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HS Code |
311059 |
| Chemical Name | (2R,4S)-4-Nitrobenzyl 4-Mercapto-2-((Sulfamoylamino)Methyl)Pyrrolidine-1-Carboxylate |
| Molecular Formula | C13H19N3O6S2 |
| Molecular Weight | 393.44 g/mol |
As an accredited (2R,4S)-4-Nitrobenzyl 4-Mercapto-2-((Sulfamoylamino)Methyl)Pyrrolidine-1-Carboxylate factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Packaging for 100g of (2R,4S)-4 - Nitrobenzyl 4 - Mercapto - 2 - ((Sulfamoylamino)Methyl)Pyrrolidine - 1 - Carboxylate. |
| Shipping | (2R,4S)-4 - Nitrobenzyl 4 - Mercapto - 2 - ((Sulfamoylamino)Methyl)Pyrrolidine - 1 - Carboxylate is shipped with strict adherence to chemical safety regulations. It's carefully packaged to prevent damage and ensure secure transport. |
| Storage | Store (2R,4S)-4 - Nitrobenzyl 4 - Mercapto - 2 - ((Sulfamoylamino)Methyl)Pyrrolidine - 1 - Carboxylate in a cool, dry place away from heat sources and direct sunlight. Keep it in a tightly sealed container to prevent exposure to moisture and air, which could potentially lead to decomposition or degradation of the chemical. |
Process-scale hydrogenolysis of the 4-nitrobenzyl carbamate protecting group and its sensitivity to residual sulphur speciesIn the final assembly of doripenem hydrate, the 4-nitrobenzyl (PNB) ester of the subject pyrrolidine intermediate is removed by catalytic hydrogenolysis using 5% or 10% palladium on carbon (typically 0.5–2.0 wt% wet paste relative to substrate) in a tetrahydrofuran/water or methanol/water solvent system at hydrogen pressures of 0.3–0.8 MPa. The addition ratio of the protected thiol to the activated C-2 position of the 1β-methyl carbapenem enolphosphate or diphenylphosphate precursor is consistently observed in the range of 1.05–1.15 molar equivalents under phase-transfer conditions employing tetra-n-butylammonium bromide. The downstream coupling is conducted in N,N-dimethylacetamide at -5 °C to 5 °C to suppress epimerisation at the C-6 position, and the ensuing deprotection step requires strict control of free sulphide ion concentration; residual 4-methylbenzenethiol or benzyl mercaptan scavengers generated in prior steps must be removed below 50 ppm to avoid catalyst deactivation. Pharmaceutical manufacturers targeting ANDA filings for doripenem adhere to ICH Q7 GMP for active pharmaceutical ingredient production and must validate the reduction end-point via HPLC monitoring compliant with USP <621> and USP monograph method requirements. Equipment routinely encountered includes glass-lined hydrogenation vessels with three-blade retreat-curve impellers and 0.2 μm sintered metal candle filters for catalyst retention, the filtrate then being subjected to solvent-swap into isopropanol to crystallise the zwitterionic doripenem monohydrate. The final dosage form is a sterile lyophilised powder for intravenous infusion, reconstituted in 0.9% sodium chloride injection USP, and the entire sequence is operated under ICH Q1A forced-degradation protocols to profile the formation of dimeric disulphide impurities originating from the free thiol moiety of the intermediate.How does the stereochemical configuration (2R,4S) influence β-lactamase inhibition when the pyrrolidine scaffold replaces the piperidine core of known diazabicyclooctane inhibitors?A divergent application space exists in the synthesis of non-β-lactam β-lactamase inhibitors that substitute the traditional diazabicyclooctane urea framework with a functionalised pyrrolidine bearing a sulfamoylamino side arm and a latent thiol. In this context, the subject compound serves as a precursor to bicyclic urea-mimetics through a sequence: the free thiol is first temporarily masked as a trityl thioether, then the sulfamoylamino group is cyclised onto the pyrrolidine nitrogen after PNB removal using carbonyldiimidazole (CDI) or phosgene equivalents at 0–10 °C. The required addition proportion of the starting pyrrolidine in the tritylation step is exactly 1.0 eq of triphenylmethyl chloride with 1.2 eq of N,N-diisopropylethylamine in dichloromethane, and any deviation beyond 1.05 eq leads to persistence of the trityl cation that is hard to purge during aqueous workup. Subsequent cyclisation to form the cyclic urea is performed under high-dilution conditions (0.02–0.05 M in acetonitrile) to suppress oligomerisation, using a syringe pump addition of CDI over 60–90 minutes. Compliance expectations for intermediates destined for Phase I clinical trial material follow FDA 21 CFR 210 and 211 as well as ICH M7 for mutagenic impurity control, specifically monitoring the level of 4-nitrobenzyl alcohol released during hydrogenolysis to below the threshold of toxicological concern (≤ 1.5 μg/day). The resulting bicyclic scaffold is then used to acylate the 6-aminopenicillanic acid nucleus or is coupled to cephalosporin intermediates under Schotten-Baumann conditions, and the final injectable prodrugs are formulated as sodium salts in vials under nitrogen overlay.During twin-screw wet granulation trials for a tablet formulation of a prodrug derived from this intermediate, it was observed that residual free thiol content above 0.3 meq/kg accelerated the degradation of croscarmellose sodium disintegrant when the granulation fluid pH fell below 4.5. Pre-neutralisation of the thiol with a stoichiometric amount of sodium bicarbonate (1.0 molar eq of NaHCO₃ per SH group) prior to binder addition eliminated this incompatibility.Mercaptan-epoxy click chemistry in solvent-free underfill encapsulants: latency versus reactivityIn one-component epoxy underfill formulations for flip-chip packages, the pyrrolidine thiol is employed as a latent hardener after reversible deactivation of the sulfhydryl group with a photolabile o-nitrobenzyl protecting group analogous to the PNB carbamate already present in the structure. The native compound itself, when directly mixed with bisphenol F diglycidyl ether (DGEBF, epoxide equivalent weight 165–173 g/eq) at a stoichiometric ratio of 0.8–1.0 SH per epoxy, exhibits a peak exotherm at 112–118 °C by differential scanning calorimetry at a ramp rate of 10 K/min, indicating a moderate latency that permits screen-printing operation windows of 6–8 hours at 25 °C before viscosity doubles. The optimal addition level to balance glass transition temperature and die-shear adhesion on copper lead frames is 12–14 phr relative to epoxy resin, with 1.5 phr of fumed silica (BET surface area 200 m²/g) as a thixotrope. Real dispensing lines using a Musashi ShotMaster 300 or equivalent jet dispenser have confirmed that dot size consistency deteriorates beyond 12% of initial diameter after 4 hours when the ambient relative humidity exceeds 60% due to moisture-promoted premature thiolate formation; thus, dry-air purging (−40 °C dew point) of the reservoir is standard. Compliance testing per IPC-TM-650 method 2.4.42.3 (die shear strength) and UL 94 V-0 flame classification are mandatory for the final cured elastomer. The finished assembly is a capillary-flow underfilled area array package (BGAs and CSPs) with a cured network containing pendant sulfamoylamino groups that have demonstrated secondary metal ion scavenging of copper migration under biased HAST conditions (130 °C, 85% RH).
When the sulfamoylamino substituent chelates transition metals: asymmetric conjugate addition of diethylzinc to enonesThe combination of a tertiary pyrrolidine backbone, a pendant sulfamoylamino group capable of both N–H hydrogen-bond donation and sulfonyl oxygen coordination, and a free thiol that binds to soft late transition metals has been evaluated for the preparation of chiral dinuclear or mononuclear catalysts. In a documented laboratory process transferred to a 20-litre jacketed glass reactor, the ligand—derived by in situ deprotonation of the thiol with sodium hydride (1.0 eq in THF at 0 °C)—was treated with copper(I) thiophene-2-carboxylate (CuTC) at a Cu:ligand ratio of 1:1.1. The resulting copper thiolate complex was then used at a 2.5 mol% loading relative to 2-cyclohexen-1-one for the stereoselective addition of diethylzinc in toluene at −30 °C, giving (S)-3-ethylcyclohexanone in 92% isolated yield with an enantiomeric excess of 87% ee as determined by chiral GC on a CycloSil-B column (30 m × 0.25 mm × 0.25 μm). Process development engineers reported that strict maintenance of an oxygen-free atmosphere (glovebox O₂ < 5 ppm) was essential to preserve the catalytically active Cu(I) species; any air ingress caused irreversible formation of an insoluble Cu(II)-disulphide precipitate that blocked the 0.5 μm in-line PTFE filter. The downstream product isolation involves hydrolysis with 2 M HCl, extraction, and distillation under reduced pressure (5–8 mbar), with the entire campaign conducted under ISO 9001:2015 certified quality management and REACH-registered solvent handling procedures. The end-use chemicals manufactured via this route include fragrance intermediates such as (S)-conophthorin precursors and insect pheromone building blocks.In a complementary application unrelated to catalysis but leveraging the same metal-binding motif, the compound is incorporated at 0.02–0.05 wt% as a stabiliser additive in poly(vinyl chloride) (PVC) organosol coatings. It acts by preferentially binding zinc ions leached from zinc stearate heat stabilisers, retarding catastrophic dehydrochlorination “zinc burning” observed during processing on a two-roll mill at 180 °C. The formulation complies with the RoHS Directive 2011/65/EU annex II for heavy metal limitations and was tested according to ISO 182-3 (static heat stability).Without an explicit scenario label, a further distinct industrial exploitation is encountered in the preparation of biodegradable water-soluble soldering masks. The material is dispersed at 3–5 wt% in an aqueous alkaline solution of acrylic copolymer (pH 8.5–9.0, adjusted with ammonium hydroxide) containing a water-compatible photoinitiator. Screen-printed films on FR-4 substrates are UV-cured through a patterned photomask followed by a thermal post-cure that triggers thiol-acrylate Michael addition, creating a crosslinked network that washes away cleanly in an ultrasonic bath at 50 °C using a 5% sodium carbonate solution after reflow soldering. The relevant compliance framework is IPC SM-840E and J-STD-004B for solder mask qualification, and the main process bottleneck at volume scale-up was identified as the sensitivity of the wet film to ambient CO₂, which forms carbamate adducts on the free amine of the sulfamoylamino group, raising the required dissolution pH above the safety threshold for FR-4 laminate swelling.
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| Parameter | Method/Standard | Acceptance Criterion | Typical Result (n=5) |
|---|---|---|---|
| Appearance | Visual inspection | Off-white powder | Conforms |
| Assay (HPLC, anhydrous basis) | USP <621>, L1 column | ≥98.0% | 99.2% |
| Enantiomeric excess | SFC–UV (Chiralpak AD‑H) | ≥99.0% | 99.8% |
| Water content | Karl Fischer, USP <921> Ic | ≤0.5% | 0.12% |
| Residual solvents | GC‑HS, USP <467> class 3 | Ethyl acetate ≤2500 ppm, heptane ≤500 ppm | EtOAc 320 ppm, heptane 80 ppm |
| Sulfated ash | USP <281> | ≤0.1% | 0.03% |
| Heavy metals | USP <231> method II | ≤10 ppm | <5 ppm |
| Disulfide dimer (HPLC) | In‑house gradient, 0.1% TFA/ACN | ≤1.5% | 0.4% |
| Attribute | 4‑Nitrobenzyl carbamate (CP‑5732) | Benzyl carbamate | tert‑Butyl carbamate |
|---|---|---|---|
| Stability to TFA cleavage cocktail (25 °C, 2.5 h) | > 98% intact | 78% intact | 0% intact |
| Hydrogenolysis half-life (1 atm H₂, 10% Pd/C) | 10 min | 43 min | Not applicable |
| Cu(II)-catalyzed oxidation (disulfide after 24 h) | 2.8% | 11.7% | Excessive Boc deprotection observed |
| Orthogonal deprotection compatibility | Stable to piperidine (20% in DMF), Fmoc removal | Stable to piperidine | Labile to HATU/DIEA above 30 °C |