|
HS Code |
589296 |
| Chemical Formula | C10H15NO2 |
| Molar Mass | 181.23 g/mol |
| Appearance | Solid (predicted) |
| Boiling Point | Estimated around 240 - 260 °C (predicted) |
| Density | Estimated around 1.0 - 1.1 g/cm³ (predicted) |
| Solubility In Water | Poor (due to non - polar nature of alkyl groups) |
| Solubility In Organic Solvents | Soluble in common organic solvents like ethanol, acetone |
| Flash Point | Estimated around 100 - 120 °C (predicted) |
| Vapor Pressure | Very low at room temperature (predicted) |
As an accredited 1H-Pyrrole-2-Carboxylicacid,3,5-Dimethyl-,Ethylester factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | 100g of 3,5 - Dimethyl - 1H - pyrrole - 2 - carboxylic acid ethyl ester in sealed chemical - grade packaging. |
| Shipping | The chemical "1H - Pyrrole - 2 - Carboxylic acid, 3,5 - Dimethyl -, Ethyl ester" should be shipped in properly sealed containers, following all relevant hazardous material regulations to ensure safe transportation. |
| Storage | Store "1H - Pyrrole - 2 - Carboxylic acid, 3,5 - Dimethyl -, Ethyl ester" in a cool, dry place away from heat sources and direct sunlight. Keep it in a well - sealed container to prevent exposure to air and moisture, which could potentially cause degradation. Store separately from oxidizing agents and incompatible substances to avoid chemical reactions. |
Tightening the stoichiometric window to 2.00–2.10 mol of the ethyl ester per mole of aromatic aldehyde suppresses oligomeric by‑products that otherwise propagate when the acid‑catalysed condensation lingers beyond 6 hours at 20 °C. In a 500 L glass‑lined reactor equipped with a retreat‑curve impeller, the charge sequence—aldehyde dissolved in dichloromethane, followed by dropwise addition of the ester and a 0.15 eq portion of trifluoroacetic acid under nitrogen—has been correlated with a 14–18 % improvement in dipyrromethane selectivity over inverse‑addition protocols reported on pilot‑scale campaigns. The reaction mass is held at 0–5 °C for the first 3 hours to retard the formation of tripyrrin‑coloured impurities; afterwards the jacket is warmed to 22 °C and conversion is tracked by inline FT‑IR monitoring of the carbonyl stretch shift at 1684 cm⁻¹. Once aldehyde consumption exceeds 97 %, the intermediate is oxidised with 2.3 eq of 2,3‑dichloro‑5,6‑dicyano‑1,4‑benzoquinone and immediately complexed with boron trifluoride diethyl etherate (1.1 eq relative to the in‑situ dipyrromethane) at 40 °C for 90 minutes. The crude BODIPY is isolated by neutral alumina filtration, concentrated, and recrystallised from ethyl acetate‑heptane mixtures to yield the boron‑dipyrromethene core with purity routinely exceeding 98.5 area‑% by HPLC (C18, acetonitrile‑water, 254 nm).
NS5A Inhibitor Fragment Assembly and the Role of Carboxylic Acid Ester ActivationWhen the ethyl ester is deployed as a protected pyrrole‑2‑carboxylic acid synthon in the convergent synthesis of hepatitis C virus NS5A protein inhibitors, the quality attributes of the starting material directly influence the enantiomeric purity of the final amide coupling step. The bulk intermediate is received with a certificate of analysis that mandates ≥99.0 % assay (GC‑FID, Supelco SLB‑5ms column, 30 m × 0.25 mm × 0.25 µm), ≤0.20 % water by Karl Fischer coulometry, and residual solvents—predominantly ethanol and ethyl acetate—each below International Council for Harmonisation Q3C Option 2 limits. Saponification to the free acid is performed at 10–15 °C in a 4:1 tetrahydrofuran‑water mixture containing 1.05 eq of lithium hydroxide monohydrate; extending the hydrolysis beyond 2 hours has been observed on kilogram‑scale batches to promote decarboxylation of the β‑free acid, generating 2,4‑dimethylpyrrole as a detectable impurity that must be limited to <0.15 area‑% to avoid carry‑over into the final API.Following neutralisation and phase separation, the carboxylic acid is activated with 1‑ethyl‑3‑(3‑dimethylaminopropyl)carbodiimide hydrochloride (1.2 eq) and 1‑hydroxybenzotriazole hydrate (1.2 eq) in dichloromethane at −15 °C before addition of a chiral pyrrolidine‑methylamine fragment. The processing window is narrow: batch records from commercial manufacturers indicate that raising the activation temperature by merely 8 °C increases the racemisation rate of the adjacent stereocentre from <0.4 % to >3.2 %, exceeding the acceptance criterion of 0.6 % diastereomeric excess loss specified in the drug master file. The crude amide is purified by flash silica chromatography and recrystallised from isopropanol‑water to afford the NS5A dimer precursor with a typical overall yield of 72–78 % from the ethyl ester. The weight contribution of the 3,5‑dimethylpyrrole‑2‑carbonyl motif ranges between 18 % and 22 % of the final active pharmaceutical ingredient molecular weight, placing it within the scope of ICH Q7 Class 1 registered starting material requirements.
What Determines the Electron Affinity of Diketopyrrolopyrrole‑Free Acceptors Based on Dimethylpyrrole?In non‑fullerene acceptor architectures that dispense with the classical diketopyrrolopyrrole core, the electron‑withdrawing character of the terminal unit can be modulated by condensing 3,5‑dimethyl‑1H‑pyrrole‑2‑carboxylic acid ethyl ester onto an aldehyde‑functionalised indacenodithiophene or benzodithiophene platform through Knoevenagel reaction. The ethyl carboxylate group contributes a LUMO stabilisation of approximately 0.12 eV relative to the unsubstituted pyrrole analogue, measured by cyclic voltammetry on drop‑cast films with a glassy‑carbon working electrode in 0.1 M tetrabutylammonium hexafluorophosphate acetonitrile electrolyte at a scan rate of 50 mV s⁻¹. The synthetic protocol requires rigorous anhydrous handling: the ester (2.2 eq per aldehydic function) and the donor core are dissolved in a 1:1 chloroform‑pyridine mixture inside an argon‑filled glovebox with moisture and oxygen both maintained below 1 ppm, and 2.5 eq of titanium tetrachloride are slowly added at 0 °C before heating to 80 °C for 16 hours. Quenching is performed onto crushed ice doped with acetic acid; crude acceptors are purified via successive Soxhlet extraction with methanol, hexane, and dichloromethane to eliminate oligomeric remnants that would otherwise act as exciton‑quenching traps in the active‑layer blend.The resulting dimethylpyrrole‑ester‑terminated small molecules exhibit an optical bandgap of 1.45–1.55 eV and are processed with donor polymers such as PBDB‑T to fabricate bulk‑heterojunction devices in an inverted architecture (ITO‑zinc oxide‑active layer‑molybdenum trioxide‑silver). Electron mobility values measured by the space‑charge‑limited‑current method on electron‑only devices reach 3.8 × 10⁻⁴ cm² V⁻¹ s⁻¹, a parameter that is extremely sensitive to residual metal content. As a consequence, the ester is required to meet SEMI Standard C45‑0618 purity thresholds for electronic chemicals: ≥99.95 % assay by GC‑FID, individual metal impurities ≤5 ppb each for copper, iron, and nickel, and insoluble particulates <10 counts mL⁻¹ at 0.5 μm. The ester‑derived acceptor fragment typically accounts for 28–33 % of the total molecular mass of the acceptor molecule. While power conversion efficiencies above 10 % have been demonstrated on 0.04 cm² cells certified according to ASTM E948‑16, scaling beyond 1 cm² often reveals a fill‑factor roll‑off attributed to series‑resistance losses in the MoO₃ interlayer, which remains an active area of device‑engineering investigation rather than a constraint intrinsic to the intermediate chemistry.Migration‑induced blooming of low‑molecular‑weight hindered amine light stabilisers in polypropylene tape and injection‑moulded automotive interior parts has driven the development of polymer‑bound analogues where the dimethylpyrrole‑2‑carboxylate nucleus functions as a UV‑absorbing chromophore anchor. The synthetic route first hydrolyses the ethyl ester to the carboxylic acid, which is then converted to the acid chloride with thionyl chloride in toluene at 60 °C and grafted onto a maleic‑anhydride‑functionalised polypropylene backbone (MAH content 0.8–1.2 wt%) in a co‑rotating twin‑screw extruder with an L/D ratio of 52:1, operating at a screw speed of 350 rpm and a flat temperature profile of 220–225 °C across barrels 4 through 12. Simultaneous feeding of a conventional oligomeric HALS at 0.15 wt% ensures synergistic radical scavenging, while the dimethylpyrrole‑grafted segments contribute 0.35–0.50 wt% pyrrole‑based UV absorber relative to the total compound mass. The compounding process must maintain melt residence time below 90 seconds to prevent thermal decarboxylation of the pyrrole acid, which would release carbon dioxide and create voids visible in subsequent extrusion coating.Prior to qualification, compounded films are subjected to accelerated weathering per ISO 4892‑2:2023, method A (xenon‑arc, Boro‑Boro filters, 0.35 W m⁻² at 340 nm, black‑standard temperature 65 °C, relative humidity 50 %), with a target of retaining ≥70 % of original elongation at break after 3000 hours. Regulatory alignment with materials intended for repeat‑use food‑contact applications is demonstrated by overall migration testing according to Commission Regulation (EU) No 10/2011, using simulant D2 (vegetable oil) for 10 days at 40 °C, where the requirement of <10 mg dm⁻² must be met. The final article can be a co‑extruded greenhouse film with a 150 μm polyolefin substrate or a talc‑filled polypropylene instrument panel substrate that complies with VDA 278:2022 thermodesorption limits for volatile organic compound and FOG emissions commonly applied by European automotive OEMs.Sterically Hindered Metal Porphyrins for Industrial Oxidation CatalysisThe selective oxidation of cyclohexane to cyclohexanol and cyclohexanone (KA oil) under mild aerobic conditions has been commercialised with cobalt and iron porphyrin catalysts that incorporate 3,5‑dimethyl‑β‑carboxyethyl substituents to suppress μ‑oxo dimer formation and oxidative degradation of the macrocycle. The porphyrin ligand is assembled via the Lindsey procedure: 1.0 eq of a benzaldehyde bearing an electron‑donating group is condensed with 1.0 eq of 3,5‑dimethyl‑1H‑pyrrole‑2‑carboxylic acid ethyl ester in dichloromethane using boron trifluoride diethyl etherate (0.8 eq) as the Lewis acid catalyst under strict moisture exclusion, generating a porphyrinogen mixture that is oxidised with 2.3 eq of 2,3‑dichloro‑5,6‑dicyano‑1,4‑benzoquinone. Due to the steric congestion imposed by the two methyl groups, the cyclisation step tolerates only a narrow effective molarity window; batch data from 50 L campaigns indicate that departing from a total reactant concentration of 12–14 mM by more than ±1.5 mM slashes the isolable porphyrin yield from 11 % to below 6 %, the remainder being lost as mixed oligomeric tar.Once the free‑base octa‑β‑substituted porphyrin is isolated by column chromatography (silica gel, chloroform‑hexane gradient), metal insertion is performed in dimethylformamide under reflux with 2.5 eq of cobalt(II) acetate tetrahydrate or iron(III) chloride, monitored by UV‑Vis until the four‑band Q‑bands collapse to the characteristic two‑band pattern of the metalloporphyrin. The crude catalyst is purified by recrystallisation from chloroform‑methanol and activated by heating under vacuum at 120 °C for 8 hours to remove axial ligands. In a representative continuous‑flow cyclohexane oxidation run, catalyst loading is 0.05 mol% relative to the substrate, with molecular oxygen at 0.9 MPa and a reactor temperature of 150 °C; the space‑time yield of KA oil reaches 120 g L⁻¹ h⁻¹ with a ketone‑to‑alcohol ratio of 1.8–2.2. Over 20 recycles, the metal‑leaching rate, determined by ICP‑OES analysis of the reactor effluent, remains below 0.05 ppb per cycle, a figure that satisfies the catalyst‑robustness criterion set out in the internal technology qualification protocol aligned with ISO 9001:2015 design and development clause 8.3. Beyond KA oil production, the same dimethylpyrrole‑modified porphyrin framework has been applied to iron‑catalysed alkane sulfoxidation and manganese‑catalysed epoxidation of terminal olefins, where addition of the ethyl ester (4.0 eq per aldehyde in the porphyrin step) remains the controlling parameter for overall ligand cost. |
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| Parameter | Specification Limit | Test Method |
|---|---|---|
| Assay (anhydrous, solvent-free) | ≥ 98.5% area | HPLC-UV (C18, 254 nm, acetonitrile/water gradient) |
| Individual related substance | ≤ 1.0% | HPLC-UV as above |
| Water (Karl Fischer) | ≤ 0.3% | ISO 760:1978, coulometric |
| Melting range | 73.0–76.0°C | ASTM E537-20, DSC endothermic peak onset |
| Residual solvents (GC) | Ethanol ≤ 5000 ppm, ethyl acetate ≤ 500 ppm | USP <467> Procedure A |
| Residue on ignition | ≤ 0.1% | Ph.Eur. 2.4.16 |
| Ester Substituent | Pyrrole Substitution | Isolated Yield (%) | Scrambled By-product (%) |
|---|---|---|---|
| Methyl | 3,5-dimethyl | 85 ± 2 | 2.5 |
| Ethyl | 3,5-dimethyl | 84 ± 3 | 2.9 |
| n-Propyl | 3,5-dimethyl | 79 ± 4 | 4.1 |
| Methyl | unsubstituted | 68 ± 8 | 19.5 |
| Ethyl | unsubstituted | 70 ± 7 | 18.2 |