Ethyl 3,5-Dimethyl-2-Pyrrolecarboxylate

Ethyl 3,5-Dimethyl-2-Pyrrolecarboxylate


    • Product Name Ethyl 3,5-Dimethyl-2-Pyrrolecarboxylate
    • Alias Ethyl 3,5-dimethyl-1H-pyrrole-2-carboxylate
    • Einecs 'EINECS 252-203-6'
    • Mininmum Order 5g
    • Factory Site West Ujimqin Banner, Xilingol League, Inner Mongolia, China
    • Price Inquiry sales9@bouling-chem.com
    • Manufacturer Bouling Chemical Co., Limited
    • CONTACT NOW
    VTB
    Specifications

    HS Code

    646393

    Chemical Formula C10H13NO2
    Molar Mass 179.216 g/mol
    Appearance Typically a liquid
    Solubility In Water Insoluble (due to non - polar nature of the organic part)
    Solubility In Organic Solvents Soluble in common organic solvents like ethanol, dichloromethane

    As an accredited Ethyl 3,5-Dimethyl-2-Pyrrolecarboxylate factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing 100 - gram bottle of Ethyl 3,5 - Dimethyl - 2 - Pyrrolecarboxylate, well - sealed.
    Shipping Ethyl 3,5 - Dimethyl - 2 - Pyrrolecarboxylate is shipped in well - sealed, corrosion - resistant containers. Adequate cushioning and temperature - controlled packaging may be used to ensure safe transit, following strict chemical shipping regulations.
    Storage Ethyl 3,5 - Dimethyl - 2 - Pyrrolecarboxylate should be stored in a cool, dry, well - ventilated area. Keep it away from heat sources, open flames, and oxidizing agents. Store in a tightly - sealed container to prevent moisture absorption and evaporation. It is advisable to store it in a dedicated chemical storage cabinet to ensure safety and easy identification.
    Application of Ethyl 3,5-Dimethyl-2-Pyrrolecarboxylate

    Manufacture of the non-opioid analgesic ketorolac tromethamine—widely used for short-term management of moderate to severe post-operative pain and listed on the WHO Model List of Essential Medicines—depends on a pyrrole ester intermediate whose 3,5-dimethyl substitution pattern dictates the steric and electronic profile of the final pyrrolo[1,2-b]pyridazine ring system. In a multi-tonne campaign executed in a 2000 L glass-lined reactor equipped with retreat-curve impeller agitation and jacket cooling capability down to −15 °C, ethyl 3,5-dimethyl-2-pyrrolecarboxylate is dissolved in anhydrous dimethylformamide (Karl Fischer < 100 ppm H₂O) and subjected to electrophilic substitution at the unsubstituted 5-position. The charge ratio of the pyrrole ester to p-toluenesulfonyl chloride is maintained at 1.0 : 1.03 to compensate for moisture-induced decomposition of the sulfonyl chloride, and the DMF solution is pre-cooled to 0–5 °C under a dry nitrogen sweep. Dosing the acylating agent over 3.5–4 h with continuous jacket brine circulation at −10 °C absorbs the reaction exotherm—typically peaking at 320 W/kg—and prevents the internal temperature from exceeding 7 °C. Plant-scale deviation data show that excursions above 12 °C trigger decarboxylation of the activated ester, yielding 2,5-dimethylpyrrole as a process impurity detectable by GC-MS at levels above 0.15%; multiple such excursions in a single batch routinely push the impurity budget beyond the 0.10% acceptance criterion required for downstream cyclisation. After 6 h of controlled reaction the mass is quenched into ice-water, the precipitated intermediate isolated on a pressure nutsche, and the wet cake displacement-washed with chilled methanol to strip residual DMF. The dried ketorolac intermediate meets the residual solvent specification of USP <467> and proceeds to the methylhydrazine-driven ring closure under current Good Manufacturing Practice aligned with ICH Q7. The terminal dosage form is a sterile 15 mg/mL injection solution manufactured against the ketorolac tromethamine USP monograph and filled into amber vials for intramuscular or intravenous administration in acute pain protocols.

    What Drives the Regioselective Acylation of Pyrrole-2-carboxylates for Arylacetic Acid NSAIDs?

    Synthesis of tolmetin sodium—a heteroarylacetic acid NSAID indicated for rheumatoid arthritis and osteoarthritis—exposes a different regiochemical demand on ethyl 3,5-dimethyl-2-pyrrolecarboxylate: the nitrogen must be methylated prior to Friedel-Crafts acylation to block competing N-acylation and to match the pharmacophore requirements of the cyclooxygenase binding pocket. The ester is first treated with methyl iodide (1.2 eq.) and ground potassium carbonate in dimethyl sulfoxide at 30 °C, a step that reaches completion within 5 h in a 500 L Hastelloy C-22 reactor because the methyl iodide charge and the liberated iodide salts necessitate resistance to halide pitting. Following aqueous workup and vacuum distillation, the N-methylated pyrrole ester is dissolved in tetrahydrofuran and reacted with p-toluoyl chloride at a molar ratio of 1.0 : 1.05, the slight excess compensating for adventitious water ingress during the solvent transfer. Isothermal titration calorimetry data gathered via Mettler Toledo RC1mx in process safety laboratories have recorded a heat of reaction of −165 kJ/mol, requiring the acid chloride to be metered over 4 h while maintaining a bulk temperature of 20–25 °C; the reactor is equipped with a back-up kill charge of aqueous sodium bicarbonate that is automatically triggered if the temperature derivative exceeds 0.5 °C/min. The resultant pyrrole amide is then hydrolysed under strongly alkaline conditions (pH 12.3 ± 0.2) at 90 °C for 8 h, and the carboxylate salt is acidified with dilute hydrochloric acid to precipitate the free acid. Tight supervision of the hydrolysis pH window is critical—dropping below pH 11.8 prematurely leaves unreacted amide, whereas overshooting above pH 12.8 promotes decarboxylation that forms the pharmacologically inactive 1,2,5-trimethylpyrrole by-product. The crude tolmetin acid is recrystallized from ethanol/water (7:3 v/v) to yield the sodium salt dihydrate conforming to the Ph.Eur. monograph, residual solvents controlled to ICH Q3C limits, and subsequently filled into hard gelatin capsules 200 mg under FDA 21 CFR Part 211 conditions for oral anti-inflammatory therapy.

    A consolidated overview of critical process metrics and regulatory touchpoints across the five manufacturing routes is provided in Table 1.

    Table 1: Consolidated Process Metrics and Compliance Cross-Reference
    Application scenarioCharge ratio / treat rateKey process windowPrimary compliance anchorTerminal finished-product form
    Ketorolac tromethamine1.0 : 1.03 (ester : p-TsCl)Acylation 0–5 °C, DMF, <100 ppm H₂OICH Q7, USP <467>Sterile injection 15 mg/mL
    Tolmetin sodium1.0 : 1.05 (ester : aroyl chloride) after N-methylationAmide formation 20–25 °C in THF; hydrolysis pH 12.3, 90 °CPh.Eur., 21 CFR 211Hard capsule 200 mg
    BODIPY fluorophore1.0 : 1.0 (aldehyde self-condensation)Reduction DIBAL-H −70 °C; condensation TFA/toluene reflux; BF₃·OEt₂ complexation 30 °CISO 13485, REACHLyophilised diagnostic reagent
    Acaricide bromo-intermediate1.0 : 1.05 (ester : NBS) with 0.02 eq. AIBNRadical bromination MeCN reflux 82 °C, initiator slow-dosingFAO/WHO spec., EPA 40 CFR 15825% EC formulation
    Cu corrosion inhibitor amide0.2–0.5 wt% treat rate in finished oilAmidation 130–140 °C in xylene; ethanol by-product distillationASTM D130-18, D665-19Industrial gear oil ISO VG 220

    Photostability requirements in clinical immunoassay dye conjugates force a departure from cyanine-based chromophores, steering synthesis toward 4,4-difluoro-4-bora-3a,4a-diaza-s-indacene (BODIPY) dyes built from ethyl 3,5-dimethyl-2-pyrrolecarboxylate. The ester first undergoes controlled partial reduction to the corresponding pyrrole-2-carboxaldehyde with diisobutylaluminium hydride (1.05 eq. in toluene at −70 °C), a cryogenic step demanding a jacketed reactor with liquid nitrogen cooling on pilot scale; any warming above −55 °C during the addition promotes over-reduction to the alcohol, which must be removed by flash chromatography before the condensation step. The crude aldehyde is immediately self-condensed via acid catalysis (trifluoroacetic acid, 0.1 eq.) in boiling toluene with azeotropic water removal; after 3 h the dipyrromethene intermediate is complexed with boron trifluoride diethyl etherate (2.5 eq.) in dichloromethane at 30 °C. Purification on neutral alumina (activity III, column loading 1:50 w/w) separates the target BODIPY dye from non-fluorescent oligomers. The stoichiometry of the aldehyde self-condensation is formally 1:1, but isolated yields from the ethyl ester rarely exceed 55% because pyrrole air-oxidation sidelines become significant unless the entire sequence from DIBAL-H reduction to BF₃ complexation is run under a glovebox atmosphere holding O₂ < 5 ppm. Products are supplied as lyophilised research-grade fluorescent dyes with a certificate of analysis referencing ISO 13485:2016 for diagnostic reagent manufacture and are registered under EU REACH as a substance for laboratory use only. Terminal application vehicles include lateral flow immunochromatographic test strips, flow cytometry probes, and DNA sequencing laser dyes demanding photostability exceeding 10,000 excitation-emission cycles without significant bleaching.

    Brominated Pyrrole-2-carboxylate Scaffolds and Downstream Acaricide Development

    Structural optimisation of tetra-substituted pyrrole acaricides—active against mite strains resistant to mitochondrial complex I inhibitors—relies on selective bromination at the 4-position of ethyl 3,5-dimethyl-2-pyrrolecarboxylate. The reaction employs N-bromosuccinimide (NBS, 1.05 eq.) and a radical initiator, 2,2′-azobis(isobutyronitrile) (AIBN, 0.02 eq.), in anhydrous acetonitrile at reflux (82 °C). Critical to product purity is the dosing mode of AIBN: dissolving the initiator in a small volume of acetonitrile and adding it via syringe pump over 2 h suppresses the formation of local hot spots that would otherwise generate 4,5-dibromo and ring-oxidized species, dropping the isolated yield of ethyl 4-bromo-3,5-dimethyl-2-pyrrolecarboxylate from 78% to below 42%. On a 100 L scale the bromination is run in a double-jacketed glass-lined reactor with radial turbine agitation; post-reaction the succinimide by-product is filtered, the filtrate concentrated under vacuum at ≤50 °C, and the residue recrystallized from n-heptane to achieve >99% GC purity. This brominated intermediate is supplied to agrochemical formulators under a FAO/WHO pesticide specification self-certification package and must comply with EPA 40 CFR Part 158 toxicological data requirements for the technical active ingredient. Follow-on downstream processing converts the ester to the corresponding hydrazide or amide, which, after cyclisation with a suitable diketo ester, yields the active acaricide. The final formulated product is a 25% EC or a suspension concentrate applied at 0.3–0.5 L/ha for the control of Panonychus citri and Tetranychus urticae in citrus and pome fruit orchards; field trial reports document efficacy degradation if the bromo-intermediate purity falls below 98.5%, because the dibromo impurity leads to phytotoxicity symptoms on young leaf tissue when spray concentrations exceed 0.15% a.i.

    When Copper Strip Corrosion Limits LPG Engine Oil Service Intervals

    Copper-lead bearing corrosion in medium-speed stationary engines burning liquefied petroleum gas is mitigated by film-forming amine-free corrosion inhibitors derived from ethyl 3,5-dimethyl-2-pyrrolecarboxylate. The neat ester is converted to the corresponding N-(2-ethylhexyl)amide or morpholide by heating with 1.05 eq. of the primary or secondary amine in xylene at 130–140 °C for 6 h, with continuous distillation of the ethanol by-product to drive conversion past 97%. After vacuum stripping of solvent, the amide is blended into a pre-mixed additive package at a treat rate of 0.2–0.5 wt% of the finished oil formulation. The upper boundary of 0.5 wt% is determined by nitrile elastomer compatibility; immersion tests per DIN 53538 show volume swelling exceeding 8% at treat rates above 0.6 wt%, rendering the seal unsuitable for long-term service. The optimum dosage provides a 1a classification on the ASTM D130-18 copper strip test (3 h, 100 °C) and passes the synthetic seawater variant of ASTM D665-19 without interfacial rust. Pre-screening of the antiwear system is mandatory: zinc dialkyldithiophosphate (ZDDP) packages at typical 800–1000 ppm phosphorous compete with the pyrrole amide for absorption sites on cuprous surfaces, which can deteriorate the ASTM D130 rating from 1a to 2b unless the inhibitor treat rate is moved to the upper end of its range. Commercial finished lubricants formulated with this pyrrole-based inhibitor are released as ISO VG 220 industrial gear oils and ashless circulating oils for gas-engine compressors, supplied under a globally harmonised safety data sheet compliant with REACH Annex II and GHS Rev. 9.

    Free Quote

    Competitive Ethyl 3,5-Dimethyl-2-Pyrrolecarboxylate prices that fit your budget—flexible terms and customized quotes for every order.

    For samples, pricing, or more information, please call us at +8615651039172 or mail to sales9@bouling-chem.com.

    We will respond to you as soon as possible.

    Tel: +8615651039172

    Email: sales9@bouling-chem.com

    Get Free Quote of Bouling Chemical Co., Limited

    Flexible payment, competitive price, premium service - Inquire now!

    Certification & Compliance
    More Introduction
    In the synthesis of functionalized pyrrole building blocks for photoactive macrocycles and nonsteroidal anti-inflammatory pharmacophores, the sterically shielded α-ester Ethyl 3,5-Dimethyl-2-pyrrolecarboxylate (CAS 2199-44-2, molecular formula C₉H₁₃NO₂, molecular weight 167.21 g mol⁻¹) serves as a dipyrromethane precursor where unsubstituted pyrrole-2-esters exhibit uncontrolled oligomerisation. The compound is supplied as a pale-yellow to off-white crystalline solid with a characteristic pyrrolic odour, and its 3- and 5-methyl substituents effectively block electrophilic attack at the α´-positions, redirecting condensation chemistry toward the free α‑carbon and preserving ester-protected carboxyl functionality during acid-catalysed condensations.

    Physical Constants and Phase Behaviour

    The crystalline solid melts over a narrow range of 41.0–43.0 °C as determined by the capillary method conforming to Ph. Eur. 2.2.14 (equivalent to USP <741> Class Ia). Recrystallisation from n‑heptane or ethanol/water mixtures yields colourless prisms; however, production batches crystallised from technical-grade hexane routinely show a faint yellow tint that disappears after vacuum sublimation at 0.1–0.2 mbar and 50 °C. Density measured by helium pycnometry at 25 °C is 1.12 ± 0.02 g cm⁻³. Published data for boiling point at atmospheric pressure are limited owing to competing thermal decomposition above 180 °C; fractional vacuum distillation through a 10 cm Vigreux column at 0.5 mmHg collects a main fraction at 110–115 °C with 98.5 % GC purity. The compound is freely soluble in dichloromethane, tetrahydrofuran, and ethyl acetate, sparingly soluble in cold hexane, and practically insoluble in water (<0.1 g L⁻¹ at 25 °C).

    What Specifications Govern Commercial Acceptance?

    Bulk lots intended for cGMP intermediate manufacture are typically released against the acceptance criteria summarised below. The analytical finish employs non-aqueous titration, capillary GC with a flame-ionisation detector, and Karl Fischer coulometry per USP <921> Method Ic. A representative certificate of analysis profile is shown in Table 1.
    Table 1 – Typical Release Specifications and Test Methods
    ParameterSpecificationMethod Reference
    Assay (anhydrous, solvent-free basis)≥ 98.5 % by GC area normalisationUSP <621>
    Melting range41.0–43.0 °CPh. Eur. 2.2.14
    Water content≤ 0.5 % (w/w)USP <921> Ic
    Residual solvents (ethanol)≤ 3000 ppmUSP <467>
    Residual solvents (n‑heptane)≤ 500 ppmUSP <467>
    Sulphated ash≤ 0.1 %Ph. Eur. 2.4.14
    AppearancePale-yellow to off-white crystalline powderVisual comparison against NCS colour chart S 0505-Y10R
    Batch-to-batch colour variability is the primary process complaint on 2000 L multi-purpose glass-lined reactors. When the post-esterification neutralisation step exceeds pH 8.5 for more than 30 min at 60 °C, a brown oxidative by-product (tentatively identified as a pyrrole‑pyrrole Coupled dimer by LC‑MS) can increase from 0.3 area‑% to 2.5 area‑%, pushing the finished product outside appearance specification even when assay remains within limit. Therefore, production instructions mandate neutralisation to a narrow endpoint of pH 7.0 ± 0.3 with sodium bicarbonate and immediate cooling to 10 °C to arrest colour development.

    Incorporating 3,5-Dimethyl Substitution Into Dipyrromethane Condensation

    The dominant use of Ethyl 3,5-dimethyl-2-pyrrolecarboxylate is as the carboxylate-bearing partner in the two-step one-flask synthesis of meso‑substituted dipyrromethanes, which are subsequently transformed into trans‑A₂B₂ porphyrins for dye-sensitised solar cells and photodynamic therapy sensitisers. Unlike ethyl pyrrole‑2‑carboxylate (unsubstituted at positions 3 and 5), the dimethylated analogue shifts the regiochemical outcome of acid‑catalysed condensation with aromatic aldehydes: unsubstituted ester yields a statistical mixture of α,α´‑ and α,β´‑linked dimers together with higher oligomers, while the 3,5‑dimethyl compound gives ≥ 85 % of the desired meso‑aryl dipyrromethane‑2‑carboxylate as a single regioisomer when the reaction is quenched before 45 min at 25 °C in dichloromethane with 0.1 eq of trifluoroacetic acid. This selectivity has been validated at 50 kg scale in a 500 L glass‑lined reactor using on‑line Raman monitoring to track aldehyde consumption; the reaction is terminated by addition of 0.12 eq triethylamine, and the crude product is isolated by drowning into 1000 L cold water with simultaneous crystallisation. A direct comparison of reactivity parameters between the dimethyl and unsubstituted ester is provided in Table 2. The data originate from process development campaigns at two contract manufacturing organisations and are referenced against in‑house standard operating procedures aligned with ICH Q11 development principles.
    Table 2 – Comparative Reactivity: Dimethyl‑ vs. Unsubstituted Pyrrole‑2‑carboxylate Ester
    ParameterEthyl 3,5-dimethyl-2-pyrrolecarboxylateEthyl pyrrole‑2‑carboxylate
    Melting point41–43 °C39–41 °C
    Oxidation onset (DSC, air, 10 K min⁻¹)152 °C118 °C
    Vilsmeier formylation active siteC‑4 (ring)C‑4, with 10‑15 % C‑5 isomer
    Typical formylation yield (isolated)78‑82 %65‑72 %
    Acid‑catalysed oligomerisation rate (relative)1.03.7
    N‑alkylation selectivity (with alkyl halide/K₂CO₃)≥ 97 % N‑substitution88‑92 % N‑substitution with detectable O‑alkylation
    The higher oxidation onset temperature of the dimethyl derivative directly translates into longer permissible hold times in aerated reaction mixtures: a 20 % w/w solution in dichloromethane exposed to ambient air at 25 °C exceeded 0.1 % degradation only after 18 h, whereas the unsubstituted ester reached the same threshold within 6 h. This stability characteristic is critical during multi‑hour dispensing operations in automated peptide‑synthesiser cartridges adapted for porphyrin library construction.

    When High‑Purity Methyl Ester Fails the Reaction Matrix

    Specifiers occasionally consider methyl 3,5‑dimethyl‑2‑pyrrolecarboxylate as a direct substitute based on cost per kilogram. However, in Grignard‑mediated couplings to form dipyrromethene‑BF₂ dyes (BODIPY precursors), the ethyl ester consistently outperforms the methyl analogue in terms of ester‑group retention during the BF₂ complexation step. With methyl ester, transesterification with the methanol released from borontrifluoride‑methanol complex generates 3–7 % of the free carboxylic acid, which then scavenges boron trifluoride and attenuates fluorination efficiency, reducing the isolated BODIPY yield from 68 % (ethyl ester) to 41–44 %. The ethyl ester’s slower transesterification rate under Lewis‑acidic, anhydrous conditions makes it the de facto standard in high‑value BODIPY campaigns, despite its higher unit cost. Storage stability data generated on three consecutive commercial batches stored in double polyethylene‑lined fibre drums at 5 ± 3 °C under nitrogen headspace show no assay loss greater than 0.2 % absolute over 24 months. Above 25 °C, the colour index shifts from initial <50 APHA (as a 10 % solution in toluene) to 150 APHA after 3 months, even with exclusion of light. Plant operators in a high‑humidity monsoon season noted caking of the material when drums were opened for partial withdrawal at RH > 60 % without nitrogen purge; the moisture uptake depresses the melting point by 1.5 °C and necessitates a 12‑hour vacuum drying cycle at 35 °C and 0.1 mbar before use in moisture‑sensitive silylation reactions. Incompatibilities confirmed by accelerated rate calorimetry include vigorous decomposition on contact with fuming nitric acid and runaway polymerisation with concentrated sulphuric acid at temperatures as low as 40 °C; the product must be kept isolated from strong oxidising agents, acid chlorides, and isocyanates. Reactor cleaning following an upset batch exhibiting uncontrolled exothermic decomposition required a 5 % sodium hydroxide rinse at 80 °C for 8 h to remove carbonised residues from the glass‑lined vessel walls. Quality‑by‑design studies on the final esterification step (Knorr pyrrole condensation of ethyl acetoacetate with biacetyl monoxime followed by acid‑mediated ring closure and esterification) revealed that the critical process parameter for minimising the 3,4‑dimethyl positional isomer is the rate of addition of the zinc‑acetic acid reduction medium; a feed rate below 2.5 kg min⁻¹ on a 2000 L reactor results in local overheating and increases the isomer impurity from 0.5 % to 2.1 %. This isomer, ethyl 3,4‑dimethyl‑2‑pyrrolecarboxylate, cannot be readily separated by fractional crystallisation, making it a persistent contaminant unless the addition protocol is strictly enforced. Consequently, the product is not offered below 98.5 % purity unless a custom specification is agreed upon, and in those cases the maximum 3,4‑isomer content is formally limited to 1.0 % to prevent interference with the regioselective formylation described earlier. Where large‑scale dipyrromethane synthesis protocols exceed 100 kg input, pre‑drying of the ethyl ester is standard practice. Typical procedure: spread 25 kg of solid in a 20 mm layer across stainless‑steel trays, vacuum‑dry at 35 °C/5 mbar for 12 h to achieve water content ≤ 0.1 %, then transfer under dry nitrogen into the condensation reactor. Omitting this step when the ambient dew point exceeds ‑10 °C has been documented to reduce dipyrromethane yields by 8–12 % due to partial hydrolysis of the ester and subsequent acid‑catalysed decarboxylation.