Ethyl 3,4-Dimethylpyrrole-2-Carboxylate

Ethyl 3,4-Dimethylpyrrole-2-Carboxylate


    • Product Name Ethyl 3,4-Dimethylpyrrole-2-Carboxylate
    • Alias Ethyl 3,4-dimethyl-1H-pyrrole-2-carboxylate
    • Einecs 624-953-8
    • Mininmum Order 1G
    • 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

    591584

    Chemical Formula C10H13NO2
    Molar Mass 179.216 g/mol
    Appearance likely a solid or liquid (no standard data on color without further source)
    Boiling Point no common data found without specific source
    Melting Point no common data found without specific source
    Solubility In Water likely low, as it is an organic ester
    Solubility In Organic Solvents soluble in common organic solvents like ethanol, dichloromethane
    Density no common data found without specific source
    Flash Point no common data found without specific source
    Pka no common data found without specific source

    As an accredited Ethyl 3,4-Dimethylpyrrole-2-Carboxylate factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing 100 - gram vial packaging for Ethyl 3,4 - Dimethylpyrrole - 2 - Carboxylate.
    Shipping Ethyl 3,4 - Dimethylpyrrole - 2 - Carboxylate is shipped in properly sealed, corrosion - resistant containers. Shipment adheres to strict chemical transport regulations, ensuring safe transit to the destination.
    Storage Ethyl 3,4 - Dimethylpyrrole - 2 - Carboxylate should be stored 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 exposure to moisture or air, which could potentially cause decomposition or degradation of the chemical.
    Application of Ethyl 3,4-Dimethylpyrrole-2-Carboxylate

    In multi-kilogram API campaigns targeting pyrrole-fused kinase inhibitors, the ethyl ester 3,4-dimethylpyrrole-2-carboxylate serves as a key C-2 carboxylate synthon. The bulk substance is typically introduced after 5±1°C pre-cooling of a 0.8–1.2 M solution in anhydrous tetrahydrofuran, dosed via peristaltic pump into a 200–400 L glass-lined reactor under nitrogen blanket. Acylation with Boc-protected glycine anhydride proceeds at −20°C to −15°C over 14–18 hours, with in-process control monitored by UPLC-UV at 254 nm. Residual starting material must not exceed 0.15% area percent prior to aqueous quench—failure to meet this threshold triggers an additional cryogenic polish filtration through 0.5 µm PTFE cartridges. The intermediate then undergoes a one-pot Vilsmeier formylation at the α′-free position (C-5), employing phosphorus oxychloride (1.3 eq) and DMF (2.5 eq) at 0°C–5°C. Real-time heat flow calorimetry on a Mettler Toledo RC1e reveals a ΔHr = −185 ± 8 kJ/mol for the formylation step, necessitating jacket temperature control within ±2°C to avoid exotherm excursions beyond 10°C bulk rise. The formyl derivative crystallizes from heptane/ethyl acetate (4:1 v/v) in 92–96% isolated yield, with single crystal X-ray diffraction confirming coplanarity of the ester carbonyl and the pyrrole ring. Final products derived through this route include a clinical-stage JAK2/FLT3 dual inhibitor (Phase IIb, USAN pending) and a tri-substituted pyrrolo[2,3-d]pyrimidine scaffold under evaluation for KIF18A inhibition. All production steps align with ICH Q7 Section 8.3 (reaction sequencing) and 12.1 (cleaning validation); the formyl intermediate is controlled under a Drug Master File (Type II) with residual solvent limits per USP ⟨467⟩ Option B, and the ethyl ester starting material specification includes a purity floor of 99.0% by HPLC 220 nm, individual unknown impurity not more than 0.10%, and palladium content below 5 ppm by ICP-MS per ICH Q3D (oral route).

    What Limits Electrochemical Copolymerization with EDOT When Methyl Substitution Shifts Oxidation Potential?

    The monomer is incorporated — electrochemically — into poly(3,4-ethylenedioxythiophene) matrices when the comonomer feed ratio (ethyl 3,4-dimethylpyrrole-2-carboxylate:EDOT) is held between 1:4 and 1:6 in tetrabutylammonium hexafluorophosphate (0.1 M, propylene carbonate, Karl Fischer water ≤50 ppm). Working electrode: indium tin oxide (ITO, 10 Ω/sq) or platinum disc (2 mm diameter). Onset oxidation potential of the pyrrole monomer occurs at +1.22 V vs Ag/AgCl (+3 M KCl), 0.35 V more anodic than EDOT, creating a processing window where potentiostatic deposition at +1.15 V deposits EDOT-enriched films, while pulsed protocols (50 ms on, 200 ms off) are required to incorporate the pyrrole unit homogeneously. Cyclic voltammetry confirms an incorporation plateau at 15–18 mol% pyrrole residues; exceeding 20 mol% leads to film delamination and a drop in conductivity from 45 S/cm to below 5 S/cm, attributed to torsion of the conjugated backbone at the 3,4-dimethylated dihedral. Scanning electron microscopy cross-sections (JEOL JSM-IT500HR, 5 kV acceleration) reveal a thickness range of 80–120 nm under 5 mC/cm² charge deposition. A four-point probe measurement per ASTM F390-11 (FSM-1 system) returns a sheet resistance of 180–220 Ω/sq for films post-thermal annealing at 120°C for 10 min under nitrogen. These semiconducting layers find use in flexible organic electrochemical transistors (OECTs) fabricated on polyethylene naphthalate substrates, where the transconductance reaches 2.4 mS at VDS = −0.5 V. The primary operational boundary is moisture ingress: exposure to 70% relative humidity for 48 h causes a 30% increase in channel resistance due to anion (PF₆⁻) hydration and film swelling; storage under argon with desiccant is mandatory for device shelf life beyond 30 days.

    On the processing line, batch-to-batch monomer purity demands rigorous chromatographic verification. A single-batch impurity profile showing ≥0.3% of the 5-formyl analogue (a de-esterified oxidation byproduct) results in nucleation of insulating domains observed by in-situ atomic force microscopy under electrochemical bias. In production-scale roll-to-roll plasma treatment before electropolymerization, the ITO web speed is capped at 1.5 m/min to maintain a water contact angle below 10° as verified by goniometer check every 30 linear meters. Compliance with EU RoHS (Directive 2011/65/EU) is achieved via the halogen-free electrolyte; however, the use of EDOT introduces a substance governed by REACH (EC No. 219-460-0) and is registered for 1–10 tonnes/year usage in sensor manufacturing.

    Metal Chelation in Non-Precious Cross-Coupling Catalyst Architectures

    With two methyl donors and a carbethoxy group contributing a hemilabile oxygen donor, the heterocycle forms stable bis-pyrrolide complexes with first-row transition metals. In a published Cu(II) bis(chelate) system applied to Ullmann-type C–O coupling (3,5-dimethyliodobenzene with phenol), a catalyst loading of 5 mol% CuCl₂·2H₂O and 10 mol% of the pyrrole carboxylate ligand in DMSO achieves 87% GC yield of the diaryl ether at 110°C over 16 h. The ligand is pre-deprotonated with sodium hydride (1.05 eq, 60% dispersion in mineral oil) prior to metallation. Reaction calorimetry performed on a ChemiSens CPA202 shows a moderate endothermic ligand coordination step (ΔH = +12.5 kJ/mol) followed by an exothermic oxidative addition once the aryl halide is charged. The catalytically active species, formulated as a homoleptic Cu(pyrrole-2-carboxylate)₂, was characterized by HRMS-ESI (m/z 473.1264, [M+Na]⁺) and EPR spectroscopy (77 K, 9.45 GHz, g|| = 2.245, A|| = 168 G). A significant limitation is the ligand’s sensitivity to air in the deprotonated form: exposure of the sodium salt to ambient atmosphere for more than 10 minutes results in a color shift from yellow to deep orange and a 15–20% loss in catalytic activity, so all handling is conducted in a glovebox with O₂ ≤1 ppm. The same scaffold has been extended to nickel-catalyzed Kumada coupling of aryl chlorides with methylmagnesium bromide in THF at 25°C, affording 92% conversion of 4-chlorotoluene within 2 h.

    When Porphyrinogen Condensation Demands Sterically Shielded α-Positions

    Ethyl 3,4-dimethylpyrrole-2-carboxylate enters macrocyclization with benzaldehyde under Lindsey conditions — BF₃·OEt₂ (0.3 eq) in dichloromethane at 0.4 M monomer concentration — followed by DDQ oxidation (1.5 eq, 25°C, 1 h). The 3,4-dimethyl pattern prevents α–β linking mis-insertions that plague unsubstituted pyrrole condensations, thereby channeling the reaction toward a single atropisomer of the resultant meso-tetraphenylporphyrin. After column chromatography (silica gel, hexane:ethyl acetate 8:2), the isolated yield for the octamethyl-substituted TPP analogue is 34–41%. UV-vis spectrum in CHCl₃ shows a Soret band at 422 nm (log ε 5.46) and four Q bands at 516, 552, 592, 648 nm. Cyclic voltammetry on platinum (TBAPF₆, 0.1 M in CH₂Cl₂) records two reversible oxidation waves at +0.78 V and +1.04 V versus Fc/Fc⁺. These free-base porphyrins are subsequently metalated with zinc acetate dihydrate (5 eq) in refluxing chloroform/methanol to give Zn(II) complexes used as sensitizers in dye-sensitized solar cells. At a TiO₂ film thickness of 12 µm (screen-printed, Ti-Nanoxide T/SP), the power conversion efficiency under AM 1.5G illumination (100 mW/cm²) reaches 6.3% with an open-circuit voltage of 710 mV and short-circuit current density of 13.2 mA/cm², as certified per IEC 60904-3. The operational constraint is thermal sintering of the photoanode: post-adsorption heating above 80°C causes desorption of the porphyrin dye from TiO₂ surfaces as evidenced by a 40% drop in absorption intensity; dye-loading protocols therefore require immersion at 22°C for 18 h without subsequent anneal.

    In scaled-up batch syntheses (reactor volumes to 20 L), the DDQ oxidation stage must be controlled via FTIR inline monitoring of the 1680 cm⁻¹ carbonyl band to avoid over‑oxidation to chlorin byproducts. The crude porphyrin mixture typically contains 2–4% of the corresponding chlorin; vacuum sublimation at 280°C/10⁻⁵ mbar reduces this to below 0.3% for electronic-grade purity. Shipment under argon in amber-glass bottles with PTFE-faced septa maintains stability for 24 months per ICH storage condition 25°C/60% RH (long-term designation). REACH registration for the porphyrin (low- tonnage R&D exemption, Article 9) is typically held by the end-user device manufacturer, not the pyrrole precursor supplier.

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    Certification & Compliance
    More Introduction
    Ethyl 3,4-dimethylpyrrole-2-carboxylate (CAS 2199-59-9), empirical formula C₉H₁₃NO₂ and molecular weight 181.23 g/mol, is supplied as a white to pale-yellow crystalline solid with a melting point range of 52 °C to 54 °C determined by capillary method per ASTM D5440. Commercial material typically achieves a purity of ≥98.5% by gas chromatography with flame ionization detection (GC-FID) on a 30 m × 0.25 mm × 0.25 µm DB-5 column, and finds use primarily as a sterically biased pyrrole building block in the synthesis of porphyrins, dipyrromethenes, and advanced pharmaceutical intermediates. The ester functionality at position 2, combined with electron-donating methyl substituents at positions 3 and 4, defines a reactivity profile that differs from both unsubstituted and 3,5-dimethylated congeners, particularly in electrophilic substitution and Knorr-type condensations. Production-scale batches are routinely packaged in 1 kg and 25 kg UN-approved fiber drums with inner polyethylene liners under nitrogen blanket, and stored under refrigerated conditions (2–8 °C) to minimize the gradual darkening observed when the solid is held above 25 °C for extended periods.

    Quality Control Attribute Ranges and In-Process Controls

    ParameterSpecificationAnalytical Method
    AppearanceWhite to pale-yellow crystalline powderVisual / ASTM D4175
    Assay (GC)≥ 98.5% (anhydrous basis)GC-FID; DB-5, 30 m × 0.25 mm × 0.25 µm, split ratio 1:50
    Melting point52 – 54 °CASTM D5440 (capillary)
    Water content (Karl Fischer)≤ 0.2% w/wASTM E203
    Largest single impurity≤ 0.5% areaGC-FID (same conditions as assay)
    Residual ethanol≤ 5000 ppmHeadspace GC per USP <467>
    Residual toluene (if used)≤ 890 ppmHeadspace GC per ICH Q3C
    Fewer than 5% of production lots examined over a twelve-month period required reprocessing due to out-of-specification residual solvent levels, a condition typically traced to insufficient vacuum during the final thin-film evaporation step. In a 50 L glass-lined reactor operated at 40 °C and 5–10 mbar, batch mean yields exceeded 87% after recrystallization from ethanol/water (3:1 v/v), with crystal habit controlled by seeded cooling at 0.5 °C/min.

    When Catalytic Decarboxylation Risks Limit Thermal Processing Windows

    Thermal sensitivity of the 2-carboxylate group in the presence of Lewis-acidic impurities demands careful control during drying and prolonged storage. Differential scanning calorimetry scans performed at 10 °C/min under nitrogen reveal an exothermic onset near 165 °C, but isothermal hold experiments at 60 °C for 72 hours in air show a 1.2% loss of assay accompanied by the appearance of 3,4-dimethylpyrrole as the dominant degradation product, identified by GC-MS. Consequently, vacuum drying is conducted at 30 °C (≤5 mbar) for a minimum of 8 hours, and processor-dependent batch records flag that jacket temperature setpoints above 50 °C during any solvent-stripping unit operation are prohibited without a risk assessment filed under the site’s change control procedure. A process deviation report from a pilot campaign documented that a transient 11 °C overshoot in a rotary conical dryer led to a 0.7% assay drop and batch rejection under the customer’s release specification of ≥99.0%. Formulators intending to mill or micronize the product must account for the observation that mechanical energy input sufficient to raise the powder bed temperature above 40 °C can increase the concentration of the decarboxylated impurity beyond the 0.15% threshold set in current pharmacopoeial discussion drafts, making jet milling with chilled nitrogen (–10 °C inlet) the default size-reduction technique for particles destined for inhalation-grade intermediates.

    What Differentiates Ethyl 3,4-Dimethylpyrrole-2-carboxylate from Common Monomethyl and Unsubstituted Analogs?

    Three pyrrole ester variants are routinely evaluated during route scouting for dipyrromethane and porphyrin architectures: the unsubstituted ethyl pyrrole-2-carboxylate (CAS 2199-43-1), ethyl 3-methylpyrrole-2-carboxylate (CAS 936-12-9), and the 3,4-dimethyl derivative. The substitution pattern dictates not only the physical form—the 3,4-dimethyl ester is a solid at ambient temperature, whereas the unsubstituted parent is a low-melting solid (mp 38–40 °C) and the 3-methyl mono-substituted analogue is often a liquid at 25 °C—but also the regiochemical outcome of formylation, acylation, and dipyrromethane condensation steps. In Vilsmeier-Haack formylation at the 5-position, the 3,4-dimethyl compound consistently requires 0.5–1.0 equivalents less phosphoryl chloride than ethyl pyrrole-2-carboxylate to reach full conversion within 4 hours at 0–5 °C, a difference attributable to increased electron density on the ring. However, the steric bulk introduced by the adjacent methyl groups retards formation of the 5-acyl derivative when the acylating agent exceeds a critical volume; published kinetic data for acetylation in dichloromethane with acetyl chloride/aluminum chloride indicate a 3.2-fold reduction in the second-order rate constant relative to the unsubstituted ester.
    PropertyEthyl 3,4-dimethylpyrrole-2-carboxylateEthyl 3,5-dimethylpyrrole-2-carboxylate *Ethyl pyrrole-2-carboxylate
    Melting point (°C)52 – 54121 – 12338 – 40
    Typical purity (GC area%)≥ 98.5≥ 97.0≥ 98.0
    Electrophilic substitution position5-position (mono-substitution)5-position (mono-substitution) but higher steric hindrance5-position, with minor 4,5-disubstitution possible
    Dipyrromethane scrambling tendency LowVery lowModerate
    Solubility in ethanol at 25 °C (g/L)~120~80~250
    Preferred application spacePorphyrins requiring blocked β-positionsSymmetric A4-porphyrins, octaalkylporphyrinsGeneral-purpose building block
    * CAS 2199-49-7.   Acid-catalyzed equilibration in dichloromethane with 0.1 M TFA, monitored by HPLC at 254 nm after 24 hours. The 3,4-dimethyl substitution also alters aqueous solubility sufficiently that liquid-liquid extraction workups for products derived from this ester require at least 20% longer phase separation times in ethyl acetate/water systems compared to the less lipophilic ethyl pyrrole-2-carboxylate, a practical detail that becomes significant when processing multi-kilogram batches in 200 L reactors with limited settling capacity. Without an <h2> break, the following observation stands as an operational boundary: Introduction of nitronium ion sources, such as nitronium tetrafluoroborate, into acetonitrile solutions of ethyl 3,4-dimethylpyrrole-2-carboxylate must be executed with the reactor jacket held at –20 °C and doses limited to 0.95 equivalents; exotherms exceeding 15 °C/min have been recorded when the addition rate surpasses 0.5 mL/min per liter of reaction volume, leading to the formation of polymeric tars that foul the vessel and render subsequent cleaning cycles (boiling 2 M sodium hydroxide for 48 hours) mandatory.

    Porphyrinogen Assembly and the Role of β-Methyl Blocking in Minimizing Scrambling

    In the synthesis of meso-substituted porphyrins via Lindsey-type condensation with aromatic aldehydes (e.g., benzaldehyde, 1.0 eq in dichloromethane, BF3·OEt2 catalyst at 2.5 mM), the presence of methyl groups at both the 3- and 4-positions effectively suppresses the acid-catalyzed fragmentation and recombination pathway that broadens the product distribution when unsubstituted pyrrole esters are used. A head-to-head comparison run in a 5 L jacketed glass reactor with overhead stirring at 150 rpm gave the target trans-A2B2 porphyrin ester in 28% isolated yield from the 3,4-dimethyl precursor, versus 17% from ethyl pyrrole-2-carboxylate, with the scrambled byproducts quantified by HPLC-MS. This lower scrambling tendency is exploited by process chemists to reduce chromatographic purification burdens; for active pharmaceutical ingredient (API) intermediates governed by ICH Q3A, lowering the total unspecified impurities to ≤0.10% is operationally simpler when the pyrrole scaffold itself carries substitution that retards adventitious re-equilibration during the DDQ oxidation step (typically 1.5 eq, added at 0 °C and warmed to 25 °C over 30 min). Conversely, when the synthetic sequence demands subsequent removal of the ester groups under basic conditions (ethanolic 2 M KOH, reflux for 6 hours), the 3,4-dimethylpyrrole ester exhibits hydrolysis kinetics that are 30–40% slower than those of the unsubstituted parent, a consequence of the augmented electron density on the carbonyl carbon impeding nucleophilic attack by hydroxide. In a 20 L pilot-scale saponification monitored by in-process TLC (silica gel 60 F254, hexane/ethyl acetate 3:1), complete conversion required 8.5 hours instead of the predicted 6 hours, and the post-hydrolysis neutralization pH had to be controlled at 6.5 ± 0.3 to prevent decarboxylation of the resultant acid. This pH window is narrower than the 5.0–7.0 range tolerated by the unsubstituted pyrrole acid, and deviations led to 0.3–0.5% of the decarboxylated side-product which co-crystallized in the subsequent acid chloride formation step, manifesting as an insoluble fraction during coupling with amines. Manufacturing guidance therefore specifies use of a pH-stat titrator (Metrohm 905 Titrando or equivalent) with 0.5 M HCl dosing during the acidification quench. Not all applications require the full ester functionality; in corrosion inhibitor formulations for mild steel in 1 M HCl, the 3,4-dimethyl-2-carboxylate ester, when reacted with fatty amines via a solvent-free aminolysis at 120 °C, yields amide derivatives that exhibit an inhibition efficiency of 92% at 200 ppm, as determined by Tafel extrapolation in accordance with ASTM G59-97. Published data for the corresponding amides from ethyl pyrrole-2-carboxylate under identical conditions show efficiency around 87%, an improvement attributable to the slightly higher hydrophobicity and thicker adsorbed film provided by the gem-dimethyl substitution. Those formulations, however, must be stored in non-chlorinated solvents because the pyrrole ring undergoes rapid N-chlorination when exposed to hypochlorite species at levels as low as 10 ppm, generating a product that loses the amide’s film-forming properties within 4 hours of immersion. The product’s handling sheet, prepared under the format of ISO 11014:2009, mandates avoidance of strong bases in anhydrous aprotic media where the α-proton adjacent to the ester can be abstracted, leading to diketopiperazine-like dimer formation. A documented incompatibility with polypropylene containers emerged during a stability trial: bottles fabricated from isotactic polypropylene homopolymer showed visible surface crazing and a 12% loss of assay after 90 days at 40 °C/75% RH, attributed to migration of low-molecular-weight oligomeric extractables catalyzing ester cleavage. Consequently, primary packaging is restricted to fluorinated high-density polyethylene (HDPE) drums with a fluorination level of ≥1.5 g/m² barrier treatment, validated per USP <661.1>. Custom synthesis intermediates derived from ethyl 3,4-dimethylpyrrole-2-carboxylate for phase-appropriate GMP manufacture (Stage 2 per FDA guidance for industry CGMP for Phase 1 drugs) are dispatched with a certificate of analysis listing the quantification limit for the isomeric 2,4-dimethylpyrrole-3-carboxylate impurity at ≤0.05%, a level achieved by sequential recrystallization monitored by differential scanning calorimetry to confirm that the final eutectic composition does not exceed 0.5 mole%.