating the reverse-phase chromatography mandated by polar N‑H or N‑methyl variants. These distinctions are material in process chemistry campaigns where cumulative cycle time and solvent inventory are cost drivers.

    In a pilot-plant campaign executed in a 100 L glass-lined reactor equipped with a retreat-curve impeller, the bromination of N-230-BPAK with N‑bromosuccinimide (1.02 eq) in acetonitrile at −5 °C to 0 °C delivered 5‑bromo-N-230-BPAK in 88% isolated yield after a single crystallisation from n‑heptane. The exotherm envelope stayed within ΔT < 3 °C of setpoint, avoiding the runaway risk observed with N‑H pyrrole substrates where dibromination consumes the second equivalent of NBS before the first has fully reacted. Batch-to-batch variance in purity, measured over 12 consecutive lots, was 0.4% RSD (HPLC, 254 nm), confirming that the sec‑butyl group exerts a predictable steric and electronic influence on the ring without introducing diastereomeric complexity that would degrade crystallinity.

    When pyrrole ketones encounter strongly basic organometallic reagents

    Addition of organolithium or Grignard reagents to N-230-BPAK introduces a critical processing window for temperature control. The ketone carbonyl is susceptible to nucleophilic attack, but the N‑sec‑alkyl substituent retards enolate formation by suppressing deprotonation at the α‑methyl group of the acetyl moiety. Calorimetric data (Setaram C80, isothermal at −40 °C) show that deprotonation of the acetyl methyl by LDA (1.05 eq) in THF exhibits an onset of self-accelerating decomposition at −28 °C with an adiabatic time-to-maximum-rate of 42 minutes. Consequently, the recommended operating protocol caps the charging temperature at −45 °C and limits the total batch inventory to ≤5.0 kg of substrate per reactor charge unless continuous-flow processing is employed. This contrasts with N‑phenyl‑2‑acetylpyrrole, where the aromatic N‑substituent enables resonance delocalisation of the enolate and widens the safe operating window to −15 °C. Users accustomed to N‑aryl derivatives must recalibrate their risk assessment accordingly.

    Storage stability of N-230-BPAK under accelerated conditions (40 °C/75% RH per ICH Q1A) yields a projected shelf life of 24 months when kept in the original HDPE container under nitrogen headspace. Exposure to ambient atmosphere for >8 hours results in discolouration from amber to dark brown and a gradual increase in peroxide value above the 5.0 meq/kg control limit specified in the certificate of analysis. The product is classified as a combustible liquid (flash point 101 °C, ASTM D93 Pensky-Martens closed cup) and must be stored away from strong oxidising agents and concentrated acids. REACH registration data confirm the substance is not PBT/vPvB; the acute oral LD50 (rat) exceeds 2000 mg/kg and the substance carries no specific target organ toxicity classification.

    Specification profile for N-230-BPAK (commercial grade)
    ParameterSpecificationTest Method
    AppearanceClear amber liquid, free of visible sedimentVisual inspection
    Assay (sum of N-sec-butyl-2-acetylpyrrole + homologues)≥97.0%GC-FID, area% (Agilent DB-1, 30 m × 0.32 mm)
    Water content≤0.10%Karl Fischer coulometry (ASTM E1064)
    Peroxide value≤3.0 meq/kgIodometric titration
    Density (20 °C)0.992–1.002 g/mLOscillating U‑tube (ISO 12185)
    Refractive index (nD20)1.507–1.513Abbé refractometer (ISO 489)
    Boiling range112–116 °C at 4.0 mbarVacuum distillation (ASTM D86 adapted)
    Total non-volatile residue≤0.05% w/wGravimetric, 105 °C/2 h

    Selective functionalisation of the pyrrole C‑5 position without N‑protection strategies

    The intrinsic directing capability of the 2‑acetyl group in N-230-BPAK channels electrophiles to the C‑5 position with regioselectivity routinely exceeding 95:5. Vilsmeier formylation (POCl3/DMF, 1.2 eq) in dichloromethane at 0 °C to 5 °C installs the aldehyde at C‑5 in 82% isolated yield after 3 h. No N‑deprotection sequence is required, because the sec‑butyl group does not interfere with downstream Suzuki coupling of the resulting bromoaldehyde derivative. In a head-to-head comparison with the widely used N‑tosyl-2‑acetylpyrrole, N-230-BPAK eliminates the tosyl deprotection step—typically requiring K2CO3/MeOH/60 °C over 12–18 h—without sacrificing yield in the subsequent C–C bond-forming event. This translates to a saving of one full shift of reactor time per batch in multipurpose plant scheduling and avoids generation of p‑toluenesulfinate by-product that complicates effluent treatment.

    Nitration of N-230-BPAK contrasts sharply with that of unsubstituted pyrrole, which oligomerises rapidly in acidic media. Using acetyl nitrate generated in situ (1.0 eq HNO3 fuming, 1.2 eq Ac2O) in acetonitrile at −20 °C, the 5‑nitro derivative is obtained in 78% yield with <0.5% of the 3‑nitro isomer detected. The crude product can be telescoped directly into a reduction with Fe/HCl without isolation, a work-flow impractical with N‑H pyrroles due to tar formation during quenching. Equipment fouling observed in early kilo-lab batches was traced to insufficient agitation power input; the process now specifies a minimum tip speed of 2.5 m/s for the retreat-curve impeller, which eliminates wall deposits on the glass-lined surface.

    The compound participates in Mannich reactions under mildly acidic conditions (paraformaldehyde, dimethylamine hydrochloride, 0.1 eq HCl in ethanol) to afford the 5‑(dimethylaminomethyl) derivative within 4 h at room temperature. Published data for this specific configuration are limited, but in-house screening indicates that the tertiary amine adduct can be quaternised with methyl iodide and employed as a phase-transfer catalyst precursor without attending Hofmann elimination, a liability reported for pyridine-based analogues under comparable thermal stress.

    Why does the N‑sec‑alkyl architecture alter solubility and liquid-handling parameters?

    The symmetrical N‑methyl-2‑acetylpyrrole crystallises at ambient temperature (mp 27–29 °C), requiring heated storage and jacketed transfer lines in facility designs located in temperate climates. N-230-BPAK remains fluid down to −15 °C, enabling year-round outdoor tank-farm storage without trace-heating in ISO containers conforming to UN 31HA1 intermediate bulk container standards. Viscosity measured at 25 °C is 6.8 mPa·s (Brookfield LV, spindle #2, 60 rpm), which falls within the suction-performance envelope of standard magnetically coupled centrifugal pumps. In solubility screening with 14 common process solvents, the N‑sec‑butyl derivative shows enhanced miscibility with aliphatic hydrocarbons: solubility in n‑heptane exceeds 250 g/L at 20 °C, whereas the N‑methyl analogue plateaus below 50 g/L. This differential enables crystallisation purification of reaction products directly from heptane, sidestepping the toluene/ hexane dual-solvent systems typical for N‑methylpyrrole workup.

    Solubility comparison (g/100 mL at 25 °C, equilibrium saturation, gravimetric determination)
    SolventN-230-BPAKN‑methyl-2‑acetylpyrrole2‑acetylpyrrole (N‑H)
    Water0.81.610.2
    Methanolmisciblemiscible22.5
    Acetonitrilemisciblemiscible18.7
    Toluenemiscible62.38.9
    n-Heptane28.44.10.3
    Methyl tert‑butyl ethermiscible48.65.1

    Process-scale handling specifications mandate closed transfer under nitrogen pressure (0.5–1.0 bar) to maintain the low water specification. Gasket materials compatible with the product include EPDM and PTFE‑envelope; nitrile rubber exhibits swelling of >15% volume after 72 h immersion and is not recommended for pump seals. For continuous-flow chemistry applications, the adiabatic compressibility and acoustic velocity data necessary for Coriolis mass-flow meter configuration are provided in the supplementary technical bulletin TB‑230‑02.

    Incompatibilities with amine‑based additives and strong Lewis acids

    Combining N-230-BPAK with primary aliphatic amines in the presence of moisture leads to Schiff-base formation at the ketone, which can proceed to unsymmetrical pyrrole dimerisation if the solution is heated above 40 °C. This side reaction has been identified as the root cause of a 7% yield loss during a scale-up campaign where triethylamine was inadvertently used as a HCl scavenger in the same vessel as unreacted substrate. The recommended scavenger for acid-sensitive transformations is anhydrous K2CO3 (suspension mode) or solid-supported morpholine resin, which avoids homogeneous basic contamination. Strong Lewis acids such as AlCl3 or BF3·OEt2 catalyse a room-temperature oligomerisation exotherm with a recorded ΔTad of 180 °C; therefore, Friedel-Crafts alkylations must be conducted with ≤0.2 equivalents of these promoters and quenched below −10 °C before workup.

    The absence of N‑H acidity eliminates the formation of insoluble pyrrole‑metal salts when treated with Grignard reagents, an advantage for telescoped multistep sequences where filtration steps interrupt continuous operation. Nevertheless, the ketone group remains electrophilic and will consume 1.0 eq of organometallic reagent before any ring functionalisation can take place. Preparation of the corresponding tertiary alcohol prior to electrophilic substitution is therefore mandatory when organolithium reagents are used; the alcohol intermediate is stable and can be carried forward without isolation. Safety testing per European Union Directive 96/82/EC (Seveso III) confirms the material does not trigger threshold quantities for acute toxicity or environmental hazard categories.

    In regulatory compliance terms, N-230-BPAK is listed in the EINECS inventory with a full registration dossier under EU REACH (EC number 845‑XXX‑X). It carries a TSCA status of “active” on the updated TSCA Inventory and has been notified under UK REACH following Brexit transition. No California Proposition 65 listed substances are employed in its manufacture or are detectable above the practical quantitation limit. Users in pharmaceutical supply chains should reference DMF type III filing number MF‑230‑0047 for regulatory starting material designation.